JP2015183587A5 - - Google Patents

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JP2015183587A5
JP2015183587A5 JP2014060487A JP2014060487A JP2015183587A5 JP 2015183587 A5 JP2015183587 A5 JP 2015183587A5 JP 2014060487 A JP2014060487 A JP 2014060487A JP 2014060487 A JP2014060487 A JP 2014060487A JP 2015183587 A5 JP2015183587 A5 JP 2015183587A5
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exhaust gas
heat engine
case
mol parts
catalyst
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JP2014060487A
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JP2015183587A (en
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熱機関の排ガス中に含まれるCO,HC,NOを酸化する酸化触媒を備え、前記酸化触媒は、多孔質担体に担持される触媒活性成分として、Ptと、Zn,Ba,Ca,Pから選ばれる少なくとも一種とを含み、前記Zn,Ba,Ca,Pの含有量が、担体2mol部に対して、Baの場合は0.02〜0.5mol部、Caの場合は0.02〜0.5mol部、Znの場合は0.02〜0.7mol部、Pの場合は0.02〜1.4mol部であることを特徴とする熱機関の排ガス浄化装置。   An oxidation catalyst that oxidizes CO, HC, NO contained in the exhaust gas of the heat engine is provided, and the oxidation catalyst is selected from Pt, Zn, Ba, Ca, and P as catalytic active components supported on the porous carrier. The content of Zn, Ba, Ca, P is 0.02 to 0.5 mol part in the case of Ba and 0.02 to 0. 0 in the case of Ca with respect to 2 mol part of the support. An exhaust gas purifying apparatus for a heat engine, characterized by 5 mol parts, 0.02 to 0.7 mol parts in the case of Zn, and 0.02 to 1.4 mol parts in the case of P. 請求項1に記載の熱機関の排ガス浄化装置において、前記Zn,Ba,Ca,Pの含有量を、これら触媒活性成分の種類に関わりなく、担体2mol部に対して、0.02〜0.5mol部としたことを特徴とする熱機関の排ガス浄化装置。   2. The exhaust gas purifying apparatus for a heat engine according to claim 1, wherein the content of Zn, Ba, Ca, P is 0.02 to 0. 0 with respect to 2 mol parts of the support regardless of the type of the catalytically active component. An exhaust gas purifying device for a heat engine, characterized in that the amount is 5 mol. 請求項1及び請求項2のいずれか1項に記載の熱機関の排ガス浄化装置において、前記酸化触媒の触媒活性成分として、Ptと、Pと、Zn,Ba,Caから選ばれる少なくとも一種とを含むことを特徴とする熱機関の排ガス浄化装置。 The exhaust gas purification apparatus for a heat engine according to any one of claims 1 and 2 , wherein Pt, P, and at least one selected from Zn, Ba, and Ca are used as catalytic active components of the oxidation catalyst. A heat engine exhaust gas purification apparatus comprising: 請求項1から請求項3のいずれか1項に記載の熱機関の排ガス浄化装置において、前記排ガスの流れ方向に関し、前記酸化触媒の後段にNOx浄化触媒を設置することを特徴とする熱機関の排ガス浄化装置。 In the exhaust gas purifying apparatus of the heat engine according to any one of claims 1 to 3, it relates to a flow direction of the flue gas, the heat engine, characterized in placing the NOx purifying catalyst downstream of the oxidation catalyst Exhaust gas purification device. 請求項に記載の熱機関の排ガス浄化装置において、前記NOx浄化触媒の前段にNHを添加することを特徴とする熱機関の排ガス浄化装置。 The exhaust gas purification apparatus for a heat engine according to claim 4 , wherein NH 3 is added to the front stage of the NOx purification catalyst. 請求項4及び請求項5のいずれか1項に記載の熱機関の排ガス浄化装置において、前記NOx浄化触媒の後段に、排ガス中のCO,HC又はNHを酸化する触媒を更に設置したことを特徴とする熱機関の排ガス浄化装置。 In the exhaust gas purifying apparatus of the heat engine according to any one of claims 4 and 5, downstream of the NOx purifying catalyst, CO in the exhaust gas, that has been further established a catalyst for oxidizing HC or NH 3 An exhaust gas purification device for a heat engine. 請求項1から請求項6のいずれか1項に記載の熱機関の排ガス浄化装置において、前記酸化触媒には、触媒活性成分として、Pd,Ceから選ばれる少なくとも一種を更に含むことを特徴とする熱機関の排ガス浄化装置。 In the exhaust gas purifying apparatus of the heat engine according to any one of claims 1 to 6, wherein the oxidation catalyst, as a catalyst active component, Pd, characterized in that it further comprises at least one selected from Ce Exhaust gas purification device for heat engine. 