Doe/netl-2012/1540 Mobility And Conformance Control For Carbon Dioxide Enhanced Oil Recovery (Co2-Eor) Via Thickeners, Foams, And Gels - U.s. Department Of Energy Page 24

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LIST OF FIGURES
1.
INTRODUCTION TO CO
ENHANCED OIL RECOVERY ..................................................................... 1
2
F
1.1. U.S. E
O
R
G
[K
, 2010 ].
IGURE
NHANCED
IL
ECOVERY WITH
ASES OVER THE PAST DECADES
OOTTUNGAL
1
F
1.2 S
I
CO
F
[L
, 1960
]. ................................................ 2
IGURE
IMPLIFIED
LLUSTRATION OF A
LOOD
INDLEY
S
2
F
1.3. CO
[
NIST
]
IGURE
DENSITY AS A FUNCTION OF TEMPERATURE AND PRESSURE
DATA FROM
WEB BOOK
2
5
F
1.4. V
CO
[
NIST
IGURE
ISCOSITY OF
AS A FUNCTION OF TEMPERATURE AND PRESSURE
DATA FROM THE
2
] ................................................................................................................................. 6
WEB BOOK
2.
POTENTIAL RECOVERY BENEFITS OF MOBILITY CONTROL ...................................................... 9
F
2.1. S
IGURE
WEEP EFFICIENCY AT BREAKTHROUGH FOR MISCIBLE DISPLACEMENT BASED ON PHYSICAL
[H
, 1960] ...................................................................................................... 9
MODEL
ABERMANN
F
2.2. S
IGURE
MOOTHED RESULTS FOR THE EFFECT OF MOBILITY RATIO ON SOLVENT BREAKTHROUGH AND
-
[C
, 1972]
POST
BREAKTHROUGH OIL RECOVERY AS A FUNCTION OF SOLVENT INJECTED
LARIDGE
10
F
2.3. V
:
IGURE
ERTICAL SWEEP EFFICIENCY AS A FUNCTION OF THE VISCOUS
GRAVITY FORCE RATIO AND THE
,
,
[C
, 1971] ...... 11
MOBILITY RATIO IN SINGLE LAYER
UNIFORM
ISOTROPIC POROUS MEDIUM
RAIG
F
2.4. E
IGURE
FFECT OF MOBILITY RATIO ON VERTICAL SWEEP AS A FUNCTION OF DIMENSIONLESS TIME FOR
-
[E
, R
M
, 1988] ....... 12
THE PISTON
LIKE DISPLACEMENT OF OIL BY WATER
NICK
EZNIK AND
ILLER
3.
CURRENT STATE-OF-THE-ART; WAG AND CONTINUOUS CO
INJECTION ............................ 13
2
F
3.1. T
CO
CO
IGURE
HE RELATIONSHIP BETWEEN
SATURATION AND THE RELATIVE PERMEABILITY OF
AND
2
2
[B
B
, 2005] ........................................................... 14
BRINE IN POROUS MEDIA
ENNION AND
ACHU
F
3.2. H
-
,
-
IGURE
IGH
PRESSURE
THREE
DIMENSIONAL PHYSICAL MODEL FOR STUDYING VOLUMETRIC SWEEP
[L
., 2008] ............................................................................................. 15
EFFICIENCY
EWIS ET AL
F
3.3. T
WAG
-
-
IGURE
HE EFFECT OF
RATIO ON OIL RECOVERY IN A QUARTER
FIVE
SPOT MISCIBLE
-
DISPLACEMENT OF DEAD CRUDE OIL FROM UNCONSOLIDATED SAND BY ETHANE IN A HIGH
[L
., 2008] .............................. 15
PRESSURE PHYSICAL MODEL WITH VERTICAL WELLS
EWIS ET AL
4.
DIRECT THICKENERS FOR CO
MOBILITY CONTROL .................................................................. 17
2
F
4.1. S
PDMS [H
., 1990; B
I
, 1990]; PFOA
IGURE
TRUCTURES OF
ARRIS ET AL
AE AND
RANI
HOMOPOLYMER
[M
C
., 1996]
FAST
CO
[H
C
LAIN ET AL
AND THE POLY
RANDOM COPOLYMER
THICKENER
UANG
2
., 2000; X
E
, 2001; X
., 2003] ............................................................. 20
ET AL
U AND
NICK
U ET AL
F
4.2. V
IGURE
ISCOSITY INCREASE CAUSED BY DISSOLUTION OF HIGH MOLECULAR WEIGHT
CO
[M
C
., 1996] ........................................................ 21
POLYFLUOROACRYLATE IN
C
LAIN ET AL
2
F
4.3. F
CO
IGURE
ALLING CYLINDER VISCOMETER RESULTS FOR THE EFFECT
VISCOSITY AS A FUNCTION OF
2
FAST
;
POLY
CONCENTRATION AND SHEAR RATE
RELATIVE VISCOSITY IS SOLUTION
/
CO
[X
., 2003] .............................. 22
VISCOSITY
PURE
VISCOSITY AT SAME CONDITIONS
U ET AL
2
F
4.4. V
CO2
CO
IGURE
ISCOSITY OF THICKENED
RELATIVE TO PURE
AS A FUNCTION OF SUPERFICIAL
2
FAST
[X
., 2003] .............................................. 22
VELOCITY AND POLY
CONCENTRATION
U ET AL
F
4.5. S
CO
-
;
IGURE
TRUCTURES OF OXYGENATED HYDROCARBON
SOLUBLE POLYMERS
POLOYVINYL
2
Β
(PVA
);
((1-O-(
)
-2,3,4,6-
-O-
-
-D-
ACETATE
C
POLY
VINYLOXY
ETHYL
TETRA
ACETYL
) (PA
GI
VE);
(PLA);
(3-
GLUCOPYRANOSIDE
C
C
AMORPHOUS POLYLACTIC ACID
OLIGOMERS OF
) (OAO);
(PVEE);
ACETOXY OXETANE
POLYVINYLETHYLETHER
OLIGOMERS OF CELLULOSE
(OCTA);
:
-
(PACD) [P
TRIACETATE
NOT SHOWN
PER
ACETYLATED CYCLODEXTRINS
OTLURI ET
., 2003]. ................................................................................................................................ 24
AL
F
4.6. A
5
%
IGURE
COMPARISON OF THE PRESSURE REQUIRED TO DISSOLVE
WT
OF THE POLYMERS AND
O
F
9
12
CO
25
C
OLIGOMERS SHOWN IN
IGURES
AND
IN
AT
AS A FUNCTION OF COMPOSITION
2
xx

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