Thermodynamics Table
-
Upload
zenin-easa -
Category
Documents
-
view
228 -
download
0
Transcript of Thermodynamics Table
-
7/24/2019 Thermodynamics Table
1/82
A P P E N D I X
ASI Units:Single-StateProperties
TABLE A.1
C onversion Factors
Area (A)1 mm2 = 1.0 106 m2 1 f t2 = 144 in.2
1 cm2 = 1.0 104 m2 = 0.1550 in.2 1 in.2 = 6.4516 cm2 = 6.4516 104 m2
1 m2 = 10.7639 ft2 1 f t2 = 0.092 903 m2
C onductivity (k)1 W /m-K = 1 J /s-m-K
= 0.577 789 B tu/h-ft-R 1 B tu/h-ft-R = 1.730 735 W /m-K
Density ()1 kg/m3 = 0.06242797 lbm/ft3 1 lbm/ft3 = 16.018 46 kg/m3
1 g/cm3 = 1000 kg/m3
1 g/cm3 = 1 kg/L
E nergy (E , U )1 J = 1 N-m = 1 kg-m2/s2
1 J = 0.737 562 lbf-ft l lbf-ft = 1.355 818 J
1 cal (Int.) = 4.18681 J = 1.28507 103B tu
1 B tu (Int.) = 1.055 056 kJ
1 erg = 1.0 107 J = 778.1693 lbf-f t
1 eV = 1.602 177 33 1019 J
Force (F )1 N = 0.224809 lbf 1 lbf = 4.448 222 N
1 kp = 9.80665 N (1 kgf)
G ravitationg = 9.80665 m/s2 g = 32.17405 f t/s2
H eat capacity (C p , C v, C ), specific entropy (s)1 kJ/kg-K = 0.238 846 Btu/lbm-R 1 B tu/lbm-R = 4.1868 kJ /kg-K
Heat flux (per unit area)1 W/m2 = 0.316 998 B tu/h-ft2 1 B tu/h-ft2 = 3.15459 W /m2
755
-
7/24/2019 Thermodynamics Table
2/82
756 APPENDIX A SI UNITS: SINGLE-STATE PROPERTIES
TABLE A.1 (continued)C onversion Factors
H eat-transfer coefficient (h)1 W/m2-K = 0.176 11 B tu/h-ft2-R 1 B tu/h-ft2-R = 5.67826 W /m2-K
L ength (L )1 mm = 0.001 m = 0.1 cm 1 ft = 12 in.
1 cm = 0.01 m = 10 mm = 0.3970 in. 1 in. = 2.54 cm = 0.0254 m
1 m = 3.28084 ft = 39.370 in. 1 ft = 0.3048 m
1 km = 0.621 371 mi 1 mi = 1.609344 km
1 mi = 1609.3 m (U S statute) 1 yd = 0.9144 m
M ass (m)
1 kg = 2.204 623 lbm 1 lbm = 0.453 592 kg1 tonne = 1000 kg 1 slug = 14.5939 kg
1 grain = 6.47989 105 kg 1 ton = 2000 lbm
M oment (torque, T)1 N-m = 0.737 562 lbf-ft 1 lbf-ft = 1.355 818 N -m
M omentum (mV)1 kg-m/s = 7.232 94 lbm-ft/s 1 lbm-ft/s = 0.138 256 kg-m/s
= 0.224809 lbf-s
Power ( Q , W)1 W = 1 J/s = 1 N -m/s 1 lbf-ft/s =1.355 818 W
=
0.737 562 lbf -ft/s =
4.626 24 Btu/hIkW = 3412.14 B tu/h 1 B tu/s = 1.055 056 kW
1 hp (metric) = 0.735 499 kW 1 hp (U K ) = 0.7457 kW
= 550 lbf-ft/s
= 2544.43 Btu/h
1 ton of 1 ton of
refrigeration = 3.516 85 kW refrigeration = 12 000 Btu/h
Pressure (P)1 P a = 1 N/m2 = 1 kg/m-s2 1 lbf/in.2 = 6.894 757 kPa
1 bar = 1.0 105Pa = 100 kPa
1 arm = 101.325 kPa 1 atm = 14.695 94 lbf/i n.2
= 1.01325 bar = 29.921 in. Hg [32F ]
= 760 mm Hg [0C ] = 33.899 5 ft H 2O [4C ]
= 10.332 56 m H 2O [4C ]1 torr = 1 mm Hg [0C ]
1 mm Hg [0C ] = 0.133 322 kPa 1 in. H g [0C ] = 0.49115 lbf/i n.2
1 m H 2O [4C ] = 9.806 38 kPa 1 in. H 2O [4
C ] = 0.036126 lbf/in.2
Specific energy (e, u)1 kJ/kg = 0.42992 B tu/lbm 1 B tu/lbm = 2.326 kJ /kg
= 334.55 lbf-ft/lbm 1 lbf-ft/lbm = 2.98907 103 kJ/kg
= 1.28507 103 Btu/lbm
-
7/24/2019 Thermodynamics Table
3/82
APPENDIX A SI UNITS: SINGLE-STATE PROPERTIES 757
TABLE A.1 (continued)C onversion Factors
Specific kinetic energy (12V
2)1 m2/s2 = 0.001 kJ /kg 1 ft2/s2 = 3.9941 105 Btu/lbm
1 kJ/kg = 1000 m2/s2 1 B tu/lbm = 25037 ft2/s2
Specific potential energy (Zg)1 m-gstd = 9.80665 10
3 kJ /kg l ft-gstd = 1.0 lbf-ft/lbm
= 4.21607 103Btu/lbm = 0.001285 Btu/lbm
= 0.002989 kJ /kg
Specific volume (v)1 cm3/g = 0.001 m3/kg
1 cm3/g = 1 L/kg1 m3/kg = 16.01846 ft3/lbm 1 ft3/lbm = 0.062 428 m3/kg
Temperature (T)1 K = 1C = 1.8 R = 1.8 F 1 R = (5/9) K
T C =T K 273.15 T F =T R 459.67
= (T F 32)/1.8 = 1.8 TC + 32
T K =T R /1.8 T R = 1.8 TK
Universal G as C onstantR = N 0k= 8.31451 kJ /kmol-K R = 1.98589 B tu/lbmol-R
= 1.98589 kcal/kmol- K = 1545.36 lbf-f t/lbmol-R
= 82.0578 atm-L /kmol-K = 0.73024 atm-ft3/lbmol-R
=
10.7317 (lbf/i n.
2
)-ft
3
/lbmol-R
Velcoity (V)1 m/s = 3.6 km/h 1 ft/s = 0.681818 mi/h
= 3.28084 ft/s = 0.3048 m/s
= 2.23694 mi/h = 1.09728 km/h
1 km/h = 0.27778 m/s 1 mi/h = 1.46667 ft/s
= 0.91134 ft/s = 0.44704 m/s
= 0.62137 mi/h = 1.609344 km/h
Volume(V)1 m3 = 35.3147 ft3 1 f t3 = 2.831 685 102 m3
1 L = 1 dm3 = 0.001 m3 1 in.3 = 1.6387 105 m3
1 Gal (US) = 3.785 412 L 1 G al (U K ) = 4.546 090 L
= 3.785 412 103 m3 1 Gal (US) = 231.00 in.3
-
7/24/2019 Thermodynamics Table
4/82
758 APPENDIX A SI UNITS: SINGLE-STATE PROPERTIES
TABLE A.2
Critical Constants
M olec. Temp. Press. Vol.Substance Formula M ass (K ) (M Pa) (m3/kg)
A mmonia N H 3 17.031 405.5 11.35 0.00426
A rgon A r 39.948 150.8 4.87 0.00188
B romine B r2 159.808 588 10.30 0.000796
C arbon dioxide C O 2 44.01 304.1 7.38 0.00212
C arbon monoxide C O 28.01 132.9 3.50 0.00333
C hlorine C 12 70.906 416.9 7.98 0.00175
F luorine F 2 37.997 144.3 5.22 0.00174
H elium H e 4.003 5.19 0.227 0.0143H ydrogen (normal) H 2 2.016 33.2 1.30 0.0323
K rypton K r 83.80 209.4 5.50 0.00109
N eon N e 20.183 44.4 2.76 0.00206
N itric oxide N O 30.006 180 6.48 0.00192
N itrogen N 2 28.013 126.2 3.39 0.0032
N itrogen dioxide N O 2 46.006 431 10.1 0.00365
N itrous oxide N 2O 44.013 309.6 7.24 0.00221
Oxygen O 2 31.999 154.6 5.04 0.00229
Sulfur dioxide SO 2 64.063 430.8 7.88 0.00191
Water H 2O 18.015 647.3 22.12 0.00317
X enon X e 131.30 289.7 5.84 0.000902
A cetylene C 2H 2 26.038 308.3 6.14 0.00433B enzene C 6H 6 78.114 562.2 4.89 0.00332
n-B utane C 4H 10 58.124 425.2 3.80 0.00439
Chlorodifluoroethane (142b) CH 3CClF 2 100.495 410.3 4.25 0.00230
Chlorodifluoromethane (22) CHC lF 2 86.469 369.3 4.97 0.00191
Dichlorofluoroethane (141) CH 3C C l2F 116.95 481.5 4.54 0.00215
Dichlorotrifluoroethane (123) CH Cl 2C F 3 152.93 456.9 3.66 0.00182
D ifluoroethane (152a) C H F2C H 3 66.05 386.4 4.52 0.00272
D ifluoromethane (32) C F2H 2 52.024 351.3 5.78 0.00236
E thane C 2H 6 30.070 305.4 4.88 0.00493
E thyl alcohol C 2H 5OH 46.069 513.9 6.14 0.00363
E thylene C 2H 4 28.054 282.4 5.04 0.00465
n-H eptane C 7H 16 100.205 540.3 2.74 0.00431n-H exane C 6H 14 86.178 507.5 3.01 0.00429
M ethane C H 4 16.043 190.4 4.60 0.00615
M ethyl alcohol C H 3OH 32.042 512.6 8.09 0.00368
n-Octane C 8H 18 114.232 568.8 2.49 0.00431
Pentafluoroethane (125) C H F2C F 3 120.022 339.2 3.62 0.00176
n-Pentane C 5H 12 72.151 469.7 3.37 0.00421
Propane C 3H 8 44.094 369.8 4.25 0.00454
Propene C 3H 6 42.081 364.9 4.60 0.00430
R efrigerant mixture R -410a 72.585 344.5 4.90 0.00218
Tetrafluoroethane (134a) C F 3C H 2F 102.03 374.2 4.06 0.00197
-
7/24/2019 Thermodynamics Table
5/82
APPENDIX A SI UNITS: SINGLE-STATE PROPERTIES 759
TABLE A.3
Properties of Selected Solids at 25C
C pSubstance (kg/m3) (kJ /kg-K )
A sphalt 2120 0.92
B rick, common 1800 0.84
C arbon, diamond 3250 0.51
Carbon, graphite 20002500 0.61
C oal 1200 1500 1.26
C oncrete 2200 0.88
G lass, plate 2500 0.80
G lass, wool 20 0.66G ranite 2750 0.89
Ice (0C ) 917 2.04
Paper 700 1.2
Plexiglass 1180 1.44
Polystyrene 920 2.3
Polyvinyl chl ori de 1380 0.96
R ubber, soft 1100 1.67
Sand, dry 1500 0.8
Salt, rock 2100 2500 0.92
Silicon 2330 0.70
Snow,firm 560 2.1
Wood, hard (oak) 720 1.26
Wood, soft (pine) 510 1.38
Wool 100 1.72
M etals
A luminum 2700 0.90
B rass, 60 40 8400 0.38
C opper, commerci al 8300 0.42
G old 19300 0.13
Iron, cast 7272 0.42
I ron, 304 St Steel 7820 0.46
L ead 11340 0.13
M agnesi um, 2% M n 1778 1.00
N ickel, 10% C r 8666 0.44
Silver, 99.9% A g 10524 0.24
Sodium 971 1.21
Tin 7304 0.22
Tungsten 19300 0.13
Zinc 7144 0.39
TABLE A.4
Properties of Some L iquids at 25C
CpSubstance (kg/m3) (kJ /kg-K )
A mmonia 604 4.84
B enzene 879 1.72
B utane 556 2.47
C C l4 1584 0.83
C O 2 680 2.9
E thanol 783 2.46
G asoline 750 2.08
G lycerine 1260 2.42K erosene 815 2.0
M ethanol 787 2.55
n-Octane 692 2.23
Oil engine 885 1.9
Oil light 910 1.8
Propane 510 2.54
R -12 1310 0.97
R -22 1190 1.26
R -32 961 1.94
R -125 1191 1.41
R -134a 1206 1.43
R -410a 1059 1.69
Water 997 4.18
L iquid metals
B ismuth, B i 10040 0.14
L ead, Pb 10660 0.16
M ercury, H g 13580 0.14
N aK (56/44) 887 1.13
Potassium, K 828 0.81
Sodium, N a 929 1.38
Tin, Sn 6950 0.24
Zinc, Zn 6570 0.50
OrTmeltif higher.
