IP Library Granted Patent US 8,722,948
Granted Patent B2
US 8,722,948 · App. 12/841,462 · Granted May 13, 2014

Method for catalytically processing slurry

Inventor: Jürgen Buchert (Schweinfurt, DE)
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Quick Facts
Patent No.
US 8,722,948
App. No.
12/841,462
Granted
May 13, 2014
Kind
B2
Abstract

In a method for thermal processing of slurry, slurry is combined with a bio-mass to produce a mixture. The mixture is subjected in a heated mixer pump to a cracking temperature, thereby allowing the mixture to catalytically undergo a cracking reaction to produce a reaction mixture which is directly outgased in the mixer pump to produce an outgased portion and a solid portion. The outgased portion and the solid portion are separately discharged from the mixer pump; with the low boiling fraction of the outgased portion allowed to cool down for further processing, and the solid portion collected in a residual matter container for further processing.

Claims (23)

1. A method of thermal processing of slurry, comprising the steps of:

combining slurry with a bio-mass to produce a mixture;

subjecting the mixture in a heated mixer pump to a cracking temperature, thereby allowing the mixture to undergo a cracking reaction to produce a reaction mixture;

directly outgasing the reaction mixture in the mixer pump to produce an outgased portion and a solid portion;

separately discharging the outgased portion and the solid portion from the mixer pump;

allowing the outgased portion to cool down for further processing;

collecting the solid portion in a residual matter container for further processing.

2. The method of claim 1 , wherein the cracking temperature is in the range of about 250° C. to about 380° C.

3. The method of claim 1 , wherein the combining step is executed upstream of the mixer pump.

4. The method of claim 1 , further comprising the step of adding a catalyst to at least one member selected from the group consisting of slurry and bio-mass.

5. The method of claim 4 , wherein the catalyst is added during the combining step of slurry and bio-mass.

6. The method of claim 1 , further comprising the step of dewatering at least one member selected from the group consisting of slurry and bio-mass before the combining step.

7. The method of claim 1 , wherein the subjecting step is executed in the presence of a nitrogen (N 2 ) atmosphere.

8. The method of claim 1 , further comprising the step of adding pure oxygen (O 2 ) or air to the solid portion in a controlled manner.

9. The method of claim 1 , further comprising the step of removing heat from the solid portion.

10. The method of claim 9 , further comprising the step of feeding back heat removed from the solid portion.

11. The method of claim 10 , wherein the removed heat is used for heating at least one member selected from the group consisting of slurry and bio-mass.

12. The method of claim 10 , wherein the removed heat is used for heating the mixer pump.

13. The method of claim 10 , wherein the removed heat is used for generating electricity.

14. The method of claim 1 , wherein the bio-mass is a biological waste material.

15. The method of claim 14 , wherein the biological waste material includes rape residues or wood residues.

16. The method of claim 4 , wherein at least one member selected from the group consisting of slurry, bio-mass, and catalyst, has a fine-grained structure.

17. The method of claim 4 , further comprising the step of recovering catalyst mass from the solid portion.

Priority Claims (1)
DE 10 2007 011 763 · Mar 10, 2007 · national
Continuity (2)
Division 11854857 · Sep 13, 2007
Related Publication 20100288622A1 · Nov 18, 2010