JPH0424531B2 - - Google Patents
Info
- Publication number
- JPH0424531B2 JPH0424531B2 JP57110948A JP11094882A JPH0424531B2 JP H0424531 B2 JPH0424531 B2 JP H0424531B2 JP 57110948 A JP57110948 A JP 57110948A JP 11094882 A JP11094882 A JP 11094882A JP H0424531 B2 JPH0424531 B2 JP H0424531B2
- Authority
- JP
- Japan
- Prior art keywords
- filter member
- ceramic
- filter
- heater wire
- honeycomb
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B38/00—Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof
- C04B38/0006—Honeycomb structures
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
- B01D39/2068—Other inorganic materials, e.g. ceramics
- B01D39/2072—Other inorganic materials, e.g. ceramics the material being particulate or granular
- B01D39/2075—Other inorganic materials, e.g. ceramics the material being particulate or granular sintered or bonded by inorganic agents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
- B01D39/2068—Other inorganic materials, e.g. ceramics
- B01D39/2093—Ceramic foam
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/021—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
- F01N3/022—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters characterised by specially adapted filtering structure, e.g. honeycomb, mesh or fibrous
- F01N3/0222—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters characterised by specially adapted filtering structure, e.g. honeycomb, mesh or fibrous the structure being monolithic, e.g. honeycombs
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/021—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
- F01N3/023—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters using means for regenerating the filters, e.g. by burning trapped particles
- F01N3/027—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters using means for regenerating the filters, e.g. by burning trapped particles using electric or magnetic heating means
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
- F01N2330/00—Structure of catalyst support or particle filter
- F01N2330/06—Ceramic, e.g. monoliths
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
- F01N2350/00—Arrangements for fitting catalyst support or particle filter element in the housing
- F01N2350/02—Fitting ceramic monoliths in a metallic housing
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
- F01N2390/00—Arrangements for controlling or regulating exhaust apparatus
- F01N2390/02—Arrangements for controlling or regulating exhaust apparatus using electric components only
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Geology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Processes For Solid Components From Exhaust (AREA)
Description
【発明の詳細な説明】
本発明は内燃機関、例えばデイーゼル機関の排
気ガス中のカーボン微粒子を捕集して浄化するよ
うにした内燃機関の微粒子補集用セラミツク部材
の製造方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for manufacturing a ceramic member for collecting particulates of an internal combustion engine, for example, a diesel engine, which collects and purifies carbon particulates in the exhaust gas of the engine.
従来、この種の装置として、米国特許第
4276071号明細書に記載されたものがある。これ
は、セラミツクハニカム構造を有したセラミツク
フイルタ部材より成り、このフイルタ部材の軸方
向に延在した多数の通路をその両端の開口部分で
互い違いに閉塞したものであり、かかる構造によ
りフイルタ部在の入口側より流入した排気ガスは
上記通路を通り、該通路に隣接した他の通路に隔
壁の多孔を経て流入し、フイルタ部在の出口側よ
り流出するようになつている。 Conventionally, this type of device was disclosed in U.S. Patent No.
There is one described in the specification of No. 4276071. This is made of a ceramic filter member having a ceramic honeycomb structure, and a large number of passages extending in the axial direction of the filter member are alternately closed at the openings at both ends. Exhaust gas flowing in from the inlet side passes through the passage, flows into another passage adjacent to the passage through the pores in the partition wall, and flows out from the outlet side of the filter portion.
上記従来のハニカム型フイルタ部材では特に上
記多数の通路を隔離する隔離の多孔を通過する間
に排気ガス中のカーボン微粒子が捕捉されるので
あるが、この捕集したカーボン微粒子を燃焼して
上記フイルタ部材の再生を図る必要がある。 In the conventional honeycomb filter member described above, carbon particulates in the exhaust gas are captured while passing through the isolation pores that isolate the numerous passages, and the collected carbon particulates are burned and filtered through the filter. It is necessary to try to recycle the parts.
そこで、カーボン微粒子を焼失させるための電
気ヒータが必要となる。この電気ヒータを上記フ
イルタ部材の入口側端面に配設することが考えら
れる。 Therefore, an electric heater is required to burn off the carbon particles. It is conceivable to arrange this electric heater on the inlet side end face of the filter member.
本発明の課題は、フイルタ部材とヒータ線との
組合せに際して簡便な製造方法により確実なヒー
タ線の保持とヒータ線とフイルタ部材との一体化
構成が具備できる製造方法を提供しようとするも
のである。 An object of the present invention is to provide a manufacturing method that can securely hold the heater wire and provide an integrated configuration of the heater wire and filter member using a simple manufacturing method when combining a filter member and a heater wire. .
