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. 07, 2017

Filed:

Jun. 28, 2012
Applicants:

Pedro Pereira Almao, Calgary, CA;

Gustavo Luis Trujillo, Calgary, CA;

Enzo Peluso, Calgary, CA;

Carmen Galarraga, Calgary, CA;

Clementina Sosa, Calgary, CA;

Carlos Scott Algara, Calgary, CA;

Francisco Lopez-linares, Calgary, CA;

Lante Antonio Carbognani Ortega, Calgary, CA;

Nestor Gregorio Zerpa Reques, Calgary, CA;

Inventors:

Pedro Pereira Almao, Calgary, CA;

Gustavo Luis Trujillo, Calgary, CA;

Enzo Peluso, Calgary, CA;

Carmen Galarraga, Calgary, CA;

Clementina Sosa, Calgary, CA;

Carlos Scott Algara, Calgary, CA;

Francisco Lopez-Linares, Calgary, CA;

Lante Antonio Carbognani Ortega, Calgary, CA;

Nestor Gregorio Zerpa Reques, Calgary, CA;

Assignee:

NEXEN ENERGY ULC, Calgary, Alberta, CA;

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 55/04 (2006.01); C10L 1/08 (2006.01); C10G 9/36 (2006.01); C10G 21/00 (2006.01);
U.S. Cl.
CPC ...
C10G 55/04 (2013.01); C10G 9/36 (2013.01); C10G 21/003 (2013.01); C10L 1/08 (2013.01); C10G 2300/1059 (2013.01); C10G 2300/1077 (2013.01); C10G 2300/206 (2013.01); C10G 2300/301 (2013.01); C10G 2300/302 (2013.01); C10G 2300/308 (2013.01);
Abstract

This invention relates to systems and methods for catalytic steam cracking of non-asphaltene containing heavy hydrocarbon fractions. The method enables upgrading heavy hydrocarbons to hydrocarbons capable of being transported through pipelines and/or a pretreated step before further treatment in an upgrading refinery, including the steps of separating the heavy hydrocarbon mixture into a light fraction, a full gasoil fraction and a vacuum residue fraction with or without at least partial reduction or asphaltenes; adding a catalyst to the full gasoil and/or to the blend of this with a reduced asphaltenes fraction and subjecting the catalyst-full gasoil and/or deasphalted oil fraction to catalytic steam cracking to form an effluent stream; separating the effluent stream into a gas stream and a liquid stream; and mixing the liquid stream with the light fraction and the vacuum residue fraction to form an upgraded oil. The system includes hardware capable of performing the method.


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