Process for converting heat stable amine salts to heat regenerable amine salts

• US 5,292,407 A
• Filed: 12/18/1992
• Issued: 03/08/1994
• Est. Priority Date: 12/18/1992
• Status: Expired due to Term

• Current Assignee: Union Carbide Chemicals & Plastics Technology Corporation (Dow, Inc.)
• Original Assignee: Union Carbide Chemicals & Plastics Technology Corporation (Dow, Inc.)
• Inventors: Roy, Veronique, Sarlis, Jean I., Hakka, Leo E.
• Primary Examiner(s): Niebling, John
• Assistant Examiner(s): Phasge, Arun S.
• Application Number:
  US07/993,015
• Time in Patent Office: 445 Days
• Field of Search: 204/182.3, 204/182.4, 204/101, 204/102, 204/131
• US Class Current: 205/431
• CPC Class Codes: B01D 53/1425 Regeneration of liquid absorbents
• CPC Class Codes: B01D 53/1468 Removing hydrogen sulfide
• CPC Class Codes: B01D 61/44 Ion-selective electrodialysis
• CPC Class Codes: C07C 209/00 Preparation of compounds containing amino groups bound to a carbon skeleton

Abstract

Processes are disclosed for converting heat stable amine salts to heat regenerable amine salts using a modified electrodialysis zone. The processes of the present invention can be used to reduce the level of heat stable salts in a lean solvent stream in an acid gas removal process and can be integrated with the acid gas removal process to utilize process streams as a source of ions.

Claims

1. A process for converting heat stable amine salts to heat regenerable amine salts which comprises:

(a) passing a feedstream comprising an amine in salt form having heat stable anions associated therewith to an electrodialysis zone having a cathode compartment, an anode compartment and at least one repeat unit comprising a reflux compartment disposed between the cathode compartment and the anode compartment, a product compartment disposed between the reflux compartment and the anode compartment, a feed compartment disposed between the product compartment and the anode compartment, and an acid compartment disposed between the feed compartment and the anode compartment, said feed stream being passed to the feed compartment;

(b) passing a reflux stream comprising a salt or acid of a heat regenerable anion to the reflux compartment;

(c) passing a direct current potential transversely across each compartment, said current being effective to cause;

(1) amine cations to dissociated from the heat stable amine salts in the feed compartment and pass into the product compartment;

(2) heat regenerable anions to dissociate from the salt or acid in the reflux compartment and pass into the product compartment; and

(3) heat stable anions to dissociate from the heat stable amine salts in the feed compartment and pass into the acid compartment; and

(d) discharging from the product compartment a product stream comprising an amine in salt form having regenerable anions associated therewith.

2. The process of claim 1 wherein, during said current passage, cations from a salt or acid of a heat regenerable anion from a reflux compartment of another repeat unit adjacent to said acid compartment pass into said acid compartment.

3. The process of claim 2 further comprising discharging from the acid compartment an acid stream comprising a salt or acid of the heat stable anion.

4. The process of claim 1 wherein the heat stable anion is selected from the group consisting of sulfate anions, thiosulfate anions, polythionate anions, thiocyanate anions, formate anions, halide anions, nitrate anions, nitrite anions, acetate anions, oxylate anions and mixtures thereof.

5. The process of claim 1 wherein the heat regenerable anion is selected from the group consisting of sulfite anions, sulfide anions, carbonate anions, hydrosulfide anions, and mixtures thereof.

6. The process of claim 1 wherein the feedstream further comprises water and the amine in free base form.

7. The process of claim 1 wherein the feedstream comprises from about 0.1 to 25 weight percent of the amine in salt form having heat stable anions associated therewith, from about 5 to 60 weight percent of the amine in free base form and from about 30 to 95 weight percent water.

8. The process of claim 1 wherein the amine is selected from the group consisting of alkanolamines, alkyleneamines, aromatic amines, heterocyclic amines and mixtures thereof.

9. The process of claim 1 wherein the salt of the heat regenerable anion is selected from the group consisting of alkali metal sulfites, alkali metal carbonates, alkaline earth metal sulfites, alkaline earth metal carbonates and alkali metal sulfide and hydrosulfides.

10. The process of claim 1 wherein the acid of the heat regenerable anion is selected from the group consisting of sulfurous acid, carbonic acid and hydrogen sulfide.

11. The process of claim 1 wherein the salt of the heat stable anion is selected from the group consisting of alkali metal sulfates, alkali metal halides, alkaline earth metal sulfates, alkaline earth metal halides, alkali metal nitrates and nitrites, alkaline earth metal nitrates and nitrites, and mixtures thereof.

12. The process of claim 1 wherein the acid of the heat stable anion is selected from sulfuric acid, hydrochloric acid, hydrofluoric acid, nitric acid, nitrous acid, acetic acid and mixtures thereof.

13. The process of claim 1 further comprising passing an aqueous carrier stream to at least one of the product compartment and the acid compartment.

14. The process of claim 1 further comprising discharging a feed effluent stream from the feed compartment and recycling at least a portion of the feed effluent stream to the feed compartment.

15. The process of claim 1 further comprising discharging a reflux effluent stream from the reflux compartment and recycling at least a portion of the reflux effluent stream to the reflux compartment.

16. A process for converting heat stable amine salts to heat regenerable amine salts which comprises:

(a) passing a feedstream comprising an amine in salt form having sulfate anions associated therewith to an electrodialysis zone having a cathode compartment, an anode compartment and at least one repeat unit comprising a reflux compartment disposed between the cathode compartment and the anode compartment, a product compartment disposed between the reflux compartment and the anode compartment, a feed compartment disposed between the product compartment and the anode compartment, and an acid compartment disposed between the feed compartment and the anode compartment, said regenerated solvent stream being passed to the feed compartment;

(b) passing a reflux stream comprising a salt or acid of a sulfite anion to the reflux compartment;

(c) passing a direct current potential transversely across each compartment, said current being effective to cause;

(1) amine cations to dissociate from the heat stable amine salts in the feed compartment and pass into the product compartment;

(2) sulfite anions to dissociate from the salt or acid in the reflux compartment and pass into the product compartment; and

(3) sulfate anions to dissociate from the heat stable amine salts in the feed compartment and pass into the acid compartment; and

(d) discharging from the product compartment a product stream comprising an amine in salt form having sulfite anions associated therewith.

17. The process of claim 16 wherein, during said current passage, cations from a salt or acid of a sulfite anion from a reflux compartment of another repeat unit adjacent to said acid compartment pass into said acid compartment.

18. The process of claim 17 further comprising discharging from the acid compartment an acid stream comprising a salt or acid of the sulfate anion.