JP2637678B2 - Drying method of ceramic cylindrical molded body - Google Patents
Drying method of ceramic cylindrical molded bodyInfo
- Publication number
- JP2637678B2 JP2637678B2 JP5129058A JP12905893A JP2637678B2 JP 2637678 B2 JP2637678 B2 JP 2637678B2 JP 5129058 A JP5129058 A JP 5129058A JP 12905893 A JP12905893 A JP 12905893A JP 2637678 B2 JP2637678 B2 JP 2637678B2
- Authority
- JP
- Japan
- Prior art keywords
- molded body
- cylindrical molded
- dried
- ceramic
- ceramic cylindrical
- 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
Landscapes
- Compositions Of Oxide Ceramics (AREA)
- Devices For Post-Treatments, Processing, Supply, Discharge, And Other Processes (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、寸法精度の優れたセラ
ミック筒状成形体を得るための乾燥方法に関するもので
ある。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a drying method for obtaining a ceramic cylinder having excellent dimensional accuracy.
【0002】[0002]
【従来の技術】セラミック筒状体を製造するのに際して
は、従来より、セラミック杯土を押し出し成形し、成形
体を支持台上に載置し、大気中で2─3日放置して自然
乾燥し、この乾燥体を焼成することが多い。しかし、押
し出し成形直後のセラミック筒状成形体は、いまだ軟弱
であるため、セラミック筒状成形体を支持台上に載置
し、自然乾燥した場合、水平方向の寸法が垂直方向の寸
法より大きくなり、楕円形状に変形することがあった。
この場合には、後の焼成工程においても、この寸法の歪
みは修正されず、楕円形状に変形した焼成体ができるた
め、問題になっていた。セラミック筒状成形体を乾燥す
る際に、このような変形を防止するため、成形体を支持
台上に載置した後、温度、湿度が調節された乾燥機内
で、調温度、調湿度乾燥する方法があった。また、押し
出し成形直後のセラミック筒状成形体の下側から空気を
吹きつけて浮上させ、これと同時に筒状成形体の内側空
間に空気を流しながら、乾燥する方法が知られている。2. Description of the Related Art In the production of a ceramic cylindrical body, conventionally, ceramic clay has been extruded and formed, and the formed body has been placed on a support table and left to stand in the air for 2 to 3 days to air dry. The dried product is often fired. However, since the ceramic cylindrical molded body immediately after extrusion molding is still soft, when the ceramic cylindrical molded body is placed on a support table and air-dried, the horizontal dimension becomes larger than the vertical dimension. In some cases, it was deformed into an elliptical shape.
In this case, even in the subsequent firing step, the distortion of the dimension is not corrected, and a fired body deformed into an elliptical shape is produced, which has been a problem. When drying the ceramic cylindrical molded body, in order to prevent such deformation, after placing the molded body on a support base, the temperature and humidity are dried in a dryer in which the temperature and humidity are adjusted. There was a way. A method is also known in which air is blown from the lower side of the ceramic cylindrical molded body immediately after extrusion molding to cause the ceramic cylindrical molded body to float, and at the same time, air is flown into the space inside the cylindrical molded body while being dried.
【0003】[0003]
【発明が解決しようとする課題】しかし、杯土の粒度分
布、杯土の水分含有量、セラミックスの種類等によって
は、セラミック筒状成形体を支持台に載置し、自然乾燥
した場合、垂直方向の寸法が水平方向の寸法より大きく
なり、縦長の楕円形状に変形することを、本発明者が初
めて発見した。また、本発明者は、成形体を支持台に載
置した後、温度、湿度が調節された乾燥機内で、調温
度、調湿度乾燥してみたが、やはり上記の変形は防止で
きず、断面が真円形状の乾燥体を得ることはできなかっ
た。However, depending on the particle size distribution of the clay, the moisture content of the clay, the type of ceramics, etc., when the ceramic cylindrical molded body is placed on a support and dried naturally, the vertical The present inventor has discovered for the first time that the dimension in the direction becomes larger than the dimension in the horizontal direction, and the shape is transformed into a vertically long elliptical shape. In addition, the present inventor, after placing the molded body on the support table, in a dryer in which the temperature and humidity were adjusted, tried drying the temperature and humidity, but again the above deformation could not be prevented, and the cross section was not able to be prevented. However, a dried product having a perfect circular shape could not be obtained.
