JP2002283329A - Manufacturing method of honeycomb formed body and drying equipment thereof - Google Patents
Manufacturing method of honeycomb formed body and drying equipment thereofInfo
- Publication number
- JP2002283329A JP2002283329A JP2001370393A JP2001370393A JP2002283329A JP 2002283329 A JP2002283329 A JP 2002283329A JP 2001370393 A JP2001370393 A JP 2001370393A JP 2001370393 A JP2001370393 A JP 2001370393A JP 2002283329 A JP2002283329 A JP 2002283329A
- Authority
- JP
- Japan
- Prior art keywords
- drying
- honeycomb formed
- formed body
- inlet
- microwave
- 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.)
- Pending
Links
Classifications
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05B—ELECTRIC HEATING; ELECTRIC LIGHT SOURCES NOT OTHERWISE PROVIDED FOR; CIRCUIT ARRANGEMENTS FOR ELECTRIC LIGHT SOURCES, IN GENERAL
- H05B2206/00—Aspects relating to heating by electric, magnetic, or electromagnetic fields covered by group H05B6/00
- H05B2206/04—Heating using microwaves
- H05B2206/046—Microwave drying of wood, ink, food, ceramic, sintering of ceramic, clothes, hair
Landscapes
- Drying Of Solid Materials (AREA)
- Devices For Post-Treatments, Processing, Supply, Discharge, And Other Processes (AREA)
Abstract
Description
【0001】[0001]
【技術分野】本発明は,ハニカム成形体の製造方法,特
にその乾燥工程および乾燥装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing a honeycomb formed body, and more particularly to a drying step and a drying apparatus for the same.
【0002】[0002]
【従来技術】セラミック製のハニカム成形体を製造する
に当たっては,粘土質のハニカム成形体を押出成形し,
これを乾燥した後,焼成する。ハニカム成形体の乾燥方
法としては,例えば特開昭63−166745号公報に
示されているように,ハニカム成形体の上方及び下方に
配置した電極間に電流を流して発生させた高周波を用い
る方法が知られている。この方法は,ハニカム成形体の
内外を均一に加熱し,乾燥速度差により生じる収縮量差
が原因となる外周スキン部の割れ,しわ等の欠陥の発生
を防止しようとするものである。2. Description of the Related Art In manufacturing a honeycomb formed body made of ceramic, a honeycomb formed body made of clay is extruded and formed.
After being dried, it is fired. As a method for drying a honeycomb formed body, for example, as disclosed in JP-A-63-166745, a method using a high frequency generated by passing a current between electrodes disposed above and below the honeycomb formed body is used. It has been known. This method is intended to uniformly heat the inside and outside of the honeycomb formed body and to prevent the occurrence of defects such as cracks and wrinkles in the outer peripheral skin portion caused by a difference in shrinkage caused by a difference in drying speed.
【0003】[0003]
【解決しようとする課題】上記乾燥方法は,従来自動車
の排ガス浄化装置の触媒担体として一般的に用いられて
きたセル壁厚さ0.30〜0.15mm,外周スキン部
の厚さ0.3〜1.0mmのハニカム成形体に対しては
有効である。しかしながら,近年の排気ガス浄化性能向
上等のニーズにより開発されてきたセル壁厚さが0.1
25mm以下で,外周スキン部の厚さが0.5mm以下
の薄壁品においては,セル壁自身の強度および外周スキ
ン部自身の強度が従来よりも低い。そのため,この薄壁
品においては,従来の高周波を用いた方法では,外周ス
キン部の欠陥発生に対する十分な対策が困難となってき
た。The above-mentioned drying method uses a cell wall thickness of 0.30 to 0.15 mm and a peripheral skin thickness of 0.3 to 0.1 mm, which has been generally used as a catalyst carrier of an exhaust gas purifying apparatus for automobiles. This is effective for a honeycomb formed body of about 1.0 mm. However, the cell wall thickness, which has been developed in response to recent needs for improving exhaust gas purification performance, is 0.1%.
In a thin-walled product having a thickness of 25 mm or less and a thickness of the outer skin portion of 0.5 mm or less, the strength of the cell wall itself and the strength of the outer skin portion itself are lower than those in the related art. Therefore, in this thin-walled product, it has become difficult to take sufficient measures against the occurrence of defects in the outer skin portion by the conventional method using high frequency.
【0004】本発明はかかる従来の問題点に鑑みてなさ
れたもので,セル壁厚さが0.125mm以下のハニカ
ム成形体を,外周スキン部に割れ,しわ等の欠陥を生じ
させることなく乾燥することができるハニカム成形体の
製造方法及び乾燥装置を提供しようとするものである。The present invention has been made in view of the above-mentioned conventional problems, and is intended to dry a honeycomb formed body having a cell wall thickness of 0.125 mm or less without causing defects such as cracks and wrinkles in an outer peripheral skin portion. It is an object of the present invention to provide a method for manufacturing a honeycomb formed body and a drying apparatus which can perform the method.
【0005】[0005]
【課題の解決手段】請求項1の発明は,厚さ0.125
mm以下のセル壁をハニカム状に配して多数のセルを設
けたセラミック製のハニカム成形体を製造する方法にお
いて,押出成形された粘土質のハニカム成形体を乾燥す
るに当たり,誘電損失が0.1以下,気孔率が10%以
上,断面開口面積比が50%以上の多孔質のセラミック
スよりなる搬送トレイに載置した上記ハニカム成形体
を,湿度が70%以上の高湿度雰囲気に晒すと共に,周
波数1000〜10000MHz領域のマイクロ波を照
射することを特徴とするハニカム成形体の製造方法にあ
る。The invention according to claim 1 has a thickness of 0.125.
In a method of manufacturing a ceramic honeycomb formed body provided with a large number of cells by arranging cell walls of not more than 1 mm in a honeycomb shape, dielectric loss is reduced to about 0.1 mm when the extruded clayey honeycomb formed body is dried. The honeycomb formed body placed on a transfer tray made of porous ceramics having a porosity of 10% or less and a cross-sectional area ratio of open area of 50% or more is exposed to a high-humidity atmosphere of 70% or more. A method for manufacturing a honeycomb formed body, which comprises irradiating a microwave having a frequency of 1,000 to 10,000 MHz.
【0006】本発明の製造方法においては,上記のごと
く,湿度が70%以上という高湿度雰囲気において上記
ハニカム成形体を加熱する。これにより,ハニカム成形
体の外周表面が変形するような急激な乾燥を防止して外
周表面を適度な湿度に保つことができる。これにより,
外周表面と内部との乾燥速度差を低減することができ
る。そのため,セル壁厚さが0.125mm以下と薄
く,外周スキン部の厚みも比較的薄い場合においても,
ハニカム成形体の内外の乾燥速度差による収縮量差を小
さくすることができる。それ故,外周スキン部の割れ,
しわ等の欠陥を防止することができる。上記高湿度雰囲
気の湿度としては高いほどより好ましく,80%以上,
あるいは過飽和状態でもよい。In the manufacturing method of the present invention, as described above, the honeycomb formed body is heated in a high humidity atmosphere having a humidity of 70% or more. Accordingly, it is possible to prevent rapid drying such that the outer peripheral surface of the honeycomb formed body is deformed, and to maintain the outer peripheral surface at an appropriate humidity. This gives
The difference in drying speed between the outer peripheral surface and the inside can be reduced. Therefore, even when the cell wall thickness is as thin as 0.125 mm or less and the outer skin portion is relatively thin,
The difference in shrinkage due to the difference in drying speed between the inside and outside of the honeycomb formed body can be reduced. Therefore, cracks in the outer skin,
Defects such as wrinkles can be prevented. The higher the humidity of the high humidity atmosphere is, the more preferable it is.
Alternatively, it may be in a supersaturated state.
【0007】また,本発明においては,上記加熱の手段
として,上記マイクロ波を用いる。これにより,上記高
湿度雰囲気での加熱を実現することができる。すなわ
ち,従来の高周波による加熱の場合,ハニカム成形体の
近傍に電極を配置する必要がある。この電極を高湿度雰
囲気内に配置すれば,電極間で放電や絶縁破壊を起こ
し,電極破損による設備故障が生じるおそれがある。In the present invention, the microwave is used as the heating means. Thereby, heating in the high humidity atmosphere can be realized. That is, in the case of the conventional high-frequency heating, it is necessary to arrange an electrode near the honeycomb formed body. If these electrodes are placed in a high humidity atmosphere, discharge or dielectric breakdown may occur between the electrodes, and equipment failure due to electrode damage may occur.
【0008】これに対し,上記マイクロ波は,導波管を
通じて導くことが可能であり,被加熱物の近傍に電極を
設ける必要がない。そのため,マイクロ波は,上記高湿
度雰囲気においても容易にハニカム成形体に到達し,こ
れを加熱することができる。このように,本発明では,
マイクロ波加熱と高湿度雰囲気との組合せによって,セ
ル壁厚さが0.125mmと非常に薄く,外周スキン部
も比較的薄い場合においても,乾燥時の外周スキン部の
割れやしわの発生を十分に防止することができる。そし
て,この乾燥時の品質向上によって,その後の焼成工程
を経て得られる焼成品としてのハニカム成形体を優れた
品質とすることができる。On the other hand, the microwave can be guided through the waveguide, and there is no need to provide an electrode near the object to be heated. Therefore, the microwave can easily reach the honeycomb formed body even in the high-humidity atmosphere and can heat it. Thus, in the present invention,
Due to the combination of microwave heating and high humidity atmosphere, even if the cell wall thickness is as thin as 0.125 mm and the outer skin is relatively thin, sufficient cracking and wrinkling of the outer skin during drying can be achieved. Can be prevented. By improving the quality at the time of drying, the honeycomb formed body as a fired product obtained through the subsequent firing step can be made to have excellent quality.
【0009】さらに,本発明においては,上記乾燥は,
誘電損失が0.1以下,気孔率が10%以上,断面開口
面積比が50%以上の多孔質のセラミックスよりなる搬
送トレイに,上記ハニカム成形体を載置して行う。上記
ハニカム成形体を乾燥時に支持する方法としては,上記
特定のセラミックスよりなる搬送トレイを用いる方法の
他に,一般的なセラミックスよりなるトレイを用いるこ
とももちろん可能である。しかしながら,上記の特定の
セラミックスよりなる搬送トレイを用いることにより,
上記ハニカム成形体の乾燥時に,ハニカム成形体とこれ
を支える部材との接触面における不具合発生を抑制する
ことができる。Further, in the present invention, the drying is performed by:
The above-described honeycomb formed body is placed on a carrier tray made of porous ceramics having a dielectric loss of 0.1 or less, a porosity of 10% or more, and a cross-sectional opening area ratio of 50% or more. As a method of supporting the honeycomb formed body at the time of drying, it is of course possible to use a tray made of general ceramics in addition to the method using the above-mentioned transfer tray made of the specific ceramics. However, by using a transfer tray made of the above specific ceramics,
During the drying of the honeycomb formed body, it is possible to suppress the occurrence of problems at the contact surface between the honeycomb formed body and a member supporting the honeycomb formed body.
