Is it necessary to install a downhole safety valve in a subsea ... - NTNU
Is it necessary to install a downhole safety valve in a subsea ... - NTNU
Is it necessary to install a downhole safety valve in a subsea ... - NTNU
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<strong>Is</strong> <strong>it</strong> <strong>necessary</strong> <strong>to</strong> <strong><strong>in</strong>stall</strong> a <strong>downhole</strong> <strong>safety</strong> <strong>valve</strong> <strong>in</strong> a <strong>subsea</strong> oil/gas well?<br />
7 Conclusions and recommendations for further<br />
work<br />
7.1 Conclusions<br />
The overall objective has been <strong>to</strong> determ<strong>in</strong>e whether or not a DHSV should be <strong><strong>in</strong>stall</strong>ed <strong>in</strong><br />
a <strong>subsea</strong> oil/gas well from a risk po<strong>in</strong>t of view. A conclusion is presented <strong>in</strong> this section.<br />
Based on the quant<strong>it</strong>ative f<strong>in</strong>d<strong>in</strong>gs <strong>in</strong> this study the DHSV reduces the risk of blowout<br />
w<strong>it</strong>h approximately 50%. A removal of the DHSV represents an <strong>in</strong>creased failure<br />
probabil<strong>it</strong>y, and two <strong>in</strong>dependent and tested well barriers are not present <strong>in</strong> all cut sets.<br />
None of the cut sets do, however, violate a required SIL3 level when the DHSV is<br />
removed from the completion.<br />
The blowout frequency caused by the DHSV dur<strong>in</strong>g workover is 1.7E-4 per well year,<br />
and 8.5E-5 per well year for a well w<strong>it</strong>hout a DHSV. The blowout frequency dur<strong>in</strong>g<br />
production is based on the assumption that all occurrences of the ‘TOP’-event, “leakage<br />
<strong>to</strong> the surround<strong>in</strong>gs”, classify as a blowout. Dur<strong>in</strong>g production the blowout frequency is<br />
found <strong>to</strong> be 4.47E-3 per well year for a well w<strong>it</strong>h a DHSV, and 1.85E-2 per well year<br />
when the DHSV is removed. In add<strong>it</strong>ion <strong>to</strong> the blowout frequency dur<strong>in</strong>g production and<br />
workover a blowout frequency caused by accidental events should be <strong>in</strong>cluded. The <strong>to</strong>tal<br />
blowout frequency is found add<strong>in</strong>g up the different contributions:<br />
f<strong>to</strong>tal = fproduction + f<strong>in</strong>tervention + (faccidential event * MFDTaccidential event)<br />
The DHSV blowout frequency contribution dur<strong>in</strong>g <strong><strong>in</strong>stall</strong>ation is not <strong>in</strong>cluded <strong>in</strong> this<br />
study. There is no data reveal<strong>in</strong>g the changes <strong>in</strong> blowout frequency when the DHSV is<br />
removed for the <strong><strong>in</strong>stall</strong>ation phase.<br />
The blowout frequencies found <strong>in</strong> the calculations are of very high. In <strong>to</strong>tal a removal of<br />
the DHSV <strong>in</strong>creases the blowout frequency by 1.13E-2 per well year. It is reasonable <strong>to</strong><br />
believe that the calculations <strong>in</strong> this report are e<strong>it</strong>her based on <strong>in</strong>sufficient data, a bad<br />
model or calculated errors. Other fac<strong>to</strong>rs may also have contributed <strong>to</strong> the high frequency.<br />
An alternative calculation method based on the proportion of the frequencies of the<br />
‘TOP’-events, and the experience data found <strong>in</strong> ref.[7] is applied. In the new calculations<br />
a removal of the DHSV will <strong>in</strong>crease the blowout frequency of 3.0E-5 per well year. The<br />
author f<strong>in</strong>ds this result more reasonable.<br />
50% of the shut-<strong>in</strong>s of a well lead<strong>in</strong>g <strong>to</strong> a workover are caused by a DHSV failure. A<br />
DHSV failure requires a workover generat<strong>in</strong>g a loss of oil production of up <strong>to</strong> $5,6<br />
million. In add<strong>it</strong>ion there will also be expenses concern<strong>in</strong>g the rental of a workover rig. A<br />
<strong>to</strong>tal cost of 20 million dollars per <strong>in</strong>tervention is therefore not unrealistic.<br />
The author cannot recommend remov<strong>in</strong>g the Downhole <strong>safety</strong> <strong>valve</strong> (DHSV) from a<br />
<strong>subsea</strong> oil/gas production well based on the f<strong>in</strong>d<strong>in</strong>gs <strong>in</strong> this thesis. Although there may be<br />
some economic advantages <strong>in</strong> remov<strong>in</strong>g the DHSV the risk of blowout should be given<br />
the greatest attention. In add<strong>it</strong>ion <strong>to</strong> caus<strong>in</strong>g pollution, the occurrence of a blowout may <strong>in</strong><br />
severe cases lead <strong>to</strong> a bad reputation among consumers and environmental organisations.<br />
Diploma thesis, <strong>NTNU</strong> 2002<br />
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