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  • Biochemistry and Biotechnology  (1,111)
  • 1990-1994  (654)
  • 1985-1989  (457)
  • 1970-1974
  • 1950-1954
  • 1992  (654)
  • 1985  (457)
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  • 1990-1994  (654)
  • 1985-1989  (457)
  • 1970-1974
  • 1950-1954
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  • 1
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 39 (1992), S. 125-131 
    ISSN: 0006-3592
    Keywords: enzymatic reaction ; liquid membrane ; transport mechanism ; emulsion stability ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An enzymatic reaction using a liquid emulsion membrane technique was studied to investigate the effects of some experimental variables on the stability of liquid membrane, enzyme deactivation, and transport of substrates and products. The hydrolysis of L-phenylalanine methyl ester by α-chymotrypsin was selected as a model reaction system. First, a transport mechanism for the substrates and products across the membrane was qualitatively identified. Second, it was found that the pH of the internal phase was one of the most important variables to determine the enzyme activity in a liquid membrane. Third, the effect of membrane phase which consists of surfactant, carrier, and organic solvent on the emulsion stability was investigated. It was found that the properties of the organic solvents greatly affect the emulsion stability. For an optimum condition, it was possible to reuse the emulsion which consists of membrane phase and internal phase without further separation. It was finally concluded that the enzyme in a liquid membrane retained 60% of its native activity in spite of vigorous mixing during the emulsification step.
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  • 2
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 39 (1992), S. 157-163 
    ISSN: 0006-3592
    Keywords: NAD electrochemical regeneration ; flowthrough electrode ; equilibrium displacement ; yeast alcohol dehydrogenase ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Electrochemical regeneration of NAD was performed in a bench scale reactor in which yeast alcohol dehydrogenase catalyzed the oxidation of ethanol. By recycling one of the products of the reaction, it was possible to displace the equilibrium and favor the production of acetaldehyde. The flow-through electrode was made of graphite felt and had a specific area of 275 cm-1. A mathematical model taking into account the enzymatic and electrochemical reaction rates as well as the mass transfer to the electrode was used to analyze the results. The limiting steps in the reactor are the electrochemical reaction for low potentials and the cofactor mass transfer for high potentials.
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  • 3
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 39 (1992), S. 176-185 
    ISSN: 0006-3592
    Keywords: molecular imprinting ; proteins ; molecular memory ; bioseparations ; organic solvents ; affinity ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: When the model protein bovine serum albumin (BSA) was dissolved in a concentrated aqueous solution of the multifunctional ligand L-malic acid, the solution was lyophilized, and the solid residue thoroughly washed with tetrahydrofuran to extract malic acid, then the resultant (“imprinted”) protein was capable of binding 26.4 ±0.9 mol equivalents of the ligand in anhydrous ethyl acetate. The nonimprinted BSA (i.e., that prepared in the same manner apart from the absence of malic acid) bound less then one-tenth of that amount under identical conditions. Furthermore, both imprinted and nonimprinted BSA exhibited little binding of L-malic acid in water. The imprinted BSA retained its “memory” for the ligand in ethyl acetate even after a prolonged incubation under vacuum; dissolution in water, however, eliminated the imprinted protein's binding capacity. The BSA imprinted with L-malic acid displayed affinity for this ligand not only in ethyl acetate but also in many other anhydrous solvents. It was found that the higher the solvent's propensity to form hydrogen bonds, the lower the protein-ligand binding in it, thus pointing to hydrogen bonds as the driving force of this binding. Studies with completely or partially cleaved BSA, with other globular proteins, glutathione, and poly(L-aspartic acid) revealed that the critical requirement for the imprintability is the presence of a sufficiently long polymeric chain. Moreover, many hydrogen-bond-forming macromolecules other than proteins, such as dextrans and their derivatives, partially hydrolyzed starch, and poly(methacrylic acid), also could be imprinted for subsequent binding in ethyl acetate. The mechanism of imprinting and binding inferred from these experiments involves a multipoint hydrogen bonding in water of each ligand molecule with two or more sites on the polymeric chain, thereby folding a segment of the latter into a cavity around the ligand; following lyophilization and extraction of the ligand, the cavities remain in organic solvents (but not in water) and give rise to ligand binding. This conclusion is supported by the results of binding of numerous malic acid analogs and related ligands to BSA imprinted with L-malic acid. Finally, BSA imprinted with malic acid was used as a selective adsorbent for a chromatographic separation of an equimolar mixture of maleic and acrylic acids in ethyl acetate.
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  • 4
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 39 (1992), S. 218-224 
    ISSN: 0006-3592
    Keywords: cholesterol ; cholesterol oxidase ; organic biocatalysis ; microemulsion ; Fourier transform infrared spectroscopy ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The enzymatic conversion of cholesterol to cholestenone by cholesterol oxidase (Brevibacterium sp.)in reversed micelles in a system composed of AOT/isooctane/water/cholesterol has been examined. The catalytic activity of the enzyme was correlated with the physicochemical properties of water in water-in-oil (w/o) microemulsion systems. In a system consisting of 3 wt % AOT in isooctane, reversed micelles started to form as the [H2O]/[AOT] (e.g., the w0) ratio increased above 4-5. The formation of reversed micelles with a core of neat (bulk) water was verified from determinations of both the partial molar volume of water and the scissors vibration of water [with Fourier transform infrared (FTIR) spectroscopy] in the w/o microemulsion systems. A plot of enzyme activity vs. w0 indicated that the hydration of enzyme molecules per se was not sufficient to give rise to catalytic activity. Instead, it appeared that the formation of an aqueous micellar core was necessary for full activation of the enzyme. Based on micelle size distribution analysis, it was estimated that about one micelle per one thousand contained an enzyme molecule. Since the apparent reaction rate could be markedly enhanced by increasing the enzyme/water ratio, we conclude that the number of enzyme-containing micelles was an important rate-limiting factor in the system.
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  • 5
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 39 (1992), S. 233-242 
    ISSN: 0006-3592
    Keywords: Interleukin-2 ; protein-free medium ; porous glass fluidized bed bioreactor ; double-membrane stirrer bioreactor ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The production of recombinant human interleukin-2 in a fluidized bed bioreactor containing porous glass carriers is described. Cultivations were carried out with different medium formulations over 80 days. Maximal cell densities and product yield could be maintained even when protein free medium was perfused, with less than 10% cell washout. Due to this effective immobilization of the cells in the reactor, continuous operation was easy to perform. Final cell densities on the order of 3.8 × 108 mL-1 intrasphere volume were reached while the interleukin-2 production rate was 0.75 mg L-1 d-1. The production rate showed a maximum of a 1.9 fold decrease compared with a homogeneous stirred bubble-free aerated system. This result was in contrast to that achieved with hybridoma cell lines, where better performance was obtained with the fluidized bed bioreactor. The situation may reflect the problems caused by the dense cell culture with adherent cells, as previously shown in a hollow-fiber bioreactor with the same cell line.
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  • 6
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 39 (1992), S. 246-249 
    ISSN: 0006-3592
    Keywords: baker's yeast ; L/A controllers ; fed-batch fermentation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: L/A controllers have extended their use from continuous to fed-batch fermentation where the control is applied from the start of an initial batch phase. As opposed to proportional integral derivative (PID) controllers where even a startup procedure is recommended prior to fed-batch, the L/A controller is not upset by an early connection. It is easily retuned continuously by means of ethanol measurements and can cope with a large range of output conditions. The performance of an L/A algorithm, which uses biomass concentration as the controlled variable, is assessed through simulation. The self-contained algorithm is relatively simple with no greater intrinsic complexity than modern PID stand alone controllers.
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  • 7
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    Biotechnology and Bioengineering 40 (1992), S. 329-333 
    ISSN: 0006-3592
    Keywords: lipase ; supercritical carbon dioxide ; kinetics ; esterification ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Myristic acid esterification has been performed by an immobilized lipase from Mucor Miehei both in n-hexane and in supercritical carbon dioxide (SCCO2). The enzyme is stable in SCCO2 at 15 MPa and 323 K. The reaction rate is influenced by the concentration of water and by the reaction medium composition. A reaction mechanism is proposed, and kinetic parameters are determined at 12.5 MPa and 313 K. Maxium velocity appears 1.5-fold higher in SCCO2 than in n-hexane; however, as solubility of myristic acid is greater in n-hexane, it is not yet definitively clear that the supercritical medium is more favorable than the classical organic solvent for this type of enzyme reaction.
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  • 8
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 40 (1992), S. 465-474 
    ISSN: 0006-3592
    Keywords: propionic acid fermentation ; Propionibacterium acidipropionici ; immobilized ; bioreactor ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Continuous propionic acid fermentations of lactate by Propionibacterium acidipropionici were studied in spiral wound fibrous bed bioreactors. Cells were imobilized by natural attachment to fiber surfaces and entrapment in the void volume within the fibrous matrix. A high cell density of ∼37 g/L was attained in the reactor and the reactor productivity was ∼4 times higher than that from a conventional batch fermentation. The bioreactor was able to operate continuously for 4 months without encountering any clogging, degeneration, or contamination problems. Also, the reactor could accept low-nutrient and low-pH feed without sacrificing much in reactor productivity. This new type of immobilized cell bioreactor is scalable and thus is suitable for industrial production of propionate. © 1992 John Wiley & Sons, Inc.
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  • 9
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    Biotechnology and Bioengineering 40 (1992), S. 498-504 
    ISSN: 0006-3592
    Keywords: separation ; Zeolite Y ; effects of cation ; glucose and fructose ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Na-, K-, Ba-, and Ca-Y were employed for the separation of fructose and glucose in an adsorption column. Effects of temperature, solvent flow rate, amount of mixture injection, and exchangeable cations on the separation were investigated. Efficiency of separation was used as a criterion to characterize the effectiveness of the separation. The transport and kinetic parameters for the column separation were also presented. From simple pulse experiments and moment analysis, the obtained process information of equilibrium and dynamic parameters might be used to design, operate, and control the separation column. © 1992 John Wiley & Sons, Inc.
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  • 10
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    Biotechnology and Bioengineering 40 (1992), S. 525-529 
    ISSN: 0006-3592
    Keywords: triosephosphate isomerase ; imobilized ; thermal stability ; kinetic approach ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The process of thermal inactivation of triosephosphate isomerase covalently attached to a silica-based support activated with p-benzoquinone was found to be a complex one. At 50°C, a characteristic activation preceding the thermal inactivation was observed. Following the intramolecular changes caused by heat, the values of KM and Vmax were determined during the activation. It was presumed that the complex thermal inactivation kinetics reflects the microheterogeneity of the immobilized enzyme molecules. The phosphate ion proved to be a better stabilizer than the substrate. © 1992 John Wiley & Sons, Inc.
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  • 11
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 40 (1992) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 12
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 40 (1992), S. 359-368 
    ISSN: 0006-3592
    Keywords: cell cycle ; hybridoma ; death ; cell arrest ; growth ; monoclonal antibody ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: As a result of recent advances in flow cytometry, renewed interest is shown in modeling the kinetic behavior of cells in culture on the basis of cell cycle parameters. An important but often overlooked kinetic variable in hybridoma cultures is the cell death rate. Not only the overall cell growth but also the kinetics of nutrient metabolism and monoclonal antibody production have been shown to depend on the cell death rate in continuous suspension hybridoma cultures. The present study shows that the death rate in hybridoma cultures is proportional to the fraction of cells arrested in the G1 phase of the cell cycle. The steady-state cell age distributions in the various phases of the division cycle have been calculated analytically. A simple mathematical model has been used to produce the profiles of the cycling and arrested cell fractions with respect to the dilution rate. The calculated steady-state growth rate, death rate, and viability profiles are shown to be in agreement with recently published experimental data from continuous suspension hybridoma cultures. © 1992 John Wiley & Sons, Inc.
