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+clear
+//
+// Variable declaration
+// From example 25.2
+Q=16.4// Total load in kW
+T_in=33// The temperature at liquid R134a enters the expansion valve in °C
+T_out=9// The temperature at liquid R134a leaves the cooler in °C
+T_e=5// The temperature at which liquid R134a evaporates in °C
+
+// Calculation
+h_v=405.23// Enthalpy of R134a,superheated to 9 C in kJ/kg
+h_f=246.71// Enthalpy of liquid R134a at 33 C in kJ/kg
+Re=h_v-h_f// Refrigerating effect in kJ/kg
+m_r=Q/Re// Required refrigerant mass flow in kg/s
+printf("\n Required refrigerant mass flow=%0.3f kg/s",m_r)
+