MOSES BASITERE 13th IWA Specialized conference on small water and wastewater Systems (SWWS)

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1 TREATMENT OF POULTRY SLAUGHTERHOUSE WASTEWATER USING A STATIC GRANULAR BED REACTOR COUPLED WITH UF MEMBRANES MOSES BASITERE 13th IWA Specialized conference on small water and wastewater Systems (SWWS)

2 Presentation outline Background The big picture Water stress in South Africa Core motives/objectives of the study Literature Review Results and Discussion Conclusion and Recommendations

3 Background Poultry slaughterhouse consume large quantities of fresh water to ensure production of hygienically safe poultry products. This result in generation of high strength wastewater which contain high levels of COD, BOD, TSS, FOG, and nutrients. The wastewater generated doesn t meet SA government s industrial wastewater discharge standards. If this wastewater is untreated, it pose severe risks to municipal sewer systems and the environment.

4 The big picture

5 Water stress The country must conserve its water resources and also treat its degraded water resource

6 Core motives/ objectives Meet discharge standards Lower discharge cost Zero liquid Effluent discharge Water re-use ISO

7 Literature review Poultry slaughterhouse wastewater characteristics Table 1: Typical poultry slaughterhouse wastewater characteristics according to literature Treatment method COD (mg/l) BOD (mg/l) TSS (mg/l) FOG (mg/l) TP (mg/l) TN (mg/l) References EGSB Basitere et al., 2016 Membrane filtration Abboah-Afari, 2011 Hybrid-UASB Rajakumar et al., 2011 UF membrane Yordanov, 2010 SGBR & SASBR Debik & Coskun, 2009 DAF & UASB De Nardi et al., 2008 DAF & UASB Del Nery et al., 2007 UASB , ,150 Chavez et al., 2005

8 Static Granular Sludge Bed Reactor &UF membranes BIOGAS BIOGAS METER METHANE FEED BACKWASH VALVE UF MEMBRANE 1 UF MEMBRANE 2 HOT WATER CIRCULATION OVERFLOW LINE SGBR FEED TANK BACKWASH VALVE GRANULES PERMEATE FEED PERMEATE BACKWASH VALVE THERMOSTATIC WATER BATH PEA GRAVEL SIEVE HOT WATER CIRCULATION PRODUCT PERISTALTIC PUMP SGBR PRODUCT TANK UF MEMBRANE 1 PERMEATE TANK UF MEMBRANE 2 PERMEATE TANK

9 Static Granular Sludge Bed Reactor operating conditions Operating conditions (HRT and OLR) for the SGBR system over a period of 64 days Dilution (%) 50 Operating Time (days) 1-19 Flow rate (L/h) HRT (hrs) None None OLR (g COD/Lday)

10 Static Granular Sludge Bed Reactor Average SGBR Feed

11 COD (mg/l.d) COD Removal (%) Results and discussions SGBR COD removal HRT: 55 HRT: 55 HRT: 55 OLR: 0.56 OLR: 0.67 OLR: 1.73 HRT: 40 OLR: % dilution 67% dilution Operating Time (days) SGBR Feed COD SGBR Product COD CCT By-Law Discharge Limit COD Removal Overall COD Removal = 93 % 0

12 TSS (mg/l) TSS Removal (%) Results and discussions SGBR TSS Removal 5000 HRT: 55 HRT: 55 HRT: 55 OLR: 0.56 OLR: 0.67 OLR: 1.73 HRT: 40 OLR: % dilution 67% dilution No dilution No dilution Operating Time (days) SGBR Feed TSS SGBR Product TSS TSS Removal Overall TSS Removal = 95%

13 ph VFA/Alkalinity Ratio Results and discussions VFA/ALKALINITY RATIO 8 0,16 7 0,14 6 0,12 5 0,10 4 0,08 3 0,06 2 0,04 1 0,02 0 0, Operating Time (days) SGBR product ph VFA/Alkalinity Ratio VFA/ALK Ratio = 0.01 to 0.14

14 Results and discussion U-F membranes Parameter Units Average SGBR Product Averaged UF Permeate mg/l Average Retention (%) COD mg/l TSS mg/l FOG

15 Results and discussion Overall perfomance SGBR TO UF Parameter Units Averaged SGBR Feed Averaged UF Permeate Overall % Removal COD mg/l TSS FOG mg/l mg/l

16 SGBR FEED SGBR product and UF

17 Conclusion and recomendations The bench-scale SGBR anaerobic digester coupled with UF membranes was successfully employed for treating poultry slaughterhouse wastewater under mesophilic conditions and different organic loading rates. The average COD, TSS and FOG removal efficiencies for the SGBR system was greater 90% over a period of 64 days. The UF membranes used as a post-treatment for the SGBR product showed an average COD, TSS and FOG removal of 63%, 88% and 29%, respectively The overall COD, TSS and FOG removal of the coupled SGBR and UF membranes was greater than 90 %.

18 THANK - YOU

19

20 City of Cape Town By-Law (2013) and SANS 241-1: 2011 parameter discharge standards [2] DWA 2010 SANS241 WCape Mangaug Parameter Units General limit Operational limits Not to exceed operation limits Temperature at point of Entry o C Conductivity ms/m < ph at COD mg/l SS mg/l TDS at C mg/l < ) Total sulphates (SO 4 mg/l < O&G mg/l TP mg/l Faecal coliforms(per 100ml) 1000 Turbidity NTU <1.0 Amonia as Nitrogen mg/l <1.0 DOC mg/l <10 Nitrates mg/l 15

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