1. Aféierung
A check valve is a mechanical non-return device that regulates fluid flow to ensure unidirectional movement in pipelines and systems.
Its core functions include: preventing backflow-induced equipment damage (Z.B., pump impeller reversal), mitigating water hammer (pressure surges from sudden flow reversal), maintaining system pressure, and preventing cross-contamination between fluid streams.
Unlike active valves (Z.B., gate or ball valves), check valves operate autonomously, responding solely to changes in fluid pressure.
This simplicity makes them reliable in critical systems where failure could result in downtime, safety hazards, or environmental harm—statistics show that 23% of pump failures in industrial settings are attributed to unchecked backflow, underscoring their importance.
2. What Is a Check Valve?
A check valve is a pressure-actuated valve comprising a valve body, a closure element (Z.B., dier Déieren, BallUS, piston), and a seating surface.
Its defining feature is the ability to automatically open under forward pressure and close under reverse pressure.
The closure element is designed to seal tightly against the seat when flow reverses, with no external actuation required.
This passive operation eliminates the need for sensors, actuators, or human intervention, making check valves suitable for remote, hazardous, or inaccessible locations (Z.B., subsea pipelines 3,000 meters deep).
Check valves are classified by their closure mechanism and are engineered to accommodate specific flow rates (0.1 zu 10,000+ gpm), pressures (vacuum to 25,000 PSS), and temperatures (-450°F to 1,800°F), ensuring versatility across liquids, op d'gaangenen, and slurries.

3. How does a Check Valve Work
Check valves operate on the principle of differential pressure (ΔP) between the upstream (inlet) and downstream (outlet) sides:
- Opening Phase: When upstream pressure exceeds downstream pressure by a threshold known as the “cracking pressure”, the closure element is pushed off its seat, creating an orifice for flow.
Cracking pressure varies by design—spring-loaded check valves typically require 0.5–5 psi, while gravity-driven swing check valves may need 1–3 psi to overcome inertia. - Flow Phase: Once open, the closure element lifts to a maximum displacement (typically 10–20% of the pipe diameter), allowing fluid to pass with minimal pressure drop.
Streamlined designs (Z.B., ball check valves) achieve pressure drops as low as 1 psi op 50 gpm, while more restrictive piston designs may incur 3–5 psi drops. - Closing Phase: When upstream pressure falls below downstream pressure (reverse flow), the closure element is forced back onto the seat by reverse pressure, gravity, or spring tension.
Closure speed is critical—fast-closing lift check valves (<0.1 Sekonnen) reduce reverse flow volume by 70% compared to slow-closing swing check valves (0.5–1 second), minimizing water hammer risk.
Fluid properties influence operation: viscous fluids (Z.B., heavy crude oil) require lower cracking pressures to overcome internal friction, while abrasive slurries demand robust closure elements (Z.B., Stellite-coated discs) to resist wear.
4. Common Types of Check Valves
Check valves come in several designs, each tailored to specific flow conditions, installation constraints, and maintenance priorities.
Swing Check Valves
- Design: Features a hinged disc (or flap) that swings open under forward flow, pivoting on a pin or hinge mounted inside the valve body.
When flow stops or reverses, gravity pulls the disc back onto the seat, creating a seal.
Swing Check Valve - Schlëssel Metriken:
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- Flow capacity: Héichheet (Cv values 15–20% higher than lift check valves of the same size). A 6-inch swing check valve, zum Beispill, has a Cv of ~300, compared to ~250 for a 6-inch lift check valve.
- Closure time: 0.5–1 second (slower than other types, increasing water hammer risk).
- Size range: 2–48 inches (ideal for large-diameter pipelines).
- Virdeeler: Low pressure drop (1–2 psi at nominal flow) and cost-effectiveness for large-scale systems.
- Ufrongnisseuren: Unsuitable for vertical upward flow (gravity may prevent proper closure); prone to “slamming” in high-velocity systems, causing noise and wear.
- Uwendungen: Municipal water distribution, large-diameter oil/gas pipelines, and low-pressure industrial loops (Z.B., cooling water circuits).
Lift Check Valves
- Design: Uses a piston, dier Déieren, or plug that lifts vertically off the seat, guided by a stem or cage to ensure alignment.
