| Size: | |
|---|---|
| pressure: | |
| Availability: | |
| Quantity: | |
3" 150LB A351 CF8 Stainless Steel Flange Globe Valve
Technical Parameters
Nominal diameter: 1/2" ~ 36" (DN15 ~ DN900)
Pressure rating: 150LB ~ 2500LB (PN20 ~ PN420)
Applicable temperature: -20℃ ~ 300℃
Applicable media: water, steam, oil products, natural gas, acid gases, etc.
Materials:
Valve body: A351 CF8
Valve cover: A351 CF8
Valve disc: A351 CF8
Valve stem: 304 or 316 stainless steel
Sealing surface: Stainless steel or hard alloy
Connection method: Flanged connection, in compliance with ANSI B16.5 standard
Operation mode: Manual (handwheel operation), with optional electric or pneumatic actuators
Design standard: ASME B16.34
Structural length: In compliance with ASME B16.10 standard
Testing standard: API 598
Product Features
Strong corrosion resistance: The A351 CF8 material has excellent corrosion resistance and is suitable for a variety of corrosive media.
Reliable sealing: Adopting a wedge-shaped valve disc design, it has reliable sealing performance and a long service life.
Flanged connection: In compliance with ANSI B16.5 standard, it is convenient for installation and has good sealing performance.
Easy operation: Equipped with a handwheel operating mechanism, it can be opened and closed quickly and operated flexibly.
Multiple options: Electric or pneumatic actuators can be equipped according to customer needs to achieve automated control.
Standards compliance: The design and manufacturing comply with ASME B16.34 standard, and the testing complies with API 598 standard.
Application Areas
Petroleum and natural gas industry: Used in oil and gas transmission pipelines to control the flow of media such as oil and natural gas.
Chemical industry: Suitable for the control of corrosive media in chemical production.
Water treatment industry: Used in water supply and drainage systems to control the opening and closing of water flow.
Energy industry: In the cooling water system and steam system of power stations, it ensures the reliable transmission of media.
Food and pharmaceutical industries: Suitable for the control of clean fluids in the food and pharmaceutical industries.
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.
Why PTFE and PFA liners fail when the chemistry is right: permeation arithmetic, vacuum collapse, cold flow and the 11:1 expansion mismatch at the flange.
C95800 and C95500 are cast to ASTM B148; C63200 is wrought to ASTM B150. Aluminum and manganese levels decide strength, weldability and valve use.
Jacket heat load arithmetic, sulfur's 159 C viscosity trap, the separate jacket pressure test and the weld failures buyers discover in year five.
API 603 and API 600 both cover bolted bonnet gate valves, but wall thickness basis, class ceiling and casting rules decide which one you can actually buy.
ISO 5208 Rates A-G explained with real numbers, how API 598, API 6D and FCI 70-2 map across, and what metal seats can honestly achieve.