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公开(公告)号：WO2014070608A1
公开(公告)日：2014-05-08
申请号：PCT/US2013/066842
申请日：2013-10-25
Applicant: CHEVRON PHILLIPS CHEMICAL COMPANY LP , KUFELD, Scott E. , KREISCHER, Bruce E. , HOTTOVY, John D.
Inventor： KUFELD, Scott E. , KREISCHER, Bruce E. , HOTTOVY, John D.
CPC classification number: C08F2/01 , B01J19/1837 , B01J2219/00162 , C08F2/14 , C08F6/00 , C08F6/003 , C08J11/02 , C08F10/02 , C08F2/00 , C08F210/16 , C08F210/14 , C08L23/06
Abstract: Processes and systems for the production for pressure management of a polymerization product flowing from a loop polymerization reactor to a separation vessel in a slurry polymerization system are disclosed herein. For example, a process comprises withdrawing the polymerization product from a loop polymerization reactor, and conveying the withdrawn polymerization product to a separation vessel via a first pressure differential and a second pressure differential. The withdrawn polymerization product may flow through the first pressure differential before flowing through the second pressure differential, and the first pressure differential may be less than the second pressure differential.
Abstract translation: 在本文中公开了用于从淤浆聚合系统中的环状聚合反应器流到分离容器的聚合产物的压力管理生产的方法和系统。 例如，一种方法包括从环路聚合反应器中取出聚合产物，并通过第一压力差和第二压差将抽出的聚合产物输送到分离容器。 撤回的聚合产物可能在流过第二压力差之前流过第一压力差，并且第一压力差可小于第二压力差。
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公开(公告)号：WO2013154907A2
公开(公告)日：2013-10-17
申请号：PCT/US2013/035274
申请日：2013-04-04
Applicant: CHEVRON PHILLIPS CHEMICAL COMPANY LP , KUFELD, Scott, E. , HOTTOVY, John, D. , CHANG, Ai-fu
Inventor： KUFELD, Scott, E. , HOTTOVY, John, D. , CHANG, Ai-fu
CPC classification number: C08F2/001 , C08F6/001 , C08F110/02 , C08J11/02 , C08J2323/06 , C08L23/04 , C08F10/02 , C08F2/14
Abstract: A process for component separation in a polymer production system, comprising separating a polymerization product stream into a gas stream and a polymer stream, wherein the gas stream comprises ethane and unreacted ethylene, distilling the gas stream into a light hydrocarbon stream, wherein the light hydrocarbon stream comprises ethane and unreacted ethylene, contacting the light hydrocarbon stream with an absorption solvent system, wherein at least a portion of the unreacted ethylene from the light hydrocarbon stream is absorbed by the absorption solvent system, and recovering a waste gas stream from the absorption solvent system, wherein the waste gas stream comprises ethane, hydrogen, or combinations thereof.
Abstract translation: 一种在聚合物生产系统中用于组分分离的方法，包括将聚合产物流分离成气流和聚合物流，其中气流包括乙烷和未反应的乙烯，将气流蒸馏成轻质烃流，其中轻烃 流包含乙烷和未反应的乙烯，使轻烃流与吸收溶剂体系接触，其中至少一部分来自轻质烃流的未反应的乙烯被吸收溶剂系统吸收，并从吸收溶剂中回收废气流 系统，其中废气流包括乙烷，氢气或其组合。
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公开(公告)号：WO2014093088A1
公开(公告)日：2014-06-19
申请号：PCT/US2013/073054
申请日：2013-12-04
Applicant: CHEVRON PHILLIPS CHEMICAL COMPANY LP , BHANDARKAR, Maruti , BENHAM, Elizabeth, A , GILL, Catherine, M , GONZALES, Rebecca, A , KUFELD, Scott, E , MUTCHLER, Joel, A , NGUYEN, Thanh , ODI, Timothy, O
Inventor： BHANDARKAR, Maruti , BENHAM, Elizabeth, A , GILL, Catherine, M , GONZALES, Rebecca, A , KUFELD, Scott, E , MUTCHLER, Joel, A , NGUYEN, Thanh , ODI, Timothy, O
CPC classification number: C08F10/02 , C08F2/14 , C08F110/02 , C08F2500/24 , C08F2/00
Abstract: A technique for polymerizing ethylene on catalyst in a first polymerization reactor and in a second polymerization reactor to form polyethylene particles, and controlling particle size of the polyethylene particles.
