Butterfly Valve

A butterfly valve is a quarter-turn rotary valve that controls flow with a circular disc mounted on a shaft across the bore. Rotating the disc 90 degrees moves it from fully closed (disc perpendicular to flow) to fully open (disc edge-on, parallel to flow). Its compact wafer-thin body, low weight, and fast actuation make it the default isolation and throttling valve for large-diameter water, HVAC, chemical, and process lines where a gate or ball valve would be too heavy or too expensive.

Butterfly valves span an enormous range, from a 50 mm (2 inch) HVAC chilled-water valve to a 6,000 mm (240 inch) hydroelectric penstock valve. The two governing standards are API 609 for petrochemical and general industry, which splits the family into Category A (concentric, resilient seated) and Category B (offset, high performance), and AWWA C504 for municipal water service.

Wafer-style resilient-seated butterfly valve with a stainless steel disc on its central stem, white elastomer seat liner, and a black lever handle with locking trigger

Photo: Muhamad ramadani, CC BY-SA 4.0, via Wikimedia Commons

This guide is aimed at industrial purchasing engineers and design engineers. It covers 6 chapters from what a butterfly valve is, its concentric and offset types, body styles, seat and disc materials, key spec parameters, to selection decisions, with 7 selection FAQs and manufacturer comparisons. All parameters reference public standards including API 609, MSS SP-67, EN 593, ISO 5752, AWWA C504, ASME B16.34, ANSI/FCI 70-2, and IEC 60534-4.

Chapter 1 / 06

What is a Butterfly Valve

A butterfly valve is a quarter-turn rotary isolation and control valve. A circular disc, roughly the diameter of the pipe bore, is fixed to a shaft (stem) that runs across the flow path. A 90-degree rotation of the stem swings the disc from a fully closed position, where it is perpendicular to the flow and pressed against a circumferential seat, to a fully open position, where it lies edge-on and parallel to the flow with the medium passing on both sides. The name comes from the way the disc resembles the wings of a butterfly pivoting on the central stem.

Functionally, the butterfly valve belongs to the same family as the ball, plug, gate, and globe valve, but it is distinguished by its extreme compactness. Because the disc rotates within the line rather than rising out of it like a gate, or filling a large cavity like a ball, the body is short in the flow direction (a wafer body can be only a few tens of millimeters thick on small sizes) and light. For large diameters above DN300, a butterfly valve can weigh a fraction of an equivalent gate valve and cost far less, which is why it dominates municipal water mains, building HVAC, fire protection, and large process headers.

Structurally, every butterfly valve has four core elements: (1) the body, which sits in the line and carries the seat; (2) the disc, the flow-control element that the stem rotates; (3) the stem or shaft, which transmits torque from the handle or actuator to the disc and is supported by bearings; (4) the seat, the sealing surface against which the disc closes, made of a resilient elastomer in concentric valves or of hardened metal in high-performance offset valves. A packing or stem seal prevents leakage to atmosphere along the shaft.

The modern resilient-seated butterfly valve was commercialized in the mid-twentieth century, and the design matured through standardization. API 609, MSS SP-67, EN 593, ISO 5752, and AWWA C504 collectively define dimensions, pressure and temperature ratings, materials, and testing. Face-to-face (laying length) dimensions are deliberately harmonized across MSS SP-67, ISO 5752, and ASME B16.10 so that valves from different manufacturers are interchangeable in a given pipe spool.

Two operating limits separate butterfly valves from gate and ball valves. First, the disc always remains in the flow path, even when fully open, so it imposes a small permanent pressure drop and is not suitable for pipelines that must be pigged. Second, soft-seated concentric valves rely on the disc rubbing the elastomer seat through the full stroke, which wears the seat over many cycles and bounds the pressure and temperature envelope. The offset (eccentric) geometries described in Chapter 2 were developed specifically to remove that rubbing and extend the valve into severe service.

