LUBRICATING OIL COMPOSITIONS FOR HYDROGEN FUELED ENGINES FOR REDUCED PRE-IGNITION
20250320424 ยท 2025-10-16
Assignee
Inventors
- Nancy Z. Diggs (Phoenix, AZ, US)
- ALEC C. LABB (HOBOKEN, NJ, US)
- RONAK M. SHAH (PISCATAWAY, NJ, US)
- DAVID A. BRASS (EAST BRUNSWICK, NJ, US)
- Dean B. Clarke (Neshanic Station, NJ, US)
- Jun Cui (Berkeley Heights, NJ, US)
Cpc classification
C10M125/24
CHEMISTRY; METALLURGY
C10N2030/43
CHEMISTRY; METALLURGY
C10M145/00
CHEMISTRY; METALLURGY
C10N2030/42
CHEMISTRY; METALLURGY
C10M109/00
CHEMISTRY; METALLURGY
International classification
C10M145/00
CHEMISTRY; METALLURGY
C10M109/00
CHEMISTRY; METALLURGY
Abstract
This invention relates to a lubricating oil composition for a hydrogen fueled internal combustion engine (H2ICE) comprising or resulting from the admixing of: (i) base oil, (ii) a functionalized polymer, (iii) an overbased magnesium based detergent, (iv) an overbased calcium based detergent and (iv) one or more, optionally borated, higher and lower molecular weight PIBSA-PAM dispersants, and one or more zinc hydrocarbyl diphosphate compounds. The composition has a total sulfated ash of less than or equal to 1.0 wt. %, a kinematic viscosity at 100 C. of 5 to 20 cSt, a total phosphorous level of less than or equal to 0.12 wt. %, and a total sulfur level of less than or equal to 0.4 wt. %. The composition provides a reduction in abnormal pre-ignition events during combustion in a H2ICE compared to a comparable composition not including the combination of the functionalized polymer, the higher molecular weight PIBSA-PAM, the lower molecular weight PIBSA-PAM, the overbased magnesium containing detergent, the overbased calcium containing detergent, and the one or more zinc hydrocarbyl diphosphate compounds. Also provided are a method of making the composition, a method of lubricating a hydrogen engine, a method of reducing abnormal combustion events in a H2ICE, and a hydrogen engine oil additive concentrate composition.
Claims
1. A lubricating oil composition for hydrogen fueled internal combustion engines (H2ICE) comprising or resulting from the admixing of: a) an oil of lubricating viscosity at greater than 50 wt. % of the composition comprising a Group II base oil, a Group III base oil, a Group IV base oil, or combinations thereof; b) a functionalized polymer at from 0.01 to 20 wt. % based upon the total weight of the lubricating oil composition, wherein the functionalized polymer comprises a partially or fully saturated olefin homopolymer or copolymer backbone and at least one functional group, having: i) an Mn of 10,000 g/mol or more (GPC-PS) of the polymer prior to functionalization, ii) where the functional group is derived from an acylating agent and a compound containing amino and/or hydroxyl groups (including but not limited to where the polymer is functionalized with an acylating agent and subsequently reacted with a compound containing amino and/or hydroxyl groups), and, iii) wherein the homopolymer or copolymer backbone is derived from monomers selected from the group consisting of C.sub.2 to C.sub.3 linear alpha olefins, and C.sub.4 to Cm conjugated dienes; c) an overbased calcium based detergent with a Total Base Number (KOH/g) greater than or equal to 9 and less than or equal to 500 and at treat level to deliver less than or equal to 1500 ppm by weight of calcium to the composition; d) an overbased magnesium based detergent with a Total Base Number (KOH/g) greater than or equal to 9 and less than or equal to 500 and at treat level to deliver at least 500 ppm by weight of magnesium to the composition; e) one or more, optionally borated, higher molecular weight polyisobutylene succinimide (PIBSA-PAM) dispersant (Mn 1600 g/mol or more), f) one or more, optionally borated, lower molecular weight polyisobutylene succinimide (PIBSA-PAM) dispersant (Mn less than 1600 g/mol), wherein the treat level of the combination of the higher molecular weight PIBSA-PAM and lower molecular weight PIBSA-PAM is from 1.0 to 10.0 wt. % of the composition, and wherein the treat level of the higher molecular weight PIBSA-PAM is from 0.5 to 8.0 wt. % of the composition; and g) one or more zinc hydrocarbyl diphosphate compounds that provide more than 0.01 wt. % zinc, and less than or equal to 0.12 wt. % of phosphorus, based upon the weight of the lubricating oil composition; and wherein the lubricating oil composition has a total sulfated ash of less than or equal to 1.0 wt. %, a kinematic viscosity at 100 C. of 5 to 20 cSt, a total phosphorous level of less than or equal to 0.12 wt. %, and a total sulfur level of less than or equal to 0.4 wt. %.
2. The composition of claim 1, wherein a frequency of abnormal pre-ignition events in the H2ICE operating at 100% load during combustion is decreased by at least 20% compared to a comparable lubricating oil composition not within the ranges specified above for the functionalized polymer, the higher molecular weight PIBSA-PAM, the lower molecular weight PIBSA-PAM, the overbased magnesium containing detergent, the overbased calcium containing detergent, and the one or more zinc hydrocarbyl diphosphate compounds.
3. The composition of claim 1, wherein the number of abnormal pre-ignition events in the H2ICE during combustion (1000 rpm, 12 bar BMEP and 1.85 air:fuel ratio (AFR)) in terms of the number of pre-ignition events per 1,000 engine cycles is less than or equal to 3, or wherein the number of abnormal pre-ignition events in the H2ICE during combustion (1200 rpm, 18 bar BMEP and 2.05 air:fuel ratio (AFR)) in terms of the number of pre-ignition events per 1,000 engine cycles is less than or equal to 3.
4. The composition of claim 1, wherein the functionalized polymer is at from 0.3 to 5 wt. % based upon the total weight of the lubricating oil composition
5. The composition of claim 1, wherein the overbased magnesium containing detergent delivers between 800 ppm to 2200 ppm by weight of total magnesium to the lubricating oil composition.
6. The composition of claim 1, wherein the overbased calcium containing detergent delivers less than or equal to 1200 ppm by weight of calcium to the lubricating oil composition.
7. The composition of claim 1, wherein the one or more zinc hydrocarbyl diphosphate compounds include hydrocarbyl groups derived from one or more primary alcohols, one or more secondary alcohols or a combination of primary and secondary alcohols.
8. The composition of claim 1 further including one or more corrosion inhibitors, rust inhibitors or combinations thereof at a treat rate of greater than or equal to 0.02 wt. % of the lubricating oil composition.
9. The composition of claim 8, wherein the composition provides for less than 5% corrosion or rust in the ASTM D1748 test for corrosion/rust protection.
10. The composition of claim 1, wherein the composition provides for substantially no aqueous separation of lubricating oil emulsions including the lubricating oil composition and up to 10 wt. % water at 0 deg. C. and 25 deg. C. in the modified ASTM D7563 test.
11. The composition of claim 1, wherein the higher molecular weight PIBSA-PAM is borated, the lower molecular weight PIBSA-PAM is borated or a combination thereof, and is/are included at a treat level to deliver from 20 ppm to 1000 ppm by weight of boron to the composition.
12. The composition of claim 1, wherein the lubricating oil composition results in a high temperature corrosion bench test (HTCBT) result of a copper strip rating less than or equal to 3 (a, b) (ASTM D6594).
13. The composition of claim 1, wherein the composition is substantially free of molybdenum.
14. The composition of claim 1, wherein the functionalized polymer is an amide or imide functionalized partially or fully saturated homo-polyisoprene having: (i) an Mw/Mn of less than 2, (ii) a Functionality Distribution (Fd) value of 3.5 or less, (iii) an Mn of 10,000 g/mol or more (GPC-PS) of the polymer prior to functionalization, and (iv) an average functionality (Fv) of 1.4 to 20 functional group grafts/polymer chain.
15. The composition of claim 1, wherein the lubricating oil composition is used as a passenger vehicle lubricant (PVL), a commercial vehicle lubricant (CVL), or a marine engine oil.
16. The composition of claim 1, wherein the hydrogen fueled internal combustion engine is a heavy duty internal combustion engine, a light duty internal combustion engine or a stationary internal combustion engine.
17. A concentrate comprising or resulting from the admixing of: from 1 to less than or equal to 50 wt. % of one or more base oils; from 1 to 30 wt. %, such as 2 to 20 wt. %, based upon the weight of the concentrate, of one or more functionalized polymers, wherein the one or more functionalized polymers comprise a partially or fully saturated olefin homopolymer or copolymer backbone and at least one functional group, having: i) an Mn of 10,000 g/mol or more (GPC-PS) of the polymer prior to functionalization, ii) where the functional group is derived from an acylating agent and a compound containing amino and/or hydroxyl groups (including but not limited to where the polymer is functionalized with an acylating agent and subsequently reacted with a compound containing amino and/or hydroxyl groups), and, iii) wherein the homopolymer or copolymer backbone is derived from monomers selected from the group consisting of C2 to C30 linear alpha olefins, and C4 to C20 conjugated dienes; from 1 to 20 wt. % of an overbased magnesium based detergent with a Total Base Number (KOH/g) greater than or equal to 9 and less than or equal to 500; from 1 to 20 wt. % of an overbased calcium based detergent with a Total Base Number (KOH/g) greater than or equal to 9 and less than or equal to 500; from 2 to 40 wt. % of one or more, optionally borated, higher molecular weight polyisobutylene succinimide (PIBSA-PAM) dispersant (Mn 1600 g/mol or more), and one or more, optionally borated, lower molecular weight polyisobutylene succinimide (PIBSA-PAM) dispersant (Mn less than 1600 g/mol); and from 2 to 20 wt. % of one or more zinc hydrocarbyl diphosphate compounds.
18. The concentrate of claim 17, wherein the one or more functionalized polymers comprise an amide, imide, and/or ester functionalized partially or fully saturated polymer comprising C.sub.4-5 olefins having: i) an Mw/Mn of less than 2, ii) a Functionality Distribution (Fd) value of 3.5 or less, iii) an Mn of 10,000 g/mol or more (GPC-PS) of the polymer prior to functionalization, and iv) an average functionality (Fv) of 1.4 to 20 functional group grafts/polymer chain, provided that, if the polymer prior to functionalization is a copolymer of isoprene and butadiene, then the Mn of the copolymer is greater than 25,000 g/mol (GPC-PS).
19. A method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine comprising: I) providing to the hydrogen fueled internal combustion engine a lubricating oil composition comprising or resulting from the admixing of: a) an oil of lubricating viscosity at greater than 50 wt. % of the composition comprising a Group II base oil, a Group III base oil, a Group IV base oil, or combinations thereof; b) a functionalized polymer at from 0.01 to 20 wt. % based upon the total weight of the lubricating oil composition, wherein the functionalized polymer comprises a partially or fully saturated olefin homopolymer or copolymer backbone and at least one functional group, having: i) an Mn of 10,000 g/mol or more (GPC-PS) of the polymer prior to functionalization, ii) where the functional group is derived from an acylating agent and a compound containing amino and/or hydroxyl groups (including but not limited to where the polymer is functionalized with an acylating agent and subsequently reacted with a compound containing amino and/or hydroxyl groups), and, iii) wherein the homopolymer or copolymer backbone is derived from monomers selected from the group consisting of C2 to C30 linear alpha olefins, and C4 to C20 conjugated dienes; c) an overbased calcium based detergent with a Total Base Number (KOH/g) greater than or equal to 9 and less than or equal to 500 and at treat level to deliver less than or equal to 1500 ppm by weight of calcium to the composition; d) an overbased magnesium based detergent with a Total Base Number (KOH/g) greater than or equal to 9 and less than or equal to 500 and at treat level to deliver at least 500 ppm by weight of magnesium to the composition; e) one or more, optionally borated, higher molecular weight polyisobutylene succinimide (PIBSA-PAM) dispersant (Mn 1600 g/mol or more), f) one or more, optionally borated, lower molecular weight polyisobutylene succinimide (PIBSA-PAM) dispersant (Mn less than 1600 g/mol), wherein the treat level of the combination of the higher molecular weight PIBSA-PAM and lower molecular weight PIBSA-PAM is from 1.0 to 10.0 wt. % of the composition, and wherein the treat level of the higher molecular weight PIBSA-PAM is from 0.5 to 8.0 wt. % of the composition; and g) one or more zinc hydrocarbyl diphosphate compounds that provide more than 0.01 wt. % zinc, and less than or equal to 0.12 wt. % of phosphorus, based upon the weight of the lubricating oil composition; and wherein the lubricating oil composition has a total sulfated ash of less than or equal to 1.0 wt. %, a kinematic viscosity at 100 C. of 5 to 20 cSt, a total phosphorous level of less than or equal to 0.12 wt. %, and a total sulfur level of less than or equal to 0.4 wt. % II) providing a fuel comprising hydrogen to the hydrogen fueled internal combustion engine; III) combusting the fuel in the hydrogen fueled internal combustion engine; and IV) measuring a number of abnormal pre-ignition events during combustion; wherein a frequency of abnormal pre-ignition events in the H2ICE operating at 100% load during combustion is decreased by at least 20% compared to a comparable lubricating oil composition not within the ranges specified above for the functionalized polymer, the higher molecular weight PIBSA-PAM, the lower molecular weight PIBSA-PAM, the overbased magnesium containing detergent, the overbased calcium containing detergent, and the one or more zinc hydrocarbyl diphosphate compounds.
20. The method of claim 19, wherein the number of abnormal pre-ignition events in the H2ICE during combustion (1000 rpm, 12 bar BMEP and 1.85 air:fuel ratio (AFR)) in terms of the number of pre-ignition events per 1,000 engine cycles is less than or equal to 3, or wherein the number of abnormal pre-ignition events in the H2ICE during combustion (1200 rpm, 18 bar BMEP and 2.05 air:fuel ratio (AFR)) in terms of the number of pre-ignition events per 1,000 engine cycles is less than or equal to 3.
21. The method of claim 19, wherein the overbased magnesium containing detergent delivers between 800 ppm to 2200 ppm by weight of total magnesium to the lubricating oil composition.
22. The method of claim 19, wherein the overbased calcium containing detergent delivers less than or equal to 1200 ppm by weight of calcium to the lubricating oil composition.
23. The method of claim 19 further including one or more corrosion inhibitors, rust inhibitors or combinations thereof at a treat rate of greater than or equal to 0.02 wt. % of the lubricating oil composition.
24. The method of claim 23, wherein the composition provides for less than 5% corrosion or rust in the ASTM D1748 test for corrosion/rust protection.
25. The method of claim 19, wherein the composition provides for substantially no aqueous separation of lubricating oil emulsions including the lubricating oil composition and up to 10 wt. % water at 0 deg. C. and 25 deg. C. in the modified ASTM D7563 test.
26. The method of claim 19, wherein the higher molecular weight PIBSA-PAM is borated, the lower molecular weight PIBSA-PAM is borated or a combination thereof, and is/are included at a treat level to deliver from 20 ppm to 1000 ppm by weight of boron to the composition.
27. The method of claim 19, wherein the lubricating oil composition results in a high temperature corrosion bench test (HTCBT) result of a copper strip rating less than or equal to 3 (a, b) (ASTM D6594).
28. The method of claim 19, wherein the composition is substantially free of molybdenum.
29. The method of claim 19, wherein the functionalized polymer is an amide or imide functionalized partially or fully saturated homo-polyisoprene having: (i) an Mw/Mn of less than 2, (ii) a Functionality Distribution (Fd) value of 3.5 or less, (iii) an Mn of 10,000 g/mol or more (GPC-PS) of the polymer prior to functionalization, and (iv) an average functionality (Fv) of 1.4 to 20 functional group grafts/polymer chain.
30. The method of claim 19, wherein the hydrogen comprises green hydrogen, blue hydrogen, grey hydrogen, brown hydrogen, or combinations thereof.
31. The method of claim 19, wherein the fuel further includes natural gas, propane, mogas, renewable fuel, or combinations thereof.
32. The method of claim 19, wherein the fuel supplied to the engine comprises at least 50 mass % hydrogen, based upon the mass of the fuel.
33. The method of claim 19, wherein the hydrogen fueled internal combustion engine (H2ICE) is spark ignited or compression ignited.
34. The method of claim 19, wherein the lubricating oil composition is used as a passenger vehicle lubricant (PVL), a commercial vehicle lubricant (CVL), or a marine engine lubricant.
Description
DETAILED DESCRIPTION OF THE INVENTION
[0087] The features of the disclosure relating, where appropriate, to each and all aspects of the disclosure, will now be described in more detail as follows.
[0088] The lubricating oil compositions of the disclosure comprise components that may or may not remain the same chemically before and after mixing with an oleaginous carrier (such as a base oil) and/or other additives. This disclosure encompasses compositions which comprise the components before mixing, or after mixing, or both before and after mixing.
[0089] The inventors have unexpectedly and surprisingly discovered that a lubricating oil composition including a combination of a functionalized polymer, an overbased magnesium based detergent, an overbased calcium based detergent, one or more, optionally borated, higher and lower molecular weight PIBSA-PAM dispersants, and one or more zinc hydrocarbyl diphosphate compounds when used in hydrogen fueled internal combustion engines (H2ICE) reduces abnormal combustion events, such as pre-ignition in the H2ICE, relative to a comparable lubricating oil composition not including the combination of the functionalized polymer, the overbased magnesium based detergent, the overbased calcium based detergent, the one or more, optionally borated, higher and lower molecular weight PIBSA-PAM dispersants, and the one or more zinc hydrocarbyl diphosphate compounds. The inventors have also unexpectedly and surprisingly discovered that such inventive lubricating oil compositions also provide for unexpected and surprising improvement in water dispersancy in the lubricating oil, as well as rust prevention and copper corrosion resistance, which are all important attributes of a lubricating oil for use in a H2ICE.
[0090] Hydrogen engine abnormal combustion is distinct and different to gasoline combustion engine low speed preignition (LSPI). In particular, a hydrogen-air mixture requires much lower minimum ignition energy than a gasoline-air mixture, that is approximately 0.02 mJ for a hydrogen-air mixture compared to 0.25 mJ for gasoline-air mixture. Additionally, a hydrogen-air mixture also exhibits shorter ignition delay than a gasoline-air mixture at high combustion temperatures and low cylinder pressures. (See, http://teams/sites/il/Conferences/Baden%20-%20International%20Engine%20Congress/2023%2010th%20International%20Engine%20Congress/13p_Matsubara_Toyota.pdf.). These factors are expected to increase the propensity for hydrogen abnormal combustion compared to gasoline pre-ignition under equivalent combustion conditions. Furthermore, the high propensity for hydrogen internal combustion engines (ICEs) to experience abnormal combustion requires lean combustion operation with air to fuel ratios of from 1.5 to 2.5 being typical. In contrast, gasoline combustion engines operate near-stoichiometrically with an air to fuel ratio of about or approximately 1.0. It is well known that fuel enrichment in gasoline engines experiencing LSPI will mitigate pre-ignition. (See, https://cris.brighton.ac.uk/ws/portalfiles/portal/31594156/Harvey_Thesis.pdf.).
Lubricating Oil Compositions And Methods of Using Such Compositions to Reduce Pre-Ignition
[0091] This invention relates to a lubricating oil composition for hydrogen fueled internal combustion engines (H2ICE) comprising or resulting from the admixing of: a) an oil of lubricating viscosity at greater than 50 wt. % of the composition comprising a Group II base oil, a Group III base oil, a Group IV base oil, or combinations thereof; b) a functionalized polymer at from 0.01 to 20 wt. % based upon the total weight of the lubricating oil composition, wherein the functionalized polymer comprises a partially or fully saturated olefin homopolymer or copolymer backbone and at least one functional group, having: [0092] i) an Mn of 10,000 g/mol or more (GPC-PS) of the polymer prior to functionalization, [0093] ii) where the functional group is derived from an acylating agent and a compound containing amino and/or hydroxyl groups (including but not limited to where the polymer is functionalized with an acylating agent and subsequently reacted with a compound containing amino and/or hydroxyl groups), and, [0094] iii) wherein the homopolymer or copolymer backbone is derived from monomers selected from the group consisting of C.sub.2 to C.sub.30 linear alpha olefins, and C.sub.4 to C.sub.20 conjugated dienes;
c) an overbased calcium based detergent with a Total Base Number (KOH/g) greater than or equal to 9 and less than or equal to 500 and at treat level to deliver less than or equal to 1500 ppm by weight of calcium to the composition; d) an overbased magnesium based detergent with a Total Base Number (KOH/g) greater than or equal to 9 and less than or equal to 500 and at treat level to deliver at least 500 ppm by weight of magnesium to the composition; e) one or more, optionally borated, higher molecular weight polyisobutylene succinimide (PIBSA-PAM) dispersant (Mn 1600 g/mol or more), f) one or more, optionally borated, lower molecular weight polyisobutylene succinimide (PIBSA-PAM) dispersant (Mn less than 1600 g/mol), wherein the treat level of the combination of the higher molecular weight PIBSA-PAM and lower molecular weight PIBSA-PAM is from 1.0 to 10.0 wt. % of the composition, and wherein the treat level of the higher molecular weight PIBSA-PAM is from 0.5 to 8.0 wt. % of the composition; and g) one or more zinc hydrocarbyl diphosphate compounds that provide more than 0.01 wt. % zinc, and less than or equal to 0.12 wt. % of phosphorus, based upon the weight of the lubricating oil composition; and wherein the lubricating oil composition has a total sulfated ash of less than or equal to 1.0 wt. %, a kinematic viscosity at 100 C. of 5 to 20 cSt, a total phosphorous level of less than or equal to 0.12 wt. %, and a total sulfur level of less than or equal to 0.4 wt. %.
[0095] This invention also relates to a method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine comprising: I) providing to the hydrogen fueled internal combustion engine a lubricating oil composition comprising or resulting from the admixing of: a) an oil of lubricating viscosity at greater than 50 wt. % of the composition comprising a Group II base oil, a Group III base oil, a Group IV base oil, or combinations thereof; b) a functionalized polymer at from 0.01 to 20 wt. % based upon the total weight of the lubricating oil composition, wherein the functionalized polymer comprises a partially or fully saturated olefin homopolymer or copolymer backbone and at least one functional group, having: [0096] i) an Mn of 10,000 g/mol or more (GPC-PS) of the polymer prior to functionalization, [0097] ii) where the functional group is derived from an acylating agent and a compound containing amino and/or hydroxyl groups (including but not limited to where the polymer is functionalized with an acylating agent and subsequently reacted with a compound containing amino and/or hydroxyl groups), and, [0098] iii) wherein the homopolymer or copolymer backbone is derived from monomers selected from the group consisting of C2 to C30 linear alpha olefins, and C4 to C20 conjugated dienes;
c) an overbased calcium based detergent with a Total Base Number (KOH/g) greater than or equal to 9 and less than or equal to 500 and at treat level to deliver less than or equal to 1500 ppm by weight of calcium to the composition; d) an overbased magnesium based detergent with a Total Base Number (KOH/g) greater than or equal to 9 and less than or equal to 500 and at treat level to deliver at least 500 ppm by weight of magnesium to the composition; e) one or more, optionally borated, higher molecular weight polyisobutylene succinimide (PIBSA-PAM) dispersant (Mn 1600 g/mol or more), f) one or more, optionally borated, lower molecular weight polyisobutylene succinimide (PIBSA-PAM) dispersant (Mn less than 1600 g/mol), wherein the treat level of the combination of the higher molecular weight PIBSA-PAM and lower molecular weight PIBSA-PAM is from 1.0 to 10.0 wt. % of the composition, and wherein the treat level of the higher molecular weight PIBSA-PAM is from 0.5 to 8.0 wt. % of the composition; and g) one or more zinc hydrocarbyl diphosphate compounds that provide more than 0.01 wt. % zinc, and less than or equal to 0.12 wt. % of phosphorus, based upon the weight of the lubricating oil composition; and wherein the lubricating oil composition has a total sulfated ash of less than or equal to 1.0 wt. %, a kinematic viscosity at 100 C. of 5 to 20 cSt, a total phosphorous level of less than or equal to 0.12 wt. %, and a total sulfur level of less than or equal to 0.4 wt. %; II) providing a fuel comprising hydrogen to the hydrogen fueled internal combustion engine; III) combusting the fuel in the hydrogen fueled internal combustion engine; and IV) measuring a number of abnormal pre-ignition events during combustion; wherein a frequency of abnormal pre-ignition events in the H2ICE operating at 100% load during combustion is decreased by at least 20% compared to a comparable lubricating oil composition not within the ranges specified above for the functionalized polymer, the higher molecular weight PIBSA-PAM, the lower molecular weight PIBSA-PAM, the overbased magnesium containing detergent, the overbased calcium containing detergent, and the one or more zinc hydrocarbyl diphosphate compounds.
[0099] The method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine may further include measuring a number of abnormal pre-ignition events during combustion at 1000 rpm, 12 bar BMEP and 1.85 air:fuel ratio (AFR)), which results in the number of pre-ignition events per 1,000 engine cycles being less than or equal to 3, or less than or equal to 2, or less than or equal to 1.
[0100] The method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine may further include measuring a number of abnormal pre-ignition events during combustion at 1200 rpm, 18 bar BMEP and 2.05 air:fuel ratio (AFR)), which results in the number of pre-ignition events per 1,000 engine cycles being less than or equal to 3, or less than or equal to 2, or less than or equal to 1.
[0101] The method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine may further include measuring a number of abnormal pre-ignition events during combustion at 1000 rpm to 1200 rpm, 12 to 18 bar BMEP and 1.5 to 2.5 air:fuel ratio (AFR)), which results in the number of pre-ignition events per 1,000 engine cycles during combustion in the H2ICE operating at full (100%) load being decreased by at least 20%, or at least 30%, or at least 40%, or at least 50%, or at least 60%, or at least 70%, or at least 80%, or at least 90% compared to a comparable lubricating oil composition not within the ranges specified above for the functionalized polymer, the higher molecular weight PIBSA-PAM, the lower molecular weight PIBSA-PAM, the overbased magnesium containing detergent, the overbased calcium containing detergent, and the one or more zinc hydrocarbyl diphosphate compounds.
[0102] The base oil or oil of lubricating viscosity used in the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may have a KV100 viscosity of less than or equal to 20 cSt, or less than or equal to 15 cSt, or less than or equal to 12 cSt, or less than 10 cSt, or less than 9 cSt, or less than 8 cSt, or less than 7 cSt, or less than 6 cSt, or less than 5 cSt, or less than 4 cSt; and may be included at greater than 50 wt. %, or greater than 60 wt./, or greater than 70 wt. %, or greater than 80 wt. %, or greater than 90 wt. %, or greater than 95 wt. % of the composition. In another form of the instant disclosure, the oil of lubricating viscosity constitutes from 60 wt. % to 95 wt. %, or 70 to 90 wt. %, or 75 to 85 wt. % of the composition, and comprises a Group II base oil and/or a Group III base oil, and is substantially free of the Group IV base oil.
[0103] The lubricating oil composition and the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the instant disclosure may have a total sulfated ash of less than or equal to 1.0 wt. %, a kinematic viscosity at 100 C. of 5 to 20 cSt, a total phosphorous level of less than or equal to 0.12 wt. %, and a total sulfur level of less than or equal to 0.4 wt. %, or less than or equal to 0.35 wt %, or less than or equal to 0.30 wt %, or less than or equal to 0.25 wt %, or less than or equal to 0.20 wt %.
[0104] The lubricating oil composition and the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the instant disclosure may alternatively include a Group V base oil as part of the oil of lubricating viscosity, wherein the Group V based oil is included in the lubricating oil composition at from 0.1 to 50 wt. %, or 0.5 to 40 wt. %, or 1.0 to 20 wt. % or 2.0 to 10 wt. %, or 3.0 to 5 wt. % of the overall composition.
[0105] In another embodiment, the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may include a base oil comprising a Group I base oil, a Group II base oil, a Group III base oil, a Group IV base oil, a Group V base oil or combinations thereof, wherein the base oil is included at greater than 60 wt. %, or greater than 70 wt./, or greater than 80 wt. %, or greater than 90 wt. %, or greater than 95 wt. % of the composition.
[0106] In another embodiment, the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may include a base oil comprising a Group I base oil, a Group II base oil, a Group III base oil, a Group IV base oil, or combinations thereof, wherein the base oil is included at greater than 60 wt. %, or greater than 70 wt. %, or greater than 80 wt. %, or greater than 90 wt. %, or greater than 95 wt. % of the composition. That is the base oil is substantially free of Group V base oil.
[0107] In yet another embodiment, the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may include a base oil comprising a Group I base oil, a Group II base oil, a Group III base oil, or combinations thereof, wherein the base oil is included at greater than 60 wt. %, or greater than 70 wt. %, or greater than 80 wt. %, or greater than 90 wt. %, or greater than 95 wt. % of the composition. That is the base oil is substantially free of both Group V base oil and Group IV base oil.
[0108] In still yet another embodiment, the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may include a base oil comprising a Group I base oil, a Group II base oil, or combinations thereof, wherein the base oil is included at greater than 60 wt. %, or greater than 70 wt. %, or greater than 80 wt. %, or greater than 90 wt. %, or greater than 95 wt. % of the composition. That is the base oil is substantially free of both Group V base oil and Group IV base oil as well as Group III base oil.
[0109] The method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE includes as part of the lubricating oil one or more functionalized polymers, wherein the functionalized polymer may be a functionalized-hydrogenated PolyIsoPrene (F-H-PI) polymer, a functionalized-Olefin polymer or copolymer (f-OCP) or a combination of a functionalized-hydrogenated PolyIsoPrene (F-H-PI) polymer and a functionalized-Olefin polymer or copolymer (f-OCP).
[0110] As described above, the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE includes a functionalized polymer at from 0.1 to 20 wt. %, or 0.2 to 20 wt. %, or 0.2 to 6 wt. %, or 0.2 to 2.0 wt. %, or 0.4 to 1.8 wt. %, or 0.6 to 1.6 wt. %, or 0.8 to 1.4 wt. %, or 1.0 to 1.2 wt. % or 0.3 to 5 wt. %, or 0.4 to 3 wt. %, or 0.5 to 2.0 wt. %, or 0.5 to 1.0 wt. %, or 0.7 to 0.9 wt. % of the composition, wherein the functionalized polymer comprises a partially or fully saturated olefin homopolymer or copolymer backbone and at least one functional group, having: [0111] i) an Mn of 10,000 g/mol or more (GPC-PS) of the polymer prior to functionalization, [0112] ii) where the functional group is derived from an acylating agent and a compound containing amino and/or hydroxyl groups (including but not limited to where the polymer is functionalized with an acylating agent and subsequently reacted with a compound containing amino and/or hydroxyl groups), and, [0113] iii) wherein the homopolymer or copolymer backbone is derived from monomers selected from the group consisting of C.sub.2 to C.sub.30 linear alpha olefins, and C.sub.4 to C.sub.20 conjugated dienes.
[0114] In one embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may includes a polymer backbone derived from one or more of ethylene, propylene, butene, butadiene, isoprene, styrene, decene, and or dodecene.
[0115] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the homopolymer or copolymer backbone is derived from monomers selected from the group consisting of C.sub.2 to C.sub.12 linear alpha olefins and C.sub.4 to C.sub.12 conjugated dienes.
[0116] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the polymer backbone is a copolymer of isoprene and butadiene.
[0117] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the polymer backbone prior to functionalization comprises at least 90% isoprene repeat units, or at least 93% isoprene repeat units, or at least 96% isoprene repeat units, or at least 99% isoprene repeat units.
[0118] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the polymer backbone is homo-polyisoprene, or an ethylene-propylene copolymer.
[0119] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the polymer backbone comprises repeat units of one or more polar monomers.
[0120] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the one or more polar monomers are selected from the group consisting of fumarates, acrylates, maleates, methacrylates, acrylamides, acrylonitriles and combinations thereof.
[0121] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the polymer prior to functionalization has an Mn of 10,000 g/mol up to 100,000 g/mol (GPC-PS), or an Mn of 20,000 g/mol up to 80,000 g/mol (GPC-PS), or an Mn of 40,000 g/mol up to 80,000 g/mol (GPC-PS).
[0122] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the polymer prior to functionalization has an Mn of at least 25,000 g/mol (GPC-PS), or Mn of at least 45,000 g/mol (GPC-PS), or Mn of at least 65,000 g/mol (GPC-PS), or Mn of at least 85,000 g/mol (GPC-PS).
[0123] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein if the polymer prior to functionalization is a copolymer of isoprene and butadiene, the Mn of the copolymer is greater than 25,000 g/mol (GPC-PS), or greater than 45,000 g/mol (GPC-PS), or greater than 65,000 g/mol (GPC-PS), or greater than 85,000 g/mol (GPC-PS).
[0124] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the polymer backbone comprises at least about 50% %, or at least 60%, or at least 70% of 1,4 insertions of monomer.
[0125] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the acylating agent is maleic anhydride, itaconic anhydride, or an unsaturated carboxylic acid such as maleic acid, fumaric acid, cinnamic acid, or a corresponding ester.
[0126] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the functional group is selected from an amide, imide, or ester.
[0127] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the compound with which the acylated polymer backbone is reacted is a monoamine or a polyamine.
[0128] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the acylated polymer backbone is reacted with one or more amines selected from the group consisting of: polyhydrocarbyl polyamines, polyalkylene polyamines, hydroxy-substituted polyamines, polyoxyalkylene polyamines, and combinations thereof.
[0129] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the acylated polymer backbone is reacted with N-phenyl-p-phenylenediamine.
[0130] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the acylated polymer backbone is reacted with one or more hydroxy-substituted polyamine selected from the group consisting of: N-hydroxyalkyl-alkylene polyamines such as N-(2-hydroxyethyl)ethylene diamine, N-(2-hydroxyethyl)piperazine, and/or N-hydroxyalkylated alkylene diamines; or with one or more polyoxyalkylene polyamines of the group consisting of: polyoxyethylene and/or polyoxypropylene diamines.
[0131] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the compound with which the acylated polymer backbone is reacted is a hydroxyl-group containing compound.
[0132] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the functionalized polymer has a Functionality Distribution (Fd) value of 3.5 or less, or 3.0 or less, or 2.5 or less, or 2.0 or less.
[0133] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the functionalized polymer has an average functionality (Fv) of 1.4 to 20, or 2.0 to 18, or 4.0 to 16, or 6.0 to 14, or 8.0 to 12 functional group grafts/polymer chain.
[0134] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the functionalized polymer has a molecular weight distribution (Mw/Mn) of less than 2, or less than 1.8, or less than 1.6, or less than 1.4, or less than 1.2.
[0135] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the functionalized polymer is an amide or imide functionalized partially or fully saturated homo-polyisoprene having: [0136] (i) an Mw/Mn of less than 2, [0137] (ii) a Functionality Distribution (Fd) value of 3.5 or less, and [0138] (iii) an Mn of 10,000 g/mol or more (GPC-PS) of the polymer prior to functionalization.
[0139] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the functionalized polymer is an amide or imide functionalized partially or fully saturated homo-polyisoprene having: [0140] (i) an Mw/Mn of less than 1.8, [0141] (ii) a Functionality Distribution (Fd) value of 2.5 or less, [0142] (iii) an average functionality (Fv) of 4 to 10 functional group grafts/polymer chain, and [0143] (iv) an Mn of from 20,000 g/mol to 50,000 g/mol (GPC-PS) of the polymer prior to functionalization.