-
7/24/2019 Thermodynamics Table
6/82
760 APPENDIX A SI UNITS: SINGLE-STATE PROPERTIES
TABLE A.5
Properties of Various I deal Gases at 25C , 100 kPa (SI Units)
C hemical M olecular R C p0 C v0
G as Formula M ass (kg/kmol) (kJ /kg-K ) (kg/m3) (kJ /kg-K ) (kJ /kg-K ) k=C p
C v
Steam H 2O 18.015 0.4615 0.0231 1.872 1.410 1.327
A cetylene C 2H 2 26.038 0.3193 1.05 1.699 1.380 1.231
A ir 28.97 0.287 1.169 1.004 0.717 1.400
A mmonia N H 3 17.031 0.4882 0.694 2.130 1.642 1.297
A rgon A r 39.948 0.2081 1.613 0.520 0.312 1.667
B utane C 4H 10 58.124 0.1430 2.407 1.716 1.573 1.091
C arbon di oxi de C O 2 44.01 0.1889 1.775 0.842 0.653 1.289
C arbon monoxide C O 28.01 0.2968 1.13 1.041 0.744 1.399
E thane C 2H 6 30.07 0.2765 1.222 1.766 1.490 1.186
E thanol C 2H 5OH 46.069 0.1805 1.883 1.427 1.246 1.145
E thylene C 2H 4 28.054 0.2964 1.138 1.548 1.252 1.237
H elium H e 4.003 2.0771 0.1615 5.193 3.116 1.667
H ydrogen H 2 2.016 4.1243 0.0813 14.209 10.085 1.409
M ethane C H 4 16.043 0.5183 0.648 2.254 1.736 1.299
M ethanol C H 3OH 32.042 0.2595 1.31 1.405 1.146 1.227
N eon N e 20.183 0.4120 0.814 1.03 0.618 1.667
N itric oxide N O 30.006 0.2771 1.21 0.993 0.716 1.387
N itrogen N 2 28.013 0.2968 1.13 1.042 0.745 1.400
N itrous oxide N 2O 44.013 0.1889 1.775 0.879 0.690 1.274n-Octane C 8H 18 114.23 0.07279 0.092 1.711 1.638 1.044
Oxygen O 2 31.999 0.2598 1.292 0.922 0.662 1.393
Propane C 3H 8 44.094 0.1886 1.808 1.679 1.490 1.126
R -12 C C l2F 2 120.914 0.06876 4.98 0.616 0.547 1.126
R -22 C H C lF 2 86.469 0.09616 3.54 0.658 0.562 1.171
R -32 C F 2H 2 52.024 0.1598 2.125 0.822 0.662 1.242
R -125 C H F 2C F 3 120.022 0.06927 4.918 0.791 0.722 1.097
R -134a C F 3C H 2F 102.03 0.08149 4.20 0.852 0.771 1.106
Sul fur di oxide SO 2 64.059 0.1298 2.618 0.624 0.494 1.263
Sul fur tri oxi de S O3 80.053 0.10386 3.272 0.635 0.531 1.196
Or saturation pressure if it is less than 100 kPa.
-
7/24/2019 Thermodynamics Table
7/82
APPENDIX A SI UNITS: SINGLE-STATE PROPERTIES 761
TABLE A.6
C onstant-Pressure Specific H eats of Various I deal Gases
C 0=C 0 + C 1 + C 22+ C 3
3 (kJ/kg K) = T(K elvin)/1000
G as Formula C 0 C 1 C 2 C 3
Steam H 2O 1.79 0.107 0.586 0.20
A cetylene C 2H 2 1.03 2.91 1.92 0.54
A ir 1.05 0.365 0.85 0.39
A mmonia N H 3 1.60 1.4 1.0 0.7
A rgon A r 0.52 0 0 0
B utane C 4H 10 0.163 5.70 1.906 0.049
C arbon dioxide C O2 0.45 1.67 1.27 0.39
C arbon monoxide C O 1.10 0.46 1.0 0.454
E thane C 2H 6 0.18 5.92 2.31 0.29
E thanol C 2H 5OH 0.2 4.65 1.82 0.03
E thylene C 2H 4 0.136 5.58 3.0 0.63
H elium H e 5.193 0 0 0
H ydrogen H 2 13.46 4.6 6.85 3.79
M ethane C H 4 1.2 3.25 0.75 0.71
M ethanol C H 3OH 0.66 2.21 0.81 0.89
N eon N e 1.03 0 0 0
N itric oxide N O 0.98 0.031 0.325 0.14
N itrogen N 2 1.11 0.48 0.96 0.42
N itrous oxide N 2O 0.49 1.65 1.31 0.42n-Octane C 8H 18 0.053 6.75 3.67 0.775
Oxygen O 2 0.88 0.0001 0.54 0.33
Propane C 3H 8 0.096 6.95 3.6 0.73
R-12 C C l2F 2 0.26 1.47 1.25 0.36
R-22 C H C l F2 0.2 1.87 1.35 0.35
R-32 C F 2H 2 0.227 2.27 0.93 0.041
R-125 C H F 2C F 3 0.305 1.68 0.284 0
R-134a C F 3C H 2F 0.165 2.81 2.23 1.11
Sulfur dioxide SO 2 0.37 1.05 0.77 0.21
Sulfur trioxide SO 3 0.24 1.7 1.5 0.46
A pproximate forms vali d from 250 K to 1200 K .Formula limi ted to maximum 500 K .
-
7/24/2019 Thermodynamics Table
8/82
762 APPENDIX A SI UNITS: SINGLE-STATE PROPERTIES
TABLE A7.1
I deal-Gas Properties of A ir, Standard E ntropy at 0.1-M Pa (1-Bar) Pressure
T u h s0T T u h s0T
(K ) (kJ /kg) (kJ /kg) (kJ /kg-K ) (K ) (kJ /kg) (kJ /kg) (kJ /kg-K )
200 142.77 200.17 6.46260 1100 845.45 1161.18 8.24449
220 157.07 220.22 6.55812 1150 889.21 1219.30 8.29616
240 171.38 240.27 6.64535 1200 933.37 1277.81 8.34596
260 185.70 260.32 6.72562 1250 977.89 1336.68 8.39402
280 200.02 280.39 6.79998 1300 1022.75 1395.89 8.44046
290 207.19 290.43 6.83521 1350 1067.94 1455.43 8.48539
298.15 213.04 298.62 6.86305 1400 1113.43 1515.27 8.52891
300 214.36 300.47 6.86926 1450 1159.20 1575.40 8.57111320 228.73 320.58 6.93413 1500 1205.25 1635.80 8.61208
340 243.11 340.70 6.99515 1550 1251.55 1696.45 8.65185
360 257.53 360.86 7.05276 1600 1298.08 1757.33 8.69051
380 271.99 381.06 7.10735 1650 1344.83 1818.44 8.72811
400 286.49 401.30 7.15926 1700 1391.80 1879.76 8.76472
420 301.04 421.59 7.20875 1750 1438.97 1941.28 8.80039
440 315.64 441.93 7.25607 1800 1486.33 2002.99 8.83516
460 330.31 462.34 7.30142 1850 1533.87 2064.88 8.86908
480 345.04 482.81 7.34499 1900 1581.59 2126.95 8.90219
500 359.84 503.36 7.38692 1950 1629.47 2189.19 8.93452
520 374.73 523.98 7.42736 2000 1677.52 2251.58 8.96611
540 389.69 544.69 7.46642 2050 1725.71 2314.13 8.99699
560 404.74 565.47 7.50422 2100 1774.06 2376.82 9.02721
580 419.87 586.35 7.54084 2150 1822.54 2439.66 9.05678
600 435.10 607.32 7.57638 2200 1871.16 2502.63 9.08573
620 450.42 628.38 7.61090 2250 1919.91 2565.73 9.11409
640 465.83 649.53 7.64448 2300 1968.79 2628.96 9.14189
660 481.34 670.78 7.67717 2350 2017.79 2692.31 9.16913
680 496.94 692.12 7.70903 2400 2066.91 2755.78 9.19586
700 512.64 713.56 7.74010 2450 2116.14 2819.37 9.22208
720 528.44 735.10 7.77044 2500 2165.48 2883.06 9.24781
740 544.33 756.73 7.80008 2550 2214.93 2946.86 9.27308
760 560.32 778.46 7.82905 2600 2264.48 3010.76 9.29790780 576.40 800.28 7.85740 2650 2314.13 3074.77 9.32228
800 592.58 822.20 7.88514 2700 2363.88 3138.87 9.34625
850 633.42 877.40 7.95207 2750 2413.73 3203.06 9.36980
900 674.82 933.15 8.01581 2800 2463.66 3267.35 9.39297
950 716.76 989.44 8.07667 2850 2513.69 3331.73 9.41576
1000 759.19 1046.22 8.13493 2900 2563.80 3396.19 9.43818
1050 802.10 1103.48 8.19081 2950 2613.99 3460.73 9.46025
1100 845.45 1161.18 8.24449 3000 2664.27 3525.36 9.48198
-
7/24/2019 Thermodynamics Table
9/82
APPENDIX A SI UNITS: SINGLE-STATE PROPERTIES 763
TABLE A7.2
T he I sentropic R elative Pressure and Relative Volume F unctions
T[K ] P r vr T[K ] P r vr T[K ] Pr vr
200 0.2703 493.47 700 23.160 20.155 1900 1327.5 0.95445
220 0.3770 389.15 720 25.742 18.652 1950 1485.8 0.87521
240 0.5109 313.27 740 28.542 17.289 2000 1658.6 0.80410
260 0.6757 256.58 760 31.573 16.052 2050 1847.1 0.74012
280 0.8756 213.26 780 34.851 14.925 2100 2052.1 0.68242
290 0.9899 195.36 800 38.388 13.897 2150 2274.8 0.63027
298.15 1.0907 182.29 850 48.468 11.695 2200 2516.2 0.58305
300 1.1146 179.49 900 60.520 9.9169 2250 2777.5 0.54020
320 1.3972 152.73 950 74.815 8.4677 2300 3059.9 0.50124340 1.7281 131.20 1000 91.651 7.2760 2350 3364.6 0.46576
360 2.1123 113.65 1050 111.35 6.2885 2400 3693.0 0.43338
380 2.5548 99.188 1100 134.25 5.4641 2450 4046.2 0.40378
400 3.0612 87.137 1150 160.73 4.7714 2500 4425.8 0.37669
420 3.6373 77.003 1200 191.17 4.1859 2550 4833.0 0.35185
440 4.2892 68.409 1250 226.02 3.6880 2600 5269.5 0.32903
460 5.0233 61.066 1300 265.72 3.2626 2650 5736.7 0.30805
480 5.8466 54.748 1350 310.74 2.8971 2700 6236.2 0.28872
500 6.7663 49.278 1400 361.62 2.5817 2750 6769.7 0.27089
520 7.7900 44.514 1450 418.89 2.3083 2800 7338.7 0.25443
540 8.9257 40.344 1500 483.16 2.0703 2850 7945.1 0.23921
560 10.182 36.676 1550 554.96 1.8625 2900 8590.7 0.22511
580 11.568 33.436 1600 634.97 1.6804 2950 9277.2 0.21205
600 13.092 30.561 1650 723.86 1.52007 3000 10007 0.19992
620 14.766 28.001 1700 822.33 1.37858
640 16.598 25.713 1750 931.14 1.25330
660 18.600 23.662 1800 1051.05 1.14204
680 20.784 21.818 1850 1182.9 1.04294
700 23.160 20.155 1900 1327.5 0.95445
T he relative pressure and relative volume are temperature functions calculated wi th two
scaling constants A 1, A 2.
P r = exp[s0T/R A 1]; vr = A 2T/P r
such that for an isentropic process (s1 = s2)
P2
P1=
Pr2
Pr1=
eS0T2
/R
eS0T1
/R
T2
T1
C p /Rand
v2
v1=
vr2
vr1
T1
T2
C v/R
where the near equalities are for the constant heat capacity approximation.
