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REDDY COMPRESSORS

Rental & temporary air

Temporary air hoses, manifolds and distribution on site

18 min read15 sections
Diesel portable air compressor on a hire job
Portable compressor for rental duty. Representative image.

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Why distribution decides what the compressor actually delivers

A rental compressor can be correctly sized and still leave tools starved at the far end of the site. The usual reason is the distribution between the machine and the user: a long run of small-bore hose, a reduced-bore coupling, a crowded manifold or a branch that serves more tools than it was meant to. The compressor gauge shows healthy pressure while the breaker, blast nozzle or process connection sees much less.

Every hose, fitting, valve and filter consumes some of the available pressure. Pressure lost in distribution is pressure the compressor had to generate and then waste. On an oil-injected screw machine, as a rule of thumb, each extra bar of discharge pressure costs about 7% more power, so raising the set pressure to compensate for a poor hose layout burns more diesel or electricity for the whole hire period.

Good distribution therefore has two aims: deliver the agreed pressure and flow at each point of use, and do it safely for the full duration of the job, across shifts, weather and changing work fronts.

How do I size a compressor hose for flow and length?

Start from the users, not the compressor. List each tool or process, its air demand at working pressure, the minimum pressure it needs at its inlet and how many will run together. A paving breaker typically uses 85–145 cfm at about 7 bar (101.5 psig); a No. 6 blast nozzle uses about 280–300 cfm at 7 bar. Sum the simultaneous demand on each branch and on the main line.

Technician connecting an air hose to a portable compressor
Connecting hoses on site. Illustrative graphic.

Then work out the pressure available for losses: compressor delivery pressure minus the minimum pressure needed at the furthest user. That margin has to cover the aftercooler, separator or dryer if fitted, the main hose, the manifold, the branch hose, couplings and any tool-side filter-regulator-lubricator.

Pressure drop in a straight hose rises roughly with the square of flow and falls very steeply with bore, approximately with the fifth power of internal diameter for the same flow and length. That is why a modest step up in bore has such a large effect. Comparing 50 mm and 38 mm bore under the same conditions, (38 ÷ 50)⁵ is about 0.25, so the larger hose loses roughly a quarter of the straight-run pressure. The relationship is approximate, does not include fittings, and should be checked against the hose maker’s data.

Use the actual internal bore, not the outside diameter or the coupling size. Hoses that look similar can differ in bore, and a single reduced-bore adapter can undo the benefit of a generous main line.

Duty on the lineTypical demand at about 7 bar (101.5 psig)What usually governs hose choice
Single breaker or rock drill85–145 cfmBranch length and tool coupling bore
Two to four breakers from one machineAbout 170–580 cfm in totalMain line bore, manifold outlets and branch lengths
One No. 6 blast nozzle280–300 cfmShort, large-bore line to the blast pot; moisture control
Two No. 6 or one No. 7–8 nozzleAbout 380–600 cfmMain line and pot hose sized together; aftercooler and separator
Plant air tie-in from a rental stationAgreed shortfall from the duty specificationHeader connection size, isolation and check valve arrangement

Figures for tools and nozzles are typical industry values and vary with wear, make and working pressure. Use the tool maker’s data when it is available.

Couplings, connectors and pressure ratings

Couplings are where most restriction and most accidents happen. Claw (universal) couplings are common on site tool hoses; ground-joint and threaded fittings appear on larger mains and plant connections; flanged connections suit high-volume stations. Mixing families with adapters adds restriction and creates points where a joint can be assembled wrongly.

  • Check the pressure rating of every component, hose, coupling, valve and manifold, against the maximum pressure the compressor can produce, not just its normal working pressure. High-pressure packages for drilling or testing can deliver 17–24 bar (246.6–348.1 psig) or more, well above the rating of ordinary tool hose.
  • Check the temperature rating. Air leaving a compressor without an aftercooler is hot, and hose lying in the Telangana or Andhra Pradesh summer sun can reach high surface temperatures on its own.
  • Use whip checks (safety restraint cables) across every claw or quick coupling and at hose-to-equipment connections, plus locking pins or clips where the coupling design provides for them.
  • Use crimped or properly banded hose ends. Worm-drive clamps on pressurised air hose are a common cause of blow-offs.
  • Avoid reduced-bore quick couplings on high-flow lines. They are convenient on small tools but can choke a breaker or blast line.

