JP2008110537A - Manufacturing method of honeycomb structure and drying device used therein - Google Patents

Manufacturing method of honeycomb structure and drying device used therein Download PDF

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JP2008110537A
JP2008110537A JP2006295126A JP2006295126A JP2008110537A JP 2008110537 A JP2008110537 A JP 2008110537A JP 2006295126 A JP2006295126 A JP 2006295126A JP 2006295126 A JP2006295126 A JP 2006295126A JP 2008110537 A JP2008110537 A JP 2008110537A
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Yoshiyuki Oribe
善行 織部
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Denso Corp
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B28WORKING CEMENT, CLAY, OR STONE
    • B28BSHAPING CLAY OR OTHER CERAMIC COMPOSITIONS; SHAPING SLAG; SHAPING MIXTURES CONTAINING CEMENTITIOUS MATERIAL, e.g. PLASTER
    • B28B11/00Apparatus or processes for treating or working the shaped or preshaped articles
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B28WORKING CEMENT, CLAY, OR STONE
    • B28BSHAPING CLAY OR OTHER CERAMIC COMPOSITIONS; SHAPING SLAG; SHAPING MIXTURES CONTAINING CEMENTITIOUS MATERIAL, e.g. PLASTER
    • B28B11/00Apparatus or processes for treating or working the shaped or preshaped articles
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    • C04B38/0006Honeycomb structures
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B15/00Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00Drying solid materials or objects by processes involving the application of heat
    • F26B3/32Drying solid materials or objects by processes involving the application of heat by development of heat within the materials or objects to be dried, e.g. by fermentation or other microbiological action
    • F26B3/34Drying solid materials or objects by processes involving the application of heat by development of heat within the materials or objects to be dried, e.g. by fermentation or other microbiological action by using electrical effects
    • F26B3/347Electromagnetic heating, e.g. induction heating or heating using microwave energy
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B9/00Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity
    • F27B9/14Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity characterised by the path of the charge during treatment; characterised by the means by which the charge is moved during treatment
    • F27B9/20Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity characterised by the path of the charge during treatment; characterised by the means by which the charge is moved during treatment the charge moving in a substantially straight path tunnel furnace
    • F27B9/24Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity characterised by the path of the charge during treatment; characterised by the means by which the charge is moved during treatment the charge moving in a substantially straight path tunnel furnace being carried by a conveyor
    • F27B9/243Endless-strand conveyor
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B9/00Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity
    • F27B9/30Details, accessories, or equipment peculiar to furnaces of these types
    • F27B9/36Arrangements of heating devices
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    • C04B2111/00Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
    • C04B2111/00474Uses not provided for elsewhere in C04B2111/00
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    • C04B2235/3427Silicates other than clay, e.g. water glass
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a manufacturing method of a honeycomb structure suppressing the deformation of a honeycomb molded object at the time of drying and preventing trouble such as cracking, wrinkles, etc., and a drying device used therein. <P>SOLUTION: The manufacturing method of the honeycomb structure has a molding process for molding the honeycomb molded object by subjecting a ceramic material, which contains at least a cordierite raw material, water and a binder, to extrusion molding to cut the extrudate into a predetermined length, a drying process for irradiating the honeycomb molded object with a microwave to dry the same, and a firing process for firing the honeycomb molded object to obtain the honeycomb structure. The drying process is divided into a plurality of steps, and in a first step S1, the center temperature of the honeycomb molded object reaches at least the curing start temperature of the binder from the start of drying, wherein the output of the microwave for irradiating the honeycomb molded object in the first step S1 is set higher than the output of the microwave of the subsequent step. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、内燃機関の排気ガス浄化フィルタ等に用いられるハニカム構造体の製造方法及びそれに用いる乾燥装置に関する。   The present invention relates to a method for manufacturing a honeycomb structure used for an exhaust gas purification filter or the like of an internal combustion engine and a drying apparatus used therefor.

セラミック製のハニカム構造体としては、ハニカム状のセル壁に囲まれた多数のセルと外周側面を覆う筒状の外周壁とを有するものが知られている。ハニカム構造体は、一般的にセラミック材料を押出成形してハニカム成形体を成形し、これを乾燥した後、焼成することによって製造される。   As a ceramic honeycomb structure, one having a large number of cells surrounded by a honeycomb-shaped cell wall and a cylindrical outer peripheral wall covering the outer peripheral side surface is known. A honeycomb structure is generally manufactured by extruding a ceramic material to form a honeycomb formed body, drying it, and firing it.

上記ハニカム構造体を製造するに当たって、ハニカム成形体を乾燥する方法としては、マイクロ波を照射させて乾燥する方法がある(特許文献1参照)。
しかしながら、上記の方法では、ハニカム成形体の中心部の乾燥速度が速くなり、中心部と外周部との乾燥収縮差によって応力が発生する。特に外周部には、中心部に向かって大きな引張応力が発生するため、セル壁に変形が生じる。その結果、外周壁に割れ、しわ等の不具合が発生する。また、マイクロ波の出力を一定としており、ハニカム成形体の温度上昇が緩やかとなるため、水分を多く含んだ状態が長くなり、上記の不具合が発生しやすい。特に、セル壁の厚みが小さくなるほど、上記の不具合は顕著に現れる。
In manufacturing the honeycomb structure, as a method of drying the honeycomb formed body, there is a method of drying by irradiating microwaves (see Patent Document 1).
However, in the above method, the drying speed of the central portion of the honeycomb formed body is increased, and stress is generated due to a difference in drying shrinkage between the central portion and the outer peripheral portion. In particular, since a large tensile stress is generated in the outer peripheral portion toward the central portion, the cell wall is deformed. As a result, defects such as cracks and wrinkles occur in the outer peripheral wall. In addition, since the microwave output is constant and the temperature rise of the honeycomb formed body is moderate, the state of containing a lot of moisture becomes long, and the above-described problems are likely to occur. In particular, as the cell wall thickness becomes smaller, the above-mentioned problem appears more remarkably.

このようなことから、押出成形したハニカム成形体の乾燥時における変形を抑制し、外周壁の割れ、しわ等の不具合を防止することができるハニカム構造体の製造方法が望まれている。   For these reasons, there is a demand for a method for manufacturing a honeycomb structure that can suppress deformation during drying of the extruded honeycomb formed body and prevent problems such as cracking and wrinkling of the outer peripheral wall.

特開2002−283331号公報JP 2002-283331 A

本発明はかかる従来の問題点に鑑みてなされたもので、押出成形したハニカム成形体の乾燥時における変形を抑制し、外周壁の割れ、しわ等の不具合を防止することができるハニカム構造体の製造方法及びそれに用いる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 such conventional problems, and is a honeycomb structure that can suppress deformation during drying of an extruded honeycomb formed body and prevent defects such as cracks and wrinkles in the outer peripheral wall. An object of the present invention is to provide a manufacturing method and a drying apparatus used therefor.

