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  • 1985-1989  (9)
  • 1
    Electronic Resource
    Electronic Resource
    s.l. : American Chemical Society
    Analytical chemistry 58 (1986), S. 108-124 
    ISSN: 1520-6882
    Source: ACS Legacy Archives
    Topics: Chemistry and Pharmacology
    Type of Medium: Electronic Resource
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  • 2
    Electronic Resource
    Electronic Resource
    s.l. : American Chemical Society
    Analytical chemistry 60 (1988), S. 131-146 
    ISSN: 1520-6882
    Source: ACS Legacy Archives
    Topics: Chemistry and Pharmacology
    Type of Medium: Electronic Resource
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  • 3
    Electronic Resource
    Electronic Resource
    [s.l.] : Nature Publishing Group
    Nature 332 (1988), S. 181-181 
    ISSN: 1476-4687
    Source: Nature Archives 1869 - 2009
    Topics: Biology , Chemistry and Pharmacology , Medicine , Natural Sciences in General , Physics
    Notes: [Auszug] Modern Biotechnology. By S. B. Primrose. Blackwell Scientific: 1987. Pp. 176. Hbk á£25, $47.50; pbk á£12.95, $24.50. Introduction to Biotechnology. By C. M. Brown, I. Campbell and F. F. Priest. Blackwell Scientific: 1987. Pp. 169. Pbk á£9.95, $22.50. ...
    Type of Medium: Electronic Resource
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  • 4
    Electronic Resource
    Electronic Resource
    Springer
    Biotechnology letters 8 (1986), S. 287-292 
    ISSN: 1573-6776
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Butyric acid conversion by a mixed methanogenic population in a pilot scale anaerobic downflow fixed-film reactor (DFFR), treating a cheese factory effluent was increased by the addition of nickel (30 mg/l NiCl2. 6H2O). The butyric acid concentration dropped abruptly (2300 to 150 mg/l) when the reactor was fed with Ni (II). Furthermore, when running two lab. scale DFFRs butyric acid utilization and methane production were slightly higher within the reactor supplemented with nickel than in the control reactor (without nickel).
    Type of Medium: Electronic Resource
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  • 5
    Electronic Resource
    Electronic Resource
    Springer
    Biotechnology techniques 3 (1989), S. 155-160 
    ISSN: 1573-6784
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary Flux performance of a poly vinylidene di-fluoride (PVDF) microfiltration membrane duringSaccharomyces cerevisiae harvesting has been studied. The initial challenge to the membrane has been found to influence subsequent flux. The permeability of the membrane is closely dependent on the pH and membrane conditioning prior to microfiltration improves the flux by more than 70%.
    Type of Medium: Electronic Resource
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  • 6
    Electronic Resource
    Electronic Resource
    Springer
    Biotechnology letters 8 (1986), S. 379-384 
    ISSN: 1573-6776
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary An anaerobic downflow fixed film (DSFF) reactor was used to treat cheese whey. The reactor was initially operated flooded (DSFF mode) and then the liquid level reduced by 67% (ATF mode); thus, the packing support was completely submerged and one third submerged respectively. The partly submerged anaerobic culture had higher gas production, and was more resistant to general and localized high VFA levels; methanogenic bacteria were acclimated to VFA levels as high as 3000 mg/l of propionate and 1600 mg/l of acetate (pH near neutrality) whilst the reactor remained stable.
    Type of Medium: Electronic Resource
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  • 7
    Electronic Resource
    Electronic Resource
    Springer
    Biotechnology techniques 1 (1987), S. 115-116 
    ISSN: 1573-6784
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary The ability of a recently developed affinity membrane to adsorb commercially prepared trypsin was investigated. Several buffered solutions of trypsin which varied in their initial concentrations from 62.5 mg/l to 1,000 mg/l, were passed through a stacked bed of seven membranes; dry wt 350 mgs. The adsorbed protein was eluted using acetic acid; 2.2 mgs to 5.3 mgs of trypsin was desorbed. The adsorption capacity tended to a maximum of 16 mg /g dry wt when the initial feed concentration of trypsin was 1 g/l. There was no loss in enzyme activity after desorption; 11,500 IU ± 500 IU.
    Type of Medium: Electronic Resource
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  • 8
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 32 (1988), S. 348-355 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Development of a novel two-layer anaerobic biofilm model is based on substrate utilization kinetics and mass transport. The model is applied to steady-state conditions for a fixed-film anaerobic reactor. The microbial film is considered to consist of two distinct biofilm layers, one adjacent to the second, with an acidogenic bacteria biofilm forming the outer layer and a methanogenic film the inner one. The model assumes that sugars are only metabolized by the first layer and converted into volatile fatty acids (VFA), while fatty acids are taken up only by the inner layer. The model is able to predict both substrate flux net uptake and methane production for steady-state conditions. The results of modeling agree with methane production experimental data published elsewhere. Further, the model shows why layered fixed-film reactors can withstand high and inhibitory concentrations of volatile fatty acids as well as severe overloading without failure.
    Additional Material: 12 Ill.
    Type of Medium: Electronic Resource
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  • 9
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 30 (1987), S. 289-296 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A two-column pilot scale downflow percolating fixed film (DPFF) anaerobic reactor treating deproteinized cheese whey (DPW) was used in this study. The system was operated at one-third of the maximum working volume in an attempt to avoid mass transfer limitations of the gas products (since two-thirds of the immobilized microbial culture was unsubmerged), as well as to minimize the effects of localized high volatile fatty acids (VFA) levels and low pH on its methanogenic activity. A new method to shorten the start-up period was used by growing methanogenic and acetogenic (H2-producers) bacteria on a synthetic medium until reaching a stable methane production rate and then switching the reactor over to DPW and allowing acidogenic growth. The start-up period was reduced to 35 days as a result of this operational mode. The reactor was able to handle 8 kg COD/ m3·d after 35 days of operation.
    Additional Material: 8 Ill.
    Type of Medium: Electronic Resource
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