Publication Date:
2011-07-15
Description:
Calculating the cyclone pressure drop, Δ p c , at a high inlet solid concentration, C s,in , is important for the design and operation of circulating fluidized bed boilers. Three typical Δ p c models that consider the effect of C s,in were selected and assessed. Compared with experimental results, it was found that only the model developed by Chen and Shi can correctly predict the variation trend of Δ p c with C s,in at high values of C s,in , but the predicted values are much greater than the measured values. It is suggested that the dissipative loss of swirling dynamic pressure should be excluded from the total dissipative loss of gas dynamic energy when the pressure tap is closely installed to the outlet and the swirl exponent could be assumed to be null for high C s,in conditions. A set of equations modified from the original C-S model is given. Compared with the experimental data obtained from the present study and some data from literature, the improved C-S model can predict Δ p c at high C s,in well. In addition, it was found that the correction of pressure tap position is more obvious than the correction of swirl exponent. Validation of the model to calculate cyclone pressure drop under a condition of high inlet solid concentration was conducted. Three models were selected and assessed. It was found that only the model of Chen and Shi could correctly predict the variation trend, however, with a remarkable overprediction. Suggestions are given for improvement under high inlet solid concentration.
Print ISSN:
0930-7516
Electronic ISSN:
1521-4125
Topics:
Chemistry and Pharmacology
,
Process Engineering, Biotechnology, Nutrition Technology
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