In terms of application scale, butterfly valves cover almost the entire range of industrial fluid handling. The smallest are DN50 (NPS 2) lever-operated HVAC and process valves; AWWA C504 governs municipal water valves from DN75 (NPS 3) to DN1800 (NPS 72); and the largest gear or hydraulically actuated valves on hydroelectric penstocks and cooling-water intakes reach several meters in diameter. Pressure spans from light vacuum and low-head water service up to ASME Class 900 on triple-offset valves, and temperature spans from cryogenic LNG to superheated steam. No single butterfly valve covers this whole envelope: the engineering task is to map the duty (media, pressure, temperature, cycle count, shutoff requirement) onto the right offset geometry, body style, and materials.

Chapter 2 / 06

Concentric and Offset Types

The single most important classification of a butterfly valve is the position of the stem relative to the disc and the bore, known as the offset or eccentricity. This geometry determines how the disc meets the seat, how much the seat wears, and therefore the pressure, temperature, and shutoff class the valve can reach. API 609 collapses these into two categories: Category A (concentric, resilient seated) and Category B (double or triple offset, high performance). The table below compares the four offset configurations.

TypeOffsetsSeatTypical Pressure ClassTypical Shutoff
Concentric (zero offset)0Resilient elastomerClass 150 to 300Bubble-tight
Single offset1Resilient / metalClass 150Bubble-tight
Double offset (high performance)2Soft or metal (eccentric)Class 150 to 600Class IV to VI
Triple offset3Metal (laminated, conical)Class 150 to 900Class IV to VI, fire-safe

Concentric (zero-offset) valves place the stem on the centerline of both the disc and the pipe bore. The disc is symmetric and rubs continuously against a resilient rubber or polymer seat through the entire 90-degree stroke. This rubbing gives excellent bubble-tight shutoff on clean fluids at low cost, which is why concentric valves cover the vast majority of water, air, HVAC, and low-pressure service. The trade-off is seat wear on every cycle and a service envelope bounded by the elastomer: roughly ASME Class 150 to 300 and the temperature limit of EPDM, NBR, FKM, or PTFE.

Double-offset (high-performance) valves move the stem behind the disc plane (first offset) and to one side of the bore centerline (second offset). This cam action lifts the disc edge off the seat almost immediately after it leaves the closed position, so the disc only contacts the seat in the last few degrees of travel. The result is far less seat wear, higher cycle life, and ratings up to Class 600. High-performance valves use a hardened or PTFE-lined seat and are widely used in chemical, hydrocarbon, and power isolation duty where a concentric valve would wear out.

Triple-offset valves add a third eccentricity: the axis of the conical sealing surface is tilted off the pipe axis. The disc and seat are now matching cones rather than cylinders, so the disc rotates into the seat like a cone seating in a cone, with zero rubbing until the final moment of closure. This frictionless, torque-seated, metal-to-metal design gives true zero-leak shutoff (commonly Class IV standard, Class V or VI optional per ANSI/FCI 70-2), fire-safe certification, and a temperature span from cryogenic (around minus 196 degrees Celsius) to roughly 425 degrees Celsius or higher, at ASME Class 150 to 900. Triple-offset valves replace gate and globe valves in severe refinery, LNG, steam, and toxic-media isolation.

A useful rule: choose concentric for clean, low-pressure, ambient-temperature fluids where first cost dominates; choose double offset when cycle life, moderate pressure, or chemical compatibility matters; choose triple offset when you need metal-to-metal zero leakage, fire-safe certification, high temperature, or steam. The price climbs steeply across the three, so do not over-specify offset geometry for a benign water line.

Chapter 3 / 06

Body Styles and End Connections

Independent of offset geometry, the body style determines how the valve attaches to the pipe and whether it can support end-of-line or dead-end service. The four common styles are wafer, lug, double-flanged, and butt-weld. Choosing the wrong style is a frequent and dangerous error, because a wafer valve installed at a dead end can blow out when the downstream flange is removed. The table below summarizes the four styles.

