Patent Application
20060073970
This application claims benefit of priority to Japanese Patent Application No. 2003-128388, filed on May 6, 2003, the contents of which are incorporated by reference herein.
The present invention relates to a honeycomb structural body that is used as a filter and the like for purifying exhaust gases discharged from an internal combustion engine such as a diesel engine or the like.
There have been proposed various honeycomb filters for purifying exhaust gases and catalyst supporting members, which are used for purifying exhaust gases discharged from internal combustion engines of vehicles such as buses, trucks and the like, and construction machines.
Specifically, for example, a honeycomb filter for purifying exhaust gases as shown in
In other words, as shown in
Moreover, with respect to the ceramic structural body of this type, there has been also proposed a catalyst supporting member in which a catalyst is supported inside the through holes, with the ends of the through holes being not sealed.
Here, the honeycomb filter for purifying exhaust gases and the honeycomb structural body to be used as the catalyst supporting member are manufactured, for example, through the following method.
In other words, first, a mixed composition containing a solvent, a binder and the like in addition to ceramic particles that are a raw material is prepared, and an extrusion-molding process or the like is carried out by using this mixed composition to manufacture a columnar formed body including a large number of through holes that are placed in parallel with one another in the length direction with a partition wall interposed therebetween, and this formed body is cut into a predetermined length.
Next, the resulting formed body is dried and moisture is dispersed, so that a dried formed body having predetermined strength that is easily handled is formed and both of the ends of the dried body are subjected to a cutting process using a cutter so that a ceramic formed body having a uniform length is manufactured.
Then, the ends of this ceramic formed body is sealed with a sealing material (plug) mainly composed of the above-mentioned ceramic particles so as to form a staggered pattern, and this is then subjected to degreasing and sintering processes, so that a porous ceramic member 30 is manufactured (see
Moreover, a protective film is stuck to each of the two end faces of the porous ceramic member 30 and, as shown in FIG. 4, a plurality of the porous ceramic members 30 are laminated through a sealing material paste that forms adhesive layers 23, so that a ceramic laminated body is assembled, and after having been dried, this is cut into a predetermined shape to prepare a ceramic block 25. Then, a sealing material paste is applied to the circumference of this ceramic block 25 to form a sealing material layer 24, and by separating the protective film, a honeycomb structural body 20 serving as a honeycomb filter for purifying exhaust gases is formed (see
Here, when the stacking process and the like of the porous ceramic members 30 are performed without carrying out the sealing process, the resulting product is utilized as a catalyst supporting member.
In the case where the honeycomb filter for purifying exhaust gases and the catalyst supporting member are manufactured through such a method, however, protruded portions and recessed portions (irregularities) of the porous ceramic member tend to appear on each of the end faces of the honeycomb filter for purifying exhaust gases or the like, due to shrinkage errors of the porous ceramic members in the manufacturing processes, positional deviations that occur upon stacking the ceramic laminated members, warps that occur in the porous ceramic members and the like.
Furthermore, in general, a honeycomb filter for purifying exhaust gases is inserted, for use, into a pipe that forms an exhaust passage in an internal combustion engine and, as described above, in the case where irregularities are formed on the end faces of the honeycomb filter for purifying exhaust gases, upon insertion into the pipe, the honeycomb filter for purifying exhaust gases tends to be inserted diagonally to cause problems after a long-term use. Moreover, in the case where the pipe has a taper-shaped narrowed portion, the end of the honeycomb filter for purifying exhaust gases tends to collide with this potion to cause damages.
In order to solve such problems, there has been proposed a honeycomb filter for purifying exhaust gases in which its two end faces are subjected to flattening processes (for example, see JP Kokai 2002-224516). Such flattening processes to be applied to the two ends of a honeycomb filter for purifying exhaust gases are effective so as to solve the above-mentioned problems; however, these processes are disadvantageous from the economic viewpoint.
Moreover, in the case where the honeycomb filter for purifying exhaust gases is used as a filter for collecting particulates, in this filter, it is necessary to prepare: through holes each of which has an opened end face on the exhaust gas flow-in side with a closed end face on the opposite side and is used for collecting particulates (hereinafter, also referred to as gas flow-in cells); and through holes each of which has a closed end face on the exhaust gas flow-in side with an opened end face on the opposite side and does not basically collect particulates (hereinafter, also referred to as gas flow-out cells). Here, a catalyst used for purifying NOx gas and the like and an NOx gas absorbing metal are placed in the respective through holes, if necessary.
In the honeycomb filter for purifying exhaust gases of this type, the gas flow-in cells effectively burn particulates, while the gas flow-out cells are allowed to efficiently purify NOx gas and the like; therefore, this filter is desirably used.
Further, there has been proposed a honeycomb filter for purifying exhaust gases in which through holes are formed so that the surface area of the wall faces of the gas flow-in cells is made greater than the surface area of the wall faces of the gas flow-out cells (for example, see JP Kokai Hei 3-49608). In the honeycomb filter for purifying exhaust gases of this type, it becomes possible to accumulate a large amount of ashes in the gas flow-in cells, and consequently to suppress an increase in the pressure loss.
Moreover, there have been proposed a catalyst supporting member in which a catalyst used for purifying NOx gas is supported only on the gas flow-in cells and a honeycomb filter for purifying exhaust gases which has a concentration gradient of the NOx gas absorbing metal wherein the concentration increases from the gas flow-in side toward the gas flow-out side (for example, see JP Kokai 2002-349238, and JP Kokai Hei 7-132226).
In the case of these honeycomb filters for purifying exhaust gases in which the shapes of the gas flow-in cells and gas flow-out cells are made uneven from each other and catalyst supporting members in which the amounts of catalyst and the like applied to the inside of the cells are made different from each other, although a superior purifying function for exhaust gases is obtained, it is difficult to distinguish the gas flow-in side and the gas flow-out side upon manufacturing, sometimes resulting in a failure in setting the amounts of catalyst and the like to be applied.
Moreover, upon stacking the porous ceramic members, a failure tends to occur in setting the orientation of the porous ceramic members; thus, a honeycomb filter for purifying exhaust gases which has the porous ceramic member stacked in an erroneous direction causes an abnormal back pressure to the internal combustion engine at the time of use, resulting in a serious trouble in the system.
Furthermore, there have been disclosed catalytic converters in which a conventional converter, which does not have a divided structure, but has an integral structure, and has through holes having no sealed ends, is provided with information regarding the dimension, weight and the like of the catalyst that is attached to the circumferential face (for example, see International Publication WO02/40215, International Publication WO02/40216, International Publication WO02/40157, JP Kokai 2002-210373, JP Kokai 2002-221032 and JP Kokai 2002-266636); however, in these catalytic converters, no information has been given with respect to the end faces. The reason for this is because these catalytic converters have an integral structure so that even upon stacking porous ceramic members that have been manufactured, no problem is raised with respect to erroneous orientation of the porous ceramic members. Moreover, since the ends of the through holes are not sealed, it is not necessary to change the kinds of catalysts depending on the gas inlet side cells and gas outlet side cells. This is because there is no difference between the gas inlet side cells and the gas outlet side cells.
