JPS60118664A - Dewaxing agent for ceramic injection formation - Google Patents
Dewaxing agent for ceramic injection formationInfo
- Publication number
- JPS60118664A JPS60118664A JP58226444A JP22644483A JPS60118664A JP S60118664 A JPS60118664 A JP S60118664A JP 58226444 A JP58226444 A JP 58226444A JP 22644483 A JP22644483 A JP 22644483A JP S60118664 A JPS60118664 A JP S60118664A
- Authority
- JP
- Japan
- Prior art keywords
- degreasing
- ceramic
- ceramic injection
- particle size
- molded body
- 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.)
- Pending
Links
Landscapes
- Compositions Of Oxide Ceramics (AREA)
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】 〔技術分野〕 本発明はセラミック射出成形用脱脂材に関する。[Detailed description of the invention] 〔Technical field〕 The present invention relates to a degreasing material for ceramic injection molding.
セラミック構造物を大量生産する方法として、射出成形
が用いられている。この射出成形let元来プラスチッ
クの成形方法の一種として発達したもので、成形材料を
射出成形機の射出シリンタ゛中で加熱溶融したのち、流
動化された成形材料を射出プランジャによって予め固く
閉じられた金形キャビティに射出注入して完全に充填し
、そこで冷却固化ないし硬化させて成形品とするもので
ある。Injection molding is used as a method for mass producing ceramic structures. Injection molding was originally developed as a type of plastic molding method, in which the molding material is heated and melted in the injection cylinder of an injection molding machine, and then the fluidized molding material is inserted into a mold tightly closed by an injection plunger. It is injected into a mold cavity to completely fill it, and then cooled and solidified or hardened to form a molded product.
セラミック構造物を製造するにあたっては、まずセラミ
ック粉末を有機粘結剤と混合し、これを上記射出成形に
より所定形状のセラミック射出成形体を成形する。次い
で、セラミック射出成形体から有機成分を流出、飛散さ
せる脱脂処理をおこなった後、所定温度に加熱して焼結
を行い、所望のセラミック構造物を得る。In manufacturing a ceramic structure, first, ceramic powder is mixed with an organic binder, and this is then injection molded to form a ceramic injection molded body of a predetermined shape. Next, a degreasing treatment is performed to cause organic components to flow out and scatter from the ceramic injection molded body, and then sintering is performed by heating to a predetermined temperature to obtain a desired ceramic structure.
ところで、上記セラミック構造物の製造工程において、
脱脂処理は重要な工程であり、通常セラミック射出成形
体を脱脂炉に入れ、不活性雰囲気中、1〜b
り行われる。このとき、セラミンク射出成形体から4!
1脂等の有機成分を流出、飛散させる一助として、脱脂
材(パッド材)を用いることがある。この脱脂材は通常
多孔質のセラミック材料からなり、セラミック射出成形
体から有機成分が円滑に除去されるのを補助する。By the way, in the manufacturing process of the above ceramic structure,
Degreasing is an important process, and is usually carried out by placing the ceramic injection molded body in a degreasing furnace in an inert atmosphere. At this time, 4! from the ceramic injection molded body!
A degreasing material (pad material) is sometimes used to help drain and scatter organic components such as 1 fat. This degreasing material is usually made of a porous ceramic material and assists in the smooth removal of organic components from the ceramic injection molded body.
従来、かかる脱脂材として、市販の粒径0.1μ〜lO
μの微粒脱脂材、または粒1!10μ〜1000μの粗
粒脱脂材が用いられている。Conventionally, as such degreasing materials, commercially available particle sizes of 0.1μ to 1O
A fine-grained degreasing material with a grain size of 1.10 to 1000 μm is used.
