Effect of Gas Stirring on External Mass Transfer, Intraparticle Diffusion and Energy Consumption during Adsorption

Gas stirring was used to study the adsorption of basic dyes onto montmorillonite clay. This technique had been demonstrated previously as being more efficient than mechanical stirring. The experimental set-up employed was a fixed-bed column connected to an air-supply system with provision for contro...

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Main Author: Olfat A. Fadali
Format: Article
Language:English
Published: Hindawi - SAGE Publishing 2003-12-01
Series:Adsorption Science & Technology
Online Access:https://doi.org/10.1260/02636170360744371
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spelling doaj-5bf65ab0bb374efba1658c5270942aee2021-04-02T16:54:08ZengHindawi - SAGE PublishingAdsorption Science & Technology0263-61742048-40382003-12-012110.1260/02636170360744371Effect of Gas Stirring on External Mass Transfer, Intraparticle Diffusion and Energy Consumption during AdsorptionOlfat A. FadaliGas stirring was used to study the adsorption of basic dyes onto montmorillonite clay. This technique had been demonstrated previously as being more efficient than mechanical stirring. The experimental set-up employed was a fixed-bed column connected to an air-supply system with provision for controlling different airflow rates at different temperatures. The dyestuff used was Basic Red (a commercial dye). The rate of dye removal was found to increase with increasing gas flow and increasing temperature. Dye removals of 86% to 55% could be achieved for contact times of 35 min to 50 min using dye concentrations between 200 mg/l and 500 mg/l at a gas flow rate of 100 cm 3 /s. The calculated Langmuir constants demonstrated that clay is a favourable adsorbent for the basic dye. Compared to powdered activated carbon (PAC), the adsorption capacity of the clay was 41.3% while the relative cost of basic dye removal was 0.024-times that of PAC. The external mass-transfer coefficient (K s ) and the intraparticle diffusion rate parameter (K p ) were calculated and evaluated as functions of gas stirring and temperature. It was found that an increase in the rate of adsorption effected by gas stirring was double that obtained by increasing the temperature due to the high turbulence induced by axial and radial flow created by gas stirring. The activation energy (E) of 5.95 kcal/mol demonstrated that adsorption of the basic dye onto clay was diffusion-controlled. The energy consumption (W) for removing a known percentage of the dye was evaluated and found to correlate with the equation W = 8.56Q 1.02 X 8.63 for 50 < Q < 100 cm 3 /s, where Q is the gas flow rate and X is the percentage dye removal.https://doi.org/10.1260/02636170360744371
collection DOAJ
language English
format Article
sources DOAJ
author Olfat A. Fadali
spellingShingle Olfat A. Fadali
Effect of Gas Stirring on External Mass Transfer, Intraparticle Diffusion and Energy Consumption during Adsorption
Adsorption Science & Technology
author_facet Olfat A. Fadali
author_sort Olfat A. Fadali
title Effect of Gas Stirring on External Mass Transfer, Intraparticle Diffusion and Energy Consumption during Adsorption
title_short Effect of Gas Stirring on External Mass Transfer, Intraparticle Diffusion and Energy Consumption during Adsorption
title_full Effect of Gas Stirring on External Mass Transfer, Intraparticle Diffusion and Energy Consumption during Adsorption
title_fullStr Effect of Gas Stirring on External Mass Transfer, Intraparticle Diffusion and Energy Consumption during Adsorption
title_full_unstemmed Effect of Gas Stirring on External Mass Transfer, Intraparticle Diffusion and Energy Consumption during Adsorption
title_sort effect of gas stirring on external mass transfer, intraparticle diffusion and energy consumption during adsorption
publisher Hindawi - SAGE Publishing
series Adsorption Science & Technology
issn 0263-6174
2048-4038
publishDate 2003-12-01
description Gas stirring was used to study the adsorption of basic dyes onto montmorillonite clay. This technique had been demonstrated previously as being more efficient than mechanical stirring. The experimental set-up employed was a fixed-bed column connected to an air-supply system with provision for controlling different airflow rates at different temperatures. The dyestuff used was Basic Red (a commercial dye). The rate of dye removal was found to increase with increasing gas flow and increasing temperature. Dye removals of 86% to 55% could be achieved for contact times of 35 min to 50 min using dye concentrations between 200 mg/l and 500 mg/l at a gas flow rate of 100 cm 3 /s. The calculated Langmuir constants demonstrated that clay is a favourable adsorbent for the basic dye. Compared to powdered activated carbon (PAC), the adsorption capacity of the clay was 41.3% while the relative cost of basic dye removal was 0.024-times that of PAC. The external mass-transfer coefficient (K s ) and the intraparticle diffusion rate parameter (K p ) were calculated and evaluated as functions of gas stirring and temperature. It was found that an increase in the rate of adsorption effected by gas stirring was double that obtained by increasing the temperature due to the high turbulence induced by axial and radial flow created by gas stirring. The activation energy (E) of 5.95 kcal/mol demonstrated that adsorption of the basic dye onto clay was diffusion-controlled. The energy consumption (W) for removing a known percentage of the dye was evaluated and found to correlate with the equation W = 8.56Q 1.02 X 8.63 for 50 < Q < 100 cm 3 /s, where Q is the gas flow rate and X is the percentage dye removal.
url https://doi.org/10.1260/02636170360744371
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