JPH10265805A - Metallic powder sintered compact and its production - Google Patents
Metallic powder sintered compact and its productionInfo
- Publication number
- JPH10265805A JPH10265805A JP7579297A JP7579297A JPH10265805A JP H10265805 A JPH10265805 A JP H10265805A JP 7579297 A JP7579297 A JP 7579297A JP 7579297 A JP7579297 A JP 7579297A JP H10265805 A JPH10265805 A JP H10265805A
- Authority
- JP
- Japan
- Prior art keywords
- compound
- organic binder
- green
- metal powder
- powder sintered
- 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.)
- Withdrawn
Links
- 239000000843 powder Substances 0.000 title claims abstract description 42
- 238000004519 manufacturing process Methods 0.000 title claims description 15
- 239000011230 binding agent Substances 0.000 claims abstract description 61
- 238000010438 heat treatment Methods 0.000 claims abstract description 36
- 238000005238 degreasing Methods 0.000 claims abstract description 29
- 238000002411 thermogravimetry Methods 0.000 claims abstract description 26
- 238000013329 compounding Methods 0.000 claims abstract description 22
- 238000005245 sintering Methods 0.000 claims abstract description 13
- 150000001875 compounds Chemical class 0.000 claims description 60
- 239000002184 metal Substances 0.000 claims description 39
- 229910052751 metal Inorganic materials 0.000 claims description 39
- 230000004580 weight loss Effects 0.000 claims description 16
- 239000005038 ethylene vinyl acetate Substances 0.000 claims description 8
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 7
- 239000012188 paraffin wax Substances 0.000 claims description 7
- 239000004793 Polystyrene Substances 0.000 claims description 6
- 238000001746 injection moulding Methods 0.000 claims description 6
- 229920002223 polystyrene Polymers 0.000 claims description 5
- 239000012778 molding material Substances 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims 1
- 238000004458 analytical method Methods 0.000 abstract 1
- 239000013585 weight reducing agent Substances 0.000 description 11
- 238000002156 mixing Methods 0.000 description 10
- 238000005336 cracking Methods 0.000 description 7
- 239000001993 wax Substances 0.000 description 4
- 239000004952 Polyamide Substances 0.000 description 3
- 239000004743 Polypropylene Substances 0.000 description 3
- 239000006096 absorbing agent Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 3
- 229920002647 polyamide Polymers 0.000 description 3
- 239000004926 polymethyl methacrylate Substances 0.000 description 3
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- -1 polypropylene Polymers 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- HTSGKJQDMSTCGS-UHFFFAOYSA-N 1,4-bis(4-chlorophenyl)-2-(4-methylphenyl)sulfonylbutane-1,4-dione Chemical compound C1=CC(C)=CC=C1S(=O)(=O)C(C(=O)C=1C=CC(Cl)=CC=1)CC(=O)C1=CC=C(Cl)C=C1 HTSGKJQDMSTCGS-UHFFFAOYSA-N 0.000 description 1
- 235000021355 Stearic acid Nutrition 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- DQXBYHZEEUGOBF-UHFFFAOYSA-N but-3-enoic acid;ethene Chemical compound C=C.OC(=O)CC=C DQXBYHZEEUGOBF-UHFFFAOYSA-N 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- NLFBCYMMUAKCPC-KQQUZDAGSA-N ethyl (e)-3-[3-amino-2-cyano-1-[(e)-3-ethoxy-3-oxoprop-1-enyl]sulfanyl-3-oxoprop-1-enyl]sulfanylprop-2-enoate Chemical compound CCOC(=O)\C=C\SC(=C(C#N)C(N)=O)S\C=C\C(=O)OCC NLFBCYMMUAKCPC-KQQUZDAGSA-N 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 1
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000004881 precipitation hardening Methods 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000008117 stearic acid Substances 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 238000002076 thermal analysis method Methods 0.000 description 1
Landscapes
- Powder Metallurgy (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、金属粉末と有機バ
インダとからなるコンパウンドを射出成形して得られた
グリーンパーツを脱脂、焼結して成る金属粉末焼結体及
びその製造方法に関する。The present invention relates to a metal powder sintered body obtained by degreasing and sintering a green part obtained by injection molding a compound comprising a metal powder and an organic binder, and a method for producing the same.
【0002】[0002]
【従来の技術】従来の金属粉末焼結体の製造方法として
は、特公平3−46522号公報に記載されたものが挙
げられる。2. Description of the Related Art As a conventional method for producing a metal powder sintered body, there is a method described in Japanese Patent Publication No. 3-46522.
【0003】上記公報には、グリーンパーツを吸収体上
に載置して加熱し、吸収体の毛細管現象による圧力ヘッ
ドによって溶融した有機バインダを前記グリーンパーツ
から吸収体へと流動させるとともに、溶融した有機バイ
ンダを分解、ガス化してアウトガスとしてグリーンパー
ツから除去する脱脂(脱バインダ)を行い、しかる後、
焼結して金属粉末焼結体を得る製造方法が記載されてい
る。[0003] The above publication discloses that a green part is placed on an absorber and heated, and an organic binder melted by a pressure head due to a capillary phenomenon of the absorber is caused to flow from the green part to the absorber and is melted. Degreasing the organic binder, gasifying it and removing it as green outgas from the green parts (binder removal).
A production method for sintering to obtain a metal powder sintered body is described.
