1 files changed, 108 insertions, 0 deletions
diff --git a/1040/CH10/EX10.2/Chapter10_Ex2.sce b/1040/CH10/EX10.2/Chapter10_Ex2.sce
new file mode 100644
index 000000000..6e803f7a1
--- /dev/null
+++ b/1040/CH10/EX10.2/Chapter10_Ex2.sce
@@ -0,0 +1,108 @@
+//Harriot P., 2003, Chemical Reactor Design (I-Edition), Marcel Dekker, Inc., USA, pp 436.
+//Chapter-10 Ex10.2 Pg No. 414
+//Title:Conversion as a function of No. of Gauzes
+//===========================================================================================================
+clear
+clc
+// COMMON 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 (Ex 10.2.a)
+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)));
+end
+//CALCULATION (Ex 10.2.b)
+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(Ex 10.2.a)
+mprintf('\n OUTPUT Ex10.2.a');
+mprintf('\n=====================================');
+mprintf('\n \tThe Ammonia Conversion');
+mprintf('\n=====================================');
+mprintf('\n\t Gauzes        Conversion');
+mprintf('\n\t  (n)             (X)');
+mprintf('\n=====================================');
+for i=1:m
+    mprintf('\n\t  %.0f  \t \t %.3f',n(i),X(i));
+end
+
+//OUTPUT(Ex 10.2.b)
+mprintf('\n\n\n OUTPUT Ex10.2.b');
+mprintf('\n==========================================');
+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
+//FILE OUTPUT
+fid= mopen('.\Chapter10-Ex2-Output.txt','w');
+mfprintf(fid,'\n OUTPUT Ex10.2.a');
+mfprintf(fid,'\n=====================================');
+mfprintf(fid,'\n \tThe Ammonia Conversion');
+mfprintf(fid,'\n=====================================');
+mfprintf(fid,'\n\t Gauzes        Conversion');
+mfprintf(fid,'\n\t  (n)             (X)');
+mfprintf(fid,'\n=====================================');
+for i=1:m
+    mfprintf(fid,'\n\t  %.0f  \t \t %.3f',n(i),X(i));
+end
+mfprintf(fid,'\n\n\n OUTPUT Ex10.2.b');
+mfprintf(fid,'\n==========================================');
+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);
+
+//====================================================END OF PROGRAM====================================================
+
+
+
+
+
+
+
+
+
+