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  • Biochemistry and Biotechnology  (879)
  • Inorganic Chemistry  (608)
  • Industrial Chemistry and Chemical Engineering  (228)
  • 1995-1999  (1,715)
  • 1990-1994
  • 1950-1954
  • 1997  (1,715)
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  • 1995-1999  (1,715)
  • 1990-1994
  • 1950-1954
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  • 1
    Electronic Resource
    Electronic Resource
    Weinheim : Wiley-Blackwell
    Chemical Engineering & Technology - CET 20 (1997), S. 144-148 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The kinetics of the liquid phase hydrogenation of 4-tert-butylphenol to form cis- and trans- 4-tert-butylcyclohexanol at 1.0-10.0 MPa and 40°C in isopropanol over a Rh catalyst has been studied. The kinetic behavior of this parallel system is described by a proposed reaction network. Keto-enol tautomeric transformation of adsorbed 4-tert-butyltetrahydrophenol and 4-tert-butylcyclohexanone is thought to be a key step, which governs the stereoselectivity of the overall complex reaction of alkylphenol hydrogenation.
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  • 2
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    Weinheim : Wiley-Blackwell
    Chemical Engineering & Technology - CET 20 (1997), S. 138-143 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The gas-phase hydrogenation of buta-1,3-diene to but-1-ene, trans- and cis-but-2-ene and butane has been performed over 0.5% Pd/γ-Al2O3 catalyst. The reaction has been investigated at atmospheric pressure and 0°C over a wide range of conversions. The kinetic model based on the present day knowledge of reaction mechanism has been advanced. The parameters of the kinetic model have been estimated through statistical data fitting. The kinetic model provides a fairly good description of selectivity in the whole range of conversions.
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  • 3
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    Weinheim : Wiley-Blackwell
    Chemical Engineering & Technology - CET 20 (1997) 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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  • 4
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    Weinheim : Wiley-Blackwell
    Chemical Engineering & Technology - CET 20 (1997), S. 149-161 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The following article concerns emulsification reaction in a continuous screw loop reactor. The influence of hydrodynamics on the emulsification process as well as the influence of some specific substances were examined. We produced oil/water model emulsions under different test conditions and we determined the correlations between the mixing behavior of the reactor and the characteristic features of the obtained emulsion. Special consideration was given to the droplet size and its distribution. Variable operating conditions of the reactor are the residence time and the rotational speed of the screw, both of which have a decisive influence on the recycle factor and the number of passages through the rotor/stator system. In addition we determined the dependence of the obtained droplet size distribution on the viscosity of the continuous and dispersed phase, on the interfacial surface tension and on the phase proportions. The influence of the specific type of emulsifying agent and its concentration has been examined as well. The positive effect of the mixing and of the recirculation on the emulsification in the screw loop reactor was particularly evident with low emulsifier concentrations and with emulsifiers with slow adsorption kinetics. The established theories for emulsion formation (Kolmogoroff, Taylor) were used for a quantitative description of the experimental results. The screw loop reactor was compared to an agitated tank reactor and a toothed-ring dispersing machine (Ultra Turrax) based on the comminution energy which is produced per unit volume of emulsion. The agitated tank reactor produced only coarsely dispersed emulsions through the entire rotational speed range, wheras the screw loop reactor and the Ultra Turrax, particularly at high rotational speeds and, therefore, high power densities, showed a similar emulsification and produced much finer dispersed emulsions.
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  • 5
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    Weinheim : Wiley-Blackwell
    Chemical Engineering & Technology - CET 20 (1997), S. 162-170 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The performance of an upflow packed-bed biofilm reactor has been analyzed under multisubstrate limitation by considering simultaneous carbon oxidation and nitrification reactions. The fasting shock load of inlet methanol concentration has a much more pronounced effect on the response of the system compared to that of inlet NH4+ -nitrogen concentration. The exit concentration of NH4+ -nitrogen drops very close to zero, thereby showing essentially complete nitrification during methanol fasting condition. Further, the concentration profiles of oxygen within the biofilm show significant variation during methanol fasting and nonfasting conditions whereas during NH4+ -nitrogen fasting conditions the oxygen concentration profile in the biofilm remains essentially unaffected.
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  • 6
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    Weinheim : Wiley-Blackwell
    Chemical Engineering & Technology - CET 20 (1997), S. 182-191 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The uncatalyzed esterification of acetic acid is described in the literature as a typical example of reactive distillation. Many rigorous models were validated using this esterification as an example. Process proposals for the production of pure ethyl acetate from ethanol and acetic acid have been determined using short-cut methods with the assumption of chemical equilibrium only. In this publication, the limitations of this esterification are clarified, using a rigorous model that was developed. The reasons why reactive distillation appears to be unfavorable for this esterification are explained. It is, however, theoretically possible to obtain ethyl acetate in high purity with different variants of the process. Different process variants are examined in this work. Construction variables that are important for the design of reactive columns, such as the number of reactive separation stages and the holdup in the column, are analyzed. Furthermore, the influence of variables dependent on the component system, such as the phase equilibrium of the reactive system and the reaction kinetics on the conversion in the column, are described. It can be shown that the short-cut methods published so far for reactive distillation, which assume chemical equilibrium, are inadequate.
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  • 7
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    Chemical Engineering & Technology - CET 20 (1997), S. 192-198 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Two devices were developed, mechanical and electrical, to measure the mechanical power relative to superficial gas velocity and stirring speed in a mechanically agitated reactor. Two bubble regimes were demonstrated. The study of gas holdup, obtained from the residence time distribution, and the bubble size, determined by interfacial area measurement, confirm these two regimes of flow. Our results show that the gas holdup, the interfacial area, and the liquid-side mass transfer coefficient are increasing functions of the energy dissipated in the solution.
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  • 8
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    Chemical Engineering & Technology - CET 20 (1997), S. 199-202 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An electrochemical technique which involved measuring the limiting current of the cathodic reduction of potassium ferricyanide was used to study the rate of mass transfer inside a cubical cavity machined in the wall of a vertical rectangular duct. Variables studied were side length, physical properties of the solution and flow rate of the solution. The mass transfer coefficient was found to decrease with increasing cavity size; in all cases, the mass transfer coefficient inside the cavity was less than that at the duct wall. Mass transfer data inside the cavity were correlated by the equation Shc = 0.525 (Sc Re de/L)0.33. Comparison of the present results with the results obtained using other cavity geometries shows that cavity geometry plays an important role in determining the rate of mass transfer inside the cavity.
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  • 9
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    Chemical Engineering & Technology - CET 20 (1997), S. 203-207 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Transient heat transfer in a mechanically agitated vessel is studied in the case of an anchor and an helical ribbon impeller using Newtonian and shear thinning fluids. Temperature stratification is found more pronounced with the anchor, making this impeller clearly inadequate for heat transfer. The impact of natural convection is evaluated first using the classical Gr/Re2 ratio. It is shown that the use of this criterion in viscous mixing is somewhat misleading. A new Grashof number is then proposed to assess the significance of the viscous and buoyancy effects in non-isothermal, non-Newtonian mixing applications. It is shown that the interpretation of this new number is strongly related to the concept of process viscosity.
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  • 10
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    Chemical Engineering & Technology - CET 20 (1997), S. 208-211 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The results of a process analysis and an experimental exploratory study of supercritical water oxidation (SCWO) show that elements of combustion technology are suitable to overcome the technical problems of SCWO. The Film Cooled Hydrothermal Burner (FCHB) which operates at 25 MPa up to 2000 K in the reaction zone keeping wall temperature under stress at 300 to 400 K shows further development potential of the Wallcooled Hydrothermal Burner (WHB) concept for SCWO, a still promising waste treatment process.
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  • 11
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    Chemical Engineering & Technology - CET 20 (1997), S. 212-219 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The Subnetwork Corollary provides some sufficient conditions for which a complex reaction network could be determined to have capacity of admitting multiple positive steady-states, if it contains a subnetwork that also admit multiple positive steady-states. A family of reaction networks, involving catalytic reactions in an isothermal continuous flow stirred tank reactor (CFSTR), is determined to have the capacity to exhibit steady-state multiplicity by implementation of the Deficiency One Algorithm and the Subnetwork Corollary. A set of rate constants and two corresponding positive steady-states are constructed for several cases.
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  • 12
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    Weinheim : Wiley-Blackwell
    Chemical Engineering & Technology - CET 20 (1997) 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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  • 13
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    Chemical Engineering & Technology - CET 20 (1997), S. 221-229 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: To review mass transfer trays from a process point of view, the dependence of efficiency on the loadings, the loading range and the maximum loadings with an acceptable tray efficiency have to be known. Comparing the results taken from experiments on Dualflex trays and from other types of trays which have been in industrial applications for many years and which are recognized as “industrial standard”, has been evaluated in this review.
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  • 14
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    Chemical Engineering & Technology - CET 20 (1997), S. 230-239 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In this contribution, a new method is proposed for determining effective macropore diffusion coefficients in porous media by digitized microphotographs of porous support materials and random walk simulations. The method introduced allows calculation of the effective diffusion coefficient as a function of the mean free path length over a wide variety of values. A versatile method for the preparation of porous substances for light microscopy is described.The frequently applied model of an active shell, which is used to model particle/solid collisions, was found to give incorrect results in conjunction with the application of the first passage time algorithm, which was applied to save computing time in the simulation of gas diffusion. It was possible to show that more realistic results are obtained if a Knudsen layer is used to model particle/solid collisions. Furthermore, in investigating diffusion in two- and three-dimensional representations of capillary tubes, it was found that results of simulations performed to calculate transport properties of fluids in porous media, based on two-dimensional model systems, cannot in any case be transferred to the corresponding three-dimensional systems.
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  • 15
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    Chemical Engineering & Technology - CET 20 (1997), S. 240-246 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The rate of the homogenous exothermic hydrolysis reaction of acetic anhydride catalyzed by sulfric acid in solvent acetic acid was estimated from nonisothermal experimental batch reactor transient temperature data. Rate equations based on three different reaction mechanisms of hydrolysis published in the literature were fitted to the experimental rate data. The experimental results on runaway and limit cycle behavior obtained with this reaction were explained by using the mechanism-based rate equations for hydrolysis in the reactor dynamic models, and good agreement was obtained between the predicted and the experimental dynamic data.
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  • 16
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    Chemical Engineering & Technology - CET 20 (1997), S. 247-258 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: New uses of artificial selective membranes, particularly ion-exchange membranes, improve on traditional methods of treating liquid mixtures before, during or after chemical or biochemical reactions. With the correct choice of ion-exchange membrane in a membrane reactor, reactions can be performed in such a way that the main product is not contaminated by undesired byproducts. Recent examples, mainly in organic chemistry, are given for eight typical ion-exchange membrane reactors: electrodialysis (ED), electrometathesis (EMT), electro-ion substitution (EIS), electro-ion injection-extraction (EIIE), coupled counter-transport (CCT), electro-electrodialysis (EED), electrohydrolysis with bipolar membranes (EHBM), and catalysis with ion-exchange membrane (IEMC).
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  • 17
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    Chemical Engineering & Technology - CET 20 (1997), S. 259-267 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In this study, a scale-down approach has been used for the simulation of the imperfect mixing on the growth processes by considering several configurations of continuous stirred tank reactor (CSTR, aerated) and plug flow tubular reactor (PFTR, not aerated). The steady-state concentrations of biomass and enzyme in a continuous culture were calculated as a function of dilution rate using modified Monod growth kinetics. A mathematical model for each combination of two bioreactors was developed to account for growth, substrate utilization (oxygen and glucose) and enzyme synthesis and decay. The model was then used to investigate biomass production and enzyme expression in relation to the volumetric fraction Uf = VPFTR/(VCSTR + VPFTR) and the recirculation ratio R = fr/(f + fr) of the fermentation system. These two mixing parameters were found to be significant factors in the biomass and enzyme production from the fermentation system. This model was also compared with some of the existing models.
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  • 18
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    Chemical Engineering & Technology - CET 20 (1997), S. 268-276 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: As an alternative to the existing bioheat transfer models a new system of two energy equations is proposed by considering the human body as a deformable porous medium. One equation is developed for the blood and the other for the peripheral skeletal tissue. It includes such significant factors as the vascular geometry and size, the blood flow and direction, thermal diffusion and the local thermal nonequilibrium between the blood and peripheral tissue. Discussion and application of both equations are given.
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  • 19
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    Chemical Engineering & Technology - CET 20 (1997), S. 282-284 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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  • 20
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    Chemical Engineering & Technology - CET 20 (1997), S. 277-281 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A new method for cleaning inner surfaces of pipes was studied both theoretically and experimentally. The method is based on the phenomenon of a sphere rotating in a pipe (levitation), when the translational movement of the sphere is restricted and the sphere is subjected to fluid flow in the pipe. The high rotation velocity causes a vibration process, which may be exploited for cleaning sediments or rust from the inner surfaces of pipes. A simplified theoretical model for the determination of the relationships among the dimensionless parameters governing the rotation phenomenon was developed. The model was validated with experimental data and found to be appropriate for engineering design of the system. Application of the cleaning method was demonstrated by cleaning the sediments and rust off the inner surface of a one-inch nominal diameter pipe.
