Evaluation of the Inverse Fluidized Bed Biological Reactor for Treating High-Strength Industrial Wastewaters
Włodzimierz Sokół, Belay Woldeyes
DOI: 10.4236/aces.2011.14034   PDF   HTML     5,150 Downloads   9,968 Views   Citations


The aim of this work was to investigate the aerobic degradation of high-strength industrial (refinery) wastewaters in the inverse fluidized bed biological reactor, in which polypropylene particles of density 910 kg/m3 were fluidized by an upward flow of gas through a bed. Measurements of chemical oxygen demand (COD) versus residence time t were performed for various ratios of settled bed volume to reactor volume (Vb/VR) and air velocities u. The largest COD reduction, namely, from 54,840 to 2,190 mg/l, i.e. a 96% COD decrease, was achieved when the reactor was operated at the ratio (Vb/VR) = 0.55, air velocity u = 0.046 m/s and t = 65 h. Thus, these values of (Vb/VR), u and t can be considered as the optimal operating parameters for a reactor when used in treatment of high-strength refinery wastewaters. In the treatment operation conducted in a reactor optimally controlled at (Vb/VR) = 0.55, u = 0.046 m/s and t = 65 h, the conversions obtained for all phenolic constituents of the wastewater were larger than 95%. The conversions of about 90% were attained for other hydrocarbons.

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W. Sokół and B. Woldeyes, "Evaluation of the Inverse Fluidized Bed Biological Reactor for Treating High-Strength Industrial Wastewaters," Advances in Chemical Engineering and Science, Vol. 1 No. 4, 2011, pp. 239-244. doi: 10.4236/aces.2011.14034.

Conflicts of Interest

The authors declare no conflicts of interest.


[1] W. Sokól and W. Korpal, “Aerobic Treatment of Wastewaters in the Inverse Fluidised Bed Biofilm Reactor,” Chemical Engineering Journal, Vol. 118, No. 3, 2006, pp. 199-205. doi:10.1016/j.cej.2005.11.013
[2] W. Sokól, “Operational Range for a Gas-Liquid-Solid Fluidized Bed Aerobic Biofilm Reactor with a Low- Density Biomass Support,” International Journal of Chemical Reaction Engineering, Vol. 8, 2010, Article ID: A111. http://www.bepress.com/ijcre/vol8/A111
[3] W. Sokól, A. Ambaw and B. Woldeyes, “Biological Wastewater Treatment in the Inverse Fluidised Bed Reactor,” Chemical Engineering Journal, Vol. 150, No. 1, 2009, pp. 63-68. doi:10.1016/j.cej.2008.12.021
[4] P. Hüppe, H. Hoke and D. C. Hempel, “Biological Treatment of Effluents from a Coal Tar Refinery Using Immobilized Biomass,” Chemical Engineering Technology, Vol. 13, No. 1, 1990, pp. 73-79. doi:10.1002/ceat.270130110
[5] A. Alvarado-Lassman, E. Rustrian, M. A. Garcia- Alvarado, G. C. Rodriguez-Jimenez and E. Houbron, “Brewery Wastewater Treatment Using Anaerobic Inverse Fluidized Bed Reactors,” Bioresource Technology, Vol. 99, 2008, pp. 3009-3015. doi:10.1016/j.biortech.2007.06.022
[6] M. Bajaj, C. Gallert and J. Winter, “Biodegradation of High Phenol Containing Synthetic Wastewater by an Aerobic Fixed Bed Reactor,” Bioresource Technology, Vol. 99, No. 17, 2008, pp. 8376-8381. doi:10.1016/j.biortech.2008.02.057
[7] A. Lohi, M. Aivarez-Cuenca, G. Anania, S. R. Upreti and L. Wan, “Biodegradation of Diesel Fuel-Contaminated Wastewater Using a Three-Phase Fluidized Bed Reactor,” Journal of Hazardous Materials, Vol. 154, No. 1-3, 2008, pp. 105-111. doi:10.1016/j.jhazmat.2007.10.001
[8] M. Rajasimman and C. Karthikeyan, “Aerobic Digestion of Starch Wastewater in a Fluidized Bed Bioreactor with Low Density Biomass Support,” Journal of Hazardous Materials, Vol. 143, No. 1-2, 2007, pp. 82-86. doi:10.1016/j.jhazmat.2006.08.071
[9] N. Fernandez, S. Montalvo, R. Borja, L. Guerrero, E. Sanchez, I. Cortes, M. F. Comenarejo, L. Traviso and F. Raposo, “Performance Evaluation of An Anaerobic Fluidized Bed Reactor With Natural Zeolite as Support Material When Treating High-Strength Distillery Wastewater,” Renewable Energy, Vol. 33, No. 11, 2008, pp. 2458- 2466. doi:10.1016/j.renene.2008.02.002
[10] P. A. Fitzgerald, “Comprehensive Monitoring of a Fluidized Bed Reactor for Anaerobic Treatment of High Strength Wastewater,” Chemical Engineering Science, Vol. 51, No. 11, 1996, pp. 2829-2834. doi:10.1016/0009-2509(96)00160-1
[11] R. Sowmeyan and G. Swaminathan, “Evaluation of Inverse Anaerobic Fluidized Bed Reactor for Treating High Strength Organic Wastewater,” Bioresource Technology, Vol. 99, No. 9, 2008, pp. 3877-3880. doi:10.1016/j.biortech.2007.08.021
[12] R. Sowmeyan and G. Swaminathan, “Performance of Inverse Anaerobic Fluidized Bed Reactor for Treating High Strength Organic Wastewater During Start-Up Phase,” Bioresource Technology, Vol. 99, No. 14, 2008, pp. 6280-6284. doi:10.1016/j.biortech.2007.12.001
[13] W. Sokól and M. R. Halfani, “Hydrodynamics of a Gas-Liquid-Solid Fluidized Bed Bioreactor with a Low Density Biomass Support,” Biochemical Engineering Journal, Vol. 3, No. 3, 1999, pp. 185-192. doi:10.1016/S1369-703X(99)00016-9
[14] D. G. Karamanev, T. Nagamune and K. Endo, “Hydrodynamics and Mass Transfer Study of a Gas-Liquid-Solid Draft Tube Spouted Bed Bioreactor,” Chemical Engi- neering Science, Vol. 47, No. 13-14, 1992, pp. 3581- 3588. doi:10.1016/0009-2509(92)85073-K
[15] B. Rusten, H. Odegaard and A. Lundar, “Aerobic Treatment of Wastewaters in a Novel Biological Reactor,” Water Science and Technology, Vol. 26, 1992, pp. 703- 708.
[16] W. Verstraete and E. van Vaerenbergh, “Aerobic Activated Sludge“, In: W. Schonborn, Ed., Biotechnology, Vol. 8, VCH Verlagessellschaft mbH, Weinheim, 1986, pp. 43-112.

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