Corpus sync: neutrality remakes, note hygiene, datasheet relocation, transformer-split cross-refs
1Scope
NOTEThis standard covers general-service compressed air systems for shop, laboratory, light-industrial, institutional, healthcare-support, and government facility applications. (1.1)
NOTEGeneral-service compressed air is the utility air that powers pneumatic tools, actuators, laboratory apparatus, blow-off and cleaning stations, and instrument loops throughout a facility. It is generated by one or more compressors, conditioned by a treatment train, accumulated in a receiver, and distributed through fixed piping to terminal outlets. This standard addresses the complete system as a coordinated assembly rather than as isolated pieces of equipment, because the air quality delivered at any outlet is the product of every upstream component working together. (1.2)
1.3The system shall be furnished complete from compressor intake through terminal outlets, including air treatment, receiver, distribution piping, condensate management, and controls.
NOTEA compressed air package specified only as a compressor leaves the air quality, storage, and distribution undefined, which is the most common source of underperforming installations. Treating the system as a whole is what lets the engineer hold a purity class at the point of use. (1.4)
NOTEThis standard applies to new construction and to expansions of existing compressed air systems. (1.5)
NOTEThis standard applies to systems operating at pressures up to 200 psig typical facility service. (1.6)
NOTEGeneral-service headers operate at 90 to 125 psig; specialty high-pressure headers may reach 200 psig. Pressures above 150 psig, or piping located in process-classified areas, shift the governing piping code from ASME B31.1 to ASME B31.3 and are addressed accordingly within this standard. (1.7)
NOTEMedical air and dental air piped to patient care areas under NFPA 99 Level 1 are excluded and are governed by Medical Gas SystemsMedical Gas and Vacuum SystemsResolves to the current edition.sync/medical-gas-systems. (1.8)
NOTELevel 1 medical air is a life-safety system with its own source equipment, alarms, certification, and dedicated piping. It must never share source equipment or distribution with general-service air. (1.9)
NOTEBreathing air for respiratory protection (OSHA 29 CFR 1910.134 Grade D) is excluded; it is a distinct safety classification with its own purity, monitoring, and alarm requirements. (1.10)
NOTEFuel gas, natural gas, propane, process piping above 200 psig, and air-driven specialty outlets are excluded and are covered by their respective standards. (1.11)
NOTESee Natural Gas PipingNatural Gas PipingResolves to the current edition.sync/natural-gas-piping, Fuel Gas PipingFacility Liquefied-Petroleum and Fuel Gas PipingResolves to the current edition.sync/fuel-gas-piping, and Plumbing SpecialtiesPlumbing SpecialtiesResolves to the current edition.sync/plumbing-specialties. Pneumatic HVAC controls tied into the building automation system are covered by HVAC Controls InstrumentationHVAC Instrumentation and Control DevicesResolves to the current edition.sync/hvac-controls-instrumentation. (1.12)
2Referenced Standards
2.1Equipment, materials, and installation shall comply with the latest adopted edition of each of the following unless a specific edition is cited.
2.2Where referenced standards conflict, the more stringent requirement shall govern unless the Engineer of Record directs otherwise in writing.