【0004】また、本発明者は、上記のセラミック筒状
成形体について、筒状成形体の下側から空気を吹きつけ
て浮上させ、これと同時に筒状成形体の内側空間に空気
を流しながら、乾燥を行ってみた。しかし、やはり上記
の変形は防止できず、断面が真円形状の乾燥体を得るこ
とはできなかった。しかも、筒状成形体の下側から空気
を吹きつけて浮上させる乾燥方法は、大量生産には全く
適しておらず、実用的ではない。Further, the present inventor has made the above-mentioned ceramic cylindrical molded body float by blowing air from the lower side of the cylindrical molded body, and at the same time, flowing air into the inner space of the cylindrical molded body. I tried drying. However, the above deformation could not be prevented, and a dried body having a perfect circular cross section could not be obtained. In addition, the drying method in which air is blown from the lower side of the cylindrical molded body to float it is not suitable for mass production at all and is not practical.
【0005】本発明の課題は、多数のセラミック筒状成
形体を乾燥する際に、水平方向の寸法と垂直方向の寸法
との間に差が生じ、所定の寸法から変形するのを防止で
きる、効率的な乾燥方法を提供することである。[0005] An object of the present invention is to prevent a large difference between a horizontal dimension and a vertical dimension when drying a large number of ceramic cylindrical molded bodies, thereby preventing deformation from a predetermined dimension. It is to provide an efficient drying method.
【0006】[0006]
【課題を解決するための手段】本発明に係るセラミック
筒状成形体の乾燥方法は、セラミック筒状成形体を支持
台の上に載置し、セラミック筒状成形体の内面側が外面
側と同等以上に早く乾燥するようにこのセラミック筒状
成形体の少なくとも内側空間に10m/秒以上の流速で
気体を流すことを特徴とする。According to the present invention, there is provided a method for drying a ceramic cylindrical molded body, comprising placing the ceramic cylindrical molded body on a support base, wherein the inner surface side of the ceramic cylindrical molded body is equal to the outer surface side. A gas is flowed at a flow rate of 10 m / sec or more into at least the inner space of the ceramic cylindrical molded body so as to dry faster.
【0007】[0007]
【作用】本発明者は、セラミック筒状成形体を支持台に
載置し、自然乾燥した場合や調温度、調湿度乾燥した場
合に、垂直方向の寸法が水平方向の寸法より大きくな
り、縦長の楕円形状に変形する現象を発見した。まず、
この現象について説明する。図3の模式図においては、
支持台の各突起3cに、それぞれ傾斜面4が形成されて
おり、一対の互いに対向する傾斜面4の間に、セラミッ
ク円筒状成形体1が載置されている。この円筒状成形体
1を幅方向に切ったとき、水平方向の寸法をaとし、垂
直方向の寸法をbとする。According to the present invention, the ceramic cylindrical molded body is placed on a support base, and when it is air-dried, or when the temperature and humidity are dried, the vertical dimension becomes larger than the horizontal dimension. Has been found to be transformed into an elliptical shape. First,
This phenomenon will be described. In the schematic diagram of FIG.
An inclined surface 4 is formed on each of the projections 3c of the support base, and the ceramic cylindrical molded body 1 is placed between a pair of opposed inclined surfaces 4. When the cylindrical molded body 1 is cut in the width direction, the horizontal dimension is a and the vertical dimension is b.
