well test analysis - fanarco will be felt at the well reservoir models a reservoir model is the...
TRANSCRIPT
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©K
APP
A 1
987-
00Well Test Analysis
Well Test Analysis, Theory
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APP
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987-
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Well Testing is Integral and Indispensable partof Reservoir Description and Management
Petrophysics/ LogsSeismic PVTCores/Geology
RESERVOIR MODEL ECONOMIC MODEL+DEVELOPMENT STRATEGY AND MANAGEMENT
=
RESERVOIR MODEL
INTERPRETATION
Well Tests
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APP
A 1
987-
00Well Test Objectives
Well Tests are conducted to :
•identify produced fluids and determine their respective volume ratios•measure dynamic reservoir pressure and temperature•obtain samples suitable for PVT analysis•determine well deliverability
PRODUCTIVITYWELL TESTING
DESCRIPTIVEWELL TESTING
evaluate reservoir parameters•evaluate completion efficiency•characterise well damage•evaluate workover or stimulation treatment•characterize reservoir heterogenities•access reservoir extent and geometry•determine hydraulic communication between wells
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APP
A 1
987-
00Interpretation Methodology
No
Yes
No
Yes
Data Validation
OKDifferentialPressure Analysis
DifferentialPressure Analysis
Identificationof
Validity
Choice of Flow period
Data Loaded
Generation of Diagnostic Plot
Pattern Recognition
Identification of Interpretation
Model
Consistency
Finalised
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APP
A 1
987-
00Types of Test
Drawdown Test
4 5 0 0
0 2 4 6 8 1 0 1 2
9 0 0
History plot (Pressure, Liquid Rate vs Time)
Description Well static, stable, shut in, open at constant flow rate
Advantages Good for limit testing as flow rate fluctuation is lesssignificant over long term
Disadvantages Difficult to make well flow at constant rateIf recently drilled, well may not be static or stable
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APP
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987-
00Types of Test
Build-up Test
4 5 0 0
0 2 4 6 8 1 0 1 2
9 0 0
History plot (Pressure, Liquid Rate vs Time)
Description Well flowing at constant rate, shut in
Advantages Constant flow rate easily achieved as it is zero
Disadvantages Difficult to make well flow at constant rateIf recently drilled, well may not be static or stable
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APP
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987-
00Types of Test
Injection Test
5 6 0 0
0 2 4 6 8 1 0 1 2
-1 0 0 0
0
History plot (Pressure, Liquid Rate vs Time)
Description Well static, stable, shut in, injection at constant rateConceptually identical to drawdown test
Advantages Better injection rate control than production rates
Disadvantages Complicated multiphase analysis unless reservoir fluid injected
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APP
A 1
987-
00Types of Test
Falloff Test
5 6 0 0
0 2 4 6 8 1 0 1 2
-1 0 0 0
0
History plot (Pressure, Liquid Rate vs Time)
Description Well injection at constant rate, shut inConceptually identical to build-up test
Advantages Constant flow rate easily achieved as it is zero
Disadvantages Complicated multiphase analysis unless reservoir fluid injected
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APP
A 1
987-
00Types of Test
Interference Test
4 9 6 5
4 9 8 5
3 8 1 3 1 8 2 3
History plot (Pressure, Liquid Rate vs Time)
Description One well is subjected to a drawdown, build-up,injection or falloff and pressure is observed in a different well or wells
Advantages Evaluates reservoir properties over a greater area
Disadvantages Requires very sensitive pressure recorders and maytake a long time
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APP
A 1
987-
00Types of Test
Isochronal Test
4 9 8 2
4 9 9 2
1 0 3 0 5 0 7 0
1 8 0 0
History plot (Pressure, Gas Rate vs Time)
Description For low productivity gas wells. Well flowed at four different rates of equal duration.Between each flow period, the well is shut in till staticconditions are reached.The last flow period is extended till stabilized flowing conditions are reached
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APP
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987-
00Types of Test
Modified Isochronal Test
4 9 6 5
4 9 8 5
5 1 5 2 5 3 5 4 5 5 5 6 5
1 8 0 0
History plot (Pressure, Gas Rate vs Time)
Description For low productivity gas wells. Well flowed at four different rates of equal duration.Between each period, the well is shut in for the same duration as the flow periodThe last flow period is extended till stabilized flowing conditions are reached
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APP
A 1
987-
00Well Test Analysis Principles
Reality Model
Reservoir Rock
Hydrocarbons
Faults
Pressure Plots
Mathematicalequations
Analysis
R&D
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APP
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Fluid flow in a porous medium is governed by:
Diffusivity Equation
Combining:
Darcy’s LawConservation of mass Diffusivity EquationEquation of state.
