Water and Steam Prandtl Number vs Temperature and Pressure

The Prandtl Number — Pr — is a dimensionless number approximating the ratio of momentum diffusivity (kinematic viscosity) to thermal diffusivity, and is often used in heat transfer and free and forced convection calculations.

The Prandtl number can be expressed as:

Pr = μ cp / k    (1)

where:

  • μ = absolute or dynamic viscosity (kg/(m·s)), (lbm/(ft·h))
  • cp = specific heat (J/(kg·K)), (Btu/lbm·°F)
  • k = thermal conductivity (W/(m·K)), (Btu/(h·ft²·°F/ft))

Below, Prandtl numbers of water at varying temperatures and 1, 10 and 100 bara (14.5, 145 and 1450 psia) are given in figures and tables.

Prandtl Number at 1 bara — °C

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Data from Engineering Toolbox — Water Prandtl Number. Liquid and gas phases at atmospheric pressure.

Prandtl Number at 1 bara — °F

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Data from Engineering Toolbox — Water Prandtl Number. Liquid and gas phases at atmospheric pressure.

Prandtl Number at 1, 10 and 100 bara (°C)

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Data from Engineering Toolbox — Water Prandtl Number. Solid lines = liquid; dashed lines = gas.

Prandtl Number at 1, 10 and 100 bara (°F)

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Data from Engineering Toolbox — Water Prandtl Number. Solid lines = liquid; dashed lines = gas.

Prandtl Number of Water
What Is the Prandtl Number?

The Prandtl number (Pr) is a dimensionless ratio of momentum diffusivity to thermal diffusivity. A value greater than 1 means the velocity boundary layer is thicker than the thermal boundary layer — the fluid resists shear flow more than it resists heat conduction. Liquid water at 20 °C has Pr ≈ 7, meaning heat diffuses roughly seven times more slowly than momentum through the fluid.

Effect of Temperature

For liquid water, Pr falls steeply with rising temperature — from about 13.6 at 0 °C (32 °F) to 1.76 at 100 °C (212 °F) — because dynamic viscosity decreases faster than thermal conductivity. This strong temperature dependence means Prandtl number must be evaluated at actual operating temperature, not at a nominal design point.

For steam (gas phase), Pr is near 0.9–1.0 and only weakly dependent on temperature over a wide range, reflecting that momentum and thermal diffusivity are similar in magnitude for gases.

Effect of Pressure and the Critical Point

At elevated pressures the boiling point rises, so liquid water can exist above 100 °C and continues to have elevated Prandtl numbers. Near the critical point of water (373.946 °C / 705 °F, 220.6 bar) specific heat diverges, causing an anomalous spike in Pr visible in the 100 bara data. This critical-point behavior has practical implications for supercritical water reactors and supercritical boilers.

Use in Heat Transfer Correlations

The Prandtl number appears in Nusselt number correlations for forced convection. The Dittus-Boelter equation for turbulent pipe flow is:

Nu = 0.023 × Re0.8 × Prn

where n = 0.4 for heating and n = 0.3 for cooling. For liquid water systems, the large variation of Pr with temperature means heat transfer coefficients are significantly higher at elevated temperatures, which is an important consideration in boiler and heat exchanger design.

Note: At the liquid-gas phase boundary, Pr is discontinuous — the liquid and gas values at the same saturation temperature differ substantially (e.g., 1.76 vs 1.035 at 100 °C, 1 bara). The tables and charts show both values at each phase boundary.

Water Prandtl Number Table: Atmospheric Pressure (1 bara)

Prandtl number of water at atmospheric pressure, temperature given as K, °C or °F:

State SI (°C) Imperial (°F)
T (K) T (°C) Pr (−) T (K) T (°F) Pr (−)
Liquid273013.62733213.6
278511.22784011.5
283109.46283509.46
293206.99297756.31
298256.133111004.56
303305.433251253.45
323503.563391502.74
348752.393531752.25
3731001.763662001.88
Gas3731001.033942500.999
3981250.9964223000.978
4231500.9784503500.964
4481750.9654784000.970
4732000.9585335000.945
5232500.9475896000.937
5733000.9396447000.930
6233500.9327008000.923
6734000.9267559000.917
7735000.91681110000.912
Water Prandtl Number Table: 1, 10 and 100 bara

Prandtl number of water at given temperatures and 1, 10 and 100 bara (14.5, 145 and 1450 psia):

State T (K) T (°C) T (°F) Pressure (bara) Pressure (psia) Pr (−)
1 bara (14.5 psia)
Liquid273.160.0132.02114.513.60
2806.944.3114.510.53
30026.980.3114.55.856
32046.9116114.53.785
34066.9152114.52.687
36086.9188114.52.040
372.75699.61211.3114.51.760
Gas372.75699.61211.3114.51.035
380107224114.51.020
400127260114.50.9938
450177350114.50.9644
500227440114.50.9512
550277530114.50.9425
600327620114.50.9354
650377710114.50.9289
700427800114.50.9231
750477890114.50.9179
800527980114.50.9132
9006271160114.50.9053
10007271340114.50.8992
11008271520114.50.8942
12009271700114.50.8897
10 bara (145 psia)
Liquid273.160.0132.021014513.55
2806.944.31014510.50
30026.980.3101455.847
32046.9116101453.781
34066.9152101452.685
36086.9188101452.040
380107224101451.632
400127260101451.362
450177350101451.000
453.028179.9355.8101450.9873
Gas453.028179.9355.8101451.167
500227440101451.010
550277530101450.9694
600327620101450.9509
650377710101450.9395
700427800101450.9308
750477890101450.9235
800527980101450.9173
9006271160101450.9069
10007271340101450.8990
11008271520101450.8928
12009271700101450.8875
100 bara (1450 psia)
Liquid273.160.0132.018100145013.12
2806.944.3100145010.23
30026.980.310014505.761
32046.911610014503.746
34066.915210014502.669
36086.918810014502.030
38010722410014501.626
40012726010014501.358
45017735010014500.9967
50022744010014500.8531
55027753010014500.8366
584.147311.00591.7910014500.9349
Gas584.147311.00591.7910014501.841
60032762010014501.494
65037771010014501.168
70042780010014501.058
75047789010014501.003
80052798010014500.9686
900627116010014500.9251
1000727134010014500.8977
1100827152010014500.8789
1200927170010014500.8655

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