JPH0288701A - Method for reproducing injection molding raw material for powder metallurgy - Google Patents
Method for reproducing injection molding raw material for powder metallurgyInfo
- Publication number
- JPH0288701A JPH0288701A JP23967388A JP23967388A JPH0288701A JP H0288701 A JPH0288701 A JP H0288701A JP 23967388 A JP23967388 A JP 23967388A JP 23967388 A JP23967388 A JP 23967388A JP H0288701 A JPH0288701 A JP H0288701A
- Authority
- JP
- Japan
- Prior art keywords
- binder
- powder
- injection molding
- ceramic
- metal
- 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
- 238000001746 injection moulding Methods 0.000 title claims abstract description 20
- 239000002994 raw material Substances 0.000 title claims abstract description 17
- 238000000034 method Methods 0.000 title claims description 19
- 238000004663 powder metallurgy Methods 0.000 title claims description 9
- 239000011230 binding agent Substances 0.000 claims abstract description 26
- 239000000843 powder Substances 0.000 claims abstract description 23
- 239000000919 ceramic Substances 0.000 claims abstract description 16
- 229910052751 metal Inorganic materials 0.000 claims abstract description 16
- 239000002184 metal Substances 0.000 claims abstract description 16
- 238000004519 manufacturing process Methods 0.000 claims abstract description 7
- 238000004898 kneading Methods 0.000 claims abstract 3
- 239000000203 mixture Substances 0.000 claims description 15
- 238000000605 extraction Methods 0.000 claims description 6
- 238000000465 moulding Methods 0.000 claims description 5
- 229920000620 organic polymer Polymers 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims 1
- 238000010298 pulverizing process Methods 0.000 claims 1
- 238000004064 recycling Methods 0.000 claims 1
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 abstract description 6
- 239000003960 organic solvent Substances 0.000 abstract description 5
- -1 polyethylene Polymers 0.000 abstract description 5
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 abstract description 3
- 239000004698 Polyethylene Substances 0.000 abstract description 3
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 abstract description 3
- 229920000573 polyethylene Polymers 0.000 abstract description 3
- 239000008096 xylene Substances 0.000 abstract description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract description 2
- 239000004793 Polystyrene Substances 0.000 abstract description 2
- 150000001491 aromatic compounds Chemical class 0.000 abstract description 2
- 229920001577 copolymer Polymers 0.000 abstract description 2
- 229920000098 polyolefin Polymers 0.000 abstract description 2
- 229920002223 polystyrene Polymers 0.000 abstract description 2
- HIXDQWDOVZUNNA-UHFFFAOYSA-N 2-(3,4-dimethoxyphenyl)-5-hydroxy-7-methoxychromen-4-one Chemical compound C=1C(OC)=CC(O)=C(C(C=2)=O)C=1OC=2C1=CC=C(OC)C(OC)=C1 HIXDQWDOVZUNNA-UHFFFAOYSA-N 0.000 abstract 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 abstract 1
- 229920000642 polymer Polymers 0.000 abstract 1
- 238000005238 degreasing Methods 0.000 description 5
- 239000002904 solvent Substances 0.000 description 5
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- MQIUGAXCHLFZKX-UHFFFAOYSA-N Di-n-octyl phthalate Natural products CCCCCCCCOC(=O)C1=CC=CC=C1C(=O)OCCCCCCCC MQIUGAXCHLFZKX-UHFFFAOYSA-N 0.000 description 2
- BJQHLKABXJIVAM-UHFFFAOYSA-N bis(2-ethylhexyl) phthalate Chemical compound CCCCC(CC)COC(=O)C1=CC=CC=C1C(=O)OCC(CC)CCCC BJQHLKABXJIVAM-UHFFFAOYSA-N 0.000 description 2
- 239000005038 ethylene vinyl acetate Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 229920001490 poly(butyl methacrylate) polymer Polymers 0.000 description 2
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 2
- 238000005979 thermal decomposition reaction Methods 0.000 description 2
- 229920001169 thermoplastic Polymers 0.000 description 2
- 239000001993 wax Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- 150000007824 aliphatic compounds Chemical class 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- 230000008094 contradictory effect Effects 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 229920000058 polyacrylate Polymers 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 238000009692 water atomization Methods 0.000 description 1
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野コ
本発明はセラミックスまたは金属の粉末冶金用射出成形
原料の再生方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for regenerating raw materials for injection molding of ceramics or metals for powder metallurgy.
