Electromagnetic-force-based dewatering for sewage sludge reduction
US-2018346363-A1 · Dec 6, 2018 · US
US11613484B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11613484-B2 |
| Application number | US-201615167324-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 27, 2016 |
| Priority date | May 29, 2015 |
| Publication date | Mar 28, 2023 |
| Grant date | Mar 28, 2023 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Solid waste, for example source separated organics (SSO) or commercial and industrial (C&I) waste or both, are treated by first pressurizing the waste against a screen to produce a solids fraction and a liquid fraction. The liquid fraction can be treated in an anaerobic digester. The solids fraction is pulverized or milled, for example with a hammer mill, preferably after being diluted. The pulverized or milled waste is separated again to provide a second solids faction and a second liquid fraction. The liquid fraction can be treated in an anaerobic digester. The solids fraction is primarily inert and can be landfilled, preferably after being washed.
Opening claim text (preview).
We claim: 1. A method of treating solid waste including organic material, the method comprising steps of, a) extruding or pressing the waste to separate a dry fraction from a wet fraction; b) diluting the dry fraction with water of digester filtrate; c) pulverizing or milling the diluted dry fraction, and separating the pulverized or milled diluted dry fraction into (i) a liquid fraction that includes residual organics and (ii) dry fraction rejects by passing the pulverized or milled diluted dry fraction to a screen that retains the dry fraction rejects and permits the passage of the liquid fraction while or after pulverizing or milling the diluted dry fraction; and d) washing the separated dry fraction rejects to remove organic film or organics. 2. The method of claim 1 wherein the wet fraction is treated in an anaerobic digester. 3. The method of claim 1 wherein the residual organics are treated in an anaerobic digester. 4. The method of claim 1 wherein wash water produced from washing the dry fraction rejects is treated by anaerobic digestion. 5. The method of claim 1 , wherein extruding or pressing the waste is performed at a pressure from 50 to 180 bar. 6. The method of claim 1 , wherein the wet fraction comprises over 80% of the organic material. 7. The method of claim 6 , wherein the wet fraction comprises over 90% of the organic material. 8. The method of claim 1 , wherein the solid waste is: source separated organics, commercial waste, industrial waste, or any combination thereof.
Fuel from waste, e.g. synthetic alcohol or diesel · CPC title
Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses · CPC title
using filter presses (C02F11/123 takes precedence) · CPC title
the feedstock being materials of biological origin · CPC title
Anaerobic digestion processes · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.