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    • 4. 发明申请
    • PROCESS FOR PREPARING ETHYLENE AND PROPYLENE
    • 制备乙烯和丙烯的方法
    • WO2013034677A1
    • 2013-03-14
    • PCT/EP2012/067492
    • 2012-09-07
    • SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.CHEWTER, Leslie, AndrewRAMESH, RajaramVAN WESTRENEN, Jeroen
    • CHEWTER, Leslie, AndrewRAMESH, RajaramVAN WESTRENEN, Jeroen
    • C07C1/20C07C4/06C07C11/04C07C11/06
    • C07C1/22C07C1/20C07C4/06C07C29/48C07C2529/42C07C2529/70C07C2529/83C07C2529/85C07D301/03Y02P30/42C07C11/04C07C11/06
    • The present invention provides aprocess for preparing ethylene and/or propylene, comprising the steps of a)contacting a stream comprising C4+ olefins with a zeolite-comprising catalyst at a temperature in the range of from 350 to 1000 °C and retrieving an olefinic product stream comprising: - ethylene and/or propylene, and - a C4+ hydrocarbon fraction, comprising paraffins, normal olefins and iso-olefins; b) subjecting at least part of the C4+ hydrocarbon fraction to an etherification process with methanol and/or ethano lwherein at least part of the iso-olefins are converted with methanol and/or ethanol to an tert-alkyl ether, and retrieving an etherification product stream; c) separating at least part of the etherification product stream into at least an ether-enriched stream and an iso- olefin-depleted C4+ hydrocarbon stream; d )withdrawing part of the iso-olefin-depleted C4+ hydrocarbon stream from the process to purge part of the paraffinic C4+ hydrocarbons; e) recycling another part of the iso-olefin-depleted C4+ hydrocarbon stream to step (a); f) converting at least part of the tert-alkyl ether in the ether-enriched stream to ethylene and/or propylene by contacting at least part of the ether-enriched stream with a molecular sieve-comprising catalyst at a temperature in the range of from 350 to 1000 °C.
    • 本发明提供了制备乙烯和/或丙烯的方法,包括以下步骤:a)在350-1000℃的温度范围内使包含C4 +烯烃的物流与含沸石的催化剂接触并回收烯烃产物流 包括: - 乙烯和/或丙烯,以及 - C4 +烃馏分,其包含链烷烃,正烯烃和异烯烃; b)使用甲醇和/或乙醇1将至少部分的C4 +烃馏分进行醚化过程,其中至少部分异烯烃用甲醇和/或乙醇转化成叔烷基醚,并回收醚化产物 流; c)将至少部分醚化产物流分离成至少一种富醚流和一种异烯烃贫化的C4 +烃流; d)从该方法中取出一部分异烯烃贫化的C4 +烃物流以清除部分链烷烃C4 +烃; e)将另一部分异烯烃贫化的C4 +烃流再循环到步骤(a); f)通过使至少部分富含乙醚的料流与含分子筛的催化剂在至少一部分乙醚和/或丙烯的温度范围内接触,将至少部分乙醚富集料流中的叔烷基醚转化为 350〜1000℃。