JPH02254106A - Production of inorganic cellular body - Google Patents
Production of inorganic cellular bodyInfo
- Publication number
- JPH02254106A JPH02254106A JP7406589A JP7406589A JPH02254106A JP H02254106 A JPH02254106 A JP H02254106A JP 7406589 A JP7406589 A JP 7406589A JP 7406589 A JP7406589 A JP 7406589A JP H02254106 A JPH02254106 A JP H02254106A
- Authority
- JP
- Japan
- Prior art keywords
- powder
- fine powder
- inorganic
- inorg
- heating
- 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.)
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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
- C04B38/06—Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof by burning-out added substances by burning natural expanding materials or by sublimating or melting out added substances
- C04B38/0615—Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof by burning-out added substances by burning natural expanding materials or by sublimating or melting out added substances the burned-out substance being a monolitic element having approximately the same dimensions as the final article, e.g. a porous polyurethane sheet or a prepreg obtained by bonding together resin particles
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Powder Metallurgy (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、二次元あるいは三次元の無機質多孔体の製造
方法に関する。セラミックス系の無機質多孔体は例えば
溶融金属中の非金属介在物を除去するフィルター等とし
て使用され、また金属系の無機質多孔体は触媒担体エレ
メントとして使用される。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for producing a two-dimensional or three-dimensional inorganic porous body. Ceramic-based inorganic porous bodies are used, for example, as filters for removing non-metallic inclusions from molten metal, and metal-based inorganic porous bodies are used as catalyst carrier elements.
〔従来の技術]
多孔質の有機高分子材料例えばウレタンフオームの骨格
に、無機質微粉末を例えば有機質接着剤と混練して塗着
し、これを加熱すると有機高分子材料の骨格は分解ある
いは蒸発して除去されまた無機質微粉末は例えば焼結し
て、無機質多孔体が得られる。[Prior art] Fine inorganic powder is kneaded with, for example, an organic adhesive and applied to the skeleton of a porous organic polymer material such as urethane foam, and when this is heated, the skeleton of the organic polymer material decomposes or evaporates. The inorganic fine powder is removed by, for example, sintering to obtain an inorganic porous body.
第3図はこの無機質多孔体を製造する方法の加熱におけ
る従来の熱処理温度の例を示す模式図である。図中1と
2の間で有機高分子材料は除去される(脱脂される)が
、この間の昇温速度が大きいと、従来は無機質多孔体に
ワレやふくれが多発するために、例えば1℃/hr〜5
0℃/hrの昇温速度で、極めて緩やかに昇温されてい
た。FIG. 3 is a schematic diagram showing an example of a conventional heat treatment temperature in heating in the method of manufacturing this inorganic porous body. The organic polymer material is removed (degreased) between 1 and 2 in the figure, but if the temperature rise rate during this period is high, cracks and blisters occur frequently in the inorganic porous material, so for example, 1°C /hr~5
The temperature was raised extremely slowly at a temperature increase rate of 0°C/hr.
図中2と3の間は、脱脂後の昇温速度の例で、この間に
無機質微粉末は焼結しあるいは還元されて焼結する。図
中4はこの還元期の例である。The period between 2 and 3 in the figure is an example of the temperature increase rate after degreasing, during which the inorganic fine powder is sintered or reduced and sintered. 4 in the figure is an example of this reduction period.
[発明が解決しようとする課題]
既に述べた如く、従来の方法では第3図の1と2の間の
昇熱速度が極めて緩やかであるため、加熱時間が長く、
従って生産性が低い。[Problems to be Solved by the Invention] As already mentioned, in the conventional method, the heating rate between 1 and 2 in FIG. 3 is extremely slow, so the heating time is long.
Therefore, productivity is low.
第3図で1と2の間の熱処理と、2と3の間の熱処理は
連続炉で連続して行う場合や、別の炉で行う場合がある
が、1と2の間の熱処理時間が長くなり過ぎると、連続
炉の場合も別の炉で行う場合も設備上あるいは工程上好
ましくない。In Figure 3, the heat treatment between 1 and 2 and the heat treatment between 2 and 3 may be performed continuously in a continuous furnace or in separate furnaces, but the heat treatment between 1 and 2 is If it is too long, it is unfavorable in terms of equipment or process, whether in a continuous furnace or in a separate furnace.
