| 1 | Absolute Gas Density | kg/m³ | Pipeline-quality natural gas commonly falls at approximately 0.65–0.90 kg/m³ when measured at 15°C and 101.325 kPa. The actual value depends on composition and reference conditions. | Provides the direct mass-per-volume value needed for storage calculations, flow conversion, transportation planning, and mass-balance checks. | Require the reported temperature, absolute pressure, gas composition, compressibility factor, and measurement uncertainty together with the density value. |
| 2 | Relative Density | Dimensionless; air = 1.000 | Natural gas commonly has a relative density of approximately 0.55–0.75 against dry air under the same reference conditions. | Allows quick comparison of gas heaviness, supports meter calculations, and helps identify major composition changes between shipments. | Confirm the air reference, reference temperature and pressure, moisture basis, and calculation method used by the supplier or laboratory. |
| 3 | Molar Mass | g/mol or kg/kmol | Typical pipeline natural gas is often within approximately 16–22 g/mol. Pure methane has a molar mass of 16.04 g/mol. | Molar mass is a key input for calculating density, relative density, mass flow, energy conversion, and gas behavior under pressure. | Check the component analysis for methane, ethane, propane, nitrogen, carbon dioxide, and heavier hydrocarbons, preferably on a clearly stated dry or wet basis. |
| 4 | Compressibility Factor (Z) | Dimensionless | For natural gas, Z is commonly below 1.00 at pipeline pressure. A broad screening range of approximately 0.85–1.00 may occur around 15°C and 1–10 MPa, depending on composition. | Prevents significant density errors when converting between standard and operating conditions, especially for high-pressure pipeline or LNG-related calculations. | Require Z to be calculated at the actual pressure and temperature using an accepted equation of state and a complete gas composition. |
| 5 | Reference Temperature and Pressure | °C and kPa or bar absolute | Common reference bases include 15°C and 101.325 kPa absolute or 0°C and 101.325 kPa absolute. Contract documents may specify another base. | The same gas can show different density values when the reference basis changes. A common basis is essential for fair international comparison and invoicing. | Put the reference conditions directly beside every density figure and ensure that all parties use absolute, not gauge, pressure. |
| 6 | Measurement Uncertainty | % of reading or % of value | For commercial gas measurement, buyers commonly seek a documented uncertainty target of approximately ±0.5% or better, subject to the contract, flow range, equipment, and calibration method. | Indicates whether a density result is reliable enough for custody transfer, customs documentation, energy settlement, and technical acceptance. | Request calibration certificates, traceability records, uncertainty budgets, operating-range limits, and the date of the latest verification. |
| 7 | Composition-Based Density Calculation | Mole fraction, % mol, and calculated kg/m³ | Density should be calculated from a representative composition covering methane, ethane, propane, heavier hydrocarbons, nitrogen, carbon dioxide, and other relevant components. | Provides an auditable link between laboratory composition, density, calorific value, and transport quantity, particularly when gas sources or cargoes change. | Review the sampling point, sampling frequency, chromatograph or laboratory method, component detection limits, analysis basis, and calculation standard stated in the contract. |