Textile Compressed Air Pipe Network Pressure Drop Modeler
Put this calculator on your own site
Paste this where you want the calculator to appear. It works on any site — WordPress, Squarespace, Webflow, Ghost or plain HTML — and needs no JavaScript of yours. It carries a link back here, which is the only thing we ask for it.
Loss falls with the fifth power of diameter. One pipe size up cuts it roughly threefold.
Pressure Drop
—bar
Lost to friction between compressor and machines
Network Performance
Air Velocity
—m/s
Pressure at Machine
—bar g
Compressor Energy Penalty
—%
Annual Cost of the Drop
—/yr
Diameter for Target Drop
—mm
Total Equivalent Length
—m
Density is taken at the working pressure and held constant along the run, which is the standard incompressible approximation and stays reasonable while the drop is a small fraction of absolute pressure — above roughly 10% it understates the loss and a compressible treatment is needed. Velocity above about 9 m/s in a main is the practical design ceiling regardless of what the pressure drop says, because velocity carries condensate and noise with it. Fittings equivalent length is where most estimates go wrong: a single poorly chosen valve or a run of tight elbows can exceed the straight pipe, and it should be built up item by item rather than guessed.
Using this calculator
About the Textile Compressed Air Pipe Network Pressure Drop Modeler
The formula
This is the expression the tool evaluates. Every term is named underneath, with the unit it must be supplied in.
Each input feeds the expression evaluated in the browser; the symbol table below names every term and its unit.
Symbols used above
Symbol
Stands for
Unit
flowRate
Free Air Flow
m³/min
pipeDiameter
Internal Pipe Diameter
mm
pipeLength
Straight Pipe Length
m
fittingsLength
Fittings Equivalent Length
m
frictionFactor
Darcy Friction Factor
f
workingPressure
Working Pressure
bar g
airTemp
Air Temperature
°C
penaltyPerTenthBar
Energy Penalty per 0.1 bar
%
compressorPower
Compressor Power
kW
runningHours
Running Hours per Year
h
tariff
Electricity Tariff
/kWh
targetDrop
Target Pressure Drop
bar
pressureDrop
Pressure Drop
bar
velocity
Air Velocity
m/s
pressureAtMachine
Pressure at Machine
bar g
compressorPenalty
Compressor Energy Penalty
%
annualPenaltyCost
Annual Cost of the Drop
/yr
recommendedDiameter
Diameter for Target Drop
mm
equivalentLength
Total Equivalent Length
m
How the result is derived
Step by step, from the values you type to the figure on screen.
The 12 inputs are read from the form on every keystroke: Free Air Flow, Internal Pipe Diameter, Straight Pipe Length, Fittings Equivalent Length, Darcy Friction Factor, Working Pressure, Air Temperature, Energy Penalty per 0.1 bar, Compressor Power, Running Hours per Year, Electricity Tariff and Target Pressure Drop.
Each value is checked against the accepted range in the input table below. A value outside its range stops the calculation rather than producing a misleading figure — the results blank out and a message appears.
The validated values are substituted into the expression above, which resolves Pressure Drop together with every supporting figure in one pass — no value is carried over from a previous entry.
The supporting outputs — Air Velocity, Pressure at Machine, Compressor Energy Penalty, Annual Cost of the Drop, Diameter for Target Drop and Total Equivalent Length — come from the same pass, so they always describe the same case as the headline figure.
Results are rounded for display only. The full-precision value is used throughout the chain, so reading a rounded intermediate figure back into the tool by hand can shift the last digit.
What each input means
Where to read each value on the floor, the unit it must be in, and the range the tool accepts.
Input
Unit
Accepted range
Default
What it means
Free Air Flow
m³/min
1 to 500 m³/min
45
Internal Pipe Diameter
mm
10 to 400 mm
80
Straight Pipe Length
m
1 to 3000 m
220
Fittings Equivalent Length
m
0 to 2000 m
65
Darcy Friction Factor
f
0.005 to 0.06 f
0.02
Working Pressure
bar g
2 to 15 bar g
7
Air Temperature
°C
0 to 80 °C
30
Energy Penalty per 0.1 bar
%
0.1 to 3 %
0.7
Compressor Power
kW
5 to 5000 kW
250
Running Hours per Year
h
100 to 8760 h
8000
Electricity Tariff
/kWh
0.001 to 2 /kWh
0.09
Target Pressure Drop
bar
0.05 to 2 bar
0.3
What the tool returns
The headline figure and every supporting value it is built from.
Output
Unit
What it tells you
Pressure Drop (headline result)
bar
Lost to friction between compressor and machines
Air Velocity
m/s
Pressure at Machine
bar g
Compressor Energy Penalty
%
Annual Cost of the Drop
/yr
Diameter for Target Drop
mm
Total Equivalent Length
m
Worked example
Given
Free Air Flow
45 m³/min
Internal Pipe Diameter
80 mm
Straight Pipe Length
220 m
Fittings Equivalent Length
65 m
Darcy Friction Factor
0.02 f
Working Pressure
7 bar g
Air Temperature
30 °C
Energy Penalty per 0.1 bar
0.7 %
Compressor Power
250 kW
Running Hours per Year
8000 h
Electricity Tariff
0.09 /kWh
Target Pressure Drop
0.3 bar
The tool loads with this case already solved — the Pressure Drop shown above is its answer. Change one value and the difference from this baseline is the sensitivity of the result to that variable.
