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  • Cell & Developmental Biology  (25,032)
  • Biochemistry and Biotechnology  (13,095)
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  • 1
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 57 (1998), S. 127-135 
    ISSN: 0006-3592
    Keywords: membrane mass spectrometer ; kinetic measurements ; anaerobic biofilm ; acetate ; inhibition ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A small, stirred, 14.4-mL tank reactor was designed to serve as a measurement cell for short-term investigation of microbial kinetics. A mass spectrometer membrane probe allowed the measurement of the dissolved gases of hydrogen, methane, oxygen, and carbon dioxide. pH was measured by an electrode and controlled by addition of acid or alkali. The highly sensitive measurement of gases with low solubility allowed rapid measurements at very low conversion. In kinetic experiments, a stepwise increase of substrate concentration (method A) and continuous feed of substrate (method B) were used, allowing quick estimation of substrate kinetics. Acetate conversion in mixed culture biofilms from a fluidized bed reactor was investigated. Substrate inhibition was found to be negligible in the concentration range studied. Experiments at various pH values showed that the undissociated acid form was the kinetic determinant. Kinetic parameters for Haldane kinetics of protons were KSH = 1.3 × 10-5 mol m-3 and KIH = 8.1 × 10-3 mol m-3. With free acid (HAc) as the rate determining species, the kinetic parameters for method A were KSHAc = 0.005 mol m-3 and KIHAc = 100 mol m-3 and for method B were KSHAc = 0.2 mol m-3 and KIHAc = 50 mol m-3. The maximum biomass activity occurred at around pH 6.5. Acetate was exclusively converted to methane and CO2 at pH 〉 6. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 127-135, 1998.
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  • 2
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 57 (1998), S. 187-197 
    ISSN: 0006-3592
    Keywords: algal cultures ; photosynthetic efficiency ; light saturation effect ; spatial dilution of light ; Arthrospira (Spirulina) platensis ; tubular and flat photobioreactors ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The light saturation effect imposes a serious limitation on the efficiency with which solar energy can be utilized in outdoor algal cultures. One solution proposed to reduce the intensity of incident solar radiation and overcome the light saturation effect is “spatial dilution of light” (i.e., distribution of the impinging photon flux on a greater photosynthetic surface area), but consistent experimental data supporting a significant positive influence of spatial light dilution on the productivity and the photosynthetic efficiency of outdoor algal cultures have never been reported. We used a coiled tubular reactor and compared a near-horizontal straight tubular reactor and a near-horizontal flat panel in outdoor cultivation of the cyanobacterium Arthrospira (Spirulina) platensis under defined operating conditions for optimum productivity. The photosynthetic efficiency achieved in the tubular systems was significantly higher because their curved surface “diluted” the impinging solar radiation and thus reduced the light saturation effect. This interpretation was supported by the results of experiments carried out in the laboratory under continuous artificial illumination using both a flat and a curved chamber reactor. The study also showed that, when the effect of light saturation is eliminated or reduced, productivity and solar irradiance are linearly correlated even at very high diurnal irradiance values, and supported findings that outdoor algal cultures are light-limited even during bright summer days. It was also observed that, besides improving the photosynthetic efficiency of the culture, spatial dilution of light also leads to higher growth rates and lowers the cellular content of accessory pigments; that is, it reduces mutual shading in the culture. The inadequacy of using volumetric productivity as the sole criterion for comparing reactors of different surface-to-volume ratio and of the areal productivity for evaluating the performance of elevated photobioreactors operated outdoors is stressed; it is furthermore suggested that the photosynthetic efficiency achieved by the culture also be calculated to provide a suitable parameter for comparison of different algal cultivation systems operated under similar climatic conditions. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 187-197, 1998.
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  • 3
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 57 (1998), S. 211-215 
    ISSN: 0006-3592
    Keywords: protein ; conformational memory ; organic solvent ; molecular imprinting ; enzyme ; catalysis ; transition state analogue ; bovine serum albumin ; β-lactoglobulin ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The induction of catalytic activity in proteins by lyophilization in the presence of a transition state analogue (biomolecular imprinting) has been attempted. It was shown that proteins which were freeze-dried with n-isopropyl-4-nitrobenzyl-amine (a transition state analogue for the reaction of dehydrofluorination of 4-fluoro-4-[p-nitrophenyl] butan-2-one) displayed higher β-elimination activity as compared to their-non-imprinted counterparts. It was also found that native bovine serum albumin has a high dehydrofluorination activity towards the above substrate with kinetic parameters rather similar to those of a catalytic antibody prepared by Shokat et al. (1989). A comparison of the kinetic parameters determined in this study with those obtained for analogous catalytic antibodies and imprinted polymers was made. © 1998 John Wiley & Sons, Inc. Biotechnol. Bioeng. 57: 211-215, 1998.
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  • 4
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 57 (1998), S. 62-70 
    ISSN: 0006-3592
    Keywords: plasmid stability ; recombinant microorganism ; continuous culture ; Pseudomonas sp. B13 FR1 pFRC20P ; degradation of aromatic compounds ; chlorobenzoate ; methylbenzoate ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Plasmid stability of recombinant Pseudomonas sp. B13 FR1 pFRC20P, a strain capable of mineralizing 3- and 4-chlorobenzoate and 4-methylbenzoate, was investigated in continuous culture. The hybrid cosmid pFRC20P enables the strain to mineralize 4-methylbenzoate. Rapid plasmid loss was observed under nonselective conditions using 3-chlorobenzoate as the substrate. Plasmid stability decreased with increasing dilution rate. Despite the growth advantage of the generated plasmid free cells a total depletion of plasmid bearing cells was not observed. After approximately 50 generations the fraction of plasmid bearing cells reached a constant level of 10%, which was stably maintained during the next 25 generations. Cells from this stage were used to inoculate a new culture that resulted in a stable level of 50% plasmid bearing cells. By a temporary substrate change to selective conditions (4-methylbenzoate), this level could be further increased to 70%. Literature models on plasmid stability could not be applied to describe the experimental data. Therefore, a new but unstructured model was developed to describe the experimental results. The model is based on the existence of three subpopulations: a plasmid free one, an original plasmid bearing one with a growth disadvantage compared to plasmid free cells, and a second plasmid bearing subpopulation with increased stability that is generated from the original one and has a growth rate comparable to the plasmid free cells. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 62-70, 1998.
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  • 5
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 57 (1998), S. 79-86 
    ISSN: 0006-3592
    Keywords: Alcaligenes eutrophus ; hydrogenase ; NADH regeneration ; HLADH ; organic solvent ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A soluble NAD-dependent hydrogenase contained in Alcaligenes eutrophus was evaluated as a coenzyme regenerating catalyst in an organic-aqueous two-phase (predominantly organic) system. The horse-liver alcohol-dehydrogenase (HLADH) catalyzed reduction of cyclohexanone to cyclohexanol was used as a model reaction. The impact of different solvents (selected to span a large variety of principal properties) on the stability and activity of the HLADH, using substrate-driven regeneration, was studied. Solvents suitable for the HLADH were then selected for an evaluation of the hydrogenase-driven coenzyme regeneration. Hydrophobic solvents such as heptane, toluene, and 1,1,1-trichloroethane were found to be suitable for the coupled reactions catalyzed by HLADH and hydrogenase. Nonimmobilized cells, permeabilized with cetyl-trimethyl-ammonium bromide, were the most efficient preparation for the regeneration of NADH. The use of this preparation in heptane (10% water) was optimized with respect to the yield obtained in the HLADH-catalyzed reduction of cyclohexanone. Using the optimized conditions, yields of 99% cyclohexanol were obtained. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 79-86, 1988.
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  • 6
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 57 (1998), S. 95-108 
    ISSN: 0006-3592
    Keywords: Xanthan fermentation ; impeller type ; power consumption ; mixing ; oxygen transfer ; Xanthan productivity ; product quality ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The rheological complexity of Xanthan fermentations presents an interesting problem from a mixing viewpoint, because the phenomena of poor bulk blending and low oxygen mass transfer rates inherent in highly viscous fermentations (and their consequences) can be systematically investigated, even at the pilot plant scale. This study in a 150 L fermentor compares the physical and biological performance of four pairs of impellers: a standard Rushton turbine, a large diameter Rushton turbine, a Prochem Maxflo T, and a Scaba 6SRGT. Accurate in-fermentor power measurements, essential for the comparison of impellers in relation to operating costs are also reported. It is demonstrated that the agitator performance in Xanthan fermentations is very specific and the choice of which impeller to use in bioreactors to obtain enhanced performance is dependant on the applied criterion. None of the criterion favored the use of the standard Rushton turbine, therefore suggesting that there are strong grounds for retrofitting these impellers with either large diameter impellers of similar design or with novel agitators. In addition, fluid dynamic modeling of cavern formation has clearly highlighted the importance of a well mixed and oxygenated region for providing the capacity for high microbial oxygen uptake rates which govern Xanthan productivity and quality. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 95-108, 1998.
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  • 7
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 57 (1998), S. 121-125 
    ISSN: 0006-3592
    Keywords: sucrose monoester synthesis ; lipase-catalyzed acylation ; water activity (a w) ; regioselectivity ; salt hydrate pair ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Sucrose monoesters of a fatty acid were synthesized by using lipase in a solvent-free system. When lipase from Mucor miehei was used as a catalyst with capric acid as the donor and sugar as the acceptor, sucrose 6-monocaprate was predominantly produced in a yield of 25.3%. The yield of product was significantly increased by the direct addition of a suitable pair of solid salt hydrates to the reaction mixture to control the water activity (aw). Among the salt hydrate pairs investigated, the barium hydroxide, 8/1H2O pair resulted in the highest yield of the product. This salt addition method was also successfully employed for acylation of primary hydroxyl groups in various unprotected mono- and disaccharides such as glucose, galactose, fructose, trehalose, mannose, maltose, and lactose. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 121-125, 1998.
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  • 8
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 57 (1998), S. 118-120 
    ISSN: 0006-3592
    Keywords: biocompatibility ; microfabrication ; biohybrid organs ; immunoisolation ; Islets of Langerhans ; silicon ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A microfabricated silicon-based biocapsule for the immunoisolation of cell transplants is presented. The biocapsule-forming process employs bulk micromachining to define cell-containing chambers within single crystalline silicon wafers. These chambers interface with the surrounding biological environment through polycrystalline silicon filter membranes. The membranes are surface micromachined to present a high density of uniform pores, thus affording sufficient permeability to oxygen, glucose, and insulin. The pore dimensions, as small as 20 nm, are designed to impede the passage of immune molecules and graft-borne viruses. The underlying filter-membrane nanotechnology has been successfully applied in controlled cell culture systems (Ferrari et al., 1995), and is under study for viral elimination in plasma fractionation protocols. Here we report the encouraging results of in vitro experiments investigating the biocompatibility of the microfabricated biocapsule, and demonstrate that encapsulated rat neonatal pancreatic islets significantly outlive and outperform controls in terms of insulin-secretion capability over periods of several weeks. These results appear to warrant further investigations on the potential of cell xenografts encapsulated within microfabricated, immunoisolating environments for the treatment of insulin-dependent diabetes. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 118-120, 1998.
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  • 9
    Electronic Resource
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 57 (1998), S. 145-154 
    ISSN: 0006-3592
    Keywords: bioavailability ; PAH ; biodegradation ; dissolution ; hydrodynamic ; mixing ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The influence of hydrodynamic conditions on the dissolution rate of crystalline naphthalene as a model polycyclic aromatic hydrocarbon (PAH) was studied in stirred batch reactors with varying impeller speeds. Mass transfer from naphthalene melts of different surface areas to the aqueous phase was measured and results were modeled according to the film theory. Results were generalized using dimensionless numbers (Reynolds, Schmidt, and Sherwood). In combined mass transfer and biodegradation experiments, the effect of hydrodynamic conditions on the degradation rate of naphthalene by Pseudomonas 8909N was studied. Experimental results were mathematically described using mass-transfer and microbiological models. The experiments allowed determination of mass-transfer and microbiological parameters separately in a single run. The biomass formation rate under mass transfer limited conditions, which is related to the naphthalene biodegradation rate, was correlated to the dimensionless Reynolds number, indicating increased bioavailability at increased mixing in the reactor liquid. The methodology presented in which mass transfer processes are quantified under sterile conditions followed by a biodegradation experiment can also be adapted to more complex and realistic systems, such as particulate, suspended PAH solids or soils with intrapartically sorbed contaminants when the appropriate mass-transfer equations are incorporated. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 145-154, 1998.
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  • 10
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 57 (1998), S. 136-144 
    ISSN: 0006-3592
    Keywords: down-flow fluidization ; bed expansion ; biofilm ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: This article describes the bed expansion characteristics of a down-flow anaerobic fluidized bed reactor treating a synthetic wastewater. Experiments were carried out in a 0.08 m diameter and 1 m length PVC column. The carrier used was ground perlite (an expanded volcanic rock). Particles characteristics were 0.968 mm in diameter, specific density of 213 kg · m-3 and Umf (minimal fluidization velocity): 2.3 m · h-1. Experimental data of terminal velocities and bed expansion parameters at several biofilm thicknesses were compared to different models predicting the bed expansion of up-flow and down-flow fluidized beds.Measured bed porosities at different liquid superficial velocities for the different biofilm thicknesses were in agreement with the Richardson-Zaki model, when Ut (particle terminal velocity) and n (expansion coefficient) were calculated by linear regression of the experimental data. Terminal velocities of particles at different biofilm thicknesses calculated from experimental bed expansion data, were found to be much smaller than those obtained when Cd (drag coefficient) is determined from the standard drag curve (Lapple and Sheperd, 1940) or with others' correlations (Karamanev and Nikolov, 1992a,b). This difference could be explained by the fact that free-rising particles do not obey Newton's law for free-settling, as proposed by Karamanev and Nikolov (1992a,b) and Karamanev et al. (1996). In the present study, the same free-rising behavior was observed for all particles (densities between 213 and 490 kg · m-3). © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 136-144, 1998.
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  • 11
    ISSN: 0006-3592
    Keywords: hybridoma ; futile cycling ; hollow fiber bioreactor ; glutamine ; NMR ; C-13 ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The effect of changes in extracellular glutamine level on metabolism of a murine hybridoma was examined with in vivo nuclear magnetic resonance (NMR) spectroscopy. Cells were cultured in a hollow-fiber bioreactor at high cell density to allow intracellular metabolite levels to be determined on a metabolically relevant time scale. Steady infusions of [1-13C] glucose were used to label glycolytic and tricarboxylic acid cycle intermediates, which permitted continuous monitoring with NMR spectroscopy during changes in environmental glutamine level. Samples of the extracellular medium were also analyzed to determine the effect of glutamine on other metabolites associated with primary and secondary metabolism. The changes in glutamine concentration had several effects on primary and secondary metabolism, depending on the rate the changes were made. For a brief reduction in feed glutamine concentration from 4 to 0 mM (which produced a rapid change from 0.67 to ∼0 mM in residual glutamine), large changes were observed in the rate of consumption of metabolites normally associated with energy production. Antibody synthesis was strongly stimulated and nitrogen metabolism was significantly altered. For a more prolonged reduction from 2.4 to 1.2 mM (which produced a slower reduction from 0.30 to 0.08 mM in residual glutamine), much smaller changes were observed even though the concentration of glutamine at the reduced feed level was very low. Energy metabolism did not appear to be limited by glutamine at 0.08 mM, which suggests that significant futile cycling may occur in energy producing pathways when excess glucose and glutamine are available. However, this concentration of extracellular glutamine appeared to affect some anabolic pathways, which require amino groups from glutamine. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 172-186, 1998.
