Index to Tables in SI Units
TABLE A-1
TABLE A-2
TABLE A-3
TABLE A-4
TABLE A-5
TABLE A-6
TABLE A-7
TABLE A-8
TABLE A-9
TABLE A-10
TABLE A-11
TABLE A-12
TABLE A-13
TABLE A-14
TABLE A-15
TABLE A-16
TABLE A-17
TABLE A-18
TABLE A-19
TABLE A-20
TABLE A-21
TABLE A-22
TABLE A-23
TABLE A-24
TABLE A-25
TABLE A-26
Copyright © 2006. Wiley. All rights reserved.
TABLE A-27
Atomic or Molecular Weights and Critical Properties of Selected Elements and Compounds
Properties of Saturated Water (Liquid–Vapor): Temperature Table
Properties of Saturated Water (Liquid–Vapor): Pressure Table
Properties of Superheated Water Vapor
Properties of Compressed Liquid Water
Properties of Saturated Water (Solid–Vapor): Temperature Table
Properties of Saturated Refrigerant 22 (Liquid–Vapor): Temperature Table
Properties of Saturated Refrigerant 22 (Liquid–Vapor): Pressure Table
Properties of Superheated Refrigerant 22 Vapor
Properties of Saturated Refrigerant 134a (Liquid–Vapor): Temperature Table
Properties of Saturated Refrigerant 134a (Liquid–Vapor): Pressure Table
Properties of Superheated Refrigerant 134a Vapor
Properties of Saturated Ammonia (Liquid–Vapor): Temperature Table
Properties of Saturated Ammonia (Liquid–Vapor): Pressure Table
Properties of Superheated Ammonia Vapor
Properties of Saturated Propane (Liquid–Vapor): Temperature Table
Properties of Saturated Propane (Liquid–Vapor): Pressure Table
Properties of Superheated Propane Vapor
Properties of Selected Solids and Liquids: cp, , and .
Ideal Gas Specific Heats of Some Common Gases
Variation of cp with Temperature for Selected Ideal Gases
Ideal Gas Properties of Air
Ideal Gas Properties of Selected Gases
Constants for the van der Waals, Redlich–Kwong, and Benedict–Webb–Rubin Equations
of State
Thermochemical Properties of Selected Substances at 298 K and 1 atm
Standard Molar Chemical Exergy, e ch (kJ/kmol), of Selected Substances at 298 K and p0
Logarithms to the Base 10 of the Equilibrium Constant K
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
718
719
720
722
724
728
729
730
731
732
736
737
738
741
742
743
747
748
749
753
754
755
756
758
762
763
764
765
Atomic or Molecular Weights and Critical Properties of Selected
Elements and Compounds
TABLE A-1
pcvc
RTc
M
(kg/kmol)
Tc
(K)
pc
(bar)
C2H2
—
NH3
26.04
28.97
17.03
309
133
406
62.8
37.7
112.8
0.274
0.284
0.242
Argon
Benzene
Butane
Ar
C6H6
C4H10
39.94
78.11
58.12
151
563
425
48.6
49.3
38.0
0.290
0.274
0.274
Carbon
Carbon dioxide
Carbon monoxide
C
CO2
CO
12.01
44.01
28.01
—
304
133
—
73.9
35.0
—
0.276
0.294
Copper
Ethane
Ethyl alcohol
Cu
C2H6
C2H5OH
63.54
30.07
46.07
—
305
516
—
48.8
63.8
—
0.285
0.249
Ethylene
Helium
Hydrogen
C2H4
He
H2
28.05
4.003
2.016
283
5.2
33.2
51.2
2.3
13.0
0.270
0.300
0.304
Methane
Methyl alcohol
Nitrogen
CH4
CH3OH
N2
16.04
32.04
28.01
191
513
126
46.4
79.5
33.9
0.290
0.220
0.291
Octane
Oxygen
Propane
C8H18
O2
C3H8
114.22
32.00
44.09
569
154
370
24.9
50.5
42.7
0.258
0.290
0.276
Propylene
Refrigerant 12
Refrigerant 22
C3H6
CCl2F2
CHClF2
42.08
120.92
86.48
365
385
369
46.2
41.2
49.8
0.276
0.278
0.267
Refrigerant 134a
Sulfur dioxide
Water
CF3CH2F
SO2
H2O
102.03
64.06
18.02
374
431
647.3
40.7
78.7
220.9
0.260
0.268
0.233
Substance
Chemical
Formula
Acetylene
Air (equivalent)
Ammonia
Zc Copyright © 2006. Wiley. All rights reserved.
Sources: Adapted from International Critical Tables and L. C. Nelson and E. F. Obert, Generalized Compressibility
Charts, Chem. Eng., 61: 203 (1954).
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
719
Table A-1
Tables in SI Units
720
Tables in SI Units
TABLE A-2
Properties of Saturated Water (Liquid–Vapor): Temperature Table
Copyright © 2006. Wiley. All rights reserved.
H2O
Specific Volume
m3/kg
Internal Energy
kJ/kg
Enthalpy
kJ/kg
Entropy
kJ/kg # K
Temp.
C
Press.
bar
Sat.
Liquid
vf 103
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Temp.
C
.01
4
5
6
8
0.00611
0.00813
0.00872
0.00935
0.01072
1.0002
1.0001
1.0001
1.0001
1.0002
206.136
157.232
147.120
137.734
120.917
0.00
16.77
20.97
25.19
33.59
2375.3
2380.9
2382.3
2383.6
2386.4
0.01
16.78
20.98
25.20
33.60
2501.3
2491.9
2489.6
2487.2
2482.5
2501.4
2508.7
2510.6
2512.4
2516.1
0.0000
0.0610
0.0761
0.0912
0.1212
9.1562
9.0514
9.0257
9.0003
8.9501
.01
4
5
6
8
10
11
12
13
14
0.01228
0.01312
0.01402
0.01497
0.01598
1.0004
1.0004
1.0005
1.0007
1.0008
106.379
99.857
93.784
88.124
82.848
42.00
46.20
50.41
54.60
58.79
2389.2
2390.5
2391.9
2393.3
2394.7
42.01
46.20
50.41
54.60
58.80
2477.7
2475.4
2473.0
2470.7
2468.3
2519.8
2521.6
2523.4
2525.3
2527.1
0.1510
0.1658
0.1806
0.1953
0.2099
8.9008
8.8765
8.8524
8.8285
8.8048
10
11
12
13
14
15
16
17
18
19
0.01705
0.01818
0.01938
0.02064
0.02198
1.0009
1.0011
1.0012
1.0014
1.0016
77.926
73.333
69.044
65.038
61.293
62.99
67.18
71.38
75.57
79.76
2396.1
2397.4
2398.8
2400.2
2401.6
62.99
67.19
71.38
75.58
79.77
2465.9
2463.6
2461.2
2458.8
2456.5
2528.9
2530.8
2532.6
2534.4
2536.2
0.2245
0.2390
0.2535
0.2679
0.2823
8.7814
8.7582
8.7351
8.7123
8.6897
15
16
17
18
19
20
21
22
23
24
0.02339
0.02487
0.02645
0.02810
0.02985
1.0018
1.0020
1.0022
1.0024
1.0027
57.791
54.514
51.447
48.574
45.883
83.95
88.14
92.32
96.51
100.70
2402.9
2404.3
2405.7
2407.0
2408.4
83.96
88.14
92.33
96.52
100.70
2454.1
2451.8
2449.4
2447.0
2444.7
2538.1
2539.9
2541.7
2543.5
2545.4
0.2966
0.3109
0.3251
0.3393
0.3534
8.6672
8.6450
8.6229
8.6011
8.5794
20
21
22
23
24
25
26
27
28
29
0.03169
0.03363
0.03567
0.03782
0.04008
1.0029
1.0032
1.0035
1.0037
1.0040
43.360
40.994
38.774
36.690
34.733
104.88
109.06
113.25
117.42
121.60
2409.8
2411.1
2412.5
2413.9
2415.2
104.89
109.07
113.25
117.43
121.61
2442.3
2439.9
2437.6
2435.2
2432.8
2547.2
2549.0
2550.8
2552.6
2554.5
0.3674
0.3814
0.3954
0.4093
0.4231
8.5580
8.5367
8.5156
8.4946
8.4739
25
26
27
28
29
30
31
32
33
34
0.04246
0.04496
0.04759
0.05034
0.05324
1.0043
1.0046
1.0050
1.0053
1.0056
32.894
31.165
29.540
28.011
26.571
125.78
129.96
134.14
138.32
142.50
2416.6
2418.0
2419.3
2420.7
2422.0
125.79
129.97
134.15
138.33
142.50
2430.5
2428.1
2425.7
2423.4
2421.0
2556.3
2558.1
2559.9
2561.7
2563.5
0.4369
0.4507
0.4644
0.4781
0.4917
8.4533
8.4329
8.4127
8.3927
8.3728
30
31
32
33
34
35
36
38
40
45
0.05628
0.05947
0.06632
0.07384
0.09593
1.0060
1.0063
1.0071
1.0078
1.0099
25.216
23.940
21.602
19.523
15.258
146.67
150.85
159.20
167.56
188.44
2423.4
2424.7
2427.4
2430.1
2436.8
146.68
150.86
159.21
167.57
188.45
2418.6
2416.2
2411.5
2406.7
2394.8
2565.3
2567.1
2570.7
2574.3
2583.2
0.5053
0.5188
0.5458
0.5725
0.6387
8.3531
8.3336
8.2950
8.2570
8.1648
35
36
38
40
45
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in SI Units
(Continued)
Copyright © 2006. Wiley. All rights reserved.
Specific Volume
m3/kg
Internal Energy
kJ/kg
Enthalpy
kJ/kg
Entropy
kJ/kg # K
Temp.
C
Press.
bar
Sat.
Liquid
vf 103
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Temp.
C
50
55
60
65
70
.1235
.1576
.1994
.2503
.3119
1.0121
1.0146
1.0172
1.0199
1.0228
12.032
9.568
7.671
6.197
5.042
209.32
230.21
251.11
272.02
292.95
2443.5
2450.1
2456.6
2463.1
2469.6
209.33
230.23
251.13
272.06
292.98
2382.7
2370.7
2358.5
2346.2
2333.8
2592.1
2600.9
2609.6
2618.3
2626.8
.7038
.7679
.8312
.8935
.9549
8.0763
7.9913
7.9096
7.8310
7.7553
50
55
60
65
70
75
80
85
90
95
.3858
.4739
.5783
.7014
.8455
1.0259
1.0291
1.0325
1.0360
1.0397
4.131
3.407
2.828
2.361
1.982
313.90
334.86
355.84
376.85
397.88
2475.9
2482.2
2488.4
2494.5
2500.6
313.93
334.91
355.90
376.92
397.96
2321.4
2308.8
2296.0
2283.2
2270.2
2635.3
2643.7
2651.9
2660.1
2668.1
1.0155
1.0753
1.1343
1.1925
1.2500
7.6824
7.6122
7.5445
7.4791
7.4159
75
80
85
90
95
100
110
120
130
140
1.014
1.433
1.985
2.701
3.613
1.0435
1.0516
1.0603
1.0697
1.0797
1.673
1.210
0.8919
0.6685
0.5089
418.94
461.14
503.50
546.02
588.74
2506.5
2518.1
2529.3
2539.9
2550.0
419.04
461.30
503.71
546.31
589.13
2257.0
2230.2
2202.6
2174.2
2144.7
2676.1
2691.5
2706.3
2720.5
2733.9
1.3069
1.4185
1.5276
1.6344
1.7391
7.3549
7.2387
7.1296
7.0269
6.9299
100
110
120
130
140
150
160
170
180
190
4.758
6.178
7.917
10.02
12.54
1.0905
1.1020
1.1143
1.1274
1.1414
0.3928
0.3071
0.2428
0.1941
0.1565
631.68
674.86
718.33
762.09
806.19
2559.5
2568.4
2576.5
2583.7
2590.0
632.20
675.55
719.21
763.22
807.62
2114.3
2082.6
2049.5
2015.0
1978.8
2746.5
2758.1
2768.7
2778.2
2786.4
1.8418
1.9427
2.0419
2.1396
2.2359
6.8379
6.7502
6.6663
6.5857
6.5079
150
160
170
180
190
200
210
220
230
240
15.54
19.06
23.18
27.95
33.44
1.1565
1.1726
1.1900
1.2088
1.2291
0.1274
0.1044
0.08619
0.07158
0.05976
850.65
895.53
940.87
986.74
1033.2
2595.3
2599.5
2602.4
2603.9
2604.0
852.45
897.76
943.62
990.12
1037.3
1940.7
1900.7
1858.5
1813.8
1766.5
2793.2
2798.5
2802.1
2804.0
2803.8
2.3309
2.4248
2.5178
2.6099
2.7015
6.4323
6.3585
6.2861
6.2146
6.1437
200
210
220
230
240
250
260
270
280
290
39.73
46.88
54.99
64.12
74.36
1.2512
1.2755
1.3023
1.3321
1.3656
0.05013
0.04221
0.03564
0.03017
0.02557
1080.4
1128.4
1177.4
1227.5
1278.9
2602.4
2599.0
2593.7
2586.1
2576.0
1085.4
1134.4
1184.5
1236.0
1289.1
1716.2
1662.5
1605.2
1543.6
1477.1
2801.5
2796.6
2789.7
2779.6
2766.2
2.7927
2.8838
2.9751
3.0668
3.1594
6.0730
6.0019
5.9301
5.8571
5.7821
250
260
270
280
290
300
320
340
360
374.14
85.81
112.7
145.9
186.5
220.9
1.4036
1.4988
1.6379
1.8925
3.155
0.02167
0.01549
0.01080
0.006945
0.003155
1332.0
1444.6
1570.3
1725.2
2029.6
2563.0
2525.5
2464.6
2351.5
2029.6
1344.0
1461.5
1594.2
1760.5
2099.3
1404.9
1238.6
1027.9
720.5
0
2749.0
2700.1
2622.0
2481.0
2099.3
3.2534
3.4480
3.6594
3.9147
4.4298
5.7045
5.5362
5.3357
5.0526
4.4298
300
320
340
360
374.14
Source: Tables A-2 through A-5 are extracted from J. H. Keenan, F. G. Keyes, P. G. Hill, and J. G. Moore, Steam Tables, Wiley, New York, 1969.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
H2O
TABLE A-2
721
722
Tables in SI Units
TABLE A-3
Properties of Saturated Water (Liquid–Vapor): Pressure Table
Copyright © 2006. Wiley. All rights reserved.
H2O
Specific Volume
m3/kg
Internal Energy
kJ/kg
Enthalpy
kJ/kg
Entropy
kJ/kg # K
Press.
bar
Temp.
C
Sat.
Liquid
vf 103
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Press.
bar
0.04
0.06
0.08
0.10
0.20
28.96
36.16
41.51
45.81
60.06
1.0040
1.0064
1.0084
1.0102
1.0172
34.800
23.739
18.103
14.674
7.649
121.45
151.53
173.87
191.82
251.38
2415.2
2425.0
2432.2
2437.9
2456.7
121.46
151.53
173.88
191.83
251.40
2432.9
2415.9
2403.1
2392.8
2358.3
2554.4
2567.4
2577.0
2584.7
2609.7
0.4226
0.5210
0.5926
0.6493
0.8320
8.4746
8.3304
8.2287
8.1502
7.9085
0.04
0.06
0.08
0.10
0.20
0.30
0.40
0.50
0.60
0.70
69.10
75.87
81.33
85.94
89.95
1.0223
1.0265
1.0300
1.0331
1.0360
5.229
3.993
3.240
2.732
2.365
289.20
317.53
340.44
359.79
376.63
2468.4
2477.0
2483.9
2489.6
2494.5
289.23
317.58
340.49
359.86
376.70
2336.1
2319.2
2305.4
2293.6
2283.3
2625.3
2636.8
2645.9
2653.5
2660.0
0.9439
1.0259
1.0910
1.1453
1.1919
7.7686
7.6700
7.5939
7.5320
7.4797
0.30
0.40
0.50
0.60
0.70
0.80
0.90
1.00
1.50
2.00
93.50
96.71
99.63
111.4
120.2
1.0380
1.0410
1.0432
1.0528
1.0605
2.087
1.869
1.694
1.159
0.8857
391.58
405.06
417.36
466.94
504.49
2498.8
2502.6
2506.1
2519.7
2529.5
391.66
405.15
417.46
467.11
504.70
2274.1
2265.7
2258.0
2226.5
2201.9
2665.8
2670.9
2675.5
2693.6
2706.7
1.2329
1.2695
1.3026
1.4336
1.5301
7.4346
7.3949
7.3594
7.2233
7.1271
0.80
0.90
1.00
1.50
2.00
2.50
3.00
3.50
4.00
4.50
127.4
133.6
138.9
143.6
147.9
1.0672
1.0732
1.0786
1.0836
1.0882
0.7187
0.6058
0.5243
0.4625
0.4140
535.10
561.15
583.95
604.31
622.25
2537.2
2543.6
2546.9
2553.6
2557.6
535.37
561.47
584.33
604.74
623.25
2181.5
2163.8
2148.1
2133.8
2120.7
2716.9
2725.3
2732.4
2738.6
2743.9
1.6072
1.6718
1.7275
1.7766
1.8207
7.0527
6.9919
6.9405
6.8959
6.8565
2.50
3.00
3.50
4.00
4.50
5.00
6.00
7.00
8.00
9.00
151.9
158.9
165.0
170.4
175.4
1.0926
1.1006
1.1080
1.1148
1.1212
0.3749
0.3157
0.2729
0.2404
0.2150
639.68
669.90
696.44
720.22
741.83
2561.2
2567.4
2572.5
2576.8
2580.5
640.23
670.56
697.22
721.11
742.83
2108.5
2086.3
2066.3
2048.0
2031.1
2748.7
2756.8
2763.5
2769.1
2773.9
1.8607
1.9312
1.9922
2.0462
2.0946
6.8212
6.7600
6.7080
6.6628
6.6226
5.00
6.00
7.00
8.00
9.00
10.0
15.0
20.0
25.0
30.0
179.9
198.3
212.4
224.0
233.9
1.1273
1.1539
1.1767
1.1973
1.2165
0.1944
0.1318
0.09963
0.07998
0.06668
761.68
843.16
906.44
959.11
1004.8
2583.6
2594.5
2600.3
2603.1
2604.1
762.81
844.84
908.79
962.11
1008.4
2015.3
1947.3
1890.7
1841.0
1795.7
2778.1
2792.2
2799.5
2803.1
2804.2
2.1387
2.3150
2.4474
2.5547
2.6457
6.5863
6.4448
6.3409
6.2575
6.1869
10.0
15.0
20.0
25.0
30.0
35.0
40.0
45.0
50.0
60.0
242.6
250.4
257.5
264.0
275.6
1.2347
1.2522
1.2692
1.2859
1.3187
0.05707
0.04978
0.04406
0.03944
0.03244
1045.4
1082.3
1116.2
1147.8
1205.4
2603.7
2602.3
2600.1
2597.1
2589.7
1049.8
1087.3
1121.9
1154.2
1213.4
1753.7
1714.1
1676.4
1640.1
1571.0
2803.4
2801.4
2798.3
2794.3
2784.3
2.7253
2.7964
2.8610
2.9202
3.0267
6.1253
6.0701
6.0199
5.9734
5.8892
35.0
40.0
45.0
50.0
60.0
70.0
80.0
90.0
100.
110.
285.9
295.1
303.4
311.1
318.2
1.3513
1.3842
1.4178
1.4524
1.4886
0.02737
0.02352
0.02048
0.01803
0.01599
1257.6
1305.6
1350.5
1393.0
1433.7
2580.5
2569.8
2557.8
2544.4
2529.8
1267.0
1316.6
1363.3
1407.6
1450.1
1505.1
1441.3
1378.9
1317.1
1255.5
2772.1
2758.0
2742.1
2724.7
2705.6
3.1211
3.2068
3.2858
3.3596
3.4295
5.8133
5.7432
5.6772
5.6141
5.5527
70.0
80.0
90.0
100.
110.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in SI Units
(Continued)
Specific Volume
m3/kg
Internal Energy
kJ/kg
Enthalpy
kJ/kg
Entropy
kJ/kg # K
Temp.
C
Sat.
Liquid
vf 103
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Press.
bar
120.
130.
140.
150.
160.
324.8
330.9
336.8
342.2
347.4
1.5267
1.5671
1.6107
1.6581
1.7107
0.01426
0.01278
0.01149
0.01034
0.009306
1473.0
1511.1
1548.6
1585.6
1622.7
2513.7
2496.1
2476.8
2455.5
2431.7
1491.3
1531.5
1571.1
1610.5
1650.1
1193.6
1130.7
1066.5
1000.0
930.6
2684.9
2662.2
2637.6
2610.5
2580.6
3.4962
3.5606
3.6232
3.6848
3.7461
5.4924
5.4323
5.3717
5.3098
5.2455
120.
130.
140.
150.
160.
170.
180.
190.
200.
220.9
352.4
357.1
361.5
365.8
374.1
1.7702
1.8397
1.9243
2.036
3.155
0.008364
0.007489
0.006657
0.005834
0.003155
1660.2
1698.9
1739.9
1785.6
2029.6
2405.0
2374.3
2338.1
2293.0
2029.6
1690.3
1732.0
1776.5
1826.3
2099.3
856.9
777.1
688.0
583.4
0
2547.2
2509.1
2464.5
2409.7
2099.3
3.8079
3.8715
3.9388
4.0139
4.4298
5.1777
5.1044
5.0228
4.9269
4.4298
170.
180.
190.
200.
220.9
Copyright © 2006. Wiley. All rights reserved.
Press.
bar
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
H2O
TABLE A-3
723
724
Tables in SI Units
Properties of Superheated Water Vapor
TABLE A-4
T
C
v
m3/kg
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
H2O
p 0.06 bar 0.006 MPa
(Tsat 36.16C)
v
m3/kg
h
kJ/kg
s
kJ/kg # K
p 0.35 bar 0.035 MPa
(Tsat 72.69C)
Sat.
80
120
23.739
27.132
30.219
2425.0
2487.3
2544.7
2567.4
2650.1
2726.0
8.3304
8.5804
8.7840
4.526
4.625
5.163
2473.0
2483.7
2542.4
2631.4
2645.6
2723.1
7.7158
7.7564
7.9644
160
200
240
33.302
36.383
39.462
2602.7
2661.4
2721.0
2802.5
2879.7
2957.8
8.9693
9.1398
9.2982
5.696
6.228
6.758
2601.2
2660.4
2720.3
2800.6
2878.4
2956.8
8.1519
8.3237
8.4828
280
320
360
42.540
45.618
48.696
2781.5
2843.0
2905.5
3036.8
3116.7
3197.7
9.4464
9.5859
9.7180
7.287
7.815
8.344
2780.9
2842.5
2905.1
3036.0
3116.1
3197.1
8.6314
8.7712
8.9034
400
440
500
51.774
54.851
59.467
2969.0
3033.5
3132.3
3279.6
3362.6
3489.1
9.8435
9.9633
10.1336
8.872
9.400
10.192
2968.6
3033.2
3132.1
3279.2
3362.2
3488.8
9.0291
9.1490
9.3194
p 0.70 bar 0.07 MPa
(Tsat 89.95C)
Copyright © 2006. Wiley. All rights reserved.
u
kJ/kg
p 1.0 bar 0.10 MPa
(Tsat 99.63C)
Sat.
100
120
2.365
2.434
2.571
2494.5
2509.7
2539.7
2660.0
2680.0
2719.6
7.4797
7.5341
7.6375
1.694
1.696
1.793
2506.1
2506.7
2537.3
2675.5
2676.2
2716.6
7.3594
7.3614
7.4668
160
200
240
2.841
3.108
3.374
2599.4
2659.1
2719.3
2798.2
2876.7
2955.5
7.8279
8.0012
8.1611
1.984
2.172
2.359
2597.8
2658.1
2718.5
2796.2
2875.3
2954.5
7.6597
7.8343
7.9949
280
320
360
3.640
3.905
4.170
2780.2
2842.0
2904.6
3035.0
3115.3
3196.5
8.3162
8.4504
8.5828
2.546
2.732
2.917
2779.6
2841.5
2904.2
3034.2
3114.6
3195.9
8.1445
8.2849
8.4175
400
440
500
4.434
4.698
5.095
2968.2
3032.9
3131.8
3278.6
3361.8
3488.5
8.7086
8.8286
8.9991
3.103
3.288
3.565
2967.9
3032.6
3131.6
3278.2
3361.4
3488.1
8.5435
8.6636
8.8342
p 1.5 bar 0.15 MPa
(Tsat 111.37C)
p 3.0 bar 0.30 MPa
(Tsat 133.55C)
Sat.
120
160
1.159
1.188
1.317
2519.7
2533.3
2595.2
2693.6
2711.4
2792.8
7.2233
7.2693
7.4665
0.606
2543.6
2725.3
6.9919
0.651
2587.1
2782.3
7.1276
200
240
280
1.444
1.570
1.695
2656.2
2717.2
2778.6
2872.9
2952.7
3032.8
7.6433
7.8052
7.9555
0.716
0.781
0.844
2650.7
2713.1
2775.4
2865.5
2947.3
3028.6
7.3115
7.4774
7.6299
320
360
400
1.819
1.943
2.067
2840.6
2903.5
2967.3
3113.5
3195.0
3277.4
8.0964
8.2293
8.3555
0.907
0.969
1.032
2838.1
2901.4
2965.6
3110.1
3192.2
3275.0
7.7722
7.9061
8.0330
440
500
600
2.191
2.376
2.685
3032.1
3131.2
3301.7
3360.7
3487.6
3704.3
8.4757
8.6466
8.9101
1.094
1.187
1.341
3030.6
3130.0
3300.8
3358.7
3486.0
3703.2
8.1538
8.3251
8.5892
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in SI Units
(Continued)
v
m3/kg
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
v
m3/kg
p 5.0 bar 0.50 MPa
(Tsat 151.86C)
h
kJ/kg
s
kJ/kg # K
p 7.0 bar 0.70 MPa
(Tsat 164.97C)
Sat.
180
200
0.3749
0.4045
0.4249
2561.2
2609.7
2642.9
2748.7
2812.0
2855.4
6.8213
6.9656
7.0592
0.2729
0.2847
0.2999
2572.5
2599.8
2634.8
2763.5
2799.1
2844.8
6.7080
6.7880
6.8865
240
280
320
0.4646
0.5034
0.5416
2707.6
2771.2
2834.7
2939.9
3022.9
3105.6
7.2307
7.3865
7.5308
0.3292
0.3574
0.3852
2701.8
2766.9
2831.3
2932.2
3017.1
3100.9
7.0641
7.2233
7.3697
360
400
440
0.5796
0.6173
0.6548
2898.7
2963.2
3028.6
3188.4
3271.9
3356.0
7.6660
7.7938
7.9152
0.4126
0.4397
0.4667
2895.8
2960.9
3026.6
3184.7
3268.7
3353.3
7.5063
7.6350
7.7571
500
600
700
0.7109
0.8041
0.8969
3128.4
3299.6
3477.5
3483.9
3701.7
3925.9
8.0873
8.3522
8.5952
0.5070
0.5738
0.6403
3126.8
3298.5
3476.6
3481.7
3700.2
3924.8
7.9299
8.1956
8.4391
p 10.0 bar 1.0 MPa
(Tsat 179.91C)
Copyright © 2006. Wiley. All rights reserved.
u
kJ/kg
p 15.0 bar 1.5 MPa
(Tsat 198.32C)
Sat.
200
240
0.1944
0.2060
0.2275
2583.6
2621.9
2692.9
2778.1
2827.9
2920.4
6.5865
6.6940
6.8817
0.1318
0.1325
0.1483
2594.5
2598.1
2676.9
2792.2
2796.8
2899.3
6.4448
6.4546
6.6628
280
320
360
0.2480
0.2678
0.2873
2760.2
2826.1
2891.6
3008.2
3093.9
3178.9
7.0465
7.1962
7.3349
0.1627
0.1765
0.1899
2748.6
2817.1
2884.4
2992.7
3081.9
3169.2
6.8381
6.9938
7.1363
400
440
500
0.3066
0.3257
0.3541
2957.3
3023.6
3124.4
3263.9
3349.3
3478.5
7.4651
7.5883
7.7622
0.2030
0.2160
0.2352
2951.3
3018.5
3120.3
3255.8
3342.5
3473.1
7.2690
7.3940
7.5698
540
600
640
0.3729
0.4011
0.4198
3192.6
3296.8
3367.4
3565.6
3697.9
3787.2
7.8720
8.0290
8.1290
0.2478
0.2668
0.2793
3189.1
3293.9
3364.8
3560.9
3694.0
3783.8
7.6805
7.8385
7.9391
p 20.0 bar 2.0 MPa
(Tsat 212.42C)
p 30.0 bar 3.0 MPa
(Tsat 233.90C)
Sat.
240
280
0.0996
0.1085
0.1200
2600.3
2659.6
2736.4
2799.5
2876.5
2976.4
6.3409
6.4952
6.6828
0.0667
0.0682
0.0771
2604.1
2619.7
2709.9
2804.2
2824.3
2941.3
6.1869
6.2265
6.4462
320
360
400
0.1308
0.1411
0.1512
2807.9
2877.0
2945.2
3069.5
3159.3
3247.6
6.8452
6.9917
7.1271
0.0850
0.0923
0.0994
2788.4
2861.7
2932.8
3043.4
3138.7
3230.9
6.6245
6.7801
6.9212
440
500
540
0.1611
0.1757
0.1853
3013.4
3116.2
3185.6
3335.5
3467.6
3556.1
7.2540
7.4317
7.5434
0.1062
0.1162
0.1227
3002.9
3108.0
3178.4
3321.5
3456.5
3546.6
7.0520
7.2338
7.3474
600
640
700
0.1996
0.2091
0.2232
3290.9
3362.2
3470.9
3690.1
3780.4
3917.4
7.7024
7.8035
7.9487
0.1324
0.1388
0.1484
3285.0
3357.0
3466.5
3682.3
3773.5
3911.7
7.5085
7.6106
7.7571
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
H2O
TABLE A-4
T
C
725
726
Tables in SI Units
(Continued)
TABLE A-4
T
C
v
m3/kg
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
v
m3/kg
u
kJ/kg
H2O
p 40 bar 4.0 MPa
(Tsat 250.4C)
s
kJ/kg # K
p 60 bar 6.0 MPa
(Tsat 275.64C)
Sat.
280
320
0.04978
0.05546
0.06199
2602.3
2680.0
2767.4
2801.4
2901.8
3015.4
6.0701
6.2568
6.4553
0.03244
0.03317
0.03876
2589.7
2605.2
2720.0
2784.3
2804.2
2952.6
5.8892
5.9252
6.1846
360
400
440
0.06788
0.07341
0.07872
2845.7
2919.9
2992.2
3117.2
3213.6
3307.1
6.6215
6.7690
6.9041
0.04331
0.04739
0.05122
2811.2
2892.9
2970.0
3071.1
3177.2
3277.3
6.3782
6.5408
6.6853
500
540
600
0.08643
0.09145
0.09885
3099.5
3171.1
3279.1
3445.3
3536.9
3674.4
7.0901
7.2056
7.3688
0.05665
0.06015
0.06525
3082.2
3156.1
3266.9
3422.2
3517.0
3658.4
6.8803
6.9999
7.1677
640
700
740
0.1037
0.1110
0.1157
3351.8
3462.1
3536.6
3766.6
3905.9
3999.6
7.4720
7.6198
7.7141
0.06859
0.07352
0.07677
3341.0
3453.1
3528.3
3752.6
3894.1
3989.2
7.2731
7.4234
7.5190
p 80 bar 8.0 MPa
(Tsat 295.06C)
Copyright © 2006. Wiley. All rights reserved.
h
kJ/kg
p 100 bar 10.0 MPa
(Tsat 311.06C)
Sat.
320
360
0.02352
0.02682
0.03089
2569.8
2662.7
2772.7
2758.0
2877.2
3019.8
5.7432
5.9489
6.1819
0.01803
0.01925
0.02331
2544.4
2588.8
2729.1
2724.7
2781.3
2962.1
5.6141
5.7103
6.0060
400
440
480
0.03432
0.03742
0.04034
2863.8
2946.7
3025.7
3138.3
3246.1
3348.4
6.3634
6.5190
6.6586
0.02641
0.02911
0.03160
2832.4
2922.1
3005.4
3096.5
3213.2
3321.4
6.2120
6.3805
6.5282
520
560
600
0.04313
0.04582
0.04845
3102.7
3178.7
3254.4
3447.7
3545.3
3642.0
6.7871
6.9072
7.0206
0.03394
0.03619
0.03837
3085.6
3164.1
3241.7
3425.1
3526.0
3625.3
6.6622
6.7864
6.9029
640
700
740
0.05102
0.05481
0.05729
3330.1
3443.9
3520.4
3738.3
3882.4
3978.7
7.1283
7.2812
7.3782
0.04048
0.04358
0.04560
3318.9
3434.7
3512.1
3723.7
3870.5
3968.1
7.0131
7.1687
7.2670
p 120 bar 12.0 MPa
(Tsat 324.75C)
p 140 bar 14.0 MPa
(Tsat 336.75C)
Sat.
360
400
0.01426
0.01811
0.02108
2513.7
2678.4
2798.3
2684.9
2895.7
3051.3
5.4924
5.8361
6.0747
0.01149
0.01422
0.01722
2476.8
2617.4
2760.9
2637.6
2816.5
3001.9
5.3717
5.6602
5.9448
440
480
520
0.02355
0.02576
0.02781
2896.1
2984.4
3068.0
3178.7
3293.5
3401.8
6.2586
6.4154
6.5555
0.01954
0.02157
0.02343
2868.6
2962.5
3049.8
3142.2
3264.5
3377.8
6.1474
6.3143
6.4610
560
600
640
0.02977
0.03164
0.03345
3149.0
3228.7
3307.5
3506.2
3608.3
3709.0
6.6840
6.8037
6.9164
0.02517
0.02683
0.02843
3133.6
3215.4
3296.0
3486.0
3591.1
3694.1
6.5941
6.7172
6.8326
700
740
0.03610
0.03781
3425.2
3503.7
3858.4
3957.4
7.0749
7.1746
0.03075
0.03225
3415.7
3495.2
3846.2
3946.7
6.9939
7.0952
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in SI Units
(Continued)
v
m3/kg
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
p 160 bar 16.0 MPa
(Tsat 347.44C)
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
p 180 bar 18.0 MPa
(Tsat 357.06C)
Sat.
360
400
0.00931
0.01105
0.01426
2431.7
2539.0
2719.4
2580.6
2715.8
2947.6
5.2455
5.4614
5.8175
0.00749
0.00809
0.01190
2374.3
2418.9
2672.8
2509.1
2564.5
2887.0
5.1044
5.1922
5.6887
440
480
520
0.01652
0.01842
0.02013
2839.4
2939.7
3031.1
3103.7
3234.4
3353.3
6.0429
6.2215
6.3752
0.01414
0.01596
0.01757
2808.2
2915.9
3011.8
3062.8
3203.2
3378.0
5.9428
6.1345
6.2960
560
600
640
0.02172
0.02323
0.02467
3117.8
3201.8
3284.2
3465.4
3573.5
3678.9
6.5132
6.6399
6.7580
0.01904
0.02042
0.02174
3101.7
3188.0
3272.3
3444.4
3555.6
3663.6
6.4392
6.5696
6.6905
700
740
0.02674
0.02808
3406.0
3486.7
3833.9
3935.9
6.9224
7.0251
0.02362
0.02483
3396.3
3478.0
3821.5
3925.0
6.8580
6.9623
p 200 bar 20.0 MPa
(Tsat 365.81C)
Copyright © 2006. Wiley. All rights reserved.
v
m3/kg
p 240 bar 24.0 MPa
Sat.
400
440
0.00583
0.00994
0.01222
2293.0
2619.3
2774.9
2409.7
2818.1
3019.4
4.9269
5.5540
5.8450
0.00673
0.00929
2477.8
2700.6
2639.4
2923.4
5.2393
5.6506
480
520
560
0.01399
0.01551
0.01689
2891.2
2992.0
3085.2
3170.8
3302.2
3423.0
6.0518
6.2218
6.3705
0.01100
0.01241
0.01366
2838.3
2950.5
3051.1
3102.3
3248.5
3379.0
5.8950
6.0842
6.2448
600
640
700
0.01818
0.01940
0.02113
3174.0
3260.2
3386.4
3537.6
3648.1
3809.0
6.5048
6.6286
6.7993
0.01481
0.01588
0.01739
3145.2
3235.5
3366.4
3500.7
3616.7
3783.8
6.3875
6.5174
6.6947
740
800
0.02224
0.02385
3469.3
3592.7
3914.1
4069.7
6.9052
7.0544
0.01835
0.01974
3451.7
3578.0
3892.1
4051.6
6.8038
6.9567
p 280 bar 28.0 MPa
p 320 bar 32.0 MPa
400
440
480
0.00383
0.00712
0.00885
2223.5
2613.2
2780.8
2330.7
2812.6
3028.5
4.7494
5.4494
5.7446
0.00236
0.00544
0.00722
1980.4
2509.0
2718.1
2055.9
2683.0
2949.2
4.3239
5.2327
5.5968
520
560
600
0.01020
0.01136
0.01241
2906.8
3015.7
3115.6
3192.3
3333.7
3463.0
5.9566
6.1307
6.2823
0.00853
0.00963
0.01061
2860.7
2979.0
3085.3
3133.7
3287.2
3424.6
5.8357
6.0246
6.1858
640
700
740
0.01338
0.01473
0.01558
3210.3
3346.1
3433.9
3584.8
3758.4
3870.0
6.4187
6.6029
6.7153
0.01150
0.01273
0.01350
3184.5
3325.4
3415.9
3552.5
3732.8
3847.8
6.3290
6.5203
6.6361
800
900
0.01680
0.01873
3563.1
3774.3
4033.4
4298.8
6.8720
7.1084
0.01460
0.01633
3548.0
3762.7
4015.1
4285.1
6.7966
7.0372
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
H2O
TABLE A-4
T
C
727
728
Tables in SI Units
Properties of Compressed Liquid Water
TABLE A-5
T
C
v 10
m3/kg
3
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
v 103
m3/kg
H2O
p 25 bar 2.5 MPa
(Tsat 223.99C)
h
kJ/kg
s
kJ/kg # K
p 50 bar 5.0 MPa
(Tsat 263.99C)
20
40
80
1.0006
1.0067
1.0280
83.80
167.25
334.29
86.30
169.77
336.86
.2961
.5715
1.0737
.9995
1.0056
1.0268
83.65
166.95
333.72
88.65
171.97
338.85
.2956
.5705
1.0720
100
140
180
1.0423
1.0784
1.1261
418.24
587.82
761.16
420.85
590.52
763.97
1.3050
1.7369
2.1375
1.0410
1.0768
1.1240
417.52
586.76
759.63
422.72
592.15
765.25
1.3030
1.7343
2.1341
200
220
Sat.
1.1555
1.1898
1.1973
849.9
940.7
959.1
852.8
943.7
962.1
2.3294
2.5174
2.5546
1.1530
1.1866
1.2859
848.1
938.4
1147.8
853.9
944.4
1154.2
2.3255
2.5128
2.9202
p 75 bar 7.5 MPa
(Tsat 290.59C)
p 100 bar 10.0 MPa
(Tsat 311.06C)
20
40
80
.9984
1.0045
1.0256
83.50
166.64
333.15
90.99
174.18
340.84
.2950
.5696
1.0704
.9972
1.0034
1.0245
83.36
166.35
332.59
93.33
176.38
342.83
.2945
.5686
1.0688
100
140
180
1.0397
1.0752
1.1219
416.81
585.72
758.13
424.62
593.78
766.55
1.3011
1.7317
2.1308
1.0385
1.0737
1.1199
416.12
584.68
756.65
426.50
595.42
767.84
1.2992
1.7292
2.1275
220
260
Sat.
1.1835
1.2696
1.3677
936.2
1124.4
1282.0
945.1
1134.0
1292.2
2.5083
2.8763
3.1649
1.1805
1.2645
1.4524
934.1
1121.1
1393.0
945.9
1133.7
1407.6
2.5039
2.8699
3.3596
p 150 bar 15.0 MPa
(Tsat 342.24C)
Copyright © 2006. Wiley. All rights reserved.
u
kJ/kg
p 200 bar 20.0 MPa
(Tsat 365.81C)
20
40
80
.9950
1.0013
1.0222
83.06
165.76
331.48
97.99
180.78
346.81
.2934
.5666
1.0656
.9928
.9992
1.0199
82.77
165.17
330.40
102.62
185.16
350.80
.2923
.5646
1.0624
100
140
180
1.0361
1.0707
1.1159
414.74
582.66
753.76
430.28
598.72
770.50
1.2955
1.7242
2.1210
1.0337
1.0678
1.1120
413.39
580.69
750.95
434.06
602.04
773.20
1.2917
1.7193
2.1147
220
260
300
Sat.
1.1748
1.2550
1.3770
1.6581
929.9
1114.6
1316.6
1585.6
947.5
1133.4
1337.3
1610.5
2.4953
2.8576
3.2260
3.6848
1.1693
1.2462
1.3596
2.036
925.9
1108.6
1306.1
1785.6
949.3
1133.5
1333.3
1826.3
2.4870
2.8459
3.2071
4.0139
p 250 bar 25 MPa
p 300 bar 30.0 MPa
20
40
100
.9907
.9971
1.0313
82.47
164.60
412.08
107.24
189.52
437.85
.2911
.5626
1.2881
.9886
.9951
1.0290
82.17
164.04
410.78
111.84
193.89
441.66
.2899
.5607
1.2844
200
300
1.1344
1.3442
834.5
1296.6
862.8
1330.2
2.2961
3.1900
1.1302
1.3304
831.4
1287.9
865.3
1327.8
2.2893
3.1741
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
729
.6113
.6108
.5176
.4375
.3689
.3102
.2602
.2176
.1815
.1510
.1252
.1035
.0853
.0701
.0574
.0469
.0381
.0309
.0250
.0201
.0161
.0129
.01
0
2
4
6
8
10
12
14
16
18
20
22
24
26
28
30
32
34
36
38
40
1.0851
1.0848
1.0844
1.0841
1.0861
1.0858
1.0854
1.0871
1.0868
1.0864
1.0881
1.0878
1.0874
1.0891
1.0888
1.0884
1.0901
1.0898
1.0894
1.0908
1.0908
1.0904
Sat.
Solid
vi 103
4419
5444
6731
8354
2413.7
2943
3600
1358.4
1640.1
1986.4
786.0
940.5
1128.6
466.7
553.7
658.8
283.8
334.2
394.4
206.1
206.3
241.7
Sat.
Vapor
vg
400.71
404.40
408.06
411.70
389.45
393.23
396.98
377.93
381.80
385.64
366.14
370.10
374.03
354.09
358.14
362.15
2728.7
2729.6
2730.5
2731.3
2725.8
2726.8
2727.8
2722.7
2723.7
2724.8
2719.2
2720.4
2721.6
2715.5
2716.8
2718.0
2711.6
2712.9
2714.2
2708.7
2708.8
2710.2
333.40
333.43
337.62
341.78
345.91
350.02
Subl.
uig
Sat.
Solid
ui
Internal Energy
kJ/kg
2328.0
2325.2
2322.4
2319.6
2336.4
2333.6
2330.8
2344.7
2342.0
2339.2
2353.1
2350.3
2347.5
2361.4
2358.7
2355.9
2369.8
2367.0
2364.2
2375.3
2375.3
2372.6
Sat.
Vapor
ug
Source: J. H. Keenan, F. G. Keyes, P. G. Hill, and J. G. Moore, Steam Tables, Wiley, New York, 1978.
Pressure
kPa
Specific Volume
m3/kg
Properties of Saturated Water (Solid–Vapor): Temperature Table
Temp.
C
TABLE A-6
Copyright © 2006. Wiley. All rights reserved.
400.71
404.40
408.06
411.70
389.45
393.23
396.98
377.93
381.80
385.64
366.14
370.10
374.03
354.09
358.14
362.15
341.78
345.91
350.02
333.40
333.43
337.62
Sat.
Solid
hi
2839.1
2839.1
2839.0
2838.9
2839.0
2839.0
2839.1
2838.6
2838.7
2838.9
2837.9
2838.2
2838.4
2837.0
2837.3
2837.6
2835.7
2836.2
2836.6
2834.8
2834.8
2835.3
Subl.
hig
Enthalpy
kJ/kg
2438.4
2434.7
2430.9
2427.2
2449.5
2445.8
2442.1
2460.6
2456.9
2453.2
2471.8
2468.1
2464.3
2482.9
2479.2
2475.5
2494.0
2490.3
2486.6
2501.4
2501.3
2497.7
Sat.
Vapor
hg
H2O
1.486
1.501
1.517
1.532
1.439
1.455
1.471
1.393
1.408
1.424
1.346
1.362
1.377
1.299
1.315
1.331
1.253
1.268
1.284
1.221
1.221
1.237
Sat.
Solid
si
11.872
11.972
12.073
12.176
11.580
11.676
11.773
11.302
11.394
11.486
11.036
11.123
11.212
10.781
10.865
10.950
10.536
10.616
10.698
10.378
10.378
10.456
Subl.
sig
Entropy
kJ/kg # K
10.386
10.470
10.556
10.644
10.141
10.221
10.303
9.909
9.985
10.062
9.690
9.762
9.835
9.481
9.550
9.619
9.283
9.348
9.414
9.156
9.157
9.219
Sat.
Vapor
sg
730
Tables in SI Units
Copyright © 2006. Wiley. All rights reserved.
R-22
TABLE A-7
Properties of Saturated Refrigerant 22 (Liquid–Vapor): Temperature Table
Specific Volume
m3/kg
Internal Energy
kJ/kg
Enthalpy
kJ/kg
Entropy
kJ/kg # K
Temp.
C
Press.
bar
Sat.
Liquid
vf 103
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Temp.
C
60
50
45
40
36
32
0.3749
0.6451
0.8290
1.0522
1.2627
1.5049
0.6833
0.6966
0.7037
0.7109
0.7169
0.7231
0.5370
0.3239
0.2564
0.2052
0.1730
0.1468
21.57
10.89
5.50
0.07
4.29
8.68
203.67
207.70
209.70
211.68
213.25
214.80
21.55
10.85
5.44
0.00
4.38
8.79
245.35
239.44
236.39
233.27
230.71
228.10
223.81
228.60
230.95
233.27
235.09
236.89
0.0964
0.0474
0.0235
0.0000
0.0186
0.0369
1.0547
1.0256
1.0126
1.0005
0.9914
0.9828
60
50
45
40
36
32
30
28
26
22
20
1.6389
1.7819
1.9345
2.2698
2.4534
0.7262
0.7294
0.7327
0.7393
0.7427
0.1355
0.1252
0.1159
0.0997
0.0926
10.88
13.09
15.31
19.76
21.99
215.58
216.34
217.11
218.62
219.37
11.00
13.22
15.45
19.92
22.17
226.77
225.43
224.08
221.32
219.91
237.78
238.66
239.53
241.24
242.09
0.0460
0.0551
0.0641
0.0819
0.0908
0.9787
0.9746
0.9707
0.9631
0.9595
30
28
26
22
20
18
16
14
12
10
2.6482
2.8547
3.0733
3.3044
3.5485
0.7462
0.7497
0.7533
0.7569
0.7606
0.0861
0.0802
0.0748
0.0698
0.0652
24.23
26.48
28.73
31.00
33.27
220.11
220.85
221.58
222.30
223.02
24.43
26.69
28.97
31.25
33.54
218.49
217.05
215.59
214.11
212.62
242.92
243.74
244.56
245.36
246.15
0.0996
0.1084
0.1171
0.1258
0.1345
0.9559
0.9525
0.9490
0.9457
0.9424
18
16
14
12
10
8
6
4
2
0
3.8062
4.0777
4.3638
4.6647
4.9811
0.7644
0.7683
0.7722
0.7762
0.7803
0.0610
0.0571
0.0535
0.0501
0.0470
35.54
37.83
40.12
42.42
44.73
223.73
224.43
225.13
225.82
226.50
35.83
38.14
40.46
42.78
45.12
211.10
209.56
208.00
206.41
204.81
246.93
247.70
248.45
249.20
249.92
0.1431
0.1517
0.1602
0.1688
0.1773
0.9392
0.9361
0.9330
0.9300
0.9271
8
6
4
2
0
2
4
6
8
10
5.3133
5.6619
6.0275
6.4105
6.8113
0.7844
0.7887
0.7930
0.7974
0.8020
0.0442
0.0415
0.0391
0.0368
0.0346
47.04
49.37
51.71
54.05
56.40
227.17
227.83
228.48
229.13
229.76
47.46
49.82
52.18
54.56
56.95
203.18
201.52
199.84
198.14
196.40
250.64
251.34
252.03
252.70
253.35
0.1857
0.1941
0.2025
0.2109
0.2193
0.9241
0.9213
0.9184
0.9157
0.9129
2
4
6
8
10
12
16
20
24
28
7.2307
8.1268
9.1030
10.164
11.313
0.8066
0.8162
0.8263
0.8369
0.8480
0.0326
0.0291
0.0259
0.0232
0.0208
58.77
63.53
68.33
73.19
78.09
230.38
231.59
232.76
233.87
234.92
59.35
64.19
69.09
74.04
79.05
194.64
191.02
187.28
183.40
179.37
253.99
255.21
256.37
257.44
258.43
0.2276
0.2442
0.2607
0.2772
0.2936
0.9102
0.9048
0.8996
0.8944
0.8893
12
16
20
24
28
32
36
40
45
50
60
12.556
13.897
15.341
17.298
19.433
24.281
0.8599
0.8724
0.8858
0.9039
0.9238
0.9705
0.0186
0.0168
0.0151
0.0132
0.0116
0.0089
83.06
88.08
93.18
99.65
106.26
120.00
235.91
236.83
237.66
238.59
239.34
240.24
84.14
89.29
94.53
101.21
108.06
122.35
175.18
170.82
166.25
160.24
153.84
139.61
259.32
260.11
260.79
261.46
261.90
261.96
0.3101
0.3265
0.3429
0.3635
0.3842
0.4264
0.8842
0.8790
0.8738
0.8672
0.8603
0.8455
32
36
40
45
50
60
Source: Tables A-7 through A-9 are calculated based on equations from A. Kamei and S. W. Beyerlein, “A Fundamental Equation for
Chlorodifluoromethane (R-22),” Fluid Phase Equilibria, Vol. 80, No. 11, 1992, pp. 71–86.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in SI Units
Copyright © 2006. Wiley. All rights reserved.
Properties of Saturated Refrigerant 22 (Liquid–Vapor): Pressure Table
Specific Volume
m3/kg
Internal Energy
kJ/kg
Enthalpy
kJ/kg
Entropy
kJ/kg # K
Press.
bar
Temp.
C
Sat.
