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  • 11
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 25 (1986), S. 29-31 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary In the butanol/isopropanol batch fermentation adsorption of alcohols can increase the substrate conversion. The fouling of adsorbants by cells and medium components is severe, but this has no measured effect on the adsorption capacity of butanol in at least three successive fermentations. With the addition of some adsorbants it was found that the fermentation was drawn towards the production of butyric and acetic acid.
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  • 12
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary A system for the continuous cultivation of plant cells has been developed, based on a commercially available 3–1 turbine-stirred fermentor. A special device was constructed to provide for homogeneous effluent from the culture at low dilution rates. Two steady states with Catharanthus roseus cells growing under glucose limitation are described with respect to biomass yield on the carbon and energy source glucose, specific oxygen consumption, specific carbon dioxide production and (by)product formation. From a carbon balance for each steady state it is shown that the flow of carbon to the culture (as glucose) practically equalled the flow of carbon from the culture (as biomass, carbon dioxide and (by)product). Biomass yields on glucose were 0.31 g/g and 0.35 g/g at dilution rates of 0.0060 l/h and 0.0081 l/h respectively. The striking difference between the obtained yield coefficients and biomass yield commonly found for batch-cultured plant cells is discussed.
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  • 13
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 37 (1992), S. 396-398 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary In a recycle system in which evaporation is used for ethanol recovery during fermentation, temperature changes of the broth in the loop will occur. These repeated temperature shocks may have an effect on the microbial ethanol production rate. In this study such repeated temperature changes were simulated in a recycle system with ethanol production by baker's yeast. The magnitude of the temperature change, as well as the time of exposure to this change were found to have an effect on the ethanol production rate. A temperature increase from 30°C in the fermentor to 35°C or more in the recycle loop led to a significantly lower ethanol concentration in the broth. This effect became negligible at a short exposure time of 18 s of the yeast to the higher temperature.
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  • 14
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Oxygen concentration profiles in immobilized recombinant cells were measured using a microsensor. Experimental results showed that the final depth of oxygen penetration in the carrageenan gel was always in the range 80–100 μm for the strains and media used, although profiles of oxygen concentration during the early stages of cell growth depended on the strain and nutrient medium used. Variations in the oxygen profiles corresponded to differences in kinetic parameters measured for the same strains and media in free-cell experiments.
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  • 15
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 28 (1988), S. 109-115 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary In large-scale bioreactors inadequate mixing may impose a continually changing environment to a microbial culture. How the culture will response to such conditions can be studied by means of well designed laboratory-scale experiments. In a two-fermentor-system the influence of continually changing glucose concentrations on the fed-batch baker's yeast production was investigated. Experiments were carried out at different circulation rates and different ratios of the fermentor volumes. The imperfect mixing of the system caused a reduction of the biomass yield and an increase in the ethanol formation. Acetic acid and glyerol were produced as well, but no clear relationship between the circulation rate and the amount of metabolites formed could be observed. The difference in performance of the culture in both fermentors was exposed clearly by the respiration quotient and the (maximum) specific oxygen consumption rate.
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  • 16
    ISSN: 1612-1112
    Keywords: Capillary electrophoresis ; Chiral separation ; γ-Cyclodextrin ; Mandelic acid enantiomers
    Source: Springer Online Journal Archives 1860-2000
    Topics: Chemistry and Pharmacology
    Notes: Summary The separation of the optical isomers of mandelic acid by capillary electrophoresis using γ-cyclodextrin as a chiral selector is presented. The mobility of the enantiomers can be regulated by adjustment of the pH, the concentration of the chiral selector and by the molarity and the temperature of the buffer. Different organic modifiers can either increase or decrease resolution. The importance of the nature of the electrolyte is evidenced by the fact that acceptable enantioseparation has only been achieved using phosphate buffer. The factors affecting the mobility are discussed. A simple equation describing the apparent mobility of the analytes in buffers containing cyclodextrins is presented. The equilibrium constant for the inclusion complex formation of mandelic acid with γ-cyclodextrin was found to be 2.8 M−1 for D-mandelic acid and 2.4 M−1 for the L-enantiomer.
