Ethane C2H6 Thermal Conductivity Temperature Pressure
Reference data and engineering information about ethane c2h6 thermal conductivity temperature pressure for fluid mechanics applications.
Overview
Engineering reference data for Ethane C2H6 Thermal Conductivity Temperature Pressure in fluid mechanics.
Key Formulas
Reynolds Number
Ratio of inertial to viscous forces — determines flow regime.
Bernoulli's Equation
Conservation of energy for steady, inviscid, incompressible flow.
Continuity Equation
Conservation of mass for incompressible flow.
Darcy-Weisbach
Pressure drop due to friction in a pipe.
Variables
| Symbol | Description | Unit |
|---|---|---|
| Reynolds number | — | |
| Fluid density | kg/m³ | |
| Flow velocity | m/s | |
| Characteristic dimension | m | |
| Dynamic viscosity | Pa·s | |
| Pressure | Pa | |
| Darcy friction factor | — |
Additional Notes
Thermal Conductivity Data Table (1 bara)
The following table provides thermal conductivity values for ethane at approximately 1 bara (14.5 psia) pressure across a range of temperatures for both liquid and gas phases.
State | Temperature(K) | Temperature(°C) | Temperature(°F) | Pressure(bara) | Pressure(psia) | Thermal Conductivity(mW/(m·K)) | Thermal Conductivity(Btu(IT)/(h·ft·°F)) |
|---|---|---|---|---|---|---|---|
| Liquid | 90.38 | -182.77 | -296.99 | 1 | 14.5 | 255.6 | 0.1477 |
| Liquid | 100 | -173 | -280 | 1 | 14.5 | 247.9 | 0.1432 |
| Liquid | 120 | -153 | -244 | 1 | 14.5 | 230 | 0.1329 |
| Liquid | 140 | -133 | -208 | 1 | 14.5 | 210.6 | 0.1217 |
| Liquid | 160 | -113 | -172 | 1 | 14.5 | 190.9 | 0.1103 |
| Liquid | 180 | -93.2 | -136 | 1 | 14.5 | 171.4 | 0.09903 |
| Liquid | 184.33 | -88.82 | -127.88 | 1 | 14.5 | 167.2 | 0.09661 |
| Gas | 184.33 | -88.82 | -127.88 | 1 | 14.5 | 9.471 | 0.00547 |
| Gas | 200 | -73.2 | -99.7 | 1 | 14.5 | 10.72 | 0.00619 |
| Gas | 220 | -53.2 | -63.7 | 1 | 14.5 | 12.47 | 0.00721 |
| Gas | 240 | -33.2 | -27.7 | 1 | 14.5 | 14.39 | 0.00831 |
| Gas | 260 | -13.2 | 8.3 | 1 | 14.5 | 16.48 | 0.00952 |
| Gas | 280 | 6.9 | 44.3 | 1 | 14.5 | 18.76 | 0.01084 |
| Gas | 300 | 26.9 | 80.3 | 1 | 14.5 | 21.22 | 0.01226 |
| Gas | 320 | 46.9 | 116 | 1 | 14.5 | 23.85 | 0.01378 |
| Gas | 340 | 66.9 | 152 | 1 | 14.5 | 26.65 | 0.0154 |
| Gas | 360 | 86.9 | 188 | 1 | 14.5 | 29.61 | 0.01711 |
| Gas | 400 | 127 | 260 | 1 | 14.5 | 35.96 | 0.02078 |
| Gas | 500 | 227 | 440 | 1 | 14.5 | 53.77 | 0.03107 |
| Gas | 600 | 327 | 620 | 1 | 14.5 | 73.34 | 0.04238 |
| Gas | 700 | 427 | 800 | 1 | 14.5 | 93.86 | 0.05423 |
| Gas | 800 | 527 | 980 | 1 | 14.5 | 114.8 | 0.06633 |
| Gas | 900 | 627 | 1160 | 1 | 14.5 | 135.9 | 0.07852 |
| Gas | 1000 | 727 | 1340 | 1 | 14.5 | 156.8 | 0.0906 |
Source: engineeringtoolbox.com
Unit Definitions and Conversions
- SI Unit: or milliwatt per meter per kelvin, .
- Imperial Units:
- : British thermal unit (IT) per hour per foot per degree Fahrenheit.
- : Inch-based unit for conductivity.
- : Kilocalorie (IT) per hour per meter per kelvin.
Phase Behavior Note
The thermal conductivity of ethane is highly dependent on its phase (liquid or gas) and proximity to the critical point. The data shows a significant drop in conductivity upon vaporization at constant temperature. For example, at 184.33 K, the liquid conductivity (~167 mW/(m·K)) is nearly 18 times higher than the vapor conductivity (~9.5 mW/(m·K)). Values generally increase with temperature in the gas phase and decrease in the liquid phase.