safety and security for co 2 geological storage while co 2 /h 2 o/rock reaction
DESCRIPTION
Safety and Security for CO 2 Geological Storage while CO 2 /H 2 O/Rock Reaction. Bo Peng Enhanced Oil Recovery Research Center, China University of Petroleum, Beijing, China Sep.23, 2009 Canberra,Australia. Content. 1. Background 2. CO2 and Salt Solution Reaction - PowerPoint PPT PresentationTRANSCRIPT
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Safety and Security for CO2 Geological Storage while CO2/H2O/Rock Reaction
Bo Peng Enhanced Oil Recovery Research Center, China University
of Petroleum, Beijing, China
Sep.23, 2009 Canberra,Australia
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Content
1. Background 2. CO2 and Salt Solution Reaction 3. CO2 and Rocks Reaction 4. Wettability of the Rock 5. Permeability of the Rock 6. Safety and Security for CO2 Storage 7. Conclusion
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1.Background1.Reduction of Green House Gas Emission---A topic which
concerned around the world nowadays. Carbon Capture and Storage(CCS) is one of the most important technology.
①
②②
2-3℃
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1.Background
Biggest Emitters 2000-2025
24%
15%
12%6%4%
4%
35%USAChinaWest EuropeRussiaIndiaJ apanOther
Top six = 66%
Cumulative CO2 Emissions 2000-2025, EIA, IEA 2002
2. Chinese Government Concerns Greatly about Reduction of CO2 Emission and Utilization of It as Resources
Chairman Hu Jintao
Primer Wen Jiabao
“973”, “863” Reseach
Projects….
Petrochina,HuanengPil
ot Test….
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1.Background3. CO2 Storage and EOR in China
Oil&Gas Reservoir,
Subsurface Salaquifer, coal
bed, ideal Place for CO2
Storage
923 billion tons of CO2 can
be storaged in reservoir,
which is 45% of global
cumulative emission in
2050.
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1. Background4. Safety and Security for CCS have attracted more and mor
e attention.
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1. Background
CO2/H2O/Rock Reaction
Wettability Permeability
EOR and CO2 storage EOR and CO2 Storage
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NaCl
Salt Solution(Aqueous Solution)
Na2SO4
MgCl2
CaCl2
CaCO3
Ca(HCO3)2
Daqing Formation Water
The Effect Factors
Pressure
Tempreture
2. CO2 and Salt Solution Reaction
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CC
1
3
5
7
8
4
6
2
1. CO2 ; 5.Higher Pressure Vessel ; 8. pHS - 3C Meter
pH Measurement System in Higher Pressure
2. CO2 and Salt Solution Reaction
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0.0 0.5 1.0 1.5 2.0 2.53.0
3.5
4.0
4.5
5.0
5.5
6.0
6.5
7.0
7.5
pH
压力 / MPa
去离子水 0.1% 0.5% 1.0%
0.0 0.5 1.0 1.5 2.0 2.5
3.0
3.5
4.0
4.5
5.0
5.5
6.0
6.5
7.0
7.5
pH
压力 / MPa
去离子水 50 mg/L 300 mg/L 800 mg/L 1000 mg/L
NaCl Solution Na2SO4 Solution
2. CO2 and Salt Solution Reaction
