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公开(公告)号:US07109290B2
公开(公告)日:2006-09-19
申请号:US11146616
申请日:2005-06-07
IPC分类号: C08F6/00
CPC分类号: B01J19/2435 , B01J8/0015 , B01J8/20 , B01J2208/00442 , B01J2208/00539 , B01J2208/00761
摘要: A method for transferring polymer within a polymerization system, comprising continuously withdrawing the polymer from the reactor and conveying the polymer from a reactor to a flash chamber via a pressure differential between the reactor and the flash chamber. A method for transferring polymer within a polymerization system comprising conveying the polymer from a reactor to a flash chamber via a pressure differential between the reactor and the flash chamber and purging interstitial gases from the polymer prior to conveying the polymer from the flash chamber to a purge column. A method for transferring polymer within a polymerization system comprising conveying the polymer from a flash chamber directly to a purge column via a pressure differential between the flash chamber and the purge column.
摘要翻译: 一种用于在聚合体系内转移聚合物的方法,包括从反应器连续地抽出聚合物并通过反应器和闪蒸室之间的压差将聚合物从反应器输送到闪蒸室。 一种用于在聚合系统内转移聚合物的方法,包括通过反应器和闪蒸室之间的压差将聚合物从反应器输送到闪蒸室,并在将聚合物从闪蒸室输送到吹扫之前从聚合物中清除间隙气体 柱。 一种用于在聚合体系内转移聚合物的方法,包括通过闪蒸室和净化塔之间的压差将聚合物从闪蒸室直接输送到吹扫塔。
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公开(公告)号:US07517947B2
公开(公告)日:2009-04-14
申请号:US11467284
申请日:2006-08-25
CPC分类号: B01J19/2435 , B01J8/0015 , B01J8/20 , B01J2208/00442 , B01J2208/00539 , B01J2208/00761
摘要: A method for transferring polymer within a polymerization system, comprising continuously withdrawing the polymer from the reactor and conveying the polymer from a reactor to a flash chamber via a pressure differential between the reactor and the flash chamber. A method for transferring polymer within a polymerization system comprising conveying the polymer from a reactor to a flash chamber via a pressure differential between the reactor and the flash chamber and purging interstitial gases from the polymer prior to conveying the polymer from the sash chamber to a purge column. A method for transferring polymer within a polymerization system comprising conveying the polymer from a flash chamber directly to a purge column via a pressure differential between the flash chamber and the purge column.
摘要翻译: 一种用于在聚合体系内转移聚合物的方法,包括从反应器连续地抽出聚合物并通过反应器和闪蒸室之间的压差将聚合物从反应器输送到闪蒸室。 一种用于在聚合体系内转移聚合物的方法,包括通过反应器和闪蒸室之间的压差将聚合物从反应器输送到闪蒸室,并在将聚合物从窗扇室输送到吹扫之前从聚合物中清除间隙气体 柱。 一种用于在聚合体系内转移聚合物的方法,包括通过闪蒸室和净化塔之间的压差将聚合物从闪蒸室直接输送到吹扫塔。
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公开(公告)号:US20120139149A1
公开(公告)日:2012-06-07
申请号:US13372979
申请日:2012-02-14
申请人: Robert R. McElvain , John D. Hottovy , Ralph W. Romig , Donald W. Verser , David H. Burns , John H. Tait , Richard Peacock , James E. Hein , Scott E. Kufeld , Carl W. Fenderson , Anurag Gupta , Dale A. Zellers , Penny A. Zellers
发明人: Robert R. McElvain , John D. Hottovy , Ralph W. Romig , Donald W. Verser , David H. Burns , John H. Tait , Richard Peacock , James E. Hein , Scott E. Kufeld , Carl W. Fenderson , Anurag Gupta , Dale A. Zellers , Penny A. Zellers
IPC分类号: B29B9/06
CPC分类号: B01J19/0013 , B01J8/0015 , B01J19/1837 , B01J19/2455 , B01J2208/00212 , B01J2208/00752 , B01J2219/00006 , B01J2219/0236 , C08F2/01 , C08F6/003 , C08F10/00 , C08F110/02 , C08L23/00 , C08F2/14
摘要: A manufacturing system for producing polyolefin includes a polymerization reactor, a flash chamber, and a purge column. In certain embodiments, the purge column may receive a solids stream directly from the flash chamber. Further, the purge column may function as a feed tank for an extruder within an extrusion/loadout system. According to certain embodiments, the manufacturing system may be configured to consume less than 445 kilowatt-hours of energy per metric ton of polyolefin produced based on consumption of electricity, steam, and fuel gas.
