Patent Application
20090291840
1. Field of the Invention
The present invention relates to a honeycomb structure.
2. Description of the Related Art
Many technologies have been developed to convert exhaust gases of automobiles; however, countermeasures currently being implemented are hardly sufficient partly due to an increase in traffic. Both in Japan and worldwide, automobile emission regulations are being further tightened. In particular, controls on NOx in diesel emissions have become notably strict. Conventionally, a decrease of NOx has been achieved by controlling engine combustion systems; however, it has become difficult for this control alone to provide a sufficient NOx decrease. As diesel NOx conversion systems for addressing such an issue, NOx reduction systems (referred to as SCR systems) which use ammonia as the reducing agent have been proposed.
Honeycomb structures are known which are used for such systems installed in automobiles and include zeolite as a catalytic component. It is, however, often the case that honeycomb structures including zeolite generally have a reduced strength. In order to deal with this problem, Japanese Laid-open Patent Application Publication No. S61-171539 proposes a zeolite-containing honeycomb structure which includes 5 to 30 wt % of inorganic fibers. Japanese Laid-open Patent Application Publication No. S61-171539 discloses that according to the zeolite-containing honeycomb structure to which inorganic fibers are added, it is possible to prevent generation of cracks during firing in the honeycomb structure manufacturing process.
On the other hand, there is a danger that fine fibrous materials, such as asbestos, may pose health hazards to humans, and especially if the fibrous materials enter people's lungs, they act for very long periods of time and may cause diseases, such as cancer and emphysema. Accordingly, the European Union (EU) classifies fibrous materials as carcinogenic to humans in EU Directive 97/69/EC. According to the EU directive, bio-soluble inorganic fibers are classified as category 0, which means no carcinogenic risks to humans. Note that according to EU Directive 97/69/EC, asbestos is classified as category 3 (carcinogenic to humans); carbon fibers are classified as category 2 (probably carcinogenic); and rock wool, glass wool and silica wool are classified as category 1 (possibly carcinogenic).
International Publication No. 2005/110578 discloses a honeycomb structure used for removing particulates in vehicular exhaust. According to International Publication No. 2005/110578, silica and an alkali metal compound, an alkaline earth metal compound, or a boron compound is included in inorganic fibers used for a seal material layer of a porous ceramic honeycomb structure and in a honeycomb structure obtained by molding inorganic fibers. In this way, the inorganic fibers and the honeycomb structure are rendered bio-soluble, thereby reducing the carcinogenic risks to humans.
The contents of Japanese Laid-open Patent Application Publication No. S61-171539 and International Publication No. 2005/110578 are incorporated herein by reference.
According to one aspect of the present invention, a honeycomb structure includes at least one honeycomb unit having a longitudinal direction and including cell walls extending along the longitudinal direction from one end face to another end face to define cells. The at least one honeycomb unit includes inorganic particles, inorganic binder, and inorganic fibers. The inorganic fibers include a bio-soluble inorganic compound.
A more complete appreciation of the invention and many of the attendant advantages thereof will be readily obtained as the same becomes better understood by reference to the following detailed description when considered in connection with the accompanying drawings, wherein:
Embodiments will now be described with reference to the accompanying drawings, wherein like reference numerals designate corresponding or identical elements throughout the various drawings.
The honeycomb structure of one embodiment of the present invention includes one or more honeycomb units, each of which is a fired body including inorganic particles, an inorganic binder and inorganic fibers and having multiple cells that are separated by cell walls in such a manner as to extend in a longitudinal direction from one end face to another end face of the fired body. One example of such a honeycomb structure is illustrated in the perspective view of
The inorganic fibers included in the honeycomb units 2 of the honeycomb structure 1 according to one embodiment of the present invention are made of a bio-soluble inorganic compound. The inorganic fibers made of the bio-soluble inorganic compound may completely dissolve in a living body within a predetermined period of time, however, a similar effect may still be achieved even if just a part of the inorganic fibers dissolves in a living body so that the molecular structure of the inorganic fibers are broken down or taken apart.
The inorganic fibers preferably include at least one of a bio-soluble alkali metal and a bio-soluble alkaline earth metal, and include about 70 percent by mass or more of SiO2 and about 2 percent by mass or less of Al2O3. Further preferably, the inorganic fibers have an average fiber length of about 30 to about 150 μm and an average fiber diameter of about 4 to about 7 μm.
