GB883850A - Process for controlling the molecular weight of vinylidene chloride polymers - Google Patents
Process for controlling the molecular weight of vinylidene chloride polymersInfo
- Publication number
- GB883850A GB883850A GB3280760A GB3280760A GB883850A GB 883850 A GB883850 A GB 883850A GB 3280760 A GB3280760 A GB 3280760A GB 3280760 A GB3280760 A GB 3280760A GB 883850 A GB883850 A GB 883850A
- Authority
- GB
- United Kingdom
- Prior art keywords
- per cent
- vinylidene chloride
- carbon
- perhalomethane
- methane
- 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
Links
Classifications
-
- 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
- C08F214/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen
- C08F214/02—Monomers containing chlorine
- C08F214/04—Monomers containing two carbon atoms
- C08F214/08—Vinylidene chloride
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Polymerisation Methods In General (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
A process for producing relatively low molecular weight copolymers of vinylidene and vinyl chlorides, containing at least 70 weight per cent of vinylidene chloride, comprises polymerizing the monomers in the presence of from 5,0 to 0,05 weight per cent of a perhalomethane chain-stopper having the general formula Y-C-X3 wherein Y is bromine or iodine and X is any halogen atom. Specified perhalomethanes are carbon tetrabromide, bromotrichloromethane, dibrodichloromethane, chlorotribromomethane, bromotrifluoromethane, dibromodifluoromethane, fluorotribromomethane, bromochlorodifluoromethane, carbon tetraiodide, bromotriiodomethane, dibromodiiodomethane, iodotribromomethane, chlorotriiodomethane, dichlorodiiodomethane, iodotrichloromethane, fluorotriiodomethane, difluorodiiodomethane and iodotrifluoromethane. Any known polymerization technique may be employed, but aqueous suspension using a water-dispersible granulating agent, such as a water-soluble cellulose ether, is preferred. The perhalomethane is preferably added to the monomer charge before dispersion in the aqueous phase. In examples, 68 parts of vinylidene chloride and 12 parts of vinyl chloride are copolymerized, using methyl cellulose as suspending agent and lauroyl peroxide as catalyst, in the presence of various chain-transfer agents. The effect of several of the above specified perhalomethanes on the per cent conversion and solution viscosity is compared with that of the following previously known chain-transfer agents: lauryl mercaptan, carbon tetrachloride, chlorodibromo methane, bromochloro methane and bromoform. Another example shows the effect of different amounts of carbon tetrabromide on the solution viscosity obtained in the above polymerization at 80% conversion.ALSO:A process for producing relatively low molecular weight copolymers of vinylidene and vinyl chlorides, containing at least 70 weight per cent of vinylidene chloride, comprises polymerising the monomers in the presence of from 5.0 to 0.05 weight per cent of a perhalomethane chainstopper having the general formula Y-C-X3 wherein Y is bromine or iodine and X is any halogen atom. Specified perhalo methanes are carbon tetrabromide, bromotrichloromethane, dibrodichloromethane, chlorotribromomethane, bromotrifluoromethane, dibromodifluoromethane, fluorotribromomethane, bromochlorodifluoromethane, carbon tetraiodide, bromotriiodomethane, dibromodiiodomethane, iodotribromomethane, chlorotriiodomethane, dichlorodiiodomethane, iodotrichloromethane, fluorotriiodomethane, difluorodiiodomethane and iodotrifluoromethane. Any known polymerisation technique may be employed but aqueous suspension using a water-dispersible granulating agent such as a water-soluble cellulose ether is preferred. The perhalomethane is preferably added to the monomer charge before dispersion in the aqueous phase. In examples 68 parts of vinylidene chloride and 12 parts of vinyl chloride are copolymerised, using methyl cellulose as suspendihg agent and lauroyl peroxide as catalyst, in the presence of various chain-transfer agents. The effect of several of the above specified perhalomethanes on the per cent conversion and solution viscosity is compared with that of the following previously known chain-transfer agents: lauryl mercaptan, carbon tetrachloride, chlorodibromo methane, bromochloro methane and bromoform. Another example shows the effect of different amounts of carbon tetrabromide on the solution viscosity obtained in the above polymerisation at 80% conversion.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3280760A GB883850A (en) | 1960-09-23 | 1960-09-23 | Process for controlling the molecular weight of vinylidene chloride polymers |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3280760A GB883850A (en) | 1960-09-23 | 1960-09-23 | Process for controlling the molecular weight of vinylidene chloride polymers |
Publications (1)
Publication Number | Publication Date |
---|---|
GB883850A true GB883850A (en) | 1961-12-06 |
Family
ID=10344279
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB3280760A Expired GB883850A (en) | 1960-09-23 | 1960-09-23 | Process for controlling the molecular weight of vinylidene chloride polymers |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB883850A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3937690A (en) * | 1972-06-19 | 1976-02-10 | Dynamit Nobel Aktiengesellschaft | Process for the preparation of thermoplastically workable fluoro-olefin polymers |
US4000356A (en) * | 1972-06-19 | 1976-12-28 | Dynamit Nobel Aktiengesellschaft | Process for the preparation of thermoplastically workable fluoro-olefin polymers |
US5003014A (en) * | 1990-05-21 | 1991-03-26 | Gaf Chemicals Corporation | Process for making copolymers of maleic anhydride and a C1 -C4 alkyl vinyl ether having a predetermined specific viscosity |
-
1960
- 1960-09-23 GB GB3280760A patent/GB883850A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3937690A (en) * | 1972-06-19 | 1976-02-10 | Dynamit Nobel Aktiengesellschaft | Process for the preparation of thermoplastically workable fluoro-olefin polymers |
US4000356A (en) * | 1972-06-19 | 1976-12-28 | Dynamit Nobel Aktiengesellschaft | Process for the preparation of thermoplastically workable fluoro-olefin polymers |
US5003014A (en) * | 1990-05-21 | 1991-03-26 | Gaf Chemicals Corporation | Process for making copolymers of maleic anhydride and a C1 -C4 alkyl vinyl ether having a predetermined specific viscosity |
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