Highly Active Catalysts Based on the Rh<sub>4</sub>(CO)<sub>12</sub> Cluster Supported on Ce<sub>0.5</sub>Zr<sub>0.5</sub> and Zr Oxides for Low-Temperature Methane Steam Reforming

Syngas and Hydrogen productions from methane are industrially carried out at high temperatures (900 &#176;C). Nevertheless, low-temperature steam reforming can be an alternative for small-scale plants. In these conditions, the process can also be coupled with systems that increase the overall ef...

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Main Authors: Andrea Fasolini, Silvia Ruggieri, Cristina Femoni, Francesco Basile
Format: Article
Language:English
Published: MDPI AG 2019-09-01
Series:Catalysts
Subjects:
Online Access:https://www.mdpi.com/2073-4344/9/10/800
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spelling doaj-54444743c153440fa4dce0429fe23d8f2020-11-25T01:35:04ZengMDPI AGCatalysts2073-43442019-09-0191080010.3390/catal9100800catal9100800Highly Active Catalysts Based on the Rh<sub>4</sub>(CO)<sub>12</sub> Cluster Supported on Ce<sub>0.5</sub>Zr<sub>0.5</sub> and Zr Oxides for Low-Temperature Methane Steam ReformingAndrea Fasolini0Silvia Ruggieri1Cristina Femoni2Francesco Basile3Department of Industrial Chemistry “Toso Montanari”, University of Bologna, V.le Risorgimento, 4, 40136 Bologna, ItalyDepartment of Industrial Chemistry “Toso Montanari”, University of Bologna, V.le Risorgimento, 4, 40136 Bologna, ItalyDepartment of Industrial Chemistry “Toso Montanari”, University of Bologna, V.le Risorgimento, 4, 40136 Bologna, ItalyDepartment of Industrial Chemistry “Toso Montanari”, University of Bologna, V.le Risorgimento, 4, 40136 Bologna, ItalySyngas and Hydrogen productions from methane are industrially carried out at high temperatures (900 &#176;C). Nevertheless, low-temperature steam reforming can be an alternative for small-scale plants. In these conditions, the process can also be coupled with systems that increase the overall efficiency such as hydrogen purification with membranes, microreactors or enhanced reforming with CO<sub>2</sub> capture. However, at low temperature, in order to get conversion values close to the equilibrium ones, very active catalysts are needed. For this purpose, the Rh<sub>4</sub>(CO)<sub>12</sub> cluster was synthetized and deposited over Ce<sub>0.5</sub>Zr<sub>0.5</sub>O<sub>2</sub> and ZrO<sub>2</sub> supports, prepared by microemulsion, and tested in low-temperature steam methane reforming reactions under different conditions. The catalysts were active at 750 &#176;C at low Rh loadings (0.05%) and outperformed an analogous Rh-impregnated catalyst. At higher Rh concentrations (0.6%), the Rh cluster deposited on Ce<sub>0.5</sub>Zr<sub>0.5</sub> oxide reached conversions close to the equilibrium values and good stability over long reaction time, demonstrating that active phases derived from Rh carbonyl clusters can be used to catalyze steam reforming reactions. Conversely, the same catalyst suffered from a fast deactivation at 500 &#176;C, likely related to the oxidation of the Rh phase due to the oxygen-mobility properties of Ce. Indeed, at 500 &#176;C the Rh-based ZrO<sub>2</sub>-supported catalyst was able to provide stable results with higher conversions. The effects of different pretreatments were also investigated: at 500 &#176;C, the catalysts subjected to thermal treatment, both under N<sub>2</sub> and H<sub>2</sub>, proved to be more active than those without the H<sub>2</sub> treatment. In general, this work highlights the possibility of using Rh carbonyl-cluster-derived supported catalysts in methane reforming reactions and, at low temperature, it showed deactivation phenomena related to the presence of reducible supports.https://www.mdpi.com/2073-4344/9/10/800hydrogenlow temperature steam reformingrh<sub>4</sub>(co)<sub>12</sub> clustermicroemulsion synthesiscezr oxidezr oxide
collection DOAJ
language English
format Article
sources DOAJ
author Andrea Fasolini
Silvia Ruggieri
Cristina Femoni
Francesco Basile
