Method and facility for treating effluents loaded with organic material, particularly by wet oxidation and with internal solid residue recycling, and purification facility therefor

• US 5,948,275 A
• Filed: 11/18/1996
• Issued: 09/07/1999
• Est. Priority Date: 03/21/1994
• Status: Expired due to Term

• Current Assignee: Veolia Water Solutions & Technologies Support
• Original Assignee: Omnium Detraitements et Devalorisation
• Inventors: Luck, Francis, Djafer, Malik, Sibony, Jacques
• Primary Examiner(s): Popovics, Robert J.
• Application Number:
  US08/718,303
• Time in Patent Office: 1,023 Days
• Field of Search: 210/762, 210/761, 210/631, 210/605, 210/628, 210/630, 210/613, 210/766, 210/903, 210/906, 210/805, 210/806, 210/175, 210/184, 210/195.1, 210/177, 210/205, 210/218
• US Class Current: 210/762
• CPC Class Codes: C02F 11/08 Wet air oxidation
• CPC Class Codes: Y10S 210/903 Nitrogenous

Abstract

An integrated method for purifying industrial and/or urban effluents containing a large amount of organic material in solution and/or suspension, wherein said effluents are treated in a wet oxidation reactor. The effluents are oxidized in the presence of at least one oxidizing gas to mineralize a large part of the organic material therein by producing a gas phase and an essentially liquid phase mainly containing soluble residual organic material, as well as an essentially inorganic solid phase in suspension. The essentially liquid phase from the reactor is subjected to liquid/solid separation to separate the solid phase, and at least a fraction of the separated solid phase is recycled in the wet oxidation reactor. Various alternative embodiments of the method include adding a catalyst and/or an agent for acidifying the recycled solid phase fraction. The facility may operate continuously or semi-continuously between interruptions.

Claims

1. A method for the purification of industrial and/or urban effluents containing a substantial proportion of soluble organic matter and/or organic matter in suspension, comprising the acts of:

treating said effluents in a wet air oxidation reactor within which said effluents are made to undergo an oxidation in the presence of at least one oxidizing gas so as to mineralize a major part of the organic matter contained in said effluents, the treating act producing, firstly, a gas phase and, secondly, an essentially liquid phase containing mainly soluble residual organic matter as well as an essentially mineral solid phase in suspension,

separating the mineral solid phase in suspension from said essentially liquid phase resulting from the treating act to isolate said solid phase; and

recycling at least a fraction of said separated solid phase within said wet air oxidation reactor.

2. Method according to claim 1, wherein the separating act is done in a separator located outside the wet air oxidation reactor.

3. Method according to claim 1, wherein the treating act is performed semi-continuously between periods of interruption, and wherein the separating act is performed within the wet air oxidation reactor during the periods of the interruption of the treating act, and further comprising:

discharging at least a part of the separated liquid phase from the reactor while retaining at least a fraction of the separated solid phase in the reactor.

4. Method according to claim 1, further comprising:

recirculating the effluent in the reactor in the course of the treating act.

5. Method according to claim 4, wherein the recirculating act is performed between periods of interruption, and wherein the separating act is performed within the wet air oxidation reactor during the periods of interruption of the recirculating act, and further comprising:

discharging at least a part of the separated liquid phase from the reactor while retaining at least a fraction of the separated solid phase in the reactor.

6. Method according to claim 1, wherein the treating act is done in the presence of catalyst, said catalyst being such that, after the separating act, said recycled solid phase contains at least 60% of said catalyst.

7. Method according to claim 6, wherein the catalyst is a metal selected from the group consisting of manganese, iron, cobalt, nickel, copper, zinc and mixtures and compounds thereof.

8. Method according to claim 7, wherein the catalyst is selected from the group consisting of soluble compounds of copper, soluble compounds of zinc and mixtures thereof.

9. Method according to claim 6, wherein the catalyst comprises a catalyst metal, and wherein a mass ratio of catalyst metal to chemical oxygen demand (COD) of the effluent before the treating act ranges from 5.10^-4 to 3.10^-1 approximately.

10. Method according to claim 1, further comprising:

adding an acidifying chemical additive to the separated solid phase.

11. Method according to claim 10, wherein the adding act adjusts the pH factor of the separated solid phase to values ranging from approximately 1 to approximately 5.

12. Method according to claim 10, wherein the chemical additive is selcted from the group consisting of sulfuric acid and organic acids.

