WO2002040424A1 - Structure en nid d'abeilles et procédé de fabrication - Google Patents
Structure en nid d'abeilles et procédé de fabrication Download PDFInfo
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- WO2002040424A1 WO2002040424A1 PCT/JP2001/009857 JP0109857W WO0240424A1 WO 2002040424 A1 WO2002040424 A1 WO 2002040424A1 JP 0109857 W JP0109857 W JP 0109857W WO 0240424 A1 WO0240424 A1 WO 0240424A1
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- silicon carbide
- strength
- young
- modulus
- honeycomb structure
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- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/515—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics
- C04B35/56—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on carbides or oxycarbides
- C04B35/565—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on non-oxide ceramics based on carbides or oxycarbides based on silicon carbide
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/88—Handling or mounting catalysts
- B01D53/885—Devices in general for catalytic purification of waste gases
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/20—Carbon compounds
- B01J27/22—Carbides
- B01J27/224—Silicon carbide
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- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/56—Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional [3D] monoliths
- B01J35/57—Honeycombs
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- C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/626—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
- C04B35/62605—Treating the starting powders individually or as mixtures
- C04B35/62625—Wet mixtures
- C04B35/6263—Wet mixtures characterised by their solids loadings, i.e. the percentage of solids
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- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/626—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
- C04B35/63—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B using additives specially adapted for forming the products, e.g.. binder binders
- C04B35/632—Organic additives
- C04B35/636—Polysaccharides or derivatives thereof
- C04B35/6365—Cellulose or derivatives thereof
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- C04B38/00—Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof
- C04B38/0006—Honeycomb structures
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2235/00—Indexing scheme associated with group B01J35/00, related to the analysis techniques used to determine the catalysts form or properties
- B01J2235/15—X-ray diffraction
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- C04B2111/00—Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
- C04B2111/00474—Uses not provided for elsewhere in C04B2111/00
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- C04B2235/50—Constituents or additives of the starting mixture chosen for their shape or used because of their shape or their physical appearance
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- C04B2235/5418—Particle size related information expressed by the size of the particles or aggregates thereof
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- Y10T428/2982—Particulate matter [e.g., sphere, flake, etc.]
Definitions
- the present invention relates to a honeycomb structure used for a filter for exhaust gas purification of automobiles, a catalyst carrier, and the like, and a method for producing the same.
- a porous material As a filter for collecting and removing particulate matter contained in dust-containing fluids such as diesel engine exhaust gas, or as a catalyst carrier for carrying a catalyst component for purifying harmful substances in exhaust gas, a porous material is used.
- Honeycomb structures are widely used. It is also known to use refractory particles such as silicon carbide (SiC) particles as a constituent material of such a honeycomb structure.
- Japanese Patent Application Laid-Open No. Hei 6-182228 discloses that a silicon carbide powder having a predetermined specific surface area and an impurity content is used as a starting material, and this is molded into a desired shape.
- a porous silicon carbide-based catalyst support having a honeycomb structure obtained by drying and firing in a temperature range of 160 to 220 is disclosed.
- Japanese Patent Application Laid-Open No. 61-265550 discloses that an oxidizable material or a refractory composition containing an oxidizable material is added with a vitrified material, mixed with a binder, mixed and mixed.
- respective silicon carbide compacts formed by adding an organic binder and a clay mineral-based, glass-based, or lithium silicate-based inorganic binder to silicon carbide powder.
- Hei 6-182228 discloses a conventional method for producing a porous silicon carbide sintered body, in which a silicon carbide particle serving as an aggregate is made of glassy flux or clay. A method is also introduced in which a binder is added and molded, and then the molded body is baked at a temperature at which the binder melts.
- Japanese Patent Publication No. Sho 6-131384 and Japanese Patent Publication No. Sand, ceramic ground product, A 1 2 0 3, T I_ ⁇ 2, Z R_ ⁇ metal oxides such as 2, silicon carbide, nitride product is granulated to a predetermined particle size made of boride or other refractory materials
- the thermal shock resistance (R) is represented by the following equation (1).
