湍流
混合(物理)
机械
色散(光学)
气泡
流化床
化学
热力学
材料科学
光学
物理
量子力学
作者
Bing Du,Liang‐Shih Fan,Fei Wei,W. Warsito
出处
期刊:Aiche Journal
[Wiley]
日期:2002-09-01
卷期号:48 (9): 1896-1909
被引量:124
标识
DOI:10.1002/aic.690480907
摘要
Abstract Gas and solids mixing characteristics in the bubbling and turbulent regimes of a gas‐solid fluidized bed are examined using helium and phosphor tracer techniques to obtain the gas and solids dispersion coefficients, respectively. The real time, quasi‐3‐D flow behavior is qualified and quantified by the electrical capacitance tomography (ECT) technique. The mixing behavior varies significantly with the flow regimes. As the gas velocity increases, axial and radial gas dispersion coefficients increase in the bubbling regime, reach a peak at U c , the transition velocity from the bubbling to turbulent regimes, and then decrease. In contrast, as the gas velocity increases, axial and radial solids dispersion coefficients increase in the bubbling regime and continuously increase through U c to the turbulent regime. Temperature and pressure have little effect on the gas and solids mixing behavior. A small quantity of fine particles is noted to drastically affect the gas and solids mixing behavior in the turbulent fluidized bed. The axial and radial dispersion coefficients of gas and solids reach their maximum when the fines content is about 15%. The ECT measurements illustrate the effect of adding fines on the flow behavior in the bed. A small quantity of fine particles disintegrate the bubble/void phase, significantly modifying bubble/void‐ and emulsion‐phase mixing behavior.
科研通智能强力驱动
Strongly Powered by AbleSci AI