JPH04125110A - Manufacture of fiber reinforced resin molding material - Google Patents
Manufacture of fiber reinforced resin molding materialInfo
- Publication number
- JPH04125110A JPH04125110A JP2244729A JP24472990A JPH04125110A JP H04125110 A JPH04125110 A JP H04125110A JP 2244729 A JP2244729 A JP 2244729A JP 24472990 A JP24472990 A JP 24472990A JP H04125110 A JPH04125110 A JP H04125110A
- Authority
- JP
- Japan
- Prior art keywords
- section
- kneading
- reinforced fiber
- fiber
- casing
- 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
- 239000000835 fiber Substances 0.000 title claims abstract description 33
- 239000011347 resin Substances 0.000 title claims abstract description 25
- 229920005989 resin Polymers 0.000 title claims abstract description 25
- 239000012778 molding material Substances 0.000 title claims description 17
- 238000004519 manufacturing process Methods 0.000 title claims description 11
- 238000004898 kneading Methods 0.000 claims abstract description 41
- 239000000463 material Substances 0.000 claims abstract description 37
- 239000012783 reinforcing fiber Substances 0.000 claims description 18
- 239000011521 glass Substances 0.000 abstract description 9
- 238000005520 cutting process Methods 0.000 abstract description 5
- 239000000945 filler Substances 0.000 abstract description 5
- 239000011256 inorganic filler Substances 0.000 abstract description 5
- 229910003475 inorganic filler Inorganic materials 0.000 abstract description 5
- 229920001187 thermosetting polymer Polymers 0.000 abstract description 5
- 238000001125 extrusion Methods 0.000 abstract description 2
- 238000011144 upstream manufacturing Methods 0.000 abstract description 2
- 239000004412 Bulk moulding compound Substances 0.000 description 5
- 239000003365 glass fiber Substances 0.000 description 5
- 229920000642 polymer Polymers 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 230000037048 polymerization activity Effects 0.000 description 3
- 238000010526 radical polymerization reaction Methods 0.000 description 3
- 150000003254 radicals Chemical class 0.000 description 3
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 238000007872 degassing Methods 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 239000007870 radical polymerization initiator Substances 0.000 description 2
- 230000003014 reinforcing effect Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- GAWIXWVDTYZWAW-UHFFFAOYSA-N C[CH]O Chemical group C[CH]O GAWIXWVDTYZWAW-UHFFFAOYSA-N 0.000 description 1
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- 125000005396 acrylic acid ester group Chemical group 0.000 description 1
- XYLMUPLGERFSHI-UHFFFAOYSA-N alpha-Methylstyrene Chemical compound CC(=C)C1=CC=CC=C1 XYLMUPLGERFSHI-UHFFFAOYSA-N 0.000 description 1
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 1
- 239000004760 aramid Substances 0.000 description 1
- 229920006231 aramid fiber Polymers 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 229910052570 clay Inorganic materials 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- -1 etc. Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 239000006082 mold release agent Substances 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 229920000193 polymethacrylate Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- HJWLCRVIBGQPNF-UHFFFAOYSA-N prop-2-enylbenzene Chemical compound C=CCC1=CC=CC=C1 HJWLCRVIBGQPNF-UHFFFAOYSA-N 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000002562 thickening agent Substances 0.000 description 1
- 229920006305 unsaturated polyester Polymers 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/76—Venting, drying means; Degassing means
- B29C48/765—Venting, drying means; Degassing means in the extruder apparatus
- B29C48/766—Venting, drying means; Degassing means in the extruder apparatus in screw extruders
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/285—Feeding the extrusion material to the extruder
- B29C48/297—Feeding the extrusion material to the extruder at several locations, e.g. using several hoppers or using a separate additive feeding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/505—Screws
- B29C48/55—Screws having reverse-feeding elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/505—Screws
- B29C48/57—Screws provided with kneading disc-like elements, e.g. with oval-shaped elements
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- 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]
本発明は強化繊維を均一に分散した繊維強化樹脂成形材
料の製造方法に関し、詳細には強化繊維の切断装置を特
別に設ける必要がなく、従って強化繊維が外気中に飛散
するのを防止することのできる繊維強化樹脂成形材料の
製造方法に関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for manufacturing a fiber-reinforced resin molding material in which reinforcing fibers are uniformly dispersed. Therefore, the present invention relates to a method for producing a fiber-reinforced resin molding material that can prevent reinforcing fibers from scattering into the outside air.
