JPS6287464A - Method of dewaxing ceramic formed body - Google Patents

Method of dewaxing ceramic formed body

Info

Publication number
JPS6287464A
JPS6287464A JP60227437A JP22743785A JPS6287464A JP S6287464 A JPS6287464 A JP S6287464A JP 60227437 A JP60227437 A JP 60227437A JP 22743785 A JP22743785 A JP 22743785A JP S6287464 A JPS6287464 A JP S6287464A
Authority
JP
Japan
Prior art keywords
degreasing
gas
heating chamber
gas concentration
predetermined value
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.)
Granted
Application number
JP60227437A
Other languages
Japanese (ja)
Other versions
JPH0660062B2 (en
Inventor
誠司 水野
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.)
Toyota Motor Corp
Original Assignee
Toyota Motor 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 Toyota Motor Corp filed Critical Toyota Motor Corp
Priority to JP60227437A priority Critical patent/JPH0660062B2/en
Publication of JPS6287464A publication Critical patent/JPS6287464A/en
Publication of JPH0660062B2 publication Critical patent/JPH0660062B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 産業上の利用分野 この発明は射出成形されたセラミック成形体中の有機結
合剤を加熱分解させて除去する脱脂方法に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to a degreasing method for removing an organic binder from an injection-molded ceramic body by thermally decomposing it.

従来の技術 周知のように、セラミック粉末に有機結合剤を混合し、
これを金型に注入する射出成形法は複雑形状品の成形に
適しており、また大量生産が可能で:あるので自動車用
エンジン部品などに幅広く採用されている。
As is well known in the art, ceramic powder is mixed with an organic binder,
The injection molding method, which involves injecting this into a mold, is suitable for molding products with complex shapes, and also enables mass production, so it is widely used for automobile engine parts.

ところでこの樹脂はセラミック成形体の焼結前に除去す
る必要があり、加熱分解により脱脂されている。
By the way, this resin needs to be removed before sintering the ceramic molded body, and is degreased by thermal decomposition.

従来この脱脂においては、急激な樹脂の熱分解によるフ
クレなどの欠陥の発生を抑制し、ざらに爆発を防止する
ためにN2ガスなどの不活性雰囲気中で加熱して脱脂が
行なわれている。しかしながら体積の大きいセラミック
成形体や肉厚部を有するセラミック成形体では内部にま
で脱脂効果を及ばしめるためかなりの高温(500’C
以上)にまで昇温させないと充分脱脂されない。しかも
脱脂反応がゆるやかに進行するように非常に遅い速度で
昇温させるために高温までの加熱は長時間を要し、作業
効率が良好でないという問題点かある。
Conventionally, this degreasing is carried out by heating in an inert atmosphere such as N2 gas in order to suppress the occurrence of defects such as blisters due to rapid thermal decomposition of the resin, and to prevent explosions. However, for ceramic molded bodies with a large volume or thick parts, the degreasing effect extends to the inside, so the temperature is quite high (50'C).
If the temperature is not raised to (above), sufficient degreasing will not occur. Moreover, since the temperature is raised at a very slow rate so that the degreasing reaction proceeds slowly, it takes a long time to heat the product to a high temperature, which poses the problem of poor working efficiency.

このため、不活性ガス雰囲気における脱脂がある程度進
行した時点から後に大気中で脱脂することが要望されて
いる。
For this reason, there is a demand for degreasing in the atmosphere after the degreasing in the inert gas atmosphere has progressed to some extent.

発明が解決しようとする問題点 しかしながら、従来考えられているこの脱脂方法では、
加熱室内でセラミック成形体を加熱するものでおり、不
活性ガスの導入から空気の導入への移行の際および空気
を導入している際に爆発の可能性かあり、作業環境とし
て危険性を伴うという問題点が市る。
Problems to be Solved by the Invention However, with this conventional degreasing method,
Ceramic molded bodies are heated in a heating chamber, and there is a risk of explosion when transitioning from introducing inert gas to introducing air, and while introducing air, making it a dangerous work environment. The problem arises.

