JPS62288011A - Manufacture of fiber reinforced resin molding - Google Patents
Manufacture of fiber reinforced resin moldingInfo
- Publication number
- JPS62288011A JPS62288011A JP61132047A JP13204786A JPS62288011A JP S62288011 A JPS62288011 A JP S62288011A JP 61132047 A JP61132047 A JP 61132047A JP 13204786 A JP13204786 A JP 13204786A JP S62288011 A JPS62288011 A JP S62288011A
- Authority
- JP
- Japan
- Prior art keywords
- fibers
- pellets
- fiber bundle
- resin
- fiber
- 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
- 239000000835 fiber Substances 0.000 title claims abstract description 101
- 229920005989 resin Polymers 0.000 title claims abstract description 39
- 239000011347 resin Substances 0.000 title claims abstract description 39
- 238000000465 moulding Methods 0.000 title claims abstract description 19
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- 239000008188 pellet Substances 0.000 claims abstract description 67
- 239000011230 binding agent Substances 0.000 claims abstract description 17
- 239000012784 inorganic fiber Substances 0.000 claims abstract description 6
- 238000002844 melting Methods 0.000 claims description 2
- 230000008018 melting Effects 0.000 claims description 2
- 239000000853 adhesive Substances 0.000 claims 1
- 230000001070 adhesive effect Effects 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 12
- 239000002904 solvent Substances 0.000 abstract description 3
- -1 acrylic ester Chemical class 0.000 description 6
- 239000003365 glass fiber Substances 0.000 description 6
- 239000000463 material Substances 0.000 description 5
- 230000000704 physical effect Effects 0.000 description 5
- 229920013716 polyethylene resin Polymers 0.000 description 4
- 239000012779 reinforcing material Substances 0.000 description 4
- 239000004743 Polypropylene Substances 0.000 description 3
- 229920002978 Vinylon Polymers 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- 239000011521 glass Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 229920000728 polyester Polymers 0.000 description 3
- 229920001155 polypropylene Polymers 0.000 description 3
- 229920002689 polyvinyl acetate Polymers 0.000 description 3
- 239000011118 polyvinyl acetate Substances 0.000 description 3
- 239000012783 reinforcing fiber Substances 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229920006122 polyamide resin Polymers 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 239000004925 Acrylic resin Substances 0.000 description 1
- 229920000178 Acrylic resin Polymers 0.000 description 1
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- 229920001328 Polyvinylidene chloride Polymers 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 1
- 238000009787 hand lay-up Methods 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229920002239 polyacrylonitrile Polymers 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 239000005033 polyvinylidene chloride Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 229920006337 unsaturated polyester resin Polymers 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/12—Making granules characterised by structure or composition
- B29B9/14—Making granules characterised by structure or composition fibre-reinforced
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Moulding By Coating Moulds (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
Abstract
Description
【発明の詳細な説明】
〈産業上の利用分野〉
本発明は、@強繊維がほぼ均一に分散されている繊維強
化樹脂成形物の製造法に関する。DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to a method for manufacturing a fiber-reinforced resin molded article in which strong fibers are almost uniformly dispersed.
〈従来の技術〉
FRP(以下FRTPを含む)は従来ガラス繊維の短繊
維または長繊維を補強材とした樹脂成形物であったが、
近年FRP用途の多様化に伴って、高強力、高伸度、高
弾性率及び軽量等の特性に優れた有機繊維や、導電性を
有する炭素繊維々ど、ガラス繊維以外の繊維を補強材と
して使用するものが増加傾向にある。<Conventional technology> FRP (hereinafter referred to as FRTP) has traditionally been a resin molded product using short or long glass fibers as reinforcement materials.
In recent years, with the diversification of FRP applications, fibers other than glass fibers, such as organic fibers with excellent properties such as high strength, high elongation, high elastic modulus, and light weight, and conductive carbon fibers, are being used as reinforcing materials. The number of items used is increasing.
