WO2004011386A1 - Aluminum titanate-based ceramic article - Google Patents

Aluminum titanate-based ceramic article Download PDF

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Publication number
WO2004011386A1
WO2004011386A1 PCT/US2003/022008 US0322008W WO2004011386A1 WO 2004011386 A1 WO2004011386 A1 WO 2004011386A1 US 0322008 W US0322008 W US 0322008W WO 2004011386 A1 WO2004011386 A1 WO 2004011386A1
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WO
WIPO (PCT)
Prior art keywords
tio
ceramic article
diesel particulate
particulate filter
2sio
Prior art date
Application number
PCT/US2003/022008
Other languages
French (fr)
Inventor
George H. Beall
Steven B. Ogunwumi
Dell J. St. Julien
Patrick D. Tepesch
Christopher J. Warren
Isabelle M. Melscoet
Original Assignee
Corning Incorporated
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Corning Incorporated filed Critical Corning Incorporated
Priority to EP03771615.6A priority Critical patent/EP1558545B1/en
Priority to JP2004524607A priority patent/JP4750415B2/en
Priority to AU2003249236A priority patent/AU2003249236A1/en
Publication of WO2004011386A1 publication Critical patent/WO2004011386A1/en
Priority to ZA2005/00853A priority patent/ZA200500853B/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/92Chemical or biological purification of waste gases of engine exhaust gases
    • B01D53/94Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
    • B01D53/944Simultaneously removing carbon monoxide, hydrocarbons or carbon making use of oxidation catalysts
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    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/01Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics
    • C04B35/46Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on titanium oxides or titanates
    • C04B35/462Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on titanium oxides or titanates based on titanates
    • C04B35/478Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on titanium oxides or titanates based on titanates based on aluminium titanates
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Definitions

