Skip to main content
Log in

Influence of alterations in culture condition and changes in perfusion parameters on the retention performance of a 20 μm spinfilter during a perfusion cultivation of a recombinant CHO cell line in pilot scale

  • Published:
Cytotechnology Aims and scope Submit manuscript

Abstract

Since 1969 much attention has been devoted to the useof spinfilter systems for retention of mammalian cellsin continuous perfusion cultivations. Previousinvestigations dealt with hydrodynamic conditions,fouling processes and upscaling. But hydrodynamicconditions and fouling processes seem to have asecondary importance in spinfilter performance duringauthentic perfusion cultivations. Obviously,alterations in culture condition are more relevantespecially during long-term processes. Therefore, ourpratical approach focussed on the performance qualityof a commercially available 20 μm spinfilterduring a perfusion cultivation of a recombinant CHOcell line in pilot scale regarding the followingissues: 1) retention of viable cells in thebioreactor; 2) removal of dead cells and cell debrisfrom the bioreactor; 3) alterations in culturecondition; and 4) changes in perfusion mode.Furthermore, we tested the performance of 20 μmspinfilters in 2 and 100 l pilot scale using solidmodel particles instead of cells. Our investigationsshowed that retention of viable cells in pilot scalewas independent of spinfilter rotation velocity andperfusion rate; the retention increased from 75 to 95%corresponding to operation time, enlarging celldiameter and enhanced formation of aggregates in theculture during the perfusion cultivation. By means ofthe Cell Counter and Analyzer System (CASY) anoperation cut off of 13 μm was determined forthis spinfilter. Using solid model particles in 2 lscale, optimal retention was achieved at a tip speedof 0.43 m s-1 (141 rpm) – furtherenhancement of spinfilter rotation velocity up to0.56 m s-1 (185 rpm) decreased the retentionrapidly. In pilot scale best retention performance wasobtained with tip speeds of 0.37 m s-1(35 rpm) and 1.26 m s-1 (120 rpm). Hence,significant retention in pilot scale could already beachieved with low agitation. Therefore, the additionof shear force protectives could be avoided so thatthe purification of the target protein from thesupernatant would be facilitated.

This is a preview of subscription content, log in via an institution to check access.

Access this article

Price excludes VAT (USA)
Tax calculation will be finalised during checkout.

Instant access to the full article PDF.

Similar content being viewed by others

References

  • Avgerinos GC, Drapeau D, Socolow JS, Mao J, Hsiao K and Broeze RJ (1990) Spinfilter perfusion systems for high density cell culture: Production of recombinant urinary type plasminogen activator in CHO cells. Biotechnology (NY) 8: 54–58.

    Google Scholar 

  • Büntemeyer H, Bödeker BGD and Lehmann J (1987) Membranestirrer-reactor for bubble-free aeration and perfusion. In: Spier RE and Griffiths JB (eds) Modern Approaches to Animal Cell Technology, Butterworth, pp. 411–419.

  • Büntemeyer H, Lütkemeyer D and Lehmann J (1991) Optimization of serum-free fermentation processes for antibody production. Cytotechnology 5: 57–67.

    Google Scholar 

  • Büntemeyer H, Stenner A and Lehmann J (1998) Rapid quantitative determination of ammonium concentration in cell culture fluid (in press).

  • Chen Z, Chen Y, Chen J and Shen C (1992) Effects of ammonium and lactate on hybridoma growth metabolism. Chin J Biotechnol 8: 255–261.

    Google Scholar 

  • Deo, YM, Mahadevan MD and Fuchs R (1996) Practical considerations in operation and scale-up of spin-filter based bioreactors for monoclonal antibody production. Biotechnol Progr 12: 57–64.

    Google Scholar 

  • Esclade LRJ, Carrel S and Peringer P (1988) Influence of the screen material on the fouling of spin filters. Biotechnol Bioeng 38: 159–168.

    Google Scholar 

  • Favre E and Thaler T (1992) An engineering analysis of rotating sieves for hybridoma cell retention in stirred tank bioreactors. Cytotechnology 9: 11–19.

    Google Scholar 

  • Fenge C, Klein C, Heuer C, Siegel U and Fraune E (1993) Aegitation, aeration and perfusion modules for cell culture bioreactors. Cytotechnology 11: 233–244.

