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Water Steam Thermal Diffusivity

Reference data and engineering information about water steam thermal diffusivity for thermodynamics applications.

watersteamthermaldiffusivity

Overview

Engineering reference data for Water Steam Thermal Diffusivity in thermodynamics.

Key Formulas

First Law

ΔU=QW\Delta U = Q - W

Energy is conserved — heat added minus work done.

Ideal Gas Law

PV=nRTPV = nRT

Relates pressure, volume, and temperature of an ideal gas.

Heat Transfer

Q=mcΔTQ = mc\Delta T

Sensible heat transfer.

Carnot Efficiency

η=1TC/TH\eta = 1 - T_C/T_H

Maximum efficiency between two temperatures.

Variables

SymbolDescriptionUnit
UUInternal energyJ
QQHeatJ
WWWorkJ
PPPressurePa
VVVolume
TTTemperatureK

Thermal Diffusivity at Atmospheric Pressure

Water thermal diffusivity data at atmospheric pressure (1 bara / 14.5 psia) for both liquid and gas phases.

19 rows
Thermal diffusivity of water at atmospheric pressure (1 bara)
State
Temperature(°C)
Temperature(°F)
Thermal Diffusivity(×10⁻⁶ m²/s)
Thermal Diffusivity(×10⁻⁶ ft²/s)
Liquid0320.1321.42
Liquid5400.1351.45
Liquid10500.1381.48
Liquid20750.1431.56
Liquid251000.1461.62
Liquid301250.1481.67
Liquid501500.1551.72
Liquid751750.1621.76
Liquid1002000.1681.79
Gas10025020.2251
Gas12530024299
Gas15035027.9349
Gas17540032.2403
Gas20050036.6522
Gas25060046.4654
Gas30070057.2801
Gas35080069962
Gas400900821137
Gas50010001111327

Source: engineeringtoolbox.com

Thermal Diffusivity vs Temperature and Pressure

Thermal diffusivity of water at various pressures including 1 bara, 10 bara, and 100 bara.

44 rows
Thermal diffusivity of water vs. temperature at 1 and 10 bara pressure
State
Temperature(°C)
Pressure(bara)
Thermal Diffusivity(×10⁻⁶ m²/s)
Thermal Diffusivity(ft²/h)
Liquid0.0110.13170.005104
Liquid6.910.13620.005277
Liquid26.910.14630.005669
Liquid46.910.1540.005968
Liquid66.910.16020.006207
Liquid86.910.16510.006397
Liquid99.6110.16760.006493
Gas99.61119.990.7748
Gas107121.20.8213
Gas127124.40.9454
Gas177132.671.266
Gas227141.791.619
Gas277151.982.014
Gas327163.32.453
Gas377175.772.936
Gas427189.363.463
Gas4771104.14.032
Gas5271119.84.644
Gas6271154.55.985
Gas72711937.479
Gas8271235.39.118
Gas9271281.310.9
Liquid0.01100.1320.00511
Liquid6.9100.13640.00528
Liquid26.9100.14640.00567
Liquid46.9100.15410.00597
Liquid66.9100.16030.00621
Liquid86.9100.16520.0064
Liquid107100.16890.00654
Liquid127100.17130.00664
Liquid177100.1720.00667
Liquid179.9100.17180.00666
Gas179.9102.4950.0967
Gas227103.7240.1443
Gas277104.8840.1893
Gas327106.0890.2359
Gas377107.3790.2859
Gas427108.770.3398
Gas4771010.270.3978
Gas5271011.870.4599
Gas6271015.380.5959
Gas7271019.280.7471
Gas8271023.560.9129
Gas9271028.21.09

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 (α0.130.17×106\alpha \approx 0.13 - 0.17 \times 10^{-6} 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 α\alpha jumps from 0.168×1060.168 \times 10^{-6} m²/s (liquid) to 20.2×10620.2 \times 10^{-6} 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:

FromToMultiply by
1 ft²/hm²/s2.581×1052.581 \times 10^{-5}
1 ft²/sm²/s0.092900.09290
1 m²/hm²/s2.7778×1042.7778 \times 10^{-4}
1 m²/sft²/s10.763910.7639
1 m²/sft²/h38750.138750.1

Interactive Charts

Water thermal diffusivity 1 bara C

Water thermal diffusivity 1 bara F

References