Fluid fuel reforming ceramic catalysts and their manufacturing methods

Claim 2

A fluid fuel reforming ceramic catalyst comprising a core of a complex oxide ceramic of transition metals, an intermediate layer of a ceramic containing alumina and silicate in which the main element is alumina covering the core, and an outer layer of a ceramic containing a noble metal alloy that covers the intermediate layer.

Claim 3

A fluid fuel reforming ceramic catalyst according to claim 1, in which the core consists essentially of complex oxides of transition metals comprising MnO 2 , Nio, CoO and CuO, the intermediate layer consists essentially of a ceramic comprised of a mixture of alumina and silicate in which the main element is alumina, and the outer layer consists essentially of a ceramic containing a noble metal alloy comprising a fired mixture of a Pt--Pd--Rh alloy and Al 2 O 3 , a Mo--Al 2 O 3 catalyst, a La 0 .5 --Sr 0 .5 CoO 3 catalyst, and an Al 2 O 3 -carried vanadium oxide catalyst and/or a Ag--Al 2 O 3 catalyst.

Claim 4

A fluid fuel reforming ceramic catalyst according to claim 2, in which the core consists of 40 to 70 parts by weight of MnO 2 and 10 to 20 parts by weight each of NiO, CoO and CuO, the intermediate layer consists of 70 to 90 parts by weight of alumina and 10 to 30 parts by weight of silicate, and the outer layer consists of 15 to 25 parts by weight of a fired mixture of a Pt--Pd--Rh alloy and Al 2 O 3 and 15 to 25 parts by weight each of a Mo--Al 2 O 3 catalyst, a La 0 .5 --Sr 0 .5 CoO 3 catalyst, and an Al 2 O 3 -carried vanadium oxide catalyst and/or a Ag--Al 2 O 3 catalyst.

Claim 5

A fluid fuel reforming ceramic catalyst according to claim 1, in which the boundaries between the core and intermediate layer and between the intermediate and outer layers have a slanted structure in which the composition of ceramics changes gradually.

Claim 6

A fluid fuel reforming ceramic catalyst according to claim 1, in which the boundaries between the core and intermediate layer and between the intermediate and outer layers have a stepped structure in which the composition of ceramics changes abruptly.

Claim 7

A fluid fuel reforming ceramic catalyst according to claim 1, in which the core is substantially spherical and the intermediate and outer layers are shaped like substantially spherical crusts.

Claim 8

A fluid fuel reforming ceramic catalyst according to claim 1, in which the core is substantially columnar and the intermediate and outer layers are substantially cylindrical.

Claim 9

A fluid reforming ceramic catalyst according to claim 1, in which the intermediate layer further contains kaoline or carbon-bearing quartz.

Claim 12

A method of manufacturing fluid fuel reforming ceramic catalysts according to claim 9, in which the intermediate and outer layers mixed with viscous substances are coated without sintering and the boundaries between the core and intermediate layer and between the intermediate and outer layers are made to have a stepped structure in which the composition of the ceramics change abruptly.

Claim 13

A method of manufacturing fluid fuel reforming ceramic catalysts according to claim 9, in which the core of a complex oxide ceramic of transition metals is formed by mixing MnO 2 , NiO, CoO and CuO with a binder, firing the mixture at 900° to 1000° C., pulverizing the fired product, and sintering the pulverized product with a binder at 1150° to 1350° C., the intermediate layer is formed by mixing alumina and silicate with a binder, firing the mixture at 1050° to 1200 C., pulverizing the fired product, making the pulverized product into a paste by adding a binder and a foaming agent, coating the paste over the core and sintering the coated layer at 900° to 1100° C., and the outer layer containing noble metals is formed by mixing a fired mixture of a Pt--Pd--Rh alloy and Al 2 O 3 , a Mo--Al 2 O 3 catalyst, a La 0 .5 --Sr 0 .5 --CoO 3 catalyst, and at least one of an Al 2 O 3 -carried vanadium oxide catalyst and a Ag--Al 2 O 3 catalyst, making the mixture into a paste by adding a binder and a foaming agent, coating the paste over the intermediate layer, and firing the coated layer at 600° to 700° C. in a reducing atmosphere.

Claim 14

A method of manufacturing fluid fuel reforming ceramic catalysts according to claim 9, in which the core consists of 40 to 70 parts by weight of MnO 2 and 10 to 20 parts by weight each of NiO, CoO and CuO, the intermediate layer consists of 70 to 90 parts by weight of alumina and 10 to 30 parts by weight of silicate, and the outer layer consists of 15 to 25 parts by weight each of a fired mixture of a Pt--Pd--Rh alloy and Al 2 O 3 , a Mo--Al 2 O 3 catalyst, a La 0 .5 --Sr 0 .5 --CoO 3 catalyst, and an Al 2 O 3 -carried vanadium oxide catalyst and/or a Ag--Al 2 O 3 catalyst.