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  • 13
    ISSN: 0006-3592
    Keywords: enzymatic peptide synthesis ; N-terminal protecting groups ; α-chymotrypsin ; experimental design ; partition constant ; reaction rate ; log P ; molecular refractivity ; response surfaces ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The influence of five different N-terminal protecting groups (For, Ac, Boc, Z, and Fmoc) and reaction conditions (temperature and dimethylformamide content) on the α-chymotrypsin-catalyzed synthesis of the dipeptide derivative X-Phe-Leu-NH2 was studied. Groups such as For, Ac, Boc, and Z always rendered good peptide yields (82% to 85%) at low reaction temperatures and DMF concentrations, which depended on the N-α protection choice. Boc and Z were the most reactive N-α groups and, in addition, the most suitable for peptide synthesis. On the other hand, the use of empirical design methodologies allowed, with minimal experimentation and by multiple regression, to deduce an equation, which correlates the logarithm of the first order kinetic constant (log k') with reaction temperature, DMF concentration, and hydrophobicity (log P values) of the different protecting groups. The predictive value of the equation was tested by comparing the performance of another protective group, such as Aloc, with the performance predicted by said equation. Experimental and calculated k' values were found to be in good agreement.
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  • 14
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    Biotechnology and Bioengineering 39 (1992), S. 575-578 
    ISSN: 0006-3592
    Keywords: protein separations ; formamide ; ethylene glycol ; downstream protein processing ; chromatography ; ion-exchange resins ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Pure formamide and ethylene glycol are used instead of water as processing media for protein chromatography. A number of common proteins are freely soluble in these solvents and most do not undergo irrersible inactivation in them. Batch adsorption studies reveal that proteins readily adsorbed to various ion-exchangers in formamide and ethyline glycol and subsequently can be completely desorbed by adding inorganic salts (LiCl and NH4NO3) to the solvents. The idea of protein separations in formamide and ethylene glycol is illustrated by column chromatography and preparative separation of mixtures of (i) oxidized A and B chains of insulin and (ii) lysozyme and ribonuclease on the anion-exchanger triethylaminoethycellulose and the cation-exchanger phosphocellulose, respectively.
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  • 15
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    Biotechnology and Bioengineering 39 (1992), S. 556-564 
    ISSN: 0006-3592
    Keywords: hybridoma ; effects of lactate concentration ; inhibition by osmotic pressure ; fed-batch culture ; antibody production rate ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: To investigate the effects of lactate on cell growth and antibody production, a new method of maintaining the lactate concentration constant in a fed-batch culture is described. When the pH was initially adjusted by sodium hydroxide, the specific growth rate decreased and specific death rate increased with an increase of lactate concentration. To investigate whether the inhibition was due to the lactate concentration itself or to the osmotic pressure, the effect of the osmotic pressure adjusted by sodium chloride was compared with that of sodium lactate. When the osmotic pressure was adjusted to same condition as that of sodium lactate using sodium chloride, the specific growth data showed the same degree of growth inhibition. It was thus evident that the inhibition to cell growth was mainly due to osmotic pressure while lactate production from glucose was found to be inhibited by the lactate itself compared with sodium chloride. The specific antibody production rate had a maximum value within a certain range of lactate concentration. Moreover, specific antibody production rate had a unified relationship with the kinetic parameter μ, in spite of the different causes of inhibition by lithium lactate and sodium lactate. A certain “trade-off” relationship between growth and antibody production existed at higher growth rates.
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  • 16
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    Biotechnology and Bioengineering 39 (1992), S. 565-574 
    ISSN: 0006-3592
    Keywords: Corynebacterium glutamicum ; continuous L-lysine fermentation ; flux analysis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Continuous culture experiments with the L-producer, Corynebacterium glutamicum, were carried out to characterize the effect of specific growth rate on fermentation yields, specific rates, productivities, and fluxes through the primary metabolism. The specific productivity of L-lysine exhibited a maximum with respect to specific growth rate, with an initial growth-associated behavior up to specific growth rates of about 0.1 h-1, and a constant specific productivity for specific growth rates in the range of about 0.1 to 0.2 h-1. The productivity dropped at specific growth rates larger than about 0.2 h-1. The yield of L-lysine on glucose increased approximately linearly with decreasing specific growth rate over the entire range studied, as did the respiratory quotient. A direct relationship was established between the culture respiratory quotient and the L-lysine yield. By explicitly accounting for glucose used for biomass synthesis, it was shown that the strain synthesizes L-lysine with an intrinsic yield, or efficiency, of about 0.41 mol L-lysine/mol glucose, compared with the theoretical yield of 0.75 mol/mol. Metabolic flux modeling based on the continuous culture data suggests that the production of ATP is not likely to be a limiting factor in L-lysine production, and that a high TCA cycle activity, coupled with a tightly controlled split of metabolite flow at the PEP node, is likely the cause of the large discrepancy between theoretical and actual yields in L-lysine fermentations.
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  • 17
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    Biotechnology and Bioengineering 39 (1992), S. 579-587 
    ISSN: 0006-3592
    Keywords: ion-exchange chromatography ; superoxide dismutase ; preparative chromatography ; DEAE-sepharose fast flow ; fronting ; type I elution curve ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Displacement effects in large-scale (total column volume vt = 150 L) and preparative ion-exchange chromatography purifying human erythrocyte superoxide dismutase are described in the present article. The biomolecules are eluted in a very small peak elution volume (〈0.2 vo) behind the salt wave using a step gradient. The theoretical peak width and retention behavior are calculated according to the model of Yamamoto. The theoretical values are then compared with the experimental data. There was a difference observed between the elution type I (also called fronting) and the experimentally obtained elution. Some instructions are given on how to achieve these phenomenona because a beneficial effect in respect to resolution and recovery of a biomolecule is observed.
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  • 18
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    Biotechnology and Bioengineering 39 (1992) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 19
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    Biotechnology and Bioengineering 39 (1992), S. 607-613 
    ISSN: 0006-3592
    Keywords: lactic acid ; Lactobacillus delbreuckii ; extractive ; fermentation ; product inhibition ; packed-column and ion-exchange resin ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Lactic acid fermentation is an end-product-inhibited reaction. The restriction imposed by lactic acid on its fermentation can be avoided by extractive fermentation techniques. Studies were performed by attaching an ion-exchange resin packed column with a 2-L fermentor for separation of lactic acid. The fermentation, in a conventional batch mode, resulted in a lactic acid yield of 0.828 g · g-1 and a lactic acid productivity of 0.313 g · L-1 · h-1. However, these could be further enhanced to 0.929 g · g-1 and 1.665 g · L-1 · h-1 by extractive fermentation techniques. The effect of temperature on extractive fermentation was remarkable and has been included in this work.
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  • 20
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    Biotechnology and Bioengineering 39 (1992), S. 589-595 
    ISSN: 0006-3592
    Keywords: free energy of growth ; Escherichia coli K-12 ; free energy of anabolism ; free energy change ; free energy of formation ; free energy of formation of cells ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Determinations of the ΔG0′ accompanying the growth of Escherichia coli K-12 on succinic acid are made using 2 different methods. The ΔG0′ accompanying catabolism could be calculated directly because the thermodynamic properties of the reactants and products are known. The ΔG′accompanying anabolism could not be calculated directly because the ΔGf value for a unit mass of cells was not known. A description is given of a deduction that the ΔG′ accompanying anabolism is zero, or nearly so. This is followed by a description of 2 methods, whereby the free energy of formation of a unit quantity of cellular substance can be calculated. The 2 values obtained by these methods are used to calculate the free-energy change accompanying anabolism, the resultant values being 1.72 and -11.68 kJ, respectively, with an average of -4.98 kJ (-1.19 kcal). This value is sufficiently close to zero that it can be considered to be so, indicating that the ΔG′ accompanying metabolism is that of catabolism alone.
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  • 21
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    Biotechnology and Bioengineering 39 (1992), S. 596-606 
    ISSN: 0006-3592
    Keywords: Hybridoma ; IgG mRNAs ; cell-associated antibody ; cellular metabolic activity ; specific antibody production rate ; semicontinuous culture ; dilution rate ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Hybridoma I.13.17 was grown in semicontinuous culture in an attempt to investigate the steady-state concentrations of key components of monoclonal antibody (MAb) synthesis (e.g., intracellular MAb, IgG messenger RNAs) at different dilution rates between 0.008 and 0.055 h-1. There was a general trend of increasing steady-state levels of total cytoplasmic RNA, total cell-associated MAb or cytoplasmic MAb, DNA synthesis rate, cellular metabolic activity, heavy (H-) and light (L-) chain IgG mRNAs with the increase in dilution rates. Increase in the half-lives of H- and L-chain mRNAs with increase in dilution rates may be sufficient to account for their increasing levels found under the same conditions. The specific growth rate was profoundly affected by the dilution rate, particularly near the lower end of the dilution rate range. Linear relationships were observed between the steady-state amounts of total cell-associated MAb and the relative levels of H- and L-chain mRNAs. Material balances on intracellular MAb demonstrated an increasing percentage of antibody not released into the growth medium (e.g., stored within the cell or anchored to the cell membrane) with increasing dilution rate. The MAb production rate per cell decreased significantly with the increase in dilution rates. No correlation was found between the relative levels of H- or L-chain mRNAs and the specific MAb production rate. Possible implications of rate-limiting steps in MAb synthesis and secretion are discussed.
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  • 22
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    Biotechnology and Bioengineering 39 (1992), S. 614-618 
    ISSN: 0006-3592
    Keywords: baculovirus ; aeration ; insect cell ; medium ; recombinant DNA ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An experimental study was undertaken to quantify the effects of infection cell density, medium condition, and surface aeration on recombinant protein yields in insect cells. In the absence of surface aeration and fresh medium, insect cells generated higher product yields (on a per cell basis) when infected with recombinant baculovirus at low cell densities, LCD (3 × 105-4 × 105 cells/mL), than at high cell densities, HCD (〉0.9 × 106 cells/mL), for two distinct baculovirus types. Surface aeration of a HCD culture infected in spent medium improved β-glactosidase yields 5-fold over the nonaerated case. Surface aeration and medium replenishment improved β-galactosidase yields of a HCD culture by 20-fold (compared to a 1.6-fold improvement for a LCD culture), resulting in cultures with productivties that were independent of the cell density at infection.
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  • 23
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    Biotechnology and Bioengineering 39 (1992), S. 629-634 
    ISSN: 0006-3592
    Keywords: biocatalyst ; cyanide degradation ; immobilized enzyme ; wastewaters ; kinetics ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: CYANIDASE@ is a new enzyme preparation capable of degrading cyanide in industrial wastewaters to ammonia and formate in an apparently one-step reaction, down to very low concentrations. This enzyme has both a high selectivity and affinity toward cyanide. A granular form of the biocatalyst was used in a recirculation fixed bed reactor in order to characterize the new biocatalyst with respect to pH, ionic strength, common ions normally present in wastewaters, mass transfer effects, and temperature. Long term stability was investigated. The kinetics of the enzymatic degradation of cyanide were studied in a batch reactor using the powdered immobilized enzyme preparation and modeled using a simple Michaelis-Menten equation.
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  • 24
    ISSN: 0006-3592
    Keywords: Modeling ; kinetics ; cyanobacteria ; photobioreactors ; Spirulina platensis ; mineral limitations ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A structured model for the culture of cyanobacteria in photobioreactors is developed on the basis of Schuster's approximations for radiative light transfer. This model is therefore limited to monodimensional geometries and kinetic aspects.Light-harvesting pigments play a crucial role in defining the profile of radiative transfer inside the culture medium and in controlling the metabolism, particularly the metabolic deviations induced by mineral limitations. Modeling therefore requires the biomass to be divided into several compartments, among which the light-harvesting compartment allows a working illuminated volume to be defined within the photobioreactor. This volume may change during batch cultures, largely decreasing as pigment concentration increases during growth but increasing as pigments are consumed during mineral limitation. This approach enables, in photobioreactors of simple parallelepipedic, geometries, kinetic parameters to be determined with high accuracy; this may then be extended to vessels of more complex geometries, such as cylindrical photobioreactors.The model is applied to controlled batch cultures of the cyanobacterium Spirulina platensis in parallelepipedic photobioreactors to assess its ability to predict the behavior of these microorganisms in conditions of light and mineral limitations. Results allowed the study of optimal operating condition for continuous cultures to be approached © 1992 John Wiley & Sons, Inc.
