It is virtually almost impossible to determine the hinge pin condition, without actually looking at the valve internal.
X-ray (with any composition)
--> from side (cross sectional circle of pin), the 'ray' have to penetrate body, hinge housing, pin itself. No one knows on what depth the over-clearance exist between the hinge and its housing
--> from front. Exact location of the hinge? Answer same as above.
First have to determine the failure mode (assuming that there are no back flow surge):
1. Are you sure no Differential Pressure (or minimum), when it is deemed to fail? No DP meaning that Check valve supposed to be close
2. When it is close, what is the leakage rate (ISO 5208)? Is it class D, G, or streaming like waterfall? or like most older design, you cannot measure pressure built up between the pump and the check valve.
Some NDE approach:
a. Some Check valve have hinge that are connected to visible bearing from the outside.If this is leaking, then either the hinge, and or sealing is damage. IF NOT
Condition should be applied: Assurance of leaking, Pressure pushes from downstream (backflow) is bigger than upstream, assuming valve is close.
b. Ultrasonic leak detector (subjective measurement by operator), find the area where biggest leak occurs
c. X-ray (Cobalt) on that area
d. Assess the contact between disc and seat. If lucky, you may even see some crack.
If crack visible and valve do close (seat and disc are mating), then that is your failure mode and not the hinge
If gape exist, then most likely either the valve's hinge or some tracing becomes hardened and block the valve from closing.
Shall this is the main pump which working almost all the time, thus Check valve remains Open for a long time. Then it is likely the hinge became fatigue.
If this is a critical pump, mind as well classify the same critical rank for Check valve subjected for periodic maintenance (visual inspection required).
Or else like many recent application in offshore field. Apply API 521, double jeopardy Check valve configuration.
Regards,
MR
Greenfield and Brownfield have one thing in common; Valve(s) is deemed to "run to fail" earlier shall compared to other equipments