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GB1228831A - - Google Patents

Info

Publication number
GB1228831A
GB1228831A GB1228831DA GB1228831A GB 1228831 A GB1228831 A GB 1228831A GB 1228831D A GB1228831D A GB 1228831DA GB 1228831 A GB1228831 A GB 1228831A
Authority
GB
United Kingdom
Prior art keywords
vessel
mixture
catalyst
outlet
reaction mixture
Prior art date
Legal status (The legal status 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 status listed.)
Expired
Application number
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 filed Critical
Publication of GB1228831A publication Critical patent/GB1228831A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18Stationary reactors having moving elements inside
    • B01J19/1812Tubular reactors
    • B01J19/1831Tubular reactors spirally, concentrically or zigzag wound
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18Stationary reactors having moving elements inside
    • B01J19/1812Tubular reactors
    • B01J19/1837Loop-type reactors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J4/00Feed or outlet devices; Feed or outlet control devices
    • B01J4/001Feed or outlet devices as such, e.g. feeding tubes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F36/00Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds
    • C08F36/02Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds the radical having only two carbon-to-carbon double bonds
    • C08F36/04Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds the radical having only two carbon-to-carbon double bonds conjugated
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00051Controlling the temperature
    • B01J2219/00074Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00087Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
    • B01J2219/00094Jackets
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/582Recycling of unreacted starting or intermediate materials

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Polymerisation Methods In General (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

1,228,831. Chemical reaction vessels; polymerization of olefines. MICHELIN & .CIE (COMPAGNIE GENERALE DES ETABS MICHELIN). 1 May, 1968 [2 May, 1967], No. 20677/68. Heading B1X. [Also in Division C3] Chemical reactions, e.g. the polymerization and copolymerization of olefines and/or diolefines, are carried out in a tubular vessel 1 (Fig. 1) forming a closed path between a point 2 where one or more components of the reaction mixture are continuously introduced through inlet 11 into the vessel and a point 3 where the reaction mixture is continuously removed through outlet 25, the mixture flowing through the vessel being separated into doses 5 by balls 6 (e.g. hollow spheres of metal) which are carried through the vessel by the reaction mixture. Intervention stations are provided along the vessel for introducing catalyst, and for withdrawing and/or recycling reaction mixture. For example, catalyst may be introduced at station 12; agitation may be effected by withdrawing mixture through outlet 14 and returning it (together with fresh catalyst or fresh monomer) through inlet 15; at a third station 20 is recycled part of the mixture withdrawn through outlet 21; and at a fourth station 23 is withdrawn a sample for checking purposes. Parts of the tubular vessel 1 are surrounded by jackets 7 for temperature-regulating fluids. The balls 6 are moved from the outlet end of vessel 1 to partition 30 in the bore 27 of block 4 by means of piston 29, which has a hemispherical cavity 33 in its base. Both the pistons 28, 29 then move away from partition 30, liberating a ball which is then entrained by the feed mixture into the inlet of vessel 1. The pistons are actuated automatically. The reaction may be carried out in a cluster of straight parallel tubes 50 (Fig. 2) connected in series by semi-circular bends 60, the various intervention stations being located in the bends, e.g. as at injection point 15. Examples relating to the polymerization of butadiene, and the copolymerization of butadiene and styrene, using heptane as solvent and lithium butyl (with or without hexamethylphosphorotriamide) as catalyst, are given in the specification; and graphs showing the molecular-weight distribution of the products are included.
GB1228831D 1967-05-02 1968-05-01 Expired GB1228831A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR104970A FR1547405A (en) 1967-05-02 1967-05-02 Process and reactor for continuously carrying out chemical reactions, in particular polymerization

Publications (1)

Publication Number Publication Date
GB1228831A true GB1228831A (en) 1971-04-21

Family

ID=8630065

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1228831D Expired GB1228831A (en) 1967-05-02 1968-05-01

Country Status (12)