【0010】すなわち,上記粘土質のハニカム成形体
は,水膜に接していると成分が溶出してしまうことがあ
る。そのため,ハニカム成形体を支える他部材との接触
部分に高湿度雰囲気からの水分あるいはハニカム成形体
から蒸発した水分が滞留した場合には,その接触部分に
おいてハニカム成形体の成分の溶出のおそれがある。こ
れに対し,上記気孔率が10%以上,断面開口面積比が
50%以上の多孔質のセラミックスよりなる搬送トレイ
に,上記ハニカム成形体を載置することにより,搬送ト
レイとハニカム成形体との接触部分近傍に水分が滞留し
ようとしても,搬送トレイの気孔を介した排水作用によ
って水分の滞留を防止することができる。上記気孔率が
10%未満,あるいは断面開口面積比が50%未満の場
合には,排水作用が十分に得られないおそれがある。[0010] That is, in the above-mentioned clay-based honeycomb molded body, components may be eluted when in contact with a water film. Therefore, if moisture from a high-humidity atmosphere or moisture evaporated from the honeycomb formed body stagnates in a contact portion with another member supporting the honeycomb formed body, there is a possibility that components of the honeycomb formed body may be eluted in the contact portion. . On the other hand, by mounting the honeycomb formed body on a transfer tray made of porous ceramics having a porosity of 10% or more and a cross-sectional opening area ratio of 50% or more, the transfer tray and the honeycomb formed body are separated. Even if the water stays in the vicinity of the contact portion, the water can be prevented from staying by the drainage action through the pores of the transport tray. If the porosity is less than 10% or the cross-sectional area ratio is less than 50%, the drainage function may not be sufficiently obtained.
【0011】また,ハニカム成形体を支える他部材が誘
電損失が大きい性質のものである場合には,ハニカム成
形体を加熱するためのマイクロ波によって,この他部材
も加熱される。この場合には,加熱された他部材からの
直接的な伝熱によって,接触部分のハニカム成形体が局
部的に高速で加熱され,変形等を引き起こすおそれがあ
る。これに対し,上記のごとく,誘電損失が0.1以下
の搬送トレイにハニカム成形体を載置することにより,
搬送トレイの加熱を回避することができ,上記不具合を
防止することができる。When the other member supporting the honeycomb formed body has a property of a large dielectric loss, the other member is also heated by the microwave for heating the honeycomb formed body. In this case, due to direct heat transfer from the heated other member, the honeycomb formed body at the contact portion may be locally heated at a high speed to cause deformation or the like. On the other hand, as described above, by placing the honeycomb formed body on the transfer tray having a dielectric loss of 0.1 or less,
Heating of the transfer tray can be avoided, and the above-described problems can be prevented.
【0012】次に,請求項2の発明のように,上記ハニ
カム成形体は,上記セルの開口端面の一方を上記搬送ト
レイの上面に当接させて載置することが好ましい。上記
搬送トレイへのハニカム成形体の載置方向は任意の方向
をとることができる。ただし,特に上記のごとくセルの
開口端面の一方を搬送トレイの上面に当接させた場合に
は,搬送トレイの気孔とハニカム成形体のセルとの連通
性を確保することができる。Next, as in the second aspect of the present invention, it is preferable that the honeycomb formed body is placed with one of the open end faces of the cell in contact with the upper surface of the transport tray. The mounting direction of the honeycomb formed body on the transport tray can be any direction. However, especially when one of the open end surfaces of the cells is brought into contact with the upper surface of the transport tray as described above, the communication between the pores of the transport tray and the cells of the honeycomb formed body can be ensured.
【0013】また,請求項3の発明のように,上記搬送
トレイは,尿素樹脂フォームよりなることが好ましい。
この場合には,上記誘電損失特性,気孔率,断面開口面
積比が上記好適な範囲にある優れた搬送トレイを容易に
得ることができる。Preferably, the transport tray is made of urea resin foam.
In this case, it is possible to easily obtain an excellent transport tray having the above-mentioned dielectric loss characteristics, porosity, and cross-sectional opening area ratio in the above-described preferred ranges.
【0014】また,請求項4の発明のように,上記ハニ
カム成形体を乾燥するに当たっては,各ハニカム成形体
は,隣接する他のハニカム成形体との間に一定の間隔を
有するように配置して乾燥することが好ましい。この場
合には,各ハニカム成形体に照射される上記マイクロ波
をより均一化することができ,乾燥ムラの発生を抑制す
ることができる。それ故,乾燥時に発生しうるトラブル
を,さらに十分に防止することができる。In drying the above-mentioned honeycomb formed body as in the invention of claim 4, each honeycomb formed body is arranged so as to have a certain interval between adjacent honeycomb formed bodies. And dried. In this case, the microwave applied to each honeycomb formed body can be made more uniform, and the occurrence of drying unevenness can be suppressed. Therefore, troubles that may occur during drying can be more sufficiently prevented.
【0015】また,請求項5の発明のように,上記ハニ
カム成形体を乾燥するに当たっては,上記ハニカム成形
体の数量に応じて上記マイクロ波の照射条件を変更する
ことが好ましい。この場合には,乾燥槽内の上記ハニカ
ム成形体の数量によらず,各ハニカム成形体に上記マイ
クロ波を均一に照射することができる。それ故,乾燥時
に発生しうるトラブルを,さらに十分に防止することが
できる。In drying the honeycomb formed body, it is preferable to change the microwave irradiation conditions according to the number of the honeycomb formed body. In this case, regardless of the number of the honeycomb formed bodies in the drying tank, each of the honeycomb formed bodies can be uniformly irradiated with the microwave. Therefore, troubles that may occur during drying can be more sufficiently prevented.
【0016】次に,請求項6の発明は,厚さ0.125
mm以下のセル壁をハニカム状に配して多数のセルを設
けたセラミック製のハニカム成形体を製造するに当た
り,押出成形された粘土質のハニカム成形体を乾燥する
乾燥装置であって,上記ハニカム成形体を収納する乾燥
槽と,該乾燥槽内を湿度が70%以上の高湿度雰囲気と
する加湿装置と,周波数1000〜10000MHz領
域のマイクロ波を上記乾燥槽内に供給するマイクロ波発
生装置と,複数のハニカム成形体を連続的に上記乾燥槽
に送入,送出する搬送装置とを有することを特徴とする
ハニカム成形体の乾燥装置である。Next, the invention according to claim 6 has a thickness of 0.125.
a honeycomb drying apparatus for drying an extruded clay-like honeycomb molded body in producing a ceramic honeycomb molded body provided with a large number of cells by arranging cell walls of not more than 1 mm in a honeycomb shape; A drying tank for storing the molded body, a humidifying device for setting the inside of the drying tank to a high humidity atmosphere having a humidity of 70% or more, and a microwave generator for supplying microwaves in a frequency range of 1000 to 10000 MHz into the drying tank. And a conveying device for continuously feeding and discharging a plurality of honeycomb formed bodies into and from the drying tank.
【0017】本発明の乾燥装置を用いれば,上記製造方
法における乾燥を容易に実現することができ,品質に優
れたハニカム成形体を製造することができる。すなわ
ち,上記乾燥槽内に乾燥すべきハニカム成形体を配置
し,上記加湿装置によって乾燥槽内の湿度を70%以上
に高めることにより高湿度雰囲気を形成する。そして,
上記マイクロ波発生装置からマイクロ波を導入すること
により,ハニカム成形体をマイクロ波加熱することがで
きる。これにより,外周スキン部に割れやしわを発生さ
せずにハニカム成形体を乾燥させることができる。By using the drying apparatus of the present invention, drying in the above-described manufacturing method can be easily realized, and a honeycomb formed body having excellent quality can be manufactured. That is, a honeycomb formed body to be dried is placed in the drying tank, and the humidity in the drying tank is increased to 70% or more by the humidifier to form a high humidity atmosphere. And
By introducing microwaves from the microwave generator, the honeycomb formed body can be microwave-heated. Thereby, the honeycomb formed body can be dried without generating cracks and wrinkles in the outer peripheral skin portion.
【0018】さらに,本発明では,上記複数のハニカム
成形体を,連続的に上記乾燥槽に送入,送出する上記搬
送装置を設けてある。そのため,上記ハニカム成形体を
連続的に乾燥することができる。したがって,上記乾燥
装置によれば,上記ハニカム成形体の外周スキン部の割
れやしわの発生を防止しながら,非常に効率良く,上記
ハニカム成形体の乾燥を行うことができる。Further, in the present invention, the above-mentioned conveying device for continuously feeding and discharging the plurality of honeycomb formed bodies into and from the drying tank is provided. Therefore, the honeycomb formed body can be continuously dried. Therefore, according to the drying device, the honeycomb formed body can be dried very efficiently while preventing the outer peripheral skin portion of the honeycomb formed body from cracking and wrinkling.
【0019】また,請求項7の発明のように,上記乾燥
槽は,複数のハニカム成形体を連続的に上記乾燥槽に送
入用及び送出用の開口部を有していると共に,その開口
部において,上記乾燥槽内の高湿度の空気と外気とが混
じり合うことを防止する遮断手段を有していることが好
ましい。この場合には,上記乾燥槽内に均一かつ高湿度
な雰囲気を形成することができる。また,上記乾燥槽内
の高湿度な空気が外部へ流出するのを抑制できるため,
小規模な加湿装置等によって所望の高湿度雰囲気を形成
することができる。According to a seventh aspect of the present invention, the drying tank has openings for feeding and discharging a plurality of honeycomb formed bodies to and from the drying tank continuously. Preferably, the section has a shut-off means for preventing the high-humidity air in the drying tank from mixing with the outside air. In this case, a uniform and high humidity atmosphere can be formed in the drying tank. In addition, since high-humidity air in the drying tank can be prevented from flowing out,
A desired high humidity atmosphere can be formed by a small-scale humidifier or the like.
【0020】また,請求項8の発明のように,上記遮断
手段は,上記開口部を遮閉する空気の流れを形成するこ
とにより,上記乾燥槽内の高湿度雰囲気と外部の雰囲気
を遮断するように構成されていることが好ましい。この
場合には,小規模かつ簡便な設備構成によって,上記の
作用効果を得ることができる。According to the present invention, the shut-off means cuts off the high-humidity atmosphere in the drying tank from the outside atmosphere by forming a flow of air which shuts off the opening. It is preferable that it is comprised as follows. In this case, the above-described effects can be obtained with a small-sized and simple equipment configuration.
