JPH06293023A - Manufacture of long-fiber reinforced thermoplastic resin composition - Google Patents
Manufacture of long-fiber reinforced thermoplastic resin compositionInfo
- Publication number
- JPH06293023A JPH06293023A JP5106245A JP10624593A JPH06293023A JP H06293023 A JPH06293023 A JP H06293023A JP 5106245 A JP5106245 A JP 5106245A JP 10624593 A JP10624593 A JP 10624593A JP H06293023 A JPH06293023 A JP H06293023A
- Authority
- JP
- Japan
- Prior art keywords
- thermoplastic resin
- fiber bundle
- contact
- discharged
- molten thermoplastic
- 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
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
-
- 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
- B29B15/00—Pretreatment of the material to be shaped, not covered by groups B29B7/00 - B29B13/00
- B29B15/08—Pretreatment of the material to be shaped, not covered by groups B29B7/00 - B29B13/00 of reinforcements or fillers
- B29B15/10—Coating or impregnating independently of the moulding or shaping step
- B29B15/12—Coating or impregnating independently of the moulding or shaping step of reinforcements of indefinite length
- B29B15/122—Coating or impregnating independently of the moulding or shaping step of reinforcements of indefinite length with a matrix in liquid form, e.g. as melt, solution or latex
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)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、長繊維強化熱可塑性樹
脂組成物の製造方法に関し、特にクロスヘッドダイ(含
浸ダイ)を用いて繊維束に溶融樹脂を含浸させるに際
し、クロスヘッドダイ内の蛇行した通路による屈曲部金
属と繊維束との接触による繊維束の損傷を防止すると共
に、溶融樹脂の含浸状態を良好にした長繊維強化熱可塑
性樹脂組成物の製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a long fiber reinforced thermoplastic resin composition, and more particularly, when a fiber bundle is impregnated with a molten resin by using a crosshead die (impregnation die), The present invention relates to a method for producing a long fiber-reinforced thermoplastic resin composition which prevents damage to a fiber bundle due to contact between a bent portion metal and a fiber bundle due to a meandering passage and improves the impregnation state of a molten resin.
【0002】[0002]
【従来の技術】平行に整列された繊維束とこれに含浸さ
れた熱可塑性樹脂から成る長繊維強化熱可塑性樹脂組成
物は、主に長軸ペレット状に製造され、機械的強度を要
求される種々の成形品に用いられている。前記組成物と
しては、繊維、代表的には連続したガラス繊維の繊維束
をクロスヘッドダイ内の通路に通し、ダイ内においてこ
れに溶融熱可塑性樹脂を含浸させ、その後賦形ダイによ
り所望の形状、例えば前記のようなペレット状に賦形し
て製造される。このような技術は例えば米国特許4,4
39,387号や特開平3−272830号公報などに
開示されている。2. Description of the Related Art A long-fiber-reinforced thermoplastic resin composition comprising a bundle of fibers arranged in parallel and a thermoplastic resin impregnated in the bundle is mainly produced in the form of long-axis pellets and is required to have mechanical strength. Used in various molded products. As the composition, a fiber, typically a fiber bundle of continuous glass fibers, is passed through a passage in a crosshead die and impregnated with a molten thermoplastic resin in the die, and then a desired shape is obtained by a shaping die. For example, it is manufactured by shaping into pellets as described above. Such a technique is disclosed, for example, in US Pat.
No. 39,387 and JP-A-3-272830.
