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:
May. 05, 2026

Filed:

Sep. 17, 2021
Applicant:

Johnson Matthey Davy Technologies Limited, London, GB;

Inventors:

Henry Arthur Claxton, London, GB;

Andrew James Coe, London, GB;

Mark Joseph Mckenna, Billingham, GB;

Paul Robert Ticehurst, London, GB;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 2/00 (2006.01); C01B 3/16 (2006.01); C01B 3/34 (2006.01); C10G 3/00 (2006.01); C10G 49/00 (2006.01); C10J 3/00 (2006.01); C10K 1/00 (2006.01); C10K 1/08 (2006.01); C10K 3/02 (2006.01); C25B 1/04 (2021.01); C25B 15/08 (2006.01);
U.S. Cl.
CPC ...
C10G 2/32 (2013.01); C01B 3/16 (2013.01); C01B 3/34 (2013.01); C10G 3/50 (2013.01); C10G 49/007 (2013.01); C10J 3/00 (2013.01); C10K 1/005 (2013.01); C10K 1/08 (2013.01); C10K 3/026 (2013.01); C25B 1/04 (2013.01); C25B 15/081 (2021.01); C01B 2203/0415 (2013.01); C01B 2203/062 (2013.01); C10G 2300/1022 (2013.01); C10G 2300/4043 (2013.01); C10G 2300/4081 (2013.01); C10J 2300/0913 (2013.01); C10J 2300/0959 (2013.01); C10J 2300/1659 (2013.01); C10J 2300/1684 (2013.01);
Abstract

A process for synthesising hydrocarbons is described comprising the steps of (a) making a synthesis gas comprising hydrogen, carbon monoxide and carbon dioxide from a feedstock in a synthesis gas generation unit, (b) removing carbon dioxide to produce a carbon dioxide stream and purified synthesis gas comprising hydrogen and carbon monoxide for synthesis in a Fischer-Tropsch hydrocarbon synthesis unit wherein (i) at least a portion of the FT water stream is fed to an electrolysis unit to provide an oxygen stream, which is fed to the synthesis gas generation unit. Carbon dioxide stream recovered from the carbon dioxide removal unit and a portion of the hydrogen stream produced by the electrolysis unit are fed to a reverse water-gas shift unit to produce a carbon monoxide stream, with carbon monoxide stream from the reverse water-gas shift unit is fed to the Fischer-Tropsch hydrocarbon synthesis unit.


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