An efficient process for sustainable and scalable hydrogen production from green ammonia
- Authors
- Cha, Junyoung; Park, Yongha; Brigljevic, Boris; Lee, Boreum; Lim, Dongjun; Lee, Taeho; Jeong, Hyangsoo; Kim, Yongmin; Sohn, Hyuntae; Mikulcic, Hrvoje; Lee, Kyung Moon; Nam, Dong Hoon; Lee, Ki Bong; Lim, Hankwon; Yoon, Chang Won; Jo, Young Suk
- Issue Date
- 12월-2021
- Publisher
- PERGAMON-ELSEVIER SCIENCE LTD
- Keywords
- Ammonia reforming; Economic analysis; Efficiency analysis; H-2 production; Process simulation
- Citation
- RENEWABLE & SUSTAINABLE ENERGY REVIEWS, v.152
- Indexed
- SCIE
SCOPUS
- Journal Title
- RENEWABLE & SUSTAINABLE ENERGY REVIEWS
- Volume
- 152
- URI
- https://scholar.korea.ac.kr/handle/2021.sw.korea/135544
- DOI
- 10.1016/j.rser.2021.111562
- ISSN
- 1364-0321
- Abstract
- This study comprehensively investigates hydrogen production from green ammonia reforming, including synthesis of catalysts, reactor development, process integration, and techno-economic analysis. In-house developed Ru/La-Al2O3 pellet catalyst having perovskite structure showed high catalytic activity of 2827 h(-1) at 450 degrees C and stability over 6700 h at 550 degrees C, exceeding the performance of the majority of powder catalysts reported in the literature. A scalable 12-faceted reactor adopting the as-produced catalyst was designed to enhance heat transfer, producing over 66 L min(-1) of hydrogen with state-of-the-art ammonia reforming efficiency of 83.6 %. Near-zero CO2 emission of hydrogen extraction from green ammonia was demonstrated by-product gas recirculation as a combustion heat source. A techno-economic assessment was conducted for system scales from 10 kW to 10 MW, demonstrating the effect of reduced minimum hydrogen selling prices from 7.03 USD kg(-1) at small modular scales to 3.98 USD kg(-1) at larger industrial scales. Sensitivity analyses indicate that hydrogen selling prices may reduce even further (up to 50 %). The suggested hydrogen production route from green NH3 demonstrates superior CO2 reduction ranging from 78 % to 95 % in kg CO2 (kg H-2)(-1) compared to biomass gasification and steam methane reforming. These findings can be used as a basis for following economic and policy studies to further validate the effectiveness of the suggested system and process for H-2 production from NH3.
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