-
7/24/2019 Thermodynamics Table
10/82
764 APPENDIX A SI UNITS: SINGLE-STATE PROPERTIES
TABLE A.8
I deal-Gas Properties of Various Substances, E ntropies at 0.1-M Pa (1-Bar) Pressure,M ass Basis
Nitrogen, Diatomic (N2) Oxygen, Diatomic (O 2)R = 0.2968 kJ /kg-K R = 0.2598 kJ /kg-KM = 28.013 kg/kmol M = 31.999 kg/kmol
T u h s0T u h s0T
(K ) (kJ /kg) (kJ /kg) (kJ /kg-K ) (kJ /kg) (kJ /kg) (kJ /kg-K )
200 148.39 207.75 6.4250 129.84 181.81 6.0466
250 185.50 259.70 6.6568 162.41 227.37 6.2499
300 222.63 311.67 6.8463 195.20 273.15 6.4168
350 259.80 363.68 7.0067 228.37 319.31 6.5590400 297.09 415.81 7.1459 262.10 366.03 6.6838
450 334.57 468.13 7.2692 296.52 413.45 6.7954
500 372.35 520.75 7.3800 331.72 461.63 6.8969
550 410.52 573.76 7.4811 367.70 510.61 6.9903
600 449.16 627.24 7.5741 404.46 560.36 7.0768
650 488.34 681.26 7.6606 441.97 610.86 7.1577
700 528.09 735.86 7.7415 480.18 662.06 7.2336
750 568.45 791.05 7.8176 519.02 713.90 7.3051
800 609.41 846.85 7.8897 558.46 766.33 7.3728
850 650.98 903.26 7.9581 598.44 819.30 7.4370
900 693.13 960.25 8.0232 638.90 872.75 7.4981
950 735.85 1017.81 8.0855 679.80 926.65 7.5564
1000 779.11 1075.91 8.1451 721.11 980.95 7.6121
1100 867.14 1193.62 8.2572 804.80 1090.62 7.7166
1200 957.00 1313.16 8.3612 889.72 1201.53 7.8131
1300 1048.46 1434.31 8.4582 975.72 1313.51 7.9027
1400 1141.35 1556.87 8.5490 1062.67 1426.44 7.9864
1500 1235.50 1680.70 8.6345 1150.48 1540.23 8.0649
1600 1330.72 1805.60 8.7151 1239.10 1654.83 8.1389
1700 1426.89 1931.45 8.7914 1328.49 1770.21 8.2088
1800 1523.90 2058.15 8.8638 1418.63 1886.33 8.2752
1900 1621.66 2185.58 8.9327 1509.50 2003.19 8.3384
2000 1720.07 2313.68 8.9984 1601.10 2120.77 8.39872100 1819.08 2442.36 9.0612 1693.41 2239.07 8.4564
2200 1918.62 2571.58 9.1213 1786.44 2358.08 8.5117
2300 2018.63 2701.28 9.1789 1880.17 2477.79 8.5650
2400 2119.08 2831.41 9.2343 1974.60 2598.20 8.6162
2500 2219.93 2961.93 9.2876 2069.71 2719.30 8.6656
2600 2321.13 3092.81 9.3389 2165.50 2841.07 8.7134
2700 2422.66 3224.03 9.3884 2261.94 2963.49 8.7596
2800 2524.50 3355.54 9.4363 2359.01 3086.55 8.8044
2900 2626.62 3487.34 9.4825 2546.70 3210.22 8.8478
3000 2729.00 3619.41 9.5273 2554.97 3334.48 8.8899
-
7/24/2019 Thermodynamics Table
11/82
APPENDIX A SI UNITS: SINGLE-STATE PROPERTIES 765
TABLE A.8 (continued)I deal-Gas Properties of Various Substances, E ntropies at 0.1-M Pa (1-Bar) Pressure,M ass Basis
Nitrogen, Diatomic (C O 2) Water (H 2O)R = 0.1889 kJ /kg-K R = 0.4615 kJ /kg-KM = 44.010 kg/kmol M = 18.015 kg/kmol
T u h s0T u h s0T
(K ) (kJ /kg) (kJ /kg) (kJ /kg-K ) (kJ /kg) (kJ /kg) (kJ /kg-K )
200 97.49 135.28 4.5439 276.38 368.69 9.7412
250 126.21 173.44 4.7139 345.98 461.36 10.1547
300 157.70 214.38 4.8631 415.87 554.32 10.4936
350 191.78 257.90 4.9972 486.37 647.90 10.7821400 228.19 303.76 5.1196 557.79 742.40 11.0345
450 266.69 351.70 5.2325 630.40 838.09 11.2600
500 307.06 401.52 5.3375 704.36 935.12 11.4644
550 349.12 453.03 5.4356 779.79 1033.63 11.6522
600 392.72 506.07 5.5279 856.75 1133.67 11.8263
650 437.71 560.51 5.6151 935.31 1235.30 11.9890
700 483.97 616.22 5.6976 1015.49 1338.56 12.1421
750 531.40 673.09 5.7761 1097.35 1443.49 12.2868
800 579.89 731.02 5.8508 1180.90 1550.13 12.4244
850 629.35 789.93 5.9223 1266.19 1658.49 12.5558
900 676.69 849.72 5.9906 1353.23 1768.60 12.6817
950 730.85 910.33 6.0561 1442.03 1880.48 12.8026
1000 782.75 971.67 6.1190 1532.61 1994.13 12.9192
1100 888.55 1096.36 6.2379 1719.05 2226.73 13.1408
1200 996.64 1223.34 6.3483 1912.42 2466.25 13.3492
1300 1106.68 1352.28 6.4515 2112.47 2712.46 13.5462
1400 1218.38 1482.87 6.5483 2318.89 2965.03 13.7334
1500 1331.50 1614.88 6.6394 2531.28 3223.57 13.9117
1600 1445.85 1748.12 6.7254 2749.24 3487.69 14.0822
1700 1561.26 1882.43 6.8068 2972.35 3756.95 14.2454
1800 1677.61 2017.67 6.8841 3200.17 4030.92 14.4020
1900 1794.78 2153.73 6.9577 3432.28 4309.18 14.5524
2000 1912.67 2290.51 7.0278 3668.24 4591.30 14.69712100 2031.21 2427.95 7.0949 3908.08 4877.29 14.8366
2200 2150.34 2565.97 7.1591 4151.28 5166.64 14.9712
2300 2270.00 2704.52 7.2206 4397.56 5459.08 15.1012
2400 2390.14 2843.55 7.2798 4646.71 5754.37 15.2269
2500 2510.74 2983.04 7.3368 4898.49 6052.31 15.3485
2600 2631.73 3122.93 7.3917 5152.73 6352.70 15.4663
2700 2753.10 3263.19 7.4446 5409.24 6655.36 15.5805
2800 2874.81 3403.79 7.4957 5667.86 6960.13 15.6914
2900 2996.84 3544.71 7.5452 5928.44 7266.87 15.7990
3000 3119.18 3685.95 7.5931 6190.86 7575.44 15.9036
-
7/24/2019 Thermodynamics Table
12/82
766 APPENDIX A SI UNITS: SINGLE-STATE PROPERTIES
TABLE A.9
I deal-Gas Properties of Various Substances (SI U nits), E ntropies at 0.1-M Pa (1-B ar)Pressure, M ole Basis
Nitrogen, Diatomic (N2) Nitrogen, M onatomic (N)
h0
f,298 = 0 kJ /kmol h0
f,298 = 472 680 kJ /kmol
M = 28.013 kg/kmol M = 14.007 kg/kmol
T (hh0
298) s0T (hh
0
298) s0T
K kJ /kmol kJ /kmol K kJ /kmol kJ /kmol
0 8670 0 6197 0
100 5768 159.812 4119 130.593
200 2857 179.985 2040 145.001
298 0 191.609 0 153.300300 54 191.789 38 153.429
400 2971 200.181 2117 159.409
500 5911 206.740 4196 164.047
600 8894 212.177 6274 167.837
700 11937 216.865 8353 171.041
800 15046 221.016 10431 173.816
900 18223 224.757 12510 176.265
1000 21463 228.171 14589 178.455
1100 24760 231.314 16667 180.436
1200 28109 234.227 18746 182.244
1300 31503 236.943 20825 183.908
1400 34936 239.487 22903 185.448
1500 38405 241.881 24982 186.883
1600 41904 244.139 27060 188.224
1700 45430 246.276 29139 189.484
1800 48979 248.304 31218 190.672
1900 52549 250.234 33296 191.796
2000 56137 252.075 35375 192.863
2200 63362 255.518 39534 194.845
2400 70640 258.684 43695 196.655
2600 77963 261.615 47860 198.322
2800 85323 264.342 52033 199.868
3000 92715 266.892 56218 201.3113200 100134 269.286 60420 202.667
3400 107577 271.542 64646 203.948
3600 115042 273.675 68902 205.164
3800 122526 275.698 73194 206.325
4000 130027 277.622 77532 207.437
4400 145078 281.209 86367 209.542
4800 160188 284.495 95457 211.519
5200 175352 287.530 104843 213.397
5600 190572 290.349 114550 215.195
6000 205848 292.984 124590 216.926
-
7/24/2019 Thermodynamics Table
13/82
APPENDIX A SI UNITS: SINGLE-STATE PROPERTIES 767
TABLE A.9 (continued)I deal-Gas Properties of Various Substances (SI U nits), Entropies at 0.1-M Pa (1-B ar)Pressure, M ole B asis
Oxygen, Diatomic(O2) Oxygen, M onatomic(O)
h0
f,298 = 0 kJ /kmol h
0
f,298 = 249 170 kJ /kmol
M = 31.999 kg/kmol M = 16.00 kg/kmol
T (h h0
298) s0T (h
h0
298) s0T
K kJ /kmol kJ /kmol K kJ /kmol kJ /kmol K
0 8683 0 6725 0
100 5777 173.308 4518 135.947
200 2868 193.483 2186 152.153
298 0 205.148 0 161.059300 54 205.329 41 161.194
400 3027 213.873 2207 167.431
500 6086 220.693 4343 172.198
600 9245 226.450 6462 176.060
700 12499 231.465 8570 179.310
800 15836 235.920 10671 182.116
900 19241 239.931 12767 184.585
1000 22703 243.579 14860 186.790
1100 26212 246.923 16950 188.783
1200 29761 250.011 19039 190.600
1300 33345 252.878 21126 192.270
1400 36958 255.556 23212 193.816
1500 40600 258.068 25296 195.254
1600 44267 260.434 27381 196.599
1700 47959 262.673 29464 197.862
1800 51674 264.797 31547 199.053
1900 55414 266.819 33630 200.179
2000 59176 268.748 35713 201.247
2200 66770 272.366 39878 203.232
2400 74453 275.708 44045 205.045
2600 82225 278.818 48216 206.714
2800 90080 281.729 52391 208.262
3000 98013 284.466 56574 209.705
3200 106022 287.050 60767 211.058
3400 114101 289.499 64971 212.332
3600 122245 291.826 69190 213.538
3800 130447 294.043 73424 214.682
4000 138705 296.161 77675 215.773
4400 155374 300.133 86234 217.812
4800 172240 303.801 94873 219.691
5200 189312 307.217 103592 221.435
5600 206618 310.423 112391 223.066
6000 224210 313.457 121264 224.597
-
7/24/2019 Thermodynamics Table
14/82
768 APPENDIX A SI UNITS: SINGLE-STATE PROPERTIES
TABLE A.9 (continued)I deal-Gas Properties of Various Substances (SI U nits), E ntropies at 0.1-M Pa (1-B ar)Pressure, M ole Basis
C arbon Dioxide (C O 2) C arbon M onoxide (C O)
h0
f,298 = 393 522 kJ /kmol h
0
f,298 = 110 527 kJ /kmol
M = 44.01 kg/kmol M = 28.01 kg/kmol
T (h h0
298) s0T (h
h0
298) s0T
K kJ /kmol kJ /kmol K kJ /kmol kJ /kmol K
0 9364 0 8671 0
100 6457 179.010 5772 165.852
200 3413 199.976 2860 186.024
298 0 213.794 0 197.651300 69 214.024 54 197.831
400 4003 225.314 2977 206.240
500 8305 234.902 5932 212.833
600 12906 243.284 8942 218.321
700 17754 250.752 12021 223.067
800 22806 257.496 15174 227.277
900 28030 263.646 18397 231.074
1000 33397 269.299 21686 234.538
1100 38885 274.528 25031 237.726
1200 44473 279.390 28427 240.679
1300 50148 283.931 31867 243.431
1400 55895 288.190 35343 246.006
1500 61705 292.199 38852 248.426
1600 67569 295.984 42388 250.707
1700 73480 299.567 45948 252.866
1800 79432 302.969 49529 254.913
1900 85420 306.207 53128 256.860
2000 91439 309.294 56743 258.716
2200 103562 315.070 64012 262.182
2400 115779 320.384 71326 265.361
2600 128074 325.307 78679 268.302
2800 140435 329.887 86070 271.044
3000 152853 334.170 93504 273.607
3200 165321 338.194 100962 276.012
3400 177836 341.988 108440 278.279
3600 190394 345.576 115938 280.422
3800 202990 348.981 123454 282.454
4000 215624 352.221 130989 284.387
4400 240992 358.266 146108 287.989
4800 266488 363.812 161285 291.290
5200 292112 368.939 176510 294.337
5600 317870 373.711 191782 297.167
6000 343782 378.180 207105 299.809
-
7/24/2019 Thermodynamics Table
15/82
APPENDIX A SI UNITS: SINGLE-STATE PROPERTIES 769
TABLE A.9 (continued)I deal-Gas Properties of Various Substances (SI U nits), Entropies at 0.1-M Pa (1-B ar)Pressure, M ole B asis
Water(H 2O) Hydroxyl(OH )
h0
f,298 = 241 826 kJ /kmol h
0
f,298 = 38987 kJ /kmol
M = 18.015 kg/kmol M = 17.007 kg/kmol
