An Experimental Study of Gas Flow Regime and Pressure Drop in a Random Packed Bed with Sinter Particles

The gas flow regime and pressure drop in a gas–solid packed bed with irregularly shaped sinter particles were experimentally investigated. Using a self-made experimental facility for data measurement, the gas flow pressure drop in a sinter bed layer was determined for various experimental conditions...

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Main Authors: Zude Cheng, Haitao Wang, Junsheng Feng, Hui Dong
Format: Article
Language:English
Published: MDPI AG 2021-02-01
Series:Energies
Subjects:
Online Access:https://www.mdpi.com/1996-1073/14/4/872
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author Zude Cheng
Haitao Wang
Junsheng Feng
Hui Dong
author_facet Zude Cheng
Haitao Wang
Junsheng Feng
Hui Dong
author_sort Zude Cheng
collection DOAJ
description The gas flow regime and pressure drop in a gas–solid packed bed with irregularly shaped sinter particles were experimentally investigated. Using a self-made experimental facility for data measurement, the gas flow pressure drop in a sinter bed layer was determined for various experimental conditions. According to the changes in the modified coefficients, <i>α</i> and <i>β</i>, for different flow regimes, the flow transitions from one regime to another in packed beds with different particle diameters were described. Furthermore, the pressure drop correlations for different flow regimes were determined, and the reliabilities of the obtained correlations were contrastively analyzed. The results show that, when the particle diameter is constant, the modified pressure drop per unit height, Δ<i>P</i>/<i>Hu</i>, increases linearly with the increasing gas superficial velocity. When the gas superficial velocity is larger than 1.15 m/s under atmospheric conditions, the gas flow regime in the sinter bed layer is the turbulent flow. Compared with the experimental correlation of the whole flow, the pressure drop correlations obtained by the piecewise fitting method provided a better prediction of the experimental values, and the average deviations of the obtained correlations for the Forchheimer flow and the turbulent flow were 5.31% and 4.07%, respectively.
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spelling doaj.art-e9239392a7d64aad86ea62d833f7c2102023-12-03T12:48:23ZengMDPI AGEnergies1996-10732021-02-0114487210.3390/en14040872An Experimental Study of Gas Flow Regime and Pressure Drop in a Random Packed Bed with Sinter ParticlesZude Cheng0Haitao Wang1Junsheng Feng2Hui Dong3School of Environment and Energy Engineering, Anhui Jianzhu University, Hefei 230601, ChinaSchool of Environment and Energy Engineering, Anhui Jianzhu University, Hefei 230601, ChinaSchool of Environment and Energy Engineering, Anhui Jianzhu University, Hefei 230601, ChinaSchool of Metallurgy, Northeastern University, Shenyang 110819, ChinaThe gas flow regime and pressure drop in a gas–solid packed bed with irregularly shaped sinter particles were experimentally investigated. Using a self-made experimental facility for data measurement, the gas flow pressure drop in a sinter bed layer was determined for various experimental conditions. According to the changes in the modified coefficients, <i>α</i> and <i>β</i>, for different flow regimes, the flow transitions from one regime to another in packed beds with different particle diameters were described. Furthermore, the pressure drop correlations for different flow regimes were determined, and the reliabilities of the obtained correlations were contrastively analyzed. The results show that, when the particle diameter is constant, the modified pressure drop per unit height, Δ<i>P</i>/<i>Hu</i>, increases linearly with the increasing gas superficial velocity. When the gas superficial velocity is larger than 1.15 m/s under atmospheric conditions, the gas flow regime in the sinter bed layer is the turbulent flow. Compared with the experimental correlation of the whole flow, the pressure drop correlations obtained by the piecewise fitting method provided a better prediction of the experimental values, and the average deviations of the obtained correlations for the Forchheimer flow and the turbulent flow were 5.31% and 4.07%, respectively.https://www.mdpi.com/1996-1073/14/4/872sinterpacked bedpressure dropparticle friction factorflow regime
spellingShingle Zude Cheng
Haitao Wang
Junsheng Feng
Hui Dong
An Experimental Study of Gas Flow Regime and Pressure Drop in a Random Packed Bed with Sinter Particles
Energies
sinter
packed bed
pressure drop
particle friction factor
flow regime
title An Experimental Study of Gas Flow Regime and Pressure Drop in a Random Packed Bed with Sinter Particles
title_full An Experimental Study of Gas Flow Regime and Pressure Drop in a Random Packed Bed with Sinter Particles
title_fullStr An Experimental Study of Gas Flow Regime and Pressure Drop in a Random Packed Bed with Sinter Particles
title_full_unstemmed An Experimental Study of Gas Flow Regime and Pressure Drop in a Random Packed Bed with Sinter Particles
title_short An Experimental Study of Gas Flow Regime and Pressure Drop in a Random Packed Bed with Sinter Particles
title_sort experimental study of gas flow regime and pressure drop in a random packed bed with sinter particles
topic sinter
packed bed
pressure drop
particle friction factor
flow regime
url https://www.mdpi.com/1996-1073/14/4/872
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