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Transient one-dimensional model of coal carbonization in a stagnant packed bed

Treść / Zawartość
Identyfikatory
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
In the present paper, the one-dimensional model for heat and mass transfer in fixed coal bed was proposed to describe the thermal and flow characteristics in a coke oven chamber. For the purpose of the studied problem, the analysis was limited to the calculations of temperature field and pyrolytic gas yield. In order to verify the model, its theoretical predictions for temperature distribution during wet coal charge carbonization were compared with the measurement results found in the literature. In general, the investigation shows good qualitative agreement between numerical and experimental data. However, some discrepancy regarding the temperature characteristics at the stage of evaporation was observed.
Rocznik
Strony
39--51
Opis fizyczny
Bibliogr. 17 poz., il.
Twórcy
  • The Szewalski Institute of Fluid-Flow Machinery, Polish Academy of Sciences, Fiszera 14, 80-231 Gdansk, Poland
autor
  • The Szewalski Institute of Fluid-Flow Machinery, Polish Academy of Sciences, Fiszera 14, 80-231 Gdansk, Poland
autor
  • The Szewalski Institute of Fluid-Flow Machinery, Polish Academy of Sciences, Fiszera 14, 80-231 Gdansk, Poland
autor
  • Institute for Chemical Processing of Coal, Zamkowa 1, 41-803 Zabrze, Poland
  • The Szewalski Institute of Fluid-Flow Machinery, Polish Academy of Sciences, Fiszera 14, 80-231 Gdansk, Poland
Bibliografia
  • [1] Kasperczyk J., Simonis W.: Die hochtemperaturverkokung von steinkohle im horizontalkammerofen bei schüttbetrieb als temperatur-zeit-reaktion. Glauckauf- Forschungshefte 32(1971), 23-34.
  • [2] Witos J., Byrtus F.: Determination of transient temperature field in a coke oven chamber in case of compacted coal charge by means of direct measurement and numerical calculations. Koks, smoła, gaz 1979, 212-219 (in Polish).
  • [3] Atkinson B., Merrick D.: Mathematical models of thermal decomposition of coal. 4. Heat transfer and temperature profiles in a coke-oven charge. Fuel 62(1983), 553-561.
  • [4] Merrick D.: Mathematical models of the thermal decomposition of coal: 2. Specific heats and heats of reaction. Fuel 62(1983), 540-546.
  • [5] Merrick D.: Mathematical models of the thermal decomposition of coal: 3. Density, porosity and contraction behaviour. Fuel 62(1983), 547-552.
  • [6] Tomeczek J., Palugniok H.: Specific heat capacity and enthalpy of coal pyrolysis at elevated temperatures. Fuel 75(1996), 1089-1093.
  • [7] Suuberg E.M.: The significance of transport effects in determining coal pyrolysisrates and yields. ACS Division of Fuel Chemistry (Preprint), New Orleans, 32(1987), (3), 51-58.
  • [8] Bien A.S., Phillips O., Wolkstein M.: Thermal conductivity of carbonaceousbriquettes. Proc. ACS Symposium on preparation and properties of coals, 4(1960), (2), 81-86.
  • [9] Nomura S., Arima T.: Coke shrinkage and coking pressure during carbonizationin a coke oven. Fuel 79(2000), 1603-1610.
  • [10] Stelmach S., Kardaś D., Polesek-Karczewska S.: Experimental verification of the non-Fourier model of heat transfer within coke oven charge. Karbo 3(2011), 156-165 (in Polish).
  • [11] Siegel R., Howell J.: Thermal Radiation Heat Transfer. Taylor Francis, London 1992.
  • [12] Anderson D.A., Tannehill J.C., Pletcher R.H.: Computational fluid mechanic sand heat transfer. Hemisphere Publishing Company, 1984.
  • [13] Polesek-Karczewska: Comparative Analysis of the Gasification Kinetics of Different Types of Biomass and Fossil Fuels. Rep. IFFM PASci 141/2008 Gdansk 2008 (in Polish).
  • [14] Postrzednik S.: Solid fuel carbonization - method of determination, basic relations. Karbo, Energochemia, Ekologia 39(1994), (9), 220-228 (in Polish).
  • [15] Alvarez R.,Pis J.J., Diez M.A., Barriocanal C., Menendez J.A., Casal M.D., Parra J.B.: Carbonization of wet and preheated coal. Effect on coke quality and its relation with textural properties. J. Anal. Appl. Pyrol. 79(1996), 1603-1610.
  • [16] Amamoto K.: Coke strength development in the coke oven. 1. Influence of maximum temperature and heating rate. Fuel 76(1997), 17-21.
  • [17] Kardas D., Polesek-Karczewska S. Mertas B.: Modelling of temperature distribution in a coke oven. Karbo 3(2009), 151-155 (in Polish).
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-99d4169b-6d14-4163-b99f-23ff61795e82
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