    Google Scholar 

  • Glacken MW, Adema E and Sinskey AJ (1988) Mathematical descriptions of hybridoma kinetics: I. Initial metabolic rates. Biotechnol Bioeng 32: 491–506.

    Google Scholar 

  • Himmelfarb P, Thayer PS and Martin HE (1969) Spin filter culture: The propagation of mammalian cells in suspension. Science 164: 555–557.

    Google Scholar 

  • Johnson M, Lanthier S, Massie B, Lefebvre G and Kamen AA (1996) Use of the Centritech Lab centrifuge for perfusion culture of hybridoma cells in protein-free medium. Biotechnol Progr 12: 855–864.

    Google Scholar 

  • Lütkemeyer D, Heidemann R, Tebbe H, Gudermann F, Schmidt M, Raditsch M and Lehmann J (1999) Pilot Scale Production of Human Prothrombin using a rCHO Cell Line. In: A. Bernard et al. (eds) Animal Cell Technology: Products from Cells, Cells as Products, Kluwer Academic Publishers, Dordrecht, pp. 99–101.

    Google Scholar 

  • Lydersen BK (1991) Perfusion cell culture systems based on ceramic matrices. In: Lydersen BK (ed) Large Scale Cell Culture Technology, Carl Hanser Verlag, pp. 169–192.

  • Ozturk SS, Riley MR and Palsson BO (1992) Effect of ammonia and lactate on hybridoma growth, metabolism and antibody production. Biotechnol Bioeng 35: 1067–1077.

    Google Scholar 

  • Rebsamen E, Goldinger W, Scheirer W, Merten O-W and Palfi GE (1987) Use of a dynamic filtration method for seperation of animal cells. In: Spier RE and Griffiths GB (eds) Modern Approaches to Animal Cell Technology. Butterworth, pp. 548–555.

  • Sanford KK, Ealre WR, Evans VJ, Waltz HK and Shannon JE (1950) The measurement to proliferation in tissue culture by enumeration of cell nuclei. JNCI 11: 733–795.

    Google Scholar 

  • Seewöster T and Lehmann J (1995) Influence of targeted asparagine starvation on extra-and intracellular amino acid pools of cultivated Chinese hamster ovary cells. Appl Microbiol Biotechnol 44: 344–350.

    Google Scholar 

  • Seewöster T and Lehmann J (1997) Cell size distribution as a parameter for the predetermination of exponential growth during repeated batch cultivation of CHO cells. Biotechnol Bioeng 55: 793–797.

    Google Scholar 

  • Sittinger M, Schultz O, Keyszer G, Minuth WW and Burmester GR (1997) Artificial tissues in perfusion culture. Int Artif Organs 20: 57–62.

    Google Scholar 

  • Tennant JR (1964) Evaluation of trypan blue technique for determination of cell viability. Transplantation 2: 685–694.

    Google Scholar 

  • Takamatsu H, Hamamoto K, Ishimaru K, Yokoyama S and Tokashiki M (1996): Large-scale perfusion culture process for suspended mammalian cells that uses a centrifuge with multiple settling zones. Appl Microbiol Biotechnol 45: 454–457.

    Google Scholar 

  • Tokashiki M, Arai T, Hamamoto K and Ishimaru K (1990) High density culture of hybridoma cells using a perfusion culture vessel with an external centrifuge. Cytotechnology 3: 239–244.

    Google Scholar 

  • Vournakis JN and Runstadler PW (1991) Optimization of the microenvirement for mammalian cell culture in flexible collagen microspheres in a fluidized-bed bioreactor. In: Ho CS, Wang DIC (eds) Animal Cell Bioreactors. Butterworth-Heinemann, pp. 305–326.

Download references

Author information

Authors and Affiliations

Authors

Corresponding author

Correspondence to Kai Iding.

Rights and permissions

Reprints and permissions

About this article

Cite this article

Iding, K., Lütkemeyer, D., Fraune, E. et al. Influence of alterations in culture condition and changes in perfusion parameters on the retention performance of a 20 μm spinfilter during a perfusion cultivation of a recombinant CHO cell line in pilot scale. Cytotechnology 34, 141–150 (2000). https://doi.org/10.1023/A:1008183508439

Download citation

  • Issue Date:

  • DOI: https://doi.org/10.1023/A:1008183508439

Navigation