| Availability: | |
|---|---|
| Quantity: | |
DN65 CF8M Stainless Steel Single Flap Wafer Check Valve
Product Features
Single-disc Design: The valve disc has a simple structure and a fast response speed, and can effectively prevent the backflow of fluids.
Low Flow Resistance Design: The flow channel is unobstructed, with low fluid resistance, improving the system efficiency.
Compact Structure: It is small in size and light in weight, saving installation space.
Strong Corrosion Resistance: The CF8M material has excellent corrosion resistance and is especially suitable for media containing chloride ions.
Convenient Installation: The clamped connection method is convenient for installation and maintenance and is suitable for various piping systems.
Technical Parameters
Nominal Diameter: 1" ~ 40" (DN25 ~ DN1000)
Nominal Pressure: 150LB (PN16 ~ PN20)
Material: CF8M (316 cast stainless steel)
Applicable Media: Water, steam, oil, natural gas, corrosive liquids
Applicable Temperature Range: -20℃ ~ 200℃
Connection Method: Clamped type
Sealing Form: Metal seal or soft seal
Design Standards: API 6D, GB/T 12238, etc.
Face-to-Face Dimension: GB/T 12238
Application Scenarios
Chemical Industry: Used for transporting corrosive chemical media, such as acetic acid and phosphoric acid, to protect the piping system from corrosion.
Petroleum and Natural Gas Industry: In oil and gas transmission pipelines, it prevents the backflow of fluids and ensures the safety of the system.
Water Treatment Industry: Used in water supply and drainage systems to prevent the backflow of water and avoid water quality pollution.
Food and Pharmaceutical Industry: Used for transporting food-grade liquids or liquid medicines, ensuring the one-way flow of fluids and meeting hygiene standards.
Offshore Engineering: Applicable to seawater desalination equipment and ship accessories, with excellent resistance to chloride ion corrosion.
Shrinkage, gas porosity, sand and hot tears in cast steel valve bodies: what radiography, ultrasonic, magnetic particle and penetrant testing each can find.
Flash vessel design and flash steam recovery: flash fraction formula, Souders-Brown sizing, hold-up, LP header and deaerator routing, failure diagnosis.
Wet shaft and dry shaft butterfly valves: what reaches the bearing, which part wears first, and why the disc stops centering in the bore.
Steam trap selection: float, inverted bucket, thermodynamic and thermostatic types, sized on load times safety factor at true differential pressure.
Between the handle and the ball there are four fits. Which one shears, which one cracks, and how a few degrees of lost motion hides a valve that never seated.
Reverse flow through a check valve has six mechanical causes. How hinge wear, debris and a moved seat ring look different, and which test finds each.
Trapped-liquid overpressure in DBB/DIB ball valves: thermal expansion arithmetic, SPE vs DPE seats, external cavity relief valve setting and the fire case.
API 598 test durations by size, why the timer starts after the pressure settles, and what a 1.5 times shell test cannot tell you about service.
Pneumatic actuator failure modes and field diagnostics: air supply quality, diaphragm rupture, spring relaxation, torque margins and partial stroke testing.
How a butterfly valve disc is fixed to its stem: taper pins, pinless hubs and through shafts, the backlash each allows, and the failures they cause.
Steam PRV station design: critical pressure ratio, Kv sizing, 1/3-2/3 parallel turndown, series stations and safety valve sizing rules.
Why LNG ball valve seats that pass warm tests leak cold at -162°C: contraction arithmetic, cold preload, PCTFE vs PTFE, ISO 28921-2 and MSS SP-134 limits.
What API 607 proves: burn sequence, 7th-edition leak limits per NPS, cavity pressure rules, API 6FA vs ISO 10497, and the clauses buyers must check.
MSS SP-80 bronze valves: the class number is a saturated steam rating, not a pressure rating. Alloys, threads, lead-free rules and where bronze stops.
Stellite or tungsten carbide for erosive service: erosion angles, hardness ratios, HVOF vs weld overlay, the 500 C limit, and the clauses that win acceptance.
Valve coating is a defect-budget decision, not a product choice: ENP vs FBE vs sprayed aluminium, holiday arithmetic, CUI and the specs that win acceptance.
Temporary and start-up strainers for commissioning: placement, plate versus mesh, blowdown discipline and the removal record that proves it was pulled.
What MSS SP-25 marking really commits to: body symbols, three-symbol trim marking, melt identification and the certificate that closes the loop.
Why ball valves pass high-pressure seat tests and fail at 0.6 MPa: seat preload arithmetic, SPE and DPE seats, DBB vs DIB-1/DIB-2, and test-proofing specs.
RF, RTJ and butt-weld valve ends compared: how each joint seals, which duty suits it, and the four assembly errors that cause most joint leaks.