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+//Variable declaration:
+T1 = 15.0                   //Water entering temperature (°C)
+T2 = 60.0                   //Water leaving temperature (°C)
+D = 0.022                   //Inside diameter of tube (m)
+V = 0.355                   //Average water flow velocity (m/s)
+TC = 150.0                  //Outside wall temperature (°C)
+//From Appendix:
+p = 993.0                   //Density of water (kg/m^3)
+mu = 0.000683               //Dynamic viscosity of water (kg/m.s)
+Cp = 4.17*10**3             //Heat capacity of water (J/kg.K)
+k = 0.63                    //Thermal conductivity of water (W/m.K)
+
+//Calculation:
+Tav1 = (T1+T2)/2.0          //Average bulk temperature of water (°C)
+Re = D*V*p/mu               //Reynolds number
+Pr = Cp*mu/k                //Prandtl number
+Tav2 = (Tav1+TC)/2.0        //Fluid's average wall temperature (°C)
+//From Appendix:
+mu_w = 0.000306             //Dynamic viscosity of fluid at wall (kg/m.s)
+//From Table 9.5:
+h = (k/D)*0.027*Re**0.8*Pr**0.33*(mu/mu_w)**0.14    //Heat transfer coefficient for water (W/m^2.K)
+
+//Result:
+printf("The heat transfer coefficient for water is : %.1f  W/m^2.K.",h)