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J. Braz. Soc. Mech. Sci. & Eng. vol.33 número especial 1

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Academic year: 2018

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Figure 1. Schematic view of the experimental facility.
Figure  2(a)  also  shows  that  for  low  mass  velocity  ( G   =  240  kg/sm 2 )  and low heat flux ( q  = 5 kW/m 2 ), the heat transfer coefficient hardly  shows any variations with quality
Figure 2. Effect of heat flux on heat transfer coefficient for different mass velocities: a)  G  = 240 kg/m 2 s, b)  G  = 440 kg/m 2 s for  T sat  = 22°C
Figure 3. Effect of mass velocity on heat transfer coefficient for different heat flux: a)  q  = 10 kW/m 2 , b)  q  = 87 kW/m 2  for  T sat = 22°C
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