Regenerable mixed copper-iron-inert support oxygen carriers for solid fuel chemical looping combustion process

Patent metadata

Field	Value
Publication number	US-9523499-B1
Application number	US-201113159553-A
Country	US
Kind code	B1
Filing date	Jun 14, 2011
Priority date	Jun 14, 2011
Publication date	Dec 20, 2016
Grant date	Dec 20, 2016

Abstract

The disclosure provides an oxygen carrier for a chemical looping cycle, such as the chemical looping combustion of solid carbonaceous fuels, such as coal, coke, coal and biomass char, and the like. The oxygen carrier is comprised of at least 24 weight % (wt %) CuO, at least 10 wt % Fe2O3, and an inert support, and is typically a calcine. The oxygen carrier exhibits a CuO crystalline structure and an absence of iron oxide crystalline structures under XRD crystallography, and provides an improved and sustained combustion reactivity in the temperature range of 600° C.-1000° C. particularly for solid fuels such as carbon and coal.

First claim

What is claimed is:

1. A method of delivering oxygen to a fuel reactor using an oxygen carrier comprising:
gathering an oxygen carrier, where the oxygen carrier is a solid-state solution having a solvent and a solute where CuO is the solvent and iron oxides are the solute, where the CuO rich copper-iron solid solution is comprised of at least 24 wt % copper and at least 10% of iron and prepared via a calcination process, and where the oxygen carrier has a CuO crystalline structure and an absence of an Fe203 crystalline structure after calcination and before reduction:
delivering the oxygen carrier to the fuel reactor, mixing a fuel and the oxygen carrier in the fuel reactor; and
maintaining the fuel reactor at a reducing temperature, where the reducing temperature is sufficient to reduce at least some portion of the oxygen carrier and oxidize at least some portion of the fuel, thereby producing a reduced carrier, thereby delivering oxygen to the fuel reactor using the oxygen carrier.

2. The method of claim 1 where the fuel is a solid carbonaceous fuel and further comprising:
generating contact between the fuel and a gasification gas in the fuel reactor; and
maintaining the fuel reactor at the reducing temperature, where the reducing temperature is further sufficient to oxidize carbon comprising the fuel when the fuel contacts the gasification gas.

3. The method of claim 1 where the oxygen carrier comprises at least 40 wt % CuO and at least 20 wt % Fe 2 O 3 .

4. The method of claim 3 where the inert support comprises alumina, bentonite, or combinations thereof, and where the inert support comprises less than 40 wt % of the oxygen carrier.

5. The method of claim 1 further comprising:
transferring the reduced carrier from the fuel reactor to an oxidizing reactor; providing an oxidizing gas to the oxidizing reactor, where the oxidizing gas comprises oxygen; and
oxidizing the reduced carrier by contacting the reduced carrier and some portion of the oxygen comprising the oxidizing gas and generating a re-oxidized carrier where the re-oxidized carrier is the solid-state solution where CuO is the solvent and iron oxides are the solute, and where the oxygen carrier has the CuO crystalline structure and the absence of the Fe 2 O 3 crystalline structure.

6. The method of claim 5 further comprising: withdrawing an exhaust stream from the fuel reactor, where the exhaust stream comprises CO 2 and H 2 0; discharging an oxidation stream from the oxidizing reactor, where the oxidation stream is comprised of the oxidizing gas less the some portion of the oxygen comprising the oxidizing gas; retrieving the re-oxidized carrier from the oxidizing reactor, thereby gathering the oxygen carrier; and repeating the delivering the oxygen carrier to the fuel reactor, the mixing the fuel and the oxygen carrier in the fuel reactor, the maintaining the fuel reactor at the reducing temperature, the transferring the reduced carrier from the fuel reactor to the oxidizing reactor, the providing the oxidizing gas to the oxidizing reactor, the oxidizing the reduced carrier, the withdrawing the exhaust stream from the fuel reactor, the discharging the oxidation stream from the oxidizing reactor, and the retrieving the re-oxidized carrier from the oxidizing reactor utilizing a second portion of fuel as the fuel and the re-oxidized carrier as the oxygen carrier.

