JP3359855B2 - Exhaust gas purification converter - Google Patents
Exhaust gas purification converterInfo
- Publication number
- JP3359855B2 JP3359855B2 JP36559397A JP36559397A JP3359855B2 JP 3359855 B2 JP3359855 B2 JP 3359855B2 JP 36559397 A JP36559397 A JP 36559397A JP 36559397 A JP36559397 A JP 36559397A JP 3359855 B2 JP3359855 B2 JP 3359855B2
- Authority
- JP
- Japan
- Prior art keywords
- mat
- exhaust gas
- converter
- thickness
- gas purification
- 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.)
- Expired - Lifetime
Links
Landscapes
- Exhaust Gas After Treatment (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、排気ガス浄化用コンバ
ーター、特に自動車等の排気ガス浄化用コンバーターに
関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a converter for purifying exhaust gas, and more particularly to a converter for purifying exhaust gas of automobiles and the like.
【0002】[0002]
【従来の技術】従来、主として車両に搭載する排気ガス
浄化用コンバーターにおいては、触媒保持体と前記触媒
保持体の外方を覆う金属製シェルと、両者の間に配置し
た無機繊維マットとよりなる。前記触媒保持体には白金
等の触媒が担持されている。触媒保持体としては、例え
ばその断面をハニカム状に成形したコージェライト担体
を用いる。2. Description of the Related Art Conventionally, an exhaust gas purifying converter mainly mounted on a vehicle comprises a catalyst holder, a metal shell covering the outside of the catalyst holder, and an inorganic fiber mat disposed therebetween. . A catalyst such as platinum is supported on the catalyst holder. As the catalyst holder, for example, a cordierite carrier whose cross section is formed into a honeycomb shape is used.
【0003】次に、無機繊維マットは、バーミキュライ
トとセラミックファイバー等との混合物が主であるが、
無機繊維のみからなるものも用いられている。前記無機
繊維は、自動車の走行中等において触媒保持体が外周の
金属製シェルと当接した際の破損を防ぎ、また、金属製
シェルと触媒保持体との間から排気ガスがリークするこ
とを防ぐために用いられている。[0003] Next, the inorganic fiber mat is mainly a mixture of vermiculite and ceramic fibers.
A fiber made of only inorganic fibers is also used. The inorganic fibers prevent the catalyst holder from being damaged when the catalyst holder comes into contact with the outer metal shell during driving of an automobile or the like, and also prevent exhaust gas from leaking from between the metal shell and the catalyst holder. Used for
【0004】前記無機繊維として、結晶質アルミナ繊維
マットを用いたものが用いられているが、結晶質アルミ
ナ繊維マットは初期の状態で極めて嵩高い為、排気ガス
浄化用コンバーターを組立る際に、樹脂フィルムで真空
パックして初期の厚みを抑える方法や、前記マットに樹
脂含浸処理し厚みを減少させることにより、前記触媒保
持体への組付け性を改善する方法が、特開平8−174
687等に挙げられている。As the inorganic fibers, those using a crystalline alumina fiber mat are used. However, since the crystalline alumina fiber mat is extremely bulky in an initial state, it is difficult to assemble a converter for purifying exhaust gas. Japanese Patent Application Laid-Open No. 8-174 discloses a method in which the initial thickness is reduced by vacuum packing with a resin film, or a method in which the mat is impregnated with a resin to reduce the thickness to improve the assemblability to the catalyst holder.
687 etc.
