JPH047373B2 - - Google Patents
Info
- Publication number
- JPH047373B2 JPH047373B2 JP59089902A JP8990284A JPH047373B2 JP H047373 B2 JPH047373 B2 JP H047373B2 JP 59089902 A JP59089902 A JP 59089902A JP 8990284 A JP8990284 A JP 8990284A JP H047373 B2 JPH047373 B2 JP H047373B2
- Authority
- JP
- Japan
- Prior art keywords
- resin
- paper
- composite composition
- resin composite
- defibrated
- 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
Links
- 239000011347 resin Substances 0.000 claims description 42
- 229920005989 resin Polymers 0.000 claims description 42
- 239000000203 mixture Substances 0.000 claims description 39
- 239000000805 composite resin Substances 0.000 claims description 30
- 239000000463 material Substances 0.000 claims description 26
- 239000000835 fiber Substances 0.000 claims description 25
- 238000000034 method Methods 0.000 claims description 23
- 238000005470 impregnation Methods 0.000 claims description 17
- 238000004519 manufacturing process Methods 0.000 claims description 11
- 238000001816 cooling Methods 0.000 claims description 10
- 239000000155 melt Substances 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- 238000009775 high-speed stirring Methods 0.000 claims description 5
- 238000002844 melting Methods 0.000 claims description 3
- 230000008018 melting Effects 0.000 claims description 3
- 239000000123 paper Substances 0.000 description 38
- 239000012530 fluid Substances 0.000 description 13
- 239000010893 paper waste Substances 0.000 description 11
- 239000001913 cellulose Substances 0.000 description 9
- 229920002678 cellulose Polymers 0.000 description 9
- 238000003756 stirring Methods 0.000 description 9
- 229920005672 polyolefin resin Polymers 0.000 description 6
- 229920011250 Polypropylene Block Copolymer Polymers 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 4
- 230000006866 deterioration Effects 0.000 description 4
- 238000007796 conventional method Methods 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 3
- 239000012778 molding material Substances 0.000 description 3
- 239000012779 reinforcing material Substances 0.000 description 3
- 229920005992 thermoplastic resin Polymers 0.000 description 3
- 239000000654 additive Substances 0.000 description 2
- 238000010009 beating Methods 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- -1 polyethylene Polymers 0.000 description 2
- 229920000098 polyolefin Polymers 0.000 description 2
- 238000010008 shearing Methods 0.000 description 2