本発明は、無機質多孔体にワレやふくれを発生させるこ
とがなく、かつ第3図の1と2の間の熱処理を短時間で
行う事ができる。無機質多孔体の製造方法を提供するも
のである。According to the present invention, the inorganic porous material does not crack or blister, and the heat treatment between 1 and 2 in FIG. 3 can be performed in a short time. A method for producing an inorganic porous body is provided.
[課題を解決するための手段および作用コ本発明は、多
孔質の有機高分子材料の骨格に無機質微粉末を接着剤に
より塗着した後、これを加熱して有機高分子材料を脱脂
し更に無機質微粉末を焼結する方法に関する。[Means and effects for solving the problem] The present invention involves coating the framework of a porous organic polymer material with inorganic fine powder using an adhesive, and then heating the powder to degrease the organic polymer material. This invention relates to a method for sintering inorganic fine powder.
本発明で多孔質の有機高分子材料とは、例えばウレタン
フオームや化学繊維で形成した網や有機質三次元織物(
株式会社有沢製作所製)等をいう。In the present invention, the porous organic polymer material is, for example, a net formed of urethane foam or chemical fiber, or an organic three-dimensional fabric (
manufactured by Arisawa Seisakusho Co., Ltd.), etc.
本発明ではこれ等の多孔質の有機高分子材料の骨格に無
機質微粉末を塗着する。無機質微粉末は、例えばCMC
やリン酸ボンドや水ガラス等の水溶液や他の適当な接着
剤を用いて有機高分子材料の骨格に塗着する。粒径が5
0μ以下の粒子よりなる無機質微粉末は、有機高分子材
料の骨格に塗着させ易い。しかし粒径が1μ以下の粒子
では、塗着した際の粒子間の間隙が小さく、後で述べる
有機高分子材料のガス状の分解生成物の逸散が困難とな
る。無機質微粉末は例えば鉄粉やステンレス鋼粉末の如
き金属粉末であってもよいし、あるいは鉄粉と金属クロ
ム粉とフェロニッケル粉を混合した2種以上の金属の混
合粉末であってもよいし、あるいは例えば鉄粉に炭素粉
を混合した金属粉と非金属粉との混合粉末であってもよ
い。In the present invention, inorganic fine powder is applied to the skeleton of these porous organic polymer materials. The inorganic fine powder is, for example, CMC.
It is applied to the skeleton of an organic polymer material using an aqueous solution such as phosphoric acid bond, water glass, or other suitable adhesive. Particle size is 5
Inorganic fine powder consisting of particles of 0 μm or less can be easily applied to the skeleton of an organic polymer material. However, particles with a particle size of 1 μm or less have small gaps between the particles when applied, making it difficult to dissipate gaseous decomposition products of the organic polymer material, which will be described later. The inorganic fine powder may be a metal powder such as iron powder or stainless steel powder, or it may be a mixed powder of two or more metals such as iron powder, metallic chromium powder, and ferronickel powder. Alternatively, it may be a mixed powder of metal powder and non-metal powder, such as iron powder mixed with carbon powder.
更に無機質微粉末は、酸化鉄粉であってもよいしあるい
は酸化鉄粉と炭素粉末との混合粉末であってもよいし、
あるいは酸化鉄粉や酸化鉄粉と炭素粉末との混合粉末に
、金属クロム粉末の如き合金元素粉末を添加した混合粉
末であってもよい。Further, the inorganic fine powder may be iron oxide powder or a mixed powder of iron oxide powder and carbon powder,
Alternatively, it may be a mixed powder in which alloying element powder such as metal chromium powder is added to iron oxide powder or a mixed powder of iron oxide powder and carbon powder.
