JPH02265703A - Injection molding method - Google Patents

Injection molding method

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Publication number
JPH02265703A
JPH02265703A JP8581689A JP8581689A JPH02265703A JP H02265703 A JPH02265703 A JP H02265703A JP 8581689 A JP8581689 A JP 8581689A JP 8581689 A JP8581689 A JP 8581689A JP H02265703 A JPH02265703 A JP H02265703A
Authority
JP
Japan
Prior art keywords
viscosity
dry body
injection
injection molding
making
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
JP8581689A
Other languages
Japanese (ja)
Other versions
JPH0675855B2 (en
Inventor
Takashi Sugano
隆志 菅野
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.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP1085816A priority Critical patent/JPH0675855B2/en
Publication of JPH02265703A publication Critical patent/JPH02265703A/en
Publication of JPH0675855B2 publication Critical patent/JPH0675855B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To avoid blister involving to the utmost during the molding period by making the viscosity of a ceramic material dry body applied to an injection mold be in a specific range. CONSTITUTION:Upon injection-molding a ceramic material dry body in vacuum, the viscosity of the material dry body is adjusted to 10<2>-10<4> poise in the shear rate of 10<1>-10<2>sec<-1>. The adjustment in the viscosity of the material dry body can be done in controlling temperature of the material dry body and making the density of ceramic powder be of the order of 50-55vol.%. Although the ceramic dry body adjusted in a predetermined viscosity is supplied to an injection mold, at this time the injection mold is performed in making the temperature of a cylinder nozzle be of 130-200 deg.C, and also making the temperature of the die be of 20-90 deg.C. Besides, it is preferred to adopt 40-50cm<2>/sec in the injection speed and 370-1500kg/cm<2> in the injection dwelling pressure.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は射出成形方法、特にセラミックス原料坏土を真
空下に射出成形するに際し、泡の巻き込みを極力少なく
し得る方法に係るものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to an injection molding method, and particularly to a method that can minimize the inclusion of bubbles when injection molding ceramic raw material clay under vacuum.

[従来の技術] セラミックスの成形手段は種々提案され、又実施されて
いるが、とりわけ精密かつ複雑な形状の成形には射出成
形が採用される。
[Prior Art] Various methods for molding ceramics have been proposed and implemented, and injection molding is particularly used for molding precise and complicated shapes.

とりわけ、高温・構造材料として使用される非酸化物系
セラミックスの成形体は精密且複雑な形状となる場合が
多く、このような成形方法として真空下における射出成
形が最適とされている。
In particular, molded bodies of non-oxide ceramics used as high-temperature/structural materials often have precise and complicated shapes, and injection molding under vacuum is considered to be the optimal molding method for such molding.

かかる成形法にあっては、成形体中に欠陥が生じない為
に種々の添加剤を添加したり、射出成形法自体を改良し
たりすることが行なわれている。
In such molding methods, various additives are added or the injection molding method itself is improved in order to prevent defects from occurring in the molded product.

[発明の解決しようとする課題] しかしながら、これら従来法にあっては、確かに射出成
形に供されるセラミックス原料坏土自体の性質を改善せ
しめることはできるが、実際の射出成形に際しては、真
空下に成形を行なうにも拘らず、大気中の空気を多少な
りとも巻き込み、これが成形品中に泡乃至空洞として残
留し、この部分が欠陥部となってしまう欠点を有してい
た。
[Problems to be Solved by the Invention] However, although these conventional methods can certainly improve the properties of the ceramic raw material clay itself used for injection molding, it is difficult to perform vacuum injection molding during actual injection molding. Even though the molding is carried out at the bottom, some air from the atmosphere is drawn in, which remains in the molded product as bubbles or cavities, resulting in defects in these areas.

