JP2013193412A - Method for manufacturing dry ceramic molding - Google Patents

Method for manufacturing dry ceramic molding Download PDF

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JP2013193412A
JP2013193412A JP2012065313A JP2012065313A JP2013193412A JP 2013193412 A JP2013193412 A JP 2013193412A JP 2012065313 A JP2012065313 A JP 2012065313A JP 2012065313 A JP2012065313 A JP 2012065313A JP 2013193412 A JP2013193412 A JP 2013193412A
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molded body
drying
ceramic molded
sealed container
dried
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JP5977549B2 (en
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Kenji Yonekura
健二 米倉
Shinzo Hayashi
伸三 林
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NGK Insulators Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a method for manufacturing a dry ceramic molding that can manufacture the dry ceramic molding of high quality with a high yield by uniformly drying the ceramic molding in a short time without causing fissures and cracks in the surface of the molding in drying the ceramic molding.SOLUTION: A method for manufacturing a dry ceramic molding includes placing a wet ceramic molding 1 in a sealed container 3 sealed except for a steam discharge port 4, placing the internal space of the sealed container 3 into a superheated steam atmosphere with moisture produced from the wet ceramic molding 1 by heating the sealed container 3 from the outside, and drying while maintaining this state.

Description

本発明は、乾燥工程を短時間で完了させることができ、しかも乾燥後の成形体にひび割れや亀裂の発生することのない乾燥セラミックス成形体の製造方法に関する。   The present invention relates to a method for producing a dried ceramic molded body that can complete the drying step in a short time and that does not cause cracks or cracks in the dried molded body.

各種セラミックス製品は、セラミックス原料を用いて成形する成形工程と、成形体を乾燥する乾燥工程と、乾燥した成形体を焼成する焼成工程と、焼成体を冷却する冷却工程とを経て製造される。これらの工程のうち、乾燥工程又は冷却工程は、自然乾燥や自然冷却によることもあるが、時間短縮を図る目的で別途加熱手段や冷却手段を用いることがある。   Various ceramic products are manufactured through a molding process of molding using ceramic raw materials, a drying process of drying the molded body, a firing process of firing the dried molded body, and a cooling process of cooling the fired body. Among these steps, the drying step or the cooling step may be due to natural drying or natural cooling, but a separate heating means or cooling means may be used for the purpose of shortening the time.

しかし、セラミックス肉厚成形体の乾燥の場合には、乾燥工程における急速な乾燥操作によってその表面と内部の間に含有する水分量の大きな変化や急激な温度差が生じると、表面に亀裂やクラックが発生するという問題があった。そのため、従来の単純な加熱手段による乾燥方法のみでは、十分な製造時間の短縮を達成することができなかった。   However, in the case of drying ceramic thick molded bodies, if a large change in the amount of moisture contained between the surface and the interior due to a rapid drying operation in the drying process or a sudden temperature difference occurs, cracks and cracks will occur on the surface. There was a problem that occurred. For this reason, it has not been possible to achieve a sufficient reduction in production time only by a conventional drying method using simple heating means.

このような問題を解決するために、さまざまな技術を用いた手法が種々提案されている。例えば、外部の湿度を一定に調節しながらセラミックス成形体を乾燥させる調湿乾燥という方法が実施されている。しかし、この調湿乾燥法でも、外部の湿度を低下させて乾燥速度を早くすると成形体の内部と外部の間に水分含有量の大きな差が発生し、成形体に亀裂やクラックが発生するという問題があった。そのため、粘土を成分として含むセラミックス肉厚成形体の乾燥の場合には、この調湿乾燥法では成形体の内部温度が約40℃という条件で実施されており、乾燥が終了するまでに1〜3週間という長期間が必要である。   In order to solve such problems, various methods using various techniques have been proposed. For example, a method called moisture conditioning drying is performed in which a ceramic molded body is dried while adjusting the external humidity to be constant. However, even in this humidity control drying method, if the external humidity is lowered to increase the drying speed, a large difference in moisture content occurs between the inside and outside of the molded body, and cracks and cracks occur in the molded body. There was a problem. Therefore, in the case of drying a ceramic thick molded body containing clay as a component, this humidity control drying method is carried out under the condition that the internal temperature of the molded body is about 40 ° C. A long period of 3 weeks is required.

この乾燥時間を短縮するために過熱水蒸気を利用する方法が実施されている(特許文献1、2参照)。これはセラミックス成形体の外部雰囲気を過熱水蒸気で満たした状態で乾燥を行う方法であって、過熱水蒸気雰囲気下で乾燥を行うことによりセラミックス成形体内外の水分量分布を少なくし、成形体内の水分拡散速度を大きくし、さらに成形体内の温度を比較的高く維持することができる。例えば、調湿乾燥法では成形体の内部温度が約40℃であったものが、過熱水蒸気を用いる方法では約100℃の温度とすることができる。   In order to shorten the drying time, a method using superheated steam has been implemented (see Patent Documents 1 and 2). This is a method of drying in a state where the external atmosphere of the ceramic molded body is filled with superheated steam. By drying in a superheated steam atmosphere, the moisture content distribution inside and outside the ceramic molded body is reduced, and the moisture in the molded body is reduced. The diffusion rate can be increased and the temperature in the molded body can be kept relatively high. For example, the internal temperature of the molded body is about 40 ° C. in the humidity drying method, but the temperature is about 100 ° C. in the method using superheated steam.

