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蒸汽发生器二次侧工质管周向非均匀传热特性
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作者 王珩沅 宣齐煜 +3 位作者 鲁政 郑皓德 司少鹏 李会雄 《化学工程》 CAS CSCD 北大核心 2024年第12期32-38,共7页
蒸汽发生器是核电系统中的关键设备,由于管内外耦合传热下螺旋管式蒸汽发生器二次侧工质的管周向非均匀传热现象及其规律未被充分认识,成为蒸汽发生器研究和设计中的难点。文中实验研究耦合一、二次侧传热下螺旋管式蒸汽发生器二次侧工... 蒸汽发生器是核电系统中的关键设备,由于管内外耦合传热下螺旋管式蒸汽发生器二次侧工质的管周向非均匀传热现象及其规律未被充分认识,成为蒸汽发生器研究和设计中的难点。文中实验研究耦合一、二次侧传热下螺旋管式蒸汽发生器二次侧工质流动沸腾下的管周向非均匀传热特性。研究发现:耦合传热下,管壁面存在明显的周向非均匀传热现象。随着二次侧工质入口过冷度Δt sub的增加,管壁面传热系数h变化不明显;随着二次侧工质系统压力p的增加,h 0°明显降低,而h 90°、h 180°、h 270°增加;随着二次侧工质质量流速G r的增加,h 0°小幅度降低,h 90°、h 180°、h 270°基本保持不变;随着一次侧工质加热温度t wat的增加,h 0°、h 270°存在先升后降的变化趋势,而h 90°、h 180°变化不明显。文中定义了周向局部不均匀性分布因子ηt或ηh来分别表示壁温t w或h在管周向分布上的差别,并得出了ηt或ηh分别随Δt sub、p、G r、t wat的变化规律。最后得出:耦合传热加热条件与恒热流密度加热条件下,二者的ηt整体上差异不大,仅ηt180°存在一定差异,而2种加热条件下的ηh存在较大差异,表明了耦合传热下管截面周向上的h分布更加不均匀。 展开更多
关键词 耦合传热 螺旋管 蒸汽发生器 非均匀 流动 沸腾
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Investigation of Nucleate Boiling on Composite Grooved Nanostructured Substrates by Molecular Dynamics
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作者 LI Zhibin WU Xiaoyi +5 位作者 SI Shaopeng LU zheng zheng haode LI Xujun CHANG Fucheng LI Huixiong 《Journal of Thermal Science》 2026年第2期611-624,共14页
The microstructural features and hydrophilic properties of surfaces are crucial in enhancing boiling heat transfer efficiency,offering a viable strategy for the thermal management of high-power electronic systems.Howe... The microstructural features and hydrophilic properties of surfaces are crucial in enhancing boiling heat transfer efficiency,offering a viable strategy for the thermal management of high-power electronic systems.However,conventional macroscopic experimental techniques and numerical simulations make it difficult to reveal the phase change process of a liquid at the microscopic scale.Consequently,this study applies molecular dynamics simulation methods to explore the phase transition behaviors of liquid water on hydrophilic nano-grooved surfaces at the nanoscale.By comprehensively analyzing the nucleation dynamics,bubble volume evolution,energy variation of water molecules within the thin liquid layer beneath the bubble,variations in heat flux during bubble growth,and the molecular motion characteristics and energy transfer mechanisms of nucleate boiling on shallow grooved structures are elucidated.The findings indicate that during bubble growth,a gradually thinning liquid layer forms beneath the bubbles.Furthermore,according to the bubble volume curve,the critical bubble radius is determined to be 1.59–1.95 nm.As the bubble volume increases,the average potential energy of the thin liquid layer exhibits a downward trend.Particularly,during bubble nucleation,the heat flux of the substrate exceeds 8×10^(−3)eV·nm^(−2)·ps^(−1).When the bubble appears,the heat flux rises;however,it decreases when a vapor film forms.The investigation of the thin liquid layer beneath the bubble not only deepens the understanding of energy transfer mechanisms during the nucleate boiling zone but also provides theoretical guidance for designing efficient heat sink components. 展开更多
关键词 liquid-vapor interface thin liquid layer molecular dynamics heat transfer
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