JPH0365311A - Carbon fiber chop - Google Patents
Carbon fiber chopInfo
- Publication number
- JPH0365311A JPH0365311A JP20032289A JP20032289A JPH0365311A JP H0365311 A JPH0365311 A JP H0365311A JP 20032289 A JP20032289 A JP 20032289A JP 20032289 A JP20032289 A JP 20032289A JP H0365311 A JPH0365311 A JP H0365311A
- Authority
- JP
- Japan
- Prior art keywords
- carbon fiber
- carbon fibers
- chops
- resin
- carbon
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 229920000049 Carbon (fiber) Polymers 0.000 title claims abstract description 84
- 239000004917 carbon fiber Substances 0.000 title claims abstract description 83
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims description 52
- 229920005989 resin Polymers 0.000 claims abstract description 21
- 239000011347 resin Substances 0.000 claims abstract description 21
- 238000005520 cutting process Methods 0.000 abstract description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 2
- 238000007664 blowing Methods 0.000 abstract 1
- 239000000835 fiber Substances 0.000 description 18
- 238000001746 injection moulding Methods 0.000 description 12
- 230000000052 comparative effect Effects 0.000 description 10
- 238000002347 injection Methods 0.000 description 9
- 239000007924 injection Substances 0.000 description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 7
- 229920002873 Polyethylenimine Polymers 0.000 description 7
- 239000012778 molding material Substances 0.000 description 7
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 6
- 229910052799 carbon Inorganic materials 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 229920005668 polycarbonate resin Polymers 0.000 description 6
- 239000004431 polycarbonate resin Substances 0.000 description 6
- 229920005992 thermoplastic resin Polymers 0.000 description 6
- 239000003795 chemical substances by application Substances 0.000 description 5
- 239000006185 dispersion Substances 0.000 description 5
- 238000011156 evaluation Methods 0.000 description 5
- 230000000704 physical effect Effects 0.000 description 5
- 238000004513 sizing Methods 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- 239000004721 Polyphenylene oxide Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000011159 matrix material Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- 229920001707 polybutylene terephthalate Polymers 0.000 description 3
- -1 polyoxymethylene Polymers 0.000 description 3
- 229920006380 polyphenylene oxide Polymers 0.000 description 3
- 239000004925 Acrylic resin Substances 0.000 description 2
- 229920000178 Acrylic resin Polymers 0.000 description 2
- 239000004677 Nylon Substances 0.000 description 2
- 239000004952 Polyamide Substances 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 description 2
- 239000003822 epoxy resin Substances 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 238000004898 kneading Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 229920001778 nylon Polymers 0.000 description 2
- 229920002647 polyamide Polymers 0.000 description 2
- 229920000647 polyepoxide Polymers 0.000 description 2
- 229920000728 polyester Polymers 0.000 description 2
- 229920000098 polyolefin Polymers 0.000 description 2
- 229920005749 polyurethane resin Polymers 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 229930040373 Paraformaldehyde Natural products 0.000 description 1
- 239000004734 Polyphenylene sulfide Substances 0.000 description 1
- 229920000297 Rayon Polymers 0.000 description 1
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 229920002239 polyacrylonitrile Polymers 0.000 description 1
- 229920000768 polyamine Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 150000004291 polyenes Chemical class 0.000 description 1
- 229920000570 polyether Polymers 0.000 description 1
- 229920006324 polyoxymethylene Polymers 0.000 description 1
- 229920001955 polyphenylene ether Polymers 0.000 description 1
- 229920000069 polyphenylene sulfide Polymers 0.000 description 1
- 229920012287 polyphenylene sulfone Polymers 0.000 description 1
- 229920000036 polyvinylpyrrolidone Polymers 0.000 description 1
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 description 1
- 239000001267 polyvinylpyrrolidone Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000002964 rayon Substances 0.000 description 1
- 239000012783 reinforcing fiber Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
Landscapes
- Reinforced Plastic Materials (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は炭素繊維をポリイミン樹脂で集束した炭素繊維
チゴップに関するものである。更に詳しくは、炭素繊維
強化樹脂の成形に直接射出成形できる成形加工性、炭素
繊維の分散性、機械強度及び導電性に優れた性能を有す
る炭素繊維チョップに関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a carbon fiber tip made of carbon fibers bundled with a polyimine resin. More specifically, the present invention relates to a carbon fiber chop that can be directly injection molded into a carbon fiber reinforced resin and has excellent moldability, carbon fiber dispersibility, mechanical strength, and electrical conductivity.
