WO2010050499A1 - 光学活性有機カルボン酸の製造方法 - Google Patents
光学活性有機カルボン酸の製造方法 Download PDFInfo
- Publication number
- WO2010050499A1 WO2010050499A1 PCT/JP2009/068484 JP2009068484W WO2010050499A1 WO 2010050499 A1 WO2010050499 A1 WO 2010050499A1 JP 2009068484 W JP2009068484 W JP 2009068484W WO 2010050499 A1 WO2010050499 A1 WO 2010050499A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- carboxylic acid
- organic carboxylic
- optically active
- enantiomers
- active organic
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D311/00—Heterocyclic compounds containing six-membered rings having one oxygen atom as the only hetero atom, condensed with other rings
- C07D311/02—Heterocyclic compounds containing six-membered rings having one oxygen atom as the only hetero atom, condensed with other rings ortho- or peri-condensed with carbocyclic rings or ring systems
- C07D311/04—Benzo[b]pyrans, not hydrogenated in the carbocyclic ring
- C07D311/58—Benzo[b]pyrans, not hydrogenated in the carbocyclic ring other than with oxygen or sulphur atoms in position 2 or 4
- C07D311/66—Benzo[b]pyrans, not hydrogenated in the carbocyclic ring other than with oxygen or sulphur atoms in position 2 or 4 with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached in position 2
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07B—GENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
- C07B57/00—Separation of optically-active compounds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/42—Separation; Purification; Stabilisation; Use of additives
- C07C51/487—Separation; Purification; Stabilisation; Use of additives by treatment giving rise to chemical modification
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07B—GENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
- C07B2200/00—Indexing scheme relating to specific properties of organic compounds
- C07B2200/07—Optical isomers
Definitions
- the present invention relates to a technique for improving the enantiomeric excess of an optically active organic carboxylic acid.
- Optically active organic carboxylic acids are very useful as raw materials for the synthesis of chemical substances that require chirality such as pharmaceuticals and agricultural chemicals.
- an optically active organic carboxylic acid becomes an important synthetic intermediate such as a pharmaceutical intermediate or a functional chemical
- various methods for obtaining an optically active form from a racemate include a preferential crystallization method, a diastereomer method, an enzyme method, and a chromatography method.
- the preferential crystallization method is a method in which desired crystals are inoculated into a racemic supersaturated solution, and only the crystals are grown and precipitated. That is, in order to resolve a racemate by the preferential crystallization method, first, the solubility of the racemate and both optically active substances is measured, and the solubility of the racemate is greater than the solubility of both optically active substances. Confirm that the melting point of both optically active compounds is higher than that of the racemic compound, that the optically active compound does not dissolve in the supersaturated solution of the racemic compound, and that the infrared absorption spectra of the racemic compound and the optically active compound match. (For example, refer nonpatent literature 1).
- the diastereomer method is a method in which an optically active acid or base is allowed to act on a racemate and separated by fractional crystallization according to the difference in solubility of the produced diastereomeric salt (see, for example, Patent Document 1).
- the optical resolution method using an enzyme utilizes the stereospecificity of the enzyme with respect to the substrate. For example, it is a method of separating a target optically active substance by allowing an ester compound to act on a microorganism-derived enzyme having hydrolytic activity and selectively hydrolyzing one of the optically active substances (see, for example, Patent Document 2). ).
- the chromatographic method using a chiral compound as a stationary phase is a method of optical resolution by the interaction of S-form, R-form and a filler.
- An object of the present invention is to provide a simple production method for obtaining an optically active organic carboxylic acid having an improved enantiomeric excess.
- the present inventors have conducted a very simple method of separating a portion of an optically active organic carboxylic acid, which is an enantiomeric mixture, from an alkali salt or a free carboxylic acid.
- the inventors have found a phenomenon that an optically active organic carboxylic acid having a higher enantiomeric excess can be obtained, and completed the present invention.
- the present invention relates to a method for producing an optically active organic carboxylic acid as shown in the following (1) to (7).
- a method for producing an optically active organic carboxylic acid wherein an enantiomer existing in excess in an organic carboxylate is separated by separating the organic carboxylic acid.
- (3) The melting point of the enantiomer equivalent mixture of the optically active organic carboxylic acid is higher than the melting point of the optically active organic carboxylic acid enantiomer of both the S-form and the R-form, the above (1) or (2 ) For producing an optically active organic carboxylic acid.
- (4) The optically active organic carboxylic acid according to any one of the above (1) to (3), wherein the optically active organic carboxylic acid is 6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid A method for producing carboxylic acid.
- the enantiomeric excess of an optically active organic carboxylic acid useful as a pharmaceutical raw material or a synthetic intermediate can be efficiently increased by a simple method.
- Examples of the method for producing an optically active organic carboxylic acid for separating an enantiomer present in excess according to the present invention include the following first method and second method. That is, the first method of the present invention is a method for fractionating enantiomers present in excess from an enantiomeric mixture of optically active organic carboxylic acids, which has a bias in the molar ratio of enantiomers present. Then, as the first neutralization step, the enantiomer mixture of the organic carboxylate is prepared by neutralizing the total amount of the enantiomer mixture of the optically active organic carboxylic acid with an alkali, and then as the second neutralization step.
- the number of moles of 0. 0 calculated from the amount of moles of the enantiomer having a small molar ratio of the enantiomers.
- An organic carboxylic acid obtained by adding 9 to 1.1 times the amount of acid and an unneutralized organic carboxylate are prepared, and then the organic carboxylic acid obtained in the second neutralization step.
- Enantiomer present in excess of the carboxylic acid salt is a method for fractionation.
- the second method of the present invention is a method for fractionating enantiomers present in excess from an enantiomeric mixture of optically active organic carboxylic acids having a bias in the molar ratio of enantiomers present.
- the enantiomeric mixture of the optically active organic carboxylic acid is added to the total number of moles of the optically active organic carboxylic acid- (the number of moles of the enantiomer having a low molar ratio among the enantiomers of the optically active organic carboxylic acid). Obtained by adding an organic carboxylate obtained by adding 0.9 to 1.1 times the number of moles of alkali calculated from (2 times amount)] and an unneutralized organic carboxylic acid.
- an enantiomer existing in excess in an organic carboxylate is separated by separating the organic carboxylate from an unneutralized organic carboxylic acid.
- the alkali or acid necessary to obtain an alkali salt of organic carboxylic acid or a free form of organic carboxylic acid in advance.
- HPLC high performance liquid chromatography
- optically active organic carboxylic acid used in the present invention examples include chroman carboxylic acids represented by the general formula (1), 2- (4-isobutylphenyl) propionic acid, and the like.
- R1, R2 and R4 to R6 each independently represent a methyl group or a hydrogen atom.
- R3 represents a hydroxyl group, a methoxy group or a hydrogen atom.
- the mixture of optically active organic carboxylic acids used in the present invention is an enantiomeric mixture in which the molar ratio of enantiomers is biased, and the method of the present invention involves the moles of both enantiomers of the above optically active organic carboxylic acids.
