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. 24, 2020

Filed:

Nov. 02, 2017
Applicant:

Shell Oil Company, Houston, TX (US);

Inventors:

Gerrit Leendert Bezemer, Amsterdam, NL;

Hans Michiel Huisman, Amsterdam, NL;

Tyrone James McKnight, Amsterdam, NL;

Wilhelmus Johannes Franciscus Scholten, Amsterdam, NL;

Wenping Yang, Amsterdam, NL;

Assignee:

SHELL OIL COMPANY, Houston, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 2/00 (2006.01); C01B 3/36 (2006.01); C01B 3/38 (2006.01); C10G 11/00 (2006.01); C10J 3/72 (2006.01); C10G 47/00 (2006.01);
U.S. Cl.
CPC ...
C10G 2/331 (2013.01); C01B 3/36 (2013.01); C01B 3/38 (2013.01); C10G 11/00 (2013.01); C10G 47/00 (2013.01); C10J 3/72 (2013.01); C01B 2203/0233 (2013.01); C01B 2203/0244 (2013.01); C01B 2203/0255 (2013.01); C01B 2203/049 (2013.01); C01B 2203/0465 (2013.01); C01B 2203/0485 (2013.01); C01B 2203/062 (2013.01); C10G 2300/1011 (2013.01); C10G 2300/1022 (2013.01); C10G 2300/1025 (2013.01); C10G 2300/4018 (2013.01); C10J 2300/1659 (2013.01); Y02P 30/20 (2015.11);
Abstract

A method of producing normally solid, normally liquid and optionally normally gaseous hydrocarbons involves contacting a gas mixture comprising hydrogen and carbon monoxide with a catalyst under elevated temperature and pressure, to convert at least part of the hydrogen and carbon monoxide into hydrocarbons. An effluent is withdrawn from the reactor and subjected to a separation step to form at least a heavy fraction and a light fraction. The heavy fraction comprises normally solid hydrocarbons, while the light fraction comprises unconverted syngas and normally liquid and optionally normally gaseous hydrocarbons. The light fraction is sent to a light ends stripper operating at a temperature of maximally 200° C. to obtain a hydrocarbons fraction comprising normally liquid hydrocarbons. The heavy fraction is subjected to flash evaporation or steam stripping to obtain a hydrocarbon stream of normally solid hydrocarbons (comprising mainly C10+ hydrocarbons).


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