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  • 1
    Digitale Medien
    Digitale Medien
    Continuous enantioselective transesterification in organic solvents. Use of suspended lipase preparations in a microfiltration membrane reactor (1995)
    s.l. : American Chemical Society
    Biotechnology progress 11 (1995), S. 436-442 
    Details
    ISSN: 1520-6033
    Quelle: ACS Legacy Archives
    Thema: Werkstoffwissenschaften, Fertigungsverfahren, Fertigung
    Materialart: Digitale Medien
    URL: http://dx.doi.org/10.1021/bp00034a011
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  • 2
    Digitale Medien
    Digitale Medien
    Structured Modeling of Bioreactors (1991)
    Oxford, UK : Blackwell Publishing Ltd
    Annals of the New York Academy of Sciences 646 (1991), S. 0 
    Details
    ISSN: 1749-6632
    Quelle: Blackwell Publishing Journal Backfiles 1879-2005
    Thema: Allgemeine Naturwissenschaft
    Materialart: Digitale Medien
    URL: http://dx.doi.org/10.1111/j.1749-6632.1991.tb18591.x
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  • 3
    Digitale Medien
    Digitale Medien
    Reaction Engineering Aspects of Conjugation in Biodegradation Processes (1994)
    Oxford, UK : Blackwell Publishing Ltd
    Annals of the New York Academy of Sciences 721 (1994), S. 0 
    Details
    ISSN: 1749-6632
    Quelle: Blackwell Publishing Journal Backfiles 1879-2005
    Thema: Allgemeine Naturwissenschaft
    Materialart: Digitale Medien
    URL: http://dx.doi.org/10.1111/j.1749-6632.1994.tb47414.x
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  • 4
    Digitale Medien
    Digitale Medien
    Degradation of 4-aminobenzenesulfonate by a two-species bacterial coculture (1996)
    Springer
    Biodegradation 7 (1996), S. 223-229 
    Details
    ISSN: 1572-9729
    Schlagwort(e): Agrobacterium radiobacter ; 4-aminobenzenesulfonate ; biodegradation ; cross-feeding ; Hydrogenophaga palleronii ; mixed culture
    Quelle: Springer Online Journal Archives 1860-2000
    Thema: Biologie , Energietechnik , Land- und Forstwirtschaft, Gartenbau, Fischereiwirtschaft, Hauswirtschaft
    Notizen: Abstract The mutualistic interactions in a 4-aminobenzenesulfonate (sulfanilate) degrading mixed bacterial culture were studied. This coculture consisted of Hydrogenophaga palleronii strain S1 and Agrobacterium radiobacter strain S2. In this coculture only strain S1 desaminated sulfanilate to catechol-4-sulfonate, which did not accumulate in the medium but served as growth substrate for strain S2. During growth in batch culture with sulfanilate as sole source of carbon, energy, nitrogen and sulfur, the relative cell numbers (colony forming units) of both strains were almost constant. None of the strains reached a cell number which was more than threefold higher than the cell number of the second strain. A mineral medium with sulfanilate was inoculated with different relative cell numbers of both strains (relative number of colony forming units S1:S2 2200:1 to 1:500). In all cases, growth was found and the proportion of both strains moved towards an about equal value of about 3:1 (strain S1:strain S2). In contrast to the coculture, strain S1 did not grow in a mineral medium in axenic culture with 4-aminobenzenesulfonate or any other simple organic compound tested. A sterile culture supernatant from strain S2 enabled strain S1 to grow with 4-aminobenzenesulfonate. The same growth promoting effect was found after the addition of a combination of 4-aminobenzoate, biotin and vitamin B12. Strain S1 grew with 4-aminobenzenesulfonate plus the three vitamins with about the same growth rate as the mixed culture in a mineral medium. When (resting) cells of strain S1 were incubated in a pure mineral medium with sulfanilate, up to 30% of the oxidized sulfanilate accumulated as catechol-4-sulfonate in the culture medium. In contrast, only minor amounts of catechol-4-sulfonate accumulated when strain S1 was grown with 4ABS in the presence of the vitamins.
