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JPH0627040B2 - Degreasing method for ceramic molded products - Google Patents
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JPH0627040B2 - Degreasing method for ceramic molded products - Google Patents

Degreasing method for ceramic molded products

Info

Publication number
JPH0627040B2
JPH0627040B2 JP63158819A JP15881988A JPH0627040B2 JP H0627040 B2 JPH0627040 B2 JP H0627040B2 JP 63158819 A JP63158819 A JP 63158819A JP 15881988 A JP15881988 A JP 15881988A JP H0627040 B2 JPH0627040 B2 JP H0627040B2
Authority
JP
Japan
Prior art keywords
furnace
ceramic molded
temperature
molded product
degreasing
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
JP63158819A
Other languages
Japanese (ja)
Other versions
JPH029770A (en
Inventor
利幸 松前
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.)
Panasonic Electric Works Co Ltd
Original Assignee
Matsushita Electric Works Ltd
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 Matsushita Electric Works Ltd filed Critical Matsushita Electric Works Ltd
Priority to JP63158819A priority Critical patent/JPH0627040B2/en
Publication of JPH029770A publication Critical patent/JPH029770A/en
Publication of JPH0627040B2 publication Critical patent/JPH0627040B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Investigating Or Analyzing Materials Using Thermal Means (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、セラミック成形品の脱脂法に関するものであ
る。
TECHNICAL FIELD The present invention relates to a degreasing method for ceramic molded articles.

[従来の技術] 一般に、セラミックスの製造工程では、セラミック粉末
に有機係合剤を添加して流動性を付与した状態で成形を
行なう。成形にはプレス成形、押出成形のほか各種成形
法が知られているが、中でも射出成形は複雑な形状のセ
ラミック成形品が得られる利点がある。しかしながら、
射出成形を行なうには、材料に高い流動性が必要である
から、有機結合剤の添加量も多くなり、成形後に不要に
なった有機結合剤を除去する脱脂という工程が必要にな
る。
[Prior Art] Generally, in the manufacturing process of ceramics, molding is performed in a state where fluidity is imparted by adding an organic engaging agent to the ceramic powder. Various molding methods are known in addition to press molding, extrusion molding, and injection molding has the advantage that a ceramic molded product having a complicated shape can be obtained. However,
In order to perform injection molding, the material needs to have high fluidity, and therefore the amount of the organic binder added increases, and a step of degreasing that removes the organic binder that is no longer needed after molding is required.

ところで、脱脂工程においては、加熱温度、炉内の雰囲
気を形成する気体の供給量、炉内の雰囲気を形成する気
体中の酸素量等の加熱条件の設定が重要であり、条件設
定が不適切であると、セラミック成形品が割れたり、表
層の剥離が生じたりする。
By the way, in the degreasing process, it is important to set the heating conditions such as the heating temperature, the supply amount of the gas that forms the atmosphere in the furnace, and the amount of oxygen in the gas that forms the atmosphere in the furnace. If so, the ceramic molded product may be cracked or the surface layer may be peeled off.

たとえば、セラミック成形製品を過度に加熱したり、急
激に温度を上昇させたりすると、有機結合剤が解して発
生する分解がすの単位時間当たりの発生量が過剰にな
り、セラミック成形品内部でのガス圧によりセラミック
成形品が割れたり、膨れたり、表層が剥離したりすると
いう問題が生じるのである。
For example, if the ceramic molded product is excessively heated or the temperature is rapidly raised, the amount of decomposition soot generated by the decomposition of the organic binder per unit time becomes excessive, and inside the ceramic molded product. The gas pressure causes a problem that the ceramic molded product is cracked, swelled, or the surface layer is peeled off.

こうした問題を解決するために、従来は、セラミック成
形品を加熱する炉内の温度を熱電対等の温度センサで検
出し、炉内の温度に対応して予め設定された昇温プログ
ラムに従って炉内の温度を制御していた。
In order to solve such a problem, conventionally, a temperature sensor such as a thermocouple is used to detect the temperature in the furnace for heating the ceramic molded product, and the temperature in the furnace is set in accordance with a preset heating program corresponding to the temperature in the furnace. The temperature was controlled.

