MXPA01000917A - Crystal modification of lipoic acid - Google Patents

Crystal modification of lipoic acid

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Publication number
MXPA01000917A
MXPA01000917A MXPA/A/2001/000917A MXPA01000917A MXPA01000917A MX PA01000917 A MXPA01000917 A MX PA01000917A MX PA01000917 A MXPA01000917 A MX PA01000917A MX PA01000917 A MXPA01000917 A MX PA01000917A
Authority
MX
Mexico
Prior art keywords
lipoic acid
mixture
solvent
toluene
solvents
Prior art date
Application number
MXPA/A/2001/000917A
Other languages
Spanish (es)
Inventor
Martin Jochen Klatt
Markus Niebel
Joachim Paust
Jens Rieger
Original Assignee
Basf Aktiengesellschaft*
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Basf Aktiengesellschaft* filed Critical Basf Aktiengesellschaft*
Publication of MXPA01000917A publication Critical patent/MXPA01000917A/en

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Abstract

The invention relates to enantiomer-free crystalline (R) or (S) lipoic acid, where the reflection line at 2&THgr;=23°is the most intensive one in the 13°to 30°range in the 2&THgr;diffractogram.

Description

"MODIFICATION OF THE GLASS OF THE LIPOIC ACID The present invention relates to a process for preparing crystalline α-lipoic acid in high yields, a new modification of the α-lipoic acid crystal and its use. Α-lipoic acid is used in the food industry and in pharmaceutical formulations. When speaking of lipoic acid below, this always refers to the enatiomerically pure (R) - or (S) -lipoic acid) compounds. Processes for preparing enantiomerically pure lipoic acid are described, for example, in Bulman-Page et al., J. Chem. Soc., Chem. Commun. 1986, 1409. In addition, the racemate can be prepared very effectively by the process described in Patent Number EP 0 586 987. Resolution of the enantiomers can be carried out using chiral amines (e.g., Patent Number 0 543 088). The (R) -lipoic acid can also be isolated from natural sources (Reed et al., JACS 1953 Volume 75, 1267). The (R) -lipoic acid can also be prepared in an enantiomerically pure form by the process described in Patent Number EP 487 986. The crude product is subsequently recrystallized from pentane, hexane or cyclohexane.
Alternatively, the crude product can be recrystallized from a 2: 1 mixture of cyclohexane / ethyl acetate (Patent Number EP 0 595 896). When the precise conditions and recrystallization yields are disclosed, a yield of 40 percent, based on the crude product, is obtained from cyclohexane at a temperature of 5 ° C to 10 ° C, and a yield of 31 percent, based on in the crude product, it is obtained at a temperature of about -15 ° C of the cyclohexane / ethyl acetate mixture. The above processes for preparing pure crystalline (R) - or (S) -a-lipoic acid provided yields that are unsatisfactory for the industrial preparation of α-lipoic acid. Increasing the yield by re-using the mother liquor for crystallization is technically complicated and usually leads to an increase in impurities that are highly undesirable in pharmaceutical processing in the food industry. An object of the present invention is to develop a process for preparing lipoic acid of pure pharmaceutical grade, in a favorable form for pharmaceutical processing. The crystalline forms produced up to now have X-ray diffractograms [registered diffractometer patterns of transmission - - using Cu Ka? »(2-theta) radiation] published by Reed and others for the cyclohexane (+) -alpha-lipoic acid and in Patent Number EP 0 593 896 (cyclohexane / ethyl acetate). We have found that this object is achieved by dissolving the α-lipoic acid in an organic solvent having a dielectric constant e of 1.95 to 2.4. The organic solution of a-lipoic acid is then cooled to a temperature of 0 ° C to -20 ° C, providing a crystalline form that is new to enantiomerically pure a-lipoic acid, has a new type of distribution of line intensity in The X-ray diffractogram is suitable for pharmaceutical processing. In addition, the product according to the present invention is obtained in high purity (with <0.1 percent impurities) in yields of 75 percent or more. The invention can be applied both in the pharmaceutical industry and in the food industry where lipoic acid is used as a food additive and also in dietary supplements. The most intense line within the range of 15 ° to 30 ° in the 2 T diffractogram of the crystalline product, according to the present invention, is a line of 23 °. The crystalline products according to the present - - invention have an intensity ratio of 2 T = 23 ° to 2 T = 18.2 ° of at least 1. In addition, the use of -Xo solvents according to the present invention having a dielectric constant of 1.95 to 2.4, has the additional advantage in relation to those described in the literature that, in crystallization, they provide a very pure crystalline product in high yields. As solvents or components of the solvent mixtures, it is possible to use, for example: straight or branched chain, saturated or monounsaturated or polyunsaturated hydrocarbons having a chain length of C5 to Cß, cycloaliphatic hydrocarbons such as cyclopentane, cyclohexane or methylcyclohexane or monohalogenated or polyhalogenated hydrocarbons, preferably chlorinated, having a chain length of 1 to 4 carbon atoms. It is possible to use either solvent mixtures such as hexane or heptane of technical grade, wherein the hexane or heptane is the main component or also the pure solvents. Preference is given to solvent mixtures of aliphatic and aromatic hydrocarbons. In addition, substituted or unsubstituted monocyclic and polycyclic aromatic products are also possible as solvents or solvent components. Examples that can be mentioned are toluene, o-, - m- and p-xylene, ethylbenzene, propylbenzene and isopropylbenzene and mesitylene. In addition, the solvents or solvent mixtures used in accordance with the present invention have to have a melting temperature of less than 0 ° C, preferably of less than -20 ° C, particularly preferably of less than -40 ° C. Preference is also given to solvents that have a low toxicity, since the resulting lipoic acid should be used as a drug or food additive. The preferred upper limit for the dielectric constant is 2.2; specific preference is given on a scale of 2.0 to 2.1. The preferred upper limit for the temperature scale of the crystallization is -5 ° C, particularly preferably -10 ° C. The process can also be carried out at lower temperatures, provided that the solvent or mixture of solvents does not become solid. A preferred lower temperature limit is -20 ° C. Preferred solvent mixtures are those of toluene or xylene with C5-C7 aliphatics in a volume ratio of 1: 1 to 1: 4; specific preference is given to a technical-grade mixture of toluene and hexane or toluene of technical quality and heptane.
- The lipoic acid is recrystallized from a solvent or solvent mixture using a weight ratio of lipoic acid to solvent preferably from 1: 5 to 1:15, particularly preferably from 1: 8 to 1:12. In the case of a mixture of solvents, the lipoic acid is preferably first dissolved in a polar mixture or in the polar solvent component and the remaining non-polar solvent component for recrystallization is then added before cooling to a temperature of 0 ° C. -20 ° C. In aqueous solution (1 gram of lipoic acid in 20 milliliters of 1N NaOH), the product obtained according to the present invention has an absorbency of < 0.300 (430 nm, path length = 1 centimeter).
Example 1 grams of the (R) -a-lipoic acid was introduced in 67 milliliters of a 1: 1 solvent mixture of technical grade toluene / hexane and at 50 ° C. This provided a solution that was filtered. The filtered material [sic] was washed with 33 milliliters of hexane (technical grade). The combined solutions were maintained at a temperature of 0 ° C to 5 ° C for 1 hour in ice water and subsequently stirred for another hour at about -15 ° C while being cooled with a mixture of ice / sodium chloride. The crystals were subsequently filtered off with suction and dried at room temperature under reduced pressure: 8.1 grams of the (R) - (+) -a-lipoic acid.
Example 2 grams of the crude (R) -a-lipoic acid was dissolved in 35 milliliters of toluene at 50 ° C. 35 milliliters of technical grade heptane was added, the solution was filtered at 50 ° C through 4 grams of silica gel F 60 and an additional 35 milliliters of technical grade heptane were added to the filtrate. The solution was cooled to 0 ° C to 5 ° C, stripped and, after 1 hour, cooled to -15 ° C at a cooling rate of 5 ° C per hour. The desired product was isolated by filtration by suction in a frit, the crystalline product was washed twice with 15 milliliters of technical grade heptane and dried in a stream of nitrogen: 8.0 grams of the (R) -a-lipoic acid, temperature of fusion of 47.9 ° -48.9 ° C; [a] 24β = 113.7 ° C, c = 1 in benzene, purity in accordance with GC = 99.95 percent analysis; all trace components < 0.05 percent per area.
The lipoic acids prepared according to the present invention were subjected to X-ray diffraction analysis using Cu-K-alpha radiation. Figure 1 shows a pulvi-diffractogram of a prior art (R) -lipoic acid of cyclohexane. Figure 2 shows a pulvidifractogram of a prior art (R) -lipoic acid of cyclohexane / ethyl acetate. Figure 3 shows a pulvidifractogram of a (R) -lipoic acid of the present invention.

