A compact catalytic foam reactor for decomposition of ammonia by the Joule-heating mechanism

被引:72
作者
Badakhsh, Arash [1 ,2 ]
Kwak, Yeonsu [1 ]
Lee, Yu-Jin [1 ]
Jeong, Hyangsoo [1 ,3 ]
Kim, Yongmin [1 ]
Sohn, Hyuntae [1 ,3 ]
Nam, Suk Woo [1 ]
Yoon, Chang Won [1 ,3 ,4 ]
Park, Chan Woo [2 ,5 ]
Jo, Young Suk [1 ]
机构
[1] Korea Inst Sci & Technol KIST, Ctr Hydrogen & Fuel Cell Res, Seoul 02792, South Korea
[2] Jeonbuk Natl Univ, Sch Mech Design Engn, Jeonju Si 54896, South Korea
[3] Korea Univ Sci & Technol, KIST Sch, Div Energy & Environm Technol, Seoul 02792, South Korea
[4] Kyung Hee Univ, KHU KIST Dept Converging Sci & Technol, Seoul 02447, South Korea
[5] Jeonbuk Natl Univ, Grad Sch, Dept Energy Storage Convers Engn, Jeonju Si 54896, South Korea
基金
新加坡国家研究基金会;
关键词
Compact reactor design; Metallic foam; Joule heating; Ammonia decomposition; Hydrogen production; Renewable energies; HYDROGEN-PRODUCTION; FUEL PROCESSOR; MICROCHANNEL REACTOR; SODIUM-BOROHYDRIDE; MEMBRANE REACTOR; RENEWABLE POWER; STEAM REFORMER; METHANOL; DESIGN; FEASIBILITY;
D O I
10.1016/j.cej.2021.130802
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Ammonia (NH3) is a viable hydrogen (H-2) carrier that allows storage and transport of H-2 using well-established infrastructure while maintaining high H-2 storage density. However, cracking NH3 into H-2 is energy-intensive. Herein, direct Joule-heating of the NiCrAl foam catalyst support is suggested and demonstrated, to minimize heat transfer scale for lower reactor volume, higher efficiency and power density than previously reported reformers. The power density of 128 W/cm(Reactor)(3) is achieved based on the lower heating value of H-2: this is 90% higher than previously reported microreactors. Also, even in a small-scale demonstration with a low internal volume of 7.7 cm(3) and a high surface-area-to-volume ratio of 5.7 cm(-1), a high reforming efficiency of 69.2% is achieved with low catalyst loadings, showing the feasibility of the concept. The as-proposed reactor concept offers a strong prospect for facile adoption of the power-to-X scheme for numerous applications including H-2 fueled islanded networks, and decarbonized energy conversion.
引用
收藏
页数:7
相关论文
共 51 条
[1]  
A.F.D. Centre, 2014, FUEL PROPERTIES COMP
[2]   Ammonia decomposition to clean hydrogen using non-thermal atmospheric-pressure plasma [J].
Akiyama, Mao ;
Aihara, Keigo ;
Sawaguchi, Tomiko ;
Matsukata, Masahiko ;
Iwamoto, Masakazu .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2018, 43 (31) :14493-14497
[3]   Improving performance of induction-heated steam methane reforming [J].
Almind, Mads Radmer ;
Vendelbo, Soren Bastholm ;
Hansen, Mikkel Fougt ;
Vinum, Morten Gotthold ;
Frandsen, Cathrine ;
Mortensen, Peter Molgaard ;
Engbaek, Jakob Soland .
CATALYSIS TODAY, 2020, 342 :13-20
[4]   Autothermal recirculating reactor (ARR) with Cu-BN composite as a stable reactor material for sustainable hydrogen release from ammonia [J].
Badakhsh, Arash ;
Cha, Junyoung ;
Park, Yongha ;
Lee, Yu-Jin ;
Jeong, Hyangsoo ;
Kim, Yongmin ;
Sohn, Hyuntae ;
Nam, Suk Woo ;
Yoon, Chang Won ;
Park, Chan Woo ;
Jo, Young Suk .
JOURNAL OF POWER SOURCES, 2021, 506
[5]   Ultra-compact microstructured methane steam reformer with integrated Palladium membrane for on-site production of pure hydrogen: Experimental demonstration [J].
Boeltken, T. ;
Wunsch, A. ;
Gietzelt, T. ;
Pfeifer, P. ;
Dittmeyer, R. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2014, 39 (31) :18058-18068
[6]   Ammonia as an efficient COx-free hydrogen carrier: Fundamentals and feasibility analyses for fuel cell applications [J].
Cha, Junyoung ;
Jo, Young Suk ;
Jeong, Hyangsoo ;
Han, Jonghee ;
Nam, Suk Woo ;
Song, Kwang Ho ;
Yoon, Chang Won .
APPLIED ENERGY, 2018, 224 :194-204
[7]   Experimental study on the hydrogen production of integrated methanol-steam reforming reactors for PEM fuel cells [J].
Chein, Rei-Yu ;
Chen, Yen-Cho ;
Lin, Yu-Sheng ;
Chung, J. N. .
INTERNATIONAL JOURNAL OF THERMAL SCIENCES, 2011, 50 (07) :1253-1262
[8]   Pd-Zn/Cu-Zn-Al catalysts prepared for methanol oxidation reforming in microchannel reactors [J].
Chen, Guangwen ;
Li, Shuhan ;
Yuan, Quan .
CATALYSIS TODAY, 2007, 120 (01) :63-70
[9]   Design and operation of an ammonia-fueled microchannel reactor for autothermal hydrogen production [J].
Chiuta, Steven ;
Bessarabov, Dmitri G. .
CATALYSIS TODAY, 2018, 310 :187-194
[10]   Performance evaluation of a high-throughput microchannel reactor for ammonia decomposition over a commercial Ru-based catalyst [J].
Chiuta, Steven ;
Everson, Raymond C. ;
Neomagus, Hein W. J. P. ;
Bessarabov, Dmitri G. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2015, 40 (07) :2921-2926