Purification of bisphenol monoester

Abstract: A bisphenol monoester represented by the formula (I): wherein R¹ is hydrogen or alkyl, R² and R³ are each alkyl, and R⁴ is alkyl, alkenyl or phenyl, is purified from a mixed solvent comprising a C₆-C₁₂ aromatic hydrocarbon solvent and a C₁-C₈ alcohol or C₂-C₃ aliphatic nitrile solvent.

Description: The present invention relates to a process for the purification of a bisphenol monoester represented by the following formula (I): wherein R 1 is hydrogen or an alkyl of 1 to 3 carbon atoms, R 2 and R 3 independently of one another are each an alkyl of 1 to 5 carbon atoms, and R 4 is an alkyl of 1 to 3 carbon atoms, an alkenyl of 2 to 4 carbon atoms or phenyl. The bisphenol monoesters represented by the above formula (I) are useful as heat deterioration inhibitors in the production or processing of butadiene polymers such as butadiene rubber (BR), styrene/butadiene copolymer rubber (SBR) and styrene/butadiene block copolymer rubber or resin (SBS) or as stabilizers for various synthetic resins, for example, polyolefins such as polyethylene and polypropylene. The process for the production of bisphenol monoesters of formula (I) is described in EP-B-0 500 323 (by the same applicant), from which the present application was divided on 24 October 1995. For purification of the bisphenol monoester represented by the formula (I), there have been known a process according to which recrystallization is carried out using petroleum ether or n-hexane as described in Examples 11 and 12 of U.S. Patent 3,984,372, and a process according to which a solvent such as toluene or N,N-dimethylacetamide used for the reaction is partially or completely distilled off and toluene or n-hexane is added to the residue to carry out purification as described in Examples of U.S. Patent 4,365,032, U.S. Patent 4,562,281 and U.S. Patent 4,774,274. However, these processes are not satisfactory in quality of the desired product because purification effect is low owing to the small difference between the solubility of the desired bisphenol monoester contained in the crude product to be purified and that of impurities. Furthermore, these processes are also not satisfactory in production on an industrial scale since production equipments become complicated when the solvent is to be recovered for economical reasons. SUMMARY OF THE INVENTION An object of the present invention is to provide a satisfactory process for purifying the bisphenol monoester of the formula (I) in an industrial scale operation. Another object of the invention is to provide a process for purifying the bisphenol monoester of the formula (I) by crystallization, with high quality, with high yield and with economy. It has been found that the desired product (I) having excellent quality can be economically obtained with high yield by crystallization using a particular mixed solvent. The present invention has been accomplished based on the above findings. Thus, the invention provides a process for purifying the crude bisphenol monoester represented by the formula (I) by using a mixed solvent comprising a first solvent selected from aromatic hydrocarbons of 6 to 12 carbon atoms and a second solvent selected from alcohols of 1 to 8 carbon atoms and aliphatic nitriles of 2 to 3 carbon atoms, and crystallizing the desired bisphenol monoester from the mixed solvent. DESCRIPTION OF THE INVENTION The bisphenol monoester of the formula (I) is preferably purified by using a mixed crystallization solvent comprising a first solvent of an aromatic hydrocarbon and a second solvent of an alcohol or an aliphatic nitrile, and crystallizing the bisphenol monoester from the mixed solvent. The bisphenol monoesters to be purified may be those produced by the process described in EP-B- 0 500 323 by the same applicant, from