
Plumbing Pipe Sizing Card
One page. DFU, drain and vent sizing, WSFU and supply, 2021 IPC.
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BuyDemand, drop budget, run length, and the layout details that decide the answer
Shop air is usually piped from whatever was on the shelf and then blamed on the compressor. This is the order the decisions actually go in, and the layout details that make a correctly calculated pipe size survive contact with a real shop.
Sizing shop air is four decisions in order: how much air you really draw at once, how much pressure you are willing to lose getting it there, how long the worst-case run actually is once fittings are counted, and only then what diameter satisfies both the drop budget and a sane velocity. Skip any of the first three and the fourth is a guess.
This guide covers the layout and the decisions. The arithmetic — Darcy-Weisbach at line density, Crane TP-410 fitting equivalents, velocity check across every common size — lives on the compressed air pipe size calculator.
The number that sizes pipe is simultaneous demand, not the sum of every tool you own and not the compressor nameplate. A one-person shop almost never runs two air tools at the same time, so the sizing flow is the largest single tool plus a realistic allowance for blowguns and leaks. A two-bay shop with a helper is a genuinely different number.
Two habits produce wrong answers here. The first is adding up every tool on the wall, which produces a main sized for a shop that does not exist. The second is using the compressor's rated SCFM, which describes what the supply can make, not what the distribution has to carry — those are only the same number if the compressor is running flat out continuously.
Work the simultaneous figure out properly with the per-tool CFM requirement calculator, then bring that number here.
A pressure drop target is not a single number applied to the pipe. It is a budget spread across the whole path from receiver to tool, and the hard-piped main is usually the smallest share of it. The benchmark used by the Compressed Air Challenge and the US Department of Energy's compressed air sourcebook is to keep total distribution loss low — commonly stated as no more than about ten percent of discharge pressure, with a design target of roughly two to three psi from receiver to point of use.
| Segment | Typical budget | Notes |
|---|---|---|
| Header / main run | 1 - 2 psi | The part this calculator sizes |
| Drop leg and take-off | 0.3 - 0.5 psi | Usually small if the drop is not undersized |
| Filter / regulator / lubricator | 1 - 3 psi | Rises sharply as the filter element loads |
| Hose and quick-couplers | 2 - 10 psi | Frequently the single largest loss in the system |
Read that table twice. A 50 ft length of 1/4 inch hose with a cheap coupler can lose more pressure than every foot of hard pipe in the building. Sizing the main to a fraction of a psi while feeding tools through a garden-hose-sized whip is a very common and very expensive way to be precise about the wrong thing.
Every 2 psi of extra discharge pressure costs roughly 1 percent more compressor power, permanently. A sloppy 10 psi distribution loss is about 5 percent on the electric bill for the life of the system — which is exactly why the budget exists.
Pipe sizing uses the longest path from the receiver to the furthest point of use, not an average and not a straight-line distance across the floor. Follow the pipe: up the wall, along the joists, around the obstruction, back down to the far bench.
Then count fittings, because an elbow is not free. Crane Technical Paper No. 410 expresses each fitting's resistance as a length-to-diameter ratio, which converts to feet of equivalent pipe once the diameter is known. On 1 inch pipe a standard 90 degree elbow is worth about 2.6 ft of straight run, and a tee taken through the branch is worth about 5.2 ft.
The practical lesson is that long sweeping bends and fewer branch tees buy real pressure back, and that a tangled short run can be worse than a clean long one.

One page. DFU, drain and vent sizing, WSFU and supply, 2021 IPC.
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Quote plumbing work and total fixture units against the drain size.
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Card, 18-page guide and the estimator workbook. All six files.
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The main is only one link. These are the parts that most often become the new restriction once the pipe itself is right.

Industrial-interchange couplers with a decent bore, so the last two inches of the system are not the biggest restriction in it.
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Lets you set pressure at the point of use instead of raising header pressure to paper over distribution losses.
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Water and scale in the bore raise real pressure drop over time. A filter at each drop keeps the pipe you sized behaving like the pipe you sized.
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A 3/8 in bore instead of 1/4 in is frequently worth more real psi at the tool than one step up in hard pipe.
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Receiver volume smooths the peak draws that a steady-flow pipe calculation assumes away.
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A dead-end main feeds the furthest drop from one direction, so the full run length applies. A closed loop feeds it from two directions, so the flow splits and the effective length to the worst-case point is roughly half the loop. That is a meaningful win for very little extra pipe: on the same diameter, halving effective length roughly halves the pressure drop.
A loop also evens out the pressure across the shop, so the bench at the far corner behaves like the one next to the receiver, and it makes adding a drop later a local job rather than a reason to re-size everything downstream.
Compressed air leaving a compressor is saturated, and it condenses as it cools in the pipe. Water collects on the bottom of the main. Every take-off detail that follows exists for that one reason.
Water in the bore is not just a finish problem. It corrodes black iron from the inside, and the scale that results roughens and narrows the pipe, which raises real pressure drop over the years relative to the number you calculated on day one.
With demand, budget, length and fitting count in hand the diameter falls out of the pressure drop equation. The calculator runs it for every common size so you can see where the cliff is — and in a typical shop the cliff is sharp, because drop scales with roughly the fifth power of diameter. One step up in pipe often cuts pressure drop by three quarters.
Pressure drop is not the only check. Velocity matters because fast-moving air strips liquid water and scale off the pipe wall and carries it to the tools, and it makes drop legs far less effective at separating condensate. Common design practice keeps mains at or below about 20 ft/s and branches below about 30 ft/s, so the calculator's recommendation has to satisfy both the drop target and the velocity ceiling.
Run your own numbersThe pipe size calculator gives pressure drop and velocity for every common size at your flow, pressure, run length and fitting count.
Open the calculatorWhen the calculated answer sits right on a size boundary, go up. Oversized air pipe costs material once and costs nothing in energy afterwards, and the extra volume behaves as useful storage. Undersized pipe is a permanent tax you pay in compressor power and in tools that never quite perform.
Size by flow and distance rather than by shop size. A single-user shop drawing 15 to 20 SCFM over a 100 ft run at 100 psig is normally comfortable in 3/4 inch Schedule 40, while a continuous sander or blast cabinet at 40 to 60 SCFM over the same distance typically needs 1 inch or 1-1/4 inch. Run the actual numbers rather than relying on shop square footage.
Loop it if the shape of the building allows. A closed loop feeds the far drop from two directions, so the effective run length is roughly half the loop, which roughly halves the pressure drop for very little extra pipe. It also evens out pressure across the shop and makes adding drops later a local job.
Liquid condensate collects on the bottom of a compressed air main. A take-off from the bottom feeds that water directly to the tool. A gooseneck over the top of the pipe, with the drop continuing past the take-off into a capped drip leg, sends water to the drain instead.
A common design target is two to three psi from receiver to point of use, with total distribution loss held under about ten percent of discharge pressure. The important part is budgeting across the whole path, since hose and quick-couplers usually lose more than the hard-piped main.
Usually yes. Larger pipe costs material once and costs nothing in energy afterwards, the extra internal volume acts as useful storage, and it leaves room for the shop to grow. The practical rule is never to go below the calculated size and to step up when the answer lands near a boundary.