炭素繊維を各種マトリックス中に混合、分散させて成る
繊維強化成形材料は、炭素繊維の優れた特性、例えば高
強度、高剛性、低比重、高電気伝導性、低熱膨張率、高
耐摩耗性などを有することから、幅広い用途が期待され
、工業的に重要な材料として注目されている。Fiber-reinforced molding materials made by mixing and dispersing carbon fibers in various matrices have the excellent properties of carbon fibers, such as high strength, high rigidity, low specific gravity, high electrical conductivity, low coefficient of thermal expansion, and high wear resistance. Because of this, it is expected to have a wide range of uses and is attracting attention as an industrially important material.
一般に、炭素繊維を各種熱可塑性樹脂に混合、分散させ
て繊維強化成形材料を得るには、数百〜数百力木から成
る炭素繊維を集束剤、例えば通常繊維強化成形材料に用
いるポリオレフィン、ポリエステル、ポリアミド(特公
昭62−7225号公報)、アクリル樹脂、エポキシ樹
脂(特開昭61−66615号公報)、フェノール樹脂
で集束し、1〜Loanに切断して炭素繊維チョップと
し、これを熱可塑性樹脂のペレット又はパウダーととも
に押出機中で溶融混練し、得られたストランドをペレタ
イズして炭素繊維強化成形材料を製造する。Generally, in order to obtain a fiber-reinforced molding material by mixing and dispersing carbon fibers in various thermoplastic resins, carbon fibers consisting of hundreds to hundreds of tensile strength are used as a sizing agent, such as polyolefin, polyester, etc., which are usually used in fiber-reinforced molding materials. , polyamide (Japanese Patent Publication No. 62-7225), acrylic resin, epoxy resin (Japanese Patent Application Laid-open No. 61-66615), and phenol resin, cut into 1~loan to make carbon fiber chops, which are then made into thermoplastic fibers. The strands are melt-kneaded together with resin pellets or powder in an extruder, and the resulting strands are pelletized to produce a carbon fiber-reinforced molding material.
このようにして得られた炭素繊維強化成形材料を射出成
形し製品を得る方法が一般的に行なわれている。A commonly used method is to injection mold the carbon fiber-reinforced molding material thus obtained to obtain a product.
従来、炭素繊維強化成形品を得る為には、あらかじめ熱
可塑性樹脂と炭素繊維チョップを押出機で、溶融混練し
、炭素繊維をマトリックス中で均一に分散させる必要が
あった。しかし、その為に押出機の溶融混練時に炭素繊
維の破断(短繊維化)が生じ、機械特性及び導電特性等
が著しく低下した。また押出機で一旦炭素繊維強化成形
材料を製造する為、生産性が劣るとい・)欠点があった
。Conventionally, in order to obtain a carbon fiber-reinforced molded product, it was necessary to melt and knead the thermoplastic resin and carbon fiber chops in an extruder in advance to uniformly disperse the carbon fibers in the matrix. However, this caused the carbon fibers to break (shorten fibers) during melt-kneading in an extruder, resulting in a significant decrease in mechanical properties, electrical conductivity, etc. Additionally, since the carbon fiber reinforced molding material is manufactured using an extruder, productivity is low.
本発明の目的は1、炭素t1iIiw、、強化戒形品の
製造において、押出機で溶融混練しで得られる炭素繊維
強化成形材料を用いることなく、直接炭素繊維チョップ
と熱可塑性樹脂のぺ]ノットとともに射出成形し、炭素
繊組の織rfii長の長い物性の優れた製品が得られる
炭素繊維チョップを提供するにある。The purpose of the present invention is 1. In the production of carbon t1iIiw, reinforced shaped articles, carbon fiber chops and thermoplastic resin are directly bonded to each other without using a carbon fiber reinforced molding material obtained by melt-kneading in an extruder. It is an object of the present invention to provide a carbon fiber chop that can be injection molded with the carbon fibers to obtain a product with a long carbon fiber weave length and excellent physical properties.
この際、該繊維チョップの集束性が不十分であるとチョ
ップが開繊して、射出成形機の供給口で詰まり炭素繊維
強化成形品中の炭素繊維含有量を均一にコントロールす
ることができない。また原料そのものが入らず成形がで
きないこともある。At this time, if the convergence of the fiber chops is insufficient, the chops will open and clog the supply port of the injection molding machine, making it impossible to uniformly control the carbon fiber content in the carbon fiber reinforced molded product. In addition, there are times when the raw material itself cannot be used and molding cannot be performed.
従って、炭素繊維チョップを直接射出成形する為には、
繊維に高い集束性を付与しチョップの開繊を肪がなけれ
ばならない。Therefore, in order to directly injection mold carbon fiber chops,
It is necessary to impart high cohesiveness to the fibers and to prevent the opening of the chops from becoming fat.
