Hydrogen production in reverse tesla valve reactor combining ethanol steam reforming and water gas shift reaction

被引:0
|
作者
Chen, Wei-Hsin [1 ,2 ,3 ]
Zhong, Meng-Hong [1 ,4 ]
Nguyen, Thanh-Binh [5 ]
Sharma, Amit Kumar [6 ,7 ]
Li, Chung-Gang [4 ]
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] Natl Cheng Kung Univ, Dept Mech Engn, Tainan 701, Taiwan
[5] Natl Kaohsiung Univ Sci & Technol, Dept Marine Environm Engn, Kaohsiung 81157, Taiwan
[6] Univ Petr & Energy Studies UPES, Appl Sci Cluster, Sch Adv Engn, Dept Chem, Energy Acres Bldg, Dehra Dun 248007, Uttaranchal, India
[7] Univ Petr & Energy Studies UPES, Ctr Alternate Energy Res CAER, R&D, Energy Acres Bldg, Dehra Dun 248007, Uttaranchal, India
关键词
Tesla valve; Hydrogen production; Steam reforming; Water gas shift reaction; Ethanol; Ethanol conversion; H-2; PRODUCTION; BIO-OIL; CATALYSTS; FLOW; DECOMPOSITION; OPTIMIZATION; SIMULATION; ENRICHMENT; NI/AL2O3; METHANE;
D O I
10.1016/j.energy.2025.134783
中图分类号
O414.1 [热力学];
学科分类号
摘要
This study uses a reverse Tesla valve (RTVR) as a reactor for ethanol steam reforming (ESR) and water gas shift reaction (WGSR) to produce hydrogen. By combining ESR with WGSR to produce hydrogen, the dual objectives of enhancing hydrogen production and mitigating the negative impacts of carbon monoxide on the reactor can be implemented. This application of the RTVR reactor in thermochemical hydrogen production represents a novel advancement in this field. Three different reactors, including RTVR, bridge-type, and rectangular-type reactors, are adopted for comparison. The results reveal that the RTVR outperforms the other reactor types, achieving higher ethanol conversion rates and greater hydrogen yield, stemming from its special flow field design. However, a drawback accompanied by the RTVR is its higher pressure drop. The study identifies optimal operating conditions, including a temperature of 600 degrees C, a steam-to-ethanol (S/E) ratio of 3, outlet pressure of 1.5 atm, and a Reynolds number of 10, under which the RTVR reaches an ethanol conversion rate of 96.76 % and a hydrogen yield of 4.7 mol (mol C2H5OH)- 1, showing its high performance. This advancement in reactor design offers the potential for more efficient hydrogen production technologies.
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页数:14
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