Air Products and Chemicals, Inc.

Shell Usa, Inc.

Shell Oil Comapny

Shell Internationale Research Maatschappij, B.v.

Robert Schouwenaar

Jose Atilio Quevedo Enriquez

Johannes Hermanus Maria Disselhorst

Mark Klokkenburg

Sayee Prasaad Balaji

Jacobus Eilers

Joachim Ottomar Wolff

Johannes Cornelis De Jong

Chengming Gao

Dominik Johannes Michael Unruh

Sven Felske

The present invention relates to a process for converting carbon dioxide and hydrogen by performing a reverse water gas shift reaction at elevated temperature, the process comprising introducing carbon dioxide, hydrogen and oxygen into a reaction vessel having an inlet and an outlet, and, wherein the reverse water gas shift reaction takes place in two different zones of the reaction vessel, being a top zone (z1) adjacent to a bottom zone (z2). The process produces a product stream comprising mainly carbon monoxide, hydrogen and water. The process is useful in reducing the carbon footprint of certain industrial technologies, and in addition, the process is useful in the production of synthesis gas.

Process and reactor for converting carbon dioxide into carbon monoxide, involving a catalyst

A process for converting carbon dioxide and hydrogen into a product stream comprising carbon monoxide, water and hydrogen by introducing carbon dioxide, hydrogen and oxygen into a reaction vessel, and performing a reverse water gas shift reaction at elevated temperature, wherein It is useful in reducing the carbon footprint of certain industrial technologies, and in production of synthesis gas.

Process and reactor for converting carbon dioxide into carbon monoxide

A process for the production of synthesis gas by partial combustion of a hydrocarbon feed using a burner with a plurality of coaxial channels, the method comprising the following steps: supplying a non-gaseous hydrocarbon feed using at least one of the plurality of coaxial channels; supplying a gaseous hydrocarbon feed using at least one of the plurality of coaxial channels; supplying an oxidizer gas using at least one of the plurality of coaxial channels; separately supplying a moderator gas using at least one of the plurality of coaxial channels; arranging the at least one channel supplying the non-gaseous hydrocarbon feed between two adjacent channels among the plurality of coaxial channels, wherein the two adjacent channels both supplying a flow containing the gaseous hydrocarbon feed or respectively supplying a flow containing the gaseous hydrocarbon feed and a flow of the moderator gas.

Production of synthesis gas

Process, reactor and burner for the gasification of a hydrocarbon fuel. The burner comprises coaxial channels for the separate supply of an oxidizer gas, a hydrocarbon fuel and a moderator gas. A coaxial channel with the smallest width is bordered by a separating wall with at least one gas exchange. The gas exchange passage can for example be formed by a retracted end of the separating wall and/or by openings in the separating wall.

Burner, reactor and process for gasification of a hydrocarbon feed

The invention provides a process to prepare a Fischer-Tropsch synthesis product from a gaseous mixture of hydrocarbons comprising methane, ethane and optional higher carbon number hydrocarbons comprising the steps of:

Process to prepare a Fischer-Tropsch synthesis product

Growing community of inventors

Amsterdam, Netherlands

Robert Schouwenaar