ISSN: 0256-1115 (print version) ISSN: 1975-7220 (electronic version)
Copyright © 2024 KICHE. All rights reserved

Articles & Issues

Language
English
Conflict of Interest
In relation to this article, we declare that there is no conflict of interest.
Publication history
Received March 21, 2021
Accepted August 21, 2021
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
Copyright © KIChE. All rights reserved.

All issues

Investigation of thin-film composite hollow fiber forward osmosis membrane for osmotic concentration: A pilot-scale study

Gas Processing Centre, College of Engineering, Qatar University, Doha, Qatar 1Department of Chemical Engineering, College of Engineering, Qatar University, Doha, Qatar 2ConocoPhillips Global Water Sustainability Centre, Qatar Science & Technology Park, Doha, Qatar
m.nasser@qu.edu.qa
Korean Journal of Chemical Engineering, January 2022, 39(1), 178-188(11), 10.1007/s11814-021-0935-9
downloadDownload PDF

Abstract

The current study applied the forward osmosis (FO) based osmotic concentration (OC) process at the pilot-scale for concentrating synthetic feed solution (FS). The process water (PW) salinity represents effluents from the gas industry, while the draw solution (DS) mimics seawater. Besides, the performance of a hollow fiber (HF) membrane manufactured from polyamide thin film composite (PA-TFC) was evaluated. The effect of operation with various feed recovery rates, flowrates and temperatures on the OC performance was examined. Outcomes reveal that the tested membrane succeeded in recovering up to 90% of FS at water flux of 6.40 LMH. The stability of OC plant was successfully demonstrated for 48 hours long-term run at 75% feed recovery as an optimum condition, where the TFC membrane achieved average water flux of 6.00 LMH, respectively. Higher DS flowrate improved the OC performance by inducing higher water permeation and FS recovery; however, it increased the undesirable reverse solute diffusion. Lastly, the permeability coefficient of the HF membrane was estimated by 2.69LMH/bar at 25°C, which significantly enhanced at higher temperatures.