Liquid
vf 103
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Press.
bar
0.40
0.50
0.60
0.70
0.80
0.90
58.86
54.83
51.40
48.40
45.73
43.30
0.6847
0.6901
0.6947
0.6989
0.7026
0.7061
0.5056
0.4107
0.3466
0.3002
0.2650
0.2374
20.36
16.07
12.39
9.17
6.28
3.66
204.13
205.76
207.14
208.34
209.41
210.37
20.34
16.03
12.35
9.12
6.23
3.60
244.69
242.33
240.28
238.47
236.84
235.34
224.36
226.30
227.93
229.35
230.61
231.74
0.0907
0.0709
0.0542
0.0397
0.0270
0.0155
1.0512
1.0391
1.0294
1.0213
1.0144
1.0084
0.40
0.50
0.60
0.70
0.80
0.90
1.00
1.25
1.50
1.75
2.00
41.09
36.23
32.08
28.44
25.18
0.7093
0.7166
0.7230
0.7287
0.7340
0.2152
0.1746
0.1472
0.1274
0.1123
1.26
4.04
8.60
12.61
16.22
211.25
213.16
214.77
216.18
217.42
1.19
4.13
8.70
12.74
16.37
233.95
230.86
228.15
225.73
223.52
232.77
234.99
236.86
238.47
239.88
0.0051
0.0175
0.0366
0.0531
0.0678
1.0031
0.9919
0.9830
0.9755
0.9691
1.00
1.25
1.50
1.75
2.00
2.25
2.50
2.75
3.00
3.25
22.22
19.51
17.00
14.66
12.46
0.7389
0.7436
0.7479
0.7521
0.7561
0.1005
0.0910
0.0831
0.0765
0.0709
19.51
22.54
25.36
27.99
30.47
218.53
219.55
220.48
221.34
222.13
19.67
22.72
25.56
28.22
30.72
221.47
219.57
217.77
216.07
214.46
241.15
242.29
243.33
244.29
245.18
0.0809
0.0930
0.1040
0.1143
0.1238
0.9636
0.9586
0.9542
0.9502
0.9465
2.25
2.50
2.75
3.00
3.25
3.50
3.75
4.00
4.25
4.50
10.39
8.43
6.56
4.78
3.08
0.7599
0.7636
0.7672
0.7706
0.7740
0.0661
0.0618
0.0581
0.0548
0.0519
32.82
35.06
37.18
39.22
41.17
222.88
223.58
224.24
224.86
225.45
33.09
35.34
37.49
39.55
41.52
212.91
211.42
209.99
208.61
207.27
246.00
246.77
247.48
248.16
248.80
0.1328
0.1413
0.1493
0.1569
0.1642
0.9431
0.9399
0.9370
0.9342
0.9316
3.50
3.75
4.00
4.25
4.50
4.75
5.00
5.25
5.50
5.75
1.45
0.12
1.63
3.08
4.49
0.7773
0.7805
0.7836
0.7867
0.7897
0.0492
0.0469
0.0447
0.0427
0.0409
43.05
44.86
46.61
48.30
49.94
226.00
226.54
227.04
227.53
227.99
43.42
45.25
47.02
48.74
50.40
205.98
204.71
203.48
202.28
201.11
249.40
249.97
250.51
251.02
251.51
0.1711
0.1777
0.1841
0.1903
0.1962
0.9292
0.9269
0.9247
0.9226
0.9206
4.75
5.00
5.25
5.50
5.75
6.00
7.00
8.00
9.00
10.00
5.85
10.91
15.45
19.59
23.40
0.7927
0.8041
0.8149
0.8252
0.8352
0.0392
0.0337
0.0295
0.0262
0.0236
51.53
57.48
62.88
67.84
72.46
228.44
230.04
231.43
232.64
233.71
52.01
58.04
63.53
68.59
73.30
199.97
195.60
191.52
187.67
183.99
251.98
253.64
255.05
256.25
257.28
0.2019
0.2231
0.2419
0.2591
0.2748
0.9186
0.9117
0.9056
0.9001
0.8952
6.00
7.00
8.00
9.00
10.00
12.00
14.00
16.00
18.00
20.00
24.00
30.25
36.29
41.73
46.69
51.26
59.46
0.8546
0.8734
0.8919
0.9104
0.9291
0.9677
0.0195
0.0166
0.0144
0.0127
0.0112
0.0091
80.87
88.45
95.41
101.87
107.95
119.24
235.48
236.89
238.00
238.86
239.51
240.22
81.90
89.68
96.83
103.51
109.81
121.56
177.04
170.49
164.21
158.13
152.17
140.43
258.94
260.16
261.04
261.64
261.98
261.99
0.3029
0.3277
0.3500
0.3705
0.3895
0.4241
0.8864
0.8786
0.8715
0.8649
0.8586
0.8463
12.00
14.00
16.00
18.00
20.00
24.00
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
R-22
TABLE A-8
731
732
Tables in SI Units
TABLE A-9
T
C
Properties of Superheated Refrigerant 22 Vapor
v
m3/kg
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
R-22
p 0.4 bar 0.04 MPa
(Tsat 58.86C)
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
p 0.6 bar 0.06 MPa
(Tsat 51.40C)
Sat.
55
50
0.50559
0.51532
0.52787
204.13
205.92
208.26
224.36
226.53
229.38
1.0512
1.0612
1.0741
0.34656
207.14
227.93
1.0294
0.34895
207.80
228.74
1.0330
45
40
35
0.54037
0.55284
0.56526
210.63
213.02
215.43
232.24
235.13
238.05
1.0868
1.0993
1.1117
0.35747
0.36594
0.37437
210.20
212.62
215.06
231.65
234.58
237.52
1.0459
1.0586
1.0711
30
25
20
0.57766
0.59002
0.60236
217.88
220.35
222.85
240.99
243.95
246.95
1.1239
1.1360
1.1479
0.38277
0.39114
0.39948
217.53
220.02
222.54
240.49
243.49
246.51
1.0835
1.0956
1.1077
15
10
5
0
0.61468
0.62697
0.63925
0.65151
225.38
227.93
230.52
233.13
249.97
253.01
256.09
259.19
1.1597
1.1714
1.1830
1.1944
0.40779
0.41608
0.42436
0.43261
225.08
227.65
230.25
232.88
249.55
252.62
255.71
258.83
1.1196
1.1314
1.1430
1.1545
p 0.8 bar 0.08 MPa
(Tsat 45.73C)
Copyright © 2006. Wiley. All rights reserved.
v
m3/kg
p 1.0 bar 0.10 MPa
(Tsat 41.09C)
Sat.
45
40
0.26503
0.26597
0.27245
209.41
209.76
212.21
230.61
231.04
234.01
1.0144
1.0163
1.0292
0.21518
211.25
232.77
1.0031
0.21633
211.79
233.42
1.0059
35
30
25
0.27890
0.28530
0.29167
214.68
217.17
219.68
236.99
239.99
243.02
1.0418
1.0543
1.0666
0.22158
0.22679
0.23197
214.29
216.80
219.34
236.44
239.48
242.54
1.0187
1.0313
1.0438
20
15
10
0.29801
0.30433
0.31062
222.22
224.78
227.37
246.06
249.13
252.22
1.0788
1.0908
1.1026
0.23712
0.24224
0.24734
221.90
224.48
227.08
245.61
248.70
251.82
1.0560
1.0681
1.0801
5
0
5
10
0.31690
0.32315
0.32939
0.33561
229.98
232.62
235.29
237.98
255.34
258.47
261.64
264.83
1.1143
1.1259
1.1374
1.1488
0.25241
0.25747
0.26251
0.26753
229.71
232.36
235.04
237.74
254.95
258.11
261.29
264.50
1.0919
1.1035
1.1151
1.1265
p 1.5 bar 0.15 MPa
(Tsat 32.08C)
p 2.0 bar 0.20 MPa
(Tsat 25.18C)
Sat.
30
25
0.14721
0.14872
0.15232
214.77
215.85
218.45
236.86
238.16
241.30
0.9830
0.9883
1.0011
0.11232
217.42
239.88
0.9691
0.11242
217.51
240.00
0.9696
20
15
10
0.15588
0.15941
0.16292
221.07
223.70
226.35
244.45
247.61
250.78
1.0137
1.0260
1.0382
0.11520
0.11795
0.12067
220.19
222.88
225.58
243.23
246.47
249.72
0.9825
0.9952
1.0076
5
0
5
0.16640
0.16987
0.17331
229.02
231.70
234.42
253.98
257.18
260.41
1.0502
1.0621
1.0738
0.12336
0.12603
0.12868
228.30
231.03
233.78
252.97
256.23
259.51
1.0199
1.0310
1.0438
10 0.17674 237.15 263.66
15 0.18015 239.91 266.93
20 0.18355 242.69 270.22
25 0.18693 245.49 273.53
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
1.0854
1.0968
1.1081
1.1193
0.13132
0.13393
0.13653
0.13912
236.54
239.33
242.14
244.97
262.81
266.12
269.44
272.79
1.0555
1.0671
1.0786
1.0899
Created from purdue on 2022-01-24 17:56:53.
Tables in SI Units
T
C
(Continued)
v
m3/kg
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
v
m3/kg
p 2.5 bar 0.25 MPa
(Tsat 19.51C)
h
kJ/kg
s
kJ/kg # K
p 3.0 bar 0.30 MPa
(Tsat 14.66C)
Sat.
15
10
0.09097
0.09303
0.09528
219.55
222.03
224.79
242.29
245.29
248.61
0.9586
0.9703
0.9831
0.07651
221.34
244.29
0.9502
0.07833
223.96
247.46
0.9623
5
0
5
0.09751
0.09971
0.10189
227.55
230.33
233.12
251.93
255.26
258.59
0.9956
1.0078
1.0199
0.08025
0.08214
0.08400
226.78
229.61
232.44
250.86
254.25
257.64
0.9751
0.9876
0.9999
10
15
20
0.10405
0.10619
0.10831
235.92
238.74
241.58
261.93
265.29
268.66
1.0318
1.0436
1.0552
0.08585
0.08767
0.08949
235.28
238.14
241.01
261.04
264.44
267.85
1.0120
1.0239
1.0357
25
30
35
40
0.11043
0.11253
0.11461
0.11669
244.44
247.31
250.21
253.13
272.04
275.44
278.86
282.30
1.0666
1.0779
1.0891
1.1002
0.09128
0.09307
0.09484
0.09660
243.89
246.80
249.72
252.66
271.28
274.72
278.17
281.64
1.0472
1.0587
1.0700
1.0811
p 3.5 bar 0.35 MPa
(Tsat 10.39C)
Copyright © 2006. Wiley. All rights reserved.
u
kJ/kg
p 4.0 bar 0.40 MPa
(Tsat 6.56C)
Sat.
10
5
0.06605
0.06619
0.06789
222.88
223.10
225.99
246.00
246.27
249.75
0.9431
0.9441
0.9572
0.05812
224.24
247.48
0.9370
0.05860
225.16
248.60
0.9411
0
5
10
0.06956
0.07121
0.07284
228.86
231.74
234.63
253.21
256.67
260.12
0.9700
0.9825
0.9948
0.06011
0.06160
0.06306
228.09
231.02
233.95
252.14
225.66
259.18
0.9542
0.9670
0.9795
15
20
25
0.07444
0.07603
0.07760
237.52
240.42
243.34
263.57
267.03
270.50
1.0069
1.0188
1.0305
0.06450
0.06592
0.06733
236.89
239.83
242.77
262.69
266.19
269.71
0.9918
1.0039
1.0158
30
35
40
45
0.07916
0.08070
0.08224
0.08376
246.27
249.22
252.18
255.17
273.97
227.46
280.97
284.48
1.0421
1.0535
1.0648
1.0759
0.06872
0.07010
0.07146
0.07282
245.73
248.71
251.70
254.70
273.22
276.75
280.28
283.83
1.0274
1.0390
1.0504
1.0616
p 4.5 bar 0.45 MPa
(Tsat 3.08C)
p 5.0 bar 0.50 MPa
(Tsat 0.12C)
Sat.
0
5
0.05189
0.05275
0.05411
225.45
227.29
230.28
248.80
251.03
254.63
0.9316
0.9399
0.9529
0.04686
226.54
249.97
0.9269
0.04810
229.52
253.57
0.9399
10
15
20
0.05545
0.05676
0.05805
233.26
236.24
239.22
258.21
261.78
265.34
0.9657
0.9782
0.9904
0.04934
0.05056
0.05175
232.55
235.57
238.59
257.22
260.85
264.47
0.9530
0.9657
0.9781
25
30
35
0.05933
0.06059
0.06184
242.20
245.19
248.19
268.90
272.46
276.02
1.0025
1.0143
1.0259
0.05293
0.05409
0.05523
241.61
244.63
247.66
268.07
271.68
275.28
0.9903
1.0023
1.0141
0.05636
0.05748
0.05859
0.05969
250.70
253.76
256.82
259.90
278.89
282.50
286.12
289.75
1.0257
1.0371
1.0484
1.0595
40 0.06308 251.20 279.59
1.0374
45 0.06430 254.23 283.17
1.0488
50 0.06552 257.28 286.76
1.0600
55
0.06672
260.34
290.36
1.0710
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
R-22
TABLE A-9
733
734
Tables in SI Units
TABLE A-9
T
C
(Continued)
v
m3/kg
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
v
m3/kg
u
kJ/kg
R-22
p 5.5 bar 0.55 MPa
(Tsat 3.08C)
Sat.
5
10
15
20
25
30
35
40
45
50
55
60
0.04271
0.04317
0.04433
0.04547
0.04658
0.04768
0.04875
0.04982
0.05086
0.05190
0.05293
0.05394
0.05495
227.53
228.72
231.81
234.89
237.95
241.01
244.07
247.13
250.20
253.27
256.36
259.46
262.58
251.02
252.46
256.20
259.90
263.57
267.23
270.88
274.53
278.17
281.82
285.47
289.13
292.80
0.03371
0.03451
0.03547
0.03639
0.03730
0.03819
0.03906
0.03992
0.04076
0.04160
0.04242
0.04324
0.04405
230.04
232.70
235.92
239.12
242.29
245.46
248.62
251.78
254.94
258.11
261.29
264.48
267.68
253.64
256.86
260.75
264.59
268.40
272.19
275.96
279.72
283.48
287.23
290.99
294.75
298.51
0.9226
0.9278
0.9411
0.9540
0.9667
0.9790
0.9912
1.0031
1.0148
1.0264
1.0378
1.0490
1.0601
0.03923
228.44
251.98
0.9186
0.04015
0.04122
0.04227
0.04330
0.04431
0.04530
0.04628
0.04724
0.04820
0.04914
0.05008
231.05
234.18
237.29
240.39
243.49
246.58
249.68
252.78
255.90
259.02
262.15
255.14
258.91
262.65
266.37
270.07
273.76
277.45
281.13
284.82
288.51
292.20
0.9299
0.9431
0.9560
0.9685
0.9808
0.9929
1.0048
1.0164
1.0279
1.0393
1.0504
p 8.0 bar 0.80 MPa
(Tsat 15.45C)
0.9117
0.9229
0.9363
0.9493
0.9619
0.9743
0.9865
0.9984
1.0101
1.0216
1.0330
1.0442
1.0552
Copyright © 2006. Wiley. All rights reserved.
p 9.0 bar 0.90 MPa
(Tsat 19.59C)
Sat.
20
30
40
50
60
70
80
90
100
110
120
130
140
150
0.02623
0.02630
0.02789
0.02939
0.03082
0.03219
0.03353
0.03483
0.03611
0.03736
0.03860
0.03982
0.04103
0.04223
0.04342
232.64
232.92
239.73
246.37
252.95
259.49
266.04
272.62
279.23
285.90
292.63
299.42
306.28
313.21
320.21
256.25
256.59
264.83
272.82
280.68
288.46
296.21
303.96
311.73
319.53
327.37
335.26
343.21
351.22
359.29
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
s
kJ/kg # K
p 6.0 bar 0.60 MPa
(Tsat 5.85C)
p 7.0 bar 0.70 MPa
(Tsat 10.91C)
Sat.
15
20
25
30
35
40
45
50
55
60
65
70
h
kJ/kg
0.02953
231.43
255.05
0.9056
0.03033
0.03118
0.03202
0.03283
0.03363
0.03440
0.03517
0.03592
0.03667
0.03741
0.03814
234.47
237.76
241.04
244.28
247.52
250.74
253.96
257.18
260.40
263.64
266.87
258.74
262.70
266.66
270.54
274.42
278.26
282.10
285.92
289.74
293.56
297.38
0.9182
0.9315
0.9448
0.9574
0.9700
0.9821
0.9941
1.0058
1.0174
1.0287
1.0400
p 10.0 bar 1.00 MPa
(Tsat 23.40C)
0.9001
0.9013
0.9289
0.9549
0.9795
1.0033
1.0262
1.0484
1.0701
1.0913
1.1120
1.1323
1.1523
1.1719
1.1912
0.02358
233.71
257.28
0.8952
0.02457
0.02598
0.02732
0.02860
0.02984
0.03104
0.03221
0.03337
0.03450
0.03562
0.03672
0.03781
0.03889
238.34
245.18
251.90
258.56
265.19
271.84
278.52
285.24
292.02
298.85
305.74
312.70
319.74
262.91
271.17
279.22
287.15
295.03
302.88
310.74
318.61
326.52
334.46
342.46
350.51
358.63
0.9139
0.9407
0.9660
0.9902
1.0135
1.0361
1.0580
1.0794
1.1003
1.1207
1.1408
1.1605
1.1790
(Continued)
T
C
v
m3/kg
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
p 12.0 bar 1.20 MPa
(Tsat 30.25C)
Sat.
40
50
60
70
80
90
100
110
120
130
140
150
160
170
0.01955
0.02083
0.02204
0.02319
0.02428
0.02534
0.02636
0.02736
0.02834
0.02930
0.03024
0.03118
0.03210
0.03301
0.03392
235.48
242.63
249.69
256.60
263.44
270.25
277.07
283.90
290.77
297.69
304.65
311.68
318.77
325.92
333.14
258.94
267.62
276.14
284.43
292.58
300.66
308.70
316.73
324.78
332.85
340.95
349.09
357.29
365.54
373.84
0.8864
0.9146
0.9413
0.9666
0.9907
1.0139
1.0363
1.0582
1.0794
1.1002
1.1205
1.1405
1.1601
1.1793
1.1983
p 16.0 bar 1.60 MPa
(Tsat 41.73C)
Copyright © 2006. Wiley. All rights reserved.
Sat.
50
60
70
80
90
100
110
120
130
140
150
160
170
0.01440
0.01533
0.01634
0.01728
0.01817
0.01901
0.01983
0.02062
0.02139
0.02214
0.02288
0.02361
0.02432
0.02503
238.00
244.66
252.29
259.65
266.86
274.00
281.09
288.18
295.28
302.41
309.58
316.79
324.05
331.37
261.04
269.18
278.43
287.30
295.93
304.42
312.82
321.17
329.51
337.84
346.19
354.56
362.97
371.42
0.8715
0.8971
0.9252
0.9515
0.9762
0.9999
1.0228
1.0448
1.0663
1.0872
1.1077
1.1277
1.1473
1.1666
v
m3/kg
u
kJ/kg
0.01124
0.01212
0.01300
0.01381
0.01457
0.01528
0.01596
0.01663
0.01727
0.01789
0.01850
0.01910
0.01969
0.02027
239.51
247.20
255.35
263.12
270.67
278.09
285.44
292.76
300.08
307.40
314.75
322.14
329.56
337.03
261.98
271.43
281.36
290.74
299.80
308.65
317.37
326.01
334.61
343.19
351.76
360.34
368.95
377.58
0.8586
0.8873
0.9167
0.9436
0.9689
0.9929
1.0160
1.0383
1.0598
1.0808
1.1013
1.1214
1.1410
1.1603
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
s
kJ/kg # K
p 14.0 bar 1.40 MPa
(Tsat 36.29C)
0.01662
0.01708
0.01823
0.01929
0.02029
0.02125
0.02217
0.02306
0.02393
0.02478
0.02562
0.02644
0.02725
0.02805
0.02884
236.89
239.78
247.29
254.52
261.60
268.60
275.56
282.52
289.49
296.50
303.55
310.64
317.79
324.99
332.26
260.16
263.70
272.81
281.53
290.01
298.34
306.60
314.80
323.00
331.19
339.41
347.65
355.94
364.26
372.64
0.8786
0.8900
0.9186
0.9452
0.9703
0.9942
1.0172
1.0395
1.0612
1.0823
1.1029
1.1231
1.1429
1.1624
1.1815
p 18.0 bar 1.80 MPa
(Tsat 46.69C)
0.01265
0.01301
0.01401
0.01492
0.01576
0.01655
0.01731
0.01804
0.01874
0.01943
0.02011
0.02077
0.02142
0.02207
p 20.0 bar 2.00 MPa
(Tsat 51.26C)
Sat.
60
70
80
90
100
110
120
130
140
150
160
170
180
h
kJ/kg
R-22
TABLE A-9
238.86
241.72
249.86
257.57
265.04
272.37
279.62
286.83
294.04
301.26
308.50
315.78
323.10
330.47
261.64
265.14
275.09
284.43
293.40
302.16
310.77
319.30
327.78
336.24
344.70
353.17
361.66
370.19
0.8649
0.8758
0.9061
0.9337
0.9595
0.9839
1.0073
1.0299
1.0517
1.0730
1.0937
1.1139
1.1338
1.1532
p 24.0 bar 2.4 MPa
(Tsat 59.46C)
0.00907
0.00913
0.01006
0.01085
0.01156
0.01222
0.01284
0.01343
0.01400
0.01456
0.01509
0.01562
0.01613
0.01663
240.22
240.78
250.30
258.89
267.01
274.85
282.53
290.11
297.64
305.14
312.64
320.16
327.70
335.27
261.99
262.68
274.43
284.93
294.75
304.18
313.35
322.35
331.25
340.08
348.87
357.64
366.41
375.20
0.8463
0.8484
0.8831
0.9133
0.9407
0.9663
0.9906
1.0137
1.0361
1.0577
1.0787
1.0992
1.1192
1.1388
735
736
Tables in SI Units
TABLE A-10
Properties of Saturated Refrigerant 134a (Liquid–Vapor): Temperature Table
Copyright © 2006. Wiley. All rights reserved.
R-134a
Specific Volume
m3/kg
Internal Energy
kJ/kg
Enthalpy
kJ/kg
Entropy
kJ/kg # K
Temp.
C
Press.
bar
Sat.
Liquid
vf 103
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Temp.
C
40
36
32
28
26
0.5164
0.6332
0.7704
0.9305
1.0199
0.7055
0.7113
0.7172
0.7233
0.7265
0.3569
0.2947
0.2451
0.2052
0.1882
0.04
4.68
9.47
14.31
16.75
204.45
206.73
209.01
211.29
212.43
0.00
4.73
9.52
14.37
16.82
222.88
220.67
218.37
216.01
214.80
222.88
225.40
227.90
230.38
231.62
0.0000
0.0201
0.0401
0.0600
0.0699
0.9560
0.9506
0.9456
0.9411
0.9390
40
36
32
28
26
24
22
20
18
16
1.1160
1.2192
1.3299
1.4483
1.5748
0.7296
0.7328
0.7361
0.7395
0.7428
0.1728
0.1590
0.1464
0.1350
0.1247
19.21
21.68
24.17
26.67
29.18
213.57
214.70
215.84
216.97
218.10
19.29
21.77
24.26
26.77
29.30
213.57
212.32
211.05
209.76
208.45
232.85
234.08
235.31
236.53
237.74
0.0798
0.0897
0.0996
0.1094
0.1192
0.9370
0.9351
0.9332
0.9315
0.9298
24
22
20
18
16
12
8
4
0
4
1.8540
2.1704
2.5274
2.9282
3.3765
0.7498
0.7569
0.7644
0.7721
0.7801
0.1068
0.0919
0.0794
0.0689
0.0600
34.25
39.38
44.56
49.79
55.08
220.36
222.60
224.84
227.06
229.27
34.39
39.54
44.75
50.02
55.35
205.77
203.00
200.15
197.21
194.19
240.15
242.54
244.90
247.23
249.53
0.1388
0.1583
0.1777
0.1970
0.2162
0.9267
0.9239
0.9213
0.9190
0.9169
12
8
4
0
4
8
12
16
20
24
3.8756
4.4294
5.0416
5.7160
6.4566
0.7884
0.7971
0.8062
0.8157
0.8257
0.0525
0.0460
0.0405
0.0358
0.0317
60.43
65.83
71.29
76.80
82.37
231.46
233.63
235.78
237.91
240.01
60.73
66.18
71.69
77.26
82.90
191.07
187.85
184.52
181.09
177.55
251.80
254.03
256.22
258.36
260.45
0.2354
0.2545
0.2735
0.2924
0.3113
0.9150
0.9132
0.9116
0.9102
0.9089
8
12
16
20
24
26
28
30
32
34
6.8530
7.2675
7.7006
8.1528
8.6247
0.8309
0.8362
0.8417
0.8473
0.8530
0.0298
0.0281
0.0265
0.0250
0.0236
85.18
88.00
90.84
93.70
96.58
241.05
242.08
243.10
244.12
245.12
85.75
88.61
91.49
94.39
97.31
175.73
173.89
172.00
170.09
168.14
261.48
262.50
263.50
264.48
265.45
0.3208
0.3302
0.3396
0.3490
0.3584
0.9082
0.9076
0.9070
0.9064
0.9058
26
28
30
32
34
36
38
40
42
44
9.1168
9.6298
10.164
10.720
11.299
0.8590
0.8651
0.8714
0.8780
0.8847
0.0223
0.0210
0.0199
0.0188
0.0177
99.47
102.38
105.30
108.25
111.22
246.11
247.09
248.06
249.02
249.96
100.25
103.21
106.19
109.19
112.22
166.15
164.12
162.05
159.94
157.79
266.40
267.33
268.24
269.14
270.01
0.3678
0.3772
0.3866
0.3960
0.4054
0.9053
0.9047
0.9041
0.9035
0.9030
36
38
40
42
44
48
52
56
60
12.526
13.851
15.278
16.813
0.8989
0.9142
0.9308
0.9488
0.0159
0.0142
0.0127
0.0114
117.22
123.31
129.51
135.82
251.79
253.55
255.23
256.81
118.35
124.58
130.93
137.42
153.33
148.66
143.75
138.57
271.68
273.24
274.68
275.99
0.4243
0.4432
0.4622
0.4814
0.9017
0.9004
0.8990
0.8973
48
52
56
60
70
80
90
100
21.162
26.324
32.435
39.742
1.0027
1.0766
1.1949
1.5443
0.0086
0.0064
0.0046
0.0027
152.22
169.88
189.82
218.60
260.15
262.14
261.34
248.49
154.34
172.71
193.69
224.74
124.08
106.41
82.63
34.40
278.43
279.12
276.32
259.13
0.5302
0.5814
0.6380
0.7196
0.8918
0.8827
0.8655
0.8117
70
80
90
100
Source: Tables A-10 through A-12 are calculated based on equations from D. P. Wilson and R. S. Basu, “Thermodynamic Properties of a New
Stratospherically Safe Working Fluid—Refrigerant 134a,” ASHRAE Trans., Vol. 94, Pt. 2, 1988, pp. 2095–2118.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in SI Units
Properties of Saturated Refrigerant 134a (Liquid–Vapor): Pressure Table
Specific Volume
m3/kg
Internal Energy
kJ/kg
Enthalpy
kJ/kg
Entropy
kJ/kg # K
Temp.
C
Sat.
Liquid
vf 103
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Press.
bar
0.6
0.8
1.0
1.2
1.4
37.07
31.21
26.43
22.36
18.80
0.7097
0.7184
0.7258
0.7323
0.7381
0.3100
0.2366
0.1917
0.1614
0.1395
3.41
10.41
16.22
21.23
25.66
206.12
209.46
212.18
214.50
216.52
3.46
10.47
16.29
21.32
25.77
221.27
217.92
215.06
212.54
210.27
224.72
228.39
231.35
233.86
236.04
0.0147
0.0440
0.0678
0.0879
0.1055
0.9520
0.9447
0.9395
0.9354
0.9322
0.6
0.8
1.0
1.2
1.4
1.6
1.8
2.0
2.4
2.8
15.62
12.73
10.09
5.37
1.23
0.7435
0.7485
0.7532
0.7618
0.7697
0.1229
0.1098
0.0993
0.0834
0.0719
29.66
33.31
36.69
42.77
48.18
218.32
219.94
221.43
224.07
226.38
29.78
33.45
36.84
42.95
48.39
208.19
206.26
204.46
201.14
198.13
237.97
239.71
241.30
244.09
246.52
0.1211
0.1352
0.1481
0.1710
0.1911
0.9295
0.9273
0.9253
0.9222
0.9197
1.6
1.8
2.0
2.4
2.8
3.2
3.6
4.0
5.0
6.0
2.48
5.84
8.93
15.74
21.58
0.7770
0.7839
0.7904
0.8056
0.8196
0.0632
0.0564
0.0509
0.0409
0.0341
53.06
57.54
61.69
70.93
78.99
228.43
230.28
231.97
235.64
238.74
53.31
57.82
62.00
71.33
79.48
195.35
192.76
190.32
184.74
179.71
248.66
250.58
252.32
256.07
259.19
0.2089
0.2251
0.2399
0.2723
0.2999
0.9177
0.9160
0.9145
0.9117
0.9097
3.2
3.6
4.0
5.0
6.0
7.0
8.0
9.0
10.0
12.0
26.72
31.33
35.53
39.39
46.32
0.8328
0.8454
0.8576
0.8695
0.8928
0.0292
0.0255
0.0226
0.0202
0.0166
86.19
92.75
98.79
104.42
114.69
241.42
243.78
245.88
247.77
251.03
86.78
93.42
99.56
105.29
115.76
175.07
170.73
166.62
162.68
155.23
261.85
264.15
266.18
267.97
270.99
0.3242
0.3459
0.3656
0.3838
0.4164
0.9080
0.9066
0.9054
0.9043
0.9023
7.0
8.0
9.0
10.0
12.0
14.0
16.0
18.0
20.0
25.0
30.0
52.43
57.92
62.91
67.49
77.59
86.22
0.9159
0.9392
0.9631
0.9878
1.0562
1.1416
0.0140
0.0121
0.0105
0.0093
0.0069
0.0053
123.98
132.52
140.49
148.02
165.48
181.88
253.74
256.00
257.88
259.41
261.84
262.16
125.26
134.02
142.22
149.99
168.12
185.30
148.14
141.31
134.60
127.95
111.06
92.71
273.40
275.33
276.83
277.94
279.17
278.01
0.4453
0.4714
0.4954
0.5178
0.5687
0.6156
0.9003
0.8982
0.8959
0.8934
0.8854
0.8735
14.0
16.0
18.0
20.0
25.0
30.0
Copyright © 2006. Wiley. All rights reserved.
Press.
bar
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
R-134a
TABLE A-11
737
738
Tables in SI Units
TABLE A-12
T
C
v
m3/kg
Properties of Superheated Refrigerant 134a Vapor
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
Copyright © 2006. Wiley. All rights reserved.
R-134a
p 0.6 bar 0.06 MPa
(Tsat 37.07C)
v
m3/kg
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
p 1.0 bar 0.10 MPa
(Tsat 26.43C)
Sat.
20
10
0.31003
0.33536
0.34992
206.12
217.86
224.97
224.72
237.98
245.96
0.9520
1.0062
1.0371
0.19170
0.19770
0.20686
212.18
216.77
224.01
231.35
236.54
244.70
0.9395
0.9602
0.9918
0
10
20
0.36433
0.37861
0.39279
232.24
239.69
247.32
254.10
262.41
270.89
1.0675
1.0973
1.1267
0.21587
0.22473
0.23349
231.41
238.96
246.67
252.99
261.43
270.02
1.0227
1.0531
1.0829
30
40
50
0.40688
0.42091
0.43487
255.12
263.10
271.25
279.53
288.35
297.34
1.1557
1.1844
1.2126
0.24216
0.25076
0.25930
254.54
262.58
270.79
278.76
287.66
296.72
1.1122
1.1411
1.1696
60
70
80
90
0.44879
0.46266
0.47650
0.49031
279.58
288.08
296.75
305.58
306.51
315.84
325.34
335.00
1.2405
1.2681
1.2954
1.3224
0.26779
0.27623
0.28464
0.29302
279.16
287.70
296.40
305.27
305.94
315.32
324.87
334.57
1.1977
1.2254
1.2528
1.2799
p 1.4 bar 0.14 MPa
(Tsat 18.80C)
p 1.8 bar 0.18 MPa
(Tsat 12.73C)
Sat.
10
0
0.13945
0.14549
0.15219
216.52
223.03
230.55
236.04
243.40
251.86
0.9322
0.9606
0.9922
0.10983
0.11135
0.11678
219.94
222.02
229.67
239.71
242.06
250.69
0.9273
0.9362
0.9684
10
20
30
0.15875
0.16520
0.17155
238.21
246.01
253.96
260.43
269.13
277.97
1.0230
1.0532
1.0828
0.12207
0.12723
0.13230
237.44
245.33
253.36
259.41
268.23
277.17
0.9998
1.0304
1.0604
40
50
60
0.17783
0.18404
0.19020
262.06
270.32
278.74
286.96
296.09
305.37
1.1120
1.1407
1.1690
0.13730
0.14222
0.14710
261.53
269.85
278.31
286.24
295.45
304.79
1.0898
1.1187
1.1472
70
80
90
100
0.19633
0.20241
0.20846
0.21449
287.32
296.06
304.95
314.01
314.80
324.39
334.14
344.04
1.1969
1.2244
1.2516
1.2785
0.15193
0.15672
0.16148
0.16622
286.93
295.71
304.63
313.72
314.28
323.92
333.70
343.63
1.1753
1.2030
1.2303
1.2573
p 2.0 bar 0.20 MPa
(Tsat 10.09C)
p 2.4 bar 0.24 MPa
(Tsat 5.37C)
Sat.
10
0
0.09933
0.09938
0.10438
221.43
221.50
229.23
241.30
241.38
250.10
0.9253
0.9256
0.9582
0.08343
224.07
244.09
0.9222
0.08574
228.31
248.89
0.9399
10
20
30
0.10922
0.11394
0.11856
237.05
244.99
253.06
258.89
267.78
276.77
0.9898
1.0206
1.0508
0.08993
0.09399
0.09794
236.26
244.30
252.45
257.84
266.85
275.95
0.9721
1.0034
1.0339
40
50
60
0.12311
0.12758
0.13201
261.26
269.61
278.10
285.88
295.12
304.50
1.0804
1.1094
1.1380
0.10181
0.10562
0.10937
260.72
269.12
277.67
285.16
294.47
303.91
1.0637
1.0930
1.1218
70
80
90
100
0.13639
0.14073
0.14504
0.14932
286.74
295.53
304.47
313.57
314.02
323.68
333.48
343.43
1.1661
1.1939
1.2212
1.2483
0.11307
0.11674
0.12037
0.12398
286.35
295.18
304.15
313.27
313.49
323.19
333.04
343.03
1.1501
1.1780
1.2055
1.2326
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
(Continued)
T
C
v
m3/kg
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
p 2.8 bar 0.28 MPa
(Tsat 1.23C)
Sat.
0
10
20
30
40
50
60
70
80
90
100
110
120
0.07193
0.07240
0.07613
0.07972
0.08320
0.08660
0.08992
0.09319
0.09641
0.09960
0.10275
0.10587
0.10897
0.11205
226.38
227.37
235.44
243.59
251.83
260.17
268.64
277.23
285.96
294.82
303.83
312.98
322.27
331.71
246.52
247.64
256.76
265.91
275.12
284.42
293.81
303.32
312.95
322.71
332.60
342.62
352.78
363.08
0.05089
0.05119
0.05397
0.05662
0.05917
0.06164
0.06405
0.06641
0.06873
0.07102
0.07327
0.07550
0.07771
0.07991
0.08208
231.97
232.87
241.37
249.89
258.47
267.13
275.89
284.75
293.73
302.84
312.07
321.44
330.94
340.58
350.35
252.32
253.35
262.96
272.54
282.14
291.79
301.51
311.32
321.23
331.25
341.38
351.64
362.03
372.54
383.18
0.9197
0.9238
0.9566
0.9883
1.0192
1.0494
1.0789
1.1079
1.1364
1.1644
1.1920
1.2193
1.2461
1.2727
Copyright © 2006. Wiley. All rights reserved.
0.03408
0.03581
0.03774
0.03958
0.04134
0.04304
0.04469
0.04631
0.04790
0.04946
0.05099
0.05251
0.05402
0.05550
0.05698
238.74
246.41
255.45
264.48
273.54
282.66
291.86
301.14
310.53
320.03
329.64
339.38
349.23
359.21
369.32
259.19
267.89
278.09
288.23
298.35
308.48
318.67
328.93
339.27
349.70
360.24
370.88
381.64
392.52
403.51
h
kJ/kg
s
kJ/kg # K
0.06322
228.43
248.66
0.9177
0.06576
0.06901
0.07214
0.07518
0.07815
0.08106
0.08392
0.08674
0.08953
0.09229
0.09503
0.09774
234.61
242.87
251.19
259.61
268.14
276.79
285.56
294.46
303.50
312.68
322.00
331.45
255.65
264.95
274.28
283.67
293.15
302.72
312.41
322.22
332.15
342.21
352.40
362.73
0.9427
0.9749
1.0062
1.0367
1.0665
1.0957
1.1243
1.1525
1.1802
1.2076
1.2345
1.2611
p 5.0 bar 0.50 MPa
(Tsat 15.74C)
0.9145
0.9182
0.9515
0.9837
1.0148
1.0452
1.0748
1.1038
1.1322
1.1602
1.1878
1.2149
1.2417
1.2681
1.2941
p 6.0 bar 0.60 MPa
(Tsat 21.58C)
Sat.
30
40
50
60
70
80
90
100
110
120
130
140
150
160
u
kJ/kg
p 3.2 bar 0.32 MPa
(Tsat 2.48C)
p 4.0 bar 0.40 MPa
(Tsat 8.93C)
Sat.
10
20
30
40
50
60
70
80
90
100
110
120
130
140
v
m3/kg
R-134a
TABLE A-12
0.04086
235.64
256.07
0.9117
0.04188
0.04416
0.04633
0.04842
0.05043
0.05240
0.05432
0.05620
0.05805
0.05988
0.06168
0.06347
0.06524
239.40
248.20
256.99
265.83
274.73
283.72
292.80
302.00
311.31
320.74
330.30
339.98
349.79
260.34
270.28
280.16
290.04
299.95
309.92
319.96
330.10
340.33
350.68
361.14
371.72
382.42
0.9264
0.9597
0.9918
1.0229
1.0531
1.0825
1.1114
1.1397
1.1675
1.1949
1.2218
1.2484
1.2746
p 7.0 bar 0.70 MPa
(Tsat 26.72C)
0.9097
0.9388
0.9719
1.0037
1.0346
1.0645
1.0938
1.1225
1.1505
1.1781
1.2053
1.2320
1.2584
1.2844
1.3100
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
0.02918
0.02979
0.03157
0.03324
0.03482
0.03634
0.03781
0.03924
0.04064
0.04201
0.04335
0.04468
0.04599
0.04729
0.04857
241.42
244.51
253.83
263.08
272.31
281.57
290.88
300.27
309.74
319.31
328.98
338.76
348.66
358.68
368.82
261.85
265.37
275.93
286.35
296.69
307.01
317.35
327.74
338.19
348.71
359.33
370.04
380.86
391.79
402.82
0.9080
0.9197
0.9539
0.9867
1.0182
1.0487
1.0784
1.1074
1.1358
1.1637
1.1910
1.2179
1.2444
1.2706
1.2963
739
TABLE A-12
T
C
v
m3/kg
(Continued)
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
p 8.0 bar 0.80 MPa
(Tsat 31.33C)
R-134a
Sat.
40
50
60
70
80
90
100
110
120
130
140
150
160
170
180
0.02547
0.02691
0.02846
0.02992
0.03131
0.03264
0.03393
0.03519
0.03642
0.03762
0.03881
0.03997
0.04113
0.04227
0.04340
0.04452
243.78
252.13
261.62
271.04
280.45
289.89
299.37
308.93
318.57
328.31
338.14
348.09
358.15
368.32
378.61
389.02
264.15
273.66
284.39
294.98
305.50
316.00
326.52
337.08
347.71
358.40
369.19
380.07
391.05
402.14
413.33
424.63
0.02020
0.02029
0.02171
0.02301
0.02423
0.02538
0.02649
0.02755
0.02858
0.02959
0.03058
0.03154
0.03250
0.03344
0.03436
0.03528
247.77
248.39
258.48
268.35
278.11
287.82
297.53
307.27
317.06
326.93
336.88
346.92
357.06
367.31
377.66
388.12
267.97
268.68
280.19
291.36
302.34
313.20
324.01
334.82
345.65
356.52
367.46
378.46
389.56
400.74
412.02
423.40
0.9066
0.9374
0.9711
1.0034
1.0345
1.0647
1.0940
1.1227
1.1508
1.1784
1.2055
1.2321
1.2584
1.2843
1.3098
1.3351
Copyright © 2006. Wiley. All rights reserved.
0.01405
0.01495
0.01603
0.01701
0.01792
0.01878
0.01960
0.02039
0.02115
0.02189
0.02262
0.02333
0.02403
0.02472
0.02541
0.02608
253.74
262.17
272.87
283.29
293.55
303.73
313.88
324.05
334.25
344.50
354.82
365.22
375.71
386.29
396.96
407.73
273.40
283.10
295.31
307.10
318.63
330.02
341.32
352.59
363.86
375.15
386.49
397.89
409.36
420.90
432.53
444.24
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
740
h
kJ/kg
s
kJ/kg # K
0.02255
0.02325
0.02472
0.02609
0.02738
0.02861
0.02980
0.03095
0.03207
0.03316
0.03423
0.03529
0.03633
0.03736
0.03838
0.03939
245.88
250.32
260.09
269.72
279.30
288.87
298.46
308.11
317.82
327.62
337.52
347.51
357.61
367.82
378.14
388.57
266.18
271.25
282.34
293.21
303.94
314.62
325.28
335.96
346.68
357.47
368.33
379.27
390.31
401.44
412.68
424.02
0.9054
0.9217
0.9566
0.9897
1.0214
1.0521
1.0819
1.1109
1.1392
1.1670
1.1943
1.2211
1.2475
1.2735
1.2992
1.3245
p 12.0 bar 1.20 MPa
(Tsat 46.32C)
0.9043
0.9066
0.9428
0.9768
1.0093
1.0405
1.0707
1.1000
1.1286
1.1567
1.1841
1.2111
1.2376
1.2638
1.2895
1.3149
p 14.0 bar 1.40 MPa
(Tsat 52.43C)
Sat.
60
70
80
90
100
110
120
130
140
150
160
170
180
190
200
u
kJ/kg
p 9.0 bar 0.90 MPa
(Tsat 35.53C)
p 10.0 bar 1.00 MPa
(Tsat 39.39C)
Sat.
40
50
60
70
80
90
100
110
120
130
140
150
160
170
180
v
m3/kg
0.01663
251.03
270.99
0.9023
0.01712
0.01835
0.01947
0.02051
0.02150
0.02244
0.02335
0.02423
0.02508
0.02592
0.02674
0.02754
0.02834
0.02912
254.98
265.42
275.59
285.62
295.59
305.54
315.50
325.51
335.58
345.73
355.95
366.27
376.69
387.21
275.52
287.44
298.96
310.24
321.39
332.47
343.52
354.58
365.68
376.83
388.04
399.33
410.70
422.16
0.9164
0.9527
0.9868
1.0192
1.0503
1.0804
1.1096
1.1381
1.1660
1.1933
1.2201
1.2465
1.2724
1.2980
p 16.0 bar 1.60 MPa
(Tsat 57.92C)
0.9003
0.9297
0.9658
0.9997
1.0319
1.0628
1.0927
1.1218
1.1501
1.1777
1.2048
1.2315
1.2576
1.2834
1.3088
1.3338
0.01208
0.01233
0.01340
0.01435
0.01521
0.01601
0.01677
0.01750
0.01820
0.01887
0.01953
0.02017
0.02080
0.02142
0.02203
0.02263
256.00
258.48
269.89
280.78
291.39
301.84
312.20
322.53
332.87
343.24
353.66
364.15
374.71
385.35
396.08
406.90
275.33
278.20
291.33
303.74
315.72
327.46
339.04
350.53
361.99
373.44
384.91
396.43
407.99
419.62
431.33
443.11
0.8982
0.9069
0.9457
0.9813
1.0148
1.0467
1.0773
1.1069
1.1357
1.1638
1.1912
1.2181
1.2445
1.2704
1.2960
1.3212
Tables in SI Units
Copyright © 2006. Wiley. All rights reserved.
Properties of Saturated Ammonia (Liquid–Vapor): Temperature Table
Specific Volume
m3/kg
Internal Energy
kJ/kg
Enthalpy
kJ/kg
Entropy
kJ/kg # K
Temp.
C
Press.
bar
Sat.
Liquid
vf 103
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Temp.
C
50
45
40
36
32
0.4086
0.5453
0.7174
0.8850
1.0832
1.4245
1.4367
1.4493
1.4597
1.4703
2.6265
2.0060
1.5524
1.2757
1.0561
43.94
22.03
0.10
17.47
35.09
1264.99
1271.19
1277.20
1281.87
1286.41
43.88
21.95
0.00
17.60
35.25
1416.20
1402.52
1388.56
1377.17
1365.55
1372.32
1380.57
1388.56
1394.77
1400.81
0.1922
0.0951
0.0000
0.0747
0.1484
6.1543
6.0523
5.9557
5.8819
5.8111
50
45
40
36
32
30
28
26
22
20
1.1950
1.3159
1.4465
1.7390
1.9019
1.4757
1.4812
1.4867
1.4980
1.5038
0.9634
0.8803
0.8056
0.6780
0.6233
43.93
52.78
61.65
79.46
88.40
1288.63
1290.82
1292.97
1297.18
1299.23
44.10
52.97
61.86
79.72
88.68
1359.65
1353.68
1347.65
1335.36
1329.10
1403.75
1406.66
1409.51
1415.08
1417.79
0.1849
0.2212
0.2572
0.3287
0.3642
5.7767
5.7430
5.7100
5.6457
5.6144
30
28
26
22
20
18
16
14
12
10
2.0769
2.2644
2.4652
2.6798
2.9089
1.5096
1.5155
1.5215
1.5276
1.5338
0.5739
0.5291
0.4885
0.4516
0.4180
97.36
106.36
115.37
124.42
133.50
1301.25
1303.23
1305.17
1307.08
1308.95
97.68
106.70
115.75
124.83
133.94
1322.77
1316.35
1309.86
1303.28
1296.61
1420.45
1423.05
1425.61
1428.11
1430.55
0.3994
0.4346
0.4695
0.5043
0.5389
5.5837
5.5536
5.5239
5.4948
5.4662
18
16
14
12
10
8
6
4
2
0
3.1532
3.4134
3.6901
3.9842
4.2962
1.5400
1.5464
1.5528
1.5594
1.5660
0.3874
0.3595
0.3340
0.3106
0.2892
142.60
151.74
160.88
170.07
179.29
1310.78
1312.57
1314.32
1316.04
1317.71
143.09
152.26
161.46
170.69
179.96
1289.86
1283.02
1276.10
1269.08
1261.97
1432.95
1435.28
1437.56
1439.78
1441.94
0.5734
0.6077
0.6418
0.6759
0.7097
5.4380
5.4103
5.3831
5.3562
5.3298
8
6
4
2
0
2
4
6
8
10
4.6270
4.9773
5.3479
5.7395
6.1529
1.5727
1.5796
1.5866
1.5936
1.6008
0.2695
0.2514
0.2348
0.2195
0.2054
188.53
197.80
207.10
216.42
225.77
1319.34
1320.92
1322.47
1323.96
1325.42
189.26
198.59
207.95
217.34
226.75
1254.77
1247.48
1240.09
1232.61
1225.03
1444.03
1446.07
1448.04
1449.94
1451.78
0.7435
0.7770
0.8105
0.8438
0.8769
5.3038
5.2781
5.2529
5.2279
5.2033
2
4
6
8
10
12
16
20
24
28
6.5890
7.5324
8.5762
9.7274
10.993
1.6081
1.6231
1.6386
1.6547
1.6714
0.1923
0.1691
0.1492
0.1320
0.1172
235.14
253.95
272.86
291.84
310.92
1326.82
1329.48
1331.94
1334.19
1336.20
236.20
255.18
274.26
293.45
312.75
1217.35
1201.70
1185.64
1169.16
1152.24
1453.55
1456.87
1459.90
1462.61
1465.00
0.9099
0.9755
1.0404
1.1048
1.1686
5.1791
5.1314
5.0849
5.0394
4.9948
12
16
20
24
28
32
36
40
45
50
12.380
13.896
15.549
17.819
20.331
1.6887
1.7068
1.7256
1.7503
1.7765
0.1043
0.0930
0.0831
0.0725
0.0634
330.07
349.32
368.67
393.01
417.56
1337.97
1339.47
1340.70
1341.81
1342.42
332.17
351.69
371.35
396.13
421.17
1134.87
1117.00
1098.62
1074.84
1050.09
1467.03
1468.70
1469.97
1470.96
1471.26
1.2319
1.2946
1.3569
1.4341
1.5109
4.9509
4.9078
4.8652
4.8125
4.7604
32
36
40
45
50
Source: Tables A-13 through A-15 are calculated based on equations from L. Haar and J. S. Gallagher, “Thermodynamic Properties of Ammonia,”
J. Phys. Chem. Reference Data, Vol. 7, 1978, pp. 635–792.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Ammonia
TABLE A-13
741
742
Tables in SI Units
TABLE A-14
Properties of Saturated Ammonia (Liquid–Vapor): Pressure Table
Copyright © 2006. Wiley. All rights reserved.
Ammonia
Specific Volume
m3/kg
Internal Energy
kJ/kg
Enthalpy
kJ/kg
Entropy
kJ/kg # K
Press.
bar
Temp.
C
Sat.