ガラス繊維を補強材にしたF RPに対し、有機繊維を
補強材とするFRPの物性向上について、ビニロン繊維
の場合について実験値に基づいて説明すれば、次の如く
である。耐衝撃性能は5倍以上、耐摩耗性能は砥石質の
もので8倍以上、他に比重が1/2で軽量効果があり、
耐アルカリ性に於ては、ガラスがアルカリ中で使用に耐
えないのに対シビニロンはアルカリ耐久性が高い。The improvement in physical properties of FRP using organic fiber as a reinforcing material compared to FRP using glass fiber as a reinforcing material will be explained based on experimental values in the case of vinylon fiber. The impact resistance is more than 5 times, the abrasion resistance is more than 8 times that of a grindstone, and the specific gravity is 1/2, making it lightweight.
Regarding alkali resistance, glass cannot withstand use in alkali, whereas Sibinyron has high alkali resistance.
このように、夫々の有機繊組。の持つ特性をガラスに代
替して又はガラスと併用して、FRPに使用されている
のは周知の通りである。In this way, each organic fiber group. It is well known that FRP is used in place of glass or in combination with glass due to its characteristics.
〈発明が解決しようとする問題点〉
しかしながらこのように夫々の有機繊維がガラス繊維に
無い優れた特性を有しているにもかかわらず、現在その
利用が、BMC,ハンドレイアップ等バッチシステム加
工法に用いられるのみで、樹脂ペレットから成形する成
形方法に於ては使用−2=
されていない。それは以下の理由による。<Problems to be solved by the invention> However, although each organic fiber has excellent properties not found in glass fiber, its use is currently limited to batch system processing such as BMC and hand layup. It is only used in the molding method, and is not used in the molding method of molding resin pellets. This is due to the following reasons.
すなわちバッチ式加工法に於て、ミキサーの中に樹脂ペ
レットと繊維を投入混合する場合、ペレットの直径が約
3samであるに対し、単繊維の直径が0.015m程
度で、両者の形状に大差があるため攪拌中繊維が偏在し
易く、繊維の均一分散に苦労が絶えない。In other words, in the batch processing method, when resin pellets and fibers are mixed in a mixer, the diameter of the pellets is about 3 sam, whereas the diameter of the single fibers is about 0.015 m, and there is a large difference in the shape of the two. Because of this, the fibers tend to be unevenly distributed during stirring, making it difficult to uniformly disperse the fibers.
く問題点を解決するための手段〉
本発明者等は、以上の問題点を解決するために研究を行
なった結果、本発明に到達した。Means for Solving the Problems> The present inventors conducted research to solve the above problems, and as a result, they arrived at the present invention.
すなわち本発明は、有機繊維または無機繊維を集束し、
結着剤で固化し、この繊維束を切断して得られる繊維束
ペレットを樹脂ペレットと混合し、この混合ペレットを
成形する際またはそれに先立って該結着剤を溶解または
溶融させて繊維を分散させることを特徴とする繊維強化
樹脂成形物の製造法である。That is, the present invention focuses organic fibers or inorganic fibers,
The fiber bundle pellets obtained by solidifying with a binder and cutting the fiber bundles are mixed with resin pellets, and the binder is dissolved or melted to disperse the fibers when or prior to molding the mixed pellets. This is a method for producing a fiber-reinforced resin molded article.
FRP用の各種樹脂は、通常、直径が2■〜4−1長さ
が2■〜3闘程度のペレット状であって、かつペレット
状態で極めて流動し易い。Various resins for FRP are usually in the form of pellets with a diameter of 2 to 4 mm and a length of 2 to 3 mm, and are extremely fluid in the pellet form.
〜3一
本発明者等は、このような形状の樹脂ペレットに繊維を
特に均一に混合するためには、繊維束ペレットを樹脂ペ
レットとほぼ同一の大きさにすればよいことも判った。~31 The present inventors have also found that in order to mix fibers particularly uniformly into resin pellets having such a shape, it is sufficient to make the fiber bundle pellets approximately the same size as the resin pellets.
すなわち、はぼ同一の大きさのペレット(樹脂ペレット
と繊維束ペレット)を先に均一混合しておき、然るのち
に繊維束ペレットを熱又は溶剤により融解させて単繊維
に分散させることによシ、バッチ式成形法であっても、
あるいは連続式成形法であっても、よジ均−分散された
成形物が得られることとなる。In other words, pellets of approximately the same size (resin pellets and fiber bundle pellets) are first mixed uniformly, and then the fiber bundle pellets are melted with heat or a solvent and dispersed into single fibers. Even if it is a batch molding method,
Alternatively, even if a continuous molding method is used, a molded product with very uniform dispersion can be obtained.
