Oxygen carrying materials
US-9777920-B2 · Oct 3, 2017 · US
US12350651B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12350651-B2 |
| Application number | US-202017636160-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 19, 2020 |
| Priority date | Aug 19, 2019 |
| Publication date | Jul 8, 2025 |
| Grant date | Jul 8, 2025 |
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Exemplary oxygen carrier particles may comprise a mesoporous support and a plurality of metal oxide-based nanoparticles immobilized on the mesoporous support. The plurality of metal oxide-based nanoparticles may comprise 10 volume percent to 80 volume percent of mesopores in the mesoporous support. A reactor may comprise a feedstock inlet in fluid communication with a carbonaceous feedstock source, a product stream outlet, and oxygen carrier particles. Exemplary reactors may be operated by providing a carbonaceous feedstock to an inlet of the reactor, providing oxygen carrier particles within the reactor, and collecting a product stream from an outlet of the reactor.
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We claim: 1. An oxygen carrier, comprising: a mesoporous silica support; and a plurality of iron oxide-based nanoparticles immobilized on the mesoporous silica support, wherein the plurality of iron oxide-based nanoparticles comprise 20 volume percent to 70 volume percent of mesopores in the mesoporous silica support; wherein the plurality of iron oxide-based nanoparticles further comprise a dopant selected from: cobalt (Co), nickel (Ni), and copper (Cu). 2. The oxygen carrier according to claim 1 , wherein the plurality of iron oxide-based nanoparticles include Fe 2 O 3 . 3. The oxygen carrier according to claim 2 , wherein each of the plurality of iron oxide-based nanoparticles comprise 22 weight percent to 86 weight percent of the mesoporous silica support. 4. The oxygen carrier according to claim 1 , wherein the mesoporous silica support is Santa Barbara Amorphous-15 silica (SBA-15), Santa Barbara Amorphous-16 silica (SBA-16), mesoporous silica MCM-41, or mesoporous silica MCM-48. 5. The oxygen carrier according to claim 1 , wherein a portion of the plurality of iron oxide-based nanoparticles is immobilized on a first type of mesoporous silica support; wherein a remainder portion of the plurality of iron oxide-based nanoparticles is immobilized on a second type of mesoporous silica support, the second type of mesoporous silica support being different from the first type of mesoporous silica support. 6. The oxygen carrier according to claim 1 , wherein the iron oxide-based nanoparticles have an average diameter of 2 nm to 50 nm; wherein the mesoporous silica support has an average diameter of about 1 μm to about 4 μm; and wherein the mesoporous silica support has an average pore diameter of about 2 nm to about 50 nm. 7. The oxygen carrier according to claim 1 , wherein a dopant concentration is 0.5 atomic percent (at %) to 15 at %. 8. The oxygen carrier according to claim 7 , wherein the dopant is copper. 9. A method of operating a reactor, the method comprising: providing a carbonaceous feedstock to an inlet of the reactor; providing oxygen carrier particles within the reactor, wherein each of the oxygen carrier particles comprises the oxygen carrier of claim 1 ; and collecting a product stream from an outlet of the reactor, the product stream including at least one of: H 2 , carbon monoxide (CO), and C 2+ hydrocarbon. 10. The method according to claim 9 , further comprising arranging the reactor as a fixed bed, a moving bed, or a fluidized bed, wherein the carbonaceous feedstock includes at least one of methane (CH 4 ), coal, carbon monoxide (CO), and carbon dioxide (CO 2 ). 11. The method according to claim 9 , further comprising: after collecting the product stream, providing an oxidizing agent to the inlet of the reactor; and collecting a second product stream from the outlet of the reactor, the second product stream including carbon monoxide (CO). 12. The method according to claim 9 , wherein the plurality of iron oxide-based nanoparticles include Fe 2 O 3 , ferrite, or combinations thereof; and wherein the mesoporous silica support is mesoporous silica SBA-15, mesoporous silica SBA-16, or mesoporous silica MCM-41. 13. The method according to claim 9 , wherein the iron oxide-based nanoparticles further comprise a dopant selected from: Co, Ni, and Cu. 14. The method according to claim 9 , wherein a carbonaceous feedstock conversion rate is greater than 95%. 15. A reactor, comprising: a feedstock inlet in fluid communication with a carbonaceous feedstock source; a product stream outlet; and oxygen carrier particles, wherein each of the oxygen carrier particles comprises the oxygen carrier of claim 1 . 16. The reactor according to claim 15 , wherein the plurality of iron oxide-based nanoparticles include Fe 2 O 3 , ferrite, or combinations thereof; wherein the iron oxide-based nanoparticles have an average diameter of 2 nm to 10 nm; wherein the mesoporous silica support has an average diameter of about 1 μm to about 4 μm; and wherein the mesoporous silica support has an average pore diameter of about 6 nm to about 11 nm.
using moving solid particles, e.g. fluidised bed technique · CPC title
in a colloidal state · CPC title
Nanoparticles · CPC title
X-ray diffraction · CPC title
Scanning electron microscopy; Transmission electron microscopy · CPC title
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