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Diffstat (limited to '1073/CH3/EX3.25')
-rwxr-xr-x | 1073/CH3/EX3.25/3_25.sce | 31 |
1 files changed, 31 insertions, 0 deletions
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)
+
+
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