Why the same compressor can have several different numbers
Buyers often put two quotations side by side and compare the free air delivery (FAD) and kilowatt figures directly. The trouble is that those figures may not describe the same thing. A brochure value may be a nominal figure for a model family. A datasheet may quote FAD at a specific working pressure under ISO 1217 conditions. A quotation may round the value or quote it at the maximum pressure rather than the pressure you actually need. A site measurement taken in a hot compressor room in May is different again.
None of these numbers is necessarily wrong. Each answers a different question. The risk comes when unlike figures are compared as if they were alike, or when a family-level figure is assumed to apply to the specific serial number being sold, rented or overhauled.
Common reasons the numbers differ:
- Different working pressure: FAD falls as discharge pressure rises, and a 10 bar (145 psig) variant usually delivers less air than the 7.5 bar (108.8 psig) variant of the same frame.
- Different reference conditions: inlet pressure, inlet temperature and humidity change the mass of air drawn in.
- Package versus bare airend: airend data excludes the losses of the inlet filter, inlet valve, cooler and separator.
- Shaft power versus electrical input: motor efficiency, fan motors, dryer load and VFD losses are included in one figure and not the other.
- Production revision: later builds may use a different airend, motor or controller with different performance.
- Condition: a worn airend, a choked separator or a slipping belt reduces delivered air on an older machine.
The key terms you need to read a performance claim
| Term | What it means | What to check |
|---|---|---|
| Free air delivery (FAD) | Volume of air delivered at the discharge, converted back to inlet conditions | Stated working pressure, test standard, package or airend basis |
| Displacement | Theoretical swept volume, mainly quoted for piston machines | Never compare displacement with another machine’s FAD |
| Normal or standard flow (Nm³/min, SCFM) | Flow converted to defined reference conditions, often 0 °C or 20 °C and 1.013 bar | Which reference conditions were used |
| Shaft power | Power at the compressor input shaft | Excludes motor losses and auxiliaries |
| Total package input power | Electrical power drawn by the whole package | Includes fans, controls and any integrated dryer |
| Specific power | Input power divided by delivered flow, in kW per m³/min | Same pressure, same power basis, same flow basis |
| Maximum working pressure | The highest pressure the package is designed to run at | Not the same as the pressure at which FAD is quoted |
For displacement compressors, ISO 1217 is the recognised test method for acceptance testing, and its annexes set out how FAD and specific energy are measured and what tolerances apply. Industry verification schemes publish data sheets in a common format so that package input power and FAD can be compared at the same pressure. When a figure is quoted without reference to a test method, treat it as a nominal value until proven otherwise.
Rank the source before you use the number
Not all sources carry the same weight. A simple ranking prevents a brochure value from quietly overriding an acceptance test, or a salesperson’s verbal figure from becoming a design basis.
| Source | Typical strength | Best use |
|---|---|---|
| Witnessed acceptance test on the actual serial | Strongest for that machine | Contract acceptance, commissioning baseline |
| Manufacturer’s data sheet for the exact model, pressure variant and revision | Strong for new machines | Comparing new packages at the same pressure |
| Third-party verified data sheet | Strong, standard format | Like-for-like comparison of packages |
| Quotation figure | Medium; depends on what it references | Shortlisting, then confirm against a data sheet |
| Brochure or catalogue range | Indicative only | Early screening of model families |
| Site measurement with calibrated instruments | Good for condition, if method recorded | Checking a used, rented or overhauled machine |
| Verbal or remembered figure | Weak | Starting point for a question, never a decision |
How to check a performance figure step by step
- Identify the machine: make, model, pressure variant, serial number and year, ideally from a nameplate photograph rather than an invoice.
- Record the source of the figure: document title, revision or date, page, and who supplied it.
- Confirm the basis: FAD or displacement, package or airend, shaft or electrical input power.
- Note the test conditions: working pressure, inlet temperature, inlet pressure, humidity, cooling-air or cooling-water temperature and test standard.
- Check applicability: does the document cover this serial and revision, this motor and this cooling arrangement?
- Normalise before comparing: put all candidates at the same working pressure and the same power basis before calculating specific power.
