JP3473295B2 - Catalyst carrier and catalyst for exhaust gas purification - Google Patents

Description

Detailed Description of the Invention

[0001]

TECHNICAL FIELD The present invention relates to an exhaust gas purifying catalyst for purifying exhaust gas emitted from an automobile engine or the like,
Regarding the carrier used for the catalyst, more specifically, nitrogen in exhaust gas containing oxygen in excess of the amount necessary to oxidize carbon monoxide (CO) and hydrocarbons (HC) contained in exhaust gas. The present invention relates to an exhaust gas purifying catalyst capable of efficiently purifying oxides (NO _x ) and a catalyst carrier used therefor.

[0002]

2. Description of the Related Art Conventionally, a three-way catalyst for purifying exhaust gas by simultaneously oxidizing CO and HC and reducing NO _x has been used as a catalyst for purifying exhaust gas of automobiles. As such a catalyst, for example, a catalyst in which a supporting layer made of γ-alumina is formed on a heat-resistant carrier such as cordierite and a noble metal catalyst such as Pt, Pd, Rh is supported on the supporting layer is widely known. There is.

By the way, the purification performance of such an exhaust gas purifying catalyst greatly differs depending on the air-fuel ratio (A / F) of the engine. That is, on the lean side where the air-fuel ratio is large, that is, where the fuel concentration is lean, the amount of oxygen in the exhaust gas increases, and C
While the oxidation reaction for purifying O and HC is active, the reduction reaction for purifying NO _x is inactive. On the contrary, on the rich side where the air-fuel ratio is small, that is, the rich side where the fuel concentration is high, the amount of oxygen in the exhaust gas is small, and the oxidation reaction becomes inactive but the reduction reaction becomes active.

On the other hand, when driving an automobile, acceleration and deceleration are frequently performed in urban areas, and the air-fuel ratio frequently changes within the range from near stoichiometric (theoretical air-fuel ratio) to the rich state. In order to meet the demand for low fuel consumption in such traveling, lean burn control for supplying an oxygen-rich mixture as much as possible is necessary. The lean burn control reduces the amount of fuel used and suppresses the generation of carbon dioxide, and is therefore preferable from the viewpoint of global environment protection.

However, the exhaust gas from the lean burn engine has a large amount of oxygen, and if a normal three-way catalyst is used under such conditions, the reduction reaction for purifying NO _x is inactive.
Therefore, there is a demand for the development of a catalyst capable of sufficiently purifying NO _x in exhaust gas from a lean burn engine, which contains a large amount of oxygen. Therefore, in lean burn, combustion is normally performed under lean conditions with excess oxygen, and a stoichiometric-rich condition is temporarily set to reduce exhaust gas into a reducing atmosphere to generate NO _x.
A system for reducing and purifying was developed. The ideal for this system, occludes NO _x in lean atmosphere, NO _x to release the NO _x occluded in the stoichiometric-rich atmosphere
A storage-reduction type exhaust gas purifying catalyst using a storage material has been developed.

For example, JP-A-5-317652 proposes a catalyst in which an alkaline earth metal and Pt are supported on a porous carrier such as alumina. According to this catalyst, when lean, NO _x is adsorbed on the alkaline earth metal,
Since it reacts with the reducing gas of HC or CO to be purified during stoichiometric-rich conditions, it has excellent NO _x purification performance even on the lean side. Other known NO _x storage materials include alkali metals and rare earth elements.

However, the exhaust gas is contained in the fuel.
SO produced by burning sulfur (S) ₂Is included
S is further oxidized by the catalytic metal in an oxygen excess atmosphere.
O₃Becomes And that is also the water contained in the exhaust gas
The steam easily turns into sulfuric acid, which is NO_xWith occlusion material
Sulfite and sulfate are generated by reaction, NO_xOcclusion material
It became clear that poisonous deterioration would occur. That is, like this
NO_xIf the storage material becomes sulfite or sulfate, NO
_xCan no longer be adsorbed, resulting in a durability test
NO_xHowever, there was a problem that the purification performance of was reduced.
This phenomenon is called "sulfur poisoning".

