# US 4,393,234 A · Process for the preparation of 3-hydroxybenzoic acid > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 4,393,234 A - Document ID: US4393234A - Status: Granted - Kind: A - Application number: 06/378,922 - Filed: 1982-05-17 - Granted: 1983-07-12 - Earliest claimed: 1981-06-04 - Assignees: Bayer Aktiengesellschaft - Inventors: Heinz U. Blank; Eike Gabel; Ernst Goldschmitt; Werner Mentzel - Web page: https://patentgrep.com/patent/US4393234A ## CPC - C07C 309/00: Sulfonic acids; Halides, esters, or anhydrides thereof - C07C 51/367: by introduction of functional groups containing oxygen only in singly bound form - C07C: ACYCLIC OR CARBOCYCLIC COMPOUNDS ## Abstract 3-Hydroxybenzoic acid is obtained by reaction with an alkali metal hydroxide at a temperature of 220.degree. to 450.degree. C. and under a pressure of 1 to 120 bars, from a technical 3-sulphobenzoic acid mixture which contains sulphuric acid and/or sulphur trioxide and which contains at least 75% by weight of 3-sulphobenzoic acid, relative to the total organic constituents present, and not more than 35% by weight of sulphuric acid and/or SO.sub.3, relative to the total mass. For this purpose, this technical 3-sulphobenzoic acid mixture, if desired after dilution with an equal volume of water, is mixed with sufficient 50 to 100% strength by weight alkali metal hydroxide wherein the remaining 50 to 0% by weight consists essentially of water, for 2.5 to 8 mols of alkali metal hydroxide to be present per mol of 3-sulphobenzoic acid, after neutralization of the sulphuric acid and all the sulpho and carboxyl groups. In general, 10 to 45% by weight of water are present in the batch. The reaction mixture is acidified with a mineral acid to a pH value of less than 4, if appropriate after dilution with water, and the 3-hydroxybenzoic acid is isolated at temperatures within the range from -5.degree. C. to +40.degree. C. ## Claims ### Claim 1 In a process for the preparation of 3-hydroxybenzoic acid by contacting 3-sulphobenzoic acid with an alkali metal hydroxide at an elevated temperature, the improvement which comprises: (A) employing a technical 3-sulphobenzoic acid mixture containing sulphuric acid and/or sulphur trioxide, which technical mixture contains at least 75% by weight of 3-sulphobenzoic acid, relative to the total organic constituents present, and not more than 35% by weight of sulphuric acid and/or SO.sub.3, relative to the total mass; (B) the technical mixture is contacted with mixing at an elevated temperature with sufficient 50 to 100% strength by weight alkali metal hydroxide, the remaining 50 to 0% by weight consisting essentially of water, such that 2.5 to 8 mols of alkali metal hydroxide are present per mol of 3-sulphobenzoic acid, after neutralization of the sulphuric acid and all of the sulpho and carboxyl groups; (C) the resultant alkaline reaction mixture is reacted at a temperature in the range of 220.degree. to 450.degree. C. under a pressure of 1 to 120 bars; and (D) the alkaline reaction mixture so obtained is acidified with a mineral acid to a pH value less than 4 and 3-hydroxy benzoic acid is recovered at a temperature in the range of -5.degree. to +40.degree. C. ### Claim 2 (depends on 1) A process according to claim 1, wherein the technical 3-sulphobenzoic acid mixture contains, relative to the total mass: 70 to 95% by weight of 3-sulphobenzoic acid, 2.5 to 7% by weight 4-sulphobenzoic acid, 0.5 to 1.5% by weight of 2-sulphobenzoic acid, 0.01 to 0.5% by weight of 3,5-disulphobenzoic acid, 0.01 to 1.5% by weight of diphenyl sulphone derivatives, 0.01 to 1.5% by weight of benzophenone derivatives and 2 to 20% by weight of SO.sub.3 whether in the form of SO.sub.3, H.sub.2 SO.sub.4, or a mixture thereof. ### Claim 3 (depends on 2) A process according to claim 2, wherein the technical mixture is diluted with water in an amount up to equal parts prior to reaction with the alkali metal hydroxide. ### Claim 4 A process for the preparation of 3-hydroxybenzoic acid which comprises: (A) contacting benzoic acid with 0.01 to 0.5 mol of sulphuric acid per mol of benzoic acid and sulphonating the reaction mixture at an elevated temperature with 1 to 1.2 mols of SO.sub.3 per mol of benzoic acid, the SO.sub.3 being in the gaseous and/or liquid form and containing 0 to 35% by weight of sulphuric acid, relative to the H.sub.2 SO.sub.4 --SO.sub.3 mixture, whereby to obtain a reaction mixture containing 3-sulphobenzoic acid; (B) the reaction mixture so obtained containing 3-sulphobenzoic acid is thereafter contacted with sufficient 50 to 100% strength by weight alkali metal hydroxide, the remaining 50 to 0% by weight consisting essentially of water, such that 2.5 to 8 mols of alkali metal hydroxide are present per mol of 3-sulphobenzoic acid, after neutralization of the sulfuric acid and all the sulpho and carboxyl groups; (C) the reaction mixture is reacted at a temperature in the range from 220.degree. to 450.degree. C. under a pressure of 1 to 120 bars; and (D) the reaction mixture so-obtained following the reaction of step C is acidified with a mineral acid to a pH less than 4 and 3-hydroxybenzoic acid is recovered at a temperature in a range from -5.degree. to +40.degree. C. ### Claim 5 (depends on 4) A process according to claim 4, wherein the benzoic acid/sulfuric acid mixture formed in step A is sulphonated with gaseous and/or liquid SO.sub.3 which can contain 0 to 35% by weight of sulphuric acid, relative to the H.sub.2 SO.sub.4 --SO.sub.3 mixture, at a temperature of 40.degree. to 