PROCESS FOR PRODUCING L - CARNITINE FROM BETA - LACTONES
EMPLOYING LIPASES
The invention relates to methods for the production of L-carnitine.
Background of the invention
Carnitine (vitamin Bt; 3-hydroxy-4-trimethylammonio-butanoate) is a quaternary
ammonium compound biosynthesized from the amino acids lysine and methionine. In
living cells, it is required for the transport of fatty acids from the cytosol into the
mitochondria during the breakdown of lipids for the generation of metabolic energy. It
is used as a nutritional supplement. Carnitine exists in two stereoisomers. The
biologically active form is L-carnitine, whilst its enantiomer, D-carnitine, is biologically
inactive. When producing L-carnitine in an industrial process, it is desirable to
produce the biologically active L-form in high purity.
Various methods were described for the industrial production of L-carnitine.
Microbiological processes are known, in which L-carnitine is produced directly by
bacteria. In other processes, a racemate is produced by organic synthesis and
separated subsequently into enantiomers.
Further, attempts have been made to synthesize L-carnitine directly from chiral
precursors. A group of potential precursors are chiral cyclic lactones. Since methods
for obtaining chiral lactones are known in principle, L-carnitine is available upon
hydrolysis of the lactone ring.
US 5,473,1 04 discloses a process for the preparation of L-carnitine from (S)-3-
hydroxybutyrolactone. The process is a two-step process, wherein in a first step (S)-
3-hydroxybutyrolactone is converted into the corresponding hydroxy-activated
lactone, whilst maintaining the ring structure. In a second step, the ring of the
activated lactone is opened and the trimethylammoniunn group is introduced with
trimethylamine. Altogether, the reaction is relatively complicated because it requires
the activation of an intermediate with harsh chemicals.
CH 680 588 A5 discloses a process for producing L-carnitine from a -lactone
precursor, wherein a chiral 2-oxetanone is converted into L-carnitine in a two-step
process. In a first step, 4-(chloromethyl)-2-oxetanone is subjected to a hydrolysis
step, in which the ring is opened and 4-chloro-3-hydroxybutyric acid is obtained. In a
subsequent step, the acid is converted into L-carnitine with trimethylamine. However,
the production of chiral -lactones requires relatively complicated heavy metal
catalysts and the yields are often not sufficient.
Nelson & Spencer (J. Org. Chem. 2000, 65, 1227-1 230) disclose a process for
obtaining enantiomerically enriched -lactones from -lactone racemates by
enzymatic resolution with lipases. The substrates used are various alkyl- and aryl- -
lactone racemates. As summarized in Table 1, the yields are only sufficient for a
limited number of reactions. The enantioselectivity depends strongly on the
substituents of the -lactone and the enantiomeric yield for the small substituent
methyl is very low (table 1) . The reactions require organic solvents, such as benzyl
alcohol, which is not desirable for industrial applications for environmental reasons.
The reaction times are relatively long (mostly 72 hours).
US 2006/0046286 discloses methods for obtaining chiral -butyrolactones and 3-
hydroxycarboxylic acid esters by enzymatic esterification from -lactones. As for
Nelson & Spencer, the use of lipases is suggested. The reactions require organic
solvents, such as toluene, and relatively long reaction times for about 16 hours. The
substrate is -butyrolactone. In most experiments, the substrate is not a racemate,
but optically active (R)^-butyrolactone. The specific reactions mostly yield { )- -
butyrolactone at enhanced enantiomeric purity, whereas (S)-3-hydroxybutyric acid
esters, if at all, are obtained only in relatively low amounts (examples 1, 6, 7).
Since enantiomerically pure L-carnitine is an important industrial product, it would be
desirable to provide further efficient processes for its production. Specifically, it would
be desirable to provide processes for the production of L-carnitine in a relatively
simple manner at a high total yield and enantiomeric yield.
Problem underlying the invention
The problem underlying the invention is to provide a method for producing Lcarnitine,
which overcomes the above-mentioned drawbacks. Specifically, the
problem is to provide an efficient and simple process for the production of L-carnitine.
