KR100883946B1 - Ceramic honeycomb structural body - Google Patents

Abstract

We propose a ceramic honeycomb structure having excellent removal characteristics and catalytic reactivity of harmful gases such as HC and NOx emitted from an internal combustion engine. It is a ceramic honeycomb structure composed of one or a plurality of combinations of porous ceramic members having a columnar honeycomb structure in which a plurality of through holes are arranged in parallel with a partition wall therebetween, and the partition wall has a pore diameter of 0.05 to 150 in a pore diameter distribution curve. When the pore having a diameter is set to the first pore group and the pore having a pore diameter of 0.006 to 0.01 μm is used as the second pore group, peaks of pore distribution are respectively shown in the region of the first pore group and the region of the second pore group. The ceramic honeycomb structured body which consists of a sintered compact which has a pore structure in which one or more (maximum values) exist.

Description

Ceramic Honeycomb Structure {CERAMIC HONEYCOMB STRUCTURAL BODY}

This application is an application which claims priority based on Japanese Patent Application No. 2004-375815 for which it applied on December 27, 2004 as a basic application.

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a ceramic honeycomb structure, and in particular, proposes a ceramic honeycomb structure used for supporting a catalyst for exhaust gas purification discharged from an internal combustion engine such as an automobile or a boiler.

As the ceramic honeycomb structure used for supporting the catalyst for exhaust gas purification of automobiles, an integral structure such as low thermally expandable cordierite is mainly used. Such a ceramic honeycomb structure is generally formed by supporting a material having a high specific surface area such as activated alumina or a catalytic metal such as platinum on its surface. In addition, for an engine used under an excess oxygen atmosphere such as a lean burn engine and a diesel engine, a NOx sorbent such as alkaline earth metal such as Ba for NOx treatment is supported on the surface of the structure.

By the way, in order to further improve the purification performance of these ceramic honeycomb structures, it is effective to increase the contact efficiency between the exhaust gas, the noble metal catalyst and the NOx sorbent. Therefore, it is important to carry the catalyst on the partition surface of the ceramic honeycomb structure in a state where the catalyst is sufficiently dispersed (see Japanese Patent Laid-Open No. 10-263416).

Moreover, as this ceramic honeycomb structure, the technique which improved reactivity by adjusting pore diameter distribution is proposed (Unexamined-Japanese-Patent No. 3-68456, Unexamined-Japanese-Patent No. 8-229412, Unexamined-Japanese-Patent No. 2001). -187318, Japanese Unexamined Patent Publication No. 2001-187320, Japanese Unexamined Patent Publication No. Hei 10-43588).

However, in the conventional ceramic honeycomb structure, a high specific surface area material (catalyst coat layer) is provided on the surface of the partition wall or the pore diameter of the partition wall is adjusted, but the catalytic reaction is not sufficient enough and needs to be improved. That is, when high specific surface area materials, such as alumina, are used for this ceramic honeycomb structure, sintering advances by heat aging and there exists a possibility that a specific surface area may fall. In addition, the supported catalyst metals such as platinum tend to aggregate to increase the particle size, thereby decreasing the specific surface area. That is, the conventional ceramic honeycomb structure needs to increase the specific surface area of the initial stage in order to make it high specific surface area after thermal aging (for use as a catalyst carrier).

Moreover, in order to improve the gas purification performance of such a ceramic honeycomb structure, it is effective to raise the contact efficiency of exhaust gas, a noble metal catalyst, and a NOx sorbent. In other words, it is effective to increase the specific surface area of the ceramic honeycomb structure serving as a support while increasing the degree of dispersion by decreasing the particle diameter of the catalyst. In this regard, the conventional cordierite honeycomb structure is designed to study the shape of the through hole, the density of the through hole, or the wall thickness in order to increase the contact efficiency with the exhaust gas catalyst. Was. However, this conventional ceramic honeycomb structure has a problem that the catalyst cannot be sufficiently dispersed in the support, and the purification performance of the exhaust gas after thermal aging deteriorates.

In addition, some conventional honeycomb structures have a large amount of catalyst supported thereon or have a larger catalyst carrier itself. However, it is not preferable to carry a large amount because precious metals such as platinum are very expensive. On the other hand, when the large-size structure is installed in an automobile, its installation space is very limited, which is not suitable.

SUMMARY OF THE INVENTION An object of the present invention is to propose a ceramic honeycomb structure having excellent catalytic reactivity and removal characteristics of harmful gases such as HC and NOx emitted from an internal combustion engine.

The present invention provides a ceramic honeycomb structure comprising one or a plurality of combinations of pillar-shaped honeycomb porous ceramic members having a plurality of through holes formed in a gas flow path in parallel with a partition wall, wherein the partition wall has a horizontal axis. In the pore diameter distribution curve having the pore diameter (μm) and the vertical axis as the log differential pore volume (cm 3 / g), pores having a pore diameter of 0.05 to 150 μm are used as the first pore group, and the pore diameter is 0.006 to 0.01 When the pore having a diameter is 2nd pore group, it is a sintered compact having a pore structure in which at least one peak (maximum value) of pore distribution exists in the region of the first pore group and the region of the second pore group, respectively. Ceramic honeycomb structure, characterized in that made.

Although the following shows an example of the more preferable structure of this invention, it is not limited only to this structure. (1) The peak of the pore diameter distribution of the pores in the region of the first pore group exists in the range of the pore diameter of 0.05 to 1.0 µm, and the ② the pore diameter distribution curve has the pore diameter of the range of 0.01 to 1.0 µm. The value of the log differential pore volume indicates an integer and is continuous. (3) The pore diameter distribution curve indicates that the pore diameter between peaks (maximum values) indicated in each region of the first pore group and the second pore group is the log differential pore volume. The value represents an integer and is continuous, ④ The partition wall has a thickness of 0.05 to 0.35 mm, ⑤ The ceramic member contains alumina as a main component, ⑥ When combining a plurality of ceramic members, each member Between the sealing material layer, ⑦ the ceramic member is provided with a catalyst on the surface of the barrier rib or the surface of each ceramic particle constituting the barrier rib, ⑧ the honeycomb structured body is As an exhaust gas purifying apparatus of the amount will be available.

1 is a graph showing an example of the pore diameter distribution curve of the ceramic honeycomb structural body according to the present invention.

2: A is sectional drawing which showed typically an example of the pore formed in the ceramic honeycomb structure of this invention.

2B and 2C are sectional views schematically showing the shape of a conventional pore.