125.degree. C., with the gaseous and/or liquid SO.sub.3 being metered into the benzoic acid/sulphuric acid mixture at such temperature of 40.degree. to 125.degree. C. and thereafter the sulphonation is completed at a temperature of 125.degree. to 170.degree. C. ### Claim 6 (depends on 4) A process according to claim 4, wherein liquid SO.sub.3 containing 0 to 35% by weight of sulphuric acid, relative to the sulphuric acid-SO.sub.3 mixture, is employed as the sulphonating agent, benzoic acid/sulphuric acid mixture is metered into the liquid SO.sub.3 at a temperature of 40.degree. to 125.degree. C. and, thereafter, the sulphonation is completed at a temperature of 125.degree. to 170.degree. C. ### Claim 7 (depends on 1) A process according to claim 1, wherein after mixing the reaction mixture containing the 3-sulphobenzoic acid with the alkali metal hydroxide, water is removed from that resultant reaction mixture by distillation. ### Claim 8 (depends on 7) A process according to claim 7, wherein the reaction of 3-sulphobenzoic acid with alkali metal hydroxide is effected at normal pressure. ### Claim 9 (depends on 1) A process according to claim 1, wherein the reaction of 3-sulphobenzoic acid with alkali metal hydroxide is effected at normal pressure and during the reaction, water is distilled off. ### Claim 10 (depends on 4) A process according to claim 4, wherein after mixing the 3-sulphobenzoic acid mixture with alkali metal hydroxide, water is removed by distillation. ### Claim 11 (depends on 10) A process according to claim 10, wherein the 3-sulphobenzoic acid mixture is mixed with the alkali metal hydroxide at normal pressure. ### Claim 12 (depends on 4) A process according to claim 4, wherein the 3-sulphobenzoic acid mixture is mixed with alkali-metal hydroxide at normal pressure and during the mixing water is distilled off. ### Claim 13 (depends on 1) A process according to claim 1, wherein 3-sulphobenzoic acid is mixed with an alkali metal hydroxide in a closed reactor in order to maintain the pressure which is formed as a result of the resultant mixing. ### Claim 14 (depends on 4) A process according to claim 4, wherein the 3-sulphobenzoic acid mixture is mixed with alkali metal hydroxide in a closed reactor in order to maintain the pressure formed as a result of the mixing. ### Claim 15 (depends on 13) A process according to claim 13, wherein said reactor is in the form of a mixing tube. ### Claim 16 (depends on 14) A process according to claim 14, wherein said reactor is in the form of a mixing tube. ### Claim 17 (depends on 1) A process according to claim 1, wherein the alkaline reaction mixture which results from contact of the 3-sulphobenzoic acid with an alkali metal hydroxide is pressure-hydrolyzed employing the autogenous steam pressure of the system or a partial steam pressure of about 5 to 80 bars. ### Claim 18 (depends on 4) A process according to claim 4, wherein the alkaline reaction mixture which results from contact of the 3-sulphobenzoic acid with an alkali metal hydroxide is pressure-hydrolyzed employing the autogenous steam pressure of the system or a partial steam pressure of about 5 to 80 bars. ### Claim 19 (depends on 17) A process according to claim 17, wherein the mixture which results from the partial hydrolysis is contacted with a mineral acid to adjust its pH to a value of about 0 to 4 and the mixture is diluted with a sufficient amount of water to dissolve inorganic salts present therein. ### Claim 20 (depends on 18) A process according to claim 18, wherein the mixture which results from the partial hydrolysis is contacted with a mineral acid to adjust its pH to a value of about 0 to 4 and the mixture is diluted with a sufficient amount of water to dissolve inorganic salts present therein. ### Claim 21 (depends on 4) A process according to claim 4, wherein the 3-sulphobenzoic acid containing mixture subjected to contact with the alkali metal hydroxide contains 64 to 93% by weight of 3-sulphobenzoic acid and not more than 35% by weight of sulphuric acid/sulphur trioxide mixture. ### Claim 22 (depends on 21) A process according to claim 21, wherein said 3-sulphobenzoic acid containing reaction mixture contains not more than 25% by weight of the mixture of sulphuric acid and sulphur trioxide. ### Claim 23 (depends on 22) A process according to claim 22, wherein said 3-sulphobenzoic acid containing mixture contains less than 15% by weight of sulphuric acid/sulphur trioxide. ### Claim 24 (depends on 4) A process according to claim 4, wherein the 3-sulphobenzoic acid containing reaction mixture which is contacted with the alkali metal hydroxide itself contains 88 to 95% by weight 3-sulphobenzoic acid, 4-7% by weight 4-sulphobenzoic acid, 0.1 to 1.5% by weight 2-sulphobenzoic acid, 0.01-0.05 3,5-disulphobenzoic acid, 0.01-1.5% by weight benzophenone derivatives and 0.01-1.5% by weight diphenyl sulphone derivatives. ### Claim 25 (depends on 1) A process according to claim 1, wherein the process is carried out without isolation of any intermediate alkali metal salt of 3-sulphobenzoic acid. ### Claim 26 (depends on 4) A process according to claim 4, wherein the process is carried out without isolation of any intermediate alkali metal salt of 3-sulphobenzoic acid. ### Claim 27 (depends on 1) A process according to claim 1, wherein the process is carried out without any intermediate removal of sulphuric acid. ### Claim 28 (depends on 4) A process according to claim 4, wherein the process is carried out without any intermediate removal of sulfuric acid.