[0144] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the functionalized polymer is derived from a homo-polyisoprene that has been acylated with maleic anhydride or maleic acid and further reacted with an N-phenylphenylene diamine.
[0145] In another embodiment, the functionalized polymer described above of the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition may include wherein the functionalized polymer is derived from an ethylene-propylene copolymer that has been acylated with maleic anhydride or maleic acid and further reacted with an N-phenylphenylene diamine.
[0146] In yet another embodiment, the functionalized polymer of the lubricating oil composition and the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the instant disclosure may include at least 50%, or at least 60%, or at least 70% of 1,4-insertions of monomer. Furthermore, the functionalized polymer of the lubricating oil composition of the instant disclosure may include a partially or fully saturated homopolyisoprene containing one or more pendant amine groups and having an Mn of 25,000 to 100,000 g/mol, or 35,000 to 90,000 g/mol, or 45,000 to 80,000 g/mol, or 55,000 to 75,000 g/mol (GPC-PS) and at least 50%, or at least 60/a, or at least 70% of 1,4-insertions prior to functionalization.
[0147] In yet another embodiment, the functionalized polymer of the lubricating oil composition and the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the instant disclosure may be absent of styrene repeat units, or absent of butadiene repeat units, or is not a homo-polyisobutylene, or is not a copolymer of isoprene and butadiene.
[0148] In yet another embodiment, the functionalized polymer of the lubricating oil composition and the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the instant disclosure may also include a non-ionic fatty alcohol ethoxylate at from 1.0 to 20 wt. %, or 3.0 to 18.0 wt. %, or 5.0 to 15.0 wt %, or 7.0 to 13.0 wt. %, or 8.0 to 10.0 wt. % of the one or more functionalized polymers.
[0149] With regard to the overbased magnesium based detergent of the lubricating oil composition and the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation, it may be a sulfonate, a salicylate, a phenate or combinations thereof. The overbased magnesium based detergent may be included in the lubricating oil composition at treat level to deliver at least 500 ppm, or at least 520 ppm, or at least 540 ppm, or at least 560 ppm, or at least 580 ppm, or at least 600 ppm, or at least 650 ppm, or at least 700 ppm, or at least 750 ppm, or at least 800 ppm, or at least 850 ppm, or at least 900 ppm, or at least 1000 ppm, or at least 1100 ppm, or at least 1200 ppm, or at least 1500 ppm by weight of magnesium to the composition. Alternatively, the overbased magnesium containing detergent used in the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may comprise an overbased magnesium salicylate, an overbased magnesium sulfonate, an overbased magnesium phenate, or combinations thereof and may be included at treat level to deliver between 100 to 5000 ppm, or 500 to 4500 ppm, or 1000 to 4000 ppm, or 1500 to 3500 ppm, or 2000 to 3000 ppm, or 400 to 1200 ppm by weight of total magnesium to the lubricating oil composition.
[0150] The overbased calcium based detergent of the lubricating oil composition and the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation may be a sulfonate, a salicylate, a phenate or combinations thereof. The overbased calcium based detergent may be included in the lubricating oil composition at treat level to deliver less than or equal to 1500 ppm, or less than or equal to 1250 ppm, or less than or equal to 1000 ppm, or less than or equal to 800 ppm, or less than or equal to 600 ppm, or less than or equal to 400 ppm, or less than or equal to 200 ppm by weight of calcium to the composition. Alternatively, the overbased calcium containing detergent used in the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may comprise an overbased calcium salicylate, an overbased calcium sulfonate, an overbased calcium phenate, or combinations thereof.
[0151] The overbased magnesium containing detergent and/or the overbased calcium containing detergent used in the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may have a Total Base Number (KOH/g) greater than or equal to 9 and less than or equal to 500, or alternatively 50 to 450, or alternatively 100 to 400, or 150 to 400, or 200 to 350, or 250 to 300 (KOH/g). In another form, the overbased magnesium containing detergent may have a TBN of 100 mgKOH/g or more (such as 200 mgKOH/g or more), and typically will have a TBN of 250 mgKOH/g or more, such as 300 mgKOH/g or more, such as from 200 to 500 mgKOH/g, 225 to 450 mgKOH/g, 250 to 400 mgKOH/g, or 300 to 350 mgKOH/g.
[0152] The method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE also includes at least one overbased calcium containing detergent with a Total Base Number (KOH/g) greater than or equal to 9 and less than or equal to 500 and included at a treat level to deliver greater than or equal to 100 ppm by weight and less than or equal to 1500 ppm of total calcium to the composition. The at least one overbased calcium containing detergent may be a calcium salicylate, a calcium sulfonate, a calcium phenate or combinations thereof, and may have a Total Base Number (KOH/g) greater than or equal to 9 and less than or equal to 500, or alternatively 50 to 450, or alternatively 100 to 400, or 150 to 400, or 200 to 350, or 250 to 300 (KOH/g). In another form, the overbased calcium containing detergent may have a TBN of 100 mgKOH/g or more (such as 200 mgKOH/g or more), and typically will have a TBN of 250 mgKOH/g or more, such as 300 mgKOH/g or more, such as from 200 to 500 mgKOH/g, 225 to 450 mgKOH/g, 250 to 400 mgKOH/g, or 300 to 350 mgKOH/g. The at least one overbased calcium containing detergent may be included at treat level to deliver greater than or equal 100 ppm, or greater than 200 ppm, or greater than 300 ppm, or greater than 500 ppm, or greater than 700 ppm, or greater than 800 ppm, or greater than 1000 ppm, or greater than 1200 ppm, or greater than 1400 ppm, or equal to 1500 ppm by weight of total calcium to the lubricating oil composition.
[0153] The method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may have a total sulfated ash of less than or equal 1.0 wt. %, or less than or equal to 0.8 wt. %, or less than or equal to 0.6 wt. %, or less than or equal to 0.4 wt. %, as measured by ASTM D874-13a (2018). The method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure of use in a H2ICE may have a total phosphorous level of less than or equal to 0.12 wt. %, or less than or equal to 0.10 wt. %, or less than or equal to 0.09 wt. %, or less than or equal to 0.08 wt. %, or less than or equal to 0.07 wt. %, or less than or equal to 0.06 wt. %, or less than or equal to 0.05 wt. %, or less than or equal to 0.04 wt. %, or less than or equal to 0.03 wt. %.
[0154] Generally, the kinematic viscosity at 100 C. (KV100) of the inventive lubricating compositions may range from 5 to 20 cSt, or 6 to 18 cSt, or 8 to 16 cSt, such as 7 to 18 cSt, such as 10 to 15 cSt, or 13 to 16 cSt, or 8 to 17 cSt, as determined according to ASTM D 445-19a). The lubricating composition of the present disclosure may be a multigrade oil identified by the viscometric descriptor SAE 15W-X, SAE 10W-X, SAE 5W-X or SAE 0W-X, where X represents any one of 8, 12, 16, 20, 30, 40, and 50; the characteristics of the different viscometric grades can be found in the SAE J300 classification. Alternately, the lubricating composition may be the form of viscosity grade SAE 15W-X, SAE 10W-X, SAE 5W-X or SAE 0W-X, such as in the form of SAE 15W-X or SAE 10W-X, wherein X represents anyone of 8, 12, 16, 20, 30, 40, and 50. Preferably X is 20, 30, or 40. Alternately, the lubricating composition of the present disclosure may be a multigrade oil identified by the viscometric descriptor SAE 0W-20, 5W-20, 10W-30, 15W-40, 5W-30, 5W-40, 10W-40. (See standard SAE J300 published January 2015 by SAE International, formerly known as Society of Automotive Engineers). Alternatively, the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may be of various SAE viscosity grades including, but not limited to, 25W-X, 20W-X, 15W-X, 10W-X, 5W-X or 0W-X, where X represents any one of 8, 12, 16, 20, 30, 40, 50 or 60.
[0155] The method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE also includes one or more, optionally borated, higher molecular weight polyisobutylene succinimide (PIBSA-PAM) dispersant (Mn 1600 g/mol or more), and one or more, optionally borated, lower molecular weight polyisobutylene succinimide (PIBSA-PAM) dispersant (Mn less than 1600 g/mol), wherein the treat level of the combination of the higher molecular weight PIBSA-PAM and lower molecular weight PIBSA-PAM is from 1.0 to 10.0 wt. % of the composition, and wherein the treat level of the higher molecular weight PIBSA-PAM is from 0.5 to 8.0 wt. % of the composition. Hence, the inventive lubricating oil compositions including the higher molecular weight PIBSA-PAM in a borated form, the lower molecular weight PIBSA-PAM in a borated or a combination thereof, are included at a treat level to deliver from 20 to 1000 ppm, or 50 to 800 ppm, or 100 to 600 ppm, or 200 to 400 ppm, or 50 to 300 ppm by weight of boron to the composition. With regard to the treat level of the combination of the one or more, optionally borated, higher molecular weight polyisobutylene succinimide (PIBSA-PAM) dispersant (Mn 1600 g/mol or more), and one or more, optionally borated, lower molecular weight polyisobutylene succinimide (PIBSA-PAM) dispersant (Mn less than 1600 g/mol), it may range from 1.0 to 10.0 wt %, or 2.0 to 9.0 wt. %, or 3.0 to 8.0 wt. %, or 4.0 to 7.0 wt. %, or 5.0 to 6.0 wt. % of the composition. The treat level of the higher molecular weight PIBSA-PAM in the composition may range from 0.5 to 8.0 wt. %, or 1.0 to 7.0 wt./, or 1.5 to 6.0 wt. %, or 2.0 to 5.5 wt. %, or 2.5 to 5.0 wt. %, or 3.0 to 4.0 wt. %, or 1.0 to 4.0 wt. % of the composition.
[0156] In another embodiment, the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may include an antiwear agent. The antiwear agent may include, but is not limited to, one or more zinc dialkyl dithiophosphate (ZDDP) compounds. More particularly, the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE also includes one or more zinc hydrocarbyl diphosphate compounds that provide more than 0.01 wt. % zinc, and less than or equal to 0.12 wt. % of phosphorus, based upon the weight of the lubricating oil composition. The ZDDP compounds may include a hydrocarbyl group of the zinc hydrocarbyl dithiophosphate which is derived from one or more primary alcohols, one or more secondary alcohols or a combination of primary and secondary alcohols. The one or more ZDDP compounds may be included in the lubricating oil at a treat level of from about 0.4 wt. % to about 1.5 wt, or 0.5 to 1.3 wt. %, or 0.6 to 1.1 wt. %, or 0.7 to 1.0 wt. %, or 0.8 to 0.9 wt % of the lubricating oil composition. In one advantageous form, the one or more zinc dialkyldithiophosphates (ZDDP) include greater than or equal to 85 wt. % secondary alcohols and less than or equal to 15 wt. % primary alcohols.
[0157] In another embodiment, the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may include one or more of the following components: one or more friction modifiers; one or more antioxidants; one or more pour point depressants; one or more anti-foaming agents; one or more viscosity modifiers; one or more dispersants other than the higher molecular weight PIBSA-PAM and the lower molecular weight PIBSA-PAM; one or more inhibitors, one or more antirust agents (rust inhibitors); one or more corrosion inhibitors, one or more seal swell agents; and/or one or more other anti-wear agents.
[0158] In another embodiment, the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may optionally include one or more corrosion inhibitors, rust inhibitors or combinations thereof at a treat rate of greater than or equal to 0.02 wt. % of the lubricating oil composition. Water is a reaction product of the combustion of a fuel containing hydrogen, and therefore corrosion of various internal components of the H2ICE due to water exposure may be addressed with proper selection of corrosion inhibitor type and treat level in the lubricating oil composition. The corrosion inhibitor or rust inhibitor, may include, but is not limited to, a non-ionic fatty alcohol ethoxylate, a substituted thiadiazole, a substituted benzotriazole, a substituted triazole, a trisubstituted borate, a primary amine, a substituted carboxylic acid functional group, a substituted ester functional group, a substituted anhydride functional group, or a combination thereof. The corrosion inhibitor and/or rust inhibitor may be included in the lubricating oil composition at a treat level of from of 0.02 wt. % to 6.0 wt. %, or 0.05 to 5.0 wt. %, or 0.1 to 4.5 wt. %, or 0.5 to 4.0 wt. %, or 1.0 to 3.5 wt. %, or 1.5 to 3.0 wt. %, or 2.0 to 2.5 wt. % of the lubricating oil composition.
[0159] The inventive lubricating oil compositions including one or more corrosion inhibitors, rust inhibitors or combinations at the treat levels indicated above provide for less than 5%, or less than 4%, or less than 3%, or less than 2%, or less than 1% corrosion or rust in the ASTM D1748 test for corrosion/rust protection. Additionally, the inventive lubricating oil compositions including one or more corrosion inhibitors, rust inhibitors or combinations at the treat levels indicated above provide for substantially no aqueous separation of lubricating oil emulsions including the lubricating oil composition and up to 10 wt. % water at 0 deg. C. and 25 deg. C. in the modified ASTM D7563 test.
[0160] The inventive lubricating oil compositions including one or more corrosion inhibitors, rust inhibitors or combinations at the treat levels indicated above also result in a high temperature corrosion bench test (HTCBT) result of a copper strip rating less than or equal to 3 (a, b), or less than or equal to 2 (a, b, c, d, e), or equal to 1 (a, b) as tested per ASTM D6594.
[0161] In another embodiment, the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may include one or more friction modifiers including, but not limited to, dimeric molybdenum dialkyldithiocarbamate (moly dimer), a trimeric molybdenum dialkyldithiocarbamate (moly trimer), or a combination thereof at a treat level to deliver from 12 ppm to 600 ppm, or 20 ppm to 500 ppm, or 30 ppm to 200 ppm, or 40 to 180 ppm, or 60 to 160 ppm, or 80 to 140 ppm, or 100 to 120 ppm by weight of molybdenum to the composition. In yet another advantageous form, the lubricating oil composition of the instant disclosure is substantially free of molybdenum, which means less than 10 ppm, or less than 5 ppm, or less than 3 ppm, or less than 2 ppm, or less than 1 ppm, based on the overall weight of the lubricating oil composition.
[0162] In another embodiment, the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may have a high temperature high shear viscosity at 150 C. (HTHS) as determined according to ASTM D4683-20 of greater than or equal to 2.6 mPa.Math.s and less than or equal to 3.2 mPa.Math.s, or greater than or equal to 2.7 mPa.Math.s and less than or equal to 3.1 mPa.Math.s, or greater than or equal to 2.85 mPa.Math.s and less than or equal to 3.0 mPa.Math.s. Alternatively, the lubricating oil composition of the instant disclosure may have a HTHS of greater than or equal to 3.5 mPa.Math.s, or greater than or equal to 3.6 mPa.Math.s, or greater than or equal to 3.7 mPa.Math.s, or greater than or equal to 3.8 mPa.Math.s, or greater than or equal to 3.9 mPa.Math.s, or greater than or equal to 4.1 mPa.Math.s, or greater than or equal to 4.3 mPa.Math.s, or greater than or equal to 4.5 mPa.Math.s.
[0163] In another embodiment, the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may include one or more antioxidants selected from one or more phenolic antioxidants, one or more sulfur based antioxidants, one or more aminic antioxidants or a combination thereof, and wherein the one or more antioxidants comprise from 1.0 to 6.0 wt. %, or 1.5 to 5.5 wt. %, or 2.0 to 5.0 wt. %, or 2.5 to 4.5 wt. %, or 3.0 to 4.0 wt. % of the overall lubricating oil composition.
[0164] The method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure may be used as a passenger vehicle lubricant (PVL), a commercial vehicle lubricant (CVL), or a marine engine lubricant.
[0165] The method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may be used in conjunction with various hydrogen containing fuel sources for combusting in the hydrogen fueled internal combustion engine, including, but not limited to fuel sources including green hydrogen, blue hydrogen, grey hydrogen, brown hydrogen, or combinations thereof. The hydrogen containing fuel source may also include other non-hydrogen fuel sources including, but not limited to, natural gas, compressed natural gas, propane, mogas (such as gasoline having an octane number of 87 or more, such as 93 more), diesel fuel (such as diesel fuel having a cetane number of 40 or more, such as 50 or more), renewable fuel (such as hydrogenated vegetable oil, fatty acid methyl ester, sustainable aviation fuel (SAF), or combinations thereof. The other non-hydrogen fuels may be included in the hydrogen containing fuel at from 1 to 75 wt. %, or 5 to 70 wt. %, or 10 to 65 wt. %, or 15 to 60 wt. %, or 20 to 55 wt. %, or 25 to 50 wt. %, or 30 to 45 wt./, or 35 to 40 wt. % of the overall fuel composition. Hence, the fuel supplied to the hydrogen fueled engine comprises at least 5 mass % hydrogen, such as at least 10 mass % hydrogen, such as at least 15 mass % hydrogen, such as 20 mass % hydrogen, such as at least 25 mass % hydrogen, such as at least 30 mass % hydrogen, such as at least 35 mass % hydrogen, such as at least 40 mass % hydrogen, such as at least 45 mass % hydrogen, such as at least 50 mass % hydrogen, such as at least 55 mass % hydrogen, such as at least 60 mass % hydrogen, such as at least 70 mass % hydrogen, such as at least 75 mass % hydrogen, such as at least 80 mass % hydrogen, such as at least 85 mass % hydrogen, such as at least 90 mass % hydrogen, such as at least 95 mass % hydrogen, such as at least 99 mass % hydrogen, such as 100 mass % hydrogen, based upon the mass of the fuel. In a preferred form, the fuel supplied to the hydrogen engine comprises substantially 100 mass % hydrogen, based upon the mass of the fuel.
[0166] In other embodiments the fuel supplied to the hydrogen fueled engine comprises at least 5 mass % hydrogen and less than 95 mass % of non-hydrogen fuel (such as hydrocarbon fuel), such as at least 10 mass % hydrogen and less than 90 mass % of non-hydrogen fuel, such as at least 15 mass % hydrogen and less than 85 mass % of non-hydrogen fuel, such as 20 mass % hydrogen and less than 80 mass % of non-hydrogen fuel, such as at least 25 mass % hydrogen and less than 75 mass % of non-hydrogen fuel, such as at least 30 mass % hydrogen and less than 70 mass % of non-hydrogen fuel, such as at least 35 mass % hydrogen and less than 65 mass % of non-hydrogen fuel, such as at least 40 mass % hydrogen and less than and less than 60 mass % of non-hydrogen fuel, such as at least 45 mass % hydrogen and less than 55 mass % of non-hydrogen fuel, such as at least 50 mass % hydrogen and less than 50 mass % of non-hydrogen fuel, such as at least 55 mass % hydrogen and less than 45 mass % of non-hydrogen fuel, such as at least 60 mass % hydrogen and less than 40 mass % of non-hydrogen fuel, such as at least 70 mass % hydrogen and less than 30 mass % of non-hydrogen fuel, such as at least 75 mass % hydrogen and less than 25 mass % of non-hydrogen fuel, such as at least 80 mass % hydrogen and less than 20 mass % of non-hydrogen fuel, such as at least 85 mass % hydrogen and less than 15 mass % of non-hydrogen fuel, such as at least 90 mass % hydrogen and less than 10 mass % of non-hydrogen fuel, such as at least 95 mass % hydrogen and less than 5 mass % of non-hydrogen fuel, such as at least 99 mass % hydrogen and less than 1 mass % of non-hydrogen fuel, based upon the mass of the fuel.
[0167] The method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may be used such that the fuel comprising hydrogen and the lubricating oil composition are combined prior to injection into a combustion chamber of the hydrogen fueled internal combustion engine (H2ICE) to form a fuel composition. Alternatively, the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may be used such that the fuel comprising hydrogen and the lubricating oil composition are combined in the combustion chamber of the hydrogen fueled internal combustion engine (H2ICE) to form a fuel composition.
[0168] The method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may be used in conjunction with a hydrogen fueled internal combustion engine (H2ICE) that is spark ignited, compression ignited, or a combination thereof. The hydrogen fueled internal combustion engine may be a heavy duty or light duty internal combustion engine. Alternatively, the hydrogen fueled internal combustion engine for use with the method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may be a stationary internal combustion engine. The hydrogen fueled internal combustion engine (H2ICE) may optionally include a turbocharger or a supercharger prior to the hydrogen fueled internal combustion engine.
[0169] The method of reducing abnormal combustion events in a hydrogen fueled internal combustion engine (H2ICE) during operation of the engine and the lubricating oil composition of the instant disclosure for use in a H2ICE may be used in a hydrogen fueled internal combustion engine (H2ICE) that operates at a BMEP ranging from 12 bar to 18 bar, or 13 to 17 bar, or 14 to 16 bar, or 15 bar, and operates at an air:fuel ratio (AFR) from 1:1 to 3:1. In particular, when the hydrogen fueled internal combustion engine operates at about 12 bar, the AFR may be 3:1 or less, 2.5:1 or less, or 2:1 or less, 1.85:1 or less, or 1.7:1 or less, or 1.6:1 or 1.5:1 or less, or 1.4:1 or less, such as 1:1 to 2:1. When the hydrogen fueled internal combustion engine operates at about 18 bar, the AFR may be 3:1, 2.5:1 or less, or 2:1 or less, 1.85:1 or less, or 1.7:1 or less, or 1.6:1 or 1.5:1 or less, or 1.4:1 or less, such as 1:1 to 2:1.
[0170] This invention also relates to the use of the lubricating oil composition described herein, to lubricate a hydrogen fueled internal combustion engine where the fuel provided to the hydrogen fueled internal combustion engine comprises: [0171] a) 1 to 100 mass % of hydrogen, [0172] b) 0 to 99 mass % of a petroleum derived fuel, and/or [0173] c) from 0 to 99 mass %, or 0.1 to 98.9 mass %, or 1 to 75 mass %, or 5 to 50 mass %, of a renewable fuel other than hydrogen, based upon the total mass of hydrogen fuel, renewable fuel and the petroleum derived fuel.
[0174] In embodiments, the fuel comprising hydrogen and the lubricating oil composition are combined in the combustion chamber to form a fuel composition, alternately the fuel comprising hydrogen and the lubricating oil composition are combined prior to injection into the combustion chamber to form a fuel composition.
[0175] In embodiments, the fuel comprising hydrogen and the lubricating oil composition comprise from 0.01 to 20 mass % of lubricating oil composition, such as from 0.025 to 15 mass % of lubricating oil composition, from 0.05 to 10 mass % of lubricating oil composition, from 0.10 to 5 mass % of lubricating oil composition, from 0.015 to 2.5 mass % of lubricating oil composition, based upon the mass of the fuel comprising hydrogen and the lubricating oil composition.
[0176] Lambda, , is the air fuel ratio (AFR) of the amount of air and fuel provided to an engine combustion chamber divided by the air fuel ratio for a stoichiometric reaction in the same engine combustion chamber under the same conditions of pressure and temperature. In a preferred embodiment, the lambda, or AFR, for hydrogen fueled engines being lubricated with the lubrication composition herein is 2.5 or less, such as 2 or less, such as 1.85 or less, such as 1.7 or less, such as 1.6 or less, such as 1.5:1 or less, such as 1.4 or less, such as 0.5 to 3, such as 1 to 2.1 such as 1.3 to 2, such as 1.4 to 1.9, such as 1.5 to 1.85. For a given hydrogen fueled engine, a lower lambda means lower cost because less air is injected into the combustion chamber allowing more fuel to be consumed and more power to be produced. Likewise, less cost is incurred in engine design and operation as more efficient lambda, 7, at higher pressures requires less specialized high pressure equipment (such as turbochargers or super chargers) to inject air into the combustion chambers, among other things. Hence, the lubricating oil compositions described herein when utilized with hydrogen fueled engines built with existing engine block technology, enable easier/more efficient retrofitting/less-redesign to be able to efficiently use hydrogen fuel. Moreover, the lubricating oil compositions described herein enables one or more of the following benefits to the H2ICE during operation: lower lambda operation by reducing oil-derived abnormal combustion events typically associated with enriched lambda operation (relative to lambda at 2 to 2.5). In turn this enables, better throttle response, improved power density, reduction in air charging complexity and cost, or reduced engine research and development.
[0177] In embodiments, the air fuel ratio (AFR) in the combustion chamber of a hydrogen fueled internal combustion engine at 12 bar (1.2 MPa), is 2.5:1 or less, or 2:1 or less, 1.85:1 or less, or 1.7:1 or less, or 1.6:1 or 1.5:1 or less, or 1.4:1 or less, such as 1:1 to 2:1 or 1.5 to 1.9.
[0178] In other embodiments, the air fuel ratio (AFR) in the combustion chamber of a hydrogen fueled internal combustion engine at 18 bar (1.8 MPa), is 2.5:1 or less, or 2:1 or less, 1.85:1 or less, or 1.7:1 or less, or 1.6:1 or 1.5:1 or less, or 1.4:1 or less, such as 1:1 to 2:1 or 1.5 to 1.9.
[0179] In still other embodiments, the ratio of air fuel ratio in the combustion chamber of a hydrogen fueled internal combustion engine at 12 bar (1.2 MPa) to the ratio of air fuel ratio in the combustion chamber of a hydrogen fueled internal combustion engine at 18 bar (1.8 MPa), is 0.75 or more, such as 0.8 or more, such as 0.85 or more, such as 0.90 or more.
[0180] The lubricating oil compositions described herein, when used in hydrogen fueled internal combustion engines, facilitate a higher Brake Mean Effective Pressure (BMEP) by allowing the engine to operate at greater power and torque without the propensity for abnormal combustion events. For example hydrogen fueled ICE's can obtain a BMEP of 12 to 18 bar.
[0181] The hydrogen fueled internal combustion engines described herein may be retrofitted engines, or engines designed for moving vehicles (such as automobiles, trucks, generators, marine vessels, etc.), stationary engines, such as heavy duty internal combustion engines or standing generators comprising internal combustion engines.
[0182] In embodiments, the lubricating compositions disclosed herein may be used in heavy-duty engines (e.g., heavy-duty vehicles having a gross vehicle weight rating of 10,000 pounds or more).
[0183] In embodiments, the lubricating compositions disclosed herein may be used as passenger car motor oil.
[0184] In embodiments, the lubricating compositions disclosed herein may be used in a passenger car or heavy duty vehicle where the hydrogen fueled internal combustion engine is a passenger car or heavy duty vehicle internal combustion engine (optionally also using gasoline, natural gas, propane and/or diesel fuel).
[0185] In embodiments, the lubricating compositions disclosed herein may be for use in a heavy duty internal combustion engines or stationary internal combustion engines.
Concentrates
[0186] A concentrate, also referred to as an additive package, adpak, or addpack, is a composition having less than 50 mass % (such as from 1 to 40 mass %, such as from 2 to 30 mass %, such as 3 to 25 mass %, such as 4 to 20 mass %, such as 5 to 15 ass %) base oil and lubricant composition additives (such as described herein) which is typically then further blended with additional Group I, II, III and/or Group IV base oil to form a lubricating oil product. The concentrate typically is absent Group IV base oil, such as polyalphaolefin, having a viscosity index of 100 or more, such as 120 or more, such as 140 or more as determined by ASTM D2270. Alternately the concentrate contains Group IV base oil, such as polyalphaolefin, having a viscosity index of 100 or more, such as 120 or more, such as 140 or more as determined by ASTM D2270 in amounts that the total concentration of the PAO in the final lubrication oil composition is less 70 mass % or less, such as 60 mass % or less, 50 mass % or less, such as 40 mass % or less, 30 mass % or less, such as 20 mass % or less, 10 mass % or less, such as 5 mass % or less, based upon the weight of the lubricating oil composition.
[0187] This disclosure also relates to concentrate compositions comprising or resulting from the admixing of: from 1 to less than or equal to 50 wt. % of one or more base oils; from 1 to 30 wt. %, such as 2 to 20 wt. %, based upon the weight of the concentrate, of one or more functionalized polymers, wherein the one or more functionalized polymers comprise a partially or fully saturated olefin homopolymer or copolymer backbone and at least one functional group, having: i) an Mn of 10,000 g/mol or more (GPC-PS) of the polymer prior to functionalization, ii) where the functional group is derived from an acylating agent and a compound containing amino and/or hydroxyl groups (including but not limited to where the polymer is functionalized with an acylating agent and subsequently reacted with a compound containing amino and/or hydroxyl groups), and iii) wherein the homopolymer or copolymer backbone is derived from monomers selected from the group consisting of C2 to C30 linear alpha olefins, and C4 to C20 conjugated dienes; from 1 to 20 wt. % of an overbased magnesium based detergent with a Total Base Number (KOH/g) greater than or equal to 9 and less than or equal to 500; from 1 to 20 wt. % of an overbased calcium based detergent with a Total Base Number (KOH/g) greater than or equal to 9 and less than or equal to 500; from 2 to 40 wt. % of one or more, optionally borated, higher molecular weight polyisobutylene succinimide (PIBSA-PAM) dispersant (Mn 1600 g/mol or more), and one or more, optionally borated, lower molecular weight polyisobutylene succinimide (PIBSA-PAM) dispersant (Mn less than 1600 g/mol); and from 2 to 20 wt. % of one or more zinc hydrocarbyl diphosphate compounds.
[0188] Alternatively, the concentrate compositions disclosed herein include the one or more functionalized polymers comprising an amide, imide, and/or ester functionalized partially or fully saturated polymer comprising C.sub.4-5 olefins having: [0189] i) an Mw/Mn of less than 2, [0190] ii) a Functionality Distribution (Fd) value of 3.5 or less, and [0191] iii) an Mn of 10,000 g/mol or more (GPC-PS) of the polymer prior to functionalization,
provided that, if the polymer prior to functionalization is a copolymer of isoprene and butadiene, then the Mn of the copolymer is greater than 25,000 g/mol (GPC-PS).
[0192] Alternatively, the concentrate compositions disclosed herein include the one or more zinc hydrocarbyl diphosphate compounds which include hydrocarbyl groups derived from one or more primary alcohols, one or more secondary alcohols or a combination of primary and secondary alcohols.
[0193] Alternatively, the concentrate compositions disclosed herein include from 0.10 to 10 wt. % of one or more corrosion inhibitors, rust inhibitors or combinations thereof selected from the group consisting of a non-ionic fatty alcohol ethoxylate, a substituted thiadiazole, a substituted benzotriazole, a substituted triazole, a trisubstituted borate, a primary amine, a substituted carboxylic acid functional group, a substituted ester functional group, a substituted anhydride functional group or a combination thereof.
[0194] The concentrate compositions disclosed herein may further comprise combining the concentrate with a base oil to form a lubricating oil composition comprising: an oil of lubricating viscosity at greater than 50 wt. % of the composition comprising a Group II base oil, a Group III base oil, a Group IV base oil, or combinations thereof; a functionalized polymer at from 0.01 to 20 wt. % based upon the total weight of the lubricating oil composition, wherein the functionalized polymer comprises a partially or fully saturated olefin homopolymer or copolymer backbone and at least one functional group, having: i) an Mn of 10,000 g/mol or more (GPC-PS) of the polymer prior to functionalization, ii) where the functional group is derived from an acylating agent and a compound containing amino and/or hydroxyl groups (including but not limited to where the polymer is functionalized with an acylating agent and subsequently reacted with a compound containing amino and/or hydroxyl groups), and, wherein the homopolymer or copolymer backbone is derived from monomers selected from the group consisting of C2 to C30 linear alpha olefins, and C4 to C20 conjugated dienes; an overbased calcium based detergent with a Total Base Number (KOH/g) greater than or equal to 9 and less than or equal to 500 and at treat level to deliver less than or equal to 1500 ppm by weight of calcium to the composition; an overbased magnesium based detergent with a Total Base Number (KOH/g) greater than or equal to 9 and less than or equal to 500 and at treat level to deliver at least 500 ppm by weight of magnesium to the composition; one or more, optionally borated, higher molecular weight polyisobutylene succinimide (PIBSA-PAM) dispersant (Mn 1600 g/mol or more), one or more, optionally borated, lower molecular weight polyisobutylene succinimide (PIBSA-PAM) dispersant (Mn less than 1600 g/mol), wherein the treat level of the combination of the higher molecular weight PIBSA-PAM and lower molecular weight PIBSA-PAM is from 1.0 to 10.0 wt. % of the composition, and wherein the treat level of the higher molecular weight PIBSA-PAM is from 0.5 to 8.0 wt. % of the composition; and one or more zinc hydrocarbyl diphosphate compounds that provide more than 0.01 wt. % zinc, and less than 0.08 wt. % of phosphorus, based upon the weight of the lubricating oil composition; and the lubricating oil composition having a total sulfated ash of less than or equal to 1.0 wt. %, a kinematic viscosity at 100 C. of 5 to 20 cSt, a total phosphorous level of less than or equal to 0.12 wt. %, a total nitrogen content of greater than or equal to 0.10 wt. %, and a total sulfur level of less than or equal to 0.4 wt. %.
[0195] Also alternatively, the resulting lubricating oil composition decreases the number or frequency of abnormal pre-ignition events in the H2ICE operating at 100% load during combustion by at least 20% compared to a comparable lubricating oil composition not within the ranges specified above for the functionalized polymer, the higher molecular weight PIBSA-PAM, the lower molecular weight PIBSA-PAM, the overbased magnesium containing detergent, the overbased calcium containing detergent, and the one or more zinc hydrocarbyl diphosphate compounds.
[0196] Concentrates may be present in the lubricating oil compositions of the instant disclosure at from of 0.5 mass % to 35 mass %, such as 5 mass % to 30 mass %, such as 7.5 mass % to 25 mass %, such as 10 to 22.5 mass %, such as 15 to 20 mass %, such as 12 to 20 mass % based upon the mass of the lubricating oil composition.
[0197] Optionally, the concentrate may be absent functionalized oil.
[0198] In embodiments, the concentrate composition may optionally be absent solvent (such as aliphatic or aromatic solvent) and/or absent functionalized base oil.
[0199] Optionally, the concentrate may be absent phenolic antioxidant.
[0200] In embodiments, the concentrate may be substantially free of or absent aminic antioxidant, such as diphenylamine, such as di (nonylphenyl) amine.
[0201] In embodiments, the concentrate may comprise from 200 to 2000 ppm, or 500 to 1500 ppm, or 1000 to 1300 ppm boron. Alternately, the concentrate may be absent boron.
[0202] In embodiments, the concentrate may comprise less than or equal to 20 (such as 15, such as 10, such as 5, such as 3, such as 1) mass %, functionalized (such as aminated) polybutene (such as polyisobutylene), such as PIBSA-PAM.
[0203] In embodiments, the concentrate may comprise acylated polymers, such as polyisobutylene succinic acid, optionally, having an Mn of 500 to 50,000 g/mol, such as 600 to 5,000 g/mol, such as 700 to 3000 g/mol. In embodiments, the concentrate may comprise acylated polymers, such as polyisobutylene succinic acid, having an Mn of 500 1600 g/mol, such as 700 to 1200 g/mol.
[0204] In embodiments, the concentrate may comprise 20 (such as 15, such as 10, such as 5, such as 3, such as 1) mass % or less block copolymer, such as block, star, random, and/or tapered block copolymer.
[0205] In embodiments, the concentrate may be substantially free of or absent block copolymer, such as block, star, random, and/or tapered block copolymer.
[0206] In embodiments, the concentrate may comprise 20 mass % or less (such as 15 mass % or less, such as 10 mass % or less, such as 5 mass % or less, such as 3 mass % or less, such as 1) mass % or less styrenic copolymer, such as block, star, random, and/or tapered styrenic block copolymer).