第1の発明は、ハニカム状のセル壁に囲まれた多数のセルと外周側面を覆う筒状の外周壁とを有するコーディエライトセラミック製のハニカム構造体を製造する方法において、
少なくともコーディエライト原料、水、及びバインダを含有するセラミック材料を押出成形して所定長さに切断し、ハニカム成形体を成形する成形工程と、
マイクロ波を照射することにより上記ハニカム成形体を乾燥する乾燥工程と、
上記ハニカム成形体を焼成して上記ハニカム構造体を得る焼成工程とを有し、
上記乾燥工程では、該乾燥工程を複数のステップに分け、乾燥開始から上記ハニカム成形体の中心部の温度が少なくとも上記バインダの硬化開始温度に達するまでを第1ステップとし、該第1ステップにおいて上記ハニカム成形体に照射するマイクロ波出力を、その後のステップのマイクロ波出力よりも高く設定することを特徴とするハニカム構造体の製造方法にある(請求項1)。
A first invention is a method of manufacturing a cordierite ceramic honeycomb structure having a large number of cells surrounded by a honeycomb-shaped cell wall and a cylindrical outer peripheral wall covering an outer peripheral side surface.
A molding step of forming a honeycomb formed body by extruding a ceramic material containing at least a cordierite raw material, water, and a binder and cutting it to a predetermined length;
A drying step of drying the honeycomb formed body by irradiation with microwaves;
A firing step of firing the honeycomb formed body to obtain the honeycomb structure,
In the drying step, the drying step is divided into a plurality of steps, and the first step is from the start of drying until the temperature of the central portion of the honeycomb formed body reaches at least the curing start temperature of the binder. A method for manufacturing a honeycomb structure is characterized in that the microwave output irradiated to the honeycomb formed body is set higher than the microwave output in the subsequent step.

本発明のハニカム構造体の製造方法において、上記乾燥工程は、複数のステップに分けられ、乾燥開始から上記ハニカム成形体の中心部の温度が少なくとも上記バインダの硬化開始温度に達するまでを第1ステップとする。そして、この第1ステップでは、上記ハニカム成形体に照射するマイクロ波出力を、その後のステップのマイクロ波出力よりも高く設定する。   In the method for manufacturing a honeycomb structured body of the present invention, the drying step is divided into a plurality of steps, and the first step is from the start of drying until the temperature of the central portion of the honeycomb formed body reaches at least the curing start temperature of the binder. And And in this 1st step, the microwave output irradiated to the said honeycomb molded object is set higher than the microwave output of a subsequent step.

すなわち、上記成形工程直後の上記ハニカム成形体は、まだ多くの水分を含んでおり、変形しやすい状態にある。本発明では、上記乾燥工程の複数のステップのうち、最初のステップである上記第1ステップの上記マイクロ波出力を最も高くしたのである。そのため、上記ハニカム成形体の温度を早期に上昇させ、上記乾燥工程のできるだけ最初の段階で上記ハニカム成形体中に含まれる水分を除去することができる。そして、上記ハニカム成形体の中心部の温度が上記バインダの硬化開始温度に達するまでの時間を短縮することができる。つまり、上記第1ステップの時間を短縮することができる。   That is, the honeycomb formed body immediately after the forming step still contains a lot of moisture and is easily deformed. In the present invention, the microwave output of the first step, which is the first step among the plurality of steps of the drying process, is made highest. Therefore, the temperature of the honeycomb formed body can be raised early, and moisture contained in the honeycomb formed body can be removed at the earliest possible stage of the drying step. And time until the temperature of the center part of the said honeycomb molded object reaches the hardening start temperature of the said binder can be shortened. That is, the time of the first step can be shortened.

これにより、上記乾燥工程全体の時間を一定とした場合、上記乾燥工程全体に占める上記第1ステップの時間を短縮することができる。そして、上記乾燥工程における上記ハニカム成形体は、水分が多く含まれた変形しやすい状態を短縮することができる。それ故に、乾燥時における上記セル壁の変形を抑制することができ、上記外周壁に割れ、しわ等の不具合が発生することを防止することができる。   Thereby, when the time of the said whole drying process is made constant, the time of the said 1st step which occupies for the said whole drying process can be shortened. And the said honeycomb molded object in the said drying process can shorten the state which is easy to deform | transform which contained much moisture. Therefore, deformation of the cell wall at the time of drying can be suppressed, and problems such as cracks and wrinkles can be prevented from occurring on the outer peripheral wall.

このように、本発明のハニカム構造体の製造方法によれば、押出成形したハニカム成形体の乾燥時における変形を抑制し、外周壁の割れ、しわ等の不具合を防止することができる。   As described above, according to the method for manufacturing a honeycomb structured body of the present invention, it is possible to suppress deformation of the extruded honeycomb formed body during drying and to prevent problems such as cracks and wrinkles on the outer peripheral wall.

第2の発明は、ハニカム状のセル壁に囲まれた多数のセルと外周側面を覆う筒状の外周壁とを有するコーディエライトセラミック製のハニカム構造体を製造するに当たって、少なくともコーディエライト原料、水、及びバインダを含有するセラミック材料を押出成形し、所定長さに切断したハニカム成形体を乾燥する乾燥装置において、
該乾燥装置は、上記ハニカム成形体を収納する乾燥槽と、該乾燥槽内において上記ハニカム成形体を連続的に搬送する搬送コンベアと、上記乾燥槽内において上記ハニカム成形体の搬送方向に複数配設されたマイクロ波を照射するマイクロ波発生装置とを有し、
上記乾燥槽は、複数のゾーンに分割され、上記ハニカム成形体が最初に搬送される第1ゾーンの上記マイクロ波発生装置は、上記ハニカム成形体が上記第1ゾーンを通過する間に、上記ハニカム成形体の中心部の温度が少なくとも上記バインダの硬化開始温度に達するようにマイクロ波出力が設定されるよう構成されており、かつ、該マイクロ波出力は、その他のゾーンよりも高いことを特徴とする乾燥装置にある(請求項7)。
According to a second aspect of the present invention, at least a cordierite raw material is used in manufacturing a cordierite ceramic honeycomb structure having a large number of cells surrounded by a honeycomb-shaped cell wall and a cylindrical outer peripheral wall covering the outer peripheral side surface. In a drying apparatus for extruding a ceramic material containing water and a binder and drying the honeycomb formed body cut into a predetermined length,
The drying apparatus includes a drying tank that accommodates the honeycomb formed body, a transport conveyor that continuously transports the honeycomb formed body in the drying tank, and a plurality of the drying apparatuses arranged in the transport direction of the honeycomb formed body in the drying tank. A microwave generator for irradiating the installed microwave,
The drying tank is divided into a plurality of zones, and the microwave generator in the first zone to which the honeycomb formed body is first conveyed is the honeycomb generator while the honeycomb formed body passes through the first zone. The microwave output is configured so that the temperature of the central portion of the molded body reaches at least the curing start temperature of the binder, and the microwave output is higher than other zones. (7).

本発明の乾燥装置において、上記乾燥槽は、複数のゾーンに分割され、上記ハニカム成形体が最初に搬送される部分に第1ゾーンが設けられている。この第1ゾーンの上記マイクロ波発生装置は、上記ハニカム成形体が上記第1ゾーンを通過する間に、上記ハニカム成形体の中心部の温度が少なくとも上記バインダの硬化開始温度に達するようにマイクロ波出力が設定され、さらにそのマイクロ波出力がその他のゾーンよりも高く設定されるよう構成されている。   In the drying apparatus of the present invention, the drying tank is divided into a plurality of zones, and a first zone is provided in a portion where the honeycomb formed body is first conveyed. The microwave generator in the first zone is configured so that the temperature of the central portion of the honeycomb formed body reaches at least the curing start temperature of the binder while the honeycomb formed body passes through the first zone. The output is set, and the microwave output is set higher than the other zones.

