Continuous production of L-carnitine with NADH regeneration by a nanofiltration membrane reactor with coimmobilized L-carnitine dehydrogenase and glucose dehydrogenase

Citation
Ss. Lin et al., Continuous production of L-carnitine with NADH regeneration by a nanofiltration membrane reactor with coimmobilized L-carnitine dehydrogenase and glucose dehydrogenase, J BIOSCI BI, 87(3), 1999, pp. 361-364
Citations number
12
Categorie Soggetti
Biotecnology & Applied Microbiology",Microbiology
Journal title
JOURNAL OF BIOSCIENCE AND BIOENGINEERING
ISSN journal
13891723 → ACNP
Volume
87
Issue
3
Year of publication
1999
Pages
361 - 364
Database
ISI
SICI code
1389-1723(199903)87:3<361:CPOLWN>2.0.ZU;2-4
Abstract
L-Carnitine dehydrogenase (CDH) was partially purified from Pseudomonas put ida IAM12014 for the stereospecific reduction of 3-dehydrocarnitine to L-ca rnitine. CDH and glucose dehydrogenase (GDH) were coimmobilized in a nanofi ltration membrane bioreactor (NFMBR) for the continuous production of L-car nitine from 3-dehydrocarnitine with NADH regeneration. In the NFMBR, NAD wa s partially immobilized through rejection by the nanofiltration membrane an d effectively regenerated by the conjugation reaction of CDH and GDH. Since 3-dehydrocarnitine was unstable at neutral pH, it was maintained under aci dic conditions (pH 0.7) and supplied to the NFMBR separately from the other substrates, glucose and coenzyme NAD. As 50 mM 3-dehydrocarnitine in HCl s olution, 0.05 mM NAD, and 100 mM glucose in 0.5 M Tris buffer (pH 8) were c ontinuously supplied to the NFMBR with immobilized CDH (200 U/ml) and GDH ( 200 U/ml) at the retention time of 80 min and temperature of 25 degrees C, the maximum conversion, reactor productivity, and NAD regeneration number w ere 78%, 113 g/l/d, and 780, respectively. The half-life of the NFMBR was l onger than 500 h.