Gate Globe Check

Valve Reference Library
Gate, Globe & Check Valves

Core manual valve theory, design, standards, materials, trims, and field application. The structural backbone of industrial piping β€” isolation, regulation, and protection.

If ball and butterfly valves dominate modern automation, gate, globe, and check valves still form the structural backbone of industrial piping systems. They are mechanically simple, highly repairable, tolerant of extreme pressure and temperature, and trusted in services where failure has consequences.

These valves define how engineers think about isolation vs regulation, pressure drop vs control, manual vs automatic behavior, and maintenance philosophy. Every other valve type borrows concepts from these three.

This page integrates the governing standards framework (API, ASME, ASTM, MSS, NACE), body materials, the API trim number system, hardfacing, bolting, and end connections into a single comprehensive reference. For the complete standards framework, see Valve Standards β†’. For the full materials and trim reference, see Valve Materials & Trims β†’.

Standards Framework β€” How Gate, Globe & Check Valves Are Governed

No single standard fully governs these valves. API defines type and behavior. ASME sets the pressure-temperature envelope and dimensions. ASTM defines materials. MSS fills the testing and marking gaps. NACE overlays sour service restrictions.

The Three-Layer Model
  • API 600 / 602 / 603 / 594 β€” Valve type, construction, and performance intent
  • ASME B16.34 + B16.10 + B16.5 β€” Pressure-temperature ratings, face-to-face dimensions, flange interface
  • MSS SP-61 + SP-25 β€” Pressure testing methodology, marking and traceability
  • ASTM A216, A351, A182, A350, A890, etc. β€” Body, trim, and bolting material specifications
  • NACE MR0175 / MR0103 β€” Sour service material restrictions when applicable
Valve Type Primary API Standard Mandatory ASME Overlay MSS Overlay Fire Test
Gate β€” OS&Y, Bolted Bonnet API 600 (14th ed. 2021) B16.34, B16.10 SP-61, SP-25 API 6FA (if required)
Gate / Globe / Check β€” Forged ≀4" API 602 (11th ed. 2022) B16.34 SP-61, SP-25 API 6FA (if required)
Gate β€” Corrosion-Resistant API 603 (10th ed. 2025) B16.34 SP-61, SP-25 API 6FA (if required)
Check Valve (Wafer/Lug/Flanged) API 594 (9th ed. 2022) B16.34, B16.10 SP-61, SP-25 API 6FA (if required)
Testing Baseline (all types) API 598 (11th ed. 2023) β€” SP-61 β€”
API Never Stands Alone EPC specifications always stack: "Valve shall comply with API 600, ASME B16.34, ASME B16.10, MSS SP-61." A vendor quoting only API compliance is non-compliant with the full specification. Every standard in the stack addresses a different engineering requirement.
API Standards β€” Detail
  • API 600 (14th ed. May 2021) β€” Bolted bonnet steel gate valves: heavy-wall, OS&Y, rising stem with backseat. The definitive refinery and pipeline gate valve standard. Always paired with ASME B16.34 and API 598.
  • API 602 (11th ed. May 2022) β€” Compact forged steel gate, globe, AND check valves (typically ≀4"). Forged body, socket weld / threaded / flanged ends. Covers all three valve types in one standard.
  • API 603 (10th ed. July 2025) β€” Corrosion-resistant gate valves: reduced wall thickness vs API 600, optimized for stainless alloys. For API 603 specifically: must still comply with ASME B16.34 β€” reduced wall does not mean reduced P-T rating, it means the material group (stainless) allows thinner walls to achieve the same rating.
  • API 594 (9th ed. Feb 2022) β€” Check valves: wafer, lug, flanged, and butt-weld. Covers swing, dual plate, lift, and tilting disc types. Includes P-T ratings, face-to-face dimensions, and testing per API 598.
  • API 598 (11th ed. 2023) β€” Mandatory testing baseline for all API valve types: shell pressure test, seat leakage test, test pressures, test durations, and acceptable leakage quantities. Referenced by API 600, 602, 603, 594, 608, 609. If a vendor's test cert does not reference API 598, the test is likely non-conforming.
  • API 574 β€” Inspection practices for piping system components including valves. Used by plant inspectors and reliability engineers during in-service inspection.
  • API 6FA (5th ed. May 2020) β€” Broad fire test applicable to all valve types. Required when fire-safe certification is specified on gate, globe, or check valves. Not API 607, which is limited to soft-seated quarter-turn valves.
ASME Standards β€” Governing the Pressure Boundary
  • ASME B16.34 (2025) β€” The core valve pressure-body standard. P-T ratings, material groups, minimum wall thickness, stem retention (anti-blowout), and end connection rules. Pressure class alone is NOT the operating pressure β€” always verify against the B16.34 P-T table for the specific body material at operating temperature.
  • ASME B16.10 (2022) β€” Standardized face-to-face and end-to-end dimensions. Critical for turnaround interchangeability. Not every valve is built to B16.10 by default β€” verify on the datasheet.
  • ASME B16.5 (2025) β€” Pipe flange dimensions, P-T ratings, bolt patterns, facing type. Governs flanged gate, globe, and check valve connections up to NPS 24. Large-diameter flanges (NPS 26+) fall under ASME B16.47.
  • ASME B16.11 (2021) β€” Forged fittings for socket weld and threaded small-bore valve connections. Class 2000/3000/6000 β€” not the same as Class 150/300/600 flanges.
  • ASME B16.20 (2023) β€” Metallic gaskets: spiral wound, RTJ oval/octagonal rings, metal jacketed. Wrong spiral wound selection = chronic body joint leaks.
  • ASME B31.3 (2024) β€” Process piping code: governs how valves are installed, tested, and accepted in refinery and chemical plant piping systems. B31.3 governs the piping system, not the valve design β€” yet controls installation, examination, and pressure testing of the complete assembly.
  • ASME B31.1 β€” Power piping code. Used for steam systems and boilers where gate and globe valves dominate.
MSS, BS, and NACE Standards
  • MSS SP-25 (2018) β€” Marking requirements: size, class, material grade, heat number. Marking must match CMTR at incoming inspection β€” a stamp without a matching CMTR is grounds for rejection.
  • MSS SP-61 (2019) β€” Pressure testing of valves: shell test and seat test logic. Often paired with API 598 or referenced as the testing basis in client specifications.
  • MSS SP-117 (2023) β€” Bellows seal valves for fugitive emissions control. Specifying bellows seal bonnet on globe valves eliminates packing as a VOC emission path.
  • BS 1873 (1975) β€” Steel globe valves: legacy standard used in BS-preference projects. Overlaps with API 602 in scope.
  • BS 1868 (1975) β€” Steel check valves: legacy standard for BS-based projects, overlapping API 594.
  • NACE MR0175 / ISO 15156 β€” Materials for upstream Hβ‚‚S service. Governs body material grades, heat treatment, and hardness limits for all wetted components including gate, globe, and check valves.
  • NACE MR0103 / ISO 17945 β€” Refinery wet Hβ‚‚S conditions. Different rules from MR0175 β€” do not conflate. Refinery gate and globe valves in sour hydrocarbon service fall under MR0103, not MR0175.

