JPS5843238A - Structural body of ceramic honeycomb and its production - Google Patents

Structural body of ceramic honeycomb and its production

Info

Publication number
JPS5843238A
JPS5843238A JP56143039A JP14303981A JPS5843238A JP S5843238 A JPS5843238 A JP S5843238A JP 56143039 A JP56143039 A JP 56143039A JP 14303981 A JP14303981 A JP 14303981A JP S5843238 A JPS5843238 A JP S5843238A
Authority
JP
Japan
Prior art keywords
honeycomb
structural body
extrusion
fluid
snaking
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.)
Pending
Application number
JP56143039A
Other languages
Japanese (ja)
Inventor
Yoshinori Narita
義則 成田
Sukehisa Makino
牧野 祐久
Takaaki Oshimura
押村 高明
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 JP56143039A priority Critical patent/JPS5843238A/en
Publication of JPS5843238A publication Critical patent/JPS5843238A/en
Pending legal-status Critical Current

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  • Filtering Materials (AREA)
  • Press-Shaping Or Shaping Using Conveyers (AREA)
  • Catalysts (AREA)
  • Exhaust Gas After Treatment (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Abstract

PURPOSE:To improve the purification efficiency of waste gases and the buffer effect against thermal impact by forming the structural body of ceramic honeycomb in such a way that plural penetrating fluid passages thereof snake from an inlet toward an outlet. CONSTITUTION:A honeycomb of a straight pipe is extruded through an extrusion die part 12 of an extrusion molding machine 11. The preceding end part thereof is gripped with a chuck 14 and the extrudate is rotated in the direction at right angles to the longitudinal direction of the molded extrudate. More specifically, an extruded molding 13 is rotated circumferentially and the rotation is reversed. By the reiterative repetition of these rotations, snaking is formed, and the fluid passages of the honeycomb are formed to desired snaking shapes by controlling the extrusion molding speed thereof, and the rotating speed and distance of the molding. Thus the contact surface area of the fluid at the specified length of such structural body is increased, and the mutual effect of the wall surfaces of the penetrating holes and the fluid is increased, whereby the purification efficiency for waste gases is improved. Since the snaking is larger in the parts nearer the outside circumferential parts of the structural body, a buffer effect against thermal impact is improved.

Description

【発明の詳細な説明】 本発明はセラミックハニカム構造体とその製造法に係り
、更に詳しくはハニカム流体通路の蛇行した形状であり
、内燃機関の排気ガス浄化用等に使用して好適な構造体
とその製造法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a ceramic honeycomb structure and a method for manufacturing the same, and more specifically to a structure in which honeycomb fluid passages have a meandering shape and are suitable for use in purifying exhaust gas of internal combustion engines, etc. and its manufacturing method.

セラミックハニカム構造体は、軽量であり、副摩耗性と
耐熱性および一応の強度特性を備えているために自動車
用排気ガス浄化触媒の担体等に広く用いられている。
Ceramic honeycomb structures are lightweight, have secondary abrasion resistance, heat resistance, and a certain level of strength, and are therefore widely used as supports for automobile exhaust gas purification catalysts.

上記、セラミックハニカム構造体は一般に押出成形法、
射出成形法等により成形される□ことにより、流体通路
たる貫通孔は押出方向に平行で直通管である。この従来
のハニカム構造体を内燃機関の排気ガス通路内に設置し
た時、排気ガス流入方向とハニカム構造体の貫通孔とが
同方向となるために通気抵抗が小さいという利点はある
が、また排気ガスと貫通孔壁面との相互作用が小さくな
る欠点がある。
The ceramic honeycomb structure mentioned above is generally produced by extrusion molding method.
By being molded by an injection molding method or the like, the through hole serving as a fluid passage is parallel to the extrusion direction and is a direct pipe. When this conventional honeycomb structure is installed in the exhaust gas passage of an internal combustion engine, the exhaust gas inflow direction and the through holes of the honeycomb structure are in the same direction, which has the advantage of low ventilation resistance. This has the disadvantage that the interaction between the gas and the wall surface of the through hole is reduced.

従って、排気ガス中のカーボン等の微粒子を貫通孔壁面
で捕集し浄化する場合には効率が悪い。また、セラミッ
クハニカム構造体を熱交換器として使用する場合も前記
と同様に流体と貫通孔壁面との相互作用が小さく熱交換
の効率を低下する。
Therefore, it is inefficient when collecting and purifying fine particles such as carbon in the exhaust gas on the wall surface of the through hole. Further, when the ceramic honeycomb structure is used as a heat exchanger, the interaction between the fluid and the wall surfaces of the through holes is small and the efficiency of heat exchange is reduced, as described above.