【0008】この円筒状成形体1を乾燥すると、図4に
示すように、乾燥体11が得られる。ここで、杯土の粒
度分布、杯土の水分含有量、セラミックスの種類等によ
っては、乾燥体11の垂直方向の寸法bが水平方向の寸
法aより大きくなり、縦長の楕円形状に変形した。しか
も、本発明者は、平坦な支持面の上でも円筒状成形体1
の乾燥実験を行ったが、やはり縦長の楕円形状に変形し
た。こうした変形は、重力の方向にも反するものであ
る。When the cylindrical molded body 1 is dried, a dried body 11 is obtained as shown in FIG. Here, depending on the particle size distribution of the clay, the moisture content of the clay, the type of ceramics, and the like, the vertical dimension b of the dried body 11 was larger than the horizontal dimension a, and was deformed into a vertically long elliptical shape. Moreover, the present inventor has found that the cylindrical molded product 1 can be formed even on a flat supporting surface.
Was subjected to a drying experiment, but was also transformed into a vertically long elliptical shape. Such deformation is also against the direction of gravity.
【0009】ここで本発明者は、筒状成形体を支持台の
上に載置し、筒状成形体の少なくとも内側空間に、10
m/秒以上の流速で気体を流し、筒状成形体の内面側が
外面側と同等以上に早く乾燥するようにしたところ、上
記のような変形が顕著に抑えられることを見いだした。
この原因は明らかではないが、水分量がまだ多い段階で
筒状成形体の内表面の乾燥を促進させておくことで、不
均一な収縮を抑制できるものと考えられる。また、本発
明の乾燥方法によれば、多数の筒状成形体を同時に処理
できるので、量産に極めて適している。Here, the present inventor places the cylindrical molded body on a support base and places at least 10 mm in the inner space of the cylindrical molded body.
When a gas was flowed at a flow rate of m / sec or more so that the inner surface side of the cylindrical molded body dries faster than the outer surface side, it was found that the above-mentioned deformation was remarkably suppressed.
Although the cause is not clear, it is considered that uneven shrinkage can be suppressed by promoting drying of the inner surface of the cylindrical molded body at a stage where the water content is still large. Further, according to the drying method of the present invention, a large number of cylindrical molded bodies can be processed at the same time, which is extremely suitable for mass production.
【0010】筒状成形体の内側空間に流す気体を空気と
すると、最もコストを低減できる。また、ボンベから気
体を供給してもよい。気体の温度は、10〜80℃でよ
く、20〜60℃が好ましい。気体を室温よりも加熱す
ると、乾燥時間を短縮しうる。[0010] When air is used as the gas flowing into the inner space of the cylindrical molded body, the cost can be reduced most. Further, gas may be supplied from a cylinder. The temperature of the gas may be from 10 to 80C, preferably from 20 to 60C. Heating the gas above room temperature can reduce the drying time.
【0011】また、筒状成形体を乾燥する際、乾燥後の
乾燥体の水分含有量が9重量%以下になるまで乾燥を行
うと、乾燥体の変形量が一層小さくなる。この際の水分
含有量が9重量%を越えると、乾燥体を空気中に放置し
たとき、乾燥体の変形が多少進行する。Further, when the cylindrical molded body is dried until the moisture content of the dried body after drying becomes 9% by weight or less, the amount of deformation of the dried body is further reduced. If the moisture content at this time exceeds 9% by weight, when the dried body is left in the air, the deformation of the dried body proceeds somewhat.
【0012】また、本発明によって筒状成形体を一次乾
燥した後、一次乾燥体を更に二次乾燥すると、焼成時の
クラック防止の点で、一層好ましい。[0012] It is more preferable that the primary dried body is further dried secondarily after the cylindrical molded body is primarily dried according to the present invention, from the viewpoint of preventing cracks during firing.
【0013】特に、寸法精度の厳しい下記のセラミック
スについて、乾燥体の垂直方向の寸法が水平方向の寸法
より大きくなり、縦長の楕円形状に変形することが判明
した。In particular, with respect to the following ceramics having strict dimensional accuracy, it has been found that the vertical dimension of the dried body becomes larger than the horizontal dimension and is deformed into a vertically long elliptical shape.
