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  • General Chemistry  (1,786)
  • Biochemistry and Biotechnology  (670)
  • Cell & Developmental Biology  (458)
  • 1995-1999  (2,914)
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  • 1996  (2,914)
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  • 1
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 49 (1996), S. 15-19 
    ISSN: 0006-3592
    Keywords: viscous fluid ; fluid dynamic study ; Xanthan solution ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Studies were conducted1 in 19-m3 fermentors (14-m3 working volume) using four Rushton turbines, four Prochem Maxflo Ts, and three Lightnin' A315s and the results in water have been reported earlier. Here, a 1.7 wt/vol% Xanthan solution has been used as the working fluid, simulating viscous broths to give Reynolds numbers (Re) between 1800 and 4500. As predicted from small-scale studies, the power numbers at these values of Re were similar to those in water. The K factor (the ratio of power draw under aerated conditions compared to non-aerated) was the same as in water at the higher values of Re, but at the lower values it fell more rapidly with increasing aeration rate and to a lower value than in water. At all times, K was higher than with Rushton turbines. Vibration characteristics were also measured. Under aerated conditions, the fermentors vibrated with an amplitude 75% to 100% less than in water due to viscous damping. With increasing air flow, the amplitude increased steadily due to the presence of very large and rapidly rising bubbles in such fluids to give values 2.5 to 3 times those in water. Nevertheless, these mechanical problems can be overcome, allowing such agitators to be used successfully in high viscosity mycelial fermentations. © 1996 John Wiley & Sons, Inc.
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  • 2
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 49 (1996), S. 20-25 
    ISSN: 0006-3592
    Keywords: filamentous fungi ; immobilization ; biofilm bioreactor ; oil emulsion ; degradation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A new type of horizontal biofilm bioreactor for continuous bioconversion of emulsified oily substrate by immobilized growing biofilm of filamentous fungi was designed, constructed, and feasibility tested. The new reactor design provides “self”-immobilization of homogenized mycelium leading to even biofilm development. This was accomplished by using stainless steel screens of optimal mesh, mounted in parallel and stretching outward from a main rotating axis of a biological rotating contractor. Each screen was equipped with a pair of stainless steel blades mounted on supports allowing for continuous biofilm “shaving” beyond a predetermined thickness, thus retaining freshly growing active biofilm surface. The feasibility of the new bioreactor was demonstrated by decalactone production from emulsified castor oil by immobilized filamentous fungi (Tyromyces sambuceus). The combination of oriented metal screens and moving blades was found to be highly effective for a model system in maintaining stable substrate emulsion in the reactor in either batchwise or continuous processing, as well as maintaining biofilm thickness with continuous removal of excess growing hyphae. © 1996 John Wiley & Sons, Inc.
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  • 3
    Electronic Resource
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 49 (1996), S. 52-62 
    ISSN: 0006-3592
    Keywords: L-phenylacetylcarbinol ; biotransformation ; benzaldehyde ; pyruvate decarboxylase ; Candida utilis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Biotransformation of benzaldehyde to L-phenylacetylcarbinol (L-PAC) as a key intermediate for L-ephedrine synthesis has been evaluated using pyruvate decarboxylase (PDC) partially purified from Candida utilis. PDC activity was enhanced by controlled fermentative metabolism and pulse feeding of glucose prior to the enzyme purification. With partially purified PDC, several enzymatic reactions occurred simultaneously and gave rise to by-products (acetaldehyde and acetoin) as well as L-PAC production. Optimal reaction conditions were determined for temperature, pH, addition of ethanol, PDC activity, benzaldehyde, and pyruvate:benzaldehyde ratio to maximize L-PAC, and minimize by-products. The highest L-PAC concentration of 28.6 g/L (190.6 mM) was achieved at 7 U/mL PDC activity and 200 mM benzaldehyde with 2.0 molar ratio of pyruvate to benzaldehyde in 40 mM potassium phosphate buffer (pH 7.0) containing 2.0 M ethanol at 4°C. © 1996 John Wiley & Sons, Inc.
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  • 4
    Electronic Resource
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 49 (1996), S. 63-69 
    ISSN: 0006-3592
    Keywords: Leuconostoc mesenteroides ; lactose catabolism ; oxygen ; stoichiometry ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Lactose metabolism of a Leuconostoc mesenteroides strain was studied in batch cultures at a pH of 6.5 and 30°C in 10 L of a modified MRS (De Man, Rogosa, Sharp) broth. The end products of this heterolactic bacterium were D-lactate, acetate, ethanol, and carbon dioxide. To test the effect of oxygen on their synthesis, the medium was sparged with different gases: nitrogen, air, and pure oxygen. When oxygen was available, oxygen uptake occurred, which caused a modification in acetate and ethanol production but not in lactate or carbon dioxide production; acetate plus ethanol together were produced in constant amounts, which were independent of the level of aeration. The influence of oxygen on end-product formation could be summed up by the general equation: lactose + x O2 → 2 D-lactate + (x + 0.1) acetate + (2 - x) ethanol + 2 CO2. Maximal oxygen uptake (x = 2) was reached under a 120 L/h flow rate of pure oxygen. In addition, this equation provided useful information on the possible pathway of galactose catabolism by a heterofermentative microorganism. © 1996 John Wiley & Sons, Inc.
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  • 5
    ISSN: 0006-3592
    Keywords: epoxide hydrolase ; Aspergillus niger ; p-nitrostyrene oxide ; optical resolution ; enantiomer separation ; chiral synthon ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The epoxide hydrolase activity of Aspergillus niger was synthesized during growth of the fungus and was shown to be associated with the soluble cell fraction. An enzyme preparation was worked out which could be used in place of the whole mycelium as biocatalyst for the hydrolysis of epoxides. The effect of four different cosolvents on enzyme activity was investigated. Consequently, dimethylsulfoxide (DMSO) was selected for epoxide solubilization. The effect of temperature on both reaction rate and enzyme stability was studied in the presence of DMSO (0.2 volume ratio). A temperature of 25°C was selected for the reaction of bioconversion. With a substrate concentration of 4.5 mM a batch reactor showed that the enzyme preparation hydrolyzed para-nitrostyrene oxide with very high enantioselectivity. The (S) enantiomer of the epoxide remained in the reaction mixture and showed an enantiomeric excess higher than 99%. The substrate concentration could be increased to 20 mM without affecting the enantiomeric excess and degree of conversion. Therefore, the method is potentially useful for the preparative resolution of epoxides. Application are in the field of chiral synthons which are important building blocks in organic synthesis. © 1996 John Wiley & Sons, Inc.
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  • 6
    Electronic Resource
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 49 (1996), S. 101-105 
    ISSN: 0006-3592
    Keywords: Xanthomonas maltophilia ; benzoic acid ; Vitreoscilla hemoglobin gene ; genetic engineering ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Xanthomonas maltophilia was transformed with the gene encoding Vitreoscilla (bacterial) hemoglobin, vgb, and the growth of the engineered strain was compared with that of the untransformed strain using benzoic acid as the sole carbon source. In general, growth of the engineered strain was greater than that of the untransformed strain; this was true for experiments using both overnight cultures and log phase cells as inocula, but particularly for the latter. In both cases the engineered strain was also more efficient than the untransformed strain in converting benzoic acid into biomass. © 1996 John Wiley & Sons, Inc.
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  • 7
    Electronic Resource
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    Biotechnology and Bioengineering 49 (1996), S. 93-100 
    ISSN: 0006-3592
    Keywords: disinfection ; chlorine ; transport ; gel bead ; biofilm ; reaction-diffusion ; Pseudomonas aeruginosa ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An artificial biofilm system consisting of Pseudomonas aeruginosa entrapped in alginate and agarose beads was used to demonstrate transport limitation of the rate of disinfection of entrapped bacteria by chlorine. Alginate gel beads with or without entrapped bacteria consumed chlorine. The specific rate of chlorine consumption increased with increasing cell loading in the gel beads and decreased with increasing bead radius. The value of an observable modulus comparing the rates of reaction and diffusion ranged from less than 0.1 to 8 depending on the bead radius and cell density. The observable modulus was largest for large (3-mm-diameter) beads with high cell loading (1.8 × 109 cfu/cm3) and smallest for small beads (0.5 mm diameter) with no cells added. A chlorine microelectrode was used to measure chlorine concentration profiles in agarose beads (3.0 mm diameter). Chlorine fully penetrated cell-free agarose beads rapidly; the concentration of chlorine at the bead center reached 50% of the bulk concentration within approximately 10 min after immersion in chlorine solution. When alginate and bacteria were incorporated into an agarose bead, pronounced chlorine concentration gradients persisted within the gel bead. Chlorine did gradually penetrate the bead, but at a greatly retarded rate; the time to reach 50% of the bulk concentration at the bead center was approximately 46 h. The overall rate of disinfection of entrapped bacteria was strongly dependent on cell density and bead radius. Small beads with low initial cell loading (0.5 mm diameter, 1.1 × 107 cfu/cm3) experienced rapid killing; viable cells could not be detected (〈1.6 × 105 cfu/cm3) after 15 min of treatment in 2.5 mg/L chlorine. In contrast, the number of viable cells in larger beads with a higher initial cell density (3.0 mm diameter, 2.2 × 109 cfu/cm3) decreased only about 20% after 6 h of treatment in the same solution. Spatially nonuniform killing of bacteria within the beads was demonstrated by measuring the transient release of viable cells during dissolution of the beads. Bacteria were killed preferentially near the bead surface. Experimental results were consistent with transport limitation of the penetration of chlorine into the artificial biofilm arising from a reaction-diffusion interaction. The methods reported here provide tools for diagnosing the mechanism of biofilm resistance to reactive antimicrobial agents in such applications as the treatment of drinking and cooling waters. © 1996 John Wiley & Sons, Inc.
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  • 8
    ISSN: 0006-3592
    Keywords: intracellular fluxes ; metabolite balance ; carbon labeling balance ; lysine ; anaplerotic reactions ; NMR spectroscopy ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: To determine the in vivo fluxes of the central metabolism we have developed a comprehensive approach exclusively based on the fundamental enzyme reactions known to be present, the fate of the carbon atoms of individual reactions, and the metabolite balance of the culture. No information on the energy balance is required, nor information on enzyme activities, or the directionalities of reactions. Our approach combines the power of 1H-detected 13C nuclear magnetic resonance spectroscopy to follow individual carbons with the simplicity of establishing carbon balances of bacterial cultures. We grew a lysine-producing strain of Corynebacterium glutamicum to the metabolic and isotopic steady state with [1-13C]glucose and determined the fractional enrichments in 27 carbon atoms of 11 amino acids isolated from the cell. Since precursor metabolites of the central metabolism are incorporated in an exactly defined manner in the carbon skeleton of amino acids, the fractional enrichments in carbons of precursor metabolites (oxaloacetate, glyceraldehyde 3-phosphate, erythrose 4-phosphate, etc.) became directly accessible. A concise and generally applicable mathematical model was established using matrix calculus to express all metabolite mass and carbon labeling balances. An appropriate all-purpose software for the iterative solution of the equations is supplied. Applying this comprehensive methodology to C. glutamicum, all major fluxes within the central metabolism were determined. The result is that the flux through the pentose phosphate pathway is 66.4% (relative to the glucose input flux of 1.49 mmol/g dry weight h), that of entry into the tricarboxylic acid cycle 62.2%, and the contribution of the succinylase pathway of lysine synthesis 13.7%. Due to the large amount and high quality of measured data in vivo exchange reactions could also be quantitated with particularly high exchange rates within the pentose phosphate pathway for the ribose 5-phosphate transketolase reaction. Moreover, the total net flux of the anaplerotic reactions was quantitated as 38.0%. Most importantly, we found that in vivo one component within these anaplerotic reactions is a back flux from the carbon 4 units of the tricarboxylic acid cycle to the carbon 3 units of glycolysis of 30.6%. © 1996 John Wiley & Sons, Inc.
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  • 9
    Electronic Resource
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 49 (1996), S. 139-150 
    ISSN: 0006-3592
    Keywords: Vitreoscilla hemoglobin ; flux analysis ; dose response ; microaerobic metabolism ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The amount of Vitreoscilla hemoglobin (VHb) expression was modulated over a broad range with an isopropyl-β-D-thiogalactopyranoside- (IPTG-) inducible plasmid, and the consequences on microaerobic Escherichia coli physiology were examined in glucose fed-batch cultivations. The effect of IPTG induction on growth under oxygen-limited conditions was most visible during late fed-batch phase where the final cell density increased initially linearly with increasing VHb concentrations, ultimately saturating at a 2.7-fold increase over the VHb-negative (Vhb-) control. During the same growth phase, the specific excretions of fermentation by-products, acetate, ethanol, formate, lactate, and succinate from the culture expressing the highest amount of VHb were reduced by 25%, 49%, 68%, 72%, and 50%, respectively, relative to the VHb- control. During the exponential growth phase, VHb exerted a positive but smaller control on growth rate, growth yield, and respiration. Varying the amount of VHb from 0 to 3.8 μmol/g dry cell weight (DCW) increased the specific growth rate, the growth yield, and the oxygen consumption rate by 33%, 35%, and 60%, respectively. Increasing VHb concentration to 3.8 μmol/g DCW suppressed the rate of carbon dioxide evolution in the exponential phase by 30%. A metabolic flux distribution analysis incorporating data from these cultivations discloses that VHb+ cells direct a larger fraction of glucose toward the pentose phosphate pathway and a smaller fraction of carbon through the tricarboxylic acid cycle from acetyl coenzyme A. The overall nicotinamide adenine dinucleotide [NAD(P)H] flux balance indicates that VHb-expressing cells generate a net NADH flux by the NADH/NADPH transhydrogenase while the VHb- cells yield a net NADPH flux under the same growth conditions. Flux distribution analysis also reveals that VHb+ cells have a smaller adenosine triphosphate (ATP) synthesis rate from substrate-level phosphorylation but a larger overall ATP production rate under microaerobic conditions. The thermodynamic efficiency of growth, based on reducing equivalents generated per unit of biomass produced, is greater for VHb+ cells. © 1996 John Wiley & Sons, Inc.
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  • 10
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 49 (1996), S. 185-196 
    ISSN: 0006-3592
    Keywords: streptomycin ; Streptomyces ; strain improvement ; continuous culture ; feedback control ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We have applied a technique of interactive continuous selection (ICS) to the isolation of streptomycin-resistant mutants of the streptomycin-producing organism, Streptomyces griseus. A series of mutants, each with a different colonial morphology and expressing successively greater resistance to streptomycin, was isolated during the course of selection. Takeover of the mutants has been correlated with changes in on-line estimates of streptomycin concentration such that these estimates may be used as a real-time measure of the genetic state of the cell population. When grown in the medium employed for ICS, mutants expressed increased antibiotic production titers; the best mutant produced 10 to 20 times more streptomycin than the parent strain. Absolute improvements in the maximum specific growth rate and intrinsic resistance to streptomycin did not account for the observed growth advantage of all mutants. Rather, each mutant exhibited relative increases in specific growth rate at increasing concentrations of streptomycin. © 1996 John Wiley & Sons, Inc.
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  • 11
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    Biotechnology and Bioengineering 49 (1996), S. 197-203 
    ISSN: 0006-3592
    Keywords: catalytic bioreactor ; multistage tower ; pilot plant ; alcohol ; fixed bed ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: This article describes the development of an industrial-scale, multistage fixed-bed tower (MFBT) bioreactor using the promoter mineral kissiris for industrial alcohol production using free cells. Specifically, we examined the parameters needed to maintain operational stability from batch to batch for long periods. Pilot plant operations used one- and two-stage fixed-bed, 7000-L bioreactors. Likewise a 100,000-L, multistage fixed-bed tower system containing layered kissiris confirmed the laboratory results. Compared with a continuous stirred tank fermentor (CSTF) with recycle, a 30% reduction of energy demand and 10%-20% of the production costs are obtained. The latter are attributed to the increased ethanol concentration and alcohol productivity. © 1996 John Wiley & Sons, Inc.