[従来の技術]
一般にセラミックスまたは金属の焼結製品を製造する工
程で焼結前の成形体は原料粉末を圧縮成形することによ
り圧粉体として得られている。これは通常上下方向から
パンチで加圧するという方法であることから、得られる
成形体の形状としては、円柱、円筒のような比較的単純
なものに限られ、より複雑な形状の製品を得るには焼結
上がりの製品に切削研削などの後加圧を施す必要がある
。[Prior Art] Generally, in the process of manufacturing sintered products of ceramics or metals, a compact before sintering is obtained as a green compact by compression molding raw material powder. Since this method usually uses punches to apply pressure from above and below, the shape of the molded product obtained is limited to relatively simple shapes such as cylinders and cylinders, and it is difficult to obtain products with more complex shapes. It is necessary to pressurize the sintered product after cutting, grinding, etc.
このような問題点を改善すべく、成形体の形状を製品に
より近づけるいわゆるニアネットシエイプ技術が種々検
討されているが、その中で最も複雑形状の成形に適して
いるのは射出成形であると考えられ、一部は工業的に採
用されつつある。この射出成形方法はセラミックスまた
は金属の粉末に10〜20重量%の有機高分子を主成分
としたバインダーを加えて混合、混練した混和物を適当
な形状のペレットとして射出成形機に供給し、所要の形
状のいわゆるグリーン成形体とする。しかる後に適当な
方法でグリーン成形体に、脱ハインダー即ち脱脂を施し
て、いわゆるブラウン体を得、これを焼結して製品とす
るという工程を踏むものである。In order to improve these problems, various so-called near-net shape technologies have been studied to bring the shape of the molded object closer to the product, but injection molding is the most suitable for molding complex shapes. Some of them are being adopted industrially. In this injection molding method, a mixture of ceramic or metal powder mixed and kneaded with 10 to 20% by weight of a binder mainly composed of an organic polymer is fed into an injection molding machine as pellets of an appropriate shape. A so-called green molded body having the shape of Thereafter, the green molded body is dehindered, ie, degreased, by an appropriate method to obtain a so-called brown body, which is then sintered to form a product.
[発明が解決しようとする課題]
これらの工程の中で脱脂は適当な有機溶媒によってバイ
ンダーを溶解抽出する方法、近年注目されている超臨界
状態の流体によってバインダーを溶解抽出する方法など
も考えられるが、前者はバインダーの溶解時に溶媒の方
が有機高分子側に移行して膨潤し成形体の形状を損うと
いう問題があり、後者は超臨界状態の流体に可溶であっ
てバインダーとして使用可能な物質が限定されるため実
用的な処方が確立されていないという問題かある。[Problems to be solved by the invention] Among these processes, degreasing can be performed by dissolving and extracting the binder using an appropriate organic solvent, or by dissolving and extracting the binder using a fluid in a supercritical state, which has been attracting attention in recent years. However, the former has the problem that when the binder is dissolved, the solvent migrates to the organic polymer side and swells, damaging the shape of the molded product, while the latter is soluble in fluids in a supercritical state and is used as a binder. The problem is that a practical prescription has not been established because the possible substances are limited.
そのため現在工業的に行れている脱脂方法は成形体が変
形を起こさない程度の昇温速度で加熱を施し、バインダ
ーを熱分解によって低分子量の気体として揮散除去する
というものである。従って本方法に使用されるバインダ
ーへ要求される特性としては成形性もさることながら、
熱分解し易く、炭化し難いという性質を具備することが
非常に重要となる。Therefore, the current industrial degreasing method is to heat the molded product at a temperature increase rate that does not cause deformation, and to volatilize and remove the binder as a low molecular weight gas through thermal decomposition. Therefore, in addition to moldability, the properties required for the binder used in this method are:
It is very important to have the properties of being easy to thermally decompose and difficult to carbonize.