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  • 25
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    Biotechnology and Bioengineering 40 (1992), S. 858-860 
    ISSN: 0006-3592
    Keywords: lipase ; cellulase activity ; enzyme bioreactor ; triglyceride hydrolysis ; cellulose membrane ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Polymeric membranes are increasingly used as supports for the immobilization of enzymes in bioreactors. One of the more common reactor types employed in lipase-catalyzed hydrolysis of oils, contains modified cellulose as a membrane material. We found that this type of material is readily attacked by cellulase present in several commercially available lipase preparations. This leads to membrane damage, reactor instability, and leakage. We conclude that cellulose membranes are not suitable as supports in bioreactors for the immobilizartion of these lipases. The development of alternative membranes is currently in progress. © 1992 John Wiley & Sons, Inc.
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  • 26
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: No Abstrect.
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  • 27
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    Biotechnology and Bioengineering 40 (1992), S. 875-888 
    ISSN: 0006-3592
    Keywords: cell concentration ; light scatter ; solid substrate ; fermentation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A novel sensor was developed, based on light scatter, to estimate the cell concentration in the presence of suspended solids. The light scatter properties of cells in the presence of suspended solids were investigated. Two crucial observations were made: first, that the light scatter from cells is essentially a linear function of cell concentration and, second, that invariant regions are present in the light scatter spectrum of cell/solid substrate mixtures. Invariant regions are wavelength intervals of the light scatter spectrum in which the light scatter reading is independent of solid substrate concentration and only a function of cell concentration. The occurrence of invariant regions is the key behavior which allowed the quantification of cell concentration in the presence of suspended solids.An algorithm was developed for the estimation, from light scatter data, of cell concentration in the presence of solid substrate. The light scatter approach was validated by comparing cell concentrations estimated by this technique to those obtained from DNA and carbon dioxide evolution rate measurements during a series of fermentations. The model system used was Bacillus subtilis var sakainensis ATCC 21394 growing on fishmeal as the sole nitrogen source.A model was developed based on the interactions of scatter and absorbance. This model reflects the hypothesis that invariant regions are caused by changes in the absorbance of the solid substrate as a function of wavelength. © 1992 John Wiley & Sons, Inc.
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  • 28
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    Biotechnology and Bioengineering 39 (1992), S. 663-671 
    ISSN: 0006-3592
    Keywords: Escherichia coli ; acetic acid ; methionine ; yeast extract ; continuous fermentation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Acetic acid formation in Escherichia coli fermentation has been studied in continuous cultures. Experimental results suggest that the limited capacity of the oxidative metabolism (perhaps the limited capacity of TCA cycle) may be responsible for acetic acid formation. At low growth rates, both anabolic and catabolic requirements may be satisfied by the oxidative metabolism. However, at high growth rates these two demands may exceed the capacity of the oxidative metabolism alone. It is proposed that under these circumstances, E. coli reorganizes the oxidative metabolism to first meet the anabolic requisition and then supply the necessary amount of energy using both the remaining capacity of the oxidative metabolism and acetic acid formation metabolism. Escherichia coli selects acetic acid synthesis as the aerobic energy source because it generates the second largest amount of ATP and NADH2. According to our proposition, acetic acid formation could be reduced by decreasing the anabolic requirement, i.e., reducing glucose uptake, or by increasing the capacity of the oxidative metabolism. These two approaches were experimentally confirmed by observing reduced acetic acid formation by reducing the glucose uptake with a yeast extract addition and enhancing the capacity of oxidative metabolism with a methionine addition.
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  • 29
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    Biotechnology and Bioengineering 39 (1992), S. 672-678 
    ISSN: 0006-3592
    Keywords: microencapsulation ; MTT assay ; polyacrylate ; artificial membrane ; metabolic activity ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Chinese hamster ovary (CHO) fibroblast cells were microencapsulated in polyacrylate membranes (HEMA-MMA: 75% HEMA) via an interfacial precipitation process. The CHO cells were observed to grow in large aggregates, attached to each other instead of to the capsule wall. When CHO cells were encapsulated at high density (4 × 106 cells/mL), the initial metabolic activity in microcapsules, as determined by the MTT assay, correlated with the polymer-cell extrusion ratio, presumably because of the dependence of encapsulation efficiency on the relative flow rates. However, there was a large variation in the metabolic activity among individual microcapsules throughout the present study. Capsules with low encapsulation efficiency (at a “seeding” density of 4 × 106 cells/mL) exhibited a rapid increase in the metabolic activity during the following week. When CHO cells were encapsulated at low density (4 × 105 cells/mL), there was only a small increase in the metabolic activity. Only a small fraction (∼5%) of the capsules exhibited a high level of metabolic activity and 40% of the capsules exhibited undetectable metabolic activity even after 2 weeks. We conclude that CHO cells, which served as model cells, survive the encapsulation process and retain an active metabolic state once enclosed by the HEMA-MMA membranes. However, the resultant microcapsules are extremely heterogeneous in the amount of retained metabolic activity.
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  • 30
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    Biotechnology and Bioengineering 39 (1992), S. 679-687 
    ISSN: 0006-3592
    Keywords: immobilized enzyme distribution ; diffusion cell ; active-site titration ; controlled-pore glass ; cell profile ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The total and active immobilized enzyme (IME) distributions in porous supports are studied both theoretically and experimentally. In order to determine experimentally the enzyme distribution profiles within a single particle, we construct a diffusion cell containing controlled-pore glass particles such that the cell would mimic a large pellet support. Our purpose is to study the interplay between the diffusion process within the interparticle void space and immobilization process in the controlled-pore glass particles onto the evolution of the (total and active) enzyme distributions. A mathematical model is developed to describe the interaction of various processes within the diffusion cell. The immobilized enzymes are determined for a system of trypsin and controlled-pore glass particles. The total amount of enzymes are determined by the amino acid analysis, and the active fraction is obtained by an active-site titration. The experimentally measured total IME profiles compare very well with that predicted by the model. The determined active enzyme profile is found to be nonuniform one, and it represents about 40% of the total enzyme immobilized in the support particles.
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  • 31
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    Biotechnology and Bioengineering 39 (1992) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
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  • 32
    ISSN: 0006-3592
    Keywords: methylotroph ; continuous culture ; oxiturbidostat ; growth-limiting substrate pulse ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The growth characteristics of a chemostat culture of the obligate methylotrophic bacterium Methylobacillus flagellatum have been determined. Steady-state cultures growing at a rate of 0.73-0.74 h-1, equal to the maximal growth rate, were obtained under oxyturbidostat cultivation conditions. The response of a chemostat culture to a pulse increase of methanol concentration was studied. It was shown that slow and rapidly growing cultures of M. flagellatum responded differently to pulse methanol addition. The growth characteristics of slow-growing cultures decreased after methanol addition compared to those of stationary chemostat cultures. The growth characteristics of rapidly growing cultures were practically unchanged with and without pulse methanol addition.
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  • 33
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    Biotechnology and Bioengineering 39 (1992), S. 707-716 
    ISSN: 0006-3592
    Keywords: Mixing ; two phase ; bioreactor ; perfluorochemical ; LLR ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The liquid-impelled loop reactor is a new column-type bioreactor. The design of this device is based on the principle of the air-lift loop reactor. In the external-loop configuration used in this work, descending perfluorochemical drops bring about circulation of the continuous aqueous phase. Mixing of this continuous phase is characterized per section of the rector. Axial-dispersion coefficients for the tube with two-phase flow are determined and correlated with the energy dissipation in the tube. Comparisons with similar systems such as bubble columns and air-lift loop reactors are made. Overall mixing parameters are derived and used for calculation of the number of circulatins needed to achieve a certain degree of mixing. The hydrodynamic model from previous work is tested for the reactor configurations of this work. It can be useful to calculate circulation times.
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  • 34
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    Biotechnology and Bioengineering 39 (1992), S. 697-706 
    ISSN: 0006-3592
    Keywords: anchorage-dependent mammalian cells ; immobilization ; fibers ; bioreactor ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Anchorage-dependent HeLa cells were successfully cultured on two fibrous materials (A07 and R100) with porosities of 75-125 and 40 μm, void fractions of 92% and 81%, and fiber diameters of 7.6 and 10.2 μm, respectively, in 100-mL spinner flasks and 2-L stirred tank bioreactors. The matrix was formed into a fixed vertical spiral configuration. All cultures displayed rapid (≤2-3 h) attachment of inoculated cells (≥95%) to the matrix, uniform coverage of the immobilizing area with viable cells, and no significant amount of cell debris in the medium. Spinner flask cultures indicated that the denser material R100 showed better results in terms of final cell density. The growth of HeLa cells on material R100 in both culture systems was similar to that observed in tissue culture dishes (specific growth rate ∼0.03-0.04 h-1, maximum cell density of 8 × 106-9 × 106 cells · mL-1, and yields of 0.4 × 108 cells · mM-1 on glucose and 2 × 108-3 × 108 cells · mM-1 on glutamine). Scale-up of this culture technique in a 2-L bioreactor under perfusion with pH and dissolved oxygen (DO) control yielded cell densities of up to 1.6 × 106 cells · mL-1. Two other anchorage-dependent mammalian cells (ADC) known to be cultured with difficulty in roller bottles or with micro carriers were easily grown on material R100 in spinner flasks. The performance of this culture technique was compared to other ADC culture systems.
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  • 35
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    Biotechnology and Bioengineering 40 (1992), S. 1085-1091 
    ISSN: 0006-3592
    Keywords: xylitol production ; Candida tropicalis ; experimental design ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The effect of culture conditions on xylitol production rate was investigated using Candida tropicalis IFO 0618. From the variance analysis of xylitol production rate, it was found that initial yeast extract concentration was highly significant (99%), while the interaction between D-xylose concentration and aeration rate was significant (95%). These results show the importance of initial yeast extract concentration and of the balance between D-xylose concentration and aeration in the production of xylitol. It was also clearly shown that C. tropicalis needed more yeast extract concentration for efficient xylitol production than for its growth. In order to enhance xylitol production rate, culture conditions were optimized by the Box-Wilson method. In this respect, initial D-xylose concentration, yeast extract concentration, and KLa were chosen as the independent factors in 23-factorial experimental design. As the result of experiments, a maximum xylitol production rate of 2.67 g/L · h was obtained when initial D-xylose concentration and yeast extract concentration were 172.0 and 21.0 g/L, respectively, and KLa was 451.50 h-1 by 90% oxygen gas. © 1992 John Wiley & Sons, Inc.
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  • 36
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    Biotechnology and Bioengineering 40 (1992), S. 1115-1118 
    ISSN: 0006-3592
    Keywords: microencapsulation ; poly(vinylamine) ; cell culture ; mechanical strength ; erythropoietin ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Poly(vinylamine) was synthesized and used to replace poly-L-lysine in forming microcapsule with alginate. Test results indicated that capsules with good mechanical strength and permeability could be obtained under the controlled treatment conditions of poly(vinylamine) and alginate. Application of the current microcapsular system to cell culture was demonstrated by the usage of erythropoietin- (EPO-) producing IW32 mouse erythroleukemia cells. The encapsulated IW32 cells grew to a density of 8 × 107 cells/mL, two times that found in the corresponding poly-L-lysine/alginate capsules. The EPO accumulation inside the microcapsule with the current encapsulation system was also higher. A concentration of 7.3 U/mL was attained as compared to 4.3 U/mL in the poly-L-lysine/alginate microcapsule. © 1992 John Wiley & Sons, Inc.
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  • 37
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    Biotechnology and Bioengineering 40 (1992) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
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  • 38
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    Biotechnology and Bioengineering 39 (1992), S. 732-740 
    ISSN: 0006-3592
    Keywords: cell disruption ; chemical permeabilization ; Escherichia coli ; fermentation ; protein recovery ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Overall protein release greater than 75% in less than 1 h can be attained by exposing exponentially growing Escherichia coli cells to 0.4 M guanidine plus 0.5% Triton X-100 at 37°C in medium. Cell growth stops immediately upon addition of the chemicals, but the cells are not lysed. Guanidine concentrations lower than 0.2 M, in conjunction with 0.5% Triton X-100, do not release significant intracellular protein, nor do they inhibit cell growth. Under these conditions, the cells undergo an adaptation that confers resistance to protein release by further treatment with guanidine and Triton X-100. Cells treated with 0.2 M guanidine plus 0.5% Triton X-100 display intermediate behavior. Protein release is approximately 35%, and growth is temporarily interrupted by an extended lag phase. Subsequent resumption of cell growth results in resistant cells and no additional protein release. This resistance is shown to be reversible and is most likely due to physiological adaptation rather than genetic mutation.
