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Transient convective heat transfer to water near the critical region in a vertical tube
Affiliation:1. School of Mechanical Engineering, Shandong University, Jinan 250061, PR China;2. Key Laboratory of High-efficiency and Clean Mechanical Manufacture (Shandong University), Ministry of Education, Jinan 250061, PR China;1. Department of Energy and Resources Engineering, College of Engineering, Peking University, Beijing, 100871, China;2. Beijing Key Laboratory for Solid Waste Utilization and Management, Peking University, Beijing 100871, China;3. Institute of Fluid Science, Tohoku University, Katahira 2-1-1, Aoba-ku, Sendai 980-8577, Japan;1. Departamento de Energia IEME, Instituto Tecnológico de Aeronáutica ITA, 12228-900, São José dos Campos, SP, Brazil;2. Divisão de Propulsão Aeronáutica, APA, Instituto de Aeronáutica e Espaço. IAE, 12228-904, São José dos Campos, SP, Brazil;1. Departament d’Enginyeria Química i Nuclear, Universitat Politècnica de València, Camí de Vera, 14, València Spain;2. Instituto de Seguridad Industrial, Radiofísica y Medioambiental, Universitat Politècnica de València, Camí de Vera, 14, València, Spain
Abstract:Numerical analysis has been carried out to investigate transient forced convective heat transfer to water near the critical region in developing flow through a vertical tube. With large variations of thermophysical properties such as density, specific heat, viscosity, and thermal conductivity near the thermodynamic critical point, heat transfer in the tube is strongly coupled with fluid flow. Buoyancy force parameter has also large variation with fluid temperature and pressure in the tube. Time dependent characteristics of fluid velocity, temperature, and heat transfer coefficient with water properties are presented and analyzed. Transient Nusselt and Stanton number distributions along the tube are also compared for various pressures in the tube. Because of heat transfer from the wall transition behavior from liquid-like phase to gas-like phase of heat transfer coefficient occurs when the fluid passes through pseudocritical temperature region in the tube. Turbulent viscosity ratio also has steep variation near the pseudocritical temperature close to the wall.
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