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Biomedical subjects

N Zach

Publications and source records attributed to N Zach.

5 recordsLinked to original sources

Stable, continuous large-scale production of human monoclonal HIV-1 antibody using a computer-controlled pilot plant.

A completely automated pilot plant used for fermentation has been employed with direct digital control (DDC) technology for monitoring and regulating growth of human cells. A human hybridoma cell line (3D6) producing anti-human immunodeficiency virus (HIV)-1 antibodies was used as a model for large-scale production (300-liter airlift fermentor) in continuous culture. Parameters controlled were pH, dissolved oxygen, temperature and the flow rate of four gases used in the process. A control strategy was implemented to achieve constant fluid velocity and mixing by maintaining the rate of gas flow at a constant level. Another advantage of this approach was that the total gas flow required for optimal fluid circulation was reduced from 1 volume gas/volume fermenter/hour (vvh) to 0.3 vvh. Use of a low flow rate eliminated the serious problems of foaming, which contributed significantly to cell destruction, shorter filter-life and other considerations. Dilution rate was optimized at laboratory scale for maximum productivity, which results in relatively low viability. At a dilution rate of 0.0076 h-1, a total cell density of 6-7 x 10(5) cells/ml with a viability of approximately 75% was maintained during long-term continuous cultivation. These growth conditions resulted in a product titer stabilized in the range of 35 micrograms IgG/ml. Batchwise purification was achieved with a recovery of more than 50% and a final purification of active monoclonal antibody representing about 99% product. Results from isoelectric focusing and Western blotting demonstrated batch-to-batch consistency of the purified human monoclonal antibody to HIV-1 during the continuous growth process.(ABSTRACT TRUNCATED AT 250 WORDS)

Antibodies, Monoclonal↗

Flow cytometry and two-dimensional electrophoresis (2-DE) for system evaluation of long term continuous perfused animal cell cultures in macroporous beads.

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.

Animals↗

Modular integrated fluidized bed bioreactor 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.

Animals↗

The use of macroporous gelatin carriers for the cultivation of mammalian cells in fluidised bed reactors.

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.

Animals↗