Properes of Saturated Steam - Pressure in Bar
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Properties of Saturated Steam - Pressure in Bar
The Saturated Steam Table with properties as boiling point, specific volume, density,
specific enthalpy, specific heat and latent heat of vaporization
Specific enthalpy Specific enthalpy
Specific
Density
Absolute Boiling
of liquid water
of steam
volume
(steam)
pressure point
(sensible heat)
(total heat)
(steam)
Latent heat of
evaporization
Specific
heat
(bar)
(oC)
(m3/kg) (kg/m3) (kJ/kg) (kcal/kg) (kJ/kg) (kcal/kg) (kJ/kg) (kcal/kg)
(kJ/kg
K)
0.02
17.51
67.006
0.015
73.45
17.54
2533.64 605.15 2460.19 587.61
1.8644
0.03
24.10
45.667
0.022
101.00
24.12
2545.64 608.02 2444.65 583.89
1.8694
0.04
28.98
34.802
0.029
121.41
29.00
2554.51 610.13 2433.10 581.14
1.8736
0.05
32.90
28.194
0.035
137.77
32.91
2561.59 611.83 2423.82 578.92
1.8774
0.06
36.18
23.741
0.042
151.50
36.19
2567.51 613.24 2416.01 577.05
1.8808
0.07
39.02
20.531
0.049
163.38
39.02
2572.62 614.46 2409.24 575.44
1.8840
0.08
41.53
18.105
0.055
173.87
41.53
2577.11 615.53 2403.25 574.01
1.8871
0.09
43.79
16.204
0.062
183.28
43.78
2581.14 616.49 2397.85 572.72
1.8899
0.1
45.83
14.675
0.068
191.84
45.82
2584.78 617.36 2392.94 571.54
1.8927
0.2
60.09
7.650
0.131
251.46
60.06
2609.86 623.35 2358.40 563.30
1.9156
0.3
69.13
5.229
0.191
289.31
69.10
2625.43 627.07 2336.13 557.97
1.9343
0.4
75.89
3.993
0.250
317.65
75.87
2636.88 629.81 2319.23 553.94
1.9506
0.5
81.35
3.240
0.309
340.57
81.34
2645.99 631.98 2305.42 550.64
1.9654
0.6
85.95
2.732
0.366
359.93
85.97
2653.57 633.79 2293.64 547.83
1.9790
0.7
89.96
2.365
0.423
376.77
89.99
2660.07 635.35 2283.30 545.36
1.9919
0.8
93.51
2.087
0.479
391.73
93.56
2665.77 636.71 2274.05 543.15
2.0040
0.9
96.71
1.869
0.535
405.21
96.78
2670.85 637.92 2265.65 541.14
2.0156
99.63
1.694
0.590
417.51
99.72
2675.43 639.02 2257.92 539.30
2.0267
1.1
102.32
1.549
0.645
428.84
102.43 2679.61 640.01 2250.76 537.59
2.0373
1.2
104.81
1.428
0.700
439.36
104.94 2683.44 640.93 2244.08 535.99
2.0476
1.3
107.13
1.325
0.755
449.19
107.29 2686.98 641.77 2237.79 534.49
2.0576
1.4
109.32
1.236
0.809
458.42
109.49 2690.28 642.56 2231.86 533.07
2.0673
1.5
111.37
1.159
0.863
467.13
111.57
2693.36 643.30 2226.23 531.73
2.0768
1.5
111.37
1.159
0.863
467.13
111.57
2693.36 643.30 2226.23 531.73
2.0768
1.6
113.32
1.091
0.916
475.38
113.54 2696.25 643.99 2220.87 530.45
2.0860
1.7
115.17
1.031
0.970
483.22
115.42 2698.97 644.64 2215.75 529.22
2.0950
1.8
116.93
0.977
1.023
490.70
117.20 2701.54 645.25 2210.84 528.05
2.1037
1.9
118.62
0.929
1.076
497.85
118.91 2703.98 645.83 2206.13 526.92
2.1124
120.23
0.885
1.129
504.71
120.55 2706.29 646.39 2201.59 525.84
2.1208
2.2
123.27
0.810
1.235
517.63
123.63 2710.60 647.42 2192.98 523.78
2.1372
2.4
126.09
0.746
1.340
529.64
126.50 2714.55 648.36 2184.91 521.86
2.1531
2.6
128.73
0.693
1.444
540.88
129.19 2718.17 649.22 2177.30 520.04
2.1685
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Properes of Saturated Steam - Pressure in Bar
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Specific
Specific enthalpy Specific enthalpy
Absolute Boiling
Density
volume
of liquid water
of steam
pressure point
(steam)
(steam)
(sensible heat)
(total heat)
Latent heat of
evaporization
Specific
heat
(bar)
(oC)
2.8
131.20
0.646
1.548
551.45
131.71 2721.54 650.03 2170.08 518.32
(kJ/kg
K)
2.1835
133.54
0.606
1.651
561.44
134.10 2724.66 650.77 2163.22 516.68
2.1981
3.5
138.87
0.524
1.908
584.28
139.55 2731.63 652.44 2147.35 512.89
2.2331
143.63
0.462
2.163
604.68
144.43 2737.63 653.87 2132.95 509.45
2.2664
4.5
147.92
0.414
2.417
623.17
148.84 2742.88 655.13 2119.71 506.29
2.2983
151.85
0.375
2.669
640.12
152.89 2747.54 656.24 2107.42 503.35
2.3289
5.5
155.47
0.342
2.920
655.81
156.64 2751.70 657.23 2095.90 500.60
2.3585
158.84
0.315
3.170
670.43
160.13 2755.46 658.13 2085.03 498.00
2.3873
6.5
161.99
0.292
3.419
684.14
163.40 2758.87 658.94 2074.73 495.54
2.4152
164.96
0.273
3.667
697.07
166.49 2761.98 659.69 2064.92 493.20
