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1.
Biotechnol Prog ; 23(2): 458-64, 2007.
Article in English | MEDLINE | ID: mdl-17311405

ABSTRACT

The amount of recombinant product obtained from mammalian cells grown in a bioreactor is in part limited by achievable cell densities and the ability of cells to remain viable over extended periods of time. In an attempt to generate cell lines capable of better bioreactor performance, we subjected the DG44 Chinese Hamster Ovary (CHO) host cell line and a recombinant production cell line to an iterative process whereby cells capable of surviving the harsh conditions in the bioreactor were selected. This selective process was termed "bioreactor evolution". Following the selective process, the "evolved" host cells attained a 2-fold increase in peak cell density and a 72% increase in integral cell area. Transient transfection experiments demonstrate that the evolved cells have the same transfection efficiency and the same secretory potential as the initial cells. The "evolved" host was also found to contain a large subpopulation of cells that did not require insulin for growth. From this, a new population of growth-factor-independent cells was obtained. These improvements in host properties should prove beneficial in the expression of recombinant proteins in fed-batch processes. The selective process was also applied to a recombinant production cell line. The evolved cells from this selection exhibited a 38% increase in peak cell density, a 30% increase in integral cell area, and a 36% increase in product titer. These increases were obtained without any appreciable impact on product quality, demonstrating the usefulness of this simple approach to improve the performance of recombinant cell lines.


Subject(s)
Biological Evolution , Bioreactors , Cell Culture Techniques/methods , Cell Line/physiology , Protein Engineering/methods , Recombinant Proteins/biosynthesis , Adaptation, Physiological/genetics , Animals , CHO Cells , Cricetinae , Cricetulus , Humans
2.
J Biotechnol ; 128(1): 50-60, 2007 Jan 30.
Article in English | MEDLINE | ID: mdl-17083990

ABSTRACT

An expression vector has been generated using a gene highly expressed under conditions found in a typical fed-batch bioreactor process. The ferritin heavy chain (HC) gene exhibits higher levels of expression in the late stages of a fed-batch bioreactor than in the early stages. This property was considered advantageous for an expression vector, since the maximal cell density would coincide with maximal expression. The rat ferritin HC genomic region was isolated and converted into an expression vector where large segments of 5' and 3' flanking regions were included in an attempt to recreate the same high level of expression in stably transfected cells. Expression from the resulting ferritin HC vector was compared to vectors containing the commonly used strong promoters, CMV IE, and SV40 early promoter/enhancer, in the generation of stable transfectants. The ferritin HC vector was able to generate cell lines with significantly higher expression levels than those under the control of the viral promoters.


Subject(s)
Apoferritins/genetics , Gene Expression Regulation/genetics , Genetic Vectors/genetics , Animals , Apoferritins/metabolism , Base Sequence , Bioreactors , CHO Cells , Cricetinae , Cricetulus , Genetic Vectors/biosynthesis , Molecular Sequence Data , Rats , S Phase/genetics , S Phase/physiology
3.
Anal Biochem ; 353(2): 204-8, 2006 Jun 15.
Article in English | MEDLINE | ID: mdl-16564018

ABSTRACT

Human IgG4 subtype antibodies have often been reported to have a significant portion (5-50%) of a heavy chain-light chain dimer ("half-antibody") on sodium dodecyl sulfate-polyacrylamide gel electrophoresis (SDS-PAGE), in which the heavy chain is not covalently linked through the hinge disulfides to another heavy chain. We demonstrate here that there can be artifactual sources of half-antibody. One occurred during SDS-PAGE sample preparation where rapid disulfide scrambling was initiated by preexisting free sulfhydryls in the monoclonal antibody (mAb) and by free sulfhydryl produced by destruction of disulfide bonds during heating. Inclusion of N-ethylmaleimide in the sample buffer prevented the disulfide scrambling. Presumably, cyclization of the flexible IgG4 hinge during this disulfide scrambling leads to the preferential separation of heavy chains. A second condition producing half-antibody was reoxidation after exposure to reductant, where 46% of the antibody was trapped in the intrachain disulfide form. The amount of half-antibody was reduced to 4% by reoxidation in the presence of a mixture of oxidized and reduced glutathione. When the improved sample preparation conditions were used, IgG4 mAb freshly isolated from cells contained 4.5-15% half-antibody, indicating that equilibration of the interchain and intrachain hinge disulfide pairing was not always attained in cells.


Subject(s)
Artifacts , Electrophoresis, Polyacrylamide Gel/methods , Immunoglobulin G/analysis , Antibodies, Monoclonal/metabolism , Cell Line , Disulfides/metabolism , Ethylmaleimide/metabolism , Ethylmaleimide/pharmacology , Humans , Immunoglobulin Fragments/analysis , Immunoglobulin Fragments/metabolism , Immunoglobulin G/isolation & purification , Immunoglobulin G/metabolism , Oxidation-Reduction
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