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Compressed Air Plant by the Numbers
Free air delivery, compression work, heat, water, dryers, pressure, receivers and distribution, worked through one factory compressor room
Calculate what a compressor room really does: the work of compression, the heat it makes, the water it condenses, and the pressure, storage and pipe choices that set the power bill.
Start readingAbout this book
Compressed air is often called a factory’s most expensive utility, and the reason is in the thermodynamics. A compressor turns electricity into pressure, but most of the electricity becomes heat on the way, and most of the pressure is then thrown away through regulators, leaks and open blowers. The compressor room is where those losses start and where many of them can be fixed.
This book follows the energy and the water through one compressor room. It begins with what “a cubic metre of air” means, calculates the ideal work of compression and compares a real compressor against it, then follows the heat the compressor makes, the water the air carries, the dryers that remove it, the pressure the system runs at, the storage and controls that decide part-load power, and the pipes that take the air to the plant. The last chapter turns the numbers into an assessment.
It serves mechanical and maintenance engineers, energy managers and plant managers who run, audit or extend compressed air plant. You need comfortable algebra, SI units and a spreadsheet. The thermodynamics is introduced as it is used. The Library’s Pneumatics by the Numbers covers the point-of-use side, cylinders, valves and leak hunting; this book stays in the compressor room and the mains.
The running case
Every chapter works on one fictional installation: CA-1, the compressor room of a packaging plant. An oil-injected rotary screw compressor with a 37 kW motor delivers 6.0 m³/min of free air at 750 kPa gauge, drawing about 41 kW at full load. Air at 25 °C and 60 per cent relative humidity enters the intake. An aftercooler cools the compressed air to 35 °C, a refrigerated dryer brings it to a pressure dew point of 3 °C, and a receiver and a main carry it to the plant, which uses an average of 4.2 m³/min over 6,000 hours a year.
This is an illustration. All flows, powers, prices, results and failures are invented for teaching and checked by calculation. They are not KEVOS® work, a real site or a measured compressor, and real compressors’ performance comes from their makers’ test data. Electricity is priced at a teaching A$0.25 per kWh and gas at A$18 per GJ, both excluding GST.
Source limits and professional responsibility
The supplied DOE Fundamentals Handbook informed the subject map and the principles of ideal gases, compression and efficiency. This book develops them in SI units with its own case, figures and exercises, and nothing is copied from the handbook’s text or examples.
This book is educational. Compressed air systems store energy in receivers and pipework, discharge air hot enough to burn and at pressures that can inject air into skin or launch debris, and contain oil that can ignite. Receivers are pressure vessels with design, registration and inspection duties under the model Work Health and Safety Regulations and the Australian Standards named in the references. Changes to pressures, safety valves, controls and receivers need competent review. Use the methods here to understand and question a system, not as authority to alter one.
Who this book is for
Mechanical and maintenance engineers, energy managers and plant managers who specify, run, audit or extend a factory's compressed air plant, from the compressor room to the main headers.
What you will learn
- Convert between free air delivery, actual volume and mass flow, and state pressure ratios correctly.
- Calculate isothermal and isentropic compression work and judge a compressor's specific power against them.
- Estimate discharge temperatures, the benefit of staging, and the heat available for recovery.
- Calculate the water condensed by aftercoolers and dryers and convert between pressure and atmospheric dew points.
- Choose pressure set points, receiver volumes, control modes and main sizes from their effect on power and pressure.
Inside this book
Chapters
- 01Free air, pressure and mass flowWork out what a cubic metre of compressed air means, convert free air delivery to mass and actual volume, state pressure ratios in absolute terms and meet the CA-1 compressor room.
- 02The work of compression and specific powerCalculate the isothermal and isentropic work to compress CA-1's air, compare its 41 kW against them, price a cubic metre of air, and compare compressors on a fair basis.
- 03Discharge temperature, staging and coolingCalculate how hot air gets in one isentropic stage, why oil injection and intercooled stages help, why an oil-flooded screw must stay above its own dew point, and what the aftercooler removes.
- 04Recover the heat of compressionFollow CA-1's 41 kW into its oil cooler, aftercooler and room, value the hot water and warm air it could supply, and keep heat recovery from cooling the oil below its dew point.
- 05Water in compressed airCalculate the water CA-1 draws in, how much its aftercooler condenses, how weather changes the load, and how to drain and dispose of the oily condensate without wasting air.
- 06Dryers and dew pointUnderstand pressure dew point, convert it to an atmospheric dew point, compare refrigerated and desiccant dryers by what they cost to run, and dry only the air that needs it.
- 07Set the pressure and stop the wastePrice each 100 kPa of CA-1's pressure, see how leaks and open blow-offs grow with it, find the pressure lost before the air leaves the room, and fix a low-pressure complaint at its cause.
- 08Receivers and compressor controlSize CA-1's receiver from its cycle time, compare load and unload, modulation and variable speed control at 70 per cent load, store air for peaks, and catch a receiver valved out of service.
- 09Size the mains and lay them outSize CA-1's main and branches from actual volume and a pressure budget, compare dead-end and ring layouts, choose suitable pipe materials and avoid a branch too small for the line it feeds.
- 10Assess the system, then choose equipmentMeasure CA-1's specific power and demand, rank the savings found in earlier chapters, see why demand comes before supply, and meet the safety duties of a compressor room.
Apply This in Practice
Use these KEVOS® tools to try the method from this reading with your own numbers.
Applies this method
Air Compressor Staging Check (Power and Discharge Temperature)
Repeats this chapter’s discharge-temperature and staging calculations for other pressure ratios and stage numbers.
