Process for capturing acid gases

Patent metadata

Field	Value
Publication number	US-9586174-B2
Application number	US-201213980161-A
Country	US
Kind code	B2
Filing date	Jan 18, 2012
Priority date	Jan 18, 2011
Publication date	Mar 7, 2017
Grant date	Mar 7, 2017

Abstract

An absorption column 1 for separating CO 2 and a second acid gas from a gas stream, the column comprising a first and second section ( 4, 5 ) for the absorption of CO 2 and the second acid gas; a solvent inlet in the second section for the addition of liquid stream 3 including an absorbent liquid for CO 2 and the second acid gas; a gas inlet ( 21 ) in the first section for the addition of a gas stream ( 2 ) containing CO 2 and the second acid gas; a gas outlet ( 15 ) in the second section of the column; a first solvent outlet ( 22 ) for the removal of at least a portion of the solvent ( 6 ) from the second section of the column and a second solvent outlet ( 23 ) for solvent stream ( 11 ) from the first section of the column; and a liquid flow distributor arrangement ( 8 ) to allow a portion of the solvent to flow from the second section of the column to the first section. A method of operating the apparatus and method of solvent extraction is also disclosed.

First claim

The claims defining the invention are as follows:

1. A post combustion capture process for removing CO 2 and at least one second acid gas from a flue gas stream including the steps of:
providing a flue gas stream containing CO 2 in the range of 1 to 30 vol %, and at least one second acid gas to an absorption column, the absorption column having at least separate first and second sections within said absorption column, the gas stream being provided to the first section of the column,
providing a solvent comprising an absorbent liquid for CO 2 and the second acid gas to the second section to flow counter current to the gas stream, said solvent successively passing through both the second section and the first section of the column, with at least a portion of said solvent being removed from the absorption column once said solvent has passed through the second section and prior to said solvent passing through the first section,
passing the gas stream through the absorption column preferentially absorbing the second acid gas into said solvent in the first section of the absorption column before passing to the second section of the absorption column where CO 2 is absorbed into said solvent,
recovering gas depleted in CO 2 and the second acid gas from the second section of the column.

2. The process of claim 1 wherein a liquid flow distributor prevents liquid from flowing directly between the second and first sections of the column while allowing gas to pass through, the solvent from the first section is removed and regenerated, and the regenerated solvent streams are returned to the second section of the absorption column.

3. The process of claim 1 wherein a liquid flow distributor between the first and second section allows liquid to flow directly from the second section to the first section and a portion of the solvent is removed from the column prior to entering the first section of the column.

4. The process of claim 1 wherein the solvent removed prior to the first section is subsequently processed to remove the CO 2 before being returned to the absorption column.

5. The process of claim 1 wherein the solvent removed from the absorption column prior to the first section is subsequently processed to remove the second acid gas and then returned to the absorption column.

6. The process of claim 1 wherein at least a portion of the solvent removed from the absorption column prior to the first section is recycled to the top of the first section.

7. The process of claim 1 wherein the second acid gas is selected from the group of SO 2 , H 2 S, HF, HCl and NO 2 .

8. The process of claim 1 wherein the gas stream contains CO 2 in the range of 3 to 30 vol %.

9. The process of claim 1 wherein the solvent stream entering the first section of the column has a CO 2 content of between 0 and 200% of the saturated CO 2 content.

Assignees

• Meuleman Erik Everhardus Bernardus
• Puxty Graeme
• Feron Paul
• Commw Scient Ind Res Org

Inventors

• Meuleman Erik Everhardus Bernardus
• Puxty Graeme
• Feron Paul

Classifications

• Y02C20/40

  of CO2 · CPC title

• B01D53/1456 Primary

  Removing acid components · CPC title

• B01D2252/20484

  with one hydroxyl group · CPC title

• B01D2257/2047

  Hydrofluoric acid · CPC title

• B01D53/1462

  Removing mixtures of hydrogen sulfide and carbon dioxide · CPC title