T (h h0
298) s0T (h
h0
298) s0T
K kJ /kmol kJ /kmol K kJ /kmol kJ /kmol K
0 9904 0 9172 0
100 6617 152.386 6140 149.591
200 3282 175.488 2975 171.592
298 0 188.835 0 183.709300 62 189.043 55 183.894
400 3450 198.787 3034 192.466
500 6922 206.532 5991 199.066
600 10499 213.051 8943 204.448
700 14190 218.739 11902 209.008
800 18002 223.826 14881 212.984
900 21937 228.460 17889 216.526
1000 26000 232.739 20935 219.735
1100 30190 236.732 24024 222.680
1200 34506 240.485 27159 225.408
1300 38941 244.035 30340 227.955
1400 43491 247.406 33567 230.347
1500 48149 250.620 36838 232.604
1600 52907 253.690 40151 234.741
1700 57757 256.631 43502 236.772
1800 62693 259.452 46890 238.707
1900 67706 262.162 50311 240.556
2000 72788 264.769 53763 242.328
2200 83153 269.706 60751 245.659
2400 93741 274.312 67840 248.743
2600 104520 278.625 75018 251.614
2800 115463 282.680 82268 254.301
3000 126548 286.504 89585 256.825
3200 137756 290.120 96960 259.205
3400 149073 293.550 104388 261.456
3600 160484 296.812 111864 263.592
3800 171981 299.919 119382 265.625
4000 183552 302.887 126940 267.563
4400 206892 308.448 142165 271.191
4800 230456 313.573 157522 274.531
5200 254216 318.328 173002 277.629
5600 278161 322.764 188598 280.518
6000 302295 326.926 204309 283.227
-
7/24/2019 Thermodynamics Table
16/82
770 APPENDIX A SI UNITS: SINGLE-STATE PROPERTIES
TABLE A.9 (continued)I deal-Gas Properties of Various Substances (SI U nits), E ntropies at 0.1-M Pa (1-B ar)Pressure, M ole Basis
H ydrogen(H 2) H ydrogen, M onatomic(H )
h0
f,298 = 0 kJ /kmol h
0
f,298 = 217 999 kJ /kmol
M = 2.016 kg/kmol M = 1.008 kg/kmol
T (h h0
298) s0T (h
h0
298) s0T
K kJ /kmol kJ /kmol K kJ /kmol kJ /kmol K
0 8467 0 6197 0
100 5467 100.727 4119 92.009
200 2774 119.410 2040 106.417
298 0 130.678 0 114.716300 53 130.856 38 114.845
400 2961 139.219 2117 120.825
500 5883 145.738 4196 125.463
600 8799 151.078 6274 129.253
700 11730 155.609 8353 132.457
800 14681 159.554 10431 135.233
900 17657 163.060 12510 137.681
1000 20663 166.225 14589 139.871
1100 23704 169.121 16667 141.852
1200 26785 171.798 18746 143.661
1300 29907 174.294 20825 145.324
1400 33073 176.637 22903 146.865
1500 36281 178.849 24982 148.299
1600 39533 180.946 27060 149.640
1700 42826 182.941 29139 150.900
1800 46160 184.846 31218 152.089
1900 49532 186.670 33296 153.212
2000 52942 188.419 35375 154.279
2200 59865 191.719 39532 156.260
2400 66915 194.789 43689 158.069
2600 74082 197.659 47847 159.732
2800 81355 200.355 52004 161.273
3000 88725 202.898 56161 162.707
3200 96187 205.306 60318 164.048
3400 103736 207.593 64475 165.308
3600 111367 209.773 68633 166.497
3800 119077 211.856 72790 167.620
4000 126864 213.851 76947 168.687
4400 142658 217.612 85261 170.668
4800 158730 221.109 93576 172.476
5200 175057 224.379 101890 174.140
5600 191607 227.447 110205 175.681
6000 208332 230.322 118519 177.114
-
7/24/2019 Thermodynamics Table
17/82
APPENDIX A SI UNITS: SINGLE-STATE PROPERTIES 771
TABLE A.9 (continued)I deal-Gas Properties of Various Substances (SI U nits), Entropies at 0.1-M Pa (1-B ar)Pressure, M ole B asis
Nitric O xide (NO ) Nitrogen Dioxide (NO 2)
h0
f,298 = 90291 kJ /kmol h
0
f,298 = 33100kJ /kmol
M = 30.006 kg/kmol M = 46.005 kg/kmol
T (h h0
298) s0T (h
h0
298) s0T
K kJ /kmol kJ /kmol K kJ /kmol kJ /kmol K
0 9192 0 10186 0
100 6073 177.031 6861 202.563
200 2951 198.747 3495 225.852
298 0 210.759 0 240.034300 55 210.943 68 240.263
400 3040 219.529 3927 251.342
500 6059 226.263 8099 260.638
600 9144 231.886 12555 268.755
700 12308 236.762 17250 275.988
800 15548 241.088 22138 282.513
900 18858 244.985 27180 288.450
1000 22229 248.536 32344 293.889
1100 25653 251.799 37606 298.904
1200 29120 254.816 42946 303.551
1300 32626 257.621 48351 307.876
1400 36164 260.243 53808 311.920
1500 39729 262.703 59309 315.715
1600 43319 265.019 64846 319.289
1700 46929 267.208 70414 322.664
1800 50557 269.282 76008 325.861
1900 54201 271.252 81624 328.898
2000 57859 273.128 87259 331.788
2200 65212 276.632 98578 337.182
2400 72606 279.849 109948 342.128
2600 80034 282.822 121358 346.695
2800 87491 285.585 132800 350.934
3000 94973 288.165 144267 354.890
3200 102477 290.587 155756 358.597
3400 110000 292.867 167262 362.085
3600 117541 295.022 178783 365.378
3800 125099 297.065 190316 368.495
4000 132671 299.007 201860 371.456
4400 147857 302.626 224973 376.963
4800 163094 305.940 248114 381.997
5200 178377 308.998 271276 386.632
5600 193703 311.838 294455 390.926
6000 209070 314.488 317648 394.926
-
7/24/2019 Thermodynamics Table
18/82
772 APPENDIX A SI UNITS: SINGLE-STATE PROPERTIES
TABLE A.10
E nthalpy of Formation and Absolute E ntropy of Various Substances at 25C , 100 kPaPressure
M h0
f s0f
Substance Formula kg/kmol State kJ /kmol kJ /kmol K
A cetylene C 2H 2 26.038 gas +226 731 200.958
A mmonia N H 3 17.031 gas 45 720 192.572
B enzene C 6H 6 78.114 gas +82 980 269.562
C arbon dioxide C O2 44.010 gas 393 522 213.795
C arbon (graphite) C 12.011 solid 0 5.740
C arbon monoxide C O 28.011 gas 110 527 197.653
E thane C 2H 6 30.070 gas 84 740 229.597E thene C 2H 4 28.054 gas +52 467 219.330
E thanol C 2H 5OH 46.069 gas 235 000 282.444
E thanol C 2H 5OH 46.069 liq 277 380 160.554
H eptane C 7H 16 100.205 gas 187 900 427.805
H exane C 6H 14 86.178 gas 167 300 387.979
Hydrogen peroxide H 2O 2 34.015 gas 136 106 232.991
M ethane C H 4 16.043 gas 74 873 186.251
M ethanol C H 3OH 32.042 gas 201 300 239.709
M ethanol C H 3OH 32.042 liq 239 220 126.809
n-B utane C 4H 10 58.124 gas 126 200 306.647
N itrogen oxide N 2O 44.013 gas +82 050 219.957
N itromethane C H3N O 2 61.04 liq 113 100 171.80
n-O ctane C 8H 18 114.232 gas 208 600 466.514
n-O ctane C 8H 18 114.232 liq 250 105 360.575
Ozone O 3 47.998 gas +142 674 238.932
Pentane C 5H 12 72.151 gas 146 500 348.945
Propane C 3H 8 44.094 gas 103 900 269.917
Propene C 3H 6 42.081 gas +20 430 267.066
Sulfur S 32.06 solid 0 32.056
Sulfur dioxide SO 2 64.059 gas 296 842 248.212
Sulfur trioxide SO 3 80.058 gas 395 765 256.769
T-T-D iesel C 14.4H 24.9 198.06 liq 174 000 525.90
Water H 2O 18.015 gas 241 826 188.834Water H 2O 18.015 liq 285 830 69.950
-
7/24/2019 Thermodynamics Table
19/82
TABLE
A.1
1
LogarithmstotheBaseeoftheEquilibrium
ConstantK
ForthereactionvAA+
vBB
vCC+
vDD,theequilibrium
constantKisdefinedas
K
=
yvCC
yvDD
yvAA
yvBB
P P0
vC+vDvAvB
,
P0
=
0.
1MPa
TempK
H2
2H
O2
2O
N2
2N
2H2O
2H2+
O2
2H2O
H2+
2OH
2CO2
2CO
+
O2
N2+
O2
2NO
N2+
2O2
2NO2
298
164.003
186.963
367.528
184.420
212.0
75
207.529
69.868
41.355
500
92.830
105.623
213.405
105.385
120.3
31
115.234
40.449
30.725
1000
39.810
45.146
99.146
46.321
51.9
51
47.052
18.709
23.039
1200
30.878
35.003
80.025
36.363
40.4
67
35.736
15.082
21.752
1400
24.467
27.741
66.345
29.222
32.2
44
27.679
12.491
20.826
1600
19.638
22.282
56.069
23.849
26.0
67
21.656
10.547
20.126
1800
15.868
18.028
48.066
19.658
21.2
58
16.987
9.035
19.577
2000
12.841
14.619
41.655
16.299
17.4
06
13.266
7.825
19.136
2200
10.356
11.826
36.404
13.546
14.2
53
10.232
6.836
18.773
2400
8.280
9.495
32.023
11.249
11.6
25
7.715
6.012
18.470
2600
6.519
7.520
28.313
9.303
9.4
02
5.594
5.316
18.214
2800
5.005
5.826
25.129
7.633
7.4
96
3.781
4.720
17.994
3000
3.690
4.356
22.367
6.184
5.8
45
2.217
4.205
17.805
3200
2.538
3.069
19.947
4.916
4.4
01
0.853
3.755
17.640
3400
1.519
1.932
17.810
3.795
3.1
28
0.346
3.359
17.496
3600
0.611
0.922
15.909
2.799
1.9
96
1.408
3.008
17.369
3800
0.201
0.017
14.205
1.906
0.9
84
2.355
2.694
17.257
4000
0.934
0.798
12.671
1.101
0.0
74
3.204
2.413
17.157
4500
2.483
2.520
9.423
0.602
1.8
47
4.985
1.824
16.953
5000
3.724
3.898
6.816
1.972
3.3
83
6.397
1.358
16.797
5500
4.739
5.027
4.672
3.098
4.6
39
7.542
0.980
16.678
6000
5.587
5.969
2.876
4.040
5.6
84
8.488
0.671
16.588
Source:ConsistentwiththermodynamicdatainJANAFThermochemicalTables,thirdedition,ThermalGroup,Dow
ChemicalU.S.A.,M
idland,MI,1985.
773
-
7/24/2019 Thermodynamics Table
20/82
-
7/24/2019 Thermodynamics Table
21/82
A P P E N D I X
BSI Units:ThermodynamicTables
775
-
7/24/2019 Thermodynamics Table
22/82
776 APPENDIX B SI UNITS: THERMODYNAMIC TABLES
TABLE B.1
Thermodynamic Properties of Water
TABLE B.1.1
Saturated Water
Specific Volume, m3/kg Internal E nergy, kJ /kg
Temp. Press. Sat. L iquid E vap. Sat. Vapor Sat. L iquid E vap. Sat. Vapor
(C ) (kPa) vf vf g vg u f u f g ug
0.01 0.6113 0.001000 206.131 206.132 0 2375.33 2375.33
5 0.8721 0.001000 147.117 147.118 20.97 2361.27 2382.24
10 1.2276 0.001000 106.376 106.377 41.99 2347.16 2389.15
15 1.705 0.001001 77.924 77.925 62.98 2333.06 2396.04
20 2.339 0.001002 57.7887 57.7897 83.94 2318.98 2402.9125 3.169 0.001003 43.3583 43.3593 104.86 2304.90 2409.76
30 4.246 0.001004 32.8922 32.8932 125.77 2290.81 2416.58
35 5.628 0.001006 25.2148 25.2158 146.65 2276.71 2423.36
40 7.384 0.001008 19.5219 19.5229 167.53 2262.57 2430.11
45 9.593 0.001010 15.2571 15.2581 188.41 2248.40 2436.81
50 12.350 0.001012 12.0308 12.0318 209.30 2234.17 2443.47
55 15.758 0.001015 9.56734 9.56835 230.19 2219.89 2450.08
60 19.941 0.001017 7.66969 7.67071 251.09 2205.54 2456.63
65 25.03 0.001020 6.19554 6.19656 272.00 2191.12 2463.12
70 31.19 0.001023 5.04114 5.04217 292.93 2176.62 2469.55
75 38.58 0.001026 4.13021 4.13123 313.87 2162.03 2475.91
80 47.39 0.001029 3.40612 3.40715 334.84 2147.36 2482.19
85 57.83 0.001032 2.82654 2.82757 355.82 2132.58 2488.40
90 70.14 0.001036 2.35953 2.36056 376.82 2117.70 2494.52
95 84.55 0.001040 1.98082 1.98186 397.86 2102.70 2500.56
100 101.3 0.001044 1.67185 1.67290 418.91 2087.58 2506.50
105 120.8 0.001047 1.41831 1.41936 440.00 2072.34 2512.34
110 143.3 0.001052 1.20909 1.21014 461.12 2056.96 2518.09