【0004】[0004]
【発明が解決しようとする課題】上述のような金属粉末
焼結体の製造方法に用いられるコンパウンドは、成形時
の潤滑性、保形性等を付加させるために数種類の有機バ
インダが配合され、これらの有機バインダはそれぞれ特
有の融点、沸点等の物性を有するので脱脂時にグリーン
パーツからアウトガスの発生する温度領域は、配合され
た有機バインダの種類によって種々存在する。The compound used in the method for producing a metal powder sintered body as described above contains several kinds of organic binders in order to add lubricity and shape retention during molding. Since these organic binders each have specific properties such as a melting point and a boiling point, there are various temperature ranges in which outgas is generated from the green parts at the time of degreasing depending on the type of the organic binder blended.
【0005】グリーンパーツからアウトガスが発生する
温度領域を調べるには、グリーンパーツ、或いはその材
料であるコンパウンドを熱重量分析するのが一般的であ
る。図1は、あるコンパウンドにて射出成形した7.7
2gのグリーンパーツを熱重量分析した結果を示すグラ
フであって、縦軸左は加熱温度[℃]、縦軸右はグリー
ンパーツの重量[g]、横軸は加熱時間[h]を示し、
曲線Aは加熱によるグリーンパーツの重量の変化、傾き
Dは加熱の際の昇温速度を示す。[0005] In order to examine the temperature region in which outgas is generated from the green parts, it is general to carry out thermogravimetric analysis of the green parts or a compound as a material thereof. FIG. 1 shows 7.7 injection-molded with a compound.
It is a graph which shows the result of thermogravimetric analysis of 2 g of green parts, the left vertical axis shows the heating temperature [° C.], the right vertical axis shows the weight [g] of the green parts, and the horizontal axis shows the heating time [h],
Curve A indicates the change in weight of the green part due to heating, and slope D indicates the rate of temperature rise during heating.
【0006】図1に示す通り、グリーンパーツの重量は
領域Bと領域Cとで大きく減少しており、領域Bと領域
Cとはその温度領域および曲線Aの傾きが異なることか
ら、異なる成分の有機バインダが段階的にアウトガスと
なってグリーンパーツから除去されていることが解る。As shown in FIG. 1, the weight of the green part is greatly reduced in the region B and the region C. Since the temperature region and the slope of the curve A are different between the region B and the region C, different components have different components. It can be seen that the organic binder is gradually outgassed and removed from the green parts.
【0007】領域Bおよび領域Cに見られるような大き
な重量減少の起こる温度領域で急激な昇温を行うと、大
量に発生したアウトガスがグリーンパーツ内部に閉じ込
められるので、焼結後の金属粉末焼結体にワレやフクレ
といった欠陥が生じ、外観品質が低下する。If the temperature is rapidly increased in a temperature region where a large weight loss occurs as seen in regions B and C, a large amount of outgas is confined inside the green parts, so that the sintered metal powder is sintered. Defects such as cracks and blisters occur in the aggregate, and the appearance quality is reduced.
【0008】ワレやフクレの発生を防ぐためには、アウ
トガスがグリーンパーツ内部に溜まることのないよう、
単位時間当たりのアウトガスの発生量を制御する、即
ち、グリーンパーツの重量が大きく減少する温度領域
(図1においては、領域B、領域C)での昇温速度を適
正化する必要がある。In order to prevent cracks and blisters from occurring, make sure that outgas does not collect inside the green parts.
It is necessary to control the amount of outgas generated per unit time, that is, to optimize the rate of temperature rise in the temperature region (region B and region C in FIG. 1) where the weight of the green parts is greatly reduced.
【0009】しかしながら、適正な昇温速度を決定する
には、一般的に予め数種類の昇温速度を任意に決めて脱
脂、焼結を行った結果、最適な昇温速度を選ぶ、という
トライアンドエラー的な手法が多用されていたため、脱
脂時の昇温速度を決定するのに多くの時間を必要とし、
生産の効率が悪かった。However, in order to determine an appropriate heating rate, generally, several kinds of heating rates are arbitrarily determined in advance, and after degreasing and sintering, an optimum heating rate is selected. Since many error-based methods were used, it took a lot of time to determine the heating rate during degreasing,
Production efficiency was poor.
【0010】本発明は、上記従来技術の課題に鑑みてな
されたものであり、脱脂時の昇温速度を効率的に決定
し、しかも、金属粉末焼結体にワレやフクレ等の欠陥を
防止して優れた外観の金属粉末焼結体を製造する方法を
提供することを目的とする。The present invention has been made in view of the above-mentioned problems of the prior art, and efficiently determines a heating rate during degreasing, and prevents defects such as cracks and blisters on a sintered metal powder. It is an object of the present invention to provide a method for producing a metal powder sintered body having excellent appearance.