7. A method of conducting a chemical looping process using an oxygen earner comprising:
gathering an oxygen carrier, where the oxygen carrier is a CuO-rich copper-iron solid solution on an inert support where the CuO-rich copper-iron solid solution is a solid-state solution having a solvent and a solute where CuO is the solvent and iron oxides are the solute, where the CuO rich copper-iron solid solution is comprised of at least 24 wt % copper and at least 10% of iron and prepared via a calcination process, and where the CuO-rich copper-iron solid solution is a material characterized by an X-ray diffraction pattern indicating a presence of a CuO crystalline structure and an absence of iron oxide crystalline structures after calcination and before reduction;
delivering the oxygen carrier to the fuel reactor;
mixing a fuel and the oxygen carrier in the fuel reactor;
combusting the fuel by maintaining the fuel reactor at a reducing temperature of from about 600° C. to about 1000° C. where the reducing temperature is sufficient to reduce at least some portion of the oxygen carrier, thereby producing a reduced carrier, and where the reducing temperature is further sufficient to oxidize at least some portion of the fuel, generating C02 and H20;
transferring the reduced carrier from the fuel reactor to an oxidizing reactor;
supplying an oxidant gas to the oxidizing reactor, where the oxidizing gas is comprised of oxygen;
oxidizing the reduced carrier by contacting the reduced carrier and some portion of the oxygen comprising the oxidizing gas and generating a re-oxidized carrier where the re-oxidized carrier is a second CuO-rich copper-iron solid solution on the inert support;
retrieving the re-oxidized carrier from the oxidizing reactor, thereby gathering the oxygen carrier; and
transporting the re-oxidized carrier from the oxidizing reactor to the fuel reactor, and repeating the delivering the oxygen carrier to the fuel reactor, the mixing the fuel and the oxygen carrier in the fuel reactor, the combusting the fuel, the transferring the reduced carrier from the fuel reactor to the oxidizing reactor, the supplying the oxidant gas to the oxidizing reactor, the oxidizing the reduced carrier, and the retrieving the re-oxidized carrier from the oxidizing reactor utilizing a second portion of fuel as the fuel and the re-oxidized carrier as the oxygen carrier,
thereby conducting the chemical looping process using the oxygen carrier.

8. The method of claim 7 where the fuel is a solid carbonaceous fuel and further comprising: generating contact between the solid carbonaceous fuel and a gasification gas in the fuel reactor; and maintaining the fuel reactor at the reducing temperature, where the reducing temperature is further sufficient to oxidize carbon comprising the solid carbonaceous fuel when the fuel contacts the gasification gas.

9. The method of claim 3 where the oxygen carrier comprises greater than 40 wt % CuO and less than or equal to 40 wt % Fe 2 0 3 .

10. The method of claim 7 where the X-ray diffraction pattern of the oxygen carrier indicates the presence of the CuO crystalline structure and the absence of the Fe 2 0 3 crystalline structure using Cu KR-1 radiation.

11. The method of claim 1 where the reducing temperature is greater than or equal to 600° C. and less than or equal to 1000° C.

12. The method of claim 11 further comprising: transferring the reduced carrier from the fuel reactor to an oxidizing reactor; providing an oxidizing gas to the oxidizing reactor, where the oxidizing gas comprises oxygen; and oxidizing the reduced carrier by contacting the reduced carrier and some portion of the oxygen comprising the oxidizing gas and generating a re-oxidized carrier where the re-oxidized carrier is the solid-state solution where CuO is the solvent and iron oxides are the solute, and where the oxygen carrier has the CuO crystalline structure and the absence of the Fe 2 0 3 crystalline structure; retrieving the re-oxidized carrier from the oxidizing reactor, thereby gathering the oxygen carrier; and transporting the re-oxidized carrier from the oxidizing reactor to the fuel reactor and repeating the delivering the oxygen carrier to the fuel reactor, the mixing the fuel and the oxygen carrier in the fuel reactor, the maintaining the fuel r

Assignees

• Siriwardane Ranjani V
• Tian Hanjing
• Us Dept Energy

Inventors

• Siriwardane Ranjani V
• Tian Hanjing

Classifications

• F23D14/22 Primary

  with separate air and gas feed ducts, e.g. with ducts running parallel or crossing each other · CPC title

• F23D14/32

  using a mixture of gaseous fuel and pure oxygen or oxygen-enriched air (F23D14/38 takes precedence) · CPC title

• Y02E20/344

  Cross-Sectional Technologies · mapped topic

• F23C99/00 Primary

  Subject-matter not provided for in other groups of this subclass · CPC title

• Y02E20/34

  Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery · CPC title