JPH0710526B2 - How to dry a green compact - Google Patents

How to dry a green compact

Info

Publication number
JPH0710526B2
JPH0710526B2 JP3350612A JP35061291A JPH0710526B2 JP H0710526 B2 JPH0710526 B2 JP H0710526B2 JP 3350612 A JP3350612 A JP 3350612A JP 35061291 A JP35061291 A JP 35061291A JP H0710526 B2 JPH0710526 B2 JP H0710526B2
Authority
JP
Japan
Prior art keywords
molded body
drying
atmosphere
temperature
water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP3350612A
Other languages
Japanese (ja)
Other versions
JPH05169420A (en
Inventor
健一 辻
洋市 山下
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Riken Corp
Original Assignee
Riken Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Riken Corp filed Critical Riken Corp
Priority to JP3350612A priority Critical patent/JPH0710526B2/en
Publication of JPH05169420A publication Critical patent/JPH05169420A/en
Publication of JPH0710526B2 publication Critical patent/JPH0710526B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Compositions Of Oxide Ceramics (AREA)
  • Devices For Post-Treatments, Processing, Supply, Discharge, And Other Processes (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、生の成形体の乾燥方法
に関し、更に詳述すれば、微粉末と水と有機バインダ
(例えばヒドロキシプロピルメチルセルロース(HPM
C)の高重合品と水とからなる)とを混練してなる混練
物によって成形された生の成形体の乾燥方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for drying a green molded body, and more specifically, fine powder, water and an organic binder (for example, hydroxypropylmethylcellulose (HPM).
The present invention relates to a method for drying a raw molded body formed by kneading a highly polymerized product of C) and water).

【0002】[0002]

【従来技術】二珪化モリブデン系のセラミックス発熱体
を製造するのに、粒子径1μm 未満の微細なセラミック
ス粉末に、HPMCの高重合体をバインダとし、適量の
水を加えて混練することにより、形状保持性を有する程
度の混練物とし、この混練物から押出し成形によって棒
状成形体とする方法が採られている。
2. Description of the Related Art In manufacturing a molybdenum disilicide-based ceramic heating element, a fine ceramic powder having a particle size of less than 1 μm is used as a binder of a high polymer of HPMC, and an appropriate amount of water is added and kneaded to form a shape. A method is adopted in which a kneaded product having a holding property is prepared, and the kneaded product is extruded into a rod-shaped molded product.

【0003】成形体の径が5mm以上になると、断面での
水分分布が不均一になり、一般に、中心部が表層部より
も水分量が多くなる傾向がある。この傾向は成形体の径
が10mm以上になると特に顕著になり、更に、一般に表層
部の方が中心部よりもグリーン密度が高くなる。このよ
うな生の成形体にあっては、自然乾燥では中心部の水分
を確実に除去することが極めて困難である。水分の除去
が不完全であると、後の脱バインダ工程で割れ等の欠陥
が発生するようになる。
When the diameter of the molded product is 5 mm or more, the water distribution in the cross section becomes non-uniform, and generally, the water content in the central portion tends to be larger than that in the surface layer portion. This tendency becomes particularly remarkable when the diameter of the molded product is 10 mm or more, and further, the green density is generally higher in the surface layer portion than in the central portion. In such a green molded body, it is extremely difficult to surely remove the water in the central portion by natural drying. If the removal of water is incomplete, defects such as cracks will occur in the subsequent binder removal step.

【0004】乾燥を確実にするため、成形直後の生の成
形体を80℃以上の熱風によって乾燥しようとすると、表
層部と中心部とで均一な乾燥速度にはならず、更に、バ
インダのHPMCの粘度変化温度に達して急激なゲル化
による急激な収縮が起こり、これが亀裂発生の原因にな
る。
[0004] In order to ensure the drying, if a fresh green body immediately after molding is dried with hot air of 80 ° C or more, a uniform drying speed is not obtained between the surface layer portion and the center portion, and further, HPMC of the binder is not used. When it reaches the temperature at which the viscosity changes, a rapid gelation causes a rapid shrinkage, which causes cracking.

