Contents of Appendix
A
SI UNITS: SINGLE-STATE PROPERTIES
755
Table A.1 Conversion Factors, 755
Table A.2 Critical Constants, 758
Table A.3 Properties of Selected Solids at 25◦ C, 759
Table A.4 Properties of Some Liquids at 25◦ C, 759
Table A.5 Properties of Various Ideal Gases at 25 ◦ C, 100 kPa (SI Units), 760
Table A.6 Constant-Pressure Specific Heats of Various Ideal Gases, 761
Table A7.1 Ideal Gas Properties of Air, Standard Entropy at 0.1-MPa (1-Bar)
Pressure, 762
Table A7.2 The Isentropic Relative Pressure and Relative Volume Functions, 763
Table A.8 Ideal Gas Properties of Various Substances, Entropies at 0.1-MPa
(1-Bar) Pressure, Mass Basis, 764
Table A.9 Ideal Gas Properties of Various Substances (SI Units), Entropies
at 0.1-MPa (1-Bar) Pressure, Mole Basis, 766
Table A.10 Enthalpy of Formation and Absolute Entropy of Various Substances
at 25◦ C, 100 kPa Pressure, 772
Table A.11 Logarithms to the Base e of the Equilibrium Constant K, 773
B
SI UNITS: THERMODYNAMIC TABLES
775
Table B.1 Thermodynamic Properties of Water, 776
Table B.2 Thermodynamic Properties of Ammonia, 794
Table B.3 Thermodynamic Properties of Carbon Dioxide, 800
Table B.4 Thermodynamic Properties of R-410a, 804
Table B.5 Thermodynamic Properties of R-134a, 810
Table B.6 Thermodynamic Properties of Nitrogen, 816
Table B.7 Thermodynamic Properties of Methane, 820
C
D
IDEAL GAS SPECIFIC HEAT
825
EQUATIONS OF STATE
827
Table D.1 Equations of State, 827
Table D.2 The Lee–Kesler Equation of State, 828
Table D.3 Saturated Liquid–Vapor Compressibilities, Lee–Kesler Simple
Fluid, 828
Table D.4 Acentric Factor for Some Substances, 828
Figure D.1 Lee–Kesler Simple Fluid Compressibility Factor, 829
Figure D.2 Lee–Kesler Simple Fluid Enthalpy Departure, 830
Figure D.3 Lee–Kesler Simple Fluid Entropy Departure, 831
753
⑦
CONTENTS OF APPENDIX
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E
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FIGURES
832
Figure E.1 Temperature–Entropy Diagram for Water, 833
Figure E.2 Pressure–Enthalpy Diagram for Ammonia, 834
Figure E.3 Pressure–Enthalpy Diagram for Oxygen, 835
Figure E.4 Psychrometric Chart, 836
F
ENGLISH UNIT TABLES
837
Table F.1 Critical Constants (English Units), 838
Table F.2 Properties of Selected Solids at 77 F, 839
Table F.3 Properties of Some Liquids at 77 F, 839
Table F.4 Properties of Various Ideal Gases at 77 F, 1 atm (English Units), 840
Table F.5 Ideal Gas Properties of Air (English Units), Standard Entropy at
1 atm = 101.325 kPa = 14.696 lbf/in.2 , 841
Table F.6 Ideal Gas Properties of Various Substances (English Units), Entropies
at 1 atm Pressure, 842
Table F.7 Thermodynamic Properties of Water, 848
Table F.8 Thermodynamic Properties of Ammonia, 859
Table F.9 Thermodynamic Properties of R-410a, 865
Table F.10 Thermodynamic Properties of R-134a, 871
Table F.11 Enthalpy of Formation and Absolute Entropy of Various Substances
at 77 F, 1 atm Pressure, 877
APPEN
TABLE A.1
Conversion Factors
Area (A)
1 mm2 = 1.0 × 10−6 m2
1 cm 2 = 1.0 × 10−4 m2 = 0.1550 in.2
1 m2 = 10.7639 ft2
1 ft2 = 144 in.2
1 in.2 = 6.4516 cm2 = 6.4516 × 10−4 m2
1 ft2 = 0.092 903 m2
Conductivity (k)
1 W/m-K = 1 J/s-m-K
= 0.577 789 Btu/h-ft-◦ R
1 Btu/h-ft-R = 1.730 735 W/m-K
Density (ρ)
1 kg/m3 = 0.06242797 lbm/ft3
1 g/cm3 = 1000 kg/m3
1 g/cm3 = 1 kg/L
Energy (E, U)
1J
= 1 N-m = 1 kg-m2 /s2
1J
= 0.737 562 lbf-ft
1 cal (Int.) = 4.186 81 J
1 erg
1 eV
= 1.0 × 10−7 J
= 1.602 177 33 × 10−19 J
Force (F)
1 N = 0.224 809 lbf
1 kp = 9.806 65 N (1 kgf)
1 lbm/ft3 = 16.018 46 kg/m3
l lbf-ft = 1.355 818 J
= 1.285 07 × 10−3 Btu
1 Btu (Int.) = 1.055 056 kJ
= 778.1693 lbf-ft
1 lbf = 4.448 222 N
Gravitation
g = 9.806 65 m/s2
g = 32.174 05 ft/s2
Heat capacity (C p , C v , C), specific entropy (s)
1 kJ/kg-K = 0.238 846 Btu/lbm-◦ R
1 Btu/lbm-◦ R = 4.1868 kJ/kg-K
Heat flux (per unit area)
1 W/m2 = 0.316 998 Btu/h-ft2
1 Btu/h-ft2 = 3.154 59 W/m2
755
X
A
DI
SI Units: Single-State
Properties
⑦
APPENDIX A
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............................................................................................................
TABLE A.1 (continued )
Conversion Factors
Heat-transfer coefficient (h)
1 W/m2 -K = 0.176 11 Btu/h-ft2 -◦ R
1 Btu/h-ft2 -◦ R = 5.678 26 W/m2 -K
Length (L)
1 mm = 0.001 m = 0.1 cm
1 cm = 0.01 m = 10 mm = 0.3970 in.
1 m = 3.280 84 ft = 39.370 in.
1 km = 0.621 371 mi
1 mi = 1609.3 m (US statute)
1 ft = 12 in.
1 in. = 2.54 cm = 0.0254 m
1 ft = 0.3048 m
1 mi = 1.609 344 km
1 yd = 0.9144 m
Mass (m)
1 kg = 2.204 623 lbm
1 tonne = 1000 kg
1 grain = 6.479 89 × 10−5 kg
1 lbm = 0.453 592 kg
1 slug = 14.5939 kg
1 ton = 2000 lbm
Moment (torque, T)
1 N-m = 0.737 562 lbf-ft
1 lbf-ft = 1.355 818 N-m
Momentum (mV )
1 kg-m/s = 7.232 94 lbm-ft/s
= 0.224 809 lbf-s
Power ( Q̇, Ẇ)
1W
1 lbm-ft/s = 0.138 256 kg-m/s
= 1 J/s = 1 N-m/s
= 0.737 562 lbf-ft/s
1 kW
= 3412.14 Btu/h
1 hp (metric) = 0.735 499 kW
1 lbf-ft/s
1 ton of
refrigeration = 3.516 85 kW
1 ton of
refrigeration = 12 000 Btu/h
Pressure (P)
1 Pa
1 bar
1 arm
= 1 N/m2 = 1 kg/m-s2
= 1.0 × 105 Pa = 100 kPa
= 101.325 kPa
= 1.013 25 bar
= 760 mm Hg [0 ◦ C]
= 10.332 56 m H2 O [4◦ C]
1 torr
= 1 mm Hg [0◦ C]
◦
1 mm Hg [0 C] = 0.133 322 kPa
1 m H2 O [4◦ C] = 9.806 38 kPa
Specific energy (e, u)
1 kJ/kg = 0.429 92 Btu/lbm
= 334.55 lbf-ft/lbm
1 Btu/s
1 hp (UK)
= 1.355 818 W
= 4.626 24 Btu/h
= 1.055 056 kW
= 0.7457 kW
= 550 lbf-ft/s
= 2544.43 Btu/h
1 lbf/in.2
= 6.894 757 kPa
1 atm
= 14.695 94 lbf/in.2
= 29.921 in. Hg [32◦ F]
= 33.8995 ft H2 O [4◦ C]
1 in. Hg [0◦ C] = 0.491 15 lbf/in.2
1 in. H2 O [4◦ C] = 0.0361 26 lbf/in.2
1 Btu/lbm = 2.326 kJ/kg
1 lbf-ft/lbm = 2.989 07 × 10−3 kJ/kg
= 1.285 07 × 10−3 Btu/lbm
............................................................................................................
APPENDIX A
SI UNITS: SINGLE-STATE PROPERTIES
TABLE A.1 (continued )
Conversion Factors
Specific kinetic energy ( 12 V2 )
1 m2 /s2 = 0.001 kJ/kg
1 kJ/kg = 1000 m2 /s2
Specific potential energy (Zg)
1 m-g std = 9.806 65 × 10−3 kJ/kg
= 4.216 07 × 10−3 Btu/lbm
1 ft2 /s2
= 3.9941 × 10−5 Btu/lbm
1 Btu/lbm = 250 37 ft2 /s2
l ft-gstd = 1.0 lbf-ft/lbm
= 0.001 285 Btu/lbm
= 0.002 989 kJ/kg
Specific volume (v)
1 cm3 /g = 0.001 m3 /kg
1 cm3 /g = 1 L/kg
1 m3 /kg = 16.018 46 ft3 /lbm
1 ft3 /lbm = 0.062 428 m3 /kg
Temperature (T)
1 K = 1◦ C = 1.8 R = 1.8 F
TC = TK − 273.15
= (TF − 32)/1.8
TK = TR/1.8
1 R = (5/9) K
TF = TR − 459.67
= 1.8 TC + 32
TR = 1.8 TK
Universal Gas Constant
R̄ = N0 k = 8.314 51 kJ/kmol-K
= 1.985 89 kcal/kmol-K
= 82.0578 atm-L/kmol-K
..............
⑦
757
R̄ = 1.985 89 Btu/lbmol-R
= 1545.36 lbf-ft/lbmol-R
= 0.730 24 atm-ft3 /lbmol-R
= 10.7317 (lbf/in.2 )-ft3 /lbmol-R
Velcoity (V)
1 m/s = 3.6 km/h
= 3.280 84 ft/s
= 2.236 94 mi/h
1 km/h = 0.277 78 m/s
= 0.911 34 ft/s
= 0.621 37 mi/h
1 ft/s = 0.681 818 mi/h
= 0.3048 m/s
= 1.097 28 km/h
1 mi/h = 1.466 67 ft/s
= 0.447 04 m/s
= 1.609 344 km/h
Volume (V )
= 35.3147 ft3
1 m3
1L
= 1 dm3 = 0.001 m3
1 Gal (US) = 3.785 412 L
= 3.785 412 × 10−3 m3
1 ft3
= 2.831 685 × 10−2 m3
1 in.3
= 1.6387 × 10−5 m3
1 Gal (UK) = 4.546 090 L
1 Gal (US) = 231.00 in.3
⑦
APPENDIX A
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TABLE A.2
Critical Constants
Substance
Formula
Molec.
Mass
Temp.
(K)
Press.
(MPa)
Vol.
(m3 /kg)
Ammonia
Argon
Bromine
Carbon dioxide
Carbon monoxide
Chlorine
Fluorine
Helium
Hydrogen (normal)
Krypton
Neon
Nitric oxide
Nitrogen
Nitrogen dioxide
Nitrous oxide
Oxygen
Sulfur dioxide
Water
Xenon
Acetylene
Benzene
n-Butane
Chlorodifluoroethane (142b)
Chlorodifluoromethane (22)
Dichlorofluoroethane (141)
Dichlorotrifluoroethane (123)
Difluoroethane (152a)
Difluoromethane (32)
Ethane
Ethyl alcohol
Ethylene
n-Heptane
n-Hexane
Methane
Methyl alcohol
n-Octane
Pentafluoroethane (125)
n-Pentane
Propane
NH3
Ar
Br2
CO2
CO
C12
F2
He
H2
Kr
Ne
NO
N2
NO2
N2 O
O2
SO2
H2 O
Xe
C2 H2
C6 H6
C4 H10
CH3 CClF2
CHClF2
CH3 CCl2 F
CHCl2 CF3
CHF2 CH3
CF2 H2
C2 H6
C2 H5 OH
C2 H4
C7 H16
C6 H14
CH4
CH3 OH
C8 H18
CHF2 CF3
C5 H12
C3 H8
17.031
39.948
159.808
44.01
28.01
70.906
37.997
4.003
2.016
83.80
20.183
30.006
28.013
46.006
44.013
31.999
64.063
18.015
131.30
26.038
78.114
58.124
100.495
86.469
116.95
152.93
66.05
52.024
30.070
46.069
28.054
100.205
86.178
16.043
32.042
114.232
120.022
72.151
44.094
405.5
150.8
588
304.1
132.9
416.9
144.3
5.19
33.2
209.4
44.4
180
126.2
431
309.6
154.6
430.8
647.3
289.7
308.3
562.2
425.2
410.3
369.3
481.5
456.9
386.4
351.3
305.4
513.9
282.4
540.3
507.5
190.4
512.6
568.8
339.2
469.7
369.8
11.35
4.87
10.30
7.38
3.50
7.98
5.22
0.227
1.30
5.50
2.76
6.48
3.39
10.1
7.24
5.04
7.88
22.12
5.84
6.14
4.89
3.80
4.25
4.97
4.54
3.66
4.52
5.78
4.88
6.14
5.04
2.74
3.01
4.60
8.09
2.49
3.62
3.37
4.25
0.00426
0.00188
0.000796
0.00212
0.00333
0.00175
0.00174
0.0143
0.0323
0.00109
0.00206
0.00192
0.0032
0.00365
0.00221
0.00229
0.00191
0.00317
0.000902
0.00433
0.00332
0.00439
0.00230
0.00191
0.00215
0.00182
0.00272
0.00236
0.00493
0.00363
0.00465
0.00431
0.00429
0.00615
0.00368
0.00431
0.00176
0.00421
0.00454
Propene
Refrigerant mixture
Tetrafluoroethane (134a)
C3 H6
R-410a
CF3 CH2 F
42.081
72.585
102.03
364.9
344.5
374.2
4.60
4.90
4.06
0.00430
0.00218
0.00197
............................................................................................................
APPENDIX A
SI UNITS: SINGLE-STATE PROPERTIES
TABLE A.3
TABLE A.4
Properties of Selected Solids at 25◦ C
Properties of Some Liquids at 25◦ C ∗
Substance
Asphalt
Brick, common
Carbon, diamond
Carbon, graphite
Coal
Concrete
Glass, plate
Glass, wool
Granite
Ice (0◦ C)
Paper
Plexiglass
Polystyrene
Polyvinyl chloride
Rubber, soft
Sand, dry
Salt, rock
Silicon
Snow, firm
Wood, hard (oak)
Wood, soft (pine)
Wool
Metals
Aluminum
Brass, 60–40
Copper, commercial
Gold
Iron, cast
Iron, 304 St Steel
Lead
Magnesium, 2% Mn
Nickel, 10% Cr
Silver, 99.9% Ag
Sodium
Tin
Tungsten
Zinc
ρ
(kg/m3 )
2120
1800
3250
2000–2500
1200–1500
2200
2500
20
2750
917
700
1180
920
1380
1100
1500
2100–2500
2330
560
720
510
100
2700
8400
8300
19300
7272
7820
11340
1778
8666
10524
971
7304
19300
7144
Cp
(kJ/kg-K)
0.92
0.84
0.51
0.61
1.26
0.88
0.80
0.66
0.89
2.04
1.2
1.44
2.3
0.96
1.67
0.8
0.92
0.70
2.1
1.26
1.38
1.72
0.90
0.38
0.42
0.13
0.42
0.46
0.13
1.00
0.44
0.24
1.21
0.22
0.13
0.39
Cp
(kJ/kg-K)
Substance
ρ
(kg/m3 )
Ammonia
Benzene
Butane
CCl4
CO2
Ethanol
Gasoline
Glycerine
Kerosene
Methanol
n-Octane
Oil engine
Oil light
Propane
R-12
R-22
R-32
R-125
R-134a
R-410a
Water
604
879
556
1584
680
783
750
1260
815
787
692
885
910
510
1310
1190
961
1191
1206
1059
997
4.84
1.72
2.47
0.83
2.9
2.46
2.08
2.42
2.0
2.55
2.23
1.9
1.8
2.54
0.97
1.26
1.94
1.41
1.43
1.69
4.18
10040
10660
13580
887
828
929
6950
6570
0.14
0.16
0.14
1.13
0.81
1.38
0.24
0.50
Liquid metals
Bismuth, Bi
Lead, Pb
Mercury, Hg
NaK (56/44)
Potassium, K
Sodium, Na
Tin, Sn
Zinc, Zn
∗ Or
T melt if higher.
..............
⑦
759
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APPENDIX A
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TABLE A.5
Properties of Various Ideal Gases at 25◦ C, 100 kPa∗ (SI Units)
Gas
Chemical
Formula
Molecular
Mass (kg/kmol)
R
(kJ/kg-K)
ρ
(kg/m3 )
C p0
(kJ/kg-K)
C v0
(kJ/kg-K)
k=
Steam
Acetylene
Air
Ammonia
Argon
Butane
Carbon dioxide
Carbon monoxide
Ethane
Ethanol
Ethylene
Helium
Hydrogen
Methane
Methanol
Neon
Nitric oxide
Nitrogen
Nitrous oxide
n-Octane
Oxygen
Propane
R-12
R-22
R-32
R-125
R-134a
R-410a
Sulfur dioxide
Sulfur trioxide
H2 O
C2 H2
—
NH3
Ar
C4 H10
CO2
CO
C2 H6
C2 H5 OH
C2 H4
He
H2
CH4
CH3 OH
Ne
NO
N2
N2 O
C8 H18
O2
C3 H8
CCl2 F2
CHClF2
CF2 H2
CHF2 CF3
CF3 CH2 F
—
SO2
SO3
18.015
26.038
28.97
17.031
39.948
58.124
44.01
28.01
30.07
46.069
28.054
4.003
2.016
16.043
32.042
20.183
30.006
28.013
44.013
114.23
31.999
44.094
120.914
86.469
52.024
120.022
102.03
72.585
64.059
80.053
0.4615
0.3193
0.287
0.4882
0.2081
0.1430
0.1889
0.2968
0.2765
0.1805
0.2964
2.0771
4.1243
0.5183
0.2595
0.4120
0.2771
0.2968
0.1889
0.07279
0.2598
0.1886
0.06876
0.09616
0.1598
0.06927
0.08149
0.11455
0.1298
0.10386
0.0231
1.05
1.169
0.694
1.613
2.407
1.775
1.13
1.222
1.883
1.138
0.1615
0.0813
0.648
1.31
0.814
1.21
1.13
1.775
0.092
1.292
1.808
4.98
3.54
2.125
4.918
4.20
2.967
2.618
3.272
1.872
1.699
1.004
2.130
0.520
1.716
0.842
1.041
1.766
1.427
1.548
5.193
14.209
2.254
1.405
1.03
0.993
1.042
0.879
1.711
0.922
1.679
0.616
0.658
0.822
0.791
0.852
0.809
0.624
0.635
1.410
1.380
0.717
1.642
0.312
1.573
0.653
0.744
1.490
1.246
1.252
3.116
10.085
1.736
1.146
0.618
0.716
0.745
0.690
1.638
0.662
1.490
0.547
0.562
0.662
0.722
0.771
0.694
0.494
0.531
1.327
1.231
1.400
1.297
1.667
1.091
1.289
1.399
1.186
1.145
1.237
1.667
1.409
1.299
1.227
1.667
1.387
1.400
1.274
1.044
1.393
1.126
1.126
1.171
1.242
1.097
1.106
1.165
1.263
1.196
∗ Or
saturation pressure if it is less than 100 kPa.
Cp
Cv
............................................................................................................
APPENDIX A
SI UNITS: SINGLE-STATE PROPERTIES
TABLE A.6
..............
⑦
761
Constant-Pressure Specific Heats of Various Ideal Gases∗
C ρ0 = C 0 + C 1 θ + C 2 θ 2 + C 3 θ 3
(kJ/kg K)
θ = T(Kelvin)/1000
Gas
Formula
C0
C1
C2
C3
Steam
Acetylene
Air
Ammonia
Argon
Butane
Carbon dioxide
Carbon monoxide
Ethane
Ethanol
Ethylene
Helium
Hydrogen
Methane
Methanol
Neon
Nitric oxide
Nitrogen
Nitrous oxide
n-Octane
Oxygen
Propane
R-12†
R-22†
R-32†
R-125†
R-134a†
Sulfur dioxide
Sulfur trioxide
H2 O
C2 H2
—
NH3
Ar
C4 H10
CO2
CO
C2 H6
C2 H5 OH
C2 H4
He
H2
CH4
CH3 OH
Ne
NO
N2
N2 O
C8 H18
O2
C3 H8
CCl2 F2
CHClF2
CF2 H2
CHF2 CF3
CF3 CH2 F
SO2
SO3
1.79
1.03
1.05
1.60
0.52
0.163
0.45
1.10
0.18
0.2
0.136
5.193
13.46
1.2
0.66
1.03
0.98
1.11
0.49
−0.053
0.88
−0.096
0.26
0.2
0.227
0.305
0.165
0.37
0.24
0.107
2.91
−0.365
1.4
0
5.70
1.67
−0.46
5.92
4.65
5.58
0
4.6
3.25
2.21
0
−0.031
−0.48
1.65
6.75
−0.0001
6.95
1.47
1.87
2.27
1.68
2.81
1.05
1.7
0.586
−1.92
0.85
1.0
0
−1.906
−1.27
1.0
−2.31
−1.82
−3.0
0
−6.85
0.75
0.81
0
0.325
0.96
−1.31
−3.67
0.54
−3.6
−1.25
−1.35
−0.93
−0.284
−2.23
−0.77
−1.5
−0.20
0.54
−0.39
−0.7
0
−0.049
0.39
−0.454
0.29
0.03
0.63
0
3.79
−0.71
−0.89
0
−0.14
−0.42
0.42
0.775
−0.33
0.73
0.36
0.35
0.041
0
1.11
0.21
0.46
∗ Approximate
† Formula
forms valid from 250 K to 1200 K.
limited to maximum 500 K.
⑦
APPENDIX A
..............762
www.elsolucionario.org
SI UNITS: SINGLE-STATE PROPERTIES
............................................................................................................
TABLE A7.1
Ideal Gas Properties of Air, Standard Entropy at 0.1-MPa (1-Bar) Pressure
T
(K)
u
(kJ/kg)
h
(kJ/kg)
s0T
(kJ/kg-K)
T
(K)
u
(kJ/kg)
h
(kJ/kg)
s0T
(kJ/kg-K)
200
220
240
260
280
290
298.15
300
320
340
360
380
400
420
440
460
480
500
520
540
560
580
600
620
640
660
680
700
720
740
760
780
800
850
900
950
1000
1050
1100
142.77
157.07
171.38
185.70
200.02
207.19
213.04
214.36
228.73
243.11
257.53
271.99
286.49
301.04
315.64
330.31
345.04
359.84
374.73
389.69
404.74
419.87
435.10
450.42
465.83
481.34
496.94
512.64
528.44
544.33
560.32
576.40
592.58
633.42
674.82
716.76
759.19
802.10
845.45
200.17
220.22
240.27
260.32
280.39
290.43
298.62
300.47
320.58
340.70
360.86
381.06
401.30
421.59
441.93
462.34
482.81
503.36
523.98
544.69
565.47
586.35
607.32
628.38
649.53
670.78
692.12
713.56
735.10
756.73
778.46
800.28
822.20
877.40
933.15
989.44
1046.22
1103.48
1161.18
6.46260
6.55812
6.64535
6.72562
6.79998
6.83521
6.86305
6.86926
6.93413
6.99515
7.05276
7.10735
7.15926
7.20875
7.25607
7.30142
7.34499
7.38692
7.42736
7.46642
7.50422
7.54084
7.57638
7.61090
7.64448
7.67717
7.70903
7.74010
7.77044
7.80008
7.82905
7.85740
7.88514
7.95207
8.01581
8.07667
8.13493
8.19081
8.24449
1100
1150
1200
1250
1300
1350
1400
1450
1500
1550
1600
1650
1700
1750
1800
1850
1900
1950
2000
2050
2100
2150
2200
2250
2300
2350
2400
2450
2500
2550
2600
2650
2700
2750
2800
2850
2900
2950
3000
845.45
889.21
933.37
977.89
1022.75
1067.94
1113.43
1159.20
1205.25
1251.55
1298.08
1344.83
1391.80
1438.97
1486.33
1533.87
1581.59
1629.47
1677.52
1725.71
1774.06
1822.54
1871.16
1919.91
1968.79
2017.79
2066.91
2116.14
2165.48
2214.93
2264.48
2314.13
2363.88
2413.73
2463.66
2513.69
2563.80
2613.99
2664.27
1161.18
1219.30
1277.81
1336.68
1395.89
1455.43
1515.27
1575.40
1635.80
1696.45
1757.33
1818.44
1879.76
1941.28
2002.99
2064.88
2126.95
2189.19
2251.58
2314.13
2376.82
2439.66
2502.63
2565.73
2628.96
2692.31
2755.78
2819.37
2883.06
2946.86
3010.76
3074.77
3138.87
3203.06
3267.35
3331.73
3396.19
3460.73
3525.36
8.24449
8.29616
8.34596
8.39402
8.44046
8.48539
8.52891
8.57111
8.61208
8.65185
8.69051
8.72811
8.76472
8.80039
8.83516
8.86908
8.90219
8.93452
8.96611
8.99699
9.02721
9.05678
9.08573
9.11409
9.14189
9.16913
9.19586
9.22208
9.24781
9.27308
9.29790
9.32228
9.34625
9.36980
9.39297
9.41576
9.43818
9.46025
9.48198
............................................................................................................
APPENDIX A
SI UNITS: SINGLE-STATE PROPERTIES
TABLE A7.2
..............
⑦
763
The Isentropic Relative Pressure and Relative Volume Functions
T[K]
Pr
vr
T[K]
Pr
vr
T[K]
200
220
240
260
280
290
298.15
300
320
340
360
380
400
420
440
460
480
500
520
540
560
580
600
620
640
660
680
700
0.2703
0.3770
0.5109
0.6757
0.8756
0.9899
1.0907
1.1146
1.3972
1.7281
2.1123
2.5548
3.0612
3.6373
4.2892
5.0233
5.8466
6.7663
7.7900
8.9257
10.182
11.568
13.092
14.766
16.598
18.600
20.784
23.160
493.47
389.15
313.27
256.58
213.26
195.36
182.29
179.49
152.73
131.20
113.65
99.188
87.137
77.003
68.409
61.066
54.748
49.278
44.514
40.344
36.676
33.436
30.561
28.001
25.713
23.662
21.818
20.155
700
720
740
760
780
800
850
900
950
1000
1050
1100
1150
1200
1250
1300
1350
1400
1450
1500
1550
1600
1650
1700
1750
1800
1850
1900
23.160
25.742
28.542
31.573
34.851
38.388
48.468
60.520
74.815
91.651
111.35
134.25
160.73
191.17
226.02
265.72
310.74
361.62
418.89
483.16
554.96
634.97
723.86
822.33
931.14
1051.05
1182.9
1327.5
20.155
18.652
17.289
16.052
14.925
13.897
11.695
9.9169
8.4677
7.2760
6.2885
5.4641
4.7714
4.1859
3.6880
3.2626
2.8971
2.5817
2.3083
2.0703
1.8625
1.6804
1.52007
1.37858
1.25330
1.14204
1.04294
0.95445
1900
1950
2000
2050
2100
2150
2200
2250
2300
2350
2400
2450
2500
2550
2600
2650
2700
2750
2800
2850
2900
2950
3000
Pr
1327.5
1485.8
1658.6
1847.1
2052.1
2274.8
2516.2
2777.5
3059.9
3364.6
3693.0
4046.2
4425.8
4833.0
5269.5
5736.7
6236.2
6769.7
7338.7
7945.1
8590.7
9277.2
10007
vr
0.95445
0.87521
0.80410
0.74012
0.68242
0.63027
0.58305
0.54020
0.50124
0.46576
0.43338
0.40378
0.37669
0.35185
0.32903
0.30805
0.28872
0.27089
0.25443
0.23921
0.22511
0.21205
0.19992
The relative pressure and relative volume are temperature functions calculated with two
scaling constants A1 , A2 .
Pr = exp[sT0 /R − A1 ];
vr = A2 T /Pr
such that for an isentropic process (s1 = s2 )
0
P2
Pr2
e ST2 /R
=
= 0
≈
P1
Pr1
e ST1 /R
"
T2
T1
#C p /R
and
v2
v r2
=
≈
v1
v r1
"
T1
T2
#Cv /R
where the near equalities are for the constant heat capacity approximation.
⑦
APPENDIX A
..............764
www.elsolucionario.org
SI UNITS: SINGLE-STATE PROPERTIES
............................................................................................................
TABLE A.8
Ideal Gas Properties of Various Substances, Entropies at 0.1-MPa (1-Bar) Pressure,
Mass Basis
Nitrogen, Diatomic (N2 )
R = 0.2968 kJ/kg-K
M = 28.013 kg/kmol
Oxygen, Diatomic (O2 )
R = 0.2598 kJ/kg-K
M = 31.999 kg/kmol
T
(K)
u
(kJ/kg)
h
(kJ/kg)
s 0T
(kJ/kg-K)
u
(kJ/kg)
h
(kJ/kg)
s 0T
(kJ/kg-K)
200
250
300
350
400
450
500
550
600
650
700
750
800
850
900
950
1000
1100
1200
1300
1400
1500
1600
1700
1800
1900
2000
2100
2200
2300
2400
2500
2600
2700
2800
2900
3000
148.39
185.50
222.63
259.80
297.09
334.57
372.35
410.52
449.16
488.34
528.09
568.45
609.41
650.98
693.13
735.85
779.11
867.14
957.00
1048.46
1141.35
1235.50
1330.72
1426.89
1523.90
1621.66
1720.07
1819.08
1918.62
2018.63
2119.08
2219.93
2321.13
2422.66
2524.50
2626.62
2729.00
207.75
259.70
311.67
363.68
415.81
468.13
520.75
573.76
627.24
681.26
735.86
791.05
846.85
903.26
960.25
1017.81
1075.91
1193.62
1313.16
1434.31
1556.87
1680.70
1805.60
1931.45
2058.15
2185.58
2313.68
2442.36
2571.58
2701.28
2831.41
2961.93
3092.81
3224.03
3355.54
3487.34
3619.41
6.4250
6.6568
6.8463
7.0067
7.1459
7.2692
7.3800
7.4811
7.5741
7.6606
7.7415
7.8176
7.8897
7.9581
8.0232
8.0855
8.1451
8.2572
8.3612
8.4582
8.5490
8.6345
8.7151
8.7914
8.8638
8.9327
8.9984
9.0612
9.1213
9.1789
9.2343
9.2876
9.3389
9.3884
9.4363
9.4825
9.5273
129.84
162.41
195.20
228.37
262.10
296.52
331.72
367.70
404.46
441.97
480.18
519.02
558.46
598.44
638.90
679.80
721.11
804.80
889.72
975.72
1062.67
1150.48
1239.10
1328.49
1418.63
1509.50
1601.10
1693.41
1786.44
1880.17
1974.60
2069.71
2165.50
2261.94
2359.01
2546.70
2554.97
181.81
227.37
273.15
319.31
366.03
413.45
461.63
510.61
560.36
610.86
662.06
713.90
766.33
819.30
872.75
926.65
980.95
1090.62
1201.53
1313.51
1426.44
1540.23
1654.83
1770.21
1886.33
2003.19
2120.77
2239.07
2358.08
2477.79
2598.20
2719.30
2841.07
2963.49
3086.55
3210.22
3334.48
6.0466
6.2499
6.4168
6.5590
6.6838
6.7954
6.8969
6.9903
7.0768
7.1577
7.2336
7.3051
7.3728
7.4370
7.4981
7.5564
7.6121
7.7166
7.8131
7.9027
7.9864
8.0649
8.1389
8.2088
8.2752
8.3384
8.3987
8.4564
8.5117
8.5650
8.6162
8.6656
8.7134
8.7596
8.8044
8.8478
8.8899
............................................................................................................
APPENDIX A
SI UNITS: SINGLE-STATE PROPERTIES
TABLE A.8 (continued )
Ideal Gas Properties of Various Substances, Entropies at 0.1-MPa (1-Bar) Pressure,
Mass Basis
Carbon Dioxide (CO2 )
R = 0.1889 kJ/kg-K
M = 44.010 kg/kmol
..............
⑦
765
Water (H2 O)
R = 0.4615 kJ/kg-K
M = 18.015 kg/kmol
T
(K)
u
(kJ/kg)
h
(kJ/kg)
s 0T
(kJ/kg-K)
u
(kJ/kg)
h
(kJ/kg)
s 0T
(kJ/kg-K)
200
250
300
350
400
450
500
550
600
650
700
750
800
850
900
950
1000
1100
1200
1300
1400
1500
1600
1700
1800
1900
2000
2100
2200
2300
2400
2500
2600
2700
2800
2900
3000
97.49
126.21
157.70
191.78
228.19
266.69
307.06
349.12
392.72
437.71
483.97
531.40
579.89
629.35
676.69
730.85
782.75
888.55
996.64
1106.68
1218.38
1331.50
1445.85
1561.26
1677.61
1794.78
1912.67
2031.21
2150.34
2270.00
2390.14
2510.74
2631.73
2753.10
2874.81
2996.84
3119.18
135.28
173.44
214.38
257.90
303.76
351.70
401.52
453.03
506.07
560.51
616.22
673.09
731.02
789.93
849.72
910.33
971.67
1096.36
1223.34
1352.28
1482.87
1614.88
1748.12
1882.43
2017.67
2153.73
2290.51
2427.95
2565.97
2704.52
2843.55
2983.04
3122.93
3263.19
3403.79
3544.71
3685.95
4.5439
4.7139
4.8631
4.9972
5.1196
5.2325
5.3375
5.4356
5.5279
5.6151
5.6976
5.7761
5.8508
5.9223
5.9906
6.0561
6.1190
6.2379
6.3483
6.4515
6.5483
6.6394
6.7254
6.8068
6.8841
6.9577
7.0278
7.0949
7.1591
7.2206
7.2798
7.3368
7.3917
7.4446
7.4957
7.5452
7.5931
276.38
345.98
415.87
486.37
557.79
630.40
704.36
779.79
856.75
935.31
1015.49
1097.35
1180.90
1266.19
1353.23
1442.03
1532.61
1719.05
1912.42
2112.47
2318.89
2531.28
2749.24
2972.35
3200.17
3432.28
3668.24
3908.08
4151.28
4397.56
4646.71
4898.49
5152.73
5409.24
5667.86
5928.44
6190.86
368.69
461.36
554.32
647.90
742.40
838.09
935.12
1033.63
1133.67
1235.30
1338.56
1443.49
1550.13
1658.49
1768.60
1880.48
1994.13
2226.73
2466.25
2712.46
2965.03
3223.57
3487.69
3756.95
4030.92
4309.18
4591.30
4877.29
5166.64
5459.08
5754.37
6052.31
6352.70
6655.36
6960.13
7266.87
7575.44
9.7412
10.1547
10.4936
10.7821
11.0345
11.2600
11.4644
11.6522
11.8263
11.9890
12.1421
12.2868
12.4244
12.5558
12.6817
12.8026
12.9192
13.1408
13.3492
13.5462
13.7334
13.9117
14.0822
14.2454
14.4020
14.5524
14.6971
14.8366
14.9712
15.1012
15.2269
15.3485
15.4663
15.5805
15.6914
15.7990
15.9036
⑦
APPENDIX A
..............766
www.elsolucionario.org
SI UNITS: SINGLE-STATE PROPERTIES
............................................................................................................
TABLE A.9
Ideal Gas Properties of Various Substances (SI Units), Entropies at 0.1-MPa (1-Bar)
Pressure, Mole Basis
Nitrogen, Diatomic (N2 )
0
h̄ f ,298 = 0 kJ/kmol
M = 28.013 kg/kmol
0
Nitrogen, Monatomic (N)
0
h̄ f ,298 = 472 680 kJ/kmol
M = 14.007 kg/kmol
0
T
K
(h̄−h̄298 )
kJ/kmol
s̄ 0T
kJ/kmol K
(h̄−h̄298 )
kJ/kmol
s̄ 0T
kJ/kmol
0
100
200
298
300
400
500
600
700
800
900
1000
1100
1200
1300
1400
1500
1600
1700
1800
1900
2000
2200
2400
2600
2800
3000
3200
3400
3600
3800
4000
4400
4800
5200
5600
6000
−8670
−5768
−2857
0
54
2971
5911
8894
11937
15046
18223
21463
24760
28109
31503
34936
38405
41904
45430
48979
52549
56137
63362
70640
77963
85323
92715
100134
107577
115042
122526
130027
145078
160188
175352
190572
205848
0
159.812
179.985
191.609
191.789
200.181
206.740
212.177
216.865
221.016
224.757
228.171
231.314
234.227
236.943
239.487
241.881
244.139
246.276
248.304
250.234
252.075
255.518
258.684
261.615
264.342
266.892
269.286
271.542
273.675
275.698
277.622
281.209
284.495
287.530
290.349
292.984
−6197
−4119
−2040
0
38
2117
4196
6274
8353
10431
12510
14589
16667
18746
20825
22903
24982
27060
29139
31218
33296
35375
39534
43695
47860
52033
56218
60420
64646
68902
73194
77532
86367
95457
104843
114550
124590
0
130.593
145.001
153.300
153.429
159.409
164.047
167.837
171.041
173.816
176.265
178.455
180.436
182.244
183.908
185.448
186.883
188.224
189.484
190.672
191.796
192.863
194.845
196.655
198.322
199.868
201.311
202.667
203.948
205.164
206.325
207.437
209.542
211.519
213.397
215.195
216.926
............................................................................................................
APPENDIX A
SI UNITS: SINGLE-STATE PROPERTIES
TABLE A.9 (continued )
Ideal Gas Properties of Various Substances (SI Units), Entropies at 0.1-MPa (1-Bar)
Pressure, Mole Basis
Oxygen, Diatomic (O2 )
0
h̄ f ,298 = 0 kJ/kmol
M = 31.999 kg/kmol
0
..............
⑦
767
Oxygen, Monatomic (O)
0
h̄ f ,298 = 249 170 kJ/kmol
M = 16.00 kg/kmol
0
T
K
(h̄ − h̄298 )
kJ/kmol
s̄ 0T
kJ/kmol K
(h̄ − h̄298 )
kJ/kmol
s̄ 0T
kJ/kmol K
0
100
200
298
300
400
500
600
700
800
900
1000
1100
1200
1300
1400
1500
1600
1700
1800
1900
2000
2200
2400
2600
2800
3000
3200
3400
3600
3800
4000
4400
4800
5200
5600
6000
−8683
−5777
−2868
0
54
3027
6086
9245
12499
15836
19241
22703
26212
29761
33345
36958
40600
44267
47959
51674
55414
59176
66770
74453
82225
90080
98013
106022
114101
122245
130447
138705
155374
172240
189312
206618
224210
0
173.308
193.483
205.148
205.329
213.873
220.693
226.450
231.465
235.920
239.931
243.579
246.923
250.011
252.878
255.556
258.068
260.434
262.673
264.797
266.819
268.748
272.366
275.708
278.818
281.729
284.466
287.050
289.499
291.826
294.043
296.161
300.133
303.801
307.217
310.423
313.457
−6725
−4518
−2186
0
41
2207
4343
6462
8570
10671
12767
14860
16950
19039
21126
23212
25296
27381
29464
31547
33630
35713
39878
44045
48216
52391
56574
60767
64971
69190
73424
77675
86234
94873
103592
112391
121264
0
135.947
152.153
161.059
161.194
167.431
172.198
176.060
179.310
182.116
184.585
186.790
188.783
190.600
192.270
193.816
195.254
196.599
197.862
199.053
200.179
201.247
203.232
205.045
206.714
208.262
209.705
211.058
212.332
213.538
214.682
215.773
217.812
219.691
221.435
223.066
224.597
⑦
APPENDIX A
..............768
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SI UNITS: SINGLE-STATE PROPERTIES
............................................................................................................
TABLE A.9 (continued )
Ideal Gas Properties of Various Substances (SI Units), Entropies at 0.1-MPa (1-Bar)
Pressure, Mole Basis
Carbon Dioxide (CO2 )
0
h̄ f ,298 = −393 522 kJ/kmol
M = 44.01 kg/kmol
0
Carbon Monoxide (CO)
0
h̄ f ,298 = −110 527 kJ/kmol
M = 28.01 kg/kmol
0
T
K
(h̄ − h̄298 )
kJ/kmol
s̄ 0T
kJ/kmol K
(h̄ − h̄298 )
kJ/kmol
0
100
200
298
300
400
500
600
700
800
900
1000
1100
1200
1300
1400
1500
1600
1700
1800
1900
2000
2200
2400
2600
2800
3000
3200
3400
3600
3800
4000
4400
4800
5200
5600
6000
−9364
−6457
−3413
0
69
4003
8305
12906
17754
22806
28030
33397
38885
44473
50148
55895
61705
67569
73480
79432
85420
91439
103562
115779
128074
140435
152853
165321
177836
190394
202990
215624
240992
266488
292112
317870
343782
0
179.010
199.976
213.794
214.024
225.314
234.902
243.284
250.752
257.496
263.646
269.299
274.528
279.390
283.931
288.190
292.199
295.984
299.567
302.969
306.207
309.294
315.070
320.384
325.307
329.887
334.170
338.194
341.988
345.576
348.981
352.221
358.266
363.812
368.939
373.711
378.180
−8671
−5772
−2860
0
54
2977
5932
8942
12021
15174
18397
21686
25031
28427
31867
35343
38852
42388
45948
49529
53128
56743
64012
71326
78679
86070
93504
100962
108440
115938
123454
130989
146108
161285
176510
191782
207105
s̄ 0T
kJ/kmol K
0
165.852
186.024
197.651
197.831
206.240
212.833
218.321
223.067
227.277
231.074
234.538
237.726
240.679
243.431
246.006
248.426
250.707
252.866
254.913
256.860
258.716
262.182
265.361
268.302
271.044
273.607
276.012
278.279
280.422
282.454
284.387
287.989
291.290
294.337
297.167
299.809
............................................................................................................
APPENDIX A
SI UNITS: SINGLE-STATE PROPERTIES
TABLE A.9 (continued )
Ideal Gas Properties of Various Substances (SI Units), Entropies at 0.1-MPa (1-Bar)
Pressure, Mole Basis
Water (H2 O)
0
h̄ f ,298 = −241 826 kJ/kmol
M = 18.015 kg/kmol
0
..............
⑦
769
Hydroxyl (OH)
0
h̄ f ,298 = 38 987 kJ/kmol
M = 17.007 kg/kmol
0
T
K
(h̄ − h̄298 )
kJ/kmol
s̄ 0T
kJ/kmol K
(h̄ − h̄298 )
kJ/kmol
0
100
200
298
300
400
500
600
700
800
900
1000
1100
1200
1300
1400
1500
1600
1700
1800
1900
2000
2200
2400
2600
2800
3000
3200
3400
3600
3800
4000
4400
4800
5200
5600
6000
−9904
−6617
−3282
0
62
3450
6922
10499
14190
18002
21937
26000
30190
34506
38941
43491
48149
52907
57757
62693
67706
72788
83153
93741
104520
115463
126548
137756
149073
160484
171981
183552
206892
230456
254216
278161
302295
0
152.386
175.488
188.835
189.043
198.787
206.532
213.051
218.739
223.826
228.460
232.739
236.732
240.485
244.035
247.406
250.620
253.690
256.631
259.452
262.162
264.769
269.706
274.312
278.625
282.680
286.504
290.120
293.550
296.812
299.919
302.887
308.448
313.573
318.328
322.764
326.926
−9172
−6140
−2975
0
55
3034
5991
8943
11902
14881
17889
20935
24024
27159
30340
33567
36838
40151
43502
46890
50311
53763
60751
67840
75018
82268
89585
96960
104388
111864
119382
126940
142165
157522
173002
188598
204309
s̄ 0T
kJ/kmol K
0
149.591
171.592
183.709
183.894
192.466
199.066
204.448
209.008
212.984
216.526
219.735
222.680
225.408
227.955
230.347
232.604
234.741
236.772
238.707
240.556
242.328
245.659
248.743
251.614
254.301
256.825
259.205
261.456
263.592
265.625
267.563
271.191
274.531
277.629
280.518
283.227
⑦
APPENDIX A
..............770
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SI UNITS: SINGLE-STATE PROPERTIES
............................................................................................................
