SOOT DISPERSANT

20190300812 ยท 2019-10-03

    Inventors

    Cpc classification

    International classification

    Abstract

    The present invention is directed to a use of a lubricant in a diesel engine to disperse soot produced by the diesel engine, the soot being dispersed without adversely affecting the viscosity of the lubricant; the lubricant comprising a major amount of oil of lubricating viscosity and a minor amount of a dispersant comprising (i) one or more olefin, (ii) one or more carboxylic acid, (iii) one or more polyetheramines and (iv) one or more aromatic amines along with co-additives.

    Claims

    1. A composition used in decreasing the amount of soot in internal combustion engine comprising a major amount of oil of lubricating viscosity and a minor amount of dispersant comprising (i) one or more olefin (ii) one or more carboxylic acid, (iii) one or more polyetheramines and (iv) one or more aromatic amines.

    2. The composition as claimed in claim 1 further comprises co-additive selected from the group consisting of a dispersant, detergent, zinc dialkyl dithiophosphates, viscosity modifiers, antioxidants, defoamants and pour point depressants.

    3. The composition as claimed in claim 1, wherein the said composition is a dispersant having formula ##STR00002##

    4. The composition as claimed in claim 3 wherein, R1 is alkyl, alkenyl, alkoxyl, aralkyl, alkaryl, or a mixture thereof having from about 20 to 60 carbon atom; R2 is alkyl, alkoxyl (or polyether) or polyethyleneamines; R3 are NH, NHalkyl, NHaryl, NHalkaryl, NHaralkyl, heavy polyamine or branched or straight chain or a mixture thereof having from about 4-18 carbon atoms. R4 is polyolefins, preferably Polyisobutylene.

    5. The composition as claimed in claim 1 wherein, the olefin is a polyisobutylene succinic anhydride having a Mn from 500 to 3500.

    6. The composition as claimed in claim 1 wherein, the carboxylic acid is a dimer acid or trimer acid having a Mn from 100-2000, or mixture of thereof.

    7. The composition as claimed in claim 6 wherein, the said dimer acid or trimer acid having from about 30-60 carbon atoms.

    8. The composition as claimed in claim 1 wherein, the polyetheramines is a triamine having a Mn from 300-5000, and triamines consist of primary and secondary amines. (Polyether including PEO, PPO or mixture of thereof.

    9. The composition as claimed in claim 1 wherein, the aromatic amines is an amine selected from the group consisting of N-phenyl-1,4-phenylenediamine, N-phenyl-1,3-phenylendiamine, and N-phenyl-1,2-phenylenediamine, amino-di-phenylamine or a mixture of thereof.

    10. The composition as claimed in claim 2 wherein, the said detergent is an oil-soluble overbased metal detergent selected from the group consisting of sulfonate, salicylate, phenate or mixture thereof having a total base number (TBN) greater than 200 present in a range of 1.5-3% w/w.

    11. The composition as claimed in claim 2, wherein the said ZDDP present in a range of 1.5-2% w/w.

    12. The composition as claimed in claim 11, wherein the alkyl group present in ZDDP have same or different hydrocarbyl radicals having from about 2-18 carbon atoms.

    13. The composition as claimed in claim 2, wherein the said antioxidants are selected from the group consisting of molybdenum based antioxidant, phenolic ester based antioxidant, and diphenyl amine based anti-oxidant or a mixture thereof.

    14. The composition as claimed in claim 13, wherein the said antioxidants are present in a range of 0-2% w/w.

    15. The composition as claimed in claim 2, wherein the said defoamer is present in a range of 0-1% w/w.

    16. The composition as claimed in claim 2, wherein the said viscosity modifier is present in a range of 7-9% w/w.

    17. The composition as claimed in claim 2, wherein the said pour point depressant is present in a range of 0-2% w/w.

    18. The use according to any preceding claim, wherein said internal combustion engine is a heavy duty diesel engine.

    Description

    DETAILED DESCRIPTION OF THE PRESENT INVENTION

    [0037] Various preferred features and embodiments will be described below by way of non-limiting illustration.