【0005】簡便な乾燥方法としては、次のような方法
がある。生の成形体をビニールシートで覆って2〜3日
間放置して成形体内の水分を略一様にしてからビニール
シートを取外し、大気中に2〜3日間放置して予備乾燥
する。次に表層部が完全には乾燥せずに中心部の水分の
抜け道が残されている状態にて熱風乾燥を行う。然し、
この方法では、乾燥に長時間を要する上に、季節や大気
の状態によって予備乾燥の進行が左右され、完全に水分
を除去した良好な成形体を安定して得るのが難しい。
As a simple drying method, there are the following methods. The green molded body is covered with a vinyl sheet and left for 2 to 3 days to make the water content in the molded body substantially uniform, and then the vinyl sheet is removed and left to stand in the atmosphere for 2 to 3 days for preliminary drying. Next, hot air drying is performed in a state where the surface layer portion is not completely dried and a moisture escape passage in the central portion is left. However,
According to this method, it takes a long time to dry, and the progress of preliminary drying depends on the season and atmospheric conditions, and it is difficult to stably obtain a good molded product from which water is completely removed.

【0006】[0006]

【発明の目的】本発明は、上記の事情に鑑みてなされた
ものであって、生の成形体を短時間で確実に乾燥でき、
欠陥のない健全な乾燥成形体が得られる、生の成形体の
乾燥方法を提供することを目的としている。
SUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances, and is capable of reliably drying a green compact in a short time,
It is an object of the present invention to provide a method for drying a green molded body, which can obtain a sound dry molded body without defects.

【0007】[0007]

【発明の構成】第一の発明は、微粉末と水と有機バイン
ダとを混練してなる混練物によって成形された生の成形
体を乾燥するに際し、成形直後の生の成形体を、雰囲気
を高相対湿度(例えば80〜90%)に保持して表層部と中
心部との水分の差が実質的になくなるように室温から徐
々に昇温させる(例えば40〜50℃に昇温)第一の工程
と、前記成形体を一定温度(例えば40〜50℃)に保持し
た状態で雰囲気の相対湿度を徐々に低下(例えば50〜60
%に低下)させ、この状態に、前記成形体中の水分と雰
囲気中の水分とが略平衡するに至る迄保持する第二の工
程と、雰囲気の相対湿度を更に低下(例えば約10%に低
下)させると共に前記成形体を昇温(例えば60〜80℃に
昇温)させ、この状態に、前記成形体中の水分と雰囲気
中の水分とが略平衡するに至る迄保持する第三の工程と
を有する、生の成形体の乾燥方法に係る。
According to a first aspect of the present invention, when drying a raw molded body formed by a kneaded product obtained by kneading fine powder, water and an organic binder, the raw molded body immediately after molding is subjected to an atmosphere. Maintaining high relative humidity (eg 80 to 90%) and gradually raising the temperature from room temperature (eg raising temperature to 40 to 50 ° C) so that the difference in water content between the surface layer and the center is substantially eliminated. And the relative humidity of the atmosphere is gradually reduced (for example, 50 to 60 ° C) while maintaining the molded body at a constant temperature (for example, 40 to 50 ° C).
%), And in this state, the second step of holding until the moisture in the molded body and the moisture in the atmosphere are substantially equilibrated, and the relative humidity of the atmosphere is further reduced (for example, to about 10%). The temperature of the molded body is lowered and the temperature of the molded body is raised (for example, to 60 to 80 ° C.), and this state is maintained until the moisture in the molded body and the moisture in the atmosphere are substantially equilibrated. And a method for drying a green molded body, the method including:

【0008】第二の発明は、微粉末と水と有機バインダ
とを混練してなる混練物によって成形された生の成形体
を乾燥するに際し、雰囲気の湿度を相対湿度80〜90%か
ら約10%に徐々に低下させると共に、成形直後の生の成
形体を前記雰囲気中で室温から60〜80℃に徐々に昇温さ
せる工程を有する、生の成形体の乾燥方法に係る。
The second aspect of the present invention is to dry a green compact formed of a kneaded material obtained by kneading fine powder, water and an organic binder, and the humidity of the atmosphere is from 80 to 90% relative humidity to about 10 %. %, And a step of gradually raising the temperature of the green molded body immediately after molding from room temperature to 60 to 80 ° C. in the atmosphere, and relates to a method for drying a green molded body.

