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Toner for developing electrostatic image |
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Method of concentrating grape juice |
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Production of frozen surimi |
| OF THE INVENTION The present invention relates to a method of production of frozen surimi which ... |
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Drinking doll having wetting and non-wetting modes |
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Diagnosing cancer by observing marker glycosaminoglycans extracted from patient |
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Hollow filament product |
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Process for the bioconversion of fumarate to L-malate
| Details |
Inventors: Schindler, Fritz;
Assignee: Huels Aktiengesellschaft (Marl, DE)
Primary Examiner: Weimar; Elizabeth
Assistant Examiner:
Attorney, Agent or Firm: Millen & White
L-malic acid is produced in a concentration of 170 to 400 g per liter and high yield by biotechnical conversion of fumaric acid neutralized with ammonium hydroxide in nutrient-free solution or suspension. Pure L-malic acid can be obtained economically therefrom with high efficiency in a quality suitable for food and pharmaceutical use. The fermentation can be carried out in simple vessels under non-sterile conditions. The conversion rate of the fumarate and the attainable concentration of L-malate are promoted by the ammonium ions. |
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DETAILED DESCRIPTION What is claimed is: 1. A process for preparing L-malate from fumarate comprising incubating under bioconversion conditions a proliferated cell mass derived from a microorganism containing fumarase effective to convert exogenous fumarate to L-malate in an aqueous solution of fumarate, said solution containing the cell mass in a concentration of from about 0. 5 to 50 g/l (calculated as dry mass) and an initial fumarate concentration of about 170-400 g per liter of liquid, calculated as fumaric acid and relative to the total volume of the solution, at least half of the fumarate being in the form of ammonium-fumarate, said incubation being maintained until the yield of L-malate, calculated as L-malic acid, reaches at least 0. 9 g per gram of initial fumarate, calculated as fumaric acid. 2. A process of claim 1, further comprising, prior to said incubating step, proliferating a microbial cell mass, derived from a microorganism containing fumarase effective to convert exogenous fumarate to L-malate, in an aqueous solution containing a source of assimilable carbon and nutrients for said microorganism, and separating the proliferated cell mass from the culture liquid. 3. A process of claim 2, wherein said nutrient solution contains 1-30 g/l of fumarate; whereby said microorganism is adapted to effect bioconversion of fumarate. 4. A process of claim 2, wherein said assimilable carbon source is corn meal, glucose, sucrose, glycerol or ethanol. 5. A process of claim 1, wherein said incubation is maintained for 0. 5-2 days, at 20. degree. -50. degree. C. and pH 3-9. 6. A process of claim 1, which further comprises recovering the freely moving cell mass produced during said bioconversion of fumarate to L-malate and using at least a portion thereof as the inoculum in at least one subsequent incubation for bioconversion of fumarate to L-malate, the initial concentration of fumarate, calculated as fumaric acid, being 170-400 g per liter of the cell-free solution, said subsequent incubation being maintained until the yield of L-malate, calculated as L-malic acid, reaches at least 0
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