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    • 8. 发明申请
    • PROCESSES FOR THE PRODUCTION OF ETHYLENE GLYCOL
    • 生产乙二醇的方法
    • WO2012104252A1
    • 2012-08-09
    • PCT/EP2012/051450
    • 2012-01-30
    • SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.VAN OGTROP, JanSMAARDIJK, Abraham AdriaanSTICHTER, Hendrik
    • VAN OGTROP, JanSMAARDIJK, Abraham AdriaanSTICHTER, Hendrik
    • C07C29/09C07C29/12C07C29/64C07C29/80C07C31/20C07C31/36C07D301/04C07D301/32C07D317/12C07D317/38
    • C07D301/22C07C29/106C07C29/12C07D301/04Y02P20/52C07C31/202
    • The invention provides a process for the production of ethylene glycol comprising the steps of: (i) supplying ethylene and oxygen and an organic chloride moderator to an ethylene oxide reactor wherein ethylene and oxygen react in the presence of a catalyst to produce ethylene oxide, thereby producing a reactor product stream; (ii) supplying the reactor product stream to an ethylene oxide absorber wherein ethylene oxide is recovered from the reactor product stream by absorption in water in the absorber section, thereby producing a fat absorbent stream; (iii) supplying the fat absorbent stream to an ethylene oxide stripper wherein the fat absorbent stream is steam stripped, thereby producing a concentrated ethylene oxide stream and a lean absorbent stream; (iv) recirculating the lean absorbent stream to the ethylene oxide absorber; (v) optionally supplying the concentrated ethylene oxide stream to one or more carboxylation reactors wherein ethylene oxide reacts with carbon dioxide to form an ethylene carbonate stream; and (vi) supplying the concentrated ethylene oxide stream and/or the ethylene carbonate stream to one or more hydrolysis reactors wherein ethylene oxide and/or ethylene carbonate reacts with water in the presence of a hydrolysis catalyst selected from one or more basic alkali metal salts to form an ethylene glycol stream; wherein the process comprises the additional steps of: (vii) removing a glycol bleed stream from the ethylene oxide stripper; and (viii) adding a base to the ethylene oxide stripper such that the pH in the bottom section of the stripper i maintained in the range of from at least 9.5 to at most 12.0.
    • 本发明提供一种生产乙二醇的方法,其包括以下步骤:(i)向环氧乙烷反应器供应乙烯和氧气和有机氯化物缓慢剂,其中乙烯和氧气在催化剂存在下反应生成环氧乙烷,从而 生产反应器产品流; (ii)将反应器产物流供应到环氧乙烷吸收器,其中通过吸收在吸收器部分中的水中从反应器产物流中回收环氧乙烷,从而产生脂肪吸收剂流; (iii)将脂肪吸收物流供应到环氧乙烷汽提器,其中吸收汽油被蒸汽汽提,从而产生浓缩的环氧乙烷物流和贫吸收物流; (iv)将贫吸收物流再循环到环氧乙烷吸收器; (v)任选地将浓缩的环氧乙烷物流供应到一个或多个羧化反应器,其中环氧乙烷与二氧化碳反应形成碳酸亚乙酯流; 和(vi)将浓缩的环氧乙烷物流和/或碳酸亚乙酯物流供应到一个或多个水解反应器,其中环氧乙烷和/或碳酸亚乙酯在水解催化剂存在下与水反应,所述水解催化剂选自一种或多种碱性碱金属盐 以形成乙二醇流; 其中所述方法包括以下附加步骤:(vii)从所述环氧乙烷汽提器除去二醇排出物流; 和(viii)向环氧乙烷汽提器中加入碱,使得汽提器i底部的pH保持在至少9.5至至多12.0的范围内。