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  • 12
    Electronic Resource
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 57 (1998), S. 198-210 
    ISSN: 0006-3592
    Keywords: Xanthan fermentation ; agitator speed ; caverns ; dissolved oxygen ; specific oxygen uptake rate ; specific Xanthan production rate ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Agitation speed affects both the extent of motion in Xanthan fermentation broths because of their rheological complexity and the rate of oxygen transfer. The combination of these two effects causes the dissolved oxygen concentration and its spatial uniformity also to change with agitator speed. Separating these complex interactions has been achieved in this study in the following way. First, the influence of agitation speeds of 500 and 1000 rpm has been investigated at a constant nonlimiting dissolved oxygen concentration of 20% of air saturation using gas blending. Under these controlled dissolved oxygen conditions, the results demonstrate that the biological performance of the culture was independent of agitation speed as long as broth homogeneity could be ensured. With the development of increasing rheological complexity lending to stagnant regions at Xanthan concentrations 〉20 g/L, it is shown that the superior bulk mixing achieved at 1000 rpm, compared with 500 rpm, leading to an increased proportion of the cells in the fermentor to be metabolically active and hence higher microbial oxygen uptake rates, was responsible for the enhanced performance. Second, the effects of varying dissolved oxygen are compared with a control in each case with an agitator speed of 1000 rpm to ensure full motion, but with a fixed, nonlimiting dissolved oxygen of 20% air saturation. The specific oxygen uptake rate of the culture in the exponential phase, determined using steady-state gas analysis data, was found to be independent of dissolved oxygen above 6% air saturation, whereas the specific growth rate of the culture was not influenced by dissolved oxygen, even at levels as low as 3%, although a decrease in Xanthan production rate could be measured. In the production phase, the critical oxygen level was determined to be 6% to 10%, so that, below this value, both specific Xanthan production rate as well as specific oxygen uptake rate decreased significantly. In addition, it is shown that the dynamic method of oxygen uptake determination is unsuitable even for moderately viscous Xanthan broths. © 1998 John Wiley & Sons, Inc. Biotechnol. Bioeng. 57: 198-210, 1998.
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  • 13
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 57 (1998), S. 216-219 
    ISSN: 0006-3592
    Keywords: liposomes ; vesicles ; microreactor ; permeability ; chymotrypsin ; enzyme ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Liposomes were prepared from 1-palmitoyl-2-oleoyl-sn-glycero-3-phosphocholine (POPC), which contained the water soluble proteinase α-chymotrypsin. This liposome entrapped enzyme showed selectivity for externally added substrates in that only small substrates (benzoyl-l-Tyr-p-nitroanilide or acetyl-l-Phe-p-nitro-anilide) - for which the liposome bilayer was permeable - were transformed into products. Large substrates (succinyl-l-Ala-l-Ala-l-Pro-l-Phe-p-nitroanilide or casein) could not penetrate from the external aqueous phase into the liposomes, and were not hydrolyzed. This substrate selectivity is entirely based on the compartimentation and permeability properties of the liposome microreactor. © 1998 John Wiley & Sons, Inc.Biotechnol. Bioeng. 57: 216-219, 1998.
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  • 14
    ISSN: 0006-3592
    Keywords: depolymerization ; kinetics ; endo -enzymes ; theoretical equation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Monitoring the time evolution of the concentration of a selected range of molecular weights of substrate, referred to as “detectable” substrate, has been used to determine endo-enzymic activities in polysaccharide depolymerizing processes. In the methodologies based on the use of dye-labeled substrates, the “detectable” substrate extends from a given molecular weight threshold downward. On the contrary, in the fluorescent probe-flow injection analysis methodology, initially developed to determine (1 → 3)-(1 → 4)-β-d-glucanase activities, the “detectable” substrate extends from a given molecular weight threshold upward. Assuming that the time evolution of the molecular weight distribution of the substrate follows the most probable distribution (the enzymic attack is random and its mechanism is single attack), a theoretical equation describing the time evolution of the concentration of “detectable” substrate (from a given molecular weight threshold upward or downward) has been deduced. This equation, Wd = Wo · (1 + αt) · e-αt, where Wd is the concentration of “detectable” substrate, Wo is the initial concentration of the substrate, t is the depolymerization time, and α is a parameter correlated through a hyperbola with the initial concentrations of enzyme and substrate and the Michaelis-Menten constant, Km, has been tested against different (1 → 3)-(1 → 4)-β-d-glucan/(1 → 3)-(1 → 4)-β-d-glucanase systems using the fluorescent probe-flow injection analysis methodology and Calcofluor as the fluorescent probe. The most important predictions of the theoretical equation, which allow accurate determination of both endo-enzymic activities and kinetic constants, have been experimentally confirmed. ©1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 387-393, 1998.
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  • 15
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    Biotechnology and Bioengineering 57 (1998), S. 394-408 
    ISSN: 0006-3592
    Keywords: pH gradient ; pH control ; urease ; immobilized enzyme system ; sequential reactions ; acid-generating reaction ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An optimal pH control technique has been developed for multistep enzymatic synthesis reactions where the optimal pH differs by several units for each step. This technique separates an acidic environment from a basic environment by the hydrolysis of urea within a thin layer of immobilized urease. With this technique, a two-step enzymatic reaction can take place simultaneously, in proximity to each other, and at their respective optimal pH. Because a reaction system involving an acid generation represents a more challenging test of this pH control technique, a number of factors that affect the generation of such a pH gradient are considered in this study. The mathematical model proposed is based on several simplifying assumptions and represents a first attempt to provide an analysis of this complex problem. The results show that, by choosing appropriate parameters, the pH control technique still can generate the desired pH gradient even if there is an acid-generating reaction in the system. ©1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 394-408, 1998.
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  • 16
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    Biotechnology and Bioengineering 58 (1998), S. 345-355 
    ISSN: 0006-3592
    Keywords: cyclodextrin ; polychlorobiphenyl ; chlorobenzoic acid ; soil ; bioremediation ; biodegradation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The possibility of enhancing the intrinsic ex-situ bioremediation of a chronically polychlorinated biphenyl-contaminated soil by using cyclodextrins was studied in this work. The soil, contaminated with a large array of polychlorinated biphenyls and deriving from a dump site where it has been stored for about 10 years, was found to contain indigenous cultivable aerobic bacteria capable of utilising biphenyl and chlorobenzoic acids. The soil was amended with inorganic nutrients and biphenyl, saturated with water, and treated in aerobic batch slurry- and fixed-phase reactors. Hydroxypropyl-β-cyclodextrin and γ-cyclodextrin, added to both reactor systems at the concentration of 10 g/L at the 39th and 100th days of treatment, were found to generally enhance the depletion rate and extent of the soil polychlorobiphenyls. Despite some abiotic losses could have affected the depletion data, experimental evidence, such as the production of metabolites tentatively characterized as chlorobenzoic acids and chloride ion accumulation in the reactors, indicated that cyclodextrins significantly enhanced the biological degradation of the soil polychlorobiphenyls. This result has been ascribed to the capability of cyclodextrins of enhancing the availability of polychlorobiphenyls in the hydrophilic soil environment populated by immobilised and suspended indigenous soil microorganisms. Both cyclodextrins were metabolised by the indigenous soil microorganisms at the concentration at which they were used. Therefore, cyclodextrins, both for their capability of enhancing the biodegradation of soil polychlorobiphenyls and for their biodegradability, can have the potential of being successfully used in the bioremediation of chronically polychlorinated biphenyl-contaminated soils. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:345-355, 1998.
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  • 17
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    Biotechnology and Bioengineering 58 (1998), S. 356-365 
    ISSN: 0006-3592
    Keywords: Escherichia coli HB101[pGEc47] ; defined medium ; batch and continuous cultivation ; transient experiments ; bioconversion ; octanoic acid ; linear inhibition kinetics ; model simulation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: E. coli HB101[pGEc47], which is able to convert octane to octanoate, but cannot oxidize octanoate further, was grown on defined medium with glucose as carbon source in batch and continuous culture. The biomass yield on glucose decreased from 0.32 ± 0.02 g g-1 in aqueous cultivations to 0.25 ± 0.02 g g-1 in the presence of octane. Maximal octanoate productivities of 0.6 g L-1 h-1 were the same as found in cultivations on complex medium. The glucose-based carbon recovery in these experiments was 99 ± 4% (in extreme, between 90% and 105%). An increase of the octane feed from 1% to 2% (v/v) or more led to washout of cells. This effect was reversible when the octane feed was decreased to its initial value of 1%. Analysis of experimental data by model simulation strongly suggested that washout was due to inhibition by octanoate only. Pulses of octanoate to a continuous culture grown on aqueous media were applied to analyze the inhibition further. Inhibition by acetate was not significant, but its presence in the medium reflected a physiological state that made the cells more sensitive to octanoate inhibition. Model simulation with linear inhibition kinetics could perfectly predict glucose consumption and the resulting glucose concentration. The linear type of inhibition was confirmed by a variety of batch experiments in the presence of different concentrations of octanoate. The glucose-based specific growth rate, μ, decreased linearly with increasing concentrations of octanoate and became zero at a threshold concentration pmax of 5.25 ± 0.25 g L-1. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:356-365, 1998.
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  • 18
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    Biotechnology and Bioengineering 58 (1998), S. 366-373 
    ISSN: 0006-3592
    Keywords: trypsin ; stabilization ; peptide synthesis ; organic solvents ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Bovine pancreatic trypsin was treated with ethylene glycol bis(succinic acid N-hydroxysuccinimide ester). Approximately 8 of 14 lysines per trypsin molecule were modified. This derivative (EG trypsin) was more stable than native between 30° and 70°C: T50 values were 59°C and 46°C, respective. EG trypsin's half-life of 25 min at 55°C was fivefold greater than native's. EG trypsin had a decreased rate of autolysis and retained more activity in aqueous mixtures of 1,4-dioxan, dimethylformamide, dimethylsulfoxide, and acetonitrile. EG trypsin had lower Km values for both amide and ester substrates; its kcat values for two amides (benzoyl-l-arginine p-nitroanilide and benzyloxycarbonyl glycyl-glycyl-arginyl-7-amino-4-methyl coumarin) increased, whereas its kcat value for an ester (thiobenzoyl benzoyloxycarbonyl-l-lysinate) decreased slightly. The specific activity (kcat/Km) of EG trypsin was increased for both amide and ester substrates. EG trypsin gave higher yields and reaction rates than native in kinetically controlled synthesis of benzoyl argininyl-leucinamide in acetonitrile and in t-butanol. Highest peptide yields occurred with EG trypsin in 95% acetonitrile, where 90% of the substrate was converted to product. No peptide synthesis occurred in 95% DMF with either form of trypsin. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:366-373, 1998.
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  • 19
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    Biotechnology and Bioengineering 58 (1998), S. 374-379 
    ISSN: 0006-3592
    Keywords: reversed micelles ; ribonuclease A ; activity ; recovery ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We have investigated the effect of two simple sugars, glucose and sucrose, on the extraction of ribonuclease A by AOT-isooctane reversed micelles. Including the sugars at concentrations up to 0.75 M in the feed solution resulted in moderate improvements in the forward transfer efficiency. The greatest effects were seen observed in the backward transfer step where both the protein recovery yield and the activity of the protein were greatly increased. Protein transfer and activity yields were also dependent on the AOT concentration. We suggest that the presence of sucrose, which was solubilized into the reversed micelles, results in preferential hydration of ribonuclease A, reducing the protein-surfactant interactions. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:374-379, 1998.
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  • 20
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    Biotechnology and Bioengineering 58 (1998), S. 387-399 
    ISSN: 0006-3592
    Keywords: population balance ; cell cycle ; hybridoma ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A cell cycle population model based on the transition probability model of Smith and Martin (1973) has been extended to include product synthesis and export. The model handles two probable mechanisms. In the direct production model, the product is the protein. In the transcription model, the product is the specific mRNA. The protein is synthesized by translation of the specific mRNA and subsequently exported. In either case, the cell density is jointly distributed in the primary product and maturity age in the cell cycle. This extended model also is capable of describing a large range of conditions, including substrate dependent batch and continuous cultures. With the use of unity maturity-velocity (but the transition rate a function of limiting substrate), the model is shown to exhibit a negative growth association between the specific productivity of monoclonal antibodies from hybridomas and the dilution rates of a chemostat. Possibilities of maturity age dependent transcription and translation are considered, and the results show that these features can amplify the specific productivity negative association with specific growth rate. While this model may provide a partial elucidation of monoclonal antibody productivity in a chemostat, the present work provides a proper framework with which probable cell cycle dependent product formation can be analyzed rigorously with a comprehensive computational model. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:387-399, 1998.
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  • 21
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    Keywords: c-jun ; cell cycle ; apoptosis ; antisense ; growth deprivation ; F-MEL ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: F-MEL cells were transfected with the c-jun antisense gene located downstream of a glucocorticoid-inducible MMTV promoter, and the obtained cells were named c-jun AS cells. When the c-jun AS cells were treated with dexamethasone (DEX) in DMEM supplemented with 10% serum, the growth of the cells was completely suppressed for a duration of 16 days with a high cell viability exceeding 86%. The c-jun expression in the c-jun AS cells was suppressed moderately in the absence of DEX and strongly in the presence of DEX. The c-jun AS cells grew well and reached a density of 106 cells/mL without supplementation of any serum components. Viability was greater than 80% after the cells had been cultured for 8 days in the absence of DEX. The c-jun AS cells stayed at a constant cell density and high viability above 80% for 8 days when they were cultured in the presence of DEX under serum deprivation. In contrast, the wild type F-MEL cells were unable to grow and died by apoptosis in 3 days under serum deprivation. Internucleosomal cleavage of DNA, a landmark of apoptosis, was clearly detectable. Thus the c-jun AS cell line that is resistant to apoptosis induced by serum deprivation and can reversibly and viably be growth-arrested was established. A dual-signal model was proposed to explain the experimental result, the interlinked regulation of apoptosis, and growth by c-jun.© 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:65-72, 1998.
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  • 22
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    Biotechnology and Bioengineering 58 (1998), S. 92-100 
    ISSN: 0006-3592
    Keywords: E. coli HB101[pGEc47] ; defined medium ; medium development ; yield coefficients ; critical dilution rate ; batch and continuous cultivation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: This paper shows that differences in growth behavior of Escherichia coli strain HB101 and strain HB101[pGEc47] can be related to yeast extract-enriched medium rather than plasmid properties. An optimal medium for growth of E. coli HB101[pGEc47] was designed based on the individual yield coefficients for specific medium components (NH4+ 6 g g-1, PO43- 14 g g-1, SO42- 50 g g-1). The yield coefficient for l-leucine depends on the glucose content of the medium (20 g g-1 for 3% glucose, 40 g g-1 for 1% glucose) and the yield coefficient for l-proline depends on the cultivation mode (20 g g-1 for batch cultivation, 44 g g-1 for continuous cultivation). Growth on defined medium after medium optimization is as rapid as on complex medium (0.42-0.45 h-1). The critical dilution rate (DR) in the defined medium above which undesired production of acetic acid occurs is in the range of 0.23-0.26 h-1. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:92-100, 1998.
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  • 23
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    Biotechnology and Bioengineering 58 (1998), S. 649-653 
    ISSN: 0006-3592
    Keywords: bioaffinity separation ; pancreatin ; trypsin ; reverse micelles ; nonionic surfactant ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Selective separation of trypsin from a mixture involving many kinds of contaminating proteins, i.e., pancreatin, was achieved using trypsin inhibitor immobilized in the reverse micelles, which were composed of a nonionic surfactant, tetra-oxyethylene monodecylether. To determine the efficient operations throughout the whole separation process we examined the operating conditions, which affect the immobilization efficiency of trypsin inhibitor and also the forward and backward extractions of trypsin. Fifty percent of the recovery of trypsin from pancreatin was realized with no loss of activity of the recovered trypsin. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58: 649-653, 1998.
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    Biotechnology and Bioengineering 58 (1998), S. 658-662 
    ISSN: 0006-3592
    Keywords: T4 lysozyme ; silica nanoparticles ; synthetic enzyme variants ; surface-induced conformational change ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Maintaining a specific molecular conformation is essential for the proper functioning of an enzyme. A substantial loss of catalytic activity can occur from the displacement caused by even a single amino acid substitution. Activity may also be lost as an enzyme undergoes a conformational change during adsorption. In this study, we investigated the effect of thermostability on the activities of three T4 lysozyme variants after adsorption to 9 nm colloidal silica particles. Less-stable T4 lysozyme variants lost more activity after adsorption than did more stable variants, apparently because they experienced more extensive structural alteration. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58: 658-662, 1998.