しかしながら、セラミック成形品の中の有機結合剤の加
熱による分解ガスの発生量は、温度に一対一に対応する
ものではない。したがって、炉内の温度に基づいて炉内
の温度を制御しても、分解ガスの発生量が過剰になる場
合がある。
However, the amount of decomposition gas generated by heating the organic binder in the ceramic molded product does not correspond to the temperature one-to-one. Therefore, even if the temperature inside the furnace is controlled based on the temperature inside the furnace, the amount of decomposition gas generated may become excessive.

このような問題点を解決するために、炉内の温度に代え
てセラミック成形品の重量を検出し、重量変化に基づい
て炉内の温度を制御する方法が考えられている(特開昭
61−163172号公報参照)。
In order to solve such a problem, a method of detecting the weight of the ceramic molded product instead of the temperature in the furnace and controlling the temperature in the furnace based on the change in weight has been proposed (Japanese Patent Laid-Open No. 61-61). 163172).

[発明が解決しようとする課題] しかしながら、セラミック成形品の重量を検出して脱脂
状態を判定しようとすると、セラミック成形品の重量の
変化率を演算しなければならず、脱脂作業を行なうたび
にセラミック成形品の重量を測定することが必要にな
る。その結果、変化率演算のための制御系のプログラム
の負担が大きくなるとともに、脱脂工程の作業時間も長
くなるという問題が発生する。
[Problems to be Solved by the Invention] However, in order to determine the degreasing state by detecting the weight of the ceramic molded product, the rate of change of the weight of the ceramic molded product must be calculated, and the degreasing work is performed every time. It is necessary to measure the weight of the ceramic molded part. As a result, the load of the control system program for calculating the change rate increases, and the work time of the degreasing process also increases.

本発明は上記問題点を解決することを目的とするもので
あり、脱脂工程において、セラミック成形品の脱脂状態
の判定を簡素化したセラミック成形品の脱脂法を提供し
ようとするものである。
The present invention is intended to solve the above problems, and an object of the present invention is to provide a degreasing method for a ceramic molded product in which the determination of the degreased state of the ceramic molded product is simplified in the degreasing step.

[課題を解決するための手段] 本発明では、上記目的を達成するために、脱脂工程にお
いて、炉内に有機結合剤が再分解する温度以下の温度に
保たれたモニタ部材を配設し、モニタ部材の状態変化に
基づいて炉内の加熱条件を制御するのである。
[Means for Solving the Problems] In the present invention, in order to achieve the above object, in the degreasing step, a monitor member, which is kept at a temperature equal to or lower than the temperature at which the organic binder is redissolved, is disposed in the furnace. The heating condition in the furnace is controlled based on the change in the state of the monitor member.

[作用] 上記構成によれば、セラミック成形品の状態を直接検出
せずに、炉内に配設したモニタ部材の状態変化に基づい
てセラミック成形品の脱脂状態を間接的に判定するか
ら、脱脂すべき個々のセラミック成形品の形状や重量等
とは無関係に炉内の加熱条件が設定できるのであり、条
件設定が容易になるのである。
[Operation] According to the above configuration, the degreasing state of the ceramic molded product is indirectly determined based on the state change of the monitor member arranged in the furnace without directly detecting the state of the ceramic molded product. The heating conditions in the furnace can be set regardless of the shape, weight, etc. of each individual ceramic molded product, and the condition setting becomes easy.

