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author | prashantsinalkar | 2017-10-10 12:27:19 +0530 |
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committer | prashantsinalkar | 2017-10-10 12:27:19 +0530 |
commit | 7f60ea012dd2524dae921a2a35adbf7ef21f2bb6 (patch) | |
tree | dbb9e3ddb5fc829e7c5c7e6be99b2c4ba356132c /3821/CH14/EX14.4/Example14_4.sce | |
parent | b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b (diff) | |
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diff --git a/3821/CH14/EX14.4/Example14_4.sce b/3821/CH14/EX14.4/Example14_4.sce new file mode 100644 index 000000000..fa5686b73 --- /dev/null +++ b/3821/CH14/EX14.4/Example14_4.sce @@ -0,0 +1,31 @@ +////Chapter No 14 Air Standard Cycles
+////Example No 14.4 Page No 304
+///Find Heat supplied process
+//input data
+clc;
+clear;
+T2=377+273; //Carnot cycle temperature in bar
+P2=20*10^5; //Carnot cycle pressure in bar
+V2=1;
+V1=5;
+V3=2;
+//Consider air as the working fluid therefore
+R=0.287; //In KJ/Kg K
+Cp=1.005; //In KJ/Kg K
+Cv=0.718; //In KJ/Kg K
+K=1.4;
+gamma1=1.4;
+
+//Calculation
+T1=T2*((V2/V1)^(gamma1-1)); //Minimum temp in degree celsius
+Qs=R*T2*log(V3/V2); //Heat supplied process in KJ/Kg
+QR=R*T1*log((V1/V2)*(V2/V3)*((T2/T1)^(1/(gamma1-1)))); //Heat Rejected Process in KJ/Kg
+etath=(1-(T1/T2))*100; //Thermal Effeiciency of the carnot cycle in %
+
+
+
+//Output
+printf('Minimum temp= %f degree celsius \n',T1);
+printf('Heat supplied process= %f KJ/Kg \n',Qs);
+printf('Heat Rejected Process= %f KJ/Kg \n',QR);
+printf('Thermal Effeiciency of the carnot cycle=%f percent \n',etath);
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