JPS6159361B2 - - Google Patents
Info
- Publication number
- JPS6159361B2 JPS6159361B2 JP13205780A JP13205780A JPS6159361B2 JP S6159361 B2 JPS6159361 B2 JP S6159361B2 JP 13205780 A JP13205780 A JP 13205780A JP 13205780 A JP13205780 A JP 13205780A JP S6159361 B2 JPS6159361 B2 JP S6159361B2
- Authority
- JP
- Japan
- Prior art keywords
- honeycomb
- metal
- shaped
- less
- powder
- 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
Links
- 239000000843 powder Substances 0.000 claims description 33
- 239000002184 metal Substances 0.000 claims description 32
- 229910052751 metal Inorganic materials 0.000 claims description 32
- 238000001125 extrusion Methods 0.000 claims description 29
- 238000005245 sintering Methods 0.000 claims description 14
- 239000002245 particle Substances 0.000 claims description 13
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 8
- 238000004519 manufacturing process Methods 0.000 claims description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 7
- 239000008119 colloidal silica Substances 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 7
- 239000000126 substance Substances 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 3
- 230000001590 oxidative effect Effects 0.000 claims description 3
- 230000004913 activation Effects 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims description 2
- 239000002923 metal particle Substances 0.000 claims 1
- 241000264877 Hippospongia communis Species 0.000 description 9
- 239000003054 catalyst Substances 0.000 description 6
- 239000000047 product Substances 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- 239000011230 binding agent Substances 0.000 description 3
- 239000000919 ceramic Substances 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 229910018626 Al(OH) Inorganic materials 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 239000000969 carrier Substances 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 239000011162 core material Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 229910010272 inorganic material Inorganic materials 0.000 description 2
- 239000011147 inorganic material Substances 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000000314 lubricant Substances 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 229910000640 Fe alloy Inorganic materials 0.000 description 1
- 206010058109 Hangnail Diseases 0.000 description 1
- 229910002656 O–Si–O Inorganic materials 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 229910002800 Si–O–Al Inorganic materials 0.000 description 1
- 229910002808 Si–O–Si Inorganic materials 0.000 description 1
- 235000021355 Stearic acid Nutrition 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000008094 contradictory effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 235000012438 extruded product Nutrition 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 1