[実施例] セラミック成形品の脱脂を行なう炉1は、第1図に示す
ように、炉1の中の温度条件を設定するヒータ2を備え
ている。炉1の中へは、バルブ3を介して空気が供給さ
れ、また、バルブ4を介して窒素等の不活性ガスが供給
される。これらのバルブ3,4は開度が連続的に調節で
きるようになっている。炉1の中の雰囲気を形成する気
体は、排出路5を通して外部に放出され、排出路5には
安全弁6が設けられる。さらに、排出路5には、酸素濃
度検出器8が配設される。酸素濃度検出器8(8aはセン
サ部、8bは本体部)の出力は、管理用コンピュータ9に
入力され、炉1から排出された酸素の濃度に基づいてヒ
ータ2の設定温度とバルブ3,4の開度とが調節され
る。ヒータ2は、管理用コンピュータ9にインタフェー
を介して接続されたサイリスタ10により制御され、こ
れにより、炉1の中の加熱昇温条件が設定される。ま
た、各バルブ3,4はそれぞれ管理用コンピュータ9に
インタフェースを介し接続されたステップモータ等の開
度調節器11,12により駆動され、炉1の中への空気
供給量と不活性ガス供給量とが調節される。
[Example] A furnace 1 for degreasing a ceramic molded product is equipped with a heater 2 for setting temperature conditions in the furnace 1, as shown in FIG. Air is supplied into the furnace 1 through the valve 3, and an inert gas such as nitrogen is supplied through the valve 4. The openings of these valves 3 and 4 can be continuously adjusted. The gas forming the atmosphere in the furnace 1 is discharged to the outside through the discharge passage 5, and the discharge passage 5 is provided with a safety valve 6. Further, an oxygen concentration detector 8 is arranged in the discharge path 5. The output of the oxygen concentration detector 8 (8a is a sensor portion, 8b is a main body portion) is input to the management computer 9, and based on the concentration of oxygen discharged from the furnace 1, the set temperature of the heater 2 and the valves 3, 4 are set. And the opening degree of are adjusted. The heater 2 is controlled by a thyristor 10 connected to the management computer 9 via an interface, whereby the heating and heating conditions in the furnace 1 are set. Further, the valves 3 and 4 are driven by opening degree adjusters 11 and 12 such as step motors which are connected to the management computer 9 via an interface, respectively, and the air supply amount and the inert gas supply amount into the furnace 1 are controlled. And are adjusted.

ところで、管理用コンピュータ9は、炉1の中に配設し
たモニタ部材の状態も制御用のデータとして利用するよ
うにしている。すなわち、第2図に示すように、炉1の
中にもモニタ部材として反射鏡25を配設し、炉1の外
に設けたHe−Neレーザ等の光源26からの光を窓27を
通して反射鏡25に照射し、反射鏡25での反射光を窓
28を通して炉1の外の受光器29で観測するようにし
ているのである。反射鏡25は水冷ジャケットに包まれ
て50℃に冷却されている。この温度は、反射鏡25に
付着する分解ガスの凝集物再分解する温度以下に設定さ
れている。受光器29は管理用コンピュータ9に接続さ
れており、管理用コンピュータ9では、受光器29での
受光量に応じてセラミック成形品20の脱脂状態を判定
し、空気供給量、不活性ガス供給量、温度を制御するの
である。
By the way, the management computer 9 also uses the state of the monitor member disposed in the furnace 1 as control data. That is, as shown in FIG. 2, a reflecting mirror 25 is provided as a monitor member in the furnace 1, and light from a light source 26 such as a He-Ne laser provided outside the furnace 1 is reflected through a window 27. The mirror 25 is irradiated and the light reflected by the reflecting mirror 25 is observed through the window 28 by the light receiver 29 outside the furnace 1. The reflecting mirror 25 is wrapped in a water cooling jacket and cooled to 50 ° C. This temperature is set to be equal to or lower than the temperature at which the aggregate of the decomposition gas adhering to the reflecting mirror 25 is decomposed again. The light receiver 29 is connected to the management computer 9, and the management computer 9 determines the degreased state of the ceramic molded article 20 according to the amount of light received by the light receiver 29, and supplies the air supply amount and the inert gas supply amount. , Control the temperature.

