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REDDY COMPRESSORS

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Receiver Transient Storage Calculator

5 min read10 sections

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1. Purpose and Engineering Decision

Compressed-air receivers are often discussed as if more storage automatically fixes low pressure. It does not. A receiver can support a short transient only when three quantities are known: the net air deficit during the event, the usable pressure band, and the event duration.

The calculator supports two primary modes: size a receiver for a defined transient, or enter an existing receiver and estimate how long it can support a defined net deficit before pressure falls to the minimum allowable value.

Decision mode

Primary output

Size receiver

Required geometric receiver volume

Check existing receiver

Estimated transient hold-up time

Check usable stored air

Free-air-equivalent release across P1 to P2

Compare local vs central storage

Same storage equation, different assumed supply response and local restrictions

2. Core Storage Relationship

For a short isothermal event with the receiver gas at approximately constant temperature and with flow stated at a defined reference pressure, the usable free-air-equivalent storage is proportional to receiver volume and the absolute pressure difference across the usable band.

V_receiver = Q_net,ref x t x P_ref,abs / (P1,abs - P2,abs)

Q_net,ref is the net reference flow deficit: transient demand minus compressor or upstream supply that continues to reach the protected zone during the event. P1 and P2 must both be absolute pressures.

Variable

Meaning

V_receiver

Required geometric receiver volume

Q_net,ref

Net deficit at the selected flow reference condition

t

Transient duration

P_ref,abs

Absolute pressure of the flow reference basis

P1,abs

Receiver pressure at start of usable discharge

P2,abs

Minimum acceptable receiver pressure

3. Generalized Mass-Balance Form

The website default should remain the transparent isothermal form above, while the advanced method is available only when the additional inputs are known.

V = [Q_ref x t x P_ref/(Z_ref x T_ref)] / [P1/(Z1 x T1) - P2/(Z2 x T2)]

If T1 = T2 = T_ref and Z1 = Z2 = Z_ref, the generalized equation reduces to the simpler pressure-band formula.

4. Net Transient Demand

Q_net = max(Q_event - Q_supply_during_event, 0)

Receiver sizing must use the air deficit that storage actually has to cover, not automatically the full event demand. If the compressor, header or upstream receiver continues to supply part of the event flow, that contribution reduces the required local storage. If supply response is uncertain, the calculator should allow a conservative zero-contribution scenario and a measured/verified contribution scenario side by side.

Event behaviour

Recommended input

Short actuator/pulse event

Peak event flow minus steady supply reaching the zone

Compressor unloaded then reloads slowly

Use the flow delivered during the actual response interval, not rated capacity

Protected instrument-air hold-up

Often use conservative supply loss or reduced-supply scenario

Remote branch with restrictive piping

Use measured/estimated branch supply during the event

Sustained demand increase

Do not rely on receiver sizing alone; investigate supply capacity

5. Input Model

Input group

Field

Validation / note

Mode

Size receiver / Hold-up time / Usable storage

Explicit selection

Demand

Event flow

Must use a declared flow basis

Demand

Supply during event

0 to event flow for storage-deficit mode

Time

Event duration

Required for sizing mode

Receiver

Existing volume

Required for hold-up mode

Pressure

Start pressure P1

Gauge or absolute, converted internally

Pressure

Minimum pressure P2

Must be lower than P1

Reference

Flow reference pressure

Absolute

Reference

Flow reference temperature

For advanced temperature correction

Advanced

Receiver temperature / Z factors

Optional; default isothermal Z=1 approximation

Output

Volume unit

L, m3, US gal where implemented

6. Pressure Band - The Most Important Design Choice

The receiver is useful only across the pressure band that can be released without violating the process minimum pressure. A receiver charged to 8 bar(g) but protecting a machine that must remain above 7.5 bar(g) has far less usable storage than the same receiver protecting a 6.0 bar(g) user.

The tool must not encourage raising plant pressure merely to create storage; pressure elevation has energy and equipment consequences that belong to the wider system decision.

7. Reference Test Case A - Local Receiver for a 20-Second Peak

A machine cluster requires 18 m3/min FAD for 20 seconds. The branch can continuously supply 10 m3/min during the event. Receiver pressure may fall from 8.0 bar(g) to 6.5 bar(g). Atmospheric/reference pressure is 1.01325 bar(a).

Input

Value

Event demand

18 m3/min FAD

Supply during event

10 m3/min FAD

Net deficit

8 m3/min FAD

Duration

20 s

P1

8.0 bar(g) = 9.01325 bar(a)

P2

6.5 bar(g) = 7.51325 bar(a)

V = 8 x (20/60) x 1.01325 / (9.01325 - 7.51325) = 1.801 m3

Reference result: approximately 1801 litres geometric receiver volume before design margin, piping volume, control response and site-specific constraints are considered.