- This method can be used when the ratios are not equal. That is, the enantiomeric excess of the optically active organic carboxylic acid is preferably 2 to 98% ee, more preferably 5 to 95% ee, still more preferably 10 to 90% ee.
- the enantiomeric excess is an abbreviation for ee, which represents the optical purity of a chiral compound.
- the high effect of the present invention can be expected when the melting point of the racemate is higher than that of the enantiomer (S-form and R-form).
- the melting point of the organic carboxylic acid is preferably 5 ° C. or higher, more preferably 10 ° C. or higher, more preferably 20 ° C. higher than that of the enantiomer (S-form and R-form). More preferably, it is higher.
- the racemate means a 50:50 equivalent mixture of S-form and R-form.
- compounds having such a melting point include 6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid, 2- (4-isobutylphenyl) propionic acid, and the like. However, it is not particularly limited to these.
- the enantiomeric mixture of optically active organic carboxylic acids having a bias in the molar ratio of enantiomers used in the raw material of the present invention should be stereoselective esterification of optically active organic carboxylic acids or use an optical resolving agent.
- an optically active organic carboxylic acid is stereoselectively esterified using a biocatalyst in the presence of an alcohol in an organic solvent, and then in the presence of an organic solvent that separates from water. It can be obtained by adding an alkali to and separating the optically active organic carboxylate of the aqueous layer from the optically active organic carboxylate of the organic layer.
- a hydrolase produced by a microorganism for example, a lipase having stereoselectivity derived from a microorganism or a modified product thereof can be used, and a lipase derived from a microorganism belonging to the genus Candida or a modified product thereof is preferable.
- the lipase produced by Candida antarctica is particularly preferable from the viewpoints of good enantioselectivity and yield, since the esterification reaction proceeds smoothly.
- the form of the biocatalyst is not particularly limited, and the enzyme can be used as it is or as an immobilized enzyme, and further microbial cells can be used as they are as a catalyst.
- Examples of the alcohol and solvent used in the esterification reaction include those described in Patent Document 2 described above.
- the reaction conditions for the esterification reaction are the same as the reaction conditions described in Patent Document 2.
- either the S-isomer or the R-isomer is selectively converted into an optically active ester, and by separating this, the molar ratio of the enantiomer is biased.
- Enantiomeric mixtures of organic carboxylic acids with certain optical activity can be prepared.
- a racemate is reacted with an optically active optical resolving agent to form a diastereomer, and then the diastereomer is separated using a difference in physical properties thereof.
- the diastereomers can be decomposed to obtain enantiomeric mixtures with biased molar ratios.
- the optical resolution agent an optically active organic amine is preferable, and optically active N-benzyl- ⁇ -phenylethylamine is more preferable.
- Various methods such as column chromatography and fractional crystallization can be applied to the separation and purification of diastereomers.
- the amount of alkali used in the first neutralization step is preferably 0.9 to 1.1 times the total number of moles of the optically active organic carboxylic acid, preferably 0.95 to 1.05.
- the double amount is more preferable, and in order to recover the target optically active organic carboxylic acid as intended, it is more preferable to adjust the amount to 1.00 times as much as possible.
- the amount of acid used in the second neutralization step is calculated from twice the number of moles of the enantiomer having a small molar ratio among the enantiomers of the optically active organic carboxylic acid.
- the amount is 0.9 to 1.1 times the number of moles, preferably 0.95 to 1.05 times, and in order to recover the target optically active organic carboxylic acid as intended, 1. More preferably, the amount is adjusted to 00 times.
- “the amount of the enantiomer of the optically active organic carboxylic acid having a low molar ratio is twice the number of moles of the enantiomer” means the excess of the enantiomer of the optically active organic carboxylic acid used in the present invention.
- the rate (ee) can also be calculated by the formula [total number of moles of optically active organic carboxylic acid ⁇ (100 ⁇ ee) / 100].
- the second neutralization step by controlling the amount of acid to be added in the above range, among the enantiomers having a large molar ratio of the optically active organic carboxylate obtained in the first neutralization step, The excess with respect to the enantiomer with a small ratio exists as a carboxylic acid alkali salt without being neutralized.
- the amount of acid used for the neutralization operation is calculated as a mole calculated from twice the number of moles of the R-form.
- the enantiomeric excess of the S-form can be increased efficiently.
- the enantiomeric excess of the R-isomer can be increased efficiently. If the amount of acid used is more than 1.1 times, the enantiomeric excess is not sufficiently increased. On the other hand, if the amount of acid used is less than 0.9 times, the enantiomeric excess of the resulting optically active organic carboxylic acid is improved, but the yield is greatly reduced.
- the amount of alkali used in the neutralization operation is [total number of moles of optically active organic carboxylic acid ⁇ (enantiomers having a low molar ratio among the enantiomers of optically active organic carboxylic acid]
- the amount is 0.9 to 1.1 times the number of moles calculated from the number of moles calculated from the number of moles]], preferably 0.95 to 1.05 times the amount of the target optically active organic carboxylic acid.
- the excess relative to the enantiomer having the small molar ratio is neutralized. It exists as a carboxylic acid alkali salt.
- the excess of the enantiomer in the S-form is sufficient if the amount of alkali used in the neutralization operation is in the above range. Can be increased efficiently.
- the R-isomer to be separated is in excess of the S-isomer, the enantiomeric excess of the R-isomer can be increased efficiently.
- the amount of alkali used is more than 1.1 times, the enantiomeric excess is not sufficiently increased.
- the amount of alkali used is less than 0.9 times, the enantiomeric excess of the resulting optically active organic carboxylic acid is improved, but the yield is greatly reduced.
- Examples of the alkali for neutralization for converting an organic carboxylic acid into a salt used in the present invention include alkali metal hydroxides, alkali metal carbonates, ammonia, and organic amines having no optical activity.
- Specific examples of the alkali metal hydroxide include sodium hydroxide, potassium hydroxide, cesium hydroxide, rubidium hydroxide, and examples of the alkali metal carbonate include sodium carbonate, potassium carbonate, cesium carbonate, and rubidium carbonate.
- Examples of organic amines having no optical activity include methylamine, dimethylamine, trimethylamine, ethylamine, diethylamine, and triethylamine.
- the alkali for neutralization is not particularly limited to these. However, since this method is different from the diastereomer resolution method, it is not necessary to use an optically active amine used for diastereomer resolution.
- Acids used to neutralize organic carboxylates include sulfuric acid, hydrochloric acid, nitric acid, potassium hydrogen sulfate, and sodium hydrogen sulfate as inorganic acids, and formic acid, acetic acid, propionic acid, and organic acids having no optical activity.
- Examples include butyric acid and the like, but are not particularly limited thereto, as long as the organic carboxylate is liberated to carboxylic acid.
- These neutralization operations are preferably performed in an aqueous solution, but can also be performed in a mixed solvent with a solvent mixed with water.