- 235000013311 vegetables Nutrition 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 206010061592 cardiac fibrillation Diseases 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000002600 fibrillogenic effect Effects 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 238000007731 hot pressing Methods 0.000 description 1
- 239000012770 industrial material Substances 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000009864 tensile test Methods 0.000 description 1
- 238000007666 vacuum forming Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Nonwoven Fabrics (AREA)
- Reinforced Plastic Materials (AREA)
Description
〔産業上の利用分野〕
本発明は紙、特に故紙、紙屑を利用した樹脂複
合材組成物の製造方法に関するものであり、産業
資材、例えばカーエアコンのケーシング等に採用
して好都合なものである。
〔従来の技術〕
近年、省資源省エネルギーの検討が様々な分野
で行われており、その効果があげられている。そ
の中で紙、特に廃棄物としての故紙、紙屑につい
てもこれを用いた樹脂複合材組成物の製造する方
法について種々の検討がなされてきた。
紙は樹脂に混合して充填材として使用した場
合、セルロースを主体とする植物繊維が強化材と
なり、この樹脂複合材組成物を用いた成形物は良
好な機械的特性が期待できる。この様に紙から得
られる、セルロースを主体とする植物繊維は安価
で良好な充填材である。しかし、セルロースを主
体とする植物繊維はその欠点として、大きな剪断
力を受けた場合、破損して短繊維化しやすく、ま
た高温雰囲気下にさらされると熱劣化するという
性質を有する。従つて、紙を利用した樹脂複合材
組成物を製造する場合、この様な欠点に注意して
製造する必要がある。
しかし、従来、例えば特公昭56−9576号公報に
記載の紙を利用した樹脂複合材組成物の製造方法
では、この様な欠点についての考慮が全くなされ
ていない。
例えば、上記公報記載の製造方法は、故紙を直
径3〜6mm程度に粗砕して、熱可塑性樹脂を添加
して保温しながら高速撹拌を与え、樹脂を溶融
し、溶融樹脂相内で故紙の叩解を行ない、叩解さ
れた故紙繊維に樹脂を含浸させて複合材を形成す
るという方法がとられている。
この様な方法で故紙入りの樹脂複合材組成物を
形成した場合、まず粗砕した故紙に熱可塑性樹脂
を添加して保温しながら高速撹拌を与えているこ
と、および溶融樹脂相内で故紙の叩解を行なうと
いう工程を経るため、複合材組成物が形成される
までに、故紙に多大な剪断力並びに熱が加わる。
そのため、故紙は解繊されてセルロースを主体と
する植物繊維の状態となるが、過度の剪断力およ
び熱のため、繊維はその後破損して短繊維化し、
また熱劣化してしまう。短繊維化し、熱栄化した
セルロースを主体とする植物繊維は、樹脂複合材
組成物中で強化材としての特性を十分には発揮で
きない。
例えば、この様な成形材料を用いて、現在最も
一般的に行われている射出成形法を用いて、成形
品を成形した場合、薄肉で複雑な形状のものは金
型より突き出すことができない。従つて現状のま
では、真空成形等の狭い範囲の用途に限られてし
まう。
〔発明の目的〕
そこで、本発明は紙を予め解繊して、セルロー
スを主体とする植物繊維の状態となし、これに溶
融樹脂物を含浸し、その後冷却することで植物繊
維の短繊維化、熱劣化を防ぐようにしたものであ
る。
〔発明の構成〕
本発明の構成は、紙を解繊する工程と、解繊物
に溶融した樹脂を含浸させる工程と、を具備す
る。
本発明において、紙を解繊する工程では、紙を
あらかじめ直径約3〜6mm程度の小片にしたもの
を高速流動混合機で高速撹拌して解繊する方法、
あるいは紙の小片をターボミル等の粉砕機により
解繊する方法、あるいは紙を小片にすることな
く、高速流動混合機あるいはグラツシユミキサー
等の粉砕機を用いて解繊する方法など、いずれの
方法も有効である。更に、これらの方法の中でタ
ーボミルを使用する方法を除いた方法は、いずれ
も水を適量加えて解繊することにより、解繊状態
はより良好となり、また解繊時の摩擦熱の影響も
少なくすることができる。なお、ここで使用する
紙は新聞紙、ダンボール紙、コピー紙などあり、
どの様な紙でも良い。
更に、本発明において、解繊物に溶融した樹脂
を含浸する工程では、解繊物に樹脂シートを熱圧
プレスして含浸するか、あるいは解繊物をシート
状に並べ、それに樹脂粉末を加えて加熱するなど
の方法が有効であり、また解繊物と樹脂を高速撹
拌して摩擦熱による温度上昇で樹脂を解繊物に溶
融含浸させる方法もよい。この方法では、高速流
動混合機中で高速撹拌するなどの方法が有効であ
るが、この場合は含浸終了と同時に回転数を落と
し、溶融状態での高速撹拌は行わない。溶融樹脂
の含浸は速やかに行つた方がよく、時間をかけす
ぎると繊維短繊維化を招き、前述の問題が生じや
すくなる。
本発明において用いる樹脂は通常成形材料とし
て用いられる熱可塑性樹脂であれば何でも良い
が、ポリエンチレン、ポリプロピレンなどのポリ
オレフイン樹脂、ポリスチレン、ポリ塩化ビニル
の様な比較的低融点の樹脂を使用した方が紙のセ
ルロールを主体とする植物繊維が樹脂含浸時に熱