The total yield as well as the chiral yield shall be high. The number of process steps
shall be relatively low and the process shall not require complicated apparatuses.
Overall, the process shall have a high be atom economy and shall be cost and labour
efficient. The chemicals used shall be readily available and should not be too
expensive.
It is a further problem underlying the invention to provide a mild process, which
avoids harsh conditions and harsh chemicals. Chemicals, which affect the
environment, such as organic solvents or heavy metals, or those which could affect
the health of the workers, such as aromatic solvents, should be avoided. Heavy
metal catalysts, which have to be removed, but nonetheless may remain as trace
impurities in the product, shall be avoided. Specifically, no expensive catalysts
comprising precious metals, such as platinum, should be used. The overall energy
input shall be low. Specifically, the reaction should be carried out at relatively low
temperatures and for relatively low reaction times.
Disclosure of the invention
Surprisingly, the problem underlying the invention is solved by the process according
to the claims. Further inventive embodiments are disclosed throughout the
description.
Subject of the invention is a process for the production of L-carnitine, wherein a -
lactone, which is a 4-(halomethyl)oxetane-2-one, is converted into L-carnitine,
wherein the process comprises an enzymatic conversion of the -lactone into (R)-4-
halo-3-hydroxybutyric acid or (R)-4-halo-3-hydroxybutyric acid ester.
The carnitine is L-carnitine ((R)-carnitine, levocarnitine). L-carnitine is the
physiologically active stereoisomer of carnitine. The reaction product of the
enzymatic conversion is an (R)-4-halo-3-hydroxybutyric acid or an ester thereof,
depending on whether the enzymatic conversion is carried out in aqueous medium or
in alcohol. This intermediate product can be converted into L-carnitine in a
subsequent reaction step. The configuration of the chiral carbon of the acid or ester
is (R), as for the corresponding L-carnitine. Thus, the subsequent conversion into Lcarnitine
can be carried out simply by replacing the halogen atom of the intermediate
by a trimethylammonium group by means of a nucleophilic substitution, whilst the
chirality remains unaffected.
In specific embodiments of the invention, the -lactone is 4-(chloromethyl)oxetane-2-
one, 4-(bromomethyl)oxetane-2-one or 4-(iodomethyl)oxetane-2-one. The use of 4-
(chloromethyl)oxetane-2-one is preferred.
Preferably, the enzyme is stereoselective for the (R)-isomer of the -lactone. In other
words, preferably the enzyme converts exclusively, or at least predominantly, the (R)-
lactone into the corresponding (R)-acid or acid ester. Thus, when the substrate is a
-lactone racemate, or at least comprises (S)-p-lactone and (R)-lactone, the enzyme
selectively converts the (R)-p-lactone into the corresponding (R)-acid or acid ester,
whereas the (S)-p-lactone remains unaffected or essentially unaffected. Thus the
corresponding (S)^-lactone remains and accumulates in the reaction mixture. Thus,
the (R)-acid or acid ester is enriched in the product. Further, the (S)-p-lactone will be
enriched in the product. Both compounds can be separated from each other due to
their different solubilities in water and organic solvent. When starting from a -lactone
racemate, an ideal enzymatic reaction would yield a mixture of 50% Mol-% (R)-acid
or acid ester (with an optical purity of 100% ee) and 50 Mol-% of residual (S)- -
lactone, which subsequently would be removed from the mixture.
In a preferred embodiment of the invention, the -lactone is a racemate. Preferably,
an enantiomeric excess of the (R)-4-halo-3-hydroxybutyric acid or (R)-4-halo-3-
hydroxybutyric acid ester is obtained. The enantiomeric excess (in relation to (S)-4-
halo-3-hydroxybutyric acid or ester) is preferably higher than 80%, more preferably
higher than 90%, 95% or 99% ee.
