- Author
- Byron Raal, CAS Founder-Editor About the author
- Checked against
- AS 1210AS/NZS 3788AS 4343
- Date last checked
- 18 August 2026
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An air receiver tank is a steel pressure vessel that stores compressed air to stabilise system pressure, smooth compressor load cycles, and buffer peak demand. Australian receivers are designed under AS 1210:2010 and inspected under AS/NZS 3788:2024 Amd 1:2025. Sizing uses V = (Q × t × Pa) / (P1 − P2); typical industrial plants run 500 to 2,000 L vessels.
How big should my air receiver tank be?

Air receiver sizing depends on compressor type and control mode. For VSD compressors, allow approximately 3 to 5 litres of receiver per L/s of compressor FAD. For load/unload control, allow 10 to 15 litres per L/s to steady header pressure and give condensate time to drop out; motor start frequency is a separate limit that belongs to start/stop control, not to load/unload. AS 1210:2010 governs the pressure vessel design, and AS/NZS 3788:2024 Amd 1:2025 governs ongoing inspection intervals.
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Free two-page PDF. Once you have the volume, that receiver may need registering with your state regulator before it goes into service. The worksheet runs the AS 4343 hazard level calculation in five lines and pairs the answer with the registration checklist for your state or territory. Email only, and the download is on the next screen.
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An air receiver tank is the most undersized and most under-specified component in the average Australian compressed air system. Plant managers tend to treat it as a passive storage vessel bolted on after compressor selection is done, when in practice it is the single component that governs how stable your system pressure runs, how often your compressor load-cycles, and how much energy your facility burns moving air from generation to point of use.
This guide is written for engineers, procurement specialists, plant managers, and maintenance leads who need to specify an air receiver correctly the first time. It covers what receivers actually do in the system, how to size them against real duty cycles, the difference between vertical and horizontal configurations, the Australian standards that govern pressure vessel selection and in-service inspection, and what a compliant installation looks like on the ground. Where the calculation gets involved we work through a real example. Where the rules come from Standards Australia or Safe Work Australia we link directly to the source.
If you are trying to decide between a 500 L and a 2,000 L receiver, or whether to go vertical to save floor space, or whether your existing tank meets AS 1210:2010 and AS/NZS 3788:2024 Amd 1:2025 inspection requirements, the answers are below.
What Is a Receiver Tank?
A receiver (sometimes spelled “air receiver”) is a steel or composite pressure vessel that sits between the compressor discharge and the plant demand. Its primary role is to stabilise system pressure by accumulating compressed air at high pressure and releasing it incrementally as the plant consumes air. Without it, every small spike in demand (a pneumatic tool firing, a valve opening) would cause the compressor to load and unload rapidly, wasting energy.
The receiver acts as a flywheel for the system: the larger and better matched it is to your duty cycle, the longer the intervals between load-unload cycles, and the less energy the compressor must burn to maintain stable pressure.
Sizes range from 20 L portable tanks (single-user workshops) to 10,000+ L vessels (large factories). Most Australian manufacturing and pharmaceutical plants run 500 to 2,000 L receivers.
Why Receiver Size Matters
The misunderstanding is common: “I’ll just order a 500 L tank and bolt it on.” In practice, every litre undersizes your system:
- Pressure swing. The swing between cut-out and cut-in (say 7.5 to 6.0 bar) is a pressure-switch setting, not a property of the tank. What receiver volume changes is how often that cycle repeats: with the same 1.5 bar band and the same demand, a 2,000 L tank takes roughly four times as long to fall from cut-out to cut-in as a 500 L tank, so the compressor loads a quarter as often. Fewer load-unload cycles and motor starts mean less energy lost to unloaded running and steadier pressure at the point of use.
- Compressor duty. A compressor designed to run at steady load is efficient. One that load-unloads dozens of times per hour is not. Undersized receivers force that load-unload cycle to happen too often.
- Moisture and oil carryover. Fast pressure swings cause sudden cooling and heating of the compressed air, which condenses water and oil. A larger receiver gives the liquid more time to settle and drain, reducing downstream contamination and equipment failure.
- Peak demand buffer. If your plant has a sudden simultaneous demand (multiple tools, a process shift), an undersized receiver cannot supply the peak without the compressor load jumping hard. A properly sized tank smooths that demand and keeps pressure stable.
How to Size an Air Receiver
Receiver sizing is driven by three variables:
- Peak air demand: L/s or m³/min.