- S is the fracture strength
- Re is the Poisson's ratio
- E is the Young's modulus
- ⁇ and 0! Are values that are specific to the material and hardly change for the same material, while S and E vary greatly depending on the porosity, microstructure, etc. of the material It is a numerical value.
- the thermal shock resistance is proportional to the strength, but is inversely proportional to the Young's modulus, so that the sintered body disclosed in Japanese Patent Application Laid-Open No. Hei 6-182228 is manufactured.
- Hei 6-182228 in which the raw material silicon carbide powder is bonded in a vitreous state, has a firing temperature of 1 Although it may be as low as 0000 to 140,000, for example, the sintered body produced by this method is used to remove particulates contained in exhaust gas discharged from a diesel engine.
- DPFs diesel particulate filters
- the filter shown in JP-B-61-13845 and JP-B-61-13846 is a porous, bottomed cylindrical body with a 5 to 20 mm thick partition wall, though it is porous. It could not be applied under high SV (space velocity) conditions such as a filter for air conditioning.
- the present invention has been made in view of such a conventional circumstance, and can be manufactured at a relatively low firing temperature at a low cost while containing refractory particles such as silicon carbide particles, and has high strength and high strength.
- An object of the present invention is to provide a honeycomb structure having thermal shock resistance, which can be suitably used as a filter for purifying automobile exhaust gas by treatment such as plugging, or as a catalyst carrier under high SV conditions, and a method for producing the same. And Disclosure of the invention
- a honeycomb structure made of a silicon carbide-based porous body and having a large number of through-holes penetrating in the axial direction partitioned by partition walls, and the strength and Young's modulus of the silicon carbide-based porous body are provided. Satisfies the following relationship:
- the strength and the Young's modulus of the silicon carbide based porous material satisfy the following relationship.
- the strength and the Young's modulus of the silicon carbide based porous material satisfy the following relationship.
- the silicon carbide-based porous body contains silicon carbide particles serving as an aggregate and metallic silicon serving as a binder.
- the clay obtained by adding the metal silicon and the organic binder to the silicon carbide particle material, mixing and kneading is formed into a honeycomb shape, and the obtained formed body is formed. After removing the organic binder in the formed body by calcination, the main structure is fired.
- the addition amount of the metal silicon is set to a total amount of the silicon carbide particle raw material and the metal silicon.
- a method for manufacturing a honeycomb structure which is in a range of 15 to 40% by weight.
- the main firing is preferably performed in a temperature range of 140 to 160 O :.
- Figure 1 is a plot of the residual strength Z room temperature strength against the temperature difference ⁇ (° C) between the electric furnace and water.
- the honeycomb structure of the present invention is made of a silicon carbide porous body, and the strength and Young's modulus of the silicon carbide porous body are set and manufactured so as to satisfy the following relationship.
- the thermal shock resistance is inversely proportional to the Young's modulus value, it is important to suppress the Young's modulus value compared to the strength value in order to improve the thermal shock resistance of the honeycomb structure. If the above value is less than 1.1, the thermal shock resistance is low.
- this material can be used as a diesel particulate filter (DPF) to remove particulates contained in exhaust gas exhausted from diesel engines.
- DPF diesel particulate filter
- the filter may be damaged in some cases due to the rapid temperature difference generated in the filter. It is not preferable because there is.
- the honeycomb structure since the ratio between the strength and the Young's modulus, which are the physical property values of the silicon carbide-based porous body constituting the honeycomb structure, is set in the relationship of the above equation, the honeycomb structure has excellent thermal shock resistance. Show. Further, it is preferable to set the strength and Young's modulus of the silicon carbide based porous material so as to satisfy the following relationship, because more excellent thermal shock resistance can be obtained.
- the strength and the Young's modulus of the silicon carbide based porous material are set so as to satisfy the following relationship, since sufficient thermal shock resistance can be obtained.
- the relationship between the strength and the Young's modulus of the silicon carbide-based porous body can be used without any problem if the honeycomb structure is assumed to be used as, for example, a DPF, if it is set so as to satisfy the following formula. Can be.