3A is a perspective view showing an example of the ceramic honeycomb structured body of the present invention.

3B is a perspective view showing an example of a collective honeycomb filter.

4 is a perspective view of an integrated honeycomb filter using a porous ceramic member.

5 is a schematic diagram of a catalytic reaction device.

6A is a graph (Example 1) showing the relationship between the pore diameter and the pore volume of the honeycomb unit according to the present invention.

6B is a graph (Example 2) showing the relationship between the pore diameter and the pore volume of the honeycomb unit according to the present invention.

6C is a graph (Example 3) showing the relationship between the pore diameter and the pore volume of the honeycomb unit according to the present invention.

6D is a graph (Examples 4 to 7) showing the relationship between the pore diameter and the pore volume of the honeycomb unit according to the present invention.

7A is a graph (Comparative Example 1) showing the relationship between the pore diameter and the pore volume of the honeycomb unit according to the comparative example.

7B is a graph (Comparative Example 2) showing the relationship between the pore diameter and the pore volume of the honeycomb unit according to the comparative example.

7C is a graph (Comparative Example 3) showing the relationship between the pore diameter and the pore volume of the honeycomb unit according to the comparative example.

Best Mode for Carrying Out the Invention

The inventor examined the pore structure of this structure (sintered compact) about the honeycomb structure made from porous ceramics used for an exhaust gas purification apparatus. In the examination, the inventor investigated the example which changed the state of the pore diameter distribution of the said structure by adjusting the kind, particle size, compounding quantity, compounding ratio, baking temperature, etc. of a raw material. As a result, the inventors have found that, for example, in the case of ceramic honeycomb structures used as catalyst carriers, even if the porosity is about the same, a large difference in purification efficiency occurs due to the difference in pore diameter distribution.

In other words, the pore structure of the partition wall of the ceramic sintered body has a pore diameter distribution curve measured by a mercury intrusion method with the horizontal axis as the pore diameter (µm) and the vertical axis as the log differential pore volume (cm 2 / g). In the range of 0.05-150 micrometers which is an area | region of a 1st pore group, one peak (maximum value) of a pore diameter distribution exists, and in the range of 0.006-0.01 micrometer which is an area | region of a 2nd pore group, When the peak is present in one or plural, preferably in two parts of the vicinity of 0.2 mu m and the vicinity of 0.009 mu m, the catalytic reactivity is good and is effective for purifying exhaust gas.

As for the mechanism by which such a phenomenon occurs, the inventor estimates as follows. FIG. 2A is a typical schematic diagram of a surface structure in a ceramic member, particularly a partition portion, in which peaks of pore diameter distribution exist in regions of the first pore group and regions of the second pore group, respectively. FIG. This surface structure is three-dimensional, as shown in the figure, pores having a large pore diameter D _{1 having} a pore diameter of 0.05 to 150 μm and pores having a small pore diameter D ₂ belonging to the second region having a pore diameter of 0.06 to 0.01 μm. Or the example which exists in parallel on the same plane is shown. In addition, this invention is not limited only to the surface structure shown, The thing of 2 types and 3 types of different hole diameters opened in the same plane may be sufficient.

2B and 2C are schematic views of the surface structure in the partition of a conventional structure, FIG. 2B is an example which exists only in the pore of a small hole diameter, and FIG. 2C is an example which exists only in the pore of a large hole diameter.

Among those shown in these figures, the pore structure shown in FIG. 2A is an example having a plurality of types of pores having different pore diameters in the so-called pores. In this case, the role of the pores of the large pore diameter D ₁ is to penetrate the exhaust gas through the pores to the inside of the partition walls, so that the reaction of the gas proceeds efficiently even inside the partition walls, thereby improving the efficiency of gas exchange before and after the reaction. It is thought to have a role to be targeted. On the other hand, the role of the pores of the small pore diameter D ₂ belonging to the _second pore group is considered to play a role of promoting the reaction of the catalyst and the exhaust gas dispersed and supported on the partition surface and inside. As a result, as having the pore structure suitable for the present invention, molecules of the exhaust gas and the like easily penetrate into the walls of the catalyst carrier.

On the other hand, in the pore structure shown in FIG. 2B, gas does not penetrate into the partition walls, and the reaction of the catalyst in the walls is weakened. In addition, although the pore structure shown in FIG. 2C penetrates into the inside of a wall, reaction with a catalyst cannot be promoted.

The pore structure which is the preferred embodiment of the present invention can be formed, for example, by changing the particle size or composition of alumina, which is a high specific surface area material constituting the catalyst carrier, and is effective as a means for increasing the catalytic activity of the honeycomb structured body. For example, in the case of a ceramic honeycomb structure having a pore structure in which a particle diameter of each of the aluminas constituting the catalyst carrier is changed and a pore diameter distribution curve as shown in FIG. Good.

That is, in the ceramic honeycomb structure, when the pore diameter distribution curve of the partition wall shows a distribution as shown in Fig. 1, the region of the first pore group consisting of pores having a pore diameter of 0.05 to 150 m and a pore diameter of 0.006 to 0.01 m When dividing into two into the area | region of the 2nd pore group which consists of phosphorus pores, when it is set as a pore structure so that each area may have a peak (maximum value), the purification efficiency of exhaust gas can be improved.

In the ceramic honeycomb structure structured as described above, when the pore distribution of the partition wall (cell wall) is made to have a peak in this region, especially for the pores in the second pore group (0.006 to 0.01 µm), the entire partition wall has a high specific surface area. As a result, the particles of the catalyst metal can be made small, and the dispersion rate can be improved. Therefore, the contact rate (efficiency) of the exhaust gas with the catalyst metal and / or the NOx storage agent is increased, and the purification efficiency of the exhaust gas can be improved.

In this case, the surface of the partition can ensure high reactivity in that the specific surface area becomes large. However, the ceramic honeycomb structure having such pore distribution has a small hole diameter in each pore, so that the gas flows inside the partition wall in the thickness direction. It can be seen that it is difficult to sufficiently infiltrate the catalytic reaction inside the partition wall.

Therefore, in preferable embodiment of this invention, it was set as the partition pore structure which a peak may generate | occur | produce in the pore diameter distribution of the said 1st pore group (0.05-150 micrometers). As a result, the gas easily penetrates to the depth in the thickness direction, and furthermore, the purification reaction of the gas also occurs on the inner surface of the partition, leading to an improvement in overall reactivity.

