Please use this identifier to cite or link to this item: http://hdl.handle.net/20.500.11889/7845
Title: A Feasible scheme for slaughterhouse wastewater treatment using an anaerobic digestion batch reactor followed by an aerobic treatment stage
Other Titles: Desalination and Water Treatment
Authors: Nassar, Abdelmajid 
Al-Najjar, Husam 
Abukmeil, Reem 
Al-Sa`ed, Rashed 
Keywords: Slaughterhouse wastewater;Wastewater characterization;Anaerobic–aerobic treatment;Industrial wastewater treatment;Sewage - Purification - Sequencing batch reactor process;Sewage - Purification;Water - Purification - Biological treatment;Slaughterhouses - Waste disposal;Water reuse
Issue Date: Nov-2022
Publisher: Desalination Publications
Source: Nassar, A., Al-Najjar, H., Abukmeil, R., Al-Sa`ed, R. 2022. A Feasible scheme for slaughterhouse wastewater treatment using an anaerobic digestion batch reactor followed by an aerobic treatment stage. Desalination and Water Treatment, 275, 260-267. DOI: https://doi.org/10.5004/dwt.2022.28966
Series/Report no.: 275;
Abstract: The sustainable management of slaughterhouse wastewater calls for feasible treatment technologies to protect the environment and public wastewater treatment facilities. The technology of an up-flow anaerobic sludge blanket provides an adequate procedural condition for the reduction of carbonaceous matter from the high organic wastewater resulting from the slaughterhouses. The scope of this research included a rapid review of current treatment technologies for slaughterhouse wastewaters and an investigation of the treatment efficiency of an aerobic stage after a pre-anaerobic treatment in a batch system. A batch reactor system of 1 m3 volume with a mixer was developed. The anaerobic stage of the batch reactor was initiated using 400 L of fresh slaughterhouse wastewater mixed with 40 L of primary sludge. Three samples from the anaerobic batch reactor were collected at a 10 d interval and then five samples were collected from the reactor after being under the aerobic condition at a 4 d interval. The removal efficiency of biochemical oxygen demand, chemical oxygen demand, total Kjeldahl nitrogen, and PO4 was 25%, 62%, 42%, and 9% in 30 d, respectively. After the start of the aeration system, the removal efficiency was improved up to 94%, 69%, and 93%, respectively, except for PO4 which showed high variations within the sampling periods.
Description: Presented at the first Palestinian-Dutch Conference on Water, Sanitation, and Hygiene (WASH), and Climate Smart Agriculture (CSA), 5–6 September 2022, Nablus, Palestinian Authority.
URI: http://hdl.handle.net/20.500.11889/7845
DOI: 10.5004/dwt.2022.28966
Appears in Collections:6. BZU Dataset Collection

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