JPH0952024A - Exhaust gas purifying material and exhaust gas purifying method - Google Patents

Abstract

PROBLEM TO BE SOLVED: To efficiently reduce and remove nitrogen oxides by specifying active species of respective catalysts and their deposition amounts as for a catalyst system in which an exhaust gas containing oxygen and nitrogen oxides is at first led to a catalyst of a mixture of silver and tungsten and then led to a catalyst carrying metals selected from silver, copper, and nickel together with rare earth metals and alkali metals. SOLUTION: Nitrogen oxides containing nitrogen oxides and oxygen in an excess amount of the theoretical reaction amount to unburned components coexisting with the nitrogen oxides are removed by reduction. At that time, an exhaust gas purifying agent to be employed consists of a first catalyst, a second catalyst, and a third catalyst, and a mixture of the first catalyst and the second catalyst is installed in the exhaust gas flowing-in side and the third catalyst is installed in the flowing-out side. The first catalyst is produced by depositing 0.2-15wt.% of silver and silver compounds in a porous inorganic oxide and the second catalyst is likewise produced by depositing 0.01-10wt.% of compounds of W, V, etc. The third catalyst is produced by depositing 0.5-30wt.% of silver, copper, nickel, and/or their compounds and at most 5wt.% of rare earth metals and alkali metals on a porous inorganic oxide.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

The present invention relates to an exhaust gas purifying material capable of effectively reducing and removing nitrogen oxides from a combustion exhaust gas containing nitrogen oxides and excess oxygen, and a purification method using the same.

[0002]

2. Description of the Related Art Excessive combustion exhaust gas emitted from internal combustion engines such as automobile engines, combustion equipment installed in factories, household fan heaters, and the like is excessive. It contains nitrogen oxides such as nitric oxide and nitrogen dioxide together with oxygen. Here, "containing excess oxygen" means that the exhaust gas contains more oxygen than the theoretical amount of oxygen necessary to burn unburned components such as carbon monoxide, hydrogen, and hydrocarbons. I do. In the following, nitrogen oxide refers to nitric oxide and / or nitrogen dioxide.

[0003] This nitrogen oxide is one of the causes of acid rain and is a major environmental problem. Therefore, various methods for removing nitrogen oxides in exhaust gas discharged from various combustion equipments are being studied.

[0004] As a method for removing nitrogen oxides from a combustion exhaust gas containing excess oxygen, a selective catalytic reduction method using ammonia is used particularly for a large-scale fixed combustion device (a large-scale combustor in a factory or the like). Has been put to practical use.

However, in this method, ammonia used as a reducing agent for nitrogen oxides is expensive, and ammonia is toxic. Therefore, the nitrogen oxides in the exhaust gas must be removed so that unreacted ammonia is not discharged. There are problems that the amount of injected ammonia must be controlled while measuring the concentration, and that the apparatus generally becomes large.

As another method, there is a non-selective catalytic reduction method in which a nitrogen oxide is reduced by using a gas such as hydrogen, carbon monoxide, or a hydrocarbon as a reducing agent. In order to reduce and remove nitrogen oxides, it is necessary to add a reducing agent in an amount equal to or more than a theoretical reaction amount with oxygen in exhaust gas, and there is a disadvantage that a large amount of the reducing agent is consumed. For this reason, the non-selective catalytic reduction method is practically effective only for exhaust gas having a low residual oxygen concentration burned near the stoichiometric air-fuel ratio, and is not practical because of poor versatility.

In view of the above, a method has been proposed for removing nitrogen oxides by using a zeolite or a catalyst carrying a transition metal on the zeolite and adding a reducing agent having a theoretical reaction amount or less with oxygen in exhaust gas (for example, Japanese Patent Application Laid-Open No. H11-157572). Kaisho 63-100919, 63-283727
No., Japanese Patent Application Laid-Open No. 1-130735). Also, a method of decomposing nitrogen oxides in exhaust gas while supplying a hydrocarbon gas using a catalyst in which an alkaline earth metal and / or silver is supported on a carrier such as γ-alumina (JP-A-4-354536) Method for reducing and removing nitrogen oxides in exhaust gas using a catalyst comprising alumina and silver-containing silica or zirconia while supplying hydrocarbons or oxygen-containing compounds (Japanese Patent Laid-Open No. 7-2)
No. 4261).

However, according to these methods, effective removal of nitrogen oxides can be obtained only in a narrow temperature range, and in the case of exhaust gas from a vehicle or the like which contains water and whose exhaust gas temperature greatly changes depending on operating conditions, The nitrogen oxide removal rate is significantly reduced.

Accordingly, it is an object of the present invention to provide a method for producing nitrogen oxides, carbon monoxide, hydrogen, hydrocarbons, and the like, such as combustion exhaust gas from a fixed combustion device and a gasoline engine, a diesel engine, or the like, which burns under oxygen excess conditions. By providing an exhaust gas purifying material and an exhaust gas purifying method capable of efficiently reducing and removing nitrogen oxides from combustion exhaust gas containing oxygen in excess of the theoretical reaction amount with respect to unburned components and containing sulfur oxides and moisture. is there.

[0010]

Means for Solving the Problems In view of the above-mentioned problems, as a result of intensive studies, the present inventors have found that a catalyst comprising a porous inorganic oxide carrying a silver component and a porous inorganic oxide carrying a W-based component. An organic compound such as ethanol reacts with exhaust gas containing oxygen and nitrogen oxides on the mixed catalyst obtained by mixing the catalysts, and reduces nitrogen oxides to nitrogen gas even in exhaust gas containing moisture, sulfur dioxide, etc. In addition, they have found that nitrogen-containing compounds such as nitrites and ammonia and aldehydes are produced as by-products. One or more of silver, copper, nickel, and rare earths capable of effectively reducing nitrogen-containing compounds to nitrogen under exhaust gas conditions containing nitrogen-containing compounds such as nitrites, ammonia, etc. and aldehydes generated with a mixed catalyst of silver and W, and rare earths Using an exhaust gas purifying material obtained by combining a catalyst comprising an element and an alkali metal with the mixed catalyst,
If any of hydrocarbons and oxygen-containing organic compounds having 2 or more carbon atoms or a fuel containing them is added to the exhaust gas, and the exhaust gas is brought into contact with the above-mentioned purifying material at a specific temperature and space velocity,
It has been discovered that nitrogen oxides can be effectively removed in a wide temperature range, and furthermore, by placing a platinum-based or platinum- and W-based catalyst behind the purifying material, the residual carbon monoxide, hydrocarbons and SOF in the exhaust gas can be reduced. (Soluble organic components) can be removed, and particularly by using platinum and a W-based catalyst,
The inventors have found that oxidation of sulfur dioxide can be suppressed in exhaust gas containing sulfur dioxide, and completed the present invention.

