Superheated Steam Table — 100 bar (10 MPa)
Specific volume, internal energy, enthalpy, entropy, density and isobaric specific heat of superheated steam at 100 bar (10 MPa), computed from IAPWS-IF97 — the same formulation the SimuPipe solver uses. Rows run from the saturation temperature (311.00 °C) to 800 °C in 20 °C steps.
| T (°C) | v (m³/kg) | ρ (kg/m³) | u (kJ/kg) | h (kJ/kg) | s (kJ/kg·K) | cp (kJ/kg·K) |
|---|---|---|---|---|---|---|
| 311.00Sat. | 0.018034 | 55.4521 | 2545.1 | 2725.5 | 5.6159 | 7.1472 |
| 320 | 0.019272 | 51.8899 | 2589.9 | 2782.7 | 5.7131 | 5.7468 |
| 340 | 0.021490 | 46.5338 | 2667.2 | 2882.1 | 5.8780 | 4.3885 |
| 360 | 0.023327 | 42.8681 | 2729.3 | 2962.6 | 6.0073 | 3.7324 |
| 380 | 0.024952 | 40.0766 | 2783.6 | 3033.1 | 6.1170 | 3.3471 |
| 400 | 0.026439 | 37.8225 | 2833.0 | 3097.4 | 6.2139 | 3.0958 |
| 420 | 0.027829 | 35.9332 | 2879.2 | 3157.5 | 6.3019 | 2.9217 |
| 440 | 0.029147 | 34.3083 | 2923.1 | 3214.6 | 6.3831 | 2.7965 |
| 460 | 0.030410 | 32.8837 | 2965.4 | 3269.5 | 6.4591 | 2.7043 |
| 480 | 0.031629 | 31.6164 | 3006.6 | 3322.9 | 6.5310 | 2.6354 |
| 500 | 0.032813 | 30.4759 | 3046.9 | 3375.1 | 6.5993 | 2.5833 |
| 520 | 0.033968 | 29.4399 | 3086.6 | 3426.3 | 6.6648 | 2.5437 |
| 540 | 0.035098 | 28.4917 | 3125.9 | 3476.9 | 6.7277 | 2.5134 |
| 560 | 0.036208 | 27.6183 | 3164.8 | 3526.9 | 6.7885 | 2.4904 |
| 580 | 0.037300 | 26.8095 | 3203.5 | 3576.5 | 6.8474 | 2.4730 |
| 600 | 0.038377 | 26.0570 | 3242.1 | 3625.8 | 6.9045 | 2.4600 |
| 620 | 0.039442 | 25.3540 | 3280.5 | 3674.9 | 6.9601 | 2.4507 |
| 640 | 0.040494 | 24.6950 | 3319.0 | 3723.9 | 7.0143 | 2.4442 |
| 660 | 0.041536 | 24.0754 | 3357.4 | 3772.7 | 7.0672 | 2.4402 |
| 680 | 0.042569 | 23.4911 | 3395.8 | 3821.5 | 7.1189 | 2.4383 |
| 700 | 0.043594 | 22.9387 | 3434.3 | 3870.3 | 7.1696 | 2.4380 |
| 720 | 0.044612 | 22.4154 | 3472.9 | 3919.0 | 7.2192 | 2.4393 |
| 740 | 0.045623 | 21.9185 | 3511.6 | 3967.9 | 7.2678 | 2.4418 |
| 760 | 0.046629 | 21.4459 | 3550.4 | 4016.7 | 7.3156 | 2.4454 |
| 780 | 0.047629 | 20.9956 | 3589.4 | 4065.7 | 7.3625 | 2.4501 |
| 800 | 0.048624 | 20.5659 | 3628.5 | 4114.7 | 7.4087 | 2.4555 |
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 100 bar (10 MPa) that pressure term is worth 486.2 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 311.00 °C. Below that temperature at 100 bar (10 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.