この発明は上記問題点を解決することを基本的な目的と
し、射出成形されたセラミック成形体を確実かつ安全に
脱脂することのできる脱脂方法を提供するものである。
The basic object of the present invention is to solve the above-mentioned problems, and to provide a degreasing method that can reliably and safely degrease an injection-molded ceramic molded body.

問題点を解決するための手段 すなわち、この発明は、セラミック成形体が配置されて
加熱される加熱室内に不活性ガスを導入して予備脱脂を
行ない、次いで空気を導入する再脱脂を行なうセラミッ
ク成形体のの脱脂方法において、加熱室内の爆発性カス
濃度を検出する検出部を設けておき、前記予備脱脂から
再脱脂へ移行するにあたって、加熱室内の爆発性ガス濃
度が所定値未満である場合に、加熱室内の不活性ガスの
導入を停止させるとともに空気を導入させ、前記ガス濃
度が所定値以上である場合には加熱室内への不活性ガス
の導入を停止して空気を導入させることなく引き続き不
活性ガスを導入し、また再脱脂中に、前記ガス濃度が所
定値以上である場合に空気の導入を停止させて、不活性
ガスを導入させるように制御することを特徴とする。
Means for Solving the Problems That is, the present invention provides a ceramic molding method in which preliminary degreasing is performed by introducing an inert gas into a heating chamber in which a ceramic molded body is placed and heated, and then air is introduced for re-degreasing. In the body degreasing method, a detection unit is provided to detect the explosive gas concentration in the heating chamber, and when the explosive gas concentration in the heating chamber is less than a predetermined value when transitioning from the preliminary degreasing to the re-degreasing, , the introduction of inert gas into the heating chamber is stopped and air is introduced, and if the gas concentration is above a predetermined value, the introduction of inert gas into the heating chamber is stopped and air is continued without being introduced. The present invention is characterized in that during re-degreasing, the introduction of air is stopped and the inert gas is introduced when the gas concentration is equal to or higher than a predetermined value.

なお、前記ガス濃度の所定値を爆発下限界値とすること
が望ましい。
Note that it is desirable that the predetermined value of the gas concentration be the lower explosive limit value.

作  用 この発明によれば加熱室内へ不活性ガスを導入する予備
脱脂から空気を導入する再脱脂へ移行するにあたって、
加熱室内のガス濃度が所定値未満である場合に不活性ガ
スの導入を停止させ、空気を導入して前記移行をおこな
わせるとともに、再脱脂中にガス濃度が所定値未満であ
るかぎり、空気の導入が続行される。一方、前記移行に
あたって、ガス濃度が所定値以上である場合には空気を
導入する再脱脂への移行はなされずに、不活性ガスが引
き続き導入される。また再脱脂の際にもガス濃度が所定
値以上になると、空気の導入を停止させて、不活性ガス
を導入させる。
Effect According to the present invention, when transitioning from preliminary degreasing in which an inert gas is introduced into the heating chamber to re-degreasing in which air is introduced,
When the gas concentration in the heating chamber is less than a predetermined value, the introduction of inert gas is stopped and air is introduced to cause the transition, and as long as the gas concentration is less than the predetermined value during re-degreasing, the introduction of inert gas is stopped. The installation continues. On the other hand, during the transition, if the gas concentration is equal to or higher than a predetermined value, the transition to re-degreasing in which air is introduced is not performed, and the inert gas is continuously introduced. Furthermore, when the gas concentration reaches a predetermined value or higher during re-degreasing, the introduction of air is stopped and an inert gas is introduced.

なお前記ガスi農度の所定値を爆発下限界値とすれば加
熱室内の爆発を有効的に防止することができる。
Note that if the predetermined value of the gas i degree is set as the lower explosion limit value, explosion within the heating chamber can be effectively prevented.

なお、この所定値を爆発下限界値より低い値に設定する
ほど安全性をより高めることができる(通常174〜1
/3)。
It should be noted that the lower this predetermined value is set than the lower explosive limit, the higher the safety can be (usually 174 to 1
/3).

