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

---
 1073/CH3/EX3.25/3_25.sce | 31 +++++++++++++++++++++++++++++++
 1 file changed, 31 insertions(+)
 create mode 100755 1073/CH3/EX3.25/3_25.sce

(limited to '1073/CH3/EX3.25')

diff --git a/1073/CH3/EX3.25/3_25.sce b/1073/CH3/EX3.25/3_25.sce
new file mode 100755
index 000000000..99160a199
--- /dev/null
+++ b/1073/CH3/EX3.25/3_25.sce
@@ -0,0 +1,31 @@
+clc;
+clear;
+//Example 3.25
+mo_dot=60   //Mass flow rate of oilin [g/s]
+mo_dot=6*10^-2  //[kg/s]
+Cpo=2.0     //Specific heat of oil in [kJ/(kg.K)]
+T1=420  //[K]
+T2=320  //[K]
+Q=mo_dot*Cpo*(T1-T2)    //Rate of heat flow in [kJ/s]
+mw_dot=mo_dot   //Mass flow rate of water   //kg/s
+t1=290  //[K]
+Cpw=4.18    //[kJ/(kg.K)]
+//For finding outlet temperature of water
+t2=t1+Q/(mw_dot*Cpw)    //[K]
+dT1=T1-t2   //[K]
+dT2=T2-t1   //[K]
+dTm=(dT1-dT2)/log(dT1/dT2)  //[K]
+ho=1.6  //Oil side heat transfer coefficient in [kW/(sq m.K)]
+hi=3.6  //Water side heat transfer coeff in [kW/(sq m.K)]
+//Overall heat transfer coefficient is:
+U=1/(1/ho+1/hi) //[kW/(m^2.K)]
+
+A=Q/(U*dTm) //[sq m]
+Do=25   //[mm]
+Do=Do/1000  //[m]
+L=A/(%pi*Do)    //Length of tube in [m]
+printf("\nOutlet temperature of water is %f K \n",round(t2));
+printf("Area of heat transfer required is %f sq m\n",A);
+printf("Length of tube required is %f m",L)
+
+
-- 
cgit