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Water Thermophysical Properties Guide

Master water properties for engineering calculations. Explore density, viscosity, specific heat, and thermal conductivity with interactive visualizations based on IAPWS-IF97 standards.

Enginist Engineering Team
Professional mechanical engineers specializing in HVAC systems, fluid mechanics, and thermodynamics with expertise in heat transfer calculations.
Reviewed by Licensed Professional Engineers
Published: November 3, 2025
Updated: November 26, 2025

Water Thermophysical Properties Guide

Quick AnswerWhat are water's thermophysical properties?
Look up water properties per IAPWS-IF97 at operating temperature. At 20°C: density 998.2 kg/m³, specific heat 4182 J/kg·K, viscosity 1.002×10⁻³ Pa·s, thermal conductivity 0.598 W/m·K.
Example

Viscosity drops 65% from 20°C to 80°C - affects pressure drop calculations by ~35%

Introduction

Water's physical properties are far from constant. Between 0°C and 100°C, viscosity drops by 85%, density decreases by 4%, and thermal conductivity increases by 20%. These variations directly impact every HVAC, piping, and heat transfer calculation you perform.

Consider this scenario: you're designing a heating system with water circulating at 80°C, but you use property values from a 20°C reference table. Your viscosity is wrong by 65%—which translates to a 35% error in pressure drop calculations. That mistake could lead to undersized pumps, inadequate flow rates, and a system that never reaches design conditions.

This guide provides accurate water property data based on IAPWS-IF97 (the international standard), explains how temperature affects each property, and shows you how to apply these values correctly in real engineering calculations.

Quick Reference: Water Properties at Common Temperatures

Water properties vary significantly with temperature. Here are the essential values engineers need most frequently:

Properties at 20°C (Standard Reference)

PropertySymbolValueUnit
Densityρ998.2kg/m³
Specific Heatcp4,182J/(kg·K)
Dynamic Viscosityμ1.002 × 10⁻³Pa·s
Kinematic Viscosityν1.004 × 10⁻⁶m²/s
Thermal Conductivityk0.598W/(m·K)
Prandtl NumberPr7.0

Core Engineering Formulas

Heat Transfer Rate: Q=m˙×cp×ΔTQ = \dot{m} \times c_p \times \Delta T

Reynolds Number (flow regime): Re=ρvDμ=vDνRe = \frac{\rho v D}{\mu} = \frac{v D}{\nu}

Pressure Drop (Darcy-Weisbach): ΔP=f×LD×ρv22\Delta P = f \times \frac{L}{D} \times \frac{\rho v^2}{2}

Worked Example

Heating System Heat Transfer Calculation

Given:

  • Mass flow rate: ṁ = 2 kg/s
  • Inlet temperature: 60°C
  • Outlet temperature: 80°C

Step 1: Find average temperature Tavg=60+802=70°CT_{avg} = \frac{60 + 80}{2} = 70°C

Step 2: Look up properties at 70°C

  • Specific heat: cp = 4,190 J/(kg·K)

Step 3: Calculate heat transfer Q=2×4190×(8060)=167,600 W=167.6 kWQ = 2 \times 4190 \times (80 - 60) = 167,600 \text{ W} = \textbf{167.6 kW}

Why accuracy matters: Using cp = 4,000 J/(kg·K) (a rough approximation) would give 160 kW—a 4.5% error that compounds through equipment selection.

Density

How Density Changes with Temperature

Water density follows a unique pattern: it increases as temperature rises from 0°C, reaches maximum at approximately 4°C, then decreases continuously as temperature increases further.

Polynomial Approximation (0-100°C): ρ(T)=999.84+0.06426T0.0085043T2+0.000063T3\rho(T) = 999.84 + 0.06426T - 0.0085043T^2 + 0.000063T^3

Where T is temperature in °C, ρ is density in kg/m³.

Density Reference Table

Temperature (°C)Density (kg/m³)Temperature (°C)Density (kg/m³)
0999.860983.2
41000.0 (max)70977.8
10999.780971.8
20998.290965.3
30995.6100958.4
40992.2150917.0
50988.0200864.7

Thermal Expansion

The volumetric expansion coefficient quantifies how much water expands per degree of temperature increase:

β=1ρdρdT\beta = -\frac{1}{\rho}\frac{d\rho}{dT}

Temperatureβ (× 10⁻⁴ K⁻¹)
20°C2.1
40°C3.8
60°C5.2
80°C6.4

Expansion Tank Example:

1000 liters of water heated from 20°C to 80°C:

ΔV=V0×ρ20ρ80ρ20=1000×998.2971.8998.2=26.4 L\Delta V = V_0 \times \frac{\rho_{20} - \rho_{80}}{\rho_{20}} = 1000 \times \frac{998.2 - 971.8}{998.2} = \textbf{26.4 L}

This volume expansion determines your expansion tank sizing requirements.

