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REDDY COMPRESSORS

Engineering

Compressed Air for Data Centres: Critical Air for Critical Infrastructure

17 min read17 sections

Who this page is for: facilities managers, critical-environment engineers, MEP consultants and operations heads responsible for data-centre campuses, colocation halls and enterprise server facilities, who need to know exactly where compressed air sits in their infrastructure, how critical each use really is, and how to engineer the air plant so it never becomes the weak link.

Key facts

  • Compressed air is not the primary means of server cooling. Heat leaves through air-handling, chilled-water, direct-expansion, evaporative or liquid-cooling systems; compressors are a small supporting utility.
  • A whole-campus control-air and sprinkler-maintenance load is typically 0.05–0.5 m³/min (1.8–17.7 cfm), excluding nitrogen generation and workshop air. The engineering problem is availability, not capacity.
  • Pneumatic control air is typically supplied at 5–7 bar(g) (72.5–101.5 psig) and regulated down at the device. Sprinkler supervisory air is far lower: typically about 1–3 bar(g) (14.5–43.5 psig) on dry-pipe systems and about 0.5–1 bar(g) (7.3–14.5 psig) on pre-action supervision, as the valve maker sets it.
  • A refrigerated dryer gives a pressure dew point of about +3 to +7 °C. Lines running outdoors or beside chilled-water mains need a desiccant dryer at about −20 °C to −40 °C.
  • Indicative air quality for control air is ISO 8573-1 class [2:4:2] or better, tightened to [2:2:2] where pipework runs cold or exposed. The device maker sets the actual requirement.
  • Usable free air in a receiver ≈ volume × usable pressure band ÷ atmospheric pressure: 2.0 m³ working between 7.0 and 5.5 bar(g) (101.5 and 79.8 psig) holds about 2.96 m³.
  • Summer plant-room temperatures in Telangana can exceed 45 °C where ventilation is poor, which is at or beyond the maximum ambient rating of many packaged compressors and refrigerated dryers.

Where compressed air actually appears on a data-centre campus

The first deliverable is a sober map. Walk every plant room, roof and generator yard and record each pneumatic consumer, its supply pressure and what it does if pressure disappears. The real load is usually smaller and more scattered than drawings suggest, while a few critical items depend on air nobody has classified.

Pneumatic actuators, dampers and valves in HVAC and chilled-water plant

Most data-centre HVAC is electrically actuated, but pneumatic actuators remain in some chilled-water plants, older enterprise buildings and large butterfly valves where fast, fail-safe stroking is wanted. A spring-return actuator has a defined fail position, which is a strength only if it was chosen deliberately: a chilled-water isolation valve that fails closed can starve a cooling loop; a damper that fails open can upset containment.

Supply is typically 5.5–7 bar(g) (79.8–101.5 psig) to a local regulator; older positioners still use a 0.2–1.0 bar(g) (2.9–14.5 psig) signal. Bleed-type positioners consume continuously, so a plant room of thirty devices can reach 0.1–0.2 m³/min (3.5–7.1 cfm) including fittings leakage.

Dry-pipe and pre-action sprinkler air supply

Dry-pipe and pre-action sprinkler networks keep their pipework charged with air or nitrogen instead of water, so a damaged head over IT equipment does not flood the hall. The supervisory gas holds a dry-pipe valve shut, or in pre-action systems lets a pipe breach raise an alarm. In service the air maintenance device feeds only a trickle. Typical supervisory pressures are about 1–3 bar(g) (14.5–43.5 psig) on dry-pipe systems, depending on the valve’s trip differential, and about 0.5–1 bar(g) (7.3–14.5 psig) on pre-action systems; the valve maker’s figures govern. After a trip or drain-down the network must be refilled within the time the applicable fire code or valve maker specifies, and supervisory pressure must never sag into the low-air alarm or trip zone.

Nitrogen, commonly at 98 % purity or higher and generated on site from compressed air, is increasingly used to limit internal corrosion and pinhole leaks. The compressor then becomes the feed-air source for the generator, which raises flow and quality requirements upstream. Moisture in sprinkler pipework collects at low points and corrodes it from inside.

Diesel generator plant support

Standby diesel sets on data-centre campuses are mostly battery-started; air-start appears only on some large engines. Where it is fitted, a receiver bank, typically charged to between 10 and 30 bar(g) (145.0–435.1 psig), must hold air for the number of start attempts the engine maker specifies, and its charging compressor must recover the bank in the specified time. The engine maker’s figures govern. Elsewhere in the yard, air serves maintenance: radiator blow-down in dusty months and tools during overhauls.

