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  • 1
    Electronic Resource
    Electronic Resource
    Springer
    Journal of industrial microbiology and biotechnology 7 (1991), S. 63-69 
    ISSN: 1476-5535
    Keywords: Flocculation ; Fluidized bed reactor ; Lactobacillus plantarum ; Lactic starter culture
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary The production of a flocculent strain ofLactobacillus plantarum was performed in a high cell density reactor: a fluidized bed reactor (FBR) with a settler and an external cell recirculation. Two variables were assessed, the recirculation rate (R) and the dilution rate (D). The effect of the latter is much more important than the effect of the former in ensuring a quick start up in the flocculation process. The cell volumetric productivities obtained with this system increase directly with dilution rate and recirculation rate. The values of cell volumetric productivities obtained are considerably higher than those obtained in continuous stirred tank reactors (CSTR) and much higher than in batch reactors.
    Type of Medium: Electronic Resource
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  • 2
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 38 (1992), S. 305-311 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Production of lactic acid using Lactobacillus delbrueckii NRRL B445 recently renamed L. rhamnosus was studied in continuously recycled packed reactors at pH 6.3 and 42° C. Four inert adsorbent supports were used for immobilization: Raschig rings of sintered glass (Schott, FRG), beads of sintered glass (Schott), beads of porous glass (Poraver; Dennert, FRG) and irregular ceramic particles (Otto Feuerfest, FRG). The best support was found to be the beads of sintered glass, yielding the highest volumetric lactic acid productivity. Zeta potentials of L. rhamnosus showed the cells to be negatively charged at all pHs studied, the charge becoming less negative with increasing ionic strength. The surface charge did not control adhesion. A comparison between the immobilization carried out in batch and continuous tests with the different supports demonstrated that extrapolation from batch adsorption curves to continuous operation can introduce large errors. The effect of dilution rate was also stidied: a saturation concentration of adsorbed cells was achieved at all dilution rates, i.e., the immobilized cell component was almost invariant. Different diameters of Poraver beads were tested; clear evidence for mass transfer limitation was shown. Finally, the effects of pH and substrate concentration under immobilization were evaluated. The results indicate that pHs above or below the optimum for suspended cell systems can be used in the immobilized reactor while maintaining lactic acid productivity. To simplify downstream processing by keeping the glucose concentration close to zero in the effluent, the glucose concentration in the feed has to be chosen in conjunction with the dilution rate.
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  • 3
    Electronic Resource
    Electronic Resource
    Springer
    Applied microbiology and biotechnology 34 (1991), S. 648-652 
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Summary A simple method of assessing the viability of a lactic starter culture is presented. The method is based on the kinetics of growth of a culture during the lag and early exponential phases. The microorganisms used throughout this work were Lactobacillus spp. The method was tested with inocula samples of different ages and with samples taken during chemostat runs, at different dilution rates. The results obtained are similar to ones describes in the literature for similar situations. The method is very easy to operate once the intrinsic parameters have been established (χmax and μmax). It needs only standard laboratory equipment and is very economical.
    Type of Medium: Electronic Resource
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  • 4
    Publication Date: 1991-02-01
    Print ISSN: 0175-7598
    Electronic ISSN: 1432-0614
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Published by Springer
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