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1997 | 41 | 06 |

Tytuł artykułu

Procesy fermentacyjne z recyrkulacja komorek. Cz.II. Przyklady zastosowan

Warianty tytułu

Języki publikacji

PL

Abstrakty

PL
W artykule przedstawiono krótki przegląd zastosowania technologii fermentacji z recyrkulacją komórek do produkcji kultur starterowych, etanolu, kwasów organicznych i enzymów. Lista ta nie wyczerpuje wszystkich możliwości, niemniej daje pogląd na potencjał zastosowawczy tej metody fermentacji.
EN
Short reviev of the application of the fermentation technology with cell recilculation, initial culture, ethanol, organic acids and enzymes were presented in this article. This list does not embraces all possibilities but gives an idea on the application potential of this fermentation method.

Wydawca

-

Rocznik

Tom

41

Numer

06

Opis fizyczny

s.29-31,tab.,bibliogr.

Twórcy

autor
  • Akademia Rolnicza, Poznan
autor

Bibliografia

  • [1] Aeschlimann A., Stockar von U.: Continuous production of lactic acid from whey permeate by Lactobacillus helveticus in a cell-recycle reactor. Enzyme Microb. Technol., 1991, 13, 811-816.
  • [2] Alfa Laval AB: Brochures on the Biostill Process (Tumba, Sweden).
  • [3] Barreto M.T.O., Melo E.P., Moreira J.L., Carrondo M.J.T.: High cell density reactor for the production of Lactobacillus planlarum. J. Ind. Microbiol., 1991, 7, 63-70.
  • [4] Bibal B., Vayssier Y., Gота G.. Pareilleux A.: High-concentration cultivation of Lactobacillus cremoris in a cell-recycle reactor. Biotechnol. Bioeng. 1991, 37, 746-754.
  • [5] Boyaval P., Corre C.: Continuous fermentation of sweet whey permeate for propionic acid production in a CSTR with UF recycle Biotechnol. Lett., 1987, 9, 801-806.
  • [6] Boyaval P., Seta J., Gavach C.: Concentrated propionic acid production by electrodialysis.. Enzyme Microb. Technol., 1993, 15, 683-686.
  • [7] Carrondo M.J.T., Crespo J.P.S.G., Moura M.J.: Proc. 4th Eur. Congress Biotechnol., 1987, Vol. 1, 97-100.
  • [8] Colman A., Roger L., Boyaval P.: Production of propionic acid from whey permeate by sequential fermentation, ultrafiltration, and cell recycling. Biotechnol. Bioeng. 1993, 42, 1091-1098.
  • [9] Denis S., Boyaval P.: Microbial enzyme production in a membrane bioreactor. Appl. Microbiol. Biotechnol., 1991, 34, 608-612.
  • [10] Fontana A., Chraibi M., Guiraud J.P., Ghommidh C.: Diffusivity measurement in a flocculating yeast layer. Biotechnol. Tech., 1991, 5, 133-138.
  • [11] Goma G., Durand G.: Nouvelles conceptions de mise en oeuvre des microorganismes et de bioreacteurs, bases sur les cultures a forte densité cellulaire. Abstract 11 Colloque S.F.M., 1986, 127-143.
  • [12] Groot IV. J., Kraayenbring M.R., Waldram R.H., van der Lans R.G.J.M., Luyben K.Ch.A.M.: Ethanol production in an integrated process of fermentation and et- hanol recovery by pervaporation. Bioprocess Eng. 1993, 8, 99-111.
  • [13] Groot W.J., Kraayenbrink M.R., Waldram RH., van der Lans R.G.J.M., Luyben K.Ch.A.M.: Ethanol production in an integrated fermentation/membrane system. Process simulations and economics. Bio- process Eng. 1993, 8, 189-201.
  • [14] Hayakawa K., Sansawa H., Nagamune T., Endo .: High density culture of Lactobacillus casei by a cross-flow culture method based on kinetic properties of the microorganism. J. Ferment. Bioeng., 1990, 70, 404-408.
  • [15] Maia A.B.R.A., Nelson D.L.: Application of gravitational sedimentation to efficient cellular recycling in continuous alcoholic fermentation. Biotechnol. Bioeng. 1993,41, 361-369.
  • [16] Mehaia M.A., Cheryan M.: Production of lactic acid from sweet whey permeate concentrates. Process Biochem. 1987, 22, 185-188.
  • [17] Nakajima M., Iwasaki K., Nabetani H., Watanabe A.: Continuous hydrolysis of soluble starch by free a-amylase and pullulanase using an ultrafiltration membrane reactor. Agric. Biol. Chem., 190, 54, 2793-2799.
  • [18] Nakajima M., Watanabe A., Jimbo N., Nishizawa K., Nakao S.: Forced-flow bioreactor for sucrose inversion using ceramic membrane activated by silinization. Biotechnol. Bioeng., 1989, 33, 856—861.
  • [19] Nomura Y., Iwahara M., Hongo M.: Continuous production of acetic acid by electrodialysis bioprocess with a computerized control of fed batch culture. J. Biotechnol., 1989, 12, 317-326.
  • [20] Nomura Y., Iwahara M., Hongo M.: Production of acetic acid by Clostridium thermoaceticum in electrodialysis culture using a fermentor equipped with an electrodialyser. World J. Microbiol Biotechnol, 1994, 10, 427-132.
  • [21] Ohlever E., Blanch H., Wilke C.R.: Appl. Biochem. Biotechnol. 1985, 11, 317-332.
  • [22] Prigent C., Corre C., Boyaval P.: Production of concentrated Streptococcus salivarius subsp. thermophilus by coupling continuous fermentation and ultrafiltration J. Dairy Res., 1988, 55, 579-587.
  • [23] Pronk W., Boswinkel G., Rietvan't K.: Parameters influencing hydrolysis kinetics of lipase in a hydrophilic membrane bioreactor. Enzyme Microb. Technol., 1992, 14, 214-220.
  • [24] Sousa M.L., Teixeira J.A.: Reduction of diffusional limitations in yeast floes. Biotechnol. Lett.. 1991, 7, 343-348.
  • [25] Sousa M.L., Teixeira J.A.: Comparative analysis of ethanolic fermentation in two continuous flocculation bioreactors and effect of flocculation additive. Bioprocess Eng., 1994, 11, 83-90.
  • [26] Teixeira J.A., Mota M.: Experimental assessment of internal diffusion limitations in yeast floes. Chem. Eng. J., 1990, 43, B13-B17.
  • [27] Verseveid van H. W., Metwally M., Sayedel M., Osman M., Schrickx J.M.: Determination od the maximum product yield from glucoamylase-producing Aspergillus niger grown in the recycling fermentor. Antonie van Leeuwenhoek, 1991, 60, 313-323.

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