Modelling of an integrated process for atmospheric carbon dioxide capture and methanation
dc.contributor.author | Tregambi, Claudio | |
dc.contributor.author | Bareschino, Piero | |
dc.contributor.author | Hanak, Dawid P. | |
dc.contributor.author | Montagnaro, Fabio | |
dc.contributor.author | Pepe, Francesco | |
dc.contributor.author | Mancusi, Erasmo | |
dc.date.accessioned | 2022-06-14T08:28:35Z | |
dc.date.available | 2022-06-14T08:28:35Z | |
dc.date.issued | 2022-04-29 | |
dc.description.abstract | Negative-emission technologies are largely investigated to better control atmospheric carbon dioxide concentration driving global warming. Calcium looping has been proposed in literature for direct air capture, but a comprehensive system analysis is still missing. Methanation of carbon dioxide can represent an alternative to geological storage, widely investigated within the power-to-gas framework. In this study, an integrated process considering the catalytic methanation of the concentrated carbon dioxide stream after capture from ambient air by a pure hydrogen stream from water electrolysis was proposed and numerically investigated. The system relies on packed bed reactors and uses calcium oxide as sorbent, and a nickel-based catalyst for methanation. A comprehensive study on the overall system performance was carried out, assuming a carbon dioxide capture target of 100 t y−1. Model computations suggest that roughly 50-in-parallel reactors, 0.5 m diameter each, are required for a continuous operation. The overall energy demand of the integrated process ranges within 344–370 GJ tCH4−1, or 215–293 GJ tCH4−1 if neglecting the humidifier. The methanation process requires 3-in-series reactors and can yield a continuous gas stream with a flow rate of 5 kg h−1 and a methane molar fraction of nearly 91%. If this stream is exploited for heat generation, a return of energy index of 16%, or 23% if neglecting the humidifier, is foreseen. The proposed process stems as viable solution towards a circular carbon economy. | en_UK |
dc.identifier.citation | Tregambi C, Bareschino P, Hanak D, et al., (2022) Modelling of an integrated process for atmospheric carbon dioxide capture and methanation. Journal of Cleaner Production, Volume 356, July 2022, Article number 131827 | en_UK |
dc.identifier.issn | 0959-6526 | |
dc.identifier.uri | https://doi.org/10.1016/j.jclepro.2022.131827 | |
dc.identifier.uri | http://dspace.lib.cranfield.ac.uk/handle/1826/18019 | |
dc.language.iso | en | en_UK |
dc.publisher | Elsevier | en_UK |
dc.rights | Attribution-NonCommercial-NoDerivatives 4.0 International | * |
dc.rights.uri | http://creativecommons.org/licenses/by-nc-nd/4.0/ | * |
dc.subject | Calcium looping | en_UK |
dc.subject | Carbon capture and utilization | en_UK |
dc.subject | Direct air capture | en_UK |
dc.subject | Limestone | en_UK |
dc.subject | Power to gas | en_UK |
dc.subject | Renewable energy | en_UK |
dc.title | Modelling of an integrated process for atmospheric carbon dioxide capture and methanation | en_UK |
dc.type | Article | en_UK |
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