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These parameters included tube inclination angle, vapour quality, refrigerant mass flux, and flow regimes.
The frictional pressure drop was found to be primarily a function of mass flux and vapour quality.
Evolution of the exit vapour quality and wall superheat as a function of heat flux are presented and analyzed.
The refrigerant mass velocity has been varied from 15 to 40 kg m−2 s−1 whereas the outlet vapour quality between 0.01 and 0.58.
For both refrigerants, the superheating at the inlet of the heat exchanger was around 15 K; the mass flux has been varied from 15 to 40 kg m−2 s−1 whereas the outlet vapour quality has been changed between 0.07 and 0.58 in order to investigate the effect of vapour quality.
A simple procedure has then been implemented to control the position of points 6 and 7, depending if the end of the expansion process is inside or outside the dome (x 6), and then fixing the positions of point 7 (vapour quality, x 7) of consequence.
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Decrease in heat transfer coefficients is also observed for lower mass fluxes and lower vapour qualities in two-phase.
The tests were carried out at saturation temperatures of 5 and 15 °C, mass fluxes from 4 to 40 kg m−2 s−1, heat fluxes from 15 to 70 kW m−2 and inlet vapour qualities ranging from 10%to90%0%.
This paper presents the experimental investigation of CO2 condensation in a horizontal smooth tube at saturation temperatures between 0 and −15 °C with mass fluxes between 50 and 200 kg m−2 s−1 and for various vapour qualities.
The heat transfer coefficients and pressure drops of the three working fluids were measured with varying saturation temperatures, mass fluxes, heat fluxes and outlet vapour qualities, which range from 60 °C to 80 °C, 86 kg/m2 s to 137 kg/m2 s, 9.8 kW/m2 to 36.8 kW/m2 and 0.5 to 1, respectively.
ILs exhibit very low vapour pressure, excellent solvation quality, variable viscosity range and thermal stabilities (Anderson et al. 2002).
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