- the silicon carbide-based porous body constituting the honeycomb structure includes metal silicon as a binder for bonding the silicon carbide particles together with silicon carbide particles serving as an aggregate.
- metal silicon as a binder for bonding the silicon carbide particles together with silicon carbide particles serving as an aggregate.
- metal silicon is used for bonding silicon carbide particles, it has a higher thermal conductivity than conventional structures that use vitreous material for bonding refractory particles. In some cases, burning particulates deposited for filter regeneration does not produce local heat that could damage the filter.
- the present invention is not a thick-walled bottomed cylindrical body as disclosed in Japanese Patent Publication No. S61-13845 Because of the honeycomb structure described above, it can be used under high SV conditions as a filter for purifying automobile exhaust gas or a catalyst carrier.
- honeycomb structure of the present invention First, metal silicon and an organic binder are used as a material for the refractory particles. Then, the mixture is mixed and kneaded by a conventional method to obtain a forming clay.
- the refractory particles used in the present invention include a viewpoint of heat resistance and the like.
- oxide A 1 2 0 3 is, Z R_ ⁇ 2, Y 2 0 3, in the carbide-based S i C, the nitride S i 3 N 4 , A1N, and other mullite.
- raw materials used for refractory particles such as silicon carbide and metallic silicon may contain trace impurities such as Fe, A 1, and Ca, but may be used as they are. It may be used after purification by chemical treatment such as chemical cleaning.
- a method using a material having a small Young's modulus, such as a metal, as a binder can be used.
- metallic silicon used in the honeycomb structure of the present invention and the method for producing the same is a binder excellent in heat resistance, corrosion resistance, ease of handling, and the like.
- the above-mentioned ratio of strength and Young's modulus has a strong correlation with the microstructure of the silicon carbide-based porous body, it is not necessary to simply use metallic silicon, and the particle diameter, composition, and firing temperature of the material are not sufficient. It is necessary to optimize the microstructural structure determined by the above.
- the metallic silicon melts during firing, wets the surface of the silicon carbide particles, and plays a role of bonding the particles.
- the appropriate addition amount of metallic silicon in the method for manufacturing a honeycomb structure according to the present invention varies depending on the particle size and shape of the silicon carbide particles, but is 15 to 40% by weight based on the total amount of the silicon carbide particles and metallic silicon. %, Preferably in the range of 15 to 35% by weight, and more preferably in the range of 18 to 32% by weight.
- the addition amount of metallic silicon is less than 15% by weight, the effect of reducing the Young's modulus by using metallic silicon is not sufficiently exhibited, which is not preferable.
- the content exceeds 40% by weight, the value of the Young's modulus increases due to the densification of the structure, which is not preferable.
- the obtained kneaded material is formed into a desired honeycomb shape by an extrusion molding method or the like. Then After the obtained molded body is calcined to remove (degrease) the organic binder contained in the molded body, main firing is performed.
- the calcination is preferably performed at a temperature lower than the temperature at which metallic silicon melts. Specifically, it may be once held at a predetermined temperature of about 150 to 700, or may be calcined by lowering the heating rate to 50: Zhr or less in a predetermined temperature range. Good.
- the heating rate may be slowed down only for a certain temperature zone or may be slowed down for a plurality of sections. You may let it.
- the calcination atmosphere may be an oxidizing atmosphere, but if the molded body contains a large amount of organic binder, it may burn violently with oxygen during the calcination, causing the molded body temperature to rise rapidly. For this reason, it is also a preferable method to suppress abnormal temperature rise of the compact by performing the treatment in an inert atmosphere such as N 2 or Ar. Suppression of this abnormal temperature rise is an important control when using a material with a large coefficient of thermal expansion (weak against thermal shock).
- the organic binder is added, for example, in an amount of 20% by weight (external part) or more based on the main raw material, it is preferable to perform calcination in the inert atmosphere.
- the refractory particles are SiC particles or other materials that may be oxidized at a high temperature
- calcining in an inert atmosphere as described above can be performed at least at a temperature higher than the temperature at which oxidation starts. It is preferable to suppress the oxidation of the molded body.
