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

被引:42
作者
TEJAYADI, S [1 ]
CHERYAN, M [1 ]
机构
[1] UNIV ILLINOIS,AGR BIOPROC LAB,URBANA,IL 61801
关键词
D O I
暂无
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 [微生物学]; 0836 [生物工程]; 090102 [作物遗传育种]; 100705 [微生物与生化药学];
摘要
The economics of incorporating membrane modules in several steps in the conversion of whey permeate to lactic acid was studied. Membrane recycle fermenters operating at a cell concentration of 40 g l(-1) resulted 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 osmosis for preconcentrating whey permeate, hollow-fiber ultrafiltration for clarification and for cell recycling) contribute about 28% of the total 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% lactate. Without these two costs; unpurified lactate could be produced for $ 0.27/kg.
引用
收藏
页码:242 / 248
页数:7
相关论文
共 19 条
[1]
Axtell O., 1986, EC EVALUATION CHEM P
[2]
CHERYAN M, 1984, PROCESS BIOCHEM, V19, P204
[3]
Cheryan M., 1986, ULTRAFILTRATION HDB
[4]
Garrett D.E., 1989, CHEM ENG EC
[5]
Gienger J. K., 1988, AICHE S SER, V84, P168
[6]
ECONOMIC-EVALUATION OF THE ACETONE-BUTANOL FERMENTATION [J].
LENZ, TG ;
MOREIRA, AR .
INDUSTRIAL & ENGINEERING CHEMISTRY PRODUCT RESEARCH AND DEVELOPMENT, 1980, 19 (04) :478-483
[7]
MEHAIA MA, 1987, PROCESS BIOCHEM, V22, P185
[8]
LACTIC-ACID FROM ACID WHEY PERMEATE IN A MEMBRANE RECYCLE BIOREACTOR [J].
MEHAIA, MA ;
CHERYAN, M .
ENZYME AND MICROBIAL TECHNOLOGY, 1986, 8 (05) :289-292
[9]
A NUMERICAL EVALUATION OF A HOLLOW FIBER EXTRACTIVE FERMENTER PROCESS FOR THE PRODUCTION OF ETHANOL [J].
NASER, SF ;
FOURNIER, RL .
BIOTECHNOLOGY AND BIOENGINEERING, 1988, 32 (05) :628-638
[10]
PACE GW, 1975, SINGLE CELL PROTEIN, V2, P330