Specific Heat Capacity

Nearly Constant Across HVAC Temperatures

Specific heat (cp) represents the energy required to raise 1 kg of water by 1 K. Unlike viscosity, specific heat varies minimally across the 0-100°C range:

Temperature (°C)cp (J/(kg·K))
04,217
204,182
354,178 (minimum)
604,185
804,197
1004,216

Engineering Practice:

For most HVAC calculations (0-100°C range):

  • Use cp = 4,186 J/(kg·K) (average value)
  • Maximum error: less than 1%

Conversion to Imperial: cp = 4.186 kJ/(kg·K) = 1.0 BTU/(lb·°F)

Heat Transfer Calculation

Q=m˙×cp×ΔTQ = \dot{m} \times c_p \times \Delta T

Example: 5 kg/s flow with 15°C temperature rise:

Q=5×4186×15=313,950 W=314 kWQ = 5 \times 4186 \times 15 = 313,950 \text{ W} = \textbf{314 kW}

Viscosity

The Property That Changes Most

Viscosity measures a fluid's resistance to flow. For water, viscosity decreases dramatically with temperature—an 85% reduction from 0°C to 100°C. This is the most temperature-sensitive property in HVAC calculations.

Dynamic Viscosity Table

Temperature (°C)μ (× 10⁻³ Pa·s)μ (cP)
01.7871.787
101.3071.307
201.0021.002
300.7980.798
400.6530.653
500.5470.547
600.4670.467
800.3550.355
1000.2820.282

Kinematic Viscosity

Kinematic viscosity is dynamic viscosity divided by density:

ν=μρ\nu = \frac{\mu}{\rho}

Temperature (°C)ν (× 10⁻⁶ m²/s)
01.787
201.004
400.658
600.475
800.365
1000.294

Kinematic viscosity simplifies Reynolds number calculations:

Re=vDνRe = \frac{vD}{\nu}

Thermal Conductivity

Increases with Temperature

Thermal conductivity (k) measures water's ability to conduct heat. Unlike viscosity, it increases with temperature (about 20% from 0°C to 100°C):

Temperature (°C)k (W/(m·K))
00.561
200.598
400.628
600.651
800.668
1000.679

Application in Heat Transfer

Convection coefficient (Dittus-Boelter correlation):

Nu=0.023×Re0.8×Pr0.4Nu = 0.023 \times Re^{0.8} \times Pr^{0.4}

h=Nu×kDh = \frac{Nu \times k}{D}

Higher thermal conductivity at elevated temperatures improves heat transfer coefficients.

Dimensionless Numbers

Prandtl Number

The Prandtl number relates momentum diffusivity to thermal diffusivity:

Pr=μ×cpk=ναPr = \frac{\mu \times c_p}{k} = \frac{\nu}{\alpha}

Temperature (°C)Pr
013.5
207.0
404.3
603.0
802.2
1001.7

Interpretation:

  • Pr > 1: Momentum diffuses faster than heat (typical for water)
  • Pr ≈ 1: Similar diffusion rates
  • Pr < 1: Heat diffuses faster (liquid metals)

Reynolds Number and Flow Regime

Re=ρvDμ=vDνRe = \frac{\rho v D}{\mu} = \frac{v D}{\nu}

Flow regimes:

  • Laminar: Re < 2,300 (smooth, layered flow)
  • Transitional: 2,300 < Re < 4,000
  • Turbulent: Re > 4,000 (chaotic, mixing flow)

Example: Water at 20°C, 1.5 m/s velocity, 50 mm pipe:

Re=1.5×0.051.004×106=74,700 (turbulent)Re = \frac{1.5 \times 0.05}{1.004 \times 10^{-6}} = 74,700 \text{ (turbulent)}

Same conditions at 80°C:

Re=1.5×0.050.365×106=205,500 (more turbulent)Re = \frac{1.5 \times 0.05}{0.365 \times 10^{-6}} = 205,500 \text{ (more turbulent)}

Lower viscosity at higher temperature significantly increases Reynolds number.

