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公开(公告)号:US08361311B2
公开(公告)日:2013-01-29
申请号:US12833485
申请日:2010-07-09
申请人: S. Mark Davis , Larry Lee Iaccino , Richard C. Stell , Steven E. Silverberg , Jiunn-Shyan Liou , Howard Freund
发明人: S. Mark Davis , Larry Lee Iaccino , Richard C. Stell , Steven E. Silverberg , Jiunn-Shyan Liou , Howard Freund
IPC分类号: C10G9/28
CPC分类号: B01J19/0053 , C10B55/10 , C10B57/04 , C10B57/06 , C10G9/36 , C10G11/18 , C10G2300/1077 , C10G2300/203 , C10G2300/206 , C10G2300/301 , C10G2300/4006 , C10G2300/807 , C10G2400/20 , C10J3/463 , C10J3/482 , C10J2300/0943 , C10J2300/0956 , C10J2300/0973
摘要: A process and apparatus for cracking a hydrocarbon feed containing resid, comprising: heating a hydrocarbon feedstock containing resid; passing said heated hydrocarbon feedstock to a vapor/liquid separator; flashing said heated hydrocarbon feedstock in said vapor/liquid separator to form a vapor phase and a liquid phase containing said resid; passing at least a portion of said resid-containing liquid phase from said vapor/liquid separator to a thermal conversion reactor operating at 649° C. or more, wherein the thermal conversion reactor contains coke particles; and converting at least a portion of said resid into olefins.
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公开(公告)号:US20130156656A1
公开(公告)日:2013-06-20
申请号:US13768640
申请日:2013-02-15
申请人: S. Mark Davis , Richard C. Stell , Jiunn-Shyan Liou , Stephen H. Brown , Paul F. Keusenkothen , Arthur R. Dinicolantonio , John J. Waldrop
发明人: S. Mark Davis , Richard C. Stell , Jiunn-Shyan Liou , Stephen H. Brown , Paul F. Keusenkothen , Arthur R. Dinicolantonio , John J. Waldrop
IPC分类号: B01J10/00
CPC分类号: B01J10/005 , C10B55/00 , C10B55/10 , C10G9/005 , C10G9/007 , C10G9/36 , C10G51/023 , C10G2300/1077 , C10G2300/301 , C10G2300/4006 , C10G2300/807 , C10G2400/20 , C10G2400/30
摘要: This invention relates to a process and system for cracking hydrocarbon feedstock containing vacuum resid comprising: (a) subjecting a vacuum resid to a first thermal conversion in a thermal conversion reactor (such as delayed coker, fluid coker, Flexicoker™, visbreaker and catalytic hydrovisbreaker) where at least 30 wt % of the vacuum resid is converted to material boiling below 1050° F. (566° C.); (b) introducing said thermally converted resid to a vapor/liquid separator, said separator being integrated into a steam cracking furnace, to form a vapor phase and liquid phase; (c) passing said vapor phase to the radiant furnace in said steam cracking furnace; and (d) recovering at least 30 wt % olefins from the material exiting the radiant furnace (based upon the weight of the total hydrocarbon material exiting the radiant furnace).
摘要翻译: 本发明涉及一种用于裂化含有真空渣油的烃原料的方法和系统,该方法和系统包括:(a)在热转化反应器(例如延迟焦化器,流体焦化器,Flexicoker TM,减粘裂化器和 催化脱硫剂),其中至少30重量%的真空渣油转化成沸点低于1050°F(566℃)的材料; (b)将所述热转化残渣引入蒸汽/液体分离器,所述分离器整合成蒸汽裂解炉,形成气相和液相; (c)将所述气相通过所述蒸汽裂解炉中的辐射炉; 和(d)从离开辐射炉的材料(基于离开辐射炉的总烃材料的重量)回收至少30重量%的烯烃。
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公开(公告)号:US09056297B2
公开(公告)日:2015-06-16
申请号:US13723591
申请日:2012-12-21
申请人: S. Mark Davis , Larry L. Iaccino , Richard C. Stell , Steven E. Silverberg , Jiunn-Shyan Liou , Howard Freund
发明人: S. Mark Davis , Larry L. Iaccino , Richard C. Stell , Steven E. Silverberg , Jiunn-Shyan Liou , Howard Freund
IPC分类号: B01J19/00 , C10B55/10 , C10B57/04 , C10B57/06 , C10G11/18 , C10J3/48 , B01J19/24 , B01J8/18 , C10G9/34 , C10G9/36 , C10J3/46
CPC分类号: B01J19/0053 , C10B55/10 , C10B57/04 , C10B57/06 , C10G9/36 , C10G11/18 , C10G2300/1077 , C10G2300/203 , C10G2300/206 , C10G2300/301 , C10G2300/4006 , C10G2300/807 , C10G2400/20 , C10J3/463 , C10J3/482 , C10J2300/0943 , C10J2300/0956 , C10J2300/0973
摘要: A process and apparatus for cracking a hydrocarbon feed containing resid, comprising: heating a hydrocarbon feedstock containing resid; passing said heated hydrocarbon feedstock to a vapor/liquid separator; flashing said heated hydrocarbon feedstock in said vapor/liquid separator to form a vapor phase and a liquid phase containing said resid; passing at least a portion of said resid-containing liquid phase from said vapor/liquid separator to a thermal conversion reactor operating at 649° C. or more, wherein the thermal conversion reactor contains coke particles; and converting at least a portion of said resid into olefins.
