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Design of micro-fluidized beds by experiments and numerical simulations : flow regims diagonis and hydrodynamic study

Abstract : Micro-fluidized bed (MFB) exhibits great advantages such as a large specific contact surface, a fast dissipation of heat (ideal for exothermic reactions) and better mass and heat transfers, but suffers from difficulties in precise control and shows strong frictional wall effect. Present study was conducted experimentally and numerically to understand fundamental hydrodynamics in MFBs. Experimental work was carried out in four MFBs of 20-4 mm compared to two relatively large beds of 100-50 mm using three types of particles (B347: 347 μm, 2475 kg/m3; B105: 105 μm, 8102 kg/m3; A63: 63.8μm, 2437 kg/m3). The ratio of static bed height (Hs) to bed diameter (Dt) was set between 1-4. Mechanical vibration was applied to the 4 mm bed. A new method for flow regimes diagnosis was developed based on pressure fluctuation analyses, which mainly include calculating the standard deviation, autocorrelation function, probability density function, power spectral density function and time-frequency analysis. Numerical simulations were performed under Eulerian-Eulerian framework in 2D. Six flow regimes were identified: fixed bed, bubbling, bubbling/slugging, slugging, slugging/turbulent and bubbling/turbulent. Partial fluidization is encountered at Hs/Dt=1-2 while slugging prevails quickly after minimum fluidization at Hs/Dt=3-4. In the 4 mm bed, fluidization of B347 particles show better fluidization quality, while an increase in Umf is observed for B105 and A63 particles. Mechanical vibration reduces partial fluidization, thus resulting in larger ΔP and smaller Umf. A larger Umb and a delayed Uc were obtained as well. Results by simulations agree reasonably well with experimental data
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Submitted on : Thursday, January 2, 2020 - 1:09:20 AM
Last modification on : Friday, October 16, 2020 - 11:22:06 AM
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  • HAL Id : tel-02426182, version 1



Haiqin Quan. Design of micro-fluidized beds by experiments and numerical simulations : flow regims diagonis and hydrodynamic study. Chemical engineering. Ecole Centrale de Lille, 2017. English. ⟨NNT : 2017ECLI0027⟩. ⟨tel-02426182⟩



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