JPS58122016A - Production of silicon carbide filter - Google Patents

Production of silicon carbide filter

Info

Publication number
JPS58122016A
JPS58122016A JP401782A JP401782A JPS58122016A JP S58122016 A JPS58122016 A JP S58122016A JP 401782 A JP401782 A JP 401782A JP 401782 A JP401782 A JP 401782A JP S58122016 A JPS58122016 A JP S58122016A
Authority
JP
Japan
Prior art keywords
silicon carbide
filter
slurry
subjected
heat
Prior art date
Legal status (The legal status 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 status listed.)
Granted
Application number
JP401782A
Other languages
Japanese (ja)
Other versions
JPH0230287B2 (en
Inventor
Shunkichi Nozaki
野崎 駿吉
Yoshinori Narita
義則 成田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Tokushu Togyo KK
Niterra Co Ltd
Original Assignee
NGK Spark Plug Co Ltd
Nippon Tokushu Togyo KK
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 NGK Spark Plug Co Ltd, Nippon Tokushu Togyo KK filed Critical NGK Spark Plug Co Ltd
Priority to JP401782A priority Critical patent/JPS58122016A/en
Publication of JPS58122016A publication Critical patent/JPS58122016A/en
Publication of JPH0230287B2 publication Critical patent/JPH0230287B2/ja
Granted legal-status Critical Current

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Abstract

PURPOSE:To realize a filter that can burn away deposits by having not only high temp. heat resistance but self-exothermic characteristic. CONSTITUTION:High polymer foam is immersed in silicon carbide slurry to fill and impregnate said slurry into the pores. If necessary, the foam is subjected to impregnating and drying again after drying, whereby skeleton of a desired thickness is formed and is later subjected to sintering, whereby a porous sintered body of silicon carbide (filter) is obtained. The high polymer foam material (impregnation) impregnated with the silicon carbide slurry is first dried, then the impregnation is treated under heating to annihilate the high polymer foam material, whereby a body with skeleton construction is obtained. The body with silicon carbide construction (uncalcined) is then subjected to primary sintering for about 30min -3hr at about 1,900-2,300 deg.C in Ar flow, whereby a porous sintered body is obtained. Said body is subjected to secondary calcination in a high pressure gaseous nitrogen atmosphere of about 1,600-2,100 deg.C and 1-200atm.

Description

【発明の詳細な説明】 本発明は通電によシ発熱可能な多孔質炭化珪素焼結俸、
即ち炭化珪素フィルタの製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a porous silicon carbide sintered shard capable of generating heat when energized;
That is, it relates to a method of manufacturing a silicon carbide filter.

従来内燃機関の排気ガス、特にディーゼル笠ンソン排気
ガス等の高温気体中に含まれる微粒子カーゴ・ン等の可
燃性微粒子物質の除去のためには、耐熱性のフィルタが
必要とされているが、単に耐熱性であるだけでは、目詰
tb等の結果、耐用期間が短かく清浄化又は取替えの手
間がかかり、実用上問題がめった。これに対し、高温耐
熱性を有するのみならず、自己発熱性を備えて付着物を
焼失することができるフィルタの実現が望まれていた。
Conventionally, heat-resistant filters are required to remove combustible particulate matter such as particulate cargo contained in high-temperature gases such as exhaust gas from internal combustion engines, especially diesel engine exhaust gas. Mere heat resistance would result in clogging tb, etc., resulting in a short service life and the hassle of cleaning or replacement, which would pose problems in practice. In response, it has been desired to realize a filter that not only has high temperature resistance but also has self-heating properties and can burn off deposits.

か\るフィルタとしては、ディーゼルエンジンの排気管
に装着する為強度、耐振動性が必要であシ、また、高温
強度、耐酸化性、耐食性も必要である。
Since such a filter is installed in the exhaust pipe of a diesel engine, it must have strength and vibration resistance, and must also have high temperature strength, oxidation resistance, and corrosion resistance.