[0207] In embodiments, the concentrate may be substantially free of or absent styrenic copolymer, such as block, star, random, and/or tapered styrenic block copolymer).
[0208] In embodiments, the concentrate may comprise less than 20 (such as less than 15, such as 10, such as less than 5, such as less than 3, such as 1) mass % of functionalized diluent, such as functionalized oil.
[0209] In embodiments, the concentrate may substantially free of or absent functionalized diluent, such as functionalized oil.
[0210] In embodiments, the concentrate may comprise less than 0.5 (such as less than 0.4, such as less than 0.3, such as less than 0.2, such as 0.1, substantially absent, no) wt %, based upon the weight of the concentrate, of secondary hydrocarbyl amine compounds and tertiary hydrocarbyl amine compounds.
[0211] In embodiments, the concentrate may be substantially absent, or may comprise no, secondary hydrocarbyl amine compounds and tertiary hydrocarbyl amine compounds.
[0212] In embodiments, the concentrate may have a kinematic viscosity at 100 C. of less than 1000 cSt, such as less than 500 cSt, such as less than 200 cSt.
[0213] In embodiments, the concentrate including the one or more of the functionalized polymers may further include a non-ionic fatty alcohol ethoxylate at from 1.0 to 20 wt. % of the one or more functionalized polymers.
[0214] This disclosure also relates to methods of making concentrate compositions comprising combining: from 1 to less than or equal to 50 wt. % of one or more base oils; from 1 to 30 wt. %, such as 2 to 20 wt. %, based upon the weight of the concentrate, of one or more functionalized polymers, wherein the one or more functionalized polymers comprise a partially or fully saturated olefin homopolymer or copolymer backbone and at least one functional group, having: i) an Mn of 10,000 g/mol or more (GPC-PS) of the polymer prior to functionalization, ii) where the functional group is derived from an acylating agent and a compound containing amino and/or hydroxyl groups (including but not limited to where the polymer is functionalized with an acylating agent and subsequently reacted with a compound containing amino and/or hydroxyl groups), and, iii) wherein the homopolymer or copolymer backbone is derived from monomers selected from the group consisting of C2 to C30 linear alpha olefins, and C4 to C20 conjugated dienes; from 1 to 20 wt. % of an overbased magnesium based detergent with a Total Base Number (KOH/g) greater than or equal to 9 and less than or equal to 500; from 1 to 20 wt. % of an overbased calcium based detergent with a Total Base Number (KOH/g) greater than or equal to 9 and less than or equal to 500; from 2 to 40 wt. % of one or more, optionally borated, higher molecular weight polyisobutylene succinimide (PIBSA-PAM) dispersant (Mn 1600 g/mol or more), and one or more, optionally borated, lower molecular weight polyisobutylene succinimide (PIBSA-PAM) dispersant (Mn less than 1600 g/mol); and from 2 to 20 wt. % of one or more zinc hydrocarbyl diphosphate compounds.
Lubricating Oil Composition Components and Concentrate Components
A. Base Oil Component
[0215] The base oil (also referred to as base stock, lubricating oil basestock, or oil of lubricating viscosity) useful herein may be a single oil or a blend of oils, and is typically a large liquid constituent of a lubricating composition, also referred to as a lubricant, into which additives and optional additional oils are blended, for example, to produce a lubricating composition, such as a final lubricant composition, a concentrate, or other lubricating composition.
[0216] A base oil may be selected from vegetable, animal, mineral, and synthetic lubricating oils, and mixtures thereof. It may range in viscosity from light distillate mineral oils to heavy lubricating oils, such as those for gas engine oil, mineral lubricating oil, motor vehicle oil, and heavy-duty diesel oil. Generally, the kinematic viscosity at 100 C. (KV100) of the base oil ranges from 1 to 30, such as 2 to 25 cSt, such as 5 to 20 cSt, as determined according to ASTM D445-19a, in particular, from 1.0 cSt to 10 cSt, from 1.5 cSt to 3.3 cSt, from 2.7 cSt to 8.1 cSt, from 3.0 cSt to 7.2 cSt, or from 2.5 cSt to 6.5 cSt. Generally, the high temperature high shear (HTHS) viscosity at 150 C. of the base oil ranges from 0.5 to 20 cP such as 1 to 10 cP, such as 2 to 5 cP as determined according to ASTM D4683-20.
[0217] Typically, when lubricating oil basestock(s) is used to make a concentrate, it may advantageously be present in a concentrate-forming amount to give a concentrate containing, from 5 wt % to 80 wt %, from 10 wt % to 70 wt %, or from 5 wt % to 50 wt % of active ingredient, based upon the weight of the concentrate.
[0218] Common oils useful as base oils include animal and vegetable oils (e.g., castor and lard oil), liquid petroleum oils, and hydrorefined and/or solvent-treated mineral lubricating oils of the paraffinic, naphthenic, and mixed paraffinic-naphthenic types. Oils derived from coal or shale are also useful base oils. Base stocks may be manufactured using a variety of different processes including, but not limited to, distillation, solvent refining, hydrogen processing, oligomerization, esterification, and re-refining.
[0219] Synthetic lubricating oils useful herein as base oils include hydrocarbon oils such as homopolymerized and copolymerized olefins, referred to as polyalphaolefins or PAO's or group IV base oils [according to the API EOLCS 1509 definition (American Petroleum Institute Publication 1509, see section E.1.3, 19.sup.th edition, January 2021, www.API.org)]. Examples of PAO's useful as base oils include: poly(ethylenes), copolymers of ethylene and propylene, polybutylenes, polypropylenes, propylene-isobutylene copolymers, chlorinated polybutylenes, poly(1-hexenes), poly(1-octenes), poly(1-decenes), homo- or co-polymers of C.sub.8 to C.sub.20 alkenes, homo- or co-polymers of C.sub.8, and/or C.sub.10, and/or C.sub.12 alkenes, C.sub.8/C.sub.10 copolymers, C.sub.8/C.sub.10/C.sub.12 copolymers, and C.sub.10/C.sub.12 copolymers, and the derivatives, analogues and homologues thereof.
[0220] In another embodiment, the base oil may comprise polyalphaolefins comprising oligomers of linear olefins having 6 to 14 carbon atoms, more preferably 8 to 12 carbon atoms, more preferably 10 carbon atoms having a Kinematic viscosity at 100 C. of 10 or more (as measured by ASTM D445); and preferably having a viscosity index (VI), as determined by ASTM D2270, of 100 or more, preferably 110 or more, more preferably 120 or more, more preferably 130 or more, more preferably 140 or more; and/or having a pour point of 5 C. or less (as determined by ASTM D97), more preferably 10 C. or less, more preferably 20 C. or less.
[0221] In another embodiment polyalphaolefin oligomers useful in the present disclosure may comprise C.sub.20 to C.sub.1500 paraffins, preferably C.sub.40 to C.sub.1000 paraffins, preferably C.sub.50 to C.sub.750 paraffins, preferably C.sub.50 to C.sub.500 paraffins. The PAO oligomers are dimers, trimers, tetramers, pentamers, etc., of C.sub.5 to C.sub.14 alpha-olefins in one embodiment, and C.sub.6 to C.sub.12 alpha-olefins in another embodiment, and C.sub.8 to C.sub.12 alpha-olefins in another embodiment. Suitable olefins include 1-pentene, 1-hexene, 1-heptene, 1-octene, 1-nonene, 1-decene, 1-undecene, and 1-dodecene. In one embodiment, the olefin is a combination of 1-octene, 1-decene, and 1-dodecene, or alternately may be substantially 1-decene, and the PAO is a mixture of dimers, trimers, tetramers, and pentamers (and higher) thereof. Useful PAO's are described more particularly in, for example, U.S. Pat. Nos. 5,171,908 and 5,783,531, and in Synthetic Lubricants and High-Performance Functional Fluids 1-52 (Leslie R. Rudnick & Ronald L. Shubkin, ed. Marcel Dekker, Inc. 1999).
[0222] PAO's useful in the present disclosure typically possess a number average molecular weight of from 100 to 21,000 g/mol in one embodiment, and from 200 to 10,000 g/mol in another embodiment, and from 200 to 7,000 g/mol in yet another embodiment, and from 200 to 2,000 g/mol in yet another embodiment, and from 200 to 500 g/mol in yet another embodiment. Desirable PAO's are commercially available as SpectraSyn Hi-Vis, SpectraSyn Low-Vis, SpectraSyn plus, SpectraSyn Elite PAO's (ExxonMobil Chemical Company, Houston Texas) and Durasyn PAO's from Ineos Oligomers USA LLC.
[0223] Synthetic lubricating oils useful as base oils also include hydrocarbon oils such as homopolymerized and copolymerized: alkylbenzenes (e.g., dodecylbenzenes, tetradecylbenzenes, dinonylbenzenes, di(2-ethylhexyl)benzenes); polyphenols (e.g., biphenyls, terphenyls, alkylated polyphenols); and alkylated diphenyl ethers, and alkylated diphenyl sulfides; and the derivatives, analogues, and homologues thereof.
[0224] Another suitable class of synthetic lubricating oils useful as base oils comprises the esters of dicarboxylic acids (e.g., phthalic acid, succinic acid, alkyl succinic acids and alkenyl succinic acids, maleic acid, azelaic acid, suberic acid, sebasic acid, fumaric acid, adipic acid, linoleic acid dimer, malonic acid, alkylmalonic acids, alkenyl malonic acids) reacted with a variety of alcohols (e.g., butyl alcohol, hexyl alcohol, dodecyl alcohol, 2-ethylhexyl alcohol, ethylene glycol, diethylene glycol monoether, propylene glycol). Specific examples of these esters include dibutyl adipate, di(2-ethylhexyl) sebacate, di-n-hexyl fumarate, dioctyl sebacate, diisooctyl azelate, diisodecyl azelate, dioctyl phthalate, didecyl phthalate, dieicosyl sebacate, the 2-ethylhexyl diester of linoleic acid dimer, and the complex ester formed by reacting one mole of sebacic acid with two moles of tetraethylene glycol and two moles of 2-ethylhexanoic acid.
[0225] Esters useful as synthetic oils herein also include those made from C.sub.5 to C.sub.12 monocarboxylic acids and polyols, and polyol ethers such as neopentyl glycol, trimethylolpropane, pentaerythritol, dipentaerythritol, and tripentaerythritol.
[0226] Desirable ester base oils are commercially available as Esterex Esters (ExxonMobil Chemical Company, Houston, Texas).
[0227] Silicon-based oils such as the polyalkyl-, polyaryl-, polyalkoxy- or polyaryloxysilicone oils and silicate oils comprise another useful class of synthetic lubricants useful herein; such oils include tetraethyl silicate, tetraisopropyl silicate, tetra-(2-ethylhexyl) silicate, tetra-(4-methyl-2-ethylhexyl)silicate, tetra-(p-tert-butyl-phenyl) silicate, hexa-(4-methyl-2-ethylhexyl)disiloxane, poly(methyl)siloxanes, and poly(methylphenyl)-siloxanes.
[0228] Other synthetic lubricating oils useful herein include liquid esters of phosphorous-containing acids (e.g., tricresyl phosphate, trioctyl phosphate, diethyl ester of decylphosphonic acid) and polymeric tetrahydrofurans.
[0229] Unrefined, refined, and re-refined oils can be used in the lubricating compositions of the present disclosure. Unrefined oils are those obtained directly from a natural or synthetic source without further purification treatment. For example, a shale oil obtained directly from retorting operations, a petroleum oil obtained directly from distillation, or an ester oil obtained directly from an esterification process and used without further treatment is considered an unrefined oil. Refined oils are similar to the unrefined oils except they have been further treated in one or more purification steps to improve one or more properties. Many such purification techniques, such as distillation, solvent extraction, acid or base extraction, filtration, and percolation are used by those in the art. Re-refined oils are oils obtained by processes similar to those used to obtain refined oils where the refining processes are applied to previously refined oils which have been previously used in service. Such re-refined oils are also referred to as reclaimed or reprocessed oils and often are additionally processed for removal of spent additive and oil breakdown products. A re-refined base oil is preferably substantially free from materials introduced through manufacturing, contamination, or previous use.
[0230] Other examples of useful base oils are gas-to-liquid (GTL) base oils, i.e., the base oil is an oil derived from hydrocarbons made from synthesis gas (syn gas) containing H2 and CO using a Fischer-Tropsch catalyst. These hydrocarbons typically require further processing in order to be useful as a base oil. For example, they may, by methods known in the art, be hydroisomerized; hydrocracked and hydroisomerized; dewaxed; or hydroisomerized and dewaxed. For further information on useful GTL base oils and blends thereof, please see U.S. Pat. No. 10,913,916 (col 4, ln 62 to col 5, ln 60) and U.S. Pat. No. 10,781,397 (col 14, ln 54 to col 15, ln 5, and col 16, ln 44 to col 17, ln 55).
[0231] In particular, oils from renewable sources, i.e., based in part on carbon and energy captured from the environment, such as biological sources, are useful herein.
[0232] The various base oils are often categorized as Group I, II, III, IV, or V according to the API EOLCS 1509 definition (American Petroleum Institute Publication 1509, see section E.1.3, 22 ns edition, October 2023, www.API.org). Generally speaking, Group I base stocks have a viscosity index of between about 80 to 120 and contain greater than about 0.03% sulfur and/or less than about 90% saturates. Group II base stocks have a viscosity index of between about 80 to 120 and contain less than or equal to about 0.03% sulfur and greater than or equal to about 90% saturates. Group III base stocks have a viscosity index greater than about 120 and contain less than or equal to about 0.03% sulfur and greater than about 90% saturates. Group IV base stocks include polyalphaolefins (PAO). Group V base stocks include base stocks not included in Groups I-IV. (Viscosity index measured by ASTM D 2270, saturates is measured by ASTM D2007, and sulfur is measured by ASTM D5185, D2622, ASTM D4294, ASTM D4927, and ASTM D3120).
[0233] Base oils for use in the formulated lubricating compositions useful in the present disclosure are any one, two, three, or more of the variety of oils described herein. In desirable embodiments, base oils for use in the formulated lubricating compositions useful in the present disclosure are those described as API Group I (including Group I+), Group II (including Group II+), Group III (including Group III+), Group IV, and Group V oils and mixtures thereof, preferably API Group II, Group III, Group IV, and Group V oils and mixtures thereof. The base oil may be a Group III, Group III+, IV, and Group V base oils due to their exceptional volatility, stability, viscometric, and cleanliness features. Minor quantities of Group I basestock, such as the amount used to dilute additives for blending into formulated lube oil products, can be tolerated but are typically kept to a minimum, e.g., amounts only associated with their use as diluent/carrier oil for additives used on an as-received basis. In regard to the Group II stocks, it is often more useful that the Group II base stock be in the higher quality range associated with that stock, i.e., a Group II stock having a viscosity index in the range from 100 to 120.
[0234] The base oil useful herein may be selected from any of the synthetic, natural, or re-refined oils (such as those typically used as crankcase lubricating oils for spark-ignited and compression-ignited engines). Mixtures of synthetic and/or natural and/or re-refined base oils may be used if desired. Multi-modal mixtures (such as bi- or tri-modal mixtures) of Group I, II, III, IV, and/or V base stocks may be used if desired.
[0235] The base oil or base oil blend used herein conveniently has a kinematic viscosity at 100 C. (KV100, as measured according to ASTM D445-19a, and reported in units of centistoke (cSt) or it its equivalent, mm2/s), of about 2 to about 40 cSt, alternately of 3 to 30 cSt, alternately 4 to 20 cSt at 100 C., alternately 5 to 10 cSt, alternately the base oil or base oil blend may have a kinematic viscosity at 100 C. of 2 to 20 cSt, of 2.5 to 12 cSt, and preferably of about 2.5 cSt to about 9 cSt.
[0236] The base oil or base oil blend preferably has a saturate content of at least 65 mass %, more preferably at least 75 mass %, such as at least 85 mass %, such as at least than 90 mass % as determined by ASTM D2007.
[0237] Preferably, the base oil or base oil blend will have a sulfur content of less than 1 mass %, preferably less than 0.6 mass %, most preferably less than 0.4 mass %, such as less than 0.3 mass based on the total mass of the lubricating composition, as measured by ASTM D5185.
[0238] In embodiments, the volatility of the base oil or base oil blend, as measured by the Noack test (ASTM D5800, procedure B), is less than or equal to 30 mass %, such as less than or equal to 25 mass %, such as less than or equal to 20 mass %, such as less than or equal to 16 mass %, such as less than or equal to 12 mass %, such as less than or equal to 10 mass %, based on the total mass of the lubricating composition.
[0239] In embodiments, the viscosity index (VI) of the base oil is at least 95, preferably at least 110, more preferably at least 120, even more preferably at least 125, most preferably from about 95 to 145, in particular from about 100 to 135 (as determined by ASTM D2270).
[0240] The base oil may be provided in a major amount, in combination with a minor amount of one or more additive components as described hereinafter, constituting a lubricant. This preparation may be accomplished by adding the additives directly to the oil or by adding the one or more additives in the form of a concentrate thereof to disperse or dissolve the additive(s). Additives may be added to the oil by any method known to those skilled in the art, either before, at the same time as, or after addition of other additives.
[0241] The base oil may be provided in a minor amount, in combination with minor amounts of one or more additive components as described hereinafter, constituting an additive concentrate. This preparation may be accomplished by adding the additives directly to the oil or by adding the one or more additives in the form of a solution, slurry or suspension thereof to disperse or dissolve the additive(s) in the oil. Additives may be added to the oil by any method known to those skilled in the art, either before, at the same time as, or after addition of other additives.
[0242] The base oil typically constitutes the major component of an engine oil lubricant composition of the present disclosure and typically is present in an amount ranging from about 50 to about 99 wt %, preferably from about 60 to about 95 wt %, preferably from about 70 to about 95 wt %, and more preferably from about 80 to about 95 wt %, based on the total weight of the composition.
[0243] Typically, one or more base oils are present in the lubricating composition in an amount of 32 wt % or more, alternately 55 wt % or more, alternately 60 wt % or more, alternately 65 wt % or more, based on the total weight of the lubricating composition. Typically, one or more base oils are present in the lubricating composition at an amount of 98 wt % or less, more preferably 95 wt % or less, even more preferably 90 wt % or less. Alternately, one or more base oils are present in the lubricating composition at from 1 to 99 mass %, alternately 50 to 97 mass %, alternately to 60 to 95 mass alternately 70 to 95 mass %, based upon the weight of the lubricating composition.
[0244] The base oils and blends thereof described above are also useful for making concentrates as well as for making lubricants therefrom.
[0245] Concentrates constitute a convenient means of handling additives before their use, as well as facilitating solution or dispersion of additives in lubricants. When preparing a lubricant that contains more than one type of additive (sometime referred to as additive components), each additive may be incorporated separately, each in the form of a concentrate. In many instances, however, it is convenient to provide a so-called additive package (also referred to as an addpack) comprising one or more additives/co-additives, such as described hereinafter, in a single concentrate.
[0246] Typically, one or more base oils are present in the concentrate composition in an amount of 50 wt % or less, alternately 40 wt % or less, alternately 30 wt % or less, alternately 20 wt % or less, based on the total weight of the concentrate composition. Typically, one or more base oils are present in the concentrate composition at an amount of 0.1 to 49 mass %, alternately 1 to 40 mass %, alternately 5 to 40 mass %, alternately to 10 to 30 mass %, alternately 15 to 25 mass %, based upon the weight of the concentrate composition.
[0247] In one form of the lubricating oil compositions disclosed herein, the compositions may comprise a Group I, Group II base oil, a Group III base oil, a Group IV base oil (preferably a Group II base oil, a Group III base oil, a Group IV base oil), or combinations thereof. In another form of the lubricating oil compositions disclosed herein, the compositions may comprise a Group II base oil, and is substantially free of the Group III base oil and the Group IV base oil.
B. Functionalized Polymer Component
i. F-OCP Functionalized Polymers
[0248] This disclosure relates to a functionalized polymer comprising a polymer that prior to functionalization has an Mn of about 10,000 g/mol or more, such as 20,000 g/mol or more, such as 25,000 g/mol or more, such as 30,000 g/mol or more, such as 35,000 g/mol or more (GPC-PS). Alternately, functionalized polymer comprises a polymer that prior to functionalization has an Mn of 10,000 to 300,000 g/mol, such as 20,000 to about 150,000 g/mol, such as 30,000 to about 125,000 g/mol, such as 35,000 to about 100,000 g/mol, such as 40,000 to 80,000 g/mol (GPC-PS). The polymer prior to functionalization may have an Mw/Mn of less than 2 (such as less than 1.6, such as less than 1.5, such as 1.4 or less, such as from 1 to 1.3, such as from 1.0 to 1.25, such as from 1.0 to 1.2, such as 1.0 to 1.15, such as from 1.0 to 1.1 as determined by GPC-PS). The polymer prior to functionalization may comprise repeat units of one or more olefins having 4 to 5 carbon atoms (preferably conjugated dienes having 4 to 5 carbon atoms) or comprise one or more C.sub.2 to C.sub.20 (such as C.sub.2 to C.sub.12, cush as C.sub.2 to C.sub.6) linear alpha olefins (such as ethylene and or propylene). Prior to functionalization the polymer (such as a C.sub.4-5 polymer or a copolymer of ethylene and or propylene) is preferably fully or partially saturated (such as fully or partially hydrogenated). The functionalized polymer may be obtained by reacting the polymer with an acylating agent to form acylated polymer and then reacting acylated polymer with an amine or alcohol to form an amide, imide, ester, or combination thereof. The functionalized polymer may also be obtained by reacting an acylated polymer (such as a commercially available maleated fully or partially hydrogenated C.sub.4-5 polymer, or a maleated olefin copolymer of ethylene and propylene) with an amine to form an amide, imide or combination thereof.
[0249] This disclosure further relates to amide, imide, and/or ester functionalized saturated (such as hydrogenated) polymers of C.sub.4-5 conjugated dienes described herein obtained by reacting fully or partially saturated (such as fully or partially hydrogenated) polymers of C.sub.4-5 conjugated dienes having an Mw/Mn of less than 2, with an acylating agent, such as maleic acid or maleic anhydride and thereafter reacting the acylated polymer with an amine (such as a polyamine) to form an imide, amide or combination thereof.
[0250] This disclosure further relates to amide, imide, and/or ester functionalized saturated (such as hydrogenated) polymers of C.sub.2 to C.sub.20 alpha olefins (such as C.sub.2 to C.sub.12 linear alpha olefins, such as ethylene and propylene homopolymers and copolymers) described herein obtained by reacting fully or partially saturated (such as fully or partially hydrogenated) polymers of C.sub.2-20 alpha olefins having an Mw/Mn of less than 3 (preferably less than 2), with an acylating agent, such as maleic acid or maleic anhydride and thereafter reacting the acylated polymer with an amine (such as a polyamine) to form an imide, amide or combination thereof.
[0251] This disclosure relates to polymers containing one or more pendant amine groups and comprising or resulting from the admixing of: at least partially (preferably completely) hydrogenated C.sub.4-5 olefin polymers and or C.sub.2-20 polymers (such as copolymers of ethylene and propylene) with an acylating agent, such as maleic acid or maleic anhydride, and thereafter reacting the acylated polymer with a polyamine to form an imide, amide or combination thereof.
[0252] In embodiments, the functionalized polymer is not prepared in aromatic solvent (such as benzene or toluene), or aromatic solvent is present at 2 wt % or less (such as 1 wt % or less, such as 0.5 wt % or less), based upon the weight of solvent, diluent, and polymer.
[0253] In embodiments, the functionalized polymer is not prepared in an alkylated naphthylenic solvent, or alkylated naphthylenic solvent is present at 5 wt % or less (such as 3 wt % or less, such as 1 wt % or less), based upon the weight of solvent, diluent, and polymer.
[0254] In embodiments, the polymer useful herein to prepare the functionalized polymer may be a homopolymer of a C.sub.2 to C.sub.20 alpha olefin (such as a homopolymer or copolymer of ethylene, propylene, butene, pentene, hexene, heptene, octene, nonene, decene, undecene, dodecene, and the like, such as a copolymer of ethylene and propylene).
[0255] The polymer useful herein to prepare the functionalized polymer may be a homopolymer of butadiene, isoprene, or the like.
[0256] In embodiments, the polymer useful herein to prepare the functionalized polymer may be a homopolymer of isoprene, or a copolymer of isoprene and less than 5 mol % (such as less than 3 mol %, such as less than 1 mol %, such as less than 0.1 mol %) comonomer.
[0257] The polymer useful herein to prepare the functionalized polymer may be copolymer of isoprene and one or more of styrene, methyl-styrene, 2,3-dimethyl-butadiene, 2-methyl-1,3-pentadiene, myrcene, 3-methyl-1,3-pentadiene, 4-methyl-1,3-pentadiene, 2-phenyl-1,3-butadiene, 2-phenyl-1,3-pentadiene, 3-phenyl-1,3 pentadiene, 2,3-dimethyl-1,3-pentadiene, 2-hexyl-1,3-butadiene, 3-methyl-1,3-hexadiene, 2-benzyl-1,3-butadiene, 2-p-tolyl-1,3-butadiene 1,3-butadiene, 1,3-pentadiene, 1,3-hexadiene, 1,3-heptadiene, 2,4-heptadiene, 1,3-octadiene, 2,4-octadiene, 3,5-octadiene, 1,3-nonadiene, 2,4-nonadiene, 3,5-nonadiene, 1,3-decadiene, 2,4-decadiene, and 3,5-decadiene, [optionally the comonomer(s) are present at less than 20 mol %, less than 5 mol %, such as less than 3 mol %, such as less than 1 mol %, such as less than 0.1 mol %].
[0258] Generally, the polymerized conjugated diene polymer useful herein to prepare the functionalized polymer includes a mixture of 1,4- and 1,2-insertions (a.k.a. 2,1-insertions; for butadiene, 1,2-insertions are the same as 3,4-insertions). As measured by 1H NMR, the polymerized conjugated diene polymer useful herein to prepare the functionalized polymer contains at least about 50% of 1,4-insertions, such as at least about 75% of 1,4 insertions, such as at least about 80% of 1,4 insertions, such as at least about 90% of 1,4 insertions, such as at least about 95% of 1,4 insertions, such as at least 98% of 1,4 insertions, based upon the total of the 2,1 insertions, 1,4 insertions, and 3,4 insertions of isoprene. For purposes of this disclosure: 1) the phrase 1,4 insertion includes 1,4 and 4,1 insertions, 2) the phrase 2,1 insertion includes 2,1 and 1,2 insertions, and 3) the phrase 3,4 insertion includes 3,4 and 4,3 insertions.
[0259] Optionally, styrene repeat units may be absent in the polymer useful herein to prepare the functionalized polymer. Optionally, styrene repeat units may be absent in the functionalized hydrogenated/saturated polymers.
[0260] Optionally, butadiene repeat units may be absent in the polymer useful herein to prepare the functionalized polymer. Optionally, butadiene repeat units may be absent in the functionalized hydrogenated/saturated polymers.
[0261] Optionally, the polymer useful herein to prepare the functionalized polymer may be not homopolybutylene. Optionally, the functionalized hydrogenated/saturated polymer may be not homopolybutylene.
[0262] Optionally, the polymer useful herein to prepare the functionalized polymer may be not homopolyisobutylene. Optionally, the functionalized hydrogenated/saturated polymer may be not homopolyisobutylene.
[0263] Optionally, the polymer useful herein to prepare the functionalized polymer may not be a copolymer of isoprene and butadiene. Optionally, the functionalized hydrogenated/saturated polymer may not be a copolymer of isoprene and butadiene.
[0264] The polymer useful herein to prepare the functionalized polymer may be copolymer of C.sub.2 to C.sub.20 alpha olefin, such as C.sub.2 to C.sub.12 alpha olefin (such as a homopolymer or copolymer of ethylene, propylene, butene, pentene, hexene, heptene, octene, nonene, decene, undecene, dodecene, and the like, such as a copolymer of ethylene and propylene).
[0265] The polymer useful herein to prepare the functionalized polymer and/or the functionalized polymer may be homopolymer or copolymer. The copolymer may be a random copolymer, a tapered block copolymer, a star copolymer, or a block copolymer. Block copolymers are formed from a monomer mixture comprising one or more first monomers (such as isobutylene), wherein, for example, a first monomer forms a discrete block of the polymer joined to a second discrete block of the polymer formed from a second monomer (such as butadiene). While block copolymers have substantially discrete blocks formed from the monomers, a tapered block copolymer may be composed of, at one end, a relatively pure first monomer and, at the other end, a relatively pure second monomer. The middle of the tapered block copolymer may be more of a gradient composition of the two monomers.
[0266] The polymer useful herein to prepare the functionalized polymer may typically have an Mn of 10,000 to 150,000 g/mol, alternately 20,000 to 150,000 g/mol, alternately 20,000 to about 150,000 g/mol, alternately 30,000 to about 125,000 g/mol, alternately 35,000 to about 100,000 g/mol, alternately 40,000 to 80,000 g/mol (GPC-PS).
[0267] Polymers useful herein to prepare the functionalized polymers may typically have an Mw/Mn (as determined by GPC-PS) of 1 to 2, alternately greater than 1 to less than 2, alternately 1.1 to 1.8, alternately 1.2 to 1.5. Alternately, the polymers useful herein to prepare the functionalized polymers may typically have an Mw/Mn of 1 or greater than 1 to less than 2 (such as less than 1.8, such as less than 1.7, such as less than 1.6, such as less than 1.5, such as less than 1.4, such as less than 1.3, such as less than 1.2, such as less than 1.15, such as less than 1.12, such as less than 1.10).
[0268] The polymers used to prepare the functionalized polymers may have an Mz (as determined by GPC-PS) of 20,000 to 150,000 g/mol, alternately 20,000 to about 150,000 g/mol, alternately 30,000 to about 125,000 g/mol, alternately 35,000 to about 100,000 g/mol, alternately 40,000 to 80,000 g/mol, alternately 40,000 to 60,000 g/mol (GPC-PS).
[0269] Polymers useful herein to prepare the functionalized polymers may have a glass transition temperature (Tg) of 25 C. or less, such as 40 C. or less, such as 50 C. or less, as determined by Differential Scanning calorimetry (DSC) using a Perkin Elmer or TA Instrument Thermal Analysis System (sample is heated from ambient to 210 C. at 10 C./minute and held at 210 C. for 5 minutes, then cooled down to 40 C. at 10 C./minute and held for 5 minutes.)
[0270] Polymers useful herein to prepare the functionalized polymers typically have a residual unsaturation of less than 3%, such less than 2%, such less than 1%, such as less than 0.5%, such as less than 0.25% based upon number of double bonds in the non-hydrogenated polymer.
[0271] Polymers useful herein to prepare the functionalized polymers typically have a residual metal (such as Li, Co, and Al) content of less than 100 ppm, such less than 50 ppm, such as less than 25 ppm, such as less than 10 ppm, such as less than 5 ppm.
Hydrogenation
[0272] The C.sub.4-5 polymers and or C.sub.2-20 linear alpha olefin polymers useful herein to prepare the functionalized polymer can be hydrogenated partially or completely by any hydrogenating agent known to one of ordinary skill in the art. For example, a saturated or partially saturated polymer can be prepared by (a) providing a C.sub.4-5 polymer and or a C.sub.2-20 linear alpha olefin polymer containing unsaturations (such as double or triple bonds); and (b) hydrogenating at least a portion or all of the unsaturations (such as double or triple bonds) in the polymer in the presence of a hydrogenation reagent. In some embodiments, the polymer is fully hydrogenated. In some embodiments, the polymer is partially hydrogenated. In some embodiments, the polymer is saturated (hydrogenated) at 50% or more, such as 60% or more, such as 70% or more, such as 80% or more, such as 90% or more, such as 95% or more, such as 98% or more, such as 99% or more, such as from 50 to 100% saturated (hydrogenated), as determined by ozone adsorption method described in Martino N. Smits and Dirkman Hoefman, Quantative Determination of Olefinic Unsaturation by Measurement of Ozone Absorption Analytical Chemistry Vol 44, No. 9, pg. 1688, 1972, Martino N. Smits.
[0273] In embodiments, the hydrogenation reagent can be hydrogen in the presence of a hydrogenation catalyst. In some embodiments, the hydrogenation catalyst is Pd, Pd/C, Pt, PtO.sub.2, Ru(PPh.sub.3).sub.2Cl.sub.2, Raney nickel, or a combination thereof. In embodiments, the catalyst is a Pd catalyst. In another embodiment, the catalyst is 5% Pd/C. In a further embodiment, the catalyst may comprise or be 10% Pd/C in a high-pressure reaction vessel and the hydrogenation reaction is allowed to proceed until completion. Generally, after completion, the reaction mixture can be washed, concentrated, and dried to yield the corresponding hydrogenated product. Alternatively, any reducing agent that can reduce a CC double bond to a CC single bond can also be used. For example, the olefin polymer can be hydrogenated by treatment with hydrazine in the presence of a catalyst, such as 5-ethyl-3-methyllumiflavinium perchlorate, under an oxygen atmosphere to give the corresponding hydrogenated products. The reduction reaction with hydrazine is disclosed in Imada et al., J Am. Chem. Soc., 127, pp. 14544-14545, (2005), which is incorporated herein by reference.
Acylation
[0274] The fully or partially saturated (hydrogenated) polymer may be chemically modified (functionalized) to provide a polymer having at least one polar functional group, such as, but not limited to, halogen, epoxy, hydroxy, amino, nitrilo, mercapto, imido, carboxy, and sulfonic acid groups of combinations thereof. The functionalized polymers can be further modified to give a more desired type of functionality. In a preferred case, the fully or partially hydrogenated polymer is functionalized by a method, which includes reacting the fully or partially hydrogenated polymer with an unsaturated carboxylic acid (or derivative thereof, such as maleic anhydride) to provide an acylated polymer (which may then be further functionalized as described below).
[0275] In some embodiments, a carboxylic acid functionality or a reactive equivalent thereof is grafted onto the polymer to form an acylated polymer. An ethylenically unsaturated carboxylic acid material is typically grafted onto the polymer backbone. These materials which are attached to the polymer typically contain at least one ethylenic bond (prior to reaction) and at least one, such as two, carboxylic acid (or its anhydride) groups or a polar group which is convertible into said carboxyl groups by oxidation or hydrolysis. Maleic anhydride or a derivative thereof is suitable. It grafts onto the polymer, to give two carboxylic acid functionalities. Examples of additional unsaturated carboxylic materials include itaconic anhydride, or the corresponding dicarboxylic acids, such as maleic acid, fumaric acid and their esters, as well as cinnamic acid and esters thereof.
[0276] The ethylenically unsaturated carboxylic acid material may be grafted onto the polymer in a number of ways. It may be grafted onto the polymer in solution or in essentially pure (molten) form with or without using a radical initiator. Free-radical induced grafting of ethylenically unsaturated carboxylic acid materials may also be conducted in solvents, such as hexane or mineral oil. It may be carried out at an elevated temperature in the range of 100 C. to 250 C., e.g., 120 C. to 190 C., or 150 C. to 180 C., e.g., above 160 C.
[0277] The free-radical initiators which may be used include peroxides, hydroperoxides, and azo compounds, typically those which have a boiling point greater than about 100 C. and which decompose thermally within the grafting temperature range to provide free radicals. Representative of these free-radical initiators include azobisisobutyronitrile and 2,5-dimethyl-hex-3-yne-2,5-bis-tertiary-butyl peroxide. The initiator may be used in an amount of 0.005% to 1% by weight based on the weight of the reaction mixture solution. The grafting may be carried out in an inert atmosphere, such as under nitrogen blanketing. The resulting acylated polymer intermediate is characterized by having carboxylic acid acylating functions as a part of its structure.
