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  • 1
    Electronic Resource
    Electronic Resource
    Oxford, UK : Blackwell Publishing Ltd
    Annals of the New York Academy of Sciences 501 (1987), S. 0 
    ISSN: 1749-6632
    Source: Blackwell Publishing Journal Backfiles 1879-2005
    Topics: Natural Sciences in General
    Type of Medium: Electronic Resource
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  • 2
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 5 (1978), S. 207-214 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary A dynamic calorimetric technique was investigated to determine the feasibility of monitoring cell growth by thermal measurements. Theoretical analysis of growth ofSaccharomyces cerevisiae on glucose showed that the correlation depends on cellular yield values but not on ethanol formation. Experiments withS. cerevisiae on a molasses-mineral salts medium resulted in a thermal yield of 4.4 kcal/g cells, consistent with our theoretical expectations.
    Type of Medium: Electronic Resource
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  • 3
    Electronic Resource
    Electronic Resource
    Springer
    Bioprocess and biosystems engineering 7 (1992), S. 205-211 
    ISSN: 1432-0797
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract This work describes the recovery of an extracellular alkaline protease from fermentation broths of a Bacillus sp ATCC 21536, at pH=10.0 using ultrafiltration (MWCO 100,000) and microfiltration (0.1 μm) membranes in hollow fiber devices. The influence of membrane pore size and polymeric material and membrane filtration performance was studied. High protein recoveries and high average flux rates were obtained with polysulfone membranes. A decrease of concentration polarization was obtained, simultaneously with enhancement of filtration flux rate and enzyme recovery by using submicron sized charged particles. These polymers lead to flocculation and adsorption of whole cells and soluble factors from the fermentation broth. The best results were obtaiend by combination of cationic (0.1%) and anionic (0.04%) polymers.
    Type of Medium: Electronic Resource
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  • 4
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Measurement of chemical concentrations is a weak link in the monitoring of fermentations. The use of a computer-controlled mass spectrometer (MS) has made possible the measurement of one or more volatile compounds on an essentially continuous basis, both in the liquid (broth) and the gas (headspace) phases. For our purposes, the MS was used, not as a spectrometer for chemical identification, but as a programmable detector for measuring concentrations of different compounds. Specifically, a computer-controlled MS was employed during the fermentation of Saccharomyces italicus, to monitor N2, O2, and CO2 concentration in the gas phase, and N2, O2, CO2, and ethanol in the liquid phase. The performance of the MS was carefully analyzed.
    Type of Medium: Electronic Resource
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  • 5
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 2 (1975), S. 9-17 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary The production of penicillin amidase fromBacillus megaterium ATCC 14945 was examined in a sulfur-limited chemostat. Below 50% of the maximum growth rate, enzyme production was independent of dilution rate; above this point production decreased as growth rate increased. A simple and defined medium forBacillus licheniformis 749/C was developed, and extracellular penicillinase production was studied in a chemostat under sulfur- and nitrogenlimited conditions. While the yield of this enzyme differed little between these growth-limiting conditions, the specific activity of the penicillinase per unit weight of extracellular protein was increased 50% under nitrogenlimited conditions. Furthermore, the proportion of extracellular enzyme was greater in continuous, than in batch culture.
    Type of Medium: Electronic Resource
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  • 6
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 15 (1982), S. 252-257 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract The effect of various carbon, nitrogen and sulfur sources on the production of heparinase by Flavobacterium heparinum in defined medium in the presence and absence of heparin as the inducer has been studied. Carbon catabolite repression has been observed in defined medium containing one of several carbon sources including simple sugars, alcohols and organic acids. Fed batch fermentations result in 10 g/l of cells and heparinase titers as high as 100,000 U/l by avoiding carbon catabolite repression. Growth on heparin as a sole carbon source resulted in both a high growth rate of 0.12 h−1 and a high specific activity of 18 U/mg. Specific heparinase activity was markedly reduced when the end products of heparin catabolism were used as carbon, nitrogen or sulfur sources in defined medium. In defined medium with a low sulfate concentration, of less than 10−3 M, specific activities as high as 8 U/mg have been observed even in the absence of the normally required inducer, heparin.