本発明は以上の欠点を解決するために成されたものであ
り、上記構造体の流体通路が入口から出口に向って蛇行
している筒状の構造体の提供と、その流体通路を所望の
蛇行形状に成形するセラミックハニカム構造体の製造法
を提供するものである。
The present invention has been made in order to solve the above-mentioned drawbacks, and provides a cylindrical structure in which the fluid passage of the structure meanders from the inlet to the outlet, and allows the fluid passage to be adjusted as desired. The present invention provides a method for manufacturing a ceramic honeycomb structure formed into a meandering shape.

本発明のセラミックハニカム構造体においては、入口か
ら出口に向って蛇行しているために構造体の一定長さに
おいての流体の接触表面積が大きくなり、また貫通孔壁
面と流体との相互作用を大きくして、排気ガスの浄化効
率を向上し、排気ガス中のカーボン尋の微粒子が構造体
通路の細孔に捕集されやすくなった。また、ハニカム構
造体の外周部分は□f%蛇行が大きいため熱衝撃に対し
て緩衝効果が・・′騙り耐熱衝撃性が実施例の笛1表に
示す如〈従来型の直通管より10−100℃向上した。
In the ceramic honeycomb structure of the present invention, since the structure meanders from the inlet to the outlet, the contact surface area of the fluid is increased over a certain length of the structure, and the interaction between the through hole wall surface and the fluid is increased. As a result, the purification efficiency of the exhaust gas is improved, and carbon particles in the exhaust gas are more likely to be collected in the pores of the structure passage. In addition, since the outer peripheral part of the honeycomb structure has a large □f% meandering, it has a buffering effect against thermal shock. The temperature improved by 100℃.

本発明の蛇行形状は第7図の斜視図に示し、A図は蛇行
曲管のみで構成されたもの、B、0図は蛇行管と直通管
との組合せの形状である。
The meandering shape of the present invention is shown in the perspective view of FIG. 7, in which Figure A shows a configuration consisting only of a meandering curved pipe, and Figures B and 0 show a combination of a meandering pipe and a straight pipe.

とれらA、B、0図に示す形状から更に蛇行ピッチを変
えることによシ所望形状のものが形成出来る。本発明で
貫通流体通路を螺線状に形成したものを除いた理由とし
て、成形体が変形して所望の形状が出来難く、また内燃
機関の排気ガス通路内に設置した場合の排気ガスと貫通
孔壁面との相互作用が比較的小さく浄化効率が従来の直
通管とあまり差がないと判断されたためである。
By further changing the meandering pitch from the shapes shown in Figures A, B, and 0, a desired shape can be formed. The reasons for excluding the structure in which the penetrating fluid passage is formed in a spiral shape in the present invention are that the molded body deforms and it is difficult to form the desired shape, and that when installed in the exhaust gas passage of an internal combustion engine, the exhaust gas and the penetrating This is because it was determined that the interaction with the hole wall surface was relatively small and the purification efficiency was not much different from that of conventional direct pipes.

以上セラミックハニカム構造体の製造法として押出成形
機の押出口金部より成形押出品の長さ方向部分に押出品
を円周方向に回転し蛇行させる装置を装着シ、成形押出
速度、成形体の回y″゛”1瞥、七”“”°“パ=″”
°“4通路を所望の蛇  状に形成することが出来る。
As described above, as a manufacturing method for a ceramic honeycomb structure, a device that rotates the extruded product in the circumferential direction from the extrusion mouth metal part of the extrusion molding machine in the longitudinal direction of the molded extruded product to meander is installed, and the molding extrusion speed is adjusted to Turns y″゛”One glance, Seven”””°“Pa=””
4 channels can be formed into a desired serpentine shape.

