TY - JOUR
T1 - UV radiation pretreatment for reverse osmosis (RO) process in ultrapure water (UPW) production
AU - Jin, Yongxun
AU - Lee, Hyunkyung
AU - Zhan, Min
AU - Hong, Seungkwan
N1 - Funding Information:
This research was supported by a grant from Technology Innovation Program ( 10052814 , Technology development of ultra-pure water process for semiconductor level industrial water and localization for 4 kinds of consumable material) funded by the Ministry of Trade, Industry and Energy, South Korea . CE cellulose acetate FDR flux decline rate IPA isopropanol alcohol LP low pressure lamp LMW low molecular weight MF microfiltration MFI modified fouling index (s/L 2 ) MFI 0.45 modified fouling index using a 0.45 μm membrane filter (s/L 2 ) MFI-UF modified fouling index ultrafiltration (s/L 2 ) MFI-UF flux modified fouling index measured under constant flux condition (s/L 2 ) MFI-UF pres modified fouling index measured under constant pressure condition (s/L 2 ) MP medium pressure lamp RO reverse osmosis SAXS small angle X-ray scattering SDI Silt Density Index (%/min) TMP transmembrane pressure (Pa) TOC total organic matter (ppm) UPW ultrapure water UV ultraviolet
PY - 2018/8/1
Y1 - 2018/8/1
N2 - In ultrapure water (UPW) production, ultraviolet (UV) radiation is an effective process for reducing microorganisms and organic matter. An increasing trend of reusing the spent UPW further encourages the adoption of UV at the upstream of reverse osmosis (RO) to mitigate membrane fouling and to enhance water quality. In this study, UV technology, both low and medium pressure lamps, was assessed for RO pretreatment in UPW production. The fouling potential of problematic pollutants (e.g., silica and IPA) was evaluated pre and post UV treatment based on fouling index under constant flux mode. We found that the rejection rate of IPA was enhanced up to 80% and thus reduced the organic fouling potential in RO. On the contrary, for inorganic nano-particle such as silica, a significant increase in fouling potential after UV exposure was observed. Zeta and small angle X-ray scattering analysis implied that this fouling potential transition was derived from silica particle agglomeration under UV radiation. The RO fouling tests corroborated findings from fouling index measurements, showing severe flux decline after UV radiation. This research provides new insight for UPW production design by revealing the influence of UV on inorganic and organic pollutants during the reclamation of spent UPW.
AB - In ultrapure water (UPW) production, ultraviolet (UV) radiation is an effective process for reducing microorganisms and organic matter. An increasing trend of reusing the spent UPW further encourages the adoption of UV at the upstream of reverse osmosis (RO) to mitigate membrane fouling and to enhance water quality. In this study, UV technology, both low and medium pressure lamps, was assessed for RO pretreatment in UPW production. The fouling potential of problematic pollutants (e.g., silica and IPA) was evaluated pre and post UV treatment based on fouling index under constant flux mode. We found that the rejection rate of IPA was enhanced up to 80% and thus reduced the organic fouling potential in RO. On the contrary, for inorganic nano-particle such as silica, a significant increase in fouling potential after UV exposure was observed. Zeta and small angle X-ray scattering analysis implied that this fouling potential transition was derived from silica particle agglomeration under UV radiation. The RO fouling tests corroborated findings from fouling index measurements, showing severe flux decline after UV radiation. This research provides new insight for UPW production design by revealing the influence of UV on inorganic and organic pollutants during the reclamation of spent UPW.
KW - Membrane fouling
KW - Modified fouling index (MFI)
KW - Reverse osmosis (RO)
KW - Ultrapure water (UPW)
KW - Ultraviolet (UV)
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U2 - 10.1016/j.desal.2018.04.019
DO - 10.1016/j.desal.2018.04.019
M3 - Article
AN - SCOPUS:85046371442
SN - 0011-9164
VL - 439
SP - 138
EP - 146
JO - Desalination
JF - Desalination
ER -