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    • 5. 发明申请
    • METHOD FOR PRODUCING LINEAR A-OLEFINS
    • 用于生产线性α-烯烃
    • WO2011095273A3
    • 2011-10-06
    • PCT/EP2011000131
    • 2011-01-13
    • LINDE AGHOFMANN KARL-HEINZZANDER HANS-JOERGWELLENHOFER ANTONMUELLER WOLFGANGWOEHL ANINA
    • HOFMANN KARL-HEINZZANDER HANS-JOERGWELLENHOFER ANTONMUELLER WOLFGANGWOEHL ANINA
    • C07C2/08C07C11/02
    • C07C2/08C07C11/02
    • The invention relates to a method for producing linear a-olefins, wherein ethylene 1a in the liquid phase is fed into the oligomerisation reactor 2. The oligomerisation reactor 2 has a mechanical stirring mechanism 2a, in order to ensure optimum blending of the liquid ethylene and the catalyst in the liquid phase. Vaporised ethylene together with light a-olefins and a small proportion of the organic solvent are removed from the top of the oligmerisation reactor 2. The gas mixture removed from the top of the reactor 2, together with gaseous fresh ethylene 7, is condensed by means of a heat exchanger 3 and a separator 4. The liquid phase removed from the separator 4 is returned by means of a circulation pump 5a as a liquid ethylene batch 1a to the oligomerisation reactor 2. The liquid products of the oligomerisation reaction are removed laterally from the bottom of the reactor 2.
    • 本发明涉及一种制备直链α-烯烃,其中乙烯是在低聚反应器中的液相进料1a上的方法。2 低聚反应器2具有机械搅拌器2a中,为了确保液体乙烯最佳混合并在液相中的催化剂。 从低聚反应器2蒸发乙烯的头部与轻微的α-烯烃和所述有机溶剂的较小比例一起抽出。 从反应器2的顶部排出的气体混合物被冷凝气态乙烯一起通过热交换器3和分离器的装置使得7。4 来自分离器4的液相取出的由循环泵5a中作为液体乙烯进料返回到低聚反应器1a的方式进行的。2 低聚反应的液体产物从侧向反应器2 8的底部抽出