Synergistic fuel additives and fuels containing the additives
US-9353326-B1 · May 31, 2016 · US
US9938479B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9938479-B2 |
| Application number | US-201615062799-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 7, 2016 |
| Priority date | Dec 2, 2002 |
| Publication date | Apr 10, 2018 |
| Grant date | Apr 10, 2018 |
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The present invention relates to the use of amines and/or Mannich adducts as detergents and/or dispersants in fuel and lubricant compositions for direct-injection gasoline engines. The invention further relates to fuel and lubricant compositions which comprise at least one such Mannich adduct, and also a bisaminoalkylated Mannich adduct.
Opening claim text (preview).
The invention claimed is: 1. A process for reducing deposits in a direct-injection gasoline engine, comprising: directly injecting a fuel into a combustion chamber of the direct injection gasoline engine through a nozzle disposed in the combustion chamber; wherein the fuel comprises a Mannich reaction mixture of (i) an reaction product of a phenol of formula HOC 6 (H 4.m )(R 9 ) m and a polyisobutene of formula HR 8 , (ii) an aldehyde of formula CHR 10 O and (iii) a secondary amine of formula HNR 1 R 2 , wherein R 9 is a C 1 -C 6 -alkyl group and m is a number from 0 to (4-n), R 8 is a polyisobutene radical which is derived from a reactive polyisobutene polymer having at least 50 mol % of terminal double bonds based on the total number of polyisobutene macromolecules, and R 10 is H or C 1 -C 6 -alkyl, R 1 and R 2 are each independently H, C 1 -C 20 -alkyl or C 3 -C 2 -cycloalkyl, and two alkyl radicals together with the nitrogen atom to which they are bonded may form a ring and the alkyl and the cycloalkyl radicals may be interrupted by one or more groups selected from O and NR 4 and/or may be substituted by one or more OR 5 or NR 6 R 7 groups, where R 4 , R 5 , R 6 and R 7 are each independently H, C 1 -C 20 -alkyl or C 3 -C 20 -cycloalkyl, R 4 , R 5 , R 6 and R 7 are each independently H, C 1 -C 20 -alkyl or C 3 -C 20 -cycloalkyl, wherein the Mannich reaction mixture comprises at least one Mannich adduct of the formula I wherein n is a number from 1 to 3, with the proviso that the sum of the molecular weights of the radicals R1 and R2 is from 120 to 1,000 g/mol. 2. The process as claimed in claim 1 , wherein the sum of the molecular weights of the radicals R 1 and R 2 is from 180 to 600 g/mol. 3. The process as claimed in claim 1 , wherein the radicals R 1 and R 2 are each independently H, C 6 -C 20 -alkyl, C 6 -C 20 -cycloalkyl, R 11 R 12 ) x —NR 4 y CR 13 R 14 ) z —NR 6 R 7 (II), R 11 R 12 ) x —O y CR 13 R 14 ) z —NR 6 R 7 (III) or R 11 R 12 ) x —NR 4 y CR 13 R 14 ) z —OR 5 (IV) where R 4 , R 5 , R 11 , R 12 , R 13 and R 14 are each independently H or C 1 -C 6 -alkyl, R 6 and R 7 are each independently H, C 1 -C 6 -alkyl or C 1 -C 6 -hydroxyalkyl, x and z are each independently a number from 1 to 20 and y is a number from 0 to 10. 4. The process as claimed in claim 1 , wherein R 8 is in the p-position to the OH group in formula I. 5. The process as claimed in claim 1 , wherein the fuel comprises the Mannich reaction mixture the form of a concentrate comprising the Mannich reaction mixture in an amount of from 0.1 to 80% by weight. 6. The process as claimed in claim 1 , further comprising combusting the fuel in the combustion chamber of the direct injection gasoline engine at a lambda value of from 0.9 to 9. 7. A process as claimed in claim 1 , wherein the Mannich reaction mixture comprises at least one Mannich adduct of the formula I.1 wherein R 8 has a number-average molecular weight of from 300 to 3000, R 1 and R 2 are each independently C 6 -C 20 -alkyl, C 6 -C 20 -cycloalkyl, R 11 R 12 ) x —NR 4 y CR 13 R 14 ) z —NR 6 R 7 (II), R 11 R 12 ) x —O y CR 13 R 14 ) z —NR 6 R 7 (III) or R 11 R 12 ) x —NR 4 y CR 13 R 14 ) z —OR 5 (IV), R 4 , R 5 , R 11 , R 12 , R 13 and R 14 are each independently H or C 1 -C 6 -alkyl, R 6 and R 7 are each independently H, C 1 -C 6 -alkyl or C 1 -C 6 -hydroxyalkyl, R 9 is a C 1 -C 6 -alkyl group, x and z are each independently a number from 1 to 20 and y is a number from 0 to 10; and m is 0 or 1. 