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| author | prashantsinalkar | 2017-10-10 12:27:19 +0530 |
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| committer | prashantsinalkar | 2017-10-10 12:27:19 +0530 |
| commit | 7f60ea012dd2524dae921a2a35adbf7ef21f2bb6 (patch) | |
| tree | dbb9e3ddb5fc829e7c5c7e6be99b2c4ba356132c /1040/CH3/EX3.4 | |
| parent | b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b (diff) | |
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initial commit / add all books
Diffstat (limited to '1040/CH3/EX3.4')
| -rw-r--r-- | 1040/CH3/EX3.4/Chapter3_Ex4.sce | 33 |
1 files changed, 33 insertions, 0 deletions
diff --git a/1040/CH3/EX3.4/Chapter3_Ex4.sce b/1040/CH3/EX3.4/Chapter3_Ex4.sce new file mode 100644 index 000000000..a4028847d --- /dev/null +++ b/1040/CH3/EX3.4/Chapter3_Ex4.sce @@ -0,0 +1,33 @@ +//Harriot P.,2003,Chemical Reactor Design (I-Edition) Marcel Dekker,Inc.,USA,pp 436.
+//Chapter-3 Ex3.4 Pg No. 101
+//Title:Volume of reactor for Gas Phase isothermal reaction
+//==================================================================================================================
+clear
+clc
+//INPUT
+//First Order Reaction
+//Basis: 1mol of feed
+k=0.45;//Rate constant of first order reaction(s-1)
+v0=120;//Volumetric flow rate(cm3/s)
+C_A0=0.8;//Initial amount of reactant A (mol)
+X_A=0.95;//Conversion in terms of reactant A
+C_inert=0.2;//Concentration of inert (Nitrogen)in feed
+
+//CALCULATION
+E_A=((2*C_A0+C_inert)-(C_A0+C_inert))/(C_A0+C_inert);//Volume fraction
+Tot_mol=(C_A0+C_inert)+(E_A);//Total No. of moles
+V=v0*((-(E_A)*X_A)+Tot_mol*(log(1/(1-X_A))))/(k);//Refer Performance Equation equation 3.44 and 3.42 in Pg No. 100
+V_l=V*10^-3;//Volume of reactor in liters
+
+//OUTPUT
+mprintf('\n\tThe Volume of the reactor required for the given conversion is %.0f cm3 or %0.2f liters',V,V_l);
+
+//FILE OUTPUT
+fid= mopen('.\Chapter3-Ex4-Output.txt','w');
+mfprintf(fid,'\n\tThe Volume of the reactor required for the given conversion is %.0f cm3 or %0.2f liters',V,V_l);
+mclose(fid);
+//==============================================================END OF PROGRAM==========================================
+
+
+
+
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