JPH0470122B2 - - Google Patents

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Publication number
JPH0470122B2
JPH0470122B2 JP32693088A JP32693088A JPH0470122B2 JP H0470122 B2 JPH0470122 B2 JP H0470122B2 JP 32693088 A JP32693088 A JP 32693088A JP 32693088 A JP32693088 A JP 32693088A JP H0470122 B2 JPH0470122 B2 JP H0470122B2
Authority
JP
Japan
Prior art keywords
temperature
mold
molding
sintered body
injection molding
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
Application number
JP32693088A
Other languages
Japanese (ja)
Other versions
JPH02171205A (en
Inventor
Shigeki Kato
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.)
NGK Insulators Ltd
Original Assignee
NGK Insulators 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 NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP32693088A priority Critical patent/JPH02171205A/en
Priority to US07/454,912 priority patent/US5066449A/en
Priority to DE3942686A priority patent/DE3942686C2/en
Publication of JPH02171205A publication Critical patent/JPH02171205A/en
Publication of JPH0470122B2 publication Critical patent/JPH0470122B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

[産業上の利用分野] 本発明は、セラミツクスを射出成形する場合に
おいて、性能の優れた射出成形品を製造するセラ
ミツクスの射出成形方法に関する。 [従来の技術] 窒化珪素、炭化珪素、サイアロン等のシリコン
セラミツクスは、金属よりも高温で安定であり、
酸化腐食やクリープ変形を受け難いところから、
近年、それをエンジン部品として利用する研究が
活発に行なわれている。例えば、これらセラミツ
クス材料からなるラジアル型タービンロータは、
金属製ロータに比べて、軽量でエンジンの作動温
度を高めることができ、熱効率に優れているため
に、自動車ターボチヤージヤーロータ或いはガス
タービンロータ等として注目を集めている。 このような、タービンロータは、複雑な三次元
形状を成す翼部を有しているため、焼結された単
純な形状の、例えば緻密な窒化珪素、炭化珪素焼
結体等の棒状或いは角状など単純な形状の素材を
研削加工によつて所望の形状に仕上げることは、
不可能に近いものであることは勿論、単に1回の
成形操作にて、そのような複雑な形状の成形体を
得ることは極めて困難である。このような複雑な
セラミツクス成形体を製造する方法として、従
来、射出成形法が広く利用されている。 セラミツクスの射出成形法は、プラスチツクの
成形を応用した成形法で、セラミツクス粉末にポ
リエチレン、ポリスチレン等の熱可塑性樹脂、可
塑剤、分散剤、ワツクス等からなる有機バインダ
ーを混合し、この混合原料を加熱して可塑性をも
たせ、成形用金型内に射出して成形する方法であ
り、得られた焼結体を脱脂し、焼成することによ
つてセラミツクス成形体を得ることができる。ま
た近年、セラミツクス粉体に可塑化媒体として主
に水を可塑剤として有機バインダーを混合し、こ
の混合原料を冷却して可塑性をもたせ、成形用金
型内に射出して成形する方法であり、得られた成
形体をバインダー除去し焼成することによつてセ
ラミツクス焼結体を得る方法も一部で検討されて
いる。この成形方法によれば、他の方法ではかな
りの工数を必要とするような複雑な部品を1回の
操作で、迅速に且つ精密で、仕上げ代の少ない成
形品を得ることができる。 このような従来から行なわれている射出成形方
法においては、成形用金型の温度について通常金
型温度を入口部から先端部まで一定にすることに
より成形が行なわれていた。 [発明が解決しようとする課題] しかしながら、成形用金型の温度を一定にした
場合には射出成形に際して金型入口部と先端部と
の間で成形材料の温度差が生じ、得られる成形体
の密度分布が不均一となり、その結果、該成形体
を焼成してできる焼結体にはクラツクが生じた
り、変形等が生じ、寸法精度、強度などが不均一
となり均一な焼結体を得ることができなかつた。 [課題を解決するための手段] そこで、本発明者は上記した従来の問題を解決
するため鋭意研究した結果、成形用金型に温度勾
配を設けるようにして成形材料を均一な温度に制
御し得ることを見出し、本発明に到達した。 即ち、本発明によれば、セラミツクスを射出成
形する方法において、加圧終了時の成形用金型近
傍の成形体温度を測定し金型に温度勾配を設ける
ことにより、成形用金型近傍の成形体温度分布が
±0.5℃以内となるようにしたことを特徴とする
セラミツクスの射出成形方法、が提供される。 [作 用] 本発明では、加圧終了時の成形用金型近傍の成
形体温度分布が±0.5℃以内となるように制御し
たものである。そのため、成形用金型温度を入口
部から先端部へ勾配を有するように設定する方
法、さらには金型内に成形材料を充填する速度
(射出速度)をコントロールする方法等がある。
本発明における具体的な例としては、第1図に示
す如く、金型入口部から測温部までの成形材料到
達時間x(sec)、金型入口部から測温部までの金
型の温度差y(℃)としたとき、x≦y≦5xの範
囲になるように金型の温度勾配を設定する。y=
xからy=5xの範囲となる理由は、成形材料
中の有機バインダーの種類及び添加量、又はセラ
ミツクス粉末の種類及び添加量によつて成形材料
の比熱又は熱伝導率が異なるため、成形体の形
状及び肉厚が異なるため、成形条件等が異なる
ため、等である。比熱が大きく熱伝導率が小さい
成形材料では金型温度の影響を受けにくいため、
成形材料到達時間xが長くても金型温度差yを小
さくでき、例えばy=xとなる。又、比熱が小さ
く熱伝導率がが大きい成形材料では金型温度の影
響を受けやすいため、成形材料到達時間xが長く
なると金型温度差yを大きくしなければならず、
例えばy=5xとなる。具体的に、例えばセラミ
ツクス材料の組成が、セラミツクス粉末48〜
60vol%、有機バインダー52〜40vol%で、かつ該
有機バインダーの組成として分子量1〜5万が3
〜15wt%、分子量200〜1000が85〜97wt%であ
り、又成形する条件が成形材料温度60〜80℃、金
型温度40〜52℃である場合には、x≦y≦5xの
範囲が好ましい。 上記のように金型温度勾配を設定すると、射出
成形された成形体の金型近傍の温度が部位に拘ら
ず±0.5℃以内とほぼ均一となつて、均質な成形
体の作製、およびそれに引続く均質な焼結体の製
造のために好ましい。成形体の温度分布が±0.5
℃以上になると、得られる成形体の密度分布が不
均一となり、その結果、該成形体を焼成してでき
る焼結体にはクラツクが生じたり、変形等が生
じ、寸法精度、強度などが不均一となり均一な焼
結体を得ることができなかつた。 また、成形用金型近傍の成形体の温度分布が±
0.5℃以上であることが必要な時点は、加圧終了
時である。一般に、射出成形は成形材料を充填し
た後所定時間高圧加圧し、次いで成形体形状付与
又は成形体内部に発生するヒケ等の欠陥を防止す
るため所定時間低圧にて保持される。加圧終了時
とは上記所定時間実施される高圧加圧処理の終了
時をいう。 金型温度の設定および射出速度の設定が終了し
た後、成形体温度測定用熱電対を取りはずし、射
出成形することになる。 上記のような金型の好ましい温度条件は、原料
の調合粉末に結合剤、ワツクス、滑剤等多量の有
機バインダーを添加して混練する有機バインダー
を用いる射出成形法にあつては、射出成形用材料
温度が金型温度よりも高いため、成形用材料が入
口部から先端部に行くに従つて冷され、成形体の
温度も入口部から先端部に行くに従つて低くな
る。これを補い成形体の温度を一定にするため、