ところで、セラミック射出成形体を微粒脱脂材中に埋設
した状態で脱脂を行うと、ff11図に模式的に示すよ
うに、セラミック射出成形体lから流出した樹脂等の有
機成分は、セラミック射出成形体1表面近傍に有機成分
に富んだ領域A(有機成分リッチ領域)を形成し、その
周囲に有機成分の少ない領域B(有機成分プア領域)が
形成される。By the way, when degreasing is performed while a ceramic injection molded body is embedded in a fine degreasing material, as schematically shown in Fig. A region A rich in organic components (organic component rich region) is formed near one surface, and a region B rich in organic components (organic component poor region) is formed around it.
この有機成分リッチ領域Aが形成されると、セラミック
射出成形体1の有機成分が流出しにくくなり、分圧差等
により亀裂、フクレ等の発生することがある。この傾向
は、セラミック射出成形体1が厚肉の場合、または複雑
形状を有する場合に顕著となる。When this organic component rich region A is formed, it becomes difficult for the organic components of the ceramic injection molded body 1 to flow out, and cracks, blisters, etc. may occur due to partial pressure differences and the like. This tendency becomes remarkable when the ceramic injection molded body 1 is thick or has a complicated shape.
また、セラミック射出成形体1を粗粒脱脂材に埋設した
状態で脱脂を行うと、第2図に模式的に示すように、セ
ラミック射出成形体1から流出した有機成分は、有機成
分リンチ領域へと有機成分プア領域Bを形成する。第1
図との違いは、有機成分リッチ領域Aが狭く、かつ密度
が高いことである。この場合も、セラミック射出成形体
1内の有機成分の流出が阻害され、前述した欠陥を生じ
易い。Furthermore, when degreasing is performed while the ceramic injection molded body 1 is buried in a coarse degreasing material, the organic components flowing out from the ceramic injection molded body 1 are transferred to the organic component lynch region, as schematically shown in FIG. and an organic component poor region B is formed. 1st
The difference from the figure is that the organic component rich region A is narrower and has a higher density. In this case as well, the outflow of organic components within the ceramic injection molded body 1 is inhibited, and the above-mentioned defects are likely to occur.
以上より、欠陥を生じることなく脱脂を行うためには、
有機成分リッチ領域Aが形成されないことが必要である
と解され、かかる条件を満たす脱脂材の開発が望まれて
いた。From the above, in order to perform degreasing without causing defects,
It is understood that it is necessary that the organic component rich region A not be formed, and it has been desired to develop a degreasing material that satisfies this condition.
本発明は、上記従来技術の問題を解決するためになされ
たもので、セラミック射出成形体内の有機成分のl”l
?F’;な流出、飛散を促進し、欠陥のないセラミッ
ク脱脂体を得ることのできるセラミック射出成形用脱脂
材を提供することを目的とする。The present invention has been made to solve the problems of the prior art described above.
? An object of the present invention is to provide a degreasing material for ceramic injection molding that can promote the flow and scattering of F'; and obtain a defect-free ceramic degreased body.
かかる目的は、本発明によれば、セラミック材料からな
る粒径50μ〜2000μの脱脂材であって、
この脱脂材は、粒径0.1μ〜100μの細粒が寄り集
まった団粒構造を有することを特徴とするセラミック射
出成形用脱脂材によって達成される。According to the present invention, such a purpose is to provide a degreasing material made of a ceramic material with a particle size of 50μ to 2000μ, which has an aggregate structure in which fine particles with a particle size of 0.1μ to 100μ are gathered together. This is achieved by a degreasing material for ceramic injection molding characterized by the following.
