Thermodynamic analysis of methanol steam reforming to produce hydrogen for HT-PEMFC: an optimization study
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Methanol steam reforming has a lower reforming temperature (473-573 K) than methane (1073-1273 K).
“Moreover, lower reforming temperature ð473 À573 KÞ than other carbon-based fuels such as methane ð1073 À1273 KÞ makes it suitable for stack integration with HT-PEM fuel cells and results in a lower CO production [1,5].”
From Comparison between 1D and 2D numerical models of a multi-tubular packed-bed reactor for methanol steam reforming (2022) · cites this paper as [1]
The lower reforming temperature of methanol steam reforming makes it suitable for stack integration with HT-PEM fuel cells and results in lower CO production.
“Moreover, lower reforming temperature ð473 À573 KÞ than other carbon-based fuels such as methane ð1073 À1273 KÞ makes it suitable for stack integration with HT-PEM fuel cells and results in a lower CO production [1,5].”
From Comparison between 1D and 2D numerical models of a multi-tubular packed-bed reactor for methanol steam reforming (2022) · cites this paper as [1]
The HT-PEM fuel cell is suitable to be integrated with an in-situ hydrogen production system without purification.
“By operating at a higher temperature, the HT-PEM fuel cell gets an improved tolerance towards carbon monoxide (CO) up to 3À 5% vol [1], making it suitable to be integrated with an in-situ hydrogen production system without purification.”
From Comparison between 1D and 2D numerical models of a multi-tubular packed-bed reactor for methanol steam reforming (2022) · cites this paper as [1]
The HT-PEM fuel cell has an improved tolerance towards carbon monoxide up to 3-5% vol.
“By operating at a higher temperature, the HT-PEM fuel cell gets an improved tolerance towards carbon monoxide (CO) up to 3À 5% vol [1], making it suitable to be integrated with an in-situ hydrogen production system without purification.”
From Comparison between 1D and 2D numerical models of a multi-tubular packed-bed reactor for methanol steam reforming (2022) · cites this paper as [1]
Cited by
Sorted by citations
Large-vscale hydrogen production and storage technologies: Current status and future directions
Olabi, A. G., bahri, A. S., Abdelghafar, A. A., Baroutaji, A., Sayed, E. T., Alami, A. H., Rezk, H., & Abdelkareem, M. A. (2021) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2020.10.110 · Cited by 492 · see citing works
Zhu, J., Cui, X., & Araya, S. S. (2022) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2022.05.109 · Cited by 39 · see citing works
- Authors
- Özcan, O., & Akın, A. N.
- Affiliations
- Kocaeli Üniversitesi (TR)
- Corresponding author
- Özcan, Orhan
- Venue
- International Journal of Hydrogen Energy
- Publisher
- Elsevier BV
- Published
- 2019-05
- Volume
- 44
- Issue
- 27
- Pages
- 14117-14126
- ISSN
- 0360-3199 (ISSN-L)
- OpenAlex
- W2912267116
- Cited by
- 101
- References
- 0
- Citations by year
- 2026: 8 · 2025: 14 · 2024: 13 · 2023: 14 · 2022: 16 · 2021: 15 · 2020: 17 · 2019: 4
- FWCI
- 2.72
- Type
- journal article
- Language
- en
- Open access
- closed
- Locations
- International Journal of Hydrogen Energy (publishedVersion)
- Kocaeli Üniversitesi - AVESİS (publishedVersion)
- Topics
- Physical Sciences › Chemical Engineering › Catalysis › Catalysts for Methane Reforming
- Physical Sciences › Energy › Energy Engineering and Power Technology › Hybrid Renewable Energy Systems
- Physical Sciences › Engineering › Biomedical Engineering › Thermochemical Biomass Conversion Processes
- Keywords
- methanol steam reforming, hydrogen production, high-temperature PEM fuel cells, thermodynamic equilibrium, process parameter optimization, response surface methodology, methanol conversion, carbon monoxide removal, product distribution
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