Simulation of mass balance behavior in a large-scale circulating fluidized bed reactor |
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Institution: | 1. Department of Chemical Engineering, Sungkyunkwan University, Republic of Korea;2. Ironmaking Research Group, Technical Research Laboratories, POSCO, Republic of Korea |
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Abstract: | We determine using a compound model the influence of the mass of granular matter on the behavior of a supercritical circulating fluidized bed (CFB) reactor. Population balance enables a stationary-regime modeling of the mass flow of granular matter inside a CFB unit in a large-scale. The simulation includes some important dynamic processes of gas-particle flows in fluidized bed such as attrition, fragmentation, elutriation, and fuel combustion. Numerical calculations with full boiler loading were performed of operational parameters such as furnace temperature, furnace pressure, feeding materials mass flows, and excess air ratio. Furthermore, three bed inventory masses were adopted as experimental variables in the simulation model of mass balance. This approach enables a sensitivity study of mass flows of granular matter inside a CFB facility. Some computational results from this population balance model obtained for a supercritical CFB reactor are presented that show consistency with the operational data for large-scale CFB units. |
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Keywords: | Bed inventory mass Mass flow of solids Circulating fluidized bed Population mass balance model Sensitivity analysis |
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