  • the instant invention relates to aluminum titanate-based ceramic articles for use in high temperature applications. Specifically the invention relates to aluminum titanate-based ceramic articles having high permeability in combination with low thermal expansion and high thermal shock resistance, and being suitable for automotive emissions control.
  • cordierite 2MgO-2Al 2 O 3 -5SiO 2
  • cordierite filters are susceptible to damage and have even catastrophically failed. Occasional thermal runaway occurs during uncontrolled regenerations resulting in localized cordierite melting.
  • SiC wall-flow filters have been made commercially available for diesel exhaust filtration.
  • SiC filters are costly to manufacture, and must be segmented due to an inherent high coefficient of thermal expansion (CTE) and poor thermal shock resistance.
  • the present invention provides such a ceramic material, and a method of making and using the same.
  • the instant invention is founded upon the discovery of aluminum titanate-based ceramic articles of high, interconnected porosity and large median pore size, further combining high permeability, and being capable of employment in high temperature applications, such as automotive emissions control, including but not limited to automotive catalytic converters, and diesel exhaust aftertreatment systems, such as diesel particulate filters.
  • Phases of aluminum titanate (Al 2 O 3 -TiO 2 ), strontium feldspar (SrO-Al 2 O 3 -2SiO 2 ), mullite (3Al 2 O 3 -2SiO 2 ), alumina (Al 2 O 3 ), and/or glass have been observed by x-ray diffraction, and electron-probe micro-analysis in the inventive ceramic. These phases are not required to be perfectly stoichiometric, or crystalline in the final product.
  • Silica and glass additions improve strength, decrease porosity, lower thermal expansion and firing temperature, and may provide resistance of the ceramic against decomposition.
  • Alumina additions increase porosity.
  • silica additions of up to 10% by weight (based on total batch weight) and alumina additions of up to 50% by weight may be made.
  • Glass having a composition represented by LlSrO-1.5Al 2 O 3 -13.6SiO 2 -TiO 2 may be added in an amount of up to 50% by weight.
  • Iron titanate and/or magnesium titanate may be substituted for up to 30% by weight of the aluminum titanate phase. These substitutions improve the resistance to decomposition of the aluminum titanate phase at temperatures between 800°-1200°C.
  • Li another aspect of the invention the inventive ceramic article exhibits a coefficient of thermal expansion (CTE), as measured from room temperature to 800°-1000°C of less than 45xl0 "7 /°C, preferably less than 25xlO "7 /°C, and more preferably less than 5x10 " 7 /°C; a porosity of up to 60% by volume, preferably up to 55% by volume, and more preferably up to 45% by volume; and, a median pore size up to 25 micrometers, preferably up to 20 micrometers, and more preferably up to 15 micrometers; and, a modulus of rapture, as measured on a solid rod of circular cross section of greater than 400 pounds per square inch (psi), preferably greater than 700 psi.
  • CTE coefficient of thermal expansion
  • an aluminum titanate-based ceramic body comprising: (a) formulating a batch of inorganic raw materials comprising sources of silica, alumina, strontium, titania, and/or iron oxide together with organic processing comprising plasticizers, lubricants, binders, and water as solvent, and mixing to form a homogeneous and plasticized mixture; (b) shaping the plasticized mixture into a green body; (c) heating the green body at 20-40°C/hr over various temperature intervals with hold temperature and times between 1100°-1650°C, preferably 1100°-1500°C for a period of 30-50 hours to develop a fired aluminum-titanate body.
  • substantially low sintering temperatures of between 1100°-1650°C, preferably 1100°-1500°C significantly reduce manufacturing costs, while maintaining low thermal expansion, high thermal shock resistance and high mechanical strength in the inventive ceramic.
  • a diesel particulate filter comprising the inventive ceramic.
  • the diesel particulate filter is comprised of a plugged, wall-flow honeycomb body having an inlet end and an outlet end and a multiplicity of cells extending from the inlet end to the outlet end, the cells having porous walls, wherein part of the total number of cells at the inlet end are plugged along a portion of their lengths, and the remaining part of cells that are open at the inlet end are plugged at the outlet end along a portion of their lengths, so that an engine exhaust stream passing through the cells of the honeycomb from the inlet end to the outlet end flows into the open cells, through the cell walls, and out of the structure through the open cells at the outlet end.
  • the diesel particulate filter comprises a honeycomb body composed of an aluminum titanate-based ceramic according to the present invention having a composition comprising u (Al 2 O 3 -TiO 2 ) + v (R) + w (3Al 2 O 3 -2SiO 2 ) + x (Al 2 O 3 ) + y (SiO 2 ) + z ( lSrO-1.5Al 2 O 3 -13.6SiO 2 -TiO 2 ) + a (Fe 2 O 3 -TiO 2 ) + b (MgO-2TiO 2 ), where, R is SrO-Al 2 O 3 -2SiO 2 or 11.2SrO-10.9Al 2 O 3 -24.1SiO 2 -TiO 2 , where u, v, w, x, y, z, a andb are weight fractions of each component such that (u+v+w+x+y+z+
  • the diesel particulate filter exhibits the following properties: a CTE (RT to 800°-1000°C) of less than 15xlO "7 /°C, preferably less than 5x10 " 7 /°C; a porosity of 30% to 50%, preferably 35% to 45% by volume; a median pore size of 5 to 20 micrometers, preferably 10 to 15 micrometers; and, a modulus of rupture, as measured by the four-point method on a cellular bar cut parallel to the direction of the channels from a honeycomb body having a cell density of 200 cells per square inch (cpsi) and 0.016 inch thick walls, of 150 to 400 psi, preferably 150 to 300 psi; a permeability of at least 0.20 x 10 "12 ⁇ j 19 9 m , preferably 0.33 to 1.00 x 10 " m ; and, a pressure drop of 5 kPa or less at an artificial carbon soot loading of up to 5 g/L
  • FIG. 1 is a graphical representation of thermal expansion as a function of
  • compositions where u 0.7(Al 2 O 3 -TiO 2 ), with the remainder being (SrO-Al 2 O 3 -2SiO 2 ); the compositions were fired at 1500°C for 4 hours;
  • FIG. 2 is a graphical representation of porosity as a function of 0 ⁇ w ⁇ 0.30(3Al 2 O 3 -
  • compositions were fired at 1500°C for 4 hours;
  • FIG. 3 is comparison of the thermal expansion (CTE)(10 "7 /°C), porosity (% volume), and median pore size (MPS) (micrometers) as a function of 0 ⁇ z ⁇ 0.30(l.lSrO-
  • FIG. 4 is a graphical representation of pressure drop value between the inlet end and outlet end (i.e., pressure drop difference) in KPa as a function of soot loading (g/L) at a gas flow rate of 210 scfm, for a diesel particulate filter comprising the inventive ceramic having a composition as provided in Example 5 of Table 1, in a sample having dimensions of 5.66 inch x 6 inch, a cell geometry of 273 cells per square inch (cpsi) with a cell wall thickness of 0.015 inch.
  • the inventive ceramic is highly refractory with a low coefficient of thermal expansion (CTE), and increased thermal durability, making it suitable for high temperature applications, including but not limited to automotive emissions control systems. Accordingly, the thermal expansion (coefficient of thermal expansion) as measured by dilatometry over a temperature range from room temperature room temperature (RT) to 800° -1000°C, is less than 45xlO "7 /°C, preferably less than 25xl0 "7 /°C, and more preferably less than 5x10 " /°C.
  • the low expansion of the inventive structure is a result of microcracking generated by anisotropic thermal expansion.
  • an advantage of the present inventive structure is that the thermal expansion hysteresis (i.e., the difference between heating and cooling curves) can be made very low. This ensures a high thermal shock resistance.
  • w ranges between 0.05-0.15.
  • the inventive ceramic is particularly suitable to high interconnected porosity and large median pore size.
  • the porosity as measured by mercury porosimetry is up to 60% by volume, preferably up to 55% by volume, and more preferably up to 45% by volume.
  • the median pore size is up to 25 micrometers, preferably up to 20 micrometers, and more preferably up to 15 micrometers.