Abstract translation: 在第一聚合反应器和第二聚合反应器中在催化剂上聚合乙烯以形成聚乙烯颗粒并控制聚乙烯颗粒的粒径的技术。
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公开(公告)号：WO2014081684A1
公开(公告)日：2014-05-30
申请号：PCT/US2013/070675
申请日：2013-11-19
Applicant: CHEVRON PHILLIPS CHEMICAL COMPANY LP , BHANDARKAR, Maruti , BENHAM, Elizabeth A , GILL, Catherine M , GONZALES, Rebecca A , KUFELD, Scott E , MUTCHLER, Joel A , NGUYEN, Thanh , ODI, Timothy O
Inventor： BHANDARKAR, Maruti , BENHAM, Elizabeth A , GILL, Catherine M , GONZALES, Rebecca A , KUFELD, Scott E , MUTCHLER, Joel A , NGUYEN, Thanh , ODI, Timothy O
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，被配置成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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公开(公告)号：WO2004007566A1
公开(公告)日：2004-01-22
申请号：PCT/US2003/022198
申请日：2003-07-17
Applicant: CHEVRON PHILLIPS CHEMICAL COMPANY LP , KUFELD, Scott, E. , BURNS, David, H. , VAIDYANATHAN, Ragavan
Inventor： KUFELD, Scott, E. , BURNS, David, H. , VAIDYANATHAN, Ragavan
IPC: C08F6/00
CPC classification number: B01D19/0005 , B01D19/0015 , B01J8/0015 , B01J8/005 , B01J19/1837 , B01J2208/00283 , B01J2208/00752 , B01J2219/00006 , C08F2/06 , C08F6/003 , C08F6/005 , C08F6/02 , C08F10/00 , C08F210/16 , Y02P20/584 , C08L23/00 , C08F2/14 , C08F210/08 , C08F210/14 , C08F4/24
Abstract: A process and apparatus for passing a polymerization effluent, comprising solid polymer, unreacted monomer, diluent and minor amounts of contaminants, to a high pressure flash where most of the fluid components are flashed and wherein a slip stream comprising diluent and minor amounts of monomer is separated from the bulk of the flashed fluid components. The slip stream is subjected to olefin removal to give an essentially olefin-free stream for recycle to a catalyst mud preparation area. The bulk of the flashed fluid components are recycled directly back to the polymerization zone without expensive olefin removal, although treatment to remove other contaminants can optionally be performed. The polymer and entrained fluid is passed to a low pressure flash zone where the fluids are flashed off, compressed and joined with the flash from the high pressure flash tank. Because the bulk of the fluids are removed in the high pressure flash, compression and cooling of product fluids prior to recycle is kept to a minimum.
