Treatment and Recycling of Wastewater by Submerged Hollow Fiber Membrane
ABSTRACT
In this study, the effects of experimental conditions including the MBR equipped novel device and different operating modes on permeate flux were studied. The results show that the MBR equipped novel device can reduce the resistance and enhance the flux, decreasing the total resistance ( Rt = 9.649) to 5.962 and increasing the permeate flux to 15 - 20 L/m2hr. The permeate flux of intermittent operating mode is more than that of continuous operation and the value of the permeate flux is between 15 l/m2hr and 20 l/m2hr. The MBR equipped novel device which adopting intermittent operating mode is most effective in this study and the value of permeate flux is between 20 l/m2hr and 25 l/m2hr.
In this study, the effects of experimental conditions including the MBR equipped novel device and different operating modes on permeate flux were studied. The results show that the MBR equipped novel device can reduce the resistance and enhance the flux, decreasing the total resistance ( Rt = 9.649) to 5.962 and increasing the permeate flux to 15 - 20 L/m2hr. The permeate flux of intermittent operating mode is more than that of continuous operation and the value of the permeate flux is between 15 l/m2hr and 20 l/m2hr. The MBR equipped novel device which adopting intermittent operating mode is most effective in this study and the value of permeate flux is between 20 l/m2hr and 25 l/m2hr.
Cite this paper
nullD. He, H. Zhou, L. Liu, D. Liang and L. Du, "Treatment and Recycling of Wastewater by Submerged Hollow Fiber Membrane," Natural Resources, Vol. 2 No. 2, 2011, pp. 71-74. doi: 10.4236/nr.2011.22009.
nullD. He, H. Zhou, L. Liu, D. Liang and L. Du, "Treatment and Recycling of Wastewater by Submerged Hollow Fiber Membrane," Natural Resources, Vol. 2 No. 2, 2011, pp. 71-74. doi: 10.4236/nr.2011.22009.
References
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[1] A. S. Malik, O. Boyko, N. Atkar and W. F. Young, “A Com-parative Study of MR Imaging Profile of Titanium Pedicle Screws,” Acta Radiologica, Vol. 42, No. 3, 2001, pp. 291-293. doi:10.1080/028418501127346846 [2] D. W. He, Y. T. Xiao and X. Li, “Treatment of Oil/Water Emulsion by Polyethylene Glycol Ultrafiltration Membrane,” Journal of Central south University, Vol. 12, No. 5, 2005, pp. 542-545. [3] N. Cicek, H. Winna, M.T. Suidan, B. E. Wrenn, V. Urbain and J. Manem, “Effectiveness of the Membrane Bioreactor in the Biodegrada-tion of High Molecular Weight Compounds,” Water Research, Vol. 32, No. 5, 1998, pp. 1553-1563. doi:10.1016/S0043-1354(97)00350-3 [4] T. Mukai, K. Taki-moto, T. Kohno and M. Okada, “Ultrafiltration Behaviour of Extracellular and Metabolic Products in Activated Sludge Sys-tem with UF Separation Process,” Water Research, Vol. 34, No. 3, 2000, pp. 902-908. doi:10.1016/S0043-1354(99)00208-0 [5] X. C. Wang and J. Wang, “Kinetic Study of Membrane Fouling under Cross-Flow Ultrafiltration Opteration,” Environmental Chemistry, Vol. 21, No. 6, 2002, pp. 552-558. [6] G. E. Wetterau, M. M. Clark and C. Anselme, “A dynamic model for predicting fouling ef-fects during the ultrafiltration of a groundwater,” Journal of Membrane Science, Vol. 109, No. 2, 1996, pp. 185-204. doi:10.1016/0376-7388(95)00200-6 [7] M. Cheryan, “Ul-trafiltration Handbook,” Technomic, Lancaster, 1986. [8] S. Kunikane, Y. Magara, M. Itoh and O. Tanaka, “A Comparative Study on the Application of Membrane Technology to the Pub-lic Water Supply,” Journal of membrane science, Vol. 102, 1995, pp. 149-154. doi:10.1016/0376-7388(94)00292-7 [9] T. Jiang, M. D. Ken-nedy, G. J. Walter, van der Meer, P. A. Vanrolleghem and J. C. Schippers, “The Role of Blocking and Cake Filtration in MBR Fouling,” Desalination, Vol. 157, 2003, pp. 335-343. doi:10.1016/S0011-9164(03)00414-4 [10] E. H. Bouhabila, R. B. A?m and B. Hervé, “Fouling Characterization in Membrane Bioreactors,” Separation and Purification Technology, Vol. 22-23, 2001, pp. 123-132. doi:10.1016/S1383-5866(00)00156-8 [11] C. Albasi, Y. Bess-iere, S. Desclaux and J. C. Remigy, “Filtration of Biological Sludge by Immersed Hollow-Fiber Membranes: Influence of Initial Permeability Choice of Operating Conditions,” Desali-nation, Vol. 146, 2002, pp. 427-431. doi:10.1016/S0011-9164(02)00527-1 [12] C. Albasi, Y. Bess-iere, S. Desclaux and J. C. Remigy, “Filtration of Biological Sludge by Immersed Hollow-Fiber Membranes: Influence of Initial Permeability Choice of Operating Conditions,” Desali-nation, Vol. 146, 2002, pp. 427-431. doi:10.1016/S0011-9164(02)00527-1 [13] C. Albasi, Y. Bess-iere, S. Desclaux and J. C. Remigy, “Filtration of biological sludge by immersed hollow-fiber membranes: influence of initial permeability choice of operating conditions,” Desalina-tion, Vol. 146, 2002, pp. 427-431. doi:10.1016/S0011-9164(02)00527-1 [14] K. J. Kim, A. G. Fane, C. J. D. Fell and D.C. Joy, “Fouling Mechanisms of Membranes during Protein Ultrafiltration,” Journal of mem-brane science, Vol. 68, No. 1, 1992, pp. 79-91. doi:10.1016/0376-7388(92)80151-9 [15] M. R. Wiesner and S. Chelam, “The promise of the membrane technology,” Envi-ronment Science and Technology, Vol. 33, No. 17, 1999, pp. 360-366. doi:10.1021/es993008l