In addition, in this invention, the pore diameter distribution of the pore which belongs to a 1st pore group is comprised so that a 1 or more peak may exist in the range of 0.05-1.0 micrometer. With such a partition structure, it can be seen that gas easily penetrates inside.

The thickness of the partition wall is about 0.05 to 0.35 mm, preferably about 0.10 to 0.30 mm, and more preferably about 0.15 to 0.25 mm in relation to the pore structure. The reason for this is that the contact area with the exhaust gas easily penetrates into the interior of the partition wall until the wall thickness exceeds 0.35 mm, thereby improving the catalyst performance. On the other hand, when the thickness of a partition is less than 0.05 mm, there exists a possibility that intensity | strength may fall.

In the above ceramic honeycomb structure, the pore diameter distribution curve has a pore diameter in the range of 0.01 to 1.0 µm among pores belonging to the first pore group, and / or a region between each peak value shown in the first and second pore groups. For, it is preferable that the value of the log differential pore volume represents an integer and be continuous. That is, as shown in the graph (indicated by the broken line) of the integrated pore volume (cc / g) in FIG. 1, it is preferable that this curve is continuously rising. If it is in this state, it is thought that it is possible to purify a wide range of gas types in spite of the ease of adsorption by the size of the molecule | numerator of exhaust gas components discharged | emitted from automobiles.

In the ceramic honeycomb structure according to the preferred embodiment of the present invention, a porous ceramic member having a columnar honeycomb structure in which a plurality of through holes (cells) are arranged in parallel with a partition wall (hereinafter, simply abbreviated as "honeycomb unit") as a structural unit It is formed by combining one or more. That is, in the present invention, when simply referred to as a ceramic honeycomb structure, the whole honeycomb unit is formed of only a single honeycomb unit other than the plurality of honeycomb units bound together via a sealing material layer (hereinafter referred to as an "integrated honeycomb structure"). (Hereinafter referred to as an "integrated honeycomb structure").

The aggregate honeycomb structure requires a sealing material layer for sealing between neighboring honeycomb units, and may form a coating material layer on the outermost layer portion. However, in the case of the integrated honeycomb structured body, since it consists of a single honeycomb unit, at least the sealant layer interposed between the honeycomb units is not necessary.

FIG. 3A is a perspective view showing a part of an example of a porous ceramic member (honeycomb unit 11) used in an aggregate honeycomb structure that is an example of the ceramic honeycomb structure of the present invention. FIG. 3B is a perspective view of an exhaust gas purifying apparatus in which a plurality of honeycomb units shown in FIG. 3A are combined to form an aggregate honeycomb structure. FIG. In the collective honeycomb structured body, the honeycomb unit 11 has a plurality of through holes (cells) 12 and partition walls (cell walls) 13 formed of gas flow paths. The honeycomb unit 11 preferably has a shape in which the honeycomb units 11 are easily joined to each other, and the cross-sectional shape of the surface orthogonal to the through hole is square, rectangular, hexagonal, fan, or the like. It can think about the combination suitably.

As shown in FIG. 3B, the collective honeycomb structure 10 is formed by forming a plurality of honeycomb units 11 through a seal layer 14 through a plurality of honeycomb units 11 to form a block shape, preferably around the outer circumference of the block. You may provide the coating material layer 16 for preventing the leakage of exhaust gas, or ensuring strength.

One of the characteristics of this collective honeycomb structure is its high strength against thermal shock and vibration. The reason for this is inferred that even when a temperature distribution occurs due to a sudden temperature change or the like in the honeycomb structure, the temperature difference in the structure can be reduced to a small degree, and the thermal shock can be alleviated by the seal layer 14. . In particular, even when the honeycomb unit causes cracks due to thermal stress or the like, the seal material layer 14 is also effective to prevent the cracks generated in the unit from advancing to the entire honeycomb structure. It is also considered to be effective in maintaining the shape as a honeycomb structure and not losing its function as a catalyst carrier by playing a role as a part of the main body (frame).

The honeycomb unit 11 constituting the collective honeycomb structure is made of porous ceramic, and has an area of the cross section orthogonal to the through hole 12 (the size of the unit itself, hereinafter simply referred to as the "cross-sectional area") of 5 to It is preferable that it is about 50 cm <2>. The reason for this is that if the cross-sectional area is less than about 5 cm 2, the cross-sectional area of the seal material layer 14 joining the plurality of honeycomb units increases, and the pressure loss increases, and the specific surface area carrying the catalyst becomes relatively small. Can not be dispersed with high efficiency. On the other hand, when the cross-sectional area exceeds about 50 cm 2, the size of this honeycomb unit becomes too large, and the thermal stress generated in each honeycomb unit cannot be sufficiently suppressed. Moreover, about 6-40 cm <2> is preferable and, as for this cross-sectional area, it is more preferable to set it as the magnitude | size of about 8-30 cm <2>.

In addition, when the size of the honeycomb unit 11 is within the above range, the honeycomb unit 11 exhibits sufficient strength against thermal shock (thermal stress) in addition to being able to suppress the pressure loss while maintaining a large specific surface area. It is practical because it shows vibration resistance and durability.

Here, the cross-sectional area of the honeycomb unit means the cross-sectional area of the honeycomb unit that is a basic unit constituting the honeycomb structure when the honeycomb structure combines a plurality of honeycomb units having different cross-sectional areas, and usually means that the cross-sectional area is the maximum. . In addition, the ratio of the total cross-sectional area of the honeycomb unit to the cross-sectional area of the honeycomb structure is preferably about 85% or more, and more preferably 90% or more. The reason is that when the ratio of the honeycomb unit is less than 85%, the ratio of the honeycomb unit to the total cross-sectional area is reduced, so that the specific surface area carrying the catalyst is relatively small, and the cross-sectional area of the sealing material layer 14 is relatively large. This is because the pressure loss increases by that minute. If the ratio is 90% or more, the pressure loss can be further reduced.

In the ceramic honeycomb structured body, it is preferable to use ceramic particles having a high specific surface area as the material constituting the honeycomb unit body.

For example, one kind or two or more kinds of particles selected from alumina, silica, zirconia, titania, cerium oxide, mullite, zeolite can be used, but alumina is preferred among them.

The porosity of such honeycomb unit is about 20 to 80%, preferably about 50 to 70%. The reason is that if the porosity is less than about 20%, gas may not be sufficiently penetrated to the inside of the wall. On the other hand, if the porosity exceeds about 80%, the strength of the ceramic member is lowered and is easily destroyed. There is.

