Method for producing dichlorophenylthioglycolic acid

Abstract: The present invention is directed to a method for producing dichlorophenylthioglycolic acid which comprises reacting monobromodichlorobenzene or trichlorobenzene with a thioglycolate in a ratio of 0.5 to 2.5 mols of the latter to 1 mol of the former in a polar solvent, and to a method for producing dichlorophenylthioglycolic acid comprising further reacting the reaction mixture obtained as above with a monohalogenoacetate. The method of the present invention is very useful, industrially advantageous and results in a high yield.

Description: The present invention relates to a method for producing dichlorophenylthioglycolic acid. Dichlorophenylthioglycolic acid is a compound which is useful as an intermediate for thioindigo pigments, chemicals for the electronic industry, pharmaceuticals and agricultural chemicals. The conventional methods for producing dichlorophenylthioglycolic acid are known as follows: (1) The method in which trichlorobenzene and sodium hydrosulfide are reacted at 125°C under increased pressure in liquid ammonia solvent in the presence of copper acetate catalyst for 10 hours to yield dichlorothiophenol, which is then reacted with sodium monochloroacetate to yield dichlorophenylthioglycolic acid with a yield of 14 to 29% [Kogyo Kagaku Zasshi, 70 , 1384 (1967)]. (2) The method in which dichlorobenzene is sulfonylchlorinated with chlorosulfuric acid and then reduced with a large amount of zinc powder under acidic conditions to yield dichlorothiophenol, which is then reacted with monochloroacetic acid to yield dichlorophenylthioglycolic acid with a yield of 81% (US Patent No. 3440288). However, these known methods respectively have the following drawbacks. In the method of (1) above, the use of liquid ammonia, which is difficult to handle, a difficult-to-dispose copper compound and an increased reaction pressure poses an operational problem. In addition, yield is low. In the method of (2) above, the process takes a long period, and a large amount of waste effluent which contains harmful heavy metals can cause environmental pollution. As stated above, both known methods have various problems and are not industrially advantageous. For this reason, attempts have been made to develop an industrially advantageous method for production in the relevant technical field, but there is no satisfactory method. It is an object of the present invention to provide an industrially advantageous method for producing dichlorophenylthioglycolic acid with a high yield. Taking note of the situation described above, the present inventors made investigations to provide an industrially advantageous method for producing dichlorophenylthioglycolic acid with a high yield under mild reaction conditions without using harmful heavy metals. As a result, the inventors found that a dichlorophenylthioglycolate can be produced by reacting monobromodichlorobenzene or trichlorobenzene with a thioglycolate as shown in the following reaction scheme A. Also, in the above-mentioned reaction, when the thioglycolate was added in excess in order to increase the yield of dichlorophenylthioglycolate, on the contrary the yield of the desired product dichlorophenylthioglycolate declined. With respect to this phenomenon, the inventors made further investigations and found that when a thioglycolate is added in excess, the reaction between the resulting dichlorophenylthioglycolate and the unreacted thioglycolate proceeds preferentially as shown in the reaction scheme B to yield a dichlorothiophenol salt and thus gives a mixture of dichlorophenylthioglycolate and dichlorothiophenol salt. On the other hand, when a monohalogenoacetate is added to this reaction mixture, the dichlorothiophenol salt changes easily to the dichlorophenylthioglycolate in accordance with the reaction scheme C. The inventors thus found that the yield improves in comparison with the production of a dichlorophenylthioglycolate in a single process in accordance with the reaction scheme A, and developed the present invention. wherein X represents a chlorine atom or bromine atom; M represents an alkali metal. Developed on the basis of these findings, the present invention relates to: (1) a method for producing dichlorophenylthioglycolic acid which comprises reacting monobromodichlorobenzene or trichlorobenzene with a thioglycolate