# US 5,350,809 A · Preparation process of chlorinated rubber > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 5,350,809 A - Document ID: US5350809A - Status: Granted - Kind: A - Application number: 08/006,315 - Filed: 1993-01-22 - Granted: 1994-09-27 - Earliest claimed: 1992-03-31 - Assignees: Asahi Denka Kogyo Kabushiki Kaisha - Inventors: Hiroshi Tsuchiya; Makoto Kokura; Yutaka Ozawa; Takaaki Sugimura - Web page: https://patentgrep.com/patent/US5350809A ## CPC - C08C 19/14: by reaction with halogens - C08C: TREATMENT OR CHEMICAL MODIFICATION OF RUBBERS ## Abstract Disclosed herein is a process for the preparation of a chlorinated rubber, wherein chlorine gas is caused to act on a polyisoprene rubber to prepare the chlorinated rubber. Chlorine gas is blown into a high-acidity aqueous dispersion of the polyisoprene rubber to chlorinate the polyisoprene rubber, whereby a chlorinated isoprene rubber with high performance is prepared stably in an aqueous medium. ## Claims ### Claim 1 A process for the preparation of a chlorinated rubber wherein chlorine gas is reacted with a polyisoprene rubber to form a chlorinated rubber, the improvement comprising: preparing an aqueous dispersion of said polyisoprene rubber; preparing an aqueous acid solution having a high concentration of acid; adding said aqueous dispersion of polyisoprene rubber dropwise into said aqueous acid solution while blowing chlorine gas into the said aqueous acid solution, thereby chlorinating said polyisoprene rubber and forming a chlorinated rubber product. ### Claim 2 (depends on 1) The process as claimed in claim 1, wherein the polyisoprene rubber is natural rubber or a synthetic polyisoprene rubber having a Mooney viscosity (ML.sub.1+4, 100.degree. C.) of 20-100. ### Claim 3 (depends on 1) The process as claimed in claim 1, wherein the acid is hydrochloric acid, sulfuric acid, nitric acid or a mixture of at least two acids thereof. ### Claim 4 (depends on 1) The process as claimed in claim 1, wherein the aqueous solution of the acid in the high concentration is an aqueous solution having an acid concentration higher than 2 wt. % but not higher than 40 wt. %. ### Claim 5 (depends on 1) The process as claimed in claim 1, wherein the aqueous solution of the acid in the high concentration is an aqueous solution having an acid concentration of 5-36 wt. %. ### Claim 6 (depends on 1) The process as claimed in claim 1, wherein an aqueous dispersion composed of a natural rubber latex with the surface active agent added thereto is added dropwise into the aqueous solution of the acid in the high concentration, said aqueous solution having an acid concentration higher than 2 wt. % but not higher than 36 wt. %. ### Claim 7 (depends on 6) The process as claimed in claim 6, wherein the surface active agent is a nonionic or nonionic-anionic surface active agent. ### Claim 8 (depends on 1) The process as claimed in claim 1, wherein an average particle size of the polyisoprene rubber in the aqueous dispersion is 100 .mu.m or smaller. ### Claim 9 (depends on 1) The process as claimed in claim 1, which comprises initiating a chlorination reaction by using a radical initiator, irradiating active rays, or combining both means thereof, and conducting chlorination under conditions of a reaction temperature of 0.degree.-90.degree. C. and a reaction time of 2-20 hours. ### Claim 10 (depends on 1) The process as claimed in claim 1, which comprises conducting chlorination until the concentration of chlorine in the resultant chlorinated rubber reaches 55-75 wt. %. ### Claim 11 A process for the preparation of a chlorinated rubber wherein chlorine gas is reacted with a polyisoprene rubber to form a chlorinated rubber, the improvement comprising: preparing an aqueous dispersion of said polyisoprene rubber; preparing an aqueous acid solution having an acid concentration between about 2 wt. % and 40 wt. %; dropwise adding or spraying said aqueous dispersion of polyisoprene rubber into said aqueous acid solution while blowing chlorine gas into said aqueous acid solution, thereby chlorinating said polyisoprene rubber and forming a chlorinated rubber product. ### Claim 12 (depends on 11) The process as claimed in claim 11 wherein an average particle size of said polyisoprene rubber in the aqueous dispersion is 100 .mu.m or smaller. ### Claim 13 (depends on 11) The process as claimed in claim 11 wherein the chlorination is initiated by using a radical initiator, irradiating active rays, or combining both means thereof, and conducting chlorination under conditions of a reaction temperature of 0.degree.-90.degree. C. and a reaction time of 2-20 hours. ### Claim 14 A process for the preparation of a chlorinated rubber wherein chlorine gas is reacted with a polyisoprene rubber to form a chlorinated rubber, the improvement comprising: preparing an aqueous dispersion of said polyisoprene rubber; preparing an aqueous acid solution having an acid concentration between about 2 wt. % and 40 wt. %; adding said aqueous dispersion of polyisoprene rubber into said aqueous acid solution in a manner such that no aggregation of the polyisoprene rubber particles occurs and wherein the average particle size of said polyisoprene rubber in the aqueous dispersion is 100.mu.m or smaller, while blowing chlorine gas into said aqueous acid solution, thereby chlorinating said polyisoprene rubber and forming a chlorinated rubber product. ### Claim 15 (depends on 14) The process as claimed in claim 14 which comprises conducting chlorination until the concentration of chlorine in the resultant chlorinated rubber reaches 55-75 wt. %.