劣化を受けにくくなり、強化材としてその特徴を
発揮する。
また、この含浸工程において繊維と樹脂以外に
繊維と樹脂との密着性を向上させるための添加剤
あるいは樹脂を第3成分として加えることによ
り、更に良好な機械的特性を発揮することができ
る。
例えば、解繊物とポリオレフイン樹脂とを高速
撹拌して摩擦熱による温度上昇でポリオレフイン
樹脂を解繊物に溶融含浸させる場合、繊維とポリ
オレフイン樹脂との密着性を向上させるための第
3成分として変性ポリオレフインを加えて、繊維
とポリオレフイン樹脂とを高速撹拌すると、まず
低融点の変性ポリオレフイン樹脂が溶融して繊維
に含浸され、繊維のぬれ性が向上し、つづいてポ
リオレフイン樹脂が溶融含浸されるため、その結
果得られる繊維物の特性はより良好である。ま
た、目的に応じて添加剤を加えることも可能であ
る。この第3成分としての樹脂は、例えば特公昭
53−1319号公報、特公昭45−36421号公報に開示
されたものを使用できる。本発明において、樹脂
の含浸終了と同時に冷却する工程では、室温に放
置して冷却してもよいが、含浸物を冷却槽に移す
などの方法が有効であり、特に高速流動混合機中
で高速撹拌して含浸したものは含浸終了と同時に
回転数を落として冷却ミキサーの様な冷却撹拌機
に排出して冷却することにより、冷却と同時に適
当な大きさの粒に造粒することができ、これはそ
のまま成形材料として用いることも可能である。
〔発明の効果〕
本発明による紙を利用した樹脂複合材組成物
は、
紙を利用した樹脂複合材組成物製造時に、紙
の解繊工程と含浸工程を分離してセルロースを
主体とする植物繊維の破損および熱劣化を制御
することができる。
解繊物と樹脂との高速撹拌による摩擦熱で樹
脂を溶解して解繊物に含浸させるため、樹脂の
溶解と含浸との両工程と同時に行なうことがで
きる。
樹脂含浸の工程において、解繊物と樹脂と
に、繊維と樹脂との密着性を向上させるための
第3成分を加えることによつて、機械的特性を
より向上することができる。
〔実施例〕
以下に本発明による実施例と、その比較例とし
ての従来方法による例を示し、その成形品として
の試験片げ機械的特性を比較した。
実施例 1
新聞紙を直径約3〜6mmの小片にしたもの30重
量%をターボミルにて粉砕し、解繊物を得る。こ
の解繊物にメルトインデツクス20のポリプロピ
レンブロツクコポリマー70重量%を投入し、高速
流動混合機を用いて、高速撹拌する。この時の摩
擦熱による温度上昇で樹脂を溶解させ、かつ解繊
物に含浸させる。含浸終了と同時に回転数を落
し、速やかに冷却ミキサーに排出して造粒し、紙
を利用した樹脂複合材組成物を得た。
実施例 2
新聞紙を直径約3〜6mmの小片にしたもの40重
量%をターボミルにて粉砕し、解繊物を得る。こ
の解繊物にメルトインデツクス20のポリプロピ
レンブロツクコポリマー60重量%を投入し、高速
流動混合機を用いて高速撹拌する。以後の工程
は、実施例1と同じ方法を用いて紙を利用した樹
脂複合材組成物を得た。
実施例 3
新聞紙30重量%を小片にすることなく、そのま
まグラツシユミキサーに投入し、更に水を新聞紙
と同じ重量加えて、高速撹拌することにより解繊
する。以後は実施例1と同じ方法を用いて紙を利
用した樹脂複合材組成物を得た。
実施例 4
新聞紙40重量%を小片にすることなく、そのま
まグラツシユミキサーに投入し、更に水を新聞紙
と同じ重量加えて、高速撹拌することにより解繊
する。以後は実施例1と同じ方法を用いて紙を利
用した樹脂複合材組成物を得た。
実施例 5
新聞紙を直径約3〜6mmの小片にしたもの30重
量%を高速流動混合機に投入し、高速撹拌するこ
とにより解繊する。この解繊物に、メルトインデ
ツクス20のポリプロピレンブロツクコポリマー
を56重量%、樹脂と紙繊維との密着性を向上させ
ることを目的としてメルトインデツクス15でオ
レフイン部が99.8重量%でエンド−ビシクロ
(2,2,1)−5−ヘプテン−2,3−無水ジカ
ルボン酸が0.2重量%付加している変性ポリオレ
フイン14重量%を投入し、高速撹拌する。この時
の摩擦熱による温度上昇で樹脂を解繊物に溶解含
浸させる。含浸終了と同時に回転数を落とし、冷
却ミキサーに排出して造粒し、紙を利用した樹脂
複合材組成物を得た。
実施例 6
新聞紙を直径約3〜6mmの小片にしたもの30重
量%をターボミルにて粉砕し、解繊物を得る。含
浸工程以降は、高速流動混合機を用いて実施例5
と同じ成分、方法を用いて紙を利用した樹脂複合
材組成物を得た。
実施例 7
新聞紙40重量%を小片にすることなく、そのま
まグラツシユミキサーに投入し、高速撹拌するこ
とにより解繊する。含浸工程以降は、高速流動混
合機を用いて、実施例5と同じ成分、方法を用い
て紙を利用した樹脂複合材組成物を得た。
実施例 8
新聞紙30重量%を小片にすることなく、そのま
ま高速流動混合機に投入し、高速撹拌することに
より解繊する。含浸工程以降は、実施例5と同じ
成分、方法を用いて紙を利用した樹脂複合材組成
物を得た。
実施例 9
新聞紙を直径約3〜6mmの小片にしたもの30重
量%を高速流動混合機に投入し、更に水を新聞紙
と同じ重量加えて、高速撹拌することにより解繊
する。含浸工程以降は、実施例5と同じ成分、方
法を用いて紙を利用した樹脂複合材組成物を得
た。
実施例 10
新聞紙30重量%を小片にすることなく、そのま
まグラツシユミキサーに投入し、更に水を新聞紙
と同じ重量加えて、高速撹拌することにより解繊
する。含浸工程以降は高速流動混合機を用いて実
施例5と同じ成分、方法を用いて紙を利用した樹
脂複合材組成物を得た。
比較例 1
新聞紙を直径約3〜6mmの小片にしたもの30重
量%に、メルトインデツクス20のポリプロピレ
ンブロツクコポリマー70重量%を高速流動混合機