【0021】また,請求項9の発明のように,上記乾燥
装置は,上記乾燥槽内にあるハニカム成形体の数量に応
じて,上記マイクロ波の照射条件を変更するように構成
されていることが好ましい。この場合には,上記乾燥槽
内にあるハニカム成形体数量が変動する場合であって
も,各ハニカム成形体に照射されるマイクロ波の量を均
一化できる。According to a ninth aspect of the present invention, the drying device is configured to change the microwave irradiation conditions according to the number of honeycomb formed bodies in the drying tank. Is preferred. In this case, even if the number of honeycomb formed bodies in the drying tank varies, the amount of microwaves applied to each honeycomb formed body can be made uniform.
【0022】また,請求項10の発明のように,上記搬
送装置は,上記乾燥槽内に送入された各ハニカム成形体
が等間隔に配置されるように,上記ハニカム成形体の供
給を調整するアキュームレータ機能を有していることが
好ましい。ここで,上記アキュムレータ機能とは,上記
搬送装置へ供給される上記ハニカム成形体の供給量のば
らつきを調整し,上記ハニカム成形体を,一定の間隔で
上記乾燥槽に送入する機能である。上記アキュームレー
タ機能によれば,上記搬送装置への上記ハニカム成形体
の供給の状況によらず,上記乾燥槽内において,各ハニ
カム成形体を等間隔に配置した状態で搬送することがで
きる。According to a tenth aspect of the present invention, the transport device adjusts the supply of the honeycomb formed bodies so that the honeycomb formed bodies fed into the drying tank are arranged at equal intervals. It is preferable to have an accumulator function. Here, the accumulator function is a function of adjusting a variation in the supply amount of the honeycomb formed body supplied to the transfer device and feeding the honeycomb formed body to the drying tank at regular intervals. According to the accumulator function, the honeycomb formed bodies can be conveyed in the drying tank in a state where they are arranged at equal intervals, regardless of the supply state of the honeycomb formed bodies to the transfer device.
【0023】また,請求項11の発明のように,上記乾
燥装置は,上記マイクロ波を導入する導入口を複数有し
ていることが好ましい。複数の導入口から,上記マイク
ロ波を照射すれば,上記乾燥槽内のマイクロ波密度のば
らつきを抑制することができる。それ故,乾燥ムラを抑
制することができ,本発明による作用効果をさらに高め
ることができる。Preferably, the drying apparatus has a plurality of inlets for introducing the microwave. By irradiating the microwaves from a plurality of inlets, variations in the microwave density in the drying tank can be suppressed. Therefore, drying unevenness can be suppressed, and the operation and effect of the present invention can be further enhanced.
【0024】また,請求項12の発明のように,上記乾
燥装置は,上記ハニカム成形体を上記乾燥槽に送入する
ための開口部近傍に設けた第1導入口と,上記ハニカム
成形体を上記乾燥槽から送出するための開口部近傍に設
けた第2導入口とを有しており,上記第1導入口は,上
記送出側の開口部に向けて上記マイクロ波を照射し,上
記第2導入口は,上記送入側の開口部に向けて上記マイ
クロ波を照射するよう構成されていることが好ましい。
搬送方向に沿って,対向する方向からマイクロ波を照射
することにより,上記乾燥槽の送入側と送出側とにおい
て,上記マイクロ波密度のばらつきを,さらに抑制する
ことができる。According to a twelfth aspect of the present invention, the drying device includes a first inlet provided near an opening through which the honeycomb formed body is fed into the drying tank; A second inlet provided in the vicinity of an opening for sending out from the drying tank; the first inlet irradiates the microwave toward the opening on the sending side; It is preferable that the second inlet is configured to irradiate the microwave toward the opening on the sending side.
By irradiating microwaves from opposite directions along the transport direction, it is possible to further suppress the variation in the microwave density between the sending side and the sending side of the drying tank.
【0025】また,請求項13の発明のように,上記乾
燥装置は,上記ハニカム成形体を上記乾燥槽に送入する
ための開口部の上側に設けた第1導入口と,上記開口部
の下側に設けた第2導入口とを有しており,上記第1導
入口及び上記第2導入口は,上記ハニカム成形体を上記
乾燥槽から送出するための開口部に向けて上記マイクロ
波を照射するよう構成されていることが好ましい。上記
のごとく,上記マイクロ波の導入口を配置することによ
り,上記乾燥槽の鉛直方向において,上記マイクロ波密
度のばらつきを,さらに抑制することができる。According to a thirteenth aspect of the present invention, the drying device further comprises a first inlet provided above an opening through which the honeycomb formed body is fed into the drying tank; A second inlet provided on the lower side, wherein the first inlet and the second inlet are connected to the microwave toward an opening for sending out the honeycomb formed body from the drying tank. Is preferably configured to be irradiated. As described above, by arranging the microwave introduction port, the variation in the microwave density in the vertical direction of the drying tank can be further suppressed.
【0026】また,請求項14の発明のように,上記乾
燥装置は,上記乾燥槽の上部に設けた第1導入口と,上
記乾燥槽の下部に設けた第2導入口を有しており,上記
第1導入口は,上記乾燥槽の下部に向って上記マイクロ
波を照射し,上記第2導入口は,上記乾燥槽の上部に向
って上記マイクロ波を照射するよう構成されていること
が好ましい。鉛直方向に沿って,対向する方向からマイ
クロ波を照射することにより,上記乾燥槽の上側と下側
とにおいて,上記マイクロ波密度のばらつきを,さらに
抑制することができる。According to a fourteenth aspect of the present invention, the drying apparatus has a first inlet provided at an upper part of the drying tank and a second inlet provided at a lower part of the drying tank. The first inlet irradiates the microwave toward a lower portion of the drying tank, and the second inlet irradiates the microwave toward an upper portion of the drying tank. Is preferred. By irradiating the microwaves from opposite directions along the vertical direction, the variation in the microwave density between the upper side and the lower side of the drying tank can be further suppressed.
【0027】また,請求項15の発明のように,上記乾
燥装置は,上記乾燥槽内側の側面であって上記搬送装置
を挟んで対向する両側面にそれぞれ設けた第1導入口と
第2導入口とを有しており,上記第1導入口は反対側の
側面に向けて上記マイクロ波を照射し,上記第2導入口
は反対側の側面に向けて上記マイクロ波を照射するよう
構成されていることが好ましい。搬送方向に直交し,か
つ地面に水平な方向に沿って,対向する方向からマイク
ロ波を照射することにより,上記搬送装置を挟んで上記
乾燥槽の両側において,上記マイクロ波密度を,さらに
抑制することができる。According to a fifteenth aspect of the present invention, the drying device comprises a first inlet port and a second inlet port provided on both sides of the inside of the drying tank opposite to each other with the transfer device interposed therebetween. And the first inlet is configured to irradiate the microwave toward the opposite side, and the second inlet is configured to irradiate the microwave toward the opposite side. Is preferred. The microwave density is further suppressed on both sides of the drying tank with the transfer device interposed therebetween by irradiating microwaves from the opposite direction along a direction perpendicular to the transfer direction and horizontal to the ground. be able to.
【0028】[0028]
【発明の実施の形態】実施形態例1 本発明の実施形態例にかかるハニカム成形体の製造方法
及び乾燥装置につき,図1,図2を用いて説明する。本
例は,図2に示すごとく,厚さt1が0.125mm以
下のセル壁11をハニカム状に配して多数のセル10を
設けたセラミック製のハニカム成形体1を製造する方法
である。本例のハニカム成形体1は,同図に示すごと
く,四角形のセル10を有し,厚さt2が0.5mm以
下の円筒状の外周スキン部12を有する形状を呈してい
る。なお,上記セル形状,全体形状は用途に合わせて変
更可能である。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiment 1 A method for manufacturing a honeycomb formed body and a drying apparatus according to an embodiment of the present invention will be described with reference to FIGS. In this example, as shown in FIG. 2, a method for manufacturing a ceramic honeycomb formed body 1 in which a plurality of cells 10 are provided by arranging cell walls 11 having a thickness t1 of 0.125 mm or less in a honeycomb shape. As shown in the figure, the honeycomb formed body 1 of this example has a rectangular cell 10 and a cylindrical outer skin portion 12 having a thickness t2 of 0.5 mm or less. The cell shape and overall shape can be changed according to the application.
【0029】本例の方法では,押出成形された粘土質の
ハニカム成形体1を乾燥するに当たり,ハニカム成形体
1を湿度が70%以上の高湿度雰囲気に晒すと共に,周
波数1000〜10000MHz領域のマイクロ波を照
射する。以下,これを詳説する。In the method of the present embodiment, when drying the extruded clay-like honeycomb formed body 1, the honeycomb formed body 1 is exposed to a high humidity atmosphere having a humidity of 70% or more and a micro-frequency of 1000 to 10,000 MHz is used. Irradiate waves. The details are described below.
【0030】本例のハニカム成形体1を製造するに当た
っては,まず,主にコーディエライトとなるセラミック
原料粉100重量部に対して,有機バインダー5重量部
と,水15重量部とを添加して混練し,粘土状のセラミ
ック原料を作製した。次に,このセラミック原料を押出
成形機(図示略)を用いてハニカム成形型より押し出す
と共に順次所定長さに切断し,粘土状のハニカム成形体
1を成形した。上記押出成形機としては,プランジャー
式,オーガ式等がある。また,本例ではハニカム成形型
のセル壁部のスリット幅を0.115mm,外周スキン
部のスリット幅を0.3mmとした。In manufacturing the honeycomb formed body 1 of this example, first, 5 parts by weight of an organic binder and 15 parts by weight of water were added to 100 parts by weight of a ceramic raw material powder mainly serving as cordierite. And kneaded to produce a clay-like ceramic raw material. Next, the ceramic raw material was extruded from a honeycomb mold using an extruder (not shown) and cut into a predetermined length to form a clay-like honeycomb molded body 1. Examples of the extruder include a plunger type and an auger type. In this example, the slit width of the cell wall of the honeycomb mold was set to 0.115 mm, and the slit width of the outer peripheral skin was set to 0.3 mm.
