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公开(公告)号:CA2163465A1
公开(公告)日:1996-05-24
申请号:CA2163465
申请日:1995-11-22
Applicant: UNION CARBIDE CHEM PLASTIC
IPC: C08F2/00 , C08F2/34 , C08F8/00 , C08F10/02 , C08F210/16 , C08F297/08 , C08L23/00 , C08L23/04
Abstract: An in situ blend formed in the gas phase in two or more reactors connected in series comprising a mixture of two types of particles of polyethylene, (i) one type of particle containing a major proportion of high molecular weight polyethylene and a minor proportion of low molecular weight polyethylene and having a relatively high split ratio and (ii) one type of particle containing a major proportion of low molecular weight polyethylene and a minor proportion of high molecular weight polyethylene and having a relatively low split ratio wherein the average particle size of the blend is at least about 300 microns; the average split ratio of the blend is in the range of about 40:60 to about 60:40; and no more than about 10 percent by weight of the particles in the blend have a split ratio below 90 percent of the average split ratio of the blend.
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公开(公告)号:ZA956456B
公开(公告)日:1996-03-14
申请号:ZA956456
申请日:1995-08-02
Applicant: UNION CARBIDE CHEM PLASTIC
Inventor: BERNIER ROBERT JOSEPH NOEL , BROWN ROBERT CECIL , BOYEN ROBERT LORENZ , WILLIAMS GARY HARRY , SCAROLA LEONARD SEBASTIAN
IPC: A61K31/35 , A61K31/352 , B60C1/00 , A61K31/40 , A61K31/4025 , A61K31/415 , A61K31/425 , A61K31/44 , A61K31/443 , A61K31/4433 , A61K31/50 , A61K31/505 , A61K31/53 , A61P9/00 , B01J8/24 , B01J23/10 , C07D311/58 , C07D311/78 , C07D311/92 , C07D311/94 , C07D405/12 , C07D405/14 , C07D409/14 , C07D417/12 , C07D491/052 , C07D493/04 , C08F2/00 , C08F2/34 , C08F2/44 , C08F4/54 , C08F4/622 , C08F4/64 , C08F4/70 , C08F10/00 , C08F10/14 , C08F36/04 , C08F36/06 , C08F210/00 , C08F210/16 , C08F210/18 , C08K3/04 , C08K3/34 , C08F , B01J
Abstract: Polymers are produced in a stirred bed or gas fluidised bed polymerisation zone of growing polymer particles by (1) introducing a stream of monomer(s), and opt. inert gas(s) or liq(s)., into the polymerisation zone; (2) continuously or intermittently introducing a catalyst; (3) continuously or intermittently withdrawing polymer; and (4) continuously withdrawing unreacted gases, compressing and cooling the gases while maintaining the temp. in the polymerisation zone below the dew pt. of at least one monomer; with the proviso that if there is only one monomer present in the feed stream, an inert gas is also present.
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公开(公告)号:MX9302963A
公开(公告)日:1993-11-01
申请号:MX9302963
申请日:1993-05-20
Applicant: UNION CARBIDE CHEM PLASTIC
Inventor: BOYSEN ROBERT LORENZ , MURE CLIFF ROBERT , SCAROLA LEONARD SEBASTIAN , RHEE AARON SEUNG-JOON
IPC: C08F2/44 , C08F2/34 , C08F210/18 , C08J3/12 , C09J109/00
Abstract: A resin particle having an inner core comprising a sticky polymer and an outer shell of an inert particulate material.
