公开(公告)号：WO2009070261A3

公开(公告)日：2009-07-16

申请号：PCT/US2008013056

申请日：2008-11-24

Applicant: UNIVATION TECH LLC ,  ROY KEVIN D ,  FORCE RANDALL L ,  SWECKER JAMES L

Inventor： ROY KEVIN D ,  FORCE RANDALL L ,  SWECKER JAMES L

IPC: B01D19/00

CPC classification number: B01D19/0005 ,  B01D19/0015 ,  C08F210/16 ,  Y10S526/912 ,  C08F2/00 ,  C08F210/08

Abstract: A system and method for integrating the removal of volatiles from a liquid hydrocarbon feed to the polyolefin polymerization system and the recovery of hydrocarbons from a polyolefin production process vent stream is provided. Th method and the system remove gases dissolved in the monomer feed to a polymerisation rector by means of a stripping column. The dissoled gases are oxygen, carbon monoxide or carbon dioxide and can be a poison for the catalys used in the poymerisation reaction. The stripping gas is a vent gas coming from the poymerisation process / apparatus or the resin purging. Possibly one single stripping column is used to remove the gases in the combined feed to the polymerisation reactor. The system and the method can be used for producing polyethylene.

Abstract translation: 提供了一种用于将液体烃进料中的挥发物从聚烯烃聚合体系中除去并从聚烯烃生产工艺排放流中回收烃的系统和方法。 Th方法和系统通过汽提塔将溶解在单体进料中的气体除去聚合反应器。 溶解的气体是氧气，一氧化碳或二氧化碳，并且可能是臭氧反应中使用的催化剂的毒物。 汽提气体是来自臭化工艺/设备或树脂吹扫的排出气体。 可能使用单个汽提塔来除去聚合反应器的组合进料中的气体。 该系统和方法可用于生产聚乙烯。

公开(公告)号：WO2009070261A2

公开(公告)日：2009-06-04

申请号：PCT/US2008013056

申请日：2008-11-24

Applicant: UNIVATION TECH LLC ,  ROY KEVIN D ,  FORCE RANDALL L ,  SWECKER JAMES L

Inventor： ROY KEVIN D ,  FORCE RANDALL L ,  SWECKER JAMES L

IPC: B01D19/00

CPC classification number: B01D19/0005 ,  B01D19/0015 ,  C08F210/16 ,  Y10S526/912 ,  C08F2/00 ,  C08F210/08

Abstract: A method and system for removing volatiles from liquid hydrocarbons being fed to a polyolefin polymerization system is provided. More specifically, a system and method for integrating the removal of volatiles from a liquid hydrocarbon feed to the polyolefin polymerization system and the recovery of hydrocarbons from a polyolefin production process vent stream is also provided.

Abstract translation: 提供了一种用于从进料到聚烯烃聚合体系中的液体烃中除去挥发物的方法和系统。 更具体地，还提供了一种用于将从液体烃进料挥发物去除到聚烯烃聚合体系和从聚烯烃生产过程排放流中回收烃的系统和方法。

公开(公告)号：WO2009070261A8

公开(公告)日：2009-06-04

申请号：PCT/US2008/013056

申请日：2008-11-24

Applicant: UNIVATION TECHNOLOGIES, LLC ,  ROY, Kevin, D. ,  FORCE, Randall, L. ,  SWECKER, James, L.

Inventor： ROY, Kevin, D. ,  FORCE, Randall, L. ,  SWECKER, James, L.

IPC: B01D19/00

Abstract: Systems and methods for removing a volatile catalyst poison from a liquid hydrocarbon are provided. In one embodiment, a process vent (106) can be introduced to a vent recovery system (108) to provide a recycle gas (110). A first portion of the recycle gas (112) and a liquid hydrocarbon (102) can be introduced to a stripper column (104) to provide a stripper vent gas (114) and a degassed liquid hydrocarbon (116) that can be introduced to a polymerization process.