制御は以下のように行なわれる。第3図に示すように、
まず、脱脂開始直後には、空気のみが供給され(太破
線)、炉1の中の温度は上昇する。このとき、反射鏡2
5の反射率(二点鎖線)は大きく、光源26からの光の大
部分は受光器29に到達する。さらに温度が上昇して有
機結合剤が分解を始めると、反射鏡25の表面付近の分
解ガスは冷却されて反射鏡25に凝集付着することにな
るから、反射率が低下することになる。こうして反射率
が急激に低下しはじめると、管理用コンピュータ9で
は、炉1の中への空気供給量を減少させるようにバルブ
3の開度を調節し、不活性ガスの供給量(細破線)を増大
させるようにバルブ4の開度を調節する。さらに、サイ
リスタ10を介して炉1の中の温度上昇率を小さくする
ようにヒータ2を制御する。このとき、酸素濃度(一点
鎖線)は低下する。また、炉1の中に供給される気体の
総量は増加するように設定される。このような制御を行
なうと、炉1の中の気体の総量が増加することにより、
炉1の中の雰囲気の更新が迅速に行なわれセラミック成
形品の表層部の分解ガスが除去されてセラミック成形品
の内部からの分解ガスの抜け道が形成され、セラミック
成形品に膨れが生じるのを防止することができる。ま
た、雰囲気が迅速に更新されることにより、炉1の中の
温度が低下してセラミック成形品が冷却され、有機結合
剤の分解が抑制されるのである。さらに、不活性ガスが
増加し酸素が減少するから、分解ガスの発生量が抑制さ
れるのである。すなわち、セラミック成形品の内部での
ガス圧の増加が抑制されるから、セラミック成形品に膨
れが生じたり、セラミック成形品が割れたりすることが
防止できるわけである。このようにして、有機結合剤が
分解しはじめるまでは、主として空気のみの雰囲気と
し、分解ガスの発生量の増加に伴なって不活性ガスの供
給量を増加させ、脱脂が十分に進むと、再び空気の供給
量を増やすようにしているのである。したがって、比較
的高価な不活性ガスのみを用いる場合に比較して、脱脂
工程におけるコストを低減することができるのである。
The control is performed as follows. As shown in FIG.
First, immediately after the start of degreasing, only air is supplied (thick broken line), and the temperature in the furnace 1 rises. At this time, the reflector 2
The reflectance (dashed double-dotted line) of 5 is large, and most of the light from the light source 26 reaches the light receiver 29. When the temperature further rises and the organic binder starts to decompose, the decomposed gas near the surface of the reflecting mirror 25 is cooled and cohesively adheres to the reflecting mirror 25, so that the reflectance is lowered. When the reflectance starts to drop sharply in this way, the management computer 9 adjusts the opening degree of the valve 3 so as to reduce the air supply amount into the furnace 1, and supplies the inert gas (thin broken line). The opening degree of the valve 4 is adjusted so as to increase. Further, the heater 2 is controlled via the thyristor 10 so as to reduce the temperature rise rate in the furnace 1. At this time, the oxygen concentration (dashed line) decreases. Also, the total amount of gas supplied into the furnace 1 is set to increase. When such control is performed, the total amount of gas in the furnace 1 increases,
The atmosphere in the furnace 1 is rapidly updated, the decomposed gas in the surface layer of the ceramic molded product is removed, the escape path of the decomposed gas from the inside of the ceramic molded product is formed, and the swelling of the ceramic molded product occurs. Can be prevented. Further, by rapidly updating the atmosphere, the temperature in the furnace 1 is lowered, the ceramic molded article is cooled, and the decomposition of the organic binder is suppressed. Furthermore, since the amount of inert gas increases and the amount of oxygen decreases, the amount of decomposition gas generated is suppressed. That is, since the increase in gas pressure inside the ceramic molded product is suppressed, it is possible to prevent the ceramic molded product from bulging or cracking. In this way, until the organic binder begins to decompose, it is mainly an atmosphere of only air, the supply amount of the inert gas is increased with the increase in the generation amount of the decomposition gas, and the degreasing progresses sufficiently, It is trying to increase the air supply again. Therefore, the cost in the degreasing process can be reduced as compared with the case where only a relatively expensive inert gas is used.

上記実施例では、空気と不活性ガスとの混合比を可変と
しているが、炉1の中に空気のみを供給し、空気から吸
着等の方法で酸素を除去するにより雰囲気を制御するよ
うにしてもよい。また、上記実施例では、モニタ部材と
して反射鏡25を用いるとともに反射鏡25での光の反
射率を観測しているが、モニタ部材として透明板を配設
して光の透過率を観測するようにしてもよい。さらに、
光ではなく、超音波等の反射率や透過率を観測するよう
にしてもよい。また、モニタ部材の重量を測定してセラ
ミック成形品の脱脂状態を間接的に判定するようにして
もよい。
In the above embodiment, the mixing ratio of air and inert gas is variable, but only the air is supplied into the furnace 1 and the atmosphere is controlled by removing oxygen from the air by a method such as adsorption. Good. Further, in the above embodiment, the reflecting mirror 25 is used as the monitor member and the light reflectance at the reflecting mirror 25 is observed. However, a transparent plate is arranged as the monitor member to observe the light transmittance. You may further,
Instead of light, the reflectance or transmittance of ultrasonic waves or the like may be observed. Alternatively, the degreased state of the ceramic molded product may be indirectly determined by measuring the weight of the monitor member.