8. Reference Test Case B - Hold-Up Time of an Existing Receiver

An existing 2,000 L receiver starts at 8.0 bar(g) and may discharge to 6.0 bar(g). A protected zone loses 6 m3/min more air than the upstream source can supply. Reference pressure is 1.01325 bar(a).

t = 2.0 x (9.01325 - 7.01325) / (6 x 1.01325) = 0.658 min

Hold-up time is approximately 39.5 seconds under the stated isothermal assumptions.

9. Reference Test Case C - Why Compressor Contribution Matters

A 12 m3/min transient lasts 10 seconds across the same 8.0 to 6.5 bar(g) band. Compare two cases: no supply contribution and 7 m3/min continuing supply.

Scenario

Net deficit

Required volume

No supply contribution

12 m3/min

1.351 m3 (1351 L)

7 m3/min continues

5 m3/min

0.563 m3 (563 L)

This comparison is why the calculator asks for supply during the event rather than assuming either zero supply or full compressor nameplate flow.

10. Local vs Central Storage

Storage location

Engineering advantage

Limitation

Local near cyclic user

Supports the transient before long/restrictive branch losses dominate

Needs local space, drainage, isolation and pressure control

Central receiver

Provides system-wide buffering and compressor control volume

May not correct a severe downstream restriction

Distributed storage

Can protect multiple zones and reduce local pressure collapse

Requires coordinated pressure bands and maintenance access

Process-protected receiver

Can provide controlled hold-up for critical utility users

Must be isolated from noncritical drains on stored air

11. Usable Storage Output

For an existing receiver, the calculator should also show usable free-air-equivalent volume across the selected pressure band.

V_free,usable = V_receiver x (P1,abs - P2,abs) / P_ref,abs

For the 2.0 m3 receiver in Test Case B, usable free-air-equivalent storage from 8.0 to 6.0 bar(g) is approximately 3.95 m3 at the stated reference pressure.

12. Output Specification

Output

Display rule

Required receiver volume

Primary result in L and m3

Net transient deficit

Demand minus continuing supply

Usable pressure band

P1, P2 and absolute pressure difference

Hold-up time

Shown when existing receiver volume is entered

Usable free-air storage

Equivalent reference-volume release

Assumptions

Isothermal / Z / temperature / flow basis / atmospheric pressure

Confidence

High / medium / preliminary

Warnings

Sustained deficit, narrow pressure band, basis mismatch, P2 >= P1, uncertain supply contribution

13. Validation and Guardrails

Condition

Required behaviour

Event flow <= 0

Block calculation

Supply during event < 0

Block calculation

Supply during event > event flow

Set net storage deficit to zero and explain no receiver volume is required for that defined deficit

P2 >= P1

Block calculation

Absolute P1 or P2 <= 0

Block calculation

Duration <= 0

Block sizing mode

Existing volume <= 0

Block hold-up mode

Flow basis missing

Gauge pressure without atmosphere

Require Patm or visible accepted default

Very long event / large volume

Warn that receiver storage may be the wrong primary solution

14. Design Margin and Non-Ideal Effects

The calculated geometric volume is a physics-based starting value, not the final vessel selection. A practical installation may require allowance for control delay, uncertainty in event flow, pressure drop between receiver and user, temperature change, inaccessible full vessel volume, future demand, simultaneous events and the actual compressor-control response.

The base result and margin-adjusted result should both remain visible.

V_selected_basis = V_calculated x (1 + margin/100)

Calculators and worked examples

These tools give indicative figures for screening, comparison and for preparing an enquiry. They run in your browser and send nothing. Prices, tariffs and efficiencies shown are example values: replace them with your own. Results are not a performance guarantee or a design certificate; final selection is confirmed by an engineer against the machine data sheet and the site.

Receiver storage sizing

Estimate the receiver volume needed to ride through a short burst of demand without the pressure falling below the limit.

The worked example below shows the method with fixed numbers. Turn on JavaScript to change the inputs.

Worked example

Inputs
  • Burst demand above compressor output (m³/min free air): 5
  • Burst duration (s): 20
  • Allowed pressure fall (bar): 0.7
Result
  • Receiver volume needed: 2,412 litres
  • 2.41 m³
  • Practical size (with 25% margin): 3,016 litres

Method. V = Q × t × P_atm / ΔP, where Q is the shortfall in free air (m³/min), t the time (min), ΔP the allowed pressure fall (bar) and P_atm = 1.013 bar. Isothermal; for a real system add a margin.

What to take from it. A receiver buys time. It does not create capacity: once it is spent the pressure keeps falling until the compressors catch up.

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