Claims (8)

- CLAIMS:
1. The enantiomerically pure R- or S-lipoic acid for which the line of reflection at 2 T = 23 ° C is the most intense within the range of 15 ° to 30 ° in the diffractogram 2 T.
2. A process for preparing crystalline lipoic acid, which comprises crystallizing the lipoic acid at a temperature of 0 ° C to -20 ° C from a solvent or mixture of solvents having a dielectric constant e of 1.95 to 2.4.
3. A process according to claim 2, wherein a solvent mixture of the aliphatic and aromatic hydrocarbons is used.
4. A process according to claim 3, wherein the solvent mixture used is a mixture of toluene and hexane or a mixture of toluene and heptane.
5. The R-lipoic acid obtainable according to claim 3 or 4.
The lipoic acid obtainable according to any of claims 2 to 4.
7. The use of lipoic acid according to claim 1, 5 or 6 to prepare drugs.
8. The use of lipoic acid according to claim 1, 5 or 6 as a food additive or as a component of dietary supplements.
MXPA/A/2001/000917A 1998-07-31 2001-01-25 Crystal modification of lipoic acid MXPA01000917A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19834608.5 1998-07-31

Publications (1)

Publication Number Publication Date
MXPA01000917A true MXPA01000917A (en) 2001-11-21

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