【0031】次に,上記押出成形により得られた薄壁の
ハニカム成形体1を図1に示す乾燥装置3を用いて乾燥
した。乾燥装置3は,同図に示すごとく,上記ハニカム
成形体1を収納する乾燥槽30と,該乾燥槽30内を湿
度が70%以上の高湿度雰囲気とする加湿装置32と,
周波数1000〜10000MHz領域のマイクロ波を
上記乾燥槽30内に供給するマイクロ波発生装置34と
を有する。Next, the thin-walled honeycomb formed body 1 obtained by the extrusion molding was dried using a drying device 3 shown in FIG. As shown in the figure, the drying device 3 includes a drying tank 30 for storing the honeycomb formed body 1, a humidifying device 32 for making the inside of the drying tank 30 a high humidity atmosphere having a humidity of 70% or more,
A microwave generator 34 for supplying microwaves in a frequency range of 1000 to 10000 MHz into the drying tank 30;
【0032】上記乾燥槽30は,後述する搬送装置4に
より運搬されるハニカム成形体1複数個分を収納できる
大きさを有している。そして,一方の側壁303の前後
上下の4角部分に,4つのマイクロ波発生装置34から
それぞれ延設された導波管340が接続されて開口して
いる。この開口部がマイクロ波導入口341である。The drying tank 30 has a size capable of accommodating a plurality of honeycomb formed bodies transported by the transport device 4 described later. Waveguides 340 extending from the four microwave generators 34 are connected to and open at the four corners of the one side wall 303 at the front, rear, upper and lower sides. This opening is the microwave introduction port 341.
【0033】また,側壁303の前後2カ所には,加湿
装置32としてのボイラーから延設され分岐した2本の
蒸気配管320が接続され開口している。この開口部が
蒸気導入口321である。この蒸気導入口321から導
入される蒸気は,上記のごとくボイラーより送られる高
温蒸気であり,その温度は80℃以上である。Two steam pipes 320 extending from a boiler as the humidifier 32 and connected are opened at two locations before and after the side wall 303. This opening is the steam inlet 321. The steam introduced from the steam inlet 321 is high-temperature steam sent from the boiler as described above, and its temperature is 80 ° C. or higher.
【0034】また本例の乾燥装置3は,上記乾燥装置
は,上記ハニカム成形体を搬送する搬送装置4を有して
おり,複数のハニカム成形体1を連続的に乾燥槽30に
送入,送出できるよう構成された連続装置となってい
る。具体的には,乾燥槽30内には,その入口部301
と出口部302とを結ぶようにベルトコンベア41が配
設されている。また,乾燥槽30の出口側外部には,ロ
ーラコンベア42が配設されている。Further, the drying device 3 of the present embodiment has a transporting device 4 for transporting the honeycomb formed body, and the plurality of honeycomb formed bodies 1 are continuously fed into the drying tank 30 to be transported. It is a continuous device configured to be able to send. Specifically, the drying tank 30 has an entrance 301 therein.
The belt conveyor 41 is provided so as to connect the outlet section 302 with the belt conveyor 41. A roller conveyor 42 is provided outside the outlet side of the drying tank 30.
【0035】そして,これらベルトコンベア41及びロ
ーラコンベア42よりなる搬送装置4は,ハニカム成形
体1を載置した搬送トレイ5を搬送するよう構成されて
いる。本例では,搬送トレイ5として,誘電損失が0.
1以下,気孔率が10%以上,断面開口面積比が50%
以上の多孔質のセラミックス,本例ではコーディエライ
ト製のものを使用した。なお,この材質は,尿素樹脂,
その他のものに変更することもできる。また,搬送トレ
イ5上においては,ハニカム成形体1のセル10の開口
端面の一方(101)を上記搬送トレイ5の上面51に
当接させて載置した。これにより,各ハニカム成形体1
は,そのセル10が鉛直方向に向くと共に,搬送トレイ
5の気孔と連通状態となる。The transport device 4 including the belt conveyor 41 and the roller conveyor 42 is configured to transport the transport tray 5 on which the honeycomb formed body 1 is placed. In this example, the transport tray 5 has a dielectric loss of 0.
1 or less, porosity is 10% or more, cross-sectional opening area ratio is 50%
The above porous ceramics, in this example, those made of cordierite were used. This material is made of urea resin,
It can be changed to something else. Further, on the transport tray 5, one of the open end surfaces (101) of the cells 10 of the honeycomb formed body 1 was placed in contact with the upper surface 51 of the transport tray 5. Thereby, each honeycomb formed body 1
The cell 10 is oriented vertically and communicates with the pores of the transport tray 5.
【0036】また,上記乾燥槽30の外部で上記ローラ
コンベア42の下方には,熱風発生装置36を配設し
た。この熱風発生装置36は,上記ローラコンベア42
上を移動してくる搬送トレイ5の下方から上方に向けて
120℃の熱風を吹き上げるよう構成されている。この
温度は上記ハニカム成形体1が含有するバインダが燃焼
しない温度である。A hot air generator 36 is provided outside the drying tank 30 and below the roller conveyor 42. The hot air generator 36 is provided with the roller conveyor 42.
It is configured to blow hot air of 120 ° C. upward from below the transport tray 5 moving upward. This temperature is a temperature at which the binder contained in the honeycomb formed body 1 does not burn.
【0037】このような構成の乾燥装置3を用いて,上
記のごとく押出成形されたハニカム成形体1を乾燥する
に当たっては,まず,図1に示すごとく,所定長さに切
断された各ハニカム成形体1を搬送トレイ5上に載置し
て順次ベルトコンベア41上に載せる。これにより,各
ハニカム成形体1は,順次乾燥槽30内に送入されてい
く。In drying the honeycomb molded body 1 extruded as described above using the drying apparatus 3 having such a configuration, first, as shown in FIG. 1, each honeycomb molded body cut to a predetermined length is formed. The body 1 is placed on the transport tray 5 and sequentially placed on the belt conveyor 41. Thereby, each honeycomb formed body 1 is sequentially fed into the drying tank 30.
【0038】乾燥槽30内に送入された各ハニカム成形
体1は,ベルトコンベア41の動きに伴って,入口部3
01側から出口部302側に移動しながら乾燥されてい
く。ここで,乾燥槽30内は,上記加湿装置32から導
入される高温蒸気によって湿度が70%以上(本例では
80%以上),温度が80℃以上の高湿度雰囲気となっ
ていると共に,上記マイクロ波発生装置34から発せら
れるマイクロ波が導入されている。そのため,乾燥槽3
0内のハニカム成形体1は,外周スキン部12の割れや
しわの発生を防止しつつ急速に乾燥される。Each of the honeycomb formed bodies 1 sent into the drying tank 30 is moved into the entrance 3 by the movement of the belt conveyor 41.
It is dried while moving from the 01 side to the outlet section 302 side. Here, the inside of the drying tank 30 has a high humidity atmosphere of 70% or more (80% or more in this example) and a temperature of 80 ° C. or more due to the high-temperature steam introduced from the humidifier 32. Microwaves emitted from the microwave generator 34 are introduced. Therefore, drying tank 3
The honeycomb formed body 1 in 0 is rapidly dried while preventing the outer skin portion 12 from cracking or wrinkling.
【0039】すなわち,上記乾燥槽30が上記のごとく
高温の高湿度雰囲気となっているので,ハニカム成形体
1が加熱される際に,外周表面が変形するような急激な
乾燥が防止され,適度な湿度に保たれる。そのため,外
周表面と内部との乾燥速度差を低減することができる。
そのため,セル壁厚さが0.125mm以下と薄い本例
のハニカム成形体1であっても,その内外の乾燥速度差
による収縮量差を小さくすることができる。それ故,外
周スキン部12の割れ,しわ等の欠陥を防止することが
できる。That is, since the drying tank 30 has a high-temperature and high-humidity atmosphere as described above, when the honeycomb formed body 1 is heated, rapid drying such that the outer peripheral surface is deformed is prevented, and the Humidity is maintained. Therefore, the difference in drying speed between the outer peripheral surface and the inside can be reduced.
Therefore, even with the honeycomb formed body 1 of the present example having a thin cell wall thickness of 0.125 mm or less, a difference in shrinkage due to a difference in drying speed between inside and outside can be reduced. Therefore, defects such as cracks and wrinkles of the outer peripheral skin portion 12 can be prevented.
【0040】また,本例においては,上記加熱の手段と
して,上記マイクロ波を用いる。マイクロ波は,上記乾
燥槽30内が上記のような高湿度雰囲気となっていて
も,導波管70を介して容易に導入できる。そのため,
複雑な設備構成をとることなく,ハニカム成形体1を容
易に誘電加熱することができる。このように,本例で
は,マイクロ波加熱と高湿度雰囲気との組合せによっ
て,セル壁厚さが0.125mm以下,外周スキン部の
厚さが0.3mm以下の薄肉品である場合においても,
乾燥時の外周スキン部12の割れやしわの発生を十分に
防止することができる。In this embodiment, the microwave is used as the heating means. The microwave can be easily introduced through the waveguide 70 even when the inside of the drying tank 30 has the high humidity atmosphere as described above. for that reason,
Dielectric heating of the honeycomb formed body 1 can be easily performed without taking a complicated equipment configuration. As described above, in this example, the combination of the microwave heating and the high-humidity atmosphere makes it possible to obtain a thin product having a cell wall thickness of 0.125 mm or less and an outer skin portion of 0.3 mm or less.
The occurrence of cracks and wrinkles in the outer skin portion 12 during drying can be sufficiently prevented.
【0041】更に,本例では,上記乾燥槽30内での高
湿度雰囲気でのマイクロ波による乾燥後,ハニカム成形
体1に対して,上記熱風発生装置36から発する熱風を
セル10を通過するように当てる。すなわち,本例で
は,ハニカム成形体1の乾燥を高湿度雰囲気でのマイク
ロ波加熱と熱風による加熱との組合せにより行う。具体
的には,乾燥前のハニカム成形体中の水分の10〜20
%がまだ残存する程度までの乾燥を上記高湿度雰囲気で
のマイクロ波加熱により行い,その後,水分含有量が5
%以下となるように熱風により完全乾燥を行う。Further, in this embodiment, after drying by microwaves in a high humidity atmosphere in the drying tank 30, hot air generated from the hot air generator 36 passes through the cell 10 to the honeycomb formed body 1. Guess. That is, in this example, the honeycomb formed body 1 is dried by a combination of microwave heating in a high humidity atmosphere and heating by hot air. Specifically, the water content of the honeycomb formed body before drying is 10 to 20%.
% Is dried by microwave heating in the high humidity atmosphere described above until the moisture content is still 5%.
% By using hot air.
