Method of obtaining phenylalanine anhydrous crystals

Abstract: A method of stably obtaining optically active phenylalanine anhydrous crystals is developed, and the anhydrous crystals having excellent handleability are produced. An inorganic salt or the like is added to an aqueous solution containing optically active phenylalanine to adjust an osmotic pressure π to 10,500 - 450 T + 4.4 T 2 (T is a crystallization/precipitation temperature), after which the optically active phenylalanine is crystallized and precipitated to obtain phenylalanine anhydrous crystals. According to the present invention, optically active phenylalanine anhydrous crystals having excellent separability can be stably obtained. Since the optically active phenylalanine anhydrous crystals could be obtained so far in the low-temperature region, the improvement in the yield or the like is expected. Thus, it is quite advantageous in view of the industrial production.

Description: The present invention relates to a method of obtaining optically active phenylalanine anhydrous crystals which are useful as a pharmaceutical starting material in the powder form, a pharmaceutical intermediate and a starting material of a sweetener. Prior Art L-phenylalanine is an essential amino acid which is nutritively indispensable, and it is industrially useful as a starting material of L-aspartyl-L-phenylalanine methyl ester which is a sweetener. A method in which optically active phenylalanine is separated from a hydrolyzate of a protein such as defatted soybean or the like, a fermentation method and a synthesis method are known as a method of producing the optically active phenylalanine. In any of these methods, crystallization and precipitation of the optically active phenylalanine are generally carried out to purify it. When the optically active phenylalanine-containing solution is crystallized and precipitated at a pH in the range of from 3 to 9, either anhydrous crystals (hereinafter referred to as "α-form crystals") or monohydrate crystals (hereinafter referred to as "β-form crystals") of the optically active phenylalanine are commonly obtained. The α-form crystals are plate or flake crystals, while the β-form crystals are fine needle crystals. Further, the α-form crystals exhibit good separability from the mother liquor, and less entrain the mother liquor. Therefore, the α-form crystals are industrially more advantageous than the β-form crystals. Thus, a method of obtaining high-quality α-form crystals stably has been variously studied. The following methods have been hitherto conducted to obtain high-quality α-form crystals. (1) A method in which sodium chloride in an amount of at least 20 g/100g·H 2 O is added to a phenylalanine-containing aqueous solution, and the mixture is cooled to 30°C or lower to crystalize and precipitate phenylalanine [Japanese Laid-Open Patent Application (Kokai) No. 91,062/1992]. (2) A method in which a surfactant such as a sorbitan alkyl ester or polyoxyethylenesorbitan alkyl ester is added to an aqueous solution containing phenylalanine and ammonium chloride to crystallize and precipitate phenylalanine [Japanese Laid-Open Patent Application (Kokai) No. 103,565/1992]. (3) A method in which when the concentration of phenylalanine in the phenylalanine fermentation liquid is above the solubility during cultivation, seed crystals of α-form crystals are added to crystalize and precipitate phenylalanine [Japanese Laid-Open Patent Application (Kokai) No. 304,971/1993]. Further, the following methods have been hitherto conducted to obtain phenylalanine in a high yield. (4) A method of isolating phenylalanine in which from 20 to 40 % by weight of ammonium sulfate are added to a phenylalanine-containing aqueous solution, and the mixture is filtered at a temperature of 30°C or lower [Japanese Laid-Open Patent Application (Kokai) No. 163,215/1993]. (5) A method of