Catalyst for converting heavy reformate to produce BTX compounds
A method of making BTX (benzene, toluene, xylene) compounds by feeding a heavy reformate stream to a reactor, where the reactor includes a composite zeolite catalyst, that contains a mixture of a desilicated mesoporous mordenite and ZSM-5, and in which the desilicated mesoporous mordenite, the ZSM-5, or both, comprise one or more impregnated metals. The composite zeolite catalyst is able to catalyze the transalkylation reaction and the dealkylation reaction simultaneously to produce the BTX compounds.
1. A method of making BTX compounds comprising benzene, toluene, and xylene, the method comprising:
feeding a heavy reformate stream to a reactor, the reactor comprising a composite zeolite catalyst,
where the composite zeolite catalyst comprises a mixture of a desilicated mesoporous mordenite in the acid form and ZSM-5,
the desilicated mesoporous mordenite has a molar Si to Al ratio of at least 30, as measured by Inductive Coupling Plasma Mass Spectrometry (ICP-MS),
the desilicated mesoporous mordenite has a surface Si/Al molar ratio greater than 50, as measured by X-ray photoelectron spectroscopy,
the composite zeolite catalyst comprises a mixture of desilicated mesoporous mordenite and ZSM-5 in a 50:50 to 90:10 weight ratio, and
the desilicated mesoporous mordenite, the ZSM-5, or both, comprise one or more impregnated metals; and
producing the BTX compounds by simultaneously performing a transalkylation reaction and a dealkylation reaction of the heavy reformate stream in the reactor, where the composite zeolite catalyst is able to catalyze the transalkylation reaction and the dealkylation reaction simultaneously.
2. The method of claim 1 , where the heavy reformate stream comprises at least 15 weight percent (wt. %) methylethylbenzene (MEB) and at least 50 wt. % trimethylbenzene (TMB), based on the total weight of the heavy reformate stream.
3. The method of claim 1 , where the one or more impregnated metals are selected from Group VI and Group VII according to IUPAC nomenclature, in which the metal in the zeolite catalyst is from 0.05 to 10 wt. %, based on the total weight of the zeolite catalyst.
4. The method of claim 1 , where the composite zeolite catalyst comprises a mixture of desilicated mesoporous mordenite and ZSM-5 in a 60:40 to 80:20 weight ratio.
5. The method of claim 1 , where the one or more impregnated metals are selected from the group consisting of molybdenum, chromium, nickel, tungsten, palladium, ruthenium, gold, rhenium, rhodium, or combinations thereof and their respective oxides.
6. The method of claim 1 , where the desilicated mesoporous mordenite, the ZSM-5, or both the desilicated mesoporous mordenite and ZSM-5 comprise 0.05 wt. % to 10 wt. % of the one or more impregnated metals.
7. The method of claim 1 , where the one or more impregnated metals comprise rhenium (Re).
8. The method of claim 7 , where the desilicated mesoporous mordenite comprises from 0.25 to 0.55 wt. % Re, based on the total weight of the zeolite catalyst.
9. The method of claim 7 , where the ZSM-5 comprises from 0.25 to 0.55 wt. % Re, based on the total weight of the zeolite catalyst.
10. The method of claim 1 , where the ZSM-5 has a Si to Al molar ratio of at least 10, as measured by ICP-MS.
11. The method of claim 1 , where the desilicated mesoporous mordenite has a micropore to mesopore volumetric ratio of less than 3.0.
12. The method of claim 1 , where the heavy reformate stream comprises at least 30 wt. % MEB or at least 70 wt. % TMB.
13. The method of claim 1 , where the desilicated mesoporous mordenite has a Brunauer-Emmet-Teller (BET) surface area of at least 420 square meters per gram (m 2 /g), an external surface area of at least 80 m 2 /g, or both.