摘要翻译: 用于生产聚烯烃的制造系统包括聚合反应器,闪蒸室和吹扫塔。 在某些实施方案中,净化塔可以直接从闪蒸室接收固体物流。 此外,吹扫塔可用作挤出/挤出系统中的挤出机的进料罐。 根据某些实施例,制造系统可以被配置为消耗基于消耗电力,蒸汽和燃料气体的每公吨聚烯烃消耗少于445千瓦小时的能量。
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公开(公告)号:US08128877B2
公开(公告)日:2012-03-06
申请号:US13207262
申请日:2011-08-10
申请人: Robert R. McElvain , John D. Hottovy , Ralph W. Romig , Donald W. Verser , David H. Burns , John H. Tait , Richard Peacock , James E. Hein , Scott E. Kufeld , Carl W. Fenderson , Anurag Gupta , Dale A. Zellers , Penny A. Zellers, legal representative
发明人: Robert R. McElvain , John D. Hottovy , Ralph W. Romig , Donald W. Verser , David H. Burns , John H. Tait , Richard Peacock , James E. Hein , Scott E. Kufeld , Carl W. Fenderson , Anurag Gupta , Dale A. Zellers
IPC分类号: B01J10/00 , C08F2/00 , C08F210/00
CPC分类号: B01J19/0013 , B01J8/0015 , B01J19/1837 , B01J19/2455 , B01J2208/00212 , B01J2208/00752 , B01J2219/00006 , B01J2219/0236 , C08F2/01 , C08F6/003 , C08F10/00 , C08F110/02 , C08L23/00 , C08F2/14
摘要: A manufacturing process for producing polyolefin, having a feed system, a reactor system including at least one polymerization reactor, a diluent/monomer recovery system, a fractionation system, and an extrusion/loadout system having an extruder. The manufacturing process is configured to consume less than 325 kilowatt-hours of electricity per metric ton of polyolefin produced.
摘要翻译: 具有进料系统的聚烯烃的制造方法,包括至少一个聚合反应器的反应器系统,稀释剂/单体回收系统,分馏系统和具有挤出机的挤出/压出系统。 制造过程被配置为每公吨生产的聚烯烃消耗少于325千瓦小时的电力。
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公开(公告)号:US20110300025A1
公开(公告)日:2011-12-08
申请号:US13207262
申请日:2011-08-10
申请人: Robert R. McElvain , John D. Hottovy , Ralph W. Romig , Donald W. Verser , David H. Burns , John H. Tait , Richard Peacock , James E. Hein , Scott E. Kufeld , Carl W. Fenderson , Anurag Gupta , Dale A. Zellers , Penny A. Zellers
发明人: Robert R. McElvain , John D. Hottovy , Ralph W. Romig , Donald W. Verser , David H. Burns , John H. Tait , Richard Peacock , James E. Hein , Scott E. Kufeld , Carl W. Fenderson , Anurag Gupta , Dale A. Zellers , Penny A. Zellers
IPC分类号: B01J19/00
CPC分类号: B01J19/0013 , B01J8/0015 , B01J19/1837 , B01J19/2455 , B01J2208/00212 , B01J2208/00752 , B01J2219/00006 , B01J2219/0236 , C08F2/01 , C08F6/003 , C08F10/00 , C08F110/02 , C08L23/00 , C08F2/14
摘要: A manufacturing process for producing polyolefin, having a feed system, a reactor system including at least one polymerization reactor, a diluent/monomer recovery system, a fractionation system, and an extrusion/loadout system having an extruder. The manufacturing process is configured to consume less than 325 kilowatt-hours of electricity per metric ton of polyolefin produced.