すなわち、押出成形直後の上記ハニカム成形体は、まだ多くの水分を含んでおり、変形しやすい状態にある。本発明の乾燥装置は、押出成形後の上記ハニカム成形体を搬入して乾燥する上記乾燥槽の複数のゾーンのうち、最初のゾーンである上記第1ゾーンにおける上記マイクロ波発生装置のマイクロ波出力が最も高く設定されるよう構成したのである。そのため、上記第1ゾーンにおいて、上記バインダが硬化を開始するまでに上記ハニカム成形体中に含まれる水分をできるだけ除去することができる。これにより、上記ハニカム成形体に水分が多く含まれ、該ハニカム成形体が変形しやすい状態を短縮することができる。それ故に、乾燥時における上記セル壁の変形を抑制することができ、上記外周壁の割れ、しわ等の不具合が発生することを防止することができる。   That is, the honeycomb formed body immediately after extrusion molding still contains a lot of moisture and is in a state of being easily deformed. The drying apparatus of the present invention is a microwave output of the microwave generator in the first zone, which is the first zone among the plurality of zones of the drying tank that carries in and drys the honeycomb formed body after extrusion molding. Is set to the highest value. Therefore, in the first zone, moisture contained in the honeycomb formed body can be removed as much as possible before the binder starts to cure. Accordingly, it is possible to shorten a state in which the honeycomb formed body contains a large amount of moisture and the honeycomb formed body is easily deformed. Therefore, deformation of the cell wall at the time of drying can be suppressed, and problems such as cracking and wrinkling of the outer peripheral wall can be prevented.

このように、本発明の乾燥装置を用いることにより、押出成形したハニカム成形体の乾燥時における変形を抑制し、外周壁の割れ、しわ等の不具合を防止することができる。   Thus, by using the drying apparatus of the present invention, it is possible to suppress deformation during drying of the extruded honeycomb formed body, and to prevent problems such as cracks and wrinkles on the outer peripheral wall.

上記第1の発明においては、上記ハニカム成形体の中心部とは、該ハニカム成形体の径方向断面における中心点、及びその中心点と同等の温度を示す中心点近傍の上記セル壁の部分である。
また、上記バインダの硬化開始温度とは、上記ハニカム成形体中のバインダが硬化を開始する温度であり、上記ハニカム成形体がゲル化し始める温度である。
In the first aspect of the invention, the central part of the honeycomb formed body is a center point in the radial cross section of the honeycomb formed body and a portion of the cell wall in the vicinity of the center point indicating a temperature equivalent to the center point. is there.
The curing start temperature of the binder is a temperature at which the binder in the honeycomb formed body starts to be cured, and is a temperature at which the honeycomb formed body starts to gel.

また、上記第1ステップでは、上記ハニカム成形体の上記中心部の温度が上記バインダの硬化開始温度に達した時点において、上記中心部と上記外周壁との温度差が5℃以下となるように、上記マイクロ波出力を設定することが好ましい(請求項2)。
この場合には、上記中心部と上記外周壁との乾燥収縮差によって生じる応力を低減し、上記ハニカム成形体の変形をさらに抑制することができる。
In the first step, when the temperature of the central portion of the honeycomb formed body reaches the curing start temperature of the binder, the temperature difference between the central portion and the outer peripheral wall is 5 ° C. or less. Preferably, the microwave output is set (claim 2).
In this case, it is possible to reduce the stress caused by the difference in drying shrinkage between the central portion and the outer peripheral wall, and to further suppress the deformation of the honeycomb formed body.

また、上記第1ステップでは、上記ハニカム成形体の単位質量当たりの上記マイクロ波出力を20W/gにすることが好ましい(請求項3)。
この場合には、上記ハニカム成形体に多くの水分が含まれている状態を確実に短縮することができ、上記ハニカム成形体の乾燥時における変形をさらに抑制することができる。
In the first step, it is preferable that the microwave output per unit mass of the honeycomb formed body is 20 W / g.
In this case, the state in which the honeycomb formed body contains a large amount of moisture can be reliably shortened, and deformation of the honeycomb formed body during drying can be further suppressed.

また、上記乾燥工程では、上記ステップ毎に上記マイクロ波出力を段階的に小さくすることが好ましい(請求項4)。
この場合には、上記乾燥工程における上記ハニカム成形体への熱衝撃を小さくすることができ、割れ等の発生を防止することができる。
Moreover, in the said drying process, it is preferable to make the said microwave output small in steps for every said step (Claim 4).
In this case, the thermal shock to the honeycomb formed body in the drying step can be reduced, and the occurrence of cracks and the like can be prevented.

また、上記乾燥工程では、上記ハニカム成形体の上記中心部と上記外周壁との温度差が5℃以下となるように、上記各ステップの上記マイクロ波出力を設定することが好ましい(請求項5)。
この場合には、上記乾燥工程全体において、上記中心部と上記外周壁との乾燥収縮差によって生じる応力を低減し、上記ハニカム成形体の変形をさらに抑制することができる。
In the drying step, the microwave output of each step is preferably set so that a temperature difference between the central portion of the honeycomb formed body and the outer peripheral wall is 5 ° C. or less. ).
In this case, in the whole drying process, stress generated by the drying shrinkage difference between the central portion and the outer peripheral wall can be reduced, and deformation of the honeycomb formed body can be further suppressed.

また、上記乾燥工程後における上記ハニカム成形体の上記セル壁の厚みは、70μm以下であることが好ましい(請求項6)。
すなわち、上記セル壁の厚みが薄い上記ハニカム成形体に対して、本発明の製造方法を用いることにより、乾燥時における上記セル壁の変形を抑制するという効果をより有効に発揮することができる。
The thickness of the cell wall of the honeycomb formed body after the drying step is preferably 70 μm or less.
That is, the effect of suppressing the deformation of the cell wall during drying can be more effectively exhibited by using the manufacturing method of the present invention for the honeycomb formed body having the thin cell wall.

また、上記乾燥工程では、それぞれのステップ間の上記マイクロ波出力を一定とすることが好ましい。
この場合には、上記マイクロ波出力を制御しやすく、上記乾燥工程を円滑に進めることができる。
なお、それぞれのステップ間の上記マイクロ波出力を一定とせずに、変化をつけることもできる。ただし、上記ステップ毎に上記マイクロ波出力を段階的に小さくする場合には、直前のステップの上記マイクロ波出力よりも小さい範囲内で設定する必要がある。
Moreover, in the said drying process, it is preferable to make the said microwave output between each step constant.
In this case, it is easy to control the microwave output, and the drying process can proceed smoothly.
It should be noted that the microwave output between each step can be changed without making it constant. However, when the microwave output is reduced step by step for each step, it is necessary to set the microwave output within a range smaller than the microwave output of the immediately preceding step.

また、上記乾燥工程では、上記ハニカム成形体の乾燥に必要なマイクロ波の合計出力を予め求めておき、これを基に合計出力範囲内で上記各ステップの上記マイクロ波出力を設定することが好ましい。
この場合には、上記乾燥工程における上記ハニカム成形体の過乾燥を防止することができる。
In the drying step, it is preferable to obtain in advance the total output of microwaves necessary for drying the honeycomb formed body, and set the microwave output of each step within the total output range based on this. .
In this case, overdrying of the honeycomb formed body in the drying step can be prevented.

上記第2の発明においては、上記第1ゾーンの上記マイクロ波発生装置は、上記ハニカム成形体の上記中心部の温度が上記バインダの硬化開始温度に達した時点において、上記中心部と上記外周壁との温度差が5℃以下となるように、上記マイクロ波出力が設定されるよう構成されていることが好ましい(請求項8)。
この場合には、上記中心部と上記外周壁との乾燥収縮差によって生じる応力を低減し、上記ハニカム成形体の変形をさらに抑制することができる。
In the second invention, the microwave generator in the first zone is configured such that the temperature of the central portion of the honeycomb formed body reaches the curing start temperature of the binder and the central portion and the outer peripheral wall. It is preferable that the microwave output is set so that the temperature difference with respect to 5 ° C. or less is set.
In this case, it is possible to reduce the stress caused by the difference in drying shrinkage between the central portion and the outer peripheral wall, and to further suppress the deformation of the honeycomb formed body.

