# US 5,344,951 A · Production of alkyl phosphites > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 5,344,951 A - Document ID: US5344951A - Status: Granted - Kind: A - Application number: 08/031,838 - Filed: 1993-03-16 - Granted: 1994-09-06 - Earliest claimed: 1993-03-16 - Assignees: Ethyl Petroleum Additives, Inc. - Inventors: Abbas Kadkhodayan - Web page: https://patentgrep.com/patent/US5344951A ## CPC - C07F 9/143: with unsaturated acyclic alcohols - C07F 9/142: with hydroxyalkyl compounds without further substituents on alkyl - C07F: ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM (metal-containing porphyrins C07D487/22) ## Abstract This invention relates to an improved process for producing diesters of phosphorous acid. The process comprises (a) reacting phosphorous acid with monohydric alcohol in a petroleum distillate solvent while maintaining a reaction mass temperature within the range of from about 130.degree. to about 138.degree. C., and (b) refluxing the reaction mass during the reaction, wherein the phosphorous acid contains about 20 up to about 35 wt. % water, the molar ratio of alcohol to phosphorous acid used is within the range of from about 2.0:1 to about 4.0:1, and water is removed from the reaction mass essentially as it is formed during steps (b) and (c). ## Claims ### Claim 1 A method for producing diesters of phosphorous acid comprising: a) charging phosphorous acid solution and solvent to a reaction vessel, wherein the phosphorous acid contains about 20 up to about 35 wt. % water; b) feeding from about 2.0 to about 4.0 moles of monohydric alcohol per mole of phosphorous acid to the reaction vessel containing phosphorous acid solution and solvent while maintaining a reaction mass temperature within the range of from about 130.degree. to about 138.degree. C. and while removing water from the reaction mass essentially as it is formed; and c) subsequently, separating alcohol and solvent from the dihydrocarbyl phosphite formed in step (b). ### Claim 2 (depends on 1) The method of claim 1 wherein the solvent is a paraffinic solvent. ### Claim 3 (depends on 2) The method of claim 2 wherein the solvent is VM&P (Varnish Makers' & Painters') naphtha having a boiling point within the range of from about 118.degree. to about 150.degree. C. ### Claim 4 (depends on 2) The method of claim 2 wherein the solvent is n-octane having a boiling point within the range of from about 125.degree. to about 127.degree. C. ### Claim 5 (depends on 1) The method of claim 1 further comprising refluxing the reaction mass during step (b). ### Claim 6 (depends on 1) The method of claim 1 wherein the weight ratio of solvent to anhydrous phosphorous acid charged to the reaction vessel ranges from about 0.8:1 to about 1.2:1. ### Claim 7 (depends on 1) The method of claim 1 wherein the monohydric alcohol is n-butanol. ### Claim 8 (depends on 1) The method of claim 1 wherein the monohydric alcohol is isobutanol. ### Claim 9 (depends on 1) The method of claim 1 wherein the molar ratio of monohydric alcohol to phosphorous acid ranges from about 2.5:1 to about 3.2:1. ### Claim 10 (depends on 1) The method of claim 1 further comprising feeding the monohydric alcohol to the reaction vessel in multiple portions so as to maintain the reaction mass temperature within the range of from about 131.degree. to about 136.degree. C. ### Claim 11 (depends on 1) The method of claim 1 wherein, prior to charging phosphorous acid and solvent, the reaction vessel contains a heel from a previous reaction wherein the heel contains diester of phosphorous acid and a minor amount of impurities. ### Claim 12 A process for producing dialkyl esters of phosphorous acid, comprising (a) charging phosphorous acid solution and a petroleum distillate solvent to a reaction vessel, (b) reacting the phosphorous acid with monohydric alcohol in the solvent while maintaining a reaction mass temperature within the range of from about 130.degree. to about 138.degree. C., and (c) refluxing the reaction mass during the reaction, wherein the phosphorous acid contains about 20 up to about 35 wt. % water, the molar ratio of alcohol to phosphorous acid used is within the range of from about 2.0: 1 to about 4.0: 1, and water is removed from the reaction mass essentially as it is formed during steps (b) and (c). ### Claim 13 (depends on 12) The process of claim 12 wherein the solvent is a paraffinic solvent. ### Claim 14 (depends on 13) The process of claim 13 wherein the paraffinic solvent is Varnish Makers' and Painters' naphtha having a boiling point within the range of from about 118.degree. to about 150.degree. C. ### Claim 15 (depends on 13) The process of claim 13 wherein the paraffinic solvent is n-octane having a boiling point within the range of from about 125.degree. to about 127.degree. C. ### Claim 16 (depends on 14) The process of claim 14 wherein the weight ratio of solvent to anhydrous phosphorous acid in the reaction mass ranges from about 0.8:1 to about 1.2:1. ### Claim 17 (depends on 16) The process of claim 16 wherein the monohydric alcohol is n-butanol. ### Claim 18 (depends on 16) The process of claim 16 wherein the monohydric alcohol is isobutanol. ### Claim 19 (depends on 17) The process of claim 17 wherein the molar ratio of monohydric alcohol to phosphorous acid ranges from about 2.5:1 to about 3.2:1. ### Claim 20 (depends on 19) The process of claim 19 wherein, prior to charging the reaction vessel with phosphorous acid and solvent, the reaction vessel contains a heel from a previous reaction wherein the heel contains diester of phosphorous acid and a minor amount of impurities.