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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 /581/CH3/EX3.3 | |
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Diffstat (limited to '581/CH3/EX3.3')
-rwxr-xr-x | 581/CH3/EX3.3/Example3_3.sci | 19 |
1 files changed, 19 insertions, 0 deletions
diff --git a/581/CH3/EX3.3/Example3_3.sci b/581/CH3/EX3.3/Example3_3.sci new file mode 100755 index 000000000..e46ce2414 --- /dev/null +++ b/581/CH3/EX3.3/Example3_3.sci @@ -0,0 +1,19 @@ +
+clear;
+clc;
+
+printf("\t Example 3.3\n");
+
+T1=293; // Entering Temperature of Water, K
+T2=313; //Exit Temperature of water, K
+m=25/60;//Condensation rate of steam, kg/s
+T3=333; // Condensation Temperature,K
+A=12; //area of exchanger, m^2
+h=2358.7*10^3; //latent heat, J/kg
+
+U=(m*h)/(A*((T2-T1)/log((T3-T1)/(T3-T2))))+0.6;
+printf("\t Overall heat transfer coefficient is : %.0f W/(m^2*K)\n",U);
+
+Mh=(m*h)/(4174*(T2-T1));
+printf("\t required flow of water is : %.2f kg/s\n",Mh);
+//End
\ No newline at end of file |