Existence of Critical Recovery and Impacts of Operational Mode on Potable Water Microfiltration
Publication: Journal of Environmental Engineering
Volume 124, Issue 12
Abstract
Results from a potable water microfiltration (MF) pilot study employing untreated surface water are reported. The effects of filtrate flux and recovery on direct flow, outside-inside, hollow fiber MF fouling rates, and backwash effectiveness are presented. Constant flux experiments suggested the existence of a critical recovery below which MF fouling rates were low and effectiveness of backwashes was high and relatively independent of the recovery. However, in the range of experimental conditions investigated, fouling rates increased dramatically and backwash effectiveness decreased steeply when this critical recovery was exceeded regardless of the flux. In general, for a fixed recovery, specific flux profiles analyzed on the basis of volume filtered per unit membrane area were insensitive to filtrate flux. Fouling was accelerated by operating membranes at constant flux rather than at constant pressure, in part, because of membrane compaction and cake compression. Changing the mode of filtration between constant flux and constant pressure is shown to have no effect on MF filtrate water quality. For any given capacity, membrane area requirements are decreased, and power requirements are increased when membranes are operated at constant flux rather than at constant pressure.
Get full access to this article
View all available purchase options and get full access to this article.
References
1.
Belfort, G., Davis, R. H., and Zydney, A. L.(1994). “The behavior of suspensions and macromolecular solutions in crossflow microfiltration.”J. Membr. Sci., 96, 1–58.
2.
Chellam, S., Jacangelo, J. G., and Bonacquisti, T. P.(1998). “Modeling and experimental verification of pilot-scale, direct flow, hollow fiber microfiltration with periodic backwashing.”Envir. Sci. and Technol., 32(1), 75–81.
3.
Chellam, S., and Wiesner, M. R.(1997). “Particle back-transport and permeate flux behavior in crossflow membrane filters.”Envir. Sci. and Technol., 31(3), 819–824.
4.
Chellam, S., and Wiesner, M. R.(1998). “Evaluation of crossflow filtration models based on shear-induced diffusion and particle adhesion: Complications induced by feed suspension polydispersivity.”J. Membr. Sci., 138(1), 83–97.
5.
Cornwell, D. A., Bishop, M. M., Bishop, T. R., McTigue, N. E., Rolan, A. T., and Bailey, T. (1991). Full-scale evaluation of declining and constant rate filtration. American Water Works Association Research Foundation, Denver, Colo.
6.
Fane, A. G.(1986). “Ultrafiltration: Factors influencing flux and rejection.”Prog. Filt. Sep., 4, 101–179.
7.
Field, R. W., Wu, D., Howell, J. A., and Gupta, B. B.(1995). “Critical flux concept for microfiltration fouling.”J. Memb. Sci., 100, 259–272.
8.
Heald, C. C. (1988). Cameron hydraulic data. Ingersoll-Rand Company, Woodcliff Lake, NJ.
9.
Jacangelo, J. G., and Buckley, C. A. (1996). “Microfiltration.”Water treatment membrane processes, J. Mallevialle, P. E. Odendaal, and M. R. Wiesner, eds., McGraw-Hill, Inc., New York, 11.1–11.39.
10.
Khatib, K., Rose, J., Barres, O., Stone, W., Bottero, J.-Y., and Anselme, C.(1997). “Physicochemical study of fouling mechanisms of ultrafiltration membrane on Biwa Lake (Japan).”J. Memb. Sci., 130, 53–62.
11.
Krasner, S. W., McGuire, M. J., Jacangelo, J. G., Patania, N. L., Reagan, K. M., and Aieta, E. M.(1989). “The occurrence of disinfection by-products in U.S. drinking water.”J. Am. Water Works Assn., 81(8), 41–53.
12.
Mallevialle, J., Anselme, C., and Marsigny, O. (1989). “Effects of humic substances on membrane processes.”Advances in chemistry, Series 219, American Chemical Society, Denver, Colo., 749–767.
13.
Matsumoto, K., Kawahara, M., and Ohya, H.(1988). “Cross-flow filtration of yeast by microporous ceramic membrane with backwashing.”J. Ferment. Technol., 66(2), 199–205.
14.
Nagata, N., Herouvis, K. J., Dziewulski, D. M., and Belfort, G.(1989). “Cross-flow membrane microfiltration of a bacterial fermentation broth.”Biotech. Bioengrg., 34, 447–466.
15.
Nakanishi, K., Tadokoro, T., and Matsuno, R.(1987). “On the specific resistance of cakes of microorganisms.”Chem. Engrg. Commun., 62, 187–201.
16.
Persson, K. M., Gekas, V., and Tragardh, G. (1995). “Study of membrane compaction and its influence on ultrafiltration water permeability.”J. Membr. Sci. 100, 155–162.
17.
Pickering, K. D., and Wiesner, M. R.(1994). “Cost model for low-pressure membrane filtration.”J. Envir. Engrg., ASCE, 119(5), 772–797.
18.
Redkar, S. G., and Davis, R. H.(1995). “Cross-flow microfiltration with high-frequency reverse filtration.”AIChE J., 41(3), 501–508.
19.
Rodgers, V. G. J., and Sparks, R. E.(1992). “Effect of transmembrane pressure pulsing on concentration polarization.”J. Membr. Sci., 68, 149–168.
20.
Romero, C. A., and Davis, R. H.(1991). “Experimental verification of the shear-induced hydrodynamic model of crossflow microfiltration.”J. Membr. Sci., 62, 249–273.
21.
Tiller, F. M., Yeh, C. S., and Leu, W. F.(1987). “Compressibility of particulate structures in relation to thickening, filtration and expression: A review.”Sep. Sci. Technol., 22, 1037–1063.
22.
Turker, M., and Hubble, J.(1987). “Membrane fouling in a constant-flux ultrafiltration cell.”J. Membr. Sci., 34, 267–281.
23.
Vladisavljevic, G. T., Milonjic, S. K., and Pavasovic, V. L.(1995). “Flux decline and gel resistance in unstirred ultrafiltration of aluminum hydrous oxide sols.”J. Colloid and Interface Sci., 176, 491–494.
24.
Wetterau, G. E., Clark, M. M., and Anselme, C.(1996). “A dynamic model of predicting fouling effects during the ultrafiltration of a groundwater.”J. Membr. Sci., 109, 185–204.
25.
Wiesner, M. R., and Aptel, P. (1996). “Mass transport and permeate flux and fouling in pressure-driven processes.”Water treatment membrane processes, J. Mallevialle, P. E. Odendaal, and M. R. Wiesner, eds., McGraw-Hill, Inc., New York, 4.1–4.30.
26.
Wiesner, M. R., and Mazounie, P.(1989). “Raw water characteristics and the selection of treatment configurations for particle removal.”J. Am. Water Works. Assn., 81(5), 80–89.
27.
Wilharm, C., and Rodgers, V. G. J.(1996). “Significance of duration and amplitude in transmembrane pressure pulsed ultrafiltration of binary protein mixtures.”J. Membr. Sci., 121, 217–228.
28.
Zeman, L. J., and Zydney, A. L. (1996). Microfiltration and ultrafiltration, Marcel Dekker, Inc., New York.
Information & Authors
Information
Published In
Copyright
Copyright © 1998 American Society of Civil Engineers.
History
Published online: Dec 1, 1998
Published in print: Dec 1998
Authors
Metrics & Citations
Metrics
Citations
Download citation
If you have the appropriate software installed, you can download article citation data to the citation manager of your choice. Simply select your manager software from the list below and click Download.