HK1005867B - Improved process for manufacturing l-(-)-carnitine from waste products having opposite configuration - Google Patents
Improved process for manufacturing l-(-)-carnitine from waste products having opposite configuration Download PDFInfo
- Publication number
- HK1005867B HK1005867B HK98104946.0A HK98104946A HK1005867B HK 1005867 B HK1005867 B HK 1005867B HK 98104946 A HK98104946 A HK 98104946A HK 1005867 B HK1005867 B HK 1005867B
- Authority
- HK
- Hong Kong
- Prior art keywords
- carnitine
- acyl
- carnitinamide
- carnitinenitrile
- lactone
- Prior art date
Links
Description
The present invention relates to an improved process for manufacturing L-(-)-carnitine from starting compounds containing an asymmetrical carbon atom having a configuration opposite to that of L-(-)-carnitine. The process of the present invention overcomes the drawbacks of conventional processes which first convert a starting compound into an achiral intermediate, generally crotonobetaine or gamma-butyrobetaine, and then convert the achiral intermediate to L-(-)-carnitine. The process of the present invention uses D-(+)-carnitinamide or D-(+)-carnitinenitrile as preferred starting compounds.
Carnitine contains a single center of asymmetry and therefore exists as two enantiomers, designated D-(+)-carnitine and L-(-)-carnitine. Of these, only L-(-)-carnitine is found in living organisms, where it functions as a vehicle for transporting fatty acids across mitochondrial membranes. Whilst L-(-)-carnitine is the physiologically-active enantiomer, racemic D.L-carnitine has conventionally been used as a therapeutic agent. It is now recognized, however, that D-(+)-carnitine is a competitive inhibitor of carnitine acyltransferases, and that it diminishes the level of L-(-)-carnitine in myocardium and skeletal muscle.
It is therefore essential that only L-(-)-carnitine be administered to patients undergoing haemodialysis treatment or treatment for cardiac or lipid metabolism disorders. The same requirement applies to the therapeutic utilization of acyl derivatives of carnitine for treating disorders of the cerebral metabolism, peripheral neuropathies, peripheral vascular diseases and the like. These disorders are typically treated with acetyl L-(-)-carnitine and propionyl L-(-)-carnitine, which are obtained by acylating L-(-)-carnitine.
Various chemical procedures have been proposed for the industrial-scale production of carnitine. Unfortunately, these procedures are not stereospecific and produce racemic mixtures of D-(+)- and L-(-)-isomers. It is thus necessary to apply resolution methods in order to separate the enantiomeric constituents of the racemate.
Typically, the D,L-racemic mixture is reacted with an optically active acid (e.g. D-(-)-tartaric acid, D-(+)-camphorsulfonic acid, (+)-dibenzoyl-D-(-)-tartaric acid, N-acetyl-L-(+)-glutamic acid and D-(+)-camphoric acid) to obtain two diastereoisomers which can be separated from each other. In the classic process disclosed in U.S. Patent 4,254,053, D-(+)-camphoric acid is used as the resolution agent of a racemic mixture of D,L-carnitinamide, obtaining D -(+)-carnitinamide as a by-product, and L -(-)-carnitinamide which, by hydrolysis, gives L-(-)-carnitine.
However, these resolution procedures are complex and costly, and in all cases result in the production of equimolar quantities of L-(-)-carnitine and D-(+)-carnitine or a precursor thereof as by-product, having configuration opposite to that of L-(-)-carnitine. Several microbiological processes have recently been proposed for producing L-(-)-carnitine via stereospecific transformation of achiral derivatives obtained from the huge amounts of D-(+)-carnitine (or of a precursor thereof, such as D-(+)-carnitinamide) which are generated as by-products in the industrial production of L-(-)-carnitine.
These processes are generally predicated upon the sterospecific hydration of crotonobetaine to L-(-)-carnitine, and differ principally by virtue of the particular microorganism employed to accomplish the biotransformation of interest. See, for example, the processes disclosed in: EP 0 121 444 (HAMARI), EP 0 122 794 (AJINOMOTO), EP 0 148 132 (SIGMA-TAU), JP 275689/87 (BIORU), JP 61067494 (SEITETSU), JP 61234794 (SEITETSU), JP 61234788 (SEITETSU), JP 61271996 (SEITETSU), JP 61271995 (SEITETSU), EP 0 410 430 (LONZA), EP 0 195 944 (LONZA), EP 0 158 194 (LONZA), and EP 0 457 735 (SIGMA-TAU).