The enzymatic conversion is carried out in the presence of a solvent. Preferably, the
solvent comprises water. Water may be present in a one-phase system or a twophase
system. In the presence of water, a (R)-4-halo-3-hydroxybutyric acid is
obtained. The enzymatic conversion is then an enzymatic hydrolysis. As a result of
the enzymatic hydrolysis, (R)-4-chloro-3-hydroxybutyric acid, (R)-4-bromo-3-
hydroxybutyric acid or (R)-4-iodo-3-hydroxybutyric acid is obtained.
Preferably, the solvent is exclusively water. When using water as a solvent, the initial
reaction mixture is a solution or suspension. In this embodiment, the reaction mixture
is preferably a one-phase system, in which a clear phase separation between an
aqueous phase and a liquid organic phase is not observed.
In another preferred embodiment of the invention, the enzymatic conversion is
carried out in a two phase system, wherein (R)-4-halo-3-hydroxybutyric acid is
enriched in the aqueous phase. In a two-phase system, the relatively non-polar -
lactone substrate is enriched in the organic phase, whereas the ionic acid product is
enriched in the aqueous phase. Thus after finishing the reaction, the phases can be
separated and the aqueous phase already comprises a relatively pure product. The
organic phase may comprise any solvent, in which the -lactone is highly soluble and
the acid is poorly soluble. In comparison, the one-phase system in aqueous medium
requires less organic solvent overall and is thus advantageous for economic and
environmental reasons.
Examples of the solvent include hydrocarbons, such as aliphatic hydrocarbons such
as pentane, hexane, heptane, octane, decane and cyclohexcane, aromatic
hydrocarbons such as toluene and xylene; halogenated hydrocarbons such as
dichloromethane, 1,2-dichloroethane, chloroform, carbontetrachloride and odichlorobenzene;
ethers such as diethyl ether, diisoproyl ether, tert-butyl methyl
ether, dimethoxyethane, ethylene glycol diethyl ether, tetrahydrofuran, 1,4-dioxane
and 1,3-dioxolane; amides such as formamide; sulfoxides such as dimethyl sulfoxide.
In another embodiment of the invention, the solvent is an alcohol, preferably an
alcohol comprising 1 to 5 carbon atoms, more preferably methanol, ethanol or
propanol. When carrying out the enzymatic conversion in an alcohol and in the
absence of water, the product is a linear ester. Subsequently, when the ester is
converted into L-carnitine, it is de-esterified.
In a preferred embodiment of the invention, after enzymatic conversion, residual -
lactone is removed from the solution. Preferably, the residual -lactone is removed
by extraction with a solvent. For example, when the solution is carried out in a onephase
system, the residual -lactone may be extracted with an ester, such as
ethylacetate, or with hexane. Preferably, multiple extractions with relatively low
amounts of solvent are carried out.
In a preferred embodiment, the enzyme is a hydrolase (Enzyme Commission number
EC 3). Hydrolases yields two products from a substrate by hydrolysis. Preferably, the
hydrolase is an esterase (EC 3.1 ) or a peptidase (EC 3.4). An esterase is a
hydrolase enzyme, such as a lipase, that hydrolyses esters into an acid and an
alcohol. A peptidase (protease) is an enzyme that conducts proteolysis, that is,
hydrolysis of a peptide bond.
In a preferred embodiment of the invention, the enzyme is a lipase. The lipase is
selective for the (R)^-lactone. Preferably, the lipase is from fungi, yeasts or bacteria.
This means that the organism was the origin of the lipase. However, the lipase may
be an artificial, especially a recombinant, lipase. Such lipases are commercially
available, for example from the companies Novozymes, Amano Enzyme or Nagase.
Preferably, the enzyme is a triacylglycerol lipase. Such lipases of enzyme class
3.1 .1 .3 catalyze hydrolysis of triglycerides into fatty acids and glycerols.
