IP Library Granted Patent US 8,591,721
Granted Patent B2
US 8,591,721 · App. 12/665,363 · Granted Nov 26, 2013

Process for mixed chemical/electrochemical treatment of a liquid medium loaded with nitrates, a device for treating such a liquid medium and applications

Inventors: Michel Reynes (Castelginest, FR); Dimiter Hadjiev (Lorient, FR)
Assignee: Firmus S.A.M.
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 8,591,721
App. No.
12/665,363
Granted
Nov 26, 2013
Kind
B2
Abstract

The invention relates, in particular, to a process for treating a liquid medium loaded with nitrates via a chemical route that mainly comprises a step of electrolysis of the liquid medium in the presence of a metal salt, the electrolysis being carried out at a pH below 5. The invention also relates to a device for treating a liquid medium loaded with nitrates and also to the applications of this process and device, in particular for reducing the level of nitrates in drainage waters.

Claims (33)

1. A method for treatment of a liquid medium containing nitrates, comprising

forming an electrolytic solution by adding a zinc metal salt to said liquid medium, wherein the zinc ion concentration in the electrolytic solution is at least 70.8 mg/L,

electrolyzing the electrolytic solution in an electrolyzer wherein the electrolytic solution is at a pH not exceeding 5, and then

forming an effluent solution that concentrates the zinc metal salt by electrodialyzing a solution output by the electrolyzing step.

2. The method according to claim 1 , wherein the concentration of the zinc metal salt is larger than 0.5 g·L −1 before the electrolyzing step.

3. The method according to claim 1 , wherein the pH of the electrolytic solution is between 2 and 5.

4. The method according to claim 1 , wherein the effluent solution is recycled to the electrolyzer and undergoes the electrolyzing step.

5. The method according to claim 4 , wherein an output of the electrolyzing step undergoes an oxidizing step and an output of the oxidizing step is recycled to the electrolyzer and undergoes the electrolyzing step.

6. The method according to claim 1 , wherein the electrolytic solution further comprises KNO 3 .

7. The method according to claim 1 , wherein the electrolytic solution further comprises Na 2 SO 4 .

8. The method according to claim 1 , wherein the electrolytic solution further comprises NaCl.

9. A method for treatment of a liquid medium containing nitrates, comprising

forming an electrolytic solution by adding a zinc metal salt to said liquid medium, wherein the zinc ion concentration in the electrolytic solution is at least 70.8 mg/L,

electrolyzing the electrolytic solution in an electrolyzer wherein the electrolytic solution is at a pH not exceeding 5, and then

forming an effluent solution that is demineralized with respect to zinc metal salt by electrodialyzing a solution output by the electrolyzing step.

10. The method according to claim 9 , wherein the concentration of the zinc metal salt is larger than 0.5 g·L −1 before the electrolyzing step.

11. The method according to claim 9 , wherein the pH of the electrolytic solution is between 2 and 5.

12. The method according to claim 9 , wherein the electrolytic solution further comprises KNO 3 .

13. The method according to claim 9 , wherein the electrolytic solution further comprises Na 2 SO 4 .

14. The method according to claim 9 , wherein the electrolytic solution further comprises NaCl.

15. A method for treatment of a liquid medium containing nitrates, comprising

forming an electrolytic solution by adding a zinc metal salt to said liquid medium, wherein the zinc ion concentration in the electrolytic solution is at least 70.8 mg/L,

electrolyzing the electrolytic solution in an electrolyzer while at pH not exceeding 5, then

oxidizing the electrolytic solution in the presence of an oxidizing agent,

each electrolyzing step conducted within an electrolysis compartment,

each oxidizing step conducted within an oxidizing compartment,

repeating the electrolyzing step and oxidizing step in an additional electrolysis compartment and additional oxidizing compartment respectively,

wherein the electrolysis compartment is located below and overlaps the oxidizing compartment directly above it,

wherein the passage of the electrolytic solution is from the lowest electrolysis compartment to the highest oxidizing compartment, and then

the electrolytic solution undergoes an electrodialyzing step.

16. The method according to claim 15 , wherein the number of repetitions of the electrolyzing step and oxidizing step is dependent on nitrate ion concentration of the electrolytic solution.

17. The method according to claim 15 , wherein the oxidizing step further comprises adding chlorine dioxide.

18. The method according to claim 17 , wherein the electrolytic solution of the oxidizing step is at a pH of 2 to 5.

Assignments (2)
CHANGE OF NAME Recorded Oct 25, 2011
From: S.A.R.L. FIRMUS
To: FIRMUS S.A.M.
Reel/Frame 027112/0284 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 17, 2010
From: REYNES, MICHEL; HADJIEV, DIMITER
To: S.A.R.L. FIRMUS
Reel/Frame 023944/0774 →
Priority Claims (1)
FR 07 55851 · Jun 19, 2007 · national
Continuity (1)
Related Publication 20100140106A1 · Jun 10, 2010