However, in the catalytic converters of this type, there has been proposed a thin-wall filter having an improved temperature raising property. Here, when the thickness of the a partition wall is made thinner, the partition wall become more likely to cause wind erosion; therefore, in order to improve the erosion resistant property, there have been proposed techniques for improving the strength of the end portion.
For example, there has been proposed a method for improving the wear resistant property of the opening end faces by making the partition wall of the end portion thicker (for example, see JP Kokai 2000-51710). Further, there has been proposed a method in which cordierite powder is adhered to the end portion (for example, see JP Kokai 2002-121085). There has been also proposed another structure in which the adhering property of a catalyst is improved at one end portion of the opening or in which a reinforced portion is formed at the partition wall in order to improve the erosion resistance (for example, see JP Kokai 2003-103181). Moreover, there has been proposed still another structure in which the pore diameter of the end portion is adjusted so as to improve the erosion resistance (for example, see JP Kokai 2003-95768). Furthermore, there has been proposed yet another method in which by forming a glass phase in a predetermined portion of the partition wall in the vicinity of the end portion or the like of the opening, the erosion resistance is improved (for example, see JP Kokai No. 2003-26488).
Further, there have been proposed various methods in which various properties are applied to the end portion in a catalytic converter and the like, such as a method for allowing slurry to adhere to the opening end portion, a method for strengthening the opening end portion and a method in which the pore distribution is changed in the opening end portion.
Moreover, in some cases, different catalyst supporting methods are used between the gas flow-in side and the gas flow-out side, and in such cases, it is necessary to distinguish the gas flow-in side and the gas flow-out side.
As described above, in recent years, with respect to catalytic converters also, it becomes necessary to clearly distinguish the gas flow-in side and the gas flow-out side, and when the end portion is misplaced, the catalytic converter fails to exert predetermined functions, resulting in a trouble in an apparatus to which the catalytic converter is attached, depending on cases.
The present invention has been devised so as to solve the above-mentioned problems, and its object is to provide a honeycomb structural body which makes it possible to clearly distinguish a side in which exhaust gases are allowed to flow in (hereinafter, also referred to as a gas flow-in side) and the other side from which exhaust gases are allowed to flow out (hereinafter, also referred to as a gas flow-out side).
The present invention is directed to a columnar honeycomb structural body made of porous ceramics in which a large number of through holes that are placed in parallel with one another in the length direction with a wall portion interposed therebetween, wherein information regarding an end face of said honeycomb structural body is displayed on a circumferential surface and/or the end face thereof.
The following description will discuss embodiments of the honeycomb structural body according to the present invention.
The honeycomb structural body according to the present invention may be any honeycomb structural body as long as it is made of a porous ceramic material and has a structure in which a large number of through holes are placed in parallel with one another in the length direction with a partition wall interposed therebetween. Therefore, the honeycomb structural body may be a columnar porous ceramic member made of a single sintered body in which a large number of through holes are placed in parallel with one another in the length direction with a partition wall interposed therebetween, or may be constituted by a plurality of columnar porous ceramic members, each having a structure in which a large number of through holes are placed in parallel with one another in the length direction with a partition wall interposed therebetween, which are combined with one another through sealing material layers.
Therefore, in the following explanations, when the two kinds of the honeycomb structural bodies are explained in a separate manner, the former structural body is referred to as the honeycomb structural body of a first embodiment, while the latter is referred to as the honeycomb structural body of a second embodiment. Further, in the case where it is not necessary to distinguish the two kinds, each of them is simply referred to as a honeycomb structural body.
Referring to
As shown in
Moreover, the honeycomb structural body 10 has a structure in which a sealing material layer 14 is formed on the circumference of a columnar body 15 in which a large number of through holes 11 are placed in parallel with one another with a partition wall 13 interposed therebetween. The sealing material layer 14 is formed to reinforce the peripheral portion of the columnar body 15, adjust the shape, and also improve the heat-insulating property of the honeycomb structural body 10.
Here, in the honeycomb structural body 10 shown in
In other words, as shown in
Therefore, the honeycomb structural body 10 shown in
Moreover, in the honeycomb structural body of the first embodiment, the end portions of the through holes need not necessarily be sealed, and when not sealed, the honeycomb structural body can be used as a catalyst supporting member on which, for example, an exhaust gas purifying catalyst is supported.
In this manner, the honeycomb structural body 10 on which the information 16 regarding the end faces is displayed on its circumferential surface is advantageous in that upon inserting it into a pipe forming an exhaust passage of an internal combustion system, it becomes possible to prevent misplacement in the direction of the honeycomb structural body 10.
Here, in the case where a catalyst is placed inside the honeycomb structural body (inside the through holes) with a density gradient being formed therein and when a catalyst is applied to only the through holes that are open on the gas flow-out side, it becomes possible to prevent missetting in the amount of application of the catalyst.
Further, even in the case where a special processing, such as an erosion preventive processing or the like, is applied to the end face of the filter, the display of the information regarding the end faces, placed on the circumferential surface and/or the end face, makes it possible to easily distinguish the gas flow-in side and the gas flow-out side and consequently to prevent misplacement in the direction of the filter.
In the case of the honeycomb structural body 10 shown in
Not limited to the characters “IN” and “OUT”, the display of information regarding the end faces may be given as other characters.
Further, not limited to the display given as characters, the information regarding the end faces of the honeycomb structural body may be given as other forms, such as a barcode, an image drawn by ink, an image drawn by a laser marker, and the like. The information regarding the end faces may be simply given by coloring.
Moreover, in the case where the information regarding the end faces is displayed on the circumferential surface of the honeycomb structural body, the display is preferably given to a portion closer to either of the corresponding end face. This clearly indicates which end face the information is related to.
Furthermore, the display may be given by attaching a label. In this case, the information regarding the end faces may be given to the label as a character, a barcode, an image drawn by ink and an image derived from barcodes.
Moreover, the information regarding the end faces is not necessarily displayed on the circumferential surface of the honeycomb structural body, and may be placed on an end face of the honeycomb structural body.
The display of information regarding the end face, given on the corresponding end face of the honeycomb structural body, makes it possible to confirm whether or not the assembling process has been accurately carried out after the installation process thereof in an exhaust-gas purifying apparatus (after installation in a metal case).
Moreover, in the case where the label is attached to the end face of the honeycomb structural body, the label can be removed after the installation in an exhaust-gas purifying apparatus (after installation in a metal case).