更にこれに使用するハニカムの押出成形口金部    
1および装置としては本発明者が先般出願した特開昭4
44−17743および特開昭t+ −1ltoix 
ノハニカム構造体の押出用口金部および押出装置に開示
されている成形口金を応用して、外周部が中央部より押
出吐出速度が早く出来る成形口金を用いるのが望ましい
。また、押出シリンダ一部を加熱しハニカム押出材の外
周部を軟らかくして流動性をあげたものを適用するのも
好ましい。一般の使用口金および装置では押出品の外径
が歪んだシ、亀裂が発生する。また、本発明者が出願し
ている特開昭j/−2ttoりおよび特開昭3.z−i
iλOjの無機質材料の押出成形法に開示されている押
出材のバインダーは成形時の硬化中にゴム状の柔軟性あ
る樹脂が好ましくそれは数秒で硬化するポリウレタン樹
脂を使用することが本発明の蛇行形成に好適なものであ
る。
Furthermore, the extrusion die part of the honeycomb used for this
1 and the device is disclosed in Japanese Unexamined Patent Publication No. 4, filed recently by the present inventor.
44-17743 and JP-A-Sho t+-1ltoix
It is desirable to apply the molding die disclosed in the extrusion die part and extrusion device of a honeycomb structure to use a forming die that allows extrusion discharge speed to be faster in the outer peripheral part than in the central part. It is also preferable to use a honeycomb extruded material whose fluidity is increased by heating a portion of the extrusion cylinder to soften the outer circumference of the honeycomb extruded material. With common ferrules and equipment, the outer diameter of the extruded product becomes distorted and cracks occur. In addition, the present inventor has filed an application for Japanese Patent Application Laid-Open No. 2003-29003 and JP-A-3. z-i
The binder of the extruded material disclosed in the extrusion molding method for inorganic materials of iλOj is preferably a rubber-like flexible resin during curing during molding, and it is preferable to use a polyurethane resin that hardens in a few seconds. It is suitable for

以下、本発明を実施例により一層具体的に説明する。Hereinafter, the present invention will be explained in more detail with reference to Examples.

実施例 押出成形装置の中心断面図を第2図に示し、図中/lは
加熱した押出シリンダーでその先端に前記した押出口金
/2を装着した内部に、別に、2Mg0・、2A120
3・jsioiからなるコージライト組成のセラミック
粉末に融水硬化型ポリウレタン樹脂を加えて混線すした
素地を入れ、約30m押出口金/Jより直通管ハニカム
を押出し、その先端部分をチャック14tにて把持する
。このチャックlダは可変モータ/jの運転によりギヤ
ー/l、/7./Iが回転して駆動を伝達する。
A central cross-sectional view of the extrusion molding apparatus according to the embodiment is shown in FIG.
3.Add water-curing polyurethane resin to ceramic powder of cordierite composition consisting of jsioi, put in a cross-wired base material, extrude a straight pipe honeycomb from an approximately 30m extrusion die/J, and hold the tip of the honeycomb with a chuck of 14t. grasp. This chuck l is operated by a variable motor /j to gears /l, /7. /I rotates and transmits the drive.

゛まだ、チャック/lはシャフト軸lりを移動し、コン
トローラ2jによシ回転速度、回転距離を決めて所望の
蛇行とすることが出来る。チャック14!とギヤーlt
はシャフト15’と異にベース−20と軸受、2/で水
中27の水槽2.2に取付けられて、チャック部分のチ
ャック/ 4tとギヤー、/ Irおよびベース20は
ハニカム13が押・出される圧力で下方に移動する構造
であり、ハニカム/3の外径、長さ寸法、□押出速度お
よびチャック部分の重量等を慕23でバランスを調整す
る構造である。ハニカムの蛇行形状は押出速度、チャッ
クの回転速度、回転距離を調節することにより決定され
る。
Still, the chuck/l can be moved along the shaft axis, and the rotational speed and rotational distance can be determined by the controller 2j to achieve a desired meandering. Chuck 14! and gear lt
Unlike the shaft 15', the base 20 and the bearing, 2/ are attached to the water tank 2.2 of the underwater 27, and the chuck part of the chuck / 4t and the gear, / Ir and the base 20 are used to extrude the honeycomb 13. It has a structure in which it moves downward by pressure, and the balance of the outer diameter, length, extrusion speed, weight of the chuck part, etc. of the honeycomb/3 is adjusted using the lever 23. The meandering shape of the honeycomb is determined by adjusting the extrusion speed, chuck rotation speed, and rotation distance.

