Techno-economic analysis of low-carbon hydrogen production by sorption enhanced steam methane reforming (SE-SMR) processes
dc.contributor.author | Yan, Yongliang | |
dc.contributor.author | Manovic, Vasilije | |
dc.contributor.author | Anthony, Edward J. | |
dc.contributor.author | Clough, Peter T. | |
dc.date.accessioned | 2020-11-09T11:19:10Z | |
dc.date.available | 2020-11-09T11:19:10Z | |
dc.date.issued | 2020-10-30 | |
dc.description.abstract | Hydrogen is an attractive energy carrier that will play a key role in future global energy transitions. This work investigates the techno-economic performance of six different sorption enhanced steam methane reforming (SE-SMR) configurations integrated with an indirect natural gas or biomass-fired calciner, oxy-fuel combustion and chemical-looping combustion for large-scale blue and carbon-negative hydrogen production. The techno-economic performance of the proposed cases was evaluated by their net efficiency, CO2 capture efficiency, levelised cost of hydrogen (LCOH), and costs of CO2 avoided and removal. A sensitivity analysis was also conducted to evaluate the key parameters and explore existing uncertainties that can affect the economic performance of the proposed SE-SMR processes. The results revealed that the proposed systems were comparable with conventional steam methane reforming (SMR) with carbon capture and storage (CCS). The LCOH of the proposed SE-SMR plants ranged from £1.90–2.80/kg, and the costs of CO2 avoided and removal ranged from £33-69/tonne and £58-107/tonne, respectively. By applying a carbon price (£16/tonne CO2), the costs of CO2 avoided and removal for the proposed SE-SMR processes could be significantly reduced. The results of cumulative discounted cash flow of SE-SMR plants at a hydrogen selling price of £3.00/kg indicated that all the investment of the proposed cases could be paid back after eight years, even if the carbon tax is zero. | en_UK |
dc.identifier.citation | Yan Y, Manovic V, Anthony EJ, Clough PT. (2020) Techno-economic analysis of low-carbon hydrogen production by sorption enhanced steam methane reforming (SE-SMR) processes. Energy Conversion and Management, Volume 226, December 2020, Article number 113530 | en_UK |
dc.identifier.issn | 0196-8904 | |
dc.identifier.uri | https://doi.org/10.1016/j.enconman.2020.113530 | |
dc.identifier.uri | http://dspace.lib.cranfield.ac.uk/handle/1826/15974 | |
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 | Blue hydrogen production | en_UK |
dc.subject | Sorption enhanced steam methane reforming | en_UK |
dc.subject | Carbon capture | en_UK |
dc.subject | Techno-economic analysis | en_UK |
dc.title | Techno-economic analysis of low-carbon hydrogen production by sorption enhanced steam methane reforming (SE-SMR) processes | en_UK |
dc.type | Article | en_UK |
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