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  • 1
    Electronic Resource
    Electronic Resource
    Springer
    Bioprocess and biosystems engineering 2 (1987), S. 65-68 
    ISSN: 1432-0797
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Cell recycle by microfiltration was used in yeast alcoholic fermentation in continuous operation. Toxins were proved to be washed by increasing dilution rate. — Specific ethanol production rate followed an exponential inhibition equation, which is function of both biomass concentration and dilution rate. — Productivity is shown to be 40 times greater than in conventional continuous operation.
    Type of Medium: Electronic Resource
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  • 2
    Electronic Resource
    Electronic Resource
    Springer
    Bioprocess and biosystems engineering 3 (1988), S. 177-180 
    ISSN: 1432-0797
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract The interactions between Schizosaccharomyces pombe and Saccharomyces spp. (S. cerevisiae, S. cerevisiae sake, S. bayanus, S. uvarum) were investigated by growing the yeasts in sterile, partially fermented glucose asparagine medium in flasks, and also in the Ecologen containing either synthetic medium or grape must be separating the adjacent chambers with membranes which allow free movement of medium but not of cells. The growth of Sch. pombe was inhibited by Saccharomyces spp. to a varied extent, but the reverse was not observed. Saccharomyces uvarum, and S. cerevisiae more strongly inhibited Sch. pombe than the other species tested. All three strains of Sch. pombe (ICV-M, BG, ATCC-16979) were inhibited by S. cerevisiae although ICV-M and ATCC strains were more sensitive than BG. The higher growth rate of S. cerevisiae resulted in the exhaustion of nutrients, and its metabolic products could possibly be responsible for the growth inhibition of Sch. pombe. In the light of the present experimental results, the suitability of a two-step fermentation process for making better quality wines from acidic grape musts is discussed.
    Type of Medium: Electronic Resource
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  • 3
    Electronic Resource
    Electronic Resource
    Springer
    Bioprocess and biosystems engineering 5 (1990), S. 123-127 
    ISSN: 1432-0797
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract A flocculating strain of Kluyveromyces marxianus was used for alcoholic fermentation in a continuous bioreactor working with zero residual concentration in effluent. Specific kinetic parameters were improved by increasing dilution rate, which is similar to results obtained with ultrafiltration systems. Specific biomass accumulation rate had always a value greater than 92.5% of specific biomass growth rate and was independent of the dilution rate. Productivity is shown to be 12.5 times greater than in conventional continuous operation and is directly proportional to dilution rate. Maximum biomass concentration also presents a linear relationship with dilution rate. The largest obtained biomass concentration is 8 times greater than in a conventional continuous fermentor.
    Type of Medium: Electronic Resource
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  • 4
    Electronic Resource
    Electronic Resource
    Springer
    Bioprocess and biosystems engineering 2 (1987), S. 175-179 
    ISSN: 1432-0797
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract The inhibitory effect of propionic acid P and biomass concentration X is studied in batch and continuous fermentations with cell recycle. In batch fermentations, the specific growth rate decreases and cancels out at a critical propionic acid concentration Pc 1; the formerly decreasing specific production rate becomes constant after Pc 1 and cancels out when a second critical propionic acid concentration Pc 2 is reached. In continuous fermentation with cell recycle, a similar inhibition is observed with biomass. The specific rates decrease and become constant at a critical biomass concentration Xc. They cancel out at different high biomass concentrations. In both cases, the specific production rate can be related to the specific growth rate by the Luedeking and Piret expression: ν=αμ+β, [1], where the constants α and β are determined by the fermentation parameters.
    Type of Medium: Electronic Resource
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  • 5
    Electronic Resource
    Electronic Resource
    Springer
    Bioprocess and biosystems engineering 7 (1991), S. 157-163 
    ISSN: 1432-0797
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract The paper presents an Intelligent CAD system for Fermentation Process Control (FPC-ICAD) based on a hierarchical architecture possessing three levels: real-time supervision level, CAD level and learning level. The aims of the learning are mainly composed of the aspects fermentation process modelling, determination of appropriate control and estimation methods, determination of the corresponding parameters and fermentation monitoring through measurement and software management. Three independent, but interactive software packages allow user to organize his system for different purposes: on-line control system (with only supervision), off-line CAD as a teaching software, off-line intelligent CAD (CAD+learning package), and on-line intelligent CAD.
