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Analysis of flow boiling heat transfer in narrow annular gaps applying the design of experiments method:

机译:应用实验方法设计分析窄环形间隙中的沸腾传热:

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The axial heat transfer coefficient during flow boiling of n-hexane was measured using infrared thermography to determine the axial wall temperature in three geometrically similar annular gaps with different widths (s?=?1.5?mm, s?=?1?mm, s?=?0.5?mm). During the design and evaluation process, the methods of statistical experimental design were applied. The following factors/parameters were varied: the heat flux q·=30?190kW/m2, the mass flux m·=30?700kg/m2s, the vapor quality x·=0.2?0.7, and the subcooled inlet temperature TU=20?60K. The test sections with gap widths of s?=?1.5?mm and s?=?1?mm had very similar heat transfer characteristics. The heat transfer coefficient increases significantly in the range of subcooled boiling, and after reaching a maximum at the transition to the saturated flow boiling, it drops almost monotonically with increasing vapor quality. With a gap width of 0.5?mm, however, the heat transfer coefficient in the range of saturated flow boiling first has a downward trend and then inc...
机译:使用红外热像仪测量正己烷流沸过程中的轴向传热系数,以确定在三个几何相似的环形间隙(不同宽度(s?=?1.5?mm,s?=?1?mm,s))中的轴向壁温度。 ?=?0.5?mm)。在设计和评估过程中,采用了统计实验设计的方法。变化了以下因素/参数:热通量q·= 30?190kW / m2,质量通量m·= 30〜700kg / m2s,蒸气质量x·= 0.2〜0.7,过冷入口温度TU = 20 60K。间隙宽度为s 1≤1.5mm和s 1≤1mm的测试部分具有非常相似的传热特性。在过冷沸腾范围内,传热系数显着增加,并且在过渡到饱和流沸腾时达到最大值后,随着蒸汽质量的提高,传热系数几乎单调下降。但是,间隙宽度为0.5?mm时,在饱和流沸腾范围内的传热系数先呈下降趋势,然后逐渐上升。

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