Dual-stage biological process for removing nitrogen from wastewater

• US 5,650,069 A
• Filed: 09/08/1995
• Issued: 07/22/1997
• Est. Priority Date: 09/08/1995
• Status: Expired due to Term

• Current Assignee: Kruger Incorporated
• Original Assignee: Kruger Incorporated
• Inventors: Nielsen, Finn M., Langslet, O. Roy, Hong, Sun-Nan
• Primary Examiner(s): McCarthy, Neil
• Assistant Examiner(s): GREEN, THEODORE
• Application Number:
  US08/525,088
• Time in Patent Office: 683 Days
• Field of Search: 210/605, 210/620, 210/622, 210/623, 210/624, 210/626, 210/629, 210/630, 210/903, 210/906
• US Class Current: 210/605
• CPC Class Codes: C02F 3/308 Biological phosphorus removal
• CPC Class Codes: Y10S 210/903 Nitrogenous
• CPC Class Codes: Y10S 210/906 Phosphorus containing

Abstract

A process for biologically removing nitrogen and other nutrients from wastewater using recycled activated sludge. A mixed liquor is formed from influent wastewater and recycled activated sludge and then treated in two successive nitrogen removal stages, each stage having an anoxic denitrification zone and an aerobic nitrification zone. The first nitrogen removal stage entails circulating the mixed liquor back and forth between the anoxic zone and the aerobic zone. The mixed liquor is then transferred to a final clarifier where activated sludge is separated from purified supernatant. To increase the NO_x^- reducing enzymatic activity of denitrification microorganisms, the activated sludge is retained in the final clarifier for a time period sufficient to permit adaptation of these microorganisms to a nitrate/nitrite-respiring metabolic pathway. To maintain high levels of denitrifying microorganisms and thereby effectuate greater nitrogen removal than previously possible, a portion of the activated sludge is recycled from the final clarifier directly into the second nitrogen removal stage.

Claims

1. An activated sludge process for biologically removing nitrogen from wastewater, comprising the steps of:

a) forming mixed liquor from influent wastewater and activated sludge;

b) treating the mixed liquor in a first nitrogen removal stage, including the substeps of;

i) directing the mixed liquor into a first anoxic zone,

ii) maintaining the mixed liquor under anoxic conditions within the first anoxic zone for a sufficient time period to permit denitrifying microorganisms to reduce nitrates and nitrites in the mixed liquor to elemental nitrogen,

iii) transferring a portion of the mixed liquor from the first anoxic zone to a first aerobic zone,

iv) aerating the mixed liquor within the first aerobic zone for a sufficient time period to permit nitrifying microorganisms to convert ammonia and organic nitrogen in the mixed liquor into nitrates and nitrites, and

v) circulating the mixed liquor between the first anoxic zone and the first aerobic zone to effectuate denitrification and nitrification;

c) treating the mixed liquor in a second nitrogen removal stage by passing the mixed liquor through a second anoxic zone and a second aerobic zone to effectuate further denitrification and nitrification;

d) transferring the mixed liquor treated in the first and second nitrogen removal stages to a final clarifier where settled sludge is separated from purified supernatant;

e) retaining the sludge in the final clarifier for a period of time sufficient to permit denitrifying microorganisms in the sludge to adapt to respiring nitrates and nitrites instead of oxygen;

f) recycling a portion of the sludge from the final clarifier to form the mixed liquor; and

g) recycling another portion of the sludge from the final clarifier into the mixed liquor between the first nitrogen removal stage and the second nitrogen removal stage so as to increase the population of microorganisms in the second nitrogen removal stage that have adapted to respiring nitrates and nitrites instead of oxygen.

2. The process of claim 1, wherein the sludge is retained in the final clarifier for a time period between 30 minutes and 4 hours.

3. The process of claim 2, wherein the sludge is retained in the final clarifier for a time period of approximately 2 hours.

4. The process of claim 1, wherein the sludge is recycled from the final clarifier at a rate of approximately 30%-80% of a wastewater influent rate into the process.

5. The process of claim 4, wherein the sludge is recycled from the final clarifier to form the mixed liquor before the first nitrogen removal stage at a rate of approximately 20%-60% of the wastewater influent rate.

6. The process of claim 4, wherein the sludge is recycled from the final clarifier into the mixed liquor between the first and second nitrogen removal stages at a rate of approximately 10%-30% of the wastewater influent rate.

7. The process of claim 1, wherein the step of treating the mixed liquor in the second nitrogen removal stage includes directing the mixed liquor from the first aerobic zone into the second anoxic zone.

