JPH0350245A - Conductive polypropylene resin foam and its production - Google Patents
Conductive polypropylene resin foam and its productionInfo
- Publication number
- JPH0350245A JPH0350245A JP18355789A JP18355789A JPH0350245A JP H0350245 A JPH0350245 A JP H0350245A JP 18355789 A JP18355789 A JP 18355789A JP 18355789 A JP18355789 A JP 18355789A JP H0350245 A JPH0350245 A JP H0350245A
- Authority
- JP
- Japan
- Prior art keywords
- foam
- weight
- resin composition
- carbon black
- density
- 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.)
- Granted
Links
- 239000006260 foam Substances 0.000 title claims abstract description 57
- 239000011347 resin Substances 0.000 title claims abstract description 17
- 229920005989 resin Polymers 0.000 title claims abstract description 17
- -1 polypropylene Polymers 0.000 title claims description 22
- 239000004743 Polypropylene Substances 0.000 title claims description 9
- 229920001155 polypropylene Polymers 0.000 title claims description 9
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- 239000011342 resin composition Substances 0.000 claims abstract description 26
- 239000006229 carbon black Substances 0.000 claims abstract description 22
- 238000002156 mixing Methods 0.000 claims abstract description 17
- 238000005187 foaming Methods 0.000 claims abstract description 15
- 229920001400 block copolymer Polymers 0.000 claims abstract description 13
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000005977 Ethylene Substances 0.000 claims abstract description 9
- 239000000155 melt Substances 0.000 claims abstract description 5
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims abstract description 5
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims abstract description 5
- 229920001903 high density polyethylene Polymers 0.000 claims description 24
- 239000004700 high-density polyethylene Substances 0.000 claims description 24
- 239000000203 mixture Substances 0.000 claims description 13
- 239000000463 material Substances 0.000 claims description 8
- 239000004594 Masterbatch (MB) Substances 0.000 claims description 7
- 238000013329 compounding Methods 0.000 claims description 2
- 239000005022 packaging material Substances 0.000 abstract description 5
- 229920001577 copolymer Polymers 0.000 description 14
- 230000007423 decrease Effects 0.000 description 8
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- 230000005611 electricity Effects 0.000 description 6
- 229920005653 propylene-ethylene copolymer Polymers 0.000 description 6
- 230000003068 static effect Effects 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 238000005192 partition Methods 0.000 description 3
- 229920000098 polyolefin Polymers 0.000 description 3
- 229920005604 random copolymer Polymers 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 241000872198 Serjania polyphylla Species 0.000 description 2
- 238000005452 bending Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000001747 exhibiting effect Effects 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 230000002401 inhibitory effect Effects 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 239000004604 Blowing Agent Substances 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000006230 acetylene black Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 229920001038 ethylene copolymer Polymers 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 239000004088 foaming agent Substances 0.000 description 1
- 239000006232 furnace black Substances 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000000615 nonconductor Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920005629 polypropylene homopolymer Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 229920002545 silicone oil Polymers 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は導電性ポリプロピレン樹脂発泡体とその製造方
法に関し、更に詳しくは、剛性が優れていて、静電気の
帯電が起らないので、電子部品や精密機械などの梱包材
として有用な導電性ポリプロピレン樹脂発泡体とその製
造方法に関する。Detailed Description of the Invention (Field of Industrial Application) The present invention relates to a conductive polypropylene resin foam and a method for manufacturing the same. The present invention relates to a conductive polypropylene resin foam useful as a packaging material for precision machinery, etc., and a method for producing the same.
(従来の技術)
発泡倍率が1.5〜5倍程度のポリオレフィン発泡体は
、適度の弾力性と緩衝性を有する素材であるため、各種
物品の梱包材としで、また製品の間仕切り材として広く
用いられている。(Prior art) Polyolefin foam with an expansion ratio of about 1.5 to 5 times is a material with appropriate elasticity and cushioning properties, so it is widely used as a packaging material for various products and as a partition material for products. It is used.
しかしながら、これらポリオレフィン発泡体はそのほと
んどが電気絶縁体であるため、表面が静電気で帯電し易
い。However, since most of these polyolefin foams are electrical insulators, their surfaces are easily charged with static electricity.
