JPS6160802A - Powder injection molding method - Google Patents

Powder injection molding method

Info

Publication number
JPS6160802A
JPS6160802A JP59179359A JP17935984A JPS6160802A JP S6160802 A JPS6160802 A JP S6160802A JP 59179359 A JP59179359 A JP 59179359A JP 17935984 A JP17935984 A JP 17935984A JP S6160802 A JPS6160802 A JP S6160802A
Authority
JP
Japan
Prior art keywords
injection molding
powder
butanol
binder
water
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
Application number
JP59179359A
Other languages
Japanese (ja)
Inventor
Tsuneo Miyashita
恒雄 宮下
Hiroaki Nishio
浩明 西尾
Yasushi Ueno
康 上野
Shoji Kubodera
久保寺 正二
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP59179359A priority Critical patent/JPS6160802A/en
Priority to SE8502882A priority patent/SE459793B/en
Priority to GB08516576A priority patent/GB2163780B/en
Priority to DE19853525752 priority patent/DE3525752A1/en
Priority to FR8512879A priority patent/FR2569683A1/en
Publication of JPS6160802A publication Critical patent/JPS6160802A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F3/00Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
    • B22F3/22Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces for producing castings from a slip
    • B22F3/222Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces for producing castings from a slip by freeze-casting or in a supercritical fluid
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F1/00Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
    • B22F1/10Metallic powder containing lubricating or binding agents; Metallic powder containing organic material
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/622Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/622Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/626Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
    • C04B35/63Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B using additives specially adapted for forming the products, e.g.. binder binders
    • C04B35/632Organic additives

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Ceramic Engineering (AREA)
  • Structural Engineering (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Powder Metallurgy (AREA)
  • Compositions Of Oxide Ceramics (AREA)
  • Ceramic Products (AREA)
  • Mold Materials And Core Materials (AREA)
  • Producing Shaped Articles From Materials (AREA)
  • Devices For Post-Treatments, Processing, Supply, Discharge, And Other Processes (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】 〔産業上の利用分野〕 この発明は、金属粉およびセラミック粉の射出成形方法
に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for injection molding metal powder and ceramic powder.

〔従来の技術〕[Conventional technology]

2%Ni −98%Fe、 5US316、ステライト
、超硬合金等の金属粉およびアルミナ、炭化ケイ素、窒
化ケイ素、ジルコニア等のセラミック粉を出発原料とし
て複雑形状の成形体を製造する有効な方法として射出成
形プロセスが知られている。
Injection is an effective method for producing molded bodies with complex shapes using metal powders such as 2%Ni -98%Fe, 5US316, stellite, and cemented carbide, and ceramic powders such as alumina, silicon carbide, silicon nitride, and zirconia as starting materials. Molding processes are known.

これら射出成形法は次の4つの工程から成り立っている
。即ち (11原料粉を有機バインダーと混合して熱可塑性混合
物とする。
These injection molding methods consist of the following four steps. That is, (11 raw material powder is mixed with an organic binder to form a thermoplastic mixture.

(2)加熱シリンダー中で混合物を軟化させたのち金型
中へ加圧しながら射出する。
(2) After the mixture is softened in a heating cylinder, it is injected into a mold while being pressurized.

(3)金型を開いて成形体を取り出す。(3) Open the mold and take out the molded object.

(4)成形体から有機バインダーを除去後、焼成し高密
度化をはかる。
(4) After removing the organic binder from the compact, it is fired to increase the density.

以上の工程から成る射出成形法の、謔は、バインダーが
握っておシ、上記工程の成否を左右するものである。バ
インダーは、粉体に成形性を付与するために、添加され
るものであり、成形性が不良だと成形体に銀状痕、溶接
線、引は等による欠陥を生ずる。
The key to the injection molding method, which consists of the above steps, is the binder, which determines the success or failure of the above steps. A binder is added to impart moldability to the powder, and if the moldability is poor, defects such as silver marks, weld lines, cracks, etc. will occur in the molded product.

成形性を向上させるためには多1aのバインダー添加が
必要であるが、反面バインダー責の増加に伴なってバイ
ンダーを除去する脱脂工すMで成形体に亀裂、発泡、変
形などの欠陥を生じ易くなるので、バインダー没を必要
最小限に抑えると共に、脱脂工程で欠陥を生じない特性
を有するバインダーの探索が従来から行なわれてきた。
In order to improve moldability, it is necessary to add a binder of 1a, but on the other hand, as the binder load increases, defects such as cracks, foaming, and deformation may occur in the molded product during degreasing to remove the binder. Therefore, searches have been made for binders that have characteristics that minimize binder sinkage and do not cause defects during the degreasing process.

現在、一般的に、バインダーとしては、低分子量ポリエ
チレン、ポリスチレン、パラフィン、微細結晶ワックス
に1熱可塑性樹脂やオイル等を少量添加したものが使わ
れている。
Currently, binders generally used include low molecular weight polyethylene, polystyrene, paraffin, and microcrystalline wax with a small amount of thermoplastic resin, oil, etc. added thereto.