【0005】[0005]
【発明が解決しようとする課題】前記無機繊維のみから
なる無機繊維を触媒保持体と金属製シェルの間に配置し
排気ガス浄化用コンバーターを組み立てる場合、予め無
機繊維をプラスチックフィルムで密封した後、フィルム
内部を真空に減圧し、前記無機繊維のみからなる無機繊
維の厚みを薄くしておく方法がとられているが、排気ガ
ス浄化用コンバーターを組み立てた後、前記プラスチッ
クフィルムが排気管内部に残る為、排気ガスが排気ガス
浄化用コンバーター内部を流れた場合、排気ガスの熱に
より、プラスチックフィルムが気化し、異臭が発生する
ばかりでなく、触媒等に吸着し、正常に排気ガス浄化シ
ステムが作動しないという問題がある。When assembling an exhaust gas purifying converter by arranging the inorganic fibers composed of only the inorganic fibers between the catalyst holder and the metal shell, the inorganic fibers are sealed in advance with a plastic film, A method has been adopted in which the inside of the film is depressurized to a vacuum and the thickness of the inorganic fibers consisting of only the inorganic fibers is reduced, but after assembling the exhaust gas purification converter, the plastic film remains inside the exhaust pipe. Therefore, when the exhaust gas flows inside the exhaust gas purification converter, the heat of the exhaust gas causes the plastic film to vaporize and not only generate an unpleasant odor, but also adsorb to the catalyst, etc., and the exhaust gas purification system operates normally. There is a problem not to do.
【0006】これに対し、前記マットに樹脂含浸処理し
厚みを減少させる方法があり、樹脂含浸量を予め少なく
しておく方法があるが、樹脂量が少ないと、前記マット
は厚み方向の復元力が極めて大きい為、マットの初期厚
みを小さくすることが困難であり、排気ガス浄化用コン
バーターを組み立てる場合、金属シェルと触媒保持体の
間にセットする事が困難であった。On the other hand, there is a method of reducing the thickness by impregnating the mat with a resin, and a method of reducing the amount of resin impregnation in advance. However, when the amount of the resin is small, the mat has a small restoring force in the thickness direction. Is extremely large, it is difficult to reduce the initial thickness of the mat, and when assembling a converter for purifying exhaust gas, it is difficult to set the mat between the metal shell and the catalyst holder.
【0007】[0007]
【課題を解決するための手段】本発明は、触媒保持体
と、前記触媒保持体の外方を覆う金属製シェルとの間に
配置する組立時充填密度が0.2g/cm3 〜0.6g
/cm3 であり、マットの厚み方向の0.1〜15%で
ある表面層に5〜30wt%、マットの厚み方向の9
9.9〜85%である内部層に0.5〜5wt%の有機
バインダーを含有し、有機バインダーの総含有率が、マ
ットの10wt%以下である結晶質アルミナ繊維マット
よりなる保持シール材によって構成される排気ガス浄化
用コンバーターにおいて、前記有機バインダーは、非電
解質水溶性高分子及びエマルジョンラテックスの混合物
を用い、固形分混合比が1:10〜10:1であること
を特徴とする排気ガス浄化用コンバーターにある。According to the present invention, the packing density at the time of assembling between a catalyst support and a metal shell that covers the outside of the catalyst support is 0.2 g / cm 3 to 0. 6g
/ Cm 3 , 5 to 30 wt% in the surface layer which is 0.1 to 15% in the thickness direction of the mat, and 9 to 9% in the thickness direction of the mat.
The inner layer of 9.9 to 85% contains an organic binder of 0.5 to 5% by weight, and the total content of the organic binder is not more than 10% by weight of the mat. In the exhaust gas purifying converter thus constituted, the organic binder uses a mixture of a non-electrolyte water-soluble polymer and an emulsion latex, and has a solid content mixing ratio of 1:10 to 10: 1. It is in the converter for purification.
【0008】まず、前記触媒保持体としては、例えばハ
ニカム状のものを用いる。また、前記触媒保持体には、
例えばコージェライト、アルミナ等により作成する。次
に、前記金属製シェルは、例えば断面が楕円形、円形の
パイプまたは、シェル状に二分割されたケースである。
次に、前記マットは結晶質アルミナ繊維である。First, for example, a honeycomb-shaped catalyst holder is used. Further, the catalyst holding body includes
For example, it is made of cordierite, alumina or the like. Next, the metal shell is, for example, a pipe having an elliptical or circular cross section, or a case divided into two in a shell shape.