Standard
Title
ANSI/CAGI B19.1
Safety Standard for Air Compressor Systems
ASME B19.3
Safety Standard for Compressor Inlets
ASME BPVC Section VIII, Div. 1
Rules for Construction of Pressure Vessels
ASME B31.1
Power Piping
ASME B31.3
Process Piping
ISO 8573-1
Compressed Air, Part 1: Contaminants and Purity Classes
ISO 8573-2 through 8573-9
Compressed Air, Test Methods for Contaminant Measurement
NFPA 99
Health Care Facilities Code
NFPA 70
National Electrical Code (Article 430)
OSHA 29 CFR 1910.169
Air Receivers
OSHA 29 CFR 1910.134
Respiratory Protection, Grade D Breathing Air
UFC 3-420-02
Unified Facilities Criteria: Compressed Air
ASHRAE 15
Safety Standard for Refrigeration Systems
ASTM A53/A53M
Pipe, Steel, Black and Hot-Dipped, Zinc-Coated, Welded and Seamless
ASTM B88
Seamless Copper Water Tube
NOTEANSI/CAGI B19.1 governs compressor system safety (controls, guarding, relief sizing) while ASME BPVC Section VIII governs the pressure vessel; the two are complementary and both apply. (2.3)
NOTEISO 8573-1 is referenced for purity classification; the latest adopted edition applies, as the standard has been under revision. (2.4)
3Submittals
3.1The Contractor shall submit the following action submittals for review before fabrication or ordering:
Product data for each compressor, dryer, filter, separator, receiver, and condensate device, including capacity, power, and noise data
Receiver tank ASME data report and nameplate information showing MAWP and code stamp
Air purity calculation demonstrating the delivered ISO 8573-1 class at each point of use
Pipe sizing calculation demonstrating total distribution pressure drop within the specified limit
Electrical coordination data: motor full-load amperes, locked-rotor amperes, and starting method
Action submittals requiredcheckbox
☐ Product data (compressor, dryer, filter, separator, receiver)
☐ Shop drawings (room layout, clearances, piping)
☐ Receiver ASME data report and nameplate
☐ Air purity calculation per use point
☐ Pipe sizing / pressure-drop calculation
☐ Electrical coordination data (FLA, LRA, starting method)
3.2The Contractor shall submit the following closeout submittals before substantial completion:
Operation and maintenance manuals for all equipment
Manufacturer warranty documentation
Record drawings of installed piping and equipment
Test and certification reports, including receiver relief valve, leak test, and dew point verification
Startup and commissioning report
Closeout submittals requiredcheckbox
☐ Operation and maintenance manuals
☐ Warranty documentation
☐ Record drawings
☐ Test and certification reports
☐ Startup and commissioning report
3.3The Contractor shall submit the following informational submittals:
Manufacturer installation instructions for each major component
Welder qualifications and weld procedure specifications where applicable
Confirmation of local sewer authority condensate discharge limits
Informational submittals requiredcheckbox
☐ Manufacturer installation instructions
☐ Welder qualifications / weld procedures
☐ Sewer authority condensate discharge limits
4Quality Assurance
4.1The compressor manufacturer shall be regularly engaged in the production of facility compressed air equipment.
4.2The compressor manufacturer shall demonstrate a minimum of five years of production of the specified compressor type.
4.3Air receivers shall be constructed, inspected, and stamped in accordance with ASME BPVC Section VIII, Division 1.
NOTEOSHA 29 CFR 1910.169 makes ASME compliance a federal requirement for air receivers, and any receiver of 1.5 cubic feet or larger operating above 15 psig must carry the ASME code stamp. (4.4)
4.5Welding of steel distribution piping shall be performed by welders qualified under ASME Section IX to the applicable weld procedure specification.
4.6The compressor and accessories shall comply with ANSI/CAGI B19.1 for safety, guarding, and relief device sizing.
4.7Compressor inlets shall be guarded in accordance with ASME B19.3.
5Environmental and Service Conditions
5.1The compressor room ambient temperature shall not exceed 100°F (38°C) under any operating condition.
NOTERotary screw and reciprocating compressors derate and the discharge air carries more moisture as inlet and ambient temperature rise. Holding the room below 100°F preserves capacity and keeps the downstream dryer load within its rating. (5.2)
5.3Compressor room ventilation shall be provided at a minimum of 1 CFM of room ventilation per 1 CFM of compressor rated intake.
NOTEThis guidance follows UFC 3-420-02 and removes both the heat of compression rejected to the room and any heat from air-cooled aftercoolers. (5.4)
5.5The intended installation environment shall be identified so that dryer dew point and piping material are selected for the worst-case exposure.
Compressor and distribution environmentradio
● Indoor, conditioned compressor room; distribution in heated space
○ Indoor compressor room; distribution through unheated or intermittently heated space
○ Outdoor or freeze-exposed compressor and/or distribution
5.6Where any portion of the distribution passes through unheated, outdoor, or freeze-exposed space, a desiccant dryer delivering the specified pressure dew point shall be provided.
NOTEA refrigerated dryer holding a 35°F to 39°F pressure dew point is adequate only where every foot of pipe stays above freezing. Routing 35°F-dew-point air through an unheated space condenses and then freezes water in the line, blocking flow and damaging tools, which is one of the most common field failures. (5.7)
5.8Equipment and piping shall be anchored to resist seismic loads in accordance with the applicable building code where the project is located in a seismic design category that requires it.
Seismic anchorage requiredradio
○ Yes, per applicable building code seismic design category
● No, low seismic design category
6Compressor
6.1The compressor type shall be selected to match the facility duty cycle, required air quality, and maximum operating pressure.
