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diff --git a/3751/CH11/EX11.13/Ex11_13.sce b/3751/CH11/EX11.13/Ex11_13.sce new file mode 100644 index 000000000..0dde95b26 --- /dev/null +++ b/3751/CH11/EX11.13/Ex11_13.sce @@ -0,0 +1,56 @@ +//Fluid Systems - By - Shiv Kumar +//Chapter 11- Centrifugal Pumps +//Example 11.13 +//To Find (i)The Discharge of the Pump (ii)The Pressure at Suction and Delivery side of the Pump. + + clc + clear + +//Given Data:- + h_st=35; //Static Head, m + h_s=4; //Suction Head, m + D=150; //Diameter of Pipes, mm + Ds=D; //Diameter of Suction Pipe, mm + Dd=D; //Diameter of Delivery Pipe, mm + h_fs=1.6; //Head loss in Suction pipe, m + h_fd=6.5; //Head loss in Delivery Pipe, m + Do=380; //Diameter of Impeller at Outlet, mm + bo=25; //Width of Impeller at Outlet, mm + N=1200; //Speed, rpm + beta_o=35; //Ezxit Blade Angle, degrees + eta_man=80/100; //Manometric Efficiency + + +//Data Used:- + g=9.81; //Acceleration due to gravity, m/s^2 + +//Computations:- + Do=Do/1000; //m + D=D/1000; //m + Ds=Ds/1000; //m + Dd=Dd/1000; //m + bo=bo/1000; //m + + Hm=h_st+h_fs+h_fd; // Manometric Head, m + uo=%pi*Do*N/60; // Tangential velocity of Impeller at Outlet, m/s + Vwo=g*Hm/(uo*eta_man); //m/s + Vfo=(uo-Vwo)*tand(beta_o); //m/s + + //(i)The Discharge of the Pump, Q + Q=%pi*Do*bo*Vfo*1000; //litres/s + + // (ii)The Pressure at Suction and Delivery side of the Pump + + A=(%pi/4)*D^2; //m^2 + Vd=Q*10^-3/A; //m/s + Vs=Vd; //m/s + Hs=h_s+h_fs+Vs^2/(2*g); //Pressure on Suction Side, m of water + h_d=h_st-h_s; //m + Hd=h_d+h_fd+Vd^2/(2*g); //Pressure on Delivery Side, m of water + + +//Result:- + printf(" (i)The Discharge of the Pump, Q =%.2f litres/s\n",Q) //The answer vary due to round off error + printf(" (ii) Pressure on Suction Side, Hs =-%.3f m of water \n",Hs) //The answer vary due to round off error + printf(" Pressure on Delivery Side, Hd =%.2f m of water \n",Hd) //The answer vary due to round off error + |