Institut Francais Du Pe'trole

Enitecnologie S.p.a.

Other

Agip Petroli

Agip S.p.a.

Ifp Energies Nouvelles

Cristina Maretto

Pierre Galtier

Vincenzo Piccolo

Giovanni Pederzani

Francois Hugues

Jean-Marc Schweitzer

Dominique Casanave

Gilles Ferschneider

Jean-Christophe Viguie

Process for the running of a reactor in which reactions take place in multiphase systems, wherein a gaseous phase prevalently consisting of CO and His bubbled into a suspension of a solid in the form of particles (catalyst) in a liquid (prevalently reaction product), according to the Fischer-Tropsch technology.

Process for the running of a reactor suitable for heterogeneous reactions combined with reactions taking place in three-phase system

Process for the charging of a catalyst and for the running of a reactor in which reactions take place in multiphase systems, wherein a gaseous phase prevalently consisting of CO and H2 is bubbled into a suspension of a solid in the form of particles (catalyst) in a liquid (prevalently reaction product), according to the Fischer-Tropsch technology.

Process for the charging of a catalyst into a reactor suitable for reactions in heterogeneous phase

Process for the running of a reactor suitable for heterogeneous reactions combined with reactions taking place in three-phase systems

A process for synthesising hydrocarbons by reacting a mixture comprising at least carbon monoxide and hydrogen in the presence of a catalyst is carried out in a three-phase reactor in which the liquid Peclet number is in the range 0 (excluded) to about 10, with a superficial gas velocity U that is preferably less than 35 cm.s , to encourage gas transfer into the liquid phase and avoid too much attrition of the catalyst grains.

Method for producing hydrocarbons from syngas in three-phase reactor

A process for converting hydrocarbons in the presence of a catalyst is described that is carried out in a three-phase reactor in which the liquid Peclet number is in the range 0 (excluded) to about 10, with a superficial gas velocity U that is preferably less than 35 cm.s , to encourage gas transfer into the liquid phase and avoid too much attrition of the catalyst grains.

Method for converting hydrocarbons in a three-phase reactor

Fischer-Tropsch process

Process for regenerating a catalyst contained within a bubble-column

Process for the optimum operation of a slurry bubble column reactor in the presence of a gas phase and a liquid phase, particularly for the Fischer-Tropsch reaction, characterized in that:

Fischer-Tropsch process with a multistage bubble column reactor

Growing community of inventors

Lodi, Italy

Cristina Maretto