METHOD FOR TREATING A CATALYST BEFORE UNLOADING
The present invention relates to a process for treating, in a reactor containing a catalytic bed, a solid catalyst, said process comprising the steps of: a) implementing, in said reactor, a gas-phase catalytic reaction at a catalytic bed temperature T1 in the presence of a hydrogen halide or giving rise to the formation of a hydrogen halide, b) causing an inert gas to flow through the catalytic bed at a catalytic bed temperature T2 that is lower than T1, the temperature T2 being greater than 30° C.
1 - 14 . (canceled)
15 . A process for treating, in a reactor containing a catalytic bed, a solid catalyst, said process comprising the steps of:
a) implementing, in said reactor, a gas-phase catalytic reaction at a catalytic bed temperature T1 in the presence of a hydrogen halide or giving rise to the formation of a hydrogen halide, and
b) causing an inert gas to flow through the catalytic bed at a catalytic bed temperature T2 that is lower than T1, the temperature T2 being greater than 30° C.
16 . The process as claimed in claim 15 , characterized in that the inert gas introduced into the reactor is at a temperature of between ambient temperature and the temperature T2.
17 . The process as claimed in claim 15 , characterized in that the inert gas introduced into the reactor is at ambient temperature.
18 . The process as claimed in claim 15 , characterized in that the hydrogen halide is hydrogen fluoride or hydrogen chloride.
19 . The process as claimed in claim 15 , characterized in that the hydrogen halide is in anhydrous form.
20 . The process as claimed in claim 15 , characterized in that the temperature T2 decreases during the implementation of step b).
21 . The process as claimed in claim 15 , characterized in that the temperature T2 decreases at a rate of less than 1° C./min during the implementation of step b).
22 . The process as claimed in claim 15 , characterized in that the inert gas flows at a flow rate of greater than 0.1 ml/min per ml of catalyst.
23 . The process as claimed in claim 15 , characterized in that the catalyst is based on carbon or based on a metal selected from the group consisting of Cr, Fe, Sb, Ni, Co, Zn, Al and Mn.
24 . The process as claimed in claim 15 , characterized in that step a) implements a gas-phase reaction between HF and a C 1 -C 4 halohydrocarbon compound A or step a) implements a gas-phase dehydrohalogenation reaction of a saturated C 1 -C 4 hydrocarbon compound B comprising at least one halogen atom to form an unsaturated C 1 -C 4 hydrocarbon compound and a hydrogen halide.
25 . The process as claimed in claim 15 , characterized in that the compound A is selected from the group consisting of 1,1,2-trichloroethane, 2-chloro-1,1,1-trifluoroethane, 1-chloro-1,1,2-trifluoroethane, 1-chloro-1,2,2-trifluoroethane, 1,1,1,3,3,3-hexachlorodifluoropropane, 1,1,1,3,3,3-hexachloropropane, 1,1,1,3,3-pentachloropropane, 2,2,3-trichloro-1,1,1,3,3-pentafluoropropane, 1,1,1,3,3,3-hexachlorodifluoropropane, 1,1-dichloro-2,2,3,3,3-pentafluoropropane, 1,3-dichloro-1,2,2,3,3-pentafluoropropane, 1,1,1,2,3-pentachloropropane, 1,1,2,2,3-pentachloropropane, 1,1,1,3,3-pentachloropropane, 1,2-dichloroethylene, 1,1,2-trichloroethylene, 1,1,2,2-tetrachloroethylene, 1,1,2-trichloro-3,3,3-trifluoropropene, hexafluoropropene, 1,1,3,3,3-pentafluoropropene, 1,3,3,3-tetrafluoropropene, 2-chloro-3,3,3-trifluoropropene, 1,1,2,3-tetrachloropropene, 2,3,3,3-tetrachloropropene, 1-chloro-3,3,3-trifluoropropene, 1,1,3,3-tetrachloropropene, 1,3,3,3-tetrachloropropene, 2,3-dichloro-1,1,1-trifluoropropane, and 2-chloro-1,1,1,2-tetrafluoropropane; or
the compound B is selected from the group consisting of 1,1-difluoroethane, 1,1,1-trifluoroethane, 2-chloro-1,1,1-trifluoroethane, 1,1,1,2-tetrafluoroethane, 1,1,2,2-tetrafluoroethane, 1,1,1,2,2-pentafluoroethane, 1,1,1,2-tetrafluoropropane, 1,1,1,2,3,3-hexafluoropropane, 1,1,1,3,3,3-hexafluoropropane, 1,1,1,2,2,3-hexafluoropropane, 1,1,1,2,2-pentafluoropropane, 1,1,1,2,3-pentafluoropropane, 1,1,1,3,3-pentafluoropropane, 2,3-dichloro-1,1,1-trifluoropropane, and 2-chloro-1,1,1,2-tetrafluoropropane.
26 . The process as claimed in claim 15 , characterized in that the process comprises a step c) of unloading the catalyst from said reactor.
27 . The process as claimed in claim 15 , characterized in that step b) comprises a step b1) of cooling the catalytic bed from the temperature T1 to T2, and then a step b2) of causing said inert gas to flow through the catalytic bed.
28 . A process for treating, in a reactor containing a catalytic bed, a solid catalyst, said process comprising the steps of:
a) implementing, in said reactor, a gas-phase catalytic reaction at a catalytic bed temperature T1 in the presence of a hydrogen halide or giving rise to the formation of a hydrogen halide, and
b) causing an inert gas to flow through the catalytic bed at a catalytic bed temperature T2 that is lower than T1, the temperature T2 decreasing during the implementation of step b).