    Materialart: Digitale Medien
    URL: http://dx.doi.org/10.1007/BF00058181
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  • 5
    Digitale Medien
    Digitale Medien
    Influence of mechanical stress on the growth of Rhizopus nigricans in stirred bioreactorsPaper presented at the “Jahrestreffen der Verfahrensigenieure”, Freiburg, September 30 to October 2, 1987. (1988)
    Weinheim : Wiley-Blackwell
    Chemical Engineering & Technology - CET 11 (1988), S. 178-187 
    Details
    ISSN: 0930-7516
    Schlagwort(e): Chemistry ; Industrial Chemistry
    Quelle: Wiley InterScience Backfile Collection 1832-2000
    Thema: Chemie und Pharmazie , Werkstoffwissenschaften, Fertigungsverfahren, Fertigung
    Notizen: This investigation was undertaken in order to examine the factors affecting mechanical damage to micro-organisms in stirred bioreactors. Growth of the mould Rhizopus nigricans was studied in stirred bioreactors at different geometrical and operating parameters. Since experimental results cannot be described by conventional key parameters, a new concept has been suggested. It is based on the analogy to processes of mechanical disintegration. It is shown that the same key parameter, i.e. the ratio of power input to flow rate, can be used for a satisfactory correlation of experimental data on mechanical damage to micro-organisms, which is an important step in the recovery of intracellular products in biotechnology.
    Zusätzliches Material: 19 Ill.
    Materialart: Digitale Medien
    URL: http://dx.doi.org/10.1002/ceat.270110124
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  • 6
    Digitale Medien
    Digitale Medien
    In vivo analysis of metabolic dynamics in Saccharomyces cerevisiae: II. Mathematical model (1997)
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 55 (1997), S. 592-608 
    Details
    ISSN: 0006-3592
    Schlagwort(e): Saccharomyces cerevisiae ; metabolic modeling ; sensitivity analysis ; glycolysis ; compartmentation ; transient response ; Chemistry ; Biochemistry and Biotechnology
    Quelle: Wiley InterScience Backfile Collection 1832-2000
    Thema: Biologie , Werkstoffwissenschaften, Fertigungsverfahren, Fertigung
    Notizen: A mathematical model of glycolysis in Saccharomyces cerevisiae is presented. The model is based on rate equations for the individual reactions and aims to predict changes in the levels of intra- and extracellular metabolites after a glucose pulse, as described in part I of this study. Kinetic analysis focuses on a time scale of seconds, thereby neglecting biosynthesis of new enzymes. The model structure and experimental observations are related to the aerobic growth of the yeast. The model is based on material balance equations of the key metabolites in the extracellular environment, the cytoplasm and the mitochondria, and includes mechanistically based, experimentally matched rate equations for the individual enzymes. The model includes removal of metabolites from glycolysis and TCC for biosynthesis, and also compartmentation and translocation of adenine nucleotides. The model was verified by in vivo diagnosis of intracellular enzymes, which includes the decomposition of the network of reactions to reduce the number of parameters to be estimated simultaneously. Additionally, sensitivity analysis guarantees that only those parameters are estimated that contribute to systems trajectory with reasonable sensitivity. The model predictions and experimental observations agree reasonably well for most of the metabolites, except for pyruvate and adenine nucleotides. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 592-608, 1997.
    Zusätzliches Material: 11 Ill.
    Materialart: Digitale Medien
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  • 7
    Digitale Medien
    Digitale Medien
    Stereoselective bioconversions in continuously operated fixed bed reactors: Modeling and process optimization (1996)
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 52 (1996), S. 459-471 
    Details
    ISSN: 0006-3592
    Schlagwort(e): continuous kinetic resolution ; fixed bed reactors ; mathematical modeling ; lipases ; Chemistry ; Biochemistry and Biotechnology
    Quelle: Wiley InterScience Backfile Collection 1832-2000
    Thema: Biologie , Werkstoffwissenschaften, Fertigungsverfahren, Fertigung
    Notizen: The nonaqueous lipase-catalyzed kinetic resolution of racemic 2-methyl-1-pentanol in a continuously operated fixed bed reactor was theoretically and experimentally studied. A 2-dimensional mathematical model was developed to predict the performance of the heterogeneous enantioselective biotransformation and to optimize the productivity and effective stereoselectivity of the process by taking pore diffusion, solid(SINGLEBOND)liquid mass transfer, convection, and axial dispersion into account. Experimental investigations were conducted with lipase from Pseudomonas sp. immobilized by ionic binding in the pores of the anion exchange resin Duolite A 568. As determined in prior initial rate experiments, the specific activities of the immobilized lipase were maximal at a water activity of approximately aw = 0.67 and revealed a significant dependence on the amount of enzyme bound to the carrier material, with enantiomeric ratios slightly increasing with increasing water activities. Continuous resolution processes were carried out at a wide range of enzyme loadings. By controlled immobilization according to the theoretically evaluated optimal enzyme loading, the continuous racemic resolution could be optimized to obtain (R)-2-methyl-1-pentanol at high productivity and enantiopurity (ee 〉 95%). The steady-state characteristics of the system could be generally predicted by the model, despite the necessity to reevaluate the kinetic properties of the immobilized lipase to account for the complex non-aqueous microkinetics in a heterogeneous environment. Further model extension introducing competitive inhibition of free water in solutions as well as water diffusion and adsorption to the biocatalyst were useful in providing a more accurate description of the experimental results. © 1996 John Wiley & Sons, Inc.
