Patent Application
20090291835
1. Field of the Invention
The present invention relates to honeycomb structures and processes for manufacturing a honeycomb structure.
2. Description of the Related Art
While various technologies have been developed for the conversion of automobile exhaust gases, there has never been a fully satisfactory exhaust gas control measure in place, partly due to the ever-increasing traffic. Automobile exhaust gas regulations are headed for further tightening, both domestically and globally. Among others, regulations of NOx in diesel exhaust gases are being enforced with increasing severity. Conventionally, NOx reduction has been attempted by controlling the engine combustion systems, but now such method is proving ineffective. Against this background, a diesel NOx conversion system has been proposed which is based on a NOx reduction system (called a selective catalytic reduction (SCR) system), where ammonia is used as a reducing agent.
As a vehicle-mounted catalyst used in such a system, a honeycomb structure containing zeolite as a catalyst component is known. Generally, honeycomb structures containing zeolite have low strength. Japanese Laid-Open Patent Application No. 61-171539 discloses a honeycomb structure containing zeolite having an inorganic fiber content of 5 to 30 wt %. The zeolite-containing honeycomb structure with inorganic fibers is capable of preventing the development of a crack during firing.
WO2006/040874 A1 discloses a honeycomb structure containing ceramic particles and inorganic fibers, where the aspect ratio of the inorganic fibers is set to be equal to or greater than (the tension strength of the fibers (GPa)/0.3), so that an improved bending strength of the honeycomb structure can be obtained.
The contents of the aforementioned documents Japanese Laid-Open Patent Application No. 61-171539 and WO2006/040874 A1 are hereby incorporated by reference herein in their entirety.
According to one aspect of the present invention, a honeycomb structure includes a honeycomb unit. The honeycomb unit has inorganic particles, an inorganic binder and inorganic fibers, and cell walls extending in a longitudinal direction of the honeycomb unit from one end face to another end face of the honeycomb unit to define cells. A value of (D90-D10)/D50, which indicates a length distribution of the inorganic fibers, is about two or less, where, when the fiber length is taken in a horizontal axis and a volume frequency is taken in a vertical axis, D10 is a fiber length at 10% by volume, D50 is a fiber length at 50% by volume, and D90 is a fiber length at 90% by volume, where D10<D50<D90.
According to another aspect of the invention, a process for manufacturing a honeycomb structure includes preparing a material paste containing inorganic particles, inorganic fibers, and an inorganic binder. The material paste is extrusion-molded into a honeycomb unit molded body having a first end face, a second end face located opposite to the first end face along a longitudinal direction of the honeycomb unit molded body, and cell walls extending along the longitudinal direction from the first end face to the second end face to define plural cells. The obtained honeycomb unit molded body is dried. The dried honeycomb unit molded body is fired to obtain a honeycomb unit of which the honeycomb structure is made. A value of (D90-D10)/D50, which indicates a length distribution of the inorganic fibers, is about two or less, where, when the fiber length is taken in a horizontal axis and a volume frequency is taken in a vertical axis, D10 is a fiber length at 10% by volume, D50 is a fiber length at 50% by volume, and D90 is a fiber length at 90% by volume, where D10<D50<D90.
These and other objects, features and advantages of the invention will be apparent to those skilled in the art from the following detailed description of the invention, when read in conjunction with the accompanying drawings in which:
Embodiments will now be described with reference to the accompanying drawings, wherein like reference numerals designate corresponding or identical elements throughout the various drawings.
A honeycomb structure according to the various embodiments of the present invention may include one or more fired honeycomb units containing inorganic particles, an inorganic binder, and inorganic fibers. The honeycomb unit includes a plurality of cells extending from one end face of the unit to another end face in a longitudinal direction thereof, where the cells are divided by cell walls.
An example of the honeycomb structure according to an embodiment is shown in a perspective view in
In accordance with an embodiment of the present invention, the inorganic fibers have a length distribution such that the value of (D90-D10)/D50 is about two or less, where D10 is a fiber length at 10% by volume, D50 is a fiber length at 50% by volume (“average fiber length”), and D90 is a fiber length at 90% by volume, where D10<D50<D90.