115 169.1 0.001056 1.03552 1.03658 482.28 2041.44 2523.72
120 198.5 0.001060 0.89080 0.89186 503.48 2025.76 2529.24
125 232.1 0.001065 0.76953 0.77059 524.72 2009.91 2534.63
130 270.1 0.001070 0.66744 0.66850 546.00 1993.90 2539.90
135 313.0 0.001075 0.58110 0.58217 567.34 1977.69 2545.03
140 361.3 0.001080 0.50777 0.50885 588.72 1961.30 2550.02
145 415.4 0.001085 0.44524 0.44632 610.16 1944.69 2554.86
150 475.9 0.001090 0.39169 0.39278 631.66 1927.87 2559.54
155 543.1 0.001096 0.34566 0.34676 653.23 1910.82 2564.04
160 617.8 0.001102 0.30596 0.30706 674.85 1893.52 2568.37
165 700.5 0.001108 0.27158 0.27269 696.55 1875.97 2572.51
170 791.7 0.001114 0.24171 0.24283 718.31 1858.14 2576.46
175 892.0 0.001121 0.21568 0.21680 740.16 1840.03 2580.19
180 1002.2 0.001127 0.19292 0.19405 762.08 1821.62 2583.70
185 1122.7 0.001134 0.17295 0.17409 784.08 1802.90 2586.98
190 1254.4 0.001141 0.15539 0.15654 806.17 1783.84 2590.01
-
7/24/2019 Thermodynamics Table
23/82
APPENDIX B SI UNITS: THERMODYNAMIC TABLES 777
TABLE B.1.1 (continued)Saturated Water
E nthalpy, kJ /kg E ntropy, kJ /kg-K
Temp. Press. Sat. L iquid E vap. Sat. Vapor Sat. L iquid E vap. Sat. Vapor(C ) (kPa) h f h f g hg s f s f g sg
0.01 0.6113 0.00 2501.35 2501.35 0 9.1562 9.1562
5 0.8721 20.98 2489.57 2510.54 0.0761 8.9496 9.0257
10 1.2276 41.99 2477.75 2519.74 0.1510 8.7498 8.9007
15 1.705 62.98 2465.93 2528.91 0.2245 8.5569 8.7813
20 2.339 83.94 2454.12 2538.06 0.2966 8.3706 8.6671
25 3.169 104.87 2442.30 2547.17 0.3673 8.1905 8.5579
30 4.246 125.77 2430.48 2556.25 0.4369 8.0164 8.4533
35 5.628 146.66 2418.62 2565.28 0.5052 7.8478 8.3530
40 7.384 167.54 2406.72 2574.26 0.5724 7.6845 8.2569
45 9.593 188.42 2394.77 2583.19 0.6386 7.5261 8.1647
50 12.350 209.31 2382.75 2592.06 0.7037 7.3725 8.0762
55 15.758 230.20 2370.66 2600.86 0.7679 7.2234 7.9912
60 19.941 251.11 2358.48 2609.59 0.8311 7.0784 7.9095
65 25.03 272.03 2346.21 2618.24 0.8934 6.9375 7.8309
70 31.19 292.96 2333.85 2626.80 0.9548 6.8004 7.7552
75 38.58 313.91 2321.37 2635.28 1.0154 6.6670 7.6824
80 47.39 334.88 2308.77 2643.66 1.0752 6.5369 7.6121
85 57.83 355.88 2296.05 2651.93 1.1342 6.4102 7.544490 70.14 376.90 2283.19 2660.09 1.1924 6.2866 7.4790
95 84.55 397.94 2270.19 2668.13 1.2500 6.1659 7.4158
100 101.3 419.02 2257.03 2676.05 1.3068 6.0480 7.3548
105 120.8 440.13 2243.70 2683.83 1.3629 5.9328 7.2958
110 143.3 461.27 2230.20 2691.47 1.4184 5.8202 7.2386
115 169.1 482.46 2216.50 2698.96 1.4733 5.7100 7.1832
120 198.5 503.69 2202.61 2706.30 1.5275 5.6020 7.1295
125 232.1 524.96 2188.50 2713.46 1.5812 5.4962 7.0774
130 270.1 546.29 2174.16 2720.46 1.6343 5.3925 7.0269
135 313.0 567.67 2159.59 2727.26 1.6869 5.2907 6.9777
140 361.3 589.11 2144.75 2733.87 1.7390 5.1908 6.9298
145 415.4 610.61 2129.65 2740.26 1.7906 5.0926 6.8832
150 475.9 632.18 2114.26 2746.44 1.8417 4.9960 6.8378
155 543.1 653.82 2098.56 2752.39 1.8924 4.9010 6.7934
160 617.8 675.53 2082.55 2758.09 1.9426 4.8075 6.7501
165 700.5 697.32 2066.20 2763.53 1.9924 4.7153 6.7078
170 791.7 719.20 2049.50 2768.70 2.0418 4.6244 6.6663
175 892.0 741.16 2032.42 2773.58 2.0909 4.5347 6.6256
180 1002.2 763.21 2014.96 2778.16 2.1395 4.4461 6.5857
185 1122.7 785.36 1997.07 2782.43 2.1878 4.3586 6.5464
190 1254.4 807.61 1978.76 2786.37 2.2358 4.2720 6.5078
-
7/24/2019 Thermodynamics Table
24/82
778 APPENDIX B SI UNITS: THERMODYNAMIC TABLES
TABLE B.1.1 (continued)Saturated Water
Specific Volume, m3/kg Internal E nergy, kJ /kg
Temp. Press. Sat. L iquid E vap. Sat. Vapor Sat. L iquid E vap. Sat. Vapor(C ) (kPa) vf vf g vg u f u f g ug
195 1397.8 0.001149 0.13990 0.14105 828.36 1764.43 2592.79
200 1553.8 0.001156 0.12620 0.12736 850.64 1744.66 2595.29
205 1723.0 0.001164 0.11405 0.11521 873.02 1724.49 2597.52
210 1906.3 0.001173 0.10324 0.10441 895.51 1703.93 2599.44
215 2104.2 0.001181 0.09361 0.09479 918.12 1682.94 2601.06
220 2317.8 0.001190 0.08500 0.08619 940.85 1661.49 2602.35
225 2547.7 0.001199 0.07729 0.07849 963.72 1639.58 2603.30
230 2794.9 0.001209 0.07037 0.07158 986.72 1617.17 2603.89
235 3060.1 0.001219 0.06415 0.06536 1009.88 1594.24 2604.11
240 3344.2 0.001229 0.05853 0.05976 1033.19 1570.75 2603.95
245 3648.2 0.001240 0.05346 0.05470 1056.69 1546.68 2603.37
250 3973.0 0.001251 0.04887 0.05013 1080.37 1522.00 2602.37
255 4319.5 0.001263 0.04471 0.04598 1104.26 1496.66 2600.93
260 4688.6 0.001276 0.04093 0.04220 1128.37 1470.64 2599.01
265 5081.3 0.001289 0.03748 0.03877 1152.72 1443.87 2596.60
270 5498.7 0.001302 0.03434 0.03564 1177.33 1416.33 2593.66
275 5941.8 0.001317 0.03147 0.03279 1202.23 1387.94 2590.17
280 6411.7 0.001332 0.02884 0.03017 1227.43 1358.66 2586.09285 6909.4 0.001348 0.02642 0.02777 1252.98 1328.41 2581.38
290 7436.0 0.001366 0.02420 0.02557 1278.89 1297.11 2575.99
295 7992.8 0.001384 0.02216 0.02354 1305.21 1264.67 2569.87
300 8581.0 0.001404 0.02027 0.02167 1331.97 1230.99 2562.96
305 9201.8 0.001425 0.01852 0.01995 1359.22 1195.94 2555.16
310 9856.6 0.001447 0.01690 0.01835 1387.03 1159.37 2546.40
315 10547 0.001472 0.01539 0.01687 1415.44 1121.11 2536.55
320 11274 0.001499 0.01399 0.01549 1444.55 1080.93 2525.48
325 12040 0.001528 0.01267 0.01420 1474.44 1038.57 2513.01
330 12845 0.001561 0.01144 0.01300 1505.24 993.66 2498.91
335 13694 0.001597 0.01027 0.01186 1537.11 945.77 2482.88
340 14586 0.001638 0.00916 0.01080 1570.26 894.26 2464.53
345 15525 0.001685 0.00810 0.00978 1605.01 838.29 2443.30
350 16514 0.001740 0.00707 0.00881 1641.81 776.58 2418.39
355 17554 0.001807 0.00607 0.00787 1681.41 707.11 2388.52
360 18651 0.001892 0.00505 0.00694 1725.19 626.29 2351.47
365 19807 0.002011 0.00398 0.00599 1776.13 526.54 2302.67
370 21028 0.002213 0.00271 0.00493 1843.84 384.69 2228.53
374.1 22089 0.003155 0 0.00315 2029.58 0 2029.58
-
7/24/2019 Thermodynamics Table
25/82
APPENDIX B SI UNITS: THERMODYNAMIC TABLES 779
TABLE B.1.1 (continued)Saturated Water
E nthalpy, kJ /kg E ntropy, kJ /kg-K
Temp. Press. Sat. L iquid E vap. Sat. Vapor Sat. L iquid E vap. Sat. Vapor(C ) (kPa) h f h f g hg s f s f g sg
195 1397.8 829.96 1959.99 2789.96 2.2835 4.1863 6.4697
200 1553.8 852.43 1940.75 2793.18 2.3308 4.1014 6.4322
205 1723.0 875.03 1921.00 2796.03 2.3779 4.0172 6.3951
210 1906.3 897.75 1900.73 2798.48 2.4247 3.9337 6.3584
215 2104.2 920.61 1879.91 2800.51 2.4713 3.8507 6.3221
220 2317.8 943.61 1858.51 2802.12 2.5177 3.7683 6.2860
225 2547.7 966.77 1836.50 2803.27 2.5639 3.6863 6.2502
230 2794.9 990.10 1813.85 2803.95 2.6099 3.6047 6.2146
235 3060.1 1013.61 1790.53 2804.13 2.6557 3.5233 6.1791
240 3344.2 1037.31 1766.50 2803.81 2.7015 3.4422 6.1436
245 3648.2 1061.21 1741.73 2802.95 2.7471 3.3612 6.1083
250 3973.0 1085.34 1716.18 2801.52 2.7927 3.2802 6.0729
255 4319.5 1109.72 1689.80 2799.51 2.8382 3.1992 6.0374
260 4688.6 1134.35 1662.54 2796.89 2.8837 3.1181 6.0018
265 5081.3 1159.27 1634.34 2793.61 2.9293 3.0368 5.9661
270 5498.7 1184.49 1605.16 2789.65 2.9750 2.9551 5.9301
275 5941.8 1210.05 1574.92 2784.97 3.0208 2.8730 5.8937
280 6411.7 1235.97 1543.55 2779.53 3.0667 2.7903 5.8570285 6909.4 1262.29 1510.97 2773.27 3.1129 2.7069 5.8198
290 7436.0 1289.04 1477.08 2766.13 3.1593 2.6227 5.7821
295 7992.8 1316.27 1441.78 2758.05 3.2061 2.5375 5.7436
300 8581.0 1344.01 1404.93 2748.94 3.2533 2.4511 5.7044
305 9201.8 1372.33 1366.38 2738.72 3.3009 2.3633 5.6642
310 9856.6 1401.29 1325.97 2727.27 3.3492 2.2737 5.6229
315 10547 1430.97 1283.48 2714.44 3.3981 2.1821 5.5803
320 11274 1461.45 1238.64 2700.08 3.4479 2.0882 5.5361
325 12040 1492.84 1191.13 2683.97 3.4987 1.9913 5.4900
330 12845 1525.29 1140.56 2665.85 3.5506 1.8909 5.4416
335 13694 1558.98 1086.37 2645.35 3.6040 1.7863 5.3903
340 14586 1594.15 1027.86 2622.01 3.6593 1.6763 5.3356
345 15525 1631.17 964.02 2595.19 3.7169 1.5594 5.2763
350 16514 1670.54 893.38 2563.92 3.7776 1.4336 5.2111
355 17554 1713.13 813.59 2526.72 3.8427 1.2951 5.1378
360 18651 1760.48 720.52 2481.00 3.9146 1.1379 5.0525
365 19807 1815.96 605.44 2421.40 3.9983 0.9487 4.9470
370 21028 1890.37 441.75 2332.12 4.1104 0.6868 4.7972
374.1 22089 2099.26 0 2099.26 4.4297 0 4.4297
-
7/24/2019 Thermodynamics Table
26/82
780 APPENDIX B SI UNITS: THERMODYNAMIC TABLES
TABLE B.1.2
Saturated Water Pressure E ntry
Specific Volume, m3/kg Internal E nergy, kJ /kg
Press. Temp. Sat. L iquid E vap. Sat. Vapor Sat. L iquid E vap. Sat. Vapor(kPa) (C ) vf u f g vg u f u f g ug
0.6113 0.01 0.001000 206.131 206.132 0 2375.3 2375.3
1 6.98 0.001000 129.20702 129.20802 29.29 2355.69 2384.98
1.5 13.03 0.001001 87.97913 87.98013 54.70 2338.63 2393.32
2 17.50 0.001001 67.00285 67.00385 73.47 2326.02 2399.48
2.5 21.08 0.001002 54.25285 54.25385 88.47 2315.93 2404.40
3 24.08 0.001003 45.66402 45.66502 101.03 2307.48 2408.51
4 28.96 0.001004 34.79915 34.80015 121.44 2293.73 2415.17
5 32.88 0.001005 28.19150 28.19251 137.79 2282.70 2420.49
7.5 40.29 0.001008 19.23674 19.23775 168.76 2261.74 2430.50
10 45.81 0.001010 14.67254 14.67355 191.79 2246.10 2437.89
15 53.97 0.001014 10.02117 10.02218 225.90 2222.83 2448.73
20 60.06 0.001017 7.64835 7.64937 251.35 2205.36 2456.71
25 64.97 0.001020 6.20322 6.20424 271.88 2191.21 2463.08
30 69.10 0.001022 5.22816 5.22918 289.18 2179.22 2468.40
40 75.87 0.001026 3.99243 3.99345 317.51 2159.49 2477.00
50 81.33 0.001030 3.23931 3.24034 340.42 2143.43 2483.85
75 91.77 0.001037 2.21607 2.21711 394.29 2112.39 2496.67
100 99.62 0.001043 1.69296 1.69400 417.33 2088.72 2506.06125 105.99 0.001048 1.37385 1.37490 444.16 2069.32 2513.48
150 111.37 0.001053 1.15828 1.15933 466.92 2052.72 2519.64
175 116.06 0.001057 1.00257 1.00363 486.78 2038.12 2524.90
200 120.23 0.001061 0.88467 0.88573 504.47 2025.02 2529.49