In addition, a porosity can be measured by a conventionally well-known method, such as the measurement by a mercury intrusion method, an Archimedes method, and a scanning electron microscope (SEM), for example.

By the way, the above-mentioned ceramic honeycomb structure can be comprised with the porous honeycomb ceramic member (honeycomb unit) manufactured by mixing the heterogeneous material like the inorganic material of a 2nd form with the inorganic material of a 1st form (an inorganic material with a large specific surface area). (Hereinafter, it is called a "high specific surface area honeycomb unit.").

It is preferable that this high specific surface area honeycomb unit contains at least ceramic particles and an inorganic binder, and also contains ceramic particles, an inorganic reinforcing material and an inorganic binder.

Such honeycomb unit can bond (adhesive) the inorganic particles to the inorganic binder. In this case, when the inorganic particles are composed of large particles having a specific surface area, the honeycomb unit is effective for obtaining a honeycomb structure having a high specific surface area per high unit volume and having a strength for stably maintaining a honeycomb shape. Become.

In addition, by adding an inorganic reinforcing material, the honeycomb unit is provided with a higher strength, thereby obtaining a honeycomb structure having a high surface area per unit volume.

Therefore, the honeycomb structured body composed of such a honeycomb unit can disperse and support the catalyst component throughout the structure, thereby ensuring a high specific surface area. In addition, about this unit, even if ceramic particle is not fully sintered, the shape maintenance in the case of heat shock and a vibration (for example, when used as a vehicle mounting) is possible.

The inorganic material of the first type used in the manufacture of the high specific surface area honeycomb unit is an inorganic material (high specific surface area particles) having a predetermined aspect ratio (long side / short side), and the inorganic material of the second type An inorganic material having an aspect ratio larger than the predetermined aspect ratio can be used. The honeycomb unit related to such material blending can improve the strength of the honeycomb unit by adding an inorganic material of the second aspect having a large aspect ratio. Here, the inorganic material of a 2nd aspect has an aspect ratio of 2-1000, Preferably it is 5-800, More preferably, it is 10-500. The reason is that, when the aspect ratio is less than 2, the inorganic material of the second aspect contributes little to the improvement of the strength of the honeycomb structure. On the other hand, the inorganic material of the second aspect tends to cause clogging in the molding die during molding. The sex may be worse. Moreover, this is because the inorganic material is bent during molding such as extrusion molding, and the length of the inorganic material is deviated, so that the contribution to the strength improvement of the honeycomb structure becomes small. In addition, what is necessary is just to use a mean value, when there is distribution in the aspect ratio of this inorganic material of a 2nd aspect.

In this invention, the inorganic material of the said 1st form may be made into the ceramic particle which has a high specific surface area, and the inorganic material of the 2nd form may be made into the inorganic fiber. This is because the strength of the honeycomb unit is improved by the inorganic fibers.

The inorganic material of the first aspect may be ceramic particles having a predetermined particle size, and the inorganic material of the second aspect may be ceramic particles having a particle size larger than that of the inorganic material of the first aspect. With such a configuration, the strength of the honeycomb unit is improved by the ceramic particles having a large particle size.

It is preferable that it is 5 times or more of the particle diameter of the inorganic material of a 1st aspect, and, as for the inorganic material of a 2nd aspect, it is more preferable that it is 10-30 times the particle diameter of the inorganic material of a 1st aspect. Specifically, it is preferable that the particle diameter of the ceramic particle which is the inorganic material of this 2nd form is about 10-60 micrometers, and it is more preferable that it is about 20-50 micrometers. The reason is that when the particle size is less than 10 m, the strength of the honeycomb structure cannot be sufficiently increased. On the other hand, when the particle size exceeds 60 m, it is easy to cause clogging in the molding die during molding, and the moldability may be deteriorated. to be.

Here, when there is distribution in the particle size of the inorganic material of the first aspect and the particle size of the inorganic material of the second aspect, the average value may be used. The ceramic particles of the inorganic material of the second aspect may be selected from a kind different from the ceramic particles of the inorganic material of the first aspect described above, and may be the same type and different in shape as the ceramic particles of the inorganic material of the second aspect (particles You may select a different shape or physical properties (for example, different crystal forms and different melting temperatures).

In the case where the inorganic material of the second aspect is ceramic particles, the particle diameter of the material can increase the strength of the honeycomb structure by the size, and therefore the aspect ratio may be the same as the inorganic material of the first aspect.

In the case where ceramic particles are used as the inorganic material of the first aspect, the ceramic particles preferably have a large specific surface area, for example, one selected from alumina, silica, zirconia, titania, cerium oxide, and mullite, or Although two or more kinds of particles can be used, alumina is particularly preferred among these.

Moreover, although it does not specifically limit as an inorganic material of a 2nd aspect, For example, nitride ceramics, such as aluminum nitride, silicon nitride, boron nitride, titanium nitride, silicon carbide, zirconium carbide, titanium carbide, tantalum carbide, tungsten carbide, etc. Oxide ceramics such as carbide ceramics, alumina, zirconia, cordierite, mullite and zirconia can be used.

When the inorganic fiber is used as the inorganic material of the first and second aspects, examples of the inorganic fiber include ceramic fibers made of alumina, silica, silica-alumina, glass, potassium titanate, aluminum borate, and the like. For example, a whisker made of alumina, silica, zirconia, titania, cerium oxide, mullite, silicon carbide, or the like can be used. These may be used independently and may use two or more types together. Of the inorganic fibers, alumina fibers are preferable.

The compounding quantity of the inorganic material (ceramic particle etc.) of a 1st aspect is about 30-97 mass%, Preferably it is 30-90 mass%, More preferably, it is 40-80 mass%, More preferably, it becomes 50-75 mass%. The reason for this is that when the blending amount of the first embodiment is less than 30 mass%, the specific surface area of the honeycomb structure becomes small, and when the catalyst component is supported, most of the catalyst component cannot be dispersed. On the other hand, when it exceeds 97 mass%, since the compounding quantity of the inorganic material (inorganic fiber etc.) of the 2nd aspect which contributes to strength improvement becomes small, it is thought that the strength of a honeycomb structure is reduced.