Here, in the case where the display is given onto the end face of the honeycomb structural body, as shown in
Moreover, the information regarding the end faces may be given to both of the circumferential surface and the end faces.
In addition to information regarding the end faces, another information, such as, for example, information regarding the manufacturing date, lot number and dimension precision of the circumferential portion, may be given to the circumferential surface and/or the end face of the honeycomb structural body. Further, information regarding weight, which is required upon setting the amount of application of a catalyst, and information regarding the dimension of the circumferential portion, may be given thereto.
Moreover, the opening diameter of the through holes formed in the honeycomb structural body of the first embodiment may be the same with respect to all the through holes, or may be different; however, the opening diameter of the gas flow-in cells is preferably made greater than the opening diameter of the gas flow-out cells. In other words, the honeycomb structural body of the first embodiment is preferably designed so that the through holes with the ends being sealed on one of face sides and the through holes with the ends being sealed at the other face side have mutually different opening diameters. Thus, it becomes possible to accumulate a large amount of ashes in the gas flow-in cells, to effectively burn the particulates, and consequently to effectively exert functions as the honeycomb filter for purifying exhaust gases.
With respect to the embodiments in which the through holes with the ends being sealed on one of face sides and the through holes with the ends being sealed at the other face side are allowed to have mutually different opening diameters, not particularly limited, for example, structures as shown in FIGS. 6(a) to 6(c) are proposed.
Here, in the honeycomb structural body of the first embodiment, the aperture ratios of the through holes of each of the end faces may be the same or different from each other; however, in the case where the honeycomb structural body of the first embodiment is arranged such that the respective end faces have mutually different aperture ratios between the through holes with the end faces on one of the sides being sealed and the through holes with the end faces on the other side being sealed, the aperture ratio on the gas flow-in side is preferably made greater. Thus, it becomes possible to accumulate a large amount of ashes in the gas flow-in cells, to suppress an increase in the pressure loss, and consequently to allow the honeycomb filter for purifying exhaust gases to effectively exert corresponding functions. Here, with respect to specific shapes of the through holes in the case where the aperture ratios on the respective end faces are different from each other, for example, shapes as shown in the above-mentioned FIGS. 6(a) to 6(c) are proposed.
Moreover, with respect to the shape of the honeycomb structural body of the first embodiment, not limited to the column shape shown in
The following description will discuss the material and the like of the honeycomb structural body of the first embodiment.
With respect to the material for the columnar body made of the porous ceramics, not particularly limited, examples thereof include: nitride ceramics such as aluminum nitride, silicon nitride, boron nitride, titanium nitride and the like; carbide ceramics such as silicon carbide, zirconium carbide, titanium carbide, tantalum carbide, tungsten carbide and the like; and oxide ceramics such as alumina, zirconia, cordierite, mullite and the like; moreover, in general, oxide ceramics such as cordierite and the like is used. These materials make it possible to cut manufacturing costs, and these materials have a comparatively small coefficient of thermal expansion, and are less likely to cause oxidation during use. Here, silicon-containing ceramics in which metallic silicon is blended in the above-mentioned ceramics and ceramics that are combined by silicon and a silicate compound may also be used, and, for example, a material prepared by blending metal silicon in silicon carbide is preferably used.
Moreover, in the case where the honeycomb structural body is used as a honeycomb filter for purifying exhaust gases, the average pore diameter is preferably set in a range from 5 to 100 μm. The average pore diameter of less than 5 μm tends to cause clogging of particulates easily. In contrast, the average pore diameter exceeding 100 μm tends to cause particulates to pass through the pores; thus, the particulates cannot be collected, making the structural body unable to function as a filter.
Here, the porosity of the porous ceramic member can be measured by using a known method, such as a mercury press-in method or the like, and a measuring method using a scanning electronic microscope (SEM).
Further, in the case where the honeycomb structural body is used as a honeycomb filter for purifying exhaust gases, although not particularly limited, the porosity of the porous ceramic member is preferably set to about 40 to 80%. When the porosity is less than 40%, the honeycomb structural body is more likely to cause clogging, while the porosity exceeding 80% causes degradation in the strength of the columnar bodies; thus, that it might be easily broken.
Here, the above-mentioned porosity can be measured by using a known method, such as a mercury press-in method, Archimedes method, a measuring method using a scanning electronic microscope (SEM), and the like.
With respect to ceramic particles to be used upon manufacturing such a columnar body, although not particularly limited, those which are less likely to shrinkage in the succeeding sintering process are preferably used, and for example, those particles, prepared by combining 100 parts by weight of ceramic particles having an average particle size from 0.3 to 50 μm with 5 to 65 parts by weight of ceramic particles having an average particle size from 0.1 to 1.0 μm, are preferably used. By mixing ceramic powders having the above-mentioned respective particle sizes at the above-mentioned blending ratio, it is possible to provide a columnar body made of porous ceramics.
In the case where, as shown in
As shown in
With respect to the inorganic binder, for example, silica sol, alumina sol and the like may be used. Each of these may be used alone or two or more kinds of these may be used in combination. Among the inorganic binders, silica sol is more preferably used.
Moreover, the lower limit of the content of the inorganic binder is preferably set to 1% by weight, more preferably, to 5% by weight, on the solid component basis. The upper limit of the content of the inorganic binder is preferably set to 30% by weight, more preferably, to 15% by weight, most preferably to 9% by weight, on the solid component basis. The content of the inorganic binder of less than 1% by weight tends to cause degradation in the bonding strength; in contrast, the content exceeding 30% by weight tends to cause degradation in the thermal conductivity.
With respect to the organic binder, examples thereof include polyvinyl alcohol, methyl cellulose, ethyl cellulose and carboxymethyl cellulose. Each of these may be used alone or two or more kinds of these may be used in combination. Among the organic binders, carboxymethyl cellulose is more preferably used.
The lower limit of the content of the above-mentioned organic binder is preferably set to 0.1% by weight, more preferably, to 0.2% by weight, most preferably, to 0.4% by weight, on the solid component basis. The upper limit of the content of the organic binder is preferably set to 5.0% by weight, more preferably, to 1.0% by weight, most preferably to 0.6% by weight, on the solid component basis. The content of the organic binder of less than 0.1% by weight tends to cause a difficulty in preventing migration of the sealing material layer; in contrast, the content exceeding 5.0% by weight tends to cause too much organic component in the rate with respect to the honeycomb structural body to be manufactured, resulting in the necessity of having to carry out a heating process as the post-process after manufacturing a honeycomb filter.
With respect to the inorganic fibers, examples thereof include ceramic fibers, such as silica-alumina, mullite, alumina, silica and the like. Each of these may be used alone or two or more kinds of these may be used in combination. Among the inorganic fibers, silica-alumina fibers are more preferably used.
