Kinetic modeling, thermodynamic, and mass-transfer studies of gas-phase glycerol dehydration to acrolein over supported silicotungstic acid catalyst
The kinetics of gas-phase glycerol dehydration in a packed-bed reactor over a highly active and stable supported silicotungstic acid catalyst with zirconium oxide and nanosized aluminum oxide (30HZ-20A) was investigated. The kinetic study is based on the optimal reaction conditions determined by res...
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my.utm.584622017-02-01T01:40:38Z http://eprints.utm.my/id/eprint/58462/ Kinetic modeling, thermodynamic, and mass-transfer studies of gas-phase glycerol dehydration to acrolein over supported silicotungstic acid catalyst Kiakalaieh, Talebian Saidina Amin, Nor Aishah TP Chemical technology The kinetics of gas-phase glycerol dehydration in a packed-bed reactor over a highly active and stable supported silicotungstic acid catalyst with zirconium oxide and nanosized aluminum oxide (30HZ-20A) was investigated. The kinetic study is based on the optimal reaction conditions determined by response surface methodology. The reaction rate followed first-order kinetics with the activation energy and frequency factor, E = 27.5 kJ/mol and A = 5.35 × 105 s-1, respectively. Based on thermodynamic analysis, the values of ΔH° and ΔS° of the endothermic reaction were 14.70 and 0.09 kJ/(mol K), respectively, and ΔG° =-12.12 kJ/mol. The mass-transfer analysis revealed the pellet sizes of dp < 1 µm proceeded under reaction-limiting conditions. Experimental results confirmed high efficacy of the tested catalyst due to unity effectiveness factor and very low Thiele modulus American Chemical Society 2015-08 Article PeerReviewed Kiakalaieh, Talebian and Saidina Amin, Nor Aishah (2015) Kinetic modeling, thermodynamic, and mass-transfer studies of gas-phase glycerol dehydration to acrolein over supported silicotungstic acid catalyst. Industrial & Engineering Chemistry Research, 54 (33). pp. 8113-8121. ISSN 0886-7798 http://dx.doi.org/10.1021/acs.iecr.5b02172 DOI:10.1021/acs.iecr.5b02172 |
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TP Chemical technology Kiakalaieh, Talebian Saidina Amin, Nor Aishah Kinetic modeling, thermodynamic, and mass-transfer studies of gas-phase glycerol dehydration to acrolein over supported silicotungstic acid catalyst |
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The kinetics of gas-phase glycerol dehydration in a packed-bed reactor over a highly active and stable supported silicotungstic acid catalyst with zirconium oxide and nanosized aluminum oxide (30HZ-20A) was investigated. The kinetic study is based on the optimal reaction conditions determined by response surface methodology. The reaction rate followed first-order kinetics with the activation energy and frequency factor, E = 27.5 kJ/mol and A = 5.35 × 105 s-1, respectively. Based on thermodynamic analysis, the values of ΔH° and ΔS° of the endothermic reaction were 14.70 and 0.09 kJ/(mol K), respectively, and ΔG° =-12.12 kJ/mol. The mass-transfer analysis revealed the pellet sizes of dp < 1 µm proceeded under reaction-limiting conditions. Experimental results confirmed high efficacy of the tested catalyst due to unity effectiveness factor and very low Thiele modulus |
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Article |
author |
Kiakalaieh, Talebian Saidina Amin, Nor Aishah |
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Kiakalaieh, Talebian Saidina Amin, Nor Aishah |
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Kiakalaieh, Talebian |
title |
Kinetic modeling, thermodynamic, and mass-transfer studies of gas-phase glycerol dehydration to acrolein over supported silicotungstic acid catalyst |
title_short |
Kinetic modeling, thermodynamic, and mass-transfer studies of gas-phase glycerol dehydration to acrolein over supported silicotungstic acid catalyst |
title_full |
Kinetic modeling, thermodynamic, and mass-transfer studies of gas-phase glycerol dehydration to acrolein over supported silicotungstic acid catalyst |
title_fullStr |
Kinetic modeling, thermodynamic, and mass-transfer studies of gas-phase glycerol dehydration to acrolein over supported silicotungstic acid catalyst |
title_full_unstemmed |
Kinetic modeling, thermodynamic, and mass-transfer studies of gas-phase glycerol dehydration to acrolein over supported silicotungstic acid catalyst |
title_sort |
kinetic modeling, thermodynamic, and mass-transfer studies of gas-phase glycerol dehydration to acrolein over supported silicotungstic acid catalyst |
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American Chemical Society |
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2015 |
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http://eprints.utm.my/id/eprint/58462/ http://dx.doi.org/10.1021/acs.iecr.5b02172 |
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13.211869 |