Heat Exchange Inside a Horizontal Pipe at the Initial Section with Complete Condensation of R142b Freon Vapor

IF 0.9 Q4 ENERGY & FUELS Thermal Engineering Pub Date : 2025-01-16 DOI:10.1134/S0040601524700563
O. O. Milman, G. G. Yankov, A. V. Kondratiev, A. V. Ptakhin, V. S. Krylov, V. B. Perov, A. A. Zhinov, A. Yu. Kartuesova
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Abstract

Heat exchange during condensation of freons has been studied quite well; however, various flow regimes of the steam-condensate mixture may arise during condensation inside heat-exchange pipes. There is a large amount of experimental data on the condensation of freons inside pipes with different internal diameters. However, the results obtained by different authors are contradictory, and experimental dependencies can give a high error in the event of a discrepancy between the calculated and actual flow regimes of the steam-condensate mixture. Due to the difficulty of identifying these modes for each such case, reliable recommendations for the calculation and design of heat exchangers must be based on experimental data. In order to obtain such materials, an experimental stand was developed and manufactured, allowing the study of condensation processes of various working fluids in a horizontal cooled tube. The working section of the stand was a copper pipe with an external diameter of 32 mm and a wall thickness of 2 mm, built into an external steel pipe with a diameter of 45 × 3 mm with an annular gap of 3.5 mm. Five chromel-copel thermocouples were installed in the gap to measure the water temperature; they were led to the measuring instruments through the wall of the outer pipe. Thermocouples were also installed in the copper pipe wall. The stand’s thermocouples were precalibrated, and the freon and cooling water consumption was determined by the differences on the flow diaphragms with an error not exceeding 1.5%. The temperatures of cooling water and condensing freon R142b along the length of the heat-exchange pipe were obtained for some flow regimes with different parameters of the working fluid at the pipe inlet. A sharp decrease in the local heat-transfer coefficient along the length of the heat-exchange pipe during complete condensation is shown and is especially significant at its inlet section. The obtained data will be used in the design of heat exchangers with condensation of R142b freon in horizontal pipes.

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R142b氟利昂蒸汽完全冷凝时水平管内初始段的热交换
氟利昂冷凝过程中的热交换问题已经得到了很好的研究;然而,在热交换管内冷凝过程中,蒸汽-冷凝水混合物可能出现不同的流动形式。在不同内径的管道内,有大量的氟利昂冷凝的实验数据。然而,不同作者得到的结果是相互矛盾的,并且实验依赖关系在计算和实际流动状态之间存在差异的情况下可能会产生很高的误差。由于很难确定每种情况下的这些模式,因此必须以实验数据为基础,对换热器的计算和设计提出可靠的建议。为了获得这种材料,开发和制造了一个实验台,可以研究各种工质在水平冷却管中的冷凝过程。支架的工作部分为外径32毫米、壁厚2毫米的铜管,内置于外径45 × 3毫米、环形间隙3.5毫米的钢管内。在间隙中安装了5个铬钴热电偶来测量水温;他们穿过外管的壁,被引到测量仪器跟前。热电偶也安装在铜管壁上。对支架热电偶进行预校准,根据流量隔膜的差异确定氟利昂和冷却水消耗量,误差不超过1.5%。在不同工质参数下,得到了不同流态下的冷却水和冷凝氟利昂R142b沿换热管长度的温度。在完全冷凝过程中,局部传热系数沿换热管长度的急剧下降,在其进口段尤为显著。所得数据将用于水平管内R142b氟利昂冷凝换热器的设计。
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来源期刊
CiteScore
1.30
自引率
20.00%
发文量
94
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