Conditions:- Reservoir is a homogeneous, isotropic, porous medium- Gravity effects can be neglected- Fluid is monophasic and of small and constant compressibility- The viscosity is constant- Pressure gradients are small- µ, ct, k and Φ are independent of pressure
}
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APP
A 1
987-
00Darcy’s law
Darcy’s Experiment
A h1
h2
h1-h2Water in
Water out
L
Manometer difference (h1 - h2)
Flow area A
Length L
Constant K
q = K Ah1 - h2
L
In Darcy’s experiment,on what did the fluid flow depend ?
more
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APP
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987-
00Darcy’s law
Darcy’s Law Linear Flow Oil Field Units
kAqµ887.2
xp −=
∂∂
Darcy’s Law Radial Flow Oil Field Units
khq
rpr µ2.141=
∂∂
Darcy, Henri-Philibert-Gaspard b. June 10, 1803, Dijon, Franced. Jan. 3, 1858, Paris
French hydraulic engineer who first derived the equation (now known as Darcy's law) that governs the laminar (nonturbulent) flow of fluids in homogeneous, porous media and who thereby established the theoretical foundation of groundwater hydrology.After studying in Paris, Darcy returned to his native city of Dijon, where he was entrusted with the design and construction of the municipal water supply system. During the course of this work, he conducted experiments on pipe flow and demonstrated that resistance to flow depended on the surface roughness of the pipe material, which previously had not been considered a factor. Planning to use the technique of water purification by filtration through sand, he also studied cases in which the pipe was filled with sand. From the data gathered, he derived the law that bears his name. The darcy is the standard unit of permeability.
Additional reading: http://www.philosophika.com/hofmann/DARCY.html
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APP
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987-
00Conservation of Mass
Mass can not be created or destroyed
What goes in = What comes out + What is left behind
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APP
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987-
00Conservation of Mass
mass in – mass out = accumulation = mass after – mass before
y∂x∂
z∂
x xx ∂+
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APP
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987-
00Equations of State
Single phase Liquid flow
Compressibility c = -
Single phase (non-ideal) Gas flow
PV = z n R T
1
V
dV
dP
The accumulation is governed by the EOS
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APP
A 1
987-
00Diffusivity Equation
Where p formation pressure, psi Φ porosityr radial distance to wellbore, ft ct total compressibility, psi-1t time, hr µ viscosity, cp∆p Laplace operator kr permeability, mD
The equation shows the influence of time and distance on the pressure
pck
tp
t
∆Φ
=∂∂
µ0002637.0General form in US field units
���
���
��
∂∂
∂∂
Φ=
∂∂
rpr
rrck
tp
t
10002637.0µ
Radial flow in US field units
2
2
0002637.0xp
ck
tp
t ∂∂
Φ=
∂∂
µLinear flow in US field units
conditions
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APP
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987-
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Boundary
Eventually the effects of the reservoir boundaries will be felt at the well
Reservoir Models
A reservoir model is the superposition ofreservoir, inner, and outer boundary conditions
Reservoir
After the well conditions, the reservoir determines the pressure behaviour
Well
The well test pressure behaviour starts with the well conditions
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APP
A 1
987-
00Defining the problem
���
���
��
∂∂
∂∂
Φ=
∂∂
rpr
rrck
tp
t
10002637.0µ
Initial condition ( ) iprtp == ,0
khQ
rpr
tr
µ2.141lim,0
=���
�∂∂
→
( )[ ] ir ptrp =∞→ ,lim
Well condition
Infinite condition
Line Source Well
conditions
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APP
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Dimensionless variables are introduced
• to simplify the reservoir models• to provide model solutions independent of units
These models incorporate physical variables such as pressure, distance, time. It would be futile to solve these problems for all combinations of variables.
Dimensionless Variables
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Permeability, viscosity, compressibility, porosity, formation volume factor and thickness are allconstant.
Dimensionless parameters are designed to eliminate the physical variables that affect quantitatively, butnot qualitatively, the reservoir response.
