METHOD FOR TRAPPING AND DECONTAMINATING A GASEOUS MEDIUM IN THE PRESENCE OF A MONOLITH COMPRISING TiO2 AND SILICA

Patent metadata

Field	Value
Publication number	US-2021094000-A1
Application number	US-201917050162-A
Country	US
Kind code	A1
Filing date	Apr 12, 2019
Priority date	Apr 26, 2018
Publication date	Apr 1, 2021
Grant date	—

Abstract

Method for treating a gaseous feedstock containing molecular oxygen and one or more volatile compounds, which method comprises the following steps:
a) bringing said gaseous feedstock containing molecular oxygen and one or more volatile organic compounds into contact with a monolith comprising silica and titanium dioxide, said monolith comprising a type-I macropore volume, of which the diameter of the pores is greater than 50 nm and less than or equal to 1000 nm, of between from 0.1 to 3 ml/g, and a type-II macropore volume, of which the diameter of the pores is greater than 1 μm and less than or equal to 10 μm, of between from 1 to 8 ml/g; b) irradiating said monolith with at least one irradiation source producing at least one wavelength lower than 400 nm in order to convert said volatile organic compounds into carbon dioxide, said step b) being carried out at a temperature between −30° C. and +200° C. and at a pressure between 0.01 MPa and 70 MPa.

First claim

1 . A method for treating a gaseous feedstock containing molecular oxygen and one or more volatile compounds, which method comprises the following steps:
a) bringing said gaseous feedstock containing molecular oxygen and one or more volatile organic compounds into contact with a monolith comprising silica and titanium dioxide, said monolith comprising a type-I macropore volume, of which the pore diameter is greater than 50 nm and less than or equal to 1000 nm, of between from 0.1 to 3 ml/g, and a type-II macropore volume, of which the pore diameter is greater than 1 μm and less than or equal to 10 μm, of between from 1 to 8 ml/g; b) irradiating said monolith with at least one irradiation source producing at least one wavelength lower than 400 nm in order to convert said volatile organic compounds into carbon dioxide, said step b) being carried out at a temperature between −30° C. and +200° C. and at a pressure between 0.01 MPa and 70 MPa.

2 . The method as claimed in claim 1 , wherein said gaseous feedstock containing molecular oxygen and one or more volatile organic compounds is diluted with a diluent fluid.

3 . The method as claimed in claim 1 , wherein the irradiation source is an artificial irradiation source.

4 . The method as claimed in claim 1 , wherein the irradiation source produces at least one wavelength between 300 and 400 nm.

5 . The method as claimed in claim 1 , wherein step a) is carried out in a flow-through fixed bed reactor or a swept fixed bed reactor.

6 . The method as claimed in claim 1 , wherein said monolith has a mesopore volume, of which the pore diameter is greater than 2 nm and less than or equal to 50 nm, of between 0.01 and 1 ml/g, preferably between 0.05 and 0.5 ml/g.

7 . The method as claimed in claim 1 , wherein said monolith also has a macropore volume, of which the pore diameter is greater than 10 μm, of less than 0.5 ml/g.

8 . The method as claimed in claim 1 , wherein said monolith has a bulk density of between 0.05 and 0.5 g/ml.

9 . The method as claimed in claim 1 , wherein said monolith has a specific surface area of between 10 and 1000 m 2 /g, preferably between 50 and 600 m 2 /g.

10 . The method as claimed in claim 1 , wherein said monolith comprises a titanium dioxide content of between 5 and 70% by weight relative to the total weight of the monolith.

11 . The method as claimed in claim 1 , wherein said monolith is prepared according to the following steps:
1) a solution containing a surfactant is mixed with an acid solution; 2) at least one soluble silica precursor is added to the solution obtained in step 1); 3) optionally, at least one liquid organic compound that is immiscible with the solution obtained in step 2) is added to the solution obtained in step 2) so as to form an emulsion; 4) the solution obtained in step 2) or the emulsion obtained in step 3) is left to mature in the wet state so as to obtain a gel; 5) the gel obtained in step 4) is washed with an organic solution; 6) the gel obtained in step 5) is dried and calcined so as to obtain a silica-based monolith; 7) a solution comprising at least one soluble precursor of titanium dioxide is impregnated in the porosity of the monolith obtained in step 6); 8) optionally, the product obtained in step 7) is dried and calcined so as to obtain a silica-based monolith containing titanium dioxide.

12 . The method as claimed in claim 11 , wherein, in step 8), drying is carried out at a temperature between 5 and 120° C.

13 . The method as claimed in claim 11 , wherein, in step 8), calcining is carried out in air with a first temperature stationary phase between 80 and 150° C. for 1 to 10 hours, then a second temperature stationary phase between 150 and 250° C. for 1 to 10 hours, and finally a third temperature stationary phase between 300 and 950° C. for 0.5 to 24 hours.

Assignees

• Ifp Energies Now

Inventors

• Bernadet Sophie
• Fecant Antoine
• Ravaine Serge
• Backov Renal-Vasco
• Le Bechec Michael
• Lacombe Sylvie

Classifications

• B01D2259/804

  UV light · CPC title

• B01D2255/20707

  Titanium · CPC title

• B01J21/063

  Titanium; Oxides or hydroxides thereof · CPC title

• B01J37/0236

  Drying, e.g. preparing a suspension, adding a soluble salt and drying · CPC title

• B01J21/08

  Silica · CPC title