Carbon dioxide recovery from an oxygen containing mixture

• US 6,174,506 B1
• Filed: 06/10/1999
• Issued: 01/16/2001
• Est. Priority Date: 06/10/1999
• Status: Expired due to Term

• Current Assignee: Praxair Technology Incorporated (Linde Plc)
• Original Assignee: Praxair Technology Incorporated (Linde Plc)
• Inventors: Chakravarti, Shrikar, Gupta, Amitabh
• Primary Examiner(s): Griffin, Steven P.
• Assistant Examiner(s): Vanoy, Timothy C
• Application Number:
  US09/329,279
• Time in Patent Office: 586 Days
• Field of Search: 423/229, 423/228, 423/220, 423/219, 952/63, 952/65
• US Class Current: 423/220
• CPC Class Codes: B01D 53/1418 Recovery of products
• CPC Class Codes: C01B 32/50 Carbon dioxide
• CPC Class Codes: Y02C 20/40 of CO2
• CPC Class Codes: Y02P 20/151 Reduction of greenhouse gas [GHG] emissions, e.g. CO2

Abstract

A process for recovering carbon dioxide from a gas containing both carbon dioxide and oxygen wherein a carbon dioxide and oxygen containing gas is first contacted with an alkanolamine solution to produce an alkanolamine loaded with carbon dioxide and oxygen, the oxygen is separated from the absorption solution, such as by stripping with a scavenging gas, such as the carbon dioxide containing fluid obtained from the separation of carbon dioxide from the alkanolamine solution or nitrogen, prior to any heating of the absorption solution, and carbon dioxide is steam stripped from the absorption solution and recovered. By stripping the oxygen out of the alkanolamine solution, oxidative degradation of the alkanolamine can be reduced.

Claims

1. A method for recovering carbon dioxide from a carbon dioxide containing gas, comprising:

a) passing a gas comprising carbon dioxide and oxygen in countercurrent contact with an absorbent solution comprising at least one alkanolamine and transferring carbon dioxide and oxygen from said gas into said absorbent solution;

b) separating oxygen from the carbon dioxide and oxygen containing absorbent solution by countercurrently contacting the carbon dioxide and oxygen containing absorbent solution with an oxygen scavenging gas to obtain an oxygen depleted, carbon dioxide containing absorbent solution;

c) heating the oxygen depleted, carbon dioxide containing absorbent solution to obtain a heated oxygen depleted, carbon dioxide containing absorbent solution;

d) separating carbon dioxide from the heated oxygen depleted, carbon dioxide containing absorbent solution, and

e) recovering carbon dioxide from the absorbent solution to obtain a regenerated absorbent solution and a carbon dioxide rich fluid.

2. The method of claim 1, wherein the carbon dioxide is separated from the heated oxygen depleted, carbon dioxide containing absorbent solution by countercurrently contacting the heated oxygen depleted, carbon dioxide containing absorbent solution with steam.

3. The method of claim 1, wherein the heat of the regenerated absorbent solution is transferred to the oxygen depleted, carbon dioxide containing solution via indirect heat exchange to obtain said heated oxygen depleted, carbon dioxide containing absorbent solution.

4. The method of claim 1, wherein said oxygen scavenging gas comprises at least a portion of said carbon dioxide rich fluid.

5. The method of claim 1, wherein said oxygen scavenging gas is nitrogen.

6. The method of claim 1, wherein oxygen scavenging gas is passed into said carbon dioxide rich fluid.