[発明の効果] 本発明は上述のように、セラミック成形品の脱脂工程に
おいて、炉内に有機結合剤が再分解する温度以下の温度
に保たれたモニタ部材を配設し、モニタ部材の状態変化
に基づいて炉内の加熱条件を制御するものであり、セラ
ミック成形品の状態を直接検出せずに、炉内に配設した
モニタ部材の状態変革に基づいてセラミック成形品の脱
脂状態を間接的に判定するから、個々のセラミック成形
品の形状や重量等とは無関係に加熱条件が設定できるの
であり、制御用プログラムの負担が軽減でき、脱脂工程
の作業量も低減できるのである。以上の方法により脱脂
行なった結果、割れや膨れのないセラミック成形品を得
ることができた。
EFFECTS OF THE INVENTION As described above, in the present invention, in the degreasing process of a ceramic molded article, a monitor member kept at a temperature equal to or lower than the temperature at which the organic binder is redissolved is disposed in the furnace, and the state of the monitor member is It controls the heating conditions in the furnace based on the changes, and indirectly detects the degreased state of the ceramic molded product based on the change of the state of the monitor member installed in the furnace without directly detecting the state of the ceramic molded product. Therefore, the heating conditions can be set independently of the shape and weight of each ceramic molded product, the load of the control program can be reduced, and the work amount of the degreasing process can be reduced. As a result of degreasing by the above method, it was possible to obtain a ceramic molded product without cracking or swelling.

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

第1図は本発明の実施例を示すシステム構成図、第2図
は同上の要部構成図、第3図同上の動作説明図である。 1……炉、2……ヒータ、3,4……バルブ、8……酸
素濃度検出器、9……管理用コンピュータ、20……セ
ラミック成形品、25……反射鏡、26……光源、2
7,28……窓、29……受光器。
FIG. 1 is a system configuration diagram showing an embodiment of the present invention, FIG. 2 is a configuration diagram of main parts of the same, and FIG. 3 is an operation explanatory diagram of the same. 1 ... Furnace, 2 ... Heater, 3, 4 ... Bulb, 8 ... Oxygen concentration detector, 9 ... Management computer, 20 ... Ceramic molded product, 25 ... Reflector, 26 ... Light source, Two
7, 28 ... Window, 29 ... Receiver.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】セラミック粉末と有機結合剤とからなるセ
ラミック成形品を炉内で加熱して有機結合剤を除去する
脱脂工程において、炉内に有機結合剤が再分解する温度
以下の温度に保たれたモニタ部材を配設し、モニタ部材
の状態変化に基づいて炉内に加熱条件を制御することを
特徴とするセラミック成形品の脱脂法。
1. In a degreasing process of heating a ceramic molded product composed of ceramic powder and an organic binder in a furnace to remove the organic binder, the temperature is maintained at a temperature equal to or lower than a temperature at which the organic binder is decomposed again in the furnace. A degreasing method for a ceramic molded article, comprising disposing a dripping monitor member and controlling heating conditions in the furnace based on a change in the state of the monitor member.
JP63158819A 1988-06-27 1988-06-27 Degreasing method for ceramic molded products Expired - Lifetime JPH0627040B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63158819A JPH0627040B2 (en) 1988-06-27 1988-06-27 Degreasing method for ceramic molded products

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63158819A JPH0627040B2 (en) 1988-06-27 1988-06-27 Degreasing method for ceramic molded products

Publications (2)

Publication Number Publication Date
JPH029770A JPH029770A (en) 1990-01-12
JPH0627040B2 true JPH0627040B2 (en) 1994-04-13

Family

ID=15680064

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63158819A Expired - Lifetime JPH0627040B2 (en) 1988-06-27 1988-06-27 Degreasing method for ceramic molded products

Country Status (1)

Country Link
JP (1) JPH0627040B2 (en)

Also Published As

Publication number Publication date
JPH029770A (en) 1990-01-12

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