Sizes diaphragm, plain-steel and open vessels per the ASHRAE Handbook (HVAC Systems & Equipment) expansion-tank equations — with automatic gauge→absolute pressure conversion, glycol & pipe-expansion correction, and selection from standard manufacturer sizes.
System & Fluid
Step 01 – 03 · Vessel type, fluid & units
01Vessel Type
02Fluid
03Units
Glycol Concentration
% by volume · expansion correction (approx.)
System Volume
Step 04 · Direct entry or kW estimate
04Method
Total System Volume
All coils, pipes, equipment & buffer tanks · litres
Chiller / Boiler Rating
kW
Buffer / Storage Volume
litres
Estimate ≈ 4.4 L/kW + buffer, +10% allowance — confirm actual volume with contractor.
Temperatures
Step 05 · Operating range
05Highest Temp (t₂)
Hottest the vessel sees · °C
Lowest Temp (t₁)
Fill / coldest · °C
Pressures & Margin
Step 06 – 09 · Each pressure tagged gauge or absolute
Enter system parameters and press Size Vessel to calculate the required expansion vessel volume and recommended standard size.
Calculation Breakdown
ASHRAE expansion-tank method
Sizing complete. Print or save as PDF — the layout reformats automatically for A4.
Notes. For internal use only — not for circulation. Valid for clean fresh water 1–99°C in HVAC systems. Pressures use gauge by default (atmospheric excluded); the tool converts to absolute for the acceptance term per ASHRAE. Pre-charge should equal the minimum (fill) pressure at the vessel. If static head exceeds 400 kPa, confirm the vessel pressure rating with the manufacturer. Glycol expansion is approximate — verify against the fluid supplier’s density data. Final selection is subject to engineering check and manufacturer confirmation.