U.S. patent application number 12/558975 was filed with the patent office on 2010-01-14 for asymmetric honeycomb wall-flow filter having improved structural strength.
Invention is credited to Douglas M. Beall, Rodney I. Frost, Weiguo Miao.
Application Number | 20100009024 12/558975 |
Document ID | / |
Family ID | 46302859 |
Filed Date | 2010-01-14 |
United States Patent
Application |
20100009024 |
Kind Code |
A1 |
Beall; Douglas M. ; et
al. |
January 14, 2010 |
Asymmetric Honeycomb Wall-Flow Filter Having Improved Structural
Strength
Abstract
A honeycomb filter includes an array of interconnecting porous
walls which define an array of first channels and second channels.
The first channels are bordered on their sides by the second
channels and have a larger hydraulic diameter than the second
channels. The first channels have a square cross-section, with
corners of the first channels having a shape, such as a bevel or
fillet, such that the thickness, t.sub.3, of the porous walls
adjoining the corners of the first channels is comparable to the
thickness, t.sub.4, of the porous walls adjoining edges of the
first and second channels. Embodiments having a corner fillet with
a radius, R.sub.c, are also disclosed. Embodiments wherein 0.30
t.sub.4.ltoreq.R.sub.c.ltoreq.1.0 t.sub.4 exhibit combinations of
low wall pressure drop and low thermal stress.
Inventors: |
Beall; Douglas M.; (Corning,
NY) ; Frost; Rodney I.; (Corning, NY) ; Miao;
Weiguo; (Corning, NY) |
Correspondence
Address: |
CORNING INCORPORATED
SP-TI-3-1
CORNING
NY
14831
US
|
Family ID: |
46302859 |
Appl. No.: |
12/558975 |
Filed: |
September 14, 2009 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
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11089642 |
Mar 24, 2005 |
7601194 |
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12558975 |
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10671166 |
Sep 25, 2003 |
7247184 |
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11089642 |
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Current U.S.
Class: |
425/462 |
Current CPC
Class: |
B01D 46/2474 20130101;
B01D 2046/2496 20130101; Y10S 55/30 20130101; Y10T 428/24149
20150115; B01D 46/2466 20130101; B28B 3/26 20130101; F01N 2330/30
20130101; B29L 2031/60 20130101; F01N 2340/00 20130101; C04B
38/0009 20130101; B01D 2046/2481 20130101; C04B 2111/00793
20130101; B29C 48/11 20190201; Y02T 10/12 20130101; B01J 35/04
20130101; B01D 46/2451 20130101; B28B 3/269 20130101; F01N 2330/48
20130101; B01D 46/247 20130101; F01N 2330/321 20130101; F01N 3/0222
20130101; C04B 38/0009 20130101; C04B 35/00 20130101; C04B 38/0003
20130101; C04B 38/0054 20130101 |
Class at
Publication: |
425/462 |
International
Class: |
B29C 47/12 20060101
B29C047/12 |
Claims
1.-16. (canceled)
17. An extrusion die assembly for making a honeycomb filter,
comprising: a cell forming die having a central region and a
peripheral region, the central region comprising an array of
discharge slots cut to define an array of first and second pins and
an array of first feedholes in communication with the array of
discharge slots, the peripheral region comprising at least a second
feedhole, the first pins having a larger cross-sectional area than
the second pins, a cross-sectional shape of the first pins selected
such that the width of the discharge slots is substantially
uniform; and a skin forming mask mounted coaxially with the cell
forming die and radially spaced from the cell forming die so as to
define a skin slot that is in selective communication with the at
least second feedhole.
18. The extrusion die assembly of claim 17, wherein the
cross-sectional shape of the first pins includes a square having
filleted corners.
19. The extrusion die assembly of claim 17, wherein the
cross-sectional shape of the first pins includes a square having
beveled corners.
20. The extrusion die assembly of claim 17, further comprising a
reservoir defined between the cell forming die and the skin forming
mask, the reservoir being in communication with the at least second
feedhole and the skin slot.
21. The extrusion die assembly of claim 17, wherein a volume of the
outer skin reservoir is adjustable to control rate of flow of batch
material to the skin slot.
Description
RELATED INVENTIONS
[0001] The present application is a continuation-in-part
application of U.S. patent application Ser. No. 10/671,166 filed
Sep. 25, 2003, entitled "Asymmetric Honeycomb Wall-Flow Filter
Having Improved Structural Strength."
