Honeycomb filter

Abstract

A honeycomb filter including a honeycomb fired body including porous cell partition walls, exhaust gas introduction cells, exhaust gas emission cells, and an outer wall on the periphery thereof. Provided that the hydraulic diameter is given by the following equation (1) and the area based on the given hydraulic diameter is given by the following equation (2), the ratio of the area based on the hydraulic diameter of an exhaust gas introduction cell to the cross-sectional area of the exhaust gas introduction cell is 0.95 to 0.98, and the ratio of the area based on the hydraulic diameter of an exhaust gas emission cell to the cross-sectional area of the exhaust gas emission cell is 0.7 to 0.9: Hydraulic diameter=(4cross-sectional area of cell)/Cross-sectional peripheral length of cell (1), Area based on the hydraulic diameter=(Hydraulic diameter/2).sup.2(2).

Claims

1. A honeycomb filter comprising: a honeycomb fired body including porous cell partition walls defining a plurality of cells that serve as channels of exhaust gas, exhaust gas introduction cells each having an open end at an exhaust gas inlet side and a plugged end at an exhaust gas outlet side, exhaust gas emission cells each having an open end at the exhaust gas outlet side and a plugged end at the exhaust gas inlet side, and an outer wall on the periphery thereof, wherein the cross-sectional shape of each exhaust gas introduction cell in a plane perpendicular to the longitudinal direction thereof is entirely uniform from the end at the exhaust gas inlet side to the end at the exhaust gas outlet side excluding the plugged portion, the cross-sectional shape of each exhaust gas emission cell in a plane perpendicular to the longitudinal direction thereof is entirely uniform from the end at the exhaust gas inlet side to the end at the exhaust gas outlet side excluding the plugged portion, the exhaust gas emission cells, except for the cells adjacent to the outer wall, are each adjacently surrounded fully by the exhaust gas introduction cells across the porous cell partition walls, the cross-sectional area of each exhaust gas emission cell is larger than the cross-sectional area of each exhaust gas introduction cell, and provided that the hydraulic diameter is given by the following equation (1) and the area based on the given hydraulic diameter is given by the following equation (2), the ratio of the area based on the hydraulic diameter of an exhaust gas introduction cell to the cross-sectional area of the exhaust gas introduction cell is 0.95 to 0.98, and the ratio of the area based on the hydraulic diameter of an exhaust gas emission cell to the cross-sectional area of the exhaust gas emission cell is 0.7 to 0.9:
Hydraulic diameter=(4cross-sectional area of cell)/Cross-sectional peripheral length of cell (1)
Area based on the hydraulic diameter=(Hydraulic diameter/2).sup.2(2).

2. The honeycomb filter according to claim 1, wherein a substantial ratio of the number of the exhaust gas introduction cells to the number of the exhaust gas emission cells (exhaust gas introduction cells: exhaust gas emission cells) is 4:1.

3. The honeycomb filter according to claim 1, wherein the cells adjacent to the outer wall include the exhaust gas introduction cells and the exhaust gas emission cells which are alternately arranged with each other.

4. The honeycomb filter according to claim 1, wherein, in a cross section perpendicular to the longitudinal direction of the cells, all the exhaust gas introduction cells, except for the cells adjacent to the outer wall, have the same cross-sectional area.

5. The honeycomb filter according to claim 1, wherein the honeycomb filter is formed by combining a plurality of honeycomb fired bodies with one another with an adhesive layer therebetween.

6. The honeycomb filter according to claim 1, wherein the thickness of the cell partition walls is 0.075 mm to 0.310 mm.

7. The honeycomb filter according to claim 1, wherein the porosity of the cell partition walls is 40 to 65%.

8. The honeycomb filter according to claim 1, wherein the honeycomb fired body is formed of silicon carbide or silicon-containing silicon carbide.

9. The honeycomb filter according to claim 1, wherein a peripheral coat layer is formed on the periphery of the honeycomb filter.

Description

BRIEF DESCRIPTION OF DRAWINGS

(1) FIG. 1 (a) and FIG. 1 (b) are each an enlarged end face view in which a portion of an end face of a honeycomb filter according to one embodiment of the present invention is enlarged.

(2) FIG. 2 is a perspective view schematically showing a honeycomb filter according to an example of a first embodiment of the present invention.

(3) FIG. 3 (a) is a perspective view schematically showing an example of a honeycomb fired body constituting the honeycomb filter shown in FIG. 2. FIG. 3(b) is a cross-sectional view of the honeycomb fired body shown in FIG. 3(a), taken along line A-A.

(4) FIG. 4 is an enlarged end face view in which a portion of an end face of the honeycomb fired body shown in FIG. 3(a) and FIG. 3(b) is enlarged.

(5) FIG. 5 is an explanatory view schematically showing how the pressure loss is measured.

(6) FIG. 6(a) is a perspective view schematically showing an example of a honeycomb fired body constituting a honeycomb filter according to a second embodiment of the present invention. FIG. 6 (b) is a cross-sectional view of the honeycomb fired body shown in FIG. 6(a), taken along line B-B.

(7) FIG. 7 is an enlarged end face view in which a portion of an end face of the honeycomb fired body shown in FIG. 6(a) and FIG. 6(b) is enlarged.

(8) FIG. 8 (a) is a perspective view schematically showing a honeycomb filter disclosed in Patent Literature 1. FIG. 8(b) is a perspective view schematically showing a honeycomb fired body constituting the honeycomb filter.

(9) FIG. 9(a) is a perspective view schematically showing a honeycomb filter disclosed in Patent Literature 2. FIG. 9(b) is a view schematically showing an end face of the honeycomb filter.

(10) FIG. 10 is a cross-sectional view schematically showing a cross section of a honeycomb filter disclosed in Patent Literature 3.

(11) FIG. 11 is a cross-sectional view schematically showing a cross section of a honeycomb fired body constituting a honeycomb filter disclosed in Patent Literature 4.

(12) FIG. 12(a) is a perspective view schematically showing a honeycomb filter according to Comparative Example 1. FIG. 12(b) is a perspective view schematically showing a honeycomb fired body constituting the honeycomb filter shown in FIG. 12(a).

DESCRIPTION OF EMBODIMENTS

(13) Hereinafter, embodiments of the present invention are specifically described. The present invention is not limited to these embodiments, and may be modified within a scope not changing the gist of the present invention.

(14) (First Embodiment)

(15) The following will describe the first embodiment which is one embodiment of the honeycomb filter of the present invention.

(16) The honeycomb filter according to the first embodiment of the present invention includes a honeycomb fired body. The honeycomb fired body includes porous cell partition walls defining a plurality of cells that serve as channels of exhaust gas, exhaust gas introduction cells each having an open end at an exhaust gas inlet side and a plugged end at an exhaust gas outlet side, exhaust gas emission cells each having an open end at the exhaust gas outlet side and a plugged end at the exhaust gas inlet side, and an outer wall on the periphery thereof.