  • FIG. 3 therein provided is a comparison of the thermal expansion (CTE)(10 " /°C), porosity (% volume), and median pore size (MPS) (micrometers) as a function of 0 ⁇ z ⁇ 0.30(l.lSrO-1.5Al 2 O 3 -13.6SiO 2 -TiO 2 ) represented on the y-axis and 0 ⁇ v ⁇ 0.30(11.2SrO-10.9Al 2 O 3 -24.1SiO 2 -TiO 2 ) represented on the x-axis.
  • CTE thermal expansion
  • MPS median pore size
  • the CTE, porosity and MPS can be controlled in inventive ceramic bodies for desired applications.
  • the inventive ceramic bodies exhibit a high modulus of rupture, as measured on a solid rod of circular cross section of greater than 400 pounds per square inch (psi), preferably greater than 700 psi.
  • a diesel particulate filter comprises a plugged, wall-flow filter body composed of the inventive ceramic having a composition preferably comprising u (Al 2 O 3 - TiO 2 ) + v (R) + w (3Al 2 O 3 -2SiO 2 ) + x (Al 2 O 3 ) + y (SiO 2 ) + z (LlSrO-1.5Al 2 O 3 -13.6SiO 2 - TiO 2 ) + a (Fe 2 O 3 -TiO 2 ) + b (MgO-2TiO 2 ), where, R is SrO-Al 2 O 3 -2SiO 2 or 11.2SrO- 10.9Al 2 O 3 -24.1SiO 2 -TiO 2 , where u, v, w, x, y, z, a and b are weight fractions of each component such that (
  • the honeycomb filter body has an inlet end and an outlet end and a multiplicity of cells extending from the inlet end to the outlet end, the cells having porous walls. Part of the total number of cells at the inlet end are plugged along a portion of their lengths, and the remaining part of cells that are open at the inlet end are plugged at the outlet end along a portion of their lengths.
  • This plugging configuration allows for engine exhaust stream passing through the cells of the honeycomb from the inlet end to the outlet end to flow into the open cells, through the cell walls, and out of the structure through the open cells at the outlet end.
  • Suitable cellular densities for diesel particulate filters range from 70 cells/in 2 (10.9 cells/cm 2 ) to 800 cells/in 2 (124 cells/cm 2 ).
  • a diesel particulate filter according to the present invention exhibits a CTE (RT to 800°-1000°C) of less than 15xl0 "7 /°C, preferably less than 5xlO "7 /°C; a porosity of 30% to 50%, preferably 35% to 45% by volume; a median pore size of 5 to 20 micrometers, preferably 10 to 15 micrometers; and, a modulus of rupture, as measured by the four-point method on a cellular bar cut parallel to the direction of the channels from a honeycomb body having a cell density of 200 cpsi and 0.016 inch thick walls, of 150 to 400 psi, preferably 150 to 300 psi; a permeability of at least 0.20 x 10 "12 m 2 , preferably 0.33 to 1
  • the invention also relates to a method of fabricating the inventive aluminum titanate-based ceramic for forming a mixture from certain inorganic powdered raw materials which include sources of silica, alumina, strontium, titania, and/or iron oxide.
  • the raw materials are blended with together with organic processing aids that may include plasticizers, lubricants, binder, and water as solvent.
  • the mixture is then shaped into a green body, optionally dried, and fired to form the product structure.
  • a pore former such as graphite or polyethylene beads, may be optionally used to improve the porosity and median pore size.
  • a pore former is a fugitive particulate material which evaporates or undergoes vaporization by combustion during drying or heating of the green body to obtain a desired, usually higher porosity and/or coarser median pore diameter. Large particle sizes in the raw materials are not preferred.
  • An alumina source is a powder which when heated to a sufficiently high temperature in the absence of other raw materials, yield substantially pure aluminum oxide, and includes alpha-alumina, a transition alumina such as gamma-alumina or rho-alumina, hydrated alumina, gibbsite, boehmite, aluminum hydroxide, and mixtures thereof.
  • the particle size of the alumina source is up to 25 micrometers.
  • a silica source includes cristobalite, non-crystalline silica such as fused silica or sol-gel silica, silicone resin, zeolite, and diatomaceous silica, kaolin, and quartz.
  • the median particle size of the silica source is up to 30 micrometers.
  • a titania source is preferably, but not limited to, rutile.
  • the median particle size of the titania source is important to avoid entrapment of unreacted oxide by the rapidly growing nuclei in the structure. Accordingly, the median particle size is up to 20 micrometers.
  • a strontium source is strontium carbonate, with a median particle size is up to 20 micrometers.
  • Iron oxide source has a median particle size of up to 0.5 micrometers.
  • the inorganic powdered raw materials are mixed with organic processing components, such as methylcellulose binder, oleic acid/triethanol amine surfactant, to form a plasticized and homogeneous mixture.
  • the plasticized mixture is shaped by any conventional means, preferably by extrusion through a honeycomb die.
  • the resulting green bodies are optionally dried, and then heated at 20-40°C/hr over various temperature intervals with hold temperature and times between 1100°-1650°C, preferably 1100°-1500°C for a period of 30-50 hours to develop the final product structure.
  • a portion of the cells of the honeycomb structure at the inlet end or face are plugged, as known in the art.
  • the plugging is only at the ends of the cells which is typically to a depth of about 1 to 20 mm, although this can vary.
  • a portion of the cells on the outlet end but not corresponding to those on the inlet end are plugged. Therefore, each cell is plugged only at one end.
  • the preferred arrangement is to have every other cell on a given face plugged in a checkered pattern.
  • Inventive samples are prepared by weighing out the dry ingredients, mixing them with organic components and water, and kneading the mixture in a stainless steel muller to form a plastic mass.
  • Table I provides parts and proportions for the powdered raw materials and forming aids.
  • triethanolamine (TEA) is first mixed with water, and then with oleic acid and/or tall oil (dispersant). The resulting solution is stored at room temperature for 24 hours and then refrigerated overnight prior to use.
  • the dry ingredients which include silica, titania, strontium carbonate, iron oxide, alumina, alumina hydroxide, silicone resin, graphite, polyethylene beads and/or methyl cellulose binder are dry mixed in a muller.
  • the tall oil/TEA/water solution is slowly added during continuous mixing to provide homogenization and plasticization.
  • the plasticized mixture is extruded through a die into honeycomb bodies having approximately 100 to 400 cpsi and a wall thickness of about 0.010 to 0.025 inch.
  • the bodies thus formed are cut to desired lengths, and heated in an oven at 85°C until dry.
  • the samples are fired in an electric furnace at rates ranging from 20°C/hr-40°C/hr over various temperature intervals with a first hold temperature at 1200°C for 4 hours, and a second hold temperature at 1500°C for 6 hours to develop the final product structure, and cooled by shutting off power to the furnace.
  • an extruded honeycomb body comprising Example 5 ceramic is end- plugged at the inlet and outlet ends with a cold-set paste made of aluminum titanate powder.
  • Dimensions of the sample include a diameter of 5.66 inches, and a length of 6 inches, a cell geometry of 273 cpsi and a cell wall thickness of 0.015 inch walls.
  • the back pressure is tested by loading the sample with artificial soot (similar to copier toner) at a flow rate of 210 scfm, for loadings ranging up to 5 g/L, and measuring the pressure drop between the inlet end and the outlet end in kPa.
  • the resulting data is graphically provided in FIG.
  • the present invention provides an aluminum titanate-based ceramic having low thermal expansion, and increased thermal durability, with applicability in automotive emissions control system, and in particular in diesel exhaust filtration where low pressure drop and low back pressure against the engine are required.
  • the inventive ceramic can be formed with these desired properties at substantially low sintering temperatures of between 1100°C-1650°C, preferably 1100°C-1500°C, significantly reducing costs associated with manufacturing thereof.