TABLE A.9 (continued )
Ideal Gas Properties of Various Substances (SI Units), Entropies at 0.1-MPa (1-Bar)
Pressure, Mole Basis
Hydrogen (H2 )
0
h̄ f ,298 = 0 kJ/kmol
M = 2.016 kg/kmol
0
Hydrogen, Monatomic (H)
0
h̄ f ,298 = 217 999 kJ/kmol
M = 1.008 kg/kmol
0
T
K
(h̄ − h̄298 )
kJ/kmol
s̄ 0T
kJ/kmol K
(h̄ − h̄298 )
kJ/kmol
0
100
200
298
300
400
500
600
700
800
900
1000
1100
1200
1300
1400
1500
1600
1700
1800
1900
2000
2200
2400
2600
2800
3000
3200
3400
3600
3800
4000
4400
4800
5200
5600
6000
−8467
−5467
−2774
0
53
2961
5883
8799
11730
14681
17657
20663
23704
26785
29907
33073
36281
39533
42826
46160
49532
52942
59865
66915
74082
81355
88725
96187
103736
111367
119077
126864
142658
158730
175057
191607
208332
0
100.727
119.410
130.678
130.856
139.219
145.738
151.078
155.609
159.554
163.060
166.225
169.121
171.798
174.294
176.637
178.849
180.946
182.941
184.846
186.670
188.419
191.719
194.789
197.659
200.355
202.898
205.306
207.593
209.773
211.856
213.851
217.612
221.109
224.379
227.447
230.322
−6197
−4119
−2040
0
38
2117
4196
6274
8353
10431
12510
14589
16667
18746
20825
22903
24982
27060
29139
31218
33296
35375
39532
43689
47847
52004
56161
60318
64475
68633
72790
76947
85261
93576
101890
110205
118519
s̄ 0T
kJ/kmol K
0
92.009
106.417
114.716
114.845
120.825
125.463
129.253
132.457
135.233
137.681
139.871
141.852
143.661
145.324
146.865
148.299
149.640
150.900
152.089
153.212
154.279
156.260
158.069
159.732
161.273
162.707
164.048
165.308
166.497
167.620
168.687
170.668
172.476
174.140
175.681
177.114
............................................................................................................
APPENDIX A
SI UNITS: SINGLE-STATE PROPERTIES
TABLE A.9 (continued )
Ideal Gas Properties of Various Substances (SI Units), Entropies at 0.1-MPa (1-Bar)
Pressure, Mole Basis
Nitric Oxide (NO)
0
h̄ f ,298 = 90 291 kJ/kmol
M = 30.006 kg/kmol
0
..............
⑦
771
Nitrogen Dioxide (NO2 )
0
h̄ f ,298 = 33 100 kJ/kmol
M = 46.005 kg/kmol
0
T
K
(h̄ − h̄298 )
kJ/kmol
s̄ 0T
kJ/kmol K
(h̄ − h̄298 )
kJ/kmol
0
100
200
298
300
400
500
600
700
800
900
1000
1100
1200
1300
1400
1500
1600
1700
1800
1900
2000
2200
2400
2600
2800
3000
3200
3400
3600
3800
4000
4400
4800
5200
5600
6000
−9192
−6073
−2951
0
55
3040
6059
9144
12308
15548
18858
22229
25653
29120
32626
36164
39729
43319
46929
50557
54201
57859
65212
72606
80034
87491
94973
102477
110000
117541
125099
132671
147857
163094
178377
193703
209070
0
177.031
198.747
210.759
210.943
219.529
226.263
231.886
236.762
241.088
244.985
248.536
251.799
254.816
257.621
260.243
262.703
265.019
267.208
269.282
271.252
273.128
276.632
279.849
282.822
285.585
288.165
290.587
292.867
295.022
297.065
299.007
302.626
305.940
308.998
311.838
314.488
−10186
−6861
−3495
0
68
3927
8099
12555
17250
22138
27180
32344
37606
42946
48351
53808
59309
64846
70414
76008
81624
87259
98578
109948
121358
132800
144267
155756
167262
178783
190316
201860
224973
248114
271276
294455
317648
s̄ 0T
kJ/kmol K
0
202.563
225.852
240.034
240.263
251.342
260.638
268.755
275.988
282.513
288.450
293.889
298.904
303.551
307.876
311.920
315.715
319.289
322.664
325.861
328.898
331.788
337.182
342.128
346.695
350.934
354.890
358.597
362.085
365.378
368.495
371.456
376.963
381.997
386.632
390.926
394.926
⑦
APPENDIX A
..............772
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SI UNITS: SINGLE-STATE PROPERTIES
............................................................................................................
TABLE A.10
Enthalpy of Formation and Absolute Entropy of Various Substances at 25◦ C, 100 kPa Pressure
Substance
Formula
M
kg/kmol
Acetylene
Ammonia
Benzene
Carbon dioxide
Carbon (graphite)
Carbon monoxide
Ethane
Ethene
Ethanol
Ethanol
Heptane
Hexane
Hydrogen peroxide
Methane
Methanol
Methanol
n-Butane
Nitrogen oxide
Nitromethane
n-Octane
n-Octane
Ozone
Pentane
Propane
Propene
Sulfur
Sulfur dioxide
Sulfur trioxide
T-T -Diesel
Water
Water
C2 H2
NH3
C6 H6
CO2
C
CO
C2 H6
C2 H4
C2 H5 OH
C2 H5 OH
C7 H16
C6 H14
H2 O2
CH4
CH3 OH
CH3 OH
C4 H10
N2 O
CH3 NO2
C8 H18
C8 H18
O3
C5 H12
C3 H8
C3 H6
S
SO2
SO3
C14.4 H24.9
H2 O
H2 O
26.038
17.031
78.114
44.010
12.011
28.011
30.070
28.054
46.069
46.069
100.205
86.178
34.015
16.043
32.042
32.042
58.124
44.013
61.04
114.232
114.232
47.998
72.151
44.094
42.081
32.06
64.059
80.058
198.06
18.015
18.015
0
State
gas
gas
gas
gas
solid
gas
gas
gas
gas
liq
gas
gas
gas
gas
gas
liq
gas
gas
liq
gas
liq
gas
gas
gas
gas
solid
gas
gas
liq
gas
liq
h̄ f
kJ/kmol
+226 731
−45 720
+82 980
−393 522
0
−110 527
−84 740
+52 467
−235 000
−277 380
−187 900
−167 300
−136 106
−74 873
−201 300
−239 220
−126 200
+82 050
−113 100
−208 600
−250 105
+142 674
−146 500
−103 900
+20 430
0
−296 842
−395 765
−174 000
−241 826
−285 830
s̄ 0f
kJ/kmol K
200.958
192.572
269.562
213.795
5.740
197.653
229.597
219.330
282.444
160.554
427.805
387.979
232.991
186.251
239.709
126.809
306.647
219.957
171.80
466.514
360.575
238.932
348.945
269.917
267.066
32.056
248.212
256.769
525.90
188.834
69.950
TABLE A.11
Logarithms to the Base e of the Equilibrium Constant K
For the reaction v A A + v B B
v C C + v D D, the equilibrium constant K is defined as
K =
2H
Temp K
H2
298
500
1000
1200
1400
1600
1800
2000
2200
2400
2600
2800
3000
3200
3400
3600
3800
4000
4500
5000
5500
6000
−164.003
−92.830
−39.810
−30.878
−24.467
−19.638
−15.868
−12.841
−10.356
−8.280
−6.519
−5.005
−3.690
−2.538
−1.519
−0.611
0.201
0.934
2.483
3.724
4.739
5.587
O2
2O
−186.963
−105.623
−45.146
−35.003
−27.741
−22.282
−18.028
−14.619
−11.826
−9.495
−7.520
−5.826
−4.356
−3.069
−1.932
−0.922
−0.017
0.798
2.520
3.898
5.027
5.969
N2
2N
−367.528
−213.405
−99.146
−80.025
−66.345
−56.069
−48.066
−41.655
−36.404
−32.023
−28.313
−25.129
−22.367
−19.947
−17.810
−15.909
−14.205
−12.671
−9.423
−6.816
−4.672
−2.876
2H2 O
−184.420
−105.385
−46.321
−36.363
−29.222
−23.849
−19.658
−16.299
−13.546
−11.249
−9.303
−7.633
−6.184
−4.916
−3.795
−2.799
−1.906
−1.101
0.602
1.972
3.098
4.040
yCvC y Dv D
y vAA y Bv B
"
2H2 + O2
P
P0
#v C +v D −v A −v B
2H2 O
−212.075
−120.331
−51.951
−40.467
−32.244
−26.067
−21.258
−17.406
−14.253
−11.625
−9.402
−7.496
−5.845
−4.401
−3.128
−1.996
−0.984
−0.074
1.847
3.383
4.639
5.684
, P 0 = 0.1 MPa
H2 + 2OH
2CO2
2CO + O2
−207.529
−115.234
−47.052
−35.736
−27.679
−21.656
−16.987
−13.266
−10.232
−7.715
−5.594
−3.781
−2.217
−0.853
0.346
1.408
2.355
3.204
4.985
6.397
7.542
8.488
N2 + O2
2NO
−69.868
−40.449
−18.709
−15.082
−12.491
−10.547
−9.035
−7.825
−6.836
−6.012
−5.316
−4.720
−4.205
−3.755
−3.359
−3.008
−2.694
−2.413
−1.824
−1.358
−0.980
−0.671
Source: Consistent with thermodynamic data in JANAF Thermochemical Tables, third edition, Thermal Group, Dow Chemical U.S.A., Midland, MI, 1985.
773
N2 + 2O2
−41.355
−30.725
−23.039
−21.752
−20.826
−20.126
−19.577
−19.136
−18.773
−18.470
−18.214
−17.994
−17.805
−17.640
−17.496
−17.369
−17.257
−17.157
−16.953
−16.797
−16.678
−16.588
2NO 2
www.elsolucionario.org
APPEN
775
X
B
DI
SI Units:
Thermodynamic
Tables
⑦
APPENDIX B
..............776
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SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.1
Thermodynamic Properties of Water
TABLE B.1.1
Saturated Water
Specific Volume, m3 /kg
Internal Energy, kJ/kg
Temp.
(◦ C)
Press.
(kPa)
Sat. Liquid
vf
Evap.
v fg
Sat. Vapor
vg
Sat. Liquid
uf
Evap.
u fg
Sat. Vapor
ug
0.01
5
10
15
20
25
30
35
40
45
50
55
60
65
70
75
80
85
90
95
100
105
110
115
120
125
130
135
140
145
150
155
160
165
170
175
180
185
190
0.6113
0.8721
1.2276
1.705
2.339
3.169
4.246
5.628
7.384
9.593
12.350
15.758
19.941
25.03
31.19
38.58
47.39
57.83
70.14
84.55
101.3
120.8
143.3
169.1
198.5
232.1
270.1
313.0
361.3
415.4
475.9
543.1
617.8
700.5
791.7
892.0
1002.2
1122.7
1254.4
0.001000
0.001000
0.001000
0.001001
0.001002
0.001003
0.001004
0.001006
0.001008
0.001010
0.001012
0.001015
0.001017
0.001020
0.001023
0.001026
0.001029
0.001032
0.001036
0.001040
0.001044
0.001047
0.001052
0.001056
0.001060
0.001065
0.001070
0.001075
0.001080
0.001085
0.001090
0.001096
0.001102
0.001108
0.001114
0.001121
0.001127
0.001134
0.001141
206.131
147.117
106.376
77.924
57.7887
43.3583
32.8922
25.2148
19.5219
15.2571
12.0308
9.56734
7.66969
6.19554
5.04114
4.13021
3.40612
2.82654
2.35953
1.98082
1.67185
1.41831
1.20909
1.03552
0.89080
0.76953
0.66744
0.58110
0.50777
0.44524
0.39169
0.34566
0.30596
0.27158
0.24171
0.21568
0.19292
0.17295
0.15539
206.132
147.118
106.377
77.925
57.7897
43.3593
32.8932
25.2158
19.5229
15.2581
12.0318
9.56835
7.67071
6.19656
5.04217
4.13123
3.40715
2.82757
2.36056
1.98186
1.67290
1.41936
1.21014
1.03658
0.89186
0.77059
0.66850
0.58217
0.50885
0.44632
0.39278
0.34676
0.30706
0.27269
0.24283
0.21680
0.19405
0.17409
0.15654
0
20.97
41.99
62.98
83.94
104.86
125.77
146.65
167.53
188.41
209.30
230.19
251.09
272.00
292.93
313.87
334.84
355.82
376.82
397.86
418.91
440.00
461.12
482.28
503.48
524.72
546.00
567.34
588.72
610.16
631.66
653.23
674.85
696.55
718.31
740.16
762.08
784.08
806.17
2375.33
2361.27
2347.16
2333.06
2318.98
2304.90
2290.81
2276.71
2262.57
2248.40
2234.17
2219.89
2205.54
2191.12
2176.62
2162.03
2147.36
2132.58
2117.70
2102.70
2087.58
2072.34
2056.96
2041.44
2025.76
2009.91
1993.90
1977.69
1961.30
1944.69
1927.87
1910.82
1893.52
1875.97
1858.14
1840.03
1821.62
1802.90
1783.84
2375.33
2382.24
2389.15
2396.04
2402.91
2409.76
2416.58
2423.36
2430.11
2436.81
2443.47
2450.08
2456.63
2463.12
2469.55
2475.91
2482.19
2488.40
2494.52
2500.56
2506.50
2512.34
2518.09
2523.72
2529.24
2534.63
2539.90
2545.03
2550.02
2554.86
2559.54
2564.04
2568.37
2572.51
2576.46
2580.19
2583.70
2586.98
2590.01
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.1.1 (continued )
..............
⑦
777
Saturated Water
Enthalpy, kJ/kg
Entropy, kJ/kg-K
Temp.
(◦ C)
Press.
(kPa)
Sat. Liquid
hf
Evap.
hfg
Sat. Vapor
hg
Sat. Liquid
sf
Evap.
sfg
Sat. Vapor
sg
0.01
5
10
15
20
25
30
35
40
45
50
55
60
65
70
75
80
85
90
95
100
105
110
115
120
125
130
135
140
145
150
155
160
165
170
175
180
185
190
0.6113
0.8721
1.2276
1.705
2.339
3.169
4.246
5.628
7.384
9.593
12.350
15.758
19.941
25.03
31.19
38.58
47.39
57.83
70.14
84.55
101.3
120.8
143.3
169.1
198.5
232.1
270.1
313.0
361.3
415.4
475.9
543.1
617.8
700.5
791.7
892.0
1002.2
1122.7
1254.4
0.00
20.98
41.99
62.98
83.94
104.87
125.77
146.66
167.54
188.42
209.31
230.20
251.11
272.03
292.96
313.91
334.88
355.88
376.90
397.94
419.02
440.13
461.27
482.46
503.69
524.96
546.29
567.67
589.11
610.61
632.18
653.82
675.53
697.32
719.20
741.16
763.21
785.36
807.61
2501.35
2489.57
2477.75
2465.93
2454.12
2442.30
2430.48
2418.62
2406.72
2394.77
2382.75
2370.66
2358.48
2346.21
2333.85
2321.37
2308.77
2296.05
2283.19
2270.19
2257.03
2243.70
2230.20
2216.50
2202.61
2188.50
2174.16
2159.59
2144.75
2129.65
2114.26
2098.56
2082.55
2066.20
2049.50
2032.42
2014.96
1997.07
1978.76
2501.35
2510.54
2519.74
2528.91
2538.06
2547.17
2556.25
2565.28
2574.26
2583.19
2592.06
2600.86
2609.59
2618.24
2626.80
2635.28
2643.66
2651.93
2660.09
2668.13
2676.05
2683.83
2691.47
2698.96
2706.30
2713.46
2720.46
2727.26
2733.87
2740.26
2746.44
2752.39
2758.09
2763.53
2768.70
2773.58
2778.16
2782.43
2786.37
0
0.0761
0.1510
0.2245
0.2966
0.3673
0.4369
0.5052
0.5724
0.6386
0.7037
0.7679
0.8311
0.8934
0.9548
1.0154
1.0752
1.1342
1.1924
1.2500
1.3068
1.3629
1.4184
1.4733
1.5275
1.5812
1.6343
1.6869
1.7390
1.7906
1.8417
1.8924
1.9426
1.9924
2.0418
2.0909
2.1395
2.1878
2.2358
9.1562
8.9496
8.7498
8.5569
8.3706
8.1905
8.0164
7.8478
7.6845
7.5261
7.3725
7.2234
7.0784
6.9375
6.8004
6.6670
6.5369
6.4102
6.2866
6.1659
6.0480
5.9328
5.8202
5.7100
5.6020
5.4962
5.3925
5.2907
5.1908
5.0926
4.9960
4.9010
4.8075
4.7153
4.6244
4.5347
4.4461
4.3586
4.2720
9.1562
9.0257
8.9007
8.7813
8.6671
8.5579
8.4533
8.3530
8.2569
8.1647
8.0762
7.9912
7.9095
7.8309
7.7552
7.6824
7.6121
7.5444
7.4790
7.4158
7.3548
7.2958
7.2386
7.1832
7.1295
7.0774
7.0269
6.9777
6.9298
6.8832
6.8378
6.7934
6.7501
6.7078
6.6663
6.6256
6.5857
6.5464
6.5078
⑦
APPENDIX B
..............778
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.1.1 (continued )
Saturated Water
Specific Volume, m3 /kg
Internal Energy, kJ/kg
Temp.
(◦ C)
Press.
(kPa)
Sat. Liquid
vf
Evap.
vfg
Sat. Vapor
vg
Sat. Liquid
uf
Evap.
u fg
Sat. Vapor
ug
195
200
205
210
215
220
225
230
235
240
245
250
255
260
265
270
275
280
285
290
295
300
305
310
315
320
325
330
335
340
345
350
355
360
365
370
374.1
1397.8
1553.8
1723.0
1906.3
2104.2
2317.8
2547.7
2794.9
3060.1
3344.2
3648.2
3973.0
4319.5
4688.6
5081.3
5498.7
5941.8
6411.7
6909.4
7436.0
7992.8
8581.0
9201.8
9856.6
10547
11274
12040
12845
13694
14586
15525
16514
17554
18651
19807
21028
22089
0.001149
0.001156
0.001164
0.001173
0.001181
0.001190
0.001199
0.001209
0.001219
0.001229
0.001240
0.001251
0.001263
0.001276
0.001289
0.001302
0.001317
0.001332
0.001348
0.001366
0.001384
0.001404
0.001425
0.001447
0.001472
0.001499
0.001528
0.001561
0.001597
0.001638
0.001685
0.001740
0.001807
0.001892
0.002011
0.002213
0.003155
0.13990
0.12620
0.11405
0.10324
0.09361
0.08500
0.07729
0.07037
0.06415
0.05853
0.05346
0.04887
0.04471
0.04093
0.03748
0.03434
0.03147
0.02884
0.02642
0.02420
0.02216
0.02027
0.01852
0.01690
0.01539
0.01399
0.01267
0.01144
0.01027
0.00916
0.00810
0.00707
0.00607
0.00505
0.00398
0.00271
0
0.14105
0.12736
0.11521
0.10441
0.09479
0.08619
0.07849
0.07158
0.06536
0.05976
0.05470
0.05013
0.04598
0.04220
0.03877
0.03564
0.03279
0.03017
0.02777
0.02557
0.02354
0.02167
0.01995
0.01835
0.01687
0.01549
0.01420
0.01300
0.01186
0.01080
0.00978
0.00881
0.00787
0.00694
0.00599
0.00493
0.00315
828.36
850.64
873.02
895.51
918.12
940.85
963.72
986.72
1009.88
1033.19
1056.69
1080.37
1104.26
1128.37
1152.72
1177.33
1202.23
1227.43
1252.98
1278.89
1305.21
1331.97
1359.22
1387.03
1415.44
1444.55
1474.44
1505.24
1537.11
1570.26
1605.01
1641.81
1681.41
1725.19
1776.13
1843.84
2029.58
1764.43
1744.66
1724.49
1703.93
1682.94
1661.49
1639.58
1617.17
1594.24
1570.75
1546.68
1522.00
1496.66
1470.64
1443.87
1416.33
1387.94
1358.66
1328.41
1297.11
1264.67
1230.99
1195.94
1159.37
1121.11
1080.93
1038.57
993.66
945.77
894.26
838.29
776.58
707.11
626.29
526.54
384.69
0
2592.79
2595.29
2597.52
2599.44
2601.06
2602.35
2603.30
2603.89
2604.11
2603.95
2603.37
2602.37
2600.93
2599.01
2596.60
2593.66
2590.17
2586.09
2581.38
2575.99
2569.87
2562.96
2555.16
2546.40
2536.55
2525.48
2513.01
2498.91
2482.88
2464.53
2443.30
2418.39
2388.52
2351.47
2302.67
2228.53
2029.58
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.1.1 (continued )
..............
⑦
779
Saturated Water
Enthalpy, kJ/kg
Entropy, kJ/kg-K
Temp.
(◦ C)
Press.
(kPa)
Sat. Liquid
hf
Evap.
h fg
Sat. Vapor
hg
Sat. Liquid
sf
Evap.
s fg
Sat. Vapor
sg
195
200
205
210
215
220
225
230
235
240
245
250
255
260
265
270
275
280
285
290
295
300
305
310
315
320
325
330
335
340
345
350
355
360
365
370
374.1
1397.8
1553.8
1723.0
1906.3
2104.2
2317.8
2547.7
2794.9
3060.1
3344.2
3648.2
3973.0
4319.5
4688.6
5081.3
5498.7
5941.8
6411.7
6909.4
7436.0
7992.8
8581.0
9201.8
9856.6
10547
11274
12040
12845
13694
14586
15525
16514
17554
18651
19807
21028
22089
829.96
852.43
875.03
897.75
920.61
943.61
966.77
990.10
1013.61
1037.31
1061.21
1085.34
1109.72
1134.35
1159.27
1184.49
1210.05
1235.97
1262.29
1289.04
1316.27
1344.01
1372.33
1401.29
1430.97
1461.45
1492.84
1525.29
1558.98
1594.15
1631.17
1670.54
1713.13
1760.48
1815.96
1890.37
2099.26
1959.99
1940.75
1921.00
1900.73
1879.91
1858.51
1836.50
1813.85
1790.53
1766.50
1741.73
1716.18
1689.80
1662.54
1634.34
1605.16
1574.92
1543.55
1510.97
1477.08
1441.78
1404.93
1366.38
1325.97
1283.48
1238.64
1191.13
1140.56
1086.37
1027.86
964.02
893.38
813.59
720.52
605.44
441.75
0
2789.96
2793.18
2796.03
2798.48
2800.51
2802.12
2803.27
2803.95
2804.13
2803.81
2802.95
2801.52
2799.51
2796.89
2793.61
2789.65
2784.97
2779.53
2773.27
2766.13
2758.05
2748.94
2738.72
2727.27
2714.44
2700.08
2683.97
2665.85
2645.35
2622.01
2595.19
2563.92
2526.72
2481.00
2421.40
2332.12
2099.26
2.2835
2.3308
2.3779
2.4247
2.4713
2.5177
2.5639
2.6099
2.6557
2.7015
2.7471
2.7927
2.8382
2.8837
2.9293
2.9750
3.0208
3.0667
3.1129
3.1593
3.2061
3.2533
3.3009
3.3492
3.3981
3.4479
3.4987
3.5506
3.6040
3.6593
3.7169
3.7776
3.8427
3.9146
3.9983
4.1104
4.4297
4.1863
4.1014
4.0172
3.9337
3.8507
3.7683
3.6863
3.6047
3.5233
3.4422
3.3612
3.2802
3.1992
3.1181
3.0368
2.9551
2.8730
2.7903
2.7069
2.6227
2.5375
2.4511
2.3633
2.2737
2.1821
2.0882
1.9913
1.8909
1.7863
1.6763
1.5594
1.4336
1.2951
1.1379
0.9487
0.6868
0
6.4697
6.4322
6.3951
6.3584
6.3221
6.2860
6.2502
6.2146
6.1791
6.1436
6.1083
6.0729
6.0374
6.0018
5.9661
5.9301
5.8937
5.8570
5.8198
5.7821
5.7436
5.7044
5.6642
5.6229
5.5803
5.5361
5.4900
5.4416
5.3903
5.3356
5.2763
5.2111
5.1378
5.0525
4.9470
4.7972
4.4297
⑦
APPENDIX B
..............780
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.1.2
Saturated Water Pressure Entry
Specific Volume, m3 /kg
Internal Energy, kJ/kg
Press.
(kPa)
Temp.
(◦ C)
Sat. Liquid
vf
Evap.
vfg
Sat. Vapor
vg
Sat. Liquid
uf
Evap.
u fg
Sat. Vapor
ug
0.6113
1
1.5
2
2.5
3
4
5
7.5
10
15
20
25
30
40
50
75
100
125
150
175
200
225
250
275
300
325
350
375
400
450
500
550
600
650
700
750
800
0.01
6.98
13.03
17.50
21.08
24.08
28.96
32.88
40.29
45.81
53.97
60.06
64.97
69.10
75.87
81.33
91.77
99.62
105.99
111.37
116.06
120.23
124.00
127.43
130.60
133.55
136.30
138.88
141.32
143.63
147.93
151.86
155.48
158.85
162.01
164.97
167.77
170.43
0.001000
0.001000
0.001001
0.001001
0.001002
0.001003
0.001004
0.001005
0.001008
0.001010
0.001014
0.001017
0.001020
0.001022
0.001026
0.001030
0.001037
0.001043
0.001048
0.001053
0.001057
0.001061
0.001064
0.001067
0.001070
0.001073
0.001076
0.001079
0.001081
0.001084
0.001088
0.001093
0.001097
0.001101
0.001104
0.001108
0.001111
0.001115
206.131
129.20702
87.97913
67.00285
54.25285
45.66402
34.79915
28.19150
19.23674
14.67254
10.02117
7.64835
6.20322
5.22816
3.99243
3.23931
2.21607
1.69296
1.37385
1.15828
1.00257
0.88467
0.79219
0.71765
0.65624
0.60475
0.56093
0.52317
0.49029
0.46138
0.41289
0.37380
0.34159
0.31457
0.29158
0.27176
0.25449
0.23931
206.132
129.20802
87.98013
67.00385
54.25385
45.66502
34.80015
28.19251
19.23775
14.67355
10.02218
7.64937
6.20424
5.22918
3.99345
3.24034
2.21711
1.69400
1.37490
1.15933
1.00363
0.88573
0.79325
0.71871
0.65731
0.60582
0.56201
0.52425
0.49137
0.46246
0.41398
0.37489
0.34268
0.31567
0.29268
0.27286
0.25560
0.24043
0
29.29
54.70
73.47
88.47
101.03
121.44
137.79
168.76
191.79
225.90
251.35
271.88
289.18
317.51
340.42
394.29
417.33
444.16
466.92
486.78
504.47
520.45
535.08
548.57
561.13
572.88
583.93
594.38
604.29
622.75
639.66
655.30
669.88
683.55
696.43
708.62
720.20
2375.3
2355.69
2338.63
2326.02
2315.93
2307.48
2293.73
2282.70
2261.74
2246.10
2222.83
2205.36
2191.21
2179.22
2159.49
2143.43
2112.39
2088.72
2069.32
2052.72
2038.12
2025.02
2013.10
2002.14
1991.95
1982.43
1973.46
1964.98
1956.93
1949.26
1934.87
1921.57
1909.17
1897.52
1886.51
1876.07
1866.11
1856.58
2375.3
2384.98
2393.32
2399.48
2404.40
2408.51
2415.17
2420.49
2430.50
2437.89
2448.73
2456.71
2463.08
2468.40
2477.00
2483.85
2496.67
2506.06
2513.48
2519.64
2524.90
2529.49
2533.56
2537.21
2540.53
2543.55
2546.34
2548.92
2551.31
2553.55
2557.62
2561.23
2564.47
2567.40
2570.06
2572.49
2574.73
2576.79
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.1.2 (continued )
..............
⑦
781
Saturated Water Pressure Entry
Enthalpy, kJ/kg
Entropy, kJ/kg-K
Press.
(kPa)
Temp.
(◦ C)
Sat. Liquid
hf
Evap.
h fg
Sat. Vapor
hg
Sat. Liquid
sf
Evap.
s fg
Sat. Vapor
sg
0.6113
1.0
1.5
2.0
2.5
3.0
4.0
5.0
7.5
10
15
20
25
30
40
50
75
100
125
150
175
200
225
250
275
300
325
350
375
400
450
500
550
600
650
700
750
800
0.01
6.98
13.03
17.50
21.08
24.08
28.96
32.88
40.29
45.81
53.97
60.06
64.97
69.10
75.87
81.33
91.77
99.62
105.99
111.37
116.06
120.23
124.00
127.43
130.60
133.55
136.30
138.88
141.32
143.63
147.93
151.86
155.48
158.85
162.01
164.97
167.77
170.43
0.00
29.29
54.70
73.47
88.47
101.03
121.44
137.79
168.77
191.81
225.91
251.38
271.90
289.21
317.55
340.47
384.36
417.44
444.30
467.08
486.97
504.68
520.69
535.34
548.87
561.45
573.23
584.31
594.79
604.73
623.24
640.21
655.91
670.54
684.26
697.20
709.45
721.10
2501.3
2484.89
2470.59
2460.02
2451.56
2444.47
2432.93
2423.66
2406.02
2392.82
2373.14
2358.33
2346.29
2336.07
2319.19
2305.40
2278.59
2258.02
2241.05
2226.46
2213.57
2201.96
2191.35
2181.55
2172.42
2163.85
2155.76
2148.10
2140.79
2133.81
2120.67
2108.47
2097.04
2086.26
2076.04
2066.30
2056.98
2048.04
2501.3
2514.18
2525.30
2533.49
2540.03
2545.50
2554.37
2561.45
2574.79
2584.63
2599.06
2609.70
2618.19
2625.28
2636.74
2645.87
2662.96
2675.46
2685.35
2693.54
2700.53
2706.63
2712.04
2716.89
2721.29
2725.30
2728.99
2732.40
2735.58
2738.53
2743.91
2748.67
2752.94
2756.80
2760.30
2763.50
2766.43
2769.13
0
0.1059
0.1956
0.2607
0.3120
0.3545
0.4226
0.4763
0.5763
0.6492
0.7548
0.8319
0.8930
0.9439
1.0258
1.0910
1.2129
1.3025
1.3739
1.4335
1.4848
1.5300
1.5705
1.6072
1.6407
1.6717
1.7005
1.7274
1.7527
1.7766
1.8206
1.8606
1.8972
1.9311
1.9627
1.9922
2.0199
2.0461
9.1562
8.8697
8.6322
8.4629
8.3311
8.2231
8.0520
7.9187
7.6751
7.5010
7.2536
7.0766
6.9383
6.8247
6.6441
6.5029
6.2434
6.0568
5.9104
5.7897
5.6868
5.5970
5.5173
5.4455
5.3801
5.3201
5.2646
5.2130
5.1647
5.1193
5.0359
4.9606
4.8920
4.8289
4.7704
4.7158
4.6647
4.6166
9.1562
8.9756
8.8278
8.7236
8.6431
8.5775
8.4746
8.3950
8.2514
8.1501
8.0084
7.9085
7.8313
7.7686
7.6700
7.5939
7.4563
7.3593
7.2843
7.2232
7.1717
7.1271
7.0878
7.0526
7.0208
6.9918
6.9651
6.9404
6.9174
6.8958
6.8565
6.8212
6.7892
6.7600
6.7330
6.7080
6.6846
6.6627
⑦
APPENDIX B
..............782
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.1.2 (continued )
Saturated Water Pressure Entry
Specific Volume, m3 /kg
Internal Energy, kJ/kg
Press.
(kPa)
Temp.
(◦ C)
Sat. Liquid
vf
Evap.
v fg
Sat. Vapor
vg
Sat. Liquid
uf
Evap.
u fg
Sat. Vapor
ug
850
900
950
1000
1100
1200
1300
1400
1500
1750
2000
2250
2500
2750
3000
3250
3500
4000
5000
6000
7000
8000
9000
10000
11000
12000
13000
14000
15000
16000
17000
18000
19000
20000
21000
22000
22089
172.96
175.38
177.69
179.91
184.09
187.99
191.64
195.07
198.32
205.76
212.42
218.45
223.99
229.12
233.90
238.38
242.60
250.40
263.99
275.64
285.88
295.06
303.40
311.06
318.15
324.75
330.93
336.75
342.24
347.43
352.37
357.06
361.54
365.81
369.89
373.80
374.14
0.001118
0.001121
0.001124
0.001127
0.001133
0.001139
0.001144
0.001149
0.001154
0.001166
0.001177
0.001187
0.001197
0.001207
0.001216
0.001226
0.001235
0.001252
0.001286
0.001319
0.001351
0.001384
0.001418
0.001452
0.001489
0.001527
0.001567
0.001611
0.001658
0.001711
0.001770
0.001840
0.001924
0.002035
0.002206
0.002808
0.003155
0.22586
0.21385
0.20306
0.19332
0.17639
0.16220
0.15011
0.13969
0.13062
0.11232
0.09845
0.08756
0.07878
0.07154
0.06546
0.06029
0.05583
0.04853
0.03815
0.03112
0.02602
0.02213
0.01907
0.01657
0.01450
0.01274
0.01121
0.00987
0.00868
0.00760
0.00659
0.00565
0.00473
0.00380
0.00275
0.00072
0
0.22698
0.21497
0.20419
0.19444
0.17753
0.16333
0.15125
0.14084
0.13177
0.11349
0.09963
0.08875
0.07998
0.07275
0.06668
0.06152
0.05707
0.04978
0.03944
0.03244
0.02737
0.02352
0.02048
0.01803
0.01599
0.01426
0.01278
0.01149
0.01034
0.00931
0.00836
0.00749
0.00666
0.00583
0.00495
0.00353
0.00315
731.25
741.81
751.94
761.67
780.08
797.27
813.42
828.68
843.14
876.44
906.42
933.81
959.09
982.65
1004.76
1025.62
1045.41
1082.28
1147.78
1205.41
1257.51
1305.54
1350.47
1393.00
1433.68
1472.92
1511.09
1548.53
1585.58
1622.63
1660.16
1698.86
1739.87
1785.47
1841.97
1973.16
2029.58
1847.45
1838.65
1830.17
1821.97
1806.32
1791.55
1777.53
1764.15
1751.3
1721.39
1693.84
1668.18
1644.04
1621.16
1599.34
1578.43
1558.29
1519.99
1449.34
1384.27
1322.97
1264.25
1207.28
1151.40
1096.06
1040.76
984.99
928.23
869.85
809.07
744.80
675.42
598.18
507.58
388.74
108.24
0
2578.69
2580.46
2582.11
2583.64
2586.40
2588.82
2590.95
2592.83
2594.5
2597.83
2600.26
2601.98
2603.13
2603.81
2604.10
2604.04
2603.70
2602.27
2597.12
2589.69
2580.48
2569.79
2557.75
2544.41
2529.74
2513.67
2496.08
2476.76
2455.43
2431.70
2404.96
2374.28
2338.05
2293.05
2230.71
2081.39
2029.58
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.1.2 (continued )
..............
⑦
783
Saturated Water Pressure Entry
Enthalpy, kJ/kg
Entropy, kJ/kg-K
Press.
(kPa)
Temp.
(◦ C)
Sat. Liquid
hf
Evap.
hfg
Sat. Vapor
hg
Sat. Liquid
sf
Evap.
s fg
Sat. Vapor
sg
850
900
950
1000
1100
1200
1300
1400
1500
1750
2000
2250
2500
2750
3000
3250
3500
4000
5000
6000
7000
8000
9000
10000
11000
12000
13000
14000
15000
16000
17000
18000
19000
20000
21000
22000
22089
172.96
175.38
177.69
179.91
184.09
187.99
191.64
195.07
198.32
205.76
212.42
218.45
223.99
229.12
233.90
238.38
242.60
250.40
263.99
275.64
285.88
295.06
303.40
311.06
318.15
324.75
330.93
336.75
342.24
347.43
352.37
357.06
361.54
365.81
369.89
373.80
374.14
732.20
742.82
753.00
762.79
781.32
798.64
814.91
830.29
844.87
878.48
908.77
936.48
962.09
985.97
1008.41
1029.60
1049.73
1087.29
1154.21
1213.32
1266.97
1316.61
1363.23
1407.53
1450.05
1491.24
1531.46
1571.08
1610.45
1650.00
1690.25
1731.97
1776.43
1826.18
1888.30
2034.92
2099.26
2039.43
2031.12
2023.08
2015.29
2000.36
1986.19
1972.67
1959.72
1947.28
1917.95
1890.74
1865.19
1840.98
1817.89
1795.73
1774.37
1753.70
1714.09
1640.12
1571.00
1505.10
1441.33
1378.88
1317.14
1255.55
1193.59
1130.76
1066.47
1000.04
930.59
856.90
777.13
688.11
583.56
446.42
124.04
0
2771.63
2773.94
2776.08
2778.08
2781.68
2784.82
2787.58
2790.00
2792.15
2796.43
2799.51
2801.67
2803.07
2803.86
2804.14
2803.97
2803.43
2801.38
2794.33
2784.33
2772.07
2757.94
2742.11
2724.67
2705.60
2684.83
2662.22
2637.55
2610.49
2580.59
2547.15
2509.09
2464.54
2409.74
2334.72
2158.97
2099.26
2.0709
2.0946
2.1171
2.1386
2.1791
2.2165
2.2514
2.2842
2.3150
2.3851
2.4473
2.5034
2.5546
2.6018
2.6456
2.6866
2.7252
2.7963
2.9201
3.0266
3.1210
3.2067
3.2857
3.3595
3.4294
3.4961
3.5604
3.6231
3.6847
3.7460
3.8078
3.8713
3.9387
4.0137
4.1073
4.3307
4.4297
4.5711
4.5280
4.4869
4.4478
4.3744
4.3067
4.2438
4.1850
4.1298
4.0044
3.8935
3.7938
3.7028
3.6190
3.5412
3.4685
3.4000
3.2737
3.0532
2.8625
2.6922
2.5365
2.3915
2.2545
2.1233
1.9962
1.8718
1.7485
1.6250
1.4995
1.3698
1.2330
1.0841
0.9132
0.6942
0.1917
0
6.6421
6.6225
6.6040
6.5864
6.5535
6.5233
6.4953
6.4692
6.4448
6.3895
6.3408
6.2971
6.2574
6.2208
6.1869
6.1551
6.1252
6.0700
5.9733
5.8891
5.8132
5.7431
5.6771
5.6140
5.5527
5.4923
5.4323
5.3716
5.3097
5.2454
5.1776
5.1044
5.0227
4.9269
4.8015
4.5224
4.4297
⑦
APPENDIX B
..............784
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.1.3
Superheated Vapor Water
Temp.
(◦ C)
Sat.
50
100
150
200
250
300
400
500
600
700
800
900
1000
1100
1200
1300
v
(m3 /kg)
14.67355
14.86920
17.19561
19.51251
21.82507
24.13559
26.44508
31.06252
35.67896
40.29488
44.91052
49.52599
54.14137
58.75669
63.37198
67.98724
72.60250
u
(kJ/kg)
h
(kJ/kg)
P = 10 kPa (45.81◦ C)
2437.89
2443.87
2515.50
2587.86
2661.27
2735.95
2812.06
2968.89
3132.26
3302.45
3479.63
3663.84
3855.03
4053.01
4257.47
4467.91
4683.68
2584.63
2592.56
2687.46
2782.99
2879.52
2977.31
3076.51
3279.51
3489.05
3705.40
3928.73
4159.10
4396.44
4640.58
4891.19
5147.78
5409.70
s
(kJ/kg-K)
8.1501
8.1749
8.4479
8.6881
8.9037
9.1002
9.2812
9.6076
9.8977
10.1608
10.4028
10.6281
10.8395
11.0392
11.2287
11.4090
14.5810
v
(m3 /kg)
3.24034
—
3.41833
3.88937
4.35595
4.82045
5.28391
6.20929
7.13364
8.05748
8.98104
9.90444
10.82773
11.75097
12.67418
13.59737
14.52054
100 kPa (99.62◦ C)
Sat.
150
200
250
300
400
500
600
700
800
900
1000
1100
1200
1300
1.69400
1.93636
2.17226
2.40604
2.63876
3.10263
3.56547
4.02781
4.48986
4.95174
5.41353
5.87526
6.33696
6.79863
7.26030
2506.06
2582.75
2658.05
2733.73
2810.41
2967.85
3131.54
3301.94
3479.24
3663.53
3854.77
4052.78
4257.25
4467.70
4683.47
2675.46
2776.38
2875.27
2974.33
3074.28
3278.11
3488.09
3704.72
3928.23
4158.71
4396.12
4640.31
4890.95
5147.56
5409.49
0.60582
0.63388
0.71629
2543.55
2570.79
2650.65
2725.30
2760.95
2865.54
h
(kJ/kg)
P = 50 kPa (81.33◦ C)
2483.85
—
2511.61
2585.61
2659.85
2734.97
2811.33
2968.43
3131.94
3302.22
3479.45
3663.70
3854.91
4052.91
4257.37
4467.82
4683.58
2645.87
—
2682.52
2780.08
2877.64
2975.99
3075.52
3278.89
3488.62
3705.10
3928.51
4158.92
4396.30
4640.46
4891.08
5147.69
5409.61
s
(kJ/kg-K)
7.5939
—
7.6947
7.9400
8.1579
8.3555
8.5372
8.8641
9.1545
9.4177
9.6599
9.8852
10.0967
10.2964
10.4858
10.6662
10.8382
200 kPa (120.23◦ C)
7.3593
7.6133
7.8342
8.0332
8.2157
8.5434
8.8341
9.0975
9.3398
9.5652
9.7767
9.9764
10.1658
10.3462
10.5182
0.88573
0.95964
1.08034
1.19880
1.31616
1.54930
1.78139
2.01297
2.24426
2.47539
2.70643
2.93740
3.16834
3.39927
3.63018
300 kPa (133.55◦ C)
Sat.
150
200
u
(kJ/kg)
2529.49
2576.87
2654.39
2731.22
2808.55
2966.69
3130.75
3301.36
3478.81
3663.19
3854.49
4052.53
4257.01
4467.46
4683.23
2706.63
2768.80
2870.46
2970.98
3071.79
3276.55
3487.03
3703.96
3927.66
4158.27
4395.77
4640.01
4890.68
5147.32
5409.26
7.1271
7.2795
7.5066
7.7085
7.8926
8.2217
8.5132
8.7769
9.0194
9.2450
9.4565
9.6563
9.8458
10.0262
10.1982
400 kPa (143.63◦ C)
6.9918
7.0778
7.3115
0.46246
0.47084
0.53422
2553.55
2564.48
2646.83
2738.53
2752.82
2860.51
6.8958
6.9299
7.1706
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.1.3 (continued )
..............
⑦
785
Superheated Vapor Water
Temp.
(◦ C)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
300 kPa (133.55◦ C)
250
300
400
500
600
700
800
900
1000
1100
1200
1300
0.79636
0.87529
1.03151
1.18669
1.34136
1.49573
1.64994
1.80406
1.95812
2.11214
2.26614
2.42013
2728.69
2806.69
2965.53
3129.95
3300.79
3478.38
3662.85
3854.20
4052.27
4256.77
4467.23
4682.99
2967.59
3069.28
3274.98
3485.96
3703.20
3927.10
4157.83
4395.42
4639.71
4890.41
5147.07
5409.03
0.37489
0.42492
0.47436
0.52256
0.57012
0.61728
0.71093
0.80406
0.89691
0.98959
1.08217
1.17469
1.26718
1.35964
1.45210
2561.23
2642.91
2723.50
2802.91
2882.59
2963.19
3128.35
3299.64
3477.52
3662.17
3853.63
4051.76
4256.29
4466.76
4682.52
2748.67
2855.37
2960.68
3064.20
3167.65
3271.83
3483.82
3701.67
3925.97
4156.96
4394.71
4639.11
4889.88
5146.58
5408.57
7.5165
7.7022
8.0329
8.3250
8.5892
8.8319
9.0575
9.2691
9.4689
9.6585
9.8389
10.0109
0.59512
0.65484
0.77262
0.88934
1.00555
1.12147
1.23722
1.35288
1.46847
1.58404
1.69958
1.81511
0.24043
0.26080
0.29314
0.32411
0.35439
0.38426
0.44331
0.50184
2576.79
2630.61
2715.46
2797.14
2878.16
2959.66
3125.95
3297.91
2769.13
2839.25
2949.97
3056.43
3161.68
3267.07
3480.60
3699.38
s
(kJ/kg-K)
2726.11
2804.81
2964.36
3129.15
3300.22
3477.95
3662.51
3853.91
4052.02
4256.53
4466.99
4682.75
2964.16
3066.75
3273.41
3484.89
3702.44
3926.53
4157.40
4395.06
4639.41
4890.15
5146.83
5408.80
7.3788
7.5661
7.8984
8.1912
8.4557
8.6987
8.9244
9.1361
9.3360
9.5255
9.7059
9.8780
600 kPa (158.85◦ C)
6.8212
7.0592
7.2708
7.4598
7.6328
7.7937
8.0872
8.3521
8.5952
8.8211
9.0329
9.2328
9.4224
9.6028
9.7749
0.31567
0.35202
0.39383
0.43437
0.47424
0.51372
0.59199
0.66974
0.74720
0.82450
0.90169
0.97883
1.05594
1.13302
1.21009
800 kPa (170.43◦ C)
Sat.
200
250
300
350
400
500
600
h
(kJ/kg)
400 kPa (143.63◦ C)
500 kPa (15 1.86◦ C)
Sat.
200
250
300
350
400
500
600
700
800
900
1000
1100
1200
1300
u
(kJ/kg)
2567.40
2638.91
2720.86
2801.00
2881.12
2962.02
3127.55
3299.07
3477.08
3661.83
3853.34
4051.51
4256.05
4466.52
4682.28
2756.80
2850.12
2957.16
3061.63
3165.66
3270.25
3482.75
3700.91
3925.41
4156.52
4394.36
4638.81
4889.61
5146.34
5408.34
6.7600
6.9665
7.1816
7.3723
7.5463
7.7078
8.0020
8.2673
8.5107
8.7367
8.9485
9.1484
9.3381
9.5185
9.6906
1000 kPa (179.91◦ C)
6.6627
6.8158
7.0384
7.2327
7.4088
7.5715
7.8672
8.1332
0.19444
0.20596
0.23268
0.25794
0.28247
0.30659
0.35411
0.40109
2583.64
2621.90
2709.91
2793.21
2875.18
2957.29
3124.34
3296.76
2778.08
2827.86
2942.59
3051.15
3157.65
3263.88
3478.44
3697.85
6.5864
6.6939
6.9246
7.1228
7.3010
7.4650
7.7621
8.0289
⑦
APPENDIX B
..............786
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.1.3 (continued )
Superheated Vapor Water
Temp.