[0278] In embodiments, the acylated polymer may have 2 or more anhydride groups per polymer molecule and may exhibit less than 10% gel. Alternately, the acylated polymer may have less than 2 anhydride groups per polymer molecule and may exhibit less than 10% gel. (See also col 17, ln 14-col 18, ln 11 of U.S. Pat. No. 5,429,758).
[0279] Alternately, in some embodiments, the acylated polymer may have a gel content of less than about 5 wt %, less than 3 wt %, less than 2 wt %, less than 1 wt %, less than 0.5 wt %, less than 0.1 wt %, or 0 wt %, where the gel content is measured by determining the amount of material that is extractable from the polymer by using boiling xylene (or cyclohexane) as an extractant. The percent of soluble and insoluble (gel) material in a polymer composition is determined by soaking a nominally 0.5 mm thick thin film specimen of polymer for 48 hours in cyclohexane at 23 C. or refluxing the thin film specimen in boiling xylene for one half hour, removing the solvent, weighing the dried residue and calculating the amount of soluble and insoluble (gel) material. This method is generally described in U.S. Pat. No. 4,311,628, which is incorporated herein by reference. For purposes of this disclosure, gel content is measured using boiling xylene, unless the sample is not soluble in xylene, then the cyclohexane method is used.
[0280] In embodiments, the acylated polymer may have a Saponification Number (SAP) of 5 g/KOH or more, such as 10 g/KOH or more, such as 20 g/KOH or more, such as 30 g/KOH or more, such as 50 g/KOH or more, such as 10 to 60 g/KOH, such as 20 to 40 g/KOH as determined by ASTM D94.
[0281] In embodiments, the acylated polymer composition may have less than 5 wt % unreacted acylating agent (such as maleic anhydride), such as less than 4 wt %, such as less than 3 wt %, such as less than 1 wt %, such as less than 0.5 wt %, such as less than 0.25 wt %, such as less than 0.1 wt %, based upon the weight of the acylated polymer composition (i.e., polymer, acylating agent, and diluent).
[0282] In embodiments, the acylation reactions described herein may take place in base oil diluent. As a side product, functionalized base oil can be produced. The oil may become acylated itself. For example, maleated base oil may be present after the acylation reactions described herein.
[0283] It is contemplated that the functionalized base oil may comprise the acylated oil and/or the reaction product of the acylated oil with an amine to form an amide, imide or combination thereof.
[0284] Preferably, the acylated oil and/or reaction product of the acylated oil with an amine or alcohol to form an amide, imide, ester, or combination thereof, may be present in a concentrate in an amount of 40 wt % or less, alternately 20 wt % or less, alternately 10 wt % or less, alternately 5 wt % or less, alternately 3 mass % or less, preferably 2 mass % or less, preferably 1 mass % or less, preferably at 0.1 mass % or less, preferably at 0 mass % (such as 0 to 40 mass %, alternately 0.01 to 40 mass/O, alternately 0.1 to 20 mass %, alternately to 1 to 10 mass %, alternately 1.5 to 5 mass %), based upon the weight of the concentrate composition.
[0285] Preferably one or more functionalized base oils, such as acylated oil and/or reaction product of the acylated oil with an amine or alcohol to form an amide, imide, ester, or combination thereof, may be present in the lubricating oil composition at an amount of 0.01 to 40 mass %, alternately 0.1 to 20 mass %, alternately to 1 to 10 mass %, alternately 1.5 to 5 mass %, (such as at 3 mass % or less, preferably 2 mass % or less, preferably 1 mass % or less, preferably at 0.1 mass % or less, preferably at 0 mass %), based upon the weight of the lubricating oil composition.
[0286] In embodiments, the acylation reactions described herein take place in solvent containing media. As a side product, acylated/functionalized solvent can be produced. In embodiments, acylated and/or functionalized solvent may be present in a concentrate composition at 3 mass % or less, preferably 2 mass % or less, preferably 1 mass % or less, preferably at 0.1 mass % or less, preferably at 0 mass %, based upon the weight of the concentrate composition. In embodiments, functionalized solvent may be present in a lubricating oil composition at 3 mass % or less, preferably 2 mass % or less, preferably 1 mass % or less, preferably at 0.1 mass % or less, preferably at 0 mass %, based upon the weight of the lubricating oil composition.
[0287] In embodiments, the acylating agent may be added in such a way as to minimize side reactions (such as reaction with base oil or other diluent present in the reaction vessel).
[0288] In embodiments, the acylating reaction may occur where the acylating agent (such as maleic acid or maleic anhydride) is added in a continuous or semi-continuous (such as intermittent) stream (such as, for example, in controlled relatively equal portions over the reaction time, or larger and/or smaller portions at different points in the reaction) to minimize functionalized base oil and other side reactions. As an example, the acylating agent may be added in a continuous fashion where the amounts of polymer and acylating agents are added in controlled stoichiometric amounts. As another example, the polymer may be added to a reaction vessel in batch fashion and the acylating agent added slowly or in a semi-continuous fashion (such as adding the acylating agent in 2 or more, such as 5 or more, such as 10 or more, such as 20 or more, such as 30 or more, such as 40 or more, such as 50 or more, such as 60 or more discrete amounts or portions). Alternately, the polymer can be added to the reaction vessel in X number of portions and the acylating agent added in 1.5X or more (such as 2X or more, such as 5X or more, such as 10X or more, such as 20X or more, such as 30X or more, such as 40X or more, such as 50X or more, such as 60X or more) number of portions. This same effect may also be achieved by diluting or concentrating a polymer solution and/or the acylating agent solution to the same or different extents.
[0289] Preferably, the acylating agent may be added in such a way as to minimize side reactions, such as in a continuous or semi-continuous fashion.
[0290] The reaction may also be run so as to minimize side reactions by using high concentrations of the polymer in diluent, such as 45 wt % or more, or 50 wt % or more, or 55 wt % or more, or 60 wt % or more in batch, semi-continuous, or continuous reactor operations. For example, the polymer (such as a hydrogenated isoprene polymer, such as hydrogenated homo-polyisoprene) may be introduced into batch, semi-continuous, or continuous reactor operations as solution or suspension (such as a slurry) in diluent (such as oil (e.g., base oil, such as a Group I, II, III, IV, and/or V base oil, such as a Group II and/or Group III base oil) or alkane solvent or diluent or a combination thereof), where the polymer may be present in the solution or suspension at 45 wt % or more (or 50 wt % or more, or 55 wt % or more, or 60 wt % or more), based upon the weight of the polymer and diluent.
[0291] In embodiments, the side reactions may be minimized by: 1) adding the acylating agent in a continuous or semi-continuous fashion, and/or 2) the polymer is introduced into batch, semi-continuous or continuous reactor operations as solution or suspension in diluent where the polymer is present at 45 wt % or more, based upon the weight of the polymer and diluent.
[0292] In embodiments, side reactions are minimized, optionally by adding the acylating agent in a continuous or semi-continuous fashion, and/or by introducing the fully or partially hydrogenated polymer (such as isoprene polymer) into batch, semi-continuous, or continuous reactor operations as solution or suspension in diluent, said solution or suspension comprising 45 wt % or more (or 50 wt % or more, or 55 wt % or more, or 60 wt % or more), of the fully or partially hydrogenated polymer, based upon the weight of the fully or partially hydrogenated polymer and diluent.
[0293] In embodiments, side reactions are minimized, optionally by adding the acylating agent in a continuous or semi-continuous fashion, and by introducing the fully or partially hydrogenated polymer (such as isoprene polymer) into batch, semi-continuous, or continuous reactor operations as solution or suspension in diluent, said solution or suspension comprising 45 wt % or more (or 50 wt % or more, or 55 wt % or more, or 60 wt % or more), of the fully or partially hydrogenated polymer, based upon the weight of the fully or partially hydrogenated polymer and diluent.
Functionalization
[0294] In embodiments, the acylated polymer may be reacted with an alcohol or an amine to form an amide, imide, ester or combinations thereof. The reaction may consist of condensation to form an imide, an amide, a half-amide, amide-ester, diester, or an amine salt. A primary amino group will typically condense to form an amide or, in the case of maleic anhydride, an imide. It is noted the amine may have a single primary amino group or multiple primary amino groups.
[0295] Suitable amines may include one or more aromatic amines, such as amines wherein a carbon atom of the aromatic ring structure is attached directly to the amino nitrogen. The amine may also be aliphatic. In embodiments aliphatic amines can be used alone or in combination with each other or in combination with aromatic amines. The amount of aromatic amine may, in some embodiments, be a major or minor amount compared with the amount of the non-aromatic amines, or in some instances, the composition may be substantially free of aromatic amine. Alternately, the composition may be substantially free of aliphatic amine.
[0296] Examples of aromatic amines which may be used herein include one or more N-arylphenylenediamine(s) represented by the formula:
##STR00001##
wherein R.sub.7 is H, NHaryl, NHalkaryl, or a branched or straight chain hydrocarbyl radical having from about 4 to about 24 carbon atoms selected from alkyl, alkenyl, alkoxyl, aralkyl or alkaryl; R.sub.9 is NH.sub.2, (NH(CH.sub.2).sub.n).sub.mNH.sub.2, NHalkyl, NHaralkyl, CH.sub.2-aryl-NH.sub.2, in which n and m each have a value from about 1 to about 10; and R.sub.8 is hydrogen, or alkyl, alkenyl, alkoxyl, aralkyl, or alkaryl, having from about 4 to about 24 carbon atoms.
[0297] Suitable N-arylphenylenediamines include N-phenylphenylenediamines (NPPDA), for example, N-phenyl-4,4-phenylenediamine, N-phenyl-1,3-phenylenediamine, and N-phenyl-1,2-phenylenediamine and N-naphthyl-1,4-phenylenediamine. Other derivatives of NPPDA may also be included, such as N-propyl-N-phenylphenylenediamine.
[0298] In embodiments, the amine reacted with the acylated polymer is an amine having at least 3 or 4 aromatic groups and may be represented by the following formula:
##STR00002##
wherein independently each variable, R.sup.1 may be hydrogen or a C.sub.1 to C.sub.5 alkyl group (typically hydrogen); R.sup.2 may be hydrogen or a C.sub.1 to C.sub.5 alkyl group (typically hydrogen); U may be an aliphatic, alicyclic or aromatic group, with the proviso that when U is aliphatic, the aliphatic group may be linear or branched alkylene group containing 1 to 5, or 1 to 2 carbon atoms; and w may be 1 to 10, or 1 to 4, or 1 to 2 (typically 1).
[0299] Other examples of aromatic amines include aniline, N-alkylanilines such as N-methyl aniline, and N-butylaniline, di-(para-methylphenyl)amine, naphthylamine, 4-aminodiphenylamine, N,N-dimethylphenylenediamine, 4-(4-nitro-phenylazo)aniline (disperse orange 3), sulfamethazine, 4-phenoxyaniline, 3-nitroaniline, 4-aminoacetanilide, 4-amino-2-hydroxy-benzoic acid phenyl ester (phenyl amino salicylate), N-(4-amino-5-methoxy-2-methyl-phenyl)-benzamide (fast violet B), N-(4-amino-2,5-dimethoxy-phenyl)-benzamide (fast blue RR), N-(4-amino-2,5-diethoxy-phenyl)-benzamide (fast blue BB), N-(4-amino-phenyl)-benzamide and 4-phenylazoaniline. Suitable amines are referenced in U.S. Pat. No. 7,790,661 and are hereby incorporated by reference.
[0300] In embodiments, the compound condensing with the acylated polymer can be represented by the following formulas:
##STR00003##
wherein X is an alkylene group containing about 1 to about 4 carbon atoms; R.sup.2, R.sup.3 and R.sup.4 are hydrocarbyl groups.
##STR00004##
wherein X is an alkylene group containing about 1 to about 4 carbon atoms; R.sup.3 and R.sup.4 are hydrocarbyl groups.
[0301] Alternately, the amine may be an amine having at least 4 aromatic groups and an aldehyde (such as formaldehyde). The aromatic amine may be represented by formula:
##STR00005##
wherein, R.sup.1 is hydrogen or a C.sub.1-5 alkyl group (typically hydrogen); R.sup.2 is hydrogen or a C.sub.1-5 alkyl group (typically hydrogen); U is an aliphatic, alicyclic or aromatic group, optionally with the proviso that when U is aliphatic, the aliphatic group may be linear or branched alkylene group containing 1, 2, 3, 4, or 5, or 1 to 2 carbon atoms; and w is 0, 1, 2, 3, 4, 5, 6, 7, 8, or 9, such as 0, 1, 2, or 3 or 0 or 1 (typically 0). For further information on such amines see, e.g., US 2017/0073606, page 5 paragraph [0064]-[0070] and European Patent No. 2 401 348.
[0302] Examples of compounds capable of condensing with the acylating agent and further having a tertiary amino group can include but are not limited to: dimethylaminopropylamine, N,N-dimethyl-aminopropy-lamine, N,N-diethyl-aminopropylamine, N,N-dimethyl-ami-noethylamine ethylenediamine, 1,2-propylenediamine, 1,3-propylenediamine, the isomeric butylenediamines, pentanediamines, hexanediamines, heptanediamines, diethylenetriamine, dipropylenetriamine, dibutylenetriamine, triethylenetetraamine, tetraethylene pentaamine, pentaethylenehexaamine, hexamethylenetetramine, and bis(hexamethylene) triamine, the diaminobenzenes, the diaminopyridines or mixtures thereof. The compounds capable of condensing with the acylating agent and further having a tertiary amino group can further include aminoalkyl substituted heterocyclic compounds such as 1-(3-aminopropyl)imidazole and 4-(3-aminopropyl)morpholine, 1-(2-aminoethyl)piperidine, 3,3-di-amino-N-methyldipropylamine, 3,3-aminobis(N,N-dimethylpropylamine). Another example of compounds capable of condensing with the acylating agent and having a tertiary amino group include alkanolamines including, but not limited to, triethanolamine, trimethanolamine, N,N-dimethylaminopropanol, N,N-di-ethylaminopropanol, N,N-diethylaminobutanol, N,N,N-tris (hydroxyethyl)amine, N,N,N-tris(hydroxymethyl)amine.
[0303] In embodiments, the polymer may be reacted with a polyether aromatic compound. Typically, the polyether aromatic compound will have at least two functional groups, each capable of reacting with a monocarboxylic acid or ester thereof, or dicarboxylic acid, anhydride or ester thereof, or mixtures thereof. In embodiments, the polyether aromatic compound is derived from an aromatic compound containing at least one amine group and wherein the poly ether is capable of reacting with a monocarboxylic acid or ester thereof, or dicarboxylic acid, anhydride or ester thereof.
[0304] Examples of suitable polyether aromatic amines include compounds having the following structure:
##STR00006##
in which A represents an aromatic aminic moiety wherein the ether groups are linked through at least one amine group on the aromatic moiety; R.sub.1 and R.sub.6 are independently hydrogen, alkyl, alkaryl, aralkyl, or aryl or mixtures thereof; R.sub.2, R.sub.3, R.sub.4, and R.sub.5 are independently hydrogen or alkyl containing from about 1 to about 6 carbon atoms of mixtures thereof; and a and x are independently integers from about 1 to about 50.
[0305] The acylated polymer may be reacted with a polyether amine or polyether polyamine. Typical polyether amine compounds contain at least one ether unit and are chain terminated with at least one amine moiety. The polyether polyamines can be based on polymers derived from C.sub.2-C.sub.6 epoxides such as ethylene oxide, propylene oxide, and butylene oxide. Examples of polyether polyamines are sold under the Jeffamine brand and are commercially available from Hunstman Corporation.
[0306] Amines useful herein for combination with the acylated polymer include one or more of: N-phenyldiamines (such as N-phenyl-1,4-phenylenediamine, N-phenyl-p-phenylenediamine (a.k.a. 4-amino-diphenylamine, ADPA), N-phenyl-1,3-phenylenediamine, N-phenyl-1,2-phenylenediamine), nitroaniline (such as 3-nitroaniline), N-phenylethane-diamine (such as N1-phenylethane-1,2-diamine), N-aminophenylacetamide (such as N-(4-aminophenyl)acetamide), morpholinopropanamine (such as 3-morpholinopropan-1-amine), and aminoethylpiperazine (such as 1-(2-aminoethyl)piperazine).
[0307] In embodiments, the functionalization (such as amination) reactions described herein may take place in diluent (such as base oil or alkane solvent). As a side product, functionalized diluent (such as functionalized base oil) can be produced. It is contemplated that the functionalized diluent (such as functionalized base oil) may comprise reaction product of the acylated diluent (such as acylated base oil) with an amine to form an amide, imide or combination thereof.
[0308] Preferably, the reaction product of the acylated diluent (such as acylated oil) with an amine or alcohol to form an amide, imide, ester, or combination thereof, may be present in a concentrate in an amount of 40 wt % or less, alternately 20 wt % or less, alternately 10 wt % or less, alternately 5 wt % or less, alternately 3 mass % or less, preferably 2 mass % or less, preferably 1 mass % or less, preferably at 0.1 mass % or less, preferably at 0 mass % (such as 0 to 40 mass %, alternately 0.01 to 40 mass %, alternately 0.1 to 20 mass %, alternately to 1 to 10 mass %, alternately 1.5 to 5 mass %), based upon the weight of the concentrate composition.
[0309] Preferably one or more functionalized base oils, such as the reaction product of the acylated diluent (such as acylated base oil) with an amine or alcohol to form an amide, imide, ester, or combination thereof, may be present in the lubricating oil composition at an amount of 0.01 to 40 mass %, alternately 0.1 to 20 mass %, alternately to 1 to 10 mass %, alternately 1.5 to 5 mass %, (such as at 3 mass % or less, preferably 2 mass % or less, preferably 1 mass % or less, preferably at 0.1 mass % or less, preferably at 0 mass %), based upon the weight of the lubricating oil composition.
[0310] In embodiments, the functionalization (such as amination) reactions described herein may take place in solvent-containing media. As a side product, functionalized solvent can be produced. In embodiments, the functionalized solvent may be present in a concentrate composition at 3 mass % or less, preferably 2 mass % or less, preferably 1 mass % or less, preferably at 0.1 mass % or less, preferably at 0 mass %, based upon the weight of the concentrate composition. In embodiments, functionalized solvent may be present in a lubricating oil composition at 3 mass % or less, preferably 2 mass % or less, preferably 1 mass % or less, preferably at 0.1 mass % or less, preferably at 0 mass %, based upon the weight of the lubricating oil composition.
[0311] In embodiments, the acylated base oil/solvent may be removed prior to functionalization.
ii. Conjugated Diene Functionalized Polymer
[0312] The functionalized polymer may be a homopolymer of C.sub.4 or C.sub.5 olefins, such as butadiene and isoprene.
[0313] In embodiments, the functionalized polymer may be a homopolymer of isoprene, or a copolymer of isoprene and less than 5 mol % (such as less than 3 mol %, such as less than 1 mol %, such as less than 0.1 mol %) comonomer.
[0314] The functionalized polymer may comprise or be a copolymer of isoprene and one or more of styrene, methyl-styrene, 2,3-dimethyl-butadiene, 2-methyl-1,3-pentadiene, myrcene, 3-methyl-1,3-pentadiene, 4-methyl-1,3-pentadiene, 2-phenyl-1,3-butadiene, 2-phenyl-1,3-pentadiene, 3-phenyl-1,3 pentadiene, 2,3-dimethyl-1,3-pentadiene, 2-hexyl-1,3-butadiene, 3-methyl-1,3-hexadiene, 2-benzyl-1,3-butadiene, 2-p-tolyl-1,3-butadiene 1,3-butadiene, 1,3-pentadiene, 1,3-hexadiene, 1,3-heptadiene, 2,4-heptadiene, 1,3-octadiene, 2,4-octadiene, 3,5-octadiene, 1,3-nonadiene, 2,4-nonadiene, 3,5-nonadiene, 1,3-decadiene, 2,4-decadiene, and 3,5-decadiene, (optionally the comonomer(s) are present at less than 20 mol %, less than 5 mol %, such as less than 3 mol %, such as less than 1 mol %, such as less than 0.1 mol %)
[0315] In embodiments, the functionalized polymer comprises 10 (such as 9, such as 8, such as 7, such as 6, such as 5, such as 4, such as 3, such as 2, such as 1) wt %, or less, based upon the weight of the functionalized polymer, of styrene monomer.
[0316] In embodiments, styrene repeat units may be absent in the functionalized polymer.
[0317] In embodiments, the functionalized polymer may be a block or taperered block copolymer that does not comprise a styrene block.
[0318] In embodiments, the functionalized polymer may be a block or taperered block copolymer comprising (or consisting of or consisting essentially of) isoprene.
[0319] In embodiments, the functionalized polymer may be a block or taperered block copolymer comprising 50 wt % or more isoprene, based upon the weight of the copolymer.
[0320] In embodiments, the functionalized polymer may be a block or taperered block copolymer comprising (or consisting of or consisting essentially of) C.sub.4s conjugated diene, preferably comprising 50 (such as 60, such as 70, such as 80, such as 90, such as 95, such as 98) wt % or more C.sub.4s conjugated diene, based upon the weight of the copolymer.
[0321] In embodiments, the functionalized polymer may be a copolymer comprising 50 (such as 60, such as 70, such as 80, such as 90, such as 95, such as 98) wt % or more isoprene, based upon the weight of the copolymer.
[0322] In embodiments, the functionalized polymer may be a copolymer comprising 50 (such as 60, such as 70, such as 80, such as 90, such as 95, such as 98) wt % or more butadiene, based upon the weight of the copolymer.
[0323] In embodiments, the functionalized polymer may be a copolymer comprising 50 (such as 60, such as 70, such as 80, such as 90, such as 95, such as 98) wt % or more butadiene and isoprene, based upon the weight of the copolymer.
[0324] In embodiments, the functionalized polymer may be a di-block copolymer comprising at least one block of isoprene homo- or co-polymer.
[0325] Optionally, butadiene repeat units may be absent in the functionalized polymer.
[0326] Optionally, the functionalized polymer may be not homopolyisobutylene.
[0327] Optionally, the functionalized polymer may be not a copolymer of isoprene and butadiene.
[0328] Generally, the polymerized conjugated diene in the functionalized polymer includes monomer units that have been inserted in the growing polymer chain by conjugated addition and non-conjugated addition In embodiments the functionalized polymer contains at least about 50% of by conjugated addition insertions, such as at least about 75% of by conjugated addition insertions, such as about 80% of by conjugated addition insertions, such as from about 85% to about 100% of by conjugated addition insertions, based upon the total number of by conjugated addition and non-conjugated insertions, as measured by .sup.13C NMR.
[0329] The insertion of isoprene most often occurs by 2,1 insertions, 1,4 insertions (trans and cis), and 3,4 insertions of isoprene. (Measurements of the insertion geometry are determined by .sup.1H NMR.) As measured by .sup.1H NMR, the functionalized isoprene polymer contains at least about 50% of 1,4-insertions, such as at least about 75% of 1,4 insertions, such as at least about 80% of 1,4 insertions, such as at least about 90% of 1,4 insertions, such as at least about 95% of 1,4 insertions, such as at least 98% of 1,4 insertions, based upon the total of the 2,1 insertions, 1,4 insertions, and 3,4 insertions of isoprene. For purposes of this disclosure: 1) the phrase 1,4 insertion includes 1,4 and 4,1 insertions, 2) the phrase 2,1 insertion includes 2,1 and 1,2 insertions, and 3) the phrase 3,4 insertion includes 3,4 and 4,3 insertions.
[0330] The functionalized polymer may be homopolymer or copolymer. Optionally, the functionalized polymer comprises a homopolymer or copolymer of isoprene. The copolymer may be a random copolymer, a tapered block copolymer, a star copolymer, or a block copolymer.
[0331] The functionalized polymer may typically have an Mn of 20,000 to 150,000 g/mol, alternately 20,000 to about 150,000 g/mol, alternately 30,000 to about 125,000 g/mol, alternately 35,000 to about 100,000 g/mol, alternately 40,000 to 80,000 g/mol (GPC-PS).
[0332] The polymer prior to functionalization may typically have an Mn/Mw (GPC-PS) of 1.0 to 2, such as 1.1 to 1.5, such as 1.1 to 1.3, such as 1.1 to 1.2. As functionalization occurs, Mw/Mn broadening may occur.
[0333] The functionalized polymer may typically have an Mw/Mn (GPC-PS) of 1 to 3, alternately 1 to 2, alternately greater than 1 to less than 2, alternately 1.05 to 1.9, alternately 1.10 to 1.8, alternately 1.10 to 1.7, alternately 1.12 to 1.6, alternately 1.13 to 1.5, alternately 1.15 to 1.4, alternately 1.15 to 1.3. Alternately, the functionalized polymer may typically have an Mw/Mn of 1 or greater than 1 to less than 2 (such as less than 1.8, such as less than 1.7, such as less than 1.6, such as less than 1.4, such as less than 1.2, such as less than 1.15, such as less than 1.12, such as less than 1.10).
[0334] In embodiments, the functionalized polymer may have a Saponification Number (SAP) of 25 (such as 28, such as 30, such as 32, such as 34) mgKOH/g or more, as determined by ASTM D94.
[0335] In embodiments, the functionalized polymer may contribute 17% or more (such as 20% or more, such as 17 to 40%, such as 20 to 30%) to the Saponification Number of the lubricating oil composition.
[0336] In embodiments, the functionalized polymer may have an average functionality of 1.4 to 20 FG grafts/polymer chain, such as 1.4 to 15 FG grafts/polymer chain, such as 3 to 12.5 FG grafts/polymer chain, such as 4 to 10 FG grafts/polymer chain, as determined by GPC-PS.
[0337] The functionalized polymer may have an average functionality of 15 (such as 14, 13, 12, 11, 10, 9, 8, 7, or 6) or less FG grafts/polymer chain, as determined by GPC-PS.
[0338] The functionalized polymer may have an average functionality of 1 (such as 1.1, 1.2, 1.3, 1.4, 1.5, 1.6, 1.7, 1.8, 1.9, 2.0, 2.1, 2.2, 2.3, 2.4, 2.5, 2.6, 2.7, 2.8, 2.9, 3.0, 3.1, 3.2, 3.3, 3.4, 3.5, 3.6, 3.7, 3.8, 3.9, or 4.0) or more FG grafts/polymer chain, as determined by GPC-PS.
[0339] The functionalized polymer may have an average functionality from 1 (such as 1.1, 1.2, 1.3, 1.4, 1.5, 1.6, 1.7, 1.8, 1.9, 2.0, 2.1, 2.2, 2.3, 2.4, 2.5, 2.6, 2.7, 2.8, 2.9, 3.0, 3.1, 3.2, 3.3, 3.4, 3.5, 3.6, 3.7, 3.8, 3.9, or 4.0) to 15 (such as 14, 13, 12,11, 10, 9, 8, 7, or 6) FG grafts/polymer chain, as determined by GPC-PS.
[0340] In embodiments, the functionalized polymer may have an aromatic content of 5% or less, such as 3% ore less, such as 1% or less, such as 0%, based upon the weight of the polymer.
[0341] In embodiments, the functionalized polymer may comprise acylated polymers of branched C.sub.4 5 monomers having an Mn of 20,000 to 500,000 g/mol having an Mw/Mn of 2 or less, such as from 1 to 2.0, as determined by GPC-PS.
[0342] In embodiments, the functionalized polymer may have a number average molecular weight (Mn) of 20,000 (such as 25,000, such as 30,000, such as 35,000 such as 40,000) g/mol or more, as determined by GPC-PS.
[0343] In embodiments, the functionalized polymer may have a weight average molecular weight (Mw) of 50,000 (such as 40,000, such as 35,000) g/mol or less, as determined by GPC-PS. In embodiments, the functionalized polymer may have a weight average molecular weight (Mw) of 1000 to 50,000 g/mol, such as 5000 to 40,000 g/mol as determined by GPC-PS.
[0344] In embodiments, the functionalized polymer may have a z average molecular weight (Mz) of 5000 to 150,000 g/mol, such as 10,000 to 150,000 g/mol, such as 15,000 to 70,000 g/mol, such as 20,000 to 150,000 g/mol, alternately 20,000 to about 150,000 g/mol, alternately 30,000 to about 125,000 g/mol, alternately 35,000 to about 100,000 g/mol, alternately 40,000 to 80,000 g/mol, alternately 40,000 to 60,000 g/mol (GPC-PS).
[0345] In embodiments, the functionalized polymer may have a gel content of less than about 5 wt %, less than 3 wt %, less than 2 wt %, less than 1 wt %, less than 0.5 wt %, less than 0.1 wt %, or 0 wt %, where the gel content is measured by determining the amount of material that is extractable from the polymer by using boiling xylene (or cyclohexane) as an extractant. The percent of soluble and insoluble (gel) material in a polymer composition is determined as described herein.
[0346] In embodiments, the functionalized polymer may have a Functionality Distribution (Fd) value of 3.5 or less (such as 3.4 or less, such as from 1 to 3.3, such as from 1.1 to 3.2, such as from 1.2 to 3.0, such as 1.4 to 2.9, as determined by GPC-PS) (Functionality Distribution (Fd) value is determined as set out in the Example section below) and an average functionality of 1.4 to 20 FG grafts/polymer chain, such as 1.4 to 15 FG grafts/polymer chain, such as 3 to 12.5 FG grafts/polymer chain, such as 4 to 10 FG grafts/polymer chain, as determined by GPC-PS.
[0347] This disclosure relates to amide, imide, and/or ester functionalized hydrogenated/saturated polymers comprising (consisting essentially of or consisting of) C.sub.4-5 olefins having an Mw/Mn of less than 2, a Functionality Distribution (Fd) value of 3.5 or less (such as 3.4 or less, such as from 1 to 3.3, such as from 1.1 to 3.2, such as from 1.2 to 3.0, such as 1.4 to 2.9, as determined by GPC-PS, and wherein, if the polymer prior to functionalization is a C.sub.4 olefin polymer such as polyisobutylene, polybutadiene, or a copolymer thereof (preferably a polyisobutylene or a copolymer of isobutylene and butadiene), then the C.sub.4 olefin polymer has an Mn of 10,000 g/mol or more (GPC-PS), and if the polymer prior to functionalization is a C.sub.4/C.sub.5 copolymer of isoprene and butadiene, then the Mn of the copolymer is greater than 25,000 Mn (GPC-PS).
[0348] This disclosure also relates to amide, imide, and/or ester functionalized hydrogenated/saturated polymers comprising 90 mol % or more isoprene repeat units, having an Mw/Mn of less than 2, a Functionality Distribution (Fd) value of 3.5 or less (such as 3.4 or less, such as from 1 to 3.3, such as from 1.1 to 3.2, such as from 1.2 to 3.0, such as 1.4 to 2.9, as determined by GPC-PS), and wherein the polymer prior to functionalization has an Mn of 30,000 g/mol or more (GPC-PS).
[0349] This disclosure also relates to amide, imide, and/or ester functionalized hydrogenated/saturated homopolymers of isoprene having an Mw/Mn of less than 2, a Functionality Distribution (Fd) value of 3.5 or less (such as 3.4 or less, such as from 1 to 3.3, such as from 1.1 to 3.2, such as from 1.2 to 3.0, such as 1.4 to 2.9, as determined by GPC-PS), and wherein the polymer prior to functionalization has an Mn of 30,000 g/mol or more (as determined by GPC-PS).
[0350] The functionalized alpha olefin polymer may be a homopolymer or copolymer of C.sub.2 to C.sub.20 linear alpha olefins, such as ethylene, propylene, butene, pentene, hexene, heptene, styrene, octene, nonene, decene, undecene, dodecene, and the like, such as a copolymer of ethylene and propylene).
[0351] In embodiments, the functionalized polymer may be a homopolymer of ethylene or propylene, or a copolymer of ethylene and or propylene. In embodiments, in a copolymer comprising ethylene and propylene copolymer, the ethylene is present in a greater molar amount. In embodiments, in a copolymer comprising ethylene and propylene copolymer, the propylene is present in a greater molar amount.
[0352] In embodiments, styrene repeat units may be absent in the functionalized polymer.
[0353] In embodiments, the functionalized polymer may be a block or taperered block copolymer that does not comprise a styrene block.
[0354] In embodiments, the functionalized polymer may be a block or taperered block copolymer comprising (or consisting of or consisting essentially of) ethylene and or propylene.
[0355] In embodiments, the functionalized polymer may be a block or taperered block copolymer comprising 50 wt % or more ethylene, based upon the weight of the copolymer.
[0356] The functionalized polymer may be homopolymer or copolymer. Optionally, the functionalized polymer comprises a homopolymer or copolymer of isoprene. The copolymer may be a random copolymer, a tapered block copolymer, a star copolymer, or a block copolymer.
[0357] The functionalized polymer may typically have an Mn of 20,000 to 150,000 g/mol, alternately 20,000 to about 150,000 g/mol, alternately 30,000 to about 125,000 g/mol, alternately 35,000 to about 100,000 g/mol, alternately 40,000 to 80,000 g/mol (GPC-PS).
[0358] The polymer prior to functionalization may typically have an Mn/Mw (GPC-PS) of 1.0 to 3, such as 1.1 to 2, such as 1.1 to 1.9, such as 1.1 to 1.8. As functionalization occurs, Mw/Mn broadening may occur.
[0359] The functionalized polymer may typically have an Mw/Mn (GPC-PS) of 1 to 3, alternately 1 to 2, alternately greater than 1 to less than 2, alternately 1.05 to 1.9, alternately 1.10 to 1.8, alternately 1.10 to 1.7, alternately 1.12 to 1.6, alternately 1.13 to 1.5, alternately 1.15 to 1.4, alternately 1.15 to 1.3. Alternately, the functionalized polymer may typically have an Mw/Mn of 1 or greater than 1 to less than 2 (such as less than 1.8, such as less than 1.7, such as less than 1.6, such as less than 1.4, such as less than 1.2, such as less than 1.15, such as less than 1.12, such as less than 1.10).
[0360] In embodiments, the functionalized polymer may have a Saponification Number (SAP) of 25 (such as 28, such as 30, such as 32, such as 34) mgKOH/g or more, as determined by ASTM D94.
[0361] In embodiments, the functionalized polymer may contribute 17% or more (such as 20% or more, such as 17 to 40%, such as 20 to 30%) to the Saponification Number of the lubricating oil composition.
[0362] In embodiments, the functionalized polymer may have an average functionality of 1.4 to 20 FG grafts/polymer chain, such as 1.4 to 15 FG grafts/polymer chain, such as 3 to 12.5 FG grafts/polymer chain, such as 4 to 10 FG grafts/polymer chain, as determined by GPC-PS.
[0363] The functionalized polymer may have an average functionality of 15 (such as 14, 13, 12, 11, 10, 9, 8, 7, or 6) or less FG grafts/polymer chain, as determined by GPC-PS.
[0364] The functionalized polymer may have an average functionality of 1 (such as 1.1, 1.2, 1.3, 1.4, 1.5, 1.6, 1.7, 1.8, 1.9, 2.0, 2.1, 2.2, 2.3, 2.4, 2.5, 2.6, 2.7, 2.8, 2.9, 3.0, 3.1, 3.2, 3.3, 3.4, 3.5, 3.6, 3.7, 3.8, 3.9, or 4.0) or more FG grafts/polymer chain, as determined by GPC-PS.
