TPWS
Thermodynamic
Properties of Water and Steam
by Howard Chao and Stella Unruh
Verification of
Thermodynamic Data
All
of the IAPWS IF-97 equations were verified and checked with the suggested
values provided in the IAPWS
IF-97 release guidelines.
Furthermore, additional values (with various units) were computed and
compared to values from NIST
(all calculated values truncated to 4 digits of precision).
|
T |
P |
V |
U |
H |
S |
CV |
CP |
Phase |
|
K |
MPa |
mL/g |
kJ/mol |
kJ/mol |
J/mol K |
J/mol K |
J/mol K |
--- |
NIST |
300 |
3 |
1.0022 |
2.0234 |
2.0775 |
7.0667 |
74.2350 |
75.1690 |
liquid |
TPWS |
300 |
3 |
1.0022 |
2.0236 |
2.0779 |
7.0675 |
74.2467 |
75.1802 |
liquid |
|
|
|
|
|
|
|
|
|
|
|
T |
P |
V |
U |
H |
S |
CV |
CP |
Phase |
|
C |
bar |
ft3/lbm |
kcal/mol |
kcal/mol |
cal/mol K |
cal/mol K |
cal/mol K |
--- |
NIST |
26.85 |
0.01 |
2216.8000 |
10.3880 |
10.9840 |
39.1980 |
6.0721 |
8.0695 |
vapor |
TPWS |
26.85 |
0.01 |
2216.8287 |
10.3885 |
10.9844 |
39.1995 |
6.0683 |
8.0865 |
vapor |
NIST |
26.85 |
0.51 |
0.0161 |
0.4846 |
0.4849 |
1.6925 |
17.7840 |
18.0010 |
liquid |
TPWS |
26.85 |
0.51 |
0.0161 |
0.4847 |
0.4849 |
1.6927 |
17.7869 |
18.0039 |
liquid |
|
|
|
|
|
|
|
|
|
|
|
T |
P |
V |
U |
H |
S |
CV |
CP |
Phase |
|
F |
atm |
mL/g |
kJ/kg |
kJ/kg |
J/g K |
J/g K |
J/g K |
--- |
NIST |
80.33 |
8 |
1.0031 |
112.4900 |
113.3100 |
0.3929 |
4.1278 |
4.1786 |
liquid |
TPWS |
80.33 |
8 |
1.0031 |
112.5049 |
113.3180 |
0.3929 |
4.1284 |
4.1791 |
liquid |
|
|
|
|
|
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|
|
T |
P |
V |
U |
H |
S |
CV |
CP |
Phase |
|
R |
psia |
m3/mol |
Btu/lbmol |
Btu/lbmol |
Btu/lbmol
R |
Btu/lbmol
R |
Btu/lbmol
R |
--- |
NIST |
600 |
1 |
0.4012 |
19056.0000 |
20246.0000 |
36.1980 |
6.1658 |
8.1858 |
vapor |
TPWS |
600 |
1 |
0.4013 |
19043.2818 |
20232.7018 |
36.1435 |
6.1499 |
8.1665 |
vapor |
NIST |
600 |
10 |
1.8325E-05 |
1952.5000 |
1953.0000 |
3.5891 |
17.1180 |
18.0200 |
liquid |
TPWS |
600 |
10 |
1.8330E-05 |
1951.0064 |
1951.5496 |
3.5834 |
17.0948 |
17.9991 |
liquid |
|
|
|
|
|
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|
|
|
|
|
T |
P |
V |
U |
H |
S |
CV |
CP |
Phase |
|
R |
psia |
ft3/lbm |
Btu/lbm |
Btu/lbm |
Btu/lbm R |
Btu/lbm R |
Btu/lbm R |
--- |
NIST |
1140.2 |
2716.9 |
0.0305 |
743.8700 |
759.1900 |
0.9372 |
0.7900 |
3.6469 |
liquid |
|
|
|
0.1105 |
1010.7000 |
1066.3000 |
1.2065 |
0.9600 |
6.6700 |
vapor |
TPWS |
1140.2 |
2716.9 |
0.0304 |
743.3031 |
758.6086 |
0.9365 |
0.7868 |
3.6126 |
liquid |
|
|
|
0.1107 |
1010.6585 |
1066.2977 |
1.2064 |
0.9153 |
6.0235 |
vapor |
|
|
|
|
|
|
|
|
|
|
|
T |
P |
V |
U |
H |
S |
CV |
CP |
Phase |
|
K |
bar |
ft3/lbmol |
kcal/mol |
kcal/mol |
cal/mol K |
cal/mol K |
cal/mol K |
--- |
NIST |
424.98 |
5 |
0.3153 |
2.7537 |
2.7590 |
8.0103 |
15.1350 |
18.5660 |
liquid |
|
|
|
108.1600 |
11.0260 |
11.8330 |
29.3680 |
7.5753 |
10.3780 |
vapor |
TPWS |
424.98 |
5 |
0.3153 |
2.7541 |
2.7564 |
8.0112 |
15.1487 |
18.5801 |
liquid |
|
|
|
108.1611 |
11.8330 |
11.8330 |
29.3684 |
7.5836 |
10.3891 |
vapor |
As
easily seen from the results, the values generated using tpws.m are
virtually equivalent to values obtained from NIST.
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