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//Variable declaration:
//From example 12.5:
Re = 73.9 //Reynolds number
mu_l = 2.82*10**-4 //Absolute viscosity of liquid water condensate (kg/m.s)
Pw = 0.2 //Wetted perimeter of rectangular plate (m)
h = 14700.0 //Heat transfer coefficient (W/m^2.K)
T_sat = 100.0 //Saturation temperature (°C)
Ts = 98.0 //Surface temperature (°C)
A = 0.2*0.4 //Heat transfer area of plate (m^2)
//Calculation:
m1 = Re*mu_l/4.0 //Mass flow rate of condensate (kg/m.s)
m = Pw*m1 //Mass flow rate of condensate (kg/s)
Co = (3.038*10**-5)*h //Condensation number
Q = h*A*(T_sat-Ts) //Heat transfer rate (W)
//Result:
printf("1. The mass flow rate of condensate is : %.4f kg/m.s.",m1)
printf("2. The heat transfer rate is : %.2f kW.",Q/10**3)
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