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Separation of volatile compounds from fermentation broth by membrane distillation

Treść / Zawartość
Identyfikatory
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
The diluted ethanol solutions and fermentation broth (Saccharomyces cerevisiae) were separated by membrane distillation (MD). Hydrophobic macroporous (pore size 0.2 ěm) capillary polypropylene membranes, Accurel PP V8/2 HF and Accurel PP S6/2, were used for these studies. The MD process can be successfully applied to remove the volatile components from the fermentation broth. Besides ethanol, propionic and acetic acids were moved from the broth to the distillate. Therefore, the course of the fermentation carried out in a membrane distillation bioreactor considerably accelerate its rate and increase the efficiency by a selective removal of fermentation products. It was found that the broth subjected to the separation did not affect the hydrophobic properties of the polypropylene membrane assembled in the MD modules.
Rocznik
Strony
56--60
Opis fizyczny
Bibliogr. 19 poz., rys.
Twórcy
autor
  • West Pomeranian University of Technology, Szczecin, Institute of Chemical Technology and Environment Engineering, ul. Pułaskiego 10, 70-322 Szczecin, Poland
Bibliografia
  • 1. Ponton, J.W. (2009). Biofuels: Thermodynamic sense and nonsense, J. Cleaner Prod., 17, 896-899. DOI:10.1016/j.jclepro.2009.02.003.
  • 2. Demirbas, A. (2007). Progress and recent trends in biofuels, Prog. Energy Combust. Sci., 33, 1–18. DOI:10.1016/j.pecs.2006.06.001.
  • 3. Grajek, W., Gumienna, M., Lasik, M. & Czarnecki, Z. (2008). Perspectives for ethanol production from starchy matherials, Przem. Chem., 87 (11), 1094–1101 (in Polish).
  • 4. Sassner, P., Galbe, M. & Zacchi, G. (2008). Technoeconomic evaluation of bioethanol production from three different lignocellulosic materials, Biomass Bioenergy, 32, 422–430. DOI:10.1016/j.biombioe.2007.10.014.
  • 5. Bai, F.W., Anderson, W.A. & Moo-Young, M. (2008). Ethanol fermentation technologies from sugar and starch feedstocks, Biotechnol. Adv., 26, 89–105. DOI:10.1016/j.biotechadv.2007.09.002.
  • 6. Morin-Couallier, E., Payot, L.T., Pastore Bertin, A. & Lameloise, M.L. (2006). Recycling of distillery effluents in alcoholic fermentation, Appl. Biochem. Biotechnol., 133, 217–238. DOI: 10.1385/ABAB:133:3:217.
  • 7. Morin-Couallier, E., Salgado-Ruiz, B., Lameloise, M.L. & Decloux, M. (2006). Usefulness of reverse osmosis in the treatment of condensates arising from the concentration of distillery vinasses, Desalination, 196, 306–317. DOI:10.1016/j.desal.2006.02.002.
  • 8. Takaya, M., Matsumoto, N. & Yanase, H. (2002). Characterization of membrane bioreactor for dry wine production, J. Biosci. Bioeng., 93 (2), 240–244. DOI:10.1016/S1389-1723(02)80021-4.
  • 9. Park, B.G., Lee, W.G., Chang, Y.K. & Chang, H.N. (1999). Long-term operation of continuous high cell density culture of Saccharomyces cerevisiae with membrane filtration and on-line cell concentration monitoring, Bioprocess Eng., 21, 97–100. DOI: 10.1007/PL00009070.
  • 10. Maiorella, B.L., Blanch, H. W. & Wilke, C.R. (1984). Economic evaluation of alternative ethanol fermentation processes, Biotechnol. Bioeng., 26, 1003–1025. DOI: 10.1002/bit.260260902
  • 11. Gyamerah, M. & Glover, J. (1996). Production of ethanol by continuous fermentation and liquid – liquid extraction, J. Chem. Tech. Biotechnol., 66, 145–152. DOI: 10.1002/(SICI)1097-4660(199606).
  • 12. Nakao, S., Saitoh, F., Asakura, T., Toda, K. & Kimura, S. (1987). Continuous ethanol extraction by pervaporation from a membrane bioreactor. J. Membr. Sci., 30, 273–287. DOI:10.1016/S0376-7388(00)80123-4.
  • 13. Miyazawa, K.I. & Kokugan, T. (1998). Effect of production removal by pervaporation on ethanol fermentation, J. Ferment. Bioeng., 86(5). 488–493. DOI:10.1016/S0922-338X(98)80157-8.
  • 14. Gryta, M. (2001). The fermentation process integrated with membrane distillation, Separ. Purif. Technol., 24, 283–296. DOI:10.1016/S1383-5866(01)00132-0.
  • 15. Gryta, M., Morawski, A.W. & Tomaszewska, M. (2000). Ethanol production in membrane distillation bioreactor, Catal. Today, 56, 159–165. DOI:10.1016/S0920-5861(99)00272-2.
  • 16. Gryta, M. & Barancewicz, M. (2010). Influence of morphology of PVDF capillary membranes on the performance of direct contact membrane distillation, J. Membr. Sci., 358, 158–167. DOI:10.1016/j.memsci.2010.04.044.
  • 17. Taylor, R. & Krishna, R. (1993). Multicomponent mass transfer, New York, USA, John Willey.
  • 18. Barancewicz, M., Sasim, M. & Gryta, M. (2009). Zastosowanie chromatografii jonowej do badania przebiegu fermentacji, Prace i Studia, 77, 89–101.
  • 19. El-Bourawi, M.S., Ding, Z., Ma, R., & Khayet, M. (2006). A framework for better understanding membrane distillation separation process, J. Membr. Sci., 285, 4–29. DOI: 10.1016/j.memsci.2006.08.002.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BPS3-0020-0045
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