JPH02270902A - Manufacture of iron sintered product - Google Patents
Manufacture of iron sintered productInfo
- Publication number
- JPH02270902A JPH02270902A JP1092280A JP9228089A JPH02270902A JP H02270902 A JPH02270902 A JP H02270902A JP 1092280 A JP1092280 A JP 1092280A JP 9228089 A JP9228089 A JP 9228089A JP H02270902 A JPH02270902 A JP H02270902A
- Authority
- JP
- Japan
- Prior art keywords
- iron
- binder
- product
- heated
- powder
- 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
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title claims abstract description 34
- 229910052742 iron Inorganic materials 0.000 title claims abstract description 8
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 6
- 238000005245 sintering Methods 0.000 claims abstract description 18
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000012298 atmosphere Substances 0.000 claims abstract description 11
- 239000001257 hydrogen Substances 0.000 claims abstract description 11
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 11
- 238000001746 injection moulding Methods 0.000 claims abstract description 9
- 230000009467 reduction Effects 0.000 claims abstract description 4
- 238000000034 method Methods 0.000 claims description 13
- 238000002347 injection Methods 0.000 claims description 5
- 239000007924 injection Substances 0.000 claims description 5
- QMQXDJATSGGYDR-UHFFFAOYSA-N methylidyneiron Chemical compound [C].[Fe] QMQXDJATSGGYDR-UHFFFAOYSA-N 0.000 claims description 2
- 239000011230 binding agent Substances 0.000 abstract description 13
- 229910052799 carbon Inorganic materials 0.000 abstract description 9
- 239000001301 oxygen Substances 0.000 abstract description 9
- 229910052760 oxygen Inorganic materials 0.000 abstract description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 5
- 238000010438 heat treatment Methods 0.000 abstract description 5
- 229910000805 Pig iron Inorganic materials 0.000 abstract description 4
- 238000011282 treatment Methods 0.000 abstract description 3
- 239000000463 material Substances 0.000 abstract description 2
- 238000001816 cooling Methods 0.000 abstract 1
- 238000005262 decarbonization Methods 0.000 abstract 1
- 150000002505 iron Chemical class 0.000 abstract 1
- 238000004898 kneading Methods 0.000 abstract 1
- 239000000843 powder Substances 0.000 description 18
- 238000005238 degreasing Methods 0.000 description 15
- 230000008569 process Effects 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- -1 white pig iron Chemical compound 0.000 description 3
- 238000000889 atomisation Methods 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000005261 decarburization Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000012778 molding material Substances 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 150000002926 oxygen Chemical class 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 239000002952 polymeric resin Substances 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000001993 wax Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F2999/00—Aspects linked to processes or compositions used in powder metallurgy
Landscapes
- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
- Powder Metallurgy (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、射出成形鉄粉成形体の焼結のための処理法に
関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a processing method for the sintering of injection molded iron powder compacts.
従来から、鉄粉を成形素材とする射出成形焼結体は、球
状あるいはそれに近い形状を有するアトマイズ法等によ
って得られた鉄粉が使用されている。BACKGROUND ART Conventionally, injection-molded sintered bodies using iron powder as a molding material have been made using iron powder obtained by an atomization method or the like and having a spherical shape or a shape close to the spherical shape.
しかしながら、アトマイズ法等によって得られた鉄粉は
生産能力が低く、且つコスト高となって多量生産には向
かない。However, iron powder obtained by the atomization method or the like has a low production capacity and is expensive, making it unsuitable for mass production.
他方、比較的低コストで微細鉄粉を得る方法として、白
銑組織を有する高炭素溶湯を急冷して破砕し、これをさ
らに機械的に破砕する方法がある。On the other hand, as a method for obtaining fine iron powder at a relatively low cost, there is a method in which a high carbon molten metal having a white pig iron structure is rapidly cooled and crushed, and then this is further mechanically crushed.
この機械的破砕に際しては、処理原料は相互に押し潰さ
れる運動が行われるために、製出した微粉末中には平板
状のものが存在する。このため、球状粉末を使用した射
出成形物と比較して、成形後のバインダー樹脂材の揮発
分の除去すなわち脱脂作業に長時間の加熱を要し、それ
が不完全だと成形体が変形するという欠点があった。During this mechanical crushing, the raw materials to be treated undergo a movement of being crushed against each other, so that the produced fine powder has a flat plate shape. For this reason, compared to injection molded products using spherical powder, long-term heating is required to remove volatile matter from the binder resin material after molding, that is, degreasing work, and if it is incomplete, the molded product will deform. There was a drawback.
