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  • 1
    Electronic Resource
    Electronic Resource
    Influence of sulfates and operational parameters on volatile fatty acids concentration profile in acidogenic phase (1991)
    Springer
    Bioprocess and biosystems engineering 6 (1991), S. 145-151 
    Details
    ISSN: 1432-0797
    Source: Springer Online Journal Archives 1860-2000
    Topics: Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Anaerobic treatment of distillery wastewaters containing high sulfate concentrations was carried out on a two-phase process. The acidogenic phase was operated so as to produce the more favourable intermediates for methanogenic bacteria coupled with maximum sulfate removal. Sulfate removal was directly affected by pH and dilution rate (D). The maximum sulfate removal and acetic acid production was achieved at pH 6.6 and D=0.035 h−1. A linear relationship between acetic acid produced and sulfate removal was observed, indicating that acetic acid was mainly produced by sulfate reducing bacteria with important operational advantages. Higher concentrations of butyric acid were obtained at low pH values and high dilution rates.
    Type of Medium: Electronic Resource
    URL: http://dx.doi.org/10.1007/BF00369251
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    Paper (German National Licenses)
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  • 2
    Electronic Resource
    Electronic Resource
    Inert supports for lactic acid fermentation —a technological assessment (1992)
    Springer
    Applied microbiology and biotechnology 38 (1992), S. 305-311 
    Details
    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.
    Type of Medium: Electronic Resource
    URL: http://dx.doi.org/10.1007/BF00170077
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  • 3
    Electronic Resource
    Electronic Resource
    Elucidation of the mechanism of lactic acid growth inhibition and production in batch cultures of Lactobacillus rhamnosus (1997)
    Springer
    Applied microbiology and biotechnology 48 (1997), S. 346-350 
    Details
    ISSN: 1432-0614
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Batch cultures of Lactobacillus rhamnosus were carried out at different pH values in order to study the limitation of growth and lactic acid production by the hydrogen ion, non-dissociated lactic acid and internal lactate concentrations. The effect of pH between 5 and 6.8 was studied at non-limiting concentrations of glucose; this is more significant for the lactic acid fermentation rate than for the maximum specific growth rate, as shown by the incomplete substrate consumption at lower values of medium pH and by the constant maximum cell mass obtained within the range of pH values studied. To check whether these results were a direct consequence of the different concentrations of the non-dissociated form of lactic acid at different external pH values, specific growth rates and lactic acid productions rates were calculated for each external pH value. The same specific growth rates were observed at the same non-dissociated lactic acid concentrations only at pH values of 5 and 5.5. For higher values of pH (pH 〉 6) the specific growth rate falls to zero as the non-dissociated lactic acid concentration decreases. This shows that generalisations made from studies performed within very narrow ranges of pH are not valid and that the non-dissociated form of lactic acid is not the only inhibiting species. The internal pH was measured experimentally for each external pH value in order to calculate the internal lactate ion concentration. This form is described to be the inhibitory one. The results obtained confirmed that the specific growth rate reached zero at approximately the same lactate concentration for all the pH values studied.
    Type of Medium: Electronic Resource
    URL: http://dx.doi.org/10.1007/s002530051060
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  • 4
    Electronic Resource
    Electronic Resource
    Operational patterns affecting lactic acid production in ultrafiltration cell recycle bioreactor (1995)
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 45 (1995), S. 320-327 
    Details
    ISSN: 0006-3592
    Keywords: cell recycle reactor ; ultrafiltration tubular membranes ; high lactic acid productivities ; best operational conditions ; different dilution rates ; start-up strategy ; membrane permeability ; long-term fermentations ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Lactic acid production with cell recycling on an ultrafiltration tubular membrane reactor was studied; higher lactic acid concentrations as well as productivities were obtained under long-term fermentations compared with other high cell density systems. Different operational conditions, namely dilution rates and start-up modes, were assessed. Performances were very different at the three different dilution rates tested (D = 0.20 h-1, D = 0.40 h-1, or D = 0.58 h-1). The different behaviours are discussed and factors responsible for them are presented. The best way to operate for lactic acid production is chosen, the dilution rate of D = 0.40 h-1 being the one providing the best overall performance. On the other hand, results show that of the two start-up modes tested, continuous start (membrane open) permits higher permeabilities throughout the operational runs than batch start (membrane closed). Operational stability was found to be directly associated with membranes that work at “steady state,” the membrane permeability being kept around 15 L/m2 h. Optimized cell bleed can improve time of operation if such membrane permeability can be maintained for a longer time. A comparison of results with those obtained in other lactic acid production systems is presented; such comparison shows that this tubular ultrafiltration membrane cell recycle reactor presents three important advantages: (1) concomitant lactic acid concentrations and productivities; (2) long periods of operation at reasonable permeabilities; and (3) good mechanical stability permitting the use of steam sterilization. © 1995 John Wiley & Sons, Inc.
    Additional Material: 10 Ill.
    Type of Medium: Electronic Resource
    URL: http://dx.doi.org/10.1002/bit.260450406
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    Paper (German National Licenses)
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