Year 2018,
Volume: 1 Issue: 2, 39 - 44, 28.03.2018
Abdullah Saghir
,
Salwa Hajjar
References
- [1]. A. Saghir, “Industrial wastewater treatment in Arabic world,” Arabic scientific publishers, Lebanon, 2017.
[2]. R. Rajakumar, T. Meenambal, P.M. Saravanan, P. Ananthanarayanan, ”Treatment of poultry slaughterhouse wastewater in hybrid upflow anaerobic sludge blanket reactor packed with pleated poly vinyl chloride rings,” Bioresource Technology. Vol. 103 (1), pp. 116–122, 2012.
[3]. E. Gengec, M. Kobya, E. Demirbas, A. Akyol and K. Oktor, “Optimization of baker's yeast wastewater using response surface methodology by electrocoagulation,” Desalination. Vol. 286, pp. 200–209, 2012.
[4]. Y. Zhou, Z. Liang and Y. Wang, “Decolorization and COD removal of secondary yeast wastewater effluents by coagulation using aluminum sulphate,” Desalination. Vol. 225, pp. 301-311, 2008.
[5]. A. Saghir. and S. Hajjar, “Anaerobic treatment for high organic load industrial wastewater by UASB reactor,” Research Journal of Aleppo university .Engineering series. Vol. 58, 2007.
[6]. T. Ciftci. and I.Oztiirk, “Nine years of full-scale anaerobic-aerobic treatment experiences with fermentation industry effluent,” Water Science and Technology. Vol. 32, No.12, pp. 131-139, 1996.
[7]. N. Deveci and G. Çiftçi, “A mathematical model for the anaerobic treatment of Baker's yeast effluents,” Waste Management. Vol. 21, No.1, pp. 99-103, 2001.
[8]. S.K. Khanal, J.C. Huang, ”Effect of high influent sulfate on anaerobic wastewater treatment,” Water Environment Research. Vol. 77, No. 7, pp. 3037-3046, 2005.
[9]. K.V. Lo, A. Chen and P.H Liao, “Anaerobic Treatment of Baker's Yeast Wastewater:II.Sulfate Removal,” Biomass: of British, Vol. 23, No. 1, pp. 25-37 ,1989.
[10]. M. Koplimaa, A. Menert, V. Blonskaja, T. Kurissoo, S. Zub, M. Saareleht, E. Vaarmets and T. Menert, ”Liquid and gas chromatographic studies of the anaerobic degradation of baker’s yeast wastewater,” Procedia Chemistry. Vol. 2, No.1,pp. 120–129, 2010.
[11]. M.E Ersahin, H. Ozgun, R.K. Dereli and I. Ozturk, “Anaerobic Treatment of Industrial Effluents:An Overview of Applications,” Available: https://www.intechopen.com/books/waste-water-treatment-and-reutilization/anaerobic-treatment-of-industrial-effluents-an-overview-of-applications, DOI: 10.5772/16032, 2011.
[12]. E.W. Rice, “Standard Methods for the Examination of Water and Wastewater,” 22nd Edition, American Public Health Association, American Water Works Association and Water Environment Federation, Washington DC, USA, 2014.
[13]. M.M. Ghangrekar, ”Design of an UASB Reactor,“ Available. https://docslide.net/documents/design-of-an-uasb-reactor.html, 2005.
[14]. S. Sung, “Anaerobic Water Treatment Technologies,” Accessed: http://www.wpeiic.ncku.edu.tw/resources/Aeaerobic%20Water%20Treatment.pdf, (2008).
[15]. M.M. Ghangrekar, ”Design of an UASB Reactor,“ https://www.scribd.com/document/86683056/Design-of-an-UASB-Reactor, 2002.
[16]. L.F Burton and G. Tchobanoglous,“Wastewater Engineering-Treatment- Disposal- Reuse,” 3rd Ed, Metcalf and Eddy. Inc ,McGraw- Hill, New York, 1991
The treatment of baker’s yeast wastewater by an up flow anaerobic sludge blanket (UASB) reactor
Year 2018,
Volume: 1 Issue: 2, 39 - 44, 28.03.2018
Abdullah Saghir
,
Salwa Hajjar
Abstract
The objective of the
research is to study the ability of baker's yeast wastewater (BYW) treatment by
a Up Flow - Anaerobic Sludge Blanket (UASB) reactor. The effect of the
temperature of BYW on the efficiency of treatment in a UASB was investigated
and the experiments showed that it is possible to achieve good removal
efficiency of chemical oxygen demand (COD) (10200-16320) mg L-1 when the
temperature of BYW is about (35±2)°C and hydraulic retention time
(HRT) = 24 h. The removal efficiency fit with temperature value of wastewater
in UASB reactor for the following values of temperature of (11±2; 16±2; 26±2; 26±2; 31±2; 35±2) °C. The removal efficiencies of
COD were: (36.6%; 37.9%; 43%; 44.2%; and 48.8%) respectively. The
effect of changing the values of HRT on the efficiency removal at a temperature
(35±2) °C value was investigated. The experiments illustrated that it is
possible to achieve good removal efficiency for high concentrations of COD when
the temperature of the BYW is fixed at (35±2) °C and HRT>=24 h. The
removal efficiency fits with HRTs values. For the following values of HRTs: (18;
24; 30; 36) h, the removal efficiencies of COD were: (32.9%; 48.8%; 48.95%; 51.3%) respectively.