Liquid
vf 103
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Press.
bar
0.40
0.50
0.60
0.70
0.80
0.90
50.36
46.53
43.28
40.46
37.94
35.67
1.4236
1.4330
1.4410
1.4482
1.4546
1.4605
2.6795
2.1752
1.8345
1.5884
1.4020
1.2559
45.52
28.73
14.51
2.11
8.93
18.91
1264.54
1269.31
1273.27
1276.66
1279.61
1282.24
45.46
28.66
14.42
2.01
9.04
19.04
1417.18
1406.73
1397.76
1389.85
1382.73
1376.23
1371.72
1378.07
1383.34
1387.84
1391.78
1395.27
0.1992
0.1245
0.0622
0.0086
0.0386
0.0808
6.1618
6.0829
6.0186
5.9643
5.9174
5.8760
0.40
0.50
0.60
0.70
0.80
0.90
1.00
1.25
1.50
1.75
2.00
33.60
29.07
25.22
21.86
18.86
1.4660
1.4782
1.4889
1.4984
1.5071
1.1381
0.9237
0.7787
0.6740
0.5946
28.03
48.03
65.10
80.08
93.50
1284.61
1289.65
1293.80
1297.33
1300.39
28.18
48.22
65.32
80.35
93.80
1370.23
1356.89
1345.28
1334.92
1325.51
1398.41
1405.11
1410.61
1415.27
1419.31
0.1191
0.2018
0.2712
0.3312
0.3843
5.8391
5.7610
5.6973
5.6435
5.5969
1.00
1.25
1.50
1.75
2.00
2.25
2.50
2.75
3.00
3.25
16.15
13.67
11.37
9.24
7.24
1.5151
1.5225
1.5295
1.5361
1.5424
0.5323
0.4821
0.4408
0.4061
0.3765
105.68
116.88
127.26
136.96
146.06
1303.08
1305.49
1307.67
1309.65
1311.46
106.03
117.26
127.68
137.42
146.57
1316.83
1308.76
1301.20
1294.05
1287.27
1422.86
1426.03
1428.88
1431.47
1433.84
0.4319
0.4753
0.5152
0.5520
0.5864
5.5558
5.5190
5.4858
5.4554
5.4275
2.25
2.50
2.75
3.00
3.25
3.50
3.75
4.00
4.25
4.50
5.36
3.58
1.90
0.29
1.25
1.5484
1.5542
1.5597
1.5650
1.5702
0.3511
0.3289
0.3094
0.2921
0.2767
154.66
162.80
170.55
177.96
185.04
1313.14
1314.68
1316.12
1317.47
1318.73
155.20
163.38
171.18
178.62
185.75
1280.81
1274.64
1268.71
1263.01
1257.50
1436.01
1438.03
1439.89
1441.63
1443.25
0.6186
0.6489
0.6776
0.7048
0.7308
5.4016
5.3774
5.3548
5.3336
5.3135
3.50
3.75
4.00
4.25
4.50
4.75
5.00
5.25
5.50
5.75
2.72
4.13
5.48
6.79
8.05
1.5752
1.5800
1.5847
1.5893
1.5938
0.2629
0.2503
0.2390
0.2286
0.2191
191.84
198.39
204.69
210.78
216.66
1319.91
1321.02
1322.07
1323.06
1324.00
192.59
199.18
205.52
211.65
217.58
1252.18
1247.02
1242.01
1237.15
1232.41
1444.77
1446.19
1447.53
1448.80
1449.99
0.7555
0.7791
0.8018
0.8236
0.8446
5.2946
5.2765
5.2594
5.2430
5.2273
4.75
5.00
5.25
5.50
5.75
6.00
7.00
8.00
9.00
10.00
9.27
13.79
17.84
21.52
24.89
1.5982
1.6148
1.6302
1.6446
1.6584
0.2104
0.1815
0.1596
0.1424
0.1285
222.37
243.56
262.64
280.05
296.10
1324.89
1328.04
1330.64
1332.82
1334.66
223.32
244.69
263.95
281.53
297.76
1227.79
1210.38
1194.36
1179.44
1165.42
1451.12
1455.07
1458.30
1460.97
1463.18
0.8649
0.9394
1.0054
1.0649
1.1191
5.2122
5.1576
5.1099
5.0675
5.0294
6.00
7.00
8.00
9.00
10.00
12.00
14.00
16.00
18.00
20.00
30.94
36.26
41.03
45.38
49.37
1.6841
1.7080
1.7306
1.7522
1.7731
0.1075
0.0923
0.0808
0.0717
0.0644
324.99
350.58
373.69
394.85
414.44
1337.52
1339.56
1340.97
1341.88
1342.37
327.01
352.97
376.46
398.00
417.99
1139.52
1115.82
1093.77
1073.01
1053.27
1466.53
1468.79
1470.23
1471.01
1471.26
1.2152
1.2987
1.3729
1.4399
1.5012
4.9625
4.9050
4.8542
4.8086
4.7670
12.00
14.00
16.00
18.00
20.00
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in SI Units
T
C
v
m3/kg
Properties of Superheated Ammonia Vapor
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
v
m3/kg
p 0.4 bar 0.04 MPa
(Tsat 50.36C)
h
kJ/kg
s
kJ/kg # K
p 0.6 bar 0.06 MPa
(Tsat 43.28C)
Sat.
50
45
2.6795
2.6841
2.7481
1264.54
1265.11
1273.05
1371.72
1372.48
1382.98
6.1618
6.1652
6.2118
1.8345
1273.27
1383.34
6.0186
40
35
30
2.8118
2.8753
2.9385
1281.01
1288.96
1296.93
1393.48
1403.98
1414.47
6.2573
6.3018
6.3455
1.8630
1.9061
1.9491
1278.62
1286.75
1294.88
1390.40
1401.12
1411.83
6.0490
6.0946
6.1390
25
20
15
3.0015
3.0644
3.1271
1304.90
1312.88
1320.87
1424.96
1435.46
1445.95
6.3882
6.4300
6.4711
1.9918
2.0343
2.0766
1303.01
1311.13
1319.25
1422.52
1433.19
1443.85
6.1826
6.2251
6.2668
10
5
0
5
3.1896
3.2520
3.3142
3.3764
1328.87
1336.88
1344.90
1352.95
1456.45
1466.95
1477.47
1488.00
6.5114
6.5509
6.5898
6.6280
2.1188
2.1609
2.2028
2.2446
1327.37
1335.49
1343.61
1351.75
1454.50
1465.14
1475.78
1486.43
6.3077
6.3478
6.3871
6.4257
p 0.8 bar 0.08 MPa
(Tsat 37.94C)
Copyright © 2006. Wiley. All rights reserved.
u
kJ/kg
p 1.0 bar 0.10 MPa
(Tsat 33.60C)
Sat.
35
30
1.4021
1.4215
1.4543
1279.61
1284.51
1292.81
1391.78
1398.23
1409.15
5.9174
5.9446
5.9900
1.1381
1284.61
1398.41
5.8391
1.1573
1290.71
1406.44
5.8723
25
20
15
1.4868
1.5192
1.5514
1301.09
1309.36
1317.61
1420.04
1430.90
1441.72
6.0343
6.0777
6.1200
1.1838
1.2101
1.2362
1299.15
1307.57
1315.96
1417.53
1428.58
1439.58
5.9175
5.9616
6.0046
10
5
0
1.5834
1.6153
1.6471
1325.85
1334.09
1342.31
1452.53
1463.31
1474.08
6.1615
6.2021
6.2419
1.2621
1.2880
1.3136
1324.33
1332.67
1341.00
1450.54
1461.47
1472.37
6.0467
6.0878
6.1281
5
10
15
20
1.6788
1.7103
1.7418
1.7732
1350.54
1358.77
1367.01
1375.25
1484.84
1495.60
1506.35
1517.10
6.2809
6.3192
6.3568
6.3939
1.3392
1.3647
1.3900
1.4153
1349.33
1357.64
1365.95
1374.27
1483.25
1494.11
1504.96
1515.80
6.1676
6.2063
6.2442
6.2816
p 1.5 bar 0.15 MPa
(Tsat 25.22C)
p 2.0 bar 0.20 MPa
(Tsat 18.86C)
Sat.
25
20
0.7787
0.7795
0.7978
1293.80
1294.20
1303.00
1410.61
1411.13
1422.67
5.6973
5.6994
5.7454
0.59460
1300.39
1419.31
5.5969
15
10
5
0.8158
0.8336
0.8514
1311.75
1320.44
1329.08
1434.12
1445.49
1456.79
5.7902
5.8338
5.8764
0.60542
0.61926
0.63294
1307.43
1316.46
1325.41
1428.51
1440.31
1452.00
5.6328
5.6781
5.7221
0
5
10
0.8689
0.8864
0.9037
1337.68
1346.25
1354.78
1468.02
1479.20
1490.34
5.9179
5.9585
5.9981
0.64648
0.65989
0.67320
1334.29
1343.11
1351.87
1463.59
1475.09
1486.51
5.7649
5.8066
5.8473
0.68640
0.69952
0.71256
0.72553
1360.59
1369.28
1377.93
1386.56
1497.87
1509.18
1520.44
1531.67
5.8871
5.9260
5.9641
6.0014
15 0.9210
1363.29 1501.44
6.0370
20 0.9382
1371.79 1512.51
6.0751
25 0.9553
1380.28 1523.56
6.1125
Moran, M. J., & Shapiro,
(2006). Fundamentals
thermodynamics.
30 H. N.0.9723
1388.76of engineering
1534.60
6.1492 Wiley.
Created from purdue on 2022-01-24 17:56:53.
Ammonia
TABLE A-15
743
744
Tables in SI Units
TABLE A-15
T
C
v
m3/kg
(Continued)
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
v
m3/kg
p 2.5 bar 0.25 MPa
(Tsat 13.67C)
Ammonia
h
kJ/kg
s
kJ/kg # K
p 3.0 bar 0.30 MPa
(Tsat 9.24C)
Sat.
10
5
0.48213
0.49051
0.50180
1305.49
1312.37
1321.65
1426.03
1435.00
1447.10
5.5190
5.5534
5.5989
0.40607
1309.65
1431.47
5.4554
0.41428
1317.80
1442.08
5.4953
0
5
10
0.51293
0.52393
0.53482
1330.83
1339.91
1348.91
1459.06
1470.89
1482.61
5.6431
5.6860
5.7278
0.42382
0.43323
0.44251
1327.28
1336.64
1345.89
1454.43
1466.61
1478.65
5.5409
5.5851
5.6280
15
20
25
0.54560
0.55630
0.56691
1357.84
1366.72
1375.55
1494.25
1505.80
1517.28
5.7685
5.8083
5.8471
0.45169
0.46078
0.46978
1355.05
1364.13
1373.14
1490.56
1502.36
1514.07
5.6697
5.7103
5.7499
30
35
40
45
0.57745
0.58793
0.59835
0.60872
1384.34
1393.10
1401.84
1410.56
1528.70
1540.08
1551.42
1562.74
5.8851
5.9223
5.9589
5.9947
0.47870
0.48756
0.49637
0.50512
1382.09
1391.00
1399.86
1408.70
1525.70
1537.26
1548.77
1560.24
5.7886
5.8264
5.8635
5.8998
p 3.5 bar 0.35 MPa
(Tsat 5.36C)
Copyright © 2006. Wiley. All rights reserved.
u
kJ/kg
p 4.0 bar 0.40 MPa
(Tsat 1.90C)
Sat.
0
10
0.35108
0.36011
0.37654
1313.14
1323.66
1342.82
1436.01
1449.70
1474.61
5.4016
5.4522
5.5417
0.30942
0.31227
0.32701
1316.12
1319.95
1339.68
1439.89
1444.86
1470.49
5.3548
5.3731
5.4652
20
30
40
0.39251
0.40814
0.42350
1361.49
1379.81
1397.87
1498.87
1522.66
1546.09
5.6259
5.7057
5.7818
0.34129
0.35520
0.36884
1358.81
1377.49
1395.85
1495.33
1519.57
1543.38
5.5515
5.6328
5.7101
60
80
100
0.45363
0.48320
0.51240
1433.55
1469.06
1504.73
1592.32
1638.18
1684.07
5.9249
6.0586
6.1850
0.39550
0.42160
0.44733
1431.97
1467.77
1503.64
1590.17
1636.41
1682.58
5.8549
5.9897
6.1169
120
140
160
0.54136
0.57013
0.59876
1540.79
1577.38
1614.60
1730.26
1776.92
1824.16
6.3056
6.4213
6.5330
0.47280
0.49808
0.52323
1539.85
1576.55
1613.86
1728.97
1775.79
1823.16
6.2380
6.3541
6.4661
180
200
0.62728
0.65572
1652.51
1691.15
1872.06
1920.65
6.6411
6.7460
0.54827
0.57322
1651.85
1690.56
1871.16
1919.85
6.5744
6.6796
p 4.5 bar 0.45 MPa
(Tsat 1.25C)
p 5.0 bar 0.50 MPa
(Tsat 4.13C)
Sat.
10
20
0.27671
0.28846
0.30142
1318.73
1336.48
1356.09
1443.25
1466.29
1491.72
5.3135
5.3962
5.4845
0.25034
0.25757
0.26949
1321.02
1333.22
1353.32
1446.19
1462.00
1488.06
5.2765
5.3330
5.4234
30
40
60
0.31401
0.32631
0.35029
1375.15
1393.80
1430.37
1516.45
1540.64
1588.00
5.5674
5.6460
5.7926
0.28103
0.29227
0.31410
1372.76
1391.74
1428.76
1513.28
1537.87
1585.81
5.5080
5.5878
5.7362
80
100
120
0.37369
0.39671
0.41947
1466.47
1502.55
1538.91
1634.63
1681.07
1727.67
5.9285
6.0564
6.1781
0.33535
0.35621
0.37681
1465.16
1501.46
1537.97
1632.84
1679.56
1726.37
5.8733
6.0020
6.1242
140 0.44205 1575.73 1774.65
160 0.46448 1613.13 1822.15
180 0.48681 1651.20 1870.26
200
0.50905
1689.97Wiley.1919.04
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals
of engineering
thermodynamics.
6.2946
6.4069
6.5155
6.6208
0.39722
0.41749
0.43765
0.45771
1574.90
1612.40
1650.54
1689.38
1773.51
1821.14
1869.36
1918.24
6.2412
6.3537
6.4626
6.5681
Created from purdue on 2022-01-24 17:56:53.
Tables in SI Units
T
C
v
m3/kg
(Continued)
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
v
m3/kg
p 5.5 bar 0.55 MPa
(Tsat 6.79C)
h
kJ/kg
s
kJ/kg # K
p 6.0 bar 0.60 MPa
(Tsat 9.27C)
Sat.
10
20
0.22861
0.23227
0.24335
1323.06
1329.88
1350.50
1448.80
1457.63
1484.34
5.2430
5.2743
5.3671
0.21038
0.21115
0.22155
1324.89
1326.47
1347.62
1451.12
1453.16
1480.55
5.2122
5.2195
5.3145
30
40
50
0.25403
0.26441
0.27454
1370.35
1389.64
1408.53
1510.07
1535.07
1559.53
5.4534
5.5345
5.6114
0.23152
0.24118
0.25059
1367.90
1387.52
1406.67
1506.81
1532.23
1557.03
5.4026
5.4851
5.5631
60
80
100
0.28449
0.30398
0.32307
1427.13
1463.85
1500.36
1583.60
1631.04
1678.05
5.6848
5.8230
5.9525
0.25981
0.27783
0.29546
1425.49
1462.52
1499.25
1581.38
1629.22
1676.52
5.6373
5.7768
5.9071
120
140
160
0.34190
0.36054
0.37903
1537.02
1574.07
1611.66
1725.07
1772.37
1820.13
6.0753
6.1926
6.3055
0.31281
0.32997
0.34699
1536.07
1573.24
1610.92
1723.76
1771.22
1819.12
6.0304
6.1481
6.2613
180
200
0.39742
0.41571
1649.88
1688.79
1868.46
1917.43
6.4146
6.5203
0.36390
0.38071
1649.22
1688.20
1867.56
1916.63
6.3707
6.4766
p 7.0 bar 0.70 MPa
(Tsat 13.79C)
Copyright © 2006. Wiley. All rights reserved.
u
kJ/kg
p 8.0 bar 0.80 MPa
(Tsat 17.84C)
Sat.
20
30
0.18148
0.18721
0.19610
1328.04
1341.72
1362.88
1455.07
1472.77
1500.15
5.1576
5.2186
5.3104
0.15958
0.16138
0.16948
1330.64
1335.59
1357.71
1458.30
1464.70
1493.29
5.1099
5.1318
5.2277
40
50
60
0.20464
0.21293
0.22101
1383.20
1402.90
1422.16
1526.45
1551.95
1576.87
5.3958
5.4760
5.5519
0.17720
0.18465
0.19189
1378.77
1399.05
1418.77
1520.53
1546.77
1572.28
5.3161
5.3986
5.4763
80
100
120
0.23674
0.25205
0.26709
1459.85
1497.02
1534.16
1625.56
1673.46
1721.12
5.6939
5.8258
5.9502
0.20590
0.21949
0.23280
1457.14
1494.77
1532.24
1621.86
1670.37
1718.48
5.6209
5.7545
5.8801
140
160
180
200
0.28193
0.29663
0.31121
0.32571
1571.57
1609.44
1647.90
1687.02
1768.92
1817.08
1865.75
1915.01
6.0688
6.1826
6.2925
6.3988
0.24590
0.25886
0.27170
0.28445
1569.89
1607.96
1646.57
1685.83
1766.61
1815.04
1863.94
1913.39
5.9995
6.1140
6.2243
6.3311
p 9.0 bar 0.90 MPa
(Tsat 21.52C)
p 10.0 bar 1.00 MPa
(Tsat 24.89C)
Sat.
30
40
0.14239
0.14872
0.15582
1332.82
1352.36
1374.21
1460.97
1486.20
1514.45
5.0675
5.1520
5.2436
0.12852
0.13206
0.13868
1334.66
1346.82
1369.52
1463.18
1478.88
1508.20
5.0294
5.0816
5.1768
50
60
80
0.16263
0.16922
0.18191
1395.11
1415.32
1454.39
1541.47
1567.61
1618.11
5.3286
5.4083
5.5555
0.14499
0.15106
0.16270
1391.07
1411.79
1451.60
1536.06
1562.86
1614.31
5.2644
5.3460
5.4960
100
120
140
0.19416
0.20612
0.21788
1492.50
1530.30
1568.20
1667.24
1715.81
1764.29
5.6908
5.8176
5.9379
0.17389
0.18478
0.19545
1490.20
1528.35
1566.51
1664.10
1713.13
1761.96
5.6332
5.7612
5.8823
0.20598
0.21638
0.22670
1604.97
1643.91
1683.44
1810.94
1860.29
1910.14
5.9981
6.1095
6.2171
160 0.22948 1606.46 1813.00
6.0530
180 0.24097 1645.24 1862.12
6.1639
Moran, M. J., & Shapiro,
(2006). Fundamentals
thermodynamics.
200 H. N.0.25237
1684.64of engineering
1911.77
6.2711 Wiley.
Created from purdue on 2022-01-24 17:56:53.
Ammonia
TABLE A-15
745
746
Tables in SI Units
(Continued)
TABLE A-15
T
C
v
m3/kg
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
v
m3/kg
p 12.0 bar 1.20 MPa
(Tsat 30.94C)
Ammonia
Copyright © 2006. Wiley. All rights reserved.
h
kJ/kg
s
kJ/kg # K
p 14.0 bar 1.40 MPa
(Tsat 36.26C)
Sat.
40
60
0.10751
0.11287
0.12378
1337.52
1359.73
1404.54
1466.53
1495.18
1553.07
4.9625
5.0553
5.2347
0.09231
0.09432
0.10423
1339.56
1349.29
1396.97
1468.79
1481.33
1542.89
4.9050
4.9453
5.1360
80
100
120
0.13387
0.14347
0.15275
1445.91
1485.55
1524.41
1606.56
1657.71
1707.71
5.3906
5.5315
5.6620
0.11324
0.12172
0.12986
1440.06
1480.79
1520.41
1598.59
1651.20
1702.21
5.2984
5.4433
5.5765
140
160
180
0.16181
0.17072
0.17950
1563.09
1601.95
1641.23
1757.26
1806.81
1856.63
5.7850
5.9021
6.0145
0.13777
0.14552
0.15315
1559.63
1598.92
1638.53
1752.52
1802.65
1852.94
5.7013
5.8198
5.9333
200
220
240
0.18819
0.19680
0.20534
1681.05
1721.50
1762.63
1906.87
1957.66
2009.04
6.1230
6.2282
6.3303
0.16068
0.16813
0.17551
1678.64
1719.35
1760.72
1903.59
1954.73
2006.43
6.0427
6.1485
6.2513
260
280
0.21382
0.22225
1804.48
1847.04
2061.06
2113.74
6.4297
6.5267
0.18283
0.19010
1802.78
1845.55
2058.75
2111.69
6.3513
6.4488
p 16.0 bar 1.60 MPa
(Tsat 41.03C)
p 18.0 bar 1.80 MPa
(Tsat 45.38C)
Sat.
60
80
0.08079
0.08951
0.09774
1340.97
1389.06
1434.02
1470.23
1532.28
1590.40
4.8542
5.0461
5.2156
0.07174
0.07801
0.08565
1341.88
1380.77
1427.79
1471.01
1521.19
1581.97
4.8086
4.9627
5.1399
100
120
140
0.10539
0.11268
0.11974
1475.93
1516.34
1556.14
1644.56
1696.64
1747.72
5.3648
5.5008
5.6276
0.09267
0.09931
0.10570
1470.97
1512.22
1552.61
1637.78
1690.98
1742.88
5.2937
5.4326
5.5614
160
180
200
0.12663
0.13339
0.14005
1595.85
1635.81
1676.21
1798.45
1849.23
1900.29
5.7475
5.8621
5.9723
0.11192
0.11801
0.12400
1592.76
1633.08
1673.78
1794.23
1845.50
1896.98
5.6828
5.7985
5.9096
220
240
260
280
0.14663
0.15314
0.15959
0.16599
1717.18
1758.79
1801.07
1844.05
1951.79
2003.81
2056.42
2109.64
6.0789
6.1823
6.2829
6.3809
0.12991
0.13574
0.14152
0.14724
1715.00
1756.85
1799.35
1842.55
1948.83
2001.18
2054.08
2107.58
6.0170
6.1210
6.2222
6.3207
p 20.0 bar 2.00 MPa
(Tsat 49.37C)
Sat.
60
80
0.06445
0.06875
0.07596
1342.37
1372.05
1421.36
1471.26
1509.54
1573.27
4.7670
4.8838
5.0696
100
120
140
0.08248
0.08861
0.09447
1465.89
1508.03
1549.03
1630.86
1685.24
1737.98
5.2283
5.3703
5.5012
160
180
200
0.10016
0.10571
0.11116
1589.65
1630.32
1671.33
1789.97
1841.74
1893.64
5.6241
5.7409
5.8530
220 0.11652 1712.82 1945.87
240 0.12182 1754.90 1998.54
260 0.12706 1797.63 2051.74
280
0.13224
1841.03Wiley.2105.50
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals
of engineering
thermodynamics.
5.9611
6.0658
6.1675
6.2665
Created from purdue on 2022-01-24 17:56:53.
u
kJ/kg
Tables in SI Units
Properties of Saturated Propane (Liquid–Vapor): Temperature Table
Copyright © 2006. Wiley. All rights reserved.
Specific Volume
m3/kg
Internal Energy
kJ/kg
Enthalpy
kJ/kg
Entropy
kJ/kg # K
Temp.
C
Press.
bar
Sat.
Liquid
vf 103
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Temp.
C
100
90
80
70
60
0.02888
0.06426
0.1301
0.2434
0.4261
1.553
1.578
1.605
1.633
1.663
11.27
5.345
2.774
1.551
0.9234
128.4
107.8
87.0
65.8
44.4
319.5
329.3
339.3
349.5
359.9
128.4
107.8
87.0
65.8
44.3
480.4
471.4
462.4
453.1
443.5
352.0
363.6
375.4
387.3
399.2
0.634
0.519
0.408
0.301
0.198
2.140
2.055
1.986
1.929
1.883
100
90
80
70
60
50
40
30
20
10
0.7046
1.110
1.677
2.444
3.451
1.694
1.728
1.763
1.802
1.844
0.5793
0.3798
0.2585
0.1815
0.1309
22.5
0.2
22.6
45.9
69.8
370.4
381.0
391.6
402.4
413.2
22.4
0.0
22.9
46.3
70.4
433.6
423.2
412.1
400.5
388.0
411.2
423.2
435.0
446.8
458.4
0.098
0.000
0.096
0.190
0.282
1.845
1.815
1.791
1.772
1.757
50
40
30
20
10
0
4
8
12
16
4.743
5.349
6.011
6.732
7.515
1.890
1.910
1.931
1.952
1.975
0.09653
0.08591
0.07666
0.06858
0.06149
94.2
104.2
114.3
124.6
135.0
423.8
428.1
432.3
436.5
440.7
95.1
105.3
115.5
125.9
136.4
374.5
368.8
362.9
356.8
350.5
469.6
474.1
478.4
482.7
486.9
0.374
0.410
0.446
0.482
0.519
1.745
1.741
1.737
1.734
1.731
0
4
8
12
16
20
24
28
32
36
8.362
9.278
10.27
11.33
12.47
1.999
2.024
2.050
2.078
2.108
0.05525
0.04973
0.04483
0.04048
0.03659
145.4
156.1
166.9
177.8
188.9
444.8
448.9
452.9
456.7
460.6
147.1
158.0
169.0
180.2
191.6
343.9
337.0
329.9
322.4
314.6
491.0
495.0
498.9
502.6
506.2
0.555
0.591
0.627
0.663
0.699
1.728
1.725
1.722
1.720
1.717
20
24
28
32
36
40
44
48
52
56
13.69
15.00
16.40
17.89
19.47
2.140
2.174
2.211
2.250
2.293
0.03310
0.02997
0.02714
0.02459
0.02227
200.2
211.7
223.4
235.3
247.4
464.3
467.9
471.4
474.6
477.7
203.1
214.9
227.0
239.3
251.9
306.5
298.0
288.9
279.3
269.2
509.6
512.9
515.9
518.6
521.1
0.736
0.772
0.809
0.846
0.884
1.715
1.712
1.709
1.705
1.701
40
44
48
52
56
60
65
70
75
80
21.16
23.42
25.86
28.49
31.31
2.340
2.406
2.483
2.573
2.683
0.02015
0.01776
0.01560
0.01363
0.01182
259.8
275.7
292.3
309.5
327.6
480.6
483.6
486.1
487.8
488.2
264.8
281.4
298.7
316.8
336.0
258.4
243.8
227.7
209.8
189.2
523.2
525.2
526.4
526.6
525.2
0.921
0.969
1.018
1.069
1.122
1.697
1.690
1.682
1.671
1.657
60
65
70
75
80
85
90
95
96.7
34.36
37.64
41.19
42.48
2.827
3.038
3.488
4.535
0.01011
0.008415
0.006395
0.004535
347.2
369.4
399.8
434.9
486.9
482.2
467.4
434.9
356.9
380.8
414.2
454.2
164.7
133.1
79.5
0.0
521.6
513.9
493.7
457.2
1.178
1.242
1.330
1.437
1.638
1.608
1.546
1.437
85
90
95
96.7
Source: Tables A-16 through A-18 are calculated based on B. A. Younglove and J. F. Ely, “Thermophysical Properties of Fluids. II. Methane,
Ethane, Propane, Isobutane and Normal Butane,” J. Phys. Chem. Ref. Data, Vol. 16, No. 4, 1987, pp. 577–598.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Propane
TABLE A-16
747
748
Tables in SI Units
TABLE A-17
Properties of Saturated Propane (Liquid–Vapor): Pressure Table
Copyright © 2006. Wiley. All rights reserved.
Propane
Specific Volume
m3/kg
Internal Energy
kJ/kg
Enthalpy
kJ/kg
Entropy
kJ/kg # K
Press.
bar
Temp.
C
Sat.
Liquid
vf 103
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Press.
bar
0.05
0.10
0.25
0.50
0.75
93.28
83.87
69.55
56.93
48.68
1.570
1.594
1.634
1.672
1.698
6.752
3.542
1.513
0.7962
0.5467
114.6
95.1
64.9
37.7
19.6
326.0
335.4
350.0
363.1
371.8
114.6
95.1
64.9
37.6
19.5
474.4
465.9
452.7
440.5
432.3
359.8
370.8
387.8
402.9
412.8
0.556
0.450
0.297
0.167
0.085
2.081
2.011
1.927
1.871
1.841
0.05
0.10
0.25
0.50
0.75
1.00
2.00
3.00
4.00
5.00
42.38
25.43
14.16
5.46
1.74
1.719
1.781
1.826
1.865
1.899
0.4185
0.2192
0.1496
0.1137
0.09172
5.6
33.1
59.8
80.8
98.6
378.5
396.6
408.7
418.0
425.7
5.4
33.5
60.3
81.5
99.5
425.7
406.9
393.3
382.0
372.1
420.3
440.4
453.6
463.5
471.6
0.023
0.139
0.244
0.324
0.389
1.822
1.782
1.762
1.751
1.743
1.00
2.00
3.00
4.00
5.00
6.00
7.00
8.00
9.00
10.00
7.93
13.41
18.33
22.82
26.95
1.931
1.960
1.989
2.016
2.043
0.07680
0.06598
0.05776
0.05129
0.04606
114.2
128.2
141.0
152.9
164.0
432.2
438.0
443.1
447.6
451.8
115.3
129.6
142.6
154.7
166.1
363.0
354.6
346.7
339.1
331.8
478.3
484.2
489.3
493.8
497.9
0.446
0.495
0.540
0.580
0.618
1.737
1.733
1.729
1.726
1.723
6.00
7.00
8.00
9.00
10.00
11.00
12.00
13.00
14.00
15.00
30.80
34.39
37.77
40.97
44.01
2.070
2.096
2.122
2.148
2.174
0.04174
0.03810
0.03499
0.03231
0.02997
174.5
184.4
193.9
203.0
211.7
455.6
459.1
462.2
465.2
467.9
176.8
187.0
196.7
206.0
215.0
324.7
317.8
311.0
304.4
297.9
501.5
504.8
507.7
510.4
512.9
0.652
0.685
0.716
0.745
0.772
1.721
1.718
1.716
1.714
1.712
11.00
12.00
13.00
14.00
15.00
16.00
17.00
18.00
19.00
20.00
46.89
49.65
52.30
54.83
57.27
2.200
2.227
2.253
2.280
2.308
0.02790
0.02606
0.02441
0.02292
0.02157
220.1
228.3
236.2
243.8
251.3
470.4
472.7
474.9
476.9
478.7
223.6
232.0
240.2
248.2
255.9
291.4
285.0
278.6
272.2
265.9
515.0
517.0
518.8
520.4
521.8
0.799
0.824
0.849
0.873
0.896
1.710
1.707
1.705
1.703
1.700
16.00
17.00
18.00
19.00
20.00
22.00
24.00
26.00
28.00
30.00
61.90
66.21
70.27
74.10
77.72
2.364
2.424
2.487
2.555
2.630
0.01921
0.01721
0.01549
0.01398
0.01263
265.8
279.7
293.1
306.2
319.2
481.7
484.3
486.2
487.5
488.1
271.0
285.5
299.6
313.4
327.1
253.0
240.1
226.9
213.2
198.9
524.0
525.6
526.5
526.6
526.0
0.939
0.981
1.021
1.060
1.097
1.695
1.688
1.681
1.673
1.664
22.00
24.00
26.00
28.00
30.00
35.00
40.00
42.48
86.01
93.38
96.70
2.862
3.279
4.535
0.009771
0.007151
0.004535
351.4
387.9
434.9
486.3
474.7
434.9
361.4
401.0
454.2
159.1
102.3
0.0
520.5
503.3
454.2
1.190
1.295
1.437
1.633
1.574
1.437
35.00
40.00
42.48
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in SI Units
Properties of Superheated Propane
v
m3/kg
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
v
m3/kg
p 0.05 bar 0.005 MPa
(Tsat 93.28C)
h
kJ/kg
s
kJ/kg # K
p 0.1 bar 0.01 MPa
(Tsat 83.87C)
Sat.
90
80
6.752
6.877
7.258
326.0
329.4
339.8
359.8
363.8
376.1
2.081
2.103
2.169
3.542
367.3
370.8
2.011
3.617
339.5
375.7
2.037
70
60
50
7.639
8.018
8.397
350.6
361.8
373.3
388.8
401.9
415.3
2.233
2.296
2.357
3.808
3.999
4.190
350.3
361.5
373.1
388.4
401.5
415.0
2.101
2.164
2.226
40
30
20
8.776
9.155
9.533
385.1
397.4
410.1
429.0
443.2
457.8
2.418
2.477
2.536
4.380
4.570
4.760
385.0
397.3
410.0
428.8
443.0
457.6
2.286
2.346
2.405
10
0
10
20
9.911
10.29
10.67
11.05
423.2
436.8
450.8
270.6
472.8
488.2
504.1
520.4
2.594
2.652
2.709
2.765
4.950
5.139
5.329
5.518
423.1
436.7
450.6
465.1
472.6
488.1
503.9
520.3
2.463
2.520
2.578
2.634
p 0.5 bar 0.05 MPa
(Tsat 56.93C)
Copyright © 2006. Wiley. All rights reserved.
u
kJ/kg
p 1.0 bar 0.1 MPa
(Tsat 42.38C)
Sat.
50
40
0.796
0.824
0.863
363.1
371.3
383.4
402.9
412.5
426.6
1.871
1.914
1.976
0.4185
378.5
420.3
1.822
0.4234
381.5
423.8
1.837
30
20
10
0.903
0.942
0.981
396.0
408.8
422.1
441.1
455.9
471.1
2.037
2.096
2.155
0.4439
0.4641
0.4842
394.2
407.3
420.7
438.6
453.7
469.1
1.899
1.960
2.019
0
10
20
1.019
1.058
1.096
435.8
449.8
464.3
486.7
502.7
519.1
2.213
2.271
2.328
0.5040
0.5238
0.5434
434.4
448.6
463.3
484.8
501.0
517.6
2.078
2.136
2.194
30
40
50
60
1.135
1.173
1.211
1.249
479.2
494.6
510.4
526.7
535.9
553.2
570.9
589.1
2.384
2.440
2.496
2.551
0.5629
0.5824
0.6018
0.6211
478.2
493.7
509.5
525.8
534.5
551.9
569.7
587.9
2.251
2.307
2.363
2.419
p 2.0 bar 0.2 MPa
(Tsat 25.43C)
p 3.0 bar 0.3 MPa
(Tsat 14.16C)
Sat.
20
10
0.2192
0.2251
0.2358
396.6
404.0
417.7
440.4
449.0
464.9
1.782
1.816
1.877
0.1496
408.7
453.6
1.762
0.1527
414.7
460.5
1.789
0
10
20
0.2463
0.2566
0.2669
431.8
446.3
461.1
481.1
497.6
514.5
1.938
1.997
2.056
0.1602
0.1674
0.1746
429.0
443.8
458.8
477.1
494.0
511.2
1.851
1.912
1.971
30
40
50
0.2770
0.2871
0.2970
476.3
491.9
507.9
531.7
549.3
567.3
2.113
2.170
2.227
0.1816
0.1885
0.1954
474.2
490.1
506.2
528.7
546.6
564.8
2.030
2.088
2.145
0.2022
0.2090
0.2157
0.2223
522.7
539.6
557.0
574.8
583.4
602.3
621.7
641.5
2.202
2.258
2.314
2.369
60
0.3070
524.3 585.7
2.283
70
0.3169
541.1 604.5
2.339
80
0.3267
558.4 623.7
2.394
90 H. N.0.3365
576.1 of engineering
643.4 thermodynamics.
2.449
Moran, M. J., & Shapiro,
(2006). Fundamentals
Wiley.
Created from purdue on 2022-01-24 17:56:53.
Propane
TABLE A-18
T
C
749
750
Tables in SI Units
(Continued)
TABLE A-18
T
C
v
m3/kg
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
v
m3/kg
p 4.0 bar 0.4 MPa
(Tsat 5.46C)
Propane
h
kJ/kg
s
kJ/kg # K
p 5.0 bar 0.5 MPa
(Tsat 1.74C)
Sat.
0
10
0.1137
0.1169
0.1227
418.0
426.1
441.2
463.5
472.9
490.3
1.751
1.786
1.848
0.09172
425.7
471.6
1.743
0.09577
438.4
486.3
1.796
20
30
40
0.1283
0.1338
0.1392
456.6
472.2
488.1
507.9
525.7
543.8
1.909
1.969
2.027
0.1005
0.1051
0.1096
454.1
470.0
486.1
504.3
522.5
540.9
1.858
1.919
1.979
50
60
70
0.1445
0.1498
0.1550
504.4
521.1
538.1
562.2
581.0
600.1
2.085
2.143
2.199
0.1140
0.1183
0.1226
502.5
519.4
536.6
559.5
578.5
597.9
2.038
2.095
2.153
80
90
100
110
0.1601
0.1652
0.1703
0.1754
555.7
573.5
591.8
610.4
619.7
639.6
659.9
680.6
2.255
2.311
2.366
2.421
0.1268
0.1310
0.1351
0.1392
554.1
572.1
590.5
609.3
617.5
637.6
658.0
678.9
2.209
2.265
2.321
2.376
p 6.0 bar 0.6 MPa
(Tsat 7.93C)
Copyright © 2006. Wiley. All rights reserved.
u
kJ/kg
p 7.0 bar 0.7 MPa
(Tsat 13.41C)
Sat.
10
20
0.07680
0.07769
0.08187
432.2
435.6
451.5
478.3
482.2
500.6
1.737
1.751
1.815
0.06598
438.0
484.2
1.733
0.06847
448.8
496.7
1.776
30
40
50
0.08588
0.08978
0.09357
467.7
484.0
500.7
519.2
537.9
556.8
1.877
1.938
1.997
0.07210
0.07558
0.07896
465.2
481.9
498.7
515.7
534.8
554.0
1.840
1.901
1.962
60
70
80
0.09729
0.1009
0.1045
517.6
535.0
552.7
576.0
595.5
615.4
2.056
2.113
2.170
0.08225
0.08547
0.08863
515.9
533.4
551.2
573.5
593.2
613.2
2.021
2.079
2.137
90
100
110
120
0.1081
0.1116
0.1151
0.1185
570.7
589.2
608.0
627.3
635.6
656.2
677.1
698.4
2.227
2.283
2.338
2.393
0.09175
0.09482
0.09786
0.1009
569.4
587.9
606.8
626.2
633.6
654.3
675.3
696.8
2.194
2.250
2.306
2.361
p 8.0 bar 0.8 MPa
(Tsat 18.33C)
p 9.0 bar 0.9 MPa
(Tsat 22.82C)
Sat.
20
30
0.05776
0.05834
0.06170
443.1
445.9
462.7
489.3
492.6
512.1
1.729
1.740
1.806
0.05129
447.2
493.8
1.726
0.05355
460.0
508.2
1.774
40
50
60
0.06489
0.06796
0.07094
479.6
496.7
514.0
531.5
551.1
570.8
1.869
1.930
1.990
0.05653
0.05938
0.06213
477.2
494.7
512.2
528.1
548.1
568.1
1.839
1.901
1.962
70
80
90
0.07385
0.07669
0.07948
531.6
549.6
567.9
590.7
611.0
631.5
2.049
2.107
2.165
0.06479
0.06738
0.06992
530.0
548.1
566.5
588.3
608.7
629.4
2.022
2.081
2.138
100
110
120
0.08222
0.08493
0.08761
586.5
605.6
625.0
652.3
673.5
695.1
2.221
2.277
2.333
0.07241
0.07487
0.07729
585.2
604.3
623.7
650.4
671.7
693.3
2.195
2.252
2.307
130
0.09026
644.8
717.0
2.388
2.442
0.07969
0.08206
643.6
663.8
715.3
737.7
2.363
2.418
140
0.09289
665.0 Wiley.
739.3
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals
of engineering
thermodynamics.
Created from purdue on 2022-01-24 17:56:53.
Tables in SI Units
(Continued)
v
m3/kg
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
p 10.0 bar 1.0 MPa
(Tsat 26.95C)
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
p 12.0 bar 1.2 MPa
(Tsat 34.39C)
Sat.
30
40
0.04606
0.04696
0.04980
451.8
457.1
474.8
497.9
504.1
524.6
1.723
1.744
1.810
0.03810
459.1
504.8
1.718
0.03957
469.4
516.9
1.757
50
60
70
0.05248
0.05505
0.05752
492.4
510.2
528.2
544.9
565.2
585.7
1.874
1.936
1.997
0.04204
0.04436
0.04657
487.8
506.1
524.4
538.2
559.3
580.3
1.824
1.889
1.951
80
90
100
0.05992
0.06226
0.06456
546.4
564.9
583.7
606.3
627.2
648.3
2.056
2.114
2.172
0.04869
0.05075
0.05275
543.1
561.8
580.9
601.5
622.7
644.2
2.012
2.071
2.129
110
120
130
140
0.06681
0.06903
0.07122
0.07338
603.0
622.6
642.5
662.8
669.8
691.6
713.7
736.2
2.228
2.284
2.340
2.395
0.05470
0.05662
0.05851
0.06037
600.4
620.1
640.1
660.6
666.0
688.0
710.3
733.0
2.187
2.244
2.300
2.355
p 14.0 bar 1.4 MPa
(Tsat 40.97C)
Copyright © 2006. Wiley. All rights reserved.
v
m3/kg
p 16.0 bar 1.6 MPa
(Tsat 46.89C)
Sat.
50
60
0.03231
0.03446
0.03664
465.2
482.6
501.6
510.4
530.8
552.9
1.714
1.778
1.845
0.02790
0.02861
0.03075
470.4
476.7
496.6
515.0
522.5
545.8
1.710
1.733
1.804
70
80
90
0.03869
0.04063
0.04249
520.4
539.4
558.6
574.6
596.3
618.1
1.909
1.972
2.033
0.03270
0.03453
0.03626
516.2
535.7
555.2
568.5
590.9
613.2
1.871
1.935
1.997
100
110
120
0.04429
0.04604
0.04774
577.9
597.5
617.5
639.9
662.0
684.3
2.092
2.150
2.208
0.03792
0.03952
0.04107
574.8
594.7
614.8
635.5
657.9
680.5
2.058
2.117
2.176
130
140
150
160
0.04942
0.05106
0.05268
0.05428
637.7
658.3
679.2
700.5
706.9
729.8
753.0
776.5
2.265
2.321
2.376
2.431
0.04259
0.04407
0.04553
0.04696
635.3
656.0
677.1
698.5
703.4
726.5
749.9
773.6
2.233
2.290
2.346
2.401
p 18.0 bar 1.8 MPa
(Tsat 52.30C)
p 20.0 bar 2.0 MPa
(Tsat 57.27C)
Sat.
60
70
0.02441
0.02606
0.02798
474.9
491.1
511.4
518.8
538.0
561.8
1.705
1.763
1.834
0.02157
0.02216
0.02412
478.7
484.8
506.3
521.8
529.1
554.5
1.700
1.722
1.797
80
90
100
0.02974
0.03138
0.03293
531.6
551.5
571.5
585.1
608.0
630.8
1.901
1.965
2.027
0.02585
0.02744
0.02892
527.1
547.6
568.1
578.8
602.5
625.9
1.867
1.933
1.997
110
120
130
0.03443
0.03586
0.03726
591.7
612.1
632.7
653.7
676.6
699.8
2.087
2.146
2.204
0.03033
0.03169
0.03299
588.5
609.2
630.0
649.2
672.6
696.0
2.059
2.119
2.178
140
150
160
0.03863
0.03996
0.04127
653.6
674.8
696.3
723.1
746.7
770.6
2.262
2.318
2.374
0.03426
0.03550
0.03671
651.2
672.5
694.2
719.7
743.5
767.6
2.236
2.293
2.349
170
0.04256
718.2
794.8
2.429
0.03790
0.03907
716.2
738.5
792.0
816.6
2.404
2.459
180 H. N.0.04383
740.4 of engineering
819.3 thermodynamics.
2.484
Moran, M. J., & Shapiro,
(2006). Fundamentals
Wiley.
Created from purdue on 2022-01-24 17:56:53.
Propane
TABLE A-18
T
C
751
752
Tables in SI Units
(Continued)
TABLE A-18
T
C
v
m3/kg
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
p 22.0 bar 2.2 MPa
(Tsat 61.90C)
Propane
u
kJ/kg
h
kJ/kg
s
kJ/kg # K
p 24.0 bar 2.4 MPa
(Tsat 66.21C)
Sat.
70
80
0.01921
0.02086
0.02261
481.8
500.5
522.4
524.0
546.4
572.1
1.695
1.761
1.834
0.01721
0.01802
0.01984
484.3
493.7
517.0
525.6
536.9
564.6
1.688
1.722
1.801
90
100
110
0.02417
0.02561
0.02697
543.5
564.5
585.3
596.7
620.8
644.6
1.903
1.969
2.032
0.02141
0.02283
0.02414
539.0
560.6
581.9
590.4
615.4
639.8
1.873
1.941
2.006
120
130
140
0.02826
0.02949
0.03069
606.2
627.3
648.6
668.4
692.2
716.1
2.093
2.153
2.211
0.02538
0.02656
0.02770
603.2
624.6
646.0
664.1
688.3
712.5
2.068
2.129
2.188
150
160
170
180
0.03185
0.03298
0.03409
0.03517
670.1
691.9
714.1
736.5
740.2
764.5
789.1
813.9
2.269
2.326
2.382
2.437
0.02880
0.02986
0.03091
0.03193
667.8
689.7
711.9
734.5
736.9
761.4
786.1
811.1
2.247
2.304
2.360
2.416
p 26.0 bar 2.6 MPa
(Tsat 70.27C)
Copyright © 2006. Wiley. All rights reserved.
v
m3/kg
p 30.0 bar 3.0 MPa
(Tsat 77.72C)
Sat.
80
90
0.01549
0.01742
0.01903
486.2
511.0
534.2
526.5
556.3
583.7
1.681
1.767
1.844
0.01263
0.01318
0.01506
488.2
495.4
522.8
526.0
534.9
568.0
1.664
1.689
1.782
100
110
120
0.02045
0.02174
0.02294
556.4
578.3
600.0
609.6
634.8
659.6
1.914
1.981
2.045
0.01654
0.01783
0.01899
547.2
570.4
593.0
596.8
623.9
650.0
1.860
1.932
1.999
130
140
150
0.02408
0.02516
0.02621
621.6
643.4
665.3
684.2
708.8
733.4
2.106
2.167
2.226
0.02007
0.02109
0.02206
615.4
637.7
660.1
675.6
701.0
726.3
2.063
2.126
2.186
160
170
180
190
0.02723
0.02821
0.02918
0.03012
687.4
709.9
732.5
755.5
758.2
783.2
808.4
833.8
2.283
2.340
2.397
2.452
0.02300
0.02390
0.02478
0.02563
682.6
705.4
728.3
751.5
751.6
777.1
802.6
828.4
2.245
2.303
2.360
2.417
p 35.0 bar 3.5 MPa
(Tsat 86.01C)
p 40.0 bar 4.0 MPa
(Tsat 93.38C)
Sat.
90
100
0.00977
0.01086
0.01270
486.3
502.4
532.9
520.5
540.5
577.3
1.633
1.688
1.788
0.00715
474.7
503.3
1.574
0.00940
512.1
549.7
1.700
110
120
130
0.01408
0.01526
0.01631
558.9
583.4
607.0
608.2
636.8
664.1
1.870
1.944
2.012
0.01110
0.01237
0.01344
544.7
572.1
597.4
589.1
621.6
651.2
1.804
1.887
1.962
140
150
160
0.01728
0.01819
0.01906
630.2
653.3
676.4
690.7
717.0
743.1
2.077
2.140
2.201
0.01439
0.01527
0.01609
621.9
645.9
669.7
679.5
707.0
734.1
2.031
2.097
2.160
170
0.01989 699.6 769.2
180
0.02068 722.9 795.3
190
0.02146 746.5 821.6
200
0.02221
770.3 Wiley.
848.0
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals
of engineering
thermodynamics.
2.261
2.319
2.376
2.433
0.01687
0.01761
0.01833
0.01902
693.4
717.3
741.2
765.3
760.9
787.7
814.5
841.4
2.222
2.281
2.340
2.397
Created from purdue on 2022-01-24 17:56:53.
Tables in SI Units
Properties of Selected Solids and Liquids: cp, , and
Specific
Heat, cp
(kJ/kg # K)
Density,
(kg/m3)
Thermal
Conductivity,
(W/m # K)
Selected Solids, 300K
Aluminium
Coal, anthracite
Copper
Granite
Iron
Lead
Sand
Silver
Soil
Steel (AISI 302)
Tin
0.903
1.260
0.385
0.775
0.447
0.129
0.800
0.235
1.840
0.480
0.227
2700
1350
8930
2630
7870
11300
1520
10500
2050
8060
7310
237
0.26
401
2.79
80.2
35.3
0.27
429
0.52
15.1
66.6
Building Materials, 300K
Brick, common
Concrete (stone mix)
Glass, plate
Hardboard, siding
Limestone
Plywood
Softwoods (fir, pine)
0.835
0.880
0.750
1.170
0.810
1.220
1.380
1920
2300
2500
640
2320
545
510
0.72
1.4
1.4
0.094
2.15
0.12
0.12
Insulating Materials, 300K
Blanket (glass fiber)
Cork
Duct liner (glass fiber, coated)
Polystyrene (extruded)
Vermiculite fill (flakes)
—
1.800
0.835
1.210
0.835
16
120
32
55
80
0.046
0.039
0.038
0.027
0.068
Saturated Liquids
Ammonia, 300K
Mercury, 300K
Refrigerant 22, 300K
Refrigerant 134a, 300K
Unused Engine Oil, 300K
Water, 275K
300K
325K
350K
375K
400K
4.818
0.139
1.267
1.434
1.909
4.211
4.179
4.182
4.195
4.220
4.256
599.8
13529
1183.1
1199.7
884.1
999.9
996.5
987.1
973.5
956.8
937.4
0.465
8.540
0.085
0.081
0.145
0.574
0.613
0.645
0.668
0.681
0.688
Copyright © 2006. Wiley. All rights reserved.
Substance
Source: Drawn from several sources, these data are only representative. Values can vary depending on
temperature, purity, moisture content, and other factors.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Table A-19
TABLE A-19
753
754
Tables in SI Units
Ideal Gas Specific Heats of Some Common Gases (kJ/kg # K)
TABLE A-20
cp
cv
Temp.
K
cp
cv
Air
k
cp
cv
Nitrogen, N2
k
Temp.
K
Oxygen, O2
250
300
350
1.003
1.005
1.008
0.716
0.718
0.721
1.401
1.400
1.398
1.039
1.039
1.041
0.742
0.743
0.744
1.400
1.400
1.399
0.913
0.918
0.928
0.653
0.658
0.668
1.398
1.395
1.389
250
300
350
400
450
500
1.013
1.020
1.029
0.726
0.733
0.742
1.395
1.391
1.387
1.044
1.049
1.056
0.747
0.752
0.759
1.397
1.395
1.391
0.941
0.956
0.972
0.681
0.696
0.712
1.382
1.373
1.365
400
450
500
550
600
650
1.040
1.051
1.063
0.753
0.764
0.776
1.381
1.376
1.370
1.065
1.075
1.086
0.768
0.778
0.789
1.387
1.382
1.376
0.988
1.003
1.017
0.728
0.743
0.758
1.358
1.350
1.343
550
600
650
700
750
800
1.075
1.087
1.099
0.788
0.800
0.812
1.364
1.359
1.354
1.098
1.110
1.121
0.801
0.813
0.825
1.371
1.365
1.360
1.031
1.043
1.054
0.771
0.783
0.794
1.337
1.332
1.327
700
750
800
900
1000
1.121
1.142
0.834
0.855
1.344
1.336
1.145
1.167
0.849
0.870
1.349
1.341
1.074
1.090
0.814
0.830
1.319
1.313
900
1000
Temp.