【0042】これにより,上記高湿度雰囲気でのマイク
ロ波加熱の制御を容易にすることができ,マイクロ波加
熱の過剰加熱によってハニカム成形体のバインダー成分
が焼失するなどの不具合を防止することができる。そし
て,過剰加熱のおそれのない温度の熱風によって精度の
よい完全乾燥を実現することができる。Thus, it is possible to easily control the microwave heating in the high humidity atmosphere, and it is possible to prevent the binder component of the honeycomb molded body from being burned out due to the excessive heating of the microwave heating. . Then, accurate and complete drying can be realized by hot air at a temperature at which there is no risk of excessive heating.
【0043】また,本例の乾燥装置4は,上記のごとく
搬送装置4を有し,連続操業可能な構成を有している。
そのため,非常に効率よく乾燥工程を行うことができ
る。また,本例の搬送トレイ5は,上記のごとく誘電損
失が0.1以下,気孔率が10%以上,断面開口面積比
が50%以上の多孔質のコーディエライトという特定の
セラミックスを用いている。そのため,上記マイクロ波
による乾燥時には,水分の滞留防止,および搬送トレイ
5の高温化防止を図ることができる。更に,熱風加熱時
には,上記気孔を通した熱風の供給によって,セル10
内への熱風の通過を容易に行うことができる。Further, the drying device 4 of the present embodiment has the transport device 4 as described above, and has a configuration capable of continuous operation.
Therefore, the drying step can be performed very efficiently. Further, as described above, the transport tray 5 of this embodiment is made of a specific ceramic such as porous cordierite having a dielectric loss of 0.1 or less, a porosity of 10% or more, and a sectional opening area ratio of 50% or more. I have. Therefore, at the time of drying by the microwave, it is possible to prevent the retention of water and the temperature of the transport tray 5 from being raised. Further, at the time of heating with hot air, the supply of hot air through the pores causes the cells 10 to be heated.
Hot air can easily pass through the inside.
【0044】実施形態例2 本例では,実施形態例1における乾燥装置3を用い,そ
の乾燥槽30に導入する高温蒸気量の変化により湿度を
変化させ,湿度と外周スキン部の品質との相関を見る実
験を行った。湿度以外の条件は実施形態例1と同様とし
た。Embodiment 2 In this embodiment, the humidity is changed by changing the amount of high-temperature steam introduced into the drying tank 30 by using the drying apparatus 3 of Embodiment 1 and the correlation between the humidity and the quality of the outer skin portion. An experiment was performed. Conditions other than the humidity were the same as those in the first embodiment.
【0045】実験結果を図3に示す。同図は,横軸を乾
燥槽30の槽内湿度,縦軸を外周スキン部の割れ・しわ
不良率をとった。各実験は,それぞれ20個のハニカム
成形体を処理し,少しでも割れ・しわのあったものを不
良品としてその個数の割合を算出して不良率とした。同
図より知られるごとく,湿度を50%より高めることに
より割れ・しわ防止効果が現れ,70%以上ではほぼ確
実に割れ・しわの防止ができることがわかった。FIG. 3 shows the experimental results. In the figure, the horizontal axis indicates the humidity in the drying tank 30 and the vertical axis indicates the crack / wrinkle defect rate of the outer skin portion. In each experiment, 20 honeycomb formed bodies were processed, and those having even slight cracks and wrinkles were regarded as defective products, and the ratio of the number was calculated as a defective rate. As is known from the figure, it was found that the effect of preventing cracks and wrinkles was exhibited by increasing the humidity above 50%, and that the cracks and wrinkles could be almost completely prevented at 70% or more.
【0046】実施形態例3 本例では,実施形態例1における搬送トレイ5の気孔率
を変化させると共に,上記と同様に乾燥槽30内の湿度
を変化させ,乾燥時の水分の滞留による不具合の有無を
みる実験を行った。搬送トレイ5の気孔率および乾燥槽
30内の湿度以外の条件は実施形態例1と同様とした。Embodiment 3 In this embodiment, the porosity of the transport tray 5 in Embodiment 1 is changed, and the humidity in the drying tank 30 is changed in the same manner as described above, thereby preventing the problem caused by the accumulation of moisture during drying. An experiment to determine the presence or absence was performed. Conditions other than the porosity of the transport tray 5 and the humidity in the drying tank 30 were the same as those in the first embodiment.
【0047】実験結果を図4に示す。同図は,横軸に搬
送トレイの気孔率を,縦軸に乾燥槽30の湿度をとった
ものである。各条件での処理は一回ずつ行い,少しでも
セル壁あるいは外壁スキン部の溶出があった場合をXと
し,なかったものを○として図にプロットした。同図よ
り知られるごとく,湿度が高いほど溶出しやすくなる
が,少なくとも湿度が70%の場合には,搬送トレイの
気孔率を10%以上とすることにより溶出を防止するこ
とができることがわかる。そして,湿度100%であっ
ても,少なくとも搬送トレイの気孔率を25%以上とす
ることにより溶出防止を図ることができることもわか
る。FIG. 4 shows the experimental results. In the figure, the porosity of the transport tray is plotted on the horizontal axis, and the humidity of the drying tank 30 is plotted on the vertical axis. The treatment under each condition was performed once, and X was plotted when there was any elution of the cell wall or outer skin portion, and O was plotted when there was no elution. As can be seen from the figure, the elution becomes easier as the humidity becomes higher. However, at least when the humidity is 70%, the elution can be prevented by setting the porosity of the transfer tray to 10% or more. Also, it can be seen that even when the humidity is 100%, elution can be prevented by setting the porosity of the transport tray to at least 25% or more.
【0048】実施形態例4 本例は,実施形態例1に示したごとく,上記ハニカム成
形体を乾燥するに当たって,上記ハニカム成形体を,ア
キュームレータ機能を有する搬送装置を用いて,乾燥槽
へ送入した例である。Fourth Embodiment In this embodiment, as described in the first embodiment, when the honeycomb formed body is dried, the honeycomb formed body is fed into a drying tank using a transfer device having an accumulator function. This is an example.
【0049】本例は,図5に示すごとく,乾燥装置3を
用いて実施される。該乾燥装置3は,実施形態例1の上
記乾燥装置3を基にして,上記搬送装置4に,上記アキ
ュームレータ機能をなすアキュームコンベア43と,該
アキュームコンベア43上において上記ハニカム成形体
1を停留させるストッパ45とを追加している。さら
に,上記乾燥装置は,実施形態例1の上記乾燥装置30
を基にして,上記乾燥槽30の開口部にエアカーテンを
形成するエア発生装置35を追加している。This embodiment is carried out by using a drying device 3 as shown in FIG. Based on the drying device 3 of the first embodiment, the drying device 3 causes the transport device 4 to hold the accumulator 43 serving as the accumulator function and the honeycomb formed body 1 on the accumulator 43. A stopper 45 is added. Further, the drying device is the same as the drying device 30 of the first embodiment.
Based on the above, an air generator 35 for forming an air curtain at the opening of the drying tank 30 is added.
【0050】ここで,エアーカーテンとは,上記乾燥槽
の内外の雰囲気が混じり合うのを防止するために,上記
乾燥槽が外部に連通する開口部がなす開口面と平行に形
成された面状のエアの流れをいう。上記アキュームコン
ベア43は,複数の円筒ローラ44よりなる。各円筒ロ
ーラ44は,その軸方向が地面と水平かつ,搬送方向と
直交する状態で取り付けられている。そして,上記アキ
ュームコンベア43は,このような円筒ローラ44が,
その搬送方向に一列に並べられたものである。さらに,
各円筒ローラ44は,図示しないモータによって連結さ
れ,図5に示すごとく,矢印R方向に回転するように構
成されている。Here, the air curtain is a plane formed in parallel with an opening formed by an opening communicating with the outside in order to prevent the atmosphere inside and outside the drying tank from being mixed. Air flow. The accumulator 43 includes a plurality of cylindrical rollers 44. Each cylindrical roller 44 is mounted so that its axial direction is horizontal to the ground and perpendicular to the transport direction. The accumulator 43 has such a cylindrical roller 44,
They are arranged in a line in the transport direction. further,
Each cylindrical roller 44 is connected by a motor (not shown), and is configured to rotate in the direction of arrow R as shown in FIG.
【0051】そして,上記アキュームコンベア43は,
上記回転する円筒ローラ44の外周面と,上記搬送トレ
イ5との間に生じる摩擦力によって,上記ハニカム成形
体1を搬送する。ここで,上記円筒ローラ44の外周面
には,滑らかな面が形成されており,上記アキュームコ
ンベア43上において上記ハニカム成形体1を停留させ
ることが容易であるように構成されている。Then, the accumulator 43 is
The honeycomb formed body 1 is transported by the frictional force generated between the outer peripheral surface of the rotating cylindrical roller 44 and the transport tray 5. Here, a smooth surface is formed on the outer peripheral surface of the cylindrical roller 44, and the honeycomb formed body 1 is configured to be easily retained on the accumulation conveyor 43.
【0052】本例では,上記ストッパ45が,上記ハニ
カム成形体1の搬送状態と停留状態とを切り替える。図
5に示すごとく,上記ストッパ45は,上記乾燥槽30
の入口部301付近において上方に向けて突出し,上記
搬送トレイ5の側面に当たるよう構成してある。In this embodiment, the stopper 45 switches the state of the honeycomb formed body 1 between the transport state and the stationary state. As shown in FIG. 5, the stopper 45 is connected to the drying tank 30.
Is configured to protrude upward near the entrance portion 301 and hit the side surface of the transport tray 5.
【0053】上記エア発生装置35は,エア配管350
と,エア噴出口351とを有し,該エア噴出口351
は,上記乾燥槽30の入口部301及び出口部302の
開口部付近に配設されている。さらに,上記エア噴出口
351は,上記開口部の対角方向に向けて送風し,開口
部が形成する開口面と平行な気流を形成するように構成
されている。The air generator 35 is provided with an air pipe 350
And an air outlet 351.
Are disposed near the openings of the inlet 301 and the outlet 302 of the drying tank 30. Further, the air ejection port 351 is configured to blow air in a diagonal direction of the opening to form an airflow parallel to an opening surface formed by the opening.
【0054】本例では,上記のごとく構成された上記乾
燥装置3を用いて,上記ハニカム成形体1の乾燥を実施
した。上記乾燥装置3に搬入した上記ハニカム成形体1
は,上記搬送トレイ5に載置され,上記アキュームコン
ベア43により搬送される。そして,上記乾燥槽30の
入口部301付近まで搬送されると,上記搬送トレイ5
が上記ストッパ23に当接し,停留する。その後,上記
ハニカム成形体1が,上記乾燥装置3に次々に搬入され
ると,上記アキュームコンベア43上において,各ハニ
カム成形体1が,順次停留する。そして,停留したハニ
カム成形体1は,上記アキュームコンベア24上で行列
を形成する。In this example, the honeycomb formed body 1 was dried by using the drying device 3 configured as described above. The honeycomb formed body 1 carried into the drying device 3
Are placed on the transport tray 5 and transported by the accumulator 43. When the sheet is conveyed to the vicinity of the entrance 301 of the drying tank 30, the transfer tray 5
Contacts the stopper 23 and stops. Thereafter, when the honeycomb formed bodies 1 are successively carried into the drying device 3, the honeycomb formed bodies 1 are sequentially stopped on the accumulation conveyor 43. Then, the stopped honeycomb formed body 1 forms a matrix on the accumulator 24.