Forward flow pushes the closure element upward, while reverse pressure (aided by gravity or a spring) forces it back down.
Lift Check Valve Parts - Schlëssel Metriken:
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- Leakage rate: <0.1 cc/min (metal-to-metal seats), achieving ANSI Class IV shutoff.
- Closure time: <0.1 Sekonnen (significantly faster than swing valves, reducing water hammer by 50%+).
- Size range: ½–12 inches (limited by manufacturing complexity for larger diameters).
- Virdeeler: Tight shutoff and suitability for high-pressure systems (wéi op 25,000 PSS).
- Ufrongnisseuren: Méi héije Drock erof (3–5 psi at nominal flow) due to the guided design.
- Uwendungen: High-pressure steam lines (1,500+ PSS), hydraulic systems, and pump discharge lines where backflow could damage impellers.
Spring-Loaded Check Valves
- Design: Integrates a coil spring that biases the closure element (disc or ball) against the seat.
The spring force determines the cracking pressure (minimum upstream pressure to open the valve), which can be adjusted by selecting springs with different tension ratings.
Spring Check Valve - Schlëssel Metriken:
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- Cracking pressure: 0.5–50 psi (customizable via spring selection).
- Orientation flexibility: Operates reliably in vertical, horizontal, or angled pipelines.
- Closure time: <0.1 Sekonnen (spring force accelerates sealing).
- Virdeeler: Prevents “fluttering” (rapid opening/closing) in low-flow systems; ideal for applications where gravity alone can’t ensure closure.
- Ufrongnisseuren: Higher pressure drop than non-spring designs (due to spring resistance); spring fatigue may occur in cyclic service (Z.B., 10,000+ Zymplen).
- Uwendungen: Pneumatic systems (Stonn, umtytsgen), fuel lines, and boiler feedwater circuits (vertical installation).
Ball Check Valves
- Design: Employs a spherical ball (typically stainless steel or plastic) that rests on a conical seat.
Forward flow lifts the ball, allowing fluid to pass around it; reverse flow pushes the ball back into the seat, creating a seal.
Ball Check Valves - Schlëssel Metriken:
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- Flow efficiency: Héichheet (Cv values 10–15% higher than piston lift check valves). A 2-inch ball check valve has a Cv of ~50, vs. ~45 for a 2-inch piston design.
- Abrasion resistance: Mëttelméisseg (metal balls outperform plastic in slurry service).
- Virdeeler: Low friction and minimal turbulence, reducing energy loss.
- Ufrongnisseuren: Plastic balls deform at temperatures >250° F; metal balls may stick in viscous fluids (Z.B., heavy oils).
- Uwendungen: Chemeschenverbriechen (low-viscosity fluids), food/beverage (sanitary designs with PTFE balls), and irrigation systems.
Pilot-Operated Check Valves
- Design: Combines a main check valve with a secondary “pilot” valve that controls the main valve’s opening.
The pilot uses external pressure (from the system or a separate source) to lift the main closure element, allowing flow only when pilot pressure is applied.
Pilot-Operated Check Valves - Schlëssel Metriken:
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- Control precision: Can be adjusted to open at specific pressure thresholds (±1 psi).
- Backflow prevention: Maintains seal even in systems with fluctuating downstream pressure.
- Virdeeler: Enables “locked” flow positions (Z.B., holding a hydraulic cylinder in place), preventing drift.
- Ufrongnisseuren: Complex design increases cost (2–3× that of standard check valves); requires compatible pilot pressure sources.
- Uwendungen: Hydraulic machinery (kranen, presses), where precise flow control and load holding are critical.
5. Key Performance Parameters and Metrics
- Cracking Pressure: Minimum ΔP to open the valve (0.5–50 psi). Critical for low-flow systems (Z.B., medizinesch Geräter) where unintended opening must be prevented.
- Pressure Drop: Energy loss across the valve, measured at nominal flow. Zum Beispill, a 2-inch swing check valve has a pressure drop of 2 psi op 100 gpm, while a lift check valve of the same size incurs 3 PSS.
- Leakage Rate: Amount of fluid bypassing the closed valve. Metal-seated valves typically achieve ANSI Class IV (0.01% of nominal flow), while soft-seated valves meet Class VI (<0.0005 mL/min per inch diameter).
