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...
Gespeichert in:
Veröffentlicht in: | Applied energy 2022-02, Vol.307, p.118183, Article 118183 |
---|---|
Hauptverfasser: | , , , , , , |
Format: | Artikel |
Sprache: | eng |
Schlagworte: | |
Online-Zugang: | Volltext |
Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
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 |