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  • 21
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    Chemical Engineering & Technology - CET 20 (1997), S. 285-286 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An ortho-experiment design and the analysis method of mathematical statistics are adopted to study the conversion of gypsum and potassium chloride to potassium sulfate in the system of K+, Ca2+, NH4+ ‖ Cl-, SO42- in H2O. Optimal reaction parameters and engineering mean are acquired to attain a conversion yield of potassium chloride of 94.52%.
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  • 22
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    Chemical Engineering & Technology - CET 20 (1997), S. 414-418 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In the present work, we employ a fuzzy logic controller (FLC) to control the unstable state of a nonlinear biological reaction. The state variable vectors consist of cell density and substrate concentration. The dilution rate is used as a manipulated variable to control the reaction dynamics. An analytic form of FLC employing Zadeh AND logic along with Center of Mass defuzzification method is considered. Simulations reveal that for servo response test, the FLC shows satisfactory performance for natural unsteady states for which a conventional PI controller is known to fail. Further simulations also show that the FLC gives satisfactory regulatory response and is relatively insensitive to the deviations in model parameters.
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  • 23
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A ‘carbon source controlled shift technique’ was developed for fermentation medium optimization in continuous culture with the objective to maximize growth rate and growth-linked product formation of a biological system. An automatic culture medium preparation system was operated together with 2 parallel stirred tank reactors and a HPLC system for on-line analysis of the carbon source concentration in the reactors. A genetic algorithm was applied for experimental design. The concentrations of 7 medium components (mineral salts and vitamins) were optimized automatically within 40 continuous experiments to result in a maximum growth rate of the methylotrophic yeast Candida boidinii and growth-linked production of the formate dehydrogenase enzyme (FDH). The specific growth rate of Candida boidinii and the specific activity of the FDH enzyme at a set-point of 420 mM methanol in the reactor were, thus, improved by 19% to 0.16 h-1 and 26% to 164 U g-1, respectively, compared to the previously used medium, which has already been previously optimized in shake flask experiments. The results of the continuous medium optimization were evaluated with a full second order seven-dimensional polynomial model (regression coefficient 96.8%).
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  • 24
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    Chemical Engineering & Technology - CET 20 (1997), S. 419-423 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: By applying the macroscopic conservation laws to a simplified jet downstream from a sudden enlargement, a new correlation of the two-phase subcritical pressure recovery is obtained. Comparisons with the set of existing data (air-water and steam-water subcritical flows) show that the predictions obtained by means of this formula are more accurate than the ones given by available analytical models. The proposed correlation presents an important improvement of the pressure recovery predictions in the case of small mass velocities. However, it can not be applied in the conditions of quality too close to one.
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    Chemical Engineering & Technology - CET 20 (1997) 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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  • 26
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    Chemical Engineering & Technology - CET 20 (1997), S. 424-428 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In paper coating make-down, a poor dispersion of pigments in coating colors may lead to coater runnability problems. This is manifested by coat defects at the paper surface, excessive coater blade wear, and an over-consumption of pigments. For this reason, high shear impellers operated at high speed are used, yielding a high energy consumption. A new method to disperse high solids mix at low energy consumption is presented. This method based on the use of a rod impeller scraping the fluid surface in the vessel, is tested on a slurry composed of calcined and delaminated clays up to a solids content of 66.7 wt.% without dispersing aids.
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  • 27
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    Chemical Engineering & Technology - CET 20 (1997), S. 429-433 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: When in contact with water, organoalkoxysilanes and other alkoxy metal compounds react to organofunctionalized polysiloxanes or heteropolysiloxanes. A new method for the continuous preparation of porous organopolysiloxane spheres was developed. Droplets of the precursor mixture are injected into the vertical reactor column. Movement of the gelating droplets is controlled by flow of the aqueous reaction medium. Advantages are adjustable residence time, minimized coalescence and low reactor height. An example shows typical product characteristics like narrow particle size distribution and macroporosity.
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  • 28
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    Chemical Engineering & Technology - CET 20 (1997), S. 435-444 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: This paper describes how gain scheduling control is applied to a continuous stirred tank reactor model. The CSTR process, equipped with a cooling system, is modelled. Based on the resulting nonlinear model, a gain scheduling controller is designed. The gain scheduling follows a scheme denoted bias compensation. Compared to earlier reported gain scheduling schemes, the proposed scheme results in a controller that is less complex, which is advantageous in the controller implementation stage. Numerous simulations are performed, using the gain scheduling controller and two choices of control input to the reactor model. The simulation results indicate that a gain scheduling controller performs better than a linear controller. Simulations using different choices of control input to the reactor model indicate that proper process design is crucial for the controlled process performance.
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  • 29
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    Chemical Engineering & Technology - CET 20 (1997), S. 445-454 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Two different layouts for the liquid-liquid extraction section of an industrial caprolactam process are evaluated. Laboratory mass transfer measurements on streams obtained from an industrial and a demonstration plant with different extraction sections are interpreted by a model describing the effect of surface contaminants on mass transfer coefficients. Indications of the impact of these layouts on the complexity of the extraction section, quality of products and efficiency of the extraction processes are given.
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    Chemical Engineering & Technology - CET 20 (1997), S. 455-461 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A time- and space-dependent model based on the piston-dispersion-exchange model for liquid flow was developed to analyze the performance of two-phase upflow and downflow fixed bed reactors and was applied to the catalytic SO2 oxidation. The hydrodynamic parameters were determined from residence time distribution measurements, using an imperfect pulse method for time-domain analysis of nonideal pulse tracer response. A transient diffusion model of the tracer in the porous particle coupled with the PDE model was used to interpret the obtained RTD curves. Gas-liquid mass transfer parameters were determined by a stationary method based on the least square fit of the calculated concentration profiles in gas phase to the experimental values. It is shown that two-phase downflow fixed bed reactor performs better at low liquid flow rates, while two-phase downflow fixed bed reactor performs better at low liquid flow rates, while two-phase upflow performs better at high liquid flow rates.
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  • 31
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    Chemical Engineering & Technology - CET 20 (1997), S. 462-468 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The autoxidation of aqueous sulfide solutions by dioxygen is studied at pH 9 and 14 and at initial sulfide concentrations between 1 and 100 mM. Disulfide as a primarary intermediate is proposed to enhance the sulfide oxidation by autocatalytically forming polysulfies. The postulate is supported by the observed acceleration of the process at increasing pH favoring the presence of disulfide rather than that of sulfur. The final reaction products thiosulfate and sulfate are proposed to result from the hydrolysis of the highly instable intermediate polythiosulfite in parallel parallel reaction pathways, assuming probabilities for breaking the sulfur chain at the α (sulfate) and β (thiosulfate) positions to be responsible for the selectivity. A reaction scheme is proposed, considering all experimental observations.
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  • 32
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    Chemical Engineering & Technology - CET 20 (1997), S. 469-474 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Bubble columns are commonly used in industry for polluted gas treatment. Based on the same principle, the droplet column which is not widely known in the literature, uses much higher gas velocities, up to 14 m/s. This study concerns the hydrodynamics and mass transfer in this apparatus, in presence or absence of solid particles. Our results have demonstrated the impact of dusts on mass transfer performance giving rise to an increase in the kL aL coefficient with decreasing particle size. However, no influence of dust on the hydrodynamics of the column has been demonstrated within the studied particle size range.A study of liquid holdups obtained by three different methods is also carried out. Our results are comparable, thus validating the methods used.
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  • 33
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    Chemical Engineering & Technology - CET 20 (1997), S. 475-477 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A simple and new model for the prediction of drop velocity as a function of dispersed phase volume fraction has been proposed on the basis of experimental knowledge of onset time of complete separation between two phases as function of the initial hold-up.
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  • 34
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    Chemical Engineering & Technology - CET 20 (1997), S. 485-490 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A dynamic model of the liquid fluidized bed containing two or more solid particle species of different size and density is presented. The model incorporates the particle mass transport mechanisms of the convection and the dispersion. The movement of the upper interface of the bed subject to a change in the liquid velocity is specified using the mass balance constraint. The particle velocities and dispersion coefficients are evaluated using correlations. The model is capable of describing the bed expansion, concentration profiles of the individual particle species, the bulk density profile, and the occurrence of layer inversion.
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  • 35
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    Chemical Engineering & Technology - CET 20 (1997), S. 491-494 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Experiments were carried out in a conventional circulating fluidised bed to measure the axial pressure profile and total pressure drop, which covered a wide range of operating conditions. Material belonging to the Geldart A (fine material) as well as the Geldart B (course material) categories have been used in the present work. Slip velocity is determined from the total pressure drop and noticed that the slip velocity is much higher than the free fall velocity of single particle for Geldart A type material, while it is approximately equal to the free fall velocity of single particle for the Geldart B type materials.A model is developed for slip velocity taking into account all the hindrance effects: particle-particle, and particle-wall, and particle agglomeration. Predictions of the present model are validated with the data due to present study and the data reported in the literature.
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  • 36
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    Chemical Engineering & Technology - CET 20 (1997), S. 478-484 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Two important structural factors that affect distillation efficiencies, the outlet weir heigh and the liquid flowpath length, are investigated. Performance and efficiency data of an industrial scale i-butane/n-butane distillation column equipped with two-pass trays are used as a basis for the calculations. A mathematical development for a new method for predicting the numbers of vapor and liquid phase transfer units is given. This method together with some other NTU calculation methods is used to assess the effect of the outlet weir height on efficiencies. The effect of outlet weir height on the Murphree tray efficiencies is investigated using the observed point efficiencies and different point efficiency to the Murphree tray efficiency relation methods. The effect of varying liquid flowpath lengths on efficiencies is studied by calculating the Murphree tray efficiencies for one-pass and two-pass trays. The results obtained using the NTU calculation method presented in this study show that a certain outlet weir height point efficiency reaches its maximum. Most of the other methods give opposite results giving a minimum for point efficiency at a certain outlet weir length. The results also show that the Murphree tray efficiencies for one-pass trays are higher than for two-pass trays. Obviously, this is caused by the longer liquid flowpath length of one-pass trays. The Murphree tray efficiencies are also calculated for an industrial-scale MTBE purification column. The column is equipped with two-pass trays in the stripping section and with one-pass trays in the rectifying section. The Murphree tray efficiencies of one-pass trays are considerably higher than the two-pass tray Murphree tray efficiencies.
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  • 37
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    Chemical Engineering & Technology - CET 20 (1997), S. 495-501 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An algorithm for the computation of design variables in layer crystallisation processes is presented, based on an algebraic solution of the moving boundary equation for heat transfer, as well as on an expression for the concentration profile. The algorithm was applied to the discontinuous crystallisation of a NaCl-H2O solution around the wall of an internally cooled cylindrical tube. Good agreement between simulation results and laboratory experiments was observed. After input of experimentally measurable values of the distribution coefficient, the algorithm enables the prediction of the following process variables along the crystallisation time: layer thickness, temperature, and composition profiles across the layer, as well as the end-values of solid and liquid mass and concentrations. Multistage processes can be studied by the series association of crystallisation cycles, enabling the determination of the optimal number of stages that meets a specific design criterion.
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  • 38
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    Chemical Engineering & Technology - CET 20 (1997) 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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  • 39
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    Chemical Engineering & Technology - CET 20 (1997), S. 502-509 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Dust explosion hazard exists in plants and facilities wherever combustible dusts are hardled. Minimum explosible concentration of dust clouds is an important factor requiring special attention for hazard evaluation if any technological equipment is to be protected by inertisation. The mathematical models available for prediction of this parameter have been analysed for their application to organic dust clouds. Solution of the most general mode for determination of minimum explosible concentration of dust clouds proposed by Mitsui and Tanaka is presented, together with the comparison with experimental data. It has been found that the model is not successful in predicting the minimum explosible concentration for organic dusts. Recommendations on requirement of development of a new model for prediction of minimum explosible concentration of an organic dust such as polyethylen have been given.
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  • 40
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    Chemical Engineering & Technology - CET 20 (1997), S. 511-521 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: When working with disperse solid matter systems, one uses the effect of vibration in numerous processes. Solid matter mixing with vibration has only occurred in very simple units up to now. By means of the 3D-vibrational mixer from the company Kuston, Kleve, the influence of vibration on bulk materials and new mixing techniques are demonstrated. The 3D-vibrational mixer is suitable for liquids and solids, does not require mixing tools that need to be cleaned, and does not carry out rotary motions which would hinder incoming lines. It is used for mixing small amounts, where the mixing tank can be used simultaneously as the transportation container, so that a transfer is unnecessary.With the aid of 4 linear motors, the vibrational amplitudes and the frequencies can be varied within wide boundaries in all three spatial directions. By analyzing the vibrational system by means of Lissajous figures, it can be demonstrated that the optimal mixing effect occurs in the case of small frequency differences between the three axes. For freeflowing bulk materials, the best possible mixing state, the uniform coincidence mixing, is achieved after 2 min.