【0011】[0011]
【課題を解決する手段】請求項1の発明は、金属粉末と
有機バインダとからなる射出成形用材料(以下、コンパ
ウンドと称する)にて射出成形を行い、得られたグリー
ンパーツを脱脂してブラウンパーツとし、ブラウンパー
ツを焼結して金属粉末焼結体を得る金属粉末焼結体の製
造方法において、グリーンパーツを脱脂する以前に、グ
リーンパーツもしくはグリーンパーツを構成するコンパ
ウンドの熱重量分析を行い、熱重量分析時の昇温速度を
Vb[℃/h]、熱重量分析時のコンパウンドの重量減
少率をWb[%/h]、グリーンパーツを構成するコン
パウンドの有機バインダ配合重量部をRb[wt%]、
基準とするコンパウンドの有機バインダ配合重量部をR
a[wt%]、基準とするコンパウンドから成るグリー
ンパーツを脱脂する際、焼結後の金属粉末焼結体にワレ
やフクレを生じないための単位時間当たりの重量減少率
をWa[%/h]、とし、Ra=10[wt%]、か
つ、Wa=1[%/h]としたとき、下記数3を満たす
昇温速度Va[℃/h]でグリーンパーツを脱脂するこ
とを特徴とする。According to a first aspect of the present invention, an injection molding material (hereinafter, referred to as a compound) comprising a metal powder and an organic binder is subjected to injection molding, and the obtained green parts are degreased to obtain brown. In the method of manufacturing a metal powder sintered body that obtains a metal powder sintered body by sintering a brown part as a part, a thermogravimetric analysis of the green part or the compound constituting the green part is performed before the green part is degreased The rate of temperature rise during thermogravimetric analysis is Vb [° C./h], the weight loss rate of the compound during thermogravimetric analysis is Wb [% / h], and the compounding part of the organic binder of the compound constituting the green part is Rb [ wt%],
The compounding amount of the organic binder of the compound as the standard is R
a [wt%], when degreasing a green part composed of a reference compound, the weight loss rate per unit time to prevent cracks and blisters in a sintered metal powder sintered body is represented by Wa [% / h. When Ra = 10 [wt%] and Wa = 1 [% / h], the green parts are degreased at a heating rate Va [° C / h] that satisfies Equation 3 below. I do.
【0012】[0012]
【数3】 (Equation 3)
【0013】請求項2の発明は、請求項1記載の金属粉
末焼結体の製造方法において、熱重量分析を行ったコン
パウンドと同じ有機バインダから構成されるとともに、
熱重量分析を行ったコンパウンドとは異なる有機バイン
ダ配合重量部であるコンパウンドの有機バインダ配合重
量部をRcとし、有機バインダ配合重量部がRcである
コンパウンドでグリーンパーツを成形し、下記数4を満
たす昇温速度Va′[℃/h]で上記グリーンパーツを
脱脂することを特徴とする。According to a second aspect of the present invention, there is provided the method for producing a metal powder sintered body according to the first aspect, wherein the metal binder comprises the same organic binder as the compound subjected to the thermogravimetric analysis.
The organic binder compounding part by weight of the compound which is different from the compound subjected to the thermogravimetric analysis is Rc, and the organic binder compounding part by weight is Rc, and a green part is formed by the compound having the organic binder compounding part by Rc, and the following formula 4 is satisfied. The green parts are degreased at a heating rate Va ′ [° C./h].
【0014】[0014]
【数4】 (Equation 4)
【0015】請求項3に係る発明は、請求項1または請
求項2記載の金属粉末焼結体の製造方法において、コン
パウンドには、有機バインダとして、パラフィンワック
スと、ポリスチレンと、エチレン−酢酸ビニル共重合体
とが含まれていることを特徴とする。According to a third aspect of the present invention, in the method for producing a metal powder sintered body according to the first or second aspect, the compound includes paraffin wax, polystyrene, and ethylene-vinyl acetate as an organic binder. And a polymer.
【0016】請求項4に係る発明は、請求項1乃至請求
項3のいずれかに記載の金属粉末焼結体の製造方法にて
製造される外観に優れた金属粉末焼結体であることを特
徴とする。 (作用)本発明によると、グリーンパーツもしくはグリ
ーンパーツを構成するコンパウンドの熱重量分析を予め
行い、結果を数3に代入することにより、該コンパウン
ドの有機バインダ配合重量部が基準とするコンパウンド
の有機バインダ配合重量部から外れた重量部であって
も、該コンパウンドの有機バインダ配合重量部を基準と
するコンパウンドの有機バインダ配合重量部(10重量
部)に換算したときに、単位時間当たりの重量減少率が
1[%/h]となるような昇温速度が設定される。According to a fourth aspect of the present invention, there is provided a metal powder sintered body having an excellent appearance manufactured by the method for manufacturing a metal powder sintered body according to any one of the first to third aspects. Features. (Function) According to the present invention, thermogravimetric analysis of a green part or a compound constituting the green part is performed in advance, and the result is substituted into Equation 3 so that the organic binder of the compound is based on the compounding part by weight of the organic binder of the compound. Even if the weight part deviates from the binder weight part, the weight loss per unit time when converted into the organic binder weight part (10 weight parts) of the compound based on the organic binder weight part of the compound. The heating rate is set such that the rate becomes 1 [% / h].
【0017】尚、上述の数3は、以下のようにして導き
出したものである。図1に示す曲線Aを経過時間で微分
すると単位時間当たりの重量減少量[g/h]が求めら
れる。The above equation (3) is derived as follows. When the curve A shown in FIG. 1 is differentiated with respect to the elapsed time, the weight reduction [g / h] per unit time is obtained.
【0018】この単位時間当たりの重量減少量は、単位
時間当たりの発生ガス量に相当し、有機バインダ配合重
量部及び加熱条件が同一であれば、グリーンパーツ(熱
重量分析を行うコンパウンドに相当)の体積と有機バイ
ンダの種類により決定される。The amount of weight loss per unit time corresponds to the amount of gas generated per unit time, and green parts (corresponding to a compound for performing thermogravimetric analysis) if the organic binder blending parts and heating conditions are the same. And the type of organic binder.