[0365] The functionalized polymer may have an average functionality from 1 (such as 1.1, 1.2, 1.3, 1.4, 1.5, 1.6, 1.7, 1.8, 1.9, 2.0, 2.1, 2.2, 2.3, 2.4, 2.5, 2.6, 2.7, 2.8, 2.9, 3.0, 3.1, 3.2, 3.3, 3.4, 3.5, 3.6, 3.7, 3.8, 3.9, or 4.0) to 15 (such as 14, 13, 12,11, 10, 9, 8, 7, or 6) FG grafts/polymer chain, as determined by GPC-PS.
[0366] In embodiments, the functionalized polymer may have a weight average molecular weight (Mw) of 50,000 (such as 40,000, such as 35,000) g/mol or less, as determined by GPC-PS. In embodiments, the functionalized polymer may have a weight average molecular weight (Mw) of 1000 to 50,000 g/mol, such as 5000 to 40,000 g/mol as determined by GPC-PS.
[0367] In embodiments, the functionalized polymer may have a z average molecular weight (Mz) of 5000 to 150,000 g/mol, such as 10,000 to 150,000 g/mol, such as 15,000 to 70,000 g/mol, such as 20,000 to 150,000 g/mol, alternately 20,000 to about 150,000 g/mol, alternately 30,000 to about 125,000 g/mol, alternately 35,000 to about 100,000 g/mol, alternately 40,000 to 80,000 g/mol, alternately 40,000 to 60,000 g/mol (GPC-PS).
[0368] In embodiments, the functionalized polymer may have a gel content of less than about 5 wt %, less than 3 wt %, less than 2 wt %, less than 1 wt %, less than 0.5 wt %, less than 0.1 wt %, or 0 wt %, where the gel content is measured by determining the amount of material that is extractable from the polymer by using boiling xylene (or cyclohexane) as an extractant. The percent of soluble and insoluble (gel) material in a polymer composition is determined as described herein.
[0369] In embodiments, the functionalized polymer may have a Functionality Distribution (Fd) value of more than 3.5 (such as 3.5 to 10, such as from 3.8 to 8, such as from 4.7 to 7, as determined by GPC-PS) (Functionality Distribution (Fd) value is determined as set out in the Example section below) and an average functionality of 1.4 to 20 FG grafts/polymer chain, such as 1.4 to 15 FG grafts/polymer chain, such as 3 to 12.5 FG grafts/polymer chain, such as 4 to 10 FG grafts/polymer chain, as determined by GPC-PS.
[0370] This disclosure also relates to amide, imide, and/or ester functionalized hydrogenated/saturated homopolymers of isoprene having an Mw/Mn of less than 2, a Functionality Distribution (Fd) value of more than 3.5 (such as 4.0 or more, such as 4.5 or more, such as 5 or more, such as 6 or more, such as 7 or more, such as from more than 3.5 to 10, such as from 4.0 to 8.5, such as from 5 to 8.0, such as 3.8 to 7, as determined by GPC-PS).
[0371] In embodiments, the functionalized polymer may have a Functionality Distribution (Fd) value of more than 3.5 (such as 3.8 or more, such as from 3.8 to 8, such as from 4.7 to 7, as determined by GPC-PS) (Functionality Distribution (Fd) value is determined as set out in the Example section below) and an average functionality of 1.4 to 20 FG grafts/polymer chain, such as 1.4 to 15 FG grafts/polymer chain, such as 3 to 12.5 FG grafts/polymer chain, such as 4 to 10 FG grafts/polymer chain, as determined by GPC-PS.
iii. F-H-PI Functionalized Polymers
[0372] The functionalized polymer component of the lubricating oil compositions and concentrate compositions disclosed herein comprises a polymer that prior to functionalization has an Mn of about 10,000 g/mol or more, such as 20,000 g/mol or more, such as 25,000 g/mol or more, such as 30,000 g/mol or more, such as 35,000 g/mol or more (GPC-PS). Alternately, functionalized polymer comprises a polymer that prior to functionalization has an Mn of 10,000 to 300,000 g/mol, such as 20,000 to about 150,000 g/mol, such as 30,000 to about 125,000 g/mol, such as 35,000 to about 100,000 g/mol, such as 40,000 to 80,000 g/mol (GPC-PS). The polymer prior to functionalization may have an Mw/Mn of less than 2 (such as less than 1.6, such as less than 1.5, such as 1.4 or less, such as from 1 to 1.3, such as from 1.0 to 1.25, such as from 1.0 to 1.2, such as 1.0 to 1.15, such as from 1.0 to 1.1 as determined by GPC-PS). The polymer prior to functionalization may comprise repeat units of one or more olefins having 4 to 5 carbon atoms (preferably conjugated dienes having 4 to 5 carbon atoms). Prior to functionalization the C.sub.4-5 polymer is preferably fully or partially saturated (such as fully or partially hydrogenated). The functionalized polymer may be obtained by reacting the C.sub.4-5 polymer with an acylating agent to form acylated polymer and then reacting acylated polymer with an amine or alcohol to form an amide, imide, ester, or combination thereof. The functionalized polymer may also be obtained by reacting an acylated C.sub.4-5 polymer (such as a commercially available maleated fully or partially hydrogenated C.sub.4-5 polymer) with an amine to form an amide, imide or combination thereof.
[0373] This disclosure further relates to lubricating oil compositions including functionalized polymers including amide, imide, and/or ester functionalized saturated (such as hydrogenated) polymers of C.sub.4-5 conjugated dienes described herein obtained by reacting fully or partially saturated (such as fully or partially hydrogenated) polymers of C.sub.4-5 conjugated dienes having an Mw/Mn of less than 2, with an acylating agent, such as maleic acid or maleic anhydride and thereafter reacting the acylated polymer with an amine (such as a polyamine) to form an imide, amide or combination thereof.
[0374] This disclosure relates to lubricating oil compositions including functionalized polymers containing one or more pendant amine groups and comprising or resulting from the admixing of: at least partially (preferably completely) hydrogenated C.sub.4-5 olefin polymers with an acylating agent, such as maleic acid or maleic anhydride, and thereafter reacting the acylated polymer with a polyamine to form an imide, amide or combination thereof.
[0375] In embodiments, the functionalized polymer is not prepared in aromatic solvent (such as benzene or toluene), or aromatic solvent is present at 2 wt % or less (such as 1 wt % or less, such as 0.5 wt % or less), based upon the weight of solvent, diluent, and polymer.
[0376] In embodiments, the functionalized polymer is not prepared in an alkylated naphthylenic solvent, or alkylated naphthylenic solvent is present at 5 wt % or less (such as 3 wt % or less, such as 1 wt % or less), based upon the weight of solvent, diluent, and polymer.
[0377] The polymer useful herein to prepare the functionalized polymer may be a homopolymer of butadiene, isoprene, or the like.
[0378] In embodiments, the polymer useful herein to prepare the functionalized polymer may be a homopolymer of isoprene, or a copolymer of isoprene and less than 5 mol % (such as less than 3 mol %, such as less than 1 mol %, such as less than 0.1 mol %) comonomer.
[0379] The polymer useful herein to prepare the functionalized polymer may be copolymer of isoprene and one or more of styrene, methyl-styrene, 2,3-dimethyl-butadiene, 2-methyl-1,3-pentadiene, myrcene, 3-methyl-1,3-pentadiene, 4-methyl-1,3-pentadiene, 2-phenyl-1,3-butadiene, 2-phenyl-1,3-pentadiene, 3-phenyl-1,3 pentadiene, 2,3-dimethyl-1,3-pentadiene, 2-hexyl-1,3-butadiene, 3-methyl-1,3-hexadiene, 2-benzyl-1,3-butadiene, 2-p-tolyl-1,3-butadiene 1,3-butadiene, 1,3-pentadiene, 1,3-hexadiene, 1,3-heptadiene, 2,4-heptadiene, 1,3-octadiene, 2,4-octadiene, 3,5-octadiene, 1,3-nonadiene, 2,4-nonadiene, 3,5-nonadiene, 1,3-decadiene, 2,4-decadiene, and 3,5-decadiene, [optionally the comonomer(s) are present at less than 20 mol %, less than 5 mol %, such as less than 3 mol %, such as less than 1 mol %, such as less than 0.1 mol %].
[0380] Generally, the polymerized conjugated diene polymer useful herein to prepare the functionalized polymer includes a mixture of 1,4- and 1,2-insertions (a.k.a. 2,1-insertions; for butadiene, 1,2-insertions are the same as 3,4-insertions). As measured by 1H NMR, the polymerized conjugated diene polymer useful herein to prepare the functionalized polymer contains at least about 50% of 1,4-insertions, such as at least about 75% of 1,4 insertions, such as at least about 80% of 1,4 insertions, such as at least about 90% of 1,4 insertions, such as at least about 95% of 1,4 insertions, such as at least 98% of 1,4 insertions, based upon the total of the 2,1 insertions, 1,4 insertions, and 3,4 insertions of isoprene. For purposes of this disclosure: 1) the phrase 1,4 insertion includes 1,4 and 4,1 insertions, 2) the phrase 2,1 insertion includes 2,1 and 1,2 insertions, and 3) the phrase 3,4 insertion includes 3,4 and 4,3 insertions.
[0381] Optionally, styrene repeat units may be absent in the polymer useful herein to prepare the functionalized polymer. Optionally, styrene repeat units may be absent in the functionalized hydrogenated/saturated polymers.
[0382] Optionally, butadiene repeat units may be absent in the polymer useful herein to prepare the functionalized polymer. Optionally, butadiene repeat units may be absent in the functionalized hydrogenated/saturated polymers.
[0383] Optionally, the polymer useful herein to prepare the functionalized polymer may be not homopolybutylene. Optionally, the functionalized hydrogenated/saturated polymer may be not homopolybutylene.
[0384] Optionally, the polymer useful herein to prepare the functionalized polymer may be not homopolyisobutylene. Optionally, the functionalized hydrogenated/saturated polymer may be not homopolyisobutylene.
[0385] Optionally, the polymer useful herein to prepare the functionalized polymer may not be a copolymer of isoprene and butadiene. Optionally, the functionalized hydrogenated/saturated polymer may not be a copolymer of isoprene and butadiene.
[0386] The polymer useful herein to prepare the functionalized polymer and/or the functionalized polymer may be homopolymer or copolymer. The copolymer may be a random copolymer, a tapered block copolymer, a star copolymer, or a block copolymer. Block copolymers are formed from a monomer mixture comprising one or more first monomers (such as isobutylene), wherein, for example, a first monomer forms a discrete block of the polymer joined to a second discrete block of the polymer formed from a second monomer (such as butadiene). While block copolymers have substantially discrete blocks formed from the monomers, a tapered block copolymer may be composed of, at one end, a relatively pure first monomer and, at the other end, a relatively pure second monomer. The middle of the tapered block copolymer may be more of a gradient composition of the two monomers.
[0387] The polymer useful herein to prepare the functionalized polymer may typically have an Mn of 20,000 to 150,000 g/mol, alternately 20,000 to about 150,000 g/mol, alternately 30,000 to about 125,000 g/mol, alternately 35,000 to about 100,000 g/mol, alternately 40,000 to 80,000 g/mol (GPC-PS).
[0388] Polymers useful herein to prepare the functionalized polymers may typically have an Mw/Mn (as determined by GPC-PS) of 1 to 2, alternately greater than 1 to less than 2, alternately 1.1 to 1.8, alternately 1.2 to 1.5. Alternately, the polymers useful herein to prepare the functionalized polymers may typically have an Mw/Mn of 1 or greater than 1 to less than 2 (such as less than 1.8, such as less than 1.7, such as less than 1.6, such as less than 1.5, such as less than 1.4, such as less than 1.3, such as less than 1.2, such as less than 1.15, such as less than 1.12, such as less than 1.10).
[0389] The polymers used to prepare the functionalized polymers may have an Mz (as determined by GPC-PS) of 20,000 to 150,000 g/mol, alternately 20,000 to about 150,000 g/mol, alternately 30,000 to about 125,000 g/mol, alternately 35,000 to about 100,000 g/mol, alternately 40,000 to 80,000 g/mol, alternately 40,000 to 60,000 g/mol (GPC-PS).
[0390] Polymers useful herein to prepare the functionalized polymers may have a glass transition temperature (Tg) of 25 C. or less, such as 40 C. or less, such as 50 C. or less, as determined by Differential Scanning calorimetry (DSC) using a Perkin Elmer or TA Instrument Thermal Analysis System (sample is heated from ambient to 210 C. at 10 C./minute and held at 210 C. for 5 minutes, then cooled down to 40 C. at 10 C./minute and held for 5 minutes.)
[0391] Polymers useful herein to prepare the functionalized polymers typically have a residual unsaturation of less than 3%, such less than 2%, such less than 1%, such as less than 0.5%, such as less than 0.25% based upon number of double bonds in the non-hydrogenated polymer.
[0392] Polymers useful herein to prepare the functionalized polymers typically have a residual metal (such as Li, Co, and Al) content of less than 100 ppm, such less than 50 ppm, such as less than 25 ppm, such as less than 10 ppm, such as less than 5 ppm.
Hydrogenation
[0393] The C.sub.4-5 polymer useful herein to prepare the functionalized polymer can be hydrogenated partially or completely by any hydrogenating agent known to one of ordinary skill in the art. For example, a saturated or partially saturated polymer can be prepared by (a) providing a C.sub.4-5 polymer containing unsaturations (such as double or triple bonds); and (b) hydrogenating at least a portion or all of the unsaturations (such as double or triple bonds) in the polymer in the presence of a hydrogenation reagent. In some embodiments, the polymer is fully hydrogenated. In some embodiments, the polymer is partially hydrogenated. In some embodiments, the polymer is saturated (hydrogenated) at 50% or more, such as 60% or more, such as 70% or more, such as 80% or more, such as 90% or more, such as 95% or more, such as 98% or more, such as 99% or more, such as from 50 to 100% saturated (hydrogenated), as determined by ozone adsorption method described in Martino N. Smits and Dirkman Hoefman, Quantative Determination of Olefinic Unsaturation by Measurement of Ozone Absorption Analytical Chemistry Vol 44, No. 9, pg. 1688, 1972, Martino N. Smits.
[0394] In embodiments, the hydrogenation reagent can be hydrogen in the presence of a hydrogenation catalyst. In some embodiments, the hydrogenation catalyst is Pd, Pd/C, Pt, PtO2, Ru(PPh3)2Cl2, Raney nickel, or a combination thereof. In embodiments, the catalyst is a Pd catalyst. In another embodiment, the catalyst is 5% Pd/C. In a further embodiment, the catalyst may comprise or be 10% Pd/C in a high-pressure reaction vessel and the hydrogenation reaction is allowed to proceed until completion. Generally, after completion, the reaction mixture can be washed, concentrated, and dried to yield the corresponding hydrogenated product. Alternatively, any reducing agent that can reduce a CC bond to a CC bond can also be used. For example, the olefin polymer can be hydrogenated by treatment with hydrazine in the presence of a catalyst, such as 5-ethyl-3-methyllumiflavinium perchlorate, under an oxygen atmosphere to give the corresponding hydrogenated products. The reduction reaction with hydrazine is disclosed in Imada et al., J Am. Chem. Soc., 127, pp. 14544-14545, (2005), which is incorporated herein by reference.
Acylation
[0395] The fully or partially saturated (hydrogenated) polymer may be chemically modified (functionalized) to provide a polymer having at least one polar functional group, such as, but not limited to, halogen, epoxy, hydroxy, amino, nitrilo, mercapto, imido, carboxy, and sulfonic acid groups of combinations thereof. The functionalized polymers can be further modified to give a more desired type of functionality. In a preferred case, the fully or partially hydrogenated polymer is functionalized by a method, which includes reacting the fully or partially hydrogenated polymer with an unsaturated carboxylic acid (or derivative thereof, such as maleic anhydride) to provide an acylated polymer (which may then be further functionalized as described below).
[0396] In some embodiments, a carboxylic acid functionality or a reactive equivalent thereof is grafted onto the polymer to form an acylated polymer. An ethylenically unsaturated carboxylic acid material is typically grafted onto the polymer backbone. These materials which are attached to the polymer typically contain at least one ethylenic bond (prior to reaction) and at least one, such as two, carboxylic acid (or its anhydride) groups or a polar group which is convertible into said carboxyl groups by oxidation or hydrolysis. Maleic anhydride or a derivative thereof is suitable. It grafts onto the polymer, to give two carboxylic acid functionalities. Examples of additional unsaturated carboxylic materials include itaconic anhydride, or the corresponding dicarboxylic acids, such as maleic acid, fumaric acid and their esters, as well as cinnamic acid and esters thereof.
[0397] The ethylenically unsaturated carboxylic acid material may be grafted onto the polymer in a number of ways. It may be grafted onto the polymer in solution or in essentially pure (molten) form with or without using a radical initiator. Free-radical induced grafting of ethylenically unsaturated carboxylic acid materials may also be conducted in solvents, such as hexane or mineral oil. It may be carried out at an elevated temperature in the range of 100 C. to 250 C., e.g., 120 C. to 190 C., or 150 C. to 180 C., e.g., above 160 C.
[0398] The free-radical initiators which may be used include peroxides, hydroperoxides, and azo compounds, typically those which have a boiling point greater than about 100 C. and which decompose thermally within the grafting temperature range to provide free radicals. Representative of these free-radical initiators include azobisisobutyronitrile and 2,5-dimethyl-hex-3-yne-2,5-bis-tertiary-butyl peroxide. The initiator may be used in an amount of 0.005% to 1% by weight based on the weight of the reaction mixture solution. The grafting may be carried out in an inert atmosphere, such as under nitrogen blanketing. The resulting acylated polymer intermediate is characterized by having carboxylic acid acylating functions as a part of its structure.
[0399] In embodiments, the acylated polymer may have 2 or more anhydride groups per polymer molecule and may exhibit less than 10% gel. Alternately, the acylated polymer may have less than 2 anhydride groups per polymer molecule and may exhibit less than 10% gel. (See also col 17, ln 14-col 18, ln 11 of U.S. Pat. No. 5,429,758).
[0400] Alternately, in some embodiments, the acylated polymer may have a gel content of less than about 5 wt %, less than 3 wt %, less than 2 wt %, less than 1 wt %, less than 0.5 wt %, less than 0.1 wt %, or 0 wt %, where the gel content is measured by determining the amount of material that is extractable from the polymer by using boiling xylene (or cyclohexane) as an extractant. The percent of soluble and insoluble (gel) material in a polymer composition is determined by soaking a nominally 0.5 mm thick thin film specimen of polymer for 48 hours in cyclohexane at 23 C. or refluxing the thin film specimen in boiling xylene for one half hour, removing the solvent, weighing the dried residue and calculating the amount of soluble and insoluble (gel) material. This method is generally described in U.S. Pat. No. 4,311,628, which is incorporated herein by reference. For purposes of this disclosure, gel content is measured using boiling xylene, unless the sample is not soluble in xylene, then the cyclohexane method is used.
[0401] In embodiments, the acylated polymer may have a Saponification Number (SAP) of 5 g/KOH or more, such as 10 g/KOH or more, such as 20 g/KOH or more, such as 30 g/KOH or more, such as 50 g/KOH or more, such as 10 to 60 g/KOH, such as 20 to 40 g/KOH as determined by ASTM D94.
[0402] In embodiments, the acylated polymer composition may have less than 5 wt % unreacted acylating agent (such as maleic anhydride), such as less than 4 wt %, such as less than 3 wt %, such as less than 1 wt %, such as less than 0.5 wt %, such as less than 0.25 wt %, such as less than 0.1 wt %, based upon the weight of the acylated polymer composition (i.e., polymer, acylating agent, and diluent).
[0403] In embodiments, the acylation reactions described herein may take place in base oil diluent. As a side product, functionalized base oil can be produced. The oil may become acylated itself. For example, maleated base oil may be present after the acylation reactions described herein.
[0404] It is contemplated that the functionalized base oil may comprise the acylated oil and/or the reaction product of the acylated oil with an amine to form an amide, imide or combination thereof.
[0405] Preferably, the acylated oil and/or reaction product of the acylated oil with an amine or alcohol to form an amide, imide, ester, or combination thereof, may be present in a concentrate in an amount of 40 wt % or less, alternately 20 wt % or less, alternately 10 wt % or less, alternately 5 wt % or less, alternately 3 mass % or less, preferably 2 mass % or less, preferably 1 mass % or less, preferably at 0.1 mass % or less, preferably at 0 mass % (such as 0 to 40 mass %, alternately 0.01 to 40 mass %, alternately 0.1 to 20 mass %, alternately to 1 to 10 mass %, alternately 1.5 to 5 mass %), based upon the weight of the concentrate composition.
[0406] Preferably one or more functionalized base oils, such as acylated oil and/or reaction product of the acylated oil with an amine or alcohol to form an amide, imide, ester, or combination thereof, may be present in the lubricating oil composition at an amount of 0.01 to 40 mass %, alternately 0.1 to 20 mass %, alternately to 1 to 10 mass %, alternately 1.5 to 5 mass %, (such as at 3 mass % or less, preferably 2 mass % or less, preferably 1 mass % or less, preferably at 0.1 mass % or less, preferably at 0 mass %), based upon the weight of the lubricating oil composition.
[0407] In embodiments, the acylation reactions described herein take place in solvent containing media. As a side product, acylated/functionalized solvent can be produced. In embodiments, acylated and/or functionalized solvent may be present in a concentrate composition at 3 mass % or less, preferably 2 mass % or less, preferably 1 mass % or less, preferably at 0.1 mass % or less, preferably at 0 mass %, based upon the weight of the concentrate composition. In embodiments, functionalized solvent may be present in a lubricating oil composition at 3 mass % or less, preferably 2 mass % or less, preferably 1 mass % or less, preferably at 0.1 mass % or less, preferably at 0 mass %, based upon the weight of the lubricating oil composition.
[0408] In embodiments, the acylating agent may be added in such a way as to minimize side reactions (such as reaction with base oil or other diluent present in the reaction vessel).
[0409] In embodiments, the acylating reaction may occur where the acylating agent (such as maleic acid or maleic anhydride) is added in a continuous or semi-continuous (such as intermittent) stream (such as, for example, in controlled relatively equal portions over the reaction time, or larger and/or smaller portions at different points in the reaction) to minimize functionalized base oil and other side reactions. As an example, the acylating agent may be added in a continuous fashion where the amounts of polymer and acylating agents are added in controlled stoichiometric amounts. As another example, the polymer may be added to a reaction vessel in batch fashion and the acylating agent added slowly or in a semi-continuous fashion (such as adding the acylating agent in 2 or more, such as 5 or more, such as 10 or more, such as 20 or more, such as 30 or more, such as 40 or more, such as 50 or more, such as 60 or more discrete amounts or portions). Alternately, the polymer can be added to the reaction vessel in X number of portions and the acylating agent added in 1.5X or more (such as 2X or more, such as 5X or more, such as 10X or more, such as 20X or more, such as 30X or more, such as 40X or more, such as 50X or more, such as 60X or more) number of portions. This same effect may also be achieved by diluting or concentrating a polymer solution and/or the acylating agent solution to the same or different extents.
[0410] Preferably, the acylating agent may be added in such a way as to minimize side reactions, such as in a continuous or semi-continuous fashion.
[0411] The reaction may also be run so as to minimize side reactions by using high concentrations of the polymer in diluent, such as 45 wt % or more, or 50 wt % or more, or 55 wt % or more, or 60 wt % or more in batch, semi-continuous, or continuous reactor operations. For example, the polymer (such as a hydrogenated isoprene polymer, such as hydrogenated homo-polyisoprene) may be introduced into batch, semi-continuous, or continuous reactor operations as solution or suspension (such as a slurry) in diluent (such as oil (e.g., base oil, such as a Group I, II, III, IV, and/or V base oil, such as a Group II and/or Group III base oil) or alkane solvent or diluent or a combination thereof), where the polymer may be present in the solution or suspension at 45 wt % or more (or 50 wt % or more, or 55 wt % or more, or 60 wt % or more), based upon the weight of the polymer and diluent.
[0412] In embodiments, the side reactions may be minimized by: 1) adding the acylating agent in a continuous or semi-continuous fashion, and/or 2) the polymer is introduced into batch, semi-continuous or continuous reactor operations as solution or suspension in diluent where the polymer is present at 45 wt % or more, based upon the weight of the polymer and diluent.
[0413] In embodiments, side reactions are minimized, optionally by adding the acylating agent in a continuous or semi-continuous fashion, and/or by introducing the fully or partially hydrogenated polymer (such as isoprene polymer) into batch, semi-continuous, or continuous reactor operations as solution or suspension in diluent, said solution or suspension comprising 45 wt % or more (or 50 wt % or more, or 55 wt % or more, or 60 wt % or more), of the fully or partially hydrogenated polymer, based upon the weight of the fully or partially hydrogenated polymer and diluent.
[0414] In embodiments, side reactions are minimized, optionally by adding the acylating agent in a continuous or semi-continuous fashion, and by introducing the fully or partially hydrogenated polymer (such as isoprene polymer) into batch, semi-continuous, or continuous reactor operations as solution or suspension in diluent, said solution or suspension comprising 45 wt % or more (or 50 wt % or more, or 55 wt % or more, or 60 wt % or more), of the fully or partially hydrogenated polymer, based upon the weight of the fully or partially hydrogenated polymer and diluent.
Functionalization
[0415] In embodiments, the acylated polymer may be reacted with an alcohol or an amine to form an amide, imide, ester or combinations thereof. The reaction may consist of condensation to form an imide, an amide, a half-amide, amide-ester, diester, or an amine salt. A primary amino group will typically condense to form an amide or, in the case of maleic anhydride, an imide. It is noted the amine may have a single primary amino group or multiple primary amino groups.
[0416] Suitable amines may include one or more aromatic amines, such as amines wherein a carbon atom of the aromatic ring structure is attached directly to the amino nitrogen. The amine may also be aliphatic. In embodiments aliphatic amines can be used alone or in combination with each other or in combination with aromatic amines. The amount of aromatic amine may, in some embodiments, be a major or minor amount compared with the amount of the non-aromatic amines, or in some instances, the composition may be substantially free of aromatic amine. Alternately, the composition may be substantially free of aliphatic amine.
[0417] Examples of aromatic amines which may be used herein include one or more N-arylphenylenediamine(s) represented by the formula:
##STR00007##
wherein R.sub.7 is H, NHaryl, NHalkaryl, or a branched or straight chain hydrocarbyl radical having from about 4 to about 24 carbon atoms selected from alkyl, alkenyl, alkoxyl, aralkyl or alkaryl; R.sub.9 is NH.sub.2, (NH(CH.sub.2).sub.n).sub.mNH.sub.2, NHalkyl, NHaralkyl, CH.sub.2-aryl-NH.sub.2, in which n and m each have a value from about 1 to about 10; and R.sub.8 is hydrogen, or alkyl, alkenyl, alkoxyl, aralkyl, or alkaryl, having from about 4 to about 24 carbon atoms.
[0418] Suitable N-arylphenylenediamines include N-phenylphenylenediamines (NPPDA), for example, N-phenyl-4,4-phenylenediamine, N-phenyl-1,3-phenylenediamine, and N-phenyl-1,2-phenylenediamine and N-naphthyl-1,4-phenylenediamine. Other derivatives of NPPDA may also be included, such as N-propyl-N-phenylphenylenediamine.
[0419] In embodiments, the amine reacted with the acylated polymer is an amine having at least 3 or 4 aromatic groups and may be represented by the following formula:
##STR00008##
wherein independently each variable, R may be hydrogen or a C.sub.1 to C.sub.5 alkyl group (typically hydrogen); R.sup.2 may be hydrogen or a C.sub.1 to C.sub.5 alkyl group (typically hydrogen); U may be an aliphatic, alicyclic or aromatic group, with the proviso that when U is aliphatic, the aliphatic group may be linear or branched alkylene group containing 1 to 5, or 1 to 2 carbon atoms; and w may be 1 to 10, or 1 to 4, or 1 to 2 (typically 1).
[0420] Other examples of aromatic amines include aniline, N-alkylanilines such as N-methyl aniline, and N-butylaniline, di-(para-methylphenyl)amine, naphthylamine, 4-aminodiphenylamine, N,N-dimethylphenylenediamine, 4-(4-nitro-phenylazo)aniline (disperse orange 3), sulfamethazine, 4-phenoxyaniline, 3-nitroaniline, 4-aminoacetanilide, 4-amino-2-hydroxy-benzoic acid phenyl ester (phenyl amino salicylate), N-(4-amino-5-methoxy-2-methyl-phenyl)-benzamide (fast violet B), N-(4-amino-2,5-dimethoxy-phenyl)-benzamide (fast blue RR), N-(4-amino-2,5-diethoxy-phenyl)-benzamide (fast blue BB), N-(4-amino-phenyl)-benzamide and 4-phenylazoaniline. Suitable amines are referenced in U.S. Pat. No. 7,790,661 and are hereby incorporated by reference.
[0421] In embodiments, the compound condensing with the acylated polymer can be represented by the following formulas:
##STR00009##
wherein X is an alkylene group containing about 1 to about 4 carbon atoms; R.sup.2, R.sup.3 and R.sup.4 are hydrocarbyl groups.
##STR00010##
wherein X is an alkylene group containing about 1 to about 4 carbon atoms; R.sup.3 and R.sup.4 are hydrocarbyl groups.
[0422] Alternately, the amine may be an amine having at least 4 aromatic groups and an aldehyde (such as formaldehyde). The aromatic amine may be represented by formula:
##STR00011##
wherein, R.sup.1 is hydrogen or a C.sub.1-5 alkyl group (typically hydrogen); R.sup.2 is hydrogen or a C.sub.1-5 alkyl group (typically hydrogen); U is an aliphatic, alicyclic or aromatic group, optionally with the proviso that when U is aliphatic, the aliphatic group may be linear or branched alkylene group containing 1, 2, 3, 4, or 5, or 1 to 2 carbon atoms; and w is 0, 1, 2, 3, 4, 5, 6, 7, 8, or 9, such as 0, 1, 2, or 3 or 0 or 1 (typically 0). For further information on such amines see, e.g., US 2017/0073606, page 5 paragraph [0064]-[0070] and European Patent No. 2 401 348.
[0423] Examples of compounds capable of condensing with the acylating agent and further having a tertiary amino group can include but are not limited to: dimethylaminopropylamine, N,N-dimethyl-aminopropy-lamine, N,N-diethyl-aminopropylamine, N,N-dimethyl-ami-noethylamine ethylenediamine, 1,2-propylenediamine, 1,3-propylenediamine, the isomeric butylenediamines, pentanediamines, hexanediamines, heptanediamines, diethylenetriamine, dipropylenetriamine, dibutylenetriamine, triethylenetetraamine, tetraethylene pentaamine, pentaethylenehexaamine, hexamethylenetetramine, and bis(hexamethylene) triamine, the diaminobenzenes, the diaminopyridines or mixtures thereof. The compounds capable of condensing with the acylating agent and further having a tertiary amino group can further include aminoalkyl substituted heterocyclic compounds such as 1-(3-aminopropyl)imidazole and 4-(3-aminopropyl)morpholine, 1-(2-aminoethyl)piperidine, 3,3-di-amino-N-methyldipropylamine, 3,3-aminobis(N,N-dimethylpropylamine). Another example of compounds capable of condensing with the acylating agent and having a tertiary amino group include alkanolamines including, but not limited to, triethanolamine, trimethanolamine, N,N-dimethylaminopropanol, N,N-di-ethylaminopropanol, N,N-diethylaminobutanol, N,N,N-tris (hydroxyethyl)amine, N,N,N-tris(hydroxymethyl)amine.
[0424] In embodiments, the polymer may be reacted with a polyether aromatic compound. Typically, the polyether aromatic compound will have at least two functional groups, each capable of reacting with a monocarboxylic acid or ester thereof, or dicarboxylic acid, anhydride or ester thereof, or mixtures thereof. In embodiments, the polyether aromatic compound is derived from an aromatic compound containing at least one amine group and wherein the poly ether is capable of reacting with a monocarboxylic acid or ester thereof, or dicarboxylic acid, anhydride or ester thereof.
[0425] Examples of suitable polyether aromatic amines include compounds having the following structure:
##STR00012##
in which A represents an aromatic aminic moiety wherein the ether groups are linked through at least one amine group on the aromatic moiety; R.sub.1 and R.sub.6 are independently hydrogen, alkyl, alkaryl, aralkyl, or aryl or mixtures thereof; R.sub.2, R.sub.3, R.sub.4, and R.sub.5 are independently hydrogen or alkyl containing from about 1 to about 6 carbon atoms of mixtures thereof; and a and x are independently integers from about 1 to about 50.
[0426] The acylated polymer may be reacted with a polyether amine or polyether polyamine. Typical polyether amine compounds contain at least one ether unit and are chain terminated with at least one amine moiety. The polyether polyamines can be based on polymers derived from C.sub.2-C.sub.6 epoxides such as ethylene oxide, propylene oxide, and butylene oxide. Examples of polyether polyamines are sold under the Jeffamine brand and are commercially available from Hunstman Corporation.
[0427] Amines useful herein for combination with the acylated polymer include one or more of: N-phenyldiamines (such as N-phenyl-1,4-phenylenediamine, N-phenyl-p-phenylenediamine (a.k.a. 4-amino-diphenylamine, ADPA), N-phenyl-1,3-phenylenediamine, N-phenyl-1,2-phenylenediamine), nitroaniline (such as 3-nitroaniline), N-phenylethane-diamine (such as N1-phenylethane-1,2-diamine), N-aminophenylacetamide (such as N-(4-aminophenyl)acetamide), morpholinopropanamine (such as 3-morpholinopropan-1-amine), and aminoethylpiperazine (such as 1-(2-aminoethyl)piperazine).
[0428] In embodiments, the functionalization (such as amination) reactions described herein may take place in diluent (such as base oil or alkane solvent). As a side product, functionalized diluent (such as functionalized base oil) can be produced. It is contemplated that the functionalized diluent (such as functionalized base oil) may comprise reaction product of the acylated diluent (such as acylated base oil) with an amine to form an amide, imide or combination thereof.
[0429] Preferably, the reaction product of the acylated diluent (such as acylated oil) with an amine or alcohol to form an amide, imide, ester, or combination thereof, may be present in a concentrate in an amount of 40 wt % or less, alternately 20 wt % or less, alternately 10 wt % or less, alternately 5 wt % or less, alternately 3 mass % or less, preferably 2 mass % or less, preferably 1 mass % or less, preferably at 0.1 mass % or less, preferably at 0 mass % (such as 0 to 40 mass %, alternately 0.01 to 40 mass %, alternately 0.1 to 20 mass %, alternately to 1 to 10 mass %, alternately 1.5 to 5 mass %), based upon the weight of the concentrate composition.
[0430] Preferably one or more functionalized base oils, such as the reaction product of the acylated diluent (such as acylated base oil) with an amine or alcohol to form an amide, imide, ester, or combination thereof, may be present in the lubricating oil composition at an amount of 0.01 to 40 mass %, alternately 0.1 to 20 mass %, alternately to 1 to 10 mass %, alternately 1.5 to 5 mass %, (such as at 3 mass % or less, preferably 2 mass % or less, preferably 1 mass % or less, preferably at 0.1 mass % or less, preferably at 0 mass %), based upon the weight of the lubricating oil composition.
