Honeycomb ceramic substrates, honeycomb extrusion dies, and methods of making honeycomb ceramic substrates
09808794 · 2017-11-07
Assignee
Inventors
- Thomas William Brew (Corning, NY)
- Jeffrey O Foster (Horseheads, NY)
- Steven John Kremer (Big Flats, NY)
- Bryan Michael Miller (Addison, NY)
Cpc classification
C04B35/00
CHEMISTRY; METALLURGY
B28B3/269
PERFORMING OPERATIONS; TRANSPORTING
C04B35/00
CHEMISTRY; METALLURGY
B29C48/11
PERFORMING OPERATIONS; TRANSPORTING
B01D46/2486
PERFORMING OPERATIONS; TRANSPORTING
B01D46/2498
PERFORMING OPERATIONS; TRANSPORTING
C04B38/0009
CHEMISTRY; METALLURGY
B01D46/2474
PERFORMING OPERATIONS; TRANSPORTING
B29C48/345
PERFORMING OPERATIONS; TRANSPORTING
C04B38/0009
CHEMISTRY; METALLURGY
International classification
B01D39/06
PERFORMING OPERATIONS; TRANSPORTING
B01D39/14
PERFORMING OPERATIONS; TRANSPORTING
B01D39/20
PERFORMING OPERATIONS; TRANSPORTING
C04B38/00
CHEMISTRY; METALLURGY
B01D46/24
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A honeycomb ceramic substrate, a method of making thereof, and a honeycomb extrusion die configured to extrude a honeycomb ceramic substrate from a batch of ceramic or ceramic-forming material is provided. The substrate may include a lattice of intersecting walls defining a honeycomb network of flow channels extending between an inlet end and an outlet end of the honeycomb substrate. Each flow channel may be defined by a plurality of channel walls of the intersecting walls with at least two of the plurality of channel walls including concave inner surfaces facing a center of the corresponding flow channel from central portions of the concave inner surfaces to concave corner portions facing the center of the corresponding flow channel.
Claims
1. A honeycomb ceramic substrate, comprising: a lattice of intersecting walls defining a honeycomb network of flow channels extending between an inlet end and an outlet end of the honeycomb substrate, wherein a first flow channel is defined by a plurality of channel walls of the intersecting walls with at least two of the plurality of channel walls including concave inner surfaces facing a center of the first flow channel, the concave inner surfaces extending from central portions of each of the concave inner surfaces to concave corner portions facing the center of the first flow channel, the concave corner portions located on either end of each concave inner surface, the concave corner portions being where each of the plurality of channel walls intersects with another one of the plurality of channel walls wherein the concave inner surfaces of the channel walls are continuously curved towards the center throughout a length of the channel walls between corresponding ones of the corner portions, a second flow channel adjacent to the first flow channel and sharing a common channel wall, wherein one side of the common channel wall comprises a concave inner surface of the concave inner surfaces and an opposing side the common channel wall includes an opposing concave inner surface facing a center of the second flow channel.
2. The honeycomb ceramic substrate of claim 1, wherein a peripheral cross-sectional shape of at least one of the flow channels is substantially defined by the equation:
3. The honeycomb ceramic substrate of claim 2, wherein at least one of n and m is in a range of from about 2.5 to about 10.
4. The honeycomb ceramic substrate of claim 2, wherein a and b are independently in a range of from about 330 microns to about 1.829 mm.
5. The honeycomb ceramic substrate of claim 2, wherein n and m are varied across the plurality of flow channels.
6. The honeycomb ceramic substrate of claim 1, wherein the channel walls are continuously curving around the center of the corresponding flow channel.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) The above and other features, aspects and advantages of the present disclosure are better understood when the following detailed description of the disclosure is read with reference to the accompanying drawings, in which:
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DETAILED DESCRIPTION
(19) The disclosure will now be described more fully hereinafter with reference to the accompanying drawings in which example embodiments are shown. Whenever possible, the same reference numerals are used throughout the drawings to refer to the same or like parts. However, the disclosure may be embodied in many different forms and should not be construed as limited to the embodiments set forth herein. These example embodiments are provided so that this disclosure will be both thorough and complete.
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(22) The honeycomb ceramic substrate 102 can have a variety of cell densities, such that a larger or smaller number of flow channels 108 can be provided per unit area. For instance, the channel density can be in the range of from about 7.75 channels/cm.sup.2 (50 channels/in.sup.2) to about 232.5 channels/cm.sup.2 (1500 channels/in.sup.2) of the honeycomb ceramic substrate 102 cross-section. As such, the examples shown in
(23) In further examples, the channel wall constructions forming the flow channels 108 can have different configurations.