一方、押出し工程を省略し、炭素繊維チョップ六熱可塑
性樹脂を直接射出成形する為、強化繊維は射出成形機の
可塑化ゾーンで容易に均一分散しなければならない。得
られる成形品中の炭素繊維の分散が悪いと外観が悪く、
物性は大きくバラツキ、強度も劣る。従って、分散性の
優れた集束剤であることが必要である。On the other hand, since the extrusion process is omitted and the carbon fiber chopped thermoplastic resin is directly injection molded, the reinforcing fibers must be easily and uniformly dispersed in the plasticization zone of the injection molding machine. Poor dispersion of carbon fibers in the resulting molded product will result in poor appearance.
Physical properties vary widely and strength is inferior. Therefore, it is necessary to use a sizing agent with excellent dispersibility.
このように、該繊維チョップは、直接射出成形する為、
高い集束性とそれに相反する優れた分散性を兼ね備えた
チョップでなければならない。In this way, since the fiber chop is directly injection molded,
The chop must have both high convergence and excellent dispersion.
又炭素繊維強化成形品を製造する際、従来法では、押出
機で一旦溶融混練し炭素繊維の分散を良くする必要があ
り、どうしても炭素繊維の繊維長が短かくなり、必要と
する力学強度、導電特性の物性を得ることが難しかった
。In addition, when manufacturing carbon fiber reinforced molded products, in the conventional method, it is necessary to once melt and knead the carbon fibers in an extruder to improve the dispersion of the carbon fibers, which inevitably shortens the fiber length of the carbon fibers and reduces the required mechanical strength. It was difficult to obtain the physical properties of conductivity.
従って、成形品中の炭素繊維の繊維長が長く、か゛つ分
散性の優れた、両方を満足する繊維チョップは、これま
でなかった。Therefore, there has never been a fiber chop that satisfies both of the long fiber length of the carbon fibers in the molded article and the excellent dispersibility.
本発明者等は、このよ・うなチョップの集束力と分散性
の相反する問題を解決し、炭素短繊維を直接成形できる
集束性の高(ハ、かつ7トリツクス中に均一に分散し、
繊維長を長く保ち、物性の優れる集束剤について検討し
た結果、本発明に至ったものである。The present inventors have solved the conflicting problem of the focusing power and dispersibility of chopping, and have achieved high focusing ability (c) that allows short carbon fibers to be directly formed, and that they can be uniformly dispersed in the 7-tricks.
The present invention was developed as a result of research into a sizing agent that maintains long fiber length and has excellent physical properties.
すなわち本発明は、炭素繊維をボリイ且ン樹脂の含有量
0.1〜・100重量で集束してなることを特徴とする
炭素繊維チョップである。That is, the present invention is a carbon fiber chop characterized in that carbon fibers are bundled with a polyurethane resin content of 0.1 to 100% by weight.
本発明において集束剤とL7て用いるポリイミン樹脂は
、分子量が1万一50万のもので、室温で固体状のもの
が好ましい。このよ・うなポリイミン樹脂としては、例
えば、ポリエチレンイミン、ボリブlコピレンイaン、
ポリブチレンイミン、1.1ジメチルエチレンイミン、
1.1−ジメチル−2メチルエチ1/ンイミン、1゜1
−ジメチル−2プロピルエチレンイミン、N−アセチル
ポリエチレンイ箋ン、N−プロビオニルポリエチl/ン
イaン、N−7’チリルポリエチレンイミン、N−バレ
リルポリエチレンイミン、N−ヘキサノイルポリエチレ
ンイミン、N−ステアロイルポリエチレンイミン、ポリ
ベンズアルドイミミン等のポリアミンおよびその誘導体
、およびそれらの混合物、あるいは変性、共重合された
ボリイゑン樹脂などがあげられる。とくに好ましくは、
ポリエチレンイミン、N−プロビオニルポリエチ1/ン
イξンがあげられる。The polyimine resin used as the sizing agent and L7 in the present invention preferably has a molecular weight of 11,500,000 and is solid at room temperature. Examples of such polyimine resins include polyethyleneimine, polyethyleneimine,
polybutyleneimine, 1.1 dimethylethyleneimine,
1.1-dimethyl-2methylethyl-imine, 1゜1
-dimethyl-2propylethyleneimine, N-acetylpolyethyleneimine, N-probionylpolyethyleneimine, N-7'tyrylpolyethyleneimine, N-valerylpolyethyleneimine, N-hexanoylpolyethyleneimine, Examples include polyamines such as N-stearoyl polyethyleneimine and polybenzaldoimimine, derivatives thereof, mixtures thereof, and modified and copolymerized polyene resins. Particularly preferably,
Examples include polyethyleneimine and N-probionyl polyethyleneimine.
