Low cost oxidation catalysts for VOC and halogenated VOC emission control
The current embodiments relate to ruthenium-containing supported catalysts, including processes for their manufacture and use, which destroy, through catalytic oxidation, hazardous compounds contained in chemical industrial emissions and otherwise produced from industrial processes.
1. An oxidation catalyst for the destruction of CO and volatile organic compounds which may include halogenated organic compounds, from an emissions stream, the oxidation catalyst comprising:
ruthenium, without any other metal from platinum group metals;
a refractory oxides support, the support comprising a solid solution or mixed oxide; and
one or both of silica and tin oxide;
wherein the solid solution or mixed oxide is chosen from the group consisting of ZrO2-CeO2, TiO2-CeO2, SnO2-CeO2, and Al2O3-CeO3.
2. An oxidation catalyst for the destruction of CO and volatile organic compounds which may include halogenated organic compounds, from an emissions stream, wherein the oxidation catalyst comprises:
a refractory oxides support comprising a mixed oxide;
and one or both of silica and tin oxide,
wherein the mixed oxide is chosen from the group consisting of ZrO 2 —CeO 2 , TiO 2 —CeO 2 , SnO 2 —CeO 2 , and A 12 O 3 —CeO 3 and the at least one platinum group metals comprises ruthenium and no other platinum group metal.
3. The oxidation catalyst of claim 2 deposited on a substrate having a honeycomb or a monolithic structure wherein the substrate is produced from the group consisting of cordierite, mullite, iron-chromium alloy and stainless steel.
4. The oxidation catalyst of claim 2 wherein the refractory oxides support is stabilized with silica or one or more rare earth metal oxides.
5. The oxidation catalyst of claim 4 wherein the rare earth oxides are selected from the group consisting of lanthanum, cerium, yttrium, praseodymium, neodymium, and mixtures thereof.
6. The oxidation catalyst of claim 2 wherein the oxidation catalyst comprises stabilized tin oxide having a surface area from 2 m 2 /g to 200 m 2 /g and a particle size of from 1 to 20 micrometers, or wherein the oxidation catalyst comprises stabilized titania having a surface area from 2 m 2 /g to 200 m 2 /g and a particle size of from 0.2 to 20 micrometers.
7. The oxidation catalyst of claim 3 wherein the ruthenium metal is deposited on the substrate at a loading that comprises from 0.3 g/L to 5 g/L.
8. The oxidation catalyst of claim 2 wherein the oxidation catalyst comprises silica, which comprises from 5% to 50%, by weight, of the oxidation catalyst.
9. The oxidation catalyst of claim 2 wherein the oxidation catalyst comprises silica selected from the group consisting of amorphous silica, precipitated silica, molecular sieves, MCM-41, SBA-15, and combinations thereof.
10. The oxidation catalyst of claim 2 wherein the oxidation catalyst comprises silica comprising amorphous silica with a surface area more than 100 m 2 /g and a particle size from 0.5-20 micrometers.
11. The oxidation catalyst of claim 2 wherein the refractory metal oxides comprise from 10% to 95%, by weight of the oxidation catalyst.
12. The oxidation catalyst of claim 1 deposited on a substrate having a honeycomb or a monolithic structure wherein the substrate is produced from the group consisting of cordierite, mullite, iron-chromium alloy and stainless steel.
13. The oxidation catalyst of claim 12 wherein the ruthenium metal is deposited on the substrate at a loading that comprises from 0.3 g/L to 5 g/L.
14. The oxidation catalyst of claim 1 wherein the refractory oxides support is stabilized with silica or one or more rare earth metal oxides.
15. The oxidation catalyst of claim 14 wherein the rare earth oxides are selected from the group consisting of lanthanum, cerium, yttrium, praseodymium, neodymium, and mixtures thereof.
16. The oxidation catalyst of claim 1 wherein the refractory metal oxides comprise from 10% to 95%, by weight of the oxidation catalyst.