- the solvent mixed with water include alcohols such as methanol, ethanol, 2-propanol, acetonitrile, dimethylformamide, and the like, but are not limited thereto. Salt solubility, substrate solubility It may be properly used depending on the situation.
- the ratio between the substrate containing the organic carboxylate and organic carboxylic acid and the solvent can be arbitrarily determined. However, in actual operation, it is preferable to consider the properties of the material to be handled. For example, organic carboxylic acid If the alkali salt is not sufficiently dissolved in the solution, the ratio of the solvent may be increased. On the other hand, it can be said that it is not preferable to extremely increase the amount of the solvent, which is accompanied by deterioration in economic efficiency or increase in environmental burden. In any case, it is better to optimize these in advance before industrial implementation.
- the temperature for forming the organic carboxylate is arbitrarily determined, but is preferably 0 to 100 ° C. from the viewpoint of operability, and may be determined in consideration of the physical properties of the substrate and the like.
- the temperature at which the organic carboxylate is neutralized is arbitrarily determined, but it is preferably 0 to 100 ° C. from the viewpoint of operability, and may be determined in consideration of the physical properties of the substrate.
- the separation temperature is preferably near room temperature in operation, the separation temperature may be determined in consideration of the physical properties of the substrate.
- Acid or alkali can be added at once, but it is preferable to add them little by little. Moreover, although it can also isolate
- the organic carboxylic acid and the organic carboxylate obtained above are separated from each other, and the organic carboxylate is recovered by adding an acid to form a free organic carboxylic acid.
- the free organic carboxylic acid if the carboxylic acid is a crystal, it is easy to separate it by filtration. Separation methods can be performed by vacuum filtration, pressure filtration, centrifugal filtration, etc., but are not particularly limited to these methods, and are appropriately efficient in consideration of crystal form and the like when industrially implemented. However, if the organic carboxylic acid is in a liquid state and has good layer separation properties with water or an aqueous solution, the separation may be performed as it is by decantation or the like.
- the organic carboxylic acid When the organic carboxylic acid is soluble in the solution, it is preferable to extract it using a solvent that does not mix with water, for example, ethyl acetate, toluene, ethyl ether, or the like. If the organic carboxylic acid solution recovered by extraction is concentrated to dryness, the organic carboxylic acid having an improved enantiomeric ratio can be easily recovered.
- a solvent that does not mix with water for example, ethyl acetate, toluene, ethyl ether, or the like.
- a carboxylic acid having a low enantiomeric excess can be efficiently converted to a carboxylic acid having a high enantiomeric excess.
- the yield of primary crystals was 0.95 g, and the optical purity of R-(+)-6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid in the crystals was 7.4% ee. there were.
- the yield of secondary crystals was 4.50 g, and the optical purity of R-(+)-6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid in the crystals was 97.3% ee. there were. Table 1 shows the results.
- Example 2 The aqueous layer recovered in (1) of Example 1 was charged into a 500 mL glass container, and heated with stirring at 50 ° C., 4.05 ml (21.97 mmol) of 21.97 ml (21.97 mmol) of 1N hydrochloric acid prepared. 97 ml ⁇ (100-81) /100 ⁇ 0.97 times) was added, and the released primary crystals were separated by filtration. Subsequently, the remaining 17.N ml of 1N hydrochloric acid was added to the obtained filtrate, and the liberated secondary crystals were separated by filtration.
- the yield of primary crystals was 0.80 g, and the optical purity of R-(+)-6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid in the crystals was 2.7% ee. there were.
- the yield of secondary crystals was 4.63 g, and the optical purity of R-(+)-6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid in the crystals was 95.4% ee. there were.
- Table 1 The results are shown in Table 1.
- Example 3 The aqueous layer collected in (1) of Example 1 was charged into a 500 mL glass container, and 4.30 ml (21.97 ml) of 21.97 ml (21.97 mmol) of 1N hydrochloric acid prepared while heating and stirring at 50 ° C. 97 ml ⁇ (100-81) /100 ⁇ 1.03 times) was added, and the released primary crystals were separated by filtration. Subsequently, the remaining 1N hydrochloric acid (17.67 ml) was added to the obtained filtrate, and the liberated secondary crystals were separated by filtration.
- the yield of primary crystals was 1.00 g, and the optical purity of R-(+)-6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid in the crystals was 8.3% ee. there were.
- the yield of secondary crystals was 4.40 g, and the optical purity of R-(+)-6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid in the crystals was 98.0% ee. there were.
- Table 1 The results are shown in Table 1.
- Comparative Example 1 The aqueous layer collected in (1) of Example 1 was charged into a 500 mL glass container, and heated to 50 ° C. while stirring at 0.88 ml (21.97 mmol) of 21.97 ml (21.97 mmol) of 1N hydrochloric acid prepared. 97 ml ⁇ (100-81) /100 ⁇ 0.21 times) was added, and the liberated primary crystals were separated by filtration. Subsequently, 21.09 ml of the remaining 1N hydrochloric acid was added to the obtained filtrate, and the liberated secondary crystals were separated by filtration.
- the yield of primary crystals was 0.21 g, and the optical purity of R-(+)-6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid in the crystals was 2.1% ee. there were.
- the yield of secondary crystals was 5.20 g, and the optical purity of R-(+)-6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid in the crystals was 84.3% ee. there were.
- Table 1 The results are shown in Table 1.
- Comparative Example 2 The aqueous layer recovered in (1) of Example 1 was charged into a 500 mL glass container, and heated and stirred at 50 ° C., 6.39 ml (21.97 ml) of 21.97 ml (21.97 mmol) of 1N hydrochloric acid prepared. 97 ml ⁇ (100-81) /100 ⁇ 1.53 times) was added, and the released primary crystals were separated by filtration. Next, 15.58 ml of the remaining 1N hydrochloric acid was added to the obtained filtrate, and the liberated secondary crystals were separated by filtration.
- the yield of primary crystals was 1.50 g, and the optical purity of R-(+)-6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid in the crystals was 37.5ee. .
- the yield of secondary crystals was 3.88 g, and the optical purity of R-(+)-6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid in the crystals was 97.9% ee. there were.
- the results are shown in Table 1.
- the yield of primary crystals was 0.94 g, and the optical purity of R-(+)-6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid in the primary crystals was 7.1%. It was ee.
- the yield of secondary crystals was 4.51 g, and the optical purity of R-(+)-6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid in the secondary crystals was 97.2%. It was ee.
- the results are shown in Table 2.
- Example 5 21.97 ml (21.97 mmol) of 1N hydrochloric acid was prepared, and the aqueous layer recovered in (1) of Example 1 was charged into a 500 mL glass container, and heated with stirring at 50 ° C., 4.13 ml (21 97 ml ⁇ (100-81) /100 ⁇ 0.99 times) was added. After free primary crystals were removed by filtration, the remaining 17.82 ml of 1N hydrochloric acid was added. The liberated secondary crystals were obtained by filtration. The yield of primary crystals was 0.95 g, and the optical purity of R-(+)-6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid in the primary crystals was 8.3%.
