This study experimentally investigated the heat transfer and pressure drop characteristics for evaporation and condensation flows of the refrigerant mixture, R245fa/R134a, which is used as a working refrigerant for a high-temperature heat pump and binary generator of an organic Rankine cycle inside horizontal tubes. The evaporation and condensation flow2 s were measured at an average saturation temperature of 40 and 60 °C, respectively, at mass velocities of 100 to 200 kg/m s, and using the following four composition refrigerant mixtures of R245fa/R134a: 90/10, 80/20, 65/35, and 55/45, mass ratios of R245fa to R134a. The evaporation and condensation heat transfer coefficients and frictional pressure drops of the refrigerant mixtures were lower than those of the pure refrigerant, R245fa. Further, the evaporation and condensation heat transfer coefficients and frictional pressure drop decreased with an increasing mass ratio of R134a. The frictional pressure drops for the evaporation and condensation flows of the refrigerant mixtures were consistent with the previous correlation; their correlation accurately predicted frictional pressure drops of pure refrigerant. The heat transfer coefficients of the refrigerant mixtures in the microfin tube contained a lower heat transfer enhancement from the spiral fins than that of the pure refrigerant. In addition, the heat transfer enhancement for the condensation flow was higher than that for the evaporation flow. Even when the refrigerant composition and mass velocity were varied, the heat transfer coefficient of the refrigerant mixtures in the microfin tube was higher than that in the smooth tube.
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