摘要翻译: 一种用于裂化含有渣油的烃进料的方法和装置,包括:加热含有残渣的烃原料; 将所述加热的烃原料通入气/液分离器; 在所述气/液分离器中闪蒸所述加热的烃原料以形成含有所述残渣的气相和液相; 将来自所述蒸汽/液体分离器的至少一部分所述残留液体相转移到在649℃或更高温度下操作的热转化反应器,其中所述热转化反应器含有焦炭颗粒; 以及将所述残留物的至少一部分转化为烯烃。
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公开(公告)号:US20130115143A1
公开(公告)日:2013-05-09
申请号:US13723591
申请日:2012-12-21
申请人: S. Mark DAVIS , Larry L. IACCINO , Richard C. STEEL , Steven E. SILVERBERG , Jiunn-Shyan LIOU , Howard FREUND
发明人: S. Mark DAVIS , Larry L. IACCINO , Richard C. STEEL , Steven E. SILVERBERG , Jiunn-Shyan LIOU , Howard FREUND
IPC分类号: B01J19/00
CPC分类号: B01J19/0053 , C10B55/10 , C10B57/04 , C10B57/06 , C10G9/36 , C10G11/18 , C10G2300/1077 , C10G2300/203 , C10G2300/206 , C10G2300/301 , C10G2300/4006 , C10G2300/807 , C10G2400/20 , C10J3/463 , C10J3/482 , C10J2300/0943 , C10J2300/0956 , C10J2300/0973
摘要: A process and apparatus for cracking a hydrocarbon feed containing resid, comprising: heating a hydrocarbon feedstock containing resid; passing said heated hydrocarbon feedstock to a vapor/liquid separator; flashing said heated hydrocarbon feedstock in said vapor/liquid separator to form a vapor phase and a liquid phase containing said resid; passing at least a portion of said resid-containing liquid phase from said vapor/liquid separator to a thermal conversion reactor operating at 649° C. or more, wherein the thermal conversion reactor contains coke particles; and converting at least a portion of said resid into olefins.
摘要翻译: 一种用于裂化含有渣油的烃进料的方法和装置,包括:加热含有残渣的烃原料; 将所述加热的烃原料通入气/液分离器; 在所述气/液分离器中闪蒸所述加热的烃原料以形成含有所述残渣的气相和液相; 将来自所述蒸汽/液体分离器的至少一部分所述残留液体相转移到在649℃或更高温度下操作的热转化反应器,其中所述热转化反应器含有焦炭颗粒; 以及将所述残留物的至少一部分转化为烯烃。
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公开(公告)号:US08399729B2
公开(公告)日:2013-03-19
申请号:US12833556
申请日:2010-07-09
申请人: S. Mark Davis , Richard C. Stell , Jiunn-Shyan Liou , Stephen H. Brown , Paul F. Keusenkothen , Arthur R. DiNicolantonio , John J. Waldrop
发明人: S. Mark Davis , Richard C. Stell , Jiunn-Shyan Liou , Stephen H. Brown , Paul F. Keusenkothen , Arthur R. DiNicolantonio , John J. Waldrop
IPC分类号: C07C4/04
CPC分类号: B01J10/005 , C10B55/00 , C10B55/10 , C10G9/005 , C10G9/007 , C10G9/36 , C10G51/023 , C10G2300/1077 , C10G2300/301 , C10G2300/4006 , C10G2300/807 , C10G2400/20 , C10G2400/30
摘要: This invention relates to a process and system for cracking hydrocarbon feedstock containing vacuum resid comprising: (a) subjecting a vacuum resid to a first thermal conversion in a thermal conversion reactor (such as delayed coker, fluid coker, Flexicoker™, visbreaker and catalytic hydrovisbreaker) where at least 30 wt % of the vacuum resid is converted to material boiling below 1050° F. (566° C.); (b) introducing said thermally converted resid to a vapor/liquid separator, said separator being integrated into a steam cracking furnace, to form a vapor phase and liquid phase; (c) passing said vapor phase to the radiant furnace in said steam cracking furnace; and (d) recovering at least 30 wt % olefins from the material exiting the radiant furnace (based upon the weight of the total hydrocarbon material exiting the radiant furnace).