本発明において、セラミック射出成形用脱脂材の材料と
しては、窒化珪素(′Si ) N 4) 、窒化アル
ミニウム(AIN) 、窒化硼素(BN)等の窒化物、
炭化珪素(SiC) 、炭化チタン(Tic)等の炭化
物、アルミナ(Al2O2)、ジルコニア(ZrO2)
、酸化チタン(TiO2)、酸化ハIJ ウA(B a
O)等の酸化物、硼化チタン(TiB 2 )、硼化
ジルコニウム(ZrBa)等の硼化物、サイアロン等の
酸窒化物、活性炭等を用いることができる。このとき、
セラミック射出成形体を構成するセラミック材料と同じ
材料または類似の材料を用いることが望ましい。In the present invention, the materials for the degreasing material for ceramic injection molding include nitrides such as silicon nitride ('Si)N4), aluminum nitride (AIN), and boron nitride (BN);
Carbides such as silicon carbide (SiC) and titanium carbide (Tic), alumina (Al2O2), zirconia (ZrO2)
, titanium oxide (TiO2), oxide oxide
Oxides such as O), borides such as titanium boride (TiB 2 ) and zirconium boride (ZrBa), oxynitrides such as Sialon, activated carbon, and the like can be used. At this time,
It is desirable to use the same or similar ceramic material that constitutes the ceramic injection molded body.
本発明において、セラミック射出成形用脱脂材の粒径と
しては50μ〜200011のものが望ましい。In the present invention, the particle size of the degreasing material for ceramic injection molding is preferably 50 μm to 200,011 μm.
また、この粒径50μ〜2000μのセラミ・ツク射出
成形用脱脂材は、その、粒径よりはるかに小さい粒径0
.1μ〜10.0μの一次粒子が、その元の形状を多分
に残した形で強固に結合した、いわゆる団粒構造を形成
していることが必要である。In addition, this degreasing material for ceramic injection molding with a particle size of 50μ to 2000μ has a particle size of 0, which is much smaller than the particle size.
.. It is necessary that primary particles of 1 μm to 10.0 μm form a so-called aggregate structure, in which the primary particles are firmly bonded together while retaining much of their original shape.
かかる団粒構造を有するセラミック射出成形用脱脂材の
製造方法としては、第3図にその概要を示すように、0
.1μ〜100μの一次粒子2を0゜1〜0.3%のポ
リビニルアルコール溶液3に入れ、十分攪拌した後、ス
プレードライヤ装置4に投入し造粒を行ってもよいしく
スプレードライヤ方式)、第4図にその概要を示すよう
に、0.1μ〜l000μの一次粒子2に水を加えて回
転させながら造粒し、ふるい6で50μ〜2000μの
範凹のものを取り出し、乾燥器7内で100〜200℃
で10〜20時間乾燥してもよい(ふるい方式)。As a method for producing a degreasing material for ceramic injection molding having such an aggregate structure, as shown in FIG.
.. Primary particles 2 of 1 μ to 100 μ are placed in a 0.1 to 0.3% polyvinyl alcohol solution 3, stirred thoroughly, and then put into a spray dryer device 4 for granulation (spray dryer method). As shown in Fig. 4, water is added to primary particles 2 of 0.1 μm to 1000 μm, granulated while rotating, particles with a diameter of 50 μm to 2000 μm are taken out with a sieve 6, and granulated in a dryer 7. 100~200℃
It may be dried for 10 to 20 hours (sieve method).
〔発明の作用〕
本発明のセラミック射出成形用脱脂材によれば、適度な
粒径を有するとともに、内部に、多数の細孔が形成され
ているため、セラミック射出成形体内部から流出した有
機成分は、セラミック射出成形体表面に滞って有機成分
リッチ領域を形成することなく、流出、飛散する。従っ
て、セラミック射出成形体内部の有機成分は流出を妨げ
られることがなく、円滑な脱脂が行われる。[Operation of the Invention] The degreasing material for ceramic injection molding of the present invention has an appropriate particle size and has a large number of pores formed inside, so that organic components flowing out from inside the ceramic injection molded body are removed. flows out and scatters without remaining on the surface of the ceramic injection molded body and forming an organic component-rich region. Therefore, the organic components inside the ceramic injection molded body are not prevented from flowing out, and smooth degreasing is performed.