このようなフィルタ材料としては炭化珪素等の通電によ
り自己発熱可能なものが考えられるが、これまで、フィ
ルタとしてもまた自己発熱性としても優れたものを製造
することは容易ではなかった。
As such a filter material, a material such as silicon carbide that can self-heat by being energized can be considered, but until now it has not been easy to manufacture a material that is excellent both as a filter and as a self-heating material.

本発明は、これら従来法の困難を解決し、目的とする通
電発熱可能な炭化珪素フィルタの製造を可能にすること
を目的とする。即ち、本発明による通電発熱可能な炭化
珪素フィルタの製造方法は高分子発泡体材料に炭化珪素
素地泥漿を含浸し、該高分子発泡体材料を熱処理により
消失せしめて炭化珪素素地スケルトン構造体を形成し、
該構造体e1900〜2300°Cの温度においてアル
ゴン中にて一次焼成し次いで1600〜2100°Cの
温度にて1〜200気圧の窒素ガス中にて二次焼成しそ
の後その両端に耐熱性電極を形成し通電可能として成る
It is an object of the present invention to solve the difficulties of these conventional methods and to make it possible to manufacture a silicon carbide filter that can generate heat when energized. That is, the method of manufacturing a silicon carbide filter capable of generating electricity through electricity according to the present invention involves impregnating a polymeric foam material with silicon carbide matrix slurry, and eliminating the polymeric foam material by heat treatment to form a silicon carbide matrix skeleton structure. death,
The structure e is first fired in argon at a temperature of 1900 to 2300°C, then secondarily fired in nitrogen gas of 1 to 200 atm at a temperature of 1600 to 2100°C, and then heat-resistant electrodes are attached to both ends. It can be formed and energized.

以下、本発明について詳述する。The present invention will be explained in detail below.

1ず、フィルタ材料としては炭化珪素の多孔質焼結体が
選択される。炭化珪素の使用により、高温(1000°
C以上)の耐食、耐酸化性が向上する。その多孔質化の
ため、本発明においては、高分子発泡体、即ち多孔質で
連続気孔を有するものをスケルトン形成の手段として用
いる。高分子発泡体としては、公知のもの、特にポリウ
レタン発りm体、軟質ポリエチレン発泡体、ポリビニル
ホルマール発泡体、ユリア発泡体等を用いることができ
る。
First, a porous sintered body of silicon carbide is selected as the filter material. By using silicon carbide, high temperature (1000°
C or higher) corrosion resistance and oxidation resistance are improved. Due to its porous nature, in the present invention a polymeric foam, ie porous and with open pores, is used as a means of skeleton formation. As the polymeric foam, known ones can be used, particularly polyurethane foam, flexible polyethylene foam, polyvinyl formal foam, urea foam, and the like.

この高分子発泡体を炭化珪素泥漿に浸漬して該泥漿をそ
の気孔中に充填、含浸し、必要に応じ乾燥後再含浸、乾
燥をくシ返して、所望厚さのスケルトンを形成し、後の
焼結によυ多孔質の炭化珪素焼結体(フィルタ)を得る
This polymer foam is immersed in silicon carbide slurry to fill and impregnate its pores with the slurry, and if necessary, after drying, it is re-impregnated and the drying process is repeated to form a skeleton with a desired thickness. A porous silicon carbide sintered body (filter) is obtained by sintering.

この目的に適した高分子発泡体としては、例えばポリウ
レタン発泡体の場合、少なくとも気孔率約50チ平均孔
径0.5〜5%のものを用いることができ、その調製は
公知の方法による。なお高分子発泡体の気孔率、孔径等
はフィルタ設計に応じて選択する。
As a polymeric foam suitable for this purpose, for example, in the case of a polyurethane foam, one having a porosity of at least about 50% and an average pore diameter of 0.5 to 5% can be used, and can be prepared by known methods. Note that the porosity, pore diameter, etc. of the polymer foam are selected depending on the filter design.

