Claims
- 1. A method for producing chlorosulfonated polyethylene with controlled addition of the amount of sulfur of the chlorosulfonated polyethylene comprising the step of chlorinating and chlorosulfonating polyethylene dissolved in halogenated hydrocarbon with a chlorinating and chlorosulfonating agent consisting of sulfuryl chloride at a reaction pressure of 1.2 to 6.5 kg/cm.sup.2 gauge pressure in the presence of a catalyst of a radical generating agent and in a binary phase system, wherein the addition amount of sulfur is controlled by adding an amine compound in a range defined by the following formula (1)
- log.sub.10 S=.alpha..multidot.log.sub.10 A+.beta. formula (1)
- wherein S denotes reaction yield (%) of sulfur of sulfuryl chloride, A denotes concentration (mol/liter) of the amine compound in halogenated hydrocarbon solvent, and .alpha.,.beta. denote constant numbers, respectively being 1.0<.alpha.<3.0 and 4.0<.beta.<12.0, and wherein the amine compound is selected from the group consisting of pyridine and quinoline, the amount of the amine compound being from at least a trace amount up to about 3.5.times.10.sup.-4 mol/liter.
- 2. The method for producing chlorosulfonated polyethylene recited in claim 1, wherein separated amount of the amine compound is successively added with progress of the reaction.
- 3. The method for producing chlorosulfonated polyethylene recited in claim 1, wherein the reaction temperature is 85.degree. to 130.degree. C.
- 4. The method of producing chlorosulfonated polyethylene recited in claim 1, wherein total amount of the amine compound is collectively added prior to start of the reaction.
- 5. The method for producing chlorosulfonated polyethylene recited in claim 1, wherein the polyethylene is used in an amount of 5 to 30 wt % to the halogenated hydrocarbon solvent.
- 6. The method for producing chlorosulfonated polyethylene recited in claim 1, wherein the polyethylene is at least one selected from the group consisting of high density polyethylene, low density polyethylene, linear low density polyethylene and ethylene copolymer such as ethylene-vinylacetate copolymer.
- 7. The method for producing chlorosulfonated polyethylene recited in claim 1, wherein the halogenated hydrocarbon used as the solvent is a halogenated aliphatic hydrocarbon and/or a halogenated aromatic hydrocarbon.
- 8. The method for producing chlorosulfonated polyethylene recited in claim 1, wherein an epoxy compound of a stabilizer is added into the resultant polymer solution.
- 9. The method for producing chlorosulfonated polyethylene recited in claim 1, wherein the radical generating agent is at least one selected from the group consisting of azo compounds and organic peroxides.
- 10. The method for producing chlorosulfonated polyethylene recited in claim 1, wherein the radical generating agent is used in an amount of not more than one weight part per 100 weight parts of the used polyethylene.
Priority Claims (1)
Number |
Date |
Country |
Kind |
57-142075 |
Aug 1982 |
JPX |
|
Parent Case Info
This application is a continuation-in-part of application Ser. No. 522,579, filed Aug. 12, 1983, now abandoned.
US Referenced Citations (2)
Foreign Referenced Citations (4)
Number |
Date |
Country |
33-7838 |
Sep 1958 |
JPX |
39-12113 |
Jun 1964 |
JPX |
56-76406 |
Jun 1981 |
JPX |
879963 |
Oct 1961 |
GBX |
Continuation in Parts (1)
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Number |
Date |
Country |
Parent |
522579 |
Aug 1983 |
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