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:
Sep. 12, 2017

Filed:

Nov. 24, 2014
Applicant:

Uop Llc, Des Plaines, IL (US);

Inventors:

Lance Awender Baird, Prospect Heights, IL (US);

Timothy A. Brandvold, Arlington Heights, IL (US);

Stanley Joseph Frey, Palatine, IL (US);

Assignee:

UOP LLC, Des Plaines, IL (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10L 1/06 (2006.01); C07C 1/22 (2006.01); C07C 5/367 (2006.01); C10G 3/00 (2006.01);
U.S. Cl.
CPC ...
C07C 1/22 (2013.01); C07C 5/367 (2013.01); C10G 3/42 (2013.01); C10G 3/47 (2013.01); C07C 2521/04 (2013.01); C07C 2521/06 (2013.01); C07C 2523/42 (2013.01); C07C 2523/44 (2013.01); Y02P 30/20 (2015.11);
Abstract

Methods and apparatuses are provided for deoxygenating pyrolysis oil. A method includes contacting a pyrolysis oil with a deoxygenation catalyst in a first reactor at deoxygenation conditions to produce a first reactor effluent. The first reactor effluent has a first oxygen concentration and a first hydrogen concentration, based on hydrocarbons in the first reactor effluent, and the first reactor effluent includes an aromatic compound. The first reactor effluent is contacted with a dehydrogenation catalyst in a second reactor at conditions that deoxygenate the first reactor effluent while preserving the aromatic compound to produce a second reactor effluent. The second reactor effluent has a second oxygen concentration lower than the first oxygen concentration and a second hydrogen concentration that is equal to or lower than the first hydrogen concentration, where the second oxygen concentration and the second hydrogen concentration are based on the hydrocarbons in the second reactor effluent.


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