【0003】[0003]
【本発明の解決しようとする課題】しかしながら、前記
文献に開示されている製造方法においては、クロスヘッ
ドダイ内の屈曲部と繊維束との最初の接触が起きる際、
繊維束の前記接触面に溶融樹脂を含浸させて保護し、毛
羽立ち等の発生を防止するという考慮は全く払われてい
なかった。またクロスヘッドダイ内における溶融樹脂の
吐出も主に一方向からのものに限られていたので、樹脂
の含浸が繊維束の他表面にまで達しにくく、そのため繊
維束の一方の面側にのみ樹脂が偏って含浸する傾向があ
った。かかる屈曲部と繊維束との接触や含浸樹脂の偏り
による未含浸繊維部分の残存により、製造工程中の繊維
(繊維束)の破断、毛羽立ちを招き、最終的には製造装
置内における糸切れを引き起こしたり、製品であるペレ
ット等に毛玉を生じさせる原因となり、またかかる製品
を原料とした成形品に品質上の欠陥を生じさせる原因と
なっていた。However, in the manufacturing method disclosed in the above document, when the first contact between the bent portion in the crosshead die and the fiber bundle occurs,
No consideration has been given to preventing the occurrence of fuzz and the like by impregnating the contact surface of the fiber bundle with a molten resin to protect it. In addition, since the molten resin was discharged mainly from one direction in the crosshead die, it was difficult for resin impregnation to reach the other surface of the fiber bundle. Had a tendency to impregnate unevenly. Due to the contact between the bent portion and the fiber bundle and the unimpregnated fiber portion remaining due to the unevenness of the impregnated resin, the fiber (fiber bundle) is broken during the manufacturing process, and fluffing is caused, and finally the yarn breaks in the manufacturing apparatus. This is a cause of causing pills or pills on the product pellets, and also causing quality defects in molded products made from such products.
【0004】[0004]
【課題を解決するための手段】本発明者等は、連続した
繊維束をクロスヘッドダイに通過させながら溶融熱可塑
性樹脂を含浸させる長繊維強化熱可塑性樹脂組成物の製
造において、上記課題を解決するため鋭意研究した結
果、溶融樹脂の吐出位置等を改善することが極めて有効
であることを見出し、本発明に到達した次第である。Means for Solving the Problems The present inventors have solved the above problems in the production of a long fiber reinforced thermoplastic resin composition in which a molten thermoplastic resin is impregnated while passing a continuous fiber bundle through a crosshead die. Therefore, as a result of earnest studies, it was found that it is extremely effective to improve the discharge position of the molten resin, and the present invention has been reached.
【0005】すなわち本発明によれば、クロスヘッドダ
イ内の上下方向に蛇行した複数の屈曲部を有する通路
に、連続した繊維束を連続的に引き抜きながら通過させ
ると共に、溶融熱可塑性樹脂を通路内に吐出させ、通過
中の前記繊維束に溶融熱可塑性樹脂を含浸させる長繊維
強化熱可塑性樹脂組成物の製造方法において、前記繊維
束と前記屈曲部頂点若しくは頂点近傍との最初の接触が
起きる位置またはその上流位置で、かつ前記通路の上部
内面または下部内面のうち前記最初の接触が起きる側か
ら溶融熱可塑性樹脂を吐出させ、前記繊維束の接触面に
前記吐出させた溶融熱可塑性樹脂を供給することを特徴
とする長繊維強化熱可塑性樹脂組成物の製造方法が提供
される。That is, according to the present invention, a continuous fiber bundle is continuously drawn while passing through a passage having a plurality of bent portions meandering in the vertical direction in the crosshead die, and a molten thermoplastic resin is passed through the passage. In the method for producing a long fiber reinforced thermoplastic resin composition in which a molten thermoplastic resin is impregnated into the fiber bundle that is being discharged, the position where the first contact between the fiber bundle and the bent portion apex or the vicinity of the apex occurs. Alternatively, the molten thermoplastic resin is discharged at the upstream position and from the side where the first contact occurs in the upper inner surface or the lower inner surface of the passage, and the discharged molten thermoplastic resin is supplied to the contact surface of the fiber bundle. A method for producing a long fiber reinforced thermoplastic resin composition is provided.
【0006】この場合において、前記熱可塑性樹脂の吐
出(第1吐出)に加えて、前記第1吐出口に対向する内
面側から溶融熱可塑性樹脂を吐出(第2吐出)させるこ
とが好ましい。この第2吐出位置に関しては、溶融熱可
塑性樹脂の繊維束への含浸性を向上させる観点から、繊
維束と最初の接触が起きる位置よりも下流で、かつ繊維
束と通路屈曲部との2度目の接触が起きる位置またはそ
の上流位置であることが好ましい。さらに溶融熱可塑性
樹脂の吐出方向と繊維束の進行方向とのなす角度(θ)
は、0゜<θ≦90゜であることが好ましい。In this case, in addition to the discharge of the thermoplastic resin (first discharge), it is preferable that the molten thermoplastic resin is discharged (second discharge) from the inner surface side facing the first discharge port. Regarding the second discharge position, from the viewpoint of improving the impregnation property of the molten thermoplastic resin into the fiber bundle, the second discharge position is located downstream of the position where the first contact with the fiber bundle occurs and the second time between the fiber bundle and the bent portion of the passage. Is preferably a position where the contact occurs or an upstream position thereof. Furthermore, the angle (θ) formed by the direction in which the molten thermoplastic resin is discharged and the direction in which the fiber bundle advances
Is preferably 0 ° <θ ≦ 90 °.
