Ethylene Ethene Acetene C2H4 Dynamic Kinematic Viscosity Temperature Pressure
Reference data and engineering information about ethylene ethene acetene c2h4 dynamic kinematic viscosity temperature pressure for fluid mechanics applications.
Overview
Engineering reference data for Ethylene Ethene Acetene C2H4 Dynamic Kinematic Viscosity 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 | — |
Ethylene Viscosity Data
Ethylene (ethene, C₂H₄) exhibits distinct viscosity behavior between its liquid and gas phases. The atmospheric boiling point of ethylene is -104 °C (-155 °F), which corresponds to a significant shift in viscosity at that temperature.
State | Temperature(K) | Temperature(°C) | Pressure(bara) | Dynamic Viscosity(μPa·s) | Kinematic Viscosity(cSt) |
|---|---|---|---|---|---|
| Liquid | 103.99 | -169.16 | 0.00122 | 685.7 | 1.048 |
| Liquid | 105 | -168 | 0.00146 | 662.5 | 1.014 |
| Liquid | 115 | -158 | 0.00697 | 488.1 | 0.762 |
| Liquid | 125 | -148 | 0.0253 | 378.7 | 0.6033 |
| Liquid | 135 | -138 | 0.0739 | 305.5 | 0.4971 |
| Liquid | 145 | -128 | 0.183 | 253.8 | 0.4221 |
| Liquid | 155 | -118 | 0.398 | 215.7 | 0.367 |
| Liquid | 165 | -108 | 0.777 | 186.4 | 0.3248 |
| Liquid | 175 | -98.2 | 1.39 | 163 | 0.2913 |
| Liquid | 185 | -88.2 | 2.33 | 143.9 | 0.2642 |
| Liquid | 195 | -78.2 | 3.69 | 127.7 | 0.2413 |
| Liquid | 205 | -68.2 | 5.56 | 113.8 | 0.2218 |
| Liquid | 215 | -58.2 | 8.05 | 101.4 | 0.2045 |
| Liquid | 225 | -48.2 | 11.3 | 90.22 | 0.1891 |
| Liquid | 235 | -38.2 | 15.3 | 79.89 | 0.1748 |
| Liquid | 245 | -28.2 | 20.4 | 70.14 | 0.1614 |
| Liquid | 255 | -18.2 | 26.5 | 60.69 | 0.1486 |
| Liquid | 265 | -8.1 | 33.9 | 51.11 | 0.1358 |
| Liquid | 275 | 1.9 | 42.8 | 40.4 | 0.1221 |
| Gas | 103.99 | -169.16 | 0.00122 | 0.773 | 195.2 |
| Gas | 105 | -168.2 | 0.00146 | 1.001 | 213.8 |
| Gas | 115 | -158.2 | 0.00697 | 2.734 | 133.5 |
| Gas | 125 | -148.2 | 0.0253 | 3.826 | 55.98 |
| Gas | 135 | -138.2 | 0.0739 | 4.558 | 24.55 |
| Gas | 145 | -128.2 | 0.183 | 5.089 | 11.83 |
| Gas | 155 | -118.2 | 0.398 | 5.511 | 6.261 |
| Gas | 165 | -108.2 | 0.777 | 5.88 | 3.599 |
| Gas | 175 | -98.2 | 1.39 | 6.228 | 2.22 |
| Gas | 185 | -88.2 | 2.33 | 6.577 | 1.452 |
| Gas | 195 | -78.2 | 3.69 | 6.941 | 0.9976 |
| Gas | 205 | -68.2 | 5.56 | 7.334 | 0.7136 |
| Gas | 215 | -58.2 | 8.05 | 7.769 | 0.5278 |
| Gas | 225 | -48.2 | 11.3 | 8.261 | 0.4013 |
| Gas | 235 | -38.2 | 15.3 | 8.834 | 0.312 |
| Gas | 245 | -28.2 | 20.4 | 9.525 | 0.247 |
| Gas | 255 | -18.2 | 26.5 | 10.4 | 0.198 |
| Gas | 265 | -8.1 | 33.9 | 11.63 | 0.1602 |
| Gas | 275 | 1.9 | 42.8 | 13.77 | 0.1294 |
Source: engineeringtoolbox.com
Viscosity Trends
Liquid ethylene: Dynamic viscosity decreases with increasing temperature — from 685.7 μPa·s at 104 K to 40.40 μPa·s at 275 K. This is characteristic of liquids, where higher thermal energy reduces intermolecular resistance to flow.
Gaseous ethylene: Dynamic viscosity increases with increasing temperature — from 0.773 μPa·s at 104 K to 13.77 μPa·s at 275 K. This behavior is typical for gases, where higher molecular velocities enhance momentum transfer between layers.
Dynamic Viscosity Unit Conversions
The following conversions are commonly used when working with ethylene viscosity data:
| Unit | Equivalent |
|---|---|
| 1 cP (centipoise) | 0.001 Pa·s = 0.01 P = 0.01 g/(cm·s) = 6.72197×10⁻⁴ lb/(ft·s) = 2.4191 lb/(ft·h) |
| 1 lb/(ft·h) | 0.00027778 lb/(ft·s) = 0.00041338 Pa·s = 0.0041338 P = 0.41338 cP |
| 1 lb/(ft·s) | 3600 lb/(ft·h) = 1.48816 Pa·s = 14.8816 P = 1488.16 cP |
| 1 kg/(m·s) | 1 Pa·s = 1 (N·s)/m² = 10 P = 1000 cP = 0.672197 lb/(ft·s) = 2419.09 lb/(ft·h) |
Kinematic Viscosity Unit Conversions
| Unit | Equivalent |
|---|---|
| 1 cm²/s | 1 St (Stokes) = 100 cSt = 1×10⁻⁴ m²/s = 1.07639×10⁻³ ft²/s |
| 1 cSt (centistokes) | 1 mm²/s = 1×10⁻⁶ m²/s = 1.07639×10⁻⁵ ft²/s |
| 1 ft²/s | 3600 ft²/h = 0.09290304 m²/s = 92903.04 cSt |
| 1 ft²/h | 2.7778×10⁻⁴ ft²/s = 2.58064×10⁻⁵ m²/s = 25.8064 cSt |
Related Ethylene Properties
For a complete understanding of ethylene thermophysical behavior, refer to the following companion pages:
- Density and Specific Weight — varies significantly near the boiling point
- Specific Heat (Heat Capacity) — temperature-dependent energy storage
- Thermal Conductivity — heat transfer characteristics