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Membrane Processes                                                                               569



                   membrane sheets and spacers into a ‘‘roll,’’ with the  Cevaal, J. N., Brunswick, R. J., Burke, J. E., and Suratt, W. B.,
                   sheets and spacers wound around a hollow tube.   Design of a reverse osmosis treatment system for nitrate
                                                                    removal for Brighton, Colorado, in: AWWA Annual Confer-
                   The feed flow enters the end of the tube with velocity
                                                                    ence, San Antonio, Texas, June 6–10, 1993.
                   parallel to the tube as a ‘‘cross-flow.’’ The permeate-
                                                               Champlin, T. L., Membrane Filtration (handout prepared for Oper-
                   flow velocity is normal to the cross-flow velocity,  ators Annual Short Course), University of Colorado, Boulder,
                   that is, the path is a spiral. The membrane sheets are  CO, March 26, 1996.
                   attached to the inner tube with small holes between  Champlin, T. L., Natural organic matter and particle fouling of
                   the sheets that receive the permeate flow.        spiral-wound nanofiltration membrane elements, Doctoral
            Spiral-wound membrane element: A spiral-wound mem-      thesis, Colorado State University, Fort Collins, CO, 1998.
                                                               Champlin, T. L. and Hendricks, D. W., Nanofiltration for treatment of
                   brane element is a double layer of membrane sheets
                                                                    low-turbidity waters, membrane fouling and removals of dis-
                   wound around a tube. Permeate spacers between the
                                                                    infection by-product precursors, Environmental Engineering
                   membrane sheets provide for permeate flow. Another  Technical Report, Department of Civil Engineering, Colorado
                   kind of spacer, that is, feed-flow spacer (of a coarse  State University, Fort Collins, CO, December 1994.
                   mesh fabric), is between the membrane sheets. Sev-  Cheryan, M., Ultrafiltration Handbook, Technomic Publishing Com-
                   eral such sheet assemblies may be wound around the  pany, Inc., Lancaster, PA, 1986.
                   tube to comprise a membrane element. This whole  Duranceau, S. J., Taylor, J. S., and Mulford, L. A., SOC removal in a
                                                                    membrane softening process, Journal of the American Water
                   element fits snugly in a cylindrical pressure vessel.
                                                                    Works Association, 84(1):68–78, January 1992.
                   An o-ring around the element fits against the pressure
                                                               Furukawa, D. H., Desalination Technology, 2006, in: AMBAG Con-
                   vessel and forces the flow to pass along the ‘‘feed-  ference, Monterey, CA, September 27, 2006 (pdf file).
                   flow’’ spacer, parallel to the tube. The permeate flow  General Electric Company, The Filtration Spectrum, General Elec-
                   enters a given spacer from the flow through the adja-  tric Company, Minnetonka, MN, 1993.
                   cent membranes and flows around the tube as a spiral  Global Water Intelligence (GWI), 19th International Desalination
                   and enters perforations along the tube; the tube  Association (IDA) Worldwide Desalting Plant Inventory,
                                                                    Media Analytic, Ltd., Oxford, U.K., 2006.
                   collects water from each leaf assembly and the per-
                                                               GWI, Desalination in 2008, Global Market Snapshot, 21st IDA World-
                   meate then passes from the tube. Figure 17.2b shows
                                                                    wide Desalting Plant Inventory, 2pp., 2008; http:==www.global-
                   a membrane element ready to insert into its pressure  waterintel.com (this site has proprietary information on market
                   vessel.                                          conditions for water services and products, changing as new
            Ultrafiltration: Characterized by membranes with pore size  information is developed).
                   between MF and NF.                          Hanft, S., Major reverse osmosis system components for water
                                                                    treatment: The global market, Report ID MST049B, Publica-
                                                                    tion ID WA1176332, 297pp., BCC Research, September 1,
                                                                    2005, http:==www.bccresearch.com=report=MST049B (obtained
            REFERENCES
                                                                    June 2009).
            Adham, S. Gramith, K., Chiu, K. P., Mysore, C., and Lainé, J. M.,  Helferrich, F., Ion Exchange, McGraw-Hill, Inc., New York, 1962.
                Development of a low pressure membrane knowledge base, in:  Hugaboom, D., Sethi, S., Crozes, G., Curl, J., and Marinas, B.,
                American Membrane Technology Association Annual Sympo-  Integrity testing for membrane filtration systems, in: American
                sium, Denver, CO, August 2–5, 2003.                 Membrane Technology Association Annual Symposium, Den-
            Amjad, Z., Ed., Reverse Osmosis—Membrane Technology, Water  ver, CO, August 2–5, 2003.
                Chemistry, and Industrial Applications, Van Nostrand Rein-  Hydranautics, http:==www.membranes.com, 2003.
                hold, New York, 1993.                          Koros, W. J., Membranes: Learning a lesson from nature, Chemical
            Amy, G. L., Alleman, B. A., and Cluff, C. B., Removal of dissolved  Engineering Progress, 91(10):68–81, October 1995.
                organic matter by nanofiltration, Journal of Environmental  Laisure, D., Sung, L., and Taylor, J. S., Fundamental membrane
                Engineering, ASCE, 116(1):200–205, 1990.            phenomena, Desalination and Water Reuse, 3(3):10–13, 1993.
            Anon., Advanced Waste Treatment Research Program Summary  Loeb, S., The Loeb-Sourirajan Membrane: How it came about,
                Report, Advanced Waste Treatment Branch, Robert A. Taft  in: Turbak, A. F., Ed., Synthetic Membranes, Volume 1,
                Sanitary Engineering Center, Federal Water Pollution Control  Desalination, ACS Symposium Series 153, American Chem-
                Administration, Cincinnati, OH, 1968.               ical Society, Washington, DC, 1981.
            ASTM, ASTM D4194-85. Standard method for operating character-  Lonsdale, H. K., The growth of membrane technology, Journal of
                istics of reverse osmosis devices, in: Annual Book of ASTM  Membrane Science, 10:81–181, Elsevier Scientific Publishing
                Standards, Water and Environmental Technology, Vol. 11.02,  Company, 1982.
                Water (II), Philadelphia, PA, 1987.            Meller, F. H., Ed., Electrodialysis (ED) & Electrodialysis Reversal
            AWWA, AWWA Membrane Technology Research Committee,      (EDR) Technology, Ionics Incorporated, Watertown, MA,
                Committee Report: Membrane processes in potable water  1984.
                treatment, Journal of the American Water Works Association,  Mickley, M. and Hamilton, B., Disposal of membrane concentrate
                84(1):59–67, January 1992.                          wastes: An AWWARF project status report, in: Proceedings,
            Baker, R. W., Membrane Technology and Applications, McGraw-  Membrane Technologies in the Water Industry, Orlando, FL,
                Hill, New York, 2000.                               March 10–13, 1991 [American Water Works Association,
            Blau, T. J., Taylor, J. S., Morris, K. E., and Mulford, L. A., DBP control  Denver, CO, 1991].
                of nanofiltration: Cost and performance, Journalofthe American  Mulder, M., Basic Principles of Membrane Technology, Kluwer
                Water Works Association, 84(12):104–116, December 1992.  Academic Publishers, Dordrecht, the Netherlands, 1991.
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