Honeycomb heater and catalytic converter

Claim 2

A honeycomb heater comprising: a honeycomb structure having a number of passages defined by partition walls; at least two electrodes in electrical contact with said honeycomb structure for energizing said honeycomb structure; a catalyst composition being formed on said partition walls of said honeycomb structure, said catalyst composition comprising ZrO 2 powder having ZrO 2 particle loaded with a catalytically active metal consisting essentially of Rh, and a composite oxide of Al 2 O 3 and CeO 2 , said composite oxide being loaded with at least one material selected from the group consisting of Pt and Pd.

Claim 3

The honeycomb heater of claim 1, wherein Rh is present in the amount of 0.01-15.0% by weight with respect to said ZrO 2 powder.

Claim 4

The honeycomb heater of claim 1, wherein said ZrO 2 powder is present in an amount of 5-50% by weight with respect to said catalyst composition.

Claim 5

The honeycomb heater of claim 1, wherein the composite oxide is loaded with Pt and a total loading amount of Pt ranges from 0.5 to 1.6 grams per liter of the honeycomb heater, and a total loading amount of Rh ranges from 0.02 to 0.3 grams per liter of the honeycomb heater.

Claim 6

The honeycomb heater of claim 1, wherein the composite oxide is loaded with Pt and a weight ratio of Rh to Pt ranges from 1/19 to 1/5.

Claim 7

The honeycomb heater of claim 1, wherein said honeycomb structure comprises 2-30% by weight of Al, 10-40% by weight of Cr, and the remainder being substantially Fe.

Claim 8

The honeycomb heater of claim 1, wherein a resistance adjusting means is disposed between said electrodes and within said honeycomb structure.

Claim 9

The honeycomb heater of claim 1, further comprising a porous layer of a heat-resistant oxide coated on said catalyst composition.

Claim 10

A catalytic converter for a fluid to be flowed therethrough, comprising: one main monolithic catalyst for disposal in a fluid stream; a honeycomb heater for disposal in said fluid stream in a location selected from the group consisting of upstream and downstream of said main monolithic catalyst, said honeycomb heater comprising a honeycomb structure having a number of passages defined by partition walls, at least two electrodes in electrical contact with said honeycomb structure for energizing said honeycomb structure, a catalyst composition formed on said partition walls of said honeycomb structure, said catalyst composition comprising ZrO 2 powder having ZrO 2 particles loaded with a catalytically active metal consisting essentially of Rh, and a composite oxide of Al 2 O 3 and CeO 2 , said composite oxide being located with at least one material selected from the group consisting of Pt and Pd; and a housing containing said main monolithic catalyst and said honeycomb heater.

Claim 11

A catalytic converter for a fluid to be flowed therethrough, comprising: one main monolithic catalyst for disposal in a fluid stream; a honeycomb heater for disposal in said fluid stream in a location selected from the group consisting of upstream and downstream of said main monolithic catalyst, said honeycomb heater comprising a honeycomb structure having a number of passages defined by partition walls, at least two electrodes in electrical contact with said honeycomb structure for energizing said honeycomb structure, a catalyst composition formed on said partition walls of said honeycomb structure, said catalyst composition comprising ZrO 2 powder having ZrO 2 particles loaded with a catalytically active metal consisting essentially of Rh, and a composite oxide of Al 2 O 3 and CeO 2 , said composite oxide being located with at least one material selected from the group consisting of Pt and Pd; and a housing containing said main monolithic catalyst and said honeycomb heater.

Claim 12

A catalytic converter for a fluid to be flowed therethrough, comprising: at least two main monolithic catalyst for disposal in a fluid stream; a honeycomb heater for disposal in said fluid stream in a location selected from the group consisting of downstream of said at least two main monolithic catalyst, upstream of said at least two main monolithic catalysts and between two of said at least two main monolithic catalysts, said honeycomb heater comprising a honeycomb structure having a number of passages defined by partition walls, at least two electrodes in electrical contact with said honeycomb structure for energizing said honeycomb structure, a catalyst composition formed on said partition walls of said honeycomb structure, said catalyst composition comprising ZrO 2 powder having ZrO 2 particles loaded with a catalytically active metal consisting essentially of Rh, and a composite oxide of Al 2 O 3 and CeO 2 , said composite oxide being loaded with at least one material selected from the group consisting of Pt and Pd; and a housing containing said at least two main monolithic catalysts and said honeycomb heater.

Claim 13

A catalytic converter for a fluid to be flowed therethrough, comprising: at least two main monolithic catalyst for disposal in a fluid stream; a honeycomb heater for disposal in said fluid stream in a location selected from the group consisting of downstream of said at least two main monolithic catalyst, upstream of said at least two main monolithic catalysts and between two of said at least two main monolithic catalysts, said honeycomb heater comprising a honeycomb structure having a number of passages defined by partition walls, at least two electrodes in electrical contact with said honeycomb structure for energizing said honeycomb structure, a catalyst composition formed on said partition walls of said honeycomb structure, said catalyst composition comprising ZrO 2 powder having ZrO 2 particles loaded with a catalytically active metal consisting essentially of Rh, and a composite oxide of Al 2 O 3 and CeO 2 , said composite oxide being loaded with at least one material selected from the group consisting of Pt and Pd; and a housing containing said at least two main monolithic catalysts and said honeycomb heater.