All brands, all models · Sales · Rentals · Service & AMC · Spare parts · Used & refurbished+91 99590 60718WhatsAppEmailSecunderabad / Hyderabad
REDDY COMPRESSORS

Compressors

Blowers vs compressors: how to choose by duty

10 min read11 sections
Variable-speed rotary screw air compressor
Variable-speed screw compressor. Representative image.

Jump to the calculator ↓

What is the difference between a blower and a compressor?

Both machines add energy to air or gas. The difference is how much pressure they add and how they are built to do it. A blower is designed for high volume at a modest pressure rise, typically a fraction of a bar up to around 1 bar (14.5 psig) for most industrial duties. A compressor is designed for higher pressure ratios, typically 7–10 bar (101.5–145 psig) for plant air and far higher for drilling, testing and process gas.

The naming is not as clean as many sales brochures suggest. A Roots blower, for example, is technically a positive-displacement machine without internal compression: it carries pockets of air from inlet to outlet and the pressure rises only when the air meets the resistance of the system. Screw blowers do have some internal compression. Centrifugal blowers and centrifugal compressors use the same dynamic principle and differ mainly in stage count, speed and pressure ratio. So the honest answer is that blowers and compressors sit on one continuum, and the duty decides where your application falls.

One classic engineering definition classes machines by pressure ratio: fans up to about 1.11, blowers about 1.11–1.20 and compressors above that. In everyday industrial practice, however, Roots, screw and multi-stage machines working at ratios up to about 2 are still sold as blowers. Treat these figures as vocabulary, not a selection rule. Every manufacturer publishes its own operating envelope, and that envelope, not a label, is what you must match.

Start with the duty, not the machine name

The wrong first question is “Do I need a blower or a compressor?” The right first question is “What flow must move through what pressure difference, for how many hours, and with what air quality?” Once that is written down, the technology choice usually becomes obvious.

Define the duty with these variables:

  • Medium: ambient air, process gas, or air carrying dust or moisture.
  • Flow: volume flow at inlet conditions (m³/min or cfm), or mass flow for process work. State minimum, normal and peak.
  • Inlet absolute pressure: atmospheric, below atmospheric (vacuum duty) or above it (booster duty).
  • Outlet absolute pressure: what the process actually needs at the point of use, plus pipe and equipment losses.
  • Differential pressure: outlet minus inlet. For blower duty this is the figure manufacturers select on.
  • Pressure ratio: absolute outlet divided by absolute inlet. This drives temperature rise and power.
  • System resistance: how back-pressure changes with flow, for example water depth over diffusers or conveying line resistance.
  • Duty pattern: continuous, cyclic, or variable, with the turndown range required.
  • Air quality: whether oil-free air is mandatory, as in wastewater aeration, food or pharmaceutical conveying.
  • Site conditions: ambient temperature, altitude, dust, noise limits and available power.

Why absolute pressure and pressure ratio matter

Gauge pressure hides what the machine is really doing. Pressure ratio is calculated from absolute pressures: ratio = absolute outlet pressure ÷ absolute inlet pressure. At sea level, atmospheric pressure is about 1.013 bar(a).

Consider two duties with the same 0.6 bar gauge rise:

  • A pressure blower drawing from atmosphere and delivering 0.6 bar(g) works at a ratio of about 1.6.
  • A vacuum blower pulling 0.4 bar(a) at the inlet and discharging to atmosphere works at a ratio of about 2.5, even though the differential is the same 0.6 bar.

The second machine runs hotter and needs a different selection, which is why vacuum and pressure blowers are rated separately. Altitude also matters: on a high-altitude site the inlet air is thinner, so the same volume flow carries less mass of oxygen, and a blower supplying an aeration tank may need more volume flow to deliver the same oxygen. For low-pressure machines, small changes in inlet pressure or temperature move the operating point more than buyers expect.