静電気が帯電すると、発泡体表面には塵埃が付着するた
め、精密機械等の梱包材として不適となる。また、LS
Iや基板をはじめとする電子部品、それを組込んだ電子
機器などの梱包に使用すると、帯電した静電気によって
これら部品や機器がその機能を喪失するという事態を招
く。When static electricity is charged, dust adheres to the surface of the foam, making it unsuitable as a packaging material for precision instruments and the like. Also, L.S.
If it is used to package electronic components such as ICs and circuit boards, as well as electronic devices incorporating them, the charged static electricity may cause these components and devices to lose their functions.
このようなことから、例えばポリエチレンに適量のカー
ボンブラックを配合し、その組成物を架橋または無架橋
で発泡せしめ、得られる発泡体を導電性にして静電気の
帯電を抑制しようという試みが行なわれている。また、
剛性や耐熱性が優れ、通雨用の箱や間仕切り用の資材と
して有用なポリプロピレンに同じくカーボンブラックを
配合して発泡せしめ、導電性の発泡体を得る努力がなさ
れている。For this reason, attempts have been made to, for example, mix an appropriate amount of carbon black with polyethylene, foam the resulting composition with or without crosslinking, and make the resulting foam conductive to suppress static electricity charging. There is. Also,
Efforts are being made to create conductive foam by blending carbon black with polypropylene, which has excellent rigidity and heat resistance and is useful as a material for rain boxes and partitions.
(発明が解決しようとする課題)
しかしながら、前者の発泡体の場合、得られる発泡体が
軟質でありすぎるため、自立性に乏しく通雨用の箱や間
仕切り材の用途には不向きである。(Problems to be Solved by the Invention) However, in the case of the former foam, the resulting foam is too soft and therefore lacks self-supporting properties, making it unsuitable for use as rain boxes or partition materials.
また、後者のポリプロピレンにカーボンブラックを配合
した場合は、一般に、その発泡倍率が低下して緩衝機能
が乏しくなり緩衝材としての用途には不向きとなる。Furthermore, when carbon black is blended with the latter polypropylene, the foaming ratio generally decreases and the cushioning function becomes poor, making it unsuitable for use as a cushioning material.
また、近年、帯電防止や静電除去のためには、その表面
抵抗率をlXl0’〜lXl0”Ω程度にすることが最
適であるとされているが、しかし、この範囲内で表面抵
抗率が管理されているものはほとんど知られていない。In addition, in recent years, it has been said that in order to prevent static electricity and remove static electricity, it is optimal to have a surface resistivity of about lXl0' to lXl0''Ω. Little is known about what is being managed.
本発明は上記したような問題を解決し、発泡倍率は1.
5〜5程度で適度の弾力性、緩衝性を有し、しかも耐熱
性や剛性にも優れ、表面抵抗率はlXl0’〜lXl0
’Ωの範囲にあってそのばらつきも小さい導電性ポリプ
ロピレン樹脂発泡体とその製造方法の提供を目的とする
。The present invention solves the above problems and has a foaming ratio of 1.
Approximately 5 to 5, it has appropriate elasticity and cushioning properties, and is also excellent in heat resistance and rigidity, and has a surface resistivity of lXl0' to lXl0.
The purpose of the present invention is to provide a conductive polypropylene resin foam that is within the Ω range and has small variations, and a method for producing the same.
(課題を解決するための手段・作用)
上記した目的を達成するために、本発明においては、エ
チレン含量20重量%以下、メルトインデックス2g/
10分以下の結晶性プロピレン−エチレンブロック共重
合体90〜50重量%と、密度0.94〜0.96 g
/c!l、メルトインデックス5−15
50重量%とを主体とする樹脂100重量部に対してカ
ーボンブラックを5〜20重量部の割合で含有してなる
樹脂組成物の押出発泡体であることを特してなる樹脂組
成物の押出発泡体が提供され、また、この押出発泡体を
製造するに際して、予め、前記高密度ポリエチレンと前
記カーボンブラックとを所定量混和してマスターバッチ
混和物とし、ついで該マスターバッチ混合物と前記結晶
性プロピレン−エチレンブロック共重合体を主体とする
配合材を所定量混和し、得られた樹脂組成物を押出発泡
することを特徴とする導電性プロピレン樹脂発泡体の製
造方法が提供される。(Means and effects for solving the problem) In order to achieve the above-mentioned object, in the present invention, the ethylene content is 20% by weight or less, the melt index is 2g/
90-50% by weight of crystalline propylene-ethylene block copolymer less than 10 minutes and density 0.94-0.96 g
/c! It is an extruded foam of a resin composition containing 5 to 20 parts by weight of carbon black to 100 parts by weight of a resin mainly consisting of 50% by weight of melt index 5-15. An extruded foam of a resin composition made of A method for producing a conductive propylene resin foam, which comprises mixing a batch mixture with a predetermined amount of a compounding material mainly composed of the crystalline propylene-ethylene block copolymer, and extruding and foaming the obtained resin composition. provided.
