Economically feasible decarbonization of the Haber-Bosch process through supercritical CO2 Allam cycle integration

[Display omitted] •Novel concept for supercritical CO2-Haber-Bosch integrated process is presented.•Comprehensive process simulation in Aspen Plus of two distinct design cases.•Techno-economic analysis at scales of 1.5, 15, and 150 ton h−1 NH3 is performed.•Both cases of the integrated process show...

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Veröffentlicht in:Applied energy 2022-02, Vol.307, p.118183, Article 118183
Hauptverfasser: Byun, Manhee, Lim, Dongjun, Lee, Boreum, Kim, Ayeon, Lee, In-Beum, Brigljević, Boris, Lim, Hankwon
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Sprache:eng
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Zusammenfassung:[Display omitted] •Novel concept for supercritical CO2-Haber-Bosch integrated process is presented.•Comprehensive process simulation in Aspen Plus of two distinct design cases.•Techno-economic analysis at scales of 1.5, 15, and 150 ton h−1 NH3 is performed.•Both cases of the integrated process show profitability at scales >5 ton h−1 NH3.•Significant gaseous CO2 emission reduction of 68%-96% compared to conventional HB. The well-established Haber-Bosch (HB) process (industrial ammonia production) is a significant contributor to the world’s carbon emissions as it is a major consumer of natural gas as well as being energy-intensive in general. This work addresses the challenge of decarbonizing the HB process in a novel way as it, for the first time, presents a conceptual process integration with a supercritical CO2 Allam power cycle, therefore transforming gaseous CO2 emissions into a valuable side product in a form of liquid CO2. Detailed process design and flowsheet simulation using Aspen Plus ® was used as a basis for scale-up and techno-economic assessment of two cases (electrical grid dependent and independent). The results indicated that using this process design NH3 production reaches profitability at scales larger than 2 ton h−1 to 5.4 ton h−1 and at current global NH3 prices, the cost of manufacturing decrease, due to scale-up stabilizes at ∼ 30 ton h−1. Finally, this novel process integration achieves a significant reduction in gaseous CO2 emissions (compared to conventional HB process) of 68 % to 96 %, which indicates great potential for economically feasible green NH3.
ISSN:0306-2619
1872-9118
DOI:10.1016/j.apenergy.2021.118183