225 124.00 0.001064 0.79219 0.79325 520.45 2013.10 2533.56
250 127.43 0.001067 0.71765 0.71871 535.08 2002.14 2537.21
275 130.60 0.001070 0.65624 0.65731 548.57 1991.95 2540.53
300 133.55 0.001073 0.60475 0.60582 561.13 1982.43 2543.55
325 136.30 0.001076 0.56093 0.56201 572.88 1973.46 2546.34
350 138.88 0.001079 0.52317 0.52425 583.93 1964.98 2548.92
375 141.32 0.001081 0.49029 0.49137 594.38 1956.93 2551.31
400 143.63 0.001084 0.46138 0.46246 604.29 1949.26 2553.55
450 147.93 0.001088 0.41289 0.41398 622.75 1934.87 2557.62
500 151.86 0.001093 0.37380 0.37489 639.66 1921.57 2561.23
550 155.48 0.001097 0.34159 0.34268 655.30 1909.17 2564.47
600 158.85 0.001101 0.31457 0.31567 669.88 1897.52 2567.40
650 162.01 0.001104 0.29158 0.29268 683.55 1886.51 2570.06
700 164.97 0.001108 0.27176 0.27286 696.43 1876.07 2572.49
750 167.77 0.001111 0.25449 0.25560 708.62 1866.11 2574.73
800 170.43 0.001115 0.23931 0.24043 720.20 1856.58 2576.79
-
7/24/2019 Thermodynamics Table
27/82
APPENDIX B SI UNITS: THERMODYNAMIC TABLES 781
TABLE B.1.2 (continued)Saturated Water Pressure E ntry
E nthalpy, kJ /kg E ntropy, kJ /kg-K
Press. Temp. Sat. L iquid E vap. Sat. Vapor Sat. L iquid E vap. Sat. Vapor(kPa) (C ) h f h f g hg s f s f g sg
0.6113 0.01 0.00 2501.3 2501.3 0 9.1562 9.1562
1.0 6.98 29.29 2484.89 2514.18 0.1059 8.8697 8.9756
1.5 13.03 54.70 2470.59 2525.30 0.1956 8.6322 8.8278
2.0 17.50 73.47 2460.02 2533.49 0.2607 8.4629 8.7236
2.5 21.08 88.47 2451.56 2540.03 0.3120 8.3311 8.6431
3.0 24.08 101.03 2444.47 2545.50 0.3545 8.2231 8.5775
4.0 28.96 121.44 2432.93 2554.37 0.4226 8.0520 8.4746
5.0 32.88 137.79 2423.66 2561.45 0.4763 7.9187 8.3950
7.5 40.29 168.77 2406.02 2574.79 0.5763 7.6751 8.2514
10 45.81 191.81 2392.82 2584.63 0.6492 7.5010 8.1501
15 53.97 225.91 2373.14 2599.06 0.7548 7.2536 8.0084
20 60.06 251.38 2358.33 2609.70 0.8319 7.0766 7.9085
25 64.97 271.90 2346.29 2618.19 0.8930 6.9383 7.8313
30 69.10 289.21 2336.07 2625.28 0.9439 6.8247 7.7686
40 75.87 317.55 2319.19 2636.74 1.0258 6.6441 7.6700
50 81.33 340.47 2305.40 2645.87 1.0910 6.5029 7.5939
75 91.77 384.36 2278.59 2662.96 1.2129 6.2434 7.4563
100 99.62 417.44 2258.02 2675.46 1.3025 6.0568 7.3593125 105.99 444.30 2241.05 2685.35 1.3739 5.9104 7.2843
150 111.37 467.08 2226.46 2693.54 1.4335 5.7897 7.2232
175 116.06 486.97 2213.57 2700.53 1.4848 5.6868 7.1717
200 120.23 504.68 2201.96 2706.63 1.5300 5.5970 7.1271
225 124.00 520.69 2191.35 2712.04 1.5705 5.5173 7.0878
250 127.43 535.34 2181.55 2716.89 1.6072 5.4455 7.0526
275 130.60 548.87 2172.42 2721.29 1.6407 5.3801 7.0208
300 133.55 561.45 2163.85 2725.30 1.6717 5.3201 6.9918
325 136.30 573.23 2155.76 2728.99 1.7005 5.2646 6.9651
350 138.88 584.31 2148.10 2732.40 1.7274 5.2130 6.9404
375 141.32 594.79 2140.79 2735.58 1.7527 5.1647 6.9174
400 143.63 604.73 2133.81 2738.53 1.7766 5.1193 6.8958
450 147.93 623.24 2120.67 2743.91 1.8206 5.0359 6.8565
500 151.86 640.21 2108.47 2748.67 1.8606 4.9606 6.8212
550 155.48 655.91 2097.04 2752.94 1.8972 4.8920 6.7892
600 158.85 670.54 2086.26 2756.80 1.9311 4.8289 6.7600
650 162.01 684.26 2076.04 2760.30 1.9627 4.7704 6.7330
700 164.97 697.20 2066.30 2763.50 1.9922 4.7158 6.7080
750 167.77 709.45 2056.98 2766.43 2.0199 4.6647 6.6846
800 170.43 721.10 2048.04 2769.13 2.0461 4.6166 6.6627
-
7/24/2019 Thermodynamics Table
28/82
782 APPENDIX B SI UNITS: THERMODYNAMIC TABLES
TABLE B.1.2 (continued)Saturated Water Pressure E ntry
Specific Volume, m3/kg Internal E nergy, kJ /kg
Press. Temp. Sat. L iquid E vap. Sat. Vapor Sat. L iquid E vap. Sat. Vapor(kPa) (C ) vf vf g vg u f u f g ug
850 172.96 0.001118 0.22586 0.22698 731.25 1847.45 2578.69
900 175.38 0.001121 0.21385 0.21497 741.81 1838.65 2580.46
950 177.69 0.001124 0.20306 0.20419 751.94 1830.17 2582.11
1000 179.91 0.001127 0.19332 0.19444 761.67 1821.97 2583.64
1100 184.09 0.001133 0.17639 0.17753 780.08 1806.32 2586.40
1200 187.99 0.001139 0.16220 0.16333 797.27 1791.55 2588.82
1300 191.64 0.001144 0.15011 0.15125 813.42 1777.53 2590.95
1400 195.07 0.001149 0.13969 0.14084 828.68 1764.15 2592.83
1500 198.32 0.001154 0.13062 0.13177 843.14 1751.3 2594.5
1750 205.76 0.001166 0.11232 0.11349 876.44 1721.39 2597.83
2000 212.42 0.001177 0.09845 0.09963 906.42 1693.84 2600.26
2250 218.45 0.001187 0.08756 0.08875 933.81 1668.18 2601.98
2500 223.99 0.001197 0.07878 0.07998 959.09 1644.04 2603.13
2750 229.12 0.001207 0.07154 0.07275 982.65 1621.16 2603.81
3000 233.90 0.001216 0.06546 0.06668 1004.76 1599.34 2604.10
3250 238.38 0.001226 0.06029 0.06152 1025.62 1578.43 2604.04
3500 242.60 0.001235 0.05583 0.05707 1045.41 1558.29 2603.70
4000 250.40 0.001252 0.04853 0.04978 1082.28 1519.99 2602.275000 263.99 0.001286 0.03815 0.03944 1147.78 1449.34 2597.12
6000 275.64 0.001319 0.03112 0.03244 1205.41 1384.27 2589.69
7000 285.88 0.001351 0.02602 0.02737 1257.51 1322.97 2580.48
8000 295.06 0.001384 0.02213 0.02352 1305.54 1264.25 2569.79
9000 303.40 0.001418 0.01907 0.02048 1350.47 1207.28 2557.75
10000 311.06 0.001452 0.01657 0.01803 1393.00 1151.40 2544.41
11000 318.15 0.001489 0.01450 0.01599 1433.68 1096.06 2529.74
12000 324.75 0.001527 0.01274 0.01426 1472.92 1040.76 2513.67
13000 330.93 0.001567 0.01121 0.01278 1511.09 984.99 2496.08
14000 336.75 0.001611 0.00987 0.01149 1548.53 928.23 2476.76
15000 342.24 0.001658 0.00868 0.01034 1585.58 869.85 2455.43
16000 347.43 0.001711 0.00760 0.00931 1622.63 809.07 2431.70
17000 352.37 0.001770 0.00659 0.00836 1660.16 744.80 2404.96
18000 357.06 0.001840 0.00565 0.00749 1698.86 675.42 2374.28
19000 361.54 0.001924 0.00473 0.00666 1739.87 598.18 2338.05
20000 365.81 0.002035 0.00380 0.00583 1785.47 507.58 2293.05
21000 369.89 0.002206 0.00275 0.00495 1841.97 388.74 2230.71
22000 373.80 0.002808 0.00072 0.00353 1973.16 108.24 2081.39
22089 374.14 0.003155 0 0.00315 2029.58 0 2029.58
-
7/24/2019 Thermodynamics Table
29/82
APPENDIX B SI UNITS: THERMODYNAMIC TABLES 783
TABLE B.1.2 (continued)Saturated Water Pressure E ntry
E nthalpy, kJ /kg E ntropy, kJ /kg-K
Press. Temp. Sat. L iquid E vap. Sat. Vapor Sat. L iquid E vap. Sat. Vapor(kPa) (C ) h f h f g hg s f s f g sg
850 172.96 732.20 2039.43 2771.63 2.0709 4.5711 6.6421
900 175.38 742.82 2031.12 2773.94 2.0946 4.5280 6.6225
950 177.69 753.00 2023.08 2776.08 2.1171 4.4869 6.6040
1000 179.91 762.79 2015.29 2778.08 2.1386 4.4478 6.5864
1100 184.09 781.32 2000.36 2781.68 2.1791 4.3744 6.5535
1200 187.99 798.64 1986.19 2784.82 2.2165 4.3067 6.5233
1300 191.64 814.91 1972.67 2787.58 2.2514 4.2438 6.4953
1400 195.07 830.29 1959.72 2790.00 2.2842 4.1850 6.4692
1500 198.32 844.87 1947.28 2792.15 2.3150 4.1298 6.4448
1750 205.76 878.48 1917.95 2796.43 2.3851 4.0044 6.3895
2000 212.42 908.77 1890.74 2799.51 2.4473 3.8935 6.3408
2250 218.45 936.48 1865.19 2801.67 2.5034 3.7938 6.2971
2500 223.99 962.09 1840.98 2803.07 2.5546 3.7028 6.2574
2750 229.12 985.97 1817.89 2803.86 2.6018 3.6190 6.2208
3000 233.90 1008.41 1795.73 2804.14 2.6456 3.5412 6.1869
3250 238.38 1029.60 1774.37 2803.97 2.6866 3.4685 6.1551
3500 242.60 1049.73 1753.70 2803.43 2.7252 3.4000 6.1252
4000 250.40 1087.29 1714.09 2801.38 2.7963 3.2737 6.07005000 263.99 1154.21 1640.12 2794.33 2.9201 3.0532 5.9733
6000 275.64 1213.32 1571.00 2784.33 3.0266 2.8625 5.8891
7000 285.88 1266.97 1505.10 2772.07 3.1210 2.6922 5.8132
8000 295.06 1316.61 1441.33 2757.94 3.2067 2.5365 5.7431
9000 303.40 1363.23 1378.88 2742.11 3.2857 2.3915 5.6771
10000 311.06 1407.53 1317.14 2724.67 3.3595 2.2545 5.6140
11000 318.15 1450.05 1255.55 2705.60 3.4294 2.1233 5.5527
12000 324.75 1491.24 1193.59 2684.83 3.4961 1.9962 5.4923
13000 330.93 1531.46 1130.76 2662.22 3.5604 1.8718 5.4323
14000 336.75 1571.08 1066.47 2637.55 3.6231 1.7485 5.3716
15000 342.24 1610.45 1000.04 2610.49 3.6847 1.6250 5.3097
16000 347.43 1650.00 930.59 2580.59 3.7460 1.4995 5.2454
17000 352.37 1690.25 856.90 2547.15 3.8078 1.3698 5.1776
18000 357.06 1731.97 777.13 2509.09 3.8713 1.2330 5.1044
19000 361.54 1776.43 688.11 2464.54 3.9387 1.0841 5.0227
20000 365.81 1826.18 583.56 2409.74 4.0137 0.9132 4.9269
21000 369.89 1888.30 446.42 2334.72 4.1073 0.6942 4.8015
22000 373.80 2034.92 124.04 2158.97 4.3307 0.1917 4.5224
22089 374.14 2099.26 0 2099.26 4.4297 0 4.4297
-
7/24/2019 Thermodynamics Table
30/82
784 APPENDIX B SI UNITS: THERMODYNAMIC TABLES
TABLE B.1.3
Superheated Vapor Water
Temp. v u h s v u h s(C ) (m3/kg) (kJ /kg) (kJ /kg) (kJ /kg-K ) (m3/kg) (kJ /kg) (kJ /kg) (kJ /kg-K )
P = 10kPa(45.81C) P = 50kPa(81.33C)
Sat. 14.67355 2437.89 2584.63 8.1501 3.24034 2483.85 2645.87 7.5939
50 14.86920 2443.87 2592.56 8.1749
100 17.19561 2515.50 2687.46 8.4479 3.41833 2511.61 2682.52 7.6947
150 19.51251 2587.86 2782.99 8.6881 3.88937 2585.61 2780.08 7.9400
200 21.82507 2661.27 2879.52 8.9037 4.35595 2659.85 2877.64 8.1579
250 24.13559 2735.95 2977.31 9.1002 4.82045 2734.97 2975.99 8.3555300 26.44508 2812.06 3076.51 9.2812 5.28391 2811.33 3075.52 8.5372
400 31.06252 2968.89 3279.51 9.6076 6.20929 2968.43 3278.89 8.8641
500 35.67896 3132.26 3489.05 9.8977 7.13364 3131.94 3488.62 9.1545
600 40.29488 3302.45 3705.40 10.1608 8.05748 3302.22 3705.10 9.4177
700 44.91052 3479.63 3928.73 10.4028 8.98104 3479.45 3928.51 9.6599
800 49.52599 3663.84 4159.10 10.6281 9.90444 3663.70 4158.92 9.8852
900 54.14137 3855.03 4396.44 10.8395 10.82773 3854.91 4396.30 10.0967
1000 58.75669 4053.01 4640.58 11.0392 11.75097 4052.91 4640.46 10.2964
1100 63.37198 4257.47 4891.19 11.2287 12.67418 4257.37 4891.08 10.4858
1200 67.98724 4467.91 5147.78 11.4090 13.59737 4467.82 5147.69 10.6662
1300 72.60250 4683.68 5409.70 14.5810 14.52054 4683.58 5409.61 10.8382
100 kPa(99.62C) 200 kPa(120.23C)