References
- [1]. A. Saghir, “Industrial wastewater treatment in Arabic world,” Arabic scientific publishers, Lebanon, 2017.
[2]. R. Rajakumar, T. Meenambal, P.M. Saravanan, P. Ananthanarayanan, ”Treatment of poultry slaughterhouse wastewater in hybrid upflow anaerobic sludge blanket reactor packed with pleated poly vinyl chloride rings,” Bioresource Technology. Vol. 103 (1), pp. 116–122, 2012.
[3]. E. Gengec, M. Kobya, E. Demirbas, A. Akyol and K. Oktor, “Optimization of baker's yeast wastewater using response surface methodology by electrocoagulation,” Desalination. Vol. 286, pp. 200–209, 2012.
[4]. Y. Zhou, Z. Liang and Y. Wang, “Decolorization and COD removal of secondary yeast wastewater effluents by coagulation using aluminum sulphate,” Desalination. Vol. 225, pp. 301-311, 2008.
[5]. A. Saghir. and S. Hajjar, “Anaerobic treatment for high organic load industrial wastewater by UASB reactor,” Research Journal of Aleppo university .Engineering series. Vol. 58, 2007.
[6]. T. Ciftci. and I.Oztiirk, “Nine years of full-scale anaerobic-aerobic treatment experiences with fermentation industry effluent,” Water Science and Technology. Vol. 32, No.12, pp. 131-139, 1996.
[7]. N. Deveci and G. Çiftçi, “A mathematical model for the anaerobic treatment of Baker's yeast effluents,” Waste Management. Vol. 21, No.1, pp. 99-103, 2001.
[8]. S.K. Khanal, J.C. Huang, ”Effect of high influent sulfate on anaerobic wastewater treatment,” Water Environment Research. Vol. 77, No. 7, pp. 3037-3046, 2005.
[9]. K.V. Lo, A. Chen and P.H Liao, “Anaerobic Treatment of Baker's Yeast Wastewater:II.Sulfate Removal,” Biomass: of British, Vol. 23, No. 1, pp. 25-37 ,1989.
[10]. M. Koplimaa, A. Menert, V. Blonskaja, T. Kurissoo, S. Zub, M. Saareleht, E. Vaarmets and T. Menert, ”Liquid and gas chromatographic studies of the anaerobic degradation of baker’s yeast wastewater,” Procedia Chemistry. Vol. 2, No.1,pp. 120–129, 2010.
[11]. M.E Ersahin, H. Ozgun, R.K. Dereli and I. Ozturk, “Anaerobic Treatment of Industrial Effluents:An Overview of Applications,” Available: https://www.intechopen.com/books/waste-water-treatment-and-reutilization/anaerobic-treatment-of-industrial-effluents-an-overview-of-applications, DOI: 10.5772/16032, 2011.
[12]. E.W. Rice, “Standard Methods for the Examination of Water and Wastewater,” 22nd Edition, American Public Health Association, American Water Works Association and Water Environment Federation, Washington DC, USA, 2014.
[13]. M.M. Ghangrekar, ”Design of an UASB Reactor,“ Available. https://docslide.net/documents/design-of-an-uasb-reactor.html, 2005.
[14]. S. Sung, “Anaerobic Water Treatment Technologies,” Accessed: http://www.wpeiic.ncku.edu.tw/resources/Aeaerobic%20Water%20Treatment.pdf, (2008).
[15]. M.M. Ghangrekar, ”Design of an UASB Reactor,“ https://www.scribd.com/document/86683056/Design-of-an-UASB-Reactor, 2002.
[16]. L.F Burton and G. Tchobanoglous,“Wastewater Engineering-Treatment- Disposal- Reuse,” 3rd Ed, Metcalf and Eddy. Inc ,McGraw- Hill, New York, 1991