NOTEFor general facility service (shops, maintenance, light laboratory) the lubricated rotary screw with a refrigerated dryer is the most common selection: it offers continuous-duty capability, good efficiency, and the lowest installed cost for its capacity. Oil-free machines carry a significant cost premium and are justified only where the application genuinely cannot tolerate any oil carryover. Reciprocating machines remain economical for intermittent-duty shops at lower first cost. (6.2)
6.3The compressor type and lubrication class shall be as scheduled.
Compressor typeselect
Lubricated rotary screw
Oil-free rotary screw
Lubricated reciprocating
Oil-free reciprocating
Scroll (oil-free)
Centrifugal
6.4Where an oil-free air purity class is required at any point of use, an oil-free compressor shall be provided.
NOTEFiltered oil-lubricated machines cannot reliably reach ISO 8573-1 Class 1 oil because oil aerosol and vapor pass through coalescing filters as their efficiency degrades. Specifying a Class 1 oil requirement while scheduling a lubricated machine generates substitution requests and field disputes. The purity requirement and the compressor selection must agree. (6.5)
6.6The compressor arrangement shall provide the redundancy and turndown the facility requires.
Compressor arrangementselect
Single compressor
Duplex (lead-lag), shared receiver and dryer
Multiple compressors with sequencing controls
6.7Where continuous facility operation depends on compressed air, a duplex (lead-lag) arrangement shall be provided so that either unit alone can carry the facility base load.
NOTELead-lag control alternates the duty unit to equalize wear and brings the lag unit on for peak demand or as standby. A single compressor leaves the facility without air during any failure or routine service of that one machine. (6.8)
6.9The compressor staging shall be selected for the required discharge pressure.
Compressor stagingradio
● Single-stage
○ Two-stage
6.10Two-stage compression shall be provided where discharge pressure exceeds approximately 125 psig or where the efficiency at sustained high pressure justifies it.
NOTESingle-stage machines are efficient and adequate for general 100 to 125 psig service. Two-stage compression with intercooling is more efficient and reaches higher pressures, which suits high-pressure headers and continuous high-load duty. (6.11)
6.12The compressor control mode shall match the facility load profile.
Compressor control modeselect
Start-stop
Load-unload
Modulation
Variable-speed drive (VSD)
6.13Variable-speed drive control should be provided where facility demand varies widely through the day, to reduce energy consumed at part load.
NOTEA VSD compressor matches motor speed to demand and avoids the unloaded-running and blow-down losses of fixed-speed control. The energy saving is largest where average demand is well below installed capacity; at near-constant full load a fixed-speed load-unload machine is competitive and simpler. (6.14)
6.15Rated capacity and discharge pressure shall be as scheduled.
Compressor rated capacity (per unit)range
SCFM
101000
Per drawings
Compressor rated discharge pressurerange
psig
90100110125150175200
6.16The compressor drive motor shall be sized and wired in accordance with NEC Article 430.
Compressor motor voltageselect
208 V, 3Φ
230 V, 3Φ
460 V, 3Φ
NOTEBranch circuit conductors for a continuous-duty motor are sized at not less than 125% of full-load current, and direct-on-line starting draws six to eight times full-load current, which governs disconnect and overcurrent selection. The motor full-load and locked-rotor amperes must be confirmed with the electrical engineer. (6.17)
7Receiver
7.1An air receiver shall be provided to store compressed air, dampen pressure pulsation, and allow condensate to drop out before distribution.
NOTEThe receiver decouples short-duration demand peaks (tool starts, actuator strokes) from compressor output, so the compressor cycles on average demand rather than chasing every transient. It also provides residence time for water and oil to separate from the air and settle to the drain. (7.2)
7.3Receiver capacity shall be sized for the facility demand profile and compressor output.
Receiver tank capacityrange
gal
602000
Per drawings
7.4The receiver shall provide a minimum of 10 minutes of storage at average system demand.
NOTEA common first-pass rule for variable-demand systems is roughly 1 gallon of receiver volume per SCFM of compressor output; the larger of the two checks governs. This follows the UFC 3-420-02 guideline. (7.5)
7.6The receiver shall be a pressure vessel constructed and stamped in accordance with ASME BPVC Section VIII, Division 1, with the MAWP shown on the nameplate.
7.7A pressure-relief device shall be installed on the receiver, set so that receiver pressure cannot exceed the MAWP by more than 10% under any condition.