(17) In addition, the exhaust gas emission cells, except for the cells adjacent to the outer wall, are each adjacently surrounded fully by the exhaust gas introduction cells across the porous cell partition walls; the cross-sectional area of each exhaust gas emission cell is larger than the cross-sectional area of each exhaust gas introduction cell; and provided that the hydraulic diameter is given by the following equation (1) and the area based on the given hydraulic diameter is given by the following equation (2), the ratio (S ratio) of the area based on the hydraulic diameter of an exhaust gas introduction cell to the cross-sectional area of the exhaust gas introduction cell is 0.95 to 0.98, and the ratio (S ratio) of the area based on the hydraulic diameter of an exhaust gas emission cell to the cross-sectional area of the exhaust gas emission cell is 0.7 to 0.9:
Hydraulic diameter=(4cross-sectional area of cell)/Cross-sectional peripheral length of cell(1),
Area based on the hydraulic diameter=(Hydraulic diameter/2).sup.2(2).

(18) Specifically, all the exhaust gas introduction cells of the present embodiment have a cross-sectional shape formed by rounding the corners of a pentagon, and the shape is entirely formed of curved lines. The S ratio is in the range of 0.95 to 0.98. In contrast, the cross-sectional shape of each exhaust gas emission cell is a square, and the S ratio is in the range of 0.785 which is in range of 0.7 to 0.9.

(19) The S ratio of the exhaust gas introduction cell is preferably 0.96 to 0.98, and the S ratio of the exhaust gas emission cell is preferably 0.75 to 0.85.

(20) The cells adjacent to the outer wall include the exhaust gas introduction cells and the exhaust gas emission cells which are alternately arranged with each other.

(21) In addition, the cross-sectional shape of each exhaust gas introduction cell in a plane perpendicular to the longitudinal direction thereof is entirely uniform from the end at the exhaust gas inlet side to the end at the exhaust gas outlet side excluding the plugged portion; and the cross-sectional shape of each exhaust gas emission cell in a plane perpendicular to the longitudinal direction thereof is entirely uniform from the end at the exhaust gas inlet side to the end at the exhaust gas outlet side excluding the plugged portion.

(22) A substantial ratio of the number of the exhaust gas introduction cells to the number of the exhaust gas emission cells (exhaust gas introduction cells:exhaust gas emission cells) is 4:1, and all the exhaust gas introduction cells, except for the cells adjacent to the outer wall, have the same cross-sectional area in a plane perpendicular to the longitudinal direction thereof, which is smaller than the cross-sectional area of each exhaust gas emission cell in a plane perpendicular to the longitudinal direction thereof.

(23) FIG. 2 is a perspective view schematically showing the honeycomb filter according to the first embodiment of the present invention.

(24) FIG. 3(a) is a perspective view schematically showing an example of a honeycomb fired body constituting the honeycomb filter shown in FIG. 2. FIG. 3(b) is a cross-sectional view of the honeycomb fired body shown in FIG. 3(a), taken along line A-A. FIG. 4 is an enlarged end face view in which a portion of an end face of the honeycomb fired body shown in FIG. 3(a) and FIG. 3(b) is enlarged.

(25) In the honeycomb filter 20 shown in FIG. 2, a ceramic block 18 is formed by combining a plurality of honeycomb fired bodies 10 with one another with an adhesive layer 15 therebetween, and a peripheral coat layer 16 is formed on the periphery of the ceramic block 18 to prevent leakage of exhaust gas. The peripheral coat layer 16 is optionally formed.

(26) The honeycomb fired body 10 has a substantially rectangular pillar shape, and as shown in FIG. 3 (a), the corners of the end faces are rounded in a curve. This prevents damage such as cracks due to concentration of thermal stress at the corners. Alternatively, the corners may be linearly chamfered.

(27) In the honeycomb filter 20 according to the first embodiment, the exhaust gas emission cells 11 each have an open end at the exhaust gas outlet side and a plugged end at the exhaust gas inlet side. The exhaust gas introduction cells 12 each have an open end at the exhaust gas inlet side and a plugged end at the exhaust gas outlet side. The material of the plug material is preferably the same as that of the honeycomb fired body.

(28) In the honeycomb fired body 10 shown in FIG. 3 (a) and FIG. 3 (b), each exhaust gas emission cell 11 having a square cross section is adjacently surrounded fully by eight exhaust gas introduction cells 12 across the porous cell partition walls 13. These exhaust gas introduction cells 12 each have a cross-sectional shape formed by rounding the corners of a pentagon, and the shape is entirely formed of curved lines. All the exhaust gas introduction cells 12, except for the cells adjacent to an outer wall 17, have the same shape. All the exhaust gas emission cells 11, except for the cells adjacent to the outer wall 17, also have the same shape.

(29) As shown in FIG. 1 (a), when a square formed by connecting the centroid of each of four adjacent exhaust gas emission cells 11 is considered as one unit of this pattern of arrangement, this unit includes four exhaust gas introduction cells 12 in such a manner that the portions sticking out from the exhaust gas emission cell 11 face one another at the center of the unit, forming a substantially cruciform shape. Four portions of the exhaust gas emission cells 11 are respectively located at the four empty corners of the square.

(30) The outer wall 17 has corners. In order to make the thickness of the outer wall excluding the corners uniform, exhaust gas emission cells 11A are formed such that their sides closest to the outer wall in a cross section perpendicular to the longitudinal direction of the cells are straight and parallel to a side defining an outer periphery of the outer wall 17. The exhaust gas introduction cells 12A are formed such that their portions closest to the outer wall 17 are aligned on a line extended from a side of each exhaust gas emission cell 11A, the side being the closest to the outer wall.

(31) In regard to the cells adjacent to the outer wall 17, the exhaust gas introduction cells 12A and the exhaust gas emission cells 11A are alternately arranged with each other. The exhaust gas introduction cells 12A each have a shape formed by rounding the corners of a pentagon, and the area of the exhaust gas introduction cell 12A is larger than that of the exhaust gas introduction cell 12 not adjacent to the outer wall 17. In contrast, the area of each exhaust gas emission cell 11A adjacent to the outer wall 17 is substantially the same as the area of each exhaust gas emission cell 11 not adjacent to the outer wall 17.

(32) The area of each exhaust gas emission cell 11A adjacent to the outer wall 17 is preferably 65 to 95%, more preferably 70 to 85%, of the area of each exhaust gas emission cell 11 other than the exhaust gas emission cells 11A adjacent to the outer wall 17.

(33) In addition, the area of each exhaust gas introduction cell 12A adjacent to the outer wall 17 is preferably 130 to 200%, more preferably 150 to 180%, of the area of each exhaust gas introduction cell 12 other than the exhaust gas introduction cells 12A adjacent to the outer wall 17.

(34) Exhaust gas emission cells 11B located at the corners of the honeycomb fired body 10 each have a substantially square shape with a rounded portion 110B in a curve. The rounded portion 110B of the exhaust gas emission cell 11B shown in FIG. 3(a) is a corner that is rounded in a curve, but the corner may be linearly chamfered. The cross-sectional area of each exhaust gas emission cell 11B is substantially the same as that of each exhaust gas emission cell 11 not adjacent to the outer wall 17.

