Automated fed-batch culture of Kluyveromyces fragilis based on a novel method for on-line estimation of cell specific growth rate

被引:26
作者
Nor, ZM [1 ]
Tamer, MI [1 ]
Scharer, JM [1 ]
Moo-Young, M [1 ]
Jervis, EJ [1 ]
机构
[1] Univ Waterloo, Dept Chem Engn, Waterloo, ON N2L 3G1, Canada
关键词
fermentation; aerobic processes; fed-batch culture; kinetic parameters; yeast; lactase;
D O I
10.1016/S1369-703X(01)00147-4
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
A corrected feed-forward control strategy was developed for automated substrate feeding in aerobic fed-batch cultures. The control strategy incorporates a novel method for on-line estimation of specific growth rate as a performance indicator of the fed-batch culture. The estimation is based on the measurement of the maximum substrate uptake rate (MSUR) using on-line dissolved oxygen (DO) concentration data and mass balances. It allows the controller to track changes in the specific growth rate to compensate for process disturbances. The control strategy was applied to fed-batch culture of Kluyveromyces fragilis to maximize the volumetric productivity of lactase. A maximum volumetric lactase productivity of 2.98 U/ml h was achieved. The control was shown to be stable throughout the culture period even at the highest cell density of 69 g/l. This technique is applicable to various aerobic systems, especially for microbial cultures showing high specific oxygen uptake rates, since it only requires on-line measurement of DO concentration without the need for off-gas analysis. In a comparison carried out with three other fed-batch control strategies (DO-stat, exponential feeding and exponential feeding with manual feedback control), the corrected feed-forward control strategy exhibited the best performance by achieving the highest volumetric lactase and biomass productivity. Crown Copyright (C) 2001 Published by Elsevier Science B.V. All rights reserved.
引用
收藏
页码:221 / 231
页数:11
相关论文
共 28 条
[1]   Dissolved oxygen concentration-controlled feeding of substrate into Kluyveromyces fragilis culture [J].
Barberis, SE ;
Segovia, RF .
BIOTECHNOLOGY TECHNIQUES, 1997, 11 (11) :797-799
[2]  
BRAFORD JK, 1987, YEAST BIOTECHNOLOGY, P200
[3]  
CASTILLO FJ, 1990, YEAST BIOTECHNOLOGY, V5, P297
[4]  
Cheng CY, 1997, BIOTECHNOL BIOENG, V56, P23, DOI 10.1002/(SICI)1097-0290(19971005)56:1<23::AID-BIT3>3.0.CO
[5]  
2-X
[6]   A DETAILED ANALYSIS OF SACCHAROMYCES-CEREVISIAE GROWTH-KINETICS IN BATCH, FED-BATCH, AND HOLLOW-FIBER BIOREACTORS [J].
COPPELLA, SJ ;
DHURJATI, P .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1989, 41 (02) :B27-B35
[7]   COLORIMETRIC METHOD FOR DETERMINATION OF SUGARS AND RELATED SUBSTANCES [J].
DUBOIS, M ;
GILLES, KA ;
HAMILTON, JK ;
REBERS, PA ;
SMITH, F .
ANALYTICAL CHEMISTRY, 1956, 28 (03) :350-356
[8]  
FIECHTER A, 1989, ADV BIOCHEM ENG, V30, P1
[9]   AN AUTOMATIC AND STERILIZABLE SAMPLER FOR LABORATORY FERMENTERS - APPLICATION TO THE ONLINE CONTROL OF GLUCOSE-CONCENTRATION [J].
GHOUL, M ;
RONAT, E ;
ENGASSER, JM .
BIOTECHNOLOGY AND BIOENGINEERING, 1986, 28 (01) :119-121
[10]   ENHANCED CELLULASE PRODUCTION IN FED-BATCH CULTURE OF TRICHODERMA-REESEI C30 [J].
HENDY, NA ;
WILKE, CR ;
BLANCH, HW .
ENZYME AND MICROBIAL TECHNOLOGY, 1984, 6 (02) :73-77