Dimensionless Variables
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APP
A 1
987-
00Dimensionless Variables
Dimensionless pressure
Dimensionless time
Dimensionless radius
And others
pkhqB
pD =1412. µ
∆
tk
c rtD
t w=
0 0002642
.Φ
∆µ
rrrDw
=
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APP
A 1
987-
00Diffusivity Equation
Re-writing the radial diffusivity equation (line source)in dimensionless terms
Well condition
( )p t rD D= =0 0,Initial condition
Boundary condition
���
���
��
∂∂
∂∂=
∂∂
D
DD
DDD
D
rpr
rrtp 1
1lim,0
−=���
�
∂∂
→ trD
DD
D
rpr
( )[ ] iDDDr trp 0,lim =∞→
The rate of pressure change is a function of some parametersand the curvature of the pressure around the point
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APP
A 1
987-
00Pressure Profile, Drawdown
- The distortion of the pressure profile when a well is openedand flowing (drawdown) is initially described by Darcy’s law.
- The “bending” of the pressure profile is concave, and the“diffusivity Equation” describes how quickly it will evolve within the reservoir
B25
Distance from the well
Pressure
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APP
A 1
987-
00Pressure profile, Build-up
- When the well is shut in, Darcy’s law shows that the profile is flat and “bent”around the wellbore, but unaltered away from the well
- This produces a pressure profile which is “convex” around the well, but still“concave” further out in the reservoir as the diffusion due to the previous drawdown continues
- For radial flow the inflexion point is a circle that moves away from the well asthe build up progresses
B25
Distance from the well
Pressure
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APP
A 1
987-
00Infinite Acting Radial Flow
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APP
A 1
987-
00Infinite Acting Radial Flow
Radial flow line
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APP
A 1
987-
00Solving the line source problem
Solved in Laplace space and inverted analytically
( ) ���
�−−=D
DiDDD t
rEtrp42
1,2
( ) ���
���
��
Φ−−−=kt
rcEkhQptrp t
ii
21.9486.70, µµ
���
� +≈ 80907.0ln21,100
22
D
DD
D
D
rtp
rtfor
Infinite Acting Radial Flow, the Semilog Approximation
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APP
A 1
987-
00Skin Effect
Skin is an additional pressure change due to heterogenities close to the wellbore
It is a deviation from the ideal inflow.
Possible causes
Pressure drop from undamaged flowing pressure (+ve skin)•Invasion of mud filtrate or cement during drilling or completion•Non-ideal perforations - too low shot density - plugged•Limited entry - partial penetration•Limited entry - partial completion•Turbulent gas flow
Pressure increase from undamaged flowing pressure (-ve skin)•Acidization or stimulation
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APP
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987-
00Skin Effect
Partial Penetration Partial Completion
Skin factor due to the partial penetration or partial completion depends on penetration ratio and the distance zw from the bottom of the reservoirh
hw
h hw
zw
hw
hzw
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APP
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987-
00Skin Effect
Positive skinDamaged well
Negative skinImproved well
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APP
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987-
00Skin Effect
Skin Factor
Skin factor is a variable used to quantify the magnitude of the skin effect
It is a dimensionless variable
SkhqB
ps=1412. µ
∆
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APP
A 1
987-
00Wellbore Storage
When we open the master valve at the beginning of a welltest, the well may produce at a constant rate at the surface.
However, the flow rate from the reservoir in to the wellbore may not be constant at all.
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APP
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987-
00Wellbore Storage or Afterflow
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APP
A 1
987-
00Wellbore Storage or Afterflow
During the wellbore storage effect
Pressure is linear function of time
∆ ∆p C t=
Where C is the Wellbore storage coefficient
CC
c r hDt w
=0 8936
2
.φ
Dimensionless wellborestorage constant
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APP
A 1
987-
00Infinite Acting Radial Flow
.
Once the wellbore storage effects are over,
and before outer boundary effects are detected,
the reservoir acts as if it were infinite
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APP
A 1
987-
00Infinite Acting Radial Flow
The Semi-log Approximation
( ) [ ]p t t SD D D= + +12
0 80907 2ln .
Replacing dimensionless variables
p pqB
kht
kc r
Swf it w
= − + + −� �162 6
08686 3 22752
.log log . .
µµΦ
( )p pqB
kht
kc r
Si wft w
− = + + −� �162 6
08686 322752
.log log . .
µµΦ
This is the equation of a straight line with slope = 162 6. qB
khµ
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APP
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987-
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Infinite Acting Radial Flow MDH Analysis
MDH Plot - used for analyzing 1st drawdown in a test sequence
( )p pqB
kht
kc r
Si wft w
− = + + −� �162 6
08686 322752
.log log . .