(35) In the honeycomb filter of the present embodiment, as described above, although the cross-sectional area of each exhaust gas introduction cell 12 is smaller than the cross-sectional area of each exhaust gas emission cell 11, the S ratio of the exhaust gas introduction cell is set to 0.95 to 0.98 to allow exhaust gas to easily flow through the exhaust gas introduction cells. Thus, the flow-through resistance (b) of the exhaust gas introduction cells can be reduced.

(36) In addition, the cross-sectional area of each exhaust gas emission cell 11 is larger than the cross-sectional area of each exhaust gas introduction cell 12. Thus, the effect of reducing the flow-through resistance (e) of the exhaust gas emission cells 11 and the outflow resistance (f) upon flowing of exhaust gas out of the honeycomb filter is high, and as a result, the pressure loss can be reduced as compared to the conventional honeycomb filter 90.

(37) In addition, generally, at an early stage, a layer of accumulated PM is mainly formed on the cell partition walls 13 separating the exhaust gas introduction cell 12 and the exhaust gas emission cell 11 from each other, specifically on the cell partition walls 13 on the exhaust gas introduction cell 12 side. Yet, since a substantial ratio of the number of the exhaust gas introduction cells 12 to the number of the exhaust gas emission cells 11 (exhaust gas introduction cells:exhaust gas emission cells) is 4:1, the passage resistance of the cell partition walls 13b and 13c separating the exhaust gas introduction cells 12 from each other is not much high. Thus, after a very short period of time, exhaust gas enters the cell partition walls 13 separating the exhaust gas introduction cells 12 from each other, and then passes through the cell partition walls 13 into the exhaust gas emission cells 11. Thus, PM gradually accumulates also on the cell partition walls 13 separating the exhaust gas introduction cells 12 from each other. As a result, PM accumulates substantially uniformly on the entire cell partition walls 13 defining the exhaust gas introduction cells 12. In the present invention, PM accumulates uniformly at an earlier stage, i.e., exhaust gas can easily pass through a larger area of cell partition walls 13 at an early stage. Thus, the initial pressure loss can be reduced.

(38) In addition, a substantial ratio of the exhaust gas introduction cells to the exhaust gas emission cells is 4:1, and the total volume of the exhaust gas introduction cells 12 can be made large. Thus, a substantial filtration area can be made sufficiently large. Also, the layer of PM accumulated on the cell partition walls 13 defining the exhaust gas introduction cells 12 is thin, and the passage resistance (d) upon passage of exhaust gas through the layer of accumulated PM is kept low. As a result, the present invention can provide a honeycomb filter in which the pressure loss at an early stage is low and the pressure loss is less likely to increase even after accumulation of PM.

(39) Owing to the above-described configuration of the outer wall 17 and its adjacent exhaust gas emission cells 11 and exhaust gas introduction cells 12, the honeycomb filter 20 according to the first embodiment achieves the following effects in addition to the effects described above: the outer wall 17 increases the strength of the honeycomb fired bodies 10, further reduces local variations in the volume ratio between the exhaust gas emission cells 11 and the exhaust gas introduction cells 12 in the honeycomb fired bodies 10, and thus allows exhaust gas to flow more uniformly. Also, exhaust gas can smoothly flow into the exhaust gas introduction cells 12 even near the outer wall 17, and the cell partition walls 13 and the outer wall 17 can function as filters, so that the pressure loss can be further reduced.

(40) In regard to the shapes of the cells, in the honeycomb filter 20 shown in FIG. 3(a) and FIG. 3(b), the exhaust gas emission cells 11, 11A, and 11B respectively have square, rectangular, and partially-rounded square cross sections, and the exhaust gas introduction cells 12 and 12A each have a shape formed by rounding the corners of a pentagon. Yet, the cross-sectional shapes of exhaust gas emission cells and the exhaust gas introduction cells constituting the honeycomb filter of the present invention are not limited to the above shapes. For example, the cross-sectional shape of the exhaust gas emission cells may be a polygon other than the square. Specifically, the cross-sectional shape of the exhaust gas emission cells may be an octagon. The cross-sectional shape of the exhaust gas introduction cells may be an ellipse or race track shape.

(41) In addition, the vertexes of the exhaust gas emission cells each having a polygonal cross section such as a square may be rounded in a curve in the cross section.

(42) The curve may be a curve (arc) obtained when a circle is divided into quarters or a curve obtained when an ellipse is divided into quarters with the major axis and a straight line perpendicular to the major axis, for example. It is particularly preferred that the vertexes of a cell having a square cross section are rounded in a curve. This prevents cracking in the cell partition walls due to concentration of stress at the corners.

(43) In addition, the honeycomb filter 20 may include, if necessary, some cells each having a cross section that includes a curve such as an arc which is a part of a circle.

(44) In the honeycomb filters shown in FIG. 2, FIG. 3(a), and FIG. 3(b), the ratio (%) of the cross-sectional area of each exhaust gas introduction cell 12 relative to the cross-sectional area of each exhaust gas emission cell 11 is preferably 30 to 50%, more preferably 35 to 45%.

(45) In the honeycomb filter of the present invention, the thickness of the cell partition walls in the honeycomb filter is preferably 0.075 to 0.310 mm.

(46) The cell partition walls having a thickness of less than 0.075 mm are so thin that the mechanical strength of the honeycomb filter is reduced. In contrast, the cell partition walls having a thickness of more than 0.310 mm are so thick that the pressure loss upon passage of exhaust gas through the cell partition walls is increased.

(47) In the honeycomb filter of the present invention, the porosity of the cell partition wall is preferably 40 to 65%.

(48) The cell partition walls having a porosity of 40 to 65% can successfully capture PM in exhaust gas, and the pressure loss due to the cell partition walls can be kept low. Thus, the present invention can provide a honeycomb filter in which the initial pressure loss is low and the pressure loss is less likely to increase even after accumulation of PM.

(49) If the cell partition walls have a porosity of less than 40%, the ratio of pores in the cell partition walls is so small that exhaust gas cannot easily pass through the cell partition walls, and the pressure loss upon passage of exhaust gas through the cell partition walls is increased. In contrast, the cell partition walls having a porosity of more than 65% have poor mechanical characteristics and is susceptible to cracking during regeneration or the like. The pore diameter and the porosity are measured by mercury porosimetry with a contact angle of 130 and a surface tension of 485 mN/m.

(50) In the honeycomb filter of the present invention, the average pore diameter of the pores in the cell partition walls is preferably 8 to 25 m.

(51) The honeycomb filter configured as described above can capture PM with high capturing efficiency while suppressing an increase in the pressure loss. If the average pore diameter of the pores contained in the cell partition walls is less than 8 m, the pores are so small that the pressure loss upon passage of exhaust gas through the cell partition walls is increased. In contrast, if the average pore diameter of the pores contained in the cell partition walls is more than 25 m, the pore diameter is so large that the PM capturing efficiency is decreased.

