production system analysiss3.amazonaws.com/noteswap-sid-1/2/5/0/4/25045dd60dbfc3d...production...
TRANSCRIPT
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Production System Analysis
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Production System Analysis
Nodal Analysis
• An analytical tool used in forecasting the performance of the various elements comprising the completion and production comprising the completion and production system. This concept is based on the a well having one flow rate implied by fixed end pressures.
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Nodal Analysis
• This procedure consist of selecting a division
point (node) in the well and dividing the
system at this point.
•The locations of the
most commonly used
nods are shown:
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Nodal Analysis
• Once a node is selected, i.e. bottom hole
pressure, the pressure is calculated from both
directions (upstream and downstream from
the node). the node).
– Inflow to the node:
– Outflow from the node:
noderppp )components (upstream =∆−
nodeFWHppp )components m(downstrea =∆+
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Nodal Analysis
• The pressure drop, Δp, in any component
varies with flow rate, q. Therefore, a plot of
node pressure versus flow rate will produce
two curves, the intersection of which will give two curves, the intersection of which will give
the conditions satisfying requirements 1 and
2, given previously. The procedure is
illustrated graphically in Fig. 1-3.
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Determination of Flowing Capacity
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Nodal Analysis
• Using a simple producing system and selecting
the wellhead as the node
– Inflow to the node:
pppp =∆−∆−
– Outflow from the node:
whtbgresrpppp =∆−∆−
whflowlinesep ppp =∆+
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node
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• The effect of the flow capacity of changing the
tubing size and the effect of a change in
flowline size.
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Nodal Analysis
• Frequently used is the procedure to select the
node between the reservoir and the piping
system.
– Inflow to the node:
– Outflow from the node:
whresrppp =∆−
wftbgflowlinesep pppp =∆+∆+
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•The effect of a change in tubing size on the
total system producing capacity when pwf is the
node pressure.
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•A case in which the well performance is controlled by
the inflow is below. In this case, the excessive pressure
drop could be caused by formation damage or
inadequate perforations.
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•A qualitative example of selecting the optimum
tubing size for a well that is producing both gas
and liquids is shown below
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Procedure for Apply Nodal Analysis
1. Determine which components in the system can be
changed. Changes are limited in some cases by
previous decisions. For example, once a certain hole
size is drilled , the casing size and , therefore, the
tubing size is limited.tubing size is limited.
2. Select one component to be optimized.
3. Select the node location that will best emphasize the
effect of the change in the selected component. This
is not critical because the same overall result will be
predicted regardless of the node location .
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Procedure for Apply Nodal Analysis
4. Develop expressions for the inflow and outflow .
5. Obtain required data to calculate pressure drop
versus rate for all the components. This may require
more data than is available, which may necessitate
per- the analysis over possible ranges of conditions.
6. Determine the effect of changing th e characteristics
of the selected component by plotting inflow versus
outflow and reading the intersection.
7. Repeat the procedure for each component that is to
be optimized.
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Reservoir Performance
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WELL PERFORMANCE EQUATIONS
• To calculate the pressure drop occurring in a
reservoir, an equation that expresses the
energy or pressure losses due to viscous shear
or friction forces as a function of velocity or or friction forces as a function of velocity or
flow rate is required. Although the form of the
equation can be quite different for various
types of fluids, the basic equation on which all
of the various forms are based is Darcy's law.
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• Linear Flow (constant area flow)
– Oil
– Gas
×+
×=−
−
− 2
2132
321
1008.9
10127.1 A
LBq
Ak
LBqpp oo
o
o
ooo
βρµ
×+
=−
−
2
16
22
2
2
1
10247.193.8
A
LZTLq
Ak
LTZqpp
g
sc
g
sc
γβµ– Gas
+
=−221
Aq
Akqpp sc
g
sc
p1 = upstream pressure, psia Z = gas deviation factor
p2 = downstream pressure, psia T = flowing temperature, oR
μo = oil viscosity, cp γg = gas gravity (air=1)
Bo = oil formation volume factor, bbl/stb qsc= gas flow rate, scf/day
L = Length of flow path, ft μg = gas viscosity, cp
Ko = permeability of oil, md Kg = permeability of gas, md
= velocity coefficient, ft-1 A = area open to flow, ft2
qo = oil flow rate, stb/dayβ
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• Radial Flow
–Oil
–Gas
SrrB
pphkq
weoo
wfeo
o +
−=
)/ln(
)(00708.0
µ
)(10703 6
wfRg pphkq
−×=
−
–Gas
pe = pressure at r=re, psia Z = gas deviation factor
pwf = well flowing pressure, psia T = flowing temperature, oR
μo = oil viscosity, cp pR = avg. reservoir pressure, psia
Bo = oil formation volume factor, bbl/stb qsc= gas flow rate, scf/day
ko = permeability of oil, md μg = gas viscosity, cp
rw = wellbore radius, ft Kg = permeability of gas, md
re = well drainage area, ft h = reservoir thickness, ft
qo = oil flow rate, stb/day qsc = gas flow rate, Mscfd
S = skin factor
)/472ln(.