金型の温度を入口部から先端部に行くに従つて上
昇させる。金型の加温方法は、例えば一般的なヒ
ーター(棒、バンド等)を用いてもよいし、液体
(水、油)を用いてもよい。 また、原料の調合粉末に少量の有機バインダー
と主に水を添加してなる坏土を用いる射出成形法
にあつては、坏土(成形用材料)の温度が金型温
度よりも低いため、成形用材料が入口部から先端
部に行くに従つて高くなる。これを補い成形体の
温度を一定にするため、金型の温度を入口部から
先端部に行くに従つて下降させるのである。な
お、本発明で使用されるセラミツク粉末として
は、従来より知られた酸化物であるアルミナ、ジ
ルコニア等のほか、いわゆるニユーセラミツクス
として知られる窒化珪素等の窒化物、炭化珪素等
の炭化物、およびこれらの複合材料等を使用する
ことができる。 [実施例] 以下、実施例に基き本発明をさらに詳細に説明
するが、本発明はこれらの実施例に限定されるも
のではない。 実施例 1 有機バインダーを用いる射出成形方法を実施し
た。以下、第2図の有機バインダーを用いる射出
成形方法を示すフローシートに従つて説明する。 セラミツクス原料の窒化珪素粉末100重量部に
対して、焼結助剤としてSrO:2重量部、
MgO:3重量部、CeO2:3重量部を添加し、こ
れらを粉砕混合して平均粒径0.5μmの調合粉末と
し、次いでスプレードライによつて平均粒径
30μmの顆粒を得た後、2.5ton/cm2の圧力で静水
圧等方加圧を行つて造粒し、これを解砕して平均
粒径30μmの粒子を得た。次に、この調合粉末100
重量部に対して、結合剤:3重量部、ワツクス:
15重量部、滑剤:2重量部を加えて混練し、これ
をペレツト状とし、次いでこれを材料温度68℃、
射出圧力400Kg/cm2、射出速度100〜300c.c./sec、
加圧時間15secで、表1に示す金型温度によつて
A,B,C各部の温度を制御しつつ第3図に示す
成形用金型内に射出成形を行ない、長さ150mm、
幅65mm、厚さ15mmの成形体を得た。その際の成形
体の温度を表1に示す。 ここで、第3図の金型には、金型温度制御用熱
電対10,10′,10″、成形体温度測定用熱電
対11,11′,11″および金型加温用ヒーター
12,12′,12″が設けられ、金型温度の制御
と成形体温度の測定が行なわれる。なお、13は
金型のゲート(入口部)、14,14′,14″は
金型内圧力検出センサーを示す。これらセンサー
の温度及び圧力のサンプリング間隔は10μsecで行
なつた。 次に、成形体を1〜3℃/hの昇温速度で400
℃まで昇温し、その温度で5時間保持して脱脂処
理を行ない、次いで7ton/cm2の圧力で静水圧等方
加圧を行なつた後常圧の窒素雰囲気下1700℃にて
1時間焼成を行ない角型の焼結体を得た。得られ
た焼結体の寸法精度および強度を表1に示す。 比較例 1、2 成形用金型の制御温度を表1に示す条件とした
以外はすべて実施例1と同じ条件によつて成形体
を作製し、角型の焼結体を得た。得られた焼結体
の寸法精度および強度を表1に示す。 実施例 2 実施例1と同じ原料を使用し、第4図に示す金
型を用いて、その制御温度を表1に示すように変
えた以外は実施例1と同じ方法で射出成形を行な
い、直径30mmφ、長さ200mmの成形体を得、更に
実施例1と同じ方法で脱脂および焼成を行ない丸
棒型の焼結体を得た。得られた焼結体の寸法精度
および強度を表1に示す。 比較例 3 成形用金型の制御温度を表1に示す条件とした
以外はすべて実施例2と同じ条件によつて作製
し、丸棒型の焼結体を得た。得られた焼結体の寸
法精度および強度を表1に示す。 実施例 3 実施例1と同じ原料を使用し、第5図a,bに
示す金型を用いてその制御温度を表1に示すよう
に変えた以外は実施例1と同じ方法で射出成形を
行ない、チツプ径150mmφ、翼高100mmのタービン
ロータ成形体を得、更に実施例1と同じ方法で脱
脂および焼成を行ないタービンロータ焼結体を得
た。得られた焼結体の寸法精度を表1に示す。 比較例 4 成形用金型の制御温度を表1に示す条件とした
以外はすべて実施例3と同じ条件によつて作製
し、タービンロータの焼結体を得た。得られた焼
結体の寸法精度を表1に示す。 上記の実施例および比較例から明らかなよう
に、金型の制御温度を入口部より先端部に行くに
従つて上げ、しかもその温度上昇が、第1図に示
す如き温度勾配の範囲内になつた場合には加圧終
了時の成形体温度は何れの部位においても±0.5
℃以内となり、寸法精度がよく、強度の高い焼結
体が得られることが分かる。
[Industrial Field of Application] The present invention relates to a ceramic injection molding method for producing injection molded products with excellent performance when injection molding ceramics. [Prior Art] Silicon ceramics such as silicon nitride, silicon carbide, and sialon are more stable at high temperatures than metals.
Because it is resistant to oxidative corrosion and creep deformation,
In recent years, research into using it as engine parts has been actively conducted. For example, radial turbine rotors made of these ceramic materials,
Compared to metal rotors, they are lightweight, can raise the operating temperature of the engine, and have excellent thermal efficiency, so they are attracting attention as automotive turbocharger rotors, gas turbine rotors, etc. Since such a turbine rotor has blades with a complicated three-dimensional shape, it is possible to use a simple sintered material such as a rod-like or square-like material such as a dense silicon nitride or silicon carbide sintered body. Finishing a material with a simple shape into a desired shape by grinding,
Needless to say, it is extremely difficult to obtain a molded article with such a complicated shape in just one molding operation. Conventionally, injection molding has been widely used as a method for manufacturing such complicated ceramic molded bodies. Ceramics injection molding is a molding method that applies plastic molding. Ceramics powder is mixed with an organic binder consisting of thermoplastic resins such as polyethylene and polystyrene, plasticizers, dispersants, wax, etc., and this mixed raw material is heated. This is a method in which the ceramic is molded to give it plasticity and then injected into a mold for molding. By degreasing the obtained sintered body and firing it, a ceramic molded body can be obtained. In addition, in recent years, a method has been developed in which ceramic powder is mixed