PROCESS FOR PREPARING POLYHYDROXY CARBOXYLIC ACID

Abstract: The present invention provides a process for producing polyhydroxycarboxylic acids having a weight-average molecular weight of 50,000 or above which are excellent as biodegradable plastics by subjecting Lactides to ring-opening polymerization in the presence of an inorganic solid acid catalyst carrying silica and/or a light metal.

Description: The present invention relates to a process for producing polyhydroxycarboxylic acids, specifically, those having a weight-average molecular weight of 50,000 or above. Said polyhydroxycarboxylic acids are useful as biodegradable plastics for food-wrapping films, beverage bottles, drug delivery systems, etc. Some methods are known as the methods for producing polyhydroxycarboxylic acids of a high molecular weight by the use of Lactides; for example, a method which comprises polymerizing, in the presence of polyvalent heavy metal oxide such as lead oxide, a lactide which is obtained by heating lactic acid (U.S. Patent No. 2,703,316), a method for producing copolymers of lactic acid and glycolic acid having an average molecular weight of 72,000 by copolymerizing, in the presence of stannous octanoate, a mixture of lactide and glycolide respectively obtained by dehydration condensation of lactic acids and glycolic acid (Japanese Published Examined Patent Application No. 14688/81), and a method for producing polylactic acids having a molecular weight of 100,000 by polymerizing DL-lactide in the presence of stannous octanoate (Japanese Published Unexamined Patent Application No. 69553/90). However, these methods, in which Lactides of high purity are necessary, require purification steps of crude lactides such as recrystallization and distillation, and thus have various problems for industrial utilization due to a number of complicated steps. US-A-2,703,316 refers to a process of producing Lactide polymers capable of being formed into tough, orientable, self-supporting thin films. This is achieved by heating lactide having a melting point of more than 120°C to a temperature above the melting point and below 200°C in the presence of 0.02% to 0.1%, based on the weight of monomeric material present, of a polyvalent metal oxide until a polymer having a tack point of 60° to 130°C is formed. T.M. Abdel-Fattah and T.J. Pinnavaia describe the synthesis and properties of tin-substituted mesoporous silica molecular sieve as a heterogeneous catalyst for Lactide ring-opening polymerization (Chem. Commun., 5 , 1996, 665-666). The catalyst which is prepared by neutral amine surfactant assembly of silicon and tin (IV) alkoxide precursors at ambient temperature is said to show promise for producing poly(L-lactic acid) with polydispersity values near 1.1. JP-A-8-193127 refers to a process for producing a lactate polymer useful as a medicinal material and a biodegradable polymer as an alternative to common resins. The process includes subjecting lactate to ring-opening polymerization by using a catalyst comprising component A and component B. The component A is a condensate prepared by reacting an aluminum alkoxide, a halogenated silicon and a phosphate ester, whereas component B comprises a trialkyl aluminum and/or a dialkyl aluminum chloride. The ratio of the aluminum weight in component B to the weight of component A is 0.02 to 0.35. The present invention relates to a process for producing polyhydroxycarboxylic acids, specifically, those having a weight-average molecular weight of 50,000 or above by polymerizing Lactides in the presence of an inorganic solid acid catalyst carrying a light metal selected from alkali metal compounds or alkaline earth metal compounds. The polyhydroxycarboxylic acids include polymers and copolymers of lactides. The Lactides include lactide and glycolide. As the Lactides, besides commercially available ones, Lactides which are synthesized from the corresponding hydroxycarboxylic acids such as lactic acid and glycolic acid according to the ordinary method may be used without purification. If necessary, these synthesized Lactides may be used after being purified by recrystallization (Japanese Published Unexamined Patent Application No. 279435/94) and distillation (PCT National Publication No. 503490/95). The Lactides can be used in combination with lactone. The lactone include γ-butyrolactone and ε-caprolactone. The lactone is preferably used in an amount of 20 wt% (hereinafter % means wt%) or below based on the amount of Lactide. Among various kinds of inorganic solid acid catalysts, inorganic solid acid