    Succinimide Dispersants

    [0038] Suitable acylating agents include hydrocarbyl carbonic acid, hydrocarbyl carbonic acid halides, hydrocarbyl sulfonic acid and hydrocarbyl sulfonic acid halides, hydrocarbyl phosphoric acid and hydrocarbyl phosphoric halides, hydrocarbyl isocyanates and hydrocarbyl succinic acylating agents. Preferred acylating agents include polyacylating agent's which provide bis ester, ester acid and/or ester lactone substituent groups. Preferred acylating agents are C8 and higher hydrocarbyl isocyanates, such as dodecyl isocyanate and hexadodecyl isocyanate and C8 or higher hydrocarbyl acylating agents, more preferably polybutenyl succinic acylating agents such as polybutenyl, or polyisobutenyl succinic anhydride (PIBSA). Preferably the hydrocarbyl succinic acylating agent will be derived from polyalkene having a number average molecular weight (M n) of from about 100 to 5000, preferably from about 200 to about 3000, more preferably from about 500 to about 2500. Acylating agents can be prepared by conventional methods known to those skilled in the art, such as chlorine-assisted, thermal and radical grafting methods. The acylating agents can be mono- or polyfunctional. Preferably, the acylating agents have functionality in the range of 1-2.5.

    Carboxylic Acid

    [0039] The acid may be a monoacid, a dimer acid, or a trimer acid. The acid may be selected from the group consisting of formic acid, acetic acid, propionic acid, butyric acid, caprylic acid, capric acid, lauric acid, myristic acid, palmitic acid, stearic, arachidic acid, behenic acid, lignoceric acid, cerotic acid, myristoleic acid, palmitoleic acid, sapienic acid, oleic acid, elaidic acid, vaccenic acid, linoleic acid, linoelaidic acid, .alpha.-linolenic acid, arachidonic acid, eicosapentaenoic acid, erucic acid, docosahexaenoic acid, and the dimer and trimer acids thereof.

    [0040] The method of preparing dimeric fatty acids or esters thereof initially involves dimerizing monomeric unsaturated fatty acids and/or esters thereof to provide a first mixture containing dimeric fatty acids and/or esters thereof, unreacted monomeric fatty acids and/or rearranged monomeric fatty acids and/or esters thereof and interesters, suitable examples include iso-octanedioic acid, octanedioic acid, nonanedioic acid (azelaic acid), decanedioic acid (sebacic acid), undecanedioic acid, dodecanedioic acid, tridecanedioic acid, tetradecanedioic acid, pentadecanoic acid or mixtures thereof. In one embodiment the polycarboxylic acid is nonanedioic acid (azelaic acid) or mixtures thereof. In one embodiment the polycarboxylic acid is adpic acid, decanedioic acid (sebacic acid) or mixtures thereof.

    Polyetheramines

    [0041] Polyetheramines can be amine-terminated polyethers such as polyethylene oxide (PEO), polypropylene oxide (PPO) or combination of PEO/PPO copolymers. For example, some of the commercial polyethers include: poly(ethyleneglycol) bis(3-aminopropylether) (34901-14-9, mw 1500), poly(propyleneglycol) bis(2-aminopropylether) (mw 230), poly(propyleneglycol) bis(2-aminopropylether) (mw 400), poly(propyleneglycol) bis(2-aminopropylether) (9046-10-0, mw 2000), poly(propyleneglycol) bis(2-aminopropylether) (mw 4000), poly(propyleneglycol)-block-poly(ethyleneglycol)-block poly(propyleneglycol) bis(2-aminopropylether) (65605-36-9) (3.5:8.5) (PO:EO) (mw 600), poly(propyleneglycol)-block-poly(ethyleneglycol)-block poly(propyleneglycol) bis(2-aminopropylether) (3.5:15.5) (PO:EO) (mw 900), poly(propyleneglycol)-block-poly(ethyleneglycol)-block poly(propyleneglycol) bis(2-aminopropylether) (3.5:40.5) (PO:EO) (mw 2000), glycerol tris[poly(propylene glycol), amine terminated] ether (64852-22-8, mw 3000 or mw 440), Trimethylolpropane tris[poly(propylene glycol), amine terminated] ether (39423-51-3, mw 440) poly(tetrahydrofuran), bis(3-aminopropyl) terminated (72088-96-1), and the like.

    Amines

    [0042] Amines which may be employed in the present invention include any that have at least one primary amino group which can react to form an imide group and at least one additional primary or secondary amino group and/or at least one hydroxyl group.

