Catalytic cracking process for the treatment of a fraction having a low conradson carbon residue
Process for the fluidized-bed catalytic cracking of a weakly coking feedstock having a Conradson carbon residue equal to or less than 0.1% by weight and a hydrogen content equal to or greater than 12.7% by weight, comprising at least a step of cracking the feedstock, a step of separating/stripping the effluents from the coked catalyst particles and a step of regenerating said particles, the process being characterized in that at least one coking, carbonaceous and/or hydrocarbonaceous effluent having a content of aromatic compounds of greater than 50% by weight, comprising more than 20% by weight of polyaromatic compounds, is recycled to homogeneously distributed and weakly coked catalyst, before regeneration, in order to adjust the delta coke of the process.
1. Plant for implementing a process for fluidized bed catalytic cracking, comprising at least a main reactor and optionally at least a secondary reactor, at least a disengager and a stripper, and a single-stage or multistage regenerator, characterized in that the stripper contains, level with a dense catalyst bed, at least one zone equipped with at least one structured packing element positioned upstream of a device for dispersing a coking fraction with respect to circulation of a stream of catalyst particles, wherein said structured packing element(s) are formed by interlacing plates, strips or fins constituting a screen, said screen occupying less than 10% of the area of flow cross section in a vessel in which it is placed, but covering, in projection on said section, the entire area thereof.
2. Plant according to claim 1 , characterized in that the stripper contains at least two zones equipped with at least one structured packing element that are associated with two fluid-dispersing devices, one for dispersing coking fractions, the other for dispersing the stripping fluid, these devices being located downstream of said structured packing elements relative to the stream of catalyst particles.
3. Plant according to claim 2 , characterized in that the coking fractions and stripping fluid dispersion devices are chosen from spraying, rod-type injectors, venturi pressurized atomizing injectors, fluidization rings and sparger tubes.
4. Plant according to claim 1 , characterized in that the stripper is located in one and the same vessel as the disengager.
5. Plant according to claim 1 , characterized in that the stripper is located in a different vessel downstream of the disengager, but still positioned upstream of the regenerator.
6. Plant according to claim 5 , characterized in that the disengager and/or the stripper comprises, respectively, at the outlet of said disengager and/or inlet of the catalyst particles into said stripper, at least one structured packing element followed by a device for dispersing stripping fluids for the pre-stripping of the catalyst particles.
7. Plant according to claim 1 , characterized in that when the stripper comprises a plurality of structured packing elements for the intercalated recycle and stripping, each structured packing element being associated with a fluid-dispersing device, the volumes occupied for the recycle and the stripping are respectively from 25 to 65% and from 35 to 75% of the volume of stripping zone or vessel.