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:
Aug. 18, 2020

Filed:

Oct. 27, 2017
Applicant:

Shell Oil Company, Houston, TX (US);

Inventors:

Ronald Jan Dogterom, Amsterdam, NL;

Gerard Pieter Van Der Laan, Amsterdam, NL;

Abderrahmane Chettouf, Amsterdam, NL;

Assignee:

SHELL OIL COMPANY, Houston, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 2/00 (2006.01); B01J 8/02 (2006.01); B01J 8/06 (2006.01); B01J 35/04 (2006.01); B01J 37/02 (2006.01); B01J 37/08 (2006.01);
U.S. Cl.
CPC ...
C10G 2/341 (2013.01); B01J 8/0292 (2013.01); B01J 8/065 (2013.01); B01J 35/04 (2013.01); B01J 37/0201 (2013.01); B01J 37/0225 (2013.01); B01J 37/0236 (2013.01); B01J 37/08 (2013.01); C10G 2/30 (2013.01); C10G 2/344 (2013.01); B01J 2208/024 (2013.01); B01J 2208/06 (2013.01); C10G 2300/1022 (2013.01);
Abstract

The present application relates to a process for producing normally gaseous, normally liquid, and optionally normally solid hydrocarbons from synthesis gas in a three-phase reactor, said reactor comprising a top middle and bottom part wherein the bottom and top part are fluidly connected via one or more reactor tubes, wherein one or more reactor tubes comprise randomly stacked catalyst bodies held stationary in the reactor tube and the reactor is at least partially filled with a liquid medium, said process comprising the steps of: (i) introducing the synthesis gas into the reactor via the bottom part; and (ii) contacting the synthesis gas with a stationary catalyst to catalytically convert the synthesis gas at an elevated temperature to obtain the normally gaseous, normally liquid, and optionally normally solid hydrocarbons from synthesis gas; (iii) withdrawing the normally gaseous, normally liquid, and optionally normally solid hydrocarbons; wherein the catalyst bodies have an open celled foam structure.


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