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Using supercritical CO2 for alginate-fouled seawater reverse osmosis cleaning and for carbonate mineral production from concentrated brine

Authors
Jung, BongyeonPark, KitaeKim, YurimHan, SeungyeonKim, SiyePark, DaheeSoo Choi, JongYoon, YeominIm, SungjuLee, Sangyoup
Issue Date
Feb-2025
Publisher
Elsevier B.V.
Keywords
Mineralization; Organic fouling; Reverse osmosis; Seawater desalination; Supercritical carbon dioxide
Citation
Separation and Purification Technology, v.354
Indexed
SCIE
SCOPUS
Journal Title
Separation and Purification Technology
Volume
354
URI
https://scholarx.skku.edu/handle/2021.sw.skku/115753
DOI
10.1016/j.seppur.2024.128627
ISSN
1383-5866
1873-3794
Abstract
Organic fouling is recognized as one of the main challenges in seawater reverse osmosis (SWRO). To overcome this challenge, membrane cleaning is routinely conducted. In this study, membrane cleaning with supercritical carbon dioxide (sCO2) was implemented. To understand the mechanism of sCO2 cleaning, the effects of pH, shear force, phase of CO2 (supercritical/gaseous), and type of organic foulant (alginate only, alginate with calcium (Ca2+) ions, or transparent exopolymer particles (TEP)) were investigated. sCO2 cleaning had 82–87 % of cleaning efficiency, regardless of foulant types. With alginate-fouled membranes, sCO2 presented 89.7 % cleaning efficiency, while de-ionized water flushing, pH 5 solution, liquid CO2 showed respective cleaning efficiencies of 12.2 %, 6.2 %, 9.3 % and 7.2 %. The superior cleaning efficiency of sCO2 for organic fouling is mainly attributed to the supercritical phase that promotes shear force and dissolution (local acidic pH). Moreover, the mineralization of brine using the spent sCO2 cleaning agent was evaluated. sCO2 was able to convert divalent ions (Ca2+ and magnesium(Mg2+)) into nano-sized carbonate precipitates (∼46 nm) that can be potentially traded to reduce water production cost and environmental burdens when brine is released into seawater. © 2024 Elsevier B.V.
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