例えば酸化鉄粉と炭素粉末との混合粉末よりなる無機質
微粉末は、後で述べる焼結化の加熱過程で酸化鉄粉は炭
素粉末によって還元されて、鋼に相当する成分の無機質
多孔体となるが、本発明の無機質粉末には、この混合粉
末も含まれる。For example, in the case of an inorganic fine powder made of a mixed powder of iron oxide powder and carbon powder, the iron oxide powder is reduced by the carbon powder during the heating process of sintering, which will be described later, and becomes an inorganic porous body with components equivalent to steel. However, the inorganic powder of the present invention also includes this mixed powder.
本発明の無機質微粉末はまた、セラミックス組成の微粉
末あるいは混合微粉末であってもよい。The inorganic fine powder of the present invention may also be a ceramic composition fine powder or mixed fine powder.
セラミックス組成の微粉末としては、例えばAQ zO
z + Zr2O3,ムライト、 SiC,SiN等の
微粉末やこれ等の混合粉末があげられる。またセラミッ
クフェライト多孔体用の微粉末としてFeOにMnO。As the fine powder of ceramic composition, for example, AQ zO
Examples include fine powders such as Z + Zr2O3, mullite, SiC, and SiN, and mixed powders of these. Also, FeO and MnO are used as fine powder for ceramic ferrite porous bodies.
ZnO、MgO等を混合したフェライト組成の微粉末で
あってもよい。A fine powder having a ferrite composition mixed with ZnO, MgO, etc. may also be used.
後で述べる如く本発明では、有機高分子材料の液化開始
温度から該液化開始温度+100℃の間の昇温速度を3
0〜b
質微粉末を用いた場合も、この昇温速度の加熱を行う事
によって、無機質多孔体、にワレやふくれを発生させる
ことはない。As described later, in the present invention, the temperature increase rate from the liquefaction start temperature of the organic polymer material to the liquefaction start temperature +100°C is set to 3.
Even in the case of using a 0-b quality fine powder, heating at this temperature increase rate will not cause cracking or blistering in the inorganic porous body.
本発明では、無機質微粉末を塗着した有機高分子材料を
、有機高分子材料を除去し無機質微粉末を焼結するため
に加熱するが、有機高分子材料の液化開始温度から該液
化開始温度+100℃の間の昇温速度を30〜b
本発明者等は、この加熱における昇温速度を研究して本
発明をなすに至った。第]−図はこの研究結果の例を示
す図である。In the present invention, an organic polymer material coated with an inorganic fine powder is heated in order to remove the organic polymer material and sinter the inorganic fine powder. The temperature increase rate between +100° C. is 30 to b. The present inventors have studied the temperature increase rate in this heating and have arrived at the present invention. Figure 1-1 is a diagram showing an example of the results of this research.
表面酸化鉄粉(C: 4 、5%、 Sj、:0.05
%、 Mn:0.35%。Surface oxidized iron powder (C: 4, 5%, Sj,: 0.05
%, Mn: 0.35%.
Cr : 0 、50%、 P:0.01%、 S:0
.01%、0ニア%)の平均粒径10μの微粉末をCM
C水溶液で混練しスラリー状とし、これをウレタンフオ
ーム(孔径: 3mm 、寸法: ]、000mmX
100mm X 20mm 、液化開始温度=250°
C)の骨格−にに浸漬法で厚さ約1mmに塗着し、10
0℃で乾燥したものを供試材とした。Cr: 0, 50%, P: 0.01%, S: 0
.. 01%, 0near%) fine powder with an average particle size of 10μ is CM
Knead with an aqueous solution of C to make a slurry, which is then made into urethane foam (pore diameter: 3 mm, dimensions: ], 000 mm
100mm x 20mm, liquefaction start temperature = 250°
The skeleton of C) was applied to a thickness of about 1 mm by dipping method, and 10
The sample material was dried at 0°C.
第1図で5は液化開始温度、6は液化開始温度+100
℃、7は焼結開始温度、8は焼結終了温度である。In Figure 1, 5 is the liquefaction start temperature, and 6 is the liquefaction start temperature +100.
