Porous catalyst and method of use for the tandem capture and conversion of carbon dioxide to hydrocarbons

Patent metadata

Field	Value
Publication number	US-2024316539-A1
Application number	US-202418611817-A
Country	US
Kind code	A1
Filing date	Mar 21, 2024
Priority date	Mar 22, 2023
Publication date	Sep 26, 2024
Grant date	—

Abstract

A porous catalyst useful in the conversion of carbon dioxide to one or more hydrocarbons, the porous catalyst containing: (i) a bimetallic oxide portion containing at least one of iron oxide and nickel oxide or carbide in combination with at least one oxide, hydroxide, and/or carbide of at least one of manganese, cobalt, copper, yttrium, zirconium, niobium, hafnium, zinc, and lanthanides; and (ii) an alkali metal oxide, hydroxide, or carbonate portion in contact with the bimetallic oxide portion; wherein the porous catalyst contains pores in the bimetallic oxide portion. A method of using the porous catalyst to convert carbon dioxide to hydrocarbons, particularly olefins, containing at least four carbon atoms, is also described.

First claim

What is claimed is:

1 . A porous catalyst useful in the conversion of carbon dioxide to one or more hydrocarbons, the porous catalyst comprising:
(i) a bimetallic oxide portion comprising at least one of iron oxide and nickel oxide in combination with at least one oxide, hydroxide, and/or carbide of at least one of manganese, cobalt, copper, yttrium, zirconium, niobium, hafnium, zinc, and lanthanides; and (ii) an alkali metal oxide, hydroxide, or carbonate portion in contact with the bimetallic oxide portion; wherein the porous catalyst contains pores in the bimetallic oxide portion.

2 . The porous catalyst of claim 1 , wherein at least 90 vol % of the pores have a size within a range of 0.5-2.5 nm.

3 . The porous catalyst of claim 1 , wherein the bimetallic oxide portion comprises at least one of iron oxide and nickel oxide in combination with at least one oxide, hydroxide, and/or carbide of at least one of copper, cobalt, manganese, and zirconium.

4 . The porous catalyst of claim 1 , wherein the bimetallic oxide portion comprises iron oxide in combination with at least one oxide, hydroxide, and/or carbide of at least one of manganese, cobalt, copper, yttrium, zirconium, niobium, hafnium, zinc, and lanthanides.

5 . The porous catalyst of claim 1 , wherein the bimetallic oxide portion comprises iron oxide in combination with at least one oxide, hydroxide, and/or carbide of at least one of copper, cobalt, manganese, and zirconium.

6 . The porous catalyst of claim 1 , wherein the porous catalyst is comprised of particles having a core-shell arrangement in which the core comprises said bimetallic oxide portion and the shell comprises said alkali metal oxide, hydroxide, or carbonate portion.

7 . The porous catalyst of claim 6 , wherein at least 90% of the particles have a particle size in a range of 50-200 nm.

8 . The porous catalyst of claim 1 , wherein the porous catalyst comprises a first layer containing said bimetallic oxide portion and a second layer containing said alkali metal oxide, hydroxide, or carbonate portion, wherein said second layer is in contact with said first layer, and said second layer is uncoated and in free contact with its gaseous environment.

9 . A method of converting carbon dioxide to one or more hydrocarbons at least a portion of which contain four carbon atoms, the method comprising contacting carbon dioxide (CO 2 ) and hydrogen (H 2 ) gases with a porous catalyst at a temperature of 100-800° C. at a pressure of 1-20 atm to result in conversion of the carbon dioxide to said one or more hydrocarbons, wherein the porous catalyst comprises:
(i) a bimetallic oxide portion comprising at least one of iron oxide and nickel oxide in combination with at least one oxide, hydroxide, and/or carbide of at least one of manganese, cobalt, copper, yttrium, zirconium, niobium, hafnium, zinc, and lanthanides; and
(ii) an alkali metal oxide, hydroxide, or carbonate portion in contact with the bimetallic oxide portion;
wherein the porous catalyst contains pores in the bimetallic oxide portion.

10 . The method of claim 9 , wherein at least 50 vol % of said hydrocarbons contain at least four carbon atoms.

11 . The method of claim 9 , wherein at least 60 vol % of said hydrocarbons contain at least four carbon atoms.

12 . The method of claim 9 , wherein at least 70 vol % of said hydrocarbons contain at least four carbon atoms.

13 . The method of claim 9 , wherein at least 80 vol % of said hydrocarbons contain at least four carbon atoms.

14 . The method of claim 9 , wherein at least a portion of said hydrocarbons are olefins containing at least four carbon atoms.

15 . The method of claim 9 , wherein at least 50 vol % of said hydrocarbons are olefins containing at least four carbon atoms.

16 . The method of claim 9 , wherein the bimetallic oxide portion of the porous catalyst comprises at least one of iron oxide and nickel oxide in combination with at least one oxide, hydroxide, and/or carbide of at least one of copper, cobalt, manganese, and zirconium.

17 . The method of claim 9 , wherein the bimetallic oxide portion of the porous catalyst comprises iron oxide in combination with at least one oxide, hydroxide, and/or carbide of at least one of manganese, cobalt, copper, yttrium, zirconium, niobium, hafnium, zinc, and lanthanides.

18 . The method of claim 9 , wherein the bimetallic oxide portion of the porous catalyst comprises iron oxide in combination with at least one oxide, hydroxide, and/or carbide of at least one of copper, cobalt, manganese, and zirconium.

19 . The method of claim 9 , wherein the porous catalyst is comprised of particles having a core-shell arrangement in which the core comprises said bimetallic oxide portion and the shell comprises said alkali metal oxide, hydroxide, or carbide portion.

20 . The method of claim 9 , wherein the porous catalyst comprises a first layer containing said bimetallic oxide portion and a second layer containing said alkali metal oxide, hydroxide, or carbonate portion, wherein said second layer is in contact with said first layer, and said second layer is uncoated and in free contact with its gaseous environment.

Assignees

• Ut Battelle Llc

Inventors

• Kidder Michelle K

Classifications

• C10G2/332

  of the iron-group · CPC title

• C10G2/50

  from carbon dioxide with hydrogen · CPC title

• C07C2523/889

  Manganese, technetium or rhenium · CPC title

• C07C2523/04

  Alkali metals · CPC title

• C07C1/12

  from carbon dioxide with hydrogen · CPC title