Gg. Benito et al., CONTINUOUS GLYCEROL PRODUCTION IN A PACKED-BED BIOREACTOR WITH IMMOBILIZED CELLS OF SACCHAROMYCES-CEREVISIAE, Bioresource technology, 49(3), 1994, pp. 209-212
Citations number
11
Categorie Soggetti
Energy & Fuels","Biothechnology & Applied Migrobiology",Agriculture
Batch and continuous glycerol fermentations of sugar beet molasses hav
e been studied using sulphite as a combining agent with the aldehyde f
unction. The processes were carried out in a vertical packed-bed react
or with Saccharomyces cerevisiae yeast cells immobilized in sintered g
lass rings. The influence of sulphite dosage and the dilution rate on
the performance of the bioreactor was studied. A maximum glycerol conc
entration of 30 g dm-3 and a productivity of 36.6 g dm-3 d-1 at T = 28
-degrees-C, pH = 6.9 with 25 g dm-3 sodium sulphite, for a dilution ra
te of 1.22 d-1, was achieved.