[従来の技術]
8j脂材粗に強化繊維(必要により更に無機質充填剤)
を分散した、BMC(バルク・モールディング・コンパ
ウンド)に代表される繊維強化樹脂成形材料を製造する
に当たっては、例えば樹脂材料と無機質充填剤の混合物
中へ、1/4〜1インチ程度の長さに切断した短繊維状
の強化I#i維を混合し、例えば双腕式ニーダ−によっ
て混練して前記強化繊維を均一に分散させることか行わ
れている。以上は、ハツチ弐BMCの製造方法であるが
、連続混練方性を用いる場合は、スクリュー式混練装置
の中に、上記鼎材料を定量的に供給し、かつ混練するこ
とがある。[Prior art] 8j Greasy material coarsely reinforced fiber (additionally inorganic filler if necessary)
When manufacturing fiber-reinforced resin molding materials, such as BMC (bulk molding compound), in which the resin material is dispersed, it is necessary to disperse The reinforcing I#i fibers in the form of cut short fibers are mixed and kneaded using, for example, a double-arm kneader to uniformly disperse the reinforcing fibers. The above is a method for producing Hatch-2 BMC, but when continuous kneading is used, the above-mentioned material may be quantitatively fed into a screw kneading device and kneaded.
上記強化繊維としてはガラス繊維を使うことか多く、ガ
ラス繊維メーカーから搬入されたガラスロービングをチ
ョッパ装置によって任意長さの短繊維に切断した後、ガ
ラス短繊維フィーダを通して上記混練装置内へ装入する
のが一般的であった。Glass fibers are often used as the reinforcing fibers, and after cutting glass roving brought in from a glass fiber manufacturer into short fibers of arbitrary length using a chopper device, they are charged into the kneading device through a short glass fiber feeder. was common.
ところがガラスロービングを切断する為の専用のチョッ
パ装着を設ける従来方式では設備コスト及び製造コスl
〜が増大し、且つさらに重要な問題として前記チョッパ
装置やガラス短繊維フィーダから短繊維が空気中に飛散
し、工場内の作業環境を悪化させるという不具合があフ
た。However, the conventional method of installing a dedicated chopper for cutting glass rovings increases equipment costs and manufacturing costs.
. . . increased, and more importantly, short fibers were scattered into the air from the chopper device and short glass fiber feeder, which worsened the working environment in the factory.
[発明が解決しようとする課題]
そこで本発明者らは、チョッパ装置を併設する必要がな
く、従って短繊維が外気中に飛散することがなく、しか
も強化繊維が期待通りの強化性能を発揮することのでき
る適正長さで樹脂材料中に分散された、繊維強化樹脂成
形材料の製造方法を提供することを目的として研究を重
ね、本発明を完成した。[Problems to be Solved by the Invention] Therefore, the present inventors have discovered that there is no need to install a chopper device, the short fibers are not scattered into the outside air, and the reinforcing fibers exhibit the expected reinforcing performance. The present invention was completed after repeated research aimed at providing a method for manufacturing a fiber-reinforced resin molding material that is dispersed in a resin material in an appropriate length.
[課題を解決するための手段]
上記目的を達成し得た本発明は、多軸スクリュー混練装
置によって樹脂材料を混練しつつ、該混練装置へ強化繊
維を長繊維状態で供給し、該強化繊維を前記混練装置内
で切断し、樹脂材料中に短繊維状の強化繊維として分散
させることを要旨とするものである。[Means for Solving the Problems] The present invention, which has achieved the above object, has a multi-screw kneading device that kneads a resin material and supplies reinforcing fibers in the form of long fibers to the kneading device. The gist is to cut the fibers in the kneading device and disperse them in the resin material as reinforcing fibers in the form of short fibers.
