Decarbonization path of natural gas combined cycle using chemical looping hydrogen generation: Thermodynamics, emissions, and economics studies

The global energy sector's reliance on fossil fuels necessitates a transition to low-carbon alternatives, with hydrogen (H 2 ) emerging as a key solution. Chemical looping H 2 generation (CLHG) offers a flexible approach using biomass (BM) or natural gas (NG) as feedstocks. This study integrates CLHG, an organic Rankine cycle, NH 3 synthesis, and a 559 MW NG combined cycle (NGCC), utilizing blended NH 3 -H 2 or pure H 2 combustion. Process simulations (Aspen Plus V14) and emission analyses (ANSYS Chemkin-Pro 2024R1) assess four cases: (1) BM-CLHG with NH 3 -H 2 , (2) BM-CLHG with H 2 , (3) NG-CLHG with NH 3 -H 2 , and (4) NG-CLHG with H 2 . NG-CLHG achieves higher H 2 efficiency, while all cases increase net power output (613.85–683.59 MW). Case 4 maintains high thermal efficiency (59.93 %), compensating for efficiency losses. BM-CLHG achieves negative CO 2 emissions (−0.76 to −0.63 t-CO 2 /MWh), while NG-CLHG achieves zero CO 2 emissions. NH 3 -H 2 combustion reduces NO x (∼6.2 ppmv) but increases N 2 O (∼222 ppmv). Economic analysis reveals a negative levelized cost of electricity for Cases 1 and 2, primarily due to CO 2 credit revenue, while Case 4 remains competitive with NGCC. To support the adoption of CLHG, stricter carbon pricing policies and CO2 storage incentives are necessary. Strategic site selection for CO 2 storage and differentiated NG taxation can improve economic viability. • Four decarbonization paths of NGCC using biomass and natural gas CLHG were explored, with H 2 and H 2 -NH 3 as NGCC fuel. • NG-CLHG achieves higher H 2 production efficiency than BM-CLHG, while BM-CLHG systems exhibit negative CO 2 emissions. • NH 3 -H 2 co-combustion results in low NO x emissions (∼6.2 ppmv) but produces high N 2 O emissions (∼222 ppmv). • BM-CLHG achieves negative LCOE from CO 2 offset revenue, while NG-CLHG with H 2 combustion offers a competitive LCOE comparable to NGCC. • Policy implications such as higher carbon prices, tax incentives, and optimized CO 2 storage strategies are crucial to improving the system competitiveness.

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Publication Details

Journal
Energy
Published
2025-08-08
DOI
https://doi.org/10.1016/j.energy.2025.137916
Citations
8
Primary Topic
Chemical Looping and Thermochemical Processes
Type
article
Field-Weighted Citation Impact
5.39

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article

Decarbonization path of natural gas combined cycle using chemical looping hydrogen generation: Thermodynamics, emissions, and economics studies

Azaria Haykal Ahmad, Muhammad Aziz
8 citations
Energy
Chemical Looping and Thermochemical Processes
5.39
article

Decarbonization path of natural gas combined cycle using chemical looping hydrogen generation: Thermodynamics, emissions, and economics studies

Azaria Haykal Ahmad, Muhammad Aziz
article en
8 citations

Abstract

The global energy sector's reliance on fossil fuels necessitates a transition to low-carbon alternatives, with hydrogen (H 2 ) emerging as a key solution. Chemical looping H 2 generation (CLHG) offers a flexible approach using biomass (BM) or natural gas (NG) as feedstocks. This study integrates CLHG, an organic Rankine cycle, NH 3 synthesis, and a 559 MW NG combined cycle (NGCC), utilizing blended NH 3 -H 2 or pure H 2 combustion. Process simulations (Aspen Plus V14) and emission analyses (ANSYS Chemkin-Pro 2024R1) assess four cases: (1) BM-CLHG with NH 3 -H 2 , (2) BM-CLHG with H 2 , (3) NG-CLHG with NH 3 -H 2 , and (4) NG-CLHG with H 2 . NG-CLHG achieves higher H 2 efficiency, while all cases increase net power output (613.85–683.59 MW). Case 4 maintains high thermal efficiency (59.93 %), compensating for efficiency losses. BM-CLHG achieves negative CO 2 emissions (−0.76 to −0.63 t-CO 2 /MWh), while NG-CLHG achieves zero CO 2 emissions. NH 3 -H 2 combustion reduces NO x (∼6.2 ppmv) but increases N 2 O (∼222 ppmv). Economic analysis reveals a negative levelized cost of electricity for Cases 1 and 2, primarily due to CO 2 credit revenue, while Case 4 remains competitive with NGCC. To support the adoption of CLHG, stricter carbon pricing policies and CO2 storage incentives are necessary. Strategic site selection for CO 2 storage and differentiated NG taxation can improve economic viability. • Four decarbonization paths of NGCC using biomass and natural gas CLHG were explored, with H 2 and H 2 -NH 3 as NGCC fuel. • NG-CLHG achieves higher H 2 production efficiency than BM-CLHG, while BM-CLHG systems exhibit negative CO 2 emissions. • NH 3 -H 2 co-combustion results in low NO x emissions (∼6.2 ppmv) but produces high N 2 O emissions (∼222 ppmv). • BM-CLHG achieves negative LCOE from CO 2 offset revenue, while NG-CLHG with H 2 combustion offers a competitive LCOE comparable to NGCC. • Policy implications such as higher carbon prices, tax incentives, and optimized CO 2 storage strategies are crucial to improving the system competitiveness.

EnergyVol. 335
RIKEN Center for Sustainable Resource Science (JP), The University of Tokyo (JP)
Japan International Cooperation Agency, Japan Society for the Promotion of Science, Japan Science and Technology Agency
Openalex Percentile: Top 4%
Chemical Looping and Thermochemical Processes
5.39
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