(52) The honeycomb filter of the present invention may include a plurality of honeycomb fired bodies or a single honeycomb fired body. Examples of materials of the honeycomb fired body include carbide ceramics such as silicon carbide, titanium carbide, tantalum carbide, and tungsten carbide; nitride ceramics such as aluminum nitride, silicon nitride, boron nitride, and titanium nitride; oxide ceramics such as alumina, zirconia, cordierite, mullite, and aluminum titanate; and silicon-containing silicon carbide. Silicon carbide or silicon-containing silicon carbide is preferred among these, because these materials are excellent in properties such as heat resistance, mechanical strength, and thermal conductivity.

(53) The silicon-containing silicon carbide is a mixture of silicon carbide and silicon metal, and is preferably silicon-containing silicon carbide containing 60 wt % or more of silicon carbide.

(54) The number of the cells per unit area in a cross section of the honeycomb fired body 10 is preferably 31 to 62 pcs/cm.sup.2 (200 to 400 pcs/inch.sup.2).

(55) The honeycomb filter of the present invention 20 is preferably formed by combining a plurality of honeycomb fired bodies each having an outer wall on the periphery thereof, with an adhesive layer therebetween. In the case where the honeycomb filter is formed by combining a plurality of honeycomb fired bodies with an adhesive layer therebetween as described above, the adhesive layer that combines the honeycomb fired bodies is prepared by applying an adhesive paste containing an inorganic binder and inorganic particles and drying the adhesive paste. The adhesive layer may further contain inorganic fibers and/or whiskers. The thickness of the adhesive layer is preferably 0.5 to 2.0 mm.

(56) The honeycomb filter according to the first embodiment of the present invention may include a peripheral coat layer on the periphery of the honeycomb filter. The material of the peripheral coat layer is preferably the same as that of the adhesive.

(57) The thickness of the peripheral coat layer is preferably 0.1 to 3.0 mm.

(58) The following will describe a method for manufacturing the honeycomb filter of the present invention.

(59) A silicon carbide is used as ceramic powder in the method described below.

(60) (1) A honeycomb molded body is manufactured by extruding a wet mixture containing ceramic powder and a binder (extrusion molding step).

(61) Specifically, first, silicon carbide powders having different average particle sizes serving as ceramic powder, an organic binder, a liquid plasticizer, a lubricant, and water are mixed to prepare a wet mixture for manufacturing a honeycomb molded body.

(62) The wet mixture may contain, if necessary, a pore-forming agent such as balloons that are fine hollow spheres formed of oxide-based ceramics, spherical acrylic particles, or graphite.

(63) Any balloons may be used. Examples thereof include alumina balloon, glass micro balloon, shirasu balloon, fly ash balloon (FA balloon), and mullite balloon. Alumina balloon is preferable among these.

(64) Subsequently, the wet mixture is fed into an extrusion machine and extruded into a honeycomb molded body having a predetermined shape.

(65) At this point, a honeycomb molded body is manufactured using a die that can make a cross-sectional shape having the cell structures (shapes and arrangement of the cells) shown in FIG. 2, FIG. 3 (a), and FIG. 3 (b).

(66) (2) The honeycomb molded body is cut into a predetermined length and dried with a drying apparatus such as a microwave drying apparatus, a hot-air drying apparatus, a dielectric drying apparatus, a reduced-pressure drying apparatus, a vacuum drying apparatus, or a freeze drying apparatus. Then, predetermined cells are plugged by placing a plug material paste that serves as a plug material (plugging step).

(67) The wet mixture can be used as the plug material paste.

(68) (3) The honeycomb molded body is heated at 300 C. to 650 C. in a degreasing furnace to remove organic matter in the honeycomb molded body (degreasing process). Subsequently, the degreased honeycomb molded body is transferred to a firing furnace and fired at 2000 C. to 2200 C. (firing process), whereby the honeycomb fired body as shown in FIG. 2, FIG. 3 (a), and FIG. 3(b) is manufactured.

(69) The plug material paste placed at the end of each cell is fired by heat into a plug material.

(70) Conventional conditions for manufacturing honeycomb fired bodies can be applied to cutting, drying, plugging, degreasing, and firing.

(71) (4) A single honeycomb fired body manufactured by the above steps may be used as-is as a honeycomb filter. However, when silicon carbide is used as ceramic powder, it is preferred that a plurality of honeycomb fired bodies are combined with one another with an adhesive layer therebetween.

(72) In such a case, a plurality of honeycomb fired bodies are stacked in series with an adhesive paste therebetween on a support table, and the honeycomb fired bodies are combined with one another (combining step), whereby a honeycomb aggregated body including a plurality of stacked honeycomb fired bodies is manufactured.

(73) The adhesive paste contains, for example, an inorganic binder, an organic binder, and inorganic particles. The adhesive paste may further contain inorganic fibers and/or whiskers.

(74) Examples of the inorganic particles contained in the adhesive paste include carbide particles and nitride particles. Specific examples thereof include silicon carbide particles, silicon nitride particles, and boron nitride particles. These may be used alone or in combination of two or more thereof. The inorganic particles are preferably silicon carbide particles having excellent thermal conductivity.

(75) Examples of the inorganic fibers and/or whiskers contained in the adhesive paste include inorganic fibers and/or whiskers made of silica-alumina, mullite, alumina, silica, or the like. These may be used alone or in combination of two or more thereof. The inorganic fibers are preferably alumina fibers. Alternatively, the inorganic fibers may be biosoluble fibers.

(76) The adhesive paste may contain, if necessary, balloons that are fine hollow spheres formed of oxide-based ceramics, spherical acrylic particles, and graphite. Any balloons may be used. Examples thereof include alumina balloon, glass micro balloon, shirasu balloon, fly ash balloon (FA balloon), and mullite balloon.

(77) (5) Subsequently, the honeycomb aggregated body is heated to solidify the adhesive paste into an adhesive layer, whereby a rectangular pillar-shaped ceramic block is manufactured.

(78) Conventional conditions for manufacturing honeycomb filters can be applied to heating and solidifying of the adhesive paste.

(79) (6) The ceramic block is subjected to cutting (cutting step).

(80) Specifically, the periphery of the ceramic block is cut with a diamond cutter, whereby a ceramic block formed in a substantially round pillar shape is manufactured.

(81) (7) A peripheral coat material paste is applied to the peripheral face of the substantially round pillar-shaped ceramic block, and is dried and solidified to forma peripheral coat layer (peripheral coat layer forming step).

(82) The adhesive paste may be used as the peripheral coat material paste. Alternatively, a paste having a composition different from the adhesive paste may be used as the peripheral coat paste.

(83) The peripheral coat layer is optional and is not necessarily formed.

(84) The peripheral coat layer helps to adjust the peripheral shape of the ceramic block to provide a round pillar-shaped honeycomb filter.

