Development of a fermentation process for production of calcium-L-lactate

被引:11
作者
Gao, Min-Tian [1 ]
Hirata, Makoto [1 ]
Toorisaka, Eiichi [1 ]
Hano, Tadashi [1 ]
机构
[1] Oita Univ, Dept Appl Chem, Oita 8701192, Japan
基金
日本学术振兴会;
关键词
Bioprocess; Fermentation; Calcium-L-lactate; Flocculation; Lactobacillus rhamnosus; LACTIC-ACID PRODUCTION; LACTOBACILLUS-CASEI; NITROGEN-SOURCES; ZINC LACTATE; HYDROLYSIS; CRYSTALLIZATION; CELLS; WATER; WHEY;
D O I
10.1016/j.cep.2008.06.002
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
This study is an effort to develop an efficient process for low-cost production Of calcium-L-lactate (CaL2). CaL2 showed higher inhibitory effect on lactate production than ammonium-L-lactate (NH4) at lactate concentration lower than 100 g/L, but it showed lower inhibitory effect at higher lactate concentration. The strain Lactobacillus rhamnosus (NBRC 3863) was resistant to glucose inhibition and final CaL2 concentration increased with initial glucose concentration increasing up to 190 g/L High-concentration CaL2 induced, however, flocculation of fermentation broth, causing incomplete fermentation. It was confirmed that stirring speed markedly influenced flocculation, an increase of the stirring speed leading to an earlier flocculation. Formation of colloidal CaL2 during fermentation was considered to be the cause of flocculation in this study. Addition of YE raised fermentation efficiency and made complete fermentation feasible. In the fermentation with 25 g/L YE, glucose was completely consumed and final CaL2 concentration of 220 g/L was obtained. when flocculation did not yet occur. In this study, CaL2 crystals and activated carbon powder were added as nucleation sites to get earlier crystallization of colloids and to decrease the inhibitory effect of CaL2, and so to increase productivity. Of the two nucleation sites, activated carbon powder showed higher performance in CaL2 Production. Finally, the feasibility of crystallization-based recovery without concentration step was discussed. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:464 / 469
页数:6
相关论文
共 17 条
[1]   Supplementation of whey with glucose and different nitrogen sources for lactic acid production by Lactobacillus delbrueckii [J].
Arasaratnam, V ;
Senthuran, A ;
Balasubramaniam, K .
ENZYME AND MICROBIAL TECHNOLOGY, 1996, 19 (07) :482-486
[2]   Solubilities of calcium and zinc lactate in water and water-ethanol mixture [J].
Cao, X ;
Lee, HJ ;
Yun, HS ;
Koo, YM .
KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2001, 18 (01) :133-135
[3]   Crystallization and dissolution Behavior of L(+) calcium and zinc lactate in ethanol-water solvent [J].
Cao, XJ ;
Lee, HJ ;
Yun, HS ;
Koo, YM .
KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2002, 19 (02) :301-304
[4]   Crystallization kinetics of calcium lactate in a mixed-suspension-mixed-product removal crystallizer [J].
Chemaly, Z ;
Muhr, H ;
Fick, M .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (07) :2803-2808
[5]   Lactic acid: recent advances in products, processes and technologies - a review [J].
Datta, Rathin ;
Henry, Michael .
JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 2006, 81 (07) :1119-1129
[6]   Acid-hydrolysis of fish wastes for lactic acid fermentation [J].
Gao, Min-Tian ;
Hirata, Makoto ;
Toorisaka, Eiichi ;
Hano, Tadashi .
BIORESOURCE TECHNOLOGY, 2006, 97 (18) :2414-2420
[7]   Study on acid-hydrolysis of spent cells for lactic acid fermentation [J].
Gao, MT ;
Hirata, M ;
Toorisaka, E ;
Hano, T .
BIOCHEMICAL ENGINEERING JOURNAL, 2006, 28 (01) :87-91
[8]   Production of L-lactic acid by electrodialysis fermentation (EDF) [J].
Gao, MT ;
Hirata, M ;
Koide, M ;
Takanashi, H ;
Hano, T .
PROCESS BIOCHEMISTRY, 2004, 39 (12) :1903-1907
[9]   Factors affecting the fermentative lactic acid production from renewable resources [J].
Hofvendahl, K ;
Hahn-Hägerdal, B .
ENZYME AND MICROBIAL TECHNOLOGY, 2000, 26 (2-4) :87-107
[10]  
Hsieh CM, 1999, PROCESS BIOCHEM, V34, P173, DOI 10.1016/S0032-9592(98)00081-8