【0014】安定化または部分安定化ジルコニア粉末、
種々の添加物を加えたまたは加えないLaMnO3 ,L
aCrO3 等のペロブスカイト系複合酸化物粉末、アル
ミナ粉末、ムライト粉末とバインダーを混練し、成形し
て得た筒状成形体。特に、イットリア安定化または部分
安定化ジルコニア粉末、La(Sr)MnO3 、La
(Ca)MnO3 粉末とバインダーを混練し、成形して
得た筒状成形体。A stabilized or partially stabilized zirconia powder,
LaMnO 3 , L with or without various additives
A cylindrical compact obtained by kneading a perovskite-based composite oxide powder such as aCrO 3 , an alumina powder, a mullite powder and a binder, and molding. In particular, yttria-stabilized or partially-stabilized zirconia powder, La (Sr) MnO 3 , La
(Ca) A cylindrical molded body obtained by kneading and molding a MnO 3 powder and a binder.
【0015】また、杯土の粒度分布を0.1〜20μm
とし、杯土の水分含有量を5〜15%としたとき、乾燥
体の垂直方向の寸法が水平方向の寸法より大きくなり、
縦長の楕円形状に変形することが判明した。Further, the particle size distribution of the clay is 0.1 to 20 μm.
And when the moisture content of the clay is 5 to 15%, the vertical dimension of the dried body becomes larger than the horizontal dimension,
It was found that it was transformed into a vertically long elliptical shape.
【0016】[0016]
【実施例】本発明で用いる支持台は、複数の細長い溝が
設けられているものが好ましく、この溝にセラミック筒
状成形体を載置できるように、溝の寸法と形状とを選択
できる。溝の幅方向輪郭は、円弧状、三角形等であって
よい。また、表面が平坦な支持台も使用できる。DESCRIPTION OF THE PREFERRED EMBODIMENTS The support base used in the present invention is preferably provided with a plurality of elongated grooves, and the dimensions and shape of the grooves can be selected so that the ceramic cylindrical molded body can be placed in these grooves. The profile in the width direction of the groove may be an arc, a triangle, or the like. A support having a flat surface can also be used.
【0017】以下、更に具体的な実験結果について述べ
る。平均粒径D50=5μmのイットリア安定化ジルコニ
ア粉末100重量部に対し、3重量部のポリビニルアル
コールを主バインダーとして加え、混練し、水分量が1
2重量%の混練物を得た。これを真空土練機に入れ、外
径が直径20mm、肉厚2mm、長さ1500mmの円筒
状成形体を押出成形した。Hereinafter, more specific experimental results will be described. To 100 parts by weight of the yttria-stabilized zirconia powder having an average particle diameter D 50 = 5 μm, 3 parts by weight of polyvinyl alcohol was added as a main binder, kneaded, and the water content was 1%.
2% by weight of a kneaded product was obtained. This was put into a vacuum kneader, and a cylindrical molded body having an outer diameter of 20 mm, a thickness of 2 mm, and a length of 1500 mm was extruded.
【0018】次いで、図1、図2、図3に模式的に示す
方法で円筒状成形体1を支持台3上に載置し、円筒状成
形体1の乾燥を行った。支持台3の平板3aは略長方形
であり、平板3aの下側に脚部3bが設けられる。平板
3aの上側面に、細長い、幅方向断面が三角形の突起3
cが、互いにほぼ平行に複数本設けられている。Next, the cylindrical molded body 1 was placed on the support 3 by a method schematically shown in FIGS. 1, 2 and 3, and the cylindrical molded body 1 was dried. The flat plate 3a of the support 3 is substantially rectangular, and a leg 3b is provided below the flat plate 3a. On the upper surface of the flat plate 3a, a projection 3 having a slender, triangular cross section in the width direction.
A plurality of c are provided substantially parallel to each other.