また、上記第1ゾーンの上記マイクロ波発生装置は、上記ハニカム成形体の単位質量当たりの上記マイクロ波出力が20W/gに設定されるよう構成されていることが好ましい(請求項9)。
この場合には、上記ハニカム成形体に多くの水分が含まれている状態を確実に短縮することができ、上記ハニカム成形体の乾燥時における変形をさらに抑制することができる。
The microwave generator in the first zone is preferably configured so that the microwave output per unit mass of the honeycomb formed body is set to 20 W / g.
In this case, the state in which the honeycomb formed body contains a large amount of moisture can be reliably shortened, and deformation of the honeycomb formed body during drying can be further suppressed.

また、上記乾燥槽の上記マイクロ波発生装置は、上記ゾーン毎に上記マイクロ波出力が段階的に小さく設定されるよう構成されていることが好ましい(請求項10)。
この場合には、上記乾燥工程における上記ハニカム成形体への熱衝撃を小さくすることができ、割れ等の発生を防止することができる。
Moreover, it is preferable that the said microwave generator of the said drying tank is comprised so that the said microwave output may be set small in steps for every said zone (Claim 10).
In this case, the thermal shock to the honeycomb formed body in the drying step can be reduced, and the occurrence of cracks and the like can be prevented.

また、上記乾燥槽の上記マイクロ波発生装置は、上記ハニカム成形体の上記中心部と上記外周壁との温度差が5℃以下となるように、上記各ゾーンの上記マイクロ波出力が設定されるよう構成されていることが好ましい(請求項11)。
この場合には、上記乾燥工程全体において、上記中心部と上記外周壁との乾燥収縮差によって生じる応力を低減し、上記ハニカム成形体の変形をさらに抑制することができる。
In the microwave generator of the drying tank, the microwave output of each zone is set so that a temperature difference between the central portion of the honeycomb formed body and the outer peripheral wall is 5 ° C. or less. It is preferable to be configured as described above (claim 11).
In this case, in the whole drying process, stress generated by the drying shrinkage difference between the central portion and the outer peripheral wall can be reduced, and deformation of the honeycomb formed body can be further suppressed.

本発明の実施例にかかるハニカム構造体の製造方法及びそれに用いる乾燥装置について説明する。
本例は、図1に示すごとく、ハニカム状のセル壁11に囲まれた多数の四角形状のセル12と外周側面を覆う筒状の外周壁13とを有するコーディエライトセラミック製のハニカム構造体1を製造する方法である。本例のハニカム構造体1は、略円柱状を呈している。なお、ハニカム構造体1の全体形状、セル12の形状等は、用途に合わせて変更することができる。
また、後述のハニカム成形体10の中心部101とは、図5に示すごとく、ハニカム成形体10の径方向断面における中心点、及びその中心点と同等の温度を示す中心点近傍のセル壁11の部分である。
A method for manufacturing a honeycomb structure according to an embodiment of the present invention and a drying apparatus used therefor will be described.
In this example, as shown in FIG. 1, a honeycomb structure made of cordierite ceramic having a large number of rectangular cells 12 surrounded by a honeycomb-shaped cell wall 11 and a cylindrical outer peripheral wall 13 covering the outer peripheral side surface. 1 is a method of manufacturing 1. The honeycomb structure 1 of the present example has a substantially cylindrical shape. Note that the overall shape of the honeycomb structure 1, the shape of the cells 12, and the like can be changed according to the application.
Further, as shown in FIG. 5, the center portion 101 of the honeycomb molded body 10 to be described later is a central point in the radial cross section of the honeycomb molded body 10 and a cell wall 11 in the vicinity of the central point indicating a temperature equivalent to the central point. It is a part of.

そして、本例のハニカム構造体1の製造方法は、少なくともコーディエライト原料、水、及びバインダを含有するセラミック材料を押出成形して所定長さに切断し、ハニカム成形体10(図1参照)を成形する成形工程と、マイクロ波を照射することによりハニカム成形体10を乾燥する乾燥工程と、ハニカム成形体10を焼成してハニカム構造体1を得る焼成工程とを行う。
乾燥工程では、該乾燥工程を複数のステップに分け、乾燥開始からハニカム成形体10の中心部101の温度が少なくともバインダの硬化開始温度に達するまでを第1ステップS1とし、該第1ステップS1においてハニカム成形体10に照射するマイクロ波出力を、その後のステップのマイクロ波出力よりも高く設定する。
以下、これを詳説する。
And the manufacturing method of the honeycomb structure 1 of this example extrude-molds the ceramic material containing at least a cordierite raw material, water, and a binder, cut | disconnects to predetermined length, and the honeycomb molded body 10 (refer FIG. 1). A forming step for forming the honeycomb structure, a drying step for drying the honeycomb formed body 10 by irradiation with microwaves, and a firing step for firing the honeycomb formed body 10 to obtain the honeycomb structure 1 are performed.
In the drying process, the drying process is divided into a plurality of steps, and the first step S1 is a period from the start of drying until the temperature of the central portion 101 of the honeycomb formed body 10 reaches at least the curing start temperature of the binder. The microwave output irradiated to the honeycomb formed body 10 is set to be higher than the microwave output in the subsequent steps.
This will be described in detail below.

<成形工程>
まず、焼成後にコーディエライトセラミックとなるセラミック材料を作製する。具体的には、コーディエライト原料100重量%に対して、水を19.5重量%、バインダを4.5重量%添加して混錬し、セラミック材料を作製する。なお、原料粉末である上記コーディエライト原料としては、最終的にコーディエライト(2MgO・2Al23・5SiO2)を主成分とする組成となるように、タルク38〜40重量%、カオリン46〜48重量%、アルミナ12〜16重量%の割合で混合したものを用いた。また、上記バインダとしては、メチルセルロースを用いた。
<Molding process>
First, a ceramic material that becomes cordierite ceramic after firing is prepared. Specifically, 19.5% by weight of water and 4.5% by weight of binder are added to 100% by weight of the cordierite raw material and kneaded to produce a ceramic material. The cordierite raw material, which is a raw material powder, includes talc of 38 to 40% by weight, kaolin so that the final composition is cordierite (2MgO · 2Al 2 O 3 · 5SiO 2 ). A mixture of 46 to 48% by weight and alumina of 12 to 16% by weight was used. Moreover, methylcellulose was used as the binder.

次いで、上記セラミック材料を押出成形機(図示略)を用いて、ハニカム成形型より押し出す。そして、順次所定長さに切断し、ハニカム成形体10を成形する。
なお、成形後のハニカム成形体10は、質量が1430g、比重が約2.0、水分率が19.5%であった。
Next, the ceramic material is extruded from a honeycomb mold using an extruder (not shown). Then, the honeycomb formed body 10 is formed by sequentially cutting to a predetermined length.
The molded honeycomb body 10 after molding had a mass of 1430 g, a specific gravity of about 2.0, and a moisture content of 19.5%.

<乾燥工程>
次いで、得られたハニカム成形体10を図2に示す乾燥装置2を用いて乾燥する。
本例の乾燥装置2は、同図に示すごとく、ハニカム成形体10を収納する乾燥槽21と、乾燥槽21内においてハニカム成形体10を連続的に搬送する搬送コンベア22と、乾燥槽21内においてハニカム成形体10の搬送方向に複数配設されたマイクロ波を照射するマイクロ波発生装置23とを有する。
<Drying process>
Next, the obtained honeycomb formed body 10 is dried using the drying apparatus 2 shown in FIG.
As shown in the figure, the drying device 2 of the present example includes a drying tank 21 that accommodates the honeycomb formed body 10, a conveyor 22 that continuously conveys the honeycomb formed body 10 in the drying tank 21, and a drying tank 21. And a microwave generator 23 for irradiating a plurality of microwaves arranged in the conveying direction of the honeycomb formed body 10.