which this application is divided, but are not limited to them. The bisphenol monoester represented by the formula (I) which is to be purified according to the present invention can usually be produced by the reaction of a 2,2'-alkylidenebis(4,6-dialkylphenol) with a carboxylic acid or a derivative thereof. The starting 2,2'-alkylidenebis(4,6-dialkylphenol) can be produced by condensing the corresponding 2,4-dialkylphenol with an aldehyde. The group represented by R 1 in the formula (I) includes hydrogen, methyl, ethyl, n-propyl and isopropyl, R 1 is preferably hydrogen or methyl. The alkyls represented by R 2 and R 3 include, for example, methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl, tert-butyl, n-pentyl and tert-pentyl. Especially, R 3 is preferably an alkyl having a quaternary carbon, namely, tert-butyl or tert-pentyl. The alkyl represented by R 4 includes methyl, ethyl, n-propyl and isopropyl. The alkenyl represented by R 4 includes, for example, vinyl, isopropenyl, 1-propenyl and 1-butenyl. R 4 may also be phenyl. Among the bisphenol monoesters represented by the formula (I), those which have an alkenyl as R 4 are preferably used as stabilizers for various polymers. Preferred examples of these bisphenol monoesters are detailed below. 2-[1-(2-hydroxy-3.5-di-t-pentylphenyl)ethyl]-4,6-di-t-pentylphenyl acrylate, 2-[1-(2-hydroxy-3,5-di-t-pentyphenyl)ethyl]-4,6-di-t-pentylphenyl methacryalte, 2-(2-hydroxy-3,5-di-t-pentylbenzyl)-4,6-di-t-pentylphenyl acrylate, 2,4-di-t-butyl-6-[1-(3,5-di-t-butyl-2-hydroxyphenyl)ethyl]phenyl acrylate, 2,4-di-t-butyl-6-(3,5-di-t-butyl-2-hydroxybenzyl)phenyl acrylate, 2,4-di-t-butyl-6-[1-(3,5-di-t-butyl-2-hydroxyphenyl)ethyl]phenyl methacrylate, 2-t-butyl-6-(3-t-butyl-2-hydroxy-5-methylbenzyl)-4-methylphenyl acrylate, 2-t-butyl-6-[1-(3-t-butyl-2-hydroxy-5-methylphenyl)ethyl]-4-methylphenyl acrylate, 2-t-butyl-6-(3-t-butyl-2-hydroxy-5-methylbenzyl)-4-methylphenyl methacrylate, 2-t-butyl-6-[1-(3-t-butyl-2-hydroxy-5-methylphenyl)propyl]-4-methylphenyl acrylate, 2-t-butyl-6-(3-t-butyl-5-ethyl-2-hydroxybenzyl)-4-ethylphenyl acrylate, 2-t-butyl-6-[1-(3-t-butyl-2-hydroxy-5-propylphenyl)ethyl]-4-propylphenyl acrylate, 2-t-butyl-6-[1-(3-t-butyl-2-hydroxy-5-isopropylphenyl)ethyl]-4-isopropylphenyl acrylate. In the present invention, such bisphenol monoester is purified by crystallization. In this case, as a crystallizing solvent is used a mixed solvent comprising a first solvent selected from aromatic hydrocarbons of 6 to 12 carbon atoms and a second solvent selected from alcohols of 1 to 8 carbon atoms and aliphatic nitriles of 2 to 3 carbon atoms. The aromatic hydrocarbons of 6 to 12 carbon atoms as the first solvent include, for example, benzene, toluene, xylene, ethylbenzene, cumene, cymene and chlorobenzene. These may be used each alone or in combination of two or more as the first solvent of the mixed solvent, but normally, either one of them is used. Among these aromatic hydrocarbons, toluene and xylene are preferred and xylene is especially preferred. The alcohols of 1 to 8 carbon atoms as one of the second solvent include, for example, methanol, ethanol, n-propanol, isopropanol, n-butanol, isobutanol, tert-butanol, n-pentanol, n-octanol, 2-ethylhexanol and cyclohexanol. The aliphatic nitriles of 2 to 3 carbon atoms include acetonitrile and propiononitrile. These alcohols and aliphatic nitriles can be used each alone or in combination of two or more as the second solvent of the mixed solvent. Among these second solvents, alcohols are preferred and, methanol is especially preferred because it is inexpensive and can be easily recovered. Generally, the aromatic hydrocarbons used as the first solvent in the mixed solvent are also used as the reaction solvent in production of the bisphenol monoester of formula (I), as described