2019
DOI: 10.5004/dwt.2019.23319
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Long-term pilot plant study using direct chlorination for biofouling control of a chlorine-resistant polyamide reverse osmosis membrane

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Cited by 5 publications
(2 citation statements)
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“…Considering this concentration and contact time, the concentration–time of contact (CT) value for this tertiary polyamide membrane was calculated to be 9,600 ppm·h. In our previous study, the intermittent addition of NaOCl at C fc = 10 ppm for 10 min every 24 h prevented biofouling during the reverse osmosis membrane filtration of secondary treated sewage from Higashi-Hiroshima Wastewater Treatment Plant, Japan . Comparing the CT value and intermittent chlorination conditions, the tertiary polyamide membrane was expected to be useful for an operation period of 7.9 years.…”
Section: Resultsmentioning
confidence: 99%
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“…Considering this concentration and contact time, the concentration–time of contact (CT) value for this tertiary polyamide membrane was calculated to be 9,600 ppm·h. In our previous study, the intermittent addition of NaOCl at C fc = 10 ppm for 10 min every 24 h prevented biofouling during the reverse osmosis membrane filtration of secondary treated sewage from Higashi-Hiroshima Wastewater Treatment Plant, Japan . Comparing the CT value and intermittent chlorination conditions, the tertiary polyamide membrane was expected to be useful for an operation period of 7.9 years.…”
Section: Resultsmentioning
confidence: 99%
“…In previous studies, the monomers used to synthesize conventional secondary amide membranes, such as trimesoyl chloride and m -phenylenediamine, were replaced by other monomers. , Kawaguchi and colleagues reported that tertiary amides were inert to free chlorine species according to their results using model compounds such as N -methylbenzanilide and N -phenylbenzanilide . Because of its chlorine resistance, N , N ′-dimethyl- m -phenylenediamine has been used in interfacial polymerization as an acidic chloride monomer; the resulting tertiary polyamide membrane showed excellent tolerance to free chlorine species compared to that of the conventional secondary polyamide , because of the physical protection of the chlorine-sensitive nitrogen. This tertiary polyamide membrane is ready to be produced at the commercial scale, and a recent paper reported the performance of tertiary polyamide membrane in the long-term pilot plant study using direct chlorination for biofouling control; however, its durability to deterioration by free chlorine and the related deterioration mechanisms should be studied to facilitate its practical application and further improvement.…”
Section: Introductionmentioning
confidence: 99%