【0007】以下、図面を参照して本発明をさらに詳細
に説明するが、当然ながら本発明は、ここに例示した装
置および方法のみに限定されるものではない。Hereinafter, the present invention will be described in more detail with reference to the drawings, but naturally the present invention is not limited to only the devices and methods illustrated herein.
【0008】図1に示すように、ロービング2から連続
した繊維束4が引き出される。この繊維束4としては、
例えばガラス繊維、炭素繊維、金属繊維、芳香族ポリア
ミド繊維等の高融点繊維等またはこれらの組み合わせが
使用でき、ロービング、ヤーン等の連続繊維が使用でき
る。引き出された繊維束4は、クロスヘッドダイ6に導
入される前に解繊することが好ましい。これにより繊維
束は通常平らな断面とされる。解繊条件を適当に設定す
ることにより、繊維束の解繊程度を未解繊状態から十分
な解繊状態まで制御することが出来るが、より十分に解
繊させることが好ましい。こうして予め処理された繊維
束4はクロスヘッドダイ6へ導入され、クロスヘッドダ
イ6内の通路14を通過する間に、溶融熱可塑性樹脂に
より含浸される。溶融熱可塑性樹脂は溶融熱可塑性樹脂
供給路12を経由して供給され、吐出口16(第1吐出
口)および17(第2吐出口)から通路14に吐出され
る。As shown in FIG. 1, a continuous fiber bundle 4 is pulled out from the roving 2. As the fiber bundle 4,
For example, glass fibers, carbon fibers, metal fibers, high melting point fibers such as aromatic polyamide fibers, or the like, or a combination thereof can be used, and continuous fibers such as roving and yarn can be used. The drawn out fiber bundle 4 is preferably defibrated before being introduced into the crosshead die 6. This gives the fiber bundle a generally flat cross section. By appropriately setting the defibration conditions, the defibration degree of the fiber bundle can be controlled from the undefibrated state to a sufficient defibrated state, but it is preferable to defibrate more sufficiently. The fiber bundle 4 thus pretreated is introduced into the crosshead die 6 and impregnated with the molten thermoplastic resin while passing through the passage 14 in the crosshead die 6. The molten thermoplastic resin is supplied through the molten thermoplastic resin supply passage 12 and is discharged from the discharge ports 16 (first discharge port) and 17 (second discharge port) to the passage 14.
【0009】前記クロスヘッドダイ6には、前記のよう
にダイの上下ほぼ中央部に繊維束4の通過する通路14
が形成されている。図1では、クロスヘッドダイ6には
一本の繊維束4のみ示しているが、実際には図中の奥行
き方向に多数の繊維束4が平行して通過し、これらに対
し同時に含浸を行うことができるようになっている。通
路14は、通路入口近傍にて直線状であるが、途中から
上下方向に蛇行している。上下方向の蛇行順序はとくに
制限はない。As described above, the crosshead die 6 has a passage 14 through which the fiber bundles 4 pass in the upper and lower central portions of the die.
Are formed. In FIG. 1, only one fiber bundle 4 is shown in the crosshead die 6, but in reality, a large number of fiber bundles 4 pass in parallel in the depth direction in the figure, and impregnation is performed on them at the same time. Is able to. The passage 14 is linear near the entrance of the passage, but meanders vertically from the middle. The meandering order in the vertical direction is not particularly limited.
