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A computational-experimental investigation on high ethylene selectivity in ethanol dehydration reaction found on WO(x)/ZrO(2)-activated carbon bi-support systems
The high ethylene selectivity exhibited on the zirconia-activated-carbon bi-support catalyst is investigated by experiment and density functional theory–based (DFT) analysis. This bi-support catalyst systems prepared by the physical mixing method for the tungsten catalyst show a significant increase...
Autores principales: | , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
Nature Publishing Group UK
2019
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Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6930307/ https://www.ncbi.nlm.nih.gov/pubmed/31875002 http://dx.doi.org/10.1038/s41598-019-56373-3 |
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author | Rittiruam, Meena Jongsomjit, Bunjerd Praserthdam, Supareak |
author_facet | Rittiruam, Meena Jongsomjit, Bunjerd Praserthdam, Supareak |
author_sort | Rittiruam, Meena |
collection | PubMed |
description | The high ethylene selectivity exhibited on the zirconia-activated-carbon bi-support catalyst is investigated by experiment and density functional theory–based (DFT) analysis. This bi-support catalyst systems prepared by the physical mixing method for the tungsten catalyst show a significant increase in ethylene selectivity up to 90% compared to the zirconia single support system (~58%) during the ethanol dehydration reaction. Besides, the optimal percent weight ratio of zirconia to activated carbon, which results in the highest ethanol conversion is 50:50. The DFT–based analysis is used to investigate high ethylene selectivity in the bi-support system. It shows that the WO(5)/zirconia is the most stable model for the zirconia single-support tungsten catalyst represented by the zirconia (101) facet of the tetrahedral phase. The carbon atoms were added to the WO(5)/zirconia to model the tungsten catalyst on the bi-support system. The Bader charge analysis is carried out to determine the electron transfer in the catalyst. The bonding between ethylene and the WO(5) active site on the catalyst is weakened when the system is bi-support, where the added carbon atoms on the catalyst in the ZrO(2) region decrease the ethylene adsorption energy. Thus, the desorption and the selectivity of ethylene are promoted. The decrease in adsorption energy can be explained via the analysis of the projected density of states (PDOS) profiles of atom involving the adsorption. It was found that the added carbon in the ZrO(2) region induces the electron transfer from the ethylene molecule to the surface, especially to the ZrO(2) region. The depletion of the electron around the ethylene molecule weakens the bonds, thus, promote desorption. Hence, the advantages of using the bi-support system in the tungsten catalyst are that the catalyst exhibit (1) high conversion due to the zirconia support and (2) high ethylene selectivity due to the added carbon promoting the desorption of ethylene via the induction of electron from an ethylene molecule to surface. |
format | Online Article Text |
id | pubmed-6930307 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2019 |
publisher | Nature Publishing Group UK |
record_format | MEDLINE/PubMed |
spelling | pubmed-69303072019-12-27 A computational-experimental investigation on high ethylene selectivity in ethanol dehydration reaction found on WO(x)/ZrO(2)-activated carbon bi-support systems Rittiruam, Meena Jongsomjit, Bunjerd Praserthdam, Supareak Sci Rep Article The high ethylene selectivity exhibited on the zirconia-activated-carbon bi-support catalyst is investigated by experiment and density functional theory–based (DFT) analysis. This bi-support catalyst systems prepared by the physical mixing method for the tungsten catalyst show a significant increase in ethylene selectivity up to 90% compared to the zirconia single support system (~58%) during the ethanol dehydration reaction. Besides, the optimal percent weight ratio of zirconia to activated carbon, which results in the highest ethanol conversion is 50:50. The DFT–based analysis is used to investigate high ethylene selectivity in the bi-support system. It shows that the WO(5)/zirconia is the most stable model for the zirconia single-support tungsten catalyst represented by the zirconia (101) facet of the tetrahedral phase. The carbon atoms were added to the WO(5)/zirconia to model the tungsten catalyst on the bi-support system. The Bader charge analysis is carried out to determine the electron transfer in the catalyst. The bonding between ethylene and the WO(5) active site on the catalyst is weakened when the system is bi-support, where the added carbon atoms on the catalyst in the ZrO(2) region decrease the ethylene adsorption energy. Thus, the desorption and the selectivity of ethylene are promoted. The decrease in adsorption energy can be explained via the analysis of the projected density of states (PDOS) profiles of atom involving the adsorption. It was found that the added carbon in the ZrO(2) region induces the electron transfer from the ethylene molecule to the surface, especially to the ZrO(2) region. The depletion of the electron around the ethylene molecule weakens the bonds, thus, promote desorption. Hence, the advantages of using the bi-support system in the tungsten catalyst are that the catalyst exhibit (1) high conversion due to the zirconia support and (2) high ethylene selectivity due to the added carbon promoting the desorption of ethylene via the induction of electron from an ethylene molecule to surface. Nature Publishing Group UK 2019-12-24 /pmc/articles/PMC6930307/ /pubmed/31875002 http://dx.doi.org/10.1038/s41598-019-56373-3 Text en © The Author(s) 2019 Open Access This article is licensed under a Creative Commons Attribution 4.0 International License, which permits use, sharing, adaptation, distribution and reproduction in any medium or format, as long as you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons license, and indicate if changes were made. The images or other third party material in this article are included in the article’s Creative Commons license, unless indicated otherwise in a credit line to the material. If material is not included in the article’s Creative Commons license and your intended use is not permitted by statutory regulation or exceeds the permitted use, you will need to obtain permission directly from the copyright holder. To view a copy of this license, visit http://creativecommons.org/licenses/by/4.0/. |
spellingShingle | Article Rittiruam, Meena Jongsomjit, Bunjerd Praserthdam, Supareak A computational-experimental investigation on high ethylene selectivity in ethanol dehydration reaction found on WO(x)/ZrO(2)-activated carbon bi-support systems |
title | A computational-experimental investigation on high ethylene selectivity in ethanol dehydration reaction found on WO(x)/ZrO(2)-activated carbon bi-support systems |
title_full | A computational-experimental investigation on high ethylene selectivity in ethanol dehydration reaction found on WO(x)/ZrO(2)-activated carbon bi-support systems |
title_fullStr | A computational-experimental investigation on high ethylene selectivity in ethanol dehydration reaction found on WO(x)/ZrO(2)-activated carbon bi-support systems |
title_full_unstemmed | A computational-experimental investigation on high ethylene selectivity in ethanol dehydration reaction found on WO(x)/ZrO(2)-activated carbon bi-support systems |
title_short | A computational-experimental investigation on high ethylene selectivity in ethanol dehydration reaction found on WO(x)/ZrO(2)-activated carbon bi-support systems |
title_sort | computational-experimental investigation on high ethylene selectivity in ethanol dehydration reaction found on wo(x)/zro(2)-activated carbon bi-support systems |
topic | Article |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6930307/ https://www.ncbi.nlm.nih.gov/pubmed/31875002 http://dx.doi.org/10.1038/s41598-019-56373-3 |
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