[作用]
本発明においては強化繊維を長繊維のまま混練装置内へ
装入する方法であるのて、チョッパ装置やカラス短繊維
フィーダが不要となり、また短繊維状態に切断されたも
のが空気中に飛散することは全くなくなった。また上記
長繊維は多軸スクリュー式混練装置において強く混練さ
れることにより、1mII′1程度から数+mmに至る
各穂長さの短繊維に切断・分散されることになり、補強
効果については従来方法に十分比肩し得るものである。[Function] In the present invention, since the reinforcing fibers are charged into the kneading device as long fibers, there is no need for a chopper device or a glass short fiber feeder, and the fibers cut into short fibers are There is no longer any scattering. In addition, the above-mentioned long fibers are strongly kneaded in a multi-screw kneading device, so that they are cut and dispersed into short fibers with each panicle length ranging from about 1 mII'1 to several + mm. This method is fully comparable to that of the previous method.
なお上記多軸スクリュー式混練装置においては、混練用
スクリューの下流側に逆流用スクリューを併設したもの
を使用することが好ましく、これによって長繊維の切断
をより確実になし得ると共に、樹脂材料への分散を均一
に行なうことかできる様になる。In the multi-screw kneading device mentioned above, it is preferable to use one that is equipped with a backflow screw on the downstream side of the kneading screw.This allows for more reliable cutting of the long fibers and also reduces the amount of damage to the resin material. This enables uniform dispersion.
[実施例]
本発明に使用される混練装置構造の 施例第1図は2軸
スクリユ一式混練装置の縦断面図、第2図は第1図のI
I −II線断面矢視図である。該混練装置1はケーシ
ング11と該ケーシング11内に互いに歯合して配設さ
れる回転スクリュー軸15a、15bを主要構成部材と
する。[Example] Example of the structure of the kneading device used in the present invention. FIG. 1 is a vertical cross-sectional view of a kneading device with two screws, and FIG.
It is a sectional view taken along the line I-II. The kneading device 1 has a casing 11 and rotating screw shafts 15a and 15b arranged in mesh with each other as main components.
該ケーシング11には樹脂材料供給部13a、充填材供
給部13b及び強化i#維供給部13cが形成され、図
示しない定量供給装置やホッパー等を介して熱硬化性樹
脂材料、無機質充填材及び強化繊維(以下単に両材料と
いうこともある)がケーシング11内へ定量的に装入さ
れる。上記強化繊維供給部13cにおいては巻回された
ガラスロービングFを巻きほどきながらケーシング11
内へ連続的に定量供給する。このときガラスロービング
Fは樹脂材料の移送流にのって引きずり込まれる様にケ
ーシング11内へ送給される。従って特別な供給手段を
必要としない。もつともガラスロービングFをケーシン
グ11内へ積極的に挿入するために、ローラ式フィーダ
等の供給手段を別に用いることを排除するものではない
。A resin material supply section 13a, a filler supply section 13b, and a reinforced i# fiber supply section 13c are formed in the casing 11, and thermosetting resin material, inorganic filler, and reinforcement are supplied via a quantitative supply device, a hopper, etc. (not shown). Fibers (hereinafter also simply referred to as both materials) are quantitatively charged into the casing 11. In the reinforcing fiber supply section 13c, the casing 11 is unwound while the wound glass roving F is unwound.
Continuously supply a fixed amount to the inside. At this time, the glass roving F is fed into the casing 11 so as to be dragged along with the transport flow of the resin material. Therefore, no special supply means are required. Of course, in order to actively insert the glass roving F into the casing 11, the use of a separate supply means such as a roller feeder is not excluded.
また前記ケーシング11の材料搬送方向下流側には脱気
口18及び成形材料吐出口14が形成され、該脱気口1
8は真空ポンプ19に接続され、一方前記吐出口14の
下流側には、必要により成形材料の形状を調整する保形
装置2が設けられる。さらにケーシング11には水冷チ
ャンバ12が形成され、水等の冷却媒体が導入され、熱
硬化性樹脂の変質を防止する。Further, a deaeration port 18 and a molding material discharge port 14 are formed on the downstream side of the casing 11 in the material conveyance direction.
