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  • 1
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 8 (1979), S. 157-165 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Three yeasts of the genus Candida (Candida intermedia, candida lipolytica and Candida tropicalis) were cultivated batchwise on three different carbon sources: glucose, acetate, and hexadecane. Growth curves, oxygen uptake rates, CO2 evolution rates and the amount of oxygen required for biomass production were determined. The data were compared and discussed from the point of maximum specific growth rate, maximum oxygen uptake rate, carbon conversion into CO2 and biomass, consumption of oxygen and available energy for cell synthesis. The results indicated a relationship between μm $$Q_{O_2 }$$ m, Ys, YO, and η for different carbon sources. YO and η were in the same order of magnitude for acetate (0.58 and 0.38 respectively) and hexadecane (0.45 and 0.40 respectively). These values were remarkably lower than those for glucose (1.26 and 0.54 respectively).
    Type of Medium: Electronic Resource
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  • 2
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 6 (1979), S. 335-339 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary This paper reports on experiments in which a fluorometer, which permits culture fluorescence to be measured in situ was coupled to a bioreactor. The fluorometer through external light excitement NADH can be made to fluoresce, thus allowing intracellular NADH profiles to be measured in response to extracellular step-changes in substrate concentration. Experiments with baker's yeast and Candida tropicalis as organisms and glucose and hexadecane as substrates are reported. The results suggest different uptake mechanisms depending on cell type and on substrate.
    Type of Medium: Electronic Resource
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  • 3
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 15 (1973), S. 861-877 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The kinetics of C. tropicalis growth were investigated with pure n-hexadecane as dispersed phase substrate. Two distinct growth phases were found: In the first phase, exponential growth was independent of stirrer speed. The onset of the second phase, one of linear growth, was determined by stirrer speed. By the use of two different fermenter types, it was shown that the drop size of the dispersed phase was not primarily responsible for the observed kinetics. It was considered that the formation of biological flocs determined the observed growth pattern. This was substantiated by the results of continuous cultures in the different fermenter types, with various substrate concentrations.
    Additional Material: 12 Ill.
    Type of Medium: Electronic Resource
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  • 4
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 43 (1994), S. 446-454 
    ISSN: 0006-3592
    Keywords: bubbles ; Pluronic F68 ; hybridoma cells ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We describe a method by which the degree of bubble saturation can be determined by measuring the velocity of single bubbles at different heights from the bubble source in pure water containing increasing concentrations of surfactants. The highest rising velocities were measured in pure water. Addition of surfactants caused a concentration-dependent and height-dependent decrease in bubble velocity; thus, bubbles are covered with surfactants as they rise, and the distance traveled until saturation is reached decreases with increased concentration of surfactant. Pluronic F68 is a potent effector of bubble saturation, 500 times more active than serum. At Pluronic F68 concentrations of 0.1% (w/v), bubbles are saturated essentially at their source. The effect of bubble saturation on the interactions between animal cells and gas bubbles was investigated by using light microscopy and a micromanipulator. In the absence of surfactants, bubbles had a killing effect on cells; hybridoma cells and Chinese hamster ovary (CHO) cells were ruptured when coming into contact with a bubble. Bubbles only partially covered by surfactants adsorbed the cells. The adsorbed cells were not damaged and they also could survive subsequent detachment. Saturated bubbles, on the other hand, did not show any interactions with cells. It is concluded that the protective effect of serum and Pluronic F68 in sparged cultivation systems is based on covering the medium-bubble interface with surfaceactive components and that cell death occurs either after contact of cells with an uncovered bubble or by adsorption of cells through partially saturated bubbles and subsequent transport of cells into the foam region. © 1994 John Wiley & Sons, Inc.
    Additional Material: 9 Ill.
    Type of Medium: Electronic Resource
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  • 5
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 20 (1978), S. 1487-1492 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 4 Ill.
    Type of Medium: Electronic Resource
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  • 6
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 39 (1992), S. 320-326 
    ISSN: 0006-3592
    Keywords: lactate dehydrogenase ; proliferation ; death ; prourokinase ; perfusion ; tumor kidney cells ; microcarriers ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A general methodology is proposed to estimate the actual specific growth and death rate of mammalian cells in continuous perfusion reactors from the monitoring of the release of the cytoplasmic enzyme lactate dehydrogenase (LDH) in the culture medium. The procedure is illustrated on a perfusion culture of human tumor kidney cells growing on microcarriers and producing prourokinase (PUK). The intracellular LDH content of living attached cells is checked to be constant during the culture. However, cells detached from the microcarriers, and counted dead because of the uptake of trypan blue, have only released part of their intracellular LDH. In the culture medium, LDH is relatively stable as the loss of activity does not exceed 5% per day. The time variation of the LDH concentration in the medium is used to calculate the total amount of lysed and actually produced cells in the reactors, hence, the actual specific rates of cell growth and death. It is thus found that the stationary phase observed after 400 h of perfusion culture is the result of equal growth and death rates, with a daily renewal of living cells on the microcarriers near 10%. Moreover, for the cell line tested, the production of PUK is associated with cellular growth.
    Additional Material: 8 Ill.
    Type of Medium: Electronic Resource
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  • 7
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 22 (1980), S. 2411-2416 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 3 Ill.
    Type of Medium: Electronic Resource
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  • 8
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 36 (1990), S. 623-629 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The production of prourokinase (PUK) by a human kidney tumor cell line is studied in long term cultures. Cells are grown on microcarriers which are retained inside the reactor by sedimentation or with a spin filter. Two modes of operation are compared: feed harvest at an average medium exchange rate of 0.3 d-1 and continuous perfusion at a higher dilution rate of 1.5 d-1. In the two systems a stable production of PUK has been maintained for more than 400 h. Kinetics of cellular growth, nutrient consumption, and metabolite and PUK excretion are similar. After an initial rapid growth period, one observes a 10-fold reduction in all the cellular metabolic activities during the stationary phase. Continuous perfusion yields a higher cell density (7 × 106 cells·mL-1) than feed harvest (3 × 106 cells·mL-1), which results in a twofold increase in the reactor productivity. But higher final enzyme activities, about 250 ru·mL-1, are obtained in the feed harvest recovered medium than in the perfusion medium, 100-150 ru·mL-1. The cumulative medium consumption per mass of product is the same in the repeated batch and in the continuous operation mode.
    Additional Material: 7 Ill.
    Type of Medium: Electronic Resource
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  • 9
    Electronic Resource
    Electronic Resource
    Springer
    Cytotechnology 7 (1991), S. 7-13 
    ISSN: 1573-0778
    Keywords: galactose ; glucose ; metabolism ; microcarrier ; reactor ; tumor cell
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Medicine , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract The culture kinetics of human tumor kidney cells (TCL 598) grown on microcarriers are compared with media initially supplemented with either glucose alone or a mixture of galactose and glucose. Growth rates and maximal cell densities are similar, but cellular death is much slower in galactose than in glucose. Galactose is metabolized at a much slower specific rate than glucose. Cells grown in the galactose medium show a different pattern of lactate and pyruvate metabolism compared to cells grown in the glucose medium. Growth with galactose also favours oxidation of glutamine to alanine.
    Type of Medium: Electronic Resource
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  • 10
    Electronic Resource
    Electronic Resource
    Weinheim : Wiley-Blackwell
    Chemie Ingenieur Technik - CIT 48 (1976), S. 1174-1175 
    ISSN: 0009-286X
    Keywords: Chemistry ; Polymer and Materials Science
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Additional Material: 3 Ill.
    Type of Medium: Electronic Resource
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