Workshop, maintenance and cleaning air

Workshop tools, tyre inflation and cleaning of filters and coils need service air. Separate it from critical control air with its own compressor or a priority valve that closes the service branch when header pressure falls. Blowing down inside the white space drives dust into equipment and is generally discouraged.

Cooling-tower, water-treatment and BMS interfaces

Water-treatment plants for cooling-tower make-up use pneumatic valves on softener and reverse-osmosis skids, air scour for filter backwash and air-operated dosing pumps. Loss of air rarely trips IT load directly, but on an evaporative system in a Hyderabad summer, stopped make-up treatment becomes a cooling problem within hours. The building management system consumes no air, but its transmitters and status contacts belong on the air register.

Duty-by-duty: pressure, flow, quality and consequence of loss

The table below is a starting point for a campus survey. Every figure is typical or indicative; replace each with the measured or specified value for your site.

DutyTypical supply pressureTypical flowIndicative ISO 8573-1 classCriticalityConsequence of loss
Pneumatic chilled-water valves and dampers5.5–7 bar(g) (79.8–101.5 psig) to regulator0.05–0.2 m³/min (1.8–7.1 cfm) per plant room[2:4:2]; [2:2:2] for cold or exposed runsHigh where valves govern cooling loopsValves go to fail position; cooling loops may isolate or lose control
Dry-pipe / pre-action air maintenanceTypically 1–3 bar(g) (14.5–43.5 psig) dry-pipe; 0.5–1 bar(g) (7.3–14.5 psig) pre-action supervision; valve maker governsTrickle in service; refill flow set by code or maker’s fill timeDew point well below the coldest pipe temperature; nitrogen where specifiedHigh (life-safety and IT protection)Low-air alarm; dry-pipe valve may trip and admit water to the network
Nitrogen generator feed airTypically 7–10 bar(g) (101.5–145.0 psig), per generator makerSeveral times the nitrogen output, per maker’s air factor[1:4:1] to [2:4:2] at generator inletHigh, as for the sprinkler systemNitrogen supply stops; fallback to air or loss of supervision
Generator air-start (where fitted)Typically 10–30 bar(g) (145.0–435.1 psig), per engine makerCharging compressor sized to recover the bank in the specified timeDry, oil-controlled air per engine makerVery high on the engines that use itEngine cannot start; loss of standby power capacity
Water-treatment valves, air scour, dosing pumps4–7 bar(g) (58.0–101.5 psig)0.1–1.5 m³/min (3.5–53.0 cfm), intermittent[3:4:3] or as skid maker requiresMedium, rising with evaporative cooling dependenceMake-up water treatment stops; cooling-tower chemistry drifts
Workshop, tools, tyres, cleaning6–7 bar(g) (87.0–101.5 psig)0.3–1.5 m³/min (10.6–53.0 cfm), intermittent[4:5:4] general serviceLowMaintenance delayed; no direct operational impact

Size the air plant to the duty, but engineer its availability to the consequence of losing the most critical device it feeds.

Criticality classification and the redundancy it justifies

Apply the tier discipline used for power and cooling, scaled to the real consequence: classify each duty, and let the highest class on a shared header decide that header’s design. See our criticality classification and service level page and the criticality and service-level worksheet.

ClassDefinitionTypical dutiesIndicative design response
A – criticalLoss affects cooling, fire protection or standby power within minutesChilled-water pneumatic valves, sprinkler air or nitrogen maintenance, air-start banksN+1 compressors as a minimum, 2N where concurrent maintainability is a stated design goal; duplex dryers and filters; receiver ride-through; essential-bus power and UPS-backed controls
B – importantLoss degrades operation within hoursWater-treatment skids, cooling-tower auxiliariesN+1 or a rapid rental connection point; alarmed; planned spares
C – convenienceLoss delays maintenance onlyWorkshop, tyres, cleaningSingle compressor acceptable; priority valve so it never robs class A air

N+1 versus 2N for air. N+1 means one compressor more than demand needs, on a shared header and treatment train. 2N means two independent trains, each carrying the whole critical load, on separate supplies and ideally separate fire compartments. Because class A air loads are small, two 100 % compressors, two dryers, duplex filtration and a ride-through receiver give 2N at compressor level at modest cost. Full 2N distribution is justified only where air feeds two separately protected halves of the facility. A second compressor is capacity; a demonstrated changeover is evidence. Our standby compressor readiness test describes how to prove it under load.

Power supply: dual feeds, generator back-up and UPS for controls

Air plant serving class A duties must be as resilient electrically as the plant it serves.