Lipases from fungi, yeasts or bacteria are often synthesized in vivo as inactive
precursors. These precursors are processed and secreted. Such lipases are typically
extracellular lipases. Mature proteins are generated by cleaving off N-terminal
peptides, such as signal peptides or propeptides. According to the invention, the
lipase is preferably a mature lipase. In other words, it is preferably in the active form.
The inventive process is preferably an in vitro process.
The lipase may comprise a catalytic triad of amino acids Ser-His-Asp. For example,
such lipases are found in yeast, such as Candida.
In preferred embodiments of the invention, the lipase is from Candida,
Pseudomonas, Aspergillus, Bacillus or Thermomyces. The lipase may be a derivative
of such a lipase, preferably one having at least 75%, preferably at least 90%,
sequence identity.
Preferably, the lipase is from Candida, Pseudomonas or Aspergillus. More
preferably, the lipase is from Pseudomonas cepacia (Burkholderia cepacia),
Pseudomonas fluorescens or Candida antarctica. The lipase may be a derivative of
such a lipase, preferably one having at least 75%, preferably at least 90%, sequence
identity.
Derivatives are obtainable by amino acid substitution, deletion, insertion or
modification. Preferably, derivatives are obtained by recombinant DNA modification
methods. Such recombinant lipases may have higher stabilities and efficiencies
compared to their natural precursors.
Especially preferred are lipases from Pseudomonas cepacia and/or lipase B from
Candida antarctica. It was found that these enzymes provide the desired products at
high total and enantiomeric yield.
In a highly preferred embodiment, the enzyme is lipase from Pseudomonas cepacia
of SEQ ID NO:1 (UniProt identifier P22088[45-364]; Joergensen et al., J. Bacteriol.
1991 ; 173, p559-567). The mature protein is a protein having 320 amino acids. It is
derived from a 364 amino acid precursor comprising a signal peptide and a
propeptide.
In another preferred embodiment, the enzyme is lipase from Pseudomonas cepacia
having an amino acid sequence different from SEQ ID NO:1 . P. cepacia comprises
several lipases with amino acid sequences of high homology with SEQ ID NO:1 . For
example, the enzyme may be P. cepacia alkaline lipase (NCBI Acc. No:
ABX71 757.1 ; Dalai et al., J. Biotechnol. Appl. Biochem. 2008; 5 1, p23-31 ) . This
alkaline lipase has about 98% sequence identity with the lipase of SEQ ID NO:1 . The
enzyme may also be P. cepacia lipase (Genbank: ABN09945.1 ; Yang et al.,
J. Mol. Catal., B Enzym. 2007; 45, p91 -96). This lipase has about 92% sequence
identity with lipase of SEQ ID NO:1 .
Lipase B from Candida antarctica of SEQ ID NO:2 (UniProt identifier P41 365[26-
342]) is a protein having 3 17 amino acids. The mature protein is derived from a 342
amino acid precursor comprising a signal peptide and a propeptide.
Preferably, the derivative is a derivative of lipase from Pseudomonas cepacia of
SEQ ID NO:1 and/or from lipase B from Candida antarctica of SEQ ID NO:2,
preferably one having at least 75%, preferably at least 90%, sequence identity
compared to SEQ ID NO:1 and/or SEQ ID NO:2.As used herein, sequence identity is
preferably determined by BLAST according to standard parameters. Derivatives of
such lipases obtainable by amino acid substitution, deletion, insertion or modification,
and methods for obtaining such derivatives, are known in the art. For example,
derivatives of lipase B from Pseudomonas cepacia having increased catalytic activity
and methods for their production are disclosed in Puech-Guenot et al.,
J. Biomol. Screen. 2008; 13(1 ) , p72-79. Derivatives of lipase B from Candida
antarctica having increased catalytic activity and methods for their production are
disclosed in Qian et al., J. Mol. Biol. 2009; 393; p 19 1-201 .
In a preferred embodiment of the invention, the enzymatic conversion is carried out
at a temperature between 0°C and 50°C, preferably between 20°C and 40°C,
specifically about 25 °C or about 30°C. The temperature is adjusted in view of the
specific enzyme used.
