Use of high halide-containing catalyst in front reactors to extend the life and selectivity of reforming catalyst

Patent metadata

Field	Value
Publication number	US-12286595-B2
Application number	US-202318322132-A
Country	US
Kind code	B2
Filing date	May 23, 2023
Priority date	Jun 17, 2022
Publication date	Apr 29, 2025
Grant date	Apr 29, 2025

Abstract

This disclosure provides processes for reforming hydrocarbons by using a series of adiabatic reactors and catalysts, in which the catalyst(s) in at least one front or upstream catalyst bed or reactor includes a higher fluoride concentration, higher chloride concentration, or both than the respective halide concentrations in the catalysts in one or more downstream catalyst beds or reactors, which has been unexpectedly discovered to extend the useful life and/or the selectivity of the catalyst system.

First claim

We claim:

1. A process for reforming hydrocarbons comprising:
a) in a first catalyst bed, contacting a feedstock containing aliphatic hydrocarbons with a first catalyst comprising an inorganic support, a Group 8-10 metal, and from about 1.0 wt % to about 5.0 wt % fluoride relative to the weight of the first catalyst prior to reduction, under conditions for aromatizing aliphatic hydrocarbons to form a first catalyst bed discharge comprising aromatic hydrocarbons and aliphatic hydrocarbons;
b) in one or more intermediate catalyst beds in series, contacting the first catalyst bed discharge with one or more independently selected intermediate catalysts, each comprising an inorganic support, a Group 8-10 metal, and fluoride, under conditions for aromatizing aliphatic hydrocarbons to form one or more intermediate catalyst bed discharges comprising aromatic hydrocarbons and aliphatic hydrocarbons; and
c) in a last catalyst bed, contacting the one or more intermediate catalyst bed discharges with a last catalyst comprising an inorganic support, a Group 8-10 metal, and from about 0.7 wt % to about 4.0 wt % fluoride relative to the weight of the last catalyst prior to reduction, under conditions for aromatizing aliphatic hydrocarbons to form a last catalyst bed discharge comprising aromatic products;
wherein the fluoride concentration of the first catalyst or the fluoride concentration of at least one of the intermediate catalysts is greater than the fluoride concentration of the last catalyst prior to reduction.

2. A process for reforming hydrocarbons according to claim 1 , wherein:
the first catalyst, any one or more of the intermediate catalysts, the last catalyst, or any combination thereof independently further comprises from about 1.5 wt % to about 4.0 wt % chloride relative to the weight of the respective first catalyst, intermediate catalyst, or last catalyst prior to reduction; and
the chloride concentration of the first catalyst or the chloride concentration of at least one of the intermediate catalysts is greater than the chloride concentration of the last catalyst prior to reduction.

3. A process for reforming hydrocarbons according to claim 2 , wherein the chloride concentration (wt %) in the one or more intermediate catalysts at startup is greater than, less than, or equal to the chloride concentration of the first catalyst prior to reduction and greater than or equal to the chloride concentration of the last catalyst prior to reduction.

4. A process for reforming hydrocarbons according to claim 1 , wherein the first catalyst bed, the one or more intermediate catalyst beds, and the last catalyst bed are each in different reactors.

5. A process for reforming hydrocarbons according to claim 1 , wherein:
the process includes from 1 to 6 intermediate catalyst beds comprising from 1 to 6 intermediate catalysts, respectively,
the first catalyst bed, the 1 to 6 intermediate catalyst beds, and the last catalyst bed are all in different reactors, and
the fluoride concentration (wt %) in each of the 1 to 6 intermediate catalysts at startup is selected independently of the fluoride concentration in any other catalyst and is at least or about the same fluoride concentration of the last catalyst prior to reduction.

6. A process for reforming hydrocarbons according to claim 1 , wherein:
the process includes 4 or 5 intermediate catalyst beds, each comprising its own respective intermediate catalyst;
the first catalyst bed, the 4 or 5 intermediate catalyst beds, and the last catalyst bed are each in different reactors; and
the volume of each of the 4 or 5 intermediate reactors is greater than or equal to the volume of the first reactor and less than or equal to the volume of the last reactor.

7. A process for reforming hydrocarbons according to claim 1 , wherein the first catalyst bed discharge and/or the one or more intermediate catalyst bed discharges are heated prior to entering the subsequent catalyst bed.