  • Essential-bus supply. Feed duty and standby compressors from different boards, both on the generator-backed essential bus. A compressor on the non-essential bus stops at the first grid outage.
  • Restart behaviour. Generator start and transfer typically takes about 10–30 seconds, mechanical loads are often reconnected in timed steps after that, and screw compressors then observe a controller restart delay before loading. Record all three for each machine, enable automatic restart deliberately, and make the receiver cover the whole gap.
  • UPS for controls. Put the sequencer, dryer controller, pressure transmitters and BMS gateway on a small UPS.
  • Dips and drives. Variable-speed drives can trip on undervoltage; set ride-through deliberately. See our electrical supply notes for supply-side checks.
  • Generator loading. Check starting current against generator step-load capability and stagger restarts after transfer.

Dryers, dew point and cold or outdoor pipe runs

Indian ambient does not freeze pipework, but liquid water still appears where lines run beside chilled-water mains, across roofs that cool after monsoon rain, and in sprinkler networks where condensate collects at low points over months.

A refrigerated dryer (+3 to +7 °C pressure dew point) suits indoor control air where pipe temperatures stay well above that. Pressure reduction lowers dew point: air dried to +5 °C at 7.0 bar(g) (101.5 psig) has an atmospheric-equivalent dew point of roughly −21 °C, and expanded to 2.0 bar(g) (29.0 psig) roughly −10 °C. None of that helps the 7 bar(g) (101.5 psig) header itself: a +3 to +7 °C pressure dew point leaves little or no margin where that header runs beside a 6–7 °C chilled-water pipe.

  • For class A air that runs outdoors, near chilled-water mains or into sprinkler networks, specify a desiccant dryer at −20 °C (ISO 8573-1 water class 3) or −40 °C (class 2) pressure dew point.
  • Duplicate the dryer so servicing never forces untreated air into the system. Our desiccant dryer guide covers purge loss and regeneration.
  • Air drawn in at 35 °C and 80 % relative humidity, dried to +5 °C pressure dew point at 7 bar(g) (101.5 psig), releases about 31 g of water per m³ of free air. At a modest 0.2 m³/min (7.1 cfm) that is close to 9 litres per day, all leaving through drains that must work.
  • Install a dew-point transmitter downstream of the dryer on class A trains and alarm it to the BMS.

Monitoring, alarms and the BMS interface

Critical air plant should report to the team that watches power and cooling, with a short, tested signal list.

  • Header pressure at the receiver outlet and at the most critical consumer, with a pre-alarm and a low alarm.
  • Run, load and fault status for each compressor, plus “standby not available” (isolated, faulted or in local mode).
  • Pressure dew point after each class A dryer, and dryer fault.
  • Sprinkler air-maintenance low pressure (usually on the fire panel; show the air plant in the cause chain).
  • Filter differential pressure and condensate drain alarm where the drains are electronic.
  • Plant-room temperature, because ambient is a leading indicator of compressor trips in May and June.

Use hard-wired volt-free contacts for the few alarms that must work when the network does not, and a serial or networked link for trends. See BMS and SCADA integration, alarms and trends and remote monitoring for the controls side, and keep the air plant inside the facility’s operational-technology security boundary.

Maintenance windows without losing air

Concurrent maintainability means every component can be serviced while the critical header stays above minimum pressure.

  • Isolation valves either side of each compressor, dryer and filter set, with a bypass or duplex arrangement for the treatment train.
  • Non-return valves on each compressor discharge so an isolated machine cannot drain the header.
  • A temporary-air connection point on the class A header for a hired compressor and dryer. Our notes on tie-in and changeover describe the sequence.
  • Method statements for each task: valve sequence, expected pressure dip and abort criteria, rehearsed before they are needed.
  • Receiver examination arranged so one vessel can be out of service while another carries the duty. Where the premises fall under factory law (the Factories Act and the applicable state factory rules, or the provisions that replace them under the Occupational Safety, Health and Working Conditions Code, 2020), vessels are examined and tested by a competent person at the intervals those rules, the design code and the insurer require; confirm your site’s position with your competent person. Our pressure vessels page covers the compressor’s internal separator vessel and the external receiver.

Documentation, testing and handover

Include the air plant in integrated systems testing. At handover and at a fixed frequency, demonstrate: loss of duty compressor with automatic standby start; loss of utility power with generator transfer and compressor restart; dryer changeover; header pressure at the critical consumer throughout each event; alarms arriving at the BMS with correct labels and timestamps. Record minimum pressure reached, time to recovery and any alarm that did not arrive.

Keep a single air-system file: the criticality register (below), single-line schematic, compressor and dryer data, receiver documents and examination records, alarm list with set points, and the results of the last test. See business-continuity and emergency air for recovery objectives.

