Method for processing used oils

Abstract

The invention relates to a method for lowering the content of polycyclic aromatic hydrocarbons (PAH) in a used lubricant composition, in which said used lubricant composition passes over activated carbon, said method not comprising a solvent extraction step.

Claims

1. A method for lowering the content of polycyclic aromatic hydrocarbons (PAHs) in a used lubricant composition, comprising the passing of said used lubricant composition over activated carbon, said method not comprising a solvent extraction, the quantity of activated carbon applied being between 0.5 and 60 g per litre of lubricant composition, wherein the method further comprises prior distillation of the used lubricant composition.

2. The method according to claim 1, wherein the quantity of activated carbon used is between 1 and 50 g per litre of lubricant composition.

3. The method according to claim 1, wherein the activated carbon is characterized by a density of between 200 and 500 kg/m.sup.3.

4. The method according to claim 1, further comprising prior filtering of the used lubricant composition.

5. The method according to claim 1, wherein the PAH is benzo-a-pyrene.

6. The method according to claim 1, further comprising before the passing of said used lubricant composition over activated carbon: one or more distillations; and filtering.

7. A method for preparing a lubricant composition comprising less than 100 ppb of each of the following PAHs : chrysene, benzo[b]fluoranthene, benzo[j]fluoranthene, benzo[k]fluoranthene, benzo[e]pyrene, benzo[a ]pyrene, dibenz[a,h]anthracene, benz[a ]anthracene, from a used lubricant composition, comprising the passing of said used lubricant composition over activated carbon.

8. The method according to claim 7, wherein the PAH is benzo-a-pyrene.

9. The method according to claim 7, further comprising prior filtering of the used lubricant composition.

10. The method according to claim 7, further comprising before the passing of said used lubricant composition over activated carbon: one or more distillation stepsdistillations; and filtering.

Description

(1) A further objective of the present invention is to provide a method for preparing a lubricant composition comprising less than 100 ppb of BaP, from used lubricant compositions. Other objectives will become apparent on reading the following description of the invention.

(2) These objectives are reached with the present invention which concerns a method for lowering the content of polycyclic aromatic hydrocarbons (PAHs) selected in particular from among chrysene, benzo[b]fluoranthene, benzo[j]fluoranthene, benzo[k]fluoranthene, benzo[e]pyrene, benzo[a]pyrene, dibenz[a,h]anthracene and/or benz[a]anthracene, from a used lubricant composition, comprising the passing of said used lubricant composition over activated carbon, said method not comprising a solvent extraction step.

(3) By solvent extraction step is meant any liquid/liquid extraction step.

(4) In the present invention, by «passing of the used lubricant composition over activated carbon» is also meant the flowing of the used lubricant composition over activated carbon.

(5) In the present invention, by used lubricant composition is meant any lubricant composition that has been used to lubricate parts, mechanical parts in particular, and particularly engine parts and notably of motor vehicle engines. Having regard to their origin—engine lubrication—these used lubricant compositions have a high PAH content, particularly from among chrysene, benzo[b]fluoranthene, benzo[j]fluoranthene, benzo[k]fluoranthene, benzo[e]pyrene, benzo[a]pyrene, dibenz[a,h]anthracene and/or benz[a]anthracene, and BaP in particular. The used lubricant compositions applied in the invention can be any lubricant composition particularly comprising base oils selected from among oils of mineral or synthetic origin, selected from among Group 1 to V class oils as classified by the API classification (or ATIEL classification equivalents) (Table A), alone or in mixtures.

(6) TABLE-US-00001 TABLE A Saturates Sulfur Viscosity Index content content VI Group I <90% >0.03% 80 ≤ VI < 120 Mineral oils Group II ≥90% ≤0.03% 80 ≤ VI < 120 Hydrocracked oils Group III ≥90% ≤0.03% ≥120 Hydrocracked or hydro- isomerized oils Group IV Polyalphaolefins (PAOs) Group V Esters and other bases not included in Groups I to IV

(7) These used lubricant compositions may also comprise any type of additive generally used in lubricant compositions e.g. detergents, anti-wear additives, extreme-pressure additives, viscosity index improvers, dispersants, antioxidants, pour point depressants, defoamers, friction modifiers and mixtures thereof.