(◦ C)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
800 kPa (170.43◦ C)
700
800
900
1000
1100
1200
1300
0.56007
0.61813
0.67610
0.73401
0.79188
0.84974
0.90758
3476.22
3661.14
3852.77
4051.00
4255.57
4466.05
4681.81
3924.27
4155.65
4393.65
4638.20
4889.08
5145.85
5407.87
0.16333
0.16930
0.19235
0.21382
0.23452
0.25480
0.29463
0.33393
0.37294
0.41177
0.45051
0.48919
0.52783
0.56646
0.60507
2588.82
2612.74
2704.20
2789.22
2872.16
2954.90
3122.72
3295.60
3474.48
3659.77
3851.62
4049.98
4254.61
4465.12
4680.86
2784.82
2815.90
2935.01
3045.80
3153.59
3260.66
3476.28
3696.32
3922.01
4153.90
4392.23
4637.00
4888.02
5144.87
5406.95
8.3770
8.6033
8.8153
9.0153
9.2049
9.3854
9.5575
0.44779
0.49432
0.54075
0.58712
0.63345
0.67977
0.72608
0.12380
0.14184
0.15862
0.17456
0.19005
0.22029
0.24998
0.27937
0.30859
0.33772
0.36678
0.39581
0.42482
0.45382
2595.95
2692.26
2781.03
2866.05
2950.09
3119.47
3293.27
3472.74
3658.40
3850.47
4048.96
4253.66
4464.18
4679.92
2794.02
2919.20
3034.83
3145.35
3254.17
3471.93
3693.23
3919.73
4152.15
4390.82
4635.81
4886.95
5143.89
5406.02
s
(kJ/kg-K)
3475.35
3660.46
3852.19
4050.49
4255.09
4465.58
4681.33
3923.14
4154.78
4392.94
4637.60
4888.55
5145.36
5407.41
8.2731
8.4996
8.7118
8.9119
9.1016
9.2821
9.4542
1400 kPa (195.07◦ C)
6.5233
6.5898
6.8293
7.0316
7.2120
7.3773
7.6758
7.9434
8.1881
8.4149
8.6272
8.8274
9.0171
9.1977
9.3698
0.14084
0.14302
0.16350
0.18228
0.20026
0.21780
0.25215
0.28596
0.31947
0.35281
0.38606
0.41924
0.45239
0.48552
0.51864
1600 kPa (201.40)◦ C)
Sat.
250
300
350
400
500
600
700
800
900
1000
1100
1200
1300
h
(kJ/kg)
1000 kPa (179.91◦ C)
1200 kPa (187.99◦ C)
Sat.
200
250
300
350
400
500
600
700
800
900
1000
1100
1200
1300
u
(kJ/kg)
2592.83
2603.09
2698.32
2785.16
2869.12
2952.50
3121.10
3294.44
3473.61
3659.09
3851.05
4049.47
4254.14
4464.65
4680.39
2790.00
2803.32
2927.22
3040.35
3149.49
3257.42
3474.11
3694.78
3920.87
4153.03
4391.53
4636.41
4887.49
5144.38
5406.49
6.4692
6.4975
6.7467
6.9533
7.1359
7.3025
7.6026
7.8710
8.1160
8.3431
8.5555
8.7558
8.9456
9.1262
9.2983
1800 kPa (207.15◦ C)
6.4217
6.6732
6.8844
7.0693
7.2373
7.5389
7.8080
8.0535
8.2808
8.4934
8.6938
8.8837
9.0642
9.2364
0.11042
0.12497
0.14021
0.15457
0.16847
0.19550
0.22199
0.24818
0.27420
0.30012
0.32598
0.35180
0.37761
0.40340
2598.38
2686.02
2776.83
2862.95
2947.66
3117.84
3292.10
3471.87
3657.71
3849.90
4048.45
4253.18
4463.71
4679.44
2797.13
2910.96
3029.21
3141.18
3250.90
3469.75
3691.69
3918.59
4151.27
4390.11
4635.21
4886.42
5143.40
5405.56
6.3793
6.6066
6.8226
7.0099
7.1793
7.4824
7.7523
7.9983
8.2258
8.4386
8.6390
8.8290
9.0096
9.1817
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.1.3 (continued )
..............
⑦
787
Superheated Vapor Water
Temp.
(◦ C)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
2000 kPa (212.42◦ C)
Sat.
250
300
350
400
450
500
600
700
800
900
1000
1100
1200
1300
0.09963
0.11144
0.12547
0.13857
0.15120
0.16353
0.17568
0.19960
0.22323
0.24668
0.27004
0.29333
0.31659
0.33984
0.36306
2600.26
2679.58
2772.56
2859.81
2945.21
3030.41
3116.20
3290.93
3470.99
3657.03
3849.33
4047.94
4252.71
4463.25
4678.97
2799.51
2902.46
3023.50
3136.96
3247.60
3357.48
3467.55
3690.14
3917.45
4150.40
4389.40
4634.61
4885.89
5142.92
5405.10
0.06668
0.07058
0.08114
0.09053
0.09936
0.10787
0.11619
0.13243
0.14838
0.16414
0.17980
0.19541
0.21098
0.22652
0.24206
2604.10
2644.00
2750.05
2843.66
2932.75
3020.38
3107.92
3285.03
3466.59
3653.58
3846.46
4045.40
4250.33
4460.92
4676.63
2804.14
2855.75
2993.48
3115.25
3230.82
3344.00
3456.48
3682.34
3911.72
4146.00
4385.87
4631.63
4883.26
5140.49
5402.81
h
(kJ/kg)
s
(kJ/kg-K)
2500 kPa (223.99◦ C)
6.3408
6.5452
6.7663
6.9562
7.1270
7.2844
7.4316
7.7023
7.9487
8.1766
8.3895
8.5900
8.7800
8.9606
9.1328
0.07998
0.08700
0.09890
0.10976
0.12010
0.13014
0.13998
0.15930
0.17832
0.19716
0.21590
0.23458
0.25322
0.27185
0.29046
3000 kPa (233.90◦ C)
Sat.
250
300
350
400
450
500
600
700
800
900
1000
1100
1200
1300
u
(kJ/kg)
2603.13
2662.55
2761.56
2851.84
2939.03
3025.43
3112.08
3287.99
3468.80
3655.30
3847.89
4046.67
4251.52
4462.08
4677.80
2803.07
2880.06
3008.81
3126.24
3239.28
3350.77
3462.04
3686.25
3914.59
4148.20
4387.64
4633.12
4884.57
5141.70
5403.95
6.2574
6.4084
6.6437
6.8402
7.0147
7.1745
7.3233
7.5960
7.8435
8.0720
8.2853
8.4860
8.6761
8.8569
9.0291
4000 kPa (250.40◦ C)
6.1869
6.2871
6.5389
6.7427
6.9211
7.0833
7.2337
7.5084
7.7571
7.9862
8.1999
8.4009
8.5911
8.7719
8.9442
0.04978
—
0.05884
0.06645
0.07341
0.08003
0.08643
0.09885
0.11095
0.12287
0.13469
0.14645
0.15817
0.16987
0.18156
2602.27
—
2725.33
2826.65
2919.88
3010.13
3099.49
3279.06
3462.15
3650.11
3843.59
4042.87
4247.96
4458.60
4674.29
2801.38
—
2960.68
3092.43
3213.51
3330.23
3445.21
3674.44
3905.94
4141.59
4382.34
4628.65
4880.63
5138.07
5400.52
6.0700
—
6.3614
6.5820
6.7689
6.9362
7.0900
7.3688
7.6198
7.8502
8.0647
8.2661
8.4566
8.6376
8.8099
⑦
APPENDIX B
..............788
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.1.3 (continued )
Superheated Vapor Water
Temp.
(◦ C)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
5000 kPa (263.99◦ C)
Sat.
300
350
400
450
500
550
600
700
800
900
1000
1100
1200
1300
0.03944
0.04532
0.05194
0.05781
0.06330
0.06857
0.07368
0.07869
0.08849
0.09811
0.10762
0.11707
0.12648
0.13587
0.14526
2597.12
2697.94
2808.67
2906.58
2999.64
3090.92
3181.82
3273.01
3457.67
3646.62
3840.71
4040.35
4245.61
4456.30
4671.96
2794.33
2924.53
3068.39
3195.64
3316.15
3433.76
3550.23
3666.47
3900.13
4137.17
4378.82
4625.69
4878.02
5135.67
5398.24
0.02352
0.02426
0.02995
0.03432
0.03817
0.04175
0.04516
0.04845
0.05481
0.06097
0.06702
0.07301
0.07896
0.08489
0.09080
2569.79
2590.93
2747.67
2863.75
2966.66
3064.30
3159.76
3254.43
3444.00
3636.08
3832.08
4032.81
4238.60
4449.45
4665.02
2757.94
2784.98
2987.30
3138.28
3271.99
3398.27
3521.01
3642.03
3882.47
4123.84
4368.26
4616.87
4870.25
5128.54
5391.46
h
(kJ/kg)
s
(kJ/kg-K)
6000 kPa (275.64◦ C)
5.9733
6.2083
6.4492
6.6458
6.8185
6.9758
7.1217
7.2588
7.5122
7.7440
7.9593
8.1612
8.3519
8.5330
8.7055
0.03244
0.03616
0.04223
0.04739
0.05214
0.05665
0.06101
0.06525
0.07352
0.08160
0.08958
0.09749
0.10536
0.11321
0.12106
8000 kPa (295.06◦ C)
Sat.
300
350
400
450
500
550
600
700
800
900
1000
1100
1200
1300
u
(kJ/kg)
2589.69
2667.22
2789.61
2892.81
2988.90
3082.20
3174.57
3266.89
3453.15
3643.12
3837.84
4037.83
4243.26
4454.00
4669.64
2784.33
2884.19
3042.97
3177.17
3301.76
3422.12
3540.62
3658.40
3894.28
4132.74
4375.29
4622.74
4875.42
5133.28
5395.97
5.8891
6.0673
6.3334
6.5407
6.7192
6.8802
7.0287
7.1676
7.4234
7.6566
7.8727
8.0751
8.2661
8.4473
8.6199
10000 kPa (311.06◦ C)
5.7431
5.7905
6.1300
6.3633
6.5550
6.7239
6.8778
7.0205
7.2812
7.5173
7.7350
7.9384
8.1299
8.3115
8.4842
0.01803
—
0.02242
0.02641
0.02975
0.03279
0.03564
0.03837
0.04358
0.04859
0.05349
0.05832
0.06312
0.06789
0.07265
2544.41
—
2699.16
2832.38
2943.32
3045.77
3144.54
3241.68
3434.72
3628.97
3826.32
4027.81
4233.97
4444.93
4660.44
2724.67
—
2923.39
3096.46
3240.83
3373.63
3500.92
3625.34
3870.52
4114.91
4361.24
4611.04
4865.14
5123.84
5386.99
5.6140
—
5.9442
6.2119
6.4189
6.5965
6.7561
6.9028
7.1687
7.4077
7.6272
7.8315
8.0236
8.2054
8.3783
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.1.3 (continued )
..............
⑦
789
Superheated Vapor Water
Temp.
(◦ C)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
15000 kPa (342.24◦ C)
Sat.
350
400
450
500
550
600
650
700
800
900
1000
1100
1200
1300
0.01034
0.01147
0.01565
0.01845
0.02080
0.02293
0.02491
0.02680
0.02861
0.03210
0.03546
0.03875
0.04200
0.04523
0.04845
2455.43
2520.36
2740.70
2879.47
2996.52
3104.71
3208.64
3310.37
3410.94
3610.99
3811.89
4015.41
4222.55
4433.78
4649.12
2610.49
2692.41
2975.44
3156.15
3308.53
3448.61
3582.30
3712.32
3840.12
4092.43
4343.75
4596.63
4852.56
5112.27
5375.94
0.001789
0.002790
0.005304
0.006735
0.008679
0.010168
0.011446
0.012596
0.013661
0.015623
0.017448
0.019196
0.020903
0.022589
0.024266
1737.75
2067.34
2455.06
2619.30
2820.67
2970.31
3100.53
3221.04
3335.84
3555.60
3768.48
3978.79
4189.18
4401.29
4615.96
1791.43
2151.04
2614.17
2821.35
3081.03
3275.36
3443.91
3598.93
3745.67
4024.31
4291.93
4554.68
4816.28
5078.97
5343.95
h
(kJ/kg)
s
(kJ/kg-K)
20000 kPa (365.81◦ C)
5.3097
5.4420
5.8810
6.1403
6.3442
6.5198
6.6775
6.8223
6.9572
7.2040
7.4279
7.6347
7.8282
8.0108
8.1839
0.00583
—
0.00994
0.01270
0.01477
0.01656
0.01818
0.01969
0.02113
0.02385
0.02645
0.02897
0.03145
0.03391
0.03636
30000 kPa
375
400
425
450
500
550
600
650
700
800
900
1000
1100
1200
1300
u
(kJ/kg)
2293.05
—
2619.22
2806.16
2942.82
3062.34
3174.00
3281.46
3386.46
3592.73
3797.44
4003.12
4211.30
4422.81
4637.95
2409.74
—
2818.07
3060.06
3238.18
3393.45
3537.57
3675.32
3809.09
4069.80
4326.37
4582.45
4840.24
5100.96
5365.10
4.9269
—
5.5539
5.9016
6.1400
6.3347
6.5048
6.6582
6.7993
7.0544
7.2830
7.4925
7.6874
7.8706
8.0441
40000 kPa
3.9303
4.4728
5.1503
5.4423
5.7904
6.0342
6.2330
6.4057
6.5606
6.8332
7.0717
7.2867
7.4845
7.6691
7.8432
0.001641
0.001908
0.002532
0.003693
0.005623
0.006984
0.008094
0.009064
0.009942
0.011523
0.012963
0.014324
0.015643
0.016940
0.018229
1677.09
1854.52
2096.83
2365.07
2678.36
2869.69
3022.61
3158.04
3283.63
3517.89
3739.42
3954.64
4167.38
4380.11
4594.28
1742.71
1930.83
2198.11
2512.79
2903.26
3149.05
3346.38
3520.58
3681.29
3978.80
4257.93
4527.59
4793.08
5057.72
5323.45
3.8289
4.1134
4.5028
4.9459
5.4699
5.7784
6.0113
6.2054
6.3750
6.6662
6.9150
7.1356
7.3364
7.5224
7.6969
⑦
APPENDIX B
..............790
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.1.4
Compressed Liquid Water
Temp.
(◦ C)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
500 kPa (151.86◦ C)
Sat.
0.01
20
40
60
80
100
120
140
160
180
200
0.001093
0.000999
0.001002
0.001008
0.001017
0.001029
0.001043
0.001060
0.001080
—
—
—
639.66
0.01
83.91
167.47
251.00
334.73
418.80
503.37
588.66
—
—
—
640.21
0.51
84.41
167.98
251.51
335.24
419.32
503.90
589.20
—
—
—
0.001286
0.000998
0.001000
0.001006
0.001015
0.001027
0.001041
0.001058
0.001077
0.001099
0.001124
0.001153
0.001187
0.001226
0.001275
1147.78
0.03
83.64
166.93
250.21
333.69
417.50
501.79
586.74
672.61
759.62
848.08
938.43
1031.34
1127.92
1154.21
5.02
88.64
171.95
255.28
338.83
422.71
507.07
592.13
678.10
765.24
853.85
944.36
1037.47
1134.30
h
(kJ/kg)
s
(kJ/kg-K)
2000 kPa (212.42◦ C)
1.8606
0.0000
0.2965
0.5722
0.8308
1.0749
1.3065
1.5273
1.7389
—
—
—
0.001177
0.000999
0.001001
0.001007
0.001016
0.001028
0.001043
0.001059
0.001079
0.001101
0.001127
0.001156
5000 kPa (263.99◦ C)
Sat
0
20
40
60
80
100
120
140
160
180
200
220
240
260
280
300
u
(kJ/kg)
906.42
0.03
83.82
167.29
250.73
334.38
418.36
502.84
588.02
674.14
761.46
850.30
908.77
2.03
85.82
169.30
252.77
336.44
420.45
504.96
590.18
676.34
763.71
852.61
2.4473
0.0001
.2962
.5716
.8300
1.0739
1.3053
1.5259
1.7373
1.9410
2.1382
2.3301
10000 kPa (311.06◦ C)
2.9201
0.0001
0.2955
0.5705
0.8284
1.0719
1.3030
1.5232
1.7342
1.9374
2.1341
2.3254
2.5128
2.6978
2.8829
0.001452
0.000995
0.000997
0.001003
0.001013
0.001025
0.001039
0.001055
0.001074
0.001195
0.001120
0.001148
0.001181
0.001219
0.001265
0.001322
0.001397
1393.00
0.10
83.35
166.33
249.34
332.56
416.09
500.07
584.67
670.11
756.63
844.49
934.07
1025.94
1121.03
1220.90
1328.34
1407.53
10.05
93.32
176.36
259.47
342.81
426.48
510.61
595.40
681.07
767.83
855.97
945.88
1038.13
1133.68
1234.11
1342.31
3.3595
0.0003
0.2945
0.5685
0.8258
1.0687
1.2992
1.5188
1.7291
1.9316
2.1274
2.3178
2.5038
2.6872
2.8698
3.0547
3.2468
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.1.4 (continued )
..............
⑦
791
Compressed Liquid Water
Temp.
(◦ C)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
15000 kPa (342.24◦ C)
Sat.
0
20
40
60
80
100
120
140
160
180
200
220
240
260
280
300
320
340
360
0.001658
0.000993
0.000995
0.001001
0.001011
0.001022
0.001036
0.001052
0.001071
0.001092
0.001116
0.001143
0.001175
0.001211
0.001255
0.001308
0.001377
0.001472
0.001631
1585.58
0.15
83.05
165.73
248.49
331.46
414.72
498.39
582.64
667.69
753.74
841.04
929.89
1020.82
1114.59
1212.47
1316.58
1431.05
1567.42
1610.45
15.04
97.97
180.75
263.65
346.79
430.26
514.17
598.70
684.07
770.48
858.18
947.52
1038.99
1133.41
1232.09
1337.23
1453.13
1591.88
0.000986
0.000989
0.000995
0.001004
0.001016
0.001029
0.001044
0.001062
0.001082
0.001105
0.001130
0.001159
0.001192
0.001230
0.001275
0.001330
0.001400
0.001492
0.001627
0.001869
0.25
82.16
164.01
246.03
328.28
410.76
493.58
576.86
660.81
745.57
831.34
918.32
1006.84
1097.38
1190.69
1287.89
1390.64
1501.71
1626.57
1781.35
29.82
111.82
193.87
276.16
358.75
441.63
524.91
608.73
693.27
778.71
865.24
953.09
1042.60
1134.29
1228.96
1327.80
1432.63
1546.47
1675.36
1837.43
h
(kJ/kg)
s
(kJ/kg-K)
20000 kPa (365.81◦ C)
3.6847
0.0004
0.2934
0.5665
0.8231
1.0655
1.2954
1.5144
1.7241
1.9259
2.1209
2.3103
2.4952
2.6770
2.8575
3.0392
3.2259
3.4246
3.6545
0.002035
0.000990
0.000993
0.000999
0.001008
0.001020
0.001034
0.001050
0.001068
0.001089
0.001112
0.001139
0.001169
0.001205
0.001246
0.001297
0.001360
0.001444
0.001568
0.001823
30000 kPa
0
20
40
60
80
100
120
140
160
180
200
220
240
260
280
300
320
340
360
380
u
(kJ/kg)
1785.47
0.20
82.75
165.15
247.66
330.38
413.37
496.75
580.67
665.34
750.94
837.70
925.89
1015.94
1108.53
1204.69
1306.10
1415.66
1539.64
1702.78
1826.18
20.00
102.61
185.14
267.82
350.78
434.04
517.74
602.03
687.11
773.18
860.47
949.27
1040.04
1133.45
1230.62
1333.29
1444.53
1571.01
1739.23
4.0137
0.0004
0.2922
0.5646
0.8205
1.0623
1.2917
1.5101
1.7192
1.9203
2.1146
2.3031
2.4869
2.6673
2.8459
3.0248
3.2071
3.3978
3.6074
3.8770
50000 kPa
0.0001
0.2898
0.5606
0.8153
1.0561
1.2844
1.5017
1.7097
1.9095
2.1024
2.2892
2.4710
2.6489
2.8242
2.9985
3.1740
3.3538
3.5425
3.7492
4.0010
0.000977
0.000980
0.000987
0.000996
0.001007
0.001020
0.001035
0.001052
0.001070
0.001091
0.001115
0.001141
0.001170
0.001203
0.001242
0.001286
0.001339
0.001403
0.001484
0.001588
0.20
80.98
161.84
242.96
324.32
405.86
487.63
569.76
652.39
735.68
819.73
904.67
990.69
1078.06
1167.19
1258.66
1353.23
1451.91
1555.97
1667.13
49.03
130.00
211.20
292.77
374.68
456.87
539.37
622.33
705.91
790.24
875.46
961.71
1049.20
1138.23
1229.26
1322.95
1420.17
1522.07
1630.16
1746.54
−0.0014
0.2847
0.5526
0.8051
1.0439
1.2703
1.4857
1.6915
1.8890
2.0793
2.2634
2.4419
2.6158
2.7860
2.9536
3.1200
3.2867
3.4556
3.6290
3.8100
⑦
APPENDIX B
..............792
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.1.5
Saturated Solid-Saturated Vapor, Water
Specific Volume, m3 /kg
Internal Energy, kJ/kg
Temp.
(◦ C)
Press.
(kPa)
Sat. Solid
vi
Evap.
vi g
Sat. Vapor
vg
Sat. Solid
ui
Evap.
ui g
Sat. Vapor
ug
0.01
0
−2
−4
−6
−8
−10
−12
−14
−16
−18
−20
−22
−24
−26
−28
−30
−32
−34
−36
−38
−40
0.6113
0.6108
0.5177
0.4376
0.3689
0.3102
0.2601
0.2176
0.1815
0.1510
0.1252
0.10355
0.08535
0.07012
0.05741
0.04684
0.03810
0.03090
0.02499
0.02016
0.01618
0.01286
0.0010908
0.0010908
0.0010905
0.0010901
0.0010898
0.0010894
0.0010891
0.0010888
0.0010884
0.0010881
0.0010878
0.0010874
0.0010871
0.0010868
0.0010864
0.0010861
0.0010858
0.0010854
0.0010851
0.0010848
0.0010844
0.0010841
206.152
206.314
241.662
283.798
334.138
394.413
466.756
553.802
658.824
785.906
940.182
1128.112
1357.863
1639.752
1986.775
2415.200
2945.227
3601.822
4416.252
5430.115
6707.021
8366.395
206.153
206.315
241.663
283.799
334.139
394.414
466.757
553.803
658.824
785.907
940.183
1128.113
1357.864
1639.753
1986.776
2415.201
2945.228
3601.823
4416.253
5430.116
6707.022
8366.396
−333.40
−333.42
−337.61
−341.78
−345.91
−350.02
−354.09
−358.14
−362.16
−366.14
−370.10
−374.03
−377.93
−381.80
−385.64
−389.45
−393.23
−396.98
−400.71
−404.40
−408.06
−411.70
2708.7
2708.7
2710.2
2711.5
2712.9
2714.2
2715.5
2716.8
2718.0
2719.2
2720.4
2721.6
2722.7
2723.7
2724.8
2725.8
2726.8
2727.8
2728.7
2729.6
2730.5
2731.3
2375.3
2375.3
2372.5
2369.8
2367.0
2364.2
2361.4
2358.7
2355.9
2353.1
2350.3
2347.5
2344.7
2342.0
2339.2
2336.4
2333.6
2330.8
2328.0
2325.2
2322.4
2319.6
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.1.5 (continued )
..............
⑦
793
Saturated Solid-Saturated Vapor, Water
Enthalpy, kJ/kg
Entropy, kJ/kg-K
Temp.
(◦ C)
Press.
(kPa)
Sat. Solid
hi
Evap.
hi g
Sat. Vapor
hg
Sat. Solid
si
Evap.
si g
Sat. Vapor
sg
0.01
0
−2
−4
−6
−8
−10
−12
−14
−16
−18
−20
−22
−24
−26
−28
−30
−32
−34
−36
−38
−40
0.6113
0.6108
0.5177
0.4376
0.3689
0.3102
0.2601
0.2176
0.1815
0.1510
0.1252
0.10355
0.08535
0.07012
0.05741
0.04684
0.03810
0.03090
0.02499
0.02016
0.01618
0.01286
−333.40
−333.42
−337.61
−341.78
−345.91
−350.02
−354.09
−358.14
−362.16
−366.14
−370.10
−374.03
−377.93
−381.80
−385.64
−389.45
−393.23
−396.98
−400.71
−404.40
−408.06
−411.70
2834.7
2834.8
2835.3
2835.7
2836.2
2836.6
2837.0
2837.3
2837.6
2837.9
2838.2
2838.4
2838.6
2838.7
2838.9
2839.0
2839.0
2839.1
2839.1
2839.1
2839.0
2838.9
2501.3
2501.3
2497.6
2494.0
2490.3
2486.6
2482.9
2479.2
2475.5
2471.8
2468.1
2464.3
2460.6
2456.9
2453.2
2449.5
2445.8
2442.1
2438.4
2434.7
2431.0
2427.2
−1.2210
−1.2211
−1.2369
−1.2526
−1.2683
−1.2839
−1.2995
−1.3150
−1.3306
−1.3461
−1.3617
−1.3772
−1.3928
−1.4083
−1.4239
−1.4394
−1.4550
−1.4705
−1.4860
−1.5014
−1.5168
−1.5321
10.3772
10.3776
10.4562
10.5358
10.6165
10.6982
10.7809
10.8648
10.9498
11.0359
11.1233
11.2120
11.3020
11.3935
11.4864
11.5808
11.6765
11.7733
11.8713
11.9704
12.0714
12.1768
9.1562
9.1565
9.2193
9.2832
9.3482
9.4143
9.4815
9.5498
9.6192
9.6898
9.7616
9.8348
9.9093
9.9852
10.0625
10.1413
10.2215
10.3028
10.3853
10.4690
10.5546
10.6447
⑦
APPENDIX B
..............794
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.2
Thermodynamic Properties of Ammonia
TABLE B.2.1
Saturated Ammonia
Specific Volume, m3 /kg
Temp.
(◦ C)
Press.
(kPa)
Sat. Liquid
vf
Evap.
v fg
Sat. Vapor
vg
−50
−45
−40
−35
−30
−25
−20
−15
−10
−5
0
5
10
15
20
25
30
35
40
45
50
55
60
65
70
75
80
85
90
95
100
105
110
115
120
125
130
132.3
40.9
54.5
71.7
93.2
119.5
151.6
190.2
236.3
290.9
354.9
429.6
515.9
615.2
728.6
857.5
1003.2
1167.0
1350.4
1554.9
1782.0
2033.1
2310.1
2614.4
2947.8
3312.0
3709.0
4140.5
4608.6
5115.3
5662.9
6253.7
6890.4
7575.7
8313.3
9107.2
9963.5
10891.6
11333.2
0.001424
0.001437
0.001450
0.001463
0.001476
0.001490
0.001504
0.001519
0.001534
0.001550
0.001566
0.001583
0.001600
0.001619
0.001638
0.001658
0.001680
0.001702
0.001725
0.001750
0.001777
0.001804
0.001834
0.001866
0.001900
0.001937
0.001978
0.002022
0.002071
0.002126
0.002188
0.002261
0.002347
0.002452
0.002589
0.002783
0.003122
0.004255
2.62557
2.00489
1.55111
1.21466
0.96192
0.76970
0.62184
0.50686
0.41655
0.34493
0.28763
0.24140
0.20381
0.17300
0.14758
0.12647
0.10881
0.09397
0.08141
0.07073
0.06159
0.05375
0.04697
0.04109
0.03597
0.03148
0.02753
0.02404
0.02093
0.01815
0.01565
0.01337
0.01128
0.00933
0.00744
0.00554
0.00337
0
2.62700
2.00632
1.55256
1.21613
0.96339
0.77119
0.62334
0.50838
0.41808
0.34648
0.28920
0.24299
0.20541
0.17462
0.14922
0.12813
0.11049
0.09567
0.08313
0.07248
0.06337
0.05555
0.04880
0.04296
0.03787
0.03341
0.02951
0.02606
0.02300
0.02028
0.01784
0.01564
0.01363
0.01178
0.01003
0.00833
0.00649
0.00426
Internal Energy, kJ/kg
Sat. Liquid
uf
Evap.
u fg
Sat. Vapor
ug
−43.82
−22.01
−0.10
21.93
44.08
66.36
88.76
111.30
133.96
156.76
179.69
202.77
225.99
249.36
272.89
296.59
320.46
344.50
368.74
393.19
417.87
442.79
467.99
493.51
519.39
545.70
572.50
599.90
627.99
656.95
686.96
718.30
751.37
786.82
825.77
870.69
929.29
1037.62
1309.1
1293.5
1277.6
1261.3
1244.8
1227.9
1210.7
1193.2
1175.2
1157.0
1138.3
1119.2
1099.7
1079.7
1059.3
1038.4
1016.9
994.9
972.2
948.9
924.8
899.9
874.2
847.4
819.5
790.4
759.9
727.8
693.7
657.4
618.4
575.9
529.1
476.2
414.5
337.7
226.9
0
1265.2
1271.4
1277.4
1283.3
1288.9
1294.3
1299.5
1304.5
1309.2
1313.7
1318.0
1322.0
1325.7
1329.1
1332.2
1335.0
1337.4
1339.4
1341.0
1342.1
1342.7
1342.7
1342.1
1340.9
1338.9
1336.1
1332.4
1327.7
1321.7
1314.4
1305.3
1294.2
1280.5
1263.1
1240.3
1208.4
1156.2
1037.6
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.2.1 (continued )
..............
⑦
795
Saturated Ammonia
Enthalpy, kJ/kg
Temp.
(◦ C)
Press.
(kPa)
−50
−45
−40
−35
−30
−25
−20
−15
−10
−5
0
5
10
15
20
25
30
35
40
45
50
55
60
65
70
75
80
85
90
95
100
105
110
115
120
125
130
132.3
40.9
54.5
71.7
93.2
119.5
151.6
190.2
236.3
290.9
354.9
429.6
515.9
615.2
728.6
857.5
1003.2
1167.0
1350.4
1554.9
1782.0
2033.1
2310.1
2614.4
2947.8
3312.0
3709.0
4140.5
4608.6
5115.3
5662.9
6253.7
6890.4
7575.7
8313.3
9107.2
9963.5
10892
11333
Entropy, kJ/kg-K
Sat. Liquid
hf
Evap.
h fg
Sat. Vapor
hg
Sat. Liquid
sf
Evap.
sfg
Sat. Vapor
sg
−43.76
−21.94
0
22.06
44.26
66.58
89.05
111.66
134.41
157.31
180.36
203.58
226.97
250.54
274.30
298.25
322.42
346.80
371.43
396.31
421.48
446.96
472.79
499.01
525.69
552.88
580.69
609.21
638.59
668.99
700.64
733.87
769.15
807.21
849.36
898.42
963.29
1085.85
1416.3
1402.8
1388.8
1374.5
1359.8
1344.6
1329.0
1312.9
1296.4
1279.4
1261.8
1243.7
1225.1
1205.8
1185.9
1165.2
1143.9
1121.8
1098.8
1074.9
1050.0
1024.1
997.0
968.5
938.7
907.2
873.9
838.6
800.8
760.2
716.2
668.1
614.6
553.8
482.3
393.0
263.7
0
1372.6
1380.8
1388.8
1396.5
1404.0
1411.2
1418.0
1424.6
1430.8
1436.7
1442.2
1447.3
1452.0
1456.3
1460.2
1463.5
1466.3
1468.6
1470.2
1471.2
1471.5
1471.0
1469.7
1467.5
1464.4
1460.1
1454.6
1447.8
1439.4
1429.2
1416.9
1402.0
1383.7
1361.0
1331.7
1291.4
1227.0
1085.9
−0.1916
−0.0950
0
0.0935
0.1856
0.2763
0.3657
0.4538
0.5408
0.6266
0.7114
0.7951
0.8779
0.9598
1.0408
1.1210
1.2005
1.2792
1.3574
1.4350
1.5121
1.5888
1.6652
1.7415
1.8178
1.8943
1.9712
2.0488
2.1273
2.2073
2.2893
2.3740
2.4625
2.5566
2.6593
2.7775
2.9326
3.2316
6.3470
6.1484
5.9567
5.7715
5.5922
5.4185
5.2498
5.0859
4.9265
4.7711
4.6195
4.4715
4.3266
4.1846
4.0452
3.9083
3.7734
3.6403
3.5088
3.3786
3.2493
3.1208
2.9925
2.8642
2.7354
2.6058
2.4746
2.3413
2.2051
2.0650
1.9195
1.7667
1.6040
1.4267
1.2268
0.9870
0.6540
0
6.1554
6.0534
5.9567
5.8650
5.7778
5.6947
5.6155
5.5397
5.4673
5.3977
5.3309
5.2666
5.2045
5.1444
5.0860
5.0293
4.9738
4.9196
4.8662
4.8136
4.7614
4.7095
4.6577
4.6057
4.3533
4.5001
4.4458
4.3901
4.3325
4.2723
4.2088
4.1407
4.0665
3.9833
3.8861
3.7645
3.5866
3.2316
⑦
APPENDIX B
..............796
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.2.2
Superheated Ammonia
Temp.
(◦ C)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
50 kPa (−46.53◦ C)
Sat.
−30
−20
−10
0
10
20
30
40
50
60
70
80
100
120
140
160
180
200
2.1752
2.3448
2.4463
2.5471
2.6474
2.7472
2.8466
2.9458
3.0447
3.1435
3.2421
3.3406
3.4390
3.6355
3.8318
4.0280
4.2240
4.4199
4.6157
1269.6
1296.2
1312.3
1328.4
1344.5
1360.7
1377.0
1393.3
1409.8
1426.3
1443.0
1459.9
1476.9
1511.4
1546.6
1582.5
1619.2
1656.7
1694.9
1378.3
1413.4
1434.6
1455.7
1476.9
1498.1
1519.3
1540.6
1562.0
1583.5
1605.1
1626.9
1648.8
1693.2
1738.2
1783.9
1830.4
1877.7
1925.7
0.7787
0.7977
0.8336
0.8689
0.9037
0.9382
0.9723
1.0062
1.0398
1.0734
1.1068
1.1401
1.2065
1.2726
1.3386
1.4044
1.4701
1.5357
1.6013
1294.1
1303.3
1320.7
1337.9
1355.0
1372.0
1389.0
1406.0
1423.0
1440.0
1457.2
1474.4
1509.3
1544.8
1580.9
1617.8
1655.4
1693.7
1732.9
1410.9
1422.9
1445.7
1468.3
1490.6
1512.8
1534.9
1556.9
1578.9
1601.0
1623.2
1645.4
1690.2
1735.6
1781.7
1828.4
1875.9
1924.1
1973.1
h
(kJ/kg)
s
(kJ/kg-K)
100 kPa (−33.60◦ C)
6.0839
6.2333
6.3187
6.4006
6.4795
6.5556
6.6293
6.7008
6.7703
6.8379
6.9038
6.9682
7.0312
7.1533
7.2708
7.3842
7.4941
7.6008
7.7045
1.1381
1.1573
1.2101
1.2621
1.3136
1.3647
1.4153
1.4657
1.5158
1.5658
1.6156
1.6653
1.7148
1.8137
1.9124
2.0109
2.1093
2.2075
2.3057
150 kPa (−25.22◦ C)
Sat.
−20
−10
0
10
20
30
40
50
60
70
80
100
120
140
160
180
200
220
u
(kJ/kg)
1284.9
1291.0
1307.8
1324.6
1341.3
1357.9
1374.5
1391.2
1407.9
1424.7
1441.5
1458.5
1475.6
1510.3
1545.7
1581.7
1618.5
1656.0
1694.3
1398.7
1406.7
1428.8
1450.8
1472.6
1494.4
1516.1
1537.7
1559.5
1581.2
1603.1
1625.1
1647.1
1691.7
1736.9
1782.8
1829.4
1876.8
1924.9
5.8401
5.8734
5.9626
6.0477
6.1291
6.2073
6.2826
6.3553
6.4258
6.4943
6.5609
6.6258
6.6892
6.8120
6.9300
7.0439
7.1540
7.2609
7.3648
200 kPa (−18.86◦ C)
5.6983
5.7465
5.8349
5.9189
5.9992
6.0761
6.1502
6.2217
6.2910
6.3583
6.4238
6.4877
6.6112
6.7297
6.8439
6.9544
7.0615
7.1656
7.2670
0.5946
—
0.6193
0.6465
0.6732
0.6995
0.7255
0.7513
0.7769
0.8023
0.8275
0.8527
0.9028
0.9527
1.0024
1.0519
1.1014
1.1507
1.2000
1300.6
—
1316.7
1334.5
1352.1
1369.5
1386.8
1404.0
1421.3
1438.5
1455.8
1473.1
1508.2
1543.8
1580.1
1617.0
1654.7
1693.2
1732.4
1419.6
—
1440.6
1463.8
1486.8
1509.4
1531.9
1554.3
1576.6
1598.9
1621.3
1643.7
1688.8
1734.4
1780.6
1827.4
1875.0
1923.3
1972.4
5.5979
—
5.6791
5.7659
5.8484
5.9270
6.0025
6.0751
6.1453
6.2133
6.2794
6.3437
6.4679
6.5869
6.7015
6.8123
6.9196
7.0239
7.1255
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.2.2 (continued )
..............
⑦
797
Superheated Ammonia
Temp.
(◦ C)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
300 kPa (−9.24◦ C)
Sat.
0
10
20
30
40
50
60
70
80
100
120
140
160
180
200
220
240
260
0.40607
0.42382
0.44251
0.46077
0.47870
0.49636
0.51382
0.53111
0.54827
0.56532
0.59916
0.63276
0.66618
0.69946
0.73263
0.76572
0.79872
0.83167
0.86455
1309.9
1327.5
1346.1
1364.4
1382.3
1400.1
1417.8
1435.4
1453.0
1470.6
1506.1
1542.0
1578.5
1615.6
1653.4
1692.0
1731.3
1771.4
1812.2
1431.7
1454.7
1478.9
1502.6
1526.0
1549.0
1571.9
1594.7
1617.5
1640.2
1685.8
1731.8
1778.3
1825.4
1873.2
1921.7
1970.9
2020.9
2071.6
0.25035
0.25757
0.26949
0.28103
0.29227
0.30328
0.31410
0.32478
0.33535
0.35621
0.37681
0.39722
0.41748
0.43764
0.45771
0.47770
0.49763
0.51749
1321.3
1333.5
1353.6
1373.0
1392.0
1410.6
1429.0
1447.3
1465.4
1501.7
1538.2
1575.2
1612.7
1650.8
1689.6
1729.2
1769.5
1810.6
1446.5
1462.3
1488.3
1513.5
1538.1
1562.2
1586.1
1609.6
1633.1
1679.8
1726.6
1773.8
1821.4
1869.6
1918.5
1968.1
2018.3
2069.3
h
(kJ/kg)
s
(kJ/kg-K)
400 kPa (−1.89◦ C)
5.4565
5.5420
5.6290
5.7113
5.7896
5.8645
5.9365
6.0060
6.0732
6.1385
6.2642
6.3842
6.4996
6.6109
6.7188
6.8235
6.9254
7.0247
7.1217
0.30942
0.31227
0.32701
0.34129
0.35520
0.36884
0.38226
0.39550
0.40860
0.42160
0.44732
0.47279
0.49808
0.52323
0.54827
0.57321
0.59809
0.62289
0.64764
500 kPa (4.13◦ C)
Sat.
10
20
30
40
50
60
70
80
100
120
140
160
180
200
220
240
260
u
(kJ/kg)
1316.4
1320.2
1339.9
1359.1
1377.7
1396.1
1414.2
1432.2
1450.1
1468.0
1503.9
1540.1
1576.8
1614.1
1652.1
1690.8
1730.3
1770.5
1811.4
1440.2
1445.1
1470.7
1495.6
1519.8
1543.6
1567.1
1590.4
1613.6
1636.7
1682.8
1729.2
1776.0
1823.4
1871.4
1920.1
1969.5
2019.6
2070.5
5.3559
5.3741
5.4663
5.5525
5.6338
5.7111
5.7850
5.8560
5.9244
5.9907
6.1179
6.2390
6.3552
6.4671
6.5755
6.6806
6.7828
6.8825
6.9797
600 kPa (9.28◦ C)
5.2776
5.3340
5.4244
5.5090
5.5889
5.6647
5.7373
5.8070
5.8744
6.0031
6.1253
6.2422
6.3548
6.4636
6.5691
6.6717
6.7717
6.8692
0.21038
0.21115
0.22154
0.23152
0.24118
0.25059
0.25981
0.26888
0.27783
0.29545
0.31281
0.32997
0.34699
0.36389
0.38071
0.39745
0.41412
0.43073
1325.2
1326.7
1347.9
1368.2
1387.8
1406.9
1425.7
1444.3
1462.8
1499.5
1536.3
1573.5
1611.2
1649.5
1688.5
1728.2
1768.6
1809.8
1451.4
1453.4
1480.8
1507.1
1532.5
1557.3
1581.6
1605.7
1629.5
1676.8
1724.0
1771.5
1819.4
1867.8
1916.9
1966.6
2017.0
2068.2
5.2133
5.2205
5.3156
5.4037
5.4862
5.5641
5.6383
5.7094
5.7778
5.9081
6.0314
6.1491
6.2623
6.3717
6.4776
6.5806
6.6808
6.7786
⑦
APPENDIX B
..............798
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.2.2 (continued )
Superheated Ammonia
Temp.
(◦ C)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
800 kPa (17.85◦ C)
Sat.
20
30
40
50
60
70
80
100
120
140
160
180
200
220
240
260
280
300
0.15958
0.16138
0.16947
0.17720
0.18465
0.19189
0.19896
0.20590
0.21949
0.23280
0.24590
0.25886
0.27170
0.28445
0.29712
0.30973
0.32228
0.33477
0.34722
1330.9
1335.8
1358.0
1379.0
1399.3
1419.0
1438.3
1457.4
1495.0
1532.5
1570.1
1608.2
1646.8
1686.1
1726.0
1766.7
1808.1
1850.2
1893.1
1458.6
1464.9
1493.5
1520.8
1547.0
1572.5
1597.5
1622.1
1670.6
1718.7
1766.9
1815.3
1864.2
1913.6
1963.7
2014.5
2065.9
2118.0
2170.9
0.10751
0.11287
0.11846
0.12378
0.12890
0.13387
0.14347
0.15275
0.16181
0.17071
0.17950
0.18819
0.19680
0.20534
0.21382
0.22225
0.23063
0.23897
1337.8
1360.0
1383.0
1404.8
1425.8
1446.2
1485.8
1524.7
1563.3
1602.2
1641.5
1681.3
1721.8
1762.9
1804.7
1847.3
1890.6
1934.6
1466.8
1495.4
1525.1
1553.3
1580.5
1606.8
1658.0
1708.0
1757.5
1807.1
1856.9
1907.1
1957.9
2009.3
2061.3
2114.0
2167.3
2221.3
h
(kJ/kg)
s
(kJ/kg-K)
1000 kPa (24.90◦ C)
5.1110
5.1328
5.2287
5.3171
5.3996
5.4774
5.5513
5.6219
5.7555
5.8811
6.0006
6.1150
6.2254
6.3322
6.4358
6.5367
6.6350
6.7310
6.8248
0.12852
—
0.13206
0.13868
0.14499
0.15106
0.15695
0.16270
0.17389
0.18477
0.19545
0.20597
0.21638
0.22669
0.23693
0.24710
0.25720
0.26726
0.27726
1200 kPa (30.94◦ C)
Sat.
40
50
60
70
80
100
120
140
160
180
200
220
240
260
280
300
320
u
(kJ/kg)
1334.9
—
1347.1
1369.8
1391.3
1412.1
1432.2
1451.9
1490.5
1528.6
1566.8
1605.2
1644.2
1683.7
1723.9
1764.8
1806.4
1848.8
1891.8
1463.4
—
1479.1
1508.5
1536.3
1563.1
1589.1
1614.6
1664.3
1713.4
1762.2
1811.2
1860.5
1910.4
1960.8
2011.9
2063.6
2116.0
2169.1
5.0304
—
5.0826
5.1778
5.2654
5.3471
5.4240
5.4971
5.6342
5.7622
5.8834
5.9992
6.1105
6.2182
6.3226
6.4241
6.5229
6.6194
6.7137
1400 kPa (36.26◦ C)
4.9635
5.0564
5.1497
5.2357
5.3159
5.3916
5.5325
5.6631
5.7860
5.9031
6.0156
6.1241
6.2292
6.3313
6.4308
6.5278
6.6225
6.7151
0.09231
0.09432
0.09942
0.10423
0.10882
0.11324
0.12172
0.12986
0.13777
0.14552
0.15315
0.16068
0.16813
0.17551
0.18283
0.19010
0.19732
0.20450
1339.8
1349.5
1374.2
1397.2
1419.2
1440.3
1481.0
1520.7
1559.9
1599.2
1638.8
1678.9
1719.6
1761.0
1803.0
1845.8
1889.3
1933.5
1469.0
1481.6
1513.4
1543.1
1571.5
1598.8
1651.4
1702.5
1752.8
1802.9
1853.2
1903.8
1955.0
2006.7
2059.0
2111.9
2165.5
2219.8
4.9060
4.9463
5.0462
5.1370
5.2209
5.2994
5.4443
5.5775
5.7023
5.8208
5.9343
6.0437
6.1495
6.2523
6.3523
6.4498
6.5450
6.6380
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.2.2 (continued )
..............