- Example 6 Charge and dissolve 6.40 g (31.02 mmol) of R-2- (4-isobutylphenyl) propionic acid with an optical purity of 50% ee and 310.2 ml (31.02 mmol) of 0.1N sodium hydroxide in a 500 mL glass container. I let you. 31.02 ml (31.02 mmol) of 1N hydrochloric acid was prepared, and 15.51 ml (31.02 ml ⁇ (100-50) / 100) of 1N hydrochloric acid was added while stirring at 25 ° C. After free primary crystals were removed by filtration, the remaining 15.5 ml of 1N hydrochloric acid was added, and free secondary crystals were obtained by filtration.
- the yield of primary crystals was 3.20 g, and the optical purity of R-2- (4-isobutylphenyl) propionic acid in the primary crystals was 14% ee.
- the yield of secondary crystals was 3.10 g, and the optical purity of R-2- (4-isobutylphenyl) propionic acid in the secondary crystals was 86% ee.
- the results are shown in Table 3.
- Example 7 21.97 ml (21.97 mmol) of 1N hydrochloric acid was prepared, and the aqueous layer collected in (1) of Example 1 was charged into a 500 mL glass container, and heated to 70 ° C. while being heated and stirred at 4.09 ml (21 97 ml ⁇ (100-81) /100 ⁇ 0.98 times) was added. After free primary crystals were removed by filtration, 17.87 ml of 1N hydrochloric acid was added. The liberated secondary crystals were obtained by filtration. The yield of primary crystals was 0.85 g, and the optical purity of R-(+)-6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid in the primary crystals was 3.5%.
- Example 8 6.00 g (23.97 mmol) of 6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid having an optical purity of 50% ee and 239.7 ml (11.98 mmol) of 0.05N sodium hydroxide was placed in a 500 mL glass container and heated and stirred at 50 ° C. for 1 hour. After 1 hour, undissolved crystals were removed by filtration, and 11.98 ml of 1N hydrochloric acid was added. The liberated secondary crystals were obtained by filtration. The yield of the primary crystal was 2.92 g, and the optical purity of the primary crystal was 5.2% ee. The yield of secondary crystals was 2.85 g, and the optical purity of the secondary crystals was 94.2% ee. The results are shown in Table 3.
- Example 9 Production of S-( ⁇ )-6-hydroxy-2,5,7,8-tetramethylchroman-2-carboxylic acid
- the mother liquor 38.1% ee
- 0.1N aqueous sodium hydroxide solution was added thereto, followed by extraction washing with 50 ml of MTBE twice.
- 28.76 ml of 1N hydrochloric acid was prepared, and 17.83 ml of 1N hydrochloric acid was first added while heating and stirring the aqueous layer collected at 50 ° C.
- the present invention provides a simple method for obtaining an optically active organic carboxylic acid having an improved enantiomeric excess from an enantiomeric mixture of optically active organic carboxylic acids having a bias in the existing molar ratio of enantiomers.
- a method can be provided.
- An optically active organic carboxylic acid with an improved enantiomeric excess is very useful as a raw material for synthesizing chemical substances such as pharmaceuticals and agricultural chemicals that require chirality.
Abstract
Description
キラルな化合物を固定相とするクロマトグラフィー法はS-体、R-体と充填材の相互作用によって光学分割する方法である。
(1)鏡像異性体の存在モル比に偏りがある、光学活性有機カルボン酸の鏡像異性体混合物から、過剰に存在する鏡像異性体を分取する方法であって、第1中和工程として、該光学活性有機カルボン酸の鏡像異性体混合物の全量をアルカリで中和して有機カルボン酸塩の鏡像異性体混合物を調製した後、第2中和工程として、第1中和工程で得られた有機カルボン酸塩の鏡像異性体混合物に、該鏡像異性体のうち存在モル比が少ない鏡像異性体のモル数の2倍量から算出されるモル数の0.9~1.1倍量の酸を加えて得られる有機カルボン酸と、未中和の有機カルボン酸塩とを調製し、次に該第2中和工程で得られた、有機カルボン酸と未中和の有機カルボン酸塩とを分離することによって、未中和の有機カルボン酸塩中の過剰に存在する鏡像異性体を分取する、光学活性有機カルボン酸の製造方法。
(2)鏡像異性体の存在モル比に偏りがある、光学活性有機カルボン酸の鏡像異性体混合物から、過剰に存在する鏡像異性体を分取する方法であって、該光学活性有機カルボン酸の鏡像異性体混合物に、[光学活性有機カルボン酸の全モル数-(光学活性有機カルボン酸の鏡像異性体のうち存在モル比が少ない鏡像異性体のモル数の2倍量)]から算出されるモル数の0.9~1.1倍量のアルカリを加えて得られる有機カルボン酸塩と、未中和の有機カルボン酸とを調製した後、得られた有機カルボン酸塩と未中和の有機カルボン酸とを分離することによって、有機カルボン酸塩中の過剰に存在する鏡像異性体を分取する、光学活性有機カルボン酸の製造方法。
(3)光学活性有機カルボン酸の鏡像異性体等量混合物の融点が、S-体及びR-体の双方の光学活性有機カルボン酸鏡像異性体の融点よりも高い、上記(1)又は(2)に記載の光学活性有機カルボン酸の製造方法。
(4)光学活性有機カルボン酸が、6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸である、上記(1)~(3)のいずれかに記載の光学活性有機カルボン酸の製造方法。
(5)光学活性有機カルボン酸が、2-(4-イソブチルフェニル)プロピオン酸である、上記(1)~(3)のいずれかに記載の光学活性有機カルボン酸の製造方法。
(6)中和用の酸として、鉱酸または光学活性を有さない有機酸を用いる、上記(1)に記載の光学活性有機カルボン酸の製造方法。
(7)中和用のアルカリとして、アルカリ金属の水酸化物若しくは炭酸塩、アンモニアまたは光学活性を有さない有機アミン類を用いる、上記(1)又は(2)に記載の光学活性有機カルボン酸の製造方法。
