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Experimental Measuring and CFD Modeling of Pulverized Coal Burnout in Drop Tube

Identyfikatory
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
An experimental facility and methodology of pulverized coal thermokinetic properties determination with the use of mathematical modeling is described in this paper. Thermokinetic properties as a mean for better understanding the nature of combustion process can be determined by an experiment using a Drop Tube Test Facility (DTTF). The test provides conditions occurring in a pulverized coal fired boiler by emulated oxygen concentration, temperature and reaction gas speed. The test presented in the paper was built recently at the Energy Research Center. Experimental data acquired from the tests are used in mathematical modeling using the code Fluent. The ANSYS Fluent 12.1 code can define different mathematical models of volatile evolution (devolatilization model) and char combustion (kinetic/diffusion surface reaction rate model) to simulate coal combustion. In this paper, a char combustion model is defined with specification of a basic equation for char combustion reaction rate. Resulting values are evaluated by decrease of pulverized coal char in the drop tube in dependence of time. The process of burnout is evaluated for comparison with experimental tests. Results acquired from the adjusted mathematical model should provide more detailed information about the combustion process in a real operation.
Rocznik
Strony
193--201
Opis fizyczny
Bibliogr. 6 poz., rys., tab.
Twórcy
autor
autor
autor
  • Energy Research Center of VSB-Technical University of Ostrava, 17. listopadu 15/2172, 708 33 Ostrava-Poruba, Czech Republic, radim.paluska@vsb.cz
Bibliografia
  • [1] Frenkel J., J., Viscous Flow of Crystalline Bodies Under the Action of Surface Tension, Journ. Phys. (Moscow) 9, 385 (1945)
  • [2] Raask E., Sintering characteristics of coal ashes by simultaneous dilatometry-electrical conductance measurements, Journal of Thermal Analysis, 16 (1979) 91-102
  • [3] Ahn Y.C., Lee J.K., Physical, chemical and electrical analysis of aerosol particles generated from industrial plants, Aerosol Science 37 (2006) 187-202
  • [4] Al-Otoom, A.Y., Elliott L.K., Wall T.F., Monghtaderi B., Measurement of the sintering kinetics of coal ash, Energy&Fuels 14 (2000) 994-1001
  • [5] Nutalapati D., Gupta R., Moghtaderi B., Wall T.F., Assessing slagging and fouling during biomass combustion: A thermodynamic approach allowing for alkali/ash reactions, Fuel processing 88 (2007) 1044-1052
  • [6] Zevenhoven-Onderwater M., Backam R., Bengt-Johan Skifvars, Hupa M., The ash chemistry in fluidised bed gasification of biomass fuels. Part I: predicting the chemistry of melting ashes and ash-bed material interaction, Fuel 80 (2001) 1489-1502
  • [7] Bengt-Johan Skifvars, Backam R., Hupa M, Characterization of the sintering tendency of ten biomass ashes in FBC conditions by a laboratory test and by phase equilibrium calculations, Fuel processing Technology 56 (1998) 55-67
  • [8] Fryda L.E., Panopoulos K.D., Kakaras E., Agglomeration in fluidised bed gasification of biomass, Powder technology 181 92008) 307-320
  • [9] Blander M., Milne T.A., Dayton D.C., Backman R., Blake D., Kuhnel V., Liniak W., Nordin A., Ljung A., Equilibrium chemistry of biomass combustion: A Round-Robin set of calculations using available computer programs and databases, Energy&Fuels 15 (2001) 344-349
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BWM4-0030-0042
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