That is, the first exhaust gas purifying material of the present invention for reducing and removing nitrogen oxides from a combustion exhaust gas containing nitrogen oxides and oxygen in an amount larger than the theoretical reaction amount of coexisting unburned components is a first catalyst, The first catalyst comprises a second catalyst and a third catalyst. (1) The first catalyst comprises a porous inorganic oxide and one or more elements and / or compounds selected from the group consisting of silver and silver compounds. (2) the second catalyst is a porous inorganic oxide formed of at least one selected from the group consisting of W, V, Mo, Mn, Nb, and Ta. (3) the third catalyst is a porous inorganic oxide, which is composed of silver as an active species;
One or more elements and / or compounds selected from the group consisting of copper and nickel 0.5 to 30% by weight (in terms of metal element)
And 5% by weight or less (element conversion value) of one or more elements selected from the group consisting of rare earth elements and alkali metal elements, and the first catalyst and the first catalyst are disposed on the exhaust gas inflow side of the exhaust gas purifying material. The mixed catalyst obtained by mixing the second catalyst and the second catalyst is provided with the third catalyst on the outflow side.

[0012] The second exhaust gas purifying material of the present invention for reducing and removing nitrogen oxides from a combustion exhaust gas containing nitrogen oxides and oxygen larger than the theoretical reaction amount of coexisting unburned components is a first catalyst, a second catalyst. , A third catalyst and a fourth catalyst. (1) The first catalyst comprises a porous inorganic oxide and one or more elements selected from the group consisting of silver and silver compounds and / or a compound 0 (2) the second catalyst is selected from the group consisting of W, V, Mo, Mn, Nb, and Ta on a porous inorganic oxide. Compound of at least one element selected from 0.01 to 10
% (In terms of metal element), and (3) the third catalyst is composed of a porous inorganic oxide and silver as an active species.
One or more elements and / or compounds selected from the group consisting of copper and nickel 0.5 to 30% by weight (in terms of metal element)
And at least one element selected from the group consisting of a rare earth element and an alkali metal element in an amount of 5% by weight or less (in terms of element). (4) The fourth catalyst contains Pt on a porous inorganic oxide. , Pd, Ru, Rh, Ir and Au, at least one element selected from the group consisting of 0.01 to 5% by weight.
A mixed catalyst comprising the first catalyst and the second catalyst mixed in order from the exhaust gas inflow side to the outflow side of the exhaust gas purifying material, and the third catalyst , And a fourth catalyst.

[0013] The third exhaust gas purifying material of the present invention for reducing and removing nitrogen oxides from a combustion exhaust gas containing nitrogen oxides and oxygen in an amount larger than the theoretical reaction amount for coexisting unburned components is a first catalyst, a second catalyst, , A third catalyst and a fourth catalyst. (1) The first catalyst comprises a porous inorganic oxide and one or more elements selected from the group consisting of silver and silver compounds and / or a compound 0 (2) the second catalyst is selected from the group consisting of W, V, Mo, Mn, Nb, and Ta on a porous inorganic oxide. Compound of at least one element selected from 0.01 to 10
% (In terms of metal element), and (3) the third catalyst is composed of a porous inorganic oxide and silver as an active species.
One or more elements and / or compounds selected from the group consisting of copper and nickel 0.5 to 30% by weight (in terms of metal element)
And at least one element selected from the group consisting of a rare earth element and an alkali metal element in an amount of 5% by weight or less (element conversion value). , V, Mo, Mn, Nb, Ta, a compound of at least one element selected from the group consisting of 0.2 to 10% by weight (in terms of a metal element), Pt, Pd, Ru, Rh, I,
at least one element selected from the group consisting of r and Au (in terms of a metal element) in an amount of 0.01 to 5% by weight (in terms of a metal element). It has a mixed catalyst obtained by mixing one catalyst and the second catalyst, the third catalyst, and a fourth catalyst.

The exhaust gas purifying method of the present invention for reducing and removing nitrogen oxides from a combustion exhaust gas containing nitrogen oxides and oxygen which is larger than the theoretical reaction amount of coexisting unburned components uses the above exhaust gas purifying material, An exhaust gas purifying material is installed in the middle of the exhaust gas conduit, and hydrocarbons and / or
Alternatively, the exhaust gas to which the oxygen-containing organic compound is added is
The method is characterized in that the nitrogen oxides are removed by contacting the purification material at 00 ° C. and reacting with hydrocarbons and / or oxygen-containing organic compounds in the exhaust gas.

[0015]

BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail. [1] Exhaust gas purifying material The first exhaust gas purifying material of the present invention comprises a first catalyst, a second catalyst, and a third catalyst. The first catalyst and the second catalyst are provided on the exhaust gas inflow side. The mixed catalyst obtained by mixing is provided with the third catalyst on the outflow side. The second and third exhaust gas purifying materials of the present invention include a first catalyst, a second catalyst, a third catalyst, and a fourth catalyst, and the first catalyst and the first catalyst are sequentially arranged from an exhaust gas inflow side to an outflow side. It has a mixed catalyst obtained by mixing a second catalyst, the third catalyst, and the fourth catalyst.

In the present invention, the above-mentioned purifying material is installed in an exhaust gas conduit, and either hydrocarbon or an oxygen-containing organic compound having 2 or more carbon atoms or a fuel containing the same is added upstream of the purifying material installation position. The exhaust gas is brought into contact with the purifying material to reduce and remove nitrogen oxides in the exhaust gas.

A first preferred embodiment of the exhaust gas purifying material of the present invention is a powdery porous inorganic oxide having a catalytically active species supported thereon, among first, second, third and fourth catalysts. A purifying material obtained by coating one or more purifying material bases. As the ceramic material forming the base of the purifying material, cordierite, mullite, alumina and a composite thereof are preferably used. In addition, a known metal material can be used for the base of the exhaust gas purifying material.