Abstract

An aluminum titanate-based ceramic article having a composition comprising u (Al2O3-TiO2) + v (R) + w (3Al2O3-2SiO2) + x (Al2O3) + y (SiO2) + z (1.1SrO-1.5Al2O3-13.6SiO2-TiO2) + a (Fe2O3-TiO2) + b (MgO-2TiO2), where, R is SrO-Al2O3-2SiO2 or 11.2SrO-10.9Al2O3-24.1SiO2-TiO2, where u, v, w, x, y, z, a and b are weight fractions of each component such that (u+v+w+x+y+z+a+b=1), and 0.5 <u≤ 0.95, 0.01 <v≤ 0.5, 0.01 <w≤ 0.5, 0 <x≤ 0.5, 0 <y≤ 0.1, 0 <z≤ 0.5, 0 <a≤ 0.3, and 0 <b≤ 0.3. A method of forming the ceramic article is provided. The ceramic article is useful in automotive emissions control systems, such as diesel exhaust filtration.

Description

ALUMINUM TITANATE-BASED CERAMIC ARTICLE
BACKGROUND OF THE INVENTION
[0001] The instant invention relates to aluminum titanate-based ceramic articles for use in high temperature applications. Specifically the invention relates to aluminum titanate-based ceramic articles having high permeability in combination with low thermal expansion and high thermal shock resistance, and being suitable for automotive emissions control. [0002] In the industry cordierite (2MgO-2Al2O3-5SiO2) has been the cost-effective material of choice for automotive emissions control applications, such diesel exhaust aftertreatment systems, due to its combination of good thermal shock resistance, filtration efficiency, and durability under most operating conditions. However, under certain circumstances cordierite filters are susceptible to damage and have even catastrophically failed. Occasional thermal runaway occurs during uncontrolled regenerations resulting in localized cordierite melting.
[0003] Another factor contributing to cordierite failure occurs when metal impurities from the engine oil, catalytic additives or corroded metal from the exhaust port liners are introduced into the filter during operation. Typically, at temperatures exceeding 1300°C, these metals form oxides which react with the cordierite structure. Evidence of the failed material are usually small holes on the filter where the metal initially deposits and reacts causing corrosion and melting of the material.
[0004] Recently, silicon carbide (SiC) wall-flow filters have been made commercially available for diesel exhaust filtration. However, SiC filters are costly to manufacture, and must be segmented due to an inherent high coefficient of thermal expansion (CTE) and poor thermal shock resistance.
[0005] A need therefore exists for a ceramic article suitable for high temperature applications, such as automotive emissions control systems without the shortfalls of currently existing materials. The present invention provides such a ceramic material, and a method of making and using the same. SUMMARY OF THE INVENTION
[0006] The instant invention is founded upon the discovery of aluminum titanate-based ceramic articles of high, interconnected porosity and large median pore size, further combining high permeability, and being capable of employment in high temperature applications, such as automotive emissions control, including but not limited to automotive catalytic converters, and diesel exhaust aftertreatment systems, such as diesel particulate filters.
[0007] In one aspect of the invention there is provided a ceramic article having a composition comprising u (Al2O3-TiO2) + v (R) + w (3 Al2O3-2SiO2) + x (Al2O3) + y (SiO2) + z (l.lSrO-1.5Al2O3-13.6SiO2-TiO2) + a (Fe2O3-TiO2) + b (MgO-2TiO2), where, R is SrO- Al2O3-2SiO2 or 11.2SrO-10.9Al2O3-24.1SiO2-TiO2, where u, v, w, x, y, z, a and b are weight fractions of each component such that (u+v+w+x+y+z+a+b=l), and 0.5 <u< 0.95, 0.01 <v< 0.5, 0.01 <w< 0.5, 0 <x< 0.5, 0 <y< 0.1, 0 <z< 0.5, 0 <a< 0.3, and 0 <b< 0.3. Phases of aluminum titanate (Al2O3-TiO2), strontium feldspar (SrO-Al2O3-2SiO2), mullite (3Al2O3-2SiO2), alumina (Al2O3), and/or glass have been observed by x-ray diffraction, and electron-probe micro-analysis in the inventive ceramic. These phases are not required to be perfectly stoichiometric, or crystalline in the final product.
[0008] Silica and glass additions improve strength, decrease porosity, lower thermal expansion and firing temperature, and may provide resistance of the ceramic against decomposition. Alumina additions increase porosity. As provided silica additions of up to 10% by weight (based on total batch weight) and alumina additions of up to 50% by weight may be made. Glass having a composition represented by LlSrO-1.5Al2O3-13.6SiO2-TiO2 may be added in an amount of up to 50% by weight. Iron titanate and/or magnesium titanate may be substituted for up to 30% by weight of the aluminum titanate phase. These substitutions improve the resistance to decomposition of the aluminum titanate phase at temperatures between 800°-1200°C.
[0009] Li another aspect of the invention the inventive ceramic article exhibits a coefficient of thermal expansion (CTE), as measured from room temperature to 800°-1000°C of less than 45xl0"7/°C, preferably less than 25xlO"7/°C, and more preferably less than 5x10" 7/°C; a porosity of up to 60% by volume, preferably up to 55% by volume, and more preferably up to 45% by volume; and, a median pore size up to 25 micrometers, preferably up to 20 micrometers, and more preferably up to 15 micrometers; and, a modulus of rapture, as measured on a solid rod of circular cross section of greater than 400 pounds per square inch (psi), preferably greater than 700 psi.
[0010] In another aspect of the invention there is provided a method of making an aluminum titanate-based ceramic body comprising: (a) formulating a batch of inorganic raw materials comprising sources of silica, alumina, strontium, titania, and/or iron oxide together with organic processing comprising plasticizers, lubricants, binders, and water as solvent, and mixing to form a homogeneous and plasticized mixture; (b) shaping the plasticized mixture into a green body; (c) heating the green body at 20-40°C/hr over various temperature intervals with hold temperature and times between 1100°-1650°C, preferably 1100°-1500°C for a period of 30-50 hours to develop a fired aluminum-titanate body. The substantially low sintering temperatures of between 1100°-1650°C, preferably 1100°-1500°C significantly reduce manufacturing costs, while maintaining low thermal expansion, high thermal shock resistance and high mechanical strength in the inventive ceramic. [0011] In another aspect of the invention there is provided a diesel particulate filter comprising the inventive ceramic. A successful application of diesel exhaust filters requires low pressure drops and low back pressure against the engine, along with high durability during thermal cycling. The diesel particulate filter is comprised of a plugged, wall-flow honeycomb body having an inlet end and an outlet end and a multiplicity of cells extending from the inlet end to the outlet end, the cells having porous walls, wherein part of the total number of cells at the inlet end are plugged along a portion of their lengths, and the remaining part of cells that are open at the inlet end are plugged at the outlet end along a portion of their lengths, so that an engine exhaust stream passing through the cells of the honeycomb from the inlet end to the outlet end flows into the open cells, through the cell walls, and out of the structure through the open cells at the outlet end. [0012] In a preferred embodiment the diesel particulate filter comprises a honeycomb body composed of an aluminum titanate-based ceramic according to the present invention having a composition comprising u (Al2O3-TiO2) + v (R) + w (3Al2O3-2SiO2) + x (Al2O3) + y (SiO2) + z ( lSrO-1.5Al2O3-13.6SiO2-TiO2) + a (Fe2O3-TiO2) + b (MgO-2TiO2), where, R is SrO-Al2O3-2SiO2 or 11.2SrO-10.9Al2O3-24.1SiO2-TiO2, where u, v, w, x, y, z, a andb are weight fractions of each component such that (u+v+w+x+y+z+a+b=l) and u = 0.6965, v = 0.225, w = 0.075, x = 0, y = 0, z = 0, a = 0.0035, and b = 0. [0013] In another embodiment the diesel particulate filter exhibits the following properties: a CTE (RT to 800°-1000°C) of less than 15xlO"7/°C, preferably less than 5x10" 7/°C; a porosity of 30% to 50%, preferably 35% to 45% by volume; a median pore size of 5 to 20 micrometers, preferably 10 to 15 micrometers; and, a modulus of rupture, as measured by the four-point method on a cellular bar cut parallel to the direction of the channels from a honeycomb body having a cell density of 200 cells per square inch (cpsi) and 0.016 inch thick walls, of 150 to 400 psi, preferably 150 to 300 psi; a permeability of at least 0.20 x 10"12 ιj 19 9 m , preferably 0.33 to 1.00 x 10" m ; and, a pressure drop of 5 kPa or less at an artificial carbon soot loading of up to 5 g/L at a flow rate of 210 scfm for a cell density of 273 cpsi, and a cell wall thickness of 0.015 inch in a 5.66"x6" sample.
BRIEF DESCRIPTION OF THE DRAWINGS
[0014] A complete understanding of the present invention may be obtained by reference to the accompanying drawings, when considered in conjunction with the subsequent detailed description, in which:
[0015] FIG. 1 is a graphical representation of thermal expansion as a function of
0<w<0.30(3Al2O3-2SiO2) for compositions where u=0.7(Al2O3-TiO2), with the remainder being (SrO-Al2O3-2SiO2); the compositions were fired at 1500°C for 4 hours;
[0016] FIG. 2 is a graphical representation of porosity as a function of 0<w<0.30(3Al2O3-
2SiO2) for compositions where u=0.7(Al2O3-TiO2), with the remainder being (SrO-Al2O3-
2SiO2); the compositions were fired at 1500°C for 4 hours;
[0017] FIG. 3 is comparison of the thermal expansion (CTE)(10"7/°C), porosity (% volume), and median pore size (MPS) (micrometers) as a function of 0<z<0.30(l.lSrO-
1.5Al2O3-13.6SiO2-TiO2) represented on the y-axis and 0<v<0.30 (11.2SrO-10.9Al2O3-
24.1SiO2-TiO2) represented on the x-axis; the compositions have u=0.6965 (Al2O3-TiO2), a=0.0045 (Fe2O3-TiO2), with the remainder being Al2O3; the compositions were fired at
1495°C for 8 hours; and,
[0018] FIG. 4 is a graphical representation of pressure drop value between the inlet end and outlet end (i.e., pressure drop difference) in KPa as a function of soot loading (g/L) at a gas flow rate of 210 scfm, for a diesel particulate filter comprising the inventive ceramic having a composition as provided in Example 5 of Table 1, in a sample having dimensions of 5.66 inch x 6 inch, a cell geometry of 273 cells per square inch (cpsi) with a cell wall thickness of 0.015 inch.
DETAILED DESCRIPTION OF THE INVENTION
[0019] The invention provides an aluminum titanate-based ceramic comprising u (Al2O3- TiO2) + v (R) + w (3Al2O3-2SiO2) + x (Al2O3) + y (SiO2) + z (LlSrO-1.5Al2O3-13.6SiO2- TiO2) + a (Fe2O3-TiO2) + b (MgO-2TiO2), where, R is SrO-Al2O3-2SiO2 or 11.2SrO- 10.9Al2O3-24.1SiO2-TiO2, where u, v, w, x, y, z, a and b are weight fractions of each component such that (u+v+w+x+y+z+a+b=l), and 0.5 <u< 0.95, 0.01 <v< 0.5, 0.01 <w< 0.5, 0 <x< 0.5, 0 <y< 0.1, 0 <z< 0.5, 0 <a< 0.3, and 0 <b< 0.3.
[0020] The inventive ceramic is highly refractory with a low coefficient of thermal expansion (CTE), and increased thermal durability, making it suitable for high temperature applications, including but not limited to automotive emissions control systems. Accordingly, the thermal expansion (coefficient of thermal expansion) as measured by dilatometry over a temperature range from room temperature room temperature (RT) to 800° -1000°C, is less than 45xlO"7/°C, preferably less than 25xl0"7/°C, and more preferably less than 5x10" /°C. The low expansion of the inventive structure is a result of microcracking generated by anisotropic thermal expansion.