- Decide what still needs verification: request a data sheet, a test report or a site measurement where the gap matters to the decision.
- Record the conclusion as confirmed, indicative or unresolved, so that the next engineer knows how far to rely on it.
Comparing quotations fairly
When a plant compares two or three new screw compressors, the most useful single figure is specific power at your actual working pressure, calculated on total package input power and FAD. A machine with slightly higher FAD but higher input power may cost more to run over its life. Because energy is usually the largest part of a compressor’s lifecycle cost, a difference of a fraction of a kW per m³/min matters on a machine that runs two or three shifts.
Points to align before comparing:
- Working pressure: compare at the pressure you will run. As a rule of thumb, each extra bar of discharge pressure costs about 7% more power.
- Control type: fixed-speed load/unload and variable-speed machines behave differently at part load. Full-load specific power alone does not tell you the part-load picture.
- Scope: integrated dryer, filters, receiver, heat recovery and controller features change input power and price.
- Cooling: air-cooled and water-cooled versions differ, and high-ambient variants may have larger coolers and fans.
- Electrical supply: 415 V, 50 Hz performance should be quoted for Indian supply, not converted from another frequency.
For part-load and station-level comparison, see our specific-power assessment method. It explains how to compare machines across a real demand profile rather than a single full-load point.
Used, rented and overhauled machines: rated is not actual
A used or refurbished compressor carries its original rating on the nameplate, but its actual delivery depends on airend clearances, inlet valve condition, separator differential pressure, oil condition, belt or coupling condition and cooling performance. A rental machine that has run hard on a quarry site will not necessarily deliver its catalogue figure without servicing.
Practical ways to check actual output on site:
- Receiver pump-up test: time how long the compressor takes to raise a receiver of known volume between two pressures, then calculate delivered air. It is simple and repeatable when the receiver volume and system isolation are known.
- Flow meter in the discharge line: a properly installed thermal or vortex meter, with adequate straight pipe, gives a direct reading.
- Electrical logging: record kW, load and unload time and pressure over a representative period to see how the machine behaves in real duty.
- Thermal indicators: discharge temperature on an oil-injected screw machine normally runs at about 75–95 °C. Higher values point to cooling or oil problems that also reduce efficiency.
Record ambient temperature with every site test. On a summer afternoon in Telangana or Andhra Pradesh, compressor-room temperatures of 45 °C or more are common, which reduces inlet air density and can bring the machine close to its high-temperature limit.
Red flags in performance claims
- A FAD figure with no stated pressure.
- Specific power calculated on shaft power and compared with another supplier’s package input power.
- Displacement figures for a piston compressor compared with a screw compressor’s FAD.
- A figure copied from a different pressure variant or an earlier production revision.
- “Equivalent to” claims for a replacement machine without a data sheet for both.
- Rounded headline values such as “100 cfm class” used as a design basis for a tool or process.
- A used machine sold on its nameplate rating with no test, no service history and no hour-meter reading.
Keeping a performance record that lasts
For each important compressor, keep a short performance file: the commissioning or acceptance data, the data sheet used at purchase, the serial and revision, and each later site measurement with its date, method, instruments, ambient conditions and the service state of the machine. When a performance complaint arises years later, this file shows whether the machine has degraded, whether demand has grown, or whether the original figure was never comparable in the first place. The same file supports overhaul-versus-replace decisions and audits.
How Reddy Compressors helps
We are an independent multi-brand compressor specialist based at Tarnaka, Secunderabad, serving industry since 2002. We sell new and used/refurbished compressors, rent from our own fleet, and service and supply spares for ELGi, Atlas Copco, Ingersoll Rand, KAESER, Chicago Pneumatic, Sullair, Doosan, Kirloskar and other brands. We are not an authorised dealer of any brand, which means we can read competing data sheets neutrally. We have tie-ups with all major and reputed brands.
- We put competing quotations on a common basis: the same working pressure, the same power basis and the same scope.
- We identify the machine from its nameplate and serial before accepting any performance claim for a used, rented or overhauled unit.
