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1.
FASEB J ; 28(11): 4764-78, 2014 Nov.
Article in English | MEDLINE | ID: mdl-25070367

ABSTRACT

The blood-brain barrier (BBB) prevents the access of therapeutic antibodies to central nervous system (CNS) targets. The engineering of bispecific antibodies in which a therapeutic "arm" is combined with a BBB-transcytosing arm can significantly enhance their brain delivery. The BBB-permeable single-domain antibody FC5 was previously isolated by phenotypic panning of a naive llama single-domain antibody phage display library. In this study, FC5 was engineered as a mono- and bivalent fusion with the human Fc domain to optimize it as a modular brain delivery platform. In vitro studies demonstrated that the bivalent fusion of FC5 with Fc increased the rate of transcytosis (Papp) across brain endothelial monolayer by 25% compared with monovalent fusion. Up to a 30-fold enhanced apparent brain exposure (derived from serum and cerebrospinal fluid pharmacokinetic profiles) of FC5- compared with control domain antibody-Fc fusions after systemic dosing in rats was observed. Systemic pharmacological potency was evaluated in the Hargreaves model of inflammatory pain using the BBB-impermeable neuropeptides dalargin and neuropeptide Y chemically conjugated with FC5-Fc fusion proteins. Improved serum pharmacokinetics of Fc-fused FC5 contributed to a 60-fold increase in pharmacological potency compared with the single-domain version of FC5; bivalent and monovalent FC5 fusions with Fc exhibited similar systemic pharmacological potency. The study demonstrates that modular incorporation of FC5 as the BBB-carrier arm in bispecific antibodies or antibody-drug conjugates offers an avenue to develop pharmacologically active biotherapeutics for CNS indications.


Subject(s)
Antibodies, Bispecific/metabolism , Biological Products/metabolism , Blood-Brain Barrier/metabolism , Animals , Antibodies, Bispecific/immunology , Biological Transport/physiology , Brain/metabolism , Humans , Immunoconjugates/metabolism , Male , Protein Engineering/methods , Rats, Wistar , Recombinant Fusion Proteins/metabolism
2.
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
3.
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
4.
Biotechnol Bioeng ; 91(7): 779-92, 2005 Sep 30.
Article in English | MEDLINE | ID: mdl-15986489

ABSTRACT

Enhanced product yields, reduction in throughput time, improved cost-effectiveness and product quality are examples of benefits gained by delaying apoptotic cell death in bioreactors. To examine the effect on recombinant protein production, bcl-x(L) was overexpressed in a CHO cell line secreting humanized monoclonal antibody directed against the alpha1beta1 integrin. When cell lines overexpressing bcl-x(L) were compared to the parent, cell viability was increased by 20% and titers by 80%. Total viable cell densities were similar and specific productivities were enhanced by almost two-fold on scale-up to bioreactors. Comparison in a chemically defined media demonstrated an even greater sustained viability in bcl-x(L) expressing cells by 50% and up to 90% increase in titer with no impact on product quality. Caspase 3 activities were monitored as a marker for apoptotic cell death. In the presence of Bcl-x(L), caspase activities were reduced to background levels. The role of Bcl-x(L) in protecting cells from premature death was further examined in studies performed in the presence of NaBu, at concentrations known to trigger cell death. Results demonstrated that cells expressing bcl-x(L) retained 88% cell viability with >2 fold increase in titer. Bcl-x(L) was similarly overexpressed in a different CHO cell line producing a humanized mAb against the chemokine MCP1. Once again, production titer was increased by 80% and viability by 75%. Together the studies have shown that overexpression of bcl-x(L) in production cell lines was able to significantly increase the titer by enhancing both the specific activity and total cell viability while maintaining product quality.


Subject(s)
Antibodies, Monoclonal/biosynthesis , Biotechnology/methods , CHO Cells/metabolism , Cell Culture Techniques , bcl-X Protein/genetics , Animals , Antibodies, Monoclonal/genetics , Antibodies, Monoclonal/immunology , Apoptosis , Bioreactors , Caspase 3 , Caspases/analysis , Cell Count , Cell Survival , Chemokine CCL2/immunology , Cricetinae , Culture Media/chemistry , Fermentation , Humans , Integrin alpha1beta1/immunology , Recombinant Proteins/biosynthesis , Recombinant Proteins/genetics , bcl-X Protein/immunology
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