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![Page 1: Acido2.ppt](https://reader036.fdocuments.us/reader036/viewer/2022070413/55cf93f2550346f57b9edcf5/html5/thumbnails/1.jpg)
Completion Fluid Damage Treatment Options.
Damage Mechanism
Solids invasion
Clay swelling Clay mobilisation
Water block
Emulsion block
Wettability damage
Precipitation of solids
Treatment Options
HCl:mud acid Solids dependent
HCl:mud acid
HCl:mud acid
Surface Tension Reduction
Dependent on emulsion external phase.
Mutual Solvents and or Surfactants
Solids dependent
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Formation Damage Treatment Options
for Different Drive Mechanisms.Formation Damage Mechanism
Water Drive
Accelerated water production after acidizing.
Asphaltene damage
Water production
Scale formation
Gas Drive
Water block
Paraffin damage
Treatment
Selective acidizing
Paravan/Solvent soaks
Aquatrol 1,2 or 3, Direxit
Depends on composition
Reduce surface tension
Paravan/Sovent soaks
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Formation Damage Mechanism
Solution Drive
Water block
Inadequate formation pressure
Organic formation damage
Combination Drive
Treatment
Reduce surface tension
Carbon Dioxide or Nitrogen
Paravan/Sovent soaks
All of the above
Formation Damage Treatment Options for Different Drive Mechanisms.
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Temperature Considerations
150°F
L
L
U
L
L
L
L
U
L
L
165°F
L
L
U
L
L
L
L
U
L
L
170°F
M
M
U
M2
L
L
L
U
L
M
180°F
M
M
U
M2
L
M
M
U
L
M
185°F
M
M
U
M2
L
M
M
U
L
M
200°F
U
M
M
U
L
M
M
M3
M
U
240°F
U
U
L
U
L
U
U
M3
M
U
Situation
Emulsion Blocks
Organic Deposition
Asphaltene Coking
Bacteria
CaCO3 Scale
BaSO4 Scale
CaSO4 Scale
Chlorination of Mutual Solvents
Rigid Emulsion Film
Are Retarded HFSystems Economical
Temperatures
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Treatment Options for Formation Damage Caused by Indigenous Minerals
Siderite,Hematite
Iron HydroxidePrecipitation
Acidize - Standard HCl/HCl:HF withproperly evaluated sequesterants
Pyrite Iron HydroxidePrecipitate.Asphaltene
Sludging
Mobile FinesFormationFines
(Feldspars,Quartz, Etc)
High Flow Rates Preflush - 7.5% HClAcidize - 7.5:1.5 HCl:HF + BoricAcid (Volume as required).Overflush - as required.
Calcite,Dolomite
>18% - HCl Only.<18% - Standard HCl/HCl:HF
CalciumFluoride
Precipitation
Contact ofcalcium ion with
HF Acid.
Oxygen RichSystems
Oxygen RichSystems
Preflush - 25 Gal/ft Xylene + 10%AceticAcidize - Standard HCl/HCl:HF withproperly evaluated sequesterants
Mineral PotentialProblems
Treatment OptionsWhat ToAvoid
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Mineral PotentialProblems
Treatment OptionsWhat ToAvoid
Kaolinite Mobile Fines Rate Control.<5%-Acidize - Standard HCL/HCL:HF>5% - Evaluate for Stress Pack
High Flow Rates
Illite Mushing Permeability > 120 Md Acidize -Standard HCl/HCl:HFPermeability < 120 md reducesurface tension to 30 Dynes/Cm2
Fresh WaterSystems
Swelling Acidize - Standard HCl/HCl:HFPerform Immersion Tests to see ifalcohol/acid blends or otheradditives are necessary to preventswelling
(Montmoril-Smectite
lonite)
Fresh WaterSystems
Chlorite Iron HydroxidePrecipitate,
Hydrous SilicatesAmorphous
Alumino Silicate
Acidize - Standard HCl/HCl:HF withproperly evaluated sequesteringagents, boric acid volume asrequired. Overflush as required
Oxygen RichSystems: Ph>2.8
InadequateSequesterant.
Buffered Acids
Treatment Options for Formation Damage Caused by Indigenous Minerals
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Chamosite Iron HydroxidePrecipitate Oxygen Rich
Systems: Ph>2.8 Acidize - Standard HCl/HCl:HF withproperly evaluated sequesterants
Mineral PotentialProblems
Treatment OptionsWhat ToAvoid
Swelling Acidize - Standard Hcl/Hcl:HfMixed LayerIllite/ Smectite
Fresh WaterSystems
Feldspars SilicaPrecipitation
> 20%- 7.5% HCl, 7.5:1.5 HCl:HF< 20%- Standard HCl/HCl:HF
High % of HF Acid
Treatment Options for Formation Damage Caused by Indigenous Minerals
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Acid Treating Volumes Based on Permeability
Average Permeability w/o Damage
Ku (md).