Body & Bonnet Materials

Body material determines pressure containment, corrosion resistance, temperature capability, weldability, and cost. ASME B16.34 ties each ASTM material group to its allowable P-T envelope. Gate and globe valves are typically cast (large sizes) or forged (small bore and high pressure).

Material Common Name ASTM Cast ASTM Forged Typical Gate/Globe/Check Service
WCB / A105 Carbon Steel A216 WCB A105 General hydrocarbon, steam, utilities β€” the default
LCC / LF2 Low-Temp Carbon Steel A352 LCC A350 LF2 Cold service, cryogenic-adjacent β€” mandatory Charpy impact testing
WC6 / F11 1ΒΌ Cr-Β½ Mo A217 WC6 A182 F11 Elevated temperature β€” steam, power generation
WC9 / F22 2ΒΌ Cr-1 Mo A217 WC9 A182 F22 Higher temperature and pressure β€” refinery heaters
CF8M / F316 316 Stainless Steel A351 CF8M A182 F316 Corrosive service β€” chemical plants, acid systems
CF8 / F304 304 Stainless Steel A351 CF8 A182 F304 Mild corrosive service β€” lower cost than CF8M
Duplex (F51) 2205 A890 CD3MN A182 F51 Chloride service β€” offshore, coastal, chemical
Alloy 20 β€” A351 CN7M B473 Sulfuric acid and phosphoric acid service
Monel β€” β€” MFG standard Marine, HF acid β€” seawater and aggressive corrosion
Low-Temperature Material Error

A216 WCB and A105 are NOT suitable for low-temperature impact-critical service. They have no mandatory Charpy impact testing requirement. A352 LCC (cast) or A350 LF2 (forged) are required for cold-service gate and globe valves. This is the most common body material procurement error on cold-climate and cryogenic projects.

Pressure Class vs Operating Pressure A Class 300 WCB gate valve is rated approximately 740 psig at ambient temperature β€” but only ~410 psig at 800Β°F. The P-T derating curve is governed by ASME B16.34 and varies by body material group. Always verify the P-T table for the actual material at the actual operating temperature. Pressure class alone is never the operating pressure.

Shared Mechanical Architecture (Gate & Globe)

Before separating gate and globe valves, understand what they share. Most real-world failures happen in the shared components, not the closure element.

Pressure Boundary Components

Body

The primary pressure-retaining component. Material choice (carbon steel, alloy steel, stainless) is driven by pressure class, temperature, corrosion allowance, and code. ASME B16.34 governs minimum wall thickness.

Bonnet

Provides access to internals and seals the body opening. Bonnet design directly affects pressure rating, fugitive emissions performance, and serviceability.

Body–Bonnet Joint

A major leak risk. Design options: bolted gasketed joint, welded joint, and pressure seal joint. ASME B16.34 governs the design envelope for each.

Bonnet Designs and What They Signal

Pressure seal bonnet valve cross section
Welded bonnet valve

Bolted Bonnet

Most common. Serviceable. Gasket is a maintenance item. The default for most industrial gate and globe valves. Governed by API 600 / 602 and ASME B16.34.

Welded Bonnet

Excellent for fugitive emissions control. Reduced serviceability β€” internals cannot be accessed without cutting. Common in API 602 forged steel valves and small-bore high-pressure service.

