J M Obón, J R Maiquez, M Cánovas, H P Kleber, J L Iborra
Index: Appl. Microbiol. Biotechnol. 51(6) , 760-4, (1999)
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The use of a biological procedure for L-carnitine production as an alternative to chemical methods must be accompanied by an efficient and highly productive reaction system. Continuous L-carnitine production from crotonobetaine was studied in a cell-recycle reactor with Escherichia coli O44 K74 as biocatalyst. This bioreactor, running under the optimum medium composition (25 mM fumarate, 5 g/l peptone), was able to reach a high cell density (26 g dry weight/l) and therefore to obtain high productivity values (6.2 g L-carnitine l-1 h-1). This process showed its feasibility for industrial L-carnitine production. In addition, resting cells maintained in continuous operation, with crotonobetaine as the only medium component, kept their biocatalytic capacity for 4 days, but the biotransformation capacity decreased progressively when this particular method of cultivation was used.
Structure | Name/CAS No. | Molecular Formula | Articles |
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Levocarnitine impurity A
CAS:927-89-9 |
C7H13NO2 |
Effect of salt stress on crotonobetaine and D(+)-carnitine b...
2003-01-01 [J. Basic Microbiol. 43(4) , 259-68, (2003)] |
Biotransformation of crotonobetaine to L(-)-carnitine in Pro...
2001-05-01 [Arch. Microbiol. 175(5) , 353-9, (2001)] |
Molecular characterization of the cai operon necessary for c...
1994-09-01 [Mol. Microbiol. 13(5) , 775-86, (1994)] |
[Metabolism of L-carnitine in enterobacteria].
1980-01-01 [Z. Allg. Mikrobiol. 20(9) , 591-4, (1980)] |
Salt stress effects on the central and carnitine metabolisms...
2007-03-01 [Biotechnol. Bioeng. 96(4) , 722-37, (2007)] |
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