繊維束ペレットを作製する基本的方法について以下に説
明する。The basic method for producing fiber bundle pellets will be described below.
まず有機繊維または無機繊維を集束し、次に熱または溶
剤によって溶解する結着剤で、好ましくは混合する樹脂
ペレットの直径に相当する太さに該集束物を固化成形し
て連続した繊維束を作る。First, organic or inorganic fibers are bundled, and then the bundle is solidified and formed into a continuous fiber bundle using a binder that dissolves with heat or a solvent, preferably to a thickness corresponding to the diameter of the resin pellets to be mixed. make.
そして、それを適当な長さ、好ましくは樹脂ペレットの
長さに相当する長さに切断することにより繊維束ペレッ
トが得られる。Then, fiber bundle pellets are obtained by cutting it into a suitable length, preferably a length corresponding to the length of the resin pellet.
繊維束ペレットの大きさとしては、直径0.5〜〜10
m 、直径/長さが0.05〜5.0である円筒状が
一応好ましいが、特に樹脂ペレットとほぼ同一の大きさ
が前述したようによ如好ましく、この点から言えば直径
1.5〜6 wax 、長さ1.5〜6wmのものがよ
シ好ましいこととなる。なお繊維束ペレットの形状とし
ては、前述したように円筒状が好ましいが、これ以外の
形状、たとえば断面形状がだ円形、矩形等であってもよ
い。断面形状が円以外の場合には、断面形状の大きさは
、同面積の円に換算してその直径が上記範囲になるよう
にするのが好ましい。The size of the fiber bundle pellet is 0.5 to 10 in diameter.
A cylindrical shape with a diameter/length of 0.05 to 5.0 is preferable, but as mentioned above, a cylindrical shape having a diameter/length of 0.05 to 5.0 is particularly preferable, and from this point of view, a diameter of 1.5 m is preferable. ~6 wax and a length of 1.5 to 6 wm are more preferred. The shape of the fiber bundle pellet is preferably cylindrical as described above, but other shapes such as an oval or rectangular cross-sectional shape may also be used. When the cross-sectional shape is other than a circle, it is preferable that the size of the cross-sectional shape is converted into a circle with the same area and its diameter falls within the above range.
繊維束ペレットは、集束した繊維全体に結着剤を含浸固
化した形態であっても、あるいは繊維束の外表部を結着
剤の皮膜で被覆成形した形態であってもよい。樹脂中で
容易に単繊維に分離させる為には、結着剤の付着量は少
い程好ましいが、切断時に形状が崩壊しないことが必要
である。The fiber bundle pellet may be in a form in which the entire bundled fibers are impregnated with a binder and solidified, or in a form in which the outer surface of the fiber bundle is coated with a film of a binder. In order to easily separate the fibers into single fibers in the resin, it is preferable that the amount of the binder attached is as small as possible, but it is necessary that the shape does not collapse during cutting.
第1図は上記の集束した繊維全体に結着剤を含浸固化し
たものを示しておシ、第2図は繊維束の外表部を結着剤
の皮膜で被覆成形したものを示し−5〜
ている。これら図中、1は単繊維、2は結着剤、3はこ
れによ如得られる繊維束ペレットを示している。また第
3図は繊維束ペレットと樹脂ペレットを混合したもので
あシ、同図中、3は繊維束ペレット、4は樹脂ペレット
である。この図からも明らかなように、本発明において
樹脂ペレットと繊維束ペレットはほぼ同一の大きさを有
しているのが好ましい。Figure 1 shows the bundled fibers impregnated with a binder and solidified, and Figure 2 shows the outer surface of the fiber bundle coated with a film of the binder. ing. In these figures, 1 indicates a single fiber, 2 a binder, and 3 a fiber bundle pellet obtained thereby. Further, FIG. 3 shows a mixture of fiber bundle pellets and resin pellets, and in the figure, 3 is a fiber bundle pellet and 4 is a resin pellet. As is clear from this figure, in the present invention, it is preferable that the resin pellet and the fiber bundle pellet have approximately the same size.
