A study on fluidization of activated carbon particles in gas-solid fluidized bed
- 17 August 2020
- journal article
- research article
- Published by Taylor & Francis in Indian Chemical Engineer
- Vol. 63 (5) , 478-490
Abstract
In this paper, the minimum fluidisation velocity ( ) of activated carbon particles in a gas–solid fluidised bed was experimentally determined using dry air as the fluidising medium. The effect of particle size and temperature on the minimum fluidisation velocity of the fluidised activated carbon particles was analysed. The particle sizes 212, 425, and 710 µm and bed temperatures of 30°C, 100°C, 200°C, and 300°C were studied. From the experimental results, it was found that the decreased with a decrease in particle size of the activated carbon particles and decreased with an increase in the temperature. Based on the experimental results, a new correlation was developed to predict at higher temperatures, since at higher temperatures, the deviation of experimental values was higher when compared with the values estimated using previously published correlations. The present study will be useful for the design of an experimental system to study the continuous adsorption and desorption of organic vapours at higher temperatures in the fluidised bed of activated carbon particles. The details of the experimental study and analysis of results are discussed in this paper.
Keywords
This publication has 28 references indexed in Scilit:
- Fluidization characteristics of lithium-titanate in gas-solid fluidized bedFusion Engineering and Design, 2011
- The minimum bubbling velocity of fluidized beds operating at high temperaturePowder Technology, 2009
- Analysis of the fluidization process of particle beds at high temperatureChemical Engineering Science, 1998
- The expansion of gas-fluidised beds in bubbling fluidisationChemical Engineering Science, 1997
- Effect of operating temperature on minimum fluidization velocityPowder Technology, 1991
- The effect of operating temperature on the velocity of minimum fluidization, bed voidage and general behaviourPowder Technology, 1982
- Fluidisation of polydisperse systemsChemical Engineering Science, 1979
- Types of gas fluidizationPowder Technology, 1973
- The ratio of terminal velocity to minimum fluidising velocity for spherical particlesThe Canadian Journal of Chemical Engineering, 1968
- A generalized method for predicting the minimum fluidization velocityAIChE Journal, 1966