℃, 7 is the sintering start temperature, and 8 is the sintering end temperature.
尚図中点線9は、従来の加熱法における昇温速度の上限
である。Note that the dotted line 9 in the figure is the upper limit of the temperature increase rate in the conventional heating method.
本発明者等は、昇温速度が250℃/分以下の範囲で、
各温度の昇温速度が無機質多孔体の焼結製品のワレやふ
くれに及ぼす影響を調査した。The present inventors have determined that within a temperature increase rate of 250°C/min or less,
We investigated the effects of heating rates at various temperatures on cracking and blistering of sintered inorganic porous products.
第1図の第1領域では昇温速度の大小に関わりなく、ワ
レやふくれのない健全な無機質多孔体が得られた。従来
はこの領域も緩やかに昇温しでいたが、この第1領域は
昇温速度が大きくても、焼結後の無機質多孔体には品質
」二の格別の支障はない。この理由は、本発明の製造方
法はII I P rAやSIP法とは異なり、無機質
微粉末を加圧して成形しないで、ウレタンフオーム等に
塗着して成形するため、粒子間の結合が緩やかで熱膨張
代の逃げ場が多く、また供試材が多孔体であるため多孔
体の貫通孔を流通するガス流によって供試材は均一に加
熱されて熱応力も小さいためと考えられる。In the first region of FIG. 1, a healthy inorganic porous material without cracks or blisters was obtained regardless of the temperature increase rate. Conventionally, the temperature in this region also rose slowly, but even if the temperature rise rate in this first region is high, there is no particular problem in the quality of the inorganic porous body after sintering. The reason for this is that unlike the IIIP rA and SIP methods, the manufacturing method of the present invention does not press and mold the inorganic fine powder, but rather coats it on urethane foam and molds it, so the bond between particles is loose. This is thought to be because there is a lot of room for thermal expansion to escape, and because the test material is porous, the test material is uniformly heated by the gas flow flowing through the through-holes of the porous material, resulting in small thermal stress.
第1図の第2領域では、昇温速度が1℃/分以下の極め
て緩やかな昇温速度の場合と、30〜b後の無機質多孔
体にはワレやふくれがなく健全である。しかし1℃/分
超〜30℃/分未満の昇温速度では、焼結後の無機質多
孔体にはワレやふくれが観察される。又201℃/分以
上の極めて早い昇温速度では、多孔体が一部又は全体が
解体してしまう。In the second region of FIG. 1, the inorganic porous body is healthy without cracks or blisters when the temperature increase rate is extremely slow at 1° C./min or less, and after 30 b. However, at a temperature increase rate of more than 1° C./min to less than 30° C./min, cracks and blisters are observed in the inorganic porous body after sintering. Furthermore, if the temperature is increased at an extremely high rate of 201° C./min or more, the porous body will partially or completely disintegrate.
第1図の第2領域では有機高分子材料の骨格の液化や熱
分解が起り、又ガス状の熱分解生成物は無機質微粉末の
粒子の間隙を通って逸散する。In the second region of FIG. 1, liquefaction and thermal decomposition of the skeleton of the organic polymer material occur, and gaseous thermal decomposition products escape through the gaps between the particles of the inorganic fine powder.
昇温速度30℃/分以下ではワレやふくれが発生する理
由は必ずしも明らかではないが、昇温速度が30℃/分
以下では、無機質微粉末で形成された外殻の内部に液化
した有機高分子材料が閉じこめられ外殻を加圧するため
にワレやふくれが発生するものと想考される。又昇温速
度が30℃/分以上ではワレやふくれが発生しない理由
も明らかではないが、昇温速度が30℃Z分以上では、
ガス状の熱分解生成物が無機質微粉末の粒子の間隙を通
って逸散し易く、従って熱分解した有機高分子材料は逐
次逸散して、無機質微粉末で形成された外殻を加圧する
事がなく、ワレやふくれを発生させない。It is not always clear why cracks and blisters occur when the heating rate is 30°C/min or less, but when the heating rate is 30°C/min or less, liquefied organic polymers form inside the outer shell formed of fine inorganic powder. It is thought that cracks and blisters occur because the molecular material is trapped and pressurizes the outer shell. Also, it is not clear why cracks and blisters do not occur when the heating rate is 30°C/min or higher, but when the heating rate is 30°C/min or higher,
The gaseous pyrolysis products tend to dissipate through the gaps between the particles of the inorganic fine powder, so the pyrolyzed organic polymer material gradually dissipates and pressurizes the outer shell formed of the inorganic fine powder. No problem, no cracking or blistering.