[課題を解決しようとする為の手段] 本発明者は、上記欠点を排除すべく、かかる成形時にお
ける泡の巻き込みを極力避は得る手段を見出すことを目
的として種々研究、検討した結果、射出成形に供される
セラミックス原料坏土の粘度を特定な範囲とすることに
よりほぼ一義的に前記目的を達成し得ることを見出した
[Means for Solving the Problems] In order to eliminate the above-mentioned drawbacks, the present inventor conducted various research and examinations with the aim of finding a means to avoid entrainment of bubbles during molding as much as possible. It has been found that the above object can be almost uniquely achieved by adjusting the viscosity of the ceramic raw material clay used for molding to a specific range.

かくして本発明は、セラミックス原料坏土を真空下に射
出成形するに際し、原料坏土の粘度を10’ NlO”
5ec−’の剪断速度において102 〜10’ボイス
に調整せしめておくことを特徴とする射出成形方法を提
供するにある。
Thus, in the present invention, when injection molding the raw material clay for ceramics under vacuum, the viscosity of the raw material clay is reduced to 10'NlO''.
An object of the present invention is to provide an injection molding method characterized in that the shear rate is adjusted to 102 to 10' voices at a shear rate of 5 ec-'.

本発明において原料坏土の粘度が前記範囲に満たない場
合には可塑剤や滑剤等の揮発による発泡が多くなり、逆
に前記範囲を超える場合には金型の形状、寸法を忠実に
転写できず、必要とする寸法精度を満足できなくなるの
で何れも不適当である。
In the present invention, if the viscosity of the raw clay is less than the above range, foaming will increase due to volatilization of plasticizers, lubricants, etc., whereas if it exceeds the above range, the shape and dimensions of the mold may not be faithfully transferred. First, both are inappropriate because the required dimensional accuracy cannot be satisfied.

そしてこれら範囲のうち、lO1〜10’ボイスを採用
する場合には、可塑剤や滑剤の発泡を実質的に防止し得
るので特に好ましい、実際、原料坏土の粘度を前記範囲
に調整せしめる手段としては種々の方法を採用し得る0
例えば、原料坏土の温度を制御したり、セラミックス粉
末の濃度を50〜55容量%程度に調整したり、バイン
ダーとなるポリエチレンやポリスチレン等の高分子融液
の粘度を調整し、たり、フタル酸エステルや脂肪酸エス
テル等の可塑剤やステアリン酸、ステアリルアルコール
、ステアリン酸エステル等の滑剤の添加量を制御したり
、更にはこれらの組み合わせにより坏土が本発明の所定
粘度になるように調整せしめる。
Among these ranges, it is particularly preferable to use lO1 to 10'voice because it can substantially prevent foaming of the plasticizer or lubricant. can adopt various methods 0
For example, controlling the temperature of raw clay, adjusting the concentration of ceramic powder to about 50 to 55% by volume, adjusting the viscosity of polymer melt such as polyethylene or polystyrene that serves as a binder, and By controlling the amount of plasticizers such as esters and fatty acid esters, and lubricants such as stearic acid, stearyl alcohol, and stearic acid esters, or by combining these, the clay is adjusted to have the predetermined viscosity of the present invention.

又、所定粘度に調整されたセラミックス坏土は、射出成
形に供されるが、このときシリンダーノズルの温度を1
30〜200℃とし、又金型温度を20〜90℃として
射出成形を実施すると成形形状に関係なく本発明の目的
を達成し得るので好ましい。
Furthermore, the ceramic clay adjusted to a predetermined viscosity is subjected to injection molding, but at this time the temperature of the cylinder nozzle is lowered to 1.
It is preferable to perform injection molding at a temperature of 30 to 200°C and a mold temperature of 20 to 90°C, since the object of the present invention can be achieved regardless of the molded shape.

なお、この際射出速度は40〜50cm”/sec 、
射出保持圧力370〜1500kg/cm”を採用する
のが適当である。
In addition, the injection speed at this time is 40 to 50 cm"/sec,
It is appropriate to adopt an injection holding pressure of 370 to 1500 kg/cm.

