ENHANCING OXYGEN-TRANSFER IN SURFACE-AERATED BIOREACTORS BY STABLE FOAMS

被引:6
作者
JU, LK
ARMIGER, WB
机构
[1] BioChem Technology, Inc., Malvern, Pennsylvania, 19355
关键词
D O I
10.1021/bp00004a005
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
To enhance oxygen transfer in surface‐aeration bioreactors, stabilized foams were generated to increase the gas‐liquid interfacial area by slowly introducing coarse bubbles into media containing fetal bovine serum. The bubble sparging rates were so low (i.e., 20 and 50 mL/h) that the contribution to oxygen transfer from these bubbles was due to foaming instead of bubbling. Furthermore, no physical cell damage caused by bubble sparging was observed. Oxygen transfer coefficients, kLa, in the bioreactors were measured in cell‐free media. Without the foam‐stabilizing agent (i.e., serum), no appreciable change in kLa was observed due to the bubble sparging. On the other hand, with serum, kLa increased with increasing serum content and bubble sparging rate and corresponded well with the degree of foaming. With 10% fetal bovine serum and a bubble sparging rate of 50 mL/h, kLa increased approximately 90% compared with no foaming. The enhancing effect of foam on oxygen transfer in surface aeration bioreactors has been further demonstrated with hybridoma cultures simultaneously grown in three identical bioreactors with and without stabilized foams. Copyright © 1990 American Institute of Chemical Engineers (AIChE)
引用
收藏
页码:262 / 265
页数:4
相关论文
共 14 条
[1]  
Glacken M.W., Fleischaker R.J., Sinskey A.J., Largescale Production of Mammalian Cells and their Products: Engineering, Principles and Barriers to Scale‐up, Ann. N.Y. Acad. Sci., 413, (1983)
[2]  
Kilburn D.G., Lilly M.D., Self D.A., Webb F.C., J. Cell Sci., 4, (1969)
[3]  
Kilburn D.G., Webb F.C., The Cultivation of Animal Cells at Controlled Dissolved Oxygen Partial Pressure, Biotechnology and Bioengineering, 10, (1968)
[4]  
Telling R.C., Submerged Culture of Hamster Kidney Cells in a Stainless Steel Vessel, Biotechnology and Bioengineering, 7, (1965)
[5]  
Handa A., Emery A.N., Spier R.E., On the Evaluation of Gas‐Liquid Interfacial Effects on Hybridoma Viability in Bubble Column Bioreactors, Dev. Biol. Stand., 66, (1987)
[6]  
MacMichael G., Armiger W.B., Lee J.F., Mutharasan R., On‐Line Measurement of Hybridoma Growth by Culture Fluorescence, Biotechnol. Tech., 1, (1987)
[7]  
Ozato K., Mayer N., Sachs D.H., Hybridoma Cell Lines Secreting Monoclonal Antibodies to Mouse H‐2 and I<sub>a</sub> Antigens, J. Immunol., 124, (1980)
[8]  
MacMichael G., The Use of Continuous Culture to Optimize the Hybridoma Culture Environment, Fed. Proc., 46, (1987)
[9]  
Bosworth J.M., Brimfield A., Naylor J.A., Hunter K.W., Measurement of Monoclonal Antibody Concentrations in Hybridoma Cultures: Comparison of Competitive Inhibition and Antigen Capture Enzyme Immunoassays, J. Immunol Methods, 62, (1983)
[10]  
Dang N.D.P., Karrer D.A., Oxygen, Transfer Coefficients by Dynamic Model Moment Analysis, Biotechnol. Bioeng., 19, (1977)