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2014 | 16 | 2 | 74-76

Article title

Carbon Shale Combustion in the Fluidized Bed Reactor

Content

Title variants

Languages of publication

EN

Abstracts

EN
The purpose of this article is to present the possibilities of coal shale combustion in furnaces with bubbling fluidized bed. Coal shale can be autothermally combusted in the fluidized bed, despite the low calorie value and high ash content of fuel. Established concentrations of CO (500 ppm) and VOC (30 mg/m3) have indicated a high conversion degree of combustible material during combustion process. Average concentrations of SO2 and NOx in the flue gas were higher than this received from the combustion of high quality hard coal, 600 ppm and 500 ppm, respectively. Optional reduction of SO2 and NOx emission may require the installation of flue gas desulphurization and de-NOx systems.

Publisher

Year

Volume

16

Issue

2

Pages

74-76

Physical description

Dates

online
26 - 6 - 2014

Contributors

  • Cracow University of Technology, Faculty of Environmental Engineering, Institute of Thermal Engineering and Air Protection, Warszawska 24, 31-155 Cracow, Poland
  • Cracow University of Technology, Faculty of Environmental Engineering, Institute of Thermal Engineering and Air Protection, Warszawska 24, 31-155 Cracow, Poland
  • Cracow University of Technology, Faculty of Environmental Engineering, Institute of Thermal Engineering and Air Protection, Warszawska 24, 31-155 Cracow, Poland
  • Cracow University of Technology, Faculty of Chemical Engineering and Technology, Institute of Inorganic Chemistry and Technology, Warszawska 24, 31-155 Cracow, Poland
author
  • Cracow University of Technology, Faculty of Chemical Engineering and Technology, Institute of Inorganic Chemistry and Technology, Warszawska 24, 31-155 Cracow, Poland

References

  • 1. Klank, M. (2010). The future of coal – a new look at its use, Energy Policy, 10(1), 41–49 (in Polish).
  • 2. Kandefer, S. (1989). Fluidized bed combustion of low-grade fuels and waste, Cracow: Cracow University of Technology Publisher, (in Polish).
  • 3. Baron, J., Bulewicz, E.M., Kandefer, S., Pilawska, M. & Żukowski, W. (2006). Environmentally-friendly Use of Waste Biomass in Protected Areas. Environ. Prot. Eng. 32 (1), 35–40.
  • 4. Porzuczek, J. (2012). Optimization of the fluidized bed boilers operation in nonstationary states. Cracow: Cracow University of Technology Publisher, monograph No. 405 (in Polish).
  • 5. Kandefer, S., Juryś, C., Bulewicz, E.M., Dyczewski, R. & Dyśko, J. (1989). Patent Republic of Poland No. 164249. Patent Office of Republic of Poland.
  • 7. Polish Committee for Standardization. (1980). Polish standard: Solid fuels. Determination of moisture content. PNG-04511:1980. Warsaw.
  • 8. Polish Committee for Standardization. (2011). Polish standard: Characterization of waste – Determination of loss on ignition of the waste, sludge and sediments. PN-EN-15169:2011. Warsaw.
  • 9. Polish Committee for Standardization. (1980). Polish standard: Solid fuels. Determination of ash by weight. PN-G-04512:1980. Warsaw.
  • 10. Żukowski, W., Baron, J., Kowarska, B. & Zabagło, J. (2010). N2O conversion in active and chemically inert fluidized bed. Environ. Prot. Eng. 36(3), 15–32. http://epe.pwr.wroc. pl/2010/zukowski_3-2010.pdf
  • 11. Anthony, E.J. & Granatstein, D.L. (2001). Sulfation phenomena in fluidized bed combustion systems. Progress in Energy and Combustion Science, 27 (2), 215–236. DOI:10.1016/ S0360-1285(00)00021-6.[Crossref]

Document Type

Publication order reference

Identifiers

YADDA identifier

bwmeta1.element.-psjd-doi-10_2478_pjct-2014-0033
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