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Sökning: onr:"swepub:oai:research.chalmers.se:d79a78b1-cf24-4d68-a56b-e7ce4f6d3da2" > O2/CO2 and O2/N2 co...

O2/CO2 and O2/N2 combustion of bituminous char particles in a bubbling fluidized bed under simulated combustor conditions

Wang, Wenkang (författare)
Nanjing Normal University
Bu, C. S. (författare)
Nanjing Normal University
Gómez-Barea, Alberto (författare)
Universidad de Sevilla,University of Seville
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Leckner, Bo G, 1936 (författare)
Chalmers tekniska högskola,Chalmers University of Technology
Wang, Xinye (författare)
Nanjing Normal University
Zhang, Jubing (författare)
Nanjing Normal University
Piao, Guilin (författare)
Nanjing Normal University
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 (creator_code:org_t)
Elsevier BV, 2018
2018
Engelska.
Ingår i: Chemical Engineering Journal. - : Elsevier BV. - 1385-8947. ; 336, s. 74-81
  • Tidskriftsartikel (refereegranskat)
Abstract Ämnesord
Stäng  
  • Most of the time char particles in commercial FB units encounter considerably lower oxygen co ncentrations than that in the entrance, say between 2% and 10%, and the effects of the oxy-fuel atmosphere on the conversion history of char particles need to be clearly treated under these conditions. In the present work, an experimental study of combustion of bituminous coal char was carried out in a laboratory FB in O 2 /CO 2 and O 2 /N 2 atmospheres under simulated FB combustor conditions at O 2 concentrations of 4–10% v/v, bed temperatures of 800–900 °C and char particle sizes of 2–8 mm by continuously measuring the concentrations of O 2 and CO in the flue gas. The results indicate that the conversion of char is controlled by diffusion of O 2 in the boundary layer of the particle in O 2 /CO 2 and O 2 /N 2 environments and that the gasification of char in O 2 /CO 2 is limited by chemical kinetics. A char conversion model, taking into account the mass transfer from the bed to the particle and the gasification kinetics of char, was built, based on the experimental results and the intrinsic reactivity of char obtained in TGA tests. Simulations, carried out under the same conditions as in the FB experiments, give good agreement in terms of burnout time and instantaneous reactivity during the conversion of single particles. Simulated results prove that the low diffusivity of O 2 in CO 2 is the main reason for the decreased reaction rate of the char particle in O 2 /CO 2 compared with O 2 /N 2 . The contribution of gasification to the consumption of char is more notable at high bed temperature (900 °C) and coarse particles (8 mm), particularly at lower oxygen concentration (4–6% v/v).

Ämnesord

TEKNIK OCH TEKNOLOGIER  -- Kemiteknik -- Kemiska processer (hsv//swe)
ENGINEERING AND TECHNOLOGY  -- Chemical Engineering -- Chemical Process Engineering (hsv//eng)
TEKNIK OCH TEKNOLOGIER  -- Kemiteknik -- Annan kemiteknik (hsv//swe)
ENGINEERING AND TECHNOLOGY  -- Chemical Engineering -- Other Chemical Engineering (hsv//eng)
TEKNIK OCH TEKNOLOGIER  -- Materialteknik -- Metallurgi och metalliska material (hsv//swe)
ENGINEERING AND TECHNOLOGY  -- Materials Engineering -- Metallurgy and Metallic Materials (hsv//eng)

Nyckelord

Combustion characteristics
Reaction kinetics
Bituminous coal-char
Fluidized bed
O /CO combustion 2 2

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