Indian campus realities: heat, dust, monsoon and growth

Hyderabad and wider Telangana form a growing data-centre region, and its climate is far from the temperate conditions many design guides assume.

  • Summer heat. April to June routinely exceeds 40 °C outdoors; a poorly ventilated compressor room reaches 45–50 °C. Duct hot cooling air out, size inlets for the full cooling-air flow, and measure room temperature on the hottest afternoon.
  • Intake air temperature. Refrigerated dryers are typically rated at reference conditions such as 35 °C inlet air and 25–35 °C ambient; above those, capacity falls and dew point rises. Apply the maker’s correction factors.
  • Dust. Build-out construction and dry-season dust load intake filters and cooler fins; pre-filter room inlets.
  • Monsoon humidity. Drains, dryer capacity and dew-point alarms are tested hardest in July to September.
  • Phased growth. Size headers and receivers for final demand; add compressors as halls are fitted out. Our compressor room installation guide covers layout and ventilation.

Worked example (illustrative)

Situation (illustrative): one class A header feeds pneumatic chilled-water valves and a pre-action sprinkler air maintenance device. How large must the receiver be to hold the header above minimum pressure if the duty compressor trips and the standby fails to auto-start, until a technician starts it manually?

  1. Demand during the event. Pneumatic valves and positioners 0.12 m³/min (4.2 cfm); sprinkler air maintenance trickle 0.03 m³/min (1.1 cfm); leakage allowance 0.05 m³/min (1.8 cfm). Total net withdrawal = 0.12 + 0.03 + 0.05 = 0.20 m³/min (7.1 cfm).
  2. Ride-through time required. Operations sets 10 minutes for alarm, attendance and manual start. Free air required = 0.20 × 10 = 2.0 m³.
  3. Usable pressure band. The receiver normally sits at 7.0 bar(g) (101.5 psig). The lowest acceptable header pressure, set by the valve actuators and the sprinkler air-maintenance device, is 5.5 bar(g) (79.8 psig). Usable band = 7.0 − 5.5 = 1.5 bar.
  4. Receiver volume (isothermal estimate). V = free air × atmospheric pressure ÷ usable band = 2.0 × 1.013 ÷ 1.5 = 1.35 m³.
  5. Margin. Add 25 % for leakage growth, gauge error and temperature effects: 1.35 × 1.25 = 1.69 m³. Select the next standard size, 2.0 m³.
  6. Check. Usable free air in 2.0 m³ = 2.0 × 1.5 ÷ 1.013 = 2.96 m³. Ride-through at 0.20 m³/min = 2.96 ÷ 0.20 = 14.8 minutes. If the leakage allowance is exceeded and withdrawal doubles to 0.40 m³/min (14.1 cfm), ride-through halves to 7.4 minutes, below target. That is the reason leakage on class A headers must be measured and kept low.
  7. What storage cannot do. After a trip and drain-down, suppose the pre-action pipework of 2.5 m³ must be refilled to a supervisory pressure of 1.0 bar(g) (14.5 psig) within 30 minutes (use the pressure and fill time that actually apply to your system). Free air needed = 2.5 × 1.0 ÷ 1.013 = 2.47 m³, a refill flow of 2.47 ÷ 30 = 0.082 m³/min (2.9 cfm). Added to the 0.20 m³/min (7.1 cfm) base load, the compressor on duty must deliver at least 0.282 m³/min (10.0 cfm) during refill. A receiver buffers a changeover; it does not replace compressor capacity.

The estimate ignores expansion cooling and assumes steady withdrawal. Check figures with the receiver transient storage calculator and confirm by a timed test.

Data-centre air system criticality register

One register per consumer or group of identical consumers; review at every hall fit-out and systems test.

FieldEntry
Campus / building / plant room
Consumer and tag number
Function (what the air does)
Header or branch it is fed from
Minimum required supply pressure, bar g (psig)
Normal and peak flow, m³/min (cfm)
Required air quality, ISO 8573-1 class and pressure dew point
Coldest pipe temperature on the route, °C
Fail position or behaviour on loss of air
Consequence of loss and time to impact
Criticality class (A / B / C)
Redundancy provided (N, N+1, 2N) and receiver ride-through, minutes
Electrical supply for compressors; UPS for controls (yes / no)
Alarms to BMS and set points
Temporary-air connection available (yes / no, location)
Last changeover test date, minimum pressure reached, recovery time
Open actions and owner
Reviewed by / date

Exceptions and cautions

  • Fire-protection systems are governed by the applicable fire code, the authority having jurisdiction and the valve maker; this page does not replace them.
  • Generator air-start systems are part of the engine maker’s scope. Follow the maker’s start-air pressure, volume, quality and recharge requirements.
  • Liquid-cooled and direct-to-chip installations use pumped coolant, not compressed air. Do not let a vendor present compressed air as a cooling solution for IT load.
  • ISO 8573-1 classes on this page are indicative. Use the device maker’s stated requirement and verify by measurement.
  • Statutory duties for pressure vessels vary with the installation. Confirm the examination regime with your competent person or factory inspectorate.