As will be seen from the graph of
Inorganic fibers where the value of D90-D10)/D50 of about two or less have relatively uniform lengths, and a honeycomb unit containing such inorganic fibers tends to provide an enhanced strength improving effect. Thus, by using such inorganic fibers in a honeycomb unit containing inorganic particles of zeolite, for example, which tends to result in a reduced strength, a sufficient strength can be readily obtained as a honeycomb structure for a vehicle-mounted catalyst or the like.
An extrusion molding raw-material composition that contains inorganic fibers where the value of (D90-D10)/D50 is about two or less do not contain excessively long fibers. Thus, such a composition when used for molding a honeycomb is less likely to suffer from the problems of the flocculation of the inorganic fibers or the severing of the fibers by the extruding screws. Furthermore, the problem of the fibers clogging the die of the extrusion molding machine and thereby producing a defective shape of the honeycomb unit can be prevented.
Thus, by using inorganic fibers where the value of (D90-D10)/D50, which indicates the length distribution of the inorganic fibers, is about two or less as a raw material, a honeycomb unit for a honeycomb structure in accordance with an embodiment of the present invention can be readily made.
A lower limit of the value of (D90-D10)/D50 is not particularly defined. However, in order to obtain the value of less than about 0.5, it is necessary to manufacture inorganic fibers having a very sharp fiber length distribution. Thus, a realistic lower limit of the value is about 0.5 or greater or about 1.0 or greater from the viewpoint of manufacture of the raw material inorganic fibers.
In accordance with a preferred embodiment of the present invention, the average fiber length and average fiber diameter of the inorganic fibers are in the ranges of from about 30 to about 150 μm and from about 4 to about 7 μm, respectively. When the average fiber length of the inorganic fibers is about 30 μm or more, a sufficient strength improving effect of the honeycomb unit can be readily obtained. When the average fiber length of the inorganic fibers is about 150 μm or less, the fibers do not flocculate readily so that a sufficient strength improving effect can be readily achieved. If the average fiber length is about 150 μm or less at the raw material stage, the fibers are not readily severed in the extrusion molding machine, and they do not readily flocculate and clog the die.
In accordance with an embodiment of the present invention, the honeycomb unit, as shown in
Preferably, the thickness of the cell wall is about 0.15 mm or more and about 0.35 mm or less, and more preferably about 0.15 mm or more and about 0.27 mm or less. When the thickness of the cell wall is about 0.15 mm or more, a sufficient strength of the honeycomb unit may be readily maintained. When the thickness of the cell wall is about 0.35 mm or less, the exhaust gas can be readily permeate inside the cell walls, thereby preventing a decrease in NOx conversion performance.
Preferably, the porosity of the cell walls of the honeycomb unit is in a range of from about 20 to about 40% and more preferably from about 25 to about 40%. From the quantitative viewpoint, when the porosity is about 20% or more, the exhaust gas can readily reach deep inside the cell walls sufficiently, thereby preventing an insufficient NOx conversion rate. If the porosity is about 40% or less, decrease in the strength of the cell walls can be prevented.
Preferably, an opening ratio, which is the areal ratio of the openings in a cross section (where the cells have openings) perpendicular to the longitudinal direction along which the cells of the honeycomb unit are arranged, is about 50% to about 65%. The ratio is preferably 50% or greater so that an increase in pressure loss can be readily prevented. The ratio is preferably about 65% or less so that a quantity of cell walls necessary for achieving a sufficient catalyst conversion performance can be readily secured.
The honeycomb unit of the honeycomb structure according to an embodiment of the present invention includes inorganic particles, an inorganic binder, and inorganic fibers.
In a honeycomb structure according to an embodiment of the present invention, the honeycomb unit includes inorganic particles as a main raw material for a substrate (cell wall). The inorganic particles may also provide a catalyst function. The inorganic particles contained in the honeycomb unit according to an embodiment of the present invention are not particularly limited. Examples of the inorganic particles include zeolite, alumina, silica, zirconia, titania, ceria, mullite, and their precursors. Among those mentioned above, alumina, such as γ alumina or boehmite, or zirconia is preferable. These different kinds of inorganic particles may be used individually or in combination. A preferable example of inorganic particles that have a catalyst function is zeolite.
