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Diffstat (limited to '1052/CH13/EX13.1/131.sce')
-rwxr-xr-x | 1052/CH13/EX13.1/131.sce | 24 |
1 files changed, 24 insertions, 0 deletions
diff --git a/1052/CH13/EX13.1/131.sce b/1052/CH13/EX13.1/131.sce new file mode 100755 index 000000000..e25505f58 --- /dev/null +++ b/1052/CH13/EX13.1/131.sce @@ -0,0 +1,24 @@ +clc;
+//Example 13.1
+//page no 136
+printf("Example 13.1 page no 136\n\n");
+//calculate average velocities for which th flow will be viscous,laminar
+//(a) water at 60 deg F in a 2-inch standard pipe
+R_e=2100//reynolds number <2100, for laminar flow
+meu_w=6.72e-4//viscosity of water,lb/ft.s
+rho_w=62.4//density of water,lb/ft^3
+D_w=2.067//diameter of pipe,ft
+v_w=(R_e*meu_w)/((D_w/12)*rho_w)//velocity of water
+printf("\n velocity v_w=%f ft/s",v_w);
+//(b) air at 60 deg F and 5 psig in a 2 inch standard pipe
+meu_a=12.1e-6//viscosity of air ,lb/ft.s
+rho_a=.1024// density of air,lb/ft^3
+D_a=0.17225//diameter of pipe ,ft
+v_a=(R_e*meu_a)/(D_a*rho_a)//velocity of air
+printf("\n velocity of air v_a=%f ft/s",v_a);
+//(c) oil of a viscosity of 300 cP and SG of .92 in a 4 inch standard pipe
+meu_o=300*6.72e-4//viscosity of oil ,lb/ft.s
+rho_o=0.92*62.4//density of oil, lb/ft^3
+D_o=.3355//diameter of pipe,ft
+v_o=round((R_e*meu_o)/(D_o*rho_o))//velocity of oil
+printf("\n velocity of oil v_o=%f ft/s",v_o);
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