JPH0721081B2 - Method for producing continuous porous sintered body - Google Patents
Method for producing continuous porous sintered bodyInfo
- Publication number
- JPH0721081B2 JPH0721081B2 JP60124184A JP12418485A JPH0721081B2 JP H0721081 B2 JPH0721081 B2 JP H0721081B2 JP 60124184 A JP60124184 A JP 60124184A JP 12418485 A JP12418485 A JP 12418485A JP H0721081 B2 JPH0721081 B2 JP H0721081B2
- Authority
- JP
- Japan
- Prior art keywords
- powder
- resin
- sintered body
- porous sintered
- molecular weight
- 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.)
- Expired - Lifetime
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- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は10〜150μmの連通気孔を有するポリオレフイ
ン系樹脂の多孔体に関するものであり、その耐薬品性や
強度あるいは通気性を活用して各種フイルター、吸液素
材あるいは気体や液体の導通材として活用される。TECHNICAL FIELD The present invention relates to a porous body of a polyolefin resin having continuous pores of 10 to 150 μm, and various chemical resistance, strength or breathability of the porous body is utilized. It is used as a filter, a liquid absorbing material, or a gas or liquid conducting material.
(従来の技術) 熱可塑性樹脂粉末を一般的には所望形状の雌型に充填
し、この金型を樹脂の溶融温度以上に加熱し、粉末樹脂
相互の界面を融着させた後に冷却して、無数の連通した
気孔を有する多孔体を成形する方法を焼結成形と称し、
また得られた焼結体を連通多孔焼結体と称する。このよ
うにして得られた多孔体の機械的引張り強度は連通多孔
体であるが為に樹脂本来の有するそれに比べて可成り低
い値のものしか得られないのが普通である。この強度を
向上させる為によく用いられる技術としては、粉末を金
型内に密に充填して焼結成形して目的を達する方法であ
る。しかしこの方法には大きな欠点がある。そのひとつ
は高密度に粉体を充填した金型を加熱した際に、金型に
接する部分の粉体が溶融状態になるにつれてその圧力に
抗しきれずに過剰の溶融流動を起こして、その結果表面
部の気孔が目詰りを起こすことである。これを解決する
為に用いられるもうひとつの方法は金型に圧力をかけて
粉体を高密度に充填し、賦形した粉体のブロツクを取り
出して開放圧力下に加熱焼結させる方法であるが、この
方法だと所望形状通りには仕上らないため、後加工(切
削加工)によつて形状修正を必要とする。(Prior Art) Generally, a thermoplastic resin powder is filled in a female mold having a desired shape, and the mold is heated to a temperature higher than the melting temperature of the resin, and the powder resin is melted at its interface and then cooled. , A method of forming a porous body having innumerable communicating pores is called sintering forming,
Further, the obtained sintered body is referred to as a continuous porous sintered body. The mechanical tensile strength of the thus obtained porous body is a continuous porous body, and therefore, it is usually possible to obtain a value which is considerably lower than that which the resin originally has. A technique often used to improve this strength is a method in which the powder is densely filled in a mold and sinter-molded to achieve the purpose. However, this method has major drawbacks. One of them is that when a mold filled with high density powder is heated, as the powder in the part in contact with the mold becomes molten, it cannot withstand the pressure and causes excessive melt flow, resulting in That is, the pores on the surface part are clogged. Another method used to solve this is to press the mold to fill the powder with high density, take out the block of the shaped powder, and heat-sinter under open pressure. However, with this method, the desired shape cannot be obtained, and therefore the shape needs to be corrected by post-processing (cutting).
焼結成形用の熱可塑性樹脂粉末としては耐薬品性に優れ
ていること、工業的に安価に入手しうること、また粉末
として入手可能なこと、焼結成形性が良いこと等の理由
からポリオレフイン樹脂粉末が広範に利用されている
が、その強度は前述の如くであり、むしろ他のプラスチ
ツクに比べて低く、その強度改良が望まれている。As a thermoplastic resin powder for sinter molding, it has excellent chemical resistance, is industrially available at low cost, is available as a powder, and has good sinter moldability. Although the resin powder is widely used, its strength is as described above and is rather lower than that of other plastics, and its strength is desired to be improved.
(発明が解決しようとする問題点) 連通多孔焼結体の引張り強度は相接する樹脂粒子間の融
着強度によつて決定される。この融着強度を上げる為に
は、ひとつは融着面積を大にすることであり、従来技術
ではその為に粉体を高密度に充填し焼結する方法をと
る。もうひとつの方法は融着力そのものを高くする方法
であるが、融着力の高い原料は溶融時の粘度が低い為に
目詰りを非常に起し易いのが通常であり実用に供されて
いない。また、従来手法のように外力で粉体を金型に高
密度に詰め込むと金型形状によつては圧力分布を生じ、
得られる多孔体の気孔径や気孔率は場所にり不均一とな
り、通気性の面では圧力損失が大となる。これらの事か
ら、原料樹脂粉末はより溶融粘度が高く目詰りしにくい
材料が好んで用いられる。しかし溶融粘度が高い材料ほ
ど溶着強度は低く、その結果得られる多孔体の引張り強
度は低いものとなる欠点がある。(Problems to be Solved by the Invention) The tensile strength of the continuous porous sintered body is determined by the fusion strength between the resin particles in contact with each other. In order to increase the fusion strength, one is to increase the fusion area, and in the conventional technique, a method of filling powder with high density and sintering is used for that purpose. Another method is to increase the cohesive strength itself, but a raw material having a high cohesive strength usually causes clogging because it has a low viscosity at the time of melting and has not been put to practical use. In addition, when the powder is packed into the mold with an external force at a high density as in the conventional method, pressure distribution is generated depending on the mold shape.