    [0043] Suitable amines may include alkylene polyamines, such as propylene diamine, dipropylene triamine, di-(1,2-butylene)triamine, and tetra-(1,2-propylene)pentamine. A further example includes the ethylene polyamines which can be depicted by the formula H2N(CH2CH2NH)nH, wherein n may be an integer from about one to about ten. These include: ethylene diamine, diethylene triamine (DETA), triethylene tetramine (TETA), tetraethylene pentamine (TEPA), pentaethylene hexamine (PEHA), Heavy polyamine (HPA) and the like, including mixtures thereof.

    [0044] Polyamines that are also suitable in preparing the dispersants described herein include N-arylphenylenediamines, such as N-phenylphenylenediamines, for example, N-phenyl-1,4-phenylenediamine, N-phenyl-1,3-phenylendiamine, and N-phenyl-1,2-phenylenediamine; aminothiazoles such as aminothiazole, aminobenzothiazole, aminobenzothiadiazole and aminoalkylthiazole; aminocarbazoles; aminoindoles; aminopyrroles; amino-indazolinonesi; aminomercaptotriazoles; aminoperimidines; aminoalkyl imidazoles, such as 1-(2-aminoethyl) imidazole, 1-(3-aminopropyl) imidazole; and aminoalkyl morpholines, such as 4-(3-aminopropyl) morpholine.

    [0045] Hydroxyamines suitable for herein include compounds, oligomers or polymers containing at least one primary or secondary amine capable of reacting with the hydrocarbyl-substituted succinic acid or anhydride. Examples of hydroxyamines suitable for use herein include aminoethylethanolamine (AEEA), aminopropyldiethanolamine (APDEA), dimethylaminopropylamine (DMAPA), ethanolamine, diethanolamine (DEA), partially propoxylated hexamethylene diamine (for example HMDA-2PO or HMDA-3PO), 3-amino-1,2-propanediol, tris(hydroxymethyl)aminomethane, and 2-amino-1,3-propanediol.

    Co-Additives

    [0046] The lubricating composition optionally contains at least one other performance additive. Typically the other performance additives include metal deactivators, defoamers, dispersant, antioxidants, antiwear agents, corrosion inhibitors, antiscuffing agents, extreme pressure agents, foam inhibitors, demulsifiers, friction modifiers, viscosity modifiers, pour point depressants and mixtures thereof. Typically, fully-formulated lubricating oil will contain one or more of these performance additives.

    Base Oils

    [0047] The term Group I base oil as used herein refers to a petroleum derived lubricating base oil having a saturates content of less than 90 wt. % (as determined by ASTM D 2007) and/or a total sulfur content of greater than 300 ppm (as determined by ASTM D 2622, ASTM D 4294, ASTM D 4297 or ASTM D 3120) and has a viscosity index (VI) of greater than or equal to 80 and less than 120 (as determined by ASTM D 2270).

    [0048] In general, a Group II base oil and Group III base oil can be any petroleum derived base oil of lubricating viscosity as defined in API Publication 1509, 14th Edition, Addendum 1, December 1998. API guidelines define a base stock as a lubricant component that may be manufactured using a variety of different processes. Group II base oils generally refer to a petroleum derived lubricating base oil having a total sulfur content equal to or less than 300 parts per million (ppm) (as determined by ASTM D 2622, ASTM D 4294, ASTM D 4927 or ASTM D 3120), a saturates content equal to or greater than 90 weight percent (as determined by ASTM D 2007), and a viscosity index (VI) of between 80 and 120 (as determined by ASTM D 2270). Group III base oils generally have less than 300 ppm sulfur, saturates content greater than 90 weight percent, and a VI of 120 or greater. In one embodiment, the Group III base stock contains at least about 95% by weight saturated hydrocarbons. In another embodiment, the Group III base stock contains at least about 99% by weight saturated hydrocarbons.