【0055】そして,上記アキュームコンベア43上に
おいて,一定数量のハニカム成形体1が停留した後,上
記ハニカム成形体1の上記乾燥槽30への送入を開始す
る。まず,上記ストッパ23を操作して,上記ハニカム
成形体1を1個搬出した後,上記ストッパ23を元の位
置に戻して残りの上記ハニカム成形体1を,再び停留さ
せる。そして,所定の間隔が経過した後,さらに,上記
ハニカム成形体1を,上記のごとく,1個搬出するとい
う一連の手順を繰り返し実施する。ここで,上記所定の
間隔は,各ハニカム成形体1が上記アキュームコンベア
24上においてなすべき間隔に応じて決定した。Then, after a certain number of the honeycomb formed bodies 1 are stopped on the accumulation conveyor 43, the feeding of the honeycomb formed bodies 1 into the drying tank 30 is started. First, after operating one of the honeycomb formed bodies 1 by operating the stopper 23, the stopper 23 is returned to the original position and the remaining honeycomb formed body 1 is stopped again. After a predetermined interval has elapsed, a series of steps of unloading one honeycomb molded body 1 as described above is repeatedly performed. Here, the predetermined interval was determined according to the interval that each honeycomb formed body 1 should make on the accumulator 24.
【0056】上記のごとく,本例によれば,上記アキュ
ームレータ機能により,上記ハニカム成形体1を上記乾
燥装置3に供給する供給タイミングと分離して,上記ハ
ニカム成形体1を,一定の間隔で上記乾燥槽30へ送入
することができる。それ故,上記乾燥槽30内におい
て,各ハニカム成形体1を常に等間隔に配置することが
できる。As described above, according to the present embodiment, the accumulator function separates the honeycomb molded body 1 from the supply timing of supplying the honeycomb molded body 1 to the drying device 3 and separates the honeycomb molded body 1 at regular intervals. It can be sent to the drying tank 30. Therefore, in the drying tank 30, the honeycomb formed bodies 1 can be always arranged at equal intervals.
【0057】また,本例では,上記乾燥槽30の開口部
にエアーカーテンを設置してある。そのため,上記乾燥
槽30への上記ハニカム成形体1の送入,送出を容易と
しながら,上記乾燥槽30内の高湿度雰囲気が外部雰囲
気と混じり合うことを防止することができる。それ故,
上記乾燥槽30内には,均一な高湿度雰囲気が精度良く
保持できる。In this embodiment, an air curtain is installed at the opening of the drying tank 30. Therefore, it is possible to prevent the high humidity atmosphere in the drying tank 30 from being mixed with the external atmosphere while facilitating the feeding and sending of the honeycomb formed body 1 to the drying tank 30. Therefore,
A uniform high humidity atmosphere can be accurately maintained in the drying tank 30.
【0058】このように,本例によれば,上記乾燥槽3
0内に保持した均一な高湿度雰囲気内において,上記ハ
ニカム成形体1に上記マイクロ波を,均一に照射するこ
とができる。そのため,上記乾燥装置3を用いて乾燥さ
れる上記ハニカム成形体1においては,乾燥ムラの発生
をさらに抑制することができる。したがって,セル壁等
の厚さが薄い上記ハニカム成形体1において,乾燥時の
外周スキン部12の割れやしわの発生を,さらに十分に
防止することができる。その他の構成及び作用効果は,
実施形態例1と同様である。As described above, according to this embodiment, the drying tank 3
In the uniform high-humidity atmosphere kept within 0, the honeycomb molded body 1 can be uniformly irradiated with the microwave. For this reason, in the honeycomb formed body 1 that is dried using the drying device 3, the occurrence of drying unevenness can be further suppressed. Therefore, in the honeycomb formed body 1 having a thin cell wall or the like, cracking and wrinkling of the outer peripheral skin portion 12 during drying can be more sufficiently prevented. Other configurations and functions and effects
This is the same as the first embodiment.
【0059】実施形態例5 本例は,実施形態例1において,上記乾燥槽30内の上
記ハニカム成形体1の数量に応じて,上記乾燥装置3の
マイクロ波出力値を調整した例である。そこで,予め,
上記乾燥装置3の適切なマイクロ波出力値を調べた。そ
の結果,図6に示すごとく,乾燥層30内のハニカム成
形体1の数量に応じてマイクロ波の出力値を設定するの
が適切であると判明した。そこで,本例では,上記乾燥
装置3を用いて,上記ハニカム成形体1を乾燥する際,
上記マイクロ波出力を,上記乾燥槽30内の上記ハニカ
ム成形体1の数量に応じて,図6に示すごとく,調整し
た。Fifth Embodiment This embodiment is an example in which the microwave output value of the drying device 3 is adjusted in accordance with the number of the honeycomb formed bodies 1 in the drying tank 30 in the first embodiment. Therefore,
An appropriate microwave output value of the drying device 3 was examined. As a result, as shown in FIG. 6, it was found that it was appropriate to set the microwave output value according to the number of honeycomb formed bodies 1 in the dry layer 30. Therefore, in this example, when the honeycomb formed body 1 is dried using the drying device 3,
The microwave output was adjusted according to the number of the honeycomb formed bodies 1 in the drying tank 30, as shown in FIG.
【0060】本例によれば,上記乾燥槽30内の上記ハ
ニカム成形体1の数量が変動する場合であっても,各ハ
ニカム成形体1に照射されるマイクロ波を均等にするこ
とができる。そのため,各ハニカム成形体1について生
じる乾燥度合いのばらつきを,有効に抑制することがで
きる。したがって,セル壁等の厚さが薄い上記ハニカム
成形体1において,乾燥時の外周スキン部12の割れや
しわの発生を,さらに十分に防止することができる。そ
の他の構成及び作用効果は,実施形態例1と同様であ
る。According to the present embodiment, even when the number of the honeycomb formed bodies 1 in the drying tank 30 fluctuates, the microwave applied to each honeycomb formed body 1 can be made uniform. Therefore, it is possible to effectively suppress the variation in the degree of drying that occurs for each honeycomb formed body 1. Therefore, in the honeycomb formed body 1 having a thin cell wall or the like, cracking and wrinkling of the outer peripheral skin portion 12 during drying can be more sufficiently prevented. Other configurations and operational effects are the same as those of the first embodiment.
【0061】実施形態例6 本例は,実施形態例1において,上記乾燥槽30内のマ
イクロ波密度のばらつきを抑制した乾燥装置を用いた例
である。図7に示すごとく,本例の乾燥装置3は,実施
形態例1における乾燥装置3を基にして,マイクロ波発
生装置と導波管とマイクロ波導入口とからなるマイクロ
波装置の配置を変更したものである。Embodiment 6 This embodiment is an example in which the drying apparatus in Embodiment 1 is used in which the variation in the microwave density in the drying tank 30 is suppressed. As shown in FIG. 7, the drying device 3 of the present example is based on the drying device 3 of the first embodiment, and the arrangement of the microwave device including the microwave generator, the waveguide, and the microwave inlet is changed. Things.
【0062】上記乾燥装置3は,上記ハニカム成形体1
を上記乾燥槽30に送入するための開口部381近傍に
設けた第1導入口344と,上記ハニカム成形体1を上
記乾燥槽30から送出するための開口部382近傍に設
けた第2導入口347とを有している。そして,上記第
1導入口344は,上記送出側の開口部382に向けて
マイクロ波を照射し,上記第2導入口347は,上記送
入側の開口部381に向けてマイクロ波を照射するよう
構成されている。The drying device 3 is provided with the honeycomb formed body 1
A first introduction port 344 provided near the opening 381 for feeding the honeycomb formed article 1 into the drying tank 30, and a second introduction port provided near the opening 382 for sending the honeycomb formed body 1 from the drying tank 30. Port 347. Then, the first inlet 344 irradiates the microwave toward the opening 382 on the sending side, and the second inlet 347 irradiates the microwave toward the opening 381 on the sending side. It is configured as follows.
【0063】本例では,以上のごとく構成された乾燥装
置3を用いて,上記ハニカム成形体1の乾燥を実施し
た。上記乾燥槽30内においては,上記乾燥槽の送入側
と送出側とにおいて,上記マイクロ波密度のばらつきが
抑制されている。そのため,上記ハニカム成形体1は,
上記乾燥槽30内を搬送される間,均一にマイクロ波の
照射を受ける。それ故,本例によれば,上記ハニカム成
形体1の乾燥が一定の速度で進行し,上記乾燥時のトラ
ブルを未然に防止することができる。その他の構成及び
作用効果については,実施形態例1と同様である。In this example, the honeycomb formed body 1 was dried using the drying apparatus 3 configured as described above. In the drying tank 30, the dispersion of the microwave density is suppressed between the sending side and the sending side of the drying tank. Therefore, the honeycomb formed body 1 is
While being conveyed in the drying tank 30, it is uniformly irradiated with microwaves. Therefore, according to this example, the drying of the honeycomb formed body 1 proceeds at a constant speed, and the trouble at the time of the drying can be prevented. Other configurations and operational effects are the same as those of the first embodiment.
【0064】実施形態例7 本例は,実施形態例1において,上記乾燥槽30内のマ
イクロ波密度のばらつきを抑制した乾燥装置を用いた例
である。図8に示すごとく,本例の乾燥装置3は,実施
形態例1における乾燥装置3を基にして,マイクロ波発
生装置と導波管とマイクロ波導入口とからなるマイクロ
波装置の配置を変更したものである。Seventh Embodiment This embodiment is an example in which the drying apparatus which suppresses the variation of the microwave density in the drying tank 30 in the first embodiment is used. As shown in FIG. 8, the drying device 3 of the present example is based on the drying device 3 of the first embodiment, and the arrangement of the microwave device including the microwave generator, the waveguide, and the microwave inlet is changed. Things.