Effect on pH by Pressure on Aqueous SystemsEffect on pH by Pressure on Aqueous Systems (25℃)
pH≈3.0
CO2:H2CO3in Water,
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0.0 0.5 1.0 1.5 2.0 2.5
3.0
3.5
4.0
4.5
5.0
5.5
6.0
6.5
7.0
pH
压力 / MPa
去离子水 50 mg/L 300 mg/L 800 mg/L 1000 mg/L
0.0 0.5 1.0 1.5 2.0 2.5
3.0
3.5
4.0
4.5
5.0
5.5
6.0
6.5
7.0
pH
压力 / MPa
去离子水 50 mg/L 200 mg/L 500 mg/L 1000 mg/L
CaCl2 SolutionMgCl2 Solution
2. CO2 and Salt Solution Reaction
Effect on pH by Pressure on Aqueous SystemsEffect on pH by Pressure on Aqueous Systems (25℃)
≈
pH≈3.0
CO2:H2CO3in Water,
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0.0 0.5 1.0 1.5 2.0 2.5
3.5
4.0
4.5
5.0
5.5
6.0
6.5
7.0
7.5
8.0
8.5
pH
压力 / MPa
去离子水 50 mg/L 300 mg/L 500 mg/L 1000mg/L
0.0 0.5 1.0 1.5 2.0 2.5
3.54.04.55.05.56.06.57.07.58.08.59.09.5
10.010.511.0
pH
压力 / MPa
去离子水 50 mg/L 300 mg/L 500 mg/L 800 mg/L
2. CO2 and Salt Solution Reaction
Effect on pH by Pressure on Aqueous SystemsEffect on pH by Pressure on Aqueous Systems (25℃)
Na2CO3 Solution NaHCO3 Solution
pH≥3.0
CO2:HCO3- in Wa
ter,
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NaCl NaHCO3 Na2CO3 Na2SO4 CaCl2 MgCl2·6H2O
1987.8 3013.11 170.38 1.00 1.99 6.97
0.0 0.5 1.0 1.5 2.0 2.5
5
6
7
8
9
10
pH
压力 / MPa
Daqing Formation Water ( mg/L )
2. CO2 and Salt Solution ReactionpH≥3.5
CO2:HCO3- in Wa
ter,
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0.0 0.5 1.0 1.5 2.0 2.52.0
2.5
3.0
3.5
4.0
4.5
5.0
5.5
6.0
pH
压力 / MPa
25℃ 40℃ 60℃
0.0 0.5 1.0 1.5 2.0 2.5
2.5
3.0
3.5
4.0
4.5
5.0
5.5
6.0
6.5
7.0
7.5
pH
压力 / MPa
25℃ 40℃ 60℃
10% CaCl2
10% MgCl2
Effect on pH by Temperture on Aqueous SystemsEffect on pH by Temperture on Aqueous Systems
2. CO2 and Salt Solution ReactionpH decrease while T goes up. H2CO3 give more H+
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Calcite PiecesCalcite PiecesHH22O + COO + CO22
Rock Surface TopograRock Surface Topographic Imagephic Image
Formation of the Solution Formation of the Solution
Calcite PowdersHH22O + COO + CO22
Permeability of Sand PipePermeability of Sand Pipe
SEMSEM
Ions Spectrum Ions Spectrum
Permeability Measurement Unit
3. CO2 and Rocks Reaction
Formation of the Solution Formation of the Solution
Rock Surface TopograRock Surface Topographic Imagephic Image
Formation of the Solution Formation of the Solution
Permeability of Sand PipePermeability of Sand Pipe
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取样1
2
3
4
P2
P1
1.CO2 ; 3.Reaction Vessel ; 4.Heating System ;
Reaction Unit in High Pressure Reaction Unit in High Pressure
3. CO2 and Rocks Reaction
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Rock CharacteristicRock Characteristic
Calcite:97.8%Calcite:97.8% ;; Dolomite:2.2%Dolomite:2.2%
d=9.
3611
d=3.
8503
d=3.
1185
d=3.
0295
d=2.
4913
d=2.
2801
d=2.
0911
d=1.
9236
d=1.
9077
d=1.
8711
d=1.
6009
d=1.
5224
d=1.
5141
d=1.
5037
d=1.