[0021] Accordingly, an advantage of the present inventive structure is that the thermal expansion hysteresis (i.e., the difference between heating and cooling curves) can be made very low. This ensures a high thermal shock resistance. Referring now to FIG. 1 there is provided a graphical representation of thermal expansion as a function of 0<w<0.30(3Al2O3- 2SiO2) for compositions where u=0.7(Al2O3-TiO2) the remainder SrO-Al2O3-2SiO2, fired at 1500°C for 4 hours. To obtain a low CTE of less than 5 x 10"7/°C, preferably w ranges between 0.05-0.15. At both lower and higher values of w, the thermal expansion increases. [0022] In addition to low thermal expansion, the inventive ceramic is particularly suitable to high interconnected porosity and large median pore size. Accordingly, the porosity as measured by mercury porosimetry is up to 60% by volume, preferably up to 55% by volume, and more preferably up to 45% by volume. The median pore size is up to 25 micrometers, preferably up to 20 micrometers, and more preferably up to 15 micrometers. Referring now to FIG. 2 there is provided a graphical representation of porosity as a function of 0<w<0.30(3Al2O3-2SiO2) for compositions where u=0.7(Al2O3-TiO2), with the remainder being (SrO-Al2O3-2SiO2), fired at 1500°C for 4 hours. A peak in porosity is obtained at w between 0.08-0.11. At both lower and higher values of w, the porosity decreases, with the lowest porosity values at w>0.25.
[0023] Referring now to FIG. 3 therein provided is a comparison of the thermal expansion (CTE)(10" /°C), porosity (% volume), and median pore size (MPS) (micrometers) as a function of 0<z<0.30(l.lSrO-1.5Al2O3-13.6SiO2-TiO2) represented on the y-axis and 0<v<0.30(11.2SrO-10.9Al2O3-24.1SiO2-TiO2) represented on the x-axis. The compositions have u=0.6965(Al2O3-TiO2), a=0.0045 (Fe2O3-TiO2) with the remainder being Al2O3, and were fired at 1495°C for 8 hours. By varying the weight fractions of both z and v, the CTE, porosity and MPS can be controlled in inventive ceramic bodies for desired applications. Also, the inventive ceramic bodies exhibit a high modulus of rupture, as measured on a solid rod of circular cross section of greater than 400 pounds per square inch (psi), preferably greater than 700 psi.
[0024] The inventive ceramic is particularly suitable for diesel exhaust filtration. In a preferred embodiment, a diesel particulate filter comprises a plugged, wall-flow filter body composed of the inventive ceramic having a composition preferably comprising u (Al2O3- TiO2) + v (R) + w (3Al2O3-2SiO2) + x (Al2O3) + y (SiO2) + z (LlSrO-1.5Al2O3-13.6SiO2- TiO2) + a (Fe2O3-TiO2) + b (MgO-2TiO2), where, R is SrO-Al2O3-2SiO2 or 11.2SrO- 10.9Al2O3-24.1SiO2-TiO2, where u, v, w, x, y, z, a and b are weight fractions of each component such that (u+v+w+x+y+z+a+b=l), and u = 0.6965, v = 0.225, w = 0.075, x = 0, y = 0, z = 0, a = 0.0035, and b = 0.
[0025] The honeycomb filter body has an inlet end and an outlet end and a multiplicity of cells extending from the inlet end to the outlet end, the cells having porous walls. Part of the total number of cells at the inlet end are plugged along a portion of their lengths, and the remaining part of cells that are open at the inlet end are plugged at the outlet end along a portion of their lengths. This plugging configuration allows for engine exhaust stream passing through the cells of the honeycomb from the inlet end to the outlet end to flow into the open cells, through the cell walls, and out of the structure through the open cells at the outlet end. Suitable cellular densities for diesel particulate filters range from 70 cells/in2 (10.9 cells/cm2) to 800 cells/in2 (124 cells/cm2). [0026] In another preferred embodiment, a diesel particulate filter according to the present invention exhibits a CTE (RT to 800°-1000°C) of less than 15xl0"7/°C, preferably less than 5xlO"7/°C; a porosity of 30% to 50%, preferably 35% to 45% by volume; a median pore size of 5 to 20 micrometers, preferably 10 to 15 micrometers; and, a modulus of rupture, as measured by the four-point method on a cellular bar cut parallel to the direction of the channels from a honeycomb body having a cell density of 200 cpsi and 0.016 inch thick walls, of 150 to 400 psi, preferably 150 to 300 psi; a permeability of at least 0.20 x 10"12 m2, preferably 0.33 to 1.00 x 10"12 m2; and, a pressure drop of 5 kPa or less at an artificial carbon soot loading of up to 5 g/L at a flow rate of 210 scfm for a cell density of 273 cpsi, and a cell wall thickness of 0.015 inch in a 5.66"x6" sample. Further, an increment in a linear dimension of less than 0.05% after the filter has been exposed two hundred times to thermal cycling at a temperature of 200° to 1100°C (18 minutes per cycle with a 3 minute hold at the top temperature) has been obtained experimentally with the inventive structures. [0027] The invention also relates to a method of fabricating the inventive aluminum titanate-based ceramic for forming a mixture from certain inorganic powdered raw materials which include sources of silica, alumina, strontium, titania, and/or iron oxide. The raw materials are blended with together with organic processing aids that may include plasticizers, lubricants, binder, and water as solvent. The mixture is then shaped into a green body, optionally dried, and fired to form the product structure. A pore former, such as graphite or polyethylene beads, may be optionally used to improve the porosity and median pore size. A pore former is a fugitive particulate material which evaporates or undergoes vaporization by combustion during drying or heating of the green body to obtain a desired, usually higher porosity and/or coarser median pore diameter. Large particle sizes in the raw materials are not preferred.
[0028] An alumina source is a powder which when heated to a sufficiently high temperature in the absence of other raw materials, yield substantially pure aluminum oxide, and includes alpha-alumina, a transition alumina such as gamma-alumina or rho-alumina, hydrated alumina, gibbsite, boehmite, aluminum hydroxide, and mixtures thereof. The particle size of the alumina source is up to 25 micrometers. A silica source includes cristobalite, non-crystalline silica such as fused silica or sol-gel silica, silicone resin, zeolite, and diatomaceous silica, kaolin, and quartz. The median particle size of the silica source is up to 30 micrometers. [0029] A titania source is preferably, but not limited to, rutile. The median particle size of the titania source is important to avoid entrapment of unreacted oxide by the rapidly growing nuclei in the structure. Accordingly, the median particle size is up to 20 micrometers. A strontium source is strontium carbonate, with a median particle size is up to 20 micrometers. Iron oxide source has a median particle size of up to 0.5 micrometers. [0030] The inorganic powdered raw materials are mixed with organic processing components, such as methylcellulose binder, oleic acid/triethanol amine surfactant, to form a plasticized and homogeneous mixture. The plasticized mixture is shaped by any conventional means, preferably by extrusion through a honeycomb die. The resulting green bodies are optionally dried, and then heated at 20-40°C/hr over various temperature intervals with hold temperature and times between 1100°-1650°C, preferably 1100°-1500°C for a period of 30-50 hours to develop the final product structure.
[0031] To obtain a wall-flow filter, a portion of the cells of the honeycomb structure at the inlet end or face are plugged, as known in the art. The plugging is only at the ends of the cells which is typically to a depth of about 1 to 20 mm, although this can vary. A portion of the cells on the outlet end but not corresponding to those on the inlet end are plugged. Therefore, each cell is plugged only at one end. The preferred arrangement is to have every other cell on a given face plugged in a checkered pattern.
[0032] To more fully illustrate the invention, the following non-limiting examples are presented. All parts, portions and percentages are on a weight basis unless otherwise stated.
EXAMPLES
[0033] Inventive samples are prepared by weighing out the dry ingredients, mixing them with organic components and water, and kneading the mixture in a stainless steel muller to form a plastic mass. Table I provides parts and proportions for the powdered raw materials and forming aids. Specifically, triethanolamine (TEA) is first mixed with water, and then with oleic acid and/or tall oil (dispersant). The resulting solution is stored at room temperature for 24 hours and then refrigerated overnight prior to use. The dry ingredients which include silica, titania, strontium carbonate, iron oxide, alumina, alumina hydroxide, silicone resin, graphite, polyethylene beads and/or methyl cellulose binder are dry mixed in a muller. The tall oil/TEA/water solution is slowly added during continuous mixing to provide homogenization and plasticization.
[0034] The plasticized mixture is extruded through a die into honeycomb bodies having approximately 100 to 400 cpsi and a wall thickness of about 0.010 to 0.025 inch. The bodies thus formed are cut to desired lengths, and heated in an oven at 85°C until dry. The samples are fired in an electric furnace at rates ranging from 20°C/hr-40°C/hr over various temperature intervals with a first hold temperature at 1200°C for 4 hours, and a second hold temperature at 1500°C for 6 hours to develop the final product structure, and cooled by shutting off power to the furnace.
[0035] The following properties are measured and included in Table II: modulus of rupture in pounds per square inch (psi) (as measured on a cellular bar cut parallel to the direction of the channels from a honeycomb body having a cell density of 200 cpsi and 0.016 inch thick walls, unless otherwise stated) porosity in % volume, median pore size in micrometers, thermal expansion 10"7/°C , and permeability 10"12 m2. A preferred composition, in terms of properties, is provided for Example 5. This composition is especially suitable for the manufacture of diesel particulate filters comprising a plugged, wall-flow honeycomb body.
[0036] Accordingly, an extruded honeycomb body comprising Example 5 ceramic is end- plugged at the inlet and outlet ends with a cold-set paste made of aluminum titanate powder. Dimensions of the sample include a diameter of 5.66 inches, and a length of 6 inches, a cell geometry of 273 cpsi and a cell wall thickness of 0.015 inch walls. The back pressure is tested by loading the sample with artificial soot (similar to copier toner) at a flow rate of 210 scfm, for loadings ranging up to 5 g/L, and measuring the pressure drop between the inlet end and the outlet end in kPa. The resulting data is graphically provided in FIG. 4 which demonstrates excellent pressure drops of between 2 kPa and 5 kPa. [0037] The effect of heat treatment on the inventive ceramic is also examined on Examples 2 and 3, with the results being provided in Table HI. Specifically, it is demonstrated that firing conditions can be employed to tailor the properties of strength, porosity, median pore size and permeability as desired or according to specific applications. [0038] In summary the present invention provides an aluminum titanate-based ceramic having low thermal expansion, and increased thermal durability, with applicability in automotive emissions control system, and in particular in diesel exhaust filtration where low pressure drop and low back pressure against the engine are required. The inventive ceramic can be formed with these desired properties at substantially low sintering temperatures of between 1100°C-1650°C, preferably 1100°C-1500°C, significantly reducing costs associated with manufacturing thereof.
[0039] It should be understood that while the present invention has been described in detail with respect to certain illustrative and specific embodiments thereof, it should not be considered limited to such but may be used in other ways without departing from the spirit of the invention and the scope of the appended claims.
Table I. Raw Materials for Inventive Examples 1-9.
Figure imgf000012_0001
Table II. Firing Conditions and Properties for Inventive Examples 1-9.
Figure imgf000013_0001
*MOR is measured on a sohd rod of circular cross section
Table III. Properties of Examples 2 and 3 as a function of heat treatment.
Figure imgf000014_0001

