Method for treating wastewater or sludge

Patent metadata

Field	Value
Publication number	US-12157689-B2
Application number	US-202017600431-A
Country	US
Kind code	B2
Filing date	Mar 27, 2020
Priority date	May 24, 2019
Publication date	Dec 3, 2024
Grant date	Dec 3, 2024

Abstract

A method for treating wastewater or sludge comprises the steps of adding the wastewater or sludge to a reactor and mixing the wastewater or sludge with a stream to thereby decrease a ratio of alkalinity to ammonium in the reactor, the reactor containing ammonium oxidising bacteria that oxidise ammonium to produce nitrite and decrease pH.

First claim

The invention claimed is:

1. A method for treating wastewater or sludge, comprising the steps of:
providing a sludge or wastewater;
splitting the sludge or wastewater into a first stream and a second stream;
providing the first stream to a reactor and mixing the first stream with a stream containing ammonium to thereby decrease a ratio of alkalinity to ammonium in the reactor, wherein the reactor contains ammonium oxidising bacteria that oxidise ammonium to produce nitrite and decrease pH; and
removing a treated stream from the reactor and feeding the treated stream and the second stream to an anammox reactor.

2. A method as claimed in claim 1 wherein the stream that decreases the ratio of alkalinity to ammonium is a stream containing ammonium that comprises a liquor or a suspension or a sludge.

3. A method as claimed in claim 1 wherein the stream that decreases the ratio of alkalinity to ammonium comprises liquor from an anaerobic digestor, or liquor from an anaerobic digester that receives sludge from a thermal hydrolysis pre-treatment, or a suspension from an anaerobic digester, or a suspension from an anaerobic digester that receives sludge from a thermal hydrolysis pre-treatment, or a sludge from an anaerobic digester, or a sludge from an anaerobic digester that receives sludge from a thermal hydrolysis pre-treatment.

4. A method as claimed in claim 1 wherein the reactor is operated such that the pH of solution or liquor in the reactor is less than 5.5, or less than 5.0, or from 4 to 5, or from 4.5 to 5.

5. A method as claimed in claim 1 wherein the step of mixing the first stream with the stream containing ammonium decreases the ratio of alkalinity to ammonium in the reactor to less than 2, calculated on a molar basis, or less than 1.9, or less than 1.8, or less than 1.7, or less than 1.6, or less than 1.5, or less than 1.4, or less than 1.3, or less than 1.2, or less than 1.1, or less than 1, or less than 0.9, or less than 0.8, or less than 0.7, or less than 0.6, or less than 0.5, calculated on a molar basis.

6. A method as claimed in claim 1 comprising the steps of feeding a wastewater or sludge to the reactor, the reactor containing ammonium oxidising bacteria (AOB) and nitrite oxidising bacteria (NOB), the AOB oxidising ammonium to reduce pH in the reactor to between 5.5 and 6.0, continuing to operate the reactor at a pH of between 5.5 and 6.0 until a population of acid resistant AOB is selected, and continuing to operate the reactor such that the acid resistant AOB oxidise ammonia and the pH within the reactor is lowered to below 5, or to between 4 to 5, or to between 4.5 to 5.

7. A method as claimed in claim 1 comprising analysing one or both of alkalinity and ammonium in a feed material supplied to the reactor, analysing the stream fed to the reactor to determine the amount of components that reduce the ratio of alkalinity to ammonium in the stream and controlling addition of the stream to achieve the desired alkalinity to ammonium ratio.

8. A method as claimed in claim 1 wherein hydraulic retention time in the reactor and solid retention time in the reactor are controlled to promote the growth of AOB and the hydraulic retention time is greater than 1 hour, or greater than 2 hours, or greater than 3 hours, or greater than 4 hours, or greater than 5 hours, or greater than 10 hours, or greater than 12 hours, or greater than 1 day, or greater than 1.5 days, or greater than 2 days, or about 6 hours, and the solids retention time is between 1 day and 100 days, or between 10 days and 30 days.

