JPH046521B2 - - Google Patents
Info
- Publication number
- JPH046521B2 JPH046521B2 JP13483388A JP13483388A JPH046521B2 JP H046521 B2 JPH046521 B2 JP H046521B2 JP 13483388 A JP13483388 A JP 13483388A JP 13483388 A JP13483388 A JP 13483388A JP H046521 B2 JPH046521 B2 JP H046521B2
- Authority
- JP
- Japan
- Prior art keywords
- clay
- mold
- molding
- ceramic
- permeable
- 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
Links
- 239000004927 clay Substances 0.000 claims description 66
- 238000000465 moulding Methods 0.000 claims description 57
- 239000000919 ceramic Substances 0.000 claims description 39
- 238000000034 method Methods 0.000 claims description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 24
- 238000002347 injection Methods 0.000 claims description 23
- 239000007924 injection Substances 0.000 claims description 23
- 239000000463 material Substances 0.000 claims description 18
- 238000004898 kneading Methods 0.000 claims description 14
- 239000000843 powder Substances 0.000 description 11
- -1 polyethylene Polymers 0.000 description 8
- 238000005245 sintering Methods 0.000 description 8
- 238000002156 mixing Methods 0.000 description 6
- 239000011230 binding agent Substances 0.000 description 5
- 238000005266 casting Methods 0.000 description 5
- 238000001746 injection moulding Methods 0.000 description 5
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 4
- 239000004810 polytetrafluoroethylene Substances 0.000 description 4
- 239000011148 porous material Substances 0.000 description 4
- 239000002270 dispersing agent Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- 239000004809 Teflon Substances 0.000 description 2
- 229920006362 Teflon® Polymers 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000005238 degreasing Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 150000001247 metal acetylides Chemical class 0.000 description 2
- 150000004767 nitrides Chemical class 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 2
- 229910010271 silicon carbide Inorganic materials 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 239000001993 wax Substances 0.000 description 2
- 230000037303 wrinkles Effects 0.000 description 2
- 239000002033 PVDF binder Substances 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 229910052581 Si3N4 Inorganic materials 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000011505 plaster Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920002620 polyvinyl fluoride Polymers 0.000 description 1
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 238000009849 vacuum degassing Methods 0.000 description 1
Landscapes
- Producing Shaped Articles From Materials (AREA)
Description
[産業上の利用分野]
本発明は、真空土練工程により調製されたセラ
ミツクス坏土を一旦坏土保持部に注入して保持し
た後、非透過性型の成形面の一部を水との接触角
が80度以上の材料から構成した成形型に加圧注入
することによるセラミツクスの成形方法及び成形
装置に関する。
[従来の技術]
従来より比較的複雑な形状を有するセラミツク
成形体の製造方法として、射出成形法、加圧鋳込
成形法及び湿式加圧成形法が知られている。
射出成形法は、セラミツク粉末とポリエチレ
ン、ポリスチレン等の樹脂及びワツクスから成る
有機バインダーを混合し、この混合原料を射出成
形機により成形し、得られた成形体を脱脂するこ
とによりセラミツク成形体を得る方法である。
加圧鋳込成形法は、セラミツク粉末、水と解膠
剤等の成形助剤を混合して泥漿とし、この泥漿を
鋳込型内に注入し、泥漿を加圧して鋳込成形する
ことによりセラミツク成形体を得る方法である。
また湿式加圧成形法は、セラミツク粉末、水と
バインダー等の成形助剤を混合混練して坏土と
し、この坏土を型内に入れて加圧成形することに
よりセラミツク成形体を得る方法である。