セラミックス成形体の通常の乾燥法によれば成形体の表面からの水分の蒸発速度が成形体内部の水分の拡散速度に比べて大きいため、成形体の内外の水分量の差が大きくなり、成形体の表面に亀裂やクラックが発生する。しかし、上述の過熱水蒸気を利用する方法では表面からの水分の蒸発が抑制されて、かつ成形体の内部温度を100℃程度と高くすることができるため水分の拡散速度が大きくなり、水分の蒸発速度が成形体内部の拡散速度とほぼ同一の状態で乾燥を進行させることができ、そのため成形体の表面に亀裂やクラックが発生することが少ない。   According to the normal drying method for ceramic molded bodies, the evaporation rate of moisture from the surface of the molded body is larger than the diffusion rate of moisture inside the molded body. Cracks and cracks occur on the body surface. However, in the above-described method using superheated steam, the evaporation of moisture from the surface is suppressed, and the internal temperature of the molded body can be increased to about 100 ° C., so that the diffusion rate of moisture increases and the evaporation of moisture occurs. Drying can proceed while the speed is almost the same as the diffusion speed inside the molded body, and therefore, cracks and cracks are less likely to occur on the surface of the molded body.

更に、この過熱水蒸気を利用する方法では、成形体の表面に凝縮水が付着することとなるため表面硬化が生じにくいという利点がある。また、遠赤外線放射を有するため内部まで伝熱が浸透し表面にクラックが発生しづらいという利点もある。   Furthermore, this method using superheated steam has the advantage that surface hardening is unlikely to occur because condensed water adheres to the surface of the molded body. In addition, since it has far-infrared radiation, it has an advantage that heat transfer penetrates into the inside and cracks are hardly generated on the surface.

このような過熱水蒸気を用いて物品を乾燥する方法は、セラミックス成形体の乾燥だけでなく、例えば、食肉や魚肉の乾燥工程にも利用されている。具体的には、食肉や魚肉を短時間で安定して高品質な状態で乾燥させたり(特許文献4参照)、或いは、木材の熱処理に利用して木材の加熱によるそりを防止した高品質の製品を得ることなどに利用されている(特許文献5参照)。   Such a method of drying an article using superheated steam is used not only for drying ceramic molded bodies but also for drying meat and fish, for example. Specifically, meat or fish meat is dried in a stable and high quality state in a short time (see Patent Document 4), or it is used for heat treatment of wood to prevent warping due to heating of wood. It is used for obtaining products (see Patent Document 5).

しかし、この過熱水蒸気を利用する方法では、乾燥操作に際して過熱水蒸気発生機などの特別な設備を備えることが必要になり、設備コストが高くなるとともに、その運用時においても過熱水蒸気発生コストが必要となり、高価になるという問題がある。   However, this method using superheated steam requires special equipment such as a superheated steam generator for the drying operation, which increases the equipment cost and also requires the superheated steam generation cost during its operation. There is a problem of becoming expensive.

特開2008−229872号公報JP 2008-229872 A 特開2007−230796号公報JP 2007-230796 A 特開平5−43300号公報JP-A-5-43300 特開2006−262706号公報JP 2006-262706 A 特開2007−136881号公報JP 2007-136881 A

本発明は、このような従来技術の有する問題点に鑑みてなされたものであり、その課題とするところは、セラミックス成形体の乾燥に際して、特に肉厚のセラミックス成形体において、成形体の表面に亀裂やクラックを発生させることなく、短時間でムラなく均一に乾燥させて高品質の乾燥セラミックス成形体を歩留まり良く製造することが可能な乾燥セラミックス成形体の製造方法を提供することにある。   The present invention has been made in view of such problems of the prior art, and the object of the present invention is to dry the ceramic molded body, particularly in the case of a thick ceramic molded body, on the surface of the molded body. An object of the present invention is to provide a method for producing a dry ceramic molded body capable of producing a high-quality dry ceramic molded body with good yield by drying uniformly and uniformly in a short time without generating cracks or cracks.

本発明者らは上記課題を達成すべく鋭意検討した結果、特別な過熱水蒸気発生機などのような設備を用いることなくとも、乾燥前のセラミックス成形体を密閉状態に覆った状態で外部から加熱し成形体から発生する水蒸気によって内部の雰囲気を過熱水蒸気雰囲気として乾燥を進行させることによってセラミックス成形体を迅速かつ均質に乾燥させることができることを見出し本発明を完成するに至った。   As a result of intensive studies to achieve the above-mentioned problems, the present inventors have heated the ceramic molded body before drying from the outside in a sealed state without using a special superheated steam generator or the like. The present invention has been completed by finding that the ceramic molded body can be dried quickly and uniformly by proceeding with the superheated steam atmosphere with the steam generated from the molded body.

即ち、本発明によれば、以下に示す乾燥セラミックス成形体の製造方法が提供される。   That is, according to this invention, the manufacturing method of the dry ceramic molded object shown below is provided.