in a ratio of 0.5 to 2.5 mols of the latter to 1 mol of the former in a polar solvent, and (2) a method for producing dichlorophenylthioglycolic acid which comprises further reacting the reaction mixture obtained from the reaction of (1) above with a monohalogenoacetate. The monobromodichlorobenzenes which can serve as a starting material for the present invention are exemplified by 1-bromo-2,5-dichlorobenzene, 1-bromo-2,4-dichlorobenzene, 1-bromo-3,4-dichlorobenzene, 1-bromo-2,3-dichlorobenzene, 1-bromo-2,6-dichlorobenzene and 1-bromo-3,5-dichlorobenzene. The trichlorobenzenes which can serve as a starting material for the present invention are exemplified by 1,2,4-trichlorobenzene, 1,2,3-trichlorobenzene and 1,3,5-trichlorobenzene. Reaction of monobromodichlorobenzene or trichlorobenzene with a thioglycolate is carried out normally in a polar solvent. The polar solvent used is not subject to limitations. Examples of polar solvents which can be used for the present invention include ethylene glycol, diethylene glycol, methanol, ethanol, butanol, N-methyl-2-pyrrolidone, N,N-dimethylformamide, N,N-dimethylacetamide, acetamide, formamide, caprolactam, 1,1-ethylenedipyrrolidone, tetramethylurea, hexamethylphosphoramide, acetonitrile, quinoline, pyridine, lutidine, picoline, dimethylsulfoxide, sulfolane and sulfolene, with preference given to dimethylsulfoxide, ethylene glycol, N-methyl-2-pyrrolidone, sulfolane and the like because they offer a high yield of the reaction product dichlorophenylthioglycolic acid. The amount of solvent used is 1 to 20 times, preferably 1 to 10 times the amount by weight of the starting trichlorobenzene or monobromodichlorobenzene. Two or more of the solvents mentioned above may be used in combination. The amount of a thioglycolate used for the present invention is normally 0.5 to 2.5 times the molar amount of monobromodichlorobenzene or trichlorobenzene. Molar ratios below 0.5 result in increase of the unreacted monobromodichlorobenzene or trichlorobenzene. When the thioglycolate is used at a molar ratio exceeding about 1.0, preference is given to the method in which the side product dichlorothiophenol salt is converted to the dichlorophenylthioglycolate by the addition of a monohalogenoacetate from the viewpoint of improvement in the yield of the desired product dichlorophenylthioglycolic acid for the reason described above. However, the use of a thioglycolate in a molar ratio exceeding 2.5 is not advantageous because the increased side production of a dichlorophenylthiophenol salt necessitates the addition of a still more amount of a monohalogenoacetate. A usable thioglycolate is produced by reacting thioglycolic acid with an alkali metal hydroxide or alkali metal carbonate. The thioglycolate described above can also be prepared in the reaction system. The alkali metal hydroxide or alkali metal carbonate used in this case is exemplified by sodium hydroxide, potassium hydroxide, sodium carbonate, sodium hydrogen carbonate, potassium carbonate and potassium hydrogen carbonate. The amount of its use is suitably 1.6 to 3.0 times the molar amount of thioglycolic acid. In the present invention, the reaction temperature for the reaction of monobromodichlorobenzene or trichlorobenzene with a thioglycolate is preferably 50 to 220°C, more preferably 80 to 190°C. Temperatures below 50°C result in too low reaction rates; temperatures above 220°C can cause yield reduction due to side reactions. Reaction time is preferably 1 to 6 hours; reaction times longer than 6 hours can result in yield reduction due to side reactions. In the case that the monohalogenoacetate is added to the reaction mixture, examples of the monohalogenoacetate include sodium monochloroacetate, potassium monochloroacetate, sodium monobromoacetate and potassium monobromoacetate. The amount of its addition is normally 1.0 to 4.0 times the molar amount of the intermediate dichlorothiophenol salt. The reaction temperature for the reaction of a dichlorothiophenol salt with a monohalogenoacetate is preferably 10 to 200°C, more preferably 50 to 120°C. A reaction time of 1 hour is sufficient because the rate of the reaction of a dichlorothiophenol salt and a monohalogenoacetate is high. By acidifying the resulting reaction mixture, the dichlorophenylthioglycolate can easily be converted to dichlorophenylthioglycolic acid. In the present