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:
Nov. 14, 2017

Filed:

Jul. 28, 2015
Applicant:

Fluor Technologies Corporation, Aliso Viejo, CA (US);

Inventors:

Ravi Ravikumar, Lancaster, CA (US);

Paul E. Koppel, Hollywood, FL (US);

Sanjiv Dabee, Aliso Viejo, CA (US);

Johnathon Zychowicz, Tustin, CA (US);

Assignee:

Fluor Technologies Corporation, Sugar Land, TX (US);

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 2/00 (2006.01); C01B 3/34 (2006.01); C10L 10/12 (2006.01); C10G 47/00 (2006.01); C10K 1/00 (2006.01); C10K 3/04 (2006.01); C01B 3/38 (2006.01); C01B 3/48 (2006.01); C10L 1/04 (2006.01);
U.S. Cl.
CPC ...
C01B 3/34 (2013.01); C01B 3/38 (2013.01); C01B 3/48 (2013.01); C10G 2/32 (2013.01); C10G 47/00 (2013.01); C10K 1/005 (2013.01); C10K 3/04 (2013.01); C10L 1/04 (2013.01); C10L 10/12 (2013.01); C01B 2203/0216 (2013.01); C01B 2203/0233 (2013.01); C01B 2203/0283 (2013.01); C01B 2203/043 (2013.01); C01B 2203/0475 (2013.01); C01B 2203/062 (2013.01); C01B 2203/063 (2013.01); C10G 2300/1022 (2013.01); C10G 2400/02 (2013.01); C10G 2400/04 (2013.01); C10G 2400/08 (2013.01); C10L 2270/026 (2013.01); C10L 2270/04 (2013.01); C10L 2290/148 (2013.01); C10L 2290/42 (2013.01); C10L 2290/541 (2013.01); C10L 2290/542 (2013.01); C10L 2290/543 (2013.01);
Abstract

A crude oil processing plant that comprises a Fischer-Tropsch reactor is disclosed. The crude oil processing plant comprises a crude oil processing section and a hydrogen production section. The hydrogen production section is coupled to a hydrocracker in the crude oil processing section to deliver a high purity hydrogen stream. The Fischer-Tropsch reactor receives a syngas stream from the hydrogen production section and produces a hydrocarbon stream. When light crude oil is processed, the hydrocracker typically has excess capacities to upgrade the hydrocarbon stream from the Fischer-Tropsch reactor.


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