また、機械的破砕の微粉砕過程においては、粉末に水分
を添加したスラリー状で行われるために、製出した微粉
末表面に酸化物層が形成されている。In addition, in the fine pulverization process of mechanical crushing, the powder is mixed with water in the form of a slurry, so that an oxide layer is formed on the surface of the fine powder produced.
そのため、IR1m砕後m砕土げ工程として、特開昭6
3−266002号公報、特願昭63−58684号出
願明細書等に記載されているように、粉末自体が含有す
る炭素や水素と接触して酸素を除去する工程が必要にな
る。この酸素除去の工程において、粉末表面の活性化に
よって焼結凝集が起こり粒径が大きくなるため、粉末の
粒径を射出成形に必要な平均10μm以下に維持するに
は、処理温度を下げ、ある程度の酸素を残さざるを得ず
、この粉末を使用した焼結体は酸化皮膜を持つ空隙部が
収縮のネックになり、低密度の成形体しか得難いという
欠点がある。Therefore, as the IR1m crushing and m crushing process,
As described in Japanese Patent Application No. 3-266002, Japanese Patent Application No. 63-58684, etc., a step is required to remove oxygen by contacting carbon and hydrogen contained in the powder itself. In this oxygen removal process, activation of the powder surface causes sintering and agglomeration, which increases the particle size. Therefore, in order to maintain the powder particle size below the average of 10 μm required for injection molding, the processing temperature must be lowered to some extent. The sintered body using this powder has the disadvantage that the voids with the oxide film become a bottleneck for shrinkage, making it difficult to obtain a molded body with only a low density.
本発明において解決すべき課題は、上記の欠点を有する
白銑等の高炭素鉄を破砕して得た平均10μm以下の微
粉末を使用して、酸素の少ない、且つ高密度の射出成形
体を得る方策を見出すことにある。The problem to be solved by the present invention is to produce a high-density injection-molded body with low oxygen content using fine powder with an average size of 10 μm or less obtained by crushing high-carbon iron such as white pig iron, which has the above-mentioned drawbacks. The goal is to find a way to obtain it.
本発明は、白銑化した急冷高炭素鉄を粉砕し、脱炭処理
を行った微細鉄粉を用いて射出成形を行い、この射出成
形体を大気雰囲気中で350℃以下の温度に加熱してバ
インダー樹脂を気化により除去し、さらに、300〜6
00℃で水素還元を行ったのち焼結を行うことによって
その課題を解決した。The present invention involves injection molding using fine iron powder obtained by pulverizing quenched high carbon iron that has been turned into white pig iron and subjecting it to decarburization treatment, and then heating this injection molded product to a temperature of 350°C or less in an atmospheric atmosphere. The binder resin is removed by vaporization, and further
This problem was solved by hydrogen reduction at 00°C followed by sintering.
射出成形には10%前後のバインダーが使用され、成形
後、これらのバインダーは樹脂工程でその大半は除去さ
れなければならない。バインダーの中にはジブリルフタ
ル酸のように低温で蒸発するものの他に、ポリプロピレ
ンのように蒸発温度の高いものもある。後者のバインダ
ーは高分子の樹脂で不活性雰囲気中では蒸発し難いが、
大気中で加熱すれば酸素と反応し、分子型の小さい蒸発
しやすい物質に変換されるため、低温で脱脂ができる。Injection molding uses around 10% binder, and after molding, most of these binders must be removed in a resin process. Some binders, such as dibryl phthalic acid, evaporate at low temperatures, while others, such as polypropylene, have high evaporation temperatures. The latter binder is a polymeric resin that is difficult to evaporate in an inert atmosphere, but
When heated in the atmosphere, it reacts with oxygen and is converted into a substance with small molecules that evaporates easily, so it can be degreased at low temperatures.
不活性雰囲気、例えば窒素中で脱脂する場合には、50
0℃前後まで加熱しなくてはならないが、大気脱脂では
300℃前後で脱脂はほぼ完了し、大幅な処理時間の短
縮がもたらされる。When degreasing in an inert atmosphere, for example nitrogen, 50
Although it is necessary to heat to around 0°C, in atmospheric degreasing, degreasing is almost completed at around 300°C, resulting in a significant reduction in processing time.