【0019】各突起3cにはそれぞれ傾斜面4が形成さ
れており、一対の互いに対向する傾斜面4の間に、上記
の円筒状成形体1が載置されている。なお、傾斜面4が
水平面となす角度は、15〜75度とすると好ましく、
30〜45度とすると更に好ましい。本実施例では、こ
の角度を45度とした。An inclined surface 4 is formed on each of the projections 3c, and the cylindrical molded body 1 is placed between a pair of opposed inclined surfaces 4. Note that the angle formed by the inclined surface 4 with the horizontal plane is preferably 15 to 75 degrees,
More preferably, the angle is 30 to 45 degrees. In the present embodiment, this angle is 45 degrees.
【0020】下記の表1に示すようにして、円筒状成形
体1の内面側及び/又は外面側に空気を流し、乾燥を行
った。即ち、表1に示す本発明例1─4、比較例5、8
においては、円筒状成形体1の内側空間5に空気を流し
た。この際の流速(m/秒)も表1に示す。本発明例4
及び比較例7、8においては、円筒状成形体1の外面側
に空気を流した。この際の流速(m/秒)も表1に示
す。As shown in Table 1 below, air was flowed on the inner surface side and / or outer surface side of the cylindrical molded body 1 to perform drying. That is, Examples 1 to 4 of the present invention and Comparative Examples 5 and 8 shown in Table 1
In, air was flowed into the inner space 5 of the cylindrical molded body 1. Table 1 also shows the flow rate (m / sec) at this time. Invention Example 4
In Comparative Examples 7 and 8, air was caused to flow on the outer surface side of the cylindrical molded body 1. Table 1 also shows the flow rate (m / sec) at this time.
【0021】また、表1に、空気を流す時間(分)を示
した。ただし、比較例6においては3日間空気を流し、
比較例7においては1日間空気を流した。Table 1 shows the time (minutes) for flowing air. However, in Comparative Example 6, air was flowed for three days,
In Comparative Example 7, air was flowed for one day.
【0022】そして、乾燥後の乾燥体11(図4参照)
の水分含有量を、乾燥体11の内面側、外面側及び乾燥
体の全体について、それぞれ測定した。また、乾燥体1
1の水平方向の寸法aと、垂直方向の寸法bの差(乾燥
体の変形量)b−a(mm)を測定した。各例について
の測定個数はそれぞれ10個とし、その平均値を表1に
示した。The dried body 11 after drying (see FIG. 4)
Was measured for the inner surface side, outer surface side, and the entire dried body 11 of the dried body 11, respectively. Dried body 1
The difference (amount of deformation of the dried body) ba (mm) between the horizontal dimension a and the vertical dimension b of 1 was measured. The number of measurements for each example was 10 and the average value is shown in Table 1.
【0023】ここで、円筒状成形体1の内側空間5に空
気を流した実験例においては、次のようにして空気を供
給した。図2に示すように円筒状成形体1を支持台3上
に載置した直後に、円筒状成形体1の内側に空気を流し
た。このとき、図1に模式的に示すように、送風機6の
吹出口にフレキシブルチューブ7の一端を取り付け、フ
レキシブルチューブ7の他端を分配機8に取り付けた。Here, in an experimental example in which air was flowed into the inner space 5 of the cylindrical molded body 1, air was supplied as follows. Immediately after the cylindrical molded body 1 was placed on the support 3 as shown in FIG. 2, air was flowed inside the cylindrical molded body 1. At this time, as schematically shown in FIG. 1, one end of the flexible tube 7 was attached to the outlet of the blower 6, and the other end of the flexible tube 7 was attached to the distributor 8.
