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21.发明申请公开(公告)号：US20150126693A1
公开(公告)日：2015-05-07
申请号：US14597475
申请日：2015-01-15
Applicant: Chevron Phillips Chemical Company, LP
Inventor： Maruti Bhandarkar , Elizabeth A. Benham , Rebecca A. Gonzales , Scott E. Kufeld , Joel A. Mutchler , Catherine M. Gill , Thanh T. Nguyen , Timothy O. Odi
CPC classification number: C08F10/02 , B01J19/242 , B01J19/2435 , B01J19/245 , B01J19/246 , B01J2219/24 , C08F2/001 , C08F2/01 , C08F110/02 , Y10S526/905 , C08F10/00 , C08F2/38 , C08F2/14
Abstract: A system and method for polymerizing olefin in the presence of a chain transfer agent in a first reactor to form a first polyolefin, discharging from the first reactor a transfer shiny having the first polyolefin and the chain transfer agent, and processing the transfer slurry in a separator to remove chain transfer agent and to provide a fluff slurry having the first polyolefin and a lower content of chain transfer agent than in the transfer slurry. The system and method provide for feeding the fluff slurry to a second reactor, polymerizing olefin in the second reactor to form a second polyolefin, and discharging from the second reactor a slurry having the second polyolefin.
Abstract translation: 一种用于在第一反应器中在链转移剂存在下使烯烃聚合以形成第一聚烯烃的系统和方法，从第一反应器排出具有第一聚烯烃和链转移剂的转移光泽，并将转移浆料加工成 分离器以除去链转移剂，并提供具有第一聚烯烃和较低含量的链转移剂的绒毛浆料，而不是转移浆料。 该系统和方法提供将绒毛浆料供给到第二反应器，在第二反应器中聚合烯烃以形成第二聚烯烃，并从第二反应器排出具有第二聚烯烃的浆料。
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公开(公告)号：US20140275450A1
公开(公告)日：2014-09-18
申请号：US13795033
申请日：2013-03-12
Applicant: Chevron Phillips Chemical Company, LP
Inventor： Maruti Bhandarkar , Elizabeth A. Benham , Rebecca A. Gonzales , Scott E. Kufeld , Joel A. Mutchler , Catherine M. Gill , Thanh T. Nguyen , Timothy O. Odi
CPC classification number: C08F110/02 , B01J19/1818 , B01J19/1837 , B01J2204/005 , C08F210/16 , C08F2/001 , C08F2/14 , C08F210/14 , C08F2500/01 , C08F2500/05 , C08F2500/08 , C08F2500/26 , C08F2500/02 , C08F2500/07
Abstract: A system and method for producing polyolefin, including a polyolefin reactor system having: a first reactor to produce a first reactor discharge stream having a first polyolefin and a first diluent; and a second reactor to receive at least a portion of the first reactor discharge stream and to produce a second reactor discharge stream having a second polyolefin and a second diluent, wherein the second diluent is different than the first diluent.
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公开(公告)号：US10799847B2
公开(公告)日：2020-10-13
申请号：US15269050
申请日：2016-09-19
Applicant: Chevron Phillips Chemical Company, LP
Inventor： Maruti Bhandarkar , Elizabeth Ann Benham , Rebecca A. Gonzales , Scott E. Kufeld , Joel A. Mutchler , Catherine M. Gill , Thanh T. Nguyen , Timothy O. Odi
Abstract: A polyolefin production system including: a first reactor configured to produce a first discharge slurry having a first polyolefin; a second reactor configured to produce a second discharge slurry having a second polyolefin; and a post-reactor treatment zone having at least a separation vessel configured to receive the second discharge slurry or both the first discharge slurry and the second discharge slurry.
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公开(公告)号：US10173951B2
公开(公告)日：2019-01-08
申请号：US15264008
申请日：2016-09-13
Applicant: Chevron Phillips Chemical Company LP
Inventor： Joseph A. Curren , Ralph W. Romig , Ji Xian Loh , Timothy O. Odi
Abstract: Processes and systems for olefin and diluent recovery utilizing one or more side columns, including a side rectifier column and/or a side degassing column, in combination with a heavies column.