4179
10 20 30 40 50 60 70
2-Theta(°
x10 3̂
25
50
75
Inte
nsity
(CP
S)
[PYL3.ASC]
3. CO2 and Rocks Reaction
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Before Reaction
Rock Surface Topographic ImageRock Surface Topographic Image
Pressure : 2 MPa ; Temperature : 25 ℃; Reaction Time : 20days
3. CO2 and Rocks Reaction
After Reaction
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Before Reaction
Rock Surface Topographic ImageRock Surface Topographic Image
Pressure : 2 MPa ; Temperature : 25 ℃; Reaction Time : 20days
3. CO2 and Rocks Reaction
After Reaction
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Ion
TimeK+ Na+ Ca2+ Mg2+
Before Reaction
1.5 3.0 12.6 1.4
After Reaction
2.7 3.26 108 6.5
Ion in the solution before/after CO2 and Rock Reaction ( mg/L )
CaCO3 + H2O + CO2 Ca2+ + 2HCO3-
3. CO2 and Rocks Reaction
Pressure : 2 MPa ; Temperature : 25 ℃; Reaction Time : 20days
Rock Surface Topographic ImageRock Surface Topographic Image
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0 2 4 6 8 10 120
10
20
30
40
50
阳离
子浓
度 /
mg/
L
反应时间 / d
K+
Na+
Ca2+
Mg2+
0 2 4 6 8 10 12-200
0
200
400
600
800
1000
1200
1400
1600
HC
O3-
浓度
/ m
g/L
反应时间 / d
Ions in Formation Water Ions in Formation Water
3. CO2 and Rocks Reaction
Pressure : 2 MPa ; Temperature : 25 ℃;
Ca2+,HCO3-↑. 8 days Stably
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Ions in Formation Water Ions in Formation Water
3. CO2 and Rocks Reaction
Pressure : 2 MPa ; Temperature : 60℃;
0 2 4 6 8 10 12
0
100
200
300
400
500
600
700
800
阳离
子浓
度 /
mg/
L
反应时间 / d
K+
Na+
Ca2+
Mg2+
0 2 4 6 8 10 12
0
500
1000
1500
2000
HC
O3-
浓度
/ m
g/L
反应时间 / d
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Ions in Formation Water Ions in Formation Water
3. CO2 and Rocks Reaction
Pressure : 2 MPa ; Temperature : 90℃;
0 2 4 6 8 10
0
50
100
150
200
250
阳离
子浓
度 /
mg/
L
反应时间 / d
K+
Na+
Ca2+
Mg2+
0 2 4 6 8-200
0
200
400
600
800
1000
1200
1400
1600
HC
O3-
浓度
/ m
g/L
反应时间 / d
CO2↑
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Sand Core + Daqing Formation WaterCO2
Permeability of Sand Core
Rock Pieces +
Non-ion water
Daqing Formation Water
Dilute Daqing Formation Water
NaCl
CaCl2
CO2Contact Angle
CO2Contact Angle
CO2
Contact Angle
4. Wettability of the Rock
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d=4.
2569
d=4.
0331
d=3.
3446
d=3.
2465
d=3.
1918
d=2.
8833
d=2.
4584
d=2.
2828
d=2.
2371
d=2.
1291
d=1.
9808
d=1.
8189
d=1.
6724
d=1.
6593
d=1.
5424
d=1.
3827
d=1.
3727
10 20 30 40 50 60
2-Theta(°
x10 3̂
10
20
30
40
50
60
70
Inte
nsity
(CP
S)
[PYL1.ASC] <2T(0)=-0.16>
Silica Sand:97.7% ; Potash feldspar:0.6% ; Calcite:0.1% Dolomite:0.6% others:1% ;
4. Wettability of the Rock
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Non-ions Non-ions
Contact Angle: Rock Pieces + Non-ions + CO2
Time( d ) θa0 θa θa0 -θa
2 120.59° 120.52° 0.07°
4 119.57° 119.09° 0.48°
6 120.14° 118.08° 2.06°
8 120.65° 120.61° 0.04°
时间( d )
0 2 4 6
θa1 121.14° 120.30° 120.94° 120.94°
PressurePressure :: 1MPa1MPaTempretureTempreture :: 25 25 ℃
θa0 –No-CO2 ; θ a – CO2 ; θa1 – Water Treatment
4. Wettability of the Rock
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Daqing Formation WatDaqing Formation Water er
Contact Angle: Rock Pieces + Non-ions + CO2
PressurePressure :: 1MPa1MPaTempretureTempreture :: 25 25 ℃
θa0 –No-CO2 ; θ a – CO2 ; θa1 – Water Treatment
4. Wettability of the Rock
时间( d ) θa0 θa θa0 -θa
2 120.78° 61.61° 59.17°
4 117.35° 43.55° 73.80°
6 119.49° 51.63° 67.86°
8 118.39° 42.31° 76.09°
时间( d ) 0 2 4 6
θa1 122.93° 106.23° 107.06° 111.88°
Contact angle ↓ 。
NO CO2, NO Contact Angle Change.