本発明はかかる課題を達成するために、燃焼に
より焼失し、ハニカム形態を有する多孔質有機材
料成形体にセラミツクスラリーを含浸する工程
と、燃焼により焼失する円筒形態の2つの多孔質
有機材料成形体にセラミツクスラリーを含浸する
工程と、前記セラミツクスラリーと同一組成のセ
ラミツクスラリーが含浸された前記円筒形態の2
つの多孔質有機材料成形体の間に電気ヒータ線を
挾持する工程と、前記セラミツクスラリーが含浸
された前記ハニカム形態の成形体の端面に前記電
気ヒータ線を間に挾持した前記成形体を圧接した
状態で焼成する工程と、を具備し、前記焼成工程
により、多孔質セラミツクハニカムフイルタ部材
の端面に、内部に前記ヒータ線を内蔵した多孔質
セラミツクプリフイルタ部材を一体化するという
手段を採用したものである。 In order to achieve the above object, the present invention includes a step of impregnating a ceramic slurry into a porous organic material molded body that is burnt out by combustion and has a honeycomb shape, and a process of impregnating a ceramic slurry into a porous organic material molded body that is burnt out by combustion and has a cylindrical shape. a step of impregnating a ceramic slurry with a ceramic slurry;
a step of sandwiching an electric heater wire between two porous organic material molded bodies; and a step of pressing the molded body with the electric heater wire sandwiched therebetween onto an end surface of the honeycomb-shaped molded body impregnated with the ceramic slurry. and a step of firing the porous ceramic honeycomb filter member in the state, and by the firing step, the porous ceramic prefilter member having the heater wire built therein is integrated with the end face of the porous ceramic honeycomb filter member. It is.
以下、本発明を図示の実施例に従つて説明す
る。 Hereinafter, the present invention will be explained according to illustrated embodiments.
第1図において、本発明に係る微粒子捕集装置
Aは内燃機関特にデイーゼル機関1の排気集合管
2に接続される。この装置Aは排気集合室2に連
通する排気ガス流入口3a及び同流出口3bを持
つた金属製の容器3を具備し、その内部に微粒子
捕集用のハニカム構造のフイルタ部材4と、この
フイルタ部材4の排気ガス入口側端面に結合した
電気ヒータ5とを有する。電気ヒータ5はフイル
タ部材4に捕集された微粒子燃焼させてフイルタ
部材4を再生するためのもので、バツテリ6によ
る通電が制御回路7により制御される。制御回路
7には、フイルタ部材4の圧力損失を測定する差
圧センサ8からの信号及び機関の回転数を検出す
る回転センサ9からの信号が入力される。 In FIG. 1, a particulate collector A according to the present invention is connected to an exhaust manifold pipe 2 of an internal combustion engine, particularly a diesel engine 1. In FIG. This device A is equipped with a metal container 3 having an exhaust gas inlet 3a and an exhaust gas outlet 3b communicating with an exhaust gas collecting chamber 2. Inside the container 3, there is a filter member 4 having a honeycomb structure for collecting particulates. It has an electric heater 5 coupled to an end surface of the filter member 4 on the exhaust gas inlet side. The electric heater 5 is used to regenerate the filter member 4 by burning the particulates collected in the filter member 4, and energization by the battery 6 is controlled by a control circuit 7. A signal from a differential pressure sensor 8 that measures the pressure loss of the filter member 4 and a signal from a rotation sensor 9 that detects the engine speed are input to the control circuit 7.
機関1からの排気ガスは流入口3aから捕集装
置Aの容器3内に流入し、フイルタ部材10,4
を通過して流出口3bより流出する。排気ガスが
フイルタ部材10,4を通過する際、同排気ガス
中のカーボン微粒子はフイルタ部材4,10に捕
集され、除去される。 Exhaust gas from the engine 1 flows into the container 3 of the collection device A from the inlet 3a, and passes through the filter members 10, 4.
and flows out from the outlet 3b. When the exhaust gas passes through the filter members 10, 4, carbon particles in the exhaust gas are collected by the filter members 4, 10 and removed.
微粒子の捕集が進んで特にフイルタ部材4の通
気抵抗が増大すると、差圧センサ8がそれに応じ
た信号を出す。差圧センサ8が検知するフイルタ
部材4の上流側、下流側の圧力差は機関回転数に
依存しても変化する。そこでセンサ回路7は差圧
センサ8からの信号と回転数センサ9からの信号
とから、フイルタ部材4の真の通気抵抗、すなわ
ち微粒子の捕集密度を求め、それば所定量に達す
ると、電気ヒータ5への通電を開始する。これに
よりヒータ5は赤熱し、微粒子(カーボンを主体
とする)を燃焼し得る温度まで温度上昇する。 As the collection of particulates progresses and the ventilation resistance of the filter member 4 increases, the differential pressure sensor 8 outputs a corresponding signal. The pressure difference between the upstream side and the downstream side of the filter member 4 detected by the differential pressure sensor 8 also changes depending on the engine speed. Therefore, the sensor circuit 7 calculates the true ventilation resistance of the filter member 4, that is, the collection density of particulates, from the signal from the differential pressure sensor 8 and the signal from the rotation speed sensor 9. Start energizing the heater 5. As a result, the heater 5 becomes red hot and the temperature rises to a temperature at which fine particles (mainly carbon) can be burned.
