1
Multi-phase flow experiments of CO 2 and brine in reservoir rocks Jean-Christophe Perrin and Sally Benson Department of Energy Resources Engineering, Stanford University THE SEQUESTRATION LAB CASE 2: flow rate effect CASE 1: heterogeneity effect LAB The goal of the Sequestration Lab is to develop the ability to predict the spatial and temporal Experimental conditions -T = 63C -P=1800 psi / 12.4 Mpa Experimental conditions -T = 50C -P=1300 psi / 9 Mpa Sample: Berea Sandstone Core-scale multiphase flow experiments and temporal distribution of CO 2 saturation and trapping through an improved understanding of the pore and core scale Otway Project Well CRC-1 Otway basin, Australia -P=1800 psi / 12.4 Mpa -Brine composition = 6g/L NaCl+ 0.5 g/L CaCl 2 Procedure -drainage at 2 mL/min -the fractional flow of CO 2 is progressively increased -steady state is achieved for each step 0 0.3 0.15 -Brine composition = 10g/L NaCl Procedure -drainage at 2.6, 1.2 and 0.5 mL/min -the fractional flow of CO 2 is progressively increased -steady state is achieved for each step Sample: 5.08 cm diameter Sample: 5.08 cm diameter 15.24 cm long k = 450mD Numerical simulations pore and core scale physics over the life cycle of a sequestration project. 5% 30% 50% f CO2 Porosity map -steady state is achieved for each step 25% 50% 80% f CO2 Total Flow rate mL/min 2.6 -steady state is achieved for each step 5.08 cm diameter 8.5 cm long k = 50mD The rock is very INTRODUCTION / BACKGROUND Relative permeability is a key concept for carbon dioxide storage. Defined in multi- phase flow in porous media as the ratio of effective permeability of a particular fluid at a particular saturation to absolute permeability of that fluid at total saturation, relative permeability controls the majority of the phenomena that are met when two (or more) fluids are flowing through rocks. 70% 85% 100% S CO2 13.19% 19.70% 23.50% Inlet Top The rock is very S CO2 5% 21% 34% 1.2 Brine Saturation The rock is very heterogeneous with a structure composed of successive layers that are not parallel to the main axis of the cylinder. Contrarily to the commonly accepted theory, the CO 2 saturation is a function of that are met when two (or more) fluids are flowing through rocks. Studying the relative permeability properties of the CO 2 -brine system in deep saline aquifers is fundamental to answer important questions that are met in the field. For instance: - What should be the pressure in the injection zone? - How big the plume is going to be? - How fast would CO 2 leak up a fault under buoyancy? - How to maximize sweep efficiency (storage capacity)? 27.80% 41.44% 55.63% The rock is very heterogeneous, with a broad distribution of pore size. The structure is clearly visible in the porosity map. There is a strong correlation porosity / CO 2 saturation with a high CO 2 saturation corresponding to a high 5% 20% 25% Inlet Top 0.5 saturation is a function of the total flow rate. As a consequence, the relative permeability varies with flow rate. The higher the flow rate, the higher the CO 2 saturation - How to maximize sweep efficiency (storage capacity)? In the laboratory, relative permeability experiments associated with fine rock characterizations are performed in order to address more fundamental issues. For instance: -What are the trapping mechanisms? - How do the external factors influence relative permeability (pressure, temperature, injection rates, rock properties/structure)? CO 2 saturation corresponding to a high porosity. There is no visible gravity override. 2% 11% 24% Effect on CO 2 saturation for different fractional flow Effect on Relative Permeability higher the CO 2 saturation and the lower the relative permeability at a given saturation. temperature, injection rates, rock properties/structure)? EXPERIMENTAL PROCEDURE Thermophysical properties of brine and CO 2 at experimental conditions 1 5 4 3 3 CONCLUSIONS Brine saturation 3 2 1 1 2 CASE 3: Gravity effect CONCLUSIONS Studying relative permeability properties of CO 2 and brine in reservoir rocks is of major importance for carbon sequestration. In the lab, we see that: -When the core is structured, the heterogeneities are controlling the spatial distribution of CO 2 at Sample: 5.08 cm dia. 20.2 cm long k = 150 mD Berea Sandstone 15% 25% 35% f CO2 S CO2 5% 7.19% 11.82% 15.75% 17.88% Porosity map Inlet Top Rock sample 3 AN ALUMINUM COREHOLDER CONTAINS THE CORE Aluminum 1/2 inch thick 3 PUMPS INJECT HIGH-PRESSURE CO 2 AND BRINE A system of dual-pumps (A & B) using electric valves injects fluids continuously and refills automatically. Max Pressure: 3750 psi. 1 SEPARATOR Used to separate the two fluids after they flow through the core. 2 A MEDICAL CT SCANNER PRODUCES IMAGES OF THE CORE’S INTERIOR DISTRIBUTION OF CO 2 AND BRINE Saturation profiles are derived from these images. Images are taken in real time 4 2 steady state. The less porous layers are hardly invaded. -When the sample is homogeneous and the injection flow rate is low enough, gravity effects become important and the CO 2 invades preferentially the top part of the core. -CO 2 saturation and relative permeability are seen to be flow rate dependant. At higher flow rate, CO 2 Conditions -T = 63C -P=1800 psi / 12.4 Mpa -Brine composition = 6g/L NaCl+0.5g/L CaCl 2 Procedure 65% 80% 90% 50% 98% 100% 95% 21.31% 24.02% 28.19% 31.46% The sample is very homogeneous with very little variations of porosity along the Aluminum 1/2 inch thick Rated to 3000 psi, 100°C For use with core up to 8 in. long (2 in. diameter) Fluids are distributed at the inlet and outlet ends by concentric grooves machined into the aluminum. Heaters keep fluid inside the core- holder at reservoir temperature. Max Pressure: 3750 psi. Flow rate: 1μL/min - 200mL/min Pump D applies confining pressure around the core to mimic reservoir conditions. Pump C creates back-pressure after separator. Also serves as a buffer container between separator and injection pumps. Images are taken in real time during injection experiments. A DATA LOGGER RECORDS: Temperature and confining pressure inside the coreholder. Flow rate, pressure, delivered volume at each pump. Pressure drop across the core. 5 2 saturation is higher and relative permeability lower. - Numerical simulations are underway to validate these observations (see Chia-Wei Kuo’s poster) as well as sub-core scale analysis (see Michael Krause’s poster). -drainage at 1mL/min -the fractional flow of CO 2 is progressively increased -steady state is achieved for each step 34.05% 36.54% 38.19% variations of porosity along the core and no visible structure. Once injected slowly into the core, CO 2 is rising up under the influence of gravity.

