Molten metal methane pyrolysis for distributed hydrogen production: Reactor design, hydrodynamics, and technoeconomic insights

Methane pyrolysis offers a compelling pathway for low-carbon hydrogen production by avoiding CO 2 emissions and enabling distributed deployment in locations with natural gas supply, thereby eliminating the need for costly hydrogen transport. While promising, the commercial deployment is constrained by the lack of detailed reactor modeling and technoeconomic assessment at small production scales. This study addresses these gaps by designing and modeling a small-scale (1–10 t-H 2 /day) bubble column reactor employing molten Ni Bi alloy catalyst for methane pyrolysis. A coupled kinetic–hydrodynamic model was developed to simulate gas holdup, bubble behavior, and conversion under different operating conditions. The reactor design was integrated into an Aspen Plus simulation of the full process, including heat recovery and hydrogen purification. Optimization of pressure, temperature, and single-pass conversion revealed that operation at 1100 °C, 15 bar, and 70–75 % conversion minimized reactor volume and cost. The lowest levelized cost of hydrogen (LCOH) achieved was $3.06/kg-H 2 without sale of carbon, significantly lower than green H 2 produced from water electrolysis and competitive with blue H 2 produced via centralized reforming when transportation costs are included. Sensitivity analysis reveals that carbon byproduct is a key economic lever; carbon sale at $250/t-C reduces LCOH by 25 %, while a price of $700/t-C would meet U.S. DOE $1/kg-H₂ target. These results demonstrate the technoeconomic viability of molten metal methane pyrolysis and highlight future opportunities. • Low-carbon H 2 production via molten metal methane pyrolysis was studied. • Reactor design was optimized by a coupled kinetic–hydrodynamic mathematical model. • Full process simulation by Aspen Plus, including novel recycle system and heat recovery. • Optimized TEA at a temperature of 1100 °C, and single-pass conversion of 70 % • Lowest LCOH of $3.06 and $2.28/kg H 2 without/with carbon sale of $250/ton

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Publication Details

Journal
Chemical Engineering Journal
Published
2025-10-21
DOI
https://doi.org/10.1016/j.cej.2025.169812
Citations
1
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
0.39
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article

Molten metal methane pyrolysis for distributed hydrogen production: Reactor design, hydrodynamics, and technoeconomic insights

Moslem Fattahi, Mohd Adnan Khan, Seyedsina Hejazi, Md Golam Kibria et al.
1 citations
Chemical Engineering Journal
Catalysts for Methane Reforming
0.39
article

Molten metal methane pyrolysis for distributed hydrogen production: Reactor design, hydrodynamics, and technoeconomic insights

Moslem Fattahi, Mohd Adnan Khan, Seyedsina Hejazi, Md Golam Kibria, Alireza Lotfollahzade Moghaddam
article en
1 citations

Abstract

Methane pyrolysis offers a compelling pathway for low-carbon hydrogen production by avoiding CO 2 emissions and enabling distributed deployment in locations with natural gas supply, thereby eliminating the need for costly hydrogen transport. While promising, the commercial deployment is constrained by the lack of detailed reactor modeling and technoeconomic assessment at small production scales. This study addresses these gaps by designing and modeling a small-scale (1–10 t-H 2 /day) bubble column reactor employing molten Ni Bi alloy catalyst for methane pyrolysis. A coupled kinetic–hydrodynamic model was developed to simulate gas holdup, bubble behavior, and conversion under different operating conditions. The reactor design was integrated into an Aspen Plus simulation of the full process, including heat recovery and hydrogen purification. Optimization of pressure, temperature, and single-pass conversion revealed that operation at 1100 °C, 15 bar, and 70–75 % conversion minimized reactor volume and cost. The lowest levelized cost of hydrogen (LCOH) achieved was $3.06/kg-H 2 without sale of carbon, significantly lower than green H 2 produced from water electrolysis and competitive with blue H 2 produced via centralized reforming when transportation costs are included. Sensitivity analysis reveals that carbon byproduct is a key economic lever; carbon sale at $250/t-C reduces LCOH by 25 %, while a price of $700/t-C would meet U.S. DOE $1/kg-H₂ target. These results demonstrate the technoeconomic viability of molten metal methane pyrolysis and highlight future opportunities. • Low-carbon H 2 production via molten metal methane pyrolysis was studied. • Reactor design was optimized by a coupled kinetic–hydrodynamic mathematical model. • Full process simulation by Aspen Plus, including novel recycle system and heat recovery. • Optimized TEA at a temperature of 1100 °C, and single-pass conversion of 70 % • Lowest LCOH of $3.06 and $2.28/kg H 2 without/with carbon sale of $250/ton

Chemical Engineering JournalVol. 524
University of Alberta (CA), University of Calgary (CA), Saudi Aramco (Saudi Arabia) (SA)
Openalex Percentile: Top 38%
Catalysts for Methane Reforming
0.39
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