すなわち、本発明の第1の方法としては、鏡像異性体の存在モル比に偏りがある、光学活性有機カルボン酸の鏡像異性体混合物から、過剰に存在する鏡像異性体を分取する方法であって、第1中和工程として、該光学活性有機カルボン酸の鏡像異性体混合物の全量をアルカリで中和して有機カルボン酸塩の鏡像異性体混合物を調製した後、第2中和工程として、第1中和工程で得られた有機カルボン酸塩の鏡像異性体混合物に、該鏡像異性体のうち存在モル比が少ない鏡像異性体のモル数の2倍量から算出されるモル数の0.9~1.1倍量の酸を加えて得られる有機カルボン酸と、未中和の有機カルボン酸塩とを調製し、次に該第2中和工程で得られた、有機カルボン酸と未中和の有機カルボン酸塩とを分離することによって、未中和の有機カルボン酸塩中の過剰に存在する鏡像異性体を分取する方法である。
鏡像異性体過剰率(enantiomeric excess)とはキラルな化合物の光学純度を表す言葉でeeと略される。eeは多い方の物質量から少ないほうの物質量を引き、全体の物質量で割った値で表される(多いほうの物質量比から少ない方の物質量比を引いても良い)。
また、対象となる有機カルボン酸の性質として、鏡像異性体(S-体及びR-体)よりも、ラセミ体の融点が高い場合に本発明の高い効果を期待できる。この観点から、有機カルボン酸の融点は、鏡像異性体(S-体及びR-体)よりも、ラセミ体の融点が5℃以上高いことが好ましく、10℃以上高いことがより好ましく、20℃以上高いことが更に好ましい。なお、ラセミ体とは、S-体及びR-体の50:50の等量混合物をいう。
具体的に、融点がこのような性質を有する化合物としては6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸、2-(4-イソブチルフェニル)プロピオン酸などが挙げられるが、特にこれらに限定されるものではない。
上記のエステル化法としては、例えば、光学活性有機カルボン酸を、有機溶媒中、アルコールの存在下、生体触媒を用いて立体選択的にエステル化した後に、水と層分離する有機溶媒の存在下にアルカリを加え、有機層の光学活性有機カルボン酸エステルから水層の光学活性有機カルボン酸塩を分離することによって得ることができる。
生体触媒としては、微生物が産生する加水分解酵素、例えば、微生物由来の立体選択性を有するリパーゼまたはその修飾物を使用することができ、キャンディダ属に属する微生物由来のリパーゼまたはその修飾物が好ましい。特に、Candida antarcticaの産生するリパーゼは該エステル化反応を円滑に進行させるので、エナンチオ選択性や収率が良好である等の点から特に好ましい。上記生体触媒の形態は特に限定されず、酵素のまま、或いは固定化酵素として、更には微生物細胞をそのまま触媒として用いることが出来る。
エステル化反応に用いるアルコール及び溶媒としては、前述した特許文献2に記載されているものが同様に挙げられる。また、エステル化反応の反応条件は、上記特許文献2に記載の反応条件と同様である。
上記の方法において、鏡像異性体混合物の一方の鏡像異性体だけが生体触媒の作用によりエステル化され、他方の鏡像異性体は未反応のまま残る。従って、上記方法によって、S-体又はR-体の何れか一方の鏡像異性体が選択的に光学活性なエステルに変換され、これを分離することにより、鏡像異性体の存在モル比に偏りがある光学活性を有する有機カルボン酸の鏡像異性体混合物を製造することができる。
光学分割剤としては、光学活性有機アミンが好ましく、光学活性なN-ベンジル-α-フェニルエチルアミンがより好ましい。ジアステレオマーの分離精製には、カラムクロマトグラフィーや分別結晶法など、各種の手法が適用可能である。
本発明の第1の方法において、第1中和工程に用いるアルカリの量は、光学活性有機カルボン酸の全モル数の0.9~1.1倍量が好ましく、0.95~1.05倍量がより好ましく、目的とする光学活性有機カルボン酸を狙い通りに回収するためには、できる限り1.00倍量に合わせることが更に好ましい。
第2中和工程では、加える酸の量を上記の範囲に制御することにより、第1中和工程で得られる光学活性有機カルボン酸塩の存在モル比が多い鏡像異性体の中で、存在モル比が少ない鏡像異性体に対する過剰分が未中和のままカルボン酸アルカリ塩として存在する。
分離しようとする両鏡像異性体において、S-体がR-体よりも過剰である場合は、中和操作に用いる酸の量は、R-体のモル数の2倍量から算出されるモル数の0.9~1.1倍量であり、0.95~1.05倍が好ましい。中和操作に用いる酸の量が上記の範囲であれは、S-体の鏡像異性体過剰率を効率的に高めることができる。逆に、分離しようとするR-体がS-体よりも過剰である場合には、R-体の鏡像異性体過剰率を効率的に高めることができる。1.1倍よりも使用する酸の量が多すぎる場合には、鏡像異性体過剰率は十分に上がらない。一方、0.9倍よりも使用する酸の量が少なすぎると、得られる光学活性有機カルボン酸の鏡像異性体過剰率は向上するが、収量が大幅に減少することになる。
中和操作に用いるアルカリの量を上記の範囲に制御することにより、光学活性有機カルボン酸の存在モル比が多い鏡像異性体の中で、存在モル比が少ない鏡像異性体に対する過剰分が中和されカルボン酸アルカリ塩として存在する。
分離しようとする両鏡像異性体において、S-体がR-体よりも過剰である場合は、中和操作に用いるアルカリの量が上記の範囲であれは、S-体の鏡像異性体過剰率を効率的に高めることができる。逆に、分離しようとするR-体がS-体よりも過剰である場合には、R-体の鏡像異性体過剰率を効率的に高めることができる。1.1倍よりも使用するアルカリの量が多すぎる場合には、鏡像異性体過剰率は十分に上がらない。一方、0.9倍よりも使用するアルカリの量が少なすぎると、得られる光学活性有機カルボン酸の鏡像異性体過剰率は向上するが、収量が大幅に減少することになる。
製造例1
6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の不斉エステル化
原料の6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸100g(399.5mmol)、メタノール60g、イソプロピルエーテル1500g、不斉エステル化触媒として固定化酵素ノボザイム435(ノボザイムス社製)40gを、5Lのステンレス製耐圧容器に仕込み、アルゴンで置換した後、80℃で24時間反応を行った。24時間後、濾過によって触媒を取り除き反応液を回収した。反応液を分析すると、原料の6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の転化率は45.0mol%、S-(-)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸メチルの光学純度は99%eeであった。一方、R-(+)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は81%eeであった。なお、光学純度の分析は高速液体クロマトグラフィー(HPLC)で行った。以上のようにして得られた反応液を10等分して、以下の試験に用いた。
(1)未反応の6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の回収
10等分した上記反応液に、0.1N水酸化ナトリウム219.7ml(399.5mmol÷10×(1-0.45)=21.97mmol)を加え、未反応の6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸をナトリウム塩となすことによって水層に除去し回収した。
上記(1)で回収した水層を500mLのガラス容器に仕込み、50℃に加温攪拌しながら、準備した1N塩酸21.97ml(21.97mmol)のうちの4.17ml(21.97mmol×(100-81)/100=4.17mmol)を加え、遊離した1次結晶を濾別した。次いで、得られた濾液に残りの1N塩酸17.80mlを加え、遊離した2次結晶を濾別した。
1次結晶の収量は0.95gとなり、結晶中のR-(+)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は7.4%eeであった。
2次結晶の収量は4.50gとなり、結晶中のR-(+)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は97.3%eeであった。表1に結果を示す。
実施例1の(1)で回収した水層を500mLのガラス容器に仕込み、50℃に加温攪拌しながら、準備した1N塩酸21.97ml(21.97mmol)のうちの4.05ml(21.97ml×(100-81)/100×0.97倍)を加え、遊離した1次結晶を濾別した。次いで、得られた濾液に残りの1N塩酸17.92mlを加え、遊離した2次結晶を濾別した。
1次結晶の収量は0.80gとなり、結晶中のR-(+)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は2.7%eeであった。
2次結晶の収量は4.63gとなり、結晶中のR-(+)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は95.4%eeであった。結果を表1に示す。
実施例1の(1)で回収した水層を500mLのガラス容器に仕込み、50℃に加温攪拌しながら、準備した1N塩酸21.97ml(21.97mmol)のうちの4.30ml(21.97ml×(100-81)/100×1.03倍)を加え、遊離した1次結晶を濾別した。次いで、得られた濾液に残りの1N塩酸17.67mlを加え、遊離した2次結晶を濾別した。
1次結晶の収量は1.00gとなり、結晶中のR-(+)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は8.3%eeであった。