Body StyleAttachmentDead-End ServiceTypical Use
WaferThrough-bolts clamp body between flangesNoInline isolation, lowest cost
LugThreaded lugs, each flange bolts to bodyYes (derated)End-of-line, removable spool
Double-flangedIntegral flanges both endsYesLarge diameter, higher pressure
Butt-weldWelded directly to pipeYesHigh-integrity, fugitive-emission service

Wafer body valves have no bolt holes through the body. The valve is sandwiched between two pipe flanges and held in place by long through-bolts that pass around the outside of the body, with the flange faces and gaskets sealing the joint. Wafer valves are the lightest and cheapest style and dominate inline isolation, but because they are merely clamped, they cannot retain pressure if one flange is removed. They must never be used at a pipe end or where downstream piping could be dismantled under pressure.

Lug body valves have threaded bolt holes (lugs) cast into the periphery of the body. Each pipe flange bolts independently into the body with its own set of bolts, so either side of the line can be disconnected while the other side stays pressurized. This makes lug valves suitable for end-of-line and dead-end isolation, and for removing a downstream spool for maintenance. Note that the dead-end pressure rating of a lug valve is usually derated, commonly to around half the inline rating, unless the manufacturer specifically certifies full dead-end duty, so always confirm the dead-end figure on the datasheet.

Double-flanged body valves have integral flanges cast on both ends, like a conventional gate or globe valve. They are the standard for large-diameter water mains and for higher-pressure service where a wafer or lug body would be impractical, because the integral flanges give the strongest, most rigid joint and full end-load capacity. AWWA C504 short-body and long-body flanged valves fall into this category for municipal water service. Butt-weld ends are welded directly into the line, eliminating flange leak paths entirely, and are preferred for high-integrity hydrocarbon and fugitive-emission service.

Face-to-face (laying length) dimensions are standardized so that a valve of a given size and body style can be replaced by another manufacturer's valve without re-spooling the pipe. API 609 references MSS SP-67, ISO 5752, and ASME B16.10 for these dimensions. When replacing an existing valve, always match the standard and series called out on the original, because short-body and long-body variants of the same nominal size have different laying lengths and are not interchangeable.

Chapter 4 / 06

Seat, Disc and Stem Materials

Three material decisions dominate butterfly valve reliability: the seat material (which sets the chemical and temperature envelope and the shutoff class), the disc material (which contacts the media and faces erosion and corrosion), and the stem material (which carries the actuation torque). For resilient-seated valves the seat is the limiting component; for metal-seated offset valves the disc and seat metallurgy together set the limit.

Soft (resilient) seats are elastomers or polymers selected to the media. The table below lists the common seat materials with their approximate continuous temperature limits and media fit. Treat these as starting points only: always verify the manufacturer's chemical compatibility chart for the exact concentration, temperature, and dwell time, because elastomer ratings vary with grade and filler.

Seat MaterialApprox. Temperature RangeGood ForAvoid
EPDM-40 to +120 CWater, steam, dilute acids/basesOils, hydrocarbons, fuels
NBR (Buna-N)-20 to +80 COils, fuels, greases, airStrong oxidizers, ketones
FKM (Viton)-20 to +200 CHydrocarbons, aggressive chemistryHot water/steam, amines
PTFE / RPTFE-50 to +200 CNear-universal chemical serviceLow torque budgets (hard seat)
Metal (laminated SS + graphite)-196 to +425+ CSteam, fire-safe, severe serviceBubble-tight on dirty soft media

EPDM is the default for clean and reclaimed water, HVAC, and dilute chemistry, serving continuously to roughly 120 to 130 degrees Celsius, but it is rapidly attacked by oils and hydrocarbons and must never be used in fuel or lube service. NBR (Buna-N) is the opposite: excellent in oils, fuels, and greases but poor in strong oxidizers, with a narrower upper temperature limit around 80 degrees Celsius. FKM (Viton) extends chemical and temperature reach to about 200 degrees Celsius for hydrocarbons and aggressive media, while PTFE offers nearly universal chemical compatibility but is hard, so it demands a higher seating torque and usually a backing seat.

Metal seats on triple-offset valves are typically a laminated stack of stainless steel and flexible graphite, which gives both a fire-safe seal and resilience to thermal cycling. They reach roughly minus 196 degrees Celsius for cryogenic LNG up to 425 degrees Celsius and beyond for steam and hot oil, far past any elastomer, and they survive media that would shred a soft seat. The cost is higher operating torque and the need for the precise cam geometry of the offset design.