In the conventional exhaust gas purifying catalyst, the adsorption
Uses activated alumina, which has excellent action, as a carrier
However, the activated alumina carrier is SO_xEasy to adsorb
Due to its quality, the fact that sulfur poisoning is promoted
There were also elephants. That is SO_xIs adsorbed on alumina,
Alumina becomes acidic and NO_xRepel each other, NO_x
NO to occlusion material_xStorage is inhibited. Further SO_xWhen
NO _xSulfate or sulfite produced from the occlusion material
NO because it is difficult to disassemble_xStorage material NO_xStorage effect restored
There was also a problem that it could not be done and the durability was impaired.

Therefore, the applicant of the present application has proposed an exhaust gas purifying catalyst in which a NO _x storage material and a catalytic noble metal are supported on a carrier composed of a composite oxide of Ti and Zr (Japanese Patent Application No. 7-43).
No. 96, not yet published at the time of filing this application). According to this exhaust gas-purifying catalyst, the composite oxide of Ti and Zr is less likely to adsorb sulfate ions and sulfite ions than alumina, and even if adsorbed to form sulfate, the sulfate is easily decomposed. It has the effect of improving heat resistance and acidity compared with the case where each of them is used alone due to the combined stabilization of Ti and Zr, and achieves both improvement of catalyst performance and prevention of sulfur poisoning. It is effective.

However, as a result of further research, Ti and Zr
It has been clarified that the exhaust gas-purifying catalyst using the carrier made of the composite oxide of No. 2 undergoes large thermal deterioration when used at high temperatures, and the NO _x purification rate after high-temperature durability is not sufficient. Therefore the present applicant has proposed a Ti-Zr-Al catalyst support in _the NO _x storage material and the catalyst noble metal and a catalyst for purification of exhaust gas obtained by supporting a made of a composite oxide (Japanese Patent Application No. 7-1
No. 79055, unpublished at the time of filing this application). According to this exhaust gas-purifying catalyst, the heat resistance is improved due to the presence of alumina. In addition, titania (TiO ₂ ) and zirconia (ZrO
_{In 2} ), sulfate ions and sulfite ions are less likely to be adsorbed than alumina. Therefore, the probability that the carried NO _x storage material comes into contact with the sulfate ion or the sulfite ion is reduced, and it is possible to prevent the SO _x and the NO _x storage material from reacting with each other to generate a sulfate or a sulfite. The sulfate or sulfite prevents the NO _x storage function of the NO _x storage material from being impaired and improves the durability.

Further, the use of the composite oxide carrier has the effect of stabilizing the composite, and the heat resistance is remarkably improved as compared with the two-component system of Ti-Zr, and it is produced by the adsorbed sulfate ion or sulfite ion. The sulfates decompose easily at low temperatures. Therefore, the probability of contact between the NO _x storage material and NO _x increases. This improves the NO _x purification capacity.

[0012]

By the way, due to the high performance of engines and the widespread use of highway networks in recent years, the exhaust gas temperature of automobiles has risen significantly. However, alumina and Zr
Even with the above exhaust gas-purifying catalyst that uses a catalyst support made of a composite oxide containing O ₂ , when it is used at a high temperature, for example, 900 ° C. or higher, the surface area of the ZrO ₂ portion is significantly reduced, and the catalyst is supported accordingly. It has been revealed that there is a problem that catalytic performance is deteriorated because sintering or solid-phase reaction occurs in the catalytic noble metal or NOx storage material.

The present invention has been made in view of such circumstances.
No,_xWhile maintaining high purification performance of sulfur
In addition to preventing poison, catalyst precious metal and
NO _xPrevent sintering and solid-state reaction of the occlusion material.
aimed to.

