Gas product behaviour using flower-like nickel-based MOF catalysts for sustainable hydrogen production from biomass

Biomass pyrolysis offers a promising pathway for converting renewable feedstocks into hydrogen-rich syngas. However, the efficiency of this process depends heavily on the catalyst used. Nickel-based catalysts, while known for their catalytic activity and cost-effectiveness, often face challenges such as deactivation and agglomeration under pyrolysis conditions. To overcome these limitations, this study explores metal-organic frameworks (MOFs) as catalysts, with additional metal promoters to enhance Ni-based systems. Ni-MOF and Ce-Ni-MOF catalysts were synthesized and systematically evaluated, focusing on variables such as catalyst type, temperature, and catalyst-to-biomass ratio. Both catalysts exhibited highly textured, flower-like structures with loosely packed sheets, providing a large surface area for enhanced catalytic reactions . Ni-MOF increased hydrogen production by 96 % (13,785 mL/g, 53.0 vol%) within 10 min compared to non-catalytic conditions. Ce-Ni-MOF showed superior long-term performance, producing 2252 mL/g (44 vol%) of H 2 and achieving 66 % and 76 % higher hydrogen yields than Ni-MOF at 20 and 30 min, respectively. Structural analysis revealed that the catalysts’ flower-like morphology remained intact after pyrolysis, with increased porosity suggesting partial evolution of the MOF structure at high temperatures. Ni-MOF exhibited an increase in nickel loading from 39.8 wt% to 59.5 wt% post-pyrolysis, which further enhanced its catalytic activity. Ce-Ni-MOF displayed a narrower particle size distribution (6–11 nm) and improved stability, with nickel loading only slightly decreasing from 20.7 wt% to 18.4 wt%, maintaining uniformity over time. Both catalysts achieved optimal catalytic activity at a 1:1 catalyst-to-biomass ratio, although Ni-MOF experienced a 61 % reduction in H 2 production at a 1:4 ratio. Higher temperatures (800 °C) further enhanced hydrogen, CO , and CH 4 yields for both catalysts. These findings demonstrate the potential of MOF-based nickel catalysts for advancing renewable hydrogen production, with Ce-Ni-MOF offering enhanced stability and long-term catalytic efficiency under various conditions.

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Publication Details

Journal
Renewable Energy
Published
2025-03-17
DOI
https://doi.org/10.1016/j.renene.2025.122886
Citations
7
Primary Topic
Catalysis and Hydrodesulfurization Studies
Type
article
Field-Weighted Citation Impact
4.99

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article

Gas product behaviour using flower-like nickel-based MOF catalysts for sustainable hydrogen production from biomass

Nabila A. Karim, Salma Samidin, Wan Nor Roslam Wan Isahak, Nowilin James Rubinsin et al.
7 citations
Renewable Energy
Catalysis and Hydrodesulfurization Studies
4.99
article

Gas product behaviour using flower-like nickel-based MOF catalysts for sustainable hydrogen production from biomass

Nabila A. Karim, Salma Samidin, Wan Nor Roslam Wan Isahak, Nowilin James Rubinsin, Manoj Pudukudy, Medhat A. Nemitallah
article en
7 citations

Abstract

Biomass pyrolysis offers a promising pathway for converting renewable feedstocks into hydrogen-rich syngas. However, the efficiency of this process depends heavily on the catalyst used. Nickel-based catalysts, while known for their catalytic activity and cost-effectiveness, often face challenges such as deactivation and agglomeration under pyrolysis conditions. To overcome these limitations, this study explores metal-organic frameworks (MOFs) as catalysts, with additional metal promoters to enhance Ni-based systems. Ni-MOF and Ce-Ni-MOF catalysts were synthesized and systematically evaluated, focusing on variables such as catalyst type, temperature, and catalyst-to-biomass ratio. Both catalysts exhibited highly textured, flower-like structures with loosely packed sheets, providing a large surface area for enhanced catalytic reactions . Ni-MOF increased hydrogen production by 96 % (13,785 mL/g, 53.0 vol%) within 10 min compared to non-catalytic conditions. Ce-Ni-MOF showed superior long-term performance, producing 2252 mL/g (44 vol%) of H 2 and achieving 66 % and 76 % higher hydrogen yields than Ni-MOF at 20 and 30 min, respectively. Structural analysis revealed that the catalysts’ flower-like morphology remained intact after pyrolysis, with increased porosity suggesting partial evolution of the MOF structure at high temperatures. Ni-MOF exhibited an increase in nickel loading from 39.8 wt% to 59.5 wt% post-pyrolysis, which further enhanced its catalytic activity. Ce-Ni-MOF displayed a narrower particle size distribution (6–11 nm) and improved stability, with nickel loading only slightly decreasing from 20.7 wt% to 18.4 wt%, maintaining uniformity over time. Both catalysts achieved optimal catalytic activity at a 1:1 catalyst-to-biomass ratio, although Ni-MOF experienced a 61 % reduction in H 2 production at a 1:4 ratio. Higher temperatures (800 °C) further enhanced hydrogen, CO , and CH 4 yields for both catalysts. These findings demonstrate the potential of MOF-based nickel catalysts for advancing renewable hydrogen production, with Ce-Ni-MOF offering enhanced stability and long-term catalytic efficiency under various conditions.

Renewable EnergyVol. 246
King Fahd University of Petroleum and Minerals (SA), Saveetha University (IN), National University of Malaysia (MY)
Ministry of Higher Education, Malaysia, Universiti Kebangsaan Malaysia
Responsible consumption and production
Openalex Percentile: Top 5%
Catalysis and Hydrodesulfurization Studies
4.99
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