Carbon dioxide recovery with composite amine blends

• US 6,165,433 A
• Filed: 06/10/1999
• Issued: 12/26/2000
• 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): Warn, Elin A
• Application Number:
  US09/329,259
• Time in Patent Office: 565 Days
• Field of Search: 423/228, 423/229, 423/437.1
• US Class Current: 423/229
• CPC Class Codes: B01D 53/1475 Removing carbon dioxide
• CPC Class Codes: B01D 53/1493 Selection of liquid materials for use as absorbents
• 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 method for recovering carbon dioxide by absorption of carbon dioxide from a gas stream into a composite recovery solvent comprising preferably a lesser concentration of one or more fast reaction rate amines and a greater concentration of one or more slow reaction rate amines.

Claims

1. A method for recovering carbon dioxide comprising:

(A) passing feed gas comprising carbon dioxide at a partial pressure of 10 psia or less in mass transfer contact with a recovery solvent comprising water, from 5 to 35 weight percent of at least one fast reaction rate amine, and from 5 to 50 weight percent of at least one slow reaction rate amine;

(B) passing carbon dioxide from the feed gas to the recovery solvent to produce carbon dioxide depleted gas and carbon dioxide loaded recovery solvent;

(C) separating carbon dioxide from the carbon dioxide loaded recovery solvent to produce carbon dioxide rich fluid; and

(D) recovering carbon dioxide rich fluid as product carbon dioxide wherein the carbon dioxide loaded recovery solvent additionally contains dissolved oxygen, and further comprising deoxygenating the carbon dioxide loaded recovery solvent prior to the separation of step (C).

2. The method of claim 1 wherein the recovery solvent is substantially free of inhibitors.

3. The method of claim 1 wherein the recovery solvent comprises from 10 to 20 weight percent monoethanolamine.

4. The method of claim 1 wherein the recovery solvent comprises from 15 to 35 weight percent diethanolamine.

5. The method of claim 1 wherein the recovery solvent comprises from 10 to 20 weight percent monoethanolamine and from 20 to 40 weight percent methyldiethanolamine.

6. The method of claim 1 wherein the recovery solvent comprises from 12 to 15 weight percent monoethanolamine and from 25 to 35 weight percent methyldiethanolamine.

7. The method of claim 1 wherein the recovery solvent comprises from 15 to 35 weight percent diethanolamine and from 15 to 40 weight percent methyldiethanolamine.

8. The method of claim 1 wherein the recovery solvent comprises from 20 to 30 weight percent diethanolamine and from 20 to 35 weight percent methyldiethanolamine.

9. A method for recovering carbon dioxide comprising:

(A) passing feed gas comprising carbon dioxide at a partial pressure of 10 psia or less in mass transfer contact with a recovery solvent comprising water and at least two different fast reaction rate amines with no slow reaction rate amine present in the recovery solvent;

(B) passing carbon dioxide from the feed gas to the recovery solvent to produce carbon dioxide depleted gas and carbon dioxide loaded recovery solvent;

(C) separating carbon dioxide from the carbon dioxide loaded recovery solvent to produce carbon dioxide rich fluid; and

(D) recovering carbon dioxide rich fluid as product carbon dioxide wherein the carbon dioxide loaded recovery solvent additionally contains dissolved oxygen, and further comprising deoxygenating the carbon dioxide loaded recovery solvent prior to the separation of step (C).