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  • 39
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    Biotechnology and Bioengineering 39 (1992), S. 753-764 
    ISSN: 0006-3592
    Keywords: immunoassay ; mathematical modeling ; analyte monitoring ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The concept of a competitive enzyme immunoassay that utilizes simultaneously the bound and the free analyte-enzyme conjugate (heterobifunctional conjugate) for signal generation in response to varying analyte concentrations in samples has been investigated. Two antigenic sites of the heterobifunctional conjugate are used in the assay for binding to immunoglobulins: the analyte derivative binds to an immobilized antibody, Ab1, and the enzyme component binds to a spatially separated immobilized antibody, Ab2. The analytical system is set up such that in the absence of analyte, the conjugate is predominantly bound in the compartment that contains Ab1. With increasing concentration of native analyte in samples, an increasing concentration of native analyte in samples, an increasing amount of conjugate migrates to the second compartment that contains Ab2. The enzyme bound in each compartment is used for signal generation. Mathematical models have been developed to determine the optimal conditions and to predict the performance of such dual-antibody systems. The theoretical predictions are supported by experimental results. The dual-antibody system has been compared with a conventional competitive enzyme immunoassay using the same reagents.
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  • 40
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    Biotechnology and Bioengineering 39 (1992), S. 741-752 
    ISSN: 0006-3592
    Keywords: enzyme treatment ; parathion hydrolase ; pesticide treatment ; toxic wastes ; waste minimization ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The increasing amounts of pesticides used throughout the world, as well as the increasingly stringent governmental regulations concerning waste disposal, mandates improved techniques of waste disposal and minimization. In this article, parathion hydrolase, an enzyme with proven effectiveness at hydrolyzing organophosphates, was used to treat a cattle dipping liquid containing the pesticide, coumaphos, which is used to kill a disease-causing tick. Waste is generated from this process when a toxic dechlorination product of coumaphos, potasan, accumulates to concentrations hazardous to the cattle. This pesticide system was used as a model to demonstrate how enzyme technology can be applied to waste treatment and minimization. Kinetic experiments showed that the hydrolysis of the two organophosphate substrates can be modeled as first-order reactions with identical rate constants. It was further shown that the enzyme is capable of hydrolyzing only dissolved substrates. Because of the eightfold greater solubility of potasan than coumaphos (16.9 vs. 2.2 μmol/L), it was possible to utilize the enzyme to hydrolyze potasan selectively. Thus, by limiting the amount of enzyme, it is possible to remove potasan selectively to extend the lifetime of the cattle dipping liquid, thereby reducing the amount of waste generated. Based upon experimental results, a mathematical model describing the system was developed and verified. The mathematical model was then used to simulate the ability of the enzyme to hydrolyze the total amount of organophosphates, and to degrade selectively all of the toxic potasan without a significant loss of coumaphos.
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  • 41
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    Biotechnology and Bioengineering 39 (1992), S. 765-774 
    ISSN: 0006-3592
    Keywords: plant cells ; suspension culture ; structured kinetic model ; tobacco cell cultures ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A new structured kinetic model has been formulated and applied to batch suspensions of Nicotiana tabacum. This model has been developed by representing culture interactions with pathways designated for structural component production, secondary metabolite synthesis, and cellular respiration. Additional provisions were made to distinguish growth-competitive secondary metabolite production from non-growth-competitive secondary metabolite production. Parameters for kinetic rate expressions within the model were estimated based upon experimental observations utilized in conjunction with numerical optimization techniques. Using these parameters, culture growth, substrate uptake, cell respiration, and total phenolics production were all successfully correlated to experimenta data from shake flask cultures of N. tabacum.
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  • 42
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    Biotechnology and Bioengineering 39 (1992), S. 775-780 
    ISSN: 0006-3592
    Keywords: formate ; Escherichia coli ; formate hydrogenlyase ; cell immobilization ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Formate hydrogenlyase (FHL) activity was induced in a strain of Escherichia coli S13 during anaerobic growth in yeast extract-tryptone medium containing 100 mM formate. The cells obtained at the optimum growth phase were immobilized in 2.5% (w/v) agar gel when 50-60% of the whole cell FHL activity was retained. The immobilized FHL system had good storage stability and recycling efficiency. In the lysis of formate, an increase of formate concentration to 1.18M increased QH2 (initial) value of the immobilized cell, and subsequently cells, hydrogen evolution, in general, ceased after 6 to 8 of incubation, resulting in incomplete lysis of formate. Presence of small amount of glucose (28 mM) was more or less quantitatively lysed with concomitant disappearence of glucose from the medium. Synthesis of formate from hydrogen and bicarbonate solution by the immobilized cells was also characterized. Presence of glucose (10 mM) in 50 mM bicarbonate solution stimulated formate synthesis by immobilized cells. The pH optimum range, Km, and specific activity of the immobilized cells for the lysis of formate were 6.8-7.2 0.4M, and 66 mL/g cell-h, respectively. The cells could fix hydrogen to the extent of 24.4% (w/w) of its own wet cell mass in a 72-h reaction cycle. Potentiality of the immobilized FHL system for biotechnological exploitation was discussed.
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    Biotechnology and Bioengineering 39 (1992), S. 781-789 
    ISSN: 0006-3592
    Keywords: dopamine ; L-dopa ; multienzyme reactor ; tyrosine phenol lyase ; tyrosine decarboxylase ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The enzymology and kinetics of tyrosine phenol lyase (TPL) from Erwinia herbicola, and tyrosine decarboxylase (TDC) from Streptococcus faecalis have been investigated for potential use in a coimmobilized multienzyme biocatalytic system for the production of dopamine. In this multienzyme biotransformation using whole cells optimized for each of the respective enzymes, TPL catalyzes the production of 3,4-dihydroxyphenyl-L-alanine (L-dopa) from catechol, pyruvate, and ammonium, and this is subsequently decarboxylated by TDC to produce dopamine. Performing the reactions simultaneously, thereby removing L-dopa, is one option for overcoming the TPL equilibrium constraints. The enzymes have different optimal pH values, so the reaction kinetics at a compromise pH of 7.1, where both enzymes could be operated simultaneously, were investigated. For the concentration range investigated, TPL followed pseudo-first-order kinetics with respect to catechol, pyruvate, and ammonium. TDC exhibited significant product inhibition as well as inhibition by combinations of catechol and pyruvate.
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    Biotechnology and Bioengineering 39 (1992), S. 794-797 
    ISSN: 0006-3592
    Keywords: mixing mechanisms ; shaker tables ; toroidal vortex ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Mixing in shaker table beakers is studied using dye dispersion to measure mixing times. Experimental conditions range from the laminar regime into the turbulent mixing. Different flow patterns occurring in the beakers are reported for the mixing. The transition Reynolds number is determined. Rotational speed of the table, volume of material to be mixed, and viscosity of the material are studied as to their effects on mixing time. A graphical mixing time correlation is provided which is useful for the translation of mixing from laboratory scale to pilot scale.
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    Biotechnology and Bioengineering 39 (1992), S. 790-793 
    ISSN: 0006-3592
    Keywords: biofilms ; kinetics ; steady state ; pseudoanalytical solution ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An extremely accurate pseudoanalytical solution for the flux of substrate into a steady-state biofilm is developed. The standard deviations between the substrate fluxes computed from the pseudoanalytical solution and the numerical solution were less than 2.6%. Additional advantages of the pseudoanalytical solution are that it has no inaccuracies around Smin* = 1 and it is composed of single continuous functions applicable to the whole Smin* region.
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    Biotechnology and Bioengineering 40 (1992), S. 1403-1411 
    ISSN: 0006-3592
    Keywords: aromatic solvents ; bioreactor ; benzene ; toluene ; xylene ; biodegradation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A novel bioreactor for the biodegradation of toxic aromatic solvents, such as benzene, toluene, and xylenes in liquid effluent stream, was developed. Silicon tubing was immersed in the completely mixed and aerated bioreactor, and liquid toluene as a model solvent was circulated within the tubing. Toluene diffused out of the tube wall and was transferred at high rate into the culture broth, where biodegradation occurred. The effect of operating parameters on the toluene transfer rate was investigated. During continuous operation, the biodegradation rate was considerably higher than those obtained using conventional methods. A mathematical model was established for continuous biodegradation, and simulation results coincided with the experimental results. The performance and operational criteria of the bioreactor were analyzed on the basis of both the experimental and simulation results. © 1992 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 40 (1992), S. 1440-1443 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
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    Biotechnology and Bioengineering 39 (1992), S. 833-858 
    ISSN: 0006-3592
    Keywords: biomass yield ; chemotrophic growth ; Gibbs energy dissipation ; thermodynamic efficiencies ; energy convertor ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Correlations for the prediction of biomass yields are valuable, and many proposals based on a number of parameters (YATP, YAve, ηo, Yc, Gibbs energy efficiencies, and enthalpy efficiencies) have been published. This article critically examines the properties of the proposed parameters with respect to the general applicability to chemotrophic growth systems, a clear relation to the Second Law of Thermodynamics, the absence of intrinsic problems, and a requirement of only black box information. It appears that none of the proposed parameters satisfies all these requirements. Particularly, the various energetic efficiency parameters suffer from major intrinsic problems. However, this article will show that the Gibbs energy dissipation per amount of produced biomass (kJ/C-mod) is a parameter which satisfies the requirements without having intrinsic problems. A simple correlation is found which provides the Gibbs energy dissipation/C-mol biomass as a function of the nature of the C-source (expressed as the carbon chain length and the degree of reduction). This dissipation appears to be nearly independent of the nature of the electron acceptor (e.g., O2, No3-, fermentation). Hence, a single correlation can describe a very wide range of microbial growth systems. In this respect, Gibbs energy dissipation is much more useful than heat production/C-mol biomass, which is strongly dependent on the electron acceptor used. Evidence is presented that even a net heat-uptake can occur in certain growth systems.The correlation of Gibbs energy dissipation thus obtained shows that dissipation/C-mol biomass increases for C-sources with smaller chain length (C6 → C1), and increases for both higher and lower degrees of reduction than 4. It appears that the dissipation/C-mol biomass can be regarded as a simple thermodynamic measure of the amount of biochemical “work” required to convert the carbon source into biomass by the proper irreversible carbon-carbon coupling and oxidation/reduction reactions. This is supported by the good correlation between the theoretical ATP requirement for biomass formation on different C-sources and the dissipation values (kJ/C-mol biomass) found. The established correlation for the Gibbs energy dissipation allows the prediction of the chemotrophic biomass yield on substrate with an error of 13% in the yield range 0.01 to 0.80 C-mol biomass/(C)-mol substrate for aerobic/anaerobic/denitrifying growth systems.
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  • 49
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    Biotechnology and Bioengineering 39 (1992) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
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    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 50
    ISSN: 0006-3592
    Keywords: Streptococcus lactis ; superoxide dismutase ; hyperbaric oxygen ; fed-batch fermentation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The production conditions of superoxide dismutase (SOD) in the cells of Streptococcus lactis by using hyperbaric oxygen (O2) are described. The SOD activity of anaerobically grown cells was 5-6 U/mg protein. When the culture broth was pressurized by O2 at 6 atm, the SOD activity was more than twice as high as that under anaerobic culture conditions. However, there is little or no significant increase in SOD activity by exogenous addition of catalase for detoxifying hydrogen peroxide accumulated in the broth and/or controlling the pH of the broth at 6.8 during the pressurization by O2. The increase in SOD activity by hyperbaric O2 was possible not only at the late-logarithmic growth phase but also at the initial time for the stationary growth phase. For improvement of SOD productivity, we tried a two-stage culture in which SOD activity in S. lactis cells was enhanced by pressurizing the culture broth using hyperbaric O2 after achievement of a high-concentration cultivation in the anerobic fermentation system with a microfiltration module.
