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ASTM D2421-21 (designation D2421 −21´1) provides the standard practice for the interconversion of component analyses of C5 and lighter hydrocarbon mixtures. The procedure allows conversions between three fundamental bases: gas-volume (mole), liquid-volume, and mass. This practice is specifically designed for hydrocarbon streams where the components are gases and light liquids at standard conditions. The values stated in SI units are to be regarded as the standard; values given in parentheses are for information only.
This standard is critically important for custody transfer applications where consistent and accurate conversion data is essential for determining vapor, liquid, or mass equivalence. The component distribution data generated by this practice can also be reliably used to calculate key physical properties such as relative density, vapor pressure, and calorific value.
A key assumption of the computation procedures is that the constituent gas-volume percentages have already been corrected for non-ideality as part of the analytical measurement process. Consequently, these gas-volume percentages are numerically equivalent to mole percentages. Furthermore, the procedure assumes the absence of nonadditivity corrections for liquid mixtures, which is approximately true only for hydrocarbon mixtures of the same carbon number and in the absence of diolefins and acetylenic compounds.
The fundamental conversion data within the standard relies on the relative density values of pure compounds at 15.6 °C / 15.6 °C (60 °F / 60 °F), primarily sourced from the Thermodynamics Research Center (TRC, now part of NIST). Special consideration is given to methane, ethylene, and acetylene, whose density values are assumed to apply as components within a liquid mixture.
The core conversion factor, which defines the volume of liquid (in millilitres) produced from 1 mL of ideal gas at standard conditions, is derived from the ideal gas law using fundamental constants.
| 🟦 Parameter | 📏 Symbol | ⚡ Value / Unit |
|---|---|---|
| Ideal Gas Constant | R | 8314.472 mL·kPa·K⁻¹·g·mol⁻¹ |
| Standard Temperature | T | 273.15 K |
| Standard Pressure | P | 101.325 kPa |
| Molar Volume (1 g-mol Ideal Gas) | V | 22414 mL |
| Liquid Density Correction Factor | — | 0.999016 |
The calculation is expressed in the standard as follows. For 1 mL of gas at 15.6 °C (60 °F) and 101.325 kPa (760 mm Hg), the equivalent liquid volume (L) at 15.6 °C (60 °F) is:
L = (273.15 K / 288.71 K) × (M / 22414) × [1 / (relative density × 0.999016)]
This simplifies to the practical working constant: L = 4.2252 × 10⁻⁵ × (M / relative density), where M is the molecular weight in g-mol.
All interconversions are explicitly referenced to a uniform set of standard conditions to ensure consistency and accuracy across different laboratories and applications. If ideal gas volumes are measured at different temperatures or pressures, they must be mathematically corrected to the standard 15.6 °C and 101.325 kPa baseline before the interconversion formulas can be applied.
| 🔍 Measurement Type | 🎯 Standard Reference Condition |
|---|---|
| Ideal Gas Volume | 15.6 °C (60 °F) @ 101.325 kPa (760 mm Hg) |
| Liquid Volume | 15.6 °C (60 °F) |
| Relative Density | 15.6 °C / 15.6 °C (60 °F / 60 °F) |
This standard provides a uniform practice for interconverting the analytical component data of C5 and lighter hydrocarbon mixtures onto a gas-volume (mole), liquid-volume, or mass basis. This is essential for consistent reporting and custody transfer calculations.
The computation procedures in D2421-21 assume that the analytical process used to obtain the gas-volume percentages has already corrected for the non-ideality of the individual components. Once this correction is applied, the gas-volume percentage is numerically equivalent to the mole percentage.
All ideal gas volumes must be referenced to a standard temperature of 15.6 °C (60 °F) and a standard pressure of 101.325 kPa (760 mm Hg). Liquid volumes are referenced to 15.6 °C (60 °F). Volumes measured at other conditions must be corrected before applying the conversion formulas.
Consistent and accurate component distribution data derived from this practice is fundamental for calculating critical physical properties, including relative density, vapor pressure, and calorific value of the hydrocarbon mixture.