Saudi Arabian Oil Company

King Abdullah University of Science and Technology

Jgc Catalysts & Chemicals Ltd.

Japan Cooperation Center Petroleum

Saudi Arabian Oil Componv

Bandar Hussain Alsolami

Bandar A Fadhel

Rami A Bamagain

Mohammed A Albuali

Ki-Hyouk Choi

Emad Naji Al-Shafei

Mohammad A Alabdullah

Ali Alsomali

Bandar K Alotaibi

Massad S Alanzi

Omer Refa Koseoglu

Aqil Jamal

Masaru Ushio

Jorge Gascon

Seiji Arakawa

Adrian Ramirez

Genrikh Shterk

Artem Russkikh

Ali M Alsomali

Modified red mud catalyst compositions, methods for production, and methods of use in dry reforming, the composition comprising: red mud material produced from an alumina extraction process from bauxite ore; and nickel oxide, the nickel oxide present at between about 5 wt. % to about 40 wt. % of the modified red mud catalyst composition.

Nickel-containing catalyst composition having enhanced acidity for dry reforming processes

Modified red mud catalyst compositions, methods for production, and methods for use, a composition including red mud material produced from an alumina extraction process from bauxite ore; nickel oxide, the nickel oxide present at between about 5 wt. % to about 40 wt. % of the modified red mud catalyst composition; and a Periodic Table Group VIB metal oxide, the Group VIB metal oxide present at between about 1 wt. % and about 30 wt. % of the modified red mud catalyst composition.

Catalyst compositions having enhanced acidity for dry reforming processes

A method and catalyst for forming higher carbon number products from carbon dioxide is provided. An exemplary catalyst includes red mud including iron and aluminum, and impregnated potassium.

Potassium-promoted red mud as a catalyst for forming hydrocarbons from carbon dioxide

Modified red mud catalyst compositions, methods for production, and methods of use in bi-reforming, the composition comprising: red mud material produced from an alumina extraction process from bauxite ore; and nickel oxide, the nickel oxide present at between about 5 wt. % to about 40 wt. % of the modified red mud catalyst composition.

Nickel-containing catalyst composition having enhanced acidity for bi-reforming processes

Modified red mud catalyst compositions, methods for production, and methods of use in steam reforming, the composition comprising: red mud material produced from an alumina extraction process from bauxite ore; and nickel oxide, the nickel oxide present at between about 5 wt. % to about 40 wt. % of the modified red mud catalyst composition.

Nickel-containing catalyst composition having enhanced acidity for steam reforming processes

Methods for autothermal reforming over a modified red mud catalyst composition, one method including providing a methane feed with oxygen and carbon dioxide to react over the modified red mud catalyst composition at increased temperature and increased pressure to produce synthesis gas comprising Hand CO, the composition comprising red mud material produced from an alumina extraction process from bauxite ore; nickel oxide, the nickel oxide present at between about 5 wt. % to about 40 wt. % of the modified red mud catalyst composition; and a Periodic Table Group VIB metal oxide, the Group VIB metal oxide present at between about 1 wt. % and about 30 wt. % of the modified red mud catalyst composition.

Catalyst compositions having enhanced acidity for autothermal reforming processes

Modified red mud catalyst compositions, methods for production, and methods of use in autothermal reforming, the composition comprising: red mud material produced from an alumina extraction process from bauxite ore; and nickel oxide, the nickel oxide present at between about 5 wt. % to about 40 wt. % of the modified red mud catalyst composition.

Nickel-containing catalyst composition having enhanced acidity for autothermal reforming processes

A system and method for converting (dry reforming) natural gas (methane) and carbon dioxide via reformer catalyst in a dry reformer into syngas including carbon monoxide and hydrogen, and discharging the syngas to a Fischer-Tropsch (FT) reactor. Supplemental hydrogen is generated via water electrolysis and added to the syngas in route to the FT reactor to increase the molar ratio of hydrogen to carbon monoxide in the syngas. The syngas may be converted via FT catalyst in the FT reactor into FT waxes.

Base oil production via dry reforming

Methods for bi-reforming with a red mud catalyst support composition, one method including providing a methane feed in the presence of carbon dioxide and steam to react over the red mud catalyst support composition at increased temperature and increased pressure to produce synthesis gas comprising Hand CO, the composition comprising red mud material produced from an alumina extraction process from bauxite ore.

Catalyst carrier for bi-reforming processes

Methods for autothermal reforming with a red mud catalyst support composition, one method including providing a methane feed with oxygen and carbon dioxide to react over the red mud catalyst support composition at increased temperature and increased pressure to produce synthesis gas comprising Hand CO, the composition comprising red mud material produced from an alumina extraction process from bauxite ore.

Catalyst carrier for autothermal reforming processes

Methods for steam reforming with a red mud catalyst support composition, one method including providing a methane feed and a steam feed to react over the red mud catalyst support composition at increased temperature and increased pressure to produce synthesis gas comprising Hand CO, the composition comprising red mud material produced from an alumina extraction process from bauxite ore.

Catalyst carrier for steam reforming processes

Methods for steam reforming over a modified red mud catalyst composition, one method including providing a methane feed and a steam feed to react over the modified red mud catalyst composition at increased temperature and increased pressure to produce synthesis gas comprising Hand CO, the composition comprising red mud material produced from an alumina extraction process from bauxite ore; nickel oxide, the nickel oxide present at between about 5 wt. % to about 40 wt. % of the modified red mud catalyst composition; and a Periodic Table Group VIB metal oxide, the Group VIB metal oxide present at between about 1 wt. % and about 30 wt. % of the modified red mud catalyst composition.

Catalyst compositions having enhanced acidity for steam reforming processes

Methods for dry reforming with a red mud catalyst support composition, one method including providing a methane feed and carbon dioxide feed to react over the red mud catalyst support composition at increased temperature and increased pressure to produce synthesis gas comprising Hand CO, the composition comprising red mud material produced from an alumina extraction process from bauxite ore.

Catalyst carrier for dry reforming processes

Methods for bi-reforming over a modified red mud catalyst composition, one method including providing a methane feed in the presence of carbon dioxide and steam to react over the modified red mud catalyst composition at increased temperature and increased pressure to produce synthesis gas comprising Hand CO, the composition comprising red mud material produced from an alumina extraction process from bauxite ore; nickel oxide, the nickel oxide present at between about 5 wt. % to about 40 wt. % of the modified red mud catalyst composition; and a Periodic Table Group VIB metal oxide, the Group VIB metal oxide present at between about 1 wt. % and about 30 wt. % of the modified red mud catalyst composition.

Catalyst compositions having enhanced acidity for bi-reforming processes

The present invention relates to a catalyst for fluidized catalytic cracking of hydrocarbon oil containing a framework-substituted zeolite-1 in which zirconium atoms and/or hafnium atoms form a part of a framework of an ultra-stable Y-type zeolite.

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Dhahran, Saudi Arabia

Bandar Hussain Alsolami