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PNNL-13501 - Pacific Northwest National Laboratory

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injection of an immiscible gas phase into confined formations<br />

(representing deep saline aquifers and reservoirs), its<br />

axisymmetric flow around the injector, and eventual<br />

buoyancy-driven transport with simultaneous dissolution<br />

and mineral trapping. In addition, a numerical model<br />

(STOMP-CO2) has been developed by adding additional<br />

phase behavior algorithms to our STOMP simulator.<br />

Results and Accomplishments<br />

Simple and easy-to-use modeling tools would be valuable<br />

for assessing the performance of a deep-well operation<br />

during and after injection. We have completed a semianalytical<br />

model (PNLCARB) and a numerical model<br />

(STOMP-CO2) by adding additional phase behavior<br />

algorithms to the STOMP simulator, to model<br />

1) multiphase, radial injection of CO2 and the growth of<br />

its area of review around the injector, 2) buoyancy-driven<br />

migration of CO2 toward the top confining layer, and<br />

3) dissolution of CO2 during injection and vertical<br />

migration, and the resulting aqueous speciation of carbon.<br />

The models effectively simulate deep-well injection of<br />

water-immiscible, gaseous or supercritical CO2.<br />

Equations governing the radial injection of CO2 into deep<br />

saline aquifers, its axisymmetric flow around the injector<br />

and eventual buoyancy-driven floating with simultaneous<br />

dissolution were formulated. The effect of pertinent fluid,<br />

reservoir and operational characteristics on the deep-well<br />

injection of CO2 was investigated. Shown in Figures 1<br />

through 4 are some key findings from simulations using<br />

PNLCARB1.0 and STOMP-CO2. Results indicate that<br />

the injected CO2 phase initially grows as a bubble radially<br />

outward, dissolves partially in the formation waters,<br />

eventually floats toward the top due to buoyancy, and<br />

settles near the top confining layer. Formation<br />

permeability, porosity, the rate and pressure of injection,<br />

and the rate of dissolution of CO2 influence the growth<br />

and ultimate distribution of the CO2 phase.<br />

Radius of CO2 bubble (Km)<br />

10<br />

8<br />

6<br />

4<br />

2<br />

Sg=0.095<br />

0.195<br />

0.295<br />

0.395<br />

0.495<br />

0.595<br />

0.695<br />

0.795<br />

0.895<br />

0<br />

0 8000 16000 24000 32000 40000<br />

Time (days)<br />

Figure 1. CO 2 saturation profiles at thousands of days after<br />

injection<br />

234 FY 2000 <strong>Laboratory</strong> Directed Research and Development Annual Report<br />

CO 2 saturation, S g<br />

1.2<br />

1.0<br />

0.8<br />

0.6<br />

0.4<br />

0.2<br />

0.0<br />

0 2000 4000 6000 8000 10000 12000 14000<br />

Radial distance, rs (m)<br />

Publication<br />

Eq. 8<br />

Eq. 4<br />

Figure 2. As a function of radial distance away from well<br />

Height of CO 2 -water contact (m)<br />

120<br />

0 5000 10000 15000 20000<br />

Radial distance from well (m)<br />

Figure 3. Effect of injection rate on ultimate CO2-water contact<br />

120<br />

100<br />

80<br />

60<br />

40<br />

20<br />

160<br />

140<br />

Qc=27540 m 3 /d<br />

Qc=275400 m 3 /d<br />

50 100 150 200<br />

Figure 4. CO 2 bubble growth prediction by STOMP-CO 2 at<br />

a low flow rate<br />

Saripalli P. 2000. Simulations using PNLCARB1.0 to<br />

model deep-well injection of CO2 for geological<br />

sequestration at Mt. Simon Site. Prepared for BCO<br />

Columbus, as a part of model validation effort for<br />

DOE-FE funded research project.<br />

A

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