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

---
 905/CH7/EX7.10/7_10.sce | 67 +++++++++++++++++++++++++++++++++++++++++++++++++
 1 file changed, 67 insertions(+)
 create mode 100755 905/CH7/EX7.10/7_10.sce

(limited to '905/CH7/EX7.10/7_10.sce')

diff --git a/905/CH7/EX7.10/7_10.sce b/905/CH7/EX7.10/7_10.sce
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+clear;
+clc;
+
+// Illustration 7.10
+// Page: 461
+
+printf('Illustration 7.10 -  Page: 461\n\n');
+
+// solution
+//*****Data*****//
+Dd = 1.15*10^-9; // [molecular diffusivity of furfural in water, square m/s]
+Dc = 2.15*10^-9; // [molecular diffusivity of furfural in toluene, square m/s]
+m = 10.15; // [equilibrium distribution coefficient, cubic m raffinate/cubic m extract]
+
+printf('Illustration 7.10(a) -  Page: 461\n\n');
+// Solution(a)
+// From example 7.8 and 7.9
+dvs = 3.26*10^-4; // [m]
+Shd = 6.6; // [sherwood number for dispersed phase]
+// From equation 7.52
+kd = Shd*Dd/dvs; // [dispersed phase mass transfer coefficient, m/s]
+printf("The dispersed-phase mass-transfer coefficient is %e m/s.\n\n",kd);
+
+printf('Illustration 7.10(b) -  Page: 461\n\n');
+// Solution(b)
+
+dd = 998;
+dc = 868; // [density of continuous phase, kg/cubic m]
+uc = 0.59*10^-3; // [viscosity of continuous phase, kg/m.s]
+ohm = 182.2; // [rpm]
+g = 9.8; // [square m/s]
+Di = 0.288; // [m]
+sigma = 0.025; // [N/m]
+phiD = 0.385;
+Dt = 0.863; // [m] 
+Scc = uc/(dc*Dc);
+Rec = Di^2*ohm/60*dc/uc;
+Fr = Di*(ohm/60)^2/g;
+Eo = dd*dvs^2*g/sigma;
+
+// From equation 7.53
+Shc = 1.237*10^-5*Rec^(2/3)*Scc^(1/3)*Fr^(5/12)*Eo^(5/4)*phiD^(-1/2)*(Di/dvs)^2*(dvs/Dt)^(1/2);
+// Therefore 
+kc = Shc*Dc/dvs; // [continuous phase mass transfer coefficient, m/s]
+printf("The continuous-phase mass-transfer coefficient is %e m/s.\n\n",kc);
+
+printf('Illustration 7.10(c) -  Page: 462\n\n');
+// Solution(c)
+
+a = 7065; // [square m/cubic m]
+Vt = 0.504; // []
+Qd = 0.097/60; // [cubic m/s]
+Qc = 0.155/60; // [cubic m/s]
+
+// From equation 7.40
+Kod = kd*kc*m/(m*kc+kd); // [m/s]
+// From equation 7.45
+N_tod = Kod*a*Vt/Qd;
+// From equation 7.46
+Emd = N_tod/(1+N_tod); 
+printf("The Murphree dispersed phase efficiency is %f.\n\n",Emd);
+
+printf('Illustration 7.10(d) -  Page: 462\n\n');
+// Solution(d)
+// From equation 7.57
+fext = Emd/(1+Emd*Qd/(m*Qc));
+printf("The fractional extraction of furfural is %f.\n\n",fext);
\ No newline at end of file
-- 
cgit