本発明が適用されるセラミックスとしては特に制限はな
く、例えば窒化珪素、炭化珪素、窒化アルミニウム等の
非酸化物系セラミックス、アルミナ、ジルコニア等が挙
げられるが、とりわけ非酸化物系セラミックスの成形に
は最適である6本発明方法が適用されるセラミックス原
料中には、その池水発明の目的を阻害しない限り、適宜
な添加物、例えば金属粉末やウィスカー等を添加するこ
とができる。
The ceramics to which the present invention is applied are not particularly limited, and include, for example, non-oxide ceramics such as silicon nitride, silicon carbide, and aluminum nitride, alumina, and zirconia. 6. Appropriate additives such as metal powders and whiskers can be added to the ceramic raw material to which the method of the present invention is applied, as long as they do not impede the purpose of the invention.

[実施例] 比表面積17rrr/gを有する炭化珪素80重量%、
ポリエチレン5重量%、ポリエチレン5重量%、ステア
リン酸1重置%、脂肪酸エステル4重量%とを常温下に
十分混線せしめることによりlO1〜102sec””
の剪断速度において粘度が102〜10’ボイスのセラ
ミックス坏土を得た。
[Example] 80% by weight of silicon carbide having a specific surface area of 17rrr/g,
By sufficiently mixing 5% by weight of polyethylene, 5% by weight of polyethylene, 1% by weight of stearic acid, and 4% by weight of fatty acid ester at room temperature, 10 to 102 sec.
A ceramic clay having a viscosity of 102 to 10'voice was obtained at a shear rate of .

かかる坏土な150℃に加熱された口径6mmのシリン
ダーノズル(射出ノズル)から、外径150a+s 、
容積320ccの80℃に保持された円板状金型キャビ
ティー内に真空下に射出し、成形を行なった。
From a cylinder nozzle (injection nozzle) with a diameter of 6 mm heated to 150 ° C., an outer diameter of 150 a + s,
Molding was performed by injecting under vacuum into a disc-shaped mold cavity having a volume of 320 cc and maintained at 80°C.

この成形体は目視による表面の泡及びX線による内部の
泡は何れも認められなかった。
In this molded article, neither bubbles on the surface nor bubbles inside were observed by X-ray observation.

Claims (1)

【特許請求の範囲】 1、セラミックス原料坏土を真空下に射出成形するに際
し、原料坏土の粘度を10^1〜10^3sec^−^
1の剪断速度において、10^1〜10^4ポイズに調
整せしめておくことを特徴とする射出成形方法。 2、セラミックス原料坏土を真空下に射出成形するに際
し、原料坏土の粘度を10^−^1〜10^3sec^
−^1の剪断速度において10^2〜10^4ポイズに
調整し、シリンダーノズルの温度を130〜200℃に
、金型温度を20〜90℃に調整しつつ射出することを
特徴とする射出成形方法。
[Claims] 1. When injection molding the ceramic raw material clay under vacuum, the viscosity of the raw material clay is set to 10^1 to 10^3 sec^-^
An injection molding method characterized in that the shear rate is adjusted to 10^1 to 10^4 poise at a shear rate of 1. 2. When injection molding ceramic raw material clay under vacuum, the viscosity of raw material clay is 10^-^1~10^3sec^
- Injection characterized by adjusting the shear rate to 10^2 to 10^4 poise at a shear rate of ^1, and injecting while adjusting the temperature of the cylinder nozzle to 130 to 200 °C and the temperature of the mold to 20 to 90 °C. Molding method.
JP1085816A 1989-04-06 1989-04-06 Injection molding method Expired - Lifetime JPH0675855B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1085816A JPH0675855B2 (en) 1989-04-06 1989-04-06 Injection molding method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1085816A JPH0675855B2 (en) 1989-04-06 1989-04-06 Injection molding method

Publications (2)

Publication Number Publication Date
JPH02265703A true JPH02265703A (en) 1990-10-30
JPH0675855B2 JPH0675855B2 (en) 1994-09-28

Family

ID=13869382

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1085816A Expired - Lifetime JPH0675855B2 (en) 1989-04-06 1989-04-06 Injection molding method

Country Status (1)

Country Link
JP (1) JPH0675855B2 (en)

Also Published As

Publication number Publication date
JPH0675855B2 (en) 1994-09-28

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