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  • 12
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    Biotechnology and Bioengineering 49 (1996), S. 204-216 
    ISSN: 0006-3592
    Keywords: expanded bed adsorption ; bakers' yeast ; G6PDH ; STREAMLINE ion exchange adsorbents ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The use of expanded beds of STREAMLINE ion exchange adsorbents for the direct extraction of an intracellular enzyme glucose-6-phosphate dehydrogenase (G6PDH) from unclarified yeast cell homogenates has been investigated. It has been demonstrated that such crude feedstocks can be applied to the bed without prior clarification steps. The purification of G6PDH from an unclarified yeast homogenate was chosen as a model system containing the typical features of a direct extraction technique. Optimal conditions for the purification were determined in small scale, packed bed experiments conducted with clarified homogenates. Results from these experiments were used to develop a preparative scale separation of G6PDH in a STREAMLINE 50 EBA apparatus. The use of an on-line rotameter for measuring and controlling the height of the expanded bed when operated in highly turbid feedstocks was demonstrated. STREAMLINE DEAE has been shown to be successful in achieving isolation of G6PDH from an unclarified homogenate with a purification factor of 12 and yield of 98% in a single step process. This ion exchange adsorbent is readily cleaned using simple cleaning-in-place procedures without affecting either adsorption or the bed expansion properties of the adsorbent after many cycles of operation. The ability of combining clarification, capture, and purification in a single step will greatly simplify downstream processing flowsheets and reduce the costs of protein purification. © 1996 John Wiley & Sons, Inc.
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  • 13
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    Biotechnology and Bioengineering 49 (1996), S. 223-227 
    ISSN: 0006-3592
    Keywords: immobilized cells ; diffusivity measurement ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A simple correlation method has been developed to predict effective diffusivities of small molecules in heterogeneous materials such as immobilized cell systems. This correlation uses a single diffusivity measurement at one cell volume fraction to predict diffusivities for any other volume fraction of cell. The method has been applied to 20 sets of published diffusivity measurements in immobilized cell systems and accurately predicts affective diffusivities of molecules for the full range of cell fractions. It may also be used to predict effective diffusivities in heterogeneous materials in which the diffusivity of a molecule in each phase and the volume fraction of each phase are known. © 1996 John Wiley & Sons, Inc.
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  • 14
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    Biotechnology and Bioengineering 49 (1996), S. 259-265 
    ISSN: 0006-3592
    Keywords: hepatocytes ; lactose-derivatized polystyrene ; polystyrene ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Hepatocytes isolated from male Fisher 344VF rats were cultured on two substrates, collagen I and a lactose-derivatized polystyrene (PS-lactose), to compare morphological and functional differences. Hepatocyte morphology changed dramatically depending upon the substrate, shown through actin cytoskeletal staining and scanning electron microscopy. Functional assays performed included albumin secretion, reduced glutathione content, UDP-glucuronosyl transferase, and cytochrome P4501A1 activity. The presence of dexamethasone and dimethylsulfoxide (DMSO) in the media was required for the maintenance of several differentiated functions for cells cultured on collagen. In general, cells cultured on the PS-lactose substrate showed a much slower loss of function over the same period of time. The maintenance of differentiated function of cells on PS-lactose was enhanced with the addition of dexamethasone and DMSO. This is the first report of a culture system in which hepatocytes, cultured on a polymer substrate without additional protein coatings or media additives, have been able to maintain differentiated functions for up to 1 week. © 1996 John Wiley & Sons, Inc.
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  • 15
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    Biotechnology and Bioengineering 49 (1996), S. 266-276 
    ISSN: 0006-3592
    Keywords: Aspergillus oryzae ; submerged growth ; morphology ; pellet formation ; protein production ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The microscopic morphology, that is, total hyphal length and total number of tips, has been characterized during batch cultivations of Aspergillus oryzae. The specific growth rate estimated by measuring the total hyphal length (μh) corresponds well with the specific growth rate estimated from dry weight measurements during cultures grown as free hyphal elements. The average tip extension rate can be described with a saturation type kinetics with respect to the average total hyphal length, and the branching frequency is closely related to the total hyphal length. For the applied strain of A. oryzae, pellet formation occurs by coagulation of spores. The agglomeration process is pH dependent and pellets are formed at pH values higher than 5, whereas low pH (〈3.5) results in growth as freely dispersed hyphal elements. The maximum specific growth rate has a broad pH optimum between 3 and 7, whereas the α-amylase production has a sharper maximum at about pH 6. During batch cultivation with pellets the growth is described well by the cube-root law when pellet fragmentation can be neglected. The kinetic parameter k in the cube-root law is derived from the growth kinetics with no mass transfer limitation, k = μh/3. Based on an oxygen balance, the active growth layer in the pellet is estimated to be 200 to 325 μm and, consequently, up to 50% of the biomass is limited by oxygen for large pellets. Ethanol production (up to 1 g L-1) was observed during batch cultivations with pellets, suggesting that ethanol is produced in the oxygen limited part of the biomass. A constitutive, low α-amylase production was observed at high glucose concentration. The specific α-amylase production was significantly higher for filamentous growth than for pellets and oxygen appears to be necessary for production of α-amylase. © 1996 John Wiley & Sons, Inc.
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  • 16
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    Biotechnology and Bioengineering 49 (1996), S. 316-327 
    ISSN: 0006-3592
    Keywords: Saccharomyces cerevisiae ; glucose transport ; glucose-6-phosphate inhibition ; kinetic modeling ; in vivo kinetics ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In the present study, the glucose transport into the yeast Saccharomyces cerevisiae has been investigated. The approach suggested is based on a rapid sampling technique for studying the dynamic response of the yeast to rapid changes in extracellular glucose concentrations. For this purpose a concentrated glucose solution has been injected into a continuous culture at steady state growth conditions resulting in a shift of the extracellular glucose level. Samples have been taken every 5 s for determination of extracellular glucose and intracellular glucose-6-phosphate concentrations. Attempts to fit the experimental observations with simulations from existing models failed. The mechanism then proposed is based on a facilitated diffusion of glucose superimposed by an inhibition of glucose-6-phosphate. The use of the so-called in vivo approach suggested in this article appears to be proper, because the investigations can be performed at defined physiological states of the microbial cultures. Furthermore, the experimental observations are not being corrupted by the preparation of the samples for the transport studies as it happens during radioactive measurements. © 1996 John Wiley & Sons, Inc.
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  • 17
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    Biotechnology and Bioengineering 49 (1996), S. 309-315 
    ISSN: 0006-3592
    Keywords: surface charge ; proteins, modified ; partitioning in aqueous system ; thaumatin ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A series of charge-modified thaumatins with different values of surface charge were partitioned in aqueous two-phase systems (ATPS) to study the effect of surface charge as a single property on partitioning. Electrophoretic mobility of the proteins in titration curves was used as a measure of surface charge. Four modified proteins derived from thaumatin with the following values of isoelectric point: 8.70, 8.15, 5.60, and 4.50 were used for partitioning. The resolution of the systems in terms of protein surface charge was calculated. Partitioning of modified thaumatins in PEG 4000/dextran systems with phosphate buffer, Tris buffer, NaCl, KCl, and sulfate salts was carried out. Among the sulfate salts tested, the addition of 50 mM Li2SO4 to the system buffered with phosphate gave the highest value of resolution for differences in surface protein charge (RSPC). It shows a decrease in the value of K (partition coefficient) with an increase in the protein's charge. The addition of 100 mM KCl to the system promoted the opposite effect on the RSPC value. Charge-modified proteins were partitioned in PEG/salt systems to investigate the ability of these systems for resolving differences in surface charge. The PEG/citrate system seemed to have almost no ability for resolving proteins on the basis of surface charge differences; PEG/phosphate systems had some capability for resolving differently charged proteins. The more negative proteins tended to have higher values of K than the more positively charged fractions. The use of charge-modified proteins allowed the investigation of the effect of protein surface charge on partitioning in aqueous two-phase systems independently from other protein parameters as they were prepared from a common parent protein thaumatin. This technique provides an interesting novel tool to investigate the effect of protein surface charge on partitioning in ATPS taking protein charge as an independent parameter. © 1996 John Wiley & Sons, Inc.
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  • 18
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    Biotechnology and Bioengineering 49 (1996), S. 334-340 
    ISSN: 0006-3592
    Keywords: ohmic heating ; growth kinetics ; metabolic activity ; Lactobacillus acidophilus ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Lactobacillus acidophilus OSU133 was inoculated into MRS broth in a fermenter vessel and incubated at 30, 35, or 45°C with agitation. Incubation temperatures were attained by conventional or ohmic heating. An electrical current at low (15 V) or high (40 V) voltage was used to heat the culture directly during fermentations under ohmic heating. The growth parameters (lag period, minimum generation time, and maximum growth) and changes in pH were determined during fermentation. Metabolic activities (consumption of glucose and production of lactic acid and bacteriocin) were determined during fermentation at 35°C under both heating methods. Lag period for L. acidophilus was affected appreciably by the method of heating, but the magnitude of these changes depended on the fermentation temperature. When fermentation was done at 30°C, lag period decreased by 94% under low-voltage ohmic, compared with conventional, heating methods. Ohmic heating did not change the generation time significantly and caused slight, but significant (p 〈 0.01) decrease in maximum growth. Therefore, the electric current enhances the early stages, but it inhibits the late stages of growth. Ohmic, compared with conventional, heating resulted in higher final pH and lower bacteriocin activity in the fermented medium. However, ohmic heating at 35°C had minimal effect on glucose utilization and lactic acid production by L. acidophilus. Results show that measurement of the electric current when ohmic heating is done at a constant voltage may be used in monitoring such fermentations. In conclusion, ohmic heating is potentially useful in certain applications related to fermented foods. © 1996 John Wiley & Sons, Inc.
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  • 19
    ISSN: 0006-3592
    Keywords: trypsin ; immobilization ; molded support ; poly(glycidyl methacrylate-co-ethylene dimethacrylate) ; porous materials ; affinity chromatography ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Trypsin immobilization onto continuous “molded” rods of porous poly(glycidyl methacrylate-co-ethylene dimethacrylate) and some applications of the conjugate have been studied. The rods polymerized within a tubular mold (chromatographic column), were treated in situ with ethylenediamine, activated with glutaraldehyde and finally modified with trypsin. The performance of the trypsin-modified rods was evaluated and compared to that of poly(glycidyl methacrylate-co-ethylene dimethacrylate) beads, modified with the same enzyme. Overall the enzyme-modified rods performed substantially better than the corresponding beads. In particular, the performance of the molded supports as enzymatic reactors or as chromatographic media benefits greatly from the enhanced mass transfer that is characteristic of the molded rod at high flow rates. © 1996 John Wiley & Sons, Inc.
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  • 20
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    Biotechnology and Bioengineering 49 (1996), S. 377-382 
    ISSN: 0006-3592
    Keywords: hybridoma ; batch culture ; dichloroacetate ; metabolism ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We have studied the effect of the pyruvate dehydrogenase (PDH) activator, dichloroacetate (DCA), on the growth, metabolism, and productivity of the PQXB ½ hybridoma cell line. In control batch cultures, cessation of growth and the onset of decline phase coincided with the time at which the media became exhausted of glutamine. Supplementation of the media with DCA (1 mM) extended the growth phase of this cell line by approximately 20 h without affecting its growth rate. This prolonged period of growth resulted in an increased maximum cell density (16%) and final antibody yield (55%). Repeat experiments showed these effects to be reproducible, with the increases in antibody yield being between 50 and 60%. DCA did not affect the specific rates of glucose utilization and lactate production. However, it decreased the specific glutamine consumption rate. This characteristic of DCA action appeared, at least in part, to provide an explanation for the extended growth phase exhibited by DCA-treated cultures, since it delayed the time at which the media became depleted of glutamine. The consumption and production kinetics for various nutrients and their metabolites in both control and DCA-treated cultures suggested that: (1) glutamine catabolism proceeded by a pathway involving conversion to glutamate by glutaminase followed by subsequent transamination by alanine aminotransferase, and (2) DCA decreased the specific glutamine consumption rate by directly or indirectly inhibiting the transamination. It is expected that the routine inclusion of DCA in media used for hybridoma cultivation will be valuable for enhancement of monoclonal antibody (Mab) yields on a laboratory scale. © 1996 John Wiley & Sons, Inc.
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  • 21
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    Biotechnology and Bioengineering 49 (1996), S. 429-436 
    ISSN: 0006-3592
    Keywords: biotransformation ; L-phenylacetylcarbinol ; immobilization ; pyruvate decarboxylase ; Candida utilis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Biotransformation of benzaldehyde to L-phenylacetylcarbinol (L-PAC) as a key intermediate for L-ephedrine has been evaluated using immobilized pyruvate decarboxylase (PDC) from Candida utilis. PDC immobilized in spherical polyacrylamide beads was found to have a longer half-life compared with free enzyme. In a batch process, the immobilized PDC generally produced lower L-PAC than free enzyme at the same concentrations of substrates due to increased by-products acetaldehyde and acetoin and reduced benzaldehyde uptake. With immobilized PDC, L-PAC formation occurred at higher benzaldehyde concentrations (up to 300 mM) with the highest L-PAC concentration being 181 mM (27.1 g/L). For a continuous process, when 50 mM benzaldehyde and 100 mM sodium pyruvate were fed into a packed-bed reactor at 4°C and pH 6.5, a productivity of 3.7 mM/h (0.56 g/L · h) L-PAC was obtained at an average concentration of 30 mM (4.5 g/L). The half-life of immobilized PDC reactor was 32 days. © 1996 John Wiley & Sons, Inc.
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  • 22
    ISSN: 0006-3592
    Keywords: Streptomyces virginiae ; autoregulator ; virginiae butanolide ; virginiamycin fermentation ; optimization ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A strategy for optimization of non-growth-associated production in batch culture employing an empirical approach was developed through the study of virginiamycin production. The strategy is formulated with two aims: attaining a high cell concentration at the beginning of the production phase without decrease in production activity; and enhancing the production activity during the production phase. As a practical example, the goal of a maximum virginiamycin (M and S) production in the batch culture of Streptomyces virginiae was set. To attain a high cell concentration in the production phase of the batch culture, that is, to extend the growth phase for as long as possible, the optimum composition and concentration of the complex medium, especially the yeast extract (YE) concentration, were first investigated. Dissolved oxygen (DO) concentration control was also a parameter considered in maintaining the production activity during the production phase. In addition, to enhance the production activity, an optimum addition strategy of an autoregulator, virginiae butanolide-C (VB-C), was investigated. Combining these measures, the optimum cultivation conditions were found to be an initial YE concentration in the complex medium of 45 g/L, the shot addition of 300 μg/L of VB-C 11.5 h after the start of the batch culture, and a DO concentration maintained above 2 mg/L. The maximum concentrations of virginiamycin M and S were about ninefold those obtained under nonoptimum cultivation conditions. Nonoptimum cultivation conditions consisted of an initial YE concentration one sixth (7.5 g/L) that of the optimum cultivation conditions, and no VB-C addition. These conditions were used as representative of the standard cultivation of virginiamycin in this study. The strategy developed here will be applicable to the production of other antibiotics, especially to the cultivation of Streptomyces species, in which a hormonelike signal material (an autoregulator) plays an important role in antibiotic production. © 1996 John Wiley & Sons, Inc.
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  • 23
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    Biotechnology and Bioengineering 49 (1996), S. 456-466 
    ISSN: 0006-3592
    Keywords: microcarrier culture ; turbulent mixing ; 3-D particle tracking ; energy dissipation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Three-dimensional particle tracking velocimetry (3-D PTV), a modern, quantitative, visualization tool, has been applied to the characterization of the flow field in the impeller region of cell culture reactor vessels. The experimental system used here is a 250-mL microcarrier spinner vessel. The studies were conducted at three different agitation rates, 90, 150, and 210 rpm, corresponding to healthy, mildly damaging, and severely damaging shear intensities, respectively. The flow can be classified into three regions: a predominantly tangential (azimuthal) flow generated by the impeller; a trailing vortex region coming off the impeller tip; and a converging flow region close to the center of the vessel. The latter two are the regions of highest velocity gradients. Energy dissipation rates due to mean velocity gradients were also calculated to characterize the impeller stream. Local specific energy dissipation rates 〉 10,000 erg/(cm3sec) · have been measured. It is proposed that the critical regions for microcarrier culture damage due to impeller hydrodynamics are the trailing vortex region and the high energy converging flow region. Graphical representation of the mean velocity flow fields and the distribution of energy dissipation rates in the impeller region are also presented here. The merits of using the dissipation function (measure of specific energy dissipation rate) as a possible scale-up parameter are also discussed. © 1996 John Wiley & Sons, Inc.