乾燥装置2は、搬送コンベア22を取り囲むように乾燥槽21を形成してある。乾燥槽21には、搬送コンベア22を貫通させると共に搬送コンベア22に載置したハニカム成形体10を通過させるための搬入口211と搬出口212とが設けられている。
また、乾燥槽21の上壁面には、全部で7基のマイクロ波発生装置23が等間隔で設けられている。マイクロ波発生装置23は、制御装置(図示略)と接続されており、この制御装置からの制御信号に基づいてマイクロ波の出力を制御して照射するように構成されている。
The drying device 2 has a drying tank 21 formed so as to surround the conveyor 22. The drying tank 21 is provided with a carry-in port 211 and a carry-out port 212 for allowing the honeycomb formed body 10 placed on the feed conveyor 22 to pass through the feed conveyor 22.
In addition, a total of seven microwave generators 23 are provided at equal intervals on the upper wall surface of the drying tank 21. The microwave generator 23 is connected to a control device (not shown), and is configured to control and irradiate a microwave output based on a control signal from the control device.

また、本例の乾燥槽21は、図2に示すごとく、ハニカム成形体10の搬送方向に複数のゾーン(第1ゾーンZ1、第2ゾーンZ2、及び第3ゾーンZ3)に分割されている。
ハニカム成形体10が最初に搬送される第1ゾーンZ1には、3基のマイクロ波発生装置23が設けられている。この第1ゾーンZ1のマイクロ波発生装置23は、ハニカム成形体10が第1ゾーンZ1を通過する間に、ハニカム成形体10の中心部101の温度が少なくともバインダの硬化開始温度(本例では約60℃)に達するようにマイクロ波出力が設定されるよう構成されている。本例では、第1ゾーンZ1の各マイクロ波発生装置23のマイクロ波出力を28.6kWとした。つまり、乾燥前のハニカム成形体10の単位質量当たりに換算して20W/gとした。
Moreover, the drying tank 21 of this example is divided | segmented into the some zone (1st zone Z1, 2nd zone Z2, and 3rd zone Z3) in the conveyance direction of the honeycomb molded object 10, as shown in FIG.
Three microwave generators 23 are provided in the first zone Z1 in which the honeycomb formed body 10 is first conveyed. In the microwave generator 23 of the first zone Z1, the honeycomb molded body 10 passes through the first zone Z1, and the temperature of the central portion 101 of the honeycomb molded body 10 is at least the binder curing start temperature (in this example, about The microwave output is set to reach 60 ° C. In this example, the microwave output of each microwave generator 23 in the first zone Z1 is 28.6 kW. That is, it was set to 20 W / g in terms of unit mass of the honeycomb formed body 10 before drying.

また、第2ゾーンZ2及び第3ゾーンZ3には、それぞれ2基のマイクロ波発生装置23が設けられている。第2ゾーンZ2及び第3ゾーンZ3のマイクロ波発生装置23のマイクロ波出力は、それぞれ20kW(14W/g)、14kW(9.8W/g)とした。
つまり、本例の各マイクロ波発生装置23のマイクロ波出力は、第1ゾーンZ1が最も高くなるように、またゾーン毎に段階的に小さくなるように設定した。
In addition, two microwave generators 23 are provided in each of the second zone Z2 and the third zone Z3. The microwave outputs of the microwave generators 23 in the second zone Z2 and the third zone Z3 were 20 kW (14 W / g) and 14 kW (9.8 W / g), respectively.
That is, the microwave output of each microwave generator 23 of this example was set so that the first zone Z1 was the highest and decreased stepwise for each zone.

なお、各ゾーンの領域及びゾーンの数は、上記7基のマイクロ波発生装置23の選択数によって変更可能であり、処理すべきハニカム成形体10の仕様に合わせて最適となるように調整することができる。もちろん、乾燥槽21に配設するマイクロ波発生装置23の数を変更したり、配設位置を調整したりすることもできる。   In addition, the area | region of each zone and the number of zones can be changed with the selection number of the said seven microwave generators 23, and it adjusts so that it may become optimal according to the specification of the honeycomb molded object 10 which should be processed. Can do. Of course, the number of the microwave generators 23 arranged in the drying tank 21 can be changed or the arrangement position can be adjusted.

このような構成の乾燥装置2を用いて、押出成形したハニカム成形体10を乾燥するに当たっては、図2に示すごとく、まずハニカム成形体10を搬送トレイ24上に載置し、これを搬送コンベア22上に載置する。これにより、ハニカム成形体10は、搬入口211から乾燥槽21内へ搬入される。乾燥槽21内に搬入されたハニカム成形体10は、搬送コンベア22によって第1ゾーンZ1、第2ゾーンZ2、及び第3ゾーンZ3を通過して搬出口212へと搬送され、その間に各マイクロ波発生装置23から照射されるマイクロ波によって乾燥されていく。その後、ハニカム成形体10は、乾燥槽21内の搬出口212から搬出される。これにより、ハニカム成形体10を乾燥する。   In drying the extruded honeycomb formed body 10 using the drying apparatus 2 having such a configuration, as shown in FIG. 2, first, the honeycomb formed body 10 is placed on the transport tray 24, and this is transported to the transport conveyor. 22 is mounted. Thereby, the honeycomb formed body 10 is carried into the drying tank 21 from the carry-in port 211. The honeycomb molded body 10 carried into the drying tank 21 passes through the first zone Z1, the second zone Z2, and the third zone Z3 by the conveyor 22 and is conveyed to the carry-out port 212. It is dried by the microwave irradiated from the generator 23. Thereafter, the honeycomb formed body 10 is unloaded from the unloading port 212 in the drying tank 21. Thereby, the honeycomb formed body 10 is dried.

すなわち、本例の乾燥工程は、3つのステップに分けることができる。ハニカム成形体10が第1ゾーンZ1を通過する第1ステップS1、第2ゾーンZ2を通過する第2ステップS2、そして第3ゾーンZ3を通過する第3ステップS3である。第1ステップS1では、ハニカム成形体10をマイクロ波出力20W/gで乾燥し、第2ステップS2では、マイクロ波出力14W/gで乾燥し、そして第3ステップS3では、マイクロ波出力9.8W/gで乾燥する。また、各ハニカム成形体10の搬入口211から搬出口212までの搬送時間は0.5時間とした。なお、図3には、各ステップにおけるマイクロ波出力(W/g)と時間(h)との関係を示した。   That is, the drying process of this example can be divided into three steps. A first step S1 in which the honeycomb formed body 10 passes through the first zone Z1, a second step S2 through which the second zone Z2 passes, and a third step S3 through which the third zone Z3 passes. In the first step S1, the honeycomb formed body 10 is dried at a microwave output of 20 W / g, in the second step S2, is dried at a microwave output of 14 W / g, and in the third step S3, the microwave output is 9.8 W. Dry at / g. The transport time from the carry-in port 211 to the carry-out port 212 of each honeycomb formed body 10 was set to 0.5 hour. FIG. 3 shows the relationship between the microwave output (W / g) and time (h) in each step.

