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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 /1073/CH3/EX3.7 | |
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-rwxr-xr-x | 1073/CH3/EX3.7/3_7.sce | 32 |
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diff --git a/1073/CH3/EX3.7/3_7.sce b/1073/CH3/EX3.7/3_7.sce new file mode 100755 index 000000000..b56e80d9d --- /dev/null +++ b/1073/CH3/EX3.7/3_7.sce @@ -0,0 +1,32 @@ +clc; +clear; +//Example 3.7 +rho=0.998 //kg/cubic m +v=20.76*10^-6 //[sq m/s] +Cp=1.009 //[kJ/kg.K] +k=0.03 //[W/m.K] +u_inf=3 //[m/s] +x=0.4 //[m] +w=1.5 //[m] +Nre_x=u_inf*x/v //Reynolds no at x=0.4 m +//Since this is less than 3*10^5.The flow is laminar upto x=0.4 m +mu=rho*v //[kg/(m.s)] + +Cp=1.009 //[kJ/kg.K] +Cp=Cp*1000 //[J/kg.K] +k=0.03 //W/(m.K) +Npr=Cp*mu/k +Nnu_x=0.332*(sqrt(Nre_x))*(Npr^(1.0/3.0)) +hx=Nnu_x*k/x //[W/(m.K)] +//Average value is twice this value +h=2*hx //[W/(m.K)] +h=10.6 //Approximation +A=x*w //Area in [sq m] +Tw=407 //[k] +T_inf=293 //[K] +Q=h*A*(Tw-T_inf) //[W] +//From both sides of the plate: +Q=2*Q //[W] +printf("The heat transferred from both sides of the plate is %d W",round(Q)); + + |