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authorpriyanka2015-06-24 15:03:17 +0530
committerpriyanka2015-06-24 15:03:17 +0530
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+clear;
+clc;
+
+// Example: 8.6
+// Page: 303
+
+printf("Example: 8.6 - Page: 303\n\n");
+
+// Solution
+
+//*****Data******//
+Tl = 273;// [K]
+Th = 313;// [K]
+H1 = 187;// [Enthalpy of saturated vapour at 273 K, kJ/kg]
+H3 = 74;// [Enthalpy of saturated liquid at 313 K,kJ/kg]
+H4 = H3;// [kJ/kg]
+H2 = 204;// [Enthalpy of Supersaturated Vapour at 273 K, kJ/kg]
+//****************//
+
+// Solution (i)
+// COP = Ql/Wnet;
+COP = ((H1 - H4)/(H2 - H1));
+printf("Enthalpy of saturated vapour is %.2f\n",COP);
+
+// Solution (ii)
+Ref_Effect = H1 - H4;// [kJ/kg]
+printf("Refrigerating Effect is %d kJ/kg\n",Ref_Effect);
+
+// Solution (iii)
+COP = Tl/(Th - Tl);
+printf("The COP of an ideal Carnot refrigerator is %.2f\n",COP);
+
+// Solution (iv)
+W = H2 - H1;// [kJ/kg]
+printf("Work done by the compression is %.2f kJ/kg\n",W); \ No newline at end of file