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Diffstat (limited to '2471/CH9/EX9.7/Ex9_7.sce')
-rwxr-xr-x | 2471/CH9/EX9.7/Ex9_7.sce | 33 |
1 files changed, 33 insertions, 0 deletions
diff --git a/2471/CH9/EX9.7/Ex9_7.sce b/2471/CH9/EX9.7/Ex9_7.sce new file mode 100755 index 000000000..78cfb2b1e --- /dev/null +++ b/2471/CH9/EX9.7/Ex9_7.sce @@ -0,0 +1,33 @@ +clear ;
+clc;
+// Example 9.7
+printf('Example 9.7\n\n');
+printf('Page No. 269\n\n');
+
+//given
+l_1 = 240;// existing length of solid brick in mm
+l_u = 25;// upgraded internal lining in mm
+l_e = 9.5;// Expanded polystyrenne in mm
+T_i = 20;// Internal temperature in degre celcius
+R_H_i = 50;// Internal Relative humidity in percent
+T_e = 0;// External temperature in degre celcius
+R_H_e = 90;// External Relative humidity in percent
+
+K = [0.123 0.059 0.714 0.286 0.055];// Thermal resistance in W/m^2-K
+V_r = [0.0 0.475 3.57 9.60 0.0];// Vapour Resistance in 10^9 N-s/kg
+
+//Refer Figure 9.3
+//From Figure 9.3, the tempeature, dew point, vapour pressure for different interface are obtained
+T = [18.01 17.06 5.51 0.89];// Temperature in degree celcius
+V_p = [1170 1148 986 550];//Vapour pressure in N/m^2
+D_P = [9.5 9.2 7.1 -1.5];// Dew point in degree celcius
+
+h = (T_i - T_e)/sum(K);// in W/m^2
+printf('The heat flow is %.2f W/m^2 \n',h)
+V_p_i = V_p(1);// Internal vapour pressure in N/m^2
+V_p_e = V_p(4);// External vapour pressure in N/m^2
+m = ((V_p_i - V_p_e)/sum(V_r))*10^-9;// in kg/s
+printf('The vapour mass flow is %.1e kg/s',m)
+
+
+
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