Disc materials are matched to the media in the same way the wetted parts of any process instrument are: ductile iron or carbon steel for water and benign service, 316 stainless or duplex 2205 for chlorides and seawater, and nickel alloys such as Hastelloy or Monel for aggressive acids. For abrasive slurry, hardfaced or ceramic-coated disc edges resist erosion at the high-velocity throttling band. Stems are normally stainless steel (such as 17-4PH or 410) sized so that the torsional and shear stress at maximum differential pressure stays within limits, since a sheared stem is a loss-of-control failure.

Chapter 5 / 06

Key Specification Parameters

Reading a butterfly valve datasheet means decoding a handful of parameters that drive selection. The same valve may list dozens of dimensions, but the eight below determine whether it fits: nominal size, pressure class, temperature rating, shutoff (leakage) class, flow coefficient Cv or Kv, operating torque, body and face-to-face standard, and certifications. Each is explained below.

Nominal size (DN / NPS) is the bore diameter, from DN50 (NPS 2) up to DN6000 (NPS 240) for the largest penstock valves. AWWA C504 covers 3 inch (75 mm) through 72 inch (1,800 mm). Size sets the flow capacity, the weight, and the torque, and must match the line, not the flow rate alone.

Pressure class is expressed as an ASME class (150, 300, 600, 900), a PN rating (PN10, PN16, PN25, PN40), or an AWWA class (25, 75, 150, 250 psi). Concentric resilient valves typically reach Class 150 to 300; double-offset reach Class 600; triple-offset reach Class 900. Note that the rated pressure derates with temperature per the body material's pressure-temperature curve, so a Class 300 body does not hold 300-class pressure at high temperature.

Temperature rating is bounded by the seat for soft-seated valves (see Chapter 4) and by the body and seat metallurgy for metal-seated valves. AWWA C504 water valves are rated for 33 to 125 degrees Fahrenheit (about 1 to 52 degrees Celsius) and pH 6 to 12; triple-offset valves run from cryogenic to roughly 425 degrees Celsius and above.

Shutoff (leakage) class follows ANSI/FCI 70-2 and IEC 60534-4. The common classes are:

  • Class IV: leakage up to 0.01 percent of rated capacity; the standard for many metal-seated valves.
  • Class V: leakage about 0.0005 percent of rated capacity; an option on high-performance and triple-offset valves.
  • Class VI: a bubble-count test for soft seats permitting only milliliters per minute, effectively zero leakage; standard for resilient elastomer seats and an option on premium metal seats.

Flow coefficient (Cv or Kv) quantifies flow capacity at a given pressure drop and disc angle. A butterfly valve's Cv rises steeply between roughly 30 and 70 degrees open, so the published Cv curve, not just the wide-open figure, governs throttling selection. Operating torque is the sum of seating, friction, and hydrodynamic (dynamic) torque; dynamic torque peaks near 70 to 80 degrees open, which is the worst case for actuator sizing, and the valve must be sized against the maximum differential pressure the disc will see.

Finally, the body and face-to-face standard (API 609 Category A or B, MSS SP-67, EN 593, ISO 5752, AWWA C504) and the certifications (fire-safe API 607 or API 6FA, fugitive emission ISO 15848, functional safety SIL per IEC 61508, plus regional approvals) must all be stated explicitly on the test certificate. A catalog claim is not a certificate; for critical service, demand the witnessed test report.

A practical note on the AWWA water-utility family: C504 valves are graded by both a pressure class and a velocity letter. The class number (25, 75, 150, or 250 psi) is the rated differential pressure, while the letter A or B denotes the maximum line velocity, where A valves are rated to 8 ft/s (2.4 m/s) and B valves to 16 ft/s (4.9 m/s) in the pipe section upstream of the valve. A C504 valve is therefore specified as, for example, Class 150B, and is intended for fresh and reclaimed water at pH 6 to 12 and 33 to 125 degrees Fahrenheit. Selecting the wrong velocity letter underrates the dynamic torque and can stall the actuator at high flow, so the velocity grade must be checked against the actual pipe velocity, not just the static pressure.