invention, when trichlorobenzene is used to obtain a 2,5-dichlorophenylthioglycolate, the solvent is distilled off, after which the reaction mixture is heated in the presence of water and cooled for crystallization to separate the side product isomeric 2,4-dichlorophenylthioglycolate. This procedure causes crystallization of 2,5-dichlorophenylthioglycolate alone, which is then acidified as above to yield 2,5-dichlorophenylthioglycolic acid with high purity. Examples of the acid used for the acidification include hydrochloric acid, sulfuric acid, nitric acid and phosphoric acid. The amount of its addition is normally 1.0 to 4.0 times, preferably 1.0 to 3.0 times the molar amount of a dichlorophenylthioglycolate. In accordance with the present invention, a dichlorophenylthioglycolate or a mixture of dichlorophenylthioglycolate and dichlorothiophenol salt can be obtained by reacting monobromodichlorobenzene or trichlorobenzene with a thioglycolate under normal pressure. Also, dichlorophenylthioglycolic acid can be obtained in an industrially advantageous way with a high yield by a very simple procedure of reacting this mixture with a monohalogenoacetate. The present invention is hereinafter described in more detail by means of the following working examples and comparative example, but the invention is not limited by these examples. Example 1 To a 300 ml four-necked flask equipped with a stirrer, a thermometer and a condenser were charged 24.9 g (0.110 mol) of 1-bromo-2,5-dichlorobenzene, 13.19 g (0.143 mol) of thioglycolic acid, 12.06 g (0.286 mol) of 95% sodium hydroxide and 100 g of dimethylsulfoxide, followed by stirring at 120°C for 4 hours. Then, after distilling off the dimethylsulfoxide under reduced pressure, 100 g of water was added to the residue. After dissolving the residue therein at 100°C, the solution was cooled for crystallization and filtered to yield sodium 2,5-dichlorophenylthioglycolate, which was then dissolved in 100 g of water with heating and acidified with concentrated hydrochloric acid, filtered and dried to yield 19.6 g of a light yellowish white powder of 2,5-dichlorophenylthioglycolic acid. The yield based on 1-bromo-2,5-dichlorobenzene was 75.1%. Example 2 To a 300 ml four-necked flask equipped with a stirrer, a thermometer and a condenser were charged 24.9 g (0.110 mol) of 1-bromo-2,5-dichlorobenzene, 13.19 g (0.143 mol) of thioglycolic acid, 12.06 g (0.286 mol) of 95% sodium hydroxide and 100 g of dimethylsulfoxide, followed by stirring at 120°C for 4 hours. After cooling to 100°C, the 2,5-dichlorothiophenol salt produced as the side product was treated with 5.13 g (0.044 mol) of sodium monochloroacetate at the same temperature for 1 hour. Then, after distilling off the dimethylsulfoxide under reduced pressure, 100 g of water was added to 54.5 g of the residue. After dissolving the residue therein at 100 °C, the solution was cooled for crystallization and filtered to yield sodium 2,5-dichlorophenylthioglycolate, which was then dissolved in 100 g of water with heating and acidified with concentrated hydrochloric acid, filtered and dried to yield 23.5 g of a light yellowish white powder of 2,5-dichlorophenylthioglycolic acid. The yield based on 1-bromo-2,5-dichlorobenzene was 90.0%. Example 3 15.4 g of a light yellowish white powder of 2,5-dichlorophenylthioglycolic acid was obtained in the same manner as in Example 1 except that the 1-bromo-2,5-dichlorobenzene was replaced with 20.0 g (0.110 mol) of 1,2,4-trichlorobenzene. The yield based on 1,2,4-trichlorobenzene was 59.0%. Example 4 19.3 g of a light yellowish white powder of 2,5-dichlorophenylthioglycolic acid was obtained in the same manner as in Example 2 except that the 1-bromo-2,5-dichlorobenzene was replaced with 20.0 g (0.110 mol) of 1,2,4-trichlorobenzene. The yield based on 1,2,4-trichlorobenzene was 74.0%. Examples 5 through 7 2,5-dichlorophenylthioglycolic acid was obtained in the same manner as in Example 4 except that reaction temperature, molar ratio of thioglycolic acid and reaction time were changed as shown in Table 1. The results are shown in Table 1. Example 8 To a 500 ml flask equipped with a thermometer, a condenser and a stirrer were added 45.2 g (0.2 mol) of 1-bromo-2,5-dichlorobenzene, 23.7 g (0.4 mol) of 95% potassium hydroxide, 18.4 g (0.2 mol) of thioglycolic acid and 320 g of N-methyl-2-pyrrolidone, followed by