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  • 1
    ISSN: 1520-6033
    Source: ACS Legacy Archives
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Type of Medium: Electronic Resource
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  • 2
    ISSN: 1573-6776
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Three alpha-amylase producing strains of Aspergillus oryzae used for recombinant protein production have been studied with respect to growth and protein production. By comparing the three strains with respect to morphology and protein production it is shown that a morphological mutant with a more dense mycelium is more efficient in producing α-amylase.
    Type of Medium: Electronic Resource
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  • 3
    Electronic Resource
    Electronic Resource
    Springer
    Biotechnology techniques 9 (1995), S. 763-766 
    ISSN: 1573-6784
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary A Sequential Injection Analysis (SIA) system for monitoring α-amylase activity is described. The SIA analyser is a further development of previously investigated Flow Injection Analysis (FIA) analyser. The analysis of α-amylase activity is based on monitoring the decoloration of an iodine-starch complex. Performances of the SIA analyser have been compared with the FIA analyser. A good agreement has been obtained between the SIA measurements and the FIA measurements.
    Type of Medium: Electronic Resource
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  • 4
    Electronic Resource
    Electronic Resource
    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 15 (1969), S. 28-34 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Simple graphical methods are given for predicting the effectiveness factors of single reactions in particles of various shapes. A collocation procedure is used for small particles, and the known asymptotic solution is used for large particles. Multiple steady states and variable fluid properties can be handled directly. Examples are given for several nonlinear reaction rate laws.
    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 42 (1993), S. 440-448 
    ISSN: 0006-3592
    Keywords: anomeric specificity ; adaptation ; sugar transport ; mannose-phosphotransferase system ; Lactococcus cremoris ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Glucose uptake in Lactococcus lactis subsp. cremoris FD1 occurs via the mannose phosphotransferase system (Man-PTS), which is quite unspecific and allows transport of many different sugars and sugar analogues. It was previously shown (Benthin, S., Nielsen, J., Villadsen, J. Biotechnol. Bioeng. 40:137-146, 1992) that the kinetics of in vivo glucose uptake in a glucose-limited chemostat culture is best described by assuming that the glucose transport system has two anomer-specific sites with a relative uptake rate of 36% through the α-site. In the present study, the existence of anomer-specific sites on Man-PTS is shown by experiments where α-glucose, β-glucose, mannose, and 2-deoxyglucose are added to glucose-limited chemostat cultures. A quantitative description of the competitive uptake of the involved sugars at the two sites is given. In a mannose-limited chemostat culture, the relative glucose flux via the α-site is 50%, corresponding to a change toward the equilibrium composition of mannose (68%). Furthermore, when the feed to a mannose-limited chemostat culture is changed to glucose, the rate of change of relative glucose flux through the α-site corresponds to constitutive synthesis of Man-PTS with 36% α-site stoichiometry in new cells. When N-acetylglucosamine (73% α-anomer at equilibrium) is the limiting substrate, the relative glucose flux through the α-site is also 48% to 50%. With a feed of α-glucose generated enzymatically from nonmetabolizable sucrose the relative glucose flux through the α-site can be as high as 78%. Finally, growth in the presence of nonmetabolizable α-methylglucoside leads to formation of cells with a relative glucose flux through the α-site of 29% to 30%. The adaptation of the flux distribution between the α- and β-site is tentatively explained by the hypothesis that two integral membrane proteins of Man-PTS are involved in this process. © 1993 John Wiley & Sons, Inc.
    Additional Material: 7 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 44 (1994), S. 165-169 
    ISSN: 0006-3592
    Keywords: penicillin ; fermentation ; media ; degradation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In Industrial production of penicillin there is a noticeable loss of the product through degradation reactions. It is shown that the degradation of penicillin-V, both in a complex and in a chemically defined medium, can be separated into a phosphate-catalyzed conversion of penicillin-V to penicilloic-V acid, overlaid by at least one other reaction in which penicillin V is degraded to as yet unknown products. Parameter values for the phosphatecatalyzed degradation are found to be independent of the type of fermentation medium. The rate of formation of other degradation products of penicillin-V is found to be significantly higher in a complex fermentation medium with corn-steep liquor in a chemically defined medium. © 1994 John Wiley & Sons, Inc.