in EP-B-0 500 323 by the same applicant, from which this application is divided, and act as a dissolving agent in crystallization since solubility of the bisphenol monoester of formula (I) is high. Therefore, when the aromatic hydrocarbon is used as the reaction solvent, the reaction step can be shifted to the crystallizing step while the reaction mixture is in the form of solution in which the aromatic hydrocarbon remains. The alcohols or aliphatic nitriles which are the second solvent are used for controlling the solubility of the bisphenol monoester of formula (I) in the first solvent thereby to improve the yield and the purification effect or for inhibition of scale deposition on crystallizing apparatuses. When the first solvent or the second solvent is used singly, quality or yield of the desired product is deteriorated. Especially when the second solvent is used alone, the aromatic hydrocarbon solvent used for mono-esterification reaction must be distilled out of the system and this is not preferred also for economical reasons in production on an industrial scale. As explained above, especially when the aromatic hydrocarbon is used as a reaction solvent in the mono-esterification, the bisphenol monoester of formula (I) to be crystallized according to the present invention may be in the form of a solution of the reaction mixture containing said aromatic hydrocarbon or may be, of course, a crystallized product obtained by removing the solvent from the reaction mixture. Especially, in the production on an industrial scale, it is desired to carry out the crystallization treatment by adding the second solvent to the aromatic hydrocarbon used as the reaction solvent in which the bisphenol monoester and impurities are dissolved. In the present invention, it is preferred to use the first solvent in an amount of 15-150% by weight based on the amount of the bisphenol monoester of formula (I). It is preferred to use the second solvent in a mixing ratio. of 0.3-4 times the weight of the first solvent. If amounts of the first solvent and the second solvent are outside the above ranges, reduction in quality or yield of the desired product may be caused or deposition of scale on crystallizing apparatuses may occur. This is not preferred. The crystallizing operation is generally carried out by first completely dissolving a crude product using the first solvent alone at a boiling temperature or lower and then adding the second solvent to the solution and, if necessary, adding a seed crystal which acts as a nucleus for crystal, and gradually cooling the solution to precipitate crystal. It is also possible in some cases to carry out the crystallization by simultaneously using the first solvent and the second solvent and dissolving the crude product therein. Furthermore, when the aromatic hydrocarbon solvent is used in the reaction step as described in EP-B-0 500 323 by the same applicant, from which this application is divided, the second solvent is added to the reaction mixture which is in the form of solution or from which a predetermined amount of the solvent has been removed by distillation or the like to increase concentration of the bisphenol monoester and subsequently, the above-mentioned operation can be effected. The precipitated crystal is separated from the mother liquor by filtration or the like, washed and dried to obtain the desired purified product. According to the purification process of the present invention, the desired product of the formula (I) having a high purity can be efficiently and economically produced with high yield. Therefore, this process is useful as a purification process in production of the bisphenol monoester of the formula (I) on an industrial scale. The present invention will be explained in more detail with reference to the following