- 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)
• Characteristics of pressure fluctuations in gas–solid fluidized bed after introduction of Geldart A particles were studied.
• Relationship between emulsified phase, bubble phase, and bed pressure fluctuation stability was explained.
• Established a prediction model for the main frequency of pressure fluctuations before bubbling fluidization.
Gas–solid separation fluidized bed is a typical method for coal separation without water utilization. Geldart A particles is also considered as the ideal dense medium to strengthen separation efficiency. Fluidization stability reflects the bed pressure fluctuations and the distribution of bubble and emulsion phases, affecting the separation performance. And the main frequency of pressure fluctuations can directly reflect the degree of pressure fluctuations. Therefore, the detailed fluidization stability is analyzed combined the method of standard deviation of pressure fluctuations, power spectral density, etc., for Geldart A particles. The results showed that maintaining an appropriate gas velocity resulted in an average bed pressure of around 2000 Pa. The main frequency is mainly concentrated around 1–1.5 Hz. Finally, a prediction model of the main frequency of pressure fluctuations is established, and the error can be controlled within ±0.15. The investigation further proved the stable fluidization of Geldart A particles and provides a method for predicting the main frequency of pressure fluctuations in the gas–solid separation fluidized bed.