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Methods for treating or rejuvenating a spent catalyst are described. These methods can employ a step of halogenating the spent catalyst, followed by decoking the halogenated spent catalyst. The halogenation step can utilize fluorine and chlorine together, or fluorine and chlorine can be applied sequ

Methods for treating or rejuvenating a spent catalyst are described. These methods can employ a step of halogenating the spent catalyst, followed by decoking the halogenated spent catalyst. The halogenation step can utilize fluorine and chlorine together, or fluorine and chlorine can be applied sequentially.

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1. A method of treating a spent catalyst comprising a transition metal and a catalyst support, the method comprising: (1) contacting the spent catalyst with a fluorine-containing stream comprising a fluorine-containing compound to produce a fluorinated spent catalyst;(2) contacting the fluorinated s

1. A method of treating a spent catalyst comprising a transition metal and a catalyst support, the method comprising: (1) contacting the spent catalyst with a fluorine-containing stream comprising a fluorine-containing compound to produce a fluorinated spent catalyst;(2) contacting the fluorinated spent catalyst with a chlorine-containing stream comprising a chlorine-containing compound to produce a fluorinated-chlorinated spent catalyst; and(3) contacting the fluorinated-chlorinated spent catalyst with a decoking gas stream comprising oxygen. 2. The method of claim 1, wherein: step (1) is conducted at a fluorination temperature in a range from about 25° C. to about 250° C.; anda concentration of fluorine (F) in the fluorine-containing stream is less than about 2,500 ppm by volume. 3. The method of claim 2, wherein the fluorine-containing stream is substantially free of oxygen-containing compounds. 4. The method of claim 1, wherein the fluorine-containing stream comprises F2 and nitrogen. 5. The method of claim 1, wherein: step (2) is conducted at a chlorination temperature in a range from about 150° C. to about 300° C.; anda concentration of chlorine (Cl) in the chlorine-containing stream is less than about 2,500 ppm by volume. 6. The method of claim 5, wherein the chlorine-containing stream is substantially free of oxygen-containing compounds. 7. The method of claim 1, wherein the chlorine-containing stream comprises Cl2 and nitrogen. 8. The method of claim 1, further comprising a halogen purge step prior to step (2), the halogen purge step comprising contacting the fluorinated spent catalyst with a halogen purge stream consisting essentially of an inert gas. 9. The method of claim 1, wherein: step (3) is conducted at a peak decoking temperature in a range from about 300° C. to about 500° C.;the decoking gas stream comprises air or a mixture of nitrogen and oxygen; andthe decoking gas stream is substantially free of halogen-containing compounds. 10. The method of claim 1, wherein the spent catalyst comprises: platinum on a KL-zeolite;a support matrix comprising alumina, silica, a mixed oxide thereof, or a mixture thereof;from about 0.025 wt. % to about 5 wt. % chlorine; andfrom about 0.025 wt. % to about 5 wt. % fluorine. 11. The method of claim 1, further comprising: a pre-drying step prior to step (1), the pre-drying step comprising contacting the spent catalyst with a pre-drying gas stream consisting essentially of an inert gas;a re-coking pretreatment step prior to step (1), the re-coking pretreatment step comprising contacting the spent catalyst with a pretreatment stream comprising molecular hydrogen and a hydrocarbon feed comprising C6-C8 alkanes and/or cycloalkanes;a partial decoking step prior to step (1), the partial decoking step comprising contacting the spent catalyst with a partial decoking gas stream comprising oxygen at a partial decoking temperature in a range from about 150° C. to about 250° C.; orany combination thereof. 12. The method of claim 1, further comprising a reducing step after step (3), the reducing step comprising contacting the de-coked catalyst with a reducing gas stream comprising molecular hydrogen. 13. The method of claim 1, further comprising: a purging step prior to step (3), the purging step comprising contacting the fluorinated-chlorinated spent catalyst with a purging stream consisting essentially of an inert gas;a hydrocarbon treatment step prior to step (3), the hydrocarbon treatment step comprising contacting the fluorinated-chlorinated spent catalyst with a hydrocarbon treatment stream comprising a hydrocarbon feed comprising C6-C8 alkanes and/or cycloalkanes; orboth. 14. A rejuvenated catalyst produced by the method of claim 1. 15. A method of treating a spent catalyst comprising a transition metal and a catalyst support, the method comprising: (1) contacting the spent catalyst with a chlorine-containing stream comprising a chlorine-containing compound to produce a chlorinated spent catalyst;(2) contacting the chlorinated spent catalyst with a fluorine-containing stream comprising a fluorine-containing compound to produce a chlorinated-fluorinated spent catalyst; and(3) contacting the chlorinated-fluorinated spent catalyst with a decoking gas stream comprising oxygen. 16. The method of claim 15, wherein: step (1) is conducted at a chlorination temperature in a range from about 150° C. to about 300° C.;a concentration of chlorine (Cl) in the chlorine-containing stream is less than about 2,500 ppm by volume;the chlorine-containing stream comprises Cl2 and nitrogen, and is substantially free of oxygen-containing compounds;step (2) is conducted at a fluorination temperature in a range from about 25° C. to about 250° C.;a concentration of fluorine (F) in the fluorine-containing stream is less than about 2,500 ppm by volume; andthe fluorine-containing stream comprises F2 and nitrogen, and is substantially free of oxygen-containing compounds. 17. The method of claim 15, wherein the spent catalyst comprises: platinum on a KL-zeolite;a support matrix comprising alumina, silica, a mixed oxide thereof, or a mixture thereof;from about 0.025 wt. % to about 5 wt. % chlorine; andfrom about 0.025 wt. % to about 5 wt. % fluorine. 18. A reforming process comprising: (A) contacting a hydrocarbon feed with an aromatization catalyst comprising a transition metal and a catalyst support under reforming conditions in a reactor system to produce an aromatic product;(B) performing step (A) for a time period sufficient to form a spent aromatization catalyst;(C) contacting the spent aromatization catalyst with a fluorine-containing stream comprising a fluorine-containing compound to produce a fluorinated spent catalyst;(D) contacting the fluorinated spent catalyst with a chlorine-containing stream comprising a chlorine-containing compound to produce a fluorinated-chlorinated spent catalyst; and(E) contacting the fluorinated-chlorinated spent catalyst with a decoking gas stream comprising oxygen. 19. The process of claim 18, wherein the reforming process is an in situ process. 20. The process of claim 18, wherein steps (C)-(E) are performed in a vessel external to the reactor system. 21. A reforming process comprising: (A) contacting a hydrocarbon feed with an aromatization catalyst comprising a transition metal and a catalyst support under reforming conditions in a reactor system to produce an aromatic product;(B) performing step (A) for a time period sufficient to form a spent aromatization catalyst;(C) contacting the spent aromatization catalyst with a chlorine-containing stream comprising a chlorine-containing compound to produce a chlorinated spent catalyst;(D) contacting the chlorinated spent catalyst with a fluorine-containing stream comprising a fluorine-containing compound to produce a chlorinated-fluorinated spent catalyst; and(E) contacting the chlorinated-fluorinated spent catalyst with a decoking gas stream comprising oxygen. 22. The process of claim 21, wherein the reforming process is an in situ process. 23. The process of claim 21, wherein steps (C)-(E) are performed in a vessel external to the reactor system.