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  • 41
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    Chemical Engineering & Technology - CET 20 (1997), S. 522-532 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The intermixing of fluidizing gas between the compartments of a compartmented circulating gas fluidized bed fitted with a V-valve and riser combination has been experimentally studied. The intermixing of fluidizing gas that flows co-current (cross flow) as well as counter-current (back flow) to the circulating solids has been investigated. At low aerations, gas cross flow increased proportionally with the increase in solid circulation rate. But at high aerations, gas cross flow increased with aeration even when solid circulation decreased. Studies on back flow of gas revealed some interesting observations. At high fluidizing bed height on upstream side back flow of V-valve, gas has been negligible. But at low upstream bed heights and low aeration in V-valve and riser back flow of V-valve, gas has been substantial.
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  • 42
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    Chemical Engineering & Technology - CET 20 (1997), S. 17-22 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Mass transfer with chemical reaction by liquid/liquid phase tranfer catalysis (LLPTC) for an isothermal batch reactor was analyzed. The results for the phase transfer catalyzed reaction system can be generally described by a pseudo first-order hypothesis, whereas the reaction system can be controlled by simultaneous mass transfer of the catalysts between two liquid phases and chemical reaction in the organic phase. The mass transfer limitation is mainly from the mass transfer step of QX from the organic phase to the aqueous phase. The concept of catalyst-effectiveness vs. physically meaningful parameters in a liquid/liquid phase transfer catalyzed reaction is introduced. The catalyst effectiveness is increased as the mass transfer factors increase, the ratio of reaction rate coefficients of aqueous forward reaction to organic increases, and the equilibrium constant in the aqueous solution increases.
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    Chemical Engineering & Technology - CET 20 (1997), S. 171-181 
    ISSN: 0930-7516
    Keywords: Chemistry ; Industrial Chemistry and Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Hydrodynamic parameters have been determined in common equipment, i.e., same column and liquid and gas distributors, for cocurrent and countercurrent two-phase flow through fixed beds. The piston/dispersion exchange model (PDE) with usual Danckwerts' boundary conditions (closed/closed system) has been used to describe the liquid flow. A new imperfect pulse method has been used to estimate the PDE model parameters directly from the experimentally nonideal input and output response. The transition between trickle flow and pulse flow, for two-phase downflow, and the occurrence of flooding, for countercurrent flow, has been investigated using a macroscopic model for the two-phase flow.
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    Biotechnology and Bioengineering 55 (1997), S. 1-10 
    ISSN: 0006-3592
    Keywords: metal biosorption ; acetone-washed yeast biomass ; Saccharomyces uvarum ; lead binding mechanisms ; X-ray photoelectron spectroscopy ; Fourier transform infrared photoacoustic spectroscopy ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The mechanism of lead cation biosorption by acetone-washed biomass of Saccharomyces uvarum was investigated by chemical modifications and spectroscopic monitoring of the cell components. Reacting the carboxyl groups with propylamine, which neutralizes these anions, considerably decreased the metallic ion uptake, indicating that negatively charged carboxyl groups play an important role in lead bisorption due to electrostatic attraction. After lead biosorption the photoacoustic Fourier transform infrared spectroscopy showed a change in the symmetrical stretch of the carboxylate groups of the acetone-washed yeast biomass, and the X-ray photoelectron spectroscopy oxygen peak was also found to be shifted. These findings support the hypothesis that lead uptake occurs mainly through binding to the carboxyl group. In X-ray photoelectron spectroscopy the nitrogen peak decreased after the biosorption of lead, suggesting that nitrogen-containing groups are also involved in the biosorption process. Acylation of amino groups was shown to increase the lead biosorption capacity. The acylation reaction converts the positively charged amino group to an amide capable of coordination to lead cations. Deproteination by boiling the biosorbent with NaOH increased the lead uptake. The acetone-washed biomass uptake of lead from an aqueous solution at ph 5.5 was 48.9 mg/g dry weight. Pure chitin adsorbed 48.8 mg lead/g dry weight. Mannan isolated from S. uvarum did not adsorb lead at all. Electrostatic attraction of the carboxyl groups and other anions present in the acetone-washed biomass, and complexation with nitrogen atoms, especially in chitin, appear to be the main mechanisms involved in lead cation biosorption. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 1-10, 1997.
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    Biotechnology and Bioengineering 55 (1997), S. 16-27 
    ISSN: 0006-3592
    Keywords: uranium ; aluminum ; biosorption ; Rhizopus arrhizus ; mechanism ; competing ions ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Uranium competitive uptake experiments by Rhizopus arrhizus were carried out at three different solution pH levels and in the presence of different concentrations of competing aluminum ions in order to examine the competing ion effect. The coion effect became more pronounced as the coion concentration in solution and pH level increased. A preliminary examination of the effect of aluminum on the rate of uranium uptake was also completed. Results showed that the presence of aluminum does not interfere with the kinetics of uranium uptake by R. arrhizus. Electron microscopic and energy dispersive X-ray analyses were also performed on samples of the biomass. The combination of spectral data and the information from the equilibrium studies and the kinetic studies suggested that aluminum interferes with the uranium biosorptive uptake capacity of R. arrhizus by the precipitation of a metastable amorphous hydroxy polymeric precipitate through a mechanism we refer to as steric competition. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 16-27, 1997.
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    Biotechnology and Bioengineering 55 (1997), S. 28-32 
    ISSN: 0006-3592
    Keywords: Alcaligenes eutrophus ; poly(3-hydroxybutyrate) ; fed-batch fermentation ; phosphate limitation ; dissolved oxygen concentration ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: High cell density fed-batch fermentation of Alcaligenes eutrophus was carried out for the production of poly(3-hydroxybutyrate) (PHB) in a 60-L fermentor. During the fermentation, pH was controlled with NH4OH solution and PHB accumulation was induced by phosphate limitation instead of nitrogen limitation. The glucose feeding was controlled by monitoring dissolved oxygen (DO) concentration and glucose concentration in the culture broth. The glucose concentration fluctuated within the range of 0-20 g/L. We have investigated the effect of initial phosphate concentration on the PHB production when the initial volume was fixed. Using an initial phosphate concentration of 5.5 g/L, the fed-batch fermentation resulted in a final cell concentration of 281 g/L, a PHB concentration of 232 g/L, and a PHB productivity of 3.14 g/L · h, which are the highest values ever reported to date. In this case, PHB content, cell yield from glucose, and PHB yield from glucose were 80, 0.46, and 0.38% (w/w), respectively. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 28-32, 1997.
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    Biotechnology and Bioengineering 53 (1997), S. 10-16 
    ISSN: 0006-3592
    Keywords: microfiltration ; fouling ; yeast ; antifoam agents ; depressurization ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The fouling effects of yeast fermentation broths of Candida utilis in the presence of various commercial antifoam agents (PPG2000, B5600, and G832) up to 4.0 mL/L were studied, using Millipore polyvinylidene fluoride 0.22-μm hydrophilic membranes (GVWP), in a stirred-cell system at 50 kPa and 700 rpm. PPG2000, which has a low value of work of adhesion (Wa of 0.81 mN/m), gave a steady flux of broth of 29 L/(h m2) and was found to have no significant fouling effect on the microfiltration of broth. G832, which has a high Wa, (26.0 mN/m) reduced the flux of the broth to 17 L/(h m2); i.e., by 42% when only 1.0 mL/L was used. However, B5600, which has a Wa of 14.3 mN/m, was found to enhance the flux of broth to 54 L/(h m2); i.e., by 86%, due to the preferential adsorption of the B5600 components onto the hydrophobic cell contents released. These results were reinforced by the depressurization experiments performed with both hydrophilic (GVWP) and hydrophobic (GVHP) membranes, using both young and aged broths. B5600 was found to be the optimum antifoam agent in this study in terms of membrane performance and defoaming efficiency. © 1997 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 53 (1997), S. 21-25 
    ISSN: 0006-3592
    Keywords: starch fermentation ; recombinant yeast ; ethanol production ; glucoamylase activity ; fed-batch culture ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Alcohol fermentation of starch was investigated using a direct starch fermenting yeast, Saccharomyces cerevisiae SR93, constructed by integrating a glucoamylase-producing gene (STA1) into the chromosome of Saccharomyces cerevisiae SH1089. The glucoamylase was constitutively produced by the recombinant yeast. The ethanol concentration produced by the recombinant yeast was 14.3 g/L which was about 1.5-fold higher than by the conventional mixed culture using an amylolytic microorganism and a fermenting microorganism. About 60% of the starch was converted into ethanol by the recombinant yeast, and the ethanol yield reached its maximum value of 0.48 at the initial starch concentration of 50 g/L. The fed-batch culture, which maintains the starch concentration in the range of 30 to 50 g/L, was used to produce a large amount of ethanol from starch. The amount of ethanol produced in the fed-batch culture increased about 20% compared to the batch culture. © 1997 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 55 (1997), S. 909-920 
    ISSN: 0006-3592
    Keywords: baculovirus ; insect cells ; metabolism ; Sf-9; high five™ ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Nutrient utilization and byproduct accumulation were monitored in Spodoptera frugiperda Sf-9 and Trichoplusia ni BTI-Tn-5B1-4 (High Five™) cell lines during growth and following viral infection in suspension cultures in order to develop a better understanding of cell metabolism and to acquire information relevant to large scale fed-batch bioreactors. The utilization of glucose, dissolved oxygen, and amino acids were monitored in Sf-9 cell cultures grown in Sf-900 II serum-free medium (SFM) and in High Five™ cell cultures grown in both Sf-900 II and Express Five SFM. Using the optimal medium for each cell line, i.e., Sf-900 II SFM for Sf-9 cells and Express Five SFM for High Five™ cells, the cell growth rate, maximum cell density, specific glucose and glutamine utilization rates, and specific alanine production rate were comparable during cell growth. In addition, the expression level of recombinant human tissue plasminogen activator was comparable in the two cell lines on a per cell basis. It was found, however, that lactate and ammonia accumulated in High Five™ cell cultures, but not in Sf-9 cell cultures. In addition, High Five™ cells utilized asparagine more rapidly than glutamine, whereas Sf-9 cells consumed only minimal asparagine, and the oxygen utilization rate was significantly higher in High Five™ cell cultures. It was also found that the medium had a significant effect on High Five™ cell metabolism, e.g., the specific glucose utilization rate and the specific lactate and alanine production rates were significantly higher in Sf-900 II SFM than in Express Five SFM. In addition, the maximum cell density and specific asparagine utilization rate were significantly higher in Express Five SFM. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55:909-920, 1997.
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    Biotechnology and Bioengineering 55 (1997), S. 921-926 
    ISSN: 0006-3592
    Keywords: green fluorescent protein ; sensor ; on-line monitoring ; quantitation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We present an intensity based sensor designed for on-line monitoring of green fluorescent protein, a revolutionary marker of protein expression. The device consisted of a blue light emitting diode as the excitation source. A band pass excitation filter cut off light longer than 490 nm. The light was directed into a bifurcated optical fiber bundle with the common end inserted into a stainless steel housing equipped with a quartz window. The fiber bundle and stainless steel housing are steam sterilizable. The emission radiation was collected through a long wave pass filter to reject the excitation light shorter than 505 nm and was detected by a photomultiplier tube. The signal was amplified and sent to a computer for recording time course data. The sensor was tested in an Escherichia coli fermentation of JM105 transformed with pBAD-GFP. The on-line signal was compared to off-line fluorescence spectrophotometer measurements. The on-line profile closely followed the off-line. Western blot data showed that with a time shift, the sensor was able to both continuously and quantitatively monitor expression of green fluorescent protein on-line in real time. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55:921-926, 1997.
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    Biotechnology and Bioengineering 56 (1997), S. 1-8 
    ISSN: 0006-3592
    Keywords: transesterification ; hydrolysis ; water activity ; cutinase ; gas ; bioreactor ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Fusarium solani cutinase supported onto Chromosorb P was used to catalyze transesterification (alcoholysis) and hydrolysis on short volatile alcohols and esters in a continuous gas/solid bioreactor. In this system, a solid phase composed of a packed enzymatic preparation was continuously percolated with carrier gas which fed substrates and removed reaction products simultaneously. A kinetic study was performed under differential operating conditions in order to get initial reaction rates. The effect of the hydration state of the biocatalyst on the kinetics was studied for 3 conditions of hydration (aw = 0.2, aw = 0.4 and aw = 0.6), the alcoholysis of propionic acid methyl ester with n-propanol, and for 5 hydration levels (from aw = 0.2 to aw = 0.6) for the hydrolysis of propionic acid methyl, ethyl or propyl esters. F. solani cutinase was found to have an unusual kinetic behavior. A sigmoid relationship between the rate of transesterification and the activity of methyl propionate was observed, suggesting some form of cooperative activation of the enzyme by one of its substrate. For the hydrolysis of short volatile propionic acid alkyl esters, threshold effects on the reaction rate, highly depending on the water activity and the substrate polarity, are reported. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 1-8, 1997.