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    Biotechnology and Bioengineering 58 (1998), S. 654-657 
    ISSN: 0006-3592
    Keywords: enzyme activation ; nonaqueous media ; lyophilization with salt ; substrate diffusion ; subtilisin Carlsberg ; thermolysin ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The dramatic activation of serine proteases in nonaqueous media resulting from lyophilization in the presence of KCl is shown to be unrelated to relaxation of potential substrate diffusional limitations. Specifically, lyophilizing subtilisin Carlsberg in the presence of KCl and phosphate buffer in different proportions, ranging from 99% (w/w) enzyme to 1% (w/w) enzyme in the final lyophilized solids, resulted in biocatalyst preparations that were not influenced by substrate diffusion. This result was made evident through use of a classical analysis whereby initial catalytic rates, normalized per weight of total enzyme in the catalyst material, were measured as a function of active enzyme for biocatalyst preparations containing different ratios of active to inactive enzyme. The active enzyme content of a given biocatalyst preparation was controlled by mixing native subtilisin with subtilisin preinactivated with PMSF, a serine protease inhibitor, and lyophilizing the enzyme mixture in the presence of different fractions of KCl and phosphate buffer. Plots of initial reaction rates as a function of percent active subtilisin in the biocatalyst were linear for all biocatalyst preparations. Thus, enzyme activation (reported elsewhere to be as high as 3750-fold in hexane for the transesterification of N-Ac-L-Phe-OEt with n-PrOH) is a manifestation of intrinsic enzyme activation and not relaxation of diffusional limitations resulting from diluted enzyme preparations. Similar activation is reported herein for thermolysin, a nonserine protease, thereby demonstrating that enzyme activation due to lyophilization in the presence of KCl may be a general phenomenon for proteolytic enzymes. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58: 654-657, 1998.
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    Biotechnology and Bioengineering 58 (1998), S. 663-667 
    ISSN: 0006-3592
    Keywords: Acidianus brierleyi ; pyrite ; bioleaching ; acidophilic thermophile ; yeast extract ; organic supplement ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The bioleaching rate of pyrite (FeS2) by the acidophilic thermophile Acidianus brierleyi was studied at 65°C and pH 1.5 with leach solutions supplemented with yeast extract. In the absence of yeast extract supplementation, A. brierleyi could grow autotrophically on pyrite, and the leaching percentage of pyrite particles (25-44 μm) reached 25% for 7 d. The bacterial growth and consequent pyrite oxidation were enhanced by the addition of yeast extract between 0.005 and 0.25% w/v: the pyrite particles were completely solubilized within 6 d. The bioleaching rate was enhanced by a factor of 1.5 when the yeast extract concentration was changed from 0.005 to 0.05% w/v. However, there was only a slight effect on the leaching rate at the yeast extract concentrations of 0.05 to 0.25% w/v, suggesting that the organic supplement level was in large excess in the pyrite bioleaching. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58: 663-667, 1998.
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    Biotechnology and Bioengineering 58 (1998), S. 119-120 
    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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  • 28
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    Biotechnology and Bioengineering 58 (1998), S. 121-124 
    ISSN: 0006-3592
    Keywords: metabolic control analysis ; metabolic engineering ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The problems of engineering increased flux in metabolic pathways are analyzed in terms of the understanding provided by metabolic control analysis. Over-expression of a single enzyme is unlikely to be effective unless it is known to have a high flux control coefficient, which can be used as an approximate predictive tool. This is likely to rule out enzymes subject to feedback inhibition, because it transfers control downstream from the inhibited enzyme to the enzymes utilizing the feedback metabolite. Although abolishing feedback inhibition can restore flux control to an enzyme, it is also likely to cause large increases in the concentrations of metabolic intermediates. Simultaneous and coordinated over-expression of most of the enzymes in a pathway can, in principle, produce substantial flux increases without changes in metabolite levels, though technically it may be difficult to achieve. It is, however, closer to the method used by cells to change flux levels, where coordinated changes in the level of activity of pathway enzymes are the norm. Another option is to increase the demand for the pathway product, perhaps by increasing its rate of excretion or removal. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:121-124, 1998.
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  • 29
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    Biotechnology and Bioengineering 58 (1998), S. 133-138 
    ISSN: 0006-3592
    Keywords: metabolic modeling ; model selection ; parameter estimation ; identification ; yeast ; stoichiometry ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A metabolic network model is one of the cornerstones of the emerging Metabolic Engineering methodology. In this article, special attention is therefore, given to the phase of model building. A five-stage structured approach to metabolic network modeling is introduced. The basic steps are: (1) to collect a priori knowledge on the reaction network and to build candidate network models, (2) to perform an a priori check of the model, (3) to estimate the unknown parameters in the model, (4) to check the identified model for acceptability from a biological and thermodynamic point of view, and (5) to validate the model with new data. The approach is illustrated with a growth system involving baker's yeast growing on mixtures of substrates. Special attention is given to the central uncertainties in metabolic network modeling, i.e., estimation of energetic parameters in the network and the choice of the source of anabolic reducing equivalents NADPH. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:133-138, 1998.
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    Biotechnology and Bioengineering 58 (1998), S. 125-132 
    ISSN: 0006-3592
    Keywords: metabolic engineering ; metabolic flux analysis ; metabolic control analysis ; thermokinetics ; Saccharomyces cerevisiae ; Penicillium chrysogenum ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Metabolic engineering has been defined as the purposeful modification of intermediary metabolism using recombinant DNA techniques. With this definition metabolic engineering includes: (1) inserting new pathways in microorganisms with the aim of producing novel metabolites, e.g., production of polyketides by Streptomyces; (2) production of heterologous peptides, e.g., production of human insulin, erythropoitin, and tPA; and (3) improvement of both new and existing processes, e.g., production of antibiotics and industrial enzymes. Metabolic engineering is a multidisciplinary approach, which involves input from chemical engineers, molecular biologists, biochemists, physiologists, and analytical chemists. Obviously, molecular biology is central in the production of novel products, as well as in the improvement of existing processes. However, in the latter case, input from other disciplines is pivotal in order to target the genetic modifications; with the rapid developments in molecular biology, progress in the field is likely to be limited by procedures to identify the optimal genetic changes. Identification of the optimal genetic changes often requires a meticulous mapping of the cellular metabolism at different operating conditions, and the application of metabolic engineering to process optimization is, therefore, expected mainly to have an impact on the improvement of processes where yield, productivity, and titer are important design factors, i.e., in the production of metabolites and industrial enzymes. Despite the prospect of obtaining major improvement through metabolic engineering, this approach is, however, not expected to completely replace the classical approach to strain improvement - random mutagenesis followed by screening. Identification of the optimal genetic changes for improvement of a given process requires analysis of the underlying mechanisms, at best, at the molecular level. To reveal these mechanisms a number of different techniques may be applied: (1) detailed physiological studies, (2) metabolic flux analysis (MFA), (3) metabolic control analysis (MCA), (4) thermodynamic analysis of pathways, and (5) kinetic modeling. In this article, these different techniques are discussed and their applications to the analysis of different processes are illustrated. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:125-132, 1998.
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  • 31
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    Biotechnology and Bioengineering 58 (1998), S. 139-148 
    ISSN: 0006-3592
    Keywords: metabolic engineering ; pathway analysis ; metabolic and energetic model ; physiological state ; Saccharomyces cerevisiae ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In this work, an integrated modeling approach based on a metabolic signal flow diagram and cellular energetics was used to model the metabolic pathway analysis for the cultivation of yeast on glucose. This approach enables us to make a clear analysis of the flow direction of the carbon fluxes in the metabolic pathways as well as of the degree of activation of a particular pathway for the synthesis of biomaterials for cell growth. The analyses demonstrate that the main metabolic pathways of Saccharomyces cerevisiae change significantly during batch culture. Carbon flow direction is toward glycolysis to satisfy the increase of requirement for precursors and energy. The enzymatic activation of TCA cycle seems to always be at normal level, which may result in the overflow of ethanol due to its limited capacity. The advantage of this approach is that it adopts both virtues of the metabolic signal flow diagram and the simple network analysis method, focusing on the investigation of the flow directions of carbon fluxes and the degree of activation of a particular pathway or reaction loop. All of the variables used in the model equations were determined on-line; the information obtained from the calculated metabolic coefficients may result in a better understanding of cell physiology and help to evaluate the state of the cell culture process. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:139-148, 1998.
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  • 32
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    Biotechnology and Bioengineering 58 (1998), S. 149-153 
    ISSN: 0006-3592
    Keywords: Metabolic Control Analysis ; flux control coefficients ; top down MCA ; metabolic engineering ; Corynebacterium glutamicum ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Grouping of reactions around key metabolite branch points can facilitate the study of metabolic control of complex metabolic networks. This top-down Metabolic Control Analysis is exemplified through the introduction of group (flux, as well as concentration) control coefficients whose magnitudes provide a measure of the relative impact of each reaction group on the overall network flux, as well as on the overall network stability, following enzymatic amplification. In this article, we demonstrate the application of previously developed theory to the determination of group flux control coefficients. Experimental data for the changes in metabolic fluxes obtained in response to the introduction of six different environmental perturbations are used to determine the group flux control coefficients for three reaction groups formed around the phosphoenolpyruvate/pyruvate branch point. The consistency of the obtained group flux control coefficient estimates is systematically analyzed to ensure that all necessary conditions are satisfied. The magnitudes of the determined control coefficients suggest that the control of lysine production flux in Corynebacterium glutamicum cells at a growth base state resides within the lysine biosynthetic pathway that begins with the PEP/PYR carboxylation anaplorotic pathway. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:149-153, 1998.
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    Biotechnology and Bioengineering 58 (1998), S. 154-161 
    ISSN: 0006-3592
    Keywords: central carbon pathways ; metabolic optimization ; ethanol production ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Many attempts to engineer cellular metabolism have failed due to the complexity of cellular functions. Mathematical and computational methods are needed that can organize the available experimental information, and provide insight and guidance for successful metabolic engineering. Two such methods are reviewed here. Both methods employ a (log)linear kinetic model of metabolism that is constructed based on enzyme kinetics characteristics. The first method allows the description of the dynamic responses of metabolic systems subject to spatiotemporal variations in their parameters. The second method considers the product-oriented, constrained optimization of metabolic reaction networks using mixed-integer linear programming methods. The optimization framework is used in order to identify the combinations of the metabolic characteristics of the glycolytic enzymes from yeast and bacteria that will maximize ethanol production. The methods are also applied to the design of microbial ethanol production metabolism. The results of the calculations are in qualitative agreement with experimental data presented here. Experiments and calculations suggest that, in resting Escherichia coli cells, ethanol production and glucose uptake rates can be increased by 30% and 20%, respectively, by overexpression of a deregulated pyruvate kinase, while increase in phosphofructokinase expression levels has no effect on ethanol production and glucose uptake rates. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:154-161, 1998.
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    Biotechnology and Bioengineering 58 (1998), S. 170-174 
    ISSN: 0006-3592
    Keywords: catabolite repression ; phosphotransferase system ; inducer exclusion ; inducer expulsion ; protein kinase ; transcriptional regulation ; transport regulation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Catabolite repression is a universal phenomenon, found in virtually all living organisms. These organisms range from the simplest bacteria to higher fungi, plants, and animals. A mechanism involving cyclic AMP and its receptor protein (CRP) in Escherichia coli was established years ago, and this mechanism has been assumed by many to serve as the prototype for catabolite repression in all organisms. However, recent studies have shown that this mechanism is restricted to enteric bacteria and their close relatives. Cyclic AMP-independent mechanisms of catabolite repression occur in other bacteria, yeast, plants, and even E. coli. In fact, single-celled organisms such as E. coli, Bacillus subtilis, and Saccharomyces cerevisiae exhibit multiple mechanisms of catabolite repression, and most of these are cyclic AMP-independent. The mechanistic features of the best of such characterized processes are briefly reviewed, and references are provided that will allow the reader to delve more deeply into these subjects. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:170-174, 1998.
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    Biotechnology and Bioengineering 58 (1998), S. 162-169 
    ISSN: 0006-3592
    Keywords: bioinformatics ; metabolic engineering ; genetic engineering ; mathematical analysis ; stoichiometry ; enzyme kinetics ; modal analysis ; genetic circuits ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Ten microbial genomes have been fully sequenced to date, and the sequencing of many more genomes is expected to be completed before the end of the century. The assignment of function to open reading frames (ORFs) is progressing, and for some genomes over 70% of functional assignments have been made. The majority of the assigned ORFs relate to metabolic functions. Thus, the complete genetic and biochemical functions of a number of microbial cells may be soon available. From a metabolic engineering standpoint, these developments open a new realm of possibilities. Metabolic analysis and engineering strategies can now be built on a sound genomic basis. An important question that now arises; how should these tasks be approached? Flux-balance analysis (FBA) has the potential to play an important role. It is based on the fundamental principle of mass conservation. It requires only the stoichiometric matrix, the metabolic demands, and some strain specific parameters. Importantly, no enzymatic kinetic data is required. In this article, we show how the genomically defined microbial metabolic genotypes can be analyzed by FBA. Fundamental concepts of metabolic genotype, metabolic phenotype, metabolic redundancy and robustness are defined and examples of their use given. We discuss the advantage of this approach, and how FBA is expected to find uses in the near future. FBA is likely to become an important analysis tool for genomically based approaches to metabolic engineering, strain design, and development. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:162-169, 1998.
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    Biotechnology and Bioengineering 58 (1998), S. 191-195 
    ISSN: 0006-3592
    Keywords: control analysis ; Lactococcus lactis ; gene expression ; flux ; oligonucleotide ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In this article, we review some of the expression systems that are available for Metabolic Control Analysis and Metabolic Engineering, and examine their advantages and disadvantages in different contexts. In a recent approach, artificial promoters for modulating gene expression in micro-organisms were constructed using synthetic degenerated oligonucleotides. From this work, a promoter library was obtained for Lactococcus lactis, containing numerous individual promoters and covering a wide range of promoter activities. Importantly, the range of promoter activities was covered in small steps of activity change. Promoter libraries generated by this approach allow for optimization of gene expression and for experimental control analysis in a wide range of biological systems by choosing from the promoter library promoters giving, e.g., 25%, 50%, 200%, and 400% of the normal expression level of the gene in question. If the relevant variable (e.g., the flux or yield) is then measured with each of these constructs, then one can calculate the control coefficient and determine the optimal expression level. One advantage of the method is that the construct which is found to have the optimal expression level is then, in principle, ready for use in the industrial fermentation process; another advantage is that the system can be used to optimize the expression of different enzymes within the same cell. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:191-195, 1998.
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    Biotechnology and Bioengineering 57 (1998), S. 571-582 
    ISSN: 0006-3592
    Keywords: TGFα ; autocrine ; modeling ; cell density ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We have developed an experimental system for testing mathematical model predictions concerning escape of autocrine ligands into the extracellular bulk medium. This system employs anti-receptor blocking antibodies against the epidermal growth factor receptor (EGFR)/transforming growth factor alpha (TGFα) receptor/ligand pair. TGFα was expressed under the control of a tetracycline-repressed promoter, together with a constitutively expressed human EGFR in B82 mouse fibroblast cells. This expression system allowed us to vary TGFα synthesis rates over a roughly 300-fold range by adjusting tetracycline concentration. TGFα accumulation in the extracellular bulk medium was then measured as a function of cell density, TGFα synthesis rate, and anti-EGFR blocking antibody concentration. Consistent with model predictions, amounts of ligand in the medium on a per cell basis were found to diminish as cell density was increased but with reduced dependence on cell density at higher ligand synthesis rates. Similarly consistent with model predictions, higher ligand synthesis rates also decreased the effect of anti-receptor blocking antibodies. Our investigation has established that we can successfully analyze and understand autocrine ligand secretion behavior from the basis of our theoretical model. ©1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 571-582, 1998.