【0009】[0009]

【実施例】以下、本発明の実施例を説明する。先ず、第
一の発明の実施例について説明する。二珪化モリブデン
(MoSi2)粉末と硼化モリブデン(α−MoB )粉末(い
ずれも粒径1μm 未満)との混合粉(混合比は85:15)
にHPMC系水溶性高分子をバインダとして1〜10重量
%(この例では6.5 重量%)を添加し、更に水を5〜15
重量%(この例では13重量%)添加して混練した。この
混練物を押出機(スクリュー式のエキストルーダ)を用
いて約15mm径の棒状のグリーン(生の)成形体とした。
EXAMPLES Examples of the present invention will be described below. First, an embodiment of the first invention will be described. Mixed powder of molybdenum disilicide (MoSi 2 ) powder and molybdenum boride (α-MoB) powder (both particle size less than 1 μm) (mixing ratio is 85:15)
1 to 10% by weight (6.5% by weight in this example) as a binder of HPMC water-soluble polymer, and 5 to 15% of water.
% (13% by weight in this example) was added and kneaded. This kneaded product was made into a rod-shaped green (raw) molded body having a diameter of about 15 mm by using an extruder (screw type extruder).

【0010】成形直後の成形体は表層が皮膜水で覆われ
ており、この皮膜は大気に触れると急激に乾燥を開始し
て表層部と内部とで水分差が大きくなり、不均一な収縮
が起る。そこで、成形直径のグリーン成形体を、相対湿
度90%に保持した乾燥室に入れ、10時間かけて乾燥室内
を室温から40℃に昇温させた。この間に、成形体表層部
の急激な乾燥を抑えると共に、表層部と中心部との水分
量の差(水分勾配)を無視し得る程度に小さくした。更
にこのステップでは、押出し成形によって発生した内部
応力が緩和される。以下、このステップを予備乾燥ステ
ップと呼ぶ。
Immediately after the molding, the surface layer of the molded body is covered with the film water, and when the film is exposed to the atmosphere, it starts to dry rapidly and the difference in water content between the surface layer and the inside becomes large, resulting in uneven shrinkage. It happens. Therefore, the green compact having the molding diameter was placed in a drying chamber kept at a relative humidity of 90%, and the temperature inside the drying chamber was raised from room temperature to 40 ° C. over 10 hours. During this period, rapid drying of the surface layer portion of the molded body was suppressed, and the difference in water content between the surface layer portion and the central portion (water content gradient) was made small enough to be ignored. Further, in this step, the internal stress generated by the extrusion molding is relaxed. Hereinafter, this step is referred to as a preliminary drying step.

【0011】次に、乾燥室内の温度を40℃に保持した儘
乾燥室内の相対温度を上記90%から60%に低下させ、成
形体の水分と雰囲気中の水分とが略平衡状態に達する迄
30〜40時間(この例では40時間)一定温度、一定湿度に
維持した。以下、このステップを恒率乾燥ステップと呼
ぶ。
Next, the relative temperature in the drying chamber kept at 40 ° C. is lowered from 90% to 60% until the moisture of the molded body and the moisture in the atmosphere reach a substantially equilibrium state.
The temperature and humidity were maintained constant for 30 to 40 hours (40 hours in this example). Hereinafter, this step is referred to as a constant rate drying step.

【0012】次に、乾燥室内の温度を徐々に80℃迄上昇
させながら雰囲気の相対湿度を上記60%から10%に低下
させた。この間の所要時間は10〜20時間(この例では20
時間) である。以下、このステップを強制乾燥ステップ
と呼ぶ。
Next, the relative humidity of the atmosphere was lowered from 60% to 10% while gradually raising the temperature in the drying chamber to 80 ° C. It takes 10 to 20 hours (20 in this example).
Time). Hereinafter, this step is called a forced drying step.

【0013】以上の、経過時間による雰囲気の湿度及び
湿度の変化は、図1に示す通りである。
The above-mentioned changes in the humidity and humidity of the atmosphere over time are as shown in FIG.

【0014】かくして得られた乾燥済みの成形体は、予
備乾燥ステップで成形体内の水分勾配が殆ど無くなり、
次の恒率乾燥ステップでこの状態を維持しながら乾燥が
進行し、最後の強制乾燥ステップで殆どの水分が除去さ
れて乾燥が完了する。この乾燥に要する全時間は50〜70
時間で、長時間を要さない。
The dried molded body thus obtained has almost no water gradient in the molded body in the preliminary drying step.
Drying proceeds while maintaining this state in the next constant rate drying step, and most of the water is removed in the final forced drying step to complete the drying. The total time required for this drying is 50-70
It doesn't take a long time.