以上の方法で押出速度2 o o wa/分、チャック
回転速度0.1 rpm Iチャン2回転反復数1g回
/分で外径tθ−−、長さ/λ0龍2貫通流体通路ピッ
チt、27調、流体通路壁厚0./jm+流体通路形状
は正方形で第1図のA図に示す蛇行ピッチP、2!−の
蛇行形成菌とB図お・よび0図に示す蛇行管と直通管を
組合せた形状に成形して、また比較品として従来型の直
通管を作成して乾燥層1aoo℃にて2時間焼成してハ
ニカム構造体とした。これら試料の内、A図および0図
に示す形状品を各3個ずつ特性を測定して下記第1表と
菌3図に示した。
In the above method, the extrusion speed was 2 o o wa/min, the chuck rotation speed was 0.1 rpm, the I-chan 2 rotation repetition rate was 1 g times/min, the outer diameter tθ--, the length/λ0, the pitch of the fluid passage through the dragon 2, t, 27 Adjustment, fluid passage wall thickness 0. /jm+The fluid passage shape is square and has a meandering pitch P, 2! as shown in Figure 1A. The meander-forming bacteria of - were molded into a shape that combines the meandering tube and straight tube shown in Figures B and 0, and a conventional straight tube was prepared as a comparison product for 2 hours in a dry layer at 1 aoooC. It was fired to form a honeycomb structure. Among these samples, the characteristics of three each of the shapes shown in Figures A and 0 were measured and are shown in Table 1 and Figure 3 below.

1゛ に 1〜〉11゜ (7) 上表で明らかな様に本発明の構造品は表面積、嵩密度の
増加は勿論であるが、耐熱衝撃性も100℃程度の向上
が確認出来た。耐熱衝撃性は電気炉加熱温度中に一20
分間保持后、空気中λSCに取出し放冷層、亀裂を調査
した。
1 to 11 degrees (7) As is clear from the table above, the structural products of the present invention not only increased in surface area and bulk density, but also improved thermal shock resistance by about 100°C. Thermal shock resistance is -20% during electric furnace heating temperature.
After holding for a minute, it was taken out to λSC in air and the cooling layer and cracks were investigated.

また、風速と圧力損失の関係を調べて第3図に示し、流
体通路蛇行のA図に示す形状品を破線で表わし、0図に
示す形状品を点線、通路直通管の比較品を実線で表わし
たものである。本発明のハニカム構造品は従来比軟菌に
比べ約30−の通気抵抗が大きくなっている。これによ
り排ガス中のカーボン等の微粒子を貫通孔壁面で捕集し
浄化する効率が向上することは明らかである。
In addition, the relationship between wind speed and pressure loss was investigated and shown in Figure 3.The shape of the product with the meandering fluid passage shown in Figure A is indicated by a broken line, the shape of the product shown in Figure 0 is indicated with a dotted line, and the comparative product with a straight passage pipe is indicated with a solid line. It is expressed. The honeycomb structured product of the present invention has a ventilation resistance that is approximately 30 - higher than that of conventional soft bacteria. It is clear that this improves the efficiency of collecting and purifying fine particles such as carbon in the exhaust gas on the wall surface of the through hole.

本発明のハニカム構造体は従来品に比較し上記した優れ
た特性のものとなり、その製造法は簡素装置をもって要
求される蛇行形状品を容易に成形することの出来るもの
である。
The honeycomb structure of the present invention has the above-mentioned superior properties compared to conventional products, and the manufacturing method thereof allows the required serpentine-shaped product to be easily formed using simple equipment.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明であるハニカム構造体の斜視(り) 図であり、A図は貫通流体通路が蛇行管形状品、B図お
よび0図は蛇行管と直通管との併用形状品、第2図はそ
の蛇行を形成する装置の断面図、第3図は通気抵抗を表
わした関係曲綜である。 /、4A、7・・・セラミックハニカム構造体、コ、!
・・・貫通流体通路、3.t・・・蛇行通路、l/・・
・シリンダー、7.2・・・口金、/3・・・押出品、
14t・・・チャック、l!・・・モータ、# 、 /
7 、 /I・・・ギヤー、/?・・・シャフト、20
・・・ペース、2/・・・軸受、2.2・・・水槽、2
3・・・銃1.21・・・水、2j・・・コントローラ (10)
Fig. 1 is a perspective view of a honeycomb structure according to the present invention, in which Fig. A shows a product in which the through-flow fluid passage is shaped like a meandering pipe, Figs. FIG. 2 is a cross-sectional view of the device that forms the meander, and FIG. 3 is a related curve representing the ventilation resistance. /, 4A, 7... Ceramic honeycomb structure, Ko,!
...through-fluid passage, 3. t...Meandering passage, l/...
・Cylinder, 7.2...cap, /3...extrusion,
14t... Chuck, l! ···motor,# , /
7, /I...gear, /? ...shaft, 20
...pace, 2/...bearing, 2.2...water tank, 2
3... Gun 1.21... Water, 2j... Controller (10)

Claims (2)

