GB1121885A - Modified bulk polymerisation process - Google Patents

Modified bulk polymerisation process

Info

Publication number
GB1121885A
GB1121885A GB941466A GB941466A GB1121885A GB 1121885 A GB1121885 A GB 1121885A GB 941466 A GB941466 A GB 941466A GB 941466 A GB941466 A GB 941466A GB 1121885 A GB1121885 A GB 1121885A
Authority
GB
United Kingdom
Prior art keywords
mixture
polymer
styrene
acrylonitrile
diluent
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
GB941466A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dart Industries Inc
Original Assignee
Rexall Drug and Chemical Co
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 Rexall Drug and Chemical Co filed Critical Rexall Drug and Chemical Co
Publication of GB1121885A publication Critical patent/GB1121885A/en
Expired legal-status Critical Current

Links

Classifications

    • 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
    • C08F279/00Macromolecular compounds obtained by polymerising monomers on to polymers of monomers having two or more carbon-to-carbon double bonds as defined in group C08F36/00
    • C08F279/02Macromolecular compounds obtained by polymerising monomers on to polymers of monomers having two or more carbon-to-carbon double bonds as defined in group C08F36/00 on to polymers of conjugated dienes

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Graft Or Block Polymers (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

Acrylonitrile and a monovinyl aromatic compound are grafted on to a rubber by a process comprising (a) polymerizing with vigorous agitation in an initial polymerization zone a mixture comprising 39 to 93.1% by weight of a monovinyl aromatic compound which is styrene, an alkyl- or halogen-substituted styrene or a mixture thereof, 4-9 to 26% of acrylonitrile, 2 to 30% of rubber and 0 to 5% of additives at 60 DEG to 140 DEG C. until 10 to 45% conversion of the initial monomers to polymer is obtained; (b) passing the resulting mixture to at least one additional zone wherein said mixture is further polymerized at a temperature up to 220 DEG C. until 85 to 100% conversion of monomers to polymer is obtained; (c) passing the resulting polymer to a devolatilization zone wherein said polymer is heated to a temperature of 80 DEG to 240 DEG C. under a pressure of 0 to 760 mm. Mg abs. and (d) recovering said devolatilized polymer, during which process from 3 to 30% of an alkyl aromatic diluent having a boiling point of 100 DEG to 200 DEG C. is added to the polymerizable mixture at step (a) or step (b), the per cent by weight of said diluent being based on the weight of the total reaction mixture. Styrene, preferably together with a minor amount of alphamethyl styrene is the preferred monovinyl aromatic compound. The preferred diluent is ethyl benzene, which may be used together with another chain regulator, e.g. tert.-dodecyl mercaptan. The polymerization may be carried out in the presence of lubricants and antioxidants, e.g. the mineral oil, trisnonylphenyl phosphite and 2,6-ditert.-butyl methylphenol used in the examples, in which styrene and acrylonitrile are grafted on to polybutadiene.
GB941466A 1965-03-12 1966-03-03 Modified bulk polymerisation process Expired GB1121885A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US43939065A 1965-03-12 1965-03-12

Publications (1)

Publication Number Publication Date
GB1121885A true GB1121885A (en) 1968-07-31

Family

ID=23744523

Family Applications (1)

Application Number Title Priority Date Filing Date
GB941466A Expired GB1121885A (en) 1965-03-12 1966-03-03 Modified bulk polymerisation process

Country Status (2)

Country Link
DE (1) DE1645196A1 (en)
GB (1) GB1121885A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4837150B1 (en) * 1969-10-22 1973-11-09
FR2436795A1 (en) * 1978-08-21 1980-04-18 Konsetov Vitaly ABS continuous prodn. by bulk graft polymerisation - using forced circulation to maintain constant temp. to give uniform prod.
EP0042985A2 (en) * 1980-06-25 1982-01-06 BASF Aktiengesellschaft Process for the preparation of vinylaromatic polymers modified by rubbers
EP0046502A1 (en) * 1980-08-27 1982-03-03 BASF Aktiengesellschaft Process for the preparation of vinylaromatic polymers modified by rubbers
FR2535727A1 (en) * 1982-11-04 1984-05-11 Mitsui Toatsu Chemicals CONTINUOUS PROCESS FOR PRODUCING HIGH IMPACT RESISTANCE RESINS, MODIFIED BY RUBBER
EP0113067A1 (en) * 1982-12-08 1984-07-11 BASF Aktiengesellschaft Process for the preparation of impact-resistant vinyl-aromatic polymers
CN111378073A (en) * 2020-04-09 2020-07-07 北方华锦化学工业股份有限公司 Process method for preparing high-fluidity low-gloss ABS resin by continuous bulk method

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4837150B1 (en) * 1969-10-22 1973-11-09
FR2436795A1 (en) * 1978-08-21 1980-04-18 Konsetov Vitaly ABS continuous prodn. by bulk graft polymerisation - using forced circulation to maintain constant temp. to give uniform prod.
EP0042985A2 (en) * 1980-06-25 1982-01-06 BASF Aktiengesellschaft Process for the preparation of vinylaromatic polymers modified by rubbers
EP0042985A3 (en) * 1980-06-25 1982-02-24 Basf Aktiengesellschaft Process for the preparation of vinylaromatic polymers modified by rubbers
EP0046502A1 (en) * 1980-08-27 1982-03-03 BASF Aktiengesellschaft Process for the preparation of vinylaromatic polymers modified by rubbers
FR2535727A1 (en) * 1982-11-04 1984-05-11 Mitsui Toatsu Chemicals CONTINUOUS PROCESS FOR PRODUCING HIGH IMPACT RESISTANCE RESINS, MODIFIED BY RUBBER
US4587294A (en) * 1982-11-04 1986-05-06 Mitsui Toatsu Chemicals, Inc. Continuous process for producing rubber modified high-impact resins
EP0113067A1 (en) * 1982-12-08 1984-07-11 BASF Aktiengesellschaft Process for the preparation of impact-resistant vinyl-aromatic polymers
CN111378073A (en) * 2020-04-09 2020-07-07 北方华锦化学工业股份有限公司 Process method for preparing high-fluidity low-gloss ABS resin by continuous bulk method

Also Published As

Publication number Publication date
DE1645196A1 (en) 1970-05-21

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