に投入し、高速撹拌する。こ時の摩擦熱で温度が
上昇し、樹脂が溶解する。この樹脂溶解状態で紙
の叩解を進ませる。その後、冷却ミキサーに排出
して冷却し、紙を利用した樹脂複合材組成物を得
た。
比較例 2
新聞紙を直径約3〜6mmの小片にしたもの40重
量%に、メルトインデツクス20のポリプロピレ
ンブロツクコポリマー60重量%を高速流動混合機
に投入し、高速撹拌する。この時の摩擦熱で温度
が上昇し、樹脂が溶解する。この樹脂様相状態で
紙の叩解を進ませる。その後、冷却ミキサーに排
出して冷却し、紙を利用した樹脂複合材組成物を
得た。
以上の実施例および比較例に述べた製造方法に
より得られた、紙を利用した樹脂複合材組成物を
用いて試験片を形成し、その機械的特性の比較を
行つた。その結果を表1に示す。
表1に示す様に、本発明による紙を利用した樹
脂複合材組成物を用いた試験片は、従来方法によ
るものよりも優れた機械的特性を示している。
従つて、本発明により、紙のセルロースを主体
とする植物繊維の特徴を十分に発揮させることが
できた。また、含浸工程で繊維と樹脂の密着性を
向上させるための第3成分を加えた場合には、更
にその効果を大とすることができた。
なお、各物性の測定方法は下記による。
(1) 引張強度 ASTM D−638
(2) 曲げ弾性率 ASTM D−790
(3) アイゾツト衝撃強度 ASTM D−256
また、伸びはASTM D−638に準拠して行つ
たが、引張試験装置のクロスヘツド移動量を試験
片平行部長さで割つて算出した。更に、表1の衝
撃強度の欄において、「ノツチ」とは試験片に設
けた溝を示す。
[Industrial Field of Application] The present invention relates to a method for producing a resin composite composition using paper, particularly waste paper and paper scraps, and is advantageous for use in industrial materials such as car air conditioner casings. . [Prior Art] In recent years, resource and energy conservation has been studied in various fields, and the results have been shown to be effective. Among these, various studies have been made regarding methods for producing resin composite compositions using paper, particularly waste paper and waste paper as waste. When paper is mixed with resin and used as a filler, plant fibers mainly composed of cellulose serve as a reinforcing material, and molded products using this resin composite composition can be expected to have good mechanical properties. Plant fibers mainly composed of cellulose obtained from paper are inexpensive and good fillers. However, vegetable fibers mainly composed of cellulose have the disadvantage that they easily break and become short fibers when subjected to large shearing forces, and are subject to thermal deterioration when exposed to high-temperature atmospheres. Therefore, when producing a resin composite composition using paper, it is necessary to be careful of such drawbacks. However, conventional methods for producing resin composite compositions using paper, such as those described in Japanese Patent Publication No. 56-9576, do not take such drawbacks into consideration at all. For example, in the manufacturing method described in the above publication, waste paper is crushed into pieces with a diameter of about 3 to 6 mm, a thermoplastic resin is added, and high-speed stirring is applied while keeping it warm, the resin is melted, and the waste paper is crushed in the molten resin phase. The method used is to perform