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+// Harriot P., 2003, Chemical Reactor Design (I-Edition), Marcel Dekker, Inc., USA, pp 436.
+//Chapter-6 Ex6.4.b Pg No.251
+//Title:Overall conversion for different velocities
+//====================================================================================================================
+clear
+clc
+//INPUT
+u_oa_by_u0=0.88;//Refer equation 3.64
+u_ob_by_u0=1.12;
+X_A=0.95;//Conversion
+L=2.5;//(ft)
+L_a=3;//Length of section a (ft)
+L_b=2;//Length of section b (ft)
+
+//CALCULATION
+k_rho_L_by_u=log(1/(1-X_A));//First Order reaction
+//For Section a
+k_rho_L_by_u_a=k_rho_L_by_u*(L_a/L)*(1/u_oa_by_u0);
+X_A_section_a=(1-exp(-k_rho_L_by_u_a));
+delP_a_by_alpha_u0_pow=L_a*(u_oa_by_u0);//Refer equation 3.64
+
+//For Section b
+k_rho_L_by_u_b=k_rho_L_by_u*(L_b/L)*(1/u_ob_by_u0);//Dimensionless Group based on ideal plug flow for first order reaction
+delP_b_by_alpha_u0_pow=L_b*u_ob_by_u0;
+X_A_section_b=(1-exp(-k_rho_L_by_u_b));
+X_A_avg=(u_oa_by_u0*X_A_section_a+u_ob_by_u0*X_A_section_b)/2;
+Percent_X_A_avg=X_A_avg*100;
+
+//OUTPUT
+//Console Output
+mprintf('\nThe overall conversion for different velocities:%0.1f%% ',Percent_X_A_avg );
+
+//File Output
+fid= mopen('.\Chapter6_Ex4_b_Output.txt','w');
+mfprintf(fid,'\nThe overall conversion for different velocities:%0.1f%% ',Percent_X_A_avg );
+mclose(fid);
+//==================================================END OF PROGRAM======================================================
+
+
+
+