一方、脱脂時間は粉体の形状によっても大きく影響を受
ける。即ち、球状体であればガス化したバインダーは比
較的抜けやすいが、平板状体を含む破砕粉の場合にはガ
ス通路が複雑になり、処理時間が不充分であると、ふく
れ1割れ等の欠陥が生じやすい。On the other hand, the degreasing time is also greatly affected by the shape of the powder. In other words, if it is a spherical object, the gasified binder will come out relatively easily, but if the crushed powder contains a flat plate-like object, the gas passage will be complicated, and if the processing time is insufficient, bulges, cracks, etc. will occur. Prone to defects.
従って、アトマイズ粉に比べ、長い脱脂時間を必要とす
る破砕粉に大気脱脂が適用できると、射出成形を行う際
の阻害要因の一つを除去できることになる。Therefore, if atmospheric degreasing can be applied to crushed powder, which requires a longer degreasing time than atomized powder, one of the factors inhibiting injection molding can be removed.
酸化物系のセラミックスで適用されている大気脱脂も金
属粉の場合には酸化の問題があるが、高炭素破砕鉄粉で
は脱炭後も若干の酸素が残っており、それが新たな酸化
を阻止するのみで大きな問題にはならない。Atmospheric degreasing applied to oxide-based ceramics also has the problem of oxidation when metal powder is used, but high-carbon crushed iron powder still has some oxygen remaining after decarburization, which causes new oxidation. It's not a big problem just to prevent it.
一°般に鉄粉の焼結工程では、窒素等の不活性雰囲気で
800℃程度まで加熱し、その後水素気流中で1200
℃以上で焼結する。しかも、この条件では、表面に酸化
皮膜を有する鉄粉は、水素富囲気に変わると即刻表面が
還元され焼結が起こる。Generally, in the sintering process of iron powder, it is heated to about 800℃ in an inert atmosphere such as nitrogen, and then heated to about 1200℃ in a hydrogen stream.
Sinter at temperatures above ℃. Moreover, under these conditions, when the iron powder having an oxide film on its surface is changed into a hydrogen-rich atmosphere, the surface is immediately reduced and sintering occurs.
従って、水素が浸透する前に周囲の焼結が進み、酸化膜
を有する空孔部が残されると成形体の収縮は妨げられず
、焼結密度は上がらず良質の成形体は得られない。Therefore, if the surrounding sintering progresses before hydrogen permeates and voids with oxide films are left behind, the shrinkage of the compact will not be prevented, the sintered density will not increase, and a good quality compact will not be obtained.
そこで、上記急冷高炭素鉄有鉄を機械破砕した微細鉄粉
を射出成形して上記大気脱脂を行った成形体の水素富囲
気における焼結挙動を調べた結果、ある特定の加熱温度
域では全面的脱酸は進行するが焼結は殆ど起こらないこ
とが判明した。Therefore, as a result of investigating the sintering behavior in a hydrogen-rich atmosphere of a compact made by injection-molding fine iron powder obtained by mechanically crushing the above-mentioned quenched high-carbon ferrous iron and performing the above-mentioned atmospheric degreasing, it was found that in a certain heating temperature range, the entire surface It was found that although deoxidation progressed, sintering hardly occurred.
すなわち、略300℃において脱酸の進行の増大に変曲
点かあり、300℃未満では実質的な焼結は起こらない
代わりに脱酸の進行も遅く反応に時間がかかり過ぎ、工
業的に適用できない。また、600℃を超えると局部的
な焼結が急速に進行し、気孔の閉塞を生じ、緻密質の焼
結体は得られない。That is, there is an inflection point in the increase in the progress of deoxidation at approximately 300°C, and below 300°C, substantial sintering does not occur, but deoxidation progresses slowly and the reaction takes too long, making it difficult to apply it industrially. Can not. On the other hand, if the temperature exceeds 600°C, local sintering progresses rapidly, pores are blocked, and a dense sintered body cannot be obtained.
従って、焼結が始まる前に成形体と水素ガスを反応させ
れば鉄粉表面の酸素が完全に除かれ、焼結温度に達した
時に健全な焼結体が得られる。Therefore, if the compact is reacted with hydrogen gas before sintering begins, oxygen on the surface of the iron powder will be completely removed, and a healthy sintered compact will be obtained when the sintering temperature is reached.
〔実施例〕
炭素含有量3.1重量%、酸素含有量8.0重量%1、
平均粒度7,6μmの破砕鉄粉を760℃で2時間加熱
し、軽い焼結体を作り、これを渦流粉砕機でほぐしたと
ころ、炭素含有IQ、 03重量%、酸素含有量0.6
重量%、平均粒度8,4μmの原料粉を得た。[Example] Carbon content 3.1% by weight, oxygen content 8.0% by weight1,
Crushed iron powder with an average particle size of 7.6 μm was heated at 760°C for 2 hours to form a light sintered body, which was loosened using a vortex mill. Carbon content IQ: 0.3% by weight, oxygen content: 0.6
A raw material powder having a weight percent and an average particle size of 8.4 μm was obtained.
