Thermodynamic and preliminary techno-economic analysis of NH3 utilization in combined cycle power plant: Comparison of direct liquid, vaporized, and cracked NH3-Based combustion methods

Ammonia (NH 3 ) is gaining attention as a promising carbon-free fuel for gas turbine combined cycle (GTCC) power generation. However, its effective utilization requires a thorough understanding of combustion characteristics, emissions, and economic feasibility. This study develops a novel process simulation framework for modeling liquid NH 3 (LNH 3 ) combustion, enabling performance, emission, and preliminary techno-economic assessments. Additionally, multiple NH 3 utilization pathways were explored, including direct LNH 3 combustion, gas-phase/vapor NH 3 (VNH 3 ) combustion, and NH 3 cracking-based methods, to identify the most efficient and cost-effective approach. The findings indicate that LNH 3 combustion generates lower NO x emissions than VNH 3 but at the cost of reduced efficiency. NH 3 cracking enhances power output and thermal efficiency with an optimal cracking reactor temperature of 500 °C. Higher cracking ratios improve efficiency and reduce the levelized cost of electricity (LCOE) in both LNH 3 and VNH 3 systems. Efficiency increases from 47.7 % (LNH 3 ) and 49.1 % (VNH 3 ) to 54 % in H 2 –N 2 combustion (complete NH 3 cracking). However, LCOE is highly sensitive to cracking reactor costs and NH 3 prices. At low NH 3 prices (320 USD/t), direct VNH 3 combustion (0.217 USD/kWh) is more economical than VNH 3 cracking (0.22 USD/kWh), whereas in LNH 3 systems, cracking is always favorable. Furthermore, a higher pressure ratio for GTCC with a lower pressure in the NH 3 cracking reactor is preferred. This research provides new insights into NH 3 combustion strategies, offering a comprehensive techno-economic evaluation to guide optimized power generation with minimal environmental impact. Future work should refine NH 3 cracking models and establish emission-compliant operational limits for commercial deployment. • LNH 3 combustion was modeled, validated, and compared to VNH 3 . • LNH 3 combustion yields lower NO x but also lower efficiency than VNH 3 . • NH 3 cracking improves power output and lowers LCOE, especially in LNH 3 . • Cracking economics depend heavily on NH 3 price and reactor cost. • High pressure ratio of the gas turbine with a low pressure of cracking reactor is preferred.

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Publication Details

Journal
International Journal of Hydrogen Energy
Published
2025-09-01
DOI
https://doi.org/10.1016/j.ijhydene.2025.151337
Citations
3
Primary Topic
Catalytic Processes in Materials Science
Type
article
Field-Weighted Citation Impact
1.55
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article

Thermodynamic and preliminary techno-economic analysis of NH3 utilization in combined cycle power plant: Comparison of direct liquid, vaporized, and cracked NH3-Based combustion methods

Azaria Haykal Ahmad, Yong Fan, Hyun Jo, Hiroshi Itô et al.
3 citations
International Journal of Hydrogen Energy
Catalytic Processes in Materials Science
1.55
article

Thermodynamic and preliminary techno-economic analysis of NH3 utilization in combined cycle power plant: Comparison of direct liquid, vaporized, and cracked NH3-Based combustion methods

Azaria Haykal Ahmad, Yong Fan, Hyun Jo, Hiroshi Itô, Muhammad Aziz, Osamu Kurata, Taku Tsujimura, Masayasu Shimura, Norihiko Iki
article en
3 citations

Abstract

Ammonia (NH 3 ) is gaining attention as a promising carbon-free fuel for gas turbine combined cycle (GTCC) power generation. However, its effective utilization requires a thorough understanding of combustion characteristics, emissions, and economic feasibility. This study develops a novel process simulation framework for modeling liquid NH 3 (LNH 3 ) combustion, enabling performance, emission, and preliminary techno-economic assessments. Additionally, multiple NH 3 utilization pathways were explored, including direct LNH 3 combustion, gas-phase/vapor NH 3 (VNH 3 ) combustion, and NH 3 cracking-based methods, to identify the most efficient and cost-effective approach. The findings indicate that LNH 3 combustion generates lower NO x emissions than VNH 3 but at the cost of reduced efficiency. NH 3 cracking enhances power output and thermal efficiency with an optimal cracking reactor temperature of 500 °C. Higher cracking ratios improve efficiency and reduce the levelized cost of electricity (LCOE) in both LNH 3 and VNH 3 systems. Efficiency increases from 47.7 % (LNH 3 ) and 49.1 % (VNH 3 ) to 54 % in H 2 –N 2 combustion (complete NH 3 cracking). However, LCOE is highly sensitive to cracking reactor costs and NH 3 prices. At low NH 3 prices (320 USD/t), direct VNH 3 combustion (0.217 USD/kWh) is more economical than VNH 3 cracking (0.22 USD/kWh), whereas in LNH 3 systems, cracking is always favorable. Furthermore, a higher pressure ratio for GTCC with a lower pressure in the NH 3 cracking reactor is preferred. This research provides new insights into NH 3 combustion strategies, offering a comprehensive techno-economic evaluation to guide optimized power generation with minimal environmental impact. Future work should refine NH 3 cracking models and establish emission-compliant operational limits for commercial deployment. • LNH 3 combustion was modeled, validated, and compared to VNH 3 . • LNH 3 combustion yields lower NO x but also lower efficiency than VNH 3 . • NH 3 cracking improves power output and lowers LCOE, especially in LNH 3 . • Cracking economics depend heavily on NH 3 price and reactor cost. • High pressure ratio of the gas turbine with a low pressure of cracking reactor is preferred.

International Journal of Hydrogen EnergyVol. 173
RIKEN Center for Sustainable Resource Science (JP), National Institute of Advanced Industrial Science and Technology (JP), The University of Tokyo (JP)
Openalex Percentile: Top 16%
Catalytic Processes in Materials Science
1.55
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