公开(公告)号：EP2195349A1

公开(公告)日：2010-06-16

申请号：EP08830948.9

申请日：2008-09-09

Applicant: ExxonMobil Research and Engineering Company

Inventor： KISS, Gabor ,  CHU, John, W. ,  REYNOLDS, Robert, P., Jr. ,  GALUSKA, Alan, A. ,  DATTA, Sudhin ,  CHAPMAN, Bryan, R. ,  BRANT, Patrick

IPC: C08F2/01

CPC classification number: C08F10/00 ,  B01J2219/00038 ,  B01J2219/0004 ,  C08F210/16 ,  C08J3/18 ,  C08F2/01 ,  C08F2/001 ,  C08F210/14 ,  C08F2500/12 ,  C08F2500/08 ,  C08F2500/20

Abstract: A process for fluid phase in-line blending of plasticized polymers by providing two or more reactor trains configured in parallel and a separator, wherein one or more of the trains produces one or more polymers and another produces one or more plasticizers; contacting in at least one train olefin monomers, catalyst systems, optional comonomers, scavengers, diluents or solvents, at a temperature above the solid-fluid phase transition temperature of the polymerization system and a pressure no lower than 10 MPa below the cloud point pressure of the polymerization system and less than 1500 MPa; forming a reactor effluent including a homogeneous polymer mixture and plasticizer-monomer mixture in each train; passing the reactor effluents through the separator; maintaining the temperature and pressure within the separator to form a fluid-fluid two-phase system; and separating the phases. The polymer-rich blend phase is conveyed to a downstream finishing stage.

公开(公告)号：EP2195349B1

公开(公告)日：2012-07-11

申请号：EP08830948.9

申请日：2008-09-09

Applicant: ExxonMobil Research and Engineering Company

Inventor： KISS, Gabor ,  CHU, John, W. ,  REYNOLDS, Robert, P., Jr. ,  GALUSKA, Alan, A. ,  DATTA, Sudhin ,  CHAPMAN, Bryan, R. ,  BRANT, Patrick

IPC: C08F10/00 ,  C08F2/01 ,  C08J3/18

CPC classification number: C08F10/00 ,  B01J2219/00038 ,  B01J2219/0004 ,  C08F210/16 ,  C08J3/18 ,  C08F2/01 ,  C08F2/001 ,  C08F210/14 ,  C08F2500/12 ,  C08F2500/08 ,  C08F2500/20

Abstract: A process for fluid phase in-line blending of plasticized polymers by providing two or more reactor trains configured in parallel and a separator, wherein one or more of the trains produces one or more polymers and another produces one or more plasticizers; contacting in at least one train olefin monomers, catalyst systems, optional comonomers, scavengers, diluents or solvents, at a temperature above the solid-fluid phase transition temperature of the polymerization system and a pressure no lower than 10 MPa below the cloud point pressure of the polymerization system and less than 1500 MPa; forming a reactor effluent including a homogeneous polymer mixture and plasticizer-monomer mixture in each train; passing the reactor effluents through the separator; maintaining the temperature and pressure within the separator to form a fluid-fluid two-phase system; and separating the phases. The polymer-rich blend phase is conveyed to a downstream finishing stage.