発明を実施するための具体的な説明 この発明の方法を実施するための装置を第1図に基づい
て説明する。加熱炉1内には射出成形されたセラミック
成形体2を収納する加熱室3が配置されており、この加
熱室3には加熱室3内を昇温させるためのヒーター(図
示しない)が配置されており、また加熱室3内のガスを
排気するための排気ダクト3aが設けられている。この
排気ダクト3aからの排気ガスは加熱炉1内を通り図示
しないダクトから加熱炉1外に排気される。またこの加
熱室3には窒素ガス導入管4および空気導入管5が連結
されており、それぞれの導入管には流量検知器(図示し
ない)を有する流量計4a。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An apparatus for carrying out the method of the present invention will be described with reference to FIG. A heating chamber 3 for storing an injection-molded ceramic molded body 2 is arranged in the heating furnace 1, and a heater (not shown) for raising the temperature inside the heating chamber 3 is arranged in the heating chamber 3. Further, an exhaust duct 3a for exhausting gas in the heating chamber 3 is provided. The exhaust gas from the exhaust duct 3a passes through the heating furnace 1 and is exhausted to the outside of the heating furnace 1 from a duct (not shown). Further, a nitrogen gas introduction pipe 4 and an air introduction pipe 5 are connected to the heating chamber 3, and each introduction pipe has a flow meter 4a having a flow rate detector (not shown).

5aが連結されており、ざらに電磁弁4b、5bが設け
られている。またさらに加熱室3にはガス濃度検出用の
ダクト6の一端が連結されており、このダクト6の他端
に加熱炉1の外部に配置されているガス濃度検知部7が
連結されている。このガス濃度検知部7は加熱室3から
導入されるガスを冷却するための冷却器7aとこの冷却
器7aにより冷却されたガスの濃度を検知するためのガ
ス検知器7bとからなる。このガス検知器7bの出力は
、加熱炉1の外面に固定されているプログラムコン1ヘ
ーラ8およびガス警報器9に連結されている。また加熱
炉1にはダンパ10か設けられており、排気の際にh目
熱至1内と外部とが通気され、ざらにh[1熱至3内を
均一に加熱するため、分解ガスを拡散させ炉外へ送り出
すため、また冷却をスムーズにさせるためのファン1a
が設けられている。
5a are connected, and solenoid valves 4b and 5b are roughly provided. Further, one end of a duct 6 for gas concentration detection is connected to the heating chamber 3, and a gas concentration detection section 7 disposed outside the heating furnace 1 is connected to the other end of this duct 6. The gas concentration detection section 7 includes a cooler 7a for cooling the gas introduced from the heating chamber 3, and a gas detector 7b for detecting the concentration of the gas cooled by the cooler 7a. The output of this gas detector 7b is connected to a program controller 1 heater 8 and a gas alarm 9 fixed to the outer surface of the heating furnace 1. The heating furnace 1 is also equipped with a damper 10, which ventilates the inside and outside of the heating furnace 1 during exhaust, and in order to uniformly heat the interior of the heating furnace 1 and the outside, the cracked gas is heated uniformly. Fan 1a for dispersing and sending it out of the furnace and for smooth cooling
is provided.

実施例 以下に、この発明の一実施例を上記装置を使用して行な
う場合について説明する。
EXAMPLE Below, a case will be described in which an example of the present invention is carried out using the above-mentioned apparatus.