The pore diameter and the porosity of the obtained porous body become uneven depending on the place, and the pressure loss becomes large in terms of air permeability. For these reasons, the raw material resin powder is preferably a material having a higher melt viscosity and less clogging. However, a material having a higher melt viscosity has a lower welding strength, and as a result, the resulting porous body has a lower tensile strength.
(問題点を解決する為の手段) 本発明は上述のような状況下にあつて、一般に入手し得
る材料を用いて、焼結成形が容易に行なえ、高い引張り
強度を有し、気孔径、気孔率とも均一性の高い、しかも
通気抵抗の少ない連通多孔焼結体を得ようとするもので
ある。(Means for Solving the Problems) The present invention, under the circumstances as described above, can be easily sintered and molded using a commonly available material, has a high tensile strength, and has a pore diameter, It is intended to obtain a continuous porous sintered body having high uniformity in porosity and low airflow resistance.
すなわち、本発明では溶融粘度の極めて高い超高分子量
ポリエチレン粉末と溶融粘度の低い溶融流動性を有する
ポリエチレン系樹脂又は/及びポリプロピレン系樹脂粉
末とを、ある限定された範囲に混合した混合粉末を焼結
成形に用いることを特徴とする。更に詳しくは、平均粒
子径が50〜500μmであり、粉体の嵩密度が0.3g/c.c.以
上であり、粉体の安息角が45度以下の超高分子量ポリエ
チレン粉末(A)と、MIが0.02〜30g/10分であり、平均
粒子径が50〜500μmであって(A)の平均粒子径に対
し3/1〜1/3の範囲であり、粉体の嵩密度が0.3g/c.c.以
上であり、粉体の安息角が45度以下のポリエチレン系樹
脂又は/及びポリプロピレン系樹脂粉末(B)とを、
(A)/(B)=85/15〜40/60(重量部)の範囲内で混
合し、これを焼結して平均気孔径10〜150μm、平均気
孔率25〜45V%(容量%)の連通気孔を有する多孔焼結
体を得ることを特徴とする。このことによつて、粉体は
特に圧力充填せずとも最密状態に充填され、気孔率の分
布も均質で、しかも引張り強度の高い連通多孔焼結体が
得られるようになる。That is, in the present invention, an ultra-high molecular weight polyethylene powder having an extremely high melt viscosity and a polyethylene resin or / and a polypropylene resin powder having a low melt viscosity and a low melt viscosity are mixed in a certain limited range to form a mixed powder. It is characterized in that it is used for consolidation. More specifically, the average particle size is 50 to 500 μm, the bulk density of the powder is 0.3 g / cc or more, and the powder has an ultrahigh molecular weight polyethylene powder (A) having an angle of repose of 45 degrees or less and MI. 0.02 to 30 g / 10 minutes, the average particle size is 50 to 500 μm, the range is 3/1 to 1/3 of the average particle size of (A), and the bulk density of the powder is 0.3 g / cc. The above is the polyethylene resin and / or polypropylene resin powder (B) having a repose angle of 45 degrees or less,
(A) / (B) = 85/15 to 40/60 (parts by weight), mixed and sintered to obtain an average pore diameter of 10 to 150 μm and an average porosity of 25 to 45 V% (volume%). It is characterized in that a porous sintered body having a continuous ventilation hole is obtained. As a result, the powder can be packed in the closest packed state without pressure packing, and a continuous porous sintered body having a uniform porosity distribution and high tensile strength can be obtained.
本発明にいう超高分子量ポリエチレン粉末(A)とは、
ASTM−D1601による粘度法で測定した分子量が60万以上
のもので、溶融時の流動性をASTM−D1238のメルトイン
デツクス値(以下MI値と称する)を用いて表わすとMI≒
0g/10分(温度;190℃、荷重;2.16Kg)の値を示すポリエ
チレン樹脂の粉末である。また、このような超高分子量
ポリエチレン樹脂粉末は、一般のポリエチレン樹脂粉末
を電子線照射や有機過酸化物等により架橋させても得ら
れるし、チーグラー・ナツタ触媒等を用いた懸濁重合等
の重合方法によつても粉体が直接得られる。また本発明
で粉末と称するものは樹脂を機械的な粉砕、化学的な粉
砕をしたもの、あるいは重合で直接得られる粉体を意味
し、更に好ましくはその粉体の平均粒子径が50〜500μ
mの範囲内であり、粉体の嵩密度が0.3g/cc以上(JIS−
K6721で測定)、粉体の安息角が45度以下(JIS−K6721
を用いて注入法で測定)のものが好ましい。また、本発
明にいうポリエチレン系樹脂又は/及びポリプロピレン
系樹脂粉末(B)とは、そのポリマー構造中にエチレン
又は/及びプロピレン単位を70モル%以上含む樹脂粉末
をいゝ、ポリエチレン樹脂、ポリプロピレン樹脂、エチ