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000008117 stearic acid Substances 0.000 description 1
- 238000005486 sulfidation Methods 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
Landscapes
- Powder Metallurgy (AREA)
Description
本発明は金属を素材とするハニカム状成形体の
製造方法に関するものである。
近年多孔性無機物質の用途開発が急速に展開さ
れ、その形状もペレツト状、ビーズ状、リング状
更にはハニカム状と多岐に亘つている。これらの
形状は、用途に応じて最適のものを選択している
が、特にハニカム状のものは、(1)圧損が小さい、
(2)比表面積が大きい、(3)取り扱い易い、(4)摩耗が
少ない、等の利点を有しているので、触媒担体或
は該担体用心材等の用途において特に重要な役割
を果す様になつてきた。
従来用いられているハニカム状成形体としては
(1) セラミツクスを押出成形したもの
(2) 金属平板と金属波板を積層したもの
が主流を占めている。しかしこれらの成形体では
上記の様な触媒分野における要求特性を十分に満
足しているとは言い難い。即ち触媒担体や該担体
用心材においては、
(A) 多孔質であると共に、コーテイング剤や触媒
の付着性が良好であること
〓〓〓
(B) 強度が十分であつて破壊し難いこと
(C) 化学的に安定であつて触媒活性に影響を及ぼ
さないこと
等の特性が要求されるが、上記(1)のセラミツクス
系担体の場合、強度を満足する為の熱処理条件と
多孔質性を満足する為の熱処理条件が相矛盾し、
又(2)の金属系担体の場合には、コーテイング剤等
の付着性を高める為の複雑な前処理が必要であ
り、夫々改善の余地が多い。
本発明はこの様な事情に着目してなされたもの
であつて、セラミツクスの多孔質性と金属の高強
度性を合わせ持つ様なハニカム状成形体を提供す
べく種々検討を重ね、本発明の構成に到達した。
即ち金属粉を主材料とし、少なくともこれにコロ
イダルシリカ及びコロイダルアルミナのいずれか
一方の酸化物を添加して混練を行ない、これを押
出ダイスから押出してハニカム状成形体を得、乾
燥後焼結するというプロセスを通ることにより、
多孔性のある高強度金属ハニカムを提供すること
ができる様になつた。
本発明において用いる金属粉とは、Fe粉、Al
粉、Cu粉、Ti粉、Zr粉、Ni粉、Cr粉並びに各種
合金粉等を含むものであつて、用途に応じて必要
なものを選択する。尚場合によつてはこれらを組
み合わせて使用することもできる。この様な金属
粉に配合されるコロイダルシリカやコロイダルア
ルミナはバインダーとしての機能を示すが、より
具体的には、Si―O―Si、或はAl―O―Alを基本
とするネツトワーク構造によつて金属粉粒子を保
持して金属骨格を形成すると共に、焼結によつて
金属―O―Si―O或は金属―O―A―Oからな
る複合焼結体を形成するものである。従つてネツ
トワーク構造によつて高強度が与えられると共
に、ネツトワークの間に多数の空隙が形成される
ことになり、多孔質性と高強度を同時に満足させ
るという本発明の目的が見事に達成されることに
なつた。
ところでハニカム状成形体の押出成形を行なう
に当つては、上記の2乃至3成分のみからなる混
練物を用いても良いが、所望により他の成分を配
合することもできる。この様な成分としては、ま
ず滑択剤が挙げられる。滑択剤は押出ノズルにお
ける押出抵抗を下げ成形作業を容易にするための
もので、例えばCMC、ステアリン酸、タルク、
ポリエチレングリコール等が例示される。又更に
他の成分としては燃焼によつて消失する物質、即
ち低分子〜高分子の有機物質が挙げられる。この
様な有機物質は燃焼によつて消失し、その後へ小
空隙を残すことによつて多孔質性を向上するもの
であるから、利用し得べき有機物質の種類につい
ては実際上殆んど無制限であるが、配合量につい
ては、金属粉に対して20重量%(以後単に%と記
述)以下に抑制すべきである。その理由は、20%
を越えた場合焼失による空隙率が過大となり、焼
結中の変形或は焼結後の強度低下を伴なうだけで
なく、押出工程における保形性も低下するからで
ある。
次に金属粉としては、押出ダイスのスリツト厚
さに対して約2/3以下の粒子径を有するもので構
成するのが良い。即ちハニカム状成形体の押出成
形においては、金属粉粒子が互いに押し合う様に
して押出ダイス内を通過するが、上記スリツト厚
さに対して約2/3より大きい粒子を用いた場合、
2個又はそれ以上の粒子が並列又は団子状になつ
てスリツト内に詰まり、茲に目詰りを招くことが
あつた。一方上記各成分を含む混練物の流動性
は、金属粉末の粒度分布、特に小粒径粉末の含有
量に大きく影響されることが分つた。即ちスリツ
ト厚さの約1/2以上の粒子径の金属粉粒子が全金
属粉末に対して20%以下であり、且つスリツト厚
さの約1/5以下の大きさの金属粉粒子が全金属粉
末に対して10%以上存在する様な場合には、押出
シリンダ及び押出ダイス内において良好な流動性
を発揮することが分つた。
押出成形機の機種や押出条件等については本発
明を制限するものではないが、押出速度が5mm/
秒に及ばないときは、ささくれやかすれ等の表面
欠陥を頻発する傾向が強く、5mm/秒以上の押出
速度を得ることが推奨される。但しこの様な速度
を確保する為には、硬化性バインダーの含有量を
高めて混練物を柔かめにすることが望まれるが、
この様な条件下においては、押出速度を高めるに
つれて押出圧力が低下し、押出圧力の低下は押出
成形物の保形性を悪化させ、乾燥終了迄の段階で
ハニカムにおける壁が変形して密着する等の不都
合が生じる。従つて押出ダイスの内面にかかる圧
力を常に90Kg/cm2以上に保持することが望まし
く、この様な条件制御を効果的に行なわせる為に
〓〓〓
は、スクリユー式押出成形機よりもプランジヤー
式押出成形機の方が好ましい。
押出成形の完了した成形品は、これを加温する
ことによつて乾燥し、次にこれを焼結する。焼結
条件殊に焼結温度や焼結時間については別段の制
限を設けないが、焼結雰囲気は次の様な基準に従
つて選択するのが良い。即ち金属粉を単に骨材と
して内在せしめる様なハニカム状成形体、例えば
鉄粉や鉄合金粉を用いる場合には、酸化等による
