Composition of additives comprising a copolymer and a resin
US-2024076567-A1 · Mar 7, 2024 · US
US10047314B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10047314-B2 |
| Application number | US-201715425427-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 6, 2017 |
| Priority date | Dec 4, 2003 |
| Publication date | Aug 14, 2018 |
| Grant date | Aug 14, 2018 |
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The use is described of polymers which contain, in copolymerized form, an α-olefin, a vinyl ester and an ester of an α,β-unsaturated carboxylic acid as an additive for fuel oils and lubricants and in particular as a cold flow improver in fuel oils. In addition, the fuel oils and lubricants additized with these polymers; and also additive packages comprising such polymers are described.
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What is claimed is: 1. A method of preparing a fuel or lubricant composition, comprising adding to the fuel or lubricant composition a polymer which comprises, in copolymerized form, an α-olefin, a vinyl ester and an ester of an α,β-unsaturated carboxylic acid. 2. The method according to claim 1 , wherein the polymer is obtained by free-radical polymerization. 3. The method according to claim 1 , wherein the polymer is composed of monomers including M1, M2 and M3 and wherein M1, M2 and M3 have the following general formulae: where R 1 is H or C 1 -C 40 -hydrocarbyl; R 2 , R 3 and R 4 are each independently H or C 1 -C 4 -alkyl; R 5 is C 1 -C 20 -hydrocarbyl; R 6 , R 7 and R 8 are each independently H or C 1 -C 4 -alkyl; and R 9 is C 1 -C 20 -hydrocarbyl. 4. The method according to claim 3 , wherein the monomers M1, M2 and M3 are present in the polymer in the following molar proportions: M1: from 0.60 to 0.98 M2: from 0.01 to 0.20 M3: from 0.01 to 0.20. 5. The method according to claim 3 , wherein the monomer M1 is ethylene. 6. The method according to claim 3 , wherein R 2 , R 3 and R 4 are each H or two of the R 2 , R 3 and R 4 radicals are each H and the other radical is methyl. 7. The method according to claim 3 , wherein R 5 is C 1 -C 9 -hydrocarbyl. 8. The method according to claim 7 , wherein R 5 is n-butyl or 2-ethylhexyl. 9. The method according to claim 6 , wherein M2 is n-butyl acrylate or 2-ethylhexyl acrylate. 10. The use method according to claim 3 , wherein M3 is vinyl acetate. 11. The method according to claim 1 , wherein the polymer is a cold flow improver. 12. A fuel oil composition comprising: a middle distillate fuel boiling in a range of 120-500° C.; and at least one polymer as defined in claim 1 , wherein a content of the middle distillate fuel is greater than a content of the polymer by weight. 13. The fuel oil composition according to claim 12 , wherein the fuel component comprises biodiesel in proportions of 0-100% by weight. 14. The fuel oil composition according to claim 12 , selected from diesel fuels, kerosene and heating oil. 15. The fuel oil composition according to claim 14 , wherein the diesel fuel is obtained by refining, coal gasification or gas liquefaction, or is a mixture of such products and is optionally mixed with renewable fuels. 16. The fuel oil composition according to claim 12 , wherein a sulfur content of the composition is at most 500 ppm. 17. A lubricant composition, comprising: a lubricant; and at least one polymer as defined in claim 1 , wherein a content of the lubricant is greater than a content of the polymer by weight. 18. The method according to claim 1 , wherein the polymer is used in combination with further cold flow improvers and/or further lubricant and fuel oil additives. 19. An additive package comprising at least one polymer as defined in claim 1 in combination with at least one further lubricant or fuel oil additive. 20. The method according to claim 4 , wherein the monomers M1, M2 and M3 are present in the polymer in the following molar proportions: M1: from 0.60 to 0.98 M2: from 0.015 to 0.17 M3: from 0.02 to 0.15. 21. The method according to claim 4 , wherein the monomers M1, M2 and M3 are present in the polymer in the following molar proportions: M1: from 0.60 to 0.98 M2: from 0.02 to 0.16 M3: from 0.02 to 0.15.
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