)(10703
weg
wfRg
scrrZT
qµ
−×=
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Linear Flow Radial flow
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Productivity Index (J)
• The relationship between well inflow rate and
pressure drawdown has often been expressed
in the form of a Productivity Index J,
q
wfR
o
pp
qJ
−=
qo = oil flow rate, stb/day
pR = avg. reservoir pressure, psia
pwf = well flowing pressure, psia
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Permeability Alteration and
Turbulence
• The magnitude of the pressure change due to the skin and turbulence, defined as:
SBqp ooo
′=∆
µ2.141
• A value for S’ (skin factor due to permeability change) can be obtained from analysis of various types of pressure transient tests.
hk
SBqp
o
oooskin
′=∆
µ2.141
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Factors Affect Productivity Index
• Phase Behavior in Reservoirs
• Relative Permeability Behavior
• Oil Viscosity Behavior
• Oil Formation Volume Factor Behavior• Oil Formation Volume Factor Behavior
–
scsc T ,p ,conditions stock tankat oil of Volume
T p,at gas dissolved its plus oil of Volume=oB
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Phase Behavior Diagram
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Relative Permeability Behavior
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Oil Viscosity Behavior
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Oil Formation Volume Factor Behavior
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Factors Affecting Inflow Performance
• For oil reservoirs
1. Decrease in kro as gas saturation increases.
2. Increase in μo as pressure decreases and gas is
evolved.evolved.
3. Shrinkage of the oil as gas is evolved when pressure
on the oil decreases.
4. Formation damage or stimulation around the well
bore
5. An increase in the turbulence as oil flow rate
increases.
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Drive Mechanisms
• The source of pressure energy to cause
the oil and gas to flow into the well bore
has a substantial effect on both the
performance of the reservoir and the performance of the reservoir and the
total production system
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Dissolved Gas Drive
• A dissolved-gas-d rive reservoir is closed from
any outside source of energy, such as water
encroachment. Its pressure is initially above
bubblepoint pressure, and, therefore, no free bubblepoint pressure, and, therefore, no free
gas exists. The only source of material to
replace the produced fluids is the expansion
of the fluids remaining in the reservoir.
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Dissolved Gas Drive
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Gas Cap Drive
• A dissolved-gas-d rive reservoir is closed from
any outside source of energy, such as water
encroachment. Its pressure is initially above
bubblepoint pressure, and, therefore, no free bubblepoint pressure, and, therefore, no free
gas exists. The only source of material to
replace the produced fluids is the expansion
of the fluids remaining in the reservoir. Some
small but usually negligible expansion of the
connate water and rock may also occur.
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Gas Cap Drive
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Water Drive
• A dissolved-gas-d rive reservoir is closed from
any outside source of energy, such as water
encroachment. Its pressure is initially above
bubblepoint pressure, and, therefore, no free bubblepoint pressure, and, therefore, no free
gas exists. The only source of material to
replace the produced fluids is the expansion
of the fluids remaining in the reservoir. Some
small but usually negligible expansion of the
connate water and rock may also occur.
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Water Drive
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Combination Drive
• In many cases, an oil reservoir will be both
saturated and in contact with an aquifer. In
this case, all three of the previously described
mechanisms may be contributing to the mechanisms may be contributing to the
reservoir drive. As oil is produced, both the
gas cap and aquifer will expand and the gas/oil
contact will drop as the oil/water contact
rises, which can cause complex production
problems.
