Alpha-olefin oligomerization using supported metal halide catalysts
    61.
    发明授权
    Alpha-olefin oligomerization using supported metal halide catalysts 失效
    使用负载金属卤化物催化剂的α-烯烃低聚

    公开(公告)号:US5451704A

    公开(公告)日:1995-09-19

    申请号:US057029

    申请日:1993-05-05

    摘要: A process for the production of hydrocarbon lubricant basestock comprises contacting C.sub.2 to C.sub.20 alpha-olefin feedstock, or mixtures thereof, e.g., 1-decene, under heterogeneous oligomerization conditions with a catalyst comprising halides of a metal component anchored on an adsorbent inorganic oxide solid, e.g., silica, by an oxygen-metal bond to provide a reaction mixture containing said hydrocarbon lubricant basestock. The catalyst is prepared by contacting the inorganic oxide solid with organic metal halide of the formula RMXY wherein R is alkyl or aryl, M is aluminum, X is halogen and Y is selected from the group consisting of halogen, alkyl, alkenyl, aryl, alkoxy, and amido moieties.

    摘要翻译: 用于生产烃润滑剂基础油料的方法包括在非均相低聚条件下使C2-C20α-烯烃原料或其混合物例如1-癸烯与包含锚定在吸附剂无机氧化物固体上的金属组分的卤化物接触, 例如二氧化硅,通过氧 - 金属键提供含有所述烃润滑剂基础油料的反应混合物。 通过使无机氧化物固体与式RMXY的有机金属卤化物接触来制备催化剂,其中R是烷基或芳基,M是铝,X是卤素,Y选自卤素,烷基,烯基,芳基,烷氧基 和酰氨基部分。

    High VI synthetic lubricants from cracked slack wax
    63.
    发明授权
    High VI synthetic lubricants from cracked slack wax 失效
    高VI合成润滑油从裂纹松散蜡

    公开(公告)号:US5146022A

    公开(公告)日:1992-09-08

    申请号:US571345

    申请日:1990-08-23

    IPC分类号: C10M107/10

    摘要: A process is disclosed for the production of synthetic lubricants having high viscosity index and thermal stability by oligomerizing a mixture of C.sub.5 -C.sub.18 or C.sub.6 -C.sub.16 alpha-olefins produced from the thermal cracking of slack wax or recycled slack wax. The oligomerization is carried out with Lewis acid catalyst. Promoted aluminum chloride is a preferred catalyst.

    摘要翻译: 公开了通过使由松散蜡或回收的松散蜡的热裂解产生的C5-C18或C6-C16α-烯烃的混合物低聚而生产具有高粘度指数和热稳定性的合成润滑剂的方法。 低聚反应用路易斯酸催化剂进行。 促进的氯化铝是优选的催化剂。

    Catalyst composition for polymerizing alpha-olefin polymers of
relatively narrow molecular weight distribution
    66.
    发明授权
    Catalyst composition for polymerizing alpha-olefin polymers of relatively narrow molecular weight distribution 失效
    用于聚合具有相对较窄分子量分布的α-烯烃聚合物的催化剂组合物

    公开(公告)号:US4668650A

    公开(公告)日:1987-05-26

    申请号:US815845

    申请日:1986-01-03

    CPC分类号: C08F10/00

    摘要: A catalyst composition for polymerizing alpha-olefins is prepared by treating a carrier containing OH groups with a liquid solution containing an excess of an organomagnesium composition with respect to the OH groups and contacting the thus-formed magnesium-containing carrier with a hydrocarbyl alcohol and at least one transition metal compound. Prior to contacting the magnesium-containing carrier with the alcohol, most of the liquid must be removed therefrom, so that it comprises not more than about 6% of the liquid. The amount of the transition metal compound is such that the molar ratio thereof to magnesium in the reaction mixture is about 0.3 to about 0.9. Also disclosed is a process for polymerizing alpha-olefins in the presence of the catalyst of the invention.

    摘要翻译: 用于聚合α-烯烃的催化剂组合物通过用含有过量的有机镁组合物的液体溶液相对于OH基团处理含有OH基团的载体并将如此形成的含镁载体与烃基接触并在 至少一种过渡金属化合物。 在使含镁载体与醇接触之前,大部分液体必须从其中除去,使其不超过约6%的液体。 过渡金属化合物的量使得其与反应混合物中的镁的摩尔比为约0.3至约0.9。 还公开了在本发明催化剂存在下聚合α-烯烃的方法。

    Production of para-isopropylphenol
    67.
    发明授权
    Production of para-isopropylphenol 失效
    对异丙基苯酚的生产

    公开(公告)号:US4391998A

    公开(公告)日:1983-07-05

    申请号:US313425

    申请日:1981-10-21

    申请人: Margaret M. Wu

    发明人: Margaret M. Wu

    IPC分类号: C07C37/14 C07C39/06

    CPC分类号: C07C37/14 C07C37/16

    摘要: Phenol is catalytically alkylated with an isopropanol or propylene alkylating agent to form high yields of an isopropylphenol product enriched in the para-isomer of isopropylphenol. Such an alkylation process is carried out under catalytic alkylation conditions including a temperature of from about 200.degree. C. to 300.degree. C. and contact with a crystalline zeolite catalyst having a silica to alumina molar ratio of at least about 12 and a constraint index of about 1 to 12.

    摘要翻译: 苯酚用异丙醇或丙烯烷基化剂催化烷基化以形成富含异丙基苯酚对位异构体的异丙基苯酚产物的高收率。 这样的烷基化方法在催化烷基化条件下进行,包括温度为约200℃至300℃,并与二氧化硅与氧化铝摩尔比至少约为12的结晶沸石催化剂接触,并且约束指数 约1至12。

    Selective hydrogenation of vinyltoluene
    68.
    发明授权
    Selective hydrogenation of vinyltoluene 失效
    乙烯基甲苯的选择性氢化

    公开(公告)号:US4379027A

    公开(公告)日:1983-04-05

    申请号:US334346

    申请日:1981-12-24

    CPC分类号: C07C7/163

    摘要: This invention provides a process for obtaining m-methylstyrene from a mixture with p-methylstyrene that comprises hydrogenating a mixture of p-methylstyrene and m-methylstyrene in the presence of a zeolite having a Constraint Index of about 1 to about 12, a silica to alumina mole ratio of at least about 12, and a dried crystal density of not less than about 1.6 grams per cubic centimeter, modified with at least one element of Group IA, IIA, IVB, or VB of the Periodic Chart of the Elements and a metal of Group VIII of the Periodic Chart of the Elements; thereby obtaining a mixture of m-methylstyrene and p-ethyltoluene, and removing p-ethyltoluene by distillation.

    摘要翻译: 本发明提供从与对甲基苯乙烯的混合物中获得间甲基苯乙烯的方法,该方法包括在约1至约12的约束指数的沸石存在下氢化对甲基苯乙烯和间甲基苯乙烯的混合物, 氧化铝摩尔比为至少约12,干燥晶体密度不小于约1.6克/立方厘米,用元素周期表的IA,IIA,IVB或VB族元素的至少一种元素修饰, 元素周期表第八组金属; 从而获得间甲基苯乙烯和对乙基甲苯的混合物,并通过蒸馏除去对乙基甲苯。