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  • 51
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    Biotechnology and Bioengineering 39 (1992), S. 877-885 
    ISSN: 0006-3592
    Keywords: adsorption ; chromatography ; gradient-elution ; isotherms ; proteins ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The overloaded band profiles of lysozyme in reversedphase preparative chromatography were recorded on a C18 chemically bonded silica column, with acetonitrile/water as the mobile phase. These experiments were carried out under isocratic conditions at 31.6, 31.9, and 32.2% acetonitrile (ACN) for loading factors up to 43% of the column saturation capacity and under linear-solvent-strength gradientelution with gradient slopes of 0.5 and 1% ACN/min, for loading factors up to 11.3%. The adsorption isotherms of lysozyme were measured for the same solvent compositions and found to be accurately accounted for by a bi-Langmuir isotherm model.With the use of a Craig model implementation of the equilibrium-dispersive model of chromatography, the band profiles of lysozyme were calculated. An excellent agreement was observed between these calculated profiles and the experimental profiles recorded at loading factors below 5%. By contrast, band profiles calculated using a Langmuir isotherm failed to describe the experimental bands. At column loadings exceeding 8%, a slight but systematic deviation takes place between calculated and experimental profiles. It is most probably explained by the considerable concentration effect of the gradient, making the band experience phase equilibrium in a concentration range that exceeds largely the one where the isotherm data have been measured.
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  • 52
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    Biotechnology and Bioengineering 39 (1992), S. 1052-1057 
    ISSN: 0006-3592
    Keywords: Holarrhena antidysenterica ; suspension culture ; conessine ; precursor feeding ; stirred tank reactor ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Precursor feeding strategy for increasing the yield of conessine, a steroidal alkaloid of Holarrhena antidysenterica, was established in cell suspension culture. A total of 50 mg/L added cholesterol was converted into 43 mg/L of alkaloid, 90% of which constituted the conessine. By applying the precursor feeding policy to the cell suspension culture in modified Murashige and Skoog (MS) medium, a total of 143 mg/L of alkaloid was produced in 8 days. In this way the alkaloid content of the cells was increased more than six times compared to that obtained in the standard MS medium. The steps leading to biotransformation of cholesterol into alkaloids were unaffected by phosphate. The shake flask data were successfully transferred to a bench scale 6-L stirred tank bioreactor in which the specific biosynthetic rate of alkaloid production was 110 mg/100 g dry cell weight per day, about 160 times higher than that of whole plant.
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  • 53
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    Biotechnology and Bioengineering 39 (1992), S. 1064-1068 
    ISSN: 0006-3592
    Keywords: strontium ; adsorption ; plant tissue ; Lycopersicon esculentum ; Nicotiana tobacum ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Various types of microbial biomass have been shown to adsorb metals dissolved in aqueous media. It has now been demonstrated that certain plant tissues are also effective for this type of adsorption process. In particular, tomato and tobacco roots harvested from field-grown plants were shown to adsorb Sr from an aqueous solution of SrCl2. Distribution coefficients in excess of 550 were measured and the adsorption isotherms at 25°C could be fitted to Langmuir-type expressions. The bioadsorbent could be regenerated and metals recovered by either a reduction in the pH to less than 2.0 or by use of a concentrated chloride salt solution.
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  • 54
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    Biotechnology and Bioengineering 39 (1992) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
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  • 55
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    Biotechnology and Bioengineering 39 (1992), S. 1080-1085 
    ISSN: 0006-3592
    Keywords: immobilization ; mitochondrial membranes ; cytochrome oxidase ; ATPase, concanavalin A-Sepharose ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A fraction (15-20% of the total protein) of a preparation of bovine submitochondrial particles (SMPs) binds to concanavalin A-sepharose. The bound membranes displayed succinate dehydrogenase, cytochrome oxidase, and ATPase activity, which, as in SMPs, were inhibited by malonate, cyanide, and oligomycin, respectively. These results indicate that the bound membranes are inner mitochondrial membranes and that they contain a glycoprotein which was recognized by concanavalin A. It was possible to repeatedly perform the three enzyme assays, one after the other, in the same gel with the bound membranes. Long-term stability tests (22 days) showed that cytochrome oxidase was much more stable in the membranes bound to the gel than in SMPs, while the ATPase activity decayed at a similar rate in the two conditions. Thus, inner mitochondrial membranes bound to ConA-Sepharose appear to be a potentially interesting model for the study of immobilized multienzymatic complexes.
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  • 56
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    Biotechnology and Bioengineering 40 (1992) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
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  • 57
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    Biotechnology and Bioengineering 40 (1992), S. 183-186 
    ISSN: 0006-3592
    Keywords: Gluconobacter oxydans ; 5-ketogluconic acid ; tartatic acid ; vanadate ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The dependence of tartaric acid production by Gluconobacter oxydans ssp. oxydans ATCC 19357 and G. oxydans ssp. suboxydans ATCC 621 on vanadate was investigated. It was found with both organisms that trataric acid could only be produced in a medium containing vanadate (NH4VO3). A proposed intermediate of the tartaric acid metabolism in G. oxydans, 5-ketogluconic acid, was tested on its reactivity in the presence of the oxidizing catalyst vanadate. It could be shown that 5-ketogluconic acid and the catalyst vanadate, but not the activity of G. oxydans, were responsible for the formation of tartaric acid. G. oxydans was not able to produce tartaric acid by itself. The stereochemical identity of the formed tartaric acid could be identified as the L-(+)-type. Oxalic acid was formed from 5-ketogluconic acid with vanadate in the absence and in the presence of G. oxydans. The ratio of oxalic acid to tartaric acid was 1:1.
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  • 58
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    Biotechnology and Bioengineering 40 (1992), S. 187-193 
    ISSN: 0006-3592
    Keywords: quantitative image analysis ; mammalian cells ; microcarriers ; culture monitoring ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Quantitative image analysis has been applied to the monitoring of cultures of a mammalian cell line on microcarriers. Procedures have been developed to investigate microcarrier colonization and cluster formation and to determine the eventual modification of cell size during cultivation using scanning electron microscopy (SEM) microphotography. The human kidney tumor cells (TCL 598) on which the procedures were tested underwent a slight size decrease during the development of the first cell layer on the microcarriers. The cluster size and the cell size remained constant during the culture stationary phase.
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  • 59
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    Biotechnology and Bioengineering 40 (1992), S. 195-206 
    ISSN: 0006-3592
    Keywords: bioconversions ; hydrolysis ; casein proteins ; catalysis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Partition coefficients in poly(ethylene glycol)/dextran aqueous two-phase systems are reported for mixed-casein and its components, α, β and κ casein. Rates of casein proteolysis by α-chymotrypsin and by trypsin are reported in single-phase and aqueous two-phase reactor systems. The advantages resulting from selective partitioning of substrates, enzymes, and products are examined in terms of relative volumetric reaction rates.
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  • 60
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    Biotechnology and Bioengineering 40 (1992), S. 235-246 
    ISSN: 0006-3592
    Keywords: Fed-batch fermentation ; concentration fluctuations ; mixing effects ; Saccharomyces cerevisiae ; circulation time distribution ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In production-scale, fed-batch fermentations, feed is often added to a single point at the top of the fermentor, which, combined with poor mixing, results in formation of a “feed zone” rich in nutrients. Frequent exposure of the culture to high concentrations of nutrients in the feed zone for sufficient duration can produce unexpected effects on its performance. The effect of the feed zone was evaluated by conducting aerobic fed-batch fermentations of Saccharomyces cerevisiae with both complex and defined media. The broth was recirculated between a recycle loop and a bench-scale fermentor, and feed was intermittently added into the recycle loop to simulate the circulation of cells through the feed zone. Experiments were carried out for a range of residence times in the recycle loop from 0.5 to 12 min. Biomass yields from the complex-media fermentations were not affected by exposure to high nutrient levels in the recycle loop for residence times up to 12 min. Ethanol consumption was reduced by as much as 50% for residence time in the loop up to 3 min. Very long exposure of yeast cells to excess nutrient levels (12 min) gave acetic acid formation. In a defined medium, the simulated feed zone effect increased biomass yield by up to 10%, but had no effect on ethanol levels. This study indicates that the feed zone effect on biomass yield in yeast fermentation, using complex substrates, will be negligible under fully aerobic conditions.
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  • 61
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    Biotechnology and Bioengineering 40 (1992), S. 260-270 
    ISSN: 0006-3592
    Keywords: oxygen transfer rate ; high-cell-density culture ; design of a double-screen annular cage impeller ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: To improve the oxygen transfer in a mammalian cell bioreactor, a new type of impeller consisting of a double-screen concentric cylindrical cage impeller (annular cage impeller in short) was designed and its mass transfer rate evaluated. This new impeller design increases the specific screen area, and the convective mass transfer rate through the annular cage was significantly increased. The oxygen transfer rates with the new impeller and the commercially available cell-lift impeller (CelliGen by New Brunswick Scientific Co.) were evaluated and their performance compared at various rates of aeration and agitation. The results showed that with the new impeller, the oxygen transfer rate was increased by 19% in water and 21% in cell-free culture medium supplemented with 10% horse serum, the total hybridoma cell concentration was increased to 3.4 × 107 cells/mL, and the IgG1 subtype monoclonal antibody (MAb) product concentration was also increased to 512 mg/L in perfusion culture of murine hybridoma cell line 62′D3. These improvements in oxygen transfer rate, cell concentration, and MAb product concentration are all very significant. The mass transfer resistance in the cell-lift impeller system was found to be mainly due to the surface area of the single-screen cage impeller. The new annular cage impeller not only provided the increased surface area for convective oxygen transfer but also protected cells from hydrodynamic shear damage, thereby achieving a significant bioprocess improvement in terms of higher viable cell concentration, higher product concentration, and higher oxygen transfer rate in the mammalian cell bioreactor system.
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  • 62
    ISSN: 0006-3592
    Keywords: free energy of protein formation ; enthalpy of protein formation ; entropy of protein formation ; energies of protein anabolism ; ATP energy conservation in protein ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Using an average of the results from three methods of calculation, estimations are made of the thermodynamic properties of a unit carbon formula weight (UCFW) of Escherichia coli K-12 protein. These resulted in values fro ΔGf of -38.09 kJ (-9.10 kcal)/ UCFW, for ΔHf of -68.18 kJ (-16.29 kcal)/UCFW, and for ΔSf of -94.2 J (-22.5 cal)/UCFW deg. The absolute entropy of one UCFW of E. coli K-12 protein is calculated to be 73.8 J/UCFW deg. Using these values, the corresponding changes in thermodynamic properties accompanying the anabolism of protein by this microorganism to from one UCFW of protein by this microorganism to from one UCFW of protein are calculated to be 1.97 kJ (0.47 kcal)/UCFW for ΔG, 0.75 kJ (0.18 kcal)/UCFW for ΔH, and -4.09 J (-0.98 cal)/UCFW deg for ΔS. All these values are sufficiently close to zero that they may be considered to be so. The question is raised as to the quantity of ATP energy conserved within the substance of the protein as it is synthesized from succinic acid. It is calculated that only 3.8% of the total free energy available from ATP that is required during protein anabolism can have been conserved within the substance of the protein, there being a net conversion of the remaninder into heat and entropy.
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  • 63
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    Biotechnology and Bioengineering 40 (1992), S. 271-279 
    ISSN: 0006-3592
    Keywords: carbon starvation ; Escherichia coli ; growth control ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The use of glucose starvation to uncouple the production of recombinant β-galactosidase from cell growth in Escherichia coli was investigated. A lacZ operon fusion to the carbon starvation-inducible cst-1 locus was used to control β-galactosidase synthesis. β-Galactosidase induction was observed only under aerobic starvation conditions, and its expression continued for 6 h following the onset of glucose starvation. The cessation of β-galactosidase expression closely correlated with the exhaustion of acetate, an overflow metabolite of glucose, from the culture medium. Our results suggest the primary role of acetate in cst-1-controlled protein expression is that of an energy source. Using this information, we metered acetate to a glucose-starved culture and produced a metabolically sluggish state, where growth was limited to a low linear rate and production of recombiant β-galactosidase occurred continuously throughout the experiment. The cst-1 controlled β-galactosidase synthesis was also induced at low dilution rates in a glucose-limited chemostat, suggesting possible applications to high-density cell systems such as glucose-limited recycle reactors. This work demonstrates that by using an appropriate promoter system and nutrient limitation, growth can be restrained while recombinant protein production is induced and maintained.
