BibTex RIS Kaynak Göster

Optimization of Two-Stage and Single-Stage Anaerobic Reactors Treating Cheese Whey

Yıl 2016, Cilt: 19 Sayı: 1, 25 - 36, 10.05.2016

Emre Yazar Kevser Cırık Şebnem Özdemır Dilek Akman Yakup Cuci Özer Çınar

https://doi.org/10.17780/ksujes.18309
Cited By: 1

Öz

The objective of this research is to compare and evaluate the methane production from cheese whey in single-stage and two-stage anaerobic treatment processes. Single stage-reactor was operated in a pilot-scale batch reactor while two-stage reactor was operated in batch-dilution and semi-continuously. Reactors were loaded with cheese whey with an chemical oxygen demand (COD) of about 38.61 g/L. Single stage system was operated at 35°C with a hydraulic retention time (HRT) of 15, 10, 7 and 4 days; respectively. The maximum methane production in the single-stage reactor was obtained at 3.86 gCOD/L.d organic loading rate (OLR) with 10 days HRT being about 0.39 L CH4 /Lreactor/g CODdeg.d; respectively. The results indicated that the use of a two-stage process for anaerobic treatment of cheese whey resulted in 4 fold higher methane yield compared to single-stage reactor system allowing better control of the acidogenic and methanogenic phases.

Anahtar Kelimeler

Anaerobic treatment; Biogas; Cheese whey; Hydraulic retention time; Methane production; Phase separation