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  • 24
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    Biotechnology and Bioengineering 49 (1996) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 25
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    Biotechnology and Bioengineering 49 (1996), S. 480-480 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 26
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    Biotechnology and Bioengineering 49 (1996), S. 481-494 
    ISSN: 0006-3592
    Keywords: Atropa belladonna ; biotransformation ; Duboisia leichhardtii × D. myoporoides, root-shoot coculture ; shooty teratoma ; tropane alkaloids ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Genetically transformed shooty teratomas of Atropa belladonna and a Duboisia leichhardtii × D. myoporoides hybrid were studied for biotransformation of tropane alkaloids in shake flasks and bioreactors. Although de novo synthesis of hyoscyamine and scopolamine was limited, shoots of both species were able to translocate and accumulate significant quantities of exogenous alkaloid. The maximum yield of scopolamine from hyoscyamine fed to the Duboisia hybrid shoots was 35% w/w; the yield of the scopolamine precursor, 6β-hydroxyhyoscyamine, was 37% w/w. Biotransformation activity was poor in A. belladonna shooty teratomas provided with exogenous hyoscyamine; however, scopolamine levels comparable with those in leaves of the whole plant accumulated in shoots fed with hairy root extract. Coculture of A. belladonna shooty teratomas and hairy roots in the same hormone-free medium was investigated as a means of providing a continuous source of hyoscyamine for conversion to scopolamine. Of the biotransformation systems tested with A. belladonna, coculture produced the highest levels of scopolamine and the highest scopolamine: hyoscyamine ratios. Cocultured shoots accumulated up to 0.84 mg g-1 dry weight scopolamine, or 3-11 times the average concentrations found in leaves of the whole plant. The scopolamine: hyoscyamine ratio in coculture ranged from 0.07 to 1.9, a significant improvement over levels of 0-0.03 normally found in A. belladonna hairy roots. Addition of Pluronic F-68 or copper sulfate to the medium and variation in initial medium pH did not improve hyoscyamine release from hairy roots. Scopolamine levels were increased using 1 μM copper sulfate or initial medium pH between 6.0 and 8.0; however, results from elicitation of hairy roots could not match the beneficial effect on scopolamine synthesis of root-shoot coculture. Addition of 0.001-1.0% (w/v) Pluronic F-68 to the roots reduced hyoscyamine release but postponed necrosis in the root tissue for up to 60 d. © 1996 John Wiley & Sons, Inc.
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  • 27
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    Biotechnology and Bioengineering 49 (1996), S. 535-543 
    ISSN: 0006-3592
    Keywords: whole cell biotransformation ; biocatalyst ; baker's yeast ; immobilization ; microencapsulation ; organic solvents ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Stable, semipermeable polyamide microcapsules were prepared by interfacial polymerization from a mixture of 1,6-hexanediamine and poly(allylamine) crosslinked with di-acid chlorides and were used to encapsulate baker's yeast. The size and distribution of cells within the capsules were investigated by a combination of laser confocal, electron scanning, and transmission electron microscopy. The encapsulated cells were studied as a biocatalyst for the model reduction of 1-phenyl-1,2-propanedione to 2-hydroxy-1-phenyl-1-propanone in a number of organic solvents. The polymerization conditions were extensively investigated and were found to greatly influence the product yield. Microencapsulated yeast cells, prepared under optimized conditions, carried out the reduction more efficiently than free cells as well as those immobilized in alginate and κ-carrageenan beads. The developed methodology should be broadly applicable to other biotransformations of interest. © 1996 John Wiley & Sons, Inc.
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  • 28
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    Biotechnology and Bioengineering 49 (1996), S. 544-552 
    ISSN: 0006-3592
    Keywords: glucose oxidase ; electropolymerization ; polypyrrole ; polyaniline ; polyindole ; polyphenylediamine ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Glucose oxidase was immobilized by electropolymerization into films of polyaniline, polyindole, polypyrrole, poly(o-phenylediamine), and polyaniline crosslinked with p-phenylenediamine. The kinetics and the behavior of the entrapped enzyme toward elevated temperature, organic solvent denaturation, and pH were investigated, along with the response of the films to electroactive species such as acetaminophen, ascorbate, cysteine, and uric acid. For most of the films, linearity to glucose extended from 7 to 10 mM. The poly(o-phenylenediamine)/glucose oxidase film gave the best signal/noise ratio and polypyrrole/glucose oxidase film gave the most reproducible current responses. No significant shift of the optimum reaction pH (5.5), except for polypyrrole (5.0), was observed after immobilization of glucose oxidase in the various films. Enzymatic activity decreased rapidly when pH was raised above 7.5. Thermodeactivation studies at 55°, 60°, and 65°C have shown polypyrrole/and poly(o-phenylediamine)/glucose oxidase films to be the most resistant enzymatic films. Poly(o-phenylenediamine) films offered the best protection against glucose oxidase deactivation in hexane, chloroform, ether, THF, and acetonitrile when compared with the other electropolymerized films. All the enzymatic films exhibited permselection toward electroactive species. © 1996 John Wiley & Sons, Inc.
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  • 29
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    Biotechnology and Bioengineering 49 (1996), S. 553-558 
    ISSN: 0006-3592
    Keywords: subtilisin ; acyl transfer reaction ; enzymatic peptide synthesis ; organic solvent ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Nucleophile specificity of subtilisin (subtilopeptidase A) was studied via acyl transfer reactions in acetonitrile containing piperidine and 10 vol% of water. Ac-Tyr-OEt was used as acyl donor and a series of amino acid derivatives, di- and tripeptides of the general structure Xaa-Gly, Gly-Xaa, Gly-Gly-Xaa (Xaa represents all natural L-amino acids except cysteine) were used as nucleophiles. The nucleophilic efficiencies of these peptides were characterized by the values of the apparent partition constants, papp, determined from the HPLC analysis of the reactions. The order of preference for the P′1 position was estimated to be: Gly 〉 hydrophilic, positively charged 〉 hydrophobic, aromatic 〉 negatively charged 〉 Leu 〉〉〉 Pro side chain. For the P′2 position the order of preference was: Gly 〉 hydrophilic, charged 〉 hydrophobic, aromatic 〉 Pro side chain. The values of papp for Gly-Gly-Xaa tripeptides cover a range of only two orders of magnitude, with lower nucleophile efficiency for those with hydrophobic amino acid residues in the P′3 position. The dipeptide with Pro in P′1 did not react at all, but a tripeptide having Pro in P′3 was a very good nucleophile. The negatively charged amino acid residues in the P′1 position result in very weak nucleophilic behavior, whereas the peptides with Asp or Glu in P′2 and P′3 are well accepted. Generally, peptides of the Gly-Xaa or Gly-Gly-Xaa series were better nucleophiles than peptides of the Xaa-Gly series. The length of the peptide chain or amidation of α-carboxyl function had no influence on nucleophilic behavior. No significant difference in nucleophile specificity between subtilopeptidase A and nagarse was observed. © 1996 John Wiley & Sons, Inc.
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  • 30
    ISSN: 0006-3592
    Keywords: lignocellulose ; biomass ; lignin degradation ; enzymatic hydrolysis ; furfural ; Aspergillus niger fermentation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The wet oxidation process of wheat straw has been studied as a pretreatment method to attain our main goal: To break down cellulose to glucose enzymatic, and secondly, to dissolve hemicellulose (e.g., for fermentation) without producing microbial inhibitors. Wet oxidation combined with base addition readily oxidizes lignin from wheat straw facilitating the polysaccharides for enzymatic hydrolysis. By using a specially constructed autoclave system, the wet oxidation process was optimized with respect to both reaction time and temperature. The best conditions (20 g/L straw, 170°C, 5 to 10 min) gave about 85% w/w yield of converting cellulose to glucose. The process water, containing dissolved hemicellulose and carboxylic acids, has proven to be a direct nutrient source for the fungus Aspergillus niger producing exo-β-xylosidase. Furfural and hydroxymethyl-furfural, known inhibitors of microbial growth when other pretreatment systems have been applied, were not observed following the wet oxidation treatment. © 1996 John Wiley & Sons, Inc.
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  • 31
    ISSN: 0006-3592
    Keywords: Saccharomyces cerevisiae ; hepatitis B surface antigen (HBsAg) ; continuous culture ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We have studied the growth rate dependence of hepatitis B surface antigen (HBsAg) p24s monomer and lipoprotein particle synthesis produced in Saccharomyces cerevisiae using galactose-limited continuous culture. The hepatitis B virus S gene, which encodes the p24s monomer, is transcribed under the control of the GAL 10p on a chimeric 2-μm plasmid harbored in a haploid yeast strain. Monomers autonomously form lipoprotein aggregates (particles) in vivo using only host-cell-derived components. Steady states were evaluated in a range from 0.015 h-1 to washout (0.143 h-1). Both p24s monomer and HBsAg particle levels, at steady state, varied in an inverse linear manner with growth rate. A consistent excess of total p24s monomer to HBsAg particle, estimated at five- to tenfold by mass, was found at all dilution rates. The average copy number of the 2-μm plasmid (carrying LEU2 selection) remained constant at 200 copies per cell from washout to 0.035 h-1. Surprisingly, the average copy number was undetectable at the lowest dilution rate tested (0.015 h-1), even though HBsAg expression was maximal. Total p24s monomer and HBsAg particle values ranged twofold over this dilution rate range. No differences in the trends for HBsAg expression and average copy number could be detected past the critical dilution rate where aerobic fermentation of galactose and ethanol overflow were observed. HBsAg expression in continuous culture was stable for at least 40 generations at 0.100 h-1. © 1996 John Wiley & Sons, Inc.
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  • 32
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    Biotechnology and Bioengineering 49 (1996), S. 601-610 
    ISSN: 0006-3592
    Keywords: aerobic ; anaerobic ; biomass separation ; bioreactor ; bubbleless ; oxygen mass transfer ; extraction of organic pollutants ; membrane ; wastewaters ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Combining membrane technology with biological reactors for the treatment of municipal and industrial wastewaters has led to the development of three generic membrane processes within bioreactors: for separation and recycle of solids; for bubbleless aeration of the bioreactor; and for extraction of priority organic pollutants from hostile industrial wastewaters. Commercial aerobic and anaerobic membrane separation bioreactors already provide a small footprint alternative to conventional biological treatment methods, producing a high-quality effluent at high organic loading rates. Both the bubbleless aeration and extractive membrane bioreactors are in the development stages. The former uses gas-permeable membranes to improve the mass transfer of oxygen to the bioreactor by providing bubbleless oxygen. By using a silicone membrane process, extractive membrane bioreactors transfer organic pollutants from chemically hostile wastewaters to a nutrient medium for subsequent biodegradation. All three membrane bioreactor (MBR) processes are comparatively and critically reviewed. © 1996 John Wiley & Sons, Inc.
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  • 33
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    Biotechnology and Bioengineering 49 (1996), S. 527-534 
    ISSN: 0006-3592
    Keywords: lipase ; immobilization ; sol-gel materials ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The commercial application of lipases as biocatalysts for organic synthesis requires simple but efficient methods to immobilize the enzyme, yielding highly stable and active biocatalysts which are easy to recover. In this study, we present a novel method to achieve lipase immobilization by entrapment in chemically inert hydrophobic silica gels which are prepared by hydrolysis of alkyl-substituted silanes in the presence of the enzyme. A typical immobilization procedure uses: an aqueous solution of lipase; sodium fluoride as a catalyst; and additives like polyvinyl alcohol or proteins and alkoxysilane derivatives like RSi-(OMe)3 with R = alkyl, aryl, or alkoxy as gel precursors. The effect of various immobilization parameters like stoichiometric ratio of water, silane, type and amount of additive, type and amount of catalyst, and type of silane has been carefully studied. The new method is applicable for a wide variety of lipases, yielding immobilized lipases with esterification activities enhanced by a factor of up to 88, compared to the commercial enzyme powders under identical conditions. Studies on the stability of sol-gel immobilized lipases under reaction conditions or storage (dry, in aqueous or organic medium) revealed an excellent retention of enzymatic activity. The possible reasons for the increased enzyme activities are discussed. © 1996 John Wiley & Sons, Inc.
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  • 34
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    Biotechnology and Bioengineering 49 (1996), S. 559-567 
    ISSN: 0006-3592
    Keywords: Acrosiphonia ; macroalgae ; tissue culture ; stirred-tank bioreactor ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A semidifferentiated tissue culture consisting of linear filaments in liquid suspension was established from Acrosiphonia coalita, a cold-water green macroalga known to express pharmacologically active oxylipins deriving from lipoxygenase metabolism of linolenic acid. The tissue was vegatively propagated by blending the filaments down to 1 to 5 mm in length prior to subculture. The filamentous A. coalita tissue suspension was successfully cultivated in an illuminated, 3-L stirred-tank bioreactor at 12°C, 0.46-vvm aeration rate, 250-rpm mixing speed, and incident illumination intensity of 77 μE m-2s-1. The mean specific growth rate over the exponential phase was 0.185 day-1 and a final cell density of 1083 mg dry cell weight (DCW) L-1 was achieved within 15 days of cultivation from an initial cell density of 200 mg DCW L-1. The addition of 3500 ppm CO2 to the aeration gas provided a maximum CO2 transfer rate of six times the maximum CO2 consumption rate and stabilized the pH to 8.0 during the light phase of growth, but did not improve biomass productivity. © 1996 John Wiley & Sons, Inc.
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  • 35
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    Biotechnology and Bioengineering 49 (1996), S. 587-598 
    ISSN: 0006-3592
    Keywords: gas phase bioreactor ; dynamic behavior ; waste air ; MEK ; MIBK ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In the work reported here, selected aspects of the dynamic behavior of biofilters for waste air treatment have been investigated. Emphasis was placed on transient state elimination of mixtures of methyl ethyl ketone (MEK) and methyl isobutyl ketone (MIBK) vapors and on explanation of the observed phenomena. The initial startup, the response of the biofilter to step changes in the pollutant loadings, responses to pollutant pulses, restarting after starvation, and the influence of step changes in gaseous phase oxygen partial pressure are presented and discussed. © 1996 John Wiley & Sons, Inc.
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  • 36
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    Biotechnology and Bioengineering 49 (1996) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
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    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 37
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    Biotechnology and Bioengineering 49 (1996), S. 611-620 
    ISSN: 0006-3592
    Keywords: anaerobic sludge ; coculture ; oxygen toxicity ; sludge activity ; wastewater treatment ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The impact of influent dissolved O2 on the characteristics of anaerobic granular sludge was investigated at various dissolved O2 concentrations (0.5-8.1 ppm) in 1- and 5-L laboratory-scale upflow anaerobic sludge bed (UASB)-like anaerobic/aerobic coupled reactors with a synthetic wastewater (carbon sources containing 75% sucrose and 25% acetate). The rate of dissolved O2 supplied to the coupled reactor was as high as 0.40 g O2/Lrx·d, and the anaerobic/aerobic coupled reactors maintained excellent methanogenic performances at a COD loading rate of 3 g COD/Lrx·d even after the reactors had been operated with dissolved O2 for 3 months. The activities of granular sludge on various substrates (glucose, propionate, and hydrogen) were not impaired, and acetate activity was even improved over a short term. However, after 3 months of operation, slight declines on the acetoclastic activities of granules were observed in the coupled reactor receiving the recirculated fluid containing 8.1 ppm dissolved O2.Methane yield in the anaerobic control reactor and anaerobic/aerobic coupled reactors revealed that a significant aerobic elimination (up to 30%) of substrate occurred in the coupled reactors, as expected. The presence of dissolved O2 in the recirculated fluid resulted in the development of fluffy biolayers on the granule surface, which imposed a negative impact on the settleability of granular sludge and caused a slightly higher sludge washout. This research shows that the anaerobic/aerobic coupled reactor can be successfully operated under O2-limited conditions and is an ideal engineered ecosystem integrating oxic and anaerobic niches. © 1996 John Wiley & Sons, Inc.