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  • 64
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    Biotechnology and Bioengineering 40 (1992), S. 289-297 
    ISSN: 0006-3592
    Keywords: batch alcoholic fermentation ; enthanol ; product inhibition ; substrate inhibition ; biomass yield ; product yield ; Saccharomyces cerevisiae ; lag time ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In ethanol fermentation, instantaneous biomass yield of the yeast Saccharmoyces cerevisiae was found to decrease (from 0.156 to 0.026) with increase in ethanol concentration (from 0 to 107 g/L), indicating a definite relationship between biomass yield and product inhibition. A suitable model was proposed to describe this decrease which incorporates the kinetic parameters of product inhibition rather than pure empirical constants. Substrate inhibition was found to occur when substrate concentration is above 150 g/L. A similar definite relationship was observed between substrate inhibition and instantaneous biomass yield. A simple empirical model is proposed to describe the declines in specfic growth rate and biomass yield due to substrate inhibition. It is observed that product inhibition does not have any effect on product yield whereas substrate inhibition significantly affects the product yield, reflecting a drop in overall product yield from 0.45 to 0.30 as the initial substrate concentration increases from 150 to 280 g/L. These results are expected to have a significant influence in formulating optimum fermentor design variables and in developing an effective control strategy for optimizing ethanol producitivity.
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  • 65
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    Biotechnology and Bioengineering 40 (1992), S. 298-305 
    ISSN: 0006-3592
    Keywords: albumin ; transferrin ; proline ; hepatocytes ; primary culture ; serum free ; long term ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A serum-free culture system for primary hepatocytes which maintains stabel high-level hepatocyte function for prolonged periods in culture has been developed. Isolated rat primary hepatocytes were cultured in serum-free media between two layer of gelled collagen in a sandwich configuration which reinstates the cellular polarity necessary for long-term function in vitro. Thsee serum-free hepatocyte cultures maintained near physiological rates of albumin and transferrin secretion for a minimum of 26 days in culture. L-Proline was shown to be critical for both the approach to steady state and maximal level of protein secretion. Analysis of does-response data gave Km values of 2.9 and 1.7 μg/mL for albumin and transferrin secretion, respectively.
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  • 66
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    Biotechnology and Bioengineering 40 (1992), S. 313-321 
    ISSN: 0006-3592
    Keywords: immunometric assay ; sandwich immunoassay ; biosensor ; off-line fermention monitoring ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A novel two-site immunofluorometric assay, which includes only one incubation step and one separation step, is described. The assay is based on using small-sized beads (0.5 μm diameter) as a soild support and measuring the unbound fraction of labeled antibody in the liquid. The use of a mixture of the solid-phase and labeled antibodies at different concentrations makes it possible to determine antigen concentration over a wide range, without an initial sample dilution. Two assays were developed: one using anti-IgG polyclonal antibodies and the other using antibovine serum albumin monoclonal antibodies. The detection range of the polyclonal antibody assay using 30-minute incubation was 0.2 to 40 μg/mL for human IgG standard. The detection range of the monoclonal antibody assay was 0.2 to 14 μg/mL for bovine serum albumin (BSA) standard with 2 minutes required for the incubation. The interassay variability for the BSA measurement was 1.9% at 4.0 μg/mL of BSA and intra-assay variability was 2.3% at 3.2 μg/mL of BSA. The principles of this assay can be applied in the measurement of any protein in a rapid and reproducible way. © 1992 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 40 (1992), S. 1190-1196 
    ISSN: 0006-3592
    Keywords: erythropoietin ; recombinant protein ; heat shock ; protein synthesis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The production of recombinant proteins by mammalian cells demands a highly controlled environment for cell cultivation. Temperature stress represents a commonly encountered disturbance in both research and process environments. In this study, we examined the effects of heat shock on the expression of recombinant human erythropoietin (EPO) in a Chinese hamster ovary (CHO) cell line. Biosynthetic radiolabeling experiments indicated that the cells exposed to a 42°C/1-hour heat shock exhibit a transient reprogramming of transcription and translation characterized by the inhibition of protein synthesis and induction of heat shock proteins. The rate of protein synthesis decreased by 50% after the heat shock, while the rate of RNA synthesis increased by 50% initially and then quickly reduced to 80% of the control level. The protein and RNA synthesis rates were fully recovered in approximately 48 hours after the heat shock. However, we found that the expression of EPO was not arrested by the heat shock. The glycosylation patterns, as examined by isoelectric focusing, of either the culture supernatant or the purified EPO were not affected by the heat shock. In contrast, a 45°C/1-hour heat shock terminated RNA and protein synthesis immediately and caused culture death in 12 hours. Cellular responses to temperature stress were affected by the metabolic state of the cells; cells maintained in serum-free medium were more sensitive than cells growing exponentially in the presence of serum. We have also examined the kinetics of metabolic responses of the cells to heat shock with respect to nutrient uptake and metabolite accumulation. © 1992 John Wiley & Sons, Inc.
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  • 68
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    Biotechnology and Bioengineering 40 (1992), S. 1286-1291 
    ISSN: 0006-3592
    Keywords: oxygen uptake rate ; hepatocytes ; cell spreading ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: One potential treatment of acute liver failure involves the use of an extracorporeal device composed of functional hepatocytes. A major issue in the design of such a large-scale device is providing the hepatocytes with a sufficient supply of oxygen and other nutrients. In this study, we have designed and characterized a simple perfusion system hepatocytes using this system. The OUR of hepatocytes was determined during the first day after seeding on a single collagen gel and during the long-term stable culture after the addition of a top layer of collagen. The OUR increased to 20.7 ± 0.57 pmol/sec/μg DNA during the first 13 hours of culture on a single collagen gel, while during the next 11 hours, the OUR declined to 10.6 ± 1.5 pmol/sec/μg DNA. In parallel with the increase in OUR during the first 10 hours, we observed significant cell spreading, suggesting that the oxygen supply to the cells may be critical for the spreading and adaptation of the anchorage-dependent hepatocytes following isolation. Addition of a top layer of collagen to hepatocyte cultures for 24 hours of culture on a single collagen layer resulted in a stable OUR for 15 days. These results indicate that OUR of hepatocytes in culture may vary depending on the phase of culture (i.e., early vs. late) and on the extracellular environment. © 1992 John Wiley & Sons, Inc.
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  • 69
    ISSN: 0006-3592
    Keywords: immobilization ; chemical adsorption ; alumina ; phosphate ; papain ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The chemical adsorption of organic phosphate compounds to alumina has been used to create surface linkers for protein immobilization. A number of particulate alumina supports were screened for their physical properties and ability to bind organic phosphate compounds. Two aluminas, termed C1 and CPC, were selected based on their suitability for subsequent testing as protein immobilization supports. Papain was successfully immobilized to these supports when derivatized with phosphate compounds containing free terminal carboxyl groups. Protein binding was enhanced when support carboxyl groups were activated with 1-ethyl-3-(3-dimethylaminopropyl)carbodiimide. The level of papain immobilization was dependent upon the length of the linker used and the mass of protein exposed to the support. © 1992 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 40 (1992), S. 1343-1352 
    ISSN: 0006-3592
    Keywords: oxygen transfer ; surface aeration ; biological enhancement ; physical blocking ; interfacial surfactant film ; interfacial cell layer ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A model was developed to evaluate the effects of cells and surfactants on oxygen transfer in surface-aerated bioreactors. The model assumed the presence of serial layers of adsorbed surfactants and microorganisms directly adjacent to the gas-liquid interface due to their surface activities, followed by a stagnant liquid layer to account for the oxygen transfer resistance in the liquid phase. The interfacial surfactant film, although posing as an additional resistance, was found to have negligible effect on the oxygen transfer rate because of its extremely small thickness as compared to the cell monolayer and the stagnant liquid layer. On the other hand, cells affect oxygen transfer by two mechanisms: the biological enhancement due to the respiration of interfacial cells and the physical blocking resulting from the semipermeable nature of cell bodies. Due to the low specific oxygen uptake rates of the sludges, the two mechanisms were found to be of comparable importance in activated-sludge systems; the oxygen transfer enhancement factor, E, varied from about 0.97 to 1.10 depending on the operating conditions. The biological enhancement effect, however, predominated in fermentations of actively growing bacteria. At relatively low agitation speed (e. g., 300 rpm), the value of E could reach about 3 to 5 in fermentations with high cell concentrations. Effects of other operating variables, such as the agitation intensity, the oxygen content in the mixed liquor, and the bulk cell concentration, on biological oxygen transfer enhancement were also studied. © 1992 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 39 (1992), S. 44-48 
    ISSN: 0006-3592
    Keywords: directional growth ; modeling ; morphology ; pellet formation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Growth of Streptomyces tendae was investigated in submerged culture. Images of several mycelia were analyzed by means of an image-processing system. The studies revealed that tip growth angles and branching outgrowth angles could be regarded as normally distributed. Based on these results, a random model for directional growth of hyphal tips as well as directional growth of branches is proposed. This model shows curved elongation of hyphal tips, so that the morphological development of a mycelium up to the formation of a pellet is predicted, similar to that observed in nature.
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  • 72
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    Biotechnology and Bioengineering 39 (1992), S. 66-74 
    ISSN: 0006-3592
    Keywords: bioleaching ; adsorption ; growth kinetics ; Thiobacillus ferrooxidans ; zinc sulfide ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The kinetics of the bioleaching of ZnS concentrate by Thiobacillus ferrooxidans was studied in a well-mixed batch reactor. Experimental studies were made at 30°C and pH 2.2 on adsorption of the bacteria to the mineral, ferric iron leaching, and bacterial leaching. The adsorption rate of the bacteria was fairly rapid in comparison with the bioleaching rate, indicating that the bacterial adsorption is at equilibrium during the leaching process. The adsorption equilibrium data were correlated by the Langmuir isotherm, which is a useful means for predicting the number of bacteria adsorbed on the mineral surface. The rate of chemical leaching varied with the concentration of ferric iron, and the first-order reaction rate constant was determined. Bioleaching in an iron-containing medium was found to take place by both direct bacterial attack on the sulfide mineral and indirect attack via ferric iron. In this case, the ferric iron was formed from the reaction product (ferrous iron) through the biological oxidation reaction. To develop rate expressions for the kinetics of bacterial growth and zinc leaching, the two bacterial actions were considered. The key parameters appearing in the rate equations, the growth yield and specific growth rate of adsorbed bacteria, were evaluated by curve fitting using the experimental data. This kinetic model allowed us to predict the liquid-phase concentrations of the leached zinc and free cells during the batch bioleaching process.
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  • 73
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    Biotechnology and Bioengineering 39 (1992), S. 108-112 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A new process for embedding cells in agarose is described. Beads were obtained by extruding an ultralow gelling temperature agarose solution in a capillary containing a hydrophobic medium flowthrough. The toxicity of the procedure has been evaluated by monitoring the energy status of agarose-embedded C6 glioma cells with 31P nuclear magnetic resonance (NMR). Suspension and microbead cultures of hybridoma cell line were compared. In suspension culture the number of cells and the antibody concentrations increased for 5 days before the stationary phase began, when the cultures were stopped. In agarose bead cultures, the gel provided an enormous support surface area (50 m2/ mL of gel). It was possible to seed 20-fold more cells. The gel pressure modified the proliferative process and antibody pattern secretion. In particular, the antibodies could be harvested for two weeks.
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    Biotechnology and Bioengineering 39 (1992), S. 121-123 
    ISSN: 0006-3592
    Keywords: Cellulomonas sp. ; Trichoderma reesei ; short fiber formation ; Avicel ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Three immunologically and enzymatically distinct endoglucanases of Cellulomonas sp. ATCC 21399 were purified previously. Endoglucanase A and endoglucanase B acted synergistically on microcrystalline cellulose (Avicel), whereas no synergistic action was observed between endoglucanase B or endoglucanase C. Only endoglucanase A was capable of hydrolyzing Avicel when acting alone and this enzyme resulted in “short fiber formation” when acting on Avicel. The end product of hydrolysis of acid swollen Avicel produced by the three endoglucanases was in all cases dominated by cellobiose and showed lower content of glucose and cellotriose. Higher cellodextrins appeared as transient end products. The results indicate that the function of endoglucanase A in the cellulase system of Cellulomonas might be very similar to the function of the cellobiohydrolases of Trichoderma reesei.
