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    • 55. 发明授权
    • Process for preparing low molecular weight, highly reactive
polyisobutylene
    • 制备低分子量,高活性聚异丁烯的方法
    • US5962604A
    • 1999-10-05
    • US973643
    • 1997-11-25
    • Hans Peter Rath
    • Hans Peter Rath
    • C08F2/00C08F4/14C08F110/10
    • C08F110/10Y02P20/582
    • Low molecular weight, highly reactive polyisobutene having an average molecular weight M.sub.n of from 500 to 20000 Dalton and containing over 80 mol % of terminal double bonds is prepared by the polymerization of isobutene or an isobutene-containing hydrocarbon stream in the liquid phase and with the aid of a boron trifluoride complex catalyst at from -40 to 0.degree. C. and at from 1 to 20 bar, by a process in which the polymerization reaction is carried out in at least two polymerization stages, the added isobutene being polymerized to a partial conversion of up to 95% in the first polymerization stage and the polymerization of the remaining isobutene being continued in one or more subsequent polymerization stages, without or after prior isolation of the polyisobutene formed in the first polymerization stage.
    • PCT No.PCT / EP96 / 02414 Sec。 371日期:1997年11月25日 102(e)1997年11月25日PCT PCT 1996年6月4日PCT公布。 出版物WO96 / 40808 日期:1996年12月19日通过异丁烯或含异丁烯的烃流的聚合制备平均分子量为500〜20000道尔顿,含有超过80摩尔%的末端双键的低分子量的高活性聚异丁烯 液相,并且在-40至0℃和1至20巴的三氟化硼配合物催化剂的帮助下,通过聚合反应在至少两个聚合阶段中进行的方法,加入的异丁烯 在第一聚合阶段中聚合至高达95%的部分转化率,并且在一个或多个后续聚合阶段中继续聚合剩余的异丁烯,而不需要或之后分离在第一聚合阶段中形成的聚异丁烯。
    • 59. 发明授权
    • Method for producing polyisobutene
    • 生产聚异丁烯的方法
    • US07217773B2
    • 2007-05-15
    • US10542928
    • 2004-01-23
    • Hans Peter RathThomas PernerHelmut Mach
    • Hans Peter RathThomas PernerHelmut Mach
    • C08F4/14C08F110/10
    • C08F110/10Y02P20/582C08F4/14C08F2500/02C08F2500/03
    • A process is described for preparing polyisobutene having a content of terminal vinylidene groups of at least 75 mol % by polymerizing isobutene or isobutenic hydrocarbon mixtures in the liquid phase in the presence of a boron trifluoride complex catalyst of the composition (BF3)a.L1b.L2c.L3d where L1 is water, a primary C1–C5-alkanol and/or a secondary C3–C5-alkanol, L2 is at least one aldehyde and/or one ketone, L3 is an ether having at least 5 carbon atoms, a secondary alkanol having at least 6 carbon atoms, a primary alkanol having at least 6 carbon atoms and/or a tertiary alkanol, the b:a ratio is in the range from 0.9 to 3.0, the c:a ratio is in the range from 0.01 to 0.5, and the d:a ratio is in the range from 0 to 1.0.
    • 描述了一种制备具有至少75mol%的末端亚乙烯基含量的聚异丁烯的方法,通过在液相中聚合异丁烯或异丁烯烃混合物,在三元组配合物催化剂存在下, 描述=“在线公式”end =“lead”?>(BF 3) a β-in-line-formula description =“In-line-formula”=“In- 其中L 1是水,主要C 1 -C 5 - 烷醇和/或 仲C 3 -C 5 - 烷醇,L 2是至少一种醛和/或一种酮,L 3, SUP>是具有至少5个碳原子的醚,具有至少6个碳原子的仲链烷醇,具有至少6个碳原子的伯烷醇和/或叔链烷醇,b:a的比例在0.9至 3.0,c:a的比例在0.01至0.5的范围内,d:a的比例为 范围从0到1.0。