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  • 38
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    Biotechnology and Bioengineering 49 (1996), S. 621-628 
    ISSN: 0006-3592
    Keywords: Kluyveromyces ; Candida utilis ; Kluyver effect ; chemostat ; biomass ; whey ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Many facultatively fermentative yeast species exhibit a “Kluyver effect”: even under oxygen-limited growth conditions, certain disaccharides that support aerobic, respiratory growth are not fermented, even though the component monosaccharides are good fermentation substrates. This article investigates the applicability of this phenomenon for high-cell-density cultivation of yeasts. In glucose-grown batch cultures of Candida utilis CBS 621, the onset of oxygen limitation led to alcoholic fermentation and, consequently, a decrease of the biomass yield on sugar. In maltose-grown cultures, alcoholic fermentation did not occur and oxygen-limited growth resulted in high biomass concentrations (90 g dry weight L-1 from 200 g L-1 maltose monohydrate in a simple batch fermentation). It was subsequently investigated whether this principle could also be applied to Kluyveromyces species exhibiting a Kluyver effect for lactose. In oxygen-limited, glucose-grown chemostat cultures of K. wickerhamii CBS 2745, high ethanol concentrations and low biomass yields were observed. Conversely, ethanol was absent and biomass yields on sugar were high in oxygen-limited chemostat cultures grown on lactose. Batch cultures of K. wickerhamii grown on lactose exhibited the same growth characteristics as the maltose-grown C. utilis cultures: absence of ethanol formation and high biomass yields. Within the species K. marxianus, the occurrence of a Kluyver effect for lactose is known to be strain dependent. Thus, K. marxianus CBS 7894 could be grown to high biomass densities in lactose-grown batch cultures, whereas strain CBS 5795 produced ethanol after the onset of oxygen limitation and, consequently, yielded low amounts of biomass. Because the use of yeast strains exhibiting a Kluyver effect obviates the need for controlled substrate-feeding strategies to avoid oxygen limitation, such strains should be excellently suited for the production of biomass and growth-related products from low-cost disaccharide-containing feedstocks. © 1996 John Wiley & Sons, Inc.
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  • 39
    ISSN: 0006-3592
    Keywords: lysine ; thermotolerant ; methylotroph ; Bacillus methanolicus ; kinetic model ; three-phase ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A simulation was developed based on experimental data obtained in a 14-L reactor to predict the growth and L-lysine accumulation kinetics, and change in volume of a large-scale (250-m3) Bacillus methanolicus methanol-based process. Homoserine auxotrophs of B. methanolicus MGA3 are unique methylotrophs because of the ability to secrete lysine during aerobic growth and threonine starvation at 50°C. Dissolved methanol (100 mM), pH, dissolved oxygen tension (0.063 atm), and threonine levels were controlled to obtain threonine-limited conditions and high-cell density (25 g dry cell weight/L) in a 14-L reactor. As a fed-batch process, the additions of neat methanol (fed on demand), threonine, and other nutrients cause the volume of the fermentation to increase and the final lysine concentration to decrease. In addition, water produced as a result of methanol metabolism contributes to the increase in the volume of the reactor. A three-phase approach was used to predict the rate of change of culture volume based on carbon dioxide production and methanol consumption. This model was used for the evaluation of volume control strategies to optimize lysine productivity. A constant volume reactor process with variable feeding and continuous removal of broth and cells (VFcstr) resulted in higher lysine productivity than a fed-batch process without volume control. This model predicts the variation in productivity of lysine with changes in growth and in specific lysine productivity. Simple modifications of the model allows one to investigate other high-lysine-secreting strains with different growth and lysine productivity characteristics. Strain NOA2#13A5-2 which secretes lysine and other end-products were modeled using both growth and non-growth-associated lysine productivity. A modified version of this model was used to simulate the change in culture volume of another L-lysine producing mutant (NOA2#13A52-8A66) with reduced secretion of end-products. The modified simulation indicated that growth-associated production dominates in strain NOA2#13A52-8A66. © 1996 John Wiley & Sons, Inc.
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  • 40
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    Biotechnology and Bioengineering 52 (1996), S. 161-165 
    ISSN: 0006-3592
    Keywords: yeast ; signaling ; regulation ; catabolite repression ; metabolism ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In this article, knowledge concerning the relation between uptake of and signaling by glucose in the yeast Saccharomyces cerevisiae is reviewed and compared to the analogous process in prokaryotes. It is concluded that (much) more fundamental knowledge concerning these processes is required before rational redesign of metabolic fluxes from glucose in yeast can be achieved. © 1996 John Wiley & Sons, Inc.
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  • 41
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    Biotechnology and Bioengineering 52 (1996) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
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  • 42
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    Biotechnology and Bioengineering 52 (1996), S. 176-182 
    ISSN: 0006-3592
    Keywords: intracellular pH ; 31P-NMR ; nitrite toxicity ; denitrification ; Pseudomonas fluorescens ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In vivo 31P-NMR was used to investigate the basis for the inhibition of denitrification by nitrite accumulated endogenously by Pseudomonas fluorescens ATCC 17822 (biotype II) at pH 7.0. Cells were immobilized in κ-carrageenan to obtain high cell concentrations in the NMR tube. Acetate and nitrate in two concentration ratios were supplied as electron donor and acceptor, respectively, to achieve different levels of nitrite accumulation. During denitrification, cells were able to maintain a pH gradient of approximately 0.4 to 0.5 units, but when nitrite accumulation reached values approximating 27 mM the transmembrane ΔpH collapsed sharply. Nitrite stimulated the reduction rate of nitrate; furthermore, at nitrite concentrations below 1 mM, activation of oxygen respiratory rates was observed in cells grown under aerobic conditions. The results provide evidence for nitrite acting as a protonophore (an uncoupler that increases the proton permeability of membranes by a shuttling mechanism). © 1996 John Wiley & Sons, Inc.
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  • 43
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    Biotechnology and Bioengineering 52 (1996), S. 1-2 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 44
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    Biotechnology and Bioengineering 52 (1996), S. 166-175 
    ISSN: 0006-3592
    Keywords: bcl-2 ; apoptosis ; cell culture ; metabolic engineering ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Cell lines derived from the hemopoetic lineages are widely used as hosts for the production of biologicals. These cell lines have been demonstrated to undergo high levels of the active death program commonly referred to as apoptosis. The effects of overexpression of the apoptosis suppressor gene bcl-2 on the properties of a Burkitt lymphoma were compared with the control cell line (transfected with a negative control plasmid) under a variety of conditions relevant to cell culture production technology. In stationary batch cultures, there was a clear reduction in both the rate of total cell death and the level of apoptosis during the decline phase of the bcl-2 transfected cell cultures as compared with that of the control cell cultures. Nutrient analysis revealed that the onset of death during the control cell cultures occurred following complete exhaustion of glutamine. However, the bcl-2 transfected cell cultures continued to grow even though glutamine had been exhausted, and a significant decline in viability only occurred when glucose had also been completely exhausted.When cells were cultured in suspension without prior adaptation, the bcl-2 transfected cells grew significantly better, suggesting that the bcl-2 gene protected the cells from apoptosis triggered by either the lack of substrate or the hydrodynamic environment. Fluorescence microscopy revealed that death of the control cells was almost entirely by apoptosis, whereas death was almost exclusively by necrosis in the delayed decline phase of the transfected cell cultures. In both instances, death occurred before total exhaustion of glucose and glutamine.The induction of apoptosis following growth arrest is a major impediment to the development of culture strategies that optimize specific productivity by reducing the growth rate. Results presented here suggest that suppression of apoptosis by bcl-2 under the condition of excess thymidine allows the maintenance of cells in a growth-arrested state for much longer than would otherwise be possible.When cells were transferred to a range of commercial serum-free media, cell growth was, in all cases, much better for the bcl-2 transfected cell line. Moreover, when cells were cultivated in glutamine-free medium, the control cells exhibited a decrease in viable cell number within the first 24 h whereas, for the bcl-2 transfected cell cultures, viable cell number did not exhibit any clear decrease until after 75 h. Clearly, these results indicate that the metabolic engineering approach can be used to alter advantageously the survival and proliferative capacity of cells in cell culture environments. © 1996 John Wiley & Sons, Inc.
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  • 45
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    Biotechnology and Bioengineering 52 (1996), S. 185-192 
    ISSN: 0006-3592
    Keywords: aqueous micellar system ; hydrophilic protein ; excluded-volume interactions ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We review our recent experimental and theoretical work aimed at investigating the potential use of two-phase aqueous micellar systems for the separation or concentration of hydrophilic biomaterials using the principle of liquid-liquid extraction. The systems studied include (1) a two-phase aqueous micellar system composed of the nonionic surfactant n-decyl tetra(ethylene oxide) (C10E4) and (2) a two-phase aqueous micellar system composed of the zwitterionic surfactant dioctanoyl phosphatidyl-choline (C8-lecithin). The experimental partitioning behavior of several hydrophilic proteins, including cytochrome c, soybean trypsin inhibitor, ovalbumin, bovine serum albumin, and catalase, in two-phase aqueous C10E4 and C8-lecithin micellar systems is reviewed. A theoretical formulation of the protein partitioning behavior, based on a description of excluded-volume interactions between the hydrophilic proteins and the micelles, is also reviewed. The theoretically predicted protein partitioning behavior is compared with that observed experimentally and is found to be in good agreement. The results of our investigation suggest that two-phase aqueous micellar systems of the type examined in this article are indeed potentially useful as extractant phases for the separation or concentration of proteins and other biomaterials. © 1996 John Wiley & Sons, Inc.
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  • 46
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    Biotechnology and Bioengineering 52 (1996), S. 204-222 
    ISSN: 0006-3592
    Keywords: protein purification ; ion exchange chromatography ; metal ion affinity ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: This study documents several alternative approaches for the optimization of the ion-exchange and affinity chromatographic purification of proteins. In these approaches, the chromatographic process has been treated as a four-stage (adsorption, washing, elution, and regeneration) operation. Central to these investigations has been the elaboration of practical iterative procedures based on the use of theoretical models describing each of these stages. Predictions derived from these models have then been evaluated in terms of experimental data obtained using batch adsorption measurements in finite bath configurations and frontal breakthrough measurements with packed beds of different dimensions, containing nonporous and porous adsorbents of different selectivities and capacities for proteins. Commencing with the kinetic and distribution parameters derived from batch equilibrium measurements, the effect of the initial concentration of the target protein, the solid-liquid volume ratio, the superficial velocity and the column dimensions on the pressure drop, production rate, concentration profile, column utilization, and yield have been determined with packed beds. The potential of these iterative approaches to simplify the determination of key mass transfer and interaction parameters required for scale-up and economic optimization of chromatographic purifications of proteins has been examined using ion exchange, immobilized metal ion affinity, and triazine dye pseudo-affinity adsorbents of different selectivity and adsorption capacities. © 1996 John Wiley & Sons, Inc.
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  • 47
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    Biotechnology and Bioengineering 52 (1996), S. 193-203 
    ISSN: 0006-3592
    Keywords: protein aggregation ; protein formulation ; specific interaction sites ; excipient screening ; affinity chromatography ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We describe a new protein characterization technique called self-interaction chromatography (SIC), which exploits the specificity of protein-protein interactions that is common to protein aggregates and enables the rapid screening of protein formulation additives as physical stabilizers against aggregation. This technique also enables the identification of specific interaction sites and the determination of their relative importance for self-association. Mannitol, glycine, and dextran 40 were tested for their stabilizing effect toward the model protein lysozyme. Dextran 40 exhibited a poor stabilizing effect. While mannitol stabilized both the native and acid-denatured forms of lysozyme, glycine stabilized the native form with respect to the denatured species. These results are in good agreement with findings in the formulation literature. The SIC shows tremendous potential as a rapid formulation development tool. We also screened two putative interaction sites for involvement in the self-association of lysozyme and estimated the associated binding energies using a binding isotherm model that we developed. The sites screened consisted of residues 41-48 and 125-128 and were selected based on their apparent importance in forming crystal contacts in several different crystal forms of lysozyme. Of the two sites, only residues 125-128 were found to influence self-association under the conditions we employed. Because the success of this technique depends on the exploitation of self-interactions between native species, several important applications are also suggested such as separating native from misfolded or variant species and probing site utilization in aggregation versus crystallization phenomena. © 1996 John Wiley & Sons, Inc.
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  • 48
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    Biotechnology and Bioengineering 50 (1996), S. 65-72 
    ISSN: 0006-3592
    Keywords: somatic embryo ; plant cell culture ; image analysis ; pattern recognition ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Somatic embryogenesis is among the most promising means of large scale plant micropropagation. The development of somatic embryos is characterized by their morphological changes. Embryos in culture usually exhibit high heterogeneity and abnormality. As conventional microscopic observation is laborious and subjective, an objective and quantitative morphokinetic description is important for further advancement of this important process technology. We developed an image analysis system capable of measuring morphological and size features of embryos. Subtle environmental effects on embryo development, which are often masked by the subjectivity of microscopic observation, are now discernible by statistically comparing the distributions of these morphological and size features. This image analysis and pattern recognition system was applied to examine the kinetics of a fed-batch culture. © 1996 John Wiley & Sons, Inc.
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  • 49
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    Biotechnology and Bioengineering 50 (1996), S. 91-97 
    ISSN: 0006-3592
    Keywords: waste-gas treatment ; trickle-bed reactor ; fungi ; biofilm ; toluene ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Removal of organic compounds like toluene from waste gases with a trickle-bed reactor can result in clogging of the reactor due to the formation of an excessive amount of biomass. We therefore limited the amount of nutrients available for growth, to prevent clogging of the reactor. As a consequence of this nutrient limitation a lower removal rate was observed. However, when a fungal culture was used to inoculate the reactor, the toluene removal rate under nutrient limiting conditions was higher. Over a period of 375 days, an average removal rate of 27 g C/(m3 h) was obtained with the reactor inoculated with the fungal culture. From the carbon balance over the reactor and the nitrogen availability it was concluded that, under these nutrient-limited conditions, large amounts of carbohydrates are probably formed. We also studied the application of a NaOH wash to remove excess biomass, as a method to prevent clogging. Under these conditions an average toluene removal rate of 35 g C/(m3 h) was obtained. After about 50 days there was no net increase in the biomass content of the reactor. The amount of biomass which was formed in the reactor equaled the amount removed by the NaOH wash. © 1996 John Wiley & Sons, Inc.
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  • 50
    ISSN: 0006-3592
    Keywords: algal culture ; bioreactor ; bioregenerative system ; energy economy ; light-emitting diode (LED) ; microsecond pulse modulation ; Chlorella pyrenoidosa ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Light-emitting diodes (LEDs) were used as the sole light source in continuous culture of the green alga Chlorella pyrenoidosa. The LEDs applied show a peak emission at 659 nm with a half-power bandwidth of 30 nm. Selection of this wavelength range, which is optimal for excitation of chlorophylls a and b in their “red” absorption bands makes all photons emitted potentially suitable for photosynthesis. No need for additional supply of blue light was found. A standardized panel with 2 LEDs cm-2 fully covered one side of the culture vessel. At standard voltage in continuous operation the light output of the diode panel appeared more than sufficient to reach maximal growth. Flash operation (5-μs pulse duration) enables potential use of higher operating voltages which may render up to three times more light output. Flat airlift fermentor-type continuous culture devices were used to estimate steady state growth rates of Chlorella pyrenoidosa as a function of the light flux (μmol photons · m-2 · s-1) and the flashing frequency of the light-emitting diodes (which determines the duration of the dark “off” time between the 5-μs “on” pulses). At the fixed voltage and turbidostat setting applied a 20-kHz frequency, which equals dark periods of 45 μs, still permitted the maximum growth rate to become nearly reached. Lower frequencies fell short of sustaining the maximal growth rate. However, the light flux decrease resulting from lowering of the flash frequency appeared to reduce the observed growth rates less than in the case of a similar flux decrease with light originating from LEDs in continuous operation. Flash application also showed reduction of the quantum requirement for oxygen evolution at defined frequencies. The frequency domain of interest was between 2 and 14 kHz. LEDs may open interesting new perspectives for studies on optimization of mixing in mass algal culture via the possibility of separation of interests in the role of modulation on light energy conversion and saturation of nutrient supply. Use of flashing LEDs in indoor algal culture yielded a major gain in energy economy in comparison to luminescent light sources. © 1996 John Wiley & Sons, Inc.