[発明が解決しようとする課題]
しかしながら、上記従来の射出成形法にあつて
は、射出成形で得られる射出成形体の脱脂工程に
長時間を要するという欠点がある。
また、加圧鋳込成形法では、成形後の保形性が
悪く、離型し難いばかりでなく、複雑な形状品は
型合わせの面よりスリツプ漏れを起しやすく、成
形時間に長時間を要する等の欠点がある。
さらに、湿式加圧成形法では離型し難く、クラ
ツクが発生しやすいという問題がある。
[課題を解決するための手段]
そこで本発明者は、上記の問題点に鑑み、鋭意
検討を重ねた結果、本発明に到達した。
即ち、本発明によれば、真空土練工程により調
製されたセラミツクス坏土を、一旦坏土保持部に
注入して保持した後、該セラミツクス坏土を、非
透過性型、または透過性型と非透過性型の組合せ
から成り、該非透過性型の成形面の一部を水との
接触角が80度以上の材料から構成した成形型に加
圧注入することを特徴とするセラミツクスの成形
方法、および、真空土練工程により調製されたセ
ラミツクス坏土を注入・保持するための注入・保
持手段と、該注入・保持手段からのセラミツクス
坏土を加圧・注入するための成形型であつて、非
透過性型、または透過性型と非透過性型の組合わ
せから成り、該非透過性型の成形面の一部を水と
の接触角が80度以上の材料から構成した成形型と
から成ることを特徴とするセラミツクスの成形装
置、が提供される。
本発明において、セラミツクス坏土を加圧注入
する成形型としては、非透過性型の成形面の一部
を水との接触角が80度以上の材料から構成してい
る。すなわち、非透過性型、または透過性型と非
透過性型の組合せから成る成形型において、非透
過性型の成形面の一部を例えば、ポリテトラフル
オルエチレン等のフツ素樹脂など、水との接触角
が80度以上、好ましくは85度以上、より好ましく
は90度以上の材料によつて形成することにより、
成形体との離型性が良くなるのである。
水との接触角が80度より小さいと、離型性が悪
くなる。特にセラミツクタービンローターの如き
複雑な形状物を成形する場合、水との接触角が90
度以上の材料を用いることは離型による欠損がな
い点から好ましい。
非透過性型の成形面の一部を構成する、水との
接触角が80度以上の材料としては、ポリテトラフ
ルオルエチレン、ポリフツ化ビニル、ポリフツ化
ビニリデン、ポリトリフルオルクロルエチレン、
テトラフルオルエチレン−パーフルオルアルキル
ビニールエーテル共重合体等のフツ素樹脂のほ
か、ポリプロピレン、各種ワツクス類、等が挙げ
られる。
また、前記材料により非透過性型の成形面の一
部を構成する手段としては、この材料で非透過性
型自体を作成してもよいが、経済性の面から非透
過性型の成形表面に被覆することにより行うこと
が好ましい。また、前記材料としてフツ素樹脂等
を用いれば、金属製の非透過製型にも容易に直接
被覆することができる。
また本発明で用いる透過製型としては、従来公
知のものが使用できる。透過性型は、空気の除去
を良くするため、通気性が良く、一方、型自体の
強度を保障し得るものであることが必要で、通
常、平均孔径が0.1〜50μmのものが使用される。
また、平均孔径が異なる型で成形面層を0.1〜50μ
mの孔径とし、下面層を50〜500μm程度の粗い
孔径とした組合せからなる二層構造の型も使用す
ることができる。透過性型の材質は限定されず、
吸水性のよい石膏の如き材質のほか、樹脂、、セ
ラミツクス、金属およびそれらの複合材料等を用
いることもできる。
また、本発明に使用する非透過性型としては従
来一般に使用されているものを用いることがで
き、例えば金型のほか合成樹脂型、ゴム型を用い
ることができる。
本発明に用いるセラミツクス坏土は、焼結助剤
を含むセラミツク粉末、成形助剤及び水から成る
ものである。
セラミツク粉末としては従来より知られている
アルミナ、ジルコニア等の酸化物のほか、いわゆ
るニユーセラミツクスとして知られている窒化珪
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。
焼結助剤としては特にその種類を限定されるも
のではなく、一般に知られているMg,Al,Y,
Ce,Zr,Sr,B,Ta等の酸化物、窒化物、炭化
物等の焼結助剤を用いることができ、使用するセ
ラミツク粉末により適宜選ばれる。
セラミツクス坏土の調合割合は、セラミツク粉
末100重量部、水10〜45重量部、成形助剤0.1〜30
重量部、好ましくはセラミツク粉末100重量部、
水15〜35重量部、成形助剤0.6〜15重量部である。
また、より好ましい水の配合割合は10〜25重量部
である。水の配合割合が10重量部未満の場合は混
練性が悪く、均質な成形用坏土が得られず、45重
量部を超えると得られる成形体の密度が低くなつ
て焼成収縮が大きくなり、寸法精度の高い製品を
得にくくなる。
一方バインダー、分散剤等の成形助剤が0.1重
量部未満であるとその効果がなく、30重量部を超
えると成形助剤の除去に時間がかかると共に製品
にクラツクが発生しやすくなり好ましくない。
真空土練工程によつてセラミツク坏土を調製す
る場合、真空土練機は一般に使用されているパツ
クミルとオーガーマシンとを組合わせた装置を使
用することができ、均質で欠陥のない坏土を得る
には、オーガースクリユー、柱環、口金等の構造
及び押出しスピード、坏土の温度調整等を考慮す
る必要がある。
真空土練工程の真空度は減圧状態であればよい
が、通常60cmHg以上が好ましい。減圧状態にな
ることによつて水の拡散が著しくなり、坏土の水
膜の生成が速くなつて均質な坏土が得られる。
又、セラミツクタービンホイールの如く高強度が
要求される製品には、坏土中の気泡が破壊発生の
原因となるため、真空度は70cmHg以上であるこ
とが好ましい。
次に本発明においては、真空土練工程により所
定に調整されたセラミツクス坏土を、一旦坏土保
持部に注入して保持させている。真空土練工程と
成形工程を分けることにより、加圧圧力を高くす
る、加圧注入スピードを速くする等の成形条件が
成形体にあわせて容易に設定でき、更に温度分布
差のない均質な坏土を準備することができ、成形
欠陥のない成形体を得ることができる。また、坏
土保持部の坏土接触部に水との接触角が80度以上
の材料を用いることにより、坏土保持部と坏土の
摩擦が少なくなり、圧力損失及び摩擦熱を小さく
することができ好ましい。
坏土保持部(即ち、注入・保持手段)としては
具体的にはプランジヤー式押出機が好ましく用い
られるが、その他通常のシリンダー等も用いるこ
とができる。
坏土保持部の成形型への注入口の大きさは、成
形体の形状・容積等によつてそれぞれ設定する必
要があり、坏土保持部と坏土の摩擦を小さくする
ため、注入口の大きさは大きいほうが好ましい。
一方、セラミツクス坏土の成形型への加圧圧力
としては、好ましくは5Kg/cm2以上、更に好まし
くは10Kg/cm2以上を用いる。圧力が5Kg/cm2より
小さいと、坏土が充填されなかつたり、また成形
体の密度が低くなつて変形を起し易い。
又、加圧圧力としては、700Kg/cm2を超える高
圧を用いることも可能であるが、高圧になること
により、成形型が大きく且つ重くなること、更に
成形機が大型化すること等から操作性が悪くな