本発明に係るセラミック射出成形用脱脂材によれば、脱
脂材粒子間の空隙、脱脂材内部の細孔率が適量に維持さ
れるため、有機成分す・ソチ領域の形成はなく円滑な有
機成分の流出、飛散が行われる。従って、脱脂時に発生
していた亀裂、フクレ等の欠陥は生じなくなり、健全な
セラミック脱脂体が得られる。According to the degreasing material for ceramic injection molding according to the present invention, the voids between the particles of the degreasing material and the porosity inside the degreasing material are maintained at an appropriate level, so there is no formation of an organic component layer and a smooth organic component. spills and scatters. Therefore, defects such as cracks and blisters that occur during degreasing no longer occur, and a healthy ceramic degreased body can be obtained.
次に、本発明の実施例について説明する。 Next, examples of the present invention will be described.
(第1実施例)
平均粒径0.9〜1.0μの窒化珪素粉末100部に対
し、ポリエチレン10部、エチルビニルアルコール12
部、可塑剤としてのジオキシフェニレン3部を180±
5℃に設定したニーダに没入し、40分程攪拌した後、
ニーダから取り出しペレタイザーで粗粉化した。次いで
、この粗粉化したペレットを140±2℃に設定された
2軸押し出し機に投入し、100cc/分の伏給璧で押
し出しを行い射出成形用ペレットを制作した。その後、
射出成形機にて射出温度180℃、型温50℃、射出圧
力900 kg/cm、射出率40cc/秒でプーリを
射出成形した。(First Example) 100 parts of silicon nitride powder with an average particle size of 0.9 to 1.0μ, 10 parts of polyethylene, 12 parts of ethyl vinyl alcohol
parts, 3 parts of dioxyphenylene as a plasticizer to 180±
After immersing it in a kneader set at 5℃ and stirring for about 40 minutes,
It was taken out from the kneader and coarsely powdered using a pelletizer. Next, the coarsely powdered pellets were put into a twin-screw extruder set at 140±2° C., and extrusion was performed at 100 cc/min with a downward feeder to produce pellets for injection molding. after that,
The pulley was injection molded using an injection molding machine at an injection temperature of 180°C, a mold temperature of 50°C, an injection pressure of 900 kg/cm, and an injection rate of 40 cc/sec.
次に、この射出成形体を脱脂炉に入れ、更に脱脂材を射
出成形体のまわりに充填した。このとき、脱脂材として
は、平均粒径が1μ(0,1〜10μの範囲の粒度分布
を示す)の窒化珪素粉末を一次粒子とし、前述のスプレ
ードライヤ方式で粒1.1100μ〜400μとしたも
のを用いた。次いで、脱脂炉内を加熱し、50℃〜50
0℃まで4゛C/h rの昇温速度で昇温させ脱脂を行
った。その後、1気圧の窒素ガス雰囲気中にて1750
℃で焼成を行った。Next, this injection molded body was placed in a degreasing furnace, and a degreasing material was further filled around the injection molded body. At this time, the primary particles of the degreasing material were silicon nitride powder with an average particle size of 1μ (showing a particle size distribution in the range of 0.1 to 10μ), and the particles were made into particles of 1.1100μ to 400μ using the above-mentioned spray dryer method. I used something. Next, the inside of the degreasing furnace is heated to 50°C to 50°C.
Degreasing was performed by raising the temperature to 0°C at a rate of 4°C/hr. After that, 1750°C in a 1 atm nitrogen gas atmosphere.
Calcination was carried out at ℃.
この結果得られた窒化珪素からなるプーリの良品率を調
べた。この良品率は、第5図に示すように、外部欠陥2
、内部欠陥3、内周欠陥4、総合の4点について調べた
。この結果を第1表に示す。The yield rate of pulleys made of silicon nitride obtained as a result was investigated. As shown in Fig. 5, this good product rate is
, internal defect 3, inner peripheral defect 4, and overall were investigated. The results are shown in Table 1.