On the other hand, JP 62044189 (SEITETSU) discloses a process for stereoselectively producing L-(-)-carnitine starting from gamma-butyrobetaine, which is in turn obtained enzymically from crotonobetaine.
All of these processes have several drawbacks. First, D-(+)-carnitine must first be converted to an achiral compound (crotonobetaine, gamma-butyrobetaine) before it can be used as the starting compound in all of the aforesaid microbiological processes.
In addition, the microbiological procedures proposed to date have not proven practicable for manufacturing L-(-)-carnitine on an industrial scale for one or more of the following reasons:
- (i) the yield of L-(-)-carnitine is extremely low;
- (ii) the microorganisms must be cultivated in a costly nutritive medium;
- (iii) the microorganism can only tolerate low concentrations [up to 2-3% (w/v)] of crotonobetaine;
- (iv) side reactions occur, such as the reduction of crotonobetaine to gamma-butyrobetaine or the oxidation of L-(-)-carnitine to 3-dehydrocarnitine. These side reactions reduce the final yield of L-(-)-carnitine.
Finally, further processes for producing L-carnitine are disclosed in EP-A-0 060 595, FR 1.513.328 and BE-664500.
EP-A-0 060 595 discloses a process wherein D-mannitol is first converted to D-mannitol acetonide, whereafter the D-mannitol is split by oxydation to glyceraldehyde acetonide, which is reduced to glycerol acetonide. Then the free hydroxyl group is exchanged with a halogen atom (chlorine) with the formation of chlorodihydroxy propane, the primary alcoholic group of which is functionalized with the acid chloride of a sulfonic acid (tosylchloride). The tosyl derivative is reacted with hydrogen cyanide to give the corresponding nitrile which, when reacted with trimethylamine gives carnitinenitrile. The nitrile group is hydrolized to give L-carnitine chloride which is finally converted to L-carnitine.
FR 1.513.328 disclosed a process for producing L-carnitine chloride starting from complex, optically active salts of N-acyl glutamic acid with carnitinenitrile hydroxide.
BE-664500 discloses a process wherein L-carnitinenitrile chloride is reacted with an alkanol (e.g. methanol) in the presence of hydrogen chloride. After removal of ammonium chloride, the reaction solution of carnitine ester chloride is evaporated under reduced pressure, the residue is taken up with water and the chloride ions removed, thus giving L-carnitine.
In order to overcome all of the aforesaid drawbacks of the known processes, in the Italian patent application RM 94 A 000 915 corresponds to EP-A-0 609 643 filed on December 21, 1992 in the name of the same applicants as the present application, not available to the public inspection at the filing date of this application, a process has been disclosed which allows high yields of L-(-)-carnitine to be obtained starting from a by-product having configuration opposite to that of L-(-)-carnitine (such as D-(+)-carnitinamide) with no need to first convert the starting by-product into an achiral intermediate.
This process which is illustrated in the following reaction scheme 1: comprises hydrolyzing a D-(+)-carnitinamide salt 1 to D-(+)-carnitine 2 and esterifying 2 into ester 3 (via known methods) wherein R1 is preferably arylalkoxy, e.g. benzyloxy.
The ester 3 is then converted to the acyl derivative 4 wherein Y, which can be the same as X, is preferably a counterion, e.g. perchlorate, imparting solubility to 4. R is preferably an alkylsulfonyl group having 1-12 carbon atoms, e.g. mesyl.
The acylation of 3 to 4 is carried out preferably in pyridine by reacting the ester 3 with an acylating agent RY wherein Y is halogen and R is an acyl group as defined above. Preferably RY is the chloride of the selected acyl group.
The ester group -COR1 of 4 (R1=benzyloxy) is hydrogenated to carboxyl group thus giving acyl D-(+)-carnitine 5 which is converted to the lactone 6 of L-(-)-carnitine. The lactonization is suitably carried out in an aqueous basic environment: either with NaHCO3 (ratio 1:1) or with an AMBERLITE IRA-402 basic resin activated in HCO3 form or with an LA2 resin. The lactone is isolated by evaporating the aqueous solution or precipitating it as a salt (for example, as tetraphenylborate or reineckate).
Finally, lactone 6 is suitably converted to L-(-)-carnitine inner salt 7. The lactone is dissolved in water and the resulting solution treated with a base such as NaHCO3 (ratio 1:1), for 8-24 hours.
