LACTIC-ACID FROM CHEESE WHEY PERMEATE - PRODUCTIVITY AND ECONOMICS OFA CONTINUOUS MEMBRANE BIOREACTOR

Citation
S. Tejayadi et M. Cheryan, LACTIC-ACID FROM CHEESE WHEY PERMEATE - PRODUCTIVITY AND ECONOMICS OFA CONTINUOUS MEMBRANE BIOREACTOR, Applied microbiology and biotechnology, 43(2), 1995, pp. 242-248
Citations number
19
Categorie Soggetti
Biothechnology & Applied Migrobiology
ISSN journal
01757598
Volume
43
Issue
2
Year of publication
1995
Pages
242 - 248
Database
ISI
SICI code
0175-7598(1995)43:2<242:LFCWP->2.0.ZU;2-V
Abstract
The economics of incorporating membrane modules in several steps in th e conversion of whey permeate to lactic acid was studied. Membrane rec ycle fermenters operating at a cell concentration of 40 g l(-1) result ed in a productivity of 22.5 g l(-1)h(-1) with a lactate concentration of 89 g l(-1) and a yield of 0.89. The membrane units (reverse osmosi s for preconcentrating whey permeate, hollow-fiber ultrafiltration for clarification and for cell recycling) contribute about 28% of the tot al fixed capital costs and less than 5% of the operating cost. The two largest costs are whey transportation and yeast extract, contributing about 35% and 38% to the total product cost of US $ 0.98/kg 85% lacta te. Without these two costs; unpurified lactate could be produced for $ 0.27/kg.