る。このため700Kg/cm2以下で行なうことが好ま
しい。
セラミツクス坏土を成形型に注入する時の加圧
注入スピードは加圧注入スピード(cm3/sec)と
成形体表面積(cm2)との比(加圧注入スピード/
成形体表面積)が0.7以上乃至10以下であること
が望ましい。
上記の比が0.7未満では成形体の表面にクラツ
クやシワ等の欠陥が発生しやすい。一方、上記の
比が10が超えても成形は可能であるが、成形装置
が大型化するため操作性が悪く、また必要以上の
経費を要し経済的でない。
[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、本発明がこれら実施例に限定されないこ
とは明らかであろう。
実施例 1
焼結助剤を含むSiC粉末(平均粒径0.7μm)100
重量部に、水25重量部、成形助剤としてバインダ
ー5重量部、分散剤1重量部を調合し、加圧ニー
ダーにて混練した。その後表−1に示す真空度で
真空土練を行ない、60mm(φ)×100mm(長さ)の
坏土を揃々押出した。次に第1図に示すタービン
ローター(翼径85mmφ、翼高30mm)用の成形装置
の坏土保持部5に坏土保持部注入口11より前記
坏土9を注入後、加圧用ピストン8を降下させ、
坏土保持部注入口11を密閉後、排出口7より坏
土保持部5の真空脱気を行なつた。その後表−1
に示す加圧力により、注入口6〔12mm(φ)〕よ
り加圧注入を行ない、20秒後に離型し、表−1に
示すような成形体を得た。
なお、比較のため、真空土練を行なわず加圧ニ
ーダーにて混練しただけの坏土の成形及び第1図
に示す非透過性型1,3及び非透過性スライドコ
ア2の成形体面には、テフロン〔ポリテトラフル
オルエチレン、接触角(θ)108度〕コーテイン
グが施されていない場合の成形も同時に行い、表
−1に示すような成形体を得た。
次に、成形体を恒温恒湿器を用いて5℃/hrの
昇温をして100℃で5時間、湿度は98%から徐々
に低下させながら乾燥した。
表−1から明らかなように、本発明の成形方法
及び成形装置を用いることにより、成形体の離型
性がよく、外観クラツクおよび乾燥後のクラツク
もない良好な成形体が得られることがわかる。
[Industrial Field of Application] The present invention involves injecting ceramic clay prepared by a vacuum clay mixing process into a clay holding part and holding it therein, and then soaking a part of the molding surface of an impermeable mold with water. This invention relates to a method and apparatus for molding ceramics by pressure injection into a mold made of a material with a contact angle of 80 degrees or more. [Prior Art] Injection molding, pressure casting, and wet pressure molding are conventionally known methods for producing ceramic molded bodies having relatively complex shapes. In the injection molding method, a ceramic molded body is obtained by mixing ceramic powder with an organic binder consisting of a resin such as polyethylene or polystyrene and wax, molding this mixed raw material with an injection molding machine, and degreasing the obtained molded body. It's a method. The pressure casting method involves mixing ceramic powder, water, and molding aids such as deflocculants to form a slurry, injecting this slurry into a casting mold, and pressurizing the slurry for casting. This is a method for obtaining ceramic molded bodies. In addition, the wet pressure molding method is a method of obtaining a ceramic molded body by mixing and kneading ceramic powder, water, and molding aids such as a binder to form a clay, and placing this clay in a mold and press-molding it. be. [Problems to be Solved by the Invention] However, the conventional injection molding method described above has a drawback in that the degreasing process of the injection molded article obtained by injection molding requires a long time. In addition, with the pressure casting method, shape retention after molding is poor, and it is difficult to release from the mold. Products with complex shapes are more likely to slip and leak than the surface of the mold, and the molding time is long. There are drawbacks such as the need for Furthermore, the wet pressure molding method has the problem that it is difficult to release from the mold and cracks are likely to occur. [Means for Solving the Problems] In view of the above-mentioned problems, the inventors of the present invention have made extensive studies