(1)湿潤したセラミックス成形体を、水蒸気排出口以外は密閉された密閉容器の内部に載置し、密閉容器の外部からの加熱によって密閉容器の内部空間を湿潤したセラミックス成形体から発生する水分により過熱水蒸気雰囲気とし、この状態を維持しつつ乾燥させる、乾燥セラミックス成形体の製造方法。 (1) Moisture generated from a ceramic molded body in which the wet ceramic molded body is placed inside a sealed sealed container except for the water vapor outlet and the internal space of the sealed container is wetted by heating from the outside of the sealed container. The manufacturing method of the dry-ceramics molded object made into superheated steam atmosphere by this, and making it dry, maintaining this state.

(2)密閉容器の内部空間の温度を100℃〜130℃に維持して乾燥させる前記(1)に記載の乾燥セラミックス成形体の製造方法。 (2) The method for producing a dried ceramic molded body according to (1), wherein the temperature of the internal space of the sealed container is maintained at 100 ° C to 130 ° C and dried.

(3)密閉容器の内部空間の温度を101℃〜120℃に維持して乾燥させる前記(1)に記載の乾燥セラミックス成形体の製造方法。 (3) The method for producing a dried ceramic molded body according to (1), wherein the temperature of the internal space of the sealed container is maintained at 101 ° C to 120 ° C and dried.

(4)密閉容器が金属製容器又は耐熱樹脂製容器である前記(1)〜(3)のいずれかに記載の乾燥セラミック成形体の製造方法。 (4) The method for producing a dried ceramic molded body according to any one of (1) to (3), wherein the sealed container is a metal container or a heat-resistant resin container.

(5)密閉容器が、その下部に水蒸気排出口を備えたものである前記(1)〜(4)のいずれかに記載の乾燥セラミック成形体の製造方法。 (5) The method for producing a dried ceramic molded body according to any one of (1) to (4), wherein the sealed container is provided with a water vapor outlet at a lower part thereof.

(6)密閉容器の外部からの加熱手段が熱風である前記(1)〜(5)のいずれかに記載の乾燥セラミック成形体の製造方法。 (6) The method for producing a dried ceramic molded body according to any one of (1) to (5), wherein the heating means from the outside of the sealed container is hot air.

(7)乾燥前のセラミックス成形体が、その肉厚が10mm以上のものである前記(1)〜(6)のいずれかに記載の乾燥セラミック成形体の製造方法。 (7) The method for producing a dried ceramic molded body according to any one of (1) to (6), wherein the ceramic molded body before drying has a thickness of 10 mm or more.

本発明の乾燥セラミックス成形体の製造方法によれば、特別な過熱水蒸気発生機のような設備を用いなくとも、湿潤したセラミックス成形体自身の水分によって密閉容器の内部に過熱水蒸気雰囲気を形成させて乾燥を進行させることができ、亀裂やクラックのない良好な品質の乾燥セラミックス成形体を短い乾燥時間で歩留まり良く製造することができる。   According to the method for producing a dry ceramic molded body of the present invention, a superheated steam atmosphere is formed inside the sealed container by the moisture of the wet ceramic molded body itself without using a special superheated steam generator. Drying can proceed, and a dry ceramic molded article of good quality free from cracks and cracks can be produced in a short drying time with good yield.

本発明に使用する乾燥装置の一例を示す説明図である。It is explanatory drawing which shows an example of the drying apparatus used for this invention. 実施例1の温度測定の結果を示すグラフである。3 is a graph showing the results of temperature measurement in Example 1. 実施例1の水分測定の結果を示すグラフである。3 is a graph showing the results of moisture measurement in Example 1. 実施例2の温度測定の結果を示すグラフである。It is a graph which shows the result of the temperature measurement of Example 2. 実施例3の温度測定の結果を示すグラフである。6 is a graph showing the results of temperature measurement in Example 3.

以下、本発明の実施の形態について説明するが、本発明は以下の実施の形態に限定されるものではなく、本発明の趣旨を逸脱しない範囲で、当業者の通常の知識に基づいて、以下の実施の形態に対し適宜変更、改良等が加えられたものも本発明の範囲に入ることが理解されるべきである。   Hereinafter, embodiments of the present invention will be described. However, the present invention is not limited to the following embodiments, and based on ordinary knowledge of those skilled in the art without departing from the spirit of the present invention. It should be understood that modifications, improvements, and the like appropriately added to the embodiments described above fall within the scope of the present invention.

一般的にセラミックスの製造方法は、セラミックス原料を用いて成形する成形工程と、成形体を乾燥する乾燥工程と、乾燥した成形体を焼成する焼成工程と、焼成体を冷却する冷却工程からなっており、このような工程を経て種々のセラミックス製品が製造される。本発明の乾燥セラミックス成形体の製造方法は、このようなセラミックスの製造工程中の乾燥工程において、過熱水蒸気雰囲気を利用して成形体を乾燥させることを特徴とするものである。   In general, a method for producing ceramics comprises a molding step of molding using a ceramic raw material, a drying step of drying the molded body, a firing step of firing the dried molded body, and a cooling step of cooling the fired body. Various ceramic products are manufactured through such processes. The method for producing a dried ceramic molded body of the present invention is characterized in that the molded body is dried using a superheated steam atmosphere in the drying step in the ceramics production process.