Pressure Seal Bonnet

Used in Class 900 and above. Internal pressure energizes the seal β€” higher pressure produces tighter sealing. Lighter than the massive bolting required at high class. Common in power generation gate and globe valves.

Bonnet choice often tells you what pressure class and service severity the valve was designed for. Pressure seal bonnets are a direct signal of Class 900+ service.

Stem, Packing, and Fugitive Emissions

Stem

Transmits operator force to the closure element. Subject to axial load, bending, and corrosion. ASME B16.34 requires anti-blowout stem design β€” the stem cannot be ejected under pressure.

Packing

Primary fugitive emission path. Requires adjustment over valve life. Material choice affects torque and leakage. For fugitive emissions compliance: ISO 15848 or API 624 testing may be required depending on the project spec.

Backseat

Allows packing replacement under pressure (with valve fully open). Not a substitute for proper isolation β€” commonly misunderstood and misused in the field. Defined and required by API 600 and API 602.

Packing failure is the most common long-term valve issue β€” not seat failure. The stem-packing interface is where valves leak first in high-cycle or thermal-cycling service.

1. Gate Valves

Isolation valves by geometry, not force. The default choice for large-diameter isolation with minimal pressure drop.

Governing Standards β€” Gate Valves
  • API 600 (14th ed. May 2021) β€” Heavy-wall bolted bonnet steel gate valves: OS&Y design, rising stem with backseat, flexible wedge standard. The definitive standard for large refinery and pipeline gate valves. Requires ASME B16.34, B16.10, and API 598 overlay.
  • API 602 (11th ed. May 2022) β€” Compact forged steel gate valves ≀4": socket weld, threaded, or flanged ends. Also covers forged globe and check valves. Requires ASME B16.34 and API 598 overlay.
  • API 603 (10th ed. July 2025) β€” Corrosion-resistant (stainless) gate valves: reduced wall thickness vs API 600, optimized for CF8M and other stainless alloys. Used in chemical plant and corrosive service. Requires ASME B16.34 and API 598.
  • API 6D (25th ed. 2021) β€” Pipeline gate valves when specified in transmission service. Gate valves under API 6D are often slab or expanding gate design β€” fundamentally different from API 600 wedge-gate valves.
  • API 598 β€” Mandatory testing for all gate valve types: shell test, seat leakage test (zero leakage for metal seat per API 598 Class A), and test durations.
  • ASME B16.34 β€” P-T ratings, wall thickness, stem anti-blowout β€” always required alongside any API gate valve standard.
  • MSS SP-25 + SP-61 β€” Marking (heat number / CMTR traceability) and pressure test method details.
  • API 6FA β€” Fire test when fire-safe gate valves are specified. API 607 does not apply to gate valves.
  • NACE MR0175 / MR0103 β€” Sour service material and hardness requirements where applicable.
Gate valve cross section showing wedge

1.1 What a Gate Valve Is Actually Doing

A gate valve uses a sliding closure element (wedge or parallel plate) that moves perpendicular to flow. When fully open, the gate is completely out of the flow path β€” turbulence is minimal and pressure drop is very low. This makes gate valves ideal for large-diameter isolation service.

1.2 Why Gate Valves Fail When Throttled

Gate valves are frequently misused as throttling valves. When partially open: flow jets impinge on the lower edge of the gate, turbulence induces vibration, seats erode rapidly, and the gate chatters and damages guides. This is not a design flaw β€” it is a misapplication.

Common Misapplication

If you need to control flow rate, use a globe valve or control valve. A gate valve held mid-stroke will destroy itself in months β€” often faster. API 600 construction is optimized for fully open and fully closed dwell β€” not modulation.

1.3 Gate Valve Closure Designs

Wedge Gate

The most common design β€” API 600

Wedge angle produces sealing force. Tighter closure increases seat stress. Sensitive to thermal expansion.

Variants:

  • Solid wedge β€” strong but prone to thermal binding
  • Flexible wedge β€” tolerates thermal growth; standard in API 600
  • Split wedge β€” self-aligning, best for high-temperature service

Used in: steam service, refinery block valves, utility isolation.

Parallel Slide Gate

No wedging stress

Parallel slide gate valve

Two parallel plates seal against seats. No wedging stress, reduced thermal binding, stable sealing across temperature swings.

Common in: steam, power generation, high-cycle isolation.

Resilient-Seated Gate

Elastomer-seated water service

Elastomer seats provide excellent shutoff at low pressure. Temperature limited. Intolerant of debris or hydrocarbons.

Used in: water, wastewater, utility systems. MSS SP-70 (cast iron) or AWWA standards typically govern water service gate valves.

Knife Gate

Cuts through solids and slurry

Knife gate valve

Thin blade cuts through solids. Not designed for pressure-tight shutoff in high-pressure service. Often unidirectional. Not governed by API 600 β€” typically MSS SP-81 or manufacturer standard.

Used in: mining, pulp & paper, sludge service.

1.4 Gate Valve Trim β€” Materials and API Trim System

Gate valves use the API trim number system (Trim 1–18) to define the material combination of seat, disc/wedge, stem, and backseat. One trim number on a datasheet replaces a paragraph of material callouts β€” provided both parties read the same version of the standard.

