Synthesis of oxygen-mobility enhanced CeO2 and use thereof

Patent metadata

Field	Value
Publication number	US-10478808-B2
Application number	US-201615191844-A
Country	US
Kind code	B2
Filing date	Jun 24, 2016
Priority date	Jul 1, 2015
Publication date	Nov 19, 2019
Grant date	Nov 19, 2019

Abstract

Disclosed are catalysts capable of catalyzing the dry reforming of methane. The catalysts have a core-shell structure with the shell surrounding the core. The shell has a redox-metal oxide phase that includes a metal dopant incorporated into the lattice framework of the redox-metal oxide phase. An active metal(s) is deposited on the surface of the shell.

First claim

The invention claimed is:

1. A catalyst comprising a core-shell structure having:
a metal oxide core, a clay core, or a zeolite core;
a shell completely surrounding the core, wherein the shell has a redox-metal phase having tin (Sn), niobium (Nb), lanthanum (La), bismuth (Bi), indium (In) or gallium (Ga), or any combination thereof incorporated into the lattice framework of the redox-metal oxide phase; and
an active-metal deposited on the surface of the shell, wherein the redox-metal oxide phase is cerium oxide (CeO 2 ),
wherein the catalyst is capable of catalyzing the production of hydrogen (H 2 ) and carbon monoxide (CO) from methane (CH 4 ) and carbon dioxide (CO 2 ).

2. The catalyst of claim 1 , wherein the metal oxide core is an alkaline earth metal aluminate core selected from magnesium aluminate, calcium aluminate, strontium aluminate, barium aluminate, or any combination thereof.

3. The catalyst of claim 2 , wherein the alkaline earth metal aluminate core is magnesium aluminate.

4. The catalyst of claim 3 , comprising:
65 wt. % to 85 wt. % magnesium aluminate;
10 wt. % to 20 wt. % cerium oxide; and
5 wt. % to 10 wt. % nickel.

5. The catalyst of claim 4 , comprising 0.5 wt. % to 2 wt. % of niobium incorporated into the lattice framework of the redox-metal oxide phase.

6. The catalyst of claim 4 , comprising 0.5 wt. % to 2 wt. % of indium incorporated into the lattice framework of the redox-metal oxide phase.

7. The catalyst of claim 4 , comprising 0.5 wt. % to 2 wt. % of lanthanum incorporated into the lattice framework of the redox-metal oxide phase.

8. The catalyst of claim 1 , wherein the active metal comprises nickel.

9. The catalyst of claim 1 , wherein the core is Al 2 O 3 and the metal deposited on the surface of the shell is nickel, rhodium, ruthenium, or platinum or any combination thereof.

10. The catalyst of claim 1 , wherein the active metal deposited on the surface of the shell is nickel, rhodium, ruthenium, iridium, platinum, palladium, gold, silver, palladium, cobalt, manganese, copper, or any combination thereof.

11. The catalyst of claim 1 , wherein the catalyst includes 5 to 50 wt. % of the redox-metal oxide phase, 0.1 to 5 wt. % of the metal dopant, and 1 to 40 wt. % of the active metal deposited on the surface of the shell.

12. A catalyst comprising a core-shell structure having:
a MgAl 2 O 4 core;
a shell completely surrounding the core, wherein the shell has a cerium oxide phase having tin (Sn), niobium (Nb), lanthanum (La), bismuth (Bi), indium (In) or gallium (Ga), incorporated into the lattice framework of the cerium oxide phase; and
nickel deposited on the surface of the shell,
wherein the catalyst is capable of catalyzing the production of hydrogen (H 2 ) and carbon monoxide (CO) from methane (CH 4 ) and carbon dioxide (CO 2 ).

13. A system for producing hydrogen (H 2 ) and carbon monoxide (CO) from methane (CH 4 ) and carbon dioxide (CO 2 ), the system comprising:
an inlet for a reactant feed comprising CH 4 and CO 2 ;
a reaction zone that is configured to be in fluid communication with the inlet, wherein the reaction zone comprises the catalyst of claim 1 ; and
an outlet configured to be in fluid communication with the reaction zone and configured to remove a first product stream comprising H 2 and CO from the reaction zone.