本発明の乾燥セラミックス成形体の製造方法においては、種々のセラミックス原料によって形成された焼成前の湿潤状態にあるセラミックス成形体を、水蒸気排出口以外は密閉された密閉容器の内部に載置し、密閉容器の外部からの加熱によって密閉容器の内部空間を湿潤したセラミックス成形体から発生する水分により過熱水蒸気雰囲気とし、この状態を維持しつつ乾燥させ、乾燥セラミック成形体を得る方法を含むものである。   In the method for producing a dried ceramic molded body of the present invention, the ceramic molded body in a wet state before firing formed by various ceramic raw materials is placed inside a sealed container other than the water vapor outlet, The method includes a method of obtaining a dry ceramic molded body by making a superheated steam atmosphere with moisture generated from a ceramic molded body in which the internal space of the sealed container is moistened by heating from the outside of the closed container and maintaining this state.

即ち、本発明においては、水蒸気排出口以外は密閉された密閉容器を用いて、その内部に焼成前の湿潤状態にあるセラミックス成形体を載置し、密閉容器の外部から加熱することによってセラミックス成形体自身が保有する水分を蒸発させ、密閉容器の内部空間に過熱水蒸気雰囲気を形成させ、この過熱水蒸気雰囲気を維持しながらセラミックス成形体を乾燥させるものである。   That is, in the present invention, using a sealed container other than the water vapor outlet, a ceramic molded body in a wet state before firing is placed inside and heated from the outside of the sealed container. The water held by the body itself is evaporated to form a superheated steam atmosphere in the internal space of the sealed container, and the ceramic molded body is dried while maintaining this superheated steam atmosphere.

この密閉容器の内部空間に過熱水蒸気雰囲気を形成させるために、外部からの加熱によってこの内部空間の温度を100℃〜130℃の温度範囲に維持することが好ましく、101℃〜120℃の温度範囲に維持することが更に好ましい。密閉容器の内部空間の温度をこのような温度に維持することによって、セラミックス成形体の内部から拡散する水分によって成形体の表面に水分が供給されるとともに、この水分が蒸発して密閉容器の内部空間を過熱水蒸気の雰囲気とすることができる。このような加熱温度とすることによって、水分の成形体内部からの拡散と表面の蒸発がバランスよく行われ、その結果として密閉容器の内部空間に十分な過熱水蒸気の雰囲気が形成され、比較的短い時間で効率よく乾燥するとともに、成形体の表面にひび割れやクラックが発生することがない。   In order to form a superheated steam atmosphere in the internal space of the sealed container, it is preferable to maintain the temperature of the internal space in a temperature range of 100 ° C. to 130 ° C. by heating from the outside, and a temperature range of 101 ° C. to 120 ° C. It is further preferable to maintain the above. By maintaining the temperature of the internal space of the sealed container at such a temperature, moisture is supplied to the surface of the molded body by the moisture diffusing from the inside of the ceramic molded body, and this moisture evaporates and the inside of the sealed container is The space can be an atmosphere of superheated steam. By setting such a heating temperature, the diffusion of moisture from the inside of the molded body and the evaporation of the surface are performed in a well-balanced manner. As a result, a sufficient superheated steam atmosphere is formed in the internal space of the sealed container and is relatively short It dries efficiently over time and does not crack or crack on the surface of the molded body.

しかし、密閉容器の内部空間の温度が100℃未満では、密閉容器内が飽和水蒸気雰囲気の為、乾燥が進行しない。   However, if the temperature of the internal space of the sealed container is less than 100 ° C., the drying does not proceed because the inside of the sealed container is a saturated water vapor atmosphere.

密閉容器の外部からの加熱時間は、乾燥するセラミックス成形体の大きさや厚さ、形状によって適宜最適な時間を決定する。例えば、一般的に厚さが80mmの直方体(100×100×80mm)の形状のセラミックス成形体の場合には、およそ30時間程度の加熱時間で乾燥を終了することができる。同じ形状のセラミックス成形体を従来の調湿乾燥法で乾燥した場合に60時間という長時間を要するのと比べて大幅に乾燥時間を短縮できる。   The heating time from the outside of the sealed container is appropriately determined depending on the size, thickness and shape of the ceramic molded body to be dried. For example, in the case of a ceramic molded body having a rectangular parallelepiped shape (100 × 100 × 80 mm) generally having a thickness of 80 mm, drying can be completed in a heating time of about 30 hours. The drying time can be greatly shortened compared with the case where a long time of 60 hours is required when a ceramic molded body having the same shape is dried by a conventional humidity control drying method.

このような本発明の方法によって湿潤したセラミックス成形体を乾燥する場合には、乾燥工程の途中のあらゆる段階で成形体の内部と表面の水分の分布を小さく維持することができる。例えば、上記の100×100×80mmの形状のセラミックス成形体の場合には、乾燥工程の途中のすべてにおいて成形体の内部と表面の水分濃度の差を3質量%程度とすることができる。   When the ceramic molded body wetted by the method of the present invention is dried, the moisture distribution inside and on the surface of the molded body can be kept small at every stage during the drying process. For example, in the case of the above-mentioned ceramic molded body having a shape of 100 × 100 × 80 mm, the difference in moisture concentration between the inside and the surface of the molded body can be set to about 3% by mass in the entire drying process.