摘要翻译: 具有进料系统的聚烯烃的制造方法,包括至少一个聚合反应器的反应器系统,稀释剂/单体回收系统,分馏系统和具有挤出机的挤出/压出系统。 制造过程被配置为每公吨生产的聚烯烃消耗少于325千瓦小时的电力。
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公开(公告)号:US08303899B2
公开(公告)日:2012-11-06
申请号:US13372979
申请日:2012-02-14
申请人: Robert R. McElvain , John D. Hottovy , Ralph W. Romig , Donald W. Verser , David H. Burns , John H. Tait , Richard Peacock , James E. Hein , Scott E. Kufeld , Carl W. Fenderson , Anurag Gupta , Dale A. Zellers , Penny A. Zellers, legal representative
发明人: Robert R. McElvain , John D. Hottovy , Ralph W. Romig , Donald W. Verser , David H. Burns , John H. Tait , Richard Peacock , James E. Hein , Scott E. Kufeld , Carl W. Fenderson , Anurag Gupta , Dale A. Zellers
CPC分类号: B01J19/0013 , B01J8/0015 , B01J19/1837 , B01J19/2455 , B01J2208/00212 , B01J2208/00752 , B01J2219/00006 , B01J2219/0236 , C08F2/01 , C08F6/003 , C08F10/00 , C08F110/02 , C08L23/00 , C08F2/14
摘要: A manufacturing system for producing polyolefin includes a polymerization reactor, a flash chamber, and a purge column. In certain embodiments, the purge column may receive a solids stream directly from the flash chamber. Further, the purge column may function as a feed tank for an extruder within an extrusion/loadout system. According to certain embodiments, the manufacturing system may be configured to consume less than 445 kilowatt-hours of energy per metric ton of polyolefin produced based on consumption of electricity, steam, and fuel gas.
摘要翻译: 用于生产聚烯烃的制造系统包括聚合反应器,闪蒸室和吹扫塔。 在某些实施方案中,净化塔可以直接从闪蒸室接收固体物流。 此外,吹扫塔可用作挤出/挤出系统中的挤出机的进料罐。 根据某些实施例,制造系统可以被配置为消耗基于消耗电力,蒸汽和燃料气体的每公吨聚烯烃消耗少于445千瓦小时的能量。
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公开(公告)号:US08017701B2
公开(公告)日:2011-09-13
申请号:US11213374
申请日:2005-08-26
申请人: Robert R. McElvain , John D. Hottovy , Ralph W. Romig , Donald W. Verser , David H. Burns , John H. Tait , Richard Peacock , James E. Hein , Scott E. Kufeld , Carl W. Fenderson , Anurag Gupta , Dale A. Zellers , Penny A. Zellers, legal representative
发明人: Robert R. McElvain , John D. Hottovy , Ralph W. Romig , Donald W. Verser , David H. Burns , John H. Tait , Richard Peacock , James E. Hein , Scott E. Kufeld , Carl W. Fenderson , Anurag Gupta , Dale A. Zellers
IPC分类号: C08F2/00 , C08F210/00
CPC分类号: B01J19/0013 , B01J8/0015 , B01J19/1837 , B01J19/2455 , B01J2208/00212 , B01J2208/00752 , B01J2219/00006 , B01J2219/0236 , C08F2/01 , C08F6/003 , C08F10/00 , C08F110/02 , C08L23/00 , C08F2/14
摘要: A manufacturing process for producing polyolefin, having a feed system, a reactor system including at least one polymerization reactor, a diluent/monomer recovery system, a fractionation system, and an extrusion/loadout system having an extruder. The manufacturing process is configured to consume less than 325 kilowatt-hours of electricity per metric ton of polyolefin produced.
摘要翻译: 具有进料系统的聚烯烃的制造方法,包括至少一个聚合反应器的反应器系统,稀释剂/单体回收系统,分馏系统和具有挤出机的挤出/压出系统。 制造过程被配置为每公吨生产的聚烯烃消耗少于325千瓦小时的电力。
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公开(公告)号:US07999044B2
公开(公告)日:2011-08-16
申请号:US12204566
申请日:2008-09-04
CPC分类号: B01J4/008 , B01J19/1837 , B01J2204/005 , B01J2219/00094 , B01J2219/00159 , C08F10/00 , C08F2/14 , C08F2/01
摘要: A flash chamber sized to receive the effluent discharged from a polyolefin reactor during normal operation of the reactor and during a reactor dump, advantageously eliminating a reactor dump tank or alternate flash tank from the equipment outlay of a polyolefin manufacturing process. The flash chamber is sized to hold at least the polyolefin solids discharged from the reactor. A condenser fluidically coupled to an overhead portion of the flash chamber is sized to condense the flow rate of vaporized hydrocarbon (e.g., diluent, monomer, etc.) discharged overhead from the flash chamber during normal operation and during the reactor dump.