References

Ansari MIH, Qurashi A, Nazeeruddin MK, J. Photochem. Photobiol. C Photochem. Rev., 35, 1 (2018)
Adham S, Hussain A, Minier-Matar J, Janson A, Sharma R, Desalination, 440, 2 (2018)
Cath TY, Childress AE, Elimelech M, J. Membr. Sci., 281(1-2), 70 (2006)
Van der Bruggen B, Luis P, Rev. Chem. Eng., 31(1), 1 (2015)
Chung TS, Luo L, Wan CF, Cui Y, Amy G, Sep. Purif. Technol., 156, 856 (2015)
Alsvik L, Hagg MB, Polymers, 5, 303 (2013)
Bao X, Wu QL, Tian JY, Shi WX, Wang W, Zhang ZQ, Zhang RJ, Zhang B, Guo Y, Shu SH, Cui FY, Chem. Eng. J., 370, 262 (2019)
Lay WCL, Chong TH, Tang CY, Fane AG, Zhang J, Liu Y, Water Sci. Technol., 61, 927 (2010)
Lutchmiah K, Verliefde ARD, Roest K, Rietveld LC, Cornelissen ER, Water Res., 58, 179 (2014)
Mazlan NM, Peshev D, Livingston AG, Desalination, 377, 138 (2016)
Klaysom C, Cath TY, Depuydt T, Vankelecom IFJ, Chem. Soc. Rev., 42, 6959 (2013)
Yangali-Quintanilla V, Li ZY, Valladares R, Li QY, Amy G, Desalination, 280(1-3), 160 (2011)
Haupt A, Lerch A, Membranes, 8, 47 (2018)
Zhao SF, Zou L, Tang CYY, Mulcahy D, J. Membr. Sci., 396, 1 (2012)
Perry M, https://www.forwardosmosistech.com/how-forward-osmosis-performance-is-limited-by-concentration-polarization, Accessed 20 August 2019 (2013).
Lee S, Boo C, Elimelech M, Hong S, J. Membr. Sci., 365(1-2), 34 (2010)
Boo C, Elimelech M, Hong S, J. Membr. Sci., 444, 148 (2013)
Ge QC, Ling MM, Chung TS, J. Membr. Sci., 442, 225 (2013)
Munirasu S, Haija MA, Banat F, Process Saf. Environ. Prot., 100, 183 (2016)
Chekli L, Phuntsho S, Kim JE, et al., J. Memb. Sci., 497 (2016).
Johnson DJ, Suwaileh WA, Mohammed AW, Hilal N, Desalination, 434, 100 (2018)
Kim JE, Kuntz J, Jang A, Kim IS, Choi JY, Phuntsho S, Shon HK, Process Saf. Environ. Prot., 127, 180 (2019)
Jalab R, Awad AM, Nasser MS, Minier-Matar J, Adham S, Judd SJ, Water Res., 163, 114879 (2019)
Veil J, Clark C, SPE Prod. Oper., 26, 234 (2011)
Veil J, U.S Produced Water Volumes and Management Practices in 2012 (2015).
Hickenbottom KL, Hancock NT, Hutchings NR, Appleton EW, Beaudry EG, Xu P, Cath TY, Desalination, 312, 60 (2013)
Minier-Matar J, Santos A, Hussain A, Janson A, Wang R, Fane AG, Adham S, Environ. Sci. Technol., 50, 6044 (2016)
Minier-Matar J, Hussain A, Janson A, Wang R, Fane AG, Adham S, Desalination, 376, 1 (2015)
Phuntsho S, Sahebi S, Majeed T, Lotfi F, Kim JE, Shon HK, Chem. Eng. J., 231, 484 (2013)
Hawari AH, Kamal N, Altaee A, Desalination, 398, 98 (2016)
Im SJ, Go GW, Lee SH, Park GH, Jang A, Desalin. Water Treat., 57, 24583 (2016)
Phuntsho S, Vigneswaran S, Kandasamy J, Hong S, Lee S, Shon HK, J. Membr. Sci., 415-416, 734 (2012)
Chakrabortty S, Pal M, Roy M, Pal P, Desalination, 365, 329 (2015)
Im SJ, Jeong S, Jang A, J. Membr. Sci., 549, 366 (2018)
Thabit MS, Hawari AH, Ammar MH, Zaidi S, Zaragoza G, Altaee A, Desalination, 461, 22 (2019)
Ren J, McCutcheon JR, Desalination, 343, 187 (2014)
Majeed T, Phuntsho S, Sahebi S, Kim JE, Yoon JK, Kim K, Shon HK, Desalin. Water Treat., 54, 817 (2015)
Arena JT, Manickam SS, Reimund KK, Brodskiy P, McCutcheon JR, Ind. Eng. Chem. Res., 54(45), 11393 (2015)
Suwaileh W, Pathak N, Shon H, Hilal N, Desalination, 485, 114455 (2020)
Mansouri S, Khalili S, Peyravi M, Jahanshahi M, Darabi RR, Ardeshiri F, Rad AS, Korean J. Chem. Eng., 35(11), 2256 (2018)
Bolto B, Zhang J, Wu X, Xie Z, Membranes, 10, 4 (2020)
Oasys Water, http://oasyswater.com/solutions/technology/ (Accessed 27 April 2020).
Sanahuja-Embuena V, Khensir G, Yusuf M, Andersen MF, Nguyen XT, Trzaskus K, Pinelo M, Helix-Nielsen C, Membranes, 9, 66 (2019)
Wang R, Shi L, Tang CYY, Chou SR, Qiu C, Fane AG, J. Membr. Sci., 355(1-2), 158 (2010)
Majeed T, Lotfi F, Phuntsho S, Yoon JK, Kim K, Shon HK, Desalin. Water Treat., 53, 1744 (2015)
Wang W, Guo Y, Liu M, Song X, Duan J, Korean J. Chem. Eng., 37(9), 1573 (2020)
Mirkhalili SM, Mousavi SA, Abadi ARS, Sadeghi M, Korean J. Chem. Eng., 34(12), 3170 (2017)
Jalab R, Awad AM, Nasser MS, Minier-matar J, Adham S, J. Environ. Chem. Eng., 8, 104494 (2020)
Wang Q, Zhou ZY, Li JQ, Tang QC, Hu YX, Desalination, 452, 75 (2019)
Feng L, Xie L, Suo G, Shao X, Dong T, Trans. Tianjin Univ., 24, 571 (2018)
Chowdhury MR, McCutcheon JR, J. Membr. Sci., 553, 189 (2018)
Ren J, Chowdhury MR, Qi J, Xia LL, Huey BD, McCutcheon JR, J. Membr. Sci., 540, 344 (2017)
You SJ, Wang XH, Zhong M, Zhong YJ, Yu C, Ren NQ, Chem. Eng. J., 198-199, 52 (2012)
Maltos RA, Regnery J, Almaraz N, Fox S, Schutter M, Cath TJ, Veres M, Coday BD, Cath TY, Desalination, 440, 99 (2018)
Xiao TT, Nghiem LD, Song JF, Bao RY, Li XM, He T, Sep. Purif. Technol., 186, 45 (2017)
Shibuya M, Yasukawa M, Takahashi T, Miyoshi T, Higa M, Matsuyama H, Desalination, 362, 34 (2015)
Zhao SS, Minier-Matar J, Chou SR, Wang R, Fane AG, Adham S, Desalination, 402, 143 (2017)
Akther N, Sodiq A, Giwa A, Daer S, Arafat HA, Hasan SW, Chem. Eng. J., 281, 502 (2015)
Heo J, Chu KH, Her N, Im J, Park YG, Cho J, Sarp S, Jang A, Jang M, Yoon Y, Desalination, 389, 162 (2016)
Shaffer DL, Werber JR, Jaramillo H, Lin SH, Elimelech M, Desalination, 356, 271 (2015)

The Korean Institute of Chemical Engineers. F5, 119, Anam-ro, Seongbuk-gu, 233 Spring Street Seoul 02856, South Korea.
TEL. No. +82-2-458-3078FAX No. +82-507-804-0669E-mail : kiche@kiche.or.kr

Copyright (C) KICHE.all rights reserved.

- Korean Journal of Chemical Engineering 상단으로