The shape and size of the substrate of the exhaust gas purifying material
Various changes can be made according to the purpose. Also, as its structure,
Examples include a honeycomb structure type, a foam type, a three-dimensional network structure type made of a fibrous refractory, a granular form, a pellet form, and the like. The catalyst may be coated on the substrate using a wash coat method, a powder method, or the like, or a wash coat method, a sol
After coating the porous inorganic oxide using a gel method or the like, the catalytically active species can be supported using a known impregnation method, an ion exchange method, or the like.

A second preferred form of the exhaust gas purifying material of the present invention is a catalyst comprising a porous inorganic oxide in the form of pellets, granules, powders, honeycombs or plates carrying a catalytically active species, or a catalyst. It is a purifying material obtained by molding a powdery porous inorganic oxide carrying each active species into pellets or granules and filling the resultant into a casing having a desired shape.

The following catalyst is formed on the purifying material of the present invention. (1) First catalyst The first catalyst comprises a porous inorganic oxide carrying one or more elements and / or compounds selected from the group consisting of silver and silver compounds, and performs nitrogen oxidation in a wide temperature range. Acts on object removal. As the porous inorganic oxide, alumina alone, or titania, silica, zirconia, zinc oxide, tin oxide,
A composite or mixed oxide of either magnesium oxide or zeolite and alumina can be used. It is preferable that the alumina content is 50% by weight or more. The use of alumina or a composite or mixed oxide of alumina improves the heat resistance and durability of the catalyst. Here, the tin oxide includes tin oxide in various oxidation states, and examples of the main tin oxide include stannous oxide and stannic oxide.

The specific surface area of the porous inorganic oxide such as alumina used for the first catalyst is preferably 10 m ² / g or more. If the specific surface area is less than 10 m ² / g, the dispersion of the silver component is reduced, and good removal of nitrogen oxides cannot be performed.
More preferable specific surface area of the porous inorganic oxide is 30 m ² /
g or more.

The silver compound is at least one selected from the group consisting of silver oxide, silver halide, silver sulfate and silver phosphate, and preferably at least one of silver oxide, silver chloride and silver sulfate. And more preferably silver oxide and / or silver chloride. The supported amount of the silver component is 0.2 to 15% by weight (in terms of silver element) based on 100% by weight of the porous inorganic oxide. If the amount is less than 0.2% by weight, the removal rate of nitrogen oxides decreases. If the silver component is carried in an amount exceeding 15% by weight, the combustion of the hydrocarbon and / or the oxygen-containing organic compound itself tends to occur, and the nitrogen oxide removal rate is rather lowered. A preferable loading amount of the silver component is 0.5 to 12% by weight.
It is.

As a method of supporting silver on an inorganic oxide such as alumina, a known impregnation method, precipitation method, or the like can be used. When using the impregnation method, the porous inorganic oxide is immersed in an aqueous solution of silver nitrate, chloride, sulfate, carbonate, or the like, or an aqueous ammonia solution. Alternatively, the porous inorganic oxide is immersed in an aqueous solution of silver nitrate, dried, and then immersed again in an aqueous solution of ammonium chloride or ammonium sulfate. To prepare silver halide by the precipitation method, silver nitrate and ammonium halide are reacted to precipitate silver halide on the porous inorganic oxide. After drying at 50 to 150 ° C., particularly at about 70 ° C., it is preferable to raise the temperature stepwise at 100 to 600 ° C. for firing. The calcination is preferably performed in air, under a stream of nitrogen containing oxygen or under a stream of hydrogen gas. When the treatment is performed under a hydrogen gas stream, it is preferable to perform the oxidation treatment at 300 to 650 ° C. at last.

(2) Second catalyst The second catalyst comprises W, V, Mo, M
It supports a compound of at least one element selected from the group consisting of n, Nb, and Ta. As the porous inorganic oxide, any of alumina, titania, zeolite, silica, and zirconia, or a composite or mixed oxide containing them can be used. Various zeolites such as ferrierite, mortenite, and ZSM-5 can be used as the zeolite. Similar to the first catalyst, the specific surface area of the porous inorganic oxide is preferably 10 m ² / g or more.

The compound of W, V, Mo, Mn, Nb and Ta is preferably an oxide. 10 porous inorganic oxides
Assuming 0% by weight, the loading amount of the W-based component is 0.01 to 10% by weight (in terms of a metal element), preferably 0.05 to 10%.
It is 8% by weight (in terms of metal element).

W, V, Mo, inorganic oxides such as alumina
As a method for supporting Mn, Nb, and Ta, a known impregnation method, precipitation method, or the like can be used. Specifically, a porous inorganic oxide is immersed and used in a solution of a salt compound of each element, for example, a solution obtained by adding oxalic acid to an ammonium salt. After drying at 50 to 150 ° C., particularly at about 70 ° C., it is preferable to raise the temperature stepwise at 100 to 600 ° C. for firing. This calcination is performed in air under a nitrogen stream containing oxygen. It is also an effective method to use metatitanic acid (hydrous titanium oxide) as a starting material instead of titania and to carry V, W, and Mo. When zeolite is used as the inorganic oxide, it is preferable to support the zeolite by an impregnation method or a known ion exchange method.

In the present invention, a mixed catalyst obtained by mixing the first catalyst and the second catalyst is used. This mixing allows the catalysis of the first catalyst and the catalysis of the second catalyst to proceed simultaneously without affecting each other. The weight ratio of the first catalyst to the second catalyst (the ratio of the total weight of the porous inorganic oxide and the catalytically active species) is preferably 1:10 to 20: 1. More preferably, the weight ratio of the first catalyst to the second catalyst is 1: 5 to 10: 1.

When the form of the purifying material is the first preferred embodiment described above, the thickness of the mixed catalyst provided on the purifying material base generally depends on the difference in thermal expansion characteristics between the base material and the mixed catalyst. Is often restricted from. The thickness of the catalyst provided on the purifying material base is preferably 300 μm or less. With such a thickness, it is possible to prevent the purifying material from being damaged by thermal shock or the like during use. A method for forming a catalyst on the surface of the purifying material base is performed by a known wash coat method or the like.

The amount of the mixed catalyst provided on the surface of the purifying material base is preferably 20 to 300 g / liter of the purifying material base. If the amount of the catalyst is less than 20 g / liter, good NOx removal cannot be performed. On the other hand, when the amount of the catalyst is 300
When the amount exceeds g / liter, the removal characteristics do not increase so much.
Pressure loss increases. More preferably, the mixed catalyst provided on the surface of the purification material substrate is 50 to 200 g of the purification material substrate.
/ Liter.