本発明においては、炭素繊組の集束剤として、ポリイミ
ン樹脂を炭素繊維に0.1−100重量、好ましくは2
〜6電景%含有せしめる。この量が0.1重量未満では
集束性が不十分で、射出成形機の供給ホラパル中におけ
る流動性が悪いので、*形品中の炭素繊維含有量が均一
とならず、チョップが開繊して、供給口で詰まり、成形
ができない。In the present invention, as a sizing agent for the carbon fiber assembly, polyimine resin is added to the carbon fibers in an amount of 0.1 to 100% by weight, preferably 2.
Contain ~6%. If this amount is less than 0.1 weight, the convergence will be insufficient and the fluidity in the Horapal supplied to the injection molding machine will be poor, so the carbon fiber content in the molded product will not be uniform and the chops will open. Then, the supply port gets clogged and molding cannot be performed.
また100重量を超えると、これを用いて得られた成形
品の力学物性である引張強度、曲げ強度等に問題が生じ
る。Moreover, if it exceeds 100 weight, problems will arise in the mechanical properties such as tensile strength and bending strength of the molded product obtained using it.
本発明の炭素繊維チョップ(゛、かさ密度が300g/
42以上、好ましくは350g/42以上である。The carbon fiber chop of the present invention (゛, bulk density is 300g/
42 or more, preferably 350g/42 or more.
かさ密度が300g/ff未満では、完全に集束されて
いるとはいえず、射出成形機の供給ポツパー中における
流動性が悪いので、射出成形機スクリフ、−への供給不
良やマトリックス樹脂への不均一分散などが生じ、連続
的な生産が困難になり、本発明の目的を十分に発揮する
ことができない。If the bulk density is less than 300g/ff, it cannot be said to be completely concentrated and the fluidity in the supply popper of the injection molding machine will be poor, resulting in poor supply to the injection molding machine scruff and - and damage to the matrix resin. Uniform dispersion occurs, making continuous production difficult and making it impossible to fully achieve the purpose of the present invention.
本発明の炭素繊維チョップの製造法は、まず適当な本数
からなる連続した炭素繊維束を、濃度0.5〜10重量
%のポリイミン樹脂の溶液の中に連続的に浸漬したのち
、200″C程度の熱風により乾燥する。次いで、所望
の長さ、例えば1〜IO閣に切断することによってポリ
イミン樹脂で集束した炭素繊維チョップが得られる。The method for manufacturing carbon fiber chops of the present invention involves first continuously immersing an appropriate number of continuous carbon fiber bundles in a polyimine resin solution with a concentration of 0.5 to 10% by weight, and then soaking the carbon fibers at 200''C. The carbon fiber chops bundled with polyimine resin are then obtained by cutting into desired lengths, for example, 1 to 10 mm.
また、炭素繊維強化成形品は、本発明の炭素繊維と熱可
塑性樹脂とを射出成形機のホッパー内に供給し、可塑化
シリンダー内で溶融し、射出成形型内に射出し、金型内
で冷却固化して成形品を取り出すことによって得られる
。成形品をより均一なものとするためには、射出成形機
にて成形を行う前に、タンブラ−1高速くキサ−などの
手段を用いて予備混合を行っても良い。Furthermore, the carbon fiber-reinforced molded product can be produced by supplying the carbon fibers and thermoplastic resin of the present invention into the hopper of an injection molding machine, melting them in the plasticizing cylinder, and injecting them into the injection mold. It is obtained by cooling and solidifying and taking out the molded product. In order to make the molded product more uniform, preliminary mixing may be performed using a high-speed tumbler or a mixer or the like before molding with an injection molding machine.
本発明において、素材として用いる炭素繊維については
、特に制限はなく、各種の公知の炭素繊維、例えばレー
ヨン、ポリアクリロニトリル、ピッチ、リグニン、炭化
水素ガスなどを用いて製造された炭素質繊維や黒鉛質繊
維及びこれらに金属をコーティングした金属被覆炭素繊
維などの中から任意に選んで用いることができる。In the present invention, the carbon fiber used as a material is not particularly limited, and there are various known carbon fibers, such as carbon fibers manufactured using rayon, polyacrylonitrile, pitch, lignin, hydrocarbon gas, etc., and graphite fibers. Any material can be selected from among fibers and metal-coated carbon fibers obtained by coating these fibers with metal.