Trim # Nominal Seat Wedge / Disc Stem / Backseat Typical Gate Valve Service
1 13Cr 410 SS 410 SS 410 SS General service
5 FHF (13Cr) Stellite hardfaced Stellite hardfaced 410 SS Severe wear, steam
8 13Cr + HF Stellite hardfaced 410 SS 410 SS General hydrocarbon β€” most common gate valve trim
10 316 316 SS 316 SS 316 SS Corrosive service
12 316 + HF Stellite hardfaced 316 SS 316 SS Corrosive + erosion
13 Alloy 20 Alloy 20 Alloy 20 Alloy 20 Acid service
16 FHF (316) Stellite hardfaced Stellite hardfaced 316 SS Severe corrosive / erosive
17 FHF (347) Stellite hardfaced Stellite hardfaced 347 SS High temp + erosion
Trim Numbers Define Internals Only API trim numbers govern seat, disc/wedge, stem, and backseat material. They say nothing about body material. Always specify body material separately on the datasheet. Trim 8 in a WCB body is fundamentally different from Trim 8 in a CF8M body β€” the trim number cannot tell you which one you have.

1.5 Gate Valve Bolting

Body Material Standard Service Bolting Sour Service Low-Temp Service
Carbon Steel (WCB / A105) A193 B7 / A194 2H A193 B7M / A194 2HM A320 L7 / A194 7
Cr-Mo (WC6 / WC9) A193 B16 / A194 4 A193 B16 / A194 4 (verify per spec) Not typical β€” high-temp alloy
300-Series SS (CF8M) A193 B8M / A194 8M A193 B8M / A194 8M A193 B8M / A194 8M
Duplex (F51) A453 Grade 660 or per project spec Confirm MR0175 compliance per spec Per project spec
Sour Service Bolting Standard A193 B7 fails by sulfide stress cracking in wet Hβ‚‚S. A193 B7M / A194 2HM (hardness-controlled) is required under NACE MR0175 and MR0103. Always verify NACE compliance on the bolt CMTR β€” not just the stamp. A NACE-stamped valve assembly with non-compliant bolting CMTRs is non-conforming.

1.6 Selection Reality

Choose Gate When

  • Line size is large
  • Pressure drop must be minimal
  • Valve will stay open or closed for long periods
  • Pigging is required (full bore)

Avoid Gate When

  • Throttling is required
  • Frequent cycling is expected
  • Tight shutoff at low pressure with debris present
  • Automation is required β€” high thrust and long stroke make gate valves expensive to automate

1.7 Gate Valve Actuation

Gate valve actuator types comparison

Gate valve actuation converts rotation to linear motion via stem threads. The actuator must overcome seat friction, packing friction, stem thread friction, differential pressure forces, and wedge geometry effects. Thrust requirements are highest at final closure.

Thermal Binding

A gate valve closed at high temperature, then cooled β€” the body contracts around the wedge, and required opening thrust may exceed actuator capability. Mitigated by flexible or split wedges, oversized actuators, and operator training not to overtighten gate valves hot.

Manual Handwheel

Small sizes. Low pressure. Infrequent operation.

Gear Operators

Large diameters. High thrust. Reduce operator effort at large sizes and high pressures.

Electric Actuators (MOV)

Precise positioning. High thrust. Thermal binding is a key sizing input. AUMA, Rotork, Limitorque type.

Hydraulic Actuators

Extremely high thrust in a compact package. Used for ESD, pipeline, and large-diameter service. Common for API 6D gate valves.

Gate Valve Actuation Engineering Rules
  • Size thrust for maximum Ξ”P, aged seat friction, and thermal effects β€” not catalog torque
  • Electric or hydraulic actuation preferred β€” pneumatic air struggles to deliver sustained thrust at gate valve scale
  • If the actuator fails, the valve fails β€” treat gate valve and actuator as one system

2. Globe Valves

Valves built to waste pressure on purpose. The mechanical basis of most control valves. The go-to choice wherever throttling stability matters more than efficiency.

Governing Standards β€” Globe Valves
  • API 602 (11th ed. May 2022) β€” Primary standard for forged steel globe valves (≀4"). Same standard covers forged gate and check valves. Socket weld, threaded, or flanged ends. Always paired with ASME B16.34 and API 598.
  • API 598 (11th ed. 2023) β€” Mandatory testing: shell pressure test, seat leakage test. Globe valves with metal seats must meet API 598 Class A seat leakage (zero leakage). Soft-seated globe valves use Class B (rated leakage).
  • ASME B16.34 (2025) β€” P-T ratings, wall thickness, anti-blowout stem requirement. Always required.
  • ASME B16.10 (2022) β€” Face-to-face dimensions for interchangeability. Critical on turnarounds where a replacement globe valve must fit the existing spool.
  • BS 1873 (1975) β€” Legacy steel globe valve standard used in BS-preference specifications. Overlaps API 602 in scope for forged globe valves.
  • MSS SP-117 (2023) β€” Bellows seal globe valves for fugitive emissions control. Eliminates packing as an emission path. Required on some process streams under environmental regulation.
  • API 6FA β€” Fire test for globe valves when fire-safe certification is specified. API 607 does not apply to globe valves.
  • NACE MR0175 / MR0103 β€” Sour service material requirements. Globe valves in wet Hβ‚‚S service require NACE-compliant body, trim, and bolting β€” each verified by CMTR.
  • ISO 15848 / API 624 β€” Fugitive emissions qualification testing for packing systems. Required when VOC emissions compliance is specified.
Globe valve cross section showing disc and seat

2.1 Operating Principle

A globe valve forces flow to change direction as it passes through the valve. The disc moves toward or away from a seat, regulating flow area gradually. This creates predictable flow control, high pressure drop, and excellent throttling stability.