and have arrived at the present invention. That is, according to the present invention, after the ceramic clay prepared by the vacuum clay kneading process is once injected into the clay holding part and held, the ceramic clay is made into a non-permeable type or a permeable type. A method for molding ceramics comprising a combination of non-permeable molds, characterized in that a part of the molding surface of the non-permeable molds is injected under pressure into a mold made of a material having a contact angle with water of 80 degrees or more. , and an injection/holding means for injecting and holding the ceramic clay prepared by the vacuum clay kneading process, and a mold for pressurizing and injecting the ceramic clay from the injection/holding means. , a non-permeable mold, or a combination of a permeable mold and a non-permeable mold, with a part of the molding surface of the non-permeable mold made of a material having a contact angle with water of 80 degrees or more. Provided is a ceramics molding device characterized by the following. In the present invention, a part of the molding surface of the non-permeable mold is made of a material having a contact angle with water of 80 degrees or more as a mold for pressure-injecting ceramic clay. In other words, in a mold consisting of a non-permeable mold or a combination of a permeable mold and a non-permeable mold, a part of the molding surface of the non-permeable mold is made of water, such as a fluororesin such as polytetrafluoroethylene. By forming the material with a contact angle of 80 degrees or more, preferably 85 degrees or more, more preferably 90 degrees or more,
This improves the releasability from the molded body. If the contact angle with water is smaller than 80 degrees, mold release properties will be poor. Especially when molding complex shapes such as ceramic turbine rotors, the contact angle with water is 90°.
It is preferable to use a material with a strength higher than 100% because there will be no damage due to mold release. Materials that form part of the non-permeable molding surface and have a contact angle with water of 80 degrees or more include polytetrafluoroethylene, polyvinyl fluoride, polyvinylidene fluoride, polytrifluorochloroethylene,
Examples include fluororesins such as tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer, polypropylene, various waxes, and the like. In addition, as a means of constructing a part of the molding surface of the non-transparent mold using the above-mentioned material, the non-transparent mold itself may be created using this material, but from the viewpoint of economy, the molding surface of the non-transparent mold It is preferable to carry out this by coating. Furthermore, if a fluororesin or the like is used as the material, it can be easily directly coated on a metal non-transparent mold. Furthermore, as the transmission mold used in the present invention, conventionally known molds can be used. Permeable molds need to have good air permeability in order to improve air removal, while also ensuring the strength of the mold itself, and are usually used with an average pore diameter of 0.1 to 50 μm. .
