TY - JOUR
T1 - Strategies for fed-batch cultivation of t-PA producing CHO cells
T2 - Substitution of glucose and glutamine and rational design of culture medium
AU - Altamirano, C.
AU - Paredes, C.
AU - Illanes, A.
AU - Cairó, J. J.
AU - Gòdia, F.
N1 - Funding Information:
Financial support from the Comisión Interministerial de Ciencia y Tecnologı́a (CICYT), Project BIO97-0542 and BIOTECH program from UE, BIO4-CT96-0556, are gratefully acknowledged. Claudia Altamirano was a fellow of the Instituto de Cooperación Iberoamericana, and Chilean Government. This work has been carried out under the framework of the Centre de Referencia en Biotecnologı́a (Generalitat de Catalunya).
PY - 2004/5/27
Y1 - 2004/5/27
N2 - A strategy for fed-batch cultivation of t-PA producing recombinant CHO cells is presented, based on the substitution of glucose and glutamine for slowly metabolized nutrients and in a rational design of the medium. Media for the batch and fed stages were based on the cell specific amino acid requirements, which allowed a more accurate determination of the initiation of the fed stage and the frequency of nutrient addition from then on. Salt concentration was also reduced in both media to avoid an increase in osmolality. As a consequence of this rational design, most amino acid did not accumulate significantly during the fed stage, as usually occurs when their supply is not based on cell requirements; also, lower amounts of by-products were obtained when osmolality level was kept low, that altogether increased viability, longevity and t-PA production when compared with a reference batch culture. Alternating glucose and galactose during the fed stage, allowed lactate detoxification of the cells through their own metabolism. This allowed an increase in cell growth and cell viability with respect to a fed-batch culture in which only glucose was used in the fed stage.
AB - A strategy for fed-batch cultivation of t-PA producing recombinant CHO cells is presented, based on the substitution of glucose and glutamine for slowly metabolized nutrients and in a rational design of the medium. Media for the batch and fed stages were based on the cell specific amino acid requirements, which allowed a more accurate determination of the initiation of the fed stage and the frequency of nutrient addition from then on. Salt concentration was also reduced in both media to avoid an increase in osmolality. As a consequence of this rational design, most amino acid did not accumulate significantly during the fed stage, as usually occurs when their supply is not based on cell requirements; also, lower amounts of by-products were obtained when osmolality level was kept low, that altogether increased viability, longevity and t-PA production when compared with a reference batch culture. Alternating glucose and galactose during the fed stage, allowed lactate detoxification of the cells through their own metabolism. This allowed an increase in cell growth and cell viability with respect to a fed-batch culture in which only glucose was used in the fed stage.
KW - CHO cells
KW - Fed-batch
KW - Galactose
KW - Glutamate
KW - Metabolism
KW - t-PA
UR - http://www.scopus.com/inward/record.url?scp=2342537013&partnerID=8YFLogxK
U2 - 10.1016/j.jbiotec.2004.02.004
DO - 10.1016/j.jbiotec.2004.02.004
M3 - Article
C2 - 15121336
AN - SCOPUS:2342537013
SN - 0168-1656
VL - 110
SP - 171
EP - 179
JO - Journal of Biotechnology
JF - Journal of Biotechnology
IS - 2
ER -