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公开(公告)号:US08343433B2
公开(公告)日:2013-01-01
申请号:US12735028
申请日:2008-12-08
申请人: Fred A. Conneway , Harvey E. Andresen , Clarence P. Stadlwieser , Donald L. Kurle , Bernie B. Osborne
发明人: Fred A. Conneway , Harvey E. Andresen , Clarence P. Stadlwieser , Donald L. Kurle , Bernie B. Osborne
IPC分类号: F28D7/16 , C07D301/10
CPC分类号: B01J19/2425 , B01J8/008 , B01J8/067 , B01J19/002 , B01J2208/00176 , B01J2208/00212 , B01J2208/00256 , B01J2208/0053 , B01J2219/00085 , B01J2219/0009 , B01J2219/00103 , B01J2219/00159 , B01J2219/00763
摘要: Apparatus, methods, and processes are provided for a tube reactor including multiple, substantially parallel reaction tubes arranged within a tube reactor shell, the reaction tubes spaced apart such that a thermal fluid can flow between the tubes and transfer heat between the tubes and the thermal fluid during operation; an inlet head defining an inlet head space, where the inlet head space is in fluid communication with an inlet end of the reaction tubes, and an outlet head including an outlet head shell and at least one insert positioned within an outlet head space defined by the outlet head, where the insert defines a reduced volume outlet head space relative to that defined by the outlet head, and where the reduced volume outlet head space is in fluid communication with an outlet end of the reaction tubes and in fluid communication with a reactor outlet.
摘要翻译: 提供了一种用于管式反应器的装置,方法和方法,其包括布置在管式反应器壳体内的多个基本上平行的反应管,反应管间隔开,使得热流体可以在管之间流动并在管之间传递热量 运行过程中的液体; 入口头,其限定入口顶部空间,其中所述入口顶部空间与所述反应管的入口端流体连通;以及出口头,所述出口头包括出口头部外壳和位于由所述入口顶部空间限定的出口顶部空间内的至少一个插入件 出口头,其中插入件相对于由出口头限定的出口顶部空间限定了减小的体积出口顶部空间,并且其中减小体积的出口顶部空间与反应管的出口端流体连通并且与反应器出口流体连通 。
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公开(公告)号:US20110034709A1
公开(公告)日:2011-02-10
申请号:US12735028
申请日:2008-12-08
申请人: Fred A. Conneway , Harvey E. Andresen , Clarence P. Stadlwieser , Donald L. Kurle , Bernie B. Osborne
发明人: Fred A. Conneway , Harvey E. Andresen , Clarence P. Stadlwieser , Donald L. Kurle , Bernie B. Osborne
IPC分类号: C07D301/02 , B01J19/00
CPC分类号: B01J19/2425 , B01J8/008 , B01J8/067 , B01J19/002 , B01J2208/00176 , B01J2208/00212 , B01J2208/00256 , B01J2208/0053 , B01J2219/00085 , B01J2219/0009 , B01J2219/00103 , B01J2219/00159 , B01J2219/00763
摘要: Apparatus, methods, and processes are provided for a tube reactor including multiple, substantially parallel reaction tubes arranged within a tube reactor shell, the reaction tubes spaced apart such that a thermal fluid can flow between the tubes and transfer heat between the tubes and the thermal fluid during operation; an inlet head defining an inlet head space, where the inlet head space is in fluid communication with an inlet end of the reaction tubes, and an outlet head including an outlet head shell and at least one insert positioned within an outlet head space defined by the outlet head, where the insert defines a reduced volume outlet head space relative to that defined by the outlet head, and where the reduced volume outlet head space is in fluid communication with an outlet end of the reaction tubes and in fluid communication with a reactor outlet.
