Process for increasing the acid gas absorption capacity of contaminated alkanolamine solutions

• US 5,393,505 A
• Filed: 07/19/1993
• Issued: 02/28/1995
• Est. Priority Date: 10/28/1987
• Status: Expired due to Fees

• Current Assignee: Mobil Oil Corporation (Exxon Mobil Corporation)
• Original Assignee: Mobil Oil Corporation (Exxon Mobil Corporation)
• Inventors: Audeh, Costandi A.
• Primary Examiner(s): Kishore, G. S.
• Assistant Examiner(s): Kulkosky, Peter F.
• Application Number:
  US08/095,569
• Time in Patent Office: 589 Days
• Field of Search: 521/26, 423/228, 423/229
• US Class Current: 423/228
• CPC Class Codes: B01D 53/1425 Regeneration of liquid absorbents
• CPC Class Codes: B01D 53/1456 Removing acid components
• CPC Class Codes: B01J 39/04 Processes using organic exchangers
• CPC Class Codes: B01J 41/05 in the strongly basic form
• CPC Class Codes: B01J 49/08 containing cationic and anionic exchangers in separate beds
• CPC Class Codes: C07C 213/10 Separation; Purification; Stabilisation; Use of additives

Abstract

The present invention includes a process for rejuvenating a spent aqueous alkanolamine solution comprising use of alkyl-substituted ammonium-containing organic base treatment to remove inorganic ions.

Claims

1. A process for rejuvenating a spent aqueous alkanolamine solution comprising the steps of:

(a) providing a fresh aqueous alkanolamine solution having alkanolamine concentration sufficient to effectively sorb an acid gas selected from the group consisting of H₂ S, CO₂, or both from a gaseous hydrocarbon stream having H₂ S, CO₂, or both dissolved therein;

(b) contacting said fresh aqueous alkanolamine solution with said hydrocarbon gas stream of step (a) whereby said fresh aqueous alkanolamine solution is enriched in said acid gas sorbed from said gaseous hydrocarbon stream;

(c) stripping said acid gas from said enriched alkanolamine solution to produce an acid-lean alkanolamine solution;

(d) recycling said acid-lean alkanolamine solution of step (c) to said contacting step (b);

(e) sequentially repeating steps (b), (c), and (d) to evolve a spent alkanolamine solution which, in its acid-lean form, is characterized by reduced acid gas sorption capacity in comparison with said fresh aqueous alkanolamine solution;

(f) removing inorganic ions from said spent alkanolamine solution;

(g) heating said spent alkanolamine solution of step (f) at temperature of from about 220°

to about 275°

C. for time of from about 0.25 to about 2 hours in the absence of added catalyst;

(h) admixing said heat-treated spent alkanolamine solution of step (g) with an aqueous solution containing from about 0.1 to about 20 weight percent of at least one alkyl-substituted ammonium-containing organic base which evolves no inorganic ionic constitutent upon dissolution in said spent alkanolamine solution and heating said admixture to reflux for time sufficient to produce a rejuvenated alkanolamine solution having at least about 80% of the acid gas sorption capacity of said fresh alkanolamine solution whereby the content of inorganic ionic constituent in said rejuvenated alkanolamine solution is less than when the same process is carried out with a base which forms an inorganic ionic constituent;

(i) charging said rejuvenated alkanolamine solution to said recycling step (d).

2. The process of claim 1 wherein said inorganic ion removal step (g) produces an alkanolamine solution containing not more than about 100 ppm inorganic anions and not more than about 150 ppm inorganic cations.

3. The process of claim 1 wherein said organic base is at least one selected from the group consisting of tetramethylammonium hydroxide, tetraethylammonium hydroxide, tetrapropylammonium hydroxide, and tetrabutylammonium hydroxide.

4. The process of claim 3 wherein said organic base comprises tetrabutylammonium hydroxide.

5. The process of claim 3 wherein said refluxing of step (h) is conducted at temperature of from about 120°

to about 140°

C.

