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. 20, 2018

Filed:

Jun. 04, 2014
Applicants:

Desmond Radlein, Waterloo, CA;

Alain Quignard, Roussillon, FR;

Inventors:

Desmond Radlein, Waterloo, CA;

Alain Quignard, Roussillon, FR;

Assignees:

IFP ENERGIES NOUVELLES, Rueil-Malmaison Cedek, FR;

Dynamotive Energy Systems, Vancouver, CA;

RADLEIN, DESMOND, Waterloo, Ontario, CA;

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C07C 1/20 (2006.01); C07C 4/02 (2006.01); C10G 47/02 (2006.01); C10G 45/04 (2006.01); C10G 3/00 (2006.01); C07C 5/10 (2006.01);
U.S. Cl.
CPC ...
C07C 1/20 (2013.01); C07C 4/02 (2013.01); C07C 5/10 (2013.01); C10G 3/44 (2013.01); C10G 3/50 (2013.01); C10G 45/04 (2013.01); C10G 47/02 (2013.01); C10G 2300/1014 (2013.01); C10G 2300/1018 (2013.01); C10G 2300/1048 (2013.01); C10G 2300/4081 (2013.01); C10G 2300/44 (2013.01); C10G 2400/02 (2013.01); C10G 2400/04 (2013.01); C10G 2400/08 (2013.01); Y02P 30/20 (2015.11);
Abstract

The present invention relates to the field of biomass derived fuels. It further relates to thermochemical production of liquids (biooils) from biomass. Specifically the present invention relates to methods of upgrading biooil. More specifically it relates to a method for upgrading biooil comprising contacting a dispersed mixture of hydrocarbon liquids, biooil, and partially upgraded biooil, with a transition metal containing catalyst and hydrogen gas at a temperature of around 330° C. and a pressure of about 1700 psi (11.7 MPa) for a period of time sufficient to reduce the oxygen content of the biooil such that it separates on cooling into an aqueous phase and an organic phase, and optionally, to further subject the organic phase to hydrotreating, hydrocracking or catalytic cracking to produce a mixture of hydrocarbons boiling in the range of gasoline, diesel and jet fuel.


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