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  • 17
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 35 (1990), S. 1078-1087 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An oxygen microsensor was used to measure internal oxygen profiles in biocatalyst particles of different diameter and activity. The particles were made of agarose gel and contained an oxygen reducing enzyme, L-lactate mono-oxygenase. The kinetics of the enzyme could be well described by the Michaelis-Menten equation. From the internal substrate concentration profile the intrinsic kinetic parameters were determined by means of fitting a simulated profile to the measurements, using Marquardt's algorithm. The intrinsic kinetic parameters found following this procedure appeared to be independent of particle radius or enzyme loading used, proving the method to be reliable. These parameters were also compared with the kinetic parameters of the free enzyme which were determined in a biological oxygen monitoring system. The intrinsic kinetic parameters showed a decrease with a factor 2.3 for Vm value and with a factor 2.7 for the Km value compared to the parameters for the free enzyme. From this the conclusion can be drawn that the immobilization as such or the carrier material not only can have an effect on the maximum intrinsic conversion rate (Vm) but also on the affinity of the enzyme (Km) for oxygen.
    Additional Material: 6 Ill.
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  • 18
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Thiosphaera pantotropha is capable of aerobic heterotrophic nitrification and both aerobic and anaerobic denitrification. These phenomena have been studied in acetate-limited aerobic and anaerobic continuous cultures supplied with ammonia and nitrate. The internal reaction rates were defined, based on biochemical knowledge. The observable external conversion rates are related through a linear equation on the basis of the specified internal reaction rates. The linear equation is a Pirt relation extended for microbial systems with multiple electron donors (acetate and ammonia) and electron acceptors (oxygen and nitrate). The coefficients in this equation were estimated from the continuous culture measurements, and are composed of parameters involved in ATP production and consumption by the microorganism. It is shown that with realistic values for these parameters, the metabolically structured model describes the aerobic as well as the anaerobic experiments.
    Additional Material: 2 Ill.
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  • 19
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An oxygen microsensor in combination with mathematical modeling was used to determine the behavior of immobilized Thiosphaera pantotropha. This organism can convert ammonia completely to nitrogen gas under aerobic conditions (coupled nitrification/denitrification) and denitrifies nitrate at highest rates under anaerobic conditions. Immobilization of T. pantotropha can result in aerobic and anaerobic zones inside the biocatalyst particle which will be advantageous for the conversion of ammonia and nitrate from wastewater. However, information of the effects of immobilization on the physiology of T. pantotropha is necessary for the development of such a system. This article gives the extension of a model developed to describe the behavior of chemostat cultures of T. pantotropha so that it can be used for immobilized cells. The original model was based on metabolic reaction equations. Kinetic and diffusion equations have now been added. Experimental verification was carried out using a stirred tank reactor and a Kluyver flask. After immobilization in agarose, the cells were grown in the particles under continuous culture conditions for 3 days. After 24 h the oxygen penetration depth showed a constant value of 100 μ, indicating that a steady state was reached. Scanning electron micrographs showed that large colonies of cells were present in this 100-μm aerobic layer.From the dynamics of the start-up phase, several parameters were determined from measurements of the oxygen concentration profiles made every few hours. The profiles simulated by the model were fitted to the measured data. The average value for the maximum specific growth rate was 0.52 h-1, and the maximum oxygen conversion rate was 1.0 mol Cmol-1 h-1. The maximum specific acetate uptake rate was 2.0 mol Cmol-1 h-1, and the Monod constant for acetate was 2.9 × 10-2 mol m-3. The maximum specific nitrification rate was 0.58 × 10-1 mol Cmol-1 h-1, and the amount of oxygen necessary for nitrification was 11% of the total oxygen uptake rate. Most of the kinetic parameters determined for the immobilized cells were in good agreement with those for the suspended cells. Only the maximum specific growth rate was significantly higher, and the maximum specific nitrification rate was some what lower than for suspended cells. The experimental results clearly show that an oxygen microsensor, in combination with mathematical modeling, can successfully be used to elucidate the kinetic behavior of immobilized, oxygen-consuming, cells.
    Additional Material: 6 Ill.
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  • 20
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 27 (1985), S. 109-116 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An approximate method for solving the nonlinear diffusion problem in the case of a power-function variation of the diffusion coefficient with concentration has been applied to a drying process with simultaneous enzyme inactivation. Experimental results obtained by air drying of soybean lipoxygenase entrapped in a glucose calcium-alginate gel are in good agreement with the predicted behavior, whereas hardly any differences occur between the results obtained with the approximate method and those obtained by a numerical solution of the original model.
    Additional Material: 6 Ill.
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