Effect of particle properties on forces on an immersed horizontal slat during start-up of a fluidized bed
Different gas-solids flow phenomenas have been observed during start-up of fluidized beds of different particulate materials. [Display omitted] •Forces on a horizontal slat during start-up of fluidized beds of different particulate materials were measured.•The immersed internals will be subject to m...
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| Published in | Chemical engineering research & design Vol. 159; pp. 105 - 114 |
|---|---|
| Main Authors | , , , |
| Format | Journal Article |
| Language | English |
| Published |
Rugby
Elsevier B.V
01.07.2020
Elsevier Science Ltd |
| Subjects | |
| Online Access | Get full text |
| ISSN | 0263-8762 1744-3563 |
| DOI | 10.1016/j.cherd.2020.04.011 |
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| Abstract | Different gas-solids flow phenomenas have been observed during start-up of fluidized beds of different particulate materials.
[Display omitted]
•Forces on a horizontal slat during start-up of fluidized beds of different particulate materials were measured.•The immersed internals will be subject to more severe during start-up of fluidized beds of small particle size.•Different gas–solids flow phenomenas have been observed during start-up of fluidized beds of different particulate materials
To study the effect of particle properties on forces acting on immersed internals during start-up of fluidized bed reactors, forces on a horizontal slat were measured in fluidized beds of four types of particulate materials (i.e. FCC catalyst particles and three silica sands of different sizes). The forces were measured by strain gauges adhered on the slat surface. Transient pressure signals were also measured synchronously by pressure transducers. The experimental results show that a high upward stress impulse appears in the measured stress signals during start-up of the fluidized beds of FCC particles and the two smaller-size silica sands. The peak stress impulse was several times larger than the magnitude of stress signals measured during steady state operation. However, in the fluidized bed of the coarsest silica sand, the peak stress impulse during start-up was much smaller, which is close to the magnitudes measured during steady state fluidization. For the three sizes of silica sands, the effective peak load densities on the slat decreased significantly with increasing particle size and were approximately proportional to the calculated fixed bed pressure drops of these beds based on Ergun equation. On the other hand, during start-up of the fluidized bed of FCC particles, particles near the bottom of the bed were difficult to mobilize and collapse, resulting in the bed expanding considerably and requiring more time to transform into a fluidized state. Potentially, internals immersed in the fluidized beds of small particles are easier to damage during the start-up stage. Effective measures (e.g. starting up the bed gradually with small increments of superficial gas velocity) must be implemented to reduce the possible risks for internals immersed in these fluidized beds. |
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| AbstractList | Different gas-solids flow phenomenas have been observed during start-up of fluidized beds of different particulate materials.
[Display omitted]
•Forces on a horizontal slat during start-up of fluidized beds of different particulate materials were measured.•The immersed internals will be subject to more severe during start-up of fluidized beds of small particle size.•Different gas–solids flow phenomenas have been observed during start-up of fluidized beds of different particulate materials
To study the effect of particle properties on forces acting on immersed internals during start-up of fluidized bed reactors, forces on a horizontal slat were measured in fluidized beds of four types of particulate materials (i.e. FCC catalyst particles and three silica sands of different sizes). The forces were measured by strain gauges adhered on the slat surface. Transient pressure signals were also measured synchronously by pressure transducers. The experimental results show that a high upward stress impulse appears in the measured stress signals during start-up of the fluidized beds of FCC particles and the two smaller-size silica sands. The peak stress impulse was several times larger than the magnitude of stress signals measured during steady state operation. However, in the fluidized bed of the coarsest silica sand, the peak stress impulse during start-up was much smaller, which is close to the magnitudes measured during steady state fluidization. For the three sizes of silica sands, the effective peak load densities on the slat decreased significantly with increasing particle size and were approximately proportional to the calculated fixed bed pressure drops of these beds based on Ergun equation. On the other hand, during start-up of the fluidized bed of FCC particles, particles near the bottom of the bed were difficult to mobilize and collapse, resulting in the bed expanding considerably and requiring more time to transform into a fluidized state. Potentially, internals immersed in the fluidized beds of small particles are easier to damage during the start-up stage. Effective measures (e.g. starting up the bed gradually with small increments of superficial gas velocity) must be implemented to reduce the possible risks for internals immersed in these fluidized beds. To study the effect of particle properties on forces acting on immersed internals during start-up of fluidized bed reactors, forces on a horizontal slat were measured in fluidized beds of four types of particulate materials (i.e. FCC catalyst particles and three silica sands of different sizes). The forces were measured by strain gauges adhered on the slat surface. Transient pressure signals were also measured synchronously by pressure transducers. The experimental results show that a high upward stress impulse appears in the measured stress signals during start-up of the fluidized beds of FCC particles and the two smaller-size silica sands. The peak stress impulse was several times larger than the magnitude of stress signals measured during steady state operation. However, in the fluidized bed of the coarsest silica sand, the peak stress impulse during start-up was much smaller, which is close to the magnitudes measured during steady state fluidization. For the three sizes of silica sands, the effective peak load densities on the slat decreased significantly with increasing particle size and were approximately proportional to the calculated fixed bed pressure drops of these beds based on Ergun equation. On the other hand, during start-up of the fluidized bed of FCC particles, particles near the bottom of the bed were difficult to mobilize and collapse, resulting in the bed expanding considerably and requiring more time to transform into a fluidized state. Potentially, internals immersed in the fluidized beds of small particles are easier to damage during the start-up stage. Effective measures (e.g. starting up the bed gradually with small increments of superficial gas velocity) must be implemented to reduce the possible risks for internals immersed in these fluidized beds. |
| Author | Liu, Duiping Yuan, Yongsheng Zhang, Yongmin Grace, John R. |
| Author_xml | – sequence: 1 givenname: Duiping surname: Liu fullname: Liu, Duiping organization: State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, PR China – sequence: 2 givenname: Yongmin surname: Zhang fullname: Zhang, Yongmin email: zym0876@gmail.com organization: State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, PR China – sequence: 3 givenname: Yongsheng surname: Yuan fullname: Yuan, Yongsheng organization: State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, PR China – sequence: 4 givenname: John R. surname: Grace fullname: Grace, John R. organization: Fluidization Research Centre, Department of Chemical and Biological Engineering, University of British Columbia, 2360 East Mall, Vancouver, Canada V6T 1Z3 |
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| CitedBy_id | crossref_primary_10_1016_j_cherd_2024_01_015 crossref_primary_10_1016_j_partic_2021_01_020 crossref_primary_10_3390_en15062061 |
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•Forces on a... To study the effect of particle properties on forces acting on immersed internals during start-up of fluidized bed reactors, forces on a horizontal slat were... |
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| SubjectTerms | Baffle Effects Fixed beds Fluidized bed Fluidized bed reactors Fluidized beds Force Horizontal loads Particle size Particles Peak load Pressure transducers Sand Silica Silicon dioxide Slat Start-up Steady state Strain gauges Transducers |
| Title | Effect of particle properties on forces on an immersed horizontal slat during start-up of a fluidized bed |
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