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. 23, 2016

Filed:

Mar. 13, 2013
Applicant:

Steve Kresnyak, Calgary, CA;

Inventor:

Steve Kresnyak, Calgary, CA;

Assignee:

Expander Energy Inc., Calgary, CA (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 9/00 (2006.01); C10G 45/02 (2006.01); C10G 45/58 (2006.01); C01B 3/34 (2006.01); C01B 3/48 (2006.01); C10G 47/00 (2006.01); C10K 1/08 (2006.01); C10K 1/32 (2006.01); C10K 3/04 (2006.01); C10K 3/06 (2006.01); C10G 1/04 (2006.01); C10G 2/00 (2006.01);
U.S. Cl.
CPC ...
C01B 3/34 (2013.01); C01B 3/48 (2013.01); C10G 1/045 (2013.01); C10G 2/32 (2013.01); C10G 9/00 (2013.01); C10G 9/007 (2013.01); C10G 45/02 (2013.01); C10G 45/58 (2013.01); C10G 47/00 (2013.01); C10K 1/08 (2013.01); C10K 1/32 (2013.01); C10K 3/04 (2013.01); C10K 3/06 (2013.01); C01B 2203/025 (2013.01); C01B 2203/0233 (2013.01); C01B 2203/0244 (2013.01); C01B 2203/043 (2013.01); C01B 2203/0405 (2013.01); C01B 2203/0485 (2013.01); C01B 2203/062 (2013.01); C01B 2203/063 (2013.01); C01B 2203/107 (2013.01); C01B 2203/1052 (2013.01); C01B 2203/1058 (2013.01); C01B 2203/1064 (2013.01); C10G 2300/203 (2013.01); C10G 2300/302 (2013.01); C10G 2300/308 (2013.01); C10G 2400/02 (2013.01); C10G 2400/04 (2013.01);
Abstract

A bitumen and heavy oil upgrading process and system is disclosed for the synthesis of hydrocarbons, an example of which is synthetic crude oil (SCO). The process integrates Fischer-Tropsch technology with gasification and hydrogen rich gas stream generation. The hydrogen rich gas generation is conveniently effected using singly or in combination a hydrogen source, a hydrogen rich vapor from hydroprocessing and the Fischer-Tropsch process, a steam methane reformer (SMR) and autothermal reformer (ATR) or a combination of SMR/ATR. The feedstock for upgrading is distilled and the bottoms fraction is gasified and converted in a Fischer-Tropsch reactor. A resultant hydrogen lean syngas is then exposed to the hydrogen rich gas stream to optimize the formation of, for example, the synthetic crude oil. Partial upgrading and the commensurate benefits is detailed as well. A system for effecting the processes is also characterized in the specification.


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