BACKGROUND OF INVENTION
[0002] Honeycomb wall-flow filters are used to remove carbonaceous
soot from exhaust of diesel engines. FIG. 1A shows a conventional
honeycomb wall-flow filter 100 having an inlet end 102, an outlet
end 104, and an array of interconnecting porous walls 106 extending
longitudinally from the inlet end 102 to the outlet end 104. The
interconnecting porous walls 106 define a grid of inlet channels
108 and outlet channels 110. At the inlet end 102, the outlet
channels 110 are end-plugged with filler material 112 while inlet
channels 108 are not end-plugged. Although not visible from the
figure, at the outlet end 104, the inlet channels 108 are
end-plugged with filler material while the outlet channels 110 are
not end-plugged. Each inlet channel 108 is bordered on all sides by
outlet channels 110 and vice versa. FIG. 1B shows a close-up view
of the cell structure used in the honeycomb filter. The porous
walls 106 defining the inlet and outlet channels (or cells) 108,
110 are straight, and the inlet and outlet cells 108, 110 have a
square cross-section and equal hydraulic diameter.
[0003] Returning to FIG. 1A, diesel exhaust flows into the
honeycomb filter 100 through the unplugged ends of the inlet
channels 108 and exits the honeycomb filter through the unplugged
ends of the outlet channels 110. Inside the honeycomb filter 100,
the diesel exhaust is forced from the inlet channels 108 into the
outlet channels 110 through the porous walls 106. As diesel exhaust
flows through the honeycomb filter 100, soot and ash particles
accumulate on the porous walls 106, decreasing the effective flow
area of the inlet channels 108. The decreased effective flow area
creates a pressure drop across the honeycomb filter, which leads to
a gradual rise in back pressure against the diesel engine. When the
pressure drop becomes unacceptable, thermal regeneration is used to
remove the soot particles trapped in the honeycomb filter. The ash
particles, which include metal oxide impurities, additives from
lubrication oils, sulfates and the like, are not combustible and
cannot be removed by thermal regeneration. During thermal
regeneration, excessive temperature spikes can occur, which can
thermally shock, crack, or even melt, the honeycomb filter.
[0004] It is desirable that the honeycomb filter has sufficient
structural strength to withstand thermal regeneration and canning.
To avoid the need for frequent thermal regeneration, it is also
desirable that the honeycomb filter has a high capacity for storing
soot and ash particles. For a cell structure in which the inlet and
outlet channels have equal hydraulic diameter, the effective flow
area of the inlet channels can easily become much smaller than that
of the outlet channels, creating a large pressure drop across the
honeycomb filter. One solution that has been proposed to reducing
this pressure drop involves making the hydraulic diameter (or
effective cross-sectional flow area) of the inlet channels larger
than that of the outlet channels. In this way, more soot and ash
particles may accumulate on the inlet portion of the porous walls,
i.e., the storage capacity is better and the pressure drop over
time is reduced.
[0005] For the conventional honeycomb cell structure shown in FIG.
1B, the hydraulic diameter of the inlet cells 108 can be made
larger than the outlet cells 110 by reducing the hydraulic diameter
of the outlet cells 110. FIG. 1C shows the honeycomb cell structure
of FIG. 1B after reducing the hydraulic diameter of the outlet cell
110 such that the outlet cell 110 now has a smaller hydraulic
diameter in comparison to the inlet cell 108. Another modification
that can be made is to increase the hydraulic diameter of the inlet
cells 108. This modification has the advantage of increasing the
effective surface area available for collecting soot and ash
particles in the inlet portion of the honeycomb filter, which
ultimately increases the overall storage capacity of the honeycomb
filter. FIG. 1D shows the honeycomb cell structure of FIG. 1C after
increasing the hydraulic diameter of the inlet cell 108. Without
changing the cell density of the honeycomb filter, any increase in
the hydraulic diameter of the inlet cell 108 would produce a
corresponding decrease in the thickness of the wall between the
adjacent corners of inlet cells 108 (compare t.sub.2 in FIG. 1D
with t.sub.1 in FIG. 1C). As the wall between the corners of the
inlet cells become thinner, the structural strength of the
honeycomb filter decreases, making the honeycomb filter more
susceptible to thermal shock and cracking during thermal
regeneration.
[0006] From the foregoing, there is desired a method of improving
the storage capacity of the honeycomb filter while maintaining good
flow rates through the honeycomb filter without significantly
reducing the structural strength of the honeycomb filter.