<焼成工程>
次いで、乾燥後のハニカム成形体10を冷却する。そして、最高温度1380℃、焼成時間72時間の条件で焼成する。
以上により、図1のハニカム構造体1を得る。
<Baking process>
Next, the dried honeycomb formed body 10 is cooled. Baking is performed under conditions of a maximum temperature of 1380 ° C. and a baking time of 72 hours.
Thus, the honeycomb structure 1 of FIG. 1 is obtained.

次に、本実施例のハニカム構造体1の製造方法の有効性を示すため、以下のような評価を行った。
まず、本実施例と同様のサイズのハニカム成形体10を成形する。このとき、予め乾燥後のセル壁11が所望の厚みとなるようにハニカム成形体10を成形する。乾燥後のセル壁11の厚みは、69μm、79μm、83μm、88μmの4種類とし、各条件について6つの試験体を用意した。次いで、上記の乾燥装置2を用い、図3に示すようなマイクロ波出力パターンでハニカム成形体10を乾燥する。そして、乾燥後のハニカム成形体10について、外周壁13の割れ、しわ等の不具合の発生の有無を目視によって観察した。
また、比較例として、図4に示すごとく、従来のようにマイクロ波出力を一定として乾燥し、実施例と同様に、外周壁13の割れ、しわ等の不具合の発生を評価した。
Next, in order to show the effectiveness of the manufacturing method of the honeycomb structure 1 of the present example, the following evaluation was performed.
First, the honeycomb formed body 10 having the same size as that of the present embodiment is formed. At this time, the honeycomb formed body 10 is formed so that the cell wall 11 after drying has a desired thickness. The thickness of the cell wall 11 after drying was four types of 69 μm, 79 μm, 83 μm, and 88 μm, and six specimens were prepared for each condition. Next, the honeycomb formed body 10 is dried with the microwave output pattern as shown in FIG. Then, the dried honeycomb formed body 10 was visually observed for occurrence of defects such as cracks and wrinkles in the outer peripheral wall 13.
As a comparative example, as shown in FIG. 4, drying was performed with the microwave output constant as in the prior art, and the occurrence of defects such as cracks and wrinkles in the outer peripheral wall 13 was evaluated in the same manner as in the example.

各条件における不具合の発生についての結果を表1に示す。
同表からわかるように、セル壁11の厚み79μm以上の条件においては、実施例、比較例共に不具合の発生は確認されなかった。しかし、セル壁11の厚み69μmの条件においては、実施例に不具合の発生は確認されなかったが、比較例の6つの試験体全てに不具合の発生が確認された。
Table 1 shows the results of occurrence of defects under each condition.
As can be seen from the table, the occurrence of defects was not confirmed in both the example and the comparative example under the condition where the thickness of the cell wall 11 was 79 μm or more. However, under the condition of the cell wall 11 having a thickness of 69 μm, no defect was confirmed in the example, but the defect was confirmed in all six test specimens of the comparative examples.

このように、実施例は、比較例に比べて乾燥後のセル壁11の厚みが薄いハニカム成形体10においても、外周壁13の割れ、しわ等の不具合の発生を防止できることがわかる。特に、セル壁11の厚みが70μm以下の条件において、上記の効果を発揮することができる。   Thus, it can be seen that the example can prevent the occurrence of defects such as cracks and wrinkles in the outer peripheral wall 13 even in the honeycomb molded body 10 in which the thickness of the cell wall 11 after drying is smaller than that of the comparative example. In particular, the above effect can be exhibited under the condition that the thickness of the cell wall 11 is 70 μm or less.

Figure 2008110537
Figure 2008110537

次に、実施例と比較例との間に差異が見られたセル壁11の厚み69μmの条件において、乾燥時におけるハニカム成形体10の温度を評価した。
まず、成形したハニカム成形体10にファイバー温度計を取り付ける。ファイバー温度計の取り付け場所は、図5に示すごとく、ハニカム成形体10の中心部101に2箇所(A1、A2)、外周壁13に2箇所(B1、B2)の計4箇所とした。次いで、ファイバー温度計で各部の温度を測定しながらハニカム成形体10を乾燥する。そして、中心部101と外周部13との最大の温度差を内外温度差ΔTとして求めた。また、乾燥開始からハニカム成形体10中に含まれるバインダが硬化を開始するバインダ硬化開始点T1までの時間を測定した。
Next, the temperature of the honeycomb formed body 10 at the time of drying was evaluated under the condition of a thickness of 69 μm of the cell wall 11 in which a difference was found between the example and the comparative example.
First, a fiber thermometer is attached to the formed honeycomb formed body 10. As shown in FIG. 5, the fiber thermometers were installed in a total of four locations, two at the center 101 of the honeycomb molded body 10 (A1, A2) and two at the outer peripheral wall 13 (B1, B2). Next, the honeycomb formed body 10 is dried while measuring the temperature of each part with a fiber thermometer. Then, the maximum temperature difference between the central portion 101 and the outer peripheral portion 13 was obtained as an internal / external temperature difference ΔT. Further, the time from the start of drying to the binder curing start point T1 at which the binder contained in the honeycomb formed body 10 starts curing was measured.

比較例では、図4に示すごとく、乾燥開始からバインダ硬化開始点T1までの時間は0.3時間であった。また、バインダ硬化開始点T1における内外温度差ΔTは約14℃であった。
これに対して実施例では、図3に示すごとく、乾燥開始からバインダ硬化開始点T1までの時間は0.2時間であった。また、バインダ硬化開始点T1における内外温度差ΔTは約4℃であった。
In the comparative example, as shown in FIG. 4, the time from the start of drying to the binder curing start point T1 was 0.3 hours. The internal / external temperature difference ΔT at the binder curing start point T1 was about 14 ° C.
On the other hand, in the example, as shown in FIG. 3, the time from the start of drying to the binder curing start point T1 was 0.2 hours. The internal / external temperature difference ΔT at the binder curing start point T1 was about 4 ° C.

このように、実施例では、比較例に比べて乾燥開始からバインダ硬化開始点T1までの時間が短縮されていることがわかる。また、バインダ硬化開始点T1における内外温度差ΔTも小さくなっていることがわかる。   Thus, in an Example, it turns out that the time from drying start to binder hardening start point T1 is shortened compared with the comparative example. It can also be seen that the internal / external temperature difference ΔT at the binder curing start point T1 is also small.

次に、上記の結果を踏まえて、本例のハニカム構造体1の製造方法における作用効果を説明する。
本例のハニカム構造体1の製造方法において、乾燥工程は、複数のステップに分けられ、乾燥開始からハニカム成形体10の中心部101の温度が少なくともバインダの硬化開始温度に達するまでを第1ステップS1とする。そして、この第1ステップS1では、ハニカム成形体10に照射するマイクロ波出力を、その後のステップ(第2ステップS2、第3ステップS3)のマイクロ波出力よりも高く設定する。
Next, based on the above results, the operational effects in the method for manufacturing the honeycomb structure 1 of the present example will be described.
In the method for manufacturing the honeycomb structure 1 of the present example, the drying process is divided into a plurality of steps. The first step is from the start of drying until the temperature of the central portion 101 of the honeycomb formed body 10 reaches at least the curing start temperature of the binder. Let S1. And in this 1st step S1, the microwave output irradiated to the honeycomb molded object 10 is set higher than the microwave output of a subsequent step (2nd step S2, 3rd step S3).