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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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Patent Agency Ranking
公开(公告)号：US20170349507A1
公开(公告)日：2017-12-07
申请号：US15671597
申请日：2017-08-08
Applicant: Chevron Phillips Chemical Company LP
Inventor： Joseph Bergmeister, III , Tin-Tack Peter Cheung , Zongxuan Hong , Timothy O. Odi , Charles D. Nolidin , Thomas J. Gonzales , Jennifer L. Nill , David W. Dockter
CPC classification number: B65G1/0492 , B01J19/24 , B01J19/245 , B01J2219/24 , B65G1/045 , B65G1/065 , B65G1/10 , B65G1/127 , B65G1/137 , B65G1/1371 , B65G1/1373 , B65G1/1378 , B65G47/57 , C07C4/04 , C07C5/05 , C07C5/09 , C07C2521/04 , C10G9/00 , C10G45/32 , C10G69/06 , C10G70/02 , C10G2400/20 , C10G2400/24 , Y10S901/01
Abstract: A process includes hydrogenating, in a reaction zone, a highly unsaturated hydrocarbon received from a hydrocarbon stream to yield a product having an unsaturated hydrocarbon, the hydrogenating step occurring in the presence of a hydrogenation catalyst which has a selectivity for conversion of the highly unsaturated hydrocarbon to the unsaturated hydrocarbon of about 90 mol % or greater based on the moles of the highly unsaturated hydrocarbon which are converted to the product, the hydrogenating step occurring in a reaction zone under conditions which include a flow index (IF) in a range of about 0.09 to about 35, wherein the IF is defined as: I F = F × [ CO ] V , wherein F is the flow rate of the hydrocarbon stream into the reaction zone in units of kg/h, [CO] is the concentration of carbon monoxide in the hydrocarbon stream in units of mol %, and V is the volume of the reaction zone in units of ft3.
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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：US20170152327A1
公开(公告)日：2017-06-01
申请号：US15429692
申请日：2017-02-10
Applicant: Chevron Phillips Chemical Company LP
Inventor： Timothy O. Odi , Ralph Romig , Anurag Gupta
CPC classification number: C08F2/01 , B01J19/1837 , B01J19/1862 , B01J19/242 , B01J19/2435 , B01J2219/00051 , B01J2219/00074 , B01J2219/00087 , B01J2219/00094 , B01J2219/24 , C08F2/001 , F28D7/106 , F28D15/00 , F28F27/02 , F28F2250/06
Abstract: A system and method for 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. The shared temperature control path is configured to combine and process coolant return streams, and to provide coolant supply for the first reactor temperature control path and the second reactor temperature control path.
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公开(公告)号：US09556283B2
公开(公告)日：2017-01-31
申请号：US14339277
申请日：2014-07-23
Applicant: Chevron Phillips Chemical Company, LP
Inventor： Maruti Bhandarkar , Elizabeth Ann Benham , Rebecca A. Gonzales , Scott E. Kufeld , Joel A. Mutchler , Catherine M. Gill , Thanh T. Nguyen , Timothy O. Odi
CPC classification number: C08F10/02 , B01J19/0006 , B01J19/06 , B01J19/1837 , B01J19/242 , B01J19/2435 , B01J19/245 , B01J19/2455 , B01J2208/0007 , B01J2208/00088 , B01J2219/00033 , B01J2219/0006 , B01J2219/00162 , B01J2219/00164 , B01J2219/24 , C08F2/01 , C08F210/16 , C08F2/14 , C08F2/001
Abstract: A system and method for discharging a transfer slurry from a first polymerization reactor through a transfer line to a second polymerization reactor, the transfer slurry including at least diluent and a first polyethylene. A product slurry is discharged from the second polymerization reactor, the product slurry including at least diluent, the first polyethylene, and a second polyethylene. The velocity, pressure drop, or pressure loss due to friction in the transfer line is determined, and a process variable adjusted in response to the velocity, pressure drop, or pressure loss not satisfying a specified value.
Abstract translation: 一种用于将转移浆料从第一聚合反应器通过输送管线排出到第二聚合反应器的系统和方法，所述转移浆料至少包括稀释剂和第一聚乙烯。 产物浆料从第二聚合反应器排出，产物浆料至少包括稀释剂，第一聚乙烯和第二聚乙烯。 确定由于传送线中的摩擦导致的速度，压降或压力损失，并且响应于速度，压降或压力损失而调节的过程变量不满足特定值。
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公开(公告)号：US20170001167A1
公开(公告)日：2017-01-05
申请号：US15269050
申请日：2016-09-19
Applicant: Chevron Phillips Chemical Company, LP
Inventor： Maruti Bhandarkar , Elizabeth Ann Benham , Rebecca A. Gonzales , Scott E. Kufeld , Joel A. Mutchler , Catherine M. Gill , Thanh T. Nguyen , Timothy O. Odi
CPC classification number: B01J19/245 , B01J19/1818 , B01J19/1825 , B01J19/1837 , B01J19/2455 , B01J19/2465 , B01J2219/00024 , B01J2219/24 , C08F2/001 , C08F2/01 , C08F10/00
Abstract: A polyolefin production system including: a first reactor configured to produce a first discharge slurry having a first polyolefin; a second reactor configured to produce a second discharge slurry having a second polyolefin; and a post-reactor treatment zone having at least a separation vessel configured to receive the second discharge slurry or both the first discharge slurry and the second discharge slurry.
Abstract translation: 一种聚烯烃生产系统，包括：第一反应器，被配置为产生具有第一聚烯烃的第一排出浆料; 第二反应器，被配置为产生具有第二聚烯烃的第二排出浆料; 以及后反应器处理区，其至少具有分配容器，所述分离容器被配置为容纳所述第二排出浆料或所述第一排出浆料和所述第二排出浆料。
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