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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 /617/CH16/EX16.7 | |
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Diffstat (limited to '617/CH16/EX16.7')
-rwxr-xr-x | 617/CH16/EX16.7/Example16_7.sci | 34 |
1 files changed, 34 insertions, 0 deletions
diff --git a/617/CH16/EX16.7/Example16_7.sci b/617/CH16/EX16.7/Example16_7.sci new file mode 100755 index 000000000..e8b91d617 --- /dev/null +++ b/617/CH16/EX16.7/Example16_7.sci @@ -0,0 +1,34 @@ +clc();
+clear;
+
+// To calculate the amount of water evaporated in per hour for a square foot of water surface
+
+u=3.82*10^-7; // Viscosity in lb-sec/ft^2
+rho=2.3*10^-3; // Density in lbsec^2/ft^4
+A=1; // Area in ft^2
+Cp=0.24; // Specific heat capacity in abtu/lbm-degF
+v=4*3600; // Velocity in ft/sec
+k=0.015; // Thermal conductivity in Btu/hr-ft-degF
+p=14.7; // Atmospheric pressure in psi
+M=29; // Avg. molecular weight of air
+T1=70+460; // Temperature of still air in degF
+T2=90+460; // temperature of surface of water in degF
+L=1; // For characteristic of 1 ft
+D=0.992; // Diffusivity in ft^2/sec
+
+// Heat transfer equation for laminar flow of a flat surface
+Ngr=32.2*L^3*((T2/T1)-1)/(u/rho)^2; // Grasshops number
+Npr=u*3600*Cp*32.2/k; // Prandtls number
+Nnu=0.75*(Ngr*Npr)^.25; // Nusselt number
+h=Nnu*k/L; // Heat transfer coefficient
+Ns=u*3600/(rho*D); // Schimdt mumber
+hmc=h*D*(Ns/Npr)^0.25/k; // Heat transfer coe
+pv1=0.18; // Vapour pressure at 40% humidity
+pv2=0.69; // Vapour pressure at saturation
+pa1=p-pv1; // Absolute pressure of air at 40% rel. humidity in psi
+pa2=p-pv2; // Absolute pressure of saturated air in psi
+pbm=(pa1+pa2)/2; // Log mean pressure in psi
+R=1544; // Universal gas constant in ft^3-psi/lbmol-degR
+T=(T1+T2)/2; // Average temperature in degR
+N=hmc*p*(pv2-pv1)*144/(R*T*pbm)*18; // mass transfer rate in lbmol/hr-ft^2
+printf("The amount of water evaporated per hour is %.4f lb mol/hr-ft^2",N);
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