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    Biotechnology and Bioengineering 57 (1998), S. 583-589 
    ISSN: 0006-3592
    Keywords: animal cell ; cell adhesion ; fluorocarbon ; liquid/liquid interface ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In general, anchorage-dependent animal cells cultivated on a solid culture substrate, such as polystyrene, are collected by trypsin treatment. This treatment may have detrimental effects such as the proteolysis of the cell membrane proteins. To avoid these effects, cell cultivation using a liquid/liquid interface system has been investigated. In this cultivation method, the cells grow at the interface between a culture medium and a hydrophobic liquid. In this study, various fluorocarbons (FC-40, FC-70, KPF-91, KPF-102, and KPF-142) were used as substrates for the interface, and the cultivation of fibroblast cells (L-929; the mouse-derived cell line) at the interfaces was investigated. Early in the cultivation period, the growth of L-929 cells depended on the substrate type. Although cell cultivation at the interfaces was possible, it was slower than that at the polystyrene surface. Cell spreading at the interfaces was relatively small, which indicates that cell adhesion at the interfaces may be weak. In particular, the cells at the MEM/FC-70 interface anchored with one another and formed multicellular hemispherical aggregations shaped like spheroids. The difference in the adhesions to the interfaces appears to be dependent on the contaminants contained in the fluorocarbons because the physical properties of the fluorocarbon did not affect the cell growth and adhesion. Moreover, subcultivation from the interfaces to the same interface was possible without trypsin treatment. In this case, the delay of the growth at the interfaces did not occur because the cells were not affected by trypsin treatment. ©1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 583-589, 1998.
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  • 39
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    Biotechnology and Bioengineering 57 (1998), S. 590-599 
    ISSN: 0006-3592
    Keywords: protein refolding ; hollow-fibre membrane ; dialysis ; carbonic anhydrase ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We have used a cellulose acetate, hollow-fibre (HF) ultrafiltration membrane to refold bovine carbonic anhydrase, loaded into the lumen space, by removing the denaturant through controlled dialysis via the shell side space. When challenged with GdnHCl-denatured carbonic anhydrase, 70% of the loaded protein reptated through the membrane into the circulating dialysis buffer. Reptation occurred because the protein, in its fully unfolded configuration, was able to pass through the pores. The loss of carbonic anhydrase through the membrane was controlled by the dialysis conditions. Dialysis against 0.05 M Tris-HCl for 30 min reduced the denaturant around the protein to a concentration that allowed the return of secondary structure, increasing the hydrodynamic radius, thus preventing protein transmission. Under these conditions a maximum of 42% of carbonic anhydrase was recovered (from a starting concentration of 5 mg/mL) with 94% activity. This is an improvement over refolding carbonic anhydrase by simple batch dilution, which gave a maximum reactivation of 85% with 35% soluble protein yield. The batch refolding of carbonic anhydrase is very sensitive to temperature; however, during HF refolding between 0 and 25°C the temperature sensitivity was considerably reduced. In order to reduce the convection forces that give rise to aggregation and promote refolding the dialyzate was slowly heated from 4 to 25°C. This slow, temperature-controlled refolding gave an improved soluble protein recovery of 55% with a reactivation yield of 90%. The effect of a number of additives on the refolding system performance were tested: the presence of PEG improved both the protein recovery and the recovered activity from the membrane, while the detergents Tween 20 and IGEPAL CA-630 increased only the refolding yield. ©1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 590-599, 1998.
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  • 40
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    Biotechnology and Bioengineering 57 (1998), S. 620-623 
    ISSN: 0006-3592
    Keywords: protein refolding ; reversed micelles ; solid-liquid extraction ; RNase A ; DNA ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: This article reports that a reversed micellar solution is useful for refolding proteins directly from a solid source. The solubilization of denatured RNase A, which had been prepared by reprecipitation from the denaturant protein solution, into reversed micelles formulated with sodium di-2-ethylhexyl sulfosuccinate (AOT) has been investigated by a solid-liquid extraction system. This method is an alternative to the ordinary protein extraction in reversed micelles based on the liquid-liquid extraction. The solid-liquid extraction method was found to facilitate the solubilization of denatured proteins more efficiently in the reversed micellar media than the ordinary phase transfer method of liquid extraction. The refolding of denatured RNase A entrapped in reversed micelles was attained by adding a redox reagent (reduced and oxidized glutathion). Enzymatic activity of RNase A was gradually recovered with time in the reversed micelles. The denatured RNase A was completely refolded within 30 h. In addition, the efficiency of protein refolding was enhanced when reversed micelles were applied to denatured RNase A containing a higher protein concentration that, in the case of aqueous media, would lead to protein aggregation. The solid-liquid extraction technique using reversed micelles affords better scale-up advantages in the direct refolding process of insoluble protein aggregates. ©1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 620-623, 1998.
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  • 41
    ISSN: 0006-3592
    Keywords: rhG-CSF ; fusion protein ; secretion efficiency ; glycosylation ; multimer ; conformation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The synthesis and secretion of recombinant human granulocyte colony-stimulating factor (rhG-CSF) are investigated in fed-batch cultures at high cell concentration of recombinant Saccharomyces cerevisiae, and some important characteristics of the secreted rhG-CSF are demonstrated. Transcription of the recombinant gene is regulated by a GAL1-10 upstream activating sequence (UASG), and the rhG-CSF is expressed in a hybrid fusion protein consisting of signal sequence of Kluyveromyces lactis killer toxin and N-terminal 24 amino acids of human interleukin 1β. The intracellular KEX2 cleavage leads to excretion of mature rhG-CSF into extracellular culture broth, and the cleavage process seems to be highly efficient. In spite of relatively low copy number the plasmid propagation is stably maintained even at nonselective culture conditions. The rhG-CSF synthesis does not depend on galactose level, whereas the production of extracellular rhG-CSF was significantly enhanced by increasing the inducer concentration above a certain level and also by supplementing the nonionic surfactant to the culture medium, which is notably due to the enhanced secretion efficiency. Various immunoblotting analyses demonstrate that none of the rhG-CSF is accumulated in the cell wall fraction and that a significant amount of intracellular rhG-CSF antibody-specific immunoreactive proteins is located in the ER. A core N-glycosylation at fused IL-1β fragment is likely to play a critical role in directing the high-level secretion of rhG-CSF, and the O-glycosylation of secreted rhG-CSF seems nearly negligible. Also the extracellular rhG-CSF is observed to exist as various multimers, and the nature of molecular interaction is evidently not the covalent disulfide bridges. The CD spectra of purified rhG-CSF and Escherichia coli-derived standard show that the conformations of both are similar and are almost identical to that reported for natural hG-CSF. ©1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 600-609, 1998.
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  • 42
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    Biotechnology and Bioengineering 57 (1998), S. 610-619 
    ISSN: 0006-3592
    Keywords: dynamic model ; Saccharomyces cerevisiae ; oxidative capacity ; feedback control ; calorimetry ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The objective of this study was to characterize the dynamic adaptation of the oxidative capacity of Saccharomyces cerevisiae to an increase in the glucose supply rate and its implications for the control of a continuous culture designed to produce biomass without allowing glucose to be diverted into the reductive metabolism. Continuous cultures subjected to a sudden shift-up in the dilution rate showed that the glucose uptake rate increased immediately to the new feeding rate but that the oxygen consumption could not follow fast enough to ensure a completely oxidative metabolism. Thus, part of the glucose assimilated was degraded by the reductive metabolism, resulting in a temporary decrease of biomass concentration, even if the final dilution rate was below Dcrit. The dynamic increase of the specific oxygen consumption rate, qO2, was characterized by an initial immediate jump followed by a first-order increase to the maximum value. It could be modeled using three parameters denoted qjumpO2, qmaxO2, and a time constant τ. The values for the first two of the parameters varied considerably from one shift to another, even when they were performed under identical conditions. On the basis of this model, a time-dependent feed flow rate function was derived that should permit an increase in the dilution rate from one value to another without provoking the appearance of reductive metabolism. The idea was to increase the glucose supply in parallel with the dynamic increase of the oxidative capacity of the culture, so that all of the assimilated glucose could always be oxidized. Nevertheless, corresponding feed-profile experiments showed that deviations in the reductive metabolism could not be completely suppressed due to variability in the model parameters. Therefore, a proportional feedback controller using heat evolution rate measurements was implemented. Calorimetry provides an excellent and rapid estimate of the metabolic activity. Satisfactory control was achieved and led to constant biomass yields. Ethanol accumulated only up to 0.49 g L-1 as compared to an accumulation of 1.82 g L-1 without on-line control in the shift-up experiment to the same final dilution rate. ©1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 610-619, 1998.
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  • 43
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    Biotechnology and Bioengineering 57 (1998), S. 624-629 
    ISSN: 0006-3592
    Keywords: thermostable esterase ; hyperthermophilic archaeon ; Pyrococcus furiosus ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A genomic library of the hyperthermophilic archaeon Pyrococcus furiosus was constructed in Escherichia coli using pBluescript II SK(+) as a cloning vector. One positive clone exhibiting thermophilic ester-hydrolyzing activity was directly detected by an in situ plate assay using the chromogenic substrate 5-bromo-4-chloro-3-indolyl-acetate. The plasmid isolated from the clone contained a 3.8 kb HindIII fragment from P. furiosus. Expression of active thermostable esterase in E. coli was independent of isopropyl-β-d-thiogalactopyranoside, suggesting that the archaeal esterase gene was heterologously controlled by its own promoter sequence, not by the vector-located lac promoter. Assays of esterase activity in heat-treated extract of the recombinant E. coli showed the highest temperature optimum (100°C) and thermostability (a half-life of 50 min at 126°C) among esterases reported to date. ©1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 624-629, 1998.
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  • 44
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    Biotechnology and Bioengineering 57 (1998), S. 642-654 
    ISSN: 0006-3592
    Keywords: animal cell culture ; growth ; cell death ; kinetics ; autoinhibitor ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Experimental data from six hybridoma cell lines grown under diverse experimental conditions in both normal continuous and perfusion cultures are analyzed with respect to the significance of nutrients and products in determining the growth and death rates of cells and with respect to their mathematical modeling. It is shown that neither nutrients (glucose and glutamine) nor the common products lactic acid, ammonia, and monoclonal antibody can be generally assumed to be the clear-limiting or inhibiting factors for most of the cultures. Correspondingly, none of the unstructured models existing in the literature can be generally applied to describe the experimental data obtained over a relatively wide range of cultivation conditions as considered in this work. Surprisingly, for all cultures the specific growth rate (μ) almost linearly correlates with the ratio of the viable cell concentration (NV) to the dilution (perfusion) rate (D). Similarly, the specific death rate (kd) is a function of the ratio of the total cell concentration (Nt) to the dilution (perfusion) rate. These results strongly suggest the formation of not yet identified critical factors or autoinhibitors that determine both the growth and death rates of hybridoma cells. Based on these observations, simple kinetic models are developed for μ and kd which describe the experimental data satisfactorily. Analysis of the experimental data with the kinetic models reveals that under the current cultivation conditions the formation rate of the autoinhibitor(s) or the sensitivity of cell growth and death to the autoinhibitor(s) is mainly affected by the medium composition. Irrespective of the cell lines, cells grown on serum-containing media have almost the same model parameters, which are distinctively different from those of cells grown on serum-free media. Furthermore, in contrast to the prevailing view, kd is shown to positively correlate with μ if the effects of cell concentration and dilution (perfusion) rate are considered. Several important implications of these findings are discussed for the optimization and control of animal cell culture. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 642-654, 1998
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  • 45
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    Biotechnology and Bioengineering 57 (1998), S. 666-675 
    ISSN: 0006-3592
    Keywords: protein ; recovery ; purification ; crystallization ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Bulk crystallization is emerging as a new industrial operation for protein recovery. Characterization of bulk protein crystallization is more complex than protein crystallization for structural study where single crystals are grown in flow cells. This is because both nucleation and crystal growth processes are taking place while the supersaturation falls. An algorithm is presented to characterize crystallization using the rates of the two kinetic processes, nucleation and growth. The values of these rates allow ready comparison of the crystallization process under different operating conditions. The crystallization, via adjustment to the isoelectric pH of a fungal lipase from clarified fermentation broth, is described for a batch stirred reactor. A maximum nucleation rate of five to six crystals formed per microliter of suspension per second and a high power dependency (≈11) on the degree of supersaturation were found. The suspended protein crystals were found to grow at a rate of up to 15-20 nm/s and also to exhibit a high power dependency (≈6) of growth rate on the degree of supersaturation. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 666-675, 1998
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  • 46
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    Biotechnology and Bioengineering 58 (1998), S. 196-203 
    ISSN: 0006-3592
    Keywords: baculovirus ; chaperone ; hsp70 ; insect cell ; immunoglobulin ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The secretion of heterologous IgG proteins in the baculovirus-insect cell expression system is accompanied by substantial insoluble immunoglobulin in the infected cells. The accumulation of these insoluble forms suggests a limitation in the processing and secretory pathway of the infected cells. As a result, cytosolic hsp70 chaperones, which are known to associate and prevent aggregation of polypeptides in vitro, have been coexpressed in the infected cells. The hsp70 protein coprecipitated with the immunoglobulin to indicate the formation of a specific hsp70-immunoglobulin complex in vivo. Immunoblot and pulse chase studies indicated that coexpression of hsp70 increased intracellular immunoglobulin solubility. Metabolic labeling experiments revealed that hsp70 increased secreted immunoglobulin levels after several days infection as compared to infection with control baculoviruses. Pulse chase studies indicated that hsp70 increases the solubility of immunoglobulin precursors that are then processed and assembled into the complete antibody oligomer. A comparison of the action of cytosolic hsp70 chaperone to the endoplasmic reticulum chaperone BiP suggests sequential action in which hsp70 increases the solubility of preprocessed immunoglobulin, while BiP enhances the solubility of processed immunoglobulin chains. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58: 196-203, 1998.
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  • 47
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    Biotechnology and Bioengineering 58 (1998), S. 175-190 
    ISSN: 0006-3592
    Keywords: protein-based polymers ; inverse temperature transitions ; hydrophobic-induced pKa shifts ; waters of hydrophobic hydration ; five axioms for protein engineering; microwave dielectric relaxation ; a universal mechanism for biological energy conversion ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Metabolism is the conversion of available energy sources to those energy forms required for sustaining and propagating living organisms; this is simply biological energy conversion. Proteins are the machines of metabolism; they are the engines of motility and the other machines that interconvert energy forms not involving motion. Accordingly, metabolic engineering becomes the use of natural protein-based machines for the good of society. In addition, metabolic engineering can utilize the principles, whereby proteins function, to design new protein-based machines to fulfill roles for society that proteins have never been called upon throughout evolution to fulfill.This article presents arguments for a universal mechanism whereby proteins perform their diverse energy conversions; it begins with background information, and then asserts a set of five axioms for protein folding, assembly, and function and for protein engineering. The key process is the hydrophobic folding and assembly transition exhibited by properly balanced amphiphilic protein sequences. The fundamental molecular process is the competition for hydration between hydrophobic and polar, e.g., charged, residues. This competition determines Tt, the onset temperature for the hydrophobic folding and assembly transition, Nhh, the numbers of waters of hydrophobic hydration, and the pKa of ionizable functions.Reported acid-base titrations and pH dependence of microwave dielectric relaxation data simultaneously demonstrate the interdependence of Tt, Nhh and the pKa using a series of microbially prepared protein-based poly(30mers) with one glutamic acid residue per 30mer and with an increasing number of more hydrophobic phenylalanine residues replacing valine residues. Also, reduction of nicotinamides and flavins is shown to lower Tt, i.e., to increase hydrophobicity.Furthermore, the argument is presented, and related to an extended Henderson-Hasselbalch equation, wherein reduction of nicotinamides represents an increase in hydrophobicity and resulting hydrophobic-induced pKa shifts become the basis for understanding a primary energy conversion (proton transport) process of mitochondria. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:175-190, 1998.