K
Carbon
Dioxide, CO2
Carbon
Monoxide, CO
Temp.
K
Hydrogen, H2
250
300
350
0.791
0.846
0.895
0.602
0.657
0.706
1.314
1.288
1.268
1.039
1.040
1.043
0.743
0.744
0.746
1.400
1.399
1.398
14.051
14.307
14.427
9.927
10.183
10.302
1.416
1.405
1.400
250
300
350
400
450
500
0.939
0.978
1.014
0.750
0.790
0.825
1.252
1.239
1.229
1.047
1.054
1.063
0.751
0.757
0.767
1.395
1.392
1.387
14.476
14.501
14.513
10.352
10.377
10.389
1.398
1.398
1.397
400
450
500
550
600
650
1.046
1.075
1.102
0.857
0.886
0.913
1.220
1.213
1.207
1.075
1.087
1.100
0.778
0.790
0.803
1.382
1.376
1.370
14.530
14.546
14.571
10.405
10.422
10.447
1.396
1.396
1.395
550
600
650
700
750
800
1.126
1.148
1.169
0.937
0.959
0.980
1.202
1.197
1.193
1.113
1.126
1.139
0.816
0.829
0.842
1.364
1.358
1.353
14.604
14.645
14.695
10.480
10.521
10.570
1.394
1.392
1.390
700
750
800
900
1000
1.204
1.234
1.015
1.045
1.186
1.181
1.163
1.185
0.866
0.888
1.343
1.335
14.822
14.983
10.698
10.859
1.385
1.380
900
1000
Source: Adapted from K. Wark, Thermodynamics, 4th ed., McGraw-Hill, New York, 1983, as based on “Tables
of Thermal Properties of Gases,” NBS Circular 564, 1955.
Table A-20
Copyright © 2006. Wiley. All rights reserved.
k
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in SI Units
TABLE A-21
755
Variation of cp with Temperature for Selected Ideal Gases
cp
R
a
bT
gT 2
dT 3
eT 4
T is in K, equations valid from 300 to 1000 K
Gas
103
106
109
1012
CO
CO2
H2
H2O
3.710
2.401
3.057
4.070
1.619
8.735
2.677
1.108
3.692
6.607
5.810
4.152
2.032
2.002
5.521
2.964
0.240
0
1.812
0.807
O2
N2
Air
SO2
3.626
3.675
3.653
3.267
1.878
1.208
1.337
5.324
7.055
2.324
3.294
0.684
6.764
0.632
1.913
5.281
2.156
0.226
0.2763
2.559
CH4
C2H2
C2H4
3.826
1.410
1.426
3.979
19.057
11.383
24.558
24.501
7.989
22.733
16.391
16.254
6.963
4.135
6.749
Monatomic
gasesa
2.5
0
0
0
0
a
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Table A-21
Copyright © 2006. Wiley. All rights reserved.
For monatomic gases, such as He, Ne, and Ar, cp is constant over a wide temperature range and is very nearly
equal to 52 R.
Source: Adapted from K. Wark, Thermodynamics, 4th ed., McGraw-Hill, New York, 1983, as based on NASA
SP-273, U.S. Government Printing Office, Washington, DC, 1971.
Table A-22
756
Tables in SI Units
TABLE A-22
Ideal Gas Properties of Air
T(K), h and u(kJ/kg), s (kJ/kg # K)
when s 01
T
h
u
s
pr
200
210
220
230
240
199.97
209.97
219.97
230.02
240.02
142.56
149.69
156.82
164.00
171.13
1.29559
1.34444
1.39105
1.43557
1.47824
0.3363
0.3987
0.4690
0.5477
0.6355
250
260
270
280
285
250.05
260.09
270.11
280.13
285.14
178.28
185.45
192.60
199.75
203.33
1.51917
1.55848
1.59634
1.63279
1.65055
290
295
300
305
310
290.16
295.17
300.19
305.22
310.24
206.91
210.49
214.07
217.67
221.25
315
320
325
330
340
315.27
320.29
325.31
330.34
340.42
350
360
370
380
390
400
410
420
430
440
vr
when s 0
h
u
s
1707.
1512.
1346.
1205.
1084.
450
460
470
480
490
451.80
462.02
472.24
482.49
492.74
322.62
329.97
337.32
344.70
352.08
2.11161
2.13407
2.15604
2.17760
2.19876
5.775
6.245
6.742
7.268
7.824
223.6
211.4
200.1
189.5
179.7
0.7329
0.8405
0.9590
1.0889
1.1584
979.
887.8
808.0
738.0
706.1
500
510
520
530
540
503.02
513.32
523.63
533.98
544.35
359.49
366.92
374.36
381.84
389.34
2.21952
2.23993
2.25997
2.27967
2.29906
8.411
9.031
9.684
10.37
11.10
170.6
162.1
154.1
146.7
139.7
1.66802
1.68515
1.70203
1.71865
1.73498
1.2311
1.3068
1.3860
1.4686
1.5546
676.1
647.9
621.2
596.0
572.3
550
560
570
580
590
554.74
565.17
575.59
586.04
596.52
396.86
404.42
411.97
419.55
427.15
2.31809
2.33685
2.35531
2.37348
2.39140
11.86
12.66
13.50
14.38
15.31
133.1
127.0
121.2
115.7
110.6
224.85
228.42
232.02
235.61
242.82
1.75106
1.76690
1.78249
1.79783
1.82790
1.6442
1.7375
1.8345
1.9352
2.149
549.8
528.6
508.4
489.4
454.1
600
610
620
630
640
607.02
617.53
628.07
638.63
649.22
434.78
442.42
450.09
457.78
465.50
2.40902
2.42644
2.44356
2.46048
2.47716
16.28
17.30
18.36
19.84
20.64
105.8
101.2
96.92
92.84
88.99
350.49
360.58
370.67
380.77
390.88
250.02
257.24
264.46
271.69
278.93
1.85708
1.88543
1.91313
1.94001
1.96633
2.379
2.626
2.892
3.176
3.481
422.2
393.4
367.2
343.4
321.5
650
660
670
680
690
659.84
670.47
681.14
691.82
702.52
473.25
481.01
488.81
496.62
504.45
2.49364
2.50985
2.52589
2.54175
2.55731
21.86
23.13
24.46
25.85
27.29
85.34
81.89
78.61
75.50
72.56
400.98
411.12
421.26
431.43
441.61
286.16
293.43
300.69
307.99
315.30
1.99194
2.01699
2.04142
2.06533
2.08870
3.806
4.153
4.522
4.915
5.332
301.6
283.3
266.6
251.1
236.8
700
710
720
730
740
713.27
724.04
734.82
745.62
756.44
512.33
520.23
528.14
536.07
544.02
2.57277
2.58810
2.60319
2.61803
2.63280
28.80
30.38
32.02
33.72
35.50
69.76
67.07
64.53
62.13
59.82
Copyright © 2006. Wiley. All rights reserved.
1. pr and vr data for use with Eqs. 6.43 and 6.44, respectively.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
pr
vr
T
TABLE A-22
757
(Continued)
T(K), h and u(kJ/kg), s (kJ/kg # K)
Copyright © 2006. Wiley. All rights reserved.
when s 01
when s 0
T
h
u
s
pr
vr
T
h
u
s
pr
vr
750
760
770
780
790
767.29
778.18
789.11
800.03
810.99
551.99
560.01
568.07
576.12
584.21
2.64737
2.66176
2.67595
2.69013
2.70400
37.35
39.27
41.31
43.35
45.55
57.63
55.54
53.39
51.64
49.86
1300
1320
1340
1360
1380
1395.97
1419.76
1443.60
1467.49
1491.44
1022.82
1040.88
1058.94
1077.10
1095.26
3.27345
3.29160
3.30959
3.32724
3.34474
330.9
352.5
375.3
399.1
424.2
11.275
10.747
10.247
9.780
9.337
800
820
840
860
880
821.95
843.98
866.08
888.27
910.56
592.30
608.59
624.95
641.40
657.95
2.71787
2.74504
2.77170
2.79783
2.82344
47.75
52.59
57.60
63.09
68.98
48.08
44.84
41.85
39.12
36.61
1400
1420
1440
1460
1480
1515.42
1539.44
1563.51
1587.63
1611.79
1113.52
1131.77
1150.13
1168.49
1186.95
3.36200
3.37901
3.39586
3.41247
3.42892
450.5
478.0
506.9
537.1
568.8
8.919
8.526
8.153
7.801
7.468
900
920
940
960
980
932.93
955.38
977.92
1000.55
1023.25
674.58
691.28
708.08
725.02
741.98
2.84856
2.87324
2.89748
2.92128
2.94468
75.29
82.05
89.28
97.00
105.2
34.31
32.18
30.22
28.40
26.73
1500
1520
1540
1560
1580
1635.97
1660.23
1684.51
1708.82
1733.17
1205.41
1223.87
1242.43
1260.99
1279.65
3.44516
3.46120
3.47712
3.49276
3.50829
601.9
636.5
672.8
710.5
750.0
7.152
6.854
6.569
6.301
6.046
1000
1020
1040
1060
1080
1046.04
1068.89
1091.85
1114.86
1137.89
758.94
776.10
793.36
810.62
827.88
2.96770
2.99034
3.01260
3.03449
3.05608
114.0
123.4
133.3
143.9
155.2
25.17
23.72
22.39
21.14
19.98
1600
1620
1640
1660
1680
1757.57
1782.00
1806.46
1830.96
1855.50
1298.30
1316.96
1335.72
1354.48
1373.24
3.52364
3.53879
3.55381
3.56867
3.58335
791.2
834.1
878.9
925.6
974.2
5.804
5.574
5.355
5.147
4.949
1100
1120
1140
1160
1180
1161.07
1184.28
1207.57
1230.92
1254.34
845.33
862.79
880.35
897.91
915.57
3.07732
3.09825
3.11883
3.13916
3.15916
167.1
179.7
193.1
207.2
222.2
18.896
17.886
16.946
16.064
15.241
1700
1750
1800
1850
1900
1880.1
1941.6
2003.3
2065.3
2127.4
1392.7
1439.8
1487.2
1534.9
1582.6
3.5979
3.6336
3.6684
3.7023
3.7354
1025
1161
1310
1475
1655
4.761
4.328
3.944
3.601
3.295
1200
1220
1240
1260
1280
1277.79
1301.31
1324.93
1348.55
1372.24
933.33
951.09
968.95
986.90
1004.76
3.17888
3.19834
3.21751
3.23638
3.25510
238.0
254.7
272.3
290.8
310.4
14.470
13.747
13.069
12.435
11.835
1950
2000
2050
2100
2150
2189.7
2252.1
2314.6
2377.4
2440.3
1630.6
1678.7
1726.8
1775.3
1823.8
3.7677
3.7994
3.8303
3.8605
3.8901
1852
2068
2303
2559
2837
3.022
2.776
2.555
2.356
2.175
2200
2250
2503.2
2566.4
1872.4
1921.3
3.9191
3.9474
3138
3464
2.012
1.864
Source: Tables A-22 are based on J. H. Keenan and J. Kaye, Gas Tables, Wiley, New York, 1945.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Table A-22
Tables in SI Units
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
758
h
0
6,601
6,938
7,280
7,627
7,979
8,335
8,697
9,063
9,364
9,431
9,807
10,186
10,570
10,959
11,351
11,748
12,148
12,552
12,960
13,372
13,787
14,206
14,628
15,054
15,483
15,916
16,351
16,791
17,232
17,678
18,126
18,576
19,029
19,485
19,945
20,407
20,870
21,337
21,807
T
0
220
230
240
250
260
270
280
290
298
300
310
320
330
340
350
360
370
380
390
400
410
420
430
440
450
460
470
480
490
500
510
520
530
540
550
560
570
580
590
0
4,772
5,026
5,285
5,548
5,817
6,091
6,369
6,651
6,885
6,939
7,230
7,526
7,826
8,131
8,439
8,752
9,068
9,392
9,718
10,046
10,378
10,714
11,053
11,393
11,742
12,091
12,444
12,800
13,158
13,521
13,885
14,253
14,622
14,996
15,372
15,751
16,131
16,515
16,902
u
0
202.966
204.464
205.920
207.337
208.717
210.062
211.376
212.660
213.685
213.915
215.146
216.351
217.534
218.694
219.831
220.948
222.044
223.122
224.182
225.225
226.250
227.258
228.252
229.230
230.194
231.144
232.080
233.004
233.916
234.814
235.700
236.575
237.439
238.292
239.135
239.962
240.789
241.602
242.405
s°
0
6,391
6,683
6,975
7,266
7,558
7,849
8,140
8,432
8,669
8,723
9,014
9,306
9,597
9,889
10,181
10,473
10,765
11,058
11,351
11,644
11,938
12,232
12,526
12,821
13,116
13,412
13,708
14,005
14,302
14,600
14,898
15,197
15,497
15,797
16,097
16,399
16,701
17,003
17,307
h
0
4,562
4,771
4,979
5,188
5,396
5,604
5,812
6,020
6,190
6,229
6,437
6,645
6,854
7,062
7,271
7,480
7,689
7,899
8,108
8,319
8,529
8,740
8,951
9,163
9,375
9,587
9,800
10,014
10,228
10,443
10,658
10,874
11,090
11,307
11,524
11,743
11,961
12,181
12,401
u
0
188.683
189.980
191.221
192.411
193.554
194.654
195.173
196.735
197.543
197.723
198.678
199.603
200.500
201.371
202.217
203.040
203.842
204.622
205.383
206.125
206.850
207.549
208.252
208.929
209.593
210.243
210.880
211.504
212.117
212.719
213.310
213.890
214.460
215.020
215.572
216.115
216.649
217.175
217.693
s°
0
7,295
7,628
7,961
8,294
8,627
8,961
9,296
9,631
9,904
9,966
10,302
10,639
10,976
11,314
11,652
11,992
12,331
12,672
13,014
13,356
13,699
14,043
14,388
14,734
15,080
15,428
15,777
16,126
16,477
16,828
17,181
17,534
17,889
18,245
18,601
18,959
19,318
19.678
20,039
h
0
5,466
5,715
5,965
6,215
6,466
6,716
6,968
7,219
7,425
7,472
7,725
7,978
8,232
8,487
8,742
8,998
9,255
9,513
9,771
10,030
10,290
10,551
10,813
11,075
11,339
11,603
11,869
12,135
12,403
12,671
12,940
13,211
13,482
13,755
14,028
14,303
14,579
14,856
15,134
u
0
178.576
180.054
181.471
182.831
184.139
185.399
186.616
187.791
188.720
188.928
190.030
191.098
192.136
193.144
194.125
195.081
196.012
196.920
197.807
198.673
199.521
200.350
201.160
201.955
202.734
203.497
204.247
204.982
205.705
206.413
207.112
207.799
208.475
209.139
209.795
210.440
211.075
211.702
212.320
s°
Water Vapor, H2O
(h°f 241,820 kJ/kmol)
T(K), h and u(kJ/kmol), s°(kJ/kmol # K)
Carbon Monoxide, CO
(h°f 110,530 kJ/kmol)
Ideal Gas Properties of Selected Gases
Carbon Dioxide, CO2
(h°f 393,520 kJ/kmol)
TABLE A-23
Copyright © 2006. Wiley. All rights reserved.
0
6,404
6,694
6,984
7,275
7,566
7,858
8,150
8,443
8,682
8,736
9,030
9,325
9,620
9,916
10,213
10,511
10,809
11,109
11,409
11,711
12,012
12,314
12,618
12,923
13,228
13,535
13,842
14,151
14,460
14,770
15,082
15,395
15,708
16,022
16,338
16,654
16,971
17,290
17,609
h
0
4,575
4,782
4,989
5,197
5,405
5,613
5,822
6,032
6,203
6,242
6,453
6,664
6,877
7,090
7,303
7,518
7,733
7,949
8,166
8,384
8,603
8,822
9,043
9,264
9,487
9,710
9,935
10,160
10,386
10,614
10,842
11,071
11,301
11,533
11,765
11,998
12,232
12,467
12,703
u
s°
0
196.171
197.461
198.696
199.885
201.027
202.128
203.191
204.218
205.033
205.213
206.177
207.112
208.020
208.904
209.765
210.604
211.423
212.222
213.002
213.765
214.510
215.241
215.955
216.656
217.342
218.016
218.676
219.326
219.963
220.589
221.206
221.812
222.409
222.997
223.576
224.146
224.708
225.262
225.808
Oxygen, O2
(h°f 0 kJ/kmol)
0
6,391
6,683
6,975
7,266
7,558
7,849
8,141
8,432
8,669
8,723
9,014
9,306
9,597
9,888
10,180
10,471
10,763
11,055
11,347
11,640
11,932
12,225
12,518
12,811
13,105
13,399
13,693
13,988
14,285
14,581
14,876
15,172
15,469
15,766
16,064
16,363
16,662
16,962
17,262
h
0
4,562
4,770
4,979
5,188
5,396
5,604
5,813
6,021
6,190
6,229
6,437
6,645
6,853
7,061
7,270
7,478
7,687
7,895
8,104
8,314
8,523
8,733
8,943
9,153
9,363
9,574
9,786
9,997
10,210
10,423
10,635
10,848
11,062
11,277
11,492
11,707
11,923
12,139
12,356
u
s°
0
182.638
183.938
185.180
186.370
187.514
188.614
189.673
190.695
191.502
191.682
192.638
193.562
194.459
195.328
196.173
196.995
197.794
198.572
199.331
200.071
200,794
201.499
202.189
202.863
203.523
204.170
204.803
205.424
206.033
206.630
207.216
207.792
208.358
208.914
209.461
209.999
210.528
211.049
211.562
Nitrogen, N2
(h°f 0 kJ/kmol)
Table A-23
0
220
230
240
250
260
270
280
290
298
300
310
320
330
340
350
360
370
380
390
400
410
420
430
440
450
460
470
480
490
500
510
520
530
540
550
560
570
580
590
T
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
759
(Continued)
h
22,280
22,754
23,231
23,709
24,190
24,674
25,160
25,648
26,138
26,631
27,125
27,622
28,121
28,622
29,124
29,629
30,135
30,644
31,154
31,665
32,179
32,694
33,212
33,730
34,251
34,773
35,296
35,821
36,347
36,876
37,405
37,935
38,467
39,000
39,535
40,070
40,607
41,145
41,685
42,226
T
600
610
620
630
640
650
660
670
680
690
700
710
720
730
740
750
760
770
780
790
800
810
820
830
840
850
860
870
880
890
900
910
920
930
940
950
960
970
980
990
17,291
17,683
18,076
18,471
18,869
19,270
19,672
20,078
20,484
20,894
21,305
21,719
22,134
22,552
22,972
23,393
23,817
24,242
24,669
25,097
25,527
25,959
26,394
26,829
27,267
27,706
28,125
28,588
29,031
29,476
29,922
30,369
30,818
31,268
31,719
32,171
32,625
33,081
33,537
33,995
u
243.199
243.983
244.758
245.524
246.282
247.032
247,773
248.507
249.233
249.952
250.663
251.368
252.065
252.755
253.439
254.117
254.787
255,452
256.110
256.762
257.408
258.048
258.682
259.311
259.934
260.551
261.164
261.770
262.371
262.968
263.559
264.146
264.728
265.304
265.877
266.444
267.007
267.566
268.119
268.670
s°
Carbon Dioxide, CO2
(h°f 393,520 kJ/kmol)
TABLE A-23
17,611
17,915
18,221
18,527
18,833
19,141
19,449
19,758
20,068
20,378
20,690
21,002
21,315
21,628
21,943
22,258
22,573
22,890
23,208
23,526
23,844
24,164
24,483
24,803
25,124
25,446
25,768
26.091
26,415
26,740
27,066
27,392
27,719
28,046
28,375
28,703
29,033
29,362
29,693
30,024
h
12,622
12,843
13,066
13,289
13,512
13,736
13,962
14,187
14,414
14,641
14,870
15,099
15,328
15,558
15,789
16,022
16,255
16,488
16,723
16,957
17,193
17,429
17,665
17,902
18,140
18,379
18,617
18,858
19,099
19,341
19,583
19,826
20,070
20,314
20,559
20,805
21,051
21,298
21,545
21,793
u
218.204
218.708
219.205
219.695
220.179
220.656
221.127
221.592
222.052
222.505
222.953
223.396
223.833
224.265
224.692
225.115
225.533
225.947
226.357
226.762
227.162
227.559
227.952
228.339
228.724
229,106
229,482
229.856
230.227
230.593
230.957
231.317
231.674
232.028
232.379
232.727
233.072
233.413
233.752
234.088
s°
20,402
20,765
21,130
21,495
21,862
22,230
22,600
22,970
23,342
23,714
24,088
24,464
24,840
25,218
25,597
25,977
26,358
26,741
27,125
27,510
27,896
28,284
28,672
29,062
29,454
29,846
30,240
30,635
31,032
31,429
31,828
32,228
32,629
33,032
33,436
33,841
34,247
34,653
35,061
35,472
h
15,413
15,693
15,975
16,257
16,541
16,826
17,112
17,399
17,688
17,978
18,268
18,561
18,854
19,148
19,444
19,741
20,039
20,339
20,639
20,941
21,245
21,549
21,855
22,162
22,470
22,779
23,090
23,402
23,715
24,029
24,345
24,662
24,980
25,300
25,621
25,943
26,265
26,588
26,913
27,240
u
212.920
213.529
214.122
214.707
215.285
215.856
216.419
216.976
217.527
218.071
218.610
219.142
219.668
220.189
220.707
221.215
221.720
222.221
222.717
223.207
223.693
224.174
224.651
225.123
225.592
226.057
226.517
226.973
227.426
227.875
228.321
228.763
229.202
229.637
230.070
230.499
230.924
231.347
231.767
232.184
s°
Water Vapor, H2O
(h°f 241,820 kJ/kmol)
T(K), h and u(kJ/kmol), s°(kJ/kmol # K)
Carbon Monoxide, CO
(h°f 110,530 kJ/kmol)
Copyright © 2006. Wiley. All rights reserved.
17,929
18,250
18,572
18,895
19,219
19,544
19,870
20,197
20,524
20,854
21,184
21,514
21,845
22,177
22,510
22,844
23,178
23,513
23,850
24,186
24,523
24,861
25,199
25,537
25,877
26,218
26,559
26,899
27,242
27,584
27,928
28,272
28,616
28,960
29,306
29,652
29,999
30,345
30,692
31.041
h
12,940
13,178
13,417
13,657
13,898
14,140
14,383
14,626
14,871
15,116
15,364
15,611
15,859
16,107
16,357
16,607
16,859
17,111
17,364
17,618
17,872
18,126
18,382
18,637
18,893
19,150
19,408
19,666
19,925
20,185
20,445
20,706
20,967
21,228
21,491
21,754
22,017
22,280
22,544
22,809
u
s°
226.346
226.877
227.400
227.918
228.429
228.932
229.430
229.920
230.405
230.885
231.358
231.827
232.291
232.748
233.201
233.649
234.091
234.528
234.960
235.387
235.810
236.230
236.644
237.055
237.462
237.864
238.264
238.660
239.051
239.439
239.823
240.203
240.580
240.953
241.323
241.689
242.052
242.411
242.768
243.120
Oxygen, O2
(h°f 0 kJ/kmol)
12,574
12,792
13,011
13,230
13,450
13,671
13,892
14,114
14,337
14,560
14,784
15,008
15,234
15,460
15,686
15,913
16,141
16,370
16,599
16,830
17,061
17,292
17,524
17,757
17,990
18,224
18,459
18,695
18,931
19,168
19,407
19,644
19,883
20,122
20,362
20,603
20,844
21,086
21,328
21,571
u
Table A-23
17,563
17,864
18,166
18,468
18,772
19,075
19,380
19,685
19,991
20,297
20,604
20,912
21,220
21,529
21,839
22,149
22,460
22,772
23,085
23,398
23,714
24,027
24,342
24,658
24,974
25,292
25,610
25,928
26,248
26,568
26,890
27,210
27,532
27,854
28,178
28,501
28,826
29,151
29,476
29,803
h
s°
212.066
212.564
213.055
213.541
214.018
214.489
214.954
215.413
215.866
216.314
216.756
217.192
217.624
218.059
218.472
218.889
219.301
219.709
220.113
220.512
220.907
221.298
221.684
222.067
222.447
222.822
223.194
223.562
223.927
224.288
224.647
225.002
225.353
225.701
226.047
226.389
226.728
227.064
227.398
227.728
Nitrogen, N2
(h°f 0 kJ/kmol)
600
610
620
630
640
650
660
670
680
690
700
710
720
730
740
750
760
770
780
790
800
810
820
830
840
850
860
870
880
890
900
910
920
930
940
950
960
970
980
990
T
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
760
(Continued)
h
42,769
43,859
44,953
46,051
47,153
48,258
49,369
50,484
51,602
52,724
53,848
54,977
56,108
57,244
58,381
59,522
60,666
61,813
62,963
64,116
65,271
66,427
67,586
68,748
69,911
71,078
72,246
73,417
74,590
76,767
76,944
78,123
79,303
80,486
81,670
82,856
84,043
85,231
T
1000
1020
1040
1060
1080
1100
1120
1140
1160
1180
1200
1220
1240
1260
1280
1300
1320
1340
1360
1380
1400
1420
1440
1460
1480
1500
1520
1540
1560
1580
1600
1620
1640
1660
1680
1700
1720
1740
68,721
69,742
70,764
63,741
64,653
65,668
66,592
67,702
58,606
59,609
60,613
61,620
62,630
53,631
54,621
55,614
56,609
57,606
48,713
49,691
50,672
51,656
52,643
43,871
44,834
45,799
46,768
47,739
39,112
40,057
41,006
41,957
42,913
34,455
35,378
36,306
37,238
38,174
u
299.482
300.177
300.863
295.901
296.632
297.356
298.072
298.781
292.114
292.888
292.654
294.411
295.161
288.106
288.934
289.743
290.542
291.333
283.847
284.722
285.586
286.439
287.283
279.307
280.238
281.158
282.066
282.962
274.445
275.444
276.430
277.403
278.362
269.215
270.293
271.354
272.400
273.430
s°
Carbon Dioxide, CO2
(h°f 393,520 kJ/kmol)
TABLE A-23
54,609
55,323
56,039
51,053
51,763
52,472
53,184
53,895
47,517
48,222
48,928
49,635
50,344
44,007
44,707
45,408
46,110
46,813
40,534
41,266
41,919
42,613
43,309
37,095
37,780
38,466
39,154
39,884
33,702
34,377
35,054
35,733
36,406
30,355
31,020
31,688
32,357
33,029
h
40,474
41,023
41,572
37,750
38,293
38,837
39,382
39,927
35,046
35,584
36,124
36,665
37,207
32,367
32,900
33,434
33,971
34,508
29,725
30,251
30,778
31,306
31,836
27,118
27,637
28,426
28,678
29,201
24,557
25,065
25,575
26,088
26,602
22,041
22,540
23,041
23,544
24,049
u
252.751
253.169
253.582
250.592
251.033
251.470
251.901
252.329
248.312
248.778
249.240
249.695
250.147
245.889
246.385
246.876
247.360
247.839
243.316
243.844
244.366
244.880
245.388
240.663
241.128
241.686
242.236
242.780
237.609
238.217
238.817
239.407
239.989
234.421
235.079
235.728
236.364
236.992
s°
67,589
68,567
69,550
62,748
63,709
64,675
65,643
66,614
57,999
58,942
59,888
60,838
61,792
53,351
54,273
55,198
56,128
57,062
48,807
49,707
50,612
51,521
52,434
44,380
45,256
46,137
47,022
47,912
40,071
40,923
41,780
42,642
43,509
35,882
36,709
37,542
38,380
39,223
h
53,455
54,267
55,083
49,445
52,240
51,039
51,841
52,646
45,528
46,304
47,084
47,868
48,655
41,711
42,466
43,226
43,989
44,756
38,000
38,732
39,470
40,213
40,960
34,403
35,112
35,827
36,546
37,270
30,925
31,611
32,301
32,997
33,698
27,568
28,228
28,895
29,567
30,243
u
256.450
257.022
257.589
253.513
254.111
254.703
255.290
255.873
250.450
251.074
251.693
252.305
252.912
247.241
247.895
248.543
249.185
249.820
243.877
244.564
245.243
245.915
246.582
240.333
241.057
241.773
242.482
243.183
236.584
237.352
238.110
238.859
239.600
232.597
233.415
234.223
235.020
235.806
s°
Water Vapor, H2O
(h°f 241,820 kJ/kmol)
T(K), h and u(kJ/kmol), s°(kJ/kmol # K)
Carbon Monoxide, CO
(h°f 110,530 kJ/kmol)
Copyright © 2006. Wiley. All rights reserved.
56,652
57,394
58,136
52,961
53,696
54,434
55,172
55,912
49,292
50,024
50,756
51,490
52,224
45,648
46,374
47,102
47,831
48,561
42,033
42,753
43,475
44,198
44,923
38,447
39,162
39,877
40,594
41,312
34,899
35,606
36,314
37,023
37,734
31,389
32,088
32,789
33,490
34,194
h
42,517
43,093
43,669
39,658
40,227
40,799
41,370
41,944
36,821
37,387
37,952
38,520
39,088
34,008
34,567
35,129
35,692
36,256
31,224
31,778
32,334
32,891
33,449
28,469
29,018
29,568
30,118
30,670
25,753
26,294
26,836
27,379
27,923
23,075
23,607
24,142
24,677
25,214
u
s°
262.571
263.005
263.435
260.333
260.791
261.242
261.690
262.132
257.965
258.450
258.928
259.402
259.870
255.454
255.968
256.475
256.978
257.474
252.776
253.325
253.868
254.404
254.932
249.906
250.497
251.079
251.653
252.219
246.818
247.454
248.081
248.698
249.307
243.471
244.164
244.844
245.513
246.171
Oxygen, O2
(h°f 0 kJ/kmol)
54,099
54,807
55,516
50,571
51,275
51,980
52,686
53,393
47,073
47,771
48,470
49,168
49,869
43,605
44,295
44,988
45,682
46,377
40,170
40,853
41,539
42,227
42,915
36,777
37,452
38,129
38,807
39,488
33,426
34,092
34,760
35,430
36,104
30,129
30,784
31,442
32,101
32,762
h
39,965
40,507
41,049
37,268
37,806
38,344
38,884
39,424
34,601
35,133
35,665
36,197
36,732
31,964
32,489
33,014
33,543
34,071
29,361
29,878
30,398
30,919
31,441
26,799
27,308
27,819
28,331
28,845
24,280
24,780
25,282
25,786
26,291
21,815
22,304
22,795
23,288
23,782
u
s°
246.166
246.580
246.990
244.028
244.464
244.896
245.324
245.747
241.768
242.228
242.685
243.137
243.585
239.375
239.865
240.350
240.827
241.301
236.831
237.353
237.867
238.376
238.878
234.115
234.673
235.223
235.766
236.302
231.199
231.799
232.391
232.973
233.549
228.057
228.706
229.344
229.973
230.591
Nitrogen, N2
(h°f 0 kJ/kmol)
Table A-23
1700
1720
1740
1600
1620
1640
1660
1680
1500
1520
1540
1560
1580
1400
1420
1440
1460
1480
1300
1320
1340
1360
1380
1200
1220
1240
1260
1280
1100
1120
1140
1160
1180
1000
1020
1040
1060
1080
T
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
761
(Continued)
u
71,787
72,812
73,840
74,868
75,897
76,929
77,962
78,996
80,031
81,067
82,105
83,144
84,185
86,791
89,404
92,023
94,648
97,277
99,912
102,552
105,197
107,849
110,504
113,166
115,832
118,500
121,172
123,849
126,528
129,212
131,898
134,589
137,283
139,982
142,681
145,385
148,089
150,801
s°
301.543
302.271
302.884
303.544
304.198
304.845
305.487
306.122
306.751
307.374
307.992
308.604
309.210
310.701
312.160
313.589
314.988
316.356
317.695
319.011
320.302
321.566
322.808
324.026
325.222
326.396
327.549
328.684
329.800
330.896
331.975
333.037
334.084
335.114
336.126
337.124
338.109
339.069
56,756
57,473
58,191
58,910
59,629
60,351
61,072
61,794
62,516
63,238
63,961
64,684
65,408
67,224
69,044
70,864
72,688
74,516
76,345
78,178
80,015
81,852
83,692
85,537
87,383
89,230
91,077
92,930
94,784
96,639
98,495
100,352
102,210
104,073
105,939
107,802
109,667
111,534
h
42,123
42,673
43,225
43,778
44,331
44,886
45,441
45,997
46,552
47,108
47,665
48,221
48,780
50,179
51,584
52,988
54,396
55,809
57,222
58,640
60,060
61,482
62,906
64,335
65,766
67,197
68,628
70,066
71,504
72,945
74,383
75,825
77,267
78,715
80,164
81,612
83,061
84,513
u
253.991
254.398
254.797
255.194
255.587
255.976
256.361
256.743
257.122
257.497
257.868
258.236
258.600
259.494
260.370
261.226
262.065
262.887
263.692
264.480
265.253
266.012
266.755
267.485
268.202
268.905
269.596
270.285
270.943
271.602
272.249
272.884
273.508
274.123
274.730
275.326
275.914
276.494
s°
Carbon Monoxide, CO
(h°f 110,530 kJ/kmol)
70,535
71,523
72,513
73,507
74,506
75,506
76,511
77,517
78,527
79,540
80,555
81,573
82,593
85,156
87,735
90,330
92,940
95,562
98,199
100,846
103,508
106,183
108,868
111,565
114,273
116,991
119,717
122,453
125,198
127,952
130,717
133,486
136,264
139,051
141,846
144,648
147,457
150,272
h
55,902
56,723
57,547
58,375
59,207
60,042
60,880
61,720
62,564
63,411
64,259
65,111
65,965
68,111
70,275
72,454
74,649
76,855
79,076
81,308
83,553
85,811
88,082
90,364
92,656
94,958
97,269
99,588
101,917
104,256
106,605
108,959
111,321
113,692
116,072
118,458
120,851
123,250
u
258.151
258.708
259.262
259.811
260.357
260.898
261.436
261.969
262.497
263.022
263.542
264.059
264.571
265.838
267.081
268.301
269.500
270.679
271.839
272.978
274.098
275.201
276.286
277.354
278.407
279,441
280.462
281.464
282.453
283.429
284.390
285.338
286.273
287.194
288.102
288.999
289.884
290.756
s°
Water Vapor, H2O
(h°f 241,820 kJ/kmol)
h
44,247
44,825
45,405
45,986
46,568
47,151
47,734
48,319
48,904
49,490
50,078
50,665
51,253
52,727
54,208
55,697
57,192
58,690
60,193
61,704
63,219
64,742
66,271
67,802
69,339
70,883
72,433
73,987
75,546
77,112
78,682
80,258
81,837
83,419
85,009
86,601
88,203
89,804
u
s°
263.861
264.283
264.701
265.113
265.521
265.925
266.326
266.722
267.115
267.505
267.891
268.275
268.655
269.588
270.504
271.399
272.278
273.136
273.981
274.809
275.625
276.424
277.207
277.979
278.738
279.485
280.219
280.942
281.654
282.357
283.048
283.728
284.399
285.060
285.713
286.355
286.989
287.614
Oxygen, O2
(h°f 0 kJ/kmol)
58,800
59,624
60,371
61,118
61,866
62,616
63,365
64,116
64,868
65,620
66,374
67,127
67,881
69,772
71,668
73,573
75,484
77,397
79,316
81,243
83,174
85,112
87,057
89,004
90,956
92,916
94,881
96,852
98,826
100,808
102,793
104,785
106,780
108,778
110,784
112,795
114,809
116,827
T(K), h and u(kJ/kmol), s°(kJ/kmol # K)
Source: Tables A-23 are based on the JANAF Thermochemical Tables, NSRDS-NBS-37, 1971.
h
86,420
87,612
88,806
90,000
91,196
92,394
93,593
94,793
95,995
97,197
98,401
99,606
100,804
103,835
106,864
109,898
112,939
115,984
119,035
122,091
125,152
128,219
131,290
134,368
137,449
140,533
143,620
146,713
149,808
152,908
156,009
159,117
162,226
165,341
168,456
171,576
174,695
177,822
T
1760
1780
1800
1820
1840
1860
1880
1900
1920
1940
1960
1980
2000
2050
2100
2150
2200
2250
2300
2350
2400
2450
2500
2550
2600
2650
2700
2750
2800
2850
2900
2950
3000
3050
3100
3150
3200
3250
Carbon Dioxide, CO2
(h°f 393,520 kJ/kmol)
TABLE A-23
Copyright © 2006. Wiley. All rights reserved.
h
u
41,594
42,139
42,685
43,231
43,777
44,324
44,873
45,423
45,973
46,524
47,075
47,627
48,181
49,567
50,957
52,351
53,749
55,149
56,553
57,958
59,366
60,779
62,195
63,613
65,033
66,455
67,880
69,306
70,734
72,163
73,593
75,028
76,464
77,902
79,341
80,782
82,224
83,668
Table A-23
56,227
56,938
57,651
58,363
59,075
59,790
60,504
61,220
61,936
62,654
63,381
64,090
64,810
66,612
68,417
70,226
72,040
73,856
75,676
77,496
79,320
81,149
82,981
84,814
86,650
88,488
90,328
92,171
94,014
95,859
97,705
99,556
101,407
103,260
105,115
106,972
108,830
110,690
s°
247.396
247.798
248.195
248.589
248.979
249.365
249.748
250.128
250.502
250.874
251.242
251.607
251.969
252.858
253.726
254.578
255.412
256.227
257.027
257.810
258.580
259.332
260.073
260.799
261.512
262.213
262.902
263.577
264.241
264.895
265.538
266.170
266.793
267.404
268.007
268.601
269.186
269.763
Nitrogen, N2
(h°f 0 kJ/kmol)
T
1760
1780
1800
1820
1840
1860
1880
1900
1920
1940
1960
1980
2000
2050
2100
2150
2200
2250
2300
2350
2400
2450
2500
2550
2600
2650
2700
2750
2800
2850
2900
2950
3000
3050
3100
3150
3200
3250
762
Tables in SI Units
Constants for the van der Waals, Redlich–Kwong, and Benedict–Webb–Rubin Equations of State
TABLE A-24
1. van der Waals and Redlich–Kwong: Constants for pressure in bar, specific volume in m3/kmol, and temperature in K
van der Waals
a
m3 2
bar a
b
kmol
b
m3
kmol
a
m3 2 12
bar a
b K
kmol
b
m3
kmol
Air
Butane (C4H10)
Carbon dioxide (CO2)
1.368
13.86
3.647
0.0367
0.1162
0.0428
15.989
289.55
64.43
0.02541
0.08060
0.02963
Carbon monoxide (CO)
Methane (CH4)
Nitrogen (N2)
1.474
2.293
1.366
0.0395
0.0428
0.0386
17.22
32.11
15.53
0.02737
0.02965
0.02677
Oxygen (O2)
Propane (C3H8)
Refrigerant 12
1.369
9.349
10.49
0.0317
0.0901
0.0971
17.22
182.23
208.59
0.02197
0.06242
0.06731
Sulfur dioxide (SO2)
Water (H2O)
6.883
5.531
0.0569
0.0305
144.80
142.59
0.03945
0.02111
Substance
Table A-24
Redlich–Kwong
Source: Calculated from critical data.
2. Benedict–Webb–Rubin: Constants for pressure in bar, specific volume in m3/kmol, and temperature in K
a
A
b
B
c
C
C4H10
CO2
CO
1.9073
0.1386
0.0371
10.218
2.7737
1.3590
0.039998
0.007210
0.002632
0.12436
0.04991
0.05454
3.206 105
1.512 104
1.054 103
1.006 106
1.404 105
8.676 103
1.101 103
8.47 105
1.350 104
0.0340
0.00539
0.0060
CH4
N2
0.0501
0.0254
1.8796
1.0676
0.003380
0.002328
0.04260
0.04074
2.579 103
7.381 102
2.287 104
8.166 103
1.244 104
1.272 104
0.0060
0.0053
Substance
Copyright © 2006. Wiley. All rights reserved.
Source: H. W. Cooper and J. C. Goldfrank, Hydrocarbon Processing, 46 (12): 141 (1967).
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in SI Units
TABLE A-25
763
Thermochemical Properties of Selected Substances at 298K and 1 atm
Enthalpy of
Formation, h°f
(kJ/kmol)
Gibbs Function
of Formation,
g°f (kJ/kmol)
Absolute
Entropy, s°
(kJ/kmol # K)
Higher,
HHV
(kJ/kg)
Lower,
LHV
(kJ/kg)
Substance
Formula
Molar Mass,
M (kg/kmol)
Carbon
Hydrogen
Nitrogen
Oxygen
C(s)
H2(g)
N2(g)
O2(g)
12.01
2.016
28.01
32.00
0
0
0
0
0
0
0
0
5.74
130.57
191.50
205.03
32,770
141,780
—
—
32,770
119,950
—
—
Carbon monoxide
Carbon dioxide
Water
Water
CO(g)
CO2(g)
H2O(g)
H2O(l)
28.01
44.01
18.02
18.02
110,530
393,520
241,820
285,830
137,150
394,380
228,590
237,180
197.54
213.69
188.72
69.95
—
—
—
—
—
—
—
—
Hydrogen peroxide
Ammonia
Oxygen
Hydrogen
H2O2(g)
NH3(g)
O(g)
H(g)
34.02
17.03
16.00
1.008
136,310
46,190
249,170
218,000
105,600
16,590
231,770
203,290
232.63
192.33
160.95
114.61
—
—
—
—
—
—
—
—
Nitrogen
Hydroxyl
Methane
Acetylene
N(g)
OH(g)
CH4(g)
C2H2(g)
14.01
17.01
16.04
26.04
472,680
39,460
74,850
226,730
455,510
34,280
50,790
209,170
153.19
183.75
186.16
200.85
—
—
55,510
49,910
—
—
50,020
48,220
Ethylene
Ethane
Propylene
Propane
C2H2(g)
C2H6(g)
C3H6(g)
C3H8(g)
28.05
30.07
42.08
44.09
52,280
84,680
20,410
103,850
68,120
32,890
62,720
23,490
219.83
229.49
266.94
269.91
50,300
51,870
48,920
50,350
47,160
47,480
45,780
46,360
Butane
Pentane
Octane
Octane
Benzene
C4H10(g)
C5H12(g)
C8H18(g)
C8H18(l)
C6H6(g)
58.12
72.15
114.22
114.22
78.11
126,150
146,440
208,450
249,910
82,930
15,710
8,200
17,320
6,610
129,660
310.03
348.40
463.67
360.79
269.20
49,500
49,010
48,260
47,900
42,270
45,720
45,350
44,790
44,430
40,580
Methyl alcohol
Methyl alcohol
Ethyl alcohol
Ethyl alcohol
CH3OH(g)
CH3OH(l)
C2H5OH(g)
C2H5OH(l)
32.04
32.04
46.07
46.07
200,890
238,810
235,310
277,690
162,140
166,290
168,570
174,890
239.70
126.80
282.59
160.70
23,850
22,670
30,590
29,670
21,110
19,920
27,720
26,800
Copyright © 2006. Wiley. All rights reserved.
Source: Based on JANAF Thermochemical Tables, NSRDS-NBS-37, 1971; Selected Values of Chemical Thermodynamic Properties, NBS Tech.
Note 270-3, 1968; and API Research Project 44, Carnegie Press, 1953. Heating values calculated.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Table A-25
Heating Values
764
Tables in SI Units
Standard Molar Chemical Exergy, e ch (kJ/kmol), of
Selected Substances at 298 K and p0
Copyright © 2006. Wiley. All rights reserved.
Table A-26
TABLE A-26
Substance
Formula
Model Ia
Model IIb
Nitrogen
Oxygen
Carbon dioxide
Water
Water
N2(g)
O2(g)
CO2(g)
H2O(g)
H2O(l)
640
3,950
14,175
8,635
45
720
3,970
19,870
9,500
900
Carbon (graphite)
Hydrogen
Sulfur
Carbon monoxide
Sulfur dioxide
C(s)
H2(g)
S(s)
CO(g)
SO2(g)
404,590
235,250
598,160
269,410
301,940
410,260
236,100
609,600
275,100
313,400
Nitrogen monoxide
Nitrogen dioxide
Hydrogen sulfide
Ammonia
Methane
Ethane
NO(g)
NO2(g)
H2S(g)
NH3(g)
CH4(g)
C2H6(g)
88,850
55,565
799,890
336,685
824,350
1,482,035
88,900
55,600
812,000
337,900
831,650
1,495,840
CH3OH(g)
CH3OH(l)
C2H5OH(g)
C2H5OH(l)
715,070
710,745
1,348,330
1,342,085
722,300
718,000
1,363,900
1,357,700
Methyl alcohol
Methyl alcohol
Ethyl alcohol
Ethyl alcohol
a
J. Ahrendts, “Die Exergie Chemisch Reaktionsfähiger Systeme,’’ VDIForschungsheft, VDI-Verlag, Dusseldorf, 579, 1977. Also see “Reference
States,’’ Energy—The International Journal, 5: 667– 677, 1980. In Model I,
p0 1.019 atm. This model attempts to impose a criterion that the reference
environment be in equilibrium. The reference substances are determined
assuming restricted chemical equilibrium for nitric acid and nitrates and
unrestricted thermodynamic equilibrium for all other chemical components of
the atmosphere, the oceans, and a portion of the Earth’s crust. The chemical
composition of the gas phase of this model approximates the composition of
the natural atmosphere.
b
J. Szargut, D. R. Morris, and F. R. Steward, Exergy Analysis of Thermal,
Chemical, and Metallurgical Processes, Hemisphere, New York, 1988. In Model
II, p0 1.0 atm. In developing this model a reference substance is selected for
each chemical element from among substances that contain the element being
considered and that are abundantly present in the natural environment, even
though the substances are not in completely mutual stable equilibrium. An
underlying rationale for this approach is that substances found abundantly in
nature have little economic value. On an overall basis, the chemical composition
of the exergy reference environment of Model II is closer than Model I to the
composition of the natural environment, but the equilibrium criterion is not
always satisfied.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in SI Units
TABLE A-27
765
Logarithms to the Base 10 of the Equilibrium Constant K
log10 K
1
2 N2
Temp.
K
H2 w
x 2H
O2 w
x 2O
N2 w
x 2N
w
x NO
H2O w
x
H2 21O2
H2O w
x
OH 21H2
CO2 w
x
CO 12O2
298
500
1000
1200
1400
71.224
40.316
17.292
13.414
10.630
81.208
45.880
19.614
15.208
12.054
159.600
92.672
43.056
34.754
28.812
15.171
8.783
4.062
3.275
2.712
40.048
22.886
10.062
7.899
6.347
46.054
26.130
11.280
8.811
7.021
45.066
25.025
10.221
7.764
6.014
5.018
2.139
0.159
0.135
0.333
537
900
1800
2160
2520
1600
1700
1800
1900
2000
8.532
7.666
6.896
6.204
5.580
9.684
8.706
7.836
7.058
6.356
24.350
22.512
20.874
19.410
18.092
2.290
2.116
1.962
1.823
1.699
5.180
4.699
4.270
3.886
3.540
5.677
5.124
4.613
4.190
3.776
4.706
4.169
3.693
3.267
2.884
0.474
0.530
0.577
0.619
0.656
2880
3060
3240
3420
3600
2100
2200
2300
2400
2500
5.016
4.502
4.032
3.600
3.202
5.720
5.142
4.614
4.130
3.684
16.898
15.810
14.818
13.908
13.070
1.586
1.484
1.391
1.305
1.227
3.227
2.942
2.682
2.443
2.224
3.434
3.091
2.809
2.520
2.270
2.539
2.226
1.940
1.679
1.440
0.688
0.716
0.742
0.764
0.784
3780
3960
4140
4320
4500
2600
2700
2800
2900
3000
2.836
2.494
2.178
1.882
1.606
3.272
2.892
2.536
2.206
1.898
12.298
11.580
10.914
10.294
9.716
1.154
1.087
1.025
0.967
0.913
2.021
1.833
1.658
1.495
1.343
2.038
1.823
1.624
1.438
1.265
1.219
1.015
0.825
0.649
0.485
0.802
0.818
0.833
0.846
0.858
4680
4860
5040
5220
5400
3100
3200
3300
3400
3500
1.348
1.106
0.878
0.664
0.462
1.610
1.340
1.086
0.846
0.620
9.174
8.664
8.186
7.736
7.312
0.863
0.815
0.771
0.729
0.690
1.201
1.067
0.942
0.824
0.712
1.103
0.951
0.809
0.674
0.547
0.332
0.189
0.054
0.071
0.190
0.869
0.878
0.888
0.895
0.902
5580
5760
5940
6120
6300
Copyright © 2006. Wiley. All rights reserved.
Source: Based on data from the JANAF Thermochemical Tables, NSRDS-NBS-37, 1971.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
CO2
CO
H2 w
x
H 2O
Temp.
R
Table A-27
1
2 O2
Index to Tables in English Units
TABLE A-1E
TABLE A-2E
TABLE A-3E
TABLE A-4E
TABLE A-5E
TABLE A-6E
TABLE A-7E
TABLE A-8E
TABLE A-9E
TABLE A-10E
TABLE A-11E
TABLE A-12E
TABLE A-13E
TABLE A-14E
TABLE A-15E
TABLE A-16E
TABLE A-17E
TABLE A-18E
TABLE A-19E
TABLE A-20E
TABLE A-21E
TABLE A-22E
TABLE A-23E
TABLE A-24E
Copyright © 2006. Wiley. All rights reserved.
