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Water Properties by Temperature — Reference

Density, specific weight, dynamic and kinematic viscosity, and vapor pressure of fresh water at atmospheric pressure. These four properties feed nearly every hydraulic calculation — Reynolds number, friction loss, settling velocity, and pump NPSH.

The Four Values You Actually Look Up

PropertySI (20°C)US (60°F)Where it is used
Density ρ998.2 kg/m³1.938 slug/ft³Momentum, drag, Reynolds number
Specific weight γ9.789 kN/m³62.37 lb/ft³Hydrostatic pressure, buoyancy, uplift
Kinematic viscosity ν1.003×10−6 m²/s1.21×10−5 ft²/sReynolds number, friction factor
Vapor pressure pv2.34 kPa abs0.256 psiaCavitation, NPSH available
The engineer's shortcut. At ordinary ambient temperatures, γ = 62.4 lb/ft³ (9.81 kN/m³) and ν = 1.0×10−6 m²/s are accurate to better than 1–2% and are what most design manuals assume. Reach for the full table when you are checking cavitation, cold-weather friction loss, or a settling / thickening process — those are the three places temperature genuinely bites.

SI Units — Fresh Water, 0 to 100°C

T (°C) ρ (kg/m³) γ (kN/m³) μ (×10−3 Pa·s) ν (×10−6 m²/s) pv (kPa abs)
0999.89.8061.7811.7850.61
51000.09.8071.5181.5190.87
10999.79.8041.3071.3061.23
15999.19.7981.1391.1391.70
20998.29.7891.0021.0032.34
25997.09.7770.8900.8933.17
30995.79.7640.7980.8004.24
40992.29.7300.6530.6587.38
50988.09.6890.5470.55312.33
60983.29.6420.4660.47419.92
70977.89.5890.4040.41331.16
80971.89.5300.3540.36447.34
90965.39.4660.3150.32670.10
100958.49.3990.2820.294101.33

US Customary — Fresh Water, 32 to 212°F

T (°F) ρ (slug/ft³) γ (lb/ft³) μ (×10−5 lb·s/ft²) ν (×10−5 ft²/s) pv (psia)
321.94062.423.7321.9240.0885
401.94062.433.2281.6640.122
501.94062.412.7301.4070.178
601.93862.372.3441.2100.256
701.93662.302.0341.0510.363
801.93462.221.7910.9260.507
1001.92762.001.4230.7390.949
1201.91861.711.1640.6071.69
1401.90861.380.9740.5112.89
1601.89661.000.8320.4394.74
1801.88360.580.7210.3837.51
2001.86960.120.6340.33911.52
2121.86059.830.5890.31714.70

Relationships

γ = ρg  ·  ν = μ/ρ  ·  Re = VL/ν

Use g = 9.807 m/s² (32.17 ft/s²). Note the unit trap in US customary work: density is in slug/ft³, not lb/ft³. The familiar 62.4 lb/ft³ is specific weight γ, not density ρ. Mixing the two is the single most common error in US-unit fluid calculations — they differ by the factor g = 32.17.

Where Temperature Actually Changes the Answer

CalculationPropertySensitivity
Hydrostatic pressure, uplift, buoyancyγNegligible — under 1% across 0–30°C
Reynolds number, friction factorνStrong — ν nearly halves from 5°C to 30°C
Pump NPSH available / cavitationpvStrong — pv rises ~5× from 5°C to 30°C
Particle settling (Stokes range)μStrong — settling velocity scales as 1/μ
Cold water is not the conservative assumption. Cold water is more viscous, so it gives a lower Reynolds number and higher friction loss — conservative for pipe sizing. But warm water has a much higher vapor pressure, so it is the governing case for cavitation and NPSH. Check pump suction at the warmest expected water temperature and pipe friction at the coldest.

Sources: White, F.M., Fluid Mechanics, Table A.1 (water properties). Munson, Young & Okiishi, Fundamentals of Fluid Mechanics, Tables B.1 and B.2. Vapor pressures follow the IAPWS-IF97 / NIST steam-table formulation. Values are for fresh water at atmospheric pressure; dissolved solids, and salinity in particular, shift density and vapor pressure and warrant source-specific data.

Checking a flow regime? Open the Reynolds calculator → · Pipe friction? Darcy-Weisbach · Settling? Stokes settling card.

Related cheat sheets and tools

Kinematic viscosity from this card feeds the Reynolds number calculator and the flow-regime thresholds. Pair it with absolute roughness for Darcy-Weisbach head loss, or with the Stokes settling card for clarifier and grit-chamber design. Vapor pressure is the term you need for pump power and NPSH checks. For full network modeling, see HydroComplete.

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