マタフロピレン、ボ)1ビニルアルコール、ポリビニル
ブチラール、ポリエチレングリコール、メチルセルロー
ス、ヒドロ牛ジプロピル音メチルセルロース、カルボキ
シ・メチルセルロース、アタクテイソク・ポリエチルセ
ルロース、ヒドロキシ・エチルセルロース等もバインダ
ーとして知られている。
Mataflopyrene, vinyl alcohol, polyvinyl butyral, polyethylene glycol, methyl cellulose, hydrodipropyl methyl cellulose, carboxy methyl cellulose, polyethyl cellulose, hydroxy ethyl cellulose, etc. are also known as binders.

成形品のh型を容易にするためにステアリン酸をバイン
ダー中に少量混合しておくことについても知られている
It is also known to incorporate small amounts of stearic acid into the binder to facilitate the h-shape of the molded article.

〔発明がy@決しようとする問題点〕[Problems that the invention attempts to solve]

粉体の射出成形法における脱脂工程においては、通常、
成形体を常温から400〜500℃まで加熱することに
よって、バインダーを分解させ蒸発除去する方法が採用
されている。この場合、成形体を最高温度まで、ゆり〈
シ加熱して、バインダーが分解して発生する蒸気の発生
速度が、成形体内の空隙を逼って外部へ放出する速度を
上廻らないようにすることが必須である。そうしないと
、成形体内で蒸気圧が高まって、亀裂、発泡、変形を生
ずることとなる。このため、この工程は、70〜100
時間を要し、射出成形性本来の高生産性の利点を損なっ
ている。これが粉体の射出成形法の最大の第1の問題点
である0 次に第2の問題点として400〜500℃まで長時間加
熱することKよる熱エネルギーの浪費があシ、これは低
温エネルギーのため、経済的に有効熱エネルギーとして
回収することを困MKさせている。
In the degreasing process in powder injection molding,
A method has been adopted in which the binder is decomposed and removed by evaporation by heating the molded body from room temperature to 400 to 500°C. In this case, the molded body is heated to the maximum temperature,
It is essential that the rate of generation of steam generated by decomposition of the binder during heating does not exceed the rate at which it fills the voids within the molded body and is released to the outside. Otherwise, vapor pressure will build up within the molded body, resulting in cracking, foaming, and deformation. Therefore, this process requires 70 to 100
This takes time and detracts from the inherent high productivity advantages of injection molding. This is the first and biggest problem of the powder injection molding method.Next, the second problem is that heating to 400-500℃ for a long time results in wasted thermal energy, which is low-temperature energy. This makes it difficult to economically recover it as effective thermal energy.

また上述のように脱脂はバインダーの熱分解に依存して
いるが、完全な脱脂は困難であり、成形体内に1炭素や
油脂が少量残留するのが普通である。これが焼成後の成
品性状を損なプ原因となることがあシ、これが第5の問
題点である。
Further, as mentioned above, degreasing depends on thermal decomposition of the binder, but complete degreasing is difficult, and it is common for a small amount of carbon and oil to remain in the molded body. This may cause deterioration of the properties of the product after firing, which is the fifth problem.

第4に、脱脂工程で回収された油脂は、バインダーの分
解生成物なのでバインダーとしての再使用は不可能であ
り、通常廃棄され、これが成形成品コストを上昇させる
一因となっている。
Fourth, since the fats and oils recovered in the degreasing process are decomposition products of the binder, they cannot be reused as a binder and are usually discarded, which is one of the reasons for increasing the cost of formed products.

上述の如き問題点を解決する方法として、水冷凍射出成
形法が知られている。この方法は、バインダーとして水
を用いることを特徴とし、同法は、例えば1μm以下の
アルミナ粉に約40容1ft%の水を混合して、常温で
粉体に可塑性を持たせて、こ、れを−5〜−10℃に冷
却した金型内に射出して、水の冷凍によって、成形体く
強度を付与し、型開きを行なって成形体を取出す。この
とき冷凍によって離型が容易となる効果がある。
A water freezing injection molding method is known as a method for solving the above-mentioned problems. This method is characterized by using water as a binder, and in this method, for example, approximately 40 volume 1 ft% of water is mixed with alumina powder of 1 μm or less to give the powder plasticity at room temperature. The mixture is injected into a mold cooled to -5 to -10°C, the molded product is given strength by freezing water, and the molded product is removed by opening the mold. At this time, freezing has the effect of facilitating release from the mold.

ついで成形体の脱水を行なう。水の飽和蒸気圧は25℃
で25−Hりであり、従来の有機バインダーと比較して
極めて高いので、常温で水分の大部分を蒸発除去するこ
とができ、自然乾燥も可能である。脱水速度を上げるた
めに真空乾燥も有効であシ、若干の加熱を行なうことに
よシ脱水時間を短縮することもできる。
The molded body is then dehydrated. The saturated vapor pressure of water is 25℃
Since it has a 25-H content, which is extremely high compared to conventional organic binders, most of the water can be removed by evaporation at room temperature, and natural drying is also possible. Vacuum drying is also effective in increasing the dehydration rate, and dehydration time can also be shortened by applying slight heating.

