Anaerobic fermentation to produce biogas

Patent metadata

Field	Value
Publication number	US-10144664-B2
Application number	US-201615209259-A
Country	US
Kind code	B2
Filing date	Jul 13, 2016
Priority date	Feb 18, 2009
Publication date	Dec 4, 2018
Grant date	Dec 4, 2018

Abstract

A process and apparatus for the anaerobic digestion of organic wastes, preferably to also produce a useful biogas, is described. The waste may have a total solids (TS) concentration of 6% or less while a digester is operated at a higher solids concentration, for example with a feed TS concentration of 8-12%. One or more separation stages downstream of the digester separate active bacteria and undigested organics from the digestate, and return separated matter to the digester. Optionally, a feed thickening apparatus and step may be provided upstream of the digester. The upstream thickener and recycle from the downstream separation stages are operated such that the TS of the combined inputs to the digester is within a desired range.

First claim

I claim:

1. A process for the treatment of a liquid comprising organic material, the process comprising steps of, anaerobic digestion of the liquid to produce a digestate; and separating solids from the digestate in two or more sequential separation steps wherein an upstream one of the two or more sequential separation steps comprises separating particles above a first size and a downstream one of the two or more sequential separation steps comprises separating particles above a second size that is smaller than the first size, wherein an amount of separated matter from each separation step that is recycled to the digester, expressed as a percentage of the total amount of separated matter, increases or is constant in the downstream direction between adjacent separation steps.

2. The process of claim 1 wherein separated solids removed from the upstream one of the separation steps are not recycled to the digester.

3. The process of claim 1 wherein a recycle stream from the downstream one of the separation steps has a solids concentration greater than a combined input solids concentration for the anaerobic digestion step.

4. The process of claim 1 further comprising a step of membrane separation downstream of the downstream one of the separation steps, wherein solids separated in the membrane separation step are recycled to the digester.

5. The process of claim 1 further comprising a step of thickening the liquid upstream of the digester.

6. The process of claim 1 wherein the upstream one of the separation steps comprises separation by one of a static screen, a vibrating screen, and a screw press.

7. A process for the treatment of a liquid comprising organic material, the process comprising steps of, anaerobic digestion of the liquid in a digester to produce a digestate; separating solids from the digestate in two or more sequential separation steps comprising a membrane separation step; and, recycling separated matter from two or more of the separation steps to the digester in two or more recycle streams wherein one of the one or more recycle streams has a total solids concentration that is above the total solids concentration of the liquid in the digester and the recycle stream from the membrane separation step has a total solids concentration that is less than the total solids concentration of the liquid in the digester.

8. The process of claim 7 further comprising a step of thickening the liquid prior to anaerobic digestion of the liquid.

9. The process of claim 8 wherein the extent of thickening of the liquid is selected so as to produce, in combination with the flow rate and solids concentration of the two or more recycle streams, a combined input solids concentration to the digester that is within a predetermined operating range.

10. The process of claim 8 wherein the thickened liquid has a TS concentration that is higher than the TS concentration of a flow rate weighted average of the TS concentrations of the thickened liquid and recycle steams.

11. The process of claim 7 wherein the liquid has a TS concentration of 6% or less.

12. The process of claim 11 wherein the digester is operated as a mixed reactor with feed, including any recirculated streams, at a combined input solids concentration of 8-12%.

13. The process of claim 7 wherein two or more post-digester effluent streams are produced.

Assignees

• Anaergia Inc

Inventors

• Benedek Andrew

Classifications

• C12P5/023

  Methane · CPC title

• B01D2311/2649

  Filtration · CPC title

• B01D61/18

  Apparatus therefor · CPC title

• C02F2203/004

  comprising a selector reactor for promoting floc-forming or other bacteria · CPC title

• B01D61/145

  Ultrafiltration · CPC title