パラフィン、ワックス、ポリエチレンから構成されるバ
インダーを鉄粉に対し10重量%混練して、通常の条件
で3 X 6 x5Qmm射出成形した。A binder composed of paraffin, wax, and polyethylene was kneaded with iron powder in an amount of 10% by weight, and the mixture was injection molded to a size of 3 x 6 x 5 Q mm under normal conditions.
これを大気雰囲気の脱脂炉に装入し、80℃から300
℃まで6℃/hr、で38時間かけて昇温した。脱脂処
理後の重量変化は、7.5%であった。この重量変化は
、バインダー量の82.5%に相当する。This was charged into a degreasing furnace in an air atmosphere, and heated from 80°C to 300°C.
The temperature was raised to 6°C/hr over 38 hours. The weight change after degreasing was 7.5%. This weight change corresponds to 82.5% of the binder amount.
これに対し、比較のために同一条件で作成した成形体を
窒素雰囲気中で80℃から500℃まで60時間から1
00時間かけて脱脂した場合には、脱脂後膨れ、表面割
れが著しく、140時間かけて初めて欠陥のない脱脂成
形体が得られた。On the other hand, for comparison, molded bodies made under the same conditions were heated from 80°C to 500°C for 60 hours to 1 hour in a nitrogen atmosphere.
When degreasing was carried out for 00 hours, the swelling and surface cracking after degreasing were significant, and a defect-free degreased molded article was obtained for the first time after 140 hours.
次に、この脱脂成形体を焼結するために常温から180
℃/時で昇温し、1300℃に5時間保持した。Next, in order to sinter this degreased molded body,
The temperature was raised at a rate of 1300° C./hour and maintained at 1300° C. for 5 hours.
この際800℃から水素を100+n 1 /分流して
得られた焼結体の密度は6,8、相対密度は87%であ
った。At this time, the density of the sintered body obtained by flowing hydrogen at 100+n 1 /minute from 800° C. was 6.8, and the relative density was 87%.
内部組織を顕微鏡によって観察した結果、内面に酸化皮
膜を有する空孔部が散見された。As a result of observing the internal structure using a microscope, pores with an oxide film on the inner surface were found here and there.
これに対して、同じ熱処理パターンで300℃からから
水素を流した焼結体の密度は7.2、相対密度が92%
であった。この内部組織を顕微鏡で観察した結果、空孔
部の内壁に酸化膜は殆ど存在しなかった。On the other hand, the density of the sintered body in which hydrogen was flowed from 300℃ using the same heat treatment pattern was 7.2, and the relative density was 92%.
Met. When this internal structure was observed under a microscope, it was found that almost no oxide film was present on the inner walls of the pores.
本発明の焼結法により、以下の効果を奏することができ
る。The sintering method of the present invention can provide the following effects.
(1) 大気中、低温での急速脱脂が可能になり、作
業効率が上がる。(1) Rapid degreasing is possible in the atmosphere at low temperatures, increasing work efficiency.
(2)原料粉末に異形粉末を含有している破砕粉を使用
しても短時間の脱脂が可能である。(2) Degreasing can be carried out in a short time even if crushed powder containing irregularly shaped powder is used as the raw material powder.
(3] 酸化膜表面を有している原料鉄粉でも、高密
度高純度の鉄焼結体を得ることができる。(3) High-density, high-purity iron sintered bodies can be obtained even with raw iron powder having an oxide film surface.
(4) したがって、それ自体工業的に低価格で得るこ
とができる破砕微粉鉄粉を射出成形用として大幅に使用
することができる。(4) Therefore, crushed fine iron powder, which itself can be obtained industrially at low cost, can be used to a large extent for injection molding.
特許出願人 吉川工業 株式会社
代 理 人 小 堀 益
手続補正書
平成元年5月22日
平成1年特 許 願第92280号
2、発明の名称
鉄焼結製品の製造方法
3、補正をする者
事件との関係 特許出願人
4、代理人
住 所 ■812 福岡市博多区博多駅前1丁目1−
1博多新三井ビル台(092) 451−8781(リ
明細書第5頁第10行「焼結する。しかも、この条件
では、」を下記の通り補正する。Patent Applicant: Yoshikawa Kogyo Co., Ltd. Agent: Kobori Procedural Amendment May 22, 1989, 1999 Patent Application No. 92280 2, Title of Invention: Process for manufacturing iron sintered products 3, Person making the amendment Relationship to the incident Patent applicant 4, agent address ■812 1-1-1 Hakata Ekimae, Hakata-ku, Fukuoka City
1 Hakata Shin-Mitsui Building Dai (092) 451-8781 (Li) Page 5, line 10 of the specification, "Sintered. Moreover, under these conditions," is corrected as follows.