【0024】分配機8には複数本のノズル9が設けられ
ている。円筒状成形体1の押出し後方部1b側の開口2
Bに、それぞれノズル9を挿入した。そして、各ノズル
9から空気を吹き出させると、この空気は円筒状成形体
1の内側空間5を流れ、押出し前方部1a側の開口2A
から吹き出した。本実施例では、空気の温度を30℃と
した。The dispenser 8 is provided with a plurality of nozzles 9. Opening 2 on the side of extrusion rear part 1b of cylindrical molded body 1
Nozzles 9 were inserted into B, respectively. When air is blown out from each nozzle 9, the air flows through the inner space 5 of the cylindrical molded body 1, and is extruded into the opening 2 </ b> A on the front part 1 a side.
Blew out from In this embodiment, the temperature of the air is set to 30 ° C.
【0025】[0025]
【表1】 [Table 1]
【0026】表1から判るように、本発明例1〜4で
は、円筒状成形体1の少なくとも内側空間5に空気を流
し、円筒状成形体1の内面側が外面側と同等以上に早く
乾燥するようにしたところ、乾燥体11の変形量(b−
a)が顕著に小さくなり、0.15mm以下になった。
一方、比較例5では、空気の流速が5mm/秒である
が、乾燥体11の変形量(b−a)は0.18mmにな
った。As can be seen from Table 1, in Examples 1 to 4 of the present invention, air is caused to flow in at least the inner space 5 of the cylindrical molded body 1 so that the inner surface side of the cylindrical molded body 1 is dried at least as quickly as the outer surface side. Then, the amount of deformation of the dried body 11 (b−
a) was remarkably reduced to 0.15 mm or less.
On the other hand, in Comparative Example 5, although the air flow rate was 5 mm / sec, the amount of deformation (ba) of the dried body 11 was 0.18 mm.
【0027】一方、比較例6では、円筒状成形体1を自
然乾燥しているが、乾燥体11の変形量が大きいし、乾
燥に3日も時間がかかるので、大量生産には向かない。
比較例7では、円筒状成形体1の外面側に空気を流し、
内側空間5には空気を流していないが、乾燥体11の変
形量が大きいし、乾燥にも時間がかかるので、大量生産
には向かない。On the other hand, in Comparative Example 6, although the cylindrical molded body 1 is naturally dried, the amount of deformation of the dried body 11 is large, and it takes three days to dry, so it is not suitable for mass production.
In Comparative Example 7, air was caused to flow on the outer surface side of the cylindrical molded body 1,
Although no air is flowed through the inner space 5, the drying body 11 is not suitable for mass production because the amount of deformation of the drying body 11 is large and drying takes time.
【0028】比較例8では、円筒状成形体1の外面側及
び内側空間5に空気を流しているが、乾燥体11におい
て、外面側の方が内面側の方よりも、水分含有量が小さ
くなり、乾燥が進んでいる。この結果、乾燥体11の変
形量は、0.35mmに達する。In Comparative Example 8, air is flown on the outer surface side and the inner space 5 of the cylindrical molded body 1. However, in the dried body 11, the moisture content is smaller on the outer surface side than on the inner surface side. And drying is progressing. As a result, the amount of deformation of the dried body 11 reaches 0.35 mm.
【0029】なお、La(Ca)MnO3 粉末、La
(Sr)MnO3 粉末、LaCrO3粉末又はアルミナ
粉末とバインダーとをそれぞれ混練した。そして、これ
らの各混練物を成形して得た各円筒状成形体について、
それぞれ上記の実験と同様の実験結果を得た。また、本
発明は、乾燥体11の水平方向の寸法aが垂直方向の寸
法bより大きくなり、横長の楕円形状に変形するような
場合にも、効果があった。Note that La (Ca) MnO 3 powder, La
(Sr) MnO 3 powder, LaCrO 3 powder or alumina powder and a binder were kneaded respectively. And about each cylindrical molded body obtained by molding each of these kneaded materials,
Experimental results similar to those described above were obtained. The present invention is also effective in the case where the horizontal dimension a of the dried body 11 becomes larger than the vertical dimension b and is deformed into a horizontally long elliptical shape.