(第2実施例)
脱脂材として、平均粒径が1μ(0,1μ〜10μの範
囲の粒度分布を示す)の窒化珪素粉末を一次粒子とし、
前述のふるい方式で粒径100μ〜400 itとした
ものを用いたこと以外は、第、l実施例と全く同じ条件
でプーリを製造した。この結果得られたプーリの良品率
を第1実施例と同様に第1表に示す。(Second Example) As a degreasing material, silicon nitride powder with an average particle size of 1μ (showing a particle size distribution in the range of 0.1μ to 10μ) was used as the primary particle,
A pulley was manufactured under exactly the same conditions as in Example 1, except that particles having a particle size of 100 μm to 400 it were used using the sieve method described above. The yield rate of the pulleys obtained as a result is shown in Table 1 as in the first example.
(第1比較例)
脱脂材として、平均粒径が1μ(0,1μ〜10μの範
囲の粒度分布を示す)の窒化珪素微粉を用いたこと以外
は、第1実施例と全く同じ条件でプーリを製造した。こ
の結果得られたプーリの良品率を第1実施例と同様に第
1表に示す。(First Comparative Example) A pulley was manufactured under exactly the same conditions as in the first example, except that silicon nitride fine powder with an average particle size of 1μ (showing a particle size distribution in the range of 0.1μ to 10μ) was used as the degreasing material. was manufactured. The yield rate of the pulleys obtained as a result is shown in Table 1 as in the first example.
(第2比較例)
脱脂材として、平均粒径が300μ(100μ〜500
μの粒度分布を示す)の窒化珪素粗粉を用いたこと以外
は、第1実施例と全く同じ条件でプーリを製造した。こ
の結果得られたブー!Jの良品率を第1実施例と同様に
第1表に示す。(Second Comparative Example) As a degreasing material, the average particle size is 300μ (100μ to 500μ).
A pulley was manufactured under exactly the same conditions as in Example 1, except that silicon nitride coarse powder having a particle size distribution of μ was used. The resulting boo! The good product rate of J is shown in Table 1 as in the first example.
第1表 各脱脂材による焼成良品率(N−100)第1
表から明らかなように、本発明に係るセラミック射出成
形用脱脂材を用いて脱脂した場合Gこは、従来の脱脂材
を用いた場合に比べ、良品率が大幅に向上しているのが
判る。Table 1: Firing good product rate (N-100) for each degreasing material 1st
As is clear from the table, when degreasing is performed using the degreasing material for ceramic injection molding according to the present invention, the yield rate is significantly improved compared to when conventional degreasing materials are used. .
第1図は従来の微粒脱脂材を用いて脱脂した場合の有機
成分の濃度割合を模式的に示す概略構成図、 第2図は
従来のネ■粒脱脂材を川0゛こ脱脂した場合の有機成分
の濃度割合を模式的に示す概略構成図、
第3図は本発明に係るセラミ・ツク射出成形用脱脂材の
製造方法の概略を示す]−程図、第4図は本発明に係る
セラミック射出成形用脱脂材の他の製造方法の概略を示
す工程図、第5図は本発明の実施例で製造したプーリの
各欠陥を示す概略構成図である。
■ −−−セラミック射出成形体
A −・有機成分リンチ領域
B−−−一有機成分プア領域
2−・−一次粒子
3− ・・ポリビニルアルコール溶液
4−一一一スプレードライヤ装置
5−−−−・脱脂材
6−・ふるい
7−・−・乾燥器
8−−−・外部欠陥
9−−m−・内部欠陥
10−m−内周欠陥
出願人 トヨタ自動胆未処も社
第1図
第2図Figure 1 is a schematic configuration diagram schematically showing the concentration ratio of organic components when degreasing using a conventional fine-grain degreaser, and Figure 2 shows the result when a conventional fine-grain degreaser is degreased with A schematic configuration diagram schematically showing the concentration ratio of organic components; FIG. 3 shows an outline of the method for producing a degreasing material for ceramic injection molding according to the present invention; FIG. 4 is a process diagram according to the present invention. FIG. 5 is a process diagram showing an outline of another manufacturing method of a degreasing material for ceramic injection molding, and FIG. 5 is a schematic diagram showing each defect in a pulley manufactured in an example of the present invention. - Ceramic injection molded body A - Organic component lynch region B --- One organic component poor region 2 -- Primary particles 3 -- Polyvinyl alcohol solution 4-11 Spray dryer device 5 ---・Degreasing material 6-・Sieve 7--・Dryer 8--・External defect 9--m-・Internal defect 10-m-Inner circumferential defect Applicant: Toyota Automobile Co., Ltd. Figure 1, Figure 2 figure