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  • 51
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    Biotechnology and Bioengineering 50 (1996) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
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  • 52
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    Biotechnology and Bioengineering 50 (1996), S. 207-210 
    ISSN: 0006-3592
    Keywords: chitosan ; solid-state fermentation ; Lentinus edodes ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A method for the laboratory-scale production and isolation of chitosan (polyglucosamine) by liquid and solidstate fermentation from Lentinus edodes was developed. The yields of isolated chitosan were 120 mg/L of fermentation medium under liquid fermentation conditions and 6.18 g/kg of fermentation medium under solid-state fermentation conditions. The latter method, which gives up to 50 times yields than other chitosan production methods from fungi, provides a new flexible and easily scaledup procedure for the production of low acetylation degree chitosan. © 1996 John Wiley & Sons, Inc.
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  • 53
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    Biotechnology and Bioengineering 50 (1996), S. 217-221 
    ISSN: 0006-3592
    Keywords: Qβ phage ; molecular evolution ; phage display ; continuous culture ; cellstat ; wall growth ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Lytic coliphage Qβ was grown in continuously cultured host bacteria using a cascade of stirred flow reactors. The apparatus was constructed so that the steady stream of exponentially growing bacterial cells passing through the stirred flow reactors served to prevent coevolution brought about by host-parasite interactions. Wall growth was the primary cause for deviation from ideal continuous culture conditions and is largely dependent on the surface structure of the host bacteria. Using an Escherichia coli strain deficient in adhesive type I pili expression, the desynchronization of single burst events could easily be followed over the course of four infection latency periods. Computer simulations based on a two-stage model for the Qβ infection cycle were in perfect agreement with the experimental data. Applications of the optimized system to strategies of molecular evolution are discussed. © 1996 John Wiley & Sons, Inc.
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  • 54
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    Biotechnology and Bioengineering 50 (1996), S. 238-247 
    ISSN: 0006-3592
    Keywords: hybridomas ; monoclonal antibody ; kinetic model ; instability ; nutrient and product effects ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An attempt has been made to mathematically describe and analyze monoclonal antibody (MAB) productivity of hybridoma cells, with particular emphasis on continuous cultures under unsteady-state conditions. A simple and unstructured general kinetic model that takes account of productivity loss during long-term cultivation, cell proliferation, and the effects of nutrients and toxic products is proposed. The model is verified with data of continuous culture from five different cell lines under a wide range of experimental conditions. Analysis of these results showed that for a reliable assessment of effects of different factors and for comparison of kinetic data on MAB production it is important to consider possible loss of MAB productivity, the time dependence of which can be modeled by an exponential function plus a constant term. Variations of nutrient concentration, particularly that of glucose, glutamine, and serum, can significantly alter MAB production under certain conditions. These effects can be described in terms of saturation kinetic and/or noncompetitive inhibition kinetics. © 1996 John Wiley & Sons, Inc.
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  • 55
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    Biotechnology and Bioengineering 50 (1996), S. 229-237 
    ISSN: 0006-3592
    Keywords: cell cycle analysis ; foreign gene expression ; MMTV promoter control ; recombinant mouse cells ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The cell cycle dependency of foreign gene expression in recombinant mouse L cells was investigated. Two different recombinant mouse L cell lines having the glucocorticoid receptor-encoding gene and the lacZ reporter gene were used in this study. The lacZ gene expression was controlled by the glucocorticoid-inducible mouse mammary tumor virus (MMTV) promoter in both cell lines. In “M4” cells the gr gene was under the control of another MMTV promoter, but in “R2” cells it was under the control of the constitutive Rous sarcoma virus promoter. These normally attachment-grown cells were adapted to suspension culture, and a dual-laser flow cytometer was used to simultaneously determine the DNA and foreign protein (β-galactosidase) content of single living cells. Expression of β-galactosidase as a function of cell cycle phase was evaluated for cells in exponential growth without any addition of the glucocorticoid inducer, dexamethasone. Cell cycle positions in the S phase were estimated on the basis of DNA content per cell, and position in the G1 phase was estimated on the basis of cell size as measured by pulse-width time of flight. The results showed that β-galactosidase synthesis occurred through all cell cycle phases, but the expression rate in the G1 phase was much lower than that in the S and G2/M phases in both cell lines. On the basis of cell size analysis, β-galactosidase expression in M4 cells (with autoinducible promoter) was found to be higher than that in R2 cells (with inducible promoter) during the G1 phase. © 1996 John Wiley & Sons, Inc.
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  • 56
    ISSN: 0006-3592
    Keywords: recombinant fusion protein ; chemical cleavage ; hydroxylamine ; insulin-like growth factor-I ; protein modification ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The application of gene fusion technology for the production of heterologous proteins in Escherichia coli has required the development of specific cleavage methods to separate the coexpressed fusion protein partner from the protein of interest. When hydroxylamine is used to cleave Asn-Gly fusion protein linkages, undesirable chemical modification of asparagine and glutamine amino acids can also occur. In this study, hydroxylamine cleavage conditions were modified to minimize unwanted chemical heterogeneity that occurred during the cleavage of the fusion protein [Met1]-pGH(1-11)-Val-Asn-IGF-I (Long-IGF-I). The cleavage reaction was shown to be dependent on the hydroxylamine concentration, temperature, and pH. Optimal cleavage conditions were identified that resulted in very low levels of chemical heterogeneity, but under these mild conditions that cleavage of the labile Asn-Gly bond was reduced. Therefore, the reaction was further modified to improve the yield of IGF-I while minimizing chemical heterogeneity. The yield of unmodified IGF-I was improved from less than 25% to greater than 70%. Analysis of the heterogeneity produced using the modified cleavage technique showed that Asn26 was converted to a hydroxamate. This variant was characterized in refolding and biological assays where it was equivalent to IGF-I. To further assess the effectiveness of the modified cleavage technique and to evaluate the potential for process scale-up, a gram-scale cleavage reaction of Long-IGF-I was carried out. The process yielded IGF-I with a low level of chemical heterogeneity that was easily removed by ion-exchange chromatography. Moreover, this work shows that the production of unmodified IGFs using hydroxylamine cleavage of fusion proteins is facilitated using the mild cleavage reaction. © 1996 John Wiley & Sons, Inc.
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  • 57
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    Biotechnology and Bioengineering 50 (1996), S. 280-290 
    ISSN: 0006-3592
    Keywords: extractive fermentation ; poly(ethyleneimine) ; aqueous two-phase system ; lactic acid ; Lactococcus lactis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The potential of an aqueous two-phase system composed of a polycation, poly(ethyleneimine) (PEI), and an uncharged polymer, (hydroxyethyl) cellulose (HEC), for extractive lactic acid fermentation was tested. Batch fermentation with 20 g/L glucose in two-phase medium using Lactococcus lactis without external pH control resulted in 3-4 times higher amount of lactate and biomass produced as compared to that in a conventional one-phase medium. Lactic acid was preferentially partitioned to the PEI-rich bottom phase. However, the cells which favored the HEC-rich top phase in a fresh two-phase medium were partitioned to a significant extent to the bottom phase after fermentation. Addition of phosphate buffer or pH adjustment to 6.5 after fermentation caused fewer cells to move to the bottom phase. With external pH control, fermentation in normal and two-phase medium showed no marked differences in glucose consumption and lactic acid yield, except that about 1.3 times higher cell density was obtained in the two-phase broth, especially at initial glucose concentrations of 50-100 g/L. Use of higher concentration of phosphate during batch fermentation in the two-phase medium with 50 g/L sugar provided a 15% higher yield of lactic acid, but the growth rate of cells was nearly half of the normal, thus affecting the productivity. Continuous fermentation with twice the normal phosphate concentration resulted in higher cell density, product yield, and productivity in two-phase medium than in monophasic medium. © 1996 John Wiley & Sons, Inc.
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  • 58
    ISSN: 0006-3592
    Keywords: metabolic engineering ; CHO cell ; E2F-1 ; serum-free cell culture ; two-dimensional electrophoresis of proteins ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Engineering of the cell cycle can be an effective means for bypassing growth factor requirements of animal cells. Cloned human E2F-1 from Nalm 6 cells was subcloned into pRc/CMV and transfected into Chinese hamster ovary (CHO) cells. Ten stable transfectant clones isolated from cells cultured under neomycin-resistance selection pressure all expressed significantly higher amounts of E2F-1 than control cells as determined by Western analysis. Confocal immunofluorescent microscopy and Southern analysis of several clones also provided evidence for the expression of cloned E2F-1 in these cells. CHO K1:E2F-1 cells are able to proliferate on well-defined serum- and protein-free basal medium and exhibit an S-phase extended by 65% compared to CHO K1 cells mitogenically stimulated by basic fibroblast growth factor (bFGF). Two-dimensional electrophoresis of the intracellular proteins of E2F-1 clones shows an increase in 236 gene products compared to CHO K1 control cells, further verifying a functional regulatory role of cloned E2F-1 in CHO cells. Among these upregulated species is the cell cycle regulatory protein, cyclin A, which has already been shown to be regulated by E2F-1 in human fibroblasts. Overexpression of cloned E2F-1 in CHO cells is a potentially useful new strategy for bypassing serum requirements in mammalian cell culture. Furthermore, such cell cycle control stimulus-protein pattern response data can contribute to a clearer understanding of complex multigene networks involved in mammalian cell cycle regulation. © 1996 John Wiley & Sons, Inc.
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  • 59
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    Biotechnology and Bioengineering 50 (1996), S. 329-335 
    ISSN: 0006-3592
    Keywords: active-site titration ; serine proteases ; organic solvents ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Calculation of kinetic constants of an enzymatic reaction in organic solvents requires knowledge of the functional active-site concentration in organic solvents, and this can be significantly different than that in water. An experimental method for active-site titration of serine proteases in organic media has been developed based on the kinetics of inhibition by phenylmethanesulfonyl fluoride (PMSF), a serine-specific inhibitor (or suicide substrate). This kinetic approach is fundamentally different from other techniques that require complete titration of all accessible enzyme active sites. This active site titration method was applied to subtilisins BPN′ and Carlsberg and α-chymotrypsin and resulted in fractions of active sites that ranged from 8 to 62% (of the fraction active in water) depending on the enzyme, the method of enzyme preparation, and the organic solvent used. The active-site concentration of subtilisin BPN′ and Carlsberg increased with increasing hydrophobicity of the solvent and with increasing solvent hydration in tetrahydrofuran. The dependence of the fraction of active sites on the nature of the organic solvent appears to be governed largely by solvent-induced inactivation caused by direct interaction of a hydrophilic solvent with the enzyme. © 1996 John Wiley & Sons, Inc.
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  • 60
    ISSN: 0006-3592
    Keywords: metabolic flux ; hybridoma cells ; mass balances ; biosynthesis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The estimation of the intracellular fluxes of mammalian cells using only the mass balances of the relevant metabolites is not possible because the set of linear equations defined by these mass balances is underdetermined. Either additional experimental flux data or additional theoretical constraints are required to find one unique flux distribution out of the solution space that is bound by the mass balances. Here, a method is developed using the latter approach. The uptake and production rates of amino acids, glucose, lactate, O2, CO2, NH4, MAB, and the intracellular amino acid pools have been determined for two different steady-states. The cellular composition {total protein and protein composition, total lipids and fatty acid distribution, total carbohydrates, DNA and RNA} has been measured to calculate the requirements for biosynthesis. It is shown to be essential to determine the uptake/production rates of ammonia and either carbon dioxide or oxygen. In mammalian cells these are cometabolites of cyclic metabolic pathways. The flux distribution that is found using the Euclidean minimum norm as the additional theoretical constraint and taking either the CO2 or the NAD(P)H mass balance into account is shown to be in agreement with the measured O2 and CO2 metabolic rates.The metabolic fluxes in hybridoma cells in continuous culture at a specific growth rate of 0.83 day-1 are estimated for a medium with (optimal medium) and without (suboptimal medium) Primatone RL, an enzymatic hydrolysate of animal tissue that causes a more than twofold increase in cell density. It is concluded that (i)The majority of the consumed glucose (〉90%) is channeled through the pentose-phosphate pathway in rapidly proliferating cells.(ii)Pyruvate oxidation and tricarboxylic acid (TCA) cycle activity are relatively low, i.e., 8% of the glucose uptake in suboptimal and 14% in optimal medium, respectively. Under both conditions, only a small fraction of pyruvate is further oxidized to CO2.(iii)The flux from glutamate to α-ketoglutarate (catalyzed by glutamate dehydrogenase) is almost zero in medium with and even slightly reversed in medium without Primatone RL. Almost all glutamate enters the TCA cycle due to the action of transaminases.(iv)Transhydrogenation plays a significant role in hybridoma cells under our experimental conditions. NADPH is produced at relatively high rates (11 × 10-12 to 13 × 10-12 mol · cell-1 · day-1) compared to other fluxes in both culture media. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 52 (1996), S. 357-363 
    ISSN: 0006-3592
    Keywords: chromium ; chromate ; naphthalene ; reduction ; kinetics ; model ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A mixed culture of Bacillus sp. K1 and Sphingomonas paucimobilis EPA 505 was exposed to chromate and naphthalene. Batch experiments showed that chromate was reduced and naphthalene was degraded by the mixed culture. Chromate reduction occurred initially at a high rate followed by a decrease in rate until chromate reduction ceased. Chromate reduction decreased in the mixed culture when a lower ratio of S. paucimobilis EPA 505 to Bacillus sp. K1 was utilized. A kinetic model incoporating a term for the cell density ratio is proposed to describe chromate reduction in the mixed culture under both chromate limited and electron donor limited conditions. The validity of the model, and its parameter values, was verified by experimental data generated under a variety of initial population compositions and a broad range of chromate concentrations. The consistent result of experimental data with model predictions implies that the model is useful for evaluating the interactions and the use of mixed culture for chromate removal. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 52 (1996), S. 364-372 
    ISSN: 0006-3592
    Keywords: fiber optic ; firefly luciferase ; in situ ; luminescence ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A method was developed to provide a real-time measurement of intracellular adenosine 5′-triphosophate (ATP) concentrations in growing Escherichia coli. The bacteria to be monitored must first be modified by inserting the cDNA for firefly luciferase expressed from a constitutive promoter. Such a construct leads to constant specific activity of firefly luciferase during both the lag phase and exponential growth. When the luciferase substrate, D-luciferin, is added to the medium, ATP within the cells is utilized in the luciferase-catalyzed reaction that produces light. The light is carried from the bioreactor to a computer-based detector by an optical fiber. The detected per cell light emission varies during exponential growth. Analysis of cytoplasm extracts shows that this variance is related to changes in the ATP concentration, which ranges from 1 to 6 times the literature value for KM. Experimental analyses demonstrated that inner filter effects are not a significant factor affecting the use of this system. The method was tested in a benchtop fermentor at cell densities above 13 g/L dry cell weight. A correction factor based on the accumulated light data is calculated and used in real time to account for consumption of luciferin from the culture broth by the light producing reaction. Dissolved oxygen concentrations must be kept above 15% of air saturation to ensure constant light output, but no detectable increase in oxygen demand is seen. The method does not significantly affect growth or production rates. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 52 (1996), S. 271-289 
    ISSN: 0006-3592
