Comparison of reverse osmosis membrane fouling characteristics in full-scale leachate treatment systems with chemical coagulation and microfiltration pre-treatments

Fouling characteristics of reverse osmosis (RO) membrane with chemical coagulation and microfiltration (MF) pre-treatment were investigated at full-scale leachate treatment systems. In chemical coagulation pre-treatment, solid separation from stabilized leachate was performed by ferric chloride coag...

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Veröffentlicht in:Water science and technology : a journal of the International Association on Water Pollution Research. - 1986. - 71(2015), 4 vom: 20., Seite 580-7
1. Verfasser: Rukapan, Weerapong (VerfasserIn)
Weitere Verfasser: Khananthai, Benyapa, Srisukphun, Thirdpong, Chiemchaisri, Wilai, Chiemchaisri, Chart
Format: Online-Aufsatz
Sprache:English
Veröffentlicht: 2015
Zugriff auf das übergeordnete Werk:Water science and technology : a journal of the International Association on Water Pollution Research
Schlagworte:Journal Article Chlorides Ferric Compounds Membranes, Artificial Water Pollutants, Chemical Nitrogen N762921K75 ferric chloride U38V3ZVV3V
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520 |a Fouling characteristics of reverse osmosis (RO) membrane with chemical coagulation and microfiltration (MF) pre-treatment were investigated at full-scale leachate treatment systems. In chemical coagulation pre-treatment, solid separation from stabilized leachate was performed by ferric chloride coagulation followed by sand filtration. Meanwhile, MF pre-treatment and the RO system utilized direct filtration using a 0.03 µm membrane without chemical addition. MF pre-treatment yielded better pollutant removals in terms of organics and nitrogen. The study on effect of pre-treatment on RO membrane fouling revealed that accumulated foulant on the RO membrane in MF pre-treatment was significantly lower than that of chemical coagulation. Nevertheless, NaOH cleaning of the fouled RO membrane after chemical coagulation pre-treatment could better recover its permeate flux, thus suggesting that the formation of a loose-structure cake layer by chemical coagulation pre-treatment could allow effective penetration of chemical cleaning and detachment of foulant layer from the membrane surface 
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650 7 |a Chlorides  |2 NLM 
650 7 |a Ferric Compounds  |2 NLM 
650 7 |a Membranes, Artificial  |2 NLM 
650 7 |a Water Pollutants, Chemical  |2 NLM 
650 7 |a Nitrogen  |2 NLM 
650 7 |a N762921K75  |2 NLM 
650 7 |a ferric chloride  |2 NLM 
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700 1 |a Khananthai, Benyapa  |e verfasserin  |4 aut 
700 1 |a Srisukphun, Thirdpong  |e verfasserin  |4 aut 
700 1 |a Chiemchaisri, Wilai  |e verfasserin  |4 aut 
700 1 |a Chiemchaisri, Chart  |e verfasserin  |4 aut 
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