(3) Third Catalyst The third catalyst is a porous inorganic oxide, comprising nickel as a catalytically active species, one or more elements and / or compounds selected from the group consisting of silver and copper, and a rare earth element. And one or more elements selected from the group consisting of alkali metal elements. As the porous inorganic oxide, any one of alumina, titania, zeolite, silica, zirconia and the like, or a composite or mixed oxide containing them is used. Various zeolites such as ferrierite, mortenite, and ZSM-5 can be used as the zeolite. Like the first catalyst, the specific surface area of the porous inorganic oxide is 10 m ² /
g or more.

The nickel compound is at least one selected from the group consisting of nickel oxides, halides, sulfates and the like. The same silver compound as the above-mentioned first catalyst can be used. The copper compound is at least one selected from the group consisting of copper oxides, halides, sulfates and the like. Assuming that the porous inorganic oxide is 100% by weight,
The total carrying amount of silver, copper and nickel is 0.5 to 30% by weight
(Metal element conversion value), and the preferable total supported amount is 1 to 1.
It is 25% by weight (in terms of metal element).

When the nickel component and the silver component are used at the same time, the weight ratio between the nickel element and the silver element is 1: 5 to 5: 1.
Similarly, the weight ratio between the nickel element and the copper element is 1: 5.
５5: 1, and the weight ratio of silver element to copper element is 1: 5
The ratio is preferably 5: 1.

Preferred rare earth elements are La, Ce, Y, N
d, and preferred alkali metal elements are Na, K, C
s and Li. Alkali metal elements and / or
Alternatively, by using a rare earth element, the durability of the catalyst is improved, and the characteristic of removing nitrogen oxides by residual hydrocarbons is improved. Assuming that the porous inorganic oxide is 100% by weight, the total carrying amount of the rare earth element and the alkali metal element is 5% by weight or less (element conversion value), preferably 4% by weight or less (element conversion value).

The active species can be supported by a known impregnation method, precipitation method,
An ion exchange method or the like can be used. When using the impregnation method, the porous inorganic oxide is immersed in an aqueous solution of a carbonate, nitrate, acetate, sulfate or the like of the catalytically active species element. In the case of a copper or nickel component, an aqueous solution of an acetate, a sulfate, a nitrate or the like is used. After drying at 50-150 ° C, especially 70 ° C, 100-
This is carried out by raising the temperature stepwise at 600 ° C. and firing. This calcination is performed in air under a nitrogen stream containing oxygen. When zeolite is used as the inorganic oxide, it is effective to carry the zeolite by an impregnation method or a known ion exchange method. The loading of the silver catalyst can be carried out in the same manner as in the first catalyst. On the third catalyst thus prepared,
Silver, nickel, and copper exist in the form of silver, nickel, copper, or any of their oxides, halides, and sulfates, respectively.

Weight ratio of first and second mixed catalysts to third catalyst (ratio of total weight of porous inorganic oxide and catalytically active species)
Is preferably 1: 5 to 20: 1. More preferably, the weight ratio of the first and second mixed catalysts to the third catalyst is 1: 2 to
10: 1.

In the case where the purifying material is in the above-described first preferred embodiment, the thickness of the third catalyst provided on the purifying material base is preferably 300 μm or less. The amount of the third catalyst provided on the surface of the purifying material base is preferably 20 to 300 g / liter based on the purifying material base.

(4) Fourth Catalyst The second exhaust gas purifying material and the third exhaust gas purifying material of the present invention are, in addition to the first catalyst, the second catalyst and the third catalyst,
It has a fourth catalyst. The fourth catalyst has a porous inorganic oxide carrying a catalytically active species, is formed on the exhaust gas outflow side, acts to remove nitrogen oxides in a low temperature region, and has a function of removing carbon monoxide and hydrocarbons. Perform oxidation removal. As the porous inorganic oxide, it is preferable to use any of alumina, titania, zeolite, silica, zirconia and the like, or a composite or mixed oxide containing them. Like the first catalyst, the specific surface area of the porous inorganic oxide is 10 m ^2.
/ G or more.

In the second exhaust gas purifying material of the present invention, at least one element selected from the group consisting of Pt, Pd, Ru, Rh, Ir and Au is used as the active species of the fourth catalyst. Among Pt, Pd, Ru, Rh and Au, it is particularly preferable to use at least one of Pt, Pd and Au. Assuming that the porous inorganic oxide is 100% by weight, the supported amount of the platinum component is 0.01 to 5% by weight (in terms of a metal element).
It is. The preferable loading amount of the platinum component is 0.01 to 4% by weight (in terms of metal element).

In the third exhaust gas purifying material of the present invention, the active species of the fourth catalyst is W, V, Mo, Mn, Nb, Ta.
And at least one element selected from the group consisting of Pt, Pd, Ru, Rh, Ir, and Au. W,
Of V, Mo, Mn, Nb and Ta, it is preferable to use W and / or V, and Pt, Pd, Ru, Rh and Au
Among them, it is particularly preferable to use at least one of Pt, Pd and Au. Assuming that the porous inorganic oxide is 100% by weight, the supported amount of the W-based component is 0.2 to 10% by weight (in terms of a metal element), and the supported amount of the platinum-based component is 0.01 to 5%.
% By weight (in terms of metal element). The preferred amount of the W-based component is 0.2 to 9% by weight (in terms of a metal element),
The preferable loading amount of the platinum component is 0.01 to 4% by weight (in terms of metal element).

By using a Pt-based or Pt / W-based catalyst, residual carbon monoxide, hydrocarbons, SOF and the like in exhaust gas can be effectively oxidized and removed. In particular, when a Pt or W-based catalyst is used, even in an exhaust gas containing sulfur dioxide, the oxidation of sulfur dioxide is suppressed, and residual carbon monoxide, hydrocarbons,
SOF and the like can be effectively oxidized and removed.

For supporting the active species on the fourth catalyst, a known impregnation method, precipitation method or the like can be used. When the impregnation method is used, the porous inorganic oxide is immersed in an aqueous solution of a carbonate, nitrate, acetate, sulfate, chloride, hexachlorometal acid, or dinitrodiamine metal compound of a catalytically active species element. After drying at 50-150 ° C, especially 70 ° C, 100-6
It is carried out by raising the temperature stepwise at 00 ° C. and firing. This calcination is performed in air under a nitrogen stream containing oxygen.
In the case of W, V, Mo, Mn, Nb, and Ta, loading can be performed by the method described for the second catalyst.