2.2 Flow Direction and Control Behavior

Globe valves are usually directional. Correct flow direction stabilizes the disc, reduces vibration, and improves control. Incorrect flow direction causes chatter, accelerates seat wear, and increases stem load.

Field Reality

Always verify flow direction before installation. An arrow on the body is not always reliable β€” confirm against the datasheet for flow-under-seat vs flow-over-seat designs. Wrong flow direction can double required actuator thrust and cause chronic instability.

2.3 Body Patterns

T-Pattern

Best throttling. Highest pressure drop. The classic globe valve geometry. Use where flow regulation is the primary requirement.

Angle Pattern

Replaces an elbow. Useful where piping turns 90Β°. Reduces one fitting and one potential leak point in the system.

Y-Pattern

Reduced pressure drop vs T-pattern. Preferred when throttling and efficiency both matter β€” offshore, high-pressure steam, where Ξ”P budget is constrained.

2.4 Disc and Plug Geometry β€” Control Trim

Globe valve disc and plug geometries

Quick Opening

Most flow occurs in the first 25% of travel. Used for on/off and emergency relief duty where fast response matters more than precise modulation.

Linear

Flow proportional to stem position. Used where system pressure drop is largely constant β€” easier to control in stable Ξ”P systems.

Equal Percentage

Equal increments of travel produce equal percentage changes in flow. The dominant trim for control valves on variable-Ξ”P systems β€” used in most refinery and process control loops.

This is why globe valves form the mechanical basis of control valves. The disc geometry is the control trim β€” what ISA calls the "valve characteristic." Choosing the wrong characteristic for the system Ξ”P profile causes poor control loop performance regardless of the positioner or controller.

2.5 Globe Valve Trim β€” Materials and API Trim System

Globe valves use the same API trim number system as gate valves. The materials page notes: "Globe valves often require higher hardfacing levels due to throttling duty." A Trim 8 gate valve (hardfaced seat only) in throttling service would fail quickly β€” globe valves in throttling service typically use Trim 5 or Trim 16 (full hardface on both seat and disc) to withstand the continuous flow impingement and wear of partial-open operation.

Trim # Nominal Seat Disc / Plug Stem Globe Valve Service Notes
1 13Cr 410 SS 410 SS 410 SS Light throttling, general service
5 FHF (13Cr) Stellite hardfaced Stellite hardfaced 410 SS Steam throttling, severe wear β€” both surfaces hardfaced for throttling duty
8 13Cr + HF Stellite hardfaced 410 SS 410 SS Isolation duty only in globe valves β€” not adequate for continuous throttling
10 316 316 SS 316 SS 316 SS Corrosive service, mild throttling
12 316 + HF Stellite hardfaced 316 SS 316 SS Corrosive + throttling service
15 FHF (304) Stellite hardfaced Stellite hardfaced 304 SS High-wear throttling in mildly corrosive service
16 FHF (316) Stellite hardfaced Stellite hardfaced 316 SS Severe throttling in corrosive / erosive service β€” the premium throttling trim
13 Alloy 20 Alloy 20 Alloy 20 Alloy 20 Acid throttling service

2.6 Globe Valve Limitations

Tradeoffs

  • Higher Ξ”P than gate valves
  • Heavier and bulkier for given size
  • Not economical at very large diameters
  • Higher thrust required at high pressure β€” especially at near-closed throttling

What You Get In Return

  • Excellent throttling stability
  • Predictable Cv across travel
  • Stable disc position under variable load
  • The control-valve foundation β€” all ISA control valve theory is built on globe valve geometry

Globes trade efficiency for control and stability.

2.7 Globe Valve Actuation

Globe valve actuators on piping

Globe valves close directly against flow. In common throttling configurations (flow-under-seat / flow-to-open), closing force rises sharply near the seat: flow velocity increases, pressure differential concentrates at the seat, and closing force escalates. This makes globe valves thrust-intensive at high Ξ”P.

Flow Under the Disc

Lower opening thrust. Stable control. Standard orientation for most globe control valves. Disc is pushed open by flow β€” actuator works with the process.

Flow Over the Disc

Higher closing thrust. Risk of chatter. Used in specific applications where fail-closed on loss of signal is assisted by flow force pushing disc onto seat.

Manual Handwheel

Small sizes, low Ξ”P service, infrequent operation.

Electric Actuators

Used for isolation or coarse control. Slower response than pneumatic. Common for remote on/off globe valves.

Pneumatic Diaphragm

Most common for modulating control service. Smooth force delivery, fast response, inherently fail-safe. The control valve standard.