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Drawdown
• The difference between the average reservoir pressure and the flowing bottomholepressure.
• The effects of drawdown on inflow • The effects of drawdown on inflow performance differs for a well with zero skin factor. The effects of both positive and negative skin factors will then be discussed.
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Positive Skin
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Negative Skin
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Effect of Depletion
• In any reservoir in which the average reservoir
pressure is not maintained above the bubble point
pressure, gas saturation will increase in the entire
drainage volume of the wells. This will cause a
decrease in the pressure function in the form of decrease in the pressure function in the form of
decreased kro, which will cause an increase in the
slope of the pressure profile and the IPR. Therefore
to maintain a constant inflow rate to a well, it will be
necessary to increase the drawdown as pR declines
from depletion
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Depletion on the Pressure Profile
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Depletion on the IPR
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Predicting Present Time IPR’s
Vogel Method
• Vogel developed and empirical equation for
the case of a depletion drive reservoir, in
which the reservoir pressure is everywhere which the reservoir pressure is everywhere
below the bubble point pressure. He arrived
at the the following relationship between
dimensionless flow rate and pressure: 2
(max)
8.02.01
−−=
R
wf
R
wf
o
o
p
p
p
p
q
q
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Vogel’s Equation
• pwf = well flowing pressure, psia
2
(max)
8.02.01
−−=
R
wf
R
wf
o
o
p
p
p
p
q
q
• pwf = well flowing pressure, psia
• pR = avg. reservoir pressure, psia
• qo = oil flow rate, stb/day
Note: qo(max) is a fictitious value of production representing a maximum drawdown, corresponding to pwf=0.
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Constant Productivity Index
• The dimensionless IPR for a well with a
constant productivity index can be calculated
from:
−= wfpq
−=
R
wf
o
o
p
p
q
q1
(max)
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Vogel Method
• The tangent of the curve represents 1/J.
Therefore, the J is the negative derivative of q
with respect to P. The negative sign is due to
the fact that the slope of the curve is negative the fact that the slope of the curve is negative
but the J is a positive quantity.
• Vogel’s equation should approximate Darcy’s
equation at very low flow rates.
oo
o
r B
HK
P
qJ
µ== max8.1(At Pwf=Pr)
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Vogel Method
• One may want to predict a well’s behavior at some
future time when the reservoir pressures deplete.
futureoo
o
futurerfutureB
K
P
q
J
=
=µ
max8.1
• Simply solving for (qmax)future we obtain
presentoo
o
future
presentr
future
present
future
B
K
P
qJ
=
=
µmax8.1
( ) ( )( )( )
=
presentr
futurer
presento
oo
futureoo
o
presentfutureP
P
k
B
B
kqq
µµmaxmax
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Predicting Future IPR’s for Oil Wells
• As the pressure in an oil reservoir declines from
depletion, the ability of the reservoir to transport oil
will also decline. This is caused from the decrease in
the pressure function as relative permeability to oil is
decreased due to increasing gas saturation. decreased due to increasing gas saturation.
• Planning the development of a reservoir with respect
to sizing equipment and planning for artificial lift, as
well as evaluating the project from an economics
standpoint, requires the ability to predict reservoir
performance in the future.
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Standing Method
• Standing published a procedure that can be
used to predict the decline in the value of
qo(max) as gas saturation in the reservoir
increases from depletion. increases from depletion.
2
(max))( 8.02.01
−−=
RF
wf
RF
wf
FoFo
p
p
p
pqq
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Fetkovich Method
• The method proposed by Fetkovich to
construct future IPR's consists of adjusting the
flow coefficient C for changes in
( )nppCq 22
−=
for changes in f(pr). He assumed that f(pr) was
a linear function of pr and, therefore, the
value of C can be adjusted as
)/( RPRFpF ppCC =
( )wfRo ppCq 2−=
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Fetkovich Method
• A value of Cp is obtained from present time
production tests, that is, tests conducted
when pR = pRP. Fetkovich assumed that the
value of the exponent n would not change. value of the exponent n would not change.
• Future IPR's can thus be generated from
n
RPRFRPRFpFo ppppCq )/)(/(22
)( =
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Well Completion Effects
• There are basically three types of
completions that may be made on a well
depending on the type of well, well
depth, and type of reservoir or depth, and type of reservoir or
formation.