まず第1に窒化珪素(S i 3 N4 ) 92VH
%、イツトリア(Y203 )  4wt%、スピネル
(MCIA1204 )4Wj%からなるセラミック粉
末と有機バインダー(パラフィン、EA、APP>を混
合したものを射出成形により所望のタービンホイールの
形状に成形した。この成形体2をセラミック粉末11中
に埋め込み加熱下3内に配置する。次いで窒素ガス導入
管4から301 / n+inで窒素ガスを流し込みな
がら2°C/hの昇温速度で450°Cまで加熱する予
備脱脂が行なわれる。その後ガス検知器7bを作動させ
、加熱下3内のガス濃度が爆発下限界の173未満であ
るか否かが検知される。この爆発下限界は、有機バイン
ダーの熱分解により発生でるプロピレン<C31−15
> 、プロパン(C3f−(8) 、ペンテン(C5H
IO> 、メタン(CH4)などのトータールのハイド
ロカーボン量を例えばプロパンに換算した場合、2.1
%となる。
First of all, silicon nitride (S i 3 N4) 92VH
%, Ittria (Y203) 4wt%, Spinel (MCIA1204) 4Wj% and an organic binder (paraffin, EA, APP>) were mixed together and molded into the desired turbine wheel shape by injection molding. 2 is embedded in ceramic powder 11 and placed in heated chamber 3.Next, preliminary degreasing is performed by heating to 450°C at a temperature increase rate of 2°C/h while flowing nitrogen gas at 301/n+in from nitrogen gas introduction pipe 4. Thereafter, the gas detector 7b is activated to detect whether the gas concentration in the heated chamber 3 is less than the lower explosive limit of 173.This lower explosive limit is generated by thermal decomposition of the organic binder. Propylene <C31-15
>, propane (C3f-(8), pentene (C5H)
IO>, for example, when the total amount of hydrocarbons such as methane (CH4) is converted to propane, it is 2.1
%.

前記検知の際にガス濃度が爆発下限界の173未満であ
る場合には、ガス検知器7bからの出力が加えられたプ
ログラムコントローラ8により電磁弁4bを閉じて窒素
ガス導入管4からの窒素ガスの導入を止め、電磁弁5b
を開いて空気導入管5がら空気を101/manで導入
させて400’Cで5時間保持する再脱脂を行ない、そ
の後にヒーターを切り冷却させた。この方法により亀裂
、フクレなどの欠陥がなく充分に脱脂された脱脂体が得
られた。
If the gas concentration is less than the lower explosive limit of 173 at the time of the detection, the program controller 8 to which the output from the gas detector 7b is applied closes the solenoid valve 4b to stop nitrogen gas from the nitrogen gas inlet pipe 4. Stop introducing the solenoid valve 5b.
The tube was opened and air was introduced through the air inlet tube 5 at a rate of 101/man to perform re-degreasing by holding the tube at 400'C for 5 hours, after which the heater was turned off and the tube was cooled. By this method, a fully degreased body without defects such as cracks and blisters was obtained.

この方法において、前記予備脱脂から再脱脂へ移行され
る際、および再脱脂の進行中に密閉容器3内のガス濃度
がガス検出器7bにより爆発下限界の173以上になる
と空気導入管5の電磁弁5bは閉じられた状態にされ、
窒素ガス導入管4の電磁弁4bは聞かれた状態にされ、
この導入管4から窒素ガスが導入される。ざらに、ガス
検出器7hからの出力が加えられるガス警報器9が作動
されて警報を発する。また前記プログラムコントローラ
8により加熱¥3のヒータは切られてファン1aにより
加熱下3内は冷却されるとともにダンパ10は全開され
、加熱下3内の加熱空気およびガスを強制的に排出させ
て加熱下3内のガス濃度を低下させるとともに爆発を引
き起こす要因となる火種をなくして爆発を未然に防止す
る。
In this method, when transitioning from the preliminary degreasing to re-degreasing, and during the progress of re-degreasing, if the gas concentration in the sealed container 3 reaches 173 or more, which is the lower explosive limit, as detected by the gas detector 7b, the electromagnetic the valve 5b is kept closed;
The solenoid valve 4b of the nitrogen gas introduction pipe 4 is set to the open state,
Nitrogen gas is introduced from this introduction pipe 4. In general, the gas alarm 9 to which the output from the gas detector 7h is applied is activated to issue an alarm. Further, the program controller 8 turns off the heater 3, and the fan 1a cools the inside of the heating chamber 3, and the damper 10 is fully opened to forcibly discharge the heated air and gas inside the heating chamber 3, thereby heating the chamber. Explosion is prevented by lowering the gas concentration in the lower part 3 and eliminating sources of fire that could cause an explosion.