本発明で使用する湿潤状態にあるセラミックス成形体は、セラミックスに対して、水、バインダ等の各種添加剤を加えて得られたセラミックス原料によって形成されたものである。セラミックスとしては、例えば、アルミナ、ムライト、ジルコニア、コージェライト等の酸化物系セラミック;炭化珪素、窒化珪素、窒化アルミニウム等の非酸化物系セラミック等を挙げることができる。また、炭化珪素/金属珪素複合材や炭化珪素/グラファイト複合材等を用いることもできる。   The wet ceramic molded body used in the present invention is formed from a ceramic raw material obtained by adding various additives such as water and a binder to ceramics. Examples of ceramics include oxide ceramics such as alumina, mullite, zirconia, and cordierite; non-oxide ceramics such as silicon carbide, silicon nitride, and aluminum nitride. A silicon carbide / metal silicon composite material, a silicon carbide / graphite composite material, or the like can also be used.

バインダとしては、例えば、ポリビニルアルコール、ポリエチレングリコール、澱粉、メチルセルロース、カルボキシメチルセルロース、ヒドロキシエチルセルロース、ヒドロキシプロピルメチルセルロース、ポリエチレンオキシド、ポリアクリル酸ソーダ、ポリアクリルアミド、ポリビニルブチラール、エチルセルロース、酢酸セルロース、ポリエチレン、エチレン−酢酸ビニル共重合体、ポリプロピレン、ポリスチレン、アクリル系樹脂、ポリアミド樹脂、グリセリン、ポリエチレングリコール、ジブチルフタレート等を挙げることができる。   Examples of the binder include polyvinyl alcohol, polyethylene glycol, starch, methyl cellulose, carboxymethyl cellulose, hydroxyethyl cellulose, hydroxypropyl methyl cellulose, polyethylene oxide, sodium polyacrylate, polyacrylamide, polyvinyl butyral, ethyl cellulose, cellulose acetate, polyethylene, and ethylene-acetic acid. Examples include vinyl copolymers, polypropylene, polystyrene, acrylic resins, polyamide resins, glycerin, polyethylene glycol, and dibutyl phthalate.

セラミックス成形体としては、種々の用途に使用するためのセラミックス製品を製造するためのもので、さまざまな形状のものに適用することが使用でき、例えば、高電圧送電線用の碍子、自動車排ガス浄化用触媒担体、自動車用セラミックス部材、焼成用窯道具などの形状の成形体としたものが挙げられる。   The ceramic molded body is for manufacturing ceramic products for use in various applications, and can be used in various shapes, such as insulators for high voltage transmission lines, automobile exhaust gas purification, etc. And a molded body having a shape such as a catalyst carrier for automobiles, a ceramic member for automobiles, and a kiln tool for firing.

本発明で使用する密閉容器は、セラミックス成形体を収納して密閉構造とすることができるものであって、150℃程度の加熱温度に対して耐熱性のある材料から構成されているものであれば特に制限されない。一般的に金属製の材料が好ましく、鉄製またはステンレス製の板で構成されたものが好ましい。耐熱性樹脂材質を使用する事も可能である。密閉容器は、セラミックス成形体を収納した後密閉状態とするが、その下部に蒸気排出口を設け、加熱乾燥の際に余分な水蒸気をここから排出させる。   The hermetic container used in the present invention is capable of accommodating a ceramic molded body to have a hermetic structure, and is made of a material that is heat resistant to a heating temperature of about 150 ° C. There is no particular limitation. In general, a metal material is preferable, and a metal or stainless steel plate is preferable. It is also possible to use a heat-resistant resin material. The sealed container is in a sealed state after the ceramic molded body is accommodated, but a steam discharge port is provided in the lower part thereof, and excess water vapor is discharged from the steam discharge port during heating and drying.

次に、図面に基づき、本発明の方法を実施する乾燥装置について説明する。図1は、熱風乾燥器の内部に密閉容器を備えた乾燥装置の一実施形態を示す。図1において、2は熱風乾燥器であり、熱風乾燥器2の内部に密閉容器3が備えられている。密閉容器3は、水蒸気排出口4以外は密閉された構造になっている。本発明では、密閉容器3の内部に焼成前の湿潤状態にあるセラミックス成形体1を載置し、密閉容器3の外部から加熱する。このようにしてセラミックス成形体1を加熱することによって、セラミックス成形体1自身が保有する水分を蒸発させ、密閉容器3の内部空間に過熱水蒸気雰囲気を形成させる。そして、この過熱水蒸気雰囲気を維持しながらセラミックス成形体1を乾燥させる。なお、密閉容器3内の空間部には、雰囲気温度測定用の熱電対5が設置される。   Next, a drying apparatus for carrying out the method of the present invention will be described with reference to the drawings. FIG. 1 shows an embodiment of a drying apparatus having a sealed container inside a hot air dryer. In FIG. 1, reference numeral 2 denotes a hot air dryer, and a sealed container 3 is provided inside the hot air dryer 2. The sealed container 3 has a sealed structure except for the water vapor outlet 4. In the present invention, the ceramic molded body 1 in a wet state before firing is placed inside the sealed container 3 and heated from the outside of the sealed container 3. By heating the ceramic molded body 1 in this way, the water held by the ceramic molded body 1 itself is evaporated, and an overheated steam atmosphere is formed in the internal space of the sealed container 3. Then, the ceramic molded body 1 is dried while maintaining this superheated steam atmosphere. A thermocouple 5 for measuring ambient temperature is installed in the space inside the sealed container 3.