【特許請求の範囲】[Claims] (1)  複数の貫通流体通路を有する筒状のセラミッ
クハニカム構造体において、上記貫通流体通路が入口か
ら出口に向って蛇行していることを特徴とするセラミッ
クハニカム構造体。
(1) A cylindrical ceramic honeycomb structure having a plurality of through fluid passages, wherein the through fluid passages meander from an inlet toward an outlet.
(2)押出成形機の押出し口金部より成形押出品の長さ
方向と直角方向に押出品を回転させる装置を設置し、押
出される成形体を円周方向に回転し、またその回転を逆
回転して、この反復繰返しによシ蛇行を形成して、その
成形押出速度、成形体の回転速度、回転距離を調節して
、ハニカムの流体通路を所望の蛇行形状に成形すること
を特徴とするセラミツクツ・二カム□構造体の製造法。
(2) Install a device that rotates the extruded product from the extrusion mouthpiece of the extrusion molding machine in a direction perpendicular to the length direction of the molded extruded product, and rotates the extruded molded product in the circumferential direction and reverses the rotation. The honeycomb is rotated to repeatedly form a meandering shape, and the extrusion speed, rotational speed of the molded body, and rotation distance are adjusted to form the fluid passages of the honeycomb into a desired meandering shape. A method for manufacturing a ceramic Nicam□ structure.
JP56143039A 1981-09-10 1981-09-10 Structural body of ceramic honeycomb and its production Pending JPS5843238A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56143039A JPS5843238A (en) 1981-09-10 1981-09-10 Structural body of ceramic honeycomb and its production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56143039A JPS5843238A (en) 1981-09-10 1981-09-10 Structural body of ceramic honeycomb and its production

Publications (1)

Publication Number Publication Date
JPS5843238A true JPS5843238A (en) 1983-03-12

Family

ID=15329478

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56143039A Pending JPS5843238A (en) 1981-09-10 1981-09-10 Structural body of ceramic honeycomb and its production

Country Status (1)

Country Link
JP (1) JPS5843238A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH024716U (en) * 1988-06-17 1990-01-12
JPH10337479A (en) * 1997-06-06 1998-12-22 Mitsubishi Heavy Ind Ltd Honeycomb type catalyst and production thereof
JP2002537147A (en) * 1999-02-18 2002-11-05 コーニング インコーポレイテッド Silica glass honeycomb structure by extrusion of silica soot
JP2003507154A (en) * 1999-08-13 2003-02-25 スリーエム イノベイティブ プロパティズ カンパニー Channel flow filter
WO2003080245A1 (en) * 2002-03-27 2003-10-02 Ngk Insulators, Ltd. Honeycomb structural body, method of manufacturing the structural body, and catalyst body using the structural body
WO2007064373A1 (en) * 2005-11-29 2007-06-07 Caterpillar Inc. Catalytic converter
US7655195B1 (en) 1999-08-30 2010-02-02 Ngk Insulators, Ltd. Undulated-wall honeycomb structure and manufacturing method thereof
JP2011523585A (en) * 2008-05-09 2011-08-18 エミテック ゲゼルシヤフト フユア エミツシオンス テクノロギー ミツト ベシユレンクテル ハフツング Particle filter with hydrolytic coating
US20170021321A1 (en) * 2005-04-14 2017-01-26 Chemical Process Engineering Research Institute Center For Research And Technology- Hellas (Certh- Gas-solid reactor

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH024716U (en) * 1988-06-17 1990-01-12
JPH0750094Y2 (en) * 1988-06-17 1995-11-15 株式会社アマダ V-shaped groove processing machine
JPH10337479A (en) * 1997-06-06 1998-12-22 Mitsubishi Heavy Ind Ltd Honeycomb type catalyst and production thereof
JP2002537147A (en) * 1999-02-18 2002-11-05 コーニング インコーポレイテッド Silica glass honeycomb structure by extrusion of silica soot
JP2003507154A (en) * 1999-08-13 2003-02-25 スリーエム イノベイティブ プロパティズ カンパニー Channel flow filter
US7655195B1 (en) 1999-08-30 2010-02-02 Ngk Insulators, Ltd. Undulated-wall honeycomb structure and manufacturing method thereof
WO2003080245A1 (en) * 2002-03-27 2003-10-02 Ngk Insulators, Ltd. Honeycomb structural body, method of manufacturing the structural body, and catalyst body using the structural body
US7497999B2 (en) 2002-03-27 2009-03-03 Ngk Insulators, Ltd. Honeycomb structural body, method of manufacturing the structural body, and catalyst body using the structural body
US20170021321A1 (en) * 2005-04-14 2017-01-26 Chemical Process Engineering Research Institute Center For Research And Technology- Hellas (Certh- Gas-solid reactor
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