Araştırma Makalesi
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Yıl 2018, Cilt: 1 Sayı: 2, 39 - 44, 28.03.2018

Öz

Kaynakça

  • [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

Yıl 2018, Cilt: 1 Sayı: 2, 39 - 44, 28.03.2018

Öz

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.

Kaynakça

  • [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
Toplam 1 adet kaynakça vardır.

Ayrıntılar

Birincil Dil İngilizce
Konular Çevre Mühendisliği
Bölüm Research Articles
Yazarlar

Abdullah Saghir

Salwa Hajjar Bu kişi benim

Yayımlanma Tarihi 28 Mart 2018
Gönderilme Tarihi 14 Şubat 2018
Kabul Tarihi 7 Mart 2018
Yayımlandığı Sayı Yıl 2018 Cilt: 1 Sayı: 2

Kaynak Göster

APA Saghir, A., & Hajjar, S. (2018). The treatment of baker’s yeast wastewater by an up flow anaerobic sludge blanket (UASB) reactor. Environmental Research and Technology, 1(2), 39-44.
AMA Saghir A, Hajjar S. The treatment of baker’s yeast wastewater by an up flow anaerobic sludge blanket (UASB) reactor. ERT. Nisan 2018;1(2):39-44.
Chicago Saghir, Abdullah, ve Salwa Hajjar. “The Treatment of baker’s Yeast Wastewater by an up Flow Anaerobic Sludge Blanket (UASB) Reactor”. Environmental Research and Technology 1, sy. 2 (Nisan 2018): 39-44.
EndNote Saghir A, Hajjar S (01 Nisan 2018) The treatment of baker’s yeast wastewater by an up flow anaerobic sludge blanket (UASB) reactor. Environmental Research and Technology 1 2 39–44.
IEEE A. Saghir ve S. Hajjar, “The treatment of baker’s yeast wastewater by an up flow anaerobic sludge blanket (UASB) reactor”, ERT, c. 1, sy. 2, ss. 39–44, 2018.
ISNAD Saghir, Abdullah - Hajjar, Salwa. “The Treatment of baker’s Yeast Wastewater by an up Flow Anaerobic Sludge Blanket (UASB) Reactor”. Environmental Research and Technology 1/2 (Nisan 2018), 39-44.
JAMA Saghir A, Hajjar S. The treatment of baker’s yeast wastewater by an up flow anaerobic sludge blanket (UASB) reactor. ERT. 2018;1:39–44.
MLA Saghir, Abdullah ve Salwa Hajjar. “The Treatment of baker’s Yeast Wastewater by an up Flow Anaerobic Sludge Blanket (UASB) Reactor”. Environmental Research and Technology, c. 1, sy. 2, 2018, ss. 39-44.
Vancouver Saghir A, Hajjar S. The treatment of baker’s yeast wastewater by an up flow anaerobic sludge blanket (UASB) reactor. ERT. 2018;1(2):39-44.