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  • 48
    ISSN: 0006-3592
    Keywords: RGD ; FMDV ; internalization ; integrins ; cell binding ; β-galactosidase ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The G-H loop of foot-and-mouth disease virus is a disordered protrusion of the VP1 protein exposed on the virion surface. This short stretch includes an arginine-glycine-aspartic acid tripeptide, a recognized integrin-binding motif, which is responsible for cell attachment and infection. Eight copies of a peptide reproducing the amino acid sequence of this FMDV ligand have been displayed in solvent-exposed regions on an enzymatically active recombinant β-galactosidase. This viral peptide segment enables the chimeric enzyme to bind mammalian cell lines with different efficiencies, probably depending on the number of suitable cell receptors present on each of them. Moreover, it also promotes the internalization of the attached enzyme, which is transiently active inside the cells. These results suggest further exploration of the potential use of short adhesion peptides of viral origin as cell attachment tags to direct the targeted delivery of both genes and enzymes, instead of whole, infectious viruses. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 59:294-301, 1998.
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  • 49
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    Biotechnology and Bioengineering 59 (1998), S. 131-143 
    ISSN: 0006-3592
    Keywords: chemometrics ; light scattering ; microbial productivity ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: This article describes the use of chemometric methods for prediction of biological parameters of cell suspensions on the basis of their light scattering profiles. Laser light is directed into a vial or flow cell containing media from the suspension. The intensity of the scattered light is recorded at 18 angles. Supervised learning methods are then used to calibrate a model relating the parameter of interest to the intensity values. Using such models opens up the possibility of estimating the biological properties of fermentor broths extremely rapidly (typically every 4 sec), and, using the flow cell, without user interaction. Our work has demonstrated the usefulness of this approach for estimation of yeast cell counts over a wide range of values (105-109 cells mL-1), although it was less successful in predicting cell viability in such suspensions. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 59:131-143, 1998.
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  • 50
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    Biotechnology and Bioengineering 59 (1998), S. 144-155 
    ISSN: 0006-3592
    Keywords: lysozyme ; protein precipitation ; thiocyanate ; hydrogen exchange ; nuclear magnetic resonance ; protein unfolding ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We have employed nuclear magnetic resonance (NMR) measurements of hydrogen exchange to identify residue-level conformational changes in hen egg white lysozyme (HEWL) as induced by salt precipitation. Deuterated HEWL was dissolved into a phosphate (H2O) buffer and precipitated at pH 2.1 upon addition of solid KSCN or (ND4)2SO4, allowing isotope labeling of unfolded regions. After 1 h, each precipitate was then dissolved at pH 3.8 to initiate refolding and preserve labeling and subsequently purified for NMR analysis. HEWL precipitated by 1.0 M KSCN exhibited increased hydrogen exchange at 14 residues out of 42 normally well-protected in the native state. Of the affected residues, 9 were situated in the β-sheet/loop domain. A similar, though less extensive, effect was observed at 0.2 M KSCN. Precipitation by 1.2 M (ND4)2SO4 resulted in none of the changes detected with KSCN. The popularity of ammonium sulfate as a precipitant is thus supported by this observed preservation of structural integrity. KSCN, in comparison, produced partial unfolding of specific regions in HEWL due most likely to known preferential interactions between -SCN and proteins. The severity of unfolding increased with KSCN concentration such that, at 1.0 M KSCN, almost the entire β-sheet/loop domain of HEWL was disrupted. Even so, a portion of the HEWL core encompassed by three α-helices remained intact, possibly facilitating precipitate dissolution. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 59: 144-155, 1998.
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  • 51
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    Biotechnology and Bioengineering 59 (1998), S. 156-162 
    ISSN: 0006-3592
    Keywords: Pseudomonas aeruginosa ; Pseudomonas fluorescens ; Klebsiella pneumoniae ; 3-amino-1,2,4-triazole ; catalase ; hydrogen peroxide ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Consortia of catalase positive bacteria consisting of Pseudomonas aeruginosa, Pseudomonas fluorescens, and Klebsiella pneumoniae, in both the planktonic form and as biofilms, disproportionate hydrogen peroxide into oxygen and water. The biofilm, however, continued to disproportionate the hydrogen peroxide in the presence of the catalase inhibitor, 3-amino-1,2,4-triazole, while the planktonic organisms did not. While the bacterial catalase-peroxidase-dismutase system was probably responsible for the disproportionation of hydrogen peroxide in both cases, biofilms resisted inhibition of this enzyme system. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 59: 156-162, 1998.
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  • 52
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    Biotechnology and Bioengineering 59 (1998), S. 163-170 
    ISSN: 0006-3592
    Keywords: enzymes ; organic solvents ; alcohol inhibition ; activity coefficients ; substrate specificity ; rate-limiting step ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Alcohol inhibition of the lipase B from Candida antarctica has been studied through two different approaches: using the same inhibitor (1-butanol) in different organic solvents and using different inhibitors (differing in chain length) in the same solvent. The competitive inhibition constant values obtained in each case correlate with the calculated activity coefficients of the substrate, suggesting that desolvation of the alcohol is the major force changed. Data dispersion observed using the second approach has been interpreted to come from contributions of enzyme-inhibitor interactions to the binding energy. On the other hand, deacylation has been found to be much less influenced by the solvent variation than the acylation step, despite of the fact that solvation of the substrate involved in this step (the alcohol) is expected to change more than for the ester. Concerning the specificity behavior of the enzyme, a bimodal pattern was observed for the deacylation rate dependence on the alcohol chain length, with the highest values for hexanol (C6) and decanol (C10). With regard to the ester specificity, ethyl caproate (C6) is the preferred one. These results have been confronted with those reported for the lipase from Candida rugosa. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 59: 163-170, 1998.
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  • 53
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    Biotechnology and Bioengineering 59 (1998), S. 171-177 
    ISSN: 0006-3592
    Keywords: 4-alkylphenols ; vanillyl alcohol oxidase ; covalent flavoprotein ; enantioselectivity ; 4-vinylphenol ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Vanillyl alcohol oxidase (VAO) from Penicillium simplicissimum catalyzes the enantioselective hydroxylation of 4-ethylphenol, 4-propylphenol, and 2-methoxy-4-propylphenol into 1-(4′-hydroxyphenyl)ethanol, 1-(4′-hydroxyphenyl)propanol, and 1-(4′-hydroxy-3′-methoxyphenyl)propanol, respectively, with an ee of 94% for the R enantiomer. The stereochemical outcome of the reactions was established by comparing the chiral GC retention times of the products to those of chiral alcohols obtained by the action of the lipases from Candida antarctica and Pseudomonas cepacia. Isotope labeling experiments revealed that the oxygen atom incorporated into the alcoholic products is derived from water. During the VAO-mediated conversion of 4-ethylphenol/4-propylphenol, 4-vinylphenol/4-propenylphenol are formed as side products. With 2-methoxy-4-propylphenol as a substrate, this competing side reaction is nearly abolished, resulting in less than 1% of the vinylic product, isoeugenol. The VAO-mediated conversion of 4-alkylphenols also results in small amounts of phenolic ketones indicative for a consecutive oxidation step. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 59:171-177, 1998.
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  • 54
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    Biotechnology and Bioengineering 59 (1998), S. 189-202 
    ISSN: 0006-3592
    Keywords: artificial neural network (ANN) ; microfiltration ; cell harvesting ; membrane fouling ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Microfiltration is an important unit operation in downstream processing. However, due to the influence of membrane fouling, prediction of the filtration performance for biological suspensions is difficult. This paper describes a modeling approach that allows a comprehensive description of filtration performance. On the basis of experimental data and linguistic information, a specific artificial neural network was developed that predicts the process behavior within a certain range of parameters. This approach allows us to analyze influences of fermentation on filtration. By using extensive simulations, the interactions of 17 parameters were examined and the fouling causes determined. The model was developed for cell harvesting of Escherichia coli through a shear-enhanced module. The method can be applied to any cross-flow filtration process. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 59:189-202, 1998.
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  • 55
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    Biotechnology and Bioengineering 59 (1998), S. 178-188 
    ISSN: 0006-3592
    Keywords: fed-batch culture ; response surface model ; optimisation ; β-galactosidase ; Sf9 cells ; baculovirus expression vector system ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Fed-batch culture can offer significant improvement in recombinant protein production compared to batch culture in the baculovirus expression vector system (BEVS), as shown by Nguyen et al. (1993) and Bedard et al. (1994) among others. However, a thorough analysis of fed-batch culture to determine its limits in improving recombinant protein production over batch culture has yet to be performed. In this work, this issue is addressed by the optimisation of single-addition fed-batch culture. This type of fed-batch culture involves the manual addition of a multi-component nutrient feed to batch culture before infection with the baculovirus. The nutrient feed consists of yeastolate ultrafiltrate, lipids, amino acids, vitamins, trace elements, and glucose, which were added to batch cultures of Spodoptera frugiperda (Sf9) cells before infection with a recombinant Autographa californica nuclear polyhedrosis virus (AcNPV) expressing β-galactosidase (β-Gal). The fed-batch production of β-Gal was optimised using response surface methods (RSM). The optimisation was performed in two stages, starting with a screening procedure to determine the most important variables and ending with a central-composite experiment to obtain a response surface model of volumetric β-Gal production. The predicted optimum volumetric yield of β-Gal in fed-batch culture was 2.4-fold that of the best yields in batch culture. This result was confirmed by a statistical analysis of the best fed-batch and batch data (with average β-Gal yields of 1.2 and 0.5 g/L, respectively) obtained from this laboratory. The response surface model generated can be used to design a more economical fed-batch operation, in which nutrient feed volumes are minimised while maintaining acceptable improvements in β-Gal yield. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 59: 178-188, 1998.
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    Biotechnology and Bioengineering 59 (1998), S. 203-213 
    ISSN: 0006-3592
    Keywords: Saccharomyces cerevisiae ; cell cycle behavior ; catabolite repression mutants ; CDC28 expression ; G1 length ; chemostat and batch cultures ; Metabolic Control Analysis ; glycolysis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In glucose-limited continuous cultures, a Crabtree positive yeast such as Saccharomyces cerevisiae displays respiratory metabolism at low dilution rates (D) and respiro-fermentative metabolism at high D. We have studied the onset of ethanol production and cell cycle behavior in glucose-limited chemostat cultures of the wild type S. cerevisiae strain CEN.PK122 (WT) and isogenic mutants, snf1 (cat1) and snf4 (cat3) defective in proteins involved in catabolite derepression and the mutant in glucose repression mig1 (cat4).The triggering of fermentative metabolism was dependent upon catabolite repression properties of yeast and was coincident with a significant decrease of G1 length. WT cells of the strain CEN.PK122 displayed respiratory metabolism up to a D of 0.2 h-1 and exhibited longer G1 lengths than the snf1 and snf4 mutants that started fermenting after a D of 0.1 and 0.15 h-1, respectively. The catabolite derepression mutant snf4 showed a significant decrease in the duration of G1 with respect to the WT. An increase of 300% to 400% in the expression of CDC28 (CDC28-lacZ) with a noticeable shortening in G1 to values lower than ∼150 min, was detected in the transformed wild type CEN.SC13-9B in glucose-limited chemostat cultures. The expression of CDC28-lacZ was analyzed in the wild type and isogenic mutant strains growing at maximal rate on glucose or in the presence of ethanol or glycerol. Two- to three-fold lower expression of the CDC28-lacZ fusion gene was detected in the snf1 or snf4 disruptants with respect to the WT and mig1 strains in the presence of all carbon sources. This effect was further shown to be growth rate-dependent exhibiting apparently, a threshold effect in the expression of the fusion gene with respect to the length of G1, similar to that shown in chemostat cultures.At the onset of fermentation, the control of the glycolytic flux was highly distributed between the uptake, hexokinase, and phosphofructokinase steps. Particularly interesting was the fact that the snf1 mutant exhibited the lowest fluxes of ethanol production, the highest of respiration and correspondingly, the branch to the tricarboxylic acid cycle was significantly rate-controling of glycolysis. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 59: 203-213, 1998.
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    Biotechnology and Bioengineering 59 (1998), S. 214-226 
    ISSN: 0006-3592
    Keywords: Saccharomyces cerevisiae ; diffusion ; encapsulation ; secretion ; screening ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: To observe events occurring in the microenvironment surrounding individual cells, a mathematical framework has been developed describing the behavior of a compound following its secretion by a single cell. This description is based on the diffusional and binding processes taking place in the vicinity of the cell surface. It allows prediction of the rate of capture and accumulation of a secreted compound around a single cell. This concept provides the basis for the design of two experimental assays for measuring single-cell secretion rates: (1) Cells are immobilized in hydrogel microbeads which contain capture sites for the secreted compound; and (2) artificial receptors are bound directly to the cell surface which are capable of binding molecules secreted by individual cells. This general methodology is developed in the specific case of the model organism Saccharomyces cerevisiae secreting a heterologous protein, but can be applied to any cell/secreted protein combination. Binding studies have shown that approximately 2 × 105 of these artificial receptors can be attached to the surface of a single yeast cell. At this surface density of a putative artificial receptor, it is predicted that single-cell secretion rates of 47 molecules/cell/sec of a 150 kDa protein can be detected. Simulations indicate that a microbead loaded with 5 × 106 capture antibodies will result in detection of secretion of this protein at rates as low as 4 molecules/cell/sec. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 59: 214-226, 1998.
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    Biotechnology and Bioengineering 58 (1998), S. 282-291 
    ISSN: 0006-3592
    Keywords: cybernetic models ; metabolic engineering ; storage pathways ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A cybernetic model is proposed to examine generic features of storage pathways. This model is capable of describing synthesis of carbon and non-carbon storage polymers. The effect of environmental conditions is evaluated using storage polymer level as a fraction of total biomass as a gauge of pathway performance. The base wild-type pathway is then analyzed to determine the effect of genetic alterations upon system performance. Proposed modifications are tested using the cybernetic model as a diagnostic tool to ascertain the ramifications of potential genetic alterations. A methodology is developed within the cybernetic framework to describe alterations of enzyme activity and over-expression of pathway enzymes. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:282-291, 1998.
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    Biotechnology and Bioengineering 58 (1998), S. 272-281 
    ISSN: 0006-3592
    Keywords: gene transfer ; retrovirus ; cell cycle ; intracellular stability ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Recombinant retroviruses are currently used as gene delivery vehicles for the purpose of gene therapy. It is generally believed that the efficiency of retroviral transduction depends on the cell cycle status of the target cells. However, it has been reported that this is not the case for the transduction of human and murine fibroblasts, in contrast to other cell types such as lymphocytes. The predictions of a mathematical model that we constructed, offer an explanation of this contradiction, based on the dynamics of the underlying processes of target cell growth and the intracellular decay of retroviral vectors. The model suggests that the utility of synchronization experiments, that are usually employed to study cell cycle specificity, is severely limited when the time scales of the above kinetic events are comparable to each other. The predictions of the model also suggest the use of retroviral vectors as cell cycle markers, as an alternative way to detect cell cycle dependence of retroviral transduction. This method obviates the need for cell synchronization and therefore, it does not perturb the cell cycle or interfere with the life cycle of retroviral vectors. Moreover, it does not depend on the intracellular stability of retroviral vectors. Our results show that in contrast to previously reported results, transduction of murine fibroblasts is cell cycle dependent, and they are consistent with the current notion that mitosis is the phase that confers transduction susceptibility. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:272-281, 1998.
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  • 60
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    Keywords: metabolic engineering ; carbon metabolism ; Escherichia coli mutants ; microbial growth ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Escherichia coli strains devoid of one or both of the two pyruvate kinase isoenzymes (PKA and PKF), were grown on minimal media in batch fermentations. The strain lacking both PKs showed a 28% decrease on its specific growth rate when compared to the wild type. However, protein and CO2 yields did not change. Using radioactive 1-C14 glucose and collecting the CO2 produced by the cultures, it was found that the mutant lacking both pyruvate kinases, metabolized glucose mainly through the pentose pathway (PP). The increased participation of the PP in glucose metabolism in this strain, was also reflected on the levels of the glucose-6-phosphate and 6-phosphogluconate dehydrogenases.© 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 58:292-295, 1998.
