AR001029A1 - Proceso para la polimerizacion de olefinas en fase gaseosa. - Google Patents

Proceso para la polimerizacion de olefinas en fase gaseosa.

Info

Publication number
AR001029A1
AR001029A1 ARP960101516A AR10151696A AR001029A1 AR 001029 A1 AR001029 A1 AR 001029A1 AR P960101516 A ARP960101516 A AR P960101516A AR 10151696 A AR10151696 A AR 10151696A AR 001029 A1 AR001029 A1 AR 001029A1
Authority
AR
Argentina
Prior art keywords
polymer
olefins
lock hopper
reactor
polymerization
Prior art date
Application number
ARP960101516A
Other languages
English (en)
Original Assignee
Bp Chem Int Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Bp Chem Int Ltd filed Critical Bp Chem Int Ltd
Publication of AR001029A1 publication Critical patent/AR001029A1/es

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1809—Controlling processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J3/00—Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
    • B01J3/02—Feed or outlet devices therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
    • B01J8/003—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor in a downward flow
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
    • B01J8/0035—Periodical feeding or evacuation
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00—Processes of polymerisation
    • C08F2/34—Polymerisation in gaseous state
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00256—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles in a heat exchanger for the heat exchange medium separate from the reactor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
    • B01J2208/00274—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant vapours
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
    • B01J2208/00292—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant solids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00743—Feeding or discharging of solids
    • B01J2208/00761—Discharging
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S526/00—Synthetic resins or natural rubbers -- part of the class 520 series
    • Y10S526/901—Monomer polymerized in vapor state in presence of transition metal containing catalyst

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Polymerisation Methods In General (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

La presente invención se relaciona con un proceso para la polimerización contínua en fase gaseosa de una o más olefinas en un reactor de lechofluidificado y/o mecánicamente agitado, que comprende una etapa para extraer el polímero fuera delreacto r, en donde una porción del lecho se transfiere alinterior de una tolva de esclusa y se aisla entonces del reactor, en la tolva de esclusa, durante un período de 5 a 120 segundos, de manera que polimerizauna cantidad sustancial de laolefina u olef inas en dicha porción, antes que el polímero así aislado en dicha porción se descargue fuera de la tolva deesclusa. El proceso reduce ventajosamente la cantidad de gas extraído con el polímero que ha de reciclarse al interior delreactor y mejora ladesgasificación del polímero mediante el calor de la reacción de polimerización durante el período de aislamiento en la tolva de esclusa.
ARP960101516A 1995-02-24 1996-02-23 Proceso para la polimerizacion de olefinas en fase gaseosa. AR001029A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR9502447A FR2731000B1 (fr) 1995-02-24 1995-02-24 Procede de polymerisation d'olefine en phase gazeuse

Publications (1)

Publication Number Publication Date
AR001029A1 true AR001029A1 (es) 1997-08-27

Family

ID=9476672

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP960101516A AR001029A1 (es) 1995-02-24 1996-02-23 Proceso para la polimerizacion de olefinas en fase gaseosa.

Country Status (29)

Country Link
US (1) US5633333A (es)
EP (1) EP0728772B1 (es)
JP (1) JP3749750B2 (es)
KR (1) KR100388326B1 (es)
CN (1) CN1097599C (es)
AR (1) AR001029A1 (es)
AT (1) ATE175683T1 (es)
AU (1) AU690002B2 (es)
BG (1) BG62444B1 (es)
BR (1) BR9600799A (es)
CA (1) CA2170101A1 (es)
CZ (1) CZ53596A3 (es)
DE (1) DE69601313T2 (es)
DZ (1) DZ1992A1 (es)
EA (1) EA000026B1 (es)
EG (1) EG20742A (es)
ES (1) ES2126980T3 (es)
FI (1) FI119936B (es)
FR (1) FR2731000B1 (es)
GR (1) GR3029452T3 (es)
HU (1) HU216912B (es)
NO (1) NO309147B1 (es)
NZ (1) NZ286042A (es)
PL (1) PL312898A1 (es)
RO (1) RO115167B1 (es)
SK (1) SK281758B6 (es)
TR (1) TR199600122A2 (es)
TW (1) TW360664B (es)
ZA (1) ZA961299B (es)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2730999B1 (fr) * 1995-02-24 1997-04-18 Bp Chemicals Snc Appareillage et procede de polymerisation d'olefine en phase gazeuse
FR2752533B1 (fr) * 1996-08-23 1998-09-18 Bp Chemicals Snc Appareillage et procede de polymerisation d'olefine en phase gazeuse
US6642316B1 (en) 1998-07-01 2003-11-04 Exxonmobil Chemical Patents Inc. Elastic blends comprising crystalline polymer and crystallizable polym
DE19922677C1 (de) 1999-05-18 2001-04-19 Elenac Gmbh Verfahren zum Trocknen und Entgasen von Polyolefinen und nach diesem Verfahren hergestelltes Polyethylen
DE19948280A1 (de) * 1999-10-06 2001-04-12 Elenac Gmbh Gasphasenpolymerisationsverfahren
ATE485319T1 (de) 2001-04-12 2010-11-15 Exxonmobil Chem Patents Inc Verfahren zur polymerisation von propylen und ethylen in lösung
US6914104B2 (en) * 2002-04-19 2005-07-05 Sumitomo Chemical Company, Limited Process for polymerization of α-olefin
JP2003313205A (ja) * 2002-04-19 2003-11-06 Sumitomo Chem Co Ltd ポリオレフィン重合方法
CN101107066B (zh) * 2005-01-26 2010-06-09 英尼奥斯欧洲有限公司 从气相聚合反应器中取出聚合物的装置和方法
EP2743278A1 (en) * 2012-12-11 2014-06-18 Basell Polyolefine GmbH Process for degassing and buffering polyolefin particles obtained by olefin polymerization
JP2024079210A (ja) 2022-11-30 2024-06-11 住友化学株式会社 オレフィン重合反応装置