201℃/分以上の昇温速度で多孔体の一部が解体する
のは、有機高分子材料が爆発的に発生するものと想考さ
れる。The reason why a part of the porous body disintegrates at a heating rate of 201° C./min or more is considered to be because the organic polymer material is generated explosively.
第1図の第3領域では、供試材のOとCが反応して酸化
鉄は還元される。しかし第3領域では昇温速度が大きい
場合も小さい場合もワレやふくれが発生することはない
。即ち第2領域の昇温速度を30〜b
例えば脱脂や酸化鉄の還元を十分に行わせるために緩や
かに昇温しでも、製品にワレやふくれが発生する事はな
い。従って第3領域の昇温は脱脂や酸化鉄の還元に適し
た条件で行う事ができる。In the third region of FIG. 1, O and C in the sample material react and iron oxide is reduced. However, in the third region, cracks and blisters do not occur regardless of whether the temperature increase rate is high or low. That is, even if the temperature rise rate in the second region is set at 30 to 30b, for example, even if the temperature is raised slowly in order to sufficiently perform degreasing and reduction of iron oxide, the product will not crack or blister. Therefore, the temperature in the third region can be raised under conditions suitable for degreasing and reducing iron oxide.
第3領域でワレやふくれが発生し難い理由は、第1領域
の説明で述べたと同様に、本発明の無機質微粉末は粒子
間の結合が緩やかで熱膨張代の逃げ場が多く、又貫通孔
を有するために均一に加熱されて熱応力も小さいためと
考えられる。The reason why cracks and blisters are less likely to occur in the third region is that, as mentioned in the explanation of the first region, the inorganic fine powder of the present invention has loose bonds between particles and has many places for thermal expansion to escape, and also has through-holes. This is thought to be due to the fact that it is heated uniformly and has low thermal stress.
第1図の第4領域では無機質微粉末が焼結化する。第4
領域においても昇温速度によってワレやふくれが発生す
る事はない。即ち第2領域の昇温を30〜200℃/分
で行う事によって、第4領域の昇温は焼結化に適した条
件で行う事ができる。In the fourth region of FIG. 1, the inorganic fine powder is sintered. Fourth
Even in this area, cracks and blisters do not occur due to the rate of temperature rise. That is, by raising the temperature in the second region at a rate of 30 to 200° C./min, the temperature in the fourth region can be raised under conditions suitable for sintering.
第4領域でワレやふくれが発生しない理由は第3領域で
述べたと同じ理由によると思われる。The reason why cracks and blisters do not occur in the fourth area is believed to be the same as that described in the third area.
以上述べた如く、本発明では、有機高分子材料の液化開
始温度から該液化開始温度+100℃の間の昇温速度を
30〜b
この急激な昇熱を行う事によって、焼結後の無機質多孔
体のワレやふくれは防止できるが、無機質微粉末を塗着
した多孔質の有機高分子材料の各骨格を、まんべんなく
急激に昇温する事は、従来の通電加熱型の熱処理炉やガ
ス焼結型の熱処理炉では容易ではない。As described above, in the present invention, by performing this rapid heating rate from the liquefaction start temperature of the organic polymer material to the liquefaction start temperature +100°C, the inorganic porous material after sintering is Although it is possible to prevent cracking and blistering of the body, it is difficult to uniformly and rapidly raise the temperature of each skeleton of a porous organic polymer material coated with fine inorganic powder using conventional electrical heating type heat treatment furnaces or gas sintering. This is not easy with a type of heat treatment furnace.