- the calcination and the subsequent main calcination may be performed as separate steps in the same or separate furnace, or may be performed as a continuous step in the same furnace.
- the former is also a preferable method, but the latter method is also preferable from the viewpoint of the total firing time and furnace operating cost.
- the temperature range for performing the main firing be 140 to 160.
- the optimum firing temperature is determined from the microstructure and the characteristic value, but is more preferably in the range of 150 to 160. It is particularly preferable that the ratio be in the range of 150 to 150.
- the melting point of metallic silicon is 140, so that a porous structure cannot be obtained. If the temperature exceeds 160, the microstructure changes, and the effect of reducing the Young's modulus by using metallic silicon is not sufficiently exhibited, which is not preferable.
- a sintered body having high thermal conductivity can be obtained because silicon carbide particles are bonded to each other.
- sintering is performed by a mechanism called evaporative condensation, so that a higher firing temperature is required to evaporate silicon carbide than the production method of the present invention, and a silicon carbide sintered body that can be used practically is used.
- it is necessary to fire at a temperature of at least 800 ° C., usually at least 200 ° C.
- the atmosphere for the main firing it is preferable to select the atmosphere for the main firing depending on the type of the refractory particles.
- silicon carbide particles are used as the refractory particles, oxidation at high temperatures is a concern. Therefore, it is preferable to use a non-oxidizing atmosphere such as N 2 or Ar at least in a temperature range higher than the temperature at which oxidation starts.
- a non-oxidizing atmosphere such as N 2 or Ar at least in a temperature range higher than the temperature at which oxidation starts.
- a SiC raw material powder having an average particle size as shown in Table 1 and a metal Si powder having an average particle size of 4 mm were blended so as to have a composition shown in the same table. Then, 6 parts by weight of methylcellulose as an organic binder, 2.5 parts by weight of a surfactant, and 24 parts by weight of water were added, and the mixture was uniformly mixed and kneaded to obtain a kneaded material for molding. The obtained kneaded material was extruded using an extruder to an outer diameter of 45 mm, a length of 120 mm, a partition wall thickness of 0.43 mm, and a cell density of 100 cells / square inch (16 cells cm 2 ). Into a honeycomb shape.
- This honeycomb formed body was calcined at 550 in an oxidizing atmosphere at 550 for 3 hours, and then fired in a non-oxidizing atmosphere at a firing temperature shown in Table 1 for 2 hours.
- a two-cam structure silicon carbide sintered body was manufactured (Example 2).
- a test piece was cut out from each of the sintered bodies, and the average pore size was measured using a mercury pouring port simeter. The diameter and porosity were measured.
- the strength was measured by a four-point bending strength test using a material testing machine, and the Young's modulus was measured and calculated from the relationship between load and displacement by a static elastic modulus test method. The results are shown in Table 1. Further, when the crystal phase was identified by X-ray diffraction, it was confirmed that the crystal phase consisted of SiC and Si.
- Example 1 Metal-silicon bond 30 20/80 1450 10 45 20 17 1.17
- Example 2 Metal-silicon bond 30 30/70 1450 10 45 20 15 1.33
- Test pieces cut from the sintered bodies of Examples 1 and 2 and Comparative Example 1 were used as samples, and these samples were dropped from an electric furnace at a predetermined temperature into water at room temperature and quenched. was measured by a four-point bending strength test.
- room temperature strength the strength of the sample before heating in the electric furnace
- residual strength the strength of the sample after quenching
- the honeycomb structure of the present invention is manufactured by the conventional recrystallization method because the strength and the Young's modulus of the silicon carbide porous body constituting the honeycomb structure are set to a predetermined ratio.
- Excellent thermal shock resistance compared to Furthermore, even though silicon carbide particles, which are refractory particles, are included, they can be sintered at a relatively low firing temperature during production, so that the production cost can be reduced, the yield can be improved, and the cost can be reduced. it can.
