Solids Flow Pattern in Circulating Fluidized-bed Boilers
Doctoral thesis, 2005
The background of this dissertation is the knowledge of circulating fluidized bed (CFB)
technology, which has reached a level enabling units of several hundred megawatts of
electricity to be constructed and employed. Yet an improved understanding of the technology
is needed in order to further develop and optimize large-scale combustion in CFB boilers,
especially since the operating conditions and the geometries of large boilers differ from those
typical for laboratory units, in which most of the research hitherto has been performed. The
suitability of combusting or co-combusting heterogeneous fuels, such as biomass and waste,
in CFB boilers also justifies further research on the technology. Based on measurements in a
235 MWe boiler, this work compares boilers and laboratory units in terms of solids flow,
solids distribution and solids wall-layer thickness. The work also studies the origins of
pressure fluctuations in large boilers and investigates their influence on the combustion
process. The gas composition and the solids flow pattern in a 30 MW boiler loop seal are
examined as well.
The flow pattern in the 235 MWe boiler was examined and a compilation of literature data
show that there are considerable differences in the flow pattern between boilers and laboratory
units. Literature correlations for prediction of the solids distribution and the thickness of the
solids wall-layer, derived from best fit to data from laboratory units, therefore give poor
accuracy when applied to boiler data. Methods to better estimate those parameters are derived
in this work. In addition, the pressure fluctuations investigated here were found to originate
mainly from two sources: the bubble flow through the dense bed and the irregularities in the
fuel feed. Occurrences of high fuel flow give pressure peaks due to a high release of volatiles,
causing concurrent dips in the air feed to the furnace. The coincidence of a high release of
volatiles and a low air feed results in a reducing environment in virtually the entire furnace,
which may hinder burnout and cause undesirable emission of hydrocarbons.
Measurements in the 30 MW boiler loop seal show that gas concentration and solids flow
depend on load, i.e. on the external solids flow, and on height above the bottom of the loop
seal. It was also found that some flue gas enters the loop seal from the cyclone and that
combustion occurs in the loop seal.
scale-up
hydrodynamics
combustion
loop seal
wall-layers
Circulating Fluidized Bed
13.00 HC2, Hörsalsvägen, Chalmers, Göteborg
Opponent: Professor Joachim Werther, Department of Chemical Engineering (Particle Technology), Technical University of Hamburg-Harburg