【0030】[0030]
【発明の効果】以上述べたように、本発明によれば、セ
ラミック筒状成形体を乾燥する際に、乾燥体の水平方向
の寸法と垂直方向の寸法との間に差が生じ、所定の寸法
から変形するのを防止できる。しかも、本発明の乾燥方
法によれば、多数の筒状成形体を同時に乾燥処理できる
ので、量産に極めて適している。As described above, according to the present invention, when the ceramic cylindrical molded body is dried, a difference is generated between the horizontal dimension and the vertical dimension of the dried body, and a predetermined value is obtained. Deformation from dimensions can be prevented. Moreover, according to the drying method of the present invention, a large number of cylindrical molded bodies can be dried at the same time, which is very suitable for mass production.
【図1】円筒状成形体1の内側空間5に気体を供給し、
乾燥している状態を模式的に示す平面図である。FIG. 1 supplies gas to an inner space 5 of a cylindrical molded body 1,
FIG. 3 is a plan view schematically showing a dry state.
【図2】複数の円筒状成形体1を支持台3の上に載置し
ている状態を示す斜視図である。FIG. 2 is a perspective view showing a state in which a plurality of cylindrical molded bodies 1 are mounted on a support 3;
【図3】複数の円筒状成形体1を支持台3の上に載置し
ている状態を、模式的に示す正面図である。FIG. 3 is a front view schematically showing a state in which a plurality of cylindrical molded bodies 1 are mounted on a support 3;
【図4】乾燥体11を支持台3の上に載置している状態
を、模式的に示す正面図である。FIG. 4 is a front view schematically showing a state in which the dried body 11 is placed on a support 3;
1 円筒状成形体 2A,2B 開口 3 支持台 5 円筒状成形体の内側 11 乾燥体 a 乾燥体11の水平方向の寸法 b 乾燥体11の垂直方向の寸法 DESCRIPTION OF SYMBOLS 1 Cylindrical molded body 2A, 2B opening 3 Support stand 5 Inside of cylindrical molded body 11 Dry body a Horizontal dimension of dry body 11 b Vertical dimension of dry body 11
Claims (4)
置し、前記セラミック筒状成形体の内面側が外面側と同
等以上に早く乾燥するようにこのセラミック筒状成形体
の少なくとも内側空間に10m/秒以上の流速で気体を
流すことを特徴とする、セラミック筒状成形体の乾燥方
法。1. A ceramic cylindrical molded body is placed on a support, and at least an inner space of the ceramic cylindrical molded body is dried so that an inner surface side of the ceramic cylindrical molded body is dried at least as quickly as an outer surface side. A method of drying a ceramic cylindrical molded body, characterized by flowing a gas at a flow rate of 10 m / sec or more.
ルコニア粉末、部分安定化ジルコニア粉末、ランタンマ
ンガネート粉末、ランタンクロマイト粉末、アルミナ粉
末およびムライト粉末からなる群より選ばれた一種以上
のセラミック粉末とバインダーとを混練し、成形して得
たセラミック筒状成形体であることを特徴とする、請求
項1記載のセラミック筒状成形体の乾燥方法。2. The ceramic tubular molded body according to claim 1, wherein the ceramic cylindrical compact is at least one ceramic powder selected from the group consisting of stabilized zirconia powder, partially stabilized zirconia powder, lanthanum manganate powder, lanthanum chromite powder, alumina powder, and mullite powder. The method for drying a ceramic tubular molded body according to claim 1, wherein the ceramic tubular molded body is obtained by kneading and molding a binder and a binder.
土の粒度分布が0.1〜20μmであり、前記杯土の水
分含有量が5〜15%であることを特徴とする、請求項
1または2記載のセラミック筒状成形体の乾燥方法。3. A method according to claim 1, wherein the particle size distribution of the clay forming the ceramic cylindrical molded body is 0.1 to 20 μm, and the water content of the clay is 5 to 15%. 3. The method for drying a ceramic cylindrical molded body according to 1 or 2.