The compounding quantity of the inorganic material (inorganic fiber, whisker etc.) of a 2nd aspect is about 3-70 mass%, Preferably it is 3-50 mass%, More preferably, it is 5-40 mass%, More preferably, 8-30 mass% is good. The reason is that when the content of the inorganic material of the second aspect is less than 3 mass%, the strength of the honeycomb structure is lowered. On the other hand, when the content of the inorganic material of the second aspect exceeds 70 mass%, the inorganic material of the form of the first aspect which contributes to the improvement of the specific surface area (ceramic Since the compounding quantity of particle | grains etc. becomes comparatively small, it is thought that the specific surface area as a honeycomb structure becomes small, and it becomes impossible to disperse a lot of catalyst components.

In manufacture of a honeycomb unit, an inorganic binder can be used. This inorganic binder is effective because high strength can be obtained even if the firing temperature of the honeycomb unit is low. As this inorganic binder, an inorganic sol, a clay binder, etc. can be used, for example. Among these, as the inorganic sol, for example, one kind or two or more kinds of inorganic sols selected from alumina sol, silica sol, titania sol, water glass, and the like can be used. As the clay-based binder, for example, one or two or more clays selected from clay, kaoline, montmorillonite, cyclic clay (sepiolite, attapulgite), or the like Binders and the like can be used.

The compounding quantity of this inorganic binder is 50 mass parts or less, Preferably it is 5-50 mass parts, More preferably, making solid content the amount which combined the inorganic material of a 1st form into the inorganic material of a 2nd form with respect to 100 mass parts. 10-40 mass parts, More preferably, 15-35 mass parts is good. The reason is considered that formability deteriorates when content of an inorganic binder exceeds 50 mass parts.

The number of through holes formed in the honeycomb unit is preferably about 15.5 to 186 pieces / cm 2 (100 to 1200 cpi) per unit cross-sectional area, 46.5 to 170.5 pieces / cm 2 (300 to 1100 cpsi), and more preferably 62.0 to 155 pieces. / Cm 2 (400-1000 cpsi) is more preferable. The reason for this is that when the number of through holes is less than 15.5 / cm 2, the area of the wall in contact with the exhaust gas inside the porous honeycomb unit decreases, while when it exceeds 186 / cm 2, the pressure loss becomes high, I think it is because production becomes difficult

It is preferable that the cross-sectional shape of the through hole formed in this honeycomb unit is approximately triangular or approximately hexagonal. This is because it is thought that the strength of the honeycomb unit can be increased (for example, isostatic strength, etc.) by increasing the strength of the honeycomb unit without degrading pressure loss or exhaust purification performance. For example, when the cross-sectional shape of the through hole is a triangle, the through hole 12 of the cross-sectional triangle faces up and down differently, or the four through holes of the cross-section triangle face each other at the vertices of the triangle. Place to form. Moreover, you may form the through-hole of a hexagonal cross section.

Further, the ceramic honeycomb structure preferably used in the present invention is effective when used as a carrier for supporting the catalyst component on the surface of the partition wall of the honeycomb unit or on the surface of each ceramic particle constituting the partition wall. In this case, this ceramic honeycomb structure becomes a honeycomb catalyst. In this case, as the catalyst component supported on the structure, for example, a noble metal, an alkali metal compound, an alkaline earth metal compound, an oxide, or the like can be used. As the noble metal, for example, one or two or more selected from platinum, palladium, and rhodium are used, and as the alkali metal compound, one or two or more compounds selected from, for example, potassium and sodium are used, and an alkaline earth metal is used. As the compound, for example, a compound such as barium is used, and as the oxide, perovskite (La _O.75 K _0.25 MnO ₃ or the like), CeO _2, or the like is used.

Such honeycomb catalysts can be used, for example, as so-called three-way catalysts or NOx storage catalysts for exhaust gas purification of automobiles. In addition, the catalyst component may be supported on the structure after the ceramic honeycomb structure is produced, or may be supported at the stage of the ceramic particles of the raw material. As the method for supporting the catalyst component, for example, an impregnation method can be applied.

Below, an example of the manufacturing method of the ceramic honeycomb structural body of this invention mentioned above is demonstrated. First, extrusion molding is carried out using a raw material paste containing the above-described raw materials (the inorganic material of the first form, the inorganic material of the second form, the inorganic binder and the like) as main components to produce a green molded body that becomes a honeycomb unit. In addition to these, an organic binder, a dispersion medium, and a molding aid may be appropriately added to the raw material paste in accordance with moldability. As the organic binder, for example, one or two or more organic binders selected from methyl cellulose, carboxymethyl cellulose, hydroxyethyl cellulose, polyethylene glycol, phenol resins and epoxy resins can be used. As for the compounding quantity of this organic binder, about 1-10 mass% is preferable with respect to a total of 100 weight part of the inorganic material of a 1st form, the inorganic material of a 2nd form, and an inorganic binder. As a dispersion medium, water, an organic solvent (benzene etc.), alcohol (methanol etc.) etc. can be used, for example. As the molding aid, for example, ethylene glycol, dextrin, fatty acid, fatty acid soap, polyvinyl alcohol and the like can be used.

For example, the raw material paste may be mixed using a mixer, an attritor, or the like, and is preferably sufficiently mixed with a kneader or the like. It is preferable to integrally shape | mold the raw material paste into the honeycomb shape which has a through hole, for example by extrusion molding.

Next, the raw molded body obtained is dried. As a drier used for this drying, a microwave drier, a hot air drier, an oilfield drier, a vacuum drier, a vacuum drier, and a freeze drier can be used, for example. It is preferable to degrease the dry molded object obtained in this way next. What is necessary is just to select the conditions to degrease suitably according to the kind and quantity of the organic substance contained in a molded object, It is preferable to set it as the conditions of about 400 degreeC and 2 hours. Next, it is preferable to heat up and bake the said dry molded object obtained continuously. As the baking conditions, it is preferable to heat to the temperature of about 600-1200 degreeC, for example.

In this firing, the reason for heating the oxide at a temperature of 600 to 1200 ° C is that when the firing temperature is less than 600 ° C, sintering of ceramic particles or the like does not proceed, and the strength as a honeycomb structure is lowered. This is because the sintering of ceramic particles or the like proceeds excessively and the specific surface area per unit volume becomes small, and the catalyst component to be supported cannot be sufficiently dispersed. Moreover, it is preferable to heat this baking temperature about 1000-2200 degreeC in the case of nitride and carbide ceramics.

Through these steps, a calcined honeycomb unit made of a porous ceramic having a plurality of through holes can be obtained.

The pore diameter distribution of the honeycomb unit thus obtained is adjusted according to the particle size and particle size distribution of the material and the addition state of the slurry.

