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author | priyanka | 2015-06-24 15:03:17 +0530 |
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committer | priyanka | 2015-06-24 15:03:17 +0530 |
commit | b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b (patch) | |
tree | ab291cffc65280e58ac82470ba63fbcca7805165 /2006/CH7/EX7.12 | |
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initial commit / add all books
Diffstat (limited to '2006/CH7/EX7.12')
-rwxr-xr-x | 2006/CH7/EX7.12/ex7_12.sce | 16 |
1 files changed, 16 insertions, 0 deletions
diff --git a/2006/CH7/EX7.12/ex7_12.sce b/2006/CH7/EX7.12/ex7_12.sce new file mode 100755 index 000000000..052d2258f --- /dev/null +++ b/2006/CH7/EX7.12/ex7_12.sce @@ -0,0 +1,16 @@ +clc;
+p1=1; // Pressure of fluid at inlet in bar
+T1=60; // Temperature of fluid at inlet in degree celcius
+p2=2.8; // Pressure of fluid at outlet in bar
+eff_d=0.80; // Diffuser efficiency
+k=1.4; // Index of reversible adiabatic process
+Cpo=1.0035; // Specific heat at constant pressure in kJ/kg K
+// (a).Actual Diffuser
+p2s=((p2-p1)/eff_d)+p1; // Isentropic pressure
+T2=(T1+273)*(p2s/p1)^((k-1)/k); // Exit temperature
+V1=sqrt (2000*Cpo*(T2-(T1+273))); // Initial Velocity
+disp ("m/s",V1,"Initial Velocity =","K",T2,"Temperature of air leaving diffuser =","(a).Actual Diffuser");
+// (b).Reversible Adiabatic diffuser
+T2s=(T1+273)*(p2/p1)^((k-1)/k); // Isentropic exit temperature
+V1=sqrt (2000*Cpo*(T2s-(T1+273))); // Initial Velocity
+disp ("m/s",V1,"Initial Velocity =","K",T2s,"Temperature of air leaving diffuser =","(b).Reversible Adiabatic diffuser");
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