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公开(公告)号:US20170152328A1
公开(公告)日:2017-06-01
申请号:US15429704
申请日:2017-02-10
Applicant: Chevron Phillips Chemical Company LP
Inventor: Timothy O. Odi , Ralph Romig , Joseph Curren , Anurag Gupta
CPC classification number: C08F2/01 , B01J19/0013 , B01J19/1837 , B01J19/1862 , B01J19/242 , B01J19/2435 , B01J2219/00051 , B01J2219/00058 , B01J2219/00085 , B01J2219/00094 , B01J2219/00103 , B01J2219/24 , C08F2/001 , F28D7/106 , F28D15/00
Abstract: A system and method for startup of a polyolefin reactor temperature control system having a first reactor temperature control path, a second reactor temperature control path, and a shared temperature control path. In some embodiments, during startup the second reactor temperature control path is configured to allow the temperature of a second reactor to rise due to the heat of the exothermic polymerization reaction occurring within reactor until reaching a predetermined setpoint temperature. In other embodiments, during startup a first reactor temperature control path is configured to include a heat exchanger used as a cooler, and a second reactor temperature control path is configured to include a heat exchanger used as a heater, to raise the temperature of the second reactor until reaching a predetermined setpoint temperature.
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公开(公告)号:US10072103B2
公开(公告)日:2018-09-11
申请号:US15646710
申请日:2017-07-11
Applicant: Chevron Phillips Chemical Company LP
Inventor: Timothy O. Odi , Ralph Romig , Joseph Curren , Anurag Gupta
CPC classification number: C08F2/01 , B01J19/0013 , B01J19/1837 , B01J19/1862 , B01J19/242 , B01J19/2435 , B01J2219/00051 , B01J2219/00058 , B01J2219/00085 , B01J2219/00094 , B01J2219/00103 , B01J2219/24 , C08F2/001 , F28D7/106 , F28D15/00
Abstract: A system and method for startup of a polyolefin reactor temperature control system having a first reactor temperature control path, a second reactor temperature control path, and a shared temperature control path. In some embodiments, during startup the second reactor temperature control path is configured to allow the temperature of a second reactor to rise due to the heat of the exothermic polymerization reaction occurring within the reactor until reaching a predetermined setpoint temperature. In other embodiments, during startup a first reactor temperature control path is configured to include a heat exchanger used as a cooler, and a second reactor temperature control path is configured to include a heat exchanger used as a heater, to raise the temperature of the second reactor until reaching a predetermined setpoint temperature.
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公开(公告)号:US20170306059A1
公开(公告)日:2017-10-26
申请号:US15646710
申请日:2017-07-11
Applicant: Chevron Phillips Chemical Company LP
Inventor: Timothy O. Odi , Ralph Romig , Joseph Curren , Anurag Gupta
CPC classification number: C08F2/01 , B01J19/0013 , B01J19/1837 , B01J19/1862 , B01J19/242 , B01J19/2435 , B01J2219/00051 , B01J2219/00058 , B01J2219/00085 , B01J2219/00094 , B01J2219/00103 , B01J2219/24 , C08F2/001 , F28D7/106 , F28D15/00
Abstract: A system and method for startup of a polyolefin reactor temperature control system having a first reactor temperature control path, a second reactor temperature control path, and a shared temperature control path. In some embodiments, during startup the second reactor temperature control path is configured to allow the temperature of a second reactor to rise due to the heat of the exothermic polymerization reaction occurring within reactor until reaching a predetermined setpoint temperature. In other embodiments, during startup a first reactor temperature control path is configured to include a heat exchanger used as a cooler, and a second reactor temperature control path is configured to include a heat exchanger used as a heater, to raise the temperature of the second reactor until reaching a predetermined setpoint temperature.
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公开(公告)号:US10730032B2
公开(公告)日:2020-08-04
申请号:US15981532
申请日:2018-05-16
Applicant: Chevron Phillips Chemical Company LP
Inventor: Kenneth A. Dooley , Jeffrey S. Lowell , Joseph Curren
IPC: C08F2/00 , C08F2/01 , C08F110/02 , B01J19/24 , B01D19/00
Abstract: Systems and methods for improved degassing of polymer flake are provided herein. These systems include a polymerization reactor configured to polymerize one or more olefin monomers and produce a product stream comprising solid polymer flake entrained in a fluid; a flash chamber configured to separate the solid polymer flake from the fluid and to produce a fluid stream and a concentrated stream; and a first degassing chamber configured to separate the concentrated stream by contacting the concentrated stream with a purge fluid comprising one or more light hydrocarbons to produce a partially degassed polymer flake stream and a purge fluid stream.