TABLE A-25E
Atomic or Molecular Weights and Critical Properties of Selected Elements and Compounds
Properties of Saturated Water (Liquid–Vapor): Temperature Table
Properties of Saturated Water (Liquid–Vapor): Pressure Table
Properties of Superheated Water Vapor
Properties of Compressed Liquid Water
Properties of Saturated Water (Solid–Vapor): Temperature Table
Properties of Saturated Refrigerant 22 (Liquid–Vapor): Temperature Table
Properties of Saturated Refrigerant 22 (Liquid–Vapor): Pressure Table
Properties of Superheated Refrigerant 22 Vapor
Properties of Saturated Refrigerant 134a (Liquid–Vapor): Temperature Table
Properties of Saturated Refrigerant 134a (Liquid–Vapor): Pressure Table
Properties of Superheated Refrigerant 134a Vapor
Properties of Saturated Ammonia (Liquid–Vapor): Temperature Table
Properties of Saturated Ammonia (Liquid–Vapor): Pressure Table
Properties of Superheated Ammonia Vapor
Properties of Saturated Propane (Liquid–Vapor): Temperature Table
Properties of Saturated Propane (Liquid–Vapor): Pressure Table
Properties of Superheated Propane Vapor
Properties of Selected Solids and Liquids: cp, r, and k
Ideal Gas Specific Heats of Some Common Gases
Variation of cp with Temperature for Selected Ideal Gases
Ideal Gas Properties of Air
Ideal Gas Properties of Selected Gases
Constants for the van der Waals, Redlich–Kwong, and Benedict–Webb–Rubin Equations
of State
Thermochemical Properties of Selected Substances at 537R and 1 atm.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
766
767
768
770
772
778
779
780
781
782
786
787
788
791
792
793
797
798
799
803
804
805
806
808
812
813
TABLE A-1E
Atomic or Molecular Weights and Critical Properties of Some Selected Elements and
Compounds
Substance
Chemical
Formula
Acetylene
Air (equivalent)
Ammonia
pcvc
RTc
M
(lb/lbmol)
Tc
(R)
pc
(atm)
C2H2
—
NH3
26.04
28.97
17.03
556
239
730
62
37.2
111.3
0.274
0.284
0.242
Argon
Benzene
Butane
Ar
C6H6
C4H10
39.94
78.11
58.12
272
1013
765
47.97
48.7
37.5
0.290
0.274
0.274
Carbon
Carbon dioxide
Carbon monoxide
C
CO2
CO
12.01
44.01
28.01
—
548
239
—
72.9
34.5
—
0.276
0.294
Copper
Ethane
Ethyl alcohol
Cu
C2H6
C2H5OH
63.54
30.07
46.07
—
549
929
—
48.2
63.0
—
0.285
0.249
Ethylene
Helium
Hydrogen
C2H4
He
H2
28.05
4.003
2.016
510
9.33
59.8
50.5
2.26
12.8
0.270
0.300
0.304
Methane
Methyl alcohol
Nitrogen
CH4
CH3OH
N2
16.04
32.04
28.01
344
924
227
45.8
78.5
33.5
0.290
0.220
0.291
Octane
Oxygen
Propane
C8H18
O2
C3H8
114.22
32.00
44.09
1025
278
666
24.6
49.8
42.1
0.258
0.290
0.276
Propylene
Refrigerant 12
Refrigerant 22
C3H6
CCl2F2
CHClF2
42.08
120.92
86.48
657
693
665
45.6
40.6
49.1
0.276
0.278
0.267
Refrigerant 134a
Sulfur dioxide
Water
CF3CH2F
SO2
H2O
102.03
64.06
18.02
673
775
1165
40.2
77.7
218.0
0.260
0.268
0.233
Copyright © 2006. Wiley. All rights reserved.
Sources: Adapted from International Critical Tables and L. C. Nelson and E. F. Obert, Generalized
Compressibility Charts, Chem. Eng., 617: 203 (1954).
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Zc 767
Table A-1E
Tables in English Units
768
Tables in English Units
Copyright © 2006. Wiley. All rights reserved.
H2O
TABLE A-2E
Properties of Saturated Water (Liquid–Vapor): Temperature Table
Specific Volume
ft3/lb
Internal Energy
Btu/lb
Enthalpy
Btu/lb
Entropy
Btu/lb # R
Temp.
F
Press.
lbf/in.2
Sat.
Liquid
vf
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Temp.
F
32
35
40
45
50
0.0886
0.0999
0.1217
0.1475
0.1780
0.01602
0.01602
0.01602
0.01602
0.01602
3305
2948
2445
2037
1704
.01
2.99
8.02
13.04
18.06
1021.2
1022.2
1023.9
1025.5
1027.2
.01
3.00
8.02
13.04
18.06
1075.4
1073.7
1070.9
1068.1
1065.2
1075.4
1076.7
1078.9
1081.1
1083.3
.00003
0.00607
0.01617
0.02618
0.03607
2.1870
2.1764
2.1592
2.1423
2.1259
32
35
40
45
50
52
54
56
58
60
0.1917
0.2064
0.2219
0.2386
0.2563
0.01603
0.01603
0.01603
0.01603
0.01604
1589
1482
1383
1292
1207
20.06
22.07
24.08
26.08
28.08
1027.8
1028.5
1029.1
1029.8
1030.4
20.07
22.07
24.08
26.08
28.08
1064.1
1063.0
1061.9
1060.7
1059.6
1084.2
1085.1
1085.9
1086.8
1087.7
0.04000
0.04391
0.04781
0.05159
0.05555
2.1195
2.1131
2.1068
2.1005
2.0943
52
54
56
58
60
62
64
66
68
70
0.2751
0.2952
0.3165
0.3391
0.3632
0.01604
0.01604
0.01604
0.01605
0.01605
1129
1056
988.4
925.8
867.7
30.09
32.09
34.09
36.09
38.09
1031.1
1031.8
1032.4
1033.1
1033.7
30.09
32.09
34.09
36.09
38.09
1058.5
1057.3
1056.2
1055.1
1054.0
1088.6
1089.4
1090.3
1091.2
1092.0
0.05940
0.06323
0.06704
0.07084
0.07463
2.0882
2.0821
2.0761
2.0701
2.0642
62
64
66
68
70
72
74
76
78
80
0.3887
0.4158
0.4446
0.4750
0.5073
0.01606
0.01606
0.01606
0.01607
0.01607
813.7
763.5
716.8
673.3
632.8
40.09
42.09
44.09
46.09
48.08
1034.4
1035.0
1035.7
1036.3
1037.0
40.09
42.09
44.09
46.09
48.09
1052.8
1051.7
1050.6
1049.4
1048.3
1092.9
1093.8
1094.7
1095.5
1096.4
0.07839
0.08215
0.08589
0.08961
0.09332
2.0584
2.0526
2.0469
2.0412
2.0356
72
74
76
78
80
82
84
86
88
90
0.5414
0.5776
0.6158
0.6562
0.6988
0.01608
0.01608
0.01609
0.01609
0.01610
595.0
559.8
527.0
496.3
467.7
50.08
52.08
54.08
56.07
58.07
1037.6
1038.3
1038.9
1039.6
1040.2
50.08
52.08
54.08
56.07
58.07
1047.2
1046.0
1044.9
1043.8
1042.7
1097.3
1098.1
1099.0
1099.9
1100.7
0.09701
0.1007
0.1044
0.1080
0.1117
2.0300
2.0245
2.0190
2.0136
2.0083
82
84
86
88
90
92
94
96
98
100
0.7439
0.7914
0.8416
0.8945
0.9503
0.01611
0.01611
0.01612
0.01612
0.01613
440.9
415.9
392.4
370.5
350.0
60.06
62.06
64.05
66.05
68.04
1040.9
1041.5
1041.2
1042.8
1043.5
60.06
62.06
64.06
66.05
68.05
1041.5
1040.4
1039.2
1038.1
1037.0
1101.6
1102.4
1103.3
1104.2
1105.0
0.1153
0.1189
0.1225
0.1261
0.1296
2.0030
1.9977
1.9925
1.9874
1.9822
92
94
96
98
100
110
120
130
140
150
1.276
1.695
2.225
2.892
3.722
0.01617
0.01621
0.01625
0.01629
0.01634
265.1
203.0
157.2
122.9
97.0
78.02
87.99
97.97
107.95
117.95
1046.7
1049.9
1053.0
1056.2
1059.3
78.02
88.00
97.98
107.96
117.96
1031.3
1025.5
1019.8
1014.0
1008.1
1109.3
1113.5
1117.8
1121.9
1126.1
0.1473
0.1647
0.1817
0.1985
0.2150
1.9574
1.9336
1.9109
1.8892
1.8684
110
120
130
140
150
160
170
180
190
200
4.745
5.996
7.515
9.343
11.529
0.01640
0.01645
0.01651
0.01657
0.01663
77.2
62.0
50.2
41.0
33.6
127.94
137.95
147.97
158.00
168.04
1062.3
1065.4
1068.3
1071.3
1074.2
127.96
137.97
147.99
158.03
168.07
1002.2
996.2
990.2
984.1
977.9
1130.1
1134.2
1138.2
1142.1
1145.9
0.2313
0.2473
0.2631
0.2787
0.2940
1.8484
1.8293
1.8109
1.7932
1.7762
160
170
180
190
200
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
769
Tables in English Units
(Continued )
Copyright © 2006. Wiley. All rights reserved.
Specific Volume
ft3/lb
Internal Energy
Btu/lb
Enthalpy
Btu/lb
Entropy
Btu/lb # R
Temp.
F
Press.
lbf/in.2
Sat.
Liquid
vf
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Temp.
F
210
212
220
230
240
14.13
14.70
17.19
20.78
24.97
0.01670
0.01672
0.01677
0.01685
0.01692
27.82
26.80
23.15
19.39
16.33
178.1
180.1
188.2
198.3
208.4
1077.0
1077.6
1079.8
1082.6
1085.3
178.1
180.2
188.2
198.3
208.4
971.6
970.3
965.3
958.8
952.3
1149.7
1150.5
1153.5
1157.1
1160.7
0.3091
0.3121
0.3241
0.3388
0.3534
1.7599
1.7567
1.7441
1.7289
1.7143
210
212
220
230
240
250
260
270
280
290
29.82
35.42
41.85
49.18
57.53
0.01700
0.01708
0.01717
0.01726
0.01735
13.83
11.77
10.07
8.65
7.47
218.5
228.6
238.8
249.0
259.3
1087.9
1090.5
1093.0
1095.4
1097.7
218.6
228.8
239.0
249.2
259.4
945.6
938.8
932.0
924.9
917.8
1164.2
1167.6
1170.9
1174.1
1177.2
0.3677
0.3819
0.3960
0.4099
0.4236
1.7001
1.6864
1.6731
1.6602
1.6477
250
260
270
280
290
300
310
320
330
340
66.98
77.64
89.60
103.00
117.93
0.01745
0.01755
0.01765
0.01776
0.01787
6.472
5.632
4.919
4.312
3.792
269.5
279.8
290.1
300.5
310.9
1100.0
1102.1
1104.2
1106.2
1108.0
269.7
280.1
290.4
300.8
311.3
910.4
903.0
895.3
887.5
879.5
1180.2
1183.0
1185.8
1188.4
1190.8
0.4372
0.4507
0.4640
0.4772
0.4903
1.6356
1.6238
1.6123
1.6010
1.5901
300
310
320
330
340
350
360
370
380
390
134.53
152.92
173.23
195.60
220.2
0.01799
0.01811
0.01823
0.01836
0.01850
3.346
2.961
2.628
2.339
2.087
321.4
331.8
342.4
353.0
363.6
1109.8
1111.4
1112.9
1114.3
1115.6
321.8
332.4
343.0
353.6
364.3
871.3
862.9
854.2
845.4
836.2
1193.1
1195.2
1197.2
1199.0
1200.6
0.5033
0.5162
0.5289
0.5416
0.5542
1.5793
1.5688
1.5585
1.5483
1.5383
350
360
370
380
390
400
410
420
430
440
247.1
276.5
308.5
343.3
381.2
0.01864
0.01878
0.01894
0.01909
0.01926
1.866
1.673
1.502
1.352
1.219
374.3
385.0
395.8
406.7
417.6
1116.6
1117.6
1118.3
1118.9
1119.3
375.1
386.0
396.9
407.9
419.0
826.8
817.2
807.2
796.9
786.3
1202.0
1203.1
1204.1
1204.8
1205.3
0.5667
0.5792
0.5915
0.6038
0.6161
1.5284
1.5187
1.5091
1.4995
1.4900
400
410
420
430
440
450
460
470
480
490
422.1
466.3
514.1
565.5
620.7
0.01943
0.01961
0.01980
0.02000
0.02021
1.1011
0.9961
0.9025
0.8187
0.7436
428.6
439.7
450.9
462.2
473.6
1119.5
1119.6
1119.4
1118.9
1118.3
430.2
441.4
452.8
464.3
475.9
775.4
764.1
752.4
740.3
727.8
1205.6
1205.5
1205.2
1204.6
1203.7
0.6282
0.6404
0.6525
0.6646
0.6767
1.4806
1.4712
1.4618
1.4524
1.4430
450
460
470
480
490
500
520
540
560
580
680.0
811.4
961.5
1131.8
1324.3
0.02043
0.02091
0.02145
0.02207
0.02278
0.6761
0.5605
0.4658
0.3877
0.3225
485.1
508.5
532.6
548.4
583.1
1117.4
1114.8
1111.0
1105.8
1098.9
487.7
511.7
536.4
562.0
588.6
714.8
687.3
657.5
625.0
589.3
1202.5
1198.9
1193.8
1187.0
1178.0
0.6888
0.7130
0.7374
0.7620
0.7872
1.4335
1.4145
1.3950
1.3749
1.3540
500
520
540
560
580
600
620
640
660
680
1541.0
1784.4
2057.1
2362
2705
0.02363
0.02465
0.02593
0.02767
0.03032
0.2677
0.2209
0.1805
0.1446
0.1113
609.9
638.3
668.7
702.3
741.7
1090.0
1078.5
1063.2
1042.3
1011.0
616.7
646.4
678.6
714.4
756.9
549.7
505.0
453.4
391.1
309.8
1166.4
1151.4
1131.9
1105.5
1066.7
0.8130
0.8398
0.8681
0.8990
0.9350
1.3317
1.3075
1.2803
1.2483
1.2068
600
620
640
660
680
700
705.4
3090
3204
0.03666
0.05053
0.0744
0.05053
801.7
872.6
947.7
872.6
822.7
902.5
167.5
0
990.2
902.5
0.9902
1.0580
1.1346
1.0580
700
705.4
Source: Tables A-2E through A-6E are extracted from J. H. Keenan, F. G. Keyes, P. G. Hill, and J. G. Moore, Steam Tables, Wiley, New York,
1969.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
H2O
TABLE A-2E
770
Tables in English Units
Copyright © 2006. Wiley. All rights reserved.
H2O
TABLE A-3E
Properties of Saturated Water (Liquid–Vapor): Pressure Table
Specific Volume
ft3/lb
Internal Energy
Btu/lb
Enthalpy
Btu/lb
Entropy
Btu/lb # R
Press.
lbf/in.2
Temp.
F
Sat.
Liquid
vf
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Evap.
sfg
Sat.
Vapor
sg
Press.
lbf/in.2
0.4
0.6
0.8
1.0
1.2
72.84
85.19
94.35
101.70
107.88
0.01606
0.01609
0.01611
0.01614
0.01616
792.0
540.0
411.7
333.6
280.9
40.94
53.26
62.41
69.74
75.90
1034.7
1038.7
1041.7
1044.0
1046.0
40.94
53.27
62.41
69.74
75.90
1052.3
1045.4
1040.2
1036.0
1032.5
1093.3
1098.6
1102.6
1105.8
1108.4
0.0800
0.1029
0.1195
0.1327
0.1436
1.9760
1.9184
1.8773
1.8453
1.8190
2.0559
2.0213
1.9968
1.9779
1.9626
0.4
0.6
0.8
1.0
1.2
1.5
2.0
3.0
4.0
5.0
115.65
126.04
141.43
152.93
162.21
0.01619
0.01623
0.01630
0.01636
0.01641
227.7
173.75
118.72
90.64
73.53
83.65
94.02
109.38
120.88
130.15
1048.5
1051.8
1056.6
1060.2
1063.0
83.65
94.02
109.39
120.89
130.17
1028.0
1022.1
1013.1
1006.4
1000.9
1111.7
1116.1
1122.5
1127.3
1131.0
0.1571
0.1750
0.2009
0.2198
0.2349
1.7867
1.7448
1.6852
1.6426
1.6093
1.9438
1.9198
1.8861
1.8624
1.8441
1.5
2.0
3.0
4.0
5.0
6.0
7.0
8.0
9.0
10
170.03
176.82
182.84
188.26
193.19
0.01645
0.01649
0.01653
0.01656
0.01659
61.98
53.65
47.35
42.41
38.42
137.98
144.78
150.81
156.25
161.20
1065.4
1067.4
1069.2
1070.8
1072.2
138.00
144.80
150.84
156.27
161.23
996.2
992.1
988.4
985.1
982.1
1134.2
1136.9
1139.3
1141.4
1143.3
0.2474
0.2581
0.2675
0.2760
0.2836
1.5819
1.5585
1.5383
1.5203
1.5041
1.8292
1.8167
1.8058
1.7963
1.7877
6.0
7.0
8.0
9.0
10
14.696
15
20
25
30
211.99
213.03
227.96
240.08
250.34
0.01672
0.01672
0.01683
0.01692
0.01700
26.80
26.29
20.09
16.31
13.75
180.10
181.14
196.19
208.44
218.84
1077.6
1077.9
1082.0
1085.3
1088.0
180.15
181.19
196.26
208.52
218.93
970.4
969.7
960.1
952.2
945.4
1150.5
1150.9
1156.4
1160.7
1164.3
0.3121
0.3137
0.3358
0.3535
0.3682
1.4446
1.4414
1.3962
1.3607
1.3314
1.7567
1.7551
1.7320
1.7142
1.6996
14.696
15
20
25
30
35
40
45
50
55
259.30
267.26
274.46
281.03
287.10
0.01708
0.01715
0.01721
0.01727
0.01733
11.90
10.50
9.40
8.52
7.79
227.93
236.03
243.37
250.08
256.28
1090.3
1092.3
1094.0
1095.6
1097.0
228.04
236.16
243.51
250.24
256.46
939.3
933.8
928.8
924.2
919.9
1167.4
1170.0
1172.3
1174.4
1176.3
0.3809
0.3921
0.4022
0.4113
0.4196
1.3064
1.2845
1.2651
1.2476
1.2317
1.6873
1.6767
1.6673
1.6589
1.6513
35
40
45
50
55
60
65
70
75
80
292.73
298.00
302.96
307.63
312.07
0.01738
0.01743
0.01748
0.01752
0.01757
7.177
6.647
6.209
5.818
5.474
262.1
267.5
272.6
277.4
282.0
1098.3
1099.5
1100.6
1101.6
1102.6
262.2
267.7
272.8
277.6
282.2
915.8
911.9
908.3
904.8
901.4
1178.0
1179.6
1181.0
1182.4
1183.6
0.4273
0.4345
0.4412
0.4475
0.4534
1.2170
1.2035
1.1909
1.1790
1.1679
1.6443
1.6380
1.6321
1.6265
1.6213
60
65
70
75
80
85
90
95
100
110
316.29
320.31
324.16
327.86
334.82
0.01761
0.01766
0.01770
0.01774
0.01781
5.170
4.898
4.654
4.434
4.051
286.3
290.5
294.5
298.3
305.5
1103.5
1104.3
1105.0
1105.8
1107.1
286.6
290.8
294.8
298.6
305.9
898.2
895.1
892.1
889.2
883.7
1184.8
1185.9
1186.9
1187.8
1189.6
0.4591
0.4644
0.4695
0.4744
0.4836
1.1574
1.1475
1.1380
1.1290
1.1122
1.6165
1.6119
1.6075
1.6034
1.5958
85
90
95
100
110
120
130
140
150
160
341.30
347.37
353.08
358.48
363.60
0.01789
0.01796
0.01802
0.01809
0.01815
3.730
3.457
3.221
3.016
2.836
312.3
318.6
324.6
330.2
335.6
1108.3
1109.4
1110.3
1111.2
1112.0
312.7
319.0
325.1
330.8
336.2
878.5
873.5
868.7
864.2
859.8
1191.1
1192.5
1193.8
1194.9
1196.0
0.4920
0.4999
0.5073
0.5142
0.5208
1.0966
1.0822
1.0688
1.0562
1.0443
1.5886
1.5821
1.5761
1.5704
1.5651
120
130
140
150
160
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in English Units
Copyright © 2006. Wiley. All rights reserved.
(Continued )
Specific Volume
ft3/lb
Internal Energy
Btu/lb
Enthalpy
Btu/lb
Entropy
Btu/lb # R
Press.
lbf/in.2
Temp.
F
Sat.
Liquid
vf
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Evap.
sfg
Sat.
Vapor
sg
Press.
lbf/in.2
170
180
190
200
250
368.47
373.13
377.59
381.86
401.04
0.01821
0.01827
0.01833
0.01839
0.01865
2.676
2.553
2.405
2.289
1.845
340.8
345.7
350.4
354.9
375.4
1112.7
1113.4
1114.0
1114.6
1116.7
341.3
346.3
351.0
355.6
376.2
855.6
851.5
847.5
843.7
825.8
1196.9
1197.8
1198.6
1199.3
1202.1
0.5270
0.5329
0.5386
0.5440
0.5680
1.0330
1.0223
1.0122
1.0025
0.9594
1.5600
1.5552
1.5508
1.5465
1.5274
170
180
190
200
250
300
350
400
450
500
417.43
431.82
444.70
456.39
467.13
0.01890
0.01912
0.01934
0.01955
0.01975
1.544
1.327
1.162
1.033
0.928
393.0
408.7
422.8
435.7
447.7
1118.2
1119.0
1119.5
1119.6
1119.4
394.1
409.9
424.2
437.4
449.5
809.8
795.0
781.2
768.2
755.8
1203.9
1204.9
1205.5
1205.6
1205.3
0.5883
0.6060
0.6218
0.6360
0.6490
0.9232
0.8917
0.8638
0.8385
0.8154
1.5115
1.4977
1.4856
1.4745
1.4644
300
350
400
450
500
550
600
700
800
900
477.07
486.33
503.23
518.36
532.12
0.01994
0.02013
0.02051
0.02087
0.02123
0.842
0.770
0.656
0.569
0.501
458.9
469.4
488.9
506.6
523.0
1119.1
1118.6
1117.0
1115.0
1112.6
460.9
471.7
491.5
509.7
526.6
743.9
732.4
710.5
689.6
669.5
1204.8
1204.1
1202.0
1199.3
1196.0
0.6611
0.6723
0.6927
0.7110
0.7277
0.7941
0.7742
0.7378
0.7050
0.6750
1.4451
1.4464
1.4305
1.4160
1.4027
550
600
700
800
900
1000
1100
1200
1300
1400
544.75
556.45
567.37
577.60
587.25
0.02159
0.02195
0.02232
0.02269
0.02307
0.446
0.401
0.362
0.330
0.302
538.4
552.9
566.7
579.9
592.7
1109.9
1106.8
1103.5
1099.8
1096.0
542.4
557.4
571.7
585.4
598.6
650.0
631.0
612.3
593.8
575.5
1192.4
1188.3
1183.9
1179.2
1174.1
0.7432
0.7576
0.7712
0.7841
0.7964
0.6471
0.6209
0.5961
0.5724
0.5497
1.3903
1.3786
1.3673
1.3565
1.3461
1000
1100
1200
1300
1400
1500
1600
1700
1800
1900
596.39
605.06
613.32
621.21
628.76
0.02346
0.02386
0.02428
0.02472
0.02517
0.277
0.255
0.236
0.218
0.203
605.0
616.9
628.6
640.0
651.3
1091.8
1087.4
1082.7
1077.7
1072.3
611.5
624.0
636.2
648.3
660.1
557.2
538.9
520.6
502.1
483.4
1168.7
1162.9
1156.9
1150.4
1143.5
0.8082
0.8196
0.8307
0.8414
0.8519
0.5276
0.5062
0.4852
0.4645
0.4441
1.3359
1.3258
1.3159
1.3060
1.2961
1500
1600
1700
1800
1900
2000
2250
2500
2750
3000
636.00
652.90
668.31
682.46
695.52
0.02565
0.02698
0.02860
0.03077
0.03431
0.188
0.157
0.131
0.107
0.084
662.4
689.9
717.7
747.3
783.4
1066.6
1050.6
1031.0
1005.9
968.8
671.9
701.1
730.9
763.0
802.5
464.4
414.8
360.5
297.4
213.0
1136.3
1115.9
1091.4
1060.4
1015.5
0.8623
0.8876
0.9131
0.9401
0.9732
0.4238
0.3728
0.3196
0.2604
0.1843
1.2861
1.2604
1.2327
1.2005
1.1575
2000
2250
2500
2750
3000
3203.6
705.44
0.05053
0.0505
872.6
872.6
902.5
0
902.5
1.0580
0
1.0580
3203.6
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
H2O
TABLE A-3E
771
772
Tables in English Units
TABLE A-4E
T
F
v
ft3/lb
Properties of Superheated Water Vapor
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
H2O
h
Btu/lb
s
Btu/lb # R
p 5 lbf/in.2
(Tsat 162.2F)
p 1 lbf/in.2
(Tsat 101.7F)
Sat.
150
200
333.6
362.6
392.5
1044.0
1060.4
1077.5
1105.8
1127.5
1150.1
1.9779
2.0151
2.0508
73.53
1063.0
1131.0
1.8441
78.15
1076.0
1148.6
1.8715
250
300
400
422.4
452.3
511.9
1094.7
1112.0
1147.0
1172.8
1195.7
1241.8
2.0839
2.1150
2.1720
84.21
90.24
102.24
1093.8
1111.3
1146.6
1171.7
1194.8
1241.2
1.9052
1.9367
1.9941
500
600
700
571.5
631.1
690.7
1182.8
1219.3
1256.7
1288.5
1336.1
1384.5
2.2235
2.2706
2.3142
114.20
126.15
138.08
1182.5
1219.1
1256.5
1288.2
1335.8
1384.3
2.0458
2.0930
2.1367
800
900
1000
750.3
809.9
869.5
1294.4
1333.9
1373.9
1433.7
1483.8
1534.8
2.3550
2.3932
2.4294
150.01
161.94
173.86
1294.7
1333.8
1373.9
1433.5
1483.7
1534.7
2.1775
2.2158
2.2520
p 10 lbf/in.2
(Tsat 193.2F)
Copyright © 2006. Wiley. All rights reserved.
u
Btu/lb
p 14.7 lbf/in.2
(Tsat 212.0F)
Sat.
200
250
38.42
38.85
41.95
1072.2
1074.7
1092.6
1143.3
1146.6
1170.2
1.7877
1.7927
1.8272
26.80
1077.6
1150.5
1.7567
28.42
1091.5
1168.8
1.7832
300
400
500
44.99
51.03
57.04
1110.4
1146.1
1182.2
1193.7
1240.5
1287.7
1.8592
1.9171
1.9690
30.52
34.67
38.77
1109.6
1145.6
1181.8
1192.6
1239.9
1287.3
1.8157
1.8741
1.9263
600
700
800
63.03
69.01
74.98
1218.9
1256.3
1294.6
1335.5
1384.0
1433.3
2.0164
2.0601
2.1009
42.86
46.93
51.00
1218.6
1256.1
1294.4
1335.2
1383.8
1433.1
1.9737
2.0175
2.0584
900
1000
1100
80.95
86.91
92.88
1333.7
1373.8
1414.7
1483.5
1534.6
1586.6
2.1393
2.1755
2.2099
55.07
59.13
63.19
1333.6
1373.7
1414.6
1483.4
1534.5
1586.4
2.0967
2.1330
2.1674
p 20 lbf/in.2
(Tsat 228.0F)
p 40 lbf/in.2
(Tsat 267.3F)
Sat.
250
300
20.09
20.79
22.36
1082.0
1090.3
1108.7
1156.4
1167.2
1191.5
1.7320
1.7475
1.7805
10.50
1093.3
1170.0
1.6767
11.04
1105.1
1186.8
1.6993
350
400
500
23.90
25.43
28.46
1126.9
1145.1
1181.5
1215.4
1239.2
1286.8
1.8110
1.8395
1.8919
11.84
12.62
14.16
1124.2
1143.0
1180.1
1211.8
1236.4
1284.9
1.7312
1.7606
1.8140
600
700
800
31.47
34.47
37.46
1218.4
1255.9
1294.3
1334.8
1383.5
1432.9
1.9395
1.9834
2.0243
15.69
17.20
18.70
1217.3
1255.1
1293.7
1333.4
1382.4
1432.1
1.8621
1.9063
1.9474
900
1000
1100
40.45
43.44
46.42
1333.5
1373.5
1414.5
1483.2
1534.3
1586.3
2.0627
2.0989
2.1334
20.20
21.70
23.20
1333.0
1373.1
1414.2
1482.5
1533.8
1585.9
1.9859
2.0223
2.0568
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in English Units
T
F
v
ft3/lb
(Continued)
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
h
Btu/lb
s
Btu/lb # R
p 80 lbf/in.2
(Tsat 312.1F)
p 60 lbf/in.2
(Tsat 292.7F)
Sat.
300
350
7.17
7.26
7.82
1098.3
1101.3
1121.4
1178.0
1181.9
1208.2
1.6444
1.6496
1.6830
5.47
1102.6
1183.6
1.6214
5.80
1118.5
1204.3
1.6476
400
500
600
8.35
9.40
10.43
1140.8
1178.6
1216.3
1233.5
1283.0
1332.1
1.7134
1.7678
1.8165
6.22
7.02
7.79
1138.5
1177.2
1215.3
1230.6
1281.1
1330.7
1.6790
1.7346
1.7838
700
800
900
11.44
12.45
13.45
1254.4
1293.0
1332.5
1381.4
1431.2
1481.8
1.8609
1.9022
1.9408
8.56
9.32
10.08
1253.6
1292.4
1332.0
1380.3
1430.4
1481.2
1.8285
1.8700
1.9087
1000
1100
1200
14.45
15.45
16.45
1372.7
1413.8
1455.8
1533.2
1585.4
1638.5
1.9773
2.0119
2.0448
10.83
11.58
12.33
1372.3
1413.5
1455.5
1532.6
1584.9
1638.1
1.9453
1.9799
2.0130
p 100 lbf/in.2
(Tsat 327.8F)
Copyright © 2006. Wiley. All rights reserved.
u
Btu/lb
p 120 lbf/in.2
(Tsat 341.3F)
Sat.
350
400
4.434
4.592
4.934
1105.8
1115.4
1136.2
1187.8
1200.4
1227.5
1.6034
1.6191
1.6517
3.730
3.783
4.079
1108.3
1112.2
1133.8
1191.1
1196.2
1224.4
1.5886
1.5950
1.6288
450
500
600
5.265
5.587
6.216
1156.2
1175.7
1214.2
1253.6
1279.1
1329.3
1.6812
1.7085
1.7582
4.360
4.633
5.164
1154.3
1174.2
1213.2
1251.2
1277.1
1327.8
1.6590
1.6868
1.7371
700
800
900
6.834
7.445
8.053
1252.8
1291.8
1331.5
1379.2
1429.6
1480.5
1.8033
1.8449
1.8838
5.682
6.195
6.703
1252.0
1291.2
1330.9
1378.2
1428.7
1479.8
1.7825
1.8243
1.8633
1000
1100
1200
8.657
9.260
9.861
1371.9
1413.1
1455.2
1532.1
1584.5
1637.7
1.9204
1.9551
1.9882
7.208
7.711
8.213
1371.5
1412.8
1454.9
1531.5
1584.0
1637.3
1.9000
1.9348
1.9679
p 140 lbf/in.2
(Tsat 353.1F)
p 160 lbf/in.2
(Tsat 363.6F)
Sat.
400
450
3.221
3.466
3.713
1110.3
1131.4
1152.4
1193.8
1221.2
1248.6
1.5761
1.6088
1.6399
2.836
3.007
3.228
1112.0
1128.8
1150.5
1196.0
1217.8
1246.1
1.5651
1.5911
1.6230
500
550
600
3.952
4.184
4.412
1172.7
1192.5
1212.1
1275.1
1300.9
1326.4
1.6682
1.6945
1.7191
3.440
3.646
3.848
1171.2
1191.3
1211.1
1273.0
1299.2
1325.0
1.6518
1.6785
1.7034
700
800
900
4.860
5.301
5.739
1251.2
1290.5
1330.4
1377.1
1427.9
1479.1
1.7648
1.8068
1.8459
4.243
4.631
5.015
1250.4
1289.9
1329.9
1376.0
1427.0
1478.4
1.7494
1.7916
1.8308
1000
1100
1200
6.173
6.605
7.036
1371.0
1412.4
1454.6
1531.0
1583.6
1636.9
1.8827
1.9176
1.9507
5.397
5.776
6.154
1370.6
1412.1
1454.3
1530.4
1583.1
1636.5
1.8677
1.9026
1.9358
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
H2O
TABLE A-4E
773
774
Tables in English Units
TABLE A-4E
T
F
v
ft3/lb
(Continued )
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
H2O
h
Btu/lb
s
Btu/lb # R
p 200 lbf/in.2
(Tsat 381.8F)
p 180 lbf/in.2
(Tsat 373.1F)
Sat.
400
450
2.533
2.648
2.850
1113.4
1126.2
1148.5
1197.8
1214.4
1243.4
1.5553
1.5749
1.6078
2.289
2.361
2.548
1114.6
1123.5
1146.4
1199.3
1210.8
1240.7
1.5464
1.5600
1.5938
500
550
600
3.042
3.228
3.409
1169.6
1190.0
1210.0
1270.9
1297.5
1323.5
1.6372
1.6642
1.6893
2.724
2.893
3.058
1168.0
1188.7
1208.9
1268.8
1295.7
1322.1
1.6239
1.6512
1.6767
700
800
900
3.763
4.110
4.453
1249.6
1289.3
1329.4
1374.9
1426.2
1477.7
1.7357
1.7781
1.8174
3.379
3.693
4.003
1248.8
1288.6
1328.9
1373.8
1425.3
1477.1
1.7234
1.7660
1.8055
1000
1100
1200
4.793
5.131
5.467
1370.2
1411.7
1454.0
1529.8
1582.6
1636.1
1.8545
1.8894
1.9227
4.310
4.615
4.918
1369.8
1411.4
1453.7
1529.3
1582.2
1635.7
1.8425
1.8776
1.9109
p 250 lbf/in.2
(Tsat 401.0F)
Copyright © 2006. Wiley. All rights reserved.
u
Btu/lb
p 300 lbf/in.2
(Tsat 417.4F)
Sat.
450
500
1.845
2.002
2.150
1116.7
1141.1
1163.8
1202.1
1233.7
1263.3
1.5274
1.5632
1.5948
1.544
1.636
1.766
1118.2
1135.4
1159.5
1203.9
1226.2
1257.5
1.5115
1.5365
1.5701
550
600
700
2.290
2.426
2.688
1185.3
1206.1
1246.7
1291.3
1318.3
1371.1
1.6233
1.6494
1.6970
1.888
2.004
2.227
1181.9
1203.2
1244.0
1286.7
1314.5
1368.3
1.5997
1.6266
1.6751
800
900
1000
2.943
3.193
3.440
1287.0
1327.6
1368.7
1423.2
1475.3
1527.9
1.7301
1.7799
1.8172
2.442
2.653
2.860
1285.4
1326.3
1367.7
1421.0
1473.6
1526.5
1.7187
1.7589
1.7964
1100
1200
1300
3.685
3.929
4.172
1410.5
1453.0
1496.3
1581.0
1634.8
1689.3
1.8524
1.8858
1.9177
3.066
3.270
3.473
1409.6
1452.2
1495.6
1579.8
1633.8
1688.4
1.8317
1.8653
1.8973
p 350 lbf/in.2
(Tsat 431.8F)
p 400 lbf/in.2
(Tsat 444.7F)
Sat.
450
500
1.327
1.373
1.491
1119.0
1129.2
1154.9
1204.9
1218.2
1251.5
1.4978
1.5125
1.5482
1.162
1.175
1.284
1119.5
1122.6
1150.1
1205.5
1209.5
1245.2
1.4856
1.4901
1.5282
550
600
700
1.600
1.703
1.898
1178.3
1200.3
1242.5
1281.9
1310.6
1365.4
1.5790
1.6068
1.6562
1.383
1.476
1.650
1174.6
1197.3
1240.4
1277.0
1306.6
1362.5
1.5605
1.5892
1.6397
800
900
1000
2.085
2.267
2.446
1283.8
1325.0
1366.6
1418.8
1471.8
1525.0
1.7004
1.7409
1.7787
1.816
1.978
2.136
1282.1
1323.7
1365.5
1416.6
1470.1
1523.6
1.6844
1.7252
1.7632
1100
1200
1300
2.624
2.799
2.974
1408.7
1451.5
1495.0
1578.6
1632.8
1687.6
1.8142
1.8478
1.8799
2.292
2.446
2.599
1407.8
1450.7
1494.3
1577.4
1621.8
1686.8
1.7989
1.8327
1.8648
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in English Units
T
F
v
ft3/lb
(Continued)
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
h
Btu/lb
s
Btu/lb # R
p 500 lbf/in.2
(Tsat 467.1F)
p 450 lbf/in.2
(Tsat 456.4F)
Sat.
500
550
1.033
1.123
1.215
1119.6
1145.1
1170.7
1205.6
1238.5
1271.9
1.4746
1.5097
1.5436
0.928
0.992
1.079
1119.4
1139.7
1166.7
1205.3
1231.5
1266.6
1.4645
1.4923
1.5279
600
700
800
1.300
1.458
1.608
1194.3
1238.2
1280.5
1302.5
1359.6
1414.4
1.5732
1.6248
1.6701
1.158
1.304
1.441
1191.1
1236.0
1278.8
1298.3
1356.7
1412.1
1.5585
1.6112
1.6571
900
1000
1100
1.752
1.894
2.034
1322.4
1364.4
1406.9
1468.3
1522.2
1576.3
1.7113
1.7495
1.7853
1.572
1.701
1.827
1321.0
1363.3
1406.0
1466.5
1520.7
1575.1
1.6987
1.7371
1.7731
1200
1300
1400
2.172
2.308
2.444
1450.0
1493.7
1538.1
1630.8
1685.9
1741.7
1.8192
1.8515
1.8823
1.952
2.075
2.198
1449.2
1493.1
1537.6
1629.8
1685.1
1741.0
1.8072
1.8395
1.8704
p 600 lbf/in.2
(Tsat 486.3F)
Copyright © 2006. Wiley. All rights reserved.
u
Btu/lb
p 700 lbf/in.2
(Tsat 503.2F)
Sat.
500
550
0.770
0.795
0.875
1118.6
1128.0
1158.2
1204.1
1216.2
1255.4
1.4464
1.4592
1.4990
0.656
1117.0
1202.0
1.4305
0.728
1149.0
1243.2
1.4723
600
700
800
0.946
1.073
1.190
1184.5
1231.5
1275.4
1289.5
1350.6
1407.6
1.5320
1.5872
1.6343
0.793
0.907
1.011
1177.5
1226.9
1272.0
1280.2
1344.4
1402.9
1.5081
1.5661
1.6145
900
1000
1100
1.302
1.411
1.517
1318.4
1361.2
1404.2
1462.9
1517.8
1572.7
1.6766
1.7155
1.7519
1.109
1.204
1.296
1315.6
1358.9
1402.4
1459.3
1514.9
1570.2
1.6576
1.6970
1.7337
1200
1300
1400
1.622
1.726
1.829
1447.7
1491.7
1536.5
1627.8
1683.4
1739.5
1.7861
1.8186
1.8497
1.387
1.476
1.565
1446.2
1490.4
1535.3
1625.8
1681.7
1738.1
1.7682
1.8009
1.8321
p 800 lbf/in.2
(Tsat 518.3F)
p 900 lbf/in.2
(Tsat 532.1F)
Sat.
550
600
0.569
0.615
0.677
1115.0
1138.8
1170.1
1199.3
1229.9
1270.4
1.4160
1.4469
1.4861
0.501
0.527
0.587
1112.6
1127.5
1162.2
1196.0
1215.2
1260.0
1.4027
1.4219
1.4652
650
700
800
0.732
0.783
0.876
1197.2
1222.1
1268.5
1305.6
1338.0
1398.2
1.5186
1.5471
1.5969
0.639
0.686
0.772
1191.1
1217.1
1264.9
1297.5
1331.4
1393.4
1.4999
1.5297
1.5810
900
1000
1100
0.964
1.048
1.130
1312.9
1356.7
1400.5
1455.6
1511.9
1567.8
1.6408
1.6807
1.7178
0.851
0.927
1.001
1310.1
1354.5
1398.7
1451.9
1508.9
1565.4
1.6257
1.6662
1.7036
1200
1300
1400
1.210
1.289
1.367
1444.6
1489.1
1534.2
1623.8
1680.0
1736.6
1.7526
1.7854
1.8167
1.073
1.144
1.214
1443.0
1487.8
1533.0
1621.7
1687.3
1735.1
1.7386
1.7717
1.8031
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
H2O
TABLE A-4E
775
776
Tables in English Units
TABLE A-4E
T
F
v
ft3/lb
(Continued )
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
H2O
h
Btu/lb
s
Btu/lb # R
p 1200 lbf/in.2
(Tsat 567.4F)
p 1000 lbf/in.2
(Tsat 544.7F)
Sat.
600
650
0.446
0.514
0.564
1109.0
1153.7
1184.7
1192.4
1248.8
1289.1
1.3903
1.4450
1.4822
0.362
0.402
0.450
1103.5
1134.4
1170.9
1183.9
1223.6
1270.8
1.3673
1.4054
1.4490
700
800
900
0.608
0.688
0.761
1212.0
1261.2
1307.3
1324.6
1388.5
1448.1
1.5135
1.5665
1.6120
0.491
0.562
0.626
1201.3
1253.7
1301.5
1310.2
1378.4
1440.4
1.4837
1.5402
1.5876
1000
1100
1200
0.831
0.898
0.963
1352.2
1396.8
1441.5
1505.9
1562.9
1619.7
1.6530
1.6908
1.7261
0.685
0.743
0.798
1347.5
1393.0
1438.3
1499.7
1557.9
1615.5
1.6297
1.6682
1.7040
1300
1400
1600
1.027
1.091
1.215
1486.5
1531.9
1624.4
1676.5
1733.7
1849.3
1.7593
1.7909
1.8499
0.853
0.906
1.011
1483.8
1529.6
1622.6
1673.1
1730.7
1847.1
1.7377
1.7696
1.8290
p 1400 lbf/in.2
(Tsat 587.2F)
Copyright © 2006. Wiley. All rights reserved.
u
Btu/lb
p 1600 lbf/in.2
(Tsat 605.1F)
Sat.
600
650
0.302
0.318
0.367
1096.0
1110.9
1155.5
1174.1
1193.1
1250.5
1.3461
1.3641
1.4171
0.255
1087.4
1162.9
1.3258
0.303
1137.8
1227.4
1.3852
700
800
900
0.406
0.471
0.529
1189.6
1245.8
1295.6
1294.8
1367.9
1432.5
1.4562
1.5168
1.5661
0.342
0.403
0.466
1177.0
1237.7
1289.5
1278.1
1357.0
1424.4
1.4299
1.4953
1.5468
1000
1100
1200
0.582
0.632
0.681
1342.8
1389.1
1435.1
1493.5
1552.8
1611.4
1.6094
1.6487
1.6851
0.504
0.549
0.592
1338.0
1385.2
1431.8
1487.1
1547.7
1607.1
1.5913
1.6315
1.6684
1300
1400
1600
0.728
0.774
0.865
1481.1
1527.2
1620.8
1669.6
1727.8
1844.8
1.7192
1.7513
1.8111
0.634
0.675
0.755
1478.3
1524.9
1619.0
1666.1
1724.8
1842.6
1.7029
1.7354
1.7955
p 1800 lbf/in.2
(Tsat 621.2F)
p 2000 lbf/in.2
(Tsat 636.0F)
Sat.
650
700
0.218
0.251
0.291
1077.7
1117.0
1163.1
1150.4
1200.4
1259.9
1.3060
1.3517
1.4042
0.188
0.206
0.249
1066.6
1091.1
1147.7
1136.3
1167.2
1239.8
1.2861
1.3141
1.3782
750
800
900
0.322
0.350
0.399
1198.6
1229.1
1283.2
1305.9
1345.7
1416.1
1.4430
1.4753
1.5291
0.280
0.307
0.353
1187.3
1220.1
1276.8
1291.1
1333.8
1407.6
1.4216
1.4562
1.5126
1000
1100
1200
0.443
0.484
0.524
1333.1
1381.2
1428.5
1480.7
1542.5
1602.9
1.5749
1.6159
1.6534
0.395
0.433
0.469
1328.1
1377.2
1425.2
1474.1
1537.2
1598.6
1.5598
1.6017
1.6398
1300
1400
1600
0.561
0.598
0.670
1475.5
1522.5
1617.2
1662.5
1721.8
1840.4
1.6883
1.7211
1.7817
0.503
0.537
0.602
1472.7
1520.2
1615.4
1659.0
1718.8
1838.2
1.6751
1.7082
1.7692
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in English Units
T
F
v
ft3/lb
(Continued)
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
h
Btu/lb
s
Btu/lb # R
p 3000 lbf/in.2
(Tsat 695.5F)
p 2500 lbf/in.2
(Tsat 668.3F)
Sat.
700
750
0.1306
0.1684
0.2030
1031.0
1098.7
1155.2
1091.4
1176.6
1249.1
1.2327
1.3073
1.3686
0.0840
0.0977
0.1483
968.8
1003.9
1114.7
1015.5
1058.1
1197.1
1.1575
1.1944
1.3122
800
900
1000
0.2291
0.2712
0.3069
1195.7
1259.9
1315.2
1301.7
1385.4
1457.2
1.4112
1.4752
1.5262
0.1757
0.2160
0.2485
1167.6
1241.8
1301.7
1265.2
1361.7
1439.6
1.3675
1.4414
1.4967
1100
1200
1300
0.3393
0.3696
0.3984
1366.8
1416.7
1465.7
1523.8
1587.7
1650.0
1.5704
1.6101
1.6465
0.2772
0.3086
0.3285
1356.2
1408.0
1458.5
1510.1
1576.6
1640.9
1.5434
1.5848
1.6224
1400
1500
1600
0.4261
0.4531
0.4795
1514.2
1562.5
1610.8
1711.3
1772.1
1832.6
1.6804
1.7123
1.7424
0.3524
0.3754
0.3978
1508.1
1557.3
1606.3
1703.7
1765.7
1827.1
1.6571
1.6896
1.7201
p 3500 lbf/in.2
Copyright © 2006. Wiley. All rights reserved.
u
Btu/lb
p 4000 lbf/in.2
650
700
750
0.0249
0.0306
0.1046
663.5
759.5
1058.4
679.7
779.3
1126.1
0.8630
0.9506
1.2440
0.0245
0.0287
0.0633
657.7
742.1
960.7
675.8
763.4
1007.5
0.8574
0.9345
1.1395
800
900
1000
0.1363
0.1763
0.2066
1134.7
1222.4
1287.6
1223.0
1336.5
1421.4
1.3226
1.4096
1.4699
0.1052
0.1462
0.1752
1095.0
1201.5
1272.9
1172.9
1309.7
1402.6
1.2740
1.3789
1.4449
1100
1200
1300
0.2328
0.2566
0.2787
1345.2
1399.2
1451.1
1496.0
1565.3
1631.7
1.5193
1.5624
1.6012
0.1995
0.2213
0.2414
1333.9
1390.1
1443.7
1481.6
1553.9
1622.4
1.4973
1.5423
1.5823
1400
1500
1600
0.2997
0.3199
0.3395
1501.9
1552.0
1601.7
1696.1
1759.2
1831.6
1.6368
1.6699
1.7010
0.2603
0.2784
0.2959
1495.7
1546.7
1597.1
1688.4
1752.8
1816.1
1.6188
1.6526
1.6841
p 4400 lbf/in.2
p 4800 lbf/in.2
650
700
750
0.0242
0.0278
0.0415
653.6
732.7
870.8
673.3
755.3
904.6
0.8535
0.9257
1.0513
0.0237
0.0271
0.0352
649.8
725.1
832.6
671.0
749.1
863.9
0.8499
0.9187
1.0154
800
900
1000
0.0844
0.1270
0.1552
1056.5
1183.7
1260.8
1125.3
1287.1
1387.2
1.2306
1.3548
1.4260
0.0668
0.1109
0.1385
1011.2
1164.8
1248.3
1070.5
1263.4
1317.4
1.1827
1.3310
1.4078
1100
1200
1300
0.1784
0.1989
0.2176
1324.7
1382.8
1437.7
1469.9
1544.7
1614.9
1.4809
1.5274
1.5685
0.1608
0.1802
0.1979
1315.3
1375.4
1431.7
1458.1
1535.4
1607.4
1.4653
1.5133
1.5555
1400
1500
1600
0.2352
0.2520
0.2681
1490.7
1542.7
1593.4
1682.3
1747.6
1811.7
1.6057
1.6399
1.6718
0.2143
0.2300
0.2450
1485.7
1538.2
1589.8
1676.1
1742.5
1807.4
1.5934
1.6282
1.6605
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
H2O
TABLE A-4E
777
778
Tables in English Units
TABLE A-5E
T
F
v
ft3/lb
Properties of Compressed Liquid Water
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
H2O
p 500 lbf/in.2
(Tsat 467.1F)
h
Btu/lb
s
Btu/lb # R
p 1000 lbf/in.2
(Tsat 544.7F)
32
50
100
0.015994
0.015998
0.016106
0.00
18.02
67.87
1.49
19.50
69.36
0.00000
0.03599
0.12932
0.015967
0.015972
0.016082
0.03
17.99
67.70
2.99
20.94
70.68
0.00005
0.03592
0.12901
150
200
300
0.016318
0.016608
0.017416
117.66
167.65
268.92
119.17
169.19
270.53
0.21457
0.29341
0.43641
0.016293
0.016580
0.017379
117.38
167.26
268.24
120.40
170.32
271.46
0.21410
0.29281
0.43552
400
Sat.
0.018608
0.019748
373.68
447.70
375.40
449.53
0.56604
0.64904
0.018550
0.021591
372.55
538.39
375.98
542.38
0.56472
0.74320
p 1500 lbf/in.2
(Tsat 596.4F)
p 2000 lbf/in.2
(Tsat 636.0F)
32
50
100
0.015939
0.015946
0.016058
0.05
17.95
67.53
4.47
22.38
71.99
0.00007
0.03584
0.12870
0.015912
0.015920
0.016034
0.06
17.91
67.37
5.95
23.81
73.30
0.00008
0.03575
0.12839
150
200
300
0.016268
0.016554
0.017343
117.10
166.87
267.58
121.62
171.46
272.39
0.21364
0.29221
0.43463
0.016244
0.016527
0.017308
116.83
166.49
266.93
122.84
172.60
273.33
0.21318
0.29162
0.43376
400
500
Sat.
0.018493
0.02024
0.02346
371.45
481.8
605.0
376.59
487.4
611.5
0.56343
0.6853
0.8082
0.018439
0.02014
0.02565
370.38
479.8
662.4
377.21
487.3
671.9
0.56216
0.6832
0.8623
p 3000 lbf/in.2
(Tsat 695.5F)
Copyright © 2006. Wiley. All rights reserved.
u
Btu/lb
p 4000 lbf/in.2
32
50
100
0.015859
0.015870
0.015987
0.09
17.84
67.04
8.90
26.65
75.91
0.00009
0.03555
0.12777
0.015807
0.015821
0.015942
0.10
17.76
66.72
11.80
29.47
78.52
0.00005
0.03534
0.12714
150
200
300
0.016196
0.016476
0.017240
116.30
165.74
265.66
125.29
174.89
275.23
0.21226
0.29046
0.43205
0.016150
0.016425
0.017174
115.77
165.02
264.43
127.73
177.18
277.15
0.21136
0.28931
0.43038
400
500
Sat.