この電気ヒータ5の赤熱化により、微粒子は加
熱され、燃焼する。燃焼は電気ヒータ5の挿着部
分から始まり、排気ガス上流側へ燃焼が拡大する
と共に、排気ガスの流れに沿つて発熱した熱量が
排気ガス下流側へ伝達されるので、排気ガス下流
側へ効率良く燃焼が拡大する。よつて電気ヒータ
5を上流側端面近傍の微粒子密度が最大なる位
置、即ちプリフイルタ部材10の内部に配置して
おけば、着火が容易になると共にフイルタ部材4
の全域に渡つて効率良く燃焼を拡大し、捕集され
た微粒子を除去することができる。この微粒子の
除去によりフイルタ部材4が再生され、通気抵抗
が低減すると、ヒータ5への通電は停止される。
勿論プリフイルタ部材10の微粒子も除去され
る。 As the electric heater 5 becomes red hot, the fine particles are heated and burned. Combustion starts from the insertion part of the electric heater 5, and the combustion expands to the upstream side of the exhaust gas, and the amount of heat generated along the flow of the exhaust gas is transmitted to the downstream side of the exhaust gas, so that efficiency is increased to the downstream side of the exhaust gas. The combustion expands well. Therefore, if the electric heater 5 is placed at a position near the upstream end face where the particle density is maximum, that is, inside the prefilter member 10, ignition becomes easier and the filter member 4
It is possible to efficiently spread combustion over the entire area and remove the collected particulates. When the filter member 4 is regenerated by removing the fine particles and the ventilation resistance is reduced, the power supply to the heater 5 is stopped.
Of course, fine particles in the prefilter member 10 are also removed.
本発明では、電気ヒータ5をプリフイルタ部材
10の内側に配置しているので、ヒータ5の加熱
時における放射損失等の熱損失が少ない。この結
果、少ない電力でフイルタ部材10,4を再生す
ることができる。また、電気ヒータ5をプリフイ
ルタ部材10に捕集された微粒子密度が最大にな
る位置に配置しているので着火及び燃焼の効率が
良い。また、電気ヒータ5は、プリフイルタ部材
10の内部に完全に固定されているので機械的強
度を大きくすることもできる。 In the present invention, since the electric heater 5 is arranged inside the prefilter member 10, there is little heat loss such as radiation loss when the heater 5 is heated. As a result, the filter members 10 and 4 can be regenerated with less electric power. Further, since the electric heater 5 is arranged at a position where the density of particulates collected by the prefilter member 10 is maximum, ignition and combustion efficiency is good. Furthermore, since the electric heater 5 is completely fixed inside the prefilter member 10, its mechanical strength can also be increased.
次に、本発明装置の具体的構成を、いくつかの
実施例に基づき説明する。 Next, the specific configuration of the device of the present invention will be explained based on some examples.
第1実施例を示す第2図〜第5図において金属
製容器は第2図のごとく2つの容器部片30,3
0aの端部どうしをプレスでかしめ付けることに
より構成された2分割型で、断面の形状は、オー
バル形又は円形をしている。この容器3の喨々
端、下流端は絞られて排気ガスの流入口3a、流
出口3bをそれぞれ構成する。 In FIGS. 2 to 5 showing the first embodiment, the metal container has two container pieces 30 and 3 as shown in FIG.
It is a two-part type constructed by caulking the ends of 0a together with a press, and the cross-sectional shape is oval or circular. The plump end and downstream end of this container 3 are constricted to form an inlet 3a and an outlet 3b for exhaust gas, respectively.
上記容器3の内側には熱的クツシヨン材として
の耐熱性を有する金属製ワイヤネツト31が配設
され、ハニカムフイルタ部材4およびプリフイル
タ部材10がその内側に配設される。フイルタ部
材4は3次元網目状の骨格を有した多孔質セラミ
ツクのハニカム構造、またプリフイルタ部材10
も同様の骨格を有した多孔質セラミツクからなつ
ていて、両部材4,10の10の側外周は、目の
細かい多孔質セラミツクよりなる強度部材43で
おおわれ、保護されている。 A metal wire net 31 having heat resistance as a thermal cushion material is disposed inside the container 3, and a honeycomb filter member 4 and a prefilter member 10 are disposed inside thereof. The filter member 4 has a porous ceramic honeycomb structure having a three-dimensional mesh skeleton, and the prefilter member 10
is also made of porous ceramic having a similar skeleton, and the outer periphery of both members 4 and 10 on the 10 side is covered and protected by a strength member 43 made of fine porous ceramic.
上記フイルタ部材4は容器3の内面に固定され
た固定板32と当接して、下流側への移動が素子
される。ワイヤネツト31と固定板32との間に
は耐熱性のシール部材33が配設され、排気ガス
の全てがフイルタ部材4,10の内部を通過する
ようになされる。フイルタ部材10は2つのフイ
ルタ部材101,102より構成してあり、この
両フイルタ部101,102の間に前記電気ヒー
タ5が挾持固定してある。また、このフイルタ部
材10は前記ハニカムフイルタ部材4の入口側端
面に一体的に接合させてある。 The filter member 4 comes into contact with a fixing plate 32 fixed to the inner surface of the container 3, and is moved downstream. A heat-resistant seal member 33 is disposed between the wire net 31 and the fixed plate 32 so that all of the exhaust gas passes through the inside of the filter members 4 and 10. The filter member 10 is composed of two filter members 101 and 102, and the electric heater 5 is sandwiched and fixed between the two filter parts 101 and 102. Further, this filter member 10 is integrally joined to the inlet side end surface of the honeycomb filter member 4.