Next, after applying the sealing material paste which becomes a sealing material layer to the surface of the honeycomb unit made of porous ceramics, neighboring ones are joined and bonded one by one sequentially, and then dried and fixed, and the honeycomb unit of predetermined size To prepare a conjugate. In this case, as the sealing material used for joining the units, for example, a mixture of ceramic particles in an inorganic binder, a mixture of inorganic fibers in an inorganic binder, a mixture of ceramic particles and inorganic fibers in an inorganic binder, and the like Can be used.

In addition, these sealing materials may add the organic binder. As the organic binder, for example, one kind or two or more kinds selected from polyvinyl alcohol, methyl cellulose, ethyl cellulose and carboxymethyl cellulose can be used. As said inorganic binder used for this sealing material, a silica sol, an alumina sol, etc. can be used, for example. These may be used independently and may use 2 or more types together. Among these inorganic binders, silica sol is preferable. Moreover, as said inorganic fiber used for this sealing material, ceramic fiber, such as silica-alumina, mullite, alumina, silica, etc. can be used, for example. These may be used independently and may use 2 or more types together. Among these inorganic fibers, silica-alumina fibers are preferred. Moreover, as said inorganic particle used for this sealing material, carbide, nitride, etc. can be used, for example, the inorganic powder or whisker etc. which consist of silicon carbide, silicon nitride, boron nitride, etc. can be used. These may be used independently and may use 2 or more types together. Among these inorganic particles, silicon carbide excellent in thermal conductivity is preferable.

The sealing material layer 14 interposed between the honeycomb units may be dense or porous, and it is preferable that the exhaust gas can be introduced therein, but the seal material layer (coating material) formed on the outer circumference of the collective honeycomb structure It is preferable that the layer) 16 consists of a compact body. This is because, in the case of the sealing material layer 16, when the aggregate type honeycomb structure of the present invention is provided in the exhaust passage of the internal combustion engine, it is necessary to prevent the exhaust gas from leaking from the outer circumference of the honeycomb structure.

Moreover, it is preferable that the sealing material layer 14 which is inserted between mutually arrange | positioned honeycomb units mutually and can be used for bonding and adhering these is about 0.5-2 mm in thickness. It is because sufficient adhesive strength cannot be obtained when the thickness of this sealing material layer 14 is less than 0.5 mm. Moreover, since this sealing material layer 14 is a part which does not function as a catalyst carrier, when the thickness exceeds 2 mm, the specific surface area per unit volume of a ceramic honeycomb structure will relatively fall, and the dispersion efficiency of a catalyst component will fall. do. Moreover, when the thickness of this sealing material layer 14 exceeds 2 mm, pressure loss will become large. The number of honeycomb units to be joined may be appropriately determined in accordance with the size of the honeycomb structure used as the honeycomb catalyst. Moreover, the joined body which joined the honeycomb unit with the sealing material is suitably cut | disconnected, grind | polished, etc. according to the magnitude | size of a ceramic honeycomb structure, and is made into a product.

As the outer circumferential surface (side surface) of the ceramic honeycomb structure, a coating material layer obtained by applying a coating material and drying-solidifying, that is, a sealing material layer 16 can be formed. This sealing material layer 16 functions effectively after aiming at the protection of the outer peripheral surface of a structure and the improvement of strength. The coating material may be the same material as the sealing material layer 14 described above, or may be a different material. These blending ratios may be the same or different blends. It is preferable that the thickness of this coating material layer 16 shall be about 0.1-2 mm. The reason for this is that when the thickness is less than 0.1 mm, the protection of the outer circumferential surface and the structure strength cannot be increased. On the other hand, when the thickness exceeds 2 mm, the specific surface area per unit volume as the honeycomb structure is relatively lowered, and the catalyst component is supported. It cannot be sufficiently dispersed.

The aggregated honeycomb structured body composed of a combination of a plurality of honeycomb units is bonded after the sealing material layer 14 is interposed (however, when the sealing material layer (coating material layer 16) is formed, the sealing material layer 16 is formed). It is preferable to calcinate after). This is because, if such a treatment is carried out, the organic binder is contained in the sealing material and the coating material so that it can be degreased. Although the conditions of calcination are suitably determined by the kind and quantity of organic substance, it is preferable at about 700 degreeC for about 2 hours. When the calcined ceramic honeycomb structure is used, the organic binder contained in the ceramic honeycomb structure does not burn and release polluted exhaust gas.

Here, as an example of the ceramic honeycomb structure, a conceptual diagram of a collective honeycomb structure 10 in which a plurality of rectangular porous honeycomb units 11 having a square cross section are joined to form a cylinder is shown in Fig. 3B. This collective honeycomb structured body 10 joins a plurality of honeycomb units 11 through the seal material layer 14, has an outer shape by cutting, and has a cylindrical shape. ) Is applied by applying a sealing material (coating material) to an outer circumferential surface of which is not opened, and forming the sealing material layer 16. In addition, for example, the honeycomb unit 11 whose cross section is a fan shape or a cross section is square may be shape | molded, these may be bonded together, and it may be made into ceramic honeycomb structures, such as a cylinder, beforehand, and a cutting process may be abbreviate | omitted.

4 is a perspective view schematically showing an integrated honeycomb structure that is another example of the ceramic honeycomb structure of the present invention. As shown in this figure, the integrated honeycomb structured body 20 is a pillar-shaped block in which a plurality of through holes 12 are arranged in parallel in the longitudinal direction with the partitions 23 interposed therebetween.

In the integrated honeycomb structured body shown in the above example, the block is formed in the same manner as the aggregated honeycomb structured 10 except that the block is an integral structure produced by sintering.

In addition, the size of the block 22 is appropriately determined in consideration of the displacement of the internal combustion engine to be used, the size of the exhaust passage, and the like. In addition, the shape should just be a columnar shape, For example, arbitrary columnar shapes, such as a columnar shape, an elliptic columnar shape, and each columnar shape, can be used.

Hereinafter, although the ceramic honeycomb structure (Example of this invention, a comparative example) produced on various conditions is demonstrated, this invention is not limited only to what is shown in these Examples.

This test was carried out to fabricate a honeycomb unit made of fiber-reinforced alumina with a change in pore diameter and pore distribution, and to confirm the effect when a catalyst coat layer made of platinum-containing alumina was formed on the surface (bulk wall surface). will be. It shows in Table 1 about the detailed description of Examples 1-7 and Comparative Examples 1-3. In addition, the manufacturing method of a honeycomb unit is as follows.