炭化珪素泥漿は1通例のものでよい。即ち凡そ0.3〜
1.0μの微粒子β型炭化珪素を(又はさらに焼結助剤
等を)一般に、アセトンやエチルアルコール等の有機溶
剤に分散させ、フェノール樹脂等の有機バインダー(ス
ケルトン構造体の乾燥強度保持が加熱の過程でできるだ
け結合力を保持可能なもの)を適量含有させる。また水
溶性ないし水性(エマルションタイプ等)の有機バイン
ダーを用いることもでき、その場合、水性泥シとするこ
ともできる。例えばβ型炭化珪素に焼結助剤及びバイン
ダー、分散剤を加えて、混合して作ることもできる。
A conventional silicon carbide slurry may be used. That is, approximately 0.3~
In general, 1.0μ fine particles of β-type silicon carbide (or a sintering aid, etc.) are dispersed in an organic solvent such as acetone or ethyl alcohol, and an organic binder such as a phenolic resin (the dry strength of the skeleton structure is maintained when heated). (which can maintain as much bonding strength as possible during the process). Furthermore, a water-soluble or water-based (emulsion type, etc.) organic binder can also be used, and in that case, it can also be made into an aqueous slurry. For example, it can be made by adding and mixing a sintering aid, a binder, and a dispersant to β-type silicon carbide.

泥漿濃度は含浸して適するよう主として粘度に基づいて
選択し、通例10〜50センチポアズ程度(常温)とす
るよう調節する。
The concentration of the slurry is selected mainly based on the viscosity so as to be suitable for impregnation, and is usually adjusted to about 10 to 50 centipoise (at room temperature).

本発明において、炭化珪素とは、純粋なものの他実質上
炭化珪素焼結体として認められるもの、例えば公知の焼
結助剤としてB4C、B 、 AIN、カーデン、又は
熱処理によシカ−ポン分の残る有機系樹脂等を部分的に
含むものを包含する。例えば84C0,5部、フェノー
ル樹脂6部を含んだものを出発原料とすることができる
In the present invention, silicon carbide refers to silicon carbide that is substantially recognized as a sintered body of silicon carbide in addition to pure silicon carbide, such as B4C, B, AIN, carden, or silicon carbide as a known sintering aid. This includes those that partially contain remaining organic resins. For example, a starting material containing 0.5 parts of 84C and 6 parts of a phenol resin can be used.

炭化珪素泥漿を含浸した高分子発泡体材料(含浸体)は
、まず乾燥されてその後含浸体を加熱処理し、高分子発
泡体材料を消失させてスケルトン構造体とする。この加
熱処理は、好ましくは真空中にて徐々に昇温し、約40
0〜1. OOO1’C,好ましくは800°Cに約3
0分〜3時間、好ましくは約1時間保持することにより
高分子発泡体材料を完全に消失させる。この際注意すべ
きことは、急激な加熱と燃焼とを防止しつつ、徐々に有
機材料を消失させることである。
The polymeric foam material (impregnated body) impregnated with the silicon carbide slurry is first dried, and then the impregnated body is heat treated to eliminate the polymeric foam material and form a skeleton structure. This heat treatment is preferably carried out by gradually increasing the temperature in a vacuum to about 40%
0-1. OOO1'C, preferably about 3 to 800°C
The polymeric foam material is completely dissipated by holding for 0 minutes to 3 hours, preferably about 1 hour. At this time, care must be taken to gradually eliminate the organic material while preventing rapid heating and combustion.

このようにして得られる炭化珪素構造体(未焼成)を次
いでAr 気流中にて凡そ1900〜2300°C1好
ましくは1950〜2100℃にて約30分〜3時間、
好ましくは約1時間焼成して一次焼結し多孔質焼結体と
する。次いで、温度凡そ1600〜2100℃、好まし
くは1800〜2000°C11〜200気圧の高圧窒
素ガス雰囲気中にて、2次焼成を行う。このようにして
焼結体の常温における比抵抗は、10Ω傷以下となる。
The silicon carbide structure thus obtained (unfired) is then heated in an Ar gas flow at approximately 1900 to 2300°C, preferably 1950 to 2100°C, for approximately 30 minutes to 3 hours.
Preferably, it is fired for about 1 hour to perform primary sintering to form a porous sintered body. Next, secondary firing is performed at a temperature of approximately 1600 to 2100°C, preferably 1800 to 2000°C, and a high pressure nitrogen gas atmosphere at 11 to 200 atm. In this way, the specific resistance of the sintered body at room temperature becomes 10Ω or less.