In addition, molding surface layers with different average pore diameters of 0.1 to 50μ
It is also possible to use a mold with a two-layer structure consisting of a combination of a pore size of 50 m and a coarse pore size of about 50 to 500 μm in the lower layer. The material of the transparent type is not limited,
In addition to materials with good water absorption such as plaster, resins, ceramics, metals, composite materials thereof, etc. can also be used. Further, as the non-transparent mold used in the present invention, those conventionally and generally used can be used, and for example, in addition to a metal mold, a synthetic resin mold or a rubber mold can be used. The ceramic clay used in the present invention consists of ceramic powder containing a sintering aid, a forming aid, and water. Ceramic powders include conventionally known oxides such as alumina and zirconia, as well as nitrides such as silicon nitride, known as new ceramics, carbides such as silicon carbide, and composite materials thereof. be able to. The type of sintering aid is not particularly limited, and the commonly known sintering aids include Mg, Al, Y,
Sintering aids such as oxides, nitrides, and carbides of Ce, Zr, Sr, B, Ta, etc. can be used, and are appropriately selected depending on the ceramic powder used. The mixing ratio of ceramic clay is 100 parts by weight of ceramic powder, 10 to 45 parts by weight of water, and 0.1 to 30 parts by weight of molding aid.
parts by weight, preferably 100 parts by weight of ceramic powder,
15 to 35 parts by weight of water and 0.6 to 15 parts by weight of molding aid.
Further, a more preferable mixing ratio of water is 10 to 25 parts by weight. If the proportion of water is less than 10 parts by weight, the kneading properties will be poor and a homogeneous clay for molding will not be obtained; if it exceeds 45 parts by weight, the density of the resulting molded product will be low and the firing shrinkage will be large. It becomes difficult to obtain products with high dimensional accuracy. On the other hand, if the amount of molding aids such as binders and dispersants is less than 0.1 parts by weight, there is no effect, and if it exceeds 30 parts by weight, it will take time to remove the molding aids and the product will be prone to cracking, which is undesirable. When preparing ceramic clay using the vacuum clay kneading process, a vacuum clay kneading machine that combines a commonly used pack mill and an auger machine can be used to produce homogeneous and defect-free clay. To achieve this, it is necessary to consider the structure of the auger screw, pillar ring, die, etc., extrusion speed, temperature adjustment of the clay, etc. The degree of vacuum in the vacuum clay kneading step may be in a reduced pressure state, but it is usually preferably 60 cmHg or more. By being in a reduced pressure state, the diffusion of water becomes significant, the formation of a water film on the clay becomes faster, and a homogeneous clay is obtained.
Furthermore, for products requiring high strength such as ceramic turbine wheels, the degree of vacuum is preferably 70 cmHg or higher, since air bubbles in the clay may cause breakage. Next, in the present invention, the ceramic clay adjusted to a predetermined value by the vacuum clay kneading process is once injected into the clay holding part and held therein. By separating the vacuum clay kneading process and the molding process, molding conditions such as increasing the pressure and pressure injection speed can be easily set according to the molded product, and it is also possible to create a homogeneous mold with no difference in temperature distribution. Soil can be prepared and a molded body without molding defects can be obtained. In addition, by using a material with a contact angle of 80 degrees or more with water for the clay contacting part of the clay holding part, the friction between the clay holding part and the clay is reduced, reducing pressure loss and frictional heat. This is preferable. Specifically, a plunger type extruder is preferably used as the clay holding part (ie, injection/holding means), but other ordinary cylinders and the like can also be used. The size of the injection port of the clay holding part into the mold needs to be set depending on the shape and volume of the molded object.In order to reduce the friction between the clay holding part and the clay, the size of the injection port The larger the size, the better. On the other hand, the pressure applied to the ceramic clay mold is preferably 5 kg/cm 2 or more, more preferably 10 kg/cm 2 or more. If the pressure is less than 5 Kg/cm 2 , the clay may not be filled or the density of the molded product will be low, making it easy to deform. It is also possible to use a high pressure of over 700 kg/cm 2 as the pressurizing pressure, but due to the high pressure, the mold becomes larger and heavier, and the molding machine becomes larger, so operation Sexuality becomes worse. For this reason, it is preferable to conduct the heating at 700 kg/cm 2 or less. The pressurized injection speed when injecting ceramic clay into a mold is the ratio of the pressurized injection speed (cm 3 /sec) to the molded object surface area (cm 2 ) (pressure injection speed /
