非混相液体中蒸发球帽液/气两相气泡的直接接触传热实验研究

IF 2.8 2区 工程技术 Q2 ENGINEERING, MECHANICAL
Ahmed R. Kareem , Hameed B. Mahood , Ali S. Baqir
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引用次数: 0

摘要

本文首次对非混相液体介质中单球帽液/气两相气泡蒸发的直接接触传热进行了实验研究。实验采用尺寸为600 mm × 100 mm × 100 mm的矩形有机玻璃柱进行。饱和温度(~ 36℃)下直径为3.5 mm的正戊烷液滴作为分散相,而蒸馏水在三种不同的初始温度下产生三个温差(ΔT),相当于Jacobs数(Ja = 18, 30和45)作为连续相。实验在连续相的活性高度(H)为500 mm时进行。利用250帧/秒的高速摄像机记录液滴沿连续相活动高度的蒸发过程。使用FASTCAM (PFV-4)和AutoCAD (3D)软件对捕获的图像进行分析,以进行精确的数据评估。观察了不同操作条件下球帽两相气泡的形成。根据实验结果,确定并分析了两相球帽泡平底面积上未汽化液体的平均厚度δ、蒸发球帽泡的大小De/Do以及用努塞尔数表示的对流换热系数Nu。正如预期的那样,实验结果表明Nu随着雷诺数(Re)和De/Do的增加而增加,与雅各布斯数(Ja)呈显著的反向效应。此外,δ随时间呈指数递减,Nu随δ的减小而增大。建立了Nu作为佩克莱特数(Pe)和Ja的函数的经验相关性,并成功地与实验数据进行了比较,在Ja = 30时最大误差约为8%。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Investigating direct-contact heat transfer of a spherical-cap liquid/vapour two-phase bubble evaporating in immiscible liquid: An experimental study
For the first time, this study presents the experimental investigation into the direct-contact heat transfer of a single spherical-cap liquid/vapour two-phase bubble evaporating in an immiscible liquid medium. The experiments were conducted using a rectangular Perspex column with dimensions of 600 mm × 100 mm × 100 mm. N-pentane droplets, with a diameter of 3.5 mm at saturation temperature (∼36 °C), served as the dispersed phase, while distilled water at three different initial temperatures, creating three temperature differences (ΔT), which is equivalent to Jacobs number (Ja = 18, 30 and 45), was used as the continuous phase. The experiments were performed at an active height in the continuous phase (H) of 500 mm. A high-speed camera operating at 250 frames per second was utilised to record the evaporation process of the droplets along the continuous phase active height. The captured images were analysed using FASTCAM (PFV-4) and AutoCAD (3D) software for precise data evaluation. The formation of the spherical-cap two-phase bubble was observed under various operating conditions. Based on the experimental output, the thickness of the yet-to-be vaporised liquid averaged over the area of the flat base of the two-phase spherical cap bubble (δ), the size of the evaporating spherical-cap two-phase bubble De/Do, and the convective heat transfer coefficient, expressed in terms of the Nusselt number (Nu), were determined and analysed. As anticipated, the experimental results demonstrated that Nu increased with a rise in the Reynolds number (Re) and De/Do with a significant inverse effect from the Jacobs number (Ja). Additionally, δ was found to decrease exponentially over time, and Nu increased as δ decreased. An empirical correlation for Nu as a function of Pecklet number (Pe) and Ja was developed and compared successfully with the experimental data with a maximum error of about 8 % at Ja = 30.
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来源期刊
Experimental Thermal and Fluid Science
Experimental Thermal and Fluid Science 工程技术-工程:机械
CiteScore
6.70
自引率
3.10%
发文量
159
审稿时长
34 days
期刊介绍: Experimental Thermal and Fluid Science provides a forum for research emphasizing experimental work that enhances fundamental understanding of heat transfer, thermodynamics, and fluid mechanics. In addition to the principal areas of research, the journal covers research results in related fields, including combined heat and mass transfer, flows with phase transition, micro- and nano-scale systems, multiphase flow, combustion, radiative transfer, porous media, cryogenics, turbulence, and novel experimental techniques.
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