IP Library Granted Patent US 10,118,851
Granted Patent B2
US 10,118,851 · App. 15/225,180 · Granted Nov 6, 2018

Process for the anaerobic fermentation of biogenic waste materials and plant for carrying out this process

Inventors: Adrian Schatz (Niederwangen, CH); René Leisner (Constance, DE)
Assignee: HITACHI ZOSEN INOVA AG
C02F11/04C02F11/121C12M21/04C12M29/04C12M29/18C12M41/36C12M47/02C12M47/14C12P5/023Y02W30/43Y02W30/47
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Quick Facts
Patent No.
US 10,118,851
App. No.
15/225,180
Granted
Nov 6, 2018
Kind
B2
Abstract

A process for the anaerobic fermentation of biogenic waste materials including the steps that a fermentation material containing the waste materials is mixed with liquid and the fermentation material suspension obtained in this manner is anaerobically fermented in a fermenter and the digest produced in the fermentation of the fermentation material suspension is dewatered of a dewatering device, wherein, with separation of press water, a press cake is obtained that has a dry matter proportion increased with respect to the digest; the press water is subjected to a solids separation, wherein a residual liquid having a dry matter proportion reduced with respect to the press water of at most 15% by weight is obtained and the residual liquid is used at least in part for the mixing according to the fermentation material step.

Claims (27)

1. A process for the anaerobic fermentation of biogenic waste materials, comprising:

a) mixing a liquid with a fermentation material containing the waste materials to obtain a fermentation material suspension, and anaerobically fermenting the fermentation material suspension in a fermenter to produce a digest;

b) dewatering the digest by means of a dewatering device to obtain a press water and a press cake having a dry matter proportion increased with respect to the digest; and

c) subjecting the press water to a solids separation to obtain a residual liquid having a dry matter proportion reduced with respect to the press water, the dry matter proportion of the residual liquid being at most 15% by weight,

wherein the residual liquid is used at least in part for the mixing according to step a).

2. The process as claimed in claim 1 , performed continuously or semi-continuously.

3. The process as claimed in claim 1 , wherein the solids separation according to step c) is performed by means of filtration and/or by means of screening, and the residual liquid is formed by the filtrate of the filtration or by the screen underflow of the screening.

4. The process as claimed in claim 1 , wherein the press water obtained in step b) and/or the residual liquid obtained in step c) is temporarily stored before the respective following step.

5. The process as claimed in claim 1 , wherein step a) comprises mixing the fermentation material in a mixing device with the residual liquid and optionally further water to obtain the fermentation material suspension.

6. The process as claimed in claim 1 , wherein the dry matter proportion in the fermentation material suspension in step a) is between 25 and 35% by weight.

7. The process as claimed in claim 1 , wherein a part of the digest, the press cake obtained during the dewatering according to step b), the residual solids obtained in the solids separation in step c), or a mixture thereof is added to the fermentation material or the fermentation material suspension as inoculum material.

8. The process as claimed in claim 1 , further comprising determining and setting to a desired value one or more parameters of the residual liquid, said parameters being selected from the group consisting of:

pH,

buffer capacity,

H 2 S content,

ammonium ion content or ammonia content,

content of fatty acids, and

content of short-chain carboxylic acids.

9. The process as claimed in claim 1 , further comprising adding at least one of the following auxiliaries or additives to the residual liquid:

acid,

lye,

buffer,

micronutrient elements or trace elements, and

macronutrient elements.

10. The process as claimed in claim 3 , wherein the solids separation according to step c) is performed by means of screening having two or more screening stages, wherein, in a first screening stage c1), a coarse fraction of solids components is separated off from the press water and from the suspension remaining from the stage c1) as screen underflow, in a subsequent second screening stage c2), a fine fraction is separated off in order to obtain the residual liquid.

11. The process as claimed in claim 1 , wherein the solids separation according to step c) is performed using a vibrating screen and/or a shaking screen.

12. The process as claimed in claim 10 , wherein the solids separation according to step c) is performed using a vibrating screen and/or a shaking screen.

Assignments (2)
CHANGE OF NAME Recorded Dec 13, 2024
From: HITACHI ZOSEN INOVA AG
To: KANADEVIA INOVA AG
Reel/Frame 069580/0109 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 3, 2016
From: SCHATZ, ADRIAN; LEISNER, RENÉ
To: HITACHI ZOSEN INOVA AG
Reel/Frame 039921/0979 →
Priority Claims (1)
EP 15179224 · Jul 31, 2015 · regional
Continuity (1)
Related Publication 20170029309A1 · Feb 2, 2017