Production of high yields of light olefins from heavy hydrocarbons
US-11891356-B2 · Feb 6, 2024 · US
US2022016609A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2022016609-A1 |
| Application number | US-202016930462-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jul 16, 2020 |
| Priority date | Jul 16, 2020 |
| Publication date | Jan 20, 2022 |
| Grant date | — |
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According to the subject matter of the present disclosure, a method of producing an aromatization catalyst may comprise producing a plurality of uncalcined ZSM-5 nanoparticles via a dry-gel method, directly mixing the plurality of uncalcined ZSM-5 nanoparticles with large pore alumina and a binder to form a ZSM-5/alumina mixture, and calcining the ZSM-5/alumina mixture to form the aromatization catalyst. The plurality of uncalcined ZSM-5 nanoparticles may have an average diameter of less than 80 nm.
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What is claimed is: 1 . A method of producing an aromatization catalyst, the method comprising: producing a plurality of uncalcined ZSM-5 nanoparticles via a dry-gel method, wherein the plurality of ZSM-5 nanoparticles has an average diameter of less than 80 nm; directly mixing the plurality of uncalcined ZSM-5 nanoparticles with large pore alumina and a binder to form a ZSM-5/alumina mixture; and calcining the ZSM-5/alumina mixture to form the aromatization catalyst; wherein the large pore alumina has a pore size of from 18 nm to 26 nm. 2 . The method of producing an aromatization catalyst of claim 1 , wherein the plurality of uncalcined ZSM-5 nanoparticles has not been subjected to centrifugation above 3,000 rpm, before being mixed with the large pore alumina and binder. 3 . The method of producing an aromatization catalyst of claim 1 , wherein the plurality of uncalcined ZSM-5 nanoparticles has not been subjected to calcination above 200° C. for more than 30 minutes, before being mixed with the large pore alumina and binder. 4 . The method of producing an aromatization catalyst of claim 1 , wherein the ZSM-5/alumina mixture is calcined at a temperature of from 400° C. to 700° C. for from 1 hour to 10 hours. 5 . The method of producing an aromatization catalyst of claim 1 , wherein the aromatization catalyst is impregnated with gallium atoms to form a Ga-ZSM-5 catalyst. 6 . The method of producing an aromatization catalyst of claim 5 , wherein the Ga-ZSM-5 catalyst is calcined. 7 . The method of producing an aromatization catalyst of claim 1 , wherein the aromatization catalyst is impregnated with a catalytic metal to form a metal-ZSM-5 catalyst, the metal-ZSM-5 catalyst comprises from 50 wt. % to 90 wt. % ZSM-5, 5 wt. % to 30 wt. % large pore alumina, 10 wt. % to 20 wt. % binder, and 0.2 wt. % to 6 wt. % catalytic metal. 8 . The method of producing an aromatization catalyst of claim 7 , wherein the catalytic metal comprises gallium. 9 . The method of producing a catalyst of claim 1 , wherein the directly mixing is extrusion. 10 . The method of producing an aromatization catalyst of claim 1 , wherein the plurality of uncalcined ZSM-5 nanoparticles has an average diameter 30 nm to 80 nm. 11 . The method of producing an aromatization catalyst of claim 1 , wherein at least 90% of the individual uncalcined ZSM-5 nanoparticles have diameters from 20 nm to 50 nm. 12 . The method of producing an aromatization catalyst of claim 1 , wherein an average pore size of the uncalcined ZSM-5 nanoparticles is from 35 nm to 55 nm. 13 . The method of producing an aromatization catalyst of claim 1 , wherein a BET surface area of the uncalcined ZSM-5 nanoparticles is from 300 m 2 /g to 600 m 2 /g. 14 . The method of producing an aromatization catalyst of claim 1 , wherein a pore volume of the uncalcined ZSM-5 nanoparticles is from 0.3 ml/g to 0.45 ml/g. 15 . (canceled) 16 . The method of producing a catalyst of claim 1 , wherein the producing the plurality of uncalcined ZSM-5 nanoparticles via the dry-gel method comprises: combining an alumina source, a structure directing agent, and a silica source to form a slurry; optionally, introducing NaOH to the slurry such that the final concentration of NaOH in the slurry is from 0.000001 g/L to 0.1 g/L; drying the slurry to form a dry-gel; and autoclaving the dry-gel in a humidified autoclave to form the plurality of uncalcined ZSM-5 nanoparticles. 17 . The method of producing an aromatization catalyst of claim 17 , wherein the water content of the dry-gel is less than 25 wt. %. 18 . The method of producing an aromatization catalyst of claim 1 , wherein the dry-gel is not agitated during autoclaving.
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