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The reduction of COD in wash wastewater from regeneration of sand filters

Identifikátory výsledku

  • Kód výsledku v IS VaVaI

    <a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F00216275%3A25310%2F18%3A39913242" target="_blank" >RIV/00216275:25310/18:39913242 - isvavai.cz</a>

  • Nalezeny alternativní kódy

    RIV/60460709:41310/18:76666

  • Výsledek na webu

  • DOI - Digital Object Identifier

Alternativní jazyky

  • Jazyk výsledku

    angličtina

  • Název v původním jazyce

    The reduction of COD in wash wastewater from regeneration of sand filters

  • Popis výsledku v původním jazyce

    The paper describes the reduction of COD and TOC in wastewater from the production of viscous fibers produced by the washing of sand filters on a laboratory scale. In addition to a significant concentration of zinc (8 – 30 mg), these waters also exhibited high values of COD (7 – 10 g/l) and TOC (2.5 – 3.1 g/l) respectively. A lot of organic substances, especially hemicellulose, residues of viscose fibers and non-ionic surfactants, are to be blamed for this. The organic matrix consisted of both solid and dissolved components, and therefore filtration was used for pre-treatment. The filtration itself has reduced the organic pollution by about 40 – 50 % depending on the porosity of the filter used. Pretreated wastewater was further oxidized by Fenton oxidation using 30% hydrogen peroxide and electrochemically generated Fe2+ ion in a 1:10 and 1: 100 molar ratios. Fenton oxidation has proven to be a highly effective tool for both COD and TOC reduction during 5 – 7 hours of oxidation, with a COD decrease by up to 95 % and a TOC decrease by 83 – 91 %. It is obvious that there is a considerable degree of mineralization of the dissolved organic matter in this case. The subsequent neutralization of the oxidized water to pH = 7.25 – 7.5 led to the simultaneous precipitation of iron ions and Zn2+ions. After their filtration, the zinc concentration dropped below 1 mg/l. Ozonation is an appealing way of purifying wastewater, as it allows water to be oxidized without pretreatment. However, the output of the available OZONSTAR 100 ozonizer with the hourly production of 1g of O3 was too low. Estimated required ozonizer output for a given type of wastewater is at least 0.1 – 0.2 kg O3/h per 1 m3. Nevertheless, both key group parameters of COD and TOC decreased in this case.

  • Název v anglickém jazyce

    The reduction of COD in wash wastewater from regeneration of sand filters

  • Popis výsledku anglicky

    The paper describes the reduction of COD and TOC in wastewater from the production of viscous fibers produced by the washing of sand filters on a laboratory scale. In addition to a significant concentration of zinc (8 – 30 mg), these waters also exhibited high values of COD (7 – 10 g/l) and TOC (2.5 – 3.1 g/l) respectively. A lot of organic substances, especially hemicellulose, residues of viscose fibers and non-ionic surfactants, are to be blamed for this. The organic matrix consisted of both solid and dissolved components, and therefore filtration was used for pre-treatment. The filtration itself has reduced the organic pollution by about 40 – 50 % depending on the porosity of the filter used. Pretreated wastewater was further oxidized by Fenton oxidation using 30% hydrogen peroxide and electrochemically generated Fe2+ ion in a 1:10 and 1: 100 molar ratios. Fenton oxidation has proven to be a highly effective tool for both COD and TOC reduction during 5 – 7 hours of oxidation, with a COD decrease by up to 95 % and a TOC decrease by 83 – 91 %. It is obvious that there is a considerable degree of mineralization of the dissolved organic matter in this case. The subsequent neutralization of the oxidized water to pH = 7.25 – 7.5 led to the simultaneous precipitation of iron ions and Zn2+ions. After their filtration, the zinc concentration dropped below 1 mg/l. Ozonation is an appealing way of purifying wastewater, as it allows water to be oxidized without pretreatment. However, the output of the available OZONSTAR 100 ozonizer with the hourly production of 1g of O3 was too low. Estimated required ozonizer output for a given type of wastewater is at least 0.1 – 0.2 kg O3/h per 1 m3. Nevertheless, both key group parameters of COD and TOC decreased in this case.

Klasifikace

  • Druh

    J<sub>SC</sub> - Článek v periodiku v databázi SCOPUS

  • CEP obor

  • OECD FORD obor

    20402 - Chemical process engineering

Návaznosti výsledku

  • Projekt

  • Návaznosti

    S - Specificky vyzkum na vysokych skolach

Ostatní

  • Rok uplatnění

    2018

  • Kód důvěrnosti údajů

    S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů

Údaje specifické pro druh výsledku

  • Název periodika

    Waste Forum

  • ISSN

    1804-0195

  • e-ISSN

  • Svazek periodika

    2018

  • Číslo periodika v rámci svazku

    2

  • Stát vydavatele periodika

    CZ - Česká republika

  • Počet stran výsledku

    10

  • Strana od-do

    98-107

  • Kód UT WoS článku

  • EID výsledku v databázi Scopus

    2-s2.0-85048975794