Numerical simulation of condensation for R410A at a different saturation temperature in mini/micro tubes. (17th April 2016)

• Record Type: Journal Article
• Authors: Zhang, Jingzhi; Li, Wei; Minkowycz, W. J.
• Is Part Of: Numerical heat transfer. Volume 69:Number 8(2016)
• Page Start: 825
• Page End: 840
• Publication Date: 2016-04-17
• Subjects: Heat -- Transmission -- Measurement -- Periodicals; Mass transfer -- Measurement -- Periodicals; Numerical analysis -- Periodicals; 621.4022
• DOI: 10.1080/10407782.2015.1090844
• Languages: English
• ISSNs: 1040-7782

Abstract

ABSTRACT: Heat transfer and pressure drop characteristics of condensation for R410A inside horizontal tubes (dh = 0.25, 1, and 4 mm) at saturation temperatures Tsat = 310, 320, and 330 K are investigated numerically. Liquid–vapor interfaces and stream traces are also presented to provide a better understanding of the effect of saturation temperature on the condensation process inside micro tubes. The results indicate that local heat transfer coefficients and pressure drop gradients increase with increasing mass flux and vapor quality and with decreasing tube diameter and saturation temperature. Liquid film thickness also increases with increasing saturation temperature because of the lower surface tension at a higher saturation temperature. When gravity dominates the condensation process, a vortex with its core lying at the bottom of the tube is found in the vapor phase region. For annular flow regime at dh = 0.25 mm, the vortex disappears, and stream traces point from the symmetry plan to the liquid–vapor interface, where the vapor phase turns into the liquid phase. Numerical heat transfer coefficients and pressure drop gradients are compared with available empirical correlations. Two new models for heat transfer coefficients and frictional pressure drop gradients are developed based on the numerical work. A reasonable agreement between predicted and numerical results is obtained.