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US4304858A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the continuous enzymatic change of water soluble α-ketocarboxylic acids into the corresponding amino acids

Assignee: Helmholtz Centre for Infection Research
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Filing: 1980-07-25
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Granted: 1981-12-08
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Expires: 2000-07-25
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Abstract

Abstract Water soluble α-ketocarboxylic acids are continuously converted in a membrane reactor into the corresponding aminoacids. The conversion takes place in the presence of a substrate specific dehydrogenase, of ammonium ions and of a nicotinamide-adenine-dinucleotide (NAD + /NADH) enlarged in molecular weight through linkage to a water soluble polymer as coenzyme. Simultaneously NADH is regenerated continuously from NAD + in presence of a formate dehydrogenase and from formate ion. The membrane must have a mean pore diameter of 1 to 3 nm. As coenzyme there is employed 0.1 to 10 mmol/l of NAD + /NADH present bound to a polyoxyethylene having an average molecular weight between 500 and 50,000. There is continuously supplied to the reactor a substrate stream which contains 50 to 100% of the maximum amount soluble, but not over 2,000 mmol/l, of the reacting α-ketocarboxylic acid in the form of a water soluble salt, an ammonium ion in an amount about equimolar to the amount of substrate and 100 to 6,000 mmol/l of a formate. There is maintained over the membrane a differential pressure of 0.1 to 15 bar. There is continuously drawn off behind the membrane a filtrate stream containing the aminoacid formed.

Inventors

  • 👤 Christian Wandrey
  • 👤 Rolf Wichmann
  • 👤 Wolfgang Leuchtenberger
  • 👤 Maria-Regina Kula
  • 👤 Andreas Buckmann

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 22:16
CPC Classifications
C; C12; C12P; C12P13/00; C12P13/04; C12P13/06; C12P1/00; C12P19/00; C12P19/26; C12P19/28; C12P19/30; C12P19/36; Y; Y10; Y10S; Y10S435/00; Y10S435/813

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 200 words
A process for continuously enzymatically converting water soluble α-ketocarboxylic acids in a membrane reactor equipped with an ultrafiltration membrane into the corresponding aminoacids comprising carrying out the conversion in the presence of a substrate specific dehydrogenase, of ammonium ions and of a nicotinamide-adenine-dinucleotide (NAD + /NADH) of increased moecular weight through linkage to a water soluble polymer as coenzyme while simultaneously regenerating NADH from NAD + in presence of a formate dehydrogenase by means of formate ion, said membrane having a mean pore diameter of 1 to 3 nm, there being employed as coenzyme 0.1 to 10 mmol/l of NAD + /NADH bound to a polyoxyethylene having an average molecular weight between 500 and 50,000, continuously supplying to the reactor a substrate stream which contains 50 to 100% of the maximum amount soluble, but not over 2,000 mmol/l, of the reacting α-ketocarboxylic acid in the form of a water soluble salt as substrate, an ammonium ion in an amount about equimolar to the amount of substrate and 100 to 6,000 mmol/l of a formate, maintaining over the membrane a differential pressure of 0.1 to 15 bar and continuously drawing off behind the membrane a filtrate stream containing the aminoacid formed.
Claim 2
Dependent Claim 200 words
A process for continuously enzymatically converting water soluble α-ketocarboxylic acids in a membrane reactor equipped with an ultrafiltration membrane into the corresponding aminoacids comprising carrying out the conversion in the presence of a substrate specific dehydrogenase, of ammonium ions and of a nicotinamide-adenine-dinucleotide (NAD + /NADH) of increased moecular weight through linkage to a water soluble polymer as coenzyme while simultaneously regenerating NADH from NAD + in presence of a formate dehydrogenase by means of formate ion, said membrane having a mean pore diameter of 1 to 3 nm, there being employed as coenzyme 0.1 to 10 mmol/l of NAD + /NADH bound to a polyoxyethylene having an average molecular weight between 500 and 50,000, continuously supplying to the reactor a substrate stream which contains 50 to 100% of the maximum amount soluble, but not over 2,000 mmol/l, of the reacting α-ketocarboxylic acid in the form of a water soluble salt as substrate, an ammonium ion in an amount about equimolar to the amount of substrate and 100 to 6,000 mmol/l of a formate, maintaining over the membrane a differential pressure of 0.1 to 15 bar and continuously drawing off behind the membrane a filtrate stream containing the aminoacid formed.
Claim 3
Dependent Claim 32 words
A process according to claim 1 wherein the formate dehydrogenase and the substrate specific dehydrogenase are added in an amount such that the ratio of their activities is between 1:1 and 1:5.
Claim 4
Dependent Claim 22 words
A process according to claim 2 wherein the substrate solution which supplied the ammonium ions and the formate ions as ammonium formate.
Claim 5
Dependent Claim 19 words
A process according to claim 1 wherein the substrate the ammonium ions and the formate ions as ammonium formate.
Claim 6
Dependent Claim 18 words
A process according to claim 1 wherein the substrate stream contains not over 1,000 mmol/l of the ketocarboxlic.
Claim 7
Dependent Claim 19 words
A process according to claim 5 wherein the formula is present in an amount of 300 to 2,000 mmol/l.
Claim 8
Dependent Claim 14 words
A process according to claim 6 wherein the pressure is 0.2 to 3 bar.
Claim 9
Dependent Claim 26 words
A process according to claim 7 wherein the ketocarboxylic acid salt is a salt of pyruvic acid, 2-oxo-4-methylvaleric acid, 2-oxo-3-methylvaleric acid, 2-oxo-3-methylbutyric acid or 2-oxovaleric acid.
Claim 10
Dependent Claim 26 words
A process according to claim 1 wherein the ketocarboxylic acid salt is a salt of pyruvic acid, 2-oxo-4-methylvaleric acid, 2-oxo-3-methylvaleric acid, 2-oxo-3-methylbutyric acid or 2-oxovaleric acid.
Claim 11
Dependent Claim 13 words
A process according to claim 8 wherein the ketocarboxylic acid is pyruvic acid.
Claim 12
Dependent Claim 14 words
A process according to claim 10 wherein the substrate specific dehydrogenase is L-alanine dehydrogenase.
Claim 13
Dependent Claim 15 words
A process according to claim 11 wherein the salt is a sodium or potassium salt.

References Cited (Backward Citations)

US3183170A Cited
US4251631A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-12-07 1985-06-08 1985-12-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-12-07 1989-06-08 1989-12-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-12-07 1993-06-08 1993-12-08 $7700.00 Window Closed / Lapsed

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