Metal ferrite oxygen carriers for conversion of CO2 to CO and fuel to syngas or CO

Patent metadata

Field	Value
Publication number	US-10864501-B2
Application number	US-201916550747-A
Country	US
Kind code	B2
Filing date	Aug 26, 2019
Priority date	May 19, 2017
Publication date	Dec 15, 2020
Grant date	Dec 15, 2020

Abstract

The invention provides a use of metal ferrite oxygen carrier for converting carbon dioxide to carbon monoxide or synthesis gas via three processes: catalytic dry reforming of methane, chemical looping dry reforming of fuel and promoting coal gasification with CO2. The metal ferrite oxygen carrier comprises MzFexOy, where MzFexOy is a chemical composition with 0<x≤4, z>0 and 0<y≤6 and M is one of Ca, Ba, and/or combinations thereof. For example, MzFexOy may be one of CaFe2O4, BaFe2O4, MgFe2O4, SrFe2O4 and/or combinations thereof. In catalytic dry reforming, methane and carbon dioxide react in the presence of metal ferrites generating a product stream comprising at least 50 vol. % CO and H2. In another embodiment, chemical looping dry reforming process where metal ferrite is reduced with a fuel and then oxidized with carbon dioxide is used for production of CO from carbon dioxide. In another embodiment, the metal ferrite is used as a promoter to produce CO continuously from coal gasification with CO2.

First claim

What is claimed is:

1. A method for chemical looping dry reforming of methane comprising:
delivering a metal ferrite oxygen carrier comprising MzFexOy to a fuel reactor, where 0<x≤4, z>0 and 0<y≤6, and where M is at least one of Mg, Ca, Ba, Sr or combinations thereof;
delivering a fuel stream to the metal 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 metal ferrite oxygen carrier and oxidize some portion of the fuel stream, and generating gaseous products containing H2, CO or CO2 gas in the fuel reactor;
delivering the reduced metal ferrite to an oxidation reactor;
oxidizing the reduced carrier by contacting the reduced carrier and carbon dioxide at an oxidizing temperature, where the oxidizing temperature is sufficient to generate an oxidizing reaction, where reactants of the oxidizing reaction comprise some portion of the carbon dioxide, some portion of the M component, and some portion of a FecOd component, where c>0 and d≥0 and where a product of the oxidizing reaction is CO and a re-oxidized carrier, where the re-oxidized carrier comprises some portion of the MzFexOy; and
withdrawing a product stream CO from the oxidation reactor, where the gaseous products comprise the product stream, and where at least >50 vol. % of the product stream consists of CO.

2. The method of claim 1 where the reducing temperature ranges from about 500° C. to about 1100° C.

3. The method of claim 1 where 2>z>0, 2≤x≤3 and 3≤y≤5.

4. The method of claim 1 where the MzFexOy comprises at least 30 wt. % of the metal ferrite oxygen carrier.

5. The method of claim 1 where the metal ferrite oxygen carrier further comprises an inert support, where the inert support comprises from about 5 wt. % to about 70 wt. % of the metal ferrite oxygen carrier.

6. The method of claim 1 wherein the inert support contains at least one of alumina, silica, zirconia, clay, titania, monolith or combinations thereof.

7. The method of claim 1 where the mixing the fuel stream and the metal ferrite oxygen carrier in the fuel reactor step generates a reduced carrier, where the reduced carrier comprises an M component and an FecOd component, where the M component comprises some portion of the M comprising the MzFexOy, and MO and where the FecOd component comprises some portion of the Fe comprising the MzFexOy, where c>0 and d≥0.

8. The method of claim 7 where the FecOd component comprises Fe 0 , FeO, Fe3O4 or Fe2O3 and M component comprises MO or MCO3.

9. The method in claim 1 where the fuel in the fuel reactor is coal, methane or bio mass.

10. The method of claim 9 wherein the methane concentration may be greater than 5 vol %.

11. The method of claim 1 wherein oxidization of 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 carbon dioxide containing gas stream to the oxidizing reactor, thereby
generating the re-oxidized carrier, producing carbon monoxide;
transferring the re-oxidized carrier from the oxidizing reactor to the fuel reactor; and
repeating the delivering the metal ferrite oxygen carrier to the fuel reactor, introducing methane or coal to the metal ferrite oxygen carrier in the fuel reactor, and the withdrawing the product stream from both the fuel reactor and the oxidizing reactor.

12. The method of claim 11 where the oxidizing temperature ranges from about 500° C. to about 1100° C.

13. The method of claim 11 wherein the carbon dioxide gas stream may be provided by carbon dioxide separated from fuel combustion streams with air or fuel chemical looping combustion streams.

Assignees

• Us Energy
• Us Dept Energy

Inventors

• Siriwardane Ranjani V

Classifications

• Y02P20/52

  using catalysts, e.g. selective catalysts · CPC title

• C01B3/42 Primary

  using moving solid particles, e.g. fluidised bed technique · CPC title

• C01B2203/0238

  the reforming step being a carbon dioxide reforming step · CPC title

• C01B2203/1047

  Group VIII metal catalysts · CPC title

• C01B2203/066

  with fuel cells · CPC title