The ratio of the weight of the first and second mixed catalysts to the weight of the fourth catalyst (the ratio of the total weight of the porous inorganic oxide and the catalytically active species) is 1: 2 to 10: 1. Is preferred. When the ratio is less than 1: 2 (the amount of the mixed catalyst is small), the nitrogen oxide purification rate decreases. On the other hand, when the ratio exceeds 10: 1 and the amount of the fourth catalyst is small, hydrocarbon, carbon monoxide, S
The oxidation characteristics of OF decrease. A more preferred ratio of the weight of the mixed catalyst to the weight of the fourth catalyst is from 1: 1 to 10: 1.

When the form of the purifying material is the first preferred embodiment described above, the thickness of the fourth catalyst provided on the purifying material base is preferably 300 μm or less. The amount of the fourth catalyst provided on the surface of the purifying material base is preferably 20 to 300 g / liter based on the purifying material base.

If the purifying material having the above-described structure is used, 150
In a wide temperature range of up to 600 ° C., good removal of nitrogen oxides can be performed even with an exhaust gas containing about 10% of moisture and sulfur oxides.

Next, the method of the present invention will be described. First, in the first purifying material of the present invention, the exhaust gas purifying material is a mixed catalyst of the first catalyst and the second catalyst facing the exhaust gas inflow side,
The third catalyst is installed in the exhaust gas conduit so as to face the outflow side. In the second and third purifying materials of the present invention, a mixed catalyst obtained by mixing the first catalyst and the second catalyst in order from the exhaust gas inflow side to the outflow side, the third catalyst, the fourth catalyst Is installed in the exhaust gas conduit.

The exhaust gas contains ethylene, propylene, etc. to a certain extent as residual hydrocarbons. However, since the amount is generally not sufficient to reduce NOx in the exhaust gas, hydrocarbons and / or oxygen-containing organic substances are supplied from outside. A compound, preferably an oxygen-containing organic compound or a reducing agent obtained by mixing the compound with a hydrocarbon fuel is introduced into the exhaust gas. The introduction position of the reducing agent
It is upstream from the position where the purifying material is installed.

As the hydrocarbons introduced from the outside, gaseous or liquid alkanes, alkenes and / or alkynes can be used under standard conditions. In particular, alkanes preferably have 2 or more carbon atoms. Specific examples of the hydrocarbon in a liquid state in a standard state include hydrocarbons such as light oil, cetane, heptane, kerosene, and gasoline. Among them, boiling point 5
Hydrocarbons at 0-350 ° C are particularly preferred. As the oxygen-containing organic compound introduced from the outside, alcohols such as ethanol and isopropyl alcohol having 2 or more carbon atoms, or a fuel containing them can be used.

The amount of the hydrocarbon and / or oxygen-containing organic compound introduced from the outside is determined by the weight ratio (weight of the reducing agent to be added / weight).
(Weight of nitrogen oxides in the exhaust gas) is preferably 0.1 to 5. If the weight ratio is less than 0.1, the removal rate of nitrogen oxides does not increase. On the other hand, if it exceeds 5, fuel efficiency will be degraded.

When a fuel containing a hydrocarbon or an oxygen-containing organic compound is added, it is preferable to use gasoline, light oil, kerosene or the like as the fuel. In this case, the amount of the reducing agent is set such that the weight ratio (the weight of the reducing agent to be added / the weight of the nitrogen oxide in the exhaust gas) is 0.1 to 5 in the same manner as described above.

In the present invention, the space velocity of the mixed catalyst of the first catalyst and the second catalyst is set to 200,000 in order to efficiently promote the reduction and removal of nitrogen oxides by the oxygen-containing organic compound and the hydrocarbon. h ^-1 or less, preferably 150,000 h ^-1
The following is assumed. The space velocity of the third catalyst 200,000 ^-1 or less, preferably 150,000H ^-1 or less. The space velocity of the fourth catalyst is 200,000 h ^-1 or less, preferably 150,000 h ^-1.
The following is assumed.

Further, in the present invention, the temperature of the exhaust gas at the purification material installation site, which is the site where the hydrocarbon and / or the oxygen-containing organic compound reacts with the nitrogen oxide, is set to 150 to 600 ° C.
To keep. If the temperature of the exhaust gas is lower than 150 ° C., the reaction between the reducing agent and the nitrogen oxide does not proceed, and it is not possible to remove the nitrogen oxide satisfactorily. On the other hand, if the temperature exceeds 600 ° C., the combustion of the hydrocarbon and / or the oxygen-containing organic compound itself starts, and the reduction and removal of nitrogen oxides cannot be performed. The preferred exhaust gas temperature is from 200 to 550 ° C, more preferably from 250 to 550 ° C.

[0052]

The present invention will be described in more detail with reference to the following specific examples. Example 1 Commercially available silica-alumina powder (silica content 5% by weight,
^3. Using an aqueous solution of silver nitrate to a specific surface area of 350 m ² / g).
1% by weight (in terms of metal element) of silver was supported, dried, and fired stepwise in air to 600 ° C. to prepare a silver-based silver catalyst (first catalyst).

Put ammonium tungstate in water,
A commercially available powdery γ-
After injecting and impregnating alumina (specific surface area: 200 m ² / g), the γ-alumina powder is separated from the solution, heated to 600 ° C. in air in a stepwise manner, and calcined to obtain 4.3 wt. % (Converted to metal element), to prepare a W-based catalyst (second catalyst).

After 0.2 g of the first catalyst and 0.06 g of the second catalyst were mixed and slurried, a commercially available cordierite honeycomb molded body (diameter: 20 mm, length: 8.3 m)
m, 400 cells / inch ² ) and after drying 600
By sintering stepwise to ° C., a W and silver-based exhaust gas purifying material (a purifying material coated with a first catalyst and a second catalyst) was prepared.

Using a copper nitrate, nickel nitrate, lanthanum nitrate, and cesium nitrate aqueous solution, 4.4% by weight of copper and 7.0% by weight of
Nickel, 0.3% by weight lanthanum and 0.3% by weight
Cesium (each metal element conversion value), copper,
A nickel-based catalyst (third catalyst) was prepared. 0.26g
After the third catalyst of the above was slurried, a honeycomb-shaped formed body (diameter 20 mm, length 8.3 m
m, 400 cells / inch ² ) and after drying 600
The mixture was calcined stepwise to ℃ to prepare a copper- and nickel-based exhaust gas purifying material (an exhaust gas purifying material coated with a third catalyst).