Next, the mat is a crystalline alumina fiber.
【0009】一般に、結晶質アルミナ繊維は嵩高い為、
初期厚みを薄くすることが必要である。触媒保持体と金
属シェルとの間に、0.2g/cm3 以上の充填密度で
配置させるには、少なくとも結晶質アルミナ繊維マット
の組立前の嵩密度が0.1g/cm3 以上なければなら
ない。尚、充填密度が0.2g/cm3 以上とする事
は、振動等によって触媒保持体がズレるのを防止する為
の必要面圧を確保する為であり、充填密度が0.6g/
cm3 以上となると、マットの復元力により、触媒保持
体を圧壊してしまったり、結晶質アルミナ繊維自体が折
れてしまうからである。Generally, crystalline alumina fibers are bulky,
It is necessary to reduce the initial thickness. In order to arrange a packing density of 0.2 g / cm 3 or more between the catalyst support and the metal shell, the bulk density of the crystalline alumina fiber mat before assembly must be at least 0.1 g / cm 3. . The packing density of 0.2 g / cm 3 or more is for securing a necessary surface pressure for preventing the catalyst holder from shifting due to vibration or the like.
This is because if it is more than cm 3 , the restoring force of the mat will cause the catalyst holder to be crushed or the crystalline alumina fiber itself will be broken.
【0010】結晶質アルミナ繊維は嵩高い為、初期厚み
を薄くする為に、樹脂含浸処理を行うが、前述した理由
から、樹脂含浸量は極力少なくする必要がある。しかし
ながら樹脂含浸量を少なくすると、前記マットを触媒保
持体に巻付けた後、金属製シェルにセットする際にマッ
ト表面がシェルと擦れて、剥離したり、ちぎれたりして
しまう。従って少なくともマットの表面層即ち厚み方向
の0.1〜15%までは、5〜30wt%の樹脂を含有
させる必要がある。好ましくは、マット厚みの0.5%
に、15wt%の樹脂を含有させる。Since the crystalline alumina fibers are bulky, a resin impregnation treatment is performed to reduce the initial thickness. However, for the above-mentioned reason, the resin impregnation amount needs to be as small as possible. However, when the resin impregnation amount is reduced, the mat surface is rubbed with the shell when the mat is wound around the catalyst holder and then set on a metal shell, and the mat is peeled or torn. Therefore, at least the surface layer of the mat, that is, up to 0.1 to 15% in the thickness direction, needs to contain 5 to 30% by weight of the resin. Preferably, 0.5% of mat thickness
Contains 15% by weight of a resin.
【0011】次に、マットの内部層にも前記マットの初
期厚みを薄くする為に、樹脂を含有させる必要がある。
前記表面層の残りの部分即ち厚み方向の99.9〜85
%に0.5〜5wt%の樹脂を含有させる。前述した理
由により、3wt%前後が好適である。Next, in order to reduce the initial thickness of the mat, a resin must be contained in the inner layer of the mat.
The remaining part of the surface layer, that is, 99.9 to 85 in the thickness direction.
% Of the resin. For the reasons described above, around 3 wt% is preferred.
【0012】次に、マットへの樹脂を含有させる方法で
あるが、一般に水溶媒を用いた樹脂をスプレー処理、ま
たはマットを含浸した後、乾燥させる。しかしながら、
高濃度の樹脂を含有させる場合、問題ないが、本発明の
ように低濃度の樹脂を含有させる場合、溶媒中の樹脂濃
度を低くした後マットに添加し乾燥させるが、この場
合、乾燥時にマイグレーション効果により、含浸した樹
脂がマット表面に集中してしまい、マット内部に樹脂が
殆ど残らない為、マットの初期厚みを薄くできないとい
う問題があった。Next, a method of incorporating the resin into the mat is generally performed by spraying the resin using an aqueous solvent or impregnating the mat, followed by drying. However,
There is no problem when a high-concentration resin is contained, but when a low-concentration resin is contained as in the present invention, the resin concentration in the solvent is reduced and then added to the mat and dried. Due to the effect, the impregnated resin concentrates on the surface of the mat, and almost no resin remains inside the mat. Therefore, there is a problem that the initial thickness of the mat cannot be reduced.