Claims

What is claimed:
1. A ceramic article having a composition comprising u (Al2O3-TiO2) + v (R) + w (3 Al O3- 2SiO2) + x (Al2O3) + y (SiO2) + z (l.lSrO-1.5Al2O3-13.6SiO2-TiO2) + a (Fe2O3-TiO2) + b (MgO-2TiO2), where, R is SrO-Al2O3-2SiO2 or 11.2SrO-10.9Al2O3-24.1SiO2-TiO2, where u, v, w, x, y, z, a and b are weight fractions of each component such that (u+v+w+x+y+z+a+b=l), and 0.5 <u< 0.95, 0.01 <v< 0.5, 0.01 <w< 0.5, 0 <x< 0.5, 0 <y< 0.1, 0 <z< 0.5, 0 <a< 0.3, and 0 <b< 0.3.
2. The ceramic article of claim 1 wherein R is SrO-Al2O3-2SiO2.
3. The ceramic article of claim 1 wherein R is 11.2SrO-10.9Al2O3-24. lSiO2-TiO2.
4. The ceramic article of claim 1 having a CTE, as measured from room temperature to 800°C -1000°C of less than 45 x 10"7/°C.
5. The ceramic article of claim 4 having a CTE, as measured from room temperature to 800°C -1000°C of less than 25 x 10"7/°C.
6. The ceramic article of claim 5 having a CTE, as measured from room temperature to 800°C -1000°C of less than 5 x 10"7/°C.
7. The ceramic article of claim 1 having a porosity of up to 60% by volume.
8. The ceramic article of claim 7 having a porosity of up to 45% by volume.
9. The ceramic article of claim 8 having a porosity of up to 55% by volume.
10. The ceramic article of claim 1 having a median pore size of up to 25 micrometers.
11. The ceramic article of claim 10 having a median pore size of up to 20 micrometers.
12. The ceramic article of claim 11 having a median pore size of up to 15 micrometers.
13. The ceramic article of claim 1 having a four-point modulus of rupture as measured on a solid rod of circular cross section of greater than 400 pounds per inch (psi).
14. The ceramic article of claim 13 having a four-point modulus of rupture as measured on a solid rod of circular cross section of greater than 700 psi.
15. A diesel particulate filter comprising the ceramic article of claim 1 and a plugged, wall- flow honeycomb filter body comprising a plurality of parallel end-plugged cell channels traversing the body from a frontal inlet end to an outlet end thereof.
16. The diesel particulate filer of claim 15 wherein the ceramic article has a composition comprising u (Al O3-TiO2) + v (R) + w (3 Al2O3-2SiO2) + x (Al2O3) + y (SiO2) + z (LlSrO-1.5Al2O3-13.6SiO2-TiO2) + a (Fe2O3-TiO2) + b (MgO-2TiO2), where, R is SrO- Al2O3-2SiO2 or 11.2SrO-10.9Al2O3-24.1SiO2-TiO2, where u, v, w, x, y, z, a and b are weight fractions of each component such that (u+v+w+x+y+z+a+b=l), and u = 0.6965, v = 0.225, w = 0.075, x = 0, y = 0, z = 0, a = 0.0035, and b = 0.
17. The diesel particulate filter of claim 16 having a CTE, as measured from room temperature to 800°C -1000°C of less than 15 x 10"7/°C.
18. The diesel particulate filter of claim 17 having a CTE, as measured from room temperature to 800°C -1000°C of less than 5 x 10"7/°C.
19. The diesel particulate filter of claim 16 having a porosity of 30% to 50% by volume.
20. The diesel particulate filter of claim 19 having a porosity of 35% to 45% by volume.
21. The diesel particulate filter of claim 16 having a median pore size of 5 to 25 micrometers.
22. The diesel particulate filter of claim 21 having a median pore size of 10 to 15 micrometers.
23. The diesel particulate filter of claim 16 having a modulus of rupture as measured by on a cellular bar having a cell density of 200 cpsi and 0.016 inch thick walls, of 150 to 400 psi.
24. The diesel particulate filter of claim 23 having a modulus of rupture as measured by on a cellular bar having a cell density of 200 cpsi and 0.016 inch thick walls of 150 to 300 psi.
25. The diesel particulate filter of claim 16 having a permeability of at least 0.20 x 10"12 m2.
26. The diesel particulate filter of claim 25 having a permeability of at least 0.33 x 10"12 m2.
27. The diesel particulate filter of claim 16 having a pressure drop of 5 kPa or less at an artificial carbon soot loading of up to 5 g/L and a flow rate of 210 standard cubic feet per minute (scfm) for a cell density of 273 cells per square inch and a cell wall thickness of about 0.015 inches.
28. A method of making an aluminum titanate-based ceramic body comprising:
(a) formulating a batch of inorganic raw materials comprising sources of silica, alumina, strontium, titania, and/or iron oxide together with organic processing comprising plasticizers, lubricants, binders, and water as solvent, and mixing to form a homogeneous and plasticized mixture;
(b) shaping the plasticized mixture into a green body;
(c) heating the green body at 20-40°C/hr over various temperature intervals with hold temperature and times between 1100°-1650°C for a period of 30-50 hours to develop a ceramic having a composition comprising u (Al2O3-TiO2) + v (R) + w (3Al2O3- 2SiO2) + x (Al2O3) + y (SiO2) + z (LlSrO-1.5Al2O3-13.6SiO2-TiO2) + a (Fe2O3-TiO2) + b (MgO-2TiO2), where, R is SrO-Al2O3-2SiO2 or 11.2SrO-10.9Al2O3-24.1SiO2- TiO2, where u, v, w, x, y, z, a and b are weight fractions of each component such that (u+v+w+x+y+z+a+b=l), and 0.5 <u< 0.95, 0.01 <v< 0.5, 0.01 <w< 0.5, 0 <x< 0.5, 0 <y< 0.1, 0 <z< 0.5, 0 <a< 0.3, and 0 <b< 0.3.
29. The method of claim 28 wherein the heating is between 1100°-1500°C.
30. The method of claim 28 wherein the shaping is done by extrusion.
31. The method of claim 30 wherein the plasticized mixture is extruded into a honeycomb green body.
32. The method of claim 28 wherein the ceramic has a composition comprising u (Al2O3- TiO2) + v (R) + w (3Al2O3-2SiO2) + x (Al2O3) + y (SiO2) + z (LlSrO-1.5Al2O3- 13.6SiO2-TiO2) + a (Fe2O3-TiO2) + b (MgO-2TiO2), where, R is SrO-Al2O3-2SiO2 or 11.2SrO-10.9Al2O3-24.1SiO2-TiO2, where u, v, w, x, y, z, a and b are weight fractions of each component such that (u+v+w+x+y+z+a+b=l), and u = 0.6965, v = 0.225, w = 0.075, x = 0, y = 0, z = 0, a = 0.0035, and b = 0.
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Cited By (43)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2425740A (en) * 2005-05-06 2006-11-08 Ford Global Tech Llc An exhaust treatment device
JP2007533591A (en) * 2004-04-21 2007-11-22 コーニング インコーポレイテッド Aluminum titanate ceramic and method for producing the same
JP2008508185A (en) * 2004-07-29 2008-03-21 コーニング インコーポレイテッド Aluminum titanate body having narrow pore size distribution and method for producing the same
US7381681B2 (en) 2004-04-21 2008-06-03 Dow Global Technologies Inc. Method for increasing the strength of porous ceramic bodies and bodies made therefrom
JP2008538096A (en) * 2005-03-07 2008-10-09 ケイエイチ ケミカルズ カンパニー、リミテッド Corrosion-resistant ceramic material, filter using the same, and manufacturing method thereof
US7438739B2 (en) 2004-07-26 2008-10-21 Dow Global Technologies Inc. Catalyzed soot filter
US7635446B2 (en) 2005-08-23 2009-12-22 Dow Global Technologies, Inc. Method for debindering ceramic honeycombs
US7713909B2 (en) 2004-10-13 2010-05-11 Dow Global Technologies Inc. Catalyzed diesel soot filter and process
US7772151B2 (en) 2006-07-21 2010-08-10 Dow Global Technologies Inc. Zone catalyzed soot filter
WO2011008461A2 (en) 2009-06-29 2011-01-20 Dow Global Technologies Inc. Ceramic honeycomb structure with applied inorganic skin
WO2011008462A1 (en) 2009-06-29 2011-01-20 Dow Global Technologies, Inc. Cement containing multi-modal fibers for making thermal shock resistant ceramic honeycomb structures
US7914718B2 (en) 2008-08-28 2011-03-29 Corning Incorporated Gas pore former in cellular monoliths
WO2011059699A1 (en) 2009-11-11 2011-05-19 Dow Global Technologies Llc Improved cement to make thermal shock resistant ceramic honeycomb structures and method to make them
WO2011082399A1 (en) 2009-12-31 2011-07-07 The Dow Global Technologies Llc. Method of making polymeric barrier coating to mitigate binder migration in a diesel particulate filter to reduce filter pressure drop and temperature gradients
US8016906B2 (en) 2007-05-04 2011-09-13 Dow Global Technologies Llc Honeycomb filter elements
US8051703B2 (en) 2009-02-27 2011-11-08 Corning Incorporated Methods for using a fluid stream to test a honeycomb body
EP2390307A1 (en) 2010-05-27 2011-11-30 Corning Incorporated Porous ceramic processing using prilled wax and non-ionic surfactant
EP2402296A1 (en) * 2009-02-25 2012-01-04 Sumitomo Chemical Company, Limited Method for producing aluminum titanate ceramic sintered body, and aluminum titanate ceramic sintered body
US8092579B2 (en) 2007-10-12 2012-01-10 Dow Global Technologies Llc Thermal shock resistant soot filter
US8101117B2 (en) 2008-05-30 2012-01-24 Corning, Incorporated Controlled gas pore formers in extruded ware
WO2012030534A1 (en) 2010-09-01 2012-03-08 Dow Global Technologies Llc Method for applying discriminating layer onto porous ceramic filters via gas-borne prefabricated porous assemblies
WO2012030533A1 (en) 2010-09-01 2012-03-08 Dow Global Technologies Llc Method for applying discriminating layer onto porous ceramic filters
US8298311B2 (en) 2006-11-15 2012-10-30 Corning Incorporated Filters with controlled submicron porosity
WO2012166222A1 (en) * 2011-05-27 2012-12-06 Corning Incorporated Method for controlling aluminum titanate ceramic filter properties
US8334043B2 (en) 2008-03-20 2012-12-18 Dow Global Technologies Llc Cement to make thermal shock resistant ceramic honeycomb structures and method to make them
WO2013048850A1 (en) 2011-09-27 2013-04-04 Dow Global Technologies Llc Cement and skinning material for ceramic honeycomb structures
US8435441B2 (en) 2007-07-31 2013-05-07 Corning Incorporated Compositions for applying to ceramic honeycomb bodies
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WO2013090214A2 (en) 2011-12-15 2013-06-20 Dow Global Technologies Llc Cement and skinning material based on a water-swellable clay, and method for producing segmented or skinned ceramic honeycomb structures
WO2013172916A1 (en) 2012-05-18 2013-11-21 Coopersurgical, Inc. Suture passer guides and related kits and methods
WO2014070537A1 (en) * 2012-10-30 2014-05-08 Corning Incorporated Ceramic precursor batch compositions for increased tonset using organic additive heteroatom polyols
US8926875B2 (en) 2008-08-28 2015-01-06 Corning Incorporated Managed pore size distribution in honeycomb substrates
US8974724B2 (en) 2006-11-29 2015-03-10 Corning Incorporated Aluminum titanate batch compositions and method
US9206087B2 (en) 2012-06-28 2015-12-08 Dow Global Technologies Llc Process for bonding arrays of ceramic filters
US9227878B2 (en) 2009-04-30 2016-01-05 Corning Incorporated Selected binders for the extrusion of ultra-thin wall cellular ceramics
US9586339B2 (en) 2011-08-26 2017-03-07 Dow Global Technologies Llc Process for preparing ceramic bodies
US9908718B2 (en) 2012-10-19 2018-03-06 Dow Global Technologies Llc Device, system, and method for lifting and moving formable and/or collapsible parts
WO2019032645A1 (en) 2017-08-11 2019-02-14 Corning Incorporated Green ceramic batch mixtures comprising an inverse emulsion and methods for forming a ceramic body
WO2020018346A1 (en) 2018-07-20 2020-01-23 Corning Incorporated System and method for detecting defects in a honeycomb body
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US11505499B2 (en) 2017-12-19 2022-11-22 Corning Incorporated Green ceramic mixtures comprising a stabilized emulsion and methods for forming a ceramic body

