Oil & Gas×Check Valves

Check Valves for Oil & Gas

Check valves in oil and gas service prevent reverse flow that could damage compressors, pumps, wellhead trees and production separators. Vajra Industrial Solutions supplies API 594 dual plate wafer check valves, API 6D swing check valves, and tilting disc non-return valves in carbon steel, LTCS and stainless steel — fully certified for hydrocarbon, sour gas and high-pressure gas pipeline service.

Key Applications — Check Valves in Oil & Gas

Pipeline Compressor Station Check Valves

On gas compression stations, check valves prevent reverse flow through idle compressor trains. Any reversal under high differential pressure would spin the compressor backwards at destructive speed. Dual plate spring-loaded check valves with fast closure characteristics are specified to minimise reverse flow before full closure.

DN150–DN600 | ASME Class 600–900 | ASTM A216 WCB / LTCS LCB | Dual Plate Spring | API 594 / API 6D | NACE MR0175

Wellhead and Christmas Tree Non-Return Valves

Check valves on wellhead Christmas trees and flowlines prevent blowback during well shut-in and workover operations. Compact high-pressure piston or ball check valves are used in small instrumentation and chemical injection lines; full-bore swing and dual plate checks handle production flowlines.

DN25–DN200 | Class 1500–2500 | ASTM A182 F316L / Duplex 2205 | API 6A / API 6D | H₂S service NACE MR0175

Pump Discharge Non-Return (Oil Transfer and Injection)

On crude oil transfer and water injection pump skids, check valves on pump discharge headers prevent backflow through idle pump units. Tilting disc check valves or spring-loaded dual plate checks are preferred for low-slam, fast-response closure that prevents water hammer in high-pressure water injection systems.

DN50–DN400 | Class 300–600 | ASTM A216 WCB / SS316 | Tilting Disc or Dual Plate | API 594 | ASME B16.34

Flare Header Non-Return Valves

Check valves on flare sub-headers and knockout drum inlet lines prevent backflow from the main flare header during upset conditions. Backflow into process areas creates fire and explosion risk. Swing check valves in low-pressure flare header duty must operate reliably at very low differential pressures (50–200 mbar).

DN200–DN900 | Class 150 / PN10–25 | ASTM A216 WCB | Swing Check | API 594 / ASME B16.34 | Sour Service NACE

Required Certifications

API 6DAPI 594ASME B16.34NACE MR0175 / ISO 15156API 598 (pressure testing)EN 10204 3.1 MTRsATEX / IECEx (offshore)

Recommended Materials

ASTM A216 WCB — Carbon steel body/disc for general oil and gas, dry gas, non-sour service
ASTM A352 LCB / LCC — Low-temperature carbon steel for arctic and cold-climate pipelines
ASTM A351 CF8M (SS 316) — Stainless steel for wet sour gas, MEG injection, chemical injection lines
Duplex 2205 (A890 4A) — Offshore topsides, chloride-bearing produced water, high H₂S service
ASTM A217 WC6 — Chrome-moly alloy for high-temperature gas plant and refinery service
ASTM A182 F51 / F53 — Duplex and super duplex forgings for compact high-pressure check valves

Selection Factors

Anti-slam / water hammer: On high-pressure injection systems and compressor stations, specify spring-loaded dual plate or tilting disc check valves with fast controlled closure — swing checks have slower closure that allows higher reverse flow velocity before slam
Sour service (NACE): Any check valve in H₂S-bearing streams must meet NACE MR0175 / ISO 15156 hardness and material requirements — body, disc, hinge pins, and springs all must comply; standard WCB may not meet requirements
Low cracking pressure: Flare header check valves must open at very low forward differential (as low as 5–50 mbar) — specify low-cracking-pressure disc geometry and light hinge springs; heavy springs prevent opening at these low DPs
Pigging compatibility: If the pipeline is piggable, specify full-bore check valves with no internal protrusions that could obstruct pig passage; reduced-bore and dual plate designs obstruct pigs
Pressure class selection: API 6D defines pressure class for pipeline check valves — Class 150 (PN20 equivalent) for gathering lines; Class 600–900 for transmission pipelines; Class 1500–2500 for wellhead and Christmas tree service
End connections: Butt weld ends preferred for high-pressure pipeline duty (no flange leakage path, lower weight); flanged RF for process plant; ring joint (RTJ) for Class 600+ pipeline service

Technical FAQs

What is the difference between API 594 and API 6D check valves?
API 594 covers wafer and wafer-lug check valves — compact, face-to-face short design that fits between standard flanges, primarily for process plant and general industrial service. API 6D specifically governs pipeline check valves — longer body, full-bore designs for oil and gas transmission and distribution systems. API 6D check valves have more stringent testing (extended shell test duration, seat leakage Class A with zero measured leakage for gas service), and are required on pipelines covered by DOT/PHMSA regulations in the USA and equivalent regulators elsewhere. For upstream production and process plant: API 594 or API 6D (either is acceptable depending on client specification). For custody transfer and mainline transmission: API 6D is mandatory.
When should a tilting disc check valve be specified instead of a swing check valve?
Tilting disc check valves are preferred over swing checks in three scenarios: (1) Water hammer prevention — the tilting disc geometry closes faster than a full-bore swing check because the disc centre of gravity is ahead of the pivot axis, providing inherent closing torque; (2) High-pressure oil and gas service where slam damage to the seat is unacceptable — the controlled disc tilt provides soft seating; (3) Vertical pipeline installation — swing checks require near-horizontal flow to stay open; tilting disc designs work in vertical upward flow because the disc tilts with the flow. Standard swing checks remain preferred for low-pressure, horizontal pipelines in water and general service where cost is the primary driver.
What cracking pressure should be specified for check valves in oil and gas service?
Cracking pressure (minimum forward differential to open the disc) varies by application: Pipeline mainline check valves: 0.05–0.1 bar cracking pressure to open reliably at low flow; Pump discharge: 0.1–0.3 bar cracking; Compressor discharge (high-pressure gas): 0.5–2 bar acceptable — the compressor will always produce enough differential; Flare header service: specify 0.01–0.05 bar cracking pressure — flare headers operate at near-atmospheric pressure; for very low-cracking duty, use flap check valves with lightweight discs and minimal or no springs. Vajra's check valve datasheets state cracking pressure per design; request specific cracking pressure as a purchase specification if it is critical to your system design.

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