Piston Actuators

High thrust in compact package. Used for high Ξ”P control and tight-shutoff globe valves. Faster than diaphragm at large sizes.

In throttling service, actuator stiffness matters. If actuator force is too low, the disc oscillates, control becomes unstable, and the valve hunts. This is why control valves are oversized on thrust and positioners are used. Globe valves dominate control applications precisely because their geometry is compatible with high thrust and precise positioning.

3. Check Valves

Automatic protection with no second chances. No operator, no control system β€” only physics.

Governing Standards β€” Check Valves
  • API 594 (9th ed. Feb 2022) β€” Primary standard: wafer, lug, flanged, and butt-weld check valves. Covers swing, dual plate, lift, and tilting disc designs. Includes P-T ratings, face-to-face dimensions, and testing per API 598. Always paired with ASME B16.34 and MSS SP-61.
  • API 602 (11th ed. May 2022) β€” Compact forged steel check valves ≀4". Same standard as for forged gate and globe. Governs small-bore high-pressure check valves in socket weld and threaded configurations.
  • API 598 (11th ed. 2023) β€” Testing baseline: shell test and seat leakage. For check valves, seat leakage testing is performed with flow in the reverse direction to verify the valve closes and seals correctly under back-pressure.
  • ASME B16.34 β€” P-T ratings and wall thickness. Always required.
  • ASME B16.10 β€” Face-to-face dimensions for flanged check valves. Dual-plate (wafer) check valves have short face-to-face β€” verify against spool before ordering.
  • BS 1868 (1975) β€” Legacy standard for steel check valves in BS-preference specifications. Overlaps API 594.
  • MSS SP-71 (2018) β€” Cast iron swing check valves for water and utility service.
  • NACE MR0175 / MR0103 β€” Sour service: body, disc/clapper, hinge pin, spring, and seat materials must all comply with hardness limits. Springs in check valves are particularly vulnerable to SSC in sour environments β€” material selection requires specific attention.
Swing check valve operation

3.1 What a Check Valve Actually Does

A check valve allows flow in one direction and closes automatically when flow reverses or decelerates. It protects pumps from backspin, compressors from reverse flow, headers from cross-contamination, and tanks from siphoning. No operator, no control system β€” only the physics of flow, gravity, spring force, and differential pressure.

3.2 The Hidden Complexity of "Simple" Check Valves

Most check valve failures occur because they are oversized β€” flow velocity is too low, the valve never reaches full open position, the disc flutters continuously against the stop, and fatigue destroys the internals within months. A check valve is not sized to match the pipe diameter β€” it is sized to match the actual flow regime in that line.

Sizing Rule

Check valves must be selected based on flow regime, not pipe size. A check valve sized to match the pipe but oversized for the actual flow will fail early due to disc flutter and internal fatigue. The minimum velocity to fully open a swing check valve is typically 2–4 ft/s depending on design β€” verify with the manufacturer's minimum velocity curve.

3.3 Common Check Valve Types

Swing Check

Gravity-assisted closure β€” API 594

Swing check valve internal hinge

  • Hinged disc swings on flow
  • Piggable in straight-through designs
  • Prone to slam at flow reversal β€” no spring assist

Used in: pipelines, low-velocity systems where slam can be managed.

Dual Plate (Double Door)

Spring-assisted wafer β€” API 594

Dual plate check valve

  • Compact wafer design β€” short face-to-face per API 594
  • Spring-assisted, significantly reduced slam vs swing check
  • Not piggable β€” the central post and dual plates block pig passage

Used in: process piping where space is limited and pigging is not required.

Silent / No-Slam Check

Spring closes before reversal

Silent check valve with spring

  • Spring forces disc closed before full flow reversal occurs
  • Minimizes water hammer β€” valve is already closed before pressure spike
  • Higher Ξ”P than swing or dual plate

Preferred near pumps and in any system where slam-induced water hammer is unacceptable.

Lift / Piston Check

Disc lifts vertically

Lift piston check valve

  • Disc lifts vertically off the seat β€” must be installed in correct orientation
  • Sensitive to fouling β€” small clearances
  • Excellent seat tightness in clean service

Used in: steam, clean liquids, vertical-flow applications.

3.4 Check Valve Trim and Materials

Check valves use the API trim number system (governed by API 594 and API 602 for forged designs). The same seat/disc/stem material philosophy applies β€” trim number calls out disc/clapper material, seat material, and hinge/pivot material. For sour service, springs must also meet NACE hardness limits β€” spring material is the most frequently overlooked non-compliance item in check valve sour service procurement.

Trim # Seat / Disc Material Hinge / Pivot Check Valve Service
1 410 SS 410 SS General hydrocarbon service
8 Seat: Stellite hardfaced / Disc: 410 SS 410 SS Erosive hydrocarbon β€” most common check valve trim
10 316 SS 316 SS Corrosive service check valves
12 Seat: Stellite hardfaced / Disc: 316 SS 316 SS Corrosive + erosive service
9 Monel Monel Marine and HF acid β€” check valves in seawater headers
13 Alloy 20 Alloy 20 Acid service check valves

3.5 Orientation and Location Matter

Horizontal vs vertical installation changes check valve behavior significantly. Gravity assists closure in horizontal swing checks and opposes it in vertical upflow configurations. Turbulent flow from elbows directly upstream destabilizes disc operation and causes premature flutter.