本発明の発泡体は、以下に述べる樹脂組成物を押出発泡
せしめて製造される。The foam of the present invention is manufactured by extruding and foaming the resin composition described below.
まず、上記樹脂組成物は、結晶性プロピレン−エチレン
ブロック共重合体と高密度ポリエチレンとカーボンブラ
ックを必須成分とする。First, the resin composition contains a crystalline propylene-ethylene block copolymer, high-density polyethylene, and carbon black as essential components.
ここで結晶性プロピレン−エチレン共重合体は本発明発
泡体の骨格となって高い剛性、優れた耐熱性の発現に資
する。The crystalline propylene-ethylene copolymer serves as the skeleton of the foam of the present invention and contributes to the development of high rigidity and excellent heat resistance.
この共重合体としては、エチレン含量が20重量%以下
でしかもMIは2g/10分以下のものが使用される。As this copolymer, one having an ethylene content of 20% by weight or less and an MI of 2 g/10 minutes or less is used.
このような共重合体は、後述する押出成形時における溶
融温度が比較的低いため、広い温度範囲に亘って樹脂組
成物の発泡に適した粘弾性を示し、その結果、良好な発
泡組織を形成して弾力性、緩衝性に優れた発泡体の製造
を可能にする。Since such copolymers have a relatively low melting temperature during extrusion molding, which will be described later, they exhibit viscoelasticity suitable for foaming resin compositions over a wide temperature range, and as a result, form a good foam structure. This makes it possible to produce foams with excellent elasticity and cushioning properties.
エチレン含量が20重量%を超えるもの、MIが2g/
10分より大きい共重合体は、均一で微細な発泡組織を
備えた発泡体にすることが極めて困難であり、しかも得
られる発泡体の耐熱性低下を招くことになる。Ethylene content exceeding 20% by weight, MI 2g/
If the copolymer is used for more than 10 minutes, it is extremely difficult to form a foam with a uniform and fine foam structure, and furthermore, the heat resistance of the resulting foam will be reduced.
エチレン含量は1〜15重量に、MIは0.1〜1、5
g/10分の結晶性プロピレン−エチレン共重合体が好
適である。Ethylene content from 1 to 15 by weight, MI from 0.1 to 1,5
g/10 min crystalline propylene-ethylene copolymer is preferred.
つぎの成分である高密度ポリエチレンは、上記した共重
合体にカーボンブラックを配合して発泡せしめるとその
発泡倍率が低下するという問題を解決する働きをし、ま
たそれ自身へのカーボンプラックの分散が良好になるた
め、得られる発泡体の表面抵抗率を任意に調節せしめる
という作用を果す。すなわち、高密度ポリエチレンは、
前記した共重合を骨格とする発泡体の剛性や緩衝性を維
持しつつ、カーボンブラックの分散性を高めて発泡体の
表面抵抗率の調節を可能にするための必須成分であり、
得られる発泡体の表面抵抗のばらつきを略2桁の範囲内
におさえることを可能にする。The next component, high-density polyethylene, works to solve the problem that the foaming ratio decreases when carbon black is blended with the above-mentioned copolymer and foamed, and it also prevents carbon plaque from dispersing into itself. The surface resistivity of the resulting foam can be adjusted as desired. In other words, high density polyethylene is
It is an essential component for increasing the dispersibility of carbon black and making it possible to adjust the surface resistivity of the foam while maintaining the rigidity and cushioning properties of the foam with the above-mentioned copolymer skeleton.
This makes it possible to suppress variations in surface resistance of the resulting foam to within a range of approximately two digits.
