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    • 7. 发明授权
    • Process for the epoxidation of olefins
    • 烯烃环氧化方法
    • US06720436B2
    • 2004-04-13
    • US10384217
    • 2003-03-07
    • Willi HofenGeorg ThieleThomas HaasWolfgang WöllPercy KampeisBärbel Kolbe
    • Willi HofenGeorg ThieleThomas HaasWolfgang WöllPercy KampeisBärbel Kolbe
    • C07D30112
    • C07D301/12
    • A process for the catalytic epoxidation of olefins in at least one reaction stage comprising: (a) reacting the olefin with hydrogen peroxide in an organic, water-miscible solvent in the presence of a titanium silicalite catalyst in a reactor while continuously feeding an inert gas stream into the reactor, (b) continuously removing an exit gas stream containing olefin oxide, unreacted olefin, oxygen and inert gas from the reactor, (c) bringing the exit gas stream into contact in an absorption unit with the same solvent as used in the reaction stage, (d) removing a solvent stream loaded with olefin and olefin oxide from the absorption unit and (e) discharging an gas stream containing oxygen and the inert gas from the absorption unit.
    • 一种用于在至少一个反应阶段中对烯烃进行催化环氧化的方法,包括:(a)在反应器中在钛硅沸石催化剂存在下,使烯烃与有机的水混溶性溶剂中的过氧化氢反应,同时连续进料惰性气体 (b)从反应器中连续除去含有烯烃氧化物,未反应的烯烃,氧和惰性气体的出口气流,(c)使出口气流与吸收单元中的相同溶剂接触, 反应阶段,(d)从吸收单元除去负载有烯烃和烯烃氧化物的溶剂流,和(e)从吸收单元排出含有氧和惰性气体的气流。
    • 10. 发明授权
    • Process for the epoxidation of olefins
    • 烯烃环氧化方法
    • US06646141B2
    • 2003-11-11
    • US10203184
    • 2002-10-04
    • Willi HofenGeorg ThieleAlexander Möller
    • Willi HofenGeorg ThieleAlexander Möller
    • C07D30112
    • C07D301/12C07D301/32
    • The present invention relates to a process for the working up of a product stream from the epoxidation of olefins that contains olefin, olefin oxide, water-miscible organic solvent and water, by separating this product stream into an overhead product containing olefin, olefin oxide and organic solvent, and into a bottom product containing organic solvent and water, wherein the separation takes place in a pre-evaporator with at most 5 theoretical separation stages, and 20 to 60% of the total amount of organic solvent introduced with the product stream is removed with the overhead product and the residue remains in the bottom product, as well as a process for the epoxidation of olefins that includes this working up stage.
    • 本发明涉及一种通过将该产物流分离成含有烯烃,烯烃氧化物的塔顶产物和来自含有烯烃,烯烃氧化物,水混溶性有机溶剂和水的烯烃的环氧化来处理产物流的方法, 有机溶剂,并进入含有有机溶剂和水的底部产物,其中分离在预蒸发器中进行至多5个理论分离阶段,并且与产物流引入的有机溶剂的总量的20至60% 用塔顶产物除去残余物残留在底部产物中,以及包括该加工阶段的烯烃环氧化方法。