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SHEAR STABLE MULTIVISCOSITY GRADE LUBRICATING OILS ALPHAOLEFIN POLYMERS OF CONTROLLED MOLECULAR SIZE AND DISTRIBUTION AND METHOD OF PREPARATION

机译:剪切尺寸稳定的剪切稳定多粘度梯度润滑油α-烯烃聚合物及其制备方法

摘要

1359067 Olefin polymers GULF RESEARCH & DEVELOPMENT CO 8 June 1972 [14 June 1971 (2) 18 April 1972 (2)] 26719/72 Heading C3P [Also in Division C5] Alpha-olefin polymers produced from a C 5 -C 12 α-olefin or mixture of C 3 -C 12 α-olefins with at least 20 mol. per cent of C 5 -C 12 α- olefins and having a weight average molecular weight Mw of 50,000 (M/84) to 1,000,000 (M/84), a number average molecular weight Mn of 4,000 (M/84) to 1,000,000 (M/84) where M is the molecular weight of the α-olefin or average molecular weight of the mixture of α-olefins, and a distribution factor Mw/Mn of 1 to 12, the upper limit of said distribution factor being 12 when Mw is 50,000 (M/84) and 2 when Mw is 1,000,000 (M/84) with the upper limit of the distribution factor proportionately decreasing from 12 to 2 as Mw increases from 50,000 (M/84) to 1,000,000 (M/84), may be prepared by reacting the monomers at 38 to 121‹ C. in the presence of hydrogen at a partial pressure of 0À007 to 10À5 kg/cmSP2/SP and a Ziegler-Natta catalyst useful for the polymerization of propylene at an olefin to catalyst weight ratio of 300 to 6000. The olefin may be 1-pentene, 1-hexane, 4-methyl-1-pentene or 1-decene, optionally in admixture with propylene, 1- butene, isobutylene or 1-octane. Preferred catalysts are titanium and vanadium halides mixed with aluminium alkyls and alkyl halides. The process may be effected batchwise or continuously, optionally in the presence of modifiers such as zinc chloride or diethyl zinc. The products may be used to improve the viscosity characteristics of lubricating oils. Examples describe the preparation of (1 to 3 and 5 to 28) polyhexenes and (4) polydecene in the presence of aluminium activated titanium trichloride and triethyl aluminium.
机译:1359067烯烃聚合物GULF RESEARCH&DEVELOPMENT CO 1972年6月8日[1971年6月14日(2)1972年4月18日(2)] 26719/72标题C3P [也在C5分部中]由C 5 -C 12α-烯烃或具有至少20摩尔的C 3 -C 12α-烯烃的混合物。 C 5 -C 12α-烯烃的百分含量,重均分子量Mw为50,000(M / 84)至1,000,000(M / 84),数均分子量Mn为4,000(M / 84)至1,000,000( M / 84),其中M是α-烯烃的分子量或α-烯烃混合物的平均分子量,分配系数Mw / Mn为1至12,当Mw时所述分配系数的上限为12为50,000(M / 84),当Mw为1,000,000(M / 84)时为2,随着Mw从50,000(M / 84)增至1,000,000(M / 84),分配因子的上限按比例从12减小至2,可以通过使单体在氢气存在下,分压为0到007到10到5-5 kg / cm 2 的条件下,在38到121℃下与用于丙烯聚合的Ziegler-Natta催化剂反应来制备烯烃与催化剂的重量比为300到6000。烯烃可以是1-戊烯,1-己烷,4-甲基-1-戊烯或1-癸烯,可选地与丙烯,1-丁烯,异丁烯r 1-辛烷。优选的催化剂是与烷基铝和烷基卤化物混合的钛和钒的卤化物。该方法可以间歇地或连续地进行,任选地在改性剂如氯化锌或二乙基锌的存在下进行。该产品可用于改善润滑油的粘度特性。实施例描述了在铝活化的三氯化钛和三乙基铝的存在下制备(1至3和5至28)多己烯和(4)聚癸烯。

著录项

  • 公开/公告号GB1359067A

    专利类型

  • 公开/公告日1974-07-10

    原文格式PDF

  • 申请/专利权人 GULF RESEARCH DEVELOPMENT CO;

    申请/专利号GB19720026719

  • 发明设计人

    申请日1972-06-08

  • 分类号C08F3/02;C10M1/18;

  • 国家 GB

  • 入库时间 2022-08-23 05:07:32

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