このような作用を示す高密度ポリエチレンとしては、密
度0.94〜0.96g/car、好ましくは0.94
〜0.95 g/Cd、M I 5〜15g/ 10分
、好ましくは7〜12g/10分のものが用いられる。High-density polyethylene exhibiting such an effect has a density of 0.94 to 0.96 g/car, preferably 0.94 g/car.
-0.95 g/Cd, MI 5-15 g/10 min, preferably 7-12 g/10 min are used.
密度0.94 g/alより低いものは高密度ポリエチ
レンとしての特性が消失しはじめて得られる発泡体の剛
性低下を招き、また密度0.96g/cdより高いもの
は前記共重合体との混和性が低下して、均一組織の発泡
体の製造は困難になるからである。If the density is lower than 0.94 g/al, the properties as high-density polyethylene will begin to disappear, leading to a decrease in the rigidity of the resulting foam, and if the density is higher than 0.96 g/cd, the miscibility with the above copolymer will decrease. This is because it becomes difficult to produce a foam with a uniform structure.
また、M15g/10分未満のような高密度ポリエチレ
ンの場合は、溶融粘度が高くなりすぎて前記共重合体や
後述のカーボンブラックとの混和性は悪化し、M115
g/10分より高いものは混和時に前記共重合体の粘弾
性を低下せしめることによりその発泡性を阻害して均一
かつ微細な発泡組織が得られなくなる。In addition, in the case of high-density polyethylene such as less than M15g/10 minutes, the melt viscosity becomes too high and the miscibility with the copolymer and carbon black described below deteriorates.
If it is higher than g/10 minutes, it will reduce the viscoelasticity of the copolymer during mixing, thereby inhibiting its foaming properties and making it impossible to obtain a uniform and fine foamed structure.
本発明の樹脂組成物における樹脂は前記結晶性プロピレ
ン−エチレンブロック共重合体と前記高密度ポリエチレ
ンを主体とするもので、両者の配合は、結晶性プロピレ
ン−エチレンブロック共重合体90〜50重量%、高密
度ポリエチレンlO〜50重量%の範囲に設定される。The resin in the resin composition of the present invention is mainly composed of the crystalline propylene-ethylene block copolymer and the high-density polyethylene, and the blend of both is 90 to 50% by weight of the crystalline propylene-ethylene block copolymer. , high density polyethylene is set in the range of lO to 50% by weight.
該ブロック共重合体の配合割合が901i量%より多い
(該高密度ポリエチレンが10重量%未満の)場合には
、発泡性が低下し、得られる発泡体の表面性が悪化゛す
る。また、該ブロック共重合体の配合割合が50重量%
未滴の(該高密度ポリエチレンが50重量%を超える)
場合には、得られる発泡体の剛性や耐熱性が不足する。If the blending ratio of the block copolymer is more than 901i (the high-density polyethylene is less than 10% by weight), the foamability will decrease and the surface properties of the resulting foam will deteriorate. In addition, the blending ratio of the block copolymer is 50% by weight.
Undropped (the high density polyethylene exceeds 50% by weight)
In some cases, the resulting foam lacks rigidity and heat resistance.
好ましい配合割合は、結晶性プロピレン−エチレンブロ
ック共重合体80〜60重量%、高密度ポリエチレン2
0〜40重量%の範囲である。The preferred blending ratio is 80 to 60% by weight of crystalline propylene-ethylene block copolymer and 2% by weight of high-density polyethylene.
It ranges from 0 to 40% by weight.
なお、樹脂組成物中の樹脂は、上記プロピレン−エチレ
ンブロック共重合体と高密度ポリエチレンの混合物のほ
か、樹脂全体の30重量%以内程度のポリプロピレンホ
モポリマー、プロピレン−エチレンランダム共重合体な
ど、他の樹脂を併用することが出来る。特に表面状態や
押出安定性改善の目的でプロピレン−エチレンランダム
共重合体を配合することは好ましい。The resin in the resin composition includes, in addition to the mixture of the propylene-ethylene block copolymer and high-density polyethylene, polypropylene homopolymer, propylene-ethylene random copolymer, etc. within 30% by weight of the total resin. These resins can be used together. In particular, it is preferable to blend a propylene-ethylene random copolymer for the purpose of improving the surface condition and extrusion stability.