通電抵抗特性として比抵抗的0.01〜lΩけ(100
0°C)のものとすることが、発熱体として好ましい。
The current carrying resistance characteristic is a specific resistance of 0.01 to 1Ω (100
0°C) is preferable as the heating element.

通電可能とするために、さらに該フィルタの両端に耐熱
性電極を形成する。この電極は例えば金属化面の形成、
その他公知の方法によることもできるが、特に、特願昭
55−”184793号に本出願人によシ開示された金
属化面を有する炭化珪素焼結体とすることが好ましい。
Heat-resistant electrodes are further formed at both ends of the filter to enable electricity to flow. This electrode can be used, for example, for the formation of metallized surfaces,
Although other known methods may be used, it is particularly preferable to use a silicon carbide sintered body having a metallized surface as disclosed by the applicant in Japanese Patent Application No. 184793/1983.

即ち、5ilO〜90重量%、残部Fe、Ni+Coの
少なく共2種以上の混合物とから成る組成物を1100
〜1800℃の温度で非酸化性雰囲気で焼結して成る金
属化面である。その他の方法として、アルミニウム金属
を溶射するメタリコン、或いは他の金属Ni、’l’i
等の溶射又は蒸着及び蒸着後のシンタリング、いわゆる
銀、白金、ルテニウム被−スト塗布後の焼きつけ、等が
ある。
That is, a composition consisting of 5ilO to 90% by weight, the balance being Fe, and a mixture of at least two or more of Ni+Co was
The metallized surface is sintered in a non-oxidizing atmosphere at a temperature of ~1800°C. Other methods include spraying metallized aluminum or other metals such as Ni, 'l'i
Thermal spraying or vapor deposition and sintering after vapor deposition, so-called baking after coating of silver, platinum, or ruthenium, etc., etc.

なお、炭化珪素フィルタの電極部を除く他の部分の表面
には、酸化防止、耐食性増大、強度劣化防止等の目的で
、公知の補助的処理を施すことが好ましい。即ち、本出
願人の出願に係る特願昭54−96998に開示の如く
、シリカ質ガラス層を0.1〜20ミクロン程度の厚さ
に形成することが有用である。この場合、フィルタは、
(通例電極部金属化処理の彼、必要に応じ電極部の保護
措置を講じた上)約1300°C以上の(好ましくは約
1500’(:りの酸化性雰囲気中で約1時間以上加熱
処理することにより、シリカ質ガラス層が形成される。
Note that the surface of the silicon carbide filter other than the electrode portions is preferably subjected to a known auxiliary treatment for the purpose of preventing oxidation, increasing corrosion resistance, preventing strength deterioration, and the like. That is, as disclosed in Japanese Patent Application No. 54-96998 filed by the present applicant, it is useful to form a siliceous glass layer with a thickness of about 0.1 to 20 microns. In this case, the filter is
Heat treatment in an oxidizing atmosphere of about 1,300°C or more (preferably about 1,500°C) for about 1 hour or more (usually after metallizing the electrodes and taking protective measures as necessary) By doing so, a siliceous glass layer is formed.

上記酸化性雰囲気としては、大気中、好ましくは、湿潤
水素又は湿潤不活性ガス中がある。
The oxidizing atmosphere may be air, preferably wet hydrogen or wet inert gas.

この7リ力質ガラス層被膜形成により、フィルタの比抵
抗は、処理前に比べ最大約5%増大するが、これは、シ
リカ質ガラス層が絶縁層を成すためであると考えられる
By forming this siliceous glass layer coating, the specific resistance of the filter increases by up to about 5% compared to before treatment, and this is thought to be because the siliceous glass layer forms an insulating layer.