with an organic binder, mainly water as a plasticizing medium, and this mixed raw material is cooled to give it plasticity, and then injected into a mold for molding. A method of obtaining a ceramic sintered body by removing the binder from the obtained molded body and firing it has also been considered in some cases. According to this molding method, a complex part that would otherwise require a considerable number of man-hours can be quickly and precisely molded with a small finishing allowance in one operation. In such conventional injection molding methods, molding is usually carried out by keeping the mold temperature constant from the inlet to the tip. [Problems to be Solved by the Invention] However, when the temperature of the molding die is kept constant, a temperature difference occurs in the molding material between the mold entrance and the tip during injection molding, and the resulting molded product The density distribution becomes uneven, and as a result, cracks or deformations occur in the sintered body produced by firing the molded body, resulting in uneven dimensional accuracy, strength, etc., resulting in a uniform sintered body. I couldn't do it. [Means for Solving the Problems] Therefore, as a result of intensive research in order to solve the above-mentioned conventional problems, the present inventors created a temperature gradient in the molding die to control the temperature of the molding material to be uniform. The present invention was achieved based on the discovery that the present invention can be obtained. That is, according to the present invention, in a method for injection molding ceramics, the temperature of the molded product near the molding die at the end of pressurization is measured and a temperature gradient is provided in the mold, thereby reducing the molding temperature near the molding die. Provided is a method for injection molding ceramics, characterized in that the body temperature distribution is within ±0.5°C. [Function] In the present invention, the temperature distribution of the molded article near the molding die at the end of pressurization is controlled to be within ±0.5°C. Therefore, there are methods such as setting the temperature of the mold so that it has a gradient from the inlet to the tip, and controlling the speed at which the molding material is filled into the mold (injection speed).
As a specific example of the present invention, as shown in FIG. When the difference is y (°C), the temperature gradient of the mold is set so that x≦y≦5x. y=
The reason for the range from x to y = 5x is that the specific heat or thermal conductivity of the molding material varies depending on the type and amount of organic binder in the molding material or the type and amount of ceramic powder added. Because the shape and wall thickness are different, the molding conditions etc. are different, etc. Molding materials with high specific heat and low thermal conductivity are less affected by mold temperature, so
Even if the molding material arrival time x is long, the mold temperature difference y can be made small, for example, y=x. In addition, molding materials with low specific heat and high thermal conductivity are easily affected by mold temperature, so as molding material arrival time x increases, mold temperature difference y must be increased.
For example, y=5x. Specifically, for example, the composition of the ceramic material is ceramic powder 48~
60vol%, organic binder 52 to 40vol%, and the composition of the organic binder is a molecular weight of 10,000 to 50,000.
~15wt%, molecular weight 200-1000 is 85-97wt%, and the molding conditions are molding material temperature 60-80℃ and mold temperature 40-52℃, the range of x≦y≦5x is preferable. When the mold temperature gradient is set as described above, the temperature near the mold of the injection-molded product becomes almost uniform within ±0.5℃ regardless of the part, making it possible to produce a homogeneous molded product and the resulting This is preferable for the subsequent production of a homogeneous sintered body. Temperature distribution of molded body is ±0.5