レン/プロピレン・コポリマーあるいはエチレンやプロ
ピレンと他のモノマー例えばブテン−1、4メチルペン
テン−1、酢酸ビニルなどとの共重合体樹脂の粉末をい
ゝ、粉末と称するものの定義と、粉体の好ましい特性は
既述のそれと同じである。またこれらのポリエチレン系
樹脂又は/及びポリプロピレン系樹脂粉末はMI=0.02〜
30g/10分(温度;190℃、荷重;2.16kg)の範囲のもので
ある。本発明では、上述の超高分子量ポリエチレン粉末
(A)とポリエチレン系樹脂又は/及びポリプロピレン
系樹脂粉末(B)とを(A)/(B)=85/15〜40/60
(重量部)の範囲に混合して用いる。この混合割合いの
範囲内において通常実施される焼結成形法で平均気孔
径、平均気孔率とも均質性の高い連通多孔焼結体が得ら
れる。好ましくは(A)/(B)=80〜20〜40/60、最
も好ましくは、80/20〜50/50(重量部)である。85/15
の混合割合いよりも該(B)が少ないと得られる多孔焼
結体の引張強度の向上効果は乏しく、また該(A)の割
合いが多いと焼結成形性が乏しく、好ましくない。40/6
0の混合割合よりも(A)が少い場合つまり(A)が40
より少い場合は(B)が60を越すことになり、(B)は
目詰りを起し易い原料であるために焼結体も目詰りを起
す。すなわち、超高分子量ポリエチレン粉末は広い焼結
条件範囲で目詰りの無い多孔焼結体となるが、欠点とし
て引張強度が脆弱である。また、ポリエチレン系樹脂又
は/及びポリプロピレン系樹脂はMI値が大なるほどその
逆の傾向を示し、更にその粉末粒子径が小さいほど同様
の傾向を有する。このことから本発明では好ましくは超
高分子量ポリエチレン粉末(A)とポリエチレン系樹脂
又は/及びポリプロピレン系樹脂粉末(B)の粉末のそ
れぞれの平均粒子径の相対的比較値(以下、平均粒径比
と称する)が3/1〜1/3の範囲内となる様な組み合わせを
行なうことが好ましい。この範囲内の平均粒径比の組み
合わせであれば、双方の粒度差による層分離現象が発現
しにくい。また、粉体の嵩密度や安息角については粉体
の焼結成形用金型等に対する充填性との相関を有する特
性値であり、嵩密度が大なるほど、安息角が小なるほど
粉体の充填性は良好である。本発明のポリオレフイン樹
脂は機械的に粉砕して嵩密度が大で、安息角の低い粉体
とすることの難しい樹脂である。このためオレフイン樹
脂の粉砕に関する提案、例えば粉砕助剤の添加や冷凍粉
砕方法、あるいは重合によつて粉体流動性の良好な重合
粉末を得る方法で得られるところの、粉体の嵩密度0.3g
/cc以上、粉体の安息角45度以下、好ましくは嵩密度0.3
5g/cc以上、安息角40度以下のものがより有用である。
粉体の嵩密度が小さく又、安息角が大きいものは金型へ
の充填性に劣り好ましくない傾向がある。又、本発明に
おいて嵩密度は実質的には、0.6g/cc以上のものは得ら
れない。又安息角は実質的には、20度以下のものは得ら
れない。The ultra high molecular weight polyethylene powder (A) referred to in the present invention means
If the molecular weight measured by the viscosity method according to ASTM-D1601 is 600,000 or more, and the fluidity during melting is expressed using the melt index value of ASTM-D1238 (hereinafter referred to as MI value), MI ≒
A polyethylene resin powder showing a value of 0 g / 10 minutes (temperature: 190 ° C., load: 2.16 Kg). Further, such ultra-high molecular weight polyethylene resin powder can be obtained by crosslinking general polyethylene resin powder with electron beam irradiation, organic peroxide, etc., or by suspension polymerization using Ziegler-Natsuta catalyst or the like. Powder can be directly obtained by the polymerization method. In the present invention, what is referred to as powder means mechanically crushed resin, chemically crushed resin, or powder obtained directly by polymerization, and more preferably, the average particle diameter of the powder is 50 to 500 μm.
Within the range of m, the bulk density of the powder is 0.3 g / cc or more (JIS-
(Measured with K6721), the repose angle of the powder is 45 degrees or less (JIS-K6721
Is measured by the injection method). The polyethylene-based resin or / and polypropylene-based resin powder (B) referred to in the present invention means resin powder containing 70 mol% or more of ethylene or / and propylene units in its polymer structure, polyethylene resin, polypropylene resin. , Ethylene / propylene copolymer or a powder of a copolymer resin of ethylene or propylene and another monomer such as butene-1, 4 methylpentene-1, vinyl acetate, etc. The preferred properties are the same as those described above. In addition, these polyethylene-based resins and / or polypropylene-based resin powders have MI = 0.02 ~
It is in the range of 30g / 10 minutes (temperature; 190 ° C, load; 2.16kg). In the present invention, the above-mentioned ultra high molecular weight polyethylene powder (A) and the polyethylene resin or / and the polypropylene resin powder (B) are (A) / (B) = 85/15 to 40/60.
