## Abstract The Carman channel model for flow in packed beds is shown to apply for the minimum fluidization velocity and homogeneous fluidized beds. The channel model also provides correlations for mass transfer in the laminar flow region and heat and mass transfer for turbulent flow in a packed be
Comparison of Fixed and Fluidized Activated Carbon Beds for Removal of Organic Vapors
β Scribed by I.E. Agranovski; S. Moustafa; R.D. Braddock
- Publisher
- John Wiley and Sons
- Year
- 2004
- Tongue
- English
- Weight
- 112 KB
- Volume
- 27
- Category
- Article
- ISSN
- 0930-7516
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β¦ Synopsis
Abstract
Activated carbons are commonly used for removal of organic vapors from exhaust air streams. Two configurations, including fixed and fluidized carbon beds are usually employed in industry to meet various requirements of the industrial process which is being used. This paper investigates the performance of such configurations and provides a comparative analysis. It was found that for thin carbon layers, the fixed bed performs more efficiently with the difference exceeding 15β% for the layers with the thickness less than 15βmm. This difference is decreasing with increase of the layer thickness and becomes less than 5β% for the beds thicker than 100βmm. Considering various advantages of the fluidized beds over fixed beds, including lower resistance to the gas flow, excellent gas distribution and minimal possibility of clogging in case of existence of alien particles in the gas, they are recommended for use with the minimal thickness of the layer to be larger than 100βmm.
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