spellingShingle Andrea Fasolini
Silvia Ruggieri
Cristina Femoni
Francesco Basile
Highly Active Catalysts Based on the Rh<sub>4</sub>(CO)<sub>12</sub> Cluster Supported on Ce<sub>0.5</sub>Zr<sub>0.5</sub> and Zr Oxides for Low-Temperature Methane Steam Reforming
Catalysts
hydrogen
low temperature steam reforming
rh<sub>4</sub>(co)<sub>12</sub> cluster
microemulsion synthesis
cezr oxide
zr oxide
author_facet Andrea Fasolini
Silvia Ruggieri
Cristina Femoni
Francesco Basile
author_sort Andrea Fasolini
title Highly Active Catalysts Based on the Rh<sub>4</sub>(CO)<sub>12</sub> Cluster Supported on Ce<sub>0.5</sub>Zr<sub>0.5</sub> and Zr Oxides for Low-Temperature Methane Steam Reforming
title_short Highly Active Catalysts Based on the Rh<sub>4</sub>(CO)<sub>12</sub> Cluster Supported on Ce<sub>0.5</sub>Zr<sub>0.5</sub> and Zr Oxides for Low-Temperature Methane Steam Reforming
title_full Highly Active Catalysts Based on the Rh<sub>4</sub>(CO)<sub>12</sub> Cluster Supported on Ce<sub>0.5</sub>Zr<sub>0.5</sub> and Zr Oxides for Low-Temperature Methane Steam Reforming
title_fullStr Highly Active Catalysts Based on the Rh<sub>4</sub>(CO)<sub>12</sub> Cluster Supported on Ce<sub>0.5</sub>Zr<sub>0.5</sub> and Zr Oxides for Low-Temperature Methane Steam Reforming
title_full_unstemmed Highly Active Catalysts Based on the Rh<sub>4</sub>(CO)<sub>12</sub> Cluster Supported on Ce<sub>0.5</sub>Zr<sub>0.5</sub> and Zr Oxides for Low-Temperature Methane Steam Reforming
title_sort highly active catalysts based on the rh<sub>4</sub>(co)<sub>12</sub> cluster supported on ce<sub>0.5</sub>zr<sub>0.5</sub> and zr oxides for low-temperature methane steam reforming
publisher MDPI AG
series Catalysts
issn 2073-4344
publishDate 2019-09-01
description Syngas and Hydrogen productions from methane are industrially carried out at high temperatures (900 &#176;C). Nevertheless, low-temperature steam reforming can be an alternative for small-scale plants. In these conditions, the process can also be coupled with systems that increase the overall efficiency such as hydrogen purification with membranes, microreactors or enhanced reforming with CO<sub>2</sub> capture. However, at low temperature, in order to get conversion values close to the equilibrium ones, very active catalysts are needed. For this purpose, the Rh<sub>4</sub>(CO)<sub>12</sub> cluster was synthetized and deposited over Ce<sub>0.5</sub>Zr<sub>0.5</sub>O<sub>2</sub> and ZrO<sub>2</sub> supports, prepared by microemulsion, and tested in low-temperature steam methane reforming reactions under different conditions. The catalysts were active at 750 &#176;C at low Rh loadings (0.05%) and outperformed an analogous Rh-impregnated catalyst. At higher Rh concentrations (0.6%), the Rh cluster deposited on Ce<sub>0.5</sub>Zr<sub>0.5</sub> oxide reached conversions close to the equilibrium values and good stability over long reaction time, demonstrating that active phases derived from Rh carbonyl clusters can be used to catalyze steam reforming reactions. Conversely, the same catalyst suffered from a fast deactivation at 500 &#176;C, likely related to the oxidation of the Rh phase due to the oxygen-mobility properties of Ce. Indeed, at 500 &#176;C the Rh-based ZrO<sub>2</sub>-supported catalyst was able to provide stable results with higher conversions. The effects of different pretreatments were also investigated: at 500 &#176;C, the catalysts subjected to thermal treatment, both under N<sub>2</sub> and H<sub>2</sub>, proved to be more active than those without the H<sub>2</sub> treatment. In general, this work highlights the possibility of using Rh carbonyl-cluster-derived supported catalysts in methane reforming reactions and, at low temperature, it showed deactivation phenomena related to the presence of reducible supports.
topic hydrogen
low temperature steam reforming
rh<sub>4</sub>(co)<sub>12</sub> cluster
microemulsion synthesis
cezr oxide
zr oxide
url https://www.mdpi.com/2073-4344/9/10/800
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