- Closure Time: Time to seal after flow reversal. Spring-loaded valves close in <0.1 Sekonnen, reducing water hammer pressure spikes by 50% vs. swing valves.
- Cycle Life: Number of open/close cycles before failure. Stainless steel valves in clean service last 100,000+ Zymplen; Stellite-coated valves in abrasive service last 10,000+ Zymplen.
6. Material, Sealing Options, and Media Compatibility
The Zouverlässegkeet, service life, and safety compliance of a check valve are heavily influenced by the choice of body material, internal trim components, an an sealing elements.
Material selection must be based on fluid chemistry, operating temperature, Dréckt, and regulatory requirements.

Using an incompatible material can cause premature wear, Korrosioun, or seal failure — leading to leakage and unplanned downtime.
Body and Trim Materials
| Material | Max Service Temp (° F) | Korrosioun Resistenz | Staang | Ëffentlech Zeffen |
| Zoss | ~ 450 | Niddereg-moderéiert | Mëttelméisseg | Potable water, Hvac, low-pressure water lines |
| Ductile Eisen | ~ 450 | Mëttelméisseg | Higher than cast iron | Municipal water, fire protection |
| De Kolbel Stol (A216 WCB) | ~800 | Mëttelméisseg (not for strong acids) | Héichheet | Steam lines, UeleP & Gas |
| Edelstol 304 | ~1000 | Héichheet (general corrosion) | Héichheet | Iessen & Gedrénks, Waasserbehandlung |
| Stainless Steel 316/316L | ~1000 | Explaz vun engem exzellenten (Chorlungs-ugeglach, Aafsaachen) | Héichheet | Chemeschenverbriechen, Marine |
| Duplexex & Super Duplex | ~ 600 | Exceptional (Chorlungs-ugeglach, brine) | Vill héich | Offshore oil/gas, Desalung |
| Bronze/Brass | ~400 | Gutt (fresh water, mild seawater) | Mëttelméisseg | Marine, Hvac, Drénkwaasser |
| PVC / CPVC | ~200 (PVC), ~210 (CPVC) | Explaz vun engem exzellenten (most acids/bases) | Wéineg bannen | Chemical dosing, Ofwaasser |
| Pvdf (Kynar®) | ~280 | Explaz vun engem exzellenten (chlorine, strong acids) | Mëttelméisseg | High-purity chemical transfer |
Engineering Notes:
- Fir abrasive slurries, use hard-facing on seating surfaces (Stellite® or tungsten carbide).
- Fir hydrogen sulfide (H₂s) Ëmfeld, follow Gebuer MR0175 / ISO 15156 material requirements.
Seat and Seal Materials
The sealing element — elastomer or thermoplastic — determines leakage performance, chemical compatibility, and temperature limits.
| Seal Material | Max Service Temp (° F) | Chatikprobiste | Typical Use Cases |
| Ephm | ~300 | Excellent in water, Damp, mëllesäuren | Potable water, Hvac, Ofwaasser |
| Nbr (Salut) | ~ 250 | Good for oils, fuels | Hydrocarbon service, Luckricanten |
| FkM (Fasonton®) | ~400 | Excellent in solvents, Aafsaachen, fuels | Chemeschen & petrochemesch |
| PTFE (TEFLon®) | ~500 | Inert to almost all chemicals | High-purity chemicals, Iessen & Phirma |
| Metal-to-Metal | 1000+ | Limited by body material | High-temp steam, erosive service |
Industry Data:
- Metal-to-metal seats achieve ANSI Class IV or V shutoff in industrial service.
- Soft seats (elastomers) can achieve ANSI Class VI (bubbelfest) sealing but are limited by temperature and chemical compatibility.
Media Compatibility Considerations
- D'Waassermonn & Drénkwaasser — EPDM or NBR seats with cast iron, ductile Eisen, or stainless steel bodies. Nsf / Ansi 61 certification required.
- Seefakeefin & Brine — 316SS, duplex stainless, or bronze bodies; EPDM seals; avoid carbon steel due to rapid corrosion.
- Hydrocarbons & Fuels — NBR or FKM seals; carbon steel or stainless steel bodies.