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    Biotechnology and Bioengineering 53 (1997), S. 372-378 
    ISSN: 0006-3592
    Keywords: glucose ; lactate ; on-line monitoring ; mammalian cell culture ; fermentation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: On-line monitoring and control of cell culture fermentation is important for optimal and consistent production of biologicals. In this work, glucose and lactate concentrations are monitored on-line using a commercially available analyzer (Model 2700, Yellow Springs Instruments, Yellow Springs, OH) during batch and perfusion hybridoma cell fermentation. Cell free samples from the reactor are obtained using a 0.45 μm hollow fiber filtering system placed in a circulation loop. The samples were analyzed at specified times and the data are collected on a computer. A process control strategy was developed to control the concentrations of glucose and lactate in a perfusion reactor where the feed rate is adjusted to maintain their concentrations at desired set points. Hybridoma cells (A10G10) were cultivated in a high density perfusion culture where cell density increased from 2 to 14 million cells/mL. During this period the control algorithm successfully adjusted the perfusion rate while maintaining constant glucose and lactate concentrations. Glucose consumption and lactate accumulation rates as well as net lactate yield on glucose were monitored continuously during perfusion culture. These metabolic rates were observed to be independent of cell concentration and were used for the estimation of viable cell density in the reactor. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 372-378, 1997.
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  • 53
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    Biotechnology and Bioengineering 53 (1997), S. 406-408 
    ISSN: 0006-3592
    Keywords: bioaffinity separation ; reverse micelles ; trypsin-trypsin inhibitor ; nonionic surfactant ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Trypsin inhibitor was converted to hydrophobic states by covalently combining cholesteryl groups using an acylation reaction, and was immobilized in reverse micelles composed of a nonionic surfactant. Using this reverse micellar phase containing trypsin inhibitor as an affinity ligand, trypsin was selectively separated with high recoveries from a mixture of several kinds of contaminating proteins by forward and backward extraction. No loss of activity of the recovered trypsin was observed through these operations. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 406-408, 1997.
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  • 54
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    Biotechnology and Bioengineering 53 (1997), S. 409-414 
    ISSN: 0006-3592
    Keywords: acylation ; pea isolate ; plant protein ; torus bioreactor ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Acetylation, which acts on the amino groups of proteins, allows to increase the solubility and the emulsifying properties of pea isolate. Acetylation by acetic anhydride was carried out in a torus microreactor in semibatch and continuous conditions. The mixing characteristics, obtained by a residence time distribution (RTD) method, are the same in batch and continuous processes. The maximum acetylation degree reached by the torus reactor is higher than with the stirred reactor. Torus reactors are more efficient than stirred ones as shown by a conversion efficiency, defined by the quantity of modified lysine groups by consumed acetic anhydride. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 409-414, 1997.
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  • 55
    ISSN: 0006-3592
    Keywords: malate dehydrogenase ; protein chromatography ; Saccharomyces cerevisiae ; direct extraction ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A novel technique for protein chromatography has been developed, which can be used to extract proteins from particulate-containing solutions (such as fermentation broths or preparations of disrupted cells) on a continuous basis, and delivers clarified streams of purified product. Adsorbents deployed in this type of contactor are based on PVA-coated perfluorocarbons derivitized with affinity ligands such as triazine dyes. In this article, we describe the application of this equipment for the continuous purification of malate dehydrogenase from an unclarified homogenate of Saccharomyces cerevisiae, using a Procion Red HE-7B-derivitized adsorbent. Although operating conditions were not optimized to produce a product of maximized purification factor, concentration, and yield, we have shown that MDH can be purified continuously in 78% yield at a rate of 70 U/min, with a purification factor of approximately 10. This corresponds to specific productivity of approximately 0.35 U/min per milliliter of settled adsorbent, a higher specific productivity than was feasible with the same adsorbent using expanded bed adsorption (EBA). © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 427-441, 1997.
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  • 56
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    Biotechnology and Bioengineering 53 (1997), S. 453-458 
    ISSN: 0006-3592
    Keywords: chemical permeabilization ; cell disruption ; urea ; EDTA ; Escherichia coli ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Extraction of intracellular protein from Escherichia coli is traditionally achieved by mechanical disruption. A chemical treatment that destroys the integrity of the bacterial cell wall and could provide an alternative technique is examined in this study. Treatment with a combination of the chelating agent ethylenediaminetet-raacetate (EDTA) (greater than 0.3 mM) and the chaotropic agent urea (6 M) is highly effective at releasing protein from uninduced E. coli. The 6 M urea in the presence of 3 mM EDTA can release cytoplasmic protein from both logarithmic-phase and stationary-phase E. coli cells at levels equivalent to mechanical disruption. The concentrations of the two chemical agents were the major variables affecting the maximum levels of protein release. Several minor variables and interactions were also identified. The kinetics of protein release is first order. For 2, 4, and 6 M urea with 3 mM EDTA, the time constant is approximately 2.5 min independent of urea concentration. Kinetics for 3 mM EDTA without urea is considerably slower, with a time constant of 12.3 min. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 453-458, 1997.
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  • 57
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    Biotechnology and Bioengineering 56 (1997), S. 130-137 
    ISSN: 0006-3592
    Keywords: manganese peroxidase ; Phanerochaete chrysosporium ; pulsed packed-bed bioreactor ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The bottleneck of the application of manganese peroxidase (MnP) on an industrial scale in pulp biobleaching or in degradation of hazardous compounds is the lack of an efficient production system. Three main problems arise for the continuous production of MnP during secondary metabolism of Phanerochaete chrysosporium: enzyme production occurs only under specific physiological conditions corresponding to C or N limitation, high O2 tension, and adequate Mn+2 concentration; the enzyme that is produced is destabilized by extracellular proteases; and excessive growth of the mycelium blocks effective oxygen transfer. To overcome these drawbacks, continuous production of MnP was optimized by selecting a suitable bioreactor configuration and the environmental and operating conditions affecting both enzyme production and stability. The combination between a proper feed rate and the application of a pulsation in a packed-bed bioreactor permitted the maintenance of continuous secretion of MnP while limiting mycelial growth and avoiding bed clogging. Environmental factors as an Mn+2 concentration of 5000 μM and high oxygen tension enhanced MnP production. The hydraulics of the bioreactor corresponding to a plug flow model with partial mixing and an operating hydraulic rentention time of 24 h were optimal to achieve stable operating conditions. This policy allowed long operation periods, obtaining higher productivities than the best reported in the literature. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 130-137, 1997.
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  • 58
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    Biotechnology and Bioengineering 53 (1997), S. 487-496 
    ISSN: 0006-3592
    Keywords: bacterial chemotaxis ; Escherichia coli ; random motility ; mathematical model ; sand core ; porous media ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The migration of chemotactic bacteria in liquid media has previously been characterized in terms of two fundamental transport coefficients - the random motility coefficient and the chemotactic sensitivity coefficient. For modeling migration in porous media, we have shown that these coefficients which appear in macroscopic balance equations can be replaced by effective values that reflect the impact of the porous media on the swimming behavior of individual bacteria. Explicit relationships between values of the coefficients in porous and liquid media were derived. This type of quantitative analysis of bacterial migration is necessary for predicting bacterial population distributions in subsurface environments for applications such as in situ bioremediation in which bacteria respond chemotactically to the pollutants that they degrade.We analyzed bacterial penetration times through sand columns from two different experimental studies reported in the literature within the context of our mathematical model to evaluate the effective transport coefficients. Our results indicated that the presence of the porous medium reduced the random motility of the bacterial population by a factor comparable to the theoretical prediction. We were unable to determine the effect of the porous medium on the chemotactic sensitivity coefficient because no chemotactic response was observed in the experimental studies. However, the mathematical model was instrumental in developing a plausible explanation for why no chemotactic response was observed. The chemical gradients may have been too shallow over most of the sand core to elicit a measurable response. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 487-496, 1997.
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  • 59
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    Biotechnology and Bioengineering 53 (1997), S. 515-522 
    ISSN: 0006-3592
    Keywords: RDX (hexahydro-1,3,5-trinitro-1,3,5-triazine ; Serratia marcescens ; biotransformation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The biotransformation of hexahydro-1,3,5-trinitro-1,3,5 triazine (RDX) has been observed in liquid culture by a consortium of bacteria found in horse manure. Five types of bacteria were found to predominate in the consortium and were isolated. The most effective of these isolates at transforming RDX was Serratia marcescens. The biotransformation of RDX by all of these bacteria was found to occur only in the anoxic stationary phase. The process of bacterial growth and RDX biotransformation was quantified for the purpose of developing a predictive type model. Cell growth was assumed to follow Monod kinetics. All of the aerobic and anoxic growth parameters were determined: μmax, Ks, and Yx/s. RDX was found to competitively inhibit cell growth in both atmospheres. Degradation of RDX by Serratia marcescens was found to proceed through the stepwise reduction of the three nitro groups to nitroso groups. Each of these reductions was found to be first order in both component and cell concentrations. The degradation rate constant for the first step in this reduction process by the consortium was 0.022 L/g cells · h compared to 0.033 L/g cells · h for the most efficient isolate. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 515-522, 1997.
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  • 60
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    Biotechnology and Bioengineering 53 (1997), S. 547-559 
    ISSN: 0006-3592
    Keywords: recombinant protein production ; protein folding ; protein secretion ; human antithrombin III ; Chinese hamster ovary cells ; serum-free culture ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Overexpression of recombinant proteins in animal cells is commonly achieved by using gene amplification techniques. Gene amplified cells possess up to several thousand genes coding for the target protein. Constitutive expression of these genes leads to high levels of the corresponding mRNA species and the immature protein in the cell. Inefficient processing of these precursors may result from their great abundance in the cell. To study the influence of elevated intracellular levels of a recombinant protein on its maturation and secretion, we examined the maturation and secretion of human antithrombin III (hATIII) in Chinese hamster ovary (CHO) cells at different levels of gene amplification. No loss of vitality was caused by elevated secretion of hATIII. As the intracellular hATIII content increased, the efficiency of hATIII secretion decreased steadily. The state of intracellular hATIII from the different cell lines was studied by determining the specific heparin cofactor activity of hATIII. Intracellular hATIII from the highest amplified cell line displayed a lowered specific heparin cofactor activity indicating the presence of malfolded, only partially folded, or incompletely or incorrectly posttranslationally modified hATIII in this cell line. Thus, the ability of CHO cells to fold and/or introduce posttranslational modifications and subsequently to secrete the recombinant protein becomes saturated, and therefore these processes may become limiting for protein secretion at highly elevated expression levels. This limitation was not due to a general exhaustion of the secretory capacity of the cells because hATIII constituted only a minor fraction of the secreted proteins, even at high expression levels. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 547-559, 1997.
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  • 61
    ISSN: 0006-3592
    Keywords: recombinant protein production ; Escherichia coli ; heparinase ; bioprocess simulation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Heparinase I from flavobacterium heparinum has several potential clinical applications; the resulting high demands on protein purity and quantity can be met by recombinant expression in Escherichia coli. Based on laboratory scale experiments with insoluble heparinase I expression followed by renaturation, a process for production of 3 kg/year of heparinase I was designed. We present a comparative analysis of the production costs of soluble and insoluble heparinase I expression, as well as a generalized approach to sensitivity analysis, based on perturbation around a base case design scenario. This may assist focusing further development on process steps for which improvements both are feasible and result in significant cost saving. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 575-582, 1997.
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  • 62
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    Biotechnology and Bioengineering 53 (1997), S. 594-600 
    ISSN: 0006-3592
    Keywords: CHO ; mammalian cells ; metalloproteinase ; recombinant protein production ; expression stability ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Stability of heterologous protein expression during production is critical for regulatory approval of vaccine and therapeutic products. Leishmania GP63, a zinc metalloproteinase that is a potential vaccine candidate, has been expressed on the surface of Chinese hamster ovary (CHO) cells. Flow cytometry was used to follow the stability of GP63 expression. Expression of proteolytically active GP63 (GP63WT) was unstable whether or not methotrexate (MTX) selection was maintained. In contrast, expression of an active site mutant (GP63E265D) was stable under MTX selection. In the absence of selection, the decline in GP63E265D expression was more gradual than the loss of GP63WT expression. Different molecular mechanisms accounted for these losses and resulted in higher growth rate nonproducer populations. A dynamic population model was used to calculate the conversion rates of GP63WT producers to nonproducers. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 594-600, 1997.
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  • 63
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    Biotechnology and Bioengineering 53 (1997), S. 583-593 
    ISSN: 0006-3592
    Keywords: bovine serum albumin ; α-chymotrypsin ; extraction ; lysozyme ; microemulsions ; reverse micelles ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The extraction of solid-phase α-chymotrypsin, bovine serum albumin (BSA), and lysozyme by water-in-oil microemulsion (w/o-ME) solution containing Aerosol-OT (AOT) was thoroughly examined as a means to maximize protein solubilization in organic solvent media. Protein extraction occurred simultaneously with the adsorption of water and AOT by the solid protein. Water and AOT were desorbed at nearly equal rates, suggesting that both materials were desorbed together as micreomulsions. The solubilization of protein increased linearly with the ratio of solid protein to extractant solution except at a high value of the ratio, where most protein-containing microemulsions were desorbed. Based on our results, a mechanistic model was developed to describe the solid-phase extraction procedure. First, microemulsions are desorbed from solution by the solid protein, resulting in the formation of a solid protein-AOT-water aggregate. Second, when a protein in the solid phase binds to a sufficient number of microemulsions, the resulting aggregate's increased hydrophobicity drives its solubilization into lipophilic solvent. Third, through the exchange of materials between the solubilized precipitate and the remaining microemulsions, protein-containing w/o-MEs are formed. The presence of adsorption is further indicated by an isotherm existing between the water, AOT, and protein content of the resulting solid phase for each protein. The driving force behind adsorption is either AOT-protein interactions or the protein's affinity for microemulsion-encapsulated water, depending on the properties of the protein and the size of the microemulsions, in agreement with the model of P. L. Luisi [Chimia, 44: 270-282 (1990)]. The second step of our model is mass transfer limited for the extraction of solid α-chymotrypsin and BSA. The extraction of solid lysozyme was limited by the occurrence of an irreversible precipitation process. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 583-593, 1997.