8 is connected to a vacuum pump 19, and on the downstream side of the discharge port 14, a shape retaining device 2 is provided to adjust the shape of the molding material if necessary. Furthermore, a water cooling chamber 12 is formed in the casing 11, into which a cooling medium such as water is introduced to prevent deterioration of the thermosetting resin.
他方平行に歯合する様に配設されたスクリュー軸15a
、15bには搬送羽根16A、混練羽根16B及び逆流
羽根16Cが形成される。該搬送羽根16Aはスクリュ
ー軸の回転によって芸人材料又は成形材料を吐出口14
の配設位置方向へ向けて移動させるらせん状の羽根であ
る(第3図参照)。また混練羽根16Bは第4図に示す
様な楕円形又は多角形状の板状のものであり、隣接して
歯合される混練羽根16B、16B同士によって材料を
押し潰す様に強く混練する。さらに逆流羽根16Cは第
5図に示す様に、前記搬送羽根16Aとは逆方向のらせ
ん状羽根であり、成形材料等を搬送羽根16Aの搬送と
は逆方向、すなわち押し戻す方向に搬送する様な作用を
発揮し、このことによって混練の効果が非常に大きなも
のとなる。The other screw shaft 15a is disposed so as to mesh with the other in parallel.
, 15b are formed with conveying blades 16A, kneading blades 16B, and backflow blades 16C. The conveying blade 16A transfers the entertainer material or molding material to the discharge port 14 by rotation of the screw shaft.
It is a spiral blade that is moved in the direction of the installation position (see Fig. 3). Further, the kneading blades 16B are in the form of an elliptical or polygonal plate as shown in FIG. 4, and the kneading blades 16B, 16B that are meshed with each other strongly knead the material so as to crush the material. Furthermore, as shown in FIG. 5, the backflow blade 16C is a spiral blade that runs in the opposite direction to the conveyance blade 16A, and conveys the molding material, etc. in the opposite direction to the conveyance of the conveyance blade 16A, that is, in the direction of pushing it back. This results in a very large kneading effect.
第1図の例においては左側から順に搬送羽根i6A、混
練羽根16B、逆流羽根16C及び搬送羽根16A、混
練羽根16B、逆流羽根16C並びに搬送羽根16Aが
配列され、各羽根の配設位置に対応して搬送部T1、充
填材混練部M1、逆流部R8及び搬送部T2、強化繊維
混練部M2、逆流部R2並びに搬送部T、が構成される
ことになる。上記搬送部、混練部及び逆流部は任意の順
に、或は任意の省略を行なったものであっても良い。In the example of FIG. 1, the conveying blade i6A, the kneading blade 16B, the backflow blade 16C, the conveyance blade 16A, the kneading blade 16B, the backflow blade 16C, and the conveyance blade 16A are arranged in order from the left side, and the arrangement position of each blade is The transport section T1, the filler kneading section M1, the backflow section R8 and the transport section T2, the reinforcing fiber kneading section M2, the backflow section R2 and the transport section T are constructed. The above-mentioned conveyance section, kneading section, and backflow section may be arranged in any order, or may be omitted in any order.
なお上記回転スクリュー軸15a、15bにおける各羽
根16A〜16Cの形状は第3〜5図にしめしたのもの
に限定されず、希望する混練度に応じて山ピッチ、山高
さ及び山幅等を任意に変更したものであっても良い。ま
た各スクリュー軸15a、15bのらせん方向は第6図
(^)に示す同方向、又は第6図(B)に示す異方向の
いずれであっても良く、スクリュー軸の回転方向(同方
向又は異方向)に応じて選択すれば良い。Note that the shapes of the blades 16A to 16C on the rotating screw shafts 15a and 15b are not limited to those shown in FIGS. 3 to 5, and the pitch, height, width, etc. of the blades can be changed as desired depending on the desired degree of kneading. It may be changed to . The helical direction of each screw shaft 15a, 15b may be the same direction as shown in FIG. 6(^) or the different direction as shown in FIG. 6(B). (different direction).