Examples. These are only illustrative, and not limitative to the scope of the invention. In the Examples, parts and percent (%) are based on the weight unless otherwise indicated. Example 1 In a reactor equipped with a thermometer, a stirrer, a reflux condenser and a dropping device were charged 2344 parts of 2,4-di-t-pentylphenol, 200 parts of xylene, 47 parts of an anionic surface active agent, 95 parts of 78% concentrated sulfuric acid and 771 parts of 30% aqueous acetaldehyde solution, and reaction was allowed to proceed with keeping the temperature at 90-100°C for 7 hours with stirring. After completion of the reaction, 3600 parts of xylene was introduced into the reaction mixture. After the aqueous layer was separated and removed, the organic layer was washed with water until it became neutral and then, water was distilled out of the system under a reduced pressure of about 200 mmHg at 90-110°C with refluxing the solvent. After the resulting condensation reaction mixture was cooled, 448 parts of acrylic acid and 1290 parts of triethylamine were charged in the reactor and the air in the reactor was replaced with nitrogen. Then, 634 parts of phosphorus oxychloride was added dropwise and the reactor was kept at 40°C for 1 hour. Thereafter, the organic layer was washed with water until it became neutral and dried by azeotropic distillation under reduced pressure. Then, methanol was added to the distillation residue (still containing xylene) to carry out crystallization thereby to obtain 2226 parts of a white crystalline 2-[1-(2-hydroxy-3,5-di-t-pentylphenyl)ethyl]-4,6-di-t-pentylphenyl acrylate having a melting point of 119-121°C. (yield: 80.5% based on dialkylphenol) Example 2 Experiment was effected in the same manner as in Example 1 except that toluene was used in place of xylene. Example 3 The procedure of Example 1 was repeated except that 535 parts of methacrylic acid was used in place of acrylic acid, thereby obtaining 2249 parts of white crystalline 2-[1-(2-hydroxy-3,5-di-t-pentylphenyl)ethyl]-4,6-di-t-pentylphenyl methacrylate having a melting point of 103-105°C. Example 4 The procedure of Example 1 was repeated except that 2063 parts of 2,4-di-t-butylphenol was used in place of 2,4-di-t-pentylphenol and toluene was used in place of xylene as a solvent, thereby obtaining 2088 parts of white crystalline 2,4-di-t-butyl-6-[1-(3,5-di-t-butyl-2-hydroxyphenyl)ethyl]phenyl acrylate having a melting point of 190-192°C. Example 5 In the same reactor as used in Example 1 were charged 1643 parts of 2-t-butyl-4-methylphenol, 800 parts of xylene, 14 parts of an anionic surface active agent, 3 parts of 96% concentrated sulfuric acid and 456 parts of 37% aqueous formaldehyde solution, and reaction was allowed to proceed for 3 hours with keeping the temperature at 90-95°C under stirring. After completion of the reaction, 890 parts of xylene was introduced therein, followed by effecting the same after-treatmentS and refluxing dehydration as in Example 1. The reaction mixture was cooled and then, 354 parts of acrylic acid and 1057 parts of triethylamine were charged therein and the air in the reactor was replaced with nitrogen. Thereafter, 464 parts of phosphorus oxychloride was added dropwise and the reactor was kept at 80°C for 1 hour. Then, the same after-treatments and crystallization operation as in Example 1 were carried out to obtain 1564 parts of white crystalline 2-t-butyl-6-(3-t-butyl-2-hydroxy-5-methybenzyl)-4-methylphenyl acrylate having a melting point of 132-134°C. Example 6 The procedure of Example 5 was repeated except that toluene was used in place of xylene and 423 parts of methacrylic acid was used in place of acrylic acid, thereby obtaining 1718 parts of white crystalline 2-t-butyl-6-(3=t=butyl-2-hydroxy-5-methylbenzyl)-4-methylphenyl methacrylate having