    Metal Detergent

    [0049] The detergents include but are not limited to overbased sulfonates, phenates, salicylates and the like overbased detergents known in the art. Overbased materials otherwise referred to as overbased or superbased salts are generally single phase, homogeneous systems characterized by a metal content in excess of that which would be present for neutralization according to the stoichiometry of the metal and the particular acidic organic compound reacted with the metal. The overbased materials are prepared by reacting an acidic material (typically an inorganic acid or lower carboxylic acid, typically carbon dioxide) with a mixture comprising an acidic organic compound, a reaction medium comprising at least one inert, organic solvent (mineral oil, naphtha, toluene, xylene, etc.) for said acidic organic material, a stoichiometric excess of a metal base, and a promoter such as a calcium chloride, acetic acid, phenol or alcohol.

    [0050] Overbased sulphonates typically have a TBN of 200 to 600 mg KOH/gm, or 300 to 500. The metal sulphonate detergent may be an alkaline earth metal or alkali metal sulphonate. For example the metal may be sodium, calcium, barium, or magnesium. Typically other detergent may be sodium, calcium, or magnesium containing detergent (typically, calcium, or magnesium containing detergent). In one embodiment the metal may be calcium.

    Friction Modifier

    [0051] Friction modifiers that are compatible with the other ingredients of the final oil may also be included. Examples of such materials include oil-soluble organo-molybdenum compounds, such oil soluble organo-molybdenum compounds include dithiocarbamates, dithiophosphates, dithiophosphinates, xanthates, thioxanthates, sulfides, and the like, and mixtures thereof.

    [0052] Particularly preferred are molybdenum dithiocarbamates, Additionally, the molybdenum compound may be an acidic molybdenum compound. These compounds will react with a basic nitrogen compound as measured by ASTM test D-664 or D-2896 titration procedure and are typically hexavalent. Included are molybdic acid, ammonium molybdate, sodium molybdate, potassium molybdate, and other alkaline metal molybdates and other molybdenum salts, e.g., hydrogen sodium molybdate, MoOCl4, MoO2Br2, Mo2O3Cl6, molybdenum trioxide or similar acidic molybdenum compounds.

    Antiwear

    [0053] ZDDP is conventionally added to lubricating oil compositions in amounts of 0.1 to 10, preferably 0.2 to 2 wt. %, based upon the total weight of the lubricating oil composition. They may be prepared in accordance with known techniques. The preferred zinc dihydrocarbyl dithiophosphates are oil soluble salts of dihydrocarbyl dithiophosphoric acids and may be represented by the following formula:

    ##STR00001##

    wherein R and R may be the same or different hydrocarbyl radicals containing from 1 to 18, preferably 2 to 12, carbon atoms and including radicals such as alkyl, alkenyl, aryl, arylalkyl, alkaryl and cycloaliphatic radicals. Particularly preferred as R and R groups are alkyl groups of 2 to 8 carbon atoms. Thus, the radicals may, for example, be ethyl, n-propyl, i-propyl, n-butyl, i-butyl, sec-butyl, amyl, n-hexyl, thexyl, n-octyl, decyl, dodecyl, octadecyl, 2-ethylhexyl, phenyl, butylphenyl, cyclohexyl, methylcyclopentyl, propenyl, butenyl. In order to obtain oil solubility, the total number of carbon atoms (i.e. R and R) in the dithiophosphoric acid will generally be about 5 or greater. The zinc dihydrocarbyl dithiophosphate can therefore comprise zinc dialkyl dithiophosphates.

    Antioxidants

    [0054] Antioxidants or oxidation inhibitors are used to minimize the effect of oil deterioration that occurs when hot oil is contacted with air. The degree and rate of oxidation will depend on temperature, air and oil flow rates and, of particular importance, on the presence of metals that may catalytically promote oxidation. Antioxidants generally function by prevention of peroxide chain reaction and/or metal catalyst deactivation. They prevent the formation of acid sludges, darkening of the oil and increases in viscosity due to the formation of polymeric materials.

    [0055] Non-limiting examples of suitable oxidation resistance (antioxidant) and thermal stability improvers are diphenly-, dinaphtyl-, and phenyl-naphthyl-amines, in which the phenyl and naphthyl groups can be substituted, for example, N,N-diphenyl phenylenediamine, p-octyldiphenylamine, p-dioctyldiphenylamine, alkylated diphenylamine, alkylated phenyl alpha naphthylamine, N-phenyl-1-naphthyl amine, N-phenyl-2-naphthyl amine, N-(p-dodecyl)-phenyl-2-naphthyl amine, di-1-naphthylamine, and di-2-naphthylamine; phenothazines such as N-alkylphenothiazines; imino(-bisbenzyl); hindered phenols such as 6-(t-butyl)phenol, 2,6-di-(t-butyl)phenol, 4-methyl-2, 6-di-(t-butyl)phenol, 4,4-methylenebis(2,6-di-{t-butyl}-phenol), esters of 3,5-di-tert-butyl-4-hydroxyhydrocinnamic acid, thiodiethylene bis-(3,5-di-tert-butyl-4-hydroxy) hydrocinnamate, esters of [[[13,5-bis(1,1-dimethylethyl)-4-hydroxyphenyl]methyl]thio]acetic acid and the like.