Abstract translation: 一种将含有固体聚合物，未反应单体，稀释剂和少量污染物的聚合流出物通到高压闪蒸的方法和装置，其中大部分流体组分被闪蒸，并且其中包含稀释剂和少量单体的滑流是 与大部分闪烁的流体组分分离。 将滑流进行烯烃除去，得到基本上无烯烃的物流，用于再循环到催化剂泥浆制备区域。 大部分闪蒸的流体组分直接回收到聚合区，而不需要昂贵的烯烃去除，尽管可以任选地进行除去其它污染物的处理。 聚合物和夹带的流体被传递到低压闪蒸区域，其中流体被闪蒸掉，压缩并与来自高压闪蒸罐的闪光接合。 因为大部分流体在高压闪蒸中被除去，所以在再循环之前将产品流体的压缩和冷却保持在最小。
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Patent Agency Ranking
公开(公告)号：WO2013154907A3
公开(公告)日：2014-01-03
申请号：PCT/US2013035274
申请日：2013-04-04
Applicant: CHEVRON PHILLIPS CHEMICAL CO , KUFELD SCOTT E , HOTTOVY JOHN D , CHANG AI-FU
Inventor： KUFELD SCOTT E , HOTTOVY JOHN D , CHANG AI-FU
CPC classification number: C08F2/001 , C08F6/001 , C08F110/02 , C08J11/02 , C08J2323/06 , C08L23/04 , C08F10/02 , C08F2/14
Abstract: A process for component separation in a polymer production system, comprising separating a polymerization product stream into a gas stream and a polymer stream, wherein the gas stream comprises ethane and unreacted ethylene, distilling the gas stream into a light hydrocarbon stream, wherein the light hydrocarbon stream comprises ethane and unreacted ethylene, contacting the light hydrocarbon stream with an absorption solvent system, wherein at least a portion of the unreacted ethylene from the light hydrocarbon stream is absorbed by the absorption solvent system, and recovering a waste gas stream from the absorption solvent system, wherein the waste gas stream comprises ethane, hydrogen, or combinations thereof.
Abstract translation: 一种聚合物生产系统中组分分离的方法，包括将聚合产物流分离成气流和聚合物流，其中气流包括乙烷和未反应的乙烯，将气流蒸馏成轻质烃流，其中轻烃 流包含乙烷和未反应的乙烯，使轻质烃流与吸收溶剂体系接触，其中至少一部分来自轻烃流的未反应乙烯被吸收溶剂体系吸收，并从吸收溶剂中回收废气流 系统，其中废气流包括乙烷，氢气或其组合。
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7.发明申请
公开(公告)号：WO2014099411A1
公开(公告)日：2014-06-26
申请号：PCT/US2013/073555
申请日：2013-12-06
Applicant: CHEVRON PHILLIPS CHEMICAL COMPANY LP , BHANDARKAR, Maruti , BENHAM, Elizabeth, A. , GILL, Catherine, M. , GONZALES, Rebecca, A. , KUFELD, Scott E , MUTCHLER, Joel, A. , NGUYEN, Thanh , ODI, Timothy, O.
Inventor： BHANDARKAR, Maruti , BENHAM, Elizabeth, A. , GILL, Catherine, M. , GONZALES, Rebecca, A. , KUFELD, Scott E , MUTCHLER, Joel, A. , NGUYEN, Thanh , ODI, Timothy, O.
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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公开(公告)号：WO2014093082A1
公开(公告)日：2014-06-19
申请号：PCT/US2013/073031
申请日：2013-12-04
Applicant: CHEVRON PHILLIPS CHEMICAL COMPANY LP , BHANDARKAR, Maruti , BENHAM, Elizabeth A. , GILL, Catherine M. , GONZALES, Rebecca A. , KUFELD, Scott E. , MUTCHLER, Joel A. , NGUYEN, Thanh , ODI, Timothy O.
Inventor： BHANDARKAR, Maruti , BENHAM, Elizabeth A. , GILL, Catherine M. , GONZALES, Rebecca A. , KUFELD, Scott E. , MUTCHLER, Joel A. , NGUYEN, Thanh , ODI, Timothy O.