In the honeycomb structure according to an embodiment of the present invention, when zeolite and other inorganic particles are used as raw material, preferably the particles strongly bind to each other based on a dehydrating condensation reaction upon firing of alumina or zirconia. Also preferably, the inorganic particles other than zeolite have an average particle size of their secondary particles that is equal to or smaller than the average particle size of the secondary particles of zeolite. Particularly, the average particle size of the inorganic particles other than zeolite is preferably about 10% to about 100% of the average particle size of zeolite. In this way, an enhanced strength of the honeycomb unit can be obtained by the binding force of the inorganic particles having a small average particle size.
The content of the inorganic particles contained in the honeycomb unit other than zeolite is preferably in a range of from about 3 to about 30 mass % and more preferably in a range of from about 5 to about 20 mass %. When the content of the inorganic particles other than zeolite is about 3 mass % or more, a sufficient contribution to the improvement in strength can be readily obtained. When the content of the inorganic particles other than zeolite is about 30 mass % or less, a decrease in the relative content of zeolite that contributes to NOx conversion can be readily prevented, thereby preventing poor NOx conversion performance.
The zeolite in the honeycomb unit includes zeolite particles that are bound by an inorganic binder or inorganic particles. Examples of zeolite include zeolite β, zeolite Y, ferrierite, ZSM-5, mordenite, faujasite, zeolite A, and zeolite L. These examples may be used either individually or in combination.
Preferably, the molar ratio of silica to alumina (silica/alumina) is in a range of from about 30 to about 50.
Another preferable example is an ion-exchanged zeolite obtained by ion-exchanging any of the aforementioned zeolites. A honeycomb unit may be formed by using zeolite that is ion-exchanged in advance; alternatively, zeolite may be ion-exchanged after a honeycomb unit is formed. A preferable example of the ion-exchanged zeolite is zeolite ion-exchanged with at least one of metal species Fe, Cu, Ni, Co, Zn, Mn, Ti, Ag, or V. These metal species may be used either individually or in combination in the ion-exchanged zeolite.
The zeolite content per apparent unit volume of the honeycomb unit according to an embodiment of the present invention is preferably about 230 g/L or more and more preferably about 245 to about 270 g/L. When the zeolite content per unit volume of the honeycomb unit is about 230 g/L or more, a decrease in NOx conversion performance can be prevented. When the zeolite content is about 270 g/L or less, a sufficient strength of the honeycomb unit or the honeycomb structure can be readily maintained.
In accordance with the present embodiment, the content (composition ratio) of zeolite in the honeycomb unit is preferably about 60 to about 80 mass %. The content of zeolite in the honeycomb unit is preferably about 60 mass % or more because zeolite contributes to NOx conversion. However, if the zeolite content alone is increased in excess of about 80 mass %, the content of other constituent substances (such as inorganic fibers or inorganic binder) would have to be reduced, so that the honeycomb unit strength tends to decrease. If the opening ratio of the honeycomb unit is reduced too much in order to increase the zeolite content, flow resistance against the exhaust gas during NOx conversion reaction may become excessive.
The zeolite includes secondary particles, of which the average particle size is preferably in a range of from about 0.5 to about 10 μm. The average particle size of the secondary particles may be measured by measuring the raw material zeolite particles that form the secondary particles before firing of the honeycomb unit.
Because the honeycomb unit is a fired product, only a solid content of the inorganic-binder-derived components remains in the honeycomb unit, the moisture of the inorganic binder having been evaporated. Thus, the term “inorganic binder” in the honeycomb unit is intended to refer to the solid content of the inorganic binder. The inorganic binder at the raw material stage may include an inorganic sol or a clay-based binder or the like. Examples of the inorganic sol are alumina sol, silica sol, titania sol, sepiolite sol, attapulgite sol, liquid glass and the like. Examples of the clay-based binder are white clay, kaolin, montmorillonite, branched-chain structure clay (such as sepiolite and attapulgite) and the like. These inorganic sols or clay-based binders may be used individually or in combination.
