//Harriot P.,2003,Chemical Reactor Design (I-Edition) Marcel Dekker,Inc. USA,pp 436. //Chapter-10 Ex10.2.b Pg No. 414 //Title:Yield as function of No. of Gauzes //=========================================================================================================== clear clc //INPUT M_NH3 = 17;//Molecular weight NH3 M_air = 29;//Molecular weight air f_air = 0.9;//Fraction of air in feed f_NH3 = (1-f_air);//Fraction of NH3 in feed myu_air = 0.0435*(10^-2);//Viscosity of air (Poise) P_atm = (100+14.7)/14.7;//Pressure of the system P_ref = 1;//Reference Pressure T_ref = 273;//Reference temperature T_inlet = 300+T_ref;//Inlet Temperature V_ref = 22400; T_surf = 700+T_ref;//Surface Temperature u0 = 1.8;//Velocity at 300 °C (m/sec) d = 0.076*(10^-1);//Size of wire (cm) D_NH3_N2 = 0.23;//Diffusivity at 298 K 1 atm(cm2/s) N = 32;//Gauzes (wires/cm) frac_N2 = 0.25*(10^(-2));//Fraction of NH3 fed into N2 (Byproduct reaction) n = [1 2 5 10 15 20];//No. of Gauzes //CALCULATION M_ave = f_air*M_air+f_NH3*M_NH3; rho = (M_ave*T_ref*P_atm)/(V_ref*T_surf*P_ref); u0_surf = u0*(T_surf/T_inlet); Re = rho*u0_surf*100*d/myu_air; Gamma = [1-32*(d)]^2;//From equation 10.5 Re_Gamma = Re/Gamma; D_NH3 = 0.23*(T_surf/298)^(1.7)*(1/7.8);// at 7.8 atm 700 °C Sc = (myu_air*P_ref)/(rho*D_NH3); j_D = 0.644*(Re_Gamma)^(-0.57);//Refer equation 10.14 k_c = j_D*(u0_surf*100/Gamma)*(1/(Sc)^(2/3)); a_dash = 2*(%pi)*(d)*N k_c_a_dash_u0 =(k_c*a_dash)/(u0_surf*100); m = length(n) for i = 1:m X(i) = (1-exp(-k_c_a_dash_u0*n(i))); Yield(i) = X(i)-frac_N2*n(i); end //OUTPUT //File Output fid=mopen('.\Chapter10_Ex2_b_Output.txt', 'w'); mfprintf(fid,'\n \tThe Ammonia Yield'); mfprintf(fid,'\n=========================================='); mfprintf(fid,'\n\t Gauzes Yield'); mfprintf(fid,'\n\t (n) (X-%fn)',frac_N2); mfprintf(fid,'\n=========================================='); for i=1:m mfprintf(fid,'\n\t %.0f \t \t %.3f',n(i),Yield(i)); end mclose(fid); //Console Output mprintf('\n \tThe Ammonia Yield'); mprintf('\n=========================================='); mprintf('\n\t Gauzes Yield'); mprintf('\n\t (n) (X-%fn)',frac_N2); mprintf('\n=========================================='); for i=1:m mprintf('\n\t %.0f \t \t %.3f',n(i),Yield(i)); end //====================================================END OF PROGRAM====================================================