Steam and water properties using the 1967 IFC Formulation for Industrial Use, and Condenser performance using the HEI (Heat Exchange Institute) method. Steam for the iPhone and iPod touch calculates the thermodynamic properties of water and steam for subcooled (compressed liquid), saturated, superheated, and supercritical conditions. MILWAUKEE VALVE HAMMONDVALVE Inches Absolute STEAM TEMPERATURE PRESSURE TABLE SATURATED STEAM TEMPERATURES Temperature Gauge Temperature Gauge Temperature Gauge Temperature Gauge.

• Steam Charts Zero Hour
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All of the properties of steam are interrelated. From any one known value you can determine any of others. These relationships are all displayed on a table called the Properties of Saturated Steam, or simply, the Steam Tables.

For any given pressure, you can read:

• the steam temperature
• the heat of the saturated liquid
• the latent heat of the steam
• the total heat of the steam
• the specific volume of the saturated liquid
• the specific volume of saturated steam.

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The following measurements are expressed in imperial values. To view these pages in SI metric units, click here.

If you know that you need a temperature of 307 degrees F, the table tells you that you need to pressurize the system to 60 psig. If you have a 15-psi steam supply, the tables tell you that you have 945 Btu/lb. of heat energy available to do work.

Properties of Saturated Steam

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(Abstracted from Keenan and Keyes, THERMODYNAMIC PROPERTIES OF STEAM, by permission of John Wiley & Sons, Inc.)

Guage Pressure (psig)	Absolute Pressure (psiA)	Steam Temp F	Heat of sat. liquid (btu/lb)	Latent Heat (btu/lb)	Total heat of steam (btu/lb)	Specific volume of sat. liquid (cu ft/lb	Specific volume of sat. steam (cu ft/lb)
29.743	0.08854	32.00	0.00	1075.8	1075.8	0.096022	3306.00
29.515	0.2	53.14	21.21	1063.8	1085.0	0.016027	1526.00
27.886	1.0	101.74	69.70	1036.3	1106.0	0.016136	333.60
19.742	5.0	162.24	130.13	1001.0	1131.1	0.016407	73.52
9.562	10.0	193.21	161.17	982.1	1143.3	0.016590	38.42
7.536	11.0	197.75	165.73	979.3	1145.0	0.016620	35.14
5.490	12.0	201.96	169.96	976.6	1146.6	0.016647	32.40
3.454	13.0	205.88	173.91	974.2	1148.1	0.016674	30.06
1.418	14.0	209.56	177.61	971.9	1149.5	0.016699	28.04
0.0	14.696	212.00	180.07	970.3	1150.4	0.016715	26.80
1.3	16.0	216.32	184.42	967.6	1152.0	0.016746	24.75
2.3	17.0	219.44	187.56	965.5	1153.1	0.016768	23.39
5.3	20.0	227.96	196.16	960.1	1156.3	0.016830	20.09
10.3	25.0	240.07	208.42	952.1	1160.6	0.016922	16.30
15.3	30.0	250.33	218.82	945.3	1164.1	0.017004	13.75
20.3	35.0	259.28	227.91	939.2	1167.1	0.017078	11.90
25.3	40.0	267.25	236.03	933.7	1169.7	0.017146	10.50
30.3	45.0	274.44	243.36	928.6	1172.0	0.017209	9.40
40.3	55.0	287.07	256.30	919.6	1175.9	0.017325	7.79
50.3	65.0	297.97	267.50	911.6	1179.1	0.017429	6.66
60.3	75.0	307.60	277.43	904.5	1181.9	0.017524	5.82
70.3	85.0	316.25	286.39	897.8	1184.2	0.017613	5.17
80.3	95.0	324.12	294.56	891.7	1186.2	0.017696	4.65
90.3	105.0	331.36	302.10	886.0	1188.1	0.017775	4.23
100.0	114.7	337.90	308.80	880.0	1188.8	0.017850	3.88
110.3	125.0	344.33	315.68	875.4	1191.1	0.017922	3.59
120.3	135.0	350.21	321.85	870.6	1192.4	0.017991	3.33
125.3	140.0	353.02	324.82	868.2	1193.0	0.018024	3.22
130.3	145.0	355.76	327.70	865.8	1193.5	0.018057	3.11
140.3	155.0	360.50	333.24	861.3	1194.6	0.018121	2.92
150.3	165.0	365.99	338.53	857.1	1195.6	0.018183	2.75
160.3	175.0	370.75	343.57	852.8	1196.5	0.018244	2.60
180.3	195.0	379.67	353.10	844.9	1198.0	0.018360	2.34
200.3	215.0	387.89	361.91	837.4	1199.3	0.018470	2.13
225.3	240.0	397.37	372.12	828.5	1200.6	0.018602	1.92
250.3	265.0	406.11	381.60	820.1	1201.7	0.018728	1.74
300.0	417.33	393.84	809.0	1202.8	0.018896	1.54
400.0	444.59	424.00	780.5	1204.5	0.019340	1.16
450.0	456.28	437.20	767.4	1204.6	0.019547	1.03