- Minimum pressure: compressor cut-in, e.g. 6.0 bar.
- Maximum pressure: compressor cut-out, e.g. 7.5 bar.
- Carry time: the measured or required duration of the demand event, in seconds. There is no generic default. Volume scales directly with this term, so a guessed few minutes against a real event of seconds oversizes the vessel by the same multiple.
The formula is:
V = ( Q × t × Pa ) / ( P1 − P2 )
where:
V = receiver volume (litres)
Q = peak plant demand (L/s)
t = the time the receiver must carry the demand on its own, with the compressor unloaded or off (seconds)
Pa = atmospheric pressure (1.01325 bar absolute)
P1 = compressor cut-out (discharge pressure in bar)
P2 = compressor cut-in (inlet air pressure in bar)
(P1 and P2 may be expressed in gauge or absolute; atmospheric pressure cancels in the differential P1 − P2 so the result is identical either way. Ensure that P_atm in the numerator always remains the absolute atmospheric value (1.01325 bar).)
This is the storage (blow-down) method: it sizes the receiver to carry a demand event from stored air alone. If instead you are sizing to limit load/unload cycling on a fixed-speed compressor, use the cycle-frequency method: V = (C × T × Pa) / (4 × (P1 − P2)), where C is compressor capacity (L/s) and T is the full load/unload cycle time (seconds); the factor 4 reflects the worst case at 50 per cent demand.
An example: Your compressor runs 7.5 bar cut-out and 6.0 bar cut-in. Your peak demand is 12 L/s. You want stored air to carry that peak for 10 minutes (600 seconds) with the compressor unloaded.
V = ( 12 × 600 × 1.01325 ) / ( 7.5 − 6.0 )
V = ( 7,295.4 ) / ( 1.5 )
V = 4,864 litres
In this case you would specify a 5,000 L receiver to give comfortable margin and account for real-world inefficiencies (compressor unload delay, condensate drain lag, minor leaks).
Rule of thumb: as a rough first pass, allow about 3 to 5 litres of receiver per L/s of compressor FAD for a VSD machine, and about 10 to 15 litres per L/s for fixed-speed load/unload control (the figure quoted at the top of this section). Treat that only as a sanity-check starting point. The receiver you actually need is set by the storage formula below, because it depends on your peak demand, the pressure window you can tolerate, and how often you are willing to let the compressor cycle. Where those are known, size from the formula, not the rule of thumb: V = (Q × t × Pa) / (P1 − P2). Our air receiver tank sizing guide works that formula through a full SI worked example and reconciles it against the cycle-frequency method.
Indicative sizing reference table
The table below sets the rule-of-thumb against typical compressor outputs as a first-pass sanity check (a 45 kW rotary screw delivers roughly 120 to 130 L/s FAD at 7 bar gauge). They are indicative only. Size from the storage formula above against your own peak demand, pressure window and acceptable cycle frequency before you buy.
| Compressor output (FAD) | Load/unload receiver (10 to 15 L per L/s) | VSD receiver (3 to 5 L per L/s) |
|---|---|---|
| 20 L/s reference point (7.5 kW class) | 200 to 300 L | 60 to 100 L |
| 20 to 50 L/s (approx 11 to 22 kW) | 200 to 750 L | 60 to 250 L |
| 50 to 90 L/s (approx 30 to 37 kW) | 500 to 1,350 L | 150 to 450 L |
| 90 to 130 L/s (approx 45 kW) | 900 to 1,950 L | 270 to 650 L |
| 130 to 250 L/s (approx 55 to 90 kW) | 1,300 to 3,750 L | 390 to 1,250 L |
Those bands look at compressor output. They do not look at pulsation. If you are sizing for one of the piston compressors, the receiver has a second job to do: a reciprocating machine pulses hard at every stroke, and it takes receiver volume of roughly 6 to 10 times the swept volume per stroke to damp that out. Run the storage formula, work out the pulsation figure as well, and buy the larger of the two. A rotary screw pulsates far less, which is why the bands above hold up better against a screw than against a piston.
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Before you lock the size in, remember the formula only sees the demand you feed it. If a chunk of that demand is leaks, the leak cost calculator shows what they are costing you, a compressed air leak detection survey finds them, and an independent compressed air audit replaces estimated peaks with measured ones.
