From b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b Mon Sep 17 00:00:00 2001
From: priyanka
Date: Wed, 24 Jun 2015 15:03:17 +0530
Subject: initial commit / add all books

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 497/CH16/EX16.4/Chap16_Ex4.sce | 62 ++++++++++++++++++++++++++++++++++++++++++
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+//Kunii D., Levenspiel O., 1991. Fluidization Engineering(II Edition). Butterworth-Heinemann, MA, pp 491
+
+//Chapter-16, Example 4, Page 422
+//Title: Dryer Kinetics and Scale-up
+//==========================================================================================================
+
+clear
+clc
+
+//INPUT
+Qfi=0.20;//Initial moisture fraction
+Qfbar=0.04;//Average final moisture fraction
+rhos=2000;//Density of solid in kg/m^3
+Cps=0.84;//Specific heat of solids in kJ/kg K
+Fo=7.6E-4;//Flow rate of solids in kg/m^3
+Tsi=20;//Inital temperature of solids in degree C
+rhog=1;//Density of gas in kg/m^3
+Cpg=1;//Specific heat of gas in kJ/kg K
+uo=0.3;//Superficial gas velocity in m/s
+Tgi=200;//Initial temperature of gas in degee C
+L=2370;//Enthalpy of liquid in kJ/kg
+Cpl=4.2;//Specific heat of liquid in kJ/kg K
+dt=0.1;//Diameter of reactor in m
+Lm=0.1;//Length of fixed bed in m
+ephsilonm=0.45;//Void fraction of fixed bed
+pi=3.14;
+Fo1=1;//Feed rate for commercial-scale reactor in kg/s
+
+//CALCULATION
+//(a)Bed temperature
+Teguess=50;//Guess value of Te
+function[fn]=solver_func(Te)//Function defined for solving the system
+    fn=(pi/4)*dt^2*uo*rhog*Cpg*(Tgi-Te)-Fo*(Qfi-Qfbar)*[L+Cpl*(Te-Tsi)]-Fo*Cps*(Te-Tsi);
+endfunction
+[Te]=fsolve(Teguess,solver_func,1E-6);//Using inbuilt function fsolve for solving Eqn.(53) for Te
+
+//(b)Drying time for a particle
+xguess=2;//Guess value of x, ie term tou/tbar
+function[fn]=solver_func1(x)//Function defined for solving the system
+    fn=1-(Qfbar/Qfi)-(1-exp(-x))/x;
+endfunction
+[x]=fsolve(xguess,solver_func1,1E-6);//Using inbuilt function fsolve for solving Eqn.(61) for x
+W=(pi/4)*dt^2*Lm*(1-ephsilonm)*rhos;//Weight of soilds in bed
+tbar=W/Fo;//Mean residence time of solids from Eqn.(59)
+tou=tbar*x;//Time for complete drying of a particle
+
+//(c)Commercial-scale dryer
+W1=Fo1*tbar;
+Atguess=5;//Guess value of area
+function[fn]=solver_func3(At)//Function defined for solving the system
+    fn=At*uo*rhog*Cpg*(Tgi-Te)-Fo1*(Qfi-Qfbar)*[L+Cpl*(Te-Tsi)]-Fo1*Cps*(Te-Tsi);
+endfunction
+[At]=fsolve(Atguess,solver_func3,1E-6);//Using inbuilt function fsolve for solving Eqn.(53) for At
+dt1=sqrt(4/pi*At);//Diameter of commercial-scale dryer
+Q1=At*uo*rhog;//Flow rate necessary for the operation
+
+//OUTPUT
+printf('\nBed temperature:%f degree C',Te);
+printf('\nTime for complete drying of particle:%fs',tou);
+printf('\nFlow rate of gas necessary for Commercial-scale dryer:%fkg/s',Q1);
+
+//====================================END OF PROGRAM ======================================================
\ No newline at end of file
-- 
cgit