XYLITOL PRODUCTION BY IMMOBILIZED RECOMBINANT SACCHAROMYCES-CEREVISIAE IN A CONTINUOUS PACKED-BED BIOREACTOR

Citation
E. Roca et al., XYLITOL PRODUCTION BY IMMOBILIZED RECOMBINANT SACCHAROMYCES-CEREVISIAE IN A CONTINUOUS PACKED-BED BIOREACTOR, Biotechnology and bioengineering, 51(3), 1996, pp. 317-326
Citations number
39
Categorie Soggetti
Biothechnology & Applied Migrobiology
ISSN journal
00063592
Volume
51
Issue
3
Year of publication
1996
Pages
317 - 326
Database
ISI
SICI code
0006-3592(1996)51:3<317:XPBIRS>2.0.ZU;2-3
Abstract
Continuous xylitol production with two different immobilized recombina nt Saccharomyces cerevisiae strains (H475 and S641), expressing low an d high xylose reductase (XR) activities, was investigated in a lab-sca le packed-bed bioreactor. The effect of hydraulic residence time (HRT; 1.3-11.3 h), substrate/cosubstrate ratio (0.5 and 1), recycling ratio (0, 5, and 10), and aeration (anaerobic and oxygen limited conditions ) were studied. The cells were immobilized by gel entrapment using Ca- alginate as support and the beads were treated with Al3+ to improve th eir mechanical strength. Xylose was converted to xylitol using glucose as cosubstrate for regeneration of NAD(P)H required in xylitol format ion and for generation of maintenance energy. The stability of the rec ombinant strains after 15 days of continuous operation was evaluated b y XR activity and plasmid retention analyses. Under anaerobic conditio ns the volumetric xylitol productivity increased with decreasing HRT w ith both strains. With a recycling ratio of 10, volumetric productivit ies as high as 3.44 and 5.80 g/L . h were obtained with the low XR str ain at HRT 1.3 h and with the high XR strain at HRT 2.6 h, respectivel y. However, the highest overall xylitol yields on xylose and on cosubs trate were reached at higher HRTs. Lowering the xylose/cosubstrate rat io from 1 to 0.5 increased the overall yield of xylitol on xylose, but the productivity and the xylitol yield on cosubstrate decreased. Unde r oxygen limited conditions the effect of the recycling ratio on produ ction parameters was masked by other factors, such as an accumulation of free cells in the bioreactor and severe genetic instability of the high XR strain. Under anaerobic conditions the instability was less se vere, causing a decrease in XR activity from 0.15 to 0.10 and from 3.1 8 to 1.49 U/mg with the low and high XR strains, respectively. At the end of the fermentation, the fraction of plasmid bearing cells in the beads was close to 100% for the low XR strain; however, it was signifi cantly lower for the high XR strain, particularly for cells from the i nterior of the beads. (C) 1996 John Wiley & Sons, Inc.