繊維束を固化させる結着剤としては、理想的には成形体
を構成する樹脂と親和性を有するものがよい。例えば不
飽和ポリエステル樹脂用としてはスチレンに溶解し易い
酢酸ビニル系やポリスチレン系のものが良好であシ、エ
ポキシ樹脂用としては、エポキシ変性酢酸ビニル系のも
のが効果的である。FRTPO場合、アクリル樹脂用と
してはアクリル酸エステル系、ポリプロピレン樹脂用と
してはポリプロピレン系、ポリエチレン樹脂用としては
ポリエチレン系のものを夫々使用するのが合理的である
。但し、成形物の用途によっては、これに限らず、現在
ガラス繊維の集束材として使用されているものであれば
一般的に使用が可能である。Ideally, the binder for solidifying the fiber bundle should be one that has affinity with the resin constituting the molded body. For example, for unsaturated polyester resins, vinyl acetate and polystyrene-based resins that are easily soluble in styrene are effective, and for epoxy resins, epoxy-modified vinyl acetate-based resins are effective. In the case of FRTPO, it is reasonable to use an acrylic ester type for acrylic resin, a polypropylene type for polypropylene resin, and a polyethylene type for polyethylene resin. However, depending on the purpose of the molded product, the material is not limited to this, and any material currently used as a binding material for glass fibers may be used.
補強材として使用する繊維としては、繊維形状を有する
ものであれば、繊維束ペレットへの加工は可能である。As long as the fibers used as the reinforcing material have a fiber shape, they can be processed into fiber bundle pellets.
%に繊維の太さが30μm以下のものが好ましく、有機
繊維としてはセルロース系、ポリアミド系、ポリビニー
ルアルコール系、ポリ塩化ビニリデン系、ポリ塩化ビニ
ル系、ポリエステル系、ポリアクリロニトリル系、ポリ
エチレン系、ポリプロピレン系、ポリウレタン系、ポリ
フラール、フェノール系、芳香族ポリアミド系、全芳香
族ポリエステル系等の繊維及び炭素繊維、無機繊維とし
ては、ガラス繊維、セラミック繊維、金属繊維等が使用
出来る。また以上の繊維を共重合変性及び複合化した繊
維を使用することも出来るO
むろん具体的に用いる繊維は、ペレットの成形条件下に
於て、さらにその後の成形条件下において、分解、溶解
、溶融等によシ補強繊維として要求される物性値を失わ
ないものである必要がある。Preferably, the fiber thickness is 30 μm or less, and organic fibers include cellulose, polyamide, polyvinyl alcohol, polyvinylidene chloride, polyvinyl chloride, polyester, polyacrylonitrile, polyethylene, and polypropylene. As the inorganic fibers, glass fibers, ceramic fibers, metal fibers, etc. can be used. Furthermore, it is also possible to use fibers obtained by copolymerizing, modifying, and compositing the above fibers.Of course, the fibers specifically used are subject to decomposition, dissolution, and melting under the pellet molding conditions and the subsequent molding conditions. It is necessary that the material does not lose the physical properties required as a reinforcing fiber.
このようにして得られた繊維束ペレットは樹脂ペレット
に混合される。その混合比は、必要とする成形物の強度
から決められるものであシ、シだがって一概には言えな
い。すなわち、より強度に優れた成形物を得たい場合に
は繊維束ペレットの割合を多くシ、逆に特に高い強度を
必要としない場合には、少量配合すればよい。The fiber bundle pellets thus obtained are mixed with resin pellets. The mixing ratio is determined based on the required strength of the molded product, so it cannot be generalized. That is, if it is desired to obtain a molded product with better strength, the proportion of the fiber bundle pellets may be increased, and conversely, if particularly high strength is not required, a small amount may be added.
繊維束ペレットを混合した後の樹脂ペレットから通常の
成形方法によシ成形物が得られる。この際またはこの成
形に先立って繊維束ペレットを結束している結着剤が溶
解または溶融して繊維束ペレットが樹脂中に単繊維に分
散する。A molded product is obtained from the resin pellets after mixing the fiber bundle pellets by a normal molding method. At this time or prior to this molding, the binder binding the fiber bundle pellets is dissolved or melted, and the fiber bundle pellets are dispersed into single fibers in the resin.
