# US 8,783,371 B2 · Subsurface capture of carbon dioxide

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- Number: US 8,783,371 B2
- Document ID: US8783371B2
- Status: Granted
- Kind: B2
- Application number: 12/655,789
- Filed: 2010-01-07
- Published: 2010-07-08
- Granted: 2014-07-22
- Earliest claimed: 2009-01-08
- Applicants: Gerald Blount; Alvin A. Siddal; Ronald W. Falta
- Inventors: Gerald Blount; Alvin A. Siddal; Ronald W. Falta
- Web page: https://patentgrep.com/patent/US8783371B2

## CPC

- E21B 41/0064: {Carbon dioxide sequestration (storing fluids in porous layers B65G5/005)}
- Y02C 20/40: of CO2
- E21B: EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- Y02C: CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]

## Abstract

A process and apparatus of separating CO2 gas from industrial off-gas source in which the CO2 containing off-gas is introduced deep within an injection well. The CO2 gases are dissolved in the, liquid within the injection well while non-CO2 gases, typically being insoluble in water or brine, are returned to the surface. Once the CO2 saturated liquid is present within the injection well, the injection well may be used for long-term geologic storage of CO2 or the CO2 saturated liquid can be returned to the surface for capturing a purified CO2 gas.

## Claims

### Claim 1

A process of separating carbon dioxide from a waste gas comprising the steps of:
transporting said waste gas from above ground to a saturation module below ground, the saturation module being within a well, the waste gas comprising carbon dioxide and non-carbon dioxide gases, the waste the to the saturation module via a supply line:
transporting a liquid within the well, the liquid flowing downward below ground and within the well;
introducing said waste gas from the supply line into the liquid contained within said well at the saturation module, the carbon dioxide dissolving into the liquid following the introduction and the liquid becoming saturated with the carbon dioxide within the well, the non-carbon dioxide gases substantially insoluble in said liquid;
returning the non-carbon dioxide gases to above-ground via a first return line from the saturation module; and
removing the liquid that has been saturated with the carbon dioxide from the well.

### Claim 2 (depends on 1)

The process according to claim 1, further comprising supplying the waste gas to the well from an industrial source.

### Claim 3 (depends on 1)

The process according to claim 1, wherein said well is about 2,000 feet below ground surface.

### Claim 4 (depends on 1)

The process according to claim 1, wherein the process utilizes more than one saturation module.

### Claim 5 (depends on 1)

The process according to claim 1, wherein the liquid is water or brine.

### Claim 6 (depends on 1)

The process according to claim 1, wherein the liquid that has been saturated with the carbon dioxide is removed from the well to above-ground via a second return line.

### Claim 7 (depends on 6)

The process according to claim 6, further comprising capturing the carbon dioxide that saturated the liquid, the carbon dioxide that is captured being substantially free of the non-carbon dioxide gases.

### Claim 8 (depends on 7)

the process according to claim 7, further comprising returning the liquid to the well in a recirculation loop.

### Claim 9 (depends on 1)

The process according to claim 1, further comprising directing the non-carbon dioxide to an energy recovery subsystem.

### Claim 10 (depends on 1)

The process according to claim 1, further comprising compressing the waste gas prior to transporting the waste gas to the saturation module within the well.

### Claim 11 (depends on 1)

The process according to claim 1, wherein the saturation module comprises a counter-flow bubble column.