NOTEOSHA 29 CFR 1910.169 requires this as a federal mandate. The relief capacity must exceed the compressor's full delivery so the receiver cannot be over-pressured even with the inlet valve fully open. (7.8)
7.9A pressure gauge shall be installed on the receiver.
7.10The pressure gauge shall be readable from the operating position.
7.11A manual drain valve shall be installed at the lowest point of the receiver.
NOTEOSHA 29 CFR 1910.169 requires a drain at the lowest point so accumulated condensate can be removed. An automatic drain may supplement the manual drain but does not replace it for inspection and service purposes. (7.12)
8Air Treatment
8.1An air treatment train shall be provided to deliver the required purity class at each point of use, addressing particulates, moisture, and oil.
NOTEISO 8573-1 classifies air independently for solid particles, water (dew point), and oil. A complete train typically comprises an aftercooler and moisture separator at the compressor discharge, a dryer sized for the required dew point, and point-of-use coalescing and particulate filtration. Each contaminant is addressed by the component suited to it; one device does not cover all three. (8.2)
8.3The required air purity class shall be specified at each point of use per ISO 8573-1.
Required ISO 8573-1 purity class (particles.water.oil)select
3.4.3 (general shop / maintenance)
2.2.2 (general laboratory)
2.2.1 (instrument air)
1.2.1 (food-contact / critical)
NOTETypical class assignments by application: general shop and maintenance air at Class 3.4.3 (particles.water.oil); instrument air at Class 2.2.1; general laboratory air at Class 2.2.2; food-contact air at Class 1.2.1 or better. The class drives the dryer dew point and the filtration grades and must be set before the train is selected. (8.4)
8.5An aftercooler shall be provided downstream of the compressor to reduce discharge air temperature and condense the bulk of the moisture before it enters the dryer.
Aftercooler typeradio
● Air-cooled
○ Water-cooled
NOTERemoving the heat of compression here drops out most of the water as liquid, which the moisture separator captures, so the dryer receives a far smaller moisture load. (8.6)
8.7A moisture separator with automatic drain shall be installed downstream of the aftercooler to remove condensed liquid before the dryer.
8.8A dryer shall be provided to deliver the pressure dew point required by the application and the distribution environment.
Dryer typeselect
Refrigerated
Desiccant (regenerative)
Combination (refrigerated + desiccant polish)
Required outlet pressure dew pointselect
35°F to 39°F (refrigerated, indoor heated distribution)
−40°F (desiccant, instrument / freeze-exposed)
−100°F (desiccant, extreme dry)
8.9A refrigerated dryer shall deliver a pressure dew point of 35°F to 39°F (2°C to 4°C) at operating pressure.
NOTEThis dew point is adequate for general-service air distributed entirely within heated indoor space and is the usual choice for shop and maintenance systems. It is not adequate where any piping is exposed to freezing temperatures. (8.10)
8.11A desiccant dryer shall be provided where the application requires a pressure dew point of −40°F (−40°C) or lower, such as instrument air or any freeze-exposed distribution.
8.12Refrigerant-circuit refrigerated dryers shall comply with ASHRAE 15.
NOTEDesiccant dryers reach −40°F pressure dew point routinely and −100°F for extreme cases. (8.13)
8.14Point-of-use coalescing and particulate filtration shall be provided to achieve the specified oil and particle classes at the use point.
Point-of-use filtration gradeselect
General-purpose particulate (5 µm)
Coalescing (1 µm, oil aerosol)
High-efficiency coalescing (0.01 µm)
Coalescing + activated carbon (oil vapor)
NOTECoalescing filters remove oil aerosol and fine particulate; a particulate after-filter protects against desiccant fines where a desiccant dryer is used. Filtration grade is selected to meet the ISO class, not over-specified, because each filter stage adds pressure drop. (8.15)
9Distribution Piping
9.1Distribution piping shall comply with ASME B31.1 for systems at or below 150 psig in non-process buildings, and with ASME B31.3 where system pressure exceeds 150 psig or where piping is in a process-classified area.
9.2The piping material shall be selected for the service pressure, air quality, and corrosion environment.
Distribution piping materialselect
Carbon steel, Schedule 40 (ASTM A53 black)
Carbon steel, Schedule 80 (ASTM A53 black)
Copper, Type L (ASTM B88)
Aluminum, modular push-fit
Stainless steel
9.3Internally galvanized steel pipe shall not be used for compressed air distribution.