【0010】本発明による長繊維強化熱可塑性樹脂組成
物の製造方法は、溶融熱可塑性樹脂を通路内に吐出させ
る位置および吐出させる方向に特徴がある。すなわちク
ロスヘッドダイ内を通過する繊維束は、前記蛇行による
通路の屈曲部頂点若しくは頂点近傍においてダイの金属
と接触するが、屈曲部18の最初の接触が起きる位置2
0またはその上流(クロスヘッドダイの入口方向)位置
で、かつ前記通路の上部内面または下部内面のうち最初
の接触が起きる側(図1の場合は通路の上部内面側)か
ら溶融熱可塑性樹脂を吐出させることが必要である。こ
れにより繊維束4がダイの金属と接触する面(図1の場
合は繊維束の上側面)に前記吐出させた溶融熱可塑性樹
脂が供給されるので、金属との接触時に溶融樹脂が潤滑
作用を発揮し、繊維束の損傷を有効に防止することが出
来る。この場合において、前記吐出位置は最初の接触が
起きる位置20でもよいが、その上流にあることが好ま
しい。このようにして繊維束の損傷、すなわち破断、毛
羽だち、飛散が防止され、繊維束のスムーズな通過と溶
融樹脂の含浸が促進される。The method for producing a long-fiber-reinforced thermoplastic resin composition according to the present invention is characterized by the position and direction in which the molten thermoplastic resin is discharged into the passage. That is, the fiber bundle passing through the crosshead die comes into contact with the metal of the die at or near the apex of the bent portion of the path due to the meandering, but at the position 2 where the first contact of the bent portion 18 occurs.
0 or the upstream thereof (in the direction of the entrance of the crosshead die) and the molten thermoplastic resin from the side of the upper inner surface or the lower inner surface of the passage where the first contact occurs (in the case of FIG. 1, the upper inner surface of the passage). It is necessary to discharge. As a result, the discharged molten thermoplastic resin is supplied to the surface of the fiber bundle 4 in contact with the metal of the die (the upper side surface of the fiber bundle in the case of FIG. 1), so that the molten resin lubricates when contacting the metal. It is possible to effectively prevent damage to the fiber bundle. In this case, the ejection position may be the position 20 at which the first contact occurs, but it is preferably located upstream thereof. In this way, damage to the fiber bundle, that is, breakage, fluffing, and scattering are prevented, and smooth passage of the fiber bundle and impregnation of the molten resin are promoted.
【0011】図1の場合は通路上部内面側で最初の接触
が起きているが、下部内面側で最初の接触が起きるクロ
スヘッドダイを用いる場合は、下部内面側から溶融熱可
塑性樹脂を吐出させることにより、同様に繊維束と金属
との接触面に溶融熱可塑性樹脂を供給することが出来
る。In the case of FIG. 1, the first contact occurs on the inner surface side of the upper part of the passage, but when using a crosshead die in which the first contact occurs on the inner surface side of the lower part, the molten thermoplastic resin is discharged from the inner surface side of the lower part. As a result, the molten thermoplastic resin can be similarly supplied to the contact surface between the fiber bundle and the metal.
【0012】本発明の好ましい態様においては、前記熱
可塑性樹脂の吐出(第1吐出)に加えて、前記第1吐出
口に対向する内面側(図1では下部内面側)から溶融熱
可塑性樹脂を吐出(第2吐出)させる。第2吐出位置は
第1吐出位置よりも下流(引き出しロール側)位置であ
る。更に第2吐出位置は、繊維束と最初の接触が起きる
位置20よりも下流で2度目の接触が起きる位置または
その上流位置であることが、溶融熱可塑性樹脂の繊維束
への含浸性を向上させる観点から、特に好ましい。すな
わち、第2吐出口17が繊維束と通路屈曲部との最初の
接触が起きる位置20またはそれよりも上流位置(第1
吐出口よりもさらに上流位置である場合も含む)にある
場合と比べて、溶融熱可塑性樹脂の含浸性は著しく改善
される。図1においては吐出口17による吐出がこれに
相当し、第1吐出口16および最初の接触が起きる位置
20よりも下流であって、2度目の接触が起きる位置2
2の上流位置にある場合である。これにより繊維束と金
属との2度目の接触においても、繊維束の金属との新た
な接触側面に溶融熱可塑性樹脂が供給され、この接触側
面も溶融熱可塑性樹脂による含浸で保護されることとな
り、また最初の接触が起きた後に、第1吐出口とは反対
側にある第2吐出口から吐出された溶融熱可塑性樹脂が
繊維束を反対側から含浸することとなるので、含浸性が
著しく向上し、含浸樹脂の偏りによる未含浸繊維部分の
残存も防止される。In a preferred embodiment of the present invention, in addition to the discharge of the thermoplastic resin (first discharge), the molten thermoplastic resin is injected from the inner surface side (the lower inner surface side in FIG. 1) facing the first discharge port. Discharge (second discharge). The second discharge position is a position downstream (on the pulling roll side) of the first discharge position. Further, the second discharge position is a position where a second contact occurs downstream of the position 20 where the first contact with the fiber bundle occurs or an upstream position thereof, so that the impregnation property of the molten thermoplastic resin into the fiber bundle is improved. It is particularly preferable from the viewpoint of the above. That is, the second discharge port 17 is at a position 20 at which the first contact between the fiber bundle and the bent portion of the passage occurs or a position upstream of the position 20 (first position).
