Design of dual-channel Swiss-roll reactor for high-performance hydrogen production from ethanol steam reforming through waste heat valorization

被引:3
|
作者
Chen, Wei-Hsin [1 ,2 ,3 ]
Calapatia, Andre Marvin A. [4 ]
Ubando, Aristotle T. [4 ,5 ,6 ]
机构
[1] Natl Cheng Kung Univ, Dept Aeronaut & Astronaut, Tainan 701, Taiwan
[2] Tunghai Univ, Res Ctr Smart Sustainable Circular Econ, Taichung 407, Taiwan
[3] Natl Chin Yi Univ Technol, Dept Mech Engn, Taichung 411, Taiwan
[4] De La Salle Univ, Dept Mech Engn, 2401 Taft Ave, Manila 0922, Philippines
[5] De La Salle Univ, Thermomechan Anal Lab, Laguna Campus,LTI Spine Rd,Laguna Blvd, Binan 4024, Laguna, Philippines
[6] De La Salle Univ, Ctr Engn & Sustainable Dev Res, 2401 Taft Ave, Manila 0922, Philippines
关键词
Ethanol steam reforming; hydrogen production; Computational fluid dynamics (CFD); Swiss-roll reactor; Waste heat valorization; Optimization; WATER-GAS SHIFT; CATALYTIC PARTIAL OXIDATION; H-2; PRODUCTION; FUEL-CELL; SUPPORTED NI; METHANE; TEMPERATURE; ENERGY; RECIRCULATION; TECHNOLOGIES;
D O I
10.1016/j.energy.2024.132506
中图分类号
O414.1 [热力学];
学科分类号
摘要
Steam reforming is one of the most economical and efficient methods for hydrogen production. However, one of its glaring issues is the heat supply, which is used to maintain the reactions. Among reactors for hydrogen production, Swiss-roll reactors have exhibited exceptional performance in sustaining the heat required for reactions. Furthermore, heat supply via waste heat recovery has been an attractive industrial prospect for improving the sustainability of hydrogen production. This study proposes a design of a novel Swiss-roll reactor with dual channels to harvest waste heat from the flue gas to sustain the steam reforming reactions. Ethanol is used as a feedstock due to its environmentally benign properties. Numerical simulations are conducted to establish the reactor's catalytic reactions and heat transfer phenomena under the variations of gas hourly space velocity (GHSV), steam-to-ethanol (S/E) ratio, and inlet flue gas temperature. Heat recovery improves at higher GHSVs and lower S/E ratios at the cost of less efficient hydrogen production, while high inlet flue gas temperature improves heat recovery and hydrogen production. The novel reactor design can fulfill complete ethanol conversion maintained by heat recovered from waste flue gas, achieving 86.6 % hydrogen production efficiency and 72.7 % heat recovery under optimal operating conditions.
引用
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页数:15
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