stirring at 140 to 150°C for 2 hours. An assay of the reaction solution by high performance liquid chromatography identified the solution as a mixture of dichlorophenylthioglycolate and dichlorothiophenol salt. Then, after distilling off the solvent, 300 g of water and 50 g of toluene were added for layer separation. To the water layer was added 45 g of concentrated hydrochloric acid, and the mixture was cooled to room temperature. The resulting crystals were filtered and dried to yield 28.7 g of 2,5-dichlorophenylthioglycolic acid. Its melting point was 129 to 131°C, and the yield was 60.5%. The results are given in Table 2. Example 9 Using the same procedure as in Example 8, 45.2 g (0.2 mol) of 1-bromo-2,5-dichlorobenzene, 23.7 g (0.4 mol) of 95% potassium hydroxide, 18.4 g (0.2 mol) of thioglycolic acid and 320 g of N-methyl-2-pyrrolidone were added, followed by stirring at 140 to 150°C for 2 hours. Then, 30.4 g (0.26 mol) of sodium monochloroacetate was added to the reaction solution, followed by stirring at 90°C for 1 hour. After distilling off the solvent, 300 g of water and 50 g of toluene were added for layer separation. To the water layer was added 45 g of concentrated hydrochloric acid, and the mixture was cooled to room temperature. The resulting crystals were filtered and dried to yield 34.0 g of 2,5-dichlorophenylthioglycolic acid with a yield of 71.7%. The results are given in Table 2. Examples 10 through 13 Using the combinations of monobromodichlorobenzene or trichlorobenzene, thioglycolic acid, potassium hydroxide and solvent listed in Table 2, the reaction was carried out in the same manner as in Example 8 or 9 to yield 2,5-dichlorophenylthioglycolic acid. The results are given in Table 2. Comparative Example In the same manner as in Example 8, 45.2 g (0.2 mol) of 1-bromo-2,5-dichlorobenzene, 23.7 g (0.4 mol) of 95% potassium hydroxide, 18.4 g (0.2 mol) of thioglycolic acid and 320 g of n-decane were added, followed by stirring at 140 to 150°C for 10 hours. In an assay of the reaction solution by high performance liquid chromatography no peak of 2,5-dichlorophenylthioglycolic acid or 2,5-dichlorothiophenol was detected. Then, 200 g of water was added to the reaction solution, and the mixture was cooled to room temperature. An assay of the n-decane solution by high performance liquid chromatography revealed that 1-bromo-2,5-dichlorobenzene remained unreacted in an amount equivalent to 98.7% of the starting material.

Claims: A method for producing dichlorophenylthioglycolic acid which comprises reacting monobromodichlorobenzene or trichlorobenzene with a thioglycolate in a ratio of 0.5 to 2.5 mols of the latter to 1 mol of the former in a polar solvent. A method for producing dichlorophenylthioglycolic acid which comprises further reacting the reaction mixture obtained from the reaction in claim 1 with a monohalogenoacetate A method according to claim 1, wherein said polar solvent is dimethylsulfoxide. A method according to claim 1, wherein said polar solvent is ethylene glycol. A method according to claim 1, wherein said polar solvent is N-methyl-2-pyrrolidone. A method according to claim 1, wherein said polar solvent is sulfolane. A method according to claim 2, wherein said monohalogenoacetate is sodium monochloroacetate. A method according to claim 2, wherein said monohalogenoacetate is sodium monobromoacetate. A method according to claim 2, wherein the amount of said monohalogenoacetate is 1.0 to 4.0 times the molar amount of the resulting dichlorothiophenol salt in said reaction mixture.

Inventors: GODA HIROSHI C O SUMITOMO SEIK, HATA HIROYUKI C O SUMITOMO SEI, KAGANO HIROKAZU C O SUMITOMO S, NAKANO MASAHITO C O SUMITOMO S, OHE TOSHIYUKI C O SUMITOMO SEI, SUZUKI MICHIO C O SUMITOMO SEI, TERAMOTO MASAKI C O SUMITOMO S, YOSHIKAWA MASATO C O SUMITOMO, GODA, HIROSHI, C/O SUMITOMO SEIKA CHEM. CO., LTD, HATA, HIROYUKI, C/O SUMITOMO SEIKA CHEM. CO., LTD., KAGANO, HIROKAZU, C/O SUMITOMO SEIKA CHEM. CO.,LTD, NAKANO, MASAHITO, C/O SUMITOMO SEIKA CHEM. CO.,LTD, OHE, TOSHIYUKI, C/O SUMITOMO SEIKA CHEM. CO., LTD, SUZUKI, MICHIO, C/O SUMITOMO SEIKA CHEM. CO., LTD., TERAMOTO, MASAKI, C/O SUMITOMO SEIKA CHEM. CO.,LTD, YOSHIKAWA, MASATO, C/O SUMITOMO SEIKA CHEM.CO.,LTD
Applicants: SUMITOMO SEIKA CHEMICALS, SUMITOMO SEIKA CHEMICALS CO., LTD.
Application year: 1991
Main classification: C07C323
IPC codes: C07C319, C07C323