crystallizing and precipitating phenylalanine in which at least 8 % by weight of ammonium sulfate are added to a phenylalanine aqueous solution obtained by an enzymatic reaction of cinnamic acid and ammonia [Japanese Laid-Open Patent Application (Kokai) No. 178,801/1993]. However, these methods have not been studied for stably obtaining the α-form crystals. Even if the α-form crystals are formed, only the concentration of each additive in the crystallizing solution has been defined. Systematic considerations have not been offered. Problems To Be Solved by the Invention The present invention relates to a method in which high-quality phenylalanine crystals are obtained while maintaining excellent handleability in the step of crystallizing and precipitating L-phenylalanine. Means Taken To Solve the Problems Optically active phenylalanine is formed as α-form crystals at a given temperature (transition point) and as β -form crystals at a temperature below the given temperature. In an aqueous system, the transition point of the optically active phenylalanine is approximately 37°C. The obtained crystals can be estimated as α-form crystals or as β-form crystals through observation using a microscope, powder X-ray analysis or the like. However, the transition point has been generally difficult to measure. The reason is that even if phenylalanine is crystallized and precipitated at a temperature of 40°C which is deemed to be within an α-crystal region, β-form crystals are precipitated when the concentration of the optically active phenylalanine in the solution becomes high and the transition point is apparently estimated to increase. The present inventors have assiduously investigated the phenomenon of crystallizing and precipitating the optically active phenylalanine, and they have carefully observed, at this time, the crystallization/precipitation temperature, the concentration of the optically active phenylalanine in the solution, the osmotic pressure of the solution and the crystal form of the optically active phenylalanine precipitated at that time. Consequently, they have found that as shown in Fig. 1, the α-form crystals are formed at a high osmotic pressure of the solution, and the β-form crystals are formed at a low osmotic pressure of the solution. The borderline between the α-crystal region and the β-crystal region has been expressed in terms of the crystallization/precipitation temperature and the osmotic pressure of the solution. Accordingly, it has been found that if the α-form crystals are obtained at a given crystallization/precipitation temperature T (°C), the optically active phenylalanine-containing solution is crystallized and precipitated upon adjusting the osmotic pressure (π) of the solution to at least 10,500 - 450 T + 4.4 T 2 , thereby making it possible to stably obtain the α-form crystals even though the crystallization/precipitation temperature T (°C) is below the transition point in a pure system. That is, even when phenylalanine is crystallized and precipitated in the aqueous system at a temperature below 37°C which is the transition point of the aqueous system, the α-form crystals which were difficult to obtain so far can be formed stably and easily upon adjusting the osmotic pressure as mentioned above. The osmotic pressure here referred to is a value measured by means of an osmometer based on freezing point depression, and the unit is mOsm/kg·H 2 O. An additive can be used to adjust the osmotic pressure π of the optically active phenylalanine-containing solution to a desired value. Any additive is available if it helps to give a desired osmotic pressure at a crystallization/precipitation temperature. The additive includes inorganic and organic compounds. Examples of the inorganic compounds include electrolytes, for example, chlorides such as aluminum chloride, ammonium chloride, potassium chloride and sodium chloride, nitrates