- Strong Acids — PTFE seats and liners; 316Ss, Pvdf, or lined ductile iron bodies.
- Damp — Carbon steel or stainless bodies with metal-to-metal seats; EPDM acceptable for low-pressure steam (<300 ° F).
- Schlauen & Abrasives — Hardened seat materials, full-port ball check designs, wear-resistant coatings.
7. Industry Applications of Check Valve
Check valves are deployed across virtually every fluid-handling industry, with each application imposing unique requirements for Drock Klass, sealing performance, response speed, a materiell Kompatibilitéit.
Their primary purpose — preventing reverse flow — protects pumps, Kompressere, Pipelines, and downstream equipment, while ensuring system integrity and compliance with industry regulations.
D'Waassermonn & Wastewater Treatment
- Funktiounen: Prevent backflow from distribution networks into clean water sources, stop reverse siphoning in pumping stations, and protect membrane filtration units from pressure surges.
- Typical Configurations: Swing check valves for low head-loss in distribution mains; ball check valves in sludge and slurry lines; spring-assisted valves in high-rise building booster systems.
- Industry Data: According to AWWA C508, swing check valves in municipal water service typically operate at flow velocities of 2–15 ft/s and pressure ratings of 125–250 psi.
- Regulatory Standards: Nsf / Ansi 61 an an 372 for drinking water contact; AWWA C508/C509 compliance.
UeleP & Gas
- Funktiounen: Maintain directional flow in crude oil pipelines, prevent backflow into compressors, and isolate sections of offshore risers during shutdowns.
- Typical Configurations: API 6D swing or dual-plate check valves in transmission pipelines; axial-flow silent check valves to minimize water hammer in gas compression stations.
- Industry Data: Offshore subsea check valves are designed to API 6A an an Nace mr0175, with pressure ratings up to 20,000 PSS and temperature ranges from -75°F to +350°F.
- Key Requirements: Sour-service metallurgy, sand erosion resistance, and low closing times (<0.2 Sekonnen) for slam prevention.
Kraaft Generation
- Funktiounen: Prevent reverse steam or feedwater flow in turbines, protect boiler feed pumps, and maintain circulation in cooling water loops.
- Typical Configurations: Lift check valves for high-pressure steam lines; spring-loaded in-line valves in condensate return systems.
- Industry Data: ASME B31.1-compliant valves in fossil-fuel plants often handle steam at 2,400 psi and 1,050°F; feedwater check valves typically have Class 1500–2500 Drock Bewäertungen.
- Special Considerations: Metal-to-metal seats, Stellite® hard-facing, and quick-closure mechanisms to prevent turbine backspin.
Chemeschen & Petrochemesch
- Funktiounen: Prevent contamination between process streams, stop reverse chemical feed into storage tanks, and protect metering pumps.
- Typical Configurations: PTFE-lined swing or ball check valves for corrosive acids; stainless steel spring-loaded check valves for solvent transfer lines.
- Industry Data: Valves must often withstand pH 0–14 fluids, chlorine service at up to 150°F, or hydrochloric acid at 30–35% concentration.
- Regulatory Standards: Compliance with Api 594 for wafer-type valves, an an ASTM F1545 for PTFE-lined equipment.
Hvac & Building Services
- Funktiounen: Prevent reverse flow in chilled water and hot water loops, protect booster pumps, and stop backflow in fire protection systems.
- Typical Configurations: Silent check valves in vertical risers; wafer dual-plate check valves for space-constrained mechanical rooms.
- Industry Data: ASHRAE guidelines suggest low head-loss designs (<1.5 psi at design flow) for energy efficiency in HVAC loops.
Marine & Offshore
- Funktiounen: Prevent seawater ingress into cooling systems, stop reverse flow in ballast systems, and protect firewater pumps.
- Typical Configurations: Bronze or duplex stainless swing check valves for seawater service; axial-flow valves for offshore risers.
- Special Considerations: Resistance to chloride pitting (ASTM G48 testing), shock resistance per MIL-S-901D for naval applications.
Iessen & Gedrénks
- Funktiounen: Maintain hygiene by preventing product backflow, avoid contamination between CIP (propper-in-Plaz) and process lines.