本発明者等は誘導加熱炉を用いて、この急激な昇温を行
ったが、何れの骨格にもまんべんなく、制御性のよい急
激な昇温か達成できた。The present inventors performed this rapid temperature increase using an induction heating furnace, and were able to achieve a rapid temperature increase with good controllability evenly over all skeletons.
[実施例1コ
3次元ウレタンフオーム(孔径:1mm、寸法:100
mm X 100+nn+ X 10mm 、液化開始
温度:230℃)にムライト粉末1μ〜45μで85%
構成されるものをリン酸アルミニウム溶液を粘着剤とし
てスプレー法でウレタンフオームの骨格に塗着し、10
0℃X30分間乾燥した後、10KHz誘導炉にて大気
雰囲気で室温から350℃まで100℃/分の高速加熱
後、15分間350℃で脱脂を実施し、その後150℃
/分の高速加熱を行い800℃で3時間焼結したところ
、健全な溶鉄濾過用のセラミックフィルターが出来た。[Example 1 Three-dimensional urethane foam (pore diameter: 1 mm, dimension: 100
mm x 100+nn+
The composition was applied to the urethane foam skeleton by a spray method using aluminum phosphate solution as an adhesive, and
After drying at 0°C for 30 minutes, high-speed heating at 100°C/min from room temperature to 350°C in the air in a 10KHz induction furnace, degreasing at 350°C for 15 minutes, and then at 150°C.
After sintering at 800°C for 3 hours with high-speed heating at a rate of 1/2 min, a healthy ceramic filter for filtration of molten iron was produced.
従来法では製造に2日間かかっていたが、1時間で製造
可能となった。The conventional method took two days to manufacture, but now it can be manufactured in one hour.
[実施例2]
エポキシ樹脂でコーティングされた3次元編物(孔径:
15mm、 ’300mmX300+nmX20mm
、液化開始温度:100℃)に粒銑を湿式粉砕した鉄粉
(C:4.0%。[Example 2] Three-dimensional knitted fabric coated with epoxy resin (pore size:
15mm, '300mmX300+nmX20mm
Iron powder (C: 4.0%) obtained by wet-pulverizing granular pig iron to a temperature at which liquefaction starts: 100°C.
Si:0.10%、Mn:0.50%、Cr:0.50
%、P:0.01%、S:0.005%、酸素:6.5
%)5μ〜15μで90%構成される粉末を、CMC水
溶液を粘着剤として含浸法により3次元編物の骨格上に
塗着し、100℃×60分乾燥した後、20KHz高周
波誘導炉にてN2雰囲気中で室温から200℃まで50
℃1分の高速加熱を実施し、200℃で10分間脱脂し
た後200℃/分の昇温速度で1200℃で自己還元焼
結を約60分実施したところ、複合材料用骨格に使用出
来る強固で健全な鉄条孔体が得られた。Si: 0.10%, Mn: 0.50%, Cr: 0.50
%, P: 0.01%, S: 0.005%, oxygen: 6.5
%) Powder composed of 90% of 5μ to 15μ was applied onto the skeleton of the three-dimensional knitted fabric by an impregnation method using a CMC aqueous solution as an adhesive, dried at 100°C for 60 minutes, and then heated with N2 in a 20KHz high-frequency induction furnace. 50℃ from room temperature to 200℃ in atmosphere
After high-speed heating for 1 minute at ℃, degreasing at 200℃ for 10 minutes, and self-reducing sintering at 1200℃ for about 60 minutes at a heating rate of 200℃/min, the result was a strong material that could be used as a composite material skeleton. A healthy bar body was obtained.
従来法では3日間かかった製造工程を2時間に短縮可能
となった。The manufacturing process, which previously took three days, can now be shortened to two hours.