NOTEAt compressed air velocities the internal zinc coating flakes off and the particles travel downstream to clog filters, regulators, and tool valves. Black steel (Schedule 40 or 80 per ASTM A53), Type L copper, or modular aluminum are the appropriate choices. (9.4)
9.5Modular aluminum push-fit piping should be considered where leak reduction and reconfigurability are priorities.
NOTEAluminum modular systems install quickly, have a smooth bore that minimizes pressure drop, and their sealed joints leak far less than threaded steel, which directly reduces the compressor energy wasted feeding a leaky distribution network. (9.6)
9.7Distribution piping shall be sized so that total pressure drop from the receiver to the worst-case outlet does not exceed the specified limit at full design flow.
Maximum total distribution pressure dropselect
2 psig (general service)
1 psig (instrument air header)
9.8Pressure at the worst-case outlet shall be verified to remain at or above 90 psig under full design load.
NOTESizing on average flow alone undersizes the header so that end-of-line tools starve at peak demand. The sizing calculation must check the farthest, highest-demand outlet under simultaneous full load, not just the steady-state condition. (9.9)
9.10A high-pressure header with pressure-reducing stations shall be provided where specialty equipment requires pressure above the general-service level.
System pressure architectureradio
● Single-pressure header (general service)
○ General-service header plus dedicated high-pressure header
NOTEWhere part of the facility needs 150 to 200 psig and the rest needs 100 psig, a dedicated high-pressure header fed by a booster, with regulators dropping to general service at the use points, is more efficient than running the whole facility at the higher pressure. (9.11)
9.12Distribution mains should be looped and sized with reserve capacity for future expansion.
NOTEA looped main feeds each branch from two directions, halving the effective length and pressure drop, and reserve capacity built in at construction is far cheaper than retrofitting a larger header later. Calling out a design reserve at the outset is a low-cost hedge against facility growth. (9.13)
9.14Instrument-quality air shall be distributed in a header separate from general shop air where instrument accuracy or actuator reliability depends on air quality.
NOTEShop air carries more particulate, moisture, and oil than instrument loops tolerate. Tapping instruments off a shop header contaminates regulators and positioners and degrades control accuracy, so the two services are kept on separate, independently treated headers. (9.15)
9.16Each branch takeoff and terminal outlet shall be located as shown.
Terminal outlet typeselect
Quick-connect coupler
Filter-regulator-lubricator (FRL) drop
Filter-regulator (no lubricator) drop
Hose reel station
9.17Outlet and branch routing, drop locations, and header extents shall be as shown on the drawings.
NOTESee compressed air distribution plan. (9.18)
10Condensate Management
10.1Condensate shall be removed automatically from the receiver, dryer, filters, and drip legs, and managed to comply with the discharge requirements.
NOTECompressed air condensate accumulates at every cool point in the system. Left in place it carries downstream as slugs of water and, in lubricated systems, oil. The drain method is selected to remove condensate reliably without wasting compressed air. (10.2)
10.3The condensate drain method shall be selected for reliability and air economy.
Condensate drain typeselect
Manual drain valve
Automatic timed solenoid drain
Zero-loss demand (electronic level) drain
10.4Zero-loss demand drains should be specified to avoid the continuous compressed air loss of timed drains.
NOTEA timed solenoid drain opens on a schedule whether or not condensate is present, venting compressed air each cycle. A demand drain opens only when a sensed liquid level requires it, eliminating that loss; the energy saving usually repays the higher device cost. (10.5)
10.6An oil-water separator shall be provided to treat condensate from all lubricated compressors before discharge to the sanitary drain.
NOTEOily condensate discharged to a sanitary drain violates environmental regulations. The separator must reduce oil content below the local sewer authority limit, which is commonly below 15 mg/L; the actual limit must be confirmed with the authority having jurisdiction. (10.7)
10.8Condensate from lubricated compressors shall not be discharged to the sanitary drain without passing through an oil-water separator that meets the local sewer authority oil-content limit.
11Cross-Connection Prohibition
11.1The general-service compressed air system shall not be cross-connected to any medical air, oxygen, vacuum, or other piped gas system.
NOTEGeneral-service air is not certified to medical purity and is not monitored or alarmed to NFPA 99 Level 1 requirements. Any physical connection between this system and a medical gas, oxygen, or other piped gas system is prohibited; the prohibition must be stated explicitly on any project touching a healthcare facility so it survives field coordination. See Medical Gas SystemsMedical Gas and Vacuum SystemsResolves to the current edition.sync/medical-gas-systems. (11.2)
11.3No connection shall be made between the general-service compressed air system and any medical air, oxygen, or other piped gas system.