(85) The honeycomb filter including the honeycomb fired bodies can be manufactured through the above steps.

(86) In the above steps, a honeycomb filter having a predetermined shape is manufactured through the cutting step. However, a honeycomb filter having a predetermined shape such as a round pillar shape may be obtained by manufacturing various shapes of honeycomb fired bodies each having an outer wall on the entire periphery in the step of manufacturing a honeycomb fired body, and combining these various shapes of honeycomb fired bodies with one another with an adhesive layer therebetween. In this case, the cutting step can be omitted.

(87) Hereinafter, the effects of the honeycomb filter of the present invention are listed.

(88) (1) In the honeycomb filter of the present embodiment, each exhaust gas emission cell is surrounded fully by the exhaust gas introduction cells across the porous cell partition walls. Thus, the cell partition walls surrounding the exhaust gas emission cell can be entirely used.

(89) (2) In the honeycomb filter of the present embodiment, although the cross-sectional area of each exhaust gas introduction cell is smaller than the cross-sectional area of each exhaust gas emission cell, the S ratio of the exhaust gas introduction cell is set to 0.95 to 0.98 to allow exhaust gas to easily flow through the exhaust gas introduction cells. Thus, the flow-through resistance (b) of the exhaust gas introduction cells can be reduced.

(90) In addition, the cross-sectional area of each exhaust gas emission cell is larger than the cross-sectional area of each exhaust gas introduction cell. Thus, the effect of reducing the flow-through resistance (e) of the exhaust gas emission cells and the outflow resistance (f) upon flowing of exhaust gas out of the honeycomb filter is high, and as a result, the pressure loss can be reduced, as compared to the conventional honeycomb filters.

(91) (3) In the honeycomb filter of the present embodiment, a substantial ratio of the number of the exhaust gas introduction cells to the number of the exhaust gas emission cells (exhaust gas introduction cells:exhaust gas emission cells) can be set to 4:1. In such a case, the passage resistance of the cell partition walls separating the exhaust gas introduction cells from each other is not much high. As a result, PM accumulates uniformly at an earlier stage, i.e., exhaust gas can easily pass through a larger area of the cell partition walls at an early stage. Thus, the initial pressure loss can be reduced.

(92) (4) The honeycomb filter of the present embodiment can have a structure in which the cross-sectional area of each exhaust gas emission cell in a plane perpendicular to the longitudinal direction thereof is larger than the cross-sectional area of each exhaust gas introduction cell in a plane perpendicular to the longitudinal direction thereof, and the cells adjacent to the outer wall include the exhaust gas introduction cells and the exhaust gas emission cells which are alternately arranged with each other. In such a case, exhaust gas flows easily from the exhaust gas introduction cells adjacent to the outer wall to the exhaust gas emission cells each having a large cross-sectional area, and exhaust gas can flow not only through partition walls that define the exhaust gas introduction cells adjacent to the outer wall but also the outer wall that defines the exhaust gas introduction cells. Thus, a substantial filtration area can be maximized. This makes it possible to provide a honeycomb filter in which the initial pressure loss is lower and the pressure loss is further less likely to increase even after accumulation of PM.

(93) (5) In the honeycomb filter of the present invention, in a cross section perpendicular to the longitudinal direction of the cells, all the exhaust gas introduction cells each can be formed by rounding the corners of a pentagon, and the shape can be entirely formed of curved lines. In such a case, it is possible to easily design the cross-sectional shape of the honeycomb fired body constituting the honeycomb filter and to form the exhaust gas introduction cells each having a wider filtration area. Thus, a honeycomb filter in which the pressure loss is lower can be provided.

(94) (6) In the honeycomb filter of the present embodiment, silicon carbide or silicon-containing silicon carbide can be used as a material of the honeycomb fired body. In such a case, a honeycomb filter having excellent heat resistance can be provided.

(95) (7) In the honeycomb filter of the present invention, a plurality of honeycomb fired bodies can be combined with one another with an adhesive layer therebetween. In such a case, the adhesive layer can act as a buffer layer during regeneration or the like, preventing the honeycomb filter from being destroyed by thermal stress. The adhesive layer can also increase the mechanical strength.

(96) (8) In the honeycomb filter of the present invention, the cell partition walls can be made as thin as 0.075 mm to 0.310 mm. In such a case, the passage resistance upon passage of exhaust gas through the cell partition walls can be reduced, and the pressure loss can be further reduced.

(97) The following will describe examples that more specifically disclose the first embodiment of the present invention. The present invention is not limited to these examples.

(98) (Example 1)

(99) A mixture was obtained by mixing 52.8% by weight of silicon carbide coarse powder having an average particle size of 22 m and 22.6% by weight of silicon carbide fine powder having an average particle size of 0.5 m. To the mixture were added 4.6% by weight of an organic binder (methylcellulose), 0.8% by weight of a lubricant (UNILUB, manufactured by NOF Corporation), 1.3% by weight of glycerin, 1.9% by weight of a pore-forming agent (acrylic resin), 2.8% by weight of oleic acid, and 13.2% by weight of water. These components were kneaded to obtain a wet mixture. Subsequently, the wet mixture was extruded (extrusion molding step).

(100) In this step, a raw honeycomb molded body having the same shape as the honeycomb fired body 10 shown in FIG. 3(a) with the cells unplugged was manufactured.

(101) Then, the raw honeycomb molded body was dried using a microwave drying apparatus to obtain a dried honeycomb molded body. Subsequently, predetermined cells of the dried honeycomb molded body were plugged by placing a plug material paste.

(102) Specifically, the cells were plugged at the end of the exhaust gas inlet side and at the end of the exhaust gas outlet side at positions shown in FIG. 3(a).

(103) The wet mixture was used as the plug material paste. After plugging the cells, the dried honeycomb molded body with the plug material paste placed in the cells was dried again with a drying apparatus.

(104) Subsequently, the dried honeycomb molded body with the plugged cells was degreased at 400 C. (degrease treatment), and further fired at 2200 C. in an argon atmosphere at normal pressure for three hours (firing treatment).

(105) In this manner, a rectangular pillar-shaped honeycomb fired body was manufactured.

(106) The length of sides and the cross-sectional area can be measured using the electron microscope and the measurement software such as image analysis and grain size distribution measurement software (Mac-View (Version 3.5), produced by Mountech Co. Ltd.) described above.

(107) The manufactured honeycomb fired body was the honeycomb fired body 10 shown in FIG. 3(a) and FIG. 3 (b) formed of a silicon carbide sintered body in which the porosity was 45%, the average pore diameter was 15 m, the size was 34.3 mm34.3 mm150 mm, the number of cells per unit area (cell density) was 345 pcs/inch.sup.2, and the thickness of the cell partition walls 13 was 0.25 mm.

(108) In a cross section of the manufactured honeycomb fired body 10 in a plane perpendicular to the longitudinal direction of the cells, each exhaust gas emission cell 11 was adjacently surrounded fully by the exhaust gas introduction cells 12.