Designing the manifold

A manifold turns one main line into several controlled outlets. On a construction site it may feed four breakers; on a plant shutdown it may split a rental station between a header connection and local maintenance points. Its job is to share air without letting one user starve or endanger another.

  • Size the manifold body and inlet for the total simultaneous flow, not for one outlet.
  • Give each outlet its own isolation valve so a branch can be shut and depressurised without stopping the others.
  • Provide a pressure gauge on the manifold and, where useful, on the furthest branch, so the operator can see distribution losses directly.
  • Fit a vent or bleed valve so the manifold and branches can be depressurised before couplings are broken.
  • Mount the manifold on a stable frame or skid above standing water and dust, with outlets facing away from walkways.
  • Label outlets by service and destination. Where breathing air, instrument air or high-pressure air is present on the same site, keep them on separate, clearly different connections so an incorrect connection is hard to make.

Breathing air is a specialist system with its own standard, purification and monitoring. It must never be taken from a general tool-air manifold.

Routing temporary hoses on a working site

A hose that is well sized but badly routed will be crushed, kinked, cut or tripped over before the job ends. Plan the route with the site team before the compressor arrives and walk it once the hose is laid.

  1. Mark the compressor position, the manifold and each work point on a simple site sketch, with real route lengths.
  2. Keep runs as short and straight as practical, with gentle bends rather than kinks; avoid coiling surplus hose near the compressor, which adds loss and traps heat.
  3. Where hoses cross roads or haul routes, use ramps or protective covers, or route overhead on supports with adequate clearance. Never leave a pressurised hose loose across vehicle movements.
  4. Keep hoses away from hot exhausts, sharp steel edges, welding and cutting work, and chemical spills.
  5. Support long vertical runs, for example up a structure or into a shaft, so the coupling is not carrying the hose weight.
  6. Allow drainage at low points on long mains so condensate does not collect and slug into tools.
  7. Record the route and update it whenever a work front moves, so the next shift knows what is live.

Moisture, oil and cleanliness in temporary lines

Compressed air leaving a compressor is saturated with water vapour. As it cools in a long hose, water condenses and collects. For breakers this mainly causes wear and, in cold conditions, icing at the exhaust. For blasting, painting, cable blowing and process connections it can spoil the work. An aftercooler and moisture separator at the compressor, with drains on the manifold, remove most free water; a refrigerated dryer, typically giving a pressure dew point around +3 °C, is added where the application needs drier air.

New or stored hoses can contain dust, rubber particles and old oil. Blow new hose through before connecting it to sensitive equipment, cap open ends during storage and transport, and keep process or oil-free duties on dedicated, clean hose. Where air enters a plant header, agree the required ISO 8573-1 quality class with the plant team and fit the filtration needed to meet it.

Commissioning and daily checks

Before handing a distribution system to the site team, pressurise it in stages and check it under real load.

  • Visual check of every joint, whip check, clip and support before pressurising.
  • Pressurise slowly with all outlets closed; listen and look for leaks; correct before opening any branch.
  • Run the expected simultaneous load and read pressure at the compressor, at the manifold and at the furthest user. The difference is your real distribution loss.
  • Confirm each outlet isolates and vents as intended.
  • Each shift: walk the route, check for damage, drain low points and separators, confirm restraints are still fitted, and log pressures at the same points.
  • Before breaking any connection: isolate, vent and confirm zero pressure on a gauge. Never uncouple a live hose.

Common distribution problems and how to fix them

SymptomLikely causeWhat to do
Good pressure at the compressor, weak tools at the far endSmall bore, long run or restrictive couplingsIncrease main bore, shorten the route, remove reduced-bore adapters
One tool slows when another startsBranch or manifold undersized for simultaneous demandSeparate branches, enlarge manifold inlet, check total demand against compressor capacity
Water at tools or in blast potNo aftercooler or separator, undrained low pointsAdd aftercooler and separator, drain points, dryer where needed
Coupling blow-off or hose whipMissing restraint, wrong clamp, damaged couplingStop, isolate and vent; replace with rated coupling and fit whip checks
Pressure falls steadily through the shiftGrowing leaks or damage, or demand creepLeak walk, log pressures, review demand with the site team

Hose selection by bore, pressure rating and coupling

The flow column shows the flow each bore carries with about 0.3 bar of loss over 30 m of straight hose at 7 bar(g) (101.5 psig). It is calculated with the standard smooth-bore formula below. Couplings, bends and adapters add to the loss, so treat these flows as an upper limit, not a target.