The lower limit of the content of the above-mentioned inorganic fibers is preferably set to 10% by weight, more preferably, to 20% by weight, on the solid component basis. The upper limit of the content of the inorganic fibers is preferably set to 70% by weight, more preferably, to 40% by weight, most preferably to 30% by weight, on the solid component basis. The content of the inorganic fibers of less than 10% by weight tends to cause degradation in the elasticity and strength, while the content exceeding 70% by weight tends to cause degradation in the thermal conductivity and a reduction in its effects as an elastic member.
With respect to the inorganic particles, examples thereof include carbides, nitrides and the like, and specific examples include inorganic powder or whiskers made from silicon carbide, silicon nitride and boron nitride. Each of these may be used alone, or two or more kinds of these may be used in combination. Among the inorganic fine particles, silicon carbide having superior thermal conductivity is preferably used.
The lower limit of the content of the above-mentioned inorganic particles is preferably set to 3% by weight, more preferably, to 10% by weight, most preferably, to 20% by weight, on the solid component basis. The upper limit of the content of the inorganic particles is preferably set to 80% by weight, more preferably, to 60% by weight, most preferably to 40% by weight, on the solid component basis. The content of the inorganic particles of less than 3% by weight tends to cause a reduction in the thermal conductivity, while the content exceeding 80% by weight tends to cause degradation in the bonding strength, when the sealing material layer is exposed to high temperature.
The lower limit of the shot content of the above-mentioned inorganic fibers is preferably set to 1% by weight, while the upper limit thereof is preferably set to 10% by weight, more preferably, to 5% by weight, most preferably to 3% by weight. Moreover, the lower limit of the fiber length is preferably set to 1 mm, while the upper limit thereof is preferably set to 100 mm, more preferably, to 50 mm, most preferably, to 20 mm.
It is difficult to set the shot content to less than 1% by weight in the manufacturing, and the shot content exceeding 10% by weight tends to damage the circumference of the columnar body. Moreover, the fiber length of less than 1 mm makes it difficult to form a honeycomb structural body with proper elasticity, while the fiber length exceeding 100 mm tends to form a shape like a pill to cause insufficient dispersion of the inorganic particles, failing to make the thickness of the sealing material layer thinner.
The lower limit of the particle size of the inorganic powder is preferably set to 0.01 μm, more preferably, to 0.1 μm. The upper limit of the particle size of the inorganic particles is preferably set to 100 μm, more preferably, to 15 μm, most preferably, to 10 μm. The particle size of the inorganic particles of less than 0.01 μm tends to cause high costs, while the particle size of the inorganic particles exceeding 100 μm tends to cause a reduction in the bonding strength and thermal conductivity.
Here, the honeycomb structural body of the first embodiment can be used as a catalyst supporting member, and in this case, a catalyst (exhaust gas purifying catalyst) used for purifying exhaust gases is supported on the honeycomb structural body.
By using the honeycomb structural body as a catalyst supporting member, toxic components in exhaust gases, such as HC, CO, NOx and the like, and HC and the like derived from organic components slightly contained in the honeycomb structural body can be positively purified.
With respect to the exhaust gas purifying catalyst, not particularly limited, examples thereof include noble metals such as platinum, palladium, rhodium and the like. Each of these noble metals may be used alone, or two or more kinds of these may be used in combination.
Here, the exhaust gas purifying catalyst, made from the above-mentioned noble metal is a so-called three-way catalyst, and with respect to the above-mentioned exhaust gas purifying catalyst, not particularly limited to the above-mentioned noble metals, any desired catalyst may be used as long as it can purify the toxic components, such as CO, HC, NOx and the like, in exhaust gases. For example, in order to purify NOx in exhaust gases, an alkali metal, an alkali-earth metal and the like may be supported thereon. Moreover, a rare-earth oxide and the like may be added as a promoter.
When the exhaust gas purifying catalyst is supported on the honeycomb structural body of the first embodiment in this manner, the toxic components such as CO, HC, NOx and the like contained in exhaust gases discharged from an internal combustion system such as an engine are made in contact with the exhaust gas purifying catalyst so that reactions, indicated by the following reaction formulas (1) to (3), are mainly accelerated.
CO+(½)O2→CO2 (1)
CmHn+(m+(n/4))O2→mCO2+(n/2)H2O (2)
CO+NO→(½)N2+CO2 (3)
Through the above-mentioned reaction formulas (1) and (2), CO and HC, contained in exhaust gases, are oxidized to CO2 and H2O, and through the above-mentioned reaction formula (3), NOx contained in the exhaust gases is reduced by CO to N2 and CO2.
In other words, in the honeycomb structural body in which the exhaust gas purifying catalyst is supported, the toxic components such as CO, HC, NOx and the like contained in exhaust gases are purified into CO2, H2O and N2, and externally discharged.
Moreover, in the case where the exhaust gas purifying catalyst is supported in the honeycomb structural body of the first embodiment, the catalyst may be supported uniformly inside the through hole, or may be supported on only a portion area inside the through hole, or may be supported in a manner so as to have a density gradient from one of the gas flow-in side and gas flow-out side toward the other side.
Here, the honeycomb structural body of the first embodiment may have a structure in which: end portions of the through holes are sealed so as to function as a honeycomb filter for purifying exhaust gases and an exhaust gas purifying catalyst is supported thereon.
In this case, the exhaust gas purifying catalyst may be supported on both of the gas flow-in cell and the gas flow-out cell, or may be supported on either one of the cells; however, it is preferably supported on only the gas flow-out cell. This is because, the resulting structure is allowed to effectively exert both of the functions as the honeycomb filter for purifying exhaust gases and the functions for purifying exhaust gases by the use of the exhaust gas purifying catalyst.
Moreover, in the case where a catalyst is supported on the honeycomb structural body of the first embodiment, in order to improve the reactivity of the catalyst, the honeycomb structural body may have thin walls (0.01 to 0.2 mm) with a high density (400 to 1500 cells/square inch (62 to 233 cells/cm2)) so that the specific surface area is increased. This structure also makes it possible to improve the temperature-raising property by utilizing exhaust gases.
When the reactivity of the catalyst is improved as described above, in particular, when the thickness of the partition wall is made thinner, the honeycomb structural body becomes more likely to cause erosion (wind erosion) due to exhaust gases. For this reason, the strength of the end portion is preferably improved by the following methods so as to prevent erosion (erosion preventive property) of the end portion on the exhaust gas flow-in side (preferably, with respect to the thickness of a portion ranging from 1 to 10 mm in the end).
