Claims
- 1. A method for purifying exhaust gas from a diesel engine, wherein carbon monoxide and hydrocarbons in the exhaust gas are oxidized to carbon dioxide and water in the presence of a catalyst, while sulfur dioxide and nitrogen monoxide in the exhaust gas pass substantially unchanged through the catalyst, comprising:
- contacting exhaust gas from a diesel engine with the catalyst to thereby oxidize carbon monoxide and hydrocarbons in the exhaust gas to purify the gas, wherein the catalyst includes an open-cell monolithic or honeycombed inert carrier of ceramic or metal,
- the inert carrier having a plurality of channels essentially parallel to a direction of flow of the exhaust gases, such that exhaust gas flows freely through the channels of the carrier, the channels having interior surfaces coated with an activity-enhancing support material which includes a mixture of aluminum oxide with titanium oxide wherein the aluminum oxide to titanium oxide weight ratio ranges from 10:90 to 70:30, wherein the activity-enhancing support material optionally includes silica, zeotite or mixtures thereof, and wherein a weight ratio between the aluminum oxide and the said titanium oxide, and optional silica and zeolite utilized for the support material is in the range of 90:10 to 10:90, thereby providing a finely divided support material,
- the activity-enhancing support material having deposited thereon a catalytically active component of at least one platinum group metal selected from the group consisting of platinum, palladium, rhodium and iridium, the platinum group metal or metals being doped with vanadium or being in contact with an oxidic vanadium compound,
- the catalyst being prepared by impregnating the activity-enhancing support material with a solution of compounds of the platinum group metals and a solution of a vanadium compound, the impregnating taking place simultaneously or successively in any desired sequence,
- thereafter drying, and optionally calcining at a temperature of at least 200.degree. C.
- 2. The method according to claim 1, characterized in that the activity-enhancing support material is present in a concentration in the range of 30-250 g/dm.sup.3 catalyst volume, the vanadium, calculated as V.sub.2 O.sub.5, is present in a concentration in the range of 0.15-15 g/dm.sup.3 catalyst volume and the platinum group metals are present in a concentration in the range of 0.1-7 g/dm.sup.3 catalyst volume.
- 3. The method according to claim 2, wherein the activity-enhancing support material is present in a concentration in the range of 75-180 g/dm.sup.3 catalyst volume.
- 4. The method according to claim 2, wherein the activity-enhancing support material is present in a concentration in the range of 90-150 g/dm.sup.3 catalyst volume.
- 5. The method according to claim 1, characterized in that the cell density of the monolithic or honeycombed inert carrier is 5 to 100 cells/cm.sup.2.
- 6. The method according to claim 5, wherein the activity-enhancing support material includes an additional material selected from the group consisting of MgO, CeO.sub.2, GeO.sub.2, SnO.sub.2, ZrO.sub.2, HfO.sub.2, ThO.sub.2, Nb.sub.2 O.sub.5, WO.sub.3, MoO.sub.3, magnesium silicate, aluminum silicate, magnesium titanate, and mixtures thereof.
- 7. The method according to claim 1, characterized in that platinum and/or palladium is present as said platinum group metal.
- 8. The method according to claim 1, wherein during calcining the catalyst is subjected to a current of gas containing hydrogen.
- 9. The method according to claim 1, wherein the activity-enhancing support material includes an additional material selected from the group consisting of MgO, CeO.sub.2, GeO.sub.2, SnO.sub.2, ZrO.sub.2, HfO.sub.2, ThO.sub.2, Nb.sub.2 O.sub.5, WO.sub.3, MoO.sub.3, magnesium silicate, aluminum silicate, magnesium titanate, and mixtures thereof.
- 10. The method according to claim 1, wherein silica is present in the activity-enhancing support material.
- 11. The method according to claim 1, wherein zirconium dioxide is present in the activity-enhancing support material.
- 12. The method according to claim 1, wherein the impregnating of the activity-enhancing support material with at least one of the vanadium compound or the platinum group metal compound takes place after depositing the activity-enhancing support material on the inert carrier.
- 13. The method according to claim 1, wherein the impregnating of the activity-enhancing support material with at least one of the vanadium compound or the platinum group metal compound takes place before depositing the activity-enhancing support material on the inert carrier.
- 14. The method according to claim 1, wherein the weight ratio of aluminum oxide to titanium oxide is in the range of 20:80 to 60:40.
Priority Claims (1)
Number |
Date |
Country |
Kind |
39 40 758.6 |
Dec 1989 |
DEX |
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RELATED APPLICATION DATA
This application is a divisional of U.S. patent application Ser. No. 07/667,211, filed Mar. 11, 1991 now U.S. Pat. No. 5,157,007, which application is a continuation in part of U.S. patent application Ser. No. 07/616,349, filed Nov. 21, 1990, now abandoned. These applications are entirely incorporated herein by reference.
US Referenced Citations (14)
Foreign Referenced Citations (18)
Number |
Date |
Country |
2009165 |
Aug 1990 |
CAX |
0145584 |
Jun 1985 |
EPX |
0174495 |
Mar 1986 |
EPX |
0211233 |
Feb 1987 |
EPX |
2231296 |
Apr 1973 |
DEX |
3141713 |
May 1983 |
DEX |
3232729 |
Mar 1984 |
DEX |
3407172 |
Sep 1985 |
DEX |
3711280 |
Oct 1988 |
DEX |
3716446 |
Dec 1988 |
DEX |
3729683 |
Mar 1989 |
DEX |
13816 |
Feb 1979 |
JPX |
266145 |
Nov 1985 |
JPX |
34972 |
Feb 1986 |
JPX |
61-120640 |
Jun 1986 |
JPX |
2268810 |
Feb 1990 |
JPX |
2207845 |
Aug 1990 |
JPX |
5-78385 |
Oct 1993 |
JPX |
Divisions (1)
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Number |
Date |
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Parent |
667211 |
Mar 1991 |
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Continuation in Parts (1)
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Number |
Date |
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Parent |
616349 |
Nov 1990 |
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