Abstract

Coal is the dominant energy resource in China. With the Chinese policy of committing to reducing peak carbon dioxide emissions and achieving carbon neutrality, coal separation has recently become a hot topic, especially the fluidized separation of fine particles. In this study, micron-sized particles were introduced to ameliorate the properties of the traditional fluidized bed. The expansion characteristics of the micron-sized-particle-dense medium were explored. A bed expansion prediction model of the micron-sized-particle-dense medium was established, and the prediction error was about 10%, providing a theoretical basis for understanding the distribution characteristics of the bed. This model also helped predict the bed density in the presence of a micron-sized-particle-dense medium, and the prediction accuracy was between 85% and 92%, providing a theoretical basis for selecting and popularizing fluidized beds for industrial separation.

Highlights

  • Key Laboratory of Coal Processing & Efficient Utilization, Ministry of Education, China University of Mining & Technology, Xuzhou 221116, China

  • In the gas–solid separation fluidized bed, the study of the two-phase distribution is helpful to analyze the distribution of the bubble phase and of the emulsion phase

  • With the increase of the bed height, the expansion rate of the emulsion phase decreased to a small extent and gradually stabilized; With the increase of superficial gas velocity, the proportion of the bubble phase showed an increasing trend as a whole, while the initial bed height had a little influence on the bubble phase

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Summary

Apparatus

The fluidized bed Plexiglas column had a 15.2 cm internal diameter (ID) and was 70 cm high. The bubble phase and emulsion phase are the main components of the fluidized bed. Bed height expansion is directly related to the above phases. Accurate monitoring of bed height variation is crucial in the analysis of the distribution of the two phases. The bed height variation was recorded by a digital camera (Nikon D3200) with 25 frames in front of the fluidized bed on the same side of the two lights

Dense Medium
FeedingIn
Two-Phase Theory
Bed Expansion Prediction
Emulsion Phase Characterization in the Fluidized Bed
Conclusions
Full Text
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