More specifically, the following methods are proposed: a method in which the partition wall of the end portion is made 1.1 to 2.5 times thicker than the base member; a method in which a glass layer is installed or the ratio of the glass component is made higher (erosion is prevented by allowing the glass to fuse rather than the base member); a method in which the pore capacity and the pore diameter are made smaller to form a dense structure (more specifically, the porosity at the end portion is made lower than the porosity of the base member except for the end portion by 3% or more or, preferably the porosity of the end portion is set to 30% or less); a method in which phosphate, aluminum diphosphate, a composite oxide between silica and alkali metal, silica sol, zirconia sol, alumina sol, titania sol, cordierite powder, cordierite cervene (scrap), talc, alumina or the like is added thereto and the corresponding portion is sintered to form a reinforced portion, and a method in which the catalyst layer is made thicker (to prepare a thickness of 1.5 times or less of the base member).
Next, the following description will discuss a manufacturing method (hereinafter, also referred to as the first manufacturing method) for the columnar honeycomb structural body made of porous ceramics of the first embodiment.
First, a material paste is prepared by adding a binder and a dispersant solution to the ceramic powder.
With respect to the above-mentioned binder, not particularly limited, examples thereof include: methylcellulose, carboxy methylcellulose, hydroxy ethylcellulose, polyethylene glycol, phenolic resin and epoxy resin.
In general, the blended amount of the above-mentioned binder is preferably set to 1 to 10 parts by weight with respect to 100 parts by weight of the ceramic powder.
With respect to the dispersant solution, not particularly limited, examples thereof include: an organic solvent such as benzene and the like; alcohol such as methanol and the like; water and the like.
An appropriate amount of the above-mentioned dispersant solution is mixed therein so that the viscosity of the material paste is set within a fixed range.
These ceramic powder, binder and dispersant solution are mixed by an attritor or the like, and sufficiently kneaded by a kneader or the like, and then extrusion-molded so that a columnar formed body having virtually the same shape as the columnar body 15 shown in
Moreover, a molding auxiliary may be added to the material paste, if necessary.
With respect to the molding auxiliary, not particularly limited, examples thereof include: ethylene glycol, dextrin, fatty acid soap, polyalcohol and the like.
Next, the ceramic formed body is dried by using a microwave drier or the like.
Then, if necessary, a mouth-sealing process is carried out so that predetermined through holes are filled with a sealing material (plug), and the resulting formed body is again subjected to a drying process using a microwave drier or the like. With respect to the sealing material (plug), not particularly limited, for example, the same material as the material paste may be used.
When the mouth-sealing process is carried out in the above-mentioned process, a honeycomb structural body, which functions as a honeycomb filter for purifying exhaust gases, is manufactured through post processes.
Next, the ceramic formed body is subjected to degreasing and firing processes under predetermined conditions so that a columnar body 15 made of porous ceramics is manufactured.
Thereafter, a sealing material layer 14 is formed on the circumference of the columnar body 15 thus manufactured.
More specifically, in the sealing material layer-forming process, first, the columnar body 15 is rotated around an axis on which it is supported in the length direction. Next, a sealing material paste is adhered to the circumference of the rotating columnar body 15 to form a sealing material paste layer.
Although not particularly limited, the rotation speed of the columnar body 15 is preferably set in a range from 2 to 10 min−1.
With respect to the sealing material paste, not particularly limited, for example, the above-mentioned inorganic binder, organic binder, material containing inorganic fibers and inorganic particles and the like can be used.
Moreover, the sealing material paste may contain a small amount of moisture, a solvent and the like, and normally, these moisture, solvent and the like are almost entirely scattered through a heating process and the like after the coating process of the sealing material paste.
In order to soften the sealing material paste and impart flowability thereto so as to be easily applied, in addition to the above-mentioned inorganic fibers, inorganic binder, organic binder and inorganic particles, this sealing material paste may contain moisture and another solvent such as acetone, alcohol or the like, in a range from 35 to 65% by weight with respect to the total weight, and the viscosity of the sealing material paste is preferably set in a range from 15 to 25 P.s (10000 to 20000 cps (cP)).
Next, the sealing material paste layer thus formed is dried at a temperature of about 120° C. to evaporate moisture to form a sealing material layer 14 so that a honeycomb structural body 10 having the sealing material layer 14 formed on the circumference on the columnar body 15 as shown in
Next, information regarding the end faces of the honeycomb structural body is displayed on the circumferential surface and/or an end face of the honeycomb structural body thus manufactured.
With respect to the method for displaying the information regarding the end faces, processes, such as an ink coating process, a laser beam irradiation process, a sandblasting process, an etching process, and the like may be used.
In the case of the ink coating, a pigment containing an inorganic oxide such as iron oxide, copper oxide, a cobalt compound such as CoO.nAl2O3 or CO3(PO4)2, TiO2 and SiO2, is preferably used so as to prevent erasure due to the use of high-temperature exhaust gases.
Here, an appropriate method is selected from the above-mentioned methods and used by taking into consideration the material, shape and the like of the honeycomb structural body.
By using the above-mentioned processes, it becomes possible to manufacture the honeycomb structural body of the first embodiment.
Referring to
As shown in
Moreover, the honeycomb structural body 20 has a structure in which a plurality of porous ceramic members 30 are combined with one another through sealing material layers 23 to form a ceramic block 25, and a sealing material layer 24 is formed on the circumference of this ceramic block 25. Here, as explained by reference to
Here, the sealing material layer 24 is placed so as to prevent exhaust gases from leaking from the peripheral portion of the ceramic block 25, when the honeycomb structural body 20 is placed in an exhaust passage of an internal combustion system.
Therefore, the honeycomb structural body 20 shown in
Here, in the same manner as the honeycomb structural body of the second embodiment, in the honeycomb structural body of the second embodiment also, the end portions of the through holes need not necessarily be sealed, and when not sealed, the honeycomb structural body can be used as a catalyst supporting member on which, for example, an exhaust gas purifying catalyst can be supported.
In the same manner as the honeycomb structural body of the first embodiment, the honeycomb structural body 20 on which the information 26 regarding the end faces is displayed on its circumferential surface is advantageous in that upon inserting it into a pipe forming an exhaust passage of an internal combustion system, it becomes possible to prevent misplacement in the direction of the honeycomb structural body 20.
Here, in the case where a catalyst is placed inside the honeycomb structural body (inside the through holes) with a density gradient being formed therein and when a catalyst is applied to only the through holes that are open on the gas flow-out side, it becomes possible to prevent missetting in the amount of application of the catalyst.
In the case of the honeycomb structural body 20 shown in
Not limited to the characters “IN” and “OUT”, the display of information regarding the end faces may be given as other display.
Further, not limited to the display given as characters, the information regarding the end faces of the honeycomb structural body may be given as other forms, such as a barcode, an image drawn in ink, an image given by a laser marker, a label and the like. The information regarding the end faces may be simply given by coloring.
In the case of the ink coating, a pigment containing an inorganic oxide such as iron oxide, copper oxide, a cobalt compound such as CoO.nAl2O3 or CO3(PO4)2, TiO2 and SiO2, is preferably used so as to prevent erasure due to the use of high-temperature exhaust gases.