    Viscosity Modifiers

    [0056] Viscosity modifiers that are compatible with the other ingredients of the final oil may also be included. Non-limiting examples of suitable viscosity index improvers include, but are not limited to, olefin copolymers, such as ethylene-propylene copolymers, styrene-isoprene copolymers, hydrated styrene-isoprene copolymers, polybutene, polyisobutylene, polymethacrylates, vinylpyrrolidone and methacrylate copolymers and dispersant type viscosity index improvers. These viscosity modifiers can optionally be grafted with grafting materials such as, for example, maleic anhydride, and the grafted material can be reacted with, for example, amines, amides, nitrogen-containing heterocyclic compounds or alcohol, to form multifunctional viscosity modifiers (dispersant-viscosity modifiers). Other examples of viscosity modifiers include star polymers (e.g., a star polymer comprising isoprene/styrene/isoprene triblock). Yet other examples of viscosity modifiers include poly alkyl(meth)acrylates of low Brookfield viscosity and high shear stability, functionalized poly alkyl(meth)acrylates with dispersant properties of high Brookfield viscosity and high shear stability, polyisobutylene having a weight average molecular weight ranging from 700 to 2,500 Daltons and mixtures thereof.

    TABLE-US-00001 TABLE 1 Finished Oil Formulation More Most Preferred Preferred Preferred COMPONENTS, Wt % Range Range Range HTHS@150, cP 3.7 3.1 2.9 Base Oil viscosity, cSt 2 25 3 20 4 16 300-400 TBN Ca and or Mg 0.5-7 1-5 1.5-3 Sulfonate (6000-7000 M. Wt. Succinimide 0.5-9 1-7 2-5 Dispersant) (2000-5000 M. Wt. Succinimide 0.05-10 0.1-7 0.2-5 Dispersant) Phosphorus from ZDDP, ppm 300-3000 400-2000 500-1600 Mo, ppm from Mo antioxidant 0-1500 0-1000 0-600 Phenolic Ester based 0-5 0-3 0-2 Anti-oxidant Diphenyl Amine based 0-5 0-3 0-2 Anti-oxidant (Defoamer) 0.001-0.5 0.005-0.2 0.01-0.1 Viscosity Modifier 0-20 0-15 0-12 (Pour point depressant) 0.01-5 0.05-2 0.1-1.5

    TABLE-US-00002 TABLE 2 Finished Oil Formulation More Most Preferred Preferred Preferred COMPONENTS, Wt % Range Range Range HTHS@150, cP 3.7 3.1 2.9 Base Oil viscosity, cSt 2 25 3 20 4 16 200-400 TBN Ca and or Mg 0.5-7 1-5 1.5-3 Salicylate (6000-7000 M. Wt. Succinimide 0.5-9 1-7 2-5 Dispersant) (2000-5000 M. Wt. Succinimide 0.05-10 0.1-7 0.2-6 Dispersant) Phosphorus from ZDDP, ppm 300-3000 400-2000 500-1600 Mo, ppm from Mo antioxidant 0-1500 0-1000 0-600 Phenolic Ester based 0-5 0-3 0-2 Anti-oxidant Diphenyl Amine based 0-5 0-3 0-2 Anti-oxidant (Defoamer) 0.001-0.5 0.005-0.2 0.01-0.1 Viscosity Modifier 0-20 0-15 0-12 (Pour point depressant) 0.01-5 0.05-2 0.1-1.5