W and silver-based purifying materials were set on the inflow side of the exhaust gas in the reaction tube, and copper and nickel-based purifying materials were set on the outflow side. Next, a gas (nitrogen monoxide, oxygen, ethanol, sulfur dioxide, nitrogen and moisture) having a composition shown in Table 1 was flowed at a flow rate of 3.48 liters per minute (standard state) (apparent space velocity of each purification material). Were about 80,000 h ^-1 ), and the temperature of the exhaust gas in the reaction tube was kept in the range of 250 to 550 ° C., and ethanol and nitrogen oxides were reacted.

The concentration of nitrogen oxides in the gas after passing through the reaction tube was measured by a chemiluminescent nitrogen oxide analyzer to determine the nitrogen oxide removal rate. Table 2 shows the results.

Table 1 Component concentration Nitric oxide 800 ppm Oxygen 10% by volume Ethanol 1560 ppm Nitrogen Residual water 10% by volume (based on the total volume of the above components)

Example 2 Using an aqueous solution of copper nitrate, lanthanum nitrate, and cesium nitrate,
In the same manner as in Example 1, powdery silica-alumina (silica content 5% by weight, specific surface area 350 m ² / g) contains 4.4% by weight of copper, 0.3% by weight of lanthanum and 0.3% by weight of lanthanum. Cesium (each converted to a metal element) was supported to prepare a copper-based catalyst (third catalyst). After slurrying 0.26 g of the third catalyst, a honeycomb formed body (diameter 20 mm, length 8.3 mm, 400 cells / inch) was prepared in the same manner as in Example 1.
² ) Coated, dried and baked to 600 ° C step by step,
A copper-based exhaust gas purifying material (an exhaust gas purifying material coated with a third catalyst) was prepared.

Powdered titania (specific surface area 35 m ² / g)
Is immersed in chloroplatinic acid aqueous solution for 20 minutes,
Dried at 0 ° C. for 2 hours, under a nitrogen stream at 120 ° C. for 2 hours,
It was baked stepwise for 1 hour from 200 to 400 ° C. Then, under a nitrogen stream containing 4% of hydrogen gas, at 50 ° C. to 400 ° C.
And then calcined at 400 ° C. for 4 hours, and further heated to 50 ° C. to 500 ° C. under a nitrogen stream containing 10% oxygen.
And then calcined at 500 ° C. for 5 hours to carry 1% by weight (in terms of metal element) of platinum with respect to titania to prepare a platinum-based catalyst (fourth catalyst). After slurrying 0.18 g of the fourth catalyst, the same honeycomb formed body (diameter 20 mm, length 6.6 mm, 400 cells / inch ² ) as in Example 1 was coated in the same manner, and dried and fired. Platinum-based purification material (purification material coated with fourth catalyst)
Was prepared.

The W, silver-based purifying material, the copper-based purifying material, and the platinum-based purifying material of Example 1 were set in this order from the inflow side to the outflow side of the exhaust gas in the reaction tube. The same reaction conditions as in Example 1 (W,
The apparent space velocities of the silver-based purifying material and the copper-based purifying material are about 80,000 h ^-1 , respectively, and the apparent space velocity of the platinum-based purifying material is about 100,000 h ^-1 ). Evaluation was performed using gas. Table 2 shows the results.

Example 3 A commercially available powdery alumina (specific surface area: 200 m ² / g) was loaded with 3.0% by weight (in terms of metal element) of silver using an aqueous silver nitrate solution, dried, and stepwise dried in air. Was fired to 600 ° C. to prepare a silver-based catalyst (first catalyst) supporting silver.

In the same manner as in Example 1, commercially available powdered alumina (specific surface area: 200
m ² / g), molybdenum of 3.0% by weight (in terms of metal element) was supported, dried, and calcined in air stepwise to 600 ° C. to prepare a Mo-based catalyst (second catalyst). .

After 0.2 g of the first catalyst and 0.06 g of the second catalyst were mixed and slurried, a commercially available cordierite honeycomb molded body (diameter: 20 mm, length: 8.3 m)
m, 400 cells / inch ² ) and after drying 600
The resultant was baked stepwise to ℃ to prepare Mo and silver-based exhaust gas purifying materials (purifying materials coated with a first catalyst and a second catalyst).

Using a copper nitrate, cerium nitrate, and potassium nitrate aqueous solution, powdered alumina (specific surface area 200 m ² / g) was mixed with 7.0% by weight of copper, 0.3% by weight of cerium and A copper-based catalyst (third catalyst) was prepared by supporting 0.4% by weight of potassium (each converted to a metal element). After slurrying 0.26 g of the third catalyst, a honeycomb formed body (having a diameter of 20 m) was prepared in the same manner as in Example 1.
m, length 8.3 mm, 400 cells / inch ² ), dried, and fired stepwise to 600 ° C. to prepare a copper-based exhaust gas purifying material (an exhaust gas purifying material coated with a third catalyst).

Mo, a silver-based purifying material, a copper-based purifying material, and the platinum-based purifying material of Example 2 were set in order from the inflow side to the outflow side of the exhaust gas in the reaction tube. The same reaction conditions as in Example 1 (Mo,
The apparent space velocities of the silver-based purifying material and the copper-based purifying material are about 80,000 h ^-1 , respectively, and the apparent space velocity of the platinum-based purifying material is about 100,000 h ^-1 ). Evaluation was performed using gas. Table 2 shows the results.

Example 4 Commercially available powdered alumina (specific surface area: 200 m ² / g) was loaded with 1.2% by weight (in terms of metal element) of vanadium oxide using ammonium vanadate in the same manner as in Example 1. Then, after drying, the mixture was calcined in air stepwise to 600 ° C. to prepare a V-based catalyst (second catalyst).

0.2 g of the first catalyst of Example 3 and 0.0
After 6 g of the second catalyst was mixed and slurried, a commercially available cordierite honeycomb-shaped formed body (20 m in diameter) was obtained.
m, length 8.3 mm, 400 cells / inch ² ), dried and baked stepwise to 600 ° C, V, silver-based exhaust gas purifying material (purification coated with first and second catalysts) Material) was prepared.

