IP Library Granted Patent US 9,403,708
Granted Patent B2
US 9,403,708 · App. 13/259,710 · Granted Aug 2, 2016

Apparatus and method for thermal hydrolysis of organic matter

Inventor: Marianne Buchmuller (Uhlingen-Birkendorf, DE)
Assignee: Eliquo Stulz GmbH
C02F11/18C02F1/025C02F9/00C02F11/04C02F11/121C02F2301/063C02F2301/066C02F2303/06
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Quick Facts
Patent No.
US 9,403,708
App. No.
13/259,710
Granted
Aug 2, 2016
Kind
B2
Abstract

The invention relates to an apparatus for thermal hydrolysis of organic matter, wherein a heating element ( 2 ) and a cooling element ( 4 ) are provisioned to heat up or cool down the organic matter. Heat exchangers are provisioned as heating element ( 2 ) and cooling element ( 4 ) which exchange heat between the organic matter and a medium. The organic matter and the medium are separate relative to each other within the heat exchangers. A throttle ( 9 ) and a decompression tank ( 10 ) are provisioned between the heating element ( 2 ) and the cooling element ( 4 ).

Claims (16)

1. An apparatus for thermal hydrolysis of organic matter comprising at least one heating element and at least one cooling element to respectively heat up or cool down the organic matter, wherein a hydrolysis reactor is provided, with the organic matter being brought to a desired hydrolysis temperature therein that is equal to or below 170° C., the heating element and cooling element comprise indirect heat exchangers, respectively, which exchange heat between the organic matter and a liquid medium, further comprising a pump to supply the medium in a circuit between the heating element and the cooling element, the hydrolysis reactor for the organic matter between the heating element and a throttle, the organic matter and the medium being separated relative to each other within each of the heat exchangers, wherein the hydrolysis reactor also is an indirect heat exchanger heating the organic matter to the desired hydrolysis temperature and wherein an additional cooling element is functionally provided between the hydrolysis reactor and the throttle, and the additional cooling element is thermally coupled to the circuit of the medium via a first additional branch.

2. The apparatus according to claim 1 , comprising a decompression tank after the throttle.

3. The apparatus according to claim 2 , wherein the decompression tank is followed by a decompression tank valve to control the pressure within the decompression tank.

4. The apparatus according to claim 1 , wherein an additional heating element for the organic matter is functionally provided between the heating element and the hydrolysis reactor, and the additional heating element is thermally coupled to the circuit of the medium via the first additional branch.

5. The apparatus according to claim 1 , wherein the flow through the first additional branch can be controlled by means of a heating mixing valve.

6. The apparatus according to claim 5 , wherein a pump for the organic matter is provided before the heating element.

7. The apparatus according to claim 1 , wherein a condensation tank for the organic matter is functionally provided after the cooling element.

8. The apparatus according to claim 7 , having a condensation tank gas valve to control the discharge of the gaseous phase of the organic matter from the condensation tank.

9. The apparatus according to claim 7 , comprising a condensate cooling element after the condensation tank to cool the organic matter.

10. The apparatus according to claim 9 , wherein the condensate cooling element is thermally coupled to the heating element and the cooling element via a second additional branch of the circuit of the medium, and a cooling mixing valve to control the distribution of the medium among the cooling element and the condensate cooling element.

11. An apparatus for thermal hydrolysis of organic matter comprising at least one heating element and at least one cooling element to respectively heat up or cool down the organic matter, the heating element and cooling element comprise heat exchangers which exchange heat between the organic matter and a liquid, the organic matter and the liquid being separated relative to each other within each of the heat exchangers, a throttle located between the heating element and the cooling element, a pump to supply the liquid in a circuit between the heating element and the cooling element, a hydrolysis reactor for the organic matter located between the heating element and the throttle, and

wherein an additional cooling element is functionally provided between the hydrolysis reactor and the throttle, and the additional cooling element is thermally coupled to the liquid circuit via a first additional branch.

12. The apparatus according to claim 11 wherein an additional heating element for the organic matter is functionally provided between the heating element and the hydrolysis reactor, and the additional heating element is thermally coupled to the liquid circuit via the first additional branch.

13. The apparatus according to claim 11 , wherein the flow through the first additional branch can be controlled by means of a heating mixing valve.

14. The apparatus according to claim 13 wherein a pump for the organic matter is provided before the heating element.

15. An apparatus for thermal hydrolysis of organic matter comprising at least one heating element and at least one cooling element to respectively heat up or cool down the organic matter, the heating element and cooling element comprise heat exchangers, which exchange heat between the organic matter and a liquid, a pump to supply the liquid in a circuit between the heating element and the cooling element, a throttle between heating element and cooling element, a condensation tank for the organic matter is functionally provided after the cooling element, a condensate cooling element after the condensation tank to cool the organic matter, the organic matter and the liquid being separated relative to each other within each of the heat exchangers, the condensate cooling element being thermally coupled to the heating element and the cooling element via a second additional branch of the liquid circuit, and a cooling mixing valve to control the distribution of the medium among the cooling element and the condensate cooling element.

Assignments (4)
CORRECTIVE ASSIGNMENT TO CORRECT THE ADDRESS OF THE ASSIGNEE PREVIOUSLY RECORDED ON REEL 038424 FRAME 0816. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Oct 14, 2016
From: SH+E GMBH
To: ELIQUO STULZ GMBH
Reel/Frame 040013/0722 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 29, 2016
From: SH+E GMBH
To: ELIQUO STULZ GMBH
Reel/Frame 038424/0816 →
CHANGE OF NAME Recorded Apr 27, 2016
From: STULZ H+E GMBH
To: SH+E GMBH
Reel/Frame 038543/0479 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 27, 2011
From: BUCHMULLER, MARIANNE
To: STULZ H+E GMBH
Reel/Frame 027130/0623 →
Priority Claims (1)
DE 10 2009 014 776 · Mar 25, 2009 · national
Continuity (1)
Related Publication 20120061318A1 · Mar 15, 2012