Catalyst systems
The present invention provides monolithic structural catalysts. The catalysts have a thin wall structure and are advantageous for catalyzing reactions of gaseous fluid or liquid fluid molecules, such as the denitration or selective catalytic reduction (SCR) of nitrogen oxides (NO x ) in combustion flue gases. In an embodiment, the honeycomb-like monolithic structural body includes catalytically active outer peripheral walls and a plurality of catalytically active thin-walled inner partition walls, the thin-walled inner partition walls adapted to enhance fluid flow through the monolithic catalytic body and to increase interaction of the fluid molecules with the catalyst body.
1. A monolithic structural catalyst body comprising:
an outer peripheral wall and
a plurality of inner partition walls having an average thickness of less than 0.22 mm,
the outer peripheral wall and the plurality of inner partition walls formed of a screened and extruded chemical composition comprising 50-99.9% by weight an inorganic oxide composition and at least 0.1% by weight a catalytically active metal functional group and one or more reinforcing agents, wherein the monolithic structural catalyst body has a hydraulic diameter greater than or equal to 100 mm, and a transverse compressive strength of at least 1.5 kg/cm 2 .
2. The monolithic structural catalyst body of claim 1 , wherein the one or more reinforcing agents comprise glass fibers, silicon carbide fibers or mixtures thereof.
3. The monolithic structural catalyst body of claim 1 , wherein the average thickness of the inner partition walls ranges from 0.05 mm to 0.20 mm.
4. The monolithic structural catalyst body of claim 1 , wherein the average thickness of the inner partition walls ranges from 0.10 mm to 0.18 mm.
5. The monolithic structural catalyst body of claim 1 , wherein the hydraulic diameter is greater than or equal to 150 mm.
6. The monolithic structural catalyst body of claim 1 , wherein the transverse compressive strength is greater than 3 kg/cm 2 .
7. The monolithic structural catalyst body of claim 1 , wherein the transverse compressive strength is greater than 4 kg/cm 2 .
8. The monolithic structural catalyst body of claim 1 , wherein the monolithic structural catalyst body has a defect level of 2% or less.
9. The monolithic structural catalyst body of claim 1 , wherein the monolithic structural catalyst body has a defect level of 0.3% or less.
10. The monolithic structural catalyst body of claim 1 further comprising additional catalytic material deposited on an inner partition wall.
11. The monolithic structural catalyst body of claim 1 further comprising additional catalytic material deposited on the outer peripheral wall.
12. The monolithic structural catalyst body of claim 1 further comprising additional catalytic material deposited on an inner partition wall and the outer peripheral wall.
13. A method of reducing the nitrogen dioxide content of a fluid comprising: flowing the fluid through a monolithic structural catalyst body comprising an outer peripheral wall and a plurality of inner partition walls having an average thickness of less than 0.22 mm, the outer peripheral wall and the plurality of inner partition walls formed of a screened and extruded chemical composition comprising 50-99.9% by weight an inorganic oxide composition and at least 0.1% by weight a catalytically active metal functional group and one or more reinforcing agents, wherein the monolithic structural catalyst body has a hydraulic diameter greater than or equal to 100 mm, and a transverse compressive strength of at least 1.5 kg/cm 2 .
14. The method of claim 13 , wherein the one or more reinforcing agents comprise glass fibers, silicon carbide fibers or mixtures thereof.
15. The method of claim 13 , wherein the average thickness of the inner partition walls ranges from 0.05 mm to 0.20 mm.
16. The method of claim 13 , wherein the average thickness of the inner partition walls ranges from 0.10 mm to 0.18 mm.
17. The method of claim 13 , wherein the hydraulic diameter is greater than or equal to 150 mm.
18. The method of claim 13 , wherein the transverse compressive strength is greater than 3 kg/cm 2 .
19. The method of claim 13 , wherein the transverse compressive strength is greater than 4 kg/cm 2 .
20. The method of claim 13 further comprising additional catalytic material deposited on an inner partition wall.
21. The method of claim 13 further comprising additional catalytic material deposited on the outer peripheral wall.
22. The method of claim 13 , wherein the fluid comprises a combustion-flue gas.
23. The method of claim 22 , wherein the temperature of the combustion flue gas ranges from 150° C. to 600° C.