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:
Jul. 15, 2025

Filed:

Apr. 21, 2021
Applicant:

Exxonmobil Technology and Engineering Company, Annandale, NJ (US);

Inventors:

Ramesh Gupta, Berkeley Heights, NJ (US);

Hugo S. Caram, Allentown, PA (US);

Anjaneya S. Kovvali, Herndon, VA (US);

Sumathy Raman, Annandale, NJ (US);

David C. Dankworth, Princeton, NJ (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C01B 3/30 (2006.01); B01J 8/00 (2006.01); B01J 8/18 (2006.01); B01J 8/24 (2006.01);
U.S. Cl.
CPC ...
C01B 3/30 (2013.01); B01J 8/003 (2013.01); B01J 8/0055 (2013.01); B01J 8/1827 (2013.01); B01J 8/1881 (2013.01); B01J 8/24 (2013.01); B01J 2208/00176 (2013.01); B01J 2208/00327 (2013.01); B01J 2208/00991 (2013.01); C01B 2203/0272 (2013.01); C01B 2203/0805 (2013.01); C01B 2203/0872 (2013.01); C01B 2203/1241 (2013.01);
Abstract

Systems and methods are provided for conversion of methane and/or other hydrocarbons to hydrogen by pyrolysis while reducing or minimizing production of carbon oxides. The conversion of hydrocarbons to hydrogen is performed in one or more pyrolysis or conversion reactors that contain a plurality of sequential fluidized beds. The fluidized beds are arranged so that the coke particles forming the fluidized bed move in a counter-current direction relative to the gas phase flow of feed (e.g., methane) and/or product (H) in the fluidized beds. By using a plurality of sequential fluidized beds, the heat transfer and management benefits of fluidized beds can be realized while also at least partially achieving the improved reaction rates that are associated with a plug flow or moving bed reactor.


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