【0013】この為、界面活性剤を用いてマイグレーシ
ョンを防止する方法がとられているが、マイグレーショ
ンを全く起こさないと、本発明のように、全体の樹脂含
有量を少なくし、且つマット表面層と内部層の樹脂含有
率を制御する事は困難である。For this reason, a method of preventing migration using a surfactant has been adopted. However, if migration does not occur at all, as in the present invention, the entire resin content is reduced and the mat surface layer is reduced. It is difficult to control the resin content of the inner layer.
【0014】かかる問題に対し本発明では、前記有機バ
インダーとして、非電解質水溶性高分子及びエマルジョ
ンラテックスの混合物を用いる。分子量の高い非電解質
水溶性高分子は、乾燥時のマイグレーションにより表面
層に移動するエマルジョンラテックスを止める働きをす
るからである。In the present invention, a mixture of a non-electrolyte water-soluble polymer and an emulsion latex is used as the organic binder. This is because the non-electrolyte water-soluble polymer having a high molecular weight functions to stop the emulsion latex moving to the surface layer due to migration during drying.
【0015】非電解質水溶性高分子のみを用いて、マッ
トを作成する事も可能であるが、非電解質水溶性高分子
は乾燥後の強度が高い為、乾燥後のマットが固くなりす
ぎて排気ガス浄化用コンバーターを組み立てる際に、触
媒保持体に巻き付ける事が困難になってしまう。かかる
理由から、前記非電解質水溶性高分子とエマルジョンラ
テックスの固形分混合比は、1:10〜10:1である
必要がある。好ましくは、1:1がよい。It is possible to prepare a mat using only the non-electrolyte water-soluble polymer, but since the non-electrolyte water-soluble polymer has a high strength after drying, the mat after drying becomes too hard and the exhaust gas is exhausted. When assembling the gas purification converter, it becomes difficult to wind the converter around the catalyst holder. For this reason, the solid content mixing ratio of the non-electrolyte water-soluble polymer and the emulsion latex needs to be 1:10 to 10: 1. Preferably, 1: 1 is good.
【0016】[0016]
【実施例】実施例1 触媒保持体としてコーディエライトモノリス外形130
mm、長さ100mm、金属製シェルとして内径138
mm、肉厚2.5mm、SUS304、長さ300m
m、のものを二分割し、分割面に幅15mmのフランジ
をつけた物。無機繊維シ−トとして厚み25mm、嵩密
度0.06g/cm3 の結晶質アルミナ繊維マット、非
電解質水溶性高分子としてポリアクリルアマイド(ポリ
アクロンV−05ミサワセラミックケミカル製)、エマ
ルジョンラテックスとして(ニポールラテックスLX−
874日本ゼオン)を用いて排気ガス浄化用コンバータ
ーを製造した。EXAMPLES Example 1 Cordierite monolith outer shape 130 as catalyst support
mm, length 100 mm, inner diameter 138 as a metal shell
mm, thickness 2.5mm, SUS304, length 300m
m, which is divided into two parts and a flange with a width of 15 mm is attached to the divided surface. A crystalline alumina fiber mat having a thickness of 25 mm and a bulk density of 0.06 g / cm 3 as an inorganic fiber sheet, polyacrylamide (Polyaclon V-05 manufactured by Misawa Ceramic Chemicals) as a non-electrolyte water-soluble polymer, and an emulsion latex (Nipole Latex LX-