How blowers and compressors compare

FactorIndustrial blowerAir compressor
Typical pressure riseFractions of a bar to about 1 bar (up to about 15 psig); vacuum duties to roughly 0.4–0.5 bar(a)Typically 7–10 bar (101.5–145 psig) for plant air; 14–28 bar (203.1–406.1 psig) for borewell drilling; higher for special duties
Typical pressure ratioLow, around 1.1–2High, often 8–11 for plant air
Flow characterLarge volume, often continuousModerate to large volume, often variable demand
Common technologiesRoots (lobe), screw blower, side-channel, centrifugal (single-stage high-speed or multi-stage)Rotary screw, reciprocating, scroll, tooth, centrifugal
Internal compressionNone (Roots) or limited (screw blower)Yes, by design
Oil in the air pathNormally oil-free compression chamberOil-injected or oil-free, depending on type
Storage and treatmentRarely uses receivers or dryers; air used directlyReceivers, dryers and filters are normal
Typical usesAeration, pneumatic conveying, combustion air, fluidisation, vacuum, agitationTools, instruments, process air, blasting, drilling, testing

Where blowers are the right choice

Blowers win wherever the process needs a large, steady volume at a low pressure. Producing that air with a 7 bar compressor and throttling it down wastes energy, because power rises with pressure ratio. As a working figure, each additional bar on a compressor costs about 7% more power, and dropping from 7 bar to well under 1 bar through a regulator throws that energy away as heat and noise.

  • Wastewater and effluent aeration: the back-pressure is set mostly by water depth over the diffusers plus losses, so the blower runs against a near-constant head. Turndown matters because oxygen demand varies through the day.
  • Pneumatic conveying: dilute-phase systems for cement, fly ash, flour, sugar and plastic granules commonly use Roots or screw blowers; dense-phase systems usually need compressors.
  • Combustion and burner air: furnaces, boilers and kilns need controlled volume at low pressure.
  • Fluidisation and aeration of bulk solids: silos, bins and air slides.
  • Vacuum duties: vacuum lifting, central vacuum and packaging lines.
  • Aquaculture and fermentation: large oil-free volumes at shallow depths.

Where a compressor is the right choice

A compressor is needed when the air must do work at higher pressure, be stored, or travel long distances. Pneumatic tools and cylinders are typically designed for about 6–7 bar (87–101.5 psig) at the tool. Instrument air, process air and air-operated valves need dry, clean air from a treated network. Construction breakers and rock drills need roughly 85–145 cfm at about 7 bar (101.5 psig), and borewell and DTH drilling needs 600–1,500 cfm at 200–400 psig (13.8–27.6 bar).

Compressors also suit variable demand better because a receiver can buffer peaks, and the plant can run base-load and trim machines. If the process needs both low-pressure bulk air and high-pressure tool air, two systems are normally cheaper to run than one high-pressure system regulated down.

Grey areas: when the choice is not obvious

Between about 1 and 3.5 bar (15–50 psig), both families compete. Dense-phase conveying, glass-bottle blowing pre-blow stages, some aeration at deep tanks and certain process duties fall here. In this band, compare these options against the actual duty:

  1. A screw blower, which has some internal compression and may be more efficient than a Roots blower at higher differentials.
  2. A low-pressure oil-free screw compressor built for 2–4 bar duty.
  3. A multi-stage or high-speed centrifugal blower, when flow is large and steady.
  4. A standard compressor with regulation, only if the volume is small or the air is already available.

For each option, ask the supplier for flow and absorbed power at your duty point and at your minimum flow, not only at rated conditions. Then compare specific power, in kW per m³/min, at the duty you will actually run.

How to select: a practical sequence

  1. Write down the process need: what the air does, at what pressure, at what flow, and for how many hours a year.
  2. Add system losses: pipework, diffusers, filters, silencers and valves, to arrive at the outlet pressure the machine must deliver.
  3. Convert to absolute pressures and work out the pressure ratio, including site altitude and the hottest ambient expected in an Indian summer.
  4. Define the turndown range needed between minimum and peak flow.
  5. Decide air-quality needs: oil-free compression chamber, inlet filtration standard and whether any treatment is needed downstream.
  6. Shortlist technologies whose operating envelope covers the whole range, not just the rated point.
  7. Compare specific power at real operating points, plus noise, heat rejection, maintenance and spares access.
  8. Plan standby: decide what happens when one machine is down, and whether a temporary hire unit can be connected.