catalysts carrying a light metal as the constituting component are used in the present invention. The light metal is selected from alkali metals such as lithium, sodium, and potassium, and alkaline earth metals such as magnesium and calcium, and aluminum. An inorganic acid addition salt of the alkali metal and the alkaline earth metal such as carbonates or bicarbonates thereof, hydroxycarboxylates thereof such as lactate or glycolate thereof, an organic acid addition salt of the alkali metal and the alkaline earth metal such as acetates, oxides, or hydroxides thereof may be used as the alkali metal and the alkaline earth metal compound. The inorganic solid acid catalyst carrying the light metal includes aluminum silicate, zeolite, acid clay, activated clay, bentonite, kaolin, talc, magnesium silicate, aluminum borate, and silicate. Usually, commercially available ones are used. When the combination of an inorganic solid catalyst and an alkali metal or an alkaline earth metal is employed, an inorganic solid acid catalyst as mentioned above is treated according to the following methods to prepare a catalyst. (1) An inorganic solid acid catalyst is treated with an aqueous solution of carbonates, bicarbonates or hydroxides of an alkali metal compound catalyst or an alkaline earth metal compound catalyst to obtain an inorganic solid acid catalyst carrying an alkali metal compound catalysts or an alkaline earth metal compound catalyst. The metal elution test is carried out in the same manner as in Example 1 to select those in which metal elution is observed, out of the thus obtained inorganic solid acid catalyst carrying an alkali metal compound catalyst or an alkaline earth metal compound catalyst. (2) Using an inorganic solid acid catalyst which inherently carries an alkali metal compound catalyst or an alkaline earth metal compound catalyst, the metal elution test is carried out in the same manner as in Example 1. The inorganic solid acid catalyst in which metal elution is observed does not need the treatment mentioned in (1) and can be used as it is. An example of such catalysts is zeolite. (3) An inorganic solid acid catalyst is added to a raw material solution together with carbanates, bicarbonates, hydroxycarboxylates, acetates, hydroxides, or oxides of an alkali metal compound catalyst or an alkaline earth metal compound catalyst. Alternatively, carbonates, bicarbonates, hydroxycarboxylates, acetates, hydroxides, or oxides of an alkali metal compound catalyst or an alkaline earth metal compound catalyst are added to a reaction mixture to which an inorganic solid acid catalyst is added. The alkali metal or the alkaline earth metal is added to a reaction mixture in such an amount that the concentration of the alkali metal or the alkaline earth metal eluted in the reaction mixture becomes 10-10,000 ppm, preferably 100-3,000 ppm. Mixtures of two or more inorganic solid acid catalysts carrying the light metal can also be used in the process of the present invention. The inorganic solid acid catalyst carrying the light metal is used in an amount of 0.03-10%, preferably 0.5-7%, more preferably 1-5% based on the amount of a Lactide in one to several portions. The inorganic solid acid catalyst carrying the light metal to be used in the present invention (hereinafter referred to simply as "the inorganic solid acid catalyst") can be added as it is or as a dispersion in a solvent such as toluene or xylene, at the start of reaction together with the starting materials or in the course of reaction. The polymerization reaction is carried out at 160-250°C, preferably 180-240°C, more preferably 180-220°C, under reduced pressure of 6.65 - 5333 Pa (0.05-40 mmHg), preferably 13.3 - 3333 Pa (0.1-25 mmHg), for 5-50 hours, preferably 10-30 hours. After the reaction was completed, the polymer or copolymer obtained in the molten state is cooled to room temperature to give solidified polyhydroxycarboxylic acid. The weight-average molecular weight of the polyhydroxycarboxylic acids obtained by the process of the present invention is usually 50,000-300,000, though it varies with the kind and amount of catalysts, reaction temperature, reaction pressure, reaction time, etc. The obtained polyhydroxycarboxylic acids usually carry 0.03-10% of an inorganic solid acid catalyst, but they can be used as such without the removal of the inorganic solid acid catalyst according to the purpose of use because of their high biodegradability. For the use in drug delivery systems, polyhydroxycarboxylic acids carrying substantially no inorganic solid acid