このようにして、この方法は、従来の射出成形法の脱脂
時間が畏すぎるという問題点を解決した。
In this way, this method solves the problem that the degreasing time of the conventional injection molding method is too long.

この方法は高温加熱が不要なので熱エネルギー的にも有
利でちゃ、また水は有機バインダー〈比べて安価であり
、必要に応じて回収再利用もできる。
This method does not require high-temperature heating, so it is advantageous in terms of thermal energy.Water is also cheaper than organic binders, and can be recovered and reused if necessary.

以上のように水冷凍射出成形法は、数多くの利点をもっ
ているが、しかし水を使用することKよシ、対象材料が
限定されるという欠点がある。即ち、金M粉の多くは水
との接触によって酸化し易く、生成した酸化物は金属粉
の焼結を阻害するので成形体の強度、靭性に問題が生ず
る。またセラミック粉のように粒子が微細化すると水分
の吸着量が増加するばかpでなく、特に結合エネルギー
の大きな活性部分に吸着されるOH−イオン量が急増す
る。そのため粒子が、微細化する桿菌温度にならなけれ
ば除去できないOH−イオンが増加することになる。
As described above, the water-refrigeration injection molding method has many advantages, but it also has the disadvantage that it uses water and is limited in the materials that can be used. That is, most of the gold M powder is easily oxidized by contact with water, and the generated oxides inhibit the sintering of the metal powder, causing problems in the strength and toughness of the molded body. Furthermore, when the particles become fine like ceramic powder, not only does the amount of moisture adsorbed increase, but also the amount of OH- ions adsorbed to active portions with particularly large binding energy rapidly increases. Therefore, OH- ions, which cannot be removed unless the particles reach the rod temperature at which they become fine, increase.

強力に吸着したOH−イオンを含む粒子は、一般に焼結
を15g害する。マグネシア粉では吸着しfcOH−″
イオンが焼結の過程で異常粒成長をひき起すことが知ら
れている。また窯化ケイ素は、吸着水分と反応してアン
モニアを放出しシリカr/C変わることも知られている
。炭化タングステンも1200℃付近で吸着水分と反応
して、水素と一酸化炭素を放出する。以上のように水分
の吸NKよって変質する材料については水冷採決による
射出成形は適用できない。
Particles containing strongly adsorbed OH-ions generally impair sintering by 15 g. Magnesia powder adsorbs fcOH-''
It is known that ions cause abnormal grain growth during the sintering process. It is also known that silica reacts with adsorbed moisture to release ammonia and convert into silica r/C. Tungsten carbide also reacts with adsorbed moisture at around 1200°C, releasing hydrogen and carbon monoxide. As mentioned above, injection molding using water cooling cannot be applied to materials that change in quality due to absorption of moisture.

この発明は以上の如き水冷採決による射出成形法の欠点
を解消すべくなされたものであり、バインダーが金属お
よびセラミック粉を汚染せず、また成形後容易にバイン
ダーが除去できる粉体の射出成形法を提供することを目
的とするものである。
This invention was made in order to solve the above-mentioned drawbacks of the injection molding method using water-cooling, and provides a powder injection molding method in which the binder does not contaminate metal and ceramic powder, and the binder can be easily removed after molding. The purpose is to provide the following.

C問題点を解決するための手段〕 前記問題点を解決するために1本発明では、水冷凍射出
成形法の水の代シに1第3ブタノール(CH3)3 C
0H(2,メチka2プロパツール)をバインダーとし
て使用することを特徴とするものである。
Means for Solving Problem C] In order to solve the above problems, the present invention uses tertiary butanol (CH3)3C as a substitute for water in the water freezing injection molding method.
It is characterized by using 0H (2, Methi ka2 Proper Tool) as a binder.

冷凍射出成形用バインダーとして、第3ブタノールは水
に優る性状を有する0即ち第6ブタノールの密度は25
℃で0.71/、−jで水の78チ1分子]d74.1
2で水の4.1倍ある。従って、単位体!Rあた夛の%
A、数は、水Ob、56 X 10−” P mot/
As a binder for frozen injection molding, tertiary butanol has properties superior to water.
0.71/1 molecule of water at -j] d74.1
2, which is 4.1 times that of water. Therefore, unit body! % of R heat
A, number is water Ob, 56 X 10-” P mot/
.

cAVc対して第6ブタノールは1.05 x 10−
” pm”/iであシ約5分の1である。これは、第5
ブタノールによって原料粉の粒子間を埋めると、脱バイ
ンダ一時に発生するガス量は水の場合の5分の1にしか
すぎないことを意味する。この点は脱バインダ一時間の
短縮にとって極めて有利である。
For cAVc, 6th butanol is 1.05 x 10-
"pm"/i is about one-fifth. This is the fifth
This means that when butanol fills the spaces between particles of raw material powder, the amount of gas generated during binder removal is only one-fifth of that in the case of water. This point is extremely advantageous in reducing the debinding time by one hour.