SUMMARY OF INVENTION
[0007] In one aspect, the invention relates to a honeycomb filter
which comprises an array of interconnecting porous walls that
define an array of first channels and second channels. The first
channels are bordered on their sides by the second channels and
have a larger hydraulic diameter than the second channels. The
first channels have a square cross-section, with corners of the
first channels having a shape such that the thickness of the porous
walls adjoining corners of the first channels is comparable to the
thickness of the porous walls adjoining edges of the first and the
second channels. Preferably, the first channels are end-plugged at
a first end of the honeycomb filter and the second channels are
end-plugged at a second end of the honeycomb filter so that flow
into the first channels pass through the porous walls and then out
of the honeycomb filter through the second channels.
[0008] According to a preferred aspect, the thickness, t.sub.3, of
the porous walls adjoining the corners of the first channels are
between 0.8 and 1.2 times the thickness, t.sub.4, of the porous
walls adjoining the edges of the first and the second channels. The
shapes of the corners of the larger hydraulic first channels
preferably include either fillets or bevels. Fillets are most
preferred as they provide the lowest combinations of wall pressure
loss and thermal stress.
[0009] According to another preferred aspect of the invention, the
corners of the larger first channels include fillets with a corner
radius, R.sub.c, selected such that R.sub.c.gtoreq.0.30 t.sub.4.
Additionally, the ratio of the hydraulic areas of the first (Inlet)
channels to the hydraulic areas of the second (Exit) channels, the
I/E ratio, is between 1.1 and 2.0, and in preferred embodiments
less than 1.5; with more preferred embodiments being between 1.1
and 1.5; and most preferably between 1.2 and 1.4.
[0010] Embodiments having an I/E ratio, defined as a width
dimension of the first channels divided by a width dimension of the
second channels, above 1.5 and wherein the corner fillet radius is
selected such that R.sub.c.gtoreq.0.50 t.sub.4 have lower pressure
drop for comparable thermal mass as compared to beveled corner
designs.
[0011] According to another yet aspect of the invention, the
corners of the first larger channels include fillets with a corner
radius, R.sub.c, having the relationship wherein R.sub.c.ltoreq.1.0
t.sub.4. Achieving this relationship ensures that the thermal
stresses in the ceramic article are not too large.
[0012] According to a further aspect of the invention, the corners
of the first larger channels preferably include fillets including a
radius, R.sub.c, wherein 0.30 t.sub.4.ltoreq.R.sub.c.ltoreq.1.0
t.sub.4. It was discovered that achieving this range of fillet
corner radius lowers pressure drop and also limits thermal stresses
in the article. More preferably, the fillet includes a radius,
R.sub.c, wherein 0.50 T.sub.4.ltoreq.R.sub.c.ltoreq.1.0
t.sub.4.
[0013] According to yet another aspect of the invention, a
honeycomb filter is provided which comprises an array of
interconnecting porous walls defining an array of first channels
and second channels, the first channels being bordered on their
sides by the second channels and having a larger hydraulic diameter
than the second channels wherein a ratio of the hydraulic diameter
of the first channels to the hydraulic diameter of the second
channels is between 1.1 to 1.5, the first channels have a square
cross-section, with corners having a fillet with a corner radius,
R.sub.c, such that a thickness (t.sub.3) of the porous walls
adjoining corners of the first channels is in a range of about 0.8
to 1.2 times the thickness (t.sub.4) of the porous walls adjoining
edges of the first and the second channels, and wherein the corner
radius, R.sub.c, is selected such that 0.30
t.sub.4.ltoreq.R.sub.c.ltoreq.1.0 t.sub.4.
[0014] In another aspect, the invention relates to a honeycomb
filter which comprises an array of interconnecting porous walls
that define an array of first channels having a square
cross-section and second channels having a square cross-section.
The first channels are bordered on their edges by the second
channels. The edges of the first channels are aligned with edges of
the bordering second channels. The first channels have a larger
hydraulic diameter than the second channels.
[0015] In yet another aspect, the invention relates to an extrusion
die assembly for making a honeycomb filter which comprises a cell
forming die having a central region and a peripheral region. The
central region comprises an array of discharge slots cut to define
an array of first and second pins and an array of first feedholes
in communication with the array of discharge slots. The peripheral
region comprises at least a second feedhole. The first pins have a
larger cross-sectional area than the second pins. The
cross-sectional shape of the first pins is selected such that the
width of the discharge slots is substantially uniform. The
extrusion die assembly also includes a skin forming mask mounted
coaxially with the cell forming die and radially spaced from the
cell forming die so as to define a skin slot that is in selective
communication with the at least second feedhole.
[0016] Other features and advantages of the invention will be
apparent from the following description and the appended
claims.