As to honeycomb structures, like ones described in Japanese Laid-open Patent Application Publication No. S61-171539, the influence of inorganic fibers on living bodies are not taken into consideration, and bioinsoluble fibers, such as alumina fibers and silica-alumina fibers, are used in the honeycomb structures.
As to the honeycomb structure described in International Publication No. 2005/110578, bio-soluble inorganic fibers are used in the sealing material of the porous ceramic and the inorganic honeycomb structure. The invention of International Publication No. 2005/110578 aims at removing particulates from the exhaust gas, and essentially aims at manufacturing a honeycomb structure having a particulate filtration system. Therefore, International Publication No. 2005/110578 does not mention the use of inorganic fibers for the purpose of improving the strength of the honeycomb structure including inorganic particles, such as zeolite, which are used for converting NOx and the like.
According to one embodiment of the present invention, it is possible to achieve a honeycomb structure which includes inorganic fibers having less influence on living bodies and serves as a conversion catalyst for automobile exhaust gas, especially for NOx.
In order to evaluate biosolubility of the inorganic fibers made of a bio-soluble inorganic compound, the degree of solubility of the inorganic compound in a physiological salt solution may be measured. For example, 0.5 g of inorganic fibers is put in 25 ml of physiological salt solution and shaken for five hours at 37° C. Then, the resultant solution is filtered so as to remove solid inorganic fibers, and elements—such as silicon, sodium, calcium, magnesium and the like—in the extraction solution into which a part of the inorganic fibers has dissolved are measured by the atomic absorption method or the like. Note that in the evaluation process, a normal physiological salt solution is used. If a total of about 100 ppm or more of the target compound is dissolved in the extraction solution, the inorganic fibers are regarded as being composed of a bio-soluble inorganic compound. In addition, based on the measurement result, the percentage of each substance eluted from the inorganic fibers can be calculated. In the case where the physiological salt solution includes measurement target elements, their concentrations are checked in advance and then subtracted from corresponding measured values.
A total of about 100 ppm or more of the target compound being dissolved in the extraction solution means that a part of the inorganic fibers can be dissolved in a living body by the body temperature, and as a result, the inorganic fibers are broken down or taken apart and cannot maintain their molecular structure. Accordingly, even if the inorganic fibers are introduced into a living body, unlike asbestos, they do not get stuck in the living body and remain at one location for a long period of time, and therefore, have no adverse effect on the living body. In embodiments of the present invention, it is preferable to use inorganic fibers classified as category 0 in EU Directive 97/69/EC.
As for specific bio-soluble compounds, many alkali metal compounds, alkaline earth metal compounds and boron compounds are known, and oxides and salt, such as Na, K, Mg, Ca, Ba and B, are examples of such. Bio-soluble fibers can be formed by including an oxide or salt (such as Na, K, Mg, Ca, Ba or B) in inorganic fibers of silica, alumina, silica-alumina, glass or the like, for example.
As for the inorganic fibers made of a bio-soluble inorganic compound, it is preferable to include about 70 percent by mass or more of SiO2 and about 2 percent by mass or less of Al2O3. Note that it is undesirable if the inorganic fibers include about 90 percent by mass or more of SiO2 since the amount of the alkali metal or the alkali earth metal contained becomes too little. Al2O3 should be contained at about 2 percent by mass or less, and no Al2O3 may be contained (i.e. 0 percent by mass). This is because many alkali metal and alkali earth metal silicates are generally bio-soluble; however, many alkali metal and alkali earth metal aluminates and aluminosilicates are bioinsoluble or have low biosolubilities.
The average fiber length and the average fiber diameter of the inorganic fibers are preferably about 30 to about 150 μm and about 4 to about 7 μm, respectively. If the average fiber length of the inorganic fibers is about 30 μm or more, it is less likely to have insufficient improvement in strength of the honeycomb unit 2. If the average fiber length of the inorganic fibers is about 150 μm or less, the inorganic fibers tend not to become massed together at the time of manufacture of the honeycomb unit 2 and cause manufacturing problems, facilitating the inorganic fibers to be evenly dispersed in the honeycomb unit 2. If the average fiber diameter of the inorganic fibers is about 4 μm or more, it is less likely to have insufficient improvement in strength of the honeycomb unit 2. If the average fiber diameter of the inorganic fibers is about 7 μm or less, the surface area of the inorganic fibers tends not to become small, and it is less likely that insufficient improvement in strength of the honeycomb unit 2 is obtained for the amount of the inorganic fibers contained.