フイルタ部101,102の多孔質セラミツク
の目の粗さの程度は、これらの軸方向長さ、横断
面積を考慮し、カーボン微粒子が捕集され、しか
も通気抵抗が極度に大きくならないように適切に
選定され得る。一般には5メツシユ〜17メツシユ
程度が使用されるが、必ずしもこの範囲に限定さ
れない。 The degree of roughness of the porous ceramics of the filter parts 101 and 102 should be determined appropriately, taking into consideration their axial length and cross-sectional area, so that fine carbon particles can be collected and the ventilation resistance will not become extremely large. Can be selected. Generally, about 5 meshes to 17 meshes are used, but the number is not necessarily limited to this range.
第6図は、本実施例で使用したフイルタ部10
1,102(直径12cm円柱状、目の粗さ13メツシ
ユ)におけるカーボン微粒子捕集密度の長さ方向
の変化の様子を示すグラフである。これによれ
ば、上流側端面より長さ方向10mmの位置でカーボ
ン捕集密度が最大になつていることが分る。これ
は、フイルタ部101,102の目の粗さに依存
し5メツシユ〜20メツシユのとき30mm〜3mmであ
る。このように、カーボンの捕集密度が最大にな
る位置をフイルタ部101,102の目の粗さに
応じて、実験により決定することができ、最大密
度を示す位置(フイルタ部材10の入口3mm〜30
mmの間)に、電気ヒータ5が配置されるようにフ
イルタ部材の厚さを選定すれば良い。例えばフイ
ルタ部材10の目の粗が20メツシユのときは約3
mm、フイルタ部材10目の粗さが8メツシユのと
きは約10mmに、フイルタ部材10の目の粗さが5
メツシユのときは約30mmに選定すれば良い。従つ
て、この数値を満足するよいに、フイルタ部材1
0を構成するフイルタ部101,102の軸方向
長さ、目の粗さを選定すればよい。また、プリフ
イルタ部材10の軸方向長さはハニカムフイルタ
部材4との通気抵抗の関係で決められるが、ハニ
カムフイルタ部材4の軸方向長さに対して1/3程
度が好ましい。 FIG. 6 shows the filter section 10 used in this example.
1,102 (cylindrical shape with a diameter of 12 cm, mesh roughness of 13 mesh) showing the change in the carbon particulate collection density in the length direction. According to this, it can be seen that the carbon collection density is maximum at a position 10 mm in the length direction from the upstream end face. This depends on the coarseness of the filter portions 101 and 102, and is 30 mm to 3 mm when there are 5 to 20 meshes. In this way, the position where the carbon collection density is maximum can be determined by experiment according to the coarseness of the filter parts 101 and 102, and the position showing the maximum density (from 3 mm to the entrance of the filter member 10) can be determined by experiment. 30
The thickness of the filter member may be selected such that the electric heater 5 is placed between For example, when the coarseness of the filter member 10 is 20 meshes, approximately 3
mm, when the coarseness of the 10th mesh of the filter member is 8 mesh, it is approximately 10mm, and the coarseness of the 10th mesh of the filter member is 5 mm.
When using mesh, select approximately 30mm. Therefore, the filter member 1 that satisfies this value should be
The axial length and mesh coarseness of the filter portions 101 and 102 constituting 0 may be selected. Further, the axial length of the prefilter member 10 is determined depending on the relationship between the honeycomb filter member 4 and the ventilation resistance, but it is preferably about 1/3 of the axial length of the honeycomb filter member 4.
前記電気ヒータ5のヒータ線5a両端はフイル
タ部材10を貫通するよいにして端子部50のタ
ーミナル51,52に接続され、これを介して制
御回路7(第1図)と接続される。ヒータ線5a
の両端部は、その際、小さな輪をなすよう曲げら
れて応力吸収部5bが設けられ、振動等によつて
もヒータ線5a及びそのターミナル51,52と
のせつぞ部が断線しないようにされる。端子部5
0においては、第3図に示す通り、基体53が容
器3の外面上に溶接により固定され、その内側に
絶縁対54を回してターミナルル51,52が配
設される。そして、絶縁材よりなるパツキン55
が装設され、カバー56がビス57にて基体53
に固定される。 Both ends of the heater wire 5a of the electric heater 5 pass through the filter member 10 and are connected to terminals 51 and 52 of a terminal portion 50, and are connected to the control circuit 7 (FIG. 1) via these terminals. Heater wire 5a
At this time, both ends of the heater wire 5a are bent to form a small ring and provided with stress absorbing portions 5b, so that the grooves between the heater wire 5a and its terminals 51 and 52 are not disconnected even by vibration or the like. Ru. Terminal part 5
0, as shown in FIG. 3, a base body 53 is fixed by welding on the outer surface of the container 3, and terminals 51 and 52 are disposed inside the base body 53 by rotating an insulating pair 54. And packing 55 made of insulating material
is installed, and the cover 56 is attached to the base 53 with screws 57.
Fixed.