置し、前記セラミック筒状成形体の内面側が外面側と同
等以上に早く乾燥するようにこのセラミック筒状成形体
の少なくとも内側空間に10m/秒以上の流速で気体を
流すことによって、一次乾燥体を得、次いで、この一次
乾燥体を二次乾燥する、セラミック筒状成形体の乾燥方
法。4. A ceramic cylindrical molded body is placed on a support table, and at least an inner space of the ceramic cylindrical molded body is dried so that an inner surface side of the ceramic cylindrical molded body is dried at least as quickly as an outer surface side. A method for drying a ceramic tubular molded body, comprising: obtaining a primary dried body by flowing a gas at a flow rate of 10 m / sec or more through the air, and then secondary drying the primary dried body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5129058A JP2637678B2 (en) | 1993-05-31 | 1993-05-31 | Drying method of ceramic cylindrical molded body |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5129058A JP2637678B2 (en) | 1993-05-31 | 1993-05-31 | Drying method of ceramic cylindrical molded body |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH06335910A JPH06335910A (en) | 1994-12-06 |
| JP2637678B2 true JP2637678B2 (en) | 1997-08-06 |
Family
ID=15000053
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5129058A Expired - Lifetime JP2637678B2 (en) | 1993-05-31 | 1993-05-31 | Drying method of ceramic cylindrical molded body |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2637678B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000043024A (en) * | 1998-07-29 | 2000-02-15 | Ibiden Co Ltd | Method and device for cut-treatment of ceramic molding |
| JP6954746B2 (en) * | 2017-02-20 | 2021-10-27 | 三菱パワー株式会社 | Ceramic molded body manufacturing method and ceramic molded body manufacturing equipment |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05285929A (en) * | 1992-04-09 | 1993-11-02 | Takeda Chem Ind Ltd | Method for drying hollow molded article |
-
1993
- 1993-05-31 JP JP5129058A patent/JP2637678B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH06335910A (en) | 1994-12-06 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US3899326A (en) | Method of making monolithic honeycombed structures | |
| EP0650944A1 (en) | Extrusion of low viscosity batch | |
| KR970000478A (en) | Cross-flow honeycomb structure and its manufacturing method | |
| CN105358298B (en) | The rapid draing of ceramic green object | |
| JP2637678B2 (en) | Drying method of ceramic cylindrical molded body | |
| JP5964205B2 (en) | Green honeycomb molded body pedestal and diesel particulate filter manufacturing method | |
| US9561985B2 (en) | Method for manufacturing ceramic honeycomb fired body | |
| PL203853B1 (en) | Method for manufacturing honeycomb structure | |
| JP2813127B2 (en) | Drying method of ceramic molded body | |
| JP4106918B2 (en) | Cutting method of honeycomb molded body | |
| US20200203748A1 (en) | Ceramic Sheet and Method for Manufacturing the Same | |
| JP7422853B2 (en) | Dielectric drying method and dielectric drying device for ceramic molded body, and manufacturing method for ceramic structure | |
| JP5267868B2 (en) | Method for manufacturing thermistor element | |
| JP2558747B2 (en) | Method for forming ceramic coil spring | |
| JPH0818320B2 (en) | Extrusion molding machine | |
| JPH0832410B2 (en) | Method for forming ceramic coil spring | |
| JP6027435B2 (en) | Manufacturing method of diesel particulate filter and cradle for green honeycomb molded body | |
| CN207387959U (en) | A kind of airing device of ceramic body | |
| CN117968355A (en) | Silicon carbide roller blank embryo extrusion suspension drying device and use method thereof | |
| JPH08103905A (en) | Hollow extrusion plate manufacturing equipment | |
| JPH0798688B2 (en) | Ceramic material for extrusion molding and extrusion molding method thereof | |
| JPH04300252A (en) | Burning of ceramic honeycomb structure | |
| WO2024034257A1 (en) | Firing jig comprising setter and bottom plate | |
| JP7253892B2 (en) | honeycomb structure | |
| JP2002348179A (en) | Method of firing cylindrical ceramic molded body |