2.4424
7.5
167.76
0.255
3.915
709.30
169.41 2764.84 660.37 2055.53 490.96
2.4690
170.42
0.240
4.162
720.94
172.19 2767.46 661.00 2046.53 488.80
2.4951
8.5
172.94
0.227
4.409
732.03
174.84 2769.89 661.58 2037.86 486.73
2.5206
175.36
0.215
4.655
742.64
177.38 2772.13 662.11 2029.49 484.74
2.5456
9.5
177.67
0.204
4.901
752.82
179.81 2774.22 662.61 2021.40 482.80
2.5702
10
179.88
0.194
5.147
762.60
182.14 2776.16 663.07 2013.56 480.93
2.5944
11
184.06
0.177
5.638
781.11
186.57 2779.66 663.91 1998.55 477.35
2.6418
12
187.96
0.163
6.127
798.42
190.70 2782.73 664.64 1984.31 473.94
2.6878
13
191.60
0.151
6.617
814.68
194.58 2785.42 665.29 1970.73 470.70
2.7327
14
195.04
0.141
7.106
830.05
198.26 2787.79 665.85 1957.73 467.60
2.7767
15
198.28
0.132
7.596
844.64
201.74 2789.88 666.35 1945.24 464.61
2.8197
16
201.37
0.124
8.085
858.54
205.06 2791.73 666.79 1933.19 461.74
2.8620
17
204.30
0.117
8.575
871.82
208.23 2793.37 667.18 1921.55 458.95
2.9036
18
207.11
0.110
9.065
884.55
211.27 2794.81 667.53 1910.27 456.26
2.9445
19
209.79
0.105
9.556
896.78
214.19 2796.09 667.83 1899.31 453.64
2.9849
20
212.37
0.100
10.047 908.56
217.01 2797.21 668.10 1888.65 451.10
3.0248
21
214.85
0.095
10.539 919.93
219.72 2798.18 668.33 1878.25 448.61
3.0643
22
217.24
0.091
11.032
930.92
222.35 2799.03 668.54 1868.11 446.19
3.1034
23
219.55
0.087
11.525
941.57
224.89 2799.77 668.71 1858.20 443.82
3.1421
24
221.78
0.083
12.020 951.90
227.36 2800.39 668.86 1848.49 441.50
3.1805
25
223.94
0.080
12.515 961.93
229.75 2800.91 668.99 1838.98 439.23
3.2187
26
226.03
0.077
13.012 971.69
232.08 2801.35 669.09 1829.66 437.01
3.2567
27
228.06
0.074
13.509 981.19
234.35 2801.69 669.17 1820.50 434.82
3.2944
28
230.04
0.071
14.008 990.46
236.57 2801.96 669.24 1811.50 432.67
3.3320
29
231.96
0.069
14.508 999.50
238.73 2802.15 669.28 1802.65 430.56
3.3695
30
233.84
0.067
15.009 1008.33 240.84 2802.27 669.31 1793.94 428.48
3.4069
(m3/kg) (kg/m3) (kJ/kg) (kcal/kg) (kJ/kg) (kcal/kg) (kJ/kg) (kcal/kg)
Example - Boiling Water at 100 oC, 0 bar Atmospheric Pressure
At atmospheric pressure (0 bar g, absolute 1 bar ), water boils at 100 oC, and 417.51 kJ of energy are required
to heat 1 kg of water from 0 oC to its evaporating temperature of 100 oC.
Therefore the specific enthalpy of water at 0 bar g (absolute 1 bar ) and 100 oC is 417.51 kJ/kg, as shown in th
table.
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Properes of Saturated Steam - Pressure in Bar
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Another 2257.92 kJ of energy are required to evaporate 1 kg of water at 100 oC into 1 kg of steam at 100 oC.
Therefore at 0 bar g (absolute 1 bar) the specific enthalpy of evaporation is 2257.19 kJ/kg, as shown in the
table.
Total specific enthalpy for steam:
hs = (417.51 kJ/kg) + (2257.92 kJ/kg)
= 2675.43 kJ/kg
Example - Boiling Water at 170 oC, 7 bar Atmospheric Pressure
Steam at atmospheric pressure is of a limited practical use because it cannot be conveyed under its own
pressure along a steam pipe to the point of use.
At 7 bar g (absolute 8 bar), the saturation temperature of water is 170.42 oC. More heat energy is required to
raise its temperature to saturation point at 7 bar g than would be needed if the water were at atmospheric
pressure. The table gives a value of 720.94 kJ to raise 1 kg of water from 0 oC to its saturation temperature of
170 oC.
The heat energy (enthalpy of evaporation) needed by the water at 7 bar g to change it into steam is actually les
than the heat energy required at atmospheric pressure. This is because the specific enthalpy of evaporation
decreases as the steam pressure increases. The evaporation heat is 2046.53 kJ/kg according the table.
Note! Because the specific volume also decreases with increasing pressure, the amount of heat energy
transferred in the same volume actually increases with steam pressure.
Related Topics
Steam and Condensate - Steam & condensate properties - capacities, pipe sizing, systems
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