beating and impregnate the beaten waste paper fibers with resin to form a composite material. When a resin composite composition containing waste paper is formed by such a method, the thermoplastic resin is first added to the coarsely crushed waste paper and then stirred at high speed while keeping it warm, and the waste paper is mixed in the molten resin phase. Due to the beating process, significant shear forces and heat are applied to the waste paper before the composite composition is formed.
As a result, the waste paper is defibrated into plant fibers mainly composed of cellulose, but due to excessive shearing force and heat, the fibers are subsequently broken and become short fibers.
It also deteriorates due to heat. Plant fibers mainly composed of cellulose that have been shortened and heat eroded cannot fully exhibit their properties as a reinforcing material in a resin composite composition. For example, when a molded article is molded using such a molding material using injection molding, which is currently the most commonly used method, thin and complicatedly shaped articles cannot be ejected from the mold. Therefore, up to now, it has been limited to a narrow range of applications such as vacuum forming. [Object of the Invention] Therefore, the present invention defibrates paper in advance to form plant fibers mainly composed of cellulose, impregnates this with a molten resin, and then cools it to make the plant fibers into short fibers. , which is designed to prevent thermal deterioration. [Configuration of the Invention] The configuration of the present invention includes the steps of defibrating paper and impregnating the defibrated material with molten resin. In the present invention, the step of defibrating paper involves a method of defibrating the paper by first cutting the paper into small pieces with a diameter of about 3 to 6 mm and stirring them at high speed with a high-speed fluid mixer;
Alternatively, there are two methods: defibrating small pieces of paper using a pulverizer such as a turbo mill, or defibrating paper using a pulverizer such as a high-speed fluid mixer or a grain mixer without cutting the paper into small pieces. It is valid. Furthermore, in all of these methods except for the method using a turbo mill, by adding an appropriate amount of water for defibration, the defibration condition is improved and the influence of frictional heat during defibration is also reduced. It can be reduced. The paper used here includes newspaper, cardboard, copy paper, etc.