In accordance with the present embodiment, the honeycomb unit contains inorganic fibers. Non-limiting examples of the inorganic fiber contained in the honeycomb unit include one or more kinds of inorganic fibers selected from alumina fibers, silica fibers, silicon carbide fibers, silica alumina fibers, glass fibers, potassium titanate fibers, and aluminum borate fibers. These inorganic fibers contribute to the improvement of the strength of the honeycomb unit. The inorganic fibers may contain short fibers such as whiskers as well as long fibers. The fiber length of the inorganic fibers, the fiber diameter, and the fiber length distribution ((D90-D10)/D50) are as described above.
The features of the inorganic fibers in the honeycomb unit in terms of shape are defined by the aspect ratio as well as the length distribution, average fiber length, and average fiber diameter of the fibers as described above. Inorganic fibers are inorganic material with large aspect ratios (fiber length/fiber diameter). Generally, the inorganic fibers are believed to be effective in enhancing the bending strength of the honeycomb structure. The aspect ratio of the inorganic fibers is preferably in a range of from about 2 to about 1000, more preferably from about 5 to about 800, and particularly preferably from about 10 to about 500. When the aspect ratio is about two or more, a decrease in the inorganic fibers' contribution to the improvement in honeycomb structure strength can be readily prevented. When the aspect ratio is about 1000 or less, the clogging of the die (mold) during molding and poor moldability can be readily prevented. Also, the inorganic fibers can be prevented from breaking during extrusion molding or the like, resulting in less variations in length and preventing a decrease in honeycomb unit strength. When the aspect ratio of the inorganic fibers has a certain distribution, the aspect ratio refers to an average value.
The content of the inorganic fibers contained in the honeycomb unit is preferably in a range of from about 3 to about 50 mass %, more preferably from about 3 to about 30 mass %, and particularly preferably from about 5 to about 20 mass %. When the inorganic fiber content is about 3 mass % or more, a decrease in the inorganic fibers' contribution to the improvement in honeycomb structure strength can be prevented. When the content is about 50 mass % or less, a decrease in the relative amount of zeolite that contributes to NOx conversion can be prevented, thereby preventing a poor NOx conversion performance of the honeycomb structure.
The cell walls of the honeycomb unit in the honeycomb structure according to an embodiment of the present invention may further support a catalyst component. Non-limiting examples of the catalyst component include a noble metal, an alkali metal compound, and an alkaline earth metal compound. Examples of the noble metal include one or more kinds selected from platinum, palladium, and rhodium. Examples of the alkali metal compound include one or more kinds of compounds selected from potassium, sodium, and the like. An example of the alkaline earth metal compound is barium or the like.
A method for manufacturing the honeycomb unit of the honeycomb structure according to an embodiment of the present invention is described. First, a raw-material paste including the above-described zeolite, inorganic fibers, and inorganic binder as main components is prepared. The material paste is then extrusion-molded, for example, to obtain a honeycomb unit molded body.
The inorganic fibers have a length distribution such that the value of (D90-D10)/D50 is about two or less, where D10 is the fiber length at 10% by volume, D50 is the fiber length at 50% by volume, and D90 is the fiber length at 90% by volume, where D10<D50<D90.
The average fiber length of the inorganic fibers is preferably in a range of from about 30 to about 150 μm, and the average fiber diameter is preferably in a range of from about 4 to about 7 μm. When the average fiber length and the average fiber diameter are in these ranges, various problems that interfere with the strength improving effect of the inorganic fiber can be more readily prevented. For example, these ranges prevent the severing of the inorganic fibers during extrusion molding, clogging of the die by flocculation of the inorganic fibers, or the defective dispersion of the inorganic fibers in the completed honeycomb unit. A desired length distribution of the inorganic fibers may be obtained by classification based on pulverization or sieving.
To the material paste, there may be further added inorganic particles other than the aforementioned zeolite, an organic binder, a pore-forming agent, a dispersion medium, a forming aid or the like as needed. Non-limiting examples of the organic binder include one or more kinds of organic binders selected from methylcellulose, carboxymethyl cellulose, hydroxyethyl cellulose, polyethyleneglycol, phenol resin, and epoxy resin.
