Compressed-air calculator

Sizing compressed-air piping

Too small a diameter imposes a permanent pressure loss; too large a diameter costs more than it should. The right diameter is chosen on two criteria: allowable pressure loss and flow velocity.

This calculator recommends a diameter for your flow and topology — dead-end or loop network — and shows the effect of each candidate diameter.

Pipe sizing

Recommended pipe diameter by pressure drop and velocity (open/closed loop).

Total length
Material & standard PN = nominal pressure (bar). PN16 (16 bar / 232 psi) = standard factory compressed-air class · PN70 (70 bar / 1015 psi) = high pressure. Schedule = steel wall-thickness series (ASME B36.10).

Open loop — pressure drop

PipeVelocityΔP
Under
Optimal
Over

Open loop — velocity (≤ 35 ft/s)

PipeVelocityΔP
Under
Optimal
Over

Closed loop — pressure drop

PipeVelocityΔP
Under
Optimal
Over

Closed loop — velocity (≤ 35 ft/s)

PipeVelocityΔP
Under
Optimal
Over

Closed loop (CAGI ½ rule): air travels at most half the length → pressure drop reduced by about one-half (CAGI ch.4); full flow (CAGI sets no “Q/2”), so velocity at full flow (upper bound). Velocity red if > 35 ft/s; ΔP red if above the limit.

Open line vs closed loop — where the length is measured
Open-line network: length from the compressor to the farthest point Loop network: air reaches the point from both sides → the tool computes over ½ length (drop ≈ half, CAGI)

Enter the real pipe length. Open line: full Q and L. Loop (CAGI ½): air travels at most ½ the length → the tool computes over ½ length (drop ≈ half) at full flow, hence a smaller diameter than an open line.

Indicative estimates — validate all results before any technical decision.