    Type of Medium: Electronic Resource
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  • 7
    Electronic Resource
    Electronic Resource
    Springer
    Bioprocess engineering 23 (2000), S. 159-166 
    ISSN: 0178-515X
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract In this work different aspects of the glucose-fructose enzymatic isomerization, using immobilized glucose isomerase, are studied and quantified. Reaction temperatures range from 40 °C to 60 °C. Intra-particle effective diffusivities (D e), determined after uptake experiments, are between 1.20 × 10−6 cm2/s, at 40 °C, and 2.52 × 10−6 cm2/s, at 60 °C. The estimated energy of activation for diffusion (E aD) is 7.71 kcal/mol. No significant adsorption of the sugars on the support gel matrix is observed. Crushed particles (φ = 150–350 μ) are used during kinetic experiments. For this range of particle diameters, inherent kinetics is approached. A reversible Michaelis–Menten rate equation is fitted to the data, providing the following parameters at pH = 7.0: k 0 = 2.15 × 10−6 g/IU/s; E a/R = 8998 K. Glucose (K G) and fructose (K F) affinity constants are essentially the same, ranging from 0.190 M, at 40 °C to 0.305 M, at 60 °C. The thermodynamic equilibrium constant is determined for the three temperatures, and the heat of reaction, estimated from a Van't Hoff plot, is ΔH = 1682 cal/mol. Independent experiments, where the reaction occurs in the presence of significant intra-particle mass transfer resistance, are used as validation tests.
    Type of Medium: Electronic Resource
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  • 8
    Electronic Resource
    Electronic Resource
    Springer
    Annals of biomedical engineering 21 (1993), S. 67-76 
    ISSN: 1573-9686
    Keywords: Immobilized enzyme reactor ; Heparinase kinetics ; Blood deheparmization ; Bioreactor modeling
    Source: Springer Online Journal Archives 1860-2000
    Topics: Medicine , Technology
    Notes: Abstract Immobilized enzyme reactors can form the basis of useful blood detoxification systems. One such reactor was developed for heparin neutralization by immobilized heparinase. In this article, reactor kinetics were studied under clinically relevant conditions. Heparin neutralization was assessedin vitro in whole human blood using (a) a well-mixed batch reactor, and (b) an oscillating, continuous-flow reactor. The kinetics of heparin neutralization in human blood were first order over the entire range of heparin and enzyme concentrations and particle fractions tested. The kinetic rate was not sensitive to physiological variations in the concentration of antithrombin, a heparin binding protein in blood. Enzyme activity did not decrease significantly over the 2 hour test period. Kinetic control of the system with minimal intraparticle diffusional limitations was suggested by the Thiele moduli (0.11–0.67) and effectiveness factors (0.98±0.01). The ratio kcat/Km obtained in batch studies was 0.0028±0.0008 cm3/μg-min. A continuous-flow oscillating reactor within a closed recirculation loop performed as a single well mixed batch reactor; there was a short mixing time of recirculating blood when compared to reaction time. A model based on this mixing pattern and the kinetics obtained in independent batch studies accurately predicted heparin neutralization profiles observed in the continuous-flow system.
    Type of Medium: Electronic Resource
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  • 9
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A novel means of extracting carboxylic acids from aqueous solutions is described which involves the use of a lipolytic enzyme to convert the acid to a more hydrophobic ester. A water-immiscible long-chain alcohol serves both as a reactant in esterifying the acid, and as a solvent for extraction of the ester. Radiochemical tracer studies of the underlying reaction and extraction equilibria established that a low equilibrium concentration of ester (0.04-0.5mM) in the presence of water is counterbalanced by the high distribution coefficient of the ester (220-3380, wt. basis). The net result is a substantial (4- to 15-fold) increase in the apparent distribution coefficient of the acid; 80%-95% of the extracted acid is in the esterified form. The method is applicable to a variety of alcohols and acids.
    Additional Material: 3 Ill.
    Type of Medium: Electronic Resource
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  • 10
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A procedure for measuring the rate of heat production from a fermentation has been developed. The method is based on measuring the rate of temperature rise of the fermentation broth resulting from metabolism, when the temperature controller is turned off. The heat accumulation measured in this manner is then corrected for heat losses and gains. A sensitive thermistor is used to follow the temperature rise with time. This procedure is shown to be as accurate as previous methods but much simpler in execution. Using this technique, the rate of heat production during metabolism was found to correlate with the rate of oxygen consumption. Experiments were performed using bacteria (E. coli and B. subtilis), a yeast (C. intermedia), and a mold (A. niger). The substrates investigated included glucose, molasses, and soy bean meal. The proportionality constant for the correlation is independent of the growth rate, slightly dependent on the substrate, and possibly dependent On the type of organism growth. This correlation has considerable potential for predicting heat evolution from the metabolism of microorganisms on simple or complex substrates and providing quantitative parameters necessary for heat removal calculations.
    Additional Material: 5 Ill.
    Type of Medium: Electronic Resource
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