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    • 3. 发明授权
    • Supported catalyst containing pseudo-boehmite and &ggr;-Al2O3, production of same and its use for producing 1,2-dichloroethane
    • 含有假勃姆石和γ-Al2O3的负载催化剂,生产方法及其用于生产1,2-二氯乙烷
    • US06680416B1
    • 2004-01-20
    • US09646003
    • 2000-09-11
    • Werner HebgenChristopher William RiekerRuprecht Meissner
    • Werner HebgenChristopher William RiekerRuprecht Meissner
    • C07C1900
    • B01J27/122C07C17/156C07C19/045
    • A process for preparing 1,2-dichloroethane by reacting about 2 mols of ethylene, about 4 mols of hydrogen chloride and about 1 mol of oxygen in the presence of a fixed bed of supported catalyst based on copper(II) chloride in only one reaction zone at a pressure of from 2 to 10 bar and at from 220 to 280° C., separating off 1,2-dichloroethane and water from the reaction mixture emerging from the reaction zone and passing most of the exhaust gas back into the reaction zone, where, prior to entry into the reaction zone, the exhaust gas is mixed with ethylene, hydrogen chloride and oxygen, and the oxygen content of the mixture does not exceed 7% by volume, and where the ethylene content of the gas mixture entering into the reaction zone is regulated so that the exhaust gas comprises less than 20% by volume of ethylene, where the supported catalyst used is obtained by tableting a mixture of pseudoboehmite and &ggr;-Al2O3 in a weight ratio from 4:1 to 1:4, if desired with addition of tableting auxiliaries, loading this support with the active components by saturating with a CuCl2/KCl solution so that the copper content is from 1 to 15% by weight and the potassium content is from 0.1 to 8% by weight, based in each case on the total weight of the catalyst, and then drying the catalyst at from 60 to 400° C.
    • 在仅一次反应的基于氯化铜(II)的固定床的负载型催化剂存在下,使约2摩尔乙烯,约4摩尔氯化氢和约1摩尔氧气反应制备1,2-二氯乙烷的方法 在2至10巴的压力和220至280℃的压力范围内,从反应区中排出的反应混合物中分离出1,2-二氯乙烷和水,并将大部分废气送回反应区 ,其中在进入反应区之前,将废气与乙烯,氯化氢和氧气混合,并且混合物的氧含量不超过7体积%,并且其中气体混合物的乙烯含量进入 对反应区进行调节,以使废气中的乙烯的含量少于20体积%,其中使用的负载催化剂是通过将重量比为4:1至1:4的假勃姆石和γ-Al2O3的混合物压片而得到的, 如果需要添加表 丁基辅助剂,用CuCl 2 / KCl溶液饱和将活性组分负载该载体,使铜含量为1〜15重量%,钾含量为0.1〜8重量%,基于 催化剂的总重量,然后在60-400℃干燥催化剂。