Infinium Technology, LLC

Anja Rumplecker Galloway

Robert Schuetzle

Dennis Schuetzle

James Bucher

Orion Hanbury

Glenn McGinnis

Matthew Caldwell

Alex Mattana

Ramer Rodriguez

Harold A Wright

Glenn Mcginnis

A process for the production of sustainable aviation fuel (SAF) with low carbon intensity. The jet fuel is produced from the reaction of hydrogen from the electrolysis of water with captured carbon dioxide. The hydrogen and carbon dioxide are reacted to product a stream comprising carbon monoxide. Hydrogen and carbon monoxide are reacted to produce n-alkanes. Alkanes are hydroisomerized to produce sustainable aviation fuel with low carbon intensity.

Production of sustainable aviation fuel from COand low-carbon hydrogen

The present invention is generally directed to a reactor for the production of low-carbon syngas from captured carbon dioxide and renewable hydrogen. The hydrogen is generated from water using an electrolyzer powered by renewable electricity or from any other method of low-carbon hydrogen production. The improved catalytic reactor is energy efficient and robust when operating at temperatures up to 1800° F. Carbon dioxide conversion efficiencies are greater than 75% with carbon monoxide selectivity of greater than 98%. The catalytic reactor is constructed of materials that are physically and chemically robust up to 1800° F. As a result, these materials are not reactive with the mixture of hydrogen and carbon dioxide or the carbon monoxide and steam products.

Catalytic reactor for the conversion of carbon dioxide and hydrogen to syngas

Provided herein are systems and methods for controlling production of low-carbon liquid fuels and chemicals. In an aspect, provided herein is a method controlling a process that produces e-fuels. In another aspect, provided herein is a system for producing an e-fuel.

Systems and methods for controlling a Power-to-X process to reduce feedstock costs

Production of fuels from low carbon electricity and from carbon dioxide by the use of a solid oxide electrolysis cell (SOEC) and Fischer-Tropsch is shown. Fischer-Tropsch is an exothermic reaction that can be used to produce steam. Steam produced from the Liquid Fuel Production (LFP) reactor system, where the Fischer-Tropsch reaction occurs, is used as feed to the SOEC. The higher temperature steam improves the efficiency of the overall electrolysis system. The integration of the LFP steam improves the efficiency of the electrolysis because the heat of vaporization for the liquid water does not have to be supplied by the electrolyzer.

Thermally integrated process for the production of liquid fuels with a solid oxide electrolyzer

The present invention is generally directed to processes and systems for the purification and conversion of COinto low-carbon or zero-carbon high quality fuels and chemicals using renewable energy. In one aspect, the present invention provides a process for producing a stream comprising at least 90 mol % CO. In certain cases, the COstream is processed to make low carbon fuels and chemicals. In this process at least a portion of the COis reacted with a stream comprising Hin a Reverse Water Gas Shift (RWGS) reactor to produce a product stream that comprises CO.

Process for purification and conversion of carbon dioxide using renewable energy

The present invention is generally directed to a reactor for the production of low-carbon syngas from captured carbon dioxide and renewable hydrogen. The hydrogen is generated from water using an electrolyzer powered by renewable electricity or from any other method of low-carbon hydrogen production. The improved catalytic reactor is energy efficient and robust when operating at temperatures up toF. Carbon dioxide conversion efficiencies are greater than% with carbon monoxide selectivity of greater than%. The catalytic reactor is constructed of materials that are physically and chemically robust up toF. As a result, these materials are not reactive with the mixture of hydrogen and carbon dioxide or the carbon monoxide and steam products. The reactor materials do not have catalytic activity or modify the physical and chemical composition of the conversion catalyst.

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San Rafael, CA, United States of America

Anja Rumplecker Galloway