[0014]

The catalyst carrier according to claim 1 for solving the above problems is a catalyst carrier used for an exhaust gas purifying catalyst, comprising: (1) a precipitation supporting method and an impregnation supporting method.
Alumina particles by at least one of the holding method and the spray supporting method.
After supporting zirconium on the child, 700 ° C or higher in an oxidizing atmosphere
A method of firing in air, (2) Alumina by the spray loading method
The combustion temperature for loading zirconium on the particles is 700
Prepared by a method selected from
Therefore, the molar ratio of Zr / Al is within the range of 1/9 to 9/1.
Lies in the fact that.

A method using the catalyst carrier according to claim 1.
The feature of the exhaust gas purifying catalyst described in 2 is that the exhaust gas purifying catalyst purifies nitrogen oxides (NO _x ), carbon monoxide (CO) and hydrocarbons (HC) in the exhaust gas under an atmosphere of excess oxygen. (1) Precipitation supporting method, impregnation supporting method and spraying
Zirco on alumina particles by at least one of the supporting methods.
After supporting nickel, calcination at 700 ℃ or higher in oxidizing atmosphere
Method, (2) Zirconium is deposited on the alumina particles by the spray loading method.
Combustion temperature when supporting konium shall be 700 ℃ or higher
Prepared by a method selected from the
With Zr / Al in the range of 1/9 to 9/1
To, the alkali metal is to become carries the _the NO _x storage material and the catalyst noble metal selected from alkaline earth metals and rare earth elements.

[0016]

[0017]

BEST MODE FOR CARRYING OUT THE INVENTION The catalyst carrier of the present invention has a structure in which a zirconia layer covers the surface of alumina particles. It is known that zirconia has lower reactivity with alkali metals and alkaline earth metals than alumina. Therefore, the solid-state reaction between the NO _x storage material and alumina, which is a factor of high temperature thermal deterioration, is suppressed by the presence of the zirconia layer, and the deactivation of the NO _x storage material can be prevented.

Since zirconia exists as a zirconia layer covering the surface of alumina particles, the specific surface area of the zirconia portion is originally lower than that in the case of existing as a complex oxide with zirconia particles or alumina. There is. Therefore, the degree of decrease in the specific surface area of the zirconia portion at a high temperature is small, so that the decrease in the specific surface area of the entire catalyst is suppressed, and the catalyst precious metal and N
Sintering of the O _x storage material is suppressed and the durability is excellent.

Further, in the exhaust gas purifying catalyst of the present invention, zirconia is less likely to adsorb sulfate ions and sulfite ions than alumina. Therefore, the probability that the carried NO _x storage material comes into contact with the sulfate ion or the sulfite ion is reduced, and it is possible to prevent the SO _x and the NO _x storage material from reacting with each other to generate a sulfate or a sulfite. The sulfate or sulfite prevents the NO _x storage function of the NO _x storage material from being impaired and improves the durability.

The ratio of Zr and Al constituting the catalyst carrier is
The molar ratio of Zr to Al is set in the range of 1/9 to 9/1.
It If Zr is more than this range, the specific surface area at a high temperature is largely reduced, and if Al is more than this range, the solid-phase reaction between the NO _x storage material and alumina is likely to proceed. As a method of forming a zirconia layer on alumina, (1) at least one of a precipitation supporting method, an impregnation supporting method, and a spray supporting method is used, and after supporting zirconium on alumina, the temperature is set to 700 ° C. or higher in an oxidizing atmosphere. And (2) a method of setting the combustion temperature at the time of supporting zirconium on alumina by the spray supporting method to 700 ° C. or higher .