つぎの成分である高密度ポリエチレンは、上記した共重
合体にカーボンブラックを配合して発泡せしめるとその
発泡倍率が低下するという問題を解決する働きをし、ま
たそれ自身へのカーボンブラックの分散が良好になるた
め、得られる発泡体の表面抵抗率を任意に調節せしめる
という作用を果す。すなわち、高密度ポリエチレンは、
前記した共重合を骨格とする発泡体の剛性や緩衝性を維
持しつつ、カーボンブラックの分散性を高めて発泡体の
表面抵抗率の調節を可能にするための必須成分であり、
得られる発泡体の表面抵抗のばらつきを略2桁の範囲内
におさえることを可能にする。The next component, high-density polyethylene, works to solve the problem that the foaming ratio decreases when carbon black is blended with the above-mentioned copolymer and foamed. The surface resistivity of the resulting foam can be adjusted as desired. In other words, high density polyethylene is
It is an essential component for increasing the dispersibility of carbon black and making it possible to adjust the surface resistivity of the foam while maintaining the rigidity and cushioning properties of the foam with the above-mentioned copolymer skeleton.
This makes it possible to suppress variations in surface resistance of the resulting foam to within a range of approximately two digits.
このような作用を示す高密度ポリエチレンとしては、密
度0.94〜0.96 g /car、好ましくは0.
94〜0.95g/cdSMI8〜l Ig/10分、
好ましくは9〜10g/10分のものが用いられる。High-density polyethylene exhibiting such an effect has a density of 0.94 to 0.96 g/car, preferably 0.94 to 0.96 g/car.
94-0.95g/cdSMI8-l Ig/10 min,
Preferably, 9 to 10 g/10 minutes is used.
密度0.94g/Cjrより低いものは高密度ポリエチ
レンとしての特性が消失しはじめて得られる発泡体の剛
性低下を招き、また密度0.96g/a/より高いもの
は前記共重合体との混和性が低下して、均一組織の発泡
体の製造は困難になるからである。If the density is lower than 0.94 g/Cjr, the properties as high-density polyethylene will begin to disappear, leading to a decrease in the rigidity of the obtained foam, and if the density is higher than 0.96 g/a/, the miscibility with the above copolymer will decrease. This is because it becomes difficult to produce a foam with a uniform structure.
また、M18g/10分未満のような高密度ポリエチレ
ンの場合は、溶融粘度が高くなりすぎて前記共重合体や
後述のカーボンブラックとの混和性は悪化し、Mrl1
g/10分より高いものは混和時に前記共重合体の粘弾
性を低下せしめることによりその発泡性を阻害して均一
かつ微細な発泡組織が得られなくなる。In addition, in the case of high-density polyethylene with an M of less than 18 g/10 minutes, the melt viscosity becomes too high and the miscibility with the copolymer and carbon black described below deteriorates.
If it is higher than g/10 minutes, it will reduce the viscoelasticity of the copolymer during mixing, thereby inhibiting its foaming properties and making it impossible to obtain a uniform and fine foamed structure.
樹脂組成物における第3の必須成分であるカーボンブラ
ックは発泡体に導電性を付与するための成分である。用
いるカーボンブラックとしては、導電性ファーネスブラ
ック、アセチレンブラックが好ましく、具体的には、ケ
ッチエンブラックEC(アクゾ社製の商品名)、パルカ
ンXC(キャボット社製の商品名)、旭HC−500(
旭カーボン社製の商品名)などをあげることができる。Carbon black, which is the third essential component in the resin composition, is a component for imparting electrical conductivity to the foam. The carbon black used is preferably conductive furnace black or acetylene black, and specifically, Ketchen Black EC (trade name manufactured by Akzo Corporation), Palcan XC (trade name manufactured by Cabot Corporation), Asahi HC-500 (trade name manufactured by Cabot Corporation), etc.
(product name manufactured by Asahi Carbon Co., Ltd.).
このカーボンブラックの樹脂組成物における配合量は樹
脂100重量部に対して5〜20重量部に設定される。The amount of carbon black in the resin composition is set at 5 to 20 parts by weight per 100 parts by weight of the resin.
この配合量が5重量部未満の場合には、得られる発泡体
の表面抵抗率はlXl0”Ωより高くなってしまい、ま
た20重量部を超える場合は表面抵抗率がlXl0’Ω
より低くなり発泡性も低下するからである。If this amount is less than 5 parts by weight, the surface resistivity of the resulting foam will be higher than lXl0'Ω, and if it exceeds 20 parts by weight, the surface resistivity will be lXl0'Ω.
