TY - JOUR
T1 - Sulfur dioxide capture under PFBC conditions
T2 - The influence of sorbent particle structure
AU - Zevenhoven, Ron
AU - Yrjas, Patrik
AU - Hupa, Mikko
N1 - Funding Information:
This is work part of the Finnish National Combustion and Gasification Research Programme LIEKKI 2. Mr. Peter Backman and Mr. K&offer Sandelin are acknowledged for doing the P-TGA experiments. Prof. Suresh Bhatia (currently at the University of Queensland, Brisbane, Australia) is acknowledged for his useful comments to the modelling procedure. Additional support from A. Ahlstrom Corp. (nowadays Foster Wheeler Energy Oy) and Enviro-power Inc. (nowadays Carbona Corp.) is acknowledged. Ron Zevenhoven acknowledges the Commission of the European Communities for support via a Human Capital and Mobility post-dot fellowship.
Copyright:
Copyright 2017 Elsevier B.V., All rights reserved.
PY - 1998/3
Y1 - 1998/3
N2 - An unreacted shrinking core model with variable effective diffusivity was applied to sulfation test data from a pressurised thermogravimetric apparatus (P-TGA) for various limestone and dolomite samples. The particle size was 250-300 μm for all sorbents. The tests were carried out under conditions typical for a pressurised fluidised bed combustor, i.e. 850 or 950°C, 1.5 MPa. Under these conditions the limestone remains uncalcined, whilst the dolomite is half-calcined. The sorbents were characterised by chemical composition analysis, particle density measurement, mercury porosimetry and BET internal surface measurement. A key parameter in this study is the conversion-dependent Thiele parameter, which reveals a shift in rate-determining mechanism during the sorbents' sulfation. The extended model allows the effect of particle structure on the reaction rate constant and the product layer diffusivity to be evaluated. Estimates for the apparent activation energy of the kinetics and the product layer diffusion can also be given, based on data from two temperatures.
AB - An unreacted shrinking core model with variable effective diffusivity was applied to sulfation test data from a pressurised thermogravimetric apparatus (P-TGA) for various limestone and dolomite samples. The particle size was 250-300 μm for all sorbents. The tests were carried out under conditions typical for a pressurised fluidised bed combustor, i.e. 850 or 950°C, 1.5 MPa. Under these conditions the limestone remains uncalcined, whilst the dolomite is half-calcined. The sorbents were characterised by chemical composition analysis, particle density measurement, mercury porosimetry and BET internal surface measurement. A key parameter in this study is the conversion-dependent Thiele parameter, which reveals a shift in rate-determining mechanism during the sorbents' sulfation. The extended model allows the effect of particle structure on the reaction rate constant and the product layer diffusivity to be evaluated. Estimates for the apparent activation energy of the kinetics and the product layer diffusion can also be given, based on data from two temperatures.
KW - Mathematical modelling
KW - Sorbents
KW - Sulfur capture
UR - http://www.scopus.com/inward/record.url?scp=0032024803&partnerID=8YFLogxK
U2 - 10.1016/S0016-2361(97)00205-6
DO - 10.1016/S0016-2361(97)00205-6
M3 - Article
AN - SCOPUS:0032024803
SN - 0016-2361
VL - 77
SP - 285
EP - 292
JO - Fuel
JF - Fuel
IS - 4
ER -