a melting point of 144-146°C. Results of the reactions in Examples 1-6 are shown in Table 1. Isolated yield (%) Quality Bisphenol compound Bisphenol monoester Total Purity (%) Melting point (°C) Example 1 94.0 85.6 64.9 80.5 99.3 119-121 Example 2 94.0 85.4 64.7 80.3 99.3 119-121 Example 3 94.0 83.7 63.5 78.7 98.5 103-105 Example 4 93.8 90.1 68.2 84.5 99.7 190-192 Example 5 95.8 81.1 79.3 77.7 98.0 132-134 Example 6 95.8 87.6 85.6 83.9 99.8 144-146 Reference Example 1 In a reactor equipped with a thermometer, a stirrer, a reflux condenser and a dropping device were charged 234.4 parts of 2,4-di-t-pentylphenol, 20 parts of xylene, 4.7 parts of an anionic surface active agent, 9.5 parts of 78% concentrated sulfuric acid and 77.1 parts of 30% aqueous acetaldehyde solution, and reaction was allowed to proceed for 7 hours keeping the temperature at 90-100°C under stirring. After completion of the reaction, 360 parts of xylene was introduced into the reaction mixture. After the aqueous layer was separated and removed, the organic layer was washed with water until it became neutral and then, water was distilled out of the system under a reduced pressure of about 200 mmHg at 90-110°C with refluxing the solvent. After the resulting condensation reaction mixture was cooled, 44.8 parts of acrylic acid and 129.0 parts of triethylamine were charged in the reactor, and the air in the reactor was replaced with nitrogen. Then, 63.4 parts of phosphorus oxychloride was added dropwise and the reactor was kept at 40°C for 1 hour. Thereafter, the organic layer was washed with water until it became neutral, and the solvent was completely distilled off under reduced pressure to obtain 252.5 parts of a crystalline distillation residue containing 2-[1-(2-hydroxy-3,5-di-t-pentylphenyl)ethyl]-4,6-di-t-pentylphenyl acrylate. This residue was analyzed to find that it contained 87.5% of monoester, 12.2% of by-products and 0.2% of unreacted materials. Reference Example 2 The procedure of Reference Example 1 was repeated except that 53.5 parts of methacrylic acid was used in place of acrylic acid, thereby obtaining 281.4 parts of a crystalline distillation residue containing 2-[1-(2-hydroxy-3,5-di-t-pentyphenyl)ethyl]-4,6-di-t-pentylphenyl methacrylate. This residue was analyzed to find that it contained 87.0% of monoester, 0.2% of unreacted materials and 12.7% of by-products. Reference Example 3 In the same reactor as used in Reference Example 1 were charged 164.3 parts of 2-t-butyl-4-methylphenol, 80 parts of xylene, 1.4 parts of an anionic surface active agent, 0.3 part of 96% concentrated sulfuric acid and 45.6 parts of 37% aqueous formaldehyde solution, and reaction was allowed to proceed for 3 hours with keeping the temperature at 90-95°C. After completion of the reaction, 89 parts of xylene was introduced thereinto, followed by effecting the same after-treatments and refluxing dehydration as in Reference Example 1. The reaction mixture was cooled and then, 35.0 parts of acrylic acid and 105.7 parts of triethylamine were charged in the reactor and the air in the reactor was replaced with nitrogen. Thereafter, 46.4 parts of phosphorus oxychloride was added dropwise and the reactor was kept at 80°C for 1 hour. Then, the same operation as in Reference Example 1 was conducted to obtain 190.8 parts of a crystalline distillation residue containing 2-t-butyl-6-(3-t-butyl-2-hydroxy-5-methylbenzyl)-4-methylphenyl acrylate. It was confirmed that the residue contained 85.5% of monoester, 4.5% of diester, 2.9% of unreacted materials and 7.1% of by-products. Reference Example 4 The procedure of Reference Example 3 was repeated except that 42.3 parts of methacrylic acid was used in place of acrylic acid, thereby obtaining 197.0 parts of a crystalline distillation residue containing 