摘要翻译: 本发明涉及一种用于裂化含有真空渣油的烃原料的方法和系统,该方法和系统包括:(a)在热转化反应器(例如延迟焦化器,流体焦化器,Flexicoker TM,减粘裂化器和催化脱硫剂)中对真空渣油进行第一热转化 ),其中至少30重量%的真空渣油转化成沸点低于1050°F(566℃)的材料; (b)将所述热转化残渣引入蒸汽/液体分离器,所述分离器整合成蒸汽裂解炉,形成气相和液相; (c)将所述气相通过所述蒸汽裂解炉中的辐射炉; 和(d)从离开辐射炉的材料(基于离开辐射炉的总烃材料的重量)回收至少30重量%的烯烃。
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公开(公告)号:US20120006722A1
公开(公告)日:2012-01-12
申请号:US12833485
申请日:2010-07-09
申请人: S. Mark Davis , Larry Lee Iaccino , Richard C. Stell , Steven E. Silverberg , Jiunn-Shyan Liou , Howard Freund
发明人: S. Mark Davis , Larry Lee Iaccino , Richard C. Stell , Steven E. Silverberg , Jiunn-Shyan Liou , Howard Freund
CPC分类号: B01J19/0053 , C10B55/10 , C10B57/04 , C10B57/06 , C10G9/36 , C10G11/18 , C10G2300/1077 , C10G2300/203 , C10G2300/206 , C10G2300/301 , C10G2300/4006 , C10G2300/807 , C10G2400/20 , C10J3/463 , C10J3/482 , C10J2300/0943 , C10J2300/0956 , C10J2300/0973
摘要: A process and apparatus for cracking a hydrocarbon feed containing resid, comprising: heating a hydrocarbon feedstock containing resid; passing said heated hydrocarbon feedstock to a vapor/liquid separator; flashing said heated hydrocarbon feedstock in said vapor/liquid separator to form a vapor phase and a liquid phase containing said resid; passing at least a portion of said resid-containing liquid phase from said vapor/liquid separator to a thermal conversion reactor operating at 649° C. or more, wherein the thermal conversion reactor contains coke particles; and converting at least a portion of said resid into olefins.
摘要翻译: 一种用于裂化含有渣油的烃进料的方法和装置,包括:加热含有残渣的烃原料; 将所述加热的烃原料通入气/液分离器; 在所述气/液分离器中闪蒸所述加热的烃原料以形成含有所述残渣的气相和液相; 将来自所述蒸汽/液体分离器的至少一部分所述残留液体相转移到在649℃或更高温度下操作的热转化反应器,其中所述热转化反应器含有焦炭颗粒; 以及将所述残留物的至少一部分转化为烯烃。
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公开(公告)号:US20120006723A1
公开(公告)日:2012-01-12
申请号:US12833556
申请日:2010-07-09
申请人: S. Mark Davis , Richard C. Stell , Jiunn-Shyan Liou , Stephen H. Brown , Paul F. Keusenkothen , Arthur R. Dinicolantonio , John J. Waldrop
发明人: S. Mark Davis , Richard C. Stell , Jiunn-Shyan Liou , Stephen H. Brown , Paul F. Keusenkothen , Arthur R. Dinicolantonio , John J. Waldrop
CPC分类号: B01J10/005 , C10B55/00 , C10B55/10 , C10G9/005 , C10G9/007 , C10G9/36 , C10G51/023 , C10G2300/1077 , C10G2300/301 , C10G2300/4006 , C10G2300/807 , C10G2400/20 , C10G2400/30
摘要: This invention relates to a process and system for cracking hydrocarbon feedstock containing vacuum resid comprising: (a) subjecting a vacuum resid to a first thermal conversion in a thermal conversion reactor (such as delayed coker, fluid coker, Flexicoker™, visbreaker and catalytic hydrovisbreaker) where at least 30 wt % of the vacuum resid is converted to material boiling below 1050° F. (566° C.); (b) introducing said thermally converted resid to a vapor/liquid separator, said separator being integrated into a steam cracking furnace, to form a vapor phase and liquid phase; (c) passing said vapor phase to the radiant furnace in said steam cracking furnace; and (d) recovering at least 30 wt % olefins from the material exiting the radiant furnace (based upon the weight of the total hydrocarbon material exiting the radiant furnace).
摘要翻译: 本发明涉及一种用于裂化含有真空渣油的烃原料的方法和系统,该方法和系统包括:(a)在热转化反应器(例如延迟焦化器,流体焦化器,Flexicoker TM,减粘裂化器和催化脱硫剂)中对真空渣油进行第一热转化 ),其中至少30重量%的真空渣油转化成沸点低于1050°F(566℃)的材料; (b)将所述热转化残渣引入蒸汽/液体分离器,所述分离器整合成蒸汽裂解炉,形成气相和液相; (c)将所述气相通过所述蒸汽裂解炉中的辐射炉; 和(d)从离开辐射炉的材料(基于离开辐射炉的总烃材料的重量)回收至少30重量%的烯烃。
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