Catalyst and process for the fluid-bed oxychlorination of ethylene to EDC
    136.
    发明授权
    Catalyst and process for the fluid-bed oxychlorination of ethylene to EDC 失效
    催化剂和乙烯流动床氧氯化为EDC的方法

    公开(公告)号:US4740642A

    公开(公告)日:1988-04-26

    申请号:US898566

    申请日:1986-08-21

    CPC classification number: B01J27/10 B01J23/78 C07C17/156

    Abstract: A fluidizable catalyst composition is provided containing about 2% to about 8% by weight of copper (about 4% to about 17% by weight of copper salt), from about 0.2% to about 10% by weight of a rare earth metal salt(s), preferably the chloride salt(s), and from about 0.25% to about 2.3% by weight of an alkali metal salt(s), preferably the chloride salt(s), all weight percents based upon the total weight of the catalyst composition. The metals are codeposited on a fluidizable, high surface area alumina support. The weight of the alkali metal employed is not over 2.5% by weight (as the chloride) and the weight ratio of the rare earth metal salt(s) to the alkali metal salt(s) must be at least 0.8:1. Such catalyst compositions are extremely useful as fluid bed catalysts in the vapor phase oxychlorination reaction of ethylene, oxygen and hydrogen chloride to produce 1,2-dichloroethane (EDC). The use of the catalysts results in improved, high percent ethylene efficiencies and high percent HCl conversions, and avoids operating problems caused by stickiness of the catalyst in the fluid bed. A combination of copper chloride, potassium chloride and one or more of the rare earth chlorides on a fluidizable gamma alumina support, produces an excellent catalyst for a fluid bed ethylene oxychlorination process.

    Abstract translation: 提供了一种可流化的催化剂组合物,其含有约2%至约8%重量的铜(约4%至约17%重量的铜盐),约0.2%至约10%重量的稀土金属盐( s),优选氯化物盐,和约0.25重量%至约2.3重量%的碱金属盐,优选氯化物盐,基于催化剂的总重量,所有重量百分比 组成。 金属共沉积在可流化的高表面积氧化铝载体上。 所使用的碱金属的重量不超过2.5重量%(作为氯化物),稀土金属盐与碱金属盐的重量比必须至少为0.8:1。 这种催化剂组合物在乙烯,氧气和氯化氢的气相氧氯化反应中作为流化床催化剂非常有用,以产生1,2-二氯乙烷(EDC)。 催化剂的使用导致乙烯效率提高,乙烯转化率高,HCl转化率高,避免了催化剂在流化床中的粘性引起的操作问题。 在可流化的γ氧化铝载体上,氯化铜,氯化钾和一种或多种稀土氯化物的组合产生用于流化床乙烯氧氯化方法的优异催化剂。

    Catalyst for the orthomethylation of phenols
    137.
    发明授权
    Catalyst for the orthomethylation of phenols 失效
    用于苯酚正甲基化的催化剂

    公开(公告)号:US4720478A

    公开(公告)日:1988-01-19

    申请号:US901902

    申请日:1986-08-29

    CPC classification number: C07C37/16

    Abstract: A process and catalyst for the orthomethylation of phenols having at least one free ortho position, wherein the phenols are reacted with methanol in a molar ratio of about 1:1 to 1:10 at about 270.degree.-340.degree. C. in the gaseous phase under a pressure of about 1-4 bar absolute and with rates per unit volume (LHSV) of about 0.05-3 h.sup.-1 in the presence of an iron oxide catalyst. This catalyst consists essentially of (a) iron oxide, (b) molybdenum oxide or tungsten oxide and (c) one or several oxides of the elements magnesium, calcium, barium, lanthanum, cerium or manganese in a metal-atomic ratio of about (a):(b):(c):of 100:0.2-10:0.2-10.

    Abstract translation: 一种用于使具有至少一个游离邻位的苯酚的正甲基化的方法和催化剂,其中所述酚在约270-140℃在气相中以约1:1至1:10的摩尔比与甲醇反应 在约1-4巴绝对压力下,在铁氧化物催化剂存在下,每单位体积(LHSV)为约0.05-3h -1。 该催化剂基本上由(a)氧化铁,(b)氧化钼或氧化钨和(c)元素镁,钙,钡,镧,铈或锰元素的一种或几种氧化物组成,金属原子比约为 a):( b):( c):100:0.2-10:0.2-10。

    Process for dimerization
    138.
    发明授权
    Process for dimerization 失效
    二聚过程

    公开(公告)号:US4687877A

    公开(公告)日:1987-08-18

    申请号:US880033

    申请日:1986-06-30

    Abstract: A process for the dimerization of propylene or a C.sub.4 olefin or the codimerization of ethylene with propylene or a C.sub.4 olefin comprising passing the olefin(s) in contact with a catalyst comprising (a) elemental potassium and (b) elemental copper, and (c) an alpha-alumina support therefor, wherein:(i) the potassium is present in the catalyst in an amount in the range of about 0.25 to about 30 percent by weight based on the weight of the catalyst;(ii) the ratio of copper to potassium, by weight, is in the range of about 0.1 to one to about 5 to one; and(iii) the process is carried out at a temperature in the range of about 75.degree. C. to about 225.degree. C. and at a pressure in the range of about atmospheric pressure to about 10,000 psig.

    Abstract translation: 丙烯或C 4烯烃二聚化或乙烯与丙烯或C 4烯烃的二聚化的方法,包括使烯烃与包含(a)元素钾和(b)元素铜的催化剂接触,和(c )一种α-氧化铝载体,其中:(i)催化剂中的钾以基于催化剂重量的约0.25至约30重量%的量存在; (ii)铜与钾的重量比在约0.1至1至约5比1的范围内; 和(iii)该方法在约75℃至约225℃的温度和约大气压至约10,000psig范围内的压力下进行。

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