6. The process of claim 1 wherein said rejuvenated alkanolamine solution of step (h) is charged to said recycling step (d) in the absence of an organic base removal step.

7. The process of claim 1 wherein step (g) further comprises reacting said aqueous alkanolamine solution at temperature of from about 240°

to about 260°

C., and step (h) further comprises admixing the alkanolamine solution with said organic base in concentration of from about 0.1 to about 20 weight percent improve the acid gas sorption capacity of the aqueous alkanolamine solution by a factor of from about 1.10 to about 1.30, whereby the content of inorganic ionic constituent in said rejuvenated alkanolamine solution is not increased and is less than with a base which forms an inorganic ionic constituent by a factor of at least about 80.

8. A process for rejuvenating a spent aqueous alkanolamine solution comprising the steps of:

(a) providing a fresh aqueous alkanolamine solution having alkanolamine concentration sufficient to effectively sorb an acid gas selected from the group consisting of H₂ S, CO₂, or both from a gaseous hydrocarbon stream having H₂ S, CO₂, or both dissolved therein;

(b) contacting said fresh aqueous alkanolamine solution with said hydrocarbon gas stream of step (a) whereby said fresh aqueous alkanolamine solution is enriched in said acid gas sorbed from said gaseous hydrocarbon stream;

(c) stripping said acid gas from said enriched alkanolamine solution to produce an acid-lean alkanolamine solution;

(d) recycling said acid-lean alkanolamine solution of step (c) to said contacting step (b);

(e) sequentially repeating steps (b), (c), and (d) to evolve a spent alkanolamine solution which, in its acid-lean form, is characterized by reduced acid gas sorption capacity in comparison with said fresh aqueous alkanolamine solution;

(f) removing inorganic ions from said spent alkanolamine solution;

(g) heating said spent alkanolamine solution of step (f) at temperature of from about 220°

to about 275°

C. for time of from about 0.25 to about 2 hours in the absence of added catalyst;

(h) admixing said heat-treated spent alkanolamine solution of step (g) with from about 0.1 to about 20 weight percent of at least one organic base selected from the group consisting of the tetraalkylammonium hydroxides which evolves no inorganic ionic constitutent upon dissolution in said spent alkanolamine solution and heating said admixture to reflux for time sufficient to produce a rejuvenated alkanolamine solution having at least about 80% of the acid gas sorption capacity of said fresh alkanolamine solution whereby the content of inorganic ionic constituent in said rejuvenated alkanolamine solution is less than when the same process is carried out with a base which forms an inorganic ionic constituent;

(i) charging said rejuvenated alkanolamine solution to said recycling step (d).

9. The process of claim 8 wherein said inorganic ion removal step (g) produces an alkanolamine solution containing not more than about 100 ppm inorganic anions and not more than about 150 ppm inorganic cations.

10. The process of claim 8 wherein said organic base is at least one selected from the group consisting of tetramethylammonium hydroxide, tetraethylammonium hydroxide, tetrapropylammonium hydroxide, and tetrabutylammonium hydroxide.

11. The process of claim 10 wherein said organic base comprises tetrabutylammonium hydroxide.

12. The process of claim 10 wherein said refluxing of step (h) is conducted at temperature of from about 120°

to about 140°

C.

13. The process of claim 8 wherein said rejuvenated alkanolamine solution of step (h) is charged to said recycling step (d) in the absence of an organic base removal step.

14. The process of claim 8 wherein step (g) further comprises heating said aqueous alkanolamine solution at temperature of from about 240°

to about 260°

C., and step (h) further comprises admixing the alkanolamine solution with said organic base in concentration of from about 0.1 to about 20 weight percent improve the acid gas sorption capacity of the aqueous alkanolamine solution by a factor of from about 1.10 to about 1.30, whereby the content of inorganic ionic constituent in said rejuvenated alkanolamine solution is not increased and is less than with a base which forms an inorganic ionic constituent by a factor of at least about 80.