以下、本発明を実施例に基づいて具体的に説明するが、本発明はこれらの実施例に限定されるものではない。   EXAMPLES Hereinafter, although this invention is demonstrated concretely based on an Example, this invention is not limited to these Examples.

(実施例1)
図1に示すような熱風乾燥器の内部に密閉容器を備えた乾燥装置を使用して、セラミックス成形体の乾燥の予備的試験を行った。
Example 1
A preliminary test of drying of the ceramic molded body was performed using a drying apparatus having a sealed container inside the hot air dryer as shown in FIG.

まず、サンプルとして100×100×80mmの直方体形状の湿潤状態のセラミックス成形体を用意した。このサンプルのセラミックス成形体を密閉容器の中に設置し、セラミックス成形体の中心部と表面および密閉容器内の空間部に温度測定用の熱電対を取り付けた。この状態で密閉容器の外側から熱風乾燥器による熱風を通して加熱を開始し、密閉容器の内部の空間温度が110℃となるようにコントロールしつつ、乾燥を行った。空間温度(雰囲気温度)を110℃として乾燥することによって、密閉容器の内部が110℃の温度の過熱水蒸気雰囲気となり、成形体の乾燥が進行した。   First, a 100 × 100 × 80 mm rectangular parallelepiped wet ceramic molded body was prepared as a sample. The ceramic molded body of this sample was placed in a sealed container, and a thermocouple for temperature measurement was attached to the center and surface of the ceramic molded body and the space in the sealed container. In this state, heating was started from the outside of the sealed container through hot air by a hot air dryer, and drying was performed while controlling the space temperature inside the sealed container to be 110 ° C. By drying at a space temperature (atmosphere temperature) of 110 ° C., the inside of the sealed container became a superheated steam atmosphere at a temperature of 110 ° C., and drying of the molded body proceeded.

乾燥途中で上記の成形体の中心部と表面、および過熱水蒸気雰囲気の3か所の温度変化を測定するとともに、乾燥開始後17時間、22時間、29時間、および47時間経過した時点((1)〜(4))でサンプルの水分分布を測定した。サンプルの水分分布は、図3に示すように、成形体を縦横5等分で25分割して縦横それぞれ5か所のサンプルを採取し、その水分量を測定した。この温度測定の結果を図2に、水分分布の変化を図3に示す。   During the drying, the temperature change at the three parts of the center and surface of the molded body and the superheated steam atmosphere was measured, and when 17 hours, 22 hours, 29 hours, and 47 hours passed after the start of drying ((1 ) To (4)), the moisture distribution of the sample was measured. As shown in FIG. 3, the moisture distribution of the sample was obtained by dividing the molded body into 25 equal parts in the vertical and horizontal directions, collecting samples at 5 locations in each of the vertical and horizontal directions, and measuring the water content. The results of this temperature measurement are shown in FIG. 2, and the change in moisture distribution is shown in FIG.

図2からわかるように、加熱開始後約5時間で過熱水蒸気雰囲気の温度は110℃となり、加熱終了までほぼこの温度で一定にコントロールされた。セラミックス成形体は、その表面も中心部も加熱開始後約5時間で101℃になり、30時間後までほぼこの温度で維持された。この期間が過熱水蒸気雰囲気の下での恒率乾燥期間である。約30時間経過して成形体の温度の上昇が見られ、恒率乾燥が終了し減率乾燥に移行したことがわかった。   As can be seen from FIG. 2, the temperature of the superheated steam atmosphere became 110 ° C. about 5 hours after the start of heating, and was controlled to be substantially constant at this temperature until the end of heating. The ceramic molded body had a temperature of 101 ° C. at about 5 hours after the start of heating, and was maintained at this temperature until about 30 hours. This period is a constant rate drying period under a superheated steam atmosphere. After about 30 hours, the temperature of the molded body was increased, and it was found that the constant rate drying was completed and the reduced rate drying was started.

この乾燥期間の途中で、図2に(1)〜(4)で示す時点でサンプルを採取して、その水分分布を求めた。その結果を図3に示す。この結果から、過熱水蒸気雰囲気の下での恒率乾燥では、(1)から(4)へと行くに従って水分量が減少してゆき乾燥が進行していることがわかった。更に、この(1)から(4)のいずれの段階においても成形体の表面の水分量と中心部の水分量の差が3%前後であり、表面と内部の水分差が非常に少ないことがわかった。   In the middle of this drying period, a sample was taken at the time indicated by (1) to (4) in FIG. 2, and its moisture distribution was determined. The result is shown in FIG. From this result, it was found that in the constant rate drying under the superheated steam atmosphere, the moisture content decreased from (1) to (4) and the drying progressed. Further, in any of the stages (1) to (4), the difference between the moisture content on the surface of the molded body and the moisture content in the central portion is about 3%, and the moisture difference between the surface and the interior is very small. all right.

(実施例2)
図1に示すような熱風乾燥器の内部に密閉容器を備えた乾燥装置を使用して、笠形状碍子実体形状のセラミックス成形体の加熱水蒸気による乾燥試験を行った。
(Example 2)
Using a drying apparatus provided with a sealed container inside a hot air dryer as shown in FIG. 1, a drying test using heated steam was performed on a ceramic body having a shaded coconut body shape.