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  • 64
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    Biotechnology and Bioengineering 56 (1997), S. 268-278 
    ISSN: 0006-3592
    Keywords: Thermotoga maritima ; Methanococcus jannaschii ; hydrogen transfer ; hyperthermophiles ; coculture ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Interactions involving hydrogen transfer were studied in a coculture of two hyperthermophilic microorganisms: Thermotoga maritima, an anaerobic heterotroph, and Methanococcus jannaschii, a hydrogenotrophic methanogen. Cell densities of T. maritima increased 10-fold when cocultured with M. jannaschii at 85°C, and the methanogen was able to grow in the absence of externally supplied H2 and CO2. The coculture could not be established if the two organisms were physically separated by a dialysis membrane, suggesting the importance of spatial proximity. The significance of spatial proximity was also supported by cell cytometry, where the methanogen was only found in cell sorts at or above 4.5 μm in samples of the coculture in exponential phase. An unstructured mathematical model was used to compare the influence of hydrogen transport and metabolic properties on mesophilic and hyperthermophilic cocultures. Calculations suggest the increases in methanogenesis rates with temperature result from greater interactions between the methanogenic and fermentative organisms, as evidenced by the sharp decline in H2 concentration in the proximity of a hyperthermophilic methanogen. The experimental and modeling results presented here illustrate the need to consider the interactions within hyperthermophilic consortia when choosing isolation strategies and evaluating biotransformations at elevated temperatures. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 268-278, 1997.
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  • 65
    ISSN: 0006-3592
    Keywords: methanol sensor ; methanol monitoring and control ; methylotrophic yeast fermentation ; Pichia pastoris ; transferrin ; shake-flask cultures ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The methylotrophic yeast Pichia pastoris can be used to express recombinant genes at high levels under the control of the methanol-inducible alcohol oxidase 1 (AOX1) promoter. Accurate regulation of the methanol concentration in P. pastoris cultures is necessary to maintain induction, while preventing accumulation of methanol to cytotoxic levels. We developed an inexpensive methanol sensor that uses a gas-permeable silicone rubber tube immersed in the culture medium and an organic solvent vapor detector. The sensor was used to monitor methanol concentration continuously throughout a fed-batch shake-flask culture of a P. pastoris clone producing the N-lobe of human transferrin. The sensor calibration was stable for the duration of the culture and the output signal accurately reflected the methanol concentration determined off-line by HPLC. A closed-loop control system utilizing this sensor was developed and used to maintain a 0.3% (v/v) methanol concentration in the culture. Use of this system resulted in a fivefold increase in volumetric protein productivity over levels obtained using the conventional fed-batch protocol. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 279-286, 1997.
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  • 66
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    Biotechnology and Bioengineering 56 (1997), S. 287-294 
    ISSN: 0006-3592
    Keywords: specific growth rate ; hyphal morphometry ; Aspergillus niger ; surface growth kinetics ; glucose effect ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Development of surface grown cultures of Aspergillus niger no. 10 was studied at two experimental levels: (a) following the time course of the biomass density (X [=] mg cm-2) and fitting the data by the logistic expression, which yielded a macroscopic specific growth rate expressed as μobs = (dX/Xdt)[1-(X/Xmax)]-1; and (b) measuring morphometric parameters like the specific elongation rate (k) of the germ tubes and their diameters (Dh), the colony rate of radial extension (ur), and the mean length of distal hyphae (Lav) to estimate the specific growth rate with the following proposed expression: μcalc = urln2[Lavln(Lav/Dh)]-1. Increases in the initial glucose concentration (10, 40, 70, 120, 200, and 300 g L-1) caused reductions in the specific growth rates, the elongation kinetics of the germ tubes, and the hyphal diameter, nevertheless, ur and Xmax presented parabolic behavior, showing their maxima in the interval of 90 to 120 g L-1 of glucose. The overall macroscopic effect of the tested concentrations of glucose on surface grown cultures of A. niger was to produce densely packed and slowly extending colonies, where changes in hyphal lengths and diameters were significant. There was good agreement between μobs and μcalc values. Hence, this work validates a kinetic model based on morphometric data to estimate the specific growth rate of molds, obtained from dry weight data, using mold cultures grown in the same solid medium i.e., agar plates. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 287-294, 1997.
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  • 67
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    Biotechnology and Bioengineering 56 (1997), S. 295-303 
    ISSN: 0006-3592
    Keywords: three phase fluidized bed reactor ; immobilized biomass ; quinoline degradation ; Comamonas acidovorans ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Quinoline degradation by Comamonas acidovorans was investigated in a three phase fluidized bed reactor at dilution rates below and above the critical value (μmax = 0.42 h-1). Quinoline was used as the sole source of carbon, nitrogen, and energy. Two attachment carriers, polyurethane foam (Bayvitec®) and modified cellulose (Aquacel®), and a gel entrapment carrier (polyvinyl alcohol) were studied and compared with regard to their effectiveness to immobilize cells. Attachment and biofilm formation was best at higher dilution rates, regardless of carrier type used. Except for the maximum biomass concentration on the carrier, YV (biomass per volume of solid particles), there was no significant difference in reactor performance between the investigated carriers under stationary conditions. The highest value for YV was found for the gel entrapment carrier (YV = 35 g L-1). In a long-term run (66 days), the gel entrapment carrier established a permanent biofilm on the surface of the gel beads after 900 h of cultivation time. Complete quinoline mineralization was achieved at a dilution rate of 2.0 h-1, which is 4.7 times higher than the critical dilution rate. Identical substrate overloads were applied to the gel entrapment and the cellulose carrier by a step increase of the quinoline feed concentration at a dilution rate of 0.8 h-1 (D ∼2μmax). The cells survived the overload, but the accumulation of quinoline and quinoline degradation products and the degradation efficiency were different for the two systems during the overload, showing the influence of the carrier type on the dynamic performance and stability of the process. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 295-303, 1997.
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    Biotechnology and Bioengineering 56 (1997), S. 304-310 
    ISSN: 0006-3592
    Keywords: crossflow membrane filtration ; Escherichia coli ; high pressure homogenization ; inclusion bodies ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Crossflow membrane filtration was used to process recombinant Escherichia coli cell lysates containing protein inclusion bodies after high pressure homogenization. The number of passes through the high pressure homogenizer changed the viscosities and average particle sizes of the cell lysates. The different cell lysates were processed with a hollow fiber unit containing microfiltration membranes and a plate and frame unit with either ultrafiltration or microfiltration membranes. There were differences in permeate flux and protein transmission for the various membranes with the best performing membranes giving permeate fluxes greater than 60 L m-2 h-1 and protein transmissions greater than 90%. For a given membrane, no differences were observed between the cell lysates following homogenization with one, two, and three passes at 83 MPa. The lack of a difference between the three lysates is due to their similarities with respect to the released macromolecules and the presence of small (〈0.1 μm) cell debris. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 304-310, 1997.
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  • 69
    ISSN: 0006-3592
    Keywords: micelle ; water-soluble polymer ; protein extraction ; phase separation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A water-soluble polymer such as polyethylene glycol (PEG), Dextran T-500 (Dx), or diethylaminoethyl-Dextran (DEAE-Dx) induced aqueous micellar solutions of octyl-β-D-thioglucoside (OTG) to phase separation at 0°C. One of the two phases thus formed is a surfactant-depleted aqueous solution (aqueous phase) of a water-soluble polymer and the other a concentrated OTG solution (surfactant-rich phase). In a combination of OTG with PEG or Dx, cytochrome P450 (P450) and cytochrome b5 (b5) were well extracted into the surfactant-rich phase. The extraction yield of P450 was slightly greater than that of b5. In contrast to PEG and Dx, DEAE-Dx markedly reduced the extraction of b5, while that of P450 remained almost unchanged. DEAE-Dx served the dual functions of inducing the phase separation and preventing the extraction of b5 into the surfactant-rich phase. This depressed extraction of b5 was reversed by the addition of potassium phosphate. DEAE-Dx and potassium phosphate proved effective in controlling the extractability of b5. The polymer-induced phase separation provides a new basis for highly efficient extraction of membrane proteins under mild conditions that should be acceptable for thermolabile membrane proteins under physiological conditions. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 311-318, 1997.
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  • 70
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    Biotechnology and Bioengineering 56 (1997), S. 340-344 
    ISSN: 0006-3592
    Keywords: subtilisin ; chymotrypsin ; substrate specificity ; organic solvents ; lyophilized enzymes ; stereoselectivity ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A simple methodology has been successfully employed to explain the solvent dependence of the substrate specificity of enzymes in organic media. This methodology, which does not require the knowledge of the enzyme structure and is thus applicable to lyophilized and other noncrystalline enzyme preparations, predicts that the kcat/KM ratio for two substrates should be proportional to their Raoult's law activity coefficients. This approach has been validated for two enzymes, subtilisin Carlsberg and α-chymotrypsin, catalyzing the propanolysis of unnatural (in addition to natural) ester substrates in a variety of anhydrous solvents. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 340-344, 1997.
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  • 71
    ISSN: 0006-3592
    Keywords: Primatone RL ; sialylation ; interferon-γ ; serum substitutes ; cell ; CHO cell culture ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Although serum-free media have been widely used in mammalian cell culture for therapeutic protein production, the effects of serum-substitutes on product quality have not been extensively examined. This study observed an adverse effect of Primatone RL, an animal tissue hydrolysate commonly used as a serum-substitute to promote cell growth, on sialylation of interferon-γ (IFN-γ) derived from Chinese hamster ovary (CHO) cell culture in both batch and fed-batch modes. In batch cultures, decreased sialylation was observed at each of the glycosylation sites (i.e., Asn25 and Asn97) of IFN-γ with the use of elevated concentrations of the peptone. Although poorest sialylation was obtained with the use of a growth-inhibiting concentration of Primatone RL, diminished sialylation was observed at the optimal peptone concentration for cell growth and product yield. Since incubation of the product in Primatone RL-supplemented acellular medium did not result in decreased sialylation, the negative effect of Primatone RL could not be attributed to extracellular desialylation of IFN-γ by components of the peptone. In the fed-batch mode, a culture utilizing a serum-free feeding medium supplemented with Primatone RL demonstrated poorer sialylation than a similar culture not fed the peptone. The results of both the batch and fed-batch experiments indicate that the adverse effect of the peptone was not due solely to ammonia accumulation. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 353-360, 1997.
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    Biotechnology and Bioengineering 54 (1997), S. 535-542 
    ISSN: 0006-3592
    Keywords: fermentor monitoring ; mass spectrometer ; Pichia stipitis ; carbon dioxide ; yeast ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An in situ sterilizable plug-in membrane inlet mass spectrometer for monitoring dissolved gases and volatiles in fermentors was constructed and tested. The design ensured a minimal distance to be traveled by analyte molecules from the bulk of the fermentation broth to the ionization chamber of the mass spectrometer. Apart from the specific cross talk due to overlapping mass peaks from different compounds, we found that carbon dioxide interfered unspecifically with all the mass peaks of other substances, changing them by the same factor. The interference changed slowly with time and could be positive or negative depending on the history of the mass spectrometer. Also, the general sensitivity of the instrument changed slowly with time. These effects can be neglected or corrected for empirically in short-term measurements. When the fermentor was aerated with a three-component gas mixture including carbon dioxide, a rapid change in the partial pressure of carbon dioxide in the gas mixture gave rise to a transient in the signal of a gas whose partial pressure was kept constant. This effect revealed a transient change in the composition of the gas mixture in the bubbles caused by net import or export of carbon dioxide during equilibration with the new gas mixture. An experimental method to determine the effective partial pressures of gases in the bubbles during steady-state transport of carbon dioxide was designed. The plug-in membrane inlet mass spectrometer was tried as a probe for oxygen and ethanol in an oxystatic culture of the yeast Pichia stipitis. We found that it was possible to keep a steady-state concentration of as little as 0.5 μM throughout the lifetime of the culture. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 54: 535-542, 1997.
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    Biotechnology and Bioengineering 54 (1997), S. 543-548 
    ISSN: 0006-3592
    Keywords: biofilm reactor ; fluidized bed reactor ; dentrification ; nitrate ; nitrite ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A uniquely simple model is developed to describe the NO3- and NO2- concentration profiles within a dentrification fluidized bed biological reactor. This simple model is compared to experimental data, and to a more complex model similar to those previously proposed in the literature. The simple model fits the experimental data at least as well as the more complex model. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 54: 543-548, 1997.