0.018334
0.019944
0.034310
368.32
476.2
783.5
378.50
487.3
802.5
0.55970
0.6794
0.9732
0.018235
0.019766
366.35
472.9
379.85
487.5
0.55734
0.6758
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in English Units
Properties of Saturated Water (Solid–Vapor): Temperature Table
Specific Volume
ft3/lb
Internal Energy
Btu/lb
Enthalpy
Btu/lb
Entropy
Btu/lb # R
Press.
lbf/in.2
Sat.
Solid
vi
Sat.
Vapor
vg 103
Sat.
Solid
ui
Subl.
uig
Sat.
Vapor
ug
Sat.
Solid
hi
Subl.
hig
Sat.
Vapor
hg
Sat.
Solid
si
Subl.
sig
Sat.
Vapor
sg
32.018
32
30
.0887
.0886
.0808
.01747
.01747
.01747
3.302
3.305
3.607
143.34
143.35
144.35
1164.6
1164.6
1164.9
1021.2
1021.2
1020.5
143.34
143.35
144.35
1218.7
1218.7
1218.9
1075.4
1075.4
1074.5
.292
.292
.294
2.479
2.479
2.489
2.187
2.187
2.195
25
20
15
.0641
.0505
.0396
.01746
.01745
.01745
4.506
5.655
7.13
146.84
149.31
151.75
1165.7
1166.5
1167.3
1018.9
1017.2
1015.5
146.84
149.31
151.75
1219.1
1219.4
1219.7
1072.3
1070.1
1067.9
.299
.304
.309
2.515
2.542
2.569
2.216
2.238
2.260
10
5
0
.0309
.0240
.0185
.01744
.01743
.01743
9.04
11.52
14.77
154.17
156.56
158.93
1168.1
1168.8
1169.5
1013.9
1012.2
1010.6
154.17
156.56
158.93
1219.9
1220.1
1220.2
1065.7
1063.5
1061.2
.314
.320
.325
2.597
2.626
2.655
2.283
2.306
2.330
5
10
15
.0142
.0109
.0082
.01742
.01741
.01740
19.03
24.66
32.2
161.27
163.59
165.89
1170.2
1170.9
1171.5
1008.9
1007.3
1005.6
161.27
163.59
165.89
1220.3
1220.4
1220.5
1059.0
1056.8
1054.6
.330
.335
.340
2.684
2.714
2.745
2.354
2.379
2.405
20
25
30
.0062
.0046
.0035
.01740
.01739
.01738
42.2
55.7
74.1
168.16
170.40
172.63
1172.1
1172.7
1173.2
1003.9
1002.3
1000.6
168.16
170.40
172.63
1220.6
1220.6
1220.6
1052.4
1050.2
1048.0
.345
.351
.356
2.776
2.808
2.841
2.431
2.457
2.485
35
40
.0026
.0019
.01737
.01737
99.2
133.8
174.82
177.00
1173.8
1174.3
998.9
997.3
174.82
177.00
1220.6
1220.6
1045.8
1043.6
.361
.366
2.874
2.908
2.513
2.542
Copyright © 2006. Wiley. All rights reserved.
Temp.
F
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
H2O
TABLE A-6E
779
780
Tables in English Units
Copyright © 2006. Wiley. All rights reserved.
R-22
TABLE A-7E
Properties of Saturated Refrigerant 22 (Liquid–Vapor): Temperature Table
Specific Volume
ft3/lb
Internal Energy
Btu/lb
Enthalpy
Btu/lb
Entropy
Btu/lb # R
Temp.
F
Press.
lbf/in.2
Sat.
Liquid
vf
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Temp.
F
80
60
55
50
45
40
4.781
8.834
10.187
11.701
13.387
15.261
0.01090
0.01113
0.01120
0.01126
0.01132
0.01139
9.6984
5.4744
4.7933
4.2123
3.7147
3.2869
10.30
5.20
3.91
2.62
1.33
0.03
87.24
89.16
89.64
90.12
90.59
91.07
10.29
5.18
3.89
2.60
1.30
0.00
106.11
103.30
102.58
101.84
101.10
100.35
95.82
98.12
98.68
99.24
99.80
100.35
0.0257
0.0126
0.0094
0.0063
0.0031
0.0000
0.2538
0.2458
0.2441
0.2424
0.2407
0.2391
80
60
55
50
45
40
35
30
25
20
15
17.335
19.624
22.142
24.906
27.931
0.01145
0.01152
0.01159
0.01166
0.01173
2.9176
2.5976
2.3195
2.0768
1.8644
1.27
2.58
3.89
5.21
6.53
91.54
92.00
92.47
92.93
93.38
1.31
2.62
3.94
5.26
6.59
99.59
98.82
98.04
97.24
96.43
100.90
101.44
101.98
102.50
103.03
0.0031
0.0061
0.0092
0.0122
0.0152
0.2376
0.2361
0.2347
0.2334
0.2321
35
30
25
20
15
10
5
0
5
10
31.233
34.829
38.734
42.967
47.545
0.01181
0.01188
0.01196
0.01204
0.01212
1.6780
1.5138
1.3688
1.2404
1.1264
7.86
9.19
10.53
11.88
13.23
93.84
94.28
94.73
95.17
95.60
7.93
9.27
10.62
11.97
13.33
95.61
94.78
93.93
93.06
92.18
103.54
104.05
104.55
105.04
105.52
0.0182
0.0211
0.0240
0.0270
0.0298
0.2308
0.2296
0.2284
0.2272
0.2261
10
5
0
5
10
15
20
25
30
35
52.486
57.808
63.529
69.668
76.245
0.01220
0.01229
0.01237
0.01246
0.01255
1.0248
0.9342
0.8531
0.7804
0.7150
14.58
15.95
17.31
18.69
20.07
96.03
96.45
96.87
97.28
97.68
14.70
16.08
17.46
18.85
20.25
91.29
90.38
89.45
88.50
87.53
105.99
106.45
106.90
107.35
107.78
0.0327
0.0356
0.0384
0.0412
0.0441
0.2250
0.2240
0.2230
0.2220
0.2210
15
20
25
30
35
40
45
50
55
60
65
83.278
90.787
98.792
107.31
116.37
125.98
0.01265
0.01275
0.01285
0.01295
0.01306
0.01317
0.6561
0.6029
0.5548
0.5112
0.4716
0.4355
21.46
22.86
24.27
25.68
27.10
28.53
98.08
98.47
98.84
99.22
99.58
99.93
21.66
23.07
24.50
25.94
27.38
28.84
86.54
85.53
84.49
83.44
82.36
81.25
108.20
108.60
108.99
109.37
109.74
110.09
0.0468
0.0496
0.0524
0.0552
0.0579
0.0607
0.2200
0.2191
0.2182
0.2173
0.2164
0.2155
40
45
50
55
60
65
70
75
80
85
90
95
136.18
146.97
158.38
170.44
183.16
196.57
0.01328
0.01340
0.01352
0.01365
0.01378
0.01392
0.4027
0.3726
0.3452
0.3200
0.2969
0.2756
29.98
31.43
32.89
34.36
35.85
37.35
100.27
100.60
100.92
101.22
101.51
101.79
30.31
31.79
33.29
34.80
36.32
37.86
80.11
78.95
77.75
76.53
75.26
73.96
110.42
110.74
111.04
111.32
111.58
111.82
0.0634
0.0661
0.0689
0.0716
0.0743
0.0771
0.2147
0.2138
0.2130
0.2121
0.2113
0.2104
70
75
80
85
90
95
100
105
110
115
120
140
210.69
225.54
241.15
257.55
274.75
352.17
0.01407
0.01422
0.01438
0.01455
0.01472
0.01555
0.2560
0.2379
0.2212
0.2058
0.1914
0.1433
38.86
40.39
41.94
43.50
45.08
51.62
102.05
102.29
102.52
102.72
102.90
103.36
39.41
40.99
42.58
44.19
45.83
52.64
72.63
71.24
69.82
68.34
66.81
60.06
112.04
112.23
112.40
112.53
112.64
112.70
0.0798
0.0825
0.0852
0.0880
0.0907
0.1019
0.2095
0.2087
0.2078
0.2069
0.2060
0.2021
100
105
110
115
120
140
Source: Tables A-7E through A-9E are calculated based on equations from A. Kamei and S. W. Beyerlein, “A Fundamental Equation for
Chlorodifluoromethane (R-22),” Fluid Phase Equilibria, Vol. 80, No. 11, 1992, pp. 71–86.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in English Units
Copyright © 2006. Wiley. All rights reserved.
Properties of Saturated Refrigerant 22 (Liquid–Vapor): Pressure Table
Specific Volume
ft3/lb
Internal Energy
Btu/lb
Enthalpy
Btu/lb
Entropy
Btu/lb # R
Press.
lbf/in.2
Temp.
F
Sat.
Liquid
vf
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Press.
lbf/in.2
5
10
15
20
25
78.62
55.66
40.67
29.22
19.84
0.01091
0.01119
0.01138
0.01153
0.01166
9.3014
4.8769
3.3402
2.5518
2.0695
9.95
4.08
0.21
2.78
5.25
87.37
89.58
91.00
92.07
92.94
9.93
4.06
0.17
2.83
5.31
105.92
102.67
100.45
98.70
97.22
95.98
98.61
100.28
101.52
102.52
0.0248
0.0098
0.0004
0.0066
0.0123
0.2532
0.2443
0.2393
0.2359
0.2333
5
10
15
20
25
30
35
40
45
50
11.82
4.77
1.54
7.27
12.53
0.01178
0.01189
0.01198
0.01207
0.01216
1.7430
1.5068
1.3277
1.1870
1.0735
7.38
9.25
10.94
12.49
13.91
93.67
94.30
94.86
95.37
95.82
7.44
9.33
11.03
12.59
14.03
95.91
94.74
93.66
92.67
91.73
103.35
104.07
104.70
105.26
105.76
0.0171
0.0212
0.0249
0.0283
0.0313
0.2313
0.2295
0.2280
0.2267
0.2256
30
35
40
45
50
55
60
65
70
75
17.41
21.96
26.23
30.26
34.08
0.01224
0.01232
0.01239
0.01247
0.01254
0.9799
0.9014
0.8345
0.7768
0.7265
15.24
16.48
17.65
18.76
19.82
96.23
96.62
96.97
97.30
97.61
15.36
16.62
17.80
18.92
19.99
90.85
90.01
89.21
88.45
87.71
106.21
106.63
107.01
107.37
107.70
0.0341
0.0367
0.0391
0.0414
0.0435
0.2245
0.2236
0.2227
0.2219
0.2212
55
60
65
70
75
80
85
90
95
100
37.71
41.18
44.49
47.67
50.73
0.01260
0.01267
0.01274
0.01280
0.01286
0.6823
0.6431
0.6081
0.5766
0.5482
20.83
21.79
22.72
23.61
24.47
97.90
98.17
98.43
98.67
98.90
21.01
21.99
22.93
23.84
24.71
86.99
86.30
85.63
84.98
84.34
108.00
108.29
108.56
108.81
109.05
0.0456
0.0475
0.0494
0.0511
0.0528
0.2205
0.2198
0.2192
0.2186
0.2181
80
85
90
95
100
110
120
130
140
150
56.52
61.92
67.00
71.80
76.36
0.01298
0.01310
0.01321
0.01332
0.01343
0.4988
0.4573
0.4220
0.3915
0.3649
26.11
27.65
29.11
30.50
31.82
99.33
99.71
100.07
100.39
100.69
26.37
27.94
29.43
30.84
32.20
83.11
81.93
80.80
79.70
78.63
109.49
109.88
110.22
110.54
110.82
0.0560
0.0590
0.0618
0.0644
0.0669
0.2170
0.2161
0.2152
0.2144
0.2136
110
120
130
140
150
160
170
180
190
200
80.69
84.82
88.78
92.58
96.24
0.01354
0.01365
0.01375
0.01386
0.01396
0.3416
0.3208
0.3023
0.2857
0.2706
33.09
34.31
35.49
36.62
37.72
100.96
101.21
101.44
101.66
101.86
33.49
34.74
35.95
37.11
38.24
77.59
76.57
75.57
74.60
73.64
111.08
111.31
111.52
111.71
111.88
0.0693
0.0715
0.0737
0.0757
0.0777
0.2128
0.2121
0.2115
0.2108
0.2102
160
170
180
190
200
225
250
275
300
325
350
104.82
112.73
120.07
126.94
133.39
139.49
0.01422
0.01447
0.01473
0.01499
0.01525
0.01552
0.2386
0.2126
0.1912
0.1732
0.1577
0.1444
40.34
42.79
45.10
47.30
49.42
51.45
102.28
102.63
102.91
103.11
103.26
103.35
40.93
43.46
45.85
48.14
50.33
52.46
71.29
69.02
66.79
64.60
62.42
60.25
112.22
112.47
112.64
112.73
112.75
112.71
0.0824
0.0867
0.0908
0.0946
0.0982
0.1016
0.2087
0.2073
0.2060
0.2047
0.2034
0.2022
225
250
275
300
325
350
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
R-22
TABLE A-8E
781
782
Tables in English Units
TABLE A-9E
T
F
v
ft3/lb
Properties of Superheated Refrigerant 22 Vapor
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
R-22
h
Btu/lb
s
Btu/lb # R
p 10 lbf/in.2
(Tsat 55.66F)
p 5 lbf/in.2
(Tsat 78.62F)
Sat.
70
60
9.3014
9.5244
9.7823
87.37
88.31
89.43
95.98
97.13
98.48
0.2532
0.2562
0.2596
4.8769
89.58
98.61
0.2443
50
40
30
10.0391
10.2952
10.5506
90.55
91.69
92.84
99.84
101.22
102.61
0.2630
0.2663
0.2696
4.9522
5.0846
5.2163
90.23
91.39
92.57
99.40
100.81
102.23
0.2462
0.2496
0.2530
20
10
0
10.8054
11.0596
11.3133
94.01
95.19
96.39
104.01
105.43
106.87
0.2728
0.2760
0.2791
5.3472
5.4775
5.6073
93.75
94.95
96.16
103.65
105.09
106.55
0.2563
0.2595
0.2627
10
20
30
40
11.5666
11.8195
12.0720
12.3242
97.60
98.83
100.07
101.33
108.31
109.77
111.25
112.74
0.2822
0.2853
0.2884
0.2914
5.7366
5.8655
5.9941
6.1223
97.39
98.63
99.88
101.15
108.01
109.49
110.98
112.49
0.2658
0.2690
0.2720
0.2751
p 15 lbf/in.2
(Tsat 40.67F)
Copyright © 2006. Wiley. All rights reserved.
u
Btu/lb
p 20 lbf/in.2
(Tsat 29.22F)
Sat.
40
30
3.3402
3.3463
3.4370
91.00
91.08
92.28
100.28
100.38
101.83
0.2393
0.2396
0.2430
2.5518
92.07
101.52
0.2359
20
10
0
3.5268
3.6160
3.7046
93.49
94.70
95.93
103.28
104.75
106.22
0.2463
0.2496
0.2529
2.6158
2.6846
2.7528
93.21
94.45
95.69
102.90
104.39
105.89
0.2391
0.2424
0.2457
10
20
30
3.7927
3.8804
3.9677
97.17
98.43
99.69
107.71
109.20
110.71
0.2561
0.2592
0.2623
2.8204
2.8875
2.9542
96.95
98.22
99.49
107.39
108.91
110.43
0.2490
0.2522
0.2553
40
50
60
70
4.0546
4.1412
4.2275
4.3136
100.97
102.26
103.57
104.89
112.23
113.76
115.31
116.87
0.2654
0.2684
0.2714
0.2744
3.0205
3.0865
3.1522
3.2176
100.78
102.09
103.40
104.73
111.97
113.52
115.08
116.65
0.2584
0.2615
0.2645
0.2675
p 25 lbf/in.2
(Tsat 19.84F)
p 30 lbf/in.2
(Tsat 11.82F)
Sat.
10
0
2.0695
2.1252
2.1812
92.94
94.18
95.45
102.52
104.02
105.54
0.2333
0.2367
0.2400
1.7430
1.7518
1.7997
93.67
93.91
95.19
103.35
103.64
105.19
0.2313
0.2319
0.2353
10
20
30
2.2365
2.2914
2.3458
96.72
98.00
99.29
107.07
108.61
110.15
0.2433
0.2466
0.2498
1.8470
1.8937
1.9400
96.48
97.78
99.09
106.74
108.30
109.86
0.2386
0.2419
0.2451
40
50
60
2.3998
2.4535
2.5068
100.59
101.91
103.23
111.70
113.27
114.84
0.2529
0.2560
0.2590
1.9858
2.0313
2.0764
100.40
101.73
103.06
111.43
113.01
114.60
0.2483
0.2514
0.2545
70
80
90
100
2.5599
2.6127
2.6654
2.7178
104.57
105.92
107.28
108.65
116.42
118.01
119.62
121.24
0.2621
0.2650
0.2680
0.2709
2.1213
2.1659
2.2103
2.2545
104.41
105.77
107.13
108.52
116.19
117.80
119.41
121.04
0.2576
0.2606
0.2635
0.2665
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in English Units
T
F
v
ft3/lb
(Continued )
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
h
Btu/lb
s
Btu/lb # R
p 50 lbf/in.2
(Tsat 12.53F)
p 40 lbf/in.2
(Tsat 1.54F)
Sat.
10
20
1.3277
1.3593
1.3960
94.86
95.99
97.33
104.70
106.06
107.67
0.2280
0.2310
0.2343
1.0735
95.82
105.76
0.2256
1.0965
96.85
107.00
0.2282
30
40
50
1.4321
1.4678
1.5032
98.66
100.01
101.35
109.27
110.88
112.49
0.2376
0.2409
0.2441
1.1268
1.1565
1.1858
98.22
99.59
100.97
108.65
110.30
111.95
0.2316
0.2349
0.2382
60
70
80
1.5381
1.5728
1.6071
102.71
104.08
105.45
114.10
115.73
117.36
0.2472
0.2503
0.2534
1.2147
1.2433
1.2716
102.35
103.74
105.13
113.60
115.25
116.90
0.2414
0.2445
0.2476
90
100
110
120
1.6413
1.6752
1.7089
1.7424
106.84
108.23
109.64
111.06
118.99
120.64
122.30
123.97
0.2564
0.2593
0.2623
0.2652
1.2996
1.3274
1.3549
1.3823
106.53
107.95
109.37
110.80
118.57
120.24
121.91
123.60
0.2507
0.2537
0.2567
0.2596
p 60 lbf/in.2
(Tsat 21.96F)
Copyright © 2006. Wiley. All rights reserved.
u
Btu/lb
p 70 lbf/in.2
(Tsat 30.26F)
Sat.
30
40
0.9014
0.9226
0.9485
96.62
97.75
99.16
106.63
108.00
109.70
0.2236
0.2264
0.2298
0.7768
97.30
107.37
0.2219
0.7994
98.71
109.07
0.2254
50
60
70
0.9739
0.9988
1.0234
100.57
101.98
103.39
111.39
113.07
114.76
0.2332
0.2365
0.2397
0.8221
0.8443
0.8660
100.15
101.59
103.03
110.81
112.53
114.25
0.2288
0.2321
0.2354
80
90
100
1.0476
1.0716
1.0953
104.80
106.22
107.65
116.44
118.13
119.82
0.2428
0.2459
0.2490
0.8874
0.9086
0.9294
104.46
105.90
107.35
115.97
117.68
119.40
0.2386
0.2418
0.2449
110
120
130
140
1.1188
1.1421
1.1653
1.1883
109.09
110.53
111.99
113.45
121.52
123.22
124.93
126.65
0.2520
0.2549
0.2579
0.2608
0.9500
0.9704
0.9907
1.0107
108.80
110.26
111.73
113.21
121.12
122.84
124.57
126.31
0.2479
0.2509
0.2539
0.2568
p 80 lbf/in.2
(Tsat 37.71F)
p 90 lbf/in.2
(Tsat 44.49F)
Sat.
40
50
0.6823
0.6871
0.7079
97.90
98.24
99.72
108.00
108.42
110.20
0.2205
0.2213
0.2248
0.6081
98.43
108.56
0.2192
0.6186
99.26
109.57
0.2212
60
70
80
0.7280
0.7478
0.7671
101.19
102.65
104.11
111.97
113.73
115.48
0.2283
0.2316
0.2349
0.6373
0.6555
0.6733
100.77
102.27
103.76
111.39
113.19
114.98
0.2247
0.2282
0.2315
90
100
110
0.7861
0.8048
0.8233
105.58
107.04
108.51
117.22
118.97
120.71
0.2381
0.2412
0.2443
0.6907
0.7078
0.7246
105.24
106.73
108.22
116.75
118.52
120.29
0.2348
0.2380
0.2411
120
130
140
150
0.8416
0.8596
0.8775
0.8953
109.99
111.47
112.96
114.46
122.45
124.20
125.96
127.72
0.2474
0.2504
0.2533
0.2562
0.7412
0.7576
0.7739
0.7899
109.71
111.20
112.71
114.22
122.06
123.83
125.60
127.38
0.2442
0.2472
0.2502
0.2531
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
R-22
TABLE A-9E
783
784
Tables in English Units
TABLE A-9E
T
F
v
ft3/lb
(Continued )
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
R-22
0.5482
0.5645
0.5980
0.6300
0.6609
0.6908
0.7201
0.7489
0.7771
0.8051
0.8327
0.8600
0.8871
0.9140
98.90
100.33
103.38
106.40
109.42
112.45
115.50
118.58
121.69
124.84
128.04
131.27
134.54
137.85
109.05
110.79
114.46
118.07
121.66
125.24
128.83
132.45
136.08
139.75
143.45
147.19
150.97
154.78
0.2181
0.2214
0.2284
0.2349
0.2412
0.2473
0.2532
0.2589
0.2645
0.2700
0.2754
0.2806
0.2858
0.2909
Copyright © 2006. Wiley. All rights reserved.
0.3915
0.4028
0.4289
0.4534
0.4768
0.4993
0.5212
0.5426
0.5636
0.5842
0.6045
0.6246
0.6445
0.6642
100.39
101.76
105.02
108.21
111.37
114.53
117.70
120.89
124.10
127.35
130.62
133.94
137.29
140.68
110.54
112.20
116.14
119.96
123.73
127.48
131.21
134.96
138.71
142.49
146.30
150.13
154.00
157.89
99.71
109.88
0.2161
0.4846
0.5130
0.5400
0.5661
0.5914
0.6161
0.6404
0.6642
0.6878
0.7110
0.7340
0.7568
102.60
105.73
108.83
111.92
115.02
118.15
121.30
124.48
127.69
130.95
134.24
137.57
113.37
117.13
120.83
124.50
128.16
131.84
135.53
139.24
142.98
146.75
150.55
154.39
0.2227
0.2295
0.2360
0.2422
0.2482
0.2541
0.2597
0.2653
0.2707
0.2760
0.2812
0.2863
Created from purdue on 2022-01-24 17:56:53.
p 160 lbf/in.2
(Tsat 80.69F)
0.2144
0.2175
0.2246
0.2313
0.2377
0.2439
0.2498
0.2556
0.2612
0.2666
0.2720
0.2773
0.2824
0.2875
0.3416
100.96
111.08
0.2128
0.3653
0.3881
0.4095
0.4301
0.4499
0.4692
0.4880
0.5065
0.5246
0.5425
0.5602
0.5777
104.26
107.56
110.81
114.03
117.25
120.47
123.72
126.99
130.30
133.63
137.00
140.41
115.08
119.06
122.94
126.77
130.57
134.37
138.18
142.00
145.84
149.70
153.60
157.62
0.2201
0.2271
0.2337
0.2400
0.2460
0.2518
0.2575
0.2631
0.2685
0.2738
0.2790
0.2841
p 180 lbf/in.2
(Tsat 88.78F)
Sat.
0.3023 101.44 111.52
100
0.3154 103.44 113.95
120
0.3369 106.88 118.11
140
0.3570 110.21 122.11
160
0.3761 113.50 126.04
180
0.3943 116.78 129.92
200
0.4120 120.05 133.78
220
0.4292 123.33 137.64
240
0.4459 126.64 141.50
260
0.4624 129.96 145.38
280
0.4786 133.32 149.28
300
0.4946 136.71 153.20
320
0.5104 140.13 157.15
340
0.5260 143.59 161.12
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
s
Btu/lb # R
0.4573
p 140 lbf/in.2
(Tsat 71.80F)
Sat.
80
100
120
140
160
180
200
220
240
260
280
300
320
h
Btu/lb
p 120 lbf/in.2
(Tsat 61.92F)
p 100 lbf/in.2
(Tsat 50.73F)
Sat.
60
80
100
120
140
160
180
200
220
240
260
280
300
u
Btu/lb
p 200 lbf/in.2
(Tsat 96.24F)
0.2115
0.2159
0.2231
0.2299
0.2364
0.2425
0.2485
0.2542
0.2598
0.2653
0.2706
0.2759
0.2810
0.2860
0.2706
0.2748
0.2957
0.3148
0.3327
0.3497
0.3661
0.3820
0.3975
0.4126
0.4275
0.4422
0.4566
0.4709
101.86
102.56
106.15
109.59
112.96
116.29
119.61
122.94
126.27
129.63
133.01
136.42
139.86
143.33
111.88
112.73
117.10
121.25
125.28
129.25
133.17
137.08
140.99
144.91
148.84
152.79
156.77
160.77
0.2102
0.2117
0.2194
0.2264
0.2330
0.2393
0.2454
0.2512
0.2569
0.2624
0.2678
0.2731
0.2782
0.2833
Tables in English Units
T
F
v
ft3/lb
(Continued)
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
h
Btu/lb
s
Btu/lb # R
p 250 lbf/in.2
(Tsat 112.73F)
p 225 lbf/in.2
(Tsat 104.82F)
Sat.
120
140
0.2386
0.2539
0.2722
102.28
105.17
108.78
112.22
115.75
120.12
0.2087
0.2149
0.2223
0.2126
0.2198
0.2378
102.63
104.10
107.90
112.47
114.27
118.91
0.2073
0.2104
0.2183
160
180
200
0.2891
0.3050
0.3202
112.26
115.67
119.06
124.30
128.38
132.40
0.2291
0.2356
0.2418
0.2540
0.2690
0.2833
111.51
115.02
118.48
123.27
127.48
131.59
0.2255
0.2321
0.2385
220
240
260
0.3348
0.3490
0.3628
122.43
125.81
129.20
136.38
140.35
144.32
0.2477
0.2535
0.2591
0.2969
0.3101
0.3229
121.91
125.33
128.76
135.66
139.69
143.71
0.2445
0.2504
0.2560
280
300
320
0.3764
0.3896
0.4027
132.61
136.05
139.51
148.29
152.28
156.29
0.2645
0.2699
0.2751
0.3354
0.3476
0.3596
132.21
135.67
139.16
147.73
151.76
155.81
0.2616
0.2669
0.2722
340
360
0.4156
0.4284
143.00
146.33
160.32
164.38
0.2802
0.2852
0.3715
0.3831
142.67
146.22
159.87
163.95
0.2773
0.2824
p 275 lbf/in.2
(Tsat 120.07F)
Copyright © 2006. Wiley. All rights reserved.
u
Btu/lb
p 300 lbf/in.2
(Tsat 126.94F)
Sat.
140
160
0.1912
0.2092
0.2250
102.91
106.96
110.73
112.64
117.61
122.19
0.2060
0.2144
0.2219
0.1732
0.1849
0.2006
103.11
105.93
109.89
112.73
116.20
121.04
0.2047
0.2105
0.2185
180
200
220
0.2395
0.2530
0.2659
144.35
117.88
121.38
126.54
130.77
134.91
0.2288
0.2353
0.2415
0.2146
0.2276
0.2399
133.64
117.26
120.83
125.56
129.91
134.15
0.2257
0.2324
0.2387
240
260
280
0.2782
0.2902
0.3018
124.85
128.32
131.80
139.02
143.10
147.17
0.2475
0.2532
0.2588
0.2516
0.2629
0.2739
124.35
127.87
131.38
138.33
142.47
146.59
0.2447
0.2506
0.2562
300
320
340
360
0.3132
0.3243
0.3353
0.3461
135.29
138.80
142.34
145.90
151.24
155.32
159.41
163.53
0.2642
0.2695
0.2747
0.2798
0.2845
0.2949
0.3051
0.3152
134.90
138.44
142.00
145.58
150.71
154.83
158.95
163.09
0.2617
0.2671
0.2723
0.2774
p 325 lbf/in.2
(Tsat 133.39F)
p 350 lbf/in.2
(Tsat 139.49F)
Sat.
140
160
0.1577
0.1637
0.1796
103.26
104.78
109.00
112.75
114.63
119.81
0.2034
0.2066
0.2151
0.1444
0.1448
0.1605
103.35
103.48
107.90
112.71
112.86
118.30
0.2022
0.2024
0.2113
180
200
220
0.1934
0.2061
0.2179
112.89
116.62
120.26
124.53
129.02
133.37
0.2226
0.2295
0.2360
0.1747
0.1874
0.1987
112.06
115.95
119.65
123.38
128.10
132.53
0.2194
0.2267
0.2333
240
260
280
0.2291
0.2398
0.2501
123.84
127.40
130.96
137.63
141.83
146.01
0.2422
0.2481
0.2538
0.2095
0.2199
0.2297
123.31
126.93
130.52
136.89
141.18
145.41
0.2396
0.2457
0.2514
300
320
340
0.2602
0.2700
0.2796
134.51
138.08
141.66
150.17
154.33
158.49
0.2593
0.2647
0.2700
0.2393
0.2486
0.2577
134.12
137.71
141.32
149.62
153.82
158.02
0.2571
0.2626
0.2679
0.2666
0.2754
144.95
148.59
162.23
166.43
0.2730
0.2781
360
0.2891 145.26 162.66
0.2752
380
0.2983
148.89
166.85
0.2802
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
R-22
TABLE A-9E
785
786
Tables in English Units
Copyright © 2006. Wiley. All rights reserved.
R-134a
TABLE A-10E
Properties of Saturated Refrigerant 134a (Liquid–Vapor): Temperature Table
Specific Volume
ft3/lb
Internal Energy
Btu/lb
Enthalpy
Btu/lb
Entropy
Btu/lb # R
Temp.
F
Press.
lbf/in.2
Sat.
Liquid
vf
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Temp.
F
40
30
20
15
10
7.490
9.920
12.949
14.718
16.674
0.01130
0.01143
0.01156
0.01163
0.01170
5.7173
4.3911
3.4173
3.0286
2.6918
0.02
2.81
5.69
7.14
8.61
87.90
89.26
90.62
91.30
91.98
0.00
2.83
5.71
7.17
8.65
95.82
94.49
93.10
92.38
91.64
95.82
97.32
98.81
99.55
100.29
0.0000
0.0067
0.0133
0.0166
0.0199
0.2283
0.2266
0.2250
0.2243
0.2236
40
30
20
15
10
5
0
5
10
15
18.831
21.203
23.805
26.651
29.756
0.01178
0.01185
0.01193
0.01200
0.01208
2.3992
2.1440
1.9208
1.7251
1.5529
10.09
11.58
13.09
14.60
16.13
92.66
93.33
94.01
94.68
95.35
10.13
11.63
13.14
14.66
16.20
90.89
90.12
89.33
88.53
87.71
101.02
101.75
102.47
103.19
103.90
0.0231
0.0264
0.0296
0.0329
0.0361
0.2230
0.2224
0.2219
0.2214
0.2209
5
0
5
10
15
20
25
30
40
50
33.137
36.809
40.788
49.738
60.125
0.01216
0.01225
0.01233
0.01251
0.01270
1.4009
1.2666
1.1474
0.9470
0.7871
17.67
19.22
20.78
23.94
27.14
96.02
96.69
97.35
98.67
99.98
17.74
19.30
20.87
24.05
27.28
86.87
86.02
85.14
83.34
81.46
104.61
105.32
106.01
107.39
108.74
0.0393
0.0426
0.0458
0.0522
0.0585
0.2205
0.2200
0.2196
0.2189
0.2183
20
25
30
40
50
60
70
80
85
90
72.092
85.788
101.37
109.92
118.99
0.01290
0.01311
0.01334
0.01346
0.01358
0.6584
0.5538
0.4682
0.4312
0.3975
30.39
33.68
37.02
38.72
40.42
101.27
102.54
103.78
104.39
105.00
30.56
33.89
37.27
38.99
40.72
79.49
77.44
75.29
74.17
73.03
110.05
111.33
112.56
113.16
113.75
0.0648
0.0711
0.0774
0.0805
0.0836
0.2178
0.2173
0.2169
0.2167
0.2165
60
70
80
85
90
95
100
105
110
115
128.62
138.83
149.63
161.04
173.10
0.01371
0.01385
0.01399
0.01414
0.01429
0.3668
0.3388
0.3131
0.2896
0.2680
42.14
43.87
45.62
47.39
49.17
105.60
106.18
106.76
107.33
107.88
42.47
44.23
46.01
47.81
49.63
71.86
70.66
69.42
68.15
66.84
114.33
114.89
115.43
115.96
116.47
0.0867
0.0898
0.0930
0.0961
0.0992
0.2163
0.2161
0.2159
0.2157
0.2155
95
100
105
110
115
120
140
160
180
200
210
185.82
243.86
314.63
400.22
503.52
563.51
0.01445
0.01520
0.01617
0.01758
0.02014
0.02329
0.2481
0.1827
0.1341
0.0964
0.0647
0.0476
50.97
58.39
66.26
74.83
84.90
91.84
108.42
110.41
111.97
112.77
111.66
108.48
51.47
59.08
67.20
76.13
86.77
94.27
65.48
59.57
52.58
43.78
30.92
19.18
116.95
118.65
119.78
119.91
117.69
113.45
0.1023
0.1150
0.1280
0.1417
0.1575
0.1684
0.2153
0.2143
0.2128
0.2101
0.2044
0.1971
120
140
160
180
200
210
Source: Tables A-10E through A-12E are calculated based on equations from D. P. Wilson and R. S. Basu, “Thermodynamic Properties of a New
Stratospherically Safe Working Fluid—Refrigerant 134a,” ASHRAE Trans., Vol. 94, Pt. 2, 1988, pp. 2095–2118.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in English Units
Properties of Saturated Refrigerant 134a (Liquid–Vapor): Pressure Table
Specific Volume
ft3/lb
Internal Energy
Btu/lb
Enthalpy
Btu/lb
Entropy
Btu/lb # R
Temp.
F
Sat.
Liquid
vf
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Press.
lbf/in.2
5
10
15
20
30
53.48
29.71
14.25
2.48
15.38
0.01113
0.01143
0.01164
0.01181
0.01209
8.3508
4.3581
2.9747
2.2661
1.5408
3.74
2.89
7.36
10.84
16.24
86.07
89.30
91.40
93.00
95.40
3.73
2.91
7.40
10.89
16.31
97.53
94.45
92.27
90.50
87.65
93.79
97.37
99.66
101.39
103.96
0.0090
0.0068
0.0171
0.0248
0.0364
0.2311
0.2265
0.2242
0.2227
0.2209
5
10
15
20
30
40
50
60
70
80
29.04
40.27
49.89
58.35
65.93
0.01232
0.01252
0.01270
0.01286
0.01302
1.1692
0.9422
0.7887
0.6778
0.5938
20.48
24.02
27.10
29.85
32.33
97.23
98.71
99.96
101.05
102.02
20.57
24.14
27.24
30.01
32.53
85.31
83.29
81.48
79.82
78.28
105.88
107.43
108.72
109.83
110.81
0.0452
0.0523
0.0584
0.0638
0.0686
0.2197
0.2189
0.2183
0.2179
0.2175
40
50
60
70
80
90
100
120
140
160
72.83
79.17
90.54
100.56
109.56
0.01317
0.01332
0.01360
0.01386
0.01412
0.5278
0.4747
0.3941
0.3358
0.2916
34.62
36.75
40.61
44.07
47.23
102.89
103.68
105.06
106.25
107.28
34.84
36.99
40.91
44.43
47.65
76.84
75.47
72.91
70.52
68.26
111.68
112.46
113.82
114.95
115.91
0.0729
0.0768
0.0839
0.0902
0.0958
0.2172
0.2169
0.2165
0.2161
0.2157
90
100
120
140
160
180
200
220
240
260
117.74
125.28
132.27
138.79
144.92
0.01438
0.01463
0.01489
0.01515
0.01541
0.2569
0.2288
0.2056
0.1861
0.1695
50.16
52.90
55.48
57.93
60.28
108.18
108.98
109.68
110.30
110.84
50.64
53.44
56.09
58.61
61.02
66.10
64.01
61.96
59.96
57.97
116.74
117.44
118.05
118.56
118.99
0.1009
0.1057
0.1101
0.1142
0.1181
0.2154
0.2151
0.2147
0.2144
0.2140
180
200
220
240
260
280
300
350
400
450
500
150.70
156.17
168.72
179.95
190.12
199.38
0.01568
0.01596
0.01671
0.01758
0.01863
0.02002
0.1550
0.1424
0.1166
0.0965
0.0800
0.0657
62.53
64.71
69.88
74.81
79.63
84.54
111.31
111.72
112.45
112.77
112.60
111.76
63.34
65.59
70.97
76.11
81.18
86.39
56.00
54.03
49.03
43.80
38.08
31.44
119.35
119.62
120.00
119.91
119.26
117.83
0.1219
0.1254
0.1338
0.1417
0.1493
0.1570
0.2136
0.2132
0.2118
0.2102
0.2079
0.2047
280
300
350
400
450
500
Copyright © 2006. Wiley. All rights reserved.
Press.
lbf/in.2
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
R-134a
TABLE A-11E
787
788
Tables in English Units
TABLE A-12E
T
F
v
ft3/lb
Properties of Superheated Refrigerant 134a Vapor
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
R-134a
h
Btu/lb
s
Btu/lb # R
p 15 lbf/in.2
(Tsat 14.25F)
p 10 lbf/in.2
(Tsat 29.71F)
Copyright © 2006. Wiley. All rights reserved.
u
Btu/lb
Sat.
20
0
4.3581
4.4718
4.7026
89.30
90.89
94.24
97.37
99.17
102.94
0.2265
0.2307
0.2391
2.9747
91.40
99.66
0.2242
3.0893
93.84
102.42
0.2303
20
40
60
4.9297
5.1539
5.3758
97.67
101.19
104.80
106.79
110.72
114.74
0.2472
0.2553
0.2632
3.2468
3.4012
3.5533
97.33
100.89
104.54
106.34
110.33
114.40
0.2386
0.2468
0.2548
80
100
120
5.5959
5.8145
6.0318
108.50
112.29
116.18
118.85
123.05
127.34
0.2709
0.2786
0.2861
3.7034
3.8520
3.9993
108.28
112.10
116.01
118.56
122.79
127.11
0.2626
0.2703
0.2779
140
160
180
200
6.2482
6.4638
6.6786
6.8929
120.16
124.23
128.38
132.63
131.72
136.19
140.74
145.39
0.2935
0.3009
0.3081
0.3152
4.1456
4.2911
4.4359
4.5801
120.00
124.09
128.26
132.52
131.51
136.00
140.57
145.23
0.2854
0.2927
0.3000
0.3072
p 20 lbf/in.2
(Tsat 2.48F)
p 30 lbf/in.2
(Tsat 15.38F)
Sat.
0
20
2.2661
2.2816
2.4046
93.00
93.43
96.98
101.39
101.88
105.88
0.2227
0.2238
0.2323
1.5408
95.40
103.96
0.2209
1.5611
96.26
104.92
0.2229
40
60
80
2.5244
2.6416
2.7569
100.59
104.28
108.05
109.94
114.06
118.25
0.2406
0.2487
0.2566
1.6465
1.7293
1.8098
99.98
103.75
107.59
109.12
113.35
117.63
0.2315
0.2398
0.2478
100
120
140
2.8705
2.9829
3.0942
111.90
115.83
119.85
122.52
126.87
131.30
0.2644
0.2720
0.2795
1.8887
1.9662
2.0426
111.49
115.47
119.53
121.98
126.39
130.87
0.2558
0.2635
0.2711
160
180
200
220
3.2047
3.3144
3.4236
3.5323
123.95
128.13
132.40
136.76
135.81
140.40
145.07
149.83
0.2869
0.2922
0.3014
0.3085
2.1181
2.1929
2.2671
2.3407
123.66
127.88
132.17
136.55
135.42
140.05
144.76
149.54
0.2786
0.2859
0.2932
0.3003
p 40 lbf/in.2
(Tsat 29.04F)
p 50 lbf/in.2
(Tsat 40.27F)
Sat.
40
60
1.1692
1.2065
1.2723
97.23
99.33
103.20
105.88
108.26
112.62
0.2197
0.2245
0.2331
0.9422
98.71
107.43
0.2189
0.9974
102.62
111.85
0.2276
80
100
120
1.3357
1.3973
1.4575
107.11
111.08
115.11
117.00
121.42
125.90
0.2414
0.2494
0.2573
1.0508
1.1022
1.1520
106.62
110.65
114.74
116.34
120.85
125.39
0.2361
0.2443
0.2523
140
160
180
1.5165
1.5746
1.6319
119.21
123.38
127.62
130.43
135.03
139.70
0.2650
0.2725
0.2799
1.2007
1.2484
1.2953
118.88
123.08
127.36
129.99
134.64
139.34
0.2601
0.2677
0.2752
200
220
240
1.6887
1.7449
1.8006
131.94
136.34
140.81
144.44
149.25
154.14
0.2872
0.2944
0.3015
1.3415
1.3873
1.4326
131.71
136.12
140.61
144.12
148.96
153.87
0.2825
0.2897
0.2969
260 1.8561 145.36 159.10
280 1.9112 149.98 164.13
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
0.3085
0.3154
1.4775
1.5221
145.18
149.82
158.85
163.90
0.3039
0.3108
Created from purdue on 2022-01-24 17:56:53.
Tables in English Units
T
F
v
ft3/lb
(Continued)
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
0.7887
0.8135
0.8604
0.9051
0.9482
0.9900
1.0308
1.0707
1.1100
1.1488
1.1871
1.2251
1.2627
1.3001
99.96
102.03
106.11
110.21
114.35
118.54
122.79
127.10
131.47
135.91
140.42
145.00
149.65
154.38
108.72
111.06
115.66
120.26
124.88
129.53
134.23
138.98
143.79
148.66
153.60
158.60
163.67
168.81
0.2183
0.2229
0.2316
0.2399
0.2480
0.2559
0.2636
0.2712
0.2786
0.2859
0.2930
0.3001
0.3070
0.3139
0.6778
0.6814
0.7239
0.7640
0.8023
0.8393
0.8752
0.9103
0.9446
0.9784
1.0118
1.0448
1.0774
1.1098
p 80 lbf/in.2
(Tsat 65.93F)
Copyright © 2006. Wiley. All rights reserved.
Sat.
80
100
120
140
160
180
200
220
240
260
280
300
320
0.5938
0.6211
0.6579
0.6927
0.7261
0.7584
0.7898
0.8205
0.8506
0.8803
0.9095
0.9384
0.9671
0.9955
102.02
105.03
109.30
113.56
117.85
122.18
126.55
130.98
135.47
140.02
144.63
149.32
154.06
158.88
110.81
114.23
119.04
123.82
128.60
133.41
138.25
143.13
148.06
153.05
158.10
163.21
168.38
173.62
s
Btu/lb # R
101.05
101.40
105.58
109.76
113.96
118.20
122.49
126.83
131.23
135.69
140.22
144.82
149.48
154.22
109.83
110.23
114.96
119.66
124.36
129.07
133.82
138.62
143.46
148.36
153.33
158.35
163.44
168.60
0.2179
0.2186
0.2276
0.2361
0.2444
0.2524
0.2601
0.2678
0.2752
0.2825
0.2897
0.2968
0.3038
0.3107
p 90 lbf/in.2
(Tsat 72.83F)
0.2175
0.2239
0.2327
0.2411
0.2492
0.2570
0.2647
0.2722
0.2796
0.2868
0.2940
0.3010
0.3079
0.3147
0.5278
0.5408
0.5751
0.6073
0.6380
0.6675
0.6961
0.7239
0.7512
0.7779
0.8043
0.8303
0.8561
0.8816
p 100 lbf/in.2
(Tsat 79.17F)
Sat. 0.4747 103.68 112.46
0.2169
80 0.4761 103.87 112.68
0.2173
100 0.5086 108.32 117.73
0.2265
120 0.5388 112.73 122.70
0.2352
140 0.5674 117.13 127.63
0.2436
160 0.5947 121.55 132.55
0.2517
180 0.6210 125.99 137.49
0.2595
200 0.6466 130.48 142.45
0.2671
220 0.6716 135.02 147.45
0.2746
240 0.6960 139.61 152.49
0.2819
260 0.7201 144.26 157.59
0.2891
280 0.7438 148.98 162.74
0.2962
300 0.7672 153.75 167.95
0.3031
320
0.7904
158.59
173.21
0.3099
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
h
Btu/lb
p 70 lbf/in.2
(Tsat 58.35F)
p 60 lbf/in.2
(Tsat 49.89F)
Sat.
60
80
100
120
140
160
180
200
220
240
260
280
300
u
Btu/lb
102.89
104.46
108.82
113.15
117.50
121.87
126.28
130.73
135.25
139.82
144.45
149.15
153.91
158.73
111.68
113.47
118.39
123.27
128.12
132.98
137.87
142.79
147.76
152.77
157.84
162.97
168.16
173.42
0.2172
0.2205
0.2295
0.2380
0.2463
0.2542
0.2620
0.2696
0.2770
0.2843
0.2914
0.2984
0.3054
0.3122
p 120 lbf/in.2
(Tsat 90.54F)
0.3941
105.06
113.82
0.2165
0.4080
0.4355
0.4610
0.4852
0.5082
0.5305
0.5520
0.5731
0.5937
0.6140
0.6339
0.6537
107.26
111.84
116.37
120.89
125.42
129.97
134.56
139.20
143.89
148.63
153.43
158.29
116.32
121.52
126.61
131.66
136.70
141.75
146.82
151.92
157.07
162.26
167.51
172.81
0.2210
0.2301
0.2387
0.2470
0.2550
0.2628
0.2704
0.2778
0.2850
0.2921
0.2991
0.3060
R-134a
TABLE A-12E
789
790
Tables in English Units
TABLE A-12E
T
F
v
ft3/lb
(Continued )
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
R-134a
106.25
110.90
115.58
120.21
124.82
129.44
134.09
138.77
143.50
148.28
153.11
157.99
162.93
167.93
114.95
120.25
125.54
130.74
135.89
141.03
146.18
151.34
156.54
161.78
167.06
172.39
177.78
183.21
0.2569
0.2595
0.2814
0.3011
0.3191
0.3361
0.3523
0.3678
0.3828
0.3974
0.4116
0.4256
0.4393
0.4529
108.18
108.77
113.83
118.74
123.56
128.34
133.11
137.90
142.71
147.55
152.44
157.38
162.36
167.40
116.74
117.41
123.21
128.77
134.19
139.53
144.84
150.15
155.46
160.79
166.15
171.55
177.00
182.49
0.2916
0.3044
0.3269
0.3474
0.3666
0.3849
0.4023
0.4192
0.4356
0.4516
0.4672
0.4826
0.4978
0.5128
s
Btu/lb # R
107.28
109.88
114.73
119.49
124.20
128.90
133.61
138.34
143.11
147.92
152.78
157.69
162.65
167.67
115.91
118.89
124.41
129.78
135.06
140.29
145.52
150.75
156.00
161.29
166.61
171.98
177.39
182.85
0.2157
0.2209
0.2303
0.2391
0.2475
0.2555
0.2633
0.2709
0.2783
0.2856
0.2927
0.2996
0.3065
0.3132
p 200 lbf/in.2
(Tsat 125.28F)
0.2154
0.2166
0.2264
0.2355
0.2441
0.2524
0.2603
0.2680
0.2755
0.2828
0.2899
0.2969
0.3038
0.3106
0.2288
108.98
117.44
0.2151
0.2446
0.2636
0.2809
0.2970
0.3121
0.3266
0.3405
0.3540
0.3671
0.3799
0.3926
0.4050
112.87
117.94
122.88
127.76
132.60
137.44
142.30
147.18
152.10
157.07
162.07
167.13
121.92
127.70
133.28
138.75
144.15
149.53
154.90
160.28
165.69
171.13
176.60
182.12
0.2226
0.2321
0.2410
0.2494
0.2575
0.2653
0.2728
0.2802
0.2874
0.2945
0.3014
0.3082
p 300 lbf/in.2
(Tsat 156.17F)
Sat. 0.1424 111.72 119.62
160 0.1462 112.95 121.07
180 0.1633 118.93 128.00
200 0.1777 124.47 134.34
220 0.1905 129.79 140.36
240 0.2021 134.99 146.21
260 0.2130 140.12 151.95
280 0.2234 145.23 157.63
300 0.2333 150.33 163.28
320 0.2428 155.44 168.92
340 0.2521 160.57 174.56
360 0.2611 165.74 180.23
380 0.2699 170.94 185.92
400
0.2786 176.18 191.64
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
0.2161
0.2254
0.2344
0.2429
0.2511
0.2590
0.2667
0.2742
0.2815
0.2887
0.2957
0.3026
0.3094
0.3162
p 180 lbf/in.2
(Tsat 117.74F)
Sat.
120
140
160
180
200
220
240
260
280
300
320
340
360
Copyright © 2006. Wiley. All rights reserved.
0.3358
0.3610
0.3846
0.4066
0.4274
0.4474
0.4666
0.4852
0.5034
0.5212
0.5387
0.5559
0.5730
0.5898
h
Btu/lb
p 160 lbf/in.2
(Tsat 109.55F)
p 140 lbf/in.2
(Tsat 100.56F)
Sat.
120
140
160
180
200
220
240
260
280
300
320
340
360
u
Btu/lb
p 400 lbf/in.2
(Tsat 179.95F)
0.2132
0.2155
0.2265
0.2363
0.2453
0.2537
0.2618
0.2696
0.2772
0.2845
0.2916
0.2986
0.3055
0.3122
0.0965
112.77
119.91
0.2102
0.0965
0.1143
0.1275
0.1386
0.1484
0.1575
0.1660
0.1740
0.1816
0.1890
0.1962
0.2032
112.79
120.14
126.35
132.12
137.65
143.06
148.39
153.69
158.97
164.26
169.57
174.90
119.93
128.60
135.79
142.38
148.64
154.72
160.67
166.57
172.42
178.26
184.09
189.94
0.2102
0.2235
0.2343
0.2438
0.2527
0.2610
0.2689
0.2766
0.2840
0.2912
0.2983
0.3051
Tables in English Units
Copyright © 2006. Wiley. All rights reserved.
