| 1 | Match the pressure rating | API 6A nominal working pressure classes include 2,000, 3,000, 5,000, 10,000, 15,000, and 20,000 psi, where applicable to the selected equipment configuration. | Compare the valve’s rated working pressure with the maximum anticipated wellhead, choke-manifold, kill-line, or standpipe pressure. Do not select a valve based only on normal operating pressure. | Pressure containment failure, leakage, equipment damage, or serious personnel exposure. |
| 2 | Verify API 6A compliance | API Specification 6A addresses wellhead and Christmas-tree equipment, including design, materials, pressure testing, documentation, and product identification requirements. | Request a current certificate or declaration of conformity, product datasheet, applicable API 6A edition, manufacturing records, pressure-test reports, and traceable identification markings. | Unverified equipment may not meet the required design, testing, or traceability controls. |
| 3 | Select the correct PSL and PR level | API 6A uses Product Specification Levels (PSL) to define quality and verification requirements, while Performance Requirement Levels (PR) address functional and environmental performance. | Confirm the required PSL and PR in the project specification. Check whether the valve is qualified for the expected pressure, temperature, cycling, and service conditions. | A valve can have the correct pressure rating but still lack the required quality or performance qualification. |
| 4 | Check temperature and material class | API 6A defines temperature classes and material classes for equipment exposed to different operating environments. The applicable range depends on the specific class and design. | Match the valve’s temperature class and material class to ambient temperature, fluid temperature, sour-service requirements, corrosion risk, and any applicable project material specification. | Seal degradation, brittle fracture, corrosion, or loss of pressure integrity. |
| 5 | Confirm connection and bore dimensions | Common connection details include nominal size, flange or threaded end type, pressure class, bore configuration, and applicable dimensional standards. | Verify nominal size, end connection, flange dimensions, bore size, bolt pattern, face-to-face length, flow direction, and compatibility with the existing drilling-fluid line. | Installation delays, forced modifications, misalignment, restricted flow, or connection leakage. |
| 6 | Evaluate flow and backflow control | Check-valve performance depends on flow direction, cracking pressure, pressure drop, closing response, fluid density, solids content, and the selected disc or piston design. | Request flow-capacity data for the actual drilling-fluid or well-control service. Confirm allowable pressure drop, minimum flow for stable opening, reverse-flow tightness, and resistance to erosion. | Unstable operation, excessive pump load, water hammer, premature wear, or inadequate backflow prevention. |
| 7 | Review testing, documentation, and maintenance access | Pressure tests should be performed using documented procedures, suitable test fluids, calibrated instruments, and acceptance criteria defined by the applicable specification and purchase requirements. | Confirm hydrostatic and functional test records, material certificates, seal information, spare-part availability, inspection intervals, repair instructions, and a clear maintenance procedure. | Difficult troubleshooting, extended downtime, undocumented integrity, or unsafe field repairs. |