If the temperature exceeds ℃, the density distribution of the obtained compact becomes uneven, and as a result, the sintered compact produced by firing the compact becomes cracked, deformed, etc., and the dimensional accuracy, strength, etc. become unstable. It was not possible to obtain a uniform sintered body. In addition, the temperature distribution of the molded object near the molding die is ±
The point at which the temperature needs to be 0.5°C or higher is at the end of pressurization. Generally, in injection molding, after filling the molding material, high pressure is applied for a predetermined period of time, and then the molded object is held at low pressure for a predetermined period of time in order to impart a shape to the molded object or to prevent defects such as sink marks occurring inside the molded object. The term "completion of pressurization" refers to the time of completion of the high-pressure pressurization process that is carried out for the predetermined period of time. After setting the mold temperature and injection speed, the thermocouple for measuring the temperature of the molded object is removed and injection molding is started. The preferred temperature conditions for the mold as described above are as follows: In the injection molding method using an organic binder, in which a large amount of organic binder such as a binder, wax, lubricant, etc. is added to the raw material blended powder and kneaded, the injection molding material Since the temperature is higher than the mold temperature, the molding material is cooled as it goes from the inlet to the tip, and the temperature of the molded body also decreases as it goes from the inlet to the tip. In order to compensate for this and keep the temperature of the molded object constant,
The temperature of the mold is increased from the inlet to the tip. As a method of heating the mold, for example, a general heater (rod, band, etc.) may be used, or a liquid (water, oil) may be used. In addition, in injection molding methods that use clay made by adding a small amount of organic binder and mainly water to the raw material blended powder, the temperature of the clay (molding material) is lower than the mold temperature. The molding material becomes higher from the inlet to the tip. In order to compensate for this and keep the temperature of the molded product constant, the temperature of the mold is lowered from the inlet to the tip. The ceramic powder used in the present invention includes conventionally known oxides such as alumina and zirconia, as well as nitrides such as silicon nitride, known as new ceramics, and carbides such as silicon carbide. Composite materials, etc. can be used. [Examples] Hereinafter, the present invention will be explained in more detail based on Examples, but the present invention is not limited to these Examples. Example 1 An injection molding process using an organic binder was carried out. Hereinafter, a description will be given according to a flow sheet showing an injection molding method using an organic binder shown in FIG. 2 parts by weight of SrO as a sintering aid for 100 parts by weight of silicon nitride powder as a ceramic raw material;
Add 3 parts by weight of MgO and 3 parts by weight of CeO 2 , grind and mix these to obtain a blended powder with an average particle size of 0.5 μm, and then spray dry to reduce the average particle size.
After obtaining granules of 30 μm, they were granulated by isostatic isostatic pressurization at a pressure of 2.5 ton/cm 2 and crushed to obtain particles with an average diameter of 30 μm. Next, this mixed powder 100
Binder: 3 parts by weight, Wax:
15 parts by weight and 2 parts by weight of lubricant were added and kneaded to form pellets, which were then heated at a material temperature of 68°C.
Injection pressure 400Kg/cm 2 , injection speed 100~300c.c./sec,
With a pressurizing time of 15 seconds, injection molding was performed in the mold shown in Figure 3 while controlling the temperature of each part A, B, and C according to the mold temperature shown in Table 1, and the length was 150 mm.
A molded body with a width of 65 mm and a thickness of 15 mm was obtained. Table 1 shows the temperature of the molded body at that time. Here, the mold shown in FIG. 3 includes thermocouples 10, 10', 10'' for controlling mold temperature, thermocouples 11, 11', 11'' for measuring molded body temperature, and heater 12, 12' and 12'' are provided to control the mold temperature and measure the temperature of the molded product. Reference numeral 13 is the gate (inlet part) of the mold, and 14, 14', and 14'' are for detecting the pressure inside the mold. Showing the sensor. The temperature and pressure sampling intervals of these sensors were 10 μsec. Next, the molded body was heated to 400 °C at a heating rate of 1 to 3 °C/h.
℃, held at that temperature for 5 hours to perform degreasing treatment, then subjected to isostatic isostatic pressurization at a pressure of 7 tons/ cm2 , and then heated to 1700℃ for 1 hour under a nitrogen atmosphere at normal pressure. Firing was performed to obtain a square sintered body. Table 1 shows the dimensional accuracy and strength of the obtained sintered body. Comparative Examples 1 and 2 A molded body was produced under the same conditions as in Example 1, except that the control temperature of the molding die was set to the conditions shown in Table 1, and a rectangular sintered body was obtained. Table 1 shows the dimensional accuracy and strength of the obtained sintered body. Example 2 Injection molding was carried out in the same manner as in Example 1, except that the same raw materials as in Example 1 were used, the mold shown in FIG. 4 was used, and the controlled temperature was changed as shown in Table 1. A molded body with a diameter of 30 mmφ and a length of 200 mm was obtained, and further degreased and fired in the same manner as in Example 1 to obtain a round bar-shaped sintered body. Table 1 shows the dimensional accuracy and strength of the obtained sintered body. Comparative Example 3 A round bar-shaped sintered body was obtained by manufacturing under the same conditions as in Example 2 except that the temperature control of the molding die was as shown in Table 1. Table 1 shows the dimensional accuracy and strength of the obtained sintered body. Example 3 Injection molding was carried out in the same manner as in Example 1, except that the same raw materials as in Example 1 were used, the molds shown in Figure 5 a and b were used, and the controlled temperature was changed as shown in Table 1. A turbine rotor molded body having a chip diameter of 150 mmφ and a blade height of 100 mm was obtained, and further degreased and fired in the same manner as in Example 1 to obtain a turbine rotor sintered body. Table 1 shows the dimensional accuracy of the obtained sintered body. Comparative Example 4 A sintered body of a turbine rotor was obtained by manufacturing under the same conditions as in Example 3 except that the control temperature of the molding die was set to the conditions shown in Table 1. Table 1 shows the dimensional accuracy of the obtained sintered body. As is clear from the above examples and comparative examples, the control temperature of the mold is increased from the inlet to the tip, and the temperature rise falls within the range of the temperature gradient shown in Figure 1. In this case, the temperature of the compact at the end of the pressurization will be ±0.5 at any location.
℃ or less, indicating that a sintered body with good dimensional accuracy and high strength can be obtained.

