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Non-circular ceramic membranes for use in wastewater treatment

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Języki publikacji
EN
Abstrakty
EN
An extensive use of membrane bioreactors in wastewater treatment often produces the effluent quality far beyond the current regulatory requirements for discharge to the environment. However, like other processes involving membranes, the severest constraint is the problem of fouling, the extent of which can be reduced by changing the flow pattern (maintaining in turbulent conditions) within the channels. In this study, the treatment of effluent from synthetic sludge production was investigated employing membrane bioreactors utilising non-circular multi-channelled membranes. Very high chemical oxygen demand (COD) and suspended solids (SS) removals were obtained for the range of pore sizes employed, up to 94% and 98%, respectively. As the pore size was increased, a decrease in efficiency was observed. Differences in the rejection behaviour are attributed to the difference in the characteristics of cakes which were formed. Specific cake resistance seems to increase moderately with diminishing pore size. The critical flux was found to be dependent on cross-flow velocity, introduction of inserts and pore size. Critical flux increased to about 82.5 l m-2 h-1 at a cross-flow velocity of 2.0 m s-1. The high critical flux can be attributed to the non-circular geometry of the channels which seems to promote turbulent flow, depolarising the solute built-up, even at low cross-flow velocity. Finally, the present paper demonstrates ways in which hydrodynamics and colloid interactions affect the critical flux.
Rocznik
Strony
53--60
Opis fizyczny
Bibliogr. 24 poz., tab., rys..
Twórcy
autor
  • School of Chemical Engineering and Analytical Science, The University of Manchester, P.O. Box 88, Manchester M60 1QD, UK
  • School of Chemical Engineering and Analytical Science, The University of Manchester, P.O. Box 88, Manchester M60 1QD, UK
autor
  • School of Chemical Engineering and Analytical Science, The University of Manchester, P.O. Box 88, Manchester M60 1QD, UK, Tel: + 44 0161 200 4368. Fax: + 44 0161 200 4399
Bibliografia
  • [1] ALMALACK M.H., ANDERSON G.K., Use of microfiltration in wastewater treatment, Water Res., 1997, 31, 3064–3072.
  • [2] FANE A.G., Membrane for water production and wastewater reuse, Desalination, 1996, 106, 1–9.
  • [3] FIELD R.W., WU D., HOWELL J.A., GUPTA B.B., Critical flux concept for microfiltration fouling, J. Membr. Sci., 1995, 100, 259–272.
  • [4] LE-CLECH P., JEFFERSON B., JUDD S.J., Impact of aeration, solids concentration and membrane characteristics on the hydraulic performance of a membrane bioreactor, J. Membr. Sci., 2003, 218, 117– 129.
  • [5] METACALF and EDDY, Wastewater Engineering Treatment and Reuse, McGraw-Hill, New York, 2003.
  • [6] CHANG I.S., LE-CLECH P., JEFFERSON B., JUDD S., Membrane fouling in membrane bioreactors for wastewater treatment, J. Environ. Eng., 2002, 128, 1018–1029.
  • [7] MADAENI S.S., FANE A.G., WILEY D.E., Factors influencing critical flux in membrane filtration of activated sludge, J. Chem. Technol. Biotechnol., 1999, 74, 539–543.
  • [8] CHANG I.S., GANDER M., JEFFERSON B., JUDD S., Low-cost membranes for use in a submerged MBR, Process Safety Environ. Protection, 2001, 79, 183–188.
  • [9] CHIU T.Y., JAMES A., Critical flux determination of non-circular multi-channel ceramic membranes using TiO2 suspensions, J. Membr. Sci., 2005, 254, 295–301.
  • [10] OECD, OECD Guidelines for Testing Chemicals, Organization for Economic Cooperation and Development, Paris, 1993, Guideline 302A & 303A.
  • [11] LARA DOMINGUEZ M.V., JAMES A.E., Use of floc physical properties in the study of sludge conditioning, Water Research, submitted for publication.
  • [12] APHA, 1992. Standard Methods for the Examination of Water and Wastewater, Section 5210, 18th ed., American Public Health Association, Water Works Association, American Water Environment Federation, Washington, DC, 5.1–5.6.
  • [13] YOURAVONG W., LEWIS M.J., GRANDISON A.S., Critical flux in ultrafiltration of skimmed milk, Trans IChemE, 2003, 81, 303–308.
  • [14] OGNIER S., WISNIEWSKI C., GRASMICK A., Membrane bioreactor fouling in sub-critical filtration conditions: a local critical flux concept, J. Membr. Sci., 2004, 229, 171–177.
  • [15] BELFORT G., DAVIS R.H., ZYDNEY A.L., The behaviour of suspensions and macromolecular solutions in crossflow microfiltration, J. Membr. Sci., 1994, 96, 1–58.
  • [16] THOMAS D.G., Forced convection mass transfer in hyperfiltration at high fluxes, Ind. Eng. Chem. Fundam., 1973, 12, 396–405.
  • [17] SCHWINGE J., WILEY D.E., FLETCHER D.F., A CFD study of unsteady flow in narrow spacer-filled channels for spiral-wound membrane modules, Desalination, 2002, 146, 195–201.
  • [18] CHEN V., Performance of partially permeable microfiltration membranes under low fouling conditions, J. Membr. Sci., 1998, 147, 265–278.
  • [19] GAN Q., ALLEN S.J., Crossflow microfiltration of a primary sewage effluent-solids retention efficiency and flux enhancement, J. Chem. Technol. Biotechnol., 1999, 74, 693–699.
  • [20] CHANG I.S., BAG S.O., LEE C.H., Effects of membrane fouling on solute rejection during membrane filtration of activated sludge, Process Biochemistry, 2001, 36, 855–860.
  • [21] LU W.M., JU S.C., Selective particle deposition in cross-flow filtration, Sep. Sci. Technol., 1989, 24, 517–540.
  • [22] ZHAO Y., ZHONG J., LI H., XU N., SHI J., Fouling and regeneration of ceramic microfiltration membranes in processing acid wastewater containing fine TiO2 particles, J. Membr. Sci., 2002, 208, 331–341.
  • [23] GUPTA B.B., HOWELL J.A., WU D., FIELD R.W., A helical baffle for cross-flow microfiltration, J. Membr. Sci., 1995, 102, 31–42.
  • [24] YEH H.M., CHEN H.Y., CHEN K.T., Membrane ultrafiltration in a tubular module with a steel rod inserted concentrically for improved performance, J. Membr. Sci., 2000, 168, 121–133.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BPG5-0011-0026
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