(実施例3]
実施例2と同様の供試材を第2図に示す2炉からなる高
周波誘導加熱炉(脱脂専用炉および焼結専用炉)を直列
に配し、脱脂炉の昇温速度:100℃/分で200℃ま
で加熱し、約60分間脱脂し、その後焼結炉に移動し、
200℃/分で1200℃まで加熱し、約60分焼結す
る事を連続的にくり返し、鉄条孔体を連続的に且つ経済
的に製造することができた。(Example 3) A high frequency induction heating furnace consisting of two furnaces (degreasing furnace and sintering furnace) shown in FIG. :Heat up to 200℃ at 100℃/min, degrease for about 60 minutes, then move to a sintering furnace,
By continuously repeating heating to 1200° C. at 200° C./min and sintering for about 60 minutes, it was possible to continuously and economically manufacture barbed wire bodies.
[発明の効果]
本発明により、無機質多孔体の製造に際して熱処理時間
が大幅に短縮化でき、かつ無機質多孔体の製品のワレや
ふくれの発生を有効に防止する事ができる。[Effects of the Invention] According to the present invention, the heat treatment time can be significantly shortened in the production of inorganic porous bodies, and the occurrence of cracking and blistering in products made of inorganic porous bodies can be effectively prevented.
第1図は熱処理の温度領域と許容昇温速度の例を示す図
第2図は実施例で使用した熱処理装置の例を示す図
第3図は従来の熱処理温度の例を示す図である。
5:液化開始温度、 6:液化開始温度+100℃、7
:焼結開始温度、 8:焼結終了温度、 9:昇温曲線
(従来法)、 ■0:被熱処理材(無機質微粉末塗着の
有機高分子材料〜無機質多孔体)、11:脱脂用高周波
炉、 12:焼結用高周波炉、13:冷却室、 14:
N2ガス、 15:被熱処理材の搬送方向、 16:シ
ールカバーFIG. 1 shows an example of the heat treatment temperature range and allowable temperature increase rate. FIG. 2 shows an example of the heat treatment apparatus used in the example. FIG. 3 shows an example of conventional heat treatment temperature. 5: Liquefaction start temperature, 6: Liquefaction start temperature +100°C, 7
: Sintering start temperature, 8: Sintering end temperature, 9: Temperature rise curve (conventional method), ■0: Material to be heat treated (organic polymer material coated with inorganic fine powder - inorganic porous body), 11: For degreasing High frequency furnace, 12: High frequency furnace for sintering, 13: Cooling chamber, 14:
N2 gas, 15: Conveyance direction of heat-treated material, 16: Seal cover
Claims (6)
接着剤により塗着した後、加熱するに際して、有機高分
子材料の液化開始温度から該液化開始温度+100℃の
間の昇温速度を30〜200℃/分として脱脂すること
を特徴とする、無機質多孔体の製造方法。(1) When heating after applying an inorganic fine powder to the framework of a porous organic polymer material using an adhesive, the rate of temperature increase from the liquefaction start temperature of the organic polymer material to the liquefaction start temperature +100°C A method for producing an inorganic porous body, the method comprising degreasing at a rate of 30 to 200°C/min.
50μの粒子よりなる無機質微粉末である、請求項(1
)に記載の無機質多孔体の製造方法。(2) More than 80% of the inorganic fine powder has a particle size of 1 μm or more
Claim (1), which is an inorganic fine powder consisting of particles of 50μ
) The method for producing an inorganic porous body.
の混合粉末あるいはこれ等と非金属との混合粉末である
、請求項(1)または(2)に記載の無機質多孔体の製
造方法。(3) The method for producing an inorganic porous body according to claim (1) or (2), wherein the inorganic fine powder is a metal powder, a mixed powder of two or more metals, or a mixed powder of these and a nonmetal.
素粉末との混合粉末あるいはこれ等に合金元素粉末を加
えた混合粉末である、請求項(1)または(2)に記載
の無機質多孔体の製造方法。(4) The inorganic fine powder according to claim (1) or (2), wherein the inorganic fine powder is an iron oxide powder, a mixed powder of iron oxide powder and carbon powder, or a mixed powder in which alloying element powder is added to these powders. Method for producing porous body.