- We carry out site checks such as pump-up tests, pressure and power logging as part of air audits, and record the method with the result.
- Our 20+ service engineers and technicians cover the whole of Telangana and Andhra Pradesh, and we supply equipment, rentals and spares across India.
What to send us
- Nameplate photographs of the compressor, motor and dryer, if fitted.
- The quotation, data sheet or brochure page containing the figure you want checked.
- Your actual working pressure at the point of use and at the compressor.
- Running hours, service history and any recent measurements.
- A short note on the decision: purchase, rental, used machine, overhaul or a performance complaint.
Frequently asked questions
What is the difference between FAD and displacement on a compressor?
Displacement is the theoretical volume swept by the compression element, usually quoted for piston compressors. Free air delivery is the air actually delivered at the discharge, converted back to inlet conditions, after leakage, heating and valve losses. FAD is always lower than displacement, often by a significant margin on small piston machines. Compare machines only on FAD at the same working pressure, never one machine’s displacement against another’s FAD.
How do I compare specific power between two compressor quotations?
Ask both suppliers for total package input power and FAD at the same working pressure, measured to the same test standard, then divide kW by m³/min. Make sure both include or exclude the same items, such as an integrated dryer or cooling fans. If one supplier quotes shaft power and the other quotes electrical input, the comparison is invalid. For variable-speed machines, compare several load points rather than full load only.
Why is my compressor delivering less air than the nameplate rating?
Common causes are a partly closing inlet valve, a choked inlet filter, high separator differential pressure, worn airend or piston rings, slipping belts, high inlet temperature, or a pressure setting higher than the rated variant. Leaks downstream can also make a healthy machine look undersized. A pump-up test or flow measurement, taken with ambient temperature recorded, shows whether the compressor itself has lost output or the demand has grown.
Does ISO 1217 apply to every compressor performance figure?
No. ISO 1217 is the recognised acceptance-test method for displacement compressors, such as screw and piston types, and many manufacturers quote FAD to it. Centrifugal compressors are tested under a different standard. A brochure or quotation may not state any standard at all. Where performance matters to a contract or a decision, ask which standard and which annex the figure refers to, and at what working pressure.
Can I trust the performance of a used compressor from its nameplate?
The nameplate tells you what the machine was designed to do, not what it does today. Delivered air on a used compressor depends on airend or cylinder wear, valve condition, separator and filter state, cooling performance and control settings. Before buying or renting a used machine, ask for running hours, service history and a simple site output test. We check identity and condition before quoting any used or refurbished unit.
How much does high ambient temperature reduce compressor output?
Hot inlet air is less dense, so the mass of air delivered falls as compressor-room temperature rises, even though volumetric FAD at inlet conditions may look similar. High ambient also raises discharge temperature and can push an air-cooled package towards its high-temperature trip. In Indian summers, good room ventilation, ducting hot cooler air outside and drawing intake air from a cool, shaded point matter as much as the rating.
Related pages
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. No prices or tariffs are assumed: enter your own to see costs. Efficiencies and other figures shown are example values: replace them with your own. Results are not a performance guarantee or a design certificate; final selection is confirmed by a service engineer against the machine data sheet and the site.
Specific power comparison
Compare two compressors on what matters over life: the electrical power needed per unit of air delivered, and what that costs a year.
The worked example below shows the method with fixed numbers. Turn on JavaScript to change the inputs.
Worked example
Inputs
- Machine A: input power (kW): 75
- Machine A: delivered flow (m³/min): 11.5
- Machine B: input power (kW): 80
- Machine B: delivered flow (m³/min): 12.6
- Running hours per year: 6000
- Air actually needed (m³/min): 11
Result
- Machine A specific power: 6.52 kW per m³/min
- Machine B specific power: 6.35 kW per m³/min
- Energy to deliver the air needed: A: 4,30,435 kWh per year
- Energy to deliver the air needed: B: 4,19,048 kWh per year
- Energy difference: 11,387 kWh per year in favour of B
- Cost difference: Enter your electricity tariff (cost per kWh) above
Method. Specific power = input kW ÷ delivered flow (m³/min) at the same pressure and reference conditions. Annual cost = kW × hours × tariff. Use the full-load input power on the same test basis for both machines.
