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公开(公告)号:ZA907745B
公开(公告)日:1991-07-31
申请号:ZA907745
申请日:1990-09-27
Applicant: UNION CARBIDE CHEM PLASTIC
Inventor: RHEE SEUNG JOON , SEUNG JOON RHEE , EDWARDS DAVID NICHOLAS , KAROL FREDERICK JOHN , DAVID NICHOLAS EDWARDS , FREDERICK JOHN KAROL , MOORHOUSE JOHN HENRY , JOHN HENRY MOORHOUSE , BAKER EDGAR CHAPMAN , LEE KIU HEE , KIU HEE LEE , EDGAR CHAPMAN BAKER , SCAROLA LEONARD SEBASTIAN , LEONARD SEBASTIAN SCAROLA
IPC: C08F2/34 , C08F2/44 , C08F32/00 , C08F36/00 , C08F136/06 , C08F210/16 , C08F210/18 , C08F232/08 , C08F293/00 , C08F297/08 , B01J , 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:PT95453A
公开(公告)日:1991-05-22
申请号:PT9545390
申请日:1990-09-27
Applicant: UNION CARBIDE CHEM PLASTIC
Inventor: LEE KIU HEE , RHEE SEUNG JOON , BAKER EDGAR CHAMPMAN , EDWARDS DAVID NICHOLAS , 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 , C09J123/16 , C08L23/16
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:BR9911394A
公开(公告)日:2001-03-13
申请号:BR9911394
申请日:1999-06-25
Applicant: UNION CARBIDE CHEM PLASTIC
IPC: B29B7/90 , B29B9/12 , C08K3/00 , C08L101/00
Abstract: There is provided a method which reduces fines while maintaining the bulk handling advantages of granular or particulate elastomers such as those produced in gas phase processes and which affords continuous bulk handling of synthetic rubbers or elastomers such as those produced in solution and/or suspension processes. The method comprises (1) feeding an crumb form elastomer or a granular elastomer which contains fines along with optionally one or more filler materials to a mixer/extruder where it is masticated and melted into a compound; (2) pumping the compound through an orifice of the mixer/extruder, and (3) cutting and forming the compound into shaped pellets ranging in size from about 0.5 to 30 mm.
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公开(公告)号:BR9804297A
公开(公告)日:2000-03-08
申请号:BR9804297
申请日:1998-10-27
Applicant: UNION CARBIDE CHEM PLASTIC
Inventor: KHANIN DAVID , SCAROLA LEONARD SEBASTIAN
Abstract: A process for the devolatilization of a thermoplastic polymer containing gaseous impurities in an apparatus having a melting zone, a mixing zone, and a reduced pressure zone, comprising: (a) (i) adding a granular blowing agent directly or via a masterbatch to the polymer prior to the introduction of the polymer into the melting zone, said blowing agent being added in an amount of about 1 to about 4 percent by weight based on the weight of the polymer or (ii) adding a gaseous blowing agent to the mixing zone; (b) melting the polymer in the melting zone; (c) mixing the molten polymer and blowing agent in the mixing zone under sufficient pressure to maintain the blowing agent in the mixture; (d) at a temperature sufficient for decomposition or expansion, (i) decomposing the granular blowing agent in the mixing zone and/or in the reduced pressure zone or (ii) expanding the gaseous blowing agent in the reduced pressure zone wherein the blowing agent in its decomposed or expanded state develops froth cells in the molten polymer; (e) in the reduced pressure zone, reducing the pressure at the surface of the molten polymer in a sufficient amount to remove essentially all of the gaseous impurities; (f) optionally, repeating steps (c), (d), and (e) at least once; and (g) recovering the polymer in an essentially unfoamed state. e
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公开(公告)号:BR9713365A
公开(公告)日:2000-01-25
申请号:BR9713365
申请日:1997-12-03
Applicant: UNION CARBIDE CHEM PLASTIC
Abstract: The present invention provides a process and apparatus for feeding powders such as fine, cohesive, or powdery particulate materials from a low pressure system to a high pressure system. There is provided in a preferred embodiment a process and apparatus of pressurizing and feeding carbon black fluff to a polymerization reactor, particularly a gas phase fluidized polymerization reactor to provide for a close-coupling of a carbon black reactor to a polymerization reactor.
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公开(公告)号:HUT76682A
公开(公告)日:1997-10-28
申请号:HU9700332
申请日:1995-08-02
Applicant: UNION CARBIDE CHEM PLASTIC
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: A61K31/35 , A61K31/352 , A61K31/40 , B60C1/00 , 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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公开(公告)号:ZA969737B
公开(公告)日:1997-06-18
申请号:ZA969737
申请日:1996-11-20
Applicant: UNION CARBIDE CHEM PLASTIC
Inventor: BERNIER ROBERT JOSEPH NOEL , ITALIAANDER ERIC THOMAS , PAEGLIS ARNIS UVI , ROZENBLAT BENJAMIN ROMAN , SCAROLA LEONARD SEBASTIAN , ARDHENOU SEN
IPC: B29C20060101 , C08J20060101 , C08K20060101 , C08J , B29C , C08K
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公开(公告)号:CZ32097A3
公开(公告)日:1997-06-11
申请号:CZ32097
申请日:1995-08-02
Applicant: UNION CARBIDE CHEM PLASTIC
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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公开(公告)号:CA2190678A1
公开(公告)日:1997-05-23
申请号:CA2190678
申请日:1996-11-19
Applicant: UNION CARBIDE CHEM PLASTIC
Inventor: BERNIER ROBERT JOSEPH NOEL , ITALIAANDER ERICH THOMAS , PAEGLIS ARNIS UVI , ROZENBLAT BENJAMIN ROMAN , SCAROLA LEONARD SEBASTIAN , SEN ARDHENDU
IPC: B29B7/42 , B29C47/00 , C08J3/00 , C08J3/20 , C08L23/00 , C08L101/00 , B29C35/02 , C08J3/24 , B29B7/76
Abstract: The present invention provides a continuous process for compounding one or more polymers and finished articles thereof. The process comprises continuously feeding at least one granular elastomer optionally with one or more thermoplastic polymers having average particle sizes of about 5mm or smaller and with optionally one or more additives to a continuous mixer where the components are masticated and melted into a compound and pumping said compound through an orifice or die.
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公开(公告)号:NO970464L
公开(公告)日:1997-03-21
申请号:NO970464
申请日:1997-02-03
Applicant: UNION CARBIDE CHEM PLASTIC
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: 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
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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