は混合微粉末である、請求項(1)または(2)に記載
の無機質多孔体の製造方法。(5) The method for producing an inorganic porous body according to claim (1) or (2), wherein the inorganic fine powder is a ceramic composition fine powder or a mixed fine powder.
度+100℃の間の昇温速度を30〜200℃/分で加
熱する装置が誘導加熱炉であることを特徴とする、請求
項(1)または(2)または(3)または(4)または
(5)に記載の無機質多孔体の製造方法。(6) Claim (1) characterized in that the device for heating the organic polymer material at a heating rate of 30 to 200°C/min from the liquefaction start temperature to the liquefaction start temperature +100°C is an induction heating furnace. The method for producing an inorganic porous body according to 1) or (2) or (3) or (4) or (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7406589A JPH02254106A (en) | 1989-03-28 | 1989-03-28 | Production of inorganic cellular body |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7406589A JPH02254106A (en) | 1989-03-28 | 1989-03-28 | Production of inorganic cellular body |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02254106A true JPH02254106A (en) | 1990-10-12 |
Family
ID=13536418
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7406589A Pending JPH02254106A (en) | 1989-03-28 | 1989-03-28 | Production of inorganic cellular body |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02254106A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109070225A (en) * | 2016-04-01 | 2018-12-21 | 株式会社Lg化学 | Method for producing metal foam |
| JP2019510883A (en) * | 2016-04-01 | 2019-04-18 | エルジー・ケム・リミテッド | Method of manufacturing metal foam |
| JP2019526710A (en) * | 2016-10-14 | 2019-09-19 | エルジー・ケム・リミテッド | Metal foam manufacturing method |
| JP2019535901A (en) * | 2016-11-30 | 2019-12-12 | エルジー・ケム・リミテッド | Metal foam manufacturing method |
| JP2020501026A (en) * | 2016-11-30 | 2020-01-16 | エルジー・ケム・リミテッド | Manufacturing method of metal foam |
| JP2020509155A (en) * | 2016-11-30 | 2020-03-26 | エルジー・ケム・リミテッド | Manufacturing method of metal foam |
-
1989
- 1989-03-28 JP JP7406589A patent/JPH02254106A/en active Pending
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109070225A (en) * | 2016-04-01 | 2018-12-21 | 株式会社Lg化学 | Method for producing metal foam |
| JP2019510883A (en) * | 2016-04-01 | 2019-04-18 | エルジー・ケム・リミテッド | Method of manufacturing metal foam |
| JP2019511635A (en) * | 2016-04-01 | 2019-04-25 | エルジー・ケム・リミテッド | Method of manufacturing metal foam |
| US11141786B2 (en) | 2016-04-01 | 2021-10-12 | Lg Chem, Ltd. | Method for manufacturing metal foam |
| US11298745B2 (en) | 2016-04-01 | 2022-04-12 | Lg Chem, Ltd. | Method for manufacturing metal foam |
| JP2019526710A (en) * | 2016-10-14 | 2019-09-19 | エルジー・ケム・リミテッド | Metal foam manufacturing method |
| JP2019535901A (en) * | 2016-11-30 | 2019-12-12 | エルジー・ケム・リミテッド | Metal foam manufacturing method |
| JP2020501026A (en) * | 2016-11-30 | 2020-01-16 | エルジー・ケム・リミテッド | Manufacturing method of metal foam |
| JP2020509155A (en) * | 2016-11-30 | 2020-03-26 | エルジー・ケム・リミテッド | Manufacturing method of metal foam |
| US11628495B2 (en) | 2016-11-30 | 2023-04-18 | Lg Chem, Ltd. | Method for manufacturing metal foam |
| US11780006B2 (en) | 2016-11-30 | 2023-10-10 | Lg Chem, Ltd. | Method for manufacturing metal foam |
| US11980942B2 (en) | 2016-11-30 | 2024-05-14 | Lg Chem, Ltd. | Method for manufacturing metal foam |
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