Saturation Properties

Vapor Pressure

The saturation pressure is the pressure at which water boils at a given temperature:

Temperature (°C)Saturation Pressure (kPa)(bar)
202.340.023
407.380.074
6019.940.199
8047.390.474
100101.331.013
120198.51.985

Antoine Equation (approximation):

log10(Psat)=8.071311730.63233.426+T\log_{10}(P_{sat}) = 8.07131 - \frac{1730.63}{233.426 + T}

Engineering Implications

1. Cavitation Prevention: System pressure must exceed saturation pressure at the hottest point: Psystem>Psat(Tmax)P_{system} > P_{sat}(T_{max})

2. Expansion Tank Pre-charge: Set above saturation pressure at maximum operating temperature.

3. Pump NPSH: Net Positive Suction Head must account for vapor pressure.

Engineering Applications

HVAC Heating System Design

Radiator Loop Heat Transfer

Given:

  • Flow rate: 0.5 kg/s
  • Supply temperature: 80°C
  • Return temperature: 60°C

Calculation:

Average temperature: 70°C Properties at 70°C: cp = 4,190 J/(kg·K)

Q=0.5×4190×(8060)=41.9 kWQ = 0.5 \times 4190 \times (80 - 60) = \textbf{41.9 kW}

Piping Pressure Drop

100m Pipeline Pressure Drop

Given:

  • Pipe: DN50 (ID = 52.5 mm)
  • Velocity: 2 m/s
  • Temperature: 60°C

Properties at 60°C:

  • ρ = 983 kg/m³
  • ν = 0.475 × 10⁻⁶ m²/s

Step 1: Reynolds Number Re=2×0.05250.475×106=221,000 (turbulent)Re = \frac{2 \times 0.0525}{0.475 \times 10^{-6}} = 221,000 \text{ (turbulent)}

Step 2: Friction Factor (Blasius) f=0.316Re0.25=0.3162210000.25=0.0146f = \frac{0.316}{Re^{0.25}} = \frac{0.316}{221000^{0.25}} = 0.0146

Step 3: Pressure Drop ΔP=0.0146×1000.0525×983×222=54,700 Pa = 0.55 bar\Delta P = 0.0146 \times \frac{100}{0.0525} \times \frac{983 \times 2^2}{2} = \textbf{54,700 Pa = 0.55 bar}

Expansion Tank Sizing

500L System Expansion

Given:

  • System volume: 500 L
  • Cold fill: 15°C
  • Maximum operating: 85°C

Density values:

  • ρ₁₅ = 999.1 kg/m³
  • ρ₈₅ = 968.6 kg/m³

Expansion volume: ΔV=500×999.1968.6999.1=15.3 L\Delta V = 500 \times \frac{999.1 - 968.6}{999.1} = \textbf{15.3 L}

With acceptance factor (~1.5-2×), specify 25-30 L expansion tank.

Our calculations are based on proven mathematical methods.

Conclusion

Accurate water properties form the foundation of every heat transfer, fluid flow, and system sizing calculation. The key insight is that viscosity dominates temperature sensitivity—dropping 85% across the 0-100°C range—while specific heat remains remarkably stable.

Export as PDF — Generate professional reports for documentation, client presentations, or permit submissions.

Using correct temperature-dependent properties isn't optional; it's the difference between systems that perform as designed and those that underperform from day one.

What Are the Key Takeaways from?

  • Always use properties at operating temperature—room temperature values cause significant errors in hot water calculations
  • Viscosity is most temperature-sensitive—65% lower at 80°C vs 20°C, directly affecting pressure drop by ~35%
  • Density variation drives expansion—~4% change from 0-100°C determines expansion tank sizing
  • Specific heat is nearly constant—use 4,186 J/(kg·K) for 0-100°C range with less than 1% error
  • IAPWS-IF97 is the international standard—ensures consistent property values across software and references
  • Glycol solutions require separate data—viscosity doubles, specific heat drops 20%, thermal conductivity drops 25%
  • Calculate Reynolds number first—determines flow regime (laminar vs turbulent) before pressure drop calculations

Where Can You Learn More About?

What Are the References for & Standards?

Primary Standards

IAPWS-IF97 Industrial Formulation 1997 for the Thermodynamic Properties of Water and Steam. The internationally accepted standard for water and steam property calculations, valid for temperatures 0-800°C and pressures 0-100 MPa.

ASHRAE Fundamentals Handbook Chapter 33: Physical Properties of Materials. Contains water property tables and thermodynamic data specifically curated for HVAC applications.

Supporting Standards & Guidelines

NIST REFPROP Reference Fluid Thermodynamic and Transport Properties Database. The definitive software for accurate fluid property calculations used in research and engineering.

ISO 80000 International Standard for Quantities and Units. Defines standard units for fluid mechanics and thermophysical property calculations.

Further Reading

Note: Standards are regularly updated. Always verify you're using the current edition applicable to your project and jurisdiction.


Disclaimer: This guide provides general technical information based on international engineering standards. Water property data uses polynomial approximations of IAPWS-IF97 formulations accurate to within ±0.5% for the 0-100°C range. Always verify calculations with applicable standards and consult licensed professional engineers for critical applications.

Frequently Asked Questions

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