⑦
799
Superheated Ammonia
Temp.
(◦ C)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
1600 kPa (41.03◦ C)
Sat.
50
60
70
80
100
120
140
160
180
200
220
240
260
280
300
320
340
360
0.08079
0.08506
0.08951
0.09372
0.09774
0.10539
0.11268
0.11974
0.12662
0.13339
0.14005
0.14663
0.15314
0.15959
0.16599
0.17234
0.17865
0.18492
0.19115
1341.2
1364.9
1389.3
1412.3
1434.3
1476.2
1516.6
1556.4
1596.1
1636.1
1676.5
1717.4
1759.0
1801.3
1844.3
1888.0
1932.4
1977.5
2023.3
1470.5
1501.0
1532.5
1562.3
1590.6
1644.8
1696.9
1748.0
1798.7
1849.5
1900.5
1952.0
2004.1
2056.7
2109.9
2163.7
2218.2
2273.4
2329.1
0.02365
0.02636
0.03024
0.03350
0.03643
0.03916
0.04174
0.04422
0.04662
0.04895
0.05123
0.05346
0.05565
0.05779
0.05990
0.06198
0.06403
0.06606
0.06806
1323.2
1369.7
1435.1
1489.8
1539.5
1586.9
1633.1
1678.9
1724.8
1770.9
1817.4
1864.5
1912.1
1960.3
2009.1
2058.5
2108.4
2159.0
2210.1
1441.4
1501.5
1586.3
1657.3
1721.7
1782.7
1841.8
1900.0
1957.9
2015.6
2073.6
2131.8
2190.3
2249.2
2308.6
2368.4
2428.6
2489.3
2550.4
h
(kJ/kg)
s
(kJ/kg-K)
2000 kPa (49.37◦ C)
4.8553
4.9510
5.0472
5.1351
5.2167
5.3659
5.5018
5.6286
5.7485
5.8631
5.9734
6.0800
6.1834
6.2839
6.3819
6.4775
6.5710
6.6624
6.7519
0.06444
0.06471
0.06875
0.07246
0.07595
0.08248
0.08861
0.09447
0.10016
0.10571
0.11116
0.11652
0.12182
0.12705
0.13224
0.13737
0.14246
0.14751
0.15253
5000 kPa (88.90◦ C)
Sat.
100
120
140
160
180
200
220
240
260
280
300
320
340
360
380
400
420
440
u
(kJ/kg)
1342.6
1344.5
1372.3
1397.8
1421.6
1466.1
1508.3
1549.3
1589.9
1630.6
1671.6
1713.1
1755.2
1797.9
1841.3
1885.4
1930.2
1975.6
2021.8
1471.5
1473.9
1509.8
1542.7
1573.5
1631.1
1685.5
1738.2
1790.2
1842.0
1893.9
1946.1
1998.8
2052.0
2105.8
2160.1
2215.1
2270.7
2326.8
4.7680
4.7754
4.8848
4.9821
5.0707
5.2294
5.3714
5.5022
5.6251
5.7420
5.8540
5.9621
6.0668
6.1685
6.2675
6.3641
6.4583
6.5505
6.6406
10000 kPa (125.20◦ C)
4.3454
4.5091
4.7306
4.9068
5.0591
5.1968
5.3245
5.4450
5.5600
5.6704
5.7771
5.8805
5.9809
6.0786
6.1738
6.2668
6.3576
6.4464
6.5334
0.00826
—
—
0.01195
0.01461
0.01666
0.01842
0.02001
0.02150
0.02290
0.02424
0.02552
0.02676
0.02796
0.02913
0.03026
0.03137
0.03245
0.03351
1206.8
—
—
1341.8
1432.2
1500.6
1560.3
1615.8
1669.2
1721.6
1773.6
1825.5
1877.6
1930.0
1982.8
2036.1
2089.8
2143.9
2198.5
1289.4
—
—
1461.3
1578.3
1667.2
1744.5
1816.0
1884.2
1950.6
2015.9
2080.7
2145.2
2209.6
2274.1
2338.7
2403.5
2468.5
2533.7
3.7587
—
—
4.1839
4.4610
4.6617
4.8287
4.9767
5.1123
5.2392
5.3596
5.4746
5.5852
5.6921
5.7955
5.8960
5.9937
6.0888
6.1815
⑦
APPENDIX B
..............800
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.3
Thermodynamic Properties of Carbon Dioxide
TABLE B.3.1
Saturated Carbon Dioxide
Specific Volume, m3 /kg
Internal Energy, kJ/kg
Temp.
(◦ C)
Press.
(kPa)
Sat. Liquid
vf
Evap.
v fg
Sat. Vapor
vg
Sat. Liquid
uf
Evap.
ufg
Sat. Vapor
ug
−50.0
−48
−46
−44
−42
−40
−38
−36
−34
−32
−30
−28
−26
−24
−22
−20
−18
−16
−14
−12
−10
−8
−6
−4
−2
0
2
4
6
8
10
12
14
16
18
20
22
24
26
28
30
31.0
682.3
739.5
800.2
864.4
932.5
1004.5
1080.5
1160.7
1245.2
1334.2
1427.8
1526.1
1629.3
1737.5
1850.9
1969.6
2093.8
2223.7
2359.3
2501.0
2648.7
2802.7
2963.2
3130.3
3304.2
3485.1
3673.3
3868.8
4072.0
4283.1
4502.2
4729.7
4965.8
5210.8
5465.1
5729.1
6003.1
6287.7
6583.7
6891.8
7213.7
7377.3
0.000866
0.000872
0.000878
0.000883
0.000889
0.000896
0.000902
0.000909
0.000915
0.000922
0.000930
0.000937
0.000945
0.000953
0.000961
0.000969
0.000978
0.000987
0.000997
0.001007
0.001017
0.001028
0.001040
0.001052
0.001065
0.001078
0.001093
0.001108
0.001124
0.001142
0.001161
0.001182
0.001205
0.001231
0.001260
0.001293
0.001332
0.001379
0.001440
0.001526
0.001685
0.002139
0.05492
0.05075
0.04694
0.04347
0.04029
0.03739
0.03472
0.03227
0.03002
0.02794
0.02603
0.02425
0.02261
0.02110
0.01968
0.01837
0.01715
0.01601
0.01495
0.01396
0.01303
0.01216
0.01134
0.01057
0.00985
0.00916
0.00852
0.00790
0.00732
0.00677
0.00624
0.00573
0.00524
0.00477
0.00431
0.00386
0.00341
0.00295
0.00247
0.00193
0.00121
0.0
0.05579
0.05162
0.04782
0.04435
0.04118
0.03828
0.03562
0.03318
0.03093
0.02886
0.02696
0.02519
0.02356
0.02205
0.02065
0.01934
0.01813
0.01700
0.01595
0.01497
0.01405
0.01319
0.01238
0.01162
0.01091
0.01024
0.00961
0.00901
0.00845
0.00791
0.00740
0.00691
0.00645
0.00600
0.00557
0.00515
0.00474
0.00433
0.00391
0.00346
0.00290
0.00214
−20.55
−16.64
−12.72
−8.80
−4.85
−0.90
3.07
7.05
11.05
15.07
19.11
23.17
27.25
31.35
35.48
39.64
43.82
48.04
52.30
56.59
60.92
65.30
69.73
74.20
78.74
83.34
88.01
92.76
97.60
102.54
107.60
112.79
118.14
123.69
129.48
135.56
142.03
149.04
156.88
166.20
179.49
203.56
302.26
298.86
295.42
291.94
288.42
284.86
281.26
277.60
273.90
270.14
266.32
262.45
258.51
254.50
250.41
246.25
242.01
237.68
233.26
228.73
224.10
219.35
214.47
209.46
204.29
198.96
193.44
187.73
181.78
175.57
169.07
162.23
154.99
147.26
138.95
129.90
119.89
108.55
95.20
78.26
51.83
0.0
281.71
282.21
282.69
283.15
283.57
283.96
284.33
284.66
284.95
285.21
285.43
285.61
285.75
285.85
285.89
285.89
285.84
285.73
285.56
285.32
285.02
284.65
284.20
283.66
283.03
282.30
281.46
280.49
279.38
278.11
276.67
275.02
273.13
270.95
268.43
265.46
261.92
257.59
252.07
244.46
231.32
203.56
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.3.1 (continued )
..............
⑦
801
Saturated Carbon Dioxide
Enthalpy, kJ/kg
Temp.
(◦ C)
Press.
(kPa)
−50.0
−48
−46
−44
−42
−40
−38
−36
−34
−32
−30
−28
−26
−24
−22
−20
−18
−16
−14
−12
−10
−8
−6
−4
−2
0
2
4
6
8
10
12
14
16
18
20
22
24
26
28
30
31.0
682.3
739.5
800.2
864.4
932.5
1004.5
1080.5
1160.7
1245.2
1334.2
1427.8
1526.1
1629.3
1737.5
1850.9
1969.6
2093.8
2223.7
2359.3
2501.0
2648.7
2802.7
2963.2
3130.3
3304.2
3485.1
3673.3
3868.8
4072.0
4283.1
4502.2
4729.7
4965.8
5210.8
5465.1
5729.1
6003.1
6287.7
6583.7
6891.8
7213.7
7377.3
Sat. Liquid
hf
−19.96
−16.00
−12.02
−8.03
−4.02
0
4.04
8.11
12.19
16.30
20.43
24.60
28.78
33.00
37.26
41.55
45.87
50.24
54.65
59.11
63.62
68.18
72.81
77.50
82.26
87.10
92.02
97.05
102.18
107.43
112.83
118.38
124.13
130.11
136.36
142.97
150.02
157.71
166.36
176.72
191.65
219.34
Entropy, kJ/kg-K
Evap.
hfg
Sat. Vapor
hg
Sat. Liquid
sf
Evap.
s fg
Sat. Vapor
sg
339.73
336.38
332.98
329.52
326.00
322.42
318.78
315.06
311.28
307.42
303.48
299.46
295.35
291.15
286.85
282.44
277.93
273.30
268.54
263.65
258.61
253.43
248.08
242.55
236.83
230.89
224.73
218.30
211.59
204.56
197.15
189.33
181.02
172.12
162.50
152.00
140.34
127.09
111.45
91.58
60.58
0.0
319.77
320.38
320.96
321.49
321.97
322.42
322.82
323.17
323.47
323.72
323.92
324.06
324.14
324.15
324.11
323.99
323.80
323.53
323.19
322.76
322.23
321.61
320.89
320.05
319.09
317.99
316.75
315.35
313.77
311.99
309.98
307.72
305.15
302.22
298.86
294.96
290.36
284.80
277.80
268.30
252.23
219.34
−0.0863
−0.0688
−0.0515
−0.0342
−0.0171
0
0.0170
0.0339
0.0507
0.0675
0.0842
0.1009
0.1175
0.1341
0.1506
0.1672
0.1837
0.2003
0.2169
0.2334
0.2501
0.2668
0.2835
0.3003
0.3173
0.3344
0.3516
0.3690
0.3866
0.4045
0.4228
0.4414
0.4605
0.4802
0.5006
0.5221
0.5449
0.5695
0.5971
0.6301
0.6778
0.7680
1.5224
1.4940
1.4659
1.4380
1.4103
1.3829
1.3556
1.3285
1.3016
1.2748
1.2481
1.2215
1.1950
1.1686
1.1421
1.1157
1.0893
1.0628
1.0362
1.0096
0.9828
0.9558
0.9286
0.9012
0.8734
0.8453
0.8167
0.7877
0.7580
0.7276
0.6963
0.6640
0.6304
0.5952
0.5581
0.5185
0.4755
0.4277
0.3726
0.3041
0.1998
0.0
1.4362
1.4252
1.4144
1.4038
1.3933
1.3829
1.3726
1.3624
1.3523
1.3423
1.3323
1.3224
1.3125
1.3026
1.2928
1.2829
1.2730
1.2631
1.2531
1.2430
1.2328
1.2226
1.2121
1.2015
1.1907
1.1797
1.1683
1.1567
1.1446
1.1321
1.1190
1.1053
1.0909
1.0754
1.0588
1.0406
1.0203
0.9972
0.9697
0.9342
0.8776
0.7680
⑦
APPENDIX B
..............802
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.3.2
Superheated Carbon Dioxide
Temp.
(◦ C)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
—
0.10499
0.11538
0.12552
0.13551
0.14538
0.15518
0.16491
0.17460
0.18425
0.19388
0.20348
0.21307
0.22264
0.23219
0.24173
0.25127
—
292.46
305.30
318.31
331.57
345.14
359.03
373.25
387.80
402.67
417.86
433.35
449.13
465.20
481.55
498.16
515.02
—
334.46
351.46
368.51
385.77
403.29
421.10
439.21
457.64
476.37
495.41
514.74
534.36
554.26
574.42
594.85
615.53
—
1.5947
1.6646
1.7295
1.7904
1.8482
1.9033
1.9561
2.0069
2.0558
2.1030
2.1487
2.1930
2.2359
2.2777
2.3183
2.3578
0.04783
0.04966
0.05546
0.06094
0.06623
0.07140
0.07648
0.08150
0.08647
0.09141
0.09631
0.10119
0.10606
0.11090
0.11573
0.12056
0.12537
1000 kPa (−40.12◦ C)
Sat.
−20
0
20
40
60
80
100
120
140
160
180
200
220
240
260
280
0.03845
0.04342
0.04799
0.05236
0.05660
0.06074
0.06482
0.06885
0.07284
0.07680
0.08074
0.08465
0.08856
0.09244
0.09632
0.10019
0.10405
283.94
298.89
313.15
327.27
341.46
355.82
370.42
385.26
400.38
415.77
431.43
447.36
463.56
480.01
496.72
513.67
530.86
322.39
342.31
361.14
379.63
398.05
416.56
435.23
454.11
473.22
492.57
512.17
532.02
552.11
572.46
593.04
613.86
634.90
h
(kJ/kg)
s
(kJ/kg-K)
800 kPa (−46.00◦ C)
400 kPa (NA)
Sat.
−40
−20
0
20
40
60
80
100
120
140
160
180
200
220
240
260
u
(kJ/kg)
282.69
287.05
301.13
314.92
328.73
342.70
356.90
371.37
386.11
401.15
416.47
432.07
447.95
464.11
480.52
497.20
514.12
320.95
326.78
345.49
363.67
381.72
399.82
418.09
436.57
455.29
474.27
493.52
513.03
532.80
552.83
573.11
593.64
614.41
1.4145
1.4398
1.5168
1.5859
1.6497
1.7094
1.7660
1.8199
1.8714
1.9210
1.9687
2.0148
2.0594
2.1027
2.1447
2.1855
2.2252
1400 kPa (−30.58◦ C)
1.3835
1.4655
1.5371
1.6025
1.6633
1.7206
1.7750
1.8270
1.8768
1.9249
1.9712
2.0160
2.0594
2.1015
2.1424
2.1822
2.2209
0.02750
0.02957
0.03315
0.03648
0.03966
0.04274
0.04575
0.04870
0.05161
0.05450
0.05736
0.06020
0.06302
0.06583
0.06863
0.07141
0.07419
285.37
294.04
309.42
324.23
338.90
353.62
368.48
383.54
398.83
414.36
430.14
446.17
462.45
478.98
495.76
512.77
530.01
323.87
335.44
355.83
375.30
394.42
413.45
432.52
451.72
471.09
490.66
510.44
530.45
550.68
571.14
591.83
612.74
633.88
1.3352
1.3819
1.4595
1.5283
1.5914
1.6503
1.7059
1.7588
1.8093
1.8579
1.9046
1.9498
1.9935
2.0358
2.0770
2.1169
2.1558
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.3.2 (continued )
..............
⑦
803
Superheated Carbon Dioxide
Temp.
(◦ C)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
2000 kPa (−19.50◦ C)
Sat.
0
20
40
60
80
100
120
140
160
180
200
220
240
260
280
300
0.01903
0.02193
0.02453
0.02693
0.02922
0.03143
0.03359
0.03570
0.03777
0.03982
0.04186
0.04387
0.04587
0.04786
0.04983
0.05180
0.05377
285.88
303.24
319.37
334.88
350.19
365.49
380.90
396.46
412.22
428.18
444.37
460.79
477.43
494.31
511.41
528.73
546.26
323.95
347.09
368.42
388.75
408.64
428.36
448.07
467.85
487.76
507.83
528.08
548.53
569.17
590.02
611.08
632.34
653.80
0.00474
—
0.00670
0.00801
0.00908
0.01004
0.01092
0.01176
0.01257
0.01335
0.01411
0.01485
0.01558
0.01630
0.01701
0.01771
0.01840
261.97
—
298.62
322.51
342.74
361.47
379.47
397.10
414.56
431.97
449.40
466.91
484.52
502.27
520.15
538.18
556.37
290.42
—
338.82
370.54
397.21
421.69
445.02
467.68
489.97
512.06
534.04
556.01
578.00
600.05
622.19
644.44
666.80
h
(kJ/kg)
s
(kJ/kg-K)
3000 kPa (−5.55◦ C)
1.2804
1.3684
1.4438
1.5109
1.5725
1.6300
1.6843
1.7359
1.7853
1.8327
1.8784
1.9226
1.9653
2.0068
2.0470
2.0862
2.1243
0.01221
0.01293
0.01512
0.01698
0.01868
0.02029
0.02182
0.02331
0.02477
0.02619
0.02759
0.02898
0.03035
0.03171
0.03306
0.03440
0.03573
6000 kPa (21.98◦ C)
Sat.
20
40
60
80
100
120
140
160
180
200
220
240
260
280
300
320
u
(kJ/kg)
284.09
290.52
310.21
327.61
344.14
360.30
376.35
392.42
408.57
424.87
441.34
457.99
474.83
491.88
509.13
526.59
544.25
320.71
329.32
355.56
378.55
400.19
421.16
441.82
462.35
482.87
503.44
524.12
544.92
565.88
587.01
608.30
629.78
651.43
1.2098
1.2416
1.3344
1.4104
1.4773
1.5385
1.5954
1.6490
1.6999
1.7485
1.7952
1.8401
1.8835
1.9255
1.9662
2.0057
2.0442
10 000 kPa
1.0206
—
1.1806
1.2789
1.3567
1.4241
1.4850
1.5413
1.5939
1.6438
1.6913
1.7367
1.7804
1.8226
1.8634
1.9029
1.9412
—
0.00117
0.00159
0.00345
0.00451
0.00530
0.00598
0.00658
0.00715
0.00768
0.00819
0.00868
0.00916
0.00962
0.01008
0.01053
0.01097
—
118.12
184.23
277.63
312.82
338.20
360.19
380.54
399.99
418.94
437.61
456.12
474.58
493.03
511.53
530.11
548.77
—
129.80
200.14
312.11
357.95
391.24
419.96
446.38
471.46
495.73
519.49
542.91
566.14
589.26
612.32
635.37
658.46
—
0.4594
0.6906
1.0389
1.1728
1.2646
1.3396
1.4051
1.4644
1.5192
1.5705
1.6190
1.6652
1.7094
1.7518
1.7928
1.8324
⑦
APPENDIX B
..............804
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.4
Thermodynamic Properties of R-410a
TABLE B.4.1
Saturated R-410a
Specific Volume, m3 /kg
Internal Energy, kJ/kg
Temp.
(◦ C)
Press.
(kPa)
Sat. Liquid
vf
Evap.
v fg
Sat. Vapor
vg
Sat. Liquid
uf
Evap.
ufg
Sat. Vapor
ug
−60
−55
−51.4
−50
−45
−40
−35
−30
−25
−20
−15
−10
−5
0
5
10
15
20
25
30
35
40
45
50
55
60
65
70
71.3
64.1
84.0
101.3
108.7
138.8
175.0
218.4
269.6
329.7
399.6
480.4
573.1
678.9
798.7
933.9
1085.7
1255.4
1444.2
1653.6
1885.1
2140.2
2420.7
2728.3
3065.2
3433.7
3836.9
4278.3
4763.1
4901.2
0.000727
0.000735
0.000741
0.000743
0.000752
0.000762
0.000771
0.000781
0.000792
0.000803
0.000815
0.000827
0.000841
0.000855
0.000870
0.000886
0.000904
0.000923
0.000944
0.000968
0.000995
0.001025
0.001060
0.001103
0.001156
0.001227
0.001338
0.001619
0.00218
0.36772
0.28484
0.23875
0.22344
0.17729
0.14215
0.11505
0.09392
0.07726
0.06400
0.05334
0.04470
0.03764
0.03182
0.02699
0.02295
0.01955
0.01666
0.01420
0.01208
0.01025
0.00865
0.00723
0.00597
0.00482
0.00374
0.00265
0.00124
0
0.36845
0.28558
0.23949
0.22418
0.17804
0.14291
0.11582
0.09470
0.07805
0.06480
0.05416
0.04553
0.03848
0.03267
0.02786
0.02383
0.02045
0.01758
0.01514
0.01305
0.01124
0.00967
0.00829
0.00707
0.00598
0.00497
0.00399
0.00286
0.00218
−27.50
−20.70
−15.78
−13.88
−7.02
−0.13
6.80
13.78
20.82
27.92
35.08
42.32
49.65
57.07
64.60
72.24
80.02
87.94
96.03
104.32
112.83
121.61
130.72
140.27
150.44
161.57
174.59
194.53
215.78
256.41
251.89
248.59
247.31
242.67
237.95
233.14
228.23
223.21
218.07
212.79
207.36
201.75
195.95
189.93
183.66
177.10
170.21
162.95
155.24
147.00
138.11
128.41
117.63
105.34
90.70
71.59
37.47
0
228.91
231.19
232.81
233.43
235.64
237.81
239.94
242.01
244.03
245.99
247.88
249.69
251.41
253.02
254.53
255.90
257.12
258.16
258.98
259.56
259.83
259.72
259.13
257.90
255.78
252.27
246.19
232.01
215.78
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.4.1 (continued )
..............
⑦
805
Saturated R-410a
Enthalpy, kJ/kg
Temp.
(◦ C)
Press.
(kPa)
−60
−55
−51.4
−50
−45
−40
−35
−30
−25
−20
−15
−10
−5
0
5
10
15
20
25
30
35
40
45
50
55
60
65
70
71.3
64.1
84.0
101.3
108.7
138.8
175.0
218.4
269.6
329.7
399.6
480.4
573.1
678.9
798.7
933.9
1085.7
1255.4
1444.2
1653.6
1885.1
2140.2
2420.7
2728.3
3065.2
3433.7
3836.9
4278.3
4763.1
4901.2
Sat. Liquid
hf
−27.45
−20.64
−15.70
−13.80
−6.92
0
6.97
13.99
21.08
28.24
35.47
42.80
50.22
57.76
65.41
73.21
81.15
89.27
97.59
106.14
114.95
124.09
133.61
143.65
154.41
166.28
180.32
202.24
226.46
Entropy, kJ/kg-K
Evap.
hfg
Sat. Vapor
hg
Sat. Liquid
sf
Evap.
s fg
Sat. Vapor
sg
279.96
275.83
272.78
271.60
267.27
262.83
258.26
253.55
248.69
243.65
238.42
232.98
227.31
221.37
215.13
208.57
201.64
194.28
186.43
178.02
168.94
159.04
148.14
135.93
121.89
105.04
82.95
43.40
0
252.51
255.19
257.08
257.80
260.35
262.83
265.23
267.54
269.77
271.89
273.90
275.78
277.53
279.12
280.55
281.78
282.79
283.55
284.02
284.16
283.89
283.13
281.76
279.58
276.30
271.33
263.26
245.64
226.46
−0.1227
−0.0912
−0.0688
−0.0603
−0.0299
0
0.0294
0.0585
0.0871
0.1154
0.1435
0.1713
0.1989
0.2264
0.2537
0.2810
0.3083
0.3357
0.3631
0.3908
0.4189
0.4473
0.4765
0.5067
0.5384
0.5729
0.6130
0.6752
0.7449
1.3135
1.2644
1.2301
1.2171
1.1715
1.1273
1.0844
1.0428
1.0022
0.9625
0.9236
0.8854
0.8477
0.8104
0.7734
0.7366
0.6998
0.6627
0.6253
0.5872
0.5482
0.5079
0.4656
0.4206
0.3715
0.3153
0.2453
0.1265
0
1.1907
1.1732
1.1613
1.1568
1.1416
1.1273
1.1139
1.1012
1.0893
1.0779
1.0671
1.0567
1.0466
1.0368
1.0272
1.0176
1.0081
0.9984
0.9884
0.9781
0.9671
0.9552
0.9421
0.9273
0.9099
0.8882
0.8583
0.8017
0.7449
⑦
APPENDIX B
..............806
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.4.2
Superheated R-410a
Temp.
(◦ C)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
50 kPa (−64.34◦ C)
Sat.
−60
−40
−20
0
20
40
60
80
100
120
140
160
180
200
220
240
0.46484
0.47585
0.52508
0.57295
0.62016
0.66698
0.71355
0.75995
0.80623
0.85243
0.89857
0.94465
0.99070
1.03671
1.08270
1.12867
1.17462
226.90
229.60
241.94
254.51
267.52
281.05
295.15
309.84
325.11
340.99
357.46
374.50
392.12
410.28
428.98
448.19
467.90
250.15
253.40
268.20
283.16
298.53
314.40
330.83
347.83
365.43
383.61
402.38
421.74
441.65
462.12
483.11
504.63
526.63
0.16540
0.16851
0.18613
0.20289
0.21921
0.23525
0.25112
0.26686
0.28251
0.29810
0.31364
0.32915
0.34462
0.36006
0.37548
0.39089
0.40628
236.36
238.72
252.34
265.90
279.78
294.12
308.97
324.37
340.35
356.89
374.00
391.66
409.87
428.60
447.84
467.58
487.78
261.17
263.99
280.26
296.33
312.66
329.40
346.64
364.40
382.72
401.60
421.04
441.03
461.56
482.61
504.16
526.21
548.73
h
(kJ/kg)
s
(kJ/kg-K)
100 kPa (−51.65◦ C)
1.2070
1.2225
1.2888
1.3504
1.4088
1.4649
1.5191
1.5717
1.6230
1.6731
1.7221
1.7701
1.8171
1.8633
1.9087
1.9532
1.9969
0.24247
—
0.25778
0.28289
0.30723
0.33116
0.35483
0.37833
0.40171
0.42500
0.44822
0.47140
0.49453
0.51764
0.54072
0.56378
0.58682
150 kPa (−43.35◦ C)
Sat.
−40
−20
0
20
40
60
80
100
120
140
160
180
200
220
240
260
u
(kJ/kg)
232.70
—
240.40
253.44
266.72
280.42
294.64
309.40
324.75
340.67
357.17
374.25
391.89
410.07
428.79
448.02
467.74
256.94
—
266.18
281.73
297.44
313.54
330.12
347.24
364.92
383.17
401.99
421.39
441.34
461.84
482.86
504.40
526.42
1.1621
—
1.2027
1.2667
1.3265
1.3833
1.4380
1.4910
1.5425
1.5928
1.6419
1.6901
1.7372
1.7835
1.8289
1.8734
1.9172
200 kPa (−37.01◦ C)
1.1368
1.1489
1.2159
1.2770
1.3347
1.3899
1.4433
1.4950
1.5455
1.5948
1.6430
1.6902
1.7366
1.7820
1.8266
1.8705
1.9135
0.12591
—
0.13771
0.15070
0.16322
0.17545
0.18750
0.19943
0.21127
0.22305
0.23477
0.24645
0.25810
0.26973
0.28134
0.29293
0.30450
239.09
—
251.18
265.06
279.13
293.59
308.53
324.00
340.02
356.60
373.74
391.43
409.66
428.41
447.67
467.41
487.63
264.27
—
278.72
295.20
311.78
328.68
346.03
363.89
382.28
401.21
420.70
440.72
461.28
482.35
503.93
526.00
548.53
1.1192
—
1.1783
1.2410
1.2995
1.3553
1.4090
1.4610
1.5117
1.5611
1.6094
1.6568
1.7032
1.7487
1.7933
1.8372
1.8803
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.4.2 (continued )
..............
⑦
807
Superheated R-410a
Temp.
(◦ C)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
300 kPa (−27.37◦ C)
Sat.
−20
0
20
40
60
80
100
120
140
160
180
200
220
240
260
280
0.08548
0.08916
0.09845
0.10720
0.11564
0.12388
0.13200
0.14003
0.14798
0.15589
0.16376
0.17159
0.17940
0.18719
0.19496
0.20272
0.21046
243.08
248.71
263.33
277.81
292.53
307.65
323.25
339.37
356.03
373.23
390.97
409.24
428.03
447.31
467.09
487.33
508.02
268.72
275.46
292.87
309.96
327.22
344.81
362.85
381.38
400.43
420.00
440.10
460.72
481.85
503.47
525.58
548.15
571.16
0.05208
0.05651
0.06231
0.06775
0.07297
0.07804
0.08302
0.08793
0.09279
0.09760
0.10238
0.10714
0.11187
0.11659
0.12129
0.12598
0.13066
248.29
259.59
275.02
290.32
305.84
321.72
338.05
354.87
372.20
390.05
408.40
427.26
446.61
466.44
486.73
507.46
528.62
274.33
287.84
306.18
324.20
342.32
360.74
379.56
398.84
418.60
438.85
459.59
480.83
502.55
524.73
547.37
570.45
593.95
h
(kJ/kg)
s
(kJ/kg-K)
400 kPa (−19.98◦ C)
1.0949
1.1219
1.1881
1.2485
1.3054
1.3599
1.4125
1.4635
1.5132
1.5617
1.6093
1.6558
1.7014
1.7462
1.7901
1.8332
1.8756
0.06475
—
0.07227
0.07916
0.08571
0.09207
0.09828
0.10440
0.11045
0.11645
0.12241
0.12834
0.13424
0.14012
0.14598
0.15182
0.15766
500 kPa (−13.89◦ C)
Sat.
0
20
40
60
80
100
120
140
160
180
200
220
240
260
280
300
u
(kJ/kg)
246.00
—
261.51
276.44
291.44
306.75
322.49
338.72
355.45
372.72
390.51
408.82
427.64
446.96
466.76
487.03
507.74
271.90
—
290.42
308.10
325.72
343.58
361.80
380.48
399.64
419.30
439.47
460.16
481.34
503.01
525.15
547.76
570.81
1.0779
—
1.1483
1.2108
1.2689
1.3242
1.3773
1.4288
1.4788
1.5276
1.5752
1.6219
1.6676
1.7125
1.7565
1.7997
1.8422
600 kPa (−8.67◦ C)
1.0647
1.1155
1.1803
1.2398
1.2959
1.3496
1.4014
1.4517
1.5007
1.5486
1.5954
1.6413
1.6862
1.7303
1.7736
1.8161
1.8578
0.04351
0.04595
0.05106
0.05576
0.06023
0.06455
0.06877
0.07292
0.07701
0.08106
0.08508
0.08907
0.09304
0.09700
0.10093
0.10486
0.10877
250.15
257.54
273.56
289.19
304.91
320.94
337.38
354.29
371.68
389.58
407.98
426.88
446.26
466.11
486.42
507.18
528.36
276.26
285.12
304.20
322.64
341.05
359.67
378.65
398.04
417.89
438.22
459.03
480.32
502.08
524.31
546.98
570.09
593.62
1.0540
1.0869
1.1543
1.2152
1.2722
1.3265
1.3787
1.4294
1.4786
1.5266
1.5736
1.6196
1.6646
1.7088
1.7521
1.7947
1.8365
⑦
APPENDIX B
..............808
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.4.2 (continued )
Superheated R-410a
Temp.
(◦ C)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
800 kPa (0.05◦ C)
Sat.
20
40
60
80
100
120
140
160
180
200
220
240
260
280
300
0.03262
0.03693
0.04074
0.04429
0.04767
0.05095
0.05415
0.05729
0.06039
0.06345
0.06649
0.06951
0.07251
0.07549
0.07846
0.08142
253.04
270.47
286.83
303.01
319.36
336.03
353.11
370.64
388.65
407.13
426.10
445.55
465.46
485.82
506.61
527.83
279.14
300.02
319.42
338.44
357.49
376.79
396.42
416.47
436.96
457.90
479.30
501.15
523.46
546.21
569.38
592.97
0.02145
0.02260
0.02563
0.02830
0.03077
0.03311
0.03537
0.03756
0.03971
0.04183
0.04391
0.04597
0.04802
0.05005
0.05207
0.05407
0.05607
256.75
263.39
281.72
299.00
316.06
333.24
350.69
368.51
386.75
405.43
424.55
444.12
464.14
484.60
505.48
526.77
548.47
282.50
290.51
312.48
332.96
352.98
372.97
393.13
413.59
434.40
455.62
477.24
499.29
521.77
544.66
567.96
591.66
615.75
h
(kJ/kg)
s
(kJ/kg-K)
1000 kPa (7.25◦ C)
1.0367
1.1105
1.1746
1.2334
1.2890
1.3421
1.3934
1.4431
1.4915
1.5388
1.5850
1.6302
1.6746
1.7181
1.7607
1.8026
0.02596
0.02838
0.03170
0.03470
0.03753
0.04025
0.04288
0.04545
0.04798
0.05048
0.05294
0.05539
0.05781
0.06023
0.06262
0.06501
1200 kPa (13.43◦ C)
Sat.
20
40
60
80
100
120
140
160
180
200
220
240
260
280
300
320
u
(kJ/kg)
255.16
267.11
284.35
301.04
317.73
334.65
351.91
369.58
387.70
406.28
425.33
444.84
464.80
485.21
506.05
527.30
281.12
295.49
316.05
335.75
355.27
374.89
394.79
415.04
435.68
456.76
478.27
500.23
522.62
545.43
568.67
592.31
1.0229
1.0730
1.1409
1.2019
1.2588
1.3128
1.3648
1.4150
1.4638
1.5113
1.5578
1.6032
1.6477
1.6914
1.7341
1.7761
1400 kPa (18.88◦ C)
1.0111
1.0388
1.1113
1.1747
1.2331
1.2881
1.3408
1.3915
1.4407
1.4886
1.5353
1.5809
1.6256
1.6693
1.7122
1.7543
1.7956
0.01819
0.01838
0.02127
0.02371
0.02593
0.02801
0.03000
0.03192
0.03380
0.03565
0.03746
0.03925
0.04102
0.04278
0.04452
0.04626
0.04798
257.94
259.18
278.93
296.88
314.35
331.80
349.46
367.43
385.79
404.56
423.77
443.41
463.49
483.99
504.91
526.25
547.97
283.40
284.90
308.71
330.07
350.64
371.01
391.46
412.13
433.12
454.47
476.21
498.36
520.92
543.88
567.25
591.01
615.14
1.0006
1.0057
1.0843
1.1505
1.2105
1.2666
1.3199
1.3712
1.4208
1.4690
1.5160
1.5618
1.6066
1.6505
1.6936
1.7358
1.7772
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.4.2 (continued )
..............
⑦
809
Superheated R-410a
Temp.
(◦ C)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
1800 kPa (28.22◦ C)
Sat.
40
60
80
100
120
140
160
180
200
220
240
260
280
300
320
340
0.01376
0.01534
0.01754
0.01945
0.02119
0.02283
0.02441
0.02593
0.02741
0.02886
0.03029
0.03170
0.03309
0.03447
0.03584
0.03720
0.03855
259.38
272.67
292.34
310.76
328.84
346.93
365.24
383.85
402.82
422.19
441.97
462.16
482.77
503.78
525.19
546.98
569.15
284.15
300.29
323.92
345.77
366.98
388.03
409.17
430.51
452.16
474.14
496.49
519.22
542.34
565.83
589.70
613.94
638.54
0.00729
0.00858
0.01025
0.01159
0.01277
0.01387
0.01489
0.01588
0.01683
0.01775
0.01865
0.01954
0.02041
0.02127
0.02212
0.02296
0.02379
258.19
274.96
298.38
319.07
338.84
358.32
377.80
397.46
417.37
437.60
458.16
479.08
500.37
522.01
544.02
566.37
589.07
280.06
300.70
329.12
353.84
377.16
399.92
422.49
445.09
467.85
490.84
514.11
537.69
561.59
585.81
610.37
635.25
660.45
h
(kJ/kg)
s
(kJ/kg-K)
2000 kPa (32.31◦ C)
0.9818
1.0344
1.1076
1.1713
1.2297
1.2847
1.3371
1.3875
1.4364
1.4839
1.5301
1.5753
1.6195
1.6627
1.7051
1.7467
1.7875
0.01218
0.01321
0.01536
0.01717
0.01880
0.02032
0.02177
0.02317
0.02452
0.02585
0.02715
0.02844
0.02970
0.03095
0.03220
0.03343
0.03465
3000 kPa (49.07◦ C)
Sat.
60
80
100
120
140
160
180
200
220
240
260
280
300
320
340
360
u
(kJ/kg)
259.72
269.07
289.90
308.88
327.30
345.64
364.12
382.86
401.94
421.40
441.25
461.50
482.16
503.21
524.66
546.49
568.69
284.09
295.49
320.62
343.22
364.91
386.29
407.66
429.20
450.99
473.10
495.55
518.37
541.56
565.12
589.05
613.35
637.99
0.9731
1.0099
1.0878
1.1537
1.2134
1.2693
1.3223
1.3732
1.4224
1.4701
1.5166
1.5619
1.6063
1.6497
1.6922
1.7338
1.7747
4000 kPa (61.90◦ C)
0.9303
0.9933
1.0762
1.1443
1.2052
1.2617
1.3150
1.3661
1.4152
1.4628
1.5091
1.5541
1.5981
1.6411
1.6833
1.7245
1.7650
0.00460
—
0.00661
0.00792
0.00897
0.00990
0.01076
0.01156
0.01232
0.01305
0.01377
0.01446
0.01514
0.01581
0.01647
0.01712
0.01776
250.37
—
285.02
309.62
331.39
352.14
372.51
392.82
413.25
433.88
454.79
475.99
497.51
519.37
541.55
564.06
586.90
268.76
—
311.48
341.29
367.29
391.75
415.53
439.05
462.52
486.10
509.85
533.83
558.08
582.60
607.42
632.54
657.95
0.8782
—
1.0028
1.0850
1.1529
1.2136
1.2698
1.3229
1.3736
1.4224
1.4696
1.5155
1.5601
1.6037
1.6462
1.6879
1.7286
⑦
APPENDIX B
..............810
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.5
Thermodynamic Properties of R-134a
TABLE B.5.1
Saturated R-134a
Specific Volume, m3 /kg
Internal Energy, kJ/kg
Temp.
(◦ C)
Press.
(kPa)
Sat. Liquid
vf
Evap.
v fg
Sat. Vapor
vg
Sat. Liquid
uf
Evap.
u fg
Sat. Vapor
ug
−70
−65
−60
−55
−50
−45
−40
−35
−30
−26.3
−25
−20
−15
−10
−5
0
5
10
15
20
25
30
35
40
45
50
55
60
65
70
75
80
85
90
95
100
101.2
8.3
11.7
16.3
22.2
29.9
39.6
51.8
66.8
85.1
101.3
107.2
133.7
165.0
201.7
244.5
294.0
350.9
415.8
489.5
572.8
666.3
771.0
887.6
1017.0
1160.2
1318.1
1491.6
1681.8
1889.9
2117.0
2364.4
2633.6
2926.2
3244.5
3591.5
3973.2
4064.0
0.000675
0.000679
0.000684
0.000689
0.000695
0.000701
0.000708
0.000715
0.000722
0.000728
0.000730
0.000738
0.000746
0.000755
0.000764
0.000773
0.000783
0.000794
0.000805
0.000817
0.000829
0.000843
0.000857
0.000873
0.000890
0.000908
0.000928
0.000951
0.000976
0.001005
0.001038
0.001078
0.001128
0.001195
0.001297
0.001557
0.001969
1.97207
1.42915
1.05199
0.78609
0.59587
0.45783
0.35625
0.28051
0.22330
0.18947
0.17957
0.14576
0.11932
0.09845
0.08181
0.06842
0.05755
0.04866
0.04133
0.03524
0.03015
0.02587
0.02224
0.01915
0.01650
0.01422
0.01224
0.01051
0.00899
0.00765
0.00645
0.00537
0.00437
0.00341
0.00243
0.00108
0
1.97274
1.42983
1.05268
0.78678
0.59657
0.45853
0.35696
0.28122
0.22402
0.19020
0.18030
0.14649
0.12007
0.09921
0.08257
0.06919
0.05833
0.04945
0.04213
0.03606
0.03098
0.02671
0.02310
0.02002
0.01739
0.01512
0.01316
0.01146
0.00997
0.00866
0.00749
0.00645
0.00550
0.00461
0.00373
0.00264
0.00197
119.46
123.18
127.52
132.36
137.60
143.15
148.95
154.93
161.06
165.73
167.30
173.65
180.07
186.57
193.14
199.77
206.48
213.25
220.10
227.03
234.04
241.14
248.34
255.65
263.08
270.63
278.33
286.19
294.24
302.51
311.06
319.96
329.35
339.51
351.17
368.55
382.97
218.74
217.76
216.19
214.14
211.71
208.99
206.05
202.93
199.67
197.16
196.31
192.85
189.32
185.70
182.01
178.24
174.38
170.42
166.35
162.16
157.83
153.34
148.68
143.81
138.71
133.35
127.68
121.66
115.22
108.27
100.68
92.26
82.67
71.24
56.25
28.19
0
338.20
340.94
343.71
346.50
349.31
352.15
355.00
357.86
360.73
362.89
363.61
366.50
369.39
372.27
375.15
378.01
380.85
383.67
386.45
389.19
391.87
394.48
397.02
399.46
401.79
403.98
406.01
407.85
409.46
410.78
411.74
412.22
412.01
410.75
407.42
396.74
382.97
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.5.1 (continued )
..............
⑦
811
Saturated R-134a
Enthalpy, kJ/kg
Entropy, kJ/k-K
Temp.
(◦ C)
Press.
(kPa)
Sat. Liquid
hf
Evap.
hfg
Sat. Vapor
hg
Sat. Liquid
sf
Evap.
s fg
Sat. Vapor
sg
−70
−65
−60
−55
−50
−45
−40
−35
−30
−26.3
−25
−20
−15
−10
−5
0
5
10
15
20
25
30
35
40
45
50
55
60
65
70
75
80
85
90
95
100
101.2
8.3
11.7
16.3
22.2
29.9
39.6
51.8
66.8
85.1
101.3
107.2
133.7
165.0
201.7
244.5
294.0
350.9
415.8
489.5
572.8
666.3
771.0
887.6
1017.0
1160.2
1318.1
1491.6
1681.8
1889.9
2117.0
2364.4
2633.6
2926.2
3244.5
3591.5
3973.2
4064.0
119.47
123.18
127.53
132.37
137.62
143.18
148.98
154.98
161.12
165.80
167.38
173.74
180.19
186.72
193.32
200.00
206.75
213.58
220.49
227.49
234.59
241.79
249.10
256.54
264.11
271.83
279.72
287.79
296.09
304.64
313.51
322.79
332.65
343.38
355.83
374.74
390.98
235.15
234.55
233.33
231.63
229.54
227.14
224.50
221.67
218.68
216.36
215.57
212.34
209.00
205.56
202.02
198.36
194.57
190.65
186.58
182.35
177.92
173.29
168.42
163.28
157.85
152.08
145.93
139.33
132.21
124.47
115.94
106.40
95.45
82.31
64.98
32.47
0
354.62
357.73
360.86
364.00
367.16
370.32
373.48
376.64
379.80
382.16
382.95
386.08
389.20
392.28
395.34
398.36
401.32
404.23
407.07
409.84
412.51
415.08
417.52
419.82
421.96
423.91
425.65
427.13
428.30
429.11
429.45
429.19
428.10
425.70
420.81
407.21
390.98
0.6645
0.6825
0.7031
0.7256
0.7493
0.7740
0.7991
0.8245
0.8499
0.8690
0.8754
0.9007
0.9258
0.9507
0.9755
1.0000
1.0243
1.0485
1.0725
1.0963
1.1201
1.1437
1.1673
1.1909
1.2145
1.2381
1.2619
1.2857
1.3099
1.3343
1.3592
1.3849
1.4117
1.4404
1.4733
1.5228
1.5658
1.1575
1.1268
1.0947
1.0618
1.0286
0.9956
0.9629
0.9308
0.8994
0.8763
0.8687
0.8388
0.8096
0.7812
0.7534
0.7262
0.6995
0.6733
0.6475
0.6220
0.5967
0.5716
0.5465
0.5214
0.4962
0.4706
0.4447
0.4182
0.3910
0.3627
0.3330
0.3013
0.2665
0.2267
0.1765
0.0870
0
1.8220
1.8094
1.7978
1.7874
1.7780
1.7695
1.7620
1.7553
1.7493
1.7453
1.7441
1.7395
1.7354
1.7319
1.7288
1.7262
1.7239
1.7218
1.7200
1.7183
1.7168
1.7153
1.7139
1.7123
1.7106
1.7088
1.7066
1.7040
1.7008
1.6970
1.6923
1.6862
1.6782
1.6671
1.6498
1.6098
1.5658
⑦
APPENDIX B
..............812
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.5.2
Superheated R-134a
Temp.
(◦ C)
v
(m3 /kg )
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
50 kPa (−40.67◦ C)
Sat.
