Condensation heat transfer on the outer surface of a horizontal annulus having surface enhancement. (February 2023)

• Record Type: Journal Article
• Authors: He, Yan; Wu, Junjie; Li, Wei; Dou, Binlin; Zheng, Boren; Zhang, Jianghui; Tang, Weiyu
• Is Part Of: International journal of heat and mass transfer. Volume 201:Part 2(2023)
• Publication Date: 2023-02
• Subjects: Double-sided enhanced tube -- Condensation -- Heat transfer coefficient -- Prediction correlation; Heat -- Transmission -- Periodicals; Mass transfer -- Periodicals; Chaleur -- Transmission -- Périodiques; Transfert de masse -- Périodiques; Electronic journals; 621.4022
• DOI: 10.1016/j.ijheatmasstransfer.2022.123588
• Languages: English
• ISSNs: 0017-9310

Abstract

Highlights: The condensation heat transfer characteristics of R410A on the outside of three enhanced tubes were experimentally investigated. Effect of surface structure, mass flux, average vapor quality, and saturation temperature on HTC and frictional pressure drop. The six correlations are evaluated and the correlation with the highest accuracy is selected and modified to obtain a predictive correlation suitable for the enhanced tubes. Abstract: Condensation heat transfer characteristics on the outer annular walls of double-sided horizontal tubes having three different enhancement geometries are investigated experimentally. The enhancement geometries are (1) a fine fin array, (2) a rectangular convex platform array, and (3) a T-shaped column array. The inner surface geometries are threads of various pitches. The experiments are with various mass fluxes, average vapor qualities, and saturation temperatures. They were conducted with refrigerant R410A. The results show the effects of enhancement geometry. Six correlations are used to predict the heat transfer coefficients of smooth tube, and the correlation with the highest accuracy is selected and corrected to obtain a new correlation suitable for the enhanced tubes. The new correlation can predict 92% of the data points within a prediction error of +22% to -30%. Frictional pressure drops are correlated with mass flux, average vapor quality, and saturation temperature. The heat transfer performances of the three experimental tubes are compared using a performance evaluation factor and the enhancement geometries with better condensation heat transfer performances are identified.