このフィルタは、かくて、高い気孔率(30〜60%)
を有しながら十分な強度(常温、高温共)を有し、耐熱
性がよく、低い電気抵抗を示すため低電圧(12〜24
v)で通電発熱し、短期間の通電によp1000°C以
上に昇温し、ディーゼルエンジン排気ガス中等のカーボ
ンの付着物を完全に焼き除去できる自己清浄性のフィル
タである。
This filter thus has a high porosity (30-60%)
It has sufficient strength (both room temperature and high temperature), good heat resistance, and low electrical resistance, so it can be used at low voltage (12 to 24
v) It is a self-cleaning filter that generates heat when energized, raises the temperature to 1000°C or more when energized for a short period of time, and can completely burn off carbon deposits such as diesel engine exhaust gas.

以上詳述の通電、本発明によれば、多孔質で微細物質の
フィルタとして用いることのできる、自己発熱性の炭化
珪素焼結体から成るフィルタかえられ、その通電発熱に
よる酸化1強度劣化等も有効に防止可能である。
According to the present invention, a filter made of a self-heating silicon carbide sintered body, which can be used as a filter for porous and fine substances, can be replaced, and the oxidation strength deterioration due to the heat generated by energization can be avoided. Can be effectively prevented.

このフィルタの通電発熱は約1200°atで長時間可
能であシ、短時間であれば凡そ1300°Cまで可能で
あり、繰り返し通電発熱によってもスポーリング抵抗の
劣化等は生じない。
The heat generated by energization of this filter can be maintained for a long time at about 1200°C, and can be heated up to about 1300°C for a short time, and the spalling resistance does not deteriorate even if the filter is repeatedly energized and heated.

従って、このフィルタは、ディーゼルエンジン排気ガス
中のカーボン(スス)等の除去に有利に用いることがで
きる外、その他任意の高温フィルタ(自己清浄性)とし
て用いることができ、また反応触媒の担体等としても有
用であることは明らかである。
Therefore, this filter can be advantageously used to remove carbon (soot) etc. from diesel engine exhaust gas, and can also be used as any other high-temperature filter (self-cleaning), and can also be used as a support for reaction catalysts, etc. It is clear that it is useful as a

以下本発明の実施例について示す。Examples of the present invention will be shown below.

実施例1 気孔率60%、平均孔径3uL、たて120cmXよこ
120(XX高さ240cWLの市販のポリウレタン発
泡体に下記の泥漿を含浸せしめ、その内部にまで泥漿を
付着させて乾燥し、この含浸乾燥を夫々3〜6回くり返
した。乾燥は大気中24 hr放置後、赤外線幅射式乾
燥器によシ100°QX 2 hr行った。
Example 1 A commercially available polyurethane foam with a porosity of 60%, an average pore diameter of 3 uL, a length of 120 cm x a width of 120 cm (XX height of 240 cWL) was impregnated with the following slurry, and the slurry was allowed to adhere to the inside of the foam and dried. The drying process was repeated 3 to 6 times.After being left in the air for 24 hours, it was dried in an infrared radiation dryer for 100°QX 2 hours.

泥 漿             重量部β−8iC(
平均粒径0.3μ)    io。
Sludge Weight part β-8iC (
Average particle size 0.3μ) io.

B、C(1/   )     0.5フエノール樹脂
(液状)固形分     6エチルアルコール    
    100この混合物をボールミルで3時間混合し
、さらにエチルアルコールを追加して泥漿の粘度を30
ポアズとした。
B, C (1/) 0.5 Phenol resin (liquid) solid content 6 Ethyl alcohol
100 This mixture was mixed in a ball mill for 3 hours, and ethyl alcohol was added to reduce the viscosity of the slurry to 30.
Poise.