874 Nippon Zeon Co., Ltd.).
【0017】まず、ポリアクリルアマイドとエマルジョ
ンラテックスを固形分重量比で1:1とした後、水で希
釈し混合液濃度を0.9%とした。次に結晶質アルミナ
繊維マットを混合液に含浸した後、多孔質板に挟み、加
圧態で、80℃で乾燥した。乾燥後得られたマットは厚
み5mm、嵩密度0.3g/cm3 であった。また、前
記マットの有機分含有量は5.8%であり、表面層の1
mmでの有機分含有量は10%で、他の部分は3%であ
った。First, polyacrylamide and emulsion latex were adjusted to a solid content weight ratio of 1: 1 and then diluted with water to a mixed solution concentration of 0.9%. Next, the crystalline alumina fiber mat was impregnated with the mixed solution, sandwiched between porous plates, and dried at 80 ° C. under pressure. The mat obtained after drying had a thickness of 5 mm and a bulk density of 0.3 g / cm 3 . Further, the organic content of the mat is 5.8%, and the content of the surface layer is 1%.
The organic content in mm was 10% and the other part was 3%.
【0018】前記マットを触媒保持体に巻付け、合わせ
部分を粘着テープで仮止めし、上下方向より金属シェル
にて圧縮して排気ガス浄化用コンバーターを組立たとこ
ろ、フランジにマットが噛み込む事なく。マットを損傷
させる事なく容易に排気ガス浄化用コンバーターが組立
られた。前記排気ガス浄化用コンバーターを実際自動車
に搭載し、エンジンを廻してみたが、異臭等は感じられ
なかった。When the mat is wound around the catalyst holder, the mating portion is temporarily fixed with an adhesive tape, and compressed with a metal shell from above and below to assemble the converter for purifying exhaust gas. No. The converter for exhaust gas purification was easily assembled without damaging the mat. When the converter for exhaust gas purification was actually mounted on an automobile and the engine was turned on, no odor or the like was felt.
【0019】[0019]
【発明の効果】本発明によれば、触媒保持体と、前記触
媒保持体の外方を覆う金属製シェルとの間に配置する組
立時充填密度が0.2g/cm3 〜0.6g/cm3 で
あり、マットの厚み方向の0.1〜15%である表面層
に5〜30wt%、マットの厚み方向の99.9〜85
%である内部層に0.5〜5wt%の有機バインダーを
含有し、有機バインダーの総含有率が、マットの10w
t%以下である結晶質アルミナ繊維マットよりなる保持
シール材によって構成される排気ガス浄化用コンバータ
ーにおいて、前記有機バインダーは、非電解質水溶性高
分子及びエマルジョンラテックスの混合物を用い、固形
分混合比が1:10〜10:1とすることにより、 容
易に排気ガス浄化用コンバーターを製造できるばかりで
なく、前記排気ガス浄化用コンバーター内部の有機分含
有量を低くすることが可能となり、使用時異臭がした
り、排気ガス浄化システムが誤動作する事がない。According to the present invention, the packing density at the time of assembly disposed between the catalyst holder and the metal shell covering the outside of the catalyst holder is 0.2 g / cm 3 to 0.6 g / 0.6 g / cm 3 . a cm 3, 5-30 wt% in the surface layer is 0.1 to 15% of the thickness direction of the mat, the thickness direction of the mat 99.9 to 85
% Of the mat contains 10 to 5 wt% of the organic binder, and the total content of the organic binder is 10 watts of the mat.
In a converter for purifying exhaust gas constituted by a holding sealing material comprising a crystalline alumina fiber mat of not more than t%, the organic binder uses a mixture of a non-electrolyte water-soluble polymer and an emulsion latex, and has a solid content mixing ratio. By setting the ratio to 1:10 to 10: 1, not only can the converter for exhaust gas purification be easily manufactured, but also the content of organic components inside the converter for exhaust gas purification can be reduced, and the unpleasant odor during use is reduced. And the exhaust gas purification system does not malfunction.