The same discipline applies to pressure-temperature derating on industrial valves. The ASME class on the body (150, 300, 600, 900) is a reference rating at a base temperature; the allowable working pressure falls as temperature rises along the pressure-temperature curve of the body material per ASME B16.34. A Class 300 carbon-steel body that holds roughly 740 psi at ambient holds substantially less at 400 degrees Celsius. Always read the working pressure off the derated curve at the actual operating temperature, and confirm the seat and seal temperature limits independently, because the body, seat, and elastomer each impose their own ceiling.

Chapter 6 / 06

Selection Decision Factors

To turn the preceding five chapters into a specific model, follow the decision sequence below. Most selection mistakes are not a single wrong number but a premature decision at the wrong level, for example fixing on a wafer body before confirming the service is not dead-end. These nine steps work as a fixed RFQ template.

  1. Function and offset type: Decide on/off isolation versus modulating control, then choose concentric (clean, low-pressure), double offset (cycle life, moderate pressure, chemistry), or triple offset (zero leak, fire-safe, high temperature, steam). Do not over-specify offset for a benign water line.
  2. Size and pressure class: Match DN / NPS to the line and select ASME class, PN, or AWWA class against the maximum working and differential pressure, remembering the pressure-temperature derating of the body material.
  3. Body style and end connection: Wafer for inline isolation only; lug or double-flanged for end-of-line or dead-end; butt-weld for high-integrity service. Confirm the dead-end pressure rating if relevant.
  4. Seat material: Match the elastomer or metal seat to media and temperature per Chapter 4. Verify the manufacturer corrosion and temperature chart for the exact concentration.
  5. Disc and stem metallurgy: Select disc material for corrosion and erosion (ductile iron, 316, duplex, nickel alloy, hardfaced for slurry) and confirm the stem is sized for maximum differential pressure to avoid shear.
  6. Shutoff class and fire-safe: Specify the required ANSI/FCI 70-2 leakage class (IV, V, or VI) and fire-safe certification (API 607 or API 6FA) where the consequence of leakage is high.
  7. Throttling and cavitation: For control duty, verify the Cv or Kv curve covers the required range within roughly 30 to 70 degrees open, and check the cavitation and choked-flow limits at the worst-case pressure drop.
  8. Actuation and torque: Size the actuator (manual lever, gearbox, electric, or pneumatic) against the maximum required torque (seating plus friction plus peak dynamic torque near 70 to 80 degrees open) times a safety factor, at the lowest available supply pressure.
  9. Standards, certifications, and total cost: Lock the face-to-face standard (API 609, MSS SP-67, EN 593, ISO 5752, AWWA C504), functional safety SIL, and fugitive-emission class, then weigh purchase price against actuator, installation, and lifecycle maintenance.

One last dimension is manufacturer serviceability: availability of seat and seal repair kits, local actuator support, witnessed test certificates, and interchangeable face-to-face dimensions for future replacement. These seem secondary at purchase but determine repair response time after years in service. Bray, EBRO, Crane, Velan, Emerson, Flowserve, and Baker Hughes maintain global service for industrial and high-performance lines, while DeZURIK, Pratt, Val-Matic, and Mueller serve AWWA water-utility duty, making them reliable choices for large projects.

FAQ

What is the difference between a concentric and a triple offset butterfly valve?

A concentric (zero-offset) butterfly valve places the stem on the centerline of both the disc and the bore, so the disc rubs against a resilient elastomer seat through the full 90-degree stroke. This gives bubble-tight shutoff at low cost but limits service to roughly ASME Class 150 to 300 and the temperature range of the elastomer. A triple offset valve adds three eccentricities: the stem is offset behind the disc plane, the stem is offset from the bore centerline, and the seat cone axis is tilted off the pipe axis. The result is a frictionless, cam-action metal-to-metal seal that only contacts at the last few degrees of closure, enabling Class IV to Class VI shutoff at Class 150 to 900 and temperatures from cryogenic to roughly 425 degrees Celsius. Concentric valves wear the seat on every cycle; triple offset valves do not.

What is the difference between a wafer-style and a lug-style butterfly valve?