ま次第6ブタノールの融点は25.66℃であり室温に
近いので、冷水循環による冷凍が可能であり、水のよう
に特別な冷凍設備が不要である。また水の凝固熱79.
4  /c4 tc対して、第6ブタノールの凝固熱は
17.1 d/d で約4.6分の1にしかすぎないの
で、これはエネルギー消費の観点から第3ブタノールを
更く有利にする。
Since the melting point of 6-butanol is 25.66°C, which is close to room temperature, it can be frozen by circulating cold water, and unlike water, special freezing equipment is not required. Also, the heat of solidification of water79.
4/c4 tc, the heat of solidification of 6-butanol is only about 4.6 times lower at 17.1 d/d, which makes tert-butanol even more advantageous from an energy consumption point of view. .

次に第6ブタノールの蒸気圧は25℃で45aH2であ
シ、水の25flHyより高い。これは脱バインダーの
容易さの点から第6ブタノールは水より有利であり、ま
た25℃の水の蒸発熱586′/−に対して、第5ブタ
ノールの蒸発熱は118−/−で約5分の1と極めて小
さく、と71.は脱バインダー所要エネルギーが水に比
べて極めて少ないことを意味する。
Next, the vapor pressure of 6-butanol is 45aH2 at 25°C, which is higher than 25flHy of water. This is because 6th butanol is more advantageous than water in terms of ease of debinding, and the heat of vaporization of water at 25°C is 586'/-, whereas the heat of vaporization of 5th butanol is 118'/-, which is approximately 5. Extremely small, 1/71. means that the energy required for debinding is extremely small compared to water.

@5ブタノールも常温付近の脱バインダー後一部が粉体
表rfJ′VC吸着する。この場合水がO)rイオンで
吸!−jるのに対して、第5ブタノールはアルキル基で
吸着する◇アルキル基はOH−イオンと違って比較的に
脱Nが容易であり、成形体の焼結に悪影響を及を重さな
い。
A part of @5-butanol also adsorbs rfJ'VC on the powder surface after debinding at room temperature. In this case, water absorbs O)r ions! In contrast, 5-butanol is adsorbed by alkyl groups. ◇Unlike OH- ions, alkyl groups are relatively easy to de-N, and do not adversely affect the sintering of the compact. .

また、第6ブタノールは安定な単一成分の物質であり、
常温付近の蒸発・凝縮、凝固によって分解、劣化は殆ん
どないので回収し再使用することができる。この点は水
と[el様に従来の有機バインダーに比べて甚だ経済的
に有利である。
In addition, 6-butanol is a stable single-component substance,
There is almost no decomposition or deterioration due to evaporation, condensation, or solidification at room temperature, so it can be recovered and reused. This point is extremely economically advantageous compared to conventional organic binders such as water and [EL].

これら第6ブタノールのバインダー量は、適用粉体の粒
度分布に王として依存する。バインダーは粒子間の空隙
を完全に満たす必要かあり、更に経験的に数容積%を上
載せした倉が必要である。
The amount of these 6-butanol binders depends largely on the particle size distribution of the applied powder. It is necessary that the binder completely fills the voids between the particles, and empirically, it is necessary to add several vol.% of the binder.

バインダー量が60容積−未満であると射出に適した流
動特性が得られず、55容撰チ多すぎるとバインダー除
去に時間がかかるのみならず欠陥を生じ易いので、バイ
ンダー1kFi30〜55容槓チであることが必要であ
る。
If the amount of binder is less than 60 volume, flow characteristics suitable for injection cannot be obtained, and if the amount is too large, it will not only take time to remove the binder but also cause defects. It is necessary that

また加熱シリンダー内での混合物の加熱温度は26〜4
0℃であることが必要である。何故ならば、第3ブタノ
ールの融点は25.66℃なので、この温度以上に保持
し溶融状態にする必要があり、また40℃以上に加熱す
ると、第6ブタノールの蒸気圧が高まり、放散損失の増
加が問題となるからである。
Also, the heating temperature of the mixture in the heating cylinder is 26 to 4
It is necessary that the temperature is 0°C. This is because the melting point of tertiary butanol is 25.66°C, so it is necessary to maintain it above this temperature to make it molten. Also, heating it above 40°C increases the vapor pressure of 6th butanol, which reduces dissipation loss. This is because the increase becomes a problem.

金型内における成形体の冷却く関しては、少くとも成形
体表面を融点以下に保って、凍結する必要があるので2
5℃以下とする。然し冷却温度が低すぎると、後工程の
脱バインダーの速度が低下するので望ましくない。また
単純水冷では不十分となシ、特別の冷熱源が必要となる
ので金型を冷却して少なくとも成形体の温度を5〜25
℃t14整する必要がある。
Regarding cooling of the molded object in the mold, it is necessary to keep the surface of the molded object at least below the melting point and freeze it.
Keep the temperature below 5℃. However, if the cooling temperature is too low, the rate of binder removal in the subsequent step will decrease, which is not desirable. In addition, simple water cooling is not sufficient, and a special cold source is required, so the mold is cooled to at least bring the temperature of the molded object to 5 to 25 degrees.
It is necessary to adjust the temperature at ℃t14.

