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

---
 617/CH9/EX9.10/Example9_10.sci | 27 +++++++++++++++++++++++++++
 1 file changed, 27 insertions(+)
 create mode 100755 617/CH9/EX9.10/Example9_10.sci

(limited to '617/CH9/EX9.10')

diff --git a/617/CH9/EX9.10/Example9_10.sci b/617/CH9/EX9.10/Example9_10.sci
new file mode 100755
index 000000000..7713dbf7b
--- /dev/null
+++ b/617/CH9/EX9.10/Example9_10.sci
@@ -0,0 +1,27 @@
+clc();
+clear;
+
+// To calculate the terminal temperature of oil and water 
+
+To1=160;                               // inlet temperature of oil in degF
+Cpo=0.5;                               // Specific heat capacity in Btu/lb-degf
+Tw1=60;                                // Inlet temperature of water in degF
+mo=1000;                               // Mass flow rate of oil in lb/hr
+mw=2500;                               // Mass flow rate of water in lb/hr
+Cpw=1;                                 // Heat capacity of water in Btu/hr
+X=mo*Cpo/(mw*Cpw);                     // Ratio of flow rates 
+UA=1.15*mo*Cpo;
+B=UA/mo*Cpo;
+
+// from the graph, we can locate the point of A and B And corresponding effectiveness ratio
+E=0.86;                                // Effectiveness ratio
+To2=To1-E*(To1-Tw1);                   // Outlet temperature of oil in degF
+printf("The outlet temperature of oil is %d degF \n",To2);
+
+q=mo*Cpo*(To1-To2);                     // Heat transferred in Btu/hr
+Tw2=Tw1+(q/(mw*Cpw));                   // Outlet temperature of oil in degF
+printf(" The outlet tempearture of water is %.1f degF",Tw2);
+
+
+
+     
\ No newline at end of file
-- 
cgit