A three-dimensional particles-based numerical model for ortho-para hydrogen continuous conversion heat exchangers in hydrogen liquefaction

IF 6.1 2区 工程技术 Q2 ENERGY & FUELS
Junjie Teng, Xinyu Wei, Shaolong Zhu, Song Fang, Shiran Bao, Xiaoqin Zhi, Limin Qiu, Kai Wang
{"title":"A three-dimensional particles-based numerical model for ortho-para hydrogen continuous conversion heat exchangers in hydrogen liquefaction","authors":"Junjie Teng,&nbsp;Xinyu Wei,&nbsp;Shaolong Zhu,&nbsp;Song Fang,&nbsp;Shiran Bao,&nbsp;Xiaoqin Zhi,&nbsp;Limin Qiu,&nbsp;Kai Wang","doi":"10.1016/j.applthermaleng.2025.126436","DOIUrl":null,"url":null,"abstract":"<div><div>Liquid hydrogen (LH<sub>2</sub>) is a promising hydrogen storage option considering its high energy density and convenience in storage and transportation. Ortho-para hydrogen conversion during hydrogen liquefaction is essential for reducing the boil-off loss of the LH<sub>2</sub> product, of which the continuous catalytic conversion is the most energy efficient. However, most existing researches adopted the homogeneous porous media model for the catalysts-filled zones, which is different from the actual layout of catalytic particles. The impact of packed catalytic particles remains unclear and requires further revelation. A three-dimensional particles-based numerical model, considering the geometry and space layout of catalytic particles, is constructed in this work. The impact of packed particles on heat transfer and conversion performance as well as internal physical fields are evaluated. Increasing flowrate ratios enhances convective heat transfer between the fluid and particles slightly and leads to improvements in conversion performance due to greater temperature gradient. Besides, a high Reynolds number enhances heat transfer performance but limits conversion efficiency, even though the conversion heat increases. Both of the concentration and conversion heat distributions are influenced by the inlet concentration of para-hydrogen. When the inlet composition deviates significantly from the equilibrium state, a substantial heat load is concentrated near the entrance, reaching 1.56 × 10<sup>6</sup> W/m<sup>3</sup> within the 80 K to 70 K range. A uniform concentration distribution along the flow directions is observed. In contrast, when the inlet composition is closer to equilibrium, the heat load is significantly lower and is expected to be released further downstream in the channels and the concentration exhibits a parabolic distribution. The work offers a new simulation method for ortho–para hydrogen continuous conversion heat exchangers, which would be useful for studying more detailed information at the particle pore scale.</div></div>","PeriodicalId":8201,"journal":{"name":"Applied Thermal Engineering","volume":"273 ","pages":"Article 126436"},"PeriodicalIF":6.1000,"publicationDate":"2025-04-10","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Applied Thermal Engineering","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S1359431125010282","RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENERGY & FUELS","Score":null,"Total":0}
引用次数: 0

Abstract

Liquid hydrogen (LH2) is a promising hydrogen storage option considering its high energy density and convenience in storage and transportation. Ortho-para hydrogen conversion during hydrogen liquefaction is essential for reducing the boil-off loss of the LH2 product, of which the continuous catalytic conversion is the most energy efficient. However, most existing researches adopted the homogeneous porous media model for the catalysts-filled zones, which is different from the actual layout of catalytic particles. The impact of packed catalytic particles remains unclear and requires further revelation. A three-dimensional particles-based numerical model, considering the geometry and space layout of catalytic particles, is constructed in this work. The impact of packed particles on heat transfer and conversion performance as well as internal physical fields are evaluated. Increasing flowrate ratios enhances convective heat transfer between the fluid and particles slightly and leads to improvements in conversion performance due to greater temperature gradient. Besides, a high Reynolds number enhances heat transfer performance but limits conversion efficiency, even though the conversion heat increases. Both of the concentration and conversion heat distributions are influenced by the inlet concentration of para-hydrogen. When the inlet composition deviates significantly from the equilibrium state, a substantial heat load is concentrated near the entrance, reaching 1.56 × 106 W/m3 within the 80 K to 70 K range. A uniform concentration distribution along the flow directions is observed. In contrast, when the inlet composition is closer to equilibrium, the heat load is significantly lower and is expected to be released further downstream in the channels and the concentration exhibits a parabolic distribution. The work offers a new simulation method for ortho–para hydrogen continuous conversion heat exchangers, which would be useful for studying more detailed information at the particle pore scale.
求助全文
约1分钟内获得全文 求助全文
来源期刊
Applied Thermal Engineering
Applied Thermal Engineering 工程技术-工程:机械
CiteScore
11.30
自引率
15.60%
发文量
1474
审稿时长
57 days
期刊介绍: Applied Thermal Engineering disseminates novel research related to the design, development and demonstration of components, devices, equipment, technologies and systems involving thermal processes for the production, storage, utilization and conservation of energy, with a focus on engineering application. The journal publishes high-quality and high-impact Original Research Articles, Review Articles, Short Communications and Letters to the Editor on cutting-edge innovations in research, and recent advances or issues of interest to the thermal engineering community.
×
引用
GB/T 7714-2015
复制
MLA
复制
APA
复制
导出至
BibTeX EndNote RefMan NoteFirst NoteExpress
×
提示
您的信息不完整,为了账户安全,请先补充。
现在去补充
×
提示
您因"违规操作"
具体请查看互助需知
我知道了
×
提示
确定
请完成安全验证×
copy
已复制链接
快去分享给好友吧!
我知道了
右上角分享
点击右上角分享
0
联系我们:info@booksci.cn Book学术提供免费学术资源搜索服务,方便国内外学者检索中英文文献。致力于提供最便捷和优质的服务体验。 Copyright © 2023 布克学术 All rights reserved.
京ICP备2023020795号-1
ghs 京公网安备 11010802042870号
Book学术文献互助
Book学术文献互助群
群 号:481959085
Book学术官方微信