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Reduction of carbon dioxide emission using adsorption - desorption cycles in a fluidised bed reactor

Wybrane pełne teksty z tego czasopisma
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Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
The paper discusses the possibility of applying the reversible reaction CaCO3 - CaO + CO2 in cyclic capture and release of CO2 directly inside a fluidised bed combustor. This would cause lowering CO2 emissions to the atmosphere, thanks to obtaining energy from burning fossil fuels. Observations made on the effect of introducing an additional external stream of CO2 on the efficiency of the chemical capture process are described. It is implied that CO2 derived from the fuel can be temporarily retained within the bed to be released later at a higher concentration. The proposed method of burning fuel in a chemically active fluidised bed could be an available method leading to CO2 isolation from flue gases and to its eventual sequestration.
Rocznik
Strony
47--56
Opis fizyczny
Bibliogr. 14 poz.
Twórcy
autor
autor
autor
autor
autor
  • Faculty of Chemical Engineering and Technology, Cracow University of Technology, ul. Warszawska 24, 31-155 Kraków, pczukows@pk.edu.pl
Bibliografia
  • [1] AVEDESIAN M.M., DAVIDSON J.F., Combustion of carbon particles in a fluidised bed, Trans. I. Chem. E., 1973, 51, 121–131.
  • [2] DENNIS J., HAYHURST A.N., MACKLEY I.G., The Ignition and Combustion of Propane/Air Mixtures in a Fluidised Bed, 17th Symposium (Int.) on Combustion, The Comb. Inst., Pittsburgh, 1982, 1205–1212.
  • [3] HAYHURST A.N., Does carbon monoxide burn inside a fluidized bed? A new model for the combustion of coal char particles in fluidized beds, Combust. Flame, 1991, 85, 155–168.
  • [4] HESKETH R.P., DAVIDSON J.F., Combustion of methane and propane in an incipiently fluidized bed, Combust. Flame, 1991, 85, 449–467.
  • [5] STUBINGTON J.F., CLOUGH S.J., The combustion rate of volatiles in a fluidized bed combustor, 14th Int. Fluidized Bed Conf., Vancouver, Ed. F.D.S. Preto, ASME, New York, 1997, Vol. 2, 1111–1122.
  • [6] ŻUKOWSKI W., The pressure pulses generated by the combustion of natural gas in bubbling fluidized beds, Combust. Flame, 2001, 130, 15–26.
  • [7] ŻUKOWSKI W., BARON J., KOWARSKA B., ZABAGŁO J., N2O conversion in active and chemically inert fluidized bed, Environment Protection Engineering, 2010, 36 (3), 15–32.
  • [8] PILAWSKA M., BARON J., ŻUKOWSKI W., Combustion of Aromatics and Esters in an Atmospheric Bubbling FBC, in Comparison with that of Natural Gas, 7th Int. Conf. on Energy for a Clean Environment, Lisbon, Portugal, 2003, paper 36.3.
  • [9] BULEWICZ E.M., ŻUKOWSKI W., KANDEFER S., PILAWSKA M., Flame flashes when bubbles explode during the combustion of gaseous mixtures in a bubbling fluidized bed, Combust. Flame, 2003, 132, 319–327.
  • [10] BARON J., BULEWICZ E.M., KANDEFER S., PILAWSKA M., ŻUKOWSKI W., HAYHURST A.N., The combustion of polymer pellets in a bubbling fluidised bed, Fuel, 2006, 85, 2494–2508.
  • [11] ŻUKOWSKI W., BARON J., BŁASZCZYK-PASTECZKA A., KANDEFER S., OLEK M., Efekty spalania propanu w inertnym i aktywnym chemicznie złożu reaktora fluidyzacyjnego, Przem. Chem., 2008, 87, 2, 214–218.
  • [12] ŻUKOWSKI W., ENGLOT S., BARON J., KANDEFER S., OLEK M., Wykorzystanie procesów kalcynacji i karbonizacji złoża wapiennego w palenisku fluidalnym do oddzielenia CO2 ze spalin, Termodynamika w nauce i gospodarce, 2008, T. II, 668–675.
  • [13] ŻUKOWSKI W., ENGLOT S., BARON J., KANDEFER S., OLEK M., Reduction of carbon dioxide emission through the sorption in situ using a fluidised bed reactor, Polish Journal of Chemical Technology, 2008, Vol. 10, No. 4, 45–48.
  • [14] BES A., Dissertation, Dynamic Process Simulation of Limestone Calcination in Normal Shaft Kilns, Fakultät für Verfahrens- und Systemtechnik, Otto-von-Guericke-Universität, Magdeburg, 2006.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BPW8-0013-0050
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