The honeycomb unit 2 of the honeycomb structure 1 according to one embodiment of the present invention has a so-called honeycomb configuration having a lot of cells (through-holes) 3 which extend parallel to one another in the longitudinal direction, as shown in
Each cross-sectional surface (a surface on which the cells 3 have their open ends) at both end faces of the honeycomb unit 2 perpendicular to the longitudinal direction of the cells 3 preferably has an aperture ratio (opening ratio) of about 50 to about 65%. Here, the aperture ratio is the ratio of the aperture area to the cross-sectional surface area. The lower limit of the aperture ratio of the honeycomb unit is preferably about 50% so as to reduce the pressure loss, and the upper limit of the aperture ratio is preferably about 65% so as to ensure the amount of cell walls that assist catalytic conversion.
The porosity of the cell walls of the honeycomb unit 2 is preferably about 25 to about 40%. From a quantitative standpoint, if the porosity is about 25% or more, the exhaust gas is likely to readily penetrate deep enough into the cell walls, whereby a sufficient NOx conversion rate is likely to be achieved. On the other hand, if the porosity is about 40% or less, the strength of the cell walls tends not be reduced.
The thickness of each cell wall of the honeycomb unit 2 is preferably between about 0.15 mm and about 0.35 mm, and more preferably between about 0.15 mm and about 0.27 mm. If the cell walls have a thickness of about 0.15 mm or more, the strength of the honeycomb unit 2 is likely to be maintained. On the other hand, if the cell walls have a thickness of about 0.35 mm or less, the exhaust gas is likely to readily penetrate deep into the cell walls, whereby a decrease in the NOx conversion performance is less likely to occur.
The honeycomb unit 2 of the honeycomb structure 1 according to one embodiment of the present invention includes inorganic particles, an inorganic binder and inorganic fibers.
In the honeycomb structure 1 according to one embodiment of the present invention, the honeycomb unit 2 includes inorganic particles. The inorganic particles are the main ingredient that makes up the base material of the honeycomb unit 2, and may have a catalytic function. The inorganic particles included in the honeycomb unit 2 are not particularly limited, and examples of such include particles of zeolite, alumina, silica, zirconia, titania, ceria, mullite and precursors of them. Zeolite is desirable in need of inorganic particles having a catalytic function.
In the case where zeolite and inorganic particles other than zeolite are used as raw materials in the honeycomb unit 2 of the honeycomb structure 1 of one embodiment of the present invention, these particles preferably provide strong binding by dehydration condensation when alumina, zirconia or the like is subjected to a firing process. Among them, alumina or zirconia is preferable. In the case of alumina, γ-alumina or boehmite is preferably used. One kind selected from these particles may solely be used as the inorganic particles of the honeycomb unit 2, or two or more kinds may be used together. In addition, secondary particles of the inorganic particles other than zeolite preferably have an average particle diameter equal to or less than that of secondary particles of zeolite. In particular, the average particle diameter of the inorganic particles other than zeolite is preferably about 1/10 to about 1/1 of that of zeolite. Accordingly, the strength of the honeycomb unit 2 is likely to be increased by the binding strength of the inorganic particles having a small average particle diameter.
The inorganic particles other than zeolite included in the honeycomb unit 2 are preferably contained at about 3 to about 30 percent by mass, and more preferably about 5 to about 20 percent by mass. If the amount of the inorganic particles other than zeolite is about 3 percent by mass or more, it is less likely to have an insufficient contribution to the increase in strength of the honeycomb unit 2. On the other hand, if the amount of the inorganic particles other than zeolite is about 30 percent by mass or less, the amount of zeolite which contributes to the NOx conversion is less likely to be reduced in comparison, whereby a decrease in the NOx conversion performance is less likely to occur.
The particles of zeolite in the honeycomb unit 2 are bound by an inorganic binder.
Zeolite preferably includes secondary particles, and the average particle diameter of the secondary particles of zeolite is preferably about 0.5 to about 10 μm. Note that the average particle diameter of the secondary particles of zeolite may be obtained by measuring the raw-material particulate zeolite forming the secondary particles prior to the firing process of the honeycomb unit 2.