- Typical Configurations: Sanitary clamp-end check valves with 316L stainless and EPDM or PTFE seats.
- Industry Data: Valves must meet 3-A Sanitary Standards an an FDA CFR 21 elastomer requirements; internal surface finishes of ≤32 μin Ra are common.
8. Advantages and Limitations
Advantages of Check Valves
- Autonomous Operation: No external power or controls, reducing failure points (99.9% reliability in clean service).
- Käschten-effikass: Lower upfront and maintenance costs vs. active valves (30–50% cheaper than automated control valves).
- Wëllzeechen: Adaptable to diverse fluids, pressures, and temperatures.
- Sécherheeten: Prevents equipment damage and environmental spills (critical in chemical processing, where backflow can release toxic substances).
Limitations of Check Valves
- Pressure Drop: Incurs energy loss (1–5 psi) that increases pumping costs in high-flow systems.
- Water Hammer Risk: Slow-closing designs (Z.B., swing valves) can cause pressure spikes up to 2× system pressure.
- Size Restrictions: Lift check valves are impractical for diameters >12 inches due to cost and weight.
- Ënnerhalt brauch: Prone to fouling in dirty fluids (Z.B., 25% of check valve failures in wastewater are due to debris buildup).
9. Standard, Certification
Check valves are not only mechanical components but also compliance-critical devices in many industries.
Their design, Kaflag vun der Fabréck, testen, and material selection are often governed by international, national, and sector-specific standards to ensure safety, performance reliability, and legal conformity.
| Ufank / Code | Rezierk | Key Requirements |
| API 6D / Iso 14313 | Pipeline valves for petroleum & natural gas | Design, Material, testen (hydrostatic, Gas), marking |
| Api 594 | Wafer-type & lug-type check valves | Face-to-face dimensions, pressure-temperature ratings |
| API 6A | Wellhead & Christmas tree equipment | Sour service, high-pressure oil & gas environments |
| Asme b16.34 | Valves — flanged, traedaded, and welding ends | Pressure-temperature ratings, material requirements |
| ASME B31.1 / B31.3 | Power piping & process piping | Inst Depalaat vum Installatioun, allowable stress, weld requirements |
| BS EN 12334 | Industrial metallic check valves | Design, Performech, and test procedures |
| AWWA C508 / C509 | Swing and resilient-seated check valves for waterworks | Zezeechnen, seat materials, performance criteria |
| MSS SP-125 | Grau Eisen & ductile iron check valves | Dimensions, Drock Bewäertungen |
| Iso 5208 | Pressure testing of metallic valves | Leakage rates (Class I–VI) |
10. Comparison with Other Valves
| D'Feature | Kontrollventil | Gate Ventil | Kugelventil | Drock Relief Ventil |
| Primärfunktioun | Prevents reverse flow automatically | Manual/motorized isolation | Quick on/off isolation, some throttling | Protects against overpressure |
| Operation Method | Pressure differential, self-acting | Manual or actuated stem | Quarter-turn manual/actuated | Spring or pilot-operated |
| Flow Direction | Unidirectional | Bidirektional | Bidirektional | Vents to atmosphere/return line |
| Flow Control Capability | Keen | On/off only | On/off + limited throttling | Keen (pressure-triggered) |
| Pressure Drop | Low–moderate (1–5 psi) | Very low | Very low | N / a |
Closing Speed |
0.05–1 s (type-dependent) | Liichte | Instant (¼ turn) | Instant upon setpoint |
| Typical Pressure Rating | Wéi op 25,000 PSS | ~2,500 psi | Wéi op 10,000 PSS | Up to system MAWP |
| Seal Performance | Class IV–VI | Class II–IV | Bubble-tight with soft seats | Leak to relieve pressure |
| Actuation Required | Nee | Jo (manual/motor) | Jo (manual/motor) | Nee (spring/pilot) |
| Typesch Uwendungen | Pump discharge, safety isolation from backflow | Pipeline Isolatioun | Isolation in oil/gas, Chemariantie | Boiler protection, safety systems |
| Maintenance Demand | Wéineg bannen | Low–moderate | Mëttelméisseg | Wéineg bannen |
| Special Features | Fully automatic | Full bore, low loss | Fast action, compact | Prevents catastrophic overpressure |
11. Check Valve Selection & Procurement Checklist
Before placing an order for a check valve, it is essential to comprehensively document all critical parameters to ensure the selected valve meets system requirements and operates reliably throughout its service life.
