- Volumes 84-95 (2024)
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Volumes 72-83 (2023)
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Volume 83
Pages 1-258 (December 2023)
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Volume 82
Pages 1-204 (November 2023)
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Volume 81
Pages 1-188 (October 2023)
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Volume 80
Pages 1-202 (September 2023)
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Volume 79
Pages 1-172 (August 2023)
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Volume 78
Pages 1-146 (July 2023)
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Volume 77
Pages 1-152 (June 2023)
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Volume 76
Pages 1-176 (May 2023)
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Volume 75
Pages 1-228 (April 2023)
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Volume 74
Pages 1-200 (March 2023)
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Volume 73
Pages 1-138 (February 2023)
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Volume 72
Pages 1-144 (January 2023)
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Volume 83
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Volumes 60-71 (2022)
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Volume 71
Pages 1-108 (December 2022)
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Volume 70
Pages 1-106 (November 2022)
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Volume 69
Pages 1-122 (October 2022)
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Volume 68
Pages 1-124 (September 2022)
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Volume 67
Pages 1-102 (August 2022)
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Volume 66
Pages 1-112 (July 2022)
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Volume 65
Pages 1-138 (June 2022)
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Volume 64
Pages 1-186 (May 2022)
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Volume 63
Pages 1-124 (April 2022)
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Volume 62
Pages 1-104 (March 2022)
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Volume 61
Pages 1-120 (February 2022)
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Volume 60
Pages 1-124 (January 2022)
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Volume 71
- Volumes 54-59 (2021)
- Volumes 48-53 (2020)
- Volumes 42-47 (2019)
- Volumes 36-41 (2018)
- Volumes 30-35 (2017)
- Volumes 24-29 (2016)
- Volumes 18-23 (2015)
- Volumes 12-17 (2014)
- Volume 11 (2013)
- Volume 10 (2012)
- Volume 9 (2011)
- Volume 8 (2010)
- Volume 7 (2009)
- Volume 6 (2008)
- Volume 5 (2007)
- Volume 4 (2006)
- Volume 3 (2005)
- Volume 2 (2004)
- Volume 1 (2003)
• Gas solid flow in an ICFBs studied by tracing a fluorescent particle.
• Particle flow behaviors in different regions analyzed systematically.
• Solid circulation rate obtained for a range of operating parameters.
• Most important parameters found to control solid circulation rate.
• Fitting solid circulation rate by correlation to yield particle flow coefficient 0.22.
Internally circulating fluidized beds (ICFBs) enable effective control of the reactions and heat distribution in reactors. The ICFB contains two or more connected fluidized regions with different gas velocities to promote controlled solid circulation. The control of solid circulation rate (G0) is a critical factor. We recorded single particle trajectories by tracing a fluorescent particle, based on which particle flow behaviors were analyzed in different regions. G0 was obtained for a wide range of operating parameters. An increase in gas velocity in the down- and upflow beds shortened the particle circulation time in both beds and G0 increased significantly. As the static bed height increased, the differential pressure on both sides of the circulation port increased, which resulted in an increase in the solid circulation rate. As the orifice area increased, the flow resistance through the orifice decreased and thus the solid circulation rate increased. G0 increased with the decrease in particle size. The gas velocity in the upflowing bed and orifice area was the most important parameter to control the solid circulation rate. G0 was compared with the experimental measurements in literature and predictions using the correlation based on Bernoulli’s equation, and they agreed well.