Ethylene Ethene C2H4 Properties
Reference data and engineering information about ethylene ethene c2h4 properties for miscellaneous applications.
Overview
Engineering reference data for Ethylene Ethene C2H4 Properties in miscellaneous.
Key Formulas
Unit Conversion
Multiply by conversion factor.
Linear Interpolation
Estimate between two known points.
Percentage
Part as fraction of whole.
Variables
| Symbol | Description | Unit |
|---|---|---|
| Input value | — | |
| Output value | — | |
| Conversion factor | — |
Thermophysical Properties Data
The following table contains key thermophysical and chemical properties of ethylene gas at 25 °C (298 K) and 1 bara unless otherwise specified.
Property | Value (SI) | Unit | Value (Imperial) | Unit |
|---|---|---|---|---|
| Autoignition temperature | 723 | K | 450 | °C |
| Boiling Point | 169 | K | -104 | °C |
| Critical density | 7.63 | mol/dm³ | 214 | kg/m³ |
| Critical pressure | 5.06 | MPa | 50.6 | bar |
| Critical temperature | 282.4 | K | 9.2 | °C |
| Critical volume | 131 | cm³/mol | 0.00467 | m³/kg |
| Density (gas) | 40.6 | mol/m³ | 1.138 | kg/m³ |
| Density (liquid, -104°C) | 20567 | mol/m³ | 577 | kg/m³ |
| Flammable (gas & liquid) | yes, highly | |||
| Flash point | 137 | K | -136 | °C |
| Gas constant (individual, R) | 296.4 | J/(kg·K) | 0.0823 | Wh/(kg·K) |
| Gibbs free energy of formation (gas) | 68 | kJ/mol | 1042 | Btu/lb |
| Heat of combustion (gas) | -1411 | kJ/mol | -21626 | Btu/lb |
| Heat of formation (gas) | 52.4 | kJ/mol | 803 | Btu/lb |
| Heat of evaporation (-104°C) | 13.6 | kJ/mol | 207.7 | Btu/lb |
| Heat capacity, Cp (gas) | 42.9 | J/(mol·K) | 1.53 | kJ/(kg·K) |
| Heat capacity, Cp (liquid, -104°C) | 67.4 | J/(mol·K) | 2.40 | kJ/(kg·K) |
| Heat capacity, Cv (gas) | 34.6 | J/(mol·K) | 1.24 | kJ/(kg·K) |
| Heat capacity, Cv (liquid, -104°C) | 38.7 | J/(mol·K) | 1.38 | kJ/(kg·K) |
| Ionization potential | 10.5 | eV | ||
| log KOW | 1.13 | |||
| Melting point | 104.15 | K | -169.0 | °C |
| Molecular Weight | 28.054 | g/mol | 0.06185 | lb/mol |
| Solubility in water (25°C) | 0.131 | mg/ml | ||
| Sound velocity | 330 | m/s | 1082 | ft/s |
| Specific Gravity (gas) | 0.978 | (relative to air) | ||
| Specific Heat Ratio (gas), Cp/Cv | 1.24 | |||
| Specific Heat Ratio (liquid), Cp/Cv | 1.74 | |||
| Specific Volume | 0.0247 | m³/mol | 0.879 | m³/kg |
| Standard molar entropy, S° (gas) | 219.32 | J/(mol·K) | 1.87 | Btu/(lb·°F) |
| Standard molar entropy, S° (liquid) | 117.8 | J/(mol·K) | 1.00 | Btu/(lb·°F) |
| Surface tension (-104°C) | 16.00 | dynes/cm | 0.016 | N/m |
| Thermal Conductivity | 0.020 | W/(m·°C) | 0.0118 | Btu/(hr·ft·°F) |
| Triple point pressure | 0.000122 | MPa | 0.0177 | psi |
| Triple point temperature | 104.0 | K | -169.16 | °C |
| Vapor (saturation) pressure | 6.9449 | MPa | 1007.30 | psi |
| Viscosity, dynamic (absolute) | 0.0103 | cP | ||
| Viscosity, kinematic | 9.05 | cSt |
Source: engineeringtoolbox.com
Phase Behavior and Critical Points
Ethylene is a gas under standard conditions. Its phase state changes with pressure and temperature, as shown on its phase diagram.
- Critical Point: This is the point on the phase diagram where the distinction between the liquid and gas phases disappears. For ethylene, this occurs at 282.4 K (9.2 °C) and 5.06 MPa. At or above this temperature and pressure, ethylene exists as a supercritical fluid.
- Triple Point: This is the unique temperature and pressure where the solid, liquid, and gas phases coexist in equilibrium. For ethylene, the triple point is at 104.0 K (-169.16 °C) and 0.000122 MPa.
- Saturation Curve: The curve between the triple point and the critical point represents the ethylene boiling point as a function of pressure (or equivalently, the saturation pressure as a function of temperature).
Related Properties and Data Sources
Detailed data for ethylene's properties as a function of temperature and pressure can be found for:
- Density and specific weight
- Dynamic and kinematic viscosity
- Specific heat (Cp and Cv)
- Thermal conductivity
Key Thermodynamic Relationships
The Specific Heat Ratio ( or ) is a fundamental property for process engineering, especially for compressible flow and compression calculations. For ethylene gas, .
The individual gas constant () can be calculated from the universal gas constant () and the molar mass (): This yields the value of listed in the properties table.