以上述べた如く、本発明の方法は、補強繊維を均一に分
散できるという大きな特長点を有しているが、この他に
、繊維束ペレットを振動フィーダー等により定量的に樹
脂ペレットおよび液相の樹脂マトリックス中に連続的に
供給できるという長所も有している。As mentioned above, the method of the present invention has the great advantage of being able to uniformly disperse reinforcing fibers, but in addition to this, the method of the present invention also has the advantage that the fiber bundle pellets are quantitatively separated into resin pellets and liquid phase using a vibrating feeder or the like. It also has the advantage of being able to be continuously supplied into the resin matrix.
以下実施例により本発明を説明する。The present invention will be explained below with reference to Examples.
実施例1
単糸6デニールのビニロン繊維200本を一構成単位と
する1200デニールの連続したマルチフィラメント糸
をボビンに捲き取シ、ボビン30個をボビンスタンドに
掛けて夫々のボビンから糸を引出して30本を合糸して
、合計36,000デニールの集束糸とし、これをポリ
酢酸ビニール樹脂槽内に導いてポリ酢酸ビニールを含浸
させ、直径3■の穴(厚さ5mのベークライト板に3.
0瓢φの穴をあけ、板をダイスで固定した。)を通して
太さ3.OWφの連続した繊維束成形物を得た。乾燥後
との繊維束を自動カッターで3.5%に切断して繊維束
ペレットを作製した。ポリ酢酸ビニール樹脂対繊維の重
量比は41:49であった。Example 1 A continuous multifilament yarn of 1,200 denier each consisting of 200 single 6-denier vinylon fibers was wound onto a bobbin, and 30 bobbins were hung on a bobbin stand and the yarn was pulled out from each bobbin. The 30 yarns were combined to make a bundled yarn with a total of 36,000 deniers, which was led into a polyvinyl acetate resin bath to be impregnated with polyvinyl acetate. ..
A hole of 0 mm diameter was drilled and the board was fixed with a die. ) through the thickness 3. A continuous fiber bundle molded product of OWφ was obtained. After drying, the fiber bundle was cut into 3.5% pieces using an automatic cutter to produce fiber bundle pellets. The weight ratio of polyvinyl acetate resin to fiber was 41:49.
このようにして得た繊維束を次のような条件で成形して
樹脂板を作製した。The fiber bundle thus obtained was molded under the following conditions to produce a resin plate.
ポリエチレン樹脂(直径2.5 wg 、長さ3.5m
の円筒形ペレット)を80部および該繊維束ペレットを
20部配合して攪拌後ホッパーに投入ロールプレス法に
より、温度165℃、圧力10kf/aA。Polyethylene resin (diameter 2.5 wg, length 3.5 m
80 parts of the cylindrical pellets) and 20 parts of the fiber bundle pellets were mixed, stirred, and then put into a hopper using a roll press method at a temperature of 165° C. and a pressure of 10 kf/aA.
時間20分、水冷ロールで冷却して仕上り厚さ2.3%
のFRTP板を作製した。対照として単糸6デニールの
同一ビニロン繊維を3.5諺にcutシfcモのを、そ
のままホッパーに投入該ポリエチレン樹脂と混練し上記
と同一条件で厚さ2.5諺のFRTP板を用意した。−
物性測定値は表−1の通りであった。Cool for 20 minutes with a water-cooled roll to a finished thickness of 2.3%.
A FRTP board was produced. As a control, a single 6-denier vinylon fiber cut into a 3.5-mm diameter was put into a hopper as it was, kneaded with the polyethylene resin, and an FRTP board with a thickness of 2.5-mm was prepared under the same conditions as above. . - The measured physical properties were as shown in Table-1.