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    Biotechnology and Bioengineering 39 (1992), S. 1-4 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
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    Biotechnology and Bioengineering 39 (1992), S. 20-26 
    ISSN: 0006-3592
    Keywords: reversed micelle ; extraction ; solubilizing water ; AOT ; protein ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The extraction of protein using reversed micelles was investigated in relation to the amount of solubilizing water in the reversed micellar organic phase. The minimal concentration of amphiphilic molecule di-2-ethylhexyl sodium sulfosuccinate (C20H37O7Na) (AOT) required for 100% cytochrome c extraction was recognized. This critical AOT concentration increased with protein concentration in the aqueous phase. On this minimal AOT condition, the molar ratio of solubilizing water to extracted protein was found to be a constant of 3500 under CKCI = 1.0 × 102 mol · m-3 in this system. This ratio means the hydrophillic surroundings required for extracting one protein molecule into the micellar organic phase under the suitable pH and salt concentration for the forward extraction. In this regard, AOT molecules seemed to take the part of water solubilizing agent in the reversed micellar extraction. This role of AOT is important to extract protein under the suitable pH and salt concentration. The amount of solubilizing water in the protein-containing system was larger than in the protein-free system. This difference shows that the water molecules accompany the extracted protein into the reversed micellar organic phase at constant ratio 2200 under CKCI = 1.0 × 102 mol · m-3, i.e., accompanying water molecules per one extracted protein. The minimal AOT concentration increased with ionic strength. On this minimal AOT condition, the molar ratio of solubilizing water to extracted protein also increased with ionic strength, so that in higher ionic strength, more solubilizing water was required. Then more AOT was required to provide the hydrophillic surroundings for protein. The pH affected the minimal AOT concentration required for 100% protein extraction.
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    Biotechnology and Bioengineering 39 (1992), S. 59-65 
    ISSN: 0006-3592
    Keywords: pet operon ; E. coli ; metabolic fluxes ; metabolic engineering ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Fermentation patterns of Escherichia coli HB101 carrying plasmids expressing cloned genes of Zymomonas mobilis pyruvate decarboxylase (PDC) and alcohol dehydrogenase li (ADH) were determined in glucose-limited complex medium in pH-controlled anaerobic batch cultivations. Time profiles of glucose, dry cell weight, succinate, formate, acetate, and ethanol were determined, as were the activities of ADH and PDC. Fluxes through the central carbon pathways were calculated for each construct utilizing exponential phase data on extracellular components and assuming quasi-steady state for intermediate metabolites. Overall biomass yields were greatest for cells expressing both PDC and ADH activities. Yields of carbon catabolite end products were similar for all PDC-expressing strains and different from those for other strains. Relative to its glucose uptake rate, the strain with greatest PDC and ADH activities produces formate and acetate more slowly and ethanol more rapidly than other strains. Strong influences of plasmid presence and metabolic coupling complicate detailed interpretations of the data.
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    Biotechnology and Bioengineering 39 (1992), S. 95-107 
    ISSN: 0006-3592
    Keywords: microcarrier culture ; shear damage ; turbulence ; model ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The effect of medium viscosity on the specific death rate of bovine embryonic kidney (BEK) cells cultured in spinner flask microcarrier cultures has been examined for various impeller speeds. Two types of media were used, a serum-containing growth medium and a serum-free maintenance medium. The latter does not support cell growth. We found that increasing medium viscosity suppresses cell death rates in both growth and maintenance medium cultures in an agitation-intensity-dependent fashion; the beneficial effect of medium viscosity in reducing the specific death rate is amplified as the agitation rate is increased. Furthermore, increasing medium viscosity has no effect on the specific death rate of the cells when the agitation rate is below a critical level. A model based on the turbulent energy content of eddies in the dissipation spectrum of turbulence of length scales on the order of magnitude of the microcarrier diameter and lower has been developed to account for cell death due to both bead-to-bead and bead-to-eddy interactions. The model constitutes a significant departure from previous efforts first because both types of interactions are accounted for simultaneously and second because the properties of a spectrum of eddies instead of the Kolmogorov-scale eddy size alone are used in the model. The model explains the functional dependence of the specific death rates on the medium viscosity at varying agitation intensities.
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    Biotechnology and Bioengineering 39 (1992), S. 117-120 
    ISSN: 0006-3592
    Keywords: enzyme hydrolysis ; cellulase ; enzyme adsorption ; nonionic surfactant ; gel filtration chromatography ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Effects of five types of nonionic surfactant having a polyoxyethylene glycol (POG) group on enzymatic hydrolysis of used newspaper were studied. The surfactants examined in this work always enhanced the saccharification. The optimum surfactant concentration was 0.05% (wt/substrate wt) in the case of POG(21) sorbitane oleic ester. Among the surfactants, POG phenyl ether types showed the highest enhancement effect, for example, with two times higher conversion at 80 h than that without surfactant. Using POG nonylphenyl ether series, the effects of surfactant were considered from the point of the HLB (hydrophile-lypophile balance) value. The GFC (gel filtration chromatography) analysis of free enzyme quantity were also done to study the effect of surfactant on enzyme adsorption onto substrate. As the HLB value increased, the free enzyme quantity and the conversion both increased. It appears that surfactants help the enzyme to desorb from the binding site on the substrate surface after the completion of saccharification at that site.
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    Biotechnology and Bioengineering 39 (1992), S. 141-147 
    ISSN: 0006-3592
    Keywords: protein engineering ; enzymes in organic solvents ; protein stabilization ; subtilisin E ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Subtilisin E was rationally engineered to improve its stability in polar organic solvents such as dimethylformamide (DMF). A charged surface residue, Asp248, was substituted by three amino acids of increasing hydrophobicity, Asn, Ala, and Leu; all three variants were stabilized with respect to wild type in 80% DMF. This stabilization was only observed in the presence of high concentrations of the organic solvent: no stability enhancements were observed in 40% DMF. In contrast, the mutation Asn218 → Ser alters internal hydrogen bonding interactions and stabilizes subtilisin E in both 40% and 80% DMF. This study provides additional evidence that substitution of surface-charged residues is a generally useful mechanism for stabilizing enzymes in organic media and that the stabilizing effects of such substitutions are unique to highly altered solvent environments. The effects of the single amino acid substitutions on free energies of stabilization are additive in the Asp248 → Asn + Asn218 → Ser combination variant, yielding an enzyme that is 3.4 times more stable than wild type in 80% DMF.
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    Biotechnology and Bioengineering 39 (1992), S. 171-175 
    ISSN: 0006-3592
    Keywords: penicillin acylase ; penicillin G ; hydrolysis ; electrodialysis ; product inhibition ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Phenylacetic acid, as inhibitory product, was formed from a hydrolysis of penicillin G by immobilized penicillin acylase. In this article, electrodialysis was applied to remove phenylacetic acid continuously from the reaction mixture and to enhance an efficiency of the reaction. When 268 and 537 mM of penicillin G solution were used as the substrate, the concentration of phenylacetic acid in the reaction mixture could be maintained at less than 81 and 126 mM, respectively, and eventually, 86% and 88% of phenylacetic acid produced were removed from the reaction mixture at the end of the hydrolysis, respectively. Times required to reach 96% and 94.8% conversion from 268 and 537 mM of initial penicillin G could be reduced to 65% and 64% respectively, by means of electrodialysis; while 3.0% and 4.3% of initial penicillin G of 268 and 537 mM were permeated out of the reaction chamber during the hydrolysis, respectively. However, a loss of penicillin G by permeation could be reduced from 4.3% to 3.4% by a repeated addition of penicillin G.
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    Biotechnology and Bioengineering 39 (1992), S. 203-210 
    ISSN: 0006-3592
    Keywords: glucose-6-acetate ; B. megaterium ; fructosyl transferase ; conversion ; sucrose-6-acetate ; sucralose ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A general method for protecting the 6 primary hydroxyl position of sucrose is described. It involves the production of glucose-6-acetate by fermentation of glucose using a strain of Bacillus megaterium followed by conversion to sucrose-6-acetate as a kinetic product using a specially selected fructosyl transferase producted by a newly isolated strain of Bacillus subtilis. The sucrose-6-acetate was found to be more lipophilic than expected, and this property aided its purification by chromatography. Pure sucrose-6-acetate may then be chlorinated and subsequently deacetylated to give the high-intensity sweetener 4,1′,6′-trichlo-4,1′,6′-trideoxygalactosucrose (sucralose) in high yields. This process involves fewer steps than are required for chemical synthesis using trityl chloride and acetic anhydride. Related intensely sweet molecules which were synthesized by similar methods included 4,1′,6′-trichloro, 4,1′,6′-trideoxy L-arabinosucrose, and 4,1′,6′-trichloro-4,6,1′,6′-tetradeoxy-galactosucrose. They were obtained from xylose and 6-deoxyglucose, respectively, via the intermediates xylsucrose and 6-deoxysucrose, formed by the reaction of the fructosyl transferase on the monosaccharide acceptors.
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    Biotechnology and Bioengineering 39 (1992) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
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    Biotechnology and Bioengineering 39 (1992), S. 27-32 
    ISSN: 0006-3592
    Keywords: electrically controlled cell culture ; promoted protein production ; MKN45 cell ; electrical effect on mammalian cells ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Protein production of mammalian cells has been promoted by applying a small constant potential to the surface of an electrode on which cells are cultured. Human carcinoma line of MKN45 cells were cultured on the surface of a platinum-coated plastic plate electrode. Low d.c. voltage of constant potential was applied to the electrode during 4-day culture to modulate the production of carcinoembryonic antigen (CEA). The amounts of both secreted and membrane-bound CEA were dependent on the applied potential during culture. Secreted CEA was more than twice in amount in the potential range from 0.2 V to 0.6 V vs. Ag/Agcl as compared with that of normal culture. In the potential range, CEA was also increased in membrane-bound form. The potential-controlled cell culture may have an enhanced effect on protein production.
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    Biotechnology and Bioengineering 39 (1992), S. 49-58 
    ISSN: 0006-3592
    Keywords: mycelial growth ; model ; simulation ; streptomycetes ; fungi ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A mathematical model for apical growth, septation, and branching of mycelial microorganisms is presented. The model consists of two parts: the determinstic part of the model is based on fundamental cellular and physical mechanisms; it represents the kinetics for growth of hyphal tips and septation of apical as well as intercalary compartments. In regard to random occurrences of hyphal growth and branching, the stochastic part deals with branching processes, tip growth directions, and outgrowth orientations of branches. The model can explain the morphological development of mycelia up to the formation of pellets. The results, as predicted by the model, correspond very closely to those observed in experiments. In addition, some unmeasured states can be ascertained, such as the distribution functions of hyphal length (biomass) and tips along pellet radii.
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    Biotechnology and Bioengineering 39 (1992), S. 85-94 
    ISSN: 0006-3592
    Keywords: xanthan ; bubble column ; air life ; mixing ; oxygen transfer limitation ; modeling ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A bubble column (0.05 m3) and an air-lift fermentor (1.2 m3) were used for the production of the exocellular microbial polysaccharide xanthan with Xanthomonas campestris in a synthetic medium. Upon oxygen depletion in the liquid, the xanthan production rate dropped sharply and then became a linear function of the oxygen transfer rate. The volumetric mass transfer coefficients for oxygen conformed to the correlation of Suh et al. Using this correlation in combination with the model for xanthan batch fermentation suggested by Peters et al., the xanthan fermentations in the bubble column were well described. The model also correctly predicted the time course of the molecular weight of the polysaccharide even when a complex medium was used. In the air-lift fermentor, however, the xanthan production rate and the xanthan yields with respect to oxygen and glucose were lower than expected at the overall oxygen transfer rate. The poor performance of the air lift was traced back to the lack of any oxygen supply in the downcomer.
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    Biotechnology and Bioengineering 39 (1992) 
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    Keywords: Chemistry ; Biochemistry and Biotechnology
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    Biotechnology and Bioengineering 39 (1992), S. 132-140 
    ISSN: 0006-3592
    Keywords: enzymatic synthesis ; continuous production ; anion-exchange ; peptide-amidase ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A simple system is introduced to produce dipeptides continuously by enzyme catalyzed condensation of amino acid esters and amino acid amides. Synthesis of N-terminal free dipeptide-amides is achieved by means of carboxypeptidase Y. The peptide-amide is deamidated utilizing a newly isolated peptide-amide is deamidated utilizing a newly isolated peptide-amidase. Separation of substrates and products is accomplished by anion-exchange chromatography. Modeling of the reactions shows that the two reactions have to be carried out in a cascade of two reactors in order to prevent hydrolysis of the peptide by the carboxypeptidase. Continuous production of Kyotorphin (H-TyrArg-OH) with a space-time yield of 257 g/L · d shows the feasibility of this concept.