Common mistakes

  1. Describing compressed air as part of server cooling in proposals or tenders.
  2. Feeding class A control air and class C workshop air from one header with no priority valve.
  3. Installing two compressors on the same electrical board and calling it redundancy.
  4. Using a refrigerated dryer for air that runs beside chilled-water mains or into sprinkler pipework.
  5. Putting the sequencer and dryer controls on raw supply, so every dip resets them.
  6. Never timing the receiver ride-through, so the first real test is an actual fault.
  7. Ventilating the compressor room for December conditions and seeing high-temperature trips in May.
  8. Leaving the air plant out of integrated systems testing and the BMS alarm list.

How Reddy Compressors helps

Reddy Compressors has been an independent multi-brand compressed-air specialist in Secunderabad since 2002. We are suppliers, not dealers, and not an authorised dealer of any make. We have tie-ups with all major and reputed brands. For critical-infrastructure air we offer:

  • Sales of new, used and refurbished compressors (Atlas Copco, Ingersoll Rand, ELGi, KAESER, Chicago Pneumatic and others), sized to the measured duty.
  • Refrigerated and desiccant dryers, filters, receivers and piping for duplex, bypassed treatment trains.
  • Service, AMC, overhaul and spare parts for all major makes, carried out by a team of more than 20 service engineers and technicians.
  • Rental compressors from our own fleet, 50–2,000 cfm (1.4–56.6 m³/min) at 2–30 bar, for planned shutdowns, temporary air during overhauls and breakdown cover.
  • Service across Telangana, Andhra Pradesh and districts within about 300 km of Hyderabad, with supply across India.

What to send us

  • A list of air consumers with their function, supply pressure and fail position, or your draft criticality register.
  • The current compressor, dryer and receiver details, with nameplate photographs.
  • A sketch of the header showing routes outdoors, on roofs or near chilled-water pipework.
  • Electrical supply arrangement for the compressors and controls.
  • Any pressure or dew-point trends, alarm logs or test results you have.
  • Planned hall fit-outs and timelines.

Use the equipment selection enquiry for new or upgraded plant, or the service and maintenance enquiry for existing equipment. Call/WhatsApp 99590 60718 or 92468 88812.

Frequently asked questions

Do data centres use compressed air to cool servers?

No. Server heat is removed by air-handling, chilled-water, direct-expansion, evaporative or liquid-cooling systems. Compressed air is a supporting utility for pneumatic valves, sprinkler air maintenance, generator plant support, workshops and water treatment.

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How big an air compressor does a data-centre campus need?

Usually small. Control-air and sprinkler maintenance loads are typically 0.05–0.5 m³/min (1.8–17.7 cfm) for a whole campus, excluding nitrogen generation and workshop air. The effort goes into redundancy, dryers, power and monitoring rather than capacity.

Should sprinkler pipework use compressed air or nitrogen?

Both are used. Nitrogen, commonly at 98 % purity or higher, generated on site from compressed air, limits internal corrosion. The choice belongs to the fire-protection designer and the applicable code. If nitrogen is used, the compressor becomes the feed-air source for the generator and must meet its flow and quality needs.

Is a refrigerated dryer enough for data-centre control air?

For indoor air in ventilated plant rooms, often yes, because it gives a pressure dew point of about +3 to +7 °C. Where lines run outdoors, on roofs, near chilled-water mains or into sprinkler networks, a desiccant dryer at around −20 °C to −40 °C pressure dew point is the safer choice.

What does N+1 mean for an air system?

It means one more compressor than the demand requires, sharing a common header and treatment. Because critical air loads are small, many sites install two compressors each able to carry the whole critical load, with two dryers and duplex filters, which gives full redundancy at compressor level.

How long should a receiver hold pressure if a compressor trips?

Long enough to cover a manual start if automatic standby start fails. Usable free air is receiver volume multiplied by the usable pressure band and divided by atmospheric pressure. Divide that by the net withdrawal to get minutes of ride-through, then confirm it with a timed test.

Should compressors be on generator back-up?

Compressors serving critical duties should be on the generator-backed essential bus, ideally duty and standby on different boards, with controls and sensors on a UPS. Check restart delays, starting current against generator step-load capability, and drive ride-through settings.

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.

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