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公开(公告)号:BR9004882A
公开(公告)日:1991-09-10
申请号:BR9004882
申请日:1990-09-28
Applicant: UNION CARBIDE CHEM PLASTIC
Inventor: RHEE SEUNG JOON , BAKER EDGAR CHAPMAN , EDWARDS DAVID NICHOLAS , LEE KIU HEE , MOORHOUSE JOHN HENRY , SCAROLA LEONARD SEBASTIAN , KAROL FREDERICK JOHN
IPC: C08F2/34 , C08F2/44 , C08F32/00 , C08F36/00 , C08F136/06 , C08F210/16 , C08F210/18 , C08F232/08 , C08F293/00 , C08F297/08
Abstract: A process for producing sticky polymers at polymerization reaction temperatures in excess of the softening temperature of the sticky polymers in a fluidized bed reactor catalyzed by a transition metal catalyst, which comprises conducting the polymerization reaction above the softening temperatures of the sticky polymers in the presence of about 0.3 to about 80 weight percent, based on the weight of the final product of an inert particulate material having a mean particle size of from about 0.01 to about 10 microns whereby polymer agglomeration of the sticky polymers is maintained at a size suitable for continuously producing the sticky polymers.
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公开(公告)号:NO904203A
公开(公告)日:1991-04-02
申请号:NO904203
申请日:1990-09-27
Applicant: UNION CARBIDE CHEM PLASTIC
Inventor: RHEE SEUNG JOON , BAKER EDGAR CHAPMAN , EDWARDS DAVID NICOLAS , LEE KIU HEE , MOORHOUSE JOHN HENRY , SCAROLA LEONARD SEBASTIAN
IPC: C08F2/34 , C08F2/44 , C08F32/00 , C08F36/00 , C08F136/06 , C08F210/16 , C08F210/18 , C08F232/08 , C08F293/00 , C08F297/08 , C08F210/00
CPC classification number: C08F2/44 , B29K2019/00 , B29K2021/00 , B29K2023/16 , B29K2105/16 , C08F210/18 , Y10S526/901 , C08F2/34
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公开(公告)号:FI904765A0
公开(公告)日:1990-09-27
申请号:FI904765
申请日:1990-09-27
Applicant: UNION CARBIDE CHEM PLASTIC
Inventor: RHEE SEUNG JOON , BAKER EDGAR CHAPMAN , EDWARDS DAVID NICHOLAS , LEE KIU HEE , MOORHOUSE JOHN HENRY , SCAROLA LEONARD SEBASTIAN , KAROL FREDERICK JOHN
IPC: C08F2/34 , C08F2/44 , C08F32/00 , C08F36/00 , C08F136/06 , C08F210/16 , C08F210/18 , C08F232/08 , C08F293/00 , C08F297/08 , C08F
Abstract: A process for producing sticky polymers at polymerization reaction temperatures in excess of the softening temperature of the sticky polymers in a fluidized bed reactor catalyzed by a transition metal catalyst, which comprises conducting the polymerization reaction above the softening temperatures of the sticky polymers in the presence of about 0.3 to about 80 weight percent, based on the weight of the final product of an inert particulate material having a mean particle size of from about 0.01 to about 10 microns whereby polymer agglomeration of the sticky polymers is maintained at a size suitable for continuously producing the sticky polymers.
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公开(公告)号:DE69710856T2
公开(公告)日:2002-07-18
申请号:DE69710856
申请日:1997-12-02
Applicant: UNION CARBIDE CHEM PLASTIC
Inventor: NEUBAUER ANTHONY CHARLES , SCAROLA LEONARD SEBASTIAN
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公开(公告)号:ES2142788T3
公开(公告)日:2000-05-01
申请号:ES90118575
申请日:1990-09-27
Applicant: UNION CARBIDE CHEM PLASTIC
Inventor: RHEE SEUNG JOON , BAKER EDGAR CHAPMAN , EDWARDS DAVID NICHOLAS , LEE KIU HEE , MOORHOUSE JOHN HENRY , SCAROLA LEONARD SEBASTIAN
IPC: C08F2/34 , C08F2/44 , C08F32/00 , C08F36/00 , C08F136/06 , C08F210/16 , C08F210/18 , C08F232/08 , C08F293/00 , C08F297/08 , C08F36/06
Abstract: A process for producing sticky polymers at polymerization reaction temperatures in excess of the softening temperature of the sticky polymers in a fluidized bed reactor catalyzed by a transition metal catalyst, which comprises conducting the polymerization reaction above the softening temperatures of the sticky polymers in the presence of about 0.3 to about 80 weight percent, based on the weight of the final product of an inert particulate material having a mean particle size of from about 0.01 to about 10 microns whereby polymer agglomeration of the sticky polymers is maintained at a size suitable for continuously producing the sticky polymers.