【0065】上記乾燥装置3は,上記ハニカム成形体1
を上記乾燥槽30に送入するための開口部381の上側
に設けた第1導入口344と,上記開口部381の下側
に設けた第2導入口347とを有している。そして,上
記第1導入口344及び上記第1導入口347は,上記
ハニカム成形体1を上記乾燥槽30から送出するための
開口部382に向けて上記マイクロ波を照射するよう構
成されている。The drying device 3 is provided with the honeycomb formed body 1
It has a first inlet 344 provided above the opening 381 for feeding the water into the drying tank 30, and a second inlet 347 provided below the opening 381. The first inlet 344 and the first inlet 347 are configured to irradiate the microwave toward the opening 382 for sending the honeycomb formed body 1 from the drying tank 30.
【0066】本例では,以上のごとく構成された乾燥装
置3を用いて,上記ハニカム成形体1の乾燥を実施し
た。上記乾燥槽30内においては,上記乾燥槽の上側と
下側とにおいて,上記搬送方向に照射される上記マイク
ロ波の密度ムラが抑制されている。そのため,上記ハニ
カム成形体1の外周面のうち,上側と下側に均一にマイ
クロ波を照射することができる。それ故,本例によれ
ば,上記ハニカム成形体1の上側部分と下側部分とで,
同じように乾燥が進行し,上記乾燥時のトラブルを未然
に防止することができる。その他の構成及び作用効果に
ついては,実施形態例1と同様である。In this example, the honeycomb formed body 1 was dried using the drying device 3 configured as described above. In the drying tank 30, unevenness in the density of the microwave irradiated in the transport direction is suppressed above and below the drying tank. Therefore, the microwave can be uniformly irradiated on the upper and lower sides of the outer peripheral surface of the honeycomb formed body 1. Therefore, according to this example, the upper part and the lower part of the honeycomb formed body 1
Similarly, the drying proceeds, and the trouble at the time of the drying can be prevented. Other configurations and operational effects are the same as those of the first embodiment.
【0067】実施形態例8 本例は,実施形態例1において,上記乾燥槽30内のマ
イクロ波密度のばらつきを抑制した乾燥装置を用いた例
である。図9に示すごとく,本例の乾燥装置3は,実施
形態例1における乾燥装置3を基にして,マイクロ波発
生装置と導波管とマイクロ波導入口とからなるマイクロ
波装置の配置を変更したものである。Eighth Embodiment This embodiment is an example in which the drying apparatus in which the variation of the microwave density in the drying tank 30 is suppressed in the first embodiment is used. As shown in FIG. 9, the drying device 3 of the present example is based on the drying device 3 of the first embodiment, and the arrangement of the microwave device including the microwave generator, the waveguide, and the microwave inlet is changed. Things.
【0068】上記乾燥装置3は,上記乾燥槽30の上部
に設けた第1導入口344と,上記乾燥槽30の下部に
設けた第2導入口347とを有している。そして,上記
第1導入口344は,上記乾燥槽30の下部に向って上
記マイクロ波を照射し,上記第2導入口347は,上記
乾燥槽30の上部に向って上記マイクロ波を照射するよ
う構成されている。The drying device 3 has a first inlet 344 provided above the drying tank 30 and a second inlet 347 provided below the drying tank 30. The first inlet 344 irradiates the microwave toward the lower part of the drying tank 30, and the second inlet 347 irradiates the microwave toward the upper part of the drying tank 30. It is configured.
【0069】本例では,以上のごとく構成された乾燥装
置3を用いて,上記ハニカム成形体1の乾燥を実施し
た。上記乾燥槽30内においては,上記乾燥槽の上側と
下側とにおいて,鉛直方向に照射される上記マイクロ波
の密度ムラが抑制されている。そのため,上記ハニカム
成形体1の両端面には,均一にマイクロ波を照射するこ
とができる。それ故,本例によれば,上記ハニカム成形
体1の上側部分と下側部分とで,同じように乾燥が進行
し,上記乾燥時のトラブルを未然に防止することができ
る。その他の構成及び作用効果については,実施形態例
1と同様である。In this example, the honeycomb formed body 1 was dried by using the drying apparatus 3 configured as described above. In the drying tank 30, the unevenness in the density of the microwave irradiated in the vertical direction is suppressed on the upper and lower sides of the drying tank. Therefore, the microwaves can be evenly applied to both end faces of the honeycomb formed body 1. Therefore, according to the present example, the drying proceeds in the same manner in the upper portion and the lower portion of the honeycomb formed body 1, and the trouble at the time of the drying can be prevented. Other configurations and operational effects are the same as those of the first embodiment.
【0070】実施形態例9 本例は,実施形態例1において,上記乾燥槽30内のマ
イクロ波密度のばらつきを抑制した乾燥装置を用いた例
である。図10に示すごとく,本例の乾燥装置3は,実
施形態例1における乾燥装置3を基にして,マイクロ波
発生装置と導波管とマイクロ波導入口とからなるマイク
ロ波装置の配置を変更したものである。Embodiment 9 This embodiment is an example in which the drying apparatus in Embodiment 1 in which the variation in the microwave density in the drying tank 30 is suppressed is used. As shown in FIG. 10, the drying device 3 of the present example is based on the drying device 3 of the first embodiment, and the arrangement of the microwave device including the microwave generator, the waveguide, and the microwave inlet is changed. Things.
【0071】上記乾燥装置3は,上記乾燥槽30の側面
303に設けた第1導入口344と,上記側面303に
対向する側面304に設けた第2導入口347とを有し
ている。そして,上記第1導入口344は,上記側面3
04に向って上記マイクロ波を照射し,上記第2導入口
347は,上記側面303に向って上記マイクロ波を照
射するよう構成されている。The drying device 3 has a first inlet 344 provided on the side surface 303 of the drying tank 30 and a second inlet 347 provided on the side 304 opposite to the side 303. The first inlet 344 is connected to the side surface 3.
The microwave is irradiated toward the side 04, and the second inlet 347 is configured to emit the microwave toward the side surface 303.
【0072】本例では,以上のごとく構成された乾燥装
置3を用いて,上記ハニカム成形体1の乾燥を実施し
た。上記乾燥槽30内においては,上記搬送装置を挟ん
で上記乾燥槽の両側において,上記マイクロ波密度のば
らつきが抑制されている。そのため,上記搬送方向に対
して,上記ハニカム成形体1の両側に均一にマイクロ波
を照射することができる。それ故,本例によれば,上記
ハニカム成形体1の両側において,同じように乾燥が進
行し,上記乾燥時のトラブルを未然に防止することがで
きる。その他の構成及び作用効果については,実施形態
例1と同様である。In this example, the honeycomb formed body 1 was dried using the drying device 3 configured as described above. In the drying tank 30, the dispersion of the microwave density is suppressed on both sides of the drying tank with the transfer device interposed therebetween. Therefore, microwaves can be uniformly irradiated on both sides of the honeycomb formed body 1 in the transport direction. Therefore, according to the present embodiment, drying proceeds in the same manner on both sides of the honeycomb formed body 1, and the trouble at the time of the drying can be prevented. Other configurations and operational effects are the same as those of the first embodiment.
【0073】なお,実施形態例6〜実施形態例9の全部
あるいは一部を組み合わせて,上記乾燥槽に上記マイク
ロ波導入口を配置することも考えられる。この場合に
は,上記乾燥装置に適用する上記乾燥槽の体積,長さ,
高さ,或いは乾燥槽に同時送入される上記ハニカム成形
体の数量等に応じて,適宜,上記マイクロ波導入口配置
の組み合わせを選択するのが良い。上記乾燥槽内におけ
る,上記マイクロ波密度のばらつきをさらに抑制するこ
とができ,本例の効果をより高めることができる。It is also conceivable to arrange the microwave inlet in the drying tank by combining all or a part of the sixth to ninth embodiments. In this case, the volume, length,
It is preferable to appropriately select the combination of the arrangement of the microwave introduction ports according to the height, the number of the honeycomb formed bodies simultaneously fed into the drying tank, and the like. The variation in the microwave density in the drying tank can be further suppressed, and the effect of the present example can be further enhanced.
【図1】実施形態例1における,乾燥装置の構成を示す
説明図。FIG. 1 is an explanatory diagram illustrating a configuration of a drying device according to a first embodiment.
【図2】実施形態例1における,(a)ハニカム成形体
の斜視図,(b)セル壁厚さを示す説明図。FIG. 2A is a perspective view of a honeycomb formed body according to the first embodiment, and FIG. 2B is an explanatory view showing a cell wall thickness.
【図3】実施形態例2における,槽内湿度と割れ・しわ
不良率との関係を示す説明図。FIG. 3 is an explanatory diagram showing a relationship between the humidity in a tank and a crack / wrinkle defective rate in a second embodiment.
【図4】実施形態例3における,搬送トレイ及び槽内湿
度とハニカム成形体の溶出との関係を示す説明図。FIG. 4 is an explanatory diagram showing a relationship between humidity in a transport tray and a tank and elution of a honeycomb formed body in a third embodiment.
【図5】実施形態例4における,乾燥装置の構成を示す
説明図。FIG. 5 is an explanatory diagram illustrating a configuration of a drying device according to a fourth embodiment.
【図6】実施形態例5の乾燥装置における,ハニカム成
形体の数量に対する適切なマイクロ波出力の関係を示す
グラフ。FIG. 6 is a graph showing a relationship between an appropriate number of honeycomb formed bodies and an appropriate microwave output in the drying apparatus according to the fifth embodiment.
【図7】実施形態例6の乾燥装置における,マイクロ波
導入口の配置を示す説明図で側面図。FIG. 7 is an explanatory side view showing an arrangement of microwave introduction ports in a drying apparatus according to a sixth embodiment.
【図8】実施形態例7の乾燥装置における,マイクロ波
導入口の配置を示す説明図で側面図。FIG. 8 is an explanatory diagram showing a side view of an arrangement of microwave introduction ports in a drying apparatus according to a seventh embodiment.
【図9】実施形態例8の乾燥装置における,マイクロ波
導入口の配置を示す説明図で側面図。FIG. 9 is an explanatory side view showing an arrangement of microwave introduction ports in the drying apparatus according to the eighth embodiment.