BRIEF DESCRIPTION OF DRAWINGS
[0017] FIG. 1A is a perspective view of a prior-art honeycomb
wall-flow filter.
[0018] FIG. 1B shows a standard honeycomb cell structure having
inlet and outlet cells with equal hydraulic diameter.
[0019] FIG. 1C shows the honeycomb cell structure of FIG. 1B after
reducing the hydraulic diameter of the outlet cells.
[0020] FIG. 1D shows the honeycomb cell structure of FIG. 1C after
increasing the hydraulic diameter of the inlet cells.
[0021] FIG. 2A is a perspective view of a honeycomb wall-flow
filter according to an embodiment of the invention.
[0022] FIG. 2B shows a honeycomb cell structure having inlet cells
and outlet cells with unequal hydraulic diameters and the inlet
cells with filleted corners according to one embodiment of the
invention.
[0023] FIG. 2C shows a honeycomb cell structure having inlet cells
and outlet cells with unequal hydraulic diameters and the inlet
cells with beveled corners according to another embodiment of the
invention.
[0024] FIG. 2D shows a honeycomb cell structure having inlet and
outlet cells with unequal hydraulic diameters and aligned edges
according to another embodiment of the invention.
[0025] FIG. 2E is a graph of hydraulic diameter of a cell as a
function of fillet radius and cell width.
[0026] FIG. 3 is a cross-section of an extrusion die assembly
according to one embodiment of the invention.
[0027] FIG. 4 is a graph of wall pressure drop vs. inlet/exit
dimension ratio (I/E ratio) according to embodiments of the
invention.
[0028] FIGS. 5-6 are graphs of thermal stress vs. wall pressure
drop according to embodiments of the invention.
[0029] FIGS. 7-8 are 3-D graphs of wall pressure drop, mechanical
displacement, and thermal stress according to embodiments of the
invention.
DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS
[0030] The invention will now be described in detail with reference
to a few preferred embodiments, as illustrated in the accompanying
drawings. In the following description, numerous specific details
are set forth in order to provide a thorough understanding of the
invention. It will be apparent, however, to one skilled in the art
that the invention may be practiced without some or all of these
specific details. In other instances, well-known features and/or
process steps have not been described in detail in order to not
unnecessarily obscure the invention. The features and advantages of
the invention may be better understood with reference to the
drawings and discussions that follow.
[0031] For illustration purposes, FIG. 2A shows a honeycomb
wall-flow filter 200 according to an embodiment of the invention.
The honeycomb filter 200 has a columnar body 202 whose
cross-sectional shape is defined by a skin (or peripheral wall)
204. The profile of the skin 204 is typically circular or
elliptical, but the invention is not limited to any particular skin
profile. The columnar body 202 has an array of interconnecting
porous walls 206, which intersect with the skin 204. The porous
walls 206 define a grid of inlet channels 208 and outlet channels
210 in the columnar body 202. The inlet and outlet channels 208,
210 extend longitudinally along the length of the columnar body
202. Typically, the columnar body 202 is made by extrusion.
Typically, the columnar body 202 is made of a ceramic material,
such as cordierite, aluminum titanate, or silicon carbide, but
could also be made of other extrudable materials, such as glass,
glass-ceramics, plastic, and metal.
[0032] The honeycomb filter 200 has an inlet end 212 for receiving
flow, e.g., exhaust gas flow, and an outlet end 214 through which
filtered flow can exit the honeycomb filter. At the inlet end 212,
end portions of the outlet channels 210 are plugged with filler
material 216 while the end portions of the inlet channels 208 are
not plugged. Typically, the filler material 216 is made of a
ceramic material, such as cordierite, aluminum titanate, or silicon
carbide. Although not visible from the figure, at the outlet end
214, end portions of inlet channels 208 are plugged with filler
material while the end portions of the outlet channels 210 are not
plugged. Partial cells near the periphery of the skin 204 are
typically plugged with filler material. Inside the honeycomb filter
200, the interconnected porous walls 206 allow flow from the inlet
channels 208 into the outlet channels 210. The porosity of the
porous walls 206 can be variable. In general, the porosity should
be such that the structural integrity of the honeycomb filter is
not compromised. For diesel filtration, the porous walls 206 may
incorporate pores having mean diameters in the range of 1 to 60
.mu.m, more preferably in a range from 10 to 50 .mu.m.
