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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/EX7.10/ex7_10.sce | |
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initial commit / add all books
Diffstat (limited to '2006/CH7/EX7.10/ex7_10.sce')
-rwxr-xr-x | 2006/CH7/EX7.10/ex7_10.sce | 25 |
1 files changed, 25 insertions, 0 deletions
diff --git a/2006/CH7/EX7.10/ex7_10.sce b/2006/CH7/EX7.10/ex7_10.sce new file mode 100755 index 000000000..d09bc6010 --- /dev/null +++ b/2006/CH7/EX7.10/ex7_10.sce @@ -0,0 +1,25 @@ +clc;
+p1=3; // Pressure of fluid at inlet in bar
+T1=150; // Temperature of fluid at inlet in degree celcius
+V1=90; // Velocity of fluid at inlet in m/s
+eff_nozzle=0.85; // Nozzle efficiency
+k=1.4; // Index of reversible adiabatic process
+p2=1/3*p1;
+// (a).Steam
+// Following are taken from steam table
+h1=2761; // specific enthalpy in kJ/kg
+s1=7.0778;// specific entropy in kJ/kg K
+s2s=s1; // Isentropic process
+sf2s=1.3026; sfg2s=6.0568;// specific entropy in kJ/kg K
+hf2=417.46; hfg2=2258; // specific enthalpy in kJ/kg
+x2s=(s2s-sf2s)/sfg2s; // Quality of steam
+h2s=hf2+x2s*hfg2;
+V2s=sqrt (2000*(h1-h2s)+V1^2); // Isentropic Velocity
+V2=sqrt (eff_nozzle) *V2s; // Actual nozzle exit velocity
+disp ("m/s (round off error)",V2," Actual nozzle exit velocity = ","(a).Steam");
+// (b).Air
+Cpo=1.0035; // Specific heat at constant pressure in kJ/kg K
+T2s=(T1+273)*(p2/p1)^((k-1)/k); // Isentropic temperature
+V2s=sqrt ((2000*Cpo*((T1+273)-T2s))+V1^2); // Isentropic Velocity and (answer mentioned in the textbook is wrong)
+V2=sqrt (eff_nozzle) *V2s; // Actual nozzle exit velocity
+disp ("m/s (answer mentioned in the textbook is wrong)",V2," Actual nozzle exit velocity = ","(b).Air");
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