【表】【table】

【表】 実施例 4 坏土を用いる射出成形方法を実施した。以下、
第6図の水系射出成形方法のフローシートに従つ
て説明する。 セラミツクス原料の窒化珪素粉末100重量部に
対して、焼結助剤としてSrO:2重量部、
MgO:3重量部、CeO2:3重量部を添加し、こ
れらを粉砕混合して平均粒径0.6μmの調合粉末と
し、次いでスプレードライによつて平均粒径
30μm程度の顆粒を得た。この顆粒100重量部に対
して、有機バインダー(メチルセルロース:7重
量部、セドランFF−200:1重量部)8重量部、
更に水を約30重量部加えて混練し、次に真空度70
cmHgで真空土練を行ない、直径52mm、長さ500mm
の坏土を得た。これを2.5ton/cm2の圧力で静水圧
等方加圧を行ない、次いで温度12℃の冷暗所で一
晩ねかし、次に坏土温度12℃、射出圧力150〜300
Kg/cm2、射出速度100〜300c.c./sec、ゲル硬化時
間1〜3分で、表2に示す金型温度によつてA,
B,C各部の温度を制御しつつ実施例1と同形状
の第3図に示す成形用金型内に射出成形を行な
い、長さ150mm、幅65mm、厚さ15mmの成形体を得
た。その際の成形体の温度を表2に示す。 次いで、成形体を恒温恒湿器で温度を60℃から
100℃まで昇温し、湿度を98%から20%まで下げ
て乾燥し、次に50℃/hの昇温速度で500℃まで
昇温し、その温度で5時間保持してバインダー除
去を行ない、次いで7ton/cm2の圧力で静水圧等方
加圧を行なつた後、常圧の窒素雰囲気下で、700
℃/hで1650℃まで昇温し、その温度で1時間焼
成を行ない角型の焼結体を得た。得られた焼結体
の寸法精度および強度を表2に示す。 比較例 5、6 成形用金型の制御温度を表2に示す条件とした
以外はすべて実施例4と同じ条件によつて作製
し、角型の焼結体を得た。得られた焼結体の寸法
精度および強度を表2に示す。 実施例 5 実施例4と同じ原料を使用し、第4図に示す金
型を用いその制御温度を表2に示すように変えた
以外は実施例4と同じ方法で射出成形を行ない、
直径30mmφ、長さ200mmの成形体を得、更に実施
例4と同じ方法でバインダー除去および焼成を行
ない丸棒型の焼結体を得た。得られた焼結体の寸
法精度および強度を表2に示す。 比較例 7 成形用金型の制御温度を表2に示す条件とした
以外はすべて実施例5と同じ条件によつて作製
し、丸棒型の焼結体を得た。得られた焼結体の寸
法精度および強度を表2に示す。 実施例 6 実施例4と同じ原料を使用し、第5図a,bに
示す金型を用いてその制御温度を表2に示すよう
に変えた以外は実施例4と同じ方法で射出成形を
行ない、チツプ径150mmφ、翼高100mmのタービン
ロータ成形体を得、更に実施例4と同じ方法でバ
インダー除去および焼成を行ないタービンロータ
の焼結体を得た。得られ焼結体の寸法精度を表2
に示す。 比較例 8 成形用金型の制御温度を表2に示す条件とした
以外はすべて実施例6と同じ条件によつて作製
し、タービンロータの焼結体を得た。得られた焼
結体の寸法精度を表2に示す。 上記の実施例4、5、6および比較例5、6、
7、8により、金型の制御温度を入口部より先端
部に行くに従つて下げ、しかもその温度降下が、
第1図に示す温度勾配の範囲内である場合には加
圧終了時の成形体温度が±0.5℃以内となり、寸
法精度がよく、強度の高い焼結体が得られること
が分る。
[Table] Example 4 An injection molding method using clay was carried out. below,
This will be explained according to the flow sheet of the water-based injection molding method shown in FIG. 2 parts by weight of SrO as a sintering aid for 100 parts by weight of silicon nitride powder as a ceramic raw material;
Add 3 parts by weight of MgO and 3 parts by weight of CeO 2 , grind and mix these to obtain a blended powder with an average particle size of 0.6 μm, and then spray dry to reduce the average particle size.
Granules of about 30 μm were obtained. For 100 parts by weight of this granule, 8 parts by weight of organic binder (methylcellulose: 7 parts by weight, Cedran FF-200: 1 part by weight),
Add about 30 parts by weight of water and knead, then vacuum at 70%.
Perform vacuum soil kneading at cmHg, diameter 52 mm, length 500 mm
Obtained the right to do so. This is subjected to isostatic pressurization at a pressure of 2.5 ton/cm 2 , and then left to rest overnight in a cool, dark place at a temperature of 12°C.
Kg/cm 2 , injection speed 100-300 c.c./sec, gel curing time 1-3 minutes, and mold temperature shown in Table 2.
Injection molding was carried out in a mold shown in FIG. 3 having the same shape as in Example 1 while controlling the temperature of each part of B and C to obtain a molded article having a length of 150 mm, a width of 65 mm and a thickness of 15 mm. Table 2 shows the temperature of the molded body at that time. Next, the molded body is kept in a constant temperature and humidity chamber at a temperature of 60℃.