(1) First, γ-alumina particles (primary particles and secondary particles in the formulation shown in Table 1, except that the average particle diameter is 2㎛) 40 mass%, silica-alumina fibers (average fiber diameter 10㎛, 10 mass parts of average fiber length, aspect ratio 10), and 50 mass% of silica sol (solids concentration 30 mass%) were mixed, and 6 weight part of methylcellulose, a plasticizer, and 100 mass parts of obtained mixtures were used as an organic binder. A small amount of lubricant was added and further mixed-kneaded to obtain a mixed composition Next, the mixed composition was extruded by an extrusion molding machine to obtain a green molded body as shown in Fig. 3A.

(2) Next, by using a microwave dryer and a hot air dryer, the raw molded body is sufficiently dried, degreased by holding at 400 ° C. for 2 hours, and then calcined at 800 ° C. for 2 hours. A honeycomb unit 11 made of porous fiber-reinforced alumina having a columnar shape (34.3 mm × 34.3 mm × 150 mm), a cell density of 93 cells / cm 2 (600 cpsi), and a cell shape of a square (square).

(3) Next, 29 mass% of γ-alumina particles, silica-alumina fiber (average fiber diameter 10 µm, average fiber length 100 µm), 7 mass%, silica sol (solid concentration 30 mass%), 34 mass%, carboxymethyl cellulose 5 mass% And 25 mass% of water were mixed to adjust the heat-resistant sealing material paste, which was applied to the side surfaces of the honeycomb unit 11 and bonded to each other, that is, to the outer surface 13 of the honeycomb unit 11. The sealing material paste is applied so as to have a thickness of 1 mm to form the sealing material layer 14, and the plurality of honeycomb units 11 are bonded to each other through the sealing material layer 14. In this way, the joined body which is an assembly type honeycomb unit is joined. Fabricated, the bonded body was cut into a cylindrical shape using a diamond cutter so that the front face was approximately point symmetrical, and the seal was placed on the outer surface of the side portion without a through hole. Coating so that the paste is 0.5mm thick and to form a sealing material layer 16 is made of a coating layer on the outer surface.

(4) The bonded body obtained after that is dried at 120 degreeC, it is hold | maintained at 700 degreeC for 2 hours, the sealing material layer 14 and the sealing material layer (coating material layer) 16 are degreased, and a cylindrical shape (diameter 143.8 mmPa × An aggregate honeycomb structural body 10 having a height of 150 mm) was obtained. They were impregnated with a platinum nitrate solution, adjusted to have a platinum weight per unit volume of the aggregated honeycomb structured body at 2 g / L, and supported by a catalyst component. The honeycomb catalyst was then maintained at 600 ° C for 1 hour.

(5) About each of the samples of these honeycomb catalysts, their pore diameters were measured by the mercury porosimetry (according to JIS 1655: 2003).

(6) The pore diameter was measured using the Shimadzu Corporation make and micromeritics automatic porosimeter autopore III 9405. The measurement range at that time was 0.006-500 micrometers, 100 micrometers-500 micrometers measured by 0.1 psia, and 0.006 micrometer-100 micrometers measured by 0.25 psia. As a result, some pole values (peaks) arose in the pore diameter distribution. The numerical value is shown in Table 2.

(7) Next, the light-off temperature shown in Table 2 was measured. This light-off temperature says reaction temperature at the time of purifying rate showing 50%, when the ratio which the density | concentration of the specific component contained in exhaust gas reduced by the catalyst is a purification rate. And when this light off temperature is low, it means that the energy required for purification | cleaning reduces. That is, it can be said that the honeycomb catalyst having a low light off temperature has high catalyst performance. Therefore, this light off temperature is used as an index which shows the catalyst performance of a honeycomb catalyst.

(8) Here, the measuring method of light off temperature is demonstrated. This measurement can be performed using the catalytic reaction apparatus 30 shown in FIG. The catalytic reaction device 30 includes a dilution gas supply part 31 composed of air and nitrogen, a circulation path 32 through which the dilution gas is passed to the honeycomb structure, a humidifier 33 humidifying the dilution gas, and a dilution gas. A heater 34 for heating, a gas mixer 35 for mixing exhaust gas components with heated diluent gas to be a reactive gas, a sample holder 36 for keeping the honeycomb structure in an airtight state, and a ceramic honeycomb structure A gas sampler 37 for sampling the reaction gas before contacting with the gas, a gas sampler 38 for sampling the reaction gas after contacting with the ceramic honeycomb structure, and a gas analyzer for analyzing the concentration of specific gas components contained in the reaction gas It consists of 39.

(9) The measurement procedure of the light-off temperature is demonstrated below. First, the honeycomb structured body is set in the sample holder 36 to flow air and nitrogen from the dilution gas supply part 31 through the flow path 32 at a predetermined flow rate. Next, the dilution gas is humidified by the humidifier 33, and the temperature of the dilution gas is adjusted by the heater 34. Subsequently, the exhaust gas component is injected into the dilution gas in circulation from the upstream of the gas mixer 35, mixed with the gas mixer 35, and the reaction gas of predetermined concentration is adjusted. The adjusted reaction gas was brought into contact with a honeycomb catalyst to purify the reaction gas. At this time, the temperature of the heater 34 is appropriately changed, the temperature of the reaction gas inside the honeycomb catalyst at each heater temperature is measured with a thermocouple (not shown), and the reaction gas sampled by the gas samplers 37 and 38. The concentration of was measured by the gas analyzer 39.

As a measurement of this light-off temperature, the thing of the shape of 34.3 mm x 150 mm of width and length was used as the honeycomb structured body of an Example and a comparative example. Catalytic reaction is reaction gas flow rate 131 (1 / mni), exhaust gas components are oxygen, carbon monoxide, sulfur dioxide, hydrocarbons, nitrogen monoxide, water vapor and nitrogen, 13% oxygen in the reaction gas, carbon monoxide concentration 300 ppm, sulfur dioxide concentration. It is set as the conditions which added the hydrocarbon concentration 200ppm-C, the nitrogen monoxide concentration 160ppm, and some humidification amount based on 8 ppm and carbon amount. In addition, the reaction temperature changes the temperature of the heater 34 to 10 degreeC pitch, and sets it to 50-400 degreeC, and the gas analyzer 39 uses carbon monoxide and a hydrocarbon among the components contained in a purification reaction gas in the meantime. The concentration measurement was performed. The purification rate is calculated by the following equation when the concentration of the reaction gas component before contacting the catalyst is CO and the concentration of the reaction gas component after contacting the catalyst is Ci.

