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  • 1
    Electronic Resource
    Electronic Resource
    Amsterdam : Elsevier
    Journal of Chromatography A 626 (1992), S. 171-180 
    ISSN: 0021-9673
    Source: Elsevier Journal Backfiles on ScienceDirect 1907 - 2002
    Topics: Chemistry and Pharmacology
    Type of Medium: Electronic Resource
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  • 2
    Electronic Resource
    Electronic Resource
    Oxford, UK : Blackwell Publishing Ltd
    FEMS microbiology letters 21 (1984), S. 0 
    ISSN: 1574-6968
    Source: Blackwell Publishing Journal Backfiles 1879-2005
    Topics: Biology
    Notes: Abstract 62 isolates of Penicillium and Aspergillus were screened for cyclopiazonic acid (CPA) production by surface and submerged culture on different media. The production of this mycotoxin was restricted to Penicillium camembertii group II (and its domesticated form P. camembertii), P. griseofulvum, and Aspergillus flavus (and its domesticated form A. oryzae). The best yield of CPA was obtained by a strain of P. griseofulvum, but several strains of P. camembertii group II were also good producers. Propionic acid (500 and 1000 mg/l medium) did not enhance the production of CPA. The best yields of CPA were obtained in submerged culture, but in some cases growth and CPA production only occured in surface culture. A simplified procedure for isolation of CPA is described.
    Type of Medium: Electronic Resource
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  • 3
    Electronic Resource
    Electronic Resource
    Springer
    Bioprocess and biosystems engineering 9 (1993), S. 205-213 
    ISSN: 1432-0797
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Fed-batch cultivations of hybridoma cell cultures for antibody production were computer simulated by a detailed structured model, that divides the cell mass into four metabolic compartments and makes use of descriptions of the most important metabolic pathways. Surprisingly the simulations indicate, that online or frequent off-line control of fed-batch hybridoma cultures may lead to low and variable yields of antibody product. With less frequently controlled fed-batch cultures the system is more stable; and there is an optimal time interval for control, that depends on the feeds selected. The product yields in optimal fed-batch cultivations, however, are seldom higher than in comparable batch cultivations.
    Type of Medium: Electronic Resource
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  • 4
    Electronic Resource
    Electronic Resource
    Springer
    Bioprocess and biosystems engineering 14 (1995), S. 23-31 
    ISSN: 1432-0797
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Production of α-amylase by a strain of Bacillus amyloliquefaciens was investigated in a cell recycle bioreactor incorporating a membrane filtration module for cell separation. Experimental fermentation studies with the B. amyloliquefaciens strain WA-4 clearly showed that incorporating cell recycling increased α-amylase yield and volumetric productivity as compared to conventional continuous fermentation. The effect of operating conditions on α-amylase production was difficult to demonstrate experimentally due to the problems of keeping the permeate and bleed rates constant over an extended period of time. Computer simulations were therefore undertaken to support the experimental data, as well as to elucidate the dynamics of α-amylase production in the cell recycle bioreactor as compared to conventional chemostat and batch fermentations. Taken together, the simulations and experiments clearly showed that low bleed rate (high recycling ratio) various a high level of α-amylase activity. The simulated fermentations revealed that this was especially pronounced at high recycling ratios. Volumetric productivity was maximum at a dilution rate of around 0.4 h−1 and a high recycling ratio. The latter had to exceed 0.75 before volumetric productivity was significantly greater than with conventional chemostat fermentation.
    Type of Medium: Electronic Resource
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  • 5
    Electronic Resource
    Electronic Resource
    Springer
    Bioprocess and biosystems engineering 8 (1992), S. 113-119 
    ISSN: 1432-0797
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Sets of simulations of run-away fermentations were structured as two-level factorial experimental designs with parameters in a mathematical model as factors. By this technique it was possible to document the robustness and sensitivity of the model and to show why run-away fermentations may be difficult to control in practice. In an engineering approach to fermentation development it is beneficial to integrate simulation of fermentation experiments with real fermentation experiments in order to get a better planning and interpretation.