The following checklist outlines the key factors to record and evaluate:
Fluid Characteristics
- Identify the fluid type (d'Waassermonn, Damp, UeleP, Gas, Chemariantie, slurry, etc.).
- Document temperature range (minimum to maximum operating temperatures).
- Note any chemical properties such as corrosiveness, pH level, and presence of abrasives or contaminants.
Pressure Requirements
- Record the maximum operating pressure (MOP) under normal conditions.
- Verify the Maximum Allowable Working Pressure (MAWP) as per system design and safety margins.
Flow Rate and Hydraulic Performance
- Determine required flow rate to be handled by the valve (Z.B., gallons per minute or cubic meters per hour).
- Specify maximum allowable pressure drop across the valve, which relates to the desired flow coefficient (CV).
Leakage and Sealing Criteria
- Define maximum acceptable leakage rate according to seat class (Z.B., ANSI/FCI Class IV for low leakage or VI for bubble-tight sealing).
- Decide between soft or metal seating based on application demands.
Solids and Viscosity Considerations
- Assess if the fluid contains solids or particulate matter and their size.
- Evaluate fluid viscosity and its impact on valve operation and sealing.
Dimensional and Connection Details
- Confirm pipeline nominal size and required valve size.
- Specify connection type: fledelen (ANSI/ASME B16.5), traedaded, Socket Weld, butt weld, or other.
Installation and Orientation Constraints
- Document valve orientation requirements (horizontal, vertical, or inclined).
- Record face-to-face dimensions and available installation clearance to ensure fit and ease of maintenance.
Environmental and External Conditions
- Consider external environmental factors such as corrosion risks, exposure to weather, possibility of burial or subsea installation.
- Specify any special coatings, Material, or design features needed for harsh environments.
Standards and Certification Requirements
- Identify applicable industry standards (Api, ANSI, Iso, Asme) and regulatory certifications (NSF, PED, UL/FM, NACE).
- Ensure the valve meets all quality and compliance benchmarks relevant to the application.
Maintenance and Support Considerations
- Evaluate accessibility for routine maintenance, inspection, and repair.
- Confirm availability of spare parts, repair kits, and technical support from the supplier.
12. Conclusioun
Check valves come in various designs—from swing to pilot-operated valves—and serve a wide range of industries, from oil and gas to pharmaceuticals, Sécherheet assuréieren, Effizienz, an reguléierbar Interieur.
By understanding key performance factors, materiell Kompatibilitéit, and applicable standards, engineers can choose the right check valve to reduce downtime and extend system life.
As industry demands grow for higher pressures, Temperaturen, an Nohaltegkeet, check valves will continue evolving, with innovations like smart sensors and advanced manufacturing techniques further improving their performance.
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Faqs
What does a check valve do?
It stops backflow, protecting equipment and maintaining correct flow direction.
How to check PCV valve?
Remove it and shake — a working PCV valve usually rattles. Also check for vacuum at idle; no vacuum may indicate clogging.
What is the difference between a check valve and a control valve?
Check valves operate passively, allowing flow in one direction only, while control valves require external actuation to regulate flow rate, Dréckt, or direction.
Can check valves be installed vertically?
Jo, but spring-loaded designs are required to ensure closure (gravity alone may fail in vertical lines). Swing check valves should be mounted horizontally.
How do I select the right check valve for my system?
Consider fluid type (Viskositéit, abrasiveness), pressure/temperature, pipe size, and required cracking pressure.
For high-pressure, tight-shutoff applications, lift check valves are preferred; for large diameters, swing check valves offer better flow capacity.
What causes water hammer, and how can check valves prevent it?
Water hammer is caused by sudden flow reversal. Fast-closing check valves (Z.B., spring-loaded or lift designs) minimize reverse flow volume, reducing pressure spikes.
How long do check valves last?
In clean service, 10–15 years; in abrasive or corrosive environments, 3–5 years with proper maintenance. Material selection (Z.B., Hastelloy vs. De Kolbel Stol) significantly impacts service life.