    Keywords: bioprocess control ; physiological state ; Escherichia coli ; plant cell culture ; mammalian cell culture perfusion ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Advances in bioprocess engineering depends ultimately on the level of understanding and control of the physiological state of the cell population. Process efficiency is strongly influenced by changes in the cellular state which should be monitored, interpreted, and, if possible, properly manipulated. In most control systems this function is not explicitly considered, which hampers process development and optimization. Conventional control logic is based on direct mapping of the growth environment into process efficiency, thereby bypassing the cell state as an intermediate control objective. Today, this limitation is well realized, and explicit monitoring and control of cellular physiology are considered to be among the most challenging tasks of modern bioprocess engineering. We present here a generic methodology for the design of systems capable of performing these advanced monitoring and control functions.The term “physiological state” is quantified by a vector composed of several process variables that convey significant information about cellular state. These variables can be selected among different classes, including specific metabolic rates, metabolic rate ratios, degees of limitation, and others. The real-time monitoring of many of these is possible using commercial sensors. The definition and calculation of representative sets of physiological state variables is demonstrated with examples from several fermentor cultures: recombinant Escherichia coli for phenylalanine production, bioluminescent E. coli (harboring lux genes driven by a heat shock protein promoter) for detection of environmental pollutants, plant cell culture of Perilla frutescensfor anthocyanin production, and perfusion cultures of recombinant mammalian cells (NS0 and CHO) for therapeutic protein production.If the physiological state vector is on-line calculated, the fermentation process can be described by its trajectory in a space defined by the vector components. Then, the goal of the control system is to maintain the physiological state of the cell as close as possible to the trajectory, providing maximum efficiency. A control structure meant to perform this function is proposed, along with the mechanism for its design. In contrast to conventional systems which work in a closed loop in respect to the cell environment, this scheme operates in a closed loop in respect to the cell state. The discussed control concept has been successfully applied to the recombinant phenylalanine production, resulting in physiologically consistent operation, total computer control, and high process efficiency. Initial results from the application of the method to perfusion mammalian cell cultures are also presented. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 52 (1996), S. 373-386 
    ISSN: 0006-3592
    Keywords: membrane-attached biofilms ; modeling ; extractive membrane bioreactor ; toxic VOC ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: This article presents a mathematical model of membrane-attached biofilm (MAB) behavior in a single-tube extractive membrane bioreactor (STEMB). MABs can be used for treatment of wastewaters containing VOCs, treatment of saline wastewaters, and nitrification processes. Extractive membrane bioreactors (EMBs) are employed to prevent the direct contact between a toxic volatile pollutant and the aerated gas by allowing counterdiffusion of substrates; i.e., pollutant diffuses from the tube side into the biofilm, whereas oxygen diffuses from the shell side into the biofilm. This reduces the air stripping problems usually found in conventional bioreactors. In this study, the biodegradation of a toxic VOC (1,2-dichloroethane, DCE) present in a synthetic wastewater has been investigated. An unstructured model is used to describe cell growth and cell decay in the MAB. The model has been verified by comparing model predicted trends with experimental data collected over 5 to 20-day periods, and has subsequently been used to model steady states in biofilm behavior over longer time scales. The model is capable of predicting the correct trends in system variables such as biofilm thickness, DCE flux across the membrane, carbon dioxide evolution, and suspended biomass. Steady states (constant biofilm thickness and DCE flux) are predicted, and factors that affect these steady states, i.e., cell endogeneous decay rate, and biofilm attrition, are investigated. Biofilm attrition does not have a great influence on biofilm behavior at low values of detachment coefficient close to those typically reported in the literature. Steady-state biofilm thickness is found to be an important variable; a thin biofilm results in a high DCE flux across the membrane, but with the penalty of a high loss of DCE via air stripping. The optimal biofilm thickness at steady state can be determined by trading off the decrease in air stripping (desirable) and the decrease in DCE flux (undesirable) which occur simultaneously as the thickness increases. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 52 (1996), S. 387-396 
    ISSN: 0006-3592
    Keywords: xylitol ; NADH regeneration ; charged membrane ; continuous production ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We have developed a new process for the production of xylitol from D-xylose by enzyme technology. An NADH-dependent xylose reductase (XR) from Candida tenuis catalyzes the reduction of xylose, which is coupled to enzymatic oxidations of D-glucose or D-xylose by glucose dehydrogenase from Bacillus cereus to make achievable an up to 10,000-fold regeneration of NADH per cycle of discontinuous conversion. Using a simple kinetic model as a tool for process optimization, suitable conditions with regard to performance and stability of the multi-component reaction system were established, and 300 g/L of substrate could be converted in yields above 96% in one single batch reaction. Due to selective and over 98% complete retention of the native coenzyme by negatively charged nanofiltration membranes used in a continuously operated enzyme reactor, a specific productivity of 80 g xylitol per liter, day, and kilounit of XR was maintained over the 150-h reaction time with only a single dosage of NADH. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 52 (1996), S. 397-403 
    ISSN: 0006-3592
    Keywords: cell harvesting ; protein separation ; Vibrio cholerae ; cross-flow microfiltration ; shear-enhanced module ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Protein, produced by a bacterial culture of recombinant Vibrio cholerae, was separated from cells in a fermentation broth by cross-flow microfiltration. A new, mechanically agitated (rotational) shear filter, the DMFTM filter from Pall, was used to perform the separation. Higher protein recovery and permeate flux than commonly obtained during cell harvesting were demonstrated using sixfold concentration followed by twofold diafiltration. The transmembrane pressure only increased by 10 kPa when the flux was kept constant at 150 L/m2 h during both concentration and diafiltration. The protein transmission was about 100% initially, and over 90% at the end of the concentration process. The protein transmission during the diafiltration was over 80%. The total recovery of protein was 97%. When using an enzymatic cleaning agent, no significant pure water flux decrease was detected during the course of the experiments. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 52 (1996), S. 404-411 
    ISSN: 0006-3592
    Keywords: anaerobic digestion ; isobutyrate ; butyrate ; isomerization ; hydrogen ; formate ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The effect of formate and hydrogen on isomerization and syntrophic degradation of butyrate and isobutyrate was investigated using a defined methanogenic culture, consisting of syntrophic isobutyrate-butyrate degrader strain IB, Methanobacterium formicicum strain T1N, and Methanosarcina mazeii strain T18. Formate and hydrogen were used to perturb syntrophic butyrate and isobutyrate degradation by the culture. The reversible isomerization between isobutyrate and butyrate was inhibited by the addition of either formate or hydrogen, indicating that the isomerization was coupled with syntrophic butyrate degradation for the culture studied. Energetic analysis indicates that the direction of isomerization between isobutyrate and butyrate is controlled by the ratio between the two acids, and the most thermodynamically favorable condition for the degradation of butyrate or isobutyrate in conjunction with the isomerization is at almost equal concentrations of isobutyrate and butyrate. The degradation of isobutyrate and butyrate was completely inhibited in the presence of a high hydrogen partial pressure (〉2000 Pa) or a measurable level of formate (10 μM or higher). Significant formate (more than 1 mM) was detected during the perturbation with hydrogen (17 to 40 kPa). Resumption of butyrate and isobutyrate degradation was related to the removal of formate. Energetic analysis supported that formate was another electron carrier, besides hydrogen, during syntrophic isobutyrate-butyrate degradation by this culture. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 52 (1996), S. 429-432 
    ISSN: 0006-3592
    Keywords: BHK ; aggregates ; porous microcarriers ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The influence of surface growth (two-dimensional microcarriers) and three-dimensional growth (aggregates and macroporous supports) in agitated, suspended batch culture systems upon growth and productivity of BHK was compared. Cultures using three porous microcarriers (CultiSpher G, Cellsnow EX, and Cytocell), one nonporous microcarrier (Cytodex 3) and natural aggregates were performed in stirred tanks using two different agitation rates (60 and 100 RPM). With the exception of Cytocell, cell growth, viability, and productivity were similar when three-dimensional structures (porous microcarriers and aggregates) were used. Nonporous microcarriers only compared well at 60 RPM as growth ceased under overagitation. These results suggest that cultures less susceptible to fluid shear are advantageous for scale-up. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 52 (1996), S. 412-422 
    ISSN: 0006-3592
    Keywords: Petunia hybrida ; chemostat cultures ; glucose limitation ; nitrate limitation ; growth ; respiration ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Nitrate-limited and glucose-limited chemostat cultures of Petunia hybrida cells were compared at a specific biomass (+extracellular product) formation rate of 0.0042 C·mol/C·mol h. The composition of the biomass differed considerably in both culture types. The N/C (mol/mol) ratio in the biomass was almost four times lower in the nitrate-limited than in the glucose-limited cultures. On a dry weight basis (g/g DW) the biomass in the nitrate-limited cultures contained about 2.5 times less ions and protein N and about 2.5 times more carbohydrates than the biomass in the glucose-limited cultures. On a fresh weight basis (mmol/g FW) the biomass in nitrate-limited and glucose-limited cultures differed mainly in carbohydrate content. The yields of biomass on glucose and oxygen were generally higher in the nitrate-limited than in the glucose-limited cultures. Average values for these parameters were 0.27 C · mol biomass/C · mol glucose and 0.42 C · mol biomass/mol O2 in the glucose-limited cultures and 0.34 C · mol biomass/C · mol glucose and 0.55 C · mol biomass/mol O2 in the nitrate-limited cultures. On a C · mol basis the total respiration was about 25% and the maximally attainable cytochrome pathway activity (measured in the presence of hydroxamate) about 30% higher in the glucose-limited than in the nitrate-limited cultures. The maximally attainable activity of the alternative pathway (measured in the presence of KCN) was significantly lower in the glucose-limited cultures. On an organic N (≈protein) basis all respiratory parameters were significantly higher in the nitrate-limited cultures. In the presence of the respiratory uncoupler carbonyl cyanide p-trifluoromethoxy phenylhydrazone (FCCP) and excess glucose, cellular respiratory activity shows its maximal activity; under these conditions the total respiration increased more than 150% in the glucose-limited and only 30% in the nitrate-limited cultures. It is suggested that glucose-limited cultures are able to react more flexibly to changes in the environmental conditions than nitrate-limited cultures. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 52 (1996), S. 423-428 
    ISSN: 0006-3592
    Keywords: hydrogenase ; organic biocatalysis ; polyethylene glycol ; modified enzymes ; sulfur ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Naturally occurring enzymes may be modified by covalently attaching hydrophobic groups that render the enzyme soluble and active in organic solvents, and have the potential to greatly expand applications of enzymatic catalysis. The reduction of elemental sulfur to hydrogen sulfide by a hydrogenase isolated from Pyrococcus furiosus has been investigated as a model system for organic biocatalysis. While the native hydrogenase catalyzed the reduction of sulfur to H2S in aqueous solution, no activity was observed when the aqueous solvent was replaced with anhydrous toluene. Hydrogenase modified with PEG p-nitrophenyl carbonate demonstrated its native biocatalytic ability in toluene when the reducing dye, benzyl viologen, was also present. Neither benzyl viologen nor PEG p-nitrophenyl carbonate alone demonstrated reducing capability. PEG modified cellulase and benzyl viologen were also incapable of reducing sulfur to H2S, indicating that the enzyme itself, and not the modification procedure, is responsible for the conversion in the nonpolar organic solvent. Sulfide production in toluene was tenfold higher than that produced in an aqueous system with equal enzyme activity, demonstrating the advantages of organic biocatalysis. Applications of bio-processing in nonaqueous media are expected to provide significant advances in the areas of fossil fuels, renewable feedstocks, organic synthesis, and environmental control technology. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 50 (1996), S. 529-540 
    ISSN: 0006-3592
    Keywords: T-lymphocytes ; immunotherapy ; HTLV-1 ; CTL ; dendritic cell ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: CD8+ cytotoxic T-lymphocytes (CTLs) have been proven, in multiple animal models, to be the most powerful antiviral and antitumor components of the immune system. We have developed a protocol to activate and expand tumor and virus peptide-specific CD8+ T-lymphocytes from the peripheral blood of healthy, human trophic leukemia virus-1 (HTLV-1) seronegative human leucocyte antigen (HLA)-A*0201 individuals. A combination of density-based separation and culture conditions was employed to isolate dendritic cells (DCs), which are the most potent antigen-presenting cells (APCs), and T-lymphocytes. The DCs were pulsed with HLA-A*0201 binding peptides and cultured with autologous T-lymphocytes to generate peptide-specific CTLs. The CTLs were generated against a nine-amino-acid peptide from the Tax protein of HTLV-1. The CTLs were expanded according to a restimulation schedule employing peptide-pulsed autologous monocytes and low-dose interleukin-2 (IL-2) to numbers in excess of 100 × 106 cells following 5 weeks of culture. Expanded cells contained primarily CD3+ T-cells, of which CD8+ T-lymphocytes constituted greater than two-thirds of the cell population. Obtained CTLs exhibited potent antigen-specific lysis of peptide-pulsed target cells in a dose-dependent fashion in in vitro 51Cr release cytotoxicity assay. This antigen-specific killing was shown to be HLA class I restricted and mediated by CD8+ T-lymphocytes. Since the T-lymphocytes were obtained from HTLV-1 seronegative donors, the generation of peptide-specific CTLs represents reliable and reproducible elicitation of a primary immune response in vitro against naive antigens and subsequent expansion of generated CTLs for adoptive immunotherapy. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 50 (1996), S. 555-561 
    ISSN: 0006-3592
    Keywords: human aortic smooth muscle cells ; shear stress ; restenosis ; growth rate ; PCNA ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: After cardiovascular intervention, smooth muscle cells (SMC) are directly exposed to blood flow and thus their behavior might be affected by fluid hemodynamic forces. The aim of this study was to determine the effect of fluid shear stress on the growth rate of SMC. Human aortic smooth muscle cells (hASMC) were seeded on fibronectin-coated glass slides and were exposed to different levels of shear stress using parallel plate flow chambers. After 24 h, cell numbers in the stationary and sheared cultures were measured by a Coulter counter. Results demonstrated that increasing shear stress significantly reduces the proliferation rate of hASMC (P 〈 0.05). Comparable lactate dehydrogenase levels in the media of stationary and flow cultures provided evidence that the reduction of cell number was not due to cell injury. Proliferating cell nuclear antigen (PCNA) immunofluorescence studies indicated that the cell cultures were not growth arrested 24 h after exposure to shear stress, and that the differences in PCNA staining between stationary control and flow cultures were comparable to the cell counts. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 50 (1996), S. 562-567 
    ISSN: 0006-3592
    Keywords: tissue engineering ; synthetic biodegradable matrix ; polyglycolic acid ; polylactic acid ; endothelial cell ; heart valve ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Tissue engineered lamb heart valve leaflets (N - 3) were constructed by repeatedly seeding a concentrated suspension of autologous myofibroblasts onto a biodegradable synthetic polymeric scaffold composed of fibers made from polyglycolic acid and polylactic acid. Over a 2-week period the cells attached to the polymer fibers, multiplied, and formed a tissue core in the shape of the matrix. The tissue core was seeded with autologous large-vessel endothelial cells that formed a monolayer which coated the outer surface of the leaflet. The tissue engineered leaflets were surgically implanted in place of the right posterior pulmonary valve leaflet of the donor lamb while on cardiopulmonary bypass. Pulmonary valve function was evaluated by two-dimensional echocardiography with color Doppler which demonstrated valve function without evidence of stenosis and with only trivial regurgitation under normal physiologic conditions. Histologically, the tissue engineered heart valve leaflets resembled native valve leaflet tissue. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 50 (1996), S. 580-586 
    ISSN: 0006-3592
    Keywords: tissue engineering ; N1E-115 neuroblastoma cells ; electrophysiological differentiation ; retinoid cytotoxicity ; teratogenesis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The cytotoxic effects of retinoids on neuroblastoma cells at various times during electrophysiological differentiation were evaluated. We used N1E-115, a clone of the murine neuroblastoma C1300 derived from the neural crest, and three retinoids: vitamin A (retinol), all-trans retinoic acid (tretinoin), and 13-cis-retinoic acid (isotretinoin). Differentiating N1E-115 cells exposed to retinoids at an isotretinoin EC50 of 16 μM exhibited the greatest vulnerability in terms of cell death during a period (8 to 10 days) that was previously found to be the most sensitive for induction of gross malformations in rodents. This finding suggested possible similarities between the in vivo and in vitro retinoid mechanism(s) of action. The greatest period of vulnerability to retinoid cytotoxicity was also found to coincide with the rapid resting membrane potential (Vm) development period, suggesting a linkage between neuronal Vm and/or electrical excitability development and vulnerability to retinoid cytotoxicity. © 1996 John Wiley & Sons, Inc.
