| Authors |
A. Shariat, SPE, R.G. Moore, SPE, S.A. Mehta, SPE, K.C. Van Fraassen, SPE,
University of Calgary; K.E. Newsham, SPE, J.A. Rushing, SPE, Apache
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| Source |
Carbon Management Technology Conference,
7-9 February 2012,
Orlando, Florida, USA
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| Preview |
Abstract
Disposal of carbon dioxide (CO2) in permeable, porous subsurface rock
formations (i.e., geological sequestration) has been identified as a viable
option for reducing greenhouse gas emissions into the Earth’s atmosphere.
Potential subsurface systems considered for geological sequestration include
depleted oil and gas reservoirs, coalbed methane and shale gas reservoirs, and
deep aquifers. Though each of these disposal systems has their advantages, deep
aquifers (mostly filled with non-potable or brackish waters) have the greatest
potential for large CO2 sequestration programs primarily because of their
relative abundance in most sedimentary basins and their large effective
capacities.
Successful selection of potential of CO2 deep aquifer sequestration sites,
however, requires an understanding of all physical and chemical trapping
mechanisms by which CO2 may be retained. Principle retention mechanisms in
aquifers include structural/stratigraphic (CO2 immobilization or trapping below
an impermeable confining layer), residual fluid (trapped as immobile fluid
phase in aquifer pore spaces), solubility (immobilized as fluid phase dissolved
in in-situ water), mineral
(immobilized as solid carbonate minerals formed from reaction with aquifer
rock), and hydrodynamic (CO2 dissolved in slow-moving water) trapping. While
all of these mechanisms contribute to CO2 sequestration, the
structural/stratigraphic and residual fluid mechanisms have the largest and
most immediate impact on trapping or retaining CO2 in aquifers.
The effectiveness of both structural/stratigraphic and residual fluid trapping
mechanisms is dependent on the capillary pressure characteristics of the
aquifer seal and formation, respectively. And, the capillary pressure
characteristics are strong functions of the interfacial tension (IFT)
properties of the carbon dioxide-water (CO2-H2O) system. Unfortunately, there
is a general lack of understanding of the CO2-H2O IFTs, particularly at
high-pressure/high-temperature (HP/HT) conditions typical of many potential
deep aquifer sites. The vast majority of published CO2-H2O IFT data were
obtained at pressures less than 10,000 psia and temperature less than about
250oF. Additionally, there are often inconsistencies among the existing data
published in the literature, thereby making it difficult to create predictive
models.
To address these inadequacies in the existing technical literature data base,
we conducted laboratory studies to measure CO2- H2O IFTs using a pendant drop
method at pressures between 1,000 and 18,000 psia and temperatures up to 400
oF. Rather than relying on correlations or previously published data, we also
measured water-vapor-saturated CO2 as well as CO2- saturated water densities
directly at each pressure and temperature. General observations from our
laboratory study include:
• CO2-H2O IFTs demonstrated a strong dependence on temperature (decreasing with
increasing temperature);
• For a given temperature, CO2-H2O IFTs were relatively insensitive to pressure
with values between 10 to 23 dynes/cm; values never fell below 10 dynes/cm for
all temperatures up to 400oF;
• Full miscibility between CO2 and H2O never occurred at any pressure and
temperature evaluated in the study;
• CO2-saturated water densities showed a strong dependence on pressure and
temperature, while water-vapor-saturated CO2 densities showed little change
from the CO2 density with no vapor content.
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