[0033] FIG. 2B shows a close-up view of the cell structure of the
honeycomb filter 200. Each inlet cell 208 is bordered by outlet
cells 210 and vice versa. To maintain good flow rates when the
honeycomb filter 200 is in use, the inlet cells 208 are made to
have a larger hydraulic diameter than the outlet cells 210. In the
illustration, the outlet cells 210 have a square geometry. In the
illustration, the inlet cells 208 also have a square geometry, but
the corners of the square include fillets 218. One purpose of the
fillets 218 is to make the thickness (t.sub.3) between the adjacent
corners of the inlet cells 208 comparable to the thickness
(t.sub.4) between the inlet cells 208 and the outlet cells 210. In
one embodiment, the thickness (t.sub.3) between the corners is in a
range of about 0.8 to 1.2 times the thickness (t.sub.4) of the wall
portion between the inlet and outlet cells. Preferably, the radius
of the fillets 218 is selected such that the thickness of the
porous walls is substantially uniform around the cells. The radius
of the fillets 218 may also be selected such that hydraulic
diameter of the inlet cells 208 is maximized for a selected cell
density and closed frontal area.
[0034] Table 1 below shows examples of cell structures having a
cell density of 200 cells/in.sup.2 (about 31 cells/cm.sup.2) and a
closed frontal area of 47%. Cell structures A and B are specific
examples of the inventive cell structure shown in FIG. 2B. Cell
structures C and D are specific examples of the prior-art cell
structure shown in FIG. 1C.
TABLE-US-00001 TABLE 1 Ratio of inlet cell hydraulic Thickness
diameter between Inlet cell to Inlet Outlet adjacent hydraulic
outlet cell cell cell Fillet corners of Cell diameter hydraulic
width width radius inlet cells Structure (mm) diameter (mm) (mm)
(mm) (mm) A 1.68 1.7 1.59 0.98 0.30 0.54 B 1.73 2.0 1.64 0.88 0.30
0.47 C 1.59 1.7 1.59 0.93 None 0.28 D 1.64 2.0 1.64 0.83 None
0.22
Hydraulic diameter, D.sub.H, of a cell is defined as follows:
D H = 4 A P ( 1 ) ##EQU00001##
where A is the cross-sectional area of the cell and P is the wetted
perimeter of the cell. For a square cell, the hydraulic diameter is
the width of the cell. For a square cell with filleted corners, the
hydraulic diameter is larger than the width of the cell.
[0035] From Table 1 above, the hydraulic diameters of the inlet
cells of the inventive cell structures A and B are larger than the
hydraulic diameters of the inlet cells of the prior-art cell
structures C and D, respectively. The larger hydraulic diameters of
the cell structures A and B are achieved while maintaining the same
cell density and closed frontal area as that of the prior-art cell
structures C and D. FIG. 2E shows how hydraulic diameter varies as
a function of fillet radius for a given cell width. The position of
the cell structures A, B, C, and D are indicated on the graph. The
graph shows that hydraulic diameter has a non-linear relationship
with fillet radius. In practice, the inlet cells can be made to
have the fillet radius corresponding to the maximum hydraulic
diameter achievable for a selected cell width.
[0036] Returning to FIG. 2B, the present invention is not limited
to inclusion of fillets 218 at the corners of the inlet cells 208.
The corners of the inlet cells 208 could be beveled, for example.
FIG. 2C shows a cell structure where the corners of the inlet cells
208 include bevels 220. In this embodiment, the inlet cells 208
have also been enlarged such that the edges of (diagonally)
adjacent inlet cells 208 are substantially aligned. This increases
the overall storage capacity of the honeycomb filter while allowing
good flow rates through the honeycomb filter to be maintained. The
bevels 220 (or fillets if used instead of bevels) enable uniformly
thick porous walls 206 to be provided around the cells. For the
cell structures shown in FIGS. 2B and 2C, and particularly in FIG.
2C, the porous walls 206 are not straight. This leads to an
increase in the thermal shock resistance of the honeycomb
structure. In the design shown in FIG. 2C, portions of the porous
walls, e.g., porous wall 206a, are common to only the inlet cells
208. These porous wall portions that are common to only the inlet
cells 208 could facilitate transfer of heat from one inlet cell to
another during thermal regeneration.