本発明に使用する材料の実施例
熱硬化性樹脂としては例えばラジカル重合活性を有する
ポリマーとラジカル重合性車量体及びラジカル重合開始
剤の混合物を用いることができる。該ラジカル重合活性
を有するポリマーとしては不飽和ポリエステル、エポキ
シ変性ポリ(メタ)アクリレート等が非限定に例示され
る。またラジカル重合性車量体としては限定されないが
、スチレン、ビニルトルエン、α−メチルスチレン等の
芳香族ビニル化合物やメチル(メタ)アクリレート、2
−ヒドロキシエチル(メタ)アクリレート等の(メタ)
アクリル酸エステル等が推奨される。これらの混合割合
はラジカル重合活性を有するポリマー50〜90fI量
%に対し、ラジカル重合性単量体50〜10重量%、及
び微量のラジカル重合開始剤を含んだものとすることが
好ましく、必要により増結剤、着色剤、離型剤等を添加
する。ただし本発明に通用される樹脂材料の種類につい
ては、−切制限されるものではない。Examples of Materials Used in the Invention As the thermosetting resin, for example, a mixture of a polymer having radical polymerization activity, a radical polymerizable polymer, and a radical polymerization initiator can be used. Examples of the polymer having radical polymerization activity include, but are not limited to, unsaturated polyesters, epoxy-modified poly(meth)acrylates, and the like. The radical polymerizable polymers include, but are not limited to, aromatic vinyl compounds such as styrene, vinyltoluene, α-methylstyrene, methyl (meth)acrylate,
- (meth) such as hydroxyethyl (meth)acrylate
Acrylic acid ester etc. are recommended. The mixing ratio of these is preferably such that 50 to 90 fI amount % of the polymer having radical polymerization activity, 50 to 10 weight % of the radical polymerizable monomer, and a trace amount of the radical polymerization initiator are included. Add thickening agent, coloring agent, mold release agent, etc. However, there is no limit to the type of resin material that can be used in the present invention.
一方無機質充填剤としては炭酸カルシウム、クレー、水
酸化アルミニウム、ガラス、シリカ等の粉末又はこれら
の混合物が例示される。他方強化繊維はガラス繊維、カ
ーボン繊維、アラミド繊維等が非限定的に例示され、繊
維束の本数は成形材料の製造速度に応じて任意に選定さ
れる。尚これら補助材料の種類についても一切制限され
ない。On the other hand, examples of inorganic fillers include powders of calcium carbonate, clay, aluminum hydroxide, glass, silica, etc., or mixtures thereof. On the other hand, non-limiting examples of reinforcing fibers include glass fibers, carbon fibers, aramid fibers, etc., and the number of fiber bundles is arbitrarily selected depending on the manufacturing speed of the molding material. Note that there are no restrictions on the types of these auxiliary materials.