公开(公告)号：WO2009075846A3

公开(公告)日：2013-10-10

申请号：PCT/US2008013565

申请日：2008-12-10

Applicant: UNIVATION TECH LLC ,  FORCE RANDALL L ,  ROY KEVIN D

Inventor： FORCE RANDALL L ,  ROY KEVIN D

IPC: F25J3/06 ,  C08F10/00 ,  F25J1/00 ,  F25J1/02 ,  F25J3/08

CPC classification number: F25J3/066 ,  C08F10/00 ,  F25J1/0015 ,  F25J1/0037 ,  F25J1/004 ,  F25J1/0045 ,  F25J1/0202 ,  F25J1/0224 ,  F25J1/0229 ,  F25J1/0236 ,  F25J1/0259 ,  F25J3/062 ,  F25J3/064 ,  F25J3/0645 ,  F25J3/08 ,  F25J2210/06 ,  F25J2210/12 ,  F25J2210/42 ,  F25J2215/04 ,  F25J2215/62 ,  F25J2220/42 ,  F25J2220/44 ,  F25J2260/02 ,  F25J2260/42 ,  F25J2260/44 ,  F25J2270/90 ,  F25J2270/904 ,  C08F2/00

Abstract: A process for integrating the recovery of hydrocarbons from a vent stream and the production of a nitrogen-rich liquid by: providing a vent to recovery including a monomer, wherein the vent to recovery originates from a polymerization process; separating the vent to recovery to form a primary recovered hydrocarbon and a primary recovered gas; separating the primary recovered gas to form a secondary recovered hydrocarbon and a warm residual gas, wherein the separation is by condensing the secondary recovered hydrocarbon, wherein an open-loop refrigeration cycle supplies cooling for the condensation, and wherein the open-loop refrigeration cycle produces a nitrogen- rich liquid; and recycling the primary recovered hydrocarbon to the polymerization process.

Abstract translation: 一种通过以下方式整合来自排气流的烃的回收和富氮液体的生产的方法：提供包括单体在内的回收通气，其中回收通气源于聚合过程; 将排气口分离以回收以形成初级回收的烃和初级回收气体; 分离初级回收的气体以形成二次回收的烃和热的残留气体，其中分离是通过冷凝二次回收的烃，其中开环制冷循环为冷凝提供冷却，其中开环制冷循环产生 富氮液体; 并将初级回收的烃再循环到聚合过程中。

公开(公告)号：WO2009075846A2

公开(公告)日：2009-06-18

申请号：PCT/US2008/013565

申请日：2008-12-10

Applicant: UNIVATION TECHNOLOGIES, LLC ,  FORCE, Randall, L. ,  ROY, Kevin, D.

Inventor： FORCE, Randall, L. ,  ROY, Kevin, D.

IPC: F25J3/02

CPC classification number: F25J3/066 ,  C08F10/00 ,  F25J1/0015 ,  F25J1/0037 ,  F25J1/004 ,  F25J1/0045 ,  F25J1/0202 ,  F25J1/0224 ,  F25J1/0229 ,  F25J1/0236 ,  F25J1/0259 ,  F25J3/062 ,  F25J3/064 ,  F25J3/0645 ,  F25J3/08 ,  F25J2210/06 ,  F25J2210/12 ,  F25J2210/42 ,  F25J2215/04 ,  F25J2215/62 ,  F25J2220/42 ,  F25J2220/44 ,  F25J2260/02 ,  F25J2260/42 ,  F25J2260/44 ,  F25J2270/90 ,  F25J2270/904 ,  C08F2/00

Abstract: A process for integrating the recovery of hydrocarbons from a vent stream and the production of a nitrogen-rich liquid by: providing a vent to recovery including a monomer, wherein the vent to recovery originates from a polymerization process; separating the vent to recovery to form a primary recovered hydrocarbon and a primary recovered gas; separating the primary recovered gas to form a secondary recovered hydrocarbon and a warm residual gas, wherein the separation is by condensing the secondary recovered hydrocarbon, wherein an open-loop refrigeration cycle supplies cooling for the condensation, and wherein the open-loop refrigeration cycle produces a nitrogen- rich liquid; and recycling the primary recovered hydrocarbon to the polymerization process.

Abstract translation: 一种通过以下方式整合来自排气流的烃的回收和富氮液体的生产的方法：提供包括单体在内的回收通气，其中回收通气源于聚合过程; 将排气口分离以回收以形成初级回收的烃和初级回收气体; 分离初级回收的气体以形成二次回收的烃和热的残留气体，其中分离是通过冷凝二次回收的烃，其中开环制冷循环为冷凝提供冷却，其中开环制冷循环产生 富氮液体; 并将初级回收的烃再循环到聚合过程中。