Haldor Topse A/s

Grundfos Holding A/s

Topsoe A/s

Kasper Emil Larsen

Peter Mølgaard Mortensen

Kim Aasberg-Petersen

Robert Klein

Sebastian Thor Wismann

Per Juul Dahl

Flemming Buus Bendixen

Alexandru Sorea

Peter Valler

Henrik Rasmussen

Michael Hultqvist

Allan Ivo Søgaard

Anders Helbo Hansen

Peter Molgaard Mortensen

A heating system and a process for heating a pressurized feed gas is provided, where the heat for the reaction is provided by resistance heating by means of electrical power.

Gas heater

Array including a first and a second monolith of a structured catalyst for carrying out an endothermic reaction of a feed gas, wherein: a) the first and second monolith include a macroscopic structure of a first and second electrically conductive material; b) each of said first and second monoliths has a number of flow channels formed therein for conveying feed gas through the monoliths; c) the array includes at least a first and a second conductor electrically connected to said first and second monoliths, respectively, and to an electrical power supply, d) the first and second monolith are electrically connected by a monolith bridge; e) the array is configured to direct an electrical current to run from the first conductor through the first monolith to a second end, then through the bridge, and then through the second monolith to the second conductor.

Endothermic reaction of a feed gas heated by resistance heating

A method is provided for rapidly switching a metal-catalysed steam methane reforming reaction of a feed gas from a first steady-state reaction condition (A) to a second steady-state reaction condition (B) or vice-versa. After applying a given voltage and/or feed gas flow, the system can work towards a thermal equilibration to reach steady state without any additional operator input.

Synthesis gas on demand

A structured catalyst for catalyzing an endothermic reaction of a feed gas to convert it to a product gas is provided.

Structured catalyst

A reactor system and a process for carrying out the reaction of a feed gas comprising an alkane such as methane, and ammonia to hydrogen cyanide and/or a nitrile are provided, where the heat for the endothermic reaction is provided by resistance heating. In particular, the reaction is the BMA (Blausäure aus Methan und Ammoniak) reaction.

Cyanide on demand

An offshore installation or offshore vessel is provided which comprises a reactor system for carrying out steam reforming of a feed gas comprising hydrocarbons.

Offshore reforming installation or vessel

A reactor system and a process for carrying out the methanol cracking reaction of a feedstock comprising methanol to hydrogen are provided, where the heat for the endothermic methanol cracking reaction is provided by resistance heating.

On demand hydrogen from methanol

A reactor system and a process for carrying out the methanol cracking and reverse water gas shift reaction of a feedstock comprising methanol to synthesis gas are provided, where the heat for the endothermic methanol cracking and reverse water gas shift reaction is provided by resistance heating.

On demand synthesis gas from methanol

A reactor system and a process for carrying out the ammonia cracking reaction of a feed gas comprising ammonia to hydrogen are provided, where the heat for the endothermic ammonia cracking reaction is provided by resistance heating.

On demand hydrogen from ammonia

A reactor system and a process for carrying out reverse water gas shift reaction of a feedstock comprising COand Hto a first product gas comprising CO are provided, where a methanation reaction take place in parallel to the reverse water gas shift reaction, and where the heat for the endothermic reverse water gas shift reaction is provided by resistance heating.

Growing community of inventors

Humlebæk, Denmark

Kasper Emil Larsen