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公开(公告)号：US20180272309A1
公开(公告)日：2018-09-27
申请号：US15995795
申请日：2018-06-01
Applicant: CHEVRON PHILLIPS CHEMICAL COMPANY LP
Inventor： Maruti Bhandarkar , Elizabeth A. Benham , Rebecca A. Gonzales , Joel A. Mutchler , Catherine M. Gill , Timothy O. Odi , Thanh T. Nguyen , Scott E. Kufeld
CPC classification number: B01J19/0013 , B01J19/1818 , B01J19/1837 , B01J2219/0004 , B01J2219/00094 , B01J2219/00103 , B01J2219/00123 , B01J2219/00247 , C07C2/06 , C08F2/001 , C08F2/01 , C08F6/001 , C08F10/00 , C08F110/02 , C08J11/02 , C08L23/00
Abstract: A system and method for a first reactor to produce a transfer slurry having a first polyolefin polymerized in the first reactor, a heat-removal zone to remove heat from the transfer slurry, and a second reactor to receive the transfer slurry cooled by the heat-removal zone, the second reactor to produce a product slurry having a product polyolefin which includes the first polyolefin and a second polyolefin polymerized in the second reactor.
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公开(公告)号：US09914676B2
公开(公告)日：2018-03-13
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
IPC: B01J19/00 , B01J19/24 , C07C4/00 , C07C4/02 , C07C4/04 , C07C5/00 , C07C5/02 , C07C5/03 , C07C5/05 , C10G45/00 , C10G45/32 , C10G69/00 , C10G69/02 , C10G69/06 , C10G70/00 , C10G70/02 , C07C5/09 , C10G9/00
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：US09861955B2
公开(公告)日：2018-01-09
申请号：US15585987
申请日：2017-05-03
Applicant: Chevron Phillips Chemical Company LP
Inventor： Ralph W. Romig , Timothy O. Odi , Jennifer F. Drew
CPC classification number: B01J20/3458 , B01D53/0438 , B01D53/0462 , B01D53/047 , B01D53/261 , B01D2253/104 , B01D2253/108 , B01D2256/24 , B01D2257/104 , B01D2257/30 , B01D2257/504 , B01D2257/70 , B01D2257/7022 , B01D2257/80 , B01D2259/40052 , B01D2259/4009 , B01D2259/402 , B01J20/3408 , B01J20/3433 , C08F10/00 , Y02C10/08
Abstract: Disclosed are embodiments of a method of regenerating a desiccant in an off-line treater of a polyolefin production process. The method may include a heating phase followed by a cooling phase. The heating phase may involve use of a regenerating gas made from heating a treated a recycle stream of the polyolefin production process to regenerate desiccant in an off-line treater. The cooling phase may involve thermosyphoning the regenerating gas, nitrogen, an olefin-free diluent, or combinations thereof in a closed-convection loop of the off-line treater.
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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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45.发明授权公开(公告)号：US09556288B2
公开(公告)日：2017-01-31
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
IPC: C08F10/02 , C08F2/12 , C08F2/38 , B01J19/18 , B01J19/24 , C08F2/00 , C08F2/01 , C08L23/02 , C08F110/02
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 slurry 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浆料，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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Patent Agency Ranking
公开(公告)号：US20170022299A9
公开(公告)日：2017-01-26
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放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：US20160355449A1
公开(公告)日：2016-12-08
申请号：US14733595
申请日：2015-06-08
Applicant: Chevron Phillips Chemical Company LP
Inventor： Timothy O. Odi , Zongxuan Hong , Joseph Bergmeister, III , Tin-Tack Peter Cheung , Charles D. Nolidin , Thomas J. Gonzales , Jennifer L. Nill , David W. Dockter
Abstract: A process comprising hydrogenating a highly unsaturated hydrocarbon in the presence of a first hydrogenation catalyst and a second hydrogenation catalyst to one or more compounds including an unsaturated hydrocarbon such that a total conversion of the highly unsaturated hydrocarbon is about 99 mol % or greater. In the process, the first hydrogenation catalyst, the second hydrogenation catalyst, or both, have a hydrogenation selectivity to the unsaturated hydrocarbon of about 90% or greater.
Abstract translation: 一种方法，包括在第一氢化催化剂和第二氢化催化剂存在下将高度不饱和烃氢化为一种或多种包括不饱和烃的化合物，使得高度不饱和烃的总转化率为约99摩尔％以上。 在该方法中，第一氢化催化剂，第二氢化催化剂或二者均具有约90％或更高的对不饱和烃的加氢选择性。
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公开(公告)号：US09403921B2
公开(公告)日：2016-08-02
申请号：US14829190
申请日：2015-08-18
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
IPC: C08F2/12 , C08F2/38 , B01J19/18 , B01J19/24 , C08F10/02 , C08F2/00 , C08F2/01 , C08L23/02 , C08F110/02
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 slurry 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.
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公开(公告)号：US20150259441A1
公开(公告)日：2015-09-17
申请号：US14725954
申请日：2015-05-29
Applicant: Chevron Phillips Chemical Company LP
Inventor： Anurag Gupta , Timothy O. Odi , Ralph W. Romig
IPC: C08F2/34 , B01J19/24 , C08F210/16
CPC classification number: C08F2/34 , B01J19/18 , B01J19/245 , B01J2219/24 , C08F2/01 , C08F6/003 , C08F6/04 , C08F210/16 , C08F2500/05 , C08L23/00 , C08F10/00 , C08F2/14 , C08F210/14
Abstract: The disclosure includes a polymerization process and an olefin polymerization system. A polymerization product is produced, a vapor phase is recovered from the polymerization product, the vapor phase is fractionated in a first column to yield a fraction stream, and the fraction stream is fractionated in a second column. A first stream of the second column, which comprises a diluent, can be recycled to a first polymerization reactor. A second stream of the second column, which comprises olefin monomer, diluent, and hydrogen, can be recycled to a second polymerization reactor. Comonomer may be recycled from the first column to the first polymerization reactor, the second polymerization reactor, or both.
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公开(公告)号：US20140318743A1
公开(公告)日：2014-10-30
申请号：US13872746
申请日：2013-04-29
Applicant: CHEVRON PHILLIPS CHEMICAL COMPANY, LP
Inventor： Timothy O. Odi , Anurag Gupta , Ralph W. Romig
IPC: F28D15/00
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.
Abstract translation: 一种具有第一反应器温度控制路径，第二反应器温度控制路径和共用温度控制路径的聚烯烃反应器温度控制系统的系统和方法。 共用温度控制路径被配置为组合和处理冷却剂返回流，并且为第一反应堆温度控制路径和第二反应堆温度控制路径提供冷却剂供应。
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