Abstract

The ongoing miniaturization of air conditioning and refrigeration systems, in order to limit, as much as possible, the refrigerant charge, calls for smaller and smaller heat exchangers. Besides, the new environmental regulations are calling for new pure refrigerants or refrigerants mixtures with lower values of global warming potentials (GWPs). In this context, this paper analyzes the possible implementation of minitubes during condensation of the azeotropic mixture R513A. Two minitubes are tested: a smooth tube with an inner diameter of 2.5 mm, and a microfin tube with an inner diameter at the fin tip of 2.4 mm. The effects of vapor quality (varied in the range 0.10–0.99), of mass velocity (varied in the range 200–1000 kg m−2 s−1), and of saturation temperature (30 °C and 40 °C) on the heat transfer coefficient are investigated. The experimental results indicate that the heat transfer coefficient increases as both vapor quality and mass velocity increase, both in the case of the smooth tube and of the microfin tube, but the slope of the heat transfer coefficient trend respect to vapor quality is higher in the case of the microfin tube. The microfin tube shows, on average, heat transfer coefficients are 79% higher than those of the smooth tube under the same working conditions. Since R513A is a possible substitute of R134a, some experimental data during condensation heat transfer are also compared against those for R134a. Finally, the experimental results are compared against values estimated by empirical correlations available in the open literature.

Highlights

  • R513A is an azeotropic mixture made of R1234yf and R134a (0.56/0.44 by mass)

  • The main purposes of these tests were to check the heat flow rate calculated on the water side and the one on the refrigerant side and to verify if the measuring technique was suitable by calculating the single phase heat transfer coefficients and by comparing these results against values predicted by well-known correlations from the literature

  • The mass velocity is calculated as reported in Equation (6) but the inner diameter diameter at the fin tip is used as Di

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Summary

Introduction

R1234yf is an HydroFluroOlefin with a Global Warming Potential lower than 1 [1], and it is placed in the A2L flammability class. R134a is among the most used HydroFluoroCarbons, not flammable (A1 flammability class), widely implemented in existing air conditioning systems, but it must be phased out in a near future due to its high GWP, which is 1430. The presence of R134a makes the mixture not flammable, whereas the presence of R1234yf lowers the warming impact of the mixture. R32 and R134a local heat transfer coefficients were measured by Matkovic et al [2]. The heat transfer coefficient increased with mass velocity and vapor quality; condensation was shear stress dominated, except some data at 100 and 200 kg m−2 s−1 , which overlapped in the graph

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