Applies this method
Compressed Air Pipe Pressure Drop
Works out pressure drop in a compressed-air pipe for other sizes and flows.
Used in Size the mains and lay them out
Applies this method
Compressed-Air Blow-Off Consumption (Nozzles, Air, Power and Cost)
Prices blow-off nozzles from their size, pressure and running hours.
Applies this method
Compressed-Air Leak Audit (Leak Flow, Power, Cost and Repair Payback)
Converts measured or estimated leaks into power and cost.
Applies this method
Compressed-Air Main Sizing (Bore, Pressure Drop, Velocity, Receiver)
Sizes a compressed-air main and includes a receiver estimate on the same basis as this chapter.
Used in Receivers and compressor control
Applies this method
Compressed-Air System Sizing
Converts each user’s air demand to free air for sizing a compressed-air system.
Used in Free air, pressure and mass flow
Applies this method
Gas Compression and Expansion Process
Calculates compression work and final temperature for any polytropic exponent.
Applies this method
Pneumatic Cylinder Sizing, Air Use and Running Cost
Converts a cylinder’s stroke volume to free air, the pneumatics side of the conversion in this chapter.
Used in Free air, pressure and mass flow
Applies this method
Velocity and Flow of Escaping Compressed Air
Shows the choked flow through an orifice, the way air escapes from a leak at line pressure.
Related Tools and Examples
Useful alongside
Compressed Gas Stored Energy Check (Isothermal Exergy, Isentropic and Brode Burst Energy, pV Product)
Uses the compressor’s specific power from this chapter to price the energy of filling a receiver, against the energy the full receiver holds.
Related to The work of compression and specific power, Receivers and compressor control
Useful alongside
Gas Compressor or Turbine Isentropic Efficiency from Measured Temperatures (Power, Entropy Generation)
Gives the isentropic discharge temperature for a pressure ratio and, for uncooled machines only, the efficiency from a measured outlet temperature.
Related to Discharge temperature, staging and cooling
Learning pathway
Find what compressed-air leaks cost
Learn how pressure setting and leaks waste compressor energy, then audit the leaks in your own system.
1 Learn
Read Set the pressure and stop the waste in Compressed Air Plant by the Numbers.
Price each 100 kPa of CA-1's pressure, see how leaks and open blow-offs grow with it, find the pressure lost before the air leaves the room, and fix a low-pressure complaint at its cause.
2 Apply
Open Compressed-Air Leak Audit (Leak Flow, Power, Cost and Repair Payback) and enter your own figures.
How much air and money are these compressed-air leaks wasting, what share of the compressor do they use, and how quickly do repairs pay back?
3 Verify
Read the tool’s feasibility and verification checks under the result, and test your answer against its stated limitations:
- Equivalent-hole estimates from surveys are rough; a drawdown or no-load test measures total leakage directly.
- Assumes the compressors unload efficiently; poor control makes leaks cost more.
- Example values are illustrations. Replace them with values for your actual task.
4 Improve
Download the decision report or copy the link with your inputs to keep a record, then change one assumption at a time and compare.
Next reading: Assess the system, then choose equipment in Compressed Air Plant by the Numbers.
References and source notes
The manuscript and worked examples are original KEVOS® writing. References inform particular concepts; their authors do not endorse this book. Web references were consulted on 27 October 2026.
- U.S. Department of Energy. DOE Fundamentals Handbook: Thermodynamics, Heat Transfer, and Fluid Flow, Volume 1 of 3 (DOE-HDBK-1012/1-92) (1992). Supplied source, a U.S. Government training handbook approved for public release with unlimited distribution. Read for its treatment of the ideal gas law, compression processes, the first and second laws and efficiency. Its imperial-unit examples and text are not reproduced; this book uses SI units and its own case.
- International Association for the Properties of Water and Steam. Revised Release on the IAPWS Industrial Formulation 1997 for the Thermodynamic Properties of Water and Steam (IAPWS R7-97) (2012 revision). Source of the saturation-pressure equation used for every water vapour pressure above 0 °C in the book; values were checked against the NIST WebBook to within 0.03 per cent.
- International Association for the Properties of Water and Steam. Revised Release on the Pressure along the Melting and Sublimation Curves of Ordinary Water Substance (IAPWS R14-08) (2011). Source of the sublimation-pressure equation used for vapour pressures over ice, needed for dew points below 0 °C.
- E. W. Lemmon, M. O. McLinden and D. G. Friend, National Institute of Standards and Technology. Thermophysical Properties of Fluid Systems, NIST Chemistry WebBook, SRD 69 (current online edition). Used to check the water saturation pressures calculated from the IAPWS equation.
- U.S. Department of Energy, Advanced Manufacturing Office, with the Compressed Air Challenge. Improving Compressed Air System Performance: A Sourcebook for Industry, third edition (2016). Government guidance used as background on control modes, storage, leaks, heat recovery and system assessment. No figures or tables are reproduced.
- International Organization for Standardization. ISO 1217, Displacement compressors, acceptance tests; ISO 8573-1, Compressed air, contaminants and purity classes (current editions). Named by number and scope only: the first for how free air delivery and specific power are measured, the second for how air quality, including pressure dew point, is specified. No classes or values are quoted.
- Standards Australia. AS 1210 Pressure vessels; AS/NZS 1200 Pressure equipment; AS 4343 Pressure equipment, hazard levels (current editions). Named by number and scope only, as the standards that govern air receiver design, the wider pressure equipment regime and hazard classification. No clauses are quoted.