すなわち、成形工程直後のハニカム成形体10は、まだ多くの水分を含んでおり、変形しやすい状態にある。本例では、乾燥工程の複数のステップのうち、最初のステップである第1ステップS1のマイクロ波出力を最も高くしたのである。そのため、ハニカム成形体10の温度を早期に上昇させ、乾燥工程のできるだけ最初の段階でハニカム成形体10中に含まれる水分を除去することができる。そして、ハニカム成形体10の中心部101の温度がバインダの硬化開始温度に達するまでの時間を短縮することができる。つまり、第1ステップS1の時間を短縮することができる。   That is, the honeycomb formed body 10 immediately after the forming process still contains a lot of moisture and is in a state of being easily deformed. In this example, the microwave output of the first step S1, which is the first step among the plurality of steps of the drying process, is made highest. Therefore, the temperature of the honeycomb formed body 10 can be raised early, and moisture contained in the honeycomb formed body 10 can be removed at the earliest possible stage of the drying process. And time until the temperature of the center part 101 of the honeycomb molded object 10 reaches the hardening start temperature of a binder can be shortened. That is, the time of the first step S1 can be shortened.

これにより、乾燥工程全体の時間を一定とした場合、乾燥工程全体に占める第1ステップS1の時間を短縮することができる。そして、乾燥工程におけるハニカム成形体10は、水分が多く含まれた変形しやすい状態を短縮することができる。それ故に、乾燥時におけるセル壁11の変形を抑制することができ、外周壁13の割れ、しわ等の不具合が発生することを防止することができる。   Thereby, when the time of the whole drying process is made constant, the time of 1st step S1 which occupies for the whole drying process can be shortened. In addition, the honeycomb formed body 10 in the drying process can shorten the state of being easily deformed and containing a large amount of moisture. Therefore, deformation of the cell wall 11 at the time of drying can be suppressed, and occurrence of problems such as cracking and wrinkling of the outer peripheral wall 13 can be prevented.

また、本例の第1ステップS1では、ハニカム成形体10の単位質量当たりのマイクロ波出力を20W/gにしている。そのため、ハニカム成形体10に多くの水分が含まれている状態を確実に短縮することができ、ハニカム成形体10の乾燥時における変形をさらに抑制することができる。   In the first step S1 of this example, the microwave output per unit mass of the honeycomb formed body 10 is set to 20 W / g. Therefore, the state in which the honeycomb formed body 10 contains a large amount of moisture can be reliably shortened, and deformation of the honeycomb formed body 10 during drying can be further suppressed.

また、第1ステップS1では、ハニカム成形体10の中心部101の温度がバインダの硬化開始温度に達した時点(バインダ硬化開始点T1)において、中心部101と外周壁13との温度差が5℃以下となるように、マイクロ波出力を設定している。そのため、中心部101と外周壁13との乾燥収縮差によって生じる応力を低減し、ハニカム成形体10の乾燥時における変形をさらに抑制することができる。   Further, in the first step S1, when the temperature of the central portion 101 of the honeycomb molded body 10 reaches the binder curing start temperature (binder curing start point T1), the temperature difference between the central portion 101 and the outer peripheral wall 13 is 5. The microwave output is set so as to be below ℃. Therefore, the stress produced by the drying shrinkage difference between the central portion 101 and the outer peripheral wall 13 can be reduced, and deformation of the honeycomb formed body 10 during drying can be further suppressed.

また、乾燥工程では、ステップ毎にマイクロ波出力を段階的に小さくしている。そのため、乾燥工程におけるハニカム成形体10への熱衝撃を小さくすることができ、割れ等の発生を防止することができる。また、ハニカム成形体10の過乾燥を防止することもできる。
また、乾燥工程では、それぞれのステップ間のマイクロ波出力を一定としている。そのため、マイクロ波出力を制御しやすく、乾燥工程を円滑に進めることができる。
In the drying process, the microwave output is reduced step by step for each step. Therefore, the thermal shock to the honeycomb formed body 10 in the drying process can be reduced, and the occurrence of cracks and the like can be prevented. Moreover, overdrying of the honeycomb formed body 10 can also be prevented.
In the drying process, the microwave output between each step is constant. Therefore, it is easy to control the microwave output, and the drying process can proceed smoothly.

また、乾燥工程後におけるハニカム成形体10のセル壁11の厚みが70μm以下である場合に、乾燥時におけるセル壁11の変形を抑制するという効果をより有効に発揮することができる。   Moreover, when the thickness of the cell wall 11 of the honeycomb formed body 10 after the drying step is 70 μm or less, the effect of suppressing the deformation of the cell wall 11 at the time of drying can be more effectively exhibited.

このように、本例のハニカム構造体の製造方法によれば、押出成形したハニカム成形体の乾燥時における変形を抑制し、外周壁の割れ、しわ等の不具合を防止することができる。   As described above, according to the method for manufacturing a honeycomb structure of the present example, deformation of the extruded honeycomb formed body during drying can be suppressed, and problems such as cracks and wrinkles on the outer peripheral wall can be prevented.

実施例における、ハニカム構造体(ハニカム成形体)を示す説明図。An explanatory view showing a honeycomb structure (honeycomb fabrication object) in an example. 実施例における、乾燥装置の構成を示す説明図。Explanatory drawing which shows the structure of the drying apparatus in an Example. 実施例における、マイクロ波出力パターンを示した説明図。Explanatory drawing which showed the microwave output pattern in an Example. 比較例における、マイクロ波出力パターンを示した説明図。Explanatory drawing which showed the microwave output pattern in a comparative example. 実施例及び比較例における、ファイバー温度計の取り付け場所を示した説明図。Explanatory drawing which showed the attachment place of the fiber thermometer in an Example and a comparative example.

符号の説明Explanation of symbols

1 ハニカム構造体
10 ハニカム成形体
101 中心部
11 セル壁
12 セル
13 外周壁
2 乾燥装置
21 乾燥槽
22 搬送コンベア
23 マイクロ波発生装置
DESCRIPTION OF SYMBOLS 1 Honeycomb structure 10 Honeycomb molded object 101 Center part 11 Cell wall 12 Cell 13 Perimeter wall 2 Drying device 21 Drying tank 22 Conveyor 23 Microwave generator

Claims (11)