The amount of the organic binder added is preferably in a range of from about 1 to about 10 parts by mass with respect to a total of 100 parts by mass of the solid content of the entire raw material. The pore-forming agent may be a powder of resin such as acrylic acid resin, polyolefin resin, polystyrene resin, or polyester resin.
The organic binder and the pore-forming agent play important roles for the adjustment of extrusion forming property or the porosity of the honeycomb unit. The amount of the pore-forming agent may be increased or decreased depending on the desired porosity. Non-limiting examples of the dispersion medium include water, an organic solvent (such as toluene), and alcohol (such as methanol). Non-limiting examples of the forming aid include ethylene glycol, dextrin, fatty acid soap, and polyalcohol.
The material paste, which is not particularly limited, is preferably mixed using a mixer or kneaded using an attritor, or sufficiently kneaded with a kneader or the like, for example. The method of forming the material paste is not particularly limited and may preferably involve extrusion molding to form the material paste into a shape having cells.
The resultant honeycomb unit molded body is then dried using a drying apparatus which is not particularly limited. Non-limiting examples of the drying apparatus include a microwave drying apparatus, a hot air drying apparatus, dielectric drying apparatus, reduced-pressure drying apparatus, vacuum drying apparatus, freeze drying apparatus and the like. The dried honeycomb unit molded body is preferably degreased. The degreasing conditions are not particularly limited and may be selected as appropriate depending on the kind or amount of organic matter contained in the molded body. Preferably, the honeycomb unit molded body is degreased at about 400° C. for about two hours.
The dried and degreased honeycomb unit molded body is further fired under conditions that are not particularly limited and may preferably include a temperature range of from about 600 to about 1200° C. and more preferably from about 600 to about 1000° C. When the firing temperature is about 600° C. or greater, sintering of zeolite can readily proceed sufficiently, thereby preventing the failure to enhance the strength of the honeycomb unit. When the firing temperature is about 1200° C. or less, the zeolite crystal does not tend to collapse, and sintering does not proceed too much, so that a porous honeycomb unit with an appropriate porosity can be readily manufactured.
The honeycomb structure according to embodiments of the present invention may include one or more honeycomb units. In the case of a honeycomb structure with plural honeycomb units, the honeycomb units are stacked so that the through holes of the cells in the individual honeycomb units are oriented in the same direction.
In the honeycomb structure 1 shown in
While the honeycomb structures according to the embodiments of the present invention shown in
First, a description is given of a process of manufacturing of a honeycomb structure having plural honeycomb units as shown in
Non-limiting examples of the adhesive material include a mixture of an inorganic binder and inorganic particles, a mixture of an inorganic binder and inorganic fibers, and a mixture of an inorganic binder with inorganic particles and inorganic fibers. An organic binder may be further added to the adhesive material. Non-limiting examples of the organic binder include one or more kinds of inorganic binders selected from polyvinyl alcohol, methylcellulose, ethylcellulose, and carboxymethyl cellulose.
The thickness of the adhesive material layer, via which the plural honeycomb units are joined, is preferably about 0.5 to about 2 mm. The number of the joined honeycomb units may be determined appropriately depending on the size of the honeycomb structure. The honeycomb joined assembly including the honeycomb units joined by interposing the adhesive material may be cut or ground to a desired honeycomb structure shape.
The outer peripheral surfaces (sides) of the honeycomb structure parallel to the longitudinal direction of the cells are coated with a coating material, which is then dried and solidified to form a coating material layer. In this way, the outer peripheral surfaces of the honeycomb structure can be protected and its strength can be enhanced.
The coating material is not particularly limited and may be the same as or differ from the adhesive material. The blending ratio of the coating material may be the same as or different from that of the adhesive material. The thickness of the coating material layer is not particularly limited; preferably, it is in a range of from about 0.1 to about 2 mm. The coating material layer may be either formed or not formed.
Preferably, the plural honeycomb units joined by the adhesive material are subjected to a heating process. When the coating material layer is provided, the plural honeycomb units, after the formation of the adhesive material layer and the coating material layer, are preferably degreased. By degreasing, the organic binder that may be contained in the adhesive material layer or the coating material layer can be degreased. The degrease conditions may be determined as needed depending on the kind or amount of organic matter contained, and may preferably include the temperature of about 700° C. and the duration of about two hours.
