Benefaction and Pyrolysis of Sirnak Asphaltite and Lignite

Abstract

Depending on advanced technological developments in energy production the low quality coals needed the most economical technologies and even in order to make it possible to produce coal-derived products. Compliance with environmental norms of coal pyrolysis or gasification of various type of coals, feasible combustion systems and energy production facilities are needed in today's modern technology, also enable the production of liquid and gaseous coal fuels. However, raw materials and chemical nature of them requires a variety of adaptation methods. This study examined the high sulfur and ash types of Kütahya, Denizli, Aydin, Soma lignite, Sirnak asphaltite and lignite. The representative samples were taken from local areas of the lignites. Fundamentally, the conditions regarding better desulfurization way, the high quality pyrolysis lignite oil production, high value light oil, coal tar and gas products were determined at the goal of high fuel producing yield.

Share and Cite:

Tosun, Y. (2014) Benefaction and Pyrolysis of Sirnak Asphaltite and Lignite. International Journal of Clean Coal and Energy, 3, 13-18. doi: 10.4236/ijcce.2014.32002.

Conflicts of Interest

The authors declare no conflicts of interest.

References

[1] Anonymous (2009) TKI Lignite Report 2009, TC Energy Ministry Reports. Ankara, Türkiye.
[2] Anonymous (2009) TTK Coal Report 2009, TC Energy Ministry Reports. Ankara, Türkiye.
[3] Boynton, R.S. and Gutschick, K.A. (1983) Lime, Industrial Minerals and Rocks. AIME, New York
[4] Culfaz, M., Ahmet, M. and Gürkan, S. (1996) Removal of Mineral Matter and Sulfur from Lignites by Alkali Treatment. Fuel Processing Technology, 47, 99-109.
http://dx.doi.org/10.1016/0378-3820(96)01005-3
[5] Reimers, G.W. and Franke, D.W. (1991) Effect of Additives on Pyrite Oxidation, RI: 9353. Bureau of Mines, Washington DC.
[6] Tosun, Y.I., Rowson, N.A. and Veasey, T.J. (1994) Bio-Column Flotation of Coal for Desulfurization and Comparison with Conventional and Column Flotation. 5th International Conference of Mineral Processing, Nevçehir, 1994.
[7] Wheelock, T.D. (1979) Chemical Cleaning, Coal Preparation. 4th Edition, AIME, New York.
[8] Yoon, R.H. (1991) Advanced Coal Cleaning, Part 2, Coal Preparation. 5th Edition, AIME, Colorado.
[9] Donskoi, E. and McElwain, D.L.S. (1999) Approximate Modelling of Coal Pyrolysis. Fuel, 78, 825-835.
http://dx.doi.org/10.1016/S0016-2361(98)00204-X
[10] Wiktorsson, L.P. and Wanzl, W. (2000) Kinetic Parameters for Coal Pyrolysis at Low and High Heating Rates—A Comparison of Data from Different Laboratory Equipment. Fuel, 79, 701-716.
http://dx.doi.org/10.1016/S0016-2361(99)00138-6
[11] Fu, W.-B. and Wang, Q.-H. (2001) A General Relationship Between the Kinetic Parameters for the Gasification of Coal Chars with CO2 and Coal Type. Fuel Processing Technology, 72, 63-77.
http://dx.doi.org/10.1016/S0378-3820(01)00184-9
[12] Liu, G., Benyon, P., Benfell, K.E., Bryant, G.W., Tate, A.G. and Boyd R.K. (2002) The Porous Structure of Bituminous Coal Chars and Its Influence on Combustion and Gasification under Chemically-Controlled Conditions. Fuel, 79, 617-625.
http://dx.doi.org/10.1016/S0016-2361(99)00185-4

Copyright © 2023 by authors and Scientific Research Publishing Inc.

Creative Commons License

This work and the related PDF file are licensed under a Creative Commons Attribution 4.0 International License.