Moreover, in the case where the information regarding the end faces is displayed on the circumferential surface of the honeycomb structural body, the display is preferably given to a portion closer to either of the corresponding end face. This is because, this clearly indicates which end face the information is related to.
Further, the information regarding the end faces is not necessarily displayed on the circumferential surface of the honeycomb structural body, and may be placed on an end face of the honeycomb structural body. Moreover, the information may be placed on both of the circumferential surface and the end face.
The display of information regarding the end face, given on the corresponding end face of the honeycomb structural body, makes it possible to confirm whether or not the assembling process has been accurately carried out after the installation process thereof in an exhaust-gas purifying apparatus (after installation in a metal case).
In addition to information regarding the end faces, other information, such as, for example, information regarding the manufacturing date, lot number and dimension precision of the circumferential portion of the product, may be given to the circumferential surface and/or the end face of the honeycomb structural body. Further, information regarding the weight, which is required upon setting the amount of application of a catalyst, and information regarding the dimension of the circumferential portion, may be given thereto.
Moreover, in the same manner as the opening diameter and the aperture ratio of the through holes formed in the honeycomb structural body of the first embodiment, the opening diameter and the aperture ratio of the through holes formed in the honeycomb structural body of the second embodiment may be the same with respect to all the through holes, or may be different with each other; however, the opening diameter of the gas flow-in cells is preferably made greater than the opening diameter of the gas flow-out cells.
In other words, the honeycomb structural body of the first embodiment is preferably designed so that the through holes with the ends being sealed on one of face sides and the through holes with the ends being sealed at the other face side have mutually different opening diameters. This is because, it becomes possible to accumulate a large amount of ashes in the gas flow-in cells, to effectively burn the particulates, and consequently to effectively exert functions as the honeycomb filter for purifying exhaust gases.
Moreover, for the same reason as described above, the honeycomb structural body of the first embodiment may be designed so that the respective end faces have mutually different aperture ratios between the through holes with the end faces on one of the sides being sealed and the through holes with the end faces on the other side being sealed.
With respect to the embodiments of the structure in which the respective end faces have mutually different opening diameters and different aperture ratios between the through holes with the end faces on one of the sides being sealed and the through holes with the end faces on the other side being sealed, in the same manner as the honeycomb structural body of the first embodiment, not particularly limited, for example, those structures as shown in FIGS. 6(a) to 6(c) are used.
Moreover, in the honeycomb structural body of the second embodiment, the end face on one of the sides is preferably subjected to a flattening treatment, and in this case, the flatness of the flattened end face is preferably set to 2 mm or less. When the flatness of the end face on one of the sides is set to 2 mm or less, the honeycomb structural body becomes less likely to cause problems upon being inserted into the pipe.
Furthermore, when the end face on one side has been subjected to the flattening treatment, the corresponding information regarding the end faces is preferably displayed on the circumferential surface and/or the end face of the honeycomb structural body.
Here, in the honeycomb structural body of the second embodiment, the flattening treatment may be carried out on both of the end faces; however, as described earlier, such a treatment is disadvantageous from the economic viewpoint.
In the present specification, the expression, “the flatness of the end face of the honeycomb structural body is set to 2 mm or less”, refers to the fact that on the end face of the honeycomb structural body, the distance of the highest protrusion from the averaged position and the distance of the lowest recess from the averaged position are set to 2 mm or less. The flatness of the end face of the honeycomb structural body can be determined by the following processes: for example, the height in the end face direction of the honeycomb structural body is measured at four positions or more, the average of the measured values is calculated, and the distance between the average value of the measured values and the maximum value is found.
The method for the above-mentioned flattening process will be described later.
Moreover, in the honeycomb structural body of the second embodiment, instead of the flattening process to be carried out on the end face of one of the sides, a plurality of the porous ceramic members may be combined with one another so as to eliminate irregularities of the porous ceramic members on the end face of one side. The reason for this will be described later.
Moreover, with respect to the shape of the honeycomb structural body of the second embodiment, not limited to the column shape shown in
The following description will discuss the material and the like of the honeycomb structural body of the second embodiment.
With respect to the material for the porous ceramic member, not particularly limited, the same materials as those described in the honeycomb structural body of the first embodiment, such as nitride ceramics, carbide ceramics, oxide ceramics and the like, may be used, and among these, silicon carbide, which has high heat resistance, superior mechanical properties and high heat conductivity, is more preferably used. Moreover, silicon-containing ceramics in which metallic silicon is blended in the above-mentioned ceramics and ceramics that are combined by silicon and a silicate compound may also be used, and, for example, a material prepared by blending metal silicon in silicon carbide is more preferably used.
With respect to the average pore diameter and the porosity of the porous ceramic member, not particularly limited, the same average pore diameter and porosity as those of the honeycomb structural body of the first embodiment are preferably used, and with respect to the particle size of ceramic particles to be used for manufacturing the porous ceramic member also, not particularly limited, the same particle size as that of the honeycomb structural body of the first embodiment may be used.
Moreover, the honeycomb structural body of the second embodiment can be used as a catalyst supporting member, and in this case, an exhaust gas purifying catalyst is supported on the honeycomb structural body. With respect to the exhaust gas purifying catalyst, the same exhaust gas purifying catalyst as the catalyst to be used when the honeycomb structural body of the first embodiment is used as the catalyst supporting member may be used.
Here, in the same manner as the honeycomb structural body of the first embodiment, the exhaust gas purifying catalyst may be supported uniformly inside the through hole of the honeycomb structural body of the second embodiment, or may be supported on only one area inside the through hole, or may be supported in a manner so as to have a density gradient from one of the gas flow-in side and gas flow-out side toward the other side.
Here, in the same manner as the honeycomb structural body of the first embodiment, the honeycomb structural body of the second embodiment may have a structure in which: end portions of the through holes are sealed so as to function as a honeycomb filter for purifying exhaust gases and an exhaust gas purifying catalyst is supported thereon.
In this case, the exhaust gas purifying catalyst may be supported on both of the gas flow-in cell and the gas flow-out cell, or may be supported on either one of the cells; however, it is preferably supported on only the gas flow-out cell. Thus, the resulting structure is allowed to effectively exert both of the functions as the honeycomb filter for purifying exhaust gases and the functions for purifying exhaust gases.
Moreover, in the case where a catalyst is supported on the honeycomb structural body of the second embodiment, in order to improve the reactivity of the catalyst, the honeycomb structural body may have thin walls (0.01 to 0.2 mm) with a high density (400 to 1500 cells/square inch (62 to 233 cells/cm2)) so that the specific surface area is increased. This structure also makes it possible to improve the temperature-raising property by utilizing exhaust gases.
