Cargando…

Coke Formation during Propane Dehydrogenation over Ga−Rh Supported Catalytically Active Liquid Metal Solutions

Supported Catalytically Active Liquid Metal Solutions (SCALMS) were recently described as a new class of heterogeneous catalysts, where the catalytic transformation takes place at the highly dynamic interface of a liquid alloy. Their application in alkane dehydrogenation has been claimed to be super...

Descripción completa

Detalles Bibliográficos
Autores principales: Wolf, Moritz, Raman, Narayanan, Taccardi, Nicola, Haumann, Marco, Wasserscheid, Peter
Formato: Online Artículo Texto
Lenguaje:English
Publicado: John Wiley and Sons Inc. 2020
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7074060/
https://www.ncbi.nlm.nih.gov/pubmed/32194874
http://dx.doi.org/10.1002/cctc.201901922
_version_ 1783506752925335552
author Wolf, Moritz
Raman, Narayanan
Taccardi, Nicola
Haumann, Marco
Wasserscheid, Peter
author_facet Wolf, Moritz
Raman, Narayanan
Taccardi, Nicola
Haumann, Marco
Wasserscheid, Peter
author_sort Wolf, Moritz
collection PubMed
description Supported Catalytically Active Liquid Metal Solutions (SCALMS) were recently described as a new class of heterogeneous catalysts, where the catalytic transformation takes place at the highly dynamic interface of a liquid alloy. Their application in alkane dehydrogenation has been claimed to be superior to classical heterogeneous catalysts, because the single atom nature of Rh dissolved in liquid Ga hinders the formation of significant amounts of coke, e. g. by oligomerisation of carbon fragments and excessive dehydrogenation. In the present study, we investigate the coking behaviour of Ga−Rh SCALMS during dehydrogenation of propane in detail by means of high‐resolution thermogravimetry. We report that the application of Ga−Rh SCALMS indeed limits the formation of coke when compared to the Ga‐free Rh catalyst, in particular when relating coke formation to the catalytic performance. Furthermore, the formed coke has been shown to be highly reactive during temperature programmed oxidation in 21 % O(2)/He with onset temperatures of approx. 150 °C enabling a regeneration of the Ga−Rh SCALMS system under mild conditions. The activation energy of the oxidation lies in the lower range of values reported for spent cracking catalysts. Monitoring the formation of coke and performance of SCALMS in situ via thermogravimetry coupled with mass spectrometry revealed the continuous formation of coke, which becomes the only process affecting the net weight change after a certain time on stream.
format Online
Article
Text
id pubmed-7074060
institution National Center for Biotechnology Information
language English
publishDate 2020
publisher John Wiley and Sons Inc.
record_format MEDLINE/PubMed
spelling pubmed-70740602020-03-17 Coke Formation during Propane Dehydrogenation over Ga−Rh Supported Catalytically Active Liquid Metal Solutions Wolf, Moritz Raman, Narayanan Taccardi, Nicola Haumann, Marco Wasserscheid, Peter ChemCatChem Full Papers Supported Catalytically Active Liquid Metal Solutions (SCALMS) were recently described as a new class of heterogeneous catalysts, where the catalytic transformation takes place at the highly dynamic interface of a liquid alloy. Their application in alkane dehydrogenation has been claimed to be superior to classical heterogeneous catalysts, because the single atom nature of Rh dissolved in liquid Ga hinders the formation of significant amounts of coke, e. g. by oligomerisation of carbon fragments and excessive dehydrogenation. In the present study, we investigate the coking behaviour of Ga−Rh SCALMS during dehydrogenation of propane in detail by means of high‐resolution thermogravimetry. We report that the application of Ga−Rh SCALMS indeed limits the formation of coke when compared to the Ga‐free Rh catalyst, in particular when relating coke formation to the catalytic performance. Furthermore, the formed coke has been shown to be highly reactive during temperature programmed oxidation in 21 % O(2)/He with onset temperatures of approx. 150 °C enabling a regeneration of the Ga−Rh SCALMS system under mild conditions. The activation energy of the oxidation lies in the lower range of values reported for spent cracking catalysts. Monitoring the formation of coke and performance of SCALMS in situ via thermogravimetry coupled with mass spectrometry revealed the continuous formation of coke, which becomes the only process affecting the net weight change after a certain time on stream. John Wiley and Sons Inc. 2020-01-07 2020-02-20 /pmc/articles/PMC7074060/ /pubmed/32194874 http://dx.doi.org/10.1002/cctc.201901922 Text en © 2019 The Authors. Published by Wiley-VCH Verlag GmbH & Co. KGaA. This is an open access article under the terms of the http://creativecommons.org/licenses/by-nc/4.0/ License, which permits use, distribution and reproduction in any medium, provided the original work is properly cited and is not used for commercial purposes.
spellingShingle Full Papers
Wolf, Moritz
Raman, Narayanan
Taccardi, Nicola
Haumann, Marco
Wasserscheid, Peter
Coke Formation during Propane Dehydrogenation over Ga−Rh Supported Catalytically Active Liquid Metal Solutions
title Coke Formation during Propane Dehydrogenation over Ga−Rh Supported Catalytically Active Liquid Metal Solutions
title_full Coke Formation during Propane Dehydrogenation over Ga−Rh Supported Catalytically Active Liquid Metal Solutions
title_fullStr Coke Formation during Propane Dehydrogenation over Ga−Rh Supported Catalytically Active Liquid Metal Solutions
title_full_unstemmed Coke Formation during Propane Dehydrogenation over Ga−Rh Supported Catalytically Active Liquid Metal Solutions
title_short Coke Formation during Propane Dehydrogenation over Ga−Rh Supported Catalytically Active Liquid Metal Solutions
title_sort coke formation during propane dehydrogenation over ga−rh supported catalytically active liquid metal solutions
topic Full Papers
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7074060/
https://www.ncbi.nlm.nih.gov/pubmed/32194874
http://dx.doi.org/10.1002/cctc.201901922
work_keys_str_mv AT wolfmoritz cokeformationduringpropanedehydrogenationovergarhsupportedcatalyticallyactiveliquidmetalsolutions
AT ramannarayanan cokeformationduringpropanedehydrogenationovergarhsupportedcatalyticallyactiveliquidmetalsolutions
AT taccardinicola cokeformationduringpropanedehydrogenationovergarhsupportedcatalyticallyactiveliquidmetalsolutions
AT haumannmarco cokeformationduringpropanedehydrogenationovergarhsupportedcatalyticallyactiveliquidmetalsolutions
AT wasserscheidpeter cokeformationduringpropanedehydrogenationovergarhsupportedcatalyticallyactiveliquidmetalsolutions