The present study deals with the removal of phosphorus from wastewater by using oven-dried alum sludge (ODS) as adsorbent that was collected from Al-Qadisiya treatment plant (Iraq); it was heated in an oven at for 24?h and then cooled at room temperature. The sludge particles were then crushed to produce a particle size of 0.5–4.75?mm. Two modes of operation are used, batch mode and fixed bed mode, in batch experiment the effect of oven-dried alum sludge doses 10–50?g/L, pH of solution 5–8 with constant initial phosphorus concentration of 5?mg/L, and constant particle size of 0.5?mm were studied. The results showed that the percent removal of phosphorus increases with the increase of oven-dried alum sludge dose, but pH of solution has insignificant effect. Batch kinetics experiments showed that equilibrium time was about 6 days. Adsorption capacity was plotted against equilibrium concentration, and isotherm models (Freundlich, Langmuir, and Freundlich-Langmuir) were used to correlate these results. In the fixed bed isothermal adsorption column, the effect of initial phosphorus concentration ( ) 5 and 10?mg/L, particle size 2.36 and 4.75?mm, influent flow rate (Q) 6 and 10?L/hr, and bed depth (H) 0.15–0.415?m were studied. The results showed that the oven-dried alum sludge was effective in adsorbing phosphorus, and percent removal of phosphorus reaches 85% with increasing of contact time and adsorbent surface area (i.e., mass of adsorbent 50?g/L with different pH). 1. Introduction Wastewater or contaminated water is a big environmental problem all over the world, in industrial plants; contaminants may be a result of side reactions, rendering the water stream an effluent status. These impurities are at low-level concentration but still need to be further reduced to levels acceptable by various destinations in the plant. Surface waters contain certain level of phosphorus (P) in various compounds, which is an important constituent of living organisms. In natural conditions the phosphorus concentration in water is balanced; that is, accessible mass of this constituent is close to the requirements of the ecological system. When the input of phosphorus to water is higher than it can be assimilated by a population of living organisms, the problem of excess phosphorus content occurs. Regulatory control on phosphorus disposal is evident all over the world recently [1–3]. Strict regulatory requirements decreased the permissible level of phosphorus concentration in wastewater at the point of disposal (i.e., 1?mg/L). This has made it very important to find
References
[1]
Environment Canada, “Proposed approach for wastewater effluent quality,” Final Report, Environment Canada, 2000.
[2]
USEPA, Environmental Assessment for the Final Effluent Limitations Guidelines, Pretreatment Standards for New and Existing Sources and New Source Performance Standards for the Centralized Waste Treatment, Prepared by Charles Tamulonis, 2000.
[3]
Department of Justice, Pollutant Substances Prevention Regulation, Department of Justice, Ottawa, Canada, 2004.
[4]
D. Zhao and A. K. Sengupta, “Ultimate removal of phosphate from wastewater using a new class of polymeric ion exchangers,” Water Research, vol. 32, no. 5, pp. 1613–1625, 1998.
[5]
L. Liberti, D. Petruzzelli, and L. De Florio, “REM NUT ion exhange plus struvite precipitation process,” Environmental Technology, vol. 22, no. 11, pp. 1313–1324, 2001.
[6]
R. G. Penetra, M. A. P. Reali, E. Foresti, and J. R. Campos, “Post-treatment of effluents from anaerobic reactor treating domestic sewage by dissolved-air flotation,” Water Science and Technology, vol. 40, no. 8, pp. 137–143, 1999.
[7]
P. Jokela, E. Ihalainen, J. Hein?nen, and M. Viitasaari, “Dissolved air flotation treatment of concentrated fish farming wastewaters,” Water Science and Technology, vol. 43, no. 8, pp. 115–121, 2001.
[8]
K. C. Yu, J. S. Chang, I. P. Chen, D. J. Chang, C. Y. Chang, and S. H. Chen, “The removal of colloid and dissolved phosphorus by coagulation and membrane microfiltration,” Journal of Environmental Science and Health A, vol. 35, no. 9, pp. 1603–1616, 2000.
