Reactive filter for motor vehicle

Patent metadata

Field	Value
Publication number	US-10837335-B2
Application number	US-201515771999-A
Country	US
Kind code	B2
Filing date	Oct 29, 2015
Priority date	Oct 29, 2015
Publication date	Nov 17, 2020
Grant date	Nov 17, 2020

Abstract

Disclosed is a reactive filter, that is a selective catalytic reduction filter or an oxidative reaction filter, including a porous substrate including internal pores having their inner surface, totally or partially, directly coated with a catalytic zeolite material resulting from an in situ hydrothermal synthesis. Also disclosed is a process for preparing such a reactive filter and the use thereof in an engine exhaust depolluting system.

First claim

The invention claimed is:

1. A selective catalytic reduction filter comprising:
a porous substrate having a particulate filter function and a catalytic reduction function, the porous substrate having an intrinsic porosity comprised by 5% and 90% and an intrinsic mean pore size comprised between 0.1 pm and 100 pm, the porous substrate comprising internal pores each having an inner surface, totally or partially, directly coated with a catalytic zeolite material resulting from an in situ hydrothermal synthesis conducted inside an autoclave reactor, in which the porous substrate is contacted with a medium comprising water, at least one zeolite material precursor derivative, at least one active catalytic species precursor, and at least one zeolite structure template agent,
wherein the inner surfaces of the internal pores are directly coated homogenously by the catalytic zeolite material in an absence of a binding substance, and
wherein the selective catalytic reduction filter is configured to treat exhaust gas emitted by a vehicle diesel engine.

2. The selective catalytic reduction filter according to claim 1 , wherein the porous substrate is selected from the group consisting of:
ceramic-like materials, ceramic materials,
cordierite ceramic, a-alumina, silicon carbide, aluminium titanate, silicon nitride, zirconia, mullite, spodumene, alumina-silica-magnesia, zirconium silicate,
one or more metal alloys, metal alloys, sintered metals, porous refractory metals,
titanium oxide, aluminium, iron, steel, sintered carbon, and
stainless steel, iron alloys, nickel alloys, chromium alloys, aluminium alloys, titanium alloys.

3. The selective catalytic reduction filter according to claim 1 , wherein the porous substrate is in a form selected from trapezoidal forms, rectangular forms, square forms, sinusoidal forms, hexagonal forms, oval forms, a honeycomb structure, a monolith structure, packed fibres, open cell foams, blocks of sintered metal alloy, and blocks of sintered carbon.

4. The selective catalytic reduction filter according to claim 1 , wherein the porous substrate comprises at least one porous wall having the internal pores having the inner surfaces, totally or partially, directly coated by the catalytic zeolite material resulting from the in situ hydrothermal synthesis,
wherein a mean size of the coated internal pores is homogeneously distributed over a thickness of said porous wall, and/or
the catalytic zeolite material is homogeneously distributed over the thickness of said porous wall in such a way that differences of mean sizes of the coated internal pores is lower than 15% between two difference depths of determination of pore mean sizes in said porous wall.

5. The selective catalytic reduction filter according to claim 4 , wherein said at least one porous wall has a thickness that is comprised between 0.05 and 0.5 mm.

6. The selective catalytic reduction filter according to claim 1 , wherein
the internal pores of the coated porous substrate have from 80 to 100% of the inner surfaces that are coated with the catalytic zeolite material, and/or
the catalytic zeolite material results from the in situ hydrothermal synthesis around a grain structure of the porous substrate.

7. The selective catalytic reduction filter according to claim 1 , wherein the amount of catalytic zeolite material or a coating thickness thereof results from the conditions of the in situ hydrothermal synthesis.

8. The selective catalytic reduction filter according to claim 1 , wherein the coated internal pores of the porous substrate have a mean pore size diameter that is lower than the mean pore size diameter within the raw substrate before coating and that is determined by filtration requirements.

9. The selective catalytic reduction filter according to claim 1 , wherein the catalytic zeolite material is realized from a material zeolite selected in the group consisting of:
FAU zeolites,
MFI zeolites,
BEA zeolites,
Zeolites A,
CHA zeolites, and
LTL zeolites.

10. The selective catalytic reduction filter according to claim 9 , wherein the catalytic zeolite material is also realized from at least one active species precursor.

11. The selective catalytic reduction filter according to claim 1 , wherein the selective catalytic reduction filter has a defined filtering efficiency in retaining engine particulates that is obtained by controlling a thickness of the catalytic zeolite material coating internal pores, and
wherein the thickness of the catalytic zeolite material coating internal pores is controlled by selecting a composition of the zeolite material precursor derivative, and by determining conditions of the in situ hydrothermal synthesis.

12. The selective catalytic reduction filter according to claim 1 , wherein the selective catalytic reduction filter is highly selective in lowering N 2 O by reduction reactions.

13. A process for preparing the selective catalytic reduction filter according to claim 1 , the process comprising:
preparing the medium comprising the water, the at least one zeolite material precursor derivative, the at least one active catalytic species precursor, and the at least one zeolite structure template agent or at least one zeolite structure directing agent;
providing the porous substrate having the intrinsic porosity comprised between 5% and 90% and the intrinsic mean pore size comprised between 0.1 μm and 100 μm;
contacting the provided porous substrate with the prepared medium;
conducting the in situ hydrothermal synthesis in the autoclave reactor in which the temperature is comprised between 160° C. and 250° C. and the duration of 30 min to 10 days; and
eliminating the zeolite structure template agent or the zeolite structure directing agent by a heating treatment at a temperature comprised between 100° C. and 1200° C. in a presence of oxygen and in a presence of an inert gas.

14. The process according to claim 13 , wherein the porous substrate comprises the internal pores having the internal surfaces contacted by the prepared medium.

15. The process according to claim 13 , wherein the contacting of the provided porous substrate with the prepared medium comprises immersing the porous substrate in a bath containing the medium.

16. The process according to claim 13 , wherein, during the conducting the in situ hydrothermal synthesis, the temperature and the duration at which the in situ hydrothermal synthesis is conducted, are adjusted depending on one or more of the thickness of the catalytic zeolite material desired to form at the inner surfaces of the internal pores, and/or the mean pore size that is desired to be obtained in the selective catalytic reduction filter.

17. The process according to claim 16 , wherein the desired mean pore size is determined depending on the size of the particles to trap.

18. The process according to claim 13 , wherein one of:
the medium comprising the water, the at least one zeolite material precursor derivative, the at least one active catalytic species precursor, and the at least one zeolite structure template agent or the at least one zeolite structure directing agent, has a viscosity that is lower than an inducing gel formation viscosity,
the at least one zeolite material precursor derivative is selected from a group consisting of silicon precursors, aluminium precursors, phosphor precursors, iron aluminium oxide precursors, and mixtures thereof,
the zeolite structure template agent or the zeolite structure directing agent is selected from weak bases and bases having a pH that is greater than 7,

Assignees

• Volvo Truck Corp
• Centre Nat Rech Scient
• Univ Claude Bernard Lyon

Inventors

• Giroir-Fendler Anne
• Gil Villarino Sonia
• Iojoiu Eduard Emil

Classifications

• B01J35/56

  Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional [3D] monoliths · CPC title

• F01N2510/063

  zeolites · CPC title

• F01N2330/30

  Honeycomb supports characterised by their structural details · CPC title

• B01D2255/9202

  Linear dimensions · CPC title

• F01N3/2828

  Ceramic multi-channel monoliths, e.g. honeycombs · CPC title