Common mistakes we see

  • Selecting on motor kW or “cfm” alone, without the pressure at which that flow is delivered.
  • Using gauge pressure for ratio calculations, which understates vacuum and high-altitude duties.
  • Running low-pressure processes from the 7 bar plant-air system through a regulator.
  • Ignoring inlet temperature: hot air drawn from inside a plant room in summer reduces mass flow and raises discharge temperature.
  • Forgetting the safety relief valve and non-return valve on a positive-displacement blower, which keeps building pressure against a blocked line.
  • Under-sizing silencers and pulsation control on Roots blowers, causing noise complaints and pipe vibration.

How Reddy Compressors helps

Reddy Compressors has worked with industrial air since 2002 from our office at Tarnaka, Secunderabad. We sell new and used or refurbished blowers, covering Roots, screw, centrifugal and side-channel types, rent them, service them and supply their spares, alongside our compressor sales, rental and service work. Because we are an independent multi-brand specialist and not an authorised dealer of any one brand, we can compare technologies neutrally against your duty. We have tie-ups with all major and reputed brands.

In practice we help you define the duty point, check whether your existing compressed-air system is being throttled to feed a low-pressure process, and recommend a blower, a low-pressure compressor or a conventional compressor accordingly. Our team of over 20 service engineers and technicians covers the whole of Telangana and Andhra Pradesh, and we supply equipment, rental machines and spares across India. Where the duty needs measurement first, we can carry out an air audit with pressure and power logging.

What to send us

  • What the air is used for and the process it serves.
  • Required flow (minimum, normal and peak) and the pressure needed at the point of use.
  • Inlet conditions: atmospheric, vacuum or boosted, plus site altitude.
  • Running hours per day and whether duty is continuous or cyclic.
  • Air-quality needs, such as oil-free air for aeration or food contact.
  • For existing machines: make, model, serial number and a nameplate photo.
  • Available power supply and space or noise constraints.

Frequently asked questions

Is a blower the same as an air compressor?

No, although they overlap. A blower moves large volumes at a small pressure rise, typically up to about 1 bar (14.5 psig), while a compressor raises air to much higher pressures, typically 7–10 bar for plant air. Some machines, such as a Roots blower, are technically positive-displacement compressors without internal compression, so the label matters less than the flow and pressure the duty actually needs.

At what pressure does a blower become a compressor?

There is no single universal cut-off. Industry rules of thumb describe blowers by low pressure ratios and compressors by higher ones, and most industrial blowers work below about 1 bar gauge. Between roughly 1 and 3.5 bar both families compete. Select from the manufacturer’s operating envelope at your actual inlet and outlet absolute pressures rather than from a name or a single threshold.

Can I use my plant air compressor instead of a blower?

You can, but it is usually expensive. Generating air at 7 bar and regulating it down to a fraction of a bar wastes most of the compression energy as heat. For large, continuous low-pressure flows such as aeration or conveying, a dedicated blower normally uses far less power. Small or occasional low-pressure needs may still be fed sensibly from an existing compressed-air network.

Which is better for pneumatic conveying, a blower or a compressor?

Dilute-phase conveying, where material is carried in suspension at lower pressure, commonly uses Roots or screw blowers. Dense-phase conveying, which moves material in slugs at higher pressure and lower velocity, usually needs a compressor and receiver. The right choice depends on material, conveying distance, line resistance and rate, so the system designer should define pressure and flow before machine selection.

Why does a Roots blower get hot and noisy?

A Roots blower has no internal compression, so air is pushed back against the discharge pressure in a sudden pulse, causing heat, noise and pulsation. Temperature rises with differential pressure and with hot inlet air. Running above its rated differential, a blocked filter or a restricted discharge line will make it worse. Correct silencers, relief valves and inlet filtration keep it within limits.

Do blowers need air dryers and receivers like compressors?

Usually not. Most blower duties use air directly, for example aeration or combustion, so dryers and large receivers are uncommon. Some conveying of moisture-sensitive powders may need air cooling or drying. Blower packages do still need good inlet filtration, a relief valve, a non-return valve and silencing to protect the machine and the process.