When the reactivity of the catalyst is improved as described above, in particular, when the thickness of the partition wall is made thinner, the honeycomb structural body becomes more likely to cause erosion (wind erosion) due to exhaust gases. For this reason, the strength of the end portion is preferably improved by the following methods so as to prevent erosion (erosion prevention property) of the end portion on the exhaust gas flow-in side (with respect to the thickness of a portion ranging from 1 to 10 mm in the end).
More specifically, the following methods are proposed: a method in which the partition wall of the end portion is made 1.1 to 2.5 times thicker than the base member; a method in which a glass layer is installed or the ratio of the glass component is made higher (erosion is prevented by allowing the glass to fuse rather than the base member); a method in which the pore capacity and the pore diameter are made smaller to form a dense structure (more specifically, the porosity at the end portion is made lower than the porosity of the base member except for the end portion by 3% or more or, preferably the porosity of the end portion is set to 30% or less); a method in which phosphate, aluminum diphosphate, a composite oxide between silica and alkali metal, silica sol, zirconia, alumina sol, titania sol, cordierite powder, cordierite cervene (scrap), talc, alumina or the like is added thereto and the corresponding portion is sintered to form a reinforced portion, and a method in which the catalyst layer is made thicker (to prepare a thickness of 1.5 times or less the base member).
As shown in
Next, referring to FIGS. 2 to 4, the following description will discuss a method (hereinafter, also referred to as the second manufacturing method) for manufacturing a honeycomb structural body of the second embodiment in which a plurality of porous ceramic members are combined with one another through a sealing material layer.
More specifically, a ceramic laminated body that constitutes a ceramic block 25 is manufactured.
The above-mentioned ceramic laminated body has a pillar-shaped structure in which a plurality of rectangular pillar-shaped porous ceramic members 30, each having a structure in which a large number of through holes 31 are placed in parallel with one another in the length direction with a partition wall 33 interposed there between, are combined with one another through sealing material layers 23.
In order to manufacture the porous ceramic member 30, first, a mixed composition is prepared by adding a binder and a dispersant solution to the above-mentioned ceramic powder.
With respect to the method for preparing the mixed composition, not particularly limited, for example, the same method as the method for preparing the material paste explained in the first manufacturing method may be used.
Next, the above-mentioned mixed composition is mixed by an attritor or the like, and sufficiently kneaded by a kneader or the like, and then extrusion-molded so that a pillar-shaped raw formed body having virtually the same shape as the porous ceramic member 30 shown in
After the above-mentioned raw formed body has been dried by using a microwave drier or the like, a mouth-sealing process which injects a sealing material (plug) to predetermined through holes, and this is again subjected to a drying process using a microwave drier or the like.
With respect to the above-mentioned sealing material (plug), not particularly limited, for example, the same material as the above-mentioned mixed composition may be used.
Next, the raw formed body that has been subjected to the mouth-sealing process is heated at 400 to 650° C. in an oxygen-containing atmosphere so as to be degreased so that the binder and the like are volatilized, as well as being decomposed and eliminated, to allow only the ceramic powder to remain therein.
Next, the formed body that has been degreased is sintered by heating it at 1400 to 2200° C. in an inert gas atmosphere such as nitrogen and argon so that the ceramics powder is sintered to produce a porous ceramic member 30.
Next, as shown in
At this process, upon assembling the porous ceramic members 30, they may be stacked so as to align only the end face on one of the sides of the porous ceramic members. This arrangement makes it possible to provide the following advantages.
In other words, a plurality of porous ceramic members 30, formed through the above-mentioned method, have slight deviations in the shape thereof due to shrinkage errors and warps that occur at the time of drying and sintering processes. For this reason, in the ceramic laminated body formed by stacking the porous ceramic members 30, raised portions and recessed portions of the porous ceramic members tend to appear on each of the end faces thereof, and in this case, as has been described earlier, problems tend to occur upon insertion of the honeycomb structural body into the pipe.
Here, in the case where the porous ceramic members are stacked so as to align only the end face on one of the sides of the porous ceramic laminated body, in the manufactured honeycomb structural body, although there are protrusions and recessions on the end face on the other side, there are aligned end face on one of the sides.
For this reason, in the case where the honeycomb structural body is inserted into the pipe, it becomes possible to avoid the above-mentioned problems by inserting it from the side having the aligned end face.
Therefore, in the honeycomb structural body of the second embodiment, upon manufacturing, the porous ceramic members are stacked so as to align only the end face on one of the sides, and information regarding the end faces is given so as to indicate the aligned end face so that it becomes possible to solve the problem caused upon insertion into the pipe.
Further, this ceramic laminated body is heated in a temperature range from 50 to 100° C. for about an hour so that the paste layer is dried and solidified to form a sealing material layer 23; thereafter, by cutting the peripheral portion thereof by using a diamond cutter or the like into a shape as shown in
With respect to the material for forming the sealing material paste that forms the sealing material layer 23, not particularly limited, for example, the same material as that of the sealing material paste described in the first manufacturing method may be used.
Moreover, prior to cutting the peripheral portion of the dried ceramic laminated body, the ceramic laminated body may be cut perpendicularly to its length direction, if necessary.
By carrying out this process, the length of the manufactured honeycomb structural body in the length direction is set to a predetermined length, and this process also corresponds to the flattening treatment carried out on the end faces of the honeycomb structural body so that, in particular, the flatness of the end face is set to 2 mm or less.
Here, the term, “length direction of the ceramic laminated body”, refers to a direction in parallel with the through holes of the porous ceramic members constituting the ceramic laminated body, and, for example, even in the case where, upon manufacturing a ceramic laminated body, a large number of porous ceramic members are laminated and bonded so that the length of a face formed by the end face of the porous ceramic members becomes longer than the length of the side face, the direction in parallel with the side face of the porous ceramic members is referred to as the length direction of the ceramic laminated body.
With respect to the method for cutting the ceramic laminated body perpendicularly to the length direction thereof, not particularly limited, for example, a method in which at a portion in the vicinity of the end faces of the ceramic laminated body in which all the porous ceramic members are superposed on one another is cut perpendicularly to the length direction of the ceramic laminated body by using a diamond cutter or the like may be used.
By using these processes, the end face of the manufactured ceramic block can be flattened, and, in particular, by using the above-mentioned method, the flatness of the end face of the ceramic block can be set to 2 mm or less.
Here, for the reason as described above, it is only necessary to carry out the flattening process on the end face on one of the sides of the ceramic block.
Next, a sealing material layer 24 is formed on the circumference of the ceramic block 25. Thus, a honeycomb structural body having a structure in which a plurality of porous ceramic members are combined with one another through sealing material layers is formed.
Here, with respect to the method for forming the sealing material layer, not particularly limited, for example, the same method as described in the manufacturing method for the first honeycomb structural body may be used.
