Experimentation and computer modeling were carried out to investigate the performance characteristics of fin-tube heat exchangers under frost conditions. As humid air passes over an evaporator coil that is below the freezing point, water condenses ont...
Experimentation and computer modeling were carried out to investigate the performance characteristics of fin-tube heat exchangers under frost conditions. As humid air passes over an evaporator coil that is below the freezing point, water condenses onto the evaporator coil surface. Moisture molecules migrate to the frosted surface and the void portion of frost layer leads to frost growth and densification of frost layer. Frost layer acts as an insulation layer between the fins and the air. In addition, the frost blocks airflow path, causing an increase in pressure drop and a decrease in airflow rate. Numerous experimental and theoretical investigations on frosting have been performed and reported, but most researches on frost formation have been focused on simple geometries such as flat plates and round tubes. Due to complex geometry of fin-tube heat exchangers and diversity of operating variables, a further study is required to design optimum heat exchanger, achieving both uniform frost distribution and delay of frost formation.
In this study, the correlations of heat transfer coefficient and friction factors for various geometries, such as the continuous and discrete flat plate finned tubes, were developed as a function of operating conditions and geometric parameters of fin-tube heat exchangers. An analytical model under frost conditions was developed using the correlations from experimental results. Computer simulations with the variation of operating conditions and geometry of fin-tube heat exchangers were performed to find out the optimal design parameters of fin-tube heat exchangers.
The developed analytical model predicted the decreasing rate of heat exchanger performance within 10% compared to the experimental results. The decreasing rate of air flow rate ratio and heat transfer rate ratio become higher at high inlet air temperatures, and relatively high humidity. Despite the same trend of frost growth rate, each driving fan had different tendency of air flow rate ratio due to its characteristic curve. R600a as an alternative refrigerant of R134a for commercial refrigeration system showed the same performance at a smaller flow rate compared to the existing system. There was a great difference in the frosting performance whether there was pipe heater or not. Smaller tube diameter had a small decreasing rate of air flow rate ratio.
Keywords : Frosting, Fin-tube heat exchanger, Heat transfer coefficient, Friction factor.