[0037] The fillets and bevels can be used to achieve a
substantially uniform porous wall thickness throughout the
honeycomb filter while maintaining a desired closed frontal area,
cell density, and ratio of hydraulic diameter of inlet cell to
outlet cell. Typically, a ratio of hydraulic diameter of inlet cell
to outlet cell in a range from 1.1 to 2.0, more preferably 1.3 to
2.0. For diesel particulate filtration, a honeycomb having cell
density in a range from 10 to 300 cells/in.sup.2 (about 1.5 to 46.5
cells/cm.sup.2), more typically in a range from 100 to 300
cells/in.sup.2 (about 15.5 to 31 cells/cm.sup.2), is considered
useful to provide sufficient thin wall surface area in a compact
structure. The thickness of the interconnecting porous walls can
vary upwards from the minimum dimension of about 0.002 in. (0.05
mm) providing structural integrity, but is generally less than
about 0.060 in (1.5 mm) to minimize filter volume. A porous wall
thickness in a range of about 0.010 to 0.030 in. (about 0.25 to
0.76 mm), preferably in a range from about 0.010 to 0.025 in.
(about 0.25 to 0.64 mm), is most often selected at the preferred
cell densities.
[0038] According to further aspects of the invention, is has been
discovered that corner fillets are more preferable over corner
bevels within certain desirable ranges of inlet-to-exit cell
dimension ratios (I/E ratios). For example, it has been discovered
that in order to reduce the principle mechanical stress in the
ceramic article, it is preferred that the corners of the inlet
cells 208 include a radius. For a particular design having a wall
thickness, t.sub.4, of about 0.0165 inch, it has been found that a
corner radii of greater than 0.005 inch provides a significant
reduction in stress as compared to designs including no corner
fillets in the inlet cells (See Table 2 below). Larger radii
designs also reduce stress as compared to non-filleted designs.
Designs including a range of radii from 0.005-0.020 inch have also
been calculated to improve the stress as compared to non-filleted
designs. Thus, for mechanical stress reasons alone, the corner
radius for such a design should be 0.005 inch or larger. More
particularly, the corner fillet radius, R.sub.c, as a function of
the wall thickness, t.sub.4, should be selected such that:
R.sub.c.gtoreq.0.30t.sub.4.
TABLE-US-00002 TABLE 2 Maximum Principle Stress versus Corner
Radius Corner Radius (inch) No 0.005 inch 0.010 inch 0.015 inch
0.020 inch Fillet Fillet Fillet Fillet Fillet Max Stress (MPa) 7.2
2.79 3.35 3.95 3.5
[0039] Additionally, it has been discovered that by increasing the
corner fillet radius, R.sub.c, the wall pressure drop (in kPa)
through the porous walls 206 can desirably be made lower. All
calculations for thermal stress, and wall pressure drop disclosed
herein in FIGS. 4-8 are at 210 CFM for a ceramic article having a
5.66 inch diameter, a 6.0 inch overall length, and a cell density
of 270 cells/inch. FIG. 4, for example, demonstrates that for
larger corner radii, R.sub.c, the wall pressure drop reduces across
the entire range of I/E ratios (approx. 1.2-1.6). I/E ratio, as
used herein, is defined as the ratio of the inlet cell width
dimension divided by the exit cell width dimension. For
square-shaped designs described herein, the width is simply the
width of the square. For irregularly shaped cell designs, i.e.,
ones for which a representative width of the inlet and exit cells
is difficult to determine, the ratio of the hydraulic diameters of
the respective inlet and exit cells provides a good estimate of the
I/E ratio. In particular, the lines labeled 420-428 compare designs
having no fillets with designs with various corner fillets. For
example, line 420 is representative of designs that have no corner
fillet for various I/E ratios; line 422 represents a family of
designs with a 0.005 inch fillet radius; line 424 represents
embodiments with a 0.010 inch fillet radius, line 426 embodiments
have a 0.015 inch fillet radius, and line 428 embodiments include a
0.020 inch fillet radius. An I/E ratio above 1.6 is not desired as
such designs may incur an overall pressure drop penalty. Designs
having area I/E ratios equal to or less than 1.5 are most
preferred, with I/E ratios of between 1.2 and 1.4 being even more
preferred. Therefore, looking at wall pressure drop alone, it
should be recognized that it is most desirable to have larger
corner radii, R.sub.c. Larger corner radii results in thinner walls
and, therefore, lower wall pressure drop. Thus, similar to the
analysis above for mechanical stress, for wall pressure drop
reasons, it is most desirable that for I/E ratios of less than 1.5,
that the corner radius, R.sub.c, be selected such that:
R.sub.c.gtoreq.0.30t.sub.4.
If the I/E ratio is above 1.5, then the corner radius, R.sub.c,
should follow the relationship:
R.sub.c.gtoreq.0.50t.sub.4.
This relationship is believed to result in a wall pressure drop
that will be better than a beveled design of the same thermal mass.