Next, information regarding the end faces of the honeycomb structural body is displayed on the circumferential surface and/or an end face of the honeycomb structural body thus manufactured. With respect to the method for displaying the information regarding the end faces, not particularly limited, the same method as described in the manufacturing method for the first honeycomb structural body may be used.
Moreover, in addition to the information regarding the end face, information regarding the honeycomb structural body such as a lot number may be displayed on the circumferential surface and/or an end face of the honeycomb structural body.
By carrying out the above-mentioned processes, it is possible to manufacture the honeycomb structural body of the second embodiment.
Here, an exhaust gas purifying catalyst may be supported on the honeycomb structural body according to the present invention that has been manufactured through the first or second manufacturing method. In other words, in the case where the honeycomb structural body according to the present invention is used as a catalyst supporting member, an exhaust gas purifying catalyst is supported thereon so that the honeycomb structural body according to the present invention is allowed to purify toxic components in exhaust gases, such as HC, CO, NOx and the like, and gases derived from organic components slightly contained in the honeycomb structural body according to the present invention.
Moreover, in the honeycomb structural body according to the present invention, information regarding the end faces is placed on the circumferential surface and/or an end face thereof; therefore, upon installing an exhaust gas purifying catalyst on only the gas flow-out cells or upon installing the catalyst inside the through holes with a density gradient, it becomes possible to prevent missetting in the amount of application of the catalyst.
Furthermore, in the case where an exhaust gas purifying catalyst is placed inside each through hole with one end of the through hole being sealed, the honeycomb structural body according to the present invention is allowed to function as a particle-collecting filter for collecting particulates in exhaust gases, and also to purify toxic components in exhaust gases, such as HC, CO, NOx and the like, and gases derived from organic components slightly contained in the honeycomb structural body according to the present invention.
The following description will discuss the present invention in detail by means of examples; however, the present invention is not intended to be limited by these examples.
(1) Powder of α-type silicon carbide having an average particle size of 10 μm (60% by weight) and powder of β-type silicon carbide having an average particle size of 0.5 μm (40% by weight) were wet-mixed, and to 100 parts by weight of the resulting mixture were added and kneaded 5 parts by weight of an organic binder (methyl cellulose) and 10 parts by weight of water to prepare a kneaded matter. After a slight amount of a plasticizer and a lubricant had been added to the kneaded matter and this had been further kneaded, the resulting kneaded matter was extrusion-molded so that a raw molded product was manufactured.
Next, the above-mentioned raw molded product was dried by using a microwave drier, and predetermined through holes were then filled with a paste having the same composition as the raw molded product, and after having been again dried by using a drier, this was degreased at 400° C., and sintered at 2200° C. in a normal-pressure argon atmosphere for 3 hours to manufacture a porous ceramic member as shown in
(2) A heat resistant sealing material paste, which contained 31% by weight of alumina fibers having a fiber length of 0.2 mm, 22% by weight of silicon carbide particles having an average particle size of 0.6 μm, 16% by weight of silica sol, 1% by weight of carboxymethyl cellulose and 30% by weight of water, was used so that, by carrying out the processes as explained by reference to
(3) Moreover, one end of the resulting ceramic laminated body was cut perpendicularly to the length direction of the ceramic laminated body by using a diamond cutter so that the flatness of the cut end face was set to 0.5 mm. Here, with respect to the flatness of the end face, heights in the end face direction along the circumference of the round shape were measured at eight portions, and the average value of the measured values was calculated; thus, the flatness was determined by finding a difference between the average value of the measured values and the maximum value of the measured values. Here, the flatness on the end face on the side that had not been subjected to the flattening treatment was 2.5 mm.
(4) Successively, the ceramic laminated body was cut in parallel with its length direction by using a diamond cutter so that a cylinder-shaped ceramic block shown in
(5) Next, a protective film (No. 315, made by Nitto Denko Corporation) made of a PET film coated with a thermosetting rubber-based sticker was stuck to each of the two ends of the ceramic block as an adhesive. Here, the protective film has the same shape as the end face of the ceramic block so that it can be stuck to the entire end face of the ceramic block through a sticking process at one time.
(6) Next, a sealing material paste layer was formed on the circumferential portion of the ceramic block by using the above-mentioned sealing material paste. Further, this sealing material paste layer was dried at 120° C. so that a cylinder-shaped honeycomb structural body having a diameter of 143.8 mm, which has sealing material layers formed between the porous ceramic members as well as on the circumferential portion of the ceramic block, with a thickness of 1.0 mm, such as a honeycomb filter 20 shown in
(7) Next, characters “IN” and “OUT” as shown in
Here, ten of these honeycomb structural bodies were prepared.
The same processes as Example 1 were carried out except that upon forming the ceramic laminated body, porous ceramic members were stacked with one end of each ceramic member being aligned and that process (3) of Example 1 was not carried out so that a honeycomb structural body was manufactured.
Here, the end face on the side at which the porous ceramic members had been stacked with aligned end face had a flatness of 1.0 mm, while the end face on the other side had a flatness of 2.5 mm. Moreover, in the present example, a character indicating “Face treated by flattening treatment” was displayed on the end face on the side in which at which the porous ceramic members were stacked with aligned end face.
Here, ten of these honeycomb structural bodies were prepared.
The same processes as those of Example 1 were carried out except that information relating the end faces was not displayed on the circumferential surface of the honeycomb structural body so that a honeycomb structural body was manufactured.
Here, ten of these honeycomb structural bodies were prepared.
With respect to each of the honeycomb structural bodies manufactured in Example 1 and Comparative Example 1, the circumferential portion was coated with a mat made of inorganic fibers, and the honeycomb structural body was then inserted into a pipe constituting an exhaust passage of an internal combustion system. Here, the honeycomb structural body manufactured in each of the examples was inserted from the side that had been subjected to the flattening treatment.
Thereafter, the internal combustion system was continuously driven for 1000 hours.
As a result, all the ten honeycomb structural bodies manufactured in Example 1 were able to be used without having any problems.
In contrast, in the case of the honeycomb structural bodies manufactured in Comparative Example 1, four of the honeycomb structural bodies out of ten had deviations on the mat portion after the continuous driving operation of 1000 hours to cause rattling. When the honeycomb structural bodies having these problems were examined, it was found that all the honeycomb structural bodies had been inserted from the end face on the side having inferior flatness, and that due to the inferior flatness, those bodies had been secured diagonally.
In other words, all the honeycomb structural bodies having problems were caused by misplacement in the direction, upon insertion into the pipe.
The honeycomb structural body according to the present invention, which has the above-mentioned arrangement, makes it possible to clearly distinguish the exhaust gas flow-in side and the exhaust gas flow-out side.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2003-128388 | May 2003 | JP | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/JP04/06424 | 5/6/2004 | WO | 7/19/2005 |
