Osmotically and thermally isolated forward osmosis – membrane distillation (FO-MD) integrated module
Valladares Linares, Rodrigo
Alsaadi, Ahmad Salem
Abu Ghdaid, Muhanned
Son, Hyuk Soo
Amy, Gary L.
KAUST DepartmentBiological and Environmental Sciences and Engineering (BESE) Division
Competitive Research Funds
Environmental Science and Engineering Program
OCRF- Special Academic Partnership
Water Desalination and Reuse Research Center (WDRC)
Online Publication Date2019-03-08
Print Publication Date2019-04-02
Permanent link to this recordhttp://hdl.handle.net/10754/631394
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AbstractIn this study, we propose a novel module design to integrate forward osmosis (FO) and membrane distillation (MD). The two processes are sealed in one module and operated simultaneously, making the system compact and suitable for a wide range of applications. To evaluate the system under large-scale module operating conditions, FO and MD experiments were performed separately. The effect of draw solution (DS) temperature on the FO performance was first assessed in terms of flux, reverse salt flux (RSF), and specific RSF (SRSF). While a higher DS temperature resulted in an increased RSF, a higher FO flux was achieved, with a lower SRSF. The influence of DS concentration on the MD performance was then investigated in terms of flux and salt rejection. High DS concentration had a slightly negative impact on MD water vapor flux, but the MD membrane was a complete barrier for DS salts. The FO-MD integrated module was simulated based on mass balance equations. Results indicated that initial DS (MD feed) flow rate and concentration are the most important factors for stable operation of the integrated module. Higher initial DS flow rate and lower initial DS concentration can achieve a higher permeate rate of the FO-MD module.
CitationKim Y, Li S, Francis L, Li Z, Linares RV, et al. (2019) Osmotically and thermally isolated forward osmosis – membrane distillation (FO-MD) integrated module. Environmental Science & Technology. Available: http://dx.doi.org/10.1021/acs.est.8b05587.
SponsorsThe research reported in this paper was supported by King Abdullah University of Science and Technology (KAUST), Saudi Arabia. Authors extend their gratitude to the Water Desalination and Reuse Center (WDRC) staff for their continuous support.
PublisherAmerican Chemical Society (ACS)