Steam tables / Saturation pressure

Saturation pressure of water against temperature

This is the line every steam system is controlled from. Along it liquid and vapour sit in equilibrium, so pressure and temperature are not independent: fix one and the other is decided. The vertical axis is logarithmic because it has to be. Pressure climbs from 0.006112 bar at 0 °C to 220.6 bar at the critical point, more than four orders of magnitude, and on a linear axis every state a heating system ever sees would be flat on the floor of the chart.

Arrive here from a chart on the steam tables page and the temperature you dialled in comes with you, marked on the curve and bolded in the table that prints beside it. The sheet is then about one operating point rather than about water in general.

Table unitsbar, °C, m³/kg, kJ/kg. Both columns of pressure, absolute and gauge, either way.
Saturation pressure bar (log scale)
Saturation pressure of water in bar against temperature in degrees Celsius, on a logarithmic pressure axis, from 0 to 373.946 °C0.010.1110100020406080100120140160180200220240260280300320340360Saturation temperature (°C)Saturation pressure (bar (log scale))
The rest of the state at 100 °C (default)
Saturation pressure1.0142 bar a · 0.0 psig
Latent heat of vaporisation2,256.5 kJ/kg
Specific volume, saturated vapour1.672 m³/kg
Saturated liquid enthalpy h_f419.1 kJ/kg
Saturated vapour enthalpy h_g2,675.6 kJ/kg
Saturation pressure along the whole saturation line
Temperature°CTemperature°FPressurebar aPressurepsigPressurepsia
032.00.006112-14.60.08865
2577.00.0317-14.20.4597
50122.00.1235-12.91.791
75167.00.386-9.15.598
100212.01.0140.014.71
125257.02.32219.033.68
150302.04.76154.469.05
175347.08.924115129.4
200392.015.55211225.5
225437.025.49355369.8
250482.039.76562576.7
275527.059.46848862.4
300572.085.881,2311,246
325617.0120.51,7331,748
350662.0165.32,3832,397
373.946705.1220.63,1853,200

Every row is a call into IAPWS-IF97 made when this page was built, not a transcription. Gauge pressure is absolute minus one standard atmosphere, 101.325 kPa, so it is negative everywhere below 99.97 °C, which is where water actually boils at one atmosphere, and a real barometer is never exactly that anyway.

Learning zone

What the steepness costs

Read the chart from the pressure side and it explains the whole economics of a steam header. Getting water to 100 °C takes 1.014 bar absolute, which is essentially free. Getting it to 180 °C takes 10.03 bar, and every component from the boiler shell to the flange bolting has to be rated for it. The curve is convex, so each extra degree of steam temperature costs more pressure than the one before it, and the pressure is what the pressure vessel code charges for.

Read it from the temperature side and it is a boiling point chart. Water in a condenser at 0.07384 bar absolute boils at 40 °C, which is why a vacuum lets a turbine exhaust into something cold. Water in a 54.4 psig heating main condenses at 150 °C, which is the temperature the coil actually delivers heat at. The gauge is a thermometer, which is the single most useful thing this line has to say.

Where it stops

The top end of this curve is real physics and not a plotting choice: the critical point, 373.946 °C and 22.064 MPa, above which there is only one phase and nothing left to draw. The bottom end is a standard’s edge rather than nature’s. Water’s triple point is 0.01 °C and 611.657 Pa, and below it there is no liquid to be in equilibrium with, but IF97 extrapolates its own saturation equation a hundredth of a degree further down to 273.15 K, where it reads 611.213 Pa. That is the floor the engine accepts, so it is where this chart and every table on this site begin.

IAPWS R7-97(2012), regions 1 to 5 implemented in full · saturation line from 0 °C to 373.946 °C · computed at page build, never transcribed