【0015】この乾燥済みの成形体は、脱バインダ処理
を施されてから焼結され、棒状焼結体となる。この棒状
焼結体は、径が約12mmになっていて、乾燥と焼結とによ
って20%寸法収縮し、欠陥のない良好な焼結体であっ
た。なお、強制乾燥ステップを終了した成形体は、次の
脱バインダ処理迄強制乾燥ステップの状態を維持してお
くのが望ましい。
The dried molded body is subjected to binder removal processing and then sintered to form a rod-shaped sintered body. This rod-shaped sintered body had a diameter of about 12 mm, was 20% in size shrinkage due to drying and sintering, and was a good sintered body without defects. In addition, it is desirable that the molded body that has completed the forced drying step be kept in the state of the forced drying step until the next binder removal processing.

【0016】次に第二の発明の実施例について説明す
る。雰囲気は、乾燥開始から乾燥終了迄の全過程に亘っ
て、相対湿度を徐々に低下させながら湿度を徐々に上昇
させるようにしても良い。
Next, an embodiment of the second invention will be described. The atmosphere may be such that the relative humidity is gradually decreased and the humidity is gradually increased throughout the entire process from the start of drying to the end of drying.

【0017】この例での生の成形体は、前記の例におけ
ると同じ条件で作製されたものである。この成形体を、
相対湿度90%の乾燥室に装入し、装入直後から乾燥室内
を徐々に約10%の相対湿度に低下させると共に、雰囲気
温度を室温から60℃に徐々に上昇させた。乾燥開始から
乾燥終了に至る全所要時間は50〜70時間(この例では前
記の例におけると同じ70時間)である。
The green compact in this example was made under the same conditions as in the previous example. This molded body,
Immediately after charging, the drying chamber with a relative humidity of 90% is gradually reduced to a relative humidity of about 10%, and the atmosphere
The temperature was raised slowly to 60 ° C. from room temperature. Drying starting total duration leading to completion of drying from 50 to 70 hours (the same 70 hours as in the examples in this example).

【0018】経過時間と雰囲気の相対湿度及び温度との
関係は、図2に示す通りである。この例では、経過時間
による相対湿度及び温度の変化は、いずれも略直線的で
ある
The relationship between relative humidity and temperature of the elapsed time and the atmosphere is as shown in FIG. In this example, changes in relative humidity and temperature over time are substantially linear.

【0019】乾燥後の成形体の状態は、前記の例におけ
ると同様であって、健全なものであった。
The state of the molded body after drying was the same as in the above example and was sound.

【0020】以上、本発明の実施例を説明したが、成形
体の形状や成形方法は他の形状、成形方法による場合で
も本発明が適用可能である。また、成形体を構成する粉
末材料やバインダも上記に限られるものではない。即
ち、本発明は、可成りの水分を含存する生の成形体の乾
燥に適用可能である。
Although the embodiments of the present invention have been described above, the present invention can be applied even when the shape of the molded body and the molding method are other shapes and molding methods. Further, the powder material and the binder forming the molded body are not limited to the above. That is, the present invention is applicable to the drying of green compacts containing a considerable amount of water.

【0021】[0021]

【発明の効果】第一の発明は、成形直後の生の成形体
を、雰囲気を高相対湿度に保持して徐々に昇温させる第
一の工程と、この湿度を一定に保持した儘雰囲気の相対
湿度を徐々に低下させる第二の工程と、雰囲気湿度を更
に低下させると共に前記成形体を加熱し保持する第三の
工程とからなっているので、第一の工程で成形体内部の
水分が略均一になり、第二の工程で水分均一の状態にて
乾燥が進行し、第三の工程にて乾燥が完了する。
According to the first aspect of the present invention, the first step of gradually raising the temperature of a green compact immediately after molding by keeping the atmosphere at a high relative humidity, and the constant atmosphere of this humidity are used. Since the second step of gradually lowering the relative humidity and the third step of further lowering the atmospheric humidity and heating and holding the molded body, the moisture inside the molded body in the first step is It becomes substantially uniform, the drying progresses in a state where the water content is uniform in the second step, and the drying is completed in the third step.

【0022】このように、第一の工程で乾燥開始後の僅
かな時間で成形体内部の水分が略均一になり、この状態
を維持しながら乾燥が進行するので、水分の不均一に起
因する欠陥が発生することなく成形体が乾燥し、信頼性
が高い上に乾燥が効率的に進行して乾燥に長時間を要し
ない。
As described above, in the first step, the moisture inside the molded body becomes substantially uniform in a short time after the start of drying, and the drying proceeds while maintaining this state. The molded body is dried without causing defects, has high reliability, and the drying progresses efficiently, so that the drying does not take a long time.