The surface area of the molded product is desirably 0.7 or more and 10 or less. If the above ratio is less than 0.7, defects such as cracks and wrinkles are likely to occur on the surface of the molded product. On the other hand, even if the ratio exceeds 10, molding is possible, but the molding equipment becomes larger, resulting in poor operability, and unnecessarily high costs are required, which is not economical. [Examples] Hereinafter, the present invention will be explained in more detail based on Examples, but it will be clear that the present invention is not limited to these Examples. Example 1 SiC powder containing sintering aid (average particle size 0.7 μm) 100
To the weight part, 25 parts by weight of water, 5 parts by weight of a binder as a molding aid, and 1 part by weight of a dispersant were mixed, and the mixture was kneaded using a pressure kneader. Thereafter, vacuum clay kneading was performed at the degree of vacuum shown in Table 1, and clay of 60 mm (φ) x 100 mm (length) was extruded. Next, after injecting the clay 9 into the clay holding part 5 of the molding device for a turbine rotor (blade diameter 85 mmφ, blade height 30 mm) shown in FIG. 1 through the clay holding part injection port 11, the pressurizing piston 8 is lower it,
After the clay holding part inlet 11 was sealed, the clay holding part 5 was vacuum degassed from the discharge port 7. Then Table-1
Pressurized injection was carried out from the injection port 6 [12 mm (φ)] using the pressure shown in FIG. For comparison, molding of clay only kneaded with a pressure kneader without vacuum kneading, and the surfaces of the molded bodies of non-permeable molds 1 and 3 and non-permeable slide core 2 shown in FIG. Molding without Teflon coating (polytetrafluoroethylene, contact angle (θ) 108 degrees) was also conducted at the same time to obtain molded products as shown in Table 1. Next, the molded body was dried at 100° C. for 5 hours using a constant temperature and humidity chamber at a rate of 5° C./hr while the humidity was gradually lowered from 98%. As is clear from Table 1, it can be seen that by using the molding method and molding apparatus of the present invention, a molded product with good mold releasability and no cracks in appearance or cracks after drying can be obtained. .
【表】
*1 翼先端部2ケ所にわずかな未充填部あ
り
実施例 2
焼結助剤を含むSi3N4粉末(平均粒径1μm)
と、成形助剤、水を表−2に示すように調合し、
加圧ニーダーを用いて混練し、その後真空土練機
(真空度75cmHg)にて60mm(φ)×70mm(長さ)
の形状をした坏土を揃々押出した。次に第2図に
示す4枚の翼形状〔翼径90mm(φ)、翼高40mm〕
をした成形型の翼部10の表面に接触角の異なつ
た材料を固着させ、表−2に示す成形条件で前記
の如く調製された坏土9を用いて500Kg/cm2の圧
力で注入口6〔24mm(φ)〕より加圧注入し、10
秒後に離型して表−2に示すような成形体を得
た。
表−2から明らかなように、成形型表面に接触
角(θ)80度以上の材料を用いることにより良好
な成形体が得られることが判つた。又、さらに複
雑形状のタービンロータ等を成形する場合には、
より離型が困難となるため、僅かなカケも発生し
ない接触角(θ)90度以上の材料を用いることが
必要なことが明らかである。
次に成形体を恒温恒湿器を用いて5℃/Hrの
昇温をして100℃で5時間、湿度は98%から徐々
に低下させながら乾燥をした。次に、熱風循環式
電気炉を用い、500℃で10時間脱脂し、その後氷
のうに詰め、3トン/cm2の圧力にてラバープレス
成形をし、その後N2雰囲気中で1730℃にて1時
間の焼結を行ない、焼結体を得た。[Table] *1 There are slight unfilled areas at two blade tips Example 2 Si 3 N 4 powder containing sintering aid (average particle size 1 μm)
, a molding aid, and water were mixed as shown in Table 2,
Knead using a pressure kneader, then use a vacuum kneader (vacuum degree 75cmHg) to 60mm (φ) x 70mm (length)
We extruded clay having the shape of . Next, the four blade shapes shown in Figure 2 [blade diameter 90 mm (φ), blade height 40 mm]
Materials with different contact angles were fixed to the surface of the wing part 10 of the mold, and the injection port was placed at a pressure of 500 kg/cm 2 using the clay 9 prepared as described above under the molding conditions shown in Table 2. 6. Inject under pressure from [24mm (φ)], 10
The mold was released after a few seconds to obtain a molded product as shown in Table 2. As is clear from Table 2, it was found that a good molded product could be obtained by using a material with a contact angle (θ) of 80 degrees or more on the surface of the mold. In addition, when molding a turbine rotor etc. with a more complex shape,
It is clear that it is necessary to use a material with a contact angle (θ) of 90 degrees or more that does not cause even the slightest chipping, since it becomes more difficult to release from the mold. Next, the molded body was dried at 100° C. for 5 hours using a constant temperature and humidity chamber at a rate of 5° C./Hr while gradually lowering the humidity from 98%. Next, it was degreased at 500℃ for 10 hours using a hot air circulation electric furnace, then packed in ice packs and rubber press molded at a pressure of 3 tons/cm 2 , and then heated at 1730℃ in an N 2 atmosphere. Sintering was performed for 1 hour to obtain a sintered body.
