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Received February 12, 2012
Accepted April 27, 2012
- This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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A comprehensive study on wastewater treatment using photo-impinging streams reactor: Continuous treatment
1Refining Technology Development Division, Research Institute of Petroleum Industry, Tehran, Iran 2Chemical Engineering Department, Amirkabir University of Technology, Tehran, Iran
sohrabi@aut.ac.ir
Korean Journal of Chemical Engineering, November 2012, 29(11), 1577-1584(8), 10.1007/s11814-012-0058-4
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Abstract
The degradation of phenol was investigated in a continuous flow impinging streams system. In the first step, statistical experimental designs were used to optimize the process of phenol degradation in a photo-impinging streams reactor. The more important factors affecting phenol degradation (p<0.05) were screened by a two-level Plackett-Burman design. Four of the latter parameters, namely phenol concentration, catalyst loading, pH and slurry flow rate, were selected for final process optimization, applying central composite design (CCD). The predicted data showed that the maximum removal efficiency of phenol (99%) could be obtained under the optimum operating conditions (phenol concentration=50 mg l^(-1), catalyst loading=2.1 g l^(-1), pH 6.2 and slurry flow rate=550ml min^(-1)). These predicted values were then verified by certain validating experiments. A good correlation was observed between the predicted data and those determined by the experimental study. This may confirm the validity of the statistical optimum strategy. Finally, continuous degradation of phenol was performed, and the results indicated a higher efficiency and an increased performance capability of the present reactor in comparison with the conventional processes.
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References
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Laokiat L, Khemthong P, Grisdanurak N, Sreearunothai P, Pattanasiriwisawa W, Klysubun W, Korean J. Chem. Eng., 29(3), 377 (2012)
Park JH, Seo YS, Kim HS, Kim IK, Korean J. Chem. Eng., 28(8), 1693 (2011)
Subramanian M, Kannan A, Chem. Eng. Sci., 65(9), 2727 (2010)
Vildozo D, Ferronato C, Sleiman M, Chovelon JM, Appl. Catal. B: Environ., 94(3-4), 303 (2010)
Van Gerven T, Mul G, Moulijn J, Stankiewicz A, Chem. Eng. Process., 46(9), 781 (2007)
Royaee SJ, Sohrabi M, Desalination, 253(1-3), 57 (2010)
Royaee SJ, Sohrabi M, Soleymani F, J. Chem. Technol. Biotechnol., 86(2), 205 (2011)
Meshram S, Limaye R, Ghodke S, Nigam S, Sonawane S, Chikate R, Chem. Eng. J., 172(2-3), 1008 (2011)
Hyoung Cho I, Duk Zoh K, Dyes Pigm., 75, 533 (2007)
Vildozo D, Ferronato C, Sleiman M, Chovelon JM, Appl. Catal. B: Environ., 94(3-4), 303 (2010)
Abdel-Fattah YR, Saeed HM, Gohar YM, El-Baz MA, Process Biochnol., 40, 1707 (2005)
Gheshlaghi R, Scharer JM, Moo-Young M, Douglas PL, Biotechnol. Bioeng., 90(6), 754 (2005)
Stanbury PF, Whitaker A, Hall SJ, Media for industrial fermentations, In: Principles of Fermentation Technology, Pergamon, 93 (1986)
Khuri AI, Cornell JA, Response surfaces: designs and analysis, New York, Marcel Dekker, ASQA Quality Press (1996)
Montgomery DC, Design and Analysis of Experiments, 5th Ed.New York, John Wiley and Sons, 170 (2001)
Ollis, E. Pelizzetti and N. Serpone N, Environ. Sci. Technol., 25, 1523 (1991)
Chiou CH, Wu CY, Juang RS, Chem. Eng. J., 139(2), 322 (2008)
Sobczynski A, Duczmal L, Zmudzinski W, J. Mol. Catal. A-Chem., 213(2), 225 (2004)
Pujara K, Kamble SP, Pangarkar VG, Ind. Eng. Chem. Res., 46(12), 4257 (2007)
Malato S, Blanco J, Richter C, Braun B, Maldonado MI, Appl. Catal. B: Environ., 17(4), 347 (1998)
Suryaman D, Hasegawa K, Kagaya S, Yoshimura T, J. Hazard. Mater., 171(1-3), 318 (2009)
Royaee SJ, Sohrabi M, Ind. Eng. Chem. Res., 51(11), 4152 (2012)