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Removal of boron from SWRO permeate by boron selective ion exchange resins containing N-methyl glucamine groups

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dc.creator KABAY, NALAN
dc.creator Yuksel, M.
dc.creator KİTİŞ, Mehmet
dc.creator KÖSEOĞLU, Hasan
dc.creator ARAR, ÖZGÜR
dc.creator BRYJAK, M.
dc.creator SEMIAT, R.
dc.creator Sarp, S.
dc.date 2008-02-29T22:00:00Z
dc.date.accessioned 2020-10-06T11:22:41Z
dc.date.available 2020-10-06T11:22:41Z
dc.identifier c3b3ec1c-6f4c-42b2-b501-faa6d3033c69
dc.identifier 10.1016/j.desal.2007.01.199
dc.identifier https://avesis.sdu.edu.tr/publication/details/c3b3ec1c-6f4c-42b2-b501-faa6d3033c69/oai
dc.identifier.uri http://acikerisim.sdu.edu.tr/xmlui/handle/123456789/71397
dc.description The objective of this study is to explore the performance of the boron selective ion exchange resins for boron removal from seawater reverse osmosis (SWRO) permeate. A lab-scale cross-flow flat-sheet configuration test unit (SEPA CF II, Osrnonics) and FilmTec RO membranes were used for batch-mode RO tests. Seawater samples containing 5.1 mg B/L were collected from the Mediterranean Sea. The chelating ion exchange resins containing N-methyl glucamine groups (Diaion CRB 02 and Dowex-XUS 43594.00 resins) were employed for batch and column-mode tests to remove boron from SWRO permeate. Optimum resin amount for boron removal from SWRO permeate was found as 1 g resin/L for both Diaion and Dowex resins. The equilibrium half-time for B removal was between 30 and 45 min for Dowex and 20-30 min for Diaion resins. Sorption kinetics for these resins fit to Ho pseudo-second-order kinetics model. Both resins exhibited large breakthrough capacities with boron leakage of less than 0.2 mg B/L. Breakthrough capacity was influenced by space velocity. Boron loaded onto the resins was quantitatively eluted with 5% H2SO4 solution.
dc.language eng
dc.rights info:eu-repo/semantics/closedAccess
dc.title Removal of boron from SWRO permeate by boron selective ion exchange resins containing N-methyl glucamine groups
dc.type info:eu-repo/semantics/article


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