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      Treatment of Poultry Slaughterhouse Wastewater (PSW) Using a Pretreatment Stage, an Expanded Granular Sludge Bed Reactor (EGSB), and a Membrane Bioreactor (MBR)

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          Abstract

          This study presents the biological treatment of poultry slaughterhouse wastewater (PSW) using a combination of a biological pretreatment stage, an expanded granular sludge bed reactor (EGSB), and a membrane bioreactor (MBR) to treat PSW. This PSW treatment was geared toward reducing the concentration of contaminants present in the PSW to meet the City of Cape Town (CoCT) discharge standards and evaluate an alternative means of treating medium- to high-strength wastewater at low cost. The EGSB used in this study was operated under mesophilic conditions and at an organic loading rate (OLR) of 69 to 456 mg COD/L·h. The pretreatment stage of this laboratory-scale (lab-scale) plant played an important role in the pretreatment of the PSW, with removal percentages varying between 20% and 50% for total suspended solids (TSS), 20% and 70% for chemical oxygen demand (COD), and 50% and 83% for fats, oil, and grease (FOG). The EGSB further reduced the concentration of these contaminants to between 25% and 90% for TSS, 20% and 80% for COD, and 20% and >95% for FOG. The last stage of this process, i.e., the membrane bioreactor (MBR), contributed to a further decrease in the concentration of these contaminants with a peak removal performance of >95% for TSS and COD and 80% for the FOG. Overall, the system (pretreatment–EGSB–MBR) exceeded 97% for TSS and COD removal and 97.5% for FOG removal. These results culminated in a product (treated wastewater) meeting the discharge standards.

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          Standard Methods for the Examination of Water and Wastewater

          "The Twenty-First Edition has continued the trend to revise methods as issues are identified and contains further refined quality assurance requirements in a number of Parts [sic] and new data on precision and bias. New methods have been added in Parts 2000, 4000, 5000, 6000, 7000, 8000, and 9000, and numerous methods have been revised. Details of these changes appear on the reverse of the title page for each part."--Pref. p. iv.
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            Anaerobic treatment of domestic wastewater in a membrane-coupled expended granular sludge bed (EGSB) reactor under moderate to low temperature

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              Anaerobic treatment of wastewater with high organic content using a stirred tank reactor coupled with a membrane filtration unit.

              Using a cross-flow membrane bioreactor, high anaerobic conversion rates of three different types of wastewater with varying organic content were achieved. Loading rates obtained were as follows: 20 g CODL(-1) x d(-1) for artificial wastewater, approximately 8 g CODL(-1) x d(-1) from vegetable processing industry (sauerkraut brine) and 6-8 g CODL(-1) x d(-1) for wastewater from an animal slaughterhouse. At stable conditions, COD-removal rates in all three wastewaters were higher than 90%. Methane yields from the treatment of artificial wastewater, sauerkraut brine, and animal slaughterhouse wastewater were in the range of 0.17-0.30, 0.20-0.34, and 0.12-0.32 L(n) x g(-1) COD(-1) fed, respectively. The complete retention of biomass and suspended solids is a unique feature of this treatment process, which combines a high loading capacity and at the same time, high COD removal rates even for complex wastewater containing high concentrations of particulate matter.
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                Author and article information

                Contributors
                Role: Academic Editor
                Journal
                Membranes (Basel)
                Membranes (Basel)
                membranes
                Membranes
                MDPI
                2077-0375
                08 May 2021
                May 2021
                : 11
                : 5
                : 345
                Affiliations
                [1 ]Bioresource Engineering Research Group (BioERG), Department of Chemical Engineering, Cape Peninsula University of Technology, P.O. Box 1906, Bellville 7535, South Africa; oneil_meyo@ 123456hotmail.com (H.B.M.); mahomet.njoya@ 123456gmail.com (M.N.)
                [2 ]Academic Support Programme for Engineering in Cape Town (ASPECT) & Water Research Group, Department of Civil Engineering, University of Cape Town, Private Bag X3, Rondebosch 7701, South Africa
                [3 ]Center of Excellence in Carbon-Based Fuels, School of Chemical and Minerals Engineering, North-West University, Private Bag X1290, Potchefstroom 2520, South Africa; karabo.ntwampe@ 123456uct.ac.za
                [4 ]Malutsa (Pty) Ltd., c/o Oude Pont and Meent Street (Malutsa House), Wellington Industrial Park, Wellington 7655, South Africa; ephraimk@ 123456malutsa.co.za
                Author notes
                [* ]Correspondence: moses.basitere@ 123456uct.ac.za ; Tel.: +27-73-870-6901
                Author information
                https://orcid.org/0000-0003-3674-0724
                Article
                membranes-11-00345
                10.3390/membranes11050345
                8151326
                8ad6bba3-6dcf-434f-9c43-5c7c5bfccd7b
                © 2021 by the authors.

                Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license ( https://creativecommons.org/licenses/by/4.0/).

                History
                : 26 March 2021
                : 27 April 2021
                Categories
                Article

                chemical oxygen demand (cod),expanded granular sludge bed reactor (egsb),fats, oil, and grease (fog),membrane bioreactor (mbr),poultry slaughterhouse wastewater (psw),total suspended solids (tss)

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