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diff --git a/497/CH14/EX14.5/Chap14_Ex5.sce b/497/CH14/EX14.5/Chap14_Ex5.sce new file mode 100755 index 000000000..74a98ae99 --- /dev/null +++ b/497/CH14/EX14.5/Chap14_Ex5.sce @@ -0,0 +1,52 @@ +//Kunii D., Levenspiel O., 1991. Fluidization Engineering(II Edition). Butterworth-Heinemann, MA, pp 491
+
+//Chapter-14, Example 5, Page 353
+//Title: Elutriation and Attrition of Catalyst
+//==========================================================================================================
+
+clear
+clc
+
+//INPUT
+dpi=[0.17;0.15;0.13;0.11;0.09;0.07;0.05;0.03;0.01];//Mean size of particles in mm
+a=[0;0.95;2.45;5.2;10.1;23.2;35.65;20.0;2.45]*10^-2;//Feed composition Fo(dpi)/Fo
+y=[0;0;0;0;0;0;0.625;10.225;159.25]*10^-6;//Elutriation and cyclone efficiency k(dpi)(1-eta(dpi))
+F=0.01;//Rate at which solids are withdrawn in kg/s
+W=40000;//Weight of bed in kg
+dp1=0.11//Initial size in mm
+dp2=0.085;//Size after shrinking in mm
+dpmin=0.01;//Minimum size in mm
+deldpi=2*10^-2;//Size inerval in mm
+t=20.8;//Time in days
+si=1;
+
+//CALCULATION
+kdash=log((dp1-dpmin)/(dp2-dpmin))/(t*24*3600);//Rate of particle shrinkage from Eqn.(24)
+n=length(dpi);
+m=2;
+Fo=0.05;//Initial value of Fo
+F1(m-1)=0;
+s=0;
+c=0;
+t=1E-6;
+while m<=n
+ R(m)=-kdash*(dpi(m)-dpmin);//Rate of size change
+ x(m)=(a(m)*Fo-W*R(m-1)*F1(m-1)/deldpi)/(F+(W*y(m))-(W*R(m)/deldpi)-3*W*R(m)/dpi(m));//Eqn.(34)
+ F1(m)=x(m)*F;
+ c=c+x(m);
+ m=m+1;
+ if abs(c-1)<t then break
+ end
+ Fo=Fo+0.0001;//Incrementing Fo
+end
+
+//OUTPUT
+mprintf('\nFeed rate with deldpi=%fmm is %fg/hr',deldpi,Fo);
+i=1;
+mprintf('\nBed composition');
+while i<=n
+ printf('\n%f',x(i)*100);
+ i=i+1;
+end
+
+//====================================END OF PROGRAM ======================================================
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