Hose IDFlow at about 0.3 bar loss per 30 mTypical dutyWorking pressure classesCoupling usually fitted
13 mm (½”)about 20 cfmBlowguns, small tools10–20 bar(g)Quick coupler or claw
19 mm (¾”)about 55 cfmWhip to one breaker or rock drill; keep it short (15 m or less)10–20 bar(g)Claw (also called crow’s foot or universal), with safety pin or clip
25 mm (1″)about 120 cfmOne heavy breaker on a longer run; small blast pot10–20 bar(g)Claw with safety pin, or threaded hose tail
32 mm (1¼”)about 230 cfmBranch to two tools; blast pot supply10–20 bar(g)Threaded (BSP) tail with crimped ferrule
38 mm (1½”)about 370 cfmNo. 6 blast nozzle supply; branch mains10–20 bar(g)Threaded or ground-joint coupling
50 mm (2″)about 780 cfmCompressor-to-manifold main; DTH drilling hose17–20 bar(g); 25–40 bar(g) drilling gradesThreaded or hammer (wing) union, restrained at both ends
63 mm (2½”)about 1,450 cfmLong mains from one large or two medium compressors10–20 bar(g)Threaded or flanged
76 mm (3″)about 2,400 cfmCombined mains from several compressors10–20 bar(g)Flanged
100 mm (4″)about 5,000 cfmPlant tie-ins and long headers10–16 bar(g)Flanged

Burst ratio. Compressed-air hose is normally built to a minimum burst pressure of four times its working pressure. Some constructions use three times. A 20 bar(g) (290 psig) hose therefore has a burst rating of about 80 bar. The burst figure is a design margin, not something you can use. Run the hose only up to its branded working pressure, and check that pressure against the compressor’s maximum pressure and the safety valve setting.

Material. Use synthetic rubber with an oil-resistant (nitrile-based) inner tube on oil-injected compressors. Carryover oil swells and softens ordinary rubber tubes. Check the temperature rating as well. Discharge air leaving a hot aftercooler on a 45 °C day can exceed the rating of light-duty PVC hybrid hose.

Worked example: Pressure drop along a hose run

The estimate uses Δp = 450 × q1.85 × L ÷ (d5 × p). Here Δp is the loss in bar, q is the free-air flow in L/s, L is the length in m, d is the internal bore in mm and p is the inlet pressure in bar(a).

The duty (illustrative) is a 600 cfm compressor at 7 bar(g) feeding a manifold 60 m away.

  • Flow: 600 ÷ 35.315 = 16.99 m³/min = 283 L/s. Inlet pressure: 7 + 1.013 = 8.013 bar(a).
  • 50 mm hose: Δp = 450 × 2831.85 × 60 ÷ (505 × 8.013) = 0.37 bar.
  • 38 mm hose: 1.46 bar. That is almost four times the 50 mm loss, as (50 ÷ 38)5 = 3.9.
  • 63 mm hose: 0.12 bar.

The cost of one reduced-bore coupling. Fit a coupling with a 25 mm bore in the middle of that 50 mm line. At 8.013 bar(a) and 30 °C the air density is 9.21 kg/m³. The mass flow is 0.283 × 1.204 = 0.341 kg/s, so the air speed in the hose is 0.341 ÷ (9.21 × 0.001963) = 18.9 m/s. Through the 25 mm bore it rises to (50 ÷ 25)² × 18.9 = 75 m/s. The contraction and re-expansion lose about 0.94 velocity heads. That is 0.94 × 9.21 × 75² ÷ 2 = 24,400 Pa, or about 0.24 bar, roughly the same loss as another 40 m of 50 mm hose. Couplings in a main must have a full bore.

Together, the hose and that one coupling lose 0.37 + 0.24 = 0.61 bar. Each extra bar of compressor discharge pressure costs about 7% more power, so making up that 0.6 bar at the compressor costs about 4% more power. For the general calculator and the distribution loss method, see distribution losses.

