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

被引:1
|
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 ; 0836 ; 090102 ; 100705 ;
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 50 条