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HomeAdvanced Materials ResearchAdvanced Materials Research Vol. 777VFAs Production Potential of Brewery Industry...

VFAs Production Potential of Brewery Industry Wastewater and Starch Wastewater

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Abstract:

The volatile fatty acids (VFAs) are kinds of effective external carbon source for enhanced biological nutrients removal. Volatile fatty acids (VFAs) production from anaerobic fermentation from cassava stillage (CS) wastewater, starch wastewater (SW) and the yellow wine wastewater (YWW) was conducted in batch tests. The VFAs production potential and the characteristics of the fermentative liquid were compared and discussed. Experimental results indicated that the cassava stillage wastewater and the starch wastewater were preferable feed for anaerobic VFAs fermentation. Acetic acid, propionic acid and butyric acid were the main components of the VFAs with respective percentage of 36.5%, 20% and 40% at the end of its fermentation.

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Environmental Biotechnology and Materials Engineering (2013)

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Periodical:

Advanced Materials Research (Volume 777)

Pages:

225-231

DOI:

https://doi.org/10.4028/www.scientific.net/AMR.777.225

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Online since:

September 2013

Authors:

Hui Liu, Lin Xie, Yin Guang Chen, Qi Zhou

Keywords:

Cassava Stillage, Starch Wastewater, Volatile Fatty Acids, Yellow Wine Wastewater

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© 2013 Trans Tech Publications Ltd. All Rights Reserved

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[1] O.H. Annalisa, Z.G. April. Comparisons of organic sources for denitrification: Biodegradability, denitrification rates, kinetic constants and practical implication for their application in WWTPs. Water Environment Federation. (2008) 253-274.

DOI: 10.2175/193864708788735510

[2] D. Bolzonella, L. Innocenti, P. Pavan. et al. Denitrification potential enhancement by addition of anaerobic fermentation products from the organic fraction of municipal solid waste. Water Science and Technology, 44(1) (2001) 187-194.

DOI: 10.2166/wst.2001.0046

[3] A. Bouzas, C. Gabaldon, P. Marzal, et al. Fermentation of municipal primary sludge: effect of SRT and solid concentration on volatile fatty acid production. 13 (2002) 863-875.

DOI: 10.1080/09593332308618359

[4] C.Y. Lee, H.S. Shin. et al. Nutrient removal using anaerobically fermented leachate of food waste in the BNR process. Water Science and Technology, 47(1) (2002) 159-165.

DOI: 10.2166/wst.2003.0042

[5] Z.X. Quan Y.S. Jin C.R. Yin. Hydrolyzed molasses as an external carbon source in biological nitrogen removal. Bioresource Technology, 96 (2005) 1690-1695.

DOI: 10.1016/j.biortech.2004.12.033

[6] L. Rodrı´guez, J. Villasenor. et al. Re-use of winery wastewaters for biological nutrient removal. Water Science & Technology. 56(2) (2007) 95-102.

DOI: 10.2166/wst.2007.477

[7] American Public Health Association (APHA), American Water Works Association(AWWA), Water Environment Federation (WEF), Standard methods for the examination of water and wastewater, 20th ed., Washington, DC: American Public Health Association, (1998).

DOI: 10.1002/j.1551-8833.1932.tb18153.x

[8] O.H. Lowry, N.J. Rosebrough, A.L. Farr, R.J. Randall, Protein measurement withthe Folin phenol reagent, J. Biol. Chem. 193 (1951) 165-175.

DOI: 10.1016/s0021-9258(19)52451-6

[9] D. Herbert, P.J. Philipps, R.E. Strange, Methods Enzymol. 5B (1971) 265-277.

[10] A. Onnis, A. Carucci & G. Cappai. Titration biosensors for the estimation of the biochemical nitrate demand of municipal and industrial wastes. Journal of Industrial Microbiology &Biotechnology, 33 (2006) 243-246.

DOI: 10.1007/s10295-005-0221-6

[11] M. Sage, G. Daufin & G. Gesan-Guiziou. Denitrification potential and rates of complex carbon source from dairy effluents in activated sludge system. Water Research, 40(14) (2006) 2747-2755.

DOI: 10.1016/j.watres.2006.04.005

[12] N. Bernet, F. Habouzit & R. Moletta. Use of an industrial effluent as a carbon source for denitrification of a high-strength wastewater, Applied Microbiology and Biotechnology. 46(1) (1996) 92-97.

DOI: 10.1007/s002530050788

[13] Y. Mokhayeri, A. Nichols, S. Murthy, et al. Examining the influence of substrates and temperature on maximum specific growth rate of denitrifiers. Water Science and Technology, 54(8) (2006) 155-162.

DOI: 10.2166/wst.2006.854

[14] M. Prentice, Sweetening up the Process: Experience with corn syrup for enhanced denitrification at the Henrico County WRF. 2nd External Carbon Source WERF. Washington, DC. (2007).

DOI: 10.2175/193864707786862071

[15] G. Cappai, A. Carucci, A. Onnis. Use of industrial wastewaters for the optimization and control of nitrogen removal processes. Water Science and Technology, 50(6) (2004), 17-24.

DOI: 10.2166/wst.2004.0354

[16] P. Kampas, S.A. Parsons, P. Pearce, et al. An internal carbon source for improving biological nutrient removal. Bioresource Technology, 100 (2009) 149–154.

DOI: 10.1016/j.biortech.2008.05.023

[17] A. Soaresa, P. Kampasa, S. Maillard, et al. Comparison between disintegrated and fermented sewage sludge for production of a carbon source suitable for biological nutrient removal. Journal of Hazardous Materials, 175 (2010) 733–739.

DOI: 10.1016/j.jhazmat.2009.10.070

[18] P. Elefsiniotis, D.G. Wareham, M.O. Smith, Use of volatile fatty acids from an acid-phase digester for denitrification. Journal of Biotechnology, 114 (2004) 289–297.

DOI: 10.1016/j.jbiotec.2004.02.016

[19] H.J. Lee, J.H. Bae, K.M. Cho, Simultaneous nitrification and denitrification in a mixed methanotrophic culture. Biotechnology Letters, 23(12) (2001) 935-941.

[20] A.A. Raghoebarsing, A. Pol, et al. A microbial consortium couples anaerobic methane oxidation to denitrification. Nature, 440 (2006) 918-921.

DOI: 10.1038/nature04617

[21] J.W. Lee, U.J. Yoo, T.H. Chung, Assessment of the availability of organic wastes as an external carbon source for denitrification. Environ. Eng. Res. 5 (2000) 193-198.

[22] Y. Chen, A.A. Randall, T. McCue, The efficiency of enhanced biological phosphorus removal from real wastewater affected by different ratios of acetic to propionic acid. Water Res. 38 (2004) 27–36.

DOI: 10.1016/j.watres.2003.08.025

[23] Z.H. Abu-ghararah, C.W. Randall, The effect of organic compounds on biological phosphorus removal. Water Science and Technology. 23 (1991) 585–594.

DOI: 10.2166/wst.1991.0508

[24] A. Gerber, E. S Mostert, C. T Winter et al. The effect of acetate and other short-chain carbon compound on the kinetics of biological nutrient removal. Water SA. 12 (1986).

[25] D. Kulikowska. Nitrogen removal from landfill leachate via the nitrite route. Brazilian Journal of Chemical Engineering. 29 (2012) 211-219.

DOI: 10.1590/s0104-66322012000200002