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    Biotechnology and Bioengineering 59 (1998), S. 724-731 
    ISSN: 0006-3592
    Keywords: microbial growth ; pH ; ionizable groups ; statistical thermodynamics ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: This paper applies a statistical thermodynamic approach to the kinetics of microbial growth influenced by pH. A general equation is developed and shown to provide a good theoretical basis for the existing pH models that have been widely used to describe the effects of pH on microbial growth kinetics. Four experimental data sets are used to test the general equation developed. The four data sets exhibited a variety of functional curve shapes, for example, symmetrical and asymmetrical bell-shaped, when the specific growth rate of microorganisms is plotted as a function of pH. All four data sets are found to be well represented by the general equation. The existing pH model was, however, found to represent only one out of four data sets, i.e., the symmetrical case. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 59:724-731, 1998.
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    Biotechnology and Bioengineering 59 (1998), S. 732-746 
    ISSN: 0006-3592
    Keywords: Desulfovibrio vulgaris ; hydrogen cycling ; kinetics ; thermodynamics ; modeling ; anaerobic ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A unified model for the growth of Desulfovibrio vulgaris under different environmental conditions is presented. The model assumes the existence of two electron transport mechanisms functioning simultaneously. One mechanism results in the evolution and consumption of hydrogen, as in the hydrogen-cycling model. The second mechanism assumes a direct transport of electrons from the donor to the acceptor, without the participation of H2. A combination of kinetic and thermodynamic conditions control the flow of electrons through each pathway. The model was calibrated using batch experiments with D. vulgaris grown on lactate, in the presence and absence of sulfate, and was verified using additional batch experiments under different conditions. The model captured the general trends of consumption of substrates and accumulation of products, including the transient accumulation and consumption of H2. Furthermore, the model estimated that 48% of the electrons transported from lactate to sulfate involved H2 production, indicating that hydrogen cycling is a fundamental process in D. vulgaris. The presence of simultaneous electron transport mechanisms might provide D. vulgaris with important ecological advantages, because it facilitates a rapid response to changes in environmental conditions. This model increases our ability to study the microbial ecology of anaerobic environments and the role of Desulfovibrio species in a variety of environments. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 59:732-746, 1998.
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    Biotechnology and Bioengineering 59 (1998), S. 747-753 
    ISSN: 0006-3592
    Keywords: enzymes ; glycosidases ; lipases ; supersaturated solutions ; organic solvents ; esterification ; glycosides ; ethyleneglycol ; sugar fatty acid esters ; surfactants ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Three ethoxylated glycosides, tetraethylene glycol β-D-glucoside, tetraethylene glycol β-D-xyloside, and methoxy triethyleneglycol β-D-glucoside, were prepared via almond β-glucoside-catalyzed (trans)glycosylation carried out in supersaturated solutions of glucose or p-nitrophenyl β-D-xyloside and the respective polyethylene glycols. The products were isolated and further modified by enzymatic esterification with Candida antarctica and Mucor miehei lipases. The latter enzyme showed a much greater selectivity for the primary hydroxyl group on the polyethylene glycol chain of the glucoside substrate, thus enabling us to obtain exclusively the corresponding monoester, ω-O-oleoyl tetraethylene glycol β-D-glucoside. Novozyme was used for the preparative synthesis of two other monoesters, 6-O-oleoyl (methoxy triethyleneglycol) β-D-glucoside and ω-O-oleoyl tetraethylene glycol β-D-xyloside. Two diesters, di-oleoyl tetraethylene glycol β-D-glucoside and tetraethylene-bis(6-0-oleoyl glucoside) were also synthesized in good yields using this lipase. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 59:747-753, 1998.
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    Biotechnology and Bioengineering 60 (1998), S. 137-146 
    ISSN: 0006-3592
    Keywords: fluorescence confocal microscopy ; microfabrication ; aminosilane ; mercaptosilane ; antibody immobilization ; heterobifunctional crosslinker ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Fluorescence confocal microscopy was used to characterize micron-sized microfabricated silicon particles and planar oxide surfaces after silanization and immobilization of IgG antibody. Surfaces treated with amino- and mercaptosilanes were tested for the presence of amine and sulfhydryl groups by labeling with specific fluorescein probes. In addition, human antibody (IgG) was immobilized to the thiol-coated microparticles using the heterobifunctional crosslinker succinimidyl 4-(N-maleimidolmethyl)-cyclohexane-1-carboxylate. Estimates of the surface density of IgG were consistent with 8.3% of a monolayer of covalently-bound antibody. Confocal images confirmed uniform layers of both silanes and antibodies on the microparticles. The sensitivity limit for the confocal measurements was determined to be as low as 1.5 × 10-5 fluors per nm2. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 137-146, 1998.
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    Biotechnology and Bioengineering 60 (1998), S. 147-155 
    ISSN: 0006-3592
    Keywords: hydrogen sulfide ; elemental sulfur ; desulfurization ; Thiobacilli ; redox potential ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The investigations described show that the formation of elemental sulfur from the biological oxidation of sulfide can be optimized by controling the redox state of the solution. The nonsoluble sulfur can be removed by gravity sedimentation and re-used as a raw material, i.e., in bioleaching processes. It was shown that, by supplying an almost stoichiometrical amount of oxygen to the recirculated gas phase, the formation of sulfate is minimized. The redox potential is mainly determined by the sulfide concentration because this compound has a high standard exchange current density with the platinum electrode surface. By maintaining a particular redox setpoint value, in fact, the reactor becomes a “sulfide-stat.” It was shown that in a sulfide-oxidizing bioreactor the measured redox potential, using a polished redox electrode, is kinetically determined rather than thermodynamically. The optimal redox value for sulfur formation is between -147 and -137 mV (H2 reference electrode, 30°C, pH 8). The presented results are currently used for controling several full-scale installations, which desulfurize biogas and high-pressure natural gas. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 147-155, 1998.
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    Biotechnology and Bioengineering 60 (1998), S. 169-179 
    ISSN: 0006-3592
    Keywords: mathematical model ; morphology ; pellet ; filamentous fungus ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In certain conditions, filamentous fungi are observed to grow exponentially during batch submerged growth. It is shown for three cases, with simple mechanistic models, that an exponential growth assumption is reasonable. The basis of these models is the identification of a growth unit, and a mechanism for its doubling with a constant generation time. The importance of the variation of morphological properties within populations is demonstrated by the comparison of computer simulations of simplified models using average values and either experimental data or computer simulations of detailed stochastic models. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 169-179, 1998.
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    Biotechnology and Bioengineering 59 (1998), S. 786-791 
    ISSN: 0006-3592
    Keywords: seleno-subtilisin ; subtilisin ; semisynthetic enzyme ; peroxidase ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A simplified and up-scaled synthesis of the semisynthetic peroxidase seleno-subtilisin was developed. Highly purified to technical grade subtilisin preparations from Bacillus licheniformis and Bacillus amyloliquefaciens were applied as starting materials. Activation of Ser 221 with phenylmethanesulfonyl fluoride, nucleophilic substitution by sodium hydrogen selenide, and oxidation to the seleninic acid with hydrogen peroxide completed the chemical active-site modification. The reactions were accomplished with a minimum of simple work-up procedures in 10 g scale. Kinetics and enantioselectivity of the preparations were tested using 1-phenylethyl hydroperoxide. For the first time, an up-scaled synthesis of a semisynthetic enzyme is available. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 59:786-791, 1998.
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    Biotechnology and Bioengineering 59 (1998), S. 776-785 
    ISSN: 0006-3592
    Keywords: protein crystallization ; impurities ; lysozyme ; purification ; solubility ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: While bulk crystallization from impure solutions is used industrially as a purification step for a wide variety of materials, it is a technique that has rarely been used for proteins. Proteins have a reputation for being difficult to crystallize and high purity of the initial crystallization solution is considered paramount for success in the crystallization. Although little is written on the purifying capability of protein crystallization or of the effect of impurities on the various aspects of the crystallization process, recent published reports show that crystallization shows promise and feasibility as a purification technique for proteins.To further examine the issue of purity in macromolecule crystallization, this study investigates the effect of the protein impurities, avidin, ovalbumin, and conalbumin at concentrations up to 50%, on the solubility, crystal face growth rates, and crystal purity of the protein lysozyme. Solubility was measured in batch experiments while a computer controlled video microscope system was used to measure the {110} and {101} lysozyme crystal face growth rates. While little effect was observed on solubility and high crystal purity was obtained ( 〉 99.99%), the effect of the impurities on the face growth rates varied from no effect to a significant face specific effect leading to growth cessation, a phenomenon that is frequently observed in protein crystal growth. The results shed interesting light on the effect of protein impurities on protein crystal growth and strengthen the feasibility of using crystallization as a unit operation for protein purification. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 59:776-785, 1998.
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    Biotechnology and Bioengineering 60 (1998), S. 156-168 
    ISSN: 0006-3592
    Keywords: fed-batch ; Candida rugosa lipase production ; control ; feeding strategy ; on-line monitoring and estimation ; lipase purification ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Simulation studies have predicted that maximum lipase activity is reached with fed-batch operation strategies. In this work, two different fed-batch operational strategies have been studied: constant substrate feeding rate and specific growth rate control. A constant substrate feeding rate strategy showed that maximum aqueous lipolytic activity (55 U/mL) was reached at low substrate feeding rates, whereas lipase tends to accumulate inside the cell at higher rates of substrate addition. In the second fed-batch strategy studied, a feedback control strategy has been developed based on the estimation of state variables (X and μ) from the measurement of indirect variables such as CER by means of mass spectrometry techniques. An on-off controller was then used to maintain the specific growth rate at the desired value by adjusting the substrate feeding rate. A constant specific growth rate strategy gave higher final levels of aqueous lipolytic activity (117 U/mL) at low specific growth rates. At higher specific growth rates the enzyme remained accumulated inside the cell, as was observed with a constant feeding fed-batch strategy. With a constant specific growth rate strategy, lipase production by Candida rugosa was enhanced 10-fold compared to a batch operation. Purification studies have demonstrated that lipolytic and esterasic specific activity ratios of Candida rugosa isoenzymes can be modified by using different operational conditions. These studies have also showed that the isoenzymes obtained in a controlled growth rate strategy are around three- to four-fold more active than those obtained in a constant feeding rate strategy. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 156-168, 1998.
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    Biotechnology and Bioengineering 60 (1998), S. 197-203 
    ISSN: 0006-3592
    Keywords: enzymes ; glycosidases ; transglycosylations ; supersaturated solutions ; glycosides ; disaccharides ; synthesis ; regioselectivity ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Enzymatic transglycosylation in supersaturated solutions of substrates was investigated using crude glycosidase preparations from barley, snail, and coffee beans. It was shown that the use of supersaturated glycoside solutions as media for transglycosylation reactions offers considerable advantages over conventional aqueous systems. These advantages include higher yields, more efficient use of the donor glycosides and improved volumetric productivity, especially in the case of poorly water-soluble substrates. The regioselectivity of the glycosylation was not significantly affected by high concentrations of acceptor glycosides. It was also shown that the regioselectivity of transfer could be directed towards secondary hydroxyl groups by the use of methyl 6-O-acetyl-α-galactopyranoside as acceptor. The value of these approaches was demonstrated by the synthesis of methyl 3- and 4-O-β-D-galactopyranosyl-α-D-galactopyranosides and methyl 3-O-β-D-galactopyranosyl-α-L-fucopyranoside on a preparative scale. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 197-203, 1998.
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    Biotechnology and Bioengineering 60 (1998), S. 204-215 
    ISSN: 0006-3592
    Keywords: immobilization ; white-rot fungi ; Lentinula edodes ; manganese peroxidase ; Mn3+ ; azlactone ; chlorophenol ; EEDQ ; biocatalyst ; bioremediation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Manganese peroxidase (MnP) purified from commercial cultures of Lentinula edodes was covalently immobilized through its carboxyl groups using an azlactone-functional copolymer derivatized with ethylenediamine and 2-ethoxy-1-ethoxycarbonyl-1,2-dihydroquinoline (EEDQ) as a coupling reagent. The tethered enzyme was employed in a two-stage immobilized MnP bioreactor for catalytic generation of chelated MnIII and subsequent oxidation of chlorophenols. Manganese peroxidase immobilized in the enzyme reactor (reactor 1) produced MnIII-chelate, which was pumped into another chemical reaction vessel (reactor 2) containing the organopollutant. Reactor 1-generated MnIII-chelates oxidized 2,4-dichlorophenol and 2,4,6-trichlorophenol in reactor 2, demonstrating a two-stage enzyme and chemical system. H2O2 and oxalate chelator concentrations were varied to optimize the immobilized MnP's oxidation of MnII to MnIII. Oxidation of 1.0 mM MnII to MnIII was initially measured at 78% efficiency under optimized conditions. After 24 h of continuous operation under optimized reaction conditions, the reactor still oxidized 1.0 mM MnII to MnIII with ∼69% efficiency, corresponding to 88% of the initial MnP activity. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 204-215, 1998.
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    Biotechnology and Bioengineering 60 (1998), S. 230-238 
    ISSN: 0006-3592
    Keywords: Escherichia coli ; metabolism ; flux ; linear optimization ; biomass composition ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The amino acid composition of proteins and the fatty acid composition of the cell membranes were measured in Escherichia coli growing exponentially in batch culture on glucose, succinate, glycerol, pyruvate, and acetate, and growing under continuous culture conditions on glucose at dilutions rates equivalent to the growth rates of the batch cultures. Although the fatty acid composition of the membranes did change significantly with carbon source and dilution rate, the amino acid content of proteins did not change significantly under either condition. A previously developed stoichiometric model of metabolism was used to calculate the fluxes through the metabolic reactions and to determine their sensitivity to changes in fatty acid and amino acid composition. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 230-238, 1998.
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    Biotechnology and Bioengineering 60 (1998), S. 216-229 
    ISSN: 0006-3592
    Keywords: model ; fungal fermentation ; morphology ; Aspergillus awamori ; agitation intensities ; dissolved oxygen tension ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Generalizing results from fungal fermentations is difficult due to their high sensitivity toward slight variation in starting conditions, poor reproducibility, and difference in strains. In this study a mathematical model is presented in which oxygen transfer, agitation intensity, dissolved oxygen tension, pellet size, formation of mycelia, the fraction of mycelia in the total biomass, carbohydrate source consumption, and biomass growth are taken into account. Two parameters were estimated from simulation, whereas all others are based on measurements or were taken from literature. Experimental data are obtained from the fermentations in both 2 L and 100 L fermentors at various conditions. Comparison of the simulation with experiments shows that the model can fairly well describe the time course of fungal growth (such as biomass and carbohydrate source concentrations) and fungal morphology (such as pellet size and the fraction of pellets in the total biomass). The model predicts that a stronger agitation intensity leads to a smaller pellet size and a lower fraction of pellets in the total biomass. At the same agitation intensity, pellet size is hardly affected by the dissolved oxygen tension, whereas the fraction of mycelia decreases slightly with an increase of the dissolved oxygen tension in the bulk. All of these are in line with observations at the corresponding conditions. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 216-229, 1998.
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  • 74
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    Keywords: HL60 cells ; CD13 ; hydrodynamic effects ; mRNA ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Flow cytometry and Northern blotting were used to examine the effects of hydrodynamic forces in stirred tank bioreactors on CD13 receptor surface content and mRNA levels of HL60 (human promyelocytic leukemia) cells. A step increase in agitation rate from 80 to 300 or 400 rpm reduced the apparent HL60 growth rate in a dose-dependent manner. This step increase in agitation rate (to 300 or 400 rpm) also increased the CD13 receptor surface content on averge by 30% and 100%, respectively. This increase in CD13 receptor surface content was correlated with a 10% and a 60% increase in CD13 mRNA levels. We also observed a significant and very reproducible drop in CD13 expression over the course of a batch bioreactor run (80 rpm). Although we have no explanation for this, we show that the decrease in CD13 receptor surface content can be (at least partially, if not fully) explained by the corresponding decrease in CD13 mRNA. HL60 cell cultures agitated at 300 and 400 rpm exhibited glucose consumption and lactate production rates that were approximately 40% and 90% greater than values of the cultures agitated at 80 rpm. The physiological and practical implications of these results are discussed. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 239-250, 1998.