摘要翻译: 提供了一种用于管式反应器的装置,方法和方法,其包括布置在管式反应器壳体内的多个基本上平行的反应管,反应管间隔开,使得热流体可以在管之间流动并在管之间传递热量 运行过程中的液体; 入口头,其限定入口顶部空间,其中所述入口顶部空间与所述反应管的入口端流体连通;以及出口头,所述出口头包括出口头部外壳和位于由所述入口顶部空间限定的出口顶部空间内的至少一个插入件 出口头,其中插入件相对于由出口头限定的出口顶部空间限定了减小的体积出口顶部空间,并且其中减小体积的出口顶部空间与反应管的出口端流体连通并且与反应器出口流体连通 。
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公开(公告)号:US20100063306A1
公开(公告)日:2010-03-11
申请号:US12460775
申请日:2009-07-24
IPC分类号: C07D301/32 , B01D3/14
CPC分类号: C07D301/32
摘要: Systems and processes for recovering alkylene oxide, including an alkylene oxide recovery column including a stripping section located in the column to convert a portion of a feed stream to a gas phase including alkylene oxide; a reabsorption section in the column above the stripping section including a water stream to reabsorb the alkylene oxide in the gas phase portion and to produce an aqueous solution, a first stripping gas to strip carbon dioxide and oxygen from the aqueous solution by converting a portion of the aqueous solution to a gaseous portion, producing an alkylene oxide stream, and a side take-off located at a bottom portion of the reabsorption section for removal of the alkylene oxide stream; a condenser to partially condense the gas phase portion; and a top take-off for removal of a light impurity fraction.
摘要翻译: 用于回收烯化氧的系统和方法,包括烯化氧回收塔,其包括位于塔中的汽提部分,以将一部分进料流转化为包含环氧烷的气相; 在汽提部分上方的塔中的再吸收部分包括水流,以重新吸收气相部分中的环氧烷并产生水溶液;第一汽提气体,从水溶液中分离二氧化碳和氧气,通过将一部分 所述水溶液形成气态部分,产生烯化氧物流,以及位于所述再吸收部分的底部以除去所述环氧烷物流的侧向排出物; 冷凝器,部分冷凝气相部分; 以及去除轻杂质馏分的顶部起飞。
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公开(公告)号:US08053586B2
公开(公告)日:2011-11-08
申请号:US12460775
申请日:2009-07-24
IPC分类号: C07D301/32 , B01D3/38 , B01D3/34
CPC分类号: C07D301/32
摘要: Systems and processes for recovering alkylene oxide, including an alkylene oxide recovery column including a stripping section located in the column to convert a portion of a feed stream to a gas phase including alkylene oxide; a reabsorption section in the column above the stripping section including a water stream to reabsorb the alkylene oxide in the gas phase portion and to produce an aqueous solution, a first stripping gas to strip carbon dioxide and oxygen from the aqueous solution by converting a portion of the aqueous solution to a gaseous portion, producing an alkylene oxide stream, and a side take-off located at a bottom portion of the reabsorption section for removal of the alkylene oxide stream; a condenser to partially condense the gas phase portion; and a top take-off for removal of a light impurity fraction.