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平9−201514(JP,A) 特開 平6−305847(JP,A) 特開 平1−204715(JP,A) (58)調査した分野(Int.Cl.7,DB名) F01N 3/28 B01D 53/00 ────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-9-201514 (JP, A) JP-A-6-305847 (JP, A) JP-A-1-204715 (JP, A) (58) Field (Int. Cl. 7 , DB name) F01N 3/28 B01D 53/00
Claims (3)
う金属製シェルとの間に配置する結晶質アルミナ繊維マ
ットよりなる保持シール材によって構成される排気ガス
浄化用コンバーターにおいて、前記マットは、排気ガス
浄化用コンバーター組立時において、表面層に5〜30
wt%、内部層に0.5〜5wt%の有機バインダーを
含有し、有機バインダーの総含有率が、マットの10w
t%以下であることを特徴とする排気ガス浄化用コンバ
ーター。1. An exhaust gas purification converter comprising a holding sealing material made of a crystalline alumina fiber mat disposed between a catalyst holding body and a metal shell covering the outside of the catalyst holding body. The mat has a surface layer of 5 to 30 when the converter for purifying exhaust gas is assembled.
The organic layer contains 0.5 to 5% by weight of an organic binder, and the total content of the organic binder is 10 watts of the mat.
A converter for purifying exhaust gas, which is not more than t%.
ーター組立時充填密度が0.2g/cm3〜0.6g/
cm3 であることを特徴とする請求項1に記載の排気
ガス浄化用コンバーター。2. The packing density of the holding sealing material at the time of assembling the converter for purifying exhaust gas is 0.2 g / cm 3 to 0.6 g / cm 3 .
The exhaust gas according to claim 1, wherein the exhaust gas is cm 3.
Converter for gas purification .
の0.1〜15%であり、前記マットの内部層がマット
の厚み方向の99.9〜85%であることを特徴とする
請求項1又は2に記載の排気ガス浄化用コンバーター。 3. The mat according to claim 1, wherein the surface layer of the mat has a thickness of 0.1 to 15% in the thickness direction of the mat, and the inner layer of the mat has a thickness of 99.9 to 85% in the thickness direction of the mat.
The exhaust gas purifying converter according to claim 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP36559397A JP3359855B2 (en) | 1997-12-22 | 1997-12-22 | Exhaust gas purification converter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP36559397A JP3359855B2 (en) | 1997-12-22 | 1997-12-22 | Exhaust gas purification converter |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH11182237A JPH11182237A (en) | 1999-07-06 |
JP3359855B2 true JP3359855B2 (en) | 2002-12-24 |
Family
ID=18484654
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP36559397A Expired - Lifetime JP3359855B2 (en) | 1997-12-22 | 1997-12-22 | Exhaust gas purification converter |
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JP (1) | JP3359855B2 (en) |
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JP2002089253A (en) * | 2000-09-11 | 2002-03-27 | Ibiden Co Ltd | Holding seal material of catalytic converter for exhaust emission control |
JP4578712B2 (en) * | 2001-04-02 | 2010-11-10 | 三菱樹脂株式会社 | Manufacturing method of heat-resistant mat |
JP5154023B2 (en) * | 2006-03-30 | 2013-02-27 | スリーエム イノベイティブ プロパティズ カンパニー | Catalyst carrier holding material and catalytic converter |
CN112526070B (en) * | 2020-03-29 | 2022-12-09 | 江苏浩汇环保科技有限公司 | LEL and VOC combination formula waste gas analysis system |
Family Cites Families (3)
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US4929429A (en) * | 1988-02-11 | 1990-05-29 | Minnesota Mining And Manufacturing Company | Catalytic converter |
JP2568472B2 (en) * | 1993-04-16 | 1997-01-08 | 日本ピラー工業株式会社 | Heat resistant composite member and molded product thereof |
JP3025445B2 (en) * | 1995-11-21 | 2000-03-27 | 三菱化学株式会社 | Catalytic converter and method for producing the same |
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1997
- 1997-12-22 JP JP36559397A patent/JP3359855B2/en not_active Expired - Lifetime
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JPH11182237A (en) | 1999-07-06 |
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