What to take from it. A small gap in specific power is multiplied by thousands of running hours. Compare on the same pressure and reference conditions.
Technical content reviewed by D. Srinivas Reddy, Managing Partner and service engineer, Reddy Compressors. Last updated 17 October 2026. How our engineering content is reviewed.
Bid normalisation: Net flow and comparable cost
Bring up to three compressor bids to one flow unit, check net flow against the requirement, then compare specific power, energy and installed cost on a like-for-like basis.
The worked example below shows the method with fixed numbers. Turn on JavaScript to change the inputs.
Worked example
Inputs
- Net flow required (m³/min): 20
- Running hours per year: 6000
- Bid A: offered flow: 21.5
- Bid A: flow unit: m³/min
- Bid A: flow stated at the required pressure?: Yes
- Bid A: internal consumption (m³/min): 1.8
- Bid A: total package input power (kW; 0 if not stated): 124
- Bid B: offered flow: 750
- Bid B: flow unit: cfm (ft³/min)
- Bid B: flow stated at the required pressure?: Yes
- Bid B: internal consumption (m³/min): 1
- Bid B: total package input power (kW; 0 if not stated): 126
- Bid C: offered flow: 22
- Bid C: flow unit: m³/min
- Bid C: flow stated at the required pressure?: No / unclear
- Bid C: internal consumption (m³/min): 0
- Bid C: total package input power (kW; 0 if not stated): 0
Result
- Bid A: offered flow: 21.5 m³/min
- Bid A: net flow: 19.7 m³/min – SHORT by 0.3 m³/min
- Bid A: specific power on net flow: 6.29 kW per m³/min (5.77 on offered flow)
- Bid A: energy per year at the required net flow: 7,55,330 for information only: this bid cannot supply the required net flow. kWh = 6.29 × 20 m³/min × 6,000 h (enter a tariff for the cost). Assumes specific power holds at this flow; use the bidder’s part-load data for a VSD or a part-load profile
- Bid A: comparable installed cost: Enter your own prices above
- Bid B: offered flow: 21.24 m³/min
- Bid B: net flow: 20.24 m³/min – meets, margin 0.24 m³/min
- Bid B: specific power on net flow: 6.23 kW per m³/min (5.93 on offered flow)
- Bid B: energy per year at the required net flow: 7,47,124 kWh = 6.23 × 20 m³/min × 6,000 h (enter a tariff for the cost). Assumes specific power holds at this flow; use the bidder’s part-load data for a VSD or a part-load profile
- Bid B: comparable installed cost: Enter your own prices above
- Bid C: offered flow: 22 m³/min (not at the required pressure)
- Bid C: net flow: Not established clarification needed: ask for data at the required pressure
- Bid C: package input power: Not stated ask the bidder for total package kW at the duty point
- Bid C: comparable installed cost: Enter your own prices above
- Eligible bids by energy at the required net flow: B (7,47,124 kWh) only one eligible bid with stated power
- Bids that pass the net-flow check: B compare cost only between these
Method. Flow is converted to m³/min (1 cfm = 0.0283168 m³/min; 1 L/s = 0.06 m³/min); this is valid only when the bids use the same reference conditions. Net flow = offered flow − internal consumption (dryer purge, drains). A bid whose data is not at the required pressure is not credited: it needs clarification, not arithmetic. Specific power = total package input kW ÷ net flow. Energy per year is compared like-for-like at the required net flow: specific power (on net flow) × required net flow × hours, so a larger machine is not charged for air the plant does not use. This assumes the specific power holds at that flow; for a VSD or a plant that runs mostly at part load, use each bidder’s supported part-load power for each hour band instead. Bids are ranked on energy only if they pass the net-flow check. Comparable installed cost = quoted price + required additions − confirmed discounts. Default: the page’s worked example B (20.0 m³/min net required at 8 bar g).
What to take from it. A low price or a larger gross flow cannot offset a failed mandatory requirement. Compare cost only between bids that pass the net-flow check.