– Open Hole Completions
– Perforated Completions
– Perforated, Gravel Packed Completions
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Open Hole Completions
• The casing is set at the top of the producing
formation and the formation is not exposed to
cement. Also, no perforations are required
• The only effect of the completion on inflow • The only effect of the completion on inflow
performance of an open hole completion will
be caused by alteration of the reservoir
permeability by damage or stimulation.
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Perforated Completions
• The most widely used completion method is
one in which the pipe is set through the
formation, and cement is used to fill the
annulus between the casing and the hole. annulus between the casing and the hole.
This, of course, requires perforating the well
to establish communication with the
producing formation. This type of completion
permits selection of the zones that are to be
opened.
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Perforation
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Perforated, Gravel Packed Completions
• In some reservoirs, the lack of cementing
material in the reservoir allows sand to be
produced into the well. When completing
wells in which the formation is incompetent or wells in which the formation is incompetent or
unconsolidated, a gravel pack completion
scheme is frequently employed. In this type of
completion, a perforated or slotted liner or a
screen liner is set inside the casing opposite
the producing formation.
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Gravel-Pack
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Well Flow Correlations
• One of the most important components in the
total well system is the well tubing. As much
as 80 percent of the total pressure loss can be
consumed in lifting the fluids from the bottom consumed in lifting the fluids from the bottom
of the hole to the surface. The flow may exist
in tubing or in the annulus between the
tubing and the casing. The wells may be
vertical of can be drilled at large deviation
angles, especially in the case of offshore wells
or wells drilled in urban areas.
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Well Flow Correlations
• Many correlations have been developed over
the years to evaluate the pressure drop
resulting from the multiphase flow of fluids in
a vertical or deviated well.a vertical or deviated well.
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Well Flow Correlations
1. Establish stable flow conditions at particular
values of qL , qg , pipe diameter, pipe angle,
etc.
2. In a test section of length ΔL , measure H and 2. In a test section of length ΔL , measure HL and
Δp. Methods for measuring HL include nuclear
densitometers, capacitance devices, quick
closing valves, etc. Flow pattern may be
observed if the test sectionis transparent.
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Well Flow Correlations
3. Calculate mixture density and elevation
component.LgLLs
gdp
HH
Θ=
−+=
sin
)1(
ρ
ρρρ
4. Calculate and acceleration and friction
component.
c
s
el g
g
dL
dp Θ=
sinρ
accelel dL
dp
dL
dp
L
p
dL
dp
−
−
∆∆
=
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Well Flow Correlations
5. Calculate a two phase friction factor
6. Change test conditions and return to step 2. H ,
fm
cTp
dL
dp
v
dgf
=2
2
ρ6. Change test conditions and return to step 2. HL,
fTP, and flow pattern should be obtained over a
wide range of conditions.
7. Develop empirical correlations for HL, FTP and
flow pattern as a function of variables that will be
known for design cases. These variables include
vsL, vsg, d, fluid properties, pipe angle, etc.
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Choke Sizing
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Choke Sizing for Liquid Flow
• Critical velocity is the velocity of sound in that
medium. This velocity is a limiting factor, so
the fluid cannot be accelerated to a large
velocity. velocity.
• The critical of any fluid is given by:
CV
ρ1.68
=∗
ρ = fluid density, lbm/ft3
C = isothermal compressibility of the fluid, psi
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Choke Sizing
• Single Phase Liquid Flow
– Calculating the pressure drop across a choke is
relatively easy. However, flow through the choke is
liquid and gas since tubing pressure is usually liquid and gas since tubing pressure is usually
below the bubble point.
