L-lactic acid production by Lactobacillus casei fermentation using different fed-batch feeding strategies

被引:146
|
作者
Ding, Shaofeng [1 ]
Tan, Tianwei [1 ]
机构
[1] Beijing Univ Chem Technol, Coll Life Sci & Technol, Key Lab Bioproc Beijing, Beijing 100029, Peoples R China
基金
美国国家科学基金会;
关键词
L-lactic acid; fermentation; batch fermentation; fed-batch fermentation; exponential fed-batch; Lactobacillus casei;
D O I
10.1016/j.procbio.2006.01.014
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
In this paper, the L-lactic acid production by Lactobacillus casei fermentation using different fed-batch feeding strategies was studied. The effects of different fed-batch methods such as pulse fed-batch, constant feed rate fed-batch, constant residual glucose concentration fed-batch and exponential fed-batch on the fermentation Of L-lactic acid were determined. According to the results of experiments, exponential fed-batch culture is an effective method for the fermentation Of L-lactic acid. The maximum lactic acid concentration (210 g 1(-1)) and L-lactic acid concentration (180 g 1(-1)) in exponential feeding glucose solution (850 g 1-1) and yeast extract (1%) was obtained, respectively. L-lactic acid yield, the maximal dry cell weight and productivity were up to 90.3%, 4.30 g 1(-1), 2.14 g 1(-1) h(-1), respectively. Comparing with the traditional batch culture, the exponential feeding glucose and yeast extract culture showed 56.5% improvement in L-lactic acid production, 68.6% improvement in dry cell weight and 59.7% improvement in productivity, respectively. (c) 2006 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1451 / 1454
页数:4
相关论文
共 50 条
  • [31] Lactic Acid Production from Old Oil Palm Trunk Sap in the Open Batch, Open Repeated Batch, Fed-Batch, and Repeated Fed-Batch Fermentation by Lactobacillus rhamnosus ATCC 10863
    Saelee, Nisa
    FERMENTATION-BASEL, 2022, 8 (09):
  • [32] Phenyllactic acid production by fed-batch fermentation of Lactobacillus plantarum CECT-221
    Rodriguez, Noelia
    Manuel Salgado, Jose
    Max, Belen
    Cortes, Sandra
    Manuel Dominguez, Jose
    JOURNAL OF BIOTECHNOLOGY, 2010, 150 : S320 - S320
  • [33] Effect of different fermentation strategies on β-mannanase production in fed-batch bioreactor system
    Germec, Mustafa
    Yatmaz, Ercan
    Karahalil, Ercan
    Turhan, Irfan
    3 BIOTECH, 2017, 7
  • [34] Effect of different fermentation strategies on β-mannanase production in fed-batch bioreactor system
    Mustafa Germec
    Ercan Yatmaz
    Ercan Karahalil
    İrfan Turhan
    3 Biotech, 2017, 7
  • [35] Biopolymer production in a fed-batch reactor using optimal feeding strategies
    Lai, Song-Yi
    Kuo, Po-Chih
    Wu, Wei
    Jang, Ming-Feng
    Chou, Yi-Shyong
    JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 2013, 88 (11) : 2054 - 2061
  • [36] Production of L(+) Lactic Acid using Lactobacillus casei from Whey
    Panesar, Parmjit S.
    Kennedy, John F.
    Knill, Charles J.
    Kosseva, Maria
    BRAZILIAN ARCHIVES OF BIOLOGY AND TECHNOLOGY, 2010, 53 (01) : 219 - 226
  • [37] CONTINUOUS PRODUCTION OF L-LACTIC ACID FROM WHEY PERMEATE BY IMMOBILIZED LACTOBACILLUS-CASEI SUBSP CASEI
    KRISCHKE, W
    SCHRODER, M
    TROSCH, W
    APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 1991, 34 (05) : 573 - 578
  • [38] Optimization of operational parameters for preparation of l-lactic acid by fermentation of waste tobacco stems with lactobacillus casei
    Zhu, Daheng
    Yang, Zengguang
    Zhang, Keke
    Ding, Tengge
    Zhang, Mianmian
    Zou, Chunyang
    Yan, Xiaojing
    Wang, Jingfen
    Jia, Yingbo
    Xi, Yu
    Tobacco Science and Technology, 2015, 48 (11): : 22 - 27
  • [39] L-lactic acid production by Lactobacillus casei fermentation with corn steep liquor-supplemented acid-hydrolysate of soybean meal
    Key Lab of Bioprocess of Beijing, College of Life Science and Technology, Beijing University of Chemical Technology, Beijing, China
    Biotechnol. J., 2006, 12 (1453-1458):
  • [40] Evaluation of L-lactic acid production in batch, fed-batch, and continuous cultures of Rhizopus sp MK-96-1196 using an airlift bioreactor
    Liu, TJ
    Miura, S
    Arimura, T
    Tei, MY
    Park, EY
    Okabe, M
    BIOTECHNOLOGY AND BIOPROCESS ENGINEERING, 2005, 10 (06) : 522 - 527