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:
Jun. 05, 2018

Filed:

May. 13, 2015
Applicant:

Ccp Technology Gmbh, München, DE;

Inventor:

Olaf Kuhl, Greifswald, DE;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C01B 3/24 (2006.01); C10G 2/00 (2006.01); C10K 3/04 (2006.01); C01B 3/12 (2006.01);
U.S. Cl.
CPC ...
C01B 3/24 (2013.01); C01B 3/12 (2013.01); C10G 2/30 (2013.01); C10G 2/32 (2013.01); C10G 2/34 (2013.01); C10K 3/04 (2013.01); C01B 2203/0272 (2013.01); C01B 2203/0283 (2013.01); C01B 2203/0288 (2013.01); C01B 2203/049 (2013.01); C01B 2203/061 (2013.01); C01B 2203/062 (2013.01); C01B 2203/0805 (2013.01); C01B 2203/0844 (2013.01); C01B 2203/0861 (2013.01); C01B 2203/0883 (2013.01); C01B 2203/1276 (2013.01); C01B 2203/141 (2013.01); C01B 2203/145 (2013.01); C10J 2300/1618 (2013.01); C10J 2300/1853 (2013.01); Y02P 20/129 (2015.11);
Abstract

A method for producing ¾-rich synthesis gas comprises the following steps: decomposing a hydrocarbon-containing fluid into an H/C-aerosol in a first hydrocarbon converter by supplying energy which is at least partly provided in the form of heat; introducing at least a first stream of the H/C-aerosol into a first sub-process which comprises the following steps: directing at least a part of the H/C-aerosol from the first hydrocarbon converter into a first C-converter; introducing COinto the first C-converter and mixing the COwith the H/C-aerosol introduced into the first C-converter; converting the mixture of H/C-aerosol and COinto a synthesis gas at a temperature of 800 to 1700° C.; mixing additional Hwith the synthesis gas for the production of H-rich synthesis gas. In a second sub-process running in parallel with the first sub-process, hydrogen Hand carbon dioxide COare produced from a hydrocarbon-containing fluid, wherein at least a portion of the COproduced in the second sub-process is introduced into the first C-converter; and wherein at least a portion of the Hproduced in the second sub-process is mixed with the synthesis gas from the first C-converter. The COwhich is needed for the conversion of C in the first C-converter can thereby be provided independently of an external source, and the entire operational sequence is easily controllable.


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