Sized it? Now check whether it needs registering
Depending on its pressure and volume, that receiver may also need registering with your state regulator before it goes into service. In New South Wales that duty runs through SafeWork NSW, and the detail sits in our guide to pressure vessel registration in NSW. That receiver may also need registering. Get the worksheet near the top of this page: a free two-page PDF that runs the AS 4343 hazard level calculation in five lines and gives you the registration checklist for your state or territory.
Selecting a Tank: Vertical vs Horizontal
Once you have your volume, the next decision is orientation. Both are pressure-code compliant if the vessel is manufactured to AS 1210:2010.
Vertical Receivers
- Footprint. Half the floor space of a horizontal tank of the same volume.
- Drainage. Condensate naturally drains to the sump at the base. Manual drain valves and auto-drains are simpler to plumb.
- Pressure drop. Longer vertical path means slightly higher friction in internal piping; negligible in most systems.
- Installation. Requires height clearance and a level concrete pad. Harder to move once installed.
Horizontal Receivers
- Footprint. Longer and lower, suitable for low-ceiling plants and workshops.
- Drainage. Condensate pools in the bottom belly. Auto-drains and manual valves require careful placement to reach the sump; trapped moisture is common.
- Inlet. Often enters tangentially (swirl inlet), which causes air-oil separation naturally.
- Weight distribution. Sits on two or more legs; requires a more robust mounting base than a vertical tank on a single pad.
Practical choice: Vertical is preferred in most Australian plants because drainage is simpler, floor space is at a premium, and the pressure-drop difference is negligible. Horizontal is chosen when height is constrained (low factory ceiling, container workshop).
Australian Standards and Compliance
Air receiver tanks in Australia are designed, manufactured, and inspected under several overlapping standards:
AS 1210:2010 Unfired Pressure Vessels (Design and Manufacture)
This is the design standard for pressure vessels in Australia. It covers wall thickness, welding quality, hydrostatic testing, and material selection. Any receiver sold in Australia must be certified to AS 1210 or equivalent; vessels built to earlier editions such as AS 1210-1997 remain compliant in service.
Key requirements:
- Certification plate must be permanently fixed to the vessel.
- Hydraulic test pressure must be clearly marked.
- Manufacturer identity and manufacturing date must be visible.
- Minimum wall thickness varies by pressure and diameter; calculated thickness must be stamped on the vessel.
AS/NZS 3788:2024 Amd 1:2025 (In-service inspection of pressure equipment)
This standard covers in-service inspection, maintenance, and periodic testing of pressure equipment in operation. Duty-holder obligations under the state and territory WHS regulations (which follow the Safe Work Australia model WHS framework) require pressure equipment to be inspected on the schedule set in this standard.
Key in-service requirements:
- External visual inspection: AS/NZS 3788:2024 Table 4.1 Item 6 bands compressed-air vessels by the pV product (design pressure in MPa multiplied by volume in litres), not by AS 4343 hazard level: above pV 150 MPa·L the external interval is 2-yearly; at or below that, the cadence is set by a competent person under Table 4.1 Note 6. Look for corrosion, dents, leaks, and condition of safety devices. Hazard level still matters for registration: under AS 4343:2014 the hazard level value for a non-harmful gas is H = 10 × P × V (Equation 2.1), so a typical 200 to 1,000 L receiver at 800 kPa design works out at hazard level C, not Level A or B.
- Internal inspection: For compressed-air receivers above pV 150 MPa·L, AS/NZS 3788:2024 Amd 1:2025 Table 4.1 Item 6 requires internal inspection at 4-year intervals (external inspection at 2-year intervals), with a 12-year extended interval available under the standard’s conditions. At or below pV 150 MPa·L, intervals are set under Table 4.1 Note 6 at the competent person’s discretion. Internal inspection is not waived outright for larger receivers; dry, well-drained air carries lower internal-corrosion risk, but confirm the interval for your vessel with the competent person.
- External inspection (additional, above pV > 150 MPa·L): 2-yearly per AS/NZS 3788:2024 Table 4.1 Item 6 for compressed-air receivers where pV exceeds 150 MPa·L. Below pV 150 MPa·L, external inspection cadence is set by a competent person; at or below pV 100 MPa·L no commissioning or first in-service inspection is required by Item 6.
- Hydrostatic testing: AS/NZS 3788:2024 Table 4.1 sets no routine hydrostatic re-test interval for in-service air receivers. A hydrostatic test is carried out when a competent person calls for one, most commonly to verify a repair or alteration (Section 6 and Appendix A.8.5 of the standard).