[0431] In embodiments, the functionalization (such as amination) reactions described herein may take place in solvent-containing media. As a side product, functionalized solvent can be produced. In embodiments, the functionalized solvent may be present in a concentrate composition at 3 mass % or less, preferably 2 mass % or less, preferably 1 mass % or less, preferably at 0.1 mass % or less, preferably at 0 mass %, based upon the weight of the concentrate composition. In embodiments, functionalized solvent may be present in a lubricating oil composition at 3 mass % or less, preferably 2 mass % or less, preferably 1 mass % or less, preferably at 0.1 mass % or less, preferably at 0 mass %, based upon the weight of the lubricating oil composition.
[0432] In embodiments, the acylated base oil/solvent may be removed prior to functionalization.
[0433] The functionalized polymer may be a homopolymer of C.sub.4 or C.sub.5 olefins, such as butadiene and isoprene.
[0434] In embodiments, the functionalized polymer may be a homopolymer of isoprene, or a copolymer of isoprene and less than 5 mol % (such as less than 3 mol %, such as less than 1 mol %, such as less than 0.1 mol %) comonomer.
[0435] The functionalized polymer may comprise or be a copolymer of isoprene and one or more of styrene, methyl-styrene, 2,3-dimethyl-butadiene, 2-methyl-1,3-pentadiene, myrcene, 3-methyl-1,3-pentadiene, 4-methyl-1,3-pentadiene, 2-phenyl-1,3-butadiene, 2-phenyl-1,3-pentadiene, 3-phenyl-1,3 pentadiene, 2,3-dimethyl-1,3-pentadiene, 2-hexyl-1,3-butadiene, 3-methyl-1,3-hexadiene, 2-benzyl-1,3-butadiene, 2-p-tolyl-1,3-butadiene 1,3-butadiene, 1,3-pentadiene, 1,3-hexadiene, 1,3-heptadiene, 2,4-heptadiene, 1,3-octadiene, 2,4-octadiene, 3,5-octadiene, 1,3-nonadiene, 2,4-nonadiene, 3,5-nonadiene, 1,3-decadiene, 2,4-decadiene, and 3,5-decadiene, (optionally the comonomer(s) are present at less than 20 mol %, less than 5 mol %, such as less than 3 mol %, such as less than 1 mol %, such as less than 0.1 mol %)
[0436] In embodiments, the functionalized polymer comprises 10 (such as 9, such as 8, such as 7, such as 6, such as 5, such as 4, such as 3, such as 2, such as 1) wt %, or less, based upon the weight of the functionalized polymer, of styrene monomer.
[0437] In embodiments, styrene repeat units may be absent in the functionalized polymer.
[0438] In embodiments, the functionalized polymer may be a block or taperered block copolymer that does not comprise a styrene block.
[0439] In embodiments, the functionalized polymer may be a block or taperered block copolymer comprising (or consisting of or consisting essentially of) isoprene.
[0440] In embodiments, the functionalized polymer may be a block or taperered block copolymer comprising 50 wt % or more isoprene, based upon the weight of the copolymer.
[0441] In embodiments, the functionalized polymer may be a block or taperered block copolymer comprising (or consisting of or consisting essentially of) C.sub.4s conjugated diene, preferably comprising 50 (such as 60, such as 70, such as 80, such as 90, such as 95, such as 98) wt % or more C.sub.4s conjugated diene, based upon the weight of the copolymer.
[0442] In embodiments, the functionalized polymer may be a copolymer comprising 50 (such as 60, such as 70, such as 80, such as 90, such as 95, such as 98) wt % or more isoprene, based upon the weight of the copolymer.
[0443] In embodiments, the functionalized polymer may be a copolymer comprising 50 (such as 60, such as 70, such as 80, such as 90, such as 95, such as 98) wt % or more butadiene, based upon the weight of the copolymer.
[0444] In embodiments, the functionalized polymer may be a copolymer comprising 50 (such as 60, such as 70, such as 80, such as 90, such as 95, such as 98) wt % or more butadiene and isoprene, based upon the weight of the copolymer.
[0445] In embodiments, the functionalized polymer may be a di-block copolymer comprising at least one block of isoprene homo- or co-polymer.
[0446] Optionally, butadiene repeat units may be absent in the functionalized polymer.
[0447] Optionally, the functionalized polymer may be not homopolyisobutylene.
[0448] Optionally, the functionalized polymer may be not a copolymer of isoprene and butadiene.
[0449] Generally, the polymerized conjugated diene in the functionalized polymer includes monomer units that have been inserted in the growing polymer chain by conjugated addition and non-conjugated addition In embodiments the functionalized polymer contains at least about 50% of by conjugated addition insertions, such as at least about 75% of by conjugated addition insertions, such as about 80% of by conjugated addition insertions, such as from about 85% to about 100% of by conjugated addition insertions, based upon the total number of by conjugated addition and non-conjugated insertions, as measured by .sup.13C NMR.
[0450] The insertion of isoprene most often occurs by 2,1 insertions, 1,4 insertions (trans and cis), and 3,4 insertions of isoprene. (Measurements of the insertion geometry are determined by .sup.1H NMR.) As measured by .sup.1H NMR, the functionalized isoprene polymer contains at least about 50% of 1,4-insertions, such as at least about 75% of 1,4 insertions, such as at least about 80% of 1,4 insertions, such as at least about 90% of 1,4 insertions, such as at least about 95% of 1,4 insertions, such as at least 98% of 1,4 insertions, based upon the total of the 2,1 insertions, 1,4 insertions, and 3,4 insertions of isoprene. For purposes of this disclosure: 1) the phrase 1,4 insertion includes 1,4 and 4,1 insertions, 2) the phrase 2,1 insertion includes 2,1 and 1,2 insertions, and 3) the phrase 3,4 insertion includes 3,4 and 4,3 insertions.
[0451] The functionalized polymer may be homopolymer or copolymer. Optionally, the functionalized polymer comprises a homopolymer or copolymer of isoprene. The copolymer may be a random copolymer, a tapered block copolymer, a star copolymer, or a block copolymer.
[0452] The functionalized polymer may typically have an Mn of 20,000 to 150,000 g/mol, alternately 20,000 to about 150,000 g/mol, alternately 30,000 to about 125,000 g/mol, alternately 35,000 to about 100,000 g/mol, alternately 40,000 to 80,000 g/mol (GPC-PS).
[0453] The polymer prior to functionalization may typically have an Mn/Mw (GPC-PS) of 1.0 to 2, such as 1.1 to 1.5, such as 1.1 to 1.3, such as 1.1 to 1.2. As functionalization occurs, Mw/Mn broadening may occur.
[0454] The functionalized polymer may typically have an Mw/Mn (GPC-PS) of 1 to 3, alternately 1 to 2, alternately greater than 1 to less than 2, alternately 1.05 to 1.9, alternately 1.10 to 1.8, alternately 1.10 to 1.7, alternately 1.12 to 1.6, alternately 1.13 to 1.5, alternately 1.15 to 1.4, alternately 1.15 to 1.3. Alternately, the functionalized polymer may typically have an Mw/Mn of 1 or greater than 1 to less than 2 (such as less than 1.8, such as less than 1.7, such as less than 1.6, such as less than 1.4, such as less than 1.2, such as less than 1.15, such as less than 1.12, such as less than 1.10).
[0455] In embodiments, the functionalized polymer may have a Saponification Number (SAP) of 25 (such as 28, such as 30, such as 32, such as 34) mgKOH/g or more, as determined by ASTM D94.
[0456] In embodiments, the functionalized polymer may contribute 17% or more (such as 20% or more, such as 17 to 40%, such as 20 to 30%) to the Saponification Number of the lubricating oil composition.
[0457] In embodiments, the functionalized polymer may have an average functionality of 1.4 to 20 FG grafts/polymer chain, such as 1.4 to 15 FG grafts/polymer chain, such as 3 to 12.5 FG grafts/polymer chain, such as 4 to 10 FG grafts/polymer chain, as determined by GPC-PS.
[0458] The functionalized polymer may have an average functionality of 15 (such as 14, 13, 12,11, 10, 9, 8, 7, or 6) or less FG grafts/polymer chain, as determined by GPC-PS.
[0459] The functionalized polymer may have an average functionality of 1 (such as 1.1, 1.2, 1.3, 1.4, 1.5, 1.6, 1.7, 1.8, 1.9, 2.0, 2.1, 2.2, 2.3, 2.4, 2.5, 2.6, 2.7, 2.8, 2.9, 3.0, 3.1, 3.2, 3.3, 3.4, 3.5, 3.6, 3.7, 3.8, 3.9, or 4.0) or more FG grafts/polymer chain, as determined by GPC-PS.
[0460] The functionalized polymer may have an average functionality from 1 (such as 1.1, 1.2, 1.3, 1.4, 1.5, 1.6, 1.7, 1.8, 1.9, 2.0, 2.1, 2.2, 2.3, 2.4, 2.5, 2.6, 2.7, 2.8, 2.9, 3.0, 3.1, 3.2, 3.3, 3.4, 3.5, 3.6, 3.7, 3.8, 3.9, or 4.0) to 15 (such as 14, 13, 12, 11, 10, 9, 8, 7, or 6) FG grafts/polymer chain, as determined by GPC-PS.
[0461] In embodiments, the functionalized polymer may have an aromatic content of 5% or less, such as 3% or less, such as 1% or less, such as 0%, based upon the weight of the polymer.
[0462] In embodiments, the functionalized polymer may comprise acylated polymers of branched C.sub.4-5 monomers having an Mn of 20,000 to 500,000 g/mol having an Mw/Mn of 2 or less, such as from 1 to 2.0, as determined by GPC-PS.
[0463] In embodiments, the functionalized polymer may have a number average molecular weight (Mn) of 20,000 (such as 25,000, such as 30,000, such as 35,000 such as 40,000) g/mol or more, as determined by GPC-PS.
[0464] In embodiments, the functionalized polymer may have a weight average molecular weight (Mw) of 50,000 (such as 40,000, such as 35,000) g/mol or less, as determined by GPC-PS. In embodiments, the functionalized polymer may have a weight average molecular weight (Mw) of 1000 to 50,000 g/mol, such as 5000 to 40,000 g/mol as determined by GPC-PS.
[0465] In embodiments, the functionalized polymer may have a z average molecular weight (Mz) of 5000 to 150,000 g/mol, such as 10,000 to 150,000 g/mol, such as 15,000 to 70,000 g/mol, such as 20,000 to 150,000 g/mol, alternately 20,000 to about 150,000 g/mol, alternately 30,000 to about 125,000 g/mol, alternately 35,000 to about 100,000 g/mol, alternately 40,000 to 80,000 g/mol, alternately 40,000 to 60,000 g/mol (GPC-PS).
[0466] In embodiments, the functionalized polymer may have a gel content of less than about 5 wt %, less than 3 wt %, less than 2 wt %, less than 1 wt %, less than 0.5 wt %, less than 0.1 wt %, or 0 wt %, where the gel content is measured by determining the amount of material that is extractable from the polymer by using boiling xylene (or cyclohexane) as an extractant. The percent of soluble and insoluble (gel) material in a polymer composition is determined as described herein.
[0467] In embodiments, the functionalized polymer may have a Functionality Distribution (Fd) value of 3.5 or less (such as 3.4 or less, such as from 1 to 3.3, such as from 1.1 to 3.2, such as from 1.2 to 3.0, such as 1.4 to 2.9, as determined by GPC-PS). Functionality Distribution (Fd) value is determined as set out in the Example section below and an average functionality of 1.4 to 20 FG grafts/polymer chain, such as 1.4 to 15 FG grafts/polymer chain, such as 3 to 12.5 FG grafts/polymer chain, such as 4 to 10 FG grafts/polymer chain, as determined by GPC-PS.
[0468] This disclosure relates to amide, imide, and/or ester functionalized hydrogenated/saturated polymers comprising (consisting essentially of or consisting of) C.sub.4-5 olefins having an Mw/Mn of less than 2, a Functionality Distribution (Fd) value of 3.5 or less (such as 3.4 or less, such as from 1 to 3.3, such as from 1.1 to 3.2, such as from 1.2 to 3.0, such as 1.4 to 2.9, as determined by GPC-PS), and wherein, if the polymer prior to functionalization is a C.sub.4 olefin polymer such as polyisobutylene, polybutadiene, or a copolymer thereof (preferably a polyisobutylene or a copolymer of isobutylene and butadiene), then the C.sub.4 olefin polymer has an Mn of 10,000 g/mol or more (GPC-PS), and if the polymer prior to functionalization is a C.sub.4/C.sub.5 copolymer of isoprene and butadiene, then the Mn of the copolymer is greater than 25,000 Mn (GPC-PS).
[0469] This disclosure also relates to amide, imide, and/or ester functionalized hydrogenated/saturated polymers comprising 90 mol % or more isoprene repeat units, having an Mw/Mn of less than 2, a Functionality Distribution (Fd) value of 3.5 or less (such as 3.4 or less, such as from 1 to 3.3, such as from 1.1 to 3.2, such as from 1.2 to 3.0, such as 1.4 to 2.9, as determined by GPC-PS), and wherein the polymer prior to functionalization has an Mn of 30,000 g/mol or more (GPC-PS).
[0470] This disclosure also relates to amide, imide, and/or ester functionalized hydrogenated/saturated homopolymers of isoprene having an Mw/Mn of less than 2, a Functionality Distribution (Fd) value of 3.5 or less (such as 3.4 or less, such as from 1 to 3.3, such as from 1.1 to 3.2, such as from 1.2 to 3.0, such as 1.4 to 2.9, as determined by GPC-PS), and wherein the polymer prior to functionalization has an Mn of 30,000 g/mol or more (as determined by GPC-PS).
[0471] The lubricating composition according to the present disclosure may further comprise one or more additives such as detergents, friction modifiers, antioxidants, pour point depressants, anti-foam agents, viscosity modifiers, dispersants, corrosion inhibitors, antiwear agents, extreme pressure additives, demulsifiers, seal compatibility agents, seal swell agents, additive diluent base oils, etc. Specific examples of such additives are described in, for example, Kirk-Othmer Encyclopedia of Chemical Technology, third edition, volume 14, pp. 477-526, and several are discussed in further detail below.
C. Detergents
[0472] The lubricating oil compositions and concentrate compositions may comprise one or more metal detergents (such as blends of metal detergents) also referred to as a detergent additive. Metal detergents typically function both as detergents to reduce or remove deposits and as acid neutralizers or rust inhibitors, thereby reducing wear and corrosion and extending engine life. Detergents generally comprise a polar head with a long hydrophobic tail, with the polar head comprising a metal salt of an acidic organic compound. The salts may contain a substantially stoichiometric amount of the metal in which case they are usually described as normal or neutral salts, and would typically have a total base number (TBN as measured by ASTM D2896) of up to 150 mgKOH/g, such as from 0 to 80 (or 5-30) mgKOH/g. A large amount of a metal base may be incorporated by reacting excess metal compound (e.g., an oxide or hydroxide) with an acidic gas (e.g., carbon dioxide). Such detergents, sometimes referred to as overbased, may have a TBN of 100 mgKOH/g or more (such as 200 mgKOH/g or more), and typically will have a TBN of 250 mgKOH/g or more, such as 300 mgKOH/g or more, such as from 200 to 800 mgKOH/g, 225 to 700 mgKOH/g, 250 to 650 mgKOH/g, or 300 to 600 mgKOH/g, such as 150 to 650 mgKOH/g.
[0473] Suitable detergents include, oil-soluble neutral and overbased sulfonates, phenates, sulfurized phenates, thiophosphonates, salicylates, naphthenates and other oil-soluble carboxylates of a metal, particularly the alkali metals (Group 1 metals, e.g., Li, Na, K, Rb) or alkaline earth metals (Group 2 metals, e.g., Be, Mg, Ca, Sr, Ba), particularly, sodium, potassium, lithium, calcium, and magnesium, such as Ca and/or Mg. Furthermore, the detergent may comprise a hybrid detergent comprising any combination of sodium, potassium, lithium, calcium, or magnesium salts of sulfonates, phenates, sulfurized phenates, thiophosphonates, salicylates, and naphthenates or other oil-soluble carboxylates of a Group 1 and/or 2 metal.
[0474] Preferably, the detergent additive(s) useful in the present disclosure comprises calcium and/or magnesium metal salts. The detergent may be a calcium and/or magnesium carboxylate (e.g., salicylates), sulfonate, or phenate detergent. More preferably, the detergent additives are selected from magnesium salicylate, calcium salicylate, magnesium sulfonate, calcium sulfonate, magnesium phenate, calcium phenate, and hybrid detergents comprising two, three, four, or more of more of these detergents and/or combinations thereof.
[0475] The metal-containing detergent may also include hybrid detergents formed with mixed surfactant systems including phenate and/or sulfonate components, e.g., phenate/salicylates, sulfonate/phenates, sulfonate/salicylates, sulfonates/phenates/salicylates, as described, for example, in U.S. Pat. Nos. 6,429,178; 6,429,179; 6,153,565; and 6,281,179. Where, for example, a hybrid sulfonate/phenate detergent is employed, the hybrid detergent would be considered equivalent to amounts of distinct phenate and sulfonate detergents introducing like amounts of phenate and sulfonate soaps, respectively.
[0476] The overbased metal-containing detergent may be sodium salts, calcium salts, magnesium salts, or mixtures thereof of the phenates, sulfur-containing phenates, sulfonates, salixarates, and salicylates. Overbased phenates and salicylates typically have a total base number of 180 to 650 mgKOH/g, such as 200 to 450 TBN mgKOH/g. Overbased sulfonates typically have a total base number of 250 to 600 mgKOH/g, or 300 to 500 mgKOH/g. In embodiments, the sulfonate detergent may be predominantly a linear alkylbenzene sulfonate detergent having a metal ratio of at least 8 as is described in paragraphs [0026] to [0037] of US Patent Application Publication No. 2005/065045 (and granted as U.S. Pat. No. 7,407,919). The overbased detergent may be present at 0 wt % to 15 wt %, or 0.1 wt % to 10 wt %, or 0.2 wt % to 8 wt %, or 0.2 wt % to 3 wt %, based upon of the lubricating composition. For example, in a heavy-duty diesel engine, the detergent may be present at 2 wt % to 3 wt % of the lubricating composition. For a passenger car engine, the detergent may be present at 0.2 wt % to 1 wt % of the lubricating composition.
[0477] The detergent additive(s) may comprise one or more magnesium sulfonate detergents. The magnesium detergent may be a neutral salt or an overbased salt. Suitably the magnesium detergent is an overbased magnesium sulfonate having a TBN of from of from 5 to 700 mgKOH/g (ASTM D2896), or from 7 to 600 mgKOH/g, or from 9 to 500 mgKOH/g, or 80 to 650 mgKOH/g, such as 200 to 500 mgKOH/g, such as 240 to 450 mgKOH/g.
[0478] Alternately, the detergent additive(s) is a magnesium salicylate. Suitably the magnesium detergent is a magnesium salicylate having TBN of from 5 to 700 mgKOH/g (ASTM D2896), or from 7 to 600 mgKOH/g, or from 9 to 500 mgKOH/g, 30 to 650 mgKOH/g, such as 50 to 500 mgKOH/g, such as 200 to 500 mgKOH/g, such as 240 to 450 mgKOH/g or alternately of 150 mgKOH/g or less, such as 100 mgKOH/g or less.
[0479] Alternately, the detergent additive(s) is a combination of magnesium salicylate and magnesium sulfonate.
[0480] The magnesium detergent provides the lubricating composition thereof with from 500-4000 ppm of magnesium atoms, suitably from 700-2000 ppm, from 800 to 1500 or from 1000-1200 ppm of magnesium atoms (ASTM D5185).
[0481] The detergent composition may comprise (or consist of) a combination of one or more magnesium sulfonate detergents and one or more calcium salicylate detergents.
[0482] The detergent may comprise one or more calcium detergents such as calcium carboxylate (e.g., salicylate), sulfonate, or phenate detergent.
[0483] Suitably the calcium detergent has a TBN of from 30 to 1400 mgKOH/g (ASTM D2896), such as 80 to 1200 mgKOH/g, such as 100 to 1000 mgKOH/g, such as 150 to 800 mgKOH/g, such as 200 to 600 mgKOH/g, such as 240 to 550 mgKOH/g, or alternately of 150 mgKOH/g or less, such as 100 mgKOH/g or less, or 200 mgKOH/g or more, or 300 mgKOH/g or more, or 350 mgKOH/g or more. The calcium detergent preferably has a TBN of greater than or equal 500, or 600, or 700, or 800, or 1000, or 1200, or 1300, or 1400 mgKOH/g.
[0484] Suitably, the calcium detergent is a calcium salicylate, sulfonate, or phenate having a TBN of from 30 to 1400 mgKOH/g, 30 to 1200 mgKOH/g (ASTM D2896), such as 50 to 1000 mgKOH/g, such as 200 to 800 mgKOH/g, such as 240 to 600 mgKOH/g or alternately of 150 mgKOH/g or less, such as 100 mgKOH/g or less, or 200 mgKOH/g or more, or 300 mgKOH/g or more, or 350 mgKOH/g or more, or 500 mgKOH/g or more, or 700 mgKOH/g or more, or 900 mgKOH/g or more, or 1100 mgKOH/g or more, or 1300 mgKOH/g or more.
[0485] Calcium detergent is typically present in amount sufficient to provide at least 400 ppm, or at least 500 ppm, or at least 520 ppm, or at least 540 ppm, or at least 560 ppm, or at least 580 ppm, or at least 600 ppm, or at least 650 ppm, or at least 700 ppm, or at least 750 ppm, or at least 800 ppm, or at least 850 ppm, or at least 900 ppm, or at least 1000 ppm, or at least 1100 ppm, or at least 1200 ppm by weight of calcium to the composition (ASTM D5185).
[0486] Suitably the total atomic amount of metal from detergent in the lubrication composition according to all aspects of the disclosure is no more than 5000 ppm, preferably no more than 4000 pm and more preferably no more than 2000 ppm (ASTM D5185). The total amount of atomic metal from detergent in the lubrication oil composition according to all aspects of the disclosure is suitably at least 500 ppm, preferably at least 800 ppm and more preferably at least 1000 ppm (ASTM D5185). The total amount of atomic metal from detergent in the lubrication oil composition according to all aspects of the disclosure is suitably from 500 to 5000 ppm, preferably from 500 to 3000 ppm and more preferably from 500 to 2500 ppm (ASTM D5185).
[0487] Sulfonate detergents may be prepared from sulfonic acids which are typically obtained by the sulfonation of alkyl substituted aromatic hydrocarbons, such as those obtained from the fractionation of petroleum or by the alkylation of aromatic hydrocarbons. Examples include those obtained by alkylating benzene, toluene, xylene, naphthalene, diphenyl, or their halogen derivatives such as chlorobenzene, chlorotoluene, and chloronaphthalene. The alkylation may be carried out in the presence of a catalyst with alkylating agents having from about 3 to more than 70 carbon atoms. The alkaryl sulfonates usually contain from about 9 to about 80 or more carbon atoms, preferably from about 16 to about 60 carbon atoms per alkyl substituted aromatic moiety. The oil soluble sulfonates or alkaryl sulfonic acids may be neutralized with oxides, hydroxides, alkoxides, carbonates, carboxylate, sulfides, hydrosulfides, nitrates, borates and ethers of the metal. The amount of metal compound is chosen having regard to the desired TBN of the final product, but typically ranges from about 100 to 220 mass (preferably at least 125 mass %) of that stoichiometrically required.
[0488] Metal salts of phenols and sulfurized phenols are prepared by reaction with an appropriate metal compound such as an oxide or hydroxide and neutral or overbased products may be obtained by methods well known in the art. Sulfurized phenols may be prepared by reacting a phenol with sulfur or a sulfur-containing compound such as hydrogen sulfide, sulfur monohalide, or sulfur dihalide, to form products which are generally mixtures of compounds in which 2 or more phenols are bridged by sulfur-containing bridges.
[0489] Carboxylate detergents, e.g., salicylates, can be prepared by reacting an aromatic carboxylic acid (such as a C.sub.5-100, C.sub.9-30, C.sub.14-24 alkyl-substituted hydroxy-benzoic acid) with an appropriate metal compound such as an oxide or hydroxide and neutral or overbased products may be obtained by methods well known in the art. The aromatic moiety of the aromatic carboxylic acid can contain heteroatoms, such as nitrogen and oxygen. Preferably, the moiety contains only carbon atoms; more preferably the moiety contains six or more carbon atoms; for example, benzene is a preferred moiety. The aromatic carboxylic acid may contain one or more aromatic moieties, such as one or more benzene rings, either fused or connected via alkylene bridges.
[0490] Preferred substituents in oil-soluble salicylic acids are alkyl substituents. In alkyl-substituted salicylic acids, the alkyl groups advantageously contain 5 to 100, preferably 9 to 30, especially 14 to 20, carbon atoms. Where there is more than one alkyl group, the average number of carbon atoms in all of the alkyl groups is preferably at least 9 to ensure adequate oil solubility.
[0491] Further, as metal organic and inorganic base salts, which are used as detergents can contribute to the sulfated ash content of a lubricating oil composition, in embodiments of the present disclosure, the amounts of such additives are minimized. In order to maintain a low sulfur level, salicylate detergents can be used and the lubricating composition herein may comprise one or more salicylate detergents (said detergents are preferably used in amounts in the range of 0.05 to 20.0 wt %, more preferably from 1.0 to 10.0 wt % and most preferably in the range of from 2.0 to 5.0 wt %, based on the total weight of the lubricating composition).
[0492] The total sulfated ash content of the lubricating composition herein is typically not greater than 1.0 wt %, alternately at a level of not greater than 0.9 wt % and alternately at a level of not greater than 0.8 wt %, based on the total weight of the lubricating composition as determined by ASTM D874.
[0493] Furthermore, it is useful that each of the detergents, independently, have a TBN (total base number) value in the range of from 10 to 700 mgKOH/g, 10 to 500 mgKOH/g, alternately in the range of from 100 to 650, alternately in the range of from 10 to 500 mgKOH/g, alternately in the range of from 30 to 350 mgKOH/g, and alternately in the range of from 50 to 300 mgKOH/g, as measured by ISO 3771.
[0494] The sulfonate detergents (such as Ca and/or Mg sulfonate detergents) may be present in an amount to deliver 0.1 wt % to 1.5 wt %, or 0.15 to 1.2 wt %, or 0.2 wt % to 0.9 wt % sulfonate soap to the lubricant composition.
[0495] The salicylate detergents (such as Ca and/or Mg salicylate detergents) are present in an amount to deliver 0.3 wt % to 1.4 wt %, or 0.35 wt % to 1.2 wt %, or 0.4 wt % to 1.0 wt % salicylate soap to the lubricant composition.
[0496] The sulfonate soap may be present in an amount 0.2 wt % to 0.8 wt % of the lubricant composition, and the salicylate soap may be present in an amount 0.3 wt % to 1.0 wt % of the lubricant composition.
[0497] The total of all alkaline earth metal detergent soap may be present in an amount 0.6 wt % to 2.1 wt %, or 0.7 wt % to 1.4 wt % of the lubricant composition.
[0498] Typically, lubricating compositions formulated for use in heavy-duty diesel engines comprise detergents at from about 0.1 to about 10 mass %, alternately from about 0.5 to about 7.5 mass alternately from about 1 to about 6.5 mass %, based on the lubricating composition.
[0499] Typically, lubricating compositions formulated for use in a passenger-car engines comprise detergents at from about 0.1 to about 10 mass %, alternately from about 0.5 to about 7.5 mass alternately from about 1 to about 6.5 mass %, based on the lubricating composition.
[0500] Typically, lubricating compositions formulated for use in a drive train (e.g., transmissions) comprise detergents at from about 0.1 to about 10 mass %, alternately from about 0.5 to about 7.5 mass %, alternately from about 2 to about 6.5 mass %, based on the lubricating composition.
D. Friction Modifiers
[0501] A friction modifier is any material or materials that can alter the coefficient of friction of a surface lubricated by any lubricant or fluid-containing such material(s). Friction modifiers, also known as friction reducers, or lubricity agents or oiliness agents, and other such agents that change the ability of base oils, formulated lubricating compositions, concentrate compositions or functional fluids, to modify the coefficient of friction of a lubricated surface may be effectively used in combination with the base oils or lubricating compositions of the present disclosure if desired. Friction modifiers that lower the coefficient of friction are particularly advantageous in combination with the base oils and lubricating compositions of this disclosure.
[0502] Illustrative friction modifiers may include, for example, organometallic compounds or materials, or mixtures thereof. Illustrative organometallic friction modifiers useful in the lubricating oil formulations of this disclosure include, for example, tungsten and/or molybdenum compounds, such as molybdenum amine, molybdenum diamine, an organotungstenate, a molybdenum dithiocarbamate, molybdenum dithiophosphates, molybdenum amine complexes, molybdenum carboxylates, and the like, and mixtures thereof. Examples of useful molybdenum-containing compounds may conveniently include molybdenum dithiocarbamates, trinuclear molybdenum compounds, for example, as described in PCT Publication No. WO 98/26030, sulfides of molybdenum and molybdenum dithiophosphate.
[0503] Other known friction modifiers comprise oil-soluble organo-molybdenum compounds. Such organo-molybdenum friction modifiers may also provide antioxidant and antiwear credits to a lubricating oil composition. Examples of such oil-soluble organo-molybdenum compounds include dithiocarbamates, dithiophosphates, dithiophosphinates, xanthates, thioxanthates, sulfides, and the like, and mixtures thereof. Particularly preferred are molybdenum dithiocarbamates, dialkyldithiophosphates, alkyl xanthates and alkylthioxanthates.
[0504] Additionally, the molybdenum compound may be an acidic molybdenum compound. These compounds will react with a basic nitrogen compound as measured by ASTM test D664 or D2896 titration procedure and are typically hexavalent. Included are molybdic acid, ammonium molybdate, sodium molybdate, potassium molybdate, and other alkali metal molybdates and other molybdenum salts, e.g., hydrogen sodium molybdate, MoOC.sub.14, MoO.sub.2Br2, Mo.sub.2O.sub.3C.sub.36, molybdenum trioxide or similar acidic molybdenum compounds.
[0505] Among the molybdenum compounds useful in the compositions of this disclosure are organo-molybdenum compounds of the formula Mo(ROCS.sub.2).sub.4 and Mo(RSCS.sub.2).sub.4, wherein R is an organo group selected from the group consisting of alkyl, aryl, aralkyl and alkoxyalkyl, generally of from 1 to 30 carbon atoms, and preferably 2 to 12 carbon atoms and most preferably alkyl of 2 to 12 carbon atoms. Especially preferred are the dialkyldithiocarbamates of molybdenum.
[0506] Another group of organo-molybdenum compounds useful in the lubricating compositions of this disclosure are trinuclear molybdenum compounds, especially those of the formula Mo3SkLnQz and mixtures thereof wherein the L are independently selected ligands having organo groups with a sufficient number of carbon atoms to render the compound soluble or dispersible in the oil, n is from 1 to 4, k varies from 4 to 7, Q is selected from the group of neutral electron-donating compounds such as water, amines, alcohols, phosphines, and ethers, and z ranges from 0 to 5 and includes non-stoichiometric values. At least 21 carbon atoms should be present among all the ligand/organo groups, such as at least 25, at least 30, or at least 35, carbon atoms.
[0507] Lubricating oil compositions useful in all aspects of the present disclosure preferably contain at least 10 ppm, or at least 12 ppm, or at least 20 ppm molybdenum. Suitably, lubricating oil compositions useful in all aspects of the present disclosure contain no more than 1000 ppm, no more than 750 ppm, no more than 500 ppm, no more than 350 ppm, or more preferably no more than 200 ppm of molybdenum. Lubricating oil compositions useful in all aspects of the present disclosure preferably contain from 12 to 350 ppm, such as 12 to 500 ppm, or 20 to 200 ppm of molybdenum (measured as atoms of molybdenum).
[0508] For more information or useful friction modifiers containing Mo, please see U.S. Pat. No. 10,829,712 (col 8, ln 58 to col 11, ln 31). Particularly preferred friction modifiers containing Mo of the instant disclosure are dimeric molybdenum dialkyldithiocarbamate (moly dimer), a trimeric molybdenum dialkyldithiocarbamate (moly trimer), or a combination thereof.
[0509] Ashless friction modifiers may be present in the lubricating oil compositions of the present disclosure and are known generally and include esters formed by reacting carboxylic acids and anhydrides with alkanols and amine-based friction modifiers. Other useful friction modifiers generally include a polar terminal group (e.g., carboxyl or hydroxyl) covalently bonded to an oleophilic hydrocarbon chain. Esters of carboxylic acids and anhydrides with alkanols are described in U.S. Pat. No. 4,702,850. Examples of other conventional organic friction modifiers are described by M. Belzer in the Journal of Tribology (1992), Vol. 114, pp. 675-682 and M. Belzer and S. Jahanmir in Lubrication Science (1988), Vol. 1, pp. 3-26. Typically, the total amount of organic ashless friction modifier in a lubricant according to the present disclosure does not exceed 5 mass %, based on the total mass of the lubricating oil composition and preferably does not exceed 2 mass % and more preferably does not exceed 0.5 mass %.
[0510] Illustrative friction modifiers useful in the lubricating compositions described herein include, for example, alkoxylated fatty acid esters, alkanolamides, polyol fatty acid esters, borated glycerol fatty acid esters, fatty alcohol ethers, and mixtures thereof.
[0511] Illustrative alkoxylated fatty acid esters include, for example, polyoxyethylene stearate, fatty acid polyglycol ester, and the like. These can include polyoxypropylene stearate, polyoxybutylene stearate, polyoxyethylene isostearate, polyoxypropylene isostearate, polyoxyethylene palmitate, and the like.
[0512] Illustrative alkanolamides include, for example, lauric acid diethylalkanolamide, palmic acid diethylalkanolamide, and the like. These can include oleic acid diethyalkanolamide, stearic acid diethylalkanolamide, oleic acid diethylalkanolamide, polyethoxylated hydrocarbylamides, polypropoxylated hydrocarbylamides, and the like.
[0513] Illustrative polyol fatty acid esters include, for example, glycerol monooleate, saturated mono-, di-, and tri-glyceride esters, glycerol monostearate, and the like. These can include polyol esters, hydroxyl-containing polyol esters, and the like.
[0514] Illustrative borated glycerol fatty acid esters include, for example, borated glycerol monooleate, borated saturated mono-, di-, and tri-glyceride esters, borated glycerol monosterate, and the like. In addition to glycerol polyols, these can include trimethylolpropane, pentaerythritol, sorbitan, and the like. These esters can be polyol monocarboxylate esters, polyol dicarboxylate esters, and on occasion polyoltricarboxylate esters. Preferred can be the glycerol monooleates, glycerol di-oleates, glycerol tri-oleates, glycerol mono-oleates, glycerol di-stearates, and glycerol tri-stearates and the corresponding glycerol mono-palmitates, glycerol di-palmitates, and glycerol tri-palmitates, and the respective isostearates, linoleates, and the like. Ethoxylated, propoxylated, and/or butoxylated fatty acid esters of polyols, especially using glycerol as underlying polyol are useful herein.
[0515] Illustrative fatty alcohol ethers include, for example, stearyl ether, myristyl ether, and the like. Alcohols, including those that have carbon numbers from C.sub.3 to C.sub.50, can be ethoxylated, propoxylated, or butoxylated to form the corresponding fatty alkyl ethers. The underlying alcohol portion can preferably be stearyl, myristyl, C.sub.11-C.sub.13 hydrocarbon, oleyl, isostearyl, and the like.
