High pressure high CO2 removal configurations and methods

• US 9,248,398 B2
• Filed: 09/16/2010
• Issued: 02/02/2016
• Est. Priority Date: 09/18/2009
• Status: Active Grant

• Current Assignee: Fluor Technologies Corporation (Fluor Corporation)
• Original Assignee: Fluor Technologies Corporation (Fluor Corporation)
• Inventors: Mak, John
• Primary Examiner(s): Orlando, Amber
• Assistant Examiner(s): HOLECEK, CABRENA L
• Application Number:
  US13/496,302
• Publication Number:
  US 20120227441A1
• Time in Patent Office: 1,965 Days
• Field of Search: None
• US Class Current: 1/1
• CPC Class Codes: B01D 2256/245 Methane
• CPC Class Codes: B01D 53/1425 Regeneration of liquid absorbents
• CPC Class Codes: B01D 53/1475 Removing carbon dioxide
• CPC Class Codes: Y02C 20/40 of CO2

Abstract

CO2 is removed from high-pressure feed gas in configurations and methods according to the inventive subject matter by contacting feed gas with cooled semi-rich solvent to form a two-phase mixture that is flashed into the bottom section of an absorber. Rich solvent from the absorber is then reduced in pressure to generate refrigeration for the semi-rich solvent and lean solvent countercurrently contacts the partially treated feed gas in the absorber to produce the semi-rich solvent. Among other advantages, cooling of the feed gas and semi-rich solvent by the pressure reduced rich solvent heats the rich solvent to allow enhanced regeneration of the solvent, and external refrigeration and heating of the solvent can be entirely avoided.

Claims

1. A method of removing CO2 from a feed gas, comprising:

contacting the feed gas with a semi-rich solvent upstream of an absorber at a pressure above an absorber operating pressure to produce a two-phase mixture comprising a rich solvent and a partially treated feed gas;

separately cooling the semi-rich solvent and the feed gas prior to producing the two-phase mixture using refrigeration content generated by pressure reduction of the rich solvent; and

flashing the two-phase mixture into a bottom section of an absorber to the absorber operating pressure.

2. The method of claim 1 wherein the partially treated feed gas countercurrently contacts a lean solvent in the absorber to so produce the semi-rich solvent.

3. The method of claim 1 wherein cooling of the semi-rich solvent and the feed gas heats the pressure-reduced rich solvent to a temperature sufficient to allow flashing of a CO2 rich vapor from the heated pressure-reduced rich solvent.

4. The method of claim 1 wherein pressure reduction of the rich solvent comprises a step of flashing of the rich solvent, thereby producing flashed vapors and pressure-reduced rich solvent, and wherein the flashed vapors are combined with the feed gas.

5. The method of claim 4 wherein the pressure-reduced rich solvent is further flashed to produce a CO2 rich vapor and a lean solvent.

6. The method of claim 1 wherein substantially all of the heat required to produce a lean solvent from the rich solvent is provided by heat content of the feed gas and the semi-rich solvent.

7. The method of claim 1 wherein substantially all of the refrigeration that is required for absorption of the CO2 from the feed gas is generated by pressure reduction of the rich solvent.