In comparison with the case where the position is further upstream from the discharge port), the impregnation property of the molten thermoplastic resin is remarkably improved. In FIG. 1, the discharge from the discharge port 17 corresponds to this, which is downstream of the first discharge port 16 and the position 20 at which the first contact occurs, and the position 2 at which the second contact occurs.
This is the case at the upstream position of 2. As a result, even in the second contact between the fiber bundle and the metal, the molten thermoplastic resin is supplied to the new contact side of the fiber bundle with the metal, and this contact side is also protected by the impregnation with the molten thermoplastic resin. Also, after the first contact occurs, the molten thermoplastic resin discharged from the second discharge port on the side opposite to the first discharge port impregnates the fiber bundle from the opposite side, so the impregnation property is remarkably high. It is improved, and the non-impregnated fiber portion is prevented from remaining due to uneven distribution of the impregnated resin.
【0013】吐出口16および17は、通路長手方向の
同じ位置にて対向して設けてもよいが、前記含浸性を向
上させる理由から、前記の位置関係にあることが特に好
ましい。The discharge ports 16 and 17 may be provided to face each other at the same position in the longitudinal direction of the passage, but it is particularly preferable to have the above-mentioned positional relationship for the reason of improving the impregnating property.
【0014】本発明において、吐出口16、17におけ
る繊維束の進行方向と吐出方向(融樹脂吐出路)のなす
角度θは、0<θ≦90°であることが好ましい。角度
θは主には二つの吐出口を設ける位置および吐出方向を
考慮してクロスヘッドダイを製作することにより変える
ことができる。図1の場合は、両吐出口に関してもθが
前記条件を満たしている。角度θは好ましくは70゜以
下である。角度θは実施可能な範囲で小さいほど、溶融
樹脂の吐出圧による繊維束の通過を妨げず、また繊維束
の損傷を防止することが出来るので好ましい。なお、図
1には2つの吐出口16、17を有する場合を示してい
るが、更に多くの吐出口をダイ内に設けてもよい。その
場合は、吐出口が進行方向に沿って上下交互に設けるこ
とが好ましい。また吐出口ごとに異なる熱可塑性樹脂を
吐出してもよい。In the present invention, it is preferable that the angle θ formed between the advancing direction of the fiber bundle at the ejection ports 16 and 17 and the ejection direction (melt resin ejection passage) is 0 <θ ≦ 90 °. The angle θ can be changed mainly by manufacturing the crosshead die in consideration of the positions where the two discharge ports are provided and the discharge direction. In the case of FIG. 1, θ also satisfies the above condition for both ejection ports. The angle θ is preferably 70 ° or less. It is preferable that the angle θ be as small as practicable, because the passage of the fiber bundle due to the discharge pressure of the molten resin is not hindered and the fiber bundle can be prevented from being damaged. Although FIG. 1 shows the case where the two ejection ports 16 and 17 are provided, more ejection ports may be provided in the die. In that case, it is preferable that the discharge ports are provided alternately in the vertical direction along the traveling direction. Also, different thermoplastic resins may be discharged for each discharge port.
【0015】上記吐出口への溶融熱可塑性樹脂の供給
は、図示していない例えばスクリュー式押出機等により
行われる。The molten thermoplastic resin is supplied to the discharge port by, for example, a screw type extruder (not shown).