Properties of Saturated Ammonia (Liquid–Vapor): Temperature Table
Specific Volume
ft3/lb
Internal Energy
Btu/lb
Enthalpy
Btu/lb
Entropy
Btu/lb # R
Temp.
F
Press.
lbf/in.2
Sat.
Liquid
vf
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Temp.
F
60
55
50
45
40
5.548
6.536
7.664
8.949
10.405
0.02278
0.02288
0.02299
0.02310
0.02322
44.7537
38.3991
33.0880
28.6284
24.8672
21.005
15.765
10.525
5.295
0.045
543.61
545.11
546.59
548.04
549.46
20.97
15.73
10.49
5.25
0.00
610.56
607.31
604.04
600.72
597.37
589.58
591.58
593.54
595.48
597.37
0.0512
0.0381
0.0253
0.0126
0.0000
1.4765
1.4627
1.4492
1.4361
1.4235
60
55
50
45
40
35
30
25
20
15
12.049
13.899
15.972
18.290
20.871
0.02333
0.02345
0.02357
0.02369
0.02381
21.6812
18.9715
16.6577
14.6744
12.9682
5.20
10.46
15.73
21.01
26.31
550.86
552.24
553.59
554.91
556.20
5.26
10.52
15.80
21.09
26.40
593.98
590.54
587.05
583.51
579.92
599.24
601.06
602.85
604.61
606.32
0.0124
0.0247
0.0369
0.0490
0.0610
1.4111
1.3992
1.3875
1.3762
1.3652
35
30
25
20
15
10
5
0
5
10
23.738
26.912
30.416
34.275
38.512
0.02393
0.02406
0.02419
0.02432
0.02446
11.4951
10.2190
9.1100
8.1430
7.2974
31.63
36.96
42.32
47.69
53.09
557.46
558.70
559.91
561.08
562.23
31.73
37.08
42.45
47.85
53.27
576.26
572.54
568.76
564.92
561.00
607.99
609.62
611.22
612.76
614.27
0.0729
0.0847
0.0964
0.1080
0.1196
1.3544
1.3440
1.3338
1.3238
1.3141
10
5
0
5
10
15
20
25
30
35
43.153
48.224
53.752
59.765
66.291
0.02460
0.02474
0.02488
0.02503
0.02517
6.5556
5.9032
5.3278
4.8188
4.3675
58.52
63.97
69.43
74.93
80.44
563.34
564.43
565.48
566.49
567.48
58.72
64.19
69.68
75.20
80.75
557.01
552.95
548.82
544.62
540.34
615.73
617.14
618.51
619.82
621.09
0.1311
0.1425
0.1539
0.1651
0.1764
1.3046
1.2953
1.2862
1.2774
1.2687
15
20
25
30
35
40
45
50
55
60
73.359
81.000
89.242
98.118
107.66
0.02533
0.02548
0.02564
0.02581
0.02597
3.9664
3.6090
3.2897
3.0040
2.7476
85.98
91.55
97.13
102.73
108.35
568.42
569.33
570.21
571.04
571.83
86.33
91.93
97.55
103.20
108.87
535.97
531.54
527.02
522.42
517.74
622.30
623.46
624.57
625.62
626.61
0.1875
0.1986
0.2096
0.2205
0.2314
1.2602
1.2518
1.2436
1.2356
1.2277
40
45
50
55
60
65
70
75
80
85
90
117.90
128.87
140.60
153.13
166.50
180.73
0.02614
0.02632
0.02650
0.02668
0.02687
0.02707
2.5171
2.3095
2.1220
1.9524
1.7988
1.6593
113.99
119.65
125.33
131.02
136.73
142.46
572.59
573.29
573.95
574.57
575.13
575.65
114.56
120.28
126.02
131.78
137.56
143.37
512.97
508.12
503.18
498.15
493.03
487.81
627.54
628.40
629.20
629.93
630.59
631.18
0.2422
0.2530
0.2636
0.2742
0.2848
0.2953
1.2199
1.2123
1.2048
1.1973
1.1900
1.1827
65
70
75
80
85
90
95
100
105
110
115
120
195.87
211.96
229.02
247.10
266.24
286.47
0.02727
0.02747
0.02768
0.02790
0.02813
0.02836
1.5324
1.4168
1.3113
1.2149
1.1266
1.0456
148.21
153.98
159.76
165.58
171.41
177.28
576.10
576.51
576.85
577.13
577.34
577.48
149.20
155.05
160.94
166.85
172.80
178.79
482.49
477.06
471.52
465.86
460.08
454.16
631.68
632.11
632.46
632.71
632.88
632.95
0.3057
0.3161
0.3264
0.3366
0.3469
0.3570
1.1756
1.1685
1.1614
1.1544
1.1475
1.1405
95
100
105
110
115
120
Source: Tables A-13E through A-15E are calculated based on equations from L. Haar and J. S. Gallagher, “Thermodynamic Properties of
Ammonia,” J. Phys. Chem. Reference Data, Vol. 7, 1978, pp. 635–792.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Ammonia
TABLE A-13E
791
792
Tables in English Units
Copyright © 2006. Wiley. All rights reserved.
Ammonia
TABLE A-14E
Properties of Saturated Ammonia (Liquid–Vapor): Pressure Table
Specific Volume
ft3/lb
Internal Energy
Btu/lb
Enthalpy
Btu/lb
Entropy
Btu/lb # R
Press.
lbf/in.2
Temp.
F
Sat.
Liquid
vf
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Press.
lbf/in.2
5
6
7
8
9
63.10
57.63
52.86
48.63
44.81
0.02271
0.02283
0.02293
0.02302
0.02311
49.320
41.594
36.014
31.790
28.477
24.24
18.51
13.52
9.09
5.09
542.67
544.32
545.74
546.98
548.09
24.22
18.49
13.49
9.06
5.05
612.56
609.02
605.92
603.13
600.60
588.33
590.54
592.42
594.08
595.55
0.0593
0.0450
0.0326
0.0218
0.0121
1.4853
1.4699
1.4569
1.4456
1.4357
5
6
7
8
9
10
12
14
16
18
41.33
35.14
29.74
24.94
20.60
0.02319
0.02333
0.02345
0.02357
0.02367
25.807
21.764
18.843
16.631
14.896
1.44
5.06
10.73
15.80
20.38
549.09
550.82
552.31
553.60
554.75
1.40
5.11
10.79
15.87
20.46
598.27
594.08
590.36
587.01
583.94
596.87
599.18
601.16
602.88
604.40
0.0033
0.0121
0.0254
0.0371
0.0476
1.4268
1.4115
1.3986
1.3874
1.3775
10
12
14
16
18
20
25
30
35
40
16.63
7.95
0.57
5.89
11.65
0.02377
0.02399
0.02418
0.02435
0.02450
13.497
10.950
9.229
7.984
7.041
24.58
33.81
41.71
48.65
54.89
555.78
557.97
559.77
561.29
562.60
24.67
33.92
41.84
48.81
55.07
581.10
574.75
569.20
564.22
559.69
605.76
608.67
611.04
613.03
614.76
0.0571
0.0777
0.0951
0.1101
0.1234
1.3687
1.3501
1.3349
1.3221
1.3109
20
25
30
35
40
45
50
55
60
65
16.87
21.65
26.07
30.19
34.04
0.02465
0.02478
0.02491
0.02503
0.02515
6.302
5.705
5.213
4.801
4.450
60.56
65.77
70.61
75.13
79.39
563.75
564.78
565.70
566.53
567.29
60.76
66.00
70.86
75.41
79.69
555.50
551.59
547.93
544.46
541.16
616.26
617.60
618.79
619.87
620.85
0.1354
0.1463
0.1563
0.1656
0.1742
1.3011
1.2923
1.2843
1.2770
1.2703
45
50
55
60
65
70
75
80
85
90
37.67
41.11
44.37
47.47
50.44
0.02526
0.02536
0.02546
0.02556
0.02566
4.1473
3.8837
3.6520
3.4466
3.2632
83.40
87.21
90.84
94.30
97.62
567.99
568.63
569.22
569.77
570.28
83.73
87.57
91.22
94.71
98.05
538.01
535.00
532.10
529.31
526.62
621.74
622.56
623.32
624.02
624.66
0.1823
0.1900
0.1972
0.2040
0.2106
1.2641
1.2583
1.2529
1.2478
1.2429
70
75
80
85
90
100
110
120
130
140
150
56.01
61.17
65.98
70.50
74.75
78.78
0.02584
0.02601
0.02618
0.02634
0.02649
0.02664
2.9497
2.6913
2.4745
2.2899
2.1309
1.9923
103.87
109.68
115.11
120.21
125.04
129.63
571.21
572.01
572.73
573.36
573.92
574.42
104.35
110.20
115.69
120.85
125.73
130.37
521.48
516.63
512.02
507.64
503.43
499.39
625.82
626.83
627.71
628.48
629.16
629.76
0.2227
0.2340
0.2443
0.2540
0.2631
0.2717
1.2340
1.2259
1.2184
1.2115
1.2051
1.1991
100
110
120
130
140
150
175
200
225
250
275
300
88.02
96.31
103.85
110.78
117.20
123.20
0.02699
0.02732
0.02764
0.02794
0.02823
0.02851
1.7128
1.5010
1.3348
1.2007
1.0901
0.9974
140.19
149.72
158.43
166.48
173.99
181.05
575.45
576.21
576.77
577.16
577.41
577.54
141.07
150.73
159.58
167.77
175.43
182.63
489.89
481.07
472.80
464.97
457.49
450.31
630.95
631.80
632.38
632.74
632.92
632.94
0.2911
0.3084
0.3240
0.3382
0.3513
0.3635
1.1856
1.1737
1.1630
1.1533
1.1444
1.1361
175
200
225
250
275
300
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in English Units
T
F
v
ft3/lb
Properties of Superheated Ammonia Vapor
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
h
Btu/lb
s
Btu/lb # R
p 8 lbf/in.2
(Tsat 48.63F)
p 6 lbf/in.2
(Tsat 57.63F)
Sat.
50
40
41.594
42.435
43.533
544.32
547.22
551.03
590.54
594.37
599.40
1.4699
1.4793
1.4915
31.790
546.98
594.08
1.4456
32.511
550.32
598.49
1.4562
30
20
10
44.627
45.715
46.800
554.84
558.66
562.47
604.42
609.45
614.47
1.5033
1.5149
1.5261
33.342
34.169
34.992
554.19
558.06
561.93
603.58
608.68
613.76
1.4682
1.4799
1.4914
0
10
20
47.882
48.960
50.035
566.29
570.12
573.95
619.49
624.51
629.54
1.5372
1.5480
1.5586
35.811
36.627
37.440
565.79
569.66
573.52
618.84
623.91
628.99
1.5025
1.5135
1.5241
30
40
50
60
51.108
52.179
53.247
54.314
577.78
581.63
585.49
589.35
634.57
639.60
644.64
649.70
1.5690
1.5791
1.5891
1.5990
38.250
39.058
39.865
40.669
577.40
581.27
585.16
589.05
634.06
639.13
644.21
649.29
1.5346
1.5449
1.5549
1.5648
p 10 lbf/in.2
(Tsat 41.33F)
Copyright © 2006. Wiley. All rights reserved.
u
Btu/lb
p 12 lbf/in.2
(Tsat 35.14F)
Sat.
40
30
25.807
25.897
26.571
549.09
549.61
553.54
596.87
597.56
602.74
1.4268
1.4284
1.4406
21.764
550.82
599.18
1.4115
22.056
552.87
601.88
1.4178
20
10
0
27.241
27.906
28.568
557.46
561.37
565.29
607.90
613.05
618.19
1.4525
1.4641
1.4754
22.621
23.182
23.739
556.85
560.82
564.78
607.12
612.33
617.53
1.4298
1.4416
1.4530
10
20
30
29.227
29.882
30.535
569.19
573.10
577.01
623.31
628.43
633.55
1.4864
1.4972
1.5078
24.293
24.843
25.392
568.73
572.67
576.61
622.71
627.88
633.03
1.4642
1.4750
1.4857
40
50
60
70
31.186
31.835
32.482
33.127
580.91
584.82
588.74
592.66
638.66
643.77
648.89
654.01
1.5181
1.5282
1.5382
1.5479
25.937
26.481
27.023
27.564
580.55
584.49
588.43
592.38
638.19
643.33
648.48
653.63
1.4961
1.5063
1.5163
1.5261
p 14 lbf/in.2
(Tsat 29.74F)
p 16 lbf/in.2
(Tsat 24.94F)
Sat.
20
10
18.843
19.321
19.807
552.31
556.24
560.26
601.16
606.33
611.61
1.3986
1.4105
1.4223
16.631
16.845
17.275
553.60
555.62
559.69
602.88
605.53
610.88
1.3874
1.3935
1.4055
0
10
20
20.289
20.768
21.244
564.27
568.26
572.24
616.86
622.10
627.31
1.4339
1.4452
1.4562
17.701
18.124
18.544
563.75
567.79
571.81
616.19
621.48
626.75
1.4172
1.4286
1.4397
30
40
50
21.717
22.188
22.657
576.22
580.19
584.16
632.52
637.71
642.89
1.4669
1.4774
1.4877
18.961
19.376
19.789
575.82
579.82
583.82
632.00
637.23
642.45
1.4505
1.4611
1.4714
60
70
80
90
23.124
23.590
24.054
24.517
588.12
592.09
596.07
600.04
648.07
653.25
658.42
663.60
1.4977
1.5076
1.5173
1.5268
20.200
20.609
21.017
21.424
587.81
591.80
595.80
599.80
647.66
652.86
658.07
663.27
1.4815
1.4915
1.5012
1.5107
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Ammonia
TABLE A-15E
793
794
Tables in English Units
TABLE A-15E
T
F
v
ft3/lb
(Continued )
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
s
Btu/lb # R
Sat.
20
10
14.896
14.919
15.306
554.75
555.00
559.13
604.40
604.72
610.14
1.3775
1.3783
1.3905
13.497
555.78
605.76
1.3687
13.730
558.55
609.40
1.3769
0
10
20
15.688
16.068
16.444
563.23
567.31
571.37
615.52
620.87
626.18
1.4023
1.4138
1.4250
14.078
14.422
14.764
562.70
566.83
570.94
614.84
620.24
625.61
1.3888
1.4005
1.4118
30
40
50
16.818
17.189
17.558
575.42
579.46
583.48
631.47
636.75
642.00
1.4359
1.4466
1.4570
15.103
15.439
15.773
575.02
579.09
583.14
630.95
636.26
641.55
1.4228
1.4335
1.4440
60
70
80
90
17.925
18.291
18.655
19.018
587.50
591.52
595.53
599.55
647.25
652.48
657.71
662.94
1.4672
1.4772
1.4869
1.4965
16.105
16.436
16.765
17.094
587.19
591.23
595.26
599.30
646.83
652.10
657.35
662.60
1.4543
1.4643
1.4741
1.4838
p 30 lbf/in.2
(Tsat 0.57F)
Ammonia
h
Btu/lb
p 20 lbf/in.2
(Tsat 16.63F)
p 18 lbf/in.2
(Tsat 20.60F)
Copyright © 2006. Wiley. All rights reserved.
u
Btu/lb
p 40 lbf/in.2
(Tsat 11.65F)
Sat.
0
10
9.2286
9.2425
9.4834
559.77
560.02
564.38
611.04
611.36
617.07
1.3349
1.3356
1.3479
7.0414
562.60
614.76
1.3109
20
30
40
9.7209
9.9554
10.187
568.70
572.97
577.21
622.70
628.28
633.80
1.3598
1.3713
1.3824
7.1965
7.3795
7.5597
566.39
570.86
575.28
619.69
625.52
631.28
1.3213
1.3333
1.3450
50
60
70
10.417
10.645
10.871
581.42
585.60
589.76
639.28
644.73
650.15
1.3933
1.4039
1.4142
7.7376
7.9134
8.0874
579.65
583.97
588.26
636.96
642.58
648.16
1.3562
1.3672
1.3778
80
90
100
110
11.096
11.319
11.541
11.762
593.90
598.04
602.16
606.28
655.54
660.91
666.27
671.62
1.4243
1.4342
1.4438
1.4533
8.2598
8.4308
8.6006
8.7694
592.52
596.75
600.97
605.17
653.69
659.20
664.67
670.12
1.3881
1.3982
1.4081
1.4178
p 50 lbf/in.2
(Tsat 21.65F)
p 60 lbf/in.2
(Tsat 30.19F)
Sat.
40
60
5.7049
5.9815
6.2733
564.78
573.30
582.31
617.60
628.68
640.39
1.2923
1.3149
1.3379
4.8009
4.9278
5.1788
566.53
571.25
580.60
619.87
626.00
638.14
1.2770
1.2894
1.3133
80
100
120
6.5574
6.8358
7.1097
591.10
599.75
608.30
651.82
663.04
674.13
1.3595
1.3799
1.3993
5.4218
5.6587
5.8910
589.66
598.52
607.23
649.90
661.39
672.68
1.3355
1.3564
1.3762
140
160
200
7.3802
7.6480
8.1776
616.80
625.28
642.27
685.13
696.09
717.99
1.4180
1.4360
1.4702
6.1198
6.3458
6.7916
615.86
624.44
641.59
683.85
694.95
717.05
1.3951
1.4133
1.4479
240
280
320
360
8.7016
9.2218
9.7391
10.254
659.44
676.88
694.65
712.79
740.00
762.26
784.82
807.73
1.5026
1.5336
1.5633
1.5919
7.2318
7.6679
8.1013
8.5325
658.87
676.38
694.21
712.40
739.21
761.58
784.22
807.20
1.4805
1.5116
1.5414
1.5702
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in English Units
T
F
v
ft3/lb
(Continued)
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
h
Btu/lb
s
Btu/lb # R
p 80 lbf/in.2
(Tsat 44.37F)
p 70 lbf/in.2
(Tsat 37.67F)
Sat.
40
60
4.1473
4.1739
4.3962
567.99
569.15
578.85
621.74
623.25
635.84
1.2641
1.2671
1.2918
3.6520
569.22
623.32
1.2529
3.8084
577.06
633.48
1.2727
80
100
120
4.6100
4.8175
5.0202
588.19
597.26
606.14
647.95
659.70
671.22
1.3147
1.3361
1.3563
4.0006
4.1862
4.3668
586.69
595.98
605.04
645.95
657.99
669.73
1.2963
1.3182
1.3388
140
160
200
5.2193
5.4154
5.8015
614.91
623.60
640.91
682.56
693.79
716.11
1.3756
1.3940
1.4289
4.5436
4.7175
5.0589
613.94
622.74
640.22
681.25
692.63
715.16
1.3583
1.3770
1.4122
240
280
320
6.1818
6.5580
6.9314
658.29
675.89
693.78
738.42
760.89
783.62
1.4617
1.4929
1.5229
5.3942
5.7256
6.0540
657.71
675.39
693.34
737.62
760.20
783.02
1.4453
1.4767
1.5067
360
400
7.3026
7.6721
712.02
730.63
806.67
830.08
1.5517
1.5796
6.3802
6.7047
711.63
730.29
806.15
829.61
1.5357
1.5636
p 90 lbf/in.2
(Tsat 50.44F)
Copyright © 2006. Wiley. All rights reserved.
u
Btu/lb
p 100 lbf/in.2
(Tsat 56.01F)
Sat.
60
80
3.2632
3.3504
3.5261
570.28
575.22
585.15
624.66
631.05
643.91
1.2429
1.2553
1.2796
2.9497
2.9832
3.1460
571.21
573.32
583.58
625.82
628.56
641.83
1.2340
1.2393
1.2644
100
120
140
3.6948
3.8584
4.0180
594.68
603.92
612.97
656.26
668.22
679.93
1.3021
1.3231
1.3430
3.3014
3.4513
3.5972
593.35
602.79
611.98
654.49
666.70
678.59
1.2874
1.3088
1.3290
160
200
240
4.1746
4.4812
4.7817
621.88
639.52
657.13
691.45
714.20
736.82
1.3619
1.3974
1.4307
3.7401
4.0189
4.2916
621.01
638.82
656.54
690.27
713.24
736.01
1.3481
1.3841
1.4176
280
320
360
400
5.0781
5.3715
5.6628
5.9522
674.89
692.90
711.24
729.95
759.52
782.42
805.62
829.14
1.4623
1.4924
1.5214
1.5495
4.5600
4.8255
5.0888
5.3503
674.39
692.47
710.86
729.60
758.82
781.82
805.09
828.68
1.4493
1.4796
1.5087
1.5368
p 110 lbf/in.2
(Tsat 61.17F)
p 120 lbf/in.2
(Tsat 65.98F)
Sat.
80
100
2.6913
2.8344
2.9791
572.01
581.97
592.00
626.83
639.71
652.69
1.2259
1.2502
1.2738
2.4745
2.5744
2.7102
572.73
580.33
590.63
627.71
637.53
650.85
1.2184
1.2369
1.2611
120
140
160
3.1181
3.2528
3.3844
601.63
610.98
620.13
665.14
677.24
689.07
1.2957
1.3162
1.3356
2.8401
2.9657
3.0879
600.46
609.97
619.24
663.57
675.86
687.86
1.2834
1.3043
1.3240
200
240
280
3.6406
3.8905
4.1362
638.11
655.96
673.88
712.27
735.20
758.13
1.3719
1.4056
1.4375
3.3254
3.5563
3.7829
637.40
655.36
673.37
711.29
734.39
757.43
1.3606
1.3946
1.4266
320
360
400
4.3788
4.6192
4.8578
692.02
710.47
729.26
781.22
804.56
828.21
1.4679
1.4971
1.5252
4.0065
4.2278
4.4473
691.58
710.08
728.92
780.61
804.02
827.74
1.4572
1.4864
1.5147
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Ammonia
TABLE A-15E
795
796
Tables in English Units
TABLE A-15E
T
F
v
ft3/lb
(Continued)
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
s
Btu/lb # R
Sat.
80
100
2.2899
2.3539
2.4824
573.36
578.64
589.23
628.48
635.30
648.98
1.2115
1.2243
1.2492
2.1309
2.1633
2.2868
573.92
576.80
587.79
629.16
632.89
647.08
1.2051
1.2119
1.2379
120
140
160
2.6048
2.7226
2.8370
599.27
608.94
618.34
661.97
674.48
686.64
1.2720
1.2932
1.3132
2.4004
2.5140
2.6204
597.85
607.90
617.34
660.08
673.07
685.27
1.2604
1.2828
1.3025
180
200
240
2.9488
3.0585
3.2734
627.57
636.69
654.77
698.55
710.31
733.57
1.3321
1.3502
1.3844
2.7268
2.8289
3.0304
626.77
635.93
654.17
697.46
709.27
732.73
1.3222
1.3401
1.3747
280
320
360
400
3.4840
3.6915
3.8966
4.1000
672.87
691.14
709.69
728.57
756.73
780.00
803.49
827.27
1.4166
1.4472
1.4766
1.5049
3.2274
3.4212
3.6126
3.8022
672.38
690.73
709.34
728.27
756.04
779.42
802.99
826.84
1.4071
1.4379
1.4674
1.4958
p 150 lbf/in.2
(Tsat 78.78F)
Ammonia
h
Btu/lb
p 140 lbf/in.2
(Tsat 74.75F)
p 130 lbf/in.2
(Tsat 70.50F)
Copyright © 2006. Wiley. All rights reserved.
u
Btu/lb
p 200 lbf/in.2
(Tsat 96.31F)
Sat.
100
140
1.9923
2.1170
2.3332
574.42
586.33
606.84
629.76
645.13
671.65
1.1991
1.2271
1.2729
1.5010
1.5190
1.6984
576.21
578.52
601.34
631.80
634.77
664.24
1.1737
1.1790
1.2299
180
220
260
2.5343
2.7268
2.9137
625.95
644.43
662.70
696.35
720.17
743.63
1.3128
1.3489
1.3825
1.8599
2.0114
2.1569
621.77
641.07
659.90
690.65
715.57
739.78
1.2726
1.3104
1.3450
300
340
380
3.0968
3.2773
3.4558
681.02
699.54
718.35
767.04
790.57
814.34
1.4141
1.4443
1.4733
2.2984
2.4371
2.5736
678.62
697.44
716.50
763.74
787.70
811.81
1.3774
1.4081
1.4375
420
460
500
3.6325
3.8079
3.9821
737.50
757.01
776.91
838.39
862.78
887.51
1.5013
1.5284
1.5548
2.7085
2.8420
2.9742
735.86
755.57
775.65
836.17
860.82
885.80
1.4659
1.4933
1.5199
540
580
4.1553
4.3275
797.19
817.85
912.60
938.05
1.5804
1.6053
3.1054
3.2357
796.10
816.94
911.11
936.77
1.5457
1.5709
p 250 lbf/in.2
(Tsat 110.78F)
p 300 lbf/in.2
(Tsat 123.20F)
Sat.
140
180
1.2007
1.3150
1.4539
577.16
595.40
617.38
632.74
656.28
684.69
1.1533
1.1936
1.2395
0.9974
1.0568
1.1822
577.54
588.94
612.75
632.94
647.65
678.42
1.1361
1.1610
1.2107
220
260
300
1.5816
1.7025
1.8191
637.61
657.03
676.17
710.82
735.85
760.39
1.2791
1.3149
1.3481
1.2944
1.3992
1.4994
634.01
654.09
673.69
705.91
731.82
756.98
1.2524
1.2895
1.3235
340
380
420
1.9328
2.0443
2.1540
695.32
714.63
734.22
784.79
809.27
833.93
1.3794
1.4093
1.4380
1.5965
1.6913
1.7843
693.16
712.74
732.55
781.85
806.70
831.67
1.3554
1.3857
1.4148
460
500
540
580
2.2624
2.3695
2.4755
2.5807
754.12
774.38
795.01
816.01
858.85
884.07
909.61
935.47
1.4657
1.4925
1.5186
1.5440
1.8759
1.9663
2.0556
2.1440
752.66
773.10
793.90
815.07
856.87
882.33
908.09
934.17
1.4428
1.4699
1.4962
1.5218
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in English Units
Properties of Saturated Propane (Liquid–Vapor): Temperature Table
Specific Volume
ft3/lb
Internal Energy
Btu/lb
Enthalpy
Btu/lb
Entropy
Btu/lb # R
Press.
lbf/in2
Sat.
Liquid
vf
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Temp.
F
140
120
100
80
60
0.6053
1.394
2.888
5.485
9.688
0.02505
0.02551
0.02601
0.02653
0.02708
128.00
58.88
29.93
16.52
9.75
51.33
41.44
31.34
21.16
10.73
139.22
143.95
148.80
153.73
158.74
51.33
41.43
31.33
21.13
10.68
204.9
200.6
196.1
191.6
186.9
153.6
159.1
164.8
170.5
176.2
0.139
0.109
0.080
0.053
0.026
0.501
0.481
0.465
0.452
0.441
140
120
100
80
60
40
20
0
10
20
16.1
25.4
38.4
46.5
55.8
0.02767
0.02831
0.02901
0.02939
0.02978
6.08
3.98
2.70
2.25
1.89
0.08
10.81
21.98
27.69
33.47
163.80
168.88
174.01
176.61
179.15
0.00
10.94
22.19
27.94
33.78
181.9
176.6
171.0
168.0
164.9
181.9
187.6
193.2
196.0
198.7
0.000
0.025
0.050
0.063
0.074
0.433
0.427
0.422
0.420
0.418
40
20
0
10
20
30
40
50
60
70
66.5
78.6
92.3
107.7
124.9
0.03020
0.03063
0.03110
0.03160
0.03213
1.598
1.359
1.161
0.9969
0.8593
39.34
45.30
51.36
57.53
63.81
181.71
184.30
186.74
189.30
191.71
39.71
45.75
51.89
58.16
64.55
161.7
158.3
154.7
151.0
147.0
201.4
204.1
206.6
209.2
211.6
0.087
0.099
0.111
0.123
0.135
0.417
0.415
0.414
0.413
0.412
30
40
50
60
70
80
90
100
110
120
144.0
165.2
188.6
214.3
242.5
0.03270
0.03332
0.03399
0.03473
0.03555
0.7433
0.6447
0.5605
0.4881
0.4254
70.20
76.72
83.38
90.19
97.16
194.16
196.46
198.71
200.91
202.98
71.07
77.74
84.56
91.56
98.76
142.9
138.4
133.7
128.7
123.3
214.0
216.2
218.3
220.3
222.1
0.147
0.159
0.171
0.183
0.195
0.411
0.410
0.410
0.409
0.408
80
90
100
110
120
130
140
150
160
170
273.3
306.9
343.5
383.3
426.5
0.03646
0.03749
0.03867
0.04006
0.04176
0.3707
0.3228
0.2804
0.2426
0.2085
104.33
111.70
119.33
127.27
135.60
204.92
206.64
208.05
209.16
209.81
106.17
113.83
121.79
130.11
138.90
117.5
111.1
104.1
96.3
87.4
223.7
225.0
225.9
226.4
226.3
0.207
0.220
0.233
0.246
0.259
0.406
0.405
0.403
0.401
0.398
130
140
150
160
170
180
190
200
206.1
473.4
524.3
579.7
616.1
0.04392
0.04696
0.05246
0.07265
0.1771
0.1470
0.1148
0.07265
144.50
154.38
166.65
186.99
209.76
208.51
204.16
186.99
148.35
158.94
172.28
195.27
76.9
63.8
44.2
0.0
225.3
222.8
216.5
195.27
0.273
0.289
0.309
0.343
0.394
0.387
0.376
0.343
180
190
200
206.1
Copyright © 2006. Wiley. All rights reserved.
Temp.
F
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Propane
TABLE A-16E
797
798
Tables in English Units
TABLE A-17E
Properties of Saturated Propane (Liquid–Vapor): Pressure Table
Copyright © 2006. Wiley. All rights reserved.
Propane
Specific Volume
ft3/lb
Internal Energy
Btu/lb
Enthalpy
Btu/lb
Entropy
Btu/lb # R
Press.
lbf/in2
Temp.
F
Sat.
Liquid
vf
Sat.
Vapor
vg
Sat.
Liquid
uf
Sat.
Vapor
ug
Sat.
Liquid
hf
Evap.
hfg
Sat.
Vapor
hg
Sat.
Liquid
sf
Sat.
Vapor
sg
Press.
lbf/in2
0.75
1.5
3
5
7.5
135.1
118.1
98.9
83.0
69.3
0.02516
0.02556
0.02603
0.02644
0.02682
104.8
54.99
28.9
18.00
12.36
48.93
40.44
30.84
22.75
15.60
140.36
144.40
149.06
152.96
156.40
48.93
40.43
30.83
22.73
15.56
203.8
200.1
196.0
192.4
189.1
154.9
159.7
165.1
169.6
173.6
0.132
0.106
0.079
0.057
0.038
0.496
0.479
0.464
0.454
0.446
0.75
1.5
3
5
7.5
10
20
30
40
50
58.8
30.7
12.1
2.1
13.9
0.02711
0.02796
0.02858
0.02909
0.02954
9.468
4.971
3.402
2.594
2.099
10.10
4.93
15.15
23.19
29.96
159.04
166.18
170.93
174.60
177.63
10.05
5.03
15.31
23.41
30.23
186.6
179.5
174.5
170.4
166.8
176.6
184.6
189.8
193.8
197.1
0.024
0.012
0.035
0.053
0.067
0.441
0.430
0.425
0.422
0.419
10
20
30
40
50
60
70
80
90
100
24.1
33.0
41.1
48.4
55.1
0.02995
0.03033
0.03068
0.03102
0.03135
1.764
1.520
1.336
1.190
1.073
35.86
41.14
45.95
50.38
54.52
180.23
182.50
184.57
186.36
188.07
36.19
41.53
46.40
50.90
55.10
163.6
160.6
157.9
155.3
152.8
199.8
202.2
204.3
206.2
207.9
0.079
0.090
0.100
0.109
0.117
0.418
0.416
0.415
0.414
0.414
60
70
80
90
100
120
140
160
180
200
67.2
78.0
87.6
96.5
104.6
0.03198
0.03258
0.03317
0.03375
0.03432
0.8945
0.7650
0.6665
0.5890
0.5261
62.08
68.91
75.17
80.99
86.46
191.07
193.68
195.97
197.97
199.77
62.79
69.75
76.15
82.12
87.73
148.1
143.7
139.5
135.5
131.4
210.9
213.5
215.7
217.6
219.2
0.131
0.144
0.156
0.166
0.176
0.412
0.412
0.411
0.410
0.409
120
140
160
180
200
220
240
260
280
300
112.1
119.2
125.8
132.1
138.0
0.03489
0.03547
0.03606
0.03666
0.03727
0.4741
0.4303
0.3928
0.3604
0.3319
91.64
96.56
101.29
105.83
110.21
201.37
202.76
204.07
205.27
206.27
93.06
98.14
103.0
107.7
112.3
127.6
123.7
120.0
116.1
112.4
220.7
221.9
223.0
223.9
224.7
0.185
0.194
0.202
0.210
0.217
0.408
0.408
0.407
0.406
0.405
220
240
260
280
300
320
340
360
380
400
143.7
149.1
154.2
159.2
164.0
0.03790
0.03855
0.03923
0.03994
0.04069
0.3067
0.2842
0.2639
0.2455
0.2287
114.47
118.60
122.66
126.61
130.51
207.17
207.96
208.58
209.07
209.47
116.7
121.0
125.3
129.4
133.5
108.6
104.7
100.9
97.0
93.0
225.3
225.8
226.2
226.4
226.5
0.224
0.231
0.238
0.245
0.251
0.404
0.403
0.402
0.401
0.400
320
340
360
380
400
450
500
600
616.1
175.1
185.3
203.4
206.1
0.04278
0.04538
0.05659
0.07265
0.1921
0.1610
0.1003
0.07265
140.07
149.61
172.85
186.99
209.87
209.27
200.27
186.99
143.6
153.8
179.1
195.3
82.2
70.4
32.2
0.0
225.9
224.2
211.4
195.3
0.266
0.282
0.319
0.343
0.396
0.391
0.367
0.343
450
500
600
616.1
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in English Units
T
F
v
ft3/lb
Properties of Superheated Propane
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
h
Btu/lb
s
Btu/lb # R
p 1.5 lbf/in2
(Tsat 118.1F)
p 0.75 lbf/in2
(Tsat 135.1F)
Sat.
130
110
104.8
106.5
113.1
140.4
141.6
146.6
154.9
156.4
162.3
0.496
0.501
0.518
54.99
144.4
159.7
0.479
56.33
146.5
162.1
0.486
90
70
50
119.6
126.1
132.7
151.8
157.2
162.7
168.4
174.7
181.2
0.535
0.551
0.568
59.63
62.92
66.20
151.7
157.1
162.6
168.2
174.5
181.0
0.503
0.520
0.536
30
10
10
139.2
145.7
152.2
168.6
174.4
180.7
187.9
194.7
201.9
0.584
0.599
0.615
69.47
72.74
76.01
168.4
174.4
180.7
187.7
194.6
201.8
0.552
0.568
0.583
30
50
70
90
158.7
165.2
171.7
178.2
187.1
193.8
200.7
207.8
209.2
216.8
224.6
232.6
0.630
0.645
0.660
0.675
79.27
82.53
85.79
89.04
187.1
193.8
200.7
207.8
209.1
216.7
224.5
232.5
0.599
0.614
0.629
0.644
p 5.0 lbf/in2
(Tsat 83.0F)
Copyright © 2006. Wiley. All rights reserved.
u
Btu/lb
p 10.0 lbf/in2
(Tsat 58.8F)
Sat.
80
60
18.00
18.15
19.17
153.0
153.8
159.4
169.6
170.6
177.1
0.454
0.456
0.473
9.468
159.0
176.6
0.441
40
20
0
20.17
21.17
22.17
165.1
171.1
177.2
183.8
190.7
197.7
0.489
0.505
0.521
9.957
10.47
10.98
80.9
86.9
93.1
99.3
106.3
113.4
1.388
1.405
1.421
20
40
60
23.16
24.15
25.14
183.5
190.1
196.9
205.0
212.5
220.2
0.536
0.552
0.567
11.49
11.99
12.49
99.5
106.1
113.0
120.8
128.3
136.1
1.436
1.452
1.467
80
100
120
140
26.13
27.11
28.09
29.07
204.0
211.3
218.8
226.5
228.2
236.4
244.8
253.4
0.582
0.597
0.611
0.626
12.99
13.49
13.99
14.48
120.0
127.3
134.9
142.6
144.1
152.3
160.7
169.4
1.482
1.497
1.512
1.526
p 20.0 lbf/in2
(Tsat 30.7F)
p 40.0 lbf/in2
(Tsat 2.1F)
Sat.
20
0
4.971
5.117
5.385
166.2
169.5
175.8
184.6
188.5
195.8
0.430
0.439
0.455
2.594
174.6
193.8
0.422
20
40
60
5.648
5.909
6.167
182.4
189.1
195.9
203.3
211.0
218.8
0.471
0.487
0.502
2.723
2.864
3.002
180.6
187.6
194.6
200.8
208.8
216.9
0.436
0.453
0.469
80
100
120
6.424
6.678
6.932
203.1
210.5
218.0
226.9
235.2
243.7
0.518
0.533
0.548
3.137
3.271
3.403
201.8
209.4
217.0
225.1
233.6
242.2
0.484
0.500
0.515
140
160
180
200
7.184
7.435
7.685
7.935
225.8
233.9
242.1
250.6
252.4
261.4
270.6
280.0
0.562
0.577
0.592
0.606
3.534
3.664
3.793
3.921
224.9
232.9
241.3
249.8
251.1
260.1
269.4
278.9
0.530
0.545
0.559
0.574
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Propane
TABLE A-18E
799
800
Tables in English Units
TABLE A-18E
T
F
(Continued )
v
ft3/lb
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
s
Btu/lb # R
Sat.
30
50
1.764
1.794
1.894
180.2
182.4
189.5
199.8
202.3
210.6
0.418
0.384
0.400
1.336
184.6
204.3
0.415
1.372
187.9
208.2
0.423
70
90
110
1.992
2.087
2.179
196.9
204.4
212.1
219.0
227.6
236.3
0.417
0.432
0.448
1.450
1.526
1.599
195.4
203.1
210.9
216.9
225.7
234.6
0.440
0.456
0.472
130
150
170
2.271
2.361
2.450
220.0
228.0
236.3
245.2
254.2
263.5
0.463
0.478
0.493
1.671
1.741
1.810
218.8
227.0
235.4
243.6
252.8
262.2
0.487
0.503
0.518
190
210
230
250
2.539
2.626
2.713
2.800
244.8
253.5
262.3
271.6
273.0
282.7
292.5
302.7
0.508
0.523
0.537
0.552
1.879
1.946
2.013
2.079
244.0
252.7
261.7
270.9
271.8
281.5
291.5
301.7
0.533
0.548
0.562
0.577
p 100 lbf/in2
(Tsat 55.1F)
Propane
h
Btu/lb
p 80.0 lbf/in2
(Tsat 41.1F)
p 60.0 lbf/in2
(Tsat 24.1F)
Copyright © 2006. Wiley. All rights reserved.
u
Btu/lb
p 120 lbf/in2
(Tsat 67.2F)
Sat.
60
80
1.073
1.090
1.156
188.1
189.9
197.8
207.9
210.1
219.2
0.414
0.418
0.435
0.8945
191.1
210.9
0.412
0.9323
196.2
216.9
0.424
100
120
140
1.219
1.280
1.340
205.7
213.7
221.9
228.3
237.4
246.7
0.452
0.468
0.483
0.9887
1.043
1.094
204.3
212.5
220.8
226.3
235.7
245.1
0.441
0.457
0.473
160
180
200
1.398
1.454
1.510
230.2
238.8
247.5
256.1
265.7
275.5
0.499
0.514
0.529
1.145
1.194
1.242
229.2
237.9
246.7
254.7
264.4
274.3
0.489
0.504
0.520
220
240
260
280
1.566
1.620
1.674
1.728
256.4
265.6
274.9
284.4
285.4
295.6
305.9
316.4
0.544
0.559
0.573
0.588
1.289
1.336
1.382
1.427
255.6
264.8
274.2
283.8
284.3
294.5
304.9
315.5
0.534
0.549
0.564
0.579
p 140 lbf/in2
(Tsat 78.0F)
p 160 lbf/in2
(Tsat 87.6F)
Sat.
80
100
0.7650
0.7705
0.8227
193.7
213.3
222.9
213.5
214.5
224.2
0.412
0.413
0.431
0.6665
196.0
215.7
0.411
0.6968
201.2
221.9
0.422
120
140
160
0.8718
0.9185
0.9635
232.4
242.1
251.7
233.8
243.5
253.2
0.448
0.464
0.480
0.7427
0.7859
0.8272
209.9
218.4
227.2
231.9
241.7
251.7
0.439
0.456
0.472
180
200
220
1.007
1.050
1.091
261.4
271.4
281.5
263.0
273.0
283.2
0.496
0.511
0.526
0.8669
0.9054
0.9430
235.9
244.9
254.0
261.6
271.7
282.0
0.488
0.504
0.519
240
260
280
300
1.132
1.173
1.213
1.252
291.7
302.1
312.7
323.6
293.5
303.9
314.6
325.5
0.541
0.556
0.571
0.585
0.9797
1.016
1.051
1.087
263.4
272.8
282.6
292.4
292.4
302.9
313.7
324.6
0.534
0.549
0.564
0.578
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in English Units
T
F
(Continued )
v
ft3/lb
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
h
Btu/lb
s
Btu/lb # R
p 200 lbf/in2
(Tsat 104.6F)
p 180 lbf/in2
(Tsat 96.5F)
Sat.
100
120
0.5890
0.5972
0.6413
198.0
199.6
208.4
217.6
219.5
229.8
0.410
0.413
0.431
0.5261
199.8
219.2
0.409
0.5591
206.8
227.5
0.424
140
160
180
0.6821
0.7206
0.7574
217.1
226.1
234.9
239.9
250.1
260.2
0.449
0.465
0.481
0.5983
0.6349
0.6694
215.8
224.9
233.9
238.0
248.4
258.7
0.441
0.458
0.475
200
220
240
0.7928
0.8273
0.8609
244.0
253.2
262.6
270.4
280.8
291.3
0.497
0.513
0.528
0.7025
0.7345
0.7656
243.1
252.4
261.7
269.1
279.6
290.1
0.491
0.506
0.522
260
280
300
320
0.8938
0.9261
0.9579
0.9894
272.1
281.8
291.8
301.9
301.9
312.7
323.7
334.9
0.543
0.558
0.572
0.587
0.7960
0.8257
0.8549
0.8837
271.4
281.1
291.1
301.3
300.9
311.7
322.8
334.0
0.537
0.552
0.567
0.581
p 220 lbf/in2
(Tsat 112.1F)
Copyright © 2006. Wiley. All rights reserved.
u
Btu/lb
p 240 lbf/in2
(Tsat 119.2F)
Sat.
120
140
0.4741
0.4906
0.5290
201.4
205.1
214.4
220.7
225.1
236.0
0.408
0.416
0.435
0.4303
0.4321
0.4704
202.8
203.2
212.9
221.9
222.4
233.8
0.408
0.409
0.428
160
180
200
0.5642
0.5971
0.6284
223.6
232.9
242.1
246.6
257.2
267.7
0.452
0.469
0.485
0.5048
0.5365
0.5664
222.4
231.6
241.1
244.8
255.5
266.3
0.446
0.463
0.480
220
240
260
0.6585
0.6875
0.7158
251.5
261.0
270.6
278.3
289.0
299.8
0.501
0.516
0.532
0.5949
0.6223
0.6490
250.5
260.1
269.8
277.0
287.8
298.7
0.496
0.511
0.527
280
300
320
340
0.7435
0.7706
0.7972
0.8235
280.5
290.5
300.6
311.0
310.8
321.9
333.1
344.6
0.547
0.561
0.576
0.591
0.6749
0.7002
0.7251
0.7496
279.8
289.8
300.1
310.5
309.8
320.9
332.3
343.8
0.542
0.557
0.571
0.586
p 260 lbf/in2
(Tsat 125.8F)
p 280 lbf/in2
(Tsat 132.1F)
Sat.
130
150
0.3928
0.4012
0.4374
204.1
206.3
216.1
223.0
225.6
237.2
0.407
0.411
0.431
0.3604
205.3
223.9
0.406
0.3932
214.5
234.9
0.424
170
190
210
0.4697
0.4995
0.5275
225.8
235.2
244.8
248.4
259.3
270.2
0.449
0.466
0.482
0.4253
0.4544
0.4815
224.4
234.1
243.8
246.5
257.7
268.8
0.443
0.461
0.477
230
250
270
0.5541
0.5798
0.6046
254.4
264.2
274.1
281.1
292.1
303.2
0.498
0.514
0.530
0.5072
0.5317
0.5553
253.5
263.3
273.3
279.8
290.9
302.1
0.494
0.510
0.525
290
310
330
350
0.6288
0.6524
0.6756
0.6984
284.0
294.3
304.7
315.2
314.3
325.7
337.2
348.8
0.545
0.560
0.574
0.589
0.5783
0.6007
0.6226
0.6441
283.4
293.5
304.0
314.6
313.4
324.7
336.3
348.0
0.540
0.555
0.570
0.585
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Propane
TABLE A-18E
801
802
Tables in English Units
TABLE A-18E
T
F
(Continued)
v
ft3/lb
u
Btu/lb
h
Btu/lb
s
Btu/lb # R
v
ft3/lb
s
Btu/lb # R
Sat.
150
170
0.3067
0.3187
0.3517
207.2
210.7
221.4
225.3
229.6
242.3
0.404
0.412
0.432
0.2639
208.6
226.2
0.402
0.2920
217.9
237.4
0.420
190
210
230
0.3803
0.4063
0.4304
231.7
241.6
251.6
254.2
265.7
277.1
0.450
0.468
0.485
0.3213
0.3469
0.3702
228.8
239.3
249.5
250.2
262.4
274.2
0.440
0.459
0.476
250
270
290
0.4533
0.4751
0.4961
261.6
271.7
281.9
288.5
299.9
311.3
0.501
0.517
0.532
0.3919
0.4124
0.4320
259.8
270.1
280.4
285.9
297.6
309.2
0.493
0.509
0.525
310
330
350
370
0.5165
0.5364
0.5559
0.5750
292.3
302.7
313.4
324.2
322.9
334.5
346.3
358.3
0.548
0.563
0.577
0.592
0.4510
0.4693
0.4872
0.5047
290.8
301.4
312.2
323.0
320.9
332.7
344.7
356.7
0.540
0.556
0.570
0.585
p 400 lbf/in2
(Tsat 164.0F)
Propane
h
Btu/lb
p 360 lbf/in2
(Tsat 154.2F)
p 320 lbf/in2
(Tsat 143.7F)
Copyright © 2006. Wiley. All rights reserved.
u
Btu/lb
p 450 lbf/in2
(Tsat 175.1F)
Sat.
170
190
0.2287
0.2406
0.2725
209.5
213.6
225.6
226.5
231.4
245.8
0.400
0.408
0.430
0.1921
209.9
225.9
0.396
0.2205
220.7
239.1
0.416
210
230
250
0.2985
0.3215
0.3424
236.7
247.4
257.8
258.8
271.2
283.2
0.450
0.468
0.485
0.2486
0.2719
0.2925
233.0
244.3
255.2
253.7
267.0
279.6
0.439
0.458
0.476
270
290
310
0.3620
0.3806
0.3984
268.3
278.8
289.4
295.1
307.0
318.9
0.502
0.518
0.534
0.3113
0.3290
0.3457
266.0
276.8
287.6
292.0
304.2
316.4
0.493
0.510
0.526
330
350
370
390
0.4156
0.4322
0.4484
0.4643
300.1
311.0
321.9
333.1
330.9
343.0
355.1
367.5
0.549
0.564
0.579
0.594
0.3617
0.3772
0.3922
0.4068
298.4
309.4
320.4
331.7
328.5
340.8
353.1
365.6
0.542
0.557
0.572
0.587
p 500 lbf/in2
(Tsat 185.3F)
p 600 lbf/in2
(Tsat 203.4F)
Sat.
190
210
0.1610
0.1727
0.2066
209.3
213.8
228.6
224.2
229.8
247.7
0.391
0.399
0.426
0.1003
200.3
211.4
0.367
0.1307
214.3
228.8
0.394
230
250
270
0.2312
0.2519
0.2704
240.9
252.4
263.6
262.3
275.7
288.6
0.448
0.467
0.485
0.1661
0.1892
0.2080
232.2
245.8
258.1
250.7
266.8
281.2
0.426
0.449
0.469
290
310
330
0.2874
0.3034
0.3186
274.6
285.6
296.6
301.2
313.7
326.1
0.502
0.519
0.534
0.2245
0.2396
0.2536
269.8
281.4
292.8
294.8
308.0
321.0
0.487
0.505
0.521
350
370
390
410
0.3331
0.3471
0.3607
0.3740
307.7
318.9
330.2
341.7
338.6
351.0
363.6
376.3
0.550
0.565
0.580
0.595
0.2669
0.2796
0.2917
0.3035
304.2
315.7
327.3
338.9
333.9
346.8
359.7
372.6
0.538
0.553
0.569
0.584
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in English Units
Properties of Selected Solids and Liquids: cp, , and
Specific
Heat, cp
(Btu/lb # R)
Density,
(lb/ft3)
Thermal
Conductivity,
(Btu/h # ft # R)
Selected Solids, 540⬚R
Aluminum
Coal, anthracite
Copper
Granite
Iron
Lead
Sand
Silver
Soil
Steel (AISI 302)
Tin
0.216
0.301
0.092
0.185
0.107
0.031
0.191
0.056
0.439
0.115
0.054
169
84.3
557
164
491
705
94.9
656
128
503
456
137
0.15
232
1.61
46.4
20.4
0.16
248
0.30
8.7
38.5
Building Materials, 540⬚R
Brick, common
Concrete (stone mix)
Glass, plate
Hardboard, siding
Limestone
Plywood
Softwoods (fir, pine)
0.199
0.210
0.179
0.279
0.193
0.291
0.330
120
144
156
40
145
34
31.8
0.42
0.81
0.81
0.054
1.24
0.069
0.069
Insulating Materials, 540⬚R
Blanket (glass fiber)
Cork
Duct liner (glass fiber, coated)
Polystyrene (extruded)
Vermiculite fill (flakes)
—
0.43
0.199
0.289
0.199
1.0
7.5
2.0
3.4
5.0
0.027
0.023
0.022
0.016
0.039
Saturated Liquids
Ammonia, 540R
Mercury, 540R
Refrigerant 22, 540R
Refrigerant 134a, 540R
Unused Engine Oil, 540R
Water, 495R
540R
585R
630R
675R
720R
1.151
0.033
0.303
0.343
0.456
1.006
0.998
0.999
1.002
1.008
1.017
37.5
845
74.0
75.0
55.2
62.42
62.23
61.61
60.79
59.76
58.55
0.269
4.94
0.049
0.047
0.084
0.332
0.354
0.373
0.386
0.394
0.398
Copyright © 2006. Wiley. All rights reserved.
