This table presents thermodynamic properties of superheated steam across industrial pressure ranges (1–12.5 MPa/10–125 bar), highlighting critical trends for engineering applications. As pressure increases:
Saturation temperatures rise (179.9°C at 1 MPa → 327.8°C at 12.5 MPa), requiring higher steam temperatures to maintain superheated conditions.
Specific volume (v) decreases sharply with pressure (e.g., at 400°C: 0.3066 m³/kg at 1 MPa vs. 0.02369 m³/kg at 12.5 MPa), impacting piping and equipment sizing.
Enthalpy (h) shows dual dependence—initially decreasing with pressure at lower temperatures (due to compressed liquid effects) but increasing at higher temperatures (e.g., 400°C values range from 3,171 kJ/kg at 1 MPa to 3,158 kJ/kg at 12.5 MPa).
Specific heat (cₚ) peaks near critical pressures (reaching 5.145 kJ/kg·K at 12.5 MPa/350°C), reflecting anomalous behavior in this region.
Entropy (s) systematically decreases with rising pressure at a given temperature (e.g., 400°C: 7.465 kJ/kg·K at 1 MPa → 6.188 kJ/kg·K at 12.5 MPa), crucial for turbine efficiency calculations.
Temp.(°C) | Specific Volumev (m³/kg) | Enthalpyh (kJ/kg) | Specific Heatcp (kJ/kg·K) | Entropys (kJ/kg·K) |
---|---|---|---|---|
200 | 0.2060 | 2827.9 | 2.013 | 6.693 |
250 | 0.2327 | 2942.6 | 2.060 | 6.924 |
300 | 0.2579 | 3051.2 | 2.134 | 7.123 |
350 | 0.2825 | 3161.7 | 2.213 | 7.302 |
Temp.(°C) | Specific Volumev (m³/kg) | Enthalpyh (kJ/kg) | Specific Heatcp (kJ/kg·K) | Entropys (kJ/kg·K) |
---|---|---|---|---|
250 | 0.07058 | 2855.8 | 2.689 | 6.287 |
300 | 0.08114 | 2993.5 | 2.903 | 6.539 |
350 | 0.09053 | 3115.3 | 3.056 | 6.742 |
400 | 0.09936 | 3230.9 | 3.179 | 6.921 |
Temp.(°C) | Specific Volumev (m³/kg) | Enthalpyh (kJ/kg) | Specific Heatcp (kJ/kg·K) | Entropys (kJ/kg·K) |
---|---|---|---|---|
300 | 0.05214 | 2925.6 | 3.255 | 6.209 |
350 | 0.05886 | 3069.3 | 3.443 | 6.451 |
400 | 0.06525 | 3213.6 | 3.565 | 6.657 |
500 | 0.07743 | 3434.7 | 3.681 | 7.038 |
Temp.(°C) | Specific Volumev (m³/kg) | Enthalpyh (kJ/kg) | Specific Heatcp (kJ/kg·K) | Entropys (kJ/kg·K) |
---|---|---|---|---|
350 | 0.03564 | 3017.0 | 4.058 | 6.230 |
400 | 0.04112 | 3177.2 | 3.978 | 6.455 |
500 | 0.05029 | 3429.3 | 3.822 | 6.840 |
600 | 0.05834 | 3681.6 | 3.773 | 7.129 |
Temp.(°C) | Specific Volumev (m³/kg) | Enthalpyh (kJ/kg) | Specific Heatcp (kJ/kg·K) | Entropys (kJ/kg·K) |
---|---|---|---|---|
350 | 0.02641 | 3045.8 | 4.229 | 6.140 |
400 | 0.03002 | 3162.2 | 4.113 | 6.313 |
500 | 0.03675 | 3373.7 | 3.921 | 6.596 |
600 | 0.04248 | 3625.3 | 3.837 | 6.902 |
Temp.(°C) | Specific Volumev (m³/kg) | Enthalpyh (kJ/kg) | Specific Heatcp (kJ/kg·K) | Entropys (kJ/kg·K) |
---|---|---|---|---|
350 | 0.02047 | 3012.1 | 5.145 | 5.946 |
400 | 0.02369 | 3158.1 | 4.646 | 6.188 |
500 | 0.02995 | 3401.7 | 4.138 | 6.513 |
600 | 0.03538 | 3669.4 | 3.938 | 6.843 |
Source: IAPWS-97 Industrial Formulation | Values shown for superheated region only (T > Tsat)