    Type of Medium: Electronic Resource
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  • 6
    ISSN: 1432-072X
    Keywords: Temperature ; Growth ; Maintenance ; Candida lipolytica ; n-alcane
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology
    Notes: Abstract The effect of growth temperature on the evolution of kinetic parameters and yields was determined for Candida lipolytica cultures with ntetradecane as substrate, in a temperature range of 18°C to 30°C, which is below the critical growth temperature in order to work only in the activation zone of these parameters. In such a culture limited by substrate transfer, growth rate depends on biological rates, related to microorganisms characteristics, and diffusional rates, related to mass transfer. The effect of temperature thus depends on the limiting step. The activation energy, calculated from exponential growth rate determinations is $$E_{\mu _m } = 63,600{\text{ }}J/mole$$ . When the activation energy is calculated from the maximal rate of cell production (determined at the growth curve's inflexion point), it's found to be E μX=71,200 J/mole in the 18°C–24°C range, and E μX=28,000 J/mole in the 24°C–30°C range. The latter one is characteristic of a diffusion-limited process. Above 24°C, growth is controlled by substrate-transfer, as physiological potentialities are preferentially increased with temperature than diffusional ones: 24°C is thus the transition temperature T t from physiological to diffusional limitation. The apparent yield is almost constant, over the 18°C to 30°C temperature range, although maintenance coefficients are very dependent on temperature. The activation energies related to maintenance coefficients for alkane and oxygen respectively are $$E_{m_s } = 82,500{\text{ }}J/mole$$ and $$E_{mO_{\text{2}} } = 86,200{\text{ }}J/mole$$ . The m s/mO 2 ratio is about 3 (g/g), whereas that, for a strict oxidation reaction of n-tetradecane ought to be 3.47 (g/g). A satisfactory correlation, relating maintenance coefficients to the maximal growth rate of yeast, is given.
    Type of Medium: Electronic Resource
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  • 7
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract To decrease activated sludge production, microbial cell lysis can be amplified to enhance cryptic growth (biomass growth on lysates). Cell breakage techniques (thermal, alkaline, acid) were studied to generate Alcaligenes eutrophus and sludge lysates and to evaluate their biodegradability. Gentle treatment conditions produced the best results. Complete cell deactivation was obtained for temperatures higher than 55 °C. The release kinetics were similar for temperatures varying from 60 °C to 100 °C. A 20-min incubation was suitable for reaching 80% of the maximum releasable carbon. In thermal-chemical hydrolysis, NaOH was the most efficient for inducing cell lysis. Carbon release was a two-step process. First an immediate release occurred, which was of the same order of magnitude for A. eutrophus and sludge [100–200 mg dissolved organic C (DOC) g total suspended solids (TSS)−1], followed by a post-treatment release. The second step was virtually equivalent to the first for sludge, and weaker for A. eutrophus (〈50 mg DOC g TSS−1). The biodegradability of the soluble fraction, both the immediate and the post-treatment carbon release, was investigated. The optimal degradation yield, obtained with sludge cells, reached 55% after 48 h of incubation and 80% after 350 h. The most consistent lysis and biodegradation results occurred at pH 10 and 60 °C after a 20-min incubation.
    Type of Medium: Electronic Resource
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  • 8
    Electronic Resource
    Electronic Resource
    Oxford, UK : Blackwell Publishing Ltd
    Journal of food science 59 (1994), S. 0 
    ISSN: 1750-3841
    Source: Blackwell Publishing Journal Backfiles 1879-2005
    Topics: Agriculture, Forestry, Horticulture, Fishery, Domestic Science, Nutrition , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A chemically defined medium with glutamic acid as nitrogen source was devised for the culture of two species of Monascus (M. ruber and M. purpureus), resulting in optimum production of their pigments and their chemical structures (both free and complexed) were compared. Structural data on two major complex pigments in aqueous solution were obtained by IR, UV, NMR and MS. They were free pigments linked to glutamic acid by amino groups, where nitrogen replaced the pyronoid oxygen.
    Type of Medium: Electronic Resource
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  • 9
    Electronic Resource
    Electronic Resource
    Oxford, UK : Blackwell Publishing Ltd
    Journal of food science 58 (1993), S. 0 
    ISSN: 1750-3841
    Source: Blackwell Publishing Journal Backfiles 1879-2005
    Topics: Agriculture, Forestry, Horticulture, Fishery, Domestic Science, Nutrition , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Following our investigations on food additive production through fermentation, we studied properties of red pigments secreted by Monascus ruber in submerged culture, using ethanol and glutamate as carbon and nitrogen sources. After extraction and purification, these colorants were suspended in water for evaluation. The stability of the extract was tested both in solution and when incorporated into meat products (sausage and pâté). The pigments added to sausage or pate remained stable when stored for 3 mo at 4°C; their stability was between 92 and 98%. Sensory tests revealed that Monascus pigments could replace some traditional food additives such as nitrite salts or cochineal.
    Type of Medium: Electronic Resource
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  • 10
    Electronic Resource
    Electronic Resource
    Amsterdam : Elsevier
    Journal of Fermentation and Bioengineering 69 (1990), S. 178-183 
    ISSN: 0922-338X
    Source: Elsevier Journal Backfiles on ScienceDirect 1907 - 2002
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Type of Medium: Electronic Resource
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