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- W2184003341 abstract "To maximize the carbon dioxide sorption efficiency in high density circulating fluidized bed reactor, the gas-solid particle flow regimes had been investigated using commercial computational fluid dynamics programs (GAMBIT and ANSYS FLUENT). The circulating fluidized bed reactor had the overall dimension of 2.00 m height, 0.30 m width and 0.05 m depth. The grid independency test was employed to study the effect of different grid or mesh size on the simulation result. The quasi-steady state operation of the system was detected from the result of grid independency test which was about 20 s to 40 s. The gas velocity was varied to investigate different flow regimes of the gas-solid particle. The results from the simulation showed that the solid particle volume fraction profiles were able to predict various flow regimes at each specific gas inlet velocity. The velocities of gas phase and solid phase were shown in this literature to provide the idea of the regime characteristic. The novel flow regime was appeared at gas inlet velocity from 0.75 m/s to 1 m/s. Due to its characteristic, this flow regime was the most appropriate regime for the carbon dioxide sorption application. Keyword: Circulating fluidized bed reactor, Computational fluid dynamics, Flow regime" @default.
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- W2184003341 date "2012-01-01" @default.
- W2184003341 modified "2023-09-27" @default.
- W2184003341 title "Computational fluid dynamics simulation of novel flow regimes in high density circulating fluidized bed reactor" @default.
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