Families Citing this family (55)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3489030B1 (en) * 2002-04-26 2004-01-19 勉 福田 Method for producing aluminum titanate-based sintered body
KR20100118141A (en) * 2002-11-01 2010-11-04 오세라 가부시키가이샤 Method for producing aluminum magnesium titanate sintered product
JP5123483B2 (en) * 2003-08-22 2013-01-23 オーセラ株式会社 Manufacturing method of honeycomb filter for exhaust gas purification
US6942713B2 (en) * 2003-11-04 2005-09-13 Corning Incorporated Ceramic body based on aluminum titanate
US7122612B2 (en) 2004-02-27 2006-10-17 Corning Incorporated Porous ceramic filters with catalyst coatings
US7071135B2 (en) * 2004-09-29 2006-07-04 Corning Incorporated Ceramic body based on aluminum titanate and including a glass phase
US20070259769A1 (en) * 2005-02-22 2007-11-08 Ellison Adam J G Aluminum titanate ceramic articles and methods of making same
JP4812316B2 (en) * 2005-03-16 2011-11-09 イビデン株式会社 Honeycomb structure
US20080110147A1 (en) * 2005-03-28 2008-05-15 Beall Douglas M Low thermal expansion articles
EP1890983B1 (en) * 2005-05-31 2012-12-12 Corning Incorporated Aluminum titanate ceramic forming batch mixtures and green bodies including pore former combinations and methods of manufacturing and firing same
US20060280905A1 (en) * 2005-06-14 2006-12-14 Ngk Insulators, Ltd. Honeycomb structure
US20070099015A1 (en) * 2005-09-15 2007-05-03 Lloyd Kamo Composite sliding surfaces for sliding members
US7700163B2 (en) * 2005-10-27 2010-04-20 Corning Incorporated Microwave process for porous ceramic filters with passivation and catalyst coatings
US20070107395A1 (en) * 2005-11-16 2007-05-17 Bilal Zuberi Extruded porous substrate and products using the same
US7959704B2 (en) * 2005-11-16 2011-06-14 Geo2 Technologies, Inc. Fibrous aluminum titanate substrates and methods of forming the same
FR2893861B1 (en) 2005-11-30 2008-01-04 Saint Gobain Ct Recherches FILTRATION STRUCTURE OF GAS BASED ON CONTROLLED WALL SURFACE POROSITY SIC GAS
CN100430321C (en) * 2006-01-12 2008-11-05 景德镇陶瓷学院 Method for preparing modified aluminium titanate material
US20070254798A1 (en) * 2006-03-31 2007-11-01 Addiego William P Peroxide containing compounds as pore formers in the manufacture of ceramic articles
US7875565B1 (en) 2006-05-31 2011-01-25 Corning Incorporated Transparent glass-ceramic armor
US10501375B2 (en) 2006-06-30 2019-12-10 Corning Incorporated Cordierite aluminum magnesium titanate compositions and ceramic articles comprising same
US8956436B2 (en) 2006-06-30 2015-02-17 Corning Incorporated Cordierite aluminum magnesium titanate compositions and ceramic articles comprising same
CN102690117B (en) * 2006-06-30 2016-11-23 康宁股份有限公司 Cordierite aluminum magnesium titanate compositions and comprise the ceramic of said composition
US7744669B2 (en) * 2006-07-14 2010-06-29 Corning Incorporated Plugging material for aluminum titanate ceramic wall flow filter manufacture
WO2008027301A2 (en) * 2006-08-29 2008-03-06 Corning Incorporated Single fire honeycomb structure and method for manufacturing same
CN101389392B (en) * 2006-08-30 2011-04-13 日立金属株式会社 Ceramic honeycomb filter
US20080138273A1 (en) * 2006-12-11 2008-06-12 Yi Jiang Wall flow reactor for hydrogen production
CN101687719A (en) * 2007-03-20 2010-03-31 康宁股份有限公司 The low-shrinkage that is used for porcelain filter stops up mixture, the honeycomb filter of obstruction and manufacture method thereof
JP5502728B2 (en) * 2007-05-31 2014-05-28 コーニング インコーポレイテッド Aluminum titanate ceramic forming batch mixture with pore former and green body
JP5293608B2 (en) 2007-09-27 2013-09-18 日立金属株式会社 Ceramic honeycomb structure and manufacturing method thereof
WO2009061397A2 (en) * 2007-11-05 2009-05-14 Corning Incorporated Low expansion cement compositions for ceramic monoliths
WO2009076985A1 (en) * 2007-12-17 2009-06-25 Imerys Services Ceramic honeycomb structures
JP5501978B2 (en) * 2007-12-21 2014-05-28 ダウ グローバル テクノロジーズ エルエルシー Improved catalyzed soot filters and methods for producing them
US8383534B2 (en) * 2008-01-21 2013-02-26 Sumitomo Chemical Company, Limited Process for producing aluminum magnesium titanate
US20090253568A1 (en) * 2008-04-02 2009-10-08 Thomas James Deneka Method of making ceramic articles using proteinous material
US20090274866A1 (en) * 2008-04-30 2009-11-05 Michelle Dawn Fabian Ceramic article and method for making it
WO2009144260A1 (en) * 2008-05-29 2009-12-03 Mann+Hummel Gmbh Filter device for removing particles from flowing gas
US8729436B2 (en) * 2008-05-30 2014-05-20 Corning Incorporated Drying process and apparatus for ceramic greenware
FR2933400B1 (en) * 2008-07-04 2010-08-20 Saint Gobain Ct Recherches OXIDE-FILLED GRAINS COMPRISING AL, TI, MG AND ZR AND CERAMIC PRODUCTS COMPRISING SUCH GRAINS
FR2933401B1 (en) * 2008-07-04 2010-07-30 Saint Gobain Ct Recherches POROUS STRUCTURE OF ALUMINA TITANATE TYPE
JP5294057B2 (en) * 2008-10-02 2013-09-18 日立金属株式会社 Method for manufacturing aluminum titanate ceramic honeycomb structure
US9956703B2 (en) * 2008-12-30 2018-05-01 Corning Incorporated Methods for cleaning dies
US8138108B2 (en) * 2009-02-27 2012-03-20 Corning Incorporated Aluminum titanate-containing ceramic-forming batch materials and methods using the same
US8056401B2 (en) * 2009-05-26 2011-11-15 Corning Incorporated In-line moisture-content measurement of ceramic materials in ceramic article manufacturing
US20100301515A1 (en) * 2009-05-29 2010-12-02 Thomas William Brew Honeycomb Extrusion Die Apparatus And Methods
US20110045233A1 (en) * 2009-08-20 2011-02-24 Sandra Lee Gray Dimensional control during firing to form aluminum titanate honeycomb structures
US20110124486A1 (en) * 2009-11-24 2011-05-26 Bonham Christine Gallaher Aluminum Titanate-Containing Ceramic-Forming Batch Materials And Methods Using The Same
US8641942B2 (en) 2010-05-12 2014-02-04 Corning Incorporated Laser scanning systems and methods for measuring extruded ceramic logs
US20120133065A1 (en) 2010-11-30 2012-05-31 Stephen John Caffrey Real-time, closed-loop shape control of extruded ceramic honeycomb structures
US10526249B2 (en) 2012-11-30 2020-01-07 Corning Incorporated Cordierite aluminum magnesium titanate compositions and ceramic articles comprising same
US9079799B2 (en) 2012-11-30 2015-07-14 Corning Incorporated Cordierite aluminum magnesium titanate compositions and ceramic articles comprising same
US9102114B1 (en) * 2013-03-15 2015-08-11 Ibiden Co., Ltd. Method for manufacturing aluminum-titanate-based ceramic honeycomb structure
MX2017015281A (en) 2015-05-29 2018-08-15 Corning Inc Honeycomb filter plugging and apparatus for honeycomb filter plugging.
JP6888087B2 (en) 2016-11-10 2021-06-16 コーニング インコーポレイテッド Composite ceramic materials, articles, and manufacturing methods
US11661379B2 (en) 2017-07-21 2023-05-30 Corning Incorporated Methods of extracting volatiles from ceramic green bodies
WO2019023186A1 (en) 2017-07-24 2019-01-31 Corning Incorporated Antioxidants in green ceramic bodies containing various oils for improved firing

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4483944A (en) * 1983-07-27 1984-11-20 Corning Glass Works Aluminum titanate-mullite ceramic articles
US4855265A (en) * 1988-04-04 1989-08-08 Corning Incorporated High temperature low thermal expansion ceramic
US5290739A (en) * 1992-09-22 1994-03-01 Corning Incorporated High temperature stabilized mullite-aluminum titanate
US6101793A (en) * 1997-04-22 2000-08-15 Matsushita Electric Industrial Co., Ltd. Exhaust gas filter, method of producing the same, and exhaust gas purification apparatus
US6620751B1 (en) * 2002-03-14 2003-09-16 Corning Incorporated Strontium feldspar aluminum titanate for high temperature applications

