Advanced options estimate parameters or accept custom constants. Pressure and compressibility outputs appear after submission. Download PDF or CSV for reports and sharing fast.
| Fluid | T (K) | Vm (m³/mol) | Tc (K) | Pc (MPa) | Pressure (kPa) | Z |
|---|---|---|---|---|---|---|
| Methane | 300 | 0.0246 | 190.56 | 4.5992 | ≈ 101.21 | ≈ 1.00 |
| Carbon dioxide | 320 | 0.0080 | 304.13 | 7.3773 | ≈ 318.0 | ≈ 0.96 |
| Nitrogen | 280 | 0.0240 | 126.19 | 3.3958 | ≈ 96.8 | ≈ 1.00 |
The Redlich–Kwong equation of state estimates real-gas pressure using temperature and molar volume:
P = RT/(Vm − b) − a / ( √T · Vm · (Vm + b) )
When critical properties are available, the parameters are estimated as:
a = 0.42748 · R² · Tc^2.5 / Pc | b = 0.08664 · R · Tc / Pc
R is the gas constant, Tc is critical temperature, and Pc is critical pressure.
Tip: Keep all inputs physically meaningful to avoid singularities.
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.