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MEMBRANE FILTRATION 12-21

                12-8.   Determine the number of racks for the Spartanburg membrane filtration system for
                   the “worst case scenario” of one rack off-line for CIP plus one rack off-line for back-
                   wash given the following design requirements:
                                       3
                        Q    max        30,300 m  /d
                                   3
                                         2
                        J      0.127 m  /h · m
                                                  2
                                            3
                           J    max   allowable        0.170 m  /h · m
                        Cleaning cycle     30 min
                         Time off-line to clean     150 s
                                                      2
                        Membrane area per module     15 m
                        Modules per rack     90
                12-9.   Determine the number of racks for the town of Agate’s membrane filtration system
                   for the worst case scenario of one rack off-line for CIP plus one rack off-line for
                   backwash given the following design requirements:
                                       3
                        Q    winter        7,600 m  /d
                                          3
                          Q    summer        10,200 m  /d
                        Winter water temperature     1 	 C
                        Summer water temperature     15 	 C
                                         2
                                   3
                        J      0.159 m  /h · m   for winter temperature
                                            3
                                                  2
                        J    max   allowable        0.267 m  /h · m   for winter temperature
                        Cleaning cycle     30 min
                        Time off-line to clean     150 s
                                                      2
                        Membrane area per module     15 m
                        Modules per rack     40
            12-7  DISCUSSION QUESTIONS

                 12-1.   Because of the change in viscosity of water, a membrane design for cold water will
                   have a higher flux and be able to treat a greater flow rate at a higher temperature.
                   True or false?

                12-2.   What is the difference between irreversible and reversible transmembrane membrane
                   pressure?
                12-3.   Describe the parameter values you would need to compare membranes from different
                   manufacturers.


            12-8  REFERENCES
           AWWA (2005)  Microfiltration and Ultrafiltration Membranes for Drinking Water,  AWWA Manual
             M53, American Water Works Association, Denver, Colorado.
           Bergman, R. A. (2005) “Membrane Processes,” in E. E Baruth (ed.),  Water Treatment Plant Design,
             McGraw-Hill, New York, pp. 13.1–13.49.
           Carmen, P. C. (1937) “Fluid Flow through Granular Beds,”  Transactions of Institute of Chemical
             Engineers,  London, vol. 15, p. 150.
           Chellam, S. and J. G. Jacangelo (1998) “Existence of Critical Recovery and Impacts of Operational Mode
             on Portable Water Microfiltration,”  Journal of Environmental Engineering,  vol. 124, no. 12,
              pp. 1211–1219.
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