An evaluation of fed-batch cultivation methods for mammalian cells based on model simulations

Special Engineering Aspects

The specific characteristics of mammalian cells discussed in Chap. 2 require adapted solutions for bioreactor design and operation. Especially, cell damage by shear stress and aeration has to be considered. Therefore this chapter starts with a detailed discussion of shear stress effects on mammalian cells (anchorage-dependent and suspendable cells) in model systems and bioreactors, respectively, and consequences for reactor design. Appropriate oxygen supply is another critical issue, as adapted oxygen supply systems are required. Techniques for immobilization of cells, either grown on microcarriers in suspension culture or within macroporous carriers in fixed bed or fluidized bed reactors, are discussed as well. With respect to the operation of bioreactors, the characteristics of different culture modes (batch, fed-batch, chemostat, perfusion) are introduced and practical examples are given. Finally, concepts for monitoring of bioreactors, including offline and online methods as well as control loops (e.g. O₂, pH), are considered.

Mathematical modeling of proteinase A overproduction by Saccharomyces cerevisiae

A simple, structured model was developed to describe the growth and product formation behavior of two recombinant strains of Saccharomyces cerevisiae (JG176 and JG180), both overproducing extracellular proteinase A. The model parameters were estimated to data from continuous fermentations obtained at steady-state conditions. Model predictions show good agreement with experimental data obtained by batch fermentations. The two concerned organisms are distinguished from each other by the type of promoter on the plasmids controlling the proteinase A expression. The proteinase A transcription is controlled by the natural proteinase A promoter in JG176 and by a tpi promoter in JG180. By means of experiments and simulations, the extracellular product formation from the two strains with different promoter systems was compared in batch and continuous fermentations. The results showed that the proteinase A formation kinetic from JG176 was a combination of growth and nongrowth associated (production in the stationary growth phase), whereas the proteinase A formation from JG180 was truly growth associated (production in the exponential growth phase). In both batch and continuous cultivations JG176 gave the highest product concentrations and volumetric productivities.