Calculate steam quality from enthalpy, entropy, volume, or mass balance in minutes. Use it on site to verify separators, traps, and boiler performance today.
Meta description (25 words): Estimate steam dryness fraction quickly for field calculations. Enter saturation properties and measurements. Get quality, vapor mass share, and checks. Export results to files instantly.
Steam quality (dryness fraction) is the mass fraction of vapor in a saturated liquid–vapor mixture: x = mv / (mv + ml).
Using saturation properties at the same state, quality can also be obtained from any mixture property: x = (y − yf) / yfg, where y is the measured property (h, s, or v), yf is saturated liquid value, and yfg is the difference between saturated vapor and liquid.
The calculator clamps results to 0–1 for reporting, and flags values outside range.
| Case | Method | Inputs | Calculated x | Quality (%) | Wetness (%) |
|---|---|---|---|---|---|
| 1 | Enthalpy | h=2300, hf=419, hfg=2257 | 0.833 | 83.3 | 16.7 |
| 2 | Entropy | s=5.50, sf=1.307, sfg=6.047 | 0.693 | 69.3 | 30.7 |
| 3 | Volume | v=0.80, vf=0.001043, vfg=1.693 | 0.472 | 47.2 | 52.8 |
| 4 | Mass balance | mv=8, ml=2 | 0.800 | 80.0 | 20.0 |
Example properties are illustrative; use your project’s steam tables for best accuracy.
Steam quality (dryness fraction, x) is the vapor mass fraction in a saturated mixture. An x of 0.90 means 90% vapor and 10% liquid by mass. In distribution lines, that liquid fraction causes erosion, water hammer risk, and unstable control at coils and heat exchangers.
Many heating and process loads perform best when quality is high. For general space-heating and coil service, crews often aim for x ≥ 0.95 at the point of use; turbine and critical control applications may target x ≥ 0.99. Lower quality increases condensate handling and can reduce delivered heat per kilogram of flow.
At a fixed pressure, the latent portion of energy scales with x. The mixture enthalpy is h = hf + x·hfg, so dropping from x=0.98 to x=0.90 reduces the latent contribution by about 8.2% of hfg. That shortfall often shows up as longer warm-up times, higher flow to meet load, and higher fuel consumption.
Quality can fall due to insufficient separation, poor insulation, long runs with pressure drops, and ineffective drainage. Common field contributors include undersized drip legs, failed steam traps, low points without drains, and carryover from boilers during rapid load changes. Fixing drainage often improves quality more than raising boiler pressure.
This calculator supports four methods. Use enthalpy or entropy when you have steam-table properties at the measured pressure/temperature. Use specific volume when density or volumetric flow is available. Use mass balance when a separator test yields measured vapor and liquid masses over a timed interval.
If computed x is below 0, the inputs likely represent subcooled liquid or mismatched saturation properties. If x exceeds 1, the steam is probably superheated or the selected hf/hfg (or equivalents) do not match the actual pressure. This tool flags both cases and reports a clamped 0–1 value for readability.
During commissioning, record quality at the boiler outlet, after separators, and at critical end points. A step drop across a separator indicates internal damage or carryover. A gradual decline along a line suggests insulation or drainage issues. Pair quality trends with trap surveys and pressure logs for faster root-cause identification.
Document your assumptions, units, and steam-table source for repeatable audits.
Steam quality is the vapor mass fraction in a wet steam mixture. A value of 1.0 is dry saturated vapor, while 0.80 means 80% vapor and 20% liquid by mass.
Quality formulas apply to saturated mixtures. If your calculation gives x > 1, it usually indicates superheat or mismatched saturation properties. Use superheated tables or instrumentation to evaluate superheat separately.
Pick the method that matches your measurements. Enthalpy and entropy work well with steam-table properties. Specific volume fits density/flow-based measurements. Mass balance is best when you can physically separate and weigh vapor and liquid.
hf, hfg, sf, sfg, vf, and vfg are saturation properties tied to a specific state. Mixing properties from different pressures introduces large error and can push x outside the 0–1 range.
Many teams target x ≥ 0.95 at the coil inlet to avoid water hammer and maintain stable control. Actual requirements depend on equipment design, line length, drainage, and operating pressure.
Traps remove condensate. Failed-closed traps can flood lines and lower quality, while failed-open traps waste steam and can distort measurements. A trap survey often improves both quality and energy performance.
Wetness is the liquid mass fraction expressed as percent: wetness = (1 − x) × 100. For example, x=0.92 corresponds to 8% wetness, meaning 8% of the mixture mass is liquid water.
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.