Description
Return ideal and compressibility-corrected gas volumes.
Physical process calculations combine supplied geometry, material properties and pressure or gas-state conventions. A density scaling, ideal-gas correction or vessel-volume term can be dimensionally consistent without verifying the actual fluid state, flow regime or equipment suitability.
Return ideal and compressibility-corrected gas volumes.
When to use this tool
Use Process Gas Compressibility Volume Factor when evaluating the stated geometric, fluid-property or gas-state term.
How to use the tool and how it works
- Enter moles, compressibility, gasConstant, temperatureK, pressure. Use the units and conventions below.
- Run the tool. Correct any format, range, or cross-field input error before interpreting the output.
- Read idealVolume, correctedVolume. Use the output convention below.
Return ideal and compressibility-corrected gas volumes. Require moles >= 0 and positive Z, gas constant, kelvin temperature and absolute pressure; idealVolume = nRT/P, correctedVolume = Z*nRT/P.1
| Input field | Meaning and units | Accepted input |
|---|---|---|
| moles | Moles | Required. Finite number; minimum 0. |
| compressibility | Positive supplied dimensionless Z; no equation of state is solved. | Required. Finite number; strictly above 0. |
| gasConstant | Gas Constant | Required. Finite number; strictly above 0. |
| temperatureK | Positive absolute gas temperature in kelvins. Unit: K. | Required. Finite number; strictly above 0. |
| pressure | Positive absolute pressure; Pa with an SI gas constant. | Required. Finite number; strictly above 0. |
| Output field | Interpretation | Returned shape |
|---|---|---|
| idealVolume | Ideal Volume | Required. Finite number. |
| correctedVolume | Corrected Volume | Required. Finite number. |
{
"input": {
"moles": 2,
"compressibility": 0.9,
"gasConstant": 8,
"temperatureK": 300,
"pressure": 100000
},
"output": {
"idealVolume": 0.048,
"correctedVolume": 0.0432
}
} Limitations and assumptions
- Units must be consistent; Z is supplied and no equation of state, phase condition or safe pressure is determined.
- Inputs must satisfy both the field types and the cross-field conditions above. Invalid input causes an error; a successful false flag or documented placeholder is a different result.
- Numeric calculations use binary floating point unless exact decimal-integer arithmetic is explicitly stated. No hidden measurement tolerance or decimal rounding is added; nonfinite or out-of-contract results are rejected. Numeric signed-zero results are exported as zero.
Alternative or Complementary methods
Use verified geometry and state-specific material data with an appropriate full engineering model for actual flow, storage or equipment design.
References
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