2次結晶の収量は4.40gとなり、結晶中のR-(+)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は98.0%eeであった。結果を表1に示す。
実施例1の(1)で回収した水層を500mLのガラス容器に仕込み、50℃に加温攪拌しながら、準備した1N塩酸21.97ml(21.97mmol)のうちの0.88ml(21.97ml×(100-81)/100×0.21倍)を加え、遊離した1次結晶を濾別した。次いで、得られた濾液に残りの1N塩酸21.09mlを加え、遊離した2次結晶を濾別した。
1次結晶の収量は0.21gとなり、結晶中のR-(+)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は2.1%eeであった。
2次結晶の収量は5.20gとなり、結晶中のR-(+)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は84.3%eeであった。結果を表1に示す。
実施例1の(1)で回収した水層を500mLのガラス容器に仕込み、50℃に加温攪拌しながら、準備した1N塩酸21.97ml(21.97mmol)のうちの6.39ml(21.97ml×(100-81)/100×1.53倍)を加え、遊離した1次結晶を濾別した。次いで、得られた濾液に残りの1N塩酸15.58mlを加え、遊離した2次結晶を濾別した。
1次結晶の収量は1.50gとなり、結晶中のR-(+)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は37.5eeであった。
2次結晶の収量は3.88gとなり、結晶中のR-(+)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は97.9%eeであった。結果を表1に示す。
(1)未反応の6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の回収
製造例1で得られた反応液を10等分したものに、0.1Nアンモニア21.97ml(39.95×(1-0.45)=21.97mmol)を加え、未反応の6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸をアンモニウム塩となすことによって水層に除去し回収した。
1N塩酸21.97ml(21.97mmol)を準備し、つづいて上記の回収した水層を500mLのガラス容器に仕込み、50℃に加温攪拌しながら、1N塩酸4.17ml(21.97ml×(100-81)/100)を加えた。遊離した一次結晶を濾過によって除いた後に、残りの1N塩酸17.8mlを加え、遊離した2次結晶を濾過によって得た。
1次結晶の収量は0.94gとなり、1次結晶中のR-(+)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は7.1%eeであった。
2次結晶の収量は4.51gとなり、2次結晶中のR-(+)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は97.2%eeであった。結果を表2に示す。
1N塩酸21.97ml(21.97mmol)を準備し、実施例1の(1)で回収した水層を500mLのガラス容器に仕込み、50℃に加温攪拌しながら、1N塩酸4.13ml(21.97ml×(100-81)/100×0.99倍)を加えた。遊離した一次結晶を濾過によって除いた後に、残りの1N塩酸17.82mlを加えた。遊離した2次結晶を濾過によって得た。
1次結晶の収量は0.95gとなり、1次結晶中のR-(+)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は8.3%eeであった。
2次結晶の収量は4.40gとなり、2次結晶中のR-(+)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は96.7%eeであった。結果を表2に示す。
1N塩酸21.97ml(21.97mmol)を準備し、実施例1の(1)で回収した水層とメタノール50mlを500mLのガラス容器に仕込み、50℃に加温攪拌しながら、1N塩酸6.37mlを加えた。遊離した一次結晶を濾過によって除いた後に、残りの1N塩酸15.60mlを加えた。遊離した2次結晶を濾過によって得た。
1次結晶の収量は1.51gとなり、1次結晶中のR-(+)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は37.5%eeであった。
2次結晶の収量は3.87gとなり、2次結晶中のR-(+)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は97.9%eeであった。結果を表2に示す。
光学純度が50%eeのR-2-(4-イソブチルフェニル)プロピオン酸6.40g(31.02mmol)と0.1N水酸化ナトリウム310.2ml(31.02mmol)を500mLのガラス容器に仕込み溶解させた。1N塩酸31.02ml(31.02mmol)を準備し、25℃で攪拌しながら、1N塩酸15.51ml(31.02ml×(100-50)/100)を加えた。遊離した一次結晶を濾過によって除いた後に、残りの1N塩酸15.5mlを加え、遊離した2次結晶を濾過によって得た。
1次結晶の収量は3.20gとなり、1次結晶中のR-2-(4-イソブチルフェニル)プロピオン酸の光学純度は14%eeであった。
2次結晶の収量は3.10gとなり、2次結晶中のR-2-(4-イソブチルフェニル)プロピオン酸の光学純度は86%eeであった。結果を表3に示す。
1N塩酸21.97ml(21.97mmol)を準備し、実施例1の(1)で回収した水層を500mLのガラス容器に仕込み、70℃に加温攪拌しながら、1N塩酸4.09ml(21.97ml×(100-81)/100×0.98倍)を加えた。遊離した一次結晶を濾過によって除いた後に、1N塩酸17.87mlを加えた。遊離した2次結晶を濾過によって得た。
1次結晶の収量は0.85gとなり、1次結晶中のR-(+)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は3.5%eeであった。
2次結晶の収量は4.57gとなり、2次結晶中のR-(+)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は95.8%eeであった。結果を表3に示す。
光学純度が50%eeの6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸6.00g(23.97mmol)と0.05N水酸化ナトリウム239.7ml(11.98mmol)を500mLのガラス容器に仕込み、1時間、50℃に加温攪拌した。1時間後に、未溶解の結晶を濾過によって除いた後に、1N塩酸11.98mlを加えた。遊離した2次結晶を濾過によって得た。
1次結晶の収量は2.92gとなり、1次結晶の光学純度は5.2%eeであった。
2次結晶の収量は2.85gとなり、2次結晶の光学純度は94.2%eeであった。結果を表3に示す。
6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸のジアステレオマー分割
6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸10.00g(39.95mmol)、R-(+)-N-ベンジル-α-フェニルエチルアミン8.45g(39.95mmol)、イソプロパノール100mlを混合し50℃まで加熱した後、2℃の温度条件下で一夜放置した。析出した結晶を濾過することにより、結晶(乾燥重量5.17g、回収率28%)と母液を回収した。
このようにして得られた結晶5.17gに1N水酸化ナトリウム水溶液12mlを加え溶解した。この溶液を50mlのメチルターシャリーブチルエーテル(MTBE)で2回抽出洗浄した後、1N塩酸12mlを加え中和した。析出した結晶を濾過乾燥し分析したところ、結晶の収量は2.75gとなり、R-(+)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は98ee%であった。
S-(-)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の製造
製造例2において、ジアステレオマー分割をした時の母液(38.1%ee)を蒸発乾燥し、そこに0.1N水酸化ナトリウム水溶液287.6ml(39.95×(1-0.28)=28.76mmol)を加え50mlのMTBEで2回抽出洗浄した。1N塩酸28.76mlを準備し、上記のようにして回収した水層を50℃に加温攪拌しながら、まず、1N塩酸17.83mlを加えた。濾過によって1次結晶を得た後、1N塩酸10.93mlを加え濾過によって2次結晶を得た。
1次結晶の収量は4.35gとなり、結晶中のS-(-)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は2.3%eeであった。
2次結晶の収量は2.70gとなり、結晶中のS-(-)-6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸の光学純度は94.6%eeであった。
Claims (7)