Claims (1)
μの脱脂材であって、 この脱脂材は、粒径0.1μ〜100μの細粒力〜寄り
集まった団粒構造を有することを特徴とするセラミック
射出成形用脱脂材。(1) Particle size 50μ to 2000 made of ceramic material
A degreasing material for ceramic injection molding, characterized in that the degreasing material has a grain size of 0.1 to 100 microns and a fine grain structure to a clustered aggregate structure.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58226444A JPS60118664A (en) | 1983-11-30 | 1983-11-30 | Dewaxing agent for ceramic injection formation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58226444A JPS60118664A (en) | 1983-11-30 | 1983-11-30 | Dewaxing agent for ceramic injection formation |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60118664A true JPS60118664A (en) | 1985-06-26 |
Family
ID=16845196
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58226444A Pending JPS60118664A (en) | 1983-11-30 | 1983-11-30 | Dewaxing agent for ceramic injection formation |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60118664A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5028367A (en) * | 1988-08-15 | 1991-07-02 | Rensselaer Polytechnic Institute | Two-stage fast debinding of injection molding powder compacts |
-
1983
- 1983-11-30 JP JP58226444A patent/JPS60118664A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5028367A (en) * | 1988-08-15 | 1991-07-02 | Rensselaer Polytechnic Institute | Two-stage fast debinding of injection molding powder compacts |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR0183997B1 (en) | Slip casting method | |
JPS6259564A (en) | Molding aid for ceramics, molded body obtained using the same and production of ceramic product | |
EP0487172A2 (en) | Molding method and molding apparatus for producing ceramics | |
WO1991012216A1 (en) | High density fused silica process and product | |
JPS60118664A (en) | Dewaxing agent for ceramic injection formation | |
JPS6172677A (en) | Dewaxing material for ceramic injection molding | |
JPS60118663A (en) | Manufacture of dewaxing agent for ceramic injection formation | |
US4970181A (en) | Process for producing ceramic shapes | |
KR100434830B1 (en) | Method for Manufacturing Homogeneous Green Bodies from the Powders of Multimodal Particle Size Distribution Using Centrifugal Casting | |
JPH0663684A (en) | Production of ceramic core for casting | |
JP3224645B2 (en) | Ceramics molding method | |
JPH06287055A (en) | Production of sintered article of ceramic | |
JPH07223879A (en) | Ceramic raw material | |
JPH03257081A (en) | Production of porous ceramics | |
JP3175455B2 (en) | Ceramics molding method | |
JPH05345304A (en) | Forming method for ceramic formed body | |
JPS60118675A (en) | Method of dewaxing ceramic injection formed body | |
JPH08108415A (en) | Ceramic molding method | |
JPH0881272A (en) | Preparation of binder for ceramic material,thermally processable material and inorganic sintered molding | |
US5514321A (en) | Reaction injection molding inorganics | |
JPS60171272A (en) | Manufacture of ceramic product | |
JPH04275101A (en) | Preparation of sintered ceramic compact | |
JPS63182251A (en) | Manufacture of ceramic powder formed body | |
JPH064503B2 (en) | Method for manufacturing ceramics sintered body | |
JPS61106464A (en) | Process for dewaxing ceramic injection molded body |