cpge research showcase poster jwd 2
TRANSCRIPT
Polymer Transport in Porous Media
Jonathan W. Driver and Dr. Gary Pope
Research Showcase in Petroleum and Geosystems Engineering • September 6, 2016
Introduction
The basic premise of polymer flooding is simple: viscosify the water used to
displace formation oil so that the displacement is stable and efficient. The
viscosity of a polymer solution derives from the resistance of a sub-micron
sized polymer macromolecule to shearing flows within the aqueous solvent.
The larger the macromolecule, the more resistance imparted, so the trend in
polymers for EOR applications has been towards higher and higher molecular
weight. There are, however, some fundamental limits to this approach. Among
other things, large polymers become prone to plugging the pore throats of
tight rocks for the simple reason that their diameter in solution approaches the
diameter of the throats. This presents an optimization design challenge: given
some knowledge of formation properties, how does one create a polymer of
the highest permissible molecular weight?
The result of the chemical processes used to synthesize EOR polymers like
partially-hydrolyzed polyacrylamide (HPAM) is a distribution of polymer
molecular weights. The shape of this distribution can be subsequently
modified by filtration and irreversible mechanical degradation.
Preliminary Experiments with Polymer Core Flooding Experiment
Blender shearing is sufficient to reduce the viscosity (and molecular weight) of
HPAM solutions. The timecourse can be characterized for reproducibility.
Experimental Design
Cores of varying permeability are to be flooded serially with polymer solutions
of increasing viscosity until a near-complete loss of permeability is observed.
The same polymer solution will be mechanically degraded to varying extents
and then subsequently filtered using filters of varying stringency to produce
solutions that vary only in polymer molecular weight.
Conclusions
Core Flooding Experiment
Acknowledgements
The Pope Lab (Pathma Liyanage, Dr. Raphael Longoria, et al.)Chevron Energy Technology CompanySNF Holding Company
Pre-flood Brine (Seawater) Permeability Measurement (CQ1 Sandstone)
mechanical shearingreduces MW of all polymermass conservative
filtrationdoes not change MW of individual moleculesremoves mass from solution
##
The approach to be employed in this project is to use shearing and filtration in
combination to prepare polymer for flooding of tight rocks, and to evaluate
plugging behavior to create the most viscous solution possible without
plugging the pore throats.
10-50 md
1. 8 min
2. 4 min
3. 2 min
4. 1 min
5. ½ min
6. 0 min
1. 0.2 µm
2. 0.4 µm
3. 0.6 µm
1. 11
2. 12
6. 16
7. 2X
26
……
µ2X > µ16
…
Q
ΔP
(measured)
Unstable
-0.02
0
0.02
0.04
0.06
0.08
0.1
0.12
0.14
00.20.40.60.811.21.4
β
Mesh Size (μm)
0.2% 3330S in 1% NaCl
20 sec blended
2 min blended
0.2 micron filtered
End
1
10
100
0.1 1 10 100 1000
Vis
co
sit
y (
cP
)
shear rate (1/s)
0.2% 3330S Blending Timecourse
0 min
1 min
2 min
4 min
8 min
16 min
0
200
400
600
800
1000
1200
1400
-30 20 70 120 170 220
Tim
e (
sec
)
Vol (mL)
Filtration Test at 15 psi
κ ≈ κ0/(1+βV)
t ≈ aV2 + bV + c
β = 2a/b
Filtration can be used to characterize polymer molecular weight distribution.
0.01 0.1 1 10 100
Sig
nal In
ten
sit
y
Pore Size (µm)
NMR Pore Body Size Distribution
Mn 1-18 MDa
HPAM
+
+
+
+
+
+
Polymer solutions plug a filter
membrane, causing a loss of
permeability.
The rate of loss of
permeability can be quantified
by measuring the curvature of
the time versus filtered
volume curve for a constant-
pressure filtration.
This parameter (β) is a
function of polymer molecular
weight distribution and filter
pore size.
By using a range of filter
pore sizes, a full
characterization of
polymer plugging
behavior can be achieved.
Plugging quickly
escalates as pore size
decreases.
Pre-filtration can be more
effective at reducing
plugging than mechanical
shearing.
19.4 cP
14.7 cP
23.1 cP
NMR can be used to estimate pore body size distribution. This is not the same
as pore throat size, but it may still correlate with plugging behavior. Below is a
pore body size distribution from a low permeability sandstone.
y = 8.2219x + 0.4353R² = 0.9992
0
1
2
3
4
5
6
7
8
9
10
0 0.2 0.4 0.6 0.8 1 1.2
ΔP
(p
si)
Q (mL/min)
𝛋 =𝐐 𝛍 𝐋
𝐀 𝚫𝐏
43 md
ISCO Pump
(water at constant
flow rate)
Design
1” Core
Holder
effluent
polymer
water 100 psi
confining
pressure
pis
ton
Transducer
L
H
Computer
Pressure Readouts from Polymer Floods with FP3330S (8 MDa) in Seawater
0
0.5
1
1.5
2
2.5
3
3.5
4
0 1 2 3 4 5 6
ΔP
(p
si)
Pore Volumes
-0.5
0
0.5
1
1.5
2
2.5
3
3.5
4
0 1 2 3 4 5 6 7
ΔP
(p
si)
Pore Volumes
-0.5
0
0.5
1
1.5
2
2.5
3
3.5
4
4.5
5
0 1 2 3 4 5
ΔP
(p
si)
Pore Volumes
Q = 0.03 mL/min
Q = 0.03 mL/min
Q = 0.03 mL/min
Q =
0.0
15 m
L/m
in
There is evidence of plugging in the second and third polymer floods, in the
form of upward drift in the pressure plateau. This is similar to what happens in
the filter paper based filtration test, but with a constant flow rate and non-
uniform pore size.
8 min sheared, 0.4 µm filtered
4 min sheared, 0.4 µm filtered
0 min sheared, 0.6 µm filtered
Residual Resistance (Post Flood with Brine)
-2
0
2
4
6
8
10
12
0 1 2 3 4 5 6 7 8
ΔP
(p
si)
Pore Volumes
Q = 0.007 mL/min
Q = 0.150 mL/min
Q = 0.100 mL/min
Q = 0.007 mL/min
Polymer is not easily removed from the core with brine, possibly due to
adverse viscosity. It appears that most of the permeability reduction is
irreversible.
• Mechanical degradation and filtration are effective tools for reducing
polymer average molecular weight and shaping the molecular weight
distribution
• Mechanical degradation can be calibrated precisely for a given polymer
under precisely controlled experimental conditions
• Filter membranes with precise pore sizes can be used to quantitatively
characterize the (non-adsorptive) plugging behavior of polymers
• The core tested plugged under the conditions explored
• This plugging appears to be robust to post-flood brine
• Accurate characterization and quantitation will require more
pore volumes of polymer to be injected
Future Plans and Goals
• Repeat the core characterization experiment for a large number of cores of
varying low permeability
• Construct relations between core properties (permeability, pore body size
distribution) and resistance factor for polymer injection with fully
characterized polymer solutions (rheology, filtration)
• Define guidelines for producing a polymer solution of maximum possible
viscosity with acceptable plugging behavior given knowledge of rock
properties
Dβ
=β*
[µm
]
κ [md]
µ [
cP]
κ [md]
Hypothetical Relations between Maximum Achievable Viscosity, Polymer Filtration Behavior, and Rock Permeability
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