【0016】こうして溶融熱可塑性樹脂による含浸の完
了した繊維束は、連続的にクロスヘッドダイ6より引き
出しロール8によって引き抜いて排出される。この排出
時には、ダイ排出口に設けられたノズル(図示せず)の
開口径により溶融熱可塑性樹脂の繊維束上の付着量を制
御することができる。The fiber bundle thus impregnated with the molten thermoplastic resin is continuously drawn out from the crosshead die 6 by the drawing roll 8 and discharged. During this discharge, the amount of the molten thermoplastic resin deposited on the fiber bundle can be controlled by the opening diameter of the nozzle (not shown) provided at the die discharge port.
【0017】排出された繊維束は必要に応じてさらに所
定の賦形ダイ(図示せず)に通過され、所定の形状に成
形され、更に必要に応じてペレタイザー10により切断
されてペレット24とされる。The discharged fiber bundle is further passed through a predetermined shaping die (not shown) if necessary, molded into a predetermined shape, and further cut by the pelletizer 10 to be pellets 24 if necessary. It
【0018】繊維束4に含浸される熱可塑性樹脂として
は、例えばポリエチレン、ポリプロピレン等のポリオレ
フィン、ポリエチレンテレフタレートやポリブチレンテ
レフタレート等のポリエステル、ナイロン6、ナイロン
66、ナイロン11、ナイロン12、ナイロン610、
ナイロン612等のポリアミド、ポリアセタール、ポリ
カーボネート、ポリウレタン、ポリフェニレンサルファ
イド、ポリフェニレンオキサイド、ポリスルフォン、ポ
リエーテルケトン、ポリエーテルアミド、ポリエーテル
イミド等のその他の熱可塑性樹脂およびこれらの組み合
わせが使用できる。これらの樹脂の分子量としては、繊
維に含浸した場合、適当な繊維強化効果を発揮するもの
であれば特に制限はない。これらの熱可塑性樹脂には、
樹脂組成物の用途、使用条件に応じて各種の添加剤、例
えば酸化防止剤、帯電防止剤、浸滑剤、可塑剤、離型
剤、難燃剤、難燃焼助剤、結晶化促進剤、着色剤等を配
合することもできる。Examples of the thermoplastic resin with which the fiber bundle 4 is impregnated include polyolefins such as polyethylene and polypropylene, polyesters such as polyethylene terephthalate and polybutylene terephthalate, nylon 6, nylon 66, nylon 11, nylon 12, nylon 610,
Other thermoplastic resins such as polyamides such as nylon 612, polyacetals, polycarbonates, polyurethanes, polyphenylene sulfides, polyphenylene oxides, polysulfones, polyetherketones, polyetheramides, polyetherimides and the like and combinations thereof can be used. The molecular weight of these resins is not particularly limited as long as it exhibits an appropriate fiber reinforcing effect when impregnated into fibers. These thermoplastics include
Various additives such as antioxidants, antistatic agents, lubricants, plasticizers, mold release agents, flame retardants, flame retarding aids, crystallization accelerators, and colorants, depending on the application and use conditions of the resin composition. It is also possible to mix the like.
【0019】[0019]
【実施例】以下実施例により本発明を更に具体的に説明
するが、本発明はこれに限定されるものではない。The present invention will be described in more detail with reference to the following examples, but the present invention is not limited thereto.
【0020】(実施例1〜4および比較例1、2)図2
〜図6に示すような構成のクロスヘッドダイ6を用い、
ガラス繊維から成る繊維束4を引き出しながら溶融ポリ
プロピレンを吐出口30(第1吐出口),32(第2吐
出口)より吐出させて含浸させ、引き出し、長さ12m
mのペレット状組成物を得た。ポリプロピレンとガラス
繊維の組成割合はいずれも表−1に示す割合に調節し
た。(Examples 1 to 4 and Comparative Examples 1 and 2) FIG.
~ Using a crosshead die 6 having a configuration as shown in Fig. 6,
While pulling out the fiber bundle 4 made of glass fiber, molten polypropylene is discharged from the discharge ports 30 (first discharge port) and 32 (second discharge port) to be impregnated, pulled out, and the length is 12 m.
m pelletized composition was obtained. The composition ratios of polypropylene and glass fiber were adjusted to the ratios shown in Table-1.