such as ammonium nitrate, potassium nitrate and sodium nitrate, carbonates such as ammonium carbonate, sulfates such as aluminum sulfate, ammonium sulfate, aluminum potassium sulfate, sodium sulfate and magnesium sulfate. Examples of the organic compounds include organic electrolytes such as sodium acetate, potassium acetate, sodium oxalate and potassium oxalate, and non-electrolytes, for example, saccharides such as galactose, glucose, fructose, mannose, sucrose, lactose and maltose, and high-molecular substances such as polyethylene glycol. Also available are monohydric alcohols such as methanol and ethanol, and polyhydric alcohols such as ethylene glycol and glycerol. These compounds may be used either singly or in combination so long as the desired osmotic pressure can be provided. The low-molecular electrolytes such as the inorganic salts are preferable in view of the increase in the osmotic pressure. Meanwhile, some additives such as sodium chloride decrease the solubility of the optically active phenylalanine. In that case, the concentration (g/100g·H 2 O, hereinafter referred to as "C1") of the optically active phenylalanine before the crystallization and precipitation is unchanged, but the concentration (hereinafter referred to as "C2") of the optically active phenylalanine in the mother liquor after the optically active phenylalanine has been crystallized and precipitated with the additive decreases, with the result that the degree of supersaturation (C1/C2) at the time of the crystallization and precipitation increases. When the degree of supersaturation C1/C2 at the time of the crystallization and precipitation exceeds 3, the β-form crystals are temporarily precipitated. Accordingly, it has to be considered that when the additive is added, the osmotic pressure is raised and the degree of supersaturation therefore increases. Consequently, it is advisable to conduct the crystallization and precipitation at C1/C2 within the range of from 1 to 3, preferably from 1 to 2. The optically active phenylalanine-containing aqueous solution includes a fermentation liquid, a solution obtained by treating the fermentation liquid with an ion-exchange resin or a decoloring agent, a solution of crude crystals obtained by crystallizing and precipitating the above-mentioned solution, and a mother liquor from which the crude crystals have been separated in the fermentation method; a protein hydrolyzate, a solution obtained by treating the protein hydrolyzate with an ion-exchange resin or a decoloring resin, a solution of crude crystals obtained by crystallizing and precipitating the above-mentioned solution, and a mother liquor from which the crude crystals have been separated in the protein hydrolysis method; and a solution obtained by reacting DL-acetylphenylalanine with an acylase. Thus, any solution is available so long as the optically active phenylalanine can be crystallized and precipitated therefrom. For instance, the optically active phenylalanine can be effectively crystallized and precipitated from the optically active phenylalanine-containing aqueous solution having a high osmotic pressure, such as the fermentation liquid because the additive for adjusting the osmotic pressure to a desired value may be used in a small amount. Examples The present invention is illustrated specifically by referring to the following Examples. In Examples, C1 refers to the concentration (g/100g·H 2 O) of optically active phenylalanine before the crystallization and precipitation, and C2 refers to the concentration (g/100g·H 2 O) of optically active phenylalanine in the mother liquor after the crystallization and precipitation. Example 1 Fifty grams of water were added to 1.7 g of L-phenylalanine L-phenylalanine crystals (made by Sigma Co.), and the crystals were dissolved therein at 60°C to prepare a L-phenylalanine solution having an L-phenylalanine concentration