Method for the Preparation of a Vanadium Based Catalyst
20190126244 ยท 2019-05-02
Assignee
Inventors
- Jakob Weiland H?j (Gentofte, DK)
- P?r L.T. Gabrielsson (Helsingborg, SE)
- Claus S. J?rgensen (Virum, DK)
Cpc classification
B01D53/9418
PERFORMING OPERATIONS; TRANSPORTING
B01J2523/00
PERFORMING OPERATIONS; TRANSPORTING
B01J35/56
PERFORMING OPERATIONS; TRANSPORTING
B01J21/063
PERFORMING OPERATIONS; TRANSPORTING
B01J23/002
PERFORMING OPERATIONS; TRANSPORTING
B01J35/393
PERFORMING OPERATIONS; TRANSPORTING
B01J37/0009
PERFORMING OPERATIONS; TRANSPORTING
B01J2523/00
PERFORMING OPERATIONS; TRANSPORTING
B01D53/8628
PERFORMING OPERATIONS; TRANSPORTING
B01J35/40
PERFORMING OPERATIONS; TRANSPORTING
International classification
B01J37/00
PERFORMING OPERATIONS; TRANSPORTING
B01J21/06
PERFORMING OPERATIONS; TRANSPORTING
B01J35/00
PERFORMING OPERATIONS; TRANSPORTING
B01J37/02
PERFORMING OPERATIONS; TRANSPORTING
B01J23/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
Method for the preparation of a catalyst comprising vanadium pentoxide supported on a metal oxide catalyst carrier comprising the steps of a) providing particles of crystalline vanadium pentoxide and particles of a metal oxide catalyst carrier; b) solid state mixing the particles and dispersing the vanadium pentoxide particles on surface of the metal oxide carrier particles; and c) anchoring the dispersed vanadium pentoxide particles on surface of the metal oxide carrier particles by calcination at a temperature above 500? C., characterized in that sintering of the vanadium pentoxide particles is suppressed by addition of an anti-sintering metal oxide component, such as tungsten trioxide, during the anchoring in step c).
Claims
1. Method for the preparation of a catalyst comprising vanadium pentoxide supported on a metal oxide catalyst carrier comprising the steps of a) providing particles of crystalline vanadium pentoxide and particles of a metal oxide catalyst carrier; b) solid state mixing the particles and dispersing the vanadium pentoxide particles on surface of the metal oxide carrier particles; and c) anchoring the dispersed vanadium pentoxide particles on surface of the metal oxide carrier particles by calcination at a temperature above 500? C., characterized in that sintering of the vanadium pentoxide particles is suppressed by addition of an anti-sintering metal oxide component during the anchoring in step c).
2. The method of claim 1, wherein the particle size of the crystalline vanadium pentoxide is between 0.5 and 10 ?m.
3. The method of claim 2, wherein the particle size is between 2 and 5 ?m.
4. The method according to claim 1, wherein the metal oxide catalyst carrier comprises titania.
5. The method according to claim 1, wherein the anti-sintering metal oxide component comprises tungsten oxide or silica and mixtures thereof.
6. The method according to claim 1, comprising the further step of preparing a washcoat by suspending the calcined particles obtained in step c) in an organic solvent.
7. The method of claim 6, wherein the washcoat contains one or more dispersions agents.
8. The method of claim 6, wherein the washcoat contains one or more binders selected from the group consisting of alumina, silica and titania.
9. The method of claim 6, comprising the further step of applying the washcoat on a monolithic substrate.
10. The method of claim 9, wherein the monolithic substrate comprises one or more corrugated sheets of non-woven fibers.
11. The method of claim 10, wherein the one or more corrugated sheets of non-woven fibers comprise glass fibers.
12. The method of claim 9, wherein the monolithic substrate is a ceramic extrudate.
13. The method of claim 10, wherein the ceramic extrudate consists of cordierite or silicon carbide.
14. The method of claim 1, comprising the further steps of preparing a paste comprising the calcined particles and extruding the paste to a full body catalyst monolith.
Description
EXAMPLE
[0022] 2 parts of V2O5 were mixed thoroughly with 98 parts of either pure TiO2 (mixture 1) or TiO2 modified with 10% WO3 (mixture 2) by dry milling with ZrO2 beads. Each of the physical mixtures was calcined in static air for 4 h at 575? C.
[0023] After calcination the surface area of mixture 1 is 48.2 m.sup.2/g and of mixture 2 61.3 m.sup.2/g.