表 −1
実施例2
単繊維3.2デニールの繊維48本を構成単位とする1
50デニールのポリエステルマルチフィラメントを50
本合糸して集束糸とし、この連続した集束糸を溶融ポリ
エチレン樹脂(旭化成工業製L−2340)にdipi
ng シて集束糸成形物を得だ。この成形物の直径は4
.3%、樹脂対繊維の重量比率は32:68であった。Table-1 Example 2 1 whose constituent unit is 48 single fibers of 3.2 denier
50 denier polyester multifilament
This continuous bundled yarn is made into a bundled yarn, and this continuous bundled yarn is dipiped into molten polyethylene resin (L-2340 manufactured by Asahi Kasei Industries).
ng to obtain a bundled yarn molded product. The diameter of this molding is 4
.. 3%, and the weight ratio of resin to fiber was 32:68.
この連続集束糸成形物を3鶏の長さに切断して繊維束ペ
レットを作製した。This continuous bundled yarn molded product was cut into three lengths to produce fiber bundle pellets.
このようにして得た繊維束30部およびポリアミド樹脂
(アミラン・東し製太さ2.5■長さ3.0−の円筒形
ペレット)70部を攪拌混合して、プレス成形機で温度
227℃で7分間200 kf/ctIの圧力で成形し
て厚さ3.2mの繊維強化樹脂板を得た。対照として繊
維束ペレットの代シに、単繊維3.2テニール、長さ3
.0■の同一ポリエステル繊維をそのまま同じ割合でポ
リアミド樹脂に混合成形して厚さ3.4−の繊維強化樹
脂板を用意した。30 parts of the fiber bundle thus obtained and 70 parts of polyamide resin (cylindrical pellets of thickness 2.5 x length 3.0 - manufactured by Amilan Toshi) were stirred and mixed, and the mixture was molded using a press molding machine at a temperature of 227°C. A fiber-reinforced resin plate with a thickness of 3.2 m was obtained by molding at a pressure of 200 kf/ctI for 7 minutes at °C. As a control, a single fiber of 3.2 tenier and length 3 was used instead of fiber bundle pellets.
.. A fiber-reinforced resin board having a thickness of 3.4 mm was prepared by mixing and molding the same polyester fibers of 0 mm in the same ratio into polyamide resin.
両者の耐衝撃値は表−2の通りであった。The impact resistance values of both were as shown in Table-2.
表 −2
実施例11実施例2にみられるように、繊維束ペレット
にして繊維を混入したものが、そうでないものより高い
物性値が得られることを確認するために、実施例1,2
の本発明品と対照品夫々を破壊して内部を詳細に観察し
た結果、何れも本発明品は補強繊維が均一に試料全体に
分散しているのに対し、対照品は著しく、繊維が偏在し
、繊維が全く存在しない部分が観察された。従って、こ
の繊維の存在しない部分が耐衝撃強力に寄与しない為に
対照品は同一繊維量を投入しても物性向上に効果を現わ
さないと推定される。Table 2 Example 11 As seen in Example 2, in order to confirm that the fiber bundle pellets mixed with fibers had higher physical property values than those without the fiber bundle pellets, Examples 1 and 2 were prepared.
As a result of destroying the inventive product and the control product and observing the insides in detail, it was found that the reinforcing fibers of the inventive product were evenly distributed throughout the sample, whereas the fibers were significantly unevenly distributed in the control product. However, some areas where no fibers were observed were observed. Therefore, it is presumed that the control product has no effect on improving physical properties even if the same amount of fiber is added, since the portion where this fiber does not exist does not contribute to impact resistance and strength.
従って、繊維を均一にマトリックス中に分散させる方法
として、繊維束ペレット投入方法は優れていることが証
明される。Therefore, the method of introducing fiber bundle pellets is proven to be an excellent method for uniformly dispersing fibers in a matrix.
第1図は結着剤を含浸固化した繊維束ぺ1ノツトの斜視
図、第2図は繊維の外周部を結着剤で被覆した繊維束ペ
レットの斜視図、第3図は樹脂ペレットと繊維束ペレッ
トの混合状態を示す斜視図である。Figure 1 is a perspective view of a fiber bundle pellet impregnated with a binder and solidified, Figure 2 is a perspective view of a fiber bundle pellet with the outer periphery of the fibers coated with a binder, and Figure 3 is a perspective view of a resin pellet and fibers. FIG. 3 is a perspective view showing a mixed state of a bundle of pellets.