Kaynakça

  • [1]. Wit JN de (2001). Lecturer’s Handbook on whey and whey products. European Whey Products Association (EWPA) 14, Rue Montoyer1000 Brussels, Belgium.
  • [2]. Farizoglu B, Keskinler B, Yildiz E, Nuhoglu A (2004). Cheese whey treatment performance of an aerobic jet loop membrane bioreactor. Process Biochemistry, 39:2283–2291.
  • [3]. Siso GMI (1996). The biotechnological utilization of cheese whey: A review. Bioresour Technol, 57:1–11.
  • [4]. Panesar PS, Kennedy JF, Gandhi DN. Bunko K (2007). Bioutilisation of whey for lactic acid production. Food Chemistry, 105: 1–14.
  • [5]. Prazeres AR, Carvalho F, Rivas J (2012). Cheese whey management: A review. Journal of Environmental Management, 110:48-68.
  • [6]. Atamer Z, Samtlebe M, Neve H, Heller KJ, Hinrichs J (2013). Review: Elimination of bacteriophages in whey and whey products. Frontiers in Microbiology, 4:1-9.
  • [7]. Smithers GW (2008). Whey and whey proteins-from ‘gutter-to-gold’. Int Dairy J, 18:695–704.
  • [8]. Göblös Sz, Portörő P, Bordás D, Kálmán M, Kiss I (2008). Comparison of the effectivities of two-phase and single-phase anaerobic sequencing batch reactors during dairy wastewater treatment. Renew Energy, 33:960-965.
  • [9]. Wang Z, Banks CJ (2003). Evaluation of a two stage anaerobic digester for the treatment of mixed abattoir wastes. Process Biochem, 38:1267-1273.
  • [10]. Demirer G, Chen S (2005). Two-phase anaerobic digestion of dairy manure. Process Biochem., 40(11):3542-3549.
  • [11]. Ke S, Shi Z (2005). Applications of twophase anaerobic degradation in industrial wastewater treatment. Int J Environ Pollut, 23:65–80.
  • [12]. Saddoud A, Hassari I, Sayadi S (2007). Anaerobic membrane reactor with phase separation for the treatment of cheese whey. Bioresour Technol, 98:2102–2108.
  • [13]. Cui F, Lee S, Kim M (2011). Removal of organics and nutrients from food wastewater using combined thermophilic two-phase anaerobic digestion and shortcut biological nitrogen removal. Water Res, 45:5279 -5286.
  • [14]. Guerrero L, Montalvo S, Coronado E, Chamy R, Poirrier P, Crutchik D, Sánchez E, De La Rubia MA, Borja R (2009). Performance evaluation of a twophase anaerobic digestion process of synthetic domestic wastewater at ambient temperature. J Environ. Sci Health A Tox Hazard Subst Environ Eng, 44(7):673- 681.
  • [15]. APHA, 2005. Standard Methods for the Examination of Water and Wastewater. American Public Health Association/American Water Works Association/Water Environment Federation, Washington D.C.
  • [16]. McCarty PL (1981). One hundred years of anaerobic digestion, anaerobic digestion, Amsterdam: Elsevier Biochemical Press BV pp: 3–22.
  • [17]. Wen Z, Liao W, Chen S (2004). Hydrolysis of animal manure lignocellulosics for reducing sugar production. Biores Technol, 91(1):31–9.
  • [18]. Mechichi T, Sayadi S (2005). Evaluating process imbalance of anaerobic digestion of olive mill wastewaters. Process Biochem, 40:139–145.
  • [19]. Ueno Y, Sasaki D, Fukui H, Haruta S, Ishii M, Igarashi Y (2006). Changes in bacterial community during fermentative hydrogen and acid production from organic waste by thermophilic anaerobic microflora. J Appl Microbiol, 101:331- 343. KSU Mühendislik Bilimleri Dergisi, 19(1),
  • [20]. Wang L, Zhou Q, Li FT (2006). Avoiding propionic acid accumulation in the anaerobic process for biohydrogen production. Biomass and Bioenergy, 30:177–182.
  • [21]. Zoetemeyer RJ, van den Heuvel JC, Cohen A (1982). pH influence on acidogenic dissimilation of glucose in an anaerobic digester. Water Res, 16:303- 311.
  • [22]. Sans C, Mata-Alavarez J (1995). Acidogenic fermentation of organic urban wastes in a plug-flow reactor under thermophilic conditions. Bioresour Technol, 54:105-110.
  • [23]. Kim JQ, Somiya I, Shin EB, Bae W, Kim SK, Kim RH (2002). Application of membrane-coupled anaerobic volatile fatty acid fermentor for dissolved organics recovery from coagulated raw sludge. Water Sci Technol, 45(12):167- 174.
  • [24]. Yu HQ, Fang HP (2003). Acidogenesis of gelatin-rich wastewater in an upflow anaerobic reactor: Influence of pH and temperature. Water Res, 37:55-66.
  • [25]. Wang Y, Zhang Y, Wang J, Meng L (2009). Effects of volatile fatty acid concentrations on methane yield and methanogenic bacteria. Biomass and Bioenergy, 33:848-853.
  • [26]. Sentürk E, İnce M, Onkal Engin G (2010). Treatment efficiency and VFA composition of a thermophilic anaerobic contact reactor treating food industry wastewater. J Hazard Mater, 176:843– 848.
  • [27]. Show KY, Zhang ZP, Tay JT, Liang DT, Lee DJ, Jiang WJ (2007). Production of hydrogen in a granular sludgebased anaerobic continuous stirred tank reactor. Int J Hydrogen Energy, 32 (18):4744– 4753.
  • [28]. de Bok FAM, Plugge CM, Stams AJM (2004). Interspecies electron transfer in methanogenic propionate degrading consortia. Water Res, 38:1368–1375.
  • [29]. Ratusznei SM, Rodrigues JAD, Zaiat M (2003). Operating feasibility of anaerobic whey treatment in a stirred sequencing batch reactor containing immobilized biomass. Water Sci Technol, 48:179–186.
  • [30]. Damasceno LHS, Rodrigues JAD, Ratusznei SM, Zaiat M, Foresti E (2007). Effects of feeding time and organic loading in an anaerobic sequencing batch biofilm reactor (ASBBR) treating diluted whey. J Environ Manag, 85:927–935.
  • [31]. Yang K, Yu Y, Hwang S (2003). Selective optimization in thermophilic acidogenesis of cheese-whey wastewater to acetic and butyric acids: partial acidification and methanation. Water Res, 37:2467–2477.