This is because the foaming properties are also lowered.
樹脂組成物は上記3成分を必須として構成されるが、更
に必要に応じて、各種充填材、難燃材、酸化防止材など
を適量配合しても不都合はない。Although the resin composition is composed of the above-mentioned three components as essential, there is no problem in adding appropriate amounts of various fillers, flame retardants, antioxidants, etc., as necessary.
本発明の発泡体は上記樹脂組成物を押出発泡して製造さ
れる。The foam of the present invention is produced by extruding and foaming the resin composition.
その場合における樹脂組成物は、まず、上記した高密度
ポリエチレンとカーボンブランクとを混和してマスター
バッチ混和物を調製する。混和は、ロール、バンバリー
ミキサ−1加圧ニーダ−、ブスコニーダー、2軸押出機
等を用いた通常の混和方式を採用すればよい。このとき
、タルクのような少量の添加物微粉末、シリコーンオイ
ルのような潤滑油を同時に添加すると混和の能率を高め
ることができる。For the resin composition in that case, first, the above-described high-density polyethylene and carbon blank are mixed to prepare a masterbatch mixture. For mixing, a conventional mixing method using rolls, a Banbury mixer 1 pressure kneader, a Busco kneader, a twin-screw extruder, etc. may be adopted. At this time, mixing efficiency can be increased by simultaneously adding a small amount of additive fine powder such as talc and a lubricating oil such as silicone oil.
この混和過程においては、カーボンブラックが高密度ポ
リエチレンに良好な状態で分散し、その結果、あたかも
高密度ポリエチレンの分子鎖にカーボンブラックが付着
して成る導電性の繊維が形成された状態となり、これが
後段の結晶性プロピレン−エチレン共重合体に均一に混
合され、結果としてカーボンブラックの均一分散が達成
されるものと考えられる。In this mixing process, carbon black is well dispersed in high-density polyethylene, and as a result, conductive fibers are formed in which carbon black is attached to the molecular chains of high-density polyethylene. It is believed that the carbon black is uniformly mixed into the crystalline propylene-ethylene copolymer in the subsequent stage, resulting in uniform dispersion of carbon black.
ついで、上記マスターバッチ混和物と結晶性プロピレン
−エチレン共重合体を混和して樹脂組成物とし、この樹
脂組成物を発泡剤の圧入口を備えた押出機の中で更に溶
融混合したのち、押出発泡せしめて目的とする発泡体を
製造することができる。このときの押出機のシリンダー
温度は160〜190℃に管理することが好ましい。Next, the masterbatch mixture and the crystalline propylene-ethylene copolymer are mixed to form a resin composition, and this resin composition is further melt-mixed in an extruder equipped with a blowing agent injection port, and then extruded. A desired foam can be produced by foaming. At this time, the cylinder temperature of the extruder is preferably controlled at 160 to 190°C.
また、発泡に用いる発泡剤としては、樹脂組成物と反応
することのない気体、例えば、窒素、炭酸ガス、空気等
を用いればよい。とくに炭酸ガスは好適である。Further, as the foaming agent used for foaming, a gas that does not react with the resin composition, such as nitrogen, carbon dioxide, air, etc., may be used. Carbon dioxide gas is particularly suitable.
(発明の実施例)
実施例1.2
第1表に示したように、密度0.942g/cnf、M
19g/10分である性状の高密度ポリエチレンとケッ
チエンブラックEC8002を表示の割合となるように
バンバリーミキサ−で混和してマスターバッチ混和物と
し、更に、これに表示のように、エチレン含量11重量
%、M [0,5g/10分である結晶性プロピレン−
エチレン共重合体を表示の割合となるように配合して混
和し、各種の樹脂組成物を調製した。(Embodiments of the invention) Example 1.2 As shown in Table 1, density 0.942 g/cnf, M
High-density polyethylene with a property of 19 g/10 minutes and Ketschen Black EC8002 are mixed in a Banbury mixer at the indicated ratio to make a masterbatch mixture, and further, as indicated, an ethylene content of 11 weight is added to the masterbatch mixture. %, M [0.5 g/10 min of crystalline propylene-
Various resin compositions were prepared by blending and mixing ethylene copolymers in the indicated proportions.
