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Is it necessary to install a downhole safety valve in a subsea ... - NTNU

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Reliabil<strong>it</strong>y data dossier<br />

Component: Tub<strong>in</strong>g hanger seals, wellhead seal and cas<strong>in</strong>g hanger seals<br />

Failure rate<br />

(10 -6 /hours)<br />

Failure mode<br />

Data source/comment<br />

0.62 Leakage, EXL Reliabil<strong>it</strong>y of well completion<br />

equipment - Phase II p.18.<br />

Operational time 2403.71 years,<br />

failures 13.*<br />

Recommended values for calculations:<br />

Failure rate (10 -6 /hrs):<br />

EXL: 0.6<br />

Test<strong>in</strong>g and ma<strong>in</strong>tenance:<br />

The Tub<strong>in</strong>g hanger and cas<strong>in</strong>g hanger seals are never tested. Repair and replacement would require<br />

a well workover.<br />

Comments and leakage paths:<br />

The tub<strong>in</strong>g hanger failure rate is approximated <strong>to</strong> be identical <strong>to</strong> the cas<strong>in</strong>g hangers. The tub<strong>in</strong>g<br />

hanger is component tested <strong>in</strong> the “Reliabil<strong>it</strong>y of well completion equipment - Phase II”<br />

rapport. The leakage is though the seals at the cas<strong>in</strong>g/ tub<strong>in</strong>g hanger and <strong>in</strong><strong>to</strong> the annulus or<br />

wellhead.<br />

* The value does not <strong>in</strong>clude <strong><strong>in</strong>stall</strong>ation failures (i.e. failure occurr<strong>in</strong>g dur<strong>in</strong>g the first six days<br />

after <strong><strong>in</strong>stall</strong>ation).<br />

D-4

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