Method and apparatus for selenium removal from high TDS wastewater
A process for removal of selenium and nitrate from waste water includes both electrochemical and bioprocessing treatment. Embodiments include use of activated walnut shell a growth media for selenium-reducing bacteria.
1. A method for removing nitrate from wastewater, comprising:
preconditioning wastewater containing nitrate, by a process comprising:
adjusting a pH of the wastewater to between 6.0 and 8.5;
removing precipitated inorganic salts from the wastewater by filtration;
electrochemically treating the wastewater to decrease the amount of at least one of oxygenated compounds and oxygen radicals, thereby reducing an oxidation reduction potential of the wastewater;
following the electrochemical treatment, treating the wastewater in at least one of a clarifier and a filter;
treating the wastewater in at least one column, said column packed with a porous media providing a surface for growth and maintenance of a biofilm upon and in the porous media, wherein said porous media is a chemically treated walnut shell media having a bulk density of 600 to 1000 Kg/m 3 and a particle size from 0.5 to 5.0 mm, wherein said biofilm reduces nitrate to form nitrogen gas; and
releasing the nitrogen gas from the at least one column into the environment.
2. The method of claim 1 , further comprising adding a carbon source to the wastewater upstream of the at least one column.
3. The method of claim 1 , wherein the walnut shell media is treated with an alkali prior to inclusion in the at least one column.
4. The method of claim 1 , further comprising filtering the wastewater subsequent to treatment in the at least one column.
5. The method of claim 4 , wherein the filtering is accomplished by at least one of media filtering, aerobic biological process and membrane filtration.
6. The method of claim 1 , further comprising physical and/or chemical treatment of the wastewater prior to treatment in the at least one column, wherein the physical treatment is clarification and the chemical treatment is pH adjustment and desaturation.
7. The method of claim 1 , wherein the oxidation reduction potential exiting the electrochemical process is reduced to less than but not including 0 mV.
8. The method of claim 1 , wherein the electrochemical treatment operates at a current density between 5 A/m 2 and 30 A/m 2 .
9. The method of claim 1 , wherein the wastewater is flue gas desulfurization blowdown water from a power plant.
10. The method of claim 1 , wherein the treatment in the column packed with a porous media has a hydraulic retention time between 30 and 60 minutes.
11. A method for treatment of wastewater from a flue gas desulfurization process, comprising:
providing wastewater from a flue gas desulfurization process, said wastewater comprising nitrate;
removing suspended solids from the wastewater;
adjusting a pH of the wastewater to between 6.0 and 8.5;
removing precipitated inorganic salts from the wastewater by filtration;
electrochemically treating the wastewater to decrease the amount of at least one of oxygenated compounds and oxygen radicals, thereby reducing an oxidation reduction potential of the wastewater;
treating the wastewater in at least one of a clarifier and a filter;
treating the wastewater containing nitrate in at least one column, said column packed with a porous media providing a surface for growth and maintenance of a biofilm upon and in the porous media, wherein the porous media is a chemically treated walnut shell media having a bulk density of 600 to 1000 Kg/m 3 and a particle size from 0.5 to 5.0 mm, wherein said biofilm reduces nitrate to form nitrogen gas;
backwashing said at least one column to remove an excess biomass from the column, wherein said backwashing does not diminish bioactivity of the biofilm growing upon and in the porous media; and
performing at least one of discharging and recycling the treated wastewater.
12. The method of claim 11 , further comprising filtering the wastewater subsequent to treatment in the at least one column.