In the above methods (1) and (2),
In order to prevent γ-alumina from being converted into α, it is preferable that the firing temperature or the combustion temperature be 1000 ° C or lower. This firing is generally performed in the air, but it can be performed in another oxidizing atmosphere. A firing time of 3 to 5 hours is generally sufficient. The firing temperature or combustion temperature needs to be 700 ° C. or higher. If this temperature is lower than 700 ° C., the formation of the zirconia layer is insufficient and the desired performance cannot be obtained.

The catalyst carrier can be formed by coating as a carrier layer on the surface of a monolith carrier substrate or a pellet substrate using cordierite or a metal carrier. Further, the monolith structure or the pellet structure may be formed only from the catalyst carrier without using other materials. As the NO _x storage material supported on the catalyst carrier, at least one selected from alkali metals, alkaline earth metals and rare earth elements is used. Examples of the alkali metal include lithium, sodium, potassium and cesium. Further, the alkaline earth metal means an element of Group 2A of the periodic table, magnesium,
Examples include calcium, strontium, and barium.
Examples of rare earth elements include scandium, yttrium, lanthanum, cerium, praseodymium, and neodymium.

The content of the NO _x storage material is 100
The range of 0.05 to 1.0 mol is desirable with respect to g. If the content is less than 0.05 mol, the NO _x storage capacity is small and the NO _x purification performance is reduced, and if the content exceeds 1.0 mol, the NO _x storage capacity is saturated and at the same time HC emission increases. Such problems occur. As the catalytic noble metal, one or more of Pt, Rh and Pd can be used, and Pt is particularly desirable. The supported amount is 0.1 to 20 g with respect to 100 g of carrier for any precious metal.
Is preferred, and 0.5 to 10 g is particularly preferred. Even if the supported amount of the catalytic noble metal is further increased, the activity is not improved, and the effective utilization cannot be achieved. Further, if the amount of the catalytic noble metal supported is less than this, sufficient activity for practical use cannot be obtained.

In order to support the NO _x storage material and the catalytic noble metal on the catalyst carrier, the chloride, nitrate or the like is used in the same manner as in the conventional method by using an impregnation method, a spray method, a slurry mixing method or the like. Can be made.

[0025]

EXAMPLES The present invention will be specifically described below with reference to examples. Example 1 (1) Preparation Step of Carrier Precursor Zirconyl nitrate and alumina powder were used in a molar ratio of Zr: A.
The mixture was stirred and mixed in water so that l = 1: 4 to obtain a mixed suspension, and a necessary amount of aqueous ammonia was used as a neutralizing agent to obtain a precipitate. This precipitate was washed, dried at 80 ° C., and calcined in air at 500 ° C. for 5 hours to prepare a carrier precursor powder. (2) Step of Preparing Catalyst Carrier The carrier precursor powder obtained above was heated in the air at 90 ° C.
A catalyst carrier powder was prepared by calcining at 0 ° C. for 3 hours.

Scanning electron micrographs of the carrier precursor powder before calcination and the catalyst carrier powder after calcination are shown in FIGS. 1 and 2, respectively. In FIGS. 1 and 2, the black portion shows alumina particles and the white portion shows zirconia particles. 1 and 2, alumina particles and zirconia particles are scattered before firing,
It is observed that after firing, the surface of the alumina particles is covered with zirconia, and a zirconia layer is formed on the surfaces of the alumina particles. (3) Step of supporting each component A predetermined amount of this catalyst carrier powder is immersed in an aqueous dinitrodiammine platinum solution having a predetermined concentration, stirred for 5 hours, evaporated to dryness, and calcined in air at 300 ° C. for 3 hours. To support platinum (Pt). The amount of Pt loaded is the amount of the catalyst carrier 10
Pt is 2 g with respect to 0 g.

Next, the catalyst carrier powder carrying Pt is
It was immersed in a barium acetate aqueous solution having a predetermined concentration, stirred for 5 hours, evaporated to dryness, and baked in the atmosphere at 300 ° C. for 3 hours to carry barium (Ba) as a NO _x storage material. The supported amount of Ba is Ba based on 100 g of the catalyst carrier.
Is 0.3 mol. Finally, the catalyst powder supporting Pt and Ba was treated in a hydrogen stream at 500 ° C. for 3 hours,
Exhaust gas purifying catalyst powder of Example 1 was prepared.

