Water Steam Thermal Diffusivity
Reference data and engineering information about water steam thermal diffusivity for thermodynamics applications.
Overview
Engineering reference data for Water Steam Thermal Diffusivity in thermodynamics.
Key Formulas
First Law
Energy is conserved — heat added minus work done.
Ideal Gas Law
Relates pressure, volume, and temperature of an ideal gas.
Heat Transfer
Sensible heat transfer.
Carnot Efficiency
Maximum efficiency between two temperatures.
Variables
| Symbol | Description | Unit |
|---|---|---|
| Internal energy | J | |
| Heat | J | |
| Work | J | |
| Pressure | Pa | |
| Volume | m³ | |
| Temperature | K |
Thermal Diffusivity at Atmospheric Pressure
Water thermal diffusivity data at atmospheric pressure (1 bara / 14.5 psia) for both liquid and gas phases.
State | Temperature(°C) | Temperature(°F) | Thermal Diffusivity(×10⁻⁶ m²/s) | Thermal Diffusivity(×10⁻⁶ ft²/s) |
|---|---|---|---|---|
| Liquid | 0 | 32 | 0.132 | 1.42 |
| Liquid | 5 | 40 | 0.135 | 1.45 |
| Liquid | 10 | 50 | 0.138 | 1.48 |
| Liquid | 20 | 75 | 0.143 | 1.56 |
| Liquid | 25 | 100 | 0.146 | 1.62 |
| Liquid | 30 | 125 | 0.148 | 1.67 |
| Liquid | 50 | 150 | 0.155 | 1.72 |
| Liquid | 75 | 175 | 0.162 | 1.76 |
| Liquid | 100 | 200 | 0.168 | 1.79 |
| Gas | 100 | 250 | 20.2 | 251 |
| Gas | 125 | 300 | 24 | 299 |
| Gas | 150 | 350 | 27.9 | 349 |
| Gas | 175 | 400 | 32.2 | 403 |
| Gas | 200 | 500 | 36.6 | 522 |
| Gas | 250 | 600 | 46.4 | 654 |
| Gas | 300 | 700 | 57.2 | 801 |
| Gas | 350 | 800 | 69 | 962 |
| Gas | 400 | 900 | 82 | 1137 |
| Gas | 500 | 1000 | 111 | 1327 |
Source: engineeringtoolbox.com
Thermal Diffusivity vs Temperature and Pressure
Thermal diffusivity of water at various pressures including 1 bara, 10 bara, and 100 bara.
State | Temperature(°C) | Pressure(bara) | Thermal Diffusivity(×10⁻⁶ m²/s) | Thermal Diffusivity(ft²/h) |
|---|---|---|---|---|
| Liquid | 0.01 | 1 | 0.1317 | 0.005104 |
| Liquid | 6.9 | 1 | 0.1362 | 0.005277 |
| Liquid | 26.9 | 1 | 0.1463 | 0.005669 |
| Liquid | 46.9 | 1 | 0.154 | 0.005968 |
| Liquid | 66.9 | 1 | 0.1602 | 0.006207 |
| Liquid | 86.9 | 1 | 0.1651 | 0.006397 |
| Liquid | 99.61 | 1 | 0.1676 | 0.006493 |
| Gas | 99.61 | 1 | 19.99 | 0.7748 |
| Gas | 107 | 1 | 21.2 | 0.8213 |
| Gas | 127 | 1 | 24.4 | 0.9454 |
| Gas | 177 | 1 | 32.67 | 1.266 |
| Gas | 227 | 1 | 41.79 | 1.619 |
| Gas | 277 | 1 | 51.98 | 2.014 |
| Gas | 327 | 1 | 63.3 | 2.453 |
| Gas | 377 | 1 | 75.77 | 2.936 |
| Gas | 427 | 1 | 89.36 | 3.463 |
| Gas | 477 | 1 | 104.1 | 4.032 |
| Gas | 527 | 1 | 119.8 | 4.644 |
| Gas | 627 | 1 | 154.5 | 5.985 |
| Gas | 727 | 1 | 193 | 7.479 |
| Gas | 827 | 1 | 235.3 | 9.118 |
| Gas | 927 | 1 | 281.3 | 10.9 |
| Liquid | 0.01 | 10 | 0.132 | 0.00511 |
| Liquid | 6.9 | 10 | 0.1364 | 0.00528 |
| Liquid | 26.9 | 10 | 0.1464 | 0.00567 |
| Liquid | 46.9 | 10 | 0.1541 | 0.00597 |
| Liquid | 66.9 | 10 | 0.1603 | 0.00621 |
| Liquid | 86.9 | 10 | 0.1652 | 0.0064 |
| Liquid | 107 | 10 | 0.1689 | 0.00654 |
| Liquid | 127 | 10 | 0.1713 | 0.00664 |
| Liquid | 177 | 10 | 0.172 | 0.00667 |
| Liquid | 179.9 | 10 | 0.1718 | 0.00666 |
| Gas | 179.9 | 10 | 2.495 | 0.0967 |
| Gas | 227 | 10 | 3.724 | 0.1443 |
| Gas | 277 | 10 | 4.884 | 0.1893 |
| Gas | 327 | 10 | 6.089 | 0.2359 |
| Gas | 377 | 10 | 7.379 | 0.2859 |
| Gas | 427 | 10 | 8.77 | 0.3398 |
| Gas | 477 | 10 | 10.27 | 0.3978 |
| Gas | 527 | 10 | 11.87 | 0.4599 |
| Gas | 627 | 10 | 15.38 | 0.5959 |
| Gas | 727 | 10 | 19.28 | 0.7471 |
| Gas | 827 | 10 | 23.56 | 0.9129 |
| Gas | 927 | 10 | 28.2 | 1.09 |
Source: engineeringtoolbox.com
Phase Transition Observations
Water undergoes a dramatic change in thermal diffusivity at the liquid-to-gas phase transition:
- Liquid water has relatively low thermal diffusivity ( m²/s), meaning heat transfers slowly through the liquid phase
- Steam has thermal diffusivity approximately 100-200 times higher than liquid water at the same temperature near the boiling point
- At atmospheric pressure, the transition occurs at 100°C (212°F) where jumps from m²/s (liquid) to m²/s (gas)
This significant difference is due to the much lower density of steam compared to liquid water, even though steam has lower thermal conductivity.
Unit Conversions
Common conversion factors for thermal diffusivity:
| From | To | Multiply by |
|---|---|---|
| 1 ft²/h | m²/s | |
| 1 ft²/s | m²/s | |
| 1 m²/h | m²/s | |
| 1 m²/s | ft²/s | |
| 1 m²/s | ft²/h |