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    Keywords: Chemistry ; Biochemistry and Biotechnology
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    Biotechnology and Bioengineering 50 (1996), S. 463-463 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
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    Biotechnology and Bioengineering 50 (1996), S. 609-616 
    ISSN: 0006-3592
    Keywords: enzyme inactivation ; substrate modulation ; product modulation ; penicillin acylase ; 6-aminopenicillanic acid ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Inactivation of immobilized penicillin acylase has been studied in the presence of substrate (penicillin G) and products (phenylacetic acid and 6-aminopenicillanic acid), under the hypothesis that substances which interact with the enzyme molecule during catalysis will have an effect on enzyme stability. The kinetics of immobilized penicillin acylase inactivation was a multistage process, decay constants being evaluated for the free-enzyme and enzyme complexes, from whose values modulation factors were determined for the effectors in each enzyme complex at each stage. 6-Aminopenicillanic acid and penicillin G stabilized the enzyme in the first stage of decay. Modulation factors in that stage were 0.96 for penicillin G and 0.98 for 6-aminopenicillanic acid. Phenylacetic acid increased the rate of inactivation in both stages, modulating factors being -2.31 and -2.23, respectively. Modulation factors influence enzyme performance in a reactor and are useful parameters for a proper evaluation. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 50 (1996), S. 675-686 
    ISSN: 0006-3592
    Keywords: biofilm ; steady state ; heterotrophs ; nitrosomonas ; nitrobacter ; model ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Through a thorough investigation of the boundary conditions for a general two-species biofilm model, a simple and fast method for solving the steady-state case is developed and presented. The methods used may be extended to biofilm models in which more than two species are considered. Four different sets of boundary conditions are possible for the two-species biofilm model. Each set is shown to be asymptotically stable. A biofilm model describing the competition between autotrophic and heterotrophic bacteria and a biofilm model considering only Nitrosomonas and Nitrobacter are used for illustration. A parameter Lcrit, critical film thickness for bacterial coexistence, is introduced from which criteria on the bulk concentrations for coexistence are derived. From these criteria it is seen that the thinner the biofilm, the more restrictive the conditions are for steady-state coexistence. For thin biofilms there may, in many cases, be no point in considering more than one species in the biofilm model. Furthermore, the gradients of the bacterial concentrations are in many cases negligible in thin biofilms, and the biofilm may then be assumed to be homogeneous. The criteria on the bulk concentrations together with the four sets of boundary conditions provide the necessary information for a direct solution of the steady-state two-species biofilm model by means of an ordinary differential and algebraic equation solver. © 1996 John Wiley & Sons, Inc.
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    Keywords: Chemistry ; Biochemistry and Biotechnology
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  • 80
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    Biotechnology and Bioengineering 50 (1996), S. 700-708 
    ISSN: 0006-3592
    Keywords: α-chymotrypsin ; organic media ; tripeptide synthesis ; CCK-8 ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
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    Notes: The enzymatic synthesis of the tripeptide derivative Z-Gly-Trp-Met-OEt is reported. This tripeptide is a fragment of the cholecystokinin C-terminal octapeptide CCK-8. Studies on the α-chymotrypsin catalyzed coupling reaction between Z-Gly-Trp-R1 and Met-R2 have focused on low water content media, using deposited enzyme on inert supports such as Celite and polyamide. The effect of additives (polar organic solvents), the acyl-donor ester structure, the C-α protecting group of the nucleophile, enzyme loading, and substrate concentration were tested. The best reaction medium found was acetonitrile containing buffer (0.5%, v/v) and triethylamine (0.5%, v/v) using the enzyme deposited on Celite as catalyst (8 mg of α-chymotrypsin/g of Celite). A reaction yield of 81% was obtained with Z-Gly-Trp-OCam as acyl donor, at an initial concentration of 80 mM. The tripeptide synthesis was scaled up to the production of 2 g of pure tripeptide with an overall yield of 71%, including reaction and purification steps. © 1996 John Wiley & Sons, Inc.
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  • 81
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    Biotechnology and Bioengineering 51 (1996), S. 1-14 
    ISSN: 0006-3592
    Keywords: biodegradation ; desorption ; mathematical model ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A mathematical model to describe polynuclear aromatic hydrocarbon (PAH) desorption, transport, and biodegradation in saturated soil was constructed by describing kinetics at a microscopic level and incorporating this description into macroscale transport equations. This approach is novel in that the macroscale predictions are made independently from a knowledge of microscale kinetics and macroscopic fluid dynamics and no adjustable parameters are used to fit the macroscopic response. It was assumed that soil organic matter, the principal site of PAH sorption, was composed of a continuum of compartments with a gamma distribution of desorption rate coefficients. The mass transport of substrates and microorganisms in a mesopore was described by diffusion and that in a macropore by one-dimensional advection and dispersion. Naphthalene was considered as a test PAH compound for initial model simulations. Three mechanisms of naphthalene biodegradation were considered: growth-associated degradation as a carbon and energy source for microbial growth; degradation for maintenance energy; and growth-independent degradation. The Haldane modification of the Monod equation was used to describe microbial growth rates and to account for possible growth inhibition by naphthalene. Multisubstrate interactions were considered and described with a noninteractive model for specific growth rates. The sensitivity of selected model parameters was analyzed under conditions when naphthalene was the sole growth-rate-limiting substrate. The time necessary to achieve a specific degree of naphthalene biodegradation was found to be proportional to the initial concentration of naphthalene in soil organic matter. The biodegradation rate of naphthalene increased when the sorption equilibrium constant of naphthalene was reduced. The presence of an alternative carbon source inhibited naphthalene biodegradation in spite of the calculated increase in biomass. © 1996 John Wiley & Sons, Inc.
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  • 82
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    Biotechnology and Bioengineering 52 (1996), S. 539-548 
    ISSN: 0006-3592
    Keywords: adsorptive membranes ; facilitated diffusion ; parametric pumping ; uphill transport ; integrated processes ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Selective extraction of a protein from a mixture can be accomplished using an adsorptive membrane and low displacement recuperative parametric pumping. Low displacement recuperative parametric pumping can lead to the preferential transport of an adsorbing solute and the rejection of nonadsorbing solutes by the adsorptive membrane. Using a protein mixture consisting of lysozyme and myoglobin, we have found the conditions under which lysozyme is preferentially transported through an ion-exchange membrane cartridge while myoglobin is rejected by the membrane. Trends observed when parameters such as the desorbent concentration, feed concentration, and flow rate are varied agree with the predictions of a mathematical model. Comparison with facilitated diffusion shows that preferential transport can lead to higher solute fluxes, albeit at lower selectivity. Additionally, preferential transport can be used to transport a solute up a concentration gradient and to selectively extract a solute from a feed that contains suspended solids. © 1996 John Wiley & Sons, Inc.
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  • 83
    ISSN: 0006-3592
    Keywords: glycerol fermentation ; Klebsiella pneumoniae ; oscillation ; hysteresis ; growth and metabolism ; substrate excess ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Oscillation and hysteresis phenomena are observed in the anaerobic continuous fermentation of glycerol by Klebsiella pneumoniae in long-term cultivations under a variety of conditions. In this work, the conditions for the occurrence of these phenomena are reported and the patterns of cell growth and metabolism under oscillation are characterized. During an oscillation period, the formation rates of CO2, H2, and formate and the consumption rate of alkali periodically pass values of maxima and minima, the latter being close to zero. The formation of biomass and fermentation products such as 1,3-propanediol, acetate, and ethanol also undergo periodic changes which shift maxima and minima. Sustained oscillation occurs only under conditions of substrate excess within a distinct regime. At pH 7.0, it is only found at dilution rates above 0.15 h-1 under the experimental conditions. At lower pH values, oscillations are more likely to happen, even at a relatively low dilution rate and low substrate excess. Whereas the amplitude of oscillations at pH 7.0 depends on both the dilution rate and the residual glycerol concentration (CGlyc) the interval of oscillations appears to be only a function of CGlyc. An increase of CGlyc in culture damps the oscillation and leads to its disappearance at CGlyc = 1100 to 1200 mmol/L (pH 7.0). The operation mode was also found to be an important parameter in determining the stability and actual state of the culture, resulting in hysteresis under certain conditions, particularly at low pH values. Generally, a large perturbation of cultivation conditions tends to cause oscillation and hysteresis. The results unambiguously demonstrate that the oscillation and hysteresis phenomena shown in this work are bound to genuine metabolic fluctuations of the microorganism. They reveal several differences and new features compared with those reported in the literature and cannot be readily explained by the mechanisms known so far. © 1996 John Wiley & Sons, Inc.
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  • 84
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    Biotechnology and Bioengineering 52 (1996), S. 572-578 
    ISSN: 0006-3592
    Keywords: nar promoter ; inducible promoter ; nitrate reductase ; anaerobic conditions ; Escherichia coli ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The nar promoter of Escherichia coli, which is maximally induced under anaerobic conditions in the presence of nitrate, was characterized to see whether the nar promoter cloned onto pBR322 can be used as an inducible promoter. To increase the expression level, the nar promoter was expressed in E. coli where active nitrate reductase cannot be expressed from the nar operon on the chromosome. A plasmid with the lacZ gene expressing β-galactosidase instead of the structural genes of the nar operon was used to simplify an assay of induction of the nar promoter. The following effects were investigated to find optimal conditions: methods of inducing the nar promoter, optimal nitrate and molybdate concentrations maximally inducing the nar promoter, the amount of expressed β-galactosidase, and induction ratio (specific β-galactosidase activity after maximal induction/specific β-galactosidase activity before induction.)The following results were obtained from the experiments: induction of the nar promoter was optimal when E. coli was grown in the presence of 1% nitrate at the beginning of culture; expression of β-galactosidase was not affected by molybdate; the induction ratio was maximal, approximately 300, when the overnight culture was grown in the flask for 2.5 h (OD600 is congruent to 1.3) before being transferred to the fermentor; the amount of β-galactosidase per cell and per medium volume was maximal when E. coli was grown under aerobic conditions to OD600 = 1.7; then the nar promoter was induced under microaerobic conditions made by lowering dissolved oxygen level (DO) to 1-2%. After approximately 6 h of induction, OD600 became 3.2 and specific β-galactosidase activity became 36,000 Miller units, equivalent to 35% of total cellular proteins, which was confirmed from sodium dodecyl sulfate-polyacrylamide gel electrophoresis. © 1996 John Wiley & Sons, Inc.
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  • 85
    ISSN: 0006-3592
    Keywords: oscillation ; Klebsiella pneumoniae ; glycerol metabolism ; metabolic fluxes ; pathway analysis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The oscillation phenomena reported in the preceding article for the anaerobic continuous fermentation of glycerol by Klebsiella pneumoniae are analyzed in terms of metabolic fluxes (metabolic rates and yields) and stoichiometry of pathways. Significant oscillations in the fluxes of CO2, H2, formic acid, ethanol, and reducing equivalents are observed which show obvious relationships to each other. Changes in the consumption or production rates of glycerol, acetic acid, 1,3-propanediol, and ATP are irregular and have relatively small amplitudes compared with their absolute values. By comparing the metabolic fluxes under oscillation and steady state that have nearly the same environmental conditions it could be shown that pyruvate metabolism is the main step affected under oscillation conditions. The specific formation rates of all the products originating from pyruvate metabolism (CO2, H2, formic acid, ethanol, acetic acid, lactic acid, and 2,3-butanediol) show significant differences under conditions of oscillation and steady state. In contrast, the specific rates of substrate uptake, ATP generation, and formation of products deriving either directly from glycerol (1,3-propanediol) or from the upstream of pyruvate metabolism (e.g., succinic acid) are not, or at least not significantly, affected during oscillation. Stoichiometric analysis of metabolic pathways confirms that other enzyme systems, in addition to pyruvate: formate-lyase, must be simultaneously involved in the pyruvate decarboxylation under both oscillation and steady-state conditions. The results strongly suggest oscillations of activities of these enzymes under oscillation conditions. It appears that the reason for the occurrence of oscillation and hysteresis lies in an unstable regulation of pyruvate metabolism of different enzymes triggered by substrate excess and drastic change(s) of environmental conditions. © 1996 John Wiley & Sons, Inc.
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  • 86
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    Biotechnology and Bioengineering 52 (1996), S. 579-590 
    ISSN: 0006-3592
    Keywords: fed batch ; hybridoma ; material balance ; reaction network ; stoichiometric analysis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A detailed reaction network of mammalian cell metabolism contains hundreds of enzymatic reactions. By grouping serial reactions into single overall reactions and separating overlapped pathways into independent reactions, the total number of reactions of the network is significantly reduced. This strategy of manipulating the reaction network avoids the manipulations of a large number of reactions otherwise needed to determine the reaction extents. A stoichiometric material balance model is developed based on the stoichiometry of the simplified reaction network. Closures of material balances on glucose and each of the 20 amino acids are achieved using experimental data from three controlled fed-batch and one-batch hybridoma cultures. Results show that the critical role of essential amino acids, except glutamine, is to provide precursors for protein synthesis. The catabolism of some of the essential amino acids, particularly isoleucine and leucine, is observed when an excess amount of these amino acids is available in the culture medium. It was found that the reduction of glutamine utilization (for reducing ammonia production) is accompanied by an increase in the uptake of nonessential amino acids (NAAs) from the culture medium. This suggests that NAAs are necessary even though they are not essential for cell growth. A glutamine balance shows that less than 20% of the glutamine nitrogen is utilized for essential roles, such as protein and nucleotide syntheses. A relatively constant percentage (about 45%) of the glutamine nitrogen is utilized for NAA biosynthesis, despite the fact that the absolute amount varies among the four experiments. As to the carbon skeleton of glutamine, a significant portion enters the tricarboxylic acid (TCA) cycle. A material balance on glucose shows that most of the glucose (81%) is converted into lactate when glucose is in excess. On the other hand, when glucose is limited, lactate production is considerably reduced, while a major portion of glucose (48%) enters the TCA cycle. The fraction of glucose used for the synthesis of cellular components ranges from 9 to 28%. © 1996 John Wiley & Sons, Inc.
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  • 87
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    Biotechnology and Bioengineering 52 (1996), S. 602-608 
    ISSN: 0006-3592
    Keywords: modeling ; microbial growth ; substrate inhibition ; inhibition sites ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: This article presents a general equation for substrate inhibition of microbial growth using a statistical thermodynamic approach. Existing empirical models adapted from enzyme kinetics, for example, the Haldane-Andrews equation, often criticized for not being physically based for microbial growth, are shown to derive from the general equation in this article, and their empirical parameters are shown to be well defined physically. Three sets of experimental data from the literature are used to test the modeling abilities of the general equation to represent experimental data. The results are compared with those obtained by fitting the same data set to a widely used empirical model existing in the literature. The general equation is found to represent all three experimental data sets better than the alternative model tested. In addition, a graphical method existing in enzyme kinetics is successfully adapted and further developed to determine the number of inhibition sites of a basic functional unit of a bacterial cell. © 1996 John Wiley & Sons, Inc.
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  • 88
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    Biotechnology and Bioengineering 52 (1996), S. 591-601 
    ISSN: 0006-3592
    Keywords: animal cell metabolism ; ATP balance ; energy metabolism ; reaction network ; stoichiometric analysis ; hybridoma ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A metabolic reaction network is developed for the estimation of the stoichiometric production of adenosine triphosphate (ATP) in animal cell culture. By using the material balance data from fed-batch and batch cultures of hybridoma cells, the stoichiometric ATP productions are determined with estimated effective P/O ratios of 2 for NADH and 1.2 for FADH2. A significant percentage of the ATP requirement (16-41%) in hybridoma cells is generated directly from free energy release without the participation of oxygen. The oxidative phosphorylation of NADH accounts for about 60% of the total ATP production in the fed-batch cultures and about 47% in the batch culture. The oxidative phosphorylation of FADH2 accounts for less then 20% of the total ATP production in all cases.A fractional model is devised to analyze the contribution of each nutrient to the ATP production. Results show that a majority of the ATP is produced from glucose metabolism (60-76%). Less than 30% of the ATP is derived from glutamine, and less than 11% is derived from other essential amino acids. The analysis also shows that the glycolytic pathway generates more ATP in the batch (41%) than in the fed-batch (〈27%) cultures. The TCA cycle provides 51-68% of the total ATP production. The calculated stoichiometric oxygen consumption differs among the batch and fed-batch cultures, depending on the glucose concentration. This result suggests that the relationship between the oxygen uptake rate (OUR) and cell growth may change with the culture conditions. However, the calculated respiratory quotient (RQ) is relatively constant in all cases.A linear relationship is obtained between the specific ATP production rate and the specific cell growth rate. The maximum ATP yield and the maintenance ATP requirement are determined based on this linear relationship. The biosynthetic ATP demand estimated from the dry cell weight and cell composition is significantly lower than that calculated from the maximum ATP yield, indicating that the non-growth-associated ATP demand may contain other factors than what is considered in the estimation of the biosynthetic ATP demand. © 1996 John Wiley & Sons, Inc.