A check valve placed too close to a pump or elbow is designed to fail early. Minimum recommendation: at least 5 to 10 pipe diameters of straight pipe upstream of the check valve. This is not a conservative suggestion β€” it is the basis of most manufacturer installation instructions and is supported by API 594 commentary.

3.6 Slam, Water Hammer, and Dynamic Loads

Water hammer and check valve slam

Water hammer is caused when flow reverses rapidly, the check valve slams shut, and kinetic energy converts to a pressure spike. This can crack valve bodies, shear hinge pins, damage pump seals, and overpressure downstream piping sections.

Non-Spring (Swing)

  • Depend on gravity and back-pressure for closure
  • Slower closure β€” reversal begins before valve is fully closed
  • More prone to slam at power failure or pump trip

Spring-Assisted (Silent / Dual Plate)

  • Spring preload closes valve before full flow reversal occurs
  • Dramatically reduced slam and water hammer
  • Higher pressure drop accepted as a trade for system protection

3.7 The Biggest Check Valve Mistake

Oversizing "to reduce pressure drop." This causes unstable operation, disc flutter, accelerated wear, hinge pin fatigue failure, and often catastrophic internal destruction. A slightly higher Ξ”P with stable operation is always better than a low-Ξ”P unstable valve that fails in months. Always obtain and verify the manufacturer's minimum velocity curve before selecting.

End Connections, Gaskets & Valve Markings

End connection selection determines installation method, leak risk, gasket type, and serviceability. Markings determine traceability. Both are specified on the datasheet and governed by distinct standards from the valve construction standard itself.

End Connection Standard Gate / Globe / Check Application
Raised Face (RF) ASME B16.5 / B16.47 Default for Class 150–600 flanged valves β€” the most common process piping configuration
Flat Face (FF) ASME B16.5 Low-pressure utilities where cast iron mating flanges require full-face gasket to avoid bending stress
Ring Type Joint (RTJ) ASME B16.5 / B16.20 Class 900 and above β€” refinery and pipeline gate and globe valves in high-pressure, high-temperature service
Butt Weld (BW) ASME B16.25 Permanent high-integrity installations β€” eliminates flange leak paths. Common for pipeline gate valves
Socket Weld (SW) ASME B16.11 Small bore (≀2") forged gate and globe valves β€” API 602 service
Threaded (NPT) ASME B1.20.1 Non-critical small bore β€” utility and instrument service only
Valve Markings Governed by MSS SP-25 Every valve must carry: NPS or DN (size), ASME pressure class, body material grade per ASTM, API trim designation, manufacturer name or mark, and heat number. Heat numbers must match the corresponding CMTR β€” inspectors verify this match at incoming inspection. A stamped valve without a matching CMTR is grounds for rejection and cannot be installed in a code-compliant system.

Actuation & Torque β€” Cross-Valve Comparison

Gate and globe valves are thrust-driven. Check valves are flow-driven and not externally actuated. Understanding the force physics prevents actuator under-sizing β€” the single most common automated valve failure mode.

Valve Type Primary Force Actuation Method Control Capability Typical Challenge
Gate Linear thrust Manual / electric / hydraulic Poor β€” isolation only High thrust, thermal binding, very large actuators
Globe Linear thrust Manual / pneumatic / electric Excellent β€” throttling and control High Ξ”P near closed, actuator stability in modulation
Check Flow-induced (hydrodynamic) None β€” not externally actuated None β€” automatic only Slam, flutter, oversizing, spring fatigue in sour service
Valve Type Electric Actuation Pneumatic Actuation Hydraulic Actuation
Gate Common β€” high thrust, MOV integration. Size for thermal binding. Watch for SSC in sour service if NACE applies to actuator components. Limited β€” pneumatic struggles to deliver sustained thrust at gate valve scale. Not preferred. Critical service preferred β€” pipelines, ESD, large diameters. Compact for the force delivered.
Globe Limited β€” slower response, used for remote isolation duty. Not preferred for modulating control. Standard β€” diaphragm and piston dominate control service. Smooth modulation, fast response, inherently fail-safe with spring return. Severe service β€” high Ξ”P and emergency shutoff where very high thrust is required in compact space.
Check Not externally actuated. Selection is by valve type (swing / dual plate / silent / lift) and spring vs gravity assist, sized for actual flow velocity in the line β€” not pipe size.
Field-Proven Engineering Rules
  • Gate valves β€” electric or hydraulic. Never undersize thrust. Size for maximum Ξ”P + thermal binding + aged seat friction.
  • Globe valves β€” pneumatic unless proven otherwise. Verify flow direction before installation.
  • Check valves β€” size for stable flow velocity at actual operating conditions, not low Ξ”P at rated pipe size.
  • If the actuator fails, the valve fails. Treat gate and globe valves and their actuators as one integrated system, not separate procurements.
Gate valves need force. Globe valves need control. Check valves need stability. Choose actuation accordingly β€” not by habit, but by physics.

For full actuation coverage including pneumatic / electric / hydraulic / electro-hydraulic architectures and the actuator selection decision tree, see the Valve Actuation reference β†’

Complete Specification Checklist

Every line item on a valve datasheet must map to a specific standard. If it doesn't, the vendor fills in the cheapest interpretation by default.