The honeycomb structure 1 shown in
In the following, a description is given of a process of manufacturing a honeycomb structure constructed of a single honeycomb unit as shown in
Concerning the aforementioned conventional honeycomb structures disclosed in Japanese Laid-Open Patent Application No. 61-171539 and W02006/040874 A1, if inorganic fibers with excessive lengths are present in the extrusion-molding step of a conventional honeycomb structure manufacturing process, the fibers may be severed in the extrusion molding machine. If this happens, desired lengths of the fibers cannot be maintained, thus adversely affecting the strength-improving effect of the inorganic fibers. Even when the fibers are not severed, the fibers may fail to sufficiently disperse among the particles of zeolite, for example, and flocculate instead, thereby accumulating at a portion of the die at the outlet of the extrusion molding machine. As a result, a defect may be caused in the cell walls, making it necessary to stop the extrusion step and clean the die.
According to an embodiment of the present invention, a honeycomb structure having a sufficient strength as a vehicle-mounted exhaust gas conversion catalyst and containing inorganic fibers that minimize the development of a defect in cell walls may be provided.
In the following, examples of honeycomb structures manufactured under various conditions are described. The present invention, however, are not limited to any of those examples.
A container for preparing a molding mixture composition was charged with 2250 parts by mass of Fe ion-exchanged zeolite p (Fe ion-exchanged amount: 3 mass %, silica/alumina ratio: 40, specific surface area: 110 m2/g, average particle size (of secondary particles; same below): 2 μm), 550 parts by mass of y alumina (average particle size: 2 μm), 2600 parts by mass of alumina sol (solid concentration: 20 mass %), 780 parts by mass of alumina fiber (average fiber diameter: 6 μm, average fiber length: 100 μm, fiber length distribution (=(D90-D10)/D50): 1.5), and 410 parts by mass of methylcellulose as an organic binder. The components were then mixed.
The alumina fibers had been pulverized in a roll mill (MRCA-1 roll crusher from Makino Corporation, with clearance 0.3 mm at 180 rpm; repeated four times), and then had their grain size distribution made uniform by sieving with a gyro-sifter type classifier.
Small amounts of plasticizer, surfactant, and lubricant were further added, and the mixture was mixed and kneaded while adjusting the viscosity by adding water, thereby obtaining a molding mixture composition. The mixture composition was extrusion-molded with an extrusion molding machine, obtaining a honeycomb molded body.
The resultant honeycomb molded body was sufficiently dried using a microwave drying apparatus and a hot air drying apparatus, and degreased at 400° C. for two hours. Thereafter, the honeycomb molded body was maintained at 700° C. for two hours for firing, thus manufacturing a rectangular-shaped honeycomb unit (cross section 35 mm×35 mm×length 150 mm), with a rectangular (square) cell shape. The thus manufactured rectangular-shaped honeycomb unit had an opening ratio of 60%, a cell density of 78 cells/cm2, and a cell wall thickness of 0.25 mm. The Fe ion-exchanged zeolite had been Fe ion-exchanged by immersing zeolite particles in an iron nitrate ammonium solution. The ion-exchanged amount was determined by ICP emission spectrometry using the ICPS-8100 spectrometer from Shimadzu Corporation.
The average fiber length and the fiber length distribution ((D90-D10)/D50) of the raw material inorganic fibers used for manufacturing the honeycomb unit are shown in Table 1 below.
A plurality of the aforementioned rectangular-shaped honeycomb units (cross section 35 mm×35 mm×length 150 mm) were manufactured, and their sides were coated with an adhesive material paste to a thickness of 1 mm. The honeycomb units were joined in 4 rows×4 columns, and dried and solidified at 120° C., obtaining a substantially rectangular-shaped honeycomb joined assembly.
The adhesive material paste had been prepared by mixing 29 mass % of alumina particles (average particle size: 2 μm), 7 mass % of alumina fibers (average fiber diameter: 6 μm, average fiber length: 100 μm), 34 mass % of alumina sol (solid concentration: 20 mass %), 5 mass % of carboxymethyl cellulose, and 25 mass % of water.
