Tri-metallic ferrite oxygen carriers for chemical looping combustion

Patent metadata

Field	Value
Publication number	US-9797594-B1
Application number	US-201514633175-A
Country	US
Kind code	B1
Filing date	Feb 27, 2015
Priority date	Sep 20, 2013
Publication date	Oct 24, 2017
Grant date	Oct 24, 2017

Abstract

The disclosure provides a tri-metallic ferrite oxygen carrier for the chemical looping combustion of carbonaceous fuels. The tri-metallic ferrite oxygen carrier comprises Cu x Fe y Mn z O 4-δ , where Cu x Fe y Mn z O 4-δ is a chemical composition. Generally, 0.5≦x≦2.0, 0.2≦y≦2.5, and 0.2≦z≦2.5, and in some embodiments, 0.8≦x≦1.2, y≦1.2, and z≧0.8. The tri-metallic ferrite oxygen carrier may be used in various applications for the combustion of carbonaceous fuels, including as an oxygen carrier for chemical looping combustion.

First claim

The invention claimed is:

1. A method of combusting a carbonaceous fuel comprising:
delivering a tri-metallic ferrite oxygen carrier to a fuel reactor, where the tri-metallic ferrite oxygen carrier comprise Cu x Fe y Mn z O 4-δ , where −0.5≦δ≦0.5, and where 0.5≦x≦2.0, 0.2≦y≦2.5, 0.2≦z≦2.5;
mixing the carbonaceous fuel and the tri-metallic ferrite oxygen carrier in the fuel reactor and maintaining the fuel reactor at a reducing temperature, where the reducing temperature is sufficient to reduce some portion of the tri-metallic ferrite oxygen carrier and oxidize some portion of carbonaceous fuel, thereby combusting the carbonaceous fuel.

2. The method of claim 1 where the reducing temperature is from about 600° C. to about 1200° C.

3. The method of claim 2 where the tri-metallic ferrite oxygen carrier comprises an inert support and the inert support comprises from about 5 wt. % to about 60 wt. % of the tri-metallic ferrite oxygen carrier and the Cu x Fe y Mn z O 4-δ comprises at least 30 wt. % of the oxygen, combined with the inert support.

4. The method of claim 3 where 0.8≦x≦1.2, y≦1.2, and z≧0.8.

5. The method of claim 3 where the inert support comprises alumina.

6. The method of claim 1 where the carbonaceous fuel is a gaseous carbonaceous fuel.

7. The method of claim 1 where the carbonaceous fuel is a solid carbonaceous fuel.

8. The method of claim 7 further comprising injecting a gasification agent into the fuel reactor.

9. The method of claim 1 where the tri-metallic ferrite oxygen is Cu x Fe y Mn z O 4-δ an oxide compound where the oxide compound is a chemical compound of copper, iron, and manganese as cations and oxygen as an anion.

10. The method of claim 9 where the mixing carbonaceous fuel and the tri-metallic ferrite oxygen carrier in the fuel reactor generates a reduced carrier, and further comprising oxidizing the reduced carrier by contacting the reduced carrier and an oxidizing gas at an oxidizing temperature, where the oxidizing gas is comprises of oxygen, and where the oxidizing temperature is sufficient to generate an oxidizing reaction, where the reactants of the oxidizing reaction comprise some portion of the oxygen and some portion of the reduced carrier, and where the product of the oxidizing reaction is a re-Oxidized carrier, where the re-oxidized carrier comprises the oxide compound.

11. The method of claim 10 where the oxidizing temperature is from about 600° C. to about 1200° C.

12. The method of claim 11 where oxidizing the reduced carrier occurs in an oxidizing reactor, and further comprising:
transferring the reduced carrier from the fuel reactor to the oxidizing reactor;
supplying the oxidizing gas to the oxidizing reactor, thereby generating the re-oxidized carrier;
transferring the re-oxidized carrier from the oxidizing reactor to the fuel reactor; and
repeating the delivering step and the contacting step utilizing an additional quantity of the carbonaceous fuel as the carbonaceous fuel and the re-oxidized carrier as the tri-metallic ferrite oxygen carrier.

13. A method of combusting a carbonaceous fuel comprising:
delivering a tri-metallic ferrite oxygen carrier to a fuel reactor, where the tri-metallic ferrite oxygen carrier comprise Cu x Fe y Mn z O 4-δ , and where 0.2<x<2.5, 0.2<y<2.5, 0.2<z<2.5, and −0.5≦δ≦0.5;
mixing the carbonaceous fuel and the tri-metallic ferrite oxygen carrier in the fuel reactor and maintaining the fuel reactor at a reducing temperature of about 600° C. to about 1200° C. and generating a reduced carrier, thereby combusting the solid carbonaceous fuel;
transferring the reduced carrier from the fuel reactor to an oxidizing reactor;
oxidizing the reduced carrier by supplying an oxidizing gas to the oxidizing reactor, where the oxidizing gas at an oxidizing temperature from about 600° C. to about 1200° C. and generating an oxidizing reaction, where the reactants of the oxidizing reaction comprises some portion of the oxygen and some portion of the reduced carrier, and where the product of the oxidizing reaction is a re-oxidized carrier, where the re-oxidized carrier comprises Cu x Fe y Mn z O 4-δ ; and
transporting the re-oxidized carrier from the oxidizing reactor to the fuel reactor; and
repeating the delivery step, the mixing step, the transferring step, and the oxidizing step utilizing an additional quantity of the carbonaceous fuel as the carbonaceous fuel and the re-oxidized carrier as the tri-metallic ferrite oxygen carrier.

14. The method of claim 13 where 0.8≦x≦1.2, y≦1.2, and z≧0.8.

15. The method of claim 14 where the tri-metallic ferrite oxygen carrier comprises an inert support and the inert support comprises from about 5 wt. % to about 60 wt. % of the tri-metallic ferrite oxygen carrier and the Cu x Fe y Mn z O 4-δ comprises at least 30 wt. % of the oxygen carrier combined with the inert support.

Assignees

• Siriwardane Ranjani V
• Fan Yueying
• Us Dept Energy

Inventors

• Siriwardane Ranjani V
• Fan Yueying

Classifications

• F23C13/08 Primary

  characterised by the catalytic material · CPC title

• F23C10/01

  in a fluidised bed of catalytic particles · CPC title

• F23C10/02

  with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed · CPC title

• F23C10/20

  Inlets for fluidisation air, e.g. grids; Bottoms · CPC title

• B01J35/40

  characterised by dimensions, e.g. grain size (in a colloidal state B01J35/23; crystallite size B01J35/77) · CPC title