The mixture is used in the range of (parts by weight). Within the range of this mixing ratio, a continuous porous sintered body having a high homogeneity in the average pore diameter and the average porosity can be obtained by the sintering forming method which is usually carried out. (A) / (B) = 80 to 20 to 40/60, and most preferably 80/20 to 50/50 (parts by weight). 85/15
If the content of (B) is less than the mixing ratio of (A), the effect of improving the tensile strength of the obtained porous sintered body is poor, and if the content of (A) is large, the sintering formability is poor, which is not preferable. 40/6
When (A) is less than the mixing ratio of 0, that is, (A) is 40
If it is less, (B) exceeds 60, and since (B) is a raw material that easily causes clogging, the sintered body also causes clogging. That is, the ultra high molecular weight polyethylene powder becomes a porous sintered body without clogging in a wide range of sintering conditions, but has a drawback that the tensile strength is weak. In addition, the polyethylene-based resin and / or the polypropylene-based resin has the opposite tendency as the MI value increases, and has the same tendency as the powder particle diameter decreases. From this, in the present invention, the relative comparison value of the average particle diameters of the ultrahigh molecular weight polyethylene powder (A) and the polyethylene resin or / and the polypropylene resin powder (B) is preferable (hereinafter, the average particle diameter ratio). It is preferable to make such a combination that the value of 3) is within the range of 3/1 to 1/3. If the combination of the average particle diameter ratios is within this range, the layer separation phenomenon due to the difference in the particle diameters of both is unlikely to occur. The bulk density and angle of repose of the powder are characteristic values that correlate with the filling property of the powder into the sinter molding die, and the higher the bulk density and the smaller the angle of repose, the more the powder is packed. The sex is good. The polyolefin resin of the present invention is a resin which is difficult to mechanically pulverize into a powder having a large bulk density and a low angle of repose. For this reason, a proposal regarding the pulverization of olefin resin, for example, a method of obtaining a polymer powder having a good powder fluidity by the addition of a pulverizing auxiliary agent, a freeze pulverization method, or a polymerization method, and a bulk density of the powder of 0.3 g
/ cc or more, the angle of repose of the powder is 45 degrees or less, preferably the bulk density is 0.3
More than 5g / cc and less than 40 degrees of repose are more useful.
A powder having a low bulk density and a large repose angle tends to be unfavorable because of poor filling in a mold. In the present invention, a bulk density of 0.6 g / cc or more cannot be obtained. Also, the angle of repose cannot be practically less than 20 degrees.
こうした選ばれた材料を用い、適切なる組み合わせを行
つた原料粉末を所望形状の焼結用金型に充填し、通常の
方法で焼結を行なうならば、得られる多孔焼結体は平均
気孔径10〜150μm、平均気孔率25〜45V%の気孔径、気
孔率とも均質性が高く、かつ通気性が良く、引張強度の
改良された連通多孔焼結体を得ることができる。尚、目
的とする多孔焼結体の厚さが厚いものである場合は、本
発明の範囲内に於て、超高分子量ポリエチレン粉末の割
合いの比較的多いものが好結果をもたらす。If the raw material powders obtained by using these selected materials and performing an appropriate combination are filled in a sintering die having a desired shape and sintered by a usual method, the resulting porous sintered body has an average pore diameter. It is possible to obtain a continuous porous sintered body having a high homogeneity in pore diameter and porosity of 10 to 150 μm and an average porosity of 25 to 45 V%, good air permeability, and improved tensile strength. When the intended porous sintered body has a large thickness, a relatively high proportion of ultra-high molecular weight polyethylene powder within the scope of the present invention produces good results.
(作用・効果) 本発明による超高分子量ポリエチレン粉末(A)と
(B)との選ばれたる材料、特性及び組み合わせによる
作用が主として、連通多孔焼結体の気孔径、気孔率、通
気性及び引張強度に及ぼす作用・効果について述べる。(Operation / Effect) The operation of the selected materials, characteristics and combination of the ultra high molecular weight polyethylene powders (A) and (B) according to the present invention is mainly effected mainly by the pore diameter, porosity, air permeability and The action and effect on the tensile strength will be described.
本発明で用いる超高分子量ポリエチレンはその溶融点以
上に加熱しても可成り大きな外圧を加えない限り元の形
状を保ち、相互の融合・融着性にも乏しい。一方、ポリ
エチレン系樹脂又は/及びポリプロピレン系樹脂は、そ
の溶融点以上に加熱するとそのMI値が示すように少しの
外圧によつても流動性を示し、相互の融合・融着性にも
富む。この特徴がいずれに片寄つていても得られる多孔
焼結体は性能的に好ましくないものとなる。好ましくは
双方の長所を有するものであるがポリオレフイン樹脂の
用途分野においては焼結成形の占める樹脂需要量は余り
にも少なく、それが為に工業的に生産・販売されていな
い。その事もあつて本発明では既存の材料の組合せによ
つてこの特徴を発現させるべく検討したものであつて、
上述の特性を有する材料の組合せがそれを可能とするこ
とを見出した。すなわち、両者の粉末を均質に混合した
材料を原料として焼結成形に供するならば、双方の欠点
が大きく解消され、かつ双方の長所が発現し、更には予
測できなかつた通気性向上にも効果があることが判つ
た。双方の樹脂粉末の特定の組合わせが何故このような
作用・効果を発現するのか未解明の部分も多いが推測で
きる範囲で説明すると、双方の混合粉末が金型内等で加
熱〜溶融〜融着していく謂ゆる焼結過程において超高分
子量ポリエチレン粉末の果たす役割りは自己融着性が乏
しく、形状を保持し、それによつて粒子間の空隙を保持
する(気孔径、気孔率を保つ)働きである。一方、ポリ
エチレン系樹脂又は/及びポリプロピレン系樹脂粉末は
溶融点以上では急速に流動化し、自己融着し相互に融合
しようとするがその粒子間に介在する超高分子量ポリエ
チレン粒子に隔まれて自己粒子同志の融着は阻害され、
その融着・融合は相接する粒子間に止まる。この現象は
顕微鏡的視野下における混合粉末の加熱溶融状態の観察
や、実際の多孔焼結体の融着面の観察によつても窺え
る。更に溶融流動状態の樹脂は形状を保持している超高
分子量ポリエチレン粒子との接触界面部で融着し、その
状態で可成り高い温度迄安定化するようである。この安
定化は重要であり、厚肉の多孔焼結体を得ようとすると
内部の樹脂粉末がその様な状態になる温度に達する迄に
は外部(金型に接する部分は特に)は更に流動して融合
が進み通常は目詰り状態になる。焼結成形における加熱
は通常は最内部の粉体が焼結不足の状態で加熱を中止
し、冷却に移るが、この間に内部は余熱により焼結す
る。この加熱中止〜冷却への移行のタイミングは焼結肉
厚が厚いほど見極めが困難であり、従来は永年の経験と
勘に頼つている部分でもあるが、本発明では粒子間の融
着が進行した後の安定性が高い為に、このタイミングが
非常にとり易く、言いかえれば焼結条件巾が広く、目詰
りしにくい原料である。このようにして本発明の原料粉
末を焼結成形したものは気孔を維持する粒子と融着して
粒子間結合の強い部分を形成する粒子とがうまく働き結
果として気孔径・気孔率が均質で引張強度の高い焼結体
となる。また、厚肉成形品であつても外部と内部の気孔
径や気孔率に差の無い〜少ない均質性の高い多孔体とな
る。また、本発明では夫々の樹脂粉体からなる連通多孔
体の通気性より優れたものがある範囲で得られる。例え
ば同粒径の両者を組み合わせた場合においてもそうであ
り、特に超高分子量ポリエチレン樹脂粉末単体のそれよ
りも通気性が良くなるという効果が認められる。この効
果となる作用・因子は未解明の部分もあるが推測では焼
結過程〜完了の間にポリエチレン系樹脂又は/及びポリ
プロピレン系樹脂粉末粒子の流動により、ひとつの塊り
であつた粒子形状が流動して棒状〜偏平になり、その為
に通気抵抗が減るものとみられる。ちなみにこのような
