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

---
 2510/CH22/EX22.24/Ex22_24.sce | 46 +++++++++++++++++++++++++++++++++++++++++++
 1 file changed, 46 insertions(+)
 create mode 100755 2510/CH22/EX22.24/Ex22_24.sce

(limited to '2510/CH22/EX22.24')

diff --git a/2510/CH22/EX22.24/Ex22_24.sce b/2510/CH22/EX22.24/Ex22_24.sce
new file mode 100755
index 000000000..365c0072e
--- /dev/null
+++ b/2510/CH22/EX22.24/Ex22_24.sce
@@ -0,0 +1,46 @@
+//Variable declaration:
+m1 = 62000                      //Mass flowrate of alcohol (lb/h)
+h1 = 365                        //Enthalpy of vapour (Btu/lb)
+cp = 1                          //Heat capacity of water (Btu/lb. F)
+T1 = 85                         //Entering temperature of water ( F)
+T2 = 120                        //Exit temperature of water ( F)
+a1 = 2.11                       //Flow area for the shell side (ft^2)
+N = 700                         //Total number of tubes
+a2 = 0.546                      //Flow area per tube (in^2/tube)
+n = 4                           //Number of tube passes
+p = 62.5                        //Density of water (lb/ft^3)
+L = 16                          //Length of condenser (ft)
+hio = 862.4                     //Cooling water inside film coefficient (Btu/h.ft^2. F)
+g = 9.8                         //Gravitational accleration (m^2/s)
+Rf = 0.003                      //Fouling factor (Btu/h.ft^2. F)
+
+//Calculation:
+Q1 = m1*h1                      //Heat loss from alcohol (Btu/h)
+Q2 = Q1                         //Heat gained by water (Btu/h)
+DT = T2-T1                      //Temperature difference ( F)
+m2 = Q2/(cp*DT)                 //Water mass flow rate (lb/h)
+LMTD = ((T2-32)-(T1-32))/log((T2-32)/(T1-32))   //Log mean temperature difference ( F)
+at = (N*a2)/(144*n)             //Total flow area for tube side (ft^2)
+G1 = m1/a1                      //Mass velocity of flow in shell side (lb/h.ft^2)
+G2 = m2/at                      //Mass velocity of flow in tube side (lb/h.ft^2)
+V = G2/(3600*p)                 //Velocity of water (ft/s)
+G3 = m1/(L*N)**(2/3)            //Loading G (lb/h.ft)
+//For alcohol:
+kf = 0.105                      //Thermal conductivity (Btu/h.ft. F)
+muf = 0.55*2.42                 //Dynamic viscosity (lb/ft.h)
+sf = 0.79                       //
+pf = sf*p                       //Density (lb/ft^3)
+h = 151*(((kf**3)*(pf**2)*g*muf)/((muf**2)*n*G3))**(1/3)   //Heat transfer coefficient for the shell side (Btu/h.ft^2. F)
+ho = h                          //Outside heat transfer coefficient of the tube bundle (Btu/h.ft^2. F)
+Uc = (hio*ho)/(hio+ho)          //Overall heat transfer coefficient for a new (clean) heat exchanger (Btu/h.ft^2. F)
+A = N*L*0.2618                  //Area for heat transfer (ft^2)
+Ud = Q1/(A*DT)                  //Design (D) overall heat transfer coefficient (Btu/h.ft^2. F)
+Rd = (Uc-Ud)/(Uc*Ud)            //Dirt (d) factor (Btu/h.ft^2. F)
+
+//Result:
+printf("The dirt (d) factor is : %.4f Btu/h.ft^2. F .",Rd)
+if (Rd>Rd) then
+    printf("Therefore, the exchanger as specified is unsuitable for these process conditions since the fouling factor is above the recommended value. Cleaning is recommended.")
+else
+    printf("Therefore, the exchanger as specified is suitable for these process conditions since the fouling factor is below the recommended value. Cleaning is not recommended.")
+end
-- 
cgit