Supercritical Water Oxidation for Toxic Organic Wastewater Disposal
Keywords:
Industrial status of SCWO, industrial wastewater, supercritical water oxidation (SCWO), toxic wastewater treatment
Abstract
The destruction of toxic organic wastewaters from munitions demilitarization and complex industrial chemicals clearly becomes an overwhelming problem if left to conventional treatment processes. Two options, incineration and supercritical water oxidation (SCWO), exist for the complete destruction of toxic organic wastewaters. Incinerator, on the one hand, has associated problems such as very high cost and public resentment; SCWO, on the other hand, has proven to be a very promising method for the treatment of various types of wastewaters with its extremely efficient organic waste destruction of 99.99% with none of the emissions associated with incineration. In this review, the concepts of SCWO, the results of and present perspectives on its applications, as well as the industrial status of SCWO are critically examined and discussed.References
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2. Bianchetta,S., U, L., and Gloyna, E. E (1999). "Supercritical water oxidation of methylphosphonicacid,"Ind Eng.Chern. Res.,38, 2902-2910.
3. Boock,L.T.(1996). A quantitative analysis of reactions in supercritical water: Experimental kinetics and mechanistic modeling, Ph.D. Dissertation, The University of Delaware.
4. Brunner, G. D. (1994). "Extraction and destruction of waste with supercritical water,"In Kiran, E., and Sengers, J. M. H. L., eds., Supercritical fluids, Kluwer Academic 697-705. Publisher, the Netherlands.
5. Croiset,E., Rice,S. E, and Hanush, RG. (1997). "Hydrogen peroxide decomposition in supercritical 2343-2352. water," AIChE J. 43, 9,
6. Downey,K W., Snow, R H., Hazlebeck,D. A, and Roberts,A J. (1995)."Corrosionand chemical agent destruction: Research on supercritical water oxidation of hazardous military wastes," Chapter 21, In Hutchenson, K W.,and Foster, N. R, eds., Innovation in supercritical fluids science and technology,ACS Symposium Series #608, American Chemical Society,Washington,D.C.
7. Fang, Z., Xu, S. K, and Kozinski,J. A (2000). "Behavior of metals during combustion of industrial organic wastes in supercritical water," Ind. Eng. Chern. Res., 39, 4536-4542.
8. Fang,Z.,Xu,S. K, Smith,Jr., R L.,Arai,K, and Kozinski,J. A. (2005). "Destruction of deca-chlorobiphenyl in supercritical water under oxidizing conditions with and without Na2C03," J. Supercrit. Fluids,33,247-258.
9. Goto, M., Nada, T., Kodama, A., and Hirose, T. (1999). "Kinetic analysis for destruction of municipal sewage sludge and alcohol distillery waste water by supercritical water oxidation," Ind. Eng. Chern.Res., 38, 1863-1865.
10. Killilea, W. R., and Swallow, K. C. (1992). "The fate of nitrogen in supercritical- water oxidation," J. Supercrit. Fluids., 5, 72-78.
11. Kritzer,P, and Dinjus,E. (2001). "Anassessment of supercritical water oxidation (SCWO): Existing problems,possible solutions and new reactor concepts," Chern. Eng. J., 83, 207-214.
12. Kronholm,J., Kuosmanen,T.,Hortonen, K.,and Riekkola,M.-L. (2003). "Destruction of PAHsfrom soil by using pressurized hot water extraction coupled with supercritical water oxidation," Waste Management,23, 253-260.
13. Lee, H.-C., In, J.-H., Hwang, K..:v.,and Lee, C.- H. (2004). "Decomposition of ethylenediaminetetraacetic acid by supercriticalwater oxidation," Ind. Eng. Chern.Res., 43,3223-3227.
14. Li, L., Generalized Chen, P, and kinetic Gloyna, model E. F. for (1991). wet oxidation of organic compounds, AIChE J., 37, 11, 1687-1697.
15. Modell,M.(1989)."Superciticalwateroxidation," In Freeman, H. M., ed., Standard handbook of hazardous waste treatment and disposal,McGraw-Hill,New York.
16. Phenix, B. D., DiNaro, J. L., Tester, J. W., Howard, J. B., and Smith, K.A. (2002). "The effectof mixingand oxidant choice on laboratory-scale measurements of supercritical water oxidation kinetics," Ind. Eng. Chern.Res.,41, 624-631.
17. Rice,S. E, and Steeper, R R (1998). "Oxidation rates of common organic compounds in supercritical water," J. Hazard. Mater., 59, 261-278.
18. Savage, P E., Gopalan, S., Mizan,T. I., Martino, C. J., and Brock,E. E. (1995). "Reactions at supercritical conditions: Application and fundamentals," AIChE J., 41, 7, 1723-1778.
19. Schmieder,H., and Abeln,J. (1999)."Supercritical water oxidation:State of the art," Chern. Eng. Technol,22, 11,903-908.
20. Sullivan, P A., and Tester, J. W. (2004). "Methylphosphonic acid oxidation kineticsin supercriticalwater,"AIChEJ., 50,3, 673-683.
21. Tester,J. W., Holgate, H. R, Armellini,F.J., Webley,P A., Killilea,W.R, Hong, G. T., and Barner, H. T. (1993). Supercritical water oxidation technology: A review of process development and fundamental research, Chapter 3, In Tedder, D. W., and Pohl'and, F. G., eds., Emerging technologies in hazardous waste management III,ACSSymposiumSeries #518, American Chemical Society, Washington, D. C.
22. Thomason, T. B., and Modell, M. (1984). "Supercritical water destruction of aqueous wastes," Hazardous Waste,1,4, 453-467.
23. Veriansyah,B., Kim,J.-D., Lee, J.-C., and Lee, Y.-W.(2005). "OPA oxidation rates in supercritical water," J. Hazard. Mater. B124, 119-124.
Published
2006-12-31
How to Cite
Veriansyah, B., Prabowo, B., & Kim, J. D. (2006). Supercritical Water Oxidation for Toxic Organic Wastewater Disposal. ASEAN Journal of Chemical Engineering, 6(1), 36-43. Retrieved from https://dev.journal.ugm.ac.id/v3/AJChE/article/view/7657
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