[9]
A. Dietze, R. Gnir?, and U. Wiesmann, “Phosphorus removal with membrane filtration for surface water treatment,” Water Science and Technology, vol. 46, no. 4-5, pp. 257–264, 2002.
[10]
W. Xie, M. Kondo, and Y. Naito, “Study on phosphorus removal using a new coagulation system,” Water Science and Technology, vol. 30, no. 6, pp. 257–262, 1994.
[11]
L. Jonsson, E. Plaza, and B. Hultman, “Experiences of nitrogen and phosphorus removal in deep-bed filters in the Stockholm area,” Water Science and Technology, vol. 36, no. 1, pp. 183–190, 1997.
[12]
F. Rogalla, G. Roudon, J. Sibony, and F. Blondeau, “Minimising nuisances by covering compact sewage treatment plants,” Water Science and Technology, vol. 25, no. 4-5, pp. 363–374, 1992.
[13]
S. Zeghal, N. Puznava, J. P. Subra, and P. Sauvegrain, “Process control for nutrients removal using lamella sedimentation and floating media filtration,” Water Science and Technology, vol. 38, no. 3, pp. 227–235, 1998.
[14]
D. G. Wareham, K. J. Hall, and D. S. Mavinic, “ORP screening protocol for biological phosphorus removal in sequencing batch reactors,” Canadian journal of civil engineering, vol. 22, no. 2, pp. 260–269, 1995.
[15]
N. R. Louzeiro, D. S. Mavinic, W. K. Oldham, A. Meisen, and I. S. Gardner, “Methanol-induced biological nutrient removal kinetics in a full-scale sequencing batch reactor,” Water Research, vol. 36, no. 11, pp. 2721–2732, 2002.
[16]
J. K. Park, J. Wang, and G. Novotny, “Wastewater characteristization for evaluation of biological phosphorus removal,” Research Report 174, Department of Natural Resources, Wisconsin, Wis, USA, 1997.
[17]
M. I. Aguilar, J. Sáez, M. Lloréns, A. Soler, and J. F. Ortu?o, “Nutrient removal and sludge production in the coagulation-flocculation process,” Water Research, vol. 36, no. 11, pp. 2910–2919, 2002.
[18]
J. G. Kim, J. H. Kim, H. S. Moon, C. M. Chon, and J. S. Ahn, “Removal capacity of water plant alum sludge for phosphorus in aqueous solutions,” Chemical Speciation and Bioavailability, vol. 14, no. 1–4, pp. 67–73, 2003.
[19]
J. R. Weber and J. Walter, Physicochemical Processes for Water Quality Control, Wiley-Inter Science, New York, NY, USA, 1972.
[20]
Metcalf and Eddy, Waste Water Engineering Treatment, Disposal and Reuse, McGrew Hill Book Company, New York, NY, USA, 1979.
[21]
W. W. Eckenfelder Jr, Application of Adsorption to Waste Water Treatment, Enviro Press, Nashville, Tenn, USA, 1981.
[22]
L. D. Benefield, J. L. Judkins, and B. L. Weanal, Process Chemistry for Water and Wastewater Treatment, Prentice Hall, New Jersey, NJ, USA, 1982.
[23]
T. D. Reynolds and P. A. Richards, Unit Operation and Processes in Environmental Engineering, PWS publishing Co, Boston, Mass, USA, 1996.
[24]
R. Sips, “Structure of a catalyst surface,” Journal of Chemical Physics, vol. 16, pp. 490–495, 1984.
[25]
S. E. Ebrahim, Evaluation of mixture adsorption and glass bed for the removal of phenol and methylene blue from water [Ph.D. thesis], University of Baghdad, Baghdad, Iraq, 2008.
[26]
M. Mortula, M. Gibbons, and G. A. Gagnon, “Phosphorus adsorption by naturally-occurring materials and industrial by-products,” Journal of Environmental Engineering and Science, vol. 6, no. 2, pp. 157–164, 2007.