The side walls of the prepared honeycomb joined assembly were cut with a diamond cutter to obtain a cylindrical assembly. The outer surfaces of the cylindrical assembly were then coated with the aforementioned adhesive material paste to a thickness of 0.5 mm, thus preparing a cylindrical honeycomb joined assembly with the same shape as shown in
Honeycomb units according to Examples 2 to 6 and Comparative Examples 1 to 4 were manufactured under the same conditions as those of Example 1, with the exception that the average fiber length of alumina fibers and the fiber length distribution were varied as shown in Table 1.
The bending strength of the honeycomb units according to Examples 1 to 6 and Comparative Examples 1 to 4 was evaluated. The bending strength of the honeycomb units was measured by the three-point bending test in accordance with JIS (Japanese Industrial Standards)-R1601. Specifically, the Instron 5582 testing machine was used to apply a breaking load W to the honeycomb structure vertically, with the span L=135 mm and at a cross-head speed of 1 mm/min. For the calculation of the bending strength a, a cross-section second moment Z was calculated by subtracting the moment of the hollow portions of the cells in advance, and the bending strength σ was calculated by an equation σ=WL/4Z.
The contents of JIS-R1601 are hereby incorporated by reference herein in its entirety.
Table 1 also shows the results of evaluation of the bending strength of the honeycomb units according to Examples 1 to 6 and Comparative Examples 1 to 4. The results of measuring the bending strength of the honeycomb units according to Examples 1 to 6 and Comparative Example 1 are shown in a graph of
As will be seen from the results shown in Table 1, the honeycomb units of Examples 1 to 6 exhibited bending strength values as high as 6.3 MPa, whereas the bending strength of the honeycomb unit of Comparative Example 1 was much smaller at 3.5MPa. Thus, it can be seen that the honeycomb units of Examples 1 to 6 are suitable for vehicle-mounted exhaust gas conversion catalysts.
Moldability of the honeycomb units was evaluated based on the extent of clogging of the molding mixture composition (raw material) during extrusion molding in the process of manufacturing the honeycomb units according to Examples 1 to 6 and Comparative Examples 1 to 4.
In the process of manufacturing of the honeycomb unit, when the honeycomb unit molded body is extrusion-molded by an extrusion molding machine, the die of the extrusion molding machine may be partly clogged by the molding mixture composition due to solidified inorganic fibers. If this happens, the cell walls of the honeycomb unit molded body may partly fail to be formed, creating a so-called “cell defect”. When a cell defect occurs, the operation of the extrusion molding machine needs to be stopped to remove the clogging in the die. In Examples 1 to 6 and Comparative Examples 1 to 4, the moldability of the molding mixture composition was considered “Poor”, as shown in Table 1, when the operation of the extrusion molding machine was stopped even once during the formation of 100 honeycomb unit molded bodies due to a cell defect caused by the clogged die. The moldability of the molding mixture composition was considered “Good” when 100 honeycomb unit molded bodies were formed without a cell defect caused by the clogging of the molding mixture composition.
As seen from the results shown in Table 1, there were no cell defects in Examples 1 to 6 and Comparative Example 1, while cell defects occurred in Comparative Examples 2 to 4. Thus, cell defects can be reliably prevented by employing inorganic fibers where the value of the fiber length distribution (D90-D10)/D50 is about two or less. Thus, a honeycomb unit with high strength can be efficiently manufactured by using such fibers in accordance with an embodiment of the present invention.
The honeycomb structures according to various embodiments of the present invention include one or more honeycomb units having high strength, and can be used for automobile exhaust gas conversion catalysts, which are required to be small in size and weight.
Although this invention has been described in detail with reference to certain embodiments, variations and modifications exist within the scope and spirit of the invention as described and defined in the following claims.
| Number | Date | Country | Kind |
|---|---|---|---|
| PCT/JP2008/059266 | May 2008 | JP | national |
The present application claims priority under 35 U.S.C. §119 to an international application PCT/JP2008/059266 filed May 20, 2008, the entire contents of which are hereby incorporated by reference.
