fundamental studies of multiphase flow jean...
TRANSCRIPT
0
500
1,000
1,500
2,000
2,500
Residential Commercial Industrial Transportation Electricity Gen.
Tg C
O2
Eq
.
FUNDAMENTAL STUDIES OF MULTIPHASE FLOW OF CO2 AND BRINE: EXPERIMENTS AND SIMULATIONS
JEAN-CHRISTOPHE PERRINLJUBA MILJKOVIC
SALLY BENSON
LABORATORY EXPERIMENTSOPPORTUNITYCT MAP OF CORE POROSITY IS USED TO CALCULATE PERMEABILITY
SIMULATIONS COMPARED TO LAB EXPERIMENTS
0
10
20
30
3.0 0.5 0.1 0.01
Injection Flow Rate (ml/min)
% C
O2
Sat
urat
ion
0
25
50
10% 90% 100%
HomogeneousHeterogeneous
FLOW RATE DEPENDENCE DECREASED SWEEP EFFICIENCY
% CO2 Injected
SIMULATION GRID SIZE DEPENDENCE
60 x 60
36 x 36
16 x 16
0 10 20 30
29.0
28.0
27.1
Grid
Res
olut
ion
% CO2 Saturation
10%
90%
100%
LAB EXPERIMENTS UNIFORM PC VARIABLE PC
CO2 SATURATION:0% 100%50%25% 75%
๏ What fraction of the pore space can be filled with CO2?๏ How big will the CO2 plume be?๏ How much CO2 will be dissolved?
๏ How much will capillary trapping immobilize CO2?๏ Can accurate models be developed to predict CO2 fate and transport?
KEY ISSUES FOR CO2 STORAGE IN DEEP SALINE AQUIFERS
CAPILLARY FORCES HETEROGENEITY GRAVITY STRUCTURE
AN ALUMINUM CORE-HOLDER CONTAINS THE CORE
A MEDICAL CT SCANNER PRODUCES IMAGES OF THE CORE’S INTERIOR DISTRIBUTION OF CO2 AND BRINE
MEASUREMENTS ARE MADE AT REALISTIC RESERVOIR CONDITIONS
NUMERICAL SIMULATIONS
Coal Petroleum Natural Gas
2004 CO2 Emissions from Fossil Fuel Combustion by Sector and Fuel Type
OPPORTUNITY FOR CARBON CAPTURE AND STORAGE (CCS)
OVERVIEW OF GEOLOGIC STORAGE OPTIONS
Answering these questions depends on the complex interplay of viscous
and capillary forces, heterogeneity, buoyancy forces, and structure on CO2
plume migration.
๏ Aluminum ½ inch thick
๏ Rated to 3000 psi, >100°C
๏ For use with core up to 8 in. (2 in. diameter)
๏ Fluids are distributed at the inlet and outlet
ends by concentric grooves machined into
the aluminum.
Pressure Port Outlet Port
Confining
Pressure Port
Pressure Port
Inlet Port
PUMPS INJECT HIGH-PRESSURE CO2 AND BRINE INTO THE CORE-HOLDER
DUAL PUMPS DUAL PUMPS๏ A system of dual-pumps
(A & B) using electric valves
injects fluids continuously and
refills automatically.
๏ Max Pressure: 3750 psi.
๏ Flow rate: 1µL/min - 200mL/min
๏ CO2 is cooled to 5°C in the
pumps to keep it liquid.
๏ Brine is kept at room temp.
A DATA LOGGER RECORDS:
๏ Temperature and confining
pressure inside the core-holder.๏ Flow rate, pressure, delivered
volume at each pump.๏ Pressure drop accross the core.
HEATERS KEEP FLUID INSIDE THE CORE-HOLDER AT RESERVOIR TEMPERATURES
CORE
ADDITIONAL PUMPS:๏ 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.
SEPARATOR:๏ Used to separate two fluids after they flow
through the core.
A MOBILE EXPERIMENT:๏ The experimental setup can be moved from
the lab to the CT scanner room.
๏ Band heaters hold core at up to 80°C.
๏ A Fluid heater keeps CO2 and brine at up to 80°C before
entering the core.
๏ Images are taken in real time during injection experiments.
๏ Saturation profiles can be derived from these images.
These measurements are necessary
for relative permeability calculations.
7.8 cm 7.8 cm
POROSITY MAP PERMEABILITY MAP
12% 33%22% 30mD 1000mD500mD
KOZENY-CARMEN
ki =!3
i
S(1! !i)2
RELATIVE PERMEABILITY CURVES ARE BASED ON EXPERIMENTAL DATA
Rel
ativ
e P
erm
eabi
lity
0
0.25
0.50
0.75
1.00
0 0.2 0.4 0.6 0.8 1.0
BRINECO2
Brine Saturation
0.2 0.4 0.6 0.8 1.0
Pc,i =
!!̄i
k̄i! J(S)
NEW CAPILLARY PRESSURE FUNCTIONAL FORM
Simulation Input Curve*
Hg Injection Data Points
1000
10,000
100,000
Cap
illar
y P
ress
ure
(Pa)
Brine Saturation *Silin Et Al. (submitted, 2007)
๏ A new functional form is fit to capillary pressure data from the rock lab.
๏ The shape of the curve can vary with respect to the porosity and permeability of each grid element i.
NEW CAPILLARY PRESSURE FUNCTIONAL FORM
INLET
SIMULATED
CORE
OUTLET
๏ TOUGH2 is a general purpose simulator.๏ Need special boundary conditions.๏ Inlet slice injects evenly over entire face of core.๏ Outlet is “out of capillary contact” with end of core.
IMPLICATIONS FOR CO2 STORAGE
๏ Core-scale lab experiments were simulated to investigate cause of CO2 saturation variations
๏ Only variable capillary pressure curves seem to account for this๏ Variable Pc reduces overall CO2 saturation๏ CO2 saturation is flowrate/grid-size dependent๏ Current field-scale simulations most likely overestimate CO2 saturation
SUMMARY
SCHEMATIC OF POSSIBLE CCS SYSTEMS
SALINE AQUIFERS HAVE THE GREATEST STORAGE CAPACITY
Saline Aquifers Oil and Gas Fields Inminable Coal Seams
GtC
O2
1000 - 10,000
675
3-15
CO2
Tank
PUMP D: Confining P
PUMP C:H2O
S
PUMP A2: CO2
SS
PUMP A1: CO2
Separa
tor
PUMP B2: H2O
S
PUMP B1: H2O
S
Fluid Heater
Pressure Regulator
Safety Valve
Shutoff Valve
R
S
Check Valve
Pressure Transducer
Particle Filter (15µm)
Electric Valve
S
Water
Chiller 5°C
R
Electric Band Heaters
Core Holder