2-t-butyl-6-(3-t-butyl-2-hydroxy-5-methylbenzyl)-4-methylphenyl methacrylate. It was confirmed that this residue contained 92.5% of monoester, 3.3% of unreacted materials and 4.2% of by-products. No diester was detected. Reference Example 5 The procedure of Reference Example 1 was repeated except that 206.3 parts of 2,4-di-t-butylphenol was used in place of 2,4-di-t-pentylphenol and toluene was used in place of xylene as a solvent, thereby obtaining 231.1 parts of a crystalline distillation residue containing 2,4-di-t-butyl-6-[1-(3,5-di-t-butyl-2-hydroxyphenyl)ethyl]phenyl acrylate. It was confirmed that this residue contained 97.0% of monoester, 0.5% of unreacted materials and 2.4% of by-products. Example 7 Fifty parts of the distillation residue obtained in Reference Example 1 was dissolved in 9 parts of xylene at 85°C and then, 22.5 parts of methanol was gradually added thereto under stirring and 0.1 part of seed crystal was introduced thereinto at 55°C. Thereafter, the mixture was kept for 1 hour at a temperature in the range of 50-55°C to precipitate crystal and was gradually cooled to 10°C, and the resulting crystal was filtered off and washed with methanol. Thereafter, the crystal was dried at 60°C under reduced pressure to obtain 40.5 parts of white crystalline 2-[1-(2-hydroxy-3,5-di-t-pentylphenyl)ethyl]-4,6-di-t-pentylphenyl acrylate having a melting point of 119-121°C. Examples 8 and 9 The procedure of Example 7 was repeated except that isopropanol was used in place of methanol in Example 8 and acetonitrile was used in place of methanol in Example 9. The desired white crystals were obtained. Example 10 The procedure of Example 7 was repeated except that toluene was used in place of xylene, thereby obtaining the desired white crystal. Example 11 The procedure of Example 7 was repeated except that 50 parts of the distillation residue obtained in Reference Example 2 was used and xylene was used in an amount of 8 parts and methanol was used in an amount of 24 parts, thereby obtaining 39.8 parts of white crystalline 2-[1-(2-hydroxy-3,5-di-t-pentylphenyl)ethyl]-4,6-di-t-pentylphenyl methacrylate having a melting point of 103-105°C. Example 12 Fifty parts of the distillation residue obtained in Reference Example 3 was dissolved in 11 parts of xylene at 110°C and then the solution was cooled to 85°C under stirring and 0.1 part of seed crystal was introduced thereinto at the same temperature. Crystal was precipitated with gradually cooling the solution and 36 parts of methanol was added at 50°C, followed by cooling to 20°C. The crystal was filtered off at that temperature, washed with methanol and dried at 60°6 under reduced pressure to obtain 41.0 parts of white crystalline 2-t-butyl-6-(3-t-butyl-2-hydroxy-5-methylbenzyl)-4-methylphenyl acrylate having a melting point of 132-134°C. Examples 13 and 14 The procedure of Example 12 was repeated except that n-butanol was used in place of methanol in Example 13 and acetonitrile was used in place of methanol in Example 14, thereby obtaining the desired white crystals. Example 15 The procedure of Example 12 was repeated except that toluene was used in place of xylene, thereby obtaining the desired white crystal. Example 16 The procedure of Example 12 was repeated except that 50 parts of the distillation residue obtained in Reference Example 4 was used, thereby obtaining 43.7 parts of white crystalline 2-t-butyl-6-(3-t-butyl-2-hydroxy-5-methylbenzyl)-4-methylphenyl methacrylate having a melting point of 144-146°C. Example 17 Fifty parts of the distillation residue obtained in Reference Example 5 was dissolved in 65 parts of toluene at 100°C and then the solution was gradually cooled under stirring to precipitate crystal. Twentyfive parts of methanol was gradually added at 80°C, followed by cooling to 20°C, and the resulting crystal was