−20
−10
0
10
20
30
40
50
60
70
80
90
100
110
120
130
0.36889
0.40507
0.42222
0.43921
0.45608
0.47287
0.48958
0.50623
0.52284
0.53941
0.55595
0.57247
0.58896
0.60544
0.62190
0.63835
0.65479
354.61
368.57
375.53
382.63
389.90
397.32
404.90
412.64
420.55
428.63
436.86
445.26
453.82
462.53
471.41
480.44
489.63
373.06
388.82
396.64
404.59
412.70
420.96
429.38
437.96
446.70
455.60
464.66
473.88
483.26
492.81
502.50
512.36
522.37
0.13139
0.13602
0.14222
0.14828
0.15424
0.16011
0.16592
0.17168
0.17740
0.18308
0.18874
0.19437
0.19999
0.20559
0.21117
0.21675
0.22231
368.06
373.44
380.85
388.36
395.98
403.71
411.59
419.60
427.76
436.06
444.52
453.13
461.89
470.80
479.87
489.08
498.45
387.77
393.84
402.19
410.60
419.11
427.73
436.47
445.35
454.37
463.53
472.83
482.28
491.89
501.64
511.54
521.60
531.80
h
(kJ/kg)
s
(kJ/kg-K)
100 kPa (−26.54◦ C)
1.7629
1.8279
1.8582
1.8878
1.9170
1.9456
1.9739
2.0017
2.0292
2.0563
2.0831
2.1096
2.1358
2.1617
2.1874
2.2128
2.2379
0.19257
0.19860
0.20765
0.21652
0.22527
0.23392
0.24250
0.25101
0.25948
0.26791
0.27631
0.28468
0.29302
0.30135
0.30967
0.31797
0.32626
150 kPa (−17.29◦ C)
Sat.
−10
0
10
20
30
40
50
60
70
80
90
100
110
120
130
140
u
(kJ/kg)
362.73
367.36
374.51
381.76
389.14
396.66
404.31
412.12
420.08
428.20
436.47
444.89
453.47
462.21
471.11
480.16
489.36
381.98
387.22
395.27
403.41
411.67
420.05
428.56
437.22
446.03
454.99
464.10
473.36
482.78
492.35
502.07
511.95
521.98
1.7456
1.7665
1.7978
1.8281
1.8578
1.8869
1.9155
1.9436
1.9712
1.9985
2.0255
2.0521
2.0784
2.1044
2.1301
2.1555
2.1807
200 kPa (−10.22◦ C)
1.7372
1.7606
1.7917
1.8220
1.8515
1.8804
1.9088
1.9367
1.9642
1.9913
2.0180
2.0444
2.0705
2.0963
2.1218
2.1470
2.1720
0.10002
0.10013
0.10501
0.10974
0.11436
0.11889
0.12335
0.12776
0.13213
0.13646
0.14076
0.14504
0.14930
0.15355
0.15777
0.16199
0.16620
372.15
372.31
379.91
387.55
395.27
403.10
411.04
419.11
427.31
435.65
444.14
452.78
461.56
470.50
479.58
488.81
498.19
392.15
392.34
400.91
409.50
418.15
426.87
435.71
444.66
453.74
462.95
472.30
481.79
491.42
501.21
511.13
521.21
531.43
1.7320
1.7328
1.7647
1.7956
1.8256
1.8549
1.8836
1.9117
1.9394
1.9666
1.9935
2.0200
2.0461
2.0720
2.0976
2.1229
2.1479
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.5.2 (continued )
..............
⑦
813
Superheated R-134a
Temp.
(◦ C)
v
(m3 /kg )
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
300 kPa (0.56◦ C)
Sat.
10
20
30
40
50
60
70
80
90
100
110
120
130
140
150
160
0.06787
0.07111
0.07441
0.07762
0.08075
0.08382
0.08684
0.08982
0.09277
0.09570
0.09861
0.10150
0.10437
0.10723
0.11008
0.11292
0.11575
378.33
385.84
393.80
401.81
409.90
418.09
426.39
434.82
443.37
452.07
460.90
469.87
478.99
488.26
497.66
507.22
516.91
398.69
407.17
416.12
425.10
434.12
443.23
452.44
461.76
471.21
480.78
490.48
500.32
510.30
520.43
530.69
541.09
551.64
0.04126
0.04226
0.04446
0.04656
0.04858
0.05055
0.05247
0.05435
0.05620
0.05804
0.05985
0.06164
0.06342
0.06518
0.06694
0.06869
0.07043
386.82
390.52
398.99
407.44
415.91
424.44
433.06
441.77
450.59
459.53
468.60
477.79
487.13
496.59
506.20
515.95
525.83
407.45
411.65
421.22
430.72
440.20
449.72
459.29
468.94
478.69
488.55
498.52
508.61
518.83
529.19
539.67
550.29
561.04
h
(kJ/kg)
s
(kJ/kg-K)
400 kPa (8.84◦ C)
1.7259
1.7564
1.7874
1.8175
1.8468
1.8755
1.9035
1.9311
1.9582
1.9850
2.0113
2.0373
2.0631
2.0885
2.1136
2.1385
2.1631
0.05136
0.05168
0.05436
0.05693
0.05940
0.06181
0.06417
0.06648
0.06877
0.07102
0.07325
0.07547
0.07767
0.07985
0.08202
0.08418
0.08634
500 kPa (15.66◦ C)
Sat.
20
30
40
50
60
70
80
90
100
110
120
130
140
150
160
170
u
(kJ/kg)
383.02
383.98
392.22
400.45
408.70
417.03
425.44
433.95
442.58
451.34
460.22
469.24
478.40
487.69
497.13
506.71
516.43
403.56
404.65
413.97
423.22
432.46
441.75
451.10
460.55
470.09
479.75
489.52
499.43
509.46
519.63
529.94
540.38
550.97
1.7223
1.7261
1.7584
1.7895
1.8195
1.8487
1.8772
1.9051
1.9325
1.9595
1.9860
2.0122
2.0381
2.0636
2.0889
2.1139
2.1386
600 kPa (21.52◦ C)
1.7198
1.7342
1.7663
1.7971
1.8270
1.8560
1.8843
1.9120
1.9392
1.9660
1.9924
2.0184
2.0440
2.0694
2.0945
2.1193
2.1438
0.03442
—
0.03609
0.03796
0.03974
0.04145
0.04311
0.04473
0.04632
0.04788
0.04943
0.05095
0.05246
0.05396
0.05544
0.05692
0.05839
390.01
—
397.44
406.11
414.75
423.41
432.13
440.93
449.82
458.82
467.94
477.18
486.55
496.05
505.69
515.46
525.36
410.66
—
419.09
428.88
438.59
448.28
457.99
467.76
477.61
487.55
497.59
507.75
518.03
528.43
538.95
549.61
560.40
1.7179
—
1.7461
1.7779
1.8084
1.8379
1.8666
1.8947
1.9222
1.9492
1.9758
2.0019
2.0277
2.0532
2.0784
2.1033
2.1279
⑦
APPENDIX B
..............814
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.5.2 (continued )
Superheated R-134a
Temp.
(◦ C)
v
(m3 /kg )
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
800 kPa (31.30◦ C)
Sat.
40
50
60
70
80
90
100
110
120
130
140
150
160
170
180
0.02571
0.02711
0.02861
0.03002
0.03137
0.03268
0.03394
0.03518
0.03639
0.03758
0.03876
0.03992
0.04107
0.04221
0.04334
0.04446
395.15
403.17
412.23
421.20
430.17
439.17
448.22
457.35
466.58
475.92
485.37
494.94
504.64
514.46
524.42
534.51
415.72
424.86
435.11
445.22
455.27
465.31
475.38
485.50
495.70
505.99
516.38
526.88
537.50
548.23
559.09
570.08
0.01676
0.01724
0.01844
0.01953
0.02055
0.02151
0.02244
0.02333
0.02420
0.02504
0.02587
0.02669
0.02750
0.02829
0.02907
402.37
406.15
416.08
425.74
435.27
444.74
454.20
463.71
473.27
482.91
492.65
502.48
512.43
522.50
532.68
422.49
426.84
438.21
449.18
459.92
470.55
481.13
491.70
502.31
512.97
523.70
534.51
545.43
556.44
567.57
h
(kJ/kg)
s
(kJ/kg-K)
1000 kPa (39.37◦ C)
1.7150
1.7446
1.7768
1.8076
1.8373
1.8662
1.8943
1.9218
1.9487
1.9753
2.0014
2.0271
2.0525
2.0775
2.1023
2.1268
0.02038
0.02047
0.02185
0.02311
0.02429
0.02542
0.02650
0.02754
0.02856
0.02956
0.03053
0.03150
0.03244
0.03338
0.03431
0.03523
1200 kPa (46.31◦ C)
Sat.
50
60
70
80
90
100
110
120
130
140
150
160
170
180
u
(kJ/kg)
399.16
399.78
409.39
418.78
428.05
437.29
446.53
455.82
465.18
474.62
484.16
493.81
503.57
513.46
523.46
533.60
419.54
420.25
431.24
441.89
452.34
462.70
473.03
483.36
493.74
504.17
514.69
525.30
536.02
546.84
557.77
568.83
1.7125
1.7148
1.7494
1.7818
1.8127
1.8425
1.8713
1.8994
1.9268
1.9537
1.9801
2.0061
2.0318
2.0570
2.0820
2.1067
1400 kPa (52.42◦ C)
1.7102
1.7237
1.7584
1.7908
1.8217
1.8514
1.8801
1.9081
1.9354
1.9621
1.9884
2.0143
2.0398
2.0649
2.0898
0.01414
—
0.01503
0.01608
0.01704
0.01793
0.01878
0.01958
0.02036
0.02112
0.02186
0.02258
0.02329
0.02399
0.02468
404.98
—
413.03
423.20
433.09
442.83
452.50
462.17
471.87
481.63
491.46
501.37
511.39
521.51
531.75
424.78
—
434.08
445.72
456.94
467.93
478.79
489.59
500.38
511.19
522.05
532.98
543.99
555.10
566.30
1.7077
—
1.7360
1.7704
1.8026
1.8333
1.8628
1.8914
1.9192
1.9463
1.9730
1.9991
2.0248
2.0502
2.0752
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.5.2 (continued )
..............
⑦
815
Superheated R-134a
Temp.
(◦ C)
v
(m3 /kg )
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
1600 kPa (57.90◦ C)
Sat.
60
70
80
90
100
110
120
130
140
150
160
170
180
0.01215
0.01239
0.01345
0.01438
0.01522
0.01601
0.01676
0.01748
0.01817
0.01884
0.01949
0.02013
0.02076
0.02138
407.11
409.49
420.37
430.72
440.79
450.71
460.57
470.42
480.30
490.23
500.24
510.33
520.52
530.81
426.54
429.32
441.89
453.72
465.15
476.33
487.39
498.39
509.37
520.38
531.43
542.54
553.73
565.02
0.00528
0.00575
0.00665
0.00734
0.00792
0.00845
0.00893
0.00937
0.00980
0.01021
0.01060
411.83
418.93
433.77
446.48
458.27
469.58
480.61
491.49
502.30
513.09
523.89
427.67
436.19
453.73
468.50
482.04
494.91
507.39
519.62
531.70
543.71
555.69
1.7051
1.7135
1.7507
1.7847
1.8166
1.8469
1.8762
1.9045
1.9321
1.9591
1.9855
2.0115
2.0370
2.0622
0.00930
—
0.00958
0.01055
0.01137
0.01211
0.01279
0.01342
0.01403
0.01461
0.01517
0.01571
0.01624
0.01676
0.001059
0.001150
0.001307
0.001698
0.002396
0.002985
0.003439
0.003814
0.004141
0.004435
328.34
346.71
368.06
396.59
426.81
448.34
465.19
479.89
493.45
506.35
334.70
353.61
375.90
406.78
441.18
466.25
485.82
502.77
518.30
532.96
s
(kJ/kg-K)
410.15
—
413.37
425.20
436.20
446.78
457.12
467.34
477.51
487.68
497.89
508.15
518.48
528.89
428.75
—
432.53
446.30
458.95
471.00
482.69
494.19
505.57
516.90
528.22
539.57
550.96
562.42
1.6991
—
1.7101
1.7497
1.7850
1.8177
1.8487
1.8783
1.9069
1.9346
1.9617
1.9882
2.0142
2.0398
4000 kPa (100.33◦ C)
1.6759
1.6995
1.7472
1.7862
1.8211
1.8535
1.8840
1.9133
1.9415
1.9689
1.9956
0.00252
—
—
0.00428
0.00500
0.00556
0.00603
0.00644
0.00683
0.00718
0.00752
6000 kPa
90
100
110
120
130
140
150
160
170
180
h
(kJ/kg)
2000 kPa (67.48◦ C)
3000 kPa (86.20◦ C)
Sat.
90
100
110
120
130
140
150
160
170
180
u
(kJ/kg)
394.86
—
—
429.74
445.97
459.63
472.19
484.15
495.77
507.19
518.51
404.94
—
—
446.84
465.99
481.87
496.29
509.92
523.07
535.92
548.57
1.6036
—
—
1.7148
1.7642
1.8040
1.8394
1.8720
1.9027
1.9320
1.9603
l0000 kPa
1.4081
1.4595
1.5184
1.5979
1.6843
1.7458
1.7926
1.8322
1.8676
1.9004
0.000991
0.001040
0.001100
0.001175
0.001272
0.001400
0.001564
0.001758
0.001965
0.002172
320.72
336.45
352.74
369.69
387.44
405.97
424.99
443.77
461.65
478.40
330.62
346.85
363.73
381.44
400.16
419.98
440.63
461.34
481.30
500.12
1.3856
1.4297
1.4744
1.5200
1.5670
1.6155
1.6649
1.7133
1.7589
1.8009
⑦
APPENDIX B
..............816
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.6
Thermodynamic Properties of Nitrogen
TABLE B.6.1
Saturated Nitrogen
Specific Volume, m3 /kg
Internal Energy, kJ/kg
Temp.
(K)
Press.
(kPa)
Sat. Liquid
vf
Evap.
v fg
Sat. Vapor
vg
Sat. Liquid
uf
Evap.
u fg
Sat. Vapor
ug
63.1
65
70
75
77.3
80
85
90
95
100
105
110
115
120
125
126.2
12.5
17.4
38.6
76.1
101.3
137.0
229.1
360.8
541.1
779.2
1084.6
1467.6
1939.3
2513.0
3208.0
3397.8
0.001150
0.001160
0.001191
0.001223
0.001240
0.001259
0.001299
0.001343
0.001393
0.001452
0.001522
0.001610
0.001729
0.001915
0.002355
0.003194
1.48074
1.09231
0.52513
0.28052
0.21515
0.16249
0.10018
0.06477
0.04337
0.02975
0.02066
0.01434
0.00971
0.00608
0.00254
0
1.48189
1.09347
0.52632
0.28174
0.21639
0.16375
0.10148
0.06611
0.04476
0.03120
0.02218
0.01595
0.01144
0.00799
0.00490
0.00319
−150.92
−147.19
−137.13
−127.04
−122.27
−116.86
−106.55
−96.06
−85.35
−74.33
−62.89
−50.81
−37.66
−22.42
−0.83
18.94
196.86
194.37
187.54
180.47
177.04
173.06
165.20
156.76
147.60
137.50
126.18
113.11
97.36
76.63
40.73
0
45.94
47.17
50.40
53.43
54.76
56.20
58.65
60.70
62.25
63.17
63.29
62.31
59.70
54.21
39.90
18.94
Enthalpy, kJ/kg
Entropy, kJ/kg-K
Temp.
(K)
Press.
(kPa)
Sat. Liquid
hf
Evap.
h fg
Sat. Vapor
hg
Sat. Liquid
sf
Evap.
s fg
Sat. Vapor
sg
63.1
65
70
75
77.3
80
85
90
95
100
105
110
115
120
125
126.2
12.5
17.4
38.6
76.1
101.3
137.0
229.1
360.8
541.1
779.2
1084.6
1467.6
1939.3
2513.0
3208.0
3397.8
−150.91
−147.17
−137.09
−126.95
−122.15
−116.69
−106.25
−95.58
−84.59
−73.20
−61.24
−48.45
−34.31
−17.61
6.73
29.79
215.39
213.38
207.79
201.82
198.84
195.32
188.15
180.13
171.07
160.68
148.59
134.15
116.19
91.91
48.88
0
64.48
66.21
70.70
74.87
76.69
78.63
81.90
84.55
86.47
87.48
87.35
85.71
81.88
74.30
55.60
29.79
2.4234
2.4816
2.6307
2.7700
2.8326
2.9014
3.0266
3.1466
3.2627
3.3761
3.4883
3.6017
3.7204
3.8536
4.0399
4.2193
3.4109
3.2828
2.9684
2.6909
2.5707
2.4415
2.2135
2.0015
1.8007
1.6068
1.4151
1.2196
1.0104
0.7659
0.3910
0
5.8343
5.7645
5.5991
5.4609
5.4033
5.3429
5.2401
5.1480
5.0634
4.9829
4.9034
4.8213
4.7307
4.6195
4.4309
4.2193
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.6.2
..............
⑦
817
Superheated Nitrogen
Temp.
(K)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
100 kPa (77.24 K)
Sat.
100
120
140
160
180
200
220
240
260
280
300
350
400
450
500
600
700
800
900
1000
0.21903
0.29103
0.35208
0.41253
0.47263
0.53254
0.59231
0.65199
0.71161
0.77118
0.83072
0.89023
1.03891
1.18752
1.33607
1.48458
1.78154
2.07845
2.37532
2.67217
2.96900
54.70
72.84
87.94
102.95
117.91
132.83
147.74
162.63
177.51
192.39
207.26
222.14
259.35
296.66
334.16
371.95
448.79
527.74
609.07
692.79
778.78
76.61
101.94
123.15
144.20
165.17
186.09
206.97
227.83
248.67
269.51
290.33
311.16
363.24
415.41
467.77
520.41
626.94
735.58
846.60
960.01
1075.68
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
200 kPa (83.62 K)
5.4059
5.6944
5.8878
6.0501
6.1901
6.3132
6.4232
6.5227
6.6133
6.6967
6.7739
6.8457
7.0063
7.1456
7.2690
7.3799
7.5741
7.7415
7.8897
8.0232
8.1451
0.11520
0.14252
0.17397
0.20476
0.23519
0.26542
0.29551
0.32552
0.35546
0.38535
0.41520
0.44503
0.51952
0.59392
0.66827
0.74258
0.89114
1.03965
1.18812
1.33657
1.48501
58.01
71.73
87.14
102.33
117.40
132.41
147.37
162.31
177.23
192.14
207.04
221.93
259.18
296.52
334.04
371.85
448.71
527.68
609.02
692.75
778.74
81.05
100.24
121.93
143.28
164.44
185.49
206.48
227.41
248.32
269.21
290.08
310.94
363.09
415.31
467.70
520.37
626.94
735.61
846.64
960.07
1075.75
5.2673
5.4775
5.6753
5.8399
5.9812
6.1052
6.2157
6.3155
6.4064
6.4900
6.5674
6.6393
6.8001
6.9396
7.0630
7.1740
7.3682
7.5357
7.6839
7.8175
7.9393
⑦
APPENDIX B
..............818
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.6.2 (continued )
Superheated Nitrogen
Temp.
(K)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
400 kPa (91.22 K)
Sat.
100
120
140
160
180
200
220
240
260
280
300
350
400
450
500
600
700
800
900
1000
0.05992
0.06806
0.08486
0.10085
0.11647
0.13186
0.14712
0.16228
0.17738
0.19243
0.20745
0.22244
0.25982
0.29712
0.33437
0.37159
0.44595
0.52025
0.59453
0.66878
0.74302
61.13
69.30
85.48
101.06
116.38
131.55
146.64
161.68
176.67
191.64
206.58
221.52
258.85
296.25
333.81
371.65
448.55
527.55
608.92
692.67
778.68
85.10
96.52
119.42
141.40
162.96
184.30
205.49
226.59
247.62
268.61
289.56
310.50
362.78
415.10
467.56
520.28
626.93
735.65
846.73
960.19
1075.89
0.03038
0.04017
0.04886
0.05710
0.06509
0.07293
0.08067
0.08835
0.09599
0.10358
0.11115
0.12998
0.14873
0.18609
0.22335
0.26056
0.29773
0.33488
0.37202
63.21
81.88
98.41
114.28
129.82
145.17
160.40
175.54
190.63
205.68
220.70
258.19
295.69
371.25
448.24
527.31
608.73
692.52
778.55
87.52
114.02
137.50
159.95
181.89
203.51
224.94
246.23
267.42
288.54
309.62
362.17
414.68
520.12
626.93
735.76
846.91
960.42
1076.16
h
(kJ/kg)
s
(kJ/kg-K)
600 kPa (96.37 K)
5.1268
5.2466
5.4556
5.6250
5.7690
5.8947
6.0063
6.1069
6.1984
6.2824
6.3600
6.4322
6.5934
6.7331
6.8567
6.9678
7.1622
7.3298
7.4781
7.6117
7.7335
0.04046
0.04299
0.05510
0.06620
0.07689
0.08734
0.09766
0.10788
0.11803
0.12813
0.13820
0.14824
0.17326
0.19819
0.22308
0.24792
0.29755
0.34712
0.39666
0.44618
0.49568
800 kPa (100.38 K)
Sat.
120
140
160
180
200
220
240
260
280
300
350
400
500
600
700
800
900
1000
u
(kJ/kg)
62.57
66.41
83.73
99.75
115.34
130.69
145.91
161.04
176.11
191.13
206.13
221.11
258.52
295.97
333.57
371.45
448.40
527.43
608.82
692.59
778.61
86.85
92.20
116.79
139.47
161.47
183.10
204.50
225.76
246.92
268.01
289.05
310.06
362.48
414.89
467.42
520.20
626.93
735.70
846.82
960.30
1076.02
5.0411
5.0957
5.3204
5.4953
5.6422
5.7696
5.8823
5.9837
6.0757
6.1601
6.2381
6.3105
6.4722
6.6121
6.7359
6.8471
7.0416
7.2093
7.3576
7.4912
7.6131
1000 kPa (103.73 K)
4.9768
5.2191
5.4002
5.5501
5.6793
5.7933
5.8954
5.9880
6.0728
6.1511
6.2238
6.3858
6.5260
6.7613
6.9560
7.1237
7.2721
7.4058
7.5277
0.02416
0.03117
0.03845
0.04522
0.05173
0.05809
0.06436
0.07055
0.07670
0.08281
0.08889
0.10401
0.11905
0.14899
0.17883
0.20862
0.23837
0.26810
0.29782
63.35
79.91
97.02
113.20
128.94
144.43
159.76
174.98
190.13
205.23
220.29
257.86
295.42
371.04
448.09
527.19
608.63
692.44
778.49
87.51
111.08
135.47
158.42
180.67
202.52
224.11
245.53
266.83
288.04
309.18
361.87
414.47
520.04
626.92
735.81
847.00
960.54
1076.30
4.9237
5.1357
5.3239
5.4772
5.6082
5.7234
5.8263
5.9194
6.0047
6.0833
6.1562
6.3187
6.4591
6.6947
6.8895
7.0573
7.2057
7.3394
7.4614
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.6.2 (continued )
..............
⑦
819
Superheated Nitrogen
Temp.
(K)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
1500 kPa (110.38 K)
Sat.
120
140
160
180
200
220
240
260
280
300
350
400
450
500
600
700
800
900
1000
0.01555
0.01899
0.02452
0.02937
0.03393
0.03832
0.04260
0.04682
0.05099
0.05512
0.05922
0.06940
0.07949
0.08953
0.09953
0.11948
0.13937
0.15923
0.17906
0.19889
62.17
74.26
93.36
110.44
126.71
142.56
158.14
173.57
188.87
204.10
219.27
257.03
294.73
332.53
370.54
447.71
526.89
608.39
692.24
778.32
85.51
102.75
130.15
154.50
177.60
200.03
222.05
243.80
265.36
286.78
308.10
361.13
413.96
466.82
519.84
626.92
735.94
847.22
960.83
1076.65
u
(kJ/kg)
0.00582
0.01038
0.01350
0.01614
0.01857
0.02088
0.02312
0.02531
0.02746
0.02958
0.03480
0.03993
0.05008
0.06013
0.07012
0.08008
0.09003
0.09996
46.03
79.98
101.35
119.68
136.78
153.24
169.30
185.10
200.72
216.21
254.57
292.70
369.06
446.57
525.99
607.67
691.65
777.85
63.47
111.13
141.85
168.09
192.49
215.88
238.66
261.02
283.09
304.94
358.96
412.50
519.29
626.95
736.35
847.92
961.73
1077.72
s
(kJ/kg-K)
2000 kPa (115.58 K)
4.8148
4.9650
5.1767
5.3394
5.4755
5.5937
5.6987
5.7933
5.8796
5.9590
6.0325
6.1960
6.3371
6.4616
6.5733
6.7685
6.9365
7.0851
7.2189
7.3409
0.01100
0.01260
0.01752
0.02144
0.02503
0.02844
0.03174
0.03496
0.03814
0.04128
0.04440
0.05209
0.05971
0.06727
0.07480
0.08980
0.10474
0.11965
0.13454
0.14942
59.25
66.90
89.37
107.55
124.42
140.66
156.52
172.15
187.62
202.97
218.24
256.21
294.05
331.95
370.05
447.33
526.59
608.14
692.04
778.16
3000 kPa (123.61 K)
Sat.
140
160
180
200
220
240
260
280
300
350
400
500
600
700
800
900
1000
h
(kJ/kg)
81.25
92.10
124.40
150.43
174.48
197.53
219.99
242.08
263.90
285.53
307.03
360.39
413.47
466.49
519.65
626.93
736.07
847.45
961.13
1077.01
4.7193
4.8116
5.0618
5.2358
5.3775
5.4989
5.6060
5.7021
5.7894
5.8696
5.9438
6.1083
6.2500
6.3750
6.4870
6.6825
6.8507
6.9994
7.1333
7.2553
10000 kPa
4.5032
4.8706
5.0763
5.2310
5.3596
5.4711
5.5702
5.6597
5.7414
5.8168
5.9834
6.1264
6.3647
6.5609
6.7295
6.8785
7.0125
7.1347
—
0.00200
0.00291
0.00402
0.00501
0.00590
0.00672
0.00749
0.00824
0.00895
0.01067
0.01232
0.01551
0.01861
0.02167
0.02470
0.02771
0.03072
—
—
0.84
47.44
82.44
108.21
129.86
149.42
167.77
185.34
202.38
243.57
283.59
362.42
441.47
521.96
604.42
689.02
775.68
20.87
76.52
122.65
158.35
188.88
216.64
242.72
267.69
291.90
350.26
406.79
517.48
627.58
738.65
851.43
966.15
1082.84
—
4.0373
4.4088
4.6813
4.8697
5.0153
5.1362
5.2406
5.3331
5.4167
5.5967
5.7477
5.9948
6.1955
6.3667
6.5172
6.6523
6.7753
⑦
APPENDIX B
..............820
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.7
Thermodynamic Properties of Methane
TABLE B.7.1
Saturated Methane
Specific Volume, m3 /kg
Internal Energy, kJ/kg
Temp. (K)
P (kPa)
vf
v fg
vg
uf
u fg
ug
90.7
95
100
105
110
111.7
115
120
125
130
135
140
145
150
155
160
165
170
175
180
185
190
190.6
11.7
19.8
34.4
56.4
88.2
101.3
132.3
191.6
269.0
367.6
490.7
641.6
823.7
1040.5
1295.6
1592.8
1935.9
2329.3
2777.6
3286.4
3863.2
4520.5
4599.2
0.002215
0.002243
0.002278
0.002315
0.002353
0.002367
0.002395
0.002439
0.002486
0.002537
0.002592
0.002653
0.002719
0.002794
0.002877
0.002974
0.003086
0.003222
0.003393
0.003623
0.003977
0.004968
0.006148
3.97941
2.44845
1.47657
0.93780
0.62208
0.54760
0.42800
0.30367
0.22108
0.16448
0.12458
0.09575
0.07445
0.05839
0.04605
0.03638
0.02868
0.02241
0.01718
0.01266
0.00846
0.00300
0
3.98163
2.45069
1.47885
0.94012
0.62443
0.54997
0.43040
0.30610
0.22357
0.16701
0.12717
0.09841
0.07717
0.06118
0.04892
0.03936
0.03177
0.02563
0.02058
0.01629
0.01243
0.00797
0.00615
−358.10
−343.79
−326.90
−309.79
−292.50
−286.74
−275.05
−257.45
−239.66
−221.65
−203.40
−184.86
−165.97
−146.65
−126.82
−106.35
−85.06
−62.67
−38.75
−12.43
18.47
69.10
101.46
496.59
488.62
478.96
468.89
458.41
454.85
447.48
436.02
423.97
411.25
397.77
383.42
368.06
351.53
333.61
314.01
292.30
267.81
239.47
205.16
159.49
67.01
0
138.49
144.83
152.06
159.11
165.91
168.10
172.42
178.57
184.32
189.60
194.37
198.56
202.09
204.88
206.79
207.66
207.24
205.14
200.72
192.73
177.96
136.11
101.46
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.7.1 (continued )
..............
⑦
821
Saturated Methane
Enthalpy, kJ/kg
Entropy, kJ/kg-K
Temp. (K)
P (kPa)
hf
h fg
hg
sf
s fg
sg
90.7
95
100
105
110
111.7
115
120
125
130
135
140
145
150
155
160
165
170
175
180
185
190
190.6
11.7
19.8
34.4
56.4
88.2
101.3
132.3
191.6
269.0
367.6
490.7
641.6
823.7
1040.5
1295.6
1592.8
1935.9
2329.3
2777.6
3286.4
3863.2
4520.5
4599.2
−358.07
−343.75
−326.83
−309.66
−292.29
−286.50
−274.74
−256.98
−238.99
−220.72
−202.13
−183.16
−163.73
−143.74
−123.09
−101.61
−79.08
−55.17
−29.33
−0.53
33.83
91.56
129.74
543.12
537.18
529.77
521.82
513.29
510.33
504.12
494.20
483.44
471.72
458.90
444.85
429.38
412.29
393.27
371.96
347.82
320.02
287.20
246.77
192.16
80.58
0
185.05
193.43
202.94
212.16
221.00
223.83
229.38
237.23
244.45
251.00
256.77
261.69
265.66
268.54
270.18
270.35
268.74
264.85
257.87
246.25
226.00
172.14
129.74
4.2264
4.3805
4.5538
4.7208
4.8817
4.9336
5.0368
5.1867
5.3321
5.4734
5.6113
5.7464
5.8794
6.0108
6.1415
6.2724
6.4046
6.5399
6.6811
6.8333
7.0095
7.3015
7.4999
5.9891
5.6545
5.2977
4.9697
4.6663
4.5706
4.3836
4.1184
3.8675
3.6286
3.3993
3.1775
2.9613
2.7486
2.5372
2.3248
2.1080
1.8824
1.6411
1.3710
1.0387
0.4241
0
10.2155
10.0350
9.8514
9.6905
9.5480
9.5042
9.4205
9.3051
9.1996
9.1020
9.0106
8.9239
8.8406
8.7594
8.6787
8.5971
8.5126
8.4224
8.3223
8.2043
8.0483
7.7256
7.4999
⑦
APPENDIX B
..............822
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.7.2
Superheated Methane
Temp.
(K)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
100 kPa (111.50K)
Sat.
125
150
175
200
225
250
275
300
325
350
375
400
425
0.55665
0.63126
0.76586
0.89840
1.02994
1.16092
1.29154
1.42193
1.55215
1.68225
1.81226
1.94220
2.07209
2.20193
167.90
190.21
230.18
269.72
309.20
348.90
389.12
430.17
472.36
516.00
561.34
608.58
657.89
709.36
223.56
253.33
306.77
359.56
412.19
464.99
518.27
572.36
627.58
684.23
742.57
802.80
865.10
929.55
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
200 kPa (120.61 K)
9.5084
9.7606
10.1504
10.4759
10.7570
11.0058
11.2303
11.4365
11.6286
11.8100
11.9829
12.1491
12.3099
12.4661
0.29422
0.30695
0.37700
0.44486
0.51165
0.57786
0.64370
0.70931
0.77475
0.84008
0.90530
0.97046
1.03557
1.10062
179.30
186.80
227.91
268.05
307.88
347.81
388.19
429.36
471.65
515.37
560.77
608.07
657.41
708.92
238.14
248.19
303.31
357.02
410.21
463.38
516.93
571.22
626.60
683.38
741.83
802.16
864.53
929.05
9.2918
9.3736
9.7759
10.1071
10.3912
10.6417
10.8674
11.0743
11.2670
11.4488
11.6220
11.7885
11.9495
12.1059
............................................................................................................
APPENDIX B
SI UNITS: THERMODYNAMIC TABLES
TABLE B.7.2 (continued )
..............
⑦
823
Superheated Methane
Temp.
(K)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
400 kPa (131.42 K)
Sat.
150
175
200
225
250
275
300
325
350
375
400
425
450
475
500
525
0.15427
0.18233
0.21799
0.25246
0.28631
0.31978
0.35301
0.38606
0.41899
0.45183
0.48460
0.51731
0.54997
0.58260
0.61520
0.64778
0.68033
191.01
223.16
264.61
305.19
345.61
386.32
427.74
470.23
514.10
559.63
607.03
656.47
708.05
761.85
817.89
876.18
936.67
252.72
296.09
351.81
406.18
460.13
514.23
568.94
624.65
681.69
740.36
800.87
863.39
928.04
994.89
1063.97
1135.29
1208.81
0.07941
0.08434
0.10433
0.12278
0.14050
0.15781
0.17485
0.19172
0.20845
0.22510
0.24167
0.25818
0.27465
0.29109
0.30749
0.32387
0.34023
0.35657
201.70
212.53
257.30
299.62
341.10
382.53
424.47
467.36
511.55
557.33
604.95
654.57
706.31
760.24
816.40
874.79
935.38
998.14
265.23
280.00
340.76
397.85
453.50
508.78
564.35
620.73
678.31
737.41
798.28
861.12
926.03
993.11
1062.40
1133.89
1207.56
1283.45
h
(kJ/kg)
s
(kJ/kg-K)
600 kPa (138.72 K)
9.0754
9.3843
9.7280
10.0185
10.2726
10.5007
10.7092
10.9031
11.0857
11.2595
11.4265
11.5879
11.7446
11.8974
12.0468
12.1931
12.3366
0.10496
0.11717
0.14227
0.16603
0.18911
0.21180
0.23424
0.25650
0.27863
0.30067
0.32264
0.34456
0.36643
0.38826
0.41006
0.43184
0.45360
800 kPa (144.40 K)
Sat.
150
175
200
225
250
275
300
325
350
375
400
425
450
475
500
525
550
u
(kJ/kg)
197.54
218.08
261.03
302.44
343.37
384.44
426.11
468.80
512.82
558.48
605.99
655.52
707.18
761.05
817.15
875.48
936.03
260.51
288.38
346.39
402.06
456.84
511.52
566.66
622.69
680.00
738.88
799.57
862.25
927.04
994.00
1063.18
1134.59
1208.18
8.9458
9.1390
9.4970
9.7944
10.0525
10.2830
10.4931
10.6882
10.8716
11.0461
11.2136
11.3754
11.5324
11.6855
11.8351
11.9816
12.1252
1000 kPa (149.13 K)
8.8505
8.9509
9.3260
9.6310
9.8932
10.1262
10.3381
10.5343
10.7186
10.8938
11.0617
11.2239
11.3813
11.5346
11.6845
11.8311
11.9749
12.1161
0.06367
0.06434
0.08149
0.09681
0.11132
0.12541
0.13922
0.15285
0.16635
0.17976
0.19309
0.20636
0.21959
0.23279
0.24595
0.25909
0.27221
0.28531
204.45
206.28
253.38
296.73
338.79
380.61
422.82
465.91
510.26
556.18
603.91
653.62
705.44
759.44
815.66
874.10
934.73
997.53
268.12
270.62
334.87
393.53
450.11
506.01
562.04
618.76
676.61
735.94
797.00
859.98
925.03
992.23
1061.61
1133.19
1206.95
1282.84
8.7735
8.7902
9.1871
9.5006
9.7672
10.0028
10.2164
10.4138
10.5990
10.7748
10.9433
11.1059
11.2636
11.4172
11.5672
11.7141
11.8580
11.9992
⑦
APPENDIX B
..............824
www.elsolucionario.org
SI UNITS: THERMODYNAMIC TABLES
............................................................................................................
TABLE B.7.2 (continued )
Superheated Methane
Temp.
(K)
v
(m3 /kg)
u
(kJ/kg)
h
(kJ/kg)
s
(kJ/kg-K)
v
(m3 /kg)
1500 kPa (158.52 K)
Sat.
175
200
225
250
275
300
325
350
375
400
425
450
475
500
525
550
0.04196
0.05078
0.06209
0.07239
0.08220
0.09171
0.10103
0.11022
0.11931
0.12832
0.13728
0.14619
0.15506
0.16391
0.17273
0.18152
0.19031
207.53
242.64
289.13
332.85
375.70
418.65
462.27
507.04
553.30
601.30
651.24
703.26
757.43
813.80
872.37
933.12
996.02
270.47
318.81
382.26
441.44
499.00
556.21
613.82
672.37
732.26
793.78
857.16
922.54
990.02
1059.66
1131.46
1205.41
1281.48
0.01160
0.01763
0.02347
0.02814
0.03235
0.03631
0.04011
0.04381
0.04742
0.05097
0.05448
0.05795
0.06139
0.06481
0.06820
0.07158
0.07495
172.96
237.70
298.52
349.08
396.67
443.48
490.62
538.70
588.18
639.34
692.38
747.43
804.55
863.78
925.11
988.53
1053.98
219.34
308.23
392.39
461.63
526.07
588.73
651.07
713.93
777.86
843.24
910.31
979.23
1050.12
1123.01
1197.93
1274.86
1353.77
h
(kJ/kg)
s
(kJ/kg-K)
2000 kPa (165.86 K)
8.6215
8.9121
9.2514
9.5303
9.7730
9.9911
10.1916
10.3790
10.5565
10.7263
10.8899
11.0484
11.2027
11.3532
11.5005
11.6448
11.7864
0.03062
0.03504
0.04463
0.05289
0.06059
0.06796
0.07513
0.08216
0.08909
0.09594
0.10274
0.10949
0.11620
0.12289
0.12955
0.13619
0.14281
4000 kPa (186.10 K)
Sat.
200
225
250
275
300
325
350
375
400
425
450
475
500
525
550
575
u
(kJ/kg)
207.01
229.90
280.91
326.64
370.67
414.40
458.59
503.80
550.40
598.69
648.87
701.08
755.43
811.94
870.64
931.51
994.51
268.25
299.97
370.17
432.43
491.84
550.31
608.85
668.12
728.58
790.57
854.34
920.06
987.84
1057.72
1129.74
1203.88
1280.13
8.4975
8.6839
9.0596
9.3532
9.6036
9.8266
10.0303
10.2200
10.3992
10.5703
10.7349
10.8942
11.0491
11.2003
11.3480
11.4927
11.6346
8000 kPa
8.0035
8.4675
8.8653
9.1574
9.4031
9.6212
9.8208
10.0071
10.1835
10.3523
10.5149
10.6725
10.8258
10.9753
11.1215
11.2646
11.4049
—
0.00412
0.00846
0.01198
0.01469
0.01705
0.01924
0.02130
0.02328
0.02520
0.02707
0.02891
0.03072
0.03251
0.03428
0.03603
0.03776
—
55.58
217.30
298.05
357.88
411.71
463.52
515.02
567.12
620.38
675.14
731.63
789.99
850.28
912.54
976.77
1042.96
—
88.54
284.98
393.92
475.39
548.15
617.40
685.39
753.34
821.95
891.71
962.92
1035.75
1110.34
1186.74
1264.99
1345.07
—
7.2069
8.1344
8.5954
8.9064
9.1598
9.3815
9.5831
9.7706
9.9477
10.1169
10.2796
10.4372
10.5902
10.7393
10.8849
11.0272
APPEN
Three types of energy storage or possession were identified in Section 1.8, of which two,
translation and intramolecular energy, are associated with the individual molecules. These
comprise the ideal gas model, with the third type, the system intermolecular potential
energy, then accounting for the behavior of real (nonideal gas) substances. This appendix
deals with the ideal gas contributions. Since these contribute to the energy, and therefore also
the enthalpy, they also contribute to the specific heat of each gas. The different possibilities
can be grouped according to the intramolecular energy contributions as follows:
C.1 MONATOMIC GASES (INERT GASES AR, HE, NE,
XE, KR; ALSO N, O, H, CL, F, . . . )
h = h translation + h electronic = h t + h e
dh
dh t
dh e
5
=
+
,
C P0 = C P0t + C P0e = R + f e (T )
dT
dT
dT
2
where the electronic contribution, f e (T ), is usually small, except at very high T (common
exceptions are O, Cl, F).
C.2 DIATOMIC AND LINEAR POLYATOMIC GASES
(N2 , O2 , CO, OH, . . . , CO2 , N2 O, . . . )
In addition to translational and electronic contributions to specific heat, these also have
molecular rotation (about the center of mass of the molecule) and also (3a − 5) independent
modes of molecular vibration of the a atoms in the molecule relative to one another, such
that
5
C P0 = C P0t + C P0r + C P0v + C P0e = R + R + f v (T ) + f e (T )
2
where the vibrational contribution is
3a−5
f v (T ) = R
i=1
[x i2 e xi /(e xi − 1)2 ],
xi =
θi
T
and the electronic contribution, fe (T ), is usually small, except at very high T (common
exceptions are O2 , NO, OH).
825
X
C
DI
Ideal Gas Specific
Heat
⑦
APPENDIX C
..............826
www.elsolucionario.org
IDEAL GAS SPECIFIC HEAT
........................................................................................................................
Example C.1
N2 , 3a − 5 = 1 vibrational mode, with θ i = 3392 K.
At T = 300 K, C P0 = 0.742 + 0.2968 + 0.0005 + ≈0 = 1.0393 kJ/kg K.
At T = 1000 K, C P0 = 0.742 + 0.2968 + 0.123 + ≈0 = 1.1618 kJ/kg K.
(an increase of 11.8% from 300 K).
Example C.2
CO2 , 3a − 5 = 4 vibrational modes, with θ i = 960 K, 960 K, 1993 K, 3380 K
At T = 300 K, C P0 = 0.4723 + 0.1889 + 0.1826 + ≈0 = 0.8438 kJ/kg K.
At T = 1000 K, C P0 = 0.4723 + 0.1889 + 0.5659 + ≈0 = 1.2271 kJ/kg K.
(an increase of 45.4% from 300 K).
C.3 NONLINEAR POLYATOMIC MOLECULES
(H2 O, NH3 , CH4 , C2 H6 , . . . )
Contributions to specific heat are similar to those for linear molecules, except that the
rotational contribution is larger and there are (3a − 6) independent vibrational modes, such
that
3
5
C P0 = C P0t + C p0r + C P0v + C P0e = R + R + f v (T ) + fe (T )
2
2
where the vibrational contribution is
3a−6
f v (T ) = R
i=1
[xi2 e xi /(e xi − 1)2 ],
xi =
θi
T
and f e (T ) is usually small, except at very high temperatures.
Example C.3
CH4 , 3a − 6 = 9 vibrational modes, with θ i = 4196 K, 2207 K (two modes), 1879 K
(three), 4343 K (three)
At T = 300 K, C P0 = 1.2958 + 0.7774 + 0.1527 + ≈0 = 2.2259 kJ/kg K.
At T = 1000 K, C P0 = 1.2958 + 0.7774 + 2.4022 + ≈0 = 4.4754 kJ/kg K.
(an increase of 101.1% from 300 K).
APPEN
Some of the most used pressure-explicit equations of state can be shown in a form with two
parameters. This form is known as a cubic equation of state and contains as a special case
the ideal-gas law:
P=
a
RT
−
v − b v 2 + cbv + db2
where (a, b) are parameters and (c, d ) define the model as shown in the following table with
the acentric factor (ω) and
b = b0 RTc /Pc
a = a0 R 2 Tc2/Pc
and
The acentric factor is defined by the saturation pressure at a reduced temperature
T r = 0.7
ω=−
ln Prsat at Tr = 0.7
−1
ln 10
TABLE D.1
Equations of State
Model
c
d
b0
a0
Ideal gas
van der Waals
Redlich–Kwong
Soave
Peng–Robinson
0
0
1
1
2
0
0
0
0
−1
0
1/8
0.08664
0.08664
0.0778
0
27/64
0.42748 Tr−1/2
2
0.42748[1 + f (1 − Tr1/2 )]
1/2 2
0.45724[1 + f (1 − Tr )]
f = 0.48 + 1.574ω − 0.176ω2
f = 0.37464 + 1.54226 ω − 0.26992ω
for Soave
2
for Peng–Robinson
827
X
D
DI
Equations of State
⑦
APPENDIX D
..............828
www.elsolucionario.org
EQUATIONS OF STATE
.............................................................................................................................
TABLE D.2
The Lee–Kesler Equation of State
The Lee–Kesler generalized equation of state is
Z=
"
#
"
#
Pr v r
γ
γ
B
C
D
c4
=1+
+ 2 + 5 + 3 2 β + 2 exp − 2
Tr
vr
vr
vr
Tr v r
vr
vr
B = b1 −
b2
b3
b4
− 2 − 3
Tr
Tr
Tr
C = c1 −
c2
c3
+ 3
Tr
Tr
D = d1 +
d2
Tr
in which
Tr =
T
P
v
, Pr =
, vr =
Tc
Pc
RTc /Pc
The set of constants is as follows:
Constant
Simple Fluids
Constant
Simple Fluids
b1
b2
b3
b4
c1
c2
0.118 119 3
0.265 728
0.154 790
0.030 323
0.023 674 4
0.018 698 4
c3
c4
d 1 × 104
d 2 × 104
β
γ
0.0
0.042 724
0.155 488
0.623 689
0.653 92
0.060 167
TABLE D.3
Saturated Liquid–Vapor Compressibilities, Lee–Kesler Simple Fluid
Tr
Pr sat
Zf
Zg
0.40
2.7E-4
6.5E-5
0.999
0.50
4.6E-3
9.5E-4
0.988
0.60
0.028
0.0052
0.957
0.70
0.099
0.017
0.897
0.80
0.252
0.042
0.807
0.85
0.373
0.062
0.747
0.90
0.532
0.090
0.673
0.95
0.737
0.132
0.569
1
1
0.29
0.29
TABLE D.4
Acentric Factor for Some Substances
Substance
Ammonia
Argon
Bromine
Helium
Neon
Nitrogen
NH3
Ar
Br2
He
Ne
N2
ω
Substance
0.25
0.001
0.108
−0.365
−0.029
0.039
Water
n-Butane
Ethane
Methane
R-32
R-125
ω
H2 O
C4 H10
C2 H6
CH4
CF2 H2
CHF2 CF3
0.344
0.199
0.099
0.011
0.277
0.305
.............................................................................................................................