第6ブタノールで凍結した成形体の離型は良好であるが
、従来の粉体射出成形方法と同様に離型剤として例えば
ステアリン酸をあらかじめ混合すると、更に良好な離型
が可能である。
Although mold release of molded bodies frozen with 6-butanol is good, even better mold release is possible if, for example, stearic acid is mixed in advance as a mold release agent, as in conventional powder injection molding methods.

以上の如く本発明の要旨は、金属粉およびセラミックス
粉の射出成形において30〜55容積−の第6ブタノー
ルを前記金属粉およびセラミックス粉と混合し、該混合
物を第5ブタノールの融点以上の温JICy4贅し、つ
いで前記混合物を、冷却された金型内に射出し、成形保
持したのち、得られた成形体の表面温度を第6ブタノー
ルの融点以下にして該成形体内の第5ブタノールを凍結
せしめ、成形体を取り出すことを特徴とする粉体の射出
成形方法である。
As described above, the gist of the present invention is to mix 30 to 55 volumes of 6-butanol with the metal powder and ceramic powder in injection molding of metal powder and ceramic powder, and to mix the mixture with JICy4 at a temperature above the melting point of the 5-butanol. Then, the mixture is injected into a cooled mold and held in the mold, and the surface temperature of the obtained molded body is lowered to below the melting point of 6th butanol to freeze the 5th butanol in the molded body. , a powder injection molding method characterized by taking out a molded body.

本発明の実施例を以下〈述べる。Examples of the present invention will be described below.

〔実施例〕 平均粒間径0.75μmo窒化ケイ素扮と焼結助剤とし
てY2O2(6重ik%)とA1103  (2重量%
)を調製し、この原料粉60容量%に対して、I¥6ブ
タノール粉40容槓チを調製する。
[Example] Silicon nitride with an average intergranular diameter of 0.75 μmo and Y2O2 (6 weight%) and A1103 (2 weight%) as sintering aids.
) and prepare a 40 volume mound of 1 yen butanol powder for 60% by volume of this raw material powder.

こ力、をニーダ−に装入し、望素雰囲気としたのち、混
練を開始する。ニーダ−の混合槽内壁は電熱ヒータ或は
温媒ヒータにより50℃に制御することKよって、第6
ブタノールは溶解し混線は進行する。混線開始して12
時間後、ヒータ電源を切り、混合槽とブレードに装着さ
れたジャケットに20℃の冷水を通し、冷却しながら5
0分間混線を続ける。この間に第6ブタノールは凍結し
、原料粉のバインダーとなってベレット状の混合物とな
る。このペレットを取出してスクリューインライン式或
はプランジャ一式射出成形機のホッパーに装入する。
After charging the mixture into a kneader and creating a desired atmosphere, kneading is started. The inner wall of the mixing tank of the kneader is controlled at 50°C by an electric heater or a hot medium heater.
Butanol dissolves and crosstalk progresses. 12 minutes after the crosstalk started
After an hour, turn off the heater power, run cold water at 20℃ through the jacket attached to the mixing tank and blade, and cool it down for 5 minutes.
Continuing to mix lines for 0 minutes. During this time, the 6th butanol freezes and becomes a binder for the raw material powder, forming a pellet-like mixture. The pellets are taken out and charged into a hopper of a screw in-line type or plunger type injection molding machine.

射出成形機の加熱シリンダーの出口温度を50℃に設定
する一方、金型に20℃の冷水を通しておく。
The outlet temperature of the heating cylinder of the injection molding machine is set at 50°C, while cold water at 20°C is passed through the mold.

次に型締、シリンダー前進、射出、保圧、型開、成形体
突出し、シリンダー後退、スクリュー後退、スクリュウ
−回転による可塑化の一連のシーケンスを行なう。
Next, a series of sequences including mold clamping, cylinder advancement, injection, holding pressure, mold opening, molded body ejection, cylinder retraction, screw retraction, and plasticization by screw rotation are performed.

成形体は表面近傍のバインダーが凝固して硬くなってお
り、離型は容易に行なわれる。この成形体を真空乾燥器
に装入し、温度を25℃に設定後最高真空度10” T
orr K真空排気する。5時間後停止し成形体を取出
し、次に真空加圧焼結炉に成形体を装入し、焼結炉を1
0−” Torr/1200℃に3時間保持して吸着物
を除去したのち、180゛0℃、窒素雰囲気9.8 k
gAG ICて6時間保持し減圧、放冷する。
The binder near the surface of the molded product solidifies and becomes hard, and the mold can be easily released from the mold. This molded body was placed in a vacuum dryer, the temperature was set at 25°C, and the maximum vacuum degree was 10” T.
orr K Evacuate. After 5 hours, stop and take out the molded body, then charge the molded body into the vacuum pressure sintering furnace, and turn the sintering furnace to 1.
After holding at 0-'' Torr/1200℃ for 3 hours to remove adsorbed substances, the temperature was 180゛0℃ and nitrogen atmosphere at 9.8K.
Hold the gAG IC for 6 hours, reduce the pressure, and let it cool.

