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    • 25. 发明授权
    • Method for producing polyisobutenes
    • 生产聚异丁烯的方法
    • US07244870B2
    • 2007-07-17
    • US10433439
    • 2001-12-11
    • Arno LangeHans Peter Rath
    • Arno LangeHans Peter Rath
    • C07C2/02C08C4/00
    • C08F10/10C08F8/00C08F110/10C08F297/00C08F2810/30C08F2810/40C08F4/06C08F2/38C08F4/14
    • Polyisobutenes in which at least 60 mol % of the polymer chains have at least one olefinically unsaturated terminal group are prepared by cationic polymerization of isobutene or isobutene-containing monomer mixtures in the condensed phase by a process in which the polymerization is carried out in the presence of an initiator system comprising i) a Lewis acid selected from covalent metal chlorides and semimetal chlorides and ii) at least one organic compound I having at least one functional group FG which forms a carbocation or a cationic complex with the Lewis acid under the polymerization conditions, where FG is selected from acyloxy, alkoxy and halogen, which are bonded to a secondary or tertiary carbon atom or to an allylic or a benzylic carbon atom, in a solvent inert toward the Lewis acid, the Lewis acid being used in less than the stoichiometric amount, based on the functional groups FG.
    • 其中至少60mol%的聚合物链具有至少一个烯属不饱和端基的聚异丁烯是通过在冷凝相中通过异丁烯或含异丁烯的单体混合物的阳离子聚合制备的,其中聚合在存在下进行 的引发剂体系,其包含i)选自共价金属氯化物和半金属氯化物的路易斯酸,和ii)至少一种在聚合条件下与路易斯酸形成碳阳离子或阳离子络合物的官能团FG的有机化合物I 其中FG选自酰基氧基,烷氧基和卤素,其在与路易斯酸呈惰性的溶剂中结合到仲或叔碳原子或烯丙基或苄基碳原子上,路易斯酸的用量小于 基于官能团FG的化学计量量。
    • 28. 发明授权
    • Method for producing low-molecular, highly reactive polyisobutylene
    • 生产低分子,高活性聚异丁烯的方法
    • US06407186B1
    • 2002-06-18
    • US09581154
    • 2000-06-12
    • Hans Peter RathUlrich KanneFrans van Deyck
    • Hans Peter RathUlrich KanneFrans van Deyck
    • C08F414
    • C08F110/10C08F6/02C08F2/001C08F4/14C08F2/14C08F2500/02C08F2500/03
    • A process for preparing low molecular weight, highly reactive polyisobutylene having an average molecular weight Mn of from 500 to 5000 Dalton and a terminal double bond content of more than 80 mol % by polymerization in the liquid phase of isobutene or hydrocarbon streams comprising isobutane [sic] with the aid of a boron trifluoride complex catalyst at from −40 to 20° C. and at from 1 to 20 bar comprises a) polymerizing until the residual isobutene content of the reaction mixture is less than 2% by weight, based on isobutene introduced, or removing residual isobutene towards the end of the polymerization until the residual isobutene content is less than 2% by weight, b) enriching the boron trifluoride complex catalyst which is obtained in the form of droplets in the disperse and/or coherent phase, c) recycling the complex-enriched phases to the polymerization and d) compensating for catalyst losses by adding boron trifluoride and, if necessary, complexing agents.
    • 一种制备低分子量高反应性聚异丁烯的方法,该聚异丁烯的平均分子量Mn为500-5000道尔顿,末端双键含量大于80mol%,通过在异丁烯或烃流的液相中聚合而得到,其中包括异丁烷 ]在-40至20℃和1至20巴之间的三氟化硼配合物催化剂的帮助下,a)聚合直到反应混合物的残余异丁烯含量小于2重量%,基于引入的异丁烯 或在聚合结束时除去残留的异丁烯,直到残余异丁烯含量小于2重量%,b)富集在分散和/或相干相中以液滴形式获得的三氟化硼配合物催化剂,c )将富含络合物的相循环到聚合反应中,d)通过加入三氟化硼和必要时的络合剂来补偿催化剂损失。