Method for making nanowire structure
US-9840773-B2 · Dec 12, 2017 · US
US2021246045A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2021246045-A1 |
| Application number | US-201716341825-A |
| Country | US |
| Kind code | A1 |
| Filing date | Oct 19, 2017 |
| Priority date | Oct 19, 2016 |
| Publication date | Aug 12, 2021 |
| Grant date | — |
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A process for gas-phase synthesis of titanium dioxide aerosol gels with controlled monomer size and crystalline phase using a diffusion flame aerosol reactor operated in a buoyancy-opposed configuration is disclosed. The process includes introducing a precursor stream into a diffusion flame aerosol reactor, introducing a fuel stream into the reactor, combusting the precursor stream and the fuel stream in a flame to form at least one nanoparticle, and operating the reactor in a down-fired buoyancy-opposed configuration to produce the aerosol gel.
Opening claim text (preview).
What is claimed is: 1 . A process for the synthesis of an aerosol gel, the process comprising: introducing a precursor stream into a diffusion flame aerosol reactor; introducing a fuel stream into the reactor; combusting the precursor stream and the fuel stream in a flame to form at least one nanoparticle; and, operating the reactor in a down-fired buoyancy-opposed configuration to produce the aerosol gel. 2 . The process of claim 1 , wherein the precursor stream comprises a metal precursor. 3 . The process of claim 2 , wherein the metal precursor comprises TTIP. 4 . The process of claim 1 , wherein the fuel stream comprises at least one of methane and oxygen. 5 . An aerosol gel produced by a diffusion flame aerosol reactor, wherein the reactor includes a precursor stream, a fuel stream, and operates in a down-fired buoyancy-opposed configuration to produce the gel. 6 . The gel of claim 5 , wherein the precursor stream comprises a metal precursor. 7 . The gel of claim 6 , wherein the metal precursor comprises TTIP. 8 . The gel of claim 5 , wherein the fuel stream comprises at least one of methane and oxygen. 9 . The gel process of claim 5 , wherein the gel has an uncrushed density of from about 0.010 g/cm 3 to about 0.030 g/cm 3 . 10 . The gel of claim 5 , wherein the gel has a crushed density of from about 0.500 g/cm 3 to about 1.50 g/cm 3 . 11 . A process for synthesizing an aerosol gel comprising aggregates, the process comprising: diffusion-limiting cluster aggregating (DLCA) of at least one nanoparticle to produce an aggregate of nanoparticles; percolating the aggregate of nanoparticles to create a percolate of the aggregated nanoparticles; and, DLCA of the percolate of aggregated nanoparticles to create an aerosol gel comprising aggregates. 12 . The process of claim 11 , wherein the synthesizing of the aerosol gel comprising aggregates occurs in a diffusion flame aerosol reactor. 13 . The process of claim 12 , wherein the reactor operates in a down-fired buoyancy-opposed configuration. 14 . The process of claim 11 , wherein the aggregate of nanoparticles comprises nanoparticles having a diameter of from about 30 nm to about 100 nm. 15 . The process of claim 11 , wherein the percolate of aggregated nanoparticles comprises nanoparticles having a diameter of from about 100 nm to about 30 μm. 16 . The process of claim 11 , wherein the gel comprises macro-aggregates. 17 . The process of claim 16 , wherein the macro-aggregates comprise particles having a diameter of from about 30 μm to about 5 mm. 18 - 25 . (canceled)
Preparation of aerosols · CPC title
being in the range 2-50 nm, i.e. mesopores · CPC title
Nanometer sized, i.e. from 1-100 nanometer · CPC title
Producing by vapour phase processes, e.g. halide oxidation · CPC title
comprising inorganic material · CPC title
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