上記手順によって、43.8mX 14.8aomX 
19.1 msと4!c8mX7.4awX 19.1
m+02種類の矩形状のキャピテイによシ成形体を作製
した。
By the above procedure, 43.8mX 14.8aomX
19.1 ms and 4! c8mX7.4awX 19.1
Molded bodies were produced using m+02 types of rectangular cavities.

この結果7.4 t*の薄形のみならず14.8−の厚
形についても脱バインダーに伴なう欠陥は認められず、
いずれについても理論密度比98チ、均一収縮した焼結
体が得られた。
As a result, no defects due to binder removal were observed not only in the thin type of 7.4 t* but also in the thick type of 14.8-t*.
In each case, uniformly shrunk sintered bodies with a theoretical density ratio of 98 cm were obtained.

本発明における金属粉およびセラミック扮の適用範囲は
前記実施例の窒化ケイ素粉に限定されず、炭化ケイ素、
アルミナ、ジルコニア、2ホウ化チタン等のセラミック
ス粉、Ni−Fe合金、ステンレス、ステライト、超硬
合金等の金属粉も含まれるものである。
The scope of application of the metal powder and ceramic material in the present invention is not limited to the silicon nitride powder of the above embodiment, but also silicon carbide,
Also included are ceramic powders such as alumina, zirconia, and titanium diboride, and metal powders such as Ni-Fe alloys, stainless steel, stellite, and cemented carbide.

〔発明の効果〕〔Effect of the invention〕

以上の如く第6ブタノールを金属粉およびセラミックス
粉の冷凍射出成形用ノくインダーとして用いる本発明方
法は、短時間の脱バインダーを可能とし、常温付近で射
出成形できるので、省エネルギーが可能であり、水を用
いた冷凍射出成形法のような原料粉の汚染がないこと、
かつ第5ブタノールの回収再利用ができるので経済的な
射出成形法である。
As described above, the method of the present invention, which uses 6-butanol as an inder for freezing injection molding of metal powders and ceramic powders, enables debinding in a short time, and injection molding can be performed at around room temperature, so it is possible to save energy. There is no contamination of the raw material powder as in the frozen injection molding method using water,
Moreover, it is an economical injection molding method because 5th butanol can be recovered and reused.

代理人 弁理士 木 村 三 朗 手 1介 抽 L[−占(自発) ’t、)”il午庁長゛+’:I’k        
 昭J1159 +r、i0 u 9 ++1、事件の
表示 特願昭59−179359号 2、発明の名称 粉体の成形方法(補正後) 3、補11:、をする者 事件との関係  特 許 出願人 名 称 (412目1本鋼管株式会社 4、代理人 7、補11らの内容 (2、特許請求の範囲Jを別紙の通り補正する。
Agent Patent attorney Kimura 3 Lawyers 1 person Draw L [-Zan (spontaneous) 't,)"Ilgo office director +': I'k
Showa J1159 +r, i0 u9 ++1, Indication of the case Patent application No. 59-179359 2, Name of the invention Method for molding powder (after amendment) 3, Supplement 11: Relationship with the case Patent Applicant name Title (412 items 1 Contents of Kouko Tube Co., Ltd. 4, Agent 7, Supplementary 11 et al. (2) Claim J is amended as shown in the attached sheet.

(3)明細書第1頁第16〜17行の「射出成形方法」
を「成形方法」と補正する。
(3) "Injection molding method" on page 1, lines 16-17 of the specification
is corrected as "molding method".

(4)同第6頁第8行と第9行間に次の文章を追加挿入
する。
(4) Add the following sentence between the 8th and 9th lines of page 6.

「有機バインダーを使う通常の射出成形法では、バイン
ダーと粉体とからなる可塑化物の変形特性が温度に対し
て敏感に変化するので、混合物の加熱可塑化機構を射出
成形機に内蔵せしめて射出温度の制御を厳密に行なう必
要がろる。これに対して水をバインダーとする可塑化物
の変形特性は常温付近では安定しているので、射出成形
機によらずに可塑化と成形を別の機械で行なうこともで
きる。例えば、混線機と型鍛造機の組み合わせがめる。
``In the normal injection molding method that uses an organic binder, the deformation characteristics of the plasticized product consisting of the binder and powder change sensitively to temperature, so a mechanism for heating and plasticizing the mixture is built into the injection molding machine. It is necessary to strictly control the temperature.On the other hand, since the deformation characteristics of plasticized materials using water as a binder are stable around room temperature, plasticization and molding can be performed separately without using an injection molding machine. It can also be done mechanically, for example, using a combination of a crosstalk machine and a die forging machine.

