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Both, solids distribution and solids fraction can be influenced by the fluidization rates of the two reactors.
Numerical results related mostly to the hydrodynamics of the reactors, such as the solids distribution and residence time are then used as input parameters in a kinetics-based process algorithm.
The current paper presents a theoretical and experimental work, which was performed at the Institute of Thermal Engineering (ITW) in Vienna/Austria to describe solids distribution and heat transfer in circulating fluidized bed boilers (CFB).
In this study, solids concentration of different types of particles shows that heavier particles have higher solids concentration laterally and axially than lighter particles; larger particles result in more compact solids distribution and such size effect is more evident at the riser bottom; more spherical particles lead to higher solids concentration.
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Longitudinal solid distribution and liquid circulation were discussed experimentally in slurry bubble column with short size draft tube.
A Eulerian model incorporating the kinetic theory for solid particles was applied to simulate the solid distribution and RTD of feeding materials.
The effect of four types of feeding methods and feeding rates on solid distribution and RTD were evaluated based on the simulation results.
Results showed that double symmetrical feeding pipe with an feeding mouth angle of 45° provides more uniform solid distribution and longer residence time compared with those of other three types.
A good agreement is obtained between the experimental data of solid distributions and the simulation results in the flow fields of liquid solid solid as well as liquid solid systems.
Modifications of literature expressions for prediction of solids flow and solids distribution are proposed, and an improved expression is formulated for prediction of the thickness of the wall layer.
In this work, data from laboratory units are compared with boiler data, and the accuracy of literature expressions for prediction of solids distribution, solids flow and wall layer thickness is reviewed.
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