A dummy choke insert was ejected from a water injection (WI) tree by force of differential pressure, while divers were working nearby. A Dive team was removing a dummy choke insert and replacing it with a choke valve insert. The WI tree had been subject to hydrate remediation works. With no hydrates evident, limited trapped or pressurised gas was expected and tested barriers and isolations were in place. During the removal of the half shell clamps that retained the dummy choke insert, unexpected differential pressure from the flowline forced the dummy choke insert (85kg in water) out of the choke valve body at significant force. The two divers were loosening the clamp bolts around the dummy choke and were therefore close by when it ejected. Neither diver was in the direct line of fire; both were unharmed.
What went wrong
- During the design of the dummy choke insert, the decision was made not to include a test port, which would have allowed venting of any pressure built up in the flowline. The port was not part of the supplier’s standard design, and there was not enough time to approve a design change to include the port;
- The project procedure instructed that the Subsea Pressure and Monitoring Manifold (SPAMM) should be left closed, so there was no local vent path from the flowline;
- When pressure differentials in the system were noted prior to the dummy choke removal, there was no recognition that readings were not as expected, and no discussions within the team relating to venting off the remaining pressure;
- Based on previous experience at the tree, gas/fluid release had been identified as a hazard in the procedure and in the HIRA (Hazard Identification and Risk Assessment), however no parameters had been set as to the expected volume or duration of the release;
- Divers continued to work to loosen the clamp while gas/fluid was escaping from the choke, as the team had assumed that previous venting had been successful, and that they were safe to proceed;
- Our member notes that “the key point throughout was the failure to understand the exact pressure within the flowline, which was the residual 2 bar head of pressure from the riser after Floating Production Storage and Offloading (FPSO) venting”.
- Design safety in at the early engineering phase of a project – in this case, inclusion of a test port;
- Ensure procedures and risk assessments are clear, unambiguous, and explicit in their requirements (rather than leaving things vague, ambiguous and implicit). This is particularly important when dealing with a pressurised system and/or with stored energy;
- When using subsea pressure gauges, ensure any reading anomalies are well understood, communicated to the full team, and recorded. If the gauge is behaving in an anomalous way, swap it out;
- When ‘line of fire’ or ‘stored energy’ is identified as a hazard, ensure that control measures are specific in how these hazards will be managed so that personnel are in a safe position. Relevant control measures may include: hard barriers, safe havens, extended hand tools or use of rigging;
- When carrying out diver intervention works involving barriers and isolations, ensure all relevant parties have had comprehensive training in isolations and barriers;
- Divers and Dive Supervisors should confirm a local vent is open before starting any work on pressurised systems;
- If any step in a procedure doesn’t look right (e.g., local vent to be left closed when working on a pressurised system), STOP the JOB: Call an all stop and seek clarification.
Members may wish to refer to (focus here on differential pressure):
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