【0021】運転性の評価としては、16Kg巻きガラ
スロービングを糸切れ無しで最後まで使用できた場合に
要する時間に対し、運転開始から最初の糸切れが起きる
までの時間をパーセントで表した。従って運転性が10
0%とは糸切れ無しを示す。また製品ペレットを1%ア
ルコール水溶液で洗浄し、洗浄液を濾過し、濾紙で捕集
したガラスの重量(ppm)を測定することにより、製
品中の未含浸ガラス量を測定した。以上の評価の結果
を、下記の表−1に示す。As the evaluation of the drivability, the time from the start of the operation to the first yarn breakage was expressed as a percentage with respect to the time required when the 16 Kg wound glass roving could be used to the end without yarn breakage. Therefore, drivability is 10
0% means no yarn breakage. Further, the product pellet was washed with a 1% aqueous alcohol solution, the washing liquid was filtered, and the weight (ppm) of the glass collected by the filter paper was measured to measure the amount of unimpregnated glass in the product. The results of the above evaluations are shown in Table 1 below.
【0022】[0022]
【表1】 [Table 1]
【0023】[0023]
【発明の効果】以上の説明および実施例により明らかな
ように、本発明による長繊維強化熱可塑性樹脂組成物の
製造方法によれば、クロスヘッドダイ内の通路の上下蛇
行による屈曲部の金属と繊維束との直接の接触を防止す
ることが出来る。これにより製造工程中の繊維の損傷、
すなわち破断、毛羽立ち、さらには製品であるペレット
等の毛玉を防止出来るようになった。また繊維束の上下
両面からの溶融熱可塑性樹脂を吐出する態様を採用する
ことにより、とりわけ第2吐出位置を繊維束と通路屈曲
部との最初の接触が起きる位置よりも下流で、かつ2度
目の接触が起きる位置またはその上流位置に設定するこ
とにより、溶融熱可塑性樹脂の繊維束への含浸性が著し
く向上し、未含浸繊維部分の残存を防止でき、前記効果
を一層高めることが出来る。As is apparent from the above description and the examples, according to the method for producing a long fiber reinforced thermoplastic resin composition of the present invention, the metal in the bent portion due to the vertical meandering of the passage in the crosshead die It is possible to prevent direct contact with the fiber bundle. This damages the fibers during the manufacturing process,
That is, it becomes possible to prevent breakage, fluffing, and pills such as product pellets. In addition, by adopting a mode in which the molten thermoplastic resin is discharged from both the upper and lower surfaces of the fiber bundle, the second discharge position is particularly downstream of the position where the first contact between the fiber bundle and the bent portion of the passage occurs, and the second time. By setting at a position where the contact occurs or an upstream position thereof, the impregnating property of the molten thermoplastic resin into the fiber bundle is remarkably improved, the unimpregnated fiber portion can be prevented from remaining, and the above effect can be further enhanced.
図1は、本発明の実施の一例を示す略図である。 図2は、実施例1のクロスヘッドダイを示す略図であ
る。 図3は、実施例2のクロスヘッドダイを示す略図であ
る。 図4は、実施例3のクロスヘッドダイを示す略図であ
る。 図5は、比較例1のクロスヘッドダイを示す略図であ
る。 図6は、比較例2のクロスヘッドダイを示す略図であ
る。 図7は、実施例4のクロスヘッドダイを示す略図であ
る。FIG. 1 is a schematic diagram showing an example of implementation of the present invention. FIG. 2 is a schematic diagram showing the crosshead die of Example 1. FIG. 3 is a schematic diagram showing a crosshead die of Example 2. FIG. 4 is a schematic diagram showing a crosshead die of Example 3. FIG. 5 is a schematic diagram showing a crosshead die of Comparative Example 1. FIG. 6 is a schematic diagram showing a crosshead die of Comparative Example 2. FIG. 7 is a schematic diagram showing a crosshead die of Example 4.