C1 of 3.4. Then, ammonium sulfate was added to the solution to provide a predetermined osmotic pressure, and was dissolved therein at 60°C. The mixture was then cooled to 30°C to crystallize and precipitate L-phenylalanine. At that time, ammonium sulfate was added in amounts of 2.5 g, 5 g, 6 g and 8 g such that the predetermined osmotic pressure became higher than 960 (= 10,500 - 450 × 30 + 4.4 × 30 × 30)(mOsm/kg·H 2 O). By comparison, ammonium sulfate was added in amounts of 0 g, 1 g and 2 g such that the osmotic pressure became lower than 960 (mOsm/kg·H 2 O), and the resulting mixtures were also crystallized and precipitated. The phenylalanine concentration in the mother liquor and the crystal form of the obtained phenylalanine are shown in Table 1. As is clear from Table 1, anhydrous crystals (α-form crystals) were obtained preferentially when the osmotic pressure was higher than 960 (mOsm/kg·H 2 O). Amount of ammonium sulfate (g) Osmotic pressure Π (mOsm/kg· H 2 O) Form of crystal precipitated Phenylalanine concentration C2(g/100g·H 2 O) C1/C2 Comparative Examples 0 160 β-form 3.1 1.1 1 516 β-form 3.0 1.1 2 784 β-form 2.9 1.2 Examples 2.5 964 α-form 2.6 1.3 5 1621 α-form 2.4 1.4 6 1861 α-form 2.2 1.5 8 2350 α-form 2.0 1.7 Example 2 Fifty grams of H 2 O were added to 1.8 g of L-phenylalanine crystals (made by Sigma Co.), and the L-phenylalanine crystals were dissolved therein at 60°C to prepare a L-phenylalanine solution having an L-phenylalanine concentration C1 of 3.6. Then, dextrose was added to the solution to provide a predetermined osmotic pressure, and was dissolved therein at 60°C. The mixture was then cooled to 25°C to crystallize and precipitate L-phenylalanine. At that time, dextrose was added in amounts of 20 g, 25 g and 30 g such that the predetermined osmotic pressure became higher than 2,000 (= 10,500 - 450 × 25 + 4.4 × 25 × 25)(mOsm/kg·H 2 O). By comparison, dextrose was added in amounts of 8 g, 12 g and 16 g such that the osmotic pressure became lower than 2,000 (mOsm/kg·H 2 O), and the resulting mixtures were also crystallized and precipitated. The phenylalanine concentration in the mother liquor and the crystal form of the obtained phenylalanine are shown in Table 2. As is clear from Table 2, anhydrous crystals (α-form crystals) were obtained preferentially when the osmotic pressure was higher than 2,000 (mOsm/kg·H 2 O). Amount of dextrose (g) Osmotic pressure Π (mOsm/kg·H 2 O) Form of crystal precipitated Phenylalanine concentration C2 (g/100g·H 2 O) C1/C2 Comparative Examples 8 1100 β-form 2.9 1.2 12 1623 β-form 3.0 1.2 16 1816 β-form 3.1 1.2 Examples 20 2182 α-form 3.3 1.1 25 2716 α-form 3.4 1.1 30 3130 α-form 3.5 1.03 Example 3 Fifty grams of water were added to 1.7 g of L-phenylalanine L-phenylalanine crystals (made by Sigma Co.), and the crystals were dissolved therein at 60°C to prepare a solution having an L-phenylalanine concentration C1 of 3.4. Then, sodium chloride was added to the solution in amounts of 6 g, 8 g, 10 g and 12 g, and was dissolved therein at 60°C to prepare four kinds of phenylalanine aqueous solutions. Subsequently, these solutions were cooled to a predetermined temperature to crystallize and precipitate L-phenylalanine. The conditions of the experiment and the results (crystal form of phenylalanine) are shown in Table 3. The osmotic pressures of the solutions which were borderlines between α-form crystals and β-form crystals at the crystallization/precipitation temperatures (25°C, 20°C, 15°C and 10°C) were 2,000, 3,260, 4,740 and 6,440 (mOsm/kg·H 2 O) respectively. Table 3 reveals that the anhydrous crystals (α-form crystals) were obtained preferentially when the osmotic pressures of the phenylalanine aqueous solutions were higher than the borderline values between α-form crystals and β-form crystals at the crystallization/precipitation temperatures of the solutions. Amount of NaCl (g) Upper