Example 2 A predetermined amount of zirconyl nitrate and alumina powder were mixed by stirring in water so that the molar ratio was Zr: Al = 1: 4 to prepare a mixed suspension. This mixed suspension was sprayed into a flame and burned at 600 ° C. to prepare a carrier precursor powder by a spraying method. This carrier precursor powder was fired in the same manner as in Example 1 to obtain a catalyst carrier powder, and Pt was similarly used.
And Ba were carried to prepare an exhaust gas purifying catalyst powder of Example 2.

(Example 3) A predetermined amount of alumina powder was immersed in a predetermined amount of a zirconyl nitrate aqueous solution having a predetermined concentration, stirred for 5 hours, evaporated to dryness, and impregnated with Zr. The molar ratio of Zr and Al is Zr: Al = 1: 4. Then, it was baked in the air at 500 ° C. for 5 hours to prepare a carrier precursor powder.

This carrier precursor powder was calcined in the same manner as in Example 1 to prepare a catalyst carrier powder, and Pt and Ba were similarly loaded to prepare an exhaust gas purifying catalyst powder of Example 3. (Example 4) A predetermined amount of zirconyl nitrate and alumina powder were mixed by stirring in water so that the molar ratio was Zr: Al = 1: 4 to prepare a mixed suspension. This mixed suspension was sprayed into a flame and burned at 900 ° C. to prepare a catalyst carrier powder by a spraying method.

Using this catalyst carrier powder, Pt and Ba were loaded in the same manner as in Example 1 to prepare an exhaust gas purifying catalyst powder of Example 4. ( Reference Example 1 ) A predetermined amount of alumina powder was mixed in 2-propanol,
The mixture was stirred at 80 ° C for 1 hour. While maintaining this at 80 ° C. and stirring, zirconium n-butoxide was added, and the mixture was heated to 80 ° C.
The stirring was continued for 2 hours. After cooling to room temperature, filtration /
The powder obtained by washing was dried and then calcined at 500 ° C. for 1 hour to obtain a catalyst carrier powder.

Using this catalyst carrier powder, Pt and Ba were loaded in the same manner as in Example 1 to prepare an exhaust gas purifying catalyst powder of Reference Example 1 . (Comparative Example 1) Exhaust gas purifying catalyst of Comparative Example 1 was carried out in the same manner as in Example 1 except that (2) the step of preparing the catalyst carrier was performed by calcining the carrier precursor in the air at 900 ° C for 3 hours. A powder was prepared.

(Comparative Example 2) Exhaust gas of Comparative Example 2 was carried out in the same manner as in Example 2 except that (2) the step of preparing the catalyst carrier was carried out by calcining the carrier precursor in the air at 900 ° C for 3 hours. A purification catalyst powder was prepared. (Comparative Example 3) A carrier precursor was heated at 900 ° C. in air for 3 hours.
Exhaust gas purification catalyst powder of Comparative Example 3 was prepared in the same manner as in Example 3 except that the step (2) of preparing the catalyst carrier, which was calcined for a time, was not performed.

(Comparative Example 4) Exhaust gas purification of Comparative Example 4 was carried out in the same manner as in Example 1 except that (1) the step of preparing the carrier precursor in Example 1 was not carried out and only alumina powder was used as the carrier. A catalyst powder for use was prepared. (Comparative Example 5) Example 1 except that (1) the carrier precursor preparation step in Example 1 was not performed and only alumina powder was used as the carrier, and (2) the catalyst carrier preparation step was not performed. Exhaust gas purifying catalyst powder of Comparative Example 5 was prepared in the same manner as in.

