Complete compressed air system.
Combine compression, cooling, treatment, storage and distribution at the required pressure and point-of-use air quality. The layout below explains the system interfaces; it is not a photograph of an installed project.
DETAILED SELECTION & OPERATION
Separate continuous flow from short 20 bar events
For a continuous 20 bar load, compare a dedicated high-pressure package against the required delivered flow at the agreed pressure and rating conditions. Do not choose from the catalogue nominal-flow number alone. Confirm minimum pressure at the machine, normal flow, process hours, control range, cooling conditions and the consequences of an unload, trip or maintenance event.
For intermittent demand, record each event's flow, duration, repetition rate and acceptable recovery time. A lower-pressure plant with a booster and local high-pressure receiver can be worth comparing where the duty is confined to one branch, but the upstream system must withstand booster inlet demand without disrupting other users. A receiver can buffer a short event; it cannot provide continuous compressor capacity.
- Log normal and peak flow separately, with one stated reference basis.
- Record the low-pressure inlet behaviour if a booster is considered.
- Place the pressure measurement point at the critical machine, not only at the compressor outlet.
- Define the recovery time and the permitted pressure band after each event.
Teaching example: framing a 20 bar selection without choosing a model
The figures below are teaching assumptions only, not a project specification or a model recommendation. Assume all flow figures share one hypothetical reference condition; they are not claimed as FAD or as the catalogue's nominal-flow basis. The exercise shows why a time-average flow, peak flow and pressure-drop budget must be kept separate.
The assumed 18.5 bar(g) minimum at the machine plus 0.3 bar treatment loss and 0.7 bar distribution/event allowance gives a 19.5 bar(g) source target before control tolerance is considered. That makes a nominal 20 bar (2.0 MPa) system a candidate for investigation, but it does not prove that any listed model will deliver the duty. The supplier must verify the complete pressure band, delivered flow and recovery with its selected controls and receiver arrangement.
| Item | Assumption | Calculation or implication |
|---|---|---|
| Point-of-use pressure | Minimum 18.5 bar(g) at one machine | Use the machine connection as the reference point. |
| Pressure allowance | 0.3 bar through treatment; 0.7 bar through distribution during the event | 18.5 + 0.3 + 0.7 = 19.5 bar(g) before control tolerance. |
| Continuous flow | 1.2 m³/min | Base demand is present throughout the example cycle. |
| Short additional event | 0.8 m³/min for 15 seconds every 120 seconds | Time-average addition = 0.8 × 15 ÷ 120 = 0.1 m³/min. |
| Average and peak flow | Same hypothetical reference condition for all flows | Average = 1.2 + 0.1 = 1.3 m³/min; simultaneous peak = 1.2 + 0.8 = 2.0 m³/min. |
| Selection step | No catalogue model is selected | Check high-pressure receiver storage and recovery, then obtain supplier-delivered-flow data at the agreed basis. |
Data needed for a 20 bar quotation
Give every bidder the same process boundary. State whether 20 bar is gauge or absolute pressure, where it is measured, the minimum/normal/maximum pressure band, and the pressure permitted during a transient. Separate continuous demand from peak events and identify the flow reference conditions. Ask for the direct-compression and booster alternatives only where both are technically relevant to the duty.
Request a line diagram and a clear inclusions schedule covering compression, cooling, separation, drying, filtration, receiver, drains, controls, relief protection and distribution interfaces. Ask the bidder to identify the exact model, rated motor power, complete-package electrical boundary, cooling duty, treatment pressure loss, maintenance scope and conditions used for delivered-flow data.
- Machine OEM pressure, flow, air-quality and transient-duty requirements.
- Ambient conditions, altitude, voltage/frequency, cooling availability, layout and noise constraints.
- Receiver design pressure, volume, drains, relief devices and applicable inspection requirements.
- Acceptance measurement points, flow basis, stabilization conditions and responsibilities.
SELECTION & OPERATION
Frequently asked questions
Which 20 bar compressor models are shown on this page?
The clean table presents verified catalogue rows with `/20` model codes and a 2 or 2.0 MPa source-table pressure entry. It includes EBLW examples at 1, 2 and 3 m³/min nominal flow and EBLGII examples from 3.5 to 33 m³/min nominal flow. It is a catalogue comparison, not a stock or lead-time statement.
Is 20 bar the same as 2.0 MPa in this model table?
Yes. This page displays the catalogue's 2 or 2.0 MPa entries as 20 bar (2.0 MPa). The project specification must still state whether the required operating pressure is gauge or absolute and identify the measurement location.
Are the listed m³/min figures FAD?
No. They retain the supplier catalogue's label of nominal volumetric flow in m³/min. The table does not call them FAD. Before comparing an offer with process demand, obtain the supplier's flow basis, reference conditions and delivered-flow information at the specified duty.
Do all 20 bar models use the same compression structure?
No. The manual describes several family-level structures, including twin-screw-and-scroll arrangements for the 1, 2 and 3 m³/min grouping and a two-stage twin-screw-and-scroll arrangement for models at 23 m³/min and above. It does not assign every individual 20 bar model a complete construction drawing, so request that information for the quoted unit.
Should a 20 bar process use a dedicated compressor or a booster?
Compare a dedicated branch where high-pressure flow is sustained or shared by several users with a lower-pressure source and booster where the demand is localized or intermittent. The decision depends on inlet stability, peak/recovery profile, storage, cooling, treatment, controls and the complete pressure boundary—not on pressure label alone.
Technical references
- Dezhou YITong electric medium/high-pressure selection catalogue ↗
Supplier catalogue source for the listed electric medium/high-pressure model examples, nominal-flow designation, pressure entries and family-level structure description.
- CAGI Performance Verification Program ↗
Why a buyer should request comparable performance data and a stated test basis rather than rely on an unqualified flow number.
- Improving Compressed Air System Performance — U.S. Department of Energy ↗
General system context for demand profiles, storage, treatment and distribution; it is not used as a model-performance guarantee.