成形材料製゛置方法の実施例
第1図に示す混練機1を用いたバルクモールディングコ
ンパウンド(以下BMCという)の製造例を以下に説明
する。上記の熱硬化性樹脂及び無機質充填材を各供給口
13a、13bを介して、一定の比率で連続的にケーシ
ング11内に定量装入する。搬送部T、において両材料
を混合しつつ充填材混練部M1へ送給する。次いで両材
料は逆流部R1における押し戻し作用を受けつつ、該充
填材混練部M1において強い混練が行なわれる。そして
搬送部T1における上流側からの押出圧力によって混練
物は搬送部T2へ送り込まれる。さらに該搬送部T2に
設けられた強化繊維供給部13cより強化繊維が成形材
料1000kg当たり20〜300kgの割合でケーシ
ング11内へ連続的に装入される。これらの材料は強化
繊維混練部M、において前述と同様に逆流部R2の作用
を受けて強く混練されると共に、ガラスロービングFは
ケーシング11内で各種寸法に切断される。そして成形
材1として搬送部T3を若干の調整を受けつつ吐出口1
4方向へ移動される。なお搬送部T3における脱気01
8を設けた脱気部Sにおいて、上記混練物を減圧雰囲気
に晒し、混練物中に混在している空気を抜気し、気泡の
少ない成形材料とすることが推奨される。そして吐出口
14より連続的に吐出される成形材料を保形装置2を通
して塊状又はシート状に加工し成形用樹脂材料として回
収する。EXAMPLE OF MOLDING MATERIAL PRODUCTION METHOD An example of manufacturing a bulk molding compound (hereinafter referred to as BMC) using the kneader 1 shown in FIG. 1 will be described below. The above thermosetting resin and inorganic filler are continuously and quantitatively charged into the casing 11 at a constant ratio through the respective supply ports 13a and 13b. In the conveyance section T, both materials are mixed and fed to the filler kneading section M1. Next, both materials are strongly kneaded in the filler kneading section M1 while being pushed back in the backflow section R1. The kneaded material is then sent to the transport section T2 by extrusion pressure from the upstream side of the transport section T1. Furthermore, reinforcing fibers are continuously charged into the casing 11 at a rate of 20 to 300 kg per 1000 kg of molding material from the reinforcing fiber supply section 13c provided in the conveying section T2. These materials are strongly kneaded in the reinforcing fiber kneading section M under the action of the backflow section R2 in the same manner as described above, and the glass roving F is cut into various sizes within the casing 11. Then, as the molded material 1, the conveying section T3 is adjusted slightly and the discharge port 1 is
Moved in 4 directions. In addition, degassing 01 in the transport section T3
It is recommended that the kneaded material be exposed to a reduced pressure atmosphere in the degassing section S provided with the molding material No. 8 to evacuate the air mixed in the kneaded material to obtain a molding material with fewer bubbles. The molding material continuously discharged from the discharge port 14 is processed into a lump or sheet shape through the shape retaining device 2 and recovered as a molding resin material.
[発明の効果コ
本発明は以上の様に構成されているので、混練装置全体
を小型に形成できると共に、短繊維の空気中への飛散を
完全に防止し環境の悪化を防げる様になった。さらに成
形材料中には各穂長さの強化繊維を均一に分散で籾るこ
ととなり、安定な強度を持つ成形用樹脂材料を製造でき
る様になった。[Effects of the Invention] Since the present invention is constructed as described above, the entire kneading device can be made compact, and the scattering of short fibers into the air can be completely prevented, thereby preventing deterioration of the environment. . Furthermore, reinforcing fibers of each ear length are uniformly dispersed in the molding material, making it possible to produce a molding resin material with stable strength.
第1図は本発明に使用する混練機の実施を示す側断面図
、第2図は第1図のII −II線断面矢視図、第3図
、第4図及び第5図は混練羽根の形状例を示す説明図、
第6図(A) 、 CB)は回転スクリュー軸の混練羽
根の組合せ例を示す平面説明図である。
1・・・混練装置 2・・・保形装置11・・・
ケーシング
15a、15b・・・回転スクリュー軸】8・・・脱気
口 19・・・真空ポンプ出願人 日本触媒
化学工業株式会社Fig. 1 is a side sectional view showing the implementation of the kneading machine used in the present invention, Fig. 2 is a sectional view taken along the line II-II in Fig. 1, and Figs. 3, 4, and 5 are kneading blades. An explanatory diagram showing an example of the shape of
FIGS. 6(A) and 6(CB) are explanatory plan views showing examples of combinations of kneading blades on the rotating screw shaft. 1...Kneading device 2...Shape retaining device 11...
Casing 15a, 15b... Rotating screw shaft] 8... Deaeration port 19... Vacuum pump applicant Nippon Shokubai Chemical Co., Ltd.