上記ハニカムフイルタ部材4は第2図の構造か
ら明白であるが、斜めより見ると第5図の構造を
有している。即ち、両図において、フイルタ部材
4は多数の通路4aが多数の隔壁4bにより隔置
されたハニカム構造を有していて、上記多数の通
路4aの両端は通路の1つ置きに互い違いにして
閉塞してある(第5図では斜線部分が閉塞部)。
従つて、フイルタ部材4内に入つた排気ガスは、
第2図の矢印に示すごとく、隔壁4bを通過す
る。 The honeycomb filter member 4 is obvious from the structure shown in FIG. 2, but when viewed obliquely, it has the structure shown in FIG. 5. That is, in both figures, the filter member 4 has a honeycomb structure in which a large number of passages 4a are separated by a large number of partition walls 4b, and both ends of the large number of passages 4a are alternately closed at every other passage. (In Fig. 5, the shaded area is the closed area).
Therefore, the exhaust gas that has entered the filter member 4 is
As shown by the arrow in FIG. 2, it passes through the partition wall 4b.
次に、上記ハニカムフイルタ部材4,10の製
法について詳細に説明する。まず、ハニカムフイ
ルタ部材4を作る成形型について述べる。 Next, a method for manufacturing the honeycomb filter members 4, 10 will be described in detail. First, a mold for making the honeycomb filter member 4 will be described.
第7図は本発明に使用される成形型容器部を図
示したものであり第7図aは平面図、第7図bは
軸断面図である。成形型容器部20は基盤状に区
画した1つ置きの区画においてその区画面積より
も小さ正方形断面を有する柱状部材21を垂直に
固着した端面22と側壁23とからなり、他の端
面は開口されている。一方、第8図は、本発明に
使用される成形型蓋部を図示したものであり、第
8図aは平面図、第8図bは軸断面図である。成
形型蓋部60は、前記の成形型容器部20と同様
に柱状部材61を垂直に固着した平板蓋62から
なる。柱状部材61の取付位置は、成形型容器部
20において柱状部材61が取付けられてない格
子状区画に取付る。また成形型蓋部60の平板に
は各区画に連通穴63が設けられ、平板の側周に
は連通孔64がもうけられている。そして成形型
容器部20と成形型蓋部60とを組み合わせて成
形型を作成する。第9図は組み合わされた成形型
の軸断面を示したものである。成形型の内部は製
造されるべきハニカム型多孔質セラミツクと同一
形状のキヤビテイ70が形成される。成形型蓋部
60と成形型容器部20との所定の組み合わせが
なされるべく成形型蓋部60の側集に設けた連通
孔64を通してビス80によつて取りはずし自在
に固着される。予め難形剤が内部に塗布された第
9図に示す組合わされた成形型に1つ置きに選択
された連通孔63からウレタンフオーム原料液を
注入する。このとき成形型内部の空気は他の残り
の連通孔63から排出され、ウレタンフオームの
注入を良くしている。 FIG. 7 shows a mold container used in the present invention, with FIG. 7a being a plan view and FIG. 7b being an axial sectional view. The mold container part 20 is composed of an end face 22 and a side wall 23, each of which has a columnar member 21 having a square cross section smaller than the area of the compartment fixed vertically in every other compartment divided into a base shape, and the other end faces are open. ing. On the other hand, FIG. 8 shows a mold lid used in the present invention, with FIG. 8a being a plan view and FIG. 8b being an axial sectional view. The mold lid part 60 is composed of a flat plate lid 62 to which a columnar member 61 is vertically fixed, similar to the mold container part 20 described above. The columnar members 61 are attached to grid-like sections of the mold container section 20 where the columnar members 61 are not attached. Further, a communication hole 63 is provided in each section of the flat plate of the mold lid 60, and a communication hole 64 is provided in the side periphery of the flat plate. Then, a mold is created by combining the mold container part 20 and the mold lid part 60. FIG. 9 shows an axial cross section of the assembled molds. A cavity 70 having the same shape as the honeycomb porous ceramic to be manufactured is formed inside the mold. In order to achieve a predetermined combination of the mold lid 60 and the mold container 20, they are removably fixed with screws 80 through a communication hole 64 provided in the side assembly of the mold lid 60. The urethane foam raw material liquid is injected into the assembled molds shown in FIG. 9, the inside of which has been previously coated with a shape-retarding agent, through communication holes 63 selected every other time. At this time, the air inside the mold is discharged from the remaining communicating holes 63, thereby improving the injection of the urethane foam.
次に上記キヤビテイ70でウレタンフオームを
発泡させて、80℃で15〜60分加熱し硬化させた。
その後に成形型腰部20と成形型蓋部60を取り
はずしてハニカム構造のウレタンフオーム成形を
得る。以上の手段によつて作成したハニカム構造
のウレタンフオーム成形体は三次元網状をなす骨
格間に細胞壁とよばれる薄膜を有するのでこのウ
レタンフオーム成形体を容器中に設置し可燃性ガ
スと空気又は酸素を導入してこれに火花点火し細
胞壁を燃焼させて除去した。次に燃成によりコー
ジエライト組成となるMgO,Al2O3,AiO2を含
む粉末と水とポリビニルアルコールとを混合撹拌
したセラミツクスラリーの中に前記成形体を浸漬
し、余分なスラリーを除いた後、100〜120℃で加
熱乾燥させ、この浸漬、乾燥を数回繰り返した。 Next, the urethane foam was foamed in the cavity 70 and cured by heating at 80° C. for 15 to 60 minutes.
