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:
Mar. 07, 2017

Filed:

Dec. 17, 2012
Applicant:

Shell Oil Company, Houston, TX (US);

Inventors:
Assignee:

SHELL OIL COMPANY, Houston, TX (US);

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 55/02 (2006.01); C10G 45/02 (2006.01); C10G 47/00 (2006.01); C10G 65/14 (2006.01); C10G 2/00 (2006.01); C10L 1/04 (2006.01);
U.S. Cl.
CPC ...
C10G 55/02 (2013.01); C10G 2/332 (2013.01); C10G 45/02 (2013.01); C10G 47/00 (2013.01); C10G 65/14 (2013.01); C10L 1/04 (2013.01); C10G 2300/1025 (2013.01); C10G 2400/04 (2013.01); C10G 2400/06 (2013.01); C10G 2400/08 (2013.01);
Abstract

A process for production of middle distillate fraction from gas-to-liquid (GTL) conversion comprising providing a feed stream comprising natural gas and separating a condensate from the feed stream to produce a condensate stream and a feed stream; processing the feed stream via a Fischer-Tropsch (FT) reaction to generate a long chain hydrocarbon product stream; processing the product stream via a heavy paraffinic conversion in order to produce a FT product stream; treating the condensate stream with a desulfurization step to generate a condensate product stream; combining the FT product stream with the condensate product stream to provide a distillate feed stream; and performing a distillation step on the distillation feed stream, wherein the processing steps occur substantially concurrently with the treating step and wherein distillation provides for isolation of middle distillate products. Middle distillate fractions and fuel oils/fuel oil blends obtained according to the process are also provided.


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