A method for optimising the operation of a facility for catalytic reforming, the facility including a multitude of reactors which have a catalyser and through which an operating gas including hydrocarbons and molecular hydrogen successively flows, wherein the composition of the operating gas in the reactors changes and wherein a product results at the outlet side of the last reactor. Specific constant characteristics as well as initial operating parameters that are present during the operation of the facility are acquired. A computational simulation of the chemical processes in the reactors then takes place, wherein results of a measurement of the chemical composition of the product at the outlet side of the last reactor is also included. A computational simulation of the chemical processes in the reactors with different varied operating parameters is subsequently carried out and set of optimised operating parameters is determined from the computed chemical composition.