Flow pattern transition characteristics in vibrated gas-solid fluidized bed of Geldart B magnetite powder using pressure drop signals analysis

Flow pattern transition characteristics in vibrated gas-solid fluidized bed of Geldart B magnetite powder using pressure drop signals analysis
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利用压降信号分析 Geldart B 磁铁矿粉振动气固流化床流型转变特性

DOI:
10.1016/j.powtec.2017.12.089
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发表时间:
2018-03
期刊:
影响因子:
5.2
通讯作者:
Xuliang Yang
Xuliang Yang
中科院分区:
工程技术2区
文献类型:
--
作者:
Yadong Zhang;Yuemin Zhao;Liang Dong;Chenlong Duan;Enhui Zhou;Junyu Lu;Bo Zhang;Xuliang Yang

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The vibrated gas-solid fluidized bed with the − 0.3 + 0.074 mm magnetite powder was utilized to study the flow pattern of bed and the effects of bubble motion on the fluidization characteristics. The results demonstrated that the standard deviation of the bed pressure fluctuation changed, as the gas velocity increased forming an inverted “U” shape plot. When the bed was in the bubbling fluidization mode, the bubbles were produced with a main frequency of 7.5 Hz and the pressure drop signal energy was high. When the bed was in a quasi-turbulent state, the bed mainly produced relatively smaller bubbles between 7.5 and 20 Hz in frequency and the pressure drop signal energy was low. As the vibration frequency increased, both the bed initiation bubbling velocityu1and the onset velocity of turbulent fluidizationu2,decreased. The values of Δu= u2− u1, firstly increased and then gradually decreased with the increase of vibration frequency. Under the condition of vibration frequencyf= 25 Hz and three different vibration amplitudesA(i.e., 1, 2 and 3 mm), the maximum values of Δuare 8.9 cm/s, 7.67 cm/s and 7.28 cm/s, respectively.
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