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| author | prashantsinalkar | 2017-10-10 12:27:19 +0530 |
|---|---|---|
| committer | prashantsinalkar | 2017-10-10 12:27:19 +0530 |
| commit | 7f60ea012dd2524dae921a2a35adbf7ef21f2bb6 (patch) | |
| tree | dbb9e3ddb5fc829e7c5c7e6be99b2c4ba356132c /926/CH3/EX3.4 | |
| parent | b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b (diff) | |
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initial commit / add all books
Diffstat (limited to '926/CH3/EX3.4')
| -rw-r--r-- | 926/CH3/EX3.4/Chapter3_Example4.sce | 26 |
1 files changed, 26 insertions, 0 deletions
diff --git a/926/CH3/EX3.4/Chapter3_Example4.sce b/926/CH3/EX3.4/Chapter3_Example4.sce new file mode 100644 index 000000000..426502ab9 --- /dev/null +++ b/926/CH3/EX3.4/Chapter3_Example4.sce @@ -0,0 +1,26 @@ +//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-3, Illustration 4, Page 55
+//Title: Calculation of temperature
+//=============================================================================
+clear
+clc
+
+//INPUT
+W = 10; //Weight of nitrogen in lb
+MW = 28; //Molecular weight of nitrogen in lb/lb mole
+P1 = 14.7; //Pressure at standard conditions in psi
+T1 = 273; //Temperature at standard conditions in K
+P2 = 150; //Maximum pressure in psi
+V2 = 30; //Given volume of nitrogen in cu ft
+
+//CALCULATIONS
+n = W/MW; //No of moles of Nitrogen at standard conditions in lb mole
+V1 = n*359; //Volume of nitrogen at standard conditions in cu ft
+T2 = T1*(P2/P1)*(V2/V1); //Temperature at given conditions in K
+T = T2-273; //Temperature at given conditions in degree C
+
+//OUTPUT
+mprintf('\n The maximum temperature to which %2.0f lb of nitrogen can be heated is %4.0f K or %4.0f degree C',W,T2,T);
+
+//========================= END OF PROGRAM ====================================
\ No newline at end of file |