Elimination of Phenol Content in Baiji Refinery Waste Water Using Ash Supported Cupper
Article Sidebar
Main Article Content
Abstract
High level of phenolic compounds is realized in some refinery waste water; fly ash waste of electrical station is applied in a trickle bed reactor to eliminate phenolic compounds contents in that wastewater. The fly ash with a cupper added was applied at different operation conditions namely pressure (5, 10, and 15), solution pH (5, 7 and 9), and 2-3 hr-1 liquid hourly space velocity. The fly ash catalyst exhibited an optimum performance in the reactor at 2 hrs-1, 150 °C and 15 bar with a pH of 5 with a phenol conversion of 93.43% within a time period of 3hrs.
Metrics
Article Details
This work is licensed under a Creative Commons Attribution 4.0 International License.
THIS IS AN OPEN ACCESS ARTICLE UNDER THE CC BY LICENSE http://creativecommons.org/licenses/by/4.0/
Plaudit
References
G. Moussavi, M. Mahmoudi, B. Barikbin, (2009), “Biological removal of phenol from strong wastewaters using a novel MSBR”, Water Research 43, 1295–1302. DOI: https://doi.org/10.1016/j.watres.2008.12.026
R. Pinto, L. Lintomen, L.F. Luz Jr., M.R.,Wolf-Maciel, (2005), “Strategy for recovering phenol from wastewater, evaluation environmental concerns”, Fluid Phase Equilibria 228, 447–457. DOI: https://doi.org/10.1016/j.fluid.2004.09.005
S.H. Lin, R.S. Juang, (2009), “Adsorption of phenol and its derivatives from water using synthetic resins and low-cost natural adsorbents: a review”, Journal of Environmental Management, 90 ,1336–1349. DOI: https://doi.org/10.1016/j.jenvman.2008.09.003
K. Rzeszutek, A. Chow, (1998), “Extraction of phenols using polyurethane membrane”, Talanta 46 507–519. DOI: https://doi.org/10.1016/S0039-9140(97)00273-7
C.G. Silva, J.L. Faria, (2009), “Effect of key operational parameters on the photocatalytic oxidation of phenol by nanocrystalline sol-gel TiO2 under UV irradiation”, Journal of Molecular Catalysis A: Chemical 305, 147–154. DOI: https://doi.org/10.1016/j.molcata.2008.12.015
I.V. Perez, S. Rogak, R. Branion, (2004), “Supercritical water oxidation of phenol and 2,4-dinitrophenol”, Journal of Supercritical Fluids, 30, 71–87. DOI: https://doi.org/10.1016/S0896-8446(03)00166-9
Misha, V.S., Mahajani, V.V., Joshi, J.B., 1995. “Wet air oxidation”. Ind. Eng. Chem. Res. 34, 2–48. DOI: https://doi.org/10.1021/ie00040a001
Fortuny, A., Font, J., Fabregat, A., 1998. “Wet air oxidation of phenol using active carbon as catalyst”. Appl. Catal. B: Environ. 19, 165–173. DOI: https://doi.org/10.1016/S0926-3373(98)00072-1
Fortuny, A., Bengoa, C., Font, J., Fabregat, A., 1999. “Bimetallic catalysts for continuous catalytic wet air oxidation of phenol”. J. Hazard. Mater.B 64, 181–193. DOI: https://doi.org/10.1016/S0304-3894(98)00245-3
J.Zhao,Z.Liu,D.Sun,(2004),”TPO–TPD study of an activated carbon- supported copper catalyst–sorbent used for catalytic dry oxidation of phenol”, J. Catal., 227, 297–303. DOI: https://doi.org/10.1016/j.jcat.2004.07.020
S.B. Wang, (2008), Environ. Sci. Technol. 42, 7055–7063. DOI: https://doi.org/10.1021/es801312m
S.B. Wang, H.M. Ang, M.O., (2008), Tade, Chemosphere, 72 1621–1635. DOI: https://doi.org/10.1016/j.chemosphere.2008.05.013
P.F. Ng, L. Li, S.B. Wang, Z.H. Zhu, G.Q. Lu, Z.F. Yan, (2007), Environ. Sci. Technol. 41, 3758–3762. DOI: https://doi.org/10.1021/es062326z
S.B.Wang,G.Q.Lu,H.Y.Zhu,(1999), Chem. Lett. 385–386. DOI: https://doi.org/10.1246/cl.1999.385
Guo, J. and Al Dahan, M.H., 2004, “Liquid holdup and pressure drop in the gas liquid concurrent downflow packed bed reactor under elevated pressure”, Chem. Eng. Sci., 59, 5387-5393. DOI: https://doi.org/10.1016/j.ces.2004.07.106
Urseanu, M.I, Boelhouwer, J.G., Bosman, H.J.M., Schroijen, J.C. and Kwant, G., 2005, “Estimation of Trickle to pulse flow regime transition and pressure drop in high pressure trickle bed reactors with organic liquids”, Chem. Eng. Journal, 111, 5-11. DOI: https://doi.org/10.1016/j.cej.2005.04.015
Al-Naimi, S.A., Al-Sudani, F.T.J., Halabia, E.K.,(2001), “Hydrodynamics and flow regime transition study of trickle bed reactor at elevated temperature and pressure”, Chemical Engineering Research and Design, 1- 10.
Pradhan B.K., N.K., (1999) Sandle, Carbon 37, 1323-1332. DOI: https://doi.org/10.1016/S0008-6223(98)00328-5
Jin Zhang, Ying Tang, Jia-Qing Xie, Jian-Zhang Li, Wei Zeng and Chang- Wei Hu, (2005), J. Serb. Chem. Soc. 70(10) 1137–1146. DOI: https://doi.org/10.2298/JSC0510137Z
Eugenia M., Suarez-Ojeda, Frank Stuber, Agust Fortuny, Azael Fabregat, Julian Carrerac, Josep Font, (2007), Applied Catalysis B: Environmental,58,105-114. DOI: https://doi.org/10.1016/j.apcatb.2004.11.017
Quintanilla, A.F. Fraile, J.A. Casas, J.J.Rodr ́ıguez, (2007), “Phenol oxidation by a sequential CWPO–CWAO treatment with a Fe/AC catalyst”, Madrid. DOI: https://doi.org/10.1016/j.jhazmat.2007.04.060
Sharma A, Nakagawa H, Miura K., (2006), Fuel; 85:2396-401. DOI: https://doi.org/10.1016/j.fuel.2006.04.007