summaryrefslogtreecommitdiff
path: root/409/CH15/EX15.2/Example15_2.sce
diff options
context:
space:
mode:
Diffstat (limited to '409/CH15/EX15.2/Example15_2.sce')
-rwxr-xr-x409/CH15/EX15.2/Example15_2.sce20
1 files changed, 20 insertions, 0 deletions
diff --git a/409/CH15/EX15.2/Example15_2.sce b/409/CH15/EX15.2/Example15_2.sce
new file mode 100755
index 000000000..597fd0bfb
--- /dev/null
+++ b/409/CH15/EX15.2/Example15_2.sce
@@ -0,0 +1,20 @@
+clear ;
+clc;
+// Example 15.2
+printf('Example 15.2\n\n');
+//Page No. 465
+// Solution
+
+// Given
+R = 10.73 ;// gas constant-[(cubic feet *psia)/(lb mol *R)]
+a = 3.49 * 10^4 ;//(psia) *(cubic feet/lb mol)^2
+b = 1.45 ;// (cubic feet)/(lb mol)
+p = 679.7 ;// Pressure -[ psia]
+n = 1.136 ;// Amount of mole -[lb mol]
+T = 683 ;// Temperature - [degree R]
+
+// Get V using Van der Waal's eqn.
+deff('[y]=g(V)','y=(V^3) -(((p*n*b) + (n*R*T))/p)*V^2 + ((n^2)*a*V/p) - ((n^3)*a*b)/p');
+V=fsolve(b,g) ;// Volume of final solution (volume of vessel) [cubic feet]
+
+printf('\nVolume of final solution (volume of vessel) is %.0f cubic feet.',V); \ No newline at end of file