APPENDIX D
FIGURE D.1 Lee–Kesler simple fluid compressibility factor.
EQUATIONS OF STATE
..............
⑦
829
⑦
APPENDIX D
..............830
www.elsolucionario.org
EQUATIONS OF STATE
.............................................................................................................................
FIGURE D.2 Lee–Kesler simple fluid enthalpy departure.
.............................................................................................................................
APPENDIX D
FIGURE D.3 Lee–Kesler simple fluid entropy departure.
EQUATIONS OF STATE
..............
⑦
831
APP
www.elsolucionario.org
E
NDIX
E
Figures
832
.............................................................................................................................................
APPENDIX E
FIGURE E.1 Temperature–entropy diagram for water.
c 1969,
Keenan, Keyes, Hill, & Moore. STEAM TABLES (International Edition–Metric Units). Copyright John Wiley & Sons, Inc.
FIGURES
..............
⑦
833
⑦
APPENDIX E
..............834
www.elsolucionario.org
FIGURES
.............................................................................................................................................
FIGURE E.2 Pressure–enthalpy diagram for ammonia.
.............................................................................................................................................
FIGURE E.3 Pressure–enthalpy diagram for oxygen.
APPENDIX E
FIGURES
..............
⑦
835
⑦
APPENDIX E
..............836
www.elsolucionario.org
FIGURES
.............................................................................................................................................
FIGURE E.4 Psychrometric chart.
APPEN
837
X
F
DI
English Unit Tables
⑦
APPENDIX F
..............838
www.elsolucionario.org
ENGLISH UNIT TABLES
.............................................................................................................................
TABLE F.1
Critical Constants (English Units)
Substance
Formula
Molec.
Mass
Temp.
(R)
Pressure
(lbf/in.2 )
Volume
(ft3 /lbm)
Ammonia
Argon
Bromine
Carbon dioxide
Carbon monoxide
Chlorine
Fluorine
Helium
Hydrogen (normal)
Krypton
Neon
Nitric oxide
Nitrogen
Nitrogen dioxide
Nitrous oxide
Oxygen
Sulfur dioxide
Water
Xenon
Acetylene
Benzene
n-Butane
Chlorodifluoroethane (142b)
Chlorodifluoromethane (22)
Dichlorodifluoroethane (141)
Dichlorotrifluoroethane (123)
Difluoroethane (152a)
Difluoromethane (32)
Ethane
Ethyl alcohol
Ethylene
n-Heptane
n-Hexane
Methane
Methyl alcohol
n-Octane
Pentafluoroethane (125)
n-Pentane
Propane
Propene
Refrigerant mixture
Tetrafluoroethane (134a)
NH3
Ar
Br2
CO2
CO
Cl2
F2
He
H2
Kr
Ne
NO
N2
NO2
N2 O
O2
SO2
H2 O
Xe
C2 H2
C6 H6
C4 H10
CH3 CClF2
CHClF2
CH3 CCl2 F
CHCl2 CF3
CHF2 CH3
CH2 F2
C2 H6
C2 H5 OH
C2 H4
C7 H16
C6 H14
CH4
CH3 OH
C8 H18
CHF2 CF3
C5 H12
C3 H8
C3 H8
R-410a
CF3 CH2 F
17.031
39.948
159.808
44.010
28.010
70.906
37.997
4.003
2.016
83.800
20.183
30.006
28.013
46.006
44.013
31.999
64.063
18.015
131.300
26.038
78.114
58.124
100.495
86.469
116.950
152.930
66.050
52.024
30.070
46.069
28.054
100.205
86.178
16.043
32.042
114.232
120.022
72.151
44.094
42.081
72.585
102.030
729.9
271.4
1058.4
547.4
239.2
750.4
259.7
9.34
59.76
376.9
79.92
324.0
227.2
775.8
557.3
278.3
775.4
1165.1
521.5
554.9
1012.0
765.4
738.5
664.7
866.7
822.4
695.5
632.3
549.7
925.0
508.3
972.5
913.5
342.7
922.7
1023.8
610.6
845.5
665.6
656.8
620.1
673.6
1646
706
1494
1070
508
1157
757
32.9
188.6
798
400
940
492
1465
1050
731
1143
3208
847
891
709
551
616
721
658
532
656
838
708
891
731
397
437
667
1173
361
525
489
616
667
711
589
0.0682
0.0300
0.0127
0.0342
0.0533
0.0280
0.0279
0.2300
0.5170
0.0174
0.0330
0.0308
0.0514
0.0584
0.0354
0.0367
0.0306
0.0508
0.0144
0.0693
0.0531
0.0703
0.0368
0.0307
0.0345
0.0291
0.0435
0.0378
0.0790
0.0581
0.0744
0.0691
0.0688
0.0990
0.0590
0.0690
0.0282
0.0675
0.0964
0.0689
0.0349
0.0311
.............................................................................................................................
APPENDIX F
ENGLISH UNIT TABLES
TABLE F.2
TABLE F.3
Properties of Selected Solids at 77 F
Properties of Some Liquids at 77 F
Substance
Asphalt
Brick, common
Carbon, diamond
Carbon, graphite
Coal
Concrete
Glass, plate
Glass, wool
Granite
Ice (32◦ F)
Paper
Plexiglas
Polystyrene
Polyvinyl chloride
Rubber, soft
Sand, dry
Salt, rock
Silicon
Snow, firm
Wood, hard (oak)
Wood, soft (pine)
Wool
Metals
Aluminum, duralumin
Brass, 60-40
Copper, commercial
Gold
Iron, cast
Iron, 304 St Steel
Lead
Magnesium, 2% Mn
Nickel, 10% Cr
Silver, 99.9% Ag
Sodium
Tin
Tungsten
Zinc
ρ
(lbm/ft3 )
132.3
112.4
202.9
125–156
75–95
137
156
1.25
172
57.2
43.7
73.7
57.4
86.1
68.7
93.6
130–156
145.5
35
44.9
31.8
6.24
170
524
518
1205
454
488
708
111
541
657
60.6
456
1205
446
Cp
(Btu/lbm R)
0.225
0.20
0.122
0.146
0.305
0.21
0.191
0.158
0.212
0.487
0.287
0.344
0.549
0.229
0.399
0.191
0.2196
0.167
0.501
0.301
0.33
0.411
0.215
0.0898
0.100
0.03082
0.100
0.110
0.031
0.239
0.1066
0.0564
0.288
0.0525
0.032
0.0927
Substance
Ammonia
Benzene
Butane
CCl4
CO2
Ethanol
Gasoline
Glycerine
Kerosene
Methanol
n-octane
Oil, engine
Oil, light
Propane
R-12
R-22
R-32
R-125
R-134a
R-410a
Water
Liquid Metals
Bismuth, Bi
Lead, Pb
Mercury, Hg
NaK (56/44)
Potassium, K
Sodium, Na
Tin, Sn
Zinc, Zn
ρ
(lbm/ft3 )
..............
⑦
839
Cp
(Btu/lbm R)
37.7
54.9
34.7
98.9
42.5
48.9
46.8
78.7
50.9
49.1
43.2
55.2
57
31.8
81.8
74.3
60
74.4
75.3
66.1
62.2
1.151
0.41
0.60
0.20
0.69
0.59
0.50
0.58
0.48
0.61
0.53
0.46
0.43
0.61
0.232
0.30
0.463
0.337
0.34
0.40
1.00
627
665
848
55.4
51.7
58
434
410
0.033
0.038
0.033
0.27
0.193
0.33
0.057
0.12
⑦
APPENDIX F
..............840
www.elsolucionario.org
ENGLISH UNIT TABLES
.............................................................................................................................
TABLE F.4
Properties of Various Ideal Gases at 77 F, 1 atm∗ (English Units)
Gas
Chemical
Formula
Mol. Mass
(lbm/lbmol)
R
(ft-lbf/lbm R)
ρ × 103
(lbm/ft3 )
C p0
C v0
(Btu/lbm R)
k
C p0 /C v0
Steam
Acetylene
Air
Ammonia
Argon
Butane
Carbon dioxide
Carbon monoxide
Ethane
Ethanol
Ethylene
Helium
Hydrogen
Methane
Methanol
Neon
Nitric oxide
Nitrogen
Nitrous oxide
n-octane
Oxygen
Propane
R-12
R-22
R-32
R-125
R-134a
R-410a
Sulfur dioxide
Sulfur trioxide
H2 O
C2 H2
—
NH3
Ar
C4 H10
CO2
CO
C2 H6
C2 H5 OH
C2 H4
He
H2
CH4
CH3 OH
Ne
NO
N2
N2 O
C8 H18
O2
C3 H8
CCl2 F2
CHClF2
CF2 H2
CHF2 CF3
CF3 CH2 F
—
SO2
SO3
18.015
26.038
28.97
17.031
39.948
58.124
44.01
28.01
30.07
46.069
28.054
4.003
2.016
16.043
32.042
20.183
30.006
28.013
44.013
114.23
31.999
44.094
120.914
86.469
52.024
120.022
102.03
72.585
64.059
80.053
85.76
59.34
53.34
90.72
38.68
26.58
35.10
55.16
51.38
33.54
55.07
386.0
766.5
96.35
48.22
76.55
51.50
55.15
35.10
13.53
48.28
35.04
12.78
17.87
29.70
12.87
15.15
21.29
24.12
19.30
1.442
65.55
72.98
43.325
100.7
150.3
110.8
70.5
76.29
117.6
71.04
10.08
5.075
40.52
81.78
50.81
75.54
70.61
110.8
5.74
80.66
112.9
310.9
221.0
132.6
307.0
262.2
185.2
163.4
204.3
0.447
0.406
0.240
0.509
0.124
0.410
0.201
0.249
0.422
0.341
0.370
1.240
3.394
0.538
0.336
0.246
0.237
0.249
0.210
0.409
0.220
0.401
0.147
0.157
0.196
0.189
0.203
0.193
0.149
0.152
1.327
1.231
1.400
1.297
1.667
1.091
1.289
1.399
1.186
1.145
1.237
1.667
1.409
1.299
1.227
1.667
1.387
1.400
1.274
1.044
1.393
1.126
1.126
1.171
1.242
1.097
1.106
1.165
1.263
1.196
∗ Or
saturation pressure if it is less than 1 atm.
0.337
0.330
0.171
0.392
0.0745
0.376
0.156
0.178
0.356
0.298
0.299
0.744
2.409
0.415
0.274
0.148
0.171
0.178
0.165
0.391
0.158
0.356
0.131
0.134
0.158
0.172
0.184
0.166
0.118
0.127
.............................................................................................................................
APPENDIX F
ENGLISH UNIT TABLES
TABLE F.5
Ideal Gas Properties of Air (English Units), Standard Entropy at 1 atm = 101.325 kPa = 14.696 lbf/in.2
..............
⑦
841
T
(R)
u
(Btu/lbm)
h
(Btu/lbm)
s 0T
(Btu/lbm R)
T
(R)
u
(Btu/lbm)
h
(Btu/lbm)
s 0T
(Btu/lbm R)
400
440
480
520
536.67
540
560
600
640
680
720
760
800
840
880
920
960
1000
1040
1080
1120
1160
1200
1240
1280
1320
1360
1400
1440
1480
1520
1560
1600
1650
1700
1750
1800
1850
1900
68.212
75.047
81.887
88.733
91.589
92.160
95.589
102.457
109.340
116.242
123.167
130.118
137.099
144.114
151.165
158.255
165.388
172.564
179.787
187.058
194.378
201.748
209.168
216.640
224.163
231.737
239.362
247.037
254.762
262.537
270.359
278.230
286.146
296.106
306.136
316.232
326.393
336.616
346.901
95.634
105.212
114.794
124.383
128.381
129.180
133.980
143.590
153.216
162.860
172.528
182.221
191.944
201.701
211.494
221.327
231.202
241.121
251.086
261.099
271.161
281.273
291.436
301.650
311.915
322.231
332.598
343.016
353.483
364.000
374.565
385.177
395.837
409.224
422.681
436.205
449.794
463.445
477.158
1.56788
1.59071
1.61155
1.63074
1.63831
1.63979
1.64852
1.66510
1.68063
1.69524
1.70906
1.72216
1.73463
1.74653
1.75791
1.76884
1.77935
1.78947
1.79924
1.80868
1.81783
1.82670
1.83532
1.84369
1.85184
1.85977
1.86751
1.87506
1.88243
1.88964
1.89668
1.90357
1.91032
1.91856
1.92659
1.93444
1.94209
1.94957
1.95689
1950
2000
2050
2100
2150
2200
2300
2400
2500
2600
2700
2800
2900
3000
3100
3200
3300
3400
3500
3600
3700
3800
3900
4000
4100
4200
4300
4400
4500
4600
4700
4800
4900
5000
5100
5200
5300
5400
357.243
367.642
378.096
388.602
399.158
409.764
431.114
452.640
474.330
496.175
518.165
540.286
562.532
584.895
607.369
629.948
652.625
675.396
698.257
721.203
744.230
767.334
790.513
813.763
837.081
860.466
883.913
907.422
930.989
954.613
978.292
1002.023
1025.806
1049.638
1073.518
1097.444
1121.414
1145.428
490.928
504.755
518.636
532.570
546.554
560.588
588.793
617.175
645.721
674.421
703.267
732.244
761.345
790.564
819.894
849.328
878.861
908.488
938.204
968.005
997.888
1027.848
1057.882
1087.988
1118.162
1148.402
1178.705
1209.069
1239.492
1269.972
1300.506
1331.093
1361.732
1392.419
1423.155
1453.936
1484.762
1515.632
1.96404
1.97104
1.97790
1.98461
1.99119
1.99765
2.01018
2.02226
2.03391
2.04517
2.05606
2.06659
2.07681
2.08671
2.09633
2.10567
2.11476
2.12361
2.13222
2.14062
2.14880
2.15679
2.16459
2.17221
2.17967
2.18695
2.19408
2.20106
2.20790
2.21460
2.22117
2.22761
2.23392
2.24012
2.24621
2.25219
2.25806
2.26383
⑦
APPENDIX F
..............842
www.elsolucionario.org
ENGLISH UNIT TABLES
.............................................................................................................................
TABLE F.6
Ideal Gas Properties of Various Substances (English Units), Entropies at 1 atm Pressure
Nitrogen, Diatomic (N2 )
0
h̄ f ,537 = 0 Btu/lbmol
M = 28.013 lbm/lbmol
0
Nitrogen, Monatomic (N)
0
h̄ f ,537 = 203 216 Btu/lbmol
M= 14.007 lbm/lbmol
0
T
R
h̄ − h̄537
Btu/lbmol
s̄ 0T
Btu/lbmol R
h̄ − h̄537
Btu/lbmol
s̄ 0T
Btu/lbmol R
0
200
400
537
600
800
1000
1200
1400
1600
1800
2000
2200
2400
2600
2800
3000
3200
3400
3600
3800
4000
4200
4400
4600
4800
5000
5500
6000
6500
7000
7500
8000
8500
9000
9500
10000
−3727
−2341
−950
0
441
1837
3251
4693
6169
7681
9227
10804
12407
14034
15681
17345
19025
20717
22421
24135
25857
27587
29324
31068
32817
34571
36330
40745
45182
49638
54109
58595
63093
67603
72125
96658
81203
0
38.877
43.695
45.739
46.515
48.524
50.100
51.414
52.552
53.561
54.472
55.302
56.066
56.774
57.433
58.049
58.629
59.175
59.691
60.181
60.647
61.090
61.514
61.920
62.308
62.682
63.041
63.882
64.654
65.368
66.030
66.649
67.230
67.777
68.294
68.784
69.250
−2664
−1671
−679
0
314
1307
2300
3293
4286
5279
6272
7265
8258
9251
10244
11237
12230
13223
14216
15209
16202
17195
18189
19183
20178
21174
22171
24670
27186
29724
32294
34903
37559
40270
43040
45875
48777
0
31.689
35.130
36.589
37.143
38.571
39.679
40.584
41.349
42.012
42.597
43.120
43.593
44.025
44.423
44.791
45.133
45.454
45.755
46.038
46.307
46.562
46.804
47.035
47.256
47.468
47.672
48.148
48.586
48.992
49.373
49.733
50.076
50.405
50.721
51.028
51.325
.............................................................................................................................
APPENDIX F
ENGLISH UNIT TABLES
TABLE F.6 (continued )
Ideal Gas Properties of Various Substances (English Units), Entropies at 1 atm Pressure
Oxygen, Diatomic (O2 )
0
h̄ f ,537 = 0 Btu/lbmol
M = 31.999 lbm/lbmol
0
..............
⑦
843
Oxygen, Monatomic (O)
0
h̄ f ,537 = 107 124 Btu/lbmol
M = 16.00 lbm/lbmol
0
T
R
h̄ − h̄537
Btu/lbmol
s̄ 0T
Btu/lbmol R
h̄ − h̄537
Btu/lbmol
s̄ 0T
Btu/lbmol R
0
200
400
537
600
800
1000
1200
1400
1600
1800
2000
2200
2400
2600
2800
3000
3200
3400
3600
3800
4000
4200
4400
4600
4800
5000
5500
6000
6500
7000
7500
8000
8500
9000
9500
10000
−3733
−2345
−955
0
446
1881
3366
4903
6487
8108
9761
11438
13136
14852
16584
18329
20088
21860
23644
25441
27250
29071
30904
32748
34605
36472
38350
43091
47894
52751
57657
62608
67600
72633
77708
82828
87997
0
42.100
46.920
48.973
49.758
51.819
53.475
54.876
56.096
57.179
58.152
59.035
59.844
60.591
61.284
61.930
62.537
63.109
63.650
64.163
64.652
65.119
65.566
65.995
66.408
66.805
67.189
68.092
68.928
69.705
70.433
71.116
71.760
72.370
72.950
73.504
74.034
−2891
−1829
−724
0
330
1358
2374
3383
4387
5389
6389
7387
8385
9381
10378
11373
12369
13364
14359
15354
16349
17344
18339
19334
20330
21327
22325
24823
27329
29847
32378
34924
37485
40063
42658
45270
47897
0
33.041
36.884
38.442
39.023
40.503
41.636
42.556
43.330
43.999
44.588
45.114
45.589
46.023
46.422
46.791
47.134
47.455
47.757
48.041
48.310
48.565
48.808
49.039
49.261
49.473
49.677
50.153
50.589
50.992
51.367
51.718
52.049
52.362
52.658
52.941
53.210
⑦
APPENDIX F
..............844
www.elsolucionario.org
ENGLISH UNIT TABLES
.............................................................................................................................
TABLE F.6 (continued )
Ideal Gas Properties of Various Substances (English Units), Entropies at 1 atm Pressure
Carbon Dioxide (CO2 )
0
h̄ f ,537 = −169 184 Btu/lbmol
M = 44.01 lbm/lbmol
T
R
0
200
400
537
600
800
1000
1200
1400
1600
1800
2000
2200
2400
2600
2800
3000
3200
3400
3600
3800
4000
4200
4400
4600
4800
5000
5500
6000
6500
7000
7500
8000
8500
9000
9500
10000
0
h̄ − h̄537
Btu/lbmol
−4026
−2636
−1153
0
573
2525
4655
6927
9315
11798
14358
16982
19659
22380
25138
27926
30741
33579
36437
39312
42202
45105
48021
50948
53885
56830
59784
67202
74660
82155
89682
97239
104823
112434
120071
127734
135426
Carbon Monoxide (CO)
0
h̄ f ,537 = −47 51 8 Btu/lbmol
M = 28.01 lbm/lbmol
0
s̄ 0T
Btu/lbmol R
h̄ − h̄537
Btu/lbmol
s̄ 0T
Btu/lbmol R
0
43.466
48.565
51.038
52.047
54.848
57.222
59.291
61.131
62.788
64.295
65.677
66.952
68.136
69.239
70.273
71.244
72.160
73.026
73.847
74.629
75.373
76.084
76.765
77.418
78.045
78.648
80.062
81.360
82.560
83.675
84.718
85.697
86.620
87.493
88.321
89.110
−3728
−2343
−951
0
441
1842
3266
4723
6220
7754
9323
10923
12549
14197
15864
17547
19243
20951
22669
24395
26128
27869
29614
31366
33122
34883
36650
41089
45548
50023
54514
59020
63539
68069
72610
77161
81721
0
40.319
45.137
47.182
47.959
49.974
51.562
52.891
54.044
55.068
55.992
56.835
57.609
58.326
58.993
59.616
60.201
60.752
61.273
61.767
62.236
62.683
63.108
63.515
63.905
64.280
64.641
65.487
66.263
66.979
67.645
68.267
68.850
69.399
69.918
70.410
70.878
.............................................................................................................................
APPENDIX F
ENGLISH UNIT TABLES
TABLE F.6 (continued )
Ideal Gas Properties of Various Substances (English Units), Entropies at 1 atm Pressure
Water (H2 O)
0
h̄ f ,537 = −103 966 Btu/lbmol
M = 18.015 lbm/lbmol
T
R
0
200
400
537
600
800
1000
1200
1400
1600
1800
2000
2200
2400
2600
2800
3000
3200
3400
3600
3800
4000
4200
4400
4600
4800
5000
5500
6000
6500
7000
7500
8000
8500
9000
9500
10000
0
h̄ − h̄537
Btu/lbmol
−4528
−2686
−1092
0
509
2142
3824
5566
7371
9241
11178
13183
15254
17388
19582
21832
24132
26479
28867
31293
33756
36251
38774
41325
43899
46496
49114
55739
62463
69270
76146
83081
90069
97101
104176
111289
118440
..............
⑦
845
Hydroxyl (OH)
0
h̄ f ,537 = 16 761 Btu/lbmol
M = 17.007 lbm/lbmol
0
s̄ 0T
Btu/lbmol R
h̄ − h̄537
Btu/lbmol
s̄ 0T
Btu/lbmol R
0
37.209
42.728
45.076
45.973
48.320
50.197
51.784
53.174
54.422
55.563
56.619
57.605
58.533
59.411
60.245
61.038
61.796
62.520
63.213
63.878
64.518
65.134
65.727
66.299
66.852
67.386
68.649
69.819
70.908
71.927
72.884
73.786
74.639
75.448
76.217
76.950
−3943
−2484
−986
0
452
1870
3280
4692
6112
7547
9001
10477
11978
13504
15054
16627
18220
19834
21466
23114
24777
26455
28145
29849
31563
33287
35021
39393
43812
48272
52767
57294
61851
66434
71043
75677
80335
0
36.521
41.729
43.852
44.649
46.689
48.263
49.549
50.643
51.601
52.457
53.235
53.950
54.614
55.235
55.817
56.367
56.887
57.382
57.853
58.303
58.733
59.145
59.542
59.922
60.289
60.643
61.477
62.246
62.959
63.626
64.250
64.838
65.394
65.921
66.422
66.900
⑦
APPENDIX F
..............846
www.elsolucionario.org
ENGLISH UNIT TABLES
.............................................................................................................................
TABLE F.6 (continued )
Ideal Gas Properties of Various Substances (English Units), Entropies at 1 atm Pressure
Hydrogen (H2 )
0
h̄ f ,537 = 0 Btu/lbmol
M = 2.016 lbm/lbmol
0
Hydrogen, Monatomic (H)
0
h̄ f ,537 = 93 723 Btu/lbmol
M = 1.008 lbm/lbmol
0
T
R
h̄ − h̄537
Btu/lbmol
s̄ 0T
Btu/lbmol R
h̄ − h̄537
Btu/lbmol
s̄ 0T
Btu/lbmol R
0
200
400
537
600
800
1000
1200
1400
1600
1800
2000
2200
2400
2600
2800
3000
3200
3400
3600
3800
4000
4200
4400
4600
4800
5000
5500
6000
6500
7000
7500
8000
8500
9000
9500
10000
−3640
−2224
−927
0
438
1831
3225
4622
6029
7448
8884
10337
11812
13309
14829
16372
17938
19525
21133
22761
24407
26071
27752
29449
31161
32887
34627
39032
43513
48062
52678
57356
62094
66889
71738
76638
81581
0
24.703
29.193
31.186
31.957
33.960
35.519
36.797
37.883
38.831
39.676
40.441
41.143
41.794
42.401
42.973
43.512
44.024
44.512
44.977
45.422
45.849
46.260
46.655
47.035
47.403
47.758
48.598
49.378
50.105
50.789
51.434
52.045
52.627
53.182
53.712
54.220
−2664
−1672
−679
0
314
1307
2300
3293
4286
5279
6272
7265
8258
9251
10244
11237
12230
13223
14215
15208
16201
17194
18187
19180
20173
21166
22159
24641
27124
29606
32088
34571
37053
39535
42018
44500
46982
0
22.473
25.914
27.373
27.927
29.355
30.463
31.368
32.134
32.797
33.381
33.905
34.378
34.810
35.207
35.575
35.917
36.238
36.539
36.823
37.091
37.346
37.588
37.819
38.040
38.251
38.454
38.927
39.359
39.756
40.124
40.467
40.787
41.088
41.372
41.640
41.895
.............................................................................................................................
APPENDIX F
ENGLISH UNIT TABLES
TABLE F.6 (continued )
Ideal Gas Properties of Various Substances (English Units), Entropies at 1 atm Pressure
Nitric Oxide (NO)
0
h̄ f ,537 = 38 818 Btu/lbmol
M = 30.006 lbm/lbmol
0
..............
⑦
847
Nitrogen Dioxide (NO2 )
0
h̄ f ,537 = 14 230 Btu/lbmol
M = 46.005 lbm/lbmol
0
T
R
h̄ − h̄537
Btu/lbmol
s̄ 0T
Btu/lbmol R
h̄ − h̄537
Btu/lbmol
s̄ 0T
Btu/lbmol R
0
200
400
537
600
800
1000
1200
1400
1600
1800
2000
2200
2400
2600
2800
3000
3200
3400
3600
3800
4000
4200
4400
4600
4800
5000
5500
6000
6500
7000
7500
8000
8500
9000
9500
10000
−3952
−2457
−979
0
451
1881
3338
4834
6372
7948
9557
11193
12853
14532
16228
17937
19657
21388
23128
24875
26629
28389
30154
31924
33698
35476
37258
41726
46212
50714
55229
59756
64294
68842
73401
77968
82544
0
43.066
48.207
50.313
51.107
53.163
54.788
56.152
57.337
58.389
59.336
60.198
60.989
61.719
62.397
63.031
63.624
64.183
64.710
65.209
65.684
66.135
66.565
66.977
67.371
67.750
68.113
68.965
69.746
70.467
71.136
71.760
72.346
72.898
73.419
73.913
74.382
−4379
−2791
−1172
0
567
2469
4532
6733
9044
11442
13905
16421
18978
21567
24182
26819
29473
32142
34823
37515
40215
42923
45637
48358
51083
53813
56546
63395
70260
77138
84026
90923
97826
104735
111648
118565
125485
0
49.193
54.789
57.305
58.304
61.034
63.333
65.337
67.118
68.718
70.168
71.493
72.712
73.838
74.885
75.861
76.777
77.638
78.451
79.220
79.950
80.645
81.307
81.940
82.545
83.126
83.684
84.990
86.184
87.285
88.306
89.258
90.149
90.986
91.777
92.525
93.235
⑦
APPENDIX F
..............848
www.elsolucionario.org
ENGLISH UNIT TABLES
.............................................................................................................................
TABLE F.7
Thermodynamic Properties of Water
TABLE F.7.1
Saturated Water
Specific Volume, ft3 /lbm
Internal Energy, Btu/lbm
Temp.
(F)
Press.
(psia)
Sat. Liquid
vf
Evap.
v fg
Sat. Vapor
vg
Sat. Liquid
uf
Evap.
ufg
Sat. Vapor
ug
32
35
40
45
50
60
70
80
90
100
110
120
130
140
150
160
170
180
190
200
210
212.0
220
230
240
250
260
270
280
290
300
310
320
330
340
350
0.0887
0.100
0.122
0.147
0.178
0.256
0.363
0.507
0.699
0.950
1.276
1.695
2.225
2.892
3.722
4.745
5.997
7.515
9.344
11.530
14.126
14.696
17.189
20.781
24.968
29.823
35.422
41.848
49.189
57.535
66.985
77.641
89.609
103.00
117.94
134.54
0.01602
0.01602
0.01602
0.01602
0.01602
0.01603
0.01605
0.01607
0.01610
0.01613
0.01617
0.01620
0.01625
0.01629
0.01634
0.01639
0.01645
0.01651
0.01657
0.01663
0.01670
0.01672
0.01677
0.01685
0.01692
0.01700
0.01708
0.01717
0.01726
0.01735
0.01745
0.01755
0.01765
0.01776
0.01787
0.01799
3301.6545
2947.5021
2445.0713
2036.9527
1703.9867
1206.7283
867.5791
632.6739
467.5865
349.9602
265.0548
203.0105
157.1419
122.8567
96.9611
77.2079
61.9983
50.1826
40.9255
33.6146
27.7964
26.7864
23.1325
19.3677
16.3088
13.8077
11.7503
10.0483
8.6325
7.4486
6.4537
5.6136
4.9010
4.2938
3.7742
3.3279
3301.6705
2947.5181
2445.0873
2036.9687
1704.0027
1206.7443
867.5952
632.6900
467.6026
349.9764
265.0709
203.0267
157.1582
122.8730
96.9774
77.2243
62.0148
50.1991
40.9421
33.6312
27.8131
26.8032
23.1492
19.3846
16.3257
13.8247
11.7674
10.0655
8.6498
7.4660
6.4712
5.6312
4.9186
4.3115
3.7921
3.3459
0
2.99
8.01
13.03
18.05
28.08
38.09
48.08
58.06
68.04
78.01
87.99
97.96
107.95
117.94
127.94
137.94
147.96
157.99
168.03
178.09
180.09
188.16
198.25
208.36
218.48
228.64
238.81
249.02
259.25
269.51
279.80
290.13
300.50
310.90
321.35
1021.21
1019.20
1015.84
1012.47
1009.10
1002.36
995.64
988.91
982.18
975.43
968.67
961.88
955.07
948.21
941.32
934.39
927.41
920.38
913.29
906.15
898.95
897.51
891.68
884.33
876.91
869.41
861.82
854.14
846.35
838.46
830.45
822.32
814.07
805.68
797.14
788.45
1021.21
1022.19
1023.85
1025.50
1027.15
1030.44
1033.72
1036.99
1040.24
1043.47
1046.68
1049.87
1053.03
1056.16
1059.26
1062.32
1065.35
1068.34
1071.29
1074.18
1077.04
1077.60
1079.84
1082.58
1085.27
1087.90
1090.46
1092.95
1095.37
1097.71
1099.96
1102.13
1104.20
1106.17
1108.04
1109.80
.............................................................................................................................
APPENDIX F
ENGLISH UNIT TABLES
TABLE F.7.1 (continued )
..............
⑦
849
Saturated Water
Enthalpy, Btu/lbm
Entropy, Btu/lbm R
Temp.
(F)
Press.
(psia)
Sat. Liquid
hf
Evap.
h fg
Sat. Vapor
hg
Sat. Liquid
sf
Evap.
s fg
Sat. Vapor
sg
32
35
40
45
50
60
70
80
90
100
110
120
130
140
150
160
170
180
190
200
210
212
220
230
240
250
260
270
280
290
300
310
320
330
340
350
0.0887
0.100
0.122
0.147
0.178
0.256
0.363
0.507
0.699
0.950
1.276
1.695
2.225
2.892
3.722
4.745
5.997
7.515
9.344
11.530
14.126
14.696
17.189
20.781
24.968
29.823
35.422
41.848
49.189
57.535
66.985
77.641
89.609
103.00
117.94
134.54
0
2.99
8.01
13.03
18.05
28.08
38.09
48.08
58.06
68.04
78.01
87.99
97.97
107.96
117.95
127.95
137.96
147.98
158.02
168.07
178.13
180.13
188.21
198.31
208.43
218.58
228.75
238.95
249.17
259.43
269.73
280.06
290.43
300.84
311.29
321.80
1075.38
1073.71
1070.89
1068.06
1065.24
1059.59
1053.95
1048.31
1042.65
1036.98
1031.28
1025.55
1019.78
1013.96
1008.10
1002.18
996.21
990.17
984.06
977.87
971.61
970.35
965.26
958.81
952.27
945.61
938.84
931.95
924.93
917.76
910.45
902.98
895.34
887.52
879.51
871.30
1075.39
1076.70
1078.90
1081.10
1083.29
1087.67
1092.04
1096.39
1100.72
1105.02
1109.29
1113.54
1117.75
1121.92
1126.05
1130.14
1134.17
1138.15
1142.08
1145.94
1149.74
1150.49
1153.47
1157.12
1160.70
1164.19
1167.59
1170.90
1174.10
1177.19
1180.18
1183.03
1185.76
1188.36
1190.80
1193.10
0
0.0061
0.0162
0.0262
0.0361
0.0555
0.0746
0.0933
0.1116
0.1296
0.1473
0.1646
0.1817
0.1985
0.2150
0.2313
0.2473
0.2631
0.2786
0.2940
0.3091
0.3121
0.3240
0.3388
0.3533
0.3677
0.3819
0.3960
0.4098
0.4236
0.4372
0.4507
0.4640
0.4772
0.4903
0.5033
2.1869
2.1703
2.1430
2.1161
2.0898
2.0388
1.9896
1.9423
1.8966
1.8526
1.8101
1.7690
1.7292
1.6907
1.6533
1.6171
1.5819
1.5478
1.5146
1.4822
1.4507
1.4446
1.4201
1.3901
1.3609
1.3324
1.3044
1.2771
1.2504
1.2241
1.1984
1.1731
1.1483
1.1238
1.0997
1.0760
2.1869
2.1764
2.1591
2.1423
2.1259
2.0943
2.0642
2.0356
2.0083
1.9822
1.9574
1.9336
1.9109
1.8892
1.8683
1.8484
1.8292
1.8109
1.7932
1.7762
1.7599
1.7567
1.7441
1.7289
1.7142
1.7001
1.6864
1.6731
1.6602
1.6477
1.6356
1.6238
1.6122
1.6010
1.5900
1.5793
⑦
APPENDIX F
..............850
www.elsolucionario.org
ENGLISH UNIT TABLES
.............................................................................................................................
TABLE F.7.1 (continued )
Saturated Water
Specific Volume, ft3 /lbm
Internal Energy, Btu/lbm
Temp.
(F)
Press.
(psia)
Sat. Liquid
vf
Evap.
v fg
Sat. Vapor
vg
Sat. Liquid
uf
Evap.
u fg
Sat. Vapor
ug
360
370
380
390
400
410
420
430
440
450
460
470
480
490
500
510
520
530
540
550
560
570
580
590
600
610
620
630
640
650
660
670
680
690
700
705.4
152.93
173.24
195.61
220.17
347.08
276.48
308.52
343.37
381.18
422.13
466.38
514.11
565.50
620.74
680.02
743.53
811.48
884.07
961.51
1044.02
1131.85
1225.21
1324.37
1429.58
1541.13
1659.32
1784.48
1916.96
2057.17
2205.54
2362.59
2528.88
2705.09
2891.99
3090.47
3203.79
0.01811
0.01823
0.01836
0.01850
0.01864
0.01878
0.01894
0.01909
0.01926
0.01943
0.01961
0.01980
0.02000
0.02021
0.02043
0.02066
0.02091
0.02117
0.02145
0.02175
0.02207
0.02241
0.02278
0.02318
0.02362
0.02411
0.02465
0.02525
0.02593
0.02673
0.02766
0.02882
0.03031
0.03248
0.03665
0.05053
2.9430
2.6098
2.3203
2.0680
1.8474
1.6537
1.4833
1.3329
1.1998
1.0816
0.9764
0.8826
0.7986
0.7233
0.6556
0.5946
0.5395
0.4896
0.4443
0.4031
0.3656
0.3312
0.2997
0.2707
0.2440
0.2193
0.1963
0.1747
0.1545
0.1353
0.1169
0.0990
0.0809
0.0618
0.0377
0
2.9611
2.6280
2.3387
2.0865
1.8660
1.6725
1.5023
1.3520
1.2191
1.1011
0.9961
0.9024
0.8186
0.7435
0.6761
0.6153
0.5604
0.5108
0.4658
0.4249
0.3876
0.3536
0.3225
0.2939
0.2676
0.2434
0.2209
0.2000
0.1804
0.1620
0.1446
0.1278
0.1112
0.0943
0.0743
0.0505
331.83
342.37
352.95
363.58
374.26
385.00
395.80
406.67
417.61
428.63
439.73
450.92
462.21
473.60
485.11
496.75
508.53
520.46
532.56
544.85
557.35
570.07
583.05
596.31
609.91
623.87
638.26
653.17
668.68
684.96
702.24
720.91
741.70
766.34
801.66
872.56
779.60
770.57
761.37
751.97
742.37
732.56
722.52
712.24
701.71
690.90
679.82
668.43
656.72
644.67
632.26
619.46
606.23
592.56
578.39
563.69
548.42
532.50
515.87
498.44
480.11
460.76
440.20
418.22
394.52
368.66
340.02
307.52
269.26
220.82
145.92
0
1111.43
1112.94
1114.31
1115.55
1116.63
1117.56
1118.32
1118.91
1119.32
1119.53
1119.55
1119.35
1118.93
1118.28
1117.37
1116.21
1114.76
1113.02
1110.95
1108.54
1105.76
1102.56
1098.91
1094.76
1090.02
1084.63
1078.46
1071.38
1063.20
1053.63
1042.26
1028.43
1010.95
987.16
947.57
872.56
.............................................................................................................................
APPENDIX F
ENGLISH UNIT TABLES
TABLE F.7.1 (continued )
..............
⑦
851
Saturated Water
Enthalpy, Btu/lbm
Entropy, Btu/lbm R
Temp.
(F)
Press.
(psia)
Sat. Liquid
hf
Evap.
h fg
Sat. Vapor
hg
Sat. Liquid
sf
Evap.
sfg
Sat. Vapor
sg
360
370
380
390
400
410
420
430
440
450
460
470
480
490
500
510
520
530
540
550
560
570
580
590
600
610
620
630
640
650
660
670
680
690
700
705.4
152.93
173.24
195.61
220.17
247.08
276.48
308.52
343.37
381.18
422.13
466.38
514.11
565.50
620.74
680.02
743.53
811.48
884.07
961.51
1044.02
1131.85
1225.21
1324.37
1429.58
1541.13
1659.32
1784.48
1916.96
2057.17
2205.54
2362.59
2528.88
2705.09
2891.99
3090.47
3203.79
332.35
342.95
353.61
364.33
375.11
385.96
396.89
407.89
418.97
430.15
441.42
452.80
464.30
475.92
487.68
499.59
511.67
523.93
536.38
549.05
561.97
575.15
588.63
602.45
616.64
631.27
646.40
662.12
678.55
695.87
714.34
734.39
756.87
783.72
822.61
902.52
862.88
854.24
845.36
836.23
826.84
817.17
807.20
796.93
786.34
775.40
764.09
752.40
740.30
727.76
714.76
701.27
687.25
672.66
657.45
641.58
624.98
607.59
589.32
570.06
549.71
528.08
505.00
480.21
453.33
423.89
391.13
353.83
309.77
253.88
167.47
0
1195.23
1197.19
1198.97
1200.56
1201.95
1203.13
1204.09
1204.82
1205.31
1205.54
1205.51
1205.20
1204.60
1203.68
1202.44
1200.86
1198.92
1196.58
1193.83
1190.63
1186.95
1182.74
1177.95
1172.51
1166.35
1159.36
1151.41
1142.33
1131.89
1119.76
1105.47
1088.23
1066.64
1037.60
990.09
902.52
0.5162
0.5289
0.5416
0.5542
0.5667
0.5791
0.5915
0.6038
0.6160
0.6282
0.6404
0.6525
0.6646
0.6767
0.6888
0.7009
0.7130
0.7251
0.7374
0.7496
0.7620
0.7745
0.7871
0.7999
0.8129
0.8262
0.8397
0.8537
0.8681
0.8831
0.8990
0.9160
0.9350
0.9575
0.9901
1.0580
1.0526
1.0295
1.0067
0.9841
0.9617
0.9395
0.9175
0.8957
0.8740
0.8523
0.8308
0.8093
0.7878
0.7663
0.7447
0.7232
0.7015
0.6796
0.6576
0.6354
0.6129
0.5901
0.5668
0.5431
0.5187
0.4937
0.4677
0.4407
0.4122
0.3820
0.3493
0.3132
0.2718
0.2208
0.1444
0
1.5688
1.5584
1.5483
1.5383
1.5284
1.5187
1.5090
1.4995
1.4900
1.4805
1.4711
1.4618
1.4524
1.4430
1.4335
1.4240
1.4144
1.4048
1.3950
1.3850
1.3749
1.3646
1.3539
1.3430
1.3317
1.3199
1.3075
1.2943
1.2803
1.2651
1.2483
1.2292
1.2068
1.1783
1.1345
1.0580
⑦
APPENDIX F
..............852
www.elsolucionario.org
ENGLISH UNIT TABLES
.............................................................................................................................
TABLE F.7.2
Superheated Vapor Water
Temp.
(F)
v
(ft3 /lbm)
u
(Btu/lbm)
h
(Btu/lbm)
s
(Btu/lbm R)
v
(ft3 /lbm)
1 psia (101.70 F)
Sat.
200
240
280
320
360
400
440
500
600
700
800
900
1000
1100
1200
1300
1400
333.58
392.51
416.42
440.32
464.19
488.05
511.91
535.76
571.53
631.13
690.72
750.30
809.88
869.45
929.03
988.60
1048.17
1107.74
1044.02
1077.49
1091.22
1105.02
1118.92
1132.92
1147.02
1161.23
1182.77
1219.30
1256.65
1294.86
1333.94
1373.93
1414.83
1456.67
1499.43
1543.13
1105.75
1150.12
1168.28
1186.50
1204.82
1223.23
1241.75
1260.37
1288.53
1336.09
1384.47
1433.70
1483.81
1534.82
1586.75
1639.61
1693.40
1748.12
38.424
38.848
41.320
43.768
46.200
48.620
51.032
53.438
57.039
63.027
69.006
74.978
80.946
86.912
92.875
98.837
104.798
110.759
116.718
122.678
1072.21
1074.67
1089.03
1103.31
1117.56
1131.81
1146.10
1160.46
1182.16
1218.85
1256.30
1294.58
1333.72
1373.74
1414.68
1456.53
1499.32
1543.03
1587.67
1633.24
1143.32
1146.56
1165.50
1184.31
1203.05
1221.78
1240.53
1259.34
1287.71
1335.48
1384.00
1433.32
1483.51
1534.57
1586.54
1639.43
1693.25
1747.99
1803.66
1860.25
h
(Btu/lbm)
s
(Btu/lbm R)
5 psia (162.20 F)
1.9779
2.0507
2.0775
2.1028
2.1269
2.1499
2.1720
2.1932
2.2235
2.2706
2.3142
2.3549
2.3932
2.4294
2.4638
2.4967
2.5281
2.5584
73.531
78.147
83.001
87.831
92.645
97.447
102.24
107.03
114.21
126.15
138.08
150.01
161.94
173.86
185.78
197.70
209.62
221.53
10 psia (193.19 F)
Sat.
200
240
280
320
360
400
440
500
600
700
800
900
1000
1100
1200
1300
1400
1500
1600
u
(Btu/lbm)
1062.99
1076.25
1090.25
1104.27
1118.32
1132.42
1146.61
1160.89
1182.50
1219.10
1256.50
1294.73
1333.84
1373.85
1414.77
1456.61
1499.38
1543.09
1131.03
1148.55
1167.05
1185.53
1204.04
1222.59
1241.21
1259.92
1288.17
1335.82
1384.26
1433.53
1483.68
1534.71
1586.66
1639.53
1693.33
1748.06
1.8441
1.8715
1.8987
1.9244
1.9487
1.9719
1.9941
2.0154
2.0458
2.0930
2.1367
2.1774
2.2157
2.2520
2.2864
2.3192
2.3507
2.3809
14.696 psia (211.99 F)
1.7877
1.7927
1.8205
1.8467
1.8713
1.8948
1.9171
1.9385
1.9690
2.0164
2.0601
2.1009
2.1392
2.1755
2.2099
2.2428
2.2743
2.3045
2.3337
2.3618
26.803
—
27.999
29.687
31.359
33.018
34.668
36.313
38.772
42.857
46.932
51.001
55.066
59.128
63.188
67.247
71.304
75.361
79.417
83.473
1077.60
—
1087.87
1102.40
1116.83
1131.22
1145.62
1160.05
1181.83
1218.61
1256.12
1294.43
1333.60
1373.65
1414.60
1456.47
1499.26
1542.98
1587.63
1633.20
1150.49
—
1164.02
1183.14
1202.11
1221.01
1239.90
1258.80
1287.27
1335.16
1383.75
1433.13
1483.35
1534.44
1586.44
1639.34
1693.17
1747.92
1803.60
1860.20
1.7567
—
1.7764
1.8030
1.8280
1.8516
1.8741
1.8956
1.9262
1.9737
2.0175
2.0584
2.0967
2.1330
2.1674
2.2003
2.2318
2.2620
2.2912
2.3194
.............................................................................................................................