Family Cites Families (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2776896A (en) 1952-10-22 1957-01-08 Cambridge Tile Mfg Company Ceramic composition having thermal shock resistance
US3578471A (en) 1969-11-10 1971-05-11 Corning Glass Works Thermal shock resistant ceramic material
JPS5919068B2 (en) 1980-03-26 1984-05-02 日本碍子株式会社 low expansion ceramics
JPS6033783B2 (en) * 1980-09-19 1985-08-05 旭硝子株式会社 aluminum titanate honeycomb
JPS6221756A (en) * 1985-07-22 1987-01-30 日本碍子株式会社 Aluminum titanate mullite base ceramic body
DE3814079A1 (en) * 1988-04-26 1989-11-09 Bayer Ag SINTER MOLDED BODY BASED ON ALUMINUM TITANATE, METHOD FOR THE PRODUCTION AND USE THEREOF
US5288672A (en) 1988-04-26 1994-02-22 Bayer Aktiensesellschaft Ceramics based on aluminum titanate, process for their production and their use
JPH02229763A (en) 1989-03-02 1990-09-12 Kitagawa Iron Works Co Ltd Ceramics for internal chill and internal chill body
JPH075361B2 (en) * 1990-04-21 1995-01-25 日本碍子株式会社 Aluminum titanate-mullite ceramic body
JP2533992B2 (en) * 1991-08-28 1996-09-11 日本碍子株式会社 Aluminum titanate ceramics and manufacturing method thereof
JP3192700B2 (en) * 1991-09-30 2001-07-30 日本碍子株式会社 Aluminum titanate ceramics and method for producing the same
JP2845046B2 (en) * 1992-08-06 1999-01-13 株式会社ブリヂストン Ceramic filter for molten stainless alloy
JP3484756B2 (en) * 1994-05-13 2004-01-06 松下電器産業株式会社 Aluminum titanate low thermal expansion porous ceramic body and method for producing the same
CA2167991C (en) 1995-01-25 1999-12-14 Kazuhiko Kumazawa Honeycomb regenerator
JP3600933B2 (en) * 2000-11-08 2004-12-15 オーセラ株式会社 Method for producing aluminum titanate-based sintered body
US6849181B2 (en) * 2002-07-31 2005-02-01 Corning Incorporated Mullite-aluminum titanate diesel exhaust filter

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4483944A (en) * 1983-07-27 1984-11-20 Corning Glass Works Aluminum titanate-mullite ceramic articles
US4855265A (en) * 1988-04-04 1989-08-08 Corning Incorporated High temperature low thermal expansion ceramic
US5290739A (en) * 1992-09-22 1994-03-01 Corning Incorporated High temperature stabilized mullite-aluminum titanate
US6101793A (en) * 1997-04-22 2000-08-15 Matsushita Electric Industrial Co., Ltd. Exhaust gas filter, method of producing the same, and exhaust gas purification apparatus
US6620751B1 (en) * 2002-03-14 2003-09-16 Corning Incorporated Strontium feldspar aluminum titanate for high temperature applications

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP1558545A4 *

Cited By (60)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2253603A1 (en) 2004-04-21 2010-11-24 Dow Global Technologies Inc. Porous ceramic bodies
JP2007533591A (en) * 2004-04-21 2007-11-22 コーニング インコーポレイテッド Aluminum titanate ceramic and method for producing the same
US7381681B2 (en) 2004-04-21 2008-06-03 Dow Global Technologies Inc. Method for increasing the strength of porous ceramic bodies and bodies made therefrom
US7381680B2 (en) 2004-04-21 2008-06-03 Dow Global Technologies Inc. Method for increasing the strength of porous ceramic bodies and bodies made therefrom
KR101192916B1 (en) * 2004-04-21 2012-10-18 코닝 인코포레이티드 Aluminum titanate ceramic articles and methods of making the same
US7438739B2 (en) 2004-07-26 2008-10-21 Dow Global Technologies Inc. Catalyzed soot filter
JP2008508185A (en) * 2004-07-29 2008-03-21 コーニング インコーポレイテッド Aluminum titanate body having narrow pore size distribution and method for producing the same
US7713909B2 (en) 2004-10-13 2010-05-11 Dow Global Technologies Inc. Catalyzed diesel soot filter and process
JP2008538096A (en) * 2005-03-07 2008-10-09 ケイエイチ ケミカルズ カンパニー、リミテッド Corrosion-resistant ceramic material, filter using the same, and manufacturing method thereof
US7833495B2 (en) 2005-05-06 2010-11-16 Ford Global Technologies, Llc Exhaust treatment device facilitating through-wall flow
GB2425740A (en) * 2005-05-06 2006-11-08 Ford Global Tech Llc An exhaust treatment device
US8133842B2 (en) 2005-05-06 2012-03-13 Ford Global Technologies, Llc Exhaust treatment device facilitating through-wall flow
US7635446B2 (en) 2005-08-23 2009-12-22 Dow Global Technologies, Inc. Method for debindering ceramic honeycombs
US7772151B2 (en) 2006-07-21 2010-08-10 Dow Global Technologies Inc. Zone catalyzed soot filter
US8298311B2 (en) 2006-11-15 2012-10-30 Corning Incorporated Filters with controlled submicron porosity
US8974724B2 (en) 2006-11-29 2015-03-10 Corning Incorporated Aluminum titanate batch compositions and method
US8016906B2 (en) 2007-05-04 2011-09-13 Dow Global Technologies Llc Honeycomb filter elements
US8435441B2 (en) 2007-07-31 2013-05-07 Corning Incorporated Compositions for applying to ceramic honeycomb bodies
US8092579B2 (en) 2007-10-12 2012-01-10 Dow Global Technologies Llc Thermal shock resistant soot filter
EP2592059A1 (en) 2007-11-30 2013-05-15 Corning Incorporated Composition for applying to honeycomb bodies
US8334043B2 (en) 2008-03-20 2012-12-18 Dow Global Technologies Llc Cement to make thermal shock resistant ceramic honeycomb structures and method to make them
EP2607333A1 (en) 2008-03-20 2013-06-26 Dow Global Technologies LLC Improved cement to make thermal shock resistant ceramic honeycomb structures and method to make them
US8101117B2 (en) 2008-05-30 2012-01-24 Corning, Incorporated Controlled gas pore formers in extruded ware
EP2915795A1 (en) 2008-08-28 2015-09-09 Corning Incorporated Managed pore size distribution in honeycomb substrates
US8926875B2 (en) 2008-08-28 2015-01-06 Corning Incorporated Managed pore size distribution in honeycomb substrates
US7914718B2 (en) 2008-08-28 2011-03-29 Corning Incorporated Gas pore former in cellular monoliths
EP2402296A4 (en) * 2009-02-25 2012-08-22 Sumitomo Chemical Co Method for producing aluminum titanate ceramic sintered body, and aluminum titanate ceramic sintered body
EP2402296A1 (en) * 2009-02-25 2012-01-04 Sumitomo Chemical Company, Limited Method for producing aluminum titanate ceramic sintered body, and aluminum titanate ceramic sintered body
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US9227878B2 (en) 2009-04-30 2016-01-05 Corning Incorporated Selected binders for the extrusion of ultra-thin wall cellular ceramics
WO2011008462A1 (en) 2009-06-29 2011-01-20 Dow Global Technologies, Inc. Cement containing multi-modal fibers for making thermal shock resistant ceramic honeycomb structures
WO2011008461A2 (en) 2009-06-29 2011-01-20 Dow Global Technologies Inc. Ceramic honeycomb structure with applied inorganic skin
WO2011059699A1 (en) 2009-11-11 2011-05-19 Dow Global Technologies Llc Improved cement to make thermal shock resistant ceramic honeycomb structures and method to make them
US9174158B2 (en) 2009-11-11 2015-11-03 Dow Global Technologies Llc Cement to make thermal shock resistant ceramic honeycomb structures and method to make them
WO2011082399A1 (en) 2009-12-31 2011-07-07 The Dow Global Technologies Llc. Method of making polymeric barrier coating to mitigate binder migration in a diesel particulate filter to reduce filter pressure drop and temperature gradients
US9593608B2 (en) 2009-12-31 2017-03-14 Dow Global Technologies Llc Method of making polymeric barrier coating to mitigate binder migration in a diesel particulate filter to reduce filter pressure drop and temperature gradients
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US8894895B2 (en) 2010-05-27 2014-11-25 Corning Incorporated Porous ceramic processing using a co-prilled wax and non-ionic surfactant mixture
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WO2014070537A1 (en) * 2012-10-30 2014-05-08 Corning Incorporated Ceramic precursor batch compositions for increased tonset using organic additive heteroatom polyols
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US9850171B2 (en) 2012-10-30 2017-12-26 Corning Incorporated Ceramic precursor batch compositions for increased stiffening onset temperature using organic additive heteroatom polyols
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EP1558545A1 (en) 2005-08-03
CN1323981C (en) 2007-07-04
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EP1558545A4 (en) 2009-10-21

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