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Properties of Saturated Steam - SI Units A Saturated Steam Table with steam properties as specific volume, density, specific enthalpy and specific entropy Sponsored Links The steam table below list the properties of steam at varying pressures and temperatures: Specific Enthalpy of Specific Absolute Specific Density Entropy Temperature Liquid Evaporation Steam pressure o Volume - ρ of Steam ( C) 2 3 3 h h h l e s (kN/m ) (m /kg) (kg/m ) -s(kJ/kg) (kJ/kg) (kJ/kg) (kJ/kgK) 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 7.095 260 280 320 360 400 440 480 500 550 600 650 700 750 800 850 900 950 1000 1050 1150 1250 1300 1500 1600 1800 2000 2100 2300 2400 2600 2700 2900 3000 3200 3400 3600 3800 4000 128.7 131.2 135.8 139.9 143.1 147.1 150.3 151.8 155.5 158.8 162.0 165.0 167.8 170.4 172.9 175.4 177.7 179.9 182.0 186.0 189.8 191.6 198.3 201.4 207.1 212.4 214.9 219.6 221.8 226.0 228.1 232.0 233.8 237.4 240.9 244.2 247.3 250.3 0.693 0.646 0.570 0.510 0.462 0.423 0.389 0.375 0.342 0.315 0.292 0.273 0.255 0.240 0.229 0.215 0.204 0.194 0.186 0.170 0.157 0.151 0.132 0.124 0.110 0.0995 0.0945 0.0868 0.0832 0.0769 0.0740 0.0689 0.0666 0.0624 0.0587 0.0554 0.0524 0.0497 1.44 1.55 1.75 1.96 2.16 2.36 2.57 2.67 2.92 3.175 3.425 3.66 3.915 4.16 4.41 4.65 4.90 5.15 5.39 5.89 6.38 6.62 7.59 8.03 9.07 10.01 10.54 11.52 12.02 13.01 13.52 14.52 15.00 16.02 17.04 18.06 19.08 21.00 540.9 551.4 570.9 588.5 604.7 619.6 633.5 640.1 655.8 670.4 684.1 697.1 709.3 720.9 732.0 742.6 752.8 762.6 772 790 807 815 845 859 885 909 920 942 952 972 981 1000 1008 1025 1042 1058 1073 1087 2177 2170 2157 2144 2133 2122 2112 2107 2096 2085 2075 2065 2056 2047 2038 2030 2021 2014 2006 1991 1977 1971 1945 1933 1910 1889 1878 1858 1849 1830 1821 1803 1794 1779 1760 1744 1728 1713 2718 2722 2728 2733 2738 2742 2746 2748 2752 2756 2759 2762 2765 2768 2770 2772 2774 2776 2778 2781 2784 2785 2790 2792 2795 2797 2798 2800 2800 2801 2802 2802 2802 2802 2802 2802 2801 2800 7.039 7.014 6.969 6.930 6.894 6.862 6.833 6.819 6.787 6.758 6.730 6.705 6.682 6.660 6.639 6.619 6.601 6.583 6.566 6.534 6.505 6.491 6.441 6.418 6.375 6.337 6.319 6.285 6.269 6.239 6.224 6.197 6.184 6.158 6.134 6.112 6.090 6.069 • • Absolute Pressure = Gauge Pressure + Atmospheric pressure. Specific enthalpy or Sensible Heat is the quantity of heat in 1 kg of water according to the selected temperature. Example - Boiling Water at 100oC and 0 bar 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 Example - Boiling Water at 170oC and 7 bar 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. Sponsored Links Related Topics • • • Flash Steam Flash steam generation; fundamentals, energy recovery from flash steam .. Thermodynamics Steam and condensate properties, fundamental thermodynamics .. Steam and Condensate Steam & condensate properties, capacities, pipe sizing and systems configuration. Steam is an essential part of modern industrial process technology. Without steam, food, textile, chemical, medical, power, heating and transport industries could not perform as they do. In this section you will find tools and information regarding steam and condensate applications. Related Documents • • • • Entropy of Superheated Steam A table with the entropy of steam superheated to temperatures above the boiling point with corresponding temperatures Sizing Steam Pipes (kg/h) Steam is a compressible gas where the mass flow capacity of the pipe lines depends on the steam pressure. This table, where pressure is in bar, velocity in m/s and capacity in kg/h, is suitable for sizing steam pipes Steam Trap Selection Guide A steam trap selection guide - Float & Thermostatic, Inverted Bucket, Bimetal Thermostatic, Impulse and Thermodynamic Disc steam traps Steam Consumption of some Typical Consumers Steam consumption rates for typical consumers in different industries • • • • • • • • • • • as bakeries, breweries, paper factories etc. Arithmetic and Logarithmic Mean Temperature Difference Arithmetic Mean Temperature Difference - AMTD - and Logarithmic Mean Temperature Difference - LMTD - definition formulas with examples - Online Mean Temperature Calculator 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 Vapor and Steam An introduction to vapor and steam Water - Specific Heat Capacity at High Temperature Specific heat capacity of water at higher temperatures - in Imperial units Water - Specific Volume and Weight Density Specific volume and weight density of water at temperatures ranging from 32 to 700 deg F, in Imperial Units Water - Saturation Pressure and Specific Weight Vapor pressure and specific weight for water at temperatures from 32 to 212 deg F - in Imperial Units Compressed Water Properties Specific volume, enthalpy and entropy of compressed water Enthalpy of Wet Steam Wet steam, dryness fraction and enthalpy Specific Volume of Wet Steam Wet steam an specific volume Stress in a Steam Boiler Shell from Boiler Pressure Calculate the stress in in a steam boiler shell from pressure Steam Pipe Pressure drop Calculator Calculate pressure drop in steam distribution pipe lines Sponsored Links ToolBox ShortList Difficult to find your favorite ToolBox page? 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