L-(-)-carnitine can suitably be purified from the salts which are formed from the X- anion, from the excess, if any, of the acyl halogenide, from pyridine, and the like, by chromatographing the aqueous solution on a strongly acidic resin such as IR 120, eluting with water and then with NH4OH, or alternatively eluting first on a strongly basic resin such as AMBERLITE IRA 402 activated in OH form and thereafter on a weakly acid resin such as AMBERLITE IRC-50.
The process of the present invention which is illustrated in the following reaction scheme 2 constitutes a remarkable improvement over the previous process.
With reference to the reaction scheme 2, D-(+)-carnitinenitrile 1 wherein X- is any anion, preferably an anion imparting solubility, such as perchlorate, tetraphenylborate, alkylsulphonate wherein the alkyl group has 1-12 carbon atoms, is converted to acyl derivative 2.
To this end, the acylation of 1 to 2 is carried out by reacting 1 with an acylating agent selected from RY wherein Y is halogen (e.g. chlorine) and the anhydride R2O wherein R is an alkylsulfonyl group having 1-12 carbon atoms, formyl or trifluoroacetyl. Preferably, the alkylsulfonyl group is selected from methanesulfonyl (mesyl), p-toluenesulfonyl (tosyl), p-bromobenzenesulfonyl (brosyl), p-nitrobenzenesulfonyl (nosyl), trifluoromethanesulfonyl (triflyl), nonafluoromethanesulfonyl (nonaflyl) and 2,2,2-trifluoroethanesulfonyl (tresyl). Mesyl is particularly preferred.
When RY is a chloride, the reaction takes place in pyridine or pyridine alkyl derivatives wherein the alkyl group is lower alkyl having 1-4 carbon atoms, or in other basic organic solvents such as triethylamine, or in inert anhydrous organic solvents such as acetonitrile or methylene chloride, in mixture with a base such as pyridine, lutidine, picoline or polyvinylpyridine.
The acylating agent is added at ratios ranging from 1:1 to 1:10, preferably 1:3. The resulting reaction mixture is kept under stirring at 0°C-50°C, for 1-24 hours.
The acyl D-(+)-carnitinenitrile 2 is converted via acid hydrolysis with conventional procedures to acyl D-(+)-carnitinamide 3 which can be directly arrived at by acylating D-(+)-carnitinamide with RY (as shown in the reaction scheme).
Hydrolysis of 2 takes place in an acid aqueous environment, at pH 0-4, at 50°C-80°C, for 10-48 hours, yielding the intermediate acyl D-(+)-carnitinamide 3 which forms acyl D-(+)-carnitine 4.
The acyl D-(+)-carnitinamide 3 is hydrolyzed to acyl D-(+)-carnitine 4 under the same conditions.
Conversion of acyl D-(+)-carnitine 4 to lactone 5 and the conversion of this latter compound to L-(-)-carnitine 6 are carried out as disclosed in the previously cited Italian patent application RM92A000915.
It should be understood that, whereas the process disclosed above has been described, for the sake of clarity, as a sequence of four distinct operating steps, the corresponding industrial process consists of two steps only. When the process of the present invention is carried out as an industrial process, the acyl D-(+)-carnitinenitrile 2 can be directly converted to L-(-)-carnitine inner salt 6 without isolating either the acyl D-(+)-carnitinamide 3 or the acyl D-(+)-carnitine 4 or the lactone 5.
In fact, the ester of acyl D-(+)-carnitinenitrile 2 is hydrolyzed in an acid environment to compound 3 and this latter to compound 4, then the resulting aqueous solution is concentrated and the concentrate is brought to pH 7-9, preferably 8-9 and kept at this pH value for 30-50 hours yielding L-(-)-carnitine. L-(-)-carnitine thus obtained is purified from any salt via treatment with acidic and basic resins.
In the following example which describes one embodiment of the process of the invention, the intermediate compounds 2, 3 and 4 were isolated so as to exhaustively characterize them from a physico-chemical standpoint.
It will be, however, apparent to any expert in organic synthesis that the industrial process comprises the following steps only:
- (a) acylating the hydroxyl group of D-(+)-carnitinenitrile 1 or D-(+)-carnitinamide 1' with an acylating agent RY, wherein R has the previously defined meanings, with the resulting formation of a leaving group OR thus obtaining acyl D-(+)-carnitinenitrile 2 or acyl D-(+)-carnitinamide 3; and
- (b) converting 2, or respectively 3 to L-(-)-carnitine inner salt 6.
