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公开(公告)号:US08987540B2
公开(公告)日:2015-03-24
申请号:US14136150
申请日:2013-12-20
Applicant: Shell Oil Company
Inventor: Jeroen Van Westrenen
IPC: C07C7/00 , C07C7/10 , C07D301/03 , C07C1/20 , C07C7/08
CPC classification number: C07C7/10 , C07C1/20 , C07C7/08 , C07D301/03 , C07C11/06
Abstract: The present invention relates to a process for removing oxygenate from an olefin stream comprising oxygenate, comprising providing to an oxygenate recovery zone the olefin stream comprising oxygenate and a solvent comprising propanol, treating the olefin stream comprising oxygenate with the solvent, and retrieving from the oxygenate recovery zone at least one oxygenate-depleted olefinic product stream comprising olefin and a spent solvent comprising at least part of the oxygenate.
Abstract translation: 本发明涉及从包含含氧化合物的烯烃流中除去含氧化合物的方法,其包括向含氧物回收区提供包含含氧化合物和包含丙醇的溶剂的烯烃流,用溶剂处理包含含氧化合物的烯烃流,以及从含氧化合物中回收 至少一种含氧化合物贫化的烯烃产物流包含烯烃和包含至少部分含氧化合物的废溶剂。
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公开(公告)号:US20150045586A1
公开(公告)日:2015-02-12
申请号:US14368569
申请日:2012-12-21
Applicant: SHELL OIL COMPANY
Inventor: Sivakumar Sadasivan Vijayakumari , Jeroen Van Westrenen
CPC classification number: C07C45/50 , C01B3/16 , C07C1/20 , C07C1/22 , C07C4/06 , C07C29/14 , C07C29/141 , C07C2521/04 , C07C2521/06 , C07C2521/08 , C07C2521/12 , C07C2529/40 , C07C2529/83 , C07C2529/84 , C07C2529/85 , Y02P30/42 , C07C11/06 , C07C11/04 , C07C31/12 , C07C47/02
Abstract: The present invention provides a process for the production of aldehydes and/or alcohols, which process comprises the steps of: (a) reacting an oxygenate and/or olefinic feed in a reactor in the presence of a molecular sieve catalyst to form an effluent comprising olefins, comprising propylene; (b) separating the effluent comprising olefins as obtained in step (a) into at least a first olefinic product fraction comprising propylene and a second olefinic product fraction; (c) subjecting at least part of the first olefinic product fraction as obtained in step (b) to a hydroformylation process to form aldehydes; (d) separating at least part of the aldehydes as obtained in step (c) into at least a first product fraction of aldehydes and a second product fraction of aldehydes; and (e) hydrogenating at least part of the aldehydes in the first and/or second product fraction of aldehydes as obtained in step (d) to form a first product fraction of alcohols and/or a second product fraction of alcohols; (f) recycling at least part of the first and/or second product fraction of alcohols obtained in step (e) to step (a).
Abstract translation: 本发明提供了一种生产醛和/或醇的方法,该方法包括以下步骤:(a)在分子筛催化剂存在下使反应器中的含氧化合物和/或烯烃进料反应形成流出物,其包含 烯烃,包括丙烯; (b)将步骤(a)中获得的包含烯烃的流出物分离成至少包含丙烯和第二烯属产物馏分的第一烯烃产物级分; (c)将步骤(b)中获得的至少部分第一烯属产物级分进行加氢甲酰化过程以形成醛; (d)将步骤(c)中获得的至少一部分醛分离成至少醛的第一产物级分和醛的第二产物级分; 和(e)将步骤(d)中获得的醛的第一和/或第二产物级分中的至少部分醛氢化以形成醇的第一产物级分和/或醇的第二产物级分; (f)将步骤(e)中获得的醇的第一和/或第二产物馏分的至少一部分再循环到步骤(a)。
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33.
公开(公告)号:US08889941B2
公开(公告)日:2014-11-18
申请号:US13727877
申请日:2012-12-27
Applicant: Shell Oil Company
Inventor: Leslie Andrew Chewter , Rajaram Ramesh , Jeroen Van Westrenen
CPC classification number: C07C1/22 , C07C1/20 , C07C7/08 , C07C41/06 , C07C2529/40 , C07C2529/70 , Y02P30/42 , C07C11/08 , C07C43/046 , C07C11/02
Abstract: The invention relates to a process for preparing lower olefins from an oxygenate, the process comprising subjecting C4 hydrocarbons obtained in an oxygenate-to-olefins conversion step to extractive distillation to obtain a stream enriched in unsaturated C4 hydrocarbons comprising isobutene and n-butenes, and a stream enriched in saturated C4 hydrocarbons; converting the isobutene in the stream enriched in unsaturated C4 hydrocarbons into an alkyl tertiary butyl ether to obtain an isobutene-depleted unsaturated C4 hydrocarbon stream and alkyl tertiary-butyl ether; and recycling at least part of the isobutene-depleted unsaturated C4 hydrocarbon stream and/or at least part of the alkyl tertiary-butyl ether, optionally after conversion into tertiary butanol and/or isobutene, to the oxygenate-to-olefins conversion step.
Abstract translation: 本发明涉及从含氧化合物制备低级烯烃的方法,该方法包括将在含氧化合物 - 烯烃转化步骤中获得的C4烃进行萃取蒸馏以获得富含不饱和C 4烃的物流,其包含异丁烯和正丁烯,以及 富含饱和C4烃的物流; 将富含不饱和C4烃的物流中的异丁烯转化为烷基叔丁基醚,得到异丁烯贫化的不饱和C 4烃物流和烷基叔丁基醚; 并且任选地在转化成叔丁醇和/或异丁烯之后将至少部分异丁烯贫化的不饱和C4烃流和/或至少部分烷基叔丁基醚再循环到含氧化合物 - 烯烃转化步骤中。
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