Manifolds for combining several rental compressors

When two or more hire compressors feed one site, the manifold has to do more than split the flow:

  1. A non-return valve on each compressor’s inlet to the manifold. Without one, a machine that unloads or stops can be back-fed from the manifold if its own minimum pressure or check valve leaks. The flow then runs out through its blowdown valve, wasting the other machines’ air. It can also try to restart against pressure.
  2. An isolation valve after each non-return valve. This lets one compressor be serviced or refuelled while the others carry on.
  3. A body sized for the combined flow. Keep the air speed in the manifold body to about 8–10 m/s. The body must also carry a pressure gauge, a drain at its low point and a vent valve.
  4. A relief valve, if needed. Fit one wherever an isolated section can be pressurised above the rating of its weakest component.
  5. Staggered pressure settings. Machines with identical regulator settings share load erratically. Set the lead machine 0.3–0.5 bar above the lag machines, so the lag machines unload first as demand falls.

Worked example (illustrative): three 750 cfm compressors feed a common manifold at 7 bar(g).

  • Combined flow: 2,250 ÷ 35.315 = 63.7 m³/min, or 1.062 m³/s of free air.
  • At 8.013 bar(a), the actual volume flow is 1.062 × 1.013 ÷ 8.013 = 0.134 m³/s.
  • At 8 m/s, the area needed is 0.134 ÷ 8 = 0.0168 m², which is a 146 mm bore. A 150 NB manifold body is suitable. At 10 m/s, the bore needed is 131 mm.

For connecting the manifold into permanent plant pipework, see tie-in and changeover.

Specifying a hire with hoses, a receiver and a manifold

A compressor alone does not make a working air supply. When asking for a complete package, specify each item so that quotes can be compared fairly:

ItemState in the enquiryWhy it matters
CompressorFree air delivery at the working pressure, the maximum pressure, and diesel or electric driveA rating at a different pressure is not comparable
Main hoseBore, length, working pressure class, and coupling type at each endSets the loss to the manifold, as in the worked example above
ReceiverVolume, pressure rating, auto drain, and valid test and inspection papersAbsorbs demand peaks when breakers or blast pots start, and collects condensate
ManifoldNumber and size of outlets, non-return valves if more than one compressor is used, gauge and drainLets compressors be combined or serviced without shutting the site
Branch hoses and whipsBore, length, and whip checks at every couplingThe usual place where flow is lost and accidents happen
TreatmentAftercooler, water separator, and a dryer if it is neededBlasting, painting and plant tie-ins need dry air

For the broader temporary-air planning process, see rental engineering.

Whip checks, stored energy and when to retire a hose

Stored energy is the reason couplings must be restrained. Thirty metres of 50 mm hose at 7 bar(g) holds 0.059 m³ of air. Released, it can deliver about 53 kJ if it expands quickly (adiabatic) and up to 98 kJ if it expands slowly (isothermal). That is comparable to the energy of a one-tonne car at 36–50 km/h, and it is concentrated in a free hose end.

Finding at inspectionAction
Exposed or cut reinforcement, blister, bulge or soft spotRetire the hose immediately
Cover cracking that reaches the reinforcement after a bend testRetire
Swollen or sticky inner tube from oil carryoverRetire, and correct the oil carryover
Ferrule moved on the hose, or a worm-drive clamp used on a mainRemake the end with a crimped ferrule or rated band clamp
Claw lugs worn, gasket missing, or safety pin or clip missingReplace the coupling half or the gasket before use
Whip check frayed, or its loops not fitted over the hose endsReplace the whip check and refit it correctly
Permanent kink or flattened sectionCut out the section and re-end the hose, or retire it
Branding illegible, or pressure class unknownDo not use at drilling or high pressure

Record the manufacture date marked on each hose and follow any maximum service age set by the site. If a pressure test is required, test hydrostatically, never with air. Test to the proof pressure the hose maker states, then inspect the hose again.

How Reddy Compressors helps

We supply rental compressors from our own fleet, 50–2,000 cfm and 2–30 bar (29–435.1 psig), diesel and electric, together with the distribution the job needs: main and branch hoses, couplings and whip checks, manifolds, aftercoolers and moisture separators, and dryers where the application calls for them. We size the hose and manifold from your list of users and route lengths, not from a standard kit.