Peyniraltı Suyu Arıtımında Tek ve Çift Aşamalı Anaerobik Reaktörün Optimizasyonu

Yıl 2016, Cilt: 19 Sayı: 1, 25 - 36, 10.05.2016

Emre Yazar Kevser Cırık Şebnem Özdemır Dilek Akman Yakup Cuci Özer Çınar

https://doi.org/10.17780/ksujes.18309
Cited By: 1

Öz

Bu çalışmanın amacı tek ve çift aşamalı anaerobik arıtım proseslerinde peyniraltı suyunda metan üretimini araştırmak ve karşılaştırmaktır. Tek aşamalı reaktör pilot ölçekli kesikli reaktörde işletilirken, çift aşamalı reaktör yarı sürekli ve kesikli olarak işletilmiştir. Reaktör, 38,61g/L kimyasal oksijen ihtiyacına (KOİ) sahip peyniraltı suyu ile yüklenmiştir. Tek aşamalı sistem 15, 10, 7 ve 4 günlük HRT’ler ile 350C’de işletilmiştir ve maksimum metan üretimi HRT’nin 10 gün olduğu işletme koşulunda 3,86 gKOİ/L.gün seviyelerine ulaşmıştır (0,39 L CH4/Lreaktör/g KOİdeg.gün). Çalışma sonuçları peyniraltı suyunun anaerobik arıtımında asidojenik ve metanojenik fazların daha iyi kontrol altına alınabildiği iki aşamalı prosesin tek aşamalı prosese göre 4 kat daha fazla metan üretim verimi elde edilebildiğini göstermiştir

Anahtar Kelimeler

Anaerobik arıtım Biyogaz Peyniraltı suyu Hidrolik bekleme süresi Metan üretimi Faz ayrımı

