Batch and Continuous Design of a Full‐Scale Treatment Facility for Removing Dissolved Natural Organic Matter

Batch and continuous flow adsorption experiments are carried out and the design of a full‐scale facility for removing dissolved natural organic matter (DNOM) from Catalan Lakewater is demonstrated. The adsorption efficiency is proportional to the temperature and the amount of adsorbent unlike pH inc...

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Veröffentlicht in:Clean : soil, air, water air, water, 2021-01, Vol.49 (1), p.n/a
Hauptverfasser: Sari, Bulent, Oztas, Ali Erdem, Keskinkan, Olcayto, Ersu, Cagatayhan Bekir
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Sprache:eng
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Zusammenfassung:Batch and continuous flow adsorption experiments are carried out and the design of a full‐scale facility for removing dissolved natural organic matter (DNOM) from Catalan Lakewater is demonstrated. The adsorption efficiency is proportional to the temperature and the amount of adsorbent unlike pH increase. The highest DNOM removal rate is obtained at 35 °C, pH 4, and an adsorbent amount of 0.8 g L−1. Optimum contact time for batch studies is 60 min at equilibrium. Correlation constants (r) of Langmuir and Freundlich isotherms are 0.8905 and 0.9739, respectively. Based on the Freundlich isotherm, the highest adsorption capacity (qmax) obtained is 2.44 and 6.01 mg DNOM/g granulated activated carbon (GAC) for raw and enriched water, respectively. Consequently, the effects of adsorbent amount, bed depth, empty bed contact time, and organic loading on removal performance are investigated in the rapid small‐scale column test (RSSCT) columns. The targeted effluent concentration of 1 mg DNOM/L can easily be achieved in the columns. At the design capacity of the facility, 15 adsorption columns with dimensions of 7 m height, 4.33 m diameter, and 22 days of operation cycle are required to remove DNOM from raw water. Dissolved natural organic matter (DNOM) is a major issue during disinfection. DNOM could be removed from the effluent of a full‐scale water treatment plant in this study, depending on temperature, pH, as well as contact time. Based on isotherm model results, design parameters for full‐scale adsorption columns could be determined.
ISSN:1863-0650
1863-0669
DOI:10.1002/clen.202000098