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Diffstat (limited to '2705/CH5/EX5.16')
-rwxr-xr-x | 2705/CH5/EX5.16/Ex5_16.sce | 40 |
1 files changed, 40 insertions, 0 deletions
diff --git a/2705/CH5/EX5.16/Ex5_16.sce b/2705/CH5/EX5.16/Ex5_16.sce new file mode 100755 index 000000000..37712f1ac --- /dev/null +++ b/2705/CH5/EX5.16/Ex5_16.sce @@ -0,0 +1,40 @@ +clear;
+clc;
+disp('Example 5.16');
+
+// aim : To determine the
+// (a) initial partial pressure of the steam and air
+// (b) final partial pressure of the steam and air
+// (c) total pressure in the container after heating
+
+// Given values
+T1 = 273+39;// initial temperature,[K]
+P1 = 100;// pressure, [MN/m^2]
+T2 = 273+120.2;// final temperature,[K]
+
+// solution
+
+// (a)
+// from the steam tables, the pressure of wet steam at 39 C is
+Pw1 = 7;// partial pressure of wet steam,[kN/m^2]
+// and by Dalton's law
+Pa1 = P1-Pw1;// initial pressure of air, [kN/m^2]
+
+mprintf('\n (a) The initial partial pressure of the steam is = %f kN/m^2',Pw1);
+mprintf('\n The initial partial pressure of the air is = %f kN/m^2\n',Pa1);
+
+// (b)
+// again from steam table, at 120.2 C the pressure of wet steam is
+Pw2 = 200;// [kN/m^2]
+
+// now since volume is constant so assuming air to be ideal gas so for air P/T=contant, hence
+Pa2 = Pa1*T2/T1 ;// [kN/m^2]
+
+mprintf(' \n(b) The final partial pressure of the steam is = %f kN/m^2',Pw2);
+mprintf('\n The final partial pressure of the air is = %f kN/m^2\n',Pa2);
+
+// (c)
+Pt = Pa2+Pw2;// using dalton's law, total pressure,[kN/m^2]
+mprintf('\n (c) The total pressure after heating is = %f kN/m^2\n',Pt);
+
+// End
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