Thereafter, the mold waist portion 20 and mold lid portion 60 are removed to obtain a honeycomb structured urethane foam. The urethane foam molded body with a honeycomb structure created by the above method has a thin film called a cell wall between the skeletons forming a three-dimensional network, so this urethane foam molded body is placed in a container and is used to absorb flammable gas and air or oxygen. was introduced and a spark was ignited to burn the cell wall and remove it. Next, the molded body was immersed in a ceramic slurry made by mixing and stirring powder containing MgO, Al 2 O 3 , and AiO 2 , which becomes a cordierite composition by combustion, water, and polyvinyl alcohol, and after removing excess slurry. , and then heated and dried at 100 to 120°C, and this immersion and drying process was repeated several times.
一方、細胞壁を除去した円筒形のウレタンフオ
ームを2個用意し、上記ハニカム部材4で説明し
たのと同じセラミツクスラリー中に2個のウレタ
ンフオームを浸漬する。余分なスラリーを除いた
後、100〜120℃で加熱乾燥させ、この浸漬、乾燥
を数回繰り返した。また、例えばCr21〜23%、
Al5.3〜5.7%、残部Feよりなる螺旋状に巻回した
ヒータ線を用意し、このヒータ線を上記スラリー
を付着させた上記ウレタンフオームの間に挾持す
る。 On the other hand, two cylindrical urethane foams with cell walls removed are prepared, and the two urethane foams are immersed in the same ceramic slurry as described for the honeycomb member 4 above. After removing excess slurry, it was heated and dried at 100 to 120°C, and this immersion and drying process was repeated several times. Also, for example, Cr21-23%,
A spirally wound heater wire made of 5.3 to 5.7% Al and the balance Fe is prepared, and this heater wire is sandwiched between the urethane foams to which the slurry is adhered.
次に、前述した、スラリー含浸のハニカム構造
ウレタンフオームに上述の、ヒータ線を間に挾持
したスラリー含浸のウレタンフオームを圧接した
状態で1300〜1470℃で2〜6時間焼成した。 Next, the slurry-impregnated urethane foam with the heater wire sandwiched therebetween was pressed against the slurry-impregnated honeycomb structure urethane foam and fired at 1300 to 1470°C for 2 to 6 hours.
これにより、第2図に示したごとく、フイルタ
部材4,10が一体構造となる。勿論、フイルタ
部材10のフイルタ部101,102も間にヒー
タ線5aを挾持した状態で互いに一体構造とな
る。これらフイルタ部材4,10を構成する多孔
質セラミツクスは第4図に示す三次元網目状の骨
格を有している。なお、ハニカムフイルタ部材4
において、前述のウレタン材料の発泡時に材料が
容器部20、蓋部60の内面に圧接してフオーム
の目がつぶれたり、あるいは目が極めて微細とな
るので、前記閉塞部4cは充分な目詰り状態とな
る。 Thereby, as shown in FIG. 2, the filter members 4 and 10 have an integral structure. Of course, the filter parts 101 and 102 of the filter member 10 also have an integral structure with the heater wire 5a sandwiched between them. The porous ceramics constituting these filter members 4, 10 have a three-dimensional mesh-like skeleton as shown in FIG. Note that the honeycomb filter member 4
In this case, when the urethane material is foamed, the material comes into pressure contact with the inner surfaces of the container section 20 and the lid section 60, causing the foam to collapse or become extremely fine, so that the closing section 4c is sufficiently clogged. becomes.
次に、第2図を用いて本発明装置の作動を説明
する。デイーゼル機関(第1図参照)より排出さ
れた排気ガスはフイルタ部材10のフイルタ部1
01,102を通過する。つまり、両フイルタ部
101,102を構成する多孔質セラミツクの三
次元網目状骨格間に形成される空間(第4図参
照)を排気ガスが通過するのである。 Next, the operation of the apparatus of the present invention will be explained using FIG. The exhaust gas discharged from the diesel engine (see Fig. 1) is filtered through the filter section 1 of the filter member 10.
Pass through 01,102. In other words, the exhaust gas passes through the space (see FIG. 4) formed between the three-dimensional mesh frameworks of the porous ceramics that constitute both filter sections 101 and 102.
そして、このフイルタ部材10を通過した排気
ガスはハニカムフイルタ部材4の多数の通路4a
に入り、隔壁4bを経て隣接する他の通路4aに
流出していく。隔壁4bは第4図の構造を有して
おり、排気ガスは上記フイルタ部101,102
と同様に三次元網目状骨格間の空間を通過するの
である。 The exhaust gas that has passed through this filter member 10 is then transferred to a large number of passages 4a of the honeycomb filter member 4.
The liquid enters the air passageway 4b and flows out into another adjacent passage 4a via the partition wall 4b. The partition wall 4b has the structure shown in FIG. 4, and the exhaust gas passes through the filter sections 101 and 102.
Similarly, it passes through the space between the three-dimensional mesh skeletons.