- it has high thermal conductivity in addition to excellent thermal shock resistance.For example, when used for DPF, it can damage the filter even if it burns the particulates deposited for filter regeneration. There is no significant heat generation. Further, since it is a porous honeycomb structure, it can be suitably used as a filter or a catalyst carrier for purifying automobile exhaust gas even under high SV conditions.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Structural Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Filtering Materials (AREA)
- Ceramic Products (AREA)
- Catalysts (AREA)
- Exhaust Gas After Treatment (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Press-Shaping Or Shaping Using Conveyers (AREA)
Description
Claims
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US10/203,518 US6746748B2 (en) | 2000-11-17 | 2001-11-12 | Honeycomb structure and process for production thereof |
| EP01981065A EP1340734A4 (en) | 2000-11-17 | 2001-11-12 | Honeycomb structure and method for making it |
| AU2002212754A AU2002212754A1 (en) | 2000-11-17 | 2001-11-12 | Honeycomb structure and method for manufacture thereof |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000-350847 | 2000-11-17 | ||
| JP2000350847A JP2002154876A (ja) | 2000-11-17 | 2000-11-17 | ハニカム構造体及びその製造方法 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2002040424A1 true WO2002040424A1 (fr) | 2002-05-23 |
Family
ID=18824003
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2001/009857 Ceased WO2002040424A1 (fr) | 2000-11-17 | 2001-11-12 | Structure en nid d'abeilles et procédé de fabrication |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US6746748B2 (ja) |
| EP (1) | EP1340734A4 (ja) |
| JP (1) | JP2002154876A (ja) |
| AU (1) | AU2002212754A1 (ja) |
| WO (1) | WO2002040424A1 (ja) |
| ZA (1) | ZA200206263B (ja) |
Families Citing this family (24)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4136319B2 (ja) * | 2000-04-14 | 2008-08-20 | 日本碍子株式会社 | ハニカム構造体及びその製造方法 |
| JP4426083B2 (ja) * | 2000-11-17 | 2010-03-03 | 日本碍子株式会社 | 炭化珪素質多孔体及びその製造方法 |
| JP4307781B2 (ja) * | 2001-03-30 | 2009-08-05 | 日本碍子株式会社 | 炭化珪素質多孔体及びその製造方法 |
| EP1550646A4 (en) * | 2002-10-07 | 2006-04-26 | Ibiden Co Ltd | HONEYCOMB STRUCTURE BODY |
| WO2004031100A1 (ja) * | 2002-10-07 | 2004-04-15 | Ibiden Co., Ltd. | ハニカム構造体 |
| JP4750343B2 (ja) * | 2002-10-23 | 2011-08-17 | 日本碍子株式会社 | 多孔質ハニカム構造体の製造方法、及びハニカム成形体 |
| US7244685B2 (en) * | 2002-11-20 | 2007-07-17 | Ngk Insulators, Ltd. | Silicon carbide porous body, process for producing the same and honeycomb structure |
| KR100865058B1 (ko) * | 2003-06-23 | 2008-10-23 | 이비덴 가부시키가이샤 | 허니컴 구조체 |
| JP4437785B2 (ja) * | 2003-08-12 | 2010-03-24 | 日本碍子株式会社 | 炭化珪素質触媒体の製造方法 |
| US7281274B2 (en) * | 2003-10-16 | 2007-10-09 | Lmp Media Llc | Electronic media distribution system |
| WO2005064128A1 (ja) * | 2003-12-25 | 2005-07-14 | Ibiden Co., Ltd. | 排気ガス浄化装置および排気ガス浄化装置の再生方法 |
| US7279213B2 (en) * | 2003-12-29 | 2007-10-09 | Corning Incorporated | High-strength thin-walled honeycombs |
| US20050158171A1 (en) * | 2004-01-15 | 2005-07-21 | General Electric Company | Hybrid ceramic matrix composite turbine blades for improved processibility and performance |
