-
公开(公告)号：US09221920B2
公开(公告)日：2015-12-29
申请号：US14286624
申请日：2014-05-23
Applicant: Chevron Phillips Chemical Company LP
Inventor： 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: C08F2/00 , C08G85/00 , G05D23/00 , B01J19/00 , B01J19/18 , C08F2/01 , B01J8/00 , C08F6/00 , C08F10/00 , C08F110/02
CPC classification number: 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
Abstract: 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.
Abstract translation: 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。
-
公开(公告)号：US09610558B2
公开(公告)日：2017-04-04
申请号：US14975423
申请日：2015-12-18
Applicant: Chevron Phillips Chemical Company LP
Inventor： 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: C08F210/00 , B01J19/18 , B01J19/00 , B01J8/00 , C08F6/00 , C08F10/00 , C08F2/01 , B01J19/24 , C08F110/02
CPC classification number: 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
Abstract: 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.
-
公开(公告)号：US20140256889A1
公开(公告)日：2014-09-11
申请号：US14286624
申请日：2014-05-23
Applicant: Chevron Phillips Chemical Company LP
Inventor： 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: C08F2/01
CPC classification number: 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
Abstract: 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.
-
4.发明申请公开(公告)号：US20140194583A1
公开(公告)日：2014-07-10
申请号：US14203842
申请日：2014-03-11
Applicant: Chevron Phillips Chemical Company LP
Inventor： John D. Hottovy , Richard Peacock
CPC classification number: C08L23/06 , B01J19/0006 , B01J19/002 , B01J19/1837 , B01J19/2455 , B01J2219/00162 , B01J2219/0027 , B01J2219/24 , C08F2/01 , C08F10/00 , C08F210/16 , C08F2/14 , C08F210/14
Abstract: A reactor system including an enclosed pressure relief system and/or a control system. The enclosed pressure relief system including a slurry separation system communicatively coupled with a pressure relief valve coupled to a loop reactor such that activation of the pressure relief valve results in discharge of a slurry from the loop reactor to the slurry separation system, wherein the slurry separation system is capable of separating solid and liquid components from gas components of the slurry and transmitting the gas components to a flare via a flare header.
Abstract translation: 包括封闭的压力释放系统和/或控制系统的反应堆系统。 封闭的压力释放系统包括浆料分离系统，其与连接到回路反应器的压力释放阀通信地联接，使得压力释放阀的激活导致浆料从环管反应器排放到浆料分离系统，其中浆料分离 系统能够将固体和液体组分与浆料的气体组分分离，并通过火炬头将气体组分传输到耀斑。
-
公开(公告)号：US20140024788A1
公开(公告)日：2014-01-23
申请号：US14033405
申请日：2013-09-20
Applicant: Chevron Phillips Chemical Company LP
Inventor： 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: C08F2/01
CPC classification number: 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
Abstract: 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.
Abstract translation: 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。
-
Patent Agency Ranking
公开(公告)号：US08569433B2
公开(公告)日：2013-10-29
申请号：US13656357
申请日：2012-10-19
Applicant: Chevron Phillips Chemical Company LP , Penny A. Zellers
Inventor： 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: C08F2/00 , C08F4/00 , C08F210/00 , B01J10/00
CPC classification number: 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
Abstract: 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.
-
公开(公告)号：US09718948B2
公开(公告)日：2017-08-01
申请号：US14737020
申请日：2015-06-11
Applicant: Chevron Phillips Chemical Company LP
Inventor： John D. Hottovy , Richard Peacock
CPC classification number: C08L23/06 , B01J19/0006 , B01J19/002 , B01J19/1837 , B01J19/2455 , B01J2219/00162 , B01J2219/0027 , B01J2219/24 , C08F2/01 , C08F10/00 , C08F210/16 , C08F2/14 , C08F210/14
Abstract: A reactor system including an enclosed pressure relief system and/or a control system. The enclosed pressure relief system including a slurry separation system communicatively coupled with a pressure relief valve coupled to a loop reactor such that activation of the pressure relief valve results in discharge of a slurry from the loop reactor to the slurry separation system, wherein the slurry separation system is capable of separating solid and liquid components from gas components of the slurry and transmitting the gas components to a flare via a flare header.
-
公开(公告)号：US08765884B2
公开(公告)日：2014-07-01
申请号：US14033405
申请日：2013-09-20
Applicant: Chevron Phillips Chemical Company LP
Inventor： 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: C08F2/00 , C08F210/00 , C08F110/02 , F01N3/20 , B01J19/00 , B01J19/18
CPC classification number: 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
Abstract: 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.
Abstract translation: 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。
-
9.发明授权公开(公告)号：US09447264B2
公开(公告)日：2016-09-20
申请号：US14203842
申请日：2014-03-11
Applicant: Chevron Phillips Chemical Company LP
Inventor： John D. Hottovy , Richard Peacock
CPC classification number: C08L23/06 , B01J19/0006 , B01J19/002 , B01J19/1837 , B01J19/2455 , B01J2219/00162 , B01J2219/0027 , B01J2219/24 , C08F2/01 , C08F10/00 , C08F210/16 , C08F2/14 , C08F210/14
Abstract: A reactor system including an enclosed pressure relief system and/or a control system. The enclosed pressure relief system including a slurry separation system communicatively coupled with a pressure relief valve coupled to a loop reactor such that activation of the pressure relief valve results in discharge of a slurry from the loop reactor to the slurry separation system, wherein the slurry separation system is capable of separating solid and liquid components from gas components of the slurry and transmitting the gas components to a flare via a flare header.
Abstract translation: 包括封闭的压力释放系统和/或控制系统的反应堆系统。 封闭的压力释放系统包括浆料分离系统，其与连接到回路反应器的压力释放阀通信地联接，使得压力释放阀的激活导致浆料从环管反应器排放到浆料分离系统，其中浆料分离 系统能够将固体和液体组分与浆料的气体组分分离，并通过火炬头将气体组分传输到耀斑。
-
公开(公告)号：US20160101399A1
公开(公告)日：2016-04-14
申请号：US14975423
申请日：2015-12-18
Applicant: Chevron Phillips Chemical Company LP
Inventor： 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 classification number: 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
Abstract: 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.
-
-
-
-
-
-
-
-
-
Search Results
11
records
(took 0.02 seconds)