Substance
Source: Drawn from several sources, these data are only representative. Values can vary depending on
temperature, purity, moisture content, and other factors.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Table A-19E
TABLE A-19E
803
804
Tables in English Units
Ideal Gas Specific Heats of Some Common Gases (Btu/lb # R)
TABLE A-20E
cp
cv
Temp.
F
k
cp
cv
Air
k
cp
cv
Nitrogen, N2
k
Temp.
F
Oxygen, O2
40
100
200
0.240
0.240
0.241
0.171
0.172
0.173
1.401
1.400
1.397
0.248
0.248
0.249
0.177
0.178
0.178
1.400
1.399
1.398
0.219
0.220
0.223
0.156
0.158
0.161
1.397
1.394
1.387
40
100
200
300
400
500
0.243
0.245
0.248
0.174
0.176
0.179
1.394
1.389
1.383
0.250
0.251
0.254
0.179
0.180
0.183
1.396
1.393
1.388
0.226
0.230
0.235
0.164
0.168
0.173
1.378
1.368
1.360
300
400
500
600
700
800
0.250
0.254
0.257
0.182
0.185
0.188
1.377
1.371
1.365
0.256
0.260
0.262
0.185
0.189
0.191
1.383
1.377
1.371
0.239
0.242
0.246
0.177
0.181
0.184
1.352
1.344
1.337
600
700
800
900
1000
1500
2000
0.259
0.263
0.276
0.286
0.191
0.195
0.208
0.217
1.358
1.353
1.330
1.312
0.265
0.269
0.283
0.293
0.194
0.198
0.212
0.222
1.364
1.359
1.334
1.319
0.249
0.252
0.263
0.270
0.187
0.190
0.201
0.208
1.331
1.326
1.309
1.298
900
1000
1500
2000
Temp.
F
Carbon
Dioxide, CO2
Carbon
Monoxide, CO
Hydrogen, H2
Temp.
F
40
100
200
0.195
0.205
0.217
0.150
0.160
0.172
1.300
1.283
1.262
0.248
0.249
0.249
0.177
0.178
0.179
1.400
1.399
1.397
3.397
3.426
3.451
2.412
2.441
2.466
1.409
1.404
1.399
40
100
200
300
400
500
0.229
0.239
0.247
0.184
0.193
0.202
1.246
1.233
1.223
0.251
0.253
0.256
0.180
0.182
0.185
1.394
1.389
1.384
3.461
3.466
3.469
2.476
2.480
2.484
1.398
1.397
1.397
300
400
500
600
700
800
0.255
0.262
0.269
0.210
0.217
0.224
1.215
1.208
1.202
0.259
0.262
0.266
0.188
0.191
0.195
1.377
1.371
1.364
3.473
3.477
3.494
2.488
2.492
2.509
1.396
1.395
1.393
600
700
800
900
1000
1500
2000
0.275
0.280
0.298
0.312
0.230
0.235
0.253
0.267
1.197
1.192
1.178
1.169
0.269
0.273
0.287
0.297
0.198
0.202
0.216
0.226
1.357
1.351
1.328
1.314
3.502
3.513
3.618
3.758
2.519
2.528
2.633
2.773
1.392
1.390
1.374
1.355
900
1000
1500
2000
Table A-20E
Copyright © 2006. Wiley. All rights reserved.
Source: Adapted from K. Wark, Thermodynamics, 4th ed., McGraw-Hill, New York, 1983, as based on “Tables
of Thermal Properties of Gases,” NBS Circular 564, 1955.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Tables in English Units
TABLE A-21E
805
Variation of cp with Temperature for Selected Ideal Gases
cp
R
a
bT
gT 2
dT 3
eT 4
T is in R, equations valid from 540 to 1800 R
Gas
103
106
109
1012
CO
CO2
H2
H2O
3.710
2.401
3.057
4.070
0.899
4.853
1.487
0.616
1.140
2.039
1.793
1.281
0.348
0.343
0.947
0.508
0.0228
0
0.1726
0.0769
O2
N2
Air
NH3
3.626
3.675
3.653
3.591
1.043
0.671
0.7428
0.274
2.178
0.717
1.017
2.576
1.160
0.108
0.328
1.437
0.2053
0.0215
0.02632
0.2601
NO
NO2
SO2
SO3
4.046
3.459
3.267
2.578
1.899
1.147
2.958
8.087
2.464
2.064
0.211
2.832
1.048
1.639
0.906
0.136
0.1517
0.3448
0.2438
0.1878
CH4
C2H2
C2H4
3.826
1.410
1.426
2.211
10.587
6.324
7.580
7.562
2.466
3.898
2.811
2.787
0.6633
0.3939
0.6429
Monatomic
gasesa
2.5
0
0
0
0
a
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Table A-21E
Copyright © 2006. Wiley. All rights reserved.
For monatomic gases, such as He, Ne, and Ar, cp is constant over a wide temperature range and is very nearly
equal to 52 R.
Source: Adapted from K. Wark, Thermodynamics, 4th ed., McGraw-Hill, New York, 1983, as based on NASA
SP-273, U.S. Government Printing Office, Washington, DC, 1971.
Table A-22E
806
Tables in English Units
TABLE A-22E
Ideal Gas Properties of Air
T(R), h and u(Btu/lb), s(Btu/lb # R)
when s 01
vr
when s 0
h
u
s
396.6
346.6
305.0
270.1
240.6
940
960
980
1000
1040
226.11
231.06
236.02
240.98
250.95
161.68
165.26
168.83
172.43
179.66
0.73509
0.74030
0.74540
0.75042
0.76019
9.834
10.61
11.43
12.30
14.18
35.41
33.52
31.76
30.12
27.17
0.7913
0.9182
1.0590
1.2147
1.3593
215.33
193.65
174.90
158.58
146.34
1080
1120
1160
1200
1240
260.97
271.03
281.14
291.30
301.52
186.93
194.25
201.63
209.05
216.53
0.76964
0.77880
0.78767
0.79628
0.80466
16.28
18.60
21.18
24.01
27.13
24.58
22.30
20.29
18.51
16.93
0.60078
0.60950
0.61793
0.62607
0.63395
1.3860
1.5742
1.7800
2.005
2.249
144.32
131.78
120.70
110.88
102.12
1280
1320
1360
1400
1440
311.79
322.11
332.48
342.90
353.37
224.05
231.63
239.25
246.93
254.66
0.81280
0.82075
0.82848
0.83604
0.84341
30.55
34.31
38.41
42.88
47.75
15.52
14.25
13.12
12.10
11.17
109.21
112.67
116.12
119.58
123.04
0.64159
0.64902
0.65621
0.66321
0.67002
2.514
2.801
3.111
3.446
3.806
94.30
87.27
80.96
75.25
70.07
1480
1520
1560
1600
1650
363.89
374.47
385.08
395.74
409.13
262.44
270.26
278.13
286.06
296.03
0.85062
0.85767
0.86456
0.87130
0.87954
53.04
58.78
65.00
71.73
80.89
10.34
9.578
8.890
8.263
7.556
177.23
182.08
186.94
191.81
196.69
126.51
129.99
133.47
136.97
140.47
0.67665
0.68312
0.68942
0.69558
0.70160
4.193
4.607
5.051
5.526
6.033
65.38
61.10
57.20
53.63
50.35
1700
1750
1800
1850
1900
422.59
436.12
449.71
463.37
477.09
306.06
316.16
326.32
336.55
346.85
0.88758
0.89542
0.90308
0.91056
0.91788
90.95
101.98
114.0
127.2
141.5
6.924
6.357
5.847
5.388
4.974
201.56
206.46
211.35
216.26
221.18
143.98
147.50
151.02
154.57
158.12
0.70747
0.71323
0.71886
0.72438
0.72979
6.573
7.149
7.761
8.411
9.102
47.34
44.57
42.01
39.64
37.44
1950
2000
2050
2100
2150
490.88
504.71
518.61
532.55
546.54
357.20
367.61
378.08
388.60
399.17
0.92504
0.93205
0.93891
0.94564
0.95222
157.1
174.0
192.3
212.1
233.5
4.598
4.258
3.949
3.667
3.410
h
u
s
pr
360
380
400
420
440
85.97
90.75
95.53
100.32
105.11
61.29
64.70
68.11
71.52
74.93
0.50369
0.51663
0.52890
0.54058
0.55172
0.3363
0.4061
0.4858
0.5760
0.6776
460
480
500
520
537
109.90
114.69
119.48
124.27
128.34
78.36
81.77
85.20
88.62
91.53
0.56235
0.57255
0.58233
0.59172
0.59945
540
560
580
600
620
129.06
133.86
138.66
143.47
148.28
92.04
95.47
98.90
102.34
105.78
640
660
680
700
720
153.09
157.92
162.73
167.56
172.39
740
760
780
800
820
840
860
880
900
920
Copyright © 2006. Wiley. All rights reserved.
1. pr and vr data for use with Eqs. 6.43 and 6.44, respectively.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
pr
vr
T
T
TABLE A-22E
(Continued )
T(R), h and u(Btu/lb), s(Btu/lb # R)
when s 01
when s 0
h
u
s
pr
vr
T
h
u
s
pr
vr
2200
2250
2300
2350
2400
560.59
574.69
588.82
603.00
617.22
409.78
420.46
431.16
441.91
452.70
0.95868
0.96501
0.97123
0.97732
0.98331
256.6
281.4
308.1
336.8
367.6
3.176
2.961
2.765
2.585
2.419
3700
3750
3800
3850
3900
998.11
1013.1
1028.1
1043.1
1058.1
744.48
756.04
767.60
779.19
790.80
1.10991
1.11393
1.11791
1.12183
1.12571
2330
2471
2618
2773
2934
.5882
.5621
.5376
.5143
.4923
2450
2500
2550
2600
2650
631.48
645.78
660.12
674.49
688.90
463.54
474.40
485.31
496.26
507.25
0.98919
0.99497
1.00064
1.00623
1.01172
400.5
435.7
473.3
513.5
556.3
2.266
2.125
1.996
1.876
1.765
3950
4000
4050
4100
4150
1073.2
1088.3
1103.4
1118.5
1133.6
802.43
814.06
825.72
837.40
849.09
1.12955
1.13334
1.13709
1.14079
1.14446
3103
3280
3464
3656
3858
.4715
.4518
.4331
.4154
.3985
2700
2750
2800
2850
2900
703.35
717.83
732.33
746.88
761.45
518.26
529.31
540.40
551.52
562.66
1.01712
1.02244
1.02767
1.03282
1.03788
601.9
650.4
702.0
756.7
814.8
1.662
1.566
1.478
1.395
1.318
4200
4300
4400
4500
4600
1148.7
1179.0
1209.4
1239.9
1270.4
860.81
884.28
907.81
931.39
955.04
1.14809
1.15522
1.16221
1.16905
1.17575
4067
4513
4997
5521
6089
.3826
.3529
.3262
.3019
.2799
2950
3000
3050
3100
3150
776.05
790.68
805.34
820.03
834.75
573.84
585.04
596.28
607.53
618.82
1.04288
1.04779
1.05264
1.05741
1.06212
876.4
941.4
1011
1083
1161
1.247
1.180
1.118
1.060
1.006
4700
4800
4900
5000
5100
1300.9
1331.5
1362.2
1392.9
1423.6
978.73
1002.5
1026.3
1050.1
1074.0
1.18232
1.18876
1.19508
1.20129
1.20738
6701
7362
8073
8837
9658
.2598
.2415
.2248
.2096
.1956
3200
3250
3300
3350
3400
849.48
864.24
879.02
893.83
908.66
630.12
641.46
652.81
664.20
675.60
1.06676
1.07134
1.07585
1.08031
1.08470
1242
1328
1418
1513
1613
0.9546
0.9069
0.8621
0.8202
0.7807
5200
5300
1454.4
1485.3
1098.0
1122.0
1.21336
1.21923
10539
11481
.1828
.1710
3450
3500
3550
3600
3650
923.52
938.40
953.30
968.21
983.15
687.04
698.48
709.95
721.44
732.95
1.08904
1.09332
1.09755
1.10172
1.10584
1719
1829
1946
2068
2196
0.7436
0.7087
0.6759
0.6449
0.6157
Copyright © 2006. Wiley. All rights reserved.
T
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Table A-22E
807
Tables in English Units
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
808
T
300
320
340
360
380
400
420
440
460
480
500
520
537
540
560
580
600
620
640
660
680
700
720
740
760
780
800
820
840
860
880
900
920
940
960
980
1000
1020
1040
1060
s°
46.353
46.832
47.289
47.728
48.148
48.555
48.947
49.329
49.698
50.058
50.408
50.750
51.032
51.082
51.408
51.726
52.038
52.343
52.641
52.934
53.225
53.503
53.780
54.051
54.319
54.582
54.839
55.093
55.343
55.589
55.831
56.070
56.305
56.536
56.765
56.990
57.212
57.432
57.647
57.861
u
1486.1
1585.4
1684.7
1783.9
1883.3
1982.6
2081.9
2181.2
2280.5
2379.8
2479.2
2578.6
2663.1
2677.9
2777.4
2876.9
2976.5
3076.2
3175.9
3275.8
3375.8
3475.9
3576.3
3676.9
3777.5
3878.4
3979.5
4081.0
4182.6
4284.5
4386.6
4489.1
4592.0
4695.0
4798.5
4902.3
5006.3
5110.8
5215.7
5320.9
s°
43.223
43.672
44.093
44.490
44.866
45.223
45.563
45.886
46.194
46.491
46.775
47.048
47.272
47.310
47.563
47.807
48.044
48.272
48.494
48.709
48.917
49.120
49.317
49.509
49.697
49.880
50.058
50.232
50.402
50.569
50.732
50.892
51.048
51.202
51.353
51.501
51.646
51.788
51.929
52.067
h
2081.9
2220.9
2359.9
2498.8
2637.9
2776.9
2916.0
3055.0
3194.0
3333.0
3472.1
3611.2
3725.1
3750.3
3889.5
4028.7
4168.0
4307.4
4446.9
4586.6
4726.2
4866.0
5006.1
5146.4
5286.8
5427.4
5568.2
5709.4
5850.7
5992.3
6134.2
6276.4
6419.0
6561.7
6704.9
6848.4
6992.2
7136.4
7281.0
7425.9
u
1512.4
1621.1
1732.1
1845.6
1961.8
2080.4
2201.7
2325.6
2452.2
2581.5
2713.3
2847.7
2963.8
2984.4
3123.7
3265.4
3409.4
3555.6
3704.0
3854.6
4007.2
4161.9
4318.6
4477.3
4637.9
4800.1
4964.2
5129.9
5297.6
5466.9
5637.7
5810.3
5984.4
6160.1
6337.4
6516.1
6696.2
6877.8
7060.9
7245.3
h
2108.2
2256.6
2407.3
2560.5
2716.4
2874.7
3035.7
3199.4
3365.7
3534.7
3706.2
3880.3
4027.5
4056.8
4235.8
4417.2
4600.9
4786.6
4974.9
5165.2
5357.6
5552.0
5748.4
5946.8
6147.0
6349.1
6552.9
6758.3
6965.7
7174.7
7385.3
7597.6
7811.4
8026.8
8243.8
8462.2
8682.1
8903.4
9126.2
9350.3
h
2367.6
2526.8
2686.0
2845.1
3004.4
3163.8
3323.2
3482.7
3642.3
3802.0
3962.0
4122.0
4258.0
4282.4
4442.8
4603.7
4764.7
4926.1
5087.8
5250.0
5412.5
5575.4
5738.8
5902.6
6066.9
6231.7
6396.9
6562.6
6728.9
6895.6
7062.9
7230.9
7399.4
7568.4
7738.0
7908.2
8078.9
8250.4
8422.4
8595.0
u
1771.8
1891.3
2010.8
2130.2
2249.8
2369.4
2489.1
2608.9
2728.8
2848.8
2969.1
3089.4
3191.9
3210.0
3330.7
3451.9
3573.2
3694.9
3816.8
3939.3
4062.1
4185.3
4309.0
4433.1
4557.6
4682.7
4808.2
4934.2
5060.8
5187.8
5315.3
5443.6
5572.4
5701.7
5831.6
5962.0
6093.0
6224.8
6357.1
6490.0
s°
40.439
40.952
41.435
41.889
42.320
42.728
43.117
43.487
43.841
44.182
44.508
44.821
45.079
45.124
45.415
45.696
45.970
46.235
46.492
46.741
46.984
47.219
47.450
47.673
47.893
48.106
48.316
48.520
48.721
48.916
49.109
49.298
49.483
49.665
49.843
50.019
50.191
50.360
50.528
50.693
Water Vapor, H2O
(h°f 104,040 Btu /lbmol)
u
1477.8
1577.1
1676.5
1775.9
1875.3
1974.8
2074.3
2173.8
2273.4
2373.3
2473.2
2573.4
2658.7
2673.8
2774.5
2875.5
2976.8
3078.4
3180.4
3282.9
3385.8
3489.2
3593.1
3697.4
3802.2
3907.5
4013.3
4119.7
4226.6
4334.1
4442.0
4550.6
4659.7
4769.4
4879.5
4990.3
5101.6
5213.3
5325.7
5438.6
s°
44.927
45.375
45.797
46.195
46.571
46.927
47.267
47.591
47.900
48.198
48.483
48.757
48.982
49.021
49.276
49.522
49.762
49.993
50.218
50.437
50.650
50.858
51.059
51.257
51.450
51.638
51.821
52.002
52.179
52.352
52.522
52.688
52.852
53.012
53.170
53.326
53.477
53.628
53.775
53.921
Oxygen, O2
(h°f 0 Btu/lbmol)
h
2073.5
2212.6
2351.7
2490.8
2630.0
2769.1
2908.3
3047.5
3186.9
3326.5
3466.2
3606.1
3725.1
3746.2
3886.6
4027.3
4168.3
4309.7
4451.4
4593.5
4736.2
4879.3
5022.9
5167.0
5311.4
5456.4
5602.0
5748.1
5894.8
6041.9
6189.6
6337.9
6486.7
6636.1
6786.0
6936.4
7087.5
7238.9
7391.0
7543.6
T(R), h and u(Btu/lbmol), s°(Btu/lbmol # R)
Carbon Monoxide, CO
(h°f 47,540 Btu/lbmol)
Ideal Gas Properties of Selected Gases
Carbon Dioxide, CO2
(h°f 169,300 Btu /lbmol)
TABLE A-23E
Copyright © 2006. Wiley. All rights reserved.
h
2082.0
2221.0
2360.0
2498.9
2638.0
2777.0
2916.1
3055.1
3194.1
3333.1
3472.2
3611.3
3729.5
3750.3
3889.5
4028.7
4167.9
4307.1
4446.4
4585.8
4725.3
4864.9
5004.5
5144.3
5284.1
5424.2
5564.4
5704.7
5845.3
5985.9
6126.9
6268.1
6409.6
6551.2
6693.1
6835.4
6977.9
7120.7
7263.8
7407.2
u
1486.2
1585.5
1684.4
1784.0
1883.4
1982.6
2082.0
2181.3
2280.6
2379.9
2479.3
2578.6
2663.1
2678.0
2777.4
2876.9
2976.4
3075.9
3175.5
3275.2
3374.9
3474.8
3574.7
3674.7
3774.9
3875.2
3975.7
4076.3
4177.1
4278.1
4379.4
4480.8
4582.6
4684.5
4786.7
4889.3
4992.0
5095.1
5198.5
5302.2
s°
41.695
42.143
42.564
42.962
43.337
43.694
44.034
44.357
44.665
44.962
45.246
45.519
45.743
45.781
46.034
46.278
46.514
46.742
46.964
47.178
47.386
47.588
47.785
47.977
48.164
48.345
48.522
48.696
48.865
49.031
49.193
49.352
49.507
49.659
49.808
49.955
50.099
50.241
50.380
50.516
Nitrogen, N2
(h°f 0 Btu /lbmol)
Table A-23E
300
320
340
360
380
400
420
440
460
480
500
520
537
540
560
580
600
620
640
660
680
700
720
740
760
780
800
820
840
860
880
900
920
940
960
980
1000
1020
1040
1060
T
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
809
T
1080
1100
1120
1140
1160
1180
1200
1220
1240
1260
1280
1300
1320
1340
1360
1380
1400
1420
1440
1460
1480
1500
1520
1540
1560
1580
1600
1620
1640
1660
1680
1700
1720
1740
1760
1780
1800
1820
1840
1860
s°
58.072
58.281
58.485
58.689
58.889
59.088
59.283
59.477
59.668
59.858
60.044
60.229
60.412
60.593
60.772
60.949
61.124
61.298
61.469
61.639
61.800
61.974
62.138
62.302
62.464
62.624
62.783
62.939
63.095
63.250
63.403
63.555
63.704
63.853
64.001
64.147
64.292
64.435
64.578
64.719
u
5426.4
5532.3
5638.7
5745.4
5851.5
5960.0
6067.8
6176.0
6284.7
6393.8
6503.1
6613.0
6723.2
6833.7
6944.7
7056.1
7167.9
7280.1
7392.6
7505.4
7618.7
7732.3
7846.4
7960.8
8075.4
8190.5
8306.0
8421.8
8537.9
8654.4
8771.2
8888.3
9005.7
9123.6
9241.6
9360.0
9478.6
9597.7
9717.0
9836.5
s°
52.203
52.337
52.468
52.598
52.726
52.852
52.976
53.098
53.218
53.337
53.455
53.571
53.685
53.799
53.910
54.021
54.129
54.237
54.344
54.448
54.522
54.665
54.757
54.858
54.958
55.056
55.154
55.251
55.347
55.411
55.535
55.628
55.720
55.811
55.900
55.990
56.078
56.166
56.253
56.339
h
7571.1
7716.8
7862.9
8009.2
8156.1
8303.3
8450.8
8598.8
8747.2
8896.0
9045.0
9194.6
9344.6
9494.8
9645.5
9796.6
9948.1
10100.0
10252.2
10404.8
10557.8
10711.1
10864.9
11019.0
11173.4
11328.2
11483.4
11638.9
11794.7
11950.9
12107.5
12264.3
12421.4
12579.0
12736.7
12894.9
13053.2
13212.0
13371.0
13530.2
u
7431.1
7618.1
7806.4
7996.2
8187.0
8379.0
8572.3
8766.6
8962.1
9158.8
9356.5
9555.3
9755.0
9955.9
10157.7
10360.5
10564.5
10769.2
10974.8
11181.4
11388.9
11597.2
11806.4
12016.5
12227.3
12439.0
12651.6
12864.8
13078.9
13293.7
13509.2
13725.4
13942.4
14160.1
14378.4
14597.4
14816.9
15037.2
15258.2
15479.7
h
9575.8
9802.6
10030.6
10260.1
10490.6
10722.3
10955.3
11189.4
11424.6
11661.0
11898.4
12136.9
12376.4
12617.0
12858.5
13101.0
13344.7
13589.1
13834.5
14080.8
14328.0
14576.0
14824.9
15074.7
15325.3
15576.7
15829.0
16081.9
16335.7
16590.2
16845.5
17101.4
17358.1
17615.5
17873.5
18132.2
18391.5
18651.5
18912.2
19173.4
h
8768.2
8942.0
9116.4
9291.4
9467.1
9643.4
9820.4
9998.0
10176.1
10354.9
10534.4
10714.5
10895.3
11076.6
11258.7
11441.4
11624.8
11808.8
11993.4
12178.8
12364.8
12551.4
12738.8
12926.8
13115.6
13305.0
13494.4
13685.7
13877.0
14069.2
14261.9
14455.4
14649.5
14844.3
15039.8
15236.1
15433.0
15630.6
15828.7
16027.6
u
6623.5
6757.5
6892.2
7027.5
7163.5
7300.1
7437.4
7575.2
7713.6
7852.7
7992.5
8132.9
8274.0
8415.5
8557.9
8700.9
8844.6
8988.9
9133.8
9279.4
9425.7
9572.7
9720.3
9868.6
10017.6
10167.3
10317.6
10468.6
10620.2
10772.7
10925.6
11079.4
11233.8
11388.9
11544.7
11701.2
11858.4
12016.3
12174.7
12333.9
s°
50.854
51.013
51.171
51.325
51.478
51.630
51.777
51.925
52.070
52.212
52.354
52.494
52.631
52.768
52.903
53.037
53.168
53.299
53.428
53.556
53.682
53.808
53.932
54.055
54.117
54.298
54.418
54.535
54.653
54.770
54.886
54.999
55.113
55.226
55.339
55.449
55.559
55.668
55.777
55.884
Water Vapor, H2O
(h°f 104,040 Btu /lbmol)
u
5552.1
5665.9
5780.3
5895.2
6010.6
6126.5
6242.8
6359.6
6476.9
6594.5
6712.7
6831.3
6950.2
7069.6
7189.4
7309.6
7430.1
7551.1
7672.4
7793.9
7916.0
8038.3
8161.1
8284.2
8407.4
8531.1
8655.1
8779.5
8904.1
9029.0
9154.1
9279.6
9405.4
9531.5
9657.9
9784.4
9911.2
10038.2
10165.6
10293.1
s°
54.064
54.204
54.343
54.480
54.614
54.748
54.879
55.008
55.136
55.262
55.386
55.508
55.630
55.750
55.867
55.984
56.099
56.213
56.326
56.437
56.547
56.656
56.763
56.869
56.975
57.079
57.182
57.284
57.385
57.484
57.582
57.680
57.777
57.873
57.968
58.062
58.155
58.247
58.339
58.428
Oxygen, O2
(h°f 0 Btu /lbmol)
h
7696.8
7850.4
8004.5
8159.1
8314.2
8469.8
8625.8
8782.4
8939.4
9096.7
9254.6
9412.9
9571.6
9730.7
9890.2
10050.1
10210.4
10371.0
10532.0
10693.3
10855.1
11017.1
11179.6
11342.4
11505.4
11668.8
11832.5
11996.6
12160.9
12325.5
12490.4
12655.6
12821.1
12986.9
13153.0
13319.2
13485.8
13652.5
13819.6
13986.8
T(R), h and u(Btu/lbmol), s°(Btu/lbmol # R)
Carbon Monoxide, CO
(h°f 47,540 Btu/lbmol)
(Continued)
Carbon Dioxide, CO2
(h°f 169,300 Btu /lbmol)
TABLE A-23E
Copyright © 2006. Wiley. All rights reserved.
u
5406.2
5510.5
5615.2
5720.1
5825.4
5931.0
6037.0
6143.4
6250.1
6357.2
6464.5
6572.3
6680.4
6788.9
6897.8
7007.0
7116.7
7226.7
7337.0
7447.6
7558.7
7670.1
7781.9
7893.9
8006.4
8119.2
8232.3
8345.7
8459.6
8573.6
8688.1
8802.9
8918.0
9033.4
9149.2
9265.3
9381.7
9498.4
9615.5
9732.8
Table A-23E
h
7551.0
7695.0
7839.3
7984.0
8129.0
8274.4
8420.0
8566.1
8712.6
8859.3
9006.4
9153.9
9301.8
9450.0
9598.6
9747.5
9896.9
10046.6
10196.6
10347.0
10497.8
10648.0
10800.4
10952.2
11104.3
11256.9
11409.7
11562.8
11716.4
11870.2
12024.3
12178.9
12333.7
12488.8
12644.3
12800.2
12956.3
13112.7
13269.5
13426.5
s°
50.651
50.783
50.912
51.040
51.167
51.291
51.413
51.534
51.653
51.771
51.887
51.001
52.114
52.225
52.335
52.444
52.551
52.658
52.763
52.867
52.969
53.071
53.171
53.271
53.369
53.465
53.561
53.656
53.751
53.844
53.936
54.028
54.118
54.208
54.297
54.385
54.472
54.559
54.645
54.729
Nitrogen, N2
(h°f 0 Btu/lbmol)
1080
1100
1120
1140
1160
1180
1200
1220
1240
1260
1280
1300
1320
1340
1360
1380
1400
1420
1440
1460
1480
1500
1520
1540
1560
1580
1600
1620
1640
1660
1680
1700
1720
1740
1760
1780
1800
1820
1840
1860
T
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
810
T
1900
1940
1980
2020
2060
2100
2140
2180
2220
2260
2300
2340
2380
2420
2460
2500
2540
2580
2620
2660
2700
2740
2780
2820
2860
2900
2940
2980
3020
3060
3100
3140
3180
3220
3260
3300
3340
3380
3420
3460
s°
64.999
65.272
65.543
65.809
66.069
66.327
66.581
66.830
67.076
67.319
67.557
67.792
68.025
68.253
68.479
68.702
68.921
69.138
69.352
69.563
69.771
69.977
70.181
70.382
70.580
70.776
70.970
71.160
71.350
71.537
71.722
71.904
72.085
72.264
72.441
72.616
72.788
72.960
73.129
73.297
u
10,077
10,318
10,560
10,803
11,048
11,293
11,539
11,787
12,035
12,284
12,534
12,784
13,035
13,287
13,541
13,794
14,048
14,303
14,559
14,815
15,072
15,330
15,588
15,846
16,105
16,365
16,625
16,885
17,146
17,408
17,670
17,932
18,195
18,458
18,722
18,986
19,250
19,515
19,780
20,045
s°
56.509
56.677
56.841
57.007
57.161
57.317
57.470
57.621
57.770
57.917
58.062
58.204
58.344
58.482
58.619
58.754
58.885
59.016
59.145
59.272
59.398
59.521
59.644
59.765
59.884
60.002
60.118
60.232
60.346
60.458
60.569
60.679
60.787
60.894
61.000
61.105
61.209
61.311
61.412
61.513
h
13,850
14,170
14,492
14,815
15,139
15,463
15,789
16,116
16,443
16,722
17,101
17,431
17,762
18,093
18,426
18,759
19,093
19,427
19,762
20,098
20,434
20,771
21,108
21,446
21,785
22,124
22,463
22,803
23,144
23,485
23,826
24,168
24,510
24,853
25,196
25,539
25,883
26,227
26,572
26,917
u
15,925
16,372
16,821
17,273
17,727
18,182
18,640
19,101
19,561
20,024
20,489
20,955
21,423
21,893
22,364
22,837
23,310
23,786
24,262
24,740
25,220
25,701
26,181
26,664
27,148
27,633
28,118
28,605
29,093
29,582
30,072
30,562
31,054
31,546
32,039
32,533
33,028
33,524
34,020
34,517
h
19,698
20,224
20,753
21,284
21,818
22,353
22,890
23,429
23,970
24,512
25,056
25,602
26,150
26,699
27,249
27,801
28,355
28,910
29,465
30,023
30,581
31,141
31,702
32,264
32,827
33,392
33,957
34,523
35,090
35,659
36,228
36,798
37,369
37,941
38,513
39,087
39,661
40,236
40,812
41,338
h
16,428
16,830
17,235
17,643
18,054
18,467
18,883
19,301
19,722
20,145
20,571
20,999
21,429
21,862
22,298
22,735
23,175
23,618
24,062
24,508
24,957
25,408
25,861
26,316
26,773
27,231
27,692
28,154
28,619
29,085
29,553
30,023
30,494
30,967
31,442
31,918
32,396
32,876
33,357
33,839
u
12,654
12,977
13,303
13,632
13,963
14,297
14,633
14,972
15,313
15,657
16,003
16,352
16,703
17,057
17,413
17,771
18,131
18,494
18,859
19,226
19,595
19,967
20,340
20,715
21,093
21,472
21,853
22,237
22,621
23,085
23,397
23,787
24,179
24,572
24,968
25,365
25,763
26,164
26,565
26,968
s°
56.097
56.307
56.514
56.719
56.920
57.119
57.315
57.509
57.701
57.889
58.077
58.261
58.445
58.625
58.803
58.980
59.155
59.328
59.500
59.669
59.837
60.003
60.167
60.330
60.490
60.650
60.809
60.965
61.120
61.274
61.426
61.577
61.727
61.874
62.022
62.167
62.312
62.454
62.597
62.738
Water Vapor, H2O
(h°f 104,040 Btu /lbmol)
u
10,549
10,806
11,063
11,321
11,581
11,841
12,101
12,363
12,625
12,888
13,151
13,416
13,680
13,946
14,212
14,479
14,746
15,014
15,282
15,551
15,821
16,091
16,362
16,633
16,905
17,177
17,450
17,723
17,997
18,271
18,546
18,822
19,098
19,374
19,651
19,928
20,206
20,485
20,763
21,043
s°
58.607
58.782
58.954
59.123
59.289
59.451
59.612
59.770
59.926
60.077
60.228
60.376
60.522
60.666
60.808
60.946
61.084
61.220
61.354
61.486
61.616
61.744
61.871
61.996
62.120
62.242
62.363
62.483
62.599
62.716
62.831
62.945
63.057
63.169
63.279
63.386
63.494
63.601
63.706
63.811
Oxygen, O2
(h°f 0 Btu /lbmol)
h
14,322
14,658
14,995
15,333
15,672
16,011
16,351
16,692
17,036
17,376
17,719
18,062
18,407
18,572
19,097
19,443
19,790
20,138
20,485
20,834
21,183
21,533
21,883
22,232
22,584
22,936
23,288
23,641
23,994
24,348
24,703
25,057
25,413
25,769
26,175
26,412
26,839
27,197
27,555
27,914
T(R), h and u(Btu/lbmol), s°(Btu/lbmol # R)
Carbon Monoxide, CO
(h°f 47,540 Btu/lbmol)
(Continued )
Carbon Dioxide, CO2
(h°f 169,300 Btu /lbmol)
TABLE A-23E
Copyright © 2006. Wiley. All rights reserved.
h
13,742
14,058
14,375
14,694
15,013
15,334
15,656
15,978
16,302
16,626
16,951
17,277
17,604
17,932
18,260
18,590
18,919
19,250
19,582
19,914
20,246
20,580
20,914
21,248
21,584
21,920
22,256
22,593
22,930
23,268
23,607
23,946
24,285
24,625
24,965
25,306
25,647
25,989
26,331
26,673
u
9,968
10,205
10,443
10,682
10,923
11,164
11,406
11,649
11,893
12,138
12,384
12,630
12,878
13,126
13,375
13,625
13,875
14,127
14,379
14,631
14,885
15,139
15,393
15,648
15,905
16,161
16,417
16,675
16,933
17,192
17,451
17,710
17,970
18,231
18,491
18,753
19,014
19,277
19,539
19,802
s°
54.896
55.061
55.223
55.383
55.540
55.694
55.846
55.995
56.141
56.286
56.429
56.570
56.708
56.845
56.980
57.112
57.243
57.372
57.499
57.625
57.750
57.872
57.993
58.113
58.231
58.348
58.463
58.576
58.688
58.800
58.910
59.019
59.126
59.232
59.338
59.442
59.544
59.646
59.747
59.846
Nitrogen, N2
(h°f 0 Btu/lbmol)
Table A-23E
T
1900
1940
1980
2020
2060
2100
2140
2180
2220
2260
2300
2340
2380
2420
2460
2500
2540
2580
2620
2660
2700
2740
2780
2820
2860
2900
2940
2980
3020
3060
3100
3140
3180
3220
3260
3300
3340
3380
3420
3460
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
811
T
3500
3540
3580
3620
3660
3700
3740
3780
3820
3860
3900
3940
3980
4020
4060
4100
4140
4180
4220
4260
4300
4340
4380
4420
4460
4500
4540
4580
4620
4660
4700
4740
4780
4820
4860
4900
5000
5100
5200
5300
s°
73.462
73.627
73.789
73.951
74.110
74.267
74.423
74.578
74.732
74.884
75.033
75.182
75.330
75.477
75.622
75.765
75.907
76.048
76.188
76.327
76.464
76.601
76.736
76.870
77.003
77.135
77.266
77.395
77.581
77.652
77.779
77.905
78.029
78.153
78.276
78.398
78.698
78.994
79.284
79.569
u
20,311
20,576
20,844
21,111
21,378
21,646
21,914
22,182
22,450
22,719
22,988
23,257
23,527
23,797
24,067
24,337
24,608
24,878
25,149
25,421
25,692
25,934
26,235
26,508
26,780
27,052
27,325
27,598
27,871
28,144
28,417
28,691
28,965
29,239
29,513
29,787
30,473
31,161
31,849
32,538
s°
61.612
61.710
61.807
61.903
61.998
62.093
62.186
62.279
62.370
62.461
61.511
62.640
62.728
62.816
62.902
62.988
63.072
63.156
63.240
63.323
63.405
63.486
63.567
63.647
63.726
63.805
63.883
63.960
64.036
64.113
64.188
64.263
64.337
64.411
64.484
64.556
64.735
64.910
65.082
65.252
h
27,262
27,608
27,954
28,300
28,647
28,994
29,341
29,688
30,036
30,384
30,733
31,082
31,431
31,780
32,129
32,479
32,829
33,179
33,530
33,880
34,231
34,582
34,934
35,285
35,637
35,989
36,341
36,693
37,046
37,398
37,751
38,104
38,457
38,811
39,164
39,518
40,403
41,289
42,176
43,063
u
35,015
35,513
36,012
36,512
37,012
37,513
38,014
38,517
39,019
39,522
40,026
40,531
41,035
41,541
42,047
42,553
43,060
43,568
44,075
44,584
45,093
45,602
46,112
46,622
47,133
47,645
48,156
48,668
49,181
49,694
50,208
50,721
51,236
51,750
52,265
52,781
54,071
55,363
56,658
57,954
h
41,965
42,543
43,121
43,701
44,280
44,861
45,442
46,023
46,605
47,188
47,771
48,355
48,939
49,524
50,109
50,695
51,282
51,868
52,456
53,044
53,632
54,221
54,810
55,400
55,990
56,581
57,172
57,764
58,356
58,948
59,541
60,134
60,728
61,322
61,916
62,511
64,000
65,491
66,984
68,471
h
34,324
34,809
35,296
35,785
36,274
36,765
37,258
37,752
38,247
38,743
39,240
39,739
40,239
40,740
41,242
41,745
42,250
42,755
43,267
43,769
44,278
44,788
45,298
45,810
46,322
46,836
47,350
47,866
48,382
48,899
49,417
49,936
50,455
50,976
51,497
52,019
53,327
54,640
55,957
57,279
u
27,373
27,779
28,187
28,596
29,006
29,418
29,831
30,245
30,661
31,077
31,495
31,915
32,335
32,757
33,179
33,603
34,028
34,454
34,881
35,310
35,739
36,169
36,600
37,032
37,465
37,900
38,334
38,770
39,207
39,645
40,083
40,523
40,963
41,404
41,856
42,288
43,398
44,512
45,631
46,754
s°
62.875
63.015
63.153
63.288
63.423
63.557
63.690
63.821
63.952
64.082
64.210
64.338
64.465
64.591
64.715
64.839
64.962
65.084
65.204
65.325
65.444
65.563
65.680
65.797
65.913
66.028
66.142
66.255
66.368
66.480
66.591
66.701
66.811
66.920
67.028
67.135
67.401
67.662
67.918
68.172
Water Vapor, H2O
(h°f 104,040 Btu/lbmol)
u
21,323
21,603
21,884
22,165
22,447
22,730
23,013
23,296
23,580
23,864
24,149
24,434
24,720
25,006
25,292
25,580
25,867
26,155
26,444
26,733
27,022
27,312
27,602
27,823
28,184
28,475
28,768
29,060
29,353
29,646
29,940
30,234
30,529
30,824
31,120
31,415
32,157
32,901
33,648
34,397
s°
63.914
64.016
64.114
64.217
64.316
64.415
64.512
64.609
64.704
64.800
64.893
64.986
65.078
65.169
65.260
65.350
64.439
65.527
65.615
65.702
65.788
65.873
65.958
66.042
66.125
66.208
66.290
66.372
66.453
66.533
66.613
66.691
66.770
66.848
66.925
67.003
67.193
67.380
67.562
67.743
Oxygen, O2
(h°f 0 Btu/lbmol)
h
28,273
28,633
28,994
29,354
29,716
30,078
30,440
30,803
31,166
31,529
31,894
32,258
32,623
32,989
33,355
33,722
34,089
34,456
34,824
35,192
35,561
35,930
36,300
36,670
37,041
37,412
37,783
38,155
38,528
38,900
39,274
39,647
40,021
40,396
40,771
41,146
42,086
43,021
43,974
44,922
T(R), h and u(Btu/lbmol), s°(Btu/lbmol # R)
Carbon Monoxide, CO
(h°f 47,540 Btu/lbmol)
(Continued)
Carbon Dioxide, CO2
(h°f 169,300 Btu /lbmol)
TABLE A-23E
Copyright © 2006. Wiley. All rights reserved.
u
20,065
20,329
20,593
20,858
21,122
21,387
21,653
21,919
22,185
22,451
22,718
22,985
23,252
23,520
23,788
24,056
24,324
24,593
24,862
25,131
25,401
25,670
25,940
26,210
26,481
26,751
27,022
27,293
27,565
27,836
28,108
28,379
28,651
28,924
29,196
29,468
30,151
30,834
31,518
32,203
Table A-23E
h
27,016
27,359
27,703
28,046
28,391
28,735
29,080
29,425
29,771
30,117
30,463
30,809
31,156
31,503
31,850
32,198
32,546
32,894
33,242
33,591
33,940
34,289
34,638
34,988
35,338
35,688
36,038
36,389
36,739
37,090
37,441
37,792
38,144
38,495
38,847
39,199
40,080
40,962
41,844
42,728
s°
59.944
60.041
60.138
60.234
60.328
60.422
60.515
60.607
60.698
60.788
60.877
60.966
61.053
61.139
61.225
61.310
61.395
61.479
61.562
61.644
61.726
61.806
61.887
61.966
62.045
62.123
62.201
62.278
62.354
62.429
62.504
62.578
62.652
62.725
62.798
62.870
63.049
63.223
63.395
63.563
Nitrogen, N2
(h°f 0 Btu /lbmol)
T
3500
3540
3580
3620
3660
3700
3740
3780
3820
3860
3900
3940
3980
4020
4060
4100
4140
4180
4220
4260
4300
4340
4380
4420
4460
4500
4540
4580
4620
4660
4700
4740
4780
4820
4860
4900
5000
5100
5200
5300
812
Tables in English Units
TABLE A-24E
Constants for the van der Waals, Redlich–Kwong, and Benedict–Webb–Rubin Equations of State
1. van der Waals and Redlich–Kwong: Constants for pressure in atm, specific volume in ft3/lbmol, and temperature in R
van der Waals
a
ft3 2
atm a
b
lbmol
b
ft3
lbmol
a
ft3 2
atm a
b 1°R2 12
lbmol
b
ft3
lbmol
Air
Butane (C4H10)
Carbon dioxide (CO2)
345
3,509
926
0.586
1.862
0.686
5,409
98,349
21,972
0.4064
1.2903
0.4755
Carbon monoxide (CO)
Methane (CH4)
Nitrogen (N2)
372
581
346
0.632
0.685
0.618
5,832
10,919
5,280
0.4382
0.4751
0.4286
Oxygen (O2)
Propane (C3H8)
Refrigerant 12
349
2,369
2,660
0.509
1.444
1.558
5,896
61,952
70,951
0.3531
1.0006
1.0796
Sulfur dioxide (SO2)
Water (H2O)
1,738
1,400
0.910
0.488
49,032
48,418
0.6309
0.3380
Substance
Table A-24E
Redlich–Kwong
Source: Calculated from critical data.
2. Benedict–Webb–Rubin: Constants for pressure in atm, specific volume in ft3/lbmol, and temperature in R
Substance
a
A
b
B
c
C
C4H10
CO2
CO
7736.7
562.3
150.6
2587.6
702.4
344.1
10.26
1.850
0.675
1.9921
0.7995
0.8737
4.214 10
1.987 108
1.385 107
8.254 10
1.152 108
7.118 106
4.527
0.348
0.555
8.724
1.384
1.540
CH4
N2
203.0
103.2
476.0
270.4
0.867
0.597
0.6824
0.6526
3.389 107
9.700 106
1.876 107
6.700 106
0.511
0.523
1.540
1.360
Copyright © 2006. Wiley. All rights reserved.
Source: H. W. Cooper and J. C. Goldfrank, Hydrocarbon Processing, 46 (12): 141 (1967).
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
9
8
Tables in English Units
TABLE A-25E
813
Thermochemical Properties of Selected Substances at 537R and 1 atm
Enthalpy of
Formation, h°f
(Btu/lbmol)
Gibbs Function
of Formation,
g°f (Btu/lbmol)
Absolute
Entropy, s°
(Btu/lbmol # R)
Higher,
HHV
(Btu/lb)
Lower,
LHV
(Btu/lb)
Substance
Formula
Molar Mass,
M (lb/lbmol)
Carbon
Hydrogen
Nitrogen
Oxygen
C(s)
H2(g)
N2(g)
O2(g)
12.01
2.016
28.01
32.00
0
0
0
0
0
0
0
0
1.36
31.19
45.74
48.98
14,100
61,000
—
—
14,100
51,610
—
—
Carbon monoxide
Carbon dioxide
Water
Water
CO(g)
CO2(g)
H2O(g)
H2O(l)
28.01
44.01
18.02
18.02
47,540
169,300
104,040
122,970
59,010
169,680
98,350
102,040
47.27
51.03
45.08
16.71
—
—
—
—
—
—
—
—
Hydrogen peroxide
Ammonia
Oxygen
Hydrogen
H2O2(g)
NH3(g)
O(g)
H(g)
34.02
17.03
16.00
1.008
58,640
19,750
107,210
93,780
45,430
7,140
99,710
87,460
55.60
45.97
38.47
27.39
—
—
—
—
—
—
—
—
Nitrogen
Hydroxyl
Methane
Acetylene
N(g)
OH(g)
CH4(g)
C2H2(g)
14.01
17.01
16.04
26.04
203,340
16,790
32,210
97,540
195,970
14,750
21,860
87,990
36.61
43.92
44.49
48.00
—
—
23,880
21,470
—
—
21,520
20,740
Ethylene
Ethane
Propylene
Propane
C2H4(g)
C2H6(g)
C3H6(g)
C3H8(g)
28.05
30.07
42.08
44.09
22,490
36,420
8,790
44,680
29,306
14,150
26,980
10,105
52.54
54.85
63.80
64.51
21,640
22,320
21,050
21,660
20,290
20,430
19,700
19,950
Butane
Pentane
Octane
Octane
Benzene
C4H10(g)
C5H12(g)
C8H18(g)
C8H18(l)
C6H6(g)
58.12
72.15
114.22
114.22
78.11
54,270
62,960
89,680
107,530
35,680
6,760
3,530
7,110
2,840
55,780
74.11
83.21
111.55
86.23
64.34
21,300
21,090
20,760
20,610
18,180
19,670
19,510
19,270
19,110
17,460
Methyl alcohol
Methyl alcohol
Ethyl alcohol
Ethyl alcohol
CH3OH(g)
CH3OH(l)
C2H5OH(g)
C2H5OH(l)
32.04
32.04
46.07
46.07
86,540
102,670
101,230
119,470
69,700
71,570
72,520
75,240
57.29
30.30
67.54
38.40
10,260
9,760
13,160
12,760
9,080
8,570
11,930
11,530
Copyright © 2006. Wiley. All rights reserved.
Source: Based on JANAF Thermochemical Tables, NSRDS-NBS-37, 1971; Selected Values of Chemical Thermodynamic Properties, NBS Tech.
Note 270-3, 1968; and API Research Project 44, Carnegie Press, 1953. Heating values calculated.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Table A-25E
Heating Values
Index to Figures and Charts
Figure A-1
Figure A-2
Figure A-3
Figure A-4
Figure A-5
Figure A-6
Figure A-7
Figure A-8
814
815
815
816
817
818
819
820
821
Copyright © 2006. Wiley. All rights reserved.
Figure A-9
Generalized compressibility chart, pR 1.0
Generalized compressibility chart, pR 10.0
Generalized compressibility chart, 10 pR 40
Generalized enthalpy correction chart
Generalized entropy correction chart
Generalized fugacity coefficient chart
Temperature–entropy diagram for water (SI units)
Enthalpy–entropy diagram for water (SI units)
Psychrometric chart for 1 atm (SI units)
Generalized compressibility chart, pR
Thermodynamics, McGraw-Hill, New York, 1960.
Figure A-1
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
814
1.0. Source: E. F. Obert, Concepts of
Figures and Charts
Generalized compressibility chart, pR
Thermodynamics, McGraw-Hill, New York, 1960.
10.0. Source: E. F. Obert, Concepts of
Copyright © 2006. Wiley. All rights reserved.
Figure A-2
Figure A-3 Generalized compressibility chart, 10
Thermodynamics, McGraw-Hill, New York, 1960.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
pR
40. Source: E. F. Obert. Concepts of
815
Copyright © 2006. Wiley. All rights reserved.
816
Figures and Charts
Figure A-4 Generalized enthalpy correction chart. Source: Adapted from G. J. Van Wylen
and R. E. Sonntag, Fundamentals of Classical Thermodynamics, 3rd. ed., English/SI, Wiley,
New York, 1986.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Copyright © 2006. Wiley. All rights reserved.
Figures and Charts
Generalized entropy correction chart. Source: Adapted from G. J. Van
Wylen and R. E. Sonntag, Fundamentals of Classical Thermodynamics, 3rd. ed.,
English/SI, Wiley, New York, 1986.
Figure A-5
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
817
818
Figures and Charts
Generalized fugacity coefficient chart. Source: G. J. Van Wylen and R. E. Sonntag,
Fundamentals of Classical Thermodynamics, 3rd. ed., English/SI, Wiley, New York, 1986.
Copyright © 2006. Wiley. All rights reserved.
Figure A-6
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Copyright © 2006. Wiley. All rights reserved.
Figures and Charts
Figure A-7
Temperature–entropy diagram for water (SI units). Source: J. H. Keenan, F. G. Keyes,
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
P. G. Hill, and J. G. Moore, Steam Tables, Wiley, New York, 1978.
Created from purdue on 2022-01-24 17:56:53.
819
Copyright © 2006. Wiley. All rights reserved.
820
Figures and Charts
Figure A-8 Enthalpy–entropy diagram for water (SI units). Source: J. B. Jones and G. A.
Hawkins, Engineering Thermodynamics, 2nd ed., Wiley, New York, 1986.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
Copyright © 2006. Wiley. All rights reserved.
Figures and Charts
Figure A-9 Psychrometric chart for 1 atm (SI units). Source: Z. Zhang and M. B. Pate, “A
Methodology for Implementing a Psychrometric Chart in a Computer Graphics System,” ASHRAE
Transactions, Vol. 94, Pt. 1, 1988.
Moran, M. J., & Shapiro, H. N. (2006). Fundamentals of engineering thermodynamics. Wiley.
Created from purdue on 2022-01-24 17:56:53.
821