14. A method of producing hydrogen (H 2 ) and carbon monoxide (CO) from methane (CH 4 ) and carbon dioxide (CO 2 ), the method comprising contacting a reactant gas stream that includes CH 4 and CO 2 with the catalyst of claim 1 under dry reaction conditions to produce a product gas stream comprising H 2 and CO, wherein the reaction conditions include a temperature of 700° C. to 950° C., a pressure of 1 bara, and a gas hourly space velocity of 500 h −1 to 100,000 h −1 .

15. The method of claim 14 , wherein the gas hourly space velocity is 73,500 h −1 .

16. The method of claim 14 , wherein the temperature is 800° C.

17. A method of making the catalyst of claim 1 , the method comprising:
(a) obtaining a solution comprising a redox-metal salt and a salt of tin (Sn), niobium (Nb), lanthanum (La), bismuth (Bi), indium (In) or gallium (Ga), or any combination thereof solubilized in the solution, wherein the weight ratio of the redox-metal salt to the salt of the Sn, Nb, La, Bi, In or Ga, or any combination thereof present in the solution is at least 5:1;
(b) impregnating a metal oxide core, a clay core, or a zeolite core, with the solution to obtain an impregnated material;
(c) drying and calcining the impregnated material to obtain a core-shell structure having:
(i) a metal oxide core, a clay core, or a zeolite core; and
(ii) a shell surrounding the core, wherein the shell has a redox-metal oxide phase formed from the redox-metal salt and Sn, Nb, La, Bi, In or Ga, or any combination thereof formed from the salt thereof that is incorporated into the lattice framework of the redox-metal oxide phase; and

(d) depositing one or more active metals on the surface of the shell.

18. The method of claim 17 , wherein the impregnated material is dried at a temperature of 50 to 150° C. for 2 to 10 hours and calcined at a temperature of 500 to 800° C. for 2 to 4 hours.

19. A catalyst comprising a core-shell structure having:
a metal oxide core, a clay core, or a zeolite core;
a shell substantially surrounding the core, wherein the shell has a redox-metal oxide phase having tin (Sn), niobium (Nb), lanthanum (La), bismuth (Bi), indium (In) or gallium (Ga) or a combination thereof, incorporated into the lattice framework of the redox-metal oxide phase; and
an active metal deposited on the surface of the shell, wherein the redox-metal oxide phase is cerium oxide,
wherein the catalyst is capable of catalyzing the production of hydrogen (H 2 ) and carbon monoxide (CO) from methane (CH 4 ) and carbon dioxide (CO 2 ).

20. A method of making the catalyst of claim 19 , the method comprising:
(a) obtaining a solution comprising a redox-metal salt and a salt of tin (Sn), niobium (Nb), lanthanum (La), bismuth (Bi), indium (In) or gallium (Ga), solubilized in the solution, wherein the weight ratio of the redox-metal salt to the salt of the metal dopant present in the solution is at least 5:1;
(b) impregnating the metal oxide core, the clay core, or the zeolite core with the solution to obtain an impregnated material;
(c) drying and calcining the impregnated material to obtain the core-shell structure having:
(i) the metal oxide core, the clay core, or the zeolite core; and
(ii) the shell substantially surrounding the core, wherein the shell has the redox-metal oxide phase formed from the redox-metal salt and Sn, Nb, La, Bi, In or Ga, or any combination thereof formed from the salt thereof that is incorporated into the lattice framework of the redox-metal oxide phase; and

(d) depositing one or more active metals on the surface of the shell to obtain the catalyst.

Assignees

• Sabic Global Technologies Bv

Inventors

• D'Souza Lawrence
• Viswanath Vinu
• Scaranto Jessica
• Ravon Ugo

Classifications

• C01B2203/0227

  containing a catalytic reforming step · CPC title

• C01B2203/107

  Platinum catalysts · CPC title

• C01B2203/1058

  Nickel catalysts · CPC title

• C01B3/40

  characterised by the catalyst · CPC title

• B01J23/20

  Vanadium, niobium or tantalum · CPC title