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In the article the analysis of issues of modelling of coal particle combustion in a fluidized bed was carried out. Moreover, the results of the validation of a new proposition of a mathematical model of single char particle combustion in a fluidized bed were presented in the paper. This model takes account of the mass loss resulting from the contact of the bed particle with the surface of a burning char particle. In the opinion of many authors, the contact of inert material with a char particle causes their fragmentation which in some conditions of combustion and hydrodynamics of bed leads to the elutriation of unburnt fine particles from the combustion chamber increasing the incomplete loss of combustion. During the model validation the mechanical coal properties i.e. Vickers hardness and fracture toughness were taken into account as presented in [2]. The wide range of experimental tests, on which basis of which the model validation allowed the determination of the possibility of the model application to predict a combustion rate in fluidized bed conditions, as well as the contribution of the erosion process to the total mass loss. It also indicated that the main reason for combustion intensification in the fluidized bed is the clearance (elimination) of ash from the surface of the burning char and the increase of mass transfer coefficient in the particle region.
Słowa kluczowe
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Tom
Strony
65--74
Opis fizyczny
Bibliogr. 15 poz., rys.
Twórcy
autor
- Czestochowa University of Technology Department of Thermal Machinery Armii Krajowej 21, 42-201 Czestochowa, Poland
Bibliografia
- [1] Pelka P. Modelling of mass loss of char particle during combustion on flow of inertmaterial. Fuel 90, 2011, 932.
- [2] Pelka P. Evolution of the structure and mechanical strength of coal particle during combustion in the atmosphere of air and the mixture oxygen and carbon dioxide. Arch. Min. Sci. 58 (3), 2013, 637.
- [3] Basu P. Combustion and Gasification In Fluidized Beds. Taylor & Francis Group. 2006.
- [4] Halder P. K., Ph.D Thesis. Combustion of single coal particles in circulating fluidized bed, Technical University of Nova Scotia, 1989.
- [5] Pillai K. K. The influence of coal type on devolatilization and combustion in fluidized beds. Journal of Institute of Energy, 54, 1981, 144.
- [6] Sekret R.. Warunki cieplno-przepływowe i emisje zanieczyszczeń w kotłach z cyrkulacyjną warstwą fluidalną dużej mocy, Roprawa habilitacyjna, Poliechnika Śląska, zeszyty naukowe nr.1694, Gliwice, 2005.
- [7] Pełka P. Erozja ziaren węgla spalanych w cyrkulacyjnej warstwie fluidalnej, monografie nr 276, Wydawnictwo Politechniki Częstochowskiej, 2014.
- [8] Basu P. and Fraser S. A. Circulating Fluidized Bed Boilers. Butterworth, Heinemann, USA, 1991.
- [9] Tomeczek J. Spalanie węgla, Skrypty uczelniane Politechniki Śląskiej, nr 1667, Gliwice, 1992.
- [10] Hoy H.R., Gill D.W. Combustion in Industrial Boilers, ed. Lund, 532, 1988.
- [11] Chirone R., Massimilla L., Salatino P. Comminution of Carbons in Fluidized Bed Combustion. Prog. Energy Combustion Sci. 17, 1991, 297.
- [12] Basu P. Combustion of coal in circulating fluidized-bed boilers: a review. Chem. Engng Sci. 54, 1999, 5547.
- [13] Basu P., Halder P. K. Combustion of single carbon particles in a fast fluidized bed of fine solids. Fuel 68, 1989, 1056.
- [14] Donsi G., Massimila L. and Miccio M. Carbon fines production and elutriation from the bed of fluidized bed combustor, Combust. Flame 41, 1981, 57.
- [15] Pelka P. Analysis of a coal particle mass loss burning in flow of inert material. Combust. Flame 156, 2009, 1604.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-b5b3659a-9412-419d-80ad-b98492d188af
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