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    Biotechnology and Bioengineering 54 (1997), S. 577-582 
    ISSN: 0006-3592
    Keywords: Streptomyces coelicolor A3(2) ; actinorhodin ; chemostat culture ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Streptomyces coelicolor was grown in variously limited chemostat cultures and the specific rate of extracellular actinorhodin production (qactinorhodin) was measured. The highest qactinorhodin values were observed in glucose- or ammonia-limited cultures, whereas almost no actinorhodin was produced in sulfate-, phosphate-, potassium-, or magnesium-limited cultures. The effect of the dilution rate on actinorhodin production was studied in glucose-limited cultures. It was found that qactinorhodin was highest at D = 0.06h-1, which was well below the maximal D value tested (0.14 h-1). This explains why, in batch cultures, actinorhodin production starts at the onset of the stationary phase. It was also found that the use of nitrilotriacetate instead of citrate as a chelating agent had a negative effect on actinorhodin production. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 577-582, 1997.
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  • 75
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    Biotechnology and Bioengineering 54 (1997), S. 567-576 
    ISSN: 0006-3592
    Keywords: continuous cultivation ; unstable steady state ; substrate inhibition ; phenol degradation ; Pseudomonas cepacia G4 ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Multiplicity of steady states of a continuous culture with an inhibitory substrate was used to estimate kinetic parameters under steady-state conditions. A continuous culture of Pseudomonas cepacia G4, using phenol as the sole source of carbon and energy, was overloaded by increasing the dilution rate above the critical dilution rate. The culture was then stabilized in the inhibitory branch by a proportional controller using the carbon dioxide concentration in the reactor exhaust gas as the controlled variable and the dilution rate as the manipulated variable. By variation of the set point, several unstable steady states in the inhibitory branch were investigated and the specific phenol conversion rates calculated. In addition, phenol degradation was investigated under substrate limitation (chemostat operation).The results show that the phenol degradation by P. cepacia can be described by the same set of inhibition parameters under substrate limitation and under high substrate concentrations in the inhibitory branch. Biomass yield and maintenance coefficients were identical. Fitting of the data to various inhibition models resulted in the best fit for the Yano and Koga equation. The well-known Haldane model, which is most often used to describe substrate inhibition by phenol, gave the poorest fit. The described method allows a precise data estimation under steady-state conditions from the maximum of the biological reaction rate up to high substrate concentrations in the inhibitory branch. Inhibition parameter estimation by controlling unstable steady states may thus be useful in avoiding discrepancies between data generated by batch runs and their application to continuous cultures which have been often described in the literature. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 54: 567-576, 1997.
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    Biotechnology and Bioengineering 54 (1997), S. 549-566 
    ISSN: 0006-3592
    Keywords: hybrid models ; neural networks ; penicillin G ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In the serial gray box modeling strategy, generally available knowledge, represented in the macroscopic balance, is combined naturally with neural networks, which are powerful and convenient tools to model the inaccurately known terms in the macroscopic balance. This article shows, for a typical biochemical conversion, that in the serial gray box modeling strategy the identification data only have to cover the input-output space of the inaccurately known term in the macroscopic balances and that the accurately known terms can be used to achieve reliable extrapolation. The strategy is demonstrated successfully on the modeling of the enzymatic (repeated) batch conversion of penicillin G, for which real-time results are presented. Compared with a more data-driven black box strategy, the serial gray box strategy leads to models with reliable extrapolation properties, so that with the same number of identification experiments the model can be applied to a much wider range of different conditions. Compared to a more knowledge-driven white box strategy, the serial gray box model structure is only based on readily available or easily obtainable knowledge, so that the development time of serial gray box models still may be short in a situation where there is no detailed knowledge of the system available. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 549-566, 1997.
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    Biotechnology and Bioengineering 55 (1997), S. 11-15 
    ISSN: 0006-3592
    Keywords: NIR spectroscopy ; bioreactor monitoring ; insect cell culture ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The purpose of this study was to develop non-invasive techniques to monitor the composition of cell culture media in insect cell bioreactors. Such a monitor could be used in conjunction with a fed-batch feeding scheme to ensure that cells are maintained in an optimal environment for growth and protein production. Glucose and glutamine concentrations in an insect cell culture bioreactor were determined off-line with near-infrared (NIR) absorption spectroscopy. Spectra were collected from 5000 to 4000 cm-1 with a 1.5-mm optical path length. Partial least squares (PLS) regression was applied to correlate the collected spectra with the concentration of the desired analytes. Under the culture conditions evaluated here, glucose and glutamine concentrations ranged from 38 to 55 mM and from 3 to 13 mM, respectively. Accurate measurements of glucose and glutamine in insect cell culture samples were possible over these entire ranges. The standard error of prediction (SEP) and mean percent error (MPE) for glutamine were 0.52 mM and 5.3%, respectively. Glucose could be measured with an SEP of 1.30 mM and an MPE of 2.3%. These levels of error are quite low considering the changing complexity of the growth media due to the shifting levels of amino acids, carbohydrates, yeastolate, proteins, and cell debris. This study represents an important step in the development of noninvasive on-line monitoring devices for cell culture bioreactors. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 11-15, 1997.
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    Biotechnology and Bioengineering 55 (1997), S. 33-40 
    ISSN: 0006-3592
    Keywords: anaerobic process control ; overload ; toxicity ; kinetic constant determination ; biosensor ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Process control of anaerobic reactors is difficult due to the complexity of the methabolic pathways in the microbial consortium and to the difficulty of detecting and monitoring process instability in short time, before the biomass is poisoned by incoming toxicants. Process control based on the Rantox biosensor is based on the following principle: the wastewater that can potentially induce an overload or contains a toxicant is first tested on a small “upstream” digester (the Rantox). This reactor makes possible to detect the potential instability and, if necessary, to divert the concentrated and/or contaminated wastewater to a buffer tank and consequently to protect the active biomass of the full-scale reactor. It is generally accepted that methanogens are the most sensitive microorganisms in anaerobic digestion. Among these bacteria, the acetoclastic methanogens are of primary importance because some 70% of the converted chemical oxyen demand (COD) mass flow passes through acetic acid. Therefore the first objective in the development of the Rantox biosensor has been to monitor the metabolism of acetoclastic methanogens in the presence of toxicants. This article presents the theoretical background required to evaluate the toxicity effects by determining the kinetic constants of the considered microorganisms from experimental data. The results of two series of calibration tests, performed in order to obtain a preliminary evaluation of the biosensor response to overload and toxicity conditions, are reported. In a second article, calibration tests will be described which refer to two prototypes of the biosensor tested in different operating conditions. The crucial point related to the Rantox, i.e., its comparison with a “normal” laboratory-scale digester to simulate a full-scale plant, will be the subject of the third (and last) article, which is planned to describe the development of this instrument. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 33-40, 1997.
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    Biotechnology and Bioengineering 55 (1997), S. 54-64 
    ISSN: 0006-3592
    Keywords: fluidized-bed adsorption ; dispersion ; particle diameter ; bed height ; frontal adsorption ; mass transport ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The influence of matrix properties and operating conditions on the performance in fluidized-bed adsorption has been studied using Streamline diethyl-aminoethyl (DEAE), an ion exchange matrix based on quartz-weighted agarose, and bovine serum albumin (BSA) as a model protein. Three different particle size fractions (120-160 μm, 120-300 μm, and 250-300 μm) were investigated. Dispersion in the liquid phase was reduced when particles with a wide size distribution were fluidized compared to narrow particle size distributions. When the mean particle diameter was reduced, the breakthrough capacities during frontal adsorption were enlarged due to a shorter diffusion path length within the matrix. At small particle diameters the effect of film mass transfer became more relevant to the adsorption performance in comparison to larger particles. Therefore matrices designed for fluidized-bed adsorption should have small particle diameter and increased mean particle density to ensure small diffusion path length in the particle and a high interstitial velocity to improve film mass transfer. Studies on the influence of sedimented matrix height on axial mixing showed an increased Bodenstein number with increasing bed length. Higher breakthrough capacities were also found for longer adsorbent beds due to reduced dispersion and improved fluid and particle side mass transfer. With increasing bed height the influence of flow rate on breakthrough capacity was reduced. For a settled bed height of 50 cm breakthrough capacities of 80% of the equilibrium capacity for flow rates varying from 3 to 9 cm/min could be achieved. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 54-64, 1997.
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    Biotechnology and Bioengineering 55 (1997), S. 82-90 
    ISSN: 0006-3592
    Keywords: toluene degradation ; xylene degradation ; Azoarcus tolulyticus ; nitrate reduction ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Groundwater from a xylene-contaminated acquifer was enriched in the laboratory in the presence of toluene, xylenes, ethylbenzene, and benzene. A pure culture that degrades toluene and m-xylene under nitrate-reducing conditions was isolated. Fatty acid analysis, 16S rRNA sequencing, and morphological traits indicate that the isolate was a strain of Azoarcus tolulyticus. The kinetics of toluene degradation under nitrate-reducing conditions by this isolate was determined. Nitrate reduction does not proceed beyond nitrite. Nitrate and toluene are substrate limiting at low concentrations, whereas toluene, nitrate, and nitrite are inhibitory at high concentrations. Several inhibition models were compared to experimental data to represent inhibition by these substrates. A kinetic model for toluene and nitrate degradation as well as for cell growth and nitrite production was developed and compared to experimental data. The results of this work may find important application in the remediation of groundwater aquifers contaminated with aromatic hydrocarbons. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 82-90, 1997.
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    Biotechnology and Bioengineering 55 (1997), S. 91-100 
    ISSN: 0006-3592
    Keywords: microfiltration ; membrane ; protein ; fouling ; filtration ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Recent studies of protein fouling have provided considerable insight into both the underlying fouling mechanisms and the mathematical description of the flux decline. However, most of the data have been obtained with a single model protein, making it difficult to generalize the results to commercially relevant process streams. Experiments were thus performed using a range of proteins with different physicochemical characteristics to determine the relationship between the protein structure and fouling behavior. Fouling in these systems occurred by two distinct mechanisms: deposition of large protein aggregates and chemical attachment of native proteins to the growing deposit. The chemical attachment generally occurred via the formation of intermolecular disulfide linkages involving a free sulfhydryl group in the native protein. Proteins without a free sulfhydryl group were typically unable to form these intermolecular linkages. The quasi-steady flux for the different proteins was proportional to the square of the protein surface charge density, consistent with a model in which protein deposition occurs when the drag force on the proteins associated with the convective filtrate flow is sufficient to overcome electrostatic repulsive interactions. These results clearly demonstrate the importance of the protein structure, charge, and reactivity in determining the rate and extent of protein fouling during microfiltration. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 91-100, 1997.
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    Biotechnology and Bioengineering 54 (1997), S. 142-152 
    ISSN: 0006-3592
    Keywords: insect cells ; baculovirus ; protein expression ; high cell density ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Per cell protein expression in virally-infected insect cells declines significantly at high cell density resulting in a decrease in volumetric productivity. Specific protein expression levels in Spodoptera frugiperda (Sf-21) cells could be increased at high cell densities by increasing the oxygen supply and by supplementing the medium with glutamine post-infection. β-Galactosidase yield was increased from 411 to 855 IU/ml by increasing the glutamine concentration in the medium by 46% and increasing the gas phase oxygen concentration from 21 to 80%. Similarly, the yield of a secreted alkaline phosphatase was increased from 14.2 to 26.2 IU/mL using the same conditions. Part of the increase in production with Sf-21 culture was due to increased release to the extra-cellular compartment at the higher oxygen concentrations. Increasing the gas phase oxygen concentration to 95% in conjunction with a 100% increase in glutamine and glucose concentrations did not improve the yield any further. Peak production under elevated oxygen and nutrient conditions occurred at 72 h about 24-48 h earlier than under normal conditions. In a Trichoplusia ni cell line (BTI-TN-5B1-4), the maximum secreted alkaline phosphatase activity was increased from 10 to 27.2 IU/mL by similarly manipulating the oxygen supply. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 54: 142-152, 1997.
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    Biotechnology and Bioengineering 55 (1997), S. 136-147 
    ISSN: 0006-3592
    Keywords: CHO cells ; glycosyl-phosphatidylinositol p97 concentration ; protein harvest ; controlled release ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Chinese hamster ovary (CHO) cells expressing the human melanoma tumour antigen, p97, were used to develop a controlled release process for the production of recombinant glycosyl-phosphatidylinositol (GPI) anchored proteins. The cells were cultured either in suspension or immobilized on porous microcarriers and p97 was selectively cleaved from the cell surface by the bacterial enzyme, phosphatidylinositol-phospholipase C (PI-PLC). The kinetics of p97 cleavage from the cell surface by PI-PLC was shown to be approximated by Michaelis-Menten kinetics. The recovered p97 concentrations were increased by reusing the PI-PLC enzyme solution to harvest multiple batches of cells. A convenient PI-PLC assay was developed to monitor the harvesting process and to determine the stability of PI-PLC under harvesting conditions. Although the Pl-PLC was stable under harvesting conditions, it rapidly adsorbed to the cell surface and was depleted from the reused enzyme solution. In order to maintain PI-PLC activity, it was necessary to add fresh PI-PLC to the reused enzyme solution before harvesting a fresh batch of cells. The maximum p97 concentration that could be obtained from harvesting CHO cells cultured on porous microcarriers was limited by the dilution effects of sample removal, adding fresh PI-PLC and liquid associated with settled microcarriers. A model was developed that adequately predicted the p97 concentration after each harvest and the maximum p97 concentration that could be achieved by this harvesting method. The dilution effects were minimized by harvesting from centrifuged suspension culture cells and the harvested p97 concentration was increased by over sixfold to 0.64 mg/mL. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 136-147, 1997.