かく得られた含浸体を、真空中にて毎分10°Cの加熱
速度で昇温し、800℃×1時間保持して、完全に有機
物を消失せしめ、生成した炭化珪素多孔体をAr気流中
にて2000〜2100°CX60分−次焼結し、ガス
置換を行ない次いで1800〜2000°014h気圧
にてN2ガス中で3時間2次焼結を行い、放冷した。
The impregnated body thus obtained was heated in vacuum at a heating rate of 10°C per minute and held at 800°C for 1 hour to completely eliminate organic matter, and the resulting porous silicon carbide body was heated in an Ar gas stream. After sintering at 2,000 to 2,100° CX for 60 minutes, gas was replaced, secondary sintering was performed at 1,800 to 2,000° C. for 3 hours in N2 gas at 14 hours of atmospheric pressure, and the mixture was allowed to cool.

次いで、重量比にて5i66%、残部Fe17チ、N1
10%、Cr7%の混合物に有機バインダ2外チ、溶剤
(アセトン)100外%を添加して成るペーストを、焼
結体の対向する側面に塗布し10−8torr  の真
空雰囲気中にて1500°C×30分焼成して、金属化
面となし焼成後面間距離200 ffLjlLの電極を
形成した。
Next, in terms of weight ratio, 5i was 66%, the balance was Fe17, and N1
A paste made by adding 2% organic binder and 100% solvent (acetone) to a mixture of 10% Cr and 7% Cr was applied to the opposite sides of the sintered body and heated at 1500° in a vacuum atmosphere of 10-8 torr. C×30 minutes of firing to form an electrode having a distance of 200 ffLjlL between the metallized surface and the blank fired surface.

該フィルタを1500°Cの湿潤水素中(ウェッタ一温
度50“、H2/N2=3A)にて処理し、炭化珪累表
面にシリカ質ガラス層を形成した。その結果比抵抗は2
〜10%増大した。この被膜処理フイルタを10000
Qx1000時間連続して大気中で加熱したが、抵抗値
の変化は認められず、強度劣化も認められなかった。こ
のフィルタ電極間に2.4VX60^で通電すると3分
間に800℃に昇温した。
The filter was treated in wet hydrogen at 1500°C (wetter temperature 50", H2/N2 = 3A) to form a siliceous glass layer on the surface of the silicon carbide layer. As a result, the specific resistance was 2.
~10% increase. 10,000 coated filters
Although it was heated continuously in the air for Qx1000 hours, no change in resistance value was observed, and no deterioration in strength was observed. When electricity was applied between the filter electrodes at 2.4V x 60^, the temperature rose to 800°C in 3 minutes.

実施例2 ディーゼルエンノン排気管の管路中に通路長50はX幅
3QQllX高さ300Bの実施例1と同様の方法で得
た炭化珪素フィルタをセットし、24Vで通電可能とし
、ディーゼルエンノン5000cc  (直噴型)6気
筒を用いて、運輸省6モードに準じ100 kmm画描
走行テストを行ない1時間毎に、2分間通電して連続テ
ストの結果、テスト後もフィルタ性能に劣化は認められ
なかった。
Example 2 A silicon carbide filter obtained in the same manner as in Example 1 with a passage length of 50 x width of 3QQll x height of 300B was set in the conduit of a diesel engine exhaust pipe, and a silicon carbide filter obtained in the same manner as in Example 1 was made to be energized at 24V. Using a 5000cc (direct injection type) 6-cylinder engine, we conducted a 100 km drawing test according to the Ministry of Transport's 6 modes, and as a result of continuous testing by energizing for 2 minutes every hour, no deterioration in filter performance was observed even after the test. I couldn't.

併気ガス中のカーボンは、ボッシュのスモーク濃度計に
よりスモーク濃度を測定したところフィルタ通過前3で
あったのがフィルタ通過後2であった。
When the smoke concentration of carbon in the mixed gas was measured using a Bosch smoke densitometer, it was 3 before passing through the filter and 2 after passing through the filter.