    TABLE-US-00003 TABLE 3 Finished Oil Formulation More Most Preferred Preferred Preferred COMPONENTS, Wt % Range Range Range HTHS@150, cP 3.7 3.1 2.9 Base Oil viscosity, cSt 2 25 3 20 4 16 200-400 TBN Ca and or Mg 0.5-7 1-5 1.5-3 Phenate (6000-7000 M. Wt. Succinimide 0.5-9 1-7 2-5 Dispersant) (2000-5000 M. Wt. Succinimide 0.05-10 0.1-7 0.2-6 Dispersant) Phosphorus from ZDDP, ppm 300-3000 400-2000 500-1600 Mo, ppm from Mo antioxidant 0-1500 0-1000 0-600 Phenolic Ester based 0-5 0-3 0-2 Anti-oxidant Diphenyl Amine based 0-5 0-3 0-2 Anti-oxidant (Defoamer) 0.001-0.5 0.005-0.2 0.01-0.1 Viscosity Modifier 0-20 0-15 0-12 (Pour point depressant) 0.01-5 0.05-2 0.1-1.5

    TABLE-US-00004 TABLE 4 Finished Oil Formulation More Most Preferred Preferred Preferred COMPONENTS, Wt % Range Range Range HTHS@150, cP 3.7 3.1 2.9 Base Oil viscosity, cSt 2 25 3 20 4 16 300-400 TBN Ca and or Mg 0-7 0-5 0-3 Sulfonate 200-400 TBN Ca and or Mg 0-7 0-5 0-3 Salicylate 200-400 TBN Ca and or Mg 0-7 0-5 0-3 Phenate (6000-7000 M. Wt. Succinimide 0.5-9 1-7 0.2-6 Dispersant) (2000-5000 M. Wt. Succinimide 0.05-10 0.1-7 0.2-5 Dispersant) Phosphorus from ZDDP, ppm 300-3000 400-2000 500-1600 Mo, ppm from Mo antioxidant 0-1500 0-1000 0-600 Phenolic Ester based 0-5 0-3 0-2 Anti-oxidant Diphenyl Amine based 0-5 0-3 0-2 Anti-oxidant (Defoamer) 0.001-0.5 0.005-0.2 0.01-0.1 Viscosity Modifier 0-20 0-15 0-12 (Pour point depressant) 0.01-5 0.05-2 0.1-1.5

    EXAMPLES

    Example 1

    [0057] Place 302 g of base oil (150N) into a 1000 ml round bottom flask equipped with stirrer, Dean Stark trap and an addition funnel and add 51 g of Trimethylolpropane poly(oxypropylene)triamine (440 g/mol) and 20 g of 4-Aminodiphenylamine (ADPA), heat the above mixture to 160-170 C. Premix 305 g of PIBSA (PIB Mn2300) and 83 g of dimer acid in a beaker and then mixture is transferred to the addition funnel and slowly added to the flask at 170 C in 1 hr. After completion of the above mixture, raise reaction temperature to 220 C and stay at 220 C for 5 hrs. yield: 754 g, Kv100: 517 cSt, TBN: 4.7 mgKOH/g, nitrogen: 0.94 wt %.

    Example 2

    [0058] Place 275 g of base oil (150N) into a 1000 ml round bottom flask equipped with stirrer, Dean Stark trap and an addition funnel and add 40 g of Trimethylolpropane poly(oxypropylene)triamine (440 g/mol) and 16 g of 4-Aminodiphenylamine (ADPA), heat the above mixture to 160-170 C. Premix 305 g of PIBSA (PIB Mn2300) and 56 g of dimer acid in a beaker and then the mixture is transferred to the addition funnel and slowly added to the flask at 170 C in 1 hr. After completion of the above mixture, raise reaction temperature to 220 C and stay at 220 C for 5 hrs. yield: 688 g, Kv100: 372 cSt, TBN: 4.3 mgKOH/g, nitrogen: 0.91 wt %.

    Example 3

    [0059] Place 260 g of base oil (150N) into a 1000 ml round bottom flask equipped with stirrer, Dean Stark trap and an addition funnel and add 34.6 g of Trimethylolpropane poly(oxypropylene)triamine and 13.6 g of 4-Aminodiphenylamine (ADPA), heat the above mixture to 160-170 C. Premix 305 g of PIBSA (PIB Mn2300) and 42 g of dimer acid in a beaker and then mixture is transferred to the addition funnel and slowly added to the flask at 170 C in 1 hr. After completion of the above mixture, raise reaction temperature to 220 C and stay at 220 C for 5 hrs. yield: 650 g, Kv100: 326 cSt, TBN: 4.2 mgKOH/g, nitrogen: 0.80 wt %.