Any kind of paper is fine. Furthermore, in the present invention, in the step of impregnating the defibrated material with molten resin, the defibrated material is impregnated by hot-pressing a resin sheet, or the defibrated material is arranged in a sheet shape and resin powder is added thereto. It is effective to heat the resin by stirring the defibrated material and the resin at high speed, and melt and impregnate the resin into the defibrated material by increasing the temperature due to frictional heat. In this method, a method such as high-speed stirring in a high-speed fluid mixer is effective, but in this case, the rotation speed is reduced as soon as impregnation is completed, and high-speed stirring in the molten state is not performed. It is better to impregnate the molten resin quickly; if it takes too long, the fibers will become short and the above-mentioned problem will likely occur. The resin used in the present invention may be any thermoplastic resin that is normally used as a molding material, but it is better to use a relatively low melting point resin such as polyolefin resin such as polyethylene or polypropylene, polystyrene, or polyvinyl chloride. The cellulose-based plant fibers are less susceptible to thermal deterioration when impregnated with resin, and exhibit their characteristics as reinforcing materials. Further, in this impregnation step, by adding an additive or a resin as a third component in addition to the fiber and resin to improve the adhesion between the fiber and the resin, even better mechanical properties can be exhibited. For example, when a defibrated material and a polyolefin resin are stirred at high speed and the temperature rises due to frictional heat, the polyolefin resin is melted and impregnated into the defibrated material. When polyolefin is added and the fibers and polyolefin resin are stirred at high speed, the modified polyolefin resin with a low melting point is first melted and impregnated into the fibers, improving the wettability of the fibers, and then the polyolefin resin is melted and impregnated. The properties of the resulting fibrous material are better. It is also possible to add additives depending on the purpose. The resin as the third component is, for example,
Those disclosed in Japanese Patent Publication No. 53-1319 and Japanese Patent Publication No. 45-36421 can be used. In the present invention, in the step of cooling the resin at the same time as the completion of impregnation, it may be allowed to cool by leaving it at room temperature, but it is effective to transfer the impregnated material to a cooling tank. The stirred and impregnated material can be granulated into particles of appropriate size at the same time as cooling by lowering the rotation speed and discharging it into a cooling mixer such as a cooling mixer to cool it. This can also be used as a molding material as it is. [Effects of the Invention] The resin composite composition using paper according to the present invention can be produced by separating the paper fibrillation process and the impregnation process during the production of the paper resin composite composition, and producing vegetable fibers mainly composed of cellulose. damage and thermal deterioration can be controlled. Since the resin is melted and impregnated into the defibrated material by the frictional heat generated by high-speed stirring between the defibrated material and the resin, both steps of dissolving the resin and impregnating the resin can be performed simultaneously. In the step of resin impregnation, mechanical properties can be further improved by adding a third component to the defibrated material and the resin to improve the adhesion between the fibers and the resin. [Example] Examples according to the present invention and examples according to the conventional method as comparative examples thereof are shown below, and the mechanical properties of test pieces as molded products are compared. Example 1 30% by weight of newspaper cut into small pieces with a diameter of about 3 to 6 mm is pulverized in a turbo mill to obtain a defibrated material. 70% by weight of a polypropylene block copolymer having a melt index of 20 is added to this defibrated material, and the mixture is stirred at high speed using a high-speed fluid mixer. At this time, the temperature rise due to frictional heat causes the resin to melt and impregnate the defibrated material. At the same time as the impregnation was completed, the rotation speed was reduced, and the mixture was immediately discharged to a cooling mixer and granulated to obtain a resin composite composition using paper. Example 2 40% by weight of newspaper cut into small pieces with a diameter of about 3 to 6 mm is pulverized in a turbo mill to obtain a defibrated material. 60% by weight of a polypropylene block copolymer having a melt index of 20 is added to this defibrated material, and the mixture is stirred at high speed using a high-speed fluid mixer. In the subsequent steps, the same method as in Example 1 was used to obtain a resin composite composition using paper. Example 3 30% by weight of newspaper is put into a grain mixer as it is without being cut into small pieces, water is added in the same weight as the newspaper, and the mixture is defibrated by stirring at high speed. Thereafter, a resin composite composition using paper was obtained using the same method as in Example 1. Example 4 40% by weight of newspaper is put into a grain mixer as it is without being cut into small pieces, water is added in the same weight as the newspaper, and the mixture is defibrated by stirring at high speed. Thereafter, a resin composite composition using paper was obtained using the same method as in Example 1. Example 5 30% by weight of newspaper cut into small pieces with a diameter of about 3 to 6 mm is placed in a high-speed fluid mixer and defibrated by stirring at high speed. To this defibrated material, 56% by weight of a polypropylene block copolymer with a melt index of 20 was added, and in order to improve the adhesion between the resin and paper fibers, an endo-bicyclo copolymer with a melt index of 15 and an olefin component of 99.8% by weight was added. 14% by weight of a modified polyolefin to which 0.2% by weight of 2,2,1)-5-heptene-2,3-dicarboxylic anhydride has been added is charged and stirred at high speed. At this time, the temperature rise due to frictional heat causes the resin to dissolve and impregnate the defibrated material. At the same time as the impregnation was completed, the rotation speed was reduced, and the mixture was discharged into a cooling mixer and granulated to obtain a resin composite composition using paper. Example 6 30% by weight of newspaper cut into small pieces with a diameter of about 3 to 6 mm was ground in a turbo mill to obtain a defibrated material. After the impregnation step, a high-speed fluid mixer was used in Example 5.