Claims (1)
、該混練装置へ強化繊維を長繊維状態で供給し、該強化
繊維を前記混練装置内で切断し、樹脂材料中に短繊維状
の強化繊維として分散させることを特徴とする繊維強化
樹脂成形材料の製造方法。While kneading the resin material with a multi-screw kneading device, reinforcing fibers are supplied in the form of long fibers to the kneading device, and the reinforcing fibers are cut in the kneading device to form reinforcing fibers in the form of short fibers in the resin material. A method for producing a fiber-reinforced resin molding material, which comprises dispersing the material.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2244729A JP2825956B2 (en) | 1990-09-14 | 1990-09-14 | Method for producing fiber-reinforced resin molding material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2244729A JP2825956B2 (en) | 1990-09-14 | 1990-09-14 | Method for producing fiber-reinforced resin molding material |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04125110A true JPH04125110A (en) | 1992-04-24 |
JP2825956B2 JP2825956B2 (en) | 1998-11-18 |
Family
ID=17123029
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2244729A Expired - Lifetime JP2825956B2 (en) | 1990-09-14 | 1990-09-14 | Method for producing fiber-reinforced resin molding material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2825956B2 (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5679456A (en) * | 1993-07-21 | 1997-10-21 | Toray Industries, Inc. | Fiber reinforced thermoplastic resin structure, process for production of same, and extruder for production of same |
US5851065A (en) * | 1993-10-29 | 1998-12-22 | Toyota Jidosha Kabushiki Kaisha | Apparatus for recycling resin scrap |
US7048431B2 (en) * | 2001-10-23 | 2006-05-23 | Krauss-Maffei Kunststoffechnik Gmbh | Plastic processing machine for producing fiber-containing thermoplastics |
JP2013208866A (en) * | 2012-03-30 | 2013-10-10 | Toshiba Mach Co Ltd | Plasticizing apparatus, injection apparatus, injection molding apparatus, extruder, and method for manufacturing molding |
JP2013208779A (en) * | 2012-03-30 | 2013-10-10 | Toshiba Mach Co Ltd | Screw, plasticizing apparatus, injection apparatus, injection molding apparatus, extruder, and method for manufacturing molding |
JP2018079597A (en) * | 2016-11-15 | 2018-05-24 | トヨタ自動車株式会社 | Method for producing fiber-reinforced resin material |
-
1990
- 1990-09-14 JP JP2244729A patent/JP2825956B2/en not_active Expired - Lifetime
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5679456A (en) * | 1993-07-21 | 1997-10-21 | Toray Industries, Inc. | Fiber reinforced thermoplastic resin structure, process for production of same, and extruder for production of same |
US5824410A (en) * | 1993-07-21 | 1998-10-20 | Toray Industries, Inc. | Fiber reinforced thermoplastic resin structure, process for production of same, and extruder for production of same |
US6060010A (en) * | 1993-07-21 | 2000-05-09 | Toray Industries, Inc. | Fiber reinforced thermoplastic resin structure, process for production of same, and extruder for production of the same |
US6428728B1 (en) | 1993-07-21 | 2002-08-06 | Toray Industries, Inc. | Fiber reinforced thermoplastic resin structure, process for production of same, and extruder for production of same |
US5851065A (en) * | 1993-10-29 | 1998-12-22 | Toyota Jidosha Kabushiki Kaisha | Apparatus for recycling resin scrap |
US7048431B2 (en) * | 2001-10-23 | 2006-05-23 | Krauss-Maffei Kunststoffechnik Gmbh | Plastic processing machine for producing fiber-containing thermoplastics |
JP2013208866A (en) * | 2012-03-30 | 2013-10-10 | Toshiba Mach Co Ltd | Plasticizing apparatus, injection apparatus, injection molding apparatus, extruder, and method for manufacturing molding |
JP2013208779A (en) * | 2012-03-30 | 2013-10-10 | Toshiba Mach Co Ltd | Screw, plasticizing apparatus, injection apparatus, injection molding apparatus, extruder, and method for manufacturing molding |
JP2018079597A (en) * | 2016-11-15 | 2018-05-24 | トヨタ自動車株式会社 | Method for producing fiber-reinforced resin material |
Also Published As
Publication number | Publication date |
---|---|
JP2825956B2 (en) | 1998-11-18 |
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