Here, zeolite may take any structure, for example, β-type, γ-type, ferrierite, ZSM-5, mordenite, faujasite, zeolite A, zeolite L or the like. One kind selected from them may solely be used, or a mixture of two or more kinds may be used instead.
As for zeolite, the mole ratio of silica to alumina (silica/alumina ratio) is preferably about 30 to about 50.
In addition, ion exchanged zeolite, which is formed by exchanging ions of the above zeolite, is preferably used. Regarding the ion exchanged zeolite, the honeycomb unit 2 may be formed by using the ion exchanged zeolite, or the honeycomb unit 2 may be formed first and ions of zeolite are then exchanged. Here, zeolite whose ions are exchanged with, for example, at least one of the following metal species is preferably used as the ion exchanged zeolite: Fe, Cu, Ni, Co, Zn, Mn, Ti, Ag and V. For the ion exchanged zeolite, one metal species selected from the above metal species may solely be used, or two or more metal species may be used instead.
The honeycomb unit 2 of the honeycomb structure 1 according to one embodiment of the present invention preferably includes about 230 g/L or more of zeolite per unit volume, and more preferably about 245 to about 270 g/L. If the apparent amount of zeolite per unit volume in the honeycomb unit 2 is about 230 g/L or more, the NOx conversion performance is less likely to decrease. If the apparent amount of zeolite is about 270 g/L or less, the strength of the honeycomb unit 2, and therefore the strength of the honeycomb structure 1, is likely to be maintained when the honeycomb unit 2 functioning as a NOx purification catalyst is formed with its necessary openings.
Zeolite in the honeycomb unit 2 of the honeycomb structure 1 according to one embodiment of the present invention is preferably contained at about 60 to about 80 percent by mass (relative proportion of zeolite in the honeycomb unit 2). Since zeolite contributes to the NOx conversion, it is preferable that a larger amount of zeolite be included in the honeycomb unit 2. However, the amounts of other component materials (e.g. the inorganic fibers and inorganic binder) would be reduced in order to increase the amount of zeolite, which is likely to cause a decrease in strength of the honeycomb unit 2. On the other hand, if the aperture ratio of the honeycomb unit 2 is set too low in order to increase the amount of zeolite, the flow resistance of the exhaust gas in the NOx conversion process may become excessively high.
Since the honeycomb unit 2 is a fired product, only the solid contents are left in the honeycomb unit 2 after water and the like in the inorganic binder evaporate. In this specification, only the solid contents in the inorganic binder are referred to as the inorganic binder in the honeycomb unit 2. The inorganic binder in a raw material form is, for example, inorganic sol, a clay binder or the like. Specific examples of inorganic sol are alumina sol, silica sol, titania sol, sepiolite sol, attapulgite sol, liquid glass and the like. Specific examples of the clay binder are white earth, kaolin, montmorillonite, clays of a double-chain structure (sepiolite and attapulgite) and the like. One kind selected from these sols and clays may solely be used, or two or more kinds may be used together.
The configuration characteristics of the inorganic fibers in the honeycomb unit 2 include the aspect ratio in addition to the above-mentioned average fiber length and average fiber diameter and the distribution of the fiber length to be described below. The inorganic fibers have a large aspect ratio (fiber length/fiber diameter), which is in general effective especially for the improvement in bending strength of the honeycomb unit 2. The aspect ratio of the inorganic fibers is preferably about 2 to about 1000, more preferably about 5 to about 800, and still more preferably about 10 to about 500. If the aspect ratio of the inorganic fibers is about 2 or more, a sufficient contribution to the increase in strength of the honeycomb unit 2 is likely to be obtained. On the other hand, if the aspect ratio of the inorganic fibers is about 1000 or less, a die tends to be insusceptible to clogging during a molding process of the honeycomb unit 2. In addition, the inorganic fibers tend not to break during a molding process of the honeycomb unit 2, such as extrusion molding, and as a result, variation in the length of the inorganic fibers is less likely to be caused, whereby a decrease in the strength of the honeycomb unit 2 is less likely to occur. In the case where the inorganic fibers range in aspect ratio, the aspect ratio is expressed as an average. Provided that the inorganic fibers include a bio-soluble compound, they do not always have to be long fibers, and may be short fibers, such as whiskers.
