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The steam table below list the properties of steam at varying pressures and temperatures:
| Absolute pressure (kPa, kN/m2) |
Temperature (oC) |
Specific Volume (m3/kg) |
Density - ρ - (kg/m3) |
Specific Enthalpy of | Specific Entropy of Steam - s - (kJ/kgK) |
||
| Liquid - hl - (kJ/kg) |
Evaporation - he - (kJ/kg) |
Steam - hs - (kJ/kg) |
|||||
| 0.8 | 3.8 | 160 | 0.00626 | 15.8 | 2493 | 2509 | 9.058 |
| 2.0 | 17.5 | 67.0 | 0.0149 | 73.5 | 2460 | 2534 | 8.725 |
| 5.0 | 32.9 | 28.2 | 0.0354 | 137.8 | 2424 | 2562 | 8.396 |
| 10.0 | 45.8 | 14.7 | 0.0682 | 191.8 | 2393 | 2585 | 8.151 |
| 20.0 | 60.1 | 7.65 | 0.131 | 251.5 | 2358 | 2610 | 7.909 |
| 28 | 67.5 | 5.58 | 0.179 | 282.7 | 2340 | 2623 | 7.793 |
| 35 | 72.7 | 4.53 | 0.221 | 304.3 | 2327 | 2632 | 7.717 |
| 45 | 78.7 | 3.58 | 0.279 | 329.6 | 2312 | 2642 | 7.631 |
| 55 | 83.7 | 2.96 | 0.338 | 350.6 | 2299 | 2650 | 7.562 |
| 65 | 88.0 | 2.53 | 0.395 | 368.6 | 2288 | 2657 | 7.506 |
| 75 | 91.8 | 2.22 | 0.450 | 384.5 | 2279 | 2663 | 7.457 |
| 85 | 95.2 | 1.97 | 0.507 | 398.6 | 2270 | 2668 | 7.415 |
| 95 | 98.2 | 1.78 | 0.563 | 411.5 | 2262 | 2673 | 7.377 |
| 100 | 99.6 | 1.69 | 0.590 | 417.5 | 2258 | 2675 | 7.360 |
| 101.33 | 100 | 1.67 | 0.598 | 419.1 | 2257 | 2676 | 7.355 |
| 110 | 102.3 | 1.55 | 0.646 | 428.8 | 2251 | 2680 | 7.328 |
| 130 | 107.1 | 1.33 | 0.755 | 449.2 | 2238 | 2687 | 7.271 |
| 150 | 111.4 | 1.16 | 0.863 | 467.1 | 2226 | 2698 | 7.223 |
| 170 | 115.2 | 1.03 | 0.970 | 483.2 | 2216 | 2699 | 7.181 |
| 190 | 118.6 | 0.929 | 1.08 | 497.8 | 2206 | 2704 | 7.144 |
| 220 | 123.3 | 0.810 | 1.23 | 517.6 | 2193 | 2711 | 7.095 |
| 260 | 128.7 | 0.693 | 1.44 | 540.9 | 2177 | 2718 | 7.039 |
| 280 | 131.2 | 0.646 | 1.55 | 551.4 | 2170 | 2722 | 7.014 |
| 320 | 135.8 | 0.570 | 1.75 | 570.9 | 2157 | 2728 | 6.969 |
| 360 | 139.9 | 0.510 | 1.96 | 588.5 | 2144 | 2733 | 6.930 |
| 400 | 143.1 | 0.462 | 2.16 | 604.7 | 2133 | 2738 | 6.894 |
| 440 | 147.1 | 0.423 | 2.36 | 619.6 | 2122 | 2742 | 6.862 |
| 480 | 150.3 | 0.389 | 2.57 | 633.5 | 2112 | 2746 | 6.833 |
| 500 | 151.8 | 0.375 | 2.67 | 640.1 | 2107 | 2748 | 6.819 |
| 550 | 155.5 | 0.342 | 2.92 | 655.8 | 2096 | 2752 | 6.787 |
| 600 | 158.8 | 0.315 | 3.175 | 670.4 | 2085 | 2756 | 6.758 |
| 650 | 162.0 | 0.292 | 3.425 | 684.1 | 2075 | 2759 | 6.730 |
| 700 | 165.0 | 0.273 | 3.66 | 697.1 | 2065 | 2762 | 6.705 |
| 750 | 167.8 | 0.255 | 3.915 | 709.3 | 2056 | 2765 | 6.682 |
| 800 | 170.4 | 0.240 | 4.16 | 720.9 | 2047 | 2768 | 6.660 |
| 850 | 172.9 | 0.229 | 4.41 | 732.0 | 2038 | 2770 | 6.639 |
| 900 | 175.4 | 0.215 | 4.65 | 742.6 | 2030 | 2772 | 6.619 |
| 950 | 177.7 | 0.204 | 4.90 | 752.8 | 2021 | 2774 | 6.601 |
| 1000 | 179.9 | 0.194 | 5.15 | 762.6 | 2014 | 2776 | 6.583 |
| 1050 | 182.0 | 0.186 | 5.39 | 772 | 2006 | 2778 | 6.566 |
| 1150 | 186.0 | 0.170 | 5.89 | 790 | 1991 | 2781 | 6.534 |