8. A process for reforming hydrocarbons according to claim 1 , wherein the first catalyst, the one or more intermediate catalysts, and the last catalyst each comprise, independently, an inorganic support comprising a zeolite, a silica-bound zeolite, a clay mineral, silica, alumina, silica-alumina, aluminum phosphate, a heteropolytungstate, titania, zirconia, magnesia, boria, zinc oxide, mixed oxides thereof, or mixtures thereof.

9. A process for reforming hydrocarbons according to claim 1 , wherein the first catalyst, the one or more intermediate catalysts, and the last catalyst each comprise, independently, an inorganic support comprising L-zeolite, X-zeolite, Y-zeolite, omega zeolite, beta zeolite, ZSM-4, ZSM-5, ZSM-10, ZSM-11, ZSM-12, ZSM-20, REY, USY, RE-USY, LZ-210, LZ-210-A, LZ-210-M, LZ-210-T, SSZ-24, SSZ-26, SSZ-31, SSZ-33, SSZ-35, SSZ-37, SSZ-41, SSZ-42, SSZ-44, MCM-58, mordenite, mazzite, 3aujasite, or combinations thereof.

10. A process for reforming hydrocarbons according to claim 1 , wherein the first catalyst, the one or more intermediate catalysts, and the last catalyst each comprise a Group 10 metal selected independently from nickel, palladium, or platinum.

11. A process for reforming hydrocarbons according to claim 1 , wherein the first catalyst, the one or more intermediate catalysts, and/or the last catalyst comprise platinum and L-zeolite.

12. A process for reforming hydrocarbons according to claim 1 , wherein the fluoride concentration (wt %) in the one or more intermediate catalysts at startup is greater than, less than, or equal to the fluoride concentration of the first catalyst prior to reduction and greater than or equal to the fluoride concentration of the last catalyst prior to reduction.

13. A process for reforming hydrocarbons according to claim 1 , wherein any one or more of the first catalyst, the intermediate catalysts, and/or the last catalyst further comprise chloride and the weight ratio of chloride to fluoride is from 1:10 to 10:1.

14. A process for reforming hydrocarbons according to claim 1 , wherein the Group 8-10 metal of each of the first catalyst, the one or more intermediate catalysts, and the last catalyst is platinum and the platinum concentration in each catalyst is selected independently from 0.3 wt % to 1.5 wt % relative to the weight of each respective catalyst prior to reduction.

15. A catalytic hydrocarbon reforming system comprising:
at least three catalyst beds in series, including an upstream first catalyst bed, a downstream last catalyst bed, and one or more intermediate catalyst beds in series between the first catalyst bed and the last catalyst bed;
a first catalyst in the first catalyst bed comprising an inorganic support, a Group 8-10 metal, and from about 1.0 wt % to about 5.0 wt % fluoride relative to the weight of the first catalyst prior to reduction;
one or more independently selected intermediate catalysts in the one or more intermediate catalyst beds, each intermediate catalyst comprising an inorganic support, a Group 8-10 metal, and fluoride; and
a last catalyst in the last catalyst bed comprising an inorganic support, a Group 8-10 metal, and from about 0.7 wt % to about 4.0 wt % fluoride relative to the weight of the last catalyst prior to reduction;
wherein the fluoride concentration of the first catalyst or the fluoride concentration of at least one of the intermediate catalysts is greater than the fluoride concentration of the last catalyst prior to reduction.

16. A catalytic hydrocarbon reforming system according to claim 15 , wherein:
the first catalyst, any one or more of the intermediate catalysts, the last catalyst,

Assignees

• Chevron Phillips Chemical Co Lp
• Chevron Philips Chemical Company Lp

Inventors

• Demmelmaier-Chang Cori A
• Bergmeister Iii Joseph
• Mcgahee Vincent D
• Alvez-Manoli Gabriela D

Classifications

• C10G2400/30

  Aromatics · CPC title

• C10G2300/70

  Catalyst aspects · CPC title

• B01J29/62

  Noble metals · CPC title

• B01J37/26

  Fluorinating · CPC title

• B01J2229/20

  to introduce other elements in the catalyst composition comprising the molecular sieve, but not specially in or on the molecular sieve itself · CPC title