Analyze z factor with flexible engineering inputs. View live results, property checks, and pressure trends. Export clean reports for field reviews and calculations today.
These values are illustrative and show how a typical engineering entry may be organized.
| Case | Pressure | Temperature | Gas Gravity | CO₂ | H₂S | Estimated Z | Note |
|---|---|---|---|---|---|---|---|
| Reservoir sample A | 2500 psia | 150 °F | 0.68 | 2.0 % | 0.5 % | ~0.88 to 0.92 | Moderate pressure sour gas case |
| Pipeline sample B | 1200 psia | 90 °F | 0.62 | 0.0 % | 0.0 % | ~0.93 to 0.98 | Lean sweet gas trend |
| Process sample C | 4200 psia | 220 °F | 0.75 | 3.5 % | 1.0 % | ~0.84 to 0.90 | High-pressure corrected case |
Tpc = 169.2 + 349.5γg − 74γg²
Ppc = 756.8 − 131γg − 3.6γg²
ε = 120(A0.9 − A1.6) + 15(B0.5 − B4)
Tpc′ = Tpc − ε
Ppc′ = Ppc × Tpc′ / [Tpc − B(1 − B)ε]
Pr = P / Ppc′
Tr = T / Tpc′
The calculator solves the implicit reduced-density equation iteratively.
ρr = 0.27Pr / (ZTr), then Z is updated until convergence.
ρg = PM / (ZRT)
Bg = 0.0282793 × Z × T / P
The z factor measures how far a real gas deviates from ideal-gas behavior. A value near 1 means nearly ideal behavior, while lower or higher values indicate stronger real-gas effects under pressure and temperature changes.
Pseudo-critical pressure and temperature normalize actual operating conditions into reduced properties. Those reduced values allow empirical gas correlations to estimate z factor across many engineering pressure and temperature ranges.
Apply sour gas correction when CO₂ or H₂S is present in meaningful amounts. Acid gases shift pseudo-critical properties and can change reduced variables enough to affect the final z-factor estimate.
This page uses Sutton for pseudo-critical estimates, Wichert-Aziz for sour-gas correction, and Dranchuk-Abou-Kassem for the z-factor solution. That combination is common for petroleum and gas engineering workflows.
Yes. Direct mode lets you enter pseudo-critical pressure and temperature from lab work, published data, or another trusted source. That is useful when gas gravity alone is not the preferred basis.
Pressure is usually the most practical sensitivity variable in field and reservoir work. Holding temperature constant helps you see how compressibility changes across the operating envelope around the submitted case.
The page still reports the latest stable estimate, but you should review the input range. Very unusual reduced conditions or inconsistent pseudo-critical data can make iterative convergence slower or less reliable.
It is useful for screening, checks, and routine engineering calculations. Final design, custody transfer, or high-risk studies should still be reviewed with laboratory data, project standards, and specialist judgment.
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.