一方で射出成形という方法はスプルー ランナなどのス
クラップの発生が不可避であり、特に原料が高価なもの
である場合では、このスクラップを再使用することが製
品の製造コストを低減するため必要不可欠となる。とこ
ろが、前述のように本方法に使用されるバインダーは脱
脂工程を考慮して熱分解特性の良好なものを採用する必
要があることから、成形て熱履歴を受ける度に劣化し易
く、成形条件の不安定さひいてはグリーン成形体の品質
のばらつきを大きくする原因となる。On the other hand, the injection molding method inevitably generates scrap such as sprue runners, and especially when raw materials are expensive, it is essential to reuse this scrap to reduce the manufacturing cost of the product. . However, as mentioned above, the binder used in this method must have good thermal decomposition properties in consideration of the degreasing process, so it tends to deteriorate each time it is subjected to thermal history during molding, and the molding conditions This causes instability and, in turn, increases variation in the quality of green molded products.
即ち、本製造工程では脱脂工程と原料混和物の再使用と
いう二つの観点から、バインダーに対して相反する特性
を要求することとなる。そして再使用を繰り返すと、後
工程のために必要な品質を具備したグリーン成形体を得
ることができなくなり、原料を廃棄しなければならなく
なる場合がほんどである。That is, in this manufacturing process, contradictory properties are required of the binder from the two viewpoints of the degreasing process and the reuse of the raw material mixture. If the material is repeatedly reused, it becomes impossible to obtain a green molded product with the quality required for subsequent processes, and in most cases, the raw material must be discarded.
本発明の技術課題は上述の欠点に鑑みて、グリーン成形
体の品質を損うことなく原料の再使用を可能にするため
になされたもので粉末冶金用射出成形原料の歩留を向上
する方法を提供することにある。In view of the above-mentioned drawbacks, the technical problem of the present invention is to enable the reuse of raw materials without impairing the quality of green molded products, and is a method for improving the yield of injection molding raw materials for powder metallurgy. Our goal is to provide the following.
[課題を解決するための手段]
前述の射出成形によってグリーン成形体を得る工程で原
料混和物のバインダー中の主成分である有機高分子とし
ては熱可塑性のものが使用できる。[Means for Solving the Problems] A thermoplastic organic polymer can be used as the main component in the binder of the raw material mixture in the step of obtaining a green molded body by injection molding.
そして熱可塑性高分子は高耐熱性のポリテトラフルオロ
エチレンのようなものを除くとそれを溶解する溶媒が存
在し、適当な組成のバインダーを使用すれば、セラミッ
クスまたは金属の粉末の特性を損うことなく溶解除去す
ることができる。Thermoplastic polymers, with the exception of highly heat-resistant polytetrafluoroethylene, require solvents to dissolve them, and if a binder with an appropriate composition is used, the properties of ceramic or metal powders will be impaired. It can be removed by dissolution without any problem.
本発明者らはかかる観点から有機溶媒に可溶であって成
形性、脱脂性に優れたバインダー処方を検討した結果、
本発明をなすに至ったものである。From this point of view, the present inventors investigated a binder formulation that is soluble in organic solvents and has excellent moldability and degreasing properties.
This is what led to the present invention.
即ち本発明によれば、セラミックス又は金属の製品を粉
末冶金によって製造する際、セラミックス又は金属の粉
末と有機高分子を主成分とするバインダーとを混合、混
線、粉砕した混和物を所要形状に射出成形する射出成形
工程で発生したスクラツブに溶媒で抽出処理を施すこと
により、前記バインダーを除去して前記スクラップに含
まれるセラミックス又は金属の粉末を回収することを特
徴とする粉末冶金用射出成形原料の再生方法が得られる
。That is, according to the present invention, when manufacturing a ceramic or metal product by powder metallurgy, a mixture of ceramic or metal powder and a binder whose main component is an organic polymer is mixed, mixed, and pulverized, and the mixture is injected into a desired shape. An injection molding raw material for powder metallurgy, characterized in that the scrub generated during the injection molding process is subjected to extraction treatment with a solvent to remove the binder and recover ceramic or metal powder contained in the scrap. A reproduction method is obtained.