多孔焼結体の気孔形状を観察すると単体のそれより縦・
横の長さが不揃いになつており、数値的には平均気孔径
のアツプと通気抵抗の減少として表われる。本発明では
引張強度の改良を主目的とするものであり、その為には
相互粒子の融着力の高いことが必須であり、その為には
混合された粉末粒子相互の融着が起こる事が前提であ
る。従つて、相互融着を示さない粉体の組み合せでは目
的を達成できない。斯様な理由から本発明では同種の樹
脂、あるいは近種の樹脂の組み合わせからなる。The ultrahigh molecular weight polyethylene used in the present invention retains its original shape even if it is heated above its melting point and unless a considerably large external pressure is applied, and is poor in mutual fusion and fusion. On the other hand, when the polyethylene resin and / or the polypropylene resin is heated above the melting point, the polyethylene resin exhibits fluidity even with a slight external pressure as shown by its MI value, and is excellent in mutual fusion and fusion. The porous sintered body obtained will be unfavorable in terms of performance regardless of which of these characteristics is biased. Although preferably having both advantages, in the application field of the polyolefin resin, the amount of resin demand occupied by sintering is too small, and therefore it is not industrially produced and sold. Therefore, in the present invention, the present invention has been studied in order to express this characteristic by the combination of existing materials.
It has been found that a combination of materials with the above properties makes it possible. That is, if the material in which both powders are homogeneously mixed is used as a raw material for sintering and molding, both defects are largely eliminated, and the advantages of both are expressed, and further, it is also effective for unpredictable improvement of air permeability. It turns out that there is. There are many unclear reasons why a specific combination of both resin powders produces such action / effect, but to explain within the range that can be inferred, both mixed powders are heated ~ melted ~ melted in the mold etc. The role of ultra-high molecular weight polyethylene powder in the so-called loose sintering process is that the self-fusing property is poor and the shape is retained, thereby maintaining the voids between particles (maintaining the pore diameter and porosity). ) Work. On the other hand, polyethylene-based resin and / or polypropylene-based resin powder rapidly fluidizes above the melting point and tries to self-bond and fuse with each other, but it is separated by ultra-high molecular weight polyethylene particles interposed between the particles and self-particles. Fusion of fellows is hindered,
The fusion and fusion stop between the adjoining particles. This phenomenon can be observed by observing the heating and melting state of the mixed powder under a microscopic view and observing the actual fusion-bonded surface of the porous sintered body. Further, the resin in the melt flow state seems to be fused at the contact interface with the ultra-high molecular weight polyethylene particles retaining the shape, and in that state, it is stabilized to a considerably high temperature. This stabilization is important, and when trying to obtain a thick-walled porous sintered body, the outside (particularly the part in contact with the mold) is further fluidized by the time the internal resin powder reaches such a temperature. Then, the fusion progresses, and it is usually in a clogging state. The heating in sinter molding is usually stopped in the state where the powder in the innermost portion is insufficient for sintering, and the process proceeds to cooling, but the inside is sintered due to residual heat. The timing of transition from this heating stop to cooling is more difficult to determine as the sintered thickness is thicker, and conventionally it is also a part that relies on years of experience and intuition, but in the present invention fusion between particles progresses Since it is highly stable after being processed, this timing is very easy to take, in other words, the range of sintering conditions is wide, and it is a raw material that does not easily clog. In this way, the raw material powder of the present invention sinter-molded works well with particles that maintain pores and particles that fuse and form a part with a strong interparticle bond, resulting in a uniform pore diameter and porosity. It becomes a sintered body with high tensile strength. In addition, even a thick-walled molded product can be a porous body having high to homogeneity with little or no difference in pore diameter and porosity between the outside and the inside. Further, according to the present invention, it is possible to obtain a porous material which is superior in air permeability to the continuous porous body made of each resin powder. This is also the case, for example, when both particles having the same particle size are combined, and in particular, the effect that the air permeability is better than that of the ultrahigh molecular weight polyethylene resin powder alone is recognized. Although there are some parts where the action and factors that cause this effect have not been clarified, it is speculated that the particle shape of one lump may be changed due to the flow of the polyethylene resin and / or polypropylene resin powder particles during the sintering process to completion. It is believed that it flows and becomes rod-shaped to flat, which reduces the ventilation resistance. By the way, when observing the pore shape of such a porous sintered body,
The lateral lengths are uneven, and are numerically expressed as an increase in average pore diameter and a decrease in ventilation resistance. In the present invention, the main purpose is to improve the tensile strength, for that purpose it is essential that the mutual particle fusion power is high, for that the fusion of mixed powder particles may occur. It is a premise. Therefore, the object cannot be achieved with a combination of powders which do not show mutual fusion. For this reason, in the present invention, the same kind of resin or a combination of similar kinds of resins is used.
