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  • 1
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 49 (1996), S. 456-466 
    ISSN: 0006-3592
    Keywords: microcarrier culture ; turbulent mixing ; 3-D particle tracking ; energy dissipation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Three-dimensional particle tracking velocimetry (3-D PTV), a modern, quantitative, visualization tool, has been applied to the characterization of the flow field in the impeller region of cell culture reactor vessels. The experimental system used here is a 250-mL microcarrier spinner vessel. The studies were conducted at three different agitation rates, 90, 150, and 210 rpm, corresponding to healthy, mildly damaging, and severely damaging shear intensities, respectively. The flow can be classified into three regions: a predominantly tangential (azimuthal) flow generated by the impeller; a trailing vortex region coming off the impeller tip; and a converging flow region close to the center of the vessel. The latter two are the regions of highest velocity gradients. Energy dissipation rates due to mean velocity gradients were also calculated to characterize the impeller stream. Local specific energy dissipation rates 〉 10,000 erg/(cm3sec) · have been measured. It is proposed that the critical regions for microcarrier culture damage due to impeller hydrodynamics are the trailing vortex region and the high energy converging flow region. Graphical representation of the mean velocity flow fields and the distribution of energy dissipation rates in the impeller region are also presented here. The merits of using the dissipation function (measure of specific energy dissipation rate) as a possible scale-up parameter are also discussed. © 1996 John Wiley & Sons, Inc.
    Additional Material: 12 Ill.
    Type of Medium: Electronic Resource
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  • 2
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 39 (1992), S. 504-510 
    ISSN: 0006-3592
    Keywords: hybridoma ; continuous culture ; dialysis ; monoclonal antibody ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Hybridoma cell growth and monoclonal antibody production in dialyzed continuous suspension culture were investigated using a 1.5-L Celligen bioreactor. Medium supplemented with 1.5% fetal bovine serum was fed directly into the reactor at a dilution rate of 0.45 d-1. Dailysis tubing with a molecular weight cut-off (MWCO) of 1000 was coiled inside the bioreactor. Fresh medium containing no serum or serum substitues passed through the dialysis tubing at flow rates of 2 to 5 L/d. The objective was to remove low molecular weight inhibitors, such as lactic acid and ammonia, by diffusion through the tubing, while continuoulsy replenishing essential nutrients by the same mechanism. Due to the low MWCO of the dialysis tubing high molecular weight components such as growth factors and antibody were not removed by the dialyzing stream. In the batch start-up phase, the monoclonal antibody (MAb) titer was almost 3 times that achieved in typical batch cultures (i.e., 170 to 180 mg/L). During dialyzed continuous operation, a substantial increase (up to 40%) in cell density, monoclonal antibody (MAb) titer, and reactor MAb productivity was observed, as compared with a conventional continuous suspension culture. The cell viability and the specific MAb productivity remained practically constant at different dialysis rates. This finding suggests that the steady state growth and death rate in continuous suspension hybridoma cultures are not direct functions of the nutrient or inhibitor concentrations.
    Additional Material: 5 Ill.
    Type of Medium: Electronic Resource
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