The Four Decisions That Define Any Gate, Globe, or Check Valve
  • Body material β€” sets the pressure-temperature envelope (ASME B16.34) and corrosion baseline (ASTM material + NACE if sour)
  • Trim (API trim number) β€” sets shutoff class, wear life, and throttling durability for gate, globe, and check valves
  • Bolting β€” the weakest link if mismatched to body material, service temperature, and sour service requirement
  • End connection & facing β€” determines installation method, gasket selection, leak risk, and serviceability
Specification Item Governing Standard Common Miss
Gate valve construction API 600 (large cast) / API 602 (forged ≀4") / API 603 (stainless) Calling only API 600 for a stainless gate valve β€” should be API 603
Globe valve construction API 602 (forged) No specific API for cast globe valves >4" β€” must specify ASME B16.34 + API 598 directly
Check valve construction API 594 (general) / API 602 (forged ≀4") Specifying only valve type (swing/dual plate) without the governing standard and API 598 test requirement
Pressure-temperature rating ASME B16.34 P-T tables by material group Using class number as max pressure at all temperatures β€” misses thermal derating
Face-to-face / end-to-end ASME B16.10 Not called out β€” vendor supplies non-standard lay length that doesn't fit the spool
Flange dimensions ASME B16.5 (≀NPS 24) / B16.47 (>NPS 24) Calling B16.5 for large-diameter gate valves that fall under B16.47
Gaskets ASME B16.20 (metallic / spiral wound / RTJ) / B16.21 (soft) Wrong spiral wound ID/OD for the flange bore; wrong RTJ ring number for the class
Pressure testing API 598 + MSS SP-61 Calling only one β€” both may be required by the client specification
Marking and traceability MSS SP-25 Heat number not matched to CMTR β€” discovered at incoming inspection after delivery
Body material ASTM (A216, A351, A352, A182, A890, etc.) WCB specified for cold service (needs LCC/LF2); A105 for low-temp (needs A350 LF2)
API trim number API 600 / 602 / 594 trim table Trim 8 specified for continuous throttling globe valve β€” needs Trim 5 or 16 (FHF) for throttling duty
Body bolting ASTM A193 / A194 / A320 / A453 B7 in sour service (needs B7M/2HM); no low-temp rating on B7 (needs L7/7)
Fire test API 6FA (gate / globe / check β€” all types) Specifying API 607 for a gate or globe valve β€” API 607 is quarter-turn soft-seated only
Sour service NACE MR0175 (upstream) / MR0103 (refinery) Conflating the two standards; check valve spring material not NACE-reviewed
Fugitive emissions API 624 / ISO 15848 (packing) / MSS SP-117 (bellows seal) Not specified when environmental regulation requires VOC compliance

Practical Engineering Summary

Gate Valves

Isolate with minimal restriction. Stay-open or stay-closed service. Avoid throttling at all costs. Governed by API 600 / 602 / 603 + API 598 + ASME B16.34. Trim via API trim number β€” Trim 8 for general hydrocarbon.

Globe Valves

Regulate by controlled pressure loss. The control-valve foundation. Verify flow direction before sizing. Governed by API 602 + API 598 + ASME B16.34. Use Trim 5 or 16 (FHF) for continuous throttling duty.

Check Valves

Protect automatically and unforgivingly. Size for flow regime, not pipe size. Stability over low Ξ”P. Governed by API 594 + API 598 + ASME B16.34. Trim via API trim number β€” spring material must meet NACE in sour service.

If you understand these three deeply, everything else in valves makes sense.
The Complete Standards Stack for Gate, Globe & Check Valves
  • API 600 / 602 / 603 / 594 β€” valve type, construction, performance requirement
  • API 598 β€” testing baseline (shell test + seat leakage) β€” always required alongside the valve standard
  • ASME B16.34 β€” pressure-temperature ratings β€” always required
  • ASME B16.10 β€” face-to-face dimensions for interchangeability
  • ASME B16.5 / B16.47 β€” flange interface dimensions and P-T ratings
  • ASTM material standards β€” body, trim, and bolting chemistry and mechanical properties
  • MSS SP-25 / SP-61 β€” marking, traceability, and testing method details
  • API 6FA β€” fire safety for gate, globe, and check (not API 607)
  • NACE MR0175 / MR0103 β€” sour service restrictions when applicable

Specifying a Gate, Globe, or Check Valve?

Send the service conditions (media, pressure, temperature, Ξ”P), line size, valve role (isolation, regulation, or protection), API trim requirement, and required fail position β€” we'll come back with a sized recommendation including trim, bolting, end connection, and actuator style.

Knowledge Check

30 questions covering gate, globe, and check valve engineering, governing standards, body materials, API trim numbers, hardfacing, bolting, actuation, fire testing, sour service, and specification pitfalls.

Standard Gate / Globe / Check Valve Procurement

For standard gate, globe, and check valves plus accessories, E4 Industrial supports procurement through our e-commerce arm at Watermain Supply.

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E4 Industrial LLC is a Houston, TX-based industrial distributor. Watermain Supply is the e-commerce arm of E4 Industrial.