本発明の炭素繊維チョップを用いて繊維強化成形品を製
造するのに使用されるマトリックスとしては、例えばポ
リカーボネート、ポリアミド、ポリエステル、ポリオキ
シメチレン、ポリフェニレンエーテル、ポリフェニレン
サルファイド、ポリエーテル・エーテルケトン、ポリオ
レフィン、ポリフェニレンスルホン、アクリル樹脂、ス
チレン系樹脂などの熱可塑性樹脂が挙げられるが、特に
ポリカーボネート樹脂は好適である。Examples of matrices used to produce fiber-reinforced molded products using the carbon fiber chop of the present invention include polycarbonate, polyamide, polyester, polyoxymethylene, polyphenylene ether, polyphenylene sulfide, polyether/etherketone, polyolefin, Examples include thermoplastic resins such as polyphenylene sulfone, acrylic resins, and styrene resins, with polycarbonate resins being particularly suitable.
次に実施例によって本発明をさらに詳細に説明する。 Next, the present invention will be explained in more detail with reference to Examples.
なお、各種物性の測定法は次のとおりである。The methods for measuring various physical properties are as follows.
〈炭素繊維チョップのかさ密度〉
50dメスシリンダーに炭素繊維チョップを充填したの
ち、メスシリンダーに上下の衝撃的振動を与え、平衡に
達した炭素繊維チョップの体積でその重さを除して求め
る。<Bulk density of carbon fiber chops> After filling a 50 d measuring cylinder with carbon fiber chops, apply vertical impact vibration to the graduated cylinder, and calculate by dividing the weight by the volume of the carbon fiber chops that has reached equilibrium.
〈炭素繊維チョップの分散性〉
炭素繊維チョップの分散性は、東芝製l575E型射出
戒形機によって成形した50mmX90mmX2.5
msの板状成形品の外観観察程度から、分散性の良否を
1〜3の3段階評価する。3が最良値である。<Dispersibility of carbon fiber chops> The dispersibility of carbon fiber chops is as follows:
Based on the appearance observation of the plate-shaped molded product of ms, the quality of dispersibility is evaluated in three grades from 1 to 3. 3 is the best value.
〈成形品中の炭素繊維の繊維長〉
成形品をルツボに取り、電気炉にて樹脂を焼く。残った
炭素繊維を顕微鏡にて拡大し、カメラで画像を取り込み
、画像処理機にて炭素繊維の長さを測定する。測定本数
は約1500本とし、その数平均値を算出し炭素繊維の
繊維長とする。<Fiber length of carbon fiber in molded product> Place the molded product in a crucible and bake the resin in an electric furnace. The remaining carbon fibers are magnified with a microscope, an image is captured with a camera, and the length of the carbon fibers is measured with an image processor. The number of fibers to be measured is about 1,500, and the average value of the fibers is calculated as the fiber length of the carbon fiber.
く力学的物性〉
炭素短繊維強化成形品の力学的物性は、JISK681
0に準拠して測定する。Mechanical properties> The mechanical properties of the short carbon fiber reinforced molded product are as per JISK681.
Measured according to 0.
〈導電性〉
炭素短繊維強化成形品の導電性は、上記、炭素繊維チョ
ップの分散性と全く同−法で得た板状成形品上に導電性
銀ペーストを一辺50鴫の正方形の平行な2辺上に塗り
、その間の電気抵抗値をもって、表面抵抗率(Ω)とし
た。<Conductivity> The conductivity of the short carbon fiber-reinforced molded product is determined by applying a conductive silver paste on a plate-shaped molded product obtained in exactly the same manner as the dispersion of the carbon fiber chops described above in parallel squares of 50 squares on each side. It was applied on two sides, and the electrical resistance value between them was defined as the surface resistivity (Ω).
実施例1
エボミンP−1000(日本触媒化学工業社製、ポリエ
チレンイミン、分子量約70,000 )を、水に5重
量%溶かし、この溶液の中に炭素繊維(旭日本カーボン
ファイバー株製ハイカーボロ712kf)のロービング
を、連続的に浸漬し、ポリエチレンイミンを炭素繊維に
5重量%付着させて、140°C5分間熱風で乾燥させ
、ストランドを得た。該ストランドを小野打製作所製り
型ギロチンカッターを用いて6mmの長さに切断して、
かさ密度380g/j!のチョップを得た。Example 1 Evomin P-1000 (manufactured by Nippon Shokubai Kagaku Kogyo Co., Ltd., polyethyleneimine, molecular weight approximately 70,000) was dissolved at 5% by weight in water, and carbon fiber (Hycarboro 712kf, manufactured by Asahi Nippon Carbon Fiber Co., Ltd.) was dissolved in this solution. The rovings were continuously dipped to adhere 5% by weight of polyethyleneimine to the carbon fibers, and dried with hot air at 140°C for 5 minutes to obtain strands. The strand was cut into a length of 6 mm using a guillotine cutter manufactured by Onouchi Seisakusho.
