Volume 35 Issue 06
Dec.  2007
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CAO Jiantao, CHENG Zhonghu, FANG Yitian, JING Huimin, WANG Yang. 加压流化床流化性质的实验与模拟研究[J]. Journal of Fuel Chemistry and Technology, 2007, 35(06): 743-747.
Citation: CAO Jiantao, CHENG Zhonghu, FANG Yitian, JING Huimin, WANG Yang. 加压流化床流化性质的实验与模拟研究[J]. Journal of Fuel Chemistry and Technology, 2007, 35(06): 743-747.

加压流化床流化性质的实验与模拟研究

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  • Corresponding author: CHENG Zhonghu
  • Received Date: 2007-03-11
  • Rev Recd Date: 2007-08-23
  • Publish Date: 2007-12-31
  • The behavior of particles and bubbles in a twodimensional jetting fluidized bed included in a pressured vessel was investigated experimentally by using the CCD camera technology that can detailedly record the behavior of bubbles. EulerianEulerian model was used to simulate the hydrodynamics of a pressurized jetting fluidized bed with a central jet and Vshaped distributor. The influence of gas velocity on the size of bubble, bed expansion ratio and jet penetration height at higher pressure was studied. Both experimental and simulation l results clearly indicate that the jet height decreases and the bubbles become more round when the gasvelocity of distributor is increased at higher pressure. When the jetting gasvelocity is increased, the jet height increases and the bubbles become slender. It has been verified that the result from hydrodynamic model shows a good agreement with experimental data, which suggests that the model can be used to study the fluidization properties in the pressurized fluidized bed.
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