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:
Dec. 22, 2015

Filed:

Apr. 23, 2012
Applicants:

John William Harris, Amsterdam, NL;

Sander Van Paasen, Amsterdam, NL;

Johan Willem Gosselink, Amsterdam, NL;

Colin John Schaverien, Amsterdam, NL;

Nicolaas Wilhelmus Joseph Way, Amsterdam, NL;

Andries Hendrik Janssen, Amsterdam, NL;

Inventors:

John William Harris, Amsterdam, NL;

Sander Van Paasen, Amsterdam, NL;

Johan Willem Gosselink, Amsterdam, NL;

Colin John Schaverien, Amsterdam, NL;

Nicolaas Wilhelmus Joseph Way, Amsterdam, NL;

Andries Hendrik Janssen, Amsterdam, NL;

Assignee:

Shell Oil Company, Houston, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 1/00 (2006.01); C10G 1/10 (2006.01); B01J 8/00 (2006.01); B01J 8/18 (2006.01); C10B 49/22 (2006.01); C10B 53/02 (2006.01); C10B 57/06 (2006.01); C10G 1/08 (2006.01); C10G 3/00 (2006.01); C10G 11/18 (2006.01); C10L 1/02 (2006.01);
U.S. Cl.
CPC ...
C10G 1/10 (2013.01); B01J 8/0055 (2013.01); B01J 8/1827 (2013.01); B01J 8/1863 (2013.01); C10B 49/22 (2013.01); C10B 53/02 (2013.01); C10B 57/06 (2013.01); C10G 1/08 (2013.01); C10G 3/57 (2013.01); C10G 11/18 (2013.01); C10L 1/02 (2013.01); C10G 2300/104 (2013.01); C10G 2300/1014 (2013.01); C10G 2300/1044 (2013.01); C10G 2300/1051 (2013.01); C10G 2300/1055 (2013.01); C10G 2300/4075 (2013.01); C10G 2300/807 (2013.01); Y02E 50/14 (2013.01);
Abstract

A process for converting a solid biomass material by contacting the solid biomass material with a catalytic cracking catalyst at a temperature of more than 400° C. in a riser reactor to produce one or more cracked products is provided, wherein the riser reactor is an internal riser reactor.


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