Comparative Example 6 The procedure of Example 1 was repeated, except that the step (1) of preparing the carrier precursor in Example 1 was not performed and only the zirconia (ZrO ₂ ) powder was used as the carrier.
An exhaust gas-purifying catalyst powder of Comparative Example 6 was prepared. (Comparative Example 7) Other than using (1) the zirconia (ZrO ₂ ) powder alone as a carrier without carrying out the step of preparing the carrier precursor in Example 1 and (2) not carrying out the step of preparing the catalyst carrier. In the same manner as in Example 1, an exhaust gas-purifying catalyst powder of Comparative Example 7 was prepared.

COMPARATIVE EXAMPLE 8 Except that in the step (1) of preparing a carrier precursor in Example 1, alumina powder and zirconia powder were mixed to prepare a carrier precursor powder composed of a mixture of individual oxides. Exhaust gas purifying catalyst powder of Comparative Example 8 was prepared in the same manner as in Example 1. Al and Zr
The molar ratio of Zr: Al = 1: 4.

(Test / Evaluation) For each of the above exhaust gas purifying catalyst powders, the NO _x purification rate was measured at the initial stage, after the sulfur poisoning durability test, and after the high temperature durability test. (1) Initial NO _x purification rate 0.5 g of each exhaust gas purifying catalyst pelletized from each exhaust gas purifying catalyst powder by a conventional method was placed in an evaluation device, and lean model exhaust gas and rich shown in Table 1 were used. The model exhaust gas on the side was alternately repeated every 2 minutes to flow at a flow rate of 2 L / min, and the initial purification rate of NO _{x in} the transient region was measured. The incoming gas temperature is 400 ° C. The results are shown in Table 4. The NO _x purification rate is defined by the following equation.

NO _x purification rate (%) = 100 × (NO _x amount in outlet gas for 1-4 minutes / NO in incoming gas for 4 minutes)
_x amount)

[0039]

[Table 1] (2) NO _x purification rate after sulfur poisoning durability test Each exhaust gas purifying catalyst pelletized from each exhaust gas purifying catalyst powder by a conventional method is placed in a durability test device, and the lean side shown in Table 2 The model exhaust gas and the model exhaust gas on the rich side are lean at an incoming gas temperature of 600 ° C.
Flowing was performed while switching rich for 4 minutes ... 1 minute, and 1 hour 15 minutes per 1 g of catalyst.

[0040] Thereafter, was measured _the NO _x purification rate in the transient region in the same manner as in the measurement of initial _the NO _x purification rate. The results are shown in Table 4.

[0041]

[Table 2] (3) NO _x purification rate after high temperature endurance test Each exhaust gas purification catalyst pelletized from each exhaust gas purification catalyst powder by a conventional method is placed in an endurance test device, and lean side model exhaust gas shown in Table 3 is obtained. And the model exhaust gas on the rich side is lean at an incoming gas temperature of 900 ° C
Rich was switched from 1 minute to 4 minutes and was run for 5 hours.

[0042] Thereafter, was measured _the NO _x purification rate in the transient region in the same manner as in the measurement of initial _the NO _x purification rate. The results are shown in Table 4.

[0043]

[Table 3]

[0044]

[Table 4] From Table 4, the exhaust gas purifying catalysts of Comparative Examples 1 to 3 are the catalysts of Example 1
It can be seen that the NO _x purification rate after high temperature endurance is lower than those of Examples 1 to 4 and the high temperature durability is inferior to Examples 1 to 4 . That is, it is apparent that the high temperature durability is improved by using the catalyst carrier which is calcined at 900 ° C. in the air as in Examples 1 to 4 .