Country Link
US (1) US3773470A (en)
AT (1) AT289386B (en)
BE (1) BE714005A (en)
CH (1) CH490113A (en)
DK (1) DK137003B (en)
ES (1) ES353414A1 (en)
FR (1) FR1547405A (en)
GB (1) GB1228831A (en)
IL (1) IL29922A (en)
LU (1) LU56003A1 (en)
NL (1) NL143822B (en)
SE (1) SE339934B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112354507A (en) * 2020-11-13 2021-02-12 山东新泽辉新材料科技有限公司 Reaction device for preparing nano magnesium hydroxide fire retardant

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4595566A (en) * 1984-05-30 1986-06-17 Halliburton Company Continuous reactor design
KR0161286B1 (en) * 1989-08-08 1999-01-15 엠. 윌킨스 Polymerization Method and Reactor
DE19539622C1 (en) * 1995-10-16 1997-06-05 Bayer Ag Tubular reactor
US6866786B2 (en) * 1998-04-03 2005-03-15 Symyx Technologies, Inc. Rapid characterization of polymers
US6265226B1 (en) * 1998-04-03 2001-07-24 Symyx Technologies, Inc. Automated sampling methods for rapid characterization of polymers
US6855258B2 (en) * 1999-04-02 2005-02-15 Symyx Technologies, Inc. Methods for characterization of polymers using multi-dimensional liquid chromatography with parallel second-dimension sampling
EP1401570B1 (en) 2001-06-13 2007-08-15 BETA Technologie AG Bulk polymerization reactors and methods for polymerization
US6730228B2 (en) * 2001-08-28 2004-05-04 Symyx Technologies, Inc. Methods and apparatus for characterization of polymers using multi-dimensional liquid chromatography with regular second-dimension sampling
US7507337B2 (en) * 2004-09-03 2009-03-24 Symyx Technologies, Inc. System and method for rapid chromatography with fluid temperature and mobile phase composition control
WO2007080161A1 (en) * 2006-01-13 2007-07-19 Akzo Nobel Coatings International B.V. Loop reactor for emulsion polymerisation
ES2693547T3 (en) 2011-10-14 2018-12-12 Council Of Scientific & Industrial Research Continuous modular reactor
WO2014167506A1 (en) 2013-04-10 2014-10-16 Council Of Scientific & Industrial Research Flow reactor with pinched pipe sections for mixing and heat transfer
US11635054B1 (en) * 2022-08-04 2023-04-25 Wilfred S. Streeter Vertical water pumping system
CN115582086A (en) * 2022-09-30 2023-01-10 宜春科丰新材料有限公司 A continuous reaction device

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2299307A (en) * 1940-02-02 1942-10-20 Cornell Machine Company Method of and apparatus for treating materials
US2478051A (en) * 1944-03-24 1949-08-02 Carl H Nordell Hydraulic air compressor
US2755742A (en) * 1954-11-10 1956-07-24 Stanolind Oil & Gas Co Well pump
US3148037A (en) * 1957-08-09 1964-09-08 George C Szego Repeating chemical reactor apparatus
US3324093A (en) * 1963-10-21 1967-06-06 Phillips Petroleum Co Loop reactor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112354507A (en) * 2020-11-13 2021-02-12 山东新泽辉新材料科技有限公司 Reaction device for preparing nano magnesium hydroxide fire retardant

Also Published As

Publication number Publication date
DK137003C (en) 1978-06-05
IL29922A0 (en) 1969-03-27
DK137003B (en) 1978-01-02
LU56003A1 (en) 1969-02-05
NL6805942A (en) 1968-11-04
IL29922A (en) 1973-03-30
SE339934B (en) 1971-11-01
BE714005A (en) 1968-10-22
CH490113A (en) 1970-05-15
ES353414A1 (en) 1969-10-01
FR1547405A (en) 1968-11-29
DE1767354B2 (en) 1976-06-16
NL143822B (en) 1974-11-15
US3773470A (en) 1973-11-20
AT289386B (en) 1971-04-26
DE1767354A1 (en) 1972-04-20

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
PCNP Patent ceased through non-payment of renewal fee