【表】【table】
【表】
*1 翼先端部2ケ所にわずかなカケがあつた。
*2 翼先端部1ケ所にわずかなカケがあつた。
実施例 3
焼結助剤を含むSi3N4粉末(平均粒径0.8μm)
100重量部に水24重量部、成形助剤としてバイン
ダー3重量部、分散剤0.5重量部を調合し、加圧
ニーダーにて混練した。その後、真空土練(真空
度76cmHg)を行ない、60mm(φ)×300mm(長さ)
の坏土を押出した。次に第3図に示すテストピー
ス型(60mm×60mm)、第4図に示すピストンキヤ
ビテイー型(外径100mm(φ)×高さ25mm)及びタ
ービンローター型(翼径75mm(φ)、翼高35mm)
をそれぞれ成形装置にセツトし、前記調製された
坏土を坏土保持部注入口11より坏土保持部5に
注入後、加圧用ピストン8を降下させ、坏土保持
部注入口11を密閉後、排出口7より坏土保持部
5の真空脱気を行なつた。その後、表−3に示す
成形条件で注入口6より加圧注入を行ない、15秒
後に離型し、表−3に示すような成形条件にて成
形し、表−3に示す成形体を得た。
なお、非透過性型1,3及び非透過性スライド
コア2の成形体面には、テフロン〔ポリテトラフ
ルオルエチレン、接触角(θ)90度〕コーテイン
グが施してある。
表−3から明らかなように、本発明の成形方法
及び成形装置を用いることにより、成形体の離型
性がよく、外観クラツクのない良好な成形体が得
られることがわかる。
また、成形型の空気の抜けが悪い部分には透過
性型の設置のみ、あるいは、透過性型から真空脱
気することにより、外観上より良好な成形体が得
られることがわかる。
さらに、加圧注入スピード/成形体表面積が
0.7以上において外観クラツク、シワのない成形
体が得られることがわかる。[Table] *1 There were slight chips in two places on the tip of the wing.
*2 There was a slight chip on one part of the wing tip.
Example 3 Si 3 N 4 powder containing sintering aid (average particle size 0.8 μm)
100 parts by weight were mixed with 24 parts by weight of water, 3 parts by weight of a binder as a molding aid, and 0.5 parts by weight of a dispersant, and kneaded using a pressure kneader. After that, vacuum soil kneading (degree of vacuum 76cmHg) was performed, and the size was 60mm (φ) x 300mm (length).
The clay was extruded. Next, the test piece type (60 mm x 60 mm) shown in Fig. 3, the piston cavity type (outside diameter 100 mm (φ) x height 25 mm) shown in Fig. 4, and the turbine rotor type (blade diameter 75 mm (φ)), Wing height 35mm)
are respectively set in the molding device, and after injecting the prepared clay into the clay holding part 5 from the clay holding part injection port 11, the pressurizing piston 8 is lowered, and after sealing the clay holding part injection port 11. Then, the clay holding part 5 was vacuum degassed through the discharge port 7. Thereafter, pressurized injection was performed from the injection port 6 under the molding conditions shown in Table 3, the mold was released after 15 seconds, and molded under the molding conditions shown in Table 3 to obtain the molded product shown in Table 3. Ta. The molded surfaces of the non-transparent molds 1 and 3 and the non-transparent slide core 2 are coated with Teflon (polytetrafluoroethylene, contact angle (θ) 90 degrees). As is clear from Table 3, by using the molding method and molding apparatus of the present invention, molded products with good mold releasability and no appearance cracks can be obtained. It is also seen that a molded article with a better appearance can be obtained by only installing a transparent mold in areas of the mold where air escape is difficult, or by performing vacuum degassing from the transparent mold. Furthermore, the pressure injection speed/molded object surface area
It can be seen that a molded article with no cracks or wrinkles in appearance can be obtained at a value of 0.7 or higher.