8. The process of claim 1 wherein the mixed liquor is circulated from the aerobic zone back to the anoxic zone in each nitrogen removal stage at a rate of approximately 100%-200% of a wastewater influent rate into the process.

9. The process of claim 1, further including the steps of treating the mixed liquor in an anaerobic stage before treating the mixed liquor in the first nitrogen removal stage;

and maintaining the mixed liquor in the anaerobic stage for a sufficient time period to allow proliferation of phosphate storing organisms.

10. A process for biologically removing nitrogen from wastewater using recycled activated sludge, comprising the steps of:

a) forming mixed liquor from influent wastewater and recycled activated sludge;

b) transferring the mixed liquor to a first nitrogen removal stage;

c) treating the mixed liquor in the first nitrogen removal stage, including the substeps of;

i) first, directing the mixed liquor into a first anoxic zone,

ii) maintaining the mixed liquor under anoxic conditions within the first anoxic zone for a sufficient time period to permit denitrifying microorganisms to reduce nitrates and nitrites in the mixed liquor to elemental nitrogen,

iii) transferring a portion of the mixed liquor from the first anoxic zone to a first aerobic zone,

iv) aerating the mixed liquor within the first aerobic zone for a sufficient time period to permit nitrifying microorganisms to convert ammonia and organic nitrogen in the mixed liquor into nitrates and nitrites, and

v) circulating the mixed liquor between the first anoxic zone and the first aerobic zone to effectuate denitrification and nitrification;

d) transferring the mixed liquor from the first nitrogen removal stage to a second nitrogen removal stage;

e) treating the mixed liquor in the second nitrogen removal stage, including the substeps of;

i) first, directing the mixed liquor into a second anoxic zone,

ii) maintaining the mixed liquor under anoxic conditions within the second anoxic zone for a sufficient time period to permit denitrifying microorganisms to further reduce nitrates and nitrites in the mixed liquor to elemental nitrogen,

iii) transferring mixed liquor from the second anoxic zone to a second aerobic zone,

iv) aerating the mixed liquor within the second aerobic zone for a sufficient time period to permit nitrifying microorganisms to further convert ammonia and organic nitrogen in the mixed liquor into nitrates and nitrites;

f) transferring mixed liquor from the second nitrogen removal stage to a final clarifier where activated sludge is separated from purified supernatant;

g) retaining the activated sludge in the final clarifier under anaerobic conditions for a period of time sufficient to permit an increase in the concentrations of nitrate and nitrite reducing enzymes within the denitrifying microorganisms in the activated sludge;

h) recycling a portion of the activated sludge from the final clarifier to form the mixed liquor before treating the mixed liquor in the first nitrogen removal stage; and

i) recycling another portion of the activated sludge from the final clarifier into the mixed liquor between the first nitrogen removal stage and the second nitrogen removal stage so as to increase the population of denitrifying microorganisms in the second anoxic zone that have adapted to respiring nitrates and nitrites instead of oxygen.

11. A biological wastewater treatment process for removing nitrogen from wastewater comprising:

a) mixing wastewater and return activated sludge to form mixed liquor;

b) directing the mixed liquor through first and second nitrification-denitrification treatment stages with each nitrification-denitrification treatment stage including both anoxic and aerobic treatment zones;

c) in each nitrification-denitrification stage, subjecting the mixed liquor to both nitrification and denitrification by biologically converting ammonia and organic nitrogen compounds to NO_x^- and then denitrifying the NO_x^- to produce elemental nitrogen;

d) directing the treated mixed liquor from the second nitrification-denitrification stage to a final clarifier and separating the treated mixed liquor into purified supernatant and activated sludge;

e) holding the activated sludge within the final clarifier under anaerobic conditions for a time period of approximately thirty minutes to four hours so as to encourage adaptation of denitrifying microorganisms to respiration of NO_x^- ;

f) returning a portion of the activated sludge from the final clarifier to where the activated sludge is mixed with influent wastewater to form the mixed liquor; and

g) returning a second portion of the activated sludge from the final clarifier to the anoxic treatment zone of the second nitrification-denitrification stage, bypassing the first nitrification-denitrification stage, wherein the denitrifying microorganisms of the activated sludge increase the denitrification rate in the anoxic treatment zone of the second nitrification-denitrification stage.

12. The process of claim 11, wherein the activated sludge held in the final clarifier is recycled to the anoxic zone of the second nitrification-denitrification stage at a flow rate of approximately 10%-30% of the flow rate of the influent wastewater.