出願人  日本特殊陶業株式会社 代理人  弁理士 加 藤 朝 道Applicant: NGK SPARK PLUG CO., LTD. Agent: Patent Attorney Asami Kafuji

Claims (1)

【特許請求の範囲】[Claims] 1)高分子発泡体材料に炭化珪素素地泥漿を含浸し、該
高分子発泡体材料全熱処理によシ消失せしめて炭化珪素
素地スケルトン構造体を形成し、該構造体を1900〜
2300°Cの温度においてアルゴン中にて一次焼成し
次いで1600〜2100°Cの温度にて1〜200気
圧の窒素ガス中にて二次焼成しその後その両端に耐熱性
電極を形成し通電可能として成る通電発熱可能な炭化珪
素フィルタの製造法。
1) A polymeric foam material is impregnated with a silicon carbide matrix slurry, and the polymeric foam material is completely heat-treated to be completely eliminated to form a silicon carbide matrix skeleton structure, and the structure is heated from 1900 to
Firstly fired in argon at a temperature of 2300°C, then secondarily fired in nitrogen gas at 1 to 200 atm at a temperature of 1600 to 2100°C, after which heat-resistant electrodes are formed on both ends to enable electricity to flow. A method for manufacturing a silicon carbide filter that can generate heat when energized.
JP401782A 1982-01-16 1982-01-16 Production of silicon carbide filter Granted JPS58122016A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP401782A JPS58122016A (en) 1982-01-16 1982-01-16 Production of silicon carbide filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP401782A JPS58122016A (en) 1982-01-16 1982-01-16 Production of silicon carbide filter

Publications (2)

Publication Number Publication Date
JPS58122016A true JPS58122016A (en) 1983-07-20
JPH0230287B2 JPH0230287B2 (en) 1990-07-05

Family

ID=11573196

Family Applications (1)

Application Number Title Priority Date Filing Date
JP401782A Granted JPS58122016A (en) 1982-01-16 1982-01-16 Production of silicon carbide filter

Country Status (1)

Country Link
JP (1) JPS58122016A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3516587A1 (en) * 1984-05-29 1985-12-05 Ibiden K.K., Oogaki, Gifu POROESIC SILICON CARBIDE SINTER AND METHOD FOR THE PRODUCTION THEREOF
US4791785A (en) * 1986-02-28 1988-12-20 Porous Element Heating Limited Removal of particulate material from a gas
DE4130630A1 (en) * 1991-09-14 1993-03-18 Forschungszentrum Juelich Gmbh METHOD FOR THE PRODUCTION OF POROESE, FLOW-THROUGH MOLDED BODIES FROM SILICON CARBIDE AND DIESEL RUSSIA FILTER ELEMENT
KR100978513B1 (en) * 2008-03-18 2010-08-27 유도향 Manufacturing method of porous molded body

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5234471U (en) * 1975-09-02 1977-03-11
JPS55167177A (en) * 1979-06-08 1980-12-26 Ngk Spark Plug Co Manufacture of silicon carbide heating body

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5234471U (en) * 1975-09-02 1977-03-11
JPS55167177A (en) * 1979-06-08 1980-12-26 Ngk Spark Plug Co Manufacture of silicon carbide heating body

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3516587A1 (en) * 1984-05-29 1985-12-05 Ibiden K.K., Oogaki, Gifu POROESIC SILICON CARBIDE SINTER AND METHOD FOR THE PRODUCTION THEREOF
US4791785A (en) * 1986-02-28 1988-12-20 Porous Element Heating Limited Removal of particulate material from a gas
EP0244061B1 (en) * 1986-02-28 1992-03-04 Porous Element Technology Limited Apparatus for the removal of particulate material from a gas
DE4130630A1 (en) * 1991-09-14 1993-03-18 Forschungszentrum Juelich Gmbh METHOD FOR THE PRODUCTION OF POROESE, FLOW-THROUGH MOLDED BODIES FROM SILICON CARBIDE AND DIESEL RUSSIA FILTER ELEMENT
US5474587A (en) * 1991-09-14 1995-12-12 Forschungszentrum Julich Gmbh Porous fluid-permeable moldings of silicon carbide and process of production
KR100978513B1 (en) * 2008-03-18 2010-08-27 유도향 Manufacturing method of porous molded body

Also Published As

Publication number Publication date
JPH0230287B2 (en) 1990-07-05

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