第4図は本発明の連通多孔焼結体の通気性を評価するた
めに用いるところの通気抵抗測定装置の概図である。同
図において、1は流量調節バルブであり、これを通じて
圧力3Kg/cm3・Gの空気8を供給する。2は流量計であ
り、1のバルブで流量を200l/mmに調整することによ
り、3の導管内に600l/mm(大気圧換算値)の空気を送
り込む。5は被験体の多孔焼結パイプであり、このパイ
プの上下は4および7のパツキンとフランジでシールさ
れている。送り込まれた空気はパイプの連通気孔から抜
け出るが、そのときの抵抗(背圧)が6の差圧計により
検出される。FIG. 4 is a schematic view of a ventilation resistance measuring device used for evaluating the air permeability of the continuous porous sintered body of the present invention. In the figure, 1 is a flow control valve through which air 8 having a pressure of 3 kg / cm 3 · G is supplied. Reference numeral 2 is a flow meter, and 600 l / mm (atmospheric pressure conversion value) of air is sent into the conduit 3 by adjusting the flow rate to 200 l / mm with the valve of 1. 5 is a porous sintered pipe of the test subject, and the upper and lower parts of this pipe are sealed with the packings 4 and 7 and the flange. The sent air escapes from the communicating holes of the pipe, and the resistance (back pressure) at that time is detected by the differential pressure gauge 6.
本発明ではこの6の差圧計により検出された背圧を通気
抵抗という。In the present invention, the back pressure detected by the differential pressure gauge 6 is referred to as ventilation resistance.
(実施例) 実施例1 数平均分子量が約330万、樹脂密度0.942g/cm2の粉体特
性の異なる超高分子量ポリエレン粉末(商品名;サンフ
アインUH−900、旭化成工業(株)製)の3種を用意し
た。このものを夫々UH−1、UH−2、UH−3とし、その
粉体特性を順に示すと粉体の粒度分布は30〜100Mesh、7
0〜200Mesh、120〜325Meshの範囲内に全体の99.5W%以
上の重量を有し、その粉体の平均粒子径は250μm、120
μm、75μm、である。また嵩密度は0.40g/cc、0.49g/
cc、0.48g/ccであり、安息角は31度、35度、39度であ
る。また、樹脂密度が0.958g/cm3の高密度ポリエチレン
樹脂粉末(商品名;サンフアインSH−800、旭化成工業
(株)製)を用意した。このものをSH−1とし、その粉
体特性を示すとMI=0.05g/10分、粉体の粒度分布は80〜
200Meshに全体の99%以上を有し、平均粒子径125μm、
嵩密度0.43g/cc、安息角29度である。これらの粉体を第
1表に併記した割合いで充分混合し、型厚2.5mmの内径3
9.5φ×長さ32cmのアルミ管の中央に型厚2.5mmの外径2
8.5φ×長さ32cmのアルミ管を置き、管の上下に蓋を有
する金型を準備し、混合粉体をアルミ管金型間隙(5.5m
m)の部分に一杯になる迄充填した。この充填時にはバ
イブレーターを用いて型全体を振動下において粉末を充
填したのみで粉体充填時に他の外圧はかけなかつた。そ
のときの型容積に対する充填粉体容積比を充填率として
記載した。次いで蓋をして、一定温度に保たれた熱風炉
内に入れ加熱した。このときの炉の温度と投入した時間
も第2表に併記した。尚、第2表に併記した加熱条件は
その試料について最適な成形条件の探索を行つた結果選
ばれた条件である。加熱終了後、室温下で10分間放置
し、次いで扇風機で風を送り冷却した。型より取出した
パイプ状の焼結体の両端を切り落し長さ300mmとした。
この多孔焼結パイプの片方に差圧計をとりつけ、他方か
ら600l/mmの量の空気を送り、そのときの差圧を通気抵
抗として記載した。次に該パイプを25mm巾に切断した
(これを以下、焼結リングと称する)。焼結リング内に
10mmφの鉄棒2本を通し、この鉄棒を上下方向に引張試
験機を用いて引張つた。このときの引張速度は50mm/min
であり、それによつて焼結リングが破断する迄に耐えた
最大荷重を引張破壊強度として、また試料UH−2の引張
破壊強度を1としたとき他の試料のそれとの比を第1表
に示した。また得られたデータを元に原料混合比と引張
破壊強度の関係を第1図に、通気抵抗との関係を第2図
に、また通気抵抗と引張破壊強度の関係を第3図に示し
た。これらのデータから本発明の範囲においては引張強
度は向上し、通気抵抗は少なく、又、第3図にみられる
ごとく同じ通気抵抗のものであれば可成り高い引張強度
を有するものである。(Example) Example 1 An ultra high molecular weight polyethylene powder (trade name: San Huain UH-900, manufactured by Asahi Kasei Co., Ltd.) having a number average molecular weight of about 3.3 million and a resin density of 0.942 g / cm 2 and different powder characteristics. Three kinds were prepared. These are designated UH-1, UH-2, and UH-3, respectively, and their powder characteristics are shown in order, and the particle size distribution of the powder is 30 to 100 Mesh, 7
Within the range of 0-200Mesh, 120-325Mesh, the total weight is 99.5W% or more, and the average particle size of the powder is 250μm, 120
μm, 75 μm. Bulk density is 0.40g / cc, 0.49g / cc
It is cc, 0.48g / cc, and the angle of repose is 31, 35, and 39 degrees. In addition, a high-density polyethylene resin powder having a resin density of 0.958 g / cm 3 (trade name: Sunfine SH-800, manufactured by Asahi Kasei Kogyo Co., Ltd.) was prepared. This is designated as SH-1, and its powder characteristics are shown as MI = 0.05g / 10min, and the particle size distribution of powder is 80-
Having more than 99% of the total in 200 Mesh, average particle size 125 μm,
It has a bulk density of 0.43 g / cc and an angle of repose of 29 degrees. Mix these powders in the proportions given in Table 1 together, and mold with a mold thickness of 2.5 mm.