Bulk density 380g/j! Got a chop.
このチョップ10重量部とポリカーボネート樹脂90重
量部とをV型ミキサーでトライブレンドした。10 parts by weight of this chop and 90 parts by weight of polycarbonate resin were triblended using a V-type mixer.
このトライブレンド物を東芝製l575E型射出戒形機
にて、評価用試験片を得た。その結果を第1表に示す、
得られた成形品の分散性評価は3であり繊維長は0.3
5mm、引張強度は1500 kg/c4゜表面電気抵
抗は、2X103Ωであった。A test piece for evaluation was obtained from this triblend product using a Toshiba Model 1575E injection molding machine. The results are shown in Table 1.
The dispersibility evaluation of the obtained molded product was 3, and the fiber length was 0.3.
5 mm, tensile strength was 1500 kg/c4°, and surface electrical resistance was 2×10 3 Ω.
比較例1
実施例1において、エボaンP−1000の濃度を0.
05重型置とし、炭素繊維に付着したポリエチ!/ンイ
aンが0.05重量%以外は、実施例1と全く同一の条
件にて炭素繊維チョップを得た。Comparative Example 1 In Example 1, the concentration of Evan P-1000 was changed to 0.
05 layered and attached to carbon fiber! Carbon fiber chops were obtained under exactly the same conditions as in Example 1, except that the amount of carbon fiber was 0.05% by weight.
得られた炭素繊維チョップのかさ密度は200g/4で
あった。また、射出成形機運転時において、供給口で詰
まりが生じ原料が供給されず運転の中断が多発した。得
られた成形品の分散性の評価は1であり、引張強度は1
100 kg/crl、表面電気抵抗は、1500X
103Ωであった。The bulk density of the obtained carbon fiber chop was 200 g/4. Furthermore, when the injection molding machine was in operation, the supply port was clogged and raw materials were not supplied, resulting in frequent interruptions in operation. The dispersibility evaluation of the obtained molded product was 1, and the tensile strength was 1.
100 kg/crl, surface electrical resistance is 1500X
It was 103Ω.
比較例2
実施例1と同様にして得られたトライブレンド物を、ス
クリューフィダー付の二軸押出機にて混練、押出して得
られたストランドをペレタイズし、繊維強化材料を得た
。次いで、東芝製l575E型射出戊形機にて、評価用
試験片を得た。得られた成形品の分散性評価は3であり
、繊維長は、o、23mm、引張強度は1300kg
/ cU、表面電気抵抗は、500X103Ωであった
。Comparative Example 2 A triblend obtained in the same manner as in Example 1 was kneaded and extruded using a twin-screw extruder equipped with a screw feeder, and the resulting strands were pelletized to obtain a fiber-reinforced material. Next, a test piece for evaluation was obtained using a Toshiba Model 1575E injection molding machine. The dispersibility evaluation of the obtained molded product was 3, the fiber length was o, 23 mm, and the tensile strength was 1300 kg.
/cU, and the surface electrical resistance was 500×10 3 Ω.
比較例3
エボ累ンの水溶液のかわりに、分子預約1800のビス
フェノールA型エポキシ樹脂をメチルエチルケトンに溶
解した溶液を用いた以久は、実施例1と同一の条件にて
炭素繊維チョップを得た。その結果を第1表に示す。Comparative Example 3 Carbon fiber chops were obtained under the same conditions as in Example 1 except that a solution of bisphenol A type epoxy resin with a molecular reservation of 1800 dissolved in methyl ethyl ketone was used instead of the aqueous solution of Evo-Yumin. The results are shown in Table 1.
比較例4
エボミンのかわりに帝国化学産業株式会社製アルコール
可溶性ナイロン溶液(グレード名:F3350E、ナイ
ロン樹脂をメトキシメチル化したもの)を用いた以外は
、実施例1と全く同一の条件にて炭素繊維チョップを得
た。その結果を第1表に示す。Comparative Example 4 Carbon fibers were prepared under exactly the same conditions as in Example 1, except that an alcohol-soluble nylon solution manufactured by Teikoku Kagaku Sangyo Co., Ltd. (grade name: F3350E, methoxymethylated nylon resin) was used instead of Evomin. Got the chop. The results are shown in Table 1.
比較例5
エボミンのかわりに、BASFジャパン株式会社製ポリ
ビニルピロリドン(商品名ニルビスコルに90)を用い
た以外は、実施例1と同一の条件にて炭素繊維チョップ
を得た。その結果を第1表に示す。Comparative Example 5 Carbon fiber chops were obtained under the same conditions as in Example 1, except that polyvinylpyrrolidone (trade name Nilviscol 90) manufactured by BASF Japan Co., Ltd. was used instead of Evomin. The results are shown in Table 1.