line: Osmotic pressure Π (mOsm/kg·H 2 O) of the solution Middle line: Form of crystal precipitated Lower line: Phenylalanine concentration C2 (g/100g·H 2 O) 25°C 20°C 15°C 10°C 6 3642 α-form 2.1 (C1/C2 = 1.6) 3666 α-form 2.0 (C1/C2 = 1.7) 3728 β-form 1.9 (C1/C2 = 1.8) 3710 β-form 1.9 (C1/C2 = 1.8) 8 4918 α-form 1.8 (C1/C2 = 1.9) 4836 α-form 1.7 (C1/C2 = 2.0) 4844 α-form 1.7 (C1/C2 = 2.0) 4855 β-form 1.6 (C1/C2 = 2.1) 10 5995 α-form 1.6 (C1/C2 = 1.2) 5960 α-form 1.5 (C1/C2 = 2.3) 6036 α-form 1.4 (C1/C2 = 2.4) 5872 β-form 1.4 (C1/C2 = 2.4) 12 7075 α-form 1.4 (C1/C2 = 2.4) 7092 α-form 1.3 (C1/C2 = 2.6) 7055 α-form 1.2 (C1/C2 = 2.8) 7020 α-form 1.2 (C1/C2 = 2.8) Example 4 L-phenylalanine crystals (made by Sigma Co.) were dissolved at 70°C, and four kinds of L-phenylalanine solutions having L-phenylalanine concentrations C1 of 5.2, 4.5, 3.5 and 3.0 were prepared. Then, 9 g of sodium chloride were added to each of the solutions, and dissolved therein at 70°C. The mixture was cooled to 15°C to crystallize and precipitate L-phenylalanine. The phenylalanine concentration in the mother liquor and the crystal form of phenylalanine are shown in Table 4. The borderline value for the osmotic pressure of the solution between α-form crystals and β-form crystals at the crystallization/precipitation temperature of 15°C was 4,740 (= 10,500 - 450 × 25 + 4.4 × 25 × 25) (mOsm/kg·H 2 O). As shown in Table 4, even if the osmotic pressure was higher than 4,740 (mOsm/kg·H 2 O), the β-form crystals were precipitated in the system with C1/C2 of 3.1 in combination with the α-form crystals. Meanwhile, only the α-form crystals were precipitated in the system with C1/C2 of less than 3. Phenylalanine concentration (g/100g·H 2 O) Osmotic pressure Π (mOsm/kg·H 2 O) Form of crystal precipitated Phenylalanine concentration C2 (g/100g·H 2 O) C1/C2 5.2 5370 α-form + β-form 1.7 3.1 4.5 5424 α-form 1.7 2.6 3.5 5484 α-form 1.7 2.1 3.0 5292 α-form 1.7 1.8 Example 5 A L-phenylalanine fermentation liquid which was produced according to Example 1 of Japanese Patent second publication (Kokoku) No. 21,079/1976 was centrifuged and sterilized. The sterile liquid was concentrated, then cooled, crystallized and precipitated. The crystals precipitated were separated, washed, and dried to obtain L-phenylalanine crude crystals having an L-phenylalanine content of 95%. The crude crystals (1.7 g) were dissolved in 50 g of water at 60°C to obtain a solution having an L-phenylalanine concentration C1 of 3.2. Subsequently, 25 g of dextrose were added to the solution, and dissolved therein at 60°C. NaCl was added to the mixture such that a predetermined osmotic pressure was reached, and was dissolved therein at 60°C. The mixed solution was cooled to 15°C to crystallize and precipitate L-phenylalanine. At that time, NaCl was added in amounts of 5 g, 6 g and 7 g such that the predetermined osmotic pressure became higher than 4,740 (= 10,500 - 450 × 15 + 4.4 × 15 × 15)(Osm/kg·H 2 O). By comparison, NaCl was added in amounts of 2 g, 3 g and 4 g such that the osmotic pressure became lower than 4,740 mOsm/kg·H 2 O, and the resulting mixtures were also crystallized and precipitated. The phenylalanine concentration in the mother liquor and the crystal form of the obtained phenylalanine are shown in Table 5. Table 5 reveals that the anhydrous crystals (α-form crystals) were obtained preferentially when the osmotic pressure was higher than 4,740 (Osm/kg·H 2 O). Amount of dextrose (g) Amount of NaCl (g) Osmotic pressure Π (mOsm/kg·H 2 O) Form of crystal precipitated C2 (g/100g ·H 2 O) C1/C2 Comparative Examples 25 2 3456 β-form 2.9 1.1 25 3 3916 β-form 2.7 1.2 25 4 4444 β-form 2.5 1.3 Examples 25 5 4872 α-form 2.4 1.3 25 6 5364 α-form 2.3 1.4 25 7 5864 α-form 2.2 1.5 Example 6 The L-phenylalanine fermentation liquid obtained in Example 5 was concentrated to obtain a solution having an L-phenylalanine concentration