排気ガス中のカーボン微粒子は格フイルタ部材
4,10の多孔質セラミツクの三次元網目状の骨
格上に衝突して骨格上に捕捉される。 The carbon particles in the exhaust gas collide with the three-dimensional mesh skeleton of the porous ceramic of the filter members 4 and 10 and are captured on the skeleton.
第6図に示したようにフイルタ部材10の内部
で捕集されたカーボン微粒子の密度が最大とな
る。そして、この密度が最大となる位置に電気ヒ
ータ5を配置しているため、再生に際して電気ヒ
ータ5に通電すればカーボン微粒子の密度の最大
の領域がまず最小に着火、燃焼し、これを火種と
して下流側に捕集されたカーボン微粒子が燃焼す
る。従つて、効率的に、捕集されたカーボン微粒
子を焼失し、除去することができるのである。 As shown in FIG. 6, the density of the carbon particles collected inside the filter member 10 becomes maximum. Since the electric heater 5 is arranged at the position where this density is maximum, when the electric heater 5 is energized during regeneration, the area with the highest density of carbon particles will first ignite and burn, and this will be used as a spark. The carbon particles collected on the downstream side are burned. Therefore, the collected carbon particles can be efficiently burned out and removed.
また、上記したハニカムフイルタ部材4の隔壁
4bは、上述のように三次元網目状骨格の間に形
成された空間が通孔となるので、通気抵抗は小さ
く圧力損失を低減できる。ちなみに、従来のハニ
カム構造フイルタ部材と前記実施例のハニカムフ
イルタ部材とをカーボン微粒子の捕集効率45%と
一定にして比較した場合、従来例は90〜100mmHg
の圧力損失であるのに対し、前記実施例では45〜
50mmHgと1/2の圧力損失ですむ。 Further, in the partition walls 4b of the honeycomb filter member 4, the spaces formed between the three-dimensional network skeletons serve as through holes as described above, so that the ventilation resistance is small and the pressure loss can be reduced. By the way, when comparing the conventional honeycomb structured filter member and the honeycomb filter member of the above example, the conventional example has a carbon particulate collection efficiency of 90 to 100 mmHg.
While the pressure loss in the above example is 45~
The pressure loss is only 50mmHg and 1/2.
なお、本発明は上述の実施例に限定されず、次
のような種々の変更が可能である。 It should be noted that the present invention is not limited to the above-described embodiments, and various modifications as described below are possible.
(1) 第10図のごとく、フイルタ部材10は一層
構造でもよい。(1) As shown in FIG. 10, the filter member 10 may have a single layer structure.
(2) ハニカムフイルタ部材4とフイルタ部材10
とを予め独立に製作した後、両者をセラミツク
接着剤により接着し焼成するようにしても勿論
よい。(2) Honeycomb filter member 4 and filter member 10
Of course, the two may be manufactured independently in advance, and then both may be bonded with a ceramic adhesive and fired.
(3) フイルタ部材10は一般のハニカム構造とし
てもよい。(3) The filter member 10 may have a general honeycomb structure.
(4) 電気ヒータ5の材質はSiC,MoSi2,TiC−
Al2O3系、TiC−TiN−Al2O3系、TiN−Al2O3
系などのセラミツク質のものでもよい。また、
前記実施例以外の他の金属材料の電気ヒータを
用いてもよい。(4) The material of the electric heater 5 is SiC, MoSi 2 , TiC−
Al 2 O 3 system, TiC-TiN-Al 2 O 3 system, TiN-Al 2 O 3
Ceramic materials such as ceramics may also be used. Also,
Electric heaters made of metal materials other than those used in the above embodiments may also be used.
(5) 各フイルタ部材4,10の材質もコージエラ
イトに限らず、種々のセラミツク材料を用いる
ことができる。(5) The material of each filter member 4, 10 is not limited to cordierite, and various ceramic materials can be used.
フイルタ部材とプリフイルタ部材とを両者のセ
ラミツク材料により組織的に一体構造とすること
ができ、従つて熱膨張による両者間の剥離を回避
することが可能となりり、プリフイルタ部材のヒ
ータ線による熱を確実にフイルタ部材側に伝達で
きるので、補集された微粒子の燃焼良好に達成で
きる。 The filter member and the pre-filter member can be structurally integrated with each other due to their ceramic materials, making it possible to avoid separation between them due to thermal expansion, and ensuring that the heat generated by the heater wire of the pre-filter member is absorbed. Since the particles can be transmitted to the filter member side, the collected particulates can be burnt efficiently.
ヒータ線はプリフイルタ部材の内部にて確実に
保持されるため、ヒータ線がそのプリフイルタ部
材の内部で移動することがなく、ヒータ線の断線
を抑制できる。 Since the heater wire is reliably held inside the prefilter member, the heater wire does not move inside the prefilter member, and breakage of the heater wire can be suppressed.
フイルタ部材とプリフイルタ部材との一体化工
程でヒータ線のプリフイルタ部材への保持が同時
に達成できるから、後工程によつてヒータ線をプ
リフイルタ部材の内部に配置する必要がなく、従
つて製造工程の簡略化を達成することができる。 Since the heater wire can be held in the prefilter member at the same time in the process of integrating the filter member and the prefilter member, there is no need to arrange the heater wire inside the prefilter member in a subsequent process, which simplifies the manufacturing process. can be achieved.
