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| author | prashantsinalkar | 2017-10-10 12:27:19 +0530 |
|---|---|---|
| committer | prashantsinalkar | 2017-10-10 12:27:19 +0530 |
| commit | 7f60ea012dd2524dae921a2a35adbf7ef21f2bb6 (patch) | |
| tree | dbb9e3ddb5fc829e7c5c7e6be99b2c4ba356132c /1040/CH7/EX7.5.b | |
| parent | b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b (diff) | |
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initial commit / add all books
Diffstat (limited to '1040/CH7/EX7.5.b')
| -rw-r--r-- | 1040/CH7/EX7.5.b/Chapter7_Ex5_b.sce | 45 | ||||
| -rw-r--r-- | 1040/CH7/EX7.5.b/Chapter7_Ex5_b_Output.txt | 5 |
2 files changed, 50 insertions, 0 deletions
diff --git a/1040/CH7/EX7.5.b/Chapter7_Ex5_b.sce b/1040/CH7/EX7.5.b/Chapter7_Ex5_b.sce new file mode 100644 index 000000000..fe7690a68 --- /dev/null +++ b/1040/CH7/EX7.5.b/Chapter7_Ex5_b.sce @@ -0,0 +1,45 @@ +//Harriot P.,2003,Chemical Reactor Design (I-Edition) Marcel Dekker,Inc., USA,pp 436.
+//Chapter-7 Ex7.5.b Pg No.293
+//Title:Dimensions of the bubble column reactor
+//===========================================================================================================
+clear
+clc
+//INPUT
+F_product_acetic_acid=0.1;// Rate of acetic acid produced (kmol/sec)
+f_CO_reacted=0.8;//80% of CO reacted
+f_CO=0.75;//Fraction of CO in feed
+T_C=180;//Temperature in (°C)
+T_K=T_C+273;//Temperature in (K)
+P_total=20;//Total Pressure (atm)
+R=82.056*(10^-3);//(cm3 atm/ K mol)
+u_g=0.1;//(m/sec)
+Conc_Rh=4*10^(-3);//Concentration of Rohdium(M)
+Conc_CH3I=1;//Concentration of Methyl Iodide(M)
+Epsilon=0.25;//Value calculated from Ex7.5.a
+
+//CALCULATION
+F_feed_CO=F_product_acetic_acid/f_CO_reacted;//Rate of flow of CO (kmol/sec)
+F_total=F_feed_CO/f_CO;
+Q=F_total*R*T_K/(P_total);
+S=Q/u_g;
+D_t=sqrt(4*S/%pi);
+r_test=(158.8*(10^(6))*exp(-8684/T_K)*(Conc_Rh)*(Conc_CH3I))*(10^(-3));//Kinetic rate at 180 (°C)
+liquid_vol= (F_product_acetic_acid/r_test)*(10^(-3));//liquid volume (m3)
+h0=liquid_vol/S;//clear liquid
+h=h0/(1-Epsilon);//aerated liquid
+
+//OUTPUT
+//Console Output
+mprintf('\n\tThe Dimensions of the reactor are ');
+mprintf('\n\tDiameter:%0.0f m',D_t);
+mprintf('\n\tHeight:%0.2f m',h);
+mprintf('\n\t The upper limit value of reactor height is 15 m and diameter is 2 m');
+//File Output
+fid= mopen('.\Chapter7_Ex5_b_Output.txt','w');
+mfprintf(fid,'\n\tThe Dimensions of the reactor are ');
+mfprintf(fid,'\n\tDiameter:%0.0f m',D_t);
+mfprintf(fid,'\n\tHeight:%0.2f m',h);
+mfprintf(fid,'\n\t The upper limit value of reactor height is 15 m and diameter is 2 m');
+mclose(fid);
+//================================================END OF PROGRAM=========================================================
+//Disclaimer: The numerically calculated value of reactor height is 14.34 m not 14.4 m as mentioned in the textbook
diff --git a/1040/CH7/EX7.5.b/Chapter7_Ex5_b_Output.txt b/1040/CH7/EX7.5.b/Chapter7_Ex5_b_Output.txt new file mode 100644 index 000000000..bf37fd4df --- /dev/null +++ b/1040/CH7/EX7.5.b/Chapter7_Ex5_b_Output.txt @@ -0,0 +1,5 @@ +
+ The Dimensions of the reactor are
+ Diameter:2 m
+ Height:14.34 m
+ The upper limit value of reactor height is 15 m and diameter is 2 m
\ No newline at end of file |