Saturated Steam Table with properties like boiling point, specific volume, density, specific enthalpy, specific heat and latent heat of vaporization

• Properties of Saturated Steam - Imperial Units

For full table - rotate the screen!

Absolute Pressure	Boiling Point	Specific Volume (steam)	Density (steam)	Specific Enthalpy of Liquid Water (sensible heat)		Specific Enthalpy of Steam (total heat)		Latent heat of Vaporization		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
11)	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
1.6	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
2	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
2.8	131.20	0.646	1.548	551.45	131.71	2721.54	650.03	2170.08	518.32	2.1835
3	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
4	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
5	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
6	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
7	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
8	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
9	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

¹⁾1 bar abs = 0 bar gauge = 100 kPa abs = atmospheric pressure

• Vacuum steam is the general term used for saturated steam at temperatures below 100°C.

Example - Boiling Water at 100 ^oC, 0 bar(100 kPa) Atmospheric Pressure

At atmospheric pressure (0 bar g, absolute 1 bar ) water boils at 100 ^oC and 417.51 kJ of energy is required to heat 1 kg of water from 0 ^oC to evaporating temperature 100 ^oC.

Therefore the specific enthalpy of water at 0 bar g (absolute 1 bar ) and 100 ^oC is 417.51 kJ/kg.
Another 2257.92 kJ of energy is 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 vaporation is 2257.19 kJ/kg.

The total specific enthalpy for steam at 0 bar gauge is:

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h_s = (417.51 kJ/kg) + (2257.92 kJ/kg)

= 2675.43 kJ/kg

Example - Boiling Water at 170 ^oC and 7 bar (700 kPa) Atmospheric Pressure

Steam at atmospheric pressure is of a limited practical use because it cannot be conveyed by its own pressure along a steam pipe to the points of use. In a steam distribution system the pressure is always more than 0 bar gauge.
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 needed when the water is at atmospheric pressure. According the table 720.94 kJ is required to raise 1 kg of water from 0 ^oC to saturation temperature 170 ^oC.
The heat energy (enthalpy of evaporation) needed at 7 bar g to vaporize the water to steam is actually less than required at atmospheric pressure. The specific enthalpy of vaporization decreases with steam pressure. The evaporation heat is 2046.53 kJ/kg at 7 bar g.

• Note! The specific volume of steam decreases with increased pressure - and the amount of heat energy distributed by the same volume increase. With higher pressure - more energy can be transferred in a steam distribution system.

Related Topics

• Steam and Condensate - Steam & condensate systems- properties, capacities, pipe sizing, systems configuration and more
• Steam Thermodynamics - Thermodynamics of steam and condensate applications

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• Condensate Lines - Flash Steam - Flash steam produced in condensate pipe lines
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• Enthalpy of Superheated Steam - Enthalpy of steam superheated to temperatures above boiling point
• Enthalpy of Wet Steam - Wet steam, the dryness fraction and enthalpy
• Entropy of Superheated Steam - Entropy of steam superheated to temperatures above saturation point
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• Pressure Drop in Steam Pipes - Steam pipes and pressure drop diagrams - imperial and metric units
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