「焼結する方法か真空中で焼結する方法がある。“There is a method of sintering or a method of sintering in a vacuum.
しかも、前の条件では、」
(2)同第5頁下から第5行口得られない。」の次に下
記の文を加入する。Moreover, under the previous conditions, ``(2) Page 5, line 5 from the bottom cannot be obtained. '', add the following sentence.
「勿論、後者の真空焼結法でも酸化被膜が除かれないの
で密度は上がらない。」``Of course, the latter vacuum sintering method does not remove the oxide layer, so the density does not increase.''
Claims (1)
を用いて射出成形を行い、この射出成形体を大気雰囲気
中で、350℃以下の温度で脱脂処理し、さらに、30
0〜600℃で水素還元を行ったのち焼結を行う鉄焼結
製品の製造方法。1. Pulverize quenched high carbon iron, perform injection molding using fine iron powder that has been decarburized, degrease the injection molded product at a temperature of 350°C or less in an air atmosphere, and further
A method for manufacturing iron sintered products, which involves performing hydrogen reduction at 0 to 600°C and then sintering.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1092280A JPH02270902A (en) | 1989-04-11 | 1989-04-11 | Manufacture of iron sintered product |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1092280A JPH02270902A (en) | 1989-04-11 | 1989-04-11 | Manufacture of iron sintered product |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02270902A true JPH02270902A (en) | 1990-11-06 |
Family
ID=14049994
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1092280A Pending JPH02270902A (en) | 1989-04-11 | 1989-04-11 | Manufacture of iron sintered product |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02270902A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2000012247A1 (en) * | 1998-08-27 | 2000-03-09 | Alliedsignal Inc. | Process for debinding and sintering metal injection molded parts made with an aqueous binder |
-
1989
- 1989-04-11 JP JP1092280A patent/JPH02270902A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2000012247A1 (en) * | 1998-08-27 | 2000-03-09 | Alliedsignal Inc. | Process for debinding and sintering metal injection molded parts made with an aqueous binder |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5380476A (en) | Method of debinding for injection molded objects | |
| JPH0254733A (en) | Manufacture of ti sintered material | |
| US4284431A (en) | Method for the production of sintered powder ferrous metal preform | |
| US2352316A (en) | Method of producing shaped bodies from powdery ferrous material | |
| JPH02270902A (en) | Manufacture of iron sintered product | |
| KR20170115374A (en) | Method for manufacturing iron-based powders | |
| JPH04285102A (en) | Production of sintered body | |
| JPH0222121B2 (en) | ||
| KR100637656B1 (en) | Method for producing ferro molybdenum using a reduction reaction and ferro molybdenum prepared using the method | |
| US8147961B2 (en) | Carburized metal material and producing method thereof | |
| KR100960624B1 (en) | Method for producing oxide dispersed alloy using wet mixing of yttrium salt and oxide dispersed alloy prepared by | |
| JPH0225501A (en) | Stainless steel powder for injection forming and production of compound for injection forming and stainless steel sintered body | |
| JP2793938B2 (en) | Manufacturing method of sintered metal parts by metal powder injection molding method | |
| JPS58722B2 (en) | Reduction sintering method for high speed steel powder | |
| CN120587488A (en) | A strong and tough metastable medium-entropy alloy and its preparation method | |
| JPH03173702A (en) | Production of sintered body | |
| JPS6389636A (en) | Manufacture of ti-alloy product | |
| CN116426784B (en) | Method for preparing particle reinforced eutectic high-entropy alloy based on laser powder bed melting technology | |
| Zhu et al. | Enhancing the densification and fatigue resistance of metal-injection-molded 4J29 Kovar alloy using hot isostatic pressing | |
| JPH01184203A (en) | Alloy powder for injected-compacting | |
| JPH0257607A (en) | Injection-molding powder and production of metallic sintered body | |
| JP2571231B2 (en) | Manufacturing method of metal sintered body | |
| JPH0257613A (en) | Production of sintered metallic material and its raw powder | |
| JPH03257101A (en) | Method for degreasing powder green compact | |
| JPH02263901A (en) | Powder for metal injection molding and its manufacturing method |