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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: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: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:US08058367B2
公开(公告)日:2011-11-15
申请号:US12632490
申请日:2009-12-07
IPC分类号: C08F2/01 , C08F110/02 , B01J19/00
CPC分类号: C08F2/002 , B01J19/0006 , B01J19/002 , B01J19/1837 , B01J2208/00734 , B01J2219/00191 , B01J2219/00247 , B01J2219/00254 , C08F2/12 , C08F10/00 , C08F10/02 , C08F110/02 , C08F2400/02 , C08F2/14 , C08F2/00 , C08F2500/24
摘要: Techniques are provided for producing polymer particles of a size just slightly larger than the size of polymer fines. The technique may prevent or limit the occurrence of reactor fouls associated with large polymer particles. The technique also may provide a greater weight percentage of solids in the reactor. The desired polymer particle size may be achieved by employing a catalyst having particles of a size determined based on the expected catalyst productivity. In certain embodiments, the catalyst particle size may be determined based on the expected catalyst productivity, the polymer particle density, the catalyst particle density, and/or the polymer particle size.
摘要翻译: 提供了用于生产尺寸略大于聚合物细粒尺寸的聚合物颗粒的技术。 该技术可以防止或限制与大聚合物颗粒相关联的反应堆污染物的发生。 该技术还可以在反应器中提供更大的固体重量百分比。 所需的聚合物粒度可以通过使用具有基于预期的催化剂生产率确定的尺寸的颗粒的催化剂来实现。 在某些实施方案中,可以基于预期的催化剂生产率,聚合物颗粒密度,催化剂颗粒密度和/或聚合物粒度来确定催化剂粒度。
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公开(公告)号:US20130137836A1
公开(公告)日:2013-05-30
申请号:US13307053
申请日:2011-11-30
申请人: George R. Rajaendran , Max P. McDaniel , Gregory G. Hendrickson , John D. Stewart , John D. Hottovy , Ted H. Cymbaluk , Suzannah Lane , Richard A. Hernandez , Elliott W. Johnson , Qing Yang , William L. Valerioti , Eric Schwerdtfeger , Albert P. Masino
发明人: George R. Rajaendran , Max P. McDaniel , Gregory G. Hendrickson , John D. Stewart , John D. Hottovy , Ted H. Cymbaluk , Suzannah Lane , Richard A. Hernandez , Elliott W. Johnson , Qing Yang , William L. Valerioti , Eric Schwerdtfeger , Albert P. Masino
CPC分类号: C08F10/02 , C08F210/16 , C08F2/002 , C08F210/14 , C08F2500/07 , C08F2/14
摘要: Methods for removing polymer skins or build-up from reactor walls in polymerization reactor systems containing a loop slurry reactor are disclosed. Such methods can employ removing some or all of the comonomer from the reactor system in combination with increasing the polymerization temperature of the loop slurry reactor.
摘要翻译: 公开了在含有环状淤浆反应器的聚合反应器系统中从反应器壁上除去聚合物表面或积聚的方法。 这样的方法可以结合提高环浆反应器的聚合温度,从反应器系统中除去一些或全部共聚单体。
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公开(公告)号:US08187547B2
公开(公告)日:2012-05-29
申请号:US13252738
申请日:2011-10-04
IPC分类号: B01J19/18 , F27B15/00 , C08F2/00 , C08F4/00 , C08F210/00 , C08F110/02
CPC分类号: C08F2/002 , B01J19/0006 , B01J19/002 , B01J19/1837 , B01J2208/00734 , B01J2219/00191 , B01J2219/00247 , B01J2219/00254 , C08F2/12 , C08F10/00 , C08F10/02 , C08F110/02 , C08F2400/02 , C08F2/14 , C08F2/00 , C08F2500/24
摘要: Techniques are provided for producing polymer particles of a size just slightly larger than the size of polymer fines. The technique may prevent or limit the occurrence of reactor fouls associated with large polymer particles. The technique also may provide a greater weight percentage of solids in the reactor. The desired polymer particle size may be achieved by employing a catalyst having particles of a size determined based on the expected catalyst productivity. In certain embodiments, the catalyst particle size may be determined based on the expected catalyst productivity, the polymer particle density, the catalyst particle density, and/or the polymer particle size.
摘要翻译: 提供了用于生产尺寸略大于聚合物细粒尺寸的聚合物颗粒的技术。 该技术可以防止或限制与大聚合物颗粒相关联的反应堆污染物的发生。 该技术还可以在反应器中提供更大的固体重量百分比。 所需的聚合物粒度可以通过使用具有基于预期的催化剂生产率确定的尺寸的颗粒的催化剂来实现。 在某些实施方案中,可以基于预期的催化剂生产率,聚合物颗粒密度,催化剂颗粒密度和/或聚合物粒度来确定催化剂粒度。
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