Kinetics Study of the Hydrodeoxygenation of Xylitol over a ReO<sub>x</sub>-Pd/CeO<sub>2</sub> Catalyst
In this study, we elucidate the reaction kinetics for the simultaneous hydrodeoxygenation of xylitol to 1,2-dideoxypentitol and 1,2,5-pentanetriol over a ReO<sub>x</sub>-Pd/CeO<sub>2</sub> (2.0 weight% Re, 0.30 weight% Pd) catalyst. The reaction was determined to be a zero-or...
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doaj-3342186e585743499812f786973865e52021-01-15T00:01:00ZengMDPI AGCatalysts2073-43442021-01-011110810810.3390/catal11010108Kinetics Study of the Hydrodeoxygenation of Xylitol over a ReO<sub>x</sub>-Pd/CeO<sub>2</sub> CatalystBlake MacQueen0Michael Royko1Bradie S. Crandall2Andreas Heyden3Yomaira J. Pagán-Torres4Jochen Lauterbach5Department of Chemical Engineering, University of South Carolina, 541 Main St., Columbia, SC 29208, USADepartment of Chemical Engineering, University of South Carolina, 541 Main St., Columbia, SC 29208, USADepartment of Chemical Engineering, University of South Carolina, 541 Main St., Columbia, SC 29208, USADepartment of Chemical Engineering, University of South Carolina, 541 Main St., Columbia, SC 29208, USADepartment of Chemical Engineering, University of Puerto Rico-Mayaguez Campus, Mayaguez, Puerto Rico 00681-9000, USADepartment of Chemical Engineering, University of South Carolina, 541 Main St., Columbia, SC 29208, USAIn this study, we elucidate the reaction kinetics for the simultaneous hydrodeoxygenation of xylitol to 1,2-dideoxypentitol and 1,2,5-pentanetriol over a ReO<sub>x</sub>-Pd/CeO<sub>2</sub> (2.0 weight% Re, 0.30 weight% Pd) catalyst. The reaction was determined to be a zero-order reaction with respect to xylitol. The activation energy was elucidated through an Arrhenius relationship as well as non-Arrhenius kinetics. The Arrhenius relationship was investigated at 150–170 °C and a constant H<sub>2</sub> pressure of 10 bar resulting in an activation energy of 48.7 ± 10.5 kJ/mol. The investigation of non-Arrhenius kinetics was conducted at 120–170 °C and a sub-Arrhenius relation was elucidated with activation energy being dependent on temperature, and ranging from 10.2–51.8 kJ/mol in the temperature range investigated. Internal and external mass transfer were investigated through evaluating the Weisz–Prater criterion and the effect of varying stirring rate on the reaction rate, respectively. There were no internal or external mass transfer limitations present in the reaction.https://www.mdpi.com/2073-4344/11/1/108heterogeneous catalysiskineticshydrodeoxygenationxylitolRheniumbiomass upgrading |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Blake MacQueen Michael Royko Bradie S. Crandall Andreas Heyden Yomaira J. Pagán-Torres Jochen Lauterbach |
spellingShingle |
Blake MacQueen Michael Royko Bradie S. Crandall Andreas Heyden Yomaira J. Pagán-Torres Jochen Lauterbach Kinetics Study of the Hydrodeoxygenation of Xylitol over a ReO<sub>x</sub>-Pd/CeO<sub>2</sub> Catalyst Catalysts heterogeneous catalysis kinetics hydrodeoxygenation xylitol Rhenium biomass upgrading |
author_facet |
Blake MacQueen Michael Royko Bradie S. Crandall Andreas Heyden Yomaira J. Pagán-Torres Jochen Lauterbach |
author_sort |
Blake MacQueen |
title |
Kinetics Study of the Hydrodeoxygenation of Xylitol over a ReO<sub>x</sub>-Pd/CeO<sub>2</sub> Catalyst |
title_short |
Kinetics Study of the Hydrodeoxygenation of Xylitol over a ReO<sub>x</sub>-Pd/CeO<sub>2</sub> Catalyst |
title_full |
Kinetics Study of the Hydrodeoxygenation of Xylitol over a ReO<sub>x</sub>-Pd/CeO<sub>2</sub> Catalyst |
title_fullStr |
Kinetics Study of the Hydrodeoxygenation of Xylitol over a ReO<sub>x</sub>-Pd/CeO<sub>2</sub> Catalyst |
title_full_unstemmed |
Kinetics Study of the Hydrodeoxygenation of Xylitol over a ReO<sub>x</sub>-Pd/CeO<sub>2</sub> Catalyst |
title_sort |
kinetics study of the hydrodeoxygenation of xylitol over a reo<sub>x</sub>-pd/ceo<sub>2</sub> catalyst |
publisher |
MDPI AG |
series |
Catalysts |
issn |
2073-4344 |
publishDate |
2021-01-01 |
description |
In this study, we elucidate the reaction kinetics for the simultaneous hydrodeoxygenation of xylitol to 1,2-dideoxypentitol and 1,2,5-pentanetriol over a ReO<sub>x</sub>-Pd/CeO<sub>2</sub> (2.0 weight% Re, 0.30 weight% Pd) catalyst. The reaction was determined to be a zero-order reaction with respect to xylitol. The activation energy was elucidated through an Arrhenius relationship as well as non-Arrhenius kinetics. The Arrhenius relationship was investigated at 150–170 °C and a constant H<sub>2</sub> pressure of 10 bar resulting in an activation energy of 48.7 ± 10.5 kJ/mol. The investigation of non-Arrhenius kinetics was conducted at 120–170 °C and a sub-Arrhenius relation was elucidated with activation energy being dependent on temperature, and ranging from 10.2–51.8 kJ/mol in the temperature range investigated. Internal and external mass transfer were investigated through evaluating the Weisz–Prater criterion and the effect of varying stirring rate on the reaction rate, respectively. There were no internal or external mass transfer limitations present in the reaction. |
topic |
heterogeneous catalysis kinetics hydrodeoxygenation xylitol Rhenium biomass upgrading |
url |
https://www.mdpi.com/2073-4344/11/1/108 |
work_keys_str_mv |
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