CPC classification number: C08F2/01 , B01J19/002 , B01J19/1837 , B01J2219/00006 , B01J2219/00033 , B01J2219/0004 , B01J2219/00162 , B01J2219/00247 , C08F10/02 , C08F210/16 , C08F2/001 , C08F2/14
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：WO2013003133A1
公开(公告)日：2013-01-03
申请号：PCT/US2012/043215
申请日：2012-06-20
Applicant: CHEVRON PHILLIPS CHEMICAL COMPANY LP , HOTTOVY, John, D , KUFELD, Scott, E
Inventor： HOTTOVY, John, D , KUFELD, Scott, E
CPC classification number: C08F110/02 , B01D1/04 , B01D1/24 , B01J8/005 , B01J19/06 , B01J19/1837 , B01J2219/00006 , C08F6/003 , C08F10/00 , C08F2/00 , C08F2/14 , C08L23/00
Abstract: The present embodiments provide a system and method for separation within a polymer production process. Specifically, a flashline heater configured according to present embodiments may provide more time than is required for complete vaporization of liquid hydrocarbons that are not entrained within a polymer fluff produced within a polymerization reactor. Such extra time may allow for liquid hydrocarbons that are entrained within the polymer fluff to be vaporized.
Abstract translation: 本实施例提供了聚合物生产过程中的分离系统和方法。 具体而言，根据本实施例构造的闪蒸加热器可以提供比在聚合反应器内产生的聚合物绒毛内不夹带的液体烃完全蒸发所需的时间更长的时间。 这种额外的时间可以允许夹带在聚合物绒毛内的液体烃被汽化。
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公开(公告)号：WO2004024780A1
公开(公告)日：2004-03-25
申请号：PCT/US2003/029071
申请日：2003-09-16
Applicant: CHEVRON PHILLIPS CHEMICAL COMPANY LP , KUFELD, Scott, E. , REID, Thomas, A. , TAIT, John, H. , BURNS, David, H. , VERSER, DONALD, W. , HOTTOVY, John, D. , HENSLEY, Harvey, D. , PRZELOMSKI, David, J. , CYMBALUK, Teddy, H. , FRANKLIN, Robert, K. , PEREZ, Ethelwoldo, P.
Inventor： KUFELD, Scott, E. , REID, Thomas, A. , TAIT, John, H. , BURNS, David, H. , VERSER, DONALD, W. , HOTTOVY, John, D. , HENSLEY, Harvey, D. , PRZELOMSKI, David, J. , CYMBALUK, Teddy, H. , FRANKLIN, Robert, K. , PEREZ, Ethelwoldo, P.
IPC: C08F2/00
CPC classification number: B01J19/1837 , B01J8/003 , B01J8/008 , C08F10/00 , C08F210/16 , C08F2/01 , C08F2/14 , C08F210/14
Abstract: A polymerization loop reactor including a loop reaction zone, a continuous takeoff, and a fluid slurry disposed in the reaction zone. A generally cylindrical wall defines the loop reaction zone. The length of the loop reaction zone and the nominal outside diameter of the generally cylindrical wall define a length / diameter ratio greater than 250. The reactor can be charged with a fluid slurry including an olefin monomer reactant, solid olefin polymer particles, and a liquid diluent. The concentration of the solid olefin polymer particles in the slurry can be greater than 40 weight percent based on the weight of polymer particles and the weight of liquid diluent. Also disclosed is a polymerization process carried out by polymerizing, in the loop reaction zone of a reactor as defined above, at least one olefin monomer in a liquid diluent to produce a fluid slurry as defined above.
Abstract translation: 一种包括环路反应区，连续起飞和设置在反应区中的流体淤浆的聚合反应器反应器。 大致圆柱形的壁限定了环路反应区域。 环路反应区的长度和大致圆柱形壁的标称外径确定了大于250的长度/直径比。反应器可以装有包含烯烃单体反应物，固体烯烃聚合物颗粒和液体的流体浆料 冲淡。 基于聚合物颗粒的重量和液体稀释剂的重量，浆料中固体烯烃聚合物颗粒的浓度可以大于40重量％。 还公开了聚合方法，其通过在液体稀释剂中的至少一种烯烃单体在如上定义的反应器的环路反应区域中聚合以产生如上所定义的流体浆料而进行。
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