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Numerical Simulation of Entrained Bubbles Flow in the Shell-Tube Heat Exchanger of MSRs Based on Population Balance Model | |
2025 | |
发表期刊 | INTERNATIONAL JOURNAL OF ENERGY RESEARCH (IF:4.3[JCR-2023],4.5[5-Year]) |
ISSN | 0363-907X |
EISSN | 1099-114X |
卷号 | 2025期号:1 |
发表状态 | 已发表 |
DOI | 10.1155/er/6907471 |
摘要 | In molten salt reactors (MSRs), a small amount of inert gas could be entrained from the free liquid surface to the primary loop, which may have obvious impacts on the heat transfer performance of the heat exchanger, the reactivity of the core, and the migration of insoluble fission products. It is necessary to understand how the bubbles flow into the reactor core, and what kinds of size distribution should they be. Meanwhile, the heat exchanger is an important and complicated place before the gas enters the core, in which the bubbles may exhibit complex behavior, such as coalescence, breakup, or retention. This research employs a coupling method between the Eulerian two-phase flow model (ETFM) and the population balance model (PBM) to simulate the two-phase flow of bubbles entrained in molten salt on the shell side of a vertical U-tube heat exchanger. The gas fraction and poly-dispersed bubble size distribution are analyzed under different calculation methods and input conditions. The results show that the distribution of gas volume fraction and bubble size are significantly influenced by the characteristics of the flow field, and the salt flow can also be affected by the bubble distribution. The bubbles exhibit obvious non-uniformity distribution, especially in the center of the separation and the backflow vortexes, and a significant accumulation of gas attachment occurs behind the baffles. The interfacial area concentration and surface heat transfer coefficient are also discussed with or without the bubble distribution. All indicate that a precise bubble spatial and size distribution is necessary when in the simulation of multiphase flow in MSRs. |
关键词 | Bubble columns Digital elevation model Flow fields Heat transfer coefficients Heat transfer performance Liquefied gases Molten salt reactor Pressurized water reactors Vortex flow Bubble distributions Bubble flow Coupling methods Eulerian Free liquid surface Heat transfer performance Molten salt Population balance modelling Size-distribution Tube heat exchangers |
URL | 查看原文 |
收录类别 | SCI ; EI |
语种 | 英语 |
资助项目 | National Natural Science Foundation of China[12005290] ; Youth Innovation Promotion Association of the Chinese Academy of Sciences[ |
WOS研究方向 | Energy & Fuels ; Nuclear Science & Technology |
WOS类目 | Energy & Fuels ; Nuclear Science & Technology |
WOS记录号 | WOS:001398709100001 |
出版者 | WILEY |
EI入藏号 | 20251418170361 |
EI主题词 | Two phase flow |
EI分类号 | 301 Fluids ; 301.1 Fluid Flow ; 302.2 Heat Transfer ; 802.1 Chemical Plants and Equipment ; 1001.1 Nuclear Power Plant Equipment and Operation ; 1001.2.1 Fission Reactors ; 1106.2 Data Handling and Data Processing ; 1106.3.1 Image Processing |
原始文献类型 | Journal article (JA) |
文献类型 | 期刊论文 |
条目标识符 | https://kms.shanghaitech.edu.cn/handle/2MSLDSTB/483893 |
专题 | 物质科学与技术学院 |
通讯作者 | Zhu, Guifeng; Zou, Yang |
作者单位 | 1.Chinese Acad Sci, Shanghai Inst Appl Phys, Reactor Phys Dept, Shanghai 201800, Peoples R China 2.Univ Chinese Acad Sci, Beijing 100049, Peoples R China 3.ShanghaiTech Univ, Sch Phys Sci & Technol, Shanghai 201210, Peoples R China |
推荐引用方式 GB/T 7714 | Wang, Ziye,Zhu, Guifeng,Zou, Yang,et al. Numerical Simulation of Entrained Bubbles Flow in the Shell-Tube Heat Exchanger of MSRs Based on Population Balance Model[J]. INTERNATIONAL JOURNAL OF ENERGY RESEARCH,2025,2025(1). |
APA | Wang, Ziye,Zhu, Guifeng,Zou, Yang,Liang, Xiaolin,Chen, Liang,&Xu, Hongjie.(2025).Numerical Simulation of Entrained Bubbles Flow in the Shell-Tube Heat Exchanger of MSRs Based on Population Balance Model.INTERNATIONAL JOURNAL OF ENERGY RESEARCH,2025(1). |
MLA | Wang, Ziye,et al."Numerical Simulation of Entrained Bubbles Flow in the Shell-Tube Heat Exchanger of MSRs Based on Population Balance Model".INTERNATIONAL JOURNAL OF ENERGY RESEARCH 2025.1(2025). |
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