比較例6
エボミンのかわりに、大日本インキ化学工業株式会社製
ポリウレタン樹脂(グリスボン6216S L )をメ
チルエチルケトンに溶解した溶液を用いた以外は、実施
例1と同一の条件にて炭素繊維チョップを得た。その結
果を第1表に示す。Comparative Example 6 Carbon fiber chops were obtained under the same conditions as in Example 1, except that instead of Evomin, a solution of polyurethane resin (Grisbon 6216S L) manufactured by Dainippon Ink and Chemicals Co., Ltd. dissolved in methyl ethyl ketone was used. . The results are shown in Table 1.
第 1
表
(以下余白)
注)使用7F・ワックス:Pc
(以下余白)
実施例2
実施例1で用いたポリカーボネート樹脂のかわりに、ポ
リブチレンテレフタレート樹脂を用いた以外は実施例1
と同一の条件で炭素繊維チョップを得た。得られた結果
を第2表に示す。Table 1 (blank below) Note) Used 7F Wax: Pc (blank below) Example 2 Example 1 except that polybutylene terephthalate resin was used instead of the polycarbonate resin used in Example 1.
Carbon fiber chops were obtained under the same conditions. The results obtained are shown in Table 2.
比較例7〜10
ポリカーボネート樹脂のかわりに、ポリブチレンテレフ
タレート樹脂を用いた以外は比較例3〜6と同一の条件
で炭素繊維チョップを得た。得られた結果を第2表に示
す。Comparative Examples 7 to 10 Carbon fiber chops were obtained under the same conditions as Comparative Examples 3 to 6, except that polybutylene terephthalate resin was used instead of polycarbonate resin. The results obtained are shown in Table 2.
(以下余白)
(4)使用マトリックス:PBT
実施例3
実施例工で用いたポリカーボネート樹脂のがわりに、ポ
リフェニレンオキサイド樹脂を用いた以外は実施例1と
同一の条件で炭素繊維チョップを得た。得られた結果を
第3表に示す。(Space below) (4) Matrix used: PBT Example 3 A carbon fiber chop was obtained under the same conditions as in Example 1, except that polyphenylene oxide resin was used instead of the polycarbonate resin used in the example process. The results obtained are shown in Table 3.
比較例11〜15
ポリカーボネート樹脂のかわりに、ポリフェニレンオキ
サイド樹脂を用いた以外は比較例3〜6と同一の条件で
炭素繊維チョップを得た。得られた結果を第3表に示す
。Comparative Examples 11 to 15 Carbon fiber chops were obtained under the same conditions as Comparative Examples 3 to 6 except that polyphenylene oxide resin was used instead of polycarbonate resin. The results obtained are shown in Table 3.
(以下余白)
使用マトリックス:ポリフェニレンオキサイド(以下余
白)
〔発明の効果〕
本発明のボリイくン樹脂で集束された炭素繊維チョップ
は、直接射出成形できる集束性と分散性を兼ね備える優
れたものであり、これを用いて炭素繊維強化成形品を製
造する場合、該チョップは、射出成形機ホッパーにおけ
る流動性が良好であって、射出成形機スクリ1−へ安定
に供給される、また可塑化シリンダー内で容易に分散し
、得られた成形品の外観も極めて良好である。(Hereinafter in the margin) Matrix used: polyphenylene oxide (hereinafter in the margin) [Effects of the invention] The carbon fiber chops bundled with the Bolikun resin of the present invention have excellent binding properties and dispersibility that can be directly injection molded. , when producing a carbon fiber reinforced molded product using this, the chop has good fluidity in the injection molding machine hopper, is stably supplied to the injection molding machine screen 1-, and is also used in the plasticizing cylinder. It is easily dispersed, and the appearance of the obtained molded product is also very good.
よって、炭素繊維強化成形品を生産するに押出し工程を
省略することができ生産性が大幅に向上する。また、該
炭素繊維チョップは直接射出成形ができるため、得られ
ゐ成形品の炭素繊維の長さが長く保たれ、機械強度及び
導電性に優れた特性を示す。Therefore, the extrusion process can be omitted when producing carbon fiber reinforced molded products, and productivity is greatly improved. Furthermore, since the carbon fiber chop can be directly injection molded, the length of the carbon fibers in the resulting molded product is maintained long and exhibits excellent mechanical strength and electrical conductivity.
