Filtration‐based perfusion of hybridoma cultures in protein‐free medium: Reduction of membrane fouling by medium supplementation with DNase I

In this study, a filtration‐based perfusion process was developed for the production of monoclonal antibodies (IgM) by suspended hybridoma cells grown in protein‐free medium. It was found that the use of protein‐free medium for perfusion culture generated the formation of numerous visible suspended particles consisting of dead cells and cellular debris aggregated into fibrous material. Surprisingly high apparent viabilities were observed in such protein‐free cultures. In addition, membrane fouling occurred more rapidly in protein‐free medium than in conventional serum‐supplemented medium. By the addition of deoxyribonuclease I (DNase I) to the protein‐free medium, it was possible to prevent the formation of aggregates and to follow the evolution of the total cell population more accurately. Moreover, DNase I significantly reduced the fouling of filtration membranes, and that, for two different types of separation systems (cross‐flow and vortex‐flow filtration) and two different types of membranes (polycarbonate and hydrophilized polysultone). From these results, it is clear that the presence of DNA fragments liberated following cellular death is playing an important role in membrane fouling. Longevity of filtration membranes was found to be considerably greater using a vortex‐flow filtration module than with a static plate‐and‐frame cross‐flow filtration module. The use of vortex‐flow filtration of conjuction with DNase I allowed maintenance of perfusion cultures for more than 1 month without membrane fouling or antibody retention and with a constant permeate IgM concentration of 250 mg/L. Hybridomacells appeared to gradually adapt to increasing rotational speed in the vortex‐flow filtration module.

[1]  J. Côté,et al.  High-performance gel permeation chromatographic analysis of immunoglobulin M produced by hybridoma cell culture , 1992 .

[2]  R. Lemieux,et al.  Hybridoma perfusion systems: A comparison study , 1992, Biotechnology and bioengineering.

[3]  D. Tidd,et al.  Partial protection of oncogene, anti-sense oligodeoxynucleotides against serum nuclease degradation using terminal methylphosphonate groups. , 1989, British Journal of Cancer.

[4]  I. Cabasso Practical Aspects in the Development of a Polymer Matrix for Ultrafiltration , 1980 .

[5]  T. Vomastek,et al.  Kinetics of development of spontaneous apoptosis in B cell hybridoma cultures. , 1993, Immunology letters.

[6]  W C Davis,et al.  A novel continuous centrifugal bioreactor for high‐density cultivation of mammalian and microbial cells , 1991, Biotechnology and bioengineering.

[7]  A. Michaels,et al.  Mechanisms of polarization and fouling of ultrafiltration membranes by proteins , 1983 .

[8]  R. Lemieux,et al.  Characterization of higher avidity monoclonal antibodies produced by murine B-cell hybridoma variants selected for increased antigen binding of membrane Ig. , 1988, Journal of immunology.

[9]  D D Ryu,et al.  Monoclonal antibody productivity and the metabolic pattern of perfusion cultures under varying oxygen tensions , 1993, Biotechnology and bioengineering.

[10]  M. Goosen,et al.  Alginate‐Polylysine Microcapsules of Controlled Membrane Molecular Weight Cutoff for Mammalian Cell Culture Engineering , 1987 .

[11]  K. Yamagiwa,et al.  Effects of antifoam with inverted cloud point on permeation and solute rejection in membrane filtration process. , 1989 .

[12]  Denis Drapeau,et al.  Spin Filter Perfusion System for High Density Cell Culture: Production of Recombinant Urinary Type Plasminogen Activator in CHO Cells , 1990, Bio/Technology.

[13]  L. Esclade,et al.  Influence of the screen material on the fouling of spin filters , 1991, Biotechnology and bioengineering.

[14]  T. Gribnau,et al.  Monitoring of the production of monoclonal antibodies by hybridomas. Part II: Characterization and purification of acid proteases present in cell culture supernatant. , 1991, Journal of biotechnology.

[15]  V. Jäger,et al.  Strategies to Increase the Efficiency of Membrane Aerated and Perfused Animal Cell Bioreactors by an Improved Medium Perfusion , 1991 .

[16]  H. Murakami Serum-free media used for cultivation of hybridomas. , 1989, Advances in biotechnological processes.

[17]  D. Nitsch,et al.  Extinction of gene expression in somatic cell hybrids--a reflection of important regulatory mechanisms? , 1993, Trends in genetics : TIG.

[18]  R. Buehler,et al.  Entrapment and Growth of Murine Hybridoma Cells in Calcium Alginate Gel Microbeads , 1989, Nature Biotechnology.

[19]  J. Young,et al.  Effect of Culture Conditions on IgM Antibody Structure, Pharmacokinetics and Activity , 1993, Bio/Technology.

[20]  M. Doko,et al.  CONSEQUENCES of FOULING and MACROMOLECULE ADSORPTION ONTO ULTRAFILTRATION MEMBRANE FOR PINEAPPLE JUICE PROCESSING , 1991 .

[21]  G. Belfort,et al.  Continuous hybridoma growth and monoclonal antibody production in hollow fiber reactors–separators , 1986, Biotechnology and bioengineering.

[22]  C. Goochee,et al.  Scaleup of Insect Cell Cultures: Protective Effects of Pluronic F-68 , 1988, Bio/Technology.

[23]  H. Gregor,et al.  Synthetic-Membrane Technology , 1978 .

[24]  V. Jäger,et al.  Proteolytic Activities in Serum-Free Supernatants of Mammalian Cell Lines , 1991 .

[25]  G. Salvesen,et al.  Human plasma proteinase inhibitors. , 1983, Annual review of biochemistry.

[26]  A. Fane,et al.  The effect of surfactant pretreatment on the ultrafiltration of proteins , 1985 .

[27]  C. Cooney,et al.  Mammalian cell and protein distributions in ultrafiltration hollow fiber bioreactors , 1990, Biotechnology and bioengineering.

[28]  B. Bellhouse,et al.  Gel layer limited haemofiltration rates can be increased by vortex mixing. , 1981, Clinical and experimental dialysis and apheresis.

[29]  B. Palsson,et al.  Serum can act as a shear protecting agent in agitated hybridoma cell cultures. , 1989, Hybridoma.

[30]  D K Robinson,et al.  Effect of specific growth rates on productivity in continuous open and partial cell retention animal cell bioreactors. , 1992, Journal of biotechnology.

[31]  F Franĕk,et al.  Nucleosomes occurring in protein‐free hybridoma cell culture Evidence for programmed cell death , 1991, FEBS letters.

[32]  J. H. Lee,et al.  Surface properties of copolymers of alkyl methacrylates with methoxy (polyethylene oxide) methacrylates and their application as protein-resistant coatings. , 1990, Biomaterials.

[33]  U. Onken,et al.  Selective recycle of viable animal cells by coupling of airlift reactor and cell settler. , 1992, Biotechnology and bioengineering.

[34]  R. Spier,et al.  A comparison of oxygenation methods fro high‐density perfusion culture of animal cells , 1993, Biotechnology and bioengineering.

[35]  R. Lemieux,et al.  Long‐term perfusion culture of hybridoma: A “grow or die” cell cycle system , 1991, Biotechnology and bioengineering.

[36]  A. Fane,et al.  The performance of ultrafiltration membranes pretreated by polymers , 1988 .

[37]  B. Maiorella,et al.  Crossflow microfiltration of animal cells , 1991, Biotechnology and bioengineering.

[38]  L. Miller,et al.  Use of tangential flow filtration in perfusion propagation of hybridoma cells for production of monoclonal antibodies. , 1989, Biotechnology and bioengineering.