The temperature was raised to 100°C, the humidity was lowered from 98% to 20% and dried, then the temperature was raised to 500°C at a heating rate of 50°C/h and the binder was removed by holding at that temperature for 5 hours. Then, after performing isostatic pressurization at a pressure of 7 ton/cm 2 , it was heated to 700 m
The temperature was raised to 1650°C at a rate of 1650°C and fired at that temperature for 1 hour to obtain a square sintered body. Table 2 shows the dimensional accuracy and strength of the obtained sintered body. Comparative Examples 5 and 6 A rectangular sintered body was obtained under the same conditions as in Example 4, except that the temperature control of the molding die was set to the conditions shown in Table 2. Table 2 shows the dimensional accuracy and strength of the obtained sintered body. Example 5 Using the same raw materials as in Example 4, injection molding was performed in the same manner as in Example 4, except that the mold shown in FIG. 4 was used and the controlled temperature was changed as shown in Table 2.
A molded body with a diameter of 30 mmφ and a length of 200 mm was obtained, and the binder was removed and fired in the same manner as in Example 4 to obtain a round bar-shaped sintered body. Table 2 shows the dimensional accuracy and strength of the obtained sintered body. Comparative Example 7 A round bar-shaped sintered body was obtained by manufacturing under the same conditions as in Example 5 except that the temperature control of the molding die was as shown in Table 2. Table 2 shows the dimensional accuracy and strength of the obtained sintered body. Example 6 Injection molding was carried out in the same manner as in Example 4, except that the same raw materials as in Example 4 were used, the molds shown in Figure 5 a and b were used, and the controlled temperature was changed as shown in Table 2. A molded turbine rotor having a chip diameter of 150 mmφ and a blade height of 100 mm was obtained, and the binder was removed and fired in the same manner as in Example 4 to obtain a sintered turbine rotor. Table 2 shows the dimensional accuracy of the obtained sintered body.
Shown below. Comparative Example 8 A sintered body of a turbine rotor was obtained by manufacturing under the same conditions as in Example 6 except that the control temperature of the molding die was set to the conditions shown in Table 2. Table 2 shows the dimensional accuracy of the obtained sintered body. Examples 4, 5, 6 and Comparative Examples 5, 6,
7 and 8, the control temperature of the mold is lowered from the inlet to the tip, and the temperature drop is
It can be seen that when the temperature gradient is within the range shown in FIG. 1, the temperature of the compact at the end of pressurization is within ±0.5° C., and a sintered compact with good dimensional accuracy and high strength can be obtained.

