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THE PRESSURE DERIVATIVE

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Tom Aage Jelmert NTNU

Department of Petroleum Engineering and Applied Geophysics

THE PRESSURE DERIVATIVE

The pressure derivative has important diagnostic properties. It is also important for making type curve analysis more reliable. The field curves may be matched against two type curves rather than one. The logarithmic pressure derivative has the advantage of being dimensionwise consistent with pressure. Hence they may be displayed in the same coordinate system.

Drawdown

During radial flow the following equation applies:

      + + = ∆ S r c kt kh B q p w t wf ln 0.809 2 4π ϕµ 2 µ

The above equation will show up as a straight line on a ∆pwf versus ln t plot. This implies that the logarithmic pressure derivative will be constant.

t d p d wf ln ∆ = kh B q π µ 4

The above equation will show up as a horizontal line in any coordinate system. By use of the chain rule the logarithmic derivative may be expressed in terms of the time derivative: dt p d t t d p d wfwf = ∆ ln

During the wellbore storage period storage period the following equation applies:

s wf C

qBt p = ∆ The logarithmic derivative becomes:

s wf C qBt t d p d = ∆ ln

which is the same right hand side as for the pressure difference, ∆p.

Flow period diagnostics is best done in a log-log coordinate system. Taking the logarithm on both sides of the above equation yields:

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[ ] C t qB p s wf log log ' log ln = + ∆

The above equation will show up as a straight line with slope one.

Wellbore storage followed by radial flow has a characteristic shape on diagnostic (log – log) plot which is shown below.

Figure 1:Pressure and pressure derivative diagnostic plot for drawdown

This example illustrates the diagnostic properties of the pressure derivative. The wellbore storage may be recognized as a straight line with unit slope and the radial flow period will show up as a horizontal line.

Buildup

The dimensionless pressure change for build up is:

pDBU = pD(∆tD)− p tD(D+ ∆tD)+p tD( )D

Suppose there are two simultaneous radial flow periods. Then the buildup may be described by the modified Horner equation

) 2 809 . 0 ) ( (ln 4 cr2 t t S t kt kh B q p p w t p BU + + + ∆ = ∆ ϕµ π µ

where ∆pBU = pwspwf . The pressure difference is illustrated below. Note that pwf is the last recorded flowing pressure.

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Figure 2: The development of ∆PBU with time. One may define an equivalent time:

t t t t t p p e + ∆ = ∆

Substitution of the equivalent time into the buildup equation yields: ) 2 809 . 0 (ln 4 cr2 S t k kh B q p w t e BU + + ∆ = ∆ ϕµ π µ

Observe that the above equation has the same appearance as the corresponding drawdown equation. The pressure derivative becomes:

kh B q t d dp e w π µ 4 ln∆ =

which will plot like a horizontal line.

Immediately after the well has been closed, fluid will continue to flow into the well. This phenomenon has been called afterflow. From the definition of equivalent time, we conclude that for small values of shutin time, there is essentially no difference between the shutin time, ∆t, and equivalent time, ∆te,. Hence:

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Suppose the well was closed during a radial flow period. Then the dimensionless buildup equation during afterflow will simplify to:

1 ln 2 pD D D DBU sD pD t t t p C t + ∆ ∆ = −

Note that the latter term is essentially be zero for small values of ∆t. Hence the buildup equation during afterflow is the same as for wellbore storage during a drawdown test. D DBU SD t p C ∆ = The equivalent dimensional equation becomes: BU S qB p t C ∆ = ∆

The above equation will show up as a straight line with unit slope on a log-log plot. The diagnostic plot for a transition from afterflow to radial flow is shown below.

Figure 3: The buildup diagnostic plot has the same appearance as for drawdown. For an old well, the condition that shutin time is small in comparison with the

production time is valid during the entire test, then the buildup equation will simplify to:     + + ∆ = ∆pBU q B ln k t 0.809 2s ϕµ π µ

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The transition between wellbore storage and radial flow will show up as the previous curves when plotted against the shutin time ∆t.

Figure 4: Pressure and pressure derivative for buildup in an old well, t>> ∆ t

Derivation algorithm

A derivative is usually approximated by a finite difference quotient. As such it is sensitive to noise. Some smoothing may be necessary to filter out high frequency noise.

Most numerical filters depend on an even sampling rate. This is rarely the case in well testing. For a non-even spacing between sampled the points, the derivative may be approximated by the slope of a least square line through neigbouring points. All points in the interval contribute to the computed derivative.

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Figure 5: Schematic of a 7 point least square filter

An alternative algorithm uses three points only, the point of interest, one to the left and one to the right.

Figure 6: Schematic of a derivation algorithm

The derivative is approximated as the weighted average between the left and right hand slopes. 1 2 2 2 1 1 x x p x x p p d ∆ + ∆ ∆ ∆ ∆ + ∆ ∆ ∆ =     ∆

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A smaller difference, ∆x, on the horizontal axis leads to a better approximation of the derivative. Hence the highest weight factor is applied to the finite difference quotient with the smallest difference ∆x.

It is recommended to start with consecutive points. If the degree of noise is

unacceptable, then the distances ∆x1 and ∆x2 have to be increased. The points 1 and 2 are selected as the first points such that

∆x1, ∆x2 ≥ L If x = ln ∆te , then L t t i ≥ 2 ln . and L t ti ≥ 1 ln

L has been called the smoothing parameter. The degree of smoothing will increase with increasing smoothing parameter. On the other hand, the accuracy of the derivative approximation will decrease. Hence L should be kept as small as possible. Experience has shown that L ≈ 0.2 is often a natural choice.

Any derivation algorithm has a problem near the ends of the interval. The calculation scheme is then running out of points. This phenomenon has been called the end effect of the pressure derivative. These regions have to be treated separately. One solution is to reduce the smoothing parameter close to the ends of the intervals.

References

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