【0019】この単位時間当たりの重量減少量と脱脂前
のグリーンパーツの重量との比率(百分率)が単位時間
当たりの重量減少率[%/h]であり、単位時間当たり
の重量減少率は、有機バインダの種類及び加熱条件(昇
温速度)が同一であれば、グリーンパーツの体積を考慮
する必要なく、有機バインダ配合重量部が多い程大きく
なる。The ratio (percentage) of the weight loss per unit time to the weight of the green part before degreasing is the weight reduction rate per unit time [% / h], and the weight reduction rate per unit time is: If the type of the organic binder and the heating conditions (heating rate) are the same, the volume of the green parts does not need to be considered, and the larger the organic binder compounding part is, the larger it becomes.
【0020】以上のことから、昇温速度を適正化すべく
単位時間当たりの発生ガス量を制御することは、単位時
間当たりの重量減少率を制御することに等しいことが解
る。一方、発明者らがコンパウンドの性質について鋭意
研究を行った結果、金属粉末に対する有機バインダ配合
重量部が10重量部(10[wt%])のときを基準と
するコンパウンドの有機バインダ配合重量部Raとした
場合、脱脂工程の全温度領域に渡って単位時間当たりの
重量減少率Waが1[%/h]を超えるとになると、焼
結後の製品にワレやフクレが発生し、外観品質が低下す
ることを知見した。From the above, it can be seen that controlling the amount of gas generated per unit time to optimize the heating rate is equivalent to controlling the rate of weight reduction per unit time. On the other hand, the inventors have conducted intensive studies on the properties of the compound, and as a result, based on the case where the amount of the organic binder mixed with the metal powder is 10 parts by weight (10 [wt%]), the compounded organic binder mixed part Ra of the compound is based on Ra. When the weight loss rate Wa per unit time exceeds 1% / h over the entire temperature range of the degreasing step, cracks and blisters are generated in the sintered product, and the appearance quality is reduced. Was found to decrease.
【0021】また、基準とするコンパウンドの有機バイ
ンダ配合重量部Ra以外の任意の有機バインダ配合重量
部Rbであるコンパウンドの場合、ワレやフクレを発生
しないための重量減少率の上限は、基準とするコンパウ
ンドの有機バインダ配合重量部Raと、有機バインダ配
合重量部Rbとの比率(Rb/Ra:有機バインダ配合
重量部比)に比例することを発見した。In addition, in the case of a compound which is an optional organic binder blending part by weight Rb other than the organic binder blending part by weight Ra of the reference compound, the upper limit of the weight reduction rate for preventing cracking and blistering is defined as the standard. It has been found that the ratio is proportional to the ratio of the organic binder compounding parts by weight Ra of the compound to the organic binder compounding parts by weight Rb (Rb / Ra: organic binder compounding parts ratio).
【0022】この点について、表1 を用いて説明する。This point will be described with reference to Table 1.
【0023】[0023]
【表1】 [Table 1]
【0024】表1は、基準とするコンパウンドを含む4
種類のコンパウンドについて、その有機バインダ成分お
よび有機バインダ配合重量部Ra,Rbと、焼結後の金
属粉末焼結体にワレやフクレを生じない重量減少率との
対応関係を示すものである。Table 1 shows the four compounds including the reference compound.
It shows the correspondence between the organic binder components and the organic binder blending parts by weight Ra and Rb of each type of compound, and the weight reduction rate at which cracks and blisters do not occur in the sintered metal powder after sintering.
【0025】表1 において、基準とするコンパウンド
は、パラフィンワックス(WAX)、ポリスチレン(P
S)、エチレン−酢酸ビニル共重合体(EVA)、アク
リル(PMMA)を主成分とし、その有機バインダ配合
重量部はRa=10wt%で、ワレやフクレを生じない
重量減少率の上限(MAX)は、約1.0[%/h]で
ある。In Table 1, the reference compounds were paraffin wax (WAX) and polystyrene (P
S), ethylene-vinyl acetate copolymer (EVA), acrylic (PMMA) as the main components, and the organic binder compounding part by weight is Ra = 10 wt%, and the upper limit of the weight reduction rate that does not cause cracking or blistering (MAX) Is about 1.0 [% / h].
【0026】上記基準とするコンパウンドに対し、コン
パウンドIは、WAX、PS、PP(ポリプロピレ
ン)、PMMAを主成分とし、有機バインダ配合重量部
はRb=11wt%で、ワレやフクレを生じない重量減
少率の上限(MAX)は、約1.1[%/h]である。In contrast to the above-mentioned compound, compound I is mainly composed of WAX, PS, PP (polypropylene) and PMMA, and the compounding part by weight of the organic binder is Rb = 11 wt%, so that weight reduction without cracking or blistering occurs. The upper limit (MAX) of the rate is about 1.1 [% / h].
【0027】また、コンパウンドIIは、WAX、PAを
主成分とし、有機バインダ配合重量部はRb=13wt
%で、ワレやフクレを生じない重量減少率の上限(MA
X)は、約1.3[%/h]である。The compound II contains WAX and PA as main components, and the compounding part by weight of the organic binder is Rb = 13 wt.
%, The upper limit of the weight loss rate that does not cause cracks or blisters (MA
X) is about 1.3 [% / h].