- Relief valve test: At each internal inspection and after any maintenance.
A compliant receiver must have:
- A calibrated safety relief valve (set slightly above operating pressure, typically 0.5 bar above cut-out).
- An isolation ball valve or equivalent (so the vessel can be de-pressurised for maintenance).
- A drain valve or auto-drain trap at the sump.
- A pressure gauge (mechanical, not digital only, for safety-critical applications).
- Labelling showing design pressure, test pressure, maximum operating temperature, and date of last internal inspection.
Safe Work Australia Model WHS Framework
State and territory WHS regulations, which follow the Safe Work Australia model WHS framework, require the duty holder (site owner or plant manager) to:
- Equipment register: keep a register of all pressure equipment on site.
- Inspection scheduling: schedule and record all inspections and tests.
- Competent-person inspection: engage a competent person (as defined by the relevant WHS/OHS regulation; a licensed Pressure Equipment Certifier or AICIP-credentialed inspector is one example) to carry out or witness in-service inspections and record the outcome.
- Design-limit operation: ensure no receiver is operated beyond its design pressure or temperature.
Inspection intervals and competency for in-service air receivers are set by the relevant jurisdiction’s enacted WHS or OHS law and regulator guidance. AS/NZS 3788:2024 (incorporating Amendment 1:2025) is the technical inspection reference standard, but it is not itself the legal source. WorkSafe Victoria’s air-receiver guidance is one example of a regulator that requires inspection by a competent person and record retention for hazard-level A to D vessels; it does not frame a single five-year Pressure Equipment Certifier certificate as the universal Australia-wide proof of compliance. Operators should check the specific inspection interval and competency requirement against their own jurisdiction’s regulator.
Installation and Commissioning
A compliant installation typically follows this sequence:
Site Preparation
- Foundation. Level concrete pad, free-draining (not in a sump or puddle). Vertical tanks need a single central pad; horizontal tanks need two or more support legs with vibration isolation pads to reduce noise transmission to the building.
- Clearance. Minimum 500 mm around the vessel for inspection, drain, and safety relief valve access. Keep clear of overhead structures.
- Drip tray (optional but recommended). A low lip or bund around the base to catch condensate spillage and minor oil carryover, especially if the auto-drain fails.
Mechanical Installation
- Piping inlet, and which side of the dryer the vessel sits on. Two arrangements are legitimate and the choice is an engineering one, not a rule. A wet receiver connects to the compressor discharge through a check valve (to prevent backflow if the compressor stops) and sits ahead of the filters and dryer, so the air cools and drops condensate and entrained oil before the dryer sees it. The catch is that the vessel holds saturated air, and a demand surge beyond the combined compressor and dryer rating gets pulled through the dryer and lifts the pressure dew point. A dry receiver sits after the filters and dryer, so a surge is met with already-dried air and the dryer only ever sees compressor output. The US Department of Energy compressed air sourcebook sets out both positions and resolves the dilemma with storage on both sides, noting that the downstream storage must be equal to or larger than the upstream storage. Choose the position from your required air quality, your dryer rated capacity and what you want the compressor controller to see, not from a rule of thumb. Where filtration is fitted, a 1 µm particulate pre-filter ahead of a high-efficiency coalescing filter (typically 0.01 µm) for oil aerosol removal is the usual pairing, with an automatic condensate drain at the lowest point. Our receiver sizing guide works the trade-off through.
- Outlet line. Run from the top of the receiver (above the liquid level) to the distribution network. A size-appropriate isolation ball valve must be fitted downstream of the receiver so the tank can be isolated for maintenance.
- Relief valve. Factory-fitted and pre-set (typically 0.5 bar above cut-out pressure). It must point downward or sideways to a safe discharge point, never upward. Discharge line should be fitted with a muffler to reduce noise.
- Drain valve. At the lowest point of the sump. An auto-drain (timer or float-type) is preferred. Manual drain is acceptable if checked daily in high-humidity climates.
- Pressure gauge. A mechanical (Bourdon-tube) gauge in addition to any digital pressure display (for safety critical installations, the mechanical gauge is the legal record). 0 to 10 bar or 0 to 25 bar scale depending on operating pressure.
- Vibration isolation. Resilient pads under the base to reduce transmission of vibration and noise to the building structure.