物性の低下を防止する為に非酸化性雰囲気下での
焼結を行なうことが望まれる。これに対しAl粉
やMg粉を用いる場合は、焼結中或は焼結後の雰
囲気を活性化雰囲気とし、酸化、炭化、窒化、硫
化等によつてハニカム表面の活性化を促進するこ
とにより、それ自身を触媒化したり、或は担体と
して触媒の付着性を改良する様なことが望まれ
る。例えばAl粉末を用いたハニカム状成形体を
非酸化性雰囲気の下で焼結した後、湿潤空気の下
で加熱すると成形体表面のAlがAl(OH)3となつ
て析出し、更にこれを乾燥アルゴン中で加熱する
とAl(OH)3が酸化されてγ―アルミナとなり、
成形体自身が優れた触媒活性を発揮する。
本発明のハニカム状成形体は上記の様にして製
造されるから、金属粉末によつて極めて強固な骨
格が形成されると共に、内部には多数の微小空隙
が残され、高度の多孔質性が発揮される。しかも
製造手段は極めて簡便であり、所期の目的を悉く
達成することができた。尚コロイダルシリカ及
び/又はコロイダルアルミナの配合割合は何ら限
定するものではないが、通常は金属粉末の5〜50
重量%程度であれば良く、ハニカム状成形体の大
きさ、ハニカムセル数、スリツト幅、更には金属
粉の比重等を考慮して適宜決定すればよいことで
ある。
次に本発明の実施例を示す。
第1表に示す組成からなる原料を配合して混練
し、下記の条件で押出成形及び焼結を行なつた。
(1) 押出成形機:100mmφプランジヤー式押出機
(2) 押出圧力 :108Kg/cm2
(3) 押出速度 :25mm/sec
(4) 成形品の大きさ:50mmφ、100セル/m2
(5) 乾燥条件 :107℃×24hrs
(6) 焼結条件
温 度:1128℃
時 間:5hrs
雰囲気:アルゴン
成形性及び焼結製品の物性等は第1表に示す通
りであつた。尚コロイダルシリカやコロイダルア
ルミナの代りに熱軟化性バインダーを用いたもの
は、焼結段階で変形してハニカム構造が崩壊し且
つ多孔性を示さなかつた。また用いたコロイダル
シリカ及びコロイダルアルミナの固形分量は、
夫々25%、20%であつた。
The present invention relates to a method for manufacturing a honeycomb-shaped molded body made of metal. In recent years, the development of applications for porous inorganic materials has progressed rapidly, and the shapes of porous inorganic materials have become diverse, including pellets, beads, rings, and even honeycombs. These shapes are selected to be optimal depending on the application, but honeycomb shapes in particular have (1) low pressure loss;
It has advantages such as (2) large specific surface area, (3) ease of handling, and (4) low wear, so it seems to play a particularly important role in applications such as catalyst carriers and core materials for such carriers. I'm getting used to it. The most commonly used honeycomb-shaped bodies are (1) extruded ceramics, and (2) laminated metal flat plates and corrugated metal plates. However, it cannot be said that these molded bodies fully satisfy the characteristics required in the field of catalysts as described above. In other words, the catalyst carrier and the core material for the carrier must be (A) porous and have good adhesion to the coating agent and catalyst.
(B) It must have sufficient strength and be difficult to break. (C) It must be chemically stable and not affect the catalytic activity. However, in the case of the ceramic carrier mentioned in (1) above, , the heat treatment conditions to satisfy strength and the heat treatment conditions to satisfy porosity are contradictory,
Furthermore, in the case of (2), a metal carrier, a complicated pretreatment is required to enhance the adhesion of a coating agent, etc., and there is a lot of room for improvement in each case. The present invention has been made in view of these circumstances, and after repeated studies to provide a honeycomb-shaped molded body that has both the porosity of ceramics and the high strength of metal, the present invention has been developed. configuration has been reached.