catalyst are preferable. The polyhydroxycarboxylic acids carrying substantially no inorganic solid acid catalyst (inorganic solid acid catalyst content: less than 0.03%) are obtained by purifying the polyhydroxycarboxylic acids carrying 0.03-10% of an inorganic solid acid catalyst. Purification can be carried out in the following manner. A polyhydroxycarboxylic acid carrying an inorganic solid acid catalyst is dissolved in a halogenated hydrocarbon such as chloroform, and the insoluble inorganic solid acid catalyst is removed by filtration. The filtrate is added to a lower alcohol such as isopropanol, and the polyhydroxycarboxylic acid precipitated is separated. For the use of the polyhydroxycarboxylic acids as biodegradable polymers, the polyhydroxycarboxylic acids carrying an inorganic solid acid catalyst or the polyhydroxycarboxylic acids with the inorganic solid acid catalyst used in the present invention or another inorganic solid acid catalyst as a degradation promoter added are usually preferable, though the polyhydroxycarboxylic acids carrying substantially no inorganic solid acid catalyst can also be used as biodegradable polymers. Examples and Comparative Examples are shown below. The weight-average molecular weight of polymers and copolymers was measured in the following manner in Examples and Comparative Examples. A polymer or copolymer was dissolved in chloroform to prepare a 0.5% solution, and the weight-average molecular weight was measured by gel permeation chromatography (GPC) using standard polystyrene of known molecular weight. As GPC columns, TOSOH G-5000, TOSOH G-3000, and TOSOH G-1000 (TOSCH CORPORATION) connected in series were used, and the measurement was carried out at a temperature of 40°C. Example 1 Lactide (100 g) was put into a 100-ml reaction vessel equipped with a stirrer and a nitrogen-introducing tube, and was molten by heating at 100°C. To the molten lactide was added 2.1 g of synthetic light aluminum silicate (Tomita Pharmaceutical Co., Ltd.) *1 , followed by heating at 150°C for 3 hours. Then, the pressure was reduced gradually to 2666 Pa (20 mmHg) over 30 minutes, followed by stirring at 195 ± 5°C for one hour. After the pressure was reduced gradually to 133 Pa (1 mmHg) over 30 minutes, the mixture was stirred at 195 ± 5°C for 7 hours to give lactic acid polymer in the molten state. The product was cooled to room temperature to give 60.30 g of light brown lactic acid polymer. The weight-average molecular weight of this polymer was 81,000. Example 2 A 90% aqueous solution of lactic acid (430 g) was put into a 500-ml reaction vessel equipped with a stirrer and a nitrogen-introducing tube. After substitution of nitrogen gas was carried out three times, the pressure was reduced to 133 Pa (1 mmHg) with stirring and the water generated was removed. Then, the temperature was raised to 150°C to give 348 g of lactide as a distillate. The obtained lactide (20 g) was put into a 100-ml reaction vessel, and was molten by heating at 150°C for three hours with stirring. To the molten lactide was added 0.4 g of synthetic light aluminum silicate (Tomita Pharmaceutical Co., Ltd.), and the temperature was raised to 195 ± 5°C. Then, the pressure was reduced gradually to 2666 Pa (20 mmHg) over 30 minutes, and the mixture was subjected to reaction for one hour. After the pressure was reduced gradually to 133 Pa (1 mmHg) over 30 minutes, the mixture was stirred at 195 ± 5°C for 10 hours to give lactic acid polymer in the molten state. The product was cooled to room temperature to give 14.10 g of white lactic acid polymer. The weight-average molecular weight of this polymer was 102,000. Example 3 The lactide obtained in Example 2 (10 g) and glycolide (10 g) were put into a 100-ml reaction vessel equipped with a stirrer and a nitrogen-introducing tube. After substitution of nitrogen gas was carried out three times, the temperature was raised to 150 ± 5°C, and the mixture was molten over 3 hours with stirring. To the resulting mixture was added 0.4 g of synthetic light aluminum silicate (Tomita Pharmaceutical Co., Ltd.), and the temperature was raised to 195 ± 5°C. The pressure was reduced gradually to 2666 Pa (20 mmHg) over 30 minutes, followed by stirring for 3 hours. After the pressure was reduced gradually to 133 Pa (1 mmHg) over 30 minutes, the mixture was stirred at 195 ± 5°C for 7 hours to give lactic acid-glycolic acid copolymer in the molten state. The product was cooled to room temperature to give 11.50 g of light brown copolymer. The weight-average molecular weight of this copolymer was 