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authorprashantsinalkar2017-10-10 12:27:19 +0530
committerprashantsinalkar2017-10-10 12:27:19 +0530
commit7f60ea012dd2524dae921a2a35adbf7ef21f2bb6 (patch)
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parentb1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b (diff)
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+clc;
+clear all;
+disp("heat transfer rate")
+d=300/1000;//m diameter
+L=3.5;//m
+delT=40;//degree C =ts-ti
+f=0.022;// friction factor
+St=f/2;
+disp("The energy balance yields Q=h*A*(ts-ta)=m*cp*(to-ti)")
+disp("h*(%pi*D*L)*(ts-(to+ti)/2)=rho*(%pi*D^2*U/4)*cp(to-ti)")
+disp("(h/(rho*U*cp))*L*(ts-to+ts-ti)/2=D/4*(to-ti)")
+disp("St*L/2*(ts-to+ts-ti)=D/4*((ts-ti)-(ts-to))")
+disp("f/8*L/2*(ts-to+ts-ti)=D/4*((ts-ti)-(ts-to))")
+disp("thus by putting the values, ")
+
+t1=(d/4-f/8*L/2)*delT/(f/8*L/2+d/4)// ts-to
+t=delT-t1;
+disp("degree C",t,"Rise in the temperature of fluid at the end =")
+