Commissioning and Testing
- Pressure test. Before connecting to the plant, confirm the receiver holds pressure for at least 1 hour with no audible leaks.
- Relief valve verification. Do not run the compressor up until the valve lifts. The valve is set about 0.5 bar above cut-out, so a correctly set valve stays shut at cut-out; forcing it open means over-pressurising the vessel to prove a fault that is not there. Check instead that the stamped set pressure suits the vessel design pressure and your cut-out, that the valve is the correct rating and within date, that it is free of corrosion, paint and debris, and that it is not weeping at normal operating pressure. Functional and bench testing is competent-person work under the manufacturer procedure or the procedure your regulator applies to the vessel. WorkSafe Victoria states that the pressure relief valve should be overhauled and bench tested by competent persons at intervals to keep it in a safe condition, with operational surveillance and monitoring built into standard operating procedures, and its inspection-interval table nominates a typical overhaul and bench-test interval of 5 years alongside yearly external inspection of the valve.
- Drain test. Activate the auto-drain or open the manual drain and confirm condensate flows cleanly. No foam or discoloured liquid (which would suggest oil carryover).
- Gauge calibration. If a mechanical gauge is fitted, it should be calibrated by an independent pressure instrument technician (not the compressor supplier) to within ±2.5% accuracy.
- Documentation. Photograph the certification plate and all safety device markings. Create a commissioning record sheet signed by the installer, the site manager, and any independent certifier. This becomes the first entry in your compliance register.
Inspection and Maintenance
Once commissioned, the receiver is governed by the AS/NZS 3788:2024 Amd 1:2025 inspection schedule. Our guide to air receiver inspection requirements covers the pV bands, the external and internal intervals, and who may carry them out.
Annual External Walk-Around (duty-holder good practice)
A 12-month external walk-around is conservative duty-holder practice aligned with state and territory regulator guidance. It is not an AS/NZS 3788:2024 Table 4.1 interval: for compressed-air vessels, Item 6 sets the external cadence by pV band, as covered above.
- Walk around the vessel and check for visible corrosion, surface cracks, dents, or deformation.
- Confirm the safety relief valve is free of debris and the discharge tube is not blocked.
- Check that all bolts and anchors are tight.
- Verify the pressure gauge needle moves smoothly and reads within ±2.5% of the true system pressure (compare with a calibrated test gauge).
- Confirm the isolation valve operates smoothly (does not jam or leak).
- Activate the manual drain or auto-drain and inspect the condensate quality (colour, odour, presence of oil).
- Record the date, findings, and signature of the inspector in your compliance register. If defects are found, report them to the site manager and compressor service provider.
Hydrostatic Re-Testing (when it actually applies)
AS/NZS 3788:2024 Table 4.1 sets no routine hydrostatic re-test interval for air receivers, whatever their age. Australian vessels are designed to AS 1210 (the current edition is AS 1210:2010; vessels built to earlier editions such as AS 1210-1997 remain compliant in service), and in-service hydrostatic testing is not a calendar cycle under either standard. A hydrostatic test is called for by a competent person where it is needed, most commonly to verify a repair or alteration under Section 6 of AS/NZS 3788:2024, with the test procedure in Appendix A.8.5. Check your certification plate and inspection records rather than assuming a 10 or 15 year cycle.
An air receiver above the AS 4343 registrable threshold must have its design registered before use, and the rules differ by state (see our Australian pressure vessel registration guide for the state-by-state picture). See for example the Victorian pressure vessel registration guide, where design registration applies but item registration does not.
Frequently asked questions
How do I size an air receiver tank for my compressor?
Use the formula: V = (Q × t × Pa) / (P1 − P2), where V is receiver volume (litres), Q is peak plant demand (L/s), t is the time the receiver must carry the demand on its own with the compressor unloaded or off (seconds), Pa is atmospheric pressure (1.01325 bar absolute), P1 is compressor cut-out pressure (bar absolute), and P2 is compressor cut-in pressure (bar absolute). As a rough first pass, allow about 3 to 5 litres of receiver per L/s of FAD for a VSD compressor and about 10 to 15 litres per L/s for fixed-speed load/unload control, but treat that only as a sanity check - the receiver you actually need is set by the formula above, driven by your peak demand, pressure window and acceptable cycle frequency.
Should I choose a vertical or horizontal air receiver?
