Patent ID: 7713489

Claim:
A process for the study and the extrapolation of an industrial or pilot unit that operates in a reactive simulated moving bed wherein a feedstock and a desorbent are supplied and an extract and a raffinate are withdrawn according to periods of time called zones and defined in the following manner: Zone 1: Time period encompassed between beginning of draw-off of the extract and end of injection of the desorbent, Zone 2: Time period encompassed between end of injection of the feedstock and beginning of the draw-off of the extract, Zone 3: Time period encompassed between beginning of draw-off of the raffinate and end of injection of the feedstock, Zone 4: Time period encompassed between the end of the injection of the desorbent and the beginning of the draw-off of the raffinate, said process comprising providing a device that comprises a first column (C 4 ) that contains the adsorbent, a second column (R 6 ) that contains catalyst and a number of tanks (B 23 to B 34 ) for supplying of the adsorption column (C 4 ) and for storage of the effluent obtained from catalytic column (R 6 ), except for certain stages of the cycle where said catalytic column is short-circuited, a cycle of said process being defined as the period of time between two successive desorbent injections and being divided into elementary stages, each elementary stage being defined by the simultaneous exchange of the tank that is used for the supply of the column and the tank that is used for the storage of the effluent of the column (R 6 ), and the device being characterized by the number of tanks that is at least equal to the number of zones of the simulated moving bed unit being studied, whereby the process operates according to a cycle that is defined as with each stage n of said cycle, with the exception of the latter, the adsorbent column (C 4 ) is supplied by the contents of the tank that has been filled by the flow of output from the column (R 6 ) (or by the flow of output from the column (C 4 ) when the column (R 6 ) is short-circuited), corresponding to the stage (n +1) of the preceding cycle, and by the fact that in the last stage of the cycle, the adsorbent column (C 4 ) is supplied by the content of the tank that has been filled by the flow of output from the column (R 6 ), or by the flow of output from the column (C 4 ) if the column (R 6 ) is short-circuited, corresponding to the first stage of the preceding cycle.