An exhaust gas-purifying catalyst system is provided with a plurality of catalyst layers including a first and a second catalyst layers, supported on a support structure. The first catalyst layer comes into contact with an exhaust gas stream firstly among the plurality of catalyst layers. The second
An exhaust gas-purifying catalyst system is provided with a plurality of catalyst layers including a first and a second catalyst layers, supported on a support structure. The first catalyst layer comes into contact with an exhaust gas stream firstly among the plurality of catalyst layers. The second catalyst layer is provided adjacent to the first catalyst layer. The first catalyst layer contains a first noble metal active component including rhodium, together with a powder of a barely soluble barium compound in an amount of 0.05 mol to 0.2 mol per volume in liter of the support structure. The second catalyst layer contains a second noble metal active component.
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What is claimed is: 1. An exhaust gas-purifying catalyst system, comprising a plurality of catalyst layers including a first and a second catalyst layers, supported on a support structure, the first catalyst layer coming into contact with an exhaust gas stream firstly among the plurality of catalys
What is claimed is: 1. An exhaust gas-purifying catalyst system, comprising a plurality of catalyst layers including a first and a second catalyst layers, supported on a support structure, the first catalyst layer coming into contact with an exhaust gas stream firstly among the plurality of catalyst layers, the second catalyst layer is provided adjacent to the first catalyst layer, the first catalyst layer containing a first noble metal active component comprising rhodium, together with a powder of a barely water-soluble barium compound comprising barium sulfate in an amount of 0.05 mol to 0.2 mol per volume in liter of the support structure the first layer also containing cerium zirconium complex oxide, the second catalyst layer containing a second noble metal active component, a barely water-soluble barium compound comprising barium sulfate in an amount of 0.05 mol to 0.2 mol per volume in liter of the support structure, the second layer also containing cerium zirconium complex oxide. 2. The catalyst system according to claim 1, wherein the first catalyst layer contains the rhodium in an amount of 0.1 to 2.0 g per volume in liter of the support structure. 3. The catalyst system according to claim 1, wherein the first catalyst layer contains a powder of a first porous oxide which supports at least a portion of the first noble metal active component. 4. The catalyst system according to claim 3, wherein the first porous oxide comprises alumina. 5. The catalyst system according to claim 3, wherein the first catalyst layer contains the first porous oxide in an amount of 30 to 100 g per volume in liter of the support structure. 6. The catalyst system according to claim 1, wherein the first noble metal active component further comprises platinum. 7. The catalyst system according to claim 6, wherein the first catalyst layer contains the platinum in an amount of 0.1 to 5.0 g per volume in liter of the support structure. 8. The catalyst system according to claim 1, wherein the second catalyst layer contains a powder of a second porous oxide which supports at least a portion of the second noble metal active component. 9. The catalyst system according to claim 8, wherein the second porous oxide comprises alumina. 10. The catalyst system according to claim 8, wherein the second catalyst layer contains the second porous oxide in an amount of 30 to 100 g per volume in liter of the support structure. 11. The catalyst system according to claim 1, wherein the second noble metal active component comprises platinum. 12. The catalyst system according to claim 1, wherein the second noble metal active component comprises palladium. 13. The catalyst system according to claim 1, wherein the second catalyst layer contains the second noble metal active component in an amount of 0.1 to 5.0 g per volume in liter of the support structure. 14. The catalyst system according to claim 1, which contains the cerium zirconium complex oxide in an amount of 50 to 200 g in total per volume in liter of the support structure. 15. The catalyst system according to claim 1, wherein the support structure is constituted by a single support body, in which the first and second catalyst layers form a laminate structure on the support body, and the first catalyst layer constitutes an uppermost layer of the laminate structure. 16. The catalyst system according to claim 1, wherein the support structure is constituted by a single support body, in which the first catalyst layer is provided at a surface zone of the support body on an upstream side with respect to the direction of the exhaust gas stream, and the second catalyst layer is provided at a surface zone of the support body on a downstream side. 17. The catalyst system according to claim 1, wherein the support structure comprises a first support body provided on an upstream side with respect to the direction of the exhaust gas stream and a second support body provided downstream of the first support body, in which the first catalyst layer is provided on a surface of the first support body and the second catalyst layer is provided on a surface of the second support body.
Nunan, John G.; Klingmann, Raoul; Andersen, Ryan J.; Clark, Davion Onuga; Moser, David Henry, Three-way catalyst having an upstream single-layer catalyst.
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