    Additional Material: 5 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 46 (1995), S. 117-131 
    ISSN: 0006-3592
    Keywords: biochemical model ; Penicillium chrysogenum ; flux analysis ; penicillin ; metabolic engineering ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Based on a review of the Penicillium chrysogenum biochemistry a stoichiometric model has been set up. The model considers 61 internal fluxes and there are 49 intracellular metabolites which are assumed to be in pseudo-steady state. In addition to the intracellular fluxes the model considers the uptake of 21 amino acids. From the stoichiometric model the maximum theoretical yield of penicillin V is calculated to 0.43 mol/mol glucose. If biosynthesis of cysteine is by direct sulfhydrylation rather than by transsulfuration, the maximum theoretical yield is about 20% higher, i.e., 0.50 mol/mol glucose. The theoretical yield decreases substantially if α-aminoadipate is converted to 6-oxo-piperidine-2-carboxylic acid (OPC). If only 40% of the α-aminoadipate is recycled, the maximum theoretical yield is 0.31 mol/mol glucose. The uptake rates of glucose, lactate, γ-aminobutyrate, and 21 amino acids were measured during fed-batch cultivations. The rates of formation of penicillin V, δ-(L-α)-aminoadipyl-L-cysteinyl-D-valine (ACV), OPC, and the pool of isopenicillin N, 6-APA, and 8-HPA were also measured. Finally the synthesis rates of the biomass constituents RNA/DNA, protein, lipid, carbohydrate, and amino carbohydrate were measured. From these measured rates and the stoichiometric model the metabolic fluxes through the different intracellular pathways are calculated. The calculations show that penicillin formation is accompanied by a large flux through the pentose phosphate (PP) pathway due to a large requirement for nicotinamide-adenine dinucleotide phosphate (NADPH) used in the biosynthesis of cysteine. If cysteine is added to the medium, the flux through the PP pathway decreases. From the stoichiometric model YxATP is calculated to 87 mmol adenosine triphosphate (ATP)/g dry weight (DW), and from the flux calculations mATP is found to 3 mmol ATP/g DW/h. © 1995 John Wiley & Sons, Inc.
    Additional Material: 9 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 49 (1996), S. 266-276 
    ISSN: 0006-3592
    Keywords: Aspergillus oryzae ; submerged growth ; morphology ; pellet formation ; protein production ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The microscopic morphology, that is, total hyphal length and total number of tips, has been characterized during batch cultivations of Aspergillus oryzae. The specific growth rate estimated by measuring the total hyphal length (μh) corresponds well with the specific growth rate estimated from dry weight measurements during cultures grown as free hyphal elements. The average tip extension rate can be described with a saturation type kinetics with respect to the average total hyphal length, and the branching frequency is closely related to the total hyphal length. For the applied strain of A. oryzae, pellet formation occurs by coagulation of spores. The agglomeration process is pH dependent and pellets are formed at pH values higher than 5, whereas low pH (〈3.5) results in growth as freely dispersed hyphal elements. The maximum specific growth rate has a broad pH optimum between 3 and 7, whereas the α-amylase production has a sharper maximum at about pH 6. During batch cultivation with pellets the growth is described well by the cube-root law when pellet fragmentation can be neglected. The kinetic parameter k in the cube-root law is derived from the growth kinetics with no mass transfer limitation, k = μh/3. Based on an oxygen balance, the active growth layer in the pellet is estimated to be 200 to 325 μm and, consequently, up to 50% of the biomass is limited by oxygen for large pellets. Ethanol production (up to 1 g L-1) was observed during batch cultivations with pellets, suggesting that ethanol is produced in the oxygen limited part of the biomass. A constitutive, low α-amylase production was observed at high glucose concentration. The specific α-amylase production was significantly higher for filamentous growth than for pellets and oxygen appears to be necessary for production of α-amylase. © 1996 John Wiley & Sons, Inc.
    Additional Material: 12 Ill.
