Abstract
Hydrogen (H2) production via steam methane reforming is a mature and cost-effective technology. However, carbon capture and storage is required to decrease its carbon dioxide (CO2) emissions. The adoption of molten carbonate fuel cells as means to capture CO2 from flue gases is attracting scientific interest thanks to their inherent thermodynamic advantage of separating CO2 while producing electricity. This study investigates and benchmarks the performance of an H2 production plant equipped with molten carbonate fuel cell for post-combustion CO2 capture, by proposing a novel configuration where the cell anode is fed with the carbon-rich off-gas from the H2 separation unit. It emerges that the process can achieve higher capture rates than the reference solvent-based plant: 85–90% with single cell, 95% with two-stage cell. Moreover, recycling the carbon-rich off gas to the anode allows for smaller cell area, and potentially lower H2 production costs compared to the benchmark.
Original language | English |
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Pages (from-to) | 37366-37384 |
Number of pages | 19 |
Journal | International Journal of Hydrogen Energy |
Volume | 48 |
Issue number | 95 |
Early online date | 27 Jun 2023 |
DOIs | |
Publication status | Published - 8 Dec 2023 |
Bibliographical note
Publisher Copyright:© 2023 Hydrogen Energy Publications LLC
Funding
This work has been funded by TotalEnergies' R&D Strategic Anticipation Program.
Funders | Funder number |
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TotalEnergies' R&D Strategic Anticipation Program |
Keywords
- steam methane reformer
- molten carbonate fuel cell
- carbon dioxide capture
- process simulation
- Techno-economic modelling