In a preferred embodiment of the invention, the enzymatic conversion is carried out in
aqueous solution comprising 0.1 to 50 weight% -lactone, more preferably between
0.1 and 10 weight% or between 0.5 and 3 weight% -lactone.
The reaction is carried out in an appropriate buffer. The buffer is adapted to the
specific enzyme used. Mostly, the pH will be approximately neutral, for example
between 5 and 9, or between 7 and 8 . If necessary, the pH may be adapted during
the reaction to remain stable by the addition of a base or an acid.
In a preferred embodiment, the reaction mixture consists of the buffer, enzyme and
-lactone. Additives might be added, for example those which enhance the stability
or the turnover of the enzyme, such as salts, metal ions or co-factors. Overall, the
reaction requires only a low number of chemicals and can be carried out in a
relatively simple manner at mild temperatures.
When a desired amount of the acid or acid ester is obtained, the reaction is
terminated. The reaction may be terminated by removing the enzyme, for example by
filtration. When using a -lactone racemate as a substrate and a highly selective
enzyme, up to 50% of the -lactone may be converted into the corresponding (R)-
acid or (R)-acid ester. After removal and isolation, residual (S)^-lactone may be
used for other reactions.
The reaction time may be between between 1 to 50 hours, preferably between 2 to
20 hours. It was found that with some enzymes an efficient turnover can be achieved
within 10 hours, specifically within 8 hours.
Mono-halogenated -lactones for carrying out the inventive ring opening reaction are
known in the art. In view of the stereoselectivity of the enzyme, a -lactone racemate
can be used in the inventive process. Mono-halogenated -lactones are obtainable
e.g. by low pressure carbonylation of the corresponding epoxides as disclosed in
US2007/02 13524 A 1 or starting from unsaturated acid using Lewis acid and
hypochlorite as described by Lopez-Lopez, Jose; Tetrahedron Letters 2007, 48(1 0),
1749-1 752.
In a preferred embodiment of the invention, chiral 4-(halomethyl)oxetane-2-ones are
obtained by a [2+2] cycloaddition reaction in the presence of a catalyst. In a specific
embodiment of the invention, a chiral -lactone is used. This may enhance the
enantiomeric yield in the inventive reaction. A chiral -lactone can be obtained by a
[2+2] cycloaddition of ketene with an aldehyde X-CH2-CHO, wherein X is selected
from CI, Br and I, in the presence of a chiral catalyst. Ketene (ethenone, formula
C2H2O) is a colorless gas, which is highly reactive due to two adjacent double bonds
in the molecule.
In a preferred embodiment of the invention, the 4-halo-3-hydroxybutyric acid or (R)-4-
halo-3-hydroxybutyric acid ester obtained in the enzymatic conversion is
subsequently converted into L-carnitine with trimethylamine (TMA). Preferably, the
halogen atom is substituted by a trimethylamine group in a nucleophilic substitution
reaction. The TMA can be brought into contact with the -lactone in the presence of a
base. The base might be added after bringing the -lactone in contact with the TMA.
In a preferred embodiment of the inventive process, the -lactone is converted into Lcarnitine
in a two-step process. In a first step, a 4-(chloromethyl)-2-oxetanone is
subjected to the enzymatic hydrolysis, in which the -lactone ring is opened and 4-
chloro-3-hydroxybutyric acid is obtained. In a subsequent step, the acid, ester is
converted into L-carnitine with trimethylamine.
An exemplified inventive process for the synthesis of L-carnitine is shown in scheme
1 below. The process comprises a [2+2] cycloaddition of ketene and an aldehyde of
the formula CI-CH2-CHO. The resulting -lactone racemate 1 is subjected to the
enzymatic ring cleavage reaction to yield the corresponding (R)-acid 2a (in water as
a solvent) or (R)-ester 2b (in alcohol). The acid 2a or ester 2b is then converted into
L-carnitine with TMA.