【表】【table】

【表】 [発明の効果] 以上説明したように、本発明のセラミツクスの
射出成形方法によれば、全体に均質な成形体が得
られ、その結果、寸法精度が良く、高強度で均質
なセラミツクス焼結体を得ることができる。
[Table] [Effects of the Invention] As explained above, according to the injection molding method for ceramics of the present invention, a molded body that is homogeneous throughout can be obtained, and as a result, a homogeneous ceramic with good dimensional accuracy and high strength can be obtained. A sintered body can be obtained.

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

第1図は本発明における成形用金型の温度勾配
を示すグラフ、第2図は有機系射出成形方法の一
例を示すフローシート、第3図、第4図及び第5
図aはそれぞれ本発明で用いる成形用金型におけ
る温度制御例を示す概要図であり、第5図bは第
5図aにおけるD方向から見た成形体の概要図、
第6図は水系射出成形方法の一例を示すフローシ
ートである。 10,10′,10″…金型温度制御用熱電対、
11,11′,11″…成形体温度測定用熱電対、
12,12′,12″…金型加温用ヒーター、13
…金型のゲート(入口部)、14,14′,14″
…金型内圧力検出センサー。
FIG. 1 is a graph showing the temperature gradient of the molding die in the present invention, FIG. 2 is a flow sheet showing an example of an organic injection molding method, and FIGS. 3, 4, and 5.
Figure a is a schematic diagram showing an example of temperature control in a molding die used in the present invention, and Figure 5 b is a schematic diagram of a molded body viewed from direction D in Figure 5 a.
FIG. 6 is a flow sheet showing an example of a water-based injection molding method. 10, 10', 10''...Thermocouple for mold temperature control,
11, 11', 11''...Thermocouple for measuring temperature of molded object,
12, 12', 12''...Mold warming heater, 13
...Mold gate (entrance), 14, 14', 14''
...In-mold pressure detection sensor.

Claims (1)

【特許請求の範囲】 1 セラミツクスを射出成形する方法において、
加圧終了時の成形用金型近傍の成形体温度を測定
し金型に温度勾配を設けることにより、成形用金
型近傍の成形体温度分布が±0.5℃以内となるよ
うにしたことを特徴とするセラミツクスの射出成
形方法。 2 さらに、成形用金型内への成形材料の射出速
度を制御する請求項1記載のセラミツクスの射出
成形方法。
[Claims] 1. A method for injection molding ceramics,
By measuring the temperature of the molded object near the molding die at the end of pressurization and creating a temperature gradient in the mold, the temperature distribution of the molded object near the molding die is within ±0.5℃. An injection molding method for ceramics. 2. The ceramic injection molding method according to claim 1, further comprising controlling the injection speed of the molding material into the mold.
JP32693088A 1988-12-23 1988-12-24 Injection molding method of ceramics Granted JPH02171205A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP32693088A JPH02171205A (en) 1988-12-24 1988-12-24 Injection molding method of ceramics
US07/454,912 US5066449A (en) 1988-12-23 1989-12-22 Injection molding process for ceramics
DE3942686A DE3942686C2 (en) 1988-12-23 1989-12-22 Ceramic injection molding process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32693088A JPH02171205A (en) 1988-12-24 1988-12-24 Injection molding method of ceramics

Publications (2)

Publication Number Publication Date
JPH02171205A JPH02171205A (en) 1990-07-02
JPH0470122B2 true JPH0470122B2 (en) 1992-11-10

Family

ID=18193355

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32693088A Granted JPH02171205A (en) 1988-12-23 1988-12-24 Injection molding method of ceramics

Country Status (1)

Country Link
JP (1) JPH02171205A (en)

Also Published As

Publication number Publication date
JPH02171205A (en) 1990-07-02

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