これら樹脂組成物を、発泡剤の圧入口を備えている口径
65Io!llの押出機に投入し、温度180℃で溶融
混合し、圧入口より炭酸ガスを圧入して押出機先端のT
ダイから大気中に押出発泡せしめた。These resin compositions were injected into a 65Io! 1 liter extruder, melted and mixed at a temperature of 180°C, and then pressurized carbon dioxide gas through the injection port and
The foam was extruded from a die into the atmosphere.
成形ロールでシート状に成形し発泡体を製造した。A foam was produced by molding into a sheet using a molding roll.
得られた発泡体につき、下記仕様で密度、曲げ弾性率、
曲げ強さ、抗張力・伸び、表面抵抗率を測定した。For the obtained foam, the density, flexural modulus,
Bending strength, tensile strength/elongation, and surface resistivity were measured.
密度 : JISK6767に準拠して測定曲げ弾性
率9曲げ強さ:JISK7203に準拠して測定。Density: Measured according to JISK6767 Flexural modulus 9 Bending strength: Measured according to JISK7203.
抗張力・伸び+JISK6767に準拠して測定。Tensile strength/elongation + Measured according to JISK6767.
表面抵抗率:JISK69i1に準拠して測定。Surface resistivity: Measured according to JISK69i1.
以上の結果を一括して第1表に示した。The above results are collectively shown in Table 1.
実施例3
実施例1で用いた高密度ポリエチレンとケッチエンブラ
ックを第1表の割合となるようにパンツくリーミキサー
で混和してマスターバッチ混和物とし、更にこれに同じ
〈実施例1で用いた結晶性プロピレン−エチレン共重合
体とプロピレン−エチレンランダム共重合体を第1表の
割合となるように配合し、実施例1と同様の方法で発泡
体を製造した。得られた発泡体の特性を実施例1と同様
にして測定し、その結果を第1表に示した。Example 3 The high-density polyethylene and Ketschen Black used in Example 1 were mixed in a pantries mixer in the proportions shown in Table 1 to form a masterbatch mixture, and the same mixture used in Example 1 was further mixed. A foam was produced in the same manner as in Example 1 by blending the crystalline propylene-ethylene copolymer and the propylene-ethylene random copolymer in the proportions shown in Table 1. The properties of the obtained foam were measured in the same manner as in Example 1, and the results are shown in Table 1.
比較例1〜5
ケッチエンブラックEC8002と第1表に示したポリ
オレフィンを表示の割合となるように混和したのち、こ
れに実施例1で用いたポリプロピレンを混和し、得られ
た樹脂組成物を用いて実施例1と同様の方法で発泡体を
製造した。得られた発泡体の特性を実施例1と同様にし
て測定し、その結果を一括して第1表に示した。Comparative Examples 1 to 5 Ketchen Black EC8002 and the polyolefin shown in Table 1 were mixed in the indicated proportions, and then the polypropylene used in Example 1 was mixed therein, and the resulting resin composition was used. A foam was produced in the same manner as in Example 1. The properties of the obtained foam were measured in the same manner as in Example 1, and the results are summarized in Table 1.
比較例6
実施例1で用いた結晶性プロピレン−エチレン共重合体
の一部をケッチエンブラックEC8002と混和したの
ち、得られたコンパウンドと残部の共重合体を混和して
樹脂組成物とした。これら樹脂組成物を用いて実施例1
と同様の方法で発泡体を製造した。この発泡体の特性を
一括して第1表に示した。Comparative Example 6 A part of the crystalline propylene-ethylene copolymer used in Example 1 was mixed with Ketchen Black EC8002, and then the resulting compound and the remaining copolymer were mixed to obtain a resin composition. Example 1 using these resin compositions
A foam was produced in a similar manner. The properties of this foam are summarized in Table 1.
(以下余白)
(発明の効果)
以上の説明で明らかなように、本発明方法で製造された
発泡体は、ポリプロピレンのみから成る発泡体(参考例
)と同等の剛性を有し、また密度も適正で弾力性、緩衝
性も優れており、そしてその表面抵抗率はlXl0’〜
lXl0”Ωと適正範囲にありしかもその値のばらつき
が小さい。(The following is a blank space) (Effect of the invention) As is clear from the above explanation, the foam produced by the method of the present invention has the same rigidity as the foam made only of polypropylene (reference example), and also has a lower density. It has appropriate elasticity and cushioning properties, and its surface resistivity is lXl0' ~
lXl0''Ω, which is within the appropriate range, and the variation in the value is small.
