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• W4313537056 abstract "This work introduces a new process concept for the conversion of CO2 to gas-to liquid (GTL) products. CO2 is first reformed to syngas via the reverse water gas shift reaction using hydrogen produced by catalytic thermal decomposition of CH4 in a Cu-Bi molten media. The produced syngas is then used to manufacture 30,000 bbl per day of syncrude in a low temperature Fischer-Tropsch reactor. The carbon and energy efficiencies of the GTL plant are 85 % and 35 %, respectively. The plant emits 21.1 g of CO2 per 1 MJ of syncrude when considering upstream emissions associated with the supply of natural gas and CO2 feed streams. This is at least 48 % lower than the CO2 emissions of GTL plants that reform CH4 to syngas, but is higher than water electrolysis-based GTL plants. The fixed capital investment of the plant and the manufacturing cost of syncrude are $1.81 billion and $140 bbl−1, respectively. The levelized price of the produced solid carbon is estimated to be $720 tonne-1 for a syncrude market price of $59 bbl−1." @default.
• W4313537056 created "2023-01-06" @default.
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• W4313537056 date "2023-01-01" @default.
• W4313537056 modified "2023-09-27" @default.
• W4313537056 title "Process design and techno-economic analysis of CO2 reformation to synthetic crude oil using H2 produced by decomposition of CH4 in a molten media" @default.
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• W4313537056 doi "https://doi.org/10.1016/j.enconman.2022.116548" @default.
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