A wafer body has no bolt holes through it: it is sandwiched between two pipe flanges and held by long through-bolts that pass around the body. It is cheaper and lighter but cannot support piping on one side, so it must never be used for dead-end service or downstream isolation. A lug body has threaded bolt holes (lugs) cast into the periphery; each flange bolts independently into the body, so either side can be removed while the line stays pressurized. Lug valves can be used for end-of-line and dead-end service, though their dead-end pressure rating is usually derated to about half the inline rating. A double-flanged body has integral flanges on both ends and is preferred for large diameters and higher pressures.

Which seat material should I choose for a resilient-seated butterfly valve?

Match the elastomer to the media and temperature. EPDM suits water, dilute acids and bases, and steam to about 120 to 130 degrees Celsius but is destroyed by hydrocarbons and oils. NBR (Buna-N) handles oils, fuels, and greases from about minus 20 to plus 80 degrees Celsius but not strong oxidizers. FKM (Viton) covers oils, hydrocarbons, and aggressive chemistry from about minus 20 to plus 200 degrees Celsius. PTFE handles nearly universal chemical compatibility from roughly minus 50 to plus 200 degrees Celsius but is harder, so it needs higher operating torque and a backing seat. For abrasive slurry or food and pharmaceutical CIP duty, specify the seat liner accordingly. Above the elastomer limits, move to a metal-seated offset valve.

Why must a wafer butterfly valve never be used for dead-end service?

A wafer body is clamped between two mating flanges by through-bolts. If the downstream flange is removed for maintenance, the only thing holding the line pressure is the upstream gasket joint and the unsupported wafer body, which can blow out or leak because there is no integral flange to retain it. Lug bodies solve this because the downstream flange bolts thread directly into the valve lugs, so the body itself becomes the end seal. When end-of-line or dead-end isolation is required, specify a lug or double-flanged body and confirm the manufacturer's dead-end pressure rating, which is typically derated to roughly 50 percent of the inline rating unless the valve is specifically certified for full dead-end duty.

How do I size actuator torque for a butterfly valve?

Required torque is the sum of seating torque (breaking the disc free from the elastomer or metal seat), bearing and stem friction torque, and hydrodynamic (dynamic) torque from flow pushing on the disc. Hydrodynamic torque peaks near 70 to 80 degrees open, not fully open, so throttling near that band is the worst case. Manufacturers publish a break-to-open and a break-to-close torque per size and pressure class; you then multiply by a safety factor, commonly 1.25 to 1.5 for on/off and higher for modulating duty, and confirm the actuator output at the lowest available air or supply pressure. AWWA C504 gives empirical dynamic torque relationships for water valves. Always size against the maximum differential pressure the disc will see, not the nominal line pressure.

Can a butterfly valve be used for throttling and flow control?

Yes, but with caveats. A butterfly valve has an inherently equal-percentage-like characteristic only across part of its travel; most of the flow change happens between about 30 and 70 degrees open, while the first and last 20 degrees do little. Effective control range is therefore roughly 30 to 70 degrees, and operating near the closed position invites cavitation, high velocity across the disc edge, and seat erosion. For modulating service, use a high-performance double-offset or triple-offset valve with a hardened disc edge, verify the Cv or Kv flow coefficient curve against your required range, and check the cavitation and choked-flow limits at the worst-case pressure drop. For tight control at low flow, a globe or dedicated control valve is often better.

What is Class VI shutoff and which butterfly valves achieve it?

Leakage classes are defined by ANSI/FCI 70-2 and IEC 60534-4. Class IV allows leakage of 0.01 percent of rated capacity, Class V about 0.0005 percent, and Class VI is a bubble-count test for soft seats that permits only a few milliliters per minute even on large valves, effectively zero leakage. Resilient (concentric) elastomer-seated valves give bubble-tight, essentially Class VI shutoff on clean water and gas at low pressure. Metal-seated triple-offset valves are typically certified to Class IV as standard and Class V or VI as an option, while also meeting fire-safe (API 607 or API 6FA) requirements that soft seats cannot. Always confirm the certified leakage class on the test certificate, since the same valve family can be offered at several classes.

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