Convective Flow Boiling in Coiled Tubes

R. E. Athey, L. Saupe
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Abstract

Convective flow boiling of liquid nitrogen has been investigated using coiled-tube heat exchangers in order to determine the heat transfer characteristics. This project focused on the identification of the primary variables involved in establishing the flow boiling coefficient for nitrogen using a coiled-tube flow configuration. The need for an accurate predictive correlation for this coefficient was recognized after an extensive testing program yielded results that did not correspond well with published information. A test method was developed which allowed for the accurate measurement of the boiling coefficient over a wide range of nitrogen flow rates, excess temperatures (Twall Tsat), and tube coil geometries. In evaluating nitrogen boiling rate data using a large number of f l ow conditions and coil geometries, it was found that va p o r i z a t i o n rates are a function of three main variables. These variables are : (1) Mass velocity of the liquid nitrogen inside the tubes; (2) Excess temperature involved in the boiling process; (3) Coiled-tube geometry, specifically the ratio of the inside tube diameter to the average coil diameter. A correlation has been developed which accounts for these va r iables. This correlation has been shown to be accurate in pre d i c t i n g the flow boiling coefficient within 10% for all cases tested.
在盘管中对流沸腾
利用盘管换热器对液氮的对流沸腾进行了研究,以确定其传热特性。本项目的重点是确定使用盘管流配置建立氮气流动沸腾系数所涉及的主要变量。在广泛的测试程序产生的结果与公布的信息不一致之后,人们认识到需要对该系数进行准确的预测相关性。开发了一种测试方法,该方法允许在宽范围内的氮气流速,过热温度(wall Tsat)和管盘管几何形状上精确测量沸腾系数。在利用大量流动条件和盘管几何形状评估氮沸腾率数据时,我们发现氮沸腾率是三个主要变量的函数。这些变量为:(1)管内液氮的质量速度;(2)沸腾过程中涉及的温度过高;(3)盘管的几何形状,特别是内管直径与平均盘管直径的比值。已经发展出一种关系来解释这些变量。这种相关性已被证明是准确的,因为在所有测试情况下,流动沸腾系数都在10%以内。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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