Ammonia as a hydrogen carrier: Simulation study of the ammonia cracker on thermo-fluid stability and key factors for scale-up

被引:9
作者
Cho, Si-Hyun [1 ]
Kim, Gyeong-Min [1 ,2 ]
Jo, Hyun-Yeong [1 ]
Bae, Yoon-Ho [1 ]
Jeon, Chung-Hwan [1 ,2 ]
机构
[1] Pusan Natl Univ, Sch Mech Engn, Pusan 46241, South Korea
[2] Pusan Natl Univ, Pusan Clean Energy Res Inst PCERI, Busan 46241, South Korea
基金
新加坡国家研究基金会;
关键词
CFD (computational fluid dynamics); Ammonia; Hydrogen; Ammonia cracking; COMMERCIAL RU/AL2O3 CATALYST; EXPERIMENTAL VALIDATION; DECOMPOSITION; GENERATION; COMBUSTION;
D O I
10.1016/j.ijhydene.2024.06.022
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
A typical technical problem in a hydrogen society is the difficulty in securing the economic efficiency of hydrogen storage and long-distance transportation. Hydrogen carriers that can convert hydrogen into other compounds are required to overcome this issue. Ammonia has many practical advantages as a hydrogen carrier and is drawing attention as a suitable substance. Therefore, a cracking technology that converts ammonia into high-purity hydrogen is necessary. In this study, a numerical computational fluid dynamics model of an ammonia cracker was developed. The flow and heat transfer characteristics were analyzed using a numerical model. The results showed that a nonuniform temperature distribution caused local cracking of ammonia and adversely affected the hydrogen production process. This results of this study can be used to help design large-scale ammonia crackers and efficient hydrogen production processes and contribute to building infrastructure for hydrogen storage/transport/utilization systems.
引用
收藏
页码:148 / 157
页数:10
相关论文
共 31 条
[1]  
[Anonymous], 2009, Ansys Inc, V15317, P1
[2]   Comparison of liquid hydrogen, methylcyclohexane and ammonia on energy efficiency and economy [J].
Aziz, Muhammad ;
Oda, Takuya ;
Kashiwagi, Takao .
INNOVATIVE SOLUTIONS FOR ENERGY TRANSITIONS, 2019, 158 :4086-4091
[3]   Mechanistic and kinetic insights into the Pt-Ru synergy during hydrogen generation from ammonia borane over PtRu/CNT nanocatalysts [J].
Chen, Wenyao ;
Li, Dali ;
Peng, Chong ;
Qian, Gang ;
Duan, Xuezhi ;
Chen, De ;
Zhou, Xinggui .
JOURNAL OF CATALYSIS, 2017, 356 :186-196
[4]   Hydrogen production from ammonia decomposition over a commercial Ru/Al2O3 catalyst in a microchannel reactor: Experimental validation and CFD simulation [J].
Chiuta, Steven ;
Everson, Raymond C. ;
Neomagus, Hein W. J. P. ;
Bessarabov, Dmitri G. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2016, 41 (06) :3774-3785
[5]   Ammonia decomposition over commercial Ru/Al2O3 catalyst: An experimental evaluation at different operative pressures and temperatures [J].
Di Carlo, Andrea ;
Vecchione, Luigi ;
Del Prete, Zaccaria .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2014, 39 (02) :808-814
[6]  
ERGUN S, 1952, CHEM ENG PROG, V48, P89
[7]  
FERZIGER JH, 1996, COMPUTATIONAL METHOD
[8]   A priori catalytic activity correlations:: the difficult case of hydrogen production from ammonia [J].
Ganley, JC ;
Thomas, FS ;
Seebauer, EG ;
Masel, RI .
CATALYSIS LETTERS, 2004, 96 (3-4) :117-122
[9]   Supply costs of green chemical energy carriers at the European border: A meta-analysis [J].
Genge, Lucien ;
Scheller, Fabian ;
Muesgens, Felix .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2023, 48 (98) :38766-38781
[10]   Techno-enviro-economic analyses of hydrogen supply chains with an ASEAN case study [J].
Hong, Xiaodong ;
Thaore, Vaishali B. ;
Karimi, Iftekhar A. ;
Farooq, Shamsuzzaman ;
Wang, Xiaonan ;
Usadi, Adam K. ;
Chapman, Bryan R. ;
Johnson, Robert A. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2021, 46 (65) :32914-32928