| 1250 | 189.8 | 0.157 | 6.38 | 807 | 1977 | 2784 | 6.505 |
| 1300 | 191.6 | 0.151 | 6.62 | 815 | 1971 | 2785 | 6.491 |
| 1500 | 198.3 | 0.132 | 7.59 | 845 | 1945 | 2790 | 6.441 |
| 1600 | 201.4 | 0.124 | 8.03 | 859 | 1933 | 2792 | 6.418 |
| 1800 | 207.1 | 0.110 | 9.07 | 885 | 1910 | 2795 | 6.375 |
| 2000 | 212.4 | 0.0995 | 10.01 | 909 | 1889 | 2797 | 6.337 |
| 2100 | 214.9 | 0.0945 | 10.54 | 920 | 1878 | 2798 | 6.319 |
| 2300 | 219.6 | 0.0868 | 11.52 | 942 | 1858 | 2800 | 6.285 |
| 2400 | 221.8 | 0.0832 | 12.02 | 952 | 1849 | 2800 | 6.269 |
| 2600 | 226.0 | 0.0769 | 13.01 | 972 | 1830 | 2801 | 6.239 |
| 2700 | 228.1 | 0.0740 | 13.52 | 981 | 1821 | 2802 | 6.224 |
| 2900 | 232.0 | 0.0689 | 14.52 | 1000 | 1803 | 2802 | 6.197 |
| 3000 | 233.8 | 0.0666 | 15.00 | 1008 | 1794 | 2802 | 6.184 |
| 3200 | 237.4 | 0.0624 | 16.02 | 1025 | 1779 | 2802 | 6.158 |
| 3400 | 240.9 | 0.0587 | 17.04 | 1042 | 1760 | 2802 | 6.134 |
| 3600 | 244.2 | 0.0554 | 18.06 | 1058 | 1744 | 2802 | 6.112 |
| 3800 | 247.3 | 0.0524 | 19.08 | 1073 | 1728 | 2801 | 6.090 |
| 4000 | 250.3 | 0.0497 | 21.00 | 1087 | 1713 | 2800 | 6.069 |
At atmospheric pressure - 0 bar gauge or absolute 101.33 kN/m2 - water boils at 100oC. 419 kJ of energy is required to heat 1 kg of water from 0oC to the saturation temperature 100�C.
Therefore, at 0 bar gauge (absolute 101.33 kN/m2) and 100oC - the specific enthalpy of water is 419
kJ/kg.
Another 2,257 kJ of energy is required to evaporate the 1 kg of water at 100oC to steam at 100oC. Therefore, at 0 bar
gauge (absolute 101.33 kN/m2) - the specific enthalpy of evaporation is 2,257 kJ/kg.
The total specific enthalpy of the steam at atmospheric pressure and 100oC can be summarized as:
hs = 419 + 2,257
= 2,676 kJ/kg
Steam at atmospheric pressure is of limited practical use. It cannot be conveyed by its own pressure along a steam pipe to the
points of consumption.
At 7 bar gauge (absolute 800 kN/m2) - the saturation temperature of water is 170oC. More heat energy is required to raise
the temperature to the saturation point at 7 bar gauge than needed for water at atmospheric pressure. From the table a value of 720.9 kJ is
needed to raise 1 kg of water from 0oC to the saturation temperature 170oC.
The heat energy (enthalpy of evaporation) needed at 7 bar gauge to evaporate the water to steam is actually less than the heat energy required
at atmospheric pressure. The specific enthalpy of evaporation decrease with steam pressure increase. The evaporation heat is 2,047 kJ/kg
according the table.
Note! Because the specific volume of steam decreases with increasing pressure, the amount of heat energy transferred in the same volume actually increases with steam pressure. In other words the same pipe may transfer more energy with high pressure steam than with low pressure steam.
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