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Superheated Steam Table — 140 bar (14 MPa)

Specific volume, internal energy, enthalpy, entropy, density and isobaric specific heat of superheated steam at 140 bar (14 MPa), computed from IAPWS-IF97 — the same formulation the SimuPipe solver uses. Rows run from the saturation temperature (336.67 °C) to 800 °C in 20 °C steps.

Superheated steam properties at 140 bar (14 MPa) from IAPWS-IF97
T (°C)v (m³/kg)ρ (kg/m³)u (kJ/kg)h (kJ/kg)s (kJ/kg·K)cp (kJ/kg·K)
336.67Sat.0.01148987.04082477.22638.15.373011.2598
3400.01199983.34122504.42672.45.42919.4878
3600.01422970.28002617.22816.45.66055.7978
3800.01586763.02542696.12918.35.81904.5496
4000.01724158.00122760.93002.25.94573.9064
4200.01846054.17022817.73076.16.05393.5132
4400.01957651.08262869.53143.66.14993.2504
4600.02061848.50202918.03206.76.23713.0648
4800.02160346.28902964.13266.56.31772.9293
5000.02254644.35443008.43324.16.39312.8278
5200.02345342.63803051.53379.86.46432.7506
5400.02433341.09713093.53434.26.53202.6911
5600.02518939.70063134.93487.56.59682.6449
5800.02602538.42503175.73540.16.65912.6086
6000.02684437.25203216.13591.96.71922.5803
6200.02764936.16743256.23643.36.77742.5580
6400.02844235.15963296.13694.36.83392.5407
6600.02922334.21933335.83745.06.88882.5274
6800.02999533.33863375.53795.46.94222.5175
7000.03075932.51123415.13845.76.99442.5103
7200.03151431.73163454.63895.87.04552.5054
7400.03226330.99503494.23945.97.09542.5025
7600.03300630.29743533.93995.97.14432.5013
7800.03374329.63543573.64046.07.19222.5017
8000.03447629.00583613.44096.07.23932.5033
Reading this table

u is not tabulated independently. Specific internal energy follows from the enthalpy and specific volume as u = h − p·v, with p in MPa and v in m³/kg (1 MPa·m³/kg = 1000 kJ/kg). At 140 bar (14 MPa) that pressure term is worth 482.7 kJ/kg at 800 °C, so u and h are far apart at high pressure and nearly equal at low pressure — a common source of error when the wrong column is read.

The first row is saturated vapour, at 336.67 °C. Below that temperature at 140 bar (14 MPa) the water is a liquid or a two-phase mixture, and this table does not apply — use the saturated tables instead.

Values are IAPWS-IF97, not interpolated. Every row is evaluated directly from the industrial formulation at that exact temperature, so there is no interpolation error between rows. If you need a temperature between the 20 °C steps, the calculator computes it exactly.

Superheated tables at other pressures