【図10】実施形態例9の乾燥装置における,マイクロ
波導入口の配置を示す説明図で上面図。FIG. 10 is an explanatory top view showing an arrangement of microwave introduction ports in a drying apparatus according to Embodiment 9;
1...ハニカム成形体, 10...セル, 11...セル壁, 12...外周スキン部, 3,6...乾燥装置, 30,60...乾燥槽, 32,62...加湿装置, 320,620...蒸気配管, 321,621...蒸気導入口, 34,64...マイクロ波発生装置, 340,640...導波管, 341,641...マイクロ波導入口, 36,66...熱風発生装置, 4...搬送装置, 41...ベルトコンベア, 42...ローラコンベア, 5...搬送トレイ, 1. . . 9. honeycomb formed body, . . Cell, 11. . . 11. cell walls, . . Outer skin part, 3,6. . . Drying device, 30, 60. . . Drying tank, 32, 62. . . Humidifier, 320, 620. . . Steam piping, 321,621. . . Steam inlet, 34, 64. . . Microwave generator, 340, 640. . . Waveguide, 341, 641. . . Microwave inlet, 36, 66. . . Hot air generator, 4. . . Transfer device, 41. . . Belt conveyor, 42. . . Roller conveyor, 5. . . Transport tray,
フロントページの続き (72)発明者 加藤 広己 愛知県刈谷市昭和町1丁目1番地 株式会 社デンソー内 Fターム(参考) 3L113 AA02 AC13 AC27 AC36 AC67 BA01 DA24 4G055 AA08 AB03 AC10 BA12 Continued on the front page (72) Inventor Hiromi Kato 1-1-1, Showa-cho, Kariya-shi, Aichi F-term in DENSO Corporation (Reference) 3L113 AA02 AC13 AC27 AC36 AC67 BA01 DA24 4G055 AA08 AB03 AC10 BA12
Claims (15)
カム状に配して多数のセルを設けたセラミック製のハニ
カム成形体を製造する方法において,押出成形された粘
土質のハニカム成形体を乾燥するに当たり,誘電損失が
0.1以下,気孔率が10%以上,断面開口面積比が5
0%以上の多孔質のセラミックスよりなる搬送トレイに
載置した上記ハニカム成形体を,湿度が70%以上の高
湿度雰囲気に晒すと共に,周波数1000〜10000
MHz領域のマイクロ波を照射することを特徴とするハ
ニカム成形体の製造方法。1. A method for manufacturing a ceramic honeycomb formed body having a large number of cells by arranging cell walls having a thickness of 0.125 mm or less in a honeycomb shape, comprising the steps of: Upon drying, the dielectric loss is 0.1 or less, the porosity is 10% or more, and the sectional opening area ratio is 5
The honeycomb formed body placed on a transfer tray made of 0% or more porous ceramics is exposed to a high humidity atmosphere having a humidity of 70% or more, and a frequency of 1000 to 10000.
A method for manufacturing a honeycomb formed body, which comprises irradiating a microwave in a MHz region.
は,上記セルの開口端面の一方を上記搬送トレイの上面
に当接させて載置することを特徴とするハニカム成形体
の製造方法。2. The method for manufacturing a honeycomb formed body according to claim 1, wherein the honeycomb formed body is placed with one of the open end surfaces of the cells in contact with the upper surface of the transport tray.
イは,尿素樹脂フォームよりなることを特徴とするハニ
カム成形体の製造方法。3. The method for manufacturing a honeycomb formed body according to claim 1, wherein the transfer tray is formed of a urea resin foam.
上記ハニカム成形体を乾燥するに当たっては,各ハニカ
ム成形体は,隣接する他のハニカム成形体との間に一定
の間隔を有するように配置して乾燥することを特徴とす
るハニカム成形体の製造方法。4. The method according to claim 1, wherein:
In drying the above-mentioned honeycomb formed body, each honeycomb formed body is arranged and dried so as to have a certain interval between adjacent honeycomb formed bodies, and is dried. .
上記ハニカム成形体を乾燥するに当たっては,上記ハニ
カム成形体の数量に応じて上記マイクロ波の照射条件を
変更することを特徴とするハニカム成形体の製造方法。5. The method according to claim 1, wherein:
A method for manufacturing a honeycomb formed body, characterized in that, when drying the honeycomb formed body, the microwave irradiation conditions are changed according to the number of the honeycomb formed body.
カム状に配して多数のセルを設けたセラミック製のハニ
カム成形体を製造するに当たり,押出成形された粘土質
のハニカム成形体を乾燥する乾燥装置であって,上記ハ
ニカム成形体を収納する乾燥槽と,該乾燥槽内を湿度が
70%以上の高湿度雰囲気とする加湿装置と,周波数1
000〜10000MHz領域のマイクロ波を上記乾燥
槽内に供給するマイクロ波発生装置と,複数のハニカム
成形体を連続的に上記乾燥槽に送入,送出する搬送装置
とを有することを特徴とするハニカム成形体の乾燥装
置。6. A method of manufacturing a ceramic honeycomb formed body having a plurality of cells by arranging cell walls having a thickness of 0.125 mm or less in a honeycomb shape, drying an extruded clay-based honeycomb formed body. A drying tank for storing the honeycomb formed article, a humidifying apparatus for setting the inside of the drying tank to a high humidity atmosphere having a humidity of 70% or more,
A honeycomb, comprising: a microwave generator for supplying microwaves in the range of 000 to 10000 MHz into the drying tank; Drying device for moldings.
のハニカム成形体を連続的に上記乾燥槽に送入用及び送
出用の開口部を有していると共に,その開口部におい
て,上記乾燥槽内の高湿度の空気と外気とが混じり合う
ことを防止する遮断手段を有していることを特徴とする
ハニカム成形体の乾燥装置。7. The drying tank according to claim 6, wherein the drying tank has openings for feeding and discharging a plurality of honeycomb formed bodies to and from the drying tank in a continuous manner. An apparatus for drying a honeycomb formed body, comprising: a shut-off means for preventing high-humidity air in a drying tank from mixing with outside air.
記開口部を遮閉する空気の流れを形成することにより,
上記乾燥槽内の高湿度雰囲気と外部の雰囲気を遮断する
ように構成されていることを特徴とするハニカム成形体
の乾燥装置。8. The device according to claim 7, wherein the blocking means forms a flow of air for blocking the opening.
An apparatus for drying a honeycomb formed body, wherein the apparatus is configured to shut off a high humidity atmosphere in the drying tank and an external atmosphere.
上記乾燥装置は,上記乾燥槽内にあるハニカム成形体の
数量に応じて,上記マイクロ波の照射条件を変更するよ
うに構成されていることを特徴とするハニカム成形体の
乾燥装置。9. The method according to claim 7, wherein:
The drying device for a honeycomb formed article, wherein the drying device is configured to change the irradiation condition of the microwave according to the number of the honeycomb formed articles in the drying tank.
て,上記搬送装置は,上記乾燥槽内に送入された各ハニ
カム成形体が等間隔に配置されるように,上記ハニカム
成形体の供給を調整するアキュームレータ機能を有して
いることを特徴とするハニカム成形体の乾燥装置。10. The honeycomb molded body according to any one of claims 7 to 9, wherein the conveying device is configured to dispose the honeycomb molded bodies sent into the drying tank at equal intervals. An apparatus for drying a honeycomb formed body, which has an accumulator function for adjusting supply.
て,上記乾燥装置は,上記マイクロ波を導入する導入口
を複数有していることを特徴とするハニカム成形体の乾
燥装置。11. The drying apparatus for a honeycomb formed body according to claim 7, wherein the drying apparatus has a plurality of inlets for introducing the microwave.
は,上記ハニカム成形体を上記乾燥槽に送入するための
開口部近傍に設けた第1導入口と,上記ハニカム成形体
を上記乾燥槽から送出するための開口部近傍に設けた第
2導入口とを有しており,上記第1導入口は,上記送出
側の開口部に向けて上記マイクロ波を照射し,上記第2
導入口は,上記送入側の開口部に向けて上記マイクロ波
を照射するよう構成されていることを特徴とするハニカ
ム成形体の乾燥装置。12. The drying apparatus according to claim 11, wherein the drying device comprises: a first inlet provided near an opening for feeding the honeycomb formed body into the drying tank; A second inlet provided in the vicinity of an opening for sending out, the first inlet irradiating the microwave toward the opening on the sending side, and irradiating the second inlet with the second inlet.
An apparatus for drying a honeycomb formed body, wherein the inlet is configured to irradiate the microwave toward the opening on the inlet side.
は,上記ハニカム成形体を上記乾燥槽に送入するための
開口部の上側に設けた第1導入口と,上記開口部の下側
に設けた第2導入口とを有しており,上記第1導入口及
び上記第2導入口は,上記ハニカム成形体を上記乾燥槽
から送出するための開口部に向けて上記マイクロ波を照
射するよう構成されていることを特徴とするハニカム成
形体の乾燥装置。13. The drying device according to claim 11, wherein the drying device includes a first inlet provided above an opening through which the honeycomb formed body is fed into the drying tank, and a drying device provided below the opening. A first inlet and a second inlet for irradiating the microwave toward an opening for sending out the honeycomb formed body from the drying tank. An apparatus for drying a formed honeycomb article, comprising:
は,上記乾燥槽の上部に設けた第1導入口と,上記乾燥
槽の下部に設けた第2導入口を有しており,上記第1導
入口は,上記乾燥槽の下部に向って上記マイクロ波を照
射し,上記第2導入口は,上記乾燥槽の上部に向って上
記マイクロ波を照射するよう構成されていることを特徴
とするハニカム成形体の乾燥装置。14. The drying device according to claim 11, wherein the drying device has a first inlet provided at an upper part of the drying tank and a second inlet provided at a lower part of the drying tank. The inlet is configured to irradiate the microwave toward a lower part of the drying tank, and the second inlet is configured to irradiate the microwave toward an upper part of the drying tank. Drying device for honeycomb formed body.
は,上記乾燥槽内側の側面であって上記搬送装置を挟ん
で対向する両側面にそれぞれ設けた第1導入口と第2導
入口とを有しており,上記第1導入口は反対側の側面に
向けて上記マイクロ波を照射し,上記第2導入口は反対
側の側面に向けて上記マイクロ波を照射するよう構成さ
れていることを特徴とするハニカム成形体の乾燥装置。15. The drying device according to claim 11, wherein the drying device has a first inlet and a second inlet provided on both sides of the inside of the drying tank opposite to each other with the transfer device interposed therebetween. The first inlet is configured to irradiate the microwave toward the opposite side surface, and the second inlet is configured to irradiate the microwave toward the opposite side surface. A drying device for honeycomb formed bodies.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
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JP2001370393A JP2002283329A (en) | 2001-01-16 | 2001-12-04 | Manufacturing method of honeycomb formed body and drying equipment thereof |
DE10201299A DE10201299A1 (en) | 2001-01-16 | 2002-01-15 | Process for manufacturing a honeycomb body and drying system |
US10/045,085 US6932932B2 (en) | 2001-01-16 | 2002-01-15 | Method of fabricating honeycomb body |
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Application Number | Priority Date | Filing Date | Title |
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JP2001-7930 | 2001-01-16 | ||
JP2001007930 | 2001-01-16 | ||
JP2001370393A JP2002283329A (en) | 2001-01-16 | 2001-12-04 | Manufacturing method of honeycomb formed body and drying equipment thereof |
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ID=26607779
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