Construction Engineering Verified Calculator

Compressed Air Receiver Sizing Calculator

Size an air receiver and find how much free air it releases over the pressure swing, the run time it gives the network, and the volume a required run time needs.

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Geometry-based calculation.Receiver volume, free-air delivery and run time from the pressure swing, computed isothermally from Boyle’s law and the ideal gas law.

Receiver pressure swing and free-air delivery A receiver vessel shown at its maximum and minimum pressure, the usable pressure swing between them, and the free air that swing releases against the network demand. P₁ max bar g P₂ min bar g ΔP FREE AIR L DEMAND L/s run time required
  • Receiver / air
  • Pressure and dimension
  • Network demand
A receiver vessel shown at its maximum and minimum pressure, the usable pressure swing between them, and the free air that swing releases against the network demand. Schematic only — not to scale and not a construction drawing. Both rectangles are the SAME vessel at the two ends of the pressure swing, not two separate tanks. Isothermal sizing. This tool sizes a receiver only; it says nothing about the compressor, its control, its duty cycle, or any pressure-vessel code.

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What this calculator does

A compressor delivers a steady flow, but a receiver is sized for the opposite question: how much free air it can hand back before the network pressure falls too far. That is what decides whether a tool keeps running between compressor cycles — and what sizes the vessel.

How to use it

  1. Enter the free air the network actually draws between compressor cycles, not the compressor’s rated output.
  2. Enter the vessel volume you are considering and the pressures the pressure switch cycles between.
  3. Enter the atmospheric pressure for your site and the gas temperature inside the receiver.
  4. The result reports the volume you would need for the run time you asked for, so you can compare it with what you have.

Governing formula

Governing Formula
V_free = V × (P₁_abs − P₂_abs) / P_atm

Where:

  • V_free = Free air released over the swing, litres
  • V = Receiver volume, litres
  • P₁_abs, P₂_abs = Maximum and minimum absolute pressure, bar
  • P_atm = Atmospheric (reference) pressure, bar absolute

Derived Equations:

Air mass held (R = 287 J/kg·K): m = P·V/(R·T)
Volume required for a run time: V_req = Q × t / (ΔP/P_atm)

Worked example — 500 L vessel between 6 and 8 bar

The figures below were produced by running this page's own engine with the example inputs (Network free-air demand (L/s), Receiver volume (L), Maximum pressure (bar g), Minimum pressure (bar g), Gas temperature (°C), Atmospheric pressure (bar a), Run time required (min)). If the calculator returns something different for the same numbers, that is a bug, not a rounding difference.

Expected results for the worked example
Free air the vessel releases987.17 L
Run time available98.72 s
Volume required for that run time911.7 L
Compression ratio1.29
Usable pressure swing2 bar a
Air held at maximum5.36 kg
Cycles per hour36.47 1/h
  1. A 2 bar swing over 1.013 bar atmosphere gives a compression ratio of 8.89.
  2. The 500 L vessel releases about 987 L of free air between the two pressures.
  3. At 10 L/s that is roughly 99 s of run time, short of the 180 s requested.
  4. A volume near 912 L would be needed for the run time requested.

Assumptions & limitations

Engineering calculation. Receiver volume, free-air delivery and run time from the pressure swing, computed isothermally from Boyle’s law and the ideal gas law.

  • Isothermal sizing.
  • Receiver AND vessel volume only.
  • No pressure vessel code allowance.
  • Free air is quoted at the atmospheric pressure entered.

This tool supports professional engineering work; it does not replace a sealed design. Confirm every result against the applicable standard and a licensed engineer before it is built.

References & standards

  • Boyle’s law and the ideal gas law — the two relations this tool applies.
  • Compressor manufacturers’ receiver sizing guidance, for the isothermal convention.
Engineering Disclaimer & Verification Notice

This calculator provides preliminary engineering estimates for informational and planning purposes. Actual reverse osmosis / engineering system performance depends on site conditions, feed-water chemistry, membrane characteristics, operating pressure, temperature, recovery limits, fouling/scaling potential, and system design. Verify results using project-specific data, manufacturer projections, and applicable engineering standards before final design or operation.