- 鏡像異性体の存在モル比に偏りがある、光学活性有機カルボン酸の鏡像異性体混合物から、過剰に存在する鏡像異性体を分取する方法であって、第1中和工程として、該光学活性有機カルボン酸の鏡像異性体混合物の全量をアルカリで中和して有機カルボン酸塩の鏡像異性体混合物を調製した後、第2中和工程として、第1中和工程で得られた有機カルボン酸塩の鏡像異性体混合物に、該鏡像異性体のうち存在モル比が少ない鏡像異性体のモル数の2倍量から算出されるモル数の0.9~1.1倍量の酸を加えて得られる有機カルボン酸と、未中和の有機カルボン酸塩とを調製し、次に該第2中和工程で得られた、有機カルボン酸と未中和の有機カルボン酸塩とを分離することによって、未中和の有機カルボン酸塩中の過剰に存在する鏡像異性体を分取する、光学活性有機カルボン酸の製造方法。
- 鏡像異性体の存在モル比に偏りがある、光学活性有機カルボン酸の鏡像異性体混合物から、過剰に存在する鏡像異性体を分取する方法であって、該光学活性有機カルボン酸の鏡像異性体混合物に、[光学活性有機カルボン酸の全モル数-(光学活性有機カルボン酸の鏡像異性体のうち存在モル比が少ない鏡像異性体のモル数の2倍量)]から算出されるモル数の0.9~1.1倍量のアルカリを加えて得られる有機カルボン酸塩と、未中和の有機カルボン酸とを調製した後、得られた有機カルボン酸塩と未中和の有機カルボン酸とを分離することによって、有機カルボン酸塩中の過剰に存在する鏡像異性体を分取する、光学活性有機カルボン酸の製造方法。
- 光学活性有機カルボン酸の鏡像異性体等量混合物の融点が、S-体及びR-体の双方の光学活性有機カルボン酸鏡像異性体の融点よりも高い、請求項1又は2に記載の光学活性有機カルボン酸の製造方法。
- 光学活性有機カルボン酸が、6-ヒドロキシ-2,5,7,8-テトラメチルクロマン-2-カルボン酸である、請求項1~3のいずれかに記載の光学活性有機カルボン酸の製造方法。
- 光学活性有機カルボン酸が、2-(4-イソブチルフェニル)プロピオン酸である、請求項1~3のいずれかに記載の光学活性有機カルボン酸の製造方法。
- 中和用の酸として、鉱酸または光学活性を有さない有機酸を用いる、請求項1に記載の光学活性有機カルボン酸の製造方法。
- 中和用のアルカリとして、アルカリ金属の水酸化物若しくは炭酸塩、アンモニアまたは光学活性を有さない有機アミン類を用いる、請求項1又は2に記載の光学活性有機カルボン酸の製造方法。
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US13/126,281 US20110251407A1 (en) | 2008-10-29 | 2009-10-28 | Process for production of optically active organic carboxylic acid |
EP09823609.4A EP2351729B1 (en) | 2008-10-29 | 2009-10-28 | Process for production of optically active organic carboxylic acid |
CN2009801436142A CN102203047B (zh) | 2008-10-29 | 2009-10-28 | 光学活性有机羧酸的制造方法 |
JP2010535812A JP5598330B2 (ja) | 2008-10-29 | 2009-10-28 | 光学活性有機カルボン酸の製造方法 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2008-278496 | 2008-10-29 | ||
JP2008278496 | 2008-10-29 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2010050499A1 true WO2010050499A1 (ja) | 2010-05-06 |
Family
ID=42128859
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2009/068484 WO2010050499A1 (ja) | 2008-10-29 | 2009-10-28 | 光学活性有機カルボン酸の製造方法 |
Country Status (5)
Country | Link |
---|---|
US (1) | US20110251407A1 (ja) |
EP (1) | EP2351729B1 (ja) |
JP (1) | JP5598330B2 (ja) |
CN (1) | CN102203047B (ja) |
WO (1) | WO2010050499A1 (ja) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2986804A1 (fr) * | 2012-02-09 | 2013-08-16 | Servier Lab | Procede de synthese enzymatique de l'acide (7s) 3,4-dimethoxybicyclo[4.2.0]octa-1,3,5-triene 7-carboxylique ou de ses esters, et application a la synthese de l'ivabradine et de ses sels |
EP3233819A1 (en) | 2014-12-16 | 2017-10-25 | Bioelectron Technology Corporation | Methods for chiral resolution of trolox |
WO2021167095A1 (ja) | 2020-02-21 | 2021-08-26 | 大日本住友製薬株式会社 | 光学分割されたトロロックス中間体およびその製造方法 |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06507159A (ja) * | 1991-05-13 | 1994-08-11 | ザ ブーツ カンパニー ピーエルシー | 治療薬 |
JPH07149688A (ja) * | 1993-11-26 | 1995-06-13 | Teikoku Chem Ind Corp Ltd | 2−アリールプロピオン酸化合物の光学分割方法 |
WO2002012221A1 (fr) * | 2000-08-03 | 2002-02-14 | Kuraray Co., Ltd. | Procede de resolution optique de l'acide (±)-6-hydroxy-2,5,7,8,-tetramethyle de coumarone-2-carboxylique |
WO2004108944A1 (ja) | 2003-06-04 | 2004-12-16 | Mitsubishi Gas Chemical Company, Inc. | 光学活性クロマンカルボン酸エステルの製造方法 |
JP2005023055A (ja) | 2003-07-04 | 2005-01-27 | Mitsubishi Gas Chem Co Inc | 新規光学活性アミン |
JP2008044856A (ja) * | 2006-08-11 | 2008-02-28 | Mitsubishi Rayon Co Ltd | α−ヒドロキシカルボン酸の製造方法 |
WO2008050829A1 (fr) * | 2006-10-26 | 2008-05-02 | Mitsubishi Gas Chemical Company, Inc. | Procédé de fabrication de l'acide s -(-)-6-hydroxy-2,5,7,8-tétraméthylchromane-2-carboxylique et produit obtenu par le procédé |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4003919A (en) * | 1973-11-19 | 1977-01-18 | Hoffmann-La Roche Inc. | Antioxidant chroman compounds |
US5015764A (en) * | 1990-06-18 | 1991-05-14 | Ethyl Corporation | Preparation of optically active aliphatic carboxylic acids |
US8178725B2 (en) * | 2005-04-21 | 2012-05-15 | Mitsubishi Gas Chemical Company, Inc. | Method of separating and collecting optically active amino acid amide |
ITMI20060179A1 (it) * | 2006-02-02 | 2007-08-03 | Abiogen Pharma Spa | Procedimento per la risoluzione di miscele racemiche e complesso diastereoisomerico di un agente risolvente e di unantiomero di interesse |
-
2009
- 2009-10-28 CN CN2009801436142A patent/CN102203047B/zh not_active Expired - Fee Related
- 2009-10-28 US US13/126,281 patent/US20110251407A1/en not_active Abandoned
- 2009-10-28 EP EP09823609.4A patent/EP2351729B1/en not_active Not-in-force
- 2009-10-28 WO PCT/JP2009/068484 patent/WO2010050499A1/ja active Application Filing
