IP Library Granted Patent US 9,957,201
Granted Patent B2
US 9,957,201 · App. 14/980,905 · Granted May 1, 2018

Producing liquid fertilizer in a biogas plant

Inventor: Rolf Liebeneiner (Stockdorf, DE)
Assignee: BEKON GmbH
C05F17/009C05F17/0258C05G3/0064C12M21/04C12M23/40C12M23/58C12M29/00C12M29/02C12M29/18C12M29/26C12M33/00C12M33/14C12M37/02C12M41/14C12M41/16C12M41/22C12M41/24C12M41/48C12M47/16C12P5/023Y02E50/343Y02P20/145Y02W30/43Y02W30/47
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Quick Facts
Patent No.
US 9,957,201
App. No.
14/980,905
Granted
May 1, 2018
Kind
B2
Abstract

A biogas plant produces both methane and liquid fertilizer by fermenting biomass. The plant includes a fermenter, a percolate tank and a sanitation tank located inside the percolate tank. Dry fermentation takes place in the fermenter and generates methane and a percolate. The percolate is circulated between the fermenter and the percolate tank. Percolate that is returned from the percolate tank to the fermenter is sprinkled over the biomass. A portion of the percolate is transferred from the percolate tank into the sanitation tank. The percolate in the sanitation tank is sanitized by heating to a Celsius temperature between 45° and 65° for a period of at least five days. The percolate in the sanitation tank is heated using both a heating device in the sanitation tank as well as heat generated from a thermophilic fermentation reaction occurring in the percolate tank. The sanitized percolate is used as liquid fertilizer.

Claims (26)

1. A method for producing liquid fertilizer, comprising:

fermenting biomass in a fermenter using dry fermentation, wherein the fermenting generates percolate;

circulating the percolate between the fermenter and a percolate tank;

transferring a first portion of the percolate from the percolate tank into a sanitation tank;

sanitizing the percolate contained in the sanitation tank using a thermophilic fermentation reaction at a Celsius temperature between 45° and 65° for a period of at least five days; and

draining the sanitized percolate as the liquid fertilizer from the sanitation tank.

2. The method of claim 1 , further comprising:

transferring a second portion of the percolate from the percolate tank into the sanitation tank after the draining of the sanitized percolate from the sanitation tank.

3. The method of claim 1 , wherein the first portion of the percolate is transferred from the percolate tank into the sanitation tank when a fill level sensor indicates that the sanitation tank is empty.

4. The method of claim 1 , wherein the first portion of the percolate is transferred from the percolate tank into the sanitation tank when a fill level sensor indicates that the percolate tank is full.

5. The method of claim 1 , wherein the sanitized percolate is drained from the sanitation tank into a storage tank.

6. The method of claim 5 , wherein the first portion of the percolate is transferred from the percolate tank into the sanitation tank when a fill level sensor indicates that the storage tank has been drained.

7. The method of claim 1 , wherein the first portion of the percolate passes through a valve from the percolate tank into the sanitation tank, and wherein the valve is closed during the sanitizing.

8. A method comprising:

generating methane by fermenting biomass in a fermenter, wherein the fermenting generates a percolate;

transferring the percolate from the fermenter to a percolate tank;

returning the percolate from the percolate tank to the fermenter and sprinkling the percolate over the biomass;

transferring a first portion of the percolate from the percolate tank into a sanitation tank;

heating the percolate contained in the sanitation tank to a Celsius temperature between 45° and 65° for a period of at least five days; and

draining the percolate from the sanitation tank.

9. The method of claim 8 , wherein the sanitation tank is arranged concentrically inside the percolate tank.

10. The method of claim 9 , wherein the heating of the percolate contained in the sanitation tank is performed using heat generated from a thermophilic fermentation reaction occurring in the percolate tank.

11. The method of claim 8 , further comprising:

transferring a second portion of the percolate from the percolate tank into the sanitation tank after the draining the percolate from the sanitation tank.

12. The method of claim 8 , wherein the first portion of the percolate is transferred from the percolate tank into the sanitation tank when a fill level sensor indicates that the sanitation tank is empty.

13. The method of claim 8 , wherein the first portion of the percolate passes through a valve from the percolate tank into the sanitation tank, and wherein the valve is closed during the period of at least five days when the percolate contained in the sanitation tank is heated to the Celsius temperature between 45° and 65°.

Assignments (2)
CHANGE OF NAME Recorded Dec 30, 2016
From: BEKON HOLDING AG
To: BEKON GMBH
Reel/Frame 041229/0120 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 28, 2015
From: LIEBENEINER, ROLF
To: BEKON HOLDING AG
Reel/Frame 037394/0354 →
Priority Claims (1)
DE 10 2013 211 3258 · Jul 5, 2013 · national
Continuity (2)
Continuation In Part PCTEP2014064338 · Jul 4, 2014
Related Publication 20160107946A1 · Apr 21, 2016