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-rw-r--r--3685/CH14/EX14.6/Ex14_6.sce30
-rw-r--r--3685/CH14/EX14.6/Ex14_6.txt5
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diff --git a/3685/CH14/EX14.6/Ex14_6.sce b/3685/CH14/EX14.6/Ex14_6.sce
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+clc
+// Given that
+te = -10 // Evaporator temperature in degree celsius
+pc = 7.675 // Condenser pressure in bar
+pf = 4.139 // Flash chamber pressure in bar
+P = 100 // Power input to compressor in kW
+printf("\n Example 14.6\n")
+// From the property table of R-134a,
+h7 = 140.96 // In kJ/kg
+hf = 113.29 // In kJ/kg
+hfg = 300.5-113.29 // In kJ/kg
+hg = 300.5 // In kJ/kg
+h1 = 288.86 // In kJ/kg
+s1 = 1.17189 // // In kJ/kgK
+s2 =s1
+//By interpolation
+h2 = 303.468 // In kJ/kg
+x8 = (h7-hf)/hfg
+m1=x8
+h5 = (1-m1)*h2 + m1*hg
+// By interpolation
+s5 = 1.7174 // In kJ/kgK
+s6=s5
+h6 = 315.79 // In kJ/kg
+m = P/((h6-h5) + (1-m1)*(h2-h1))
+m_e = (1-m1)*m
+COP = m_e*(h1-hf)/P
+printf("\n The COP of the plant is %f, \n The mass flow rate of refrigerant in the evaporator is %f kg/s",COP,m_e)
+
+
diff --git a/3685/CH14/EX14.6/Ex14_6.txt b/3685/CH14/EX14.6/Ex14_6.txt
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+
+ Example 14.6
+
+ The COP of the plant is 5.935060,
+ The mass flow rate of refrigerant in the evaporator is 3.380453 kg/s \ No newline at end of file