A mathematical model for atmospheric staged circulating fluidized bed combustion, which takes fluid dynamics, combustion, heat transfer, pollutants formation and retention, into account was developed in the Institute of Engineering Thermophysics (IET) recently. The model of gas solid flow at the bottom of the combustor was treated by the two-phase theory of fluidized bed and in the upper region as a core-annulus flow structure. The chemical species CO, CO2, H2, H2O, CH4, O2 and N2 were considered in the reaction process. The mathematical model consisted of sub-models of fluid namics, coal heterogeneous and gas homogeneous chemical reactions, heat transfer, particle fragmentation and attrition, mass and energy balance etc. The developed code was applied to simulate an operating staged circulating fluidized bed combustion boiler of early design and the results were in good agreement with the operating data. The main submodels and simulation results are given in this paper.
[1]
L. H. Chen,et al.
Fluidized bed freeboard phenomena: Entrainment and elutriation
,
1982
.
[2]
M. J. Rhodes,et al.
Modelling the flow structure of upward-flowing gas-solids suspensions
,
1990
.
[3]
Nicolas Kalogerakis,et al.
Modelling the internal flow structure of circulating fluidized beds
,
1989
.
[4]
Matteo D'Amore,et al.
Some issues in modelling bubbling and circulating fluidized-bed coal combustors
,
1995
.
[5]
G. H. Penner,et al.
Asymmetric induction in Diels–Alder reactions of α-alkoxyorthoquinodimethanes
,
1989
.
[6]
Octave Levenspiel,et al.
Entrainment of solids from fluidized beds I. Hold-up of solids in the freeboard II. Operation of fast fluidized beds
,
1990
.
[7]
Derek Geldart,et al.
A model for the circulating fluidized bed
,
1987
.
[8]
Mooson Kwauk,et al.
The Dynamics of Fast Fluidization
,
1980
.
[9]
Mathematical modelling of circulating fluidized bed reactors by reference to a solids decomposition reaction and coal combustion
,
1987
.
[10]
J. R. Arthur.
Reactions between carbon and oxygen
,
1951
.