Process for the removal of heat stable amine salts

• US 20020020625A1
• Filed: 05/04/2001
• Published: 02/21/2002
• Est. Priority Date: 05/02/2000
• Status: Active Grant

• Current Assignee: Electrosep Technologies Inc.
• Original Assignee: Carolyn H. Byszewski
• Inventors: Byszewski, Carolyn H.
• Granted Patent: US 6,517,700 B2
• Time in Patent Office: Days
• US Class Current: 204/518
• CPC Class Codes: B01D 53/1425 Regeneration of liquid absorbents
• CPC Class Codes: B01D 61/44 Ion-selective electrodialysis
• CPC Class Codes: B01D 61/445 with bipolar membranes; Water splitting
• CPC Class Codes: C07C 209/84 Purification

Abstract

A process is disclosed for removing heat stable amine salts using an electrodialysis process. The process 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. A base is added to the electrodialysis unit in order to permit the recovery of the heat stable amine salts as salts corresponding to the base added. The purified amine solution can be used again to remove acid gases from a gas stream.

Claims

1. A process for removing heat-stable amine salts from a contaminated aqueous amine solution, comprising

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

(b) passing a base stream comprising a base to the base 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) base anions to dissociate from the base in the base compartment and pass into the product compartment;

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

(d) discharging from the product compartment a product stream comprising at least in part an amine in free base form in which the level of heat stable amine salts and/or non heat stable amine salts has been lowered.

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

3. 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.

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

5. The process of claim 1 wherein the base is selected from the group consisting of alkali metal oxides, alkali metal hydroxides, alkaline earth oxides, alkaline earth hydroxides, metal oxides and metal hydroxides.

9. The process of claim 5 further comprising discharging a waste effluent stream from the waste compartment and recycling at least a portion of the waste stream to the waste compartment.

11. The process of claim 5 wherein the source or regenerable anions is selected from a group consisting of alkali metal and akali earth salts in which the anions are heat regenerable.

12. The process of claim 5 wherein the source of regenerable anions is comprised of acids of heat regenerable anions.

14. The process of claim 11 wherein the feedstream further comprises water and the amine in free base form.

15. The process of claim 11 further comprising discharging a product-feed effluent stream from the feed compartment and recycling at least a portion of the product-feed effluent stream to the feed compartment.

16. The process of claim 11 further comprising discharging a waste effluent stream from the waste compartment and recycling at least a portion of the waste stream to the waste compartment.

6. A process for removing heat-stable amine salts from a contaminated aqueous amine solution, comprising

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

(b) passing a anion source stream comprising a base or a source of regenerable anions in either salt or acid form to the anion source 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;

(2) base anions or regenerable anions to dissociate in the anion source compartment and pass into the product compartment;

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

(d) discharging from the product-feed compartment a product stream comprising at least in part an amine in free base form or in a regenerable form in which the level of heat stable amine salts has been lowered.

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

8. The process of claim 6 further comprising discharging a product-feed effluent stream from the product-feed compartment and recycling at least a portion of the product-feed effluent stream to the feed compartment.

10. The process of claim 6 wherein the base is selected from the group consisting of alkali metal oxides, alkali metal hydroxides, alkaline earth oxides, alkaline earth hydroxides, metal oxides and metal hydroxides.

13. A process for removing heat-stable amine salts from a contaminated aqueous amine solution, comprising

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

.

(b) 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 product-feed compartment;

(2) hydroxyl anions to be generated in the bi-polar membranes and pass into the product-feed compartment, (3) heat stable anions to dissociate from the heat stable amine salts in the product-feed compartment and pass into the salt compartment, (4) protons to be generated in the bi-polar membranes and pass into the waste compartment and

(d) discharging from the product-feed compartment a product stream comprising at least in part an amine in free base form in which the level of heat stable amine salts and/or non heat stable amine salts has been lowered.