Reduction catalyst, and chemical reactor, reduction method and reduction product-producing system employing the catalyst
US-2018209053-A1 · Jul 26, 2018 · US
US11998900B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11998900-B2 |
| Application number | US-202217863719-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 13, 2022 |
| Priority date | Jul 13, 2022 |
| Publication date | Jun 4, 2024 |
| Grant date | Jun 4, 2024 |
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A method of immobilizing a metal catalyst in a porous support includes additively forming a precursor structure on a substrate from a metal catalyst and at least one of a metal oxide or a metal cluster compound; exposing the precursor structure to a vapor of an organic linker; and reacting the at least one of the metal oxide or the metal cluster compound in the precursor structure with the organic linker to form a porous support that immobilizes the metal catalyst.
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What is claimed is: 1. A method of immobilizing a metal catalyst in a porous support, the method comprising: additively forming a precursor structure on a substrate from a metal catalyst and at least one of metal oxides or metal cluster compounds; exposing the precursor structure to a vapor of an organic linker; and reacting the at least one of the metal oxide or the metal cluster compound in the precursor structure with the organic linker to form a porous support that immobilizes the metal catalyst. 2. The method of claim 1 , comprising additively forming the precursor structure via an aerosol jetting process, a binder jetting process, or a material jetting process. 3. The method of claim 1 , wherein the metal catalyst comprises nanoparticles of a precious metal catalyst. 4. The method of claim 1 , wherein the metal catalyst comprises at least one of gold, silver, ruthenium, rhodium, palladium, osmium, iridium, platinum, chromium, tungsten, molybdenum, iron, or cobalt. 5. The method of claim 1 , wherein the metal catalyst has an average particle size of about 1 nm to about 20 nm. 6. The method of claim 1 , wherein the metal catalyst is present in an amount of about 1 to about 5% based on a total weight of the porous support. 7. The method of claim 1 , wherein the precursor structure is formed from the metal catalyst and the metal oxide, and the metal oxide comprises at least one of zinc oxide, aluminum oxide, magnesium oxide, iron oxide, cobalt oxide, nickel oxide, copper oxide, calcium oxide, barium oxide, cerium oxide, manganese oxide, gallium oxide, cadmium oxide, titanium oxide, zirconium oxide, or magnesium aluminum oxide. 8. The method of claim 1 , wherein the precursor structure is formed from the metal catalyst and the metal cluster compound, and the metal cluster compound comprises at least one of a titanium-based cluster compound or a zirconium-based cluster compound. 9. The method of claim 1 , wherein the metal oxide and the metal cluster compound have an average particle size of about 10 nm to about 100 μm. 10. The method of claim 1 , wherein the precursor structure comprises the metal catalyst disposed in a matrix formed from at least one of the metal oxide or the metal cluster compound, and the matrix has pores with a pore size of about 200 nm to about 1 mm. 11. The method of claim 1 , further comprising controlling the pore size of the matrix by dispensing a porous particle as a dispersed phase through one deposition head and dispensing the metal catalyst and at least one of the metal oxide or the metal cluster compound through another deposition head. 12. The method of claim 1 , further comprising statistically characterizing pores' variability within an additive manufacturing process and dependency on additive manufacturing parameters, and stochastically or parametrically optimizing the additive manufacturing parameters to provide a selected pore size, morphology, distribution, or a combination thereof of the precursor structure. 13. The method of claim 1 , wherein the organic linker comprises at least one of a carboxylate or an imidazolate. 14. The method of claim 1 , wherein the substrate is an electrode or an internal packing material. 15. The method of claim 1 , comprising reacting the at least one of the metal oxide or the metal cluster compound in the precursor structure with the organic linker at a temperature of about 80° C. to about 100° C. to form the porous support. 16. The method of claim 1 , comprising reacting the at least one of the metal oxide or the metal cluster compound in the precursor structure with the organic linker at a pressure of about 0.001 bar to about 1 bar to form the porous support. 17. The method of claim 1 , wherein the additively forming, the exposing, and the reacting occur in a single reactor chamber. 18. The method of claim 1 , further comprising exposing the porous support to a temperature of about 120° C. to about 150° C. at a subatmospheric pressure of about 0.0001 bar to about 0.001 bar to activate the porous support. 19. The method of claim 1 , wherein the porous support is a metal-organic framework, and the metal-organic framework is a crystalline network comprising inorganic nodes linked by organic moieties, the inorganic nodes formed from the at least one of the metal oxide or the metal cluster compound, and the organic moieties formed from the organic linker. 20. The method of claim 19 , wherein the porous support comprises pores having a pore size of about 5 to about 20 angstroms; and at least a portion of the metal catalyst is disposed in the pores. 21. The method of claim 1 , wherein the porous support has a multimodal pore size distribution comprising first pore sizes from about 5 to about 20 angstroms, attributed to intrinsic porosity of the porous support, second pore sizes from about 1 nm to about 200 nm, and third pore sizes from about 200 nm to about 1 mm. 22. The method of claim 1 , wherein the porous support is discontinuous and has a predetermined pattern. 23. The method of claim 1 , wherein the porous support has a first portion and a second portion, and the first portion and the second portion have at least one of a different thickness; a different shape; a different metal catalyst; or a porous support. 24. The method of claim 1 , comprising: additively forming the precursor structure on the substrate via an aerosol jetting process, a binder jetting process, or a material jetting process from the metal catalyst and at least one of the metal oxides or the metal cluster compounds in a reactor chamber equipped with a heater, the metal catalyst comprising nanoparticles of a precious metal; introducing the vapor of the organic linker into the reactor chamber; exposing the precursor structure to the vapor of the organic linker in the reactor chamber; reacting the at least one of the metal oxide or the metal cluster compound in the precursor structure with the organic linker in the reactor chamber at a temperature of about 80° C. to about 100° C. to form the porous support; and exposing the porous support to a temperature of about 120° C. to about 150° C. at a subatmospheric pressure of about 0.0001 bar to about 0.001 bar to activate the porous support forming a supported catalyst, the supported catalyst comprising a metal-organic framework having pores with a pore size of from about 5 to about 20 angstroms and at least a portion of the metal catalyst disposed in the pores.
Nanoparticles · CPC title
characterised by their shape or configuration · CPC title
Deposition of compounds, mixtures or solid solutions, e.g. borides, carbides, nitrides · CPC title
Coating cavities or hollow spaces, e.g. interior of tubes; Infiltration of porous substrates · CPC title
immobilised by covalent linkages, i.e. pendant complexes with optional linking groups · CPC title
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