Visualisation of flow boiling heat transfer in a microtube

被引：3

作者：

Celata, G. P. ^{[1
]}

Cumo, M. ^{[2
]}

Dossevi, D. ^{[3
]}

Jilisen, R. T. M. ^{[4
]}

Saha, S. K. ^{[5
]}

Zummo, G. ^{[1
]}

机构：

[1] ENEA, Rome, Italy

[2] Univ Roma La Sapienza, Rome, Italy

[3] Univ Nantes, Nantes, France

[4] Eindhoven Univ Technol, NL-5600 MB Eindhoven, Netherlands

[5] Bengal Engn & Sci Univ, Howrah, W Bengal, India

来源：

HEAT AND MASS TRANSFER | 2011年 / 47卷 / 08期

关键词：

Heat Transfer Coefficient; Test Section; Mass Flow Rate; Mass Flux; Slug Flow;

D O I：

10.1007/s00231-011-0846-0

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

This paper presents the results of the flow boiling patterns and heat transfer coefficients of FC-72 in a small tube. The internal diameter of the tube is 0.48 mm, with a heated length of 73 mm. The mass flow rate varies from 50 to 3,000 kg/m(2)-s. The microtube is made of Pyrex in order to obtain the visualisation of the flow pattern along the heated channel. Different types of flow pattern have been observed: bubbly flow, deformed bubbly flow, bubbly/slug flow, slug flow, slug/annular flow, and annular flow. The experiments show the presence of flow instabilities in a large portion of the tests at low mass flow rates and low subcooling. Flow patterns in presence of flow instabilities are mainly characterized by bubbly/slug flow and slug/annular flow. Heat transfer rates have been studied in all flow pattern conditions. The two groups of results, with flow instabilities and without flow instabilities, show similar heat transfer behaviour. The heat transfer characteristics of the pipes have been studied in comparison with mass flux and vapour quality.

引用

页码：941 / 949

页数：9

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