【0028】また、コンパウンドIIIは、WAX、ポリ
アミド(PA)、EVA、PMMAを主成分とし、有機
バインダ配合重量部はRb=6wt%で、ワレやフクレ
を生じない重量減少率の上限(MAX)は、約0.6
[%/h]である。The compound III contains WAX, polyamide (PA), EVA, and PMMA as main components, and the compounding part by weight of the organic binder is Rb = 6 wt%, and the upper limit of the weight reduction rate which does not cause cracking or blistering (MAX) Is about 0.6
[% / H].
【0029】表1から、基準とするコンパウンドの有機
バインダ配合重量部Raと、その他のコンパウンドI〜I
IIの有機バインダ配合重量部Rbとの比率Rb/Raを
とると、その他のコンパウンドI〜IIIにおけるワレやフ
クレを発生しないための重量減少率は、比率Rb/Ra
を比例係数として、基準とするコンパウンドにおけるワ
レやフクレを発生しないための重量減少率に比例するこ
とがわかる。From Table 1, it can be seen that the organic binder blending parts by weight Ra of the reference compound and the other compounds I to I
Taking the ratio Rb / Ra with the organic binder blending part by weight Rb of II, the weight reduction rate of the other compounds I to III for preventing cracks and blisters is represented by the ratio Rb / Ra.
It can be understood that the proportional coefficient is proportional to the weight reduction rate for preventing generation of cracks and blisters in the reference compound.
【0030】さらに、任意の有機バインダ配合重量部R
bであるコンパウンドを任意の昇温速度Vbで熱重量分
析した時の重量減少率Wb[%/h]と、上記単位時間
当たりの重量減少率Wa[%/h]との比率(Wa/W
b)、及び、上記有機バインダ配合重量部比の逆数(R
a/Rb)を上記熱分析時の昇温速度Vb[℃/h]に
乗して得た値、即ち、昇温速度Vaは、焼結後の金属粉
末焼結体にワレやフクレが発生しない昇温速度の上限で
あることを見出した。Further, an optional amount of an organic binder compounded by weight R
b) The ratio (Wa / W) of the weight loss rate Wb [% / h] when performing thermogravimetric analysis at an arbitrary heating rate Vb and the weight loss rate Wa [% / h] per unit time.
b) and the reciprocal (R
a / Rb) multiplied by the temperature rise rate Vb [° C./h] at the time of the thermal analysis, that is, the temperature rise rate Va is such that cracks and blisters occur in the sintered metal powder after sintering. Was found to be the upper limit of the heating rate.
【0031】これらの結果から数3を導くに至った。ま
た、熱重量分析を行ったコンパウンドと同じ有機バイン
ダから構成されるとともに、熱重量分析を行ったコンパ
ウンドとは異なる有機バインダ配合重量部であるコンパ
ウンドの有機バインダ配合重量部Rcと、熱重量分析を
行ったコンパウンドの有機バインダ配合重量部Rbとの
比率(Rc/Rb)の逆数を、上記昇温速度Vaに乗し
て得た値、即ち、昇温速度Va′は、焼結後の金属粉末
焼結体にワレやフクレが発生しない昇温速度の上限であ
ることを見出し、数4を導くに至った。From these results, Equation 3 was derived. In addition, the thermogravimetric analysis is performed by using the same organic binder as the compound subjected to the thermogravimetric analysis, and the organic binder compounding part by weight Rc of the compound which is different from the compound subjected to the thermogravimetric analysis. The value obtained by multiplying the reciprocal of the ratio (Rc / Rb) of the compound obtained and the organic binder blending part by weight Rb by the above-mentioned heating rate Va, that is, the heating rate Va ′ is the value of the sintered metal powder. They found that the upper limit of the heating rate was such that cracks and blisters did not occur in the sintered body, and led to Equation 4.
【0032】[0032]
(実施の形態1)本実施の形態について図2を用いて説
明する。(Embodiment 1) This embodiment will be described with reference to FIG.
【0033】図2は本実施の形態でグリーンパーツ1の
外観形状および寸法を示している。図2に示すグリーン
パーツ1は、幅12mm、高さ8mm、長さ20mmで
あり、1つの側面に長さ方向の溝を有し、幅方向の断面
が凹字形状を呈している。FIG. 2 shows the external shape and dimensions of the green part 1 in this embodiment. The green part 1 shown in FIG. 2 has a width of 12 mm, a height of 8 mm, and a length of 20 mm, has a longitudinal groove on one side surface, and has a concave cross section in the width direction.
【0034】上記グリーンパーツ1は、パラフィンワッ
クス、アクリル、ポリスチレン、エチレン−酢酸ビニル
共重合体(EVA)を主成分とした有機バインダをSU
S316L粉末に対して11重量部(Rb=11[wt
%])配合して混練したコンパウンドを成形して得たも
のである。The green part 1 is made of an organic binder mainly composed of paraffin wax, acrylic, polystyrene, and ethylene-vinyl acetate copolymer (EVA).
11 parts by weight (Rb = 11 [wt.
%]) Obtained by molding a compounded and kneaded compound.
【0035】上記グリーンパーツ1を脱脂するに当た
り、予め熱重量分析機(TGA)を用い、Vb=50
[℃/h]の昇温速度でグリーンパーツ1を加熱して熱
重量分析を行った結果、熱重量分析時の重量減少率は最
大でWb=2.2[%/h]であった。Before degreasing the green part 1, a thermogravimetric analyzer (TGA) was used to obtain Vb = 50.
The thermogravimetric analysis was performed by heating the green part 1 at a rate of temperature rise of [° C./h]. As a result, the maximum weight loss rate in the thermogravimetric analysis was Wb = 2.2 [% / h].