(109) The exhaust gas introduction cells 12 and 12A each had a cross-sectional shape formed by rounding the corners of a pentagon, and the shape was entirely formed of curved lines. The cross-sectional area of the exhaust gas introduction cell 12 was 0.806 mm.sup.2. In addition, the cross-sectional area of each exhaust gas introduction cell 12A adjacent to the outer wall 17 was 1.354 mm.sup.2 (see FIG. 4). The S ratio of the exhaust gas introduction cell was 0.974.

(110) The cross-sectional shape of each exhaust gas emission cell 11 was a square, the length of the side 11a was 1.503 mm, and the cross-sectional area of each exhaust gas emission cell 11 was 2.259=.sup.2. The S ratio of each exhaust gas emission cell was 0.785.

(111) Each exhaust gas emission cell 11B located at the four corners of the honeycomb fired body 10 had a cross-sectional area of 1.478 mm.sup.2.

(112) In contrast, in regard to the exhaust gas emission cells 11A, the length of a side 11Aa perpendicular to the outer wall 17 was 1.234 mm (see FIG. 4).

(113) The honeycomb fired body 10 had a rectangular pillar shape in which the corners of the end face were rounded in a curve. The total aperture ratio of the exhaust gas introduction cells and the exhaust gas emission cells of the honeycomb fired body 10 was 61.3%, and the area ratio of the cell partition walls was 38.7%.

(114) Subsequently, a plurality of honeycomb fired bodies were combined with one another using an adhesive paste containing 30% by weight of alumina fibers having an average fiber length of 20 m, 21% by weight of silicon carbide particles having an average particle size of 0.6 m, 15% by weight of silica sol, 5.6% by weight of carboxymethyl cellulose, and 28.4% by weight of water. Further, the adhesive paste was dried and solidified at 120 C. to form an adhesive layer, whereby a rectangular pillar-shaped ceramic block was manufactured.

(115) Subsequently, the periphery of the rectangular pillar-shaped ceramic block was cut out using a diamond cutter, whereby a substantially round pillar-shaped ceramic block was manufactured.

(116) Subsequently, a sealing material paste having the same composition as the adhesive paste was applied to the peripheral face of the ceramic block. The sealing material paste was dried and solidified at 120 C. to form a peripheral coat layer, whereby a round pillar-shaped honeycomb filter was manufactured.

(117) The aperture ratio of the exhaust gas introduction cells 12 in the honeycomb filter was 32.9%, and the aperture ratio of the exhaust gas emission cells 11 in the honeycomb filter was 24.3%.

(118) The honeycomb filter had a diameter of 143.8 mm and a longitudinal length of 150 mm.

(119) (Comparative Example 1)

(120) The extrusion molding step was performed as in Example 1 to obtain a raw honeycomb molded body, except that the cross-sectional shapes of the exhaust gas introduction cells and the exhaust gas emission cells were patterned as shown in FIG. 12(b) and that the cells were not plugged. Then, the raw honeycomb molded body was dried using a microwave drying apparatus to obtain a dried honeycomb molded body. Subsequently, predetermined cells of the dried honeycomb molded body were plugged by placing a plug material paste. The cells were plugged at positions as shown in FIG. 12(b).

(121) As a result, a honeycomb molded body in which the cells were plugged at the end of the exhaust gas inlet side and at the end of the exhaust gas outlet side at positions as shown in FIG. 12(b) was obtained.

(122) Subsequently, the steps as in Example 1 were performed to manufacture a honeycomb fired body 150 shown in FIG. 12(a) and FIG. 12(b), and a honeycomb filter 140 was manufactured.

(123) In a cross section of the manufactured honeycomb fired body 150 in a plane perpendicular to the longitudinal direction of the cells, all the exhaust gas introduction cells 152 except for exhaust gas introduction cells 152A and 152B adjacent to an outer wall 157 were octagonal.

(124) The sides facing exhaust gas emission cells 151 were vertical or horizontal sides, each having a length of 1.11 mm.

(125) The other sides facing the exhaust gas introduction cells 152, 152A, and 152B were hypotenuse sides, each having a length of 0.27 mm.

(126) All the exhaust gas emission cells 151 and 151A were square, and the length of the sides forming the cross-sectional shape of the exhaust gas emission cells 151 and 151A was 0.96 mm.

(127) In regard to each exhaust gas introduction cell 152B located at the four corners, the length of a side adjacent to the outer wall 157 was 1.23 mm, the length of a vertical or horizontal side was 1.04 mm, the length of a hypotenuse side was 0.27 mm, and the cross-sectional area was 1.48 mm.sup.2.

(128) In contrast, in regard to each exhaust gas introduction cell 152A, the length of a side adjacent to the outer wall 157 was 1.49 mm, the length of a vertical side parallel to the side adjacent to the outer wall 157 was 1.11 mm, the length of a horizontal side connected at a right angle to the side adjacent to the outer wall 157 was 1.04 mm, the length of a hypotenuse side was 0.27 mm, and the cross-sectional area was 1.79 mm.sup.2.

(129) The thickness of the cell partition walls 153 was 0.25 mm, and the thickness of the outer wall 157 was 0.35 mm.

(130) The cross-sectional area of each exhaust gas introduction cell 152 was 2.17 mm.sup.2, and the cross-sectional area of each exhaust gas emission cell 151 was 0.93 mm.sup.2. Specifically, the cross-sectional area of each exhaust gas introduction cell 152 was larger than the cross-sectional area of each exhaust gas emission cell 151. The S ratio of each exhaust gas introduction cell was 0.895. The S ratio of each exhaust gas emission cell was 0.785. In addition, the total aperture ratio of the exhaust gas introduction cells and the exhaust gas emission cells of the honeycomb fired body 10 was 66.0%, and the area ratio of the cell partition walls was 34.0%.

(131) (Comparative Example 2)

(132) Honeycomb fired bodies and a honeycomb filter were manufactured as in Comparative Example 1, except that the cells were plugged at positions shown in FIG. 11.

(133) As for the honeycomb fired bodies manufactured in Example 1 and Comparative Examples 1 and 2, the pressure loss at an early stage in the honeycomb fired bodies were measured using an initial pressure loss measuring device as shown in FIG. 5.

(134) (Measurement of Pressure Loss)

(135) FIG. 5 is an explanatory view schematically showing a pressure loss measuring device.

(136) A pressure loss measuring device 210 includes a blower 211, an exhaust gas pipe 212 connected to the blower 211, a metal casing 213 fixedly containing the honeycomb fired body 10 therein, and a manometer 214 whose tubes are arranged in such a manner to allow detection of the pressure of gas before and after flowing through the honeycomb fired body 10. Specifically, with the pressure loss measuring device 210, the pressure loss is measured by flowing gas through the honeycomb filter 10 and measuring the pressure of the gas before and after flowing through the honeycomb filter 10.

(137) The blower 211 was operated at a flow gas rate of 10 m.sup.3/h, and the pressure loss was measured.

