The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Feb. 06, 2024

Filed:

Jun. 24, 2021
Applicant:

Fraunhofer-gesellschaft Zur Förderung Der Angewandten Forschung E.v., Munich, DE;

Inventors:

Andreas Hornung, Karlsruhe, DE;

Andreas Apfelbacher, Amberg, DE;

Miloud Ouadi, Birmingham, GB;

Johannes Neumann, Hersbruck, DE;

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10B 53/02 (2006.01); C10G 1/02 (2006.01); C10C 5/00 (2006.01); C10G 1/10 (2006.01); C10G 3/00 (2006.01); C10L 1/02 (2006.01); C10B 53/00 (2006.01); C10K 3/02 (2006.01); C10B 53/07 (2006.01); C10B 57/12 (2006.01); C10B 57/18 (2006.01);
U.S. Cl.
CPC ...
C10B 53/02 (2013.01); C10B 53/00 (2013.01); C10B 53/07 (2013.01); C10B 57/12 (2013.01); C10B 57/18 (2013.01); C10C 5/00 (2013.01); C10G 1/02 (2013.01); C10G 1/10 (2013.01); C10G 3/00 (2013.01); C10G 3/44 (2013.01); C10K 3/02 (2013.01); C10L 1/02 (2013.01); C10G 2300/1003 (2013.01); C10G 2300/1011 (2013.01); C10G 2300/1014 (2013.01); C10G 2300/1018 (2013.01); C10G 2400/30 (2013.01); C10L 2290/02 (2013.01); Y02E 50/10 (2013.01); Y02P 30/20 (2015.11);
Abstract

A method for producing a pyrolysis oil is described. In said method, a feedstock to be treated is first pyrolyzed in a pyrolysis zone, in which the feedstock is heated to a temperature of 250 degrees Celsius to 700 degrees Celsius; and pyrolyzed solids and pyrolysis vapors are formed. The pyrolysis vapors are then reformed at a temperature of 450 degrees Celsius to 1,200 degrees Celsius in a post-conditioning zone, in which the pyrolysis vapors are brought into contact with a catalyst bed, wherein the pyrolysis oil is formed. In this case, the catalyst comprises a pyrolyzed solid, which can be obtained according to the pyrolysis, described above. Finally the pyrolysis oil is separated from the additional pyrolysis products, which are formed, in a separation unit.


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