Claims (1)
量%で集束してなることを特徴とする炭素繊維チョップ
。1. A carbon fiber chop characterized by being made by bundling carbon fibers with a polyimine resin content of 0.1 to 10% by weight.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20032289A JPH0365311A (en) | 1989-08-03 | 1989-08-03 | Carbon fiber chop |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20032289A JPH0365311A (en) | 1989-08-03 | 1989-08-03 | Carbon fiber chop |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0365311A true JPH0365311A (en) | 1991-03-20 |
Family
ID=16422373
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20032289A Pending JPH0365311A (en) | 1989-08-03 | 1989-08-03 | Carbon fiber chop |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0365311A (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102391655A (en) * | 2011-09-08 | 2012-03-28 | 成都理工大学 | Preparation method of octodecyl trimethyl ammonium bromide antibacterial solid paraffin |
| CN102391654A (en) * | 2011-09-08 | 2012-03-28 | 成都理工大学 | Preparation method of enhanced modified octodecyl trimethyl ammonium bromide antibacterial solid paraffin |
| CN102550555A (en) * | 2011-09-08 | 2012-07-11 | 成都理工大学 | Preparation method for dodecyl trimethyl ammonium bromide (DTAB) antibacterial solid paraffin |
| JP2013166922A (en) * | 2012-01-20 | 2013-08-29 | Toray Ind Inc | Molding material |
| JP2013166921A (en) * | 2012-01-20 | 2013-08-29 | Toray Ind Inc | Fiber-reinforced polypropylene-based resin composition |
| US20140356612A1 (en) * | 2012-01-20 | 2014-12-04 | Toray Industries, Inc. | Fiber-reinforced polypropylene resin composition, molding material and prepreg |
| WO2018154867A1 (en) | 2017-02-24 | 2018-08-30 | 東レ株式会社 | Sizing-coated carbon fiber bundle, thermoplastic resin composition, molded body, method for manufacturing sizing-coated carbon fiber bundle, and method for manufacturing molded body |
| JP2019523350A (en) * | 2016-07-19 | 2019-08-22 | ヘクセル コーポレイション | Composite carbon fiber |
| WO2022092194A1 (en) | 2020-10-30 | 2022-05-05 | 三洋化成工業株式会社 | Fiber sizing agent composition, fiber bundle, fiber product, and composite material |
| US12241200B2 (en) | 2018-08-02 | 2025-03-04 | Sanyo Chemical Industries, Ltd. | Sizing agent composition for fibers, fiber bundle, fiber product and composite material |
-
1989
- 1989-08-03 JP JP20032289A patent/JPH0365311A/en active Pending
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102391655A (en) * | 2011-09-08 | 2012-03-28 | 成都理工大学 | Preparation method of octodecyl trimethyl ammonium bromide antibacterial solid paraffin |
| CN102391654A (en) * | 2011-09-08 | 2012-03-28 | 成都理工大学 | Preparation method of enhanced modified octodecyl trimethyl ammonium bromide antibacterial solid paraffin |
| CN102550555A (en) * | 2011-09-08 | 2012-07-11 | 成都理工大学 | Preparation method for dodecyl trimethyl ammonium bromide (DTAB) antibacterial solid paraffin |
| JP2013166922A (en) * | 2012-01-20 | 2013-08-29 | Toray Ind Inc | Molding material |
| JP2013166921A (en) * | 2012-01-20 | 2013-08-29 | Toray Ind Inc | Fiber-reinforced polypropylene-based resin composition |
| US20140356612A1 (en) * | 2012-01-20 | 2014-12-04 | Toray Industries, Inc. | Fiber-reinforced polypropylene resin composition, molding material and prepreg |
| US9879123B2 (en) * | 2012-01-20 | 2018-01-30 | Toray Industries, Inc. | Fiber-reinforced polypropylene resin composition, molding material and prepreg |
| JP2019523350A (en) * | 2016-07-19 | 2019-08-22 | ヘクセル コーポレイション | Composite carbon fiber |
| WO2018154867A1 (en) | 2017-02-24 | 2018-08-30 | 東レ株式会社 | Sizing-coated carbon fiber bundle, thermoplastic resin composition, molded body, method for manufacturing sizing-coated carbon fiber bundle, and method for manufacturing molded body |
| KR20190058676A (en) | 2017-02-24 | 2019-05-29 | 도레이 카부시키가이샤 | Sizing agent-coated carbon fiber bundle, thermoplastic resin composition, molded article, sizing agent-coated carbon fiber bundle manufacturing method, and molded article manufacturing method |
| US12241200B2 (en) | 2018-08-02 | 2025-03-04 | Sanyo Chemical Industries, Ltd. | Sizing agent composition for fibers, fiber bundle, fiber product and composite material |
| WO2022092194A1 (en) | 2020-10-30 | 2022-05-05 | 三洋化成工業株式会社 | Fiber sizing agent composition, fiber bundle, fiber product, and composite material |
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