– If the exit velocity is below critical, the flow is:
ρP
Cdq c
∆= 22800
dc = choke throat diameter, in
ΔP = differential pressure across the choke, psi
C is given from the Flow Coefficient Graph
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Graph of Flow Coefficients for flow
through chokes (Crane, 1957)
http://www.scribd.com/doc/21335619/Throug
h-valves-Pipes-and-Fittings
Reynolds number is given by
µρVd
&928
Re =
h-valves-Pipes-and-Fittings
Accessed Feb 24, 2010
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Choke Sizing
• In the case of gas exiting an open-ended flow
line, the sonic velocity is given by:
kZT
T = temperature, oR
γg = gas specific gravity relative to air
Z = compressibility factor
k = ratio of gas specific heat at constant volume to constant pressure (k=cp/cv)
or obtained from Specific Heat Ratios for Hydrocarbon Vapors Graph
g
g
kZTV
γ4.41=∗
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Choke Sizing
• The gas flow rate at critical velocity is given by
sceg
gZPT
TPdVQ
2122
2∗∗ =
Q = Gas flow rate, MMSCFD
T = Gas temperature, oR
P = Pressure, pisa
D = Pipe diameter, in
V*g = Sonic velocity in gas at P and T, ft/s
Z = Gas compressibility factor at P and T
sce
gZPT
Q2122
=
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Choke Sizing for Gas Flow
• Gas flow through a small diameter exit can be
described by below.
[ ]kkkupdrr
kg
APCq /)1(/22
5.155 +−
= [ ]
g
rrk
gT
q1
2 −
−
=γ
Cd = Choke discharge coefficient
A = Choke throat area, in2
T = Inlet temperature, oR
Pup = Upstream gas pressure, psia
k = gas specific heat ratio, cp/cv
r = Pdn/Pup if ≥ ro
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Choke Sizing for Two Phase Flow
• Choked flow for a gas liquid mixture is difficult to
mode, and only empirical correlations are available.
Two presently available are the Gilbert and the Ros
correlations, give asBRAq )(
C
B
pL
upd
RAqP
64
)(=
Pup = upstream pressure, psig (Gilbert), psia (Ros)
qL= liquid flow rate, bbl/day
d64 = choke diameter in 64ths”
Correlation A B C
Gilbert 10.00 0.546 1.89
Ross 17.40 0.500 2.00
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Choke Sizing
• To ensure the flow is critical, the equation by
Wallis can be used to calculate the critical
velocity.
( )2/1−
λλ( )2/1
2*2*
−
∗
++=
LL
L
gg
g
ggLLVV
Vρλ
ρ
λλρλρ
V* = critical velocity
γ = in-situ volume fraction of each phase
ρ = density of gas and liquid, lbm/ft3
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Flow in Pipes and Restrictions
(vertical wells)(vertical wells)
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Two Phase Flow
• Variables
– Liquid Holdup- fraction of an element of pipe that
is occupied by liquid at some instant.
element pipe ain liquid of volume=
– Gas Holdup- relative in-situ volume of liquid and
gas expressed in terms of the volume fraction.
element pipe theof volume
element pipe ain liquid of volume=LH
Hg = 1- HL
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Two Phase Flow
• Variables
– No-Slip Liquid Holdup-the ratio of the volume of
liquid in a pipe element that would exist if the gas
and liquid traveled at the same velocity (no and liquid traveled at the same velocity (no
slippage) divided by the volume of the pipe
element..
g
Lq+
=L
L
q
qγ
qL= sum of the in-situ oil and water
qg= the in-situ gas flow rate
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Two Phase Flow
• Variables
– No-Slip Gas- gas void fraction can be defined as
q
g
Lgq+
=−=L
g
q
q1 λγ
qL= sum of the in-situ oil and water
qg= the in-situ gas flow rate
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Two Phase Flow
• Variables
– Density- The density of an oil/water mixture may
be calculated from the oil and water densities and
flow rates if no slippage between the oil and water flow rates if no slippage between the oil and water
phases is assumed.
wwooL ff ρρρ +=
where
and fw = 1-fo
wo
oo
qf
+=
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Two Phase Flow
• Variables
– Velocity- the velocity that phase would exhibit if it
flowed through the total cross sectional area of
the pipe alone.gq=
the pipe alone.
AvL
gq=
•The actual area through which the gas flows is
reduced by the presence of the liquid to AHg.
Therefore, the actual gas velocity is calculated from:
g
gAH
vgq=
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Two Phase Flow Patterns
• Whenever two fluids with different physical
properties flow simultaneously in a pipe, there
is a wide range of possible flow patterns. By
flow pattern, reference is made to the flow pattern, reference is made to the
distribution of each phase in the pipe relative
to the other phase.
