2016
DOI: 10.15671/hjbc.20164420570
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Electrosoption of Aromatic Organic Acids From Aqueous Solutions Onto Granular Activated Carbon Electrodes for Water Purification

Abstract: Ö Z E T S u arıtma sistemleri, artan insan nüfusu ve çevre kirliliği sonucunda oldukça önemli hale gelmiştir. Bu çalışmada, benzoik asit (BA) ve nikotinik asitin (NA) sulu çözeltilerinden, aktiflenmiş karbon elektrotlar (ACEs) üzerine elektrosorpsiyon yolu ile uzaklaştırılmaları incelenmiştir. ACEs, endüstriyel olarak elde edilebilen granüllü aktiflenmiş karbon ve polietilen bağlayıcı kullanılarak üretilmiştir. Elektrosorpsiyon sırasında organik moleküllerin derişimlerinde oluşan değişimler, online UV-Vis spek… Show more

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Cited by 4 publications
(3 citation statements)
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“…Similar trends have been observed with 2,4-dichlorophenoxyacetic acid (Fig. 8f) (Bayram et al, 2018), acilan blau dye (Koparal et al, 2002), burdem orange II (Gerçel, 2016), BA and NA (Bayram, 2016), metribuzin (Kitous et al, 2009) and BA (Bayram and Ayranci, 2012b) electrosorptions. It was assumed that the EDL thickness at the polarized adsorbent surface decreased with an increasing flow regime (Bayram et al, 2018).…”
Section: Residence Time Flow Rate Reactor Volume and Adsorbent Loadsupporting
confidence: 85%
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“…Similar trends have been observed with 2,4-dichlorophenoxyacetic acid (Fig. 8f) (Bayram et al, 2018), acilan blau dye (Koparal et al, 2002), burdem orange II (Gerçel, 2016), BA and NA (Bayram, 2016), metribuzin (Kitous et al, 2009) and BA (Bayram and Ayranci, 2012b) electrosorptions. It was assumed that the EDL thickness at the polarized adsorbent surface decreased with an increasing flow regime (Bayram et al, 2018).…”
Section: Residence Time Flow Rate Reactor Volume and Adsorbent Loadsupporting
confidence: 85%
“…It constitutes the basis to determine and predict the performance of systems during the optimization step in batch mode and for the subsequent scale-up phase. The kinetic data for electrosorption of many organic species onto carbon electrodes fit quite well with the pseudo-first-order kinetic model (Ayranci and Conway, 2001;Bayram andAyranci, 2012b, 2012a;Han et al, 2006b). Since high surface areas of the electrodes (e.g., porous carbon materials) are used most of the time in electrosorption, the kinetic rate is often limited by the electric current and not by diffusion.…”
Section: Modeling In Batch and Continuous Modesmentioning
confidence: 60%
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