【0036】尚、重量に変化がなくなる温度は370℃
であった。次に、上記Vb及びWb、並びに、基準とす
るコンパウンドの有機バインダ配合重量部Ra=10
[wt%]、基準とするコンパウンドから成るグリーン
パーツを脱脂する際、焼結後の金属粉末にワレやフクレ
を生じないための単位時間当たりの重量減少率Wa=1
[%/h]を数3に代入し、脱脂時の昇温速度をVa=
20.7[℃/h]と求めた。The temperature at which the weight does not change is 370 ° C.
Met. Next, the above-mentioned Vb and Wb, and the organic binder blending part by weight of the reference compound Ra = 10
[Wt%], weight loss per unit time Wa = 1 to prevent cracking or blistering in the sintered metal powder when degreasing a green part made of a reference compound
[% / H] is substituted into Equation 3, and the temperature rising rate at the time of degreasing is Va =
It was determined to be 20.7 [° C./h].
【0037】次に、常温から、脱脂が終了する370℃
まで昇温速度Va=20.7[℃/h]で昇温し、37
0℃で5時間保持した後脱脂を終了した。尚、常温から
370℃まで昇温する時間は16時間54分であった。Next, from normal temperature, 370 ° C. at which degreasing is completed
Up to Va = 20.7 [° C./h]
After maintaining at 0 ° C. for 5 hours, degreasing was completed. The time required to raise the temperature from room temperature to 370 ° C. was 16 hours and 54 minutes.
【0038】そして、得られたブラウンパーツを132
0℃の真空下で焼結し、得られた金属粉末焼結体の外観
を測定したところ、ワレやフクレ等は特に見られず、そ
の外観品質は良好であった。 (実施の形態2)本実施の形態では、グリーンパーツ1
を構成するコンパウンドの有機バインダの成分を上記実
施の形態1と同様とし、有機バインダ配合重量部が10
重量部(Rc=[10wt%])のコンパウンドを用い
て図2に示すグリーンパーツ1を射出成形法により成形
した。Then, the obtained brown parts are
Sintering was performed under a vacuum of 0 ° C., and the appearance of the obtained metal powder sintered body was measured. As a result, no cracks or blisters were observed, and the appearance quality was good. (Embodiment 2) In this embodiment, the green parts 1
The components of the organic binder of the compound are the same as those in the first embodiment, and the compounding amount of the organic binder is 10 parts by weight.
The green part 1 shown in FIG. 2 was molded by an injection molding method using a compound by weight (Rc = [10 wt%]).
【0039】本実施の形態では、有機バインダの成分が
上記実施の形態1と同様であるため、実施の形態1にお
ける数1の結果をそのまま用い、数4に上記Rb、Rc
を代入し、昇温速度Va′=22.7℃/hと求め、実
施の形態1と同様に370℃まで昇温し、370℃で5
時間保持した後、脱脂を終了した。In this embodiment, since the components of the organic binder are the same as those in the first embodiment, the result of the equation (1) in the first embodiment is used as it is, and the above Rb and Rc are used in the equation (4).
Is calculated to obtain a heating rate Va ′ = 22.7 ° C./h, and the temperature is increased to 370 ° C. as in the first embodiment.
After holding for a time, the degreasing was completed.
【0040】尚、常温から370℃まで昇温する時間は
15時間25分であった。そして、得られたグリーンパ
ーツ1を上記実施の形態1と同様の条件で焼結した後、
得られた金属粉末焼結体の外観を測定したところ、ワレ
やフクレ等は特に見られず、その外観品質は良好であっ
た。 (実施の形態3)本実施の形態について図3を用いて説
明する。The time required to raise the temperature from room temperature to 370 ° C. was 15 hours and 25 minutes. Then, after sintering the obtained green part 1 under the same conditions as in the first embodiment,
When the appearance of the obtained metal powder sintered body was measured, cracks, blisters and the like were not particularly observed, and the appearance quality was good. (Embodiment 3) This embodiment will be described with reference to FIG.
【0041】図3は本実施の形態におけるグリーンパー
ツの外観形状および寸法を示している。図3に示すグリ
ーンパーツ2は、1つの側壁が凸状の曲面となっている
立体であり、最大幅18mm、高さ8mm、長さ25m
m、前面の幅12mm、背面の幅10mmとなってい
る。FIG. 3 shows the external shape and dimensions of the green part in the present embodiment. The green part 2 shown in FIG. 3 is a solid body in which one side wall has a convex curved surface, and has a maximum width of 18 mm, a height of 8 mm, and a length of 25 m.
m, the front width is 12 mm, and the back width is 10 mm.
【0042】上記グリーンパーツ2は、パラフィンワッ
クス、ポリスチレン、EVA、ポリプロピレン、ステア
リン酸を主成分とした有機バインダを17−4PH粉末
に対して6重量部配合して混練したコンパウンドを成形
して得たものである。The green part 2 was obtained by molding a compound obtained by mixing and kneading 6 parts by weight of an organic binder mainly composed of paraffin wax, polystyrene, EVA, polypropylene and stearic acid with 17-4PH powder. Things.
【0043】上記グリーンパーツ2を脱脂するに当た
り、予め熱重量分析機(TGA)を用い、Vb=30
[℃/h]の昇温速度でグリーンパーツ2を加熱して熱
重量分析を行った結果、熱重量分析時の重量減少率は最
大でWb=0.8[%/h]であった。Before degreasing the green parts 2, a thermogravimetric analyzer (TGA) was used to obtain Vb = 30.