filtered off at that temperature. The crystal was washed with methanol and dried at 60°C under reduced pressure to obtain 45.1 parts of white crystalline 2,4-di-t-butyl-6-[1-(3,5-di-t-butyl-2-hydroxyphenyl)ethyl]phenyl acrylate having a melting point of 190-192°C. Results of crystallization obtained in the above Examples 7-17 are shown in Table 2. Crystallizing solvents Crystallizing yield (%) Quality Purity (%) Transmittance (%) Melting point (°C) Example 7 xylene/methanol 91.9 99.3 98.5 119-121 Example 8 xylene/isopropanol 91.7 99.3 98.7 119-121 Example 9 xylene/acetonitrile 92.0 99.3 98.0 119-121 Example 10 toluene /methanol 92.2 99.4 98.7 119-121 Example 11 xylene/methanol 90.1 98.5 98.5 103-105 Example 12 xylene/methanol 94.0 98.0 99.6 132-134 Example 13 xylene/n-butanol 93.5 98.2 99.8 132-134 Example 14 xylene/acetonitrile 94.0 98.0 99.5 132-134 Example 15 toluene/methanol 93.8 98.1 99.7 132-134 Example 16 xylene/methanol 94.1 99.8 99.3 144-146 Example 17 toluene/methanol 92.7 99.7 98.0 190-192

Claims: A process for purifying a bisphenol monoester represented by the formula (I), wherein R 1 is hydrogen or an alkyl of 1 to 3 carbon atoms, R 2 and R 3 independently of one another are each an alkyl of 1 to 5 carbon atoms, and R 4 is an alkyl of 1 to 3 carbon atoms, an alkenyl of 2 to 4 carbon atoms or phenyl, which process comprises crystallising said bisphenol monoester from a mixed solvent comprising a first solvent selected from aromatic hydrocarbons of 6 to 12 carbon atoms and a second solvent selected from alcohols of 1 to 8 carbon atoms and aliphatic nitriles of 2 to 3 carbon atoms. The Process of Claim 1, wherein the first solvent is an aromatic hydrocarbon selected from benzene, toluene, xylene, ethylbenzene, cumene, cymene and chlorobenzene, and the second solvent is an alcohol selected from methanol, ethanol, n-propanol, isopropanol, n-butanol, isobutanol, tert-butanol, n-pentanol, n-octanol, 2-ethylhexanol and cyclohexanol, or an aliphatic nitrile selected from acetonitrile and propiononitrile. The process of Claim 2, wherein the first solvent is toluene or xylene, and the second solvent is methanol. The process of Claim 1, wherein the first solvent is used in an amount of 15 to 150% by weight based on the amount of the bisphenol monoester of the formula (I), and the second solvent is used in a ratio of 0.3 to 4 times the weight of the first solvent. The process of Claim 1, wherein the crystallizing is effected by preparing a solution of the bisphenol monoester of the formula(I) in the first solvent alone, and then adding the second solvent to the solution followed by cooling to precipitate a purified crystal of the bisphenol monoester. The process of Claim 5, wherein the solution of the bisphenol monoester in the first solvent alone is a reaction mixture obtained in the production of the bisphenol monoester or a solution in which the first solvent used in the production of the bisphenol monoester is partially removed from the reaction mixture. The process of Claim 1, wherein R 4 in the formula (I) is the alkenyl. The process of Claim 7, wherein the bisphenol monoester of the formula (I) is 2-[ 1-(2-hydroxy-3,5-di-t-pentylphenyl)ethyl-4,6-di-t-pentylphenyl acrylate, 2-[ 1-(2-hydroxy-3,5-di-t-pentylphenyl)ethyl]-4,6-di-t-pentylphenyl methacrylate, 2-t-butyl-6-(3-t-butyl-2-hydroxy-5-methylbenzyl)-4-methylphenyl acrylate, 2-t-butyl-6-(3-t-butyl-2-hydroxy-5-methylbenzyl)-4-methylphenyl methacrylate, or 2, 4-di-t-butyl-6-[1-(3,5 di-t-butyl-2-hydroxyphenyl)ethyl]phenyl acrylate.

Inventors: INOUE KIKUMITSU, KAZUAKI YAMAMOTO, MANJI SASAKI, SHINICHI YACHIGO, INOUE, KIKUMITSU, KAZUAKI, YAMAMOTO, MANJI, SASAKI, SHINICHI, YACHIGO
Applicants: SUMITOMO CHEMICAL CO, SUMITOMO CHEMICAL COMPANY LIMITED
Application year: 1992
Main classification: C07C67
IPC codes: C07C67