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+//Fluid Systems- By Shiv Kumar
+//Chapter 5- Francis Turbine
+//Example 5.12
+ clc
+ clear
+
+//Given Data:-
+ Dp=5; //Diameter at Penstock, m
+ P=61000; //Output Power, kW
+ Q=110; //Discharge, m^3/s
+ N=160; //Speed, rpm
+ eta_H=94/100; //Hydraulic Efficiency
+ Do=4; //Diameter of Runner at Inlet, m
+ bo=1; //Width of Runner at Inlet, m
+ Ddi=4.2; //Entry Diameter to Draft Tube, m
+ V2=2.2; //Velocity in Tail Race, m/s
+ p_by_rho_g=58; //Static Pressure Head (p/(rho*g)) , m
+ Z=2.8; //Level of Measurement above Tail Race, m
+ loss=25; //Percentage of loss in Draft Tube (of Velocity Head at its Entry)
+ Z1=2.2; //Level of Runner Exit above Tail Race, m
+
+//Data Required:-
+ rho=1000; //Density of Water, Kg/m^3
+ g=9.81; //Acceleration due to gravity, m/s^2
+
+//Computations:-
+ Vp=4*Q/(%pi*Dp^2); //Velocity in Penstock, m/s
+ Vo=4*Q/(%pi*Ddi^2); //Velocity at Entry to the Draft Tube, m/s
+ Hp=p_by_rho_g+Z+Vp^2/(2*g); //Head just before Entry to Runner, m
+ H=Hp-V2^2/(2*g); //Working Head, m
+
+ //(a)Overall Efficiency
+ eta_o=P*1000/(rho*Q*g*H)*100; //In Percentage
+
+ // (b) The Direction of Flow relative to the Runner at Inlet
+ ui=%pi*Do*N/60; //m/s
+ Vwi=eta_H*g*H/ui; //m/s
+ Vfi=Q/(%pi*Do*bo); //m/s
+ beta_i=180-atand(Vfi/(ui-Vwi)); //degrees
+
+ // (c) The Pressure Head at entry to Draft Tube, p1/(rho*g)
+ //By Applying Bernoulli's Equation with,
+ Z2=0;
+ p2_by_rho_g=0;
+ hf=(loss/100)*Vo^2/(2*g);
+
+ p1_by_rho_g=p2_by_rho_g+(V2^2-Vo^2)/(2*g)+(Z2-Z1)+hf; //m
+
+
+//Results:-
+ printf("(a)The Overall Efficiency, eta_o=%.2f Percent\n",eta_o) //The Answer Vary due to Round off Error
+ printf("(b)The Direction of Flow relative to the Runner at Inlet, beta_i=%.2f Degrees \n",beta_i) //The Answer Vary due to Round off Error
+ printf("(c) The Pressure Head at entry to Draft Tube, p1/(rho*g)=%.2f m (vaccum)\n",abs(p1_by_rho_g))
+
+