PROCESS FOR THE PRODUCTION OF ALKYLENE CARBONATE
    1.
    发明申请
    PROCESS FOR THE PRODUCTION OF ALKYLENE CARBONATE 有权
    生产亚烷基碳酸酯的方法

    公开(公告)号:US20110108762A1

    公开(公告)日:2011-05-12

    申请号:US12993136

    申请日:2009-05-19

    IPC分类号: C07D317/36 C09K3/00

    CPC分类号: C07D317/36 C07D317/38

    摘要: The invention relates to a process for the production of an alkylene carbonate by the reaction of an alkylene oxide with carbon dioxide in the presence of a phosphonium catalyst in which process (a) the alkylene oxide, carbon dioxide and phosphonium catalyst are continuously introduced into a reaction zone from which a product stream containing alkylene carbonate and phosphonium catalyst is withdrawn; (b) alkylene carbonate and a stream containing phosphoniura catalyst are separated from the product stream; (c) the alkylene carbonate, separated in step (b), is recovered as product; and (d) the stream containing phosphoniura catalyst, separated in step (b), is recycled to the reaction zone, in which process a treatment of alkylene carbonate and/or catalyst with a sorption agent comprising carbon is carried out.

    摘要翻译: 本发明涉及在鏻催化剂存在下,通过烯化氧与二氧化碳的反应制备碳酸亚烷基酯的方法,其中方法(a)将环氧烷,二氧化碳和鏻催化剂连续引入 取出含有碳酸亚烷基酯和鏻催化剂的产物流的反应区; (b)将碳酸亚烃酯和含有膦酰氧基催化剂的物流与产物流分离; (c)在步骤(b)中分离的碳酸亚烃酯作为产物回收; 和(d)将在步骤(b)中分离的含有膦酰氧基催化剂的料流再循环到反应区,在该方法中,用含碳吸附剂处理碳酸亚烷基酯和/或催化剂。

    Process for the production of alkylene carbonate and use of alkylene carbonate thus produced in the manufacture of an alkane diol and a dialkyl carbonate
    2.
    发明授权
    Process for the production of alkylene carbonate and use of alkylene carbonate thus produced in the manufacture of an alkane diol and a dialkyl carbonate 有权
    用于制备碳酸亚烷基酯的方法和在制备烷烃二醇和碳酸二烷基酯中如此制备的亚烷基碳酸酯的用途

    公开(公告)号:US07456299B2

    公开(公告)日:2008-11-25

    申请号:US11677997

    申请日:2007-02-22

    IPC分类号: C07D317/08

    摘要: An alkylene carbonate is produced by the reaction of an alkylene oxide with carbon dioxide in the presence of a phosphonium compound as catalyst in a process in which (a) the alkylene oxide, carbon dioxide and the phosphonium catalyst are continuously introduced into a reaction zone from which a product stream containing alkylene carbonate and catalyst is withdrawn, (b) alkylene carbonate and a mixture of alkylene carbonate and phosphonium catalyst are separated from the product stream, (c) the alkylene carbonate, separated in step (b), is recovered as product, and (d) the mixture of alkylene carbonate and phosphonium catalyst is continuously recycled to the reaction zone. The alkylene carbonate thus produced is suitably reacted with an alkanol to produce an alkane diol and a dialkyl carbonate.

    摘要翻译: 在鏻化合物作为催化剂的存在下,通过烯化氧与二氧化碳的反应制备碳酸亚烃酯,其中(a)将环氧烷,二氧化碳和鏻催化剂从 取出含有碳酸亚烃酯和催化剂的产物流,(b)碳酸亚烷基酯和碳酸亚烃酯和鏻催化剂的混合物与产物流分离,(c)将步骤(b)中分离的碳酸亚烃酯回收为 产物,和(d)碳酸亚烷基酯和鏻催化剂的混合物连续循环到反应区。 这样制得的碳酸亚烃酯适当地与烷醇反应生成烷烃二醇和碳酸二烷基酯。

    Process for the production of alkylene carbonate
    3.
    发明授权
    Process for the production of alkylene carbonate 有权
    碳酸亚烷基酯的制备方法

    公开(公告)号:US08735607B2

    公开(公告)日:2014-05-27

    申请号:US12993136

    申请日:2009-05-19

    IPC分类号: C07D317/36 C07D317/38

    CPC分类号: C07D317/36 C07D317/38

    摘要: The invention relates to a process for the production of an alkylene carbonate by the reaction of an alkylene oxide with carbon dioxide in the presence of a phosphonium catalyst in which process (a) the alkylene oxide, carbon dioxide and phosphonium catalyst are continuously introduced into a reaction zone from which a product stream containing alkylene carbonate and phosphonium catalyst is withdrawn; (b) alkylene carbonate and a stream containing phosphoniura catalyst are separated from the product stream; (c) the alkylene carbonate, separated in step (b), is recovered as product; and (d) the stream containing phosphoniura catalyst, separated in step (b), is recycled to the reaction zone, in which process a treatment of alkylene carbonate and/or catalyst with a sorption agent comprising carbon is carried out.

    摘要翻译: 本发明涉及在鏻催化剂存在下,通过烯化氧与二氧化碳的反应制备碳酸亚烷基酯的方法,其中方法(a)将环氧烷,二氧化碳和鏻催化剂连续引入 取出含有碳酸亚烷基酯和鏻催化剂的产物流的反应区; (b)将碳酸亚烃酯和含有膦酰氧基催化剂的物流与产物流分离; (c)在步骤(b)中分离的碳酸亚烃酯作为产物回收; 和(d)将在步骤(b)中分离的含有膦酰氧基催化剂的料流再循环到反应区,在该方法中,用含碳吸附剂处理碳酸亚烷基酯和/或催化剂。