【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
成形方法及び成形装置によれば、成形時間が短
く、成形時に漏れが生じず、さらに離型性が良
く、外観にクラツク、変形がない良好な成形体を
得ることができる。[Table] [Effects of the Invention] As explained above, according to the ceramic molding method and molding apparatus of the present invention, the molding time is short, no leakage occurs during molding, the mold releasability is good, and the appearance is improved. , a good molded product without deformation can be obtained.
第1図〜第4図はそれぞれ本発明の実施例であ
るセラミツクスの成形装置を示す断面図である。
1……非透過性型、2……非透過性スライドコ
ア、3……非透過性型、4……透過性型、5……
坏土保持部、6……注入口、7……排出口、8…
…加圧用ピストン、9……坏土、10……翼部、
11……坏土保持部注入口、12……排出口。
1 to 4 are cross-sectional views showing ceramic molding apparatuses that are embodiments of the present invention. 1... Non-transparent type, 2... Non-transparent slide core, 3... Non-transparent type, 4... Transparent type, 5...
Clay holding part, 6... Inlet, 7... Outlet, 8...
...pressurizing piston, 9... clay, 10... wing section,
11... Clay holding part inlet, 12... Outlet.
Claims (1)
坏土を、一旦坏土保持部に注入して保持した後、
該セラミツク坏土を、非透過性型、または透過性
型と非透過性型の組合せから成り、該非透過性型
の成形面の一部を水との接触角が80度以上の材料
から構成した成形型に加圧注入することを特徴と
するセラミツクスの成形方法。 2 真空土練工程により調製されたセラミツクス
坏土を注入・保持するための注入・保持手段と、
該注入・保持手段からのセラミツクス坏土を加
圧・注入するための成形型であつて、非透過性
型、または透過性型と非透過性型の組合わせから
成り、該非透過性型の成形面の一部を水との接触
角が80度以上の材料から構成した成形型とから成
ることを特徴とするセラミツクスの成形装置。[Claims] 1. Once the ceramic clay prepared by the vacuum clay kneading process is injected into the clay holding part and held,
The ceramic clay is made of a non-permeable type or a combination of a permeable type and a non-permeable type, and a part of the molding surface of the non-permeable mold is made of a material having a contact angle with water of 80 degrees or more. A ceramic molding method characterized by pressurized injection into a mold. 2. Injection/holding means for injecting/holding the ceramic clay prepared by the vacuum clay kneading process;
A mold for pressurizing and injecting the ceramic clay from the injection/holding means, which is composed of a non-permeable mold or a combination of a permeable mold and a non-permeable mold, and the molding die of the non-permeable mold. A ceramic molding device comprising a mold whose surface is partially made of a material having a contact angle with water of 80 degrees or more.
Priority Applications (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13483388A JPH01304902A (en) | 1988-06-01 | 1988-06-01 | Method and apparatus for forming ceramic |
| DE1989627185 DE68927185T2 (en) | 1988-06-01 | 1989-05-31 | Molding process and device for manufacturing ceramic objects |
| EP19890305442 EP0345022B1 (en) | 1988-06-01 | 1989-05-31 | Method for producing ceramics sintered article |
| EP91203145A EP0487172B1 (en) | 1988-06-01 | 1989-05-31 | Molding method and molding apparatus for producing ceramics |
| DE1989602279 DE68902279T2 (en) | 1988-06-01 | 1989-05-31 | METHOD FOR THE PRODUCTION OF SINTERED CERAMIC ITEMS. |
| US07/624,540 US5238627A (en) | 1988-06-01 | 1990-12-06 | Method for producing ceramics sintered article and molding method and molding apparatus to be used therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13483388A JPH01304902A (en) | 1988-06-01 | 1988-06-01 | Method and apparatus for forming ceramic |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01304902A JPH01304902A (en) | 1989-12-08 |
| JPH046521B2 true JPH046521B2 (en) | 1992-02-06 |
Family
ID=15137528
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13483388A Granted JPH01304902A (en) | 1988-06-01 | 1988-06-01 | Method and apparatus for forming ceramic |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01304902A (en) |
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|---|---|---|---|---|
| US9945613B2 (en) | 2012-09-20 | 2018-04-17 | Apple Inc. | Heat exchangers in sapphire processing |
| US10328605B2 (en) | 2014-02-04 | 2019-06-25 | Apple Inc. | Ceramic component casting |
-
1988
- 1988-06-01 JP JP13483388A patent/JPH01304902A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01304902A (en) | 1989-12-08 |
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