Regeneration of anion exchange resins by catalyzed electrochemical reduction

• US 6,358,396 B1
• Filed: 05/08/2000
• Issued: 03/19/2002
• Est. Priority Date: 05/08/2000
• Status: Expired due to Term

• Current Assignee: UT-Battelle LLC
• Original Assignee: UT-Battelle LLC
• Inventors: Gu, Baohua, Brown, Gilbert M.
• Primary Examiner(s): Phasge, Arun S.
• Application Number:
  US09/566,036
• Time in Patent Office: 680 Days
• Field of Search: 205/688, 205/704, 210/670, 210/673
• US Class Current: 205/704
• CPC Class Codes: B01J 49/07 containing anionic exchangers
• CPC Class Codes: B01J 49/57 for anionic exchangers
• CPC Class Codes: C02F 1/42 by ion-exchange ion-exchange in general B01J
• CPC Class Codes: C02F 2101/12 Halogens or halogen-containing compounds
• CPC Class Codes: C02F 2103/06 Contaminated groundwater or leachate

Abstract

Anion exchange resins sorbed with perchlorate may be regenerated by a combination of chemical reduction of perchlorate to chloride using a reducing agent and an electrochemical reduction of the oxidized reducing agent. Transitional metals including Ti, Re, and V are preferred chemical reagents for the reduction of perchlorate to chloride. Complexing agents such as oxalate are used to prevent the precipitation of the oxidized Ti(IV) species, and ethyl alcohol may be added to accelerate the reduction kinetics of perchlorate. The regeneration may be performed by continuously recycling the regenerating solution through the resin bed and an electrochemical cell so that the secondary waste generation is minimized.

Claims

1. A method for the regeneration of a strong-base anion exchange resin sorbed with perchlorate (ClO₄⁻

) comprising;

addition of an aqueous complexed metal reducing agent selected from the group consisting of Ti(III) and Re(V) to convert perchlorate to chloride;

eluting the column with a dilute acid; and

optionally eluting the column with a solution of NaCl.

2. A method according to claim 1 wherein the complexed metal reducing agent is complexed with a chelating agent selected from the group consisting of oxalic acid, EDTA, citric acid and DTPA.

3. A method according to claim 2 wherein the chelating agent is oxalic acid in a concentration of 10 mM to 2 M.

4. A method according to claim 1 wherein the complexed metal reducing agent is provided in an aqueous solution further containing an acid and an organic solvent.

5. A method according to claim 4 wherein the organic solvent is selected from the group consisting of methanol, ethanol, isopropanol, glycols and glycol ethers.

6. A method according to claim 5 wherein the organic solvent comprises up to 90% of the aqueous solution.

7. A method according to claim 4 wherein the acid is selected from the group consisting of sulfuric acid, hydrochloric acid and phosphoric acid.

8. A method according to claim 7 wherein the acid in the aqueous solution is in a concentration of 1 mM to 3 M.

9. A method according to claim 1 wherein the reducing agent is a Ti(III) compound present in a concentration of 1 mM to 1 M.

10. A method according to claim 1 wherein the complexed reducing agent is a Re(V)MeO₂ compound present in a concentration of 0.1 mM to 0.2 M.

11. A method according to claim 10 wherein a vanadium(II)/vanadium(III)/vanadium(IV) couple is used to catalyze the reduction of Re(VII) to Re(V) species.

12. A method according to claim 11 wherein the vanadium catalyst is present in a range of 0.1 mM to 0.2M.

13. A method according to claim 1 which is performed in an anoxic system.

14. A method according to claim 1 wherein the dilute acid used to elute the column is hydrochloric acid.

15. A method according to claim 1 further comprising regenerating the reduced form of the catalyst in an electrochemical cell.