(24) In the examples shown in
(25) As mentioned above, the flow channels 108 of the honeycomb ceramic substrate 102 may be a superellipse, also known as a Lame curve, generally elliptical or even square-like or rectangular-like with concave channel walls and concave corner portions in order to obtain an optimized flow channel shape for an open frontal area (OFA) and a geometric surface area (GSA) of the flow channels 108. By controlling the length of the channel walls 110 and a degree of curvature of the channel walls 110 and corner portions 118, various desired flow channel shapes may be obtained. For example, a peripheral cross-sectional shape of at least one of the flow channels 108 may be substantially defined by Equation (I).
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(27) As is illustrated in
(28) In an example, at least one of n and m may be in a range of from about 2.5 to about 10. In another example, a and b may be independently in a range of from about 330 microns (0.013 inches) to about 1.829 mm (0.072 inches). In a further example, a thickness of the plurality of channel walls 110 between adjacent ones of the flow channels 108 may be in a range of from about 25.4 microns (0.001 inches) to about 482.6 microns (0.019 inches).
(29) In yet another example, the channel walls 110 in each flow channel 108 may have substantially identical lengths. In further examples, at least two of the channel walls 110 in each flow channel 108 may have a length that is the same. Additionally, the channel walls 110 of each flow channel 108 may be symmetric to each other.
(30) Equation (I) results in a flow channel 108 having gently curved inner surfaces 116 with more pronounced curved corners 118. Even with corners 118 that have a more pronounced curvature than the gently curved inner surfaces 116, each of the channel walls 110 of the flow channels 108 are continuously curved toward a center 125 of the corresponding flow channel 108 throughout the length of the channel wall between corresponding concave corner portions. In further examples, the entire inner surface of the flow channel is continuously concave about the entire periphery of the flow channel, wherein the inner surface is defined by gently concave channel walls 110 and more pronounced concave corner portions 118 that seamlessly transition with one another about the inner periphery of the inner surface of the flow channels.
(31) The exponents n and m of Equation (I) are tuned, depending on the flow channel density and a thickness of the channel walls 110 between adjacent flow channels, to meet the above-referenced attributes in order to minimize coating buildup in the corner portions 118 and maximize open frontal area. The examples illustrated in
(32) For example,
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(35) The concavity of the inner surfaces 116 may compensate for some of the open area of the flow channel 108 that is lost due to the curved flow channel shape. Flow channel density and the thickness of the channel walls 110 between adjacent flow channels 108 may additionally be selected to optimize flow channel shape for a desired GSA. Further, the concavity of the inner surfaces 116 may provide the flow channels 108 with increased strength and resistance to buckling and rotational failures by increasing a moment of inertia, or decreasing a slenderness ratio, of each of the channel walls 110. This increased strength may afford reduced thicknesses of the channel walls 110 between adjacent flow channels 108, thereby further optimizing open frontal area and reduction of weight of the honeycomb ceramic substrate 102.
(36) In an example, Table 1 compares square flow channels in a honeycomb ceramic substrate having a channel density of 93 channels/cm.sup.2 (600 channels/in.sup.2) with elliptical flow channels in a honeycomb ceramic substrate having n and m equal to 3.5 with a channel density of 93 channels/cm.sup.2 (600 channels/in.sup.2).
(37) TABLE-US-00001 TABLE 1 Flow Channel Density 93 channels/cm 93 channels/cm (600 channels/in.sup.2) (600 channels/in.sup.2) Square n and m = 3.5 Channel Wall Thickness 76.2 microns 76.2 microns Between Flow Channels (0.003 inches) (0.003 inches) Equivalent Fillet Radius of 76.2 microns 254 microns Channel Walls (0.003 inches) (0.01 inches) MIF (uncoated) 0.69 1.24
(38) While an equivalent fillet radius of the channel walls is greater in the elliptical flow channel than in the square flow channel, a mechanical integrity factor (MIF) of the elliptical flow channel is greater than an MIF of the square flow channel. The MIF, represented by Equation (II) below, is a dimensionless structural property that is directly proportional to a load carrying capability parallel to the channel walls and along a diagonal of the flow channel, where “t” is the channel wall thickness between flow channels, “l” is the distance between channel wall centers, and “R” is the effective corner radius, as is illustrated in
MIF*100=t/1*(t/(1−t−2*R))*100 (II)
(39) Further, the equivalent fillet radius of the channel walls is defined by the group of equations listed below in Table 2, where “a”, “b”, and “c” represent the three sides of a triangle, “A” is the area of the triangle, and “r” is the equivalent fillet radius of the channel walls.