Multi-phase flow experiments of CO2 ... - Stanford University

  • Upload
    others

  • View
    4

  • Download
    0

Embed Size (px)

Citation preview

Page 1: Multi-phase flow experiments of CO2 ... - Stanford University

Multi-phase flow experiments of CO2 and brine in reservoir rocksJean-Christophe Perrin and Sally Benson

Department of Energy Resources Engineering, Stanford University

THE SEQUESTRATION LAB

CASE 2: flow rate effectCASE 1: heterogeneity effectLABThe goal of the Sequestration Lab is to develop the ability to predict the spatial and temporal

Experimental conditions

-T = 63C-P=1800 psi / 12.4 Mpa

Experimental conditions

-T = 50C-P=1300 psi / 9 MpaSample:

Berea Sandstone

Core-scale multiphase flowexperiments

and temporal distribution of CO2saturation and trapping through an improved understanding of the pore and core scale

Otway ProjectWell CRC-1

Otway basin, Australia

-P=1800 psi / 12.4 Mpa-Brine composition = 6g/L NaCl+ 0.5 g/L CaCl2

Procedure

-drainage at 2 mL/min-the fractional flow of CO2 is progressivelyincreased-steady state is achieved for each step

0 0.30.15

-P=1300 psi / 9 Mpa-Brine composition = 10g/L NaCl

Procedure

-drainage at 2.6, 1.2 and 0.5 mL/min-the fractional flow of CO2 is progressivelyincreased-steady state is achieved for each step

Sample:5.08 cm diameter

Sample:5.08 cm diameter15.24 cm longk = 450mDNumerical

simulations

pore and core scale physics over the life cycle of a sequestration project.

5% 30% 50%fCO2

Porosity map

-steady state is achieved for each step

25% 50% 80%fCO2

TotalFlow rate

mL/min

2.6

-steady state is achieved for each step5.08 cm diameter8.5 cm longk = 50mD

The rock is very

INTRODUCTION / BACKGROUNDRelative permeability is a key concept for carbon dioxide storage. Defined in multi-phase flow in porous media as the ratio of effective permeability of a particular fluid at a particular saturation to absolute permeability of that fluid at total saturation, relative permeability controls the majority of the phenomena that are met when two (or more) fluids are flowing through rocks.