A resin composite composition using paper was obtained using the same ingredients and method. Example 7 40% by weight of newspaper was put into a grain mixer without being cut into small pieces and defibrated by stirring at high speed. After the impregnation step, a resin composite composition using paper was obtained using the same components and method as in Example 5 using a high-speed fluid mixer. Example 8 30% by weight of newspaper was put into a high-speed fluid mixer without being cut into small pieces, and defibrated by stirring at high speed. After the impregnation step, the same ingredients and method as in Example 5 were used to obtain a resin composite composition using paper. Example 9 30% by weight of newspaper cut into small pieces with a diameter of about 3 to 6 mm is put into a high-speed fluid mixer, water is added in the same weight as the newspaper, and the mixture is defibrated by stirring at high speed. After the impregnation step, the same ingredients and method as in Example 5 were used to obtain a resin composite composition using paper. Example 10 30% by weight of newspaper is put into a grain mixer as it is without being cut into small pieces, water is added in the same weight as the newspaper, and the mixture is defibrated by stirring at high speed. After the impregnation step, a resin composite composition using paper was obtained using the same components and method as in Example 5 using a high-speed fluid mixer. Comparative Example 1 30% by weight of newspaper cut into small pieces of about 3 to 6 mm in diameter and 70% by weight of a polypropylene block copolymer with a melt index of 20 are placed in a high-speed fluid mixer and stirred at high speed. The frictional heat generated at this time raises the temperature and melts the resin. The paper is beaten in this resin-dissolved state. Thereafter, it was discharged into a cooling mixer and cooled to obtain a resin composite composition using paper. Comparative Example 2 40% by weight of newspaper cut into small pieces of about 3 to 6 mm in diameter and 60% by weight of a polypropylene block copolymer with a melt index of 20 are placed in a high-speed fluid mixer and stirred at high speed. The frictional heat at this time raises the temperature and melts the resin. The paper is beaten in this resin-like state. Thereafter, it was discharged into a cooling mixer and cooled to obtain a resin composite composition using paper. A test piece was formed using a resin composite composition using paper obtained by the manufacturing method described in the above Examples and Comparative Examples, and the mechanical properties thereof were compared. The results are shown in Table 1. As shown in Table 1, the test pieces using the paper-based resin composite composition according to the present invention exhibit better mechanical properties than those made using the conventional method. Therefore, according to the present invention, the characteristics of paper fibers mainly composed of cellulose can be fully exhibited. Moreover, when a third component was added to improve the adhesion between the fiber and the resin in the impregnation step, the effect could be further enhanced. The method for measuring each physical property is as follows. (1) Tensile strength ASTM D-638 (2) Flexural modulus ASTM D-790 (3) Izot impact strength ASTM D-256 The elongation was conducted in accordance with ASTM D-638, but the crosshead of the tensile test device It was calculated by dividing the amount of movement by the length of the parallel part of the specimen. Furthermore, in the impact strength column of Table 1, "notch" refers to a groove provided in the test piece.
