Modeling and experimental studies on intermittent starch feeding and citrate addition in simultaneous saccharification and fermentation of starch to flavor compounds

被引:9
作者
Chavan, Abhijit R. [1 ]
Raghunathan, Anuradha [1 ]
Venkatesh, K. V. [1 ]
机构
[1] Indian Inst Technol, Dept Chem Engn, Bombay 400076, Maharashtra, India
关键词
Lactobacillus rhamnosus; Glucoamylase; SSF; Diacetyl; Acetoin; Lactic acid; Mathematical model; Citrate addition; Intermittent addition of starch; LACTIC-ACID; MICROBIAL-GROWTH; SACCHAROMYCES-CEREVISIAE; STRAW;
D O I
10.1007/s10295-008-0520-9
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
Simultaneous saccharification and fermentation (SSF) is a combined process of saccharification of a renewable bioresource and fermentation process to produce products, such as lactic acid and ethanol. Recently, SSF has been extensively used to convert various sources of cellulose and starch into fermentative products. Here, we present a study on production of buttery flavors, namely diacetyl and acetoin, by growing Lactobacillus rhamnosus on a starch medium containing the enzyme glucoamylase. We further develop a structured kinetics for the SSF process, which includes enzyme and growth kinetics. The model was used to simulate the effect of pH and temperature on the SSF process so as to obtain optimum operating conditions. The model was experimentally verified by conducting SSF using an initial starch concentration of 100 g/L. The study demonstrated that the developed kinetic was able to suggest strategies for improved productivities. The developed model was able to accurately predict the enhanced productivity of flavors in a three stage process with intermittent addition of starch. Experimental and simulations demonstrated that citrate addition can also lead to enhanced productivity of flavors. The developed optimal model for SSF was able to capture the dynamics of SSF in batch mode as well as in a three stage process. The structured kinetics was also able to quantify the effect of multiple substrates present in the medium. The study demonstrated that structured kinetic models can be used in the future for design and optimization of SSF as a batch or a fed-batch process.
引用
收藏
页码:509 / 519
页数:11
相关论文
共 26 条
  • [1] SIMULTANEOUS SACCHARIFICATION AND FERMENTATION OF CELLULOSE TO LACTIC-ACID
    ABE, S
    TAKAGI, M
    [J]. BIOTECHNOLOGY AND BIOENGINEERING, 1991, 37 (01) : 93 - 96
  • [2] Simultaneous saccharification and fermentation of starch to lactic acid
    Anuradha, R
    Suresh, AK
    Venkatesh, KV
    [J]. PROCESS BIOCHEMISTRY, 1999, 35 (3-4) : 367 - 375
  • [3] ANURADHA R, 1999, THESIS INDIAN I TECH
  • [4] OPTIMIZATION OF BATCH PROCESSES INVOLVING SIMULTANEOUS ENZYMATIC AND MICROBIAL REACTIONS
    ASENJO, JA
    SUN, WH
    SPENCER, JL
    [J]. BIOTECHNOLOGY AND BIOENGINEERING, 1991, 37 (11) : 1087 - 1094
  • [5] Cardenas I. L. B. de, 1989, Current Microbiology, V18, P351, DOI 10.1007/BF01571127
  • [6] DIXIT JB, 2003, J BIOSCI BIOENG, V96, P481
  • [7] An optimal model for microbial growth in a multiple substrate environment: simultaneous and sequential utilization
    Doshi, P
    Venkatesh, KV
    [J]. PROCESS BIOCHEMISTRY, 1998, 33 (06) : 663 - 670
  • [8] HUGENHOLTZ J, 1993, FEMS MICROBIOL REV, V12, P165, DOI [10.1016/0168-6445(93)90062-E, 10.1111/j.1574-6976.1993.tb00017.x]
  • [9] Statistical optimization of simultaneous saccharification and L(+)-lactic acid fermentation from cassava bagasse using mixed culture of lactobacilli by response surface methodology
    John, Rojan P.
    Sukumaran, Rajeev K.
    Nampoothiri, K. Madhavan
    Pandey, Ashok
    [J]. BIOCHEMICAL ENGINEERING JOURNAL, 2007, 36 (03) : 262 - 267
  • [10] CYBERNETIC MODELING OF MICROBIAL-GROWTH ON MULTIPLE SUBSTRATES
    KOMPALA, DS
    RAMKRISHNA, D
    TSAO, GT
    [J]. BIOTECHNOLOGY AND BIOENGINEERING, 1984, 26 (11) : 1272 - 1281