The inorganic fibers in the honeycomb unit 2 are preferably contained at about 3 to about 50 percent by mass, more preferably about 3 to about 30 percent by mass, and still more preferably about 5 to about 20 percent by mass. If the amount of the inorganic fibers is about 3 percent by mass or more, it is less likely to have an insufficient contribution to the increase in strength of the honeycomb unit 2. On the other hand, if the amount of the inorganic fibers is about 50 percent by mass or less, the amount of zeolite which contributes to the NOx conversion is less likely to be reduced in comparison, whereby a decrease in the NOx conversion performance is less likely to occur.
A catalytic component may be supported on the cell walls of the honeycomb unit 2 in the honeycomb structure 1 of one embodiment of the present invention. The catalytic component is not particularly limited, and may include a noble metal, an alkali metal compound or an alkaline earth metal compound. Such a noble metal catalyst may be formed by selecting one or more kinds from, for example, platinum, palladium and rhodium. The alkali metal compound catalyst may include one or more kinds selected from, for example, potassium and sodium. The alkaline earth metal compound catalyst may be, for example, a barium compound or the like.
Next is described an example of a method of manufacturing the honeycomb structure 2 of the above-described honeycomb structure 1 according to one embodiment of the present invention. First a honeycomb-unit molded body is manufactured by, for example, extrusion molding using a raw material paste that consists primarily of the above-described inorganic particles, inorganic fibers and inorganic binder.
For the inorganic fibers, the above-described bio-soluble inorganic compound is used. The inorganic fibers preferably include an alkali metal or an alkali earth metal, and include about 70 percent by mass or more of SiO2 and about 2 percent by mass or less of Al2O3. Accordingly, biosolubility of the inorganic fibers is readily obtained. In addition, it is preferable to use inorganic fibers having an average fiber length of about 30 to about 150 μm. To set the average fiber length in this range is likely to allow the following problems to be prevented: in the manufacturing process of the honeycomb-unit molded body, breakage of the inorganic fibers during the extrusion molding or clogging of a die due to aggregation of the inorganic fibers; and insufficient dispersion of the inorganic fibers in the completed honeycomb unit 2, which leads to a reduced contribution to the increase in strength of the honeycomb unit 2. The inorganic fibers each having a length in a desired range may be manufactured by a classification process including pulverization, screening and the like.
The raw material paste preferably includes, as inorganic particles, zeolite and the above-described inorganic particles other than zeolite. In addition to the inorganic particles, an organic binder, a pore-forming material, a dispersion medium, a shaping aid and the like may accordingly be added to the raw material paste. The kinds of the organic binder are not particularly limited, and examples of such are one or more kinds of organic binders selected from methylcellulose, carboxylmethylcellulose, hydroxylethylcellulose, polyethylene glycol, phenolic resin, epoxy resin and the like. The relative quantity of the organic binder to be blended is preferably about 1 to about 10 parts by mass when the total of the solid contents of the raw materials is 100 parts by mass. As the pore-forming material, resin powder of, for example, an acrylate resin, a polyolefin resin, a polystyrene resin, a polyester resin or the like may be used. The organic binder and pore-forming material are important for adjusting the extrusion molding performance and the porosity of the honeycomb unit 2, and the amount of the pore-forming material is increased or decreased according to a desired porosity. The kinds of the dispersion medium are not particularly limited, and examples of such are water, organic solvents (e.g. toluene), alcohols (e.g. methanol) and the like. The kinds of the shaping aid are not particularly limited, and examples of such are ethylene glycols, dextrins, fatty acid soaps, polyalcohols and the like.
The raw material paste is not particularly limited, but is preferably mixed and kneaded. For instance, the paste may be mixed using a mixer, attriter or the like, or may be sufficiently kneaded by a kneader or the like. The method of forming and shaping the raw material paste is not particularly limited; however, extrusion molding, for example, is preferable to form a shape having cells.
Next, the resultant molded body is dried. A drying apparatus used to dry the molded body is not particularly limited, and examples of such are a microwave drying apparatus, a hot air drying apparatus, a dielectric drying apparatus, a reduced-pressure drying apparatus, a vacuum drying apparatus and a freeze drying apparatus and the like. Also, the dried molded body is preferably degreased. Degreasing conditions are not particularly limited and should be appropriately determined according to the kinds and amounts of organic substances included in the molded body; yet, the molded body is degreased preferably at about 400° C. for about two hours. Next, the dried and degreased molded body is fired. Firing conditions are not particularly limited; yet, the molded body is fired preferably at about 600 to about 1200° C., and more preferably at about 600 to about 1000° C. If the firing temperature is about 600° C. or more, sintering of zeolite and the like is likely to be efficiently progressed, which facilitates an increase in the strength of the honeycomb unit 2. On the other hand, if the firing temperature is about 1200° C. or less, zeolite crystals is less likely to collapse or sintering is less likely to be excessively progressed, which facilitate manufacturing the porous honeycomb unit 2 having a desirable porosity.