    Example 4

    [0060] Place 246 g of base oil (150N) into a 1000 ml round bottom flask equipped with stirrer, Dean Stark trap and an addition funnel and add 28.7 g of Trimethylolpropane poly(oxypropylene)triamine (440 g/mol) and 11.4 g of 4-Aminodiphenylamine (ADPA), heat the above mixture to 160-170 C. Premix 305 g of PIBSA (PIB Mn2300) and 28 g of dimer acid in a beaker and then mixture is transferred to the addition funnel and slowly added to the flask at 170 C in 1 hr. After completion of the above mixture, raise reaction temperature to 220 C and stay at 220 C for 5 hrs. Yield: 614 g, Kv100: 311 cSt, TBN: 3.2 mgKOH/g, nitrogen: 0.7 wt %.

    Example 5

    [0061] Place 240 g of base oil (150N) into a 1000 ml round bottom flask equipped with stirrer, Dean Stark trap and an addition funnel and add 24.5 g of Trimethylolpropane poly(oxypropylene)triamine (440 g/mol) and 10.2 g of 4-Aminodiphenylamine (ADPA), heat the above mixture to 160-170 C. Premix 305 g of PIBSA (PIB Mn2300) and 21 g of dimer acid in a beaker and then mixture is transferred to the addition funnel and slowly added to the flask at 170 C in 1 hr. After completion of the above mixture, raise reaction temperature to 220 C and stay at 220 C for 5 hrs. yield: 597 g, Kv100: 305 cSt, TBN: 2.5 mgKOH/g, nitrogen: 0.68 wt %.

    Example 6

    [0062] Place 238 g of base oil (150N) into a 1000 ml round bottom flask equipped with stirrer, Dean Stark trap and an addition funnel and add 30.8 g of Trimethylolpropane poly(oxypropylene)triamine (440 g/mol) and 4.1 g of 4-Aminodiphenylamine (ADPA), heat the above mixture to 160-170 C. Premix 305 g of PIBSA (PIE Mn2300) and 21 g of dimer acid in a beaker and then mixture is transferred to the addition funnel and slowly added to the flask at 170 C in 1 hr. After completion of the above mixture, raise reaction temperature to 220 C and stay at 220 C for 5 hrs. yield: 595 g, Kv100: 335 cSt, TBN: 2.2 mgKOH/g, nitrogen: 0.6 wt %.

    Example 7

    Bench Test Results for Soot Dispersant Performance

    [0063] The inventive soot dispersant from example 1 to 6 were blended into a fully formulated HDDE oil which contained conventional dispersant, detergents, ZDDP, antioxidants, viscosity modifier and base oil (table 2)

    [0064] Above oils were blended with 6 wt % carbon black (Vulcan XC-72) in a beaker with high speed stirrer for 20-30 min, and then evaluated in a rotational rheometer, the rheological measurement of the carbon black containing oils was based on ASTM D-6895. A flow behaviour rate index and rotational viscosity at shear rate of 100 l/s for each oil were reported in the following table. Oils exhibited strong soot handling ability when rate index is close to 1.0 and rotational viscosity is low.

    TABLE-US-00005 TABLE 5 Dispersant % Oil 1 Oil 2 Oil 3 Oil 4 Oil 5 Oil 6 Oil 7 Oil 8 Conventional Dispersant 4.5 1.0 1.0 1.0 1.0 1.0 1.0 2.5 Soot Dispersant Example 1 3.5 Soot Dispersant Example 2 3.5 2.0 Soot Dispersant Example 3 3.5 Soot Dispersant Example 4 3.5 Soot Dispersant Example 5 3.5 Soot Dispersant Example 6 3.5 Total 4.5 4.5 4.5 4.5 4.5 4.5 4.5 4.5 Rate Index 0.57 0.95 0.96 0.96 0.92 0.59 0.49 0.88 Viscosity at 100 1/s 69.11 20.3 21.09 20.83 21.40 61.70 79.40 28.43

    [0065] As shown in the table 5, the inventive soot dispersants example 1 to 4 exhibited excellent soot handling capability than conventional dispersant.