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    • 5. 发明申请
    • PROCESS FOR PRODUCING A CHLORINATED C3-6 ALKANE
    • 生产氯化C3-6烷烃的方法
    • US20160107955A1
    • 2016-04-21
    • US14882492
    • 2015-10-14
    • SPOLEK PRO CHEMICKOU A HUTNI VYROBU A.S.
    • Karel FILASPavel KUBICEKZdenek ONDRUSPetr SLADEK
    • C07C17/02C07C19/01
    • C07C17/02C07C17/275C07C17/38C07C17/383C07C19/01Y02P20/582
    • Disclosed is a process for producing a chlorinated C3-6 alkane comprising providing a reaction mixture comprising an alkene and carbon tetrachloride in a principal alkylation zone to produce chlorinated C3-6 alkane in the reaction mixture, and extracting a portion of the reaction mixture from the principal alkylation zone, wherein: a) the concentration of the chlorinated C3-6 alkane in the reaction mixture in the principal alkylation zone is maintained at a level such that the molar ratio of chlorinated C3-6 alkane:carbon tetrachloride in the reaction mixture extracted from the alkylation zone does not exceed 95:5 when the principal alkylation zone is in continuous operation; and/or b) the reaction mixture extracted from the principal alkylation zone additionally comprises alkene and the reaction mixture is subjected to a dealkenation step in which at least about 50% or more by weight of the alkene present in the reaction mixture is extracted therefrom and at least about 50% of the extracted alkene is fed back into the reaction mixture provided in the principal alkylation zone; and/or c) the reaction mixture present in the principal alkylation zone and extracted from the principal alkylation zone additionally comprises a catalyst, and the reaction mixture extracted from the principal alkylation zone is subjected to an aqueous treatment step in which the reaction mixture is contacted with an aqueous medium in an aqueous treatment zone, a biphasic mixture is formed and an organic phase comprising catalyst is extracted from the biphasic mixture.
    • 公开了一种生产氯化C3-6烷烃的方法,包括在主要烷基化区提供包含烯烃和四氯化碳的反应混合物,以在反应混合物中产生氯化的C 3-6烷烃,并从反应混合物中提取一部分反应混合物 主要烷基化区,其中:a)主烷基化区中反应混合物中氯化C3-6烷烃的浓度维持在使得反应混合物中氯化C 3-6烷烃:四氯化碳的摩尔比提取 当主烷基化区连续运行时,烷基化区不超过95:5; 和/或b)从主要烷基化区提取的反应混合物另外包含烯烃,并且将反应混合物进行脱烯烃化步骤,其中提取反应混合物中存在的烯烃的至少约50重量%或更多, 将提取的烯烃的至少约50%反馈到主烷基化区提供的反应混合物中; 和/或c)主要烷基化区中存在并从主要烷基化区提取的反应混合物另外包含催化剂,并且从主烷基化区提取的反应混合物经受水处理步骤,其中反应混合物接触 与含水介质在水处理区中形成双相混合物,从双相混合物中提取含有催化剂的有机相。