9.5φ x 32 cm long aluminum tube with a 2.5 mm outer diameter 2 in the center
Place an aluminum tube of 8.5φ x 32 cm in length and prepare a mold with lids on the top and bottom of the pipe.
Fill the part m) until it is full. At the time of this filling, the vibrator was used to fill the whole mold under vibration with the powder, and no other external pressure was applied during the powder filling. The filling powder volume ratio to the mold volume at that time was described as the filling rate. Then, it was covered and heated in a hot air oven kept at a constant temperature. Table 2 also shows the furnace temperature and the charging time. The heating conditions shown in Table 2 are the conditions selected as a result of searching the optimum molding conditions for the sample. After completion of heating, the mixture was left at room temperature for 10 minutes, and then blown with a fan to cool it. Both ends of the pipe-shaped sintered body taken out from the mold were cut off to have a length of 300 mm.
A differential pressure gauge was attached to one of the porous sintered pipes, and air of an amount of 600 l / mm was sent from the other side, and the differential pressure at that time was described as ventilation resistance. Next, the pipe was cut into a width of 25 mm (hereinafter, referred to as a sintered ring). In the sintering ring
Two 10 mmφ iron bars were passed through and the iron bars were pulled vertically using a tensile tester. The pulling speed at this time is 50 mm / min
As a result, the maximum load withstanding the fracture of the sintered ring was taken as the tensile breaking strength, and when the tensile breaking strength of sample UH-2 was set to 1, the ratio with that of other samples is shown in Table 1. Indicated. Based on the obtained data, the relationship between the raw material mixture ratio and the tensile breaking strength is shown in Fig. 1, the relationship with the ventilation resistance is shown in Fig. 2, and the relationship between the ventilation resistance and the tensile breaking strength is shown in Fig. 3. . From these data, in the range of the present invention, the tensile strength is improved, the ventilation resistance is small, and as shown in FIG. 3, the one having the same ventilation resistance has considerably high tensile strength.
実施例2 実施例1で用いたUH−2と、樹脂密度0.955g/cm3、MIが
20g/10mmの高密度ポリエチレン樹脂粉末(JP)を準備し
た。このJPの粉体の粒度分布は45〜200Meshの間の全体
の99%以上を有し、その平均粒子径は250μm、粉体の
嵩密度は0.41g/cc、安息角は31度である。このUH−2と
JPを第2表に示した割合いで充分混合し、実施例1と同
様の操作で焼結成形を行つた。得られたパイプ状の焼結
体についてその特性を同様に評価した結果を第2表に記
載した。得られたデータから超高分子量ポリエチレン粉
末に組み合わせるポリエチレン系樹脂又は/及びポリプ
ロピレン系樹脂のMI値が高いものは、その量がある程度
以上になると気孔径が不安定になり易い傾向を示すが、
本発明の範囲内では引張強度向上と通気抵抗の減少効果
が認められる。 Example 2 UH-2 used in Example 1 and resin density 0.955g / cm 3 , MI
20 g / 10 mm high density polyethylene resin powder (JP) was prepared. The particle size distribution of the JP powder is 99% or more of the whole between 45 to 200 mesh, the average particle diameter is 250 μm, the bulk density of the powder is 0.41 g / cc, and the angle of repose is 31 degrees. With this UH-2
Sufficiently mixed JP in the proportions shown in Table 2, and sintered and molded in the same manner as in Example 1. Table 2 shows the results of similarly evaluating the properties of the obtained pipe-shaped sintered body. From the obtained data, the polyethylene resin or / and the polypropylene resin to be combined with the ultra high molecular weight polyethylene powder having a high MI value shows a tendency that the pore diameter tends to become unstable when the amount exceeds a certain level,
Within the scope of the present invention, the effects of improving tensile strength and reducing ventilation resistance are recognized.
