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公开(公告)号:US20110269997A1
公开(公告)日:2011-11-03
申请号:US13002078
申请日:2009-07-02
申请人: Irvin B. Cox , Thomas C. Eisenschmid , Ronald R. Peterson , Rainer Papp , Ludwig Herk , Anthony G. Abatjoglou
发明人: Irvin B. Cox , Thomas C. Eisenschmid , Ronald R. Peterson , Rainer Papp , Ludwig Herk , Anthony G. Abatjoglou
IPC分类号: C07C45/00
CPC分类号: C07C45/50 , C07C45/78 , Y02P20/584 , C07C47/02
摘要: A process of controlling heavies in a recycle catalyst stream, particularly, for use in a continuous hydroformylation process of converting an olefin with synthesis gas in the presence of a hydroformylation catalyst to form an aldehyde product stream with subsequent separation of the catalyst for recycle to the hydroformylation step. Heavies are controlled, and preferably reduced, by means of feeding a recycle gas stream, taken as a portion of an over-head stream from a condenser, back to a vaporizer wherein the aldehyde product stream is separated.
摘要翻译: 控制再循环催化剂流中重质的方法,特别是用于在加氢甲酰化催化剂存在下用合成气转化烯烃以形成醛产物流的连续加氢甲酰化方法,随后将催化剂分离以再循环至 加氢甲酰化步骤。 通过将循环气流(作为来自冷凝器的过头物流的一部分)返回到蒸发器(其中醛产物流被分离)进料来控制和优选地减少重量。
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公开(公告)号:US08404903B2
公开(公告)日:2013-03-26
申请号:US13002078
申请日:2009-07-02
申请人: Irvin B. Cox , Thomas C. Eisenschmid , Ronald R. Peterson , Rainer Papp , Ludwig Herk , Anthony G. Abatjoglou
发明人: Irvin B. Cox , Thomas C. Eisenschmid , Ronald R. Peterson , Rainer Papp , Ludwig Herk , Anthony G. Abatjoglou
IPC分类号: C07C45/50
CPC分类号: C07C45/50 , C07C45/78 , Y02P20/584 , C07C47/02
摘要: A process of controlling heavies in a recycle catalyst stream, particularly, for use in a continuous hydroformylation process of converting an olefin with synthesis gas in the presence of a hydroformylation catalyst to form an aldehyde product stream with subsequent separation of the catalyst for recycle to the hydroformylation step. Heavies are controlled, and preferably reduced, by means of feeding a recycle gas stream, taken as a portion of an over-head stream from a condenser, back to a vaporizer wherein the aldehyde product stream is separated.
摘要翻译: 控制再循环催化剂流中重质的方法,特别是用于在加氢甲酰化催化剂存在下用合成气转化烯烃以形成醛产物流的连续加氢甲酰化方法,随后将催化剂分离以再循环至 加氢甲酰化步骤。 通过将循环气流(作为来自冷凝器的过头物流的一部分)返回到蒸发器(其中醛产物流被分离)进料来控制和优选地减少重量。
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