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diff --git a/926/CH8/EX8.3/Chapter8_Example3.sce b/926/CH8/EX8.3/Chapter8_Example3.sce new file mode 100644 index 000000000..888c33113 --- /dev/null +++ b/926/CH8/EX8.3/Chapter8_Example3.sce @@ -0,0 +1,28 @@ +//Hougen O.A., Watson K.M., Ragatz R.A., 2004. Chemical process principles Part-1: Material and Energy Balances(II Edition). CBS Publishers & Distributors, New Delhi, pp 504
+
+//Chapter-8, Illustration 3, Page 278
+//Title: Calculation of heat of vaporization
+//=============================================================================
+clear
+clc
+
+//INPUT
+T = 200; //Given temperature in degree F
+TC = 232.5; //Critical temperature of Freon 12 in degree F
+SRTR = .516; //Heat of vaporization factor of Freon 12 from Table 27, Page 278
+
+//CALCULATION
+TR = (T+460)/(TC+460); //Reduced temperature of freon 12 at 200 degree F
+Lamda_1 = 7707; //Molal heat of vaporization of water at TR=0.951 in BTU per lb-mole obtained from Table page 279
+Lamda_2 = Lamda_1*SRTR; //Heat of vaporization of freon 12 at 200 degree F
+
+//OUTPUT
+// Console Output
+mprintf('\n Heat of vaporization of freon 12 at 200 degree F = %4.0f BTU per lb-mole',Lamda_2);
+
+// File Output
+fd= mopen('.\Chapter8_Example3_Output.txt','w'); // PRN: File name and path changed NAR
+mfprintf(fd,'\n Heat of vaporization of freon 12 at 200 degree F = %4.0f BTU per lb-mole',Lamda_2);
+mclose(fd);
+
+//=================================END OF PROGRAM==============================
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