【0023】第二の発明は、雰囲気の湿度を相対湿度80
〜90%から約10%に徐々に低下させると共に、成形直後
の生の成形体を前記雰囲気中で室温から60〜80℃に徐々
に昇温させるようにしているので、乾燥処理の前段で成
形体内部の水分が略均一になり、前記第一の発明による
効果と同様の効果が奏せられる。
The second aspect of the present invention is that the relative humidity is 80%.
Since it is gradually decreased from ~ 90% to about 10% and the temperature of the green compact immediately after molding is gradually raised from room temperature to 60-80 ° C in the atmosphere, The moisture inside the body becomes substantially uniform, and the same effects as the effects according to the first aspect of the invention can be obtained.

【図面の簡単な説明】[Brief description of drawings]

【図1】第一の発明の実施例の成形体乾燥における経過
時間による雰囲気の湿度及び温度の変化を示すグラフで
ある。
FIG. 1 is a graph showing changes in humidity and temperature of an atmosphere depending on elapsed time in drying a molded body according to an example of the first invention.

【図2】第二の発明の実施例の成形体乾燥における経過
時間による雰囲気の湿度及び温度の変化を示すグラフで
ある。
FIG. 2 is a graph showing changes in the humidity and temperature of the atmosphere depending on the elapsed time in drying the molded body of the example of the second invention.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 微粉末と水と有機バインダとを混練して
なる混練物によって成形された生の成形体を乾燥するに
際し、 成形直後の生の成形体を、雰囲気を高相対湿度に保持し
て表層部と中心部との水分の差が実質的になくなるよう
に室温から徐々に昇温させる第一の工程と、 前記成形体の温度を一定に保持した状態で雰囲気の相対
湿度を徐々に低下させ、この状態に、前記成形体中の水
分と雰囲気中の水分とが略平衡するに至る迄保持する第
二の工程と、 雰囲気の相対湿度を更に低下させると共に前記成形体を
昇温させ、この状態に、前記成形体中の水分と雰囲気中
の水分とが略平衡するに至る迄保持する第三の工程とを
有する、生の成形体の乾燥方法。
1. When drying a raw molded body formed by a kneaded product obtained by kneading fine powder, water and an organic binder, the raw molded body immediately after molding is kept at a high relative humidity atmosphere. The first step of gradually raising the temperature from room temperature so that the difference in water content between the surface layer portion and the central portion is substantially eliminated, and gradually changing the relative humidity of the atmosphere while keeping the temperature of the molded body constant. The second step of lowering the water content and keeping it in this state until the water content in the molded body and the water content in the atmosphere are approximately equilibrated, and further lowering the relative humidity of the atmosphere and raising the temperature of the molded body. In this state, a third step of holding until the water in the molded body and the water in the atmosphere are substantially equilibrated, the method for drying a green molded body.
【請求項2】 微粉末と水と有機バインダとを混練して
なる混練物によって成形された生の成形体を乾燥するに
際し、雰囲気の湿度を相対湿度80〜90%から約10%に徐
々に低下させると共に、成形直後の生の成形体を前記雰
囲気中で室温から60〜80℃に徐々に昇温させる工程を有
する、生の成形体の乾燥方法。
2. When drying a green compact formed by kneading a fine powder, water and an organic binder, the humidity of the atmosphere is gradually changed from 80 to 90% relative humidity to about 10% relative humidity. A method for drying a green molded body, which comprises a step of gradually lowering the temperature of the green molded body immediately after molding from room temperature to 60 to 80 ° C. in the atmosphere while the temperature is gradually lowered.
JP3350612A 1991-11-11 1991-11-11 How to dry a green compact Expired - Lifetime JPH0710526B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3350612A JPH0710526B2 (en) 1991-11-11 1991-11-11 How to dry a green compact

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Application Number Priority Date Filing Date Title
JP3350612A JPH0710526B2 (en) 1991-11-11 1991-11-11 How to dry a green compact

Publications (2)

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JPH05169420A JPH05169420A (en) 1993-07-09
JPH0710526B2 true JPH0710526B2 (en) 1995-02-08

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2813127B2 (en) * 1994-03-11 1998-10-22 日本碍子株式会社 Drying method of ceramic molded body
JP2015024645A (en) * 2013-06-21 2015-02-05 日本特殊陶業株式会社 Ceramic extruded body and manufacturing method thereof, and ceramic fired body and manufacturing method thereof

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2592727B2 (en) * 1991-06-07 1997-03-19 株式会社イナックス Green substrate drying equipment with continuous drying oven

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JPH05169420A (en) 1993-07-09

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