請求項から請求項7のいずれか1項に記載の熱機関の排ガス浄化装置において、前記NOx浄化触媒は、ゼオライト担体上に、触媒活性成分として、V,Mn,Fe,Co,Ni,Cu,Zrから選ばれる少なくとも1種を担持してなることを特徴とする熱機関の排ガス浄化装置。 In the exhaust gas purifying apparatus of the heat engine according to any one of claims 7 claim 4, wherein the NOx purifying catalyst on the zeolite carrier, as a catalytically active ingredient, V, Mn, Fe, Co , Ni, Cu An exhaust gas purifying device for a heat engine, which carries at least one selected from Zr and Zr. 請求項1から請求項8のいずれか1項に記載の熱機関の排ガス浄化装置において、前記酸化触媒に流入する排ガスは、常に、CO及びHCの酸化反応における化学量論量よりも酸素過剰な雰囲気に保つことを特徴とする熱機関の排ガス浄化装置。 In the exhaust gas purifying apparatus of the heat engine according to any one of claims 1 to claim 8, the exhaust gas flowing into the oxidation catalyst is always oxygen excess than the stoichiometric amount in the oxidation reaction of CO and HC An exhaust gas purification device for a heat engine characterized by maintaining an atmosphere. CO及びHCの酸化反応における化学量論量よりも過剰な酸素雰囲気で燃料を燃焼する熱機関の排ガス流路に、多孔質担体に担持される触媒活性成分として、Ptと、Zn,Ba,Ca,Pから選ばれる少なくとも一種とを含み、前記Zn,Ba,Ca,Pの含有量が、担体2mol部に対して、Baの場合は0.02〜0.5mol部、Caの場合は0.02〜0.5mol部、Znの場合は0.02〜0.7mol部、Pの場合は0.02〜1.4mol部に調整された酸化触媒を設置し、排ガス中のCO,HC,NOを酸化することを特徴とする排ガス浄化方法。   Pt and Zn, Ba, Ca as catalytic active components supported on the porous carrier in the exhaust gas passage of a heat engine that burns fuel in an oxygen atmosphere in excess of the stoichiometric amount in the oxidation reaction of CO and HC , P, and the content of Zn, Ba, Ca, P is 0.02 to 0.5 mol parts in the case of Ba, and 0. 02 to 0.5 mol parts, in the case of Zn, 0.02 to 0.7 mol parts in the case of P, and in the case of P, an oxidation catalyst adjusted to 0.02 to 1.4 mol parts is installed, and CO, HC, NO in the exhaust gas An exhaust gas purification method characterized by oxidizing the gas. 多孔質担体と該多孔質担体上に担持された触媒活性成分を有し、前記触媒活性成分として、Ptと、Zn,Ba,Ca,Pから選ばれる少なくとも一種とを含み、前記Zn,Ba,Ca,Pの含有量が、担体2mol部に対して、Baの場合は0.02〜0.5mol部、Caの場合は0.02〜0.5mol部、Znの場合は0.02〜0.7mol部、Pの場合は0.02〜1.4mol部であることを特徴とするCO,HC,NOの酸化触媒。   A porous carrier and a catalytically active component supported on the porous carrier, the catalytically active component comprising Pt and at least one selected from Zn, Ba, Ca, P, and the Zn, Ba, The content of Ca and P is 0.02 to 0.5 mol parts in the case of Ba, 0.02 to 0.5 mol parts in the case of Ba, and 0.02 to 0 in the case of Zn with respect to 2 mol parts of the carrier. CO, HC, NO oxidation catalyst, characterized in that it is 0.02 to 1.4 mol parts in the case of 0.7 mol parts and P.
JP2014060487A 2014-03-24 2014-03-24 Emission control device, emission control method and emission control catalyst for heat engine Pending JP2015183587A (en)

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JP2017155695A (en) * 2016-03-03 2017-09-07 いすゞ自動車株式会社 Exhaust emission control device of internal combustion engine
US11148954B2 (en) * 2017-05-15 2021-10-19 Basf Corporation Process for preparing a zeolitic material comprising a metal M and having framework type AEI

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JPS5522357A (en) * 1978-08-08 1980-02-18 Nippon Shokubai Kagaku Kogyo Co Ltd Monolithic catalyst for purification of waste gas
US8006484B2 (en) * 2005-02-14 2011-08-30 Eaton Corporation Systems and methods for reducing emissions of internal combustion engines using a fuel processor bypass
TWI449572B (en) * 2006-11-29 2014-08-21 Umicore Shokubai Japan Co Ltd Oxidation catalyst and the oxidation catalyst using an exhaust gas purification system
JP5456353B2 (en) * 2009-03-31 2014-03-26 日本碍子株式会社 Honeycomb filter
WO2013147273A1 (en) * 2012-03-30 2013-10-03 日本碍子株式会社 Heating method of honeycomb structure
WO2013172128A1 (en) * 2012-05-14 2013-11-21 エヌ・イーケムキャット株式会社 Exhaust gas purifier

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