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Forward osmosis membrane

A.K. Ghosh, R.C. Bindal, S. Prabhakar, P.K. Tewari, Concentration of ammonium diuranate effluent by reverse osmosis and forward osmosis membrane processes. Desal. Water Treat., 2013, 52(1-3), 2014. http //dx.doi.org/10.1080/ 19443994.2013.808449. [Pg.721]

A. AchUh, T.Y. Cath, E.A. Marchand, A.E. ChUdress, The forward osmosis membrane bioreactor A low fouling alternative to MBR processes. Desalination 2009, 239, 10-21. [Pg.841]

E.R. Comelissen, D. Harmsen, K.P. de Korte, C.J. Ruiken, J.-J. Qin, H. Oo, L.P. Wessels, Membrane fouling and process performance of forward osmosis membranes on activated sludge. Journal of Membrane Science 2008, 319, 158-168. [Pg.841]

In contrast to a neutral membrane, the positively charged forward osmosis membrane provides double electric repulsions to the salt transfer through the membrane in the active layer facing feed water configuration. This results in a reduction of the salt penetration, while in the active layer facing draw solution config-... [Pg.330]

Tiraferri, A., Tip, N.Y., Phillip, W.A. et al. (2011) Relating performance of thin-film composite forward osmosis membranes to support layer formation and structure. Journal of Membrane Science, 367 (1-2), 340-352. [Pg.297]

Benny D. Freeman (membrane science oxidatively stable desalination and forward osmosis membrane materials bioinspired membranes to control fouling of water purification membranes physical aging of glassy polymeric materials and membranes), Richard B. [Pg.34]

Jin, X., She, Q., Ang, X. Tang C.Y. (2012) Removal of boron and arsenic by forward osmosis membrane influence of membrane orientation and organic fouling. Journal of Membrane Science, 389, 182-187. [Pg.309]

Removal of inorganic and organic trace contaminants by forward osmosis membranes... [Pg.312]

Jin, X., Tang, C.Y., Gu, Y, She, Q. Qi, S. (2011) Boric acid permeation in forward osmosis membrane processes modeling, experiments, and implications. Environmental Science Technology, 45 (6), 2323-2330. [Pg.329]

Jin, X., Shan, X, Wang, C., Wei, J. Tang, C.Y. (2012a) Rejection of pharmaceuticals by forward osmosis membranes. Journal of Hazardous Materials, 227-228, 55-61. [Pg.329]

Mi, B. Elimelech, M. (2008) Chemical and physical aspects of organic fouling of forward osmosis membranes. Journal of Membrane Science, 320 (1-2), 292-302. [Pg.329]

Tang, C.Y, She, Q., Lay, W.C.L., Wang, R. Fane, A.G. (2010) Coupled effects of internal concentration polarization fouling on flux behavior of forward osmosis membranes during humic acid filtration. [Pg.329]

Figure 16.18 Flux performance of 2 commercially available RO membranes from GE Water (AG, CE) and a cellulose triacetate forward osmosis membranes from Hydration Technology Innovations (CTA). The draw solution used was a 6M ammonia-carbon dioxide solution and the feed solution was a 0.5M sodium chloride solution. The temperature of the test was 50°G Reprinted from REF16-B7. Tests were done in a custom built, crossflow, benchtop FO testing system. Figure 16.18 Flux performance of 2 commercially available RO membranes from GE Water (AG, CE) and a cellulose triacetate forward osmosis membranes from Hydration Technology Innovations (CTA). The draw solution used was a 6M ammonia-carbon dioxide solution and the feed solution was a 0.5M sodium chloride solution. The temperature of the test was 50°G Reprinted from REF16-B7. Tests were done in a custom built, crossflow, benchtop FO testing system.
Song XX, Liu ZY, Sun D (2011) Nano gives the answer breaking the bottleneck of internal concentration polarization with a nanofiber composite forward osmosis membrane for a high water production rate. Adv Mater 23 3256-3260... [Pg.354]

Liu, X., S. Qi, Y. Li, L. Yang, B. Cao, and C. Y. Tang. 2013. Synthesis and characterization of novel antibacterial silver nanocomposite nanofiltration and forward osmosis membranes based on layer-by-layer assembly. Water Res. 47 3081-3092. [Pg.156]

Q. Yang, K.Y. Wang, and T.S. Chung. (2009). Dual-layer hollow fibers with enhanced flux as novel forward osmosis membranes for water production. Environ. Sci. Technol. 43 2800-2805. [Pg.245]

M. Amini, M. Jahanshahi, A. Rahimpour. Synthesis of novel thin film nanocomposite (TFN) forward osmosis membranes using functionahzed multi-waUed carbon nanotubes, Journal of Membrane Science 435 (2013) 233-241. [Pg.505]

N.Y. Yip, A. Tirafeiri, W.A. Phillip, J.D. Schiffman, M. Elimelech, High performance thin-film composite forward osmosis membrane. Environmental Science Technology... [Pg.506]

C. Qiu, S. Qi, C.Y. Tang, Synthesis of high flux forward osmosis membranes by chemically crosslinked layer-by-layer polyelectrolytes, Journal of Membrane Science, 381 (2011)74-80. [Pg.565]

In liquid separation, hollow fiber membranes based on PBI have shown excellent performance for pervaporation dehydration of organic liquids. For example, a dual layer PEI-PBI hollow fiber membrane with an outer selective layer of PBI showed better performance than most other polymeric membranes in pervaporation dehydration of ethylene glycol. Sulfonation modifications of PBI membranes have demonstrated excellent separation efficacies in the dehydration of acetic acid. Studies have shown that PBI hollow fiber membranes were effective in separating chromates from solutions. Also, PBI nanofiltration hollow fiber membranes are promising candidates as forward osmosis membranes. In gas separation, recent studies sponsored by the Department of Energy at Los Alamos National Laboratories and SRI International demonstrated potential applications of PBI membranes in carbon capture and Hj purification from synthesis gas streams at elevated temperatures. H2/CO2 selectivity > 40 has been achieved at H2 permeability of 200 GPU at 250°C. ... [Pg.208]


See other pages where Forward osmosis membrane is mentioned: [Pg.1251]    [Pg.52]    [Pg.278]    [Pg.48]    [Pg.328]    [Pg.332]   
See also in sourсe #XX -- [ Pg.396 , Pg.397 ]




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