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR381364A (fr) * 1907-06-07 1908-01-10 George Ellison Dispositifs destinés à la protection des moteurs d'induction à courant alternatif
US3785966A (en) * 1971-04-08 1974-01-15 Agency Ind Science Techn Method for discharging particulate solid from high pressure vessel
AU576409B2 (en) * 1984-12-31 1988-08-25 Mobil Oil Corporation Fluidized bed olefin polymerization process
FR2642429B1 (fr) * 1989-01-31 1991-04-19 Bp Chimie Sa Procede et appareil de polymerisation d'olefines en phase gazeuse dans un reacteur a lit fluidise
US5200477A (en) * 1991-02-22 1993-04-06 Union Carbide Chemicals & Plastics Technology Corporation Process for producing sticky polymers
FR2693730B1 (fr) * 1992-07-16 1994-09-30 Bp Chemicals Snc Réacteur à lit fluidisé et procédé de soutirage.
US5543478A (en) * 1992-12-29 1996-08-06 Nippon Petrochemicals Company, Limited Method for operating reactor for polymerizing olefins
JP3077940B2 (ja) * 1993-04-26 2000-08-21 エクソン・ケミカル・パテンツ・インク 流動層重合法のための安定な操作条件を決定する方法
FR2730999B1 (fr) * 1995-02-24 1997-04-18 Bp Chemicals Snc Appareillage et procede de polymerisation d'olefine en phase gazeuse

Also Published As

Publication number Publication date
US5633333A (en) 1997-05-27
KR100388326B1 (ko) 2003-09-13
FI960854A (fi) 1996-08-25
ES2126980T3 (es) 1999-04-01
AU690002B2 (en) 1998-04-09
JPH08253517A (ja) 1996-10-01
TR199600122A2 (tr) 1996-10-21
GR3029452T3 (en) 1999-05-28
CN1138049A (zh) 1996-12-18
HU9600435D0 (en) 1996-04-29
EA199600005A2 (ru) 1996-07-01
SK281758B6 (sk) 2001-07-10
BR9600799A (pt) 1997-12-23
DZ1992A1 (fr) 2002-10-15
CN1097599C (zh) 2003-01-01
ATE175683T1 (de) 1999-01-15
HUP9600435A2 (en) 1997-04-28
DE69601313D1 (de) 1999-02-25
DE69601313T2 (de) 1999-05-27
EG20742A (en) 1999-12-29
JP3749750B2 (ja) 2006-03-01
NO960738L (no) 1996-08-26
EP0728772B1 (en) 1999-01-13
SK23196A3 (en) 1997-03-05
AU4448596A (en) 1996-09-05
EA199600005A3 (ru) 1996-12-30
NO960738D0 (no) 1996-02-23
BG100383A (bg) 1996-11-29
PL312898A1 (en) 1996-09-02
HUP9600435A3 (en) 1997-11-28
EA000026B1 (ru) 1998-02-26
FI119936B (fi) 2009-05-15
EP0728772A1 (en) 1996-08-28
CZ53596A3 (en) 1996-09-11
FI960854A0 (fi) 1996-02-23
RO115167B1 (ro) 1999-11-30
ZA961299B (en) 1997-08-19
TW360664B (en) 1999-06-11
HU216912B (hu) 1999-10-28
KR960031492A (ko) 1996-09-17
CA2170101A1 (en) 1996-08-25
NO309147B1 (no) 2000-12-18
BG62444B1 (bg) 1999-11-30
FR2731000B1 (fr) 1997-04-18
FR2731000A1 (fr) 1996-08-30
NZ286042A (en) 1997-07-27

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