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    Biotechnology and Bioengineering 55 (1997), S. 170-181 
    ISSN: 0006-3592
    Keywords: metabolic reaction model ; physiological state recognition ; Corynebacterium glutamicum ; lysine fermentation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A metabolic reaction model was developed for the lysine fermentation process by Corynebacterium glutamicum AJ-3462 to estimate the physiological state of the cells - that is, the growth and production activity, and the flux distribution of metabolites - from on-line measurable rates only. First, the extended Kalman filter was applied to eliminate noise in the measured rates. Then, using the metabolic reaction model, the lysine production rate and flux distribution were calculated. The estimation results allowed the physiological state of lysine production to be recognized, and an appropriate measure corresponding to the estimated state, such as intermittent addition of glucose and/or leucine, to be taken to maintain a high level of lysine productivity in batch culture. Finally, application of the recognition system enabled lysine to be produced from glucose at a higher yield than that from glucose- or leucine-limited exponential fed-batch cultures. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 170-181, 1997.
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    Biotechnology and Bioengineering 55 (1997), S. 399-407 
    ISSN: 0006-3592
    Keywords: lipase ; chiral kinetics ; organic solvent ; micelle ; emulsion ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Lipase from Pseudomonas cepacia was used for asymmetric hydrolysis of the substrate (±)1-chloro-2-acetoxy-3-(1-naphthyloxy)-propane, which is a precursor for (S)-(-)-β-blocker synthesis. Because this substrate is insoluble in water and partially soluble in hydrophobic solvents such as hexane and octane, a mixture of hydrophilic organic solvents and aqueous buffer was used to study the initial reaction rates. Because of the amphipathic nature of the substrate, it can remain in three different forms: (1) monomeric (solution); (2) micellar; and (3) emulsion, depending on the acetone and substrate concentrations in the medium. This behavior is presented in a phase diagram. The enzyme was found to be active with micelle as well as emulsion form of the substrate, whereas it showed negligible activity with the monomeric form. Michaelis-Menten constants were determined experimentally for the emulsion and micellar part of the substrate. The initial rate of hydrolysis (v0) goes through a maximum with respect to the acetone content of the mixture. It is due to the combined effect of various factors occurring simultaneously with the increase in acetone content in the solvent. These phenomena are discussed based on the interfacial activation of lipase, deactivation of the enzyme at very high acetone concentration, and increase in critical micelle concentration (CMC) and critical emulsion concentration (CEC) with the increase in acetone content in the solvent. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 399-407, 1997.
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    Biotechnology and Bioengineering 55 (1997), S. 390-398 
    ISSN: 0006-3592
    Keywords: γ-IFN ; sialylation ; glycosylation ; sialidase ; CHO cell culture ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Since sialic acid content is known to be a critical determinant of the biological properties of glycoproteins, it is essential to characterize and monitor sialylation patterns of recombinant glycoproteins intended for therapeutic use. This study reports site- and branch-specific differences in sialylation of human interferon-γ (IFN-γ) derived from Chinese hamster ovary (CHO) cell culture. Sialylation profiles were quantitated by reversed-phase HPLC separations of the site-specific pools of tryptic glycopeptides representing IFN-γ's two potential N-linked glycosylation sites (i.e., Asn25 and Asn97). Although sialylation at each glycosylation site was found to be incomplete, glycans of Asn25 were more heavily sialylated than those of Asn97. Furthermore, Man(α1-3) arms of the predominant complex biantennary structures were more favorably sialylated than Man(α1-6) branches at each glycosylation site. When the sialylation profile was analyzed throughout a suspension batch culture, sialic acid content at each site and branch was found to be relatively constant until a steady decrease in sialylation was observed coincident with loss of cell viability. The introduction of a competitive inhibitor of sialidase into the culture supernatant prevented the loss of sialic acid after the onset of cell death but did not affect sialylation prior to cell death. This finding indicated that incomplete sialylation prior to loss of cell viability could be attributed to incomplete intracellular sialylation while the reduction in sialylation following loss of cell viability was due to extracellular sialidase activity resulting from cell lysis. Thus, both intracellular and extracellular processes defined the sialic acid content of the final product. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 390-398, 1977.
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    Biotechnology and Bioengineering 55 (1997), S. 419-426 
    ISSN: 0006-3592
    Keywords: metabolic engineering ; glycogen synthesis ; glycogen degradation ; carbon metabolism ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In metabolic engineering, systems which allow coordinated control of two metabolic pathways can be useful. We designed two expression systems and demonstrated their application by coordinating glycogen synthesis and degradation. The first expression vector pMSW2 expressed the glycogen synthesis genes in one operon and the glycogen degradation gene in a separate, coordinately regulated operon. The plasmid was designed to switch off expression of the first operon and activate expression of the second operon on addition of IPTG. As an alternative means to control glycogen synthesis and degradation pathways, we constructed expression vector pGTSD100, which contains the native Escherichia coli glycogen synthesis and degradation operon under control of the tac promoter. Both expression vectors work successfully to control the net synthesis and degradation of glycogen. In cultures of the E. coli strain TA3476 carrying the plasmid pMSW2, before the addition of IPTG, glycogen continued to accumulate in the culture. About three hours after IPTG was added, glycogen levels began to decrease. When no IPTG was added to cultures of TA3476:pMSW2, glycogen accumulated in the cells as before but the rate of degradation of glycogen was much lower. When IPTG was added to TA3476:pMSW2, the total cell protein at the end of batch cultivation was approximately 15% higher compared to cultures without IPTG addition. The extra biomass was formed during the glycogen degradation phase. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 419-426, 1997.
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    Biotechnology and Bioengineering 55 (1997), S. 439-446 
    ISSN: 0006-3592
    Keywords: cell culture viability ; apoptosis ; IL-6 ; hybridomas ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Sp2/0 hybridoma cells die principally by apoptosis in batch culture. We have found that cultures of the Sp2/0 hybridoma exhibit increased viability in response to interleukin 6 (IL-6) supplementation relative to control cultures during serum shiftdown experiments. When shifted from a medium containing 10% fetal bovine serum (FBS) to a medium with 1% FBS, IL-6 supplemented cultures displayed viabilities and viable cell densities similar to control cultures containing 10% FBS. The degree of the survival response induced varied in accordance with the severity of the shiftdown, as cells resuspended in a high serum medium showed little observable enhancement in viability. The extension in culture viability was not accompanied by an observable decrease in growth relative to control cultures, indicating that the effect was not a consequence of growth inhibition. These results suggest the existence of serum components with behavior functionally similar to IL-6, with respect to enhancing cell survival, and that under certain experimental conditions IL-6 serves as a survival factor. In contrast to the extended viability displayed by cultures supplemented with IL-6, Sp2/0 cultures transfected with IL-6 cDNA expression vectors displayed a growth inhibitory response relative to control cultures. This inhibitory response was characterized by an extended lag phase following inoculation, and a decrease in batch culture cell yield. The depression in cell yield varied with serum concentration, with the largest depression occurring at high serum concentrations. We conclude that interactions between components in serum, presumably growth factors, and cytokines play an important role in altering the behavior of industrially relevant cell lines in culture. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 439-446, 1997.
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    Biotechnology and Bioengineering 55 (1997), S. 283-288 
    ISSN: 0006-3592
    Keywords: chloroperoxidase ; Caldariomyces fumago ; indole ; total turnover number ; space-time yield ; membrane reactor ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Chloroperoxidase from Caldariomyces fumago was applied for the oxidation of indole to oxindole using hydrogen peroxide as the oxidant in aqueous t-butyl alcohol medium. Different ways of adding the oxidant, various reactor types, and the use of a hydrogen peroxide-stat were compared, resulting in a 20-fold increase of the total turnover number (ttn) and space-time yield (sty). The highest ttn of 〉860,000 was obtained in a fed-batch reactor, whereas the highest sty of 120 g/(L · d) was reached in a continuously operated enzyme membrane reactor. The results were compared to other enzyme systems already established for the synthesis of amino acids and carbohydrates. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 283-288, 1997.
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    Biotechnology and Bioengineering 55 (1997), S. 480-489 
    ISSN: 0006-3592
    Keywords: pentachlorophenol ; Mycobacterium chlorophenolicum ; adsorption and desorption ; isotherm model ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The sorption behavior of pentachlorophenol (PCP) by the Gram-positive bacterium Mycobacterium chlorophenolicum PCP-1 was quantitatively characterized in this work, with emphasis on the effects of biomass and pH and on the reversibility of PCP adsorption. Both the adsorption and desorption of PCP showed a fast kinetic, reaching an equilibrium in less than 1.5-min mixing under the experimental conditions. For PCP concentrations up to 600 μmol/L no saturation of the adsorption was observed and the adsorption isotherms can be adequately described by the Freundlich equation. The adsorption capacity (qads) of M. chlorophenolicum PCP-1 increased significantly with decreasing biomass in the low concentration range (below 0.5 g/L). The biomass concentration merely affected the capacity constant K of the Freundlich model while the intensity parameter n remained constant. The qads also increased with decreasing pH, particularly at acidic pH values. Again, the pH effect was mainly reflected by the change of K. Based on these results a correlation for qads, in which K is a function of both biomass concentration and pH, was obtained to describe the adsorption isotherms at different biomass concentrations and pH values. The desorption of PCP was also found to be strongly affected by pH. At pH 5.4 the adsorption was almost completely irreversible, while a nearly complete desorption was obtained at pH 7. The effect of pH on the sorption behavior was found to be related to the ionization of PCP. The irreversibly adsorbed PCP is a strict function of concentration of undissociated PCP, while the reversibly adsorbed PCP correlates well with the concentration of ionic PCP. The irreversible adsorption has a much higher adsorption capacity than the reversible adsorption. These findings led to the derivation of a semimechanistic model that satisfactorily describes the sorption of PCP by M. chlorophenolicum. The results obtained also give clues to the patterns and mechanism(s) of PCP adsorption by microbial cells. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 480-489, 1997.
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  • 91
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    Biotechnology and Bioengineering 55 (1997), S. 497-504 
    ISSN: 0006-3592
    Keywords: glucose ; glucose oxidase ; biosensor ; on-line monitoring ; 1,1′-dimethylferrocene ; mammalian cells ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A flow injection analysis (FIA) biosensor system has been developed for on-line determination of glucose during mammalian cell cultivation. The culture sample was peristaltically withdrawn from the bioreactor and after cell separation by a steam sterilizable ceramic microfilter, the filtrate was continuously fed to the FIA mediated-biosensor system at 4 mLh-1, whereas the cell-containing retentate was recirculated to the bioreactor. In the amperometric biosensor system, glucose oxidase was covalently immobilized onto a preactivated nylon membrane and attached to the sensing area of a platinum working electrode. The enzyme reaction was coupled with the mediator 1,1′-dimethylferricinium (DMFe+)-cyclodextrin inclusion complex to recycle the reduced glucose oxidase to its original active state. 1,1′-Dimethylferrocene (DMFe) was then reoxidized to DMFe+ at the surface of the platinum electrode poised at + 0.15 V vs silver/silver chloride. The FIA mediated-biosensor was linear up to 6 mM glucose, with a detection limit of 0.1 mM, and possessed excellent reproducibility (± 0.4 %, 95 % confidence interval) over 123 repeated analyses during a 62 h continuous operation. The immobilized glucose oxidase was stable for up to 7 days when applied to glucose measurement during 5-10 day fed-batch cultivation of 293S mammalian cells. The results obtained from the mediated-biosensor system compared well with the hexokinase and HPLC data. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 497-504, 1997
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  • 92
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    Biotechnology and Bioengineering 56 (1997), S. 361-371 
    ISSN: 0006-3592
    Keywords: biofilms ; bioremediation ; toluene ; vapor phase bioreactors ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A Pseudomonas putida 54G biofilm was grown on toluene vapor supplied as the sole external carbon and energy source in a flat plate biofilm reactor. Enumerations of cells in the biofilm were made using culture techniques (selective and nonselective for toluene) and microscopic techniques (total and respiring cells), and an analysis of the progression of the state of the culture was made by examination of various fractions of the populations. Long-term exposure to higher levels of toluene produced the following trends: (i) lower fraction of total cells that respired; (ii) lower fraction of culturable cells that also grew on toluene; (iii) higher fraction of respiring cells that could not grow on toluene plates; and (iv) a relatively constant fraction of total cells that could not be cultured on toluene. Respiration rate was determined using oxygen microsensors, and the fraction of the total respiration that was not associated with toluene uptake increased with higher toluene exposure. A combination of cryosectioning and respiration rate data was used to demonstrate that more respiring cells and a higher respiration rate both occurred at the base of the film, suggesting a deterioration in physiological state with continued exposure to toluene. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 361-371, 1997.