Thus, it should be recognized that, as shown in FIG. 4, for a
corner radii, R.sub.c, of 0.005 inch and an I/E ratio of 1.5 or
less, the calculated wall pressure drop of this radiused design is
less than for a comparable beveled design with the same thermal
mass (labeled as 430). It should also be recognized from FIG. 4,
that as the corner radius becomes larger (e.g., for a 0.010 inch
corner fillet radius, R.sub.c), the improvement as compared to a
beveled corner design is evidenced for all articles having an I/E
ratio of 1.6 and below. For example, for comparable filleted and
beveled corner designs at an I/E ratio of about 1.3, it can be seen
that an approximately 12% reduction in calculated wall pressure
drop is achieved for the filleted corner design having a corner
radius of 0.005 inch as compared to the beveled corner design of
comparable thermal mass. Thus, it has been discovered that certain
filleted corner designs unexpectedly offer an advantage of lower
wall pressure drop as compared to beveled designs for certain
desired ranges of I/E ratio. Accordingly, fillet corners are more
preferred as compared to beveled corners.
[0040] The inventors herein have further discovered that, as the
corner radius, R.sub.c, becomes larger, penalties due to higher
thermal stress in the article become a dominant design
consideration (See FIGS. 5-8). For example, FIGS. 5 and 7
illustrate plots of thermal stress (MPa) versus wall pressure drop
(KPa) for designs including various fillet corner radii each having
an I/E ratio of 1.3. For example, the point labeled 20 refers to an
unfilleted design (R.sub.c=0.00 inch); point 22 refers to a design
with a 0.005 inch corner radius; point 24 has a 0.010 inch radius;
point 26 has a 0.015 inch radius; and point 28 has an 0.020 inch
radius. Thus, it should be apparent that although a larger radii is
desired for mechanical stress and wall pressure drop reasons, for
thermal stress reasons, the corner fillet radius should be
minimized to some extent. Thus, there are competing design criteria
concerning the corner radius. In particular, the corner radius for
this design should be preferably less than 0.015 inch as shown by
FIG. 5 as above that size radius, thermal stresses increase
dramatically and at a high rate. Further limiting the corner radius
to preferably less than about 0.012 inch thereby limits thermal
stresses in the ceramic article to be approximately equal to or
less than the beveled design (labeled 30) of equivalent thermal
mass. Thus, it should be recognized that for designs having I/E
ratios of about 1.3, it is desirable, in order to limit thermal
stresses, that the following relationship is followed:
R.sub.c.ltoreq.1.0t.sub.4.
[0041] FIGS. 6 and 8 illustrate plots of thermal stress (MPa)
versus pressure drop (KPa) in the same way as FIGS. 5 and 7, except
that these designs all have an I/E ratio of 1.6. As shown therein,
point 20 refers to an unfilleted design; point 22 refers to a
design with a 0.005 inch corner radius, R.sub.c; point 24 is design
with a 0.010 inch radius; point 26 refers to a design with a 0.015
inch radius; and point 28 is a design with a 0.020 inch radius. A
comparable thermal mass beveled design is labeled 30. Thus, it
should be recognized that for designs having I/E ratios of about
1.6, it is also desirable, in order to limit thermal stresses, to
design the corner radius, R.sub.c, such that:
R.sub.c.ltoreq.1.0t.sub.4,
and in order to have thermal stress equal to or lower than an
equivalent thermal mass beveled design with lower wall pressure
drop than comparable beveled designs, then it is desired that:
0.50T.sub.4.ltoreq.R.sub.c.ltoreq.1.0t.sub.4.
[0042] Thus, it has been discovered that for designs having an I/E
ratio of between 1.2 to 1.6, fillets are most desired. Designs
having corner fillet radiuses following the relationship:
0.30t.sub.4.ltoreq.R.sub.c.ltoreq.1.0t.sub.4,
are most desired because they exhibit low pressure drop and low
thermal stress as well as low principle stress. Even more preferred
designs include filleted corners with the following the
relationship:
0.50t.sub.4.ltoreq.R.sub.c.ltoreq.0.75t.sub.4.
This range takes advantage of the lower pressure drops achievable,
while limiting the thermal stresses produced within the article in
use. Most preferably, I/E ratios are desired to be between 1.2 and
1.5. As should be seen from FIG. 5, for designs having I/E ratio of
about 1.3, a minima (at point 24) is included in the plot of stress
versus pressure drop. This plot illustrates that designs having
filleted corners with 0.30 t.sub.4.ltoreq.R.sub.c.ltoreq.1.0
t.sub.4 have combinations of low wall pressure drop and low thermal
stress. Further, FIGS. 5-6 demonstrate that for I/E ratios of
between about 1.3 and 1.6, certain filleted designs are generally
preferable over designs having beveled corners in that they have
combinations of lower wall pressure drop and comparable or lower
thermal stresses.