Further, comparing Comparative Example 4 and Comparative Example 5,
The difference between the presence and absence of calcination at 900 ° C. in the air is small, and comparison between Example 1 and Comparative Example 1 and Comparison between Comparative Example 4 and Comparative Example 5 shows that when the carrier does not contain zirconia, 900
It can be seen that the effect of firing at ℃ is small. That is, the effect of such a calcination treatment is effective when the carrier contains zirconia, and the formation of the zirconia layer reduces the specific surface area of the zirconia portion and suppresses the reduction of the catalyst surface area, and at the same time, the solid phase at a high temperature. It is presumed that the reaction is suppressed.

Further, comparing Comparative Example 6 and Comparative Example 7, similarly, the initial activity and the activity after endurance are decreased by baking at 900 ° C. in the air. And Example 1 and Comparative Example 1
From the comparison with Comparative Example 6 and the comparison between Comparative Example 6 and Comparative Example 7, it can be seen that the effect of the firing treatment is exhibited when zirconia and alumina coexist. A comparison between Example 1 and Comparative Example 8 revealed that the use of a catalyst carrier having a zirconia layer formed on the surface of alumina particles significantly improved the purification performance including sulfur poisoning resistance, and the single oxides were mixed together. It can be seen that the catalyst carrier does not improve the high temperature durability and the sulfur poisoning durability even if calcined at 900 ° C.

[0047]

That is, according to the catalyst carrier of the present invention, since the surface of the alumina particles is coated with zirconia, the surface ratio of the exposed alumina is low. Further, when used as a catalyst, the degree of decrease in the specific surface area of the entire catalyst caused by the decrease in the specific surface area of the zirconia portion is small.

Therefore, according to the exhaust gas purifying catalyst of the present invention using this catalyst carrier, the solid phase reaction between the NO _x storage material and alumina and the sintering of the catalytic noble metal and the NO _x storage material at high temperature are prevented. . And since zirconia prevents sulfur poisoning and ensures high heat resistance of alumina, while maintaining high NO _x purification performance,
It has excellent durability because it can overcome the two obstacles of sulfur poisoning and high temperature heat deterioration.

[Brief description of drawings]

FIG. 1 is a scanning micrograph showing a particle structure of a cross section of a carrier precursor before firing at 900 ° C. in one example of the present invention.

FIG. 2 is a scanning micrograph showing a particle structure of a cross section of a catalyst carrier after firing at 900 ° C. in one example of the present invention.

─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. ⁷ Identification code FI B01D 53/36 104A (56) References JP-A-55-67331 (JP, A) JP-A-8-57314 (JP, A) JP-A-50-90590 (JP, A) JP-A-7-232064 (JP, A) (58) Fields investigated (Int.Cl. ⁷ , DB name) B01J 21/00 -38/74 B01D 53/86 B01D 53/94

Claims (2)

(57) [Claims] 1. A catalyst carrier used for an exhaust gas purifying catalyst.
And (1) precipitation support method, impregnation support method and spray support method
Zirconium on alumina particles by at least one method of
After supporting the glass, it is baked at 700 ° C or higher in an oxidizing atmosphere.
Method, (2) Zirconium on alumina particles by the spray loading method
How to set the combustion temperature to 700 ℃ or higher when supporting um
Prepared by a method selected from the
Zr / Al is in the range of 1/9 to 9/1 . 2. Nitric acid in exhaust gas under an atmosphere of excess oxygen
Compounds (NO _x ), carbon monoxide (CO) and hydrocarbons (H
An exhaust gas-purifying catalyst for purifying C), which comprises (1) precipitation
At least one of a supporting method, an impregnating supporting method, and a spray supporting method.
After supporting zirconium on alumina particles at 700 ° C or higher
Method of firing in an oxidizing atmosphere above, (2) Spray loading
Method for loading zirconium on alumina particles by
For the method selected from the method of setting the baking temperature to 700 ° C or higher
Is prepared, and the molar ratio of Zr / Al is 1/9 to 9
Alkali metal, alkali
Touch and _the NO _x storage material selected from alkaline earth metals and rare earth elements
Exhaust gas purification characterized by supporting precious metal
Catalyst.