µµΦ
∆ p m
mqBkh
=162 6. µ
khqBm
=162 6. µ
Sp pm
kc r
i hr
t w=
−− +� �1151 32271
2. log .Φµ
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APP
A 1
987-
00Principle of Superposition
Principle of Superposition
The response of a system to a number of perturbations is exactly equal to the sum of the responses to each perturbation as if they were present by themselves
In well test analysis, the Principle of Superposition in Time allows us to determine the reservoir response to a well flowing at a variable rate by using only constant rate solutions
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APP
A 1
987-
00Principle of Superposition – Build-up
Build-up Superposition
4 2 0 0
5 1 5 2 5 3 5
9 0 0
History plot (Pressure, Liquid Rate vs Time)
5 7 0 0
5 1 5 2 5 3 5
-1 0 0 0
0
History plot (Pressure, L iquid Rate vs Time)
4 5 0 0
5 1 5 2 5 3 5
9 0 0
History plot (Pressure, Liquid Rate vs Time)
+ =
1000 STB/DFlow rate
For all 36 hours
1000 STB/DInjection
For last 24 hours
1000 STB/DFlow for 12 hours
Build-up for 24 hours
The well is producing at q until time tp, we want to find the pressure at time (tp+∆t)- As equations are linear (not normally true) we can usethe principle of superposition
The pressure change due to a combination of previous production periods is equal to the superposition of individual changes due to each production phase
- The shut-in pressure at time (tp+ ∆t) is mathematically equivalent to a continuation of the drawdown at rate q, combined with an injection at rate -q from time tp
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APP
A 1
987-
00Principle of Superposition – Build-up
flowrate
pressure
pi
∆PDD
∆t∆PBU
timeinjection (-q) from time tptp
tp
drawdown (q) from time 0
-q
q
Build-up Superposition
The well is producing at q until time tp, we want to find the pressure at time (tp+∆t)- As equations are linear (not normally true) we can usethe principle of superposition
The pressure change due to a combination of previous production periods is equal to the superposition of individual changes due to each production phase
- The shut-in pressure at time (tp+ ∆t) is mathematically equivalent to a continuation of the drawdown at rate q, combined with an injection at rate -q from time tp
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APP
A 1
987-
00Principle of Superposition – Build-up
Build-up Superposition
flowrate
pressure
pi
∆PDD
∆t∆PBU
timeinjection (-q) from time tptp
tp
drawdown (q) from time 0
-q
q ( ) ( ) ( )p p t p t t p tD D pD D pD D D DBU= − + −[ ]∆ ∆
( )p p
qBkh
k t tc r
k tc rWS i
p
t W t W= −
+−�
���
�
�
��
��
1412 12 2 2
.ln ln
µµ µ
∆Φ
∆Φ
( )p p
qBkh
t ttws i
p= −
+162 6.log
µ ∆∆
This is the equation of a straight line with slope =162 6. qB
khµ
tp
The well is producing at q until time tp, we want to find the pressure at time (tp+∆t)- As equations are linear (not normally true) we can usethe principle of superposition
The pressure change due to a combination of previous production periods is equal to the superposition of individual changes due to each production phase
- The shut-in pressure at time (tp+ ∆t) is mathematically equivalent to a continuation of the drawdown at rate q, combined with an injection at rate -q from time tp
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APP
A 1
987-
00
Infinite Acting Radial FlowHorner Analysis
Horner Plot - used for analyzing a build-up after a constant rate Dd
mqBkh
=162 6. µ
khqBm
=162 6. µ
( )p p
qBkh
t ttws i
p= −
+162 6.log
µ ∆∆
( )log
t tt
p + ∆∆
Sp p
mtt
kc r
hr wf p
p t w=
−+
+�� �� − +
�
���
��
11511
3 22712. log log .
Φ µ
If reservoir is truly infinite, extrapolated p*=pi
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APP
A 1
987-
00Principle of Superposition – Multi-rate
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APP
A 1
987-
00Principle of Superposition – Multi-rate
( )p t t pqBkh
q qq q
t t tmr n ii i
n nj
j
n
i
n
( ).
log log+ = −−−
−� �−−
− =
−
=
−
∆ ∆ ∆ ∆162 6 1
1 1
1
1
1µ
Expanding the build-up superposition technique for multiple rate changes, the equation with the semi-log approximation is
m Superposition Function