Methanesulfonyl chloride (14.2 g; 123 mmoles) was added over a period of 5 minutes to a solution of D-carnitinenitrile perchlorate 1 (10 g; 41 mmoles) in anhydrous pyridine (200 mL).
The solution was kept under stirring for 1 hour, then poured into an Erlenmeyer flask containing Et2O (800 mL) under stirring. The precipitate which formed was crystallized from hot CH3CN/iPrOH (filtering off the insoluble residue in hot CH3CN).The crystalline product thus obtained was triturated with hot iPrOH yielding 9.4 g of compound 2.
Yield = 71%
Differential thermal analysis = the compounds melts at 155°C.
[α] = +43° (C=1% H2O)
| C% | H% | N% | Cl% | |
| Calculated | 29.26 | 5.34 | 8.73 | 11.05 |
| Found | 30.21 | 5.35 | 8.47 | 10.97 |
Methanesulfonyl chloride (9.88 g; 86.31 mmoles) was added over a 5-minute period to a solution of D-carnitinamide perchlorate 1' (15 g; 57.54 mmoles) in anhydrous pyridine (300 mL).
The solution was kept under stirring at room temperature for 1 h and 15 minutes, then poured into an Erlenmeyer flask containing Et2O (2.5 L) under stirring. The precipitate thus obtained was refluxed with iPrOH which was then decanted. The undissolved solid residue was further washed with iPrOH and then dried yielding 10.2 g of compound 3.
Yield= 52%
Differential thermal analysis = the compound melts at 156-158°C
[α] = +21.5° (C=1% H2O)
1HNMR(DMSO)d6): δ 7.60 and 7.20(2s,2H,-CONH2),5.4(m,1H,-CHOMs), 4.0-3.62(4m,2H,-CH2N+Me3),3.35(s,3H,CH3SO3-),3.15(s,9H,N+Me3), 2.8-2.7(m,2H,-CH2CON)
13CNMR(D2O): δ 175.272; 74.831; 70.798; 56.871; 41.521; 41.308 IR (Kbr) = ν (cm-1)1696 (-C= O), 1333 and 1174 (CH3SO3-)
HPLC
Column=Nucleosil 5-SA Diameter 4.0 mm Length= 200 mm
Eluant = CH3CN/KH2PO4 50 mM (65/35) pH=3.5 with H3PO4
Flow rate= 0.75 mL/min
Retention time= 19.83 min.
Detector= RI Waters 410
| C% | H% | N% | Cl% | S% | |
| Calculated | 28.36 | 5.65 | 8.31 | 10.46 | 9.46 |
| Found | 28.74 | 5.60 | 7.89 | 10.2è | 9.25 |
A solution of methanesulfonyl D-carnitinenitrile perchlorate 2 (2 g; 6.23 mmoles) in 12N HCl (40 mL) was heated at 50°C under stirring for 36 hours.
The reaction proceeds via the formation of methanesulfonyl-D-carnitinamide 3 as shown by HPLC analysis after 2 hours from reaction beginning.
At the end of the reaction the solution was brought to dryness under vacuum giving an oily solid which was taken up with CH3CN. The insoluble solid was filtered off and the filtrate poured in Et2O; the precipitate thus obtained was isolated by decantation, washed with Et2O and dried under vacuum yielding 2 g of the raw product 4.
Methanesulfonyl-D-carnitinamide 3.
HPLC
Column=Nucleosil 5-SA Diameter 4.0 mm Length= 200 mm
Eluant = CH3CN/KH2PO4 50 mM(65/35) pH=3.5 with H3PO4
Flow rate= 0.75 mL/min
Retention time= 19.83 min.
Detector= RI Waters 410
Methanesulfonyl-D-carnitine 4.
HPLC
Column=Nucleosil 5-SA Diameter 4.0 mm Length= 200 mm
Eluant = CH3CN/KH2PO4 50 mM (65/35) pH=3.5 with H3PO4
Flow rate= 0.75 mL/min
Retention time= 11.38 min.
Detector= RI Waters 410
1HNMR(D2O): δ 5.70 and 5.6(m,1H,-CHOMs),
4.06-3.75(m,2H,-CH2N+Me3),3.33(s,3H,CH3SO3-),
3.27(s,9H,N+Me3),3.15-3.00(m,2H,-CH2COOH)
The product thus obtained was used as such, without further purification, in the reaction sequence disclosed in the previously cited Italian patent application RM 92 A 000195 to obtain L-carnitine inner salt.