Scheme 1: Synthesis of L-carnitine
In a preferred embodiment of the invention, the TMA is recycled during the process.
Since TMA is available in gaseous form, it can be led through the reaction fluid,
collected and recycled. In the reaction medium, dissolved TMA can be separated
from the mixture after reaction is finished (e. g by distillation) and reintroduced in the
process. Preferably, the TMA is reintroduced into the reaction pathway in a cyclic
process. TMA is commercially available in the form of a pure gas (Fluka Chemicals)
or in the form of an aqueous solution of 10 to 40 wt.%. The amount of TMA in the
reaction mixture may be between 1 and 3 equivalents, preferably between 1 and 2.5
equivalents. However, the amount and excess of TMA is less critical than the amount
of metal hydroxide, because it can be recycled during the reaction and reintroduced
into the reaction chamber.
Another subject of the invention is a process for the production of a (R)-4-halo-3-
hydroxybutyric acid or (R)-4-halo-3-hydroxybutyric acid ester, wherein the process
comprises an enzymatic conversion of a -lactone, which is a 4-(halomethyl)oxetane-
2-one, into (R)-4-halo-3-hydroxybutyric acid or (R)-4-halo-3-hydroxybutyric acid ester.
These reaction products are valuable intermediates for the production of L-carnitine.
They may be converted into L-carnitine in a simple nucleophilic substitution, wherein
the chirality remains unaffected. In addition, they might be used for the synthesis of
other organic compounds or derivatives of L-carnitine.
In a preferred embodiment of the invention, in the enzymatic conversion the total
yield of (R)-4-halo-3-hydroxybutyric acid or (R)-4-halo-3-hydroxybutyric acid ester is
between 40% and 50%, based on the total initial amount of -lactone, and/or the
enantiomeric purity of the (R)-4-halo-3-hydroxybutyric acid or (R)-4-halo-3-
hydroxybutyric acid ester is at least 90%, more preferably at least 95%.
The inventive process solves the problems underlying the invention. The process is
relatively simple and economical and requires only a low number of process steps.
Thus side reactions are avoided and the total yield and enantiomeric yield are high.
Since the enzymatic conversion may use enzymatic resolution, it is possible to start
from a -lactone racemate. Thus, it is not necessary to use expensive chiral
reactants.
The reaction conditions are mild, because neither harsh chemicals, such as heavy
metal catalysts, nor high amounts of organic solvents are necessary. The process
requires relatively low amounts of energy for heating. In principle, only enzymes are
necessary as additives, which can be removed easily and are generally nonhazardous.
The intermediate is thus especially applicable for producing the food
additive L-carnitine.
Examples
An enzymatic resolution was carried out in a one-phase aqueous system. The
substrate was a 4-(chloromethyl)oxetane-2-one racemate, which was converted into
a mixture of (R)-4-chloro-3-hydroxybutyric acid and residual (S)-p-lactone as
illustrated by scheme 2 below.
(R)-2 (S)-1
Scheme 2: Enzymatic resolution of a -lactone racemate according to the
examples.
Analytics
The reaction is monitored by gas chromatography (GC) on a Lipodex E column. 4-
(Chloromethyl)-2-oxetanone 1 is analyzed by GC on a Lipodex E column. 4-Chloro-3-
hydroxybutyric acid 2 is derivatized using a chiral, fluorescent reagent. The reaction
mixture is analyzed by HPLC using an ODS-column and flourimetric detection.
Examples 1 to 5
To a solution or suspension of 12.5 mg enzyme in 5.0 mL potassium phosphate
buffer (0.1 M, pH 7.5), 50 mg 4-(chloromethyl)-2-oxetanone 1 is added and the
reaction mixture is stirred at 30°C. The pH is continually adjusted to 7.5 with 0.5 M
KOH. At regular intervals, 200 L samples are taken, extracted with 400 L ethyl
acetate, filtered and analyzed by chiral GC. After complete hydrolysis of the (R)-
enantiomer, the enzyme is centrifuged off and the reaction mixture is extracted twice
with 5.0 mL ethyl acetate. (R)-4-chloro-3-hydroxy butyric acid 2 is obtained as
aqueous solution. Reactions were carried out with different lipases as summarized in
table 1 below. Conversion and enantiomeric purities are shown in table 1. (S)-1 and
(R)-2 are both obtained at high enantiomeric purity. The reaction time at 30°C was
only between 4 to 8 hours.
