Why did they chose 1.40MPA and 1.60MPA and not 1.45MPA and 1.50MPa since it is closer to 0.15436?

Principles of Heat Transfer (Activate Learning with these NEW titles from Engineering!)
8th Edition
ISBN:9781305387102
Author:Kreith, Frank; Manglik, Raj M.
Publisher:Kreith, Frank; Manglik, Raj M.
Chapter6: Forced Convection Over Exterior Surfaces
Section: Chapter Questions
Problem 6.12P
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Why did they chose 1.40MPA and 1.60MPA and not 1.45MPA and 1.50MPa since it is closer to 0.15436?
4G. 46 17:27 O A
0.00
* 36 4
KB/s
Stepl
a)
"Temperature (T)= 250°c
sptei fie volume (v) = 0.15436 m³/rg
P, u, h, s.
Given
find.
Step2
b)
from
steam
P= 1•40 M1a
P = 1.60 MPa
O·14184
2692.3 291g.2 6.6732
O. 16350
2698-3 2927.2 6.7467
use linear faterpolation.
Na - NI P- Pi)
Pa -Pi
V= V+
0.14184 -D.16350
'xLP -1-40)
O.154 36 =
O.163 50 +
1.60 - 1-4o
1.484 MPa
specițic intennal Euvrgy
2692.3 - 2698-3
2698. 3 +
x(t-484 -1-40)
1.60 -1-40
2695• 78 KT/Kg
Enthalpy.
2919.2 -2027-2
2927.2 +
x (1.484 - 1-40)
1.60 - 1-40
29a3. 84 KT/rg
Eutrophy
S= 6.7467 +
6.6732 - 6.7467
1.b0 -l.40
x (1.484 -l140)
6.71 683
VX
Transcribed Image Text:4G. 46 17:27 O A 0.00 * 36 4 KB/s Stepl a) "Temperature (T)= 250°c sptei fie volume (v) = 0.15436 m³/rg P, u, h, s. Given find. Step2 b) from steam P= 1•40 M1a P = 1.60 MPa O·14184 2692.3 291g.2 6.6732 O. 16350 2698-3 2927.2 6.7467 use linear faterpolation. Na - NI P- Pi) Pa -Pi V= V+ 0.14184 -D.16350 'xLP -1-40) O.154 36 = O.163 50 + 1.60 - 1-4o 1.484 MPa specițic intennal Euvrgy 2692.3 - 2698-3 2698. 3 + x(t-484 -1-40) 1.60 -1-40 2695• 78 KT/Kg Enthalpy. 2919.2 -2027-2 2927.2 + x (1.484 - 1-40) 1.60 - 1-40 29a3. 84 KT/rg Eutrophy S= 6.7467 + 6.6732 - 6.7467 1.b0 -l.40 x (1.484 -l140) 6.71 683 VX
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