< 0.1 md
0.1 - 1.0 md
1.0 - 10 md
10- 50 md
> 50 md
Normal HClRange Gal/ft
(L/M)
15-25(185-310)
25-50 (310-620)
35-75(430-930)
50-100(620-1240)
50-100(620-1240)
Normal HCl:HF Range Gal/ft
(L/M)
Not Recommended
35-50(430-620)
75-100(930-1240)
100-150(1240-1865)
100-200(1240-2480)
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Recommended Treating Volume of HCl:HF in
Gallons Per Square Foot of Pay
GALLONS PER FOOT OF TREATED INTERVAL
TR
EA
TIN
G R
AD
IUS
(F
t)
0 100 200 300 400 500 600 700 800 900 0
1
2
3
4
5
6
7 20 gallonsper sq.ft
15 gallonsper sq.ft
10 gallonsper sq.ft
5 gallons per sq.ft
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Volume of 12:3 HCl:HF Required to Treat a 3.0 Inch Damage Zone -
Gallons Per Foot of Pay. Temperature
100° F
Gal/ft
70
50
50
50
50
50
50
150° F
Gal/ft
80
65
55
50
50
50
50
200° F
Gal/ft
100
75
65
55
50
50
50
250° F
Gal/ft
120
80
75
65
50
50
50
Pump Rate
BPM/ft
0.001
0.005
0.010
0.025
0.050
0.100
0.200
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Volume of 12:3 HCl:HF Required to Treat a 6.0 Inch Damage Zone - Gallons Per
Foot of Pay. Temperature
100° F
Gal/ft
350
275
225
175
140
130
150° F
Gal/ft
350
350
300
250
200
160
200° F
Gal/ft
350
350
350
325
260
210
250° F
Gal/ft
350
350
350
350
320
260
Pump Rate
BPM/ft
0.005
0.010
0.025
0.050
0.100
0.200
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Gallons Per Foot of Treating Fluid for
Differing Porosities.
BA
RR
EL
S P
ER
FO
OT
OF
SA
ND
TH
ICK
NE
SS
0 1 2 3 4 5 6 7 0
20
40
60
80
100
120
140
160
180
200 220
240
260
280
300
320
340
360
380
400
35 % Porosity
100 %Porosity
RADIUS DISTANCE IN FEET FROM WALL OF 7 INCH WELLBORE
GA
LL
ON
S P
ER
FO
OT
OF
SA
ND
TH
ICK
NE
SS
9
8
7
6
5
4
3
2
1
0
5.0 % Porosity
15 % Porosity
25 % Porosity
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Acid Selection Based On %Carbonate & Temperature.
Temp°F (°C)
< 200(93)
200-250(93-121)
250-350(121-177)
>350(177)
Temp °F (°C)
< 250(121)
250-350(121-177)
>350(177)
5.0 to 15%
75 gal/ft(930 L/M)15% HCl
followed byHCl: HF
50 gal/ft(620 L/M)7.5% HCl
followed byHCl: HF
35 gal/ft(430 L/M)
7.5% HCl +10% Formicfollowed byFormic:HF
35 gal/ft(430 L/M)
10% Formicfollowed byFormic:HF
10 to 15%
75 gal/ft(930 L/M)15% HCl
then washperforations
withHCl: HF
50 gal/ft(620 L/M)
7.5% HCl +10% Formic
35 gal/ft(430 L/M)
10% Formic
> 15%
100 gal/ft(1240 L/M)15% HCl
50 gal/ft(620 L/M)
7.5% HCl +10% Formic
35 gal/ft(430 L/M)
10% Formic
Percentage of Carbonate in the Formation
< 5.0%
50 gal/ft(620 L/M)
15% HCl followed by HCl: HF
35 gal/ft(430 L/M)7.5% HCl
followed byHCl: HF
35 gal/ft(430 L/M)
10% Formic Formic:HCl
or Formic:HF
35 gal/ft(430 L/M)
10% Formicor Formic:HF
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HCl Acid Strength Based on Formation Solubility
Formation Solubility(Percentage)
0 -10
10 - 20
20 - 40
Greater than 40
Acid Strength(Percentage)
3 - 5
5 - 7.5
7.5 - 10
10 - 28
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Flow Improvement Ratio of Various Treating Solutions
in Berea Sandstones
Treating Volume : Gallons Per Square Foot
Flo
w I
mp
rove
men
t R
atio
K
20.00.0 2.5 5.0 7.5 10.0 12.5 15.0 17.51.0
1.5
2.0
2.5
3.0
7.5% HCl - 4% HF
15% HCl - 4% HF
15% HCl - 3% HF
15% HCl
15% HCl - 7% HF
15% HCl - 2% HF
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Recommended Preflush Volume in Gallons of 15%
HCl Per Foot of Pay for Various Radii.
