首页> 外文期刊>JSME International Journal. Series B, Fluids and Thermal Engineering >Critical heat fluxes of subcooled water flow boiling against Inlet subcooling in short vertical tube
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Critical heat fluxes of subcooled water flow boiling against Inlet subcooling in short vertical tube

机译:短立管中过冷水流对入口过冷沸腾的临界热通量

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The critical heat fluxes (CHFs) of subcooled water flow boiling for the test tube inner diameters (d = 3 and 6 mm) and the heated lengths (L = 67, 120 and 150 mm) are systematically measured for the flow velocities (u = 4.0 to 13.3 m/s), the inlet subcoolings (△T{sub}(sub,in) = 48 to 148 K), the outlet subcoolings (△T{sub}(sub,out) = 10.5 to 95.1 K), the inlet pressure (P{sub}(in) = 753 to 995'kPa) and the outlet pressure (P{sub}(out) = 720 to 887 kPa). The SUS304 tubes of L = 67, 120 and 150mm for d = 3mm and L = 150mm for d = 6mm are used. The values of L/d are 22, 40 and 50 for d = 3 mm, and 25 for d = 6 mm, respectively. The CHFs, q{sub}(cr,sub) for a fixed △T{sub}(sub,out) become gradually lower with an increase in the L/d in the whole experimental range. The CHF correlation against outlet subcooling, which has been previously derived for Lid lower than 16, was modified to new one containing the Lid effect based on these experimental data. Furthermore, the relation between q{sub}(cr,sub) and L/d for a fixed △T{sub}(sub,in) was checked. The values of q{sub}(cr,sub) for a fixed △T{sub}(sub,in) became exponentially lower with the increase in L/d. CHF correlation against inlet subcooling has been given based on the experimental data for L/d ranging from 4.08 to 50. The correlations against outlet and inlet subcoolings can describe not only the CHFs obtained in this work for the inner diameter of 3 and 6 mm at the outlet pressure of around 800 kPa but also the authors' published CHFs data (1 611 points) for the wide ranges of P{sub}(in) = 159 kPa to 1 MPa, d = 3 to 12 mm, L =33 to 150 mm and u = 4.0 to 13.3 m/s within 15% difference for 30 K < △T{sub}(sub,out) ≤ 140 K and 40 K ≤△T{sub}(sub,in) ≤ 151 K.
机译:对于流速,系统地测量了试管内径(d = 3和6 mm)和加热长度(L = 67、120和150 mm)的过冷沸腾水的临界热通量(CHF)。 4.0至13.3 m / s),入口过冷(△T {sub}(sub,in)= 48至148 K),出口过冷(△T {sub}(sub,out)= 10.5至95.1 K),入口压力(P {sub}(in)= 753至995'kPa)和出口压力(P {sub}(out)= 720至887 kPa)。使用d = 3mm时L = 67、120和150mm的SUS304管,而d = 6mm时使用L = 150mm的SUS304管。 d = 3 mm的L / d值分别为22、40和50,d = 6 mm的L / d值为25。在整个实验范围内,随着L / d的增加,固定△T {sub}(sub,out)的CHF q {sub}(cr,sub)逐渐降低。根据这些实验数据,先前导出的Lid小于16的CHF与出口过冷的相关性已修改为包含Lid效应的新CHF相关性。此外,对于固定的△T {sub}(sub,in),检查了q {sub}(cr,sub)和L / d之间的关系。随着L / d的增加,固定的△T {sub}(sub,in)的q {sub}(cr,sub)值呈指数下降。已经基于L / d从4.08到50的实验数据给出了CHF与进口过冷的相关性。与出口和进口过冷的相关性不仅可以描述在这项工作中获得的内径为3和6 mm的CHF。出口压力约为800 kPa,而且作者发表的CHFs数据(1611点)适用于宽范围的P {sub}(in)= 159 kPa至1 MPa,d = 3至12 mm,L = 33至对于30 K <△T {sub}(sub,out)≤140 K和40 K≤△T {sub}(sub,in)≤151 K,150 mm和u = 4.0至13.3 m / s在15%的差异之内。

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