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+///Chapter No 11 Steam Boilers

+////Example 11.16 Page No 247

+///Find Theoretical draught produced in water

+//Input data

+clc;

+clear;

+hw=1.9;           //Drauhgt water in cm

+Tg=290+273;       //Temp of flue gases in degree celsius 

+Ta=20+273;        //Ambient temp in degree celsius

+ma=22;            //Flue gases formed in kg/Kg of coal

+d=1.8;            //Fuel burnt in m

+pi=3.142;

+g=9.81;

+

+//Calculation

+H=(hw/(353*(1/Ta-1/Tg*((ma+1)/ma))))*10; //Theoretical draught produced in water column in m

+H1=round(H*(((Tg/Ta)*(ma/(ma+1))-1)));          //Theoretical draught produced in hot gas column n m

+V=sqrt(2*g*H1);                     //Velocity of tthe flue gases in the chimney in m/s 

+rhog=((353*(ma+1))/(ma*Tg));             //Density  of flue gases in Kg/m^3

+mg=rhog*((pi/4)*d^2)*V;                 //Mass of gas flowing through the chimney in Kg/s

+

+//Output

+printf('Theoretical draught produced in water column= %f m \n ',H);

+printf('Theoretical draught produced in hot gas column= %f m \n',H1);

+printf('Velocity of tthe flue gases in the chimney= %f m \n',V);

+printf('Density  of flue gases=%f Kg/m^3 \n',rhog);

+printf('Mass of gas flowing through the chimney= %f Kg/s \n',mg);