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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.
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.
| 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 β€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 |
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 |
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.
Before separating gate and globe valves, understand what they share. Most real-world failures happen in the shared components, not the closure element.
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.
Provides access to internals and seals the body opening. Bonnet design directly affects pressure rating, fugitive emissions performance, and serviceability.
A major leak risk. Design options: bolted gasketed joint, welded joint, and pressure seal joint. ASME B16.34 governs the design envelope for each.


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

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.
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.
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.
The most common design β API 600
Wedge angle produces sealing force. Tighter closure increases seat stress. Sensitive to thermal expansion.
Variants:
Used in: steam service, refinery block valves, utility isolation.
No wedging stress

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.
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.
Cuts through solids and slurry

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.
Gate valves use the API trim number system (Trim 1β18) 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 |
| 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 |

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.
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.
Small sizes. Low pressure. Infrequent operation.
Large diameters. High thrust. Reduce operator effort at large sizes and high pressures.
Precise positioning. High thrust. Thermal binding is a key sizing input. AUMA, Rotork, Limitorque type.
Extremely high thrust in a compact package. Used for ESD, pipeline, and large-diameter service. Common for API 6D gate 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.

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.
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.
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.
Best throttling. Highest pressure drop. The classic globe valve geometry. Use where flow regulation is the primary requirement.
Replaces an elbow. Useful where piping turns 90Β°. Reduces one fitting and one potential leak point in the system.
Reduced pressure drop vs T-pattern. Preferred when throttling and efficiency both matter β offshore, high-pressure steam, where ΞP budget is constrained.

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.
Flow proportional to stem position. Used where system pressure drop is largely constant β easier to control in stable ΞP systems.
Equal increments of travel produce equal percentage changes in flow. The dominant trim for control valves on variable-ΞP systems β used in most refinery and process control loops.
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 |
Globes trade efficiency for control and stability.

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 ΞP.
Lower opening thrust. Stable control. Standard orientation for most globe control valves. Disc is pushed open by flow β actuator works with the process.
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.
Small sizes, low ΞP service, infrequent operation.
Used for isolation or coarse control. Slower response than pneumatic. Common for remote on/off globe valves.
Most common for modulating control service. Smooth force delivery, fast response, inherently fail-safe. The control valve standard.
High thrust in compact package. Used for high ΞP control and tight-shutoff globe valves. Faster than diaphragm at large sizes.
Automatic protection with no second chances. No operator, no control system β only physics.

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.
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.
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 2β4 ft/s depending on design β verify with the manufacturer's minimum velocity curve.
Gravity-assisted closure β API 594

Used in: pipelines, low-velocity systems where slam can be managed.
Spring-assisted wafer β API 594

Used in: process piping where space is limited and pigging is not required.
Spring closes before reversal

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

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

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.
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 ΞP with stable operation is always better than a low-ΞP unstable valve that fails in months. Always obtain and verify the manufacturer's minimum velocity curve before selecting.
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 150β600 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 (β€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 |
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 ΞP 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 ΞP 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. | ||
For full actuation coverage including pneumatic / electric / hydraulic / electro-hydraulic architectures and the actuator selection decision tree, see the Valve Actuation reference β
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.
| Specification Item | Governing Standard | Common Miss |
|---|---|---|
| Gate valve construction | API 600 (large cast) / API 602 (forged β€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 β€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 (β€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 |
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.
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.
Protect automatically and unforgivingly. Size for flow regime, not pipe size. Stability over low ΞP. Governed by API 594 + API 598 + ASME B16.34. Trim via API trim number β spring material must meet NACE in sour service.
Send the service conditions (media, pressure, temperature, ΞP), 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.
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.
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