Vertical receivers save floor space (half the footprint of horizontal tanks of the same volume) and offer simpler drainage because condensate naturally drains to the sump at the base. Horizontal receivers suit low-ceiling plants and workshops, but condensate pools in the bottom belly and trapped moisture is common. Vertical is preferred in most Australian plants because drainage is simpler, floor space is at a premium, and the pressure-drop difference is negligible.
What Australian standards apply to air receiver tanks?
Air receivers in Australia are designed and manufactured under AS 1210:2010 (Unfired Pressure Vessels, Design and Manufacture). In-service inspection, maintenance, and periodic testing are governed by AS/NZS 3788:2024 Amd 1:2025 (In-service inspection of pressure equipment). The Safe Work Australia model WHS framework, enacted in state and territory WHS regulations, requires pressure equipment to be inspected on the schedule set in AS/NZS 3788:2024 Amd 1:2025 (for receivers above pV 150 MPa·L, internal inspection at 4-year intervals and external at 2-year intervals, with a 12-year extended interval available under the standard’s conditions; at or below 150 MPa·L per Table 4.1 Note 6) documented by a competent person as defined in the relevant state or territory WHS or OHS regulation. There is no single national inspector licence, so confirm the competency requirement with your jurisdiction’s regulator.
How often must my air receiver be inspected?
Per AS/NZS 3788:2024 Amd 1:2025 Table 4.1 Item 6, compressed-air receivers above pV 150 MPa·L require external inspection 2-yearly and internal inspection 4-yearly, with a 12-year extended interval available under the standard’s conditions; at or below pV 150 MPa·L intervals are set under Table 4.1 Note 6 at the competent person’s discretion, and at or below pV 100 MPa·L no commissioning or first in-service inspection is required. The 12-month annual external visual referenced elsewhere on this page is a separate, more conservative duty-holder practice aligned with state and territory regulator guidance rather than an Item 6 requirement. Table 4.1 sets no routine hydrostatic re-test interval; a hydrostatic test is called for by a competent person where needed, most commonly to verify a repair or alteration (Section 6 and Appendix A.8.5 of the standard).
How does an air receiver tank handle pressure surge from the compressor?
An air receiver buffers the compressor discharge against pulsation and demand surge. Reciprocating piston compressors pulse strongly at each stroke; receiver volume should be 6 to 10 times the swept volume per stroke to dampen them. Rotary screw compressors pulsate less but the receiver damps the same way. Without proper sizing, pulsation fatigues piping joints, distorts gauges, and shortens filter and regulator life. The buffer also handles demand spikes: when several tools fire together, the receiver supplies stored air while the compressor catches up, preventing pressure drop at point of use.
How should I manage condensate drainage from my air receiver?
Compressed air at 7 bar typically yields about 10 to 25 litres of condensate per 1,000 m³ of free air delivered in warm Australian conditions (less in cool southern climates, and approaching 30 litres only in tropical extremes), collecting at the lowest point of the receiver. Receivers are built with a drain point at the sump, and drain condition is checked at routine external inspections. Best practice is a zero-loss electronic auto-drain (level-sensing), which discharges only when condensate is present and avoids the air loss of a timer solenoid. Manual drainage is acceptable in small workshops if checked daily; failure to drain causes internal pitting, elevated dew point, and faster filter saturation. Vertical receivers drain to a central sump; horizontal receivers need careful drain placement because condensate pools across the bottom belly.
Spec the right tank once, not three times.
Receiver selection depends on demand, usable pressure range and controls. Send the supplier your operating evidence and ask them to explain the proposed size and peak-event recovery. We can review your brief and discuss a suitable Australian provider if one is available. We ask for your written permission before an introduction and explain any referral payment arrangement. There is no cost to enquire.
Related reading:
- Compressed Air System Design Guide: How to plan your whole system from compressor selection to point-of-use.
- Compressor Selection Guide: Matching compressor displacement (m³/min) to duty cycle and peak demand.
- Air Quality and ISO 8573-1:2010 Purity Classes: Particulate, water, and oil contamination limits.
- Compressed Air Piping and Sizing Guide: Matching pipe diameter to airflow rate and allowable pressure drop.
- Air Receiver Maintenance and Inspection Protocol: Condensate management, corrosion prevention, and compliance documentation.
- Air Coolers and Separators: Types and Selection: How to remove heat, moisture, and oil before the receiver.
- Energy Audit Guide: How to measure system efficiency and identify savings opportunities.