GA
LL
ON
S O
F 1
5 %
HC
l P
ER
FO
OT
OF
PA
Y
0 1 2 3 4 5 6
TREATING RADIUS (FEET)
1
10
100
1000
1.0 % HCl Solubility
5.0 % HCl Solubility
10 % HCl Solubility
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Selective Acidizing Treatment Options
Situation
Oil Well - Non Gravel Packed
Oil Well - Gravel Packed
Gas Well
Treatment
SAF Mark II
SAF
65 Quality Foam Preflush
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Relative Retarding Action of Different Systems
RegularAcid
HCl Acid
HCl:HF
Mixture ofHCl + Organic
Super-Sol (EQH) Acids
ChemicallyRetarded Acid
Sta-Live Acid Systems
Retarded Mud Sol Systems. (HCl:HF)
SGMA
PhysicallyRetarded Acid
Gelled Acids and Crosslinked Acid.
SRA-3 Emulsified Acid.
Sandstone Acid
Least MostRetardation
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Carbon Dioxide and Nitrogen Guidelines.
Reservoir Type
Gas.
Low Pressure Gas.
Oil, (Above the Bubble Point).
Oil, (Below the Bubble Point).
Water Injection or Disposal Well.
Nitrogen
Yes
Yes
(3, 4)
Yes
(3, 4)
Carbon Dioxide
Yes (1)
(2)
Yes
Yes
(3, 4)
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Injection Rates (Non-Fracturing) into Permeable Formations at
Various Differential Pressures.
0 100 200 300 400 500 600 700 800 900 1000
P=2000 PSI
P=2500 PSI
P=1500 PSI
P=1000 PSI
P= 500 PSI
P= 200 PSI
0 1000 2000 3000 4000 5000 6000 7000 8000 9000 10000
0
10
20
30
40
50
FORMATION CAPACITY, kh - md.ft.
INJE
CT
ION
RA
TE
Q -
BA
RR
EL
S P
ER
MIN
UT
E
0
1
2
3
4
5 DARCEY'S EQUATION FOR RADIAL FLOW
Drainage Radius = 5.0 ftInjected Fluid Viscosity = 1.0 cpDifferential Pressure ( P)
Treating Pressure (+ Plus)Hydrostatic Column (- Minus)Reservoir Pressure = psi
Formation Capacity (kh)Average Effective Permeabilityx Thickness of Sand Body = md. ft.
( For small volume treatments in partially saturated reservoirs)
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Recommended Acid Strengths at Different Temperatures.
Temperature
Up to 180° F (82° C)
180° F to 220° F(82° C to 104 °C)
Above 220° F (104° C)
MaximumHCl Strength
15%
10%
7.5%
MaximumHCl:HF Strength
12:3%
9:3%
7.5:1.5%
Common Strengths Of HCl: HF MIxtures% HCl
6.07.5121515
% HF
0.51.53.03.04.0
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Reaction of Acids on Limestone at Various Concentrations.
Acid
HCl *
Acetic
Formic
Concentration%
15*2025
15*2025
15*2025
Calcium CarbonateDissolvedPer Gallon.
Pounds
1.842.503.22
1.081.431.80
1.421.902.40
Carbon DioxideFormed
Per Gallon.cu.ft.
6.999.47
12.20
4.095.416.82
5.387.209.09
Calcium SaltFormed
Per Gallon.Pounds
2.042.753.57
1.712.252.84
1.842.473.12
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Amount of Limestone Dissolved by 1000 Gallons of
HCl Acid
STRENGTH OF HYDROCHLORIC ACID %
0.0 1.0 2.0 3.0 4.0 5.0 6.0 7.0 8.0 9.0
10.011.012.013.014.015.016.017.018.019.020.021.0
0
500
1000
1500
2000
2500
3000
3500
0 2 4 6 8 10 12 14 16 18 20 22 24 26 28
Ft3
OF
LIM
ES
TO
NE
DIS
SO
LV
ED
BY
10
00
GA
LL
ON
S O
F H
Cl
AC
ID
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Relative Reaction Rates of 15% HCl with
Limestone Formations at 75° F.
0 5 10 15 20 25 30 350
10
20
30
40
50
60
70
80
90
100
* Atmospheric pressure at sea level
Curve
ABCD
Pressurepsi
14.7 *400800
1200
To
tal
Rea
ctio
n,
%
Minutes
D
C
A
B
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Relative Reaction Rates of 15% HCl with
Limestone Formations at 140° F.
Minutes
0 5 10 15 20 25 30 350
10
20
30
40
50
60
70
80
90
100 T
ota
l R
eact
ion
, %
Curve
ABCD
Pressurepsi
14.7 *40012002000
* Atmospheric pressure at sea level
A
B
D
C
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Relative Reaction Rates of 15% HCl with
Dolomite Formations at 75° F.
Minutes
0 20 40 60 80 100 120 140 0
10
20
30
40
50
60
70
80
90
100
To
tal
Rea
ctio
n,
%
* Atmospheric pressure at sea level
Curve
AB
Pressurepsi
14.7 *2000
A B
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Relative Reaction Rates of 15% HCl with
Dolomite Formations at 140° F.
0 10 20 30 40 50 60 700
10
20
30
40
50
60
70
80
90
100
To
tal
Rea
ctio
n,
%
Minutes
A
B
C D
* Atmospheric pressure at sea level
Curve
ABCD
Pressurepsi
14.7 *400
12002000