Sat. 1.69400 2506.06 2675.46 7.3593 0.88573 2529.49 2706.63 7.1271
150 1.93636 2582.75 2776.38 7.6133 0.95964 2576.87 2768.80 7.2795
200 2.17226 2658.05 2875.27 7.8342 1.08034 2654.39 2870.46 7.5066
250 2.40604 2733.73 2974.33 8.0332 1.19880 2731.22 2970.98 7.7085
300 2.63876 2810.41 3074.28 8.2157 1.31616 2808.55 3071.79 7.8926
400 3.10263 2967.85 3278.11 8.5434 1.54930 2966.69 3276.55 8.2217
500 3.56547 3131.54 3488.09 8.8341 1.78139 3130.75 3487.03 8.5132
600 4.02781 3301.94 3704.72 9.0975 2.01297 3301.36 3703.96 8.7769
700 4.48986 3479.24 3928.23 9.3398 2.24426 3478.81 3927.66 9.0194
800 4.95174 3663.53 4158.71 9.5652 2.47539 3663.19 4158.27 9.2450
900 5.41353 3854.77 4396.12 9.7767 2.70643 3854.49 4395.77 9.4565
1000 5.87526 4052.78 4640.31 9.9764 2.93740 4052.53 4640.01 9.6563
1100 6.33696 4257.25 4890.95 10.1658 3.16834 4257.01 4890.68 9.8458
1200 6.79863 4467.70 5147.56 10.3462 3.39927 4467.46 5147.32 10.0262
1300 7.26030 4683.47 5409.49 10.5182 3.63018 4683.23 5409.26 10.1982
300 kPa(133.55C) 400 kPa(143.63C)
Sat. 0.60582 2543.55 2725.30 6.9918 0.46246 2553.55 2738.53 6.8958
150 0.63388 2570.79 2760.95 7.0778 0.47084 2564.48 2752.82 6.9299
200 0.71629 2650.65 2865.54 7.3115 0.53422 2646.83 2860.51 7.1706
-
7/24/2019 Thermodynamics Table
31/82
APPENDIX B SI UNITS: THERMODYNAMIC TABLES 785
TABLE B.1.3 (continued)Superheated Vapor Water
Temp. v u h s v u h s(C ) (m3/kg) (kJ /kg) (kJ /kg) (kJ /kg-K ) (m3/kg) (kJ /kg) (kJ /kg) (kJ /kg-K )
300 kPa(133.55C) 400 kPa(143.63C)
250 0.79636 2728.69 2967.59 7.5165 0.59512 2726.11 2964.16 7.3788
300 0.87529 2806.69 3069.28 7.7022 0.65484 2804.81 3066.75 7.5661
400 1.03151 2965.53 3274.98 8.0329 0.77262 2964.36 3273.41 7.8984
500 1.18669 3129.95 3485.96 8.3250 0.88934 3129.15 3484.89 8.1912
600 1.34136 3300.79 3703.20 8.5892 1.00555 3300.22 3702.44 8.4557
700 1.49573 3478.38 3927.10 8.8319 1.12147 3477.95 3926.53 8.6987
800 1.64994 3662.85 4157.83 9.0575 1.23722 3662.51 4157.40 8.9244
900 1.80406 3854.20 4395.42 9.2691 1.35288 3853.91 4395.06 9.1361
1000 1.95812 4052.27 4639.71 9.4689 1.46847 4052.02 4639.41 9.3360
1100 2.11214 4256.77 4890.41 9.6585 1.58404 4256.53 4890.15 9.5255
1200 2.26614 4467.23 5147.07 9.8389 1.69958 4466.99 5146.83 9.7059
1300 2.42013 4682.99 5409.03 10.0109 1.81511 4682.75 5408.80 9.8780
500 kPa(151.86C) 600 kPa(158.85C)
Sat. 0.37489 2561.23 2748.67 6.8212 0.31567 2567.40 2756.80 6.7600
200 0.42492 2642.91 2855.37 7.0592 0.35202 2638.91 2850.12 6.9665
250 0.47436 2723.50 2960.68 7.2708 0.39383 2720.86 2957.16 7.1816
300 0.52256 2802.91 3064.20 7.4598 0.43437 2801.00 3061.63 7.3723350 0.57012 2882.59 3167.65 7.6328 0.47424 2881.12 3165.66 7.5463
400 0.61728 2963.19 3271.83 7.7937 0.51372 2962.02 3270.25 7.7078
500 0.71093 3128.35 3483.82 8.0872 0.59199 3127.55 3482.75 8.0020
600 0.80406 3299.64 3701.67 8.3521 0.66974 3299.07 3700.91 8.2673
700 0.89691 3477.52 3925.97 8.5952 0.74720 3477.08 3925.41 8.5107
800 0.98959 3662.17 4156.96 8.8211 0.82450 3661.83 4156.52 8.7367
900 1.08217 3853.63 4394.71 9.0329 0.90169 3853.34 4394.36 8.9485
1000 1.17469 4051.76 4639.11 9.2328 0.97883 4051.51 4638.81 9.1484
1100 1.26718 4256.29 4889.88 9.4224 1.05594 4256.05 4889.61 9.3381
1200 1.35964 4466.76 5146.58 9.6028 1.13302 4466.52 5146.34 9.5185
1300 1.45210 4682.52 5408.57 9.7749 1.21009 4682.28 5408.34 9.6906
800 kPa(170.43C) 1000 kPa(179.91C)
Sat. 0.24043 2576.79 2769.13 6.6627 0.19444 2583.64 2778.08 6.5864
200 0.26080 2630.61 2839.25 6.8158 0.20596 2621.90 2827.86 6.6939
250 0.29314 2715.46 2949.97 7.0384 0.23268 2709.91 2942.59 6.9246
300 0.32411 2797.14 3056.43 7.2327 0.25794 2793.21 3051.15 7.1228
350 0.35439 2878.16 3161.68 7.4088 0.28247 2875.18 3157.65 7.3010
400 0.38426 2959.66 3267.07 7.5715 0.30659 2957.29 3263.88 7.4650
500 0.44331 3125.95 3480.60 7.8672 0.35411 3124.34 3478.44 7.7621
600 0.50184 3297.91 3699.38 8.1332 0.40109 3296.76 3697.85 8.0289
-
7/24/2019 Thermodynamics Table
32/82
786 APPENDIX B SI UNITS: THERMODYNAMIC TABLES
TABLE B.1.3 (continued)Superheated Vapor Water
Temp. v u h s v u h s(C ) (m3/kg) (kJ /kg) (kJ /kg) (kJ /kg-K ) (m3/kg) (kJ /kg) (kJ /kg) (kJ /kg-K )
800 kPa(170.43C) 1000 kPa(179.91C)
700 0.56007 3476.22 3924.27 8.3770 0.44779 3475.35 3923.14 8.2731
800 0.61813 3661.14 4155.65 8.6033 0.49432 3660.46 4154.78 8.4996
900 0.67610 3852.77 4393.65 8.8153 0.54075 3852.19 4392.94 8.7118
1000 0.73401 4051.00 4638.20 9.0153 0.58712 4050.49 4637.60 8.9119
1100 0.79188 4255.57 4889.08 9.2049 0.63345 4255.09 4888.55 9.1016
1200 0.84974 4466.05 5145.85 9.3854 0.67977 4465.58 5145.36 9.2821
1300 0.90758 4681.81 5407.87 9.5575 0.72608 4681.33 5407.41 9.4542
1200kPa(187.99C) 1400 kPa(195.07C)
Sat. 0.16333 2588.82 2784.82 6.5233 0.14084 2592.83 2790.00 6.4692
200 0.16930 2612.74 2815.90 6.5898 0.14302 2603.09 2803.32 6.4975
250 0.19235 2704.20 2935.01 6.8293 0.16350 2698.32 2927.22 6.7467
300 0.21382 2789.22 3045.80 7.0316 0.18228 2785.16 3040.35 6.9533
350 0.23452 2872.16 3153.59 7.2120 0.20026 2869.12 3149.49 7.1359
400 0.25480 2954.90 3260.66 7.3773 0.21780 2952.50 3257.42 7.3025
500 0.29463 3122.72 3476.28 7.6758 0.25215 3121.10 3474.11 7.6026
600 0.33393 3295.60 3696.32 7.9434 0.28596 3294.44 3694.78 7.8710
700 0.37294 3474.48 3922.01 8.1881 0.31947 3473.61 3920.87 8.1160800 0.41177 3659.77 4153.90 8.4149 0.35281 3659.09 4153.03 8.3431
900 0.45051 3851.62 4392.23 8.6272 0.38606 3851.05 4391.53 8.5555
1000 0.48919 4049.98 4637.00 8.8274 0.41924 4049.47 4636.41 8.7558
1100 0.52783 4254.61 4888.02 9.0171 0.45239 4254.14 4887.49 8.9456
1200 0.56646 4465.12 5144.87 9.1977 0.48552 4464.65 5144.38 9.1262
1300 0.60507 4680.86 5406.95 9.3698 0.51864 4680.39 5406.49 9.2983
1600kPa (201.40)C) 1800 kPa(207.15C)
Sat. 0.12380 2595.95 2794.02 6.4217 0.11042 2598.38 2797.13 6.3793
250 0.14184 2692.26 2919.20 6.6732 0.12497 2686.02 2910.96 6.6066
300 0.15862 2781.03 3034.83 6.8844 0.14021 2776.83 3029.21 6.8226
350 0.17456 2866.05 3145.35 7.0693 0.15457 2862.95 3141.18 7.0099
400 0.19005 2950.09 3254.17 7.2373 0.16847 2947.66 3250.90 7.1793
500 0.22029 3119.47 3471.93 7.5389 0.19550 3117.84 3469.75 7.4824
600 0.24998 3293.27 3693.23 7.8080 0.22199 3292.10 3691.69 7.7523
700 0.27937 3472.74 3919.73 8.0535 0.24818 3471.87 3918.59 7.9983
800 0.30859 3658.40 4152.15 8.2808 0.27420 3657.71 4151.27 8.2258
900 0.33772 3850.47 4390.82 8.4934 0.30012 3849.90 4390.11 8.4386
1000 0.36678 4048.96 4635.81 8.6938 0.32598 4048.45 4635.21 8.6390
1100 0.39581 4253.66 4886.95 8.8837 0.35180 4253.18 4886.42 8.8290
1200 0.42482 4464.18 5143.89 9.0642 0.37761 4463.71 5143.40 9.0096
1300 0.45382 4679.92 5406.02 9.2364 0.40340 4679.44 5405.56 9.1817
-
7/24/2019 Thermodynamics Table
33/82
APPENDIX B SI UNITS: THERMODYNAMIC TABLES 787
TABLE B.1.3 (continued)Superheated Vapor Water
Temp. v u h s v u h s(C ) (m3/kg) (kJ /kg) (kJ /kg) (kJ /kg-K ) (m3/kg) (kJ /kg) (kJ /kg) (kJ /kg-K )
2000kPa(212.42C) 2500 kPa(223.99C)
Sat. 0.09963 2600.26 2799.51 6.3408 0.07998 2603.13 2803.07 6.2574
250 0.11144 2679.58 2902.46 6.5452 0.08700 2662.55 2880.06 6.4084
300 0.12547 2772.56 3023.50 6.7663 0.09890 2761.56 3008.81 6.6437
350 0.13857 2859.81 3136.96 6.9562 0.10976 2851.84 3126.24 6.8402
400 0.15120 2945.21 3247.60 7.1270 0.12010 2939.03 3239.28 7.0147
450 0.16353 3030.41 3357.48 7.2844 0.13014 3025.43 3350.77 7.1745
500 0.17568 3116.20 3467.55 7.4316 0.13998 3112.08 3462.04 7.3233
600 0.19960 3290.93 3690.14 7.7023 0.15930 3287.99 3686.25 7.5960
700 0.22323 3470.99 3917.45 7.9487 0.17832 3468.80 3914.59 7.8435
800 0.24668 3657.03 4150.40 8.1766 0.19716 3655.30 4148.20 8.0720
900 0.27004 3849.33 4389.40 8.3895 0.21590 3847.89 4387.64 8.2853
1000 0.29333 4047.94 4634.61 8.5900 0.23458 4046.67 4633.12 8.4860
1100 0.31659 4252.71 4885.89 8.7800 0.25322 4251.52 4884.57 8.6761
1200 0.33984 4463.25 5142.92 8.9606 0.27185 4462.08 5141.70 8.8569
1300 0.36306 4678.97 5405.10 9.1328 0.29046 4677.80 5403.95 9.0291
3000kPa(233.90C) 4000 kPa(250.40C)
Sat. 0.06668 2604.10 2804.14 6.1869 0.04978 2602.27 2801.38 6.0700250 0.07058 2644.00 2855.75 6.2871
300 0.08114 2750.05 2993.48 6.5389 0.05884 2725.33 2960.68 6.3614
350 0.09053 2843.66 3115.25 6.7427 0.06645 2826.65 3092.43 6.5820
400 0.09936 2932.75 3230.82 6.9211 0.07341 2919.88 3213.51 6.7689
450 0.10787 3020.38 3344.00 7.0833 0.08003 3010.13 3330.23 6.9362
500 0.11619 3107.92 3456.48 7.2337 0.08643 3099.49 3445.21 7.0900
600 0.13243 3285.03 3682.34 7.5084 0.09885 3279.06 3674.44 7.3688
700 0.14838 3466.59 3911.72 7.7571 0.11095 3462.15 3905.94 7.6198
800 0.16414 3653.58 4146.00 7.9862 0.12287 3650.11 4141.59 7.8502
900 0.17980 3846.46 4385.87 8.1999 0.13469 3843.59 4382.34 8.0647
1000 0.19541 4045.40 4631.63 8.4009 0.14645 4042.87 4628.65 8.2661
1100 0.21098 4250.33 4883.26 8.5911 0.15817 4247.96 4880.63 8.4566
1200 0.22652 4460.92 5140.49 8.7719 0.16987 4458.60 5138.07 8.6376
1300 0.24206 4676.63 5402.81 8.9442 0.18156 4674.29 5400.52 8.8099
-
7/24/2019 Thermodynamics Table
34/82
788 APPENDIX B SI UNITS: THERMODYNAMIC TABLES
TABLE B.1.3 (continued)Superheated Vapor Water
Temp. v u h s v u h s(C ) (m3/kg) (kJ /kg) (kJ /kg) (kJ /kg-K ) (m3/kg) (kJ /kg) (kJ /kg) (kJ /kg-K )
5000kPa(263.99C) 6000 kPa(275.64C)
Sat. 0.03944 2597.12 2794.33 5.9733 0.03244 2589.69 2784.33 5.8891
300 0.04532 2697.94 2924.53 6.2083 0.03616 2667.22 2884.19 6.0673
350 0.05194 2808.67 3068.39 6.4492 0.04223 2789.61 3042.97 6.3334
400 0.05781 2906.58 3195.64 6.6458 0.04739 2892.81 3177.17 6.5407
450 0.06330 2999.64 3316.15 6.8185 0.05214 2988.90 3301.76 6.7192
500 0.06857 3090.92 3433.76 6.9758 0.05665 3082.20 3422.12 6.8802
550 0.07368 3181.82 3550.23 7.1217 0.06101 3174.57 3540.62 7.0287