[0043] FIG. 2D shows another cell structure where the edges of the
inlet cells 208 are aligned with edges of the outlet cells 210 and
the thickness of the porous walls 206 is uniform throughout the
honeycomb filter without the use of a bevel or fillet at the
corners of the inlet cells 208. However, a fillet or bevel to the
corners of the inlet cells 208 can further improve the structural
strength of the honeycomb filter. The porous walls 206 in this
embodiment are even less straight than the porous walls in the
embodiments previously described, leading to further improvement in
thermal shock resistance.
[0044] Honeycomb extrusion dies suitable for the manufacture of the
honeycomb filter described above would have pin arrays including
pins of alternating size. The corners of alternating pins could be
rounded or beveled. For illustration purposes, FIG. 3 shows a
vertical cross-section of an extrusion die assembly 300. The
extrusion die assembly 300 includes a cell forming die 302 and a
skin forming mask 304. The cell forming die 300 is used to form the
interconnecting porous walls that define the inlet and outlet cells
of the honeycomb filter. The cell forming die 302 cooperate with
the skin forming mask 304 to define the shape and thickness of the
skin of the honeycomb filter. The cell forming die 302 has a
central region 306. An array of discharge slots 308 is cut in the
central region 306 to define an array of inlet and outlet pins 310,
312. In one embodiment, the transverse cross-section of the inlet
and outlet pins 310, 312 is square, with each corner of the inlet
pins 310 including a fillet or bevel.
[0045] The central region 306 of the cell forming die 302 further
includes an array of central feedholes 314, which extend from the
inlet face 315 of the die to the array of discharge slots 308. The
central feedholes 314 supply batch material to the discharge slots
308. The size and location of the central feedholes 314 relative to
the discharge slots 308 are selected to achieve a desired flow rate
through the discharge slots 308. As an example, a central feedhole
308 may correspond to each or every other discharge slot 308 or may
correspond to each or every other intersection of the discharge
slots 308.
[0046] The cell forming die 302 also includes a peripheral region
316 formed contiguous with the central region 306. The peripheral
region 316 provides a mounting surface 318 for the skin forming
mask 304 and includes feedholes 318 for feeding batch material to
spaces around the cell forming die 302. In one embodiment, a shim
320 is interposed between the mounting surface 318 and the skin
forming mask 304 to define a skin forming reservoir 322 between the
peripheral region 316 and the skin forming mask 304. The feedholes
318 in the peripheral region 316 supply batch material to the skin
forming reservoir 322. The skin forming mask 304 is radially spaced
from the central region 306 to define a skin slot 324, which is in
communication with the skin forming reservoir 322. Batch material
is extruded through the skin slot 324 to form the skin of the
honeycomb filter. The volume of the reservoir 322 can be adjusted
to control the rate at which batch material is supplied into the
skin slot 324.
[0047] In operation, batch material is fed into the feedholes 314,
318 in the cell forming die 302 and extruded through the discharge
slots 308 and the skin forming slot 324. The volume of the batch
material in the skin forming reservoir 322 is dependent on the
extent of the radial overhang of the skin forming mask 304 over the
skin forming reservoir 322. The rate of flow of batch material into
the skin forming slot determines the character of the skin, while
the rate of flow of batch material into the discharge slots
determine the character of the porous walls.
[0048] The extrusion die assembly described above can be
manufactured using existing methods for making extrusion dies. The
cell forming die may be made by machining holes in a lower portion
of a block that is made of a machinable material. These holes would
serve as feedholes. A process such as plunge electrical discharge
machining can be used to cut the discharge slots in the upper
portion of the block. Pins remain on the upper portion of the block
after the slots are cut. The pins at the periphery of the block can
be shortened or completely removed to provide a mounting surface
for the skin forming mask. The discharge slots could have any of
the geometries described above in conjunction with the cell
structure of the honeycomb filter.
[0049] While the invention has been described with respect to a
limited number of embodiments, those skilled in the art, having
benefit of this disclosure, will appreciate that other embodiments
can be devised which do not depart from the scope of the invention
as disclosed herein. Accordingly, the scope of the invention should
be limited only by the attached claims.
* * * * *