Monoclonal antibody production using the porous glass bead immobilization technique. Serum-free perfusion.
Explore the source record for details and available documents.
Biomedical subjects
Publications and source records attributed to T Gaida.
Explore the source record for details and available documents.
Immobilization of r-CHO cells at high density using macroporous polyethylene carriers in a modular fluidized bed reactor is demonstrated. Specific growth rates of the cells are measured by incorporation of BrdU. At a cell density of about 10(8) cells/ml a stable growth rate of 0.004 h-1 was established. Total release of proteins into the culture supernatant during protein-free perfusion was analyzed by 2-DE in various phases of the long-term culture showing very similar patterns indicating a constant pattern of gene expression.
As most high density and immobilized fermentation systems do not allow the direct quantitative determination of cell density, two flow cytometric methods (the determination of incorporation of bromodeoxyuridine into newly synthesized DNA and the increase in mitotic cells by colchicine blockage) were evaluated as to their suitability to measure true division rates of cells in bioreactors. The BrdU method gave division rates identical to the growth rates measured by cell count, while the colchicine block method gave values that were lower and varied with the cell line. This is due to the cytotoxicity of colchicine and makes a calibration of the method for each cell line necessary. Both methods have been successfully used to measure division rates of rCHO cells immobilized in an alginate matrix as well as in macroporous carriers in a fluidised bed system and in dialysis culture.
A nonrecombinant human melanoma cell line and recombinant chinese hamster ovary (CHO) cells were used as examples for long-term in vitro cultivation in protein-free media. The method used to monitor the consistency of protein release by these mammalian cells was two-dimensional electrophoresis with immobilized pH gradient. Secreted proteins from a melanoma cell line cultivated in a continuous fermentation system over a period of 22 months were monitored. Two-dimensional patterns of secreted proteins were compared and the stability of their composition was determined over a period of nearly 14 months, with significant pattern variation being observed after 14 months. The protein pattern from this extended in vitro culture was compared to those of the very same melanoma cell line recultivated after being frozen in liquid nitrogen for more than 2 years. Due to the high resolution of complex polypeptide mixtures and the possibility to detect even minor differences in the composition of protein patterns, we propose the two-dimensional electrophoresis as a tool for quality assessment in animal cell culture technology.
We describe the design and demonstrate the application of a modular integrated fluidized bed bioreactor system. Basically the system is a reactor vessel equipped with an extending cylinder and a liquid distributor plate. Instead of an external recirculation loop, as used in existing fluidized bed systems, a low shear stress impeller is used as the recirculation pump. The system has several unique features, such as modular exchangeable elements, efficient oxygenation and the option of operating as a stirred tank-, a packed bed- or a fluidized bed reactor. An example of a fluidized bed run using CHO-K1 cells is shown. Under standard culture conditions a 100-fold increase in cell density (up to 1.2 x 10(8) cells/ml) was achieved.
A fluidised bed system for the cultivation of mammalian cells on a new type of macroporous gelatin microcarrier is described. The volumetric cell densities achieved under controlled conditions for two 'standard cell lines' (VERO, CHO) were one order of magnitude higher compared to conventional techniques using spherical microcarriers. The system can be potentially used for both anchorage dependent and independent cells.