YYÜ GCRIS Basic veritabanının içerik oluşturulması ve kurulumu Research Ecosystems (https://www.researchecosystems.com) tarafından devam etmektedir. Bu süreçte gördüğünüz verilerde eksikler olabilir.
 

Treatment of Slaughterhouse Wastewater With the Electrochemical Oxidation Process: Role of Operating Parameters on Treatment Efficiency and Energy Consumption

dc.authorid Yilmaz, Alper Erdem/0000-0002-0666-7653
dc.authorscopusid 57209016651
dc.authorscopusid 42762577800
dc.authorwosid Yılmaz, Alper/Aaw-3750-2021
dc.authorwosid Ozturk, Dilara/Aad-7387-2019
dc.contributor.author Ozturk, Dilara
dc.contributor.author Yilmaz, Alper Erdem
dc.date.accessioned 2025-05-10T17:33:38Z
dc.date.available 2025-05-10T17:33:38Z
dc.date.issued 2019
dc.department T.C. Van Yüzüncü Yıl Üniversitesi en_US
dc.department-temp [Ozturk, Dilara] Van Yuzuncu Yil Univ, Dept Environm Engn, Fac Engn, Van, Turkey; [Yilmaz, Alper Erdem] Ataturk Univ, Fac Engn, Dept Environm Engn, Erzurum, Turkey en_US
dc.description Yilmaz, Alper Erdem/0000-0002-0666-7653 en_US
dc.description.abstract In this study, investigation of the applicability and efficiency of electrochemical oxidation (EO) processes for slaughterhouse wastewater was targeted by evaluating the treatment efficiency and energy consumption values together. The effect of operating parameters such as type of supporting electrolyte (SE) (Na2SO4, NaNO3 and NaCl), concentration of SE (0.01-0.1 M), initial wastewater pH (3-9), current density (CD) (4.73-14.20 mA/cm(2)) and dilution rate of wastewater (1/1-1/4) on removal of chemical oxygen demand (COD), total organic carbon (TOC), total nitrogen (TN), total suspended solids (TSS) and color were investigated. The most effective electrolyte type was observed as NaCl. With the use of 0.025 M NaCl and 25 degrees C reaction temperature, at fixed 4.73 mA/cm 2 CD and pH of 7.03 for 4 h reaction time, the optimum conditions for both energy consumption and removal efficiency for treatment of SWW were obtained. At optimum conditions, TSS, TOC, COD, TN and color removal efficiencies were found as; 99.5%, 88.0%, 92.2%, 93.5% and 99.9%, respectively, and the energy consumption under these conditions were 153.57 kWh/m(3) and 14.12 kWh/kg COD. The energy cost was calculated as 1.69 $/kg COD. Also, results distinctly show that almost full mineralization of organics is obtained after 4 h treatment. Unluckily, taking into account the large volumes of effluent produced per slaughtering cycle, the need for long treatment times is impractical, yet if the reactor is developed to include hydrodynamic conditions or combined with another treatment process which is shorter than the EO treatment time a novel setup may be possible. en_US
dc.description.woscitationindex Science Citation Index Expanded
dc.identifier.doi 10.1016/j.jwpe.2019.100834
dc.identifier.issn 2214-7144
dc.identifier.scopus 2-s2.0-85064408679
dc.identifier.scopusquality Q1
dc.identifier.uri https://doi.org/10.1016/j.jwpe.2019.100834
dc.identifier.uri https://hdl.handle.net/20.500.14720/13560
dc.identifier.volume 31 en_US
dc.identifier.wos WOS:000485817000035
dc.identifier.wosquality Q1
dc.language.iso en en_US
dc.publisher Elsevier en_US
dc.relation.publicationcategory Makale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı en_US
dc.rights info:eu-repo/semantics/closedAccess en_US
dc.subject Electrochemical Oxidation en_US
dc.subject Slaughterhouse Wastewater en_US
dc.subject Energy Consumption en_US
dc.title Treatment of Slaughterhouse Wastewater With the Electrochemical Oxidation Process: Role of Operating Parameters on Treatment Efficiency and Energy Consumption en_US
dc.type Article en_US

Files