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公开(公告)号:US20160264490A1
公开(公告)日:2016-09-15
申请号:US15032810
申请日:2014-10-30
Applicant: SHELL OIL COMPANY
Inventor: Richard Addison SANBORN , Bernardus Maria GEERTSHUIS , Leslie Andrew CHEWTER , Ye-Mon CHEN
CPC classification number: C07C1/20 , B01J29/90 , C07C4/06 , C07C2529/00 , C07C2529/40 , Y02P20/584 , C07C11/02
Abstract: A process for converting oxygenates to olefins comprising: a) feeding an oxygenate stream to a reactor; b) contacting the oxygenate stream with a molecular sieve catalyst to form products and coke on the catalyst; c) passing the products and entrained catalyst into a first gas/solid separation device to separate the products from the catalyst; d) removing the products from the first gas/solid separation device; e) passing a portion of the catalyst from the reactor to a regenerator; f) regenerating the catalyst in the regenerator by contacting it with a regeneration medium to combust the coke on the catalyst and form combustion products; and g) passing the combustion products and entrained catalyst into a second gas/solid separation device to separate the combustion products from the catalyst wherein the separation efficiency of the first gas/solid separation device is greater than the separation efficiency of the second gas/solid separation device.
Abstract translation: 一种将含氧物转化成烯烃的方法,包括:a)将含氧化合物物流送入反应器; b)使含氧物流与分子筛催化剂接触以在催化剂上形成产物和焦炭; c)将产物和夹带的催化剂通入第一气/固分离装置以将产物与催化剂分离; d)从第一气/固分离装置中取出产品; e)将一部分催化剂从反应器通入再生器; f)通过使再生器与再生介质接触来再生催化剂,使催化剂上的焦炭燃烧并形成燃烧产物; 并且g)将燃烧产物和夹带的催化剂通入第二气/固分离装置,以将燃烧产物与催化剂分离,其中第一气/固分离装置的分离效率大于第二气/固分离装置的分离效率 分离装置