したがって、精密機械や各種電子機器の梱包材、間仕切
り材として好適で、その工業的価値は大である。Therefore, it is suitable for packaging materials and partitioning materials for precision machines and various electronic devices, and has great industrial value.
Claims (3)
ス2g/10分以下の結晶性プロピレン−エチレンブロ
ック共重合体90〜50重量%と、密度0.94〜0.
96g/cm^3、メルトインデックス5〜15g/1
0分の高密度ポリエチレン10〜50重量%とを主体と
する樹脂100重量部に対してカーボンブラックを5〜
20重量部の割合で含有してなる樹脂組成物の押出発泡
体であることを特徴とする導電性ポリプロピレン樹脂発
泡体。(1) A crystalline propylene-ethylene block copolymer having an ethylene content of 20% by weight or less, a melt index of 2g/10min or less, and a density of 0.94-0.
96g/cm^3, melt index 5-15g/1
5 to 5 parts by weight of carbon black to 100 parts by weight of a resin mainly composed of 10 to 50% by weight of high-density polyethylene
A conductive polypropylene resin foam, characterized in that it is an extruded foam of a resin composition containing 20 parts by weight.
る請求項1記載の導電性プロピレン樹脂発泡体。(2) The conductive propylene resin foam according to claim 1, which has a surface resistivity of 1 x 10^4 to 1 x 10^9 Ω.
るに際して、予め、前記高密度ポリエチレンと前記カー
ボンブラックとを所定量混和してマスターバッチ混和物
とし、ついで該マスターバッチ混和物と前記結晶性プロ
ピレン−エチレンブロック共重合体を主体とする配合材
を所定量混和し、得られた樹脂組成物を押出発泡するこ
とを特徴とする導電性プロピレン樹脂発泡体の製造方法
。(3) When producing an extruded foam of the resin composition according to claim 1, a predetermined amount of the high-density polyethylene and the carbon black are mixed in advance to form a masterbatch mixture, and then the masterbatch mixture is A method for producing a conductive propylene resin foam, comprising mixing a predetermined amount of a compounding material mainly composed of the crystalline propylene-ethylene block copolymer, and extruding and foaming the obtained resin composition.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18355789A JP2773907B2 (en) | 1989-07-18 | 1989-07-18 | Conductive polypropylene resin foam and method for producing the same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18355789A JP2773907B2 (en) | 1989-07-18 | 1989-07-18 | Conductive polypropylene resin foam and method for producing the same |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0350245A true JPH0350245A (en) | 1991-03-04 |
JP2773907B2 JP2773907B2 (en) | 1998-07-09 |
Family
ID=16137889
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP18355789A Expired - Lifetime JP2773907B2 (en) | 1989-07-18 | 1989-07-18 | Conductive polypropylene resin foam and method for producing the same |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2773907B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6419810B1 (en) | 1998-11-26 | 2002-07-16 | Tetsuo Tanaka | Method of manufacturing an optical fiber connector |
EP1816158A1 (en) * | 2006-02-06 | 2007-08-08 | Borealis Technology Oy | Extruded polyolefin for the manufacture of cellular material |
JP2012214625A (en) * | 2011-03-31 | 2012-11-08 | Sekisui Chem Co Ltd | Resin foam and method of manufacturing the same |
-
1989
- 1989-07-18 JP JP18355789A patent/JP2773907B2/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6419810B1 (en) | 1998-11-26 | 2002-07-16 | Tetsuo Tanaka | Method of manufacturing an optical fiber connector |
EP1816158A1 (en) * | 2006-02-06 | 2007-08-08 | Borealis Technology Oy | Extruded polyolefin for the manufacture of cellular material |
WO2007090519A1 (en) * | 2006-02-06 | 2007-08-16 | Borealis Technology Oy | Extruded polyolefin for the manufacture of cellular material |
JP2012214625A (en) * | 2011-03-31 | 2012-11-08 | Sekisui Chem Co Ltd | Resin foam and method of manufacturing the same |
Also Published As
Publication number | Publication date |
---|---|
JP2773907B2 (en) | 1998-07-09 |
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