Water treatment method and water treatment apparatus
US-2024383788-A1 · Nov 21, 2024 · US
US10919792B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10919792-B2 |
| Application number | US-201314405175-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 15, 2013 |
| Priority date | Jun 11, 2012 |
| Publication date | Feb 16, 2021 |
| Grant date | Feb 16, 2021 |
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A system and method is provided for water and wastewater treatment. The system comprises a fixed film biological process and a ballasted flocculation process.
Opening claim text (preview).
The invention claimed is: 1. A method for treating wastewater, comprising: introducing a source of wastewater to a fixed film biological reactor to provide a fixed film effluent; adding a magnetic ballast to the fixed film effluent to provide a ballasted effluent; separating the ballasted effluent into a treated effluent and ballasted solids in a clarifier; magnetically separating the ballasted solids into recovered ballast and ballast-free solids; adding at least a portion of the ballast-free solids to the source of wastewater; and adding at least a portion of the recovered ballast to the fixed film effluent, wherein no cleaning solution is used for ballast recovery. 2. The method of claim 1 , further comprising adding a flocculant to the ballasted effluent. 3. The method of claim 1 , further comprising adding a coagulant to the fixed film effluent to provide a coagulated effluent. 4. The method of claim 3 , further comprising adding a portion of the ballast-free solids to at least one of the fixed film effluent, and the coagulated effluent. 5. The method of claim 3 , further comprising adding a portion of the ballasted solids to at least one of the source of wastewater, the fixed film effluent, and the coagulated effluent. 6. The method of claim 1 , wherein the fixed film effluent comprises 50 mg/l to 300 mg/l of biological solids. 7. The method of claim 1 , wherein the ballast comprises magnetite. 8. The method of claim 1 , wherein the wastewater is treated at a rate of between 200 gallons per day per square foot of a surface area of the clarifier to 6,000 gallons per day per square foot of the surface area of the clarifier. 9. The method of claim 1 , wherein the magnetic ballast has a particle size of less than 40 μm. 10. The method of claim 9 , wherein the magnetic ballast has a particle size of less than 20 μm. 11. The method of claim 1 , wherein the magnetic ballast is added in a dry or powdered form. 12. The method of claim 1 , further comprising subjecting the ballasted solids to mechanical shearing prior to magnetic separation. 13. The method of claim 1 , wherein at least one of a coagulation tank, a ballast feed tank, and a flocculation tank is integrated into the clarifier. 14. The method of claim 1 , further comprising bypassing the fixed film biological reactor during a high flow event. 15. The method of claim 1 , further comprising subjecting the wastewater to clarification upstream of the fixed film biological reactor.
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