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(Poly) production method of alkylene glycol mono alkyl ether luxury

机译:(聚)亚烷基二醇单烷基醚奢侈品的生产方法

摘要

PROBLEM TO BE SOLVED: To provide a method for producing (poly)alkylene glycol mono(higher alkyl) ether in high selectivity and high yield by reacting a long chain olefin with a (poly)alkylene glycol in the presence of a crystalline metalosilicate as a catalyst, and returning a (poly)alkylene glycol di(higher alkyl) ether, etc., obtained as a by-product to the reaction system. ;SOLUTION: (A) An 8-30C olefin having an ethylenically unsaturated bond, e.g. dodecene, is reacted with (B) a (poly)alkylene glycol, e.g. monoethylene glycol, in the presence of a crystalline metalosilicate as a catalyst, and a (poly) alkylene glycol di(higher alkyl) ether, etc., obtained by the reaction as a byproduct is continuously recovered and successively recycled to the reaction system. The molar ratio of the component B to the component A is 0.05-20, the formulating percentage of the catalyst of component C to component A is 0.1-100wt.%. The reaction is performed at 50-250°C under a pressure of a normal pressure to 20kg/cm2 for 0.1-100hr.;COPYRIGHT: (C)1998,JPO
机译:解决的问题:提供一种在结晶金属硅酸盐存在下通过使长链烯烃与(聚)亚烷基二醇反应以高选择性和高收率生产(聚)亚烷基二醇单(高级烷基)醚的方法。催化剂,并将作为副产物获得的(聚)亚烷基二醇二(高级烷基)醚等返回到反应体系中。 ;解决方案:(A)具有烯键式不饱和键的8-30C烯烃,例如C。使十二碳烯与(B)一种(聚)亚烷基二醇,例如二亚甲基二醇反应。在结晶性金属硅酸盐作为催化剂的存在下,单乙二醇和通过反应作为副产物获得的(聚)亚烷基二醇二(高级烷基)醚等被连续回收并相继循环到反应体系中。组分B与组分A的摩尔比为0.05-20,组分C与组分A的催化剂的配制百分比为0.1-100wt。%。反应在50-25℃,常压至20kg / cm 2 的压力下进行0.1-100小时。;版权:(C)1998,JPO

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