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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 />

undesired events, correspond<strong>in</strong>g <strong>to</strong> the upper horizontal l<strong>in</strong>e <strong>in</strong> the ALARP-pr<strong>in</strong>ciple. A<br />

s<strong>it</strong>uation is unacceptable and must be treated further if a Quant<strong>it</strong>ative Risk Assessment (QRA)<br />

reveals higher probabil<strong>it</strong>ies than accepted. The ALARP-pr<strong>in</strong>ciple shown <strong>in</strong> Figure 3-1 is<br />

commonly accepted. In the ALARP region add<strong>it</strong>ional efforts may be performed <strong>to</strong> reduce the<br />

risk further. A weigh<strong>in</strong>g of cost and risk is done.<br />

Unacceptable region<br />

The ALARP or Tolerabil<strong>it</strong>y<br />

region (Risk is undertaken only<br />

if a benef<strong>it</strong> is desired)<br />

Broadly acceptable region<br />

(No need for detailed work <strong>to</strong><br />

demonstrate ALARP)<br />

Negligible risk<br />

Figure 3-1 Levels of risk and the ALARP pr<strong>in</strong>ciple [32]<br />

Risk cannot be justified except<br />

<strong>in</strong> extraord<strong>in</strong>ary circumstances<br />

Tolerable only if risk reduction<br />

is impracticable or <strong>it</strong>s cost is<br />

grossly disproportionate <strong>to</strong> the<br />

improvement ga<strong>in</strong>ed<br />

Tolerable if cost of reduction<br />

would exceed the improvement<br />

ga<strong>in</strong>ed<br />

Necessary <strong>to</strong> ma<strong>in</strong>ta<strong>in</strong><br />

assurance that risk rema<strong>in</strong>s at<br />

this level<br />

3.2 Safety <strong>in</strong>tegr<strong>it</strong>y level (SIL)<br />

The Norwegian Oil Industry Association has provided recommended guidel<strong>in</strong>es for the<br />

application of IEC 61508 and IEC 61511 standards <strong>in</strong> the petroleum activ<strong>it</strong>ies on the<br />

Norwegian Cont<strong>in</strong>ental Shelf. A list of m<strong>in</strong>imum <strong>safety</strong> <strong>in</strong>tegr<strong>it</strong>y levels (SIL) for the most<br />

common <strong>safety</strong> functions has been provided. [28]<br />

SIL is a discrete level for specify<strong>in</strong>g the <strong>safety</strong> <strong>in</strong>tegr<strong>it</strong>y requirements of the <strong>safety</strong> functions.<br />

The SIL requirements are based on experience, w<strong>it</strong>h a design practice that has resulted <strong>in</strong> an<br />

adequate <strong>safety</strong> level. This reduces the need for time-consum<strong>in</strong>g SIL calculations on “standard<br />

solutions” and ensures a m<strong>in</strong>imum level of <strong>safety</strong>. Another advantage of us<strong>in</strong>g pre-determ<strong>in</strong>ed<br />

SIL is that these figures can be used as <strong>in</strong>put <strong>to</strong> a Quant<strong>it</strong>ative Risk Analysis (QRA) dur<strong>in</strong>g<br />

early design stages and thereby set between the risk analysis and the <strong>in</strong>tegr<strong>it</strong>y levels for<br />

important <strong>safety</strong> functions.<br />

For several <strong>safety</strong> functions <strong>it</strong> is difficult <strong>to</strong> establish generic def<strong>in</strong><strong>it</strong>ions. Due <strong>to</strong> process<br />

specific cond<strong>it</strong>ions, design and operational philosophies etc., the number of f<strong>in</strong>al elements <strong>to</strong><br />

be activated will differ from case <strong>to</strong> case. Consequently, several of the requirements are given<br />

on a sub-function level.<br />

It is important <strong>to</strong> emphasise that SIL requirements are m<strong>in</strong>imum values, and therefore need <strong>to</strong><br />

be verified w<strong>it</strong>h respect <strong>to</strong> the overall risk level. If the QRA reveals that the overall risk level is<br />

<strong>to</strong>o high, e.g. due <strong>to</strong> a particularly large number of high pressure wells or risers, then this could<br />

trigger a stricter requirement <strong>to</strong> one or more of the <strong>safety</strong> functions. Table 3-2 is found <strong>in</strong> ref.<br />

[28] and shows the quantification of the four different SIL levels. The SIL requirement applies<br />

only <strong>to</strong> a complete function, i.e. the field sensor, the logic solver and the f<strong>in</strong>al element. It is<br />

therefore <strong>in</strong>correct <strong>to</strong> refer <strong>to</strong> any <strong>in</strong>dividual <strong>it</strong>em or equipment hav<strong>in</strong>g a <strong>safety</strong> <strong>in</strong>tegr<strong>it</strong>y level.<br />

Diploma thesis, <strong>NTNU</strong> 2002<br />

9

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