摘要翻译: 闪蒸室的尺寸适于接收在反应堆的正常操作期间和反应器堆放期间从聚烯烃反应器排出的流出物,有利地从聚烯烃制造过程的设备消耗中消除反应堆倾倒罐或替代闪蒸罐。 闪蒸室的尺寸至少保持从反应器排出的聚烯烃固体。 流体耦合到闪蒸室的顶部部分的冷凝器的尺寸被设定为在正常操作期间和在反应堆堆放期间冷凝从闪蒸室排出的汽化烃(例如稀释剂,单体等)的流速。
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公开(公告)号:US20100056707A1
公开(公告)日:2010-03-04
申请号:US12204566
申请日:2008-09-04
CPC分类号: B01J4/008 , B01J19/1837 , B01J2204/005 , B01J2219/00094 , B01J2219/00159 , C08F10/00 , C08F2/14 , C08F2/01
摘要: A flash chamber sized to receive the effluent discharged from a polyolefin reactor during normal operation of the reactor and during a reactor dump, advantageously eliminating a reactor dump tank or alternate flash tank from the equipment outlay of a polyolefin manufacturing process. The flash chamber is sized to hold at least the polyolefin solids discharged from the reactor. A condenser fluidically coupled to an overhead portion of the flash chamber is sized to condense the flow rate of vaporized hydrocarbon (e.g., diluent, monomer, etc.) discharged overhead from the flash chamber during normal operation and during the reactor dump.
摘要翻译: 闪蒸室的尺寸适于接收在反应堆的正常操作期间和反应器堆放期间从聚烯烃反应器排出的流出物,有利地从聚烯烃制造过程的设备消耗中消除反应堆倾倒罐或替代闪蒸罐。 闪蒸室的尺寸至少保持从反应器排出的聚烯烃固体。 流体耦合到闪蒸室的顶部部分的冷凝器的尺寸被设定为在正常操作期间和在反应堆堆放期间冷凝从闪蒸室排出的汽化烃(例如稀释剂,单体等)的流速。
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10.
公开(公告)号:US07033545B2
公开(公告)日:2006-04-25
申请号:US10251662
申请日:2002-09-20
申请人: Scott E. Kufeld , Thomas A. Reid , John H. Tait , David H. Burns , Donald W. Verser , Harvey D. Hensley , David J. Przelomski , Teddy H. Cymbaluk , Robert K. Franklin , Ethelwoldo P. Perez , John D. Hottovy
发明人: Scott E. Kufeld , Thomas A. Reid , John H. Tait , David H. Burns , Donald W. Verser , Harvey D. Hensley , David J. Przelomski , Teddy H. Cymbaluk , Robert K. Franklin , Ethelwoldo P. Perez , John D. Hottovy
CPC分类号: B01J19/1837 , B01J8/003 , B01J8/008 , C08F10/00 , C08F210/16 , C08F2/01 , C08F2/14 , C08F210/14
摘要: A polymerization loop reactor including a loop reaction zone, a continuous takeoff, and a fluid slurry disposed in the reaction zone. A generally cylindrical wall defines the loop reaction zone. The length of the loop reaction zone and the nominal outside diameter of the generally cylindrical wall define a length/diameter ratio greater than 250. The reactor can be charged with a fluid slurry including an olefin monomer reactant, solid olefin polymer particles, and a liquid diluent. The concentration of the solid olefin polymer particles in the slurry can be greater than 40 weight percent based on the weight of polymer particles and the weight of liquid diluent. Also disclosed is a polymerization process carried out by polymerizing, in the loop reaction zone of a reactor as defined above, at least one olefin monomer in a liquid diluent to produce a fluid slurry as defined above.
摘要翻译: 一种包括环路反应区,连续起飞和设置在反应区中的流体淤浆的聚合反应器反应器。 大致圆柱形的壁限定了环路反应区域。 环路反应区的长度和大致圆柱形壁的标称外径确定了大于250的长度/直径比。反应器可以装有包含烯烃单体反应物,固体烯烃聚合物颗粒和液体的流体浆料 冲淡。 基于聚合物颗粒的重量和液体稀释剂的重量,浆料中固体烯烃聚合物颗粒的浓度可以大于40重量%。 还公开了聚合方法,其通过在液体稀释剂中的至少一种烯烃单体在如上定义的反应器的环路反应区域中聚合以产生如上所定义的流体浆料而进行。
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