HIGH VIABLE CELL CONCENTRATION FED-BATCH CULTURES OF HYBRIDOMA CELLS THROUGH ONLINE NUTRIENT FEEDING

被引:134
作者
ZHOU, WC
REHM, J
HU, WS
机构
[1] Department of Chemical Engineering and Materials Sciences, University of Minnesota, Minneapolis, Minnesota, 55455-0132
[2] Merck Research Laboratories, Merck & Co, Inc., Rahway, New Jersey, 07065
关键词
HYBRIDOMA CELLS; PROCESS CONTROL; ENERGY METABOLISM; ONLINE NUTRIENT FEEDING; FED-BATCH CULTURE;
D O I
10.1002/bit.260460611
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 hybridoma cell line was cultivated in fed-batch cultures using a low-protein, serum-free medium. On-line oxygen uptake rate (OUR) measurement was used to adjust the nutrient feeding rate based on glucose consumption, which was estimated on-line using the stoichiometric relations between glucose and oxygen consumption. Through on-line control of the nutrient feeding rate, not only sufficient nutrients were supplied for cell growth and antibody production, but also the concentrations of glucose and other important nutrients such as amino acids were maintained at low levels during the cell growth phase. During the cultivation, cell metabolism changed from high lactate production and low oxygen consumption to low lactate production and high oxygen consumption. As a result the accumulation of lactate was reduced and the growth phase was extended. In comparison with the batch cultures, in which cells reached a concentration of approximately 2 x 10(6) cells/mL, a very high concentration of 1.36 x 10(7) cells/mL with a high cell viability (>90%) was achieved in the fed-batch culture. By considering the consumption of glucose and amino acids, as well as the production of cell mass, metabolites, and antibodies, a well-closed material balance was established. Our results demonstrate the value of coupling on-line OUR measurement and the stoichiometric relations for dynamic nutrient feeding in high cell concentration fed-batch cultures. (C) 1995 John Wiley & Sons, Inc.
引用
收藏
页码:579 / 587
页数:9
相关论文
共 24 条
[1]   MONOCLONAL-ANTIBODY PROCESS-DEVELOPMENT USING MEDIUM CONCENTRATES [J].
BIBILA, TA ;
RANUCCI, CS ;
GLAZOMITSKY, K ;
BUCKLAND, BC ;
AUNINS, JG .
BIOTECHNOLOGY PROGRESS, 1994, 10 (01) :87-96
[2]   INDUSTRIAL-PRODUCTION OF MONOCLONAL-ANTIBODIES AND THERAPEUTIC PROTEINS BY DIALYSIS FERMENTATION [J].
COMER, MJ ;
KEARNS, MJ ;
WAHL, J ;
MUNSTER, M ;
LORENZ, T ;
SZPERALSKI, B ;
KOCH, S ;
BEHRENDT, U ;
BRUNNER, H .
CYTOTECHNOLOGY, 1990, 3 (03) :295-299
[3]   LOSS OF VIABILITY IN HYBRIDOMA CELL-CULTURE - A KINETIC-STUDY [J].
DODGE, TC ;
JI, GY ;
HU, WS .
ENZYME AND MICROBIAL TECHNOLOGY, 1987, 9 (10) :607-611
[4]  
FLEISCHAKER RJ, 1981, THESIS MIT CAMBRIDGE
[5]   CELL-VOLUME MEASUREMENT AS AN ESTIMATION OF MAMMALIAN-CELL BIOMASS [J].
FRAME, KK ;
HU, WS .
BIOTECHNOLOGY AND BIOENGINEERING, 1990, 36 (02) :191-197
[6]   CATABOLIC CONTROL OF MAMMALIAN-CELL CULTURE [J].
GLACKEN, MW .
BIO-TECHNOLOGY, 1988, 6 (09) :1041-&
[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]  
Hu W S, 1987, Dev Biol Stand, V66, P279
[9]  
HU W-S, 1992, Current Opinion in Biotechnology, V3, P110, DOI 10.1016/0958-1669(92)90137-8
[10]   ANIMAL-CELL BIOREACTORS - RECENT ADVANCES AND CHALLENGES TO SCALE-UP [J].
HU, WS ;
PESHWA, MV .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1991, 69 (02) :409-420