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. Author manuscript; available in PMC: 2018 Aug 1.
Published in final edited form as: Int J Refrig. 2017 May 19;80:52–65. doi: 10.1016/j.ijrefrig.2017.05.014

Figure 1.

Figure 1

Normalized forced-convection evaporation heat-transfer coefficient and pressure drop for R32 and R1234yf as a function of mass flux (D=7 mm, smooth tube, Tsat = 0 °C, q=10 kW·m−2)