    Type of Medium: Electronic Resource
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  • 9
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 55 (1997), S. 831-840 
    ISSN: 0006-3592
    Keywords: isotopomer mapping matrix ; isotopomer modeling ; metabolic flux analysis ; 13C NMR ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Within the last decades NMR spectroscopy has undergone tremendous development and has become a powerful analytical tool for the investigation of intracellular flux distributions in biochemical networks using 13C-labeled substrates. Not only are the experiments much easier to conduct than experiments employing radioactive tracer elements, but NMR spectroscopy also provides additional information on the labeling pattern of the metabolites. Whereas the maximum amount of information obtainable with 14C-labeled substrates is the fractional enrichment in the individual carbon atom positions, NMR spectroscopy can also provide information on the degree of labeling at neighboring carbon atom positions by analyzing multiplet patterns in NMR spectra or using 2-dimensional NMR spectra. It is possible to quantify the mole fractions of molecules that show a specific labeling pattern, i.e., information of the isotopomer distribution in metabolite pools can be obtained. The isotopomer distribution is the maximum amount of information that in theory can be obtained from 13C-tracer studies. The wealth of information contained in NMR spectra frequently leads to overdetermined algebraic systems. Consequently, fluxes must be estimated by nonlinear least squares analysis, in which experimental labeling data is compared with simulated steady state isotopomer distributions. Hence, mathematical models are required to compute the steady state isotopomer distribution as a function of a given set of steady state fluxes. Because 2n possible labeling patterns exist in a molecule of n carbon atoms, and each pattern corresponds to a separate state in the isotopomer model, these models are inherently complex. Model complexity, so far, has restricted usage of isotopomer information to relatively small metabolic networks. A general methodology for the formulation of isotopomer models is described. The model complexity of isotopomer models is reduced to that of classical metabolic models by expressing the 2n isotopomer mass balances of a metabolite pool in a single matrix equation. Using this approach an isotopomer model has been implemented that describes label distribution in primary carbon metabolism, i.e., in a metabolic network including the Embden-Meyerhof-Parnas and pentose phosphate pathway, the tricarboxylic acid cycle, and selected anaplerotic reaction sequences. The model calculates the steady state label distribution in all metabolite pools as a function of the steady state fluxes and is applied to demonstrate the effect of selected anaplerotic fluxes on the labeling pattern of the pathway intermediates. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55:831-840, 1997.
    Additional Material: 9 Ill.
    Type of Medium: Electronic Resource
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  • 10
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 40 (1992), S. 137-146 
    ISSN: 0006-3592
    Keywords: anomeric specificity ; mechanism of glucose uptake ; Lactococcus cremoris ; Escherichia coli ; Saccharomyces cerevisiae ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The mechanism and kinetics of the glucose uptake systems of three representative microorganisms are studied during cultivation in a chemostat. The three microorganisms are Lactococcus cremoris, Escherichia coli, and Saccharomyces cervisiae. Two models describing respectively competitive and independent uptake of the two glucose anomers are tested on experimental data where α- and β-glucose are determined by flow injection analysis after pulse addition of the pure anomers to a chemostat. The very accurate experimental results are used to give a convincingly clear model discrimination for all three microorganisms. The uptake of glucose by S. cervisiae occurs by a competitive mechanism with preference for α-glucose (Kα = 32 mg/L and Kβ = 48 mg/L). Surprisingly, the glucose uptake by the two bacteria is shown to be mediated by anomer specific transport systems with no competitive inhibition from the other glucose anomer. This novel finding has not been described in the literature on the phosphotransferase system. In L. cremoris the relative uptake rates of the glucose anomers match the equilibrium composition exactly (36% α-glucose). In E. coli the relative uptake rate of α-glucose at glucose unlimited growth is 26%, which means preference for β-glucose. However, the saturation constants of the two sites in E. coli are Kα = 2 mg/L and Kα = 15 mg/L, and a preference for α-glucose is exhibited at very low glucose concentrations. The results are of considerable improtance in relation to enzyme based on-line measurements during fermentations as well as to the modeling of glucose limited growth and product formation.
    Additional Material: 9 Ill.
    Type of Medium: Electronic Resource
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