Membranes 2013, 3(3), 155-168; doi:10.3390/membranes3030155
Article

Temperature and Pressure Effects of Desalination Using a MFI-Type Zeolite Membrane

1 Institute for Sustainability and Innovation, College of Engineering and Science, Victoria University, Hoppers Lane, Werribee 3030, Australia 2 Chosun Refractory Co. Ltd., Taein Dong, Kwangyang-si, Jeonlanam-do 545-893, Korea 3 Department of Chemical Engineering, Sunchon National University, Maegok Dong, Suncheon 540-742, Korea 4 Ceramics (Aust.) Pty. Ltd., Rivulet Crescent, Albion Park Rail 2527, Australia 5 Research Services Office, Flinders University, Adelaide 5001, Australia
* Author to whom correspondence should be addressed.
Received: 16 June 2013; in revised form: 8 July 2013 / Accepted: 9 July 2013 / Published: 17 July 2013
(This article belongs to the Special Issue Membranes and Water Treatment)
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Abstract: Zeolites are potentially a robust desalination alternative, as they are chemically stable and possess the essential properties needed to reject ions. Zeolite membranes could desalinate “challenging” waters, such as saline secondary effluent, without any substantial pre-treatment, due to the robust mechanical properties of ceramic membranes. A novel MFI-type zeolite membrane was developed on a tubular α-Al2O3 substrate by a combined rubbing and secondary hydrothermal growth method. The prepared membrane was characterised by scanning electron microscopy (SEM), X-ray photoelectron spectroscopy (XPS) and single gas (He or N2) permeation and underwent desalination tests with NaCl solutions under different pressures (0.7 MPa and 7 MPa). The results showed that higher pressure resulted in higher Na+ rejection and permeate flux. The zeolite membrane achieved a good rejection of Na+ (~82%) for a NaCl feed solution with a TDS (total dissolved solids) of 3000 mg·L−1 at an applied pressure of 7 MPa and 21 °C. To explore the opportunity for high salinity and high temperature desalination, this membrane was also tested with high concentration NaCl solutions (up to TDS 90,000 mg·L−1) and at 90 °C. This is the first known work at such high salinities of NaCl. It was found that increasing the salinity of the feed solution decreased both Na+ rejection and flux. An increase in testing temperature resulted in an increase in permeate flux, but a decrease in ion rejection.
Keywords: desalination; MFI-type zeolite membrane; rubbing method; seeded secondary growth

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MDPI and ACS Style

Zhu, B.; Kim, J.H.; Na, Y.-H.; Moon, I.-S.; Connor, G.; Maeda, S.; Morris, G.; Gray, S.; Duke, M. Temperature and Pressure Effects of Desalination Using a MFI-Type Zeolite Membrane. Membranes 2013, 3, 155-168.

AMA Style

Zhu B, Kim JH, Na Y-H, Moon I-S, Connor G, Maeda S, Morris G, Gray S, Duke M. Temperature and Pressure Effects of Desalination Using a MFI-Type Zeolite Membrane. Membranes. 2013; 3(3):155-168.

Chicago/Turabian Style

Zhu, Bo; Kim, Jun H.; Na, Yong-Han; Moon, Il-Shik; Connor, Greg; Maeda, Shuichi; Morris, Gayle; Gray, Stephen; Duke, Mikel. 2013. "Temperature and Pressure Effects of Desalination Using a MFI-Type Zeolite Membrane." Membranes 3, no. 3: 155-168.

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