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•Two phase
vertical flow vertical flow
patterns
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93-96 Effects of Variables on Well
Performance
• During the producing life of a well or field
many conditions can change that will affect
the well's flowing performance. Also,
conditions can change from well to well in a conditions can change from well to well in a
field at a given time, and conditions can
certainly vary among fields.
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Effects of Variables on Well
Performance
• Some of these variables that can change
are…
1. Liquid Flow Rate
2. Gas/Liquid Ratio2. Gas/Liquid Ratio
3. Water/Oil Ratio or Water Cut
4. Liquid Viscosity
5. Tubing Diameter and Slippage
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Liquid Flow Rate
• The effect of increasing liquid rate will be an
increase in both HL and fluid velocity. This will
cause an increase in both the hydrostatic and
friction. The effect may be seen graphically in friction. The effect may be seen graphically in
Figure 3-22 that was constructed by choosing
some general well conditions and holding
everything constant except qL.
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Gas/Liquid Ratio
• The GLR has more effect on two-phase flowing pressure gradients than any other variable. In a depletion-type field the gas/oil ratio will usually increase with time until late in the life of the reservoir. The GLR may decrease if water cut reservoir. The GLR may decrease if water cut increases.
• The GLR has the most effect on the hydrostatic component of the pressure gradient equation because HL will decrease as GLR increases. However, the total flow rate will increase, and the friction loss depends on the flow rate squared.
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Water/Oil Ratio or Water Cut
• The total pressure gradient in the well will
increase as fw increases. This results from an
increase in liquid density if the water is
heavier than the oil and also from a heavier than the oil and also from a
decreasing GLR, since the free gas in the
tubing comes primarily from the oil only. The
effect may be expressed graphically in Figures
3-25 and 3-26.
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Figure 3-25 shows only the effect of increased liquid
density while the total effect is shown in Figure 3-26.
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Liquid Viscosity
• The effects of liquid viscosity on pressure drop are very
difficult to isolate. This results from the fact that the
concept of a gas/liquid mixture viscosity has no
physical meaning. The liquid viscosity will affect HL to
some degree and will also increase the shearing some degree and will also increase the shearing
stresses in the liquid and, therefore, the friction
pressure drop. If an oil/water mixture is present,
dispersions or emulsions may form and cause a very
large increase in the pressure gradient. At the present
time, there is no method to accurately predict the
viscosity of an oil/water mixture, much less the
viscosity of a gas/oil/water mixture.
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The combined effects of
decreasing API gravity
and increasing viscosity
for a gas/oil mixture are
shown qualitatively in
Liquid Viscosity
shown qualitatively in
Figure 3-27. If water
were present, the effects
would probably be even
more pronounced.
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Tubing Diameter and Slippage
• The selection of the proper tubing size to install in a
well is one of the most critical and the most
neglected functions of a production engineer. In
many cases the tubing size will be selected based on
such criteria as what has been used in the past or such criteria as what has been used in the past or
what is available on the pipe rack. A total system
analysis, which combines the reservoir and piping
system performance, is required to select the proper
tubing size, but the effects of tubing size on velocity
and slippage will be discussed.
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• As the tubing size increases, the velocity of the mixture
decreases and eventually the velocity will be too low to
lift the liquids to the surface. The well will then begin
to load up with liquids and may eventually die. The
tubing size at which a well will begin to load or the
maximum tubing size which will sustain flow can be
determined from a plot such as Figure 3-29.
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Tubing Diameter
and Slippage
•The effect of declining production
rate and, therefore, velocity for a
particular tubing size can be shown
qualitatively in Figure 3-30. For a
particular tubing size, well depth,
wellhead pressure and as/liquid wellhead pressure and as/liquid
ratio, there will exist a minimum
production rate that will keep the
well unloaded.
•Figure 3-31 shows the effect of
tubing diameter on the minimum
rate. This type of information is
valuable in determining at what rate
a well will begin to load for various
tubing sizes.
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Use of Prepared Pressure Traverse
Curves
• In some cases it is not feasible for the field engineer to conduct an involved computer study to calculate a traverse or to calculate the pressure drop in a tubing string for give field conditions. In some cases, it may be advantageous to construct some cases, it may be advantageous to construct a set of pressure traverse curves for hypothetical values of the variables such as qL ,GLR, d, fw , etc. These curves can then be used to estimate the pressure drop that would occur in a well producing under similar conditions.
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