この場合、混線は室温で行ない、可塑化物を型鍛造機の
型内へ装入して型鍛造を行なう」(5)同第6頁第9行
の「水冷凍射出成形法」を「水冷線成形法」と補正する
In this case, cross-wiring is performed at room temperature, and the plasticized material is charged into the mold of a die forging machine to perform die forging.'' (5) ``Water-cooled injection molding method'' in line 9 of page 6 of the same Corrected as "molding method".

(6)同第7頁第9行9第11行、第14〜15行の「
射出成形」を「成形」と補正する。
(6) "Page 7, line 9, line 9, line 11, lines 14-15"
"injection molding" is corrected to "molding".

(7)同第7頁第18行第8頁第2行の「冷凍射出成形
」を「冷凍成形」と補正する。
(7) "Freeze injection molding" on page 7, line 18, line 2 of page 8 is corrected to "freeze molding."

(8)同第8頁第7行の「cdVC対して」を「に対し
てjと補正する。
(8) "For cdVC" on page 8, line 7 is corrected to "j for cdVC."

(9)同第11頁第4行、第8行及び第15〜第16行
の「射出成形」を「成形」と補正する。
(9) "Injection molding" on page 11, lines 4, 8, and 15 to 16 is corrected to "molding."

へり同第11頁第12行の「射出し」を「装入し」と補
正する。
"Injection" on page 11, line 12 of the same page is corrected to "charging."

02)同第13頁第17行と第18行間に次の文章を追
加挿入する。
02) Add the following sentence between page 13, line 17 and line 18.

1次に、@3ブタノールをバインダーに使った冷凍型鍛
造法の実施例について述べる。
First, an example of a frozen die forging method using @3-butanol as a binder will be described.

〔実施例〕〔Example〕

平均粒径0.75μ風の窒化ケイ素粉と焼結助剤トLテ
Ytos(6重量%)とA40g(2重量%)1用意す
る。さらにこの原料粉60容積%に対して第3ブタノー
ル$40容積チ相当量を用意する。
Prepare silicon nitride powder with an average particle size of 0.75 μm, sintering aid Ytos (6% by weight), and 40 g (2% by weight) of A. Furthermore, an amount equivalent to $40 volume of tertiary butanol is prepared for 60 volume % of this raw material powder.

この両者を加圧型ニーダ−に装入し窒素雰囲気としたの
ち、混線を開始する。ニーグー内壁を電熱ヒーターによ
り加熱し60℃に保持する。これによって第6ブタノー
ルが溶解し混線が進行する。
After charging both of them into a pressurized kneader and creating a nitrogen atmosphere, crosstalk is started. The inner wall of Nigu was heated with an electric heater and maintained at 60°C. As a result, the 6th butanol dissolves and crosstalk progresses.

混練と同時に加圧*により混練物に加圧操1’!”を加
え脱泡圧密する。そして12時間後可塑化した混線物を
とり出す。これを、直方体に成形して20℃の冷水を通
して冷却された鍛造金型内VC¥入し、直ちに圧縮成形
し、約6分間保持する。成形体は表面近傍の第6ブタノ
ールが硬くなりており、離型は容易に行ないつる。この
成形体を真空乾燥器に装入し、温度を25℃に設定後段
高真空度10’Torr IC真空排気し第6ブタノー
ルを蒸発除去する。
At the same time as kneading, pressurize* is applied to the kneaded material 1'! After 12 hours, the plasticized mixture was taken out. This was molded into a rectangular parallelepiped, placed in a forging mold cooled by running cold water at 20°C, and immediately compression-molded. , and held for about 6 minutes.The 6th butanol near the surface of the molded product is hard, so it can be easily released from the mold.The molded product is placed in a vacuum dryer, and the temperature is set at 25°C. The 6th butanol was evaporated and removed by IC evacuation at a vacuum degree of 10' Torr.

6時“間後停止し成形体を取出す。次に真空加圧焼結炉
に成形体を装入する。そして真空度10Torr。
After 6 hours, the molded body was stopped and the molded body was taken out.Then, the molded body was charged into a vacuum pressurized sintering furnace.Then, the vacuum degree was 10 Torr.

1000℃に3時間保持して吸着物を除去したのち、1
800℃、窒素雰囲気、 9.8 k17/ cλGK
で3時間保持後減圧、放冷する。冷却後成形体を取出し
てダイヤモンド研削によりパリ取りを行なう。
After holding at 1000°C for 3 hours to remove adsorbed substances,
800℃, nitrogen atmosphere, 9.8 k17/cλGK
After holding for 3 hours, the pressure was reduced and allowed to cool. After cooling, the compact is taken out and deburred by diamond grinding.

