From 7f60ea012dd2524dae921a2a35adbf7ef21f2bb6 Mon Sep 17 00:00:00 2001
From: prashantsinalkar
Date: Tue, 10 Oct 2017 12:27:19 +0530
Subject: initial commit / add all books

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 1040/CH3/EX3.6/Chapter3_Ex6.sce | 36 ++++++++++++++++++++++++++++++++++++
 1 file changed, 36 insertions(+)
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(limited to '1040/CH3/EX3.6/Chapter3_Ex6.sce')

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+//Harriot P.,2003,Chemical Reactor Design (I-Edition) Marcel Dekker,Inc.,USA,pp 436.
+//Chapter-3 Ex3.6 Pg No. 114 
+//Title: Optimum reaction temperature 
+//===========================================================================================================
+clear
+clc
+//INPUT
+del_H=-20*10^3;//Heat of reaction(cal)
+T_eq=[500 700];//Equivalent temperatures (K)
+R=1.987;//Gas Constant (cal/mol K)
+E2_by_E1=2;//Ratio of activation energy
+
+//CALCULATION
+T_opt(1)=T_eq(1)/(1+(log(E2_by_E1)*(R/(-del_H)))*T_eq(1));//Refer equation 3.63 Pg No. 113 
+T_opt(2)=T_eq(2)/(1+(log(E2_by_E1)*(R/(-del_H)))*T_eq(2));
+delta_T(1)=T_eq(1)-T_opt(1);
+delta_T(2)=T_eq(2)-T_opt(2);
+
+
+//OUTPUT
+mprintf('\n  \t   \t Temperature_1\t Temperature_2  ');
+mprintf('\n  \t   \t==================================');
+mprintf('\n(T_eq - T_opt)(K):  \t%0.0f     \t\t%0.0f',delta_T(1),delta_T(2));
+mprintf('\n   T_opt(K):\t \t%0.0f\t\t%0.0f', T_opt(1),T_opt(2));
+
+fid= mopen('.\Chapter3-Ex6-Output.txt','w');
+mfprintf(fid,'\n  \t   \t Temperature_1\t Temperature_2  ');
+mfprintf(fid,'\n  \t   \t==================================');
+mfprintf(fid,'\n(T_eq - T_opt)(K):  \t%0.0f     \t\t%0.0f',delta_T(1),delta_T(2));
+mfprintf(fid,'\n   T_opt(K):\t \t%0.0f\t\t%0.0f', T_opt(1),T_opt(2));
+mclose(fid);
+
+//=========================================================END OF PROGRAM=====================================
+//Disclaimer:There is an arithmetic error in  the optimum temperatures obtained in the textbook.  
+// Based on the values (T_eq - T_opt)1=17 and  (T_eq - T_opt)2=32 the optimum temperatures obtained are 
+// T_opt1=483 K and T_opt2=668 K respectively.
-- 
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