Field guide

Compressor, blower or vacuum pump: The three-way choice

All three move gas, but each is built for a different job. The simplest way to remember it: a compressor makes pressure, a blower makes flow, and a vacuum pump makes vacuum.

Air compressorBlowerVacuum pump
JobStore usable energy as pressureMove large volumes at modest pressureRemove gas to reach pressure below atmospheric
Typical rangeIndustrial plants commonly 7 to 16 bar; special duties go far higherUp to about 1 bar(g)Rough vacuum through high and ultra-high vacuum
Common typesScrew, reciprocating, scroll, centrifugal, axialRoots, screw, centrifugal, side channelRotary vane, liquid ring, dry screw, Roots booster, turbomolecular
Typical usesTools, automation, painting, packaging, instrument airWastewater aeration, conveying, combustion air, ventilationPackaging, drying, degassing, holding and lifting, coating, semiconductor

Choosing between them

  1. Start with the pressure or vacuum level the process needs
  2. Then the flow, and whether it varies through the day
  3. Check the gas: clean air, humid, dusty, or carrying vapour
  4. Check contamination limits (oil-free or dry running)
  5. Compare energy cost over the machine’s life, not only price
  6. Plan redundancy and maintenance access

Using a compressor to do a blower’s job, or the other way round, wastes energy. Aeration at 0.5 to 1 bar served by a 7 bar compressor is a classic example. For the technologies see Roots blowers, screw blowers, side-channel blowers, industrial vacuum systems and vacuum selection.

Efficiency and monitoring

Energy is the largest running cost for all three. Variable-speed drives, good controls, leak control and heat recovery help. Vibration, temperature, pressure, flow and power trends reveal faults early; see maintenance and condition monitoring.

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.

Pressure ratio for a blower or compressor duty

Turn inlet and outlet pressures, gauge or absolute, into absolute pressures, differential and pressure ratio, and see where the duty sits between blowers and compressors.

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

Worked example

Inputs
  • Inlet pressure (in the unit below): 0
  • Inlet pressure unit: bar g
  • Outlet pressure (in the unit below): 0.6
  • Outlet pressure unit: bar g
  • Local atmospheric pressure (bar a): 1.013
  • Inlet temperature (°C): 30
  • Ratio of specific heats k (air 1.4): 1.4
Result
  • Inlet, absolute: 1.013 bar a
  • Outlet, absolute: 1.613 bar a (0.6 bar g, 8.7 psig)
  • Differential pressure: 0.6 bar = 600 mbar = 8.7 psi
  • Pressure ratio: 1.592 absolute outlet ÷ absolute inlet
  • Where the duty sits: Blower territory Roots, screw, side-channel or centrifugal blower
  • Ideal discharge temperature, internal compression: 73 °C
  • Ideal discharge temperature, Roots blower: 81 °C (no internal compression; real machines run hotter still)

Method. p(abs) = p(gauge) + local atmospheric pressure (about 1.013 bar a at sea level, lower at altitude). Differential = outlet − inlet (absolute). Pressure ratio = absolute outlet ÷ absolute inlet. Ideal discharge temperature: with internal compression (screw, centrifugal, compressor) T₂ = T₁ × r^((k−1)/k); a Roots blower has no internal compression, so ideally T₂ = T₁ × (1 + (r − 1)(k − 1)/k), which is hotter. Vocabulary bands used here: up to about 1.1 fan range; up to about 2 the duty is sold as a blower (Roots, screw, side-channel, centrifugal); about 2 to 4.5 (roughly 1–3.5 bar g from atmosphere) is the grey area where screw blowers, low-pressure oil-free screw compressors and multistage centrifugals compete; plant-air compressors work at about 8–11. Select from the maker’s envelope, not a label.

What to take from it. Gauge pressure hides the duty. The same 0.6 bar differential is a ratio of about 1.6 as a pressure blower and about 2.5 as a vacuum blower, and the vacuum duty runs hotter.

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.

Talk to Reddy Compressors

Tell us the job. We will send the right answer.

Buying, hiring, servicing or looking for a part: share what the air must run, the pressure and the site. A nameplate photo is often enough to start.

+91 99590 60718+91 92468 88812