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Pressure : 1 MPa Tempture : 25 ℃
Effect of Ions on Contact Angle Effect of Ions on Contact Angle
2 3 4 5 6 7 8
0
10
20
30
40
50
60
70
80
90
100
110
120
接触
角变
化 /
°
反应时间 / d
100% 去离子水 25% 大庆模拟水 +75% 去离子水 50% 大庆模拟水 +50% 去离子水 75% 大庆模拟水 +25% 去离子水100 % 大庆模拟水
4. Wettability of the Rock
More Daqing Water, More change on contact angle
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Pressure : 1 MPa Tempture : 25 ℃
Effect of Ions on Contact Angle Effect of Ions on Contact Angle
4. Wettability of the Rock
2 3 4 5 6 7 8
0
10
20
30
40
50
60
70
80
90
100
接触
角变
化 /
°
反应时间 / d
去离子水 0.01mol/kg 0.1mol/kg 0.5mol/kg
2 3 4 5 6 7 8
0
20
40
60
80
100
接触
角变
化 /
°
反应时间 / d
去离子水 0.01mol/kg 0.1mol/kg 0.5mol/kg
NaCl CaCl2
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5. Permeability of the Rock
1.N2 2.CO2 3. 5.Sand Filling Model 6. Pumper
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d=4.
2529
d=3.
3421
d=2.
4558
d=2.
2812
d=2.
2355
d=2.
1272
d=1.
9787
d=1.
8175
d=1.
6715
d=1.
6585
d=1.
5413
d=1.
3818
d=1.
3715
10 20 30 40 50 60 70
2-Theta(°
x10 3̂
25
50
75
Inte
nsity
(CP
S)
[PYL6.ASC]
Silica Sand:98.1.7% ; Potash feldspar:0.3% ; Calcite:0.3% Dolomite:1.2% others:0.1% ;
5. Permeability of the Rock
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Time(CO2)( d )
P ( kPa ) Permeability( mD )
Changement (%)
0 5.5 111.3 -2 5.0 122.5 10
7 4.0 153.1 37.6
Time(CO2)( d )
P ( kPa ) Permeability( mD )
Changement (%)
0 5.0 125.8 -
7 4.0 157.3 25
14 3.0 209.7 66.7
Effect of CO2 on permeability of Sand CoreEffect of CO2 on permeability of Sand Core
L : 50. 24 mm ; D: 25 .00 mm ; S : 25.57% ; T : 30℃
L : 51.60mm ; D : 25 mm ; S : 31.23% ; T : 30℃
5. Permeability of the Rock
CO2 Increase the permeability 。
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-2 0 2 4 6 8 10 12 14 16200
400
600
800
1000
1200
1400
反应时间 / d
渗透
率 /
mD
放置
通入 CO2
0 5 10 15 20100
150
200
250
300
350
400
渗透
率 /
mD
反应时间 /d
放置
通入 N2
通入 CO2
P:2MPa ; Reaction T: 65℃; Test T : 25 ℃
Silica sand: Calcit=1 : 1
5. Permeability of the Rock
Effect of CO2 on Permeability of Sand Filling Model Effect of CO2 on Permeability of Sand Filling Model
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6.Safety and Security for CO2 Storage
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6.Safety and Security for CO2 Storage
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6.Conclusion1. After carbon dioxide injection, pH of single brine, Daqing modeled
water dropped and then gradually decreased to a steady value. Magnesium chloride and calcium chloride solution (wt%=10%) pH decreased with temperature increase.
2. The SEM study shows that dissolution occurs on calcite surface. The Ca2+ and HCO3- concentration increased with reaction time to steady values. The time reach to steady is shorter with temperature increase.
3. The permeability of sand pipe filled with calcite and quartz increased with reaction time.
4. When inject into CO2, contact angle of cores slice in Daqing modeled water decreased and the proportion of Daqing modeled water is bigger, the change of contact angle is bigger.
5. The Safety and Security for CO2 Storage is correlated to the CO2/H2O/Rocks Reactions
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Thanks for your attention!