【表】【table】
Claims (1)
脂を含浸させる工程と、含浸終了後に冷却する工
程と、を有した樹脂複合材組成の製造方法。 2 前記解繊工程には適量の水が加えられている
特許請求の範囲第1項記載の樹脂複合材組成の製
造方法。 3 前記含浸工程は、前記解繊工程による解繊物
と前記樹脂とを高速撹拌して両者の摩擦熱による
温度上昇で該樹脂を前記解繊物に溶融含浸させる
構成を包含する特許請求の範囲第1項記載の樹脂
複合材組成の製造方法。 4 前記解繊工程には適量の水が加えられている
特許請求の範囲第3項記載の樹脂複合材組成の製
造方法。 5 前記含浸工程は、前記樹脂と前記解繊工程に
よる解繊物の繊維との密着性を向上させる第3成
分とを溶融させて該溶融物を前記解繊物に含浸さ
せる構成を包含する特許請求の範囲第1項記載の
樹脂複合材組成の製造方法。 6 前記含浸工程における樹脂および第3成分の
溶融は、該樹脂、前記第3成分、および前記解繊
物の高速撹拌による摩擦熱により生ずる特許請求
の範囲第5項記載の樹脂複合材組成の製造方法。 7 前記解繊工程には適量の水が加えられている
特許請求の範囲第5項または第6項何れか一つに
記載樹脂複合材組成の製造方法。[Scope of Claims] 1. A method for producing a resin composite material composition, comprising the steps of defibrating paper, impregnating the defibrated material with molten resin, and cooling after completion of the impregnation. 2. The method for producing a resin composite composition according to claim 1, wherein an appropriate amount of water is added to the defibration step. 3. Claims that the impregnation step includes a configuration in which the defibrated material from the defibrating step and the resin are stirred at high speed and the resin is melted and impregnated into the defibrated material by a temperature rise due to frictional heat between the two. 2. A method for producing a resin composite composition according to item 1. 4. The method for producing a resin composite composition according to claim 3, wherein an appropriate amount of water is added to the defibration step. 5. A patent that includes a configuration in which the impregnation step involves melting the resin and a third component that improves the adhesion between the resin and the fibers of the defibrated product obtained in the defibrating step, and impregnating the defibrated product with the melt. A method for producing a resin composite composition according to claim 1. 6. Manufacturing a resin composite composition according to claim 5, wherein the resin and the third component are melted in the impregnation step by frictional heat caused by high-speed stirring of the resin, the third component, and the defibrated material. Method. 7. The method for producing a resin composite composition according to claim 5 or 6, wherein an appropriate amount of water is added to the defibration step.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59089902A JPS60233134A (en) | 1984-05-04 | 1984-05-04 | Preparation of resin composite material composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59089902A JPS60233134A (en) | 1984-05-04 | 1984-05-04 | Preparation of resin composite material composition |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60233134A JPS60233134A (en) | 1985-11-19 |
| JPH047373B2 true JPH047373B2 (en) | 1992-02-10 |
Family
ID=13983655
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59089902A Granted JPS60233134A (en) | 1984-05-04 | 1984-05-04 | Preparation of resin composite material composition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60233134A (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4846315B2 (en) * | 2005-09-22 | 2011-12-28 | ダイセルポリマー株式会社 | Method for producing cellulose fiber-containing thermoplastic resin composition |
| JP4846405B2 (en) * | 2006-03-27 | 2011-12-28 | 北越紀州製紙株式会社 | Method for producing paper-containing thermoplastic resin composition |
| JP2008297479A (en) * | 2007-06-01 | 2008-12-11 | Daicel Polymer Ltd | Method for producing cellulose fiber-containing thermoplastic resin composition |
| JP5395496B2 (en) * | 2008-09-12 | 2014-01-22 | ダイセルポリマー株式会社 | Method for producing cellulose fiber-containing thermoplastic resin composition |
| JP6469068B2 (en) * | 2016-12-12 | 2019-02-13 | 富士紙管株式会社 | Synthetic resin composition containing fiber components and method for producing the same |
| CN117405284B (en) * | 2023-12-15 | 2024-03-01 | 南京中鑫智电科技有限公司 | Pressure early warning method and system for sleeve oil hole plug assembly |
-
1984
- 1984-05-04 JP JP59089902A patent/JPS60233134A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60233134A (en) | 1985-11-19 |
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