- 2009-10-28 JP JP2010535812A patent/JP5598330B2/ja not_active Expired - Fee Related
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06507159A (ja) * | 1991-05-13 | 1994-08-11 | ザ ブーツ カンパニー ピーエルシー | 治療薬 |
JPH07149688A (ja) * | 1993-11-26 | 1995-06-13 | Teikoku Chem Ind Corp Ltd | 2−アリールプロピオン酸化合物の光学分割方法 |
WO2002012221A1 (fr) * | 2000-08-03 | 2002-02-14 | Kuraray Co., Ltd. | Procede de resolution optique de l'acide (±)-6-hydroxy-2,5,7,8,-tetramethyle de coumarone-2-carboxylique |
WO2004108944A1 (ja) | 2003-06-04 | 2004-12-16 | Mitsubishi Gas Chemical Company, Inc. | 光学活性クロマンカルボン酸エステルの製造方法 |
JP2005023055A (ja) | 2003-07-04 | 2005-01-27 | Mitsubishi Gas Chem Co Inc | 新規光学活性アミン |
JP2008044856A (ja) * | 2006-08-11 | 2008-02-28 | Mitsubishi Rayon Co Ltd | α−ヒドロキシカルボン酸の製造方法 |
WO2008050829A1 (fr) * | 2006-10-26 | 2008-05-02 | Mitsubishi Gas Chemical Company, Inc. | Procédé de fabrication de l'acide s -(-)-6-hydroxy-2,5,7,8-tétraméthylchromane-2-carboxylique et produit obtenu par le procédé |
Non-Patent Citations (3)
Title |
---|
HIROSHI YAMANAKA, YASUHISA TASHIRO, KIKAN KAGAKU SOSETSU, 1989, pages 4 - 5 |
HIROSHI YAMANAKA: "Kogaku Kasseitai no Preparation", KOGAKU ISEITAI NO BUNRI [KIKAN KAGAKU SOSETSU], vol. 6, 10 June 1999 (1999-06-10), pages 2 - 14, XP008146717 * |
See also references of EP2351729A4 * |
Also Published As
Publication number | Publication date |
---|---|
JP5598330B2 (ja) | 2014-10-01 |
CN102203047B (zh) | 2013-12-11 |
EP2351729B1 (en) | 2014-01-22 |
CN102203047A (zh) | 2011-09-28 |
JPWO2010050499A1 (ja) | 2012-03-29 |
US20110251407A1 (en) | 2011-10-13 |
EP2351729A4 (en) | 2012-08-01 |
EP2351729A1 (en) | 2011-08-03 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP5598330B2 (ja) | 光学活性有機カルボン酸の製造方法 | |
WO2011010579A1 (ja) | 光学活性ニペコタミドの製造方法 | |
JPH06184091A (ja) | 光学活性メチオニンアミドの調製法 | |
EP2168943B1 (en) | Method for producing optically active trans-2-aminocyclohexanol and intermediate of optically active trans-2-aminocyclohexanol | |
US5254756A (en) | Process for the production of (2R,3E)-4-halo-3-buten-2-ols | |
JPH04308550A (ja) | ジオールのアルコールへの立体選択的変換方法 | |
US6028217A (en) | Optically active salts of 2-hydroxymethyl-3-phenylpropionic acid with cis-1-amino-2-indanol, α-methylbenzylamine, or 3-methyl-2-phenyl-1-butylamine | |
US5243070A (en) | Process for resolution of racemates of 2,2-dimethylcyclopropanecarboxylic acid | |
US5126267A (en) | Protected hydroxy method for alcohol-ester separation | |
EP1290209A1 (en) | Method for preparing an r- or s-form of alpha-substituted heterocyclic carboxylic acid and a counter enantiomeric form of alpha-substituted heterocyclic carboxylic acid ester thereto using enzyme | |
WO2001092553A1 (en) | Method for optically resolving a racemic alpha-substituted heterocyclic carboxylic acid using enzyme | |
MX2007011006A (es) | Proceso para preparar acidos e-(2s)-alquil-5-halopent-4-enoicos enantiopuros y esteres. | |
JP4093608B2 (ja) | 光学活性2−フェノキシプロピオン酸の製造方法 | |
JP2505456B2 (ja) | 乳酸の分離方法 | |
JPH0584094A (ja) | 光学活性アルコールの製造法 | |
JPH05500966A (ja) | 再結晶によるアルコール―エステル分離 | |
EP3725766A1 (en) | Method for producing 2-octylglycine ester having optical activity | |
JP5157997B2 (ja) | DL−tert−ロイシンアミドの製造方法 | |
KR101510637B1 (ko) | 신규한 l-클로페라스틴의 중간체 및 그 제조 방법 | |
JP2000136163A (ja) | 2−ヒドロキシ−4−フェニルブタン酸の光学分割方法 | |
EP1484314A1 (en) | Process for production of optically active beta-phenylalanine derivatives | |
JP2003144190A (ja) | 光学活性s−6−ヒドロキシ−2,5,7,8−テトラメチルクロマン−2−カルボン酸の製造方法 | |
JP2004051604A (ja) | 光学活性2−アミノ−2−(2−ナフチル)エタノール類の製造方法およびその中間体 | |
JP2008295302A (ja) | 光学活性エステル誘導体および/または光学活性カルボン酸の製造方法 | |
JP2008273921A (ja) | アルカンジオールの製造方法 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
WWE | Wipo information: entry into national phase |
Ref document number: 200980143614.2 Country of ref document: CN |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 09823609 Country of ref document: EP Kind code of ref document: A1 |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2010535812 Country of ref document: JP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2009823609 Country of ref document: EP |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
WWE | Wipo information: entry into national phase |
Ref document number: 13126281 Country of ref document: US |