上記手順によって、43.8mX 14.81WIx1
9.1鵡と46.8朋X Z4鴎×191簡の2種類の
矩形状キャピテイにより成形体を作製した。この結果、
7、4 、mの薄形のみならず14.8 mの厚形VC
ついても脱バインダーに伴なう欠陥はみられず、いずれ
についても理論密度比98%の均一収縮した焼結体が得
られた」 (6)同第14頁第6行、第8行及び第9行の「射出成
形」を「成形」と補正する。
By the above procedure, 43.8mX 14.81WIx1
Molded bodies were produced using two types of rectangular cavities: 9.1-inch and 46.8-inch x Z4-guan x 191-inch. As a result,
Not only thin VC of 7, 4, m, but also thick VC of 14.8 m.
However, no defects due to binder removal were observed, and uniformly shrunken sintered bodies with a theoretical density ratio of 98% were obtained in all cases.'' (6) Page 14, lines 6, 8, and Correct “injection molding” in line 9 to “molding”.

特許請求の範囲(補正) 「金属粉およびセラミックス粉の成形において。Scope of claims (amendment) “For forming metal powders and ceramic powders.

60〜55容積チの第6ブタノールを前記金W4紛およ
びセラミックス粉と混合し、該混合物を第3ブタノール
の、融点以上の温度に調整し、ついで前記混合物を、冷
却された金型内に装入し、成形保持したのち、得られた
成形体の表面温度を第6ブタノールの融点以下にして該
成形体内の第5ブタノールを凍結せしめ、成形体ををり
出すことを特徴とする粉体の成形方法。」
60 to 55 volumes of tertiary butanol are mixed with the gold W4 powder and ceramic powder, the mixture is adjusted to a temperature higher than the melting point of tertiary butanol, and then the mixture is placed in a cooled mold. The method of producing powder is characterized in that the surface temperature of the obtained molded body is lowered to below the melting point of the 6th butanol to freeze the 5th butanol in the molded body, and the molded body is taken out. Molding method. ”

Claims (1)

【特許請求の範囲】[Claims] (1)金属粉およびセラミックス粉の射出成形において
、30〜55容積%の第3ブタノールを前記金属粉およ
びセラミックス粉と混合し、該混合物を第3ブタノール
の融点以上の温度に調整し、ついで前記混合物を、冷却
された金型内に射出し、成形保持したのち、得られた成
形体の表面温度を第3ブタノールの融点以下にして該成
形体内の第3ブタノールを凍結せしめ、成形体を取り出
すことを特徴とする粉体の射出成形方法。
(1) In injection molding of metal powder and ceramic powder, 30 to 55% by volume of tertiary butanol is mixed with the metal powder and ceramic powder, the mixture is adjusted to a temperature equal to or higher than the melting point of tertiary butanol, and then the After injecting the mixture into a cooled mold and holding the mold, the surface temperature of the obtained molded body is lowered to below the melting point of tertiary butanol to freeze the tertiary butanol in the molded body, and the molded body is taken out. A powder injection molding method characterized by:
JP59179359A 1984-08-30 1984-08-30 Powder injection molding method Pending JPS6160802A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP59179359A JPS6160802A (en) 1984-08-30 1984-08-30 Powder injection molding method
SE8502882A SE459793B (en) 1984-08-30 1985-06-11 PROCEDURE FOR THE POWDER FORMING
GB08516576A GB2163780B (en) 1984-08-30 1985-07-01 Method of moulding powder materials
DE19853525752 DE3525752A1 (en) 1984-08-30 1985-07-19 METHOD FOR MOLDING POWDERS
FR8512879A FR2569683A1 (en) 1984-08-30 1985-08-29 PROCESS FOR MOLDING POWDER MATERIALS

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59179359A JPS6160802A (en) 1984-08-30 1984-08-30 Powder injection molding method

Publications (1)

Publication Number Publication Date
JPS6160802A true JPS6160802A (en) 1986-03-28

Family

ID=16064467

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59179359A Pending JPS6160802A (en) 1984-08-30 1984-08-30 Powder injection molding method

Country Status (5)

Country Link
JP (1) JPS6160802A (en)
DE (1) DE3525752A1 (en)
FR (1) FR2569683A1 (en)
GB (1) GB2163780B (en)
SE (1) SE459793B (en)

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US5047182A (en) * 1987-11-25 1991-09-10 Ceramics Process Systems Corporation Complex ceramic and metallic shaped by low pressure forming and sublimative drying
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JPS60218401A (en) * 1984-04-12 1985-11-01 Nobuyuki Takahashi Method for freeze-forming metallic powder

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Publication number Priority date Publication date Assignee Title
JPS61263703A (en) * 1985-05-20 1986-11-21 トヨタ自動車株式会社 Injection molding method of powder

Also Published As

Publication number Publication date
FR2569683A1 (en) 1986-03-07
SE8502882D0 (en) 1985-06-11
GB8516576D0 (en) 1985-08-07
DE3525752A1 (en) 1986-03-13
GB2163780A (en) 1986-03-05
GB2163780B (en) 1987-05-28
SE8502882L (en) 1986-03-01
SE459793B (en) 1989-08-07
DE3525752C2 (en) 1987-12-03

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