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diff --git a/1040/CH3/EX3.1/Chapter3_Ex1.sce b/1040/CH3/EX3.1/Chapter3_Ex1.sce new file mode 100644 index 000000000..fa16b2c9b --- /dev/null +++ b/1040/CH3/EX3.1/Chapter3_Ex1.sce @@ -0,0 +1,27 @@ +//Harriot P.,2003,Chemical Reactor Design (I-Edition) Marcel Dekker,Inc.,USA,pp 436.
+//Chapter-1 Ex3.1 Pg No.84
+//Title:Time to reach desired conversion for bimolecular batch reaction
+//========================================================================================
+clear
+clc
+//INPUT
+C_A0=1;//Assuming 1mol basis for the limiting reactant
+C_B0_old=1.02;//2% Excess of reactant B is supplied
+R_old=C_B0_old/C_A0;//Refer equation 3.7 Pg No.
+X_A=0.995;// Conversion interms of limiting reactant
+t_old=6.5;//Time required for the given conversion (hr)
+C_B0_new=1.05;//5% Excess of reactant B
+R_new=C_B0_new/C_A0;//Refer equation 3.7 Pg No.83
+
+//CALCULATION
+k=(log((R_old-X_A)/(R_old*(1-X_A)))/((R_old-1)*t_old *C_A0));
+t_new=log((R_new-X_A)/(R_new*(1-X_A)))/((R_new-1)*k*C_A0);
+
+//OUTPUT
+mprintf('\nTime required to achieve required conversion for 5%% excess of B= %f hr',t_new);
+
+//FILE OUTPUT
+fid=mopen('.\Chapter3-Ex1-Output.txt','w');
+mfprintf(fid,'\nTime required to achieve required conversion for 5%% excess of B= %f hr',t_new);
+mclose(fid);
+//=================================================END OF PROGRAM==================================
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