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公开(公告)号:US09822193B2
公开(公告)日:2017-11-21
申请号:US15429704
申请日:2017-02-10
Applicant: Chevron Phillips Chemical Company LP
Inventor: Timothy O. Odi , Ralph Romig , Joseph Curren , Anurag Gupta
CPC classification number: C08F2/01 , B01J19/0013 , B01J19/1837 , B01J19/1862 , B01J19/242 , B01J19/2435 , B01J2219/00051 , B01J2219/00058 , B01J2219/00085 , B01J2219/00094 , B01J2219/00103 , B01J2219/24 , C08F2/001 , F28D7/106 , F28D15/00
Abstract: A system and method for startup of a polyolefin reactor temperature control system having a first reactor temperature control path, a second reactor temperature control path, and a shared temperature control path. In some embodiments, during startup the second reactor temperature control path is configured to allow the temperature of a second reactor to rise due to the heat of the exothermic polymerization reaction occurring within reactor until reaching a predetermined setpoint temperature. In other embodiments, during startup a first reactor temperature control path is configured to include a heat exchanger used as a cooler, and a second reactor temperature control path is configured to include a heat exchanger used as a heater, to raise the temperature of the second reactor until reaching a predetermined setpoint temperature.
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公开(公告)号:US11173468B2
公开(公告)日:2021-11-16
申请号:US16921247
申请日:2020-07-06
Applicant: Chevron Phillips Chemical Company LP
Inventor: Kenneth A. Dooley , Jeffrey S. Lowell , Joseph Curren
IPC: C08F210/16 , C08F2/01 , B01J19/24 , B01D19/00 , C08F110/02
Abstract: Systems and methods for improved degassing of polymer flake are provided herein. These systems include a polymerization reactor configured to polymerize one or more olefin monomers and produce a product stream comprising solid polymer flake entrained in a fluid; a flash chamber configured to separate the solid polymer flake from the fluid and to produce a fluid stream and a concentrated stream; and a first degassing chamber configured to separate the concentrated stream by contacting the concentrated stream with a purge fluid comprising one or more light hydrocarbons to produce a partially degassed polymer flake stream and a purge fluid stream.
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公开(公告)号:US20200330954A1
公开(公告)日:2020-10-22
申请号:US16921247
申请日:2020-07-06
Applicant: Chevron Phillips Chemical Company LP
Inventor: Kenneth A. Dooley , Jeffrey S. Lowell , Joseph Curren
IPC: B01J19/24 , B01D19/00 , C08F110/02
Abstract: Systems and methods for improved degassing of polymer flake are provided herein. These systems include a polymerization reactor configured to polymerize one or more olefin monomers and produce a product stream comprising solid polymer flake entrained in a fluid; a flash chamber configured to separate the solid polymer flake from the fluid and to produce a fluid stream and a concentrated stream; and a first degassing chamber configured to separate the concentrated stream by contacting the concentrated stream with a purge fluid comprising one or more light hydrocarbons to produce a partially degassed polymer flake stream and a purge fluid stream.
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公开(公告)号:US20190351386A1
公开(公告)日:2019-11-21
申请号:US15981532
申请日:2018-05-16
Applicant: Chevron Phillips Chemical Company LP
Inventor: Kenneth A. Dooley , Jeffrey S. Lowell , Joseph Curren
IPC: B01J19/24 , C08F110/02 , B01D19/00
Abstract: Systems and methods for improved degassing of polymer flake are provided herein. These systems include a polymerization reactor configured to polymerize one or more olefin monomers and produce a product stream comprising solid polymer flake entrained in a fluid; a flash chamber configured to separate the solid polymer flake from the fluid and to produce a fluid stream and a concentrated stream; and a first degassing chamber configured to separate the concentrated stream by contacting the concentrated stream with a purge fluid comprising one or more light hydrocarbons to produce a partially degassed polymer flake stream and a purge fluid stream.
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