Pick pressure or temperature, then view key steam properties instantly on site. Download a report, save a CSV, and compare example data for checks.
| Pressure (kPa) | Tsat (°C) | hf (kJ/kg) | hg (kJ/kg) | vg (m³/kg) |
|---|---|---|---|---|
| 100 | 99.61 | 417.5 | 2675.5 | 1.694 |
| 500 | 151.83 | 640.1 | 2748.7 | 0.375 |
| 1000 | 179.88 | 761.7 | 2778.1 | 0.194 |
| 2000 | 212.38 | 908.6 | 2799.5 | 0.0996 |
Values above are rounded for quick checks and demonstrations.
For any property Y between two table points:
The calculator brackets your input and interpolates each property.
Mixture properties use saturated endpoints:
Where x is dryness fraction from 0 to 1.
At the same pressure as saturation, a simple approximation is used:
This is not a substitute for certified superheat tables.
Steam supports concrete curing, temporary heating, cleaning, and pressure tests. Knowing saturation temperature at a given pressure helps avoid under‑heating (slow strength gain) or over‑heating (thermal cracking). Small pressure shifts change saturation temperature, so tables help standardize procedures.
Portable steam units often operate around 100 to 1000 kPa depending on load and safety settings. Across that band, saturation temperature rises from about 100°C to roughly 180°C. This calculator interpolates within the embedded dataset for fast planning checks.
The main energy transfer in saturated steam is condensation. Near 100 kPa, latent heat h_fg is about 2250 kJ/kg, so one kilogram of steam can release substantial heat as it condenses on forms or blankets. Estimating h_fg helps size fuel, water, and runtime.
Steam in long lines may be wet due to heat loss or poor separation. Quality x describes the vapor fraction. With x = 0.9, only 90% is vapor, and enthalpy falls. The tool applies h = h_f + x(h_g − h_f) and similar relations for s and v.
Some applications prefer superheated steam to limit condensation in hoses. Superheat changes specific volume and energy content. For quick estimates, the calculator uses an approximation at the same pressure with ideal‑gas volume and constant c_p. Confirm final values with certified superheat tables.
Project documents may use bar, psi, °F, or SI units. Conversion mistakes can create incorrect setpoints and paperwork. The calculator converts inputs and can display outputs in SI or Imperial, aligning with specifications, commissioning forms, and inspection logs.
Exporting CSV supports sharing with supervisors and quality teams, while the PDF snapshot fits daily reports. Record the input basis, output units, and rounding so others can reproduce results. Use the notes area to state whether saturated, wet, or superheated mode was used. Include measured line losses and hose length to explain deviations clearly.
Steam systems must follow relief settings, hose ratings, and controlled venting. Verify whether your pressure is gauge or absolute before comparing to tables. Measure temperature at the point of use. Calculations support decisions, but never replace safety procedures. Lockout, drain condensate, and keep personnel clear of discharge during startup.
It uses absolute pressure for saturation properties. If you measure gauge pressure, add local atmospheric pressure (about 101 kPa) before comparing to the saturation results.
The embedded dataset covers common field pressures and temperatures. If your input is outside those limits, the tool clamps to the nearest endpoint to avoid misleading extrapolation.
It provides a quick estimate only. Use it for early planning or comparisons, then verify with certified superheat tables or a validated thermodynamic package for final design.
Quality is the mass fraction of vapor in a liquid‑vapor mixture. x = 1 is dry saturated vapor, x = 0 is saturated liquid, and intermediate values represent wet steam.
Heat losses, pressure drop along hoses, non‑condensable gases, and sensor placement can all shift observed temperature. Check pressure at the measurement point and confirm insulation and trap performance.
Saturation temperature supports setpoint control, while h_fg indicates available heat from condensation. Specific volume helps with hose sizing, and exporting results helps document curing conditions.
Record input basis, pressure or temperature, unit system, and mode (saturated, wet, or superheated). Attach the PDF snapshot and keep the CSV for traceability and later recalculation.
Accurate steam properties help control heat, costs, and safety.
Important Note: All the Calculators listed in this site are for educational purpose only and we do not guarentee the accuracy of results. Please do consult with other sources as well.