[0516] Useful concentrations of friction modifiers may range from 0.01 wt % to 5 wt %, or about 001 wt % to about 2.5 wt %, or about 0.05 wt % to about 1.5 wt %, or about 0.051 wt % to about 1 wt %. Concentrations of molybdenum-containing materials are often described in terms of Mo metal concentration. Advantageous concentrations of Mo may range from 12 ppm to 350 ppm or more, and often with a preferred range of 20 to 200 ppm. Friction modifiers of all types may be used alone or in mixtures with the materials of this disclosure. Often mixtures of two or more friction modifiers, or mixtures of fiction modifier(s) with alternate surface-active material(s), are also desirable. For example, combinations of Mo-containing compounds with polyol fatty acid esters, such as glycerol mono-oleate are useful herein.
E. Antioxidants
[0517] Antioxidants retard the oxidative degradation of base oils during service. Such degradation may result in deposits on metal surfaces, the presence of sludge, a viscosity increase in a lubricant, and the like. A wide variety of oxidation inhibitors that are useful in lubricating oil compositions. See Lubricants and Related Products, Klamann, Wiley VCH, 1984; U.S. Pat. Nos. 4,798,684 and 5,084,197, for example.
[0518] Useful antioxidants include hindered phenols. These phenolic antioxidants may be ashless (metal-free) phenolic compounds or neutral or basic metal salts of certain phenolic compounds. Typical phenolic antioxidant compounds are the hindered phenolics, which contain a sterically hindered hydroxyl group, and these include those derivatives of dihydroxy aryl compounds in which the hydroxyl groups are in the o- or p-position to each other. Typical phenolic antioxidants include the hindered phenols substituted with C.sub.6+ alkyl groups and the alkylene coupled derivatives of these hindered phenols. Examples of phenolic materials of this type 2-t-butyl-4-heptyl phenol; 2-t-butyl-4-octyl phenol; 2-t-butyl-4-dodecyl phenol; 2,6-di-t-butyl-4-heptyl phenol; 2,6-di-t-butyl-4-dodecyl phenol; 2-methyl-6-t-butyl-4-heptyl phenol; and 2-methyl-6-t-butyl-4-dodecyl phenol. Other useful hindered mono-phenolic antioxidants may include, for example, hindered 2,6-di-alkyl-phenolic proprionic ester derivatives. Bis-phenolic antioxidants may also be advantageously used herein. Examples of ortho-coupled phenols include: 2,2-bis(4-heptyl-6-t-butyl-phenol); 2,2-bis(4-octyl-6-t-butyl-phenol); and 2,2-bis(4-dodecyl-6-t-butyl-phenol). Para-coupled bisphenols include, for example, 4,4-bis(2,6-di-t-butyl-phenol) and 4,4-methylene-bis(2,6-di-t-butyl-phenol).
[0519] Effective amounts of one or more catalytic antioxidants may also be used. The catalytic antioxidants comprise an effective amount of a) one or more oil soluble polymetal organic compounds; and effective amounts of b) one or more substituted N,N-diaryl-o-phenylenediamine compounds or c) one or more hindered phenol compounds; or a combination of both b) and c). Catalytic antioxidants useful herein are more fully described in U.S. Pat. No. 8,048,833.
[0520] Non-phenolic oxidation inhibitors, which may be used include aromatic amine antioxidants and these may be used either as such or in combination with phenolics. Typical examples of non-phenolic antioxidants include: alkylated and non-alkylated aromatic amines such as aromatic monoamines of the formula R.sub.8R.sub.9R.sub.10N, where R.sub.8 is an aliphatic, aromatic or substituted aromatic group, R.sub.9 is an aromatic or a substituted aromatic group, and R.sub.10 is H, alkyl, aryl or R.sub.11S(O)XR.sub.12 where R.sub.11 is an alkylene, alkenylene, or aralkylene group, R.sub.12 is an alkyl group, or an alkenyl, aryl, or alkaryl group, and x is 0, 1, or 2. The aliphatic group R.sub.8 may contain from 1 to about 20 carbon atoms, and preferably contains from about 6 to 12 carbon atoms. The aliphatic group is typically a saturated aliphatic group. Preferably, both R.sub.8 and R.sub.9 are aromatic or substituted aromatic groups, and the aromatic group may be a fused ring aromatic group such as naphthyl. Aromatic groups R.sub.8 and R.sub.9 may be joined together with other groups such as S.
[0521] Typical aromatic amines antioxidants have alkyl substituent groups of at least about 6 carbon atoms. Examples of aliphatic groups include hexyl, heptyl, octyl, nonyl, and decyl. Generally, the aliphatic groups will not contain more than about 14 carbon atoms. The general types of amine antioxidants useful in the present compositions include diphenylamines, phenyl naphthylamines, phenothiazines, imidodibenzyls and diphenyl phenylene diamines. Mixtures of two or more aromatic amines are also useful. Polymeric amine antioxidants can also be used. Particular examples of aromatic amine antioxidants useful in the present disclosure include: p,p-dioctyldiphenylamine; t-octylphenyl-alpha-naphthylamine; phenyl-alpha-naphthylamine; and p-octylphenyl-alpha-naphthylamine.
[0522] Sulfur-containing antioxidants are also useful herein. In particular, one or more oil-soluble or oil-dispersible sulfur-containing antioxidant(s) can be used as an antioxidant additive. For example, sulfurized alkyl phenols and alkali or alkaline earth metal salts thereof also are useful antioxidants herein. Suitably, the lubricating oil composition(s) of the present disclosure may include the one or more sulfur-containing antioxidant(s) in an amount to provide the lubricating oil composition with from 0.02 to 0.2, preferably from 0.02 to 0.15, even more preferably 0.02 to 0.1, even more preferably 0.04 to 0.1, mass % sulfur based on the total mass of the lubricating oil composition. Optionally the oil-soluble or oil-dispersible sulfur-containing antioxidant(s) are selected from sulfurized C.sub.4 to C.sub.25 olefin(s), sulfurized aliphatic (C.sub.7 to C.sub.29)hydrocarbyl fatty acid ester(s), ashless sulfurized phenolic antioxidant(s), sulfur-containing organo-molybdenum compound(s), and combinations thereof. For further information on sulfurized materials useful as antioxidants herein, please see U.S. Pat. No. 10,731,101 (col 15, ln 55 to col 22, ln 12).
[0523] Antioxidants useful herein include hindered phenols and/or arylamines. These antioxidants may be used individually by type or in combination with one another.
[0524] Typical antioxidants include: Irganox L67, Irganox L135, Ethanox 4702, Lanxess Additin RC 7110; Ethanox 4782J; Irganox 1135, Irganox 5057, sulfurized lard oil and palm oil fatty acid methyl ester.
[0525] Antioxidant additives may be used in an amount of about 0.01 to 10 (alternately 0.01 to 5, alternately 0.01 to 3 wt %, alternately 1 to 6 wt %, alternately 2 to 5 wt %, alternately 3 to 4 wt %, alternately about 0.03 to 5 wt %, alternately 0.05 to less than 3 wt %, based upon the weight of the lubricating composition.
[0526] Compositions according to the present disclosure may contain an additive having a different enumerated function that also has secondary effects as an antioxidant (for example, phosphorus-containing antiwear agents (such as ZDDP) may also have antioxidant effects). These additives are not included as antioxidants for purposes of determining the amount of antioxidant in a lubricating oil composition or concentrate herein.
F. Pour Point Depressants
[0527] Conventional pour point depressants (also known as lube oil flow improvers) may be added to the compositions of the present disclosure if desired. These pour point depressants may be added to lubricating compositions of the present disclosure to lower the minimum temperature at which the fluid will flow or can be poured. Examples of suitable pour point depressants include polymethacrylates, polyacrylates, polyarylamides, condensation products of haloparaffin waxes and aromatic compounds, vinyl carboxylate polymers, and terpolymers of dialkylfumarates, vinyl esters of fatty acids and allyl vinyl ethers. U.S. Pat. Nos. 1,815,022; 2,015,748; 2,191,498; 2,387,501; 2,655,479; 2,666,746; 2,721,877; 2,721,878; and 3,250,715 describe useful pour point depressants and/or the preparation thereof. Such additives may be used in an amount of about 0.01 to 5 wt %, preferably about 0.01 to 1.5 wt %, based upon the weight of the lubricating composition.
G. Anti-Foam Agents
[0528] Anti-foam agents may advantageously be added to lubricant compositions described herein. These agents prevent or retard the formation of stable foams. Silicones and/organic polymers are typical anti-foam agents. For example, polysiloxanes, such as silicon oil or polydimethyl siloxane, provide anti-foam properties.
[0529] Anti-foam agents are commercially available and may be used in minor amounts such as 5 wt % or less, 3 wt % or less, 1 wt % or less, 0.1 wt % or less, such as from 5 to wt % to 0.1 ppm such as from 3 wt % to 0.5 ppm, such as from 1 wt % to 10 ppm.
[0530] For example, it may be that the lubricating oil composition comprises an anti-foam agent comprising polyalkyl siloxane, such as a polydialkyl siloxane, for example, wherein the alkyl is a C.sub.1-C.sub.10 alkyl group, e.g., a polydimethylsiloxane (PDMS), also known as a silicone oil. Alternately, the siloxane is a poly(R.sup.3)siloxane, wherein R.sup.3 is one or more same or different linear branched or cyclic hydrocarbyls, such as alkyls or aryls, typically having 1 to 20 carbon atoms. It may be that, for example, the lubricating oil composition comprises a polymeric siloxane compound according to Formula 1 below wherein R.sup.1 and R.sup.2 are independently methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, nonyl or decyl, phenyl, naphthyl, alkyl substituted phenyl, or isomers thereof (such as methyl, phenyl) and n is from 2 to 1000, such as 50 to 450, alternately such as 40 to 100.
[0531] Additionally, or alternatively, it may be that the lubricating oil composition comprises an organo-modified siloxane (OMS), such as a siloxane modified with an organo group such as a polyether (e.g., ethylene-propyleneoxide copolymer), long chain hydrocarbyl (e.g., C.sub.11-C.sub.100 alkyl), or aryl (e.g., C.sub.6-C.sub.14 aryl). It may be that, for example, the lubricating oil composition comprises an organo-modified siloxane compound according to Formula 1, wherein n is from 2 to 2000, such as 50 to 450 (alternately such as 40 to 100), and wherein R.sup.1 and R.sup.2 are the same or different, optionally wherein each of R.sup.1 and R.sup.2 is, independently an organo group, such as an organo group selected from polyether (e.g., ethylene-propyleneoxide copolymer), long chain hydrocarbyl (e.g., C.sub.11-C.sub.100 alkyl), or aryl (e.g., C.sub.6-C.sub.14 aryl). Preferably, one of R.sup.1 and R.sup.2 is CH.sub.3.
##STR00013##
[0532] Based on the total weight of the lubricant composition, the siloxane according to Formula 1 is incorporated so as to provide about 0.1 to less than about 30 ppm Si, or about 0.1 to about 25 ppm Si, or about 0.1 to about 20 ppm Si, or about 0.1 to about 15 ppm Si, or about 0.1 to about 10 ppm Si. More preferably, it is in the range of about 3-10 ppm Si.
[0533] In embodiments, silicone anti-foam agents useful herein are available from Dow Corning Corporation and Union Carbide Corporation, such as Dow Corning FS-1265 (1000 centistokes), Dow Corning DC-200, and Union Carbide UC-L45. Silicone anti-foamants useful herein include polydimethylsiloxane, phenyl-methyl polysiloxane, linear, cyclic or branched siloxanes, silicone polymers and copolymers, and/organo-silicone copolymers. Also, a siloxane polyether copolymer Anti-foamant available from OSI Specialties, Inc. of Farmington Hills, Michigan and may be substituted or included. One such material is sold as SILWET-L-7220.
[0534] Acrylate polymer anti-foam agent can also be used herein. Typical acrylate anti-foamants include polyacrylate anti-foamant available from Monsanto Polymer Products Co. known as PC-1244. A preferred acrylate polymer anti-foam agent useful herein is PX 3841 (i.e., an alkyl acrylate polymer), commercially available from Dorf Ketl, also referred to as Mobilad C402.
[0535] In embodiments, a combination of silicone anti-foamant and acrylate anti-foamant can be used, such as at a weight ratio of the silicone anti-foamant to the acrylate anti-foamant of from about 5:1 to about 1:5, see, for example, US Patent Application Publication No. 2021/0189283.
H. Viscosity Modifiers
[0536] Viscosity modifiers (also referred to as viscosity index improvers or viscosity improvers) can be included in the lubricating compositions and concentrate compositions described herein. Viscosity modifiers provide lubricants with high and low temperature operability. These additives impart shear stability at elevated temperatures and acceptable viscosity at low temperatures. Suitable viscosity modifiers include high molecular weight hydrocarbons, polyesters, and viscosity modifier dispersants that can function as both a viscosity modifier and a dispersant. Typical molecular weights of these polymers are between about 10,000 to 1,500,000 g/mol, more typically about 20,000 to 1,200,000 g/mol, and even more typically between about 50,000 and 1,000,000 g/mol.
[0537] Examples of suitable viscosity modifiers are linear or star-shaped polymers and copolymers of methacrylate, butadiene, olefins, or alkylated styrenes. Polyisobutylene is a commonly used viscosity modifier. Another suitable viscosity modifier is polymethacrylate (copolymers of various chain length alkyl methacrylates, for example), some formulations of which also serve as pour point depressants. Other suitable viscosity modifiers include copolymers of ethylene and propylene, hydrogenated block copolymers of styrene and isoprene, and polyacrylates (copolymers of various chain length acrylates, for example). Specific examples include styrene-isoprene or styrene-butadiene based polymers of 50,000 to 200,000 g/mol molecular weight.
[0538] Copolymers useful as viscosity modifiers include those commercially available from Chevron Oronite Company LLC under the trade designation PARATONE (such as PARATONE 8921, PARATONE 68231, and PARATONE 8941); from Afton Chemical Corporation under the trade designation HiTEC (such as HiTECT 5850B, and HiTEC 5777); and from The Lubrizol Corporation under the trade designation Lubrizol 7067C. Hydrogenated polyisoprene star polymers useful as viscosity modifiers herein include those commercially available from Infineum International Limited, e.g., under the trade designation SV200T and SV600T. Hydrogenated diene-styrene block copolymers useful as viscosity modifiers herein are commercially available from Infineum International Limited, e.g., under the trade designation SV 50.
[0539] Polymers useful as viscosity modifiers herein include polymethacrylate or polyacrylate polymers, such as linear polymethacrylate or polyacrylate polymers, such as those available from Evnoik Industries under the trade designation Viscoplex (e.g., Viscoplex 6-954) or star polymers which are available from Lubrizol Corporation under the trade designation Asteric (e.g., Lubrizol 87708 and Lubrizol 87725).
[0540] Vinyl aromatic-containing polymers useful as viscosity modifiers herein may be derived from vinyl aromatic hydrocarbon monomers, such as styrenic monomers, such as styrene. Illustrative vinyl aromatic-containing copolymers useful herein may be represented by the following general formula: A-B wherein A is a polymeric block derived predominantly from vinyl aromatic hydrocarbon monomer (such as styrene), and B is a polymeric block derived predominantly from conjugated diene monomer (such as isoprene).
[0541] Vinyl aromatic-containing polymers useful as viscosity modifiers may have a Kinematic viscosity at 100 C. of 20 cSt or less, such as 15 cSt or less, such as 12 cSt or less, but may be diluted (such as in Group I, II, and/or III basestock) to higher Kinematic viscosities at 100 C., such as to 40 cSt or more, such as 100 cSt or more, such as 1000 cSt or more, such as 1000 to 2000 cSt.).
[0542] Typically, the viscosity modifiers may be used in an amount of about 0.01 to about 10 wt %, such as about 0.1 to about 7 wt %, such as 0.1 to about 4 wt %, such as about 0.2 to about 2 wt %, such as about 0.2 to about 1 wt %, and such as about 0.2 to about 0.5 wt %, based on the total weight of the formulated lubricant composition.
[0543] Viscosity modifiers are typically added as concentrates, in large amounts of diluent oil. The as delivered viscosity modifier typically contains from 20 wt % to 75 wt % of an active polymer for polymethacrylate or polyacrylate polymers, or from 8 wt % to 20 wt % of an active polymer for olefin copolymers, hydrogenated polyisoprene star polymers, or hydrogenated diene-styrene block copolymers, in the as delivered polymer concentrate.
i) Dispersants
[0544] During engine operation, oil-insoluble oxidation byproducts are produced. Dispersants help keep these byproducts in solution, thus diminishing their deposition on metal surfaces. Dispersants used in the formulation of the lubricating compositions herein may be ashless or ash-forming in nature. Preferably, the dispersant is ashless. So called ashless dispersants are organic materials that form substantially no ash upon combustion. For example, non-metal-containing or borated metal-free dispersants are considered ashless. In contrast, metal-containing detergents tend to form ash upon combustion.
[0545] Dispersants useful herein typically contain a polar group attached to a relatively high molecular weight hydrocarbon chain. The polar group typically contains at least one element of nitrogen, oxygen, or phosphorus. Typical hydrocarbon chains contain 40 to 500, such as 50 to 400 carbon atoms.
Dispersants of (Poly)Alkenylsuccinic Derivatives
[0546] A particularly useful class of dispersants includes the (poly)alkenylsuccinic derivatives, typically produced by the reaction of a long chain hydrocarbyl-substituted succinic compound, usually a hydrocarbyl-substituted succinic anhydride, with a polyhydroxy or polyamino compound. The long chain hydrocarbyl group constituting the oleophilic portion of the molecule which confers solubility in the oil, is often a polyisobutylene group (typically the long chain hydrocarbyl group, such as a polyisobutylene group, has an Mn of 400 to 3000 g/mol, such as 450 to 2500 g/mol). Many examples of this type of dispersant are well known commercially and in the literature. Exemplary US Patents describing such dispersants include U.S. Pat. Nos. 3,172,892; 3,2145,707; 3,219,666; 3,316,177; 3,341,542; 3,444,170; 3,454,607; 3,541,012; 3,630,904; 3,632,511; 3,787,374 and 4,234,435. Other types of dispersants are described in U.S. Pat. Nos. 3,036,003; 3,200,107; 3,254,025; 3,275,554; 3,438,757; 3,454,555; 3,565,804; 3,413,347; 3,697,574; 3,725,277; 3,725,480; 3,726,882; 4,454,059; 3,329,658; 3,449,250; 3,519,565; 3,666,730; 3,687,849; 3,702,300; 4,100,082; 5,705,458. A further description of dispersants useful herein may be found, for example, in European Patent Applications Nos. 0 471 071 and 0 451 380, to which reference is made for this purpose.
[0547] Hydrocarbyl-substituted succinic acid and hydrocarbyl-substituted succinic anhydride derivatives are useful dispersants. In particular, succinimide, succinate esters, or succinate ester amides prepared by the reaction of a hydrocarbon-substituted succinic acid or anhydride compound (typically having at least 25 carbon atoms, such as 28 to 400 carbon atoms, in the hydrocarbon substituent), with at least one equivalent of a polyhydroxy or polyamino compound (such as an alkylene amine) are particularly useful herein. Hydrocarbyl-substituted succinic acid and hydrocarbyl-substituted succinic anhydride derivatives may have a number average molecular weight of at least 400 g/mol, such as at least 900 g/mol, such as at least 1500 g/mol, such as from 400 to 4000 g/mol, such as from 800 to 3000, such as from 2000 to 2800 g/mol, such from about 2100 to 2500 g/mol, and such as from about 2200 to about 2400 g/mol.
[0548] Succinimides, which are particularly useful herein, are formed by the condensation reaction between: 1) hydrocarbyl-substituted succinic anhydrides, such as polyisobutylene succinic anhydride (PIBSA); and 2) polyamine (PAM). Examples of suitable polyamines include: polyhydrocarbyl polyamines, polyalkylene polyamines, hydroxy-substituted polyamines, polyoxyalkylene polyamines, and combinations thereof. Examples of polyamines include tetraethylene pentamine, pentaethylene hexamine, tetraethylenepentamine (TEPA), pentaethylenehaxamine (PEHA), N-phenyl-p-phenylenediamine (ADPA), and other polyamines having an average of 5, 6, 7, 8, or 9 nitrogen atoms per molecule. Mixtures where the average number of nitrogen atoms per polyamine molecule is greater than 7 are commonly called heavy polyamines or H-PAMs and may be commercially available under trade names such as HPA and HPA-X from Dow Chemical, E-100T from Huntsman Chemical, et al. Examples of hydroxy-substituted polyamines include N-hydroxyalkyl-alkylene polyamines such as N-(2-hydroxyethyl)ethylene diamine, N-(2-hydroxyethyl)piperazine, and/or N-hydroxyalkylated alkylene diamines of the type described, for example, in U.S. Pat. No. 4,873,009. Examples of polyoxyalkylene polyamines include polyoxyethylene and/or polyoxypropylene diamines and triamines (as well as co-oligomers thereof) having an average Mn from about 200 to about 5000 g/mol. Products of this type are commercially available under the tradename Jeffamine. Representative examples of useful succinimides are shown in U.S. Pat. Nos. 3,087,936; 3,172,892; 3,219,666; 3,272,746; 3,322,670; 3,652,616; 3,948,800; and 6,821,307; and CA Patent No. 1,094,044.
[0549] The dispersants may comprise one or more, optionally borated, higher molecular weight (Mn 1600 g/mol or more, such as 1800 to 3000 g/mol) succinimides and one or more, optionally borated, lower molecular weight (Mn less than 1600 g/mol) succinimides, where the higher molecular weight may be 1600 to 3000 g/mol, such as 1700 to 2800 g/mol, such as 1800 to 2500 g/mol, such as 1850 to 2300 g/mol; and the lower molecular weight may be 600 to less than 1600 g/mol, such as 650 to 1500 g/mol, such as 700 to 1400 g/mol, such as 800 to 1300 g/mol, such as 850 to 1200 g/mol such as 900 to 1150 g/mol, such as 900 to 1000 g/mol. The higher molecular weight succinimide dispersant may be present in the lubricating composition in an amount of from 0.5 to 10 wt %, or from 0.8 to 6 wt %, or from 1.0 to 5 wt %, or from 1.5 to 5 wt %, or from 1.5 to 4.0 wt %; and the lower molecular weight succinimides dispersant may be present in the lubricating composition in an amount of from 1 to 5 wt %, or from 1.5 to 4.8 wt %, or from 1.8 to 4.6 wt %, or from 1.9 to 4.6 wt %, or at 2 wt % or more, such as 2 to 5 wt %. The lower molecular weight succinimides may differ from the higher molecular weight succinimides, by 500 g/mol or more, such as by 750 g/mol or more, such as by 1000 g/mol or more, such as by 1200 g/mol or more, such as by 500 to 3000 g/mol, such as by 750 to 2000 g/mol, such as by 1000 to 1500 g/mol.
[0550] Succinate esters useful as dispersants include those formed by the condensation reaction between hydrocarbyl-substituted succinic anhydrides and alcohols or polyols. For example, the condensation product of a hydrocarbyl-substituted succinic anhydride and pentaerythritol is a useful dispersant.
[0551] Succinate ester amides useful herein are formed by a condensation reaction between hydrocarbyl-substituted succinic anhydrides and alkanol amines. Suitable alkanol amines include ethoxylated polyalkylpolyamines, propoxylated polyalkylpolyamines, and polyalkenylpolyamines such as polyethylene polyamines and/or propoxylated hexamethylenediamine. Representative examples are shown in U.S. Pat. No. 4,426,305.
[0552] Hydrocarbyl-substituted succinic anhydrides (such as PIBSA) esters of hydrocarbyl bridged aryloxy alcohols are also useful as dispersants herein. For information on such dispersants, please see U.S. Pat. No. 7,485,603, particularly, col 2, ln 65 to col 6, ln 22 and col 23, ln 40 to col 26, ln 46. In particular, PIBSA esters of methylene-bridged naphthyloxy ethanol (i.e., 2-hydroxyethyl-1-naphthol ether (or hydroxy-terminated ethylene oxide oligomer ether of naphthol) are useful herein.
[0553] The molecular weight of the hydrocarbyl-substituted succinic anhydrides used in the preceding paragraphs will typically range from 350 to 4000 g/mol, such as 400 to 3000 g/mol, such as 450 to 2800 g/mol, such as 800 to 2500 g/mol. The above (poly)alkenylsuccinic derivatives can be post-reacted with various reagents such as sulfur, oxygen, formaldehyde, carboxylic acids such as oleic acid.
[0554] The dispersants may be present in the lubricant in an amount 0.1 mass % to 20 mass % of the composition, such as 0.2 to 15 mass %, such as 0.25 to 10 mass %, such as 0.3 to 5 mass %, such as 1.0 mass % to 3.0 mass %, of the lubricating oil composition.
[0555] The above (poly)alkenylsuccinic derivatives, can also be post reacted with boron compounds such as boric acid, borate esters or highly borated dispersants, to form borated dispersants generally having from about 0.1 to about 5 moles of boron per mole of dispersant reaction product.
[0556] Dispersants useful herein include borated succinimides, including those derivatives from mono-succinimides, bis-succinimides, and/or mixtures of mono- and bis-succinimides, wherein the hydrocarbyl succinimide is derived from a hydrocarbylene group such as polyisobutylene having an Mn of from about 300 to about 5000 g/mol, or from about 500 to about 3000 g/mol, or about 1000 to about 2000 g/mol, or a mixture of such hydrocarbylene groups, often with high terminal vinylic groups.
[0557] The boron-containing dispersant may be present at 0.01 wt % to 20 wt %, or 0.1 wt % to 15 wt %,or 0.1 wt % to 10 wt %,or 0.5 wt % to 8 wt %,or 1.0 wt % to 6.5 wt %,or 0.5 wt % to 2.2 wt % of the lubricating composition.
[0558] The boron-containing dispersant may be present in an amount to deliver boron to the composition at 15 ppm to 2000 ppm, or 25 ppm to 1000 ppm, or 40 ppm to 600 ppm, or 80 ppm to 350 ppm.
[0559] The borated dispersant may be used in combination with non-borated dispersant and may be the same or different compound as the non-borated dispersant. In one embodiment, the lubricating composition may include one or more boron-containing dispersants and one or more non-borated dispersants, wherein the total amount of dispersant may be 0.01 wt % to 20 wt %, or 0.1 wt % to 15 wt %,or 0.1 wt % to 10 wt %,or 0.5 wt % to 8 wt %,or 1.0 wt % to 6.5 wt %,or 0.5 wt % to 2.2 wt % of the lubricating composition and wherein the ratio of borated dispersant to non-boroated dispersant may be 1:10 to 10:1 (weight:weight) or 1:5 to 3:1 or 1:3 to 2:1.
[0560] The dispersant may comprise one or more borated or unborated poly(alkenyl)succinimides, where the polyalkyenyl is derived from polyisobutylene and the imide is derived from a polyamine (PIBSA-PAM).
[0561] The dispersant may comprise one or more PIBSA-PAMs, where the PIB is derived from polyisobutylene having an Mn of from 600 to 5000, such as from 700 to 4000, such as from 800 to 3000, such as from 900 to 2500 g/mol and the polyamine is derived from hydrocarbyl-substituted polyamines, such as tetraethylene pentamine, pentaethylene hexamine, tetraethylenepentamine (TEPA), pentaethylenehaxamine (PEHA), N-phenyl-p-phenylenediamine (ADPA), and other polyamines having an average of 5, 6, 7, 8, or 9 nitrogen atoms per molecule). The dispersant may be borated, typically at levels of up to 4 mass % such as from 1 to 3 mass %. The dispersant may comprise one or more borated and one or more non-borated PIBSA-PAM's. The dispersant may comprise one or more borated PIBSA-PAM's derived from a PIB having an Mn of 700 to 1800 g/mol (such as 800 to 1500 g/mol) and one or more non-borated PIBSA-PAM's derived from a PIB having an Mn of more than 1800 to 5000 g/mol (such as 2000 to 3000 g/mol). The dispersant may comprise one or more non-borated PIBSA-PAM's derived from a PIB having an Mn of 700 to 1800 g/mol (such as 800 to 1500 g/mol) and one or more borated PIBSA-PAM's derived from a PIB having an Mn of more than 1800 to 5000 g/mol (such as 2000 to 3000 g/mol).
[0562] The dispersant may comprise PIBSA derived from a PIB having an Mn of 700 to 5000 g/mol (such as 800 to 3000 g/mol) and one or more borated or non-borated PIBSA-PAM's derived from a PIB having an Mn of 700 to 5000 g/mol.
[0563] The dispersant may comprise PIBSA derived from a PIB having an Mn of 700 to 5000 g/mol (such as 800 to 3000 g/mol) and one or more borated PIBSA-PAM's derived from a PIB having an Mn of 700 to 1800 g/mol (such as 800 to 1500 g/mol) and one or more non-borated PIBSA-PAM's derived from a PIB having an Mn of more than 1800 to 5000 g/mol (such as 2000 to 3000 g/mol). The dispersant may comprise PIBSA derived from a PIB having an Mn of 700 to 5000 g/mol (such as 800 to 3000 g/mol) one or more non-borated PIBSA-PAM's derived from a PIB having an Mn of 700 to 1800 g/mol (such as 800 to 1500 g/mol) and one or more borated PIBSA-PAM's derived from a PIB having an Mn of more than 1800 to 5000 g/mol (such as 2000 to 3000 g/mol).
[0564] The dispersant may comprise one or more borated or non-borated PIBSA-PAM's and one or more PIBSA-esters of hydrocarbyl bridged aryloxy alcohols.
[0565] The dispersant may comprise one or more borated and one or more non-borated PIBSA-PAM's.
[0566] The dispersant may comprise one or more, optionally borated, higher molecular weight (Mn 1600 g/mol or more, such as 1800 to 3000 g/mol) PIBSA-PAM's and one or more, optionally borated, lower molecular weight (Mn less than 1600 g/mol) PIBSA-PAM's, where the higher molecular weight may be 1600 to 3000 g/mol, such as 1700 to 2800 g/mol, such as 1800 to 2500 g/mol, such as 1850 to 2300 g/mol; and the lower molecular weight may be 600 to less than 1600 g/mol, such as 650 to 1500 g/mol, such as 700 to 1400 g/mol, such as 800 to 1300 g/mol, such as 850 to 1200 g/mol, such as 900 to 11500 g/mol, such as 900 to 100 g/mol. The higher molecular weight PIBSA-PAM dispersant may be present in the lubricating composition in an amount of from 0.5 to 10 wt %, or from 0.8 to 6 wt %, or from 1.0 to 5 wt %, or from 1.5 to 5 wt % or from 1.5 to 4.0 wt %; and the lower molecular weight PIBSA-PAM dispersant may be present in the lubricating composition in an amount of from 1 to 5 wt %, or from 1.5 to 4.8 wt %, or from 1.8 to 4.6 wt %, or from 1.9 to 4.6 wt %, or at 2 wt % or more, such as 2 to 5 wt %.
[0567] In one preferred form, the dispersant may comprise one or more, optionally borated, higher molecular weight (Mn 1600 g/mol or more) PIBSA-PAM's and one or more, optionally borated, lower molecular weight (Mn less than 1600 g/mol) PIBSA-PAM's, where the higher molecular weight PIBSA-PAM's are included in the lubricating oil composition at less than or equal to 2.5 wt %, or less than or equal to 1.5 wt %, or less than or equal to 0.5 wt %, or 0.0 wt %. In the preferred form wherein the dispersant comprises one or more, optionally borated, higher molecular weight (Mn 1600 g/mol or more) PIBSA-PAM's and one or more, optionally borated, lower molecular weight (Mn less than 1600 g/mol) PIBSA-PAM's, the treat level of the combination of the higher molecular weight PIBSA-PAM's and the lower molecular weight PIBSA-PAM's may range for 1.0 to 6.0 wt %, or 1.5 to 5.5 wt %, or 2.0 to 5.0 wt %, or 2.5 to 4.5 wt %, or 3.0 to 4.0 wt %.
Dispersants of Mannich Bases
[0568] Mannich base dispersants useful herein are typically made from the reaction of an amine component, a hydroxy aromatic compound (substituted or unsubstituted, such as alkyl substituted), such as alkylphenols, and an aldehyde, such as formaldehyde. See U.S. Pat. Nos. 4,767,551 and 10,899,986. Process aids and catalysts, such as oleic acid and sulfonic acids, can also be part of the reaction mixture. Representative examples are shown in U.S. Pat. Nos. 3,697,574; 3,703,536; 3,704,308; 3,751,365; 3,756,953; 3,798,165; 3,803,039; 4,231,759; 9,938,479; 7,491,248; and 10,899,986, and PCT Publication No. WO 01/42399.
Dispersants of Polymethacrylate or Polyacrylate Derivatives
[0569] Polymethacrylate or polyacrylate derivatives are another class of dispersants useful herein. These dispersants are typically prepared by reacting a nitrogen-containing monomer and a methacrylic or acrylic acid esters containing 5-25 carbon atoms in the ester group. Representative examples are shown in U.S. Pat. Nos. 2,100,993, and 6,323,164. Polymethacrylate and polyacrylate dispersants are typically lower molecular weights.
[0570] The lubricating composition of the disclosure typically comprises dispersant at 0.1 mass % to 20 mass % of the composition, such as 0.2 to 15 mass %, such as 0.25 to 10 mass %, such as 0.3 to 5 mass %, such as 2.0 mass % to 4.0 mass % of the lubricating oil composition. Alternately the dispersant may be present at 0.1 wt % to 5 wt %, or 0.01 wt % to 4 wt % of the lubricating composition.
[0571] For further information on dispersants useful herein, please see U.S. Pat. No. 10,829,712, col 13, in 36 to col 16, in 67 and U.S. Pat. No. 7,485,603, col 2, in 65 to col 6, in 22, col 8, in 25 to col 14, in 53, and col 23, in 40 to col 26, in 46.
[0572] Compositions according to the present disclosure may contain an additive having a different enumerated function that also has secondary effects as a dispersant (for example, Component B Functionalized Polymer described above, may also have dispersant effects). These additives are not included as dispersants for purposes of determining the amount of dispersant in a lubricating oil composition or concentrate herein.
J. Corrosion Inhibitors/Anti-Rust Agents
[0573] Corrosion inhibitors may be used to reduce the corrosion of metals and are often alternatively referred to as metal deactivators or metal passivators. Some corrosion inhibitors may alternatively be characterized as antioxidants.
[0574] Suitable corrosion inhibitors may include nitrogen and/or sulfur-containing heterocyclic compounds such as triazoles (e.g., benzotriazoles), substituted thiadiazoles, imidazoles, thiazoles, tetrazoles, hydroxyquinolines, oxazolines, imidazolines, thiophenes, indoles, indazoles, quinolines, benzoxazines, dithiols, oxazoles, oxatriazoles, pyridines, piperazines, triazines and derivatives of any one or more thereof. A particular corrosion inhibitor is a benzotriazole represented by the structure:
##STR00014##
wherein R.sup.8 is absent (hydrogen) or is a C.sub.1 to C.sub.20 hydrocarbyl or substituted hydrocarbyl group which may be linear or branched, saturated or unsaturated. It may contain ring structures that are alkyl or aromatic in nature and/or contain heteroatoms such as N, O, or S. Examples of suitable compounds may include benzotriazole, alkyl-substituted benzotriazoles (e.g., tolyltriazole, ethylbenzotriazole, hexylbenzotriazole, octylbenzotriazole, etc.), aryl substituted benzotriazole, alkylaryl- or arylalkyl-substituted benzotriazoles, and the like, as well as combinations thereof. For instance, the triazole may comprise or be a benzotriazole and/or an alkylbenzotriazole in which the alkyl group contains from 1 to about 20 carbon atoms or from 1 to about 8 carbon atoms. Non-limiting examples of such corrosion inhibitors may comprise or be benzotriazole, tolyltriazole, and/or optionally, substituted benzotriazoles such as Irgamet 39, which is commercially available from BASF of Ludwigshafen, Germany. A preferred corrosion inhibitor may comprise or be benzotriazole and/or tolyltriazole.