12Noise and Vibration Control
12.1The compressor shall be isolated to limit structure-borne noise and vibration transmitted to adjacent occupied spaces.
Compressor vibration isolationradio
● Spring isolators (over 10 hp)
○ Neoprene pads (10 hp and under)
NOTEUntreated compressors are a chronic source of complaints in occupied buildings because vibration travels through the slab and piping into walls and ceilings. Isolation at the machine and at every pipe connection interrupts that path. (12.2)
12.3Spring vibration isolators shall be provided under each compressor rated above 10 hp.
12.4Flexible pipe connectors not less than 18 in. long shall be installed at all compressor air connections.
NOTEThe flexible connector decouples the rigid distribution piping from the vibrating compressor so that pulsation and vibration are not transmitted into the building piping. (12.5)
13Testing
13.1The distribution piping shall be pressure-tested after installation and before concealment or insulation.
NOTETesting before the piping is buried, insulated, or enclosed allows leaks to be found and corrected while joints are still accessible. (13.2)
13.3Steel distribution piping shall be hydrostatically tested at 1.5 times MAWP in accordance with ASME B31.1, or pneumatically leak-tested at 110% of operating pressure with soap-bubble inspection of all joints where a pneumatic test is approved.
Piping test methodradio
○ Hydrostatic at 1.5× MAWP (ASME B31.1)
● Pneumatic at 110% operating pressure, soap-bubble inspection
13.4The receiver pressure-relief device shall be tested and certified to relieve at its set pressure before the system is placed in service.
13.5The delivered air dew point shall be verified at the dryer outlet to confirm it meets the specified pressure dew point.
NOTEDew point is the single most common air-quality shortfall and is easily measured at startup with an inline hygrometer; verifying it confirms the dryer is performing to specification. (13.6)
13.7The delivered air purity shall be verified against the specified ISO 8573-1 class using the test methods of ISO 8573-2 through 8573-9 where the application requires documented purity.
14Installation
14.1Equipment shall be installed level, anchored, and with the manufacturer's required service clearances.
NOTEAdequate clearance around compressors, dryers, and filters is required for filter changes, oil service, and coil cleaning; crowding the equipment guarantees deferred maintenance. (14.2)
14.3Distribution piping shall be installed with a uniform slope toward drip legs so that condensate drains to a collection point and does not pool in the line.
NOTEMains are pitched in the direction of flow and branch takeoffs are taken from the top of the main, so condensate runs to drip legs rather than being carried into the branch. (14.4)
14.5Branch connections shall be taken from the top of the distribution main.
14.6Drip legs with drain valves shall be installed at the low points of the distribution system and at the base of risers.
14.7Pipe supports shall be spaced in accordance with the applicable piping code for the pipe material and size.
14.8Each piece of equipment and each isolation valve shall be labeled to identify its service and the equipment it serves.
15Delivery, Storage, and Handling
15.1Equipment and piping shall be delivered in the manufacturer's packaging and protected from weather, dust, and physical damage until installation.
15.2Pipe ends and equipment connections capped at the factory must stay capped until connected, because debris that enters open piping migrates to filters and valves during startup.
15.3Pipe and fitting openings shall remain capped or plugged until the piping is connected.
15.4Compressors and receivers shall be stored upright.
15.5Compressors and receivers shall not be subjected to loads or impacts that could damage the pressure vessel or rotating assembly.
16Warranty
16.1The compressor and air treatment equipment shall be warranted against defects in materials and workmanship for the period specified.
Equipment warranty periodselect
1
2
5
16.2Extended airend or compression-element warranties offered by the manufacturer should be obtained where available.
NOTEThe compression element (airend on a rotary screw, pump on a reciprocating machine) is the highest-value component and many manufacturers offer extended coverage on it; capturing that coverage at purchase protects the largest replacement cost. (16.3)
17Spare Parts
17.1A complete set of consumable spare parts shall be furnished for first-year maintenance.
NOTECompressors and dryers consume filters, separators, and lubricant on a regular schedule. Delivering a first-year set with the equipment prevents the system from running on degraded consumables while replacements are procured. (17.2)
17.3The following spare parts shall be furnished with the equipment:
One complete set of intake and oil filters per compressor
One complete set of coalescing and particulate filter elements
One oil-water separator cartridge where applicable
One set of compressor lubricant for the first oil change