この実施例では上述のように予備脱脂から再脱脂への移
行にあたって、もしくは再脱脂中に爆発性ガス濃度が爆
発下限界の173以上の場合に、ヒーターを切りダンパ
を全開させて加熱下3内のガス濃度を低下させ、またガ
ス警報器9を作動させて警報を発するようにしたが、こ
の発明としては必ずしも必要なものではない。但し、こ
のような作動を行なわせることにより爆発の回避を確実
なものとすることができ、また周囲に危険を知らしめる
ことができる。また、この実施例では不活性ガスとして
窒素ガスを用いたが、アルゴンなどの他の不活性ガスを
用いることも可能で娶る。
In this embodiment, as mentioned above, when transitioning from pre-degreasing to re-degreasing, or if the explosive gas concentration exceeds the lower explosive limit of 173 during re-degreasing, the heater is turned off, the damper is fully opened, and the Although the gas alarm 9 is activated to issue an alarm, this is not necessarily necessary for the present invention. However, by performing such an operation, it is possible to ensure the avoidance of an explosion, and it is also possible to notify the surroundings of the danger. Furthermore, although nitrogen gas was used as the inert gas in this embodiment, other inert gases such as argon may also be used.

発明の詳細 な説明したようにこの発明によれば、予備脱脂から再脱
脂への移行の際および再脱脂の進行の際に、密閉容器内
のガス濃度を検知し、このガス濃度が所定値未満である
場合に脱脂を進行させ、ガス濃度が所定値以上では脱脂
を停止させて密閉容器内に不活性ガスを導入するように
制御するので脱脂作業を安全に行なうことができ、この
安全性に基づき予備脱脂と再脱脂からなる脱脂作業を現
実に行なうことができるため、欠陥のない良好な脱脂体
を得る効果がある。
DETAILED DESCRIPTION OF THE INVENTION According to the present invention, the gas concentration in the sealed container is detected during the transition from preliminary degreasing to re-degreasing and during the progress of re-degreasing, and when the gas concentration is less than a predetermined value. When the gas concentration exceeds a predetermined value, the degreasing is controlled to proceed, and when the gas concentration exceeds a predetermined value, the degreasing is stopped and an inert gas is introduced into the sealed container, so the degreasing work can be performed safely. Based on this method, degreasing work consisting of preliminary degreasing and re-degreasing can actually be carried out, which has the effect of obtaining a good degreased body without defects.

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

第1図はこの発明の一実施例に用いる装置の平面概略図
、第2図は同じく正面略解図、第3図は同じく右側面概
略図でおる。 1・・・加熱炉、 2・・・セラミック成形体、 3・
・・力ロ熱至、 4・・・窒素ガス導入管、 5・・・
空気導入管、7・・・ガス濃度検出部、 7b・・・ガ
ス検出器、 8・・・プログラムコントローラー、 9
・・・ガス警報器、10・・・循環/排気切換ダンパ。
FIG. 1 is a schematic plan view of an apparatus used in an embodiment of the present invention, FIG. 2 is a schematic front view, and FIG. 3 is a schematic right side view. 1...Heating furnace, 2...Ceramic molded body, 3.
・・Power Ro heat, 4... Nitrogen gas introduction pipe, 5...
Air introduction pipe, 7... Gas concentration detection section, 7b... Gas detector, 8... Program controller, 9
...Gas alarm, 10...Circulation/exhaust switching damper.