In the same manner as in Example 1, 4.5% by weight of copper and 2.5% by weight of powdery titania (specific surface area: 35 m ² / g) were prepared using an aqueous solution of copper nitrate, nickel nitrate, and lanthanum nitrate.
, And 0.4% by weight of lanthanum (each converted to a metal element) to prepare a copper-nickel catalyst (third catalyst). After slurrying 0.26 g of the third catalyst, a honeycomb formed body (20 m in diameter) was prepared in the same manner as in Example 1.
m, length 8.3 mm, 400 cells / inch ² ), dried and baked stepwise to 600 ° C to prepare copper and nickel based exhaust gas purifying materials (exhaust gas purifying materials coated with a third catalyst). did.

In the same manner as in Example 2, powdery titania (specific surface area: 35 m ² / g) was loaded with 1% by weight (converted to metal element) of Pt with respect to titania using an aqueous chloroplatinic acid solution, and then vanadic acid was added. 3.3 wt% (converted to a metal element) of V oxide is supported on powdered titania on which platinum is supported in the same manner as the second catalyst using ammonium, and a V-platinum-based catalyst (fourth catalyst) ) Was prepared. After slurrying 0.18 g of the third catalyst, it was coated on a honeycomb-shaped formed body (diameter 20 mm, length 6.6 mm, 400 cells / inch ² ) in the same manner as in Example 1, dried, and stepwise heated to 600 ° C. To prepare a V, platinum-based exhaust gas purifying material (an exhaust gas purifying material coated with a fourth catalyst).

V, silver-based purifying material, copper, nickel-based purifying material, V, and platinum-based purifying material were set in order from the inflow side to the outflow side of the exhaust gas in the reaction tube. The same reaction conditions as in Example 1 (V, the apparent space velocity of the silver-based purifying material and the apparent space velocity of the copper and nickel-based purifying materials were respectively about 80,000 h ^-1 , and the apparent space velocity of the V- and platinum-based purifying materials was about 100 2,000 h ⁻¹ ), and evaluation was performed using a gas having a composition shown in Table 1.
Table 2 shows the results.

Example 5 In the same manner as in Example 1, copper alumina, nickel nitrate and sodium nitrate were used to prepare a powdery alumina (specific surface area: 200
m ² / g), supporting 4.4% by weight of copper, 5.0% by weight of nickel and 0.2% by weight of sodium (respectively in terms of metal elements). ) Was prepared. After slurrying 0.26 g of the third catalyst, it was coated on a honeycomb-shaped formed body (diameter 20 mm, length 8.3 mm, 400 cells / inch ² ) in the same manner as in Example 1, dried, and stepwise cooled to 600 ° C. To prepare a copper- and nickel-based exhaust gas purifying material (an exhaust gas purifying material coated with a third catalyst).

The W, silver-based purifying material, the copper and nickel-based purifying material of Example 1, and the platinum-based purifying material of Example 2 were set in this order from the inflow side to the outflow side of the exhaust gas in the reaction tube. Example 1
(W, silver-based purifying material and copper and nickel-based purifying materials each have an apparent space velocity of about 80,000 h ^-1.
And the apparent space velocity of the platinum-based purification material is about 100,0.
00h ^-1 ), and was evaluated using a gas having a composition shown in Table 1. Table 2 shows the results.

Example 6 Commercial powdery alumina (specific surface area: 200 m ² / g) and powdered stannic oxide (specific surface area: 71 m ² / g) were mixed in a ratio of 95: 5.
In the same manner as in Example 1, 4.1 wt% (in terms of a metal element) of silver was supported on the powder mixed in the same weight ratio as in Example 1, and after drying, it was gradually heated to 600 ° C. in air. By calcining, a silver-based catalyst (first catalyst) carrying silver was prepared.

After 0.2 g of the first catalyst and 0.06 g of the second catalyst of Example 1 were mixed and slurried, a commercially available cordierite honeycomb-shaped molded product (20 mm in diameter,
8.3 mm long, 400 cells / inch ² )
After drying, it is baked step by step to 600 ° C, W, silver-based exhaust gas purifying material (purifying material coated with first catalyst and second catalyst)
Was prepared.

The W, silver-based purifying material, copper and nickel-based purifying material of Example 1 were set in order from the inflow side to the outflow side of the exhaust gas in the reaction tube. Under the same reaction conditions as in Example 1 (the apparent space velocities of W, a silver-based purifying material, and copper and nickel-based purifying materials are each about 80,000 h ^-1 ), using a gas having a composition shown in Table 1. An evaluation was performed. Table 2 shows the results.

Comparative Example 1 A commercially available alumina powder (specific surface area: 200 m ² / g) was loaded with 3.0% by weight (in terms of a metal element) of silver using an aqueous silver nitrate solution, dried, and stepwise dried in air. By baking to 600 ° C., a silver-based catalyst (first catalyst) was prepared. 0.54 g of the first catalyst was used in the same manner as in Example 1 to obtain a commercially available cordierite honeycomb-shaped formed body (diameter: 20 mm, length: 16.6 m)
m, 400 cells / inch ² ) to prepare a silver-based exhaust gas purifying material.

The silver-based purifying material was set on the inflow side of the exhaust gas in the reaction tube, and the platinum-based purifying material of Example 2 was set on the outflow side. Under the same reaction conditions as in Example 1 (the apparent space velocity of the silver-based purifying material is about 40,000 h ^-1 and the apparent space velocity of the platinum-based purifying material is about 100,000 h ^-1 ). Evaluation was performed using a gas having the composition shown. Table 2 shows the results.

Table 2 Removal rate of nitrogen oxides (NOx) Removal rate of nitrogen oxides (%) Reaction temperature (° C.) 250 300 350 400 450 500 550 Example 1 76.0 90.3 80.8 68.6 56.0 41.0 34.3 Example 2 75.0 89.3 82.3 68.5 57.2 39.9 35.5 Example 3 73.3 87.5 80.6 68.3 58.3 54.0 43.2 Example 4 74.7 88.9 78.9 69.0 57.5 52.1 40.3 Example 5 77.2 90.5 77.2 67.0 56.0 42.5 35.6 Example 6 78.4 90.3 78.2 67.0 54.0 38.2 34.4 Comparative example 1 25.6 56.5 60.6 58.6 55.9 43.3 35.7

As can be seen from Table 2, as compared with Comparative Example 1 using a purifying material composed of a silver-based or Pt-based catalyst, in Examples 1 to 6 using the purifying material of the present invention, nitrogen in a wide exhaust gas temperature range was used. Good removal of oxides was observed.