The thermogravimetric analysis was performed by heating the green part 2 at a rate of temperature rise of [° C./h]. As a result, the maximum weight loss rate in the thermogravimetric analysis was Wb = 0.8 [% / h].
【0044】尚、重量に変化がなくなる温度は350℃
であった。次に、上記Vb及びWb、並びに、基準とす
るコンパウンドの有機バインダ配合重量部Ra=10
[wt%]、基準とするコンパウンドからなるグリーン
パーツを脱脂する際、焼結後の金属粉末にワレやフクレ
を生じないための単位時間当たりの重量減少率Wa=1
[%/h]を数3に代入し、脱脂時の昇温速度をVa=
62.5[℃/h]と求めた。The temperature at which the weight does not change is 350 ° C.
Met. Next, the above-mentioned Vb and Wb, and the organic binder blending part by weight of the reference compound Ra = 10
[Wt%], weight loss per unit time Wa = 1 to prevent cracking or blistering in the sintered metal powder when degreasing a green part composed of a reference compound
[% / H] is substituted into Equation 3, and the temperature rising rate at the time of degreasing is Va =
It was determined to be 62.5 [° C./h].
【0045】この昇温速度でグリーンパーツ2を室温か
ら加熱して脱脂するとパラフィンワックスが急激に軟化
してしまい、グリーンパーツ2の形状が全体的に変形し
てしまう。When the green part 2 is heated from room temperature and degreased at this heating rate, the paraffin wax softens rapidly and the shape of the green part 2 is entirely deformed.
【0046】そのため、グリーンパーツ2の脱脂は、パ
ラフィンワックスの除去がほぼ完了する120℃までを
比較的緩やかな25[℃/h]の昇温速度とし、120
℃を超える温度領域からは62.5[℃/h]で加熱
し、350℃で5時間保持して終了した。Therefore, the green parts 2 are degreased at a relatively gentle rate of 25 [° C./h] until 120 ° C., at which the removal of paraffin wax is almost completed, at a rate of 120 ° C./h.
Heating was performed at 62.5 [° C./h] from the temperature range exceeding ° C., and the temperature was maintained at 350 ° C. for 5 hours, thus completing the process.
【0047】そして、得られたブラウンパーツ2を13
20℃の真空下で焼結し、固溶化熱処理、析出硬化処理
の焼き入れを行って得た金属粉末焼結体は、ワレやフク
レ等が特に見られず、その外観品質は良好であった。 (比較例1)実施の形態1記載のグリーンパーツ1を実
施の形態2で求めた昇温速度(22.7℃)にて加熱脱
脂し、実施の形態1と同様に焼結を行った後、得られた
金属粉末焼結体のワレやフクレを測定した。Then, 13 parts of the obtained brown parts 2 were obtained.
The metal powder sintered body obtained by sintering in a vacuum at 20 ° C. and quenching the solution heat treatment and the precipitation hardening treatment was free from cracks, blisters, etc., and had a good appearance quality. . (Comparative Example 1) After the green part 1 described in the first embodiment is heated and degreased at the heating rate (22.7 ° C.) determined in the second embodiment, and then sintered as in the first embodiment, Then, cracks and blisters of the obtained metal powder sintered body were measured.
【0048】この時の金属粉末焼結体には、上面の中央
部に周辺よりも0.5mmの盛り上がり、つまり、フク
レが認められ、その外観品質は低下していた。 (比較例2)実施の形態2記載のグリーンパーツ1を1
20℃までを25[℃/h]の昇温速度で加熱し、12
0℃を超える温度領域ではTGAによる熱重量分析時で
の昇温速度と同じ昇温速度(Vb=50[℃/h])で
370℃まで加熱し、更に370℃で5時間保持した後
脱脂を終了した。At this time, the metal powder sintered body had a swelling of 0.5 mm at the center of the upper surface from the periphery, that is, blisters were recognized, and the appearance quality was deteriorated. (Comparative Example 2) One green part 1 described in the second embodiment
Heat to 20 ° C at a heating rate of 25 [° C / h],
In the temperature range exceeding 0 ° C., the temperature is increased to 370 ° C. at the same heating rate (Vb = 50 [° C./h]) as in the thermogravimetric analysis by TGA, and further maintained at 370 ° C. for 5 hours, followed by degreasing. Finished.
【0049】これを更に実施の形態1及び実施の形態2
と同様の条件で焼結し、得られた金属粉末焼結体を確認
したところ、上面の中央部が盛り上がって更にワレが発
生し、その外観品質は低下していた。This is further reduced to Embodiments 1 and 2.
Sintering was performed under the same conditions as described above, and the obtained metal powder sintered body was confirmed. As a result, the central portion of the upper surface was raised, further cracking occurred, and the appearance quality was reduced.
【0050】上記各実施の形態及び各比較例の結果から
も解る通り、本発明の方法による効果は明白であり、ワ
レやフクレ等の外観不良のない金属粉末焼結体を製造す
ることが可能となる。As can be seen from the results of each of the above embodiments and comparative examples, the effect of the method of the present invention is clear, and it is possible to manufacture a metal powder sintered body having no defective appearance such as cracks and blisters. Becomes
【0051】[0051]
【発明の効果】本発明によると、ワレやフクレのない優
れた外観の金属粉末焼結体を製造するための脱脂時の昇
温速度を容易に設定すること、即ち、脱脂条件を効率的
に短期間で設定することが可能であり、特にワレやフク
レの発生しやすい厚肉製品を脱脂、焼結する際には効果
的である。According to the present invention, the rate of temperature rise during degreasing for producing a metal powder sintered body having excellent appearance without cracks and blisters can be easily set, that is, the degreasing conditions can be efficiently adjusted. It can be set in a short period of time, and is particularly effective when degreasing and sintering a thick product in which cracks and blisters are easily generated.
