| Availability: | |
|---|---|
| Quantity: | |
2" 150LB Stainless Steel A351 CF8 Flange End Swing Check Valve
Design Features
Swing Type Structure: The valve disc rotates around the axis of the valve seat, with quick opening and closing actions, low fluid resistance, and can effectively prevent the backflow of media.
Full Bore Design: The passage inside the valve body is consistent with the inner diameter of the pipeline, ensuring the smooth flow of media, reducing pressure loss, and improving the overall efficiency of the system.
Reliable Sealing Performance: The valve disc and valve seat are precisely machined and use high-quality sealing materials to ensure a good sealing effect under normal working pressure and prevent media leakage.
Strong Corrosion Resistance: The stainless steel of A351 CF8 material has excellent anti-corrosion performance, can resist the erosion of various chemical media, extend the service life of the valve, and reduce maintenance costs.
Compliance with International Standards: Its design and manufacture comply with international standards such as API 6D and BS 1868, ensuring the quality and reliability of the product and meeting the engineering specification requirements of different countries and regions.
Technical Parameters
Nominal Diameter: 1/2" ~ 48" (DN15 ~ DN1200)
Pressure Rating: 150LB ~ 2500LB (PN20 ~ PN420)
Applicable Temperature: -29℃ ~ 300℃
Applicable Media: Non-corrosive and weakly corrosive media such as water, oil, and natural gas.
Connection Method: Flange connection (RF)
Design Standards: API 6D, BS 1868
Testing Standards: API 598
Flange Standards: ASME B16.5, ASME B16.47
Face-to-Face Dimension Standards: ASME B16.10
Application Fields
It is widely used in the piping systems of industries such as petroleum, chemical engineering, natural gas, water treatment, shipbuilding, and offshore engineering to prevent the backflow of media, ensure one-way flow of fluids, and guarantee the safe operation of the system. For example, it prevents the backflow of oil products in petroleum transmission pipelines and controls the flow direction of corrosive media in the chemical production process.
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.