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  • 75
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    Biotechnology and Bioengineering 60 (1998), S. 271-276 
    ISSN: 0006-3592
    Keywords: recombinant ; E. coli ; fed-batch ; protein production ; post-induction feeding ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The effect of post-induction nutrient feeding strategies on the production of bioadhesive protein using an IPTG inducible expression system in Escherichia coli was investigated. Cells were cultured in an exponential fed-batch mode to the OD600 of ca. 100 (48 gDCW/L) prior to induction. Six different post-induction nutrient feeding strategies (pH-stat, exponential, constant and linear change in feeding rate with three different slopes) were then applied, and bioadhesive protein production was examined. It was found that post-induction cell growth was independent of nutrient feeding rate. However, bioadhesive protein production was significantly affected by post-induction feeding strategies. Linearly changing post-induction feeding rate with a suitable slope allowed production of bioadhesive protein up to 5.3 g/L, which was higher than that obtained by the other post-induction feeding strategies. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 271-276, 1998.
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  • 76
    ISSN: 0006-3592
    Keywords: HL60 cells ; CD13 ; serum ; hydrodynamic effects ; mRNA ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The effects of serum medium concentration on the CD13 receptor surface content and mRNA levels of HL60 (human promyelocytic leukemia) cells were examined using flow cytometry and Northern blotting. Increasing the serum concentration from 2.5% to 10% and from 5% to 10% increased the CD13 receptor surface content of HL60 cells by 100% and 25%, respectively, in spinner flasks agitated at 60 rpm. In bioreactors at 80 rpm, increasing the serum concentration from 2.5% to 10% and from 5% to 10% increased the CD13 receptor surface content by 60% and 35%, respectively. This increase in CD13 receptor surface content was correlated with a 30% and a 20% increase in CD13 mRNA levels. Increasing serum concentrations also increased the average HL60 cell size under non-damaging conditions (60 rpm in spinner flasks, 80 rpm in bioreactors). Under conditions of agitation at 300 rpm in 2 L bioreactors, increasing serum concentrations (2.5% vs. 10%, 5% vs. 10%) allowed for higher HL60 apparent growth rates, but decreased the CD13 receptor surface content and mRNA levels. In view of our earlier findings on the effects of agitation on the CD13 antigen, these data suggest that serum reduces the transduction of mechanical forces that affect CD13 expression. At 300 rpm, HL60 cells cultured in 10% serum exhibited glucose consumption and lactate production rates that were approximately 50% and 60% lower than the values of cells cultured in 5% and 2.5% serum, respectively. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 259-268, 1998.
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  • 77
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    Biotechnology and Bioengineering 60 (1998), S. 77-87 
    ISSN: 0006-3592
    Keywords: membrane fouling ; microfiltration ; backpulsing ; cell recovery ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A promising method for reducing membrane fouling during crossflow microfiltration of biological suspensions is backpulsing. Very short backpulses (0.1-1.0 s) have been used to increase the net flux for washed bacterial suspensions and whole bacterial fermentation broths. The net fluxes under optimum backpulsing conditions for the washed bacteria are approximately 10-fold higher than those obtained during normal crossflow microfiltration operation, whereas only a 2-fold improvement in the net flux is achieved for the fermentation broths. A theory is presented that is based on external fouling during forward filtration and nonuniform cleaning of the membrane during reverse filtration. The model contains an adjustable parameter which is a measure of the cleaning efficiency during backpulsing; the cleaning efficiency found by fitting the model to the experiments increases with increasing frequency and duration of the backpulses. The theory predicts an optimum backpulsing frequency, as was observed experimentally. An economic analysis shows that crossflow microfiltration with backpulsing has lower costs than centrifugation, rotary vacuum filtration, and crossflow microfiltration without backpulsing. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 77-87, 1998.
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  • 78
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    Biotechnology and Bioengineering 60 (1998), S. 88-96 
    ISSN: 0006-3592
    Keywords: molybdenum ; uranium ; immobilized cells ; dissimilatory reduction ; Desulfovibrio ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Intact cells of Desulfovibrio desulfuricans were immobilized in polyacrylamide gel and used to remove soluble U and Mo from water by enzymatically mediated reduction reactions in column reactors. Formate or lactate served as the electron donor and oxidized U(VI) and Mo(VI) species served as electron acceptors. Greater than 99% removal efficiencies were achieved for both metals with initial concentrations of 5 mg/L U and 10 mg/L Mo. Hydraulic residence times in the columns were between 24 and 36 h. Sulfate concentrations as high as 2000 mg/L did not inhibit reduction of U or Mo in the columns. However, nitrate inhibited uranium reduction at concentrations near 50 mg/L and inhibited molybdenum reduction at concentrations near 150 mg/L. The results indicate that enzymatic reduction of U and Mo by immobilized cells of D. desulfuricans may be a practical method for removing these contaminants from solution in continuous-flow reactors. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 88-96, 1998.
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  • 79
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    Biotechnology and Bioengineering 60 (1998), S. 97-104 
    ISSN: 0006-3592
    Keywords: fixed-bed bioreactor ; pressure drop ; biofilm growth monitoring ; Biofor ; friction factor ; Reynolds number ; wastewater treatment ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The possibility of following the biomass growth by pressure drop measurement was investigated in an aerated cocurrent upflow fixed-bed bioreactor continuously fed with wastewater containing industrial organic pollutants. The experiments were carried out in a biological filtration oxygenated reactor (Biofor) pilot plant packed with expanded clay balls (Biolite) of 2.7-mm diameter, which served as biomass carriers. The column was equipped for on-line pressure drop measurements. Correlation between pressure drop measurements and Reynolds numbers of air and water were determined in experiments carried out without biomass. Under operating conditions with biomass, it was demonstrated that column clogging and the operating time between washing cycles can be predicted depending on the volumetric organic load for a given total organic carbon inlet concentration. The biological activity of the fixed biomass was estimated from the oxygen consumption rate per unit time and carrier area. The oxygen consumption rate measurements demonstrated that the biological activity depends on the inlet substrate concentration, and that the Biofor column was most efficient between 75 and 100 g m-3 of total organic carbon inlet concentration. In the course of the wastewater treatment, using pressure drop measurements, the equivalent diameter of the Biolite particles, the reduced column macroporosity, and the biofilm thickness were calculated. An expression correlating biofilm density and biofilm thickness, as determined from the pressure drop measurements, was proposed. Good agreement was found between the fixed biomass in the reactor, determined as volatile suspended solids, and the biologically active biomass, estimated by respirometry. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 97-104, 1998.
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  • 80
    ISSN: 0006-3592
    Keywords: Monte Carlo simulation ; depolymerization ; endo-enzymes ; single-attack mechanism ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A Monte Carlo simulation of the depolymerization of linear homopolymers by specific endo-enzymes exhibiting random-attack probability and a single-attack mechanism has been developed. The program simulates the “real” depolymerization versus time of a polydisperse sample of substrate by a specific endo-enzyme. Given the initial mass distribution and concentration of the substrate, the initial concentration of the enzyme, and its Michaelis-Menten constant, the program simulates the evolution of the mass distribution of the substrate with the depolymerization time. When tested against experimental data from the depolymerization of barley (1→3),(1→4)-β-D-glucan by malt endo-(1→3),(1→4)-β-D-glucanase, monitored using the Calcofluor-FIA method with fluorescent detection, excellent results were obtained. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 105-113, 1998.
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  • 81
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    Biotechnology and Bioengineering 60 (1998), S. 627-635 
    ISSN: 0006-3592
    Keywords: airlift reactor ; biofilm ; hydrodynamics ; mass transfer ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The hydrodynamics and mass transfer, specifically the effects of gas velocity and the presence and type of solids on the gas hold-up and volumetric mass transfer coefficient, were studied on a lab-scale airlift reactor with internal draft tube. Basalt particles and biofilm-coated particles were used as solid phase. Three distinct flow regimes were observed with increasing gas flow rate. The influence of the solid phase on the hydrodynamics was a peculiar characteristic of the regimes. The volumetric mass transfer coefficient was found to decrease with increasing solid loading and particle size. This could be predominantly related to the influence that the solid has on gas hold-up. The ratio between gas hold-up and volumetric mass transfer coefficient was found to be independent of solid loading, size, or density, and it was proven that the presence of solids in airlift reactors lowers the number of gas bubbles without changing their size. To evaluate scale effects, experimental results were compared with theoretical and empirical models proposed for similar systems. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 627-635, 1998.
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  • 82
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    Biotechnology and Bioengineering 61 (1998), S. 7-12 
    ISSN: 0006-3592
    Keywords: tyrphostins ; directed sorting method ; solid-phase organic synthesis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Using solid-phase organic synthesis, we have prepared a 432-member (18 × 8 × 3) sample library based on the AG 490 “tyrphostin” template. By utilizing 432 reactors each equipped with a unique radiofrequency memory ID tag, the 432 products could be obtained as discrete entities (i.e., not as mixtures) via 18 + 8 + 3, or 29 reactions. Reading each ID tag after each reaction step permitted the “directed sorting” of reactors into appropriate reaction vessels containing multiple reactors. After synthesis, all products were cleaved from the solid-phase support and lyophilized to afford powders. Characterization of 5% of the library members by NMR and mass spectrometry provided verification of structure. In addition, TLC analysis of every library member provided evidence that most (or all) are composed of a single major organic compound. Some 88% of these samples were obtained in amounts of between 5 and 19 mg. Using this reaction sequence and the “directed sorting” approach, the synthesis of much larger AG 490-based libraries can be envisioned. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng (Comb Chem) 61:7-12, 1998.
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  • 83
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    Biotechnology and Bioengineering 61 (1998), S. 17-22 
    ISSN: 0006-3592
    Keywords: combinatorial library ; polymer supported quench ; 4-thiazolidinones ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A one-pot, three-component, solution-phase synthesis of 2,3-disubstituted and 2,3,5-trisubstituted 4-thiazolidinones is described. Poly(styrene-co-divinylbenzene)-supports functionalized with tris(2-aminoethyl)amine and 2-amino-ethanethiol are used to remove excess reagents from the desired product upon completion of the reaction. Simple filtration followed by concentration provides products of sufficient purity for biological evaluation. This approach has been used for a parallel combinatorial generation of a library of multi-substituted 4-thiazolidinones. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng (Comb Chem) 61:17-22, 1998.
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  • 84
    ISSN: 0006-3592
    Keywords: parallel array technology ; solid-phase organic synthesis ; hydroxamic acids ; automated synthesis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An automated, 96-well parallel array synthesizer for solid-phase organic synthesis has been designed and constructed. The instrument employs a unique reagent array delivery format, in which each reagent utilized has a dedicated plumbing system. An inert atmosphere is maintained during all phases of a synthesis, and temperature can be controlled via a thermal transfer plate which holds the injection molded reaction block. The reaction plate assembly slides in the X-axis direction, while eight nozzle blocks holding the reagent lines slide in the Y-axis direction, allowing for the extremely rapid delivery of any of 64 reagents to 96 wells. In addition, there are six banks of fixed nozzle blocks, which deliver the same reagent or solvent to eight wells at once, for a total of 72 possible reagents. The instrument is controlled by software which allows the straightforward programming of the synthesis of a larger number of compounds. This is accomplished by supplying a general synthetic procedure in the form of a command file, which calls upon certain reagents to be added to specific wells via lookup in a sequence file. The bottle position, flow rate, and concentration of each reagent is stored in a separate reagent table file. To demonstrate the utility of the parallel array synthesizer, a small combinatorial library of hydroxamic acids was prepared in high throughput mode for biological screening. Approximately 1300 compounds were prepared on a 10 μmole scale (3-5 mg) in a few weeks. The resulting crude compounds were generally 〈80% pure, and were utilized directly for high throughput screening in antibacterial assays. Several active wells were found, and the activity was verified by solution-phase synthesis of analytically pure material, indicating that the system described herein is an efficient means for the parallel synthesis of compounds for lead discovery. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng (Comb Chem) 61:33-45, 1998.
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  • 85
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    Biotechnology and Bioengineering 61 (1998), S. 55-60 
    ISSN: 0006-3592
    Keywords: FMOC deprotection ; solid-phase synthesis ; polymer resins ; automated synthesis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Base-catalyzed cleavage of the 9-fluorenylmethoxycarbonyl (FMOC) group and subsequent analysis by UV spectrophotometry is commonly employed to measure the “loading” of functional groups on solid support. Recent work suggests that 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU) may be superior to piperidine (the most commonly used base for the cleavage) for quantitative analysis by UV. We have compared deprotection of FMOC-bearing compounds by both DBU and piperidine, and have observed by GC-MS the formation of a dibenzofulvene-piperidine adduct (piperidine deprotection), and the formation of unassociated dibenzofulvene (DBU deprotection). We have further been able to use GC analysis of dibenzofulvene produced in the DBU deprotection mixture in a quantitative analysis of resin loading, which gave results comparable to UV methods. Sample preparation for this method has been automated using the Nautilus 2400 organic synthesizer to reduce the amount of operator time and increase throughput of sample analysis. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng (Comb Chem) 61:55-60, 1998
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  • 86
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    Biotechnology and Bioengineering 61 (1998), S. 77-79 
    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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  • 87
    ISSN: 0006-3592
    Keywords: radio-frequency tag distributor ; Irori microkans ; 96-well format ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A novel parallel radio-frequency (RF) tag distributor has been developed which allows for distribution of RF tags into Irori microkans in 96-well format. The distributor has a holding capacity of ∼1000 RF tags and distributes RF tags in groups of 12. Using the distributor, a block of 96 microkans can be filled with RF tags in less than 30 sec resulting in significant time savings over one-at-a-time manual RF tag distribution. The distributor may also be of utility as a solid-phase synthesis tool for dispensing resin enclosed in capsules (which have the same shape as RF tags). © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng (Comb Chem) 61:93-94, 1998.
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  • 88
    ISSN: 0006-3592
    Keywords: gene delivery ; gene therapy ; generation of guanidines on solid support ; polyamines ; polyguanidines ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The development of new gene delivery technologies is a prerequisite towards gene therapy clinical trials. Because gene delivery mediated by viral vectors remains of limited scope due to immunological and propagation risks, the development of new non-viral gene delivery systems is of crucial importance. We have synthesized a secondary library of mono-functionalized poly-(guanidinium)amines generated from a library of mono-functionalized polyamines applying the concept of “libraries from libraries.” The method allows a quick and easy access to mono-functionalized geometrically varied poly-(guanidinium)amines. The new building blocks were introduced into cationic lipids to obtain novel poly-(guanidinium)amine lipids, which are potential DNA vectors for gene delivery. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng (Comb Chem) 61:81-87, 1998.
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  • 89
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    Biotechnology and Bioengineering 61 (1998), S. 89-92 
    ISSN: 0006-3592
    Keywords: solid phase chemistry ; Merrifield linker ; Suzuki coupling ; Stille coupling ; Pd(0) mediated C-S bond formation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We report the convenient generation of chloromethylated polystyrene surfaces (Merrifield linker)3 on SynPhase™ crowns. It was demonstrated that these novel surfaces can be successfully employed for peptide chemistry as well as Pd(0) mediated cross-couplings. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng (Comb Chem) 61:89-92, 1998.
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  • 90
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    Biotechnology and Bioengineering 60 (1998), S. 689-698 
    ISSN: 0006-3592
    Keywords: purification ; cation exchange chromatography ; cell culture ; cell culture medium ; serum free ; therapeutic antibodies ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A shortcut purification sequence for therapeutic proteins should consist of three steps: capture, purification, and polishing. Special emphasis has been put on direct capture of human monoclonal antibodies from culture supernatants with ion-exchangers avoiding pretreatment steps such as desalting, dilution, and other means to reduce the ionic strength. CM-HyperD, a cation-exchanger composed of an inorganic macroporous support filled with a viscoelastic gel with a high charge density was used. Capture of monoclonal antibodies from clarified hybridoma cell culture grown in media supplemented with fetal calf serum was investigated. Screening of different pH conditions and buffers for the load step showed that monoclonal antibodies were efficiently bound by CM-HyperD at pH 4.0 and 5.0 at an ionic strength equivalent to culture supernatant. Combination of negative purification with Q-Sepharose FF and capturing with CM-HyperD gave sufficient yield and resolution. Implementation of wash steps with higher conductivity did not improve the purity, but decreased the yield. Interestingly, high flow rates improved the purity. When antibodies were captured from serumfree culture supernatant the antibody could be eluted in a single peak with substantial reduction of contaminants. Capturing of antibodies by ion-exchange sorbents from culture supernatant is possible despite the high salt content. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 689-698, 1998.
