Renewable Hydrogen Production with Steam Reforming of Ethanol Using Siliceous Mesocellular Foam‐Supported Nickel Catalysts

Nickel (Ni) catalysts loaded on siliceous mesocellular foam (MCF‐S) are synthesized via the wet impregnation method with 3, 5, 10, and 15 wt% NiO loadings and different aging levels (no, partial, and full ageing) to determine how both factors affect the progress of the ethanol steam reforming (ESR)...

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Main Authors: Pradeep S. Murthy, Igor R. K. Rombaut, Huajuan Ling, Yongwen Tao, Mengjing Ye, Fangyuan Chen, Jun Huang
Format: Article
Language:English
Published: Wiley-VCH 2023-11-01
Series:Advanced Energy & Sustainability Research
Subjects:
Online Access:https://doi.org/10.1002/aesr.202300064
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author Pradeep S. Murthy
Igor R. K. Rombaut
Huajuan Ling
Yongwen Tao
Mengjing Ye
Fangyuan Chen
Jun Huang
author_facet Pradeep S. Murthy
Igor R. K. Rombaut
Huajuan Ling
Yongwen Tao
Mengjing Ye
Fangyuan Chen
Jun Huang
author_sort Pradeep S. Murthy
collection DOAJ
description Nickel (Ni) catalysts loaded on siliceous mesocellular foam (MCF‐S) are synthesized via the wet impregnation method with 3, 5, 10, and 15 wt% NiO loadings and different aging levels (no, partial, and full ageing) to determine how both factors affect the progress of the ethanol steam reforming (ESR) reaction. After extensive material characterization testing to determine material porosity, crystallinity, and Ni metal particle size and spatial location, as well as reaction testing at 300–700 °C and 4 H2O: 1 EtOH molar ratio, the fully aged 10 wt% Ni/MCF‐S possesses the strongest structural stability and catalytic activity, reaching 100% EtOH conversion and 68% H2 selectivity at 700 °C. The aging disperses and embeds more Ni nanoparticles within the walls of the mesopores, which promote the ESR reaction from easier diffusion and more active site contact within the pores. Furthermore, the catalyst reveals little signs of deactivation, as the structure remains virtually unchanged, and any coke formed is on the silica support and not over the Ni nanoparticles after the ESR reaction. Such results have demonstrated a proven applicability for ESR and a further need to research about aging effects toward improving structural properties and the catalytic reaction activity.
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spelling doaj.art-bd90c3a1e26643758537c097892209b32023-11-08T09:38:04ZengWiley-VCHAdvanced Energy & Sustainability Research2699-94122023-11-01411n/an/a10.1002/aesr.202300064Renewable Hydrogen Production with Steam Reforming of Ethanol Using Siliceous Mesocellular Foam‐Supported Nickel CatalystsPradeep S. Murthy0Igor R. K. Rombaut1Huajuan Ling2Yongwen Tao3Mengjing Ye4Fangyuan Chen5Jun Huang6School of Chemical and Biomolecular Engineering Sydney Nano Institute The University of Sydney Sydney NSW 2006 AustraliaSchool of Chemical and Biomolecular Engineering Sydney Nano Institute The University of Sydney Sydney NSW 2006 AustraliaSchool of Chemical and Biomolecular Engineering Sydney Nano Institute The University of Sydney Sydney NSW 2006 AustraliaSchool of Chemical and Biomolecular Engineering Sydney Nano Institute The University of Sydney Sydney NSW 2006 AustraliaSchool of Chemical and Biomolecular Engineering Sydney Nano Institute The University of Sydney Sydney NSW 2006 AustraliaYunnan Key Lab of Soil Carbon Sequestration and Pollution Control Faculty of Environmental Science and Engineering Kunming University of Science and Technology Kunming 680500 ChinaSchool of Chemical and Biomolecular Engineering Sydney Nano Institute The University of Sydney Sydney NSW 2006 AustraliaNickel (Ni) catalysts loaded on siliceous mesocellular foam (MCF‐S) are synthesized via the wet impregnation method with 3, 5, 10, and 15 wt% NiO loadings and different aging levels (no, partial, and full ageing) to determine how both factors affect the progress of the ethanol steam reforming (ESR) reaction. After extensive material characterization testing to determine material porosity, crystallinity, and Ni metal particle size and spatial location, as well as reaction testing at 300–700 °C and 4 H2O: 1 EtOH molar ratio, the fully aged 10 wt% Ni/MCF‐S possesses the strongest structural stability and catalytic activity, reaching 100% EtOH conversion and 68% H2 selectivity at 700 °C. The aging disperses and embeds more Ni nanoparticles within the walls of the mesopores, which promote the ESR reaction from easier diffusion and more active site contact within the pores. Furthermore, the catalyst reveals little signs of deactivation, as the structure remains virtually unchanged, and any coke formed is on the silica support and not over the Ni nanoparticles after the ESR reaction. Such results have demonstrated a proven applicability for ESR and a further need to research about aging effects toward improving structural properties and the catalytic reaction activity.https://doi.org/10.1002/aesr.202300064ethanol steam reforminghydrogen productionsiliceous mesocellular foamNi
spellingShingle Pradeep S. Murthy
Igor R. K. Rombaut
Huajuan Ling
Yongwen Tao
Mengjing Ye
Fangyuan Chen
Jun Huang
Renewable Hydrogen Production with Steam Reforming of Ethanol Using Siliceous Mesocellular Foam‐Supported Nickel Catalysts
Advanced Energy & Sustainability Research
ethanol steam reforming
hydrogen production
siliceous mesocellular foam
Ni
title Renewable Hydrogen Production with Steam Reforming of Ethanol Using Siliceous Mesocellular Foam‐Supported Nickel Catalysts
title_full Renewable Hydrogen Production with Steam Reforming of Ethanol Using Siliceous Mesocellular Foam‐Supported Nickel Catalysts
title_fullStr Renewable Hydrogen Production with Steam Reforming of Ethanol Using Siliceous Mesocellular Foam‐Supported Nickel Catalysts
title_full_unstemmed Renewable Hydrogen Production with Steam Reforming of Ethanol Using Siliceous Mesocellular Foam‐Supported Nickel Catalysts
title_short Renewable Hydrogen Production with Steam Reforming of Ethanol Using Siliceous Mesocellular Foam‐Supported Nickel Catalysts
title_sort renewable hydrogen production with steam reforming of ethanol using siliceous mesocellular foam supported nickel catalysts
topic ethanol steam reforming
hydrogen production
siliceous mesocellular foam
Ni
url https://doi.org/10.1002/aesr.202300064
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