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Determining optimal conditions for lignite flotation by design of experiments and the halbich upgrading curve

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Języki publikacji
EN
Abstrakty
EN
In this study conditions for flotation of low rank coal (lignite of Tuncbilek, Turkey) were investigated in detail. The experiments were performed using the 3-variable 2-level (23) full factorial experimental design with four base point replicates, and the results were analyzed by the regression model, Fischer test (F-test) and Halbich’s upgrading curve for the responses of ash content (or combustible matter grade) and the combustible matter recovery. The results obtained from the analysis indicated that while every factor considerably affected the combustible matter recovery, both collector (kerosene) and frother (AF65) significantly influenced the ash contents of the carbonaceous matter products. The only effective mutual interaction influencing recovery was caused by the kerosene-aeration interaction, while the interaction of kerosene-aeration and kerosene-AF65 and interactions of all factors (kerosene-AF65-aeration) were significant for the ash content of the products. Basing on the grade–recovery Halbich upgrading curve, regression model and a criterion for optimum of flotation results, it was found that a coal product with combustible matter grade of 91.09% and 71% combustible matter recovery can be obtained provided that it is processed at the higher level of kerosene (3 kg/Mg), higher level of frother AF65 (40 ppm) and lower aeration rate level of (0.16 cm/s).
Rocznik
Strony
535--546
Opis fizyczny
Bibliogr. 23 poz., rys., tab.
Twórcy
autor
  • Dumlupinar University, Department of Mining Engineering, Kutahya, Turkey, Tel.: +90 537 3862002; Fax.: +90 274 2652066
Bibliografia
  • 1. AKDEMİR Ü., SÖNMEZ İ., 2003. Investigation of coal and ash recovery and entrainment in flotation, Fuel Processing Technology, 82, 1–9.
  • 2. AKTAS Z., WOODBURN E.T., 1995. The effect of non-ionic reagent adsorption on the froth structure and flotation performance of two low rank British coal. Powder Technology, 83,149–158.
  • 3. APLAN FF., 1976. Flotation, In: Fuerstenau MC, editor. AM Gaudin memorial volume. New York: AIME, 1235–64. (From the paper of Yakup Cebeci (2002))
  • 4. ATESOK G., BOYLU F., ÇELİK M.S., 2001. Carrier flotation for desulfurization and deashing of difficult-to-float coals, Minerals Engineering, 14, 661–670.
  • 5. BOX G.E.P., HUNTER W.G., HUNTER J.S., 1978. Statistics for Experiments.Wiley, New York.
  • 6. CEBECİ Y., 2002. The investigation of the floatability improvement of Yozgat Ayrıdam lignite using various collectors. Fuel, 81, 281–289.
  • 7. DRZYMALA J., 2006. Atlas of upgrading curves used in separation and mineral science and technology Part I, Physico-chemical Problems in Mineral Processing, 40, 19–29.
  • 8. DRZYMALA J., 2007. Atlas of upgrading curves used in separation and mineral science and technology Part II, Physico-chemical Problems in Mineral Processing, 41, 27–35.
  • 9. DRZYMALA J., KOWALCZUK P.B., FOSZCZ D., MUSZER A., HENC T., LUSZCZKIEWICZ A., 2012. Analysis of separation results by means of the grade-recovery Halbich upgrading curve, XXVI International Mineral Processing Congress, September 20–24.
  • 10. EVANS G.M., ATKINSON B., JAMESON G.J., 1995, The Jameson Cell. Flotation Science and Engineering, ed. Matis K.A., Marcel Dekker Inc., 331‒363.
  • 11. GÜLEN J., TOPRAK S., PİŞKİN S., 2012. Batıkömürlerineaitbazıkarakteristiközellikler, Karaelmas Science and Engineering Journal, 1, 27–33, Turkey.
  • 12. JIA R., HARRIS G.H., FUERSTENAU D.W., 2000. An improved class of universal collectors for the flotation of oxidized and/or low-rank coal, International Journal of Mineral Processing, 58, 99–118.
  • 13. KELEBEK Ş., DEMIR U., SAHBAZ O., UCAR A., CINAR M., KARAGUZEL C., OTEYAKA B., 2008. The effects of dodecylamine, kerosene and pH on batch flotation of Turkey's Tuncbilek coal, Int. Journal of Mineral Processing, 88, p65–71.
  • 14. KELLY E.G., SPOTTISWOOD D. J., 1982. Introduction to Mineral Processing, Wiley, New York
  • 15. KOWALCZUK P. B., SAHBAZ O., DRZYMALA J., 2011, Maximum size of floating particles in different flotation cells, Minerals Engineering, 24, 766–771.
  • 16. LASKOWSKİ J.S., TLHONE T., WILLIAMS P., DING K., 2003. Fundamental Properties of the polyoxypropylene alkyl ether flotation frothers, International Journal of Mineral Processing, 72, 289–299.
  • 17. MELO F., 2005.Fundemental Properties of flotaiton frothers and their effect on flotation, Master of Applied Science Thesis, The University of British Columbia, Canada.
  • 18. MOHANTY M.K., HONAKER R.Q., 1999. A comperative evaluation of the leading advanced flotation technologies. Minerals Engineering, 12, 1–13.
  • 19. NAIK P., REDDY P.S.R., MISRA N., 2004. Optimization of coal flotation using statistical technique, Fuel Processing Technology, 85, 1473–1485.
  • 20. NAIK, P., P.S.R. REDDY and N. MISRA, 2005. Interpretation of interaction effects and optimization of reagent dosages for fine coal flotation, International Journal of Mineral Processing, 75, p. 83–90.
  • 21. POLAT M., POLAT H., CHANDER S., 2003. Physical and chemical interactions in coal flotation, International journal of Mineral Processing, 72, 199–213.
  • 22. ŞAHBAZ O., UCAR A., OTEYAKA B., 2013.Velocity gradient and maximum floatable particle size in the Jameson cell. Minerals Engineering, 41, 79–85.
  • 23. VAPUR H., BAYAT O., UÇURUM M.,, 2010. Coal flotation optimization using modified flotation parameters and combustible matter recovery in a Jameson cell. Energy Conservation and Management, 51, 1891–1897. LY E.G., SPOTTISWOOD D. J., 1982. Introduction to Mineral Processing, Wiley, New York
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-ba68394f-2e15-4945-a088-9b37473c0ecd
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