Wastewater treatment with in-film microbial heating

Patent metadata

Field	Value
Publication number	US-10981817-B2
Application number	US-201815875511-A
Country	US
Kind code	B2
Filing date	Jan 19, 2018
Priority date	Jan 19, 2018
Publication date	Apr 20, 2021
Grant date	Apr 20, 2021

Abstract

A technique for wastewater treatment involves ensuring that all paths for wastewater must pass through at least one porous microbial support to go from the inlet to the outlet, and allowing a biofilm to grow on the porous microbial support under microaerobic conditions (concentration of oxygen between 0.05 and 0.35 mg/L). The biofilm formed comprises a population of anaerobic microbes for digesting organics in the wastewater including methanogenic microbes, and an aerobic methanotrophic and heterotrophic population that catabolizes methane from the methanogenic microbes, and oxygen from the injector, to produce heat. The support may be an electrode, and the technique is applied in a microbial electrolysis cell, with substantial COD removal rates.

First claim

The invention claimed is:

1. A method for wastewater treatment comprising:
providing a reactor having at least two porous microbial supports that are conductive in parallel or series such that a wastewater must pass through the at least two porous microbial supports to exit;
supplying the wastewater at an inlet of the reactor;
supplying oxygen into the reactor to permit a consortium of microbes to define a biofilm on the at least two porous microbial supports, the biofilm comprising anaerobic electroactive and methanogenic microbes covered, and protected from oxygen, by a layer of aerobic methanotrophs and heterotrophs; and
supplying up to 10 A at 0.5-1.5 V power with at least one power supply to the at least two porous microbial supports to define an anodic and a cathodic microbial support, forming a microbial electrolysis cell,

wherein the methanotrophs catabolize methane produced by the methanogenic microbes and the oxygen supplied, to provide heat within the biofilm for the growth of the biofilm and decomposition of organics within the wastewater, and wherein supplying oxygen into the reactor includes supplying oxygen to both the anodic and the cathodic microbial supports.

2. The method of claim 1 wherein the at least two porous microbial supports define in the reactor at least one sludge and/or scum collection region.

3. The method of claim 1 wherein the oxygen is supplied adjacent or directly to at least one of the at least two porous microbial supports.

4. The method of claim 3 wherein the oxygen is supplied so that the concentration of oxygen in the wastewater is between 0.05 and 0.35 mg/L averaged over the wastewater volume in the reactor in an operating interval of 12 min. or less.

5. The method of claim 4 wherein the supplied power is intermittent, having a period of less than 20 min. and a duty cycle of at least 10%.

6. The method of claim 3 wherein the microbial electrolysis cell is operated such that the biofilm naturally formed exhibits bioelectrochemical activity.

7. The method of claim 4 wherein a wastewater treatment control processor is adapted to monitor a parameter of the wastewater by coupling to the at least one power supply.

8. The method of claim 2 wherein the at least two porous microbial supports are substantially larger than the at least one sludge and/or scum collection region.

9. A flow-through wastewater treatment reactor comprising:
a reactor having an inlet for wastewater, an outlet for treated water, and intermediate the inlet and outlet, at least two porous microbial supports that are conductive through which the wastewater must pass to go from the inlet to the outlet;
an air injector for introducing oxygen into the reactor to microaerate the wastewater; and
at least one power supply coupled to two of the at least two porous microbial supports, wherein the at least two porous microbial supports are separated from each other by a porous insulator defining at least one anode and at least one cathode, the at least one power supply adapted to supply power to the at least two porous microbial supports of up to 10 A at 0.5-1.5 V such that a microbial electrolysis cell is formed,

whereby biofilms formed on the at least two porous microbial supports comprise: a population of anaerobic microbes for digesting organics in the wastewater, including methanogenic microbes, and an aerobic methanotrophic and heterotrophic population that catabolizes methane from the methanogenic microbes and organic matter, respectively, and oxygen from the injector and an anodophilic microorganism layer intimate with the at least one anode, underlying the methanogenic microbes.

10. The reactor of claim 9 wherein one of the at least two porous microbial supports is a part of a cartridge insertable in the reactor in a slot thereof.

11. The reactor of claim 9 wherein two of the at least two porous microbial supports are arranged in parallel or series, and the air injector is located proximate or inside at least one of the at least two porous microbial supports.

12. The reactor of claim 9 wherein the air injector is adapted to supply air at a rate that maintains a concentration of oxygen in the wastewater between 0.05 and 0.35 mg/L averaged over the wastewater volume in the reactor in an operating interval of 12 min. or less.

13. The reactor of claim 9 wherein the supplied electrical power is intermittent, having a period of less than 20 min. and a duty cycle of at least 10%.

14. The reactor of claim 9 further comprising: a vent for collecting biogas from the reactor; at least one sludge and/or scum collection region spatially separated from the at least two porous microbial support; or a spent sludge trap for collecting inert solids.

15. The reactor of claim 9 wherein the biofilms further comprise: H 2 S oxidizing aerobic heterotrophic microbes; or a population of ammonium nitrifying aerobic and/or anodophilic and cathodophilic microbes.

16. The reactor of claim 12 further comprising a wastewater treatment control processor adapted to monitor a parameter of the wastewater by determining one of power, current, resistance, or voltage of a lead of the at least one power supply.

17. The reactor of claim 9 wherein wastewater is drawn through the reactor by gravity alone.

18. The reactor of claim 10 wherein the injector is a part of the cartridge, the air injector adapted to supply volumes of the air so that an aeration to wastewater flow ratio of 3.5 to 14 (UL) is maintained.

19. The reactor of claim 9 wherein the biofilms at the at least two porous microbial supports are less than 1 mm thick and are adapted for bioelectrochemical decomposition involving: oxidation of organics at the at least one anode, production of H 2 at the electrode that is cathodic, and/or production of CH 4 ; and/or CH 4 oxidation by the aerobic methanotrophic and heterotrophic populations.

Assignees

• Nat Res Council Canada

Inventors

• Tartakovsky Boris
• Kleiner Yehuda

Classifications

• C02F2101/30

  Organic compounds · CPC title

• C02F3/005 Primary

  Combined electrochemical biological processes (aeration by electrolytically produced oxygen bubbles C02F3/202) · CPC title

• C02F3/301 Primary

  Aerobic and anaerobic treatment in the same reactor · CPC title

• C02F2103/32

  from the food or foodstuff industry, e.g. brewery waste waters · CPC title

• C02F2101/16

  Nitrogen compounds, e.g. ammonia · CPC title