We are an independent multi-brand business, not an authorised dealer, and we sell, rent and service ELGi, Atlas Copco, Ingersoll Rand, KAESER, Chicago Pneumatic, Doosan and other makes. We have tie-ups with all major and reputed brands. With over 20 service engineers and technicians, our teams support hire jobs across Telangana and Andhra Pradesh, and we supply compressors, accessories and spares across India. On hire jobs we change oil and service every 300 running hours, and we can provide operators where agreed.

Call +91 99590 60718 or +91 92468 88812, WhatsApp +91 99590 60718 or email reddycompressors@gmail.com. Our office is at Srinilayam, 12-13-200, First Floor, Street No. 1, Tarnaka, Secunderabad 500017.

What to send us

  • List of tools or processes, with air demand and minimum pressure for each
  • How many will run at the same time, and on which branch
  • A sketch or photo of the site with approximate route lengths and road crossings
  • Required air quality (general tool air, dry air for blasting or coating, plant header class)
  • Hire duration, working hours per day and any planned moves of work fronts
  • Existing hoses or fittings you intend to use, with bore and pressure rating

Frequently asked questions

What size air hose do I need for a 400 cfm compressor?

It depends on how far the air must travel and how many users share it. A 400 cfm machine feeding a manifold close by may use a large main hose to the manifold and smaller branches to each tool. Over longer distances the main bore has to increase to keep the pressure drop within your margin. Send us the route length, tools and working pressure and we will size the main and branch hoses so the furthest tool still sees its required pressure.

Why do my breakers lose power at the end of a long hose?

The most likely cause is pressure drop in the distribution. Long small-bore hose, reduced-bore couplings or too many tools on one branch can take a large share of the compressor’s pressure before the air reaches the breaker. Check pressure at the compressor and at the tool under load; the difference shows the loss. A larger bore main line, shorter route or a properly sized manifold usually restores performance without changing the compressor.

Are whip checks mandatory on compressed-air hoses?

Site rules and your safety procedures decide what is mandatory, but restraining pressurised couplings is widely regarded as essential good practice. A claw coupling that parts under pressure can whip violently and cause serious injury. Fit a whip check across each coupling and at hose-to-equipment joints, use locking pins where provided, and always isolate and vent before uncoupling. We supply restraints with our rental hoses.

Can I run several tools from one compressor with a manifold?

Yes, provided the compressor’s delivered flow at working pressure covers the simultaneous demand of all the tools, with some margin, and the manifold and main hose are sized for the combined flow. Each outlet should have its own isolation valve and the manifold a gauge and vent. If the total demand exceeds the compressor, tools will slow and pressure will fall, so we size the machine and distribution together.

How do I stop water coming out of my air hose on site?

Water forms as hot, saturated air cools in the hose. Fit an aftercooler and moisture separator at the compressor, drain the separator and low points regularly, and avoid long undrained dips in the hose route. For blasting, coating, cable blowing or plant connections, add a refrigerated dryer, which typically gives a pressure dew point around +3 °C. We can supply aftercoolers, separators and dryers with rental compressors.

Can I use ordinary hose with a high-pressure drilling compressor?

Only if every hose, coupling and fitting is rated above the maximum pressure the compressor can produce. Drilling and testing packages commonly deliver 17–24 bar (246.6–348.1 psig) and some reach 35 bar (507.6 psig), which exceeds the rating of ordinary tool hose. Check the marked working pressure on each component and replace anything unrated or damaged before connecting it.

Does compressor hire include hoses, a receiver and a manifold?

Hoses, couplings, manifolds, aftercoolers, separators and dryers can be hired with Reddy Compressors’ fleet compressors, but ask for each item to be listed in the quote. A useful package names the main hose bore, length and pressure class, the receiver volume and test papers, and the number of manifold outlets. It also confirms non-return valves when several compressors feed one manifold, along with whip checks and any aftercooler, separator or dryer. Give the hire company your tool list, the tools that run at the same time, and the route lengths, so that the hoses and manifold are sized for the flow.

What is an air compressor manifold used for?

