润滑科技信息平台

Surfactants and dispersants by in-line reaction

专利摘要

A surfactant is synthesized from an amine or an alcohol and a hydrocarbyl-substituted succinic acylating agent by feeding the amine or alcohol into a stream comprising the hydrocarbyl substituted succinic acylating agent, to form a combined stream; passing the combined stream through an in-line mixer so as to effect premixing and initial reaction of the components; and thereafter passing the combined stream into a reactor, where the combined stream is further processed to form the surfactant. ......

基本信息

专利类型:
发明专利
申请/专利号:
US09/841217
申请日期:
2001-04-24
专利申请人:
路博润公司
分类号:
["B01F17/00","C09K23/00","C10M133/44","C10M129/66"]
发明/设计人:
EPPS, DONALD E. ， SEPELAK, TIMOTHY C. ， OXLEY, STEVEN C. ， MARTIN, FREDERIC J.
权利要求: What is claimed is:1. A method for synthesizing a surfactant from an amine or an alcohol and a hydrocarbyl-substituted succinic acylating agent, comprising:feeding the amine or alcohol into a stream comprising the hydrocarbyl substituted succinic acylating agent, to form a combined stream;passing said combined stream through an in-line mixer so as to effect premixing and initial reaction of the components; and thereafterpassing the combined stream into at least one reactor, wherein said combined stream is further processed to form said surfactant.2. The method of claim 1 wherein the combined stream is passed through the in-line mixer at a temperature of about 80 to about 160.degree. C.3. The method of claim 2 wherein the temperature is about 90 to about 130.degree. C.4. The method of claim 1 wherein the residence time of the combined stream after entering the in-line mixer and before entering the subsequent reactor is at least about 15 seconds.5. The method of claim 4 wherein the residence time is about 0.3 to about 20 minutes.6. The method of claim 1 wherein the in-line mixer provides a degree of mixing of the components expressed as a coefficient of variation of at most about 3.5.7. The method of claim 1 wherein the in-line mixer is a static mixer.8. The method of claim 7 wherein the static mixer comprises a multiplicity of right handed and left handed blade elements.9. The method of claim 1 wherein the mixture is reacted in the reactor at a temperature of about 80 to about 220.degree. C.10. The method of claim 9 wherein the temperature in the reactor is about 100 to about 200.degree. C.11. The method of claim 1 wherein water of reaction is removed from the reactor.12. The method of claim 1 wherein the reactor is a stirred reactor.13. The method of claim 12 wherein the stirred reactor is a continuous stirred tank reactor.14. The method of claim 12 wherein the stirred reactor is a stirred batch reactor.15. The method of claim 1 wherein the residence time in the reactor is about 0.1 to about 20 hours.16. The method of claim 15 wherein the residence time in the reactor is about 0.5 to about 10 hours.17. The method of claim 13 further comprising passing the product from the continuous stirred tank reactor into a second continuous stirred tank reactor.18. The method of claim 1 wherein the amine or alcohol comprises an amine.19. The method of claim 18 wherein the amine comprises a polyamine.20. The method of claim 19 wherein the polyamine comprises a polyethyleneamine.21. The method of claim 20 wherein the polyethyleneamine contains on average about 3 to about 8 nitrogen atoms.22. The method of claim 19 wherein the polyamine comprises amine still bottoms.23. The method of claim 18 wherein the amine is an aminoalcohol containing at least one N--H group.24. The method of claim 23 wherein the aminoalcohol comprises dimethylaminoethanol or diethylaminoethanol.25. The method of claim 1 wherein the hydrocarbyl-substituted succinic acylating agent comprises a hydrocarbyl-substituted succinic anhydride.26. The method of claim 25 wherein the stream which comprises hydrocarbyl-substituted succinic anhydride also comprises diluent oil.27. The method of claim 25 wherein the hydrocarbyl-substituted succinic anhydride comprises a polyisobutene-substituted succinic anhydride.28. The method of claim 27 wherein the polyisobutene substituent has a number average molecular weight of about 500 to about 5000.29. The method of claim 27 wherein the polyisobutene substituent has a number average molecular weight of about 900 to about 3000.30. The method of claim 1 wherein the hydrocarbyl-substituted succinic acylating agent is prepared by the use of chlorine.31. The method of claim 1 wherein the hydrocarbyl-substituted succinic acylating agent comprises material represented by the structure ##STR3##where R is H or methyl and Pbt represents a fragment of a polyisobutene substituent.32. The method of claim 27 wherein the dispersant has a carbonyl: nitrogen mole ratio of about 1:0.7 to about 1:2.5.33. The method of claim 1 wherein the surfactant is a dispersant.34. The method of claim 33 wherein the dispersant is a succinimide dispersant.35. The method of claim 1 wherein the surfactant is an amine salt.36. A method for synthesizing a surfactant from water and a hydrocarbyl-substituted succinic anhydride, comprising:feeding the water into a stream comprising the hydrocarbyl substituted succinic anhydride, to form a combined stream;passing said combined stream through an in-line mixer so as to effect premixing and initial reaction of the components; and thereafterpassing the combined stream into at least one reactor, wherein said combined stream is further processed to form said surfactant.37. The composition prepared by the process of claim 1.38. A lubricant comprising the composition of claim 37 and an oil of lubricating viscosity.