Haldor Topsoe A/s

Haldor Topse A/s

Christophe Duwig

Pär L Gabrielsson

Poul Erik Højlund Nielsen

Per Juul Dahl

Max Thorhauge

Ton V W Janssens

Jesper Norsk

Svend-Erik Mikkelsen

Marcus Almqvist

Ton Vw Janssens

Ton VW Janssens

Process and reaction system for the preparation of methanol comprising two reaction units, wherein a first unit is operated on a mixture of fresh synthesis gas and unconverted synthesis gas and a second unit solely with unconverted synthesis gas.

Process and reaction system for the preparation of methanol

Method of operating a compression ignition engine on ether containing fuel obtained by on board conversion of an alcohol containing primary fuel and a system for use in the method. The ether containing fuel is prepared by dehydration of liquid alcohol containing fuel in present of a dehydration catalyst arranged in a radial flow reactor within a fuel accumulation chamber in a common rail.

Method and system for operating a compression ignition engine on alcohol containing fuels

Method of operating a compression ignition engine on ether containing fuel obtained by on board conversion of an alcohol containing primary fuel, and a system for use in the method. The alcohol containing primary fuel is heated within a dehydration reactor by indirect heat exchange with ether containing fuel prepared in the dehydration reactor by dehydrating the alcohol containing primary fuel. The ether containing fuel is cooled prior to withdrawal from the reactor as a result of the indirect heat exchange with the alcohol containing primary fuel.

Method and system for operating a compression ignition engine on alcohol containing primary fuels

Method and reactor for performing Fischer-Tropsch (FT) synthesis with controlled steam partial pressure by introducing cool points in the FT reactor, typically in form of cooled solid surfaces. At the surface, the low temperature will force condensation of the water into a liquid film. Thereby, the partial pressure of steam in the gas and reactor will not exceed significantly the vapor partial pressure at the liquid film and water from the gas stream will be removed as it is produced, i.e. steam induced deactivation is avoided. In addition, the decrease of hydrogen and carbon monoxide partial pressures due to dilution by steam will be kept low ensuring a constant high reaction rate.

Method and reactor for performing fischer-tropsch synthesis

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Malmö, Sweden

Christophe Duwig