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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 /1309/CH7/EX7.1 | |
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initial commit / add all books
Diffstat (limited to '1309/CH7/EX7.1')
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-rwxr-xr-x | 1309/CH7/EX7.1/Result7_1.pdf | bin | 0 -> 94313 bytes | |||
-rwxr-xr-x | 1309/CH7/EX7.1/ch7_1.sce | 64 |
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diff --git a/1309/CH7/EX7.1/Figure7_1.jpeg b/1309/CH7/EX7.1/Figure7_1.jpeg Binary files differnew file mode 100755 index 000000000..1fd5736f2 --- /dev/null +++ b/1309/CH7/EX7.1/Figure7_1.jpeg diff --git a/1309/CH7/EX7.1/Result7_1.pdf b/1309/CH7/EX7.1/Result7_1.pdf Binary files differnew file mode 100755 index 000000000..6ce8becb5 --- /dev/null +++ b/1309/CH7/EX7.1/Result7_1.pdf diff --git a/1309/CH7/EX7.1/ch7_1.sce b/1309/CH7/EX7.1/ch7_1.sce new file mode 100755 index 000000000..e82146a44 --- /dev/null +++ b/1309/CH7/EX7.1/ch7_1.sce @@ -0,0 +1,64 @@ +clc;
+clear;
+printf("\t\t\tChapter7_example1\n\n\n");
+printf("\t\t\tSolution to part (a)\n");
+// determination of boundary layer growth with length
+// properties of air at 27 degree celsius from appendix table D.1
+rou=1.177; // density in kg/cu.m
+v=15.68e-6; // viscosity in sq.m/s
+L=0.5; // length in m
+V_inf=1; // air velocity in m/s
+Re= (V_inf*L)/v; // Reynolds Number
+printf("The Reynolds Number is %.2e ",Re);
+// Reynolds Number is less than 5e5 hence the flow is laminar and Blasius Solution applies
+x=[0 0.125 0.25 0.375 0.5]; // distances in m where boundary layer growth is determined
+[n,m]=size(x);
+for i=1:m
+ delta(i)=5*x(i)^0.5/(V_inf/v)^0.5;
+end
+subplot(211);
+plot(x,delta);
+a=gca();
+newTicks=a.x_ticks;
+newTicks(2)=[0;0.125;0.25;0.375;0.5];
+newTicks(3)=['0';'0.125';'0.25';'0.375';'0.50'];
+a.x_ticks=newTicks;
+title('Boundary-layer growth with distance');
+xlabel('x, m');
+ylabel('delta, m^(1/2)');
+printf("\n\t\t\tSolution to part (b)\n");
+// produce graph of velocity distribution at x=0.25 m
+eta=0:5;
+[p,q]=size(eta);
+f=[0 0.32979 0.62977 0.84605 0.95552 0.99155];//value for f for corresponding eta value from Table 7.1
+for j=1:q
+ y(j)=eta(j)*(v*0.25)^0.5;
+end
+printf("\n\t\t\tResults of Calculations for Example 7.1\n");
+printf("\teta\t\ty,m\t\t\tf=vx, m/s\n");
+for i=1:q
+printf("\t%d\t\t%.2e\t\t%.5f\n",eta(i),y(i),f(i));
+end
+subplot(212);
+plot(f,y);
+b=gca();
+newTicks1=b.x_ticks;
+newTicks1(2)=[0;0.25;0.5;0.75;1.0];
+newTicks1(3)=['0';'0.25';'0.5';'0.75';'1.0'];
+b.x_ticks=newTicks1;
+newTicks2=b.y_ticks;
+newTicks2(2)=[0;0.0025;0.005;0.0075;0.010];
+newTicks2(3)=['0';'0.0025';'0.005';'0.0075';'0.010'];
+b.y_ticks=newTicks2;
+title('Velocity Distribution at x=0.25 m');
+xlabel('Vx, m/s');
+ylabel('y, m');
+printf("\t\t\tSolution to part (c)\n");
+// calculation of absolute viscosity
+gc=1;
+mu=rou*v/gc;
+printf("\nThe absolute viscosity is %.3e N.s/sq.m",mu);
+b=1; // width in m
+Df=0.664*V_inf*mu*b*(Re)^0.5;
+printf("\nThe skin-drag is %.2e N",Df);
+printf("\nThe skin-drag including both sides of plate is %.2e N",2*Df);
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