(8) Preferably, in the method of the invention, the amount of activated carbon used is between 0.5 and 60 g of activated carbon per litre of used lubricant composition, preferably between 0.5 and 50 g/l, preferably from 1 to 50 g/l, preferably between 1 and 30 g/l, e.g. between 5 and 60 g/l, preferably between 5 and 50 g/l.

(9) The pass rate of the used lubricant composition can be between1 m.sup.3/h and 15 m.sup.3/h, e.g. between 5 and10 m.sup.3/h.

(10) Preferably, in the method of the invention, the activated carbon is characterized by a density of between 200 and 500 kg/m.sup.3, measured for example in accordance with standard ASTDM D2854.

(11) Preferably, the activated carbon is coal carbon preferably comprising from 70 to 95%, advantageously from 80 to 90% of carbon by weight.

(12) Advantageously, the method of the invention may comprise a prior step to filter the used lubricant composition. This filtration can be conducted using any method known to persons skilled in the art. This filtering step may or may not be a particulate filtration step. For example, it can be performed using systems of diatomaceous earth type. In particularly advantageous manner, this step allows extended activity of the activated carbon by increasing its lifetime and hence the time between two renewals or two reactivations of the activated carbon. Reactivation of the activated carbon can be carried out using any method known to skilled persons to regenerate the activated carbon e.g. by high temperature treatment for example at 800° C. or higher. This prior filtration step allows an extended time period over which the passing of the used oil over the activated carbon is efficient in terms of lowering of PAH content, preferably of BaP.

(13) The method of the invention may advantageously comprise one or more prior distillation steps of the used lubricant composition. These distillation steps can be carried out using any technique known to skilled persons. Advantageously, the method of the invention may comprise a distillation step to remove water, followed by a distillation step to remove diesel and finally a distillation step under reduced pressure. For example, the distillations can be conducted at a temperature of between 100 and 400° C., and at a pressure of between 50 and 2000 Pa.

(14) The method of the invention may advantageously comprise the following prior steps: one or more distillation steps; and a filtering step.

(15) These steps are such as defined above.

(16) Advantageously the method of the invention allows significant lowering of the PAH content of the regenerated lubricant composition. Advantageously, with the method of the invention it is possible to obtain a regenerated lubricant composition comprising less than 100 ppb of each of the following PAHs: chrysene, benzo[b]fluoranthene, benzo[j]fluoranthene, benzo[k]fluoranthene, benzo[e]pyrene, benzo[a]pyrene, dibenz[a,h]anthracene, benz[a]anthracene . The content of these PAHs being determined according to standard EN 16143.

(17) Preferably the PAH is benzo[a]pyrene (BaP). Advantageously the method of the invention allows significant lowering of the BaP content in the regenerated lubricant composition.

(18) Advantageously, with the method of the invention it is possible to obtain a regenerated lubricant composition comprising less than 100 ppb of BaP.

(19) The present invention also concerns a method for preparing a lubricant composition comprising less than 100 ppb of each of the following PAHs: chrysene, benzo[b]fluoranthene, benzo[j]fluoranthene, benzo[k]fluoranthene, benzo[e]pyrene, benzo[a]pyrene, dibenz[a,h]anthracene, benz[a]anthracene, preferably less than 100 ppb of BaP, from a used lubricant composition, comprising the passing of said used lubricant composition over activated carbon.

(20) Preferably, in the method of the invention, the amount of activated charcoal used is between 0.5 and 60 g of activated carbon per litre of used lubricant composition, preferably between 0.5 and 50 g/l, preferably from 1 to 50 g/l, preferably between 1 and 30 g/l, e.g. between 5 and 60 g/l, preferably between 5 and 50 g/l.