[0081]

As described above in detail, the use of the exhaust gas purifying material of the present invention makes it possible to efficiently remove nitrogen oxides in exhaust gas containing excess oxygen in a wide temperature range. INDUSTRIAL APPLICABILITY The exhaust gas purifying material and the purification method of the present invention can be widely used for purifying exhaust gas of various types of combustors, automobiles and the like.

──────────────────────────────────────────────────続 き Continuation of the front page (51) Int.Cl. ⁶ Identification code Agency reference number FI Technical indication location B01J 23/68 B01J 23/76 A 23/76 29/068 A 29/068 29/076 A 29 / 076 B01D 53/36 102H 102A 102B 102C

Claims (8)

[Claims] 1. An exhaust gas purifying material for reducing and removing nitrogen oxides from a combustion exhaust gas containing nitrogen oxides and oxygen in an amount larger than a theoretical reaction amount of coexisting unburned components, wherein the exhaust gas purifying material is a first catalyst, The first catalyst comprises a second catalyst and a third catalyst. (1) The first catalyst comprises a porous inorganic oxide and one or more elements and / or compounds selected from the group consisting of silver and silver compounds. 15% by weight (silver element conversion value)
(2) the second catalyst comprises a porous inorganic oxide formed of a compound of at least one element selected from the group consisting of W, V, Mo, Mn, Nb, and Ta; 1
0% by weight (in terms of a metal element) and (3)
The third catalyst is a porous inorganic oxide, in which at least one element and / or compound selected from the group consisting of silver, copper, and nickel as active species is 0.5 to 30% by weight (in terms of a metal element), 5% by weight or less (element conversion value) of one or more elements selected from the group consisting of rare earth elements and alkali metal elements
And a mixed catalyst obtained by mixing the first catalyst and the second catalyst on the exhaust gas inflow side of the exhaust gas purifying material, and the third catalyst on the outflow side. Exhaust gas purifying material. 2. An exhaust gas purifying material for reducing and removing nitrogen oxides from a combustion exhaust gas containing nitrogen oxides and oxygen in an amount larger than a theoretical reaction amount of coexisting unburned components, wherein the exhaust gas purifying material is a first catalyst, It comprises a second catalyst, a third catalyst and a fourth catalyst. (1) The first catalyst comprises a porous inorganic oxide and one or more elements selected from the group consisting of silver and silver compounds and / or (2) The second catalyst comprises a porous inorganic oxide containing W, V, Mo, Mn, Nb, and Ta.
And (3) the third catalyst is active on a porous inorganic oxide. One or more elements and / or compounds selected from the group consisting of silver, copper, and nickel as seeds 0.5 to 30% by weight (in terms of metal elements) and one or more elements selected from the group consisting of rare earth elements and alkali metal elements (4) The fourth catalyst is selected from the group consisting of Pt, Pd, Ru, Rh, Ir, and Au on a porous inorganic oxide. At least one element;
A mixed catalyst which carries 01 to 5% by weight (in terms of a metal element) and which is obtained by mixing the first catalyst and the second catalyst in order from the exhaust gas inflow side to the outflow side of the exhaust gas purifying material;
An exhaust gas purifying material comprising the third catalyst and a fourth catalyst. 3. An exhaust gas purifying material for reducing and removing nitrogen oxides from a combustion exhaust gas containing nitrogen oxides and oxygen in an amount larger than a theoretical reaction amount of coexisting unburned components, wherein the exhaust gas purifying material is a first catalyst, It comprises a second catalyst, a third catalyst and a fourth catalyst. (1) The first catalyst comprises a porous inorganic oxide and one or more elements selected from the group consisting of silver and silver compounds and / or (2) The second catalyst comprises a porous inorganic oxide containing W, V, Mo, Mn, Nb, and Ta.
And (3) the third catalyst is active on a porous inorganic oxide. One or more elements and / or compounds selected from the group consisting of silver, copper, and nickel as seeds 0.5 to 30% by weight (in terms of metal elements) and one or more elements selected from the group consisting of rare earth elements and alkali metal elements (4) The fourth catalyst is selected from the group consisting of W, V, Mo, Mn, Nb, and Ta on a porous inorganic oxide. 0.2 to 10% by weight of a compound of at least one element (in terms of a metal element) and Pt, P
and at least one element selected from the group consisting of d, Ru, Rh, Ir, and Au, in a range of 0.01 to 5% by weight (in terms of a metal element), from the exhaust gas inflow side of the exhaust gas purifying material. An exhaust gas purifying material comprising: a mixed catalyst obtained by mixing the first catalyst and the second catalyst in order toward an outflow side; a third catalyst; and a fourth catalyst. 4. The exhaust gas purifying material according to claim 1, wherein said W, V, Mo, Mn, Nb, Ta.
Is an oxide, the silver compound is a silver oxide,
At least one selected from the group consisting of silver halide, silver sulfate and silver phosphate, wherein the nickel compound is nickel oxide and / or nickel sulfate; and the copper compound is copper oxide and / or copper An exhaust gas purifying material characterized by being a sulfate. 5. The exhaust gas purifying material according to claim 1, wherein the porous inorganic oxide is alumina alone in the first catalyst, or titania, silica, zirconia, zinc oxide, tin oxide, Magnesium oxide, composite or mixed oxide of any of zeolite and alumina, composite, or mixed of any of alumina, titania, zeolite, silica, zirconia or second or third catalyst, third catalyst and fourth catalyst An exhaust gas purifying material characterized by being an oxide. 6. The exhaust gas purifying material according to claim 1, wherein at least one of the first, second, third, and fourth catalysts is a ceramic or metal substrate. An exhaust gas purifying material characterized by being coated on the surface. 7. The exhaust gas purifying material according to claim 1, wherein at least one of the first, second, third, and fourth catalysts is in the form of a pellet, a granule, or a honeycomb. Or an exhaust gas purifying material having a plate shape. 8. The method for reducing nitrogen oxides from a combustion exhaust gas containing the nitrogen oxides and oxygen in an amount larger than the theoretical reaction amount for the co-existing unburned components, using the exhaust gas purifying material according to any one of claims 1 to 7. In the exhaust gas purifying method for removing, the exhaust gas purifying material is installed in the middle of an exhaust gas conduit, and the exhaust gas to which a hydrocarbon and / or an oxygen-containing organic compound is added at an upstream side of the purifying material is subjected to the purifying material at 150 to 600 ° C. Exhaust gas purifying method, wherein the nitrogen oxides are removed by contact with a hydrocarbon and / or an oxygen-containing organic compound in the exhaust gas.