2 ロービング 4 繊維束 6 クロスヘッドダイ 8 引き出しロール 10 ペレタイザー 12 溶融熱可塑性樹脂供給路 14 通路 16 第1吐出口 17 第2吐出口 18 屈曲部 20 最初の接触が起きる位置 22 2度目の接触が起きる位置 24 ペレット 30 第1吐出部 32 第2吐出部 2 Roving 4 Fiber bundle 6 Crosshead die 8 Drawer roll 10 Pelletizer 12 Molten thermoplastic resin supply path 14 Passage 16 First discharge port 17 Second discharge port 18 Bent part 20 First contact occurs 22 Second contact occurs Position 24 Pellet 30 First discharge part 32 Second discharge part
Claims (4)
た複数の屈曲部を有する通路に、連続した繊維束を連続
的に引き抜きながら通過させると共に、溶融熱可塑性樹
脂を通路内に吐出させ、通過中の前記繊維束に溶融熱可
塑性樹脂を含浸させる長繊維強化熱可塑性樹脂組成物の
製造方法において、前記繊維束と前記屈曲部頂点若しく
は頂点近傍との最初の接触が起きる位置またはその上流
位置で、かつ前記通路の上部内面または下部内面のうち
前記最初の接触が起きる側から溶融熱可塑性樹脂を吐出
させ、前記繊維束の接触面に前記吐出させた溶融熱可塑
性樹脂を供給することを特徴とする長繊維強化熱可塑性
樹脂組成物の製造方法。1. A continuous fiber bundle is continuously drawn while passing through a passage having a plurality of bent portions that meander in the vertical direction in a crosshead die, and a molten thermoplastic resin is discharged into the passage and is passed therethrough. In the method for producing a long fiber reinforced thermoplastic resin composition in which the fiber bundle is impregnated with a molten thermoplastic resin, at the position where the first contact between the fiber bundle and the bent portion apex or the vicinity of the apex occurs or an upstream position thereof. And, the molten thermoplastic resin is discharged from the side where the first contact occurs among the upper inner surface or the lower inner surface of the passage, and the discharged molten thermoplastic resin is supplied to the contact surface of the fiber bundle. A method for producing a long fiber reinforced thermoplastic resin composition.
加えて、前記第1吐出口に対向する内面側から溶融熱可
塑性樹脂を吐出(第2吐出)させることを特徴とする請
求項1記載の長繊維強化熱可塑性樹脂組成物の製造方
法。2. The molten thermoplastic resin is discharged (second discharge) from the inner surface side facing the first discharge port, in addition to the discharge (first discharge) of the thermoplastic resin. 1. The method for producing the long fiber reinforced thermoplastic resin composition according to 1.
が起きる位置よりも下流で、かつ2度目の接触が起きる
位置またはその上流位置であることを特徴とする請求項
2記載の長繊維強化熱可塑性樹脂組成物の製造方法。3. The length according to claim 2, wherein the second discharging position is located downstream of the position where the first contact with the fiber bundle occurs, and at the position where the second contact occurs or the upstream position thereof. A method for producing a fiber-reinforced thermoplastic resin composition.
進行方向とのなす角度(θ)は、0゜<θ≦90゜であ
ることを特徴とする請求項1ないし3記載のいずれかの
長繊維強化熱可塑性樹脂組成物の製造方法。4. The angle (θ) formed by the discharge direction of the molten thermoplastic resin and the advancing direction of the fiber bundle is 0 ° <θ ≦ 90 °. 1. A method for producing a long fiber-reinforced thermoplastic resin composition.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10624593A JP3321240B2 (en) | 1993-04-08 | 1993-04-08 | Method for producing long fiber reinforced thermoplastic resin composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10624593A JP3321240B2 (en) | 1993-04-08 | 1993-04-08 | Method for producing long fiber reinforced thermoplastic resin composition |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH06293023A true JPH06293023A (en) | 1994-10-21 |
JP3321240B2 JP3321240B2 (en) | 2002-09-03 |
Family
ID=14428732
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Application Number | Title | Priority Date | Filing Date |
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JP10624593A Expired - Lifetime JP3321240B2 (en) | 1993-04-08 | 1993-04-08 | Method for producing long fiber reinforced thermoplastic resin composition |
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JP (1) | JP3321240B2 (en) |
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