本発明において、射出成形工程で発生するスクラップと
は、スプルー ランナー等をいい、スプルーとは、射出
成形型に注入される供給穴あるいは、導管中に凝固する
混合物をいい、ランナーとは、射出成形機のスプルーと
金型キャビティのゲートを結ぶ溝に発生する凝固した混
和物をいう。In the present invention, scrap generated during the injection molding process refers to sprue runners, etc. Sprue refers to the supply hole or mixture solidified in the conduit that is injected into the injection mold, and the runner refers to the injection molding process. This is the solidified mixture that forms in the groove that connects the sprue of the machine and the gate of the mold cavity.
本発明は、成形工程で熱履歴を受はバインダーが劣化し
て使用可能となった混和物を溶解抽出を施すことにより
セラミックスまたは金属の粉末を回収することによって
粉末冶金用射出成形原料として再使用する方法を提供す
るものである。従って、本発明によれば粉末の歩留を実
質的に100%とすることが可能となり、殊に原料粉末
が高価なものである場合は効果は大となる。また当然抽
出したバインダーは廃棄することとなるが前述のように
バインダーの添加量は10〜20重量%と少いので、特
に高価なものを使用しなければ問題とならない。In the present invention, the binder deteriorates due to thermal history during the molding process, and the mixture becomes usable. By dissolving and extracting the mixture, the ceramic or metal powder is recovered and reused as a raw material for injection molding for powder metallurgy. This provides a method to do so. Therefore, according to the present invention, it is possible to achieve a powder yield of substantially 100%, which is especially effective when the raw material powder is expensive. Naturally, the extracted binder must be discarded, but as mentioned above, the amount of binder added is as small as 10 to 20% by weight, so this will not be a problem unless a particularly expensive one is used.
本発明に使用されるバインダーとしては一般的な有機溶
媒に150°C前後までの温度で可溶なものであれば何
でも使用でき例としてはポリエチレン、各種ポリオレフ
ィン、各種アクリル系高分子、ポリスチレン、及びそれ
らの共重合体、各種ワックス等が挙げられる。抽出温度
を150℃前後としたのは過度に高温の条件では粉末へ
の影響が懸念されるからである。また溶媒としては粉末
に影響を及はさないものであれば何でも良く、ベンゼン
、キシレン等の芳香族化合物、酢酸エチル等のエステル
類、ヘキサン等の脂肪族化合物、及びアルコール、エー
テル等が例として挙げられる。As the binder used in the present invention, anything can be used as long as it is soluble in a general organic solvent at a temperature of up to about 150°C. Examples include polyethylene, various polyolefins, various acrylic polymers, polystyrene, and Examples include copolymers thereof and various waxes. The reason why the extraction temperature was set at around 150°C is because there is a concern that excessively high temperature conditions may affect the powder. Any solvent may be used as long as it does not affect the powder; examples include aromatic compounds such as benzene and xylene, esters such as ethyl acetate, aliphatic compounds such as hexane, alcohol, and ether. Can be mentioned.
そして抽出装置としては各種のものか使用できるが、た
とえばソックスレー抽出器のようなものを採用すれば、
抽出効率か高いばかりでなく、溶媒を再使用できるので
有利である。Various types of extraction equipment can be used; for example, if a Soxhlet extractor is used,
Not only is the extraction efficiency high, but the solvent can be reused, which is advantageous.
以下に実施例を挙げ、説明するが、本発明がこれに限定
されるものではないことは勿論である。Examples will be described below, but it goes without saying that the present invention is not limited thereto.
