| Availability: | |
|---|---|
| Quantity: | |
Stainless Steel 1PC Reduce Bore FNPT X MNPT Thread Ball Valve
Product Features
Strong Corrosion Resistance: Made of 304 or 316 stainless steel, it can resist the corrosion of various chemical media and is suitable for multiple fluid media such as water, oil, gas, and acidic liquids.
Compact Design: With a single-piece structure, it is small in size and convenient for installation in pipeline systems with limited space.
Reliable Sealing: Equipped with high-quality PTFE sealing materials, it ensures a good sealing effect even under low pressure.
Quick Opening and Closing: Quick opening and closing can be achieved by rotating the handle by 90 degrees, and it is easy to operate.
Multiple Thread Options: One end is female NPT (FNPT) and the other end is male NPT (MNPT). The thread standard is NPT. Users can choose the appropriate thread type according to actual needs.
Blowout-Proof Stem Design: Equipped with a blowout-proof stem to ensure the operational safety under high-pressure conditions.
Technical Parameters
Size Range: 1/4"~4" (DN6~DN100)
Working Pressure: 1000WOG
Working Temperature: -20℃~180℃ (-4°F~302°F)
Valve Body Material: 304 or 316 stainless steel
Sealing Material: PTFE
Connection Method: One end is female NPT (FNPT) and the other end is male NPT (MNPT).
Design Standards: Comply with international standards such as ANSI B16.34 and API 608.
Testing Standards: API 598
Application Fields
Industrial Field: In industries such as petroleum, chemical engineering, and pharmaceuticals, it is used to control the flow of various fluid media.
Municipal Engineering: In urban water supply and drainage systems, it is used to control the distribution and transportation of water.
Shipbuilding Industry: In the cooling water system, fuel oil system, etc. of ships, it is used to ensure the normal operation of ships.
Food and Beverage Industry: Due to its good hygienic performance, it can be used for fluid control in food processing and beverage production.
HVAC: Used to control the flow of media such as cooling water and hot water to ensure the normal operation of the system.
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.