Intimate coupling of photocatalysis and biodegradation in a photocatalytic circulating-bed biofilm reactor
View Patent ↗Systems and methods are provided for intimately coupling advanced oxidation process (AOP) with biodegradation for the treatment of contaminated water. The system comprises a particulate bed having carrier particles that have a microbial film effective for biodegrading contaminants in the contaminated water. An advanced oxidation reagent is irradiated by a radiation source to provide an advanced oxidation reagent effective for oxidizing recalcitrant compounds in the contaminated water to form biodegradable byproducts. The microbial film is effective for biodegrading the byproducts substantially immediately after they are produced. The carrier particles are also effective for protecting the microbial film from the radiation and/or the recalcitrant compounds.
1. A system for the treatment of contaminated water, comprising:
a particulate bed comprising a plurality of porous carrier particles having a microbial film deposited therein and effective for biodegrading at least one contaminant present within a body of water;
a reaction vessel having an internal volume configured to recirculate the particulate bed that is disposed within the internal volume;
at least one advanced oxidation reagent source disposed within the internal volume of the reaction vessel;
a fluidizing mechanism configured to fluidize the particulate bed carrier particles and the at least one advanced oxidation reagent source; and
a radiation source configured to irradiate at least a portion of the advanced oxidation reagent source contained within the reaction vessel with radiation to provide at least one advanced oxidation reagent.
2. The system of claim 1 , wherein the radiation source comprises an ultraviolet light source.
3. The system of claim 1 , wherein the radiation source comprises a visible light source.
4. The system of claim 1 , wherein the fluidizing mechanism comprises a gas supply in communication with the reaction vessel.
5. The system of claim 4 , wherein the gas supply is configured to provide an oxygen-containing gas to the reaction vessel.
6. The system of claim 1 , wherein the fluidizing mechanism comprises a mechanical agitator.
7. The system of claim 1 , wherein the reaction vessel comprises a contaminated water inlet, a gas inlet, a treated water outlet, and a gas outlet in communication with the internal volume of the reaction vessel.
8. The system of claim 1 , wherein the advanced oxidation reagent source comprises TiO 2 .
9. The system of claim 8 , wherein TiO 2 is disposed within the internal volume of the reaction vessel in slurry form.
10. The system of claim 8 , wherein at least one of the plurality of porous carrier particles is partially impregnated with TiO 2 .
11. The system of claim 1 , wherein at least one of the plurality of porous carrier particles is partially impregnated with the advanced oxidation reagent source.
12. The system of claim 1 , wherein the advanced oxidation reagent is configured to oxidize the at least one contaminant to form a byproduct.
13. The system of claim 12 , wherein the microbial film is configured to biodegrade the byproduct.
14. The system of claim 1 , wherein the at least one contaminant comprises at least one recalcitrant compound.
15. The system of claim 14 , wherein the porous carrier particles are configured to protect at least some of the microbial film from the at least one recalcitrant compound.
16. The system of claim 1 , wherein the advanced oxidation reagent source is a photocatalyst.
17. A method of treating contaminated water, comprising:
providing a plurality of porous carrier particles having a microbial film effective for biodegrading at least one contaminant present within a body of water;
providing at least one advanced oxidation reagent source capable of providing at least one advanced oxidation reagent when subjected to radiation;
introducing the plurality of porous carrier particles and the at least one advanced oxidation reagent source into an internal volume of a reaction vessel;
introducing contaminated water containing at least one contaminant into the internal volume of the reaction vessel to thereby contact the contaminated water with the microbial film and with the at least one advanced oxidation reagent source; and
irradiating the at least one advanced oxidation reagent source with radiation to provide at least one advanced oxidation reagent capable of oxidizing the at least one contaminant in the contaminated water and to provide at least one advanced oxidation degradation product.
18. The method of claim 17 , wherein irradiating the at least one advanced oxidation reagent source with radiation comprises irradiating the at least one advanced oxidation reagent source with ultraviolet radiation.
19. The method of claim 17 , wherein irradiating the at least one advanced oxidation reagent source with radiation comprises irradiating the at least one advanced oxidation reagent source with radiation in the visible light spectrum.
20. The method of claim 17 , wherein the microbial film is effective for biodegrading the at least one advanced oxidation degradation product.
21. The method of claim 17 , wherein the advanced oxidation reagent source is TiO 2 .
22. The method of claim 17 , further comprising studding at least the surface of the porous carrier particles with the advanced oxidation reagent source.
23. The method of claim 17 , wherein providing the at least one advanced oxidation reagent source comprises providing the source in slurry form.
24. The method of claim 17 , wherein the at least one contaminant comprises at least one recalcitrant compound and at least one biodegradable compound, wherein the microbial film is effective for biodegrading the at least one biodegradable compound substantially simultaneously with the advanced oxidation reagent oxidizing the recalcitrant compound to provide the at least one advanced oxidation degradation product.