600 0.07869 3273.01 3666.47 7.2588 0.06525 3266.89 3658.40 7.1676
700 0.08849 3457.67 3900.13 7.5122 0.07352 3453.15 3894.28 7.4234
800 0.09811 3646.62 4137.17 7.7440 0.08160 3643.12 4132.74 7.6566
900 0.10762 3840.71 4378.82 7.9593 0.08958 3837.84 4375.29 7.8727
1000 0.11707 4040.35 4625.69 8.1612 0.09749 4037.83 4622.74 8.0751
1100 0.12648 4245.61 4878.02 8.3519 0.10536 4243.26 4875.42 8.2661
1200 0.13587 4456.30 5135.67 8.5330 0.11321 4454.00 5133.28 8.4473
1300 0.14526 4671.96 5398.24 8.7055 0.12106 4669.64 5395.97 8.6199
8000kPa(295.06C) 10000 kPa(311.06C)
Sat. 0.02352 2569.79 2757.94 5.7431 0.01803 2544.41 2724.67 5.6140300 0.02426 2590.93 2784.98 5.7905
350 0.02995 2747.67 2987.30 6.1300 0.02242 2699.16 2923.39 5.9442
400 0.03432 2863.75 3138.28 6.3633 0.02641 2832.38 3096.46 6.2119
450 0.03817 2966.66 3271.99 6.5550 0.02975 2943.32 3240.83 6.4189
500 0.04175 3064.30 3398.27 6.7239 0.03279 3045.77 3373.63 6.5965
550 0.04516 3159.76 3521.01 6.8778 0.03564 3144.54 3500.92 6.7561
600 0.04845 3254.43 3642.03 7.0205 0.03837 3241.68 3625.34 6.9028
700 0.05481 3444.00 3882.47 7.2812 0.04358 3434.72 3870.52 7.1687
800 0.06097 3636.08 4123.84 7.5173 0.04859 3628.97 4114.91 7.4077
900 0.06702 3832.08 4368.26 7.7350 0.05349 3826.32 4361.24 7.6272
1000 0.07301 4032.81 4616.87 7.9384 0.05832 4027.81 4611.04 7.8315
1100 0.07896 4238.60 4870.25 8.1299 0.06312 4233.97 4865.14 8.0236
1200 0.08489 4449.45 5128.54 8.3115 0.06789 4444.93 5123.84 8.2054
1300 0.09080 4665.02 5391.46 8.4842 0.07265 4660.44 5386.99 8.3783
-
7/24/2019 Thermodynamics Table
35/82
APPENDIX B SI UNITS: THERMODYNAMIC TABLES 789
TABLE B.1.3 (continued)Superheated Vapor Water
Temp. v u h s v u h s(C ) (m3/kg) (kJ /kg) (kJ /kg) (kJ /kg-K ) (m3/kg) (kJ /kg) (kJ /kg) (kJ /kg-K )
15000 kPa (342.24C) 20000 kPa(365.81C)
Sat. 0.01034 2455.43 2610.49 5.3097 0.00583 2293.05 2409.74 4.9269
350 0.01147 2520.36 2692.41 5.4420
400 0.01565 2740.70 2975.44 5.8810 0.00994 2619.22 2818.07 5.5539
450 0.01845 2879.47 3156.15 6.1403 0.01270 2806.16 3060.06 5.9016
500 0.02080 2996.52 3308.53 6.3442 0.01477 2942.82 3238.18 6.1400
550 0.02293 3104.71 3448.61 6.5198 0.01656 3062.34 3393.45 6.3347
600 0.02491 3208.64 3582.30 6.6775 0.01818 3174.00 3537.57 6.5048
650 0.02680 3310.37 3712.32 6.8223 0.01969 3281.46 3675.32 6.6582
700 0.02861 3410.94 3840.12 6.9572 0.02113 3386.46 3809.09 6.7993
800 0.03210 3610.99 4092.43 7.2040 0.02385 3592.73 4069.80 7.0544
900 0.03546 3811.89 4343.75 7.4279 0.02645 3797.44 4326.37 7.2830
1000 0.03875 4015.41 4596.63 7.6347 0.02897 4003.12 4582.45 7.4925
1100 0.04200 4222.55 4852.56 7.8282 0.03145 4211.30 4840.24 7.6874
1200 0.04523 4433.78 5112.27 8.0108 0.03391 4422.81 5100.96 7.8706
1300 0.04845 4649.12 5375.94 8.1839 0.03636 4637.95 5365.10 8.0441
30000 kPa 40000 kPa
375 0.001789 1737.75 1791.43 3.9303 0.001641 1677.09 1742.71 3.8289400 0.002790 2067.34 2151.04 4.4728 0.001908 1854.52 1930.83 4.1134
425 0.005304 2455.06 2614.17 5.1503 0.002532 2096.83 2198.11 4.5028
450 0.006735 2619.30 2821.35 5.4423 0.003693 2365.07 2512.79 4.9459
500 0.008679 2820.67 3081.03 5.7904 0.005623 2678.36 2903.26 5.4699
550 0.010168 2970.31 3275.36 6.0342 0.006984 2869.69 3149.05 5.7784
600 0.011446 3100.53 3443.91 6.2330 0.008094 3022.61 3346.38 6.0113
650 0.012596 3221.04 3598.93 6.4057 0.009064 3158.04 3520.58 6.2054
700 0.013661 3335.84 3745.67 6.5606 0.009942 3283.63 3681.29 6.3750
800 0.015623 3555.60 4024.31 6.8332 0.011523 3517.89 3978.80 6.6662
900 0.017448 3768.48 4291.93 7.0717 0.012963 3739.42 4257.93 6.9150
1000 0.019196 3978.79 4554.68 7.2867 0.014324 3954.64 4527.59 7.1356
1100 0.020903 4189.18 4816.28 7.4845 0.015643 4167.38 4793.08 7.3364
1200 0.022589 4401.29 5078.97 7.6691 0.016940 4380.11 5057.72 7.5224
1300 0.024266 4615.96 5343.95 7.8432 0.018229 4594.28 5323.45 7.6969
-
7/24/2019 Thermodynamics Table
36/82
790 APPENDIX B SI UNITS: THERMODYNAMIC TABLES
TABLE B.1.4
C ompressed L iquid Water
Temp. v u h s v u h s(C ) (m3/kg) (kJ /kg) (kJ /kg) (kJ /kg-K ) (m3/kg) (kJ /kg) (kJ /kg) (kJ /kg-K )
500 kPa(151.86C) 2000 kPa(212.42C)
Sat. 0.001093 639.66 640.21 1.8606 0.001177 906.42 908.77 2.4473
0.01 0.000999 0.01 0.51 0.0000 0.000999 0.03 2.03 0.0001
20 0.001002 83.91 84.41 0.2965 0.001001 83.82 85.82 .2962
40 0.001008 167.47 167.98 0.5722 0.001007 167.29 169.30 .5716
60 0.001017 251.00 251.51 0.8308 0.001016 250.73 252.77 .8300
80 0.001029 334.73 335.24 1.0749 0.001028 334.38 336.44 1.0739
100 0.001043 418.80 419.32 1.3065 0.001043 418.36 420.45 1.3053
120 0.001060 503.37 503.90 1.5273 0.001059 502.84 504.96 1.5259
140 0.001080 588.66 589.20 1.7389 0.001079 588.02 590.18 1.7373
160 0.001101 674.14 676.34 1.9410
180 0.001127 761.46 763.71 2.1382
200 0.001156 850.30 852.61 2.3301
5000kPa(263.99C) 10000 kPa(311.06C)
Sat 0.001286 1147.78 1154.21 2.9201 0.001452 1393.00 1407.53 3.3595
0 0.000998 0.03 5.02 0.0001 0.000995 0.10 10.05 0.0003
20 0.001000 83.64 88.64 0.2955 0.000997 83.35 93.32 0.2945
40 0.001006 166.93 171.95 0.5705 0.001003 166.33 176.36 0.568560 0.001015 250.21 255.28 0.8284 0.001013 249.34 259.47 0.8258
80 0.001027 333.69 338.83 1.0719 0.001025 332.56 342.81 1.0687
100 0.001041 417.50 422.71 1.3030 0.001039 416.09 426.48 1.2992
120 0.001058 501.79 507.07 1.5232 0.001055 500.07 510.61 1.5188
140 0.001077 586.74 592.13 1.7342 0.001074 584.67 595.40 1.7291
160 0.001099 672.61 678.10 1.9374 0.001195 670.11 681.07 1.9316
180 0.001124 759.62 765.24 2.1341 0.001120 756.63 767.83 2.1274
200 0.001153 848.08 853.85 2.3254 0.001148 844.49 855.97 2.3178
220 0.001187 938.43 944.36 2.5128 0.001181 934.07 945.88 2.5038
240 0.001226 1031.34 1037.47 2.6978 0.001219 1025.94 1038.13 2.6872
260 0.001275 1127.92 1134.30 2.8829 0.001265 1121.03 1133.68 2.8698
280 0.001322 1220.90 1234.11 3.0547
300 0.001397 1328.34 1342.31 3.2468
-
7/24/2019 Thermodynamics Table
37/82
APPENDIX B SI UNITS: THERMODYNAMIC TABLES 791
TABLE B.1.4 (continued)C ompressed L iquid Water
Temp. v u h s v u h s(C ) (m3/kg) (kJ /kg) (kJ /kg) (kJ /kg-K ) (m3/kg) (kJ /kg) (kJ /kg) (kJ /kg-K )
15000 kPa (342.24C) 20000 kPa(365.81C)
Sat. 0.001658 1585.58 1610.45 3.6847 0.002035 1785.47 1826.18 4.0137
0 0.000993 0.15 15.04 0.0004 0.000990 0.20 20.00 0.0004
20 0.000995 83.05 97.97 0.2934 0.000993 82.75 102.61 0.2922
40 0.001001 165.73 180.75 0.5665 0.000999 165.15 185.14 0.5646
60 0.001011 248.49 263.65 0.8231 0.001008 247.66 267.82 0.8205
80 0.001022 331.46 346.79 1.0655 0.001020 330.38 350.78 1.0623
100 0.001036 414.72 430.26 1.2954 0.001034 413.37 434.04 1.2917120 0.001052 498.39 514.17 1.5144 0.001050 496.75 517.74 1.5101
140 0.001071 582.64 598.70 1.7241 0.001068 580.67 602.03 1.7192
160 0.001092 667.69 684.07 1.9259 0.001089 665.34 687.11 1.9203
180 0.001116 753.74 770.48 2.1209 0.001112 750.94 773.18 2.1146
200 0.001143 841.04 858.18 2.3103 0.001139 837.70 860.47 2.3031
220 0.001175 929.89 947.52 2.4952 0.001169 925.89 949.27 2.4869
240 0.001211 1020.82 1038.99 2.6770 0.001205 1015.94 1040.04 2.6673
260 0.001255 1114.59 1133.41 2.8575 0.001246 1108.53 1133.45 2.8459
280 0.001308 1212.47 1232.09 3.0392 0.001297 1204.69 1230.62 3.0248
300 0.001377 1316.58 1337.23 3.2259 0.001360 1306.10 1333.29 3.2071
320 0.001472 1431.05 1453.13 3.4246 0.001444 1415.66 1444.53 3.3978
340 0.001631 1567.42 1591.88 3.6545 0.001568 1539.64 1571.01 3.6074
360 0.001823 1702.78 1739.23 3.8770
30000 kPa 50000 kPa
0 0.000986 0.25 29.82 0.0001 0.000977 0.20 49.03 0.0014
20 0.000989 82.16 111.82 0.2898 0.000980 80.98 130.00 0.2847
40 0.000995 164.01 193.87 0.5606 0.000987 161.84 211.20 0.5526
60 0.001004 246.03 276.16 0.8153 0.000996 242.96 292.77 0.8051
80 0.001016 328.28 358.75 1.0561 0.001007 324.32 374.68 1.0439
100 0.001029 410.76 441.63 1.2844 0.001020 405.86 456.87 1.2703
120 0.001044 493.58 524.91 1.5017 0.001035 487.63 539.37 1.4857
140 0.001062 576.86 608.73 1.7097 0.001052 569.76 622.33 1.6915
160 0.001082 660.81 693.27 1.9095 0.001070 652.39 705.91 1.8890
180 0.001105 745.57 778.71 2.1024 0.001091 735.68 790.24 2.0793
200 0.001130 831.34 865.24 2.2892 0.001115 819.73 875.46 2.2634
220 0.001159 918.32 953.09 2.4710 0.001141 904.67 961.71 2.4419
240 0.001192 1006.84 1042.60 2.6489 0.001170 990.69 1049.20 2.6158
260 0.001230 1097.38 1134.29 2.8242 0.001203 1078.06 1138.23 2.7860
280 0.001275 1190.69 1228.96 2.9985 0.001242 1167.19 1229.26 2.9536
300 0.001330 1287.89 1327.80 3.1740 0.001286 1258.66 1322.95 3.1200
320 0.001400 1390.64 1432.63 3.3538 0.001339 1353.23 1420.17 3.2867
340 0.001492 1501.71 1546.47 3.5425 0.001403 1451.91 1522.07 3.4556
360 0.001627 1626.57 1675.36 3.7492 0.001484 1555.97 1630.16 3.6290
380 0.001869 1781.35 1837.43 4.0010 0.001588 1667.13 1746.54 3.8100
-
7/24/2019 Thermodynamics Table
38/82
792 APPENDIX B SI UNITS: THERMODYNAMIC TABLES
TABLE B.1.5
Saturated Solid-Saturated Vapor, Water
Specific Volume, m3/kg Internal E nergy, kJ /kg
Temp. Press. Sat. Solid E vap. Sat. Vapor Sat. Solid E vap. Sat. Vapor(C ) (kPa) vi vi g vg ui ui g ug
0.01 0.6113 0.0010908 206.152 206.153 333.40 2708.7 2375.3
0 0.6108 0.0010908 206.314 206.315 333.42 2708.7 2375.3
2 0.5177 0.0010905 241.662 241.663 337.61 2710.2 2372.5
4 0.4376 0.0010901 283.798 283.799 341.78 2711.5 2369.8
6 0.3689 0.0010898 334.138 334.139 345.91 2712.9 2367.0
8 0.3102 0.0010894 394.413 394.414 350.02 2714.2 2364.2
10 0.2601 0.0010891 466.756 466.757 354.09 2715.5 2361.4
12 0.2176 0.0010888 553.802 553.803 358.14 2716.8 2358.7
14 0.1815 0.0010884 658.824 658.824 362.16 2718.0 2355.9
16 0.1510 0.0010881 785.906 785.907 366.14 2719.2 2353.1
18 0.1252 0.0010878 940.182 940.183 370.10 2720.4 2350.3
20 0.10355 0.0010874 1128.112 1128.113 374.03 2721.6