Techno-economic analysis and life cycle assessment for electrochemical ammonia production using proton conducting membrane. (1st January 2020)

• Record Type: Journal Article
• Authors: Gomez, Jamie R.; Baca, John; Garzon, Fernando
• Is Part Of: International journal of hydrogen energy. Volume 45:Number 1(2020)
• Page Start: 721
• Page End: 737
• Publication Date: 2020-01-01
• Subjects: Techno-economic modeling -- Ammonia economy -- Hydrogen economy -- Electrochemical ammonia synthesis; Hydrogen as fuel -- Periodicals; Hydrogène (Combustible) -- Périodiques; Hydrogen as fuel; Periodicals; 665.81
• DOI: 10.1016/j.ijhydene.2019.10.174
• Languages: English
• ISSNs: 0360-3199

Abstract

Abstract: Green ammonia production is facing increasing interest on a global scale as a hydrogen carrier for power generation as well as fertilizer for food production. The conventional Haber-Bosch method for ammonia synthesis is energy demanding, requires high purity hydrogen, and is based on fossil fuels. A preliminary techno-economic model for electrochemical ammonia synthesis at near ambient pressure using feed rates of 32 metric ton/day for hydrogen and 135 metric ton/day for nitrogen is presented in this study. Various pathways using different methods for nitrogen generation and hydrogen production were investigated to gain insight into added energy savings per metric ton of ammonia. Electrochemical synthesis using electrolysis for hydrogen and cryogenic nitrogen was found to be a potentially viable pathway for green ammonia. The profitability metrics including discounted cash flow rate of return, net present value and discounted payback period were estimated to be 8%, $40 MM, and 4–6 years respectively for this pathway. The cost of electricity, conversion rate, and conversion efficiency dominate the tonnage cost of ammonia and were used to assess the feasibility of the model. A life cycle assessment was also conducted to assess the environmental impact of a well to product ammonia process. Highlights: Integrated electrochemical ammonia systems with renewable intermittent sources has. linear scalability advantages. Energy consumption of at least 17 MWh per metric ton for electrochemical ammonia. Number of modules decreases with current density. Specific energy decreases as the production rate increases.