In This Article
- 1.Why Valve Testing Standards Exist
- 2.Types of Tests Required
- 3.API 598 Test Pressures and Durations
- 4.ISO 5208 Leakage Rate Classes
- 5.Material Traceability and Documentation
- 6.Third-Party Inspection (TPI) Witness Testing
Why Valve Testing Standards Exist
A valve that leaks internally (across the seat) or externally (through the body, bonnet, or gland) in service can cause product loss, process upsets, safety hazards, and regulatory non-compliance. Factory testing per recognised standards gives the buyer confidence that the valve will perform as specified. The three dominant standards are: API 598 (Valve Inspection and Testing) — the North American benchmark published by the American Petroleum Institute; ISO 5208 (Industrial valves — Pressure testing of metallic valves) — the international standard harmonised with EN 12266; and BS 6755 Part 1 — the British standard, now largely superseded by ISO 5208 for export valves but still specified by some UK-origin projects.
Types of Tests Required
- Shell (Hydrostatic Body) Test: Verifies structural integrity of the valve body, bonnet, and all pressure-containing parts; conducted at 1.5x the 38°C (100°F) pressure-temperature rating with the valve half-open and both ends closed; no visible leakage permitted
- High-Pressure Seat (Closure) Test: Verifies the seating element can hold pressure; typically conducted at 1.1x the CWP (cold working pressure) with pressure applied from one side, then the other; accepted leakage depends on valve type and leakage class
- Low-Pressure Seat Test (API 598 / EN 12266-1): Conducted at 0.6 MPa (87 psi) air or nitrogen to detect seat leakage — particularly relevant for soft-seated valves with elastomeric seating
- Backseat Test (Rising Stem Globe and Gate Valves Only): Verifies that the backseat can isolate the stuffing box from process pressure — allows gland repacking under pressure; tested at 1.1x CWP with stem fully open and outlet closed
- Pneumatic Shell Test (Optional): Conducted at 0.6 MPa air when hydrostatic test is not feasible — valve is submerged in water or coated with leak-detection fluid; zero leakage required; API 598 permits as alternative for small-bore valves or when liquid contamination is unacceptable (e.g. oxygen service)
API 598 Test Pressures and Durations
| Test Type | Test Medium | Test Pressure | Duration (NPS ≤ 2") | Duration (NPS 2.5"-6") | Duration (NPS ≥ 8") |
|---|---|---|---|---|---|
| Shell Hydrostatic | Water | 1.5 x rated CWP at 38°C | 15 s | 60 s | 120 s |
| High-Pressure Seat | Water or air | 1.1 x rated CWP | 15 s | 60 s | 120 s |
| Low-Pressure Seat | Air or N2 (0.6 MPa) | 0.6 MPa (87 psi) | 15 s | 60 s | 120 s |
| Backseat (where applicable) | Water | 1.1 x rated CWP | 15 s | 60 s | 120 s |
ISO 5208 Leakage Rate Classes
ISO 5208 defines leakage acceptance criteria by lettered classes. Higher letter = tighter (lower) permitted leakage. The engineer specifies the required class in the valve datasheet or purchase order.
| ISO 5208 Class | Max. Leakage Rate | Typical Application |
|---|---|---|
| A (Zero leakage) | No visible leakage; zero drops for liquid, zero bubbles for gas | Cryogenic, toxic gas, oxygen service; fire-safe applications |
| B | 0.006 ml/min per mm NPS for liquid | General process valves — API 6D ball and gate valves (soft-seated) |
| C | 0.018 ml/min per mm NPS for liquid | Metal-seated valves — API 6D Class B equivalent |
| D | 0.11 ml/min per mm NPS for liquid | Metal-seated butterfly and gate valves in less critical service |
| EE (gas) | 0.006 ml/min per mm NPS as gas | Gas isolation valves — ASME Class 150-300 metal-seated |
| FF (gas) | 0.18 ml/min per mm NPS as gas | Standard gas valve seat test |
| G | 1.8 ml/min per mm NPS for liquid | Loose metal-seated valves; throttling valves |
Material Traceability and Documentation
- EN 10204 Type 3.1 Mill Test Report (MTR): Material properties of the actual heat of steel used for pressure-containing parts — chemical composition and mechanical properties certified by the steel mill's authorised inspection representative; required for ASME Section VIII, PED, and most API-spec valves
- EN 10204 Type 3.2: Mill test report countersigned by an independent, accredited third-party inspection body (TUV, Bureau Veritas, Lloyds) — required on nuclear, critical offshore, and some defence projects
- Positive Material Identification (PMI): On-site XRF or OES analysis of valve body and trim materials per API 578 — required for alloy valves (SS, duplex, Inconel, Hastelloy) to prevent material mix-up
- Hydrostatic Test Report: Record of actual test pressures, durations, temperature, test medium, and inspector name — forms part of the valve data book or dossier
- Certificate of Conformance (CoC): Manufacturer's declaration that the valve was manufactured and tested in accordance with the specified standard(s) and purchase order requirements
Third-Party Inspection (TPI) Witness Testing
For critical applications — offshore platforms, nuclear facilities, LNG terminals, high-alloy valves — purchasers often appoint a Third-Party Inspection (TPI) agency such as Bureau Veritas, SGS, Intertek, or TUV to witness factory hydrostatic and seat tests. The TPI inspector verifies that test equipment is calibrated, test pressures and durations meet the specified standard, and results match the reported documentation. Vajra Industrial Solutions arranges TPI witness testing for export orders requiring third-party certification.
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