13. Method according to claim 1, wherein, with a rate of recycling defined as being equal to the inverse of the fraction of recycled solid to total separated solid phase, the solid phase is recycled at a rate of recycling ranging from 1 to 20.

14. Method according to claim 1, further comprising:

biologically treating an aqueous phase coming from the separating act at exit from said reactor.

15. Method according to claim 14, further comprising:

adjusting operating parameters of the treating act to regulate a nitrogen to chemical oxygen demand ratio of the aqueous phase coming from the separating act, wherein said operating parameters include temperature, pressure, period of stay, and quality of catalyst.

16. Method according to claim 1, characterized in that the treating act is done at a temperature ranging from about 100°

C. to about 350°

C., under a total absolute pressure ranging from about 5 bars to about 160 bars.

17. Method according to claim 16, wherein a quantity of oxygen introduced into said wet air oxidation reactor provides a ratio of oxygen to chemical oxygen demand (COD) of the non-treated effluent ranging from approximately 0.5 to 2.0.

18. Method according to claim 1 carried out in a treatment line for the industrial and/or urban effluents, wherein the essentially liquid phase coming from the treating act contains ammonia, and further comprising:

stripping ammonia from the essentially liquid phase by means of a gas jet, in order to produce a second liquid phase signifcantly depleted in ammonia and a second gas phase containing oxygen and ammonia gas; and

oxidizing the second gas phase so as to obtain a third gas phase resulting from the essentially complete oxidation of ammonia into nitrogen oxides NO and NO2 as well as carbon monoxide and volatile organic compounds into carbon dioxide; and

reintroducing said third gas phase into the treatment line for said effluents to be treated.

19. Method according to claim 18, further comprising:

converting the third gas phase at least partially into nitrites before the reintroducing act.

20. Method according to claim 19, wherein the reintroducing act is selected from the group consisting of:

reinjecting the third gas phase into the wet air oxidation reactor to accelerate oxidation and limit production of NH4 during oxidation of the effluents,

disinfecting an aqueous phase of the treatment line,

acidifying the solid phase coming from the treating act, and

stabilizing sludge.

21. Method according to claim 1, wherein the effluents treated include residual sludge of urban or industrial water treatment facilities.

22. An installation for the purification of industrial and/or urban effluents containing a substantial proportion of soluble organic matter and/or organic matter in suspension, the installation comprising:

a continuous wet air oxidation reactor for treating said effluents within which said effluents are made to undergo an oxidation in the presence of at least one oxidizing gas so as to mineralize a major part of the organic matter contained in said effluents to produce, firstly, a gas phase and, secondly, an essentially liquid phase containing mainly soluble residual organic matter as well as an essentially mineral solid phase in suspension; and

a separator distinct from said reactor for separating the essentially mineral solid phase in suspension from the essentially liquid phase to isolate the solid phase;

an inlet conduit connecting the reactor to the separator, the inlet conduit receiving the essentially liquid phase produced by the reactor and transferring the essentially liquid phase to the separator; and

a return conduit connecting the separator to the reactor, the return conduit recycling at least a fraction of the separated solid phase to said reactor.

23. Installation according to claim 22, further comprising:

a heat exchanger within the wet air oxidation reactor enabling the heating of the effluents entering said wet air oxidation reactor with heat from the separated liquid phase at exit from the reactor.

24. The installation according to claim 22, further comprising:

a main water treatment unit coupled to the reactor, the main water treatment unit providing effluents to the reactor, the main water treatment unit having a head which receives the liquid phase resulting from the treatment of the effluents.

25. An installation for the purification of industrial and/or urban effluents containing a substantial proportion of soluble organic matter and/or organic matter in suspension, the installation comprising:

a wet air oxidation reactor for treating said effluents within which said effluents are made to undergo an oxidation in the presence of at least one oxidizing gas so as to mineralize a major part of the organic matter contained in said effluents to produce, firstly, a gas phase and, secondly, an essentially liquid phase containing mainly soluble residual organic matter as well as an essentially mineral solid phase in suspension, the reactor further separating the essentially mineral solid phase in suspension from the essentially liquid phase to isolate the solid phase; and

means for draining of the separated liquid phase and at least a first fraction of the separated solid phase from the reactor while retaining and recycling at least a second fraction of the separated solid phase within the reactor.