まず、サンプルとして、笠直径(大)250mm×笠直径(小)200mm×胴直径100mmの4枚笠の笠形状碍子の湿潤状態にある成形体を用意した。このサンプルのセラミックス成形体を密閉容器の中に設置し、セラミックス成形体の胴の中心部と表面、笠の表面および密閉容器内の空間部(過熱水蒸気雰囲気)に温度測定用の熱電対を取り付けた。この状態で密閉容器の外側から熱風乾燥器による熱風を通して加熱を開始し、笠形状碍子実体形状のセラミックス成形体の乾燥を行った。空間温度(過熱水蒸気雰囲気温度)を111℃として乾燥することによって、密閉容器の内部が111℃の温度の過熱水蒸気雰囲気となり、成形体の乾燥が進行した。乾燥開始後約90hrで加熱を終わり、セラミックス成形体の乾燥を終了した。   First, as a sample, a molded body in a wet state of a 4-shade shade-shaped insulator having a shade diameter (large) of 250 mm, a shade diameter (small) of 200 mm, and a trunk diameter of 100 mm was prepared. Place the ceramic molded body of this sample in a sealed container, and attach thermocouples for temperature measurement to the center and surface of the body of the ceramic molded body, the surface of the shade, and the space inside the sealed container (superheated steam atmosphere). It was. In this state, heating was started from the outside of the hermetic container through hot air by a hot air dryer, and the shade-shaped cocoon body-shaped ceramic molded body was dried. By drying the space temperature (superheated steam atmosphere temperature) at 111 ° C., the inside of the sealed container became a superheated steam atmosphere at a temperature of 111 ° C., and drying of the molded body proceeded. Heating was completed after about 90 hours from the start of drying, and drying of the ceramic molded body was completed.

この乾燥試験の結果、笠の部分にキレやひび割れは見られず、良好な乾燥品を得ることができた。また、この乾燥操作において、その途中で上記の笠形状碍子のセラミックス成形体の胴中心部、胴表面、笠表面および過熱水蒸気雰囲気の4か所の温度変化を測定した。その結果を図4に示す。   As a result of this drying test, no cracks or cracks were found in the shade, and a good dry product could be obtained. Further, during this drying operation, temperature changes were measured at four locations on the middle of the ceramic molded body of the above-mentioned shade-shaped insulator, the barrel surface, the shade surface, and the superheated steam atmosphere. The result is shown in FIG.

図4からわかるように、碍子の胴部の温度は約104℃で乾燥が進行し、笠の先端部において乾燥が早く進行し、笠先端部の温度が早く上昇し始めるが、成形体全体の温度差は小さかった。   As can be seen from FIG. 4, drying proceeds at a temperature of about 104 ° C. at the insulator body, and drying proceeds quickly at the tip of the shade, and the temperature at the tip of the shade begins to rise quickly. The temperature difference was small.

(実施例3)
サンプルとして実施例2と同じ笠形状碍子のセラミックス成形体を用いて、空間温度(過熱水蒸気雰囲気温度)を103℃とする以外は実施例2とまったく同じ乾燥操作によって笠形状碍子実体形状のセラミックス成形体の乾燥を行った。この場合は、乾燥開始後約180hrで加熱を終わり、セラミックス成形品の乾燥を終了した。
(Example 3)
Using the same shade shaped ceramic molded body as in Example 2 as a sample, the shade shaped palm body shaped ceramic was formed by the same drying operation as in Example 2 except that the space temperature (superheated steam atmosphere temperature) was 103 ° C. The body was dried. In this case, the heating was finished about 180 hours after the start of drying, and the drying of the ceramic molded product was finished.

この乾燥試験の結果、笠の部分にキレやひび割れは見られず、良好な乾燥品を得ることができた。また、この乾燥操作において、その途中で上記の笠形状碍子のセラミックス成形体の胴中心部、胴表面、笠表面および過熱水蒸気雰囲気の4か所の温度変化を測定した。その結果を図5に示す。   As a result of this drying test, no cracks or cracks were found in the shade, and a good dry product could be obtained. Further, during this drying operation, temperature changes were measured at four locations on the middle of the ceramic molded body of the above-mentioned shade-shaped insulator, the barrel surface, the shade surface, and the superheated steam atmosphere. The result is shown in FIG.

図5からわかるように、碍子の胴部だけでなく笠の先端部の温度もほぼ102℃と同じ温度でありその温度差は非常に小さい。そのため水分の成形体内部の移動速度が遅く、乾燥に長時間を要した。   As can be seen from FIG. 5, the temperature at the tip of the shade as well as the body of the insulator is almost the same as 102 ° C., and the temperature difference is very small. Therefore, the moving speed of moisture inside the molded body is slow, and it takes a long time for drying.

(実施例4)
実施例2と同様の方法によって、図1に示すような熱風乾燥器の内部に密閉容器を備えた乾燥装置を使用して、次の2種類の笠形状碍子実体形状のセラミックス成形体の加熱水蒸気による乾燥試験を行った。その結果を表1に示す。
Example 4
In the same manner as in Example 2, using a drying apparatus having a sealed container inside a hot air dryer as shown in FIG. 1, the following two types of shaded body-shaped ceramic molded body heated steam A drying test was performed. The results are shown in Table 1.