【図1】コンパウンドを熱重量分析した結果を示すグラ
フ。FIG. 1 is a graph showing the results of thermogravimetric analysis of a compound.
【図2】実施の形態1及び2におけるグリーンパーツの
形状及び寸法を示す図。FIG. 2 is a diagram illustrating shapes and dimensions of green parts according to the first and second embodiments.
【図3】実施の形態3におけるグリーンパーツの形状及
び寸法を示す図。FIG. 3 is a diagram showing the shape and dimensions of a green part according to a third embodiment.
1、2 グリーンパーツ 1,2 green parts
Claims (4)
成形用材料(以下、コンパウンドと称する)にて射出成
形を行い、得られた成形体(以下、グリーンパーツと称
する)を脱脂してブラウンパーツとし、ブラウンパーツ
を焼結して金属粉末焼結体を得る金属粉末焼結体の製造
方法において、 グリーンパーツを脱脂する以前に、グリーンパーツもし
くはグリーンパーツを構成するコンパウンドの熱重量分
析を行い、 熱重量分析時の昇温速度をVb[℃/h]、 熱重量分析時のコンパウンドの重量減少率をWb[%/
h]、 グリーンパーツを構成するコンパウンドの有機バインダ
配合重量部をRb[wt%]、 基準とするコンパウンドの有機バインダ配合重量部をR
a[wt%]、 基準とするコンパウンドから成るグリーンパーツを脱脂
する際、焼結後の金属粉末焼結体にワレやフクレを生じ
ないための単位時間当たりの重量減少率をWa[%/
h]、 とし、Ra=10[wt%]、かつ、Wa=1[%/
h]としたとき、下記数1を満たす昇温速度Va[℃/
h]でグリーンパーツを脱脂することを特徴とする金属
粉末焼結体の製造方法。 【数1】 An injection molding material (hereinafter, referred to as a compound) comprising a metal powder and an organic binder is subjected to injection molding, and the obtained molded body (hereinafter, referred to as a green part) is degreased to obtain a brown part. And, in the method of manufacturing a metal powder sintered body to obtain a metal powder sintered body by sintering the brown parts, before degreasing the green parts, a thermogravimetric analysis of the green parts or the compounds constituting the green parts, The rate of temperature rise during thermogravimetric analysis was Vb [° C./h], and the weight loss rate of the compound during thermogravimetric analysis was Wb [% /
h], Rb [wt%] is the compounding amount of the organic binder of the compound constituting the green part, and R is the compounding part of the organic binder of the reference compound.
a [wt%], when degreasing a green part composed of a reference compound, the weight loss rate per unit time to prevent cracks and blisters in the sintered metal powder sintered body is represented by Wa [% /
h], and Ra = 10 [wt%] and Wa = 1 [% /
h], the heating rate Va [° C. /
h) degreasing the green parts in step h). (Equation 1)
機バインダから構成されるとともに、熱重量分析を行っ
たコンパウンドとは異なる有機バインダ配合重量部であ
るコンパウンドの有機バインダ配合重量部をRcとし、 有機バインダ配合重量部がRcであるコンパウンドでグ
リーンパーツを成形し、 下記数2を満たす昇温速度Va′[℃/h]で上記グリ
ーンパーツを脱脂することを特徴とする請求項1記載の
金属粉末焼結体の製造方法。 【数2】 2. The composition comprising the same organic binder as the compound subjected to the thermogravimetric analysis, and the organic binder compounding part by weight of the compound which is different from the compound subjected to the thermogravimetric analysis is Rc, 2. The metal according to claim 1, wherein a green part is formed from a compound in which the organic binder compounding part by weight is Rc, and the green part is degreased at a heating rate Va '[° C./h] satisfying the following equation (2). A method for manufacturing a powder sintered body. (Equation 2)
パラフィンワックスと、ポリスチレンと、エチレン−酢
酸ビニル共重合体とが含まれていることを特徴とする請
求項1又は請求項2記載の金属粉末焼結体の製造方法。3. The compound as an organic binder,
The method for producing a metal powder sintered body according to claim 1 or 2, wherein the method includes a paraffin wax, polystyrene, and an ethylene-vinyl acetate copolymer.
金属粉末焼結体の製造方法にて製造される外観に優れた
金属粉末焼結体。4. A metal powder sintered body having an excellent appearance produced by the method for producing a metal powder sintered body according to claim 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7579297A JPH10265805A (en) | 1997-03-27 | 1997-03-27 | Metallic powder sintered compact and its production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7579297A JPH10265805A (en) | 1997-03-27 | 1997-03-27 | Metallic powder sintered compact and its production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH10265805A true JPH10265805A (en) | 1998-10-06 |
Family
ID=13586427
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7579297A Withdrawn JPH10265805A (en) | 1997-03-27 | 1997-03-27 | Metallic powder sintered compact and its production |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH10265805A (en) |
-
1997
- 1997-03-27 JP JP7579297A patent/JPH10265805A/en not_active Withdrawn
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A300 | Withdrawal of application because of no request for examination |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 20040601 |