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  • 91
    ISSN: 0006-3592
    Keywords: immobilized metal affinity precipitation ; α-amylase inhibitor ; wheat ; poly(N-isopropylacrylamide) ; vinylimidazole ; iminodiacetic acid ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A method for purifying α-amylase inhibitor from wheat meal based on immobilized metal affinity with a thermosensitive copolymer is developed. The studies represent the thermoprecipitation properties of the copolymers of N-isopropylacrylamide (NIPAM) with iminodiacetic acid (IDA) and 1-vinylimidazole (VI), respectively. The polymer which is obtained by the copolymerization of 1-vinylimidazole and N-isopropylacrylamide, charged with Cu(II), exhibited specific interaction of the metal ions to the protein inhibitor. The precipitation was induced by salt and the recovery of the amylase inhibitor was achieved by dissolving the inhibitor-polymer complex in imidazole buffer and subsequent precipitation of the polymer. A single family of the α-amylase inhibitor was recovered from the polymer with 89% yield and about fourfold purification. The SDS-PAGE pattern showed significant purification of the inhibitor. The binding of the inhibitor to the Cu(II)-polymer conjugate depends upon the Cu(II) concentration in the copolymer and also upon the concentration of the protein. The recovered polymer could be reused with reasonable efficiency. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 59:695-704, 1998.
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  • 92
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    Biotechnology and Bioengineering 59 (1998), S. 705-713 
    ISSN: 0006-3592
    Keywords: algal growth ; photobioreactor ; light/dark cycles ; photoinhibition ; airlift reactor ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The effect of light/dark cycles on the growth of the red microalga Porphyridium sp. was studied in a tubular loop bioreactor with light/dark cycles of different frequencies and in two 35-L reactors: a bubble column reactor and an air-lift reactor. Photon flux densities were in the range of 50 to 300 μE m-2 s-1, and flow rates were 1 to 10 L min-1. Under conditions of low illumination and high flow rates, similar results were obtained for the bubble column and air-lift reactors. However, higher productivities - in terms of biomass and polysaccharide - were recorded in the air-lift reactor under high light intensity and low gas flow rates. The interactions of both photosynthesis and photoinhibition with the fluid dynamics in the bioreactors was taken as the main element that allowed us to interpret the differences in performance of the bubble column and the air-lift reactor. It is suggested that the cyclic distribution of dark periods in the air-lift reactor facilitates better recovery from the photoinhibition damage suffered by the cells. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 59:705-713, 1998.
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  • 93
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    Biotechnology and Bioengineering 61 (1998), S. 107-118 
    ISSN: 0006-3592
    Keywords: combinatorial chemistry ; tumor therapy ; porphyrinoids ; liposomes ; mass spectrometry ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Reported here is the preparation of tetraphenylporphyrin libraries via efficient combinatorial solution-phase syntheses, their purification, and preliminary results from a bioorganic study on their uptake in liposome membranes. Libraries with up to 666 components were prepared with substituents including Br, CF3, Cl, CN, CO2Me, Et, F, OAc, and Ph. Further, a first example for the synthesis of more diverse libraries via a “latent libraries” approach is presented. This involves masking polar groups with lipophilic protecting groups. After purification of the latent library, the masking protecting groups are removed in a quantitative reaction that produces the library compounds as the only non-volatile components. Libraries were characterized by laser desorption time-of-flight mass spectrometry, NMR, and UV-vis spectroscopy. In vitro uptake into membranes of small sonicated liposomes was measured, both in terms of total porphyrin incorporation and in terms of structure-incorporation relationships. The latter were determined from isotopically-resolved laser-desorption mass spectra under conditions that yield quantitative results. Smaller libraries showed increased uptake of porphyrins bearing OH and CF3 substituents and lower uptake of ester-, alkyl-, and halide-bearing porphyrins. This structure-dependent selectivity disappears for larger libraries, however, where uniformly high uptake is observed, i.e., at a constant lipid:porphyrin ratio the total porphyrin incorporation is higher for libraries than for single compounds of similar polarity. We propose that the decreased concentration of individual compounds in large libraries is responsible for this effect. Membrane incorporation has previously been shown to correlate with photodynamic activity in vitro and in vivo.16 Therefore, these results may help to explain why photodynamic therapy of tumors, a modern anti-cancer treatment modality, is successfully performed with a complex mixture of porphyrins. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng (Comb Chem) 61:107-118, 1998.
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  • 94
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    Biotechnology and Bioengineering 57 (1998), S. 71-78 
    ISSN: 0006-3592
    Keywords: acetate ; E. coli ; metabolic flux ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The productivity of Escherichia coli as a producer of recombinant proteins is affected by its metabolic properties, especially by acetate production. Two commercially used E. coli strains, BL21 (λDE3) and JM109, differ significantly in their acetate production during batch fermentation at high initial glucose concentrations. E. coli BL21 grows to an optical density (OD, 600 nm) of 100 and produces no more than 2 g/L acetate, while E. coli JM109 grows to an OD (600 nm) of 80 and produces up to 14 g/L acetate. Even in fed-batch fermentation, when glucose concentration is maintained between 0.5 and 1.0 g/L, JM109 accumulates 4 times more acetate than BL21. To investigate the difference between the two strains, metabolites and enzymes involved in carbon utilization and acetate production were analyzed (isocitrate, ATP, phosphoenolpyruvate, pyruvate, isocitrate lyase, and isocitrate dehydrogenase). The results showed that during batch fermentation isocitrate lyase activity and isocitrate concentration were higher in BL21 than in JM109, while pyruvate concentration was higher in JM109. The activation of the glyoxylate shunt pathway at high glucose concentrations is suggested as a possible explanation for the lower acetate accumulation in E. coli BL21. Metabolic flux analysis of the batch cultures supports the activity of the glyoxylate shunt in E. coli BL21. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 71-78, 1998.
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  • 95
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    Biotechnology and Bioengineering 57 (1998), S. 87-94 
    ISSN: 0006-3592
    Keywords: flow cytometry ; spectrofluorymetry ; intracellular protein and nucleic acids quantification ; cell viability ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The use of flow cytometry (FCM) to quantitatively analyze intracellular compounds is studied. FCM is a very useful technique for individual cell studies in microbial systems, and gives access to information which cannot be obtained in any other way. Nevertheless, it provides data in arbitrary units, that is, relative data. This analytical technique could be employed for kinetic modeling of microbial systems and even for internal phenomena analysis, but for this purpose, absolute data - that is concentration of intracellular compounds - must be used.In this work, relative flow cytometry data are transformed into absolute data by means of calibrations employing the same fluorochromes with another technique: spectrofluorymetry. Calibrations of DNA, RNA, and protein intracellular concentrations are presented for the bacteria, Xanthomonas campestris. Other analytical methods, based on biochemical determinations, were also employed to quantify intracellular compounds, but the results obtained are very poor compared with those achieved by means of spectrofluorymetry (SFM). Calibration equations and data obtained by both techniques are given. Evolutions of protein and nucleic acids during Xanthomonas campestris growth and xanthan gum production are shown. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 87-94, 1998.
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  • 96
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 57 (1998), S. 109-117 
    ISSN: 0006-3592
    Keywords: nanofiltration ; selectivity ; inorganic membrane ; peptide ; pH ; ionic strength ; polyelectrolyte ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Nanofiltration (NF) membrane technology shows interesting potentials for separating organic components on the basis of solute charge and size in the range of 300-1000 g mol-1. Separation properties of two inorganic NF membranes were studied with a set of 10 small peptides (molecular mass range: 300-900 g mol-1; 3 〈 pI 〈 10) contained in a well-characterized tryptic β casein hydrolysate. Peptides transmission strongly depended on ionic interactions in the system. Physicochemical conditions such as ionic strength and especially pH were crucial to the separation, because the membrane and peptides showed amphoteric properties. Thus, the three categories of peptides (acid, basic, neutral) were separated according to their pI because of presumed concentration gradients of charged peptides at the membrane: positive for basic peptides and negative for acid peptides. At optimum pH 8 this led to high transmissions of basic peptides (even over 100%), intermediate transmissions for neutral peptides, and low transmissions for acid peptides. The addition of multicharged cationic and anionic species in the hydrolysate induced a markedly enhanced selectivity when the polyelectrolyte was a membrane coion and a complete reversion of selectivity when it was a membrane counterion. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 109-117, 1988.
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  • 97
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 57 (1998), S. 155-163 
    ISSN: 0006-3592
    Keywords: endogenous respiration ; activated sludge ; multi-time scales ; identifiability ; observability ; model reduction ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In this article, an autonomous four-compartment model that describes the endogenous respiration in an aerobic biodegradation process is proposed and analyzed theoretically. First, the multi-time scale of the system's behavior, to be taken into account in subsequent analyses, is emphasized. Then, an identifiability and observability study, given measurements of MLVSS (mixed liquor volatile suspended solids) and respiration rate, is performed for use under practical circumstances, such as in state and parameter estimation. It appears that the process is observable, but not fully identifiable. Hence, for the identification of some of the model parameters, additional measurements or experiments, also indicated here, have to be performed. Furthermore, it is shown that, under quasi-steady state conditions which, in general, appear shortly after initialization of an endogenous respiration experiment, the model can be reduced significantly. Finally, results of parameter estimation from available data are presented and discussed. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 155-163, 1998.
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  • 98
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 57 (1998), S. 164-171 
    ISSN: 0006-3592
    Keywords: cell death ; apoptosis ; bcl -2 ; cell culture ; cell viability ; growth factors ; survival factors ; abortive proliferation ; hybridomas ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Cultures of the CRL-1606 hybridoma (ATCC) have been reported to undergo continuous proliferation with simultaneous death during nutrient limited fed-batch fermentations. The bcl-2 proto-oncogene has been shown to prevent cell death under a variety of otherwise death inducing conditions. We were interested in elucidating the nature of the massive death observed in cultures of CRL-1606, specifically with respect to the possible environmental causes, and the ability of overexpressed human bcl-2 (hbcl-2) to mitigate cell death. Abortive proliferation, or continuous proliferation in the presence of continuous death, could be induced in serum free cultures of CRL-1606 through the withdrawal of insulin provided the culture was competent for cell proliferation. Culture competency for proliferation was found to be solely determined by the presence of cell culture nutrients. Abortive proliferation was defective in cultures transfected with hbcl-2 and the enhanced viability observed resulted from an increased viable cell population and at the expense of the nonviable cell population normally found in untransfected cultures. Abortive proliferation was also observed in serum containing cultures upon serum shiftdowns. Like the insulin-supplemented serum free culture system, hbcl-2 transfected cultures exhibited defects in the abortive proliferation process. These results suggest that the massive death observed during nutrient-limited fed-batch fermentation originate, in part, from growth or survival factor limitations. Hence, approaches to design cell culture media that account for the cell's proliferation requirements without accounting for the cell's survival requirements may represent a cell death sentence. Given the transformed nature of the hybridomas, we conclude that the abortive proliferation of CRL-1606 is a consequence of inappropriate cell cycle entry in a survival factor limited environment. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 164-171, 1998.
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  • 99
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 57 (1998), S. 631-641 
    ISSN: 0006-3592
    Keywords: ceramic membrane ; water-oil ; shear rate ; transmembrane pressure ; pore size ; lumen diameter ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Recovery of an aqueous bioconversion product from complex, two-phase Pseudomonas putida broths containing 20% (v/v) soybean oil presents a significant challenge for downstream processing. Although not used before in multiple-phase separation for complex biotech products, crossflow filtration employing ceramic filters is one of the most attractive options which allow the design of integrated, continuous bioconversion processes. As a first attempt, we studied multichannel, monolithic ceramic membranes of different nominal pore sizes and lumen diameters under steady-state conditions. The best performance was obtained with 0.2-μm-pore/3-mm-lumen membrane, which completely rejected both cells and oil droplets from the permeate, creating a clear aqueous product stream. Although the same separation was achieved, the 50K molecular weight cut-off (MWCO) ultrafilter showed greater irreversible but similar reversible resistance, in addition to an order-of-magnitude higher membrane resistance. Larger nominal pore microfilters, such as 0.45 and 1.0 μm, experienced both cell and oil leakage even at low transmembrane pressure (10 psig). Attributed to greater shear at the same recirculation rate, smaller lumen filters did provide greater permeate flux. However, for practical purposes, the 0.2-μm-pore/4-mm-lumen ceramic membrane was chosen for further evaluation. Transmembrane pressures up to 50 psig provided only marginal gains in filtration performance, whereas increasing shear rate resulted in linear increases in steady-state flux, presumably due to formation of shear-sensitive, complex gel/oil/cell layer near the membrane surface. A nominal shear rate of 9200 s-1 and 20 psig transmembrane pressure were chosen as optimal operating conditions. Additional studies in a clean system revealed that as low as 5% (v/v) soybean oil in deionized (DI) water resulted in an order-of-magnitude decline in steady-state permeate flux. Breakthrough of oil droplets occurred at 35 psig transmembrane pressure. The severe fouling and breakthrough phenomena disappeared in the presence of washed cells for transmembrane pressure up to 43 psig, implying an oil/cell layer coating the membrane surface, thus preventing oil penetration. Serious membrane fouling was also experienced in microfiltration of oil-free, cell-free supernatant and oil-free whole broth. Consequently, soluble proteins/surfactants were suspected to be the major membrane foulants. Interestingly, soybean oil up to 30% (v/v) enhanced the flux, presumably through complicated interactions with the major foulants. Regeneration of membrane was best achieved with protease and hot caustic/bleach treatments, supporting the hypothesized fouling mechanisms mentioned above. This work provides process and system information for batch microfiltration runs in the future, to be reported elsewhere as Part II of this work. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 631-641, 1998
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  • 100
    ISSN: 0006-3592
    Keywords: islets of Langerhans ; microencapsulation ; poly(ethylene glycol) ; photopolymerization ; hydrogels ; bioartificial organs ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A method has been defined to interfacially photopolymerize poly(ethylene glycol) diacrylates (PEG diacrylates) to form a crosslinked hydrogel membrane upon the surfaces of porcine islets of Langerhans to serve as an immune barrier for allo- and xenotransplantation. A sensitivity study of six key parameters in the interfacial photopolymerization process was performed to aid in determination of the optimal encapsulation conditions, leading to the most uniform hydrogel membranes and viable islets. The key parameters included the concentrations of the components of the initiation scheme, namely eosin Y, triethanolamine, and 1-vinyl 2-pyrrolidinone. Other parameters investigated included the duration and flux of laser irradiation and the PEG diacrylate molecular weight. Each parameter was doubled and halved from the standard conditions used in the encapsulation process while holding all the remaining parameters at the standard conditions. The effects of changing each parameter on islet viability, encapsulation efficiency, and gel thickness were quantified. Islet viability was sensitive to the duration of laser illumination, viability significantly increasing as the duration was reduced. Encapsulation efficiency was sensitive to the concentrations of eosin Y, triethanolamine, and 1-vinyl 2-pyrrolidinone, to the laser flux, and to the PEG diacrylate molecular weight. Increasing the concentration of eosin Y significantly improved the encapsulation efficiency, while decreasing the concentration of 1-vinyl 2-pyrrolidinone and increasing the concentration of triethanolamine had the greatest effects in significantly reducing the encapsulation efficiency. Gel thickness was sensitive to the concentrations of triethanolamine and 1-vinyl 2-pyrrolidinone, to the duration of laser illumination, and to the PEG diacrylate molecular weight. Increasing the PEG diacrylate molecular weight significantly increased the gel thickness, while decreasing the concentration of 1-vinyl 2-pyrrolidinone and increasing the concentration of triethanolamine had the greatest effects in significantly reducing the gel thickness. From this sensitivity study, conditions were determined to encapsulate porcine islets, resulting in greater than 90% islet viability and greater than 90% encapsulation efficiency. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 655-665, 1998
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