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+clc;
+//Example 25.5
+//page no 373
+printf("Example 25.5 page no 373\n\n");
+//gas(propane) flows through a catalyst tower
+Mw=44.1//molecular weight
+P=4320//pressre at the bottom of the catalyst bed,psf
+R=10.73//gas constant
+T=960//temperature,Rankine
+rho=P*Mw/(R*T*144)//density of propane
+L=50//height of bed,ft
+D=20//diameter of bed,ft
+V=%pi*D^2*L/4//bed volume
+theta=10//contact time,s
+e=0.4//bed porosity
+q=V*e/theta//volumetric flow rate
+v_s=4*q/(%pi*D^2)//superficial velocity
+printf("\n superficial velocity v_s=%f ft/s",v_s);
+v_i=v_s/e//interstitial velocity
+printf("\n interstitial velocity v_i=%f ft/s",v_i);
+rho_s=77.28//ultimate density(spheres )
+rho_b=(1-e)*rho_s//bulk density
+printf("\n bulk density rho_b=%f lb/ft^3",rho_b);
+d_p=0.0833//diameter of particles
+a_p=6/d_p//specific surface area
+printf("\n specific surface area a_p=%f ft^-1",a_p);
+a_b=a_p*(1-e)//bed specific surface
+printf("\n bed specific surface a_b=%f ft^-1",a_b)