That is, metal powder is used as the main material, at least an oxide of either colloidal silica or colloidal alumina is added thereto, kneaded, extruded through an extrusion die to obtain a honeycomb-shaped molded body, and dried and sintered. By going through the process of
It has now become possible to provide a porous, high-strength metal honeycomb. The metal powder used in the present invention is Fe powder, Al
powder, Cu powder, Ti powder, Zr powder, Ni powder, Cr powder, and various alloy powders, etc., and select the necessary one according to the application. In some cases, these may be used in combination. Colloidal silica and colloidal alumina that are blended into such metal powders function as binders, but more specifically, they can be used for network structures based on Si-O-Si or Al-O-Al. Therefore, the metal powder particles are held to form a metal skeleton, and a composite sintered body made of metal-O-Si-O or metal-O-A-O is formed by sintering. Therefore, the network structure provides high strength and a large number of voids are formed between the networks, successfully achieving the object of the present invention to simultaneously satisfy porosity and high strength. It was decided that it would be done. By the way, when carrying out extrusion molding of a honeycomb-shaped molded body, a kneaded product consisting only of the above two or three components may be used, but other components may also be blended as desired. Examples of such components include lubricants. The lubricant is used to reduce the extrusion resistance in the extrusion nozzle and make the molding process easier, such as CMC, stearic acid, talc,
Examples include polyethylene glycol. Further, other components include substances that disappear by combustion, ie, low-molecular to high-molecular organic substances. Since such organic substances disappear through combustion and improve porosity by leaving small voids behind, there is practically no limit to the types of organic substances that can be used. However, the blending amount should be suppressed to 20% by weight or less (hereinafter simply referred to as %) based on the metal powder. The reason is 20%
This is because if it exceeds the porosity due to burnout, the porosity becomes excessive, which not only causes deformation during sintering or a decrease in strength after sintering, but also reduces shape retention during the extrusion process. Next, it is preferable that the metal powder has a particle diameter that is about 2/3 or less of the slit thickness of the extrusion die. That is, in extrusion molding of a honeycomb shaped body, metal powder particles pass through an extrusion die in such a way that they are pressed against each other, but when particles larger than about 2/3 of the slit thickness are used,
Two or more particles could become stuck in the slit in parallel or in clusters, leading to clogging of the screw. On the other hand, it has been found that the fluidity of the kneaded product containing the above-mentioned components is greatly influenced by the particle size distribution of the metal powder, especially the content of small particle size powder. In other words, metal powder particles with a particle size of about 1/2 or more of the slit thickness account for 20% or less of the total metal powder, and metal powder particles with a size of about 1/5 or less of the slit thickness account for 20% or less of the total metal powder. It has been found that when the amount is 10% or more based on the powder, good fluidity is exhibited in the extrusion cylinder and extrusion die. The present invention is not limited to the extrusion molding machine model, extrusion conditions, etc., but the extrusion speed is 5 mm/
If the extrusion speed is less than 5 mm/sec, there is a strong tendency for surface defects such as hangnails and scratches to occur frequently, so it is recommended to obtain an extrusion speed of 5 mm/sec or more. However, in order to ensure such speed, it is desirable to increase the content of curable binder to make the kneaded material soft.