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  • 93
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    Biotechnology and Bioengineering 56 (1997), S. 380-390 
    ISSN: 0006-3592
    Keywords: insect cells ; baculovirus ; bcl-2 ; recombinant proteins ; cell viability ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The effect of bcl-2 expression on cell viability and recombinant protein synthesis was investigated in the Spodoptera frugiperda Sf-9 and Trichoplusia ni BTI-Tn-5B1-4 (High Five™) insect cell lines. It was found that coinfection with a baculovirus expressing bcl-2 [Autographa californica nuclear polyhedrosis virus (AcNPV)-bcl2] extended the life span of High Five™ cells but not Sf-9 cells when compared to infection with recombinant baculoviruses expressing either human tissue plasminogen activator (AcNPV-tPA) or Escherichia coli β-galactosidase (AcNPV-βgal). Similar results were obtained in coinfection experiments; i.e., AcNPV-bcl2 coinfection increased the life span of High Five™ cells over that of cells infected with either AcNPV-tPA or AcNPV-βgal alone, but they did not affect the life span of coinfected Sf-9 cells. Coinfection of Sf-9 cells with AcNPV-bcl2 and AcNPV-βgal resulted in a decrease in the maximum β-gal expression levels of over 90% when compared to infection with AcNPV-βgal alone. A similar trend was found in the β-gal mRNA levels. Coinfection also resulted in a reduced β-gal expression level in High Five™ cells, but the reduction was consistent with what would be expected when two recombinant viruses compete for use of the cellular machinery. In contrast to the inhibitory effect of AcNPV-bcl2 coinfection on βgal expression, t-PA expression levels were either not affected (Sf-9 cells) or were increased 50% (High Five™ cells) over those obtained by infection with AcNPV-tPA alone. These results support the hypotheses that bcl-2 can inhibit transcription of genes under polyhedrin promoter control and that β-gal expression levels, but not t-PA expression levels, are controlled at the transcriptional level. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 380-390, 1997.
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  • 94
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    Biotechnology and Bioengineering 56 (1997), S. 398-421 
    ISSN: 0006-3592
    Keywords: Escherichia coli ; metabolism ; flux ; linear optimization ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A stoichiometric model of metabolism was developed to describe the balance of metabolic reactions during steady-state growth of Escherichia coli on glucose (or metabolic intermediates) and mineral salts. The model incorporates 153 reversible and 147 irreversible reactions and 289 metabolites from several metabolic data bases for the biosynthesis of the macromolecular precursors, coenzymes, and prosthetic groups necessary for synthesis of all cellular macromolecules. Correlations describing how the cellular composition changes with growth rate were developed from experimental data and were used to calculate the drain of precursors to macromolecules, coenzymes, and prosthetic groups from the metabolic network for the synthesis of those macromolecules at a specific growth rate. Energy requirements for macromolecular polymerization and proofreading, transport of metabolites, and maintenance of transmembrane gradients were included in the model rather than a lumped maintenance energy term. The underdetermined set of equations was solved using the Simplex algorithm, employing realistic objective functions and constraints; the drain of precursors, coenzymes, and prosthetic groups and the energy requirements for the synthesis of macromolecules served as the primary set of constraints. The model accurately predicted experimentally determined metabolic fluxes for aerobic growth on acetate or acetate plus glucose. In addition, the model predicted the genetic and metabolic regulation that must occur for growth under different conditions, such as the opening of the glyoxylate shunt during growth on acetate and the branching of the tricarboxylic acid cycle under anaerobic growth. Sensitivity analyses were performed to determine the flexibility of pathways and the effects of different rates and growth conditions on the distribution of fluxes. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 398-421, 1997.
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  • 95
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    Biotechnology and Bioengineering 56 (1997), S. 433-440 
    ISSN: 0006-3592
    Keywords: simple dissolution-reaction model ; enzymatic conversion ; solid substrate suspension ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Although reactions in substrate suspension are employed in industry for several bioconversion processes, there appears to be no quantitative model available in the literature to rationalize the optimization of these processes. We present a simple model that incorporates the kinetics of substrate dissolution and a simultaneous enzymatic reaction. The model was tested in the α-chymotrypsin-catalyzed hydrolysis of an aqueous suspension of dimethyl benzylmethylmalonate to a homogeneous solution of enantiomerically pure monoester. This reaction occurs in the bulk phase, so catalysis by enzyme absorbed at the solid-liquid interface plays no role. The value of the parameters in the model (i.e., the mass transfer coefficient of substrate dissolution (kL), the substrate solubility, and the rate constant for the enzymatic reaction) were determined in separate experiments. Using these parameter values, the model gave a good quantitative prediction of the rate of the overall dissolution-reaction process. When the particle size distribution is known, kL may also be calculated instead. The model seems to be applicable also for other poorly soluble substrates, other enzymes, and other solvents. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 433-440, 1997.
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  • 96
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    Biotechnology and Bioengineering 55 (1997), S. 831-840 
    ISSN: 0006-3592
    Keywords: isotopomer mapping matrix ; isotopomer modeling ; metabolic flux analysis ; 13C NMR ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Within the last decades NMR spectroscopy has undergone tremendous development and has become a powerful analytical tool for the investigation of intracellular flux distributions in biochemical networks using 13C-labeled substrates. Not only are the experiments much easier to conduct than experiments employing radioactive tracer elements, but NMR spectroscopy also provides additional information on the labeling pattern of the metabolites. Whereas the maximum amount of information obtainable with 14C-labeled substrates is the fractional enrichment in the individual carbon atom positions, NMR spectroscopy can also provide information on the degree of labeling at neighboring carbon atom positions by analyzing multiplet patterns in NMR spectra or using 2-dimensional NMR spectra. It is possible to quantify the mole fractions of molecules that show a specific labeling pattern, i.e., information of the isotopomer distribution in metabolite pools can be obtained. The isotopomer distribution is the maximum amount of information that in theory can be obtained from 13C-tracer studies. The wealth of information contained in NMR spectra frequently leads to overdetermined algebraic systems. Consequently, fluxes must be estimated by nonlinear least squares analysis, in which experimental labeling data is compared with simulated steady state isotopomer distributions. Hence, mathematical models are required to compute the steady state isotopomer distribution as a function of a given set of steady state fluxes. Because 2n possible labeling patterns exist in a molecule of n carbon atoms, and each pattern corresponds to a separate state in the isotopomer model, these models are inherently complex. Model complexity, so far, has restricted usage of isotopomer information to relatively small metabolic networks. A general methodology for the formulation of isotopomer models is described. The model complexity of isotopomer models is reduced to that of classical metabolic models by expressing the 2n isotopomer mass balances of a metabolite pool in a single matrix equation. Using this approach an isotopomer model has been implemented that describes label distribution in primary carbon metabolism, i.e., in a metabolic network including the Embden-Meyerhof-Parnas and pentose phosphate pathway, the tricarboxylic acid cycle, and selected anaplerotic reaction sequences. The model calculates the steady state label distribution in all metabolite pools as a function of the steady state fluxes and is applied to demonstrate the effect of selected anaplerotic fluxes on the labeling pattern of the pathway intermediates. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55:831-840, 1997.
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  • 97
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    Biotechnology and Bioengineering 55 (1997), S. 864-879 
    ISSN: 0006-3592
    Keywords: Corynebacterium glutamicum mutants ; transconjugation ; intracellular flux analysis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The physiology and central carbon metabolism of Corynebacterium glutamicum was investigated through the study of specific disruption mutants. Mutants deficient in phosphoenolpyruvate carboxylase (PPC) and/or pyruvate kinase (PK) activity were constructed by disrupting the corresponding gene(s) via transconjugation. Standard batch fermentations were carried out with these mutants and results were evaluated in the context of intracellular flux analysis. The following were determined. (a) There is a significant reduction in the glycolytic pathway flux in the pyruvate kinase deficient mutants during growth on glucose, also evidenced by secretion of dihydroxyacetone and glyceraldehyde. The resulting metabolic overflow is accommodated by the pentose phosphate pathway (PPP) acting as mechanism for dissimilating, in the form of CO2, large amounts of accumulated intermediates. (b) The high activity through the PPP causes an overproduction of reducing power in the form of NADPH. The overproduction of biosynthetic reducing power, as well as the shortage of NADPH produced via the tricarboxylic acid cycle (as evidenced by a reduced citrate synthase flux), are compensated by an increased activity of the transhydrogenase (THD) enzyme catalyzing the reaction NADPH + NAD+↔NADP+ + NADH. The presence of active THD was also confirmed directly by enzymatic assays. (c) Specific glucose uptake rates declined during the course of fermentation and this decline was more pronounced in the case of a double mutant strain deficient in both PPC and PK. Specific ATP consumption rates similarly declined during the course of the batch. However, they were approximately the same for all strains, indicating that energetic requirements for biosynthesis and maintenance are independent of the specific genetic background of a strain. The above results underline the importance of intracellular flux analysis, not only for producing a static set of intracellular flux estimates, but also for uncovering changes occurring in the course of a batch fermentation or as result of specific genetic modifications. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55:864-879, 1997.
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  • 98
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    Biotechnology and Bioengineering 55 (1997), S. 890-908 
    ISSN: 0006-3592
    Keywords: metabolic engineering ; N-linked glycosylation ; mathematical model ; CHO cells ; glycoform ; oligosaccharides ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Metabolic engineering of N-linked oligosaccharide biosynthesis to produce novel glycoforms or glycoform distributions of a recombinant glycoprotein can potentially lead to an improved therapeutic performance of the glycoprotein product. Effective engineering of this pathway to maximize the fractions of beneficial glycoforms within the glycoform population of a target glycoprotein can be aided by a mathematical model of the N-linked glycosylation process. A mathematical model is presented here, whose main function is to calculate the expected qualitative trends in the N-linked oligosaccharide distribution resulting from changes in the levels of one or more enzymes involved in the network of enzyme-catalyzed reactions that accomplish N-linked oligosaccharide biosynthesis. It consists of mass balances for 33 different oligosaccharide species N-linked to a specified protein that is being transported through the different compartments of the Golgi complex. Values of the model parameters describing Chinese hamster ovary (CHO) cells were estimated from literature information. A basal set of kinetic parameters for the enzyme-catalyzed reactions acting on free oligosaccharide substrates was also obtained from the literature. The solution of the system for this basal set of parameters gave a glycoform distribution consisting mainly of complex-galactosylated oligosaccharides distributed in structures with different numbers of antennae in a fashion similar to that observed for various recombinant proteins produced in CHO cells. Other simulations indicate that changes in the oligosaccharide distribution could easily result from alteration in glycoprotein productivity within the range currently attainable in industry. The overexpression of N-acetylglucosaminyltransferase III in CHO cells was simulated under different conditions to test the main function of the model. These simulations allow a comparison of different strategies, such as simultaneous overexpression of several enzymes or spatial relocation of enzymes, when trying to optimize a particular glycoform distribution. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55:890-908, 1997.
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  • 99
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    Biotechnology and Bioengineering 55 (1997), S. 940-940 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: No abstract.
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  • 100
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    Biotechnology and Bioengineering 55 (1997), S. 927-939 
    ISSN: 0006-3592
    Keywords: CHO cells ; human secreted alkaline phosphatase ; tumor suppressor genes ; green fluorescent protein ; cell cycle ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We have established a novel production process which allows up to fourfold higher production of a model secreted protein, the human secreted alkaline phosphatase (SEAP), in Chinese hamster ovary (CHO) cells. A cytostatic production phase is established in which cell proliferation is inhibited or completely abolished. Such a cytostatic production phase is established by overexpression of the tumor suppressor genes p21, p27, or p53175P (a p53 mutant showing specific loss of apoptotic function) under transcriptional control of a tetracycline-repressible promoter (PhCMV*-1). In order to minimize complications due to possible clonal variation of selected, stable cell lines, our investigations are based on transiently transfected subpopulations, that have become a useful tool in industrial R&D. These subpopulations have been selected by flow cytometry for the expression of genes encoded on a dicistronic expression vector. These vectors contain a dicistronic expression unit consisting of the genes encoding the green fluorescent protein (GFP) or SEAP, followed by one of the cytostatic genes p21, p27 or p53175P encoded by the second cistron. p21, p27 as well as p53175P block the cell cycle of CHO cells in the G1-phase for a prolonged period. However, these G1-arrested cells remain viable and proliferation proficient upon repression of expression of the cytostatic gene. All three of the cytostatic genes studied provided similar regulation of proliferation, and also similar enhancements in SEAP production, suggesting that higher productivity may be a general and intrinsic feature of G1-phase arrested CHO cells. Overall productivity is most likely enhanced because growth-arrested cells do not need to devote cellular resources to biomass production. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55:927-939, 1997.
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