ハニカム状のセル壁に囲まれた多数のセルと外周側面を覆う筒状の外周壁とを有するコーディエライトセラミック製のハニカム構造体を製造する方法において、
少なくともコーディエライト原料、水、及びバインダを含有するセラミック材料を押出成形して所定長さに切断し、ハニカム成形体を成形する成形工程と、
マイクロ波を照射することにより上記ハニカム成形体を乾燥する乾燥工程と、
上記ハニカム成形体を焼成して上記ハニカム構造体を得る焼成工程とを有し、
上記乾燥工程では、該乾燥工程を複数のステップに分け、乾燥開始から上記ハニカム成形体の中心部の温度が少なくとも上記バインダの硬化開始温度に達するまでを第1ステップとし、該第1ステップにおいて上記ハニカム成形体に照射するマイクロ波出力を、その後のステップのマイクロ波出力よりも高く設定することを特徴とするハニカム構造体の製造方法。
In a method of manufacturing a honeycomb structure made of cordierite ceramic having a large number of cells surrounded by a honeycomb-shaped cell wall and a cylindrical outer peripheral wall covering the outer peripheral side surface,
A molding step of forming a honeycomb formed body by extruding a ceramic material containing at least a cordierite raw material, water, and a binder and cutting it to a predetermined length;
A drying step of drying the honeycomb formed body by irradiation with microwaves;
A firing step of firing the honeycomb formed body to obtain the honeycomb structure,
In the drying step, the drying step is divided into a plurality of steps, and the first step is from the start of drying until the temperature of the central portion of the honeycomb formed body reaches at least the curing start temperature of the binder. A method for manufacturing a honeycomb structured body, characterized in that a microwave output applied to the honeycomb formed body is set higher than a microwave output in a subsequent step.
請求項1において、上記第1ステップでは、上記ハニカム成形体の上記中心部の温度が上記バインダの硬化開始温度に達した時点において、上記中心部と上記外周壁との温度差が5℃以下となるように、上記マイクロ波出力を設定することを特徴とするハニカム構造体の製造方法。   In Claim 1, in the said 1st step, when the temperature of the said center part of the said honeycomb molded object reaches the hardening start temperature of the said binder, the temperature difference of the said center part and the said outer peripheral wall is 5 degrees C or less. Thus, the manufacturing method of the honeycomb structure characterized by setting the said microwave output. 請求項1又は2において、上記第1ステップでは、上記ハニカム成形体の単位質量当たりの上記マイクロ波出力を20W/gとすることを特徴とするハニカム構造体の製造方法。   3. The method for manufacturing a honeycomb structure according to claim 1, wherein in the first step, the microwave output per unit mass of the honeycomb formed body is set to 20 W / g. 請求項1〜3のいずれか1項において、上記乾燥工程では、上記ステップ毎に上記マイクロ波出力を段階的に小さくすることを特徴とするハニカム構造体の製造方法。   The method for manufacturing a honeycomb structure according to any one of claims 1 to 3, wherein in the drying step, the microwave output is reduced stepwise for each step. 請求項1〜4のいずれか1項において、上記乾燥工程では、上記ハニカム成形体の上記中心部と上記外周壁との温度差が5℃以下となるように、上記各ステップの上記マイクロ波出力を設定することを特徴とするハニカム構造体の製造方法。   5. The microwave output according to claim 1, wherein, in the drying step, the microwave output of each step is set so that a temperature difference between the central portion of the honeycomb formed body and the outer peripheral wall is 5 ° C. or less. A method for manufacturing a honeycomb structure, characterized in that 請求項1〜5のいずれか1項において、上記乾燥工程後における上記ハニカム成形体の上記セル壁の厚みが70μm以下であることを特徴とするハニカム構造体の製造方法。   The method for manufacturing a honeycomb structure according to any one of claims 1 to 5, wherein a thickness of the cell wall of the honeycomb formed body after the drying step is 70 µm or less. ハニカム状のセル壁に囲まれた多数のセルと外周側面を覆う筒状の外周壁とを有するコーディエライトセラミック製のハニカム構造体を製造するに当たって、少なくともコーディエライト原料、水、及びバインダを含有するセラミック材料を押出成形し、所定長さに切断したハニカム成形体を乾燥する乾燥装置において、
該乾燥装置は、上記ハニカム成形体を収納する乾燥槽と、該乾燥槽内において上記ハニカム成形体を連続的に搬送する搬送コンベアと、上記乾燥槽内において上記ハニカム成形体の搬送方向に複数配設されたマイクロ波を照射するマイクロ波発生装置とを有し、
上記乾燥槽は、複数のゾーンに分割され、上記ハニカム成形体が最初に搬送される第1ゾーンの上記マイクロ波発生装置は、上記ハニカム成形体が上記第1ゾーンを通過する間に、上記ハニカム成形体の中心部の温度が少なくとも上記バインダの硬化開始温度に達するようにマイクロ波出力が設定されるよう構成されており、かつ、該マイクロ波出力は、その他のゾーンよりも高いことを特徴とする乾燥装置。
In manufacturing a cordierite ceramic honeycomb structure having a large number of cells surrounded by a honeycomb-shaped cell wall and a cylindrical outer peripheral wall covering the outer peripheral side surface, at least a cordierite raw material, water, and a binder are used. In a drying apparatus for extruding a ceramic material containing and drying a honeycomb formed body cut into a predetermined length,
The drying apparatus includes a drying tank that accommodates the honeycomb formed body, a transport conveyor that continuously transports the honeycomb formed body in the drying tank, and a plurality of the drying apparatuses arranged in the transport direction of the honeycomb formed body in the drying tank. A microwave generator for irradiating the installed microwave,
The drying tank is divided into a plurality of zones, and the microwave generator in the first zone to which the honeycomb formed body is first conveyed is the honeycomb generator while the honeycomb formed body passes through the first zone. The microwave output is configured so that the temperature of the central portion of the molded body reaches at least the curing start temperature of the binder, and the microwave output is higher than other zones. Drying equipment to do.
請求項7において、上記第1ゾーンの上記マイクロ波発生装置は、上記ハニカム成形体の上記中心部の温度が上記バインダの硬化開始温度に達した時点において、上記中心部と上記外周壁との温度差が5℃以下となるように、上記マイクロ波出力が設定されるよう構成されていることを特徴とする乾燥装置。   8. The microwave generator according to claim 7, wherein the temperature of the central portion and the outer peripheral wall is reached when the temperature of the central portion of the honeycomb formed body reaches the curing start temperature of the binder. The drying apparatus, wherein the microwave output is set so that the difference is 5 ° C. or less. 請求項7又は8において、上記第1ゾーンの上記マイクロ波発生装置は、上記ハニカム成形体の単位質量当たりの上記マイクロ波出力が20W/gに設定されるよう構成されていることを特徴とする乾燥装置。   In Claim 7 or 8, the said microwave generator of the said 1st zone is comprised so that the said microwave output per unit mass of the said honeycomb molded object may be set to 20 W / g. Drying equipment. 請求項7〜9のいずれか1項において、上記乾燥槽の上記マイクロ波発生装置は、上記ゾーン毎に上記マイクロ波出力が段階的に小さく設定されるよう構成されていることを特徴とする乾燥装置。   The drying apparatus according to any one of claims 7 to 9, wherein the microwave generator of the drying tank is configured so that the microwave output is set to be small step by step for each of the zones. apparatus. 請求項7〜10のいずれか1項において、上記乾燥槽の上記マイクロ波発生装置は、上記ハニカム成形体の上記中心部と上記外周壁との温度差が5℃以下となるように、上記各ゾーンの上記マイクロ波出力が設定されるよう構成されていることを特徴とする乾燥装置。   In any one of Claims 7-10, the said microwave generator of the said drying tank WHEREIN: Said each so that the temperature difference of the said center part of the said honeycomb molded object and the said outer peripheral wall may be 5 degrees C or less. A drying apparatus configured to set the microwave output of the zone.
JP2006295126A 2006-10-31 2006-10-31 Manufacturing method of honeycomb structure and drying device used therein Pending JP2008110537A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012086558A (en) * 2010-09-21 2012-05-10 Sumitomo Chemical Co Ltd Device and method for drying green honeycomb molding, and method for manufacturing ceramic honeycomb structure
JP2013057414A (en) * 2011-09-07 2013-03-28 Ngk Insulators Ltd Drying furnace for ceramic
US11999075B2 (en) 2019-08-14 2024-06-04 Corning Incorporated Systems and methods for reducing surface oil streaks on wet extrudate by irradiation

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Publication number Priority date Publication date Assignee Title
US8020314B2 (en) * 2008-10-31 2011-09-20 Corning Incorporated Methods and apparatus for drying ceramic green bodies with microwaves
EP4193104B1 (en) * 2020-08-05 2024-06-19 System Ceramics S.p.A. Dryer for ceramic products

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012086558A (en) * 2010-09-21 2012-05-10 Sumitomo Chemical Co Ltd Device and method for drying green honeycomb molding, and method for manufacturing ceramic honeycomb structure
JP2013057414A (en) * 2011-09-07 2013-03-28 Ngk Insulators Ltd Drying furnace for ceramic
US11999075B2 (en) 2019-08-14 2024-06-04 Corning Incorporated Systems and methods for reducing surface oil streaks on wet extrudate by irradiation

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