APPENDIX F
ENGLISH UNIT TABLES
u
(Btu/lbm)
h
(Btu/lbm)
TABLE F.7.2 (continued )
..............
⑦
853
Superheated Vapor Water
Temp.
(F)
v
(ft3 /lbm)
u
(Btu/lbm)
h
(Btu/lbm)
s
(Btu/lbm R)
v
(ft3 /lbm)
20 psia (227.96 F)
Sat.
240
280
320
360
400
440
500
600
700
800
900
1000
1100
1200
1300
1400
1500
1600
20.091
20.475
21.734
22.976
24.206
25.427
26.642
28.456
31.466
34.466
37.460
40.450
43.437
46.422
49.406
52.389
55.371
58.352
61.333
1082.02
1086.54
1101.36
1116.01
1130.55
1145.06
1159.59
1181.46
1218.35
1255.91
1294.27
1333.47
1373.54
1414.51
1456.39
1499.19
1542.92
1587.58
1633.15
1156.38
1162.32
1181.80
1201.04
1220.14
1239.17
1258.19
1286.78
1334.80
1383.47
1432.91
1483.17
1534.30
1586.32
1639.24
1693.08
1747.85
1803.54
1860.14
40 psia (267.26 F)
1.7320
1.7405
1.7676
1.7929
1.8168
1.8395
1.8611
1.8919
1.9395
1.9834
2.0243
2.0626
2.0989
2.1334
2.1663
2.1978
2.2280
2.2572
2.2854
10.501
—
10.711
11.360
11.996
12.623
13.243
14.164
15.685
17.196
18.701
20.202
21.700
23.196
24.690
26.184
27.677
29.169
30.660
60 psia (292.73 F)
Sat.
320
360
400
440
500
600
700
800
900
1000
1100
1200
1300
1400
1500
1600
1800
2000
7.177
7.485
7.924
8.353
8.775
9.399
10.425
11.440
12.448
13.452
14.454
15.454
16.452
17.449
18.445
19.441
20.436
22.426
24.415
1098.33
1109.46
1125.31
1140.77
1156.01
1178.64
1216.31
1254.35
1293.03
1332.46
1372.71
1413.81
1455.80
1498.69
1542.48
1587.18
1632.79
1726.69
1824.02
1178.02
1192.56
1213.29
1233.52
1253.44
1283.00
1332.06
1381.37
1431.24
1481.82
1533.19
1585.39
1638.46
1692.42
1747.28
1803.04
1859.70
1975.69
2095.10
s
(Btu/lbm R)
1092.27
—
1097.31
1112.81
1127.98
1142.95
1157.82
1180.06
1217.33
1255.14
1293.65
1332.96
1373.12
1414.16
1456.09
1498.94
1542.70
1587.38
1632.97
1170.00
—
1176.59
1196.90
1216.77
1236.38
1255.84
1284.91
1333.43
1382.42
1432.08
1482.50
1533.74
1585.86
1638.85
1692.75
1747.56
1803.29
1859.92
1.6767
—
1.6857
1.7124
1.7373
1.7606
1.7827
1.8140
1.8621
1.9063
1.9474
1.9859
2.0222
2.0568
2.0897
2.1212
2.1515
2.1807
2.2089
80 psia (312.06 F)
1.6444
1.6633
1.6893
1.7134
1.7360
1.7678
1.8165
1.8609
1.9022
1.9408
1.9773
2.0119
2.0448
2.0764
2.1067
2.1359
2.1641
2.2178
2.2685
5.474
5.544
5.886
6.217
6.541
7.017
7.794
8.561
9.322
10.078
10.831
11.583
12.333
13.082
13.830
14.577
15.324
16.818
18.310
1102.56
1105.95
1122.53
1138.53
1154.15
1177.19
1215.28
1253.57
1292.41
1331.95
1372.29
1413.46
1455.51
1498.43
1542.26
1586.99
1632.62
1726.54
1823.88
1183.61
1188.02
1209.67
1230.56
1250.98
1281.07
1330.66
1380.31
1430.40
1481.14
1532.63
1584.93
1638.08
1692.09
1746.99
1802.79
1859.48
1975.50
2094.94
1.6214
1.6270
1.6541
1.6790
1.7022
1.7346
1.7838
1.8285
1.8700
1.9087
1.9453
1.9799
2.0129
2.0445
2.0749
2.1041
2.1323
2.1861
2.2367
⑦
APPENDIX F
..............854
www.elsolucionario.org
ENGLISH UNIT TABLES
.............................................................................................................................
TABLE F.7.2 (continued )
Superheated Vapor Water
Temp.
(F)
v
(ft3 /lbm)
u
(Btu/lbm)
h
(Btu/lbm)
s
(Btu/lbm R)
v
(ft3 /lbm)
100 psia (327.85 F)
Sat.
350
400
450
500
550
600
700
800
900
1000
1100
1200
1300
1400
1500
1600
1800
2000
4.4340
4.5917
4.9344
5.2646
5.5866
5.9032
6.2160
6.8340
7.4455
8.0528
8.6574
9.2599
9.8610
10.4610
11.0602
11.6588
12.2570
13.4525
14.6472
1105.76
1115.39
1136.21
1156.20
1175.72
1195.02
1214.23
1252.78
1291.78
1331.45
1371.87
1413.12
1455.21
1498.18
1542.04
1586.79
1632.44
1726.38
1823.74
1187.81
1200.36
1227.53
1253.62
1279.10
1304.25
1329.26
1379.24
1429.56
1480.47
1532.08
1584.47
1637.69
1691.76
1746.71
1802.54
1859.25
1975.32
2094.78
2.2892
2.3609
2.5477
2.7238
2.8932
3.0580
3.3792
3.6932
4.0029
4.3097
4.6145
4.9178
5.2200
5.5214
5.8222
6.1225
6.7223
7.3214
1114.55
1123.45
1146.44
1167.96
1188.65
1208.87
1248.76
1288.62
1328.90
1369.77
1411.36
1453.73
1496.91
1540.93
1585.81
1631.55
1725.62
1823.02
1199.28
1210.83
1240.73
1268.77
1295.72
1322.05
1373.82
1425.31
1477.04
1529.28
1582.15
1635.74
1690.10
1745.28
1801.29
1858.15
1974.41
2093.99
h
(Btu/lbm)
s
(Btu/lbm R)
150 psia (358.47 F)
1.6034
1.6191
1.6517
1.6812
1.7085
1.7340
1.7582
1.8033
1.8449
1.8838
1.9204
1.9551
1.9882
2.0198
2.0502
2.0794
2.1076
2.1614
2.2120
3.0163
—
3.2212
3.4547
3.6789
3.8970
4.1110
4.5309
4.9441
5.3529
5.7590
6.1630
6.5655
6.9670
7.3677
7.7677
8.1673
8.9657
9.7633
200 psia (381.86 F)
Sat.
400
450
500
550
600
700
800
900
1000
1100
1200
1300
1400
1500
1600
1800
2000
u
(Btu/lbm)
1111.19
—
1130.10
1151.47
1171.93
1191.88
1211.58
1250.78
1290.21
1330.18
1370.83
1412.24
1454.47
1497.55
1541.49
1586.30
1632.00
1726.00
1823.38
1194.91
—
1219.51
1247.36
1274.04
1300.05
1325.69
1376.55
1427.44
1478.76
1530.68
1583.31
1636.71
1690.93
1745.99
1801.91
1858.70
1974.86
2094.38
1.5704
—
1.5997
1.6312
1.6598
1.6862
1.7110
1.7568
1.7989
1.8381
1.8750
1.9098
1.9430
1.9747
2.0052
2.0345
2.0627
2.1165
2.1672
300 psia (417.42 F)
1.5464
1.5600
1.5938
1.6238
1.6512
1.6767
1.7234
1.7659
1.8055
1.8425
1.8776
1.9109
1.9427
1.9732
2.0025
2.0308
2.0847
2.1354
1.5441
—
1.6361
1.7662
1.8878
2.0041
2.2269
2.4421
2.6528
2.8604
3.0660
3.2700
3.4730
3.6751
3.8767
4.0777
4.4790
4.8794
1118.14
—
1135.37
1159.47
1181.85
1203.24
1244.63
1285.41
1326.31
1367.65
1409.60
1452.24
1495.63
1539.82
1584.82
1630.66
1724.85
1822.32
1203.86
—
1226.20
1257.52
1286.65
1314.50
1368.26
1420.99
1473.58
1526.45
1579.80
1633.77
1688.43
1743.84
1800.03
1857.04
1973.50
2093.20
1.5115
—
1.5365
1.5701
1.5997
1.6266
1.6751
1.7187
1.7589
1.7964
1.8317
1.8653
1.8972
1.9279
1.9573
1.9857
2.0396
2.0904
.............................................................................................................................
APPENDIX F
ENGLISH UNIT TABLES
u
(Btu/lbm)
h
(Btu/lbm)
TABLE F.7.2 (continued )
..............
⑦
855
Superheated Vapor Water
Temp.
(F)
v
(ft3 /lbm)
u
(Btu/lbm)
h
(Btu/lbm)
s
(Btu/lbm R)
v
(ft3 /lbm)
400 psia (444.69 F)
Sat.
450
500
550
600
700
800
900
1000
1100
1200
1300
1400
1500
1600
1700
1800
2000
1.1619
1.1745
1.2843
1.3834
1.4760
1.6503
1.8163
1.9776
2.1357
2.2917
2.4462
2.5995
2.7520
2.9039
3.0553
3.2064
3.3573
3.6585
1119.44
1122.63
1150.11
1174.56
1197.33
1240.38
1282.14
1323.69
1365.51
1407.81
1450.73
1494.34
1538.70
1583.83
1629.77
1676.52
1724.08
1821.61
1205.45
1209.57
1245.17
1276.95
1306.58
1362.54
1416.59
1470.07
1523.59
1577.44
1631.79
1686.76
1742.40
1798.78
1855.93
1913.86
1972.59
2092.41
600 psia (486.33 F)
1.4856
1.4901
1.5282
1.5605
1.5892
1.6396
1.6844
1.7252
1.7632
1.7989
1.8327
1.8648
1.8956
1.9251
1.9535
1.9810
2.0076
2.0584
0.7702
—
0.7947
0.8749
0.9456
1.0728
1.1900
1.3021
1.4108
1.5173
1.6222
1.7260
1.8289
1.9312
2.0330
2.1345
2.2357
2.4375
800 psia (518.36 F)
Sat.
550
600
650
700
800
900
1000
1100
1200
1300
1400
1500
1600
1700
1800
2000
0.5691
0.6154
0.6776
0.7324
0.7829
0.8764
0.9640
1.0482
1.1300
1.2102
1.2892
1.3674
1.4448
1.5218
1.5985
1.6749
1.8271
1115.02
1138.83
1170.10
1197.22
1222.08
1268.45
1312.88
1356.71
1400.52
1444.60
1489.11
1534.17
1579.85
1626.19
1673.25
1721.03
1818.80
1199.26
1229.93
1270.41
1305.64
1337.98
1398.19
1455.60
1511.88
1567.81
1623.76
1679.97
1736.59
1793.74
1851.49
1909.89
1968.98
2089.28
s
(Btu/lbm R)
1118.54
—
1127.97
1158.23
1184.50
1231.51
1275.42
1318.36
1361.15
1404.20
1447.68
1491.74
1536.44
1581.84
1627.98
1674.88
1722.55
1820.20
1204.06
—
1216.21
1255.36
1289.49
1350.62
1407.55
1462.92
1517.79
1572.66
1627.80
1683.38
1739.51
1796.26
1853.71
1911.87
1970.78
2090.84
1.4464
—
1.4592
1.4990
1.5320
1.5871
1.6343
1.6766
1.7155
1.7519
1.7861
1.8186
1.8497
1.8794
1.9080
1.9355
1.9622
2.0131
1000 psia (544.74 F)
1.4160
1.4469
1.4861
1.5186
1.5471
1.5969
1.6408
1.6807
1.7178
1.7525
1.7854
1.8167
1.8467
1.8754
1.9031
1.9298
1.9808
0.4459
0.4534
0.5140
0.5637
0.6080
0.6878
0.7610
0.8305
0.8976
0.9630
1.0272
1.0905
1.1531
1.2152
1.2769
1.3384
1.4608
1109.86
1114.77
1153.66
1184.74
1212.03
1261.21
1307.26
1352.17
1396.77
1441.46
1486.45
1531.88
1577.84
1624.40
1671.61
1719.51
1817.41
1192.37
1198.67
1248.76
1289.06
1324.54
1388.49
1448.08
1505.86
1562.88
1619.67
1676.53
1733.67
1791.21
1849.27
1907.91
1967.18
2087.74
1.3903
1.3965
1.4450
1.4822
1.5135
1.5664
1.6120
1.6530
1.6908
1.7260
1.7593
1.7909
1.8210
1.8499
1.8777
1.9046
1.9557
⑦
APPENDIX F
..............856
www.elsolucionario.org
ENGLISH UNIT TABLES
.............................................................................................................................
TABLE F.7.2 (continued )
Superheated Vapor Water
Temp.
(F)
v
(ft3 /lbm)
u
(Btu/lbm)
h
(Btu/lbm)
s
(Btu/lbm R)
v
(ft3 /lbm)
1500 psia (596.38 F)
Sat.
650
700
750
800
850
900
1000
1100
1200
1300
1400
1500
1600
1700
1800
1900
2000
0.2769
0.3329
0.3716
0.4049
0.4350
0.4631
0.4897
0.5400
0.5876
0.6334
0.6778
0.7213
0.7641
0.8064
0.8482
0.8899
0.9313
0.9725
1091.81
1146.95
1183.44
1214.13
1241.79
1267.69
1292.53
1340.43
1387.16
1433.45
1479.68
1526.06
1572.77
1619.90
1667.53
1715.73
1764.53
1813.97
1168.67
1239.34
1286.60
1326.52
1362.53
1396.23
1428.46
1490.32
1550.26
1609.25
1667.82
1726.28
1784.86
1843.72
1902.98
1962.73
2023.03
2083.91
u
(Btu/lbm)
0.02447
0.02867
0.06332
0.10523
0.12833
0.14623
0.16152
0.17520
0.19954
0.22129
0.24137
0.26029
0.27837
0.29586
0.31291
0.32964
0.34616
0.36251
657.71
742.13
960.69
1095.04
1156.47
1201.47
1239.20
1272.94
1333.90
1390.11
1443.72
1495.73
1546.73
1597.12
1647.17
1697.11
1747.10
1797.27
675.82
763.35
1007.56
1172.93
1251.46
1309.71
1358.75
1402.62
1481.60
1553.91
1622.38
1688.39
1752.78
1816.11
1878.79
1941.11
2003.32
2065.60
s
(Btu/lbm R)
2000 psia (635.99 F)
1.3358
1.4012
1.4429
1.4766
1.5058
1.5321
1.5562
1.6001
1.6398
1.6765
1.7108
1.7431
1.7738
1.8301
1.8312
1.8582
1.8843
1.9096
0.1881
0.2057
0.2487
0.2803
0.3071
0.3312
0.3534
0.3945
0.4325
0.4685
0.5031
0.5368
0.5697
0.6020
0.6340
0.6656
0.6971
0.7284
1066.63
1091.06
1147.74
1187.32
1220.13
1249.46
1276.78
1328.10
1377.17
1425.19
1472.74
1520.15
1567.64
1615.37
1663.45
1711.97
1760.99
1810.56
4000 psia
650
700
750
800
850
900
950
1000
1100
1200
1300
1400
1500
1600
1700
1800
1900
2000
h
(Btu/lbm)
1136.25
1167.18
1239.79
1291.07
1333.80
1372.03
1407.58
1474.09
1537.23
1598.58
1658.95
1718.81
1778.48
1838.18
1898.08
1958.32
2018.99
2080.15
1.2861
1.3141
1.3782
1.4216
1.4562
1.4860
1.5126
1.5598
1.6017
1.6398
1.6751
1.7082
1.7395
1.7692
1.7976
1.8248
1.8511
1.8765
8000 psia
0.8574
0.9345
1.1395
1.2740
1.3352
1.3789
1.4143
1.4449
1.4973
1.5423
1.5823
1.6188
1.6525
1.6841
1.7138
1.7420
1.7689
1.7948
0.02239
0.02418
0.02671
0.03061
0.03706
0.04657
0.05721
0.06722
0.08445
0.09892
0.11161
0.12309
0.13372
0.14373
0.15328
0.16251
0.17151
0.18034
627.01
688.59
755.67
830.67
915.81
1003.68
1079.59
1141.04
1236.84
1314.18
1382.27
1444.85
1503.78
1560.12
1614.58
1667.69
1719.85
1771.38
660.16
724.39
795.21
875.99
970.67
1072.63
1164.28
1240.55
1361.85
1460.62
1547.50
1627.08
1701.74
1772.89
1841.49
1908.27
1973.75
2038.36
0.8278
0.8844
0.9441
1.0095
1.0832
1.1596
1.2259
1.2791
1.3595
1.4210
1.4718
1.5158
1.5549
1.5904
1.6229
1.6531
1.6815
1.7083
.............................................................................................................................
APPENDIX F
ENGLISH UNIT TABLES
u
(Btu/lbm)
h
(Btu/lbm)
TABLE F.7.3
..............
⑦
857
Compressed Liquid Water
Temp.
(F)
v
(ft3 /lbm)
u
(Btu/lbm)
h
(Btu/lbm)
s
(Btu/lbm R)
v
(ft3 /lbm)
500 psia (467.12 F)
Sat.
32
50
75
100
125
150
175
200
225
250
275
300
325
350
375
400
425
450
0.01975
0.01599
0.01599
0.0160
0.0161
0.0162
0.0163
0.0165
0.0166
0.0168
0.0170
0.0172
0.0174
0.0177
0.0180
0.0183
0.0186
0.0190
0.0194
447.69
0.00
18.02
42.98
67.87
92.75
117.66
142.62
167.64
192.76
217.99
243.36
268.91
294.68
320.70
347.01
373.68
400.77
428.39
449.51
1.48
19.50
44.46
69.36
94.24
119.17
144.14
168.18
194.31
219.56
244.95
270.52
296.32
322.36
348.70
375.40
402.52
430.19
1000 psia (544.74 F)
0.6490
0.0000
0.0360
0.0838
0.1293
0.1728
0.2146
0.2547
0.2934
0.3308
0.3670
0.4022
0.4364
0.4698
0.5025
0.5345
0.5660
0.5971
0.6280
0.02159
0.01597
0.01599
0.0160
0.0161
0.0162
0.0163
0.0164
0.0166
0.0168
0.0169
0.0171
0.0174
0.0176
0.0179
0.0182
0.0185
0.0189
0.0193
538.37
0.02
17.98
42.87
67.70
92.52
117.37
142.28
167.25
192.30
217.46
242.77
268.24
293.91
319.83
346.02
372.55
399.47
426.89
2000 psia (635.99 F)
Sat.
50
75
100
125
150
175
200
225
250
275
300
325
350
400
450
500
600
0.02565
0.01592
0.0160
0.0160
0.0161
0.0162
0.0164
0.0165
0.0167
0.0169
0.0171
0.0173
0.0176
0.0178
0.0184
0.0192
0.0201
0.0233
662.38
17.91
42.66
67.36
92.07
116.82
141.62
166.48
191.42
216.45
241.61
266.92
292.42
318.14
370.38
424.03
479.84
605.37
671.87
23.80
48.57
73.30
98.04
122.84
147.68
172.60
197.59
222.69
247.93
273.33
298.92
324.74
377.20
431.13
487.29
613.99
s
(Btu/lbm R)
542.36
2.98
20.94
45.83
70.67
95.51
120.39
145.32
170.32
195.40
220.60
245.94
271.45
297.17
323.14
349.39
375.98
402.97
430.47
0.74318
0.0000
0.0359
0.0836
0.1290
0.1724
0.2141
0.2542
0.2928
0.3301
0.3663
0.4014
0.4355
0.4688
0.5014
0.5333
0.5647
0.5957
0.6263
8000 psia
0.8622
0.0357
0.0832
0.1284
0.1716
0.2132
0.2531
0.2916
0.3288
0.3648
0.3998
0.4337
0.4669
0.4993
0.5621
0.6231
0.6832
0.8086
—
0.01563
0.0157
0.01577
0.01586
0.01597
0.01610
0.01623
0.01639
0.01655
0.01675
0.01693
0.01714
0.01737
0.01788
0.01848
0.01918
0.02106
—
17.38
41.42
65.49
89.62
113.81
138.04
162.31
186.61
210.97
235.39
259.91
284.53
309.29
359.26
409.94
461.56
569.36
—
40.52
64.65
88.83
113.10
137.45
161.87
186.34
210.87
235.47
260.16
284.97
309.91
335.01
385.73
437.30
489.95
600.53
—
0.0342
0.0804
0.1246
0.1670
0.2078
0.2471
0.2849
0.3214
0.3567
0.3909
0.4241
0.4564
0.4878
0.5486
0.6069
0.6633
0.7728
⑦
APPENDIX F
..............858
www.elsolucionario.org
ENGLISH UNIT TABLES
.............................................................................................................................
TABLE F.7.4
Saturated Solid–Saturated Vapor, Water (English Units)
Specific Volume, ft3 /lbm
Internal Energy, Btu/lbm
Temp.
(F)
Press.
(lbf/in.2 )
Sat. Solid
vi
Sat. Vapor
vg × 10−3
Sat. Solid
ui
Evap.
ui g
Sat. Vapor
ug
32.02
32
30
25
20
15
10
5
0
−5
−10
−15
−20
−25
−30
−35
−40
0.08866
0.08859
0.08083
0.06406
0.05051
0.03963
0.03093
0.02402
0.01855
0.01424
0.01086
0.00823
0.00620
0.00464
0.00346
0.00256
0.00187
0.017473
0.01747
0.01747
0.01746
0.01745
0.01745
0.01744
0.01743
0.01742
0.01742
0.01741
0.01740
0.01740
0.01739
0.01738
0.01737
0.01737
3.302
3.305
3.607
4.505
5.655
7.133
9.043
11.522
14.761
19.019
24.657
32.169
42.238
55.782
74.046
98.890
134.017
−143.34
−143.35
−144.35
−146.84
−149.31
−151.75
−154.16
−156.56
−158.93
−161.27
−163.59
−165.89
−168.16
−170.40
−172.63
−174.82
−177.00
1164.5
1164.5
1164.9
1165.7
1166.5
1167.3
1168.1
1168.8
1169.5
1170.2
1170.8
1171.5
1172.1
1172.7
1173.2
1173.8
1174.3
1021.2
1021.2
1020.5
1018.9
1017.2
1015.6
1013.9
1012.2
1010.6
1008.9
1007.3
1005.6
1003.9
1002.3
1000.6
998.9
997.3
Enthalpy, Btu/lbm
Entropy, Btu/lbm R
Temp.
(F)
Press.
(lbf/in.2 )
Sat. Solid
hi
Evap.
hi g
Sat. Vapor
hg
Sat. Liquid
si
Evap.
si g
Sat. Vapor
sg
32.02
32
30
25
20
15
10
5
0
−5
−10
−15
−20
−25
−30
−35
−40
0.08866
0.08859
0.08083
0.06406
0.05051
0.03963
0.03093
0.02402
0.01855
0.01424
0.01086
0.00823
0.00620
0.00464
0.00346
0.00256
0.00187
−143.34
−143.35
−144.35
−146.84
−149.31
−151.75
−154.16
−156.56
−158.93
−161.27
−163.59
−165.89
−168.16
−170.40
−172.63
−174.82
−177.00
1218.7
1218.7
1218.8
1219.1
1219.4
1219.6
1219.8
1220.0
1220.2
1220.3
1220.4
1220.5
1220.5
1220.6
1220.6
1220.6
1220.5
1075.4
1075.4
1074.5
1072.3
1070.1
1067.9
1065.7
1063.5
1061.2
1059.0
1056.8
1054.6
1052.4
1050.2
1048.0
1045.7
1043.5
−0.2916
−0.2917
−0.2938
−0.2990
−0.3042
−0.3093
−0.3145
−0.3197
−0.3248
−0.3300
−0.3351
−0.3403
−0.3455
−0.3506
−0.3557
−0.3608
−0.3659
2.4786
2.4787
2.4891
2.5154
2.5422
2.5695
2.5973
2.6256
2.6544
2.6839
2.7140
2.7447
2.7761
2.8081
2.8406
2.8737
2.9084
2.1869
2.1870
2.1953
2.2164
2.2380
2.2601
2.2827
2.3059
2.3296
2.3539
2.3788
2.4044
2.4307
2.4575
2.4849
2.5129
2.5425
.............................................................................................................................
TABLE F.8
Thermodynamic Properties of Ammonia
APPENDIX F
ENGLISH UNIT TABLES
..............
⑦
859
psia: medición de presión que incluye la presión atmosférica
TABLE F.8.1
Saturated Ammonia
Specific Volume, ft3 /lbm
Internal Energy, Btu/lbm
Temp.
(F)
Press.
(psia)
Sat. Liquid
vf
Evap.
v fg
Sat. Vapor
vg
Sat. Liquid
uf
Evap.
u fg
Sat. Vapor
ug
−60
−50
−40
−30
−28.0
−20
−10
0
10
20
30
40
50
60
70
80
90
100
110
120
130
140
150
160
170
180
190
200
210
220
230
240
250
260
270.1
5.547
7.663
10.404
13.898
14.696
18.289
23.737
30.415
38.508
48.218
59.756
73.346
89.226
107.641
128.849
153.116
180.721
211.949
247.098
286.473
330.392
379.181
433.181
492.742
558.231
630.029
708.538
794.183
887.424
988.761
1098.766
1218.113
1347.668
1488.694
1643.742
0.02277
0.02299
0.02322
0.02345
0.02350
0.02369
0.02394
0.02420
0.02446
0.02474
0.02502
0.02532
0.02564
0.02597
0.02631
0.02668
0.02706
0.02747
0.02790
0.02836
0.02885
0.02938
0.02995
0.03057
0.03124
0.03199
0.03281
0.03375
0.03482
0.03608
0.03759
0.03950
0.04206
0.04599
0.06816
44.7397
33.0702
24.8464
18.9490
17.9833
14.6510
11.4714
9.0861
7.2734
5.8792
4.7945
3.9418
3.2647
2.7221
2.2835
1.9260
1.6323
1.3894
1.1870
1.0172
0.8740
0.7524
0.6485
0.5593
0.4822
0.4153
0.3567
0.3051
0.2592
0.2181
0.1807
0.1460
0.1126
0.0781
0
44.7625
33.0932
24.8696
18.9724
18.0068
14.6747
11.4953
9.1103
7.2979
5.9039
4.8195
3.9671
3.2903
2.7481
2.3098
1.9526
1.6594
1.4168
1.2149
1.0456
0.9028
0.7818
0.6785
0.5899
0.5135
0.4472
0.3895
0.3388
0.2941
0.2542
0.2183
0.1855
0.1547
0.1241
0.0682
−20.92
−10.51
−0.04
10.48
12.59
21.07
31.73
42.46
53.26
64.12
75.06
86.07
97.16
108.33
119.58
130.92
142.36
153.89
165.53
177.28
189.17
201.20
213.40
225.80
238.42
251.33
264.58
278.24
292.43
307.28
323.03
340.05
359.03
381.74
446.09
564.27
556.84
549.25
541.50
539.93
533.57
252.47
517.18
508.71
500.04
491.17
482.09
472.78
463.24
453.44
443.37
433.01
422.34
411.32
399.92
388.10
375.82
363.01
349.61
335.53
320.66
304.87
287.96
269.70
249.72
227.47
202.02
171.57
131.74
0
543.36
546.33
549.20
551.98
552.52
554.64
557.20
559.64
561.96
564.16
566.23
568.15
569.94
571.56
573.02
574.30
573.37
576.23
576.85
577.20
577.27
577.02
576.41
575.41
573.95
571.99
569.45
566.20
562.13
557.00
550.50
542.06
530.60
513.48
446.09
⑦
APPENDIX F
..............860
www.elsolucionario.org
.............................................................................................................................
ENGLISH UNIT TABLES
TABLE F.8.1 (continued )
Saturated Ammonia
Enthalpy, Btu/lbm
Entropy, Btu/lbm R
Temp.
(F)
Press.
(psia)
Sat. Liquid
hf
Evap.
hfg
Sat. Vapor
hg
Sat. Liquid
sf
Evap.
s fg
Sat. Vapor
sg
−60
−50
−40
−30
−28.0
−20
−10
0
10
20
30
40
50
60
70
80
90
100
110
120
130
140
150
160
170
180
190
200
210
220
230
240
250
260
270.1
5.547
7.663
10.404
13.898
14.696
18.289
23.737
30.415
38.508
48.218
59.756
73.346
89.226
107.641
128.849
153.116
180.721
211.949
247.098
286.473
330.392
379.181
433.181
492.742
558.231
630.029
708.538
794.183
887.424
988.761
1098.766
1218.113
1347.668
1488.694
1643.742
−20.89
−10.48
0
10.54
12.65
21.15
31.84
42.60
53.43
64.34
75.33
86.41
97.58
108.84
120.21
131.68
143.26
154.97
166.80
178.79
190.93
203.26
215.80
228.58
241.65
255.06
268.88
283.20
298.14
313.88
330.67
348.95
369.52
394.41
466.83
610.19
603.73
597.08
590.23
588.84
583.15
575.85
568.32
560.54
552.50
544.18
535.59
526.68
517.46
507.89
497.94
487.60
476.83
465.59
453.84
441.54
428.61
415.00
400.61
385.35
369.08
351.63
332.80
312.27
289.63
264.21
234.93
199.65
153.25
0
589.30
593.26
597.08
600.77
601.49
604.31
607.69
610.92
613.97
616.84
619.52
622.00
624.26
626.30
628.09
629.62
630.86
631.80
632.40
632.63
632.47
631.87
630.80
629.19
627.00
624.14
620.51
616.00
610.42
603.51
594.89
583.87
569.17
547.66
466.83
−0.0510
−0.0252
0
0.0248
0.0297
0.0492
0.0731
0.0967
0.1200
0.1429
0.1654
0.1877
0.2097
0.2314
0.2529
0.2741
0.2951
0.3159
0.3366
0.3571
0.3774
0.3977
0.4180
0.4382
0.4586
0.4790
0.4997
0.5208
0.5424
0.5647
0.5882
0.6132
0.6410
0.6743
0.7718
1.5267
1.4737
1.4227
1.3737
1.3641
1.3263
1.2806
1.2364
1.1935
1.1518
1.1113
1.0719
1.0334
0.9957
0.9589
0.9227
0.8871
0.8520
0.8173
0.7829
0.7488
0.7147
0.6807
0.6465
0.6120
0.5770
0.5412
0.5045
0.4663
0.4261
0.3831
0.3358
0.2813
0.2129
0
1.4758
1.4485
1.4227
1.3985
1.3938
1.3755
1.3538
1.3331
1.3134
1.2947
1.2768
1.2596
1.2431
1.2271
1.2117
1.1968
1.1822
1.1679
1.1539
1.1400
1.1262
1.1125
1.0987
1.0847
1.0705
1.0560
1.0410
1.0253
1.0087
0.9909
0.9713
0.9490
0.9224
0.8872
0.7718
.............................................................................................................................
APPENDIX F
ENGLISH UNIT TABLES
TABLE F.8.2
..............
⑦
861
Superheated Ammonia
Temp.
F
v
ft3 /lbm
h
Btu/lbm
s
Btu/lbm R
5 psia (−63.09 F)
Sat.
−40
−20
0
20
40
60
80
100
120
140
160
180
200
220
240
260
280
49.32002
52.3487
54.9506
57.5366
60.1099
62.6732
65.2288
67.7782
70.3228
72.8637
75.4015
77.9370
80.4706
83.0026
85.5334
88.0631
90.5918
93.1199
588.05
599.56
609.53
619.51
629.50
639.52
649.57
659.67
669.84
680.06
690.36
700.74
711.20
721.75
732.39
743.13
753.96
764.90
1.4846
1.5128
1.5360
1.5582
1.5795
1.5999
1.6197
1.6387
1.6572
1.6752
1.6926
1.7097
1.7263
1.7425
1.7584
1.7740
1.7892
1.8042
20 psia (−16.63 F)
Sat.
0
20
40
60
80
100
120
140
160
180
200
220
240
260
280
300
320
13.49628
14.0774
14.7635
15.4385
16.1051
16.7651
17.4200
18.0709
18.7187
19.3640
20.0073
20.6491
21.2895
21.9288
22.5673
23.2049
23.8419
24.4783
605.47
614.54
625.30
635.94
646.51
657.02
667.51
678.01
688.53
699.09
709.71
720.39
731.14
741.97
752.88
763.89
774.99
786.18
1.3680
1.3881
1.4111
1.4328
1.4535
1.4734
1.4925
1.5109
1.5287
1.5461
1.5629
1.5794
1.5954
1.6111
1.6265
1.6416
1.6564
1.6709
v
ft3 /lbm
h
Btu/lbm
s
Btu/lbm R
10 psia (−41.33 F)
25.80648
25.8962
27.2401
28.5674
29.8814
31.1852
32.4809
33.7703
35.0549
36.3356
37.6133
38.8886
40.1620
41.4338
42.7043
43.9737
45.2422
46.5100
596.58
597.27
607.60
617.88
628.12
638.34
648.56
658.80
669.07
679.38
689.75
700.19
710.70
721.30
731.98
742.74
753.61
764.56
1.4261
1.4277
1.4518
1.4746
1.4964
1.5173
1.5374
1.5567
1.5754
1.5935
1.6111
1.6282
1.6449
1.6612
1.6771
1.6928
1.7081
1.7231
25 psia (−7.95 F)
10.95013
11.1771
11.7383
12.2881
12.8291
13.3634
13.8926
14.4176
14.9395
15.4589
15.9763
16.4920
17.0065
17.5198
18.0322
18.5439
19.0548
19.5652
608.37
612.82
623.86
634.72
645.46
656.12
666.73
677.32
687.91
698.54
709.20
719.93
730.72
741.58
752.52
763.55
774.67
785.89
1.3494
1.3592
1.3827
1.4049
1.4260
1.4461
1.4654
1.4840
1.5020
1.5194
1.5363
1.5528
1.5689
1.5847
1.6001
1.6152
1.6301
1.6446
v
ft3 /lbm
h
Btu/lbm
s
Btu/lbm R
15 psia (−27.27 F)
17.66533
—
17.9999
18.9086
19.8036
20.6880
21.5641
22.4338
23.2985
24.1593
25.0170
25.8723
26.7256
27.5774
28.4278
29.2772
30.1256
30.9733
601.75
—
605.63
616.22
626.72
637.15
647.54
657.91
668.29
678.70
689.14
699.64
710.21
720.84
731.56
742.36
753.24
764.23
1.3921
1.4010
1.4245
1.4469
1.4682
1.4886
1.5082
1.5271
1.5453
1.5630
1.5803
1.5970
1.6134
1.6294
1.6451
1.6604
1.6755
30 psia (−0.57 F)
9.22850
9.2423
9.7206
10.1872
10.6447
11.0954
11.5407
11.9820
12.4200
12.8554
13.2888
13.7206
14.1511
14.5804
15.0088
15.4365
15.8634
16.2898
610.74
611.06
622.39
633.49
644.41
655.21
665.93
676.62
687.29
697.98
708.70
719.47
730.29
741.19
752.16
763.21
774.36
785.59
1.3342
1.3349
1.3591
1.3817
1.4032
1.4236
1.4431
1.4618
1.4799
1.4975
1.5145
1.5311
1.5472
1.5630
1.5785
1.5936
1.6085
1.6231
⑦
APPENDIX F
..............862
www.elsolucionario.org
ENGLISH UNIT TABLES
.............................................................................................................................
TABLE F.8.2 (continued )
Superheated Ammonia
Temp.
F
v
ft3 /lbm
h
Btu/lbm
s
Btu/lbm R
v
ft3 /lbm
35 psia (5.89 F)
Sat.
20
40
60
80
100
120
140
160
180
200
220
240
260
280
300
320
340
7.98414
8.2786
8.6860
9.0841
9.4751
9.8606
10.2420
10.6202
10.9957
11.3692
11.7410
12.1115
12.4808
12.8493
13.2169
13.5838
13.9502
14.3160
612.73
620.90
632.23
643.34
654.29
665.14
675.92
686.67
697.42
708.19
719.01
729.87
740.80
751.80
762.88
774.04
785.29
796.64
1.3214
1.3387
1.3618
1.3836
1.4043
1.4240
1.4430
1.4612
1.4788
1.4959
1.5126
1.5288
1.5447
1.5602
1.5753
1.5902
1.6049
1.6192
4.80091
4.9277
5.1787
5.4217
5.6586
5.8909
6.1197
6.3456
6.5694
6.7915
7.0121
7.2316
7.4501
7.6678
7.8848
8.1011
8.3169
8.5323
619.57
625.69
637.82
649.57
661.05
672.34
683.50
694.59
705.64
716.68
727.73
738.83
749.97
761.17
772.45
783.80
795.24
806.77
1.2764
1.2888
1.3126
1.3348
1.3557
1.3755
1.3944
1.4126
1.4302
1.4472
1.4637
1.4798
1.4955
1.5108
1.5259
1.5406
1.5551
1.5693
s
Btu/lbm R
v
ft3 /lbm
40 psia (11.66 F)
7.04135
7.1964
7.5596
7.9132
8.2596
8.6004
8.9370
9.2702
9.6008
9.9294
10.2562
10.5817
10.9061
11.2296
11.5522
11.8741
12.1955
12.5163
60 psia (30.19 F)
Sat.
40
60
80
100
120
140
160
180
200
220
240
260
280
300
320
340
360
h
Btu/lbm
614.45
619.39
630.96
642.26
653.37
664.33
675.21
686.04
696.86
707.69
718.54
729.44
741.40
751.43
762.54
773.72
785.00
796.36
1.3103
1.3206
1.3443
1.3665
1.3874
1.4074
1.4265
1.4449
1.4626
1.4798
1.4965
1.5128
1.5287
1.5442
1.5594
1.5744
1.5890
1.6034
621.44
622.94
635.52
647.62
659.37
670.88
682.21
693.44
704.60
715.73
726.87
738.03
749.23
760.49
771.81
783.21
794.68
806.24
1.2635
1.2665
1.2912
1.3140
1.3354
1.3556
1.3749
1.3933
1.4110
1.4281
1.4448
1.4610
1.4767
1.4922
1.5073
1.5221
1.5366
1.5509
s
Btu/lbm R
50 psia (21.66 F)
5.70491
—
5.9814
6.2731
6.5573
6.8356
7.1096
7.3800
7.6478
7.9135
8.1775
8.4400
8.7014
8.9619
9.2216
9.4805
9.7389
9.9967
70 psia (37.68 F)
4.14732
4.1738
4.3961
4.6099
4.8174
5.0201
5.2191
5.4153
5.6093
5.8014
5.9921
6.1816
6.3702
6.5579
6.7449
6.9313
7.1171
7.3025
h
Btu/lbm
617.30
—
628.37
640.07
651.49
662.70
673.79
684.78
695.73
706.67
717.61
728.59
739.62
750.70
761.86
773.09
784.40
795.80
1.2917
—
1.3142
1.3372
1.3588
1.3792
1.3986
1.4173
1.4352
1.4526
1.4695
1.4859
1.5018
1.5175
1.5327
1.5477
1.5624
1.5769
80 psia (44.38 F)
3.65200
—
3.8083
4.0005
4.1861
4.3667
4.5435
4.7174
4.8890
5.0588
5.2270
5.3941
5.5602
5.7254
5.8900
6.0538
6.2172
6.3801
623.02
—
633.16
645.63
657.66
669.39
680.90
692.27
703.55
714.79
726.00
737.23
748.50
759.80
771.17
782.61
794.12
805.71
1.2523
—
1.2721
1.2956
1.3175
1.3381
1.3577
1.3763
1.3942
1.4115
1.4283
1.4446
1.4604
1.4759
1.4911
1.5059
1.5205
1.5348
.............................................................................................................................
APPENDIX F
ENGLISH UNIT TABLES
TABLE F.8.2 (continued )
..............
⑦
863
Superheated Ammonia
Temp.
F
v
ft3 /lbm
h
Btu/lbm
s
Btu/lbm R
v
ft3 /lbm
90 psia (50.45 F)
Sat.
60
80
100
120
140
160
180
200
220
240
260
280
300
320
340
360
380
3.26324
3.3503
3.5260
3.6947
3.8583
4.0179
4.1745
4.3287
4.4811
4.6319
4.7816
4.9302
5.0779
5.2250
5.3714
5.5173
5.6626
5.8076
624.36
630.74
643.59
655.92
667.88
679.58
691.10
702.50
713.83
725.13
736.43
747.75
759.11
770.53
782.01
793.56
805.18
816.90
1.2423
1.2547
1.2790
1.3014
1.3224
1.3423
1.3612
1.3793
1.3967
1.4136
1.4300
1.4459
1.4615
1.4767
1.4916
1.5063
1.5206
1.5348
1.99226
1.9997
2.1170
2.2275
2.3331
2.4351
2.5343
2.6313
2.7267
2.8207
2.9136
3.0056
3.0968
3.1873
3.2772
3.3667
3.4557
3.5442
629.45
630.36
644.81
658.37
671.31
683.80
695.99
707.96
719.79
731.54
743.24
754.93
766.63
778.37
790.15
801.99
813.90
825.88
1.1986
1.2003
1.2265
1.2504
1.2723
1.2928
1.3122
1.3306
1.3483
1.3653
1.3818
1.3978
1.4134
1.4287
1.4436
1.4582
1.4726
1.4867
s
Btu/lbm R
v
ft3 /lbm
100 psia (56.02 F)
2.94969
2.9831
3.1459
3.3013
3.4513
3.5972
3.7400
3.8804
4.0188
4.1558
4.2915
4.4261
4.5599
4.6930
4.8254
4.9573
5.0887
5.2196
150 psia (78.79 F)
Sat.
80
100
120
140
160
180
200
220
240
260
280
300
320
340
360
380
400
h
Btu/lbm
625.52
628.25
641.51
654.16
666.36
678.24
689.91
701.44
712.87
724.25
735.63
747.01
758.42
769.88
781.40
792.99
804.66
816.40
1.2334
1.2387
1.2637
1.2867
1.3082
1.3283
1.3475
1.3658
1.3834
1.4004
1.4169
1.4329
1.4485
1.4638
1.4788
1.4935
1.5079
1.5220
630.64
—
639.77
654.13
667.67
680.62
693.17
705.44
717.51
729.46
741.33
753.16
764.99
776.84
788.72
800.65
812.64
824.70
1.1850
1.2015
1.2267
1.2497
1.2710
1.2909
1.3098
1.3278
1.3451
1.3619
1.3781
1.3939
1.4092
1.4243
1.4390
1.4535
1.4677
s
Btu/lbm R
125 psia (68.28 F)
2.37866
—
2.4597
2.5917
2.7177
2.8392
2.9574
3.0730
3.1865
3.2985
3.4091
3.5187
3.6274
3.7353
3.8426
3.9493
4.0555
4.1613
175 psia (88.03 F)
1.71282
—
1.7762
1.8762
1.9708
2.0614
2.1491
2.2345
2.3181
2.4002
2.4813
2.5613
2.6406
2.7192
2.7972
2.8746
2.9516
3.0282
h
Btu/lbm
627.80
—
636.11
649.59
662.44
674.83
686.90
698.74
710.44
722.04
733.59
745.13
756.68
768.27
779.89
791.58
803.33
815.15
1.2143
—
1.2299
1.2544
1.2770
1.2980
1.3178
1.3366
1.3546
1.3720
1.3887
1.4050
1.4208
1.4362
1.4514
1.4662
1.4807
1.4949
200 psia (96.31 F)
1.50102
—
1.5190
1.6117
1.6984
1.7807
1.8598
1.9365
2.0114
2.0847
2.1569
2.2280
2.2984
2.3680
2.4370
2.5056
2.5736
2.6412
631.49
—
634.45
649.71
663.90
677.36
690.30
702.87
715.20
727.35
739.39
751.38
763.33
775.30
787.28
799.30
811.38
823.51
1.1731
—
1.1785
1.2052
1.2293
1.2514
1.2719
1.2913
1.3097
1.3273
1.3443
1.3607
1.3767
1.3922
1.4074
1.4223
1.4368
1.4511
⑦
APPENDIX F
..............864
www.elsolucionario.org
ENGLISH UNIT TABLES
.............................................................................................................................
TABLE F.8.2 (continued )
Superheated Ammonia
Temp.
F
v
ft3 /lbm
h
Btu/lbm
s
Btu/lbm R
v
ft3 /lbm
250 psia (110.78 F)
Sat.
120
140
160
180
200
220
240
260
280
300
320
340
360
380
400
420
440
1.20063
1.2384
1.3150
1.3863
1.4539
1.5188
1.5815
1.6426
1.7024
1.7612
1.8191
1.8762
1.9328
1.9887
2.0442
2.0993
2.1540
2.2083
632.43
640.21
655.95
670.53
684.34
697.59
710.45
723.05
735.46
747.76
759.98
772.18
784.37
796.59
808.83
821.13
833.48
845.90
1.1528
1.1663
1.1930
1.2170
1.2389
1.2593
1.2785
1.2968
1.3142
1.3311
1.3474
1.3633
1.3787
1.3938
1.4085
1.4230
1.4372
1.4512
0.73876
0.7860
0.8392
0.8880
0.9338
0.9773
1.0192
1.0597
1.0992
1.1379
1.1758
1.2131
1.2499
1.2862
1.3221
1.3576
1.3928
1.4277
631.50
647.06
664.44
680.32
695.21
709.40
723.10
736.47
749.60
762.58
775.45
788.27
801.06
813.85
826.66
839.51
852.39
865.34
1.1070
1.1324
1.1601
1.1845
1.2067
1.2273
1.2466
1.2650
1.2825
1.2993
1.3156
1.3315
1.3469
1.3619
1.3767
1.3911
1.4053
1.4192
s
Btu/lbm R
v
ft3 /lbm
300 psia (123.20 F)
0.99733
—
1.0568
1.1217
1.1821
1.2394
1.2943
1.3474
1.3991
1.4497
1.4994
1.5482
1.5965
1.6441
1.6913
1.7380
1.7843
1.8302
400 psia (143.97 F)
Sat.