[実施例]
水アトマイズ法によって5US304の合金を平均粒径
約11μmの粉末とした。この粉末と数平均分子ft:
60,000のポリメタクリル酸ブチル(PBMA)
、酢酸ビニル含m : 25 mole%で数平均分子
量:110,000のエチレン−酢酸ビニル共重合体(
EVA)、数平均公刊ト2.000のポリエチレンワッ
クス(PEWAX)及びフタル酸ジオクチル(DOP)
を第1表の重量%となるように秤量して混線、粉砕し、
射出成形用の混和物を得た。この混和物を160°Cと
いう温度で射出成形し、発生したスプルー ランナをソ
ックスレー抽出器によりキシレンにて100℃で5Hr
、抽出を行った。抽出器より取り出した5US304の
粉末の炭素を分析したところ87p、p、mであって、
バインダーはほぼ100%除去され、原料粉末として再
使用可能の状態であった。[Example] An alloy of 5US304 was made into powder with an average particle size of about 11 μm by a water atomization method. This powder and number average molecule ft:
60,000 polybutyl methacrylate (PBMA)
, an ethylene-vinyl acetate copolymer with a vinyl acetate content of 25 mole% and a number average molecular weight of 110,000 (
EVA), polyethylene wax (PEWAX) with a number average published value of 2.000 and dioctyl phthalate (DOP)
Weigh it to the weight percentage shown in Table 1, mix it up, crush it,
A mixture for injection molding was obtained. This mixture was injection molded at a temperature of 160°C, and the resulting sprue runners were heated in xylene at 100°C for 5 hours using a Soxhlet extractor.
, the extraction was performed. When the carbon of the 5US304 powder taken out from the extractor was analyzed, it was 87p, p, m,
Almost 100% of the binder was removed, and the powder could be reused as a raw material powder.
以下宗日
[発明の効果]
以上述べたように、本発明によれば粉末冶金用射出成形
原料のセラミックス又は、金属粉末の原料歩留を実質的
に100%とすることが可能となりセラミックス又は金
属製品製造のためのコストダウンに寄与するところは大
であり、工業上非常に有益である。[Effects of the Invention] As described above, according to the present invention, it is possible to make the raw material yield of ceramics or metal powder, which is an injection molding raw material for powder metallurgy, substantially 100%. It greatly contributes to reducing the cost of manufacturing products, and is extremely useful industrially.
Claims (1)
造する際、セラミックス又は金属の粉末と、有機高分子
を主成分とするバインダーとを混合、混練、粉砕した混
和物を所要の形状に射出成形する射出成形工程で発生し
たスクラップに、抽出処理を施すことにより、前記バイ
ンダーを除去して、前記スクラップからセラミックス又
は金属の粉末を回収することを特徴とする粉末冶金用射
出成形原料の再生方法。1. When manufacturing ceramic or metal products by powder metallurgy, injection molding is performed by mixing, kneading, and pulverizing a mixture of ceramic or metal powder and a binder whose main component is an organic polymer into the desired shape. A method for recycling injection molding raw materials for powder metallurgy, characterized in that scraps generated in a molding process are subjected to extraction treatment to remove the binder and recover ceramic or metal powder from the scraps.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23967388A JPH0288701A (en) | 1988-09-27 | 1988-09-27 | Method for reproducing injection molding raw material for powder metallurgy |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23967388A JPH0288701A (en) | 1988-09-27 | 1988-09-27 | Method for reproducing injection molding raw material for powder metallurgy |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0288701A true JPH0288701A (en) | 1990-03-28 |
Family
ID=17048208
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP23967388A Pending JPH0288701A (en) | 1988-09-27 | 1988-09-27 | Method for reproducing injection molding raw material for powder metallurgy |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0288701A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100414160B1 (en) * | 2000-10-16 | 2004-01-07 | 한국과학기술연구원 | A Process for Producing Porous Stainless Steel with Gradient Pore Structures Using Stainless Steel Scrap Fiber |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61153201A (en) * | 1984-12-27 | 1986-07-11 | Tdk Corp | Method for regenerating scrap of magnet containing rare earth element |
JPS61287702A (en) * | 1985-06-17 | 1986-12-18 | 日本鋼管株式会社 | Method of molding powdered body |
-
1988
- 1988-09-27 JP JP23967388A patent/JPH0288701A/en active Pending
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JPS61153201A (en) * | 1984-12-27 | 1986-07-11 | Tdk Corp | Method for regenerating scrap of magnet containing rare earth element |
JPS61287702A (en) * | 1985-06-17 | 1986-12-18 | 日本鋼管株式会社 | Method of molding powdered body |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100414160B1 (en) * | 2000-10-16 | 2004-01-07 | 한국과학기술연구원 | A Process for Producing Porous Stainless Steel with Gradient Pore Structures Using Stainless Steel Scrap Fiber |
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