9. A method as claimed in claim 1 wherein the reactor comprises an aerobic reactor.

10. A method as claimed in claim 1 for treating a sludge from an anaerobic sludge digester, the method comprising:
feeding the sludge from the anaerobic sludge digester to the reactor, wherein the reactor has a population comprising ammonium oxidising bacteria (AOB) and nitrite oxidising bacteria (NOB), wherein the AOB oxidise ammonium to form nitrite and to lower pH to between 5.5 and 6.5, or to between 5.5 and 6;
continuing to operate the reactor for a period of time until an acid resistant AOB population is selected and is formed, whereby the acid resistant AOB population oxidises ammonia to thereby lower the pH in the reactor to less than 5.5; and
continuing to operate the reactor at a pH of less than 5.5 such that nitrite and free nitrous acid are formed in the reactor, whereby pH of less than 5.5 is attained in the reactor by in-situ generation of hydrogen ions/protons without requiring addition of external acid and wherein an external source of nitrite is not used.

11. A method as claimed in claim 1 , wherein the stream that decreases the ratio of alkalinity to ammonium is a sewage or wastewater or sewage sludge having a ratio of alkalinity to ammonium of less than 2.0, calculated on a molar basis, or less than 1.9, or less than 1.8, or less than 1.7, or less than 1.6, or less than 1.5, or less than 1.4, or less than 1.3, or less than 1.2, or less than 1.1, or less than 1, or less than 0.9, or less than 0.8, or less than 0.7, or less than 0.6, or less than 0.5, calculated on a molar basis, and wherein the stream that decreases the ratio of alkalinity to ammonium is fed to the reactor containing ammonium oxidizing bacteria (AOB), such that the AOB oxidise ammonia to reduce or maintain pH below 5.5, or below 5.0, or from 4 to 5, or from 4.5 to 5, or less than or equal to 3, or from 1 to 3, or from 1.5 to 3, or from 2 to 3 in the reactor.

12. A method as claimed in claim 11 wherein the ratio of alkalinity to ammonium in the reactor is less than 2.0, calculated on a molar basis, or less than 1.9, or less than 1.8, or less than 1.7, or less than 1.6, or less than 1.5, or less than 1.4, or less than 1.3, or less than 1.2, or less than 1.1, or less than 1, or less than 0.9, or less than 0.8, or less than 0.7, or less than 0.6, or less than 0.5, calculated on a molar basis.

13. A method as claimed in claim 1 , further comprising the steps of:
selectively promoting growth of acid resistant ammonium oxidising bacteria in the reactor by feeding the stream that decreases the ratio of alkalinity to ammonium to the reactor,
wherein the stream that decreases the ratio of alkalinity to ammonium is a sewage or wastewater or sewage sludge or a liquor having a ratio of alkalinity to ammonium of less than 2.0, calculated on a molar basis, or less than 1.9, or less than 1.8, or less than 1.7, or less than 1.6, or less than 1.5, or less than 1.4, or less than 1.3, or less than 1.2, or less than 1.1, or less than 1, or less than 0.9, or less than 0.8, or less than 0.7, or less than 0.6, or less than 0.5, calculated on a molar basis,

until a population of AOB that can generate a pH of less than 3 is obtained; and
supplying metal containing sludge to the reactor containing the population of acid resistant AOB, whereby the pH in the reactor is maintained at less than or equal to 3; or
inoculating the population of acid resistant AOB to a second reactor and supplying metal containing sludge to the second reactor, whereby the pH in the second reactor is maintained at less than or equal to 3;
such that metals in the sludge are at least partly dissolved in a liquid which is separated from the sludge to thereby at least partly remove the metals from the sludge.

14. A method as claimed in claim 13 wherein the reactor to which the stream that decreases the ratio of alkalinity to ammonium is fed is operated for 5-15 days, or around 10 days, to cause the pH to drop to around 6, and the reactor is continued to operate for between 40 and 70 days, or between 50 and 60 days and th

Assignees

• Univ Queensland

Inventors

• Wang Zhiyao

Classifications

• C02F2103/005

  Black water originating from toilets · CPC title

• C02F2103/002

  Grey water, e.g. from clothes washers, showers or dishwashers · CPC title

• C02F11/02 Primary

  Biological treatment · CPC title

• C02F2101/16

  Nitrogen compounds, e.g. ammonia · CPC title

• Y02W10/20

  Sludge processing · CPC title