Hybridomas in a bioreactor cascade: Modeling and determination of growth and death kinetics

被引:8
作者
Bakker, WAM [1 ]
Schafer, T [1 ]
Beeftink, HH [1 ]
Tramper, J [1 ]
DeGooijer, CD [1 ]
机构
[1] AGR UNIV WAGENINGEN,DEPT FOOD SCI,FOOD & BIOPROC ENGN GRP,NL-6700 EV WAGENINGEN,NETHERLANDS
关键词
hybridomas; serum-free medium; monoclonal antibodies; reactor series; kinetics; modeling;
D O I
10.1007/BF00365349
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
Hybridomas were cultured under steady-state conditions in a series of two continuous stirred-tank reactors (CSTRs), using a serum-free medium. The substrate not completely converted in the first CSTR, was transported with the cells to the second one and very low growth rates, high death rates, and lysis of viable cells were observed in this second CSTR. These conditions are hardly accessible in a single vessel, because such experiments would be extremely time-consuming and unstable due to a low viability. In contrast to what is often observed in literature, kinetic parameters could thus be derived without the neccessity for extrapolation to lower growth rates. Good agreement with literature averages for other hybridomas was found. Furthermore, showing that the reactor series is a valuable research tool for kinetic studies under extreme conditions, the possibility to observe cell death under stable and defined steady-state conditions offers interesting opportunities to investigate apoptosis and necrosis. Additionally, a model was developed that describes hybridoma growth and monoclonal antibody production in the bioreactor cascade on the basis of glutamine metabolism. Good agreement between the model and the experiments was found.
引用
收藏
页码:263 / 277
页数:15
相关论文
共 29 条
[1]   CONTINUOUS PRODUCTION OF LACTIC-ACID FROM WHEY PERMEATE BY LACTOBACILLUS-HELVETICUS IN 2 CHEMOSTATS IN SERIES [J].
AESCHLIMANN, A ;
DISTASI, L ;
VONSTOCKAR, U .
ENZYME AND MICROBIAL TECHNOLOGY, 1990, 12 (12) :926-932
[2]   SPECIFIC MONOCLONAL-ANTIBODY PRODUCTIVITY AND THE CELL CYCLE-COMPARISONS OF BATCH, CONTINUOUS AND PERFUSION CULTURES [J].
ALRUBEAI, M ;
EMERY, AN ;
CHALDER, S ;
JAN, DC .
CYTOTECHNOLOGY, 1992, 9 (1-3) :85-97
[3]   KINETICS OF NUTRIENT-LIMITED TRANSPORT AND MICROBIAL-GROWTH [J].
BUTTON, DK .
MICROBIOLOGICAL REVIEWS, 1985, 49 (03) :270-297
[4]   Bioreactors in series: An overview of design procedures and practical applications [J].
deGooijer, CD ;
Bakker, WAM ;
Beeftink, HH ;
Tramper, J .
ENZYME AND MICROBIAL TECHNOLOGY, 1996, 18 (03) :202-219
[5]   KINETIC-STUDY OF HYBRIDOMA CELL-GROWTH IN CONTINUOUS CULTURE .2. BEHAVIOR OF PRODUCERS AND COMPARISON TO NONPRODUCERS [J].
FRAME, KK ;
HU, WS .
BIOTECHNOLOGY AND BIOENGINEERING, 1991, 38 (09) :1020-1028
[6]   KINETIC-STUDY OF HYBRIDOMA CELL-GROWTH IN CONTINUOUS CULTURE .1. A MODEL FOR NONPRODUCING CELLS [J].
FRAME, KK ;
HU, WS .
BIOTECHNOLOGY AND BIOENGINEERING, 1991, 37 (01) :55-64
[7]   REDUCTION OF WASTE PRODUCT EXCRETION VIA NUTRIENT CONTROL - POSSIBLE STRATEGIES FOR MAXIMIZING PRODUCT AND CELL YIELDS ON SERUM IN CULTURES OF MAMMALIAN-CELLS [J].
GLACKEN, MW ;
FLEISCHAKER, RJ ;
SINSKEY, AJ .
BIOTECHNOLOGY AND BIOENGINEERING, 1986, 28 (09) :1376-1389
[8]   DETERMINATION OF CELL-LYSIS AND DEATH KINETICS IN CONTINUOUS HYBRIDOMA CULTURES FROM THE MEASUREMENT OF LACTATE-DEHYDROGENASE RELEASE [J].
GOERGEN, JL ;
MARC, A ;
ENGASSER, JM .
CYTOTECHNOLOGY, 1993, 11 (03) :189-195
[9]   MINIMUM TANK VOLUMES FOR CFST BIOREACTORS IN SERIES [J].
HILL, GA ;
ROBINSON, CW .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1989, 67 (05) :818-824
[10]   A KINETIC-ANALYSIS OF HYBRIDOMA GROWTH AND METABOLISM IN CONTINUOUS SUSPENSION-CULTURE ON SERUM-FREE MEDIUM [J].
HILLER, GW ;
AESCHLIMANN, AD ;
CLARK, DS ;
BLANCH, HW .
BIOTECHNOLOGY AND BIOENGINEERING, 1991, 38 (07) :733-741