(138) The initial pressure loss was 5.87 kPa in the honeycomb fired body according to Comparative Example 1, and was 4.02 kPa in the honeycomb fired body according to Comparative Example 2. In contrast, in the honeycomb fired body according to Example 1, the initial pressure loss was 3.66 kPa, indicating a lower initial pressure loss, although the aperture ratio of the honeycomb fired body according to Example 1 was lower by about 4.7% than that of the honeycomb fired bodies according to Comparative Examples 1 and 2.

(139) (Second Embodiment)

(140) The following will describe the honeycomb filter according to the second embodiment of the present invention.

(141) The honeycomb filter according to the second embodiment includes a honeycomb fired body including porous cell partition walls defining a plurality of cells that serve as channels of exhaust gas, exhaust gas introduction cells each having an open end at an exhaust gas inlet side and a plugged end at an exhaust gas outlet side, exhaust gas emission cells each having an open end at the exhaust gas outlet side and a plugged end at the exhaust gas inlet side, and an outer wall on the periphery thereof.

(142) In addition, the exhaust gas emission cells, except for the cells adjacent to the outer wall, are each adjacently surrounded fully by the exhaust gas introduction cells across the porous cell partition walls; the cells adjacent to the outer wall include the exhaust gas introduction cells and the exhaust gas emission cells; the cross-sectional area of each exhaust gas emission cell is larger than the cross-sectional area of each exhaust gas introduction cell; and provided that the hydraulic diameter is given by the following equation (1) and the area based on the given hydraulic diameter is given by the following equation (2), the ratio (S ratio) of the area based on the hydraulic diameter of an exhaust gas introduction cell to the cross-sectional area of the exhaust gas introduction cell is 0.95 to 0.98, and the ratio (S ratio) of the area based on the hydraulic diameter of an exhaust gas emission cell to the cross-sectional area of the exhaust gas emission cell is 0.7 to 0.9:
Hydraulic diameter=(4cross-sectional area of cell)/Cross-sectional peripheral length of cell(1),
Area based on the hydraulic diameter=(Hydraulic diameter/2).sup.2(2).

(143) Specifically, all the exhaust gas introduction cells of the present embodiment have a cross-sectional shape formed by rounding the corners of a pentagon, and the shape is entirely formed of curved lines. The S ratio is in the range of 0.95 to 0.98. In contrast, the cross-sectional shape of each exhaust gas emission cell is an octagon, and the S ratio is 0.895 which is in the range of 0.7 to 0.9.

(144) The cells adjacent to the outer wall include the exhaust gas introduction cells and the exhaust gas emission cells which are alternately arranged with each other.

(145) In addition, the cross-sectional shape of each exhaust gas introduction cell in a plane perpendicular to the longitudinal direction thereof is entirely uniform from the end at the exhaust gas inlet side to the end at the exhaust gas outlet side excluding the plugged portion; and the cross-sectional shape of each exhaust gas emission cell in a plane perpendicular to the longitudinal direction thereof is entirely uniform from the end at the exhaust gas inlet side to the end at the exhaust gas outlet side excluding the plugged portion.

(146) A substantial ratio of the number of the exhaust gas introduction cells to the number of the exhaust gas emission cells (exhaust gas introduction cells:exhaust gas emission cells) is 4:1. All the exhaust gas introduction cells, except for the cells adjacent to the outer wall, have the same cross-sectional area in a plane perpendicular to the longitudinal direction thereof, which is smaller than the cross-section area of each exhaust emission cell in a plane perpendicular to the longitudinal direction thereof.

(147) Specifically, the honeycomb filter according to the second embodiment is a honeycomb filter similar to the honeycomb filter according to the first embodiment, and the basic cell shapes and arrangement are the same as those in the honeycomb filter according to the first embodiment. However, the honeycomb filter according to the second embodiment is different from the honeycomb filter according to the first embodiment in that the cross-sectional shape of the exhaust gas emission cells is an octagon formed by chamfering the corners of a square linearly.

(148) FIG. 6(a) is a perspective view schematically showing an example of a honeycomb fired body constituting the honeycomb filter according to the second embodiment of the present invention. FIG. 6 (b) is a cross-sectional view of the honeycomb fired body shown in FIG. 6(a), taken along line B-B. FIG. 7 is an enlarged end face view in which a portion of an end face of the honeycomb fired body according to the second embodiment, which is shown in FIG. 6, is enlarged. The structure of the honeycomb filter is the same as that of the honeycomb filter 20, except that the shapes of the exhaust gas emission cells constituting the honeycomb fired body are as shown in FIG. 6(a) and FIG. 6(b). Thus, the drawing thereof is omitted.

(149) A honeycomb fired body 30 shown in FIG. 6(a) and FIG. 6(b) is basically the same as the honeycomb fired body 10 shown in FIG. 3(a) constituting the honeycomb filter 20, except that each exhaust gas emission cell 31 has an octagonal cross-sectional shape formed by chamfering the corners of a square. Each exhaust gas emission cell 31 having an octagonal cross section is adjacently surrounded fully, across porous cell partition walls 33, by eight exhaust gas introduction cells 32 each having a cross-sectional shape formed by rounding the corners of a pentagon. All the exhaust gas introduction cells 32, except for the cells adjacent to an outer wall 37, have the same shape which is formed by rounding the corners of a pentagon, and the shape is entirely formed of curved lines. Two exhaust gas introduction cells 32 adjacent to one side of the cross section of the exhaust gas emission cell 31 have cross-sectional shapes that face away from each other, and these cells are slightly sticking out from a side 31a of the exhaust gas emission cell 31. All the exhaust gas emission cells 31, except for the cells adjacent to the outer wall 37, also have the same shape.

(150) In the honeycomb filter of the second embodiment, the ratio of the number of the exhaust gas introduction cells 32 to the number of the exhaust gas emission cells 31 (exhaust gas introduction cells:exhaust gas emission cell) is 4:1. Thus, the number of the exhaust gas introduction cells 32 is four times that of the exhaust gas emission cells 31.

(151) The outer wall 37 is configured in the same manner as in the honeycomb filter 20 according to the first embodiment.

(152) In regard to the cells adjacent to the outer wall 37, exhaust gas introduction cells 32A and exhaust gas emission cells 31A are alternately arranged with each other. The exhaust gas introduction cells 32A are pentagonal, and the area of the rectangular portion of the pentagon of the gas introduction cells 32A is larger than that of the exhaust gas introduction cell 32 not adjacent to the outer wall 37. In contrast, the shape and the area of each exhaust gas emission cell 31A adjacent to the outer wall 37 are the same as those of each exhaust gas emission cell 31 not adjacent to the outer wall 37.

(153) The area of each exhaust gas emission cell 31A adjacent to the outer wall 37 is preferably 65 to 90%, more preferably 70 to 85%, of the area of each exhaust gas emission cell 31 other than the exhaust gas emission cells 31A adjacent to the outer wall 37.

