IP Library Granted Patent US 9,308,498
Granted Patent B2
US 9,308,498 · App. 14/857,526 · Granted Apr 12, 2016

Exhaust gas treating catalyst and exhaust gas purification apparatus using the same

Inventors: Masatoshi Katsuki (Yokohama, JP); Shuuji Fujii (Yokohama, JP); Atsushi Ueda (Ikeda, JP); Yusuke Yamada (Ikeda, JP)
Assignee: MITSUBISHI HEAVY INDUSTRIES, LTD.
B01D53/9431B01D53/9422B01D53/9477B01J23/002B01J23/898F01N13/009B01D2255/1023B01D2255/1025B01D2255/207B01D2255/2042B01D2255/2063B01D2255/20738B01D2255/402B01D2258/012B01J2523/00
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Quick Facts
Patent No.
US 9,308,498
App. No.
14/857,526
Granted
Apr 12, 2016
Kind
B2
Abstract

An exhaust gas treating catalyst further improved in denitrification performance is provided. It is an exhaust gas treating catalyst containing a complex oxide represented by the general formula ABO 3 , where the A-site is composed of a lanthanoid (La) and barium (Ba), and the B-site is composed of iron (Fe), niobium (Nb) and palladium (Pd).

Claims (42)

1. An exhaust gas purification apparatus for reducing nitrogen oxides in an exhaust gas to purify the exhaust gas, comprising:

trapping means for trapping particulate matter in the exhaust gas; and

an exhaust gas treating catalyst for reducing nitrogen oxides in an exhaust gas to purify the exhaust gas, the exhaust gas treating catalyst containing a complex oxide represented by a general formula ABO 3 , where

the A-site is composed of a lanthanoid (La) and barium (Ba),

the B-site is composed of iron (Fe), niobium (Nb) and palladium (Pd), and

fulfills {La x Ba (1-x) }{Fe y Nb (1-y) } (1-z) Pd z O 3 ,

where x is in a range of more than 0.30, but 0.95 or less, y is in a range of 0.07 or more, but 0.94 or less, and z is in a range of 0.01 or more, but 0.10 or less, and

the complex oxide has such a structure that the barium functions as a NOx storing agent, and the niobium act on the palladium to accelerate NO oxidation and NOx reduction,

the exhaust gas treating catalyst being disposed downstream of the trapping means in a flow-through direction of the exhaust gas.

2. The exhaust gas purification apparatus according to claim 1 ,

where x is in a range of more than 0.60, but less than 0.80, y is in a range of 0.63 or more, but 0.88 or less, and z is in a range of 0.02 or more, but 0.04 or less.

3. The exhaust gas purification apparatus according to claim 1 , further comprising:

an oxidation catalyst for oxidizing unburned hydrocarbons, carbon monoxide, nitrogen oxides, and a black smoke carbon component in the exhaust gas, the oxidation catalyst being disposed upstream of the trapping means in the flow-through direction of the exhaust gas.

4. An exhaust gas purification apparatus for reducing nitrogen oxides in an exhaust gas to purify the exhaust gas, comprising:

trapping means for trapping particulate matter in the exhaust gas; and

an exhaust gas treating catalyst for reducing nitrogen oxides in an exhaust gas to purify the exhaust gas, the exhaust gas treating catalyst containing a complex oxide represented by a general formula ABO 3 , where

the A-site is composed of a lanthanoid (La) and barium (Ba),

the B-site is composed of iron (Fe), niobium (Nb) and palladium (Pd),

further containing at least one additional precious metal (PM2) comprising Pt, Rh Ir and Ru, other than palladium (Pd), and

fulfills PM2/−{La x Ba (1-x) }{Fe y Nb (1-y) } (1-z) Pd z O 3 ,

where x is in a range of more than 0.30, but 0.95 or less, y is in a range of 0.07 or more, but 0.94 or less, and z is in a range of 0.01 or more, but 0.10 or less, and

the complex oxide has such a structure that the barium functions as a NOx storing agent, and the niobium act on the palladium to accelerate NO oxidation and NOx reduction,

the exhaust gas treating catalyst being disposed downstream of the trapping means in a flow-through direction of the exhaust gas.

5. The exhaust gas purification apparatus according to claim 4 ,

where x is in a range of more than 0.60, but less than 0.80, y is in a range of 0.63 or more, but 0.88 or less, and z is in a range of 0.02 or more, but 0.04 or less.

6. The exhaust gas purification apparatus according to claim 4 , further comprising:

an oxidation catalyst for oxidizing unburned hydrocarbons, carbon monoxide, nitrogen oxides, and a black smoke carbon component in the exhaust gas, the oxidation catalyst being disposed upstream of the trapping means in the flow-through direction of the exhaust gas.

7. An exhaust gas purification apparatus for reducing nitrogen oxides in an exhaust gas to purify the exhaust gas, comprising:

trapping means for trapping particulate matter in the exhaust gas; and

an exhaust gas treating catalyst for reducing nitrogen oxides in an exhaust gas to purify the exhaust gas, the exhaust gas treating catalyst containing a complex oxide represented by a general formula ABO 3 , where

the A-site is composed of a lanthanoid (La) and barium (Ba),

the B-site is composed of iron (Fe), niobium (Nb) and palladium (Pd),

further containing at least one additional precious metal (PM2) comprising Pt, Rh Ir and Ru, other than palladium (Pd), and

fulfills PM2/−{La x Ba (1-x) }{Fe y Nb (1-y) } (1-z) Pd z O 3 ,

where x is in a range of more than 0.30, but 0.95 or less, y is in a range of 0.07 or more, but 0.94 or less, and z is in a range of 0.01 or more, but 0.10 or less, and

the complex oxide has such a structure that the barium functions as a NOx storing agent, and the niobium act on the palladium to accelerate NO oxidation and NOx reduction,

the exhaust gas treating catalyst being disposed downstream of the trapping means in a flow-through direction of the exhaust gas,

wherein the at least one precious metal is contained in an amount of 0.1 wt. % or more based on the complex oxide.

8. The exhaust gas purification apparatus according to claim 7 ,

where x is in a range of more than 0.60, but less than 0.80, y is in a range of 0.63 or more, but 0.88 or less, and z is in a range of 0.02 or more, but 0.04 or less.

9. The exhaust gas purification apparatus according to claim 7 , further comprising:

an oxidation catalyst for oxidizing unburned hydrocarbons, carbon monoxide, nitrogen oxides, and a black smoke carbon component in the exhaust gas, the oxidation catalyst being disposed upstream of the trapping means in the flow-through direction of the exhaust gas.

Priority Claims (1)
JP 2008-280727 · Oct 31, 2008 · national
Continuity (2)
Division 13126965
Related Publication 20160001230A1 · Jan 7, 2016