Spray-Drying process for producing a dry caritine powder or granulate
US-9084431-B2 · Jul 21, 2015 · US
US9523106B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9523106-B2 |
| Application number | US-201213557922-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 25, 2012 |
| Priority date | Jul 27, 2011 |
| Publication date | Dec 20, 2016 |
| Grant date | Dec 20, 2016 |
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Subject of the invention is a process for the production of L-carnitine, wherein a β-lactone, which is a 4-(halomethyl)oxetane-2-one, is converted into L-carnitine, wherein the process comprises an enzymatic conversion of the β-lactone into (R)-4-halo-3-hydroxybutyric acid or (R)-4-halo-3-hydroxybutyric acid ester.
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The invention claimed is: 1. A process for the production of L-carnitine, wherein a β-lactone, which is a 4-(halomethyl)oxetane-2-one, is converted into L-carnitine, wherein the process comprises enzymatic conversion of the β-lactone into (R)-4-halo-3-hydroxybutyric acid, wherein the enzymatic conversion is carried out with a lipase in an aqueous medium, the lipase having the amino acid sequence of SEQ ID NO: 1 or SEQ ID NO: 2, wherein the enantiomeric purity of the (R)-4-halo-3-hydroxybutyric acid is at least 95% e.e., and conversion of (R)-4-halo-3-hydroxybutyric acid into L-carnitine with trimetylamine. 2. The process of claim 1 , wherein the β-lactone is a racemate. 3. The process of claim 2 , wherein an enantiomeric excess of the (R)-4-halo-3-hydroxybutyric acid is obtained. 4. The process of claim 1 , 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. 5. The process of claim 1 , wherein after enzymatic conversion, residual β-lactone is removed from the solution. 6. The process of claim 5 , wherein the residual β-lactone is removed by extraction with a solvent. 7. The process of claim 1 , wherein the lipase is from Candida, Pseudomonas, Aspergillus, Bacillus or Thermomyces. 8. The process of claim 1 , wherein the lipase is from Pseudomonas cepacia, Pseudomonas fluorescens , or Candida antarctica. 9. The process of claim 1 , wherein the enzymatic conversion is carried out at a temperature between 0° C. and 50° C., and/or wherein the enzymatic conversion is carried out in an aqueous solution comprising 0.1 to 10 weight % β-lactone. 10. The process of claim 9 , wherein the enzymatic conversion is carried out at a temperature between 20° C. and 40° C., and/or wherein the enzymatic conversion is carried out in aqueous solution comprising 0.1 to 10 weight % β-lactone. 11. The process of claim 1 , in which the β-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 Cl, Br and I. 12. The process of claim 1 , wherein the total yield of (R)-4-halo-3-hydroxybutyric acid in the enzymatic conversion is between 40% and 50%, based on the total initial amount of β-lactone. 13. The process of claim 1 , wherein the reaction time of the enzymatic conversion of the β-lactone into (R)-4-halo-3-hydroxybutyric acid is less than 10 hours.
Hydroxy-carboxylic acids · CPC title
by esterification of carboxylic acid groups in the enantiomers or the inverse reaction · CPC title
Carnitine; Butyrobetaine; Crotonobetaine · CPC title
Carboxylic acid esters · CPC title
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