Catalytically active particle filter having a high degree of filtering efficiency
US-2024017213-A1 · Jan 18, 2024 · US
US2021106977A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2021106977-A1 |
| Application number | US-201816608568-A |
| Country | US |
| Kind code | A1 |
| Filing date | Apr 23, 2018 |
| Priority date | Apr 28, 2017 |
| Publication date | Apr 15, 2021 |
| Grant date | — |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
The invention relates to a photocatalytic carbon dioxide reduction method carried out in liquid and/or gas phase under irradiation, using a photocatalyst containing a first semiconductor, particles comprising one or more metallic-state elements M, and a second semiconductor SC, wherein the method is carried out by contacting a feedstock containing the CO 2 and at least one sacrificial compound with the photocatalyst, then irradiating the photocatalyst such that the CO 2 is reduced, and oxidising the sacrificial compound in order to produce an effluent containing at least in part C1 or above carbon molecules other than CO 2 .
Opening claim text (preview).
1 . A photocatalytic carbon dioxide reduction process carried out in the liquid phase and/or in the gas phase under irradiation using a photocatalyst in the form of a porous monolith containing at least one semiconductor, which process comprises the following steps: a) a feedstock containing carbon dioxide and at least one sacrificial compound is brought into contact with a photocatalyst which is in the form of a porous monolith comprising a bulk density of less than or equal to 0.25 g/ml; b) the photocatalyst is irradiated with at least one irradiation source producing at least one wavelength lower than the bandgap of said photocatalyst, said step b) being carried out at a temperature of between −10° C. and 200° C., and at a pressure of between 0.01 MPa and 70 MPa. 2 . The process as claimed in claim 1 , wherein, when said process is carried out in the gas phase, the sacrificial compound is a gaseous compound chosen from water, aqueous ammonia, hydrogen, methane and an alcohol. 3 . The process as claimed in claim 1 , wherein, when the process is carried out in the liquid phase, the sacrificial compound is a soluble solid or liquid compound chosen from water, aqueous ammonia, an alcohol, an aldehyde or an amine. 4 . The process as claimed in claim 1 , wherein the irradiation source is an artificial or natural irradiation source. 5 . The process as claimed in claim 1 , wherein the photocatalyst in the form of a porous monolith has a mesoporous volume, of which the pore diameter is greater than 0.2 nm and less than or equal to 50 nm, of between 0.01 and 1 ml/g. 6 . The process as claimed in claim 1 , wherein the photocatalyst in the form of a porous monolith has a type-I macroporous volume, of which the pore diameter is greater than 50 nm and less than or equal to 1000 nm, of between 0.1 and 3 ml/g. 7 . The process as claimed in claim 1 , wherein the photocatalyst in the form of a porous monolith has a type-II macroporous volume, of which the pore diameter is greater than 1 μm and less than or equal to 10 μm, of between 0.1 and 8 ml/g. 8 . The process as claimed in claim 1 , wherein the photocatalyst in the form of a porous monolith comprises a mesoporosity and/or a type-I macroporosity and/or a type-II macroporosity. 9 . The process as claimed in claim 1 , wherein the photocatalyst in the form of a porous monolith comprises a macroporous volume, of which the pore diameter is greater than 10 μm, of less than 0.5 ml/g. 10 . The process as claimed in claim 1 , wherein the photocatalyst in the form of a porous monolith comprises a bulk density of less than 0.19 g/ml. 11 . The process as claimed in claim 1 , wherein the photocatalyst in the form of a porous monolith has a specific surface area of between 10 and 1000 m 2 /g. 12 . The process as claimed in claim 1 , wherein the photocatalyst in the form of a porous monolith comprises at least one semiconductor and at least one inorganic phase containing silica or alumina not absorbing photons with an energy greater than 4 eV. 13 . The process as claimed in claim 1 , in which the semiconductor content is between 5% and 70% by weight relative to the total weight of the photocatalyst. 14 . The process as claimed in claim 1 , wherein the photocatalyst in the form of a porous monolith consists of said semiconductor in monolith form. 15 . The process as claimed in claim 1 , wherein the semiconductor is chosen from TiO 2 , ZnO, Cu 2 O, CuO, Ce 2 O 3 , CeO 2 , In 2 O 3 , SiC, ZnS and In 2 S 3 , alone or as a mixture.
Bulk density · CPC title
Indexing scheme associated with group B01J35/00, related to the analysis techniques used to determine the catalysts form or properties · CPC title
Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional [3D] monoliths · CPC title
UV light · CPC title
Specific surface · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.