    Zusätzliches Material: 10 Ill.
    Materialart: Digitale Medien
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  • 8
    Digitale Medien
    Digitale Medien
    Sophorolipid Production with High Yields on Whey Concentrate and Rapeseed Oil without Consumption of Lactose (1998)
    Springer
    Biotechnology letters 20 (1998), S. 805-807 
    Details
    ISSN: 1573-6776
    Quelle: Springer Online Journal Archives 1860-2000
    Thema: Werkstoffwissenschaften, Fertigungsverfahren, Fertigung
    Notizen: Abstract Sophorolipids were produced by single-step batch cultivation of Candida bombicola ATCC 22214 on deproteinized whey concentrate and repeated feed of rapeseed oil. A mild sterilization method for whey was developed. High yields of 280 g dry sophorolipids l−1 were obtained from deproteinized whey concentrate containing 100 g lactose l−1 and 300 g rapeseed oil l−1. Surprisingly, the whey lactose was not consumed by the organism. Growth only on the oil was assumed and a high lipase activity of 24 U per g cell dry weight resulted.
    Materialart: Digitale Medien
    URL: http://dx.doi.org/10.1023/B:BILE.0000015927.29348.1a
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  • 9
    Digitale Medien
    Digitale Medien
    Production of sophorolipids in high concentration from deproteinized whey and rapeseed oil in a two stage fed batch process using Candida bombicola ATCC 22214 and Cryptococcus curvatus ATCC 20509 (1998)
    Springer
    Biotechnology letters 20 (1998), S. 1153-1156 
    Details
    ISSN: 1573-6776
    Schlagwort(e): Candida bombicola ; Cryptococcus curvatus ; whey ; lactose ; sophorolipids ; biosurfactant
    Quelle: Springer Online Journal Archives 1860-2000
    Thema: Werkstoffwissenschaften, Fertigungsverfahren, Fertigung
    Notizen: Abstract High concentrations of 422 g sophorolipids l−1 were produced using a two-stage cultivation process: first deproteinized whey concentrate (DWC) containing 110 g lactose l−1 was used for cultivation of the yeast Cryptococcus curvatus ATCC 20509, resulting in 34 g dry weight l−1, 20 g single-cell oil l−1 and reducing the chemical oxygen demand (COD) from 159 g l−1 to 35 g oxygen l−1. Afterwards cells were disrupted by passing the cell suspension directly through a high pressure laboratory homogeniser. After autoclavation, the resulting crude cell extract containing the single-cell oil served as substrate for growth of Candida bombicola ATCC 22214 and for sophorolipid production in a second stage. When the single-cell oil was consumed, repeated feeding of 400 g rapeseed oil l−1 was started increasing the yield of sophorolipids to 422 g l−1. A simple technique for product isolation, sedimentation, could be used to harvest the crude sophorolipids. © Rapid Science Ltd. 1998
    Materialart: Digitale Medien
    URL: http://dx.doi.org/10.1023/A:1005332605003
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  • 10
    Digitale Medien
    Digitale Medien
    In vivo analysis of metabolic dynamics in Saccharomyces cerevisiae : I. Experimental observations (1997)
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 55 (1997), S. 305-316 
    Details
    ISSN: 0006-3592
    Schlagwort(e): Saccharomyces cerevisiae ; intracellular metabolites ; glycolysis ; adenine nucleotide pool ; glucose effect ; metabolic dynamics ; Chemistry ; Biochemistry and Biotechnology
    Quelle: Wiley InterScience Backfile Collection 1832-2000
    Thema: Biologie , Werkstoffwissenschaften, Fertigungsverfahren, Fertigung
    Notizen: The goal of this work was to obtain rapid sampling technique to measure transient metabolites in vivo. First, a pulse of glucose was added to a culture of the yeast Saccharomyces cerevisiae growing aerobically under glucose limitation. Next, samples were removed at 2 to 5 s intervals and quenched using methods that depend on the metabolite measured. Extracellular glucose, excreted products, as well as glycolytic intermediates (G6P, F6P, FBP, GAP, 3-PG, PEP, Pyr) and cometabolites (ATP, ADP, AMP, NAD+, NADH) were measured using enzymatic or HPLC methods. Significant differences between the adenine nucleotide concentrations in the cytoplasm and mitochondria indicated the importance of compartmentation for the regulation of the glycolysis. Changes in the intra- and extracellular levels of metabolites confirmed that glycolysis is regulated on a time scale of seconds. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 305-316, 1997.
    Zusätzliches Material: 11 Ill.
    Materialart: Digitale Medien
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