Claims (1)
、この繊維束を切断して得られる繊維束ペレットを樹脂
ペレットと混合し、この混合ペレットを成形する際また
はそれに先立って該結着剤を溶解または溶融させて繊維
を分散させることを特徴とする繊維強化樹脂成形物の製
造法。1. Organic fibers or inorganic fibers are bundled, solidified with a binder, and the fiber bundle pellets obtained by cutting the fiber bundles are mixed with resin pellets, and the binding is performed during or prior to molding the mixed pellets. A method for producing a fiber-reinforced resin molded article, which comprises dispersing fibers by dissolving or melting an adhesive.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61132047A JPS62288011A (en) | 1986-06-06 | 1986-06-06 | Manufacture of fiber reinforced resin molding |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61132047A JPS62288011A (en) | 1986-06-06 | 1986-06-06 | Manufacture of fiber reinforced resin molding |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62288011A true JPS62288011A (en) | 1987-12-14 |
Family
ID=15072276
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61132047A Pending JPS62288011A (en) | 1986-06-06 | 1986-06-06 | Manufacture of fiber reinforced resin molding |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62288011A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994029373A1 (en) * | 1993-06-10 | 1994-12-22 | Dsm N.V. | Composition comprising a matrix polymer, fibrous reinforcing material and a binder and a method for injection moulding such a composition |
JP2009072091A (en) * | 2007-09-19 | 2009-04-09 | Toho Kogyo Kk | Breeding block for aquatic animal and plant |
JP2018523718A (en) * | 2015-12-22 | 2018-08-23 | ストラクチャード ポリマーズ, インコーポレイテッドStructured Polymers, Inc. | System and method for producing consumable powder |
US10343303B2 (en) | 2012-03-13 | 2019-07-09 | Structured Polymers, Inc. | Materials for powder-based additive manufacturing processes |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS565714A (en) * | 1979-06-28 | 1981-01-21 | Aisin Seiki Co Ltd | Reinforced thermoplastic resin pellet |
JPS568218A (en) * | 1979-06-29 | 1981-01-28 | Unitika Ltd | Preparation of master pellet for preparing glass-fiber- reinforced thermoplastic polyester resin and molding material |
JPS6018315A (en) * | 1983-07-11 | 1985-01-30 | Toshiba Chem Corp | Conductive molding material |
-
1986
- 1986-06-06 JP JP61132047A patent/JPS62288011A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS565714A (en) * | 1979-06-28 | 1981-01-21 | Aisin Seiki Co Ltd | Reinforced thermoplastic resin pellet |
JPS568218A (en) * | 1979-06-29 | 1981-01-28 | Unitika Ltd | Preparation of master pellet for preparing glass-fiber- reinforced thermoplastic polyester resin and molding material |
JPS6018315A (en) * | 1983-07-11 | 1985-01-30 | Toshiba Chem Corp | Conductive molding material |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994029373A1 (en) * | 1993-06-10 | 1994-12-22 | Dsm N.V. | Composition comprising a matrix polymer, fibrous reinforcing material and a binder and a method for injection moulding such a composition |
BE1007210A3 (en) * | 1993-06-10 | 1995-04-25 | Dsm Nv | Composition comprising a matrix polymer, fibrous reinforcement AND A BINDER, AND METHOD FOR MOULDING OF SUCH COMPOSITION. |
JP2009072091A (en) * | 2007-09-19 | 2009-04-09 | Toho Kogyo Kk | Breeding block for aquatic animal and plant |
US10343303B2 (en) | 2012-03-13 | 2019-07-09 | Structured Polymers, Inc. | Materials for powder-based additive manufacturing processes |
JP2018523718A (en) * | 2015-12-22 | 2018-08-23 | ストラクチャード ポリマーズ, インコーポレイテッドStructured Polymers, Inc. | System and method for producing consumable powder |
JP2019081367A (en) * | 2015-12-22 | 2019-05-30 | ストラクチャード ポリマーズ, インコーポレイテッドStructured Polymers, Inc. | System and method for production of consumable powder |
US10307935B2 (en) | 2015-12-22 | 2019-06-04 | Structured Polymers, Inc. | Systems and methods for producing consumable powder |
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