摘要翻译: 用于回收烯化氧的系统和方法,包括烯化氧回收塔,其包括位于塔中的汽提部分,以将一部分进料流转化为包含环氧烷的气相; 在汽提部分上方的塔中的再吸收部分包括水流,以重新吸收气相部分中的环氧烷并产生水溶液;第一汽提气体,从水溶液中分离二氧化碳和氧气,通过将一部分 所述水溶液形成气态部分,产生烯化氧物流,以及位于所述再吸收部分的底部以除去所述环氧烷物流的侧向排出物; 冷凝器,部分冷凝气相部分; 以及去除轻杂质馏分的顶部起飞。
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公开(公告)号:US08845863B2
公开(公告)日:2014-09-30
申请号:US12460752
申请日:2009-07-24
申请人: Clarence P. Stadlwieser , Bernie B. Osborne , John P. Dever , Harvey E. Andresen , Michael L. Hutchison , Steven R. Osborne , Liping L. Zhang , Michael Habenschuss , Andrew Addie , Donald R. Culp
发明人: Clarence P. Stadlwieser , Bernie B. Osborne , John P. Dever , Harvey E. Andresen , Michael L. Hutchison , Gary L. Culp , Steven R. Osborne , Liping L. Zhang , Michael Habenschuss , Andrew Addie
IPC分类号: B01D3/00 , B01D3/14 , C07D301/32 , C07D303/00 , C07C43/00 , C07C31/18
CPC分类号: C07D301/32
摘要: Processes and systems for purifying ethylene oxide, including introducing a feed stream including ethylene oxide to a heat exchanger to heat the feed stream, feeding the heated feed stream to a distillation apparatus base below a first stage, removing from the distillation apparatus an impurity fraction as a top exit stream from the distillation apparatus located at a top take-off on the distillation apparatus, removing from the distillation apparatus an ethylene oxide stream of 99.7 weight percent purity, based on the total weight of the ethylene oxide stream, from the distillation apparatus, and removing from the distillation apparatus an aldehyde enriched fraction as a bottom stream from the distillation apparatus, where the aldehyde enriched fraction is fed directly to a glycol reactor.
摘要翻译: 用于纯化环氧乙烷的方法和系统,包括将包含环氧乙烷的进料流引入热交换器以加热进料流,将加热的进料流输送到第一阶段以下的蒸馏装置底部,从蒸馏装置中除去杂质馏分如 来自位于蒸馏装置的顶部排出口的蒸馏装置的顶部出口物流,从蒸馏装置除去基于环氧乙烷料流的总重量为99.7重量%的纯度的环氧乙烷物流,来自蒸馏装置 ,并从蒸馏装置中将来自蒸馏装置的作为底部物流的富含醛的馏分除去,其中富含醛的馏分直接进料到二醇反应器中。
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公开(公告)号:US20100036170A1
公开(公告)日:2010-02-11
申请号:US12460752
申请日:2009-07-24
申请人: Clarence P. Stadlwieser , Bernie B. Osborne , John P. Dever , Harvey E. Andresen , Michael L. Hutchision , Gary L. Culp , Donald Culp , Stephen R. Osborne , Liping Zhang , Michael Habenschuss , Andrew Addie
发明人: Clarence P. Stadlwieser , Bernie B. Osborne , John P. Dever , Harvey E. Andresen , Michael L. Hutchision , Gary L. Culp , Donald Culp , Stephen R. Osborne , Liping Zhang , Michael Habenschuss , Andrew Addie
CPC分类号: C07D301/32
摘要: Processes and systems for purifying ethylene oxide, including introducing a feed stream including ethylene oxide to a heat exchanger to heat the feed stream, feeding the heated feed stream to a distillation apparatus base below a first stage, removing from the distillation apparatus an impurity fraction as a top exit stream from the distillation apparatus located at a top take-off on the distillation apparatus, removing from the distillation apparatus an ethylene oxide stream of 99.7 weight percent purity, based on the total weight of the ethylene oxide stream, from the distillation apparatus, and removing from the distillation apparatus an aldehyde enriched fraction as a bottom stream from the distillation apparatus, where the aldehyde enriched fraction is fed directly to a glycol reactor.
摘要翻译: 用于纯化环氧乙烷的方法和系统,包括将包含环氧乙烷的进料流引入热交换器以加热进料流,将加热的进料流输送到第一阶段以下的蒸馏装置底部,从蒸馏装置中除去杂质馏分如 来自位于蒸馏装置的顶部排出口的蒸馏装置的顶部出口物流,从蒸馏装置除去基于环氧乙烷料流的总重量为99.7重量%的纯度的环氧乙烷物流,来自蒸馏装置 ,并从蒸馏装置中将来自蒸馏装置的作为底部物流的富含醛的馏分除去,其中富含醛的馏分直接进料到二醇反应器中。
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