Under such conditions, as the extrusion speed increases, the extrusion pressure decreases, and the decrease in extrusion pressure deteriorates the shape retention of the extruded product, and the walls of the honeycomb deform and adhere tightly until the end of drying. Such inconveniences may occur. Therefore, it is desirable to always maintain the pressure applied to the inner surface of the extrusion die at 90 kg/cm 2 or more, and in order to effectively control such conditions,
A plunger type extrusion molding machine is preferable to a screw type extrusion molding machine. The molded product that has been extruded is dried by heating, and then sintered. Although there are no particular restrictions on the sintering conditions, especially the sintering temperature and time, the sintering atmosphere is preferably selected in accordance with the following criteria. In other words, when using a honeycomb-shaped molded body in which metal powder is simply incorporated as an aggregate, such as iron powder or iron alloy powder, sintering in a non-oxidizing atmosphere is necessary to prevent deterioration of physical properties due to oxidation, etc. It is desirable to do so. On the other hand, when using Al powder or Mg powder, the atmosphere during or after sintering is made into an activating atmosphere, and the activation of the honeycomb surface is promoted through oxidation, carbonization, nitridation, sulfidation, etc. It is desired that the catalyst itself be catalyzed or used as a carrier to improve the adhesion of the catalyst. For example, when a honeycomb-shaped molded body using Al powder is sintered in a non-oxidizing atmosphere and then heated in humid air, Al on the surface of the molded body precipitates as Al(OH) 3 . When heated in dry argon, Al(OH) 3 is oxidized to γ-alumina,
The molded body itself exhibits excellent catalytic activity. Since the honeycomb-shaped molded body of the present invention is manufactured as described above, an extremely strong skeleton is formed by the metal powder, and a large number of micro voids are left inside, resulting in a highly porous structure. Demonstrated. Furthermore, the manufacturing method was extremely simple, and all of the intended objectives could be achieved. The blending ratio of colloidal silica and/or colloidal alumina is not limited in any way, but it is usually 5 to 50% of the metal powder.
The amount may be approximately % by weight, and may be appropriately determined in consideration of the size of the honeycomb-shaped molded body, the number of honeycomb cells, the slit width, the specific gravity of the metal powder, etc. Next, examples of the present invention will be shown. Raw materials having the composition shown in Table 1 were blended and kneaded, and extrusion molding and sintering were performed under the following conditions. (1) Extrusion molding machine: 100mmφ plunger type extruder (2) Extrusion pressure: 108Kg/cm 2 (3) Extrusion speed: 25mm/sec (4) Size of molded product: 50mmφ, 100 cells/m 2 (5) Drying conditions: 107°C x 24hrs (6) Sintering conditions: Temperature: 1128°C Time: 5hrs Atmosphere: Argon The formability and physical properties of the sintered product were as shown in Table 1. In addition, when a heat-softening binder was used instead of colloidal silica or colloidal alumina, the honeycomb structure was deformed during the sintering stage and the honeycomb structure collapsed, and no porosity was exhibited. In addition, the solid content of colloidal silica and colloidal alumina used is
They were 25% and 20%, respectively.
【表】
〓〓〓
[Table] 〓〓〓
【表】
第1表に見られる如く本発明で得られるハニカ
ム状成形体では焼結時の変形が無く、優れた多孔
性が発揮された。
〓〓〓
[Table] As shown in Table 1, the honeycomb-shaped molded body obtained by the present invention was not deformed during sintering and exhibited excellent porosity. 〓〓〓
Claims (1)
イダルアルミナを配合した混練物を押出ダイスか
ら押出してハニカム状成形体を得、乾燥後焼結す
ることを特徴とする金属製ハニカム状成形体の製
造方法。 2 特許請求の範囲第1項において、金属粉とし
てその最大粒子径が押出ダイスのスリツト厚さに
対して約2/3以下であり、且つスリツト厚さの約
1/2以上の粒径の粒子が全体の20%以下であり、
更にスリツト厚さの約1/5以下の大きさの金属粒
子を全体の10%以上含むものを用いる金属製ハニ
カム状成形体の製造方法。 3 特許請求の範囲第1又は2項において、押出
ダイスの内面にかかる圧力が90Kg/cm2以上で且つ
ダイス通過時の線速度が5mm/秒以上となる様に
押出す金属製ハニカム状成形体の製造方法。 4 特許請求の範囲第1〜3項のいずれかにおい
て、非酸化性雰囲気の下で焼結を行なう金属製ハ
ニカム状成形体の製造方法。 5 特許請求の範囲第1〜3項のいずれかにおい
て、ハニカム表面の活性化を促進する雰囲気下で
焼結を行なう金属製ハニカム状成形体の製造方
法。 6 特許請求の範囲第1〜5項のいずれかにおい
て、金属粉に、コロイダルシリカ及び/又はコロ
イダルアルミナを配合した混練物として、有機物
質を含有するものを用いる金属製ハニカム状成形
体の製造方法。[Scope of Claims] 1. A metal honeycomb-shaped body, characterized in that a honeycomb-shaped body is obtained by extruding a kneaded mixture of metal powder and colloidal silica and/or colloidal alumina through an extrusion die, which is dried and then sintered. Method for manufacturing a molded object. 2. In claim 1, the maximum particle diameter of the metal powder is about 2/3 or less of the slit thickness of an extrusion die, and about 2/3 or less of the slit thickness of the extrusion die.