Table 1: Summary of conditions and results of examples 1 to 5.
CLAIMS
1. A process for the production of L-carnitine, wherein a -lactone, which is a 4-
(halomethyl)oxetane-2-one, is converted into L-carnitine, wherein the process
comprises an enzymatic conversion of the -lactone into (R)-4-halo-3-
hydroxybutyric acid or (R)-4-halo-3-hydroxybutyric acid ester.
2 . The process of at least one of the preceding claims, wherein the -lactone is a
racemate.
3 . The process of claim 2, wherein an enantiomeric excess of the (R)-4-halo-3-
hydroxybutyric acid or (R)-4-halo-3-hydroxybutyric acid ester is obtained.
4 . The process of at least one of the preceding claims, wherein the enzymatic
conversion is carried out in an aqueous medium and (R)-4-halo-3-hydroxybutyric
acid is obtained.
5 . The process of at least one of the preceding claims, wherein the enzymatic
conversion is carried out in a two phase solution, wherein (R)-4-halo-3-
hydroxybutyric acid is enriched in the aqueous phase.
6 . The process of at least one of the preceding claims, wherein, after enzymatic
conversion, residual -lactone is removed from the solution.
7 . The process of claim 6, wherein the residual -lactone is removed by extraction
with a solvent.
8 . The process of at least one of the preceding claims, wherein the enzyme is a
lipase.
9 . The process of at least one of the preceding claims, wherein the lipase is from
Candida, Pseudomonas, Aspergillus, Bacillus or Thermomyces, or a derivative of
such a lipase having at least 75%, preferably at least 90%, sequence identity.
10 .The process of at least one of the preceding claims, wherein the lipase is from
Pseudomonas cepacia, Pseudomonas fluorescens, Candida Antarctica, the
lipase preferably having the amino acid sequence of SEQ ID NO:1 or
SEQ ID NO:2, or a derivative of such a lipase having at least 75%, preferably at
least 90%, sequence identity.
11.The process of at least one of the preceding claims, wherein the enzymatic
conversion is carried out at a temperature between 0°C and 50°C, preferably
between 20°C and 40°C, and/or wherein the enzymatic conversion is carried out
in aqueous solution comprising 0.1 to 10 weight% -lactone.
12 .The process of at least one of the preceding claims, in which the -lactone is
synthesized in a preceding step in a [2+2] cycloaddition of ketene and an
aldehyde of the formula X-CH2-CHO, wherein X is selected from CI, Br and I .
13 .The process of at least one of the preceding claims, wherein the 4-halo-3-
hydroxybutyric acid or (R)-4-halo-3-hydroxybutyric acid ester obtained in the
enzymatic conversion is converted into L-carnitine with trimethylamine.
The process of at least one of the preceding claims, wherein the total yield of (R)-
4-halo-3-hydroxybutyric acid or (R)-4-halo-3-hydroxybutyric acid ester in the
enzymatic conversion is between 40% and 50%, based on the total initial amount
of -lactone, and/or wherein the enantiomeric purity of the (R)-4-halo-3-
hydroxybutyric acid or (R)-4-halo-3-hydroxybutyric acid ester is at least 90%.
15 .A process for the production of a (R)-4-halo-3-hydroxybutyric acid or (R)-4-halo-3-
hydroxybutyric acid ester, wherein the process comprises an enzymatic
conversion of a -lactone, which is a 4-(halomethyl)oxetane-2-one, into (R)-4-
halo-3-hydroxybutyric acid or (R)-4-halo-3-hydroxybutyric acid ester.