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  • 89
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    Biotechnology and Bioengineering 52 (1996) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
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    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 90
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    Biotechnology and Bioengineering 52 (1996), S. 631-631 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
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  • 91
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    Biotechnology and Bioengineering 52 (1996), S. 633-647 
    ISSN: 0006-3592
    Keywords: Monte Carlo simulation ; plasmid replication ; bacterial division cycle ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Plasmids have cell cycle replication patterns that need to be considered in models of their replication dynamics. To compare current theories for control of plasmid replication with experimental data for timing of plasmid replication with the cell cycle, a Monte Carlo simulation of plasmid replication and partition was developed. High-copy plasmid replication was simulated by incorporating equations previously developed from the known molecular biology of ColE1-type plasmids into the cell-cycle simulation. Two types of molecular mechanisms for low-copy plasmid replication were tested: accumulation of an initiator protein in proportion to cell mass and binding of the plasmid origin to the cell membrane. The low-copy plasmids were partitioned actively, with a specific mechanism to mediate the transfer from mother to daughter cells, whereas the high-copy plasmids were partitioned passively with cell mass.The simulation results and experimental data demonstrate cell-cycle-specific replication for the low-copy F plasmid and cell-cycle-independent replication for the high-copy pBR322, ColBM, and R6K plasmids. The simulation results indicate that synchronous replication at multiple plasmid origins is critical for the cell-cycle-specific pattern observed in rapidly growing cells. Variability in the synchrony of initiation of multiple plasmid origins give rise to a cell-cycle-independent pattern and is offered as a plausible explanation for the controversy surrounding the replication pattern of the low-copy plasmids. A comparison of experimental data and simulation results for the low-copy F plasmid at several growth rates indicates that either initiation mechanism would be sufficient to explain the timing of replication with the cell cycle. The simulation results also demonstrate that, although cell-cycle-specific and cell-cycle independent replication patterns give rise to very different gene-expression patterns during short induction periods in age-selected populations, long-term expression of genes encoded on low-copy and high-copy plasmids in exponentially growing cells have nearly the same patterns. These results may be important for the future use of low-copy plasmids as expression vectors and validate the use of simpler models for high-copy plasmids that do not consider cell-cycle phenomena. © 1996 John Wiley & Sons, Inc.
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  • 92
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    Biotechnology and Bioengineering 51 (1996), S. 120-125 
    ISSN: 0006-3592
    Keywords: chemotaxis ; single cell ; capillary ; Escherichia coli ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A new method was developed which enables chemotaxis parameters to be measured at a single-cell level inside a capillary for the first time. The chemotaxis chamber consists of two reservoirs communicating through a capillary tube 50 μm in diameter. Chemotaxis parameters are measured inside the capillary using image analysis, after a nearly linear attractant concentration gradient has been generated along the capillary by diffusion. Compared to previously published techniques, this method provides a well-characterized chemoattractant concentration profile in addition to allowing single-cell parameters to be measured inside a fine capillary. This procedure was used to measure the single-cell chemotaxis parameters for Escherichia coli K12, and the results are compared to published data on single E. coli cells chemotaxing in bulk. © 1996 John Wiley & Sons, Inc.
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  • 93
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    Biotechnology and Bioengineering 51 (1996), S. 126-130 
    ISSN: 0006-3592
    Keywords: chlorophenol ; peroxidase ; immobilization ; magnetite ; immobilized enzyme ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Immobilization of horseradish peroxidase on magnetite and removal of chlorophenols using immobilized enzyme were investigated. Immobilization by physical adsorption on magnetite was much more effective than that by the crosslinking method, and the enzyme was found to be immobilized at 100% of retained activity. In addition, it was discovered that horseradish peroxidase was selectively adsorbed on magnetite, and the immobilization resulted in a 20-fold purification rate for crude enzyme. When immobilized peroxidase was used to treat a solution containing various chlorophenols, p-chlorophenol, 2,4-dichlorophenol, 2,4,5-trichlorophenol, 2,4,6-trichlorophenol, 2,3,4,6-tetrachlorophenol, and pentachlorophenol, each chlorophenol was almost 100% removed, and also the removal of total organic carbon (TOC) and adsorbable organic halogen (AOX) reached more than 90%, respectively. However, in the case of soluble peroxidase, complete removal of each chlorophenol could not be attained, and in particular, the removal of 2,4,5-trichlorophenol was the lowest, with a removal rate of only 36%. © 1996 John Wiley & Sons, Inc.
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  • 94
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    Biotechnology and Bioengineering 51 (1996), S. 141-147 
    ISSN: 0006-3592
    Keywords: L-DOPA ; tyrosinase ; enzyme immobilization ; nylon 6,6 ; inactivation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The production of L-DOPA immobilized on chemically modified nylon 6,6 membranes was studied in a batch reactor. Tyrosinase was immobilized on nylon using glutaraldehyde as a crosslinking agent. The effects of membrane pore size and glutaraldehyde concentration upon enzyme uptake and L-DOPA production were investigated. Enzyme uptake was unaffected by glutaraldehyde concentration; approximately 70% uptake was observed when 25% w/v (group 1), 5% (group 2), and 3% (group 3) glutaraldehyde were used, indicating that glutaraldehyde was in excess. Similarly, uptake was the same for membranes with 0.20 and 10 μm pore sizes.Membranes produced using different levels of glutaraldehyde exhibited dramatically different capacities for L-DOPA production, despite the fact that enzyme uptake was equivalent. Membranes from groups 2 and 3 (5% and 3% glutaraldehyde) produced L-DOPA at a rate of 1.70 mg L-1 h-1 over 170 h in a 500-mL batch reactor. However, no free L-DOPA was detected when group 1 membranes were used. Experimental evidence suggests that L-DOPA was produced, but remained bound to these membranes via excess glutaraldehyde left over from the immobilization process. Membrane pore size also effected L-DOPA production; less production was observed when 10-μm membranes were used, despite equivalent enzyme uptake. The observed difference in production may be due to differences in the pore density on the two types of membranes which could affect the access of the substrate to the immobilized enzyme.The results of these studies indicate that tyrosinase can be effectively immobilized on nylon 6,6. L-DOPA production was optimal when 0.20-μm-pore-size membranes were activated with 3-5% glutaraldehyde. Stability studies indicated a 20% reduction in activity over 14 days when the immobilized enzyme was used under turnover conditions. © 1996 John Wiley & Sons, Inc.
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  • 95
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    Biotechnology and Bioengineering 51 (1996), S. 271-280 
    ISSN: 0006-3592
    Keywords: immuno-isolation ; fibroblasts ; gene therapy ; β-glucuronidase ; β-hexosaminidase ; Matrigel ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Current human gene therapy relies on genetic modification of the patient's own cells. An alternate nonautologous approach is to use universal cell lines engineered to secrete therapeutic products. Protection with immunoisolation devices before implantation would allow the use of the same recombinant cell line for treating different patients, thus potentially lowering the cost of treatment. To study the properties of a mechanically stable synthetic biomaterial, hydroxyethyl methyacrylate-methyl methacrylate (HEMA-MMA) as the immuno-isolation device, we encapsulated recombinant mouse fibroblast cells engineered to secrete products ranging from 27 to 300 kDa in size (human growth hormone, mouse β-hexosaminidase and β-glucuronidase) in the presence or absence of the extracellular matrix Matrigel. Both viability and cell number in the microcapsules increased with time after encapsulation and cell morphology indicated viable cell growth, thus showing that the capsule membrane barrier was compatible with nutrient/waste exchange necessary for normal metabolic activity.The intracellular levels of these recombinant gene products were constant throughout the experimental period of 22 days in the presence or absence of Matrigel, thus demonstrating that the microenvironment did not lead to downregulation of the transgenes. However, the extracellular levels of the gene products secreted from the cells and trapped within the microcapsules were dependent on the molecular size of the product and presence of Matrigel. With the 27-kDa human growth hormone, the presence of Matrigel caused its retention within this intracapsular space, but its release from the microcapsules to the culture medium was not impeded. With the 120-kDa β-hexosaminidase or the 300-kDa β-glucuronidase, they were retained within the microcapsule space regardless of the presence or absence of Matrigel, and their passage from the microcapsules to the media was totally blocked. In conclusion, the HEMA-MMA microcapsules are supportive of recombinant cell growth and maintained their molecular cutoff at ∼100 kDa. Inclusion of extracellular matrix was unable to improve cell growth and may impede the exit of some gene products. © 1996 John Wiley & Sons, Inc.
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  • 96
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    Biotechnology and Bioengineering 51 (1996), S. 305-316 
    ISSN: 0006-3592
    Keywords: ATP ; regeneration ; ATPase ; ATP synthase ; electrodialysis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We investigated the possibility of using thermostable ATP synthase (TF0F1) for a new ATP regeneration method. TF0F1 was purified from a thermophilic bacterium, PS3, and reconstituted into liposomes. ATP synthesis experiments showed that TF0F1 liposomes could synthesize ATP in micromole concentrations by acid-base change. The acid-base change was repeated six times over an 11-day period with no detectable loss of activity at the reaction temperature (45°C). Given these encouraging results, we conceptualized and modeled a system to synthesize ATP using ATP synthase with energy supplied by acid-base change. In this system, liposomes containing ATP synthase are immobilized on small glass spheres that facilitate separation of buffers from the liposomes after the acid-base change. Compared to an alternate system that uses membranes to separate the buffers from the liposomes, the glass spheres reduce inefficient mixing of acidic and basic buffers during the acid-base change. To increase the ATP synthesis yield, this system uses electrodialysis to regenerate a potassium gradient after the acid-base change. It also employs water-splitting electrodialysis to regenerate KOH and HCl required to adjust the pH of acidic and basic buffers. All reagents are recycled, so electrical energy is the only required input. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 51 (1996), S. 327-341 
    ISSN: 0006-3592
    Keywords: Candida rugosa ; immobilization ; olive oil hydrolysis ; phenylglycidate ; glutaraldehyde ; adipic dihydrazide ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The aim of this study was to evaluate the immobilization of lipase from Candida rugosa on a nylon support by methods used to attach biomolecules to solid supports through their carbohydrate moieties. The carbohydrate groups were converted to dialdehydes by treatment with sodium periodate. The length of exposure and the periodate amount were optimized to the point where almost total activity retention was obtained. Tests of the immobilized enzyme showed the expressed activity to be significantly higher than the activity obtained with the unimmobilized enzyme. The use of reverse micelles as a way of delivering water to the enzyme was tested and found to give significantly higher activities. The immobilized enzyme activity was also tested with other substrates, one of which was a chiral ester. The immobilized enzyme was found to have high stereoselective efficiency and activity toward racemic methyl methoxyphenyl glycidate, a chiral intermediate used in the manufacture of the drug diltiazem. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 51 (1996), S. 375-383 
    ISSN: 0006-3592
    Keywords: cellulase ; enzyme recycling ; enzyme adsorption ; lignocellulosic hydrolysis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Past technoeconomic modeling work has identified the relatively large contribution that enzymatic hydrolysis adds to the total cost of producing ethanol from lignocellulosic substrates. This cost was primarily due to the high concentration of enzyme and long incubation time that was required to obtain complete hydrolysis. Although enzyme and substrate concentration and end-product inhibition influenced the rate of hydrolysis, the effect was less pronounced during the initial stages of hydrolysis. During this time most of the cellulases were adsorbed onto the unhydrolyzed residue. By recycling the cellulases adsorbed to the residual substrate remaining after an initial 24 h, a high rate of hydrolysis, with low overall residence time and minimal cellulase input, could be achieved for several rounds of enzyme recycle. A comparison of the front end (pretreatment, fractionation, and hydrolysis) of a softwood/hardwood to ethanol process indicated that the lignin associated with the softwood-derived cellulose stream limited the number of times the cellulose containing residue could be recycled. © 1996 John Wiley & Sons, Inc.
    Additional Material: 7 Ill.
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  • 99
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 51 (1996), S. 410-421 
    ISSN: 0006-3592
    Keywords: lysozyme ; thermal stability ; 1H NMR ; conformational flexibility ; melting temperature ; PEG ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The reversible folding destabilization of hen lysozyme has been confirmed by a melting temperature (Tm) decrease in aqueous poly(ethylene glycol) (PEG). The percent denatured, extracted from the histidine 15 C2H (H15 C2H) native and denatured peak areas from 500-MHz one-dimensional proton nuclear magnetic resonance (1D 1H NMR) spectra in D2O, was analyzed through denaturation temperatures at 0% and 20% (w/w) PEG 1000. The lysozyme (3.5 mM) Tm decreased by 4.2°C and 7.1°C in 20% (w/w) PEG 1000 at pH 3.8 and 3.0, respectively. The Tm decreased with increasing lysozyme concentration. Additionally, the temperature-induced resonance migrations of 17 protons from 8 residues indicate that the native lysozyme structure undergoes temperature-induced conformational changes. The changes were essentially identical in both 0% and 20% (w/w) PEG 1000 at both pH 3.0 and 3.8. This small, local restructuring of the hydrophobic box region may be a manifestation of temperature-dependent solution hydrophobicity, whereas active-site cleft fluctuations may be due to the inherent active-site flexibility. The lysozyme structure in PEG at 35°C was determined to be essentially native from the 1H nuclear Overhauser effect spectroscopy (NOESY) fingerprint regions. Additionally, lysozyme chemical shifts, from 1D spectra, in PEG 200, 300, and 1000 at 35°C and various concentrations were essentially identical, further confirming that the conformation remains native in various PEG solutions. © 1996 John Wiley & Sons, Inc.
    Additional Material: 6 Ill.
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  • 100
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 51 (1996), S. 237-247 
    ISSN: 0006-3592
    Keywords: biosorption ; sorption ; uranium ; iron ; Pseudomonas aeruginosa ; bacteria ; remediation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Pseudomonas aeruginosa strain CSU, a nongenetically engineered bacterial strain known to bind dissolved hexavalent uranium (as UO22+ and/or its cationic hydroxo complexes), was characterized with respect to its sorptive activity (equilibrium and dynamics). Living, heat-killed, permeabilized, and unreconstituted lyophilized cells were all capable of binding uranium. The uranium biosorption equilibrium could be described by the Langmuir isotherm. The rate of uranium adsorption increased following permeabilization of the outer and/or cytoplasmic membrane by organic solvents such as acetone. P. aeruginosa CSU biomass was significantly more sorptive toward uranium than certain novel, patented biosorbents derived from algal or fungal biomass sources. P. aeruginosa CSU biomass was also competitive with commercial cation-exchange resins, particularly in the presence of dissolved transition metals. Uranium binding by P. aeruginosa CSU was clearly pH dependent. Uranium loading capacity increased with increasing pH under acidic conditions, presumably as a function of uranium speciation and due to the H+ competition at some binding sites. Nevertheless, preliminary evidence suggests that this microorganism is also capable of binding anionic hexavalent uranium complexes. Ferric iron was a strong inhibitor of uranium binding to P. aeruginosa CSU biomass, and the presence of uranium also decreased the Fe3+ loading when the biomass was not saturated with Fe3+, suggesting that Fe3+ and uranium may share the same binding sites on biomass. Although the equilibrium loading capacity of uranium was greater than that of Fe3+, this biomass showed preference of binding Fe3+ over uranium. Thus, a two-stage process in which iron and uranium are removed in consecutive steps was proposed for efficient use of the biomass as a biosorbent in uranium removal from mine wastewater, especially acidic leachates. © 1996 John Wiley & Sons, Inc.
    Additional Material: 8 Ill.
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