GB950221A - Improvements in or relating to butadiene polymers - Google Patents

Improvements in or relating to butadiene polymers

Info

Publication number
GB950221A
GB950221A GB3940361A GB3940361A GB950221A GB 950221 A GB950221 A GB 950221A GB 3940361 A GB3940361 A GB 3940361A GB 3940361 A GB3940361 A GB 3940361A GB 950221 A GB950221 A GB 950221A
Authority
GB
United Kingdom
Prior art keywords
titanium
catalyst
alcohol
aluminium
butadiene
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
GB3940361A
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.)
Phillips Petroleum Co
Original Assignee
Phillips Petroleum 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 Phillips Petroleum Co filed Critical Phillips Petroleum Co
Publication of GB950221A publication Critical patent/GB950221A/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
    • C08F136/00Homopolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds
    • C08F136/02Homopolymers 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
    • C08F136/04Homopolymers 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
    • C08F136/06Butadiene
    • 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
    • C08F2410/00Features related to the catalyst preparation, the catalyst use or to the deactivation of the catalyst
    • C08F2410/04Dual catalyst, i.e. use of two different catalysts, where none of the catalysts is a metallocene

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

Butadiene is polymerized using a catalyst comprising (A) an organometallic compound having the formula RnM where M is aluminium, gallium, indium, beryllium, mercury, zinc or cadmium and R is an alkyl, cycloalkyl, aryl, aralkyl or an alkaryl radical containing from 1 to 20 carbon atoms per molecule and n is equal to the valence of M, and (B) a member selected from the group consisting of (1) titanium tetraiodide, and when M is aluminium, (2) mixtures of titanium tetraiodide and titanium tetrachloride and (3) iodine and a titanium halide TiX4 where X is chlorine or bromine. The butadiene is contacted with (A) to form an admixture therewith and then the admixture is contacted with incremental amounts of the (B) component. The term "incremental" covers either stepwise or continuous addition. Long lists of suitable catalyst components are given. The polymerization is usually carried out in a diluent, lists of which are given. In a batch process, the reaction mixture is inactivated by treating with an alcohol or water and the polymer is then separated and may be further purified. In a continuous process the total effluent is pumped to a catalyst-in-activating zone where an alcohol, for example, is added. If necessary a precipitating agent may then be added and the polymer separated from the diluent and alcohol which may be re-used after being fractionally distilled. A polybutadiene having a cis-content of 85 to 98% or higher may be produced. In the example the catalyst is triisobutyl aluminium, titanium tetraiodide and titanium tetrachloride and the solvent is toluene.
GB3940361A 1960-12-19 1961-11-03 Improvements in or relating to butadiene polymers Expired GB950221A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US7689360A 1960-12-19 1960-12-19

Publications (1)

Publication Number Publication Date
GB950221A true GB950221A (en) 1964-02-19

Family

ID=22134810

Family Applications (1)

Application Number Title Priority Date Filing Date
GB3940361A Expired GB950221A (en) 1960-12-19 1961-11-03 Improvements in or relating to butadiene polymers

Country Status (1)

Country Link
GB (1) GB950221A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4699960A (en) * 1985-07-01 1987-10-13 Enichem Elastomeri, S.P.A. Process for the polymerization or copolymerization of butadiene

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4699960A (en) * 1985-07-01 1987-10-13 Enichem Elastomeri, S.P.A. Process for the polymerization or copolymerization of butadiene

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