The honeycomb structure 1 of one embodiment of the present invention includes one or more honeycomb units 2. In the case where the honeycomb structure 1 includes two or more honeycomb units 2, the honeycomb units 2 are stacked in such a manner that the through-holes of the cells of each honeycomb unit 2 are aligned in the same direction.
The honeycomb structures 1 shown in
First, a method of manufacturing the honeycomb structure 1 including multiple honeycomb units 2, as shown in
The adhesive 5 is not particularly limited, and examples of such are a mixture of inorganic binder and inorganic particles, a mixture of inorganic binder and inorganic fibers, a mixture of inorganic binder, inorganic particles and inorganic fibers, and the like. Furthermore, an organic binder may be added to these mixtures. The kinds of the organic binder are not particularly limited, and examples of such are one or more kinds selected from polyvinyl alcohols, methylcellulose, ethyl cellulose, carboxylmethylcellulose and the like.
The thickness of the adhesive layer joining the multiple honeycomb units 2 is preferably about 0.5 to about 2 mm. The number of honeycomb units 2 to be joined may be determined according to the size of the honeycomb structure 1. The honeycomb-unit assembly formed by joining multiple honeycomb units 2 to each other by the adhesive 5 may accordingly be cut and polished.
A coating material is applied on the peripheral surface (lateral face) of the honeycomb structure 1, on which the through-holes do not have their open ends, and then dried and solidified to form the coating layer 6. Accordingly, the peripheral surface of the honeycomb structure 1 is protected, and the strength of the honeycomb structure 1 is increased. The coating material is not particularly limited, and the same material as the adhesive 5 may or may not be used as the coating material. In addition, the coating material may or may not have the same compounding ratio of that of the adhesive 5. The thickness of the coating layer 6 is not particularly limited; yet, it is preferable to be about 0.1 to about 2 mm. The coating layer 6 may or may not be formed.
After joined by the adhesive 5, the multiple honeycomb units 2 are preferably heat-treated. In the case where the coating layer 6 is provided, a degreasing treatment is preferably carried out after the adhesive layer and the coating layer are formed. In the case where an organic binder is included in the adhesive layer and the coating layer 6, the organic binder is degreased by the degreasing treatment. Degreasing conditions may be determined according to the kinds and amounts of organic substances included in the adhesive layer and the coating layer 6; yet, degreasing at about 700° C. for about two hours is preferable.
A schematic diagram of one example of the honeycomb structure 1 is given in
Second, a method of manufacturing the honeycomb structure 1 including a single honeycomb unit 2, as shown in
Next are described examples of the honeycomb structure 1 actually manufactured with various conditions. Note that the present invention is not limited to these examples.
The honeycomb unit of Example 1 was manufactured as follows. The following substances were mixed together in a container for making a molding mixed composition: 2600 parts by mass of Fe ion-exchanged β zeolite (Fe ion-exchanged amount, 3 percent by mass; silica-alumina ratio, 40; average particle diameter, 2 μm (the “average particle diameter” refers to that of secondary particles, the same shall apply below)); 2600 parts by mass of alumina sol (solid concentration, 20 percent by mass); 780 parts by mass of inorganic fibers (average fiber diameter, 4 μm, and average fiber length, 80 μm, the chemical composition is shown in TABLE 1); and 410 parts by mass of methylcellulose as an organic binder. In addition, small amounts of plasticizer, surfactant and lubricant agent were added, and then, the mixture was further mixed and kneaded while water was added to adjust the viscosity to form a molding mixed composition. Subsequently, extrusion molding was performed by an extrusion molding machine using the molding mixed composition to thereby obtain a raw honeycomb-unit molded body. Fe ion-exchanged zeolite was formed by performing Fe ion-exchange, in which zeolite particles were impregnated in ammonium iron nitrate solution. The amount of ion-exchange was determined by an IPC emission spectrometer using an ICPS-8100 (Shimazu)).
