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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/CH7/EX7.6.b | |
parent | b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b (diff) | |
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Diffstat (limited to '1040/CH7/EX7.6.b')
-rw-r--r-- | 1040/CH7/EX7.6.b/Chapter7_Ex6_b.sce | 48 | ||||
-rw-r--r-- | 1040/CH7/EX7.6.b/Chapter7_Ex6_b_Output.txt | 3 |
2 files changed, 51 insertions, 0 deletions
diff --git a/1040/CH7/EX7.6.b/Chapter7_Ex6_b.sce b/1040/CH7/EX7.6.b/Chapter7_Ex6_b.sce new file mode 100644 index 000000000..dc1e0f2f9 --- /dev/null +++ b/1040/CH7/EX7.6.b/Chapter7_Ex6_b.sce @@ -0,0 +1,48 @@ +//Harriot P.,2003,Chemical Reactor Design (I-Edition) Marcel Dekker,Inc., USA,pp 436.
+//Chapter-7 Ex7.6.b Pg No.300
+//Title:Power of agitator before and after air is on
+//======================================================================================================================
+clear
+clc
+//INPUT
+Da_by_Dt=(1/3);
+Da=1.333;//(m)
+N=120;//(rpm)
+N_conv=(N/60);//(sec-1)
+Press_top=1;//Pressure at the top of the vessel (atm)
+myu_soln=1.5*(10^(-3));//Viscosity of solution (Pa sec)
+rho=1000;//Density of water (kg/m3)
+ug_sup1=3*(10^(-2));//based on 30(°C) and 1 (atm).
+S=12.6;//Value calculated for cross section area in Ex7.6.b
+
+//CALCULATION
+Re=(rho*N_conv*Da^2)/myu_soln;
+N_p=6;//For a standard turbine
+N_p_pitched=1.7;//For a pitched-blade turbine
+P0=(N_p*rho*(N_conv^3)*(Da^5))*(10^(-3));//Refer equation 7.73 (kW)
+//If the turbine is 2 m from the bottom, or 10 m below the surface,the pressure is about 2 atm since 1atm= 10.3 m water
+Press_bottom=2
+ug_sup2=ug_sup1/Press_bottom;
+Q=ug_sup2*S;
+N_Ae=Q/(N_conv*(Da^3));
+Pg_by_P0=0.55;//From figure 7.15 based on N_Ae value calculated
+Pg=Pg_by_P0*P0;//When aerated
+P0_pitched=(N_p_pitched/N_p)*P0;
+Pg_by_P0_pitched=0.8;//Solution reaching the upper stirrers is already aerated
+Pg_pitched=Pg_by_P0_pitched*P0_pitched;
+Tot_Pow_no_air=P0+Press_bottom*P0_pitched;//Total power when no air is presented
+Tot_Pow_aerated=Pg+Press_bottom*Pg_pitched;//Total power when it is aerated
+
+//OUTPUT
+//ConsoleOutput
+mprintf('\n\tThe total power required for the agitator before the air is turned on: %0.0f kW',Tot_Pow_no_air);
+mprintf('\n\tThe total power required for the agitator after the air is turned on: %0.0f kW',Tot_Pow_aerated);
+//File Output
+fid= mopen('.\Chapter7_Ex6_b_Output.txt','w');
+mfprintf(fid,'\n\tThe total power required for the agitator before the air is turned on: %0.0f kW',Tot_Pow_no_air);
+mfprintf(fid,'\n\tThe total power required for the agitator after the air is turned on: %0.0f kW',Tot_Pow_aerated);
+mclose('all')
+//=========================================================END OF PROGRAM===============================================
+
+
+
diff --git a/1040/CH7/EX7.6.b/Chapter7_Ex6_b_Output.txt b/1040/CH7/EX7.6.b/Chapter7_Ex6_b_Output.txt new file mode 100644 index 000000000..360317b09 --- /dev/null +++ b/1040/CH7/EX7.6.b/Chapter7_Ex6_b_Output.txt @@ -0,0 +1,3 @@ +
+ The total power required for the agitator before the air is turned on: 316 kW
+ The total power required for the agitator after the air is turned on: 203 kW
\ No newline at end of file |