Claims (2)

【特許請求の範囲】[Claims] (1)セラミック成形体が配置されて加熱される加熱室
内に不活性ガスを導入して予備脱脂を行ない、次いで空
気を導入する再脱脂を行なうセラミック成形体の脱脂方
法において、加熱室内の爆発性ガス濃度を検出する検出
部を設けておき、前記予備脱脂から再脱脂へ移行するに
あたつて加熱室内の爆発性ガス濃度が所定値未満である
場合に、加熱室内への不活性ガスの導入を停止させると
ともに空気を導入させ、前記ガス濃度が所定値以上であ
る場合には加熱室内への不活性ガスの導入を停止して空
気を導入させることなく引き続き不活性ガスを導入し、
また再脱脂中に、前記ガス濃度が所定値以上である場合
に空気の導入を停止させて、不活性ガスを導入させるよ
うに制御することを特徴とするセラミック成形体の脱脂
方法。
(1) In a method of degreasing a ceramic molded body in which preliminary degreasing is performed by introducing an inert gas into the heating chamber in which the ceramic molded body is placed and heated, and then re-degreasing is performed by introducing air, explosive A detection unit that detects the gas concentration is provided, and when the explosive gas concentration in the heating chamber is less than a predetermined value when transitioning from the preliminary degreasing to the re-degreasing, an inert gas is introduced into the heating chamber. is stopped and air is introduced, and if the gas concentration is equal to or higher than a predetermined value, the introduction of inert gas into the heating chamber is stopped and the inert gas is continuously introduced without introducing air;
A method for degreasing a ceramic molded body, characterized in that during re-degreasing, when the gas concentration is equal to or higher than a predetermined value, the introduction of air is stopped and an inert gas is introduced.
(2)前記ガス濃度の所定値は爆発下限界値であること
を特徴とする特許請求の範囲第1項記載のセラミック成
形体の脱脂方法。
(2) The method for degreasing a ceramic molded body according to claim 1, wherein the predetermined value of the gas concentration is a lower explosive limit value.
JP60227437A 1985-10-12 1985-10-12 Degreasing method for ceramic molded body Expired - Fee Related JPH0660062B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60227437A JPH0660062B2 (en) 1985-10-12 1985-10-12 Degreasing method for ceramic molded body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60227437A JPH0660062B2 (en) 1985-10-12 1985-10-12 Degreasing method for ceramic molded body

Publications (2)

Publication Number Publication Date
JPS6287464A true JPS6287464A (en) 1987-04-21
JPH0660062B2 JPH0660062B2 (en) 1994-08-10

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006232590A (en) * 2005-02-23 2006-09-07 Ngk Insulators Ltd Method for manufacturing ceramic structure
JP2007001843A (en) * 2005-06-27 2007-01-11 Ngk Insulators Ltd Degreasing method
CN116444263A (en) * 2023-03-15 2023-07-18 先导薄膜材料(安徽)有限公司 Sintering process of indium tin oxide target

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4974705A (en) * 1972-11-20 1974-07-18
JPS50126011A (en) * 1974-03-07 1975-10-03
JPS60145966A (en) * 1984-01-07 1985-08-01 トヨタ自動車株式会社 Method of dewaxing ceramic injection formed body

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4974705A (en) * 1972-11-20 1974-07-18
JPS50126011A (en) * 1974-03-07 1975-10-03
JPS60145966A (en) * 1984-01-07 1985-08-01 トヨタ自動車株式会社 Method of dewaxing ceramic injection formed body

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006232590A (en) * 2005-02-23 2006-09-07 Ngk Insulators Ltd Method for manufacturing ceramic structure
EP1696194A3 (en) * 2005-02-23 2009-04-01 Ngk Insulators, Ltd. Method for producing ceramic structure
JP2007001843A (en) * 2005-06-27 2007-01-11 Ngk Insulators Ltd Degreasing method
JP4523499B2 (en) * 2005-06-27 2010-08-11 日本碍子株式会社 Degreasing method
CN116444263A (en) * 2023-03-15 2023-07-18 先导薄膜材料(安徽)有限公司 Sintering process of indium tin oxide target
CN116444263B (en) * 2023-03-15 2024-02-27 先导薄膜材料(安徽)有限公司 Sintering process of indium tin oxide target

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