The obtained raw honeycomb-unit molded body was sufficiently dried using a microwave drying apparatus and a hot air drying apparatus, and then subjected to a degreasing treatment at 400° C. for two hours. The raw honeycomb-unit molded body was subsequently fired at 700° C. for two hours to thereby manufacture a square pillar honeycomb unit (cross section 35 mm×35 mm×length 150 mm) having quadrangular (square) cells. The manufactured square pillar honeycomb unit had an aperture ratio of 65%, a cell density of 73 cells/cm2 and a wall thickness of 0.25 mm.
TABLE 1 shows the chemical composition, average fiber length and average fiber diameter of the inorganic fibers used to manufacture the honeycomb unit of Example 1.
An adhesive paste was applied on the lateral face (face parallel to the longitudinal direction of the cells) of the manufactured plurality of square pillar honeycomb unit to form an adhesive layer having a thickness of 1 mm, and then dried and solidified at 120° C. Subsequently, honeycomb units manufactured in the same manner were arranged in 4 rows and 4 columns and then joined to form a substantially rectangular pillar honeycomb-unit assembly. The adhesive paste was made by mixing 29 percent by mass of alumina particles (average particle diameter, 2 μm), 7 percent by mass of inorganic fibers (the same inorganic fibers used to manufacture the honeycomb units), 34 percent by mass of alumina sol (solid concentration, 20 percent by mass), 5 percent by mass of carboxylmethylcellulose and 25 percent by mass of water. Next, a cutting process was performed on the lateral side of the manufactured honeycomb-unit assembly using a diamond cutter so as to shape the honeycomb-unit assembly into a cylindrical form, and the above adhesive paste was applied on the outer surface of the lateral side of the cylindrical honeycomb-unit assembly so as to form a coating layer having a thickness of 0.5 mm. In this manner, a cylindrical honeycomb-unit assembly having the same shape as that of the honeycomb structure 1 of
Apart from the differences in the type of inorganic fibers used (chemical composition), the fiber length and the fiber diameter, honeycomb units of Example 2 and Comparative Examples 1 and 2 were manufactured in the same manner as the honeycomb unit of Example 1. TABLE 1 shows manufacturing conditions changed for Example 2 and Comparative Examples 1 and 2.
A cylindrical honeycomb portion was cut out from each of the honeycomb unit of Examples 1 and 2 and Comparative Examples 1 and 2 in such a manner as to have a diameter of 30 mm and a length of 50 mm, and used as an evaluation sample. The obtained evaluation samples were aged under a simulated condition by heating them at 700° C. for 48 hours, and then maintained at 300° C. Then, 300° C.-heated vehicular exhaust simulant gas having a composition as shown in TABLE 2 was introduced into each evaluation sample at a space velocity (SV) of 35000/hr. For each evaluation sample, the reduction rate (%) of a NO component in the simulant gases was determined by measuring the NO component, within the evaluation sample, on both the gas inflow end and the gas discharge end. The reduction rate is regarded as the NOx conversion rate (%). Measurement results of the NOx conversion rates are shown in TABLE 1. It is understood from TABLE 1 that the NOx conversion rates were hardly influenced by the types of inorganic fibers, and were sufficient in all Examples 1 and 2 and Comparative Examples 1 and 2, ranging between 94% and 95%.
The inorganic fibers included in the honeycomb structure according to one embodiment of the present invention do not pose health hazards to living beings, and therefore, there is no need to worry about their influence to living beings, including human bodies, during manufacturing and use and after disposal. In addition, the honeycomb structure according to one embodiment of the present invention is applicable as an environmentally-benign and safe catalyst and catalyst carrier used for automobile exhaust conversion. In particular, the honeycomb structure of the present invention is suitable for use as a NOx conversion catalyst of an SCR system (diesel emission conversion system), which uses zeolite.
Obviously, numerous modifications and variations of the present invention are possible in light of the above teachings. It is therefore to be understood that within the scope of the appended claims, the invention may be practiced otherwise than as specifically described herein.
The present application claims priority under 35 U.S.C §120 to International Application No. PCT/JP2008/059267, filed May 20, 2008, the entire contents of which are incorporated herein by reference.
| Number | Date | Country | |
|---|---|---|---|
| Parent | PCT/JP2008/059267 | May 2008 | US |
| Child | 12493623 | US |