The reaction was carried out as described for the reaction starting from methanesulfonyl D-carnitinenitrile perchlorate 2.
Claims (3)
- A process for producing L-(-)-carnitine from a precursor thereof having opposite configuration selected from D-(+)-carnitinenitrile 1 and D-(+)-carnitinamide 1' having the formula 1 and 1' wherein X- is any counterionn which comprises:(a) converting the precursor 1 or 1' to acyl D-(+)-carnitinenitrile 2 or acyl D-(+)-carnitinamide 3 having the formulas wherein R is selected from alkylsulfonyl having 1-12 carbon atoms, formyl and trifluoroacetyl, by acylating 1, respectively 1', with an acylating agent selected from the anhydride R2O and RY wherein R has the previously defined meaning, Y is halogen, preferably chlorine, in an inert organic solvent selected from pyridine or alkylpyridine wherein the alkyl group is a lower alkyl having 1-4 carbon atoms, triethylamine, acetonitrile or methylene chloride, the acylating agent being added at ratios ranging from 1:1 to 1:10, preferably 1:3 at 0°C-50°C, for 1-24 hours.(b) converting the acyl D-(+)-carnitinenitrile 2 or the acyl D-(+)-carnitinamide 3 via acid hydrolysis at pH 0-4, at 50°C-80°C, for 10-48 hours, to acyl D-(+)-carnitine 4 of the formula(c) reacting said acyl D-(+)-carnitine 4 with a base selected from NaHCO3. AMBERLITE IRA-402 basic resin activated in HCO3 form or LA2 resin thereby preparing lactone 5 of L-(-)-carnitine of the formula:(d) converting said lactone 5 to L-(-)-carnitine by reacting lactone 5 with an aqueous basic solution, preferably NaHCO3, ratio 1:1, for 8-24 hours and isolating L-(-)-carnitine inner salt by contacting the L-(-)-carnitine containing solution with an ion exchange resin.
- The process of claim 1, wherein said steps (b), (c) and (d) are carried out as a single step, without isolating said intermediate compounds 2, 3, 4 and 5.
- The process of claims 1 or 2 wherein:X- is halogenide, preferably chloride, sulphate, phosphate, perchlorate, metaperiodate, tetraphenylborate, or alkylsulfonate having 1-12 carbon atoms; andR is methanesulfonyl (mesyl), p-toluenesulfonyl (tosyl), p-bromobenzenesulfonyl (brosyl), p-nitrobenzenesulfonyl (nosyl), trifluoromethanesulfonyl (triflyl), nonfluoromethanesulfonyl (nonaflyl) and 2,2,2-trifluoroethanesulfonyl (tresyl), preferably mesyl.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| ITRM930226 | 1993-04-08 | ||
| ITRM930226A IT1261230B (en) | 1993-04-08 | 1993-04-08 | IMPROVED PROCEDURE FOR THE PREPARATION OF L - (-) - CARNITINA STARTING FROM ITS PRECURSORS WITH OPPOSED CONFIGURATION. |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| HK1005867A1 HK1005867A1 (en) | 1999-01-29 |
| HK1005867B true HK1005867B (en) | 1999-01-29 |
Family
ID=
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5599978A (en) | Process for manufacturing L-(-)-carnitine from a waste product having opposite configuration | |
| HK1005861B (en) | Process for manufacturing l-(-)-carnitine from a waste product having opposite configuration | |
| EP0623588B1 (en) | Improved process for manufacturing L-(-)-carnitine from waste products having opposite configuration | |
| EP0624568B1 (en) | Improved process for manufacturing L-(-)-carnitine from a waste product having opposite configuration | |
| US5532409A (en) | Process for producing R-aminocarnitine and S-aminocarnitine | |
| DE69920007T2 (en) | CHEMICAL PROCESS FOR THE STEREOSELECTIVE SYNTHESIS OF R - (-) - CARNITINE | |
| HK1005723B (en) | Improved process for manufacturing l-(-)-carnitine from a waste product having opposite configuration | |
| EP1224161B1 (en) | Nitroxy derivatives of (r) and (s)-carnitine | |
| KR100614545B1 (en) | Method for producing R-(-)-carnitine | |
| HK1005867B (en) | Improved process for manufacturing l-(-)-carnitine from waste products having opposite configuration | |
| US5714619A (en) | Process for the preparation of (S)-β-hydroxy-γ-butyrolactone | |
| EP0287523A2 (en) | Process for producing (-) N-acetylaminocarnitine and (+) N-acetylaminocarnitine |