A manifold splits one compressor’s output into several isolated outlets, or combines several compressors into one supply. Each outlet has its own valve, so tools can be connected or removed without stopping the others. A good manifold also has a gauge, a low-point drain and a vent valve. When several compressors are combined, each inlet needs a non-return valve and an isolation valve. The body should be sized to keep the air speed to about 8–10 m/s. For three 750 cfm machines at 7 bar(g), that means a body of about 150 mm bore.

What pressure rating should a compressor hose have?

The hose’s branded working pressure must be at least the compressor’s maximum pressure, including the safety valve setting. Nominal working pressure alone is not enough. For a standard 7–10 bar(g) compressor, a 17–20 bar(g) hose is common. Drilling compressors at 25–35 bar(g) need hose and couplings rated for that duty along their whole length. Compressed-air hose is normally made with a burst pressure four times its working pressure. That margin is for safety, and you should never use it as extra working capacity.

When should a compressor hose be replaced?

Replace a compressor hose straight away if the reinforcement is exposed or cut, or if it has a blister, bulge or soft spot. Replace it too if the inner tube is swollen by oil, or if the ferrule has slipped on the hose. Replace worn claw lugs, missing gaskets, missing safety pins and frayed whip checks before the hose is used again. Cut out permanent kinks, or retire the hose. If the branding is illegible, keep it off high-pressure work. Inspect the hose at every set-up and record its manufacture date against the site’s service-age rule.

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.

Pipe pressure drop and sizing

Check the pressure drop and air velocity in a compressed-air line, or find the smallest bore that keeps the drop within a target.

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

Worked example

Inputs
  • Flow (m³/min free air): 12
  • Inlet pressure (bar g): 7
  • Pipe length (m): 150
  • Inside diameter (mm): 80
  • Roughness (mm): 0.046
  • Fittings allowance (% extra length): 30
  • Air temperature (°C): 30
  • Target pressure drop (bar): 0.1
Result
  • Pressure drop: 0.059 bar (0.839% of the inlet gauge pressure)
  • Air velocity: 5.22 m/s
  • Reynolds number: 2,06,066
  • Smallest bore for the target drop: 73 mm inside diameter
  • Velocity check: Within the common rule-of-thumb range for mains (roughly up to 15–20 m/s)

Method. Darcy–Weisbach: ΔP = f × (L/D) × ρv²/2, with the friction factor f from the Swamee–Jain relation and air density taken at mean line pressure. Fittings are allowed for as extra equivalent length. Typical commercial steel roughness is about 0.046 mm.

What to take from it. Pressure drop varies roughly with the fifth power of the bore at constant flow, so a larger main is a cheap way to hold pressure.

Technical content reviewed by D. Srinivas Reddy, Managing Partner and service engineer, Reddy Compressors. Last updated 7 November 2026. How our engineering content is reviewed.

Compressed air demand estimate

Add up the air your tools and processes use, apply duty and simultaneity, then add leakage and growth allowances to reach a capacity to enquire about.

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

Worked example

Inputs
  • Unit for the air each tool uses: L/s
  • Group A: number of tools: 6
  • Group A: free air each (in the unit above): 4
  • Group A: duty (%): 40
  • Group B: number of tools: 2
  • Group B: free air each (in the unit above): 15
  • Group B: duty (%): 60
  • Group C: number of tools: 1
  • Group C: free air each (in the unit above): 40
  • Group C: duty (%): 80
  • Simultaneity of all tools (%): 65
  • Leakage allowance (%): 15
  • Growth allowance (%): 10
Result
  • Connected demand: 94 L/s = 199 cfm
  • Average demand (duty-weighted): 59.6 L/s = 126 cfm
  • Simultaneous peak: 61.1 L/s = 129 cfm
  • Design basis (higher of average and peak): 61.1 L/s = 129 cfm
  • Design capacity with allowances: 77.29 L/s = 4.64 m³/min = 163.8 cfm

Method. Average demand = Σ(number × air per tool × duty). Peak = Σ(number × air per tool) × simultaneity. The peak can never be lower than the average, so the design basis is the higher of the two. Design capacity = design basis × (1 + leakage) × (1 + growth).

What to take from it. Leakage and growth allowances move the answer as much as any single tool. Where you can, replace catalogue figures with measured ones.

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