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    Biotechnology and Bioengineering 39 (1992), S. 164-170 
    ISSN: 0006-3592
    Keywords: pellet morphology ; submerged growth ; image analysis ; Streptomyces tendae ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Many filamentous bacteria and fungi tend to form pellets, or mixtures of dispersed mycelium and pellets in liquid fermentation broths. In some cases, a specific kind of morphology is required for optimum product yield. When quantitative analysis and characterization of the pellet morphology are needed, an image processing system can be used. It allows a fast and reproducible analysis of the frequency distribution of pellet size, mean pellet size, contents of pellets, or their shape. The use of such a system allows for an on-line analysis. For a demonstration of the method, results of two fermentations of Streptomyces tendae are shown.
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    Biotechnology and Bioengineering 39 (1992), S. 195-202 
    ISSN: 0006-3592
    Keywords: Nicotiana glauca ; media pH ; feedback inhibition ; Amberlite columns ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Transformed roots of Nicotiana glauce synthesize the alkaloids nicotine and anabasine at levels reflecting the parent plants. Media composition, strength, and pH were evaluated with respect to biomass yield and productivity. Full-strength Gamborg's B5 medium proved the best for biomass yield while half-strength, or low-salt, medium enhanced alkaloid accumulation. A detailed investigation of media nitrate levels demonstrated how these may be manipulated to promote growth and intracellular or extracellular alkaloid levels. High nitrate concentrations were found to significantly enhance media alkaloid levels at the end of the growth phase. Media pH is also important, although transformed roots will grow in Gamborg's B5 medium between pH 3 and 9, root biomass is favored by an increase in medium alkalinity, while alkaloid release is encouraged by mildly acidic pH.Transformed roots release a proportion of their secondary metabolites into the growth medium. By continually removing root products, any feedback inhibition on enzymatic reactions is reduced, as are the toxic effects resulting from product accumulation. In this article we describe the use of Amberlite resins (XAD-2 and XAD-4) to enhance alkaloid levels (nicotine and anabasine) of hairy root cultures of Nicotiana glauca by a factor of 10 with no adverse effect on root growth. The performance of the Amberlite columns was subsequently investigated with respect to alkaloid adsorption and desorption, including an evaluation of the effects of pH and loading capacity. The resins also adsorb media constituents which are identified and quantified as part of this work. Resulting nutritional stresses are thought to be partly responsible for enhancing secondary metabolism at the expense of biomass yield. However, the net effects of using Amberlite resins as a means of product removal significantly increases the overall product yield and the extent to which products are released into the growth medium.
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    Biotechnology and Bioengineering 39 (1992), S. 225-232 
    ISSN: 0006-3592
    Keywords: electroconductive heating ; electrical pretreatment ; thermal death kinetics ; zygo Saccharomyces bailii ; Escherichia coli ; microorganisms ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Suspensions of yeast cell (zygo Saccharomyces bailii) in a phosphate buffer solution were subjected to conventional (hot water) and ohmic (electric current) heating under identical temperature histories. Experiments were also conducted with cells of Escherichia coli to compare the lethal effect of combination of sublethal electrical preteatment and conventional heating with conventional heating. The kinetic parameters (D,Z,K and Ea) were determined for both organisms during different treatments. There was no significant difference in the death rate of yeast cells during conventional and ohmic heating at the voltage range used in this study. Results of electrical pretreatment and conventional heating on E. coli indicated differences under certain conditions when compared with pure conventional heating. Thus it is concluded that microbial death during ohmic heating was due primarily to thermal effects with no significant effect of electric current per se. Sublethal electrical pretreatment appears to offer potential for increased bacterial inactivation in certain cases.
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    Biotechnology and Bioengineering 39 (1992), S. 251-261 
    ISSN: 0006-3592
    Keywords: monoclonal antibody secretory pathway ; structured kinetic model ; factorial design ; steady-state simulations ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Steady-state simulations using our previously developed structured kinetic model of antibody synthesis and secretion by hybridoma cells are used here in conjunction with factorial design analysis to identify intracellular parameters important in determining the specific antibody secretion rate and predict the dependence of this rate on cell specific growth rate. Simulation results suggest that the specific growth rate, the assembly rate of the heavy and light chains and the heavy- and -chain gene dosage can significantly affect the rate of antibody secretion. Based on these results, environmental and/or genetic manipulation approaches are proposed for maximizing the specific antibody secretion rate and the antibody volumetric productivity in large-scale antibody production systems.
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  • 93
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    Keywords: cellulase, soluble-insoluble ; enzyme, soluble-insoluble ; rice straw hydrolysis ; hydrolysis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A reversibly soluble-autoprecipitating cellulase was prepared by covalently immobilizing Meicelase on an enteric coating polymer (AS-L, hydroxypropyl methylcellulose acetate succinate). The immobilized enzyme (M-AS) was reversibly soluble-insoluble depending on the pH of the reaction medium. Moreover, the enzymatic activity of M-AS, in a soluble state, for microcrystalline cellulose was higher than that of the conventional solid immobilized enzyme. On the other hand, M-AS, in an insoluble state, and good properties of self-sedimentation, and a large portion of M-AS spontaneously precipitated for about 15 min at pH 3.8. In the repeated hydrolysis of rice straw, delignified with sodium hydroxide using a bioreactor with a conical bottom, M-AS was separated batchwise from a production solution by self-sedimentation in a conical bottom of the bioreactor. When delignified, rice straw was hydrolyzed repeatedly by reuse of M-AS; the total amount of soluble sugar produced from 5 g of delignified rice straw was 2.7 g. Further, by the hydrolysis method with repeated removal of reaction inhibitors (soluble sugar), the time required for converting the same amount of delignified rice straw to soluble sugar was significantly reduced, as compared with that by the standard reaction method.
    Additional Material: 6 Ill.
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  • 94
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 39 (1992), S. 281-286 
    ISSN: 0006-3592
    Keywords: chitin ; chitosan ; Mucor rouxii ; polysaccharides ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The isolation of chitosan from a fungal source offers the potential of a product with controlled physicochemical properties not obtainable by the commercial chemical conversion of crustacean chitin. A variety of culture and processing protocols using Mucor rouxii were studied for their effects on biomass yield and chitosan molecular weight. Weight-averaged molecular weight determined by gel permeation chromotography ranged from 2.0 × 105 to approximately 1.4 × 106 daltons. The chitosan yield ranged from 5% to 10% of total biomass dry weight and from 30% to 40% of the cell wall. Of the culture parameters studied, length of incubation and medium composition effected biomass production and molecular weight. Modification of the processing protocol, including the type and strength of acid, and cell wall disruption in acid prior to refluxing were used to optimize the efficiency of chitosan extraction.The degree of deacetylation of fungal and commercial chitosans was compared using infrared spectrometry, titration, and first derivative of UV absorbance spectrometry. The chitosan obtained directly from the fungal cell wall had a higher degree of deacetylation than commercial chitosan from the chemical conversion process.
    Additional Material: 5 Ill.
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  • 95
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 39 (1992), S. 293-304 
    ISSN: 0006-3592
    Keywords: control ; fermentation ; baker's yeast ; high cell density ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A methodology for the design and evalution of bioprocess control strategies is presented. The strategies manage nutrient supply with demand and vary with the metabolic condition and phase of fermentation operation. Six carbon source addition strategies are based on different combinations of available measurements; they are described and evaluated under different operating conditions for yeast cultivation. It is concluded that a single control strategy is not the most appropriate under all possible operating conditions. An oxygen uptake rate-based control strategy performs better with a mean respiratory quotient (RQ) value less than 1.1 during an oxygen limitation than an ethanol control strategy which had a mean RQ of 14. The designed strategies and an approach of applying the strategy that best matches fermentation conditions consistently enables achievement of high cell densities 78.7 g DCW/L and yields 0.50 g DCW/g glucose as the mean values for three fermentations.
    Additional Material: 8 Ill.
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  • 96
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 39 (1992), S. 314-319 
    ISSN: 0006-3592
    Keywords: affinity chromatographic reactor ; dynamic affinity ; coenzyme regeneration ; NAD regeneration ; bioreactor ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The affinity chromatographic reactor (ACR) is a bioreactor which utilizes the dynamic interaction or the dynamic affinity between a free coenzyme and immobilized enzymes for the highly efficient regeneration of dissociable coenzymes. Dynamic affinity between free NAD and immobilized alcohol dehydrogenase (ADH) in ACR was investigated by three different methods. ADH catalyzed both oxidation and reduction of NAD, consuming propionaldehyde and ethanol. The theoretical model under consideration elucidated a criterion for the expression of the dynamic affinity as a relationship among the affinity constants and the concentrations of a coenzyme and immobilized enzyme. This criterion was confirmed experimentally by the measurements of the retention time of NAD and the half-life period of the reactor activity after one-shot pulse injection of NAD to ACR. In the stability measurement of the immobilized enzyme, it became clear that ADH was more stable at the higher concentration in immobilization. Although the present case of coenzyme cycling by a single enzyme is very special, with limited chance for the direct application, the results obtained here provide a theoretical basis for ACR with multienzymes-which is of more general use.
    Additional Material: 9 Ill.
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  • 97
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 39 (1992), S. 305-313 
    ISSN: 0006-3592
    Keywords: inoculation protocol ; anchorage-dependent cells ; microcarriers ; initial cell attachment ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The environmental conditions under which anchorage-dependent mammalian cells are grown are not necessarily those under which a culture should be initiated. Cell attachment is a physical process, and those factors which affect forces involved in cell attachment differ from the biological factors which affect cell growth. We have conducted an extensive experimental study to define clearly the optimal environmental conditions for MRC-5 cell attachment onto microcarriers. These inoculation conditions are particularly important when the serial propagation of mammalian cells on microcarriers is considered as in a human vaccine production process. The conditions which were investigated are: initial serum content (% v/v), initial pH, inoculation level (cells/bead), agitation rate (rpm), and the concentration of microcarriers (g/L). The initial distribution of attached cells was found to have a significant affect on the overall efficiency of anchorage-dependent cell cultures, and was used to evaluate attachment efficiency. Based on the experimental results, we propose an optimized protocol for the inoculation of microcarrier cultures.
    Additional Material: 12 Ill.
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  • 98
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 39 (1992), S. 336-342 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Gluconic acid and sorbitol were simultaneously produced from glucose and Jerusalem artichoke using a glucose-fructose oxidoreductase of Zymomonas mobilis and inulinase. Inulinase was immobilized on chitin by cross-linking with glutaraldehyde. Cells of Z. mobilis permeabilized with toluene were coimmobilized with chitin-immobilized inulinase in alginate beads. The optimum amounts of both chitin-immobilized inulinase and permeabilized cells for coimmobilization were determined, and operational conditions were optimized. In a continuous stirred tank reactor operation, the maximum productivities for gluconic acid and sorbitol were about 19.2 and 21.3 g/L/h, respectively, at the dilution rate of 0.23 h-1 and the substrate concentration of 20%, but operational stability was low because of the abrasion of the beads. As an approach to increase the operational stability, a recycle packed-bed reactor (RPBR) was employed. In RPBR operation, the maximum productivities for gluconic acid and sorbitol were found to be 23.4 and 26.0 g/L/h, respectively, at the dilution rate of 0.35 h-1 and the substrate concentration of 20% when the recirculation rate was fixed at 900 mL/h. Coimmobilized enzymes were stable for 250 h in a recycle packed-bed reactor without any loss of activity, while half-life in a continuous stirred tank reactor (CSTR) was observed to be about 150 h.
    Additional Material: 10 Ill.
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  • 99
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 39 (1992), S. 351-353 
    ISSN: 0006-3592
    Keywords: gas metering ; biogas production ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An automated metering system was developed for measuring biogas production from laboratory scale biogas digestors. The gas metering system is based on the principle of liquid displacement with a 100-mL reversible cycle and registration. The gas meter is made entirely of plastic and rubber materials resistant to the corrosive components of biogas (e.g., H2S) and requires a 12 to 15 VDC power supply.
    Additional Material: 3 Ill.
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  • 100
    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.
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