Table of Contents
Water Thermophysical Properties Guide
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)
| Property | Symbol | Value | Unit |
|---|---|---|---|
| Density | ρ | 998.2 | kg/m³ |
| Specific Heat | cp | 4,182 | J/(kg·K) |
| Dynamic Viscosity | μ | 1.002 × 10⁻³ | Pa·s |
| Kinematic Viscosity | ν | 1.004 × 10⁻⁶ | m²/s |
| Thermal Conductivity | k | 0.598 | W/(m·K) |
| Prandtl Number | Pr | 7.0 | — |
Core Engineering Formulas
Heat Transfer Rate:
Reynolds Number (flow regime):
Pressure Drop (Darcy-Weisbach):
Worked Example
Temperature Matters
Water viscosity at 80°C is 65% lower than at 20°C. This single factor can reduce pressure drop by 35%, completely changing pump selection. Always use properties at your actual operating temperature.
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):
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) |
|---|---|---|---|
| 0 | 999.8 | 60 | 983.2 |
| 4 | 1000.0 (max) | 70 | 977.8 |
| 10 | 999.7 | 80 | 971.8 |
| 20 | 998.2 | 90 | 965.3 |
| 30 | 995.6 | 100 | 958.4 |
| 40 | 992.2 | 150 | 917.0 |
| 50 | 988.0 | 200 | 864.7 |
Thermal Expansion
The volumetric expansion coefficient quantifies how much water expands per degree of temperature increase:
| Temperature | β (× 10⁻⁴ K⁻¹) |
|---|---|
| 20°C | 2.1 |
| 40°C | 3.8 |
| 60°C | 5.2 |
| 80°C | 6.4 |
Expansion Tank Example:
1000 liters of water heated from 20°C to 80°C:
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)) |
|---|---|
| 0 | 4,217 |
| 20 | 4,182 |
| 35 | 4,178 (minimum) |
| 60 | 4,185 |
| 80 | 4,197 |
| 100 | 4,216 |
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
Example: 5 kg/s flow with 15°C temperature rise:
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) |
|---|---|---|
| 0 | 1.787 | 1.787 |
| 10 | 1.307 | 1.307 |
| 20 | 1.002 | 1.002 |
| 30 | 0.798 | 0.798 |
| 40 | 0.653 | 0.653 |
| 50 | 0.547 | 0.547 |
| 60 | 0.467 | 0.467 |
| 80 | 0.355 | 0.355 |
| 100 | 0.282 | 0.282 |
Critical for Pressure Drop
Viscosity at 80°C is 65% lower than at 20°C. Using room temperature viscosity for hot water systems causes:
- Reynolds number underestimate: ~65%
- Friction factor error: ~15-20%
- Pressure drop overestimate: ~35%
Kinematic Viscosity
Kinematic viscosity is dynamic viscosity divided by density:
| Temperature (°C) | ν (× 10⁻⁶ m²/s) |
|---|---|
| 0 | 1.787 |
| 20 | 1.004 |
| 40 | 0.658 |
| 60 | 0.475 |
| 80 | 0.365 |
| 100 | 0.294 |
Kinematic viscosity simplifies Reynolds number calculations:
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)) |
|---|---|
| 0 | 0.561 |
| 20 | 0.598 |
| 40 | 0.628 |
| 60 | 0.651 |
| 80 | 0.668 |
| 100 | 0.679 |
Application in Heat Transfer
Convection coefficient (Dittus-Boelter correlation):
Higher thermal conductivity at elevated temperatures improves heat transfer coefficients.
Dimensionless Numbers
Prandtl Number
The Prandtl number relates momentum diffusivity to thermal diffusivity:
| Temperature (°C) | Pr |
|---|---|
| 0 | 13.5 |
| 20 | 7.0 |
| 40 | 4.3 |
| 60 | 3.0 |
| 80 | 2.2 |
| 100 | 1.7 |
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
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:
Same conditions at 80°C:
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) |
|---|---|---|
| 20 | 2.34 | 0.023 |
| 40 | 7.38 | 0.074 |
| 60 | 19.94 | 0.199 |
| 80 | 47.39 | 0.474 |
| 100 | 101.33 | 1.013 |
| 120 | 198.5 | 1.985 |
Antoine Equation (approximation):
Engineering Implications
1. Cavitation Prevention: System pressure must exceed saturation pressure at the hottest point:
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
Piping Pressure Drop
Expansion Tank Sizing
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?
- Heat Loss Calculator Guide - Building heating load calculations using water properties
- Expansion Tank Guide - Thermal expansion calculations for closed systems
- Cooling Load Guide - Chilled water system calculations
- Water Properties Calculator - Interactive calculator for instant property lookup
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
- NIST Physical Measurement Laboratory - Authoritative measurement data and standards
- IAPWS Technical Guidance Documents - Detailed implementation guidance for property calculations
- CoolProp Open-Source Library - Free thermophysical property library implementing IAPWS-IF97
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.