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公开(公告)号:AT190069T
公开(公告)日:2000-03-15
申请号:AT90118575
申请日:1990-09-27
Applicant: UNION CARBIDE CHEM PLASTIC
Inventor: RHEE SEUNG JOON , BAKER EDGAR CHAPMAN , EDWARDS DAVID NICHOLAS , LEE KIU HEE , MOORHOUSE JOHN HENRY , SCAROLA LEONARD SEBASTIAN , KAROL FREDERICK JOHN
IPC: C08F2/34 , C08F2/44 , C08F32/00 , C08F36/00 , C08F136/06 , C08F210/16 , C08F210/18 , C08F232/08 , C08F293/00 , C08F297/08 , C08F36/06
Abstract: A process for producing sticky polymers at polymerization reaction temperatures in excess of the softening temperature of the sticky polymers in a fluidized bed reactor catalyzed by a transition metal catalyst, which comprises conducting the polymerization reaction above the softening temperatures of the sticky polymers in the presence of about 0.3 to about 80 weight percent, based on the weight of the final product of an inert particulate material having a mean particle size of from about 0.01 to about 10 microns whereby polymer agglomeration of the sticky polymers is maintained at a size suitable for continuously producing the sticky polymers.
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公开(公告)号:AT184886T
公开(公告)日:1999-10-15
申请号:AT95928289
申请日:1995-08-02
Applicant: UNION CARBIDE CHEM PLASTIC , BERNIER ROBERT JOSEPH NOEL , BOYSEN ROBERT LORENZ , BROWN ROBERT CECIL , GOODE MARK GREGORY , MOORHOUSE JOHN HENRY , OLSEN ROBERT DARRELL , SCAROLA LEONARD SEBASTIAN , SPRIGG THOMAS EDWARD , WANG DUAN FAN , WILLIAMS GARY HARRY
Inventor: BERNIER ROBERT JOSEPH NOEL , BOYSEN ROBERT LORENZ , BROWN ROBERT CECIL , GOODE MARK GREGORY , MOORHOUSE JOHN HENRY , OLSEN ROBERT DARRELL , SCAROLA LEONARD SEBASTIAN , SPRIGG THOMAS EDWARD , WANG DUAN-FAN , WILLIAMS GARY HARRY
IPC: B60C1/00 , A61K31/35 , A61K31/352 , A61K31/40 , A61K31/4025 , A61K31/415 , A61K31/425 , A61K31/44 , A61K31/443 , A61K31/4433 , A61K31/50 , A61K31/505 , A61K31/53 , A61P9/00 , B01J8/24 , B01J23/10 , C07D311/58 , C07D311/78 , C07D311/92 , C07D311/94 , C07D405/12 , C07D405/14 , C07D409/14 , C07D417/12 , C07D491/052 , C07D493/04 , C08F2/00 , C08F2/34 , C08F2/44 , C08F4/54 , C08F4/622 , C08F4/64 , C08F4/70 , C08F10/00 , C08F10/14 , C08F36/04 , C08F36/06 , C08F210/00 , C08F210/16 , C08F210/18 , C08K3/04 , C08K3/34
Abstract: Polymers are produced in a stirred bed or gas fluidised bed polymerisation zone of growing polymer particles by (1) introducing a stream of monomer(s), and opt. inert gas(s) or liq(s)., into the polymerisation zone; (2) continuously or intermittently introducing a catalyst; (3) continuously or intermittently withdrawing polymer; and (4) continuously withdrawing unreacted gases, compressing and cooling the gases while maintaining the temp. in the polymerisation zone below the dew pt. of at least one monomer; with the proviso that if there is only one monomer present in the feed stream, an inert gas is also present.
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