(154) In addition, the area of each exhaust gas introduction cell 32A adjacent to the outer wall 37 is preferably 130 to 200%, more preferably 150 to 180%, of the area of each exhaust gas introduction cell 32 other than the exhaust gas introduction cells 32A adjacent to the outer wall 37.

(155) Exhaust gas emission cells 31B located at the corners of the honeycomb fired body 30 also have the same shape as other exhaust gas emission cells 31.

(156) In the honeycomb filter of the present embodiment, as described above, although the cross-sectional area of each exhaust gas introduction cell 32 is smaller than the cross-sectional area of each exhaust gas emission cell 31, the S ratio of the exhaust gas introduction cell is set to 0.95 to 0.98 to allow exhaust gas to easily flow through the exhaust gas introduction cells. Thus, the flow-through resistance (b) of the exhaust gas introduction cells can be reduced.

(157) In addition, the cross-sectional area of each exhaust gas emission cell 11 is larger than the cross-sectional area of each exhaust gas introduction cell 12. Thus, the effect of reducing the flow-through resistance (e) of the exhaust gas emission cells 311 and the outflow resistance (f) upon flowing of exhaust gas out of the honeycomb filter is high, and as a result, the pressure loss can be reduced as compared to the conventional honeycomb filter 90.

(158) Since the cross-sectional shape of each exhaust gas emission cell 31 is an octagon, the flow-through resistance (e) of the exhaust gas emission cells 31 and the outflow resistance (f) upon flowing of exhaust gas out of the honeycomb filter are further reduced, as compared to the honeycomb filter 20 according to the first embodiment.

(159) The cross section of the exhaust gas emission cell 31 is an octagon. This octagon is point-symmetric with respect to the centroid. Each hypotenuse side (indicated with 31b in FIG. 7) has the same length, and each vertical or horizontal side (indicated with 31a in FIG. 7) has the same length. In addition, four hypotenuse sides and four vertical or horizontal sides are alternately arranged with each other, and the angle formed between one hypotenuse side and one vertical or horizontal side is 135.

(160) The hypotenuse side generally refers to the longest side that is opposite to the right angle in a right-angled triangle; however, herein, for convenience of explanation, a side formed by chamfering a corner of a square is referred to as a hypotenuse side, and a side other than the hypotenuse side is referred to as a vertical or horizontal side.

(161) In the honeycomb filter of the present embodiment, at an early stage, a layer of accumulated PM is mainly formed on the cell partition walls 33 separating the exhaust gas introduction cell 32 and the exhaust gas emission cell 31 from each other, specifically on the cell partition walls 33 on the exhaust gas introduction cell 32 side. After a very short period of time, exhaust gas enters the cell partition walls 33 separating the exhaust gas introduction cells 32 from each other, and then passes through the cell partition walls 33 into the exhaust gas emission cells 31. Thus, PM gradually accumulates also on the cell partition walls 33 separating the exhaust gas introduction cells 32 from each other. As a result, PM accumulates substantially uniformly on the entire cell partition walls 33 defining the exhaust gas introduction cells 32. In the present invention, PM accumulates uniformly at an earlier stage, i.e., exhaust gas can easily pass through a greater number of cell partition walls 33 at an early stage. Thus, the initial pressure loss can be reduced.

(162) In addition, a substantial ratio of the number of the exhaust gas introduction cells 12 to the number of the exhaust gas emission cells 11 (exhaust gas introduction cells:exhaust gas emission cells) is 4:1, and the total volume of the exhaust gas introduction cells 12 can be made large. Thus, a substantial filtration area can be made sufficiently large. A layer of PM accumulated on the cell partition walls 33 defining the exhaust gas introduction cells 32 is thin, and the passage resistance (d) upon passage of exhaust gas through the layer of accumulated PM is kept low. As a result, the present invention can provide a honeycomb filter in which the pressure loss at an early stage is low and the pressure loss is less likely to increase even after accumulation of PM.

(163) Owing to the above-described configuration of the outer wall 37 and its adjacent exhaust gas emission cells 31 and exhaust gas introduction cells 32, the honeycomb filter 30 according to the present embodiment achieves the following effects in addition to the effects described above: the outer wall 37 increases the strength of the honeycomb fired body 30, further reduces local variations in the volume ratio between the exhaust gas emission cells 31 and the exhaust gas introduction cells 32 in the honeycomb fired body 30, and thus allows exhaust gas to flow more uniformly. Also, exhaust gas can smoothly flow into the exhaust gas introduction cells 32 even near the outer wall 37, and the cell partition walls 33 and the outer wall 37 can function as filters. As a result, the pressure loss can be further reduced.

(164) In the honeycomb filter of the present embodiment including the honeycomb fired body shown in FIG. 6(a) and FIG. 6 (b), the ratio (%) of the cross-sectional area of each exhaust gas introduction cell 32 relative to the cross-sectional area of each exhaust gas emission cell 31 is preferably 30 to 50%, more preferably 35 to 45%.

(165) In the honeycomb filter according to the second embodiment, preferably, the thickness of the cell partition walls of the honeycomb filter, the porosity of the cell partition walls, and the average pore diameter of the pores in the cell partition walls are the same as those of the honeycomb filter of the first embodiment.

(166) The honeycomb filter according to the second embodiment may include a plurality of honeycomb fired bodies or a single honeycomb fired body. The honeycomb fired body is preferably formed of the same material as that of the honeycomb fired body according to the first embodiment. The number of cells per unit area in the cross section of the honeycomb fired body 10 is also preferably the same as that of the honeycomb fired body according to the first embodiment.

(167) The honeycomb filter according to the first embodiment of the present invention may include a peripheral coat layer on the periphery thereof. The material of the peripheral coat layer is preferably the same as that of the adhesive.

(168) The thickness of the peripheral coat layer is preferably 0.1 to 3.0 mm.

(169) The honeycomb filter of the present embodiment can be manufactured by the same method described for the first embodiment of the present invention, except that a die of a different shape is used in the extrusion molding step.

(170) The honeycomb filter according to the present embodiment is the same as the honeycomb filter according to the first embodiment in terms of the basic arrangement of the cells, shape, plugging, and the like, and thus can achieve the same effects (1) to (8) described for the first embodiment. Further, since the cross-sectional shape of each exhaust gas emission cell 31 is an octagon, the flow-through resistance (e) of the exhaust gas emission cells and the outflow resistance (f) upon flowing of exhaust gas out of the honeycomb filter are further reduced, as compared to the honeycomb filter 20 according to the first embodiment.

REFERENCE SIGNS LIST

(171) 10, 30: Honeycomb fired body 20: Honeycomb filter 11, 11A, 11B, 31, 31A, 31B: Exhaust gas emission cell 11a, 11Aa, 31a, 31b: Side (side of the exhaust gas emission cell) 12, 12A, 32, 32A: Exhaust gas introduction cell 12a, 32a: Side (side of the exhaust gas introduction cell) 13, 13a, 13b, 13c, 33: Cell partition wall 15: Adhesive layer 16: Peripheral coat layer 17, 37: Outer wall 18: Ceramic block