[0575] Additionally, or alternatively, the corrosion inhibitor may include one or more substituted thiadiazoles represented by the structure:
##STR00015##
wherein R.sub.15 and R.sub.16 are independently hydrogen or a hydrocarbon group, which group may be aliphatic or aromatic, including cyclic, alicyclic, aralkyl, aryl and alkaryl, and wherein each w is independently 1, 2, 3, 4, 5, or 6 (preferably 2, 3, or 4, such as 2). These substituted thiadiazoles are derived from the 2,5-dimercapto-1,3,4-thiadiazole (DMTD) molecule. Many derivatives of DMTD have been described in the art, and any such compounds may be included in the fluid used in the present disclosure. For example, U.S. Pat. Nos. 2,719,125; 2,719,126; and 3,087,937; describe the preparation of various 2, 5-bis-(hydrocarbon dithio)-1,3,4-thiadiazoles.
[0576] Further, additionally or alternatively, the corrosion inhibitor may include one or more other derivatives of DMTD, such as a carboxylic ester in which R.sub.15 and R.sub.16 may be joined to the sulfide sulfur atom through a carbonyl group. Preparation of these thioester-containing DMTD derivatives is described, for example, in U.S. Pat. No. 2,760,933. DMTD derivatives produced by condensation of DMTD with alpha-halogenated aliphatic carboxylic acids having at least 10 carbon atoms are described, for example, in U.S. Pat. No. 2,836,564. This process produces DMTD derivatives wherein R.sub.15 and R.sub.16 are HOOCCH(R.sub.19)(R.sub.19 being a hydrocarbyl group). DMTD derivatives further produced by amidation or esterification of these terminal carboxylic acid groups may also be useful.
[0577] The preparation of 2-hydrocarbyldithio-5-mercapto-1,3,4-thiadiazoles is described, for example, in U.S. Pat. No. 3,663,561.
[0578] A class of DMTD derivatives may include mixtures of a 2-hydrocarbyldithio-5-mercapto-1,3,4-thiadiazole and a 2,5-bis-hydrocarbyldithio-1,3,4-thiadiazole. Such mixtures may be sold under the tradename HiTEC 4313 and are commercially available from Afton Chemical Company.
[0579] The preparation of 2-hydrocarbyldithio-5-mercapto-1,3,4-thiadiazoles is described, for example, in U.S. Pat. No. 3,663,561.
[0580] A class of DMTD derivatives may include mixtures of a 2-hydrocarbyldithio-5-mercapto-1,3,4-thiadiazole and a 2,5-bis-hydrocarbyldithio-1,3,4-thiadiazole. Such mixtures may be sold under the tradename HiTEC 4313 and are commercially available from Afton Chemical Company.
[0581] Still further, additionally or alternatively, the corrosion inhibitor may include a trifunctional borate having the structure, B(OR.sub.46).sub.3, in which each R.sub.46 may be the same or different. As the borate may typically be desirably compatible with the non-aqueous medium of the composition, each R.sub.46 may, in particular, comprise or be a hydrocarbyl C.sub.1-C.sub.8 moiety. For compositions in which the non-aqueous medium comprises or is a lubricating oil basestock, for example, better compatibility can typically be achieved when the hydrocarbyl moieties are each at least C.sub.4. Non-limiting examples of such corrosion inhibitors thus include, but are not limited to, triethylborate, tripropylborates such as triisopropylborate, tributylborates such as tri-tert-butylborate, tripentylborates, trihexylborates, trioctylborates such as tri-(2-ethylhexyl)borate, monohexyl dibutylborate, and the like, as well as combinations thereof.
[0582] When used, a corrosion inhibitor may comprise a substituted thiadiazole, a substituted benzotriazole, a substituted triazole, a trisubstituted borate, or a combination thereof.
[0583] When desired, corrosion inhibitors can be used in any effective amount, but, when used, may typically be used in amounts from about 0.001 wt % to 5.0 wt %, based on the weight of the composition, e.g., from 0.005 wt % to 3.0 wt % or from 0.01 wt % to 1.0 wt %. Alternately, such additives may be used in an amount of about 0.01 to 5 wt %, preferably about 0.01 to 1.5 wt %, based upon the weight of the lubricating composition.
[0584] In some embodiments, 3,4-oxypyridinone-containing compositions may contain substantially no (e.g., 0, or less than 0.001 wt %, 0.0005 wt % or less, not intentionally added, and/or absolutely no) triazoles, benzotriazoles, substituted thiadiazoles, imidazoles, thiazoles, tetrazoles, hydroxyquinolines, oxazolines, imidazolines, thiophenes, indoles, indazoles, quinolines, benzoxazines, dithiols, oxazoles, oxatriazoles, pyridines, piperazines, triazines, derivatives thereof, combinations thereof, or all corrosion inhibitors.
[0585] Compositions according to the present disclosure may contain an additive having a different enumerated function that also has secondary effects as a corrosion inhibitor (for example, Component B Functionalized Polymer described above, may also have corrosion inhibitor effects). These additives are not included as corrosion inhibitor for purposes of determining the amount of corrosion inhibitor in a lubricating oil composition or concentrate herein.
K. Antiwear Agents
[0586] The lubricating oil compositions and concentrate compositions of the present disclosure can contain one or more antiwear agents that can reduce friction and excessive wear. Any antiwear agent known by a person of ordinary skill in the art may be used in the lubricating oil composition. Non-limiting examples of suitable antiwear agents include zinc dithiophosphate, metal (e.g., Pb, Sb, Mo, and the like) salts of dithiophosphates, metal (e.g., Zn, Pb, Sb, Mo, and the like) salts of dithiocarbamates, metal (e.g., Zn, Pb, Sb, and the like) salts of fatty acids, boron compounds, phosphate esters, phosphite esters, amine salts of phosphoric acid esters or thiophosphoric acid esters, reaction products of dicyclopentadiene and thiophosphoric acids and combinations thereof. The amount of the antiwear agent may vary from about 0.01 wt % to about 5 wt %, from about 0.05 wt % to about 3 wt %, or from about 0.1 wt % to about 1 wt %, based on the total weight of the lubricating oil composition.
[0587] In embodiments, the antiwear agent is or comprises a dihydrocarbyl dithiophosphate metal salt, such as zinc dialkyl dithiophosphate compounds. The metal of the dihydrocarbyl dithiophosphate metal salt may be an alkali or alkaline earth metal, or aluminum, lead, tin, molybdenum, manganese, nickel, or copper. In some embodiments, the metal is zinc. In other embodiments, the alkyl group of the dihydrocarbyl dithiophosphate metal salt has from about 3 to about 22 carbon atoms, from about 3 to about 18 carbon atoms, from about 3 to about 12 carbon atoms, or from about 3 to about 8 carbon atoms. In further embodiments, the alkyl group is linear or branched.
[0588] Useful antiwear agents also include substituted or unsubstituted thiophosphoric acids, and salts thereof include zinc-containing compounds such as zinc dithiophosphate compounds selected from zinc dialkyl-, diaryl- and/or alkylaryl-dithiophosphates.
[0589] A metal alkylthiophosphate and more particularly a metal dialkyl dithio phosphate in which the metal constituent is zinc, or zinc dialkyl dithio phosphate (ZDDP) can be a useful component of the lubricating compositions of this disclosure. ZDDP can be derived from primary alcohols, secondary alcohols or mixtures thereof. ZDDP compounds generally are of the formula Zn[SP(S)(OR.sub.1)(OR.sub.2)].sub.2 where R.sub.1 and R.sub.2 are C.sub.1-C.sub.18 alkyl groups, preferably C.sub.2-C.sub.12 alkyl groups. These alkyl groups may be straight chain or branched. Alcohols used in the ZDDP can be 2-propanol, butanol, secondary butanol, pentanols, hexanols such as 4-methyl-2-pentanol, n-hexanol, n-octanol, 2-ethyl hexanol, alkylated phenols, and the like. Mixtures of secondary alcohols or of primary and secondary alcohol can be used. Alkyl aryl groups may also be used. Useful zinc dithiophosphates include secondary zinc dithiophosphates such as those available from The Lubrizol Corporation under the trade designations LZ 677A, LZ 1095 and LZ 1371, from Chevron Oronite under the trade designation OLOA 262 and from Afton Chemical under the trade designation HiTEC 7169.
[0590] In embodiments, the zinc compound can be a zinc dithiocarbamate complex, such as the zinc dithiocarbamates represented by the formula:
##STR00016##
where each R.sub.1 is independently a linear, cyclic, or branched, saturated or unsaturated, aliphatic hydrocarbon moiety having from 1 to about 10 carbon atoms, n is 0, 1, or 2, L is a ligand that saturates the coordination sphere of zinc, and x is 0, 1, 2, 3, or 4. In certain embodiments, the ligand, L, is selected from the group consisting of water, hydroxide, ammonia, amino, amido, alkylthiolate, halide, and combinations thereof.
[0591] The antiwear additives, such as ZDDP and/or the zinc carbamates, are typically used in amounts of from about 0.4 wt % to about 1.2 wt %, preferably from about 0.5 wt % to about 1.0 wt %, and more preferably from about 0.6 wt % to about 0.8 wt %, based on the total weight of the lubricating composition, although more or less can often be used advantageously. Preferably, the antiwear additive is ZDDP, preferably a secondary ZDDP, and is present in an amount of from about 0.6 to 1.0 wt % of the total weight of the lubricating composition. The lubricating oil compositions of the instant disclosure preferably include one or more ZDDPs at a treat level to deliver less than or equal to 1200 ppm, or 1000 ppm, or 800 ppm, or 600 ppm, or 400 ppm, or 200 ppm, or 0 ppm by weight of phosphorous to the composition.
[0592] Antiwear additives useful herein also include boron-containing compounds, such as borate esters, borated fatty amines, borated epoxides, alkali metal (or mixed alkali metal or alkaline earth metal) borates and borated overbased metal salts.
[0593] Compositions according to the present disclosure may contain an additive having a different enumerated function that also has secondary effects as an antiwear agent (for example, Component B Functionalized Polymer described above, may also have antiwear effects). These additives are not included as antiwear agents for purposes of determining the amount of antiwear agents in a lubricating oil composition or concentrate herein.
L. Demulsifiers
[0594] Demulsifiers useful herein include those described in U.S. Pat. No. 10,829,712 (col 20, In 34-40). Typically, a small amount of a demulsifying component may be used herein. A preferred demulsifying component is described in European Patent No. 330 522. It is obtained by reacting an alkylene oxide with an adduct obtained by reacting a bis-epoxide with a polyhydric alcohol. Such additives may be used in an amount of about 0.001 to 5 wt %, preferably about 0.01 to 2 wt %.
M. Seal Compatibility Agents and Seal Swell Agents
[0595] Other optional additives include seal compatibility agents such as organic phosphates, aromatic esters, aromatic hydrocarbons, esters (butylbenzyl phthalate, for example), and polybutenyl succinic anhydride. Such additives may be used in an amount of about 0.001 to 5 wt %, preferably about 0.01 to 2 wt %. In embodiments the seal compatibility agents are sea swell agents, such as PIBSA (polyisobutenyl succinic anhydride).
N. Extreme Pressure Agents
[0596] The lubricating oil compositions and concentrate compositions of the present disclosure can contain one or more extreme pressure agents that can prevent sliding metal surfaces from seizing under conditions of extreme pressure. Any extreme pressure agent known by a person of ordinary skill in the art may be used in the lubricating oil composition. Generally, the extreme pressure agent is a compound that can combine chemically with a metal to form a surface film that prevents the welding of asperities in opposing metal surfaces under high loads. Non-limiting examples of suitable extreme pressure agents include sulfurized animal or vegetable fats or oils, sulfurized animal or vegetable fatty acid esters, fully or partially esterified esters of trivalent or pentavalent acids of phosphorus, sulfurized olefins, dihydrocarbyl polysulfides, sulfurized Diels-Alder adducts, sulfurized dicyclopentadiene, sulfurized or co-sulfurized mixtures of fatty acid esters and monounsaturated olefins, co-sulfurized blends of fatty acid, fatty acid ester and alpha-olefin, functionally substituted dihydrocarbyl polysulfides, thia-aldehydes, thia-ketones, epithio compounds, sulfur-containing acetal derivatives, co-sulfurized blends of terpene and acyclic olefins, and poly sulfide olefin products, amine salts of phosphoric acid esters or thiophosphoric acid esters, and combinations thereof. The amount of the extreme pressure agent may vary from about 0.01 wt % to about 5 wt %, from about 0.05 wt % to about 3 wt %, or from about 0.1 wt % to about 1 wt %, based on the total weight of the lubricating oil composition.
O. Non-Basestock Unsaturated Hydrocarbons
[0597] The lubricating oil compositions and concentrate compositions of the present disclosure can contain one or more unsaturated hydrocarbons. These unsaturated hydrocarbons are distinct from any baseoils (lubricating oil basestocks of Group I, II, III, IV and/or V) and/or viscosity modifiers that may be present in the compositions and always have at least one (and typically only one, in the case of linear alpha-olefins, or LAOs) unsaturation per molecule. Without being bound by theory, the unsaturation(s) may provide an antioxidation functionality and/or a sulfur-trapping functionality that may supplement and/or replace one or more antioxidant additives and/or one or more corrosion inhibitor additives, but unsaturated hydrocarbons (LAOs) will typically not provide the only antioxidant nor the only corrosion inhibition functionality in lubrication oil compositions. Non-limiting examples of unsaturated hydrocarbons can include one or more unsaturated C.sub.12-C.sub.60 hydrocarbons (such as C.sub.12-C.sub.48 hydrocarbons, C.sub.12-C.sub.36 hydrocarbons, C.sub.12-C.sub.30 hydrocarbons, or C.sub.12-C.sub.24 hydrocarbons). When only one unsaturation is present, the unsaturated hydrocarbons may be termed linear alpha-olefins (LAOs). Other non-limiting examples of unsaturated hydrocarbons can include oligomers/polymers of polyisobutylenes that have retained (or been post-polymerization modified to exhibit) a (near-) terminal unsaturation, and/or blends thereof. When present, unsaturated hydrocarbons (LAOs) may be present from 0.01 to 5 wt % (in particular, 0.1 to 3 mass %, alternately 0.1 to 1.5 mass %), based on total weight of the lubricating oil composition.
[0598] When lubricating oil compositions contain one or more of the additives discussed above, the additive(s) are typically blended into the composition in an amount sufficient for it to perform its intended function. Typical amounts of such additives useful in the present disclosure, especially for use in crankcase lubricants, are shown in the Table below.
[0599] It is noted that many of the additives are shipped from the additive manufacturer as a concentrate, containing one or more additives together, with a certain amount of base oil or other diluents. Accordingly, the weight amounts in the table below, as well as other amounts mentioned herein, are directed to the amount of active ingredient (that is the non-diluent portion of the ingredient). The weight percent (mass %) indicated below is based on the total weight of the lubricating oil composition.
TABLE-US-00001 Typical Amounts of Lubricating Oil Components Additive Formulations A (mass % a.i.) B (mass % a.i.) C (mass % a.i.) Dispersant 0.1-20 0.5-10 1-6 Detergents 0.1-20 0.2-10 0.3-9 Corrosion Inhibitor and/or Anti- 0-7 0.01-5 0.05-1.5 rust Overbased Ca detergent 0.1-10 0.2-5 0.3-4.5 Overbased Mg detergent 0.1-10 0.2-5 0.4-4.5 High MW PIBSA-PAM 0-20 0.5-8 1 to 4 Low MW PIBSA-PAM 0.1-20 0.5-10 1-6 Antioxidant 0.01-10 0.1-5 0.1-4 Pour Point Depressant 0-8 0.005-5 0.01-1.5 Anti-foaming Agent 0-1 0.001-0.5 0.005-0.15 Functionalized Polymer 0.01-10 0.1-5 0.5-2 Friction Modifier 0-2 0.1-1 0.2-0.5 Antiwear Agent 0.01-10 0.1-5 0.5-3 Viscosity Modifier 0-15 0.1-10 0.25-3 Seal Swell Agents 0-10 0.01-5 0.1-2 Extreme Pressure Agents 0-10 0.01-5 0.1-3 Unsaturated Hydrocarbons (LAOs) 0-10 0.01-5 0.1-3 Base stock Balance (such Balance Balance as 50 to 95%)
[0600] The foregoing additives are typically commercially available materials. These additives may be added independently, but are usually pre-combined in packages, which can be obtained from suppliers of lubricant oil additives. Additive packages with a variety of ingredients, proportions and characteristics are available and selection of the appropriate package will take the use of the ultimate composition into account.
Fuel Compositions
[0601] This disclosure also relates to a method of lubricating a passenger or commercial vehicle hydrogen fueled internal combustion engine during operation of the engine comprising: (i) providing to a crankcase of the vehicle hydrogen internal combustion engine a vehicle crankcase lubricating oil composition described herein; (ii) providing a hydrogen containing fuel in the vehicle hydrogen internal combustion engine; and (iii) combusting the fuel in the vehicle hydrogen internal combustion engine, such as a spark-ignited or compression-ignited two- or four-stroke reciprocating engines.
[0602] This disclosure also relates to a fuel composition comprising the lubricating oil compositions described herein and a hydrogen containing fuel, wherein the hydrogen fuel may include hydrogen selected from green hydrogen, blue hydrogen, grey hydrogen, brown hydrogen, or combinations thereof. The hydrogen containing fuel may optionally include other non-hydrogen containing fuels, including, but not limited to, natural gas, propane, mogas, renewable fuel, or combinations thereof. The renewable fuel component may be produced from vegetable oil (such as palm oil, rapeseed oil, soybean oil, jatropha oil), microbial oil (such as algae oil), animal fats (such as cooking oil, animal fat, and/or fish fat) and/or biogas. Renewable fuel refers to biofuel produced from biological resources formed through contemporary biological processes. In an embodiment, the renewable fuel component is produced by means of a hydrotreatment process. Hydrotreatment involves various reactions where molecular hydrogen reacts with other components, or the components undergo molecular conversions in the presence of molecular hydrogen and a solid catalyst. The reactions include, but are not limited to, hydrogenation, hydrodeoxygenation, hydrodesulfurization, hydrodenitrification, hydrodemetallization, hydrocracking, and isomerization. The renewable fuel component may have different distillation ranges, which provide the desired properties to the component, depending on the intended use.
Uses
[0603] The lubricating compositions disclosed herein may be used to lubricate mechanical engine components, particularly in hydrogen fueled internal combustion engines, e.g., spark-ignited or compression-ignited, two- or four-stroke reciprocating hydrogen fueled engines, by adding the lubricant thereto. Typically, they are crankcase lubricants, such as passenger car motor oils or heavy-duty engine lubricants.
[0604] In particular, the lubricating compositions disclosed herein are suitably used in the lubrication of the crankcase of a compression-ignited, hydrogen fueled internal combustion engine, such as a heavy-duty engine.
[0605] In particular, the lubricating compositions disclosed herein are suitably used in the lubrication of the crankcase of a spark-ignited turbo charged hydrogen fueled internal combustion engine.
[0606] In embodiments, the lubricating oils disclosed herein are used in spark-assisted high compression hydrogen fueled internal combustion engines.
[0607] In embodiments, the lubricating compositions disclosed herein are suitably used in the lubrication of the crankcase of an hydrogen fueled engine for a heavy-duty vehicle (i.e., a heavy-duty vehicle having a gross vehicle weight rating of 10,000 pounds or more.)
[0608] In particular, lubricating oil formulations of this disclosure are particularly useful in compression-ignited hydrogen fueled internal combustion engines, i.e., heavy-duty engines, employing low viscosity oils, such as API FA-4 and future oil categories, in which wear protection of the valve train becomes challenging.
[0609] Also, the lubricating compositions described herein may be useful as lubricants for natural gas engines [e.g., natural gas is the fuel the engines run on, commonly called GEOs or (natural) gas engine oils].
[0610] The lubricating compositions described herein may be used to lubricate mechanical engine components, particularly in hydrogen fueled internal combustion engines, e.g., spark-ignited or compression-ignited two- or four-stroke reciprocating engines, by adding the lubricant thereto.
[0611] The lubricating compositions described herein are particularly suitable for hydrogen fueled internal combustion engines that are prone to piston-liner wear from a long duration of operation, hence the invention might extend engine lifetime.
[0612] Also, the lubricating compositions described herein are useful as lubricants for ammonia fueled engines and the like [e.g., ammonia fuel (or hydrogen combined with ammonia fuel) or ammonia combined with hydrocarbon fuel, such as gasoline or diesel fuel) is the fuel the combusted in the internal combustion engine].
[0613] The following non-limiting examples are provided to illustrate the disclosure.
EXPERIMENTAL
[0614] All molecular weights are number average molecular weights (Mn) reported in g/mol, as determined by gel permeation chromatography using polystyrene standards, unless otherwise noted. A.I., a.i., and ai are wt % active ingredient, unless otherwise indicated.
Testing Procedures
[0615] Sulfated ash (SASH) content is measured by ASTM D874.
[0616] Phosphorus, Calcium, Zinc, Boron, Molybdenum, and Magnesium and Silicon content are measured by ASTM D5185.
[0617] KV100 is Kinematic viscosity measured at 100 C. according to ASTM D445-19a.
[0618] KV40 is Kinematic viscosity measured at 40 C. according to ASTM D445-19a.
[0619] Sulfur content in oil is measured by ASTM D5185.
[0620] High Temperature High Shear Viscosity, (HTHS or HTHS150) measures the high temperature high shear viscosity of the lubricating oil and is determined at 150 C. according to ASTM D4683 and is reported in cPs.
[0621] High Temperature Corrosion Bench Test (HTCBT) measures the corrosion resistance of a lubricating oil and is determined as described in ASTM D6594.
[0622] The Modified ASTM D7563 Emulsion test measures the ability of the lubricating oil to disperse water in the form of an emulsion. In the Modified ASTM D7563 Emulsion test, 10% water by mass is mixed with an oil and agitated in a high-speed blender. The emulsion is then stored in a graduated cylinder at 0 deg. C. and 25 deg. C. for 168 hours. The mixtures are then observed, and the presence of an aqueous layer is reported.
[0623] The ASTM D1748 Rust test measures the ability of the lubricating oil to resistant rust formation of iron based metals when used in an engine.
[0624] Pre-Ignition testing of lubricating oil compositions for Abnormal Combustion Events was measured using the following method. Abnormal combustion events (pre-ignition) were determined as follows: data regarding pre-ignition occurrences was generated using a turbocharged, port fueled Daimler OM936 7.7 liter, 6 cylinder engine, modified to run on hydrogen fuel with a reduction in compression ratio to 10-12:1, upscaling of fuel injectors and turbocharger system, adaption of the blowby system to prevent high concentrations of hydrogen in the crankcase, and adaption of a CNG-based engine control system modified for lean burn operation. The engine was operated under conditions between 12 to 18 bar brake mean effective pressure, between engine speeds of about 1000 to 1200 rpm and at air to fuel ratio (AFR) between 1.85 and 2.05. For each cycle (a cycle being 2 piston cycles (up/down, up/down), data was collected on peak pressure and mass faction burned over the duration of each cycle. Post processing of the data included calculation of combustion metrics, verification of operating parameters being within target limits, and detection of pre-ignition events (statistical procedure outlined below). From the above data, outliers, which are potential occurrences of pre-ignition were collected. For each pre-ignition cycle, data recorded included peak pressure (PP), MFB03.5 (crank angle at 3.5% mass fraction burned), cycle number and engine cylinder. A cycle was identified as having a pre-ignition event if both of the crank angle corresponding to MFB03.5 of the fuel and the cylinder PP are outliers. Outliers were determined relative to the distribution of a particular cylinder and test segment in which it occurs. Determination of outliers was an iterative process involving calculation of the mean and standard deviation of PP and MFB03.5 for each segment and cylinder; and cycles with parameters that exceed n standard deviations from the mean. The number of standard deviations n, used as a limit for determining outliers, is a function of the number of cycles in the test and was calculated using the Grubbs' test for outliers. Outliers were identified in the severe tail of each distribution. That is, if n is the number of standard deviations obtained from Grubbs' test for outliers, an outlier for PP is identified as one exceeding the mean plus n standard deviations of peak pressure. Likewise, an outlier for MFB03.5 was identified as one being lower than the mean less n standard deviations of MFB03.5. Data was further examined to ensure that the outliers indicated an occurrence of pre-ignition, rather than some other abnormal combustion event or an electrical sensor error.
[0625] As used herein, Brake Mean Effective Pressure (BMEP) is the mean effective pressure calculated from measured brake torque. The word brake denotes the actual torque or power available at the engine flywheel, as measured on a dynamometer. Thus, BMEP is a measure of the useful power output of the engine. BMEP is defined as the work accomplished during an engine cycle, divided by the engine swept volume; the engine torque normalized by engine displacement and can be calculated using the following formula: BMEP=(2Tn)/(Vd), where T is torque (Nm), n is the number of revolutions per cycle, Vd is displacement (m.sup.3). For a 4 stroke engine n is 2, for a 2 stroke engine n is 1. Its unit are bars.
Materials
TABLE-US-00002 Component Chart Additional Lubricating Oil Components Description F-H-PI Functionalized Polymer Functionalized hydrogenated isoprene block copolymer produced according to the procedure disclosed in USSN 63/379,006, filed Oct. 11, 2022, ai 28% in oil Borated PIBSA-PAM Polyisobutylene succinimide having 1 to 3 mass % boron, based upon a PIB having an Mn of about 900-1050 g/mol in oil, ai ~40-50 PIBSA ester dispersant PIBSA ester of hydrocarbyl-bridged naphthyloxy alcohol in oil diluted to about 40% ai. See U.S. Pat. No. 7,485,603. PIBSA-PAM (2000 + Mn PIB) Polyisobutylene succinimide based upon a PIB having an Mn of about 2000-2300 g/mol in oil, ai ~45-60 PIBSA-PAM (900 + Mn) Polyisobutylene succinimide based upon a PIB having an Mn of about 900-1050 g/mol in oil, ai ~45-55 Calcium sulfonate-300 TBN Calcium sulfonate detergent having a TBN of approximately 300 mgKOH/g (on an as diluted basis) in oil, ai ~55 Magnesium sulfonate-400 TBN magnesium sulfonate detergent having a TBN of approximately 400 mgKOH/g (on an as diluted basis) in oil, ai ~57 ZDDP Zinc dialkyl dithiophosphate in oil, where the alkyl groups are derived from a mixture of 1 and 2 alcohols, 75-92 ai Mo Friction modifier Trimeric Mo dialkyldithiocarbamate compound in oil, ~45 ai DPA antioxidant Alkylated diphenylamine antioxidant Sulfurized FAME Sulfurized Fatty Acid Methyl Ester, derived from Lard Oil, Rapeseed Oil and/or Palm Oil PIBSA-2000 + Mn Polyisobutylene succinate having an Mn of approximately 2000-2300 g/mol in oil, ai ~70-75 Polyisobutylene- 900+ Polyisobutylene having an Mn of approximately 900-1050 g/mol Anti-foamant Polydimethylsiloxane Lube oil flow improver Fumarate-Vinyl Acetate copolymer in oil EP copolymer-viscosity modifier Ethylene-propylene copolymer viscosity modifier in oil (shear stability index ~25)
EXAMPLES
Example 1
[0626] Two inventive lubricating oil compositions were prepared according to the formulations in Table 1 below. The two inventive lubricants were tested in the modified ASTM D7563 Emulsion test with both inventive lubricants yielding no aqueous layer (100% emulsion).
[0627] D94 The effect of the combination of functionalized polymer, low and high MW PIBSA-PAM dispersant, overbased magnesium containing detergent, overbased calcium containing detergent, and ZDDP in the inventive lubricating oils in providing significantly improved water dispersancy in the modified ASTM D7563 Emulsion test is surprising and unexpected.
TABLE-US-00003 TABLE 1 Inventive1 Inventive2 Modified ASTM D7563 Emulsion test No aqueous layer, 100% emulsion Dispersant Low MW Borated PIBSA-PAM 0.2 0.7 Low MW Unborated PIBSA-PAM 0.5 High MW Unborated PIBSA-PAM 2.2 3.3 F-H-PI 0.5 0.7 Detergent Ca Sulf, TBN = 300 0.4 0.4 Mg Sulf, TBN = 405 0.7 0.7 ZDDP ZDDP 0.7 0.7 BS Total Gr Il 84.0 77.4 KV100 9.8 16.2 SASH 0.9 0.9 Ca, ppm 830 830 Mg, ppm 1090 1090 N % 0.16 0.21 P % 0.08 0.08 S % 0.30 0.31 The remainder of the oil is made up of antioxidants, friction modifier, seal swell agents, antifoam, lube oil flow improver, diluent oil, and viscosity modifier.
Example 2
[0628] One inventive lubricating oil composition and one comparative lubricating oil composition were prepared according to the formulations in Table 2 below. The two lubricants were tested in the ASTM D1748 rust test with the comparative example failing the test and the inventive example passing and exhibiting no rust. As can be seen, the combination of the low MW PIBSA-PAM and the high MW PIBSA-PAM provided outstanding rust prevention to the inventive lubricating oil, which is particularly advantageous for a lubricant used in a H2ICE because of the water generated as a result of the combustion of the hydrogen based fuel.
[0629] The effect of the combination of functionalized polymer, low and high MW PIBSA-PAM dispersant, overbased magnesium containing detergent, overbased calcium containing detergent, and ZDDP in the inventive lubricating oil in providing significantly improved ASTM D1748 rust test performance is surprising and unexpected.
TABLE-US-00004 TABLE 2 Comparative Inventive ASTM D1748 Rust Test Fail No rust Dispersant Low MW Borated PIBSA-PAM 0.7 Low MW Unborated PIBSA-PAM 0.5 High MW Unborated PIBSA-PAM 3.4 3.3 PIBSA ester dispersant 0.3 F-H-PI 0.7 Detergent Ca Sulf, TBN = 300 0.5 0.4 Mg Sulf, TBN = 405 0.6 0.7 ZDDP ZDDP 1.1 0.7 BS Total Gr II 77.4 77.4 KV100 14.8 16.2 SASH 1.0 0.9 Ca, ppm 1050 830 Mg, ppm 1000 1090 N % 0.11 0.21 P % 0.12 0.08 S % 0.31 0.31 The remainder of the oil is made up of antioxidants, friction modifier, ZDDP, seal swell agents, antifoam, lube oil flow improver, diluent oil, and viscosity modifier.
Example 3
[0630] One inventive lubricating oil composition and two comparative lubricating oil compositions were prepared according to the formulations in Table 3 below. The three lubricants were tested for abnormal combustion performance in a H2ICE by measuring the number of pre-ignition events per 1000 cycles (measured at 1000 rpm, 12 bar BMEP and 1.85 air:fuel ratio (AFR)) with the results also shown in Table 3 below. The inventive example including a combination of functionalized polymer, low and high MW PIBSA-PAM dispersant, overbased magnesium containing detergent, overbased calcium containing detergent, and ZDDP provided significantly lower pre-ignition events relative to the two comparative examples not including this combination of lubricating oil additives.
[0631] The effect of the combination of functionalized polymer, low and high MW PIBSA-PAM dispersant, overbased magnesium containing detergent, overbased calcium containing detergent, and ZDDP in the inventive lubricating oil for decreasing the propensity of abnormal combustion events in hydrogen fueled internal combustion engines (H2ICE) is surprising and unexpected.
TABLE-US-00005 TABLE 3 Inventive comparative comparative # PI events/1000 cycles, 12 bar 1.85 AFR 2.32 3.68 6.74 Dispersant Low MW Borated PIBSA-PAM 0.2 0.0 0.0 Low MW Unborated PIBSA-PAM 1.0 0.0 0.0 High MW Unborated PIBSA-PAM 1.1 3.4 3.3 F-H-PI 0.6 0.0 0.0 Det Ca Sulf, TBN = 300 0.5 0.5 3.0 Mg Sulf, TBN = 405 0.6 0.6 0.0 ZDDP ZDDP 0.8 1.1 0.1 BS Total Gr II 82.1 46.3 0.0 Total Gr III 0.0 30.0 78.3 KV100 9.7 15.9 14.1 SASH 0.9 1.0 2.0 Ca ppm 988 1047 6265 Mg ppm 934 1003 10 N % 0.15 0.11 0.09 P % 0.08 0.12 0.02 S % 0.29 0.29 0.17 The remainder of the oil is made up of antioxidants, friction modifier, ZDDP, seal swell agents, antifoam, lube oil flow improver, diluent oil, and viscosity modifier.
Example 4
[0632] Two inventive lubricating oil compositions and one comparative lubricating oil composition were prepared according to the formulations in Table 4 below. The three lubricants were tested in the ASTM D6594 high temperature corrosion bench test (HTCBT) for copper corrosion resistance. As can be seen in Table 4 below, the two inventive lubricants including a combination of functionalized polymer, low and high MW PIBSA-PAM dispersant, overbased magnesium containing detergent, overbased calcium containing detergent, and ZDDP provided a significantly lower copper strip rating (1a, and hence better copper corrosion resistance) than the comparative lubricant not including this combination of lubricating oil additives.
[0633] The effect of the combination of functionalized polymer, low and high MW PIBSA-PAM dispersant, overbased magnesium containing detergent, overbased calcium containing detergent, and ZDDP in the lubricating oil in providing significantly improved copper corrosion resistance is surprising and unexpected.
TABLE-US-00006 TABLE 4 Comparative Inventive 1 Inventive 2 Dispersant Low MW Borated PIBSA-PAM 0.2 0.2 0.2 Low MW Unborated PIBSA-PAM 1.5 1.5 1.5 High MW Unborated PIBSA- 1.7 1.7 1.7 PAM F-H-PI with non-ionic fatty 0.0 0.3 0.6 alcohol ethoxylate Det Ca Sulf, TBN = 300 0.4 0.4 0.4 Mg Sulf, TBN = 405 0.5 0.5 0.5 ZDDP ZDDP 0.8 0.8 0.8 BS Total Gr Il 22.1 22.1 22.1 Total Gr III 60.6 59.4 58.3 KV100 7.4 8.2 9.0 Ca ppm 932 993 968 Mg ppm 730 744 744 N % 0.16 0.18 0.17 P % 0.08 0.08 0.08 S % 0.31 0.31 0.29 HTCBT Result Cu (ppm) 66 16 9 Cu strip (rating) 4a 1a 1a The remainder of the oil is made up of antioxidants, friction modifier, ZDDP, seal swell agents, antifoam, lube oil flow improver, diluent oil, and viscosity modifier.
[0634] All documents described herein are incorporated by reference herein, including any priority documents and/or testing procedures, to the extent they are not inconsistent with this text. As is apparent from the foregoing general description and the specific embodiments, while forms of the invention have been illustrated and described, various modifications can be made without departing from the spirit and scope of the invention. Accordingly, it is not intended that the invention be limited thereby.