第1図は本発明の(A)と(B)との混合割合と製品の
引張り破壊強度との関係、第2図は同通気抵抗との関
係、第3図は同通気抵抗と引張破壊強度との関係を示
す。第4図は本発明の連通多孔焼結体の通気性を評価す
るために用いるところの通気抵抗測定装置の概図であ
る。同図において、1は流量調節バルブであり、8は供
給空気、2は流量計、3は導管、5は被験体の多孔焼結
パイプ、4および7はパツキンとフランジによるシー
ル、6は抵抗(背圧)測定用差圧計である。FIG. 1 shows the relationship between the mixing ratio of (A) and (B) of the present invention and the tensile fracture strength of the product, FIG. 2 shows the relationship with the ventilation resistance, and FIG. 3 shows the ventilation resistance and the tensile fracture strength. Shows the relationship with. FIG. 4 is a schematic view of a ventilation resistance measuring device used for evaluating the air permeability of the continuous porous sintered body of the present invention. In the figure, 1 is a flow control valve, 8 is supply air, 2 is a flow meter, 3 is a conduit, 5 is a porous sintered pipe of a test object, 4 and 7 are seals by packing and flange, and 6 is resistance ( This is a differential pressure gauge for measuring back pressure.
Claims (1)
嵩密度が0.3g/c.c.以上であり、粉体の安息角が45度以
下の超高分子量ポリエチレン粉末(A)と、MIが0.02〜
30g/10分であり、平均粒子径が50〜500μmであって
(A)の平均粒子径に対し3/1〜1/3の範囲であり、粉体
の嵩密度が0.3g/c.c.以上であり、粉体の安息角が45度
以下のポリエチレン系樹脂又は/及びポリプロピレン系
樹脂粉末(B)とを、(A)/(B)=85/15〜40/60
(重量部)の範囲内で混合し、これを焼結して平均気孔
径10〜150μm、平均気孔率25〜45V%(容量%)の連通
気孔を有する多孔焼結体を得ることを特徴とする連通多
孔焼結体の製造方法。1. An ultra high molecular weight polyethylene powder (A) having an average particle diameter of 50 to 500 μm, a bulk density of powder of 0.3 g / cc or more, and a repose angle of 45 degrees or less, and MI. Is 0.02 ~
30 g / 10 minutes, the average particle size is 50 to 500 μm, the range is 3/1 to 1/3 of the average particle size of (A), and the bulk density of the powder is 0.3 g / cc or more. Yes, the polyethylene resin or / and the polypropylene resin powder (B) having an angle of repose of 45 degrees or less is (A) / (B) = 85/15 to 40/60
(Parts by weight) mixed and sintered to obtain a porous sintered body having continuous pores with an average pore diameter of 10 to 150 μm and an average porosity of 25 to 45 V% (volume%). A method for producing a continuous porous sintered body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60124184A JPH0721081B2 (en) | 1985-06-10 | 1985-06-10 | Method for producing continuous porous sintered body |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60124184A JPH0721081B2 (en) | 1985-06-10 | 1985-06-10 | Method for producing continuous porous sintered body |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61283634A JPS61283634A (en) | 1986-12-13 |
| JPH0721081B2 true JPH0721081B2 (en) | 1995-03-08 |
Family
ID=14879056
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60124184A Expired - Lifetime JPH0721081B2 (en) | 1985-06-10 | 1985-06-10 | Method for producing continuous porous sintered body |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0721081B2 (en) |
Families Citing this family (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH082572B2 (en) * | 1990-11-09 | 1996-01-17 | 株式会社小松製作所 | Method for producing ultrahigh molecular weight polyethylene porous body and product thereof |
| DE4341497A1 (en) * | 1993-12-06 | 1995-06-08 | Hoechst Ag | Process for the production of porous moldings |
| JPH10205534A (en) * | 1997-01-17 | 1998-08-04 | Nippon Thompson Co Ltd | Linear motion guide unit with lubrication plate |
| JP4236217B2 (en) * | 1997-09-09 | 2009-03-11 | 日本トムソン株式会社 | Linear motion guidance unit |
| JP3935247B2 (en) * | 1997-09-18 | 2007-06-20 | 日本トムソン株式会社 | Linear motion guidance unit |
| US6113274A (en) * | 1999-04-15 | 2000-09-05 | Tsubaki Nakashima Co., Ltd. | Linear guideway having spacers and spacer ball |
| US6176149B1 (en) | 1999-05-28 | 2001-01-23 | Tsubaki Nakashima Co., Ltd. | Ball screw having spacers |
| US6415676B1 (en) | 1999-10-26 | 2002-07-09 | Tsubaki Nakashima Co., Ltd. | Ball screw device having spacers |
| JP4730864B2 (en) * | 2000-06-13 | 2011-07-20 | 旭化成ケミカルズ株式会社 | Sheet used for suction and apparatus using the same |
| JP4761608B2 (en) * | 2000-06-14 | 2011-08-31 | 旭化成ケミカルズ株式会社 | Method for producing porous body for suction |
| MX2009001794A (en) * | 2006-08-18 | 2009-07-22 | Porex Corp | Sintered polymeric materials and applications thereof. |
| WO2012173812A1 (en) | 2011-06-15 | 2012-12-20 | Porex Corporation | Sintered porous plastic liquid barrier media and applications thereof |
| CN111965072A (en) * | 2020-07-28 | 2020-11-20 | 济南裕兴化工有限责任公司 | A method for evaluating the cohesion of titanium dioxide |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4037241A (en) * | 1975-10-02 | 1977-07-19 | Texas Instruments Incorporated | Shaped emitters with buried-junction structure |
-
1985
- 1985-06-10 JP JP60124184A patent/JPH0721081B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61283634A (en) | 1986-12-13 |
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