第1図は本発明の微粒子捕集装置の取付位置を
示す部分破断面図、第2図に本発明装置の一実施
例を示す断面図、第3図は第2図の電気ヒータの
端子構造を示す断面図、第4図は第2図のフイル
タ部材4,10の組織を示す斜視図、第5図は第
2図のハニカムフイルタ部材4を示す斜視図、第
6図は本発明の一実施例における作用説明に供す
る特性図、第7図a,bおよび第8図a,bは第
2図のハニカムフイルタ部材4の製造に用いる型
を示すもので、各図aは平面図、各図bは各図
aX−X、Y−Y断面図、第9図は第7,8図の
型を組合せた状態を示す断面図、第10図は本発
明の他の実施例を示す断面図である。
4……ハニカムフイルタ部材、4a……通路、
4b……隔壁、4c……閉塞部、5……電気ヒー
タ、10……フイルタ部材。
Fig. 1 is a partially broken sectional view showing the mounting position of the particle collection device of the present invention, Fig. 2 is a sectional view showing an embodiment of the device of the present invention, and Fig. 3 is the terminal structure of the electric heater of Fig. 2. FIG. 4 is a perspective view showing the organization of the filter members 4 and 10 in FIG. 2, FIG. 5 is a perspective view showing the honeycomb filter member 4 in FIG. Characteristic diagrams of FIGS. 7a and 7b and FIGS. 8a and 8b, used to explain the operation in the embodiment, show the mold used for manufacturing the honeycomb filter member 4 shown in FIG. Figure b is each figure
9 is a sectional view showing a combination of the molds shown in FIGS. 7 and 8, and FIG. 10 is a sectional view showing another embodiment of the present invention. 4... honeycomb filter member, 4a... passage,
4b...Partition wall, 4c...Closing portion, 5...Electric heater, 10...Filter member.
Claims (1)
孔質有機材料成形体にセラミツクスラリーを含浸
する工程と、燃焼により焼失する円筒形態の2つ
の多孔質有機材料成形体にセラミツクスラリーを
含浸する工程と、前記セラミツクスラリーと同一
組成のセラミツクスラリーが含浸された前記円筒
形態の2つの多孔質有機材料成形体の間に電気ヒ
ータ線を挾持する工程と、前記セラミツクスラリ
ーが含浸された前記ハニカム形態の成形体の端面
に前記電気ヒータ線を間に挾持した前記成形体を
圧接した状態で焼成する工程と、を具備し、前記
焼成工程により、多孔質セラミツクハニカムフイ
ルタ部材の端面に、内部に前記ヒータ線を内蔵し
た多孔質セラミツクプリフイルタ部材を一体化し
たことを特徴とする内燃機関の微粒子補集用セラ
ミツク部材の製造方法。1. A step of impregnating a ceramic slurry into a porous organic material molded body having a honeycomb shape that is burnt out by combustion; a step of impregnating a ceramic slurry into two cylindrical shaped porous organic material molded bodies that are burnt out by combustion; sandwiching an electric heater wire between the two cylindrical porous organic material molded bodies impregnated with a ceramic slurry having the same composition as the ceramic slurry; a step of firing the molded body with the electric heater wire sandwiched between the ends thereof in pressure contact, and the firing step incorporates the heater wire inside the end surface of the porous ceramic honeycomb filter member. 1. A method for manufacturing a ceramic member for collecting particulates in an internal combustion engine, characterized by integrating a porous ceramic prefilter member.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57110948A JPS59520A (en) | 1982-06-28 | 1982-06-28 | Fine grain arresting device for internal-combustion engine |
| US06/725,510 US4662911A (en) | 1982-03-18 | 1985-04-22 | Equipment for trapping particulates in engine exhaust gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57110948A JPS59520A (en) | 1982-06-28 | 1982-06-28 | Fine grain arresting device for internal-combustion engine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59520A JPS59520A (en) | 1984-01-05 |
| JPH0424531B2 true JPH0424531B2 (en) | 1992-04-27 |
Family
ID=14548599
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57110948A Granted JPS59520A (en) | 1982-03-18 | 1982-06-28 | Fine grain arresting device for internal-combustion engine |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59520A (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4744216A (en) * | 1986-10-20 | 1988-05-17 | Ford Motor Company | Electrical ignition device for regeneration of a particulate trap |
| JPS63140112U (en) * | 1987-03-06 | 1988-09-14 | ||
| JPH0643452Y2 (en) * | 1988-02-08 | 1994-11-14 | 株式会社三五 | Silencer |
| JPH0737386B2 (en) * | 1988-10-12 | 1995-04-26 | 参天製薬株式会社 | Suspension type pyrenoxine eye drops |
| JPH0913946A (en) * | 1995-06-28 | 1997-01-14 | Mitsubishi Heavy Ind Ltd | Exhaust gas purifying device with black smoke removing device |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS56103618U (en) * | 1980-01-07 | 1981-08-13 | ||
| JPS57198309A (en) * | 1981-05-29 | 1982-12-04 | Nippon Soken Inc | Removing apparatus for particles in internal-combustion engine |
-
1982
- 1982-06-28 JP JP57110948A patent/JPS59520A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59520A (en) | 1984-01-05 |
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