How to use it
Work through the input groups in order — Pipework and Air & Cost. The defaults are a realistic case, so you can change one value at a time and watch what moves.
There is no calculate button. Every figure recalculates as you type or drag, which is what makes this usable for a what-if sweep rather than a single answer.
Read Pressure Drop in the dark results panel — that is the headline figure, expressed in bar.
Check the supporting rows underneath (Air Velocity, Pressure at Machine, Compressor Energy Penalty, Annual Cost of the Drop, Diameter for Target Drop and Total Equivalent Length) before acting on the headline — they are where an implausible input usually shows itself first.
Reset to defaults returns every field to the reference case, which is the quickest way to check whether a surprising result came from the tool or from an input you had changed earlier.
Where this is used
Process planning — establishing Pressure Drop before a trial is booked, so machine time and material in Advanced Utility & Power Quality are committed against a calculated figure rather than an estimate.
Costing and quotation — Pressure Drop is an input to the cost sheet, and quoting from a worked number rather than a remembered one is what keeps a margin intact.
Troubleshooting — when the floor result drifts from plan, entering the measured values (starting with Free Air Flow) shows how much of the gap in Pressure Drop each variable explains.
Teaching and study — the accepted ranges bracket normal Advanced Utility & Power Quality practice, so moving one variable at a time shows the shape of the relationship rather than a single answer.
Assumptions and limits
Density is taken at the working pressure and held constant along the run, which is the standard incompressible approximation and stays reasonable while the drop is a small fraction of absolute pressure — above roughly 10% it understates the loss and a compressible treatment is needed. Velocity above about 9 m/s in a main is the practical design ceiling regardless of what the pressure drop says, because velocity carries condensate and noise with it. Fittings equivalent length is where most estimates go wrong: a single poorly chosen valve or a run of tight elbows can exceed the straight pipe, and it should be built up item by item rather than guessed.
Every input is bounded to the range normal practice occupies (Free Air Flow 1 to 500 m³/min, Internal Pipe Diameter 10 to 400 mm and Straight Pipe Length 1 to 3000 m, and so on for the rest). Those bounds are guard rails against typing errors, not a claim that the formula fails one unit outside them.
The calculation is deterministic: the same inputs always give the same result. It carries no allowance for machine condition, operator skill, ambient conditions or lot-to-lot material variation unless an input above explicitly represents one.
Nothing is sent anywhere. The maths runs in your browser, so the numbers you type never leave the page.
Questions people ask
What do I need to know before using the Textile Compressed Air Pipe Network Pressure Drop Modeler?
Have these to hand: Free Air Flow, Internal Pipe Diameter, Straight Pipe Length, Fittings Equivalent Length, Darcy Friction Factor, Working Pressure, Air Temperature, Energy Penalty per 0.1 bar, Compressor Power, Running Hours per Year, Electricity Tariff and Target Pressure Drop. With those entered, the tool returns Pressure Drop immediately.
What exactly is Pressure Drop?
Lost to friction between compressor and machines. It is reported in bar. It is derived from Free Air Flow, Internal Pipe Diameter, Straight Pipe Length, Fittings Equivalent Length, Darcy Friction Factor, Working Pressure, Air Temperature, Energy Penalty per 0.1 bar, Compressor Power, Running Hours per Year, Electricity Tariff and Target Pressure Drop, and is the figure the rest of the Advanced Utility & Power Quality calculation is built around.
Which units does this calculator expect?
Enter Free Air Flow in m³/min, Internal Pipe Diameter in mm, Straight Pipe Length in m, Fittings Equivalent Length in m, Darcy Friction Factor in f, Working Pressure in bar g, Air Temperature in °C, Energy Penalty per 0.1 bar in %, Compressor Power in kW, Running Hours per Year in h, Electricity Tariff in /kWh and Target Pressure Drop in bar. Mixing unit systems is the most common cause of a result that looks an order of magnitude wrong — convert before typing, not after reading.
What are the other figures under the main result?
They are the intermediate quantities the calculation passes through: Air Velocity, Pressure at Machine, Compressor Energy Penalty, Annual Cost of the Drop, Diameter for Target Drop and Total Equivalent Length. They are shown because a headline number nobody can trace is a number nobody trusts — checking them against your own expectation is the fastest way to confirm the inputs were read as you intended.
Can I rely on this for a production decision?
Density is taken at the working pressure and held constant along the run, which is the standard incompressible approximation and stays reasonable while the drop is a small fraction of absolute pressure — above roughly 10% it understates the loss and a compressible treatment is needed. Velocity above about 9 m/s in a main is the practical design ceiling regardless of what the pressure drop says, because velocity carries condensate and noise with it. Fittings equivalent length is where most estimates go wrong: a single poorly chosen valve or a run of tight elbows can exceed the straight pipe, and it should be built up item by item rather than guessed. Treat the output as an engineering estimate that narrows the trial window, not as a substitute for the trial.