Energy efficient system and process for treating sludge
US-9527760-B2 · Dec 27, 2016 · US
US9809481B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9809481-B2 |
| Application number | US-201615005469-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 25, 2016 |
| Priority date | Jan 27, 2015 |
| Publication date | Nov 7, 2017 |
| Grant date | Nov 7, 2017 |
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A waste stream is treated by anaerobic digestion. A process is described involves a step of separating solids from digestate, and returning separated solids to a digester. Optionally, there may be a step of solids separation in which larger solids are removed from the digester. A process and apparatus are described for treating waste sludge from a wastewater treatment plant in an anaerobic digester. Feed sludge is thickened or solids are separated from digestate and returned to the digester. Additional co-digestion waste may be added to the digester. The process and apparatus may be used in a retrofit of an existing wastewater treatment plant.
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I claim: 1. A process for treating WWTP sludge comprising the steps of, feeding the WWTP sludge at 12-20% TS to an anaerobic digester; operating the anaerobic digester at 6-12% TS without recuperative thickening; and, dewatering digestate in two stages. 2. The process of claim 1 further comprising adding nutrients to the digester in an amount effective to alleviate ammonia toxicity. 3. The process of claim 1 further comprising mixing the digester with a hydraulic or electric motor mixer. 4. The process of claim 1 comprising feeding the WWTP sludge at 15-20% TS to the anaerobic digester. 5. The process of claim 1 wherein the digestate is dewatered without a polymeric dewatering aid in a first stage and dewatered with a polymeric dewatering aid in a second stage. 6. The process of claim 1 wherein a portion of the WWTP sludge is dewatered before being fed to the anaerobic digester. 7. A process for treating WWTP sludge comprising the steps of, feeding the WWTP sludge at 1-5% TS to an anaerobic digester; operating the anaerobic digester at 4-6% TS; and, providing recuperative thickening for the digester by way of a side stream thickener; and, adding a polymeric thickening aid in the side stream, wherein the polymeric thickening aid is added at 3 kg/MT-TSS or less. 8. The process of claim 7 wherein waste digestate is dewatered separately from the side stream. 9. The process of claim 8 wherein a polymeric thickening aid is added at 7 kg/MT-TSS or less for dewatering. 10. The process of any claim 7 further comprising mixing the digester with a hydraulic or electric motor mixer.
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