(40) TABLE-US-00002 TABLE 2 a = sqrt((x1 − x2).sup.2 + (y1 − y2).sup.2) b = sqrt((x2 − x3).sup.2 + (y2 − y3).sup.2) a = sqrt((x3 − x1).sup.2 + (y3 − y1).sup.2) s = (a + b + c)/2 A = sqrt(s * (s − a) * (s − b) * (s − c)) r = a * b * c/(4 * A)
(41) Table 3 compares other strength advantages of elliptical flow channels over square flow channels based on other product variants. For example, a slenderness ratio is used to compare the strength of the channel walls. Smaller slenderness ratios are more resistant to failures at equivalent loadings. Additionally to be noted is the fact that the channel wall thickness between the elliptical flow channels is less than the channel wall thickness between the square flow channels. When the square and elliptical flow channels having equivalent flow channel densities are compared, the elliptical flow channel having a thinner channel wall has a lower slenderness ratio than the comparable square flow channel having a thicker channel wall. In other words, the elliptical flow channel designs have the lower slenderness ratios, which indicates a higher resistance to buckling loading. Buckling failure is often seen in the extrusion of substrates having thin channel walls when adjacent channel wall velocities are not uniform. Buckling failure is one of the principle reasons for rejected extruded ware.
(42) TABLE-US-00003 TABLE 3 Flow Channel 93 (600) 93 (600) 69.75 (450) 62 (400) 62 (400) 139.5 (900) 139.5 (900) Density - channels/cm.sup.2 (channels/in.sup.2) Channel Wall 88.9 57.15 57.15 88.9 106.68 68.58 57.15 Thickness (0.0035) (0.00225) (0.00225) (0.0035) (0.0042) (0.0027) (0.00225) Between Flow Channels - microns (inches) Flow Channel Square Elliptical Elliptical Square Square Square Elliptical Shape Distance 1.036 1.036 1.197 1.270 1.270 0.847 0.847 Between (0.0408) (0.0408) (0.04714) (0.05) (0.05) (0.03333) (0.03333) Channel Wall Centers - mm (inches) Radius of 269.2 342.9 403.9 315.0 327.7 215.9 241.3 Gyration X - (0.0106) (0.0135) (0.0159) (0.0124) (0.0129) (0.0085) (0.0095) microns (inches) Slenderness 1.92 1.51 1.48 2.02 1.94 1.96 1.75 Ratio
(43) The Slenderness Ratio is the quotient of the distance between the channel wall centers, the radius of gyration around the x-axis, and 2. The Slenderness Ratio is applied to determine the critical buckling stress 6 between the channel wall centers, as is shown in Equation (III) below.
σ=π.sup.2E/(Slenderness Ratio) (III)
(44) where E is the Young's modulus of the channel wall material.
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(49) In addition, Table 4 highlights several performance attributes of an elliptical flow channel having a channel density of 69.75 channels/cm.sup.2 (450 channels/in.sup.2), a channel wall thickness between flow channels of 63.5 microns (0.0025 inches), and m and n values equal to 3.6 in comparison with alternative hexagonal and square flow channels. Of note, the elliptical flow channel substantially matches the hexagonal flow channel's exhaust performance characteristics while providing close to 40% increased strength over the hexagonal flow channel.
(50) TABLE-US-00004 TABLE 4 Elliptical, Flow Channel Shape Hexagonal Square n and m = 3.6 Flow Channel Density - 93 (600) 93 (600) 69.75 (450) channels/cm.sup.2 (channels/in.sup.2) Channel Wall Thickness 76.2 (0.003) 76.2 (0.003) 63.5 (0.0025) Between Flow Channels - microns (inches) Equivalent Fillet 76.2 (0.003) 76.2 (0.003) 304.8 (0.012) Radius of Channel Walls - microns (inches) OFA (coated) 0.84 0.78 0.84 GSA (coated) 31.6 35.3 31.3 MIF (uncoated) 0.46 0.69 0.64 Resistance to Flow 491 709 452 (RTF) (coated)
(51) The OFA, the GSA, and RTF are calculated as is provided in Equations (IV), (V), and (VI) below, respectively. The OFA is used to compare substrates for back pressure. The GSA is used to compare substrates for conversion efficiency. For example, a higher GSA translates into a higher conversion efficiency or capability for the substrate. The RTF is a measure of the resistance to flow through the channels.