8. The process as claimed in claim 1 , further comprising combusting the fuel in the combustion chamber of the direct injection gasoline engine under lean conditions. 9. The process as claimed in claim 1 , wherein the Mannich reaction mixture does not comprise water. 10. The process as claimed in claim 1 , wherein the Mannich reaction mixture further comprises the phenolic reaction product. 11. The process as claimed in claim 1 , wherein the Mannich reaction mixture further comprises the phenolic reaction product in an amount of from 5 to 10 mol % based on the total amount of the Mannich reaction mixture. 12. The process as claimed in claim 1 , wherein the phenolic reaction product mixture comprises a 2,4-R 8 -substituted phenolic product. 13. The process as claimed in claim 1 , wherein the phenolic reaction product mixture comprises a 2,4-R 8 -substituted phenolic product in an amount of 5 to 10 mol % based on the total amount of the phenol. 14. A process for reducing deposits in a direct-injection gasoline engine, comprising: directly injecting a fuel into a combustion chamber of the direct injection gasoline engine through a nozzle disposed in the combustion chamber; wherein the fuel comprises a Mannich reaction mixture of (i) an reaction product of a phenol of formula HOC 6 H (4-m) (R 9 ) m and a polyisobutene of formula HR 8 , (ii) an aldehyde of formula CHR 10 O and (iii) a secondary amine of formula HNR 1 R 2 , wherein R 9 is a C 1 -C 6 -alkyl group and m is a number from 0 to (4-n), R 8 is a polyisobutene radical which is derived from reactive a polyisobutene polymer having at least 50 mol % of terminal double bonds based on the total number of polyisobutene macromolecules, and R 10 is H or C 1 -C 6 -alkyl, R 1 and R 2 are each independently H, C 1 -C 20 -alkyl or C 3 -C 20 -cycloalkyl, and two alkyl radicals together with the nitrogen atom to which they are bonded may form a ring and the alkyl and the cycloalkyl radicals may be interrupted by one or more groups selected from O and NR 4 and/or may be substituted by one or more OR 5 or NR 6 R 7 groups, where R 4 , R 5 , R 6 and R 7 are each independently H, C 1 -C 20 -alkyl or C 3 -C 20 -cycloalkyl, R 4 , R 5 , R 6 and R 7 are each independently H, C 1 -C 20 -alkyl or C 3 -C 20 -cycloalkyl, wherein the Mannich reaction mixture comprises at least one Mannich adduct of the formula I wherein n is 2, with the proviso that the sum of the molecular weights of the radicals R 1 and R 2 is from 120 to 1,000 g/mol. 15. The process as claimed in claim 14 , wherein the sum of the molecular weights of the radicals R 1 and R 2 is from 180 to 600 g/mol. 16. The process as claimed in claim 14 , wherein the radicals R 1 and R 2 are each independently H, C 6 -C 20 -alkyl, C 6 -C 20 -cycloalkyl, R 11 R 12 ) x —NR 4 y CR 13 R 14 ) z —NR 6 R 7 (II), R 11 R 12 ) x —O y CR 13 R 14 ) z —NR 6 R 7 (III) or R 11 R 12 ) x —NR 4 y CR 13 R 14 ) z —OR 5 (IV) where R 4 , R 5 , R 11 , R 12 , R 13 and R 14 are each independently H or C 1 -C 6 -alkyl, R 6 and R 7 are each independently H, C 1 -C 6 -alkyl or C 1 -C 6 -hydroxyalkyl, x and z are each independently a number from 1 to 20 and y is a number from 0 to 10. 17. The process as claimed in claim 14 , wherein R 8 is in the p-position to the OH group in formula I. 18. The process as claimed in claim 14 , wherein the fuel comprises the Mannich reaction mixture the form of a concentrate comprising the Mannich reaction mixtu
containing hydroxy groups · CPC title
fractions, e.g. lubricants, solvents, naphta, bitumen, tars, terpentine · CPC title
Well defined compounds, e.g. hexane, benzene · CPC title
having cycloaliphatic groups · CPC title
compounds of uncertain formula; reaction products where mixtures of compounds are obtained · CPC title
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