Hydrophobic polydimethylsiloxane thin-film composite membranes for the efficient pervaporative desalination of seawater and brines
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ArticleAuthors
Genduso, GiuseppeMissinne, Anton
Ali, Zain

Ogieglo, Wojciech
Van der Bruggen, Bart
Pinnau, Ingo

KAUST Department
Advanced Membranes and Porous Materials Research CenterBiological and Environmental Science and Engineering (BESE) Division
Chemical Engineering Program
Physical Science and Engineering (PSE) Division
KAUST Grant Number
BAS/1/1323-01-01Date
2021-09-29Online Publication Date
2021-09-29Print Publication Date
2022-01Embargo End Date
2022-09-29Submitted Date
2021-01-09Permanent link to this record
http://hdl.handle.net/10754/672039
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The pervaporative desalination of synthetic seawater and brines was studied to explore the water flux and salt rejection of a thin-film composite (TFC) membrane made of polydimethylsiloxane (PDMS) dip-coated on porous polysulfone support. Despite the hydrophobic nature of rubbery PDMS, we demonstrate that nonporous TFC membranes exhibit remarkable pervaporative desalination performance as evidenced by very high water permeance and 99.8±0.2% NaCl rejection. For comparison, two commercial hydrophilic polyamide thin-film composite membranes designed for reverse osmosis (RO) were also tested in pervaporation mode. At the highest temperature explored (85 °C) the PDMS thin-film composite membrane produced an outstanding pure water flux of ∼70 kg m-2 h-1, which was 2.6 times higher than that of the best commercial RO membrane tested in this work. Although the presence of salt in the feed water reduced water flux to 36 kg m-2 h-1 (at a brine sodium chloride concentration of 70,000 ppm and 85 °C), the hydrophobic PDMS composite membrane performed among the best compared with previously reported hydrophilic TFC polymer membranes.Citation
Genduso, G., Missinne, A., Ali, Z., Ogieglo, W., Van der Bruggen, B., & Pinnau, I. (2021). Hydrophobic polydimethylsiloxane thin-film composite membranes for the efficient pervaporative desalination of seawater and brines. Separation and Purification Technology, 119819. doi:10.1016/j.seppur.2021.119819Sponsors
This work was supported by funding from King Abdullah University of Science and Technology (BAS/1/1323-01-01).Publisher
Elsevier BVAdditional Links
https://linkinghub.elsevier.com/retrieve/pii/S1383586621015264ae974a485f413a2113503eed53cd6c53
10.1016/j.seppur.2021.119819