C1 of 4.0 (g/100g·H 2 O). Then, ammonium sulfate was added to the solution such that this solution was adjusted to a predetermined osmotic pressure, and was then dissolved therein at 40°C. The mixed solution was cooled to 20°C to crystallize and precipitate L-phenylalanine. At that time, ammonium sulfate was added in amounts of 8 g, 10 g and 12 g such that the predetermined osmotic pressure became higher than 3,260 (= 10,500 - 450 × 20 + 4.4 × 20 × 20)(mOsm/kg·H 2 O). By comparison, ammonium sulfate was added in amounts of 2 g, 4 g and 6 g such that the osmotic pressure became lower than 3,260 (mOsm/kg·H 2 O), and the resulting mixtures were also crystallized and precipitated. The phenylalanine concentration in the mother liquor and the crystal form of the obtained phenylalanine are shown in Table 6. Table 6 reveals that the anhydrous crystals (α-form crystals) were obtained preferentially when the osmotic pressure was higher than 3,260 (mosm/kg·H 2 O). Amount of ammonium sulfate (g) Osmotic pressure Π (mOsm/kg·H 2 O) Form of crystal precipitated Phenylalanine concentration C2 (g/100g·H 2 O) C1/C2 Comparative Examples 2 1992 β-form 2.7 1.5 4 2567 β-form 2.6 1.5 6 2890 β-form 2.4 1.7 Examples 8 3450 α-form 2.2 1.8 10 3966 α-form 2.0 2.0 12 4376 α-form 1.8 2.2 Effects of the Invention As has been described above, according to the present invention, the optically active phenylalanine anhydrous crystals having excellent separability can be stably obtained. Since the optically active phenylalanine anhydrous crystals could be obtained so far in the low-temperature region, the improvement in the yield or the like is expected. Thus, it is quite advantageous in view of the industrial production. Brief Explanation of the Drawings Fig. 1 is a graphical representation showing the crystal form of optically active phenylalanine precipitated wherein the crystallization/precipitation temperature is plotted as the ordinate and the osmotic pressure of the solution as the abscissa respectively.

Claims: A method of obtaining optically active phenylalanine anhydrous crystals from an aqueous solution containing optically active phenylalanine, which comprises crystallizing and precipitating the optically active phenylalanine from a saturated solution of optically active phenylalanine, wherein the crystallization/precipitation temperature T is not higher than 37°C, the osmotic pressure π (mOsm/kg·H 2 O) of the saturated solution is at least 10,500 - 450 T + 4.4 T 2 wherein T is the crystallization/precipitation temperature (°C), and the ratio C1/C2 is between 1 and 3, wherein C1 represents the phenylalanine concentration in the optically active phenylalanine containing aqueous solution and C2 represents the phenylalanine concentration in the mother liquor after the crystallization and precipitation of the optically active phenylalanine at the crystallization/precipitation temperature T has been carried out. The method of claim 1, wherein the osmotic pressure π (mOsm/kg·H 2 O) recited in claim 1 is adjusted to at least 10,500 - 450 T + 4.4 T 2 with an additive. The method of claim 2, wherein the additive is selected from the group consisting of aluminum chloride, ammonium chloride, potassium chloride, sodium chloride, ammonium nitrate, potassium nitrate, sodium nitrate, ammonium carbonate, aluminum sulfate, ammonium sulfate, potassium sulfate, aluminum sulfate, sodium sulfate, magnesium sulfate, sodium acetate, potassium acetate, sodium oxalate, potassium oxalate, galactose, glucose, fructose, mannose, sucrose, lactose, maltose, methanol, ethanol, propanol, and mixtures thereof.

Inventors: SANO CHIAKI, SATO TAKERU, SANO, CHIAKI, SATO, TAKERU, Sano, Chiaki, c/o Technology &amp; Engineering Lab., Sato, Takeru, c/o Technology &amp; Engineering Lab.
Applicants: AJINOMOTO KK, AJINOMOTO CO., INC.
Application year: 1995
Main classification: C07C227
IPC codes: C07C227, C07C229