Method for treating an effluent using simultaneous nitrification/denitrification in a biological filter

• US 6,632,365 B1
• Filed: 08/15/2001
• Issued: 10/14/2003
• Est. Priority Date: 12/23/1998
• Status: Expired due to Term

• Current Assignee: OTV SA SA
• Original Assignee: OTV SA SA
• Inventors: Le Tallec, Xavier, Payraudeau, Michele
• Primary Examiner(s): Barry, Chester T.
• Application Number:
  US09/856,831
• Time in Patent Office: 790 Days
• Field of Search: 210/615, 210/616, 210/617, 210/618, 210/629, 210/739, 210/622, 210/800, 210/807, 210/746, 210/150
• US Class Current: 210/617
• CPC Class Codes: C02F 2209/04 Oxidation reduction potential [ORP]
• CPC Class Codes: C02F 2209/05 Conductivity or salinity
• CPC Class Codes: C02F 2209/15 N03-N
• CPC Class Codes: C02F 2209/16 Total nitrogen (tkN-N)
• CPC Class Codes: C02F 2209/225 in the gas phase
• CPC Class Codes: C02F 3/006 Regulation methods for biological treatment
• CPC Class Codes: C02F 3/06 using submerged filters
• CPC Class Codes: C02F 3/301 Aerobic and anaerobic treatment in the same reactor
• CPC Class Codes: C02F 3/302 Nitrification and denitrification treatment C02F3/308 takes precedence
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage

Abstract

The invention concerns a method and installation for the treatment of excess sludge derived from biological wastewater treatment plants. The method is characterized in that it consists of associating at least one digestion step (4) and at least one wet oxidation step (2) of said sludge, said wet oxidation step being conducted at a temperature of between 50° C. and 180° C. and at a pressure of between 2 and 40 bar.

Claims

1. A method of simultaneously performing nitrification and denitrification of a wastewater effluent, comprising:

a. directing the wastewater through a biological filter with cultures fixed to at least one bed of granular material;

b. continuously aerating and supplying oxygen to substantially the entirety of said bed of granular material;

c. measuring at least one parameter representing the oxygen consumption of said fixed cultures;

d. adjusting the supply of oxygen to the bed of granular material in relation to the results of measuring said parameter and of a set-value thereof; and

e. wherein the wastewater passing through the biological filter and the granular material is simultaneously nitrified and denitrified.

2. The method of claim 1 wherein said set value of said parameter is determined in relationship to the nitrogen content of said effluent or by a level of pollution measured at the outlet of said biological filter.

3. The method of claim 1 wherein the method produces a treated effluent and wherein the method further comprises recirculating at least a part of the treated effluent through the biological filter.

4. The method of claim 3 comprising recycling the treated effluent at a recycled rate of between 75% and 400%.

5. The method of claim 1 wherein the biological filter is vertically oriented and wherein the effluent is vertically directed through the biological filter.

6. The method of claim 2 wherein the effluent is directed into a lower portion of the biological filter and caused to move upwardly through the biological filter.

7. The method of claim 1 wherein said parameter is selected from the group consisting of:

the concentration of dissolved oxygen, the redox potential, the ammonium concentration, the nitrate concentration, and the NADH concentration of the treated effluent.

8. The method of claim 1 wherein measuring said parameter is conducted on the treated effluent leaving said biological filter.

9. The method of claim 1 wherein measuring said parameter is conducted on the effluent being transmitted through said biological filter.

10. The method of claim 1 wherein measuring said parameter comprises measuring the concentration of dissolved oxygen in the treated effluent.

11. The method of claim 10 including adjusting the oxygen supplied to the granular material so as to maintain the concentration of oxygen of the treated effluent at a value of between 3 and 8 mg/l.

12. The method of claim 11 including adjusting the oxygen supplied to the granular material so as to maintain the concentration of dissolved oxygen of the treated effluent at a value of between 4 and 7 mg/l.

13. The method of claim 1 including adding to said effluent at least one source of carbon.

14. The method of claim 1 including subjecting the treated effluent leaving the biological filter to additional denitrification.

15. An installation for carrying out the method of claim 1 including at least one biological filter including granular material, and adjustable oxygen supply means for adjustably supplying oxygen to the biological filter.

16. The installation of claim 15 further including means for measuring at least one parameter representing the oxygen consumption of fixed cultures on the granular material and wherein the oxygen supply means is adjustable in response to the measurement of the oxygen consumption of said fixed cultures such that the oxygen being supplied to the biological filter can be increased or decreased.

17. The installation of claim 15 wherein the biological filter is an ascending type and comprises a fluidized bed of granular material and a recirculation line that permits treated effluent to be recirculated through the biological filter.

18. The installation of claim 16 wherein said measurement means includes at least one dissolved oxygen concentration sensor positioned above a bed of granular material forming a part of the biological filter.

19. The installation of claim 18 wherein the dissolved oxygen concentration sensor is positioned approximately 5 cm to 40 cm above the granular material.

20. The installation of claim 15 comprising at least one separating unit to separate the treated effluent from the granular material.