| WO2005094967A1 (ja) * | 2004-03-31 | 2005-10-13 | Ngk Insulators, Ltd. | ハニカム構造体及びその製造方法 |
| JP2009035452A (ja) * | 2007-08-02 | 2009-02-19 | Taiheiyo Cement Corp | 多孔体及びその製造方法 |
| US20090174279A1 (en) * | 2008-01-08 | 2009-07-09 | General Electric Company | Stator Bar Components with High Thermal Conductivity Resins, Varnishes, and Putties |
| US7655868B2 (en) * | 2008-01-08 | 2010-02-02 | General Electric Company | Stator bar components with high thermal conductivity |
| JP2012030215A (ja) * | 2010-07-02 | 2012-02-16 | Denso Corp | ハニカム構造体及びその製造方法 |
| JP5189629B2 (ja) * | 2010-09-21 | 2013-04-24 | 日本碍子株式会社 | 排ガス浄化用ハニカム構造体及び排ガス浄化用ハニカム触媒体 |
| CN102489322B (zh) * | 2011-12-29 | 2013-12-11 | 重庆材料研究院 | 柴油汽车尾气净化催化剂及制备方法和净化装置 |
| JP5568792B2 (ja) * | 2012-03-26 | 2014-08-13 | 日本ファインセラミックス株式会社 | 多孔体の製造方法 |
| JP6059954B2 (ja) * | 2012-10-30 | 2017-01-11 | 日本碍子株式会社 | ハニカムフィルタ |
| US9321189B1 (en) * | 2013-03-15 | 2016-04-26 | Ibiden Co., Ltd. | Method for manufacturing ceramic honeycomb structure |
| US20220023826A1 (en) * | 2020-07-21 | 2022-01-27 | Ben Wen | Method of preparing an adsorption material for a vaporizer |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS638264A (ja) * | 1986-06-25 | 1988-01-14 | 東海高熱工業株式会社 | 炭化ケイ素系複合材料 |
| JPH0517227A (ja) * | 1991-07-02 | 1993-01-26 | Agency Of Ind Science & Technol | 炭化珪素/金属珪素複合体及びその製造方法 |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE19710105A1 (de) * | 1997-03-12 | 1998-09-17 | Sgl Technik Gmbh | Mit Graphitkurzfasern verstärkter Siliciumcarbidkörper |
| JP4136319B2 (ja) * | 2000-04-14 | 2008-08-20 | 日本碍子株式会社 | ハニカム構造体及びその製造方法 |
| JP3607939B2 (ja) * | 2000-06-16 | 2005-01-05 | 独立行政法人産業技術総合研究所 | 炭化ケイ素−窒化ホウ素複合材料の反応合成 |
| JP4426083B2 (ja) * | 2000-11-17 | 2010-03-03 | 日本碍子株式会社 | 炭化珪素質多孔体及びその製造方法 |
| US6699429B2 (en) * | 2001-08-24 | 2004-03-02 | Corning Incorporated | Method of making silicon nitride-bonded silicon carbide honeycomb filters |
-
2000
- 2000-11-17 JP JP2000350847A patent/JP2002154876A/ja active Pending
-
2001
- 2001-11-12 US US10/203,518 patent/US6746748B2/en not_active Expired - Lifetime
- 2001-11-12 EP EP01981065A patent/EP1340734A4/en not_active Withdrawn
- 2001-11-12 WO PCT/JP2001/009857 patent/WO2002040424A1/ja not_active Ceased
- 2001-11-12 AU AU2002212754A patent/AU2002212754A1/en not_active Abandoned
-
2002
- 2002-08-06 ZA ZA200206263A patent/ZA200206263B/en unknown
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS638264A (ja) * | 1986-06-25 | 1988-01-14 | 東海高熱工業株式会社 | 炭化ケイ素系複合材料 |
| JPH0517227A (ja) * | 1991-07-02 | 1993-01-26 | Agency Of Ind Science & Technol | 炭化珪素/金属珪素複合体及びその製造方法 |
Non-Patent Citations (1)
| Title |
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| See also references of EP1340734A4 * |
Also Published As
| Publication number | Publication date |
|---|---|
| EP1340734A4 (en) | 2006-06-07 |
| US20030021948A1 (en) | 2003-01-30 |
| JP2002154876A (ja) | 2002-05-28 |
| ZA200206263B (en) | 2004-03-24 |
| AU2002212754A1 (en) | 2002-05-27 |
| EP1340734A1 (en) | 2003-09-03 |
| US6746748B2 (en) | 2004-06-08 |
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