Particles with a particle size of 1/2 or more account for 20% or less of the total,
A method for producing a metal honeycomb-shaped molded body using a material containing 10% or more of the total metal particles having a size of about 1/5 or less of the slit thickness. 3. In claim 1 or 2, the metal honeycomb-shaped formed product is extruded so that the pressure applied to the inner surface of the extrusion die is 90 kg/cm 2 or more and the linear velocity when passing through the die is 5 mm/sec or more. manufacturing method. 4. A method for manufacturing a metal honeycomb-shaped molded body according to any one of claims 1 to 3, wherein sintering is performed in a non-oxidizing atmosphere. 5. A method for manufacturing a metal honeycomb-shaped formed body according to any one of claims 1 to 3, wherein sintering is performed in an atmosphere that promotes activation of the honeycomb surface. 6. A method for producing a metal honeycomb-shaped formed body according to any one of claims 1 to 5, using a kneaded product containing colloidal silica and/or colloidal alumina containing an organic substance in metal powder. .
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13205780A JPS5757804A (en) | 1980-09-22 | 1980-09-22 | Production of honeycomb-shaped molding made of metal |
| US06/304,684 US4582677A (en) | 1980-09-22 | 1981-09-22 | Method for producing honeycomb-shaped metal moldings |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13205780A JPS5757804A (en) | 1980-09-22 | 1980-09-22 | Production of honeycomb-shaped molding made of metal |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5757804A JPS5757804A (en) | 1982-04-07 |
| JPS6159361B2 true JPS6159361B2 (en) | 1986-12-16 |
Family
ID=15072502
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13205780A Granted JPS5757804A (en) | 1980-09-22 | 1980-09-22 | Production of honeycomb-shaped molding made of metal |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5757804A (en) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59145703A (en) * | 1983-02-09 | 1984-08-21 | Toyo Tire & Rubber Co Ltd | Sintering method of metallic powder |
| JPS6132307A (en) * | 1984-07-20 | 1986-02-15 | 日立電線株式会社 | Electric wire/cable |
| JPS6132308A (en) * | 1984-07-20 | 1986-02-15 | 日立電線株式会社 | Wire and cable |
| JPS6244506A (en) * | 1985-08-21 | 1987-02-26 | Yoshida Kogyo Kk <Ykk> | Manufacture of porous sintered body of stainless steel powder |
| KR20010081565A (en) * | 2000-02-16 | 2001-08-29 | 박양자 | Method of manufacturing grind stone use for a carbide alloy powder |
| EP2544580B1 (en) | 2010-03-09 | 2021-07-14 | Smart Medical Systems Ltd | Balloon endoscope and methods of manufacture and use thereof |
| CN112932386A (en) | 2011-03-07 | 2021-06-11 | 智能医疗系统有限公司 | Balloon-equipped endoscope device and method thereof |
| PT2999552T (en) | 2013-05-21 | 2018-12-27 | Smart Medical Systems Ltd | Endoscope reprocessing system and method |
| CN107105986B (en) | 2014-12-22 | 2019-11-05 | 智能医疗系统有限公司 | Balloon endoscope reprocessing system and method |
| US10835107B2 (en) | 2015-04-03 | 2020-11-17 | Smart Medical Systems Ltd. | Endoscope electro-pneumatic adaptor |
-
1980
- 1980-09-22 JP JP13205780A patent/JPS5757804A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5757804A (en) | 1982-04-07 |
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