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Well Barriers                                                219


              the fluid barrier becomes the priority, and must be carried out before
              operations resume. Failure of the secondary barriers is contained by acti-
              vating shear and blind rams (tertiary barrier).



              6.2.1 Mechanical barriers
              Mechanical barriers must be verified by pressure testing. Where possible,
              the test should be in the direction of flow. Closed barriers are usually
              tested when they are first installed. Normally, open barriers should be
              tested at the time of installation and then at intervals in accordance with
              regulatory requirements. For example, in the United Kingdom and
              Norwegian sectors of the North Sea, Christmas tree valves are normally
              integrity tested every six months.
                 There are several types of mechanical barrier elements, these include:
             •  Production packer (annulus barrier).
             •  Tubing hanger seals (annulus barrier). Hanger seal integrity is tested
                via ports in the wellhead and by performing an annulus pressure test.
             •  Wellhead annulus valves (or Valve Removal (VR) plugs in the side
                outlet bore).
             •  Drilling, coiled tubing, and wireline BOPs.
             •  Plugs. Some operating companies will only consider a mechanical
                plug equipped with chevron seals to be a barrier if it can be tested in
                the direction of flow. This is because a chevron seal (V-packing) can
                only hold pressure in one direction. Most plugs are dressed with two
                sets of seals, one for each direction of flow. Testing in one direction
                only tests part of the seal stack. Solid slab seals solve this problem, but
                are not available for all wireline set plugs.
             •  Tubing or wireline retrievable SCSSSV. There are many conflicting
                views about the use of downhole safety valves as a well control barrier.
                However, many operating companies permit the use of the SCSSSV,
                providing it can be inflow tested in the direction of flow. Safety valve
                acceptance is normally based on a zero leak rate rather than the API
                permissible leak rate of 400 cc/minute for liquids or 15 scf/minute
                    2
                gas. Ideally, a small differential pressure from below is needed to keep
                the flapper seated. However, the risk of dropped objects must be con-
                sidered, since the closed flapper valve in a safety valve does not have
                the resilience of, e.g., a wireline set bridge plug.
             •  Annulus SCSSSV.
             •  Surface controlled downhole “lubricator valve.”
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