Table 3:
Proposed model
𝑛
-hexane results.
Iteration
𝑇
𝑓
𝐺
[K]
𝑇
−
[K]
𝑘
−
g
[W/m
⋅
K]
𝑐
−
𝑝
g
[kJ/kg
⋅
K]
𝑇
+
[K]
𝑘
+
g
[W/m
⋅
K]
𝑐
+
𝑝
𝑔
[kJ/kg
⋅
K]
𝐿
𝑒
−
𝐿
𝑒
+
𝑛
𝐴
𝐵
𝑇
𝑓
[K]
𝑟
𝑓
/
𝑟
𝑠
K
[
1
0
3
c
m
2
/
s
]
|
𝑇
𝑓
𝐺
−
𝑇
𝑓
|
[K]
1
2100
1221.0
0.106872
2.6318
1199.0
0.077116
1.1739
2.80
0.82
0.18
0.95
63.43
2349.1
11.79
7.32
249.1
2
2349.1
1345.6
0.114822
3.0807
1323.6
0.085242
1.1968
2.45
0.77
0.17
0.96
68.46
2387.7
10.95
7.83
38.6
3
2387.7
1364.9
0.116093
3.1512
1342.9
0.086586
1.2003
2.41
0.76
0.16
0.96
69.38
2394.6
10.81
7.91
6.9
4
2394.6
1368.3
0.116320
3.1638
1346.3
0.086827
1.2010
2.40
0.76
0.16
0.96
69.54
2395.8
10.79
7.92
1.2
Fixed variables:
𝑇
𝑠
=
𝑇
b
o
i
l
=
3
4
2
K
,
𝑇
∞
=
2
9
8
K
,
𝜌
𝑙
=
6
5
9
kg/
m
3
,
Δ
ℎ
𝑐
=
4
5
0
9
1
kJ/kg,
ℎ
𝑓
𝑔
=
3
5
5
kJ/kg,
𝜐
=
1
5
.
2
,
𝜒
−
𝐹
=
0
.
5
5
,
𝜒
−
𝑂
𝑥
=
0
.
4
5
,
𝑌
−
𝐹
=
0
.
7
9
,
𝑌
−
𝑂
𝑥
=
0
.
2
1
.