(21) The method of the invention may advantageously comprise a prior step to filter the used lubricant composition such as defined above.

(22) The method of the invention may advantageously comprise one or more prior distillation steps of the used lubricant composition such as defined above.

(23) The method of the invention may advantageously comprise the following prior steps: one or more distillation steps; and a filtering step.

(24) These steps are such as defined above.

(25) The present application will now be described with the aid of nonlimiting examples. The characteristics of a reference used lubricant composition (Ref. Composition), subjected to a prior distillation and filtration, are given in the Table below.

(26) TABLE-US-00002 Standard used for determination of Reference characteristics composition Colour NF ISO 2049 L4.5 Viscosity at 100° C. NF EN ISO 3104 5.28 (mm.sup.2/s) Viscosity at 40° C. NF EN ISO 3104 28.8 (mm.sup.2/s) Viscosity Index NF ISO 2909 117 Pour point in 3 bases ISO 3016 −12 (° C.) CCS at −20° C. (mPa .Math. s) ASTM D 5293 1270 CCS at −25° C. (mPa .Math. s) 2326 Refractive Index at ASTM D 1747 1.4707 20° C. Density at 15° C. NF EN ISO 12185 854.9 (kg/m3) Deaeration (50° C.) NF ISO 9120 6.6 min Cleveland flash point NF EN ISO 2592 234 (° C.) Noack volatility (% m), CEC-L-40-A93 9.80% procedure B Sulfur content ASTM D 2622 0.22% Simulated TBP IP480 178 Cut points T95-T5 (° C.)

(27) This reference composition was treated with the method of the invention and passed over different activated carbons; the resulting compositions (compositions 1 to 8) were analysed to determine the PAH composition thereof on the basis of standard NF EN 16143.

(28) TABLE-US-00003 Activated carbon: Activated carbon: HPC-MAXX 830 ® CPG LF ® from from Chemviron Carbon Chemviron Carbon Ref. Compo- Compo- Compo- Compo- Compo- Composition sition 1 sition 2 sition 3 Composition 4 Composition 5 Composition 6 sition 7 sition 8 quantity of 0 1 5 10 30 50 10 30 50 activated carbon (g/l of composition) Benz[a]anthracene mg/kg 3.4 2.6 0.8 0.3 <0.1 <0.1 0.3 <0.1 <0.1 Chrysene mg/kg 2.7 2.1 0.6 0.2 <0.1 <0.1 0.2 <0.1 <0.1 Benzo[b]fluoranthene mg/kg 4.3 3 0.6 0.2 <0.1 <0.1 0.2 <0.1 <0.1 Benzo[j]fluoranthene mg/kg 0.9 0.6 <0.1 <0.1 <0.1 <0.1 <0.1 <0.1 <0.1 Benzo[k]fluoranthene mg/kg 1.1 0.8 0.2 <0.1 <0.1 <0.1 <0.1 <0.1 <0.1 Benzo[e] mg/kg 5.2 3.7 0.8 0.3 <0.1 <0.1 0.3 <0.1 <0.1 pyrene Benzo[a] mg/kg 4.3 2.7 0.4 0.1 <0.1 <0.1 0.1 <0.1 <0.1 pyrene Dibenz[a,h] mg/kg 0.5 0.4 <0.1 <0.1 <0.1 <0.1 <0.1 <0.1 <0.1 anthracene Total mg/kg 22.5 15.9 3.4 1 0 0 1 0 0 PAH

(29) These results show that the method of the invention advantageously allows lowering of the quantity of PAHs in used lubricant compositions, and in particular lowering of BaP.

(30) Additionally, with the method of the invention it is possible to improve the colour of the resulting lubricant compositions, as shown in the Table below.

(31) TABLE-US-00004 Colour ASTM D1500 Reference composition 4.5 Composition 1 3.9 Composition 2 3.6 Composition 3 3.4 Composition 4 3.2 Composition 5 3.1 Composition 6 3.3 Composition 7 3.3 Composition 8 3.2