Kaynakça

  • [1]. Wit JN de (2001). Lecturer’s Handbook on whey and whey products. European Whey Products Association (EWPA) 14, Rue Montoyer1000 Brussels, Belgium.
  • [2]. Farizoglu B, Keskinler B, Yildiz E, Nuhoglu A (2004). Cheese whey treatment performance of an aerobic jet loop membrane bioreactor. Process Biochemistry, 39:2283–2291.
  • [3]. Siso GMI (1996). The biotechnological utilization of cheese whey: A review. Bioresour Technol, 57:1–11.
  • [4]. Panesar PS, Kennedy JF, Gandhi DN. Bunko K (2007). Bioutilisation of whey for lactic acid production. Food Chemistry, 105: 1–14.
  • [5]. Prazeres AR, Carvalho F, Rivas J (2012). Cheese whey management: A review. Journal of Environmental Management, 110:48-68.
  • [6]. Atamer Z, Samtlebe M, Neve H, Heller KJ, Hinrichs J (2013). Review: Elimination of bacteriophages in whey and whey products. Frontiers in Microbiology, 4:1-9.
  • [7]. Smithers GW (2008). Whey and whey proteins-from ‘gutter-to-gold’. Int Dairy J, 18:695–704.
  • [8]. Göblös Sz, Portörő P, Bordás D, Kálmán M, Kiss I (2008). Comparison of the effectivities of two-phase and single-phase anaerobic sequencing batch reactors during dairy wastewater treatment. Renew Energy, 33:960-965.
  • [9]. Wang Z, Banks CJ (2003). Evaluation of a two stage anaerobic digester for the treatment of mixed abattoir wastes. Process Biochem, 38:1267-1273.
  • [10]. Demirer G, Chen S (2005). Two-phase anaerobic digestion of dairy manure. Process Biochem., 40(11):3542-3549.
  • [11]. Ke S, Shi Z (2005). Applications of twophase anaerobic degradation in industrial wastewater treatment. Int J Environ Pollut, 23:65–80.
  • [12]. Saddoud A, Hassari I, Sayadi S (2007). Anaerobic membrane reactor with phase separation for the treatment of cheese whey. Bioresour Technol, 98:2102–2108.
  • [13]. Cui F, Lee S, Kim M (2011). Removal of organics and nutrients from food wastewater using combined thermophilic two-phase anaerobic digestion and shortcut biological nitrogen removal. Water Res, 45:5279 -5286.
  • [14]. Guerrero L, Montalvo S, Coronado E, Chamy R, Poirrier P, Crutchik D, Sánchez E, De La Rubia MA, Borja R (2009). Performance evaluation of a twophase anaerobic digestion process of synthetic domestic wastewater at ambient temperature. J Environ. Sci Health A Tox Hazard Subst Environ Eng, 44(7):673- 681.
  • [15]. APHA, 2005. Standard Methods for the Examination of Water and Wastewater. American Public Health Association/American Water Works Association/Water Environment Federation, Washington D.C.
  • [16]. McCarty PL (1981). One hundred years of anaerobic digestion, anaerobic digestion, Amsterdam: Elsevier Biochemical Press BV pp: 3–22.
  • [17]. Wen Z, Liao W, Chen S (2004). Hydrolysis of animal manure lignocellulosics for reducing sugar production. Biores Technol, 91(1):31–9.
  • [18]. Mechichi T, Sayadi S (2005). Evaluating process imbalance of anaerobic digestion of olive mill wastewaters. Process Biochem, 40:139–145.
  • [19]. Ueno Y, Sasaki D, Fukui H, Haruta S, Ishii M, Igarashi Y (2006). Changes in bacterial community during fermentative hydrogen and acid production from organic waste by thermophilic anaerobic microflora. J Appl Microbiol, 101:331- 343. KSU Mühendislik Bilimleri Dergisi, 19(1),
  • [20]. Wang L, Zhou Q, Li FT (2006). Avoiding propionic acid accumulation in the anaerobic process for biohydrogen production. Biomass and Bioenergy, 30:177–182.
  • [21]. Zoetemeyer RJ, van den Heuvel JC, Cohen A (1982). pH influence on acidogenic dissimilation of glucose in an anaerobic digester. Water Res, 16:303- 311.
  • [22]. Sans C, Mata-Alavarez J (1995). Acidogenic fermentation of organic urban wastes in a plug-flow reactor under thermophilic conditions. Bioresour Technol, 54:105-110.
  • [23]. Kim JQ, Somiya I, Shin EB, Bae W, Kim SK, Kim RH (2002). Application of membrane-coupled anaerobic volatile fatty acid fermentor for dissolved organics recovery from coagulated raw sludge. Water Sci Technol, 45(12):167- 174.
  • [24]. Yu HQ, Fang HP (2003). Acidogenesis of gelatin-rich wastewater in an upflow anaerobic reactor: Influence of pH and temperature. Water Res, 37:55-66.
  • [25]. Wang Y, Zhang Y, Wang J, Meng L (2009). Effects of volatile fatty acid concentrations on methane yield and methanogenic bacteria. Biomass and Bioenergy, 33:848-853.
  • [26]. Sentürk E, İnce M, Onkal Engin G (2010). Treatment efficiency and VFA composition of a thermophilic anaerobic contact reactor treating food industry wastewater. J Hazard Mater, 176:843– 848.
  • [27]. Show KY, Zhang ZP, Tay JT, Liang DT, Lee DJ, Jiang WJ (2007). Production of hydrogen in a granular sludgebased anaerobic continuous stirred tank reactor. Int J Hydrogen Energy, 32 (18):4744– 4753.
  • [28]. de Bok FAM, Plugge CM, Stams AJM (2004). Interspecies electron transfer in methanogenic propionate degrading consortia. Water Res, 38:1368–1375.
  • [29]. Ratusznei SM, Rodrigues JAD, Zaiat M (2003). Operating feasibility of anaerobic whey treatment in a stirred sequencing batch reactor containing immobilized biomass. Water Sci Technol, 48:179–186.
  • [30]. Damasceno LHS, Rodrigues JAD, Ratusznei SM, Zaiat M, Foresti E (2007). Effects of feeding time and organic loading in an anaerobic sequencing batch biofilm reactor (ASBBR) treating diluted whey. J Environ Manag, 85:927–935.
  • [31]. Yang K, Yu Y, Hwang S (2003). Selective optimization in thermophilic acidogenesis of cheese-whey wastewater to acetic and butyric acids: partial acidification and methanation. Water Res, 37:2467–2477.
Toplam 31 adet kaynakça vardır.

Ayrıntılar

Birincil Dil İngilizce
Bölüm Araştırma Makalesi
Yazarlar

Emre Yazar

Kevser Cırık

Şebnem Özdemır

Dilek Akman

Yakup Cuci

Özer Çınar

Yayımlanma Tarihi 10 Mayıs 2016
Gönderilme Tarihi 21 Mart 2016
Yayımlandığı Sayı Yıl 2016Cilt: 19 Sayı: 1

Kaynak Göster

APA Yazar, E., Cırık, K., Özdemır, Ş., Akman, D., vd. (2016). Optimization of Two-Stage and Single-Stage Anaerobic Reactors Treating Cheese Whey. Kahramanmaraş Sütçü İmam Üniversitesi Mühendislik Bilimleri Dergisi, 19(1), 25-36. https://doi.org/10.17780/ksujes.18309

Cited By

Two-Stage anaerobic digestion in agroindustrial waste treatment: A review
Journal of Environmental Management
Paulo André Cremonez
https://doi.org/10.1016/j.jenvman.2020.111854