160
180
200
220
240
260
280
300
320
340
360
380
400
420
440
460
480
h
Btu/lbm
632.63
—
647.32
663.27
678.07
692.08
705.55
718.63
731.44
744.07
756.58
769.02
781.43
793.84
806.27
818.72
831.23
843.78
1.1356
—
1.1605
1.1866
1.2101
1.2317
1.2518
1.2708
1.2888
1.3062
1.3228
1.3390
1.3547
1.3701
1.3850
1.3997
1.4141
1.4282
625.39
—
630.48
652.67
671.78
689.03
705.06
720.26
734.88
749.09
763.02
776.75
790.34
803.86
817.32
830.76
844.21
857.67
1.0620
—
1.0700
1.1041
1.1327
1.1577
1.1803
1.2011
1.2206
1.2391
1.2567
1.2737
1.2901
1.3060
1.3215
1.3366
1.3514
1.3658
s
Btu/lbm R
350 psia (134.14 F)
0.85027
—
0.8696
0.9309
0.9868
1.0391
1.0886
1.1362
1.1822
1.2270
1.2708
1.3138
1.3561
1.3979
1.4391
1.4798
1.5202
1.5602
600 psia (175.93 F)
0.47311
—
0.4834
0.5287
0.5680
0.6035
0.6366
0.6678
0.6976
0.7264
0.7542
0.7814
0.8079
0.8340
0.8595
0.8847
0.9095
0.9340
h
Btu/lbm
632.28
—
637.87
655.48
671.46
686.34
700.47
714.08
727.32
740.31
753.12
765.82
778.46
791.07
803.67
816.30
828.95
841.65
1.1205
—
1.1299
1.1588
1.1842
1.2071
1.2282
1.2479
1.2666
1.2844
1.3015
1.3180
1.3340
1.3496
1.3648
1.3796
1.3942
1.4085
800 psia (200.65 F)
0.33575
—
—
—
0.3769
0.4115
0.4419
0.4694
0.4951
0.5193
0.5425
0.5648
0.5864
0.6074
0.6279
0.6480
0.6677
0.6871
615.67
—
—
—
642.62
665.08
684.62
702.36
718.93
734.69
749.89
764.68
779.19
793.50
807.68
821.76
835.80
849.80
1.0242
—
—
—
1.0645
1.0971
1.1246
1.1489
1.1710
1.1915
1.2108
1.2290
1.2465
1.2634
1.2797
1.2955
1.3109
1.3260
.............................................................................................................................
APPENDIX F
ENGLISH UNIT TABLES
TABLE F.9
..............
⑦
865
Thermodynamic Properties of R-410a
TABLE F.9.1
Saturated R-410a
Specific Volume, ft3 /lbm
Internal Energy, Btu/lbm
Temp.
(F)
Press.
(psia)
Sat. Liquid
vf
Evap.
v fg
Sat. Vapor
vg
Sat. Liquid
uf
Evap.
u fg
Sat. Vapor
ug
−80
−70
−60.5
−60
−50
−40
−30
−20
−10
0
10
20
30
40
50
60
70
80
90
100
110
120
130
140
150
160
160.4
8.196
11.152
14.696
14.905
19.598
25.387
32.436
40.923
51.034
62.967
76.926
93.128
111.796
133.163
157.473
184.980
215.951
250.665
289.421
332.541
380.377
433.323
491.841
556.488
627.997
707.371
710.859
0.01158
0.01173
0.01187
0.01188
0.01204
0.01220
0.01237
0.01255
0.01275
0.01295
0.01316
0.01339
0.01364
0.01391
0.01420
0.01451
0.01486
0.01525
0.01569
0.01619
0.01679
0.01750
0.01841
0.01966
0.02170
0.03054
0.03490
6.6272
4.9609
3.8243
3.7736
2.9123
2.2770
1.8011
1.4397
1.1615
0.9448
0.7741
0.6382
0.5289
0.4402
0.3676
0.3076
0.2576
0.2156
0.1800
0.1495
0.1231
0.1000
0.0792
0.0599
0.0405
0.0080
0
6.6388
4.9726
3.8362
3.7855
2.9243
2.2892
1.8135
1.4522
1.1742
0.9578
0.7873
0.6516
0.5426
0.4541
0.3818
0.3221
0.2724
0.2308
0.1957
0.1657
0.1399
0.1175
0.0976
0.0796
0.0622
0.0385
0.0349
−13.12
−9.88
−6.78
−6.62
−3.35
−0.06
3.26
6.60
9.96
13.37
16.81
20.29
23.82
27.41
31.06
34.78
38.57
42.46
46.46
50.59
54.88
59.37
64.18
69.46
75.78
88.87
92.77
111.09
108.94
106.88
106.77
104.55
102.30
100.00
97.65
95.23
92.75
90.20
87.55
84.81
81.95
78.96
75.82
72.50
68.97
65.20
61.12
56.64
51.65
45.92
38.99
29.65
6.57
0
97.97
99.07
100.09
100.15
101.20
102.24
103.25
104.24
105.20
106.12
107.00
107.84
108.63
109.36
110.02
110.59
111.07
111.44
111.66
111.70
111.52
111.02
110.09
108.46
105.43
95.44
92.77
⑦
APPENDIX F
..............866
www.elsolucionario.org
ENGLISH UNIT TABLES
.............................................................................................................................
TABLE F.9.1 (continued )
Saturated R-410a
Enthalpy, Btu/lbm
Entropy, Btu/lbm R
Temp.
(F)
Press.
(psia)
Sat. Liquid
hf
Evap.
h fg
Sat. Vapor
hg
Sat. Liquid
sf
Evap.
s fg
Sat. Vapor
sg
−80
−70
−60.5
−60
−50
−40
−30
−20
−10
0
10
20
30
40
50
60
70
80
90
100
110
120
130
140
150
160
160.4
8.196
11.152
14.696
14.905
19.598
25.387
32.436
40.923
51.034
62.967
76.926
93.128
111.796
133.163
157.473
184.980
215.951
250.665
289.421
332.541
380.377
433.323
491.841
556.488
627.997
707.371
710.859
−13.10
−9.85
−6.75
−6.59
−3.30
0
3.33
6.69
10.08
13.52
17.00
20.52
24.11
27.75
31.47
35.27
39.17
43.17
47.30
51.58
56.06
60.78
65.85
71.49
78.30
92.87
97.36
121.14
119.18
117.28
117.17
115.11
113.00
110.81
108.55
106.20
103.76
101.22
98.55
95.75
92.80
89.67
86.35
82.79
78.97
74.84
70.31
65.31
59.66
53.12
45.16
34.36
7.62
0
108.04
109.33
110.52
110.59
111.81
113.00
114.14
115.24
116.29
117.28
118.21
119.07
119.85
120.55
121.14
121.62
121.96
122.14
122.14
121.90
121.36
120.44
118.97
116.65
112.65
100.49
97.36
−0.0327
−0.0243
−0.0164
−0.0160
−0.0079
0
0.0078
0.0155
0.0231
0.0306
0.0380
0.0453
0.0526
0.0599
0.0671
0.0744
0.0816
0.0889
0.0963
0.1038
0.1115
0.1194
0.1277
0.1368
0.1476
0.1707
0.1779
0.3191
0.3059
0.2938
0.2932
0.2810
0.2692
0.2579
0.2469
0.2362
0.2257
0.2155
0.2055
0.1955
0.1857
0.1759
0.1662
0.1563
0.1463
0.1361
0.1256
0.1146
0.1029
0.0901
0.0753
0.0564
0.0123
0
0.2864
0.2816
0.2774
0.2772
0.2731
0.2692
0.2657
0.2624
0.2592
0.2563
0.2535
0.2508
0.2482
0.2456
0.2431
0.2405
0.2379
0.2353
0.2325
0.2294
0.2261
0.2223
0.2178
0.2121
0.2040
0.1830
0.1779
.............................................................................................................................
APPENDIX F
ENGLISH UNIT TABLES
u
(Btu/lbm)
h
(Btu/lbm)
TABLE F.9.2
..............
⑦
867
Superheated R-410a
Temp.
(F)
v
(ft3 /lbm)
u
(Btu/lbm)
h
(Btu/lbm)
s
(Btu/lbm R)
v
(ft3 /lbm)
5 psia (−94.86 F)
Sat.
−80
−60
−40
−20
0
20
40
60
80
100
120
140
160
180
200
220
10.5483
11.0228
11.6486
12.2654
12.8764
13.4834
14.0874
14.6893
15.2895
15.8884
16.4863
17.0832
17.6795
18.2752
18.8704
19.4653
20.0597
96.32
98.45
101.31
104.21
107.16
110.17
113.24
116.39
119.61
122.90
126.28
129.73
133.26
136.88
140.57
144.34
148.19
106.08
108.65
112.09
115.56
119.07
122.64
126.27
129.98
133.75
137.60
141.53
145.54
149.62
153.78
158.03
162.35
166.75
10 psia (−73.61 F)
0.2943
0.3012
0.3100
0.3185
0.3266
0.3346
0.3423
0.3499
0.3573
0.3646
0.3717
0.3787
0.3857
0.3925
0.3992
0.4059
0.4125
5.5087
—
5.7350
6.0583
6.3746
6.6864
6.9950
7.3014
7.6060
7.9093
8.2115
8.5128
8.8134
9.1135
9.4130
9.7121
10.0109
15 psia (−59.77 F)
Sat.
−40
−20
0
20
40
60
80
100
120
140
160
180
200
220
240
260
3.7630
3.9875
4.2063
4.4201
4.6305
4.8385
5.0447
5.2495
5.4531
5.6559
5.8580
6.0595
6.2605
6.4611
6.6613
6.8613
7.0609
100.17
103.31
106.43
109.56
112.72
115.94
119.21
122.55
125.97
129.45
133.01
136.64
140.35
144.14
148.01
151.95
155.97
110.61
114.37
118.10
121.83
125.58
129.37
133.22
137.13
141.10
145.15
149.27
153.46
157.73
162.08
166.50
170.99
175.57
s
(Btu/lbm R)
98.67
—
100.75
103.77
106.80
109.87
112.98
116.16
119.41
122.73
126.12
129.59
133.14
136.76
140.46
144.24
148.10
108.87
—
111.37
114.98
118.60
122.24
125.93
129.67
133.49
137.37
141.32
145.34
149.44
153.62
157.88
162.21
166.62
0.2833
—
0.2896
0.2985
0.3069
0.3150
0.3228
0.3305
0.3379
0.3453
0.3525
0.3595
0.3665
0.3733
0.3801
0.3868
0.3934
20 psia (−49.24 F)
0.2771
0.2862
0.2949
0.3032
0.3112
0.3189
0.3265
0.3339
0.3411
0.3482
0.3552
0.3621
0.3688
0.3755
0.3821
0.3887
0.3951
2.8688
2.9506
3.1214
3.2865
3.4479
3.6068
3.7638
3.9194
4.0739
4.2274
4.3803
4.5325
4.6842
4.8355
4.9865
5.1372
5.2876
101.28
102.81
106.04
109.24
112.46
115.71
119.01
122.38
125.81
129.31
132.88
136.52
140.25
144.04
147.91
151.86
155.89
111.90
113.73
117.59
121.41
125.22
129.06
132.94
136.88
140.88
144.95
149.09
153.30
157.58
161.94
166.37
170.88
175.46
0.2728
0.2772
0.2862
0.2946
0.3027
0.3106
0.3182
0.3257
0.3329
0.3401
0.3471
0.3540
0.3608
0.3675
0.3741
0.3807
0.3871
⑦
APPENDIX F
..............868
www.elsolucionario.org
ENGLISH UNIT TABLES
.............................................................................................................................
TABLE F.9.2 (continued )
Superheated R-410a
Temp.
(F)
v
(ft3 /lbm)
u
(Btu/lbm)
h
(Btu/lbm)
s
(Btu/lbm R)
v
(ft3 /lbm)
30 psia (−33.24 F)
Sat.
−20
0
20
40
60
80
100
120
140
160
180
200
220
240
260
280
1.9534
2.0347
2.1518
2.2647
2.3747
2.4827
2.5892
2.6944
2.7988
2.9024
3.0054
3.1079
3.2099
3.3116
3.4130
3.5142
3.6151
102.93
105.22
108.59
111.91
115.24
118.61
122.02
125.49
129.02
132.62
136.29
140.03
143.84
147.73
151.69
155.73
159.83
113.77
116.52
120.53
124.48
128.43
132.39
136.39
140.45
144.56
148.73
152.97
157.28
161.66
166.11
170.64
175.23
179.90
1.0038
1.0120
1.0783
1.1405
1.2001
1.2579
1.3143
1.3696
1.4242
1.4780
1.5313
1.5842
1.6367
1.6888
1.7407
1.7924
1.8438
105.91
106.37
110.13
113.76
117.34
120.91
124.51
128.14
131.83
135.57
139.37
143.23
147.16
151.16
155.23
159.37
163.58
117.05
117.60
122.11
126.42
130.66
134.88
139.10
143.35
147.64
151.98
156.37
160.82
165.34
169.92
174.56
179.27
184.05
h
(Btu/lbm)
s
(Btu/lbm R)
40 psia (−21.00 F)
0.2668
0.2732
0.2821
0.2905
0.2986
0.3063
0.3139
0.3213
0.3285
0.3356
0.3425
0.3494
0.3561
0.3628
0.3693
0.3758
0.3822
1.4843
1.4892
1.5833
1.6723
1.7581
1.8418
1.9238
2.0045
2.0844
2.1634
2.2418
2.3197
2.3971
2.4742
2.5510
2.6275
2.7037
60 psia (−2.34 F)
Sat.
0
20
40
60
80
100
120
140
160
180
200
220
240
260
280
300
u
(Btu/lbm)
104.14
104.33
107.89
111.34
114.76
118.19
121.66
125.17
128.73
132.36
136.05
139.81
143.64
147.54
151.52
155.56
159.68
115.13
115.35
119.61
123.72
127.78
131.83
135.90
140.00
144.16
148.37
152.64
156.98
161.38
165.86
170.40
175.01
179.69
0.2627
0.2632
0.2727
0.2814
0.2897
0.2977
0.3053
0.3128
0.3201
0.3273
0.3343
0.3412
0.3479
0.3546
0.3612
0.3677
0.3741
75 psia (8.71 F)
0.2570
0.2582
0.2678
0.2766
0.2849
0.2929
0.3005
0.3080
0.3153
0.3224
0.3294
0.3362
0.3430
0.3496
0.3561
0.3626
0.3690
0.8071
—
0.8393
0.8926
0.9429
0.9911
1.0379
1.0835
1.1283
1.1724
1.2159
1.2590
1.3016
1.3439
1.3860
1.4278
1.4694
106.89
—
109.15
112.96
116.66
120.33
124.00
127.69
131.42
135.20
139.03
142.92
146.88
150.90
154.99
159.14
163.36
118.09
—
120.80
125.35
129.75
134.09
138.40
142.73
147.08
151.47
155.90
160.39
164.94
169.55
174.22
178.96
183.76
0.2538
—
0.2595
0.2688
0.2775
0.2857
0.2935
0.3011
0.3085
0.3157
0.3227
0.3296
0.3364
0.3431
0.3497
0.3562
0.3626
.............................................................................................................................
APPENDIX F
ENGLISH UNIT TABLES
u
(Btu/lbm)
h
(Btu/lbm)
TABLE F.9.2 (continued )
..............
⑦
869
Superheated R-410a
Temp.
(F)
v
(ft3 /lbm)
u
(Btu/lbm)
h
(Btu/lbm)
s
(Btu/lbm R)
v
(ft3 /lbm)
100 psia (23.84 F)
Sat.
40
60
80
100
120
140
160
180
200
220
240
260
280
300
320
340
0.6069
0.6433
0.6848
0.7238
0.7611
0.7971
0.8323
0.8666
0.9004
0.9336
0.9665
0.9990
1.0312
1.0632
1.0950
1.1266
1.1580
108.15
111.53
115.48
119.32
123.12
126.92
130.73
134.57
138.46
142.40
146.39
150.45
154.57
158.75
163.00
167.31
171.69
119.38
123.43
128.16
132.72
137.21
141.67
146.13
150.61
155.12
159.68
164.28
168.94
173.65
178.43
183.26
188.16
193.12
125 psia (36.33 F)
0.2498
0.2580
0.2673
0.2759
0.2840
0.2919
0.2994
0.3068
0.3140
0.3210
0.3278
0.3346
0.3412
0.3478
0.3542
0.3606
0.3669
0.4845
0.4918
0.5288
0.5626
0.5945
0.6250
0.6544
0.6830
0.7109
0.7384
0.7654
0.7920
0.8184
0.8445
0.8703
0.8960
0.9215
150 psia (47.06 F)
Sat.
60
80
100
120
140
160
180
200
220
240
260
280
300
320
340
360
0.4016
0.4236
0.4545
0.4830
0.5099
0.5356
0.5604
0.5845
0.6081
0.6312
0.6540
0.6764
0.6986
0.7205
0.7423
0.7639
0.7853
109.83
112.82
117.13
121.25
125.28
129.28
133.27
137.28
141.33
145.41
149.54
153.72
157.96
162.26
166.61
171.03
175.51
120.98
124.58
129.74
134.66
139.43
144.14
148.83
153.51
158.20
162.93
167.69
172.50
177.35
182.26
187.22
192.23
197.31
s
(Btu/lbm R)
109.10
109.93
114.21
118.26
122.21
126.11
130.01
133.93
137.88
141.87
145.91
150.00
154.15
158.36
162.63
166.96
171.36
120.31
121.30
126.44
131.28
135.96
140.57
145.15
149.73
154.32
158.95
163.61
168.32
173.08
177.89
182.76
187.69
192.68
0.2465
0.2485
0.2586
0.2677
0.2763
0.2844
0.2921
0.2996
0.3069
0.3141
0.3210
0.3278
0.3346
0.3411
0.3476
0.3540
0.3604
175 psia (56.51 F)
0.2438
0.2508
0.2606
0.2695
0.2779
0.2859
0.2936
0.3010
0.3082
0.3153
0.3222
0.3290
0.3356
0.3422
0.3486
0.3550
0.3612
0.3417
0.3472
0.3766
0.4029
0.4274
0.4505
0.4727
0.4941
0.5150
0.5353
0.5553
0.5750
0.5944
0.6135
0.6325
0.6513
0.6699
110.40
111.27
115.91
120.24
124.41
128.52
132.60
136.68
140.77
144.90
149.07
153.29
157.56
161.88
166.26
170.70
175.19
121.47
122.51
128.11
133.29
138.25
143.11
147.90
152.68
157.45
162.24
167.06
171.91
176.81
181.75
186.74
191.79
196.89
0.2414
0.2434
0.2540
0.2634
0.2721
0.2804
0.2882
0.2958
0.3032
0.3103
0.3173
0.3241
0.3309
0.3375
0.3439
0.3503
0.3566
⑦
APPENDIX F
..............870
www.elsolucionario.org
ENGLISH UNIT TABLES
.............................................................................................................................
TABLE F.9.2 (continued )
Superheated R-410a
Temp.
(F)
v
(ft3 /lbm)
u
(Btu/lbm)
h
(Btu/lbm)
s
(Btu/lbm R)
v
(ft3 /lbm)
200 psia (65.00 F)
Sat.
80
100
120
140
160
180
200
220
240
260
280
300
320
340
360
380
0.2962
0.3174
0.3424
0.3652
0.3865
0.4068
0.4262
0.4451
0.4634
0.4813
0.4989
0.5162
0.5333
0.5502
0.5668
0.5834
0.5997
110.85
114.59
119.17
123.51
127.73
131.90
136.05
140.21
144.39
148.60
152.85
157.15
161.50
165.90
170.36
174.88
179.45
121.81
126.34
131.84
137.02
142.04
146.96
151.83
156.68
161.54
166.41
171.32
176.26
181.24
186.26
191.34
196.47
201.65
0.1310
0.1383
0.1574
0.1729
0.1865
0.1990
0.2106
0.2216
0.2322
0.2424
0.2522
0.2619
0.2713
0.2805
0.2895
0.2985
0.3073
111.37
113.71
120.01
125.42
130.44
135.25
139.94
144.57
149.16
153.75
158.34
162.96
167.61
172.29
177.01
181.77
186.58
121.06
123.95
131.66
138.22
144.25
149.98
155.53
160.97
166.35
171.69
177.02
182.34
187.69
193.05
198.44
203.86
209.32
h
(Btu/lbm)
s
(Btu/lbm R)
300 psia (92.55 F)
0.2392
0.2477
0.2578
0.2669
0.2754
0.2834
0.2912
0.2987
0.3059
0.3130
0.3199
0.3267
0.3333
0.3398
0.3463
0.3526
0.3588
0.1876
—
0.1967
0.2176
0.2356
0.2519
0.2671
0.2815
0.2952
0.3084
0.3212
0.3337
0.3460
0.3580
0.3698
0.3814
0.3929
400 psia (113.82 F)
Sat.
120
140
160
180
200
220
240
260
280
300
320
340
360
380
400
420
u
(Btu/lbm)
111.69
—
113.96
119.37
124.26
128.90
133.41
137.84
142.25
146.64
151.05
155.49
159.95
164.45
169.00
173.60
178.24
122.10
—
124.88
131.45
137.34
142.89
148.24
153.47
158.63
163.77
168.89
174.01
179.16
184.33
189.53
194.77
200.05
0.2317
—
0.2367
0.2483
0.2582
0.2673
0.2758
0.2839
0.2916
0.2991
0.3063
0.3133
0.3202
0.3269
0.3335
0.3399
0.3463
600 psia (146.21 F)
0.2247
0.2297
0.2428
0.2536
0.2632
0.2720
0.2803
0.2882
0.2957
0.3031
0.3102
0.3171
0.3238
0.3305
0.3370
0.3434
0.3496
0.0688
—
—
0.0871
0.1026
0.1146
0.1249
0.1342
0.1427
0.1508
0.1584
0.1657
0.1728
0.1796
0.1863
0.1928
0.1991
106.83
—
—
115.40
122.94
129.11
134.69
139.96
145.05
150.03
154.95
159.83
164.71
169.58
174.47
179.39
184.33
114.47
—
—
125.06
134.33
141.83
148.55
154.85
160.89
166.77
172.53
178.23
183.89
189.52
195.15
200.79
206.44
0.2075
—
—
0.2248
0.2396
0.2511
0.2612
0.2703
0.2788
0.2869
0.2946
0.3020
0.3091
0.3161
0.3229
0.3295
0.3360
.............................................................................................................................
APPENDIX F
ENGLISH UNIT TABLES
TABLE F.10
..............
⑦
871
Thermodynamic Properties of R-134a
TABLE F.10.1
Saturated R-134a
Specific Volume, ft3 /lbm
Internal Energy, Btu/lbm
Temp.
(F)
Press.
(psia)
Sat. Liquid
vf
Evap.
v fg
Sat. Vapor
vg
Sat. Liquid
uf
Evap.
u fg
Sat. Vapor
ug
−100
−90
−80
−70
−60
−50
−40
−30
−20
−15.3
−10
0
10
20
30
40
50
60
70
80
90
100
110
120
130
140
150
160
170
180
190
200
210
214.1
0.951
1.410
2.047
2.913
4.067
5.575
7.511
9.959
13.009
14.696
16.760
21.315
26.787
33.294
40.962
49.922
60.311
72.271
85.954
101.515
119.115
138.926
161.122
185.890
213.425
243.932
277.630
314.758
355.578
400.392
449.572
503.624
563.438
589.953
0.01077
0.01083
0.01091
0.01101
0.01111
0.01122
0.01134
0.01146
0.01159
0.01166
0.01173
0.01187
0.01202
0.01218
0.01235
0.01253
0.01271
0.01291
0.01313
0.01335
0.01360
0.01387
0.01416
0.01448
0.01483
0.01523
0.01568
0.01620
0.01683
0.01760
0.01862
0.02013
0.02334
0.03153
39.5032
27.3236
19.2731
13.8538
10.1389
7.5468
5.7066
4.3785
3.4049
3.0350
2.6805
2.1340
1.7162
1.3928
1.1398
0.9395
0.7794
0.6503
0.5451
0.4588
0.3873
0.3278
0.2777
0.2354
0.1993
0.1684
0.1415
0.1181
0.0974
0.0787
0.0614
0.0444
0.0238
0
39.5139
27.3345
19.2840
13.8648
10.1501
7.5580
5.7179
4.3900
3.4165
3.0466
2.6922
2.1458
1.7282
1.4050
1.1521
0.9520
0.7921
0.6632
0.5582
0.4721
0.4009
0.3416
0.2919
0.2499
0.2142
0.1836
0.1572
0.1343
0.1142
0.0963
0.0801
0.0645
0.0471
0.0315
50.47
52.03
53.96
56.19
58.64
61.27
64.04
66.90
69.83
71.25
72.83
75.88
78.96
82.09
85.25
88.45
91.68
94.95
98.27
101.63
105.04
108.51
112.03
115.62
119.29
123.04
126.89
130.86
134.99
139.32
143.97
149.19
156.18
164.65
94.15
93.89
93.27
92.38
91.26
89.99
88.58
87.09
85.53
84.76
83.91
82.24
80.53
78.78
76.99
75.16
73.27
71.32
69.31
67.22
65.04
62.77
60.38
57.85
55.17
52.30
49.21
45.85
42.12
37.91
32.94
26.59
16.17
0
144.62
145.92
147.24
148.57
149.91
151.26
152.62
153.99
155.36
156.02
156.74
158.12
159.50
160.87
162.24
163.60
164.95
166.28
167.58
168.85
170.09
171.28
172.41
173.48
174.46
175.34
176.11
176.71
177.11
177.23
176.90
175.79
172.34
164.65
⑦
APPENDIX F
..............872
www.elsolucionario.org
ENGLISH UNIT TABLES
.............................................................................................................................
TABLE F.10.1 (continued )
Saturated R-134a
Enthalpy, Btu/lbm
Entropy, Btu/lbm R
Temp.
(F)
Press.
(psia)
Sat. Liquid
hf
Evap.
h fg
Sat. Vapor
hg
Sat. Liquid
sf
Evap.
s fg
Sat. Vapor
sg
−100
−90
−80
−70
−60
−50
−40
−30
−20
−15.3
−10
0
10
20
30
40
50
60
70
80
90
100
110
120
130
140
150
160
170
180
190
200
210
214.1
0.951
1.410
2.047
2.913
4.067
5.575
7.511
9.959
13.009
14.696
16.760
21.315
26.787
33.294
40.962
49.922
60.311
72.271
85.954
101.515
119.115
138.926
161.122
185.890
213.425
243.932
277.630
314.758
355.578
400.392
449.572
503.624
563.438
589.953
50.47
52.04
53.97
56.19
58.65
61.29
64.05
66.92
69.86
71.28
72.87
75.92
79.02
82.16
85.34
88.56
91.82
95.13
98.48
101.88
105.34
108.86
112.46
116.12
119.88
123.73
127.70
131.81
136.09
140.62
145.52
151.07
158.61
168.09
101.10
101.02
100.58
99.85
98.90
97.77
96.52
95.16
93.72
93.02
92.22
90.66
89.04
87.36
85.63
83.83
81.97
80.02
77.98
75.84
73.58
71.19
68.66
65.95
63.04
59.90
56.49
52.73
48.53
43.74
38.05
30.73
18.65
0
151.57
153.05
154.54
156.04
157.55
159.06
160.57
162.08
163.59
164.30
165.09
166.58
168.06
169.53
170.98
172.40
173.79
175.14
176.46
177.72
178.92
180.06
181.11
182.07
182.92
183.63
184.18
184.53
184.63
184.36
183.56
181.80
177.26
168.09
0.1563
0.1605
0.1657
0.1715
0.1777
0.1842
0.1909
0.1976
0.2044
0.2076
0.2111
0.2178
0.2244
0.2310
0.2375
0.2440
0.2504
0.2568
0.2631
0.2694
0.2757
0.2819
0.2882
0.2945
0.3008
0.3071
0.3135
0.3200
0.3267
0.3336
0.3409
0.3491
0.3601
0.3740
0.2811
0.2733
0.2649
0.2562
0.2474
0.2387
0.2300
0.2215
0.2132
0.2093
0.2051
0.1972
0.1896
0.1821
0.1749
0.1678
0.1608
0.1540
0.1472
0.1405
0.1339
0.1272
0.1205
0.1138
0.1069
0.0999
0.0926
0.0851
0.0771
0.0684
0.0586
0.0466
0.0278
0
0.4373
0.4338
0.4306
0.4277
0.4251
0.4229
0.4208
0.4191
0.4175
0.4169
0.4162
0.4150
0.4140
0.4132
0.4124
0.4118
0.4112
0.4108
0.4103
0.4099
0.4095
0.4091
0.4087
0.4082
0.4077
0.4070
0.4061
0.4051
0.4037
0.4020
0.3995
0.3957
0.3879
0.3740
.............................................................................................................................
APPENDIX F
ENGLISH UNIT TABLES
u
(Btu/lbm)
h
(Btu/lbm)
TABLE F.10.2
..............
⑦
873
Superheated R-134a
Temp.
(F)
v
(ft3 /lbm)
u
(Btu/lbm)
h
(Btu/lbm)
s
(Btu/lbm R)
v
(ft3 /lbm)
5 psia (−53.51 F)
Sat.
−20
0
20
40
60
80
100
120
140
160
180
200
220
240
260
280
300
320
8.3676
9.1149
9.5533
9.9881
10.4202
10.8502
11.2786
11.7059
12.1322
12.5578
12.9828
13.4073
13.8314
14.2551
14.6786
15.1019
15.5250
15.9478
16.3706
150.78
156.03
159.27
162.58
165.99
169.48
173.06
176.73
180.49
184.33
188.27
192.29
196.39
200.58
204.86
209.21
213.65
218.17
222.78
158.53
164.47
168.11
171.83
175.63
179.52
183.50
187.56
191.71
195.95
200.28
204.69
209.19
213.77
218.44
223.19
228.02
232.93
237.92
15 psia (−14.44 F)
0.4236
0.4377
0.4458
0.4537
0.4615
0.4691
0.4766
0.4840
0.4913
0.4985
0.5056
0.5126
0.5195
0.5263
0.5331
0.5398
0.5464
0.5530
0.5595
2.9885
—
3.1033
3.2586
3.4109
3.5610
3.7093
3.8563
4.0024
4.1476
4.2922
4.4364
4.5801
4.7234
4.8665
5.0093
5.1519
5.2943
5.4365
30 psia (15.15 F)
Sat.
20
40
60
80
100
120
140
160
180
200
220
240
260
280
300
320
340
360
1.5517
1.5725
1.6559
1.7367
1.8155
1.8929
1.9691
2.0445
2.1192
2.1933
2.2670
2.3403
2.4133
2.4860
2.5585
2.6309
2.7030
2.7750
2.8469
160.21
161.09
164.73
168.41
172.14
175.92
179.77
183.68
187.68
191.74
195.89
200.12
204.42
208.80
213.27
217.81
222.42
227.12
231.89
168.82
169.82
173.93
178.05
182.21
186.43
190.70
195.03
199.44
203.92
208.48
213.11
217.82
222.61
227.47
232.41
237.43
242.53
247.70
s
(Btu/lbm R)
156.13
—
158.58
162.01
165.51
169.07
172.70
176.41
180.20
184.08
188.03
192.07
196.19
200.40
204.68
209.05
213.50
218.03
222.64
164.42
—
167.19
171.06
174.97
178.95
183.00
187.12
191.31
195.59
199.95
204.39
208.91
213.51
218.19
222.96
227.80
232.72
237.73
0.4168
—
0.4229
0.4311
0.4391
0.4469
0.4545
0.4620
0.4694
0.4767
0.4838
0.4909
0.4978
0.5047
0.5115
0.5182
0.5248
0.5314
0.5379
40 psia (28.83 F)
0.4136
0.4157
0.4240
0.4321
0.4400
0.4477
0.4552
0.4625
0.4697
0.4769
0.4839
0.4908
0.4976
0.5044
0.5110
0.5176
0.5241
0.5306
0.5370
1.1787
—
1.2157
1.2796
1.3413
1.4015
1.4604
1.5184
1.5757
1.6324
1.6886
1.7444
1.7999
1.8552
1.9102
1.9650
2.0196
2.0741
2.1285
162.08
—
164.18
167.95
171.74
175.57
179.46
183.41
187.43
191.52
195.69
199.93
204.24
208.64
213.11
217.66
222.28
226.99
231.76
170.81
—
173.18
177.42
181.67
185.95
190.27
194.65
199.09
203.60
208.18
212.84
217.57
222.37
227.25
232.20
237.23
242.34
247.52
0.4125
—
0.4173
0.4256
0.4336
0.4414
0.4490
0.4565
0.4637
0.4709
0.4780
0.4849
0.4918
0.4985
0.5052
0.5118
0.5184
0.5248
0.5312
⑦
APPENDIX F
..............874
www.elsolucionario.org
ENGLISH UNIT TABLES
.............................................................................................................................
TABLE F.10.2 (continued )
Superheated R-134a
Temp.
(F)
v
(ft3 /lbm)
u
(Btu/lbm)
h
(Btu/lbm)
s
(Btu/lbm R)
v
(ft3 /lbm)
60 psia (49.72 F)
Sat.
60
80
100
120
140
160
180
200
220
240
260
280
300
320
340
360
380
400
0.7961
0.8204
0.8657
0.9091
0.9510
0.9918
1.0318
1.0712
1.1100
1.1484
1.1865
1.2243
1.2618
1.2991
1.3362
1.3732
1.4100
1.4468
1.4834
164.91
166.95
170.89
174.85
178.82
182.85
186.92
191.06
195.26
199.54
203.88
208.30
212.79
217.36
222.00
226.71
231.51
236.37
241.31
173.75
176.06
180.51
184.94
189.38
193.86
198.38
202.95
207.59
212.29
217.05
221.89
226.80
231.78
236.83
241.96
247.16
252.43
257.78
0.4794
0.4809
0.5122
0.5414
0.5691
0.5957
0.6215
0.6466
0.6712
0.6954
0.7193
0.7429
0.7663
0.7895
0.8125
0.8353
0.8580
0.8806
168.74
168.93
173.20
177.42
181.62
185.84
190.08
194.38
198.72
203.13
207.60
212.14
216.74
221.42
226.16
230.98
235.87
240.83
177.61
177.83
182.68
187.44
192.15
196.86
201.58
206.34
211.15
216.00
220.91
225.88
230.92
236.03
241.20
246.44
251.75
257.13
h
(Btu/lbm)
s
(Btu/lbm R)
80 psia (65.81 F)
0.4113
0.4157
0.4241
0.4322
0.4400
0.4476
0.4550
0.4623
0.4694
0.4764
0.4833
2.4902
0.4969
0.5035
0.1501
0.5166
0.5230
0.5294
0.5357
0.5996
—
0.6262
0.6617
0.6954
0.7279
0.7595
0.7903
0.8205
0.8503
0.8796
0.9087
0.9375
0.9661
0.9945
1.0227
1.0508
1.0788
1.1066
100 psia (79.08 F)
Sat.
80
100
120
140
160
180
200
220
240
260
280
300
320
340
360
380
400
u
(Btu/lbm)
167.04
—
169.97
174.06
178.15
182.25
186.39
190.58
194.83
199.14
203.51
207.95
212.47
217.05
221.71
226.44
231.24
236.12
241.07
175.91
—
179.24
183.86
188.44
193.03
197.64
202.28
206.98
211.72
216.53
221.41
226.34
231.35
236.43
241.58
246.80
252.09
257.46
0.4105
—
0.4168
0.4252
0.4332
0.4410
0.4485
0.4559
0.4632
0.4702
0.4772
0.4841
0.4909
0.4975
0.5041
0.5107
0.5171
0.5235
0.5298
125 psia (93.09 F)
0.4100
0.4104
0.4192
0.4276
0.4356
0.4433
0.4508
0.4581
0.4653
0.4723
0.4792
0.4861
0.4928
0.4994
0.5060
0.5124
0.5188
0.5252
0.3814
—
0.3910
0.4171
0.4413
0.4642
0.4861
0.5073
0.5278
0.5480
0.5677
0.5872
0.6064
0.6254
0.6442
0.6629
0.6814
0.6998
170.46
—
172.01
176.43
180.77
185.10
189.43
193.79
198.19
202.64
207.15
211.72
216.35
221.05
225.81
230.65
235.56
240.53
179.28
—
181.06
186.08
190.98
195.84
200.68
205.52
210.40
215.32
220.28
225.30
230.38
235.51
240.71
245.98
251.32
256.72
0.4094
—
0.4126
0.4214
0.4297
0.4377
0.4454
0.4529
0.4601
0.4673
0.4743
0.4811
0.4879
0.4946
0.5012
0.5077
0.5141
0.5205
.............................................................................................................................
APPENDIX F
ENGLISH UNIT TABLES
u
(Btu/lbm)
h
(Btu/lbm)
TABLE F.10.2 (continued )
..............
⑦
875
Superheated R-134a
Temp.
(F)
v
(ft3 /lbm)
u
(Btu/lbm)
h
(Btu/lbm)
s
(Btu/lbm R)
v
(ft3 /lbm)
150 psia (105.13 F)
Sat.
120
140
160
180
200
220
240
260
280
300
320
340
360
380
400
0.3150
0.3332
0.3554
0.3761
0.3955
0.4141
0.4321
0.4496
0.4666
0.4833
0.4998
0.5160
0.5320
0.5479
0.5636
0.5792
171.87
175.33
179.85
184.31
188.74
193.18
197.64
202.14
206.69
211.29
215.95
220.67
225.46
230.32
235.24
240.23
180.61
184.57
189.72
194.75
199.72
204.67
209.63
214.62
219.64
224.70
229.82
235.00
240.23
245.52
250.88
256.31
200 psia (125.25 F)
0.4089
0.4159
0.4246
0.4328
0.4407
0.4484
0.4558
0.4630
0.4701
0.4770
0.4838
0.4906
0.4972
0.5037
0.5102
0.5166
0.2304
—
0.2459
0.2645
0.2814
0.2971
0.3120
0.3262
0.3400
0.3534
0.3664
0.3792
0.3918
0.4042
0.4165
0.4286
250 psia (141.87 F)
Sat.
160
180
200
220
240
260
280
300
320
340
360
380
400
0.1783
0.1955
0.2117
0.2261
0.2394
0.2519
0.2638
0.2752
0.2863
0.2971
0.3076
0.3180
0.3282
0.3382
175.50
180.42
185.49
190.38
195.18
199.94
204.70
209.47
214.27
219.12
224.01
228.95
233.95
239.01
183.75
189.46
195.28
200.84
206.26
211.60
216.90
222.21
227.52
232.86
238.24
243.66
249.13
254.65
s
(Btu/lbm R)
174.00
—
177.72
182.54
187.23
191.86
196.46
201.08
205.72
210.40
215.13
219.91
224.74
229.64
234.60
239.62
182.53
—
186.82
192.33
197.64
202.85
208.01
213.15
218.31
223.48
228.69
233.94
239.24
244.60
250.01
255.48
0.4080
—
0.4152
0.4242
0.4327
0.4407
0.4484
0.4559
0.4631
0.4702
0.4772
0.4840
0.4907
0.4973
0.5038
0.5103
300 psia (156.14 F)
0.4068
0.4162
0.4255
0.4340
0.4421
0.4498
0.4573
0.4646
0.4717
0.4786
0.4854
0.4921
0.4987
0.5052
0.1428
0.1467
0.1637
0.1779
0.1905
0.2020
0.2128
0.2230
0.2328
0.2423
0.2515
0.2605
0.2693
0.2779
176.50
177.70
183.44
188.71
193.77
198.72
203.62
208.50
213.39
218.30
223.25
228.24
233.29
238.38
184.43
185.84
192.53
198.59
204.35
209.93
215.43
220.88
226.31
231.75
237.21
242.70
248.24
253.81
0.4055
0.4078
0.4184
0.4278
0.4364
0.4445
0.4522
0.4597
0.4669
0.4740
0.4809
0.4877
0.4944
0.5009
⑦
APPENDIX F
..............876
www.elsolucionario.org
ENGLISH UNIT TABLES
.............................................................................................................................
TABLE F.10.2 (continued )
Superheated R-134a
Temp.
(F)
v
(ft3 /lbm)
u
(Btu/lbm)
h
(Btu/lbm)
s
(Btu/lbm R)
v
(ft3 /lbm)
400 psia (179.92 F)
Sat.
180
200
220
240
260
280
300
320
340
360
380
400
0.0965
0.0966
0.1146
0.1277
0.1386
0.1484
0.1573
0.1657
0.1737
0.1813
0.1886
0.1957
0.2027
177.23
177.26
184.44
190.41
195.92
201.21
206.38
211.49
216.58
221.68
226.79
231.93
237.12
184.37
184.41
192.92
199.86
206.19
212.20
218.03
223.76
229.44
235.09
240.75
246.42
252.12
u
(Btu/lbm)
0.01640
0.01786
0.02069
0.03426
0.05166
0.06206
0.06997
0.07662
0.08250
0.08786
0.09284
0.09753
136.22
144.85
155.27
173.83
187.78
196.16
203.08
209.37
215.33
221.11
226.78
232.39
138.49
147.32
158.14
178.58
194.95
204.77
212.79
220.00
226.78
233.30
239.66
245.92
s
(Btu/lbm R)
500 psia (199.36 F)
0.4020
0.4020
0.4152
0.4255
0.4347
0.4432
0.4512
0.4588
0.4662
0.4733
0.4803
0.4872
0.4939
0.0655
—
0.0666
0.0867
0.0990
0.1089
0.1174
0.1252
0.1323
0.1390
0.1454
0.1516
0.1575
175.90
—
176.38
185.78
192.46
198.40
204.00
209.41
214.74
220.01
225.27
230.53
235.82
750 psia
180
200
220
240
260
280
300
320
340
360
380
400
h
(Btu/lbm)
181.96
—
182.54
193.80
201.62
208.47
214.86
220.99
226.98
232.87
238.73
244.56
250.39
0.3960
—
0.3969
0.4137
0.4251
0.4347
0.4435
0.4517
0.4594
0.4669
0.4741
0.4812
0.4880
1000 psia
0.3285
0.3421
0.3583
0.3879
0.4110
0.4244
0.4351
0.4445
0.4531
0.4611
0.4688
0.4762
0.01593
0.01700
0.01851
0.02102
0.02603
0.0341
0.04208
0.04875
0.05441
0.05938
0.06385
0.06797
134.77
142.70
151.26
160.95
172.59
184.70
194.58
202.67
209.79
216.36
222.61
228.67
137.71
145.84
154.69
164.84
177.40
191.01
202.37
211.69
219.86
227.35
234.43
241.25
0.3262
0.3387
0.3519
0.3666
0.3843
0.4029
0.4181
0.4302
0.4406
0.4498
0.4583
0.4664
.............................................................................................................................
APPENDIX F
ENGLISH UNIT TABLES
TABLE F.11
..............
⑦
877
Enthalpy of Formation and Absolute Entropy of Various Substances at 77 F, 1 atm Pressure
Substance
Formula
M
lbm/lbmol
Acetylene
Ammonia
Benzene
Carbon dioxide
Carbon (graphite)
Carbon monoxide
Ethanol
Ethanol
Ethane
Ethene
Heptane
Hexane
Hydrogen peroxide
Methane
Methanol
Methanol
n-Butane
Nitrogen oxide
Nitromethane
n-Octane
n-Octane
Ozone
Pentane
Propane
Propene
Sulfur
Sulfur dioxide
Sulfur trioxide
T-T-Diesel
Water
Water
C2 H2
NH3
C6 H6
CO2
C
CO
C2 H5 OH
C2 H5 OH
C2 H6
C2 H4
C7 H16
C6 H14
H2 O2
CH4
CH3 OH
CH3 OH
C4 H10
N2 O
CH3 NO2
C8 H18
C8 H18
O3
C5 H12
C3 H8
C3 H6
S
SO2
SO3
C14.4 H24.9
H2 O
H2 O
26.038
17.031
78.114
44.010
12.011
28.011
46.069
46.069
30.070
28.054
100.205
86.178
34.015
16.043
32.042
32.042
58.124
44.013
61.04
114.232
114.232
47.998
72.151
44.094
42.081
32.06
64.059
80.058
198.06
18.015
18.015
0
State
gas
gas
gas
gas
solid
gas
gas
liq
gas
gas
gas
gas
gas
gas
gas
liq
gas
gas
liq
gas
liq
gas
gas
gas
gas
solid
gas
gas
liq
gas
liq
h̄ f
Btu/lbmol
s̄ 0f
Btu/lbmol R
+97 477
−19 656
+35 675
−169 184
0
−47 518
−101 032
−119 252
−36 432
+22 557
−80 782
−71 926
−58 515
−32 190
−86 543
−102 846
−54 256
+35 275
−48 624
−89 682
−107 526
+61 339
−62 984
−44 669
+8 783
0
−127 619
−170 148
−74 807
−103 966
−122 885
47.972
45.969
64.358
51.038
1.371
47.182
67.434
38.321
54.812
52.360
102.153
92.641
55.623
44.459
57.227
30.261
73.215
52.510
41.034
111.399
86.122
57.042
83.318
64.442
63.761
7.656
59.258
61.302
125.609
45.076
16.707