initial commit / add all books

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diff --git a/1309/CH6/EX6.1/ch6_1.sce b/1309/CH6/EX6.1/ch6_1.sce
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+clc;
+clear;
+printf("\t\t\tChapter6_example1\n\n\n");
+// Determination of the fluid outlet tetnperature and the tube-wall temperature at the outlet.
+// properties of ethylene glycol at 20 degree celsius from appendix table C5
+Cp_20=2382;
+rou_20=1.116*1000;
+v_20=19.18e-6;
+kf_20=.249;
+a_20=.939e-7;
+Pr_20=204;
+// specifications of 1/2 standard type M seamless copper water tubing from appendix table F2
+OD=1.588/100;
+ID=1.446/100;
+A=1.642e-4;
+Q=3.25e-6;
+V=Q/A;
+printf("\nThe average flow velocity is %.1f m/s",V*100);
+// calculation of Reynold's Number to check flow regime
+Re=V*ID/v_20;
+printf("\nThe Reynolds Number is %.1f",Re);
+// since Re>he 2100, the flow regime is laminar and the hydrodynamic length can be calculated as
+Z_h=0.05*ID*Re;
+printf("\nThe hydrodynamic length is %.1f cm",Z_h*100);
+Tbi=20; // bulk-fluid inlet temperature in degree celsius
+qw=2200; // incident heat flux in W/m^2
+L=3; // Length of copper tube in m
+R=ID/2; // inner radius in m
+Tbo=Tbi+(2*qw*a_20*L)/(V*kf_20*R);
+printf("\nThe bulk-fluid outlet temperature is %.1f degree celsius",Tbo);
+// This result is based on fluid properties evaluated at 20°C. taken as a first approximation
+Z_t=0.05*ID*Re*Pr_20;
+printf("\nThe thermal entry length is %.1f m",Z_t);
+Two=Tbo+(11*qw*ID)/(48*kf_20); // The wall temperature at outlet in degree celsius
+printf("\nThe wall temperature at outlet is %.1f degree celsius",Two);
+//The result is based on first approximation based on flow properties evaluated at the fluid inlet temperature.