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Scale-up rules for flocculation

Identifikátory výsledku

  • Kód výsledku v IS VaVaI

    <a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F68407700%3A21220%2F17%3A00313226" target="_blank" >RIV/68407700:21220/17:00313226 - isvavai.cz</a>

  • Výsledek na webu

    <a href="http://dx.doi.org/10.1016/j.minpro.2017.08.003" target="_blank" >http://dx.doi.org/10.1016/j.minpro.2017.08.003</a>

  • DOI - Digital Object Identifier

    <a href="http://dx.doi.org/10.1016/j.minpro.2017.08.003" target="_blank" >10.1016/j.minpro.2017.08.003</a>

Alternativní jazyky

  • Jazyk výsledku

    angličtina

  • Název v původním jazyce

    Scale-up rules for flocculation

  • Popis výsledku v původním jazyce

    We present here a study of three baffled tanks, 0.15 m, 0.20m and 0.30min inner diameter, agitated by Rushton turbine, with reference to scaling up the flocculation kinetics. A clay slurry was used as a model wastewater. The experimentswere carried out at mixing intensity 40 W/m3 and clay concentration 0.58 g/L. The model wastewater was flocculated with the Sokoflok 16A organic flocculent (solution 0.1 wt%) in the range of dimensionless flocculent dosage DF from 0.448 to 5.241 mg/g. The flocs that formed were separated bymeans of sedimentation. The operational conditions were designed according to following proposed scale-up rules: i) P/V = const., ii) tF * = N.tF=const., iii)DF * =const. and iv) used=const. Applying the proposed scale-up rules, the flocculation efficiency was found to be practically the same irrespective of vessel size and flocculation dosage. For the given flocculated system and process conditions, the maximum degree of turbidity removal Ze * max=96.1± 0.6% was found for dimensionless flocculation time 1916 ± 5% and dimensionless flocculent dosage DF * =3.128 mg/g ± 8%, regardless of vessel size. The approach to scale-up proposed by Camp (1955) is discussed and criticized in the light of present-day mixing theory, and an explanation is offered of the shortcomings of this approach, and why it gives incorrect scale-up results.

  • Název v anglickém jazyce

    Scale-up rules for flocculation

  • Popis výsledku anglicky

    We present here a study of three baffled tanks, 0.15 m, 0.20m and 0.30min inner diameter, agitated by Rushton turbine, with reference to scaling up the flocculation kinetics. A clay slurry was used as a model wastewater. The experimentswere carried out at mixing intensity 40 W/m3 and clay concentration 0.58 g/L. The model wastewater was flocculated with the Sokoflok 16A organic flocculent (solution 0.1 wt%) in the range of dimensionless flocculent dosage DF from 0.448 to 5.241 mg/g. The flocs that formed were separated bymeans of sedimentation. The operational conditions were designed according to following proposed scale-up rules: i) P/V = const., ii) tF * = N.tF=const., iii)DF * =const. and iv) used=const. Applying the proposed scale-up rules, the flocculation efficiency was found to be practically the same irrespective of vessel size and flocculation dosage. For the given flocculated system and process conditions, the maximum degree of turbidity removal Ze * max=96.1± 0.6% was found for dimensionless flocculation time 1916 ± 5% and dimensionless flocculent dosage DF * =3.128 mg/g ± 8%, regardless of vessel size. The approach to scale-up proposed by Camp (1955) is discussed and criticized in the light of present-day mixing theory, and an explanation is offered of the shortcomings of this approach, and why it gives incorrect scale-up results.

Klasifikace

  • Druh

    J<sub>imp</sub> - Článek v periodiku v databázi Web of Science

  • CEP obor

  • OECD FORD obor

    20703 - Mining and mineral processing

Návaznosti výsledku

  • Projekt

  • Návaznosti

    I - Institucionalni podpora na dlouhodoby koncepcni rozvoj vyzkumne organizace

Ostatní

  • Rok uplatnění

    2017

  • Kód důvěrnosti údajů

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

Údaje specifické pro druh výsledku

  • Název periodika

    International Journal of Mineral Processing

  • ISSN

    0301-7516

  • e-ISSN

    1879-3525

  • Svazek periodika

    167

  • Číslo periodika v rámci svazku

    august

  • Stát vydavatele periodika

    NL - Nizozemsko

  • Počet stran výsledku

    7

  • Strana od-do

    79-85

  • Kód UT WoS článku

    000412962500010

  • EID výsledku v databázi Scopus

    2-s2.0-85028467639