    Type of Medium: Electronic Resource
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  • 6
    Electronic Resource
    Electronic Resource
    Springer
    Bioprocess and biosystems engineering 8 (1992), S. 157-163 
    ISSN: 1432-0797
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Three different commercially available stirred tank reactors for mammalian cell culturing were compared for the ability to support hybridoma cell growth and monoclonal antibody production in batch mode operation. Despite quite similar vessel geometries differences were found both in growth and production profiles in the systems. These differences can possibly be related to the different aeration modes used in the bioreactors, and the levels of shear stress created by stirrer and agitator in the tanks.
    Type of Medium: Electronic Resource
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  • 7
    Electronic Resource
    Electronic Resource
    Springer
    Bioprocess and biosystems engineering 13 (1995), S. 59-68 
    ISSN: 1432-0797
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Enzyme production in a cell recycle fermentation system was studied by computer simulations, using a mathematical model of α-amylase production by Bacillus amyloliquefaciens. The model was modified so as to enable simulation of enzyme production by hypothetical organisms having different production kinetics at different fermentation conditions important for growth and production. The simulations were designed as a two-level factorial assay, the factor studied being fermentation with or without cell recycling, repression of product synthesis by glucose, kinetic production constants, product degradation by a protease, mode of fermentation, and starch versus glucose as the substrate carbon source. The main factor of importance for ensuring high enzyme production was cell recycling. Product formation kinetics related to the stationary growth phase combined with continuous fermentation with cell recycling also had a positive impact. The effect was greatest when two or more of these three factors were present in combinations, none of them alone guaranteeing a good result. Product degradation by a protease decreased the amount of product obtained; however, when combined with cell recycling, the protease effect was overshadowed by the increased production. Simulation of this type should prove a useful tool for analyzing troublesome fermentations and for identifying production organisms for further study in integrated fermentation systems.
    Type of Medium: Electronic Resource
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  • 8
    Electronic Resource
    Electronic Resource
    Springer
    Bioprocess and biosystems engineering 8 (1992), S. 173-181 
    ISSN: 1432-0797
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract The product formation during batch fermentation with recombinant E. coli containing a runaway replication plasmid has been examined. Theoretical modelling is combined with experimental work to study the effect of operating conditions. In particular the influence of induction profile has been investigated. High sensitivity to operating conditions is observed, and both model and experimental data illustrate the presence of very narrow limits for an optimal induction profile.
    Type of Medium: Electronic Resource
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  • 9
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 13 (1981), S. 29-33 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Fed-batch fermentations with Penicillum chrysogenum, strain S 3723, were fed with glucose as carbon source or with a mixture of glucose and acetic acid. When 20% of the carbon source was acetic acid, yields of penicillin-V were 25% higher than in fermentations where glucose was the only carbon source in the feed. The increased yield was due to higher specific productivity and/or cell mass. The effect was seen in fermentations where the carbon source was fed at a constant rate and the pH kept automatically at 6.5 by addition of inorganic acid or base, as well as in fermentations where pH controlled the addition of feed.
    Type of Medium: Electronic Resource
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  • 10
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 44 (1996), S. 724-730 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract  Overproduction of proteinase A by recombinant Saccharomyces cerevisiae was investigated by cultivations in a cell-recycling bioreactor. Membrane filtration was used to separate cells from the broth. Recycling ratios and dilution rates were varied and the effect on enzyme production was studied both experimentally and by computer simulations. Experiments and simulations showed that cell mass and product concentration were enhanced by high ratios of recycling. Additional simulations showed that the proteinase A concentration decreased drastically at high dilution rates and the optimal volumetric productivities were at high dilution rates just below washout and at high ratios of recycling. Cell-recycling fermentation gave much higher volumetric productivities and stable product concentrations in contrast to simple continuous fermentation.
    Type of Medium: Electronic Resource
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