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authorprashantsinalkar2017-10-10 12:27:19 +0530
committerprashantsinalkar2017-10-10 12:27:19 +0530
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+clear;
+clc;
+printf('FUNDAMENTALS OF HEAT AND MASS TRANSFER \n Incropera / Dewitt / Bergman / Lavine \n EXAMPLE 13.2 Page 821 \n')// Example 13.2
+
+// View Factors of known surface Geometries
+
+// (1) Sphere within Cube
+F12a = 1 ;//By Inspection
+F21a = (%pi/6)*F12a ; //By Reciprocity
+
+// (2) Partition within a Square Duct
+F11b = 0 ;//By Inspection
+//By Symmetry F12 = F13
+F12b = (1-F11b)/2 ; //By Summation Rule
+F21b = sqrt(2)*F12b ; //By Reciprocity
+
+// (3) Circular Tube
+//From Table 13.2 or 13.5, with r3/L = 0.5 and L/r1 = 2
+F13c = .172;
+F11c = 0; //By Inspection
+F12c = 1 - F11c - F13c ;//By Summation Rule
+F21c = F12c/4 ;//By Reciprocity
+
+printf('\n Desired View Factors may be obtained from inspection, the reciprocity rule, the summation rule and/or use of charts \n (1) Sphere within Cube F21 = %.3f \n (2) Partition within a Square Duct F21 = %.3f \n (3) Circular Tube F21 = %.3f',F21a,F21b,F21c); \ No newline at end of file