OFA=(1−t/L).sup.2−(4−π)(R/L).sup.2 (IV) where “t” is the channel wall thickness between flow channels, “L” is the distance between channel wall centers, and “R” is the effective corner radius, as is illustrated in
GSA=(4(L−t)/L.sup.2)−(((8−2π)R)/L.sup.2) (V) where “t” is the channel wall thickness between flow channels, “L” is the distance between channel wall centers, and “R” is the effective corner radius, as is illustrated in
RTF=2f/((OFA*Dh.sup.2)w) (VI) where “f” is the fanning friction factor, “Dh” is the hydraulic diameter of the flow channel, and “w” is the width
(52) Table 5 highlights further variants of the elliptical flow channel concept. As Table 5 shows, the elliptical flow channel is designed to allow thinner channel wall thicknesses while maintaining equivalent product strength and improving OFA and GSA on a 900 channel/inch substrate.
(53) TABLE-US-00005 TABLE 5 Flow Channel Shape Square Elliptical Flow Channel Density - 139.5 (900) 139.5 (900) channels/cm.sup.2 (channels/in.sup.2) Channel Wall Thickness 68.58 (0.0027) 57.15 (0.00225) Between Flow Channels - microns (inches) Equivalent Fillet 50.8 (0.002) 124.46 (0.0049) Radius of Channel Walls - microns (inches) OFA (coated) 84.2 86 GSA (coated) 43.3 43.8 MIF (uncoated) 0.74 0.72 RTF (coated) 867 857
(54) Equation (I) may also be translated into x and y coordinates to yield Equation (VII) and Equation (VIII), respectively.
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(57) Referring to
(58) As shown, in one example, the extruding device 406 can include a twin-screw extruder including twin screws 410a, 410b configured to be rotated by respective motors 412a, 412b to mix and compress the batch 402 of ceramic or ceramic-forming batch material as it travels along a path 414 toward the honeycomb extrusion die 408. The extruding device 406 includes an extrusion axis wherein the ceramic-forming substrate can be extruded from the honeycomb extrusion die 408 along an extrusion direction substantially parallel to the extrusion axis.
(59) As shown in
(60) At least one wall slot 422 may be defined between facing sides (e.g., 505a/505c, 505b/505d, 505c/505a, 505d/505b) of two adjacent die pins of the plurality of die pins 420. As shown, each of the facing sides may be convex facing each other from central portions thereof to corresponding end portions of the facing sides. Consequently, the wall slot 422 defined therebetween, may be concave toward central portions of the two adjacent die pins.
(61) For example, with reference to the die pin shown in
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(63) As is somewhat inversely illustrated in
(64) In an example, at least one of n and m may be in a range of from about 2.5 to about 10. In another example, a and b may be independently in a range of from about 330 microns (0.013 inches) to about 1.829 mm (0.072 inches). In a further example, the die pins 420 may be arranged in the matrix and spaced from one another to have a die pin density in a range of from about 7.75 die pins/cm.sup.2 (50 die pins/in.sup.2) to about 232.5 die pins/cm.sup.2 (1500 die pins/in.sup.2). In an additional example, a thickness of the intersecting slots 422 between adjacent ones of the die pins 420 may be in a range of from about 25.4 microns (0.001 inches) to about 482.6 microns (0.019 inches).
(65) In yet another example, the sides of each of the die pins 420 may have a length that is the same. Further, at least two of the sides of each of the die pins 420 may have a length that is the same. In still another example, the sides of each of the die pins 420 may be symmetric to each other. In addition, the sides and corner portions of each of the die pins 420 may be continuously curved around the center of the corresponding die pin 420.
(66) In addition, the shape of the die pin 420 either may be the same or varied along an entire length of the die pin 420. For example, the shape of the die pin 420 on the outer face 503 may extend a depth of 127 microns (0.005 inches) from the outer face 503 along the length of the die pin 420, with the remaining length of the die pin 420 being formed in a different shape. In another example, the shape of die pin 420 on the outer face 503 may extend a depth of 30% to 50% of the length of the die pin 420 from the outer face 503 along the length of the die pin 420 while the remaining length of the die pin 420 is formed in a different shape. For instance, in one example, the die pins may be formed by Electrical Discharge Machining (EDM) wire machining the entire length of the die pin. After forming the initial die pin shape, a subsequent machining step may be carried out by plunge EDM machining an electrode having the desired shape of the die pin at the outer face of the die pin. In such examples, the plunge EDM may extend a depth of 127 microns (0.005 inches) and/or to a depth of from about 30% to about 50% of the length of the die pin. As such, the shape of the die pin at the outer face may comprise the shape of the electrode while the remaining shape is defined by the initial wire EDM machining procedure.
(67) Turning back to
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(69) Referring to
(70) It will be apparent to those skilled in the art that various modifications and variations can be made to the present disclosure without departing from the spirit and scope of the disclosure. Thus, it is intended that the present disclosure cover the modifications and variations of this disclosure provided they come within the scope of the appended claims and their equivalents.