Purification rate (%) = (CO-Ci) / CO x 100

Then, the temperature of the reaction gas in a honeycomb catalyst was made into reaction temperature, and the relationship of each reaction temperature and purification rate was obtained. Then, the obtained reaction temperature was plotted on the horizontal axis and the purification rate was plotted on the vertical axis, and the temperature at which the purification rate was 50% was obtained from the plotted data, and this temperature was defined as the light-off temperature.

The results of the test are shown in Table 2. As shown in Table 2, the pore diameter distribution is in the range of the present invention (FIGS. 6A to 6D) has low light off temperatures (CO and HC), and the exhaust gas purification efficiency is improved. 7A to 7C show that both the light-off temperatures CO and HC are high, and this exhaust gas purification efficiency is deteriorated.

A B C D Firing temperature Primary Particles 0.03 μm Secondary Particles 2 μm Primary Particles 0.03 μm Secondary Particles 20 μm Primary Particles 0.05 μm Secondary Particles 2 μm Primary Particles 0.05 μm Secondary Particles 20 μm   Example One 100% - - - 800 ℃ 2 50% 50% - 800 ℃ 3 25% 25% 25% 25% 800 ℃ 4 40% 10% 40% 10% 800 ℃ 5 40% 10% 40% 10% 800 ℃ 6 40% 10% 40% 10% 800 ℃ 7 40% 10% 40% 10% 800 ℃ Comparative Example One 100% - - - 1100 ℃ 2 40% 10% 40% 10% 1100 ℃ 3 - - - 100% 1000 ℃

Pore diameter distribution state (㎛) Wall thickness (mm) Light off temperature CO (℃) Light off temperature HC (℃) Example 1 0.006 to 0.01 μm peak None (discontinuous) 0.05 ~ 0.5㎛ peak None (discontinuous) 0.2 107 154 Example 2 0.006 to 0.01 μm peak 0.02 to 0.05 peak 0.05 ~ 0.5㎛ peak None (discontinuous) 0.2 106 149 Example 3 0.006 to 0.01 μm peak 0.02 to 0.05 peak 0.05 ~ 0.5㎛ peak 0.5 ~ 1.0㎛ peak 0.2 106 151 Example 4 0.006 to 0.01 μm peak Yes (continuous) 0.05 ~ 0.5㎛ peak Yes (continuous) 0.2 107 155 Example 5 0.006 to 0.01 μm peak Yes (continuous) 0.05 ~ 0.5㎛ peak Yes (continuous) 0.1 110 157 Example 6 0.006 to 0.01 μm peak Yes (continuous) 0.05 ~ 0.5㎛ peak Yes (continuous) 0.2 116 163 Example 7 (Reference Example 1) 0.006 to 0.01 μm peak Yes (continuous) 0.05 ~ 0.5㎛ peak Yes (continuous) 0.3 128 166 Comparative Example 1 0.05 ~ 0.6㎛ peak None (discontinuous) 0.2 156 196 Comparative Example 2 0.05 ~ 0.5㎛ peak Yes (continuous) 0.2 154 191 Comparative Example 3 0.02 to 0.05 peak 0.05 ~ 0.5㎛ peak None (discontinuous) 0.2 152 186

According to this invention, when a partition is divided into the area | region of the 1st pore group which has a pore whose pore diameter is 0.05-150 micrometers, and the area | region of the 2nd pore group which has a pore whose pore diameter is 0.006-0.01 micrometer, Since it is set as the ceramic honeycomb structure which has a pore distribution in which the peak (maximum value) of one or more pore distribution exists in an area | region, it can be set as the honeycomb structure for exhaust gas purification apparatuses with high purification efficiency of a harmful exhaust gas.

In addition to the exhaust gas purification apparatus of an internal combustion engine, the present invention can be used as an exhaust gas purification apparatus or a filter discharged from a boiler, a heating furnace, a gas turbine, or various industrial processes.

In particular, the use of the ceramic honeycomb structure according to the present invention can be used not only as a catalyst carrier for exhaust gas purification of various apparatuses above, but also as an apparatus for purification of exhaust gas of a diesel engine. In addition, the honeycomb structure can be used not only for the above-mentioned purposes but also for use (for example, an adsorbent for adsorbing a gas component or a liquid component) without using a catalyst component.

Claims (18)

A porous ceramic member having a columnar honeycomb structure in which a plurality of through-holes made of gas flow paths are arranged in parallel with a partition wall as a ceramic honeycomb structure comprising a plurality of combinations having a sealing material layer interposed therebetween, The porous ceramic member comprises ceramic particles and at least one inorganic fiber selected from ceramic fibers and whiskers, The partition wall has a pore diameter distribution curve in which the horizontal axis is pore diameter (μm) and the vertical axis is log differential pore volume (cm 3 / g), and the pore having a pore diameter of 0.05 to 150 μm is the first pore group. When the pore having a pore diameter of 0.006 to 0.01 µm is the second pore group, one or more peaks (maximum values) of pore distribution exist in the region of the first pore group and the region of the second pore group, respectively. A ceramic honeycomb structure, comprising a sintered body having a pore structure. The method of claim 1, The peak of the pore diameter distribution of the pores in the region of the first pore group exists in the range of the pore diameter of 0.05-1.0 micrometer, The ceramic honeycomb structure characterized by the above-mentioned. The method according to claim 1 or 2, The ceramic honeycomb structure according to claim 1, wherein the pore diameter distribution curve is continuous, in which a pore diameter ranges from 0.01 to 1.0 µm and the log differential pore volume represents an integer. The method according to claim 1 or 2, In the pore diameter distribution curve, the ceramic honeycomb is characterized in that the pore diameter between peaks (maximum values) shown in each region of the first pore group and the second pore group is continuous with the value of the log differential pore volume indicating an integer. Structure. The method according to claim 1 or 2, The partition wall is a ceramic honeycomb structure, characterized in that the thickness of 0.05 ~ 0.35mm. The method according to claim 1 or 2, The ceramic honeycomb structure according to claim 1, wherein the ceramic member contains alumina as a main component. The method according to claim 1 or 2, The ceramic member is a ceramic honeycomb structure, characterized in that the catalyst is applied to the partition wall surface or the surface of each ceramic particle constituting the partition wall. delete delete delete delete delete delete delete delete delete delete delete

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