Precipitated and calcined composition based on zirconium oxide and cerium oxide
US-2015375203-A1 · Dec 31, 2015 · US
US10773208B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10773208-B2 |
| Application number | US-201615768058-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 14, 2016 |
| Priority date | Oct 16, 2015 |
| Publication date | Sep 15, 2020 |
| Grant date | Sep 15, 2020 |
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A process for treating gaseous effluents developed in a coffee roasting installation making it possible to treat gaseous effluents developed in a coffee roasting installation, in which the effluents are passed through an oxidative catalytic converter. Within the catalytic converter use is made of a catalyst selected from the group including: a) a catalyst including a porous faujasite support containing copper oxide nanoparticles in a quantity of between 2% and 7% of the total weight of the catalyst; b) a catalyst including a porous γ-alumina support containing copper oxide nanoparticles in a quantity of between 2% and 7% of the total weight of the catalyst; and c) a catalyst including a mesoporous zeolite or silica support containing iron nanoparticles in a quantity of between 2% and 7% of the total weight of the catalyst.
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The invention claimed is: 1. A method for processing the gaseous effluents developed in a coffee roasting installation ( 1 ), wherein said effluents are conveyed through an oxidising catalytic converter ( 5 ), and wherein in said catalytic converter use is made of a catalyst comprising a mesoporous silica support, consisting of iron nanoparticles in an amount comprised between 2% and 7% of the total weight of the catalyst. 2. The method according to claim 1 , wherein said mesoporous silica is an SBA-15 silica. 3. The method according to claim 1 , wherein before being admitted to the catalytic converter said gaseous effluents are heated to a temperature comprised between 350° C. and 500° C. 4. The method according to claim 1 , wherein said iron nanoparticles are provided in an amount equal to 5% of the total weight of the catalyst. 5. The method according to claim 1 , wherein before being admitted to the catalytic converter said gaseous effluents are heated to a temperature comprised between 400° C. and 450° C. 6. The method according to claim 1 , wherein said iron nanoparticles are deposited on said supports with the Incipient Wetting Impregnation (IWI) technique. 7. A method for processing the gaseous effluents developed in a coffee roasting installation ( 1 ), wherein said effluents are conveyed through an oxidising catalytic converter ( 5 ) and wherein in said catalytic converter ( 5 ) use is made of a catalyst comprising a porous γ-alumina support consisting of nanoparticles of copper in an amount comprised between 2% and 7% of the total weight of the catalyst. 8. The method according to claim 7 , wherein before being admitted to the catalytic converter ( 5 ) said gaseous effluents are heated to a temperature comprised between 350° C. and 500° C. 9. The method according to claim 7 , wherein said nanoparticles of copper are provided in an amount equal to 5% of the total weight of the catalyst. 10. The method according to claim 7 , wherein before being admitted to the catalytic converter said gaseous effluents are heated to a temperature comprised between 400° C. and 450° C. 11. The method according to claim 7 , wherein said nanoparticles of copper are deposited on said supports with the Incipient Wetting Impregnation (IWI) technique.
Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters · CPC title
Zeolites · CPC title
Organic compounds not provided for in groups B01D2257/00 - B01D2257/602 · CPC title
Iron · CPC title
Copper · CPC title
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