Figure 2013193412
Figure 2013193412

この結果からわかるように、本発明の過熱水蒸気雰囲気による乾燥法の場合には、従来の調湿乾燥法による乾燥に比べて1/2から1/3という短時間で乾燥を行うことができ、しかも得られた乾燥品にキレやひび割れが発生することなく良好な品質の乾燥品を得ることができた。   As can be seen from this result, in the case of the drying method using the superheated steam atmosphere of the present invention, the drying can be performed in a short time of 1/2 to 1/3 compared with the drying by the conventional humidity conditioning drying method, In addition, it was possible to obtain a dry product of good quality without occurrence of cracks or cracks in the obtained dry product.

本発明のセラミックス成形体の製造方法は、従来の方法に比べて特別な過熱水蒸気加熱装置などを用いることなく、従来の方法に比べて短時間でセラミックス成形体の乾燥を行うことができ、かつ良好な乾燥品を得ることができ、送電線用碍子その他セラミックス成形体を用いるさまざまな窯業製品の製造において有用である。   The method for producing a ceramic molded body of the present invention can dry a ceramic molded body in a shorter time than the conventional method without using a special superheated steam heating device or the like compared to the conventional method, and A good dry product can be obtained, which is useful in the production of various ceramic products using insulators for power transmission lines and other ceramic molded bodies.

1.セラミックス成形体
2.熱風乾燥器
3.密閉容器
4.水蒸気排出口
5.熱電対
1. Ceramic compact 1. 2. Hot air dryer Airtight container 4. 4. Water vapor outlet thermocouple

Claims (7)

湿潤したセラミックス成形体を、水蒸気排出口以外は密閉された密閉容器の内部に載置し、密閉容器の外部からの加熱によって密閉容器の内部空間を湿潤したセラミックス成形体から発生する水分により過熱水蒸気雰囲気とし、この状態を維持しつつ乾燥させる、乾燥セラミックス成形体の製造方法。   The wet ceramic molded body is placed inside a sealed sealed container except for the water vapor outlet, and superheated steam is generated by moisture generated from the ceramic molded body that has moistened the internal space of the sealed container by heating from the outside of the sealed container. A method for producing a dried ceramic molded body, which is dried while maintaining this state in an atmosphere. 密閉容器の内部空間の温度を100℃〜130℃に維持して乾燥させる請求項1に記載の乾燥セラミックス成形体の製造方法。   The method for producing a dried ceramic molded body according to claim 1, wherein the temperature of the internal space of the sealed container is maintained at 100C to 130C and is dried. 密閉容器の内部空間の温度を101℃〜120℃に維持して乾燥させる請求項1に記載の乾燥セラミックス成形体の製造方法。   The method for producing a dried ceramic molded article according to claim 1, wherein the temperature of the internal space of the sealed container is maintained at 101C to 120C to be dried. 密閉容器が金属製容器又は耐熱樹脂製容器である請求項1〜3のいずれか1項に記載の乾燥セラミック成形体の製造方法。   The method for producing a dry ceramic molded body according to any one of claims 1 to 3, wherein the sealed container is a metal container or a heat-resistant resin container. 密閉容器が、その下部に水蒸気排出口を備えたものである請求項1〜4のいずれか1項に記載の乾燥セラミック成形体の製造方法。   The method for producing a dried ceramic molded body according to any one of claims 1 to 4, wherein the sealed container is provided with a water vapor outlet at a lower portion thereof. 密閉容器の外部からの加熱手段が熱風である請求項1〜5のいずれか1項に記載の乾燥セラミック成形体の製造方法。   The method for producing a dried ceramic molded body according to any one of claims 1 to 5, wherein the heating means from the outside of the sealed container is hot air. 乾燥前のセラミックス成形体が、その肉厚が10mm以上のものである請求項1〜6のいずれか1項に記載の乾燥セラミック成形体の製造方法。   The method for producing a dried ceramic molded body according to any one of claims 1 to 6, wherein the thickness of the ceramic molded body before drying is 10 mm or more.
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KR101567380B1 (en) 2014-12-12 2015-11-10 유용호 Frame for clay composition, producing device and method for the same

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CN111673894B (en) * 2020-06-22 2021-06-22 苏州海宏水泥制品有限公司 Automatic tubular pile autoclaved maintenance method and device and storage medium

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JPS565711A (en) * 1979-06-27 1981-01-21 Younosuke Shirohata Frame body for drying largeesized clayey molding
JPH0380935A (en) * 1989-08-22 1991-04-05 Kobe Steel Ltd Method for drying molded body
JPH0587452A (en) * 1991-09-25 1993-04-06 Ngk Insulators Ltd Drying method for thick ceramics
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JPS565711A (en) * 1979-06-27 1981-01-21 Younosuke Shirohata Frame body for drying largeesized clayey molding
JPH0380935A (en) * 1989-08-22 1991-04-05 Kobe Steel Ltd Method for drying molded body
JPH0587452A (en) * 1991-09-25 1993-04-06 Ngk Insulators Ltd Drying method for thick ceramics
JP2008229872A (en) * 2007-03-16 2008-10-02 Ngk Insulators Ltd Manufacturing method of dried ceramic molded object

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KR101567380B1 (en) 2014-12-12 2015-11-10 유용호 Frame for clay composition, producing device and method for the same

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