Počet záznamů: 1  

Implementation of electrocoagulation for reduction of Zn in an outlet stream from waste incineration plant

  1. 1.
    SYSNO ASEP0570849
    Druh ASEPJ - Článek v odborném periodiku
    Zařazení RIVJ - Článek v odborném periodiku
    Poddruh JČlánek ve WOS
    NázevImplementation of electrocoagulation for reduction of Zn in an outlet stream from waste incineration plant
    Tvůrce(i) Krystyník, Pavel (UH-J) RID, ORCID, SAI
    Klusoň, Petr (UCHP-M) RID, ORCID, SAI
    Mašín, P. (CZ)
    Šyc, Michal (UCHP-M) RID, SAI, ORCID
    Jadrný, J. (CZ)
    Krušinová, Zuzana (UH-J) ORCID, SAI, RID
    Číslo článku109368
    Zdroj.dok.Chemical Engineering and Processing: Process Intensification. - : Elsevier - ISSN 0255-2701
    Roč. 188, June (2023)
    Poč.str.9 s.
    Forma vydáníOnline - E
    Jazyk dok.eng - angličtina
    Země vyd.CH - Švýcarsko
    Klíč. slovaelectrocoagulation ; Zn removal ; full scale ; municipal incineration plant ; iron electrodes
    Vědní obor RIVDJ - Znečištění a kontrola vody
    Obor OECDEnvironmental sciences (social aspects to be 5.7)
    Vědní obor RIV – spolupráceÚstav chemických procesů - Průmyslová chemie a chemické inženýrství
    CEPTH03030388 GA TA ČR - Technologická agentura ČR
    Způsob publikováníOmezený přístup
    Institucionální podporaUH-J - RVO:67985874 ; UCHP-M - RVO:67985858
    UT WOS001039664300001
    EID SCOPUS85151912343
    DOI10.1016/j.cep.2023.109368
    AnotaceThe paper is focusing on the full-scale operation of electrocoagulation for Zn removal from wastewater with origin in a municipal incineration plant. The process was custom designed for continuous full-scale operation. Total capacity of the process varied between 1200 and 1400L/h. This was achieved by two simultaneous electrocoagulation cells operated in parallel. Residual concentrations of Zn in the treated water were consistently lower than 0.5 mg/L during the testing period. Residual concentrations of Zn and other accompanying contaminants were reduced below the desired limits (current limit for Zn in outlet water is 1.5 mg/L). The process cost was critically assessed. The electricity consumption for the operation of electrocoagulation cells is 0.75–1.1 kWh/m3 of purified water. A more significant expense is the consumption of electrode cartridges. The service life of electrode cartridges with a plate thickness of 5 mm is about 1 200 m3 of water/electrode pack, which represents a cost of around 0.6–1 EUR/m3 out of total 1.6 EUR/m3 of purified water. Waste incineration plants usually produce their own electricity therefore technologies like electrocoagulation become affordable and competitive.
    PracovištěÚstav pro hydrodynamiku
    KontaktSoňa Hnilicová, hnilicova@ih.cas.cz, Tel.: 233 109 003
    Rok sběru2024
    Elektronická adresahttps://www.sciencedirect.com/science/article/pii/S0255270123001058?via%3Dihub
Počet záznamů: 1  

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