65,000. Example 4 The lactide obtained in Example 2 (19 g) and glycolide (1 g) were put into a 100-ml reaction vessel equipped with a stirrer and a nitrogen-introducing tube. After substitution of nitrogen gas was carried out three times, the mixture was stirred at 150°C for 3 hours in a stream of nitrogen. To the resulting mixture was added 0.4 g of Baylith 5A [synthetic zeolite (Kurita Water Industries Ltd.)] *2 , and the temperature was raised to 195 ± 5°C. The pressure was reduced gradually to 2666 Pa (20 mmHg) over 30 minutes, followed by stirring for one hour. After the pressure was reduced gradually to 133 Pa (1 mmHg) over 30 minutes, the mixture was stirred at 195 ± 5°C for 9 hours to give lactic acid-glycolic acid copolymer in the molten state. The product was cooled to room temperature to give 14.64 g of white copolymer. The weight-average molecular weight of this copolymer was 73,000. Example 5 The lactide obtained in Example 2 (10 g) and γ-butyrolactone (10 g) were put into a 100-ml reaction vessel equipped with a stirrer and a nitrogen-introducing tube. After substitution of nitrogen gas was carried out three times, the mixture was molten by stirring at 150°C for 3 hours in a stream of nitrogen. To the resulting mixture was added 0.4 g of synthetic light aluminum silicate (Tomita Pharmaceutical Co., Ltd.), and the temperature was raised to 195 ± 5°C. The pressure was reduced gradually to 2666 Pa (20 mmHg) over 30 minutes, followed by stirring at 195 ± 5°C for 3 hours. After the pressure was reduced gradually to 133 Pa (1 mmHg) over 30 minutes, the mixture was stirred at 195 ± 5°C for 7 hours to give lactic acid-butyrolactone copolymer in the molten state. The product was cooled to room temperature to give 14.15 g of light brown copolymer. The weight-average molecular weight of this copolymer was 88,000. Example 6 The lactide obtained in Example 2 (17 g) and ε-caprolactone (3 g) were put into a 100-ml reaction vessel equipped with a stirrer and a nitrogen-introducing tube. After substitution of nitrogen gas was carried out three times, the mixture was molten by stirring at 150°C for 3 hours in a stream of nitrogen. To the resulting mixture was added 0.4 g of synthetic light aluminum silicate (Tomita Pharmaceutical Co., Ltd.), and the temperature was raised to 195 ± 5°C. The pressure was reduced gradually to 2666 Pa (20 mmHg) over 30 minutes, followed by stirring at 195 ± 5°C for 3 hours. After the pressure was reduced gradually to 133 Pa (1 mmHg) over 30 minutes, the mixture was stirred at 195 ± 5°C for 7 hours to give lactic acid-caprolactone copolymer in the molten state. The product was cooled to room temperature to give 12.11 g of light brown copolymer. The weight-average molecular weight of this copolymer was 82,000. Comparative Example 1 The same procedure as in Example 2 was repeated except that 0.2 g of stannous octanoate was used instead of aluminum silicate to give lactic acid polymer. The weight-average molecular weight of this lactic acid polymer was 14,000. Comparative Example 2 The same procedure as in Example 2 was repeated except that 2.1 g of lead oxide was used instead of aluminum silicate to give lactic acid polymer. The weight-average molecular weight of this lactic acid polymer was 18,000. The present invention provides polyhydroxycarboxylic acids having a weight-average molecular weight of 50,000 or above which are useful as biodegradable plastics for food-wrapping films, beverage bottles, drug delivery systems, etc.

Claims: A process for producing a polyhydroxycarboxylic acid, which comprises polymerizing a Lactide in the presence of an inorganic solid acid catalyst carrying a light metal compound selected from alkali metal compounds or alkaline earth metal compounds. A process according to Claim 1, wherein the Lactide is lactide or glycolide. A process according to Claim 1, wherein the inorganic solid acid catalyst is selected from the group consisting of aluminum silicate, zeolite, acid clay, activated clay, bentonite, kaolin, talc, magnesium silicate, aluminum borate, or silicate. A process according to claim 1, wherein the alkali metal is selected from the group consisting of lithium, sodium and potassium; or the alkaline earth metal is selected from the group consisting of magnesium and calcium.

Inventors: MURAYAMA TOSHIKAZU, TSUZAKI NOBUKO, YANAGISAWA NORIO, YOKOMORI YOROZU, MURAYAMA, TOSHIKAZU, TSUZAKI, NOBUKO, YANAGISAWA, NORIO, YOKOMORI, YOROZU
Applicants: KYOWA HAKKO KOGYO KK, KYOWA HAKKO KOGYO CO., LTD.
Application year: 1996
Main classification: C08G63
IPC codes: C08G63