70% 85% 100%

SCO2 13.19% 19.70% 23.50%

Inlet

Top

The rock is very

SCO2 5% 21% 34%

2.6

1.2

Brine Saturation

The rock is very heterogeneous with a structure composed of successive layers that are not parallel to the main axis of the cylinder. Contrarily to the commonly accepted theory, the CO2

saturation is a function of that are met when two (or more) fluids are flowing through rocks.Studying the relative permeability properties of the CO2-brine system in deep saline aquifers is fundamental to answer important questions that are met in the field. For instance:- What should be the pressure in the injection zone?- How big the plume is going to be?- How fast would CO2 leak up a fault under buoyancy?- How to maximize sweep efficiency (storage capacity)?

27.80% 41.44% 55.63%

The rock is very heterogeneous, with a broad distribution of pore size. The structure is clearly visible in the porosity map. There is a strong correlation porosity / CO2 saturation with a high CO2 saturation corresponding to a high

5% 20% 25%

Inlet

Top

0.5

2

saturation is a function of the total flow rate. As a consequence, the relative permeability varies with flow rate.

The higher the flow rate, the higher the CO2 saturation - How to maximize sweep efficiency (storage capacity)?

In the laboratory, relative permeability experiments associated with fine rock characterizations are performed in order to address more fundamental issues. For instance:-What are the trapping mechanisms?- How do the external factors influence relative permeability (pressure, temperature, injection rates, rock properties/structure)?

CO2

satu

rati

on

corresponding to a high porosity. There is no visible gravity override.

2% 11% 24%

Effect on CO2 saturationfor different fractional flow

Effect on Relative Permeability

higher the CO2 saturation and the lower the relative permeability at a given saturation.

temperature, injection rates, rock properties/structure)?

EXPERIMENTAL PROCEDURE

Thermophysical properties of brine and CO2 at experimental conditions

1 5

4

3

3

CONCLUSIONS

Brine saturation

3

2

11

2 CASE 3: Gravity effect CONCLUSIONSStudying relative permeability properties of CO2

and brine in reservoir rocks is of major importance for carbon sequestration. In the lab, we see that:-When the core is structured, the heterogeneities are controlling the spatial distribution of CO2 at

Sample:5.08 cm dia.20.2 cm longk = 150 mD

Berea Sandstone15% 25% 35%fCO2

SCO2

5%

7.19% 11.82% 15.75% 17.88%

Porosity map

Inlet

Top

Rock sample

3

AN ALUMINUM COREHOLDERCONTAINS THE CORE Aluminum 1/2 inch thick

3PUMPS INJECT HIGH-PRESSURE CO2 AND BRINE

A system of dual-pumps (A & B) using electric valves injects fluids continuously and refills automatically. Max Pressure: 3750 psi.

1

SEPARATOR Used to separate the two fluids after theyflow through the core.

2A MEDICAL CT SCANNER

PRODUCES IMAGES OF THECORE’S INTERIOR DISTRIBUTIONOF CO2 AND BRINE Saturation profiles arederived from these images. Images are taken in real time

4

are controlling the spatial distribution of CO2 at steady state. The less porous layers are hardly invaded.-When the sample is homogeneous and the injection flow rate is low enough, gravity effects become important and the CO2 invades preferentially the top part of the core.-CO2 saturation and relative permeability are seen to be flow rate dependant. At higher flow rate, CO2

Conditions

-T = 63C-P=1800 psi / 12.4 Mpa-Brine composition = 6g/L NaCl+0.5g/L CaCl2

Procedure

65% 80% 90%50%

98% 100%95%

21.31% 24.02% 28.19% 31.46%

The sample is very homogeneous with very little variations of porosity along the

Aluminum 1/2 inch thick Rated to 3000 psi, 100°C For use with core up to 8 in.long (2 in. diameter) Fluids are distributed at theinlet and outlet ends by concentricgrooves machined into the aluminum. Heaters keep fluid inside the core-holder at reservoir temperature.

Max Pressure: 3750 psi. Flow rate: 1µL/min - 200mL/min Pump D applies confining pressure around the coreto mimic reservoir conditions. Pump C creates back-pressure after separator. Alsoserves as a buffer container between separator andinjection pumps.

Images are taken in real timeduring injection experiments.

A DATA LOGGER RECORDS: Temperature and confiningpressure inside the coreholder. Flow rate, pressure, deliveredvolume at each pump. Pressure drop across the core.

5

to be flow rate dependant. At higher flow rate, CO2

saturation is higher and relative permeability lower. - Numerical simulations are underway to validate these observations (see Chia-Wei Kuo’s poster) as well as sub-core scale analysis (see Michael Krause’s poster).

-drainage at 1mL/min-the fractional flow of CO2 is progressivelyincreased-steady state is achieved for each step

34.05% 36.54% 38.19%

variations of porosity along the core and no visible structure. Once injected slowly into the core, CO2 is rising up under the influence of gravity.