JPH05253997A - Die for extruding machine - Google Patents

Die for extruding machine

Info

Publication number
JPH05253997A
JPH05253997A JP4052793A JP5279392A JPH05253997A JP H05253997 A JPH05253997 A JP H05253997A JP 4052793 A JP4052793 A JP 4052793A JP 5279392 A JP5279392 A JP 5279392A JP H05253997 A JPH05253997 A JP H05253997A
Authority
JP
Japan
Prior art keywords
die
resin
eye
edge
outlet
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
Application number
JP4052793A
Other languages
Japanese (ja)
Inventor
Yoshitomi Urabe
好富 浦部
Yoshihiro Inoue
義弘 井上
Kazuhiro Yoshida
和弘 吉田
Kenichi Haga
健一 芳賀
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Kasei Corp
Original Assignee
Mitsubishi Kasei Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsubishi Kasei Corp filed Critical Mitsubishi Kasei Corp
Priority to JP4052793A priority Critical patent/JPH05253997A/en
Publication of JPH05253997A publication Critical patent/JPH05253997A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To control remarkably generation of the discharge from the eye at the time of extrusion molding, and curing is made remarkable by high-viscous grade of polycarbonate having especially high shearing rate, by forming a tapered part having a half vertical angle of 4-20 deg. on an outlet part of a die. CONSTITUTION:A tapered part 1 having a half vertical angle of 4-20 deg. is formed on an outlet part of a flow path of a die. Since the tapered part 1 is provided on the outlet of a die hole like this, expansion of resin by a Barus effect is completed on this side than an edge part and the resin neither stick nor stay on an edge 4, the title die is free from dwell, oxidation and heat deterioration of a polymer and generation of the discharge from the eye is controlled remarkably. Then it is not preferable since when the half vertical angle theta of the tapered part 1 is less than 4 deg., a control effect in generation of the discharge from the eye is insufficient and when the same exceeds 20 deg., resin is accumulated and becomes apt to burn at the time of cleaning of the edge 4.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は樹脂の成形に用いられる
押出機のダイに関する。詳しくはポリカーボネートなど
の熱可塑性樹脂の成形時の目ヤニの発生を著しく抑制で
きる押出機用ダイに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an extruder die used for molding a resin. More specifically, the present invention relates to an extruder die capable of remarkably suppressing the occurrence of eye crevices during molding of a thermoplastic resin such as polycarbonate.

【0002】[0002]

【従来の技術】押出成形は最も汎用的な成形方法であ
り、成形金型(ダイ)の形状等については広く研究され
ている。例えばダイの流路の断面形状は目的に応じて様
々の形状があり、様々な形状について圧力降下やせん断
速度などの流動特性が調べられており、またメルトフラ
クチャーの発生防止のためダイ入口の流路にテーパを付
けるなどの工夫も知られている(SPEジャーナル,4
23(1960))。しかし、ダイの流路出口のエッジ
形状については直角かせいぜい角を丸めてRを付ける程
度しか知られていなかった。
2. Description of the Related Art Extrusion molding is the most general molding method, and the shape of a molding die has been widely studied. For example, the cross-sectional shape of the flow path of the die has various shapes according to the purpose, and the flow characteristics such as pressure drop and shear rate have been investigated for various shapes, and the flow at the die inlet has been investigated to prevent the occurrence of melt fracture. It is also known to devise ways such as tapering the road (SPE Journal, 4
23 (1960)). However, regarding the edge shape of the flow path outlet of the die, it has been known only to round the right angle and round the angle at most.

【0003】[0003]

【発明が解決しようとする課題】ところで、ポリカーボ
ネートなどの熱可塑性樹脂を押出成形しペレット化する
際に、目ヤニと通称される劣化物がダイの流路出口で発
生、付着し、これが製品に混入し、不良品となるという
問題があった。劣化物が製品に同伴するのを防ぐには頻
繁に掃除する必要があり、生産能力の低下や生産ロスの
増大の要因となっていた。
By the way, when a thermoplastic resin such as polycarbonate is extruded and pelletized, a deteriorated material commonly referred to as an eye crocodile is generated and adhered at the flow path outlet of the die, and this deteriorates the product. There is a problem that it is mixed and becomes a defective product. Frequent cleaning is required to prevent deterioration products from being carried along with the product, which has been a factor in lowering production capacity and increasing production loss.

【0004】[0004]

【課題を解決するための手段】本発明者らはダイ流路出
口での目ヤニの発生の抑制につき鋭意検討した結果、ダ
イの流路(以下「ダイホール」という)の出口のエッジ
に滞留した樹脂が酸化劣化及び熱劣化して目ヤニが発生
するのであり、ダイホール出口部にテーパを設けること
により目ヤニ発生を著しく抑制できることを見出し本発
明に達した。
Means for Solving the Problems As a result of diligent studies on the suppression of the occurrence of eye dents at the exit of the die flow path, the present inventors have accumulated at the exit edge of the flow path of the die (hereinafter referred to as "die hole"). The present invention has been accomplished by finding that the resin is oxidatively deteriorated and thermally deteriorated to cause eye blemishes. Therefore, the present invention has been found to be able to remarkably suppress the eye rosiness generation by providing a taper at the die hole outlet portion.

【0005】すなわち、本発明の要旨はダイの流路出口
部に、半頂角4〜20°のテーパを形成したことを特徴
とする押出機用ダイに存する。以下、本発明を図面を参
照しながら詳細に説明する。図1は本発明のダイホール
出口部の縦断面を模式的に表わした図面である。本発明
のダイはダイホール出口部にテーパ部(1)を形成した
ことを特徴とする。
That is, the gist of the present invention resides in an extruder die characterized in that a taper having a half-vertical angle of 4 to 20 ° is formed at the outlet of the flow path of the die. Hereinafter, the present invention will be described in detail with reference to the drawings. FIG. 1 is a diagram schematically showing a vertical cross section of a die hole outlet portion of the present invention. The die of the present invention is characterized in that a taper portion (1) is formed at the exit portion of the die hole.

【0006】テーパー部(1)の角度は半頂角θが4〜
20°である。4°未満では目ヤニ発生の抑制効果が不
十分である。20°を超えるとエッジ(4)掃除時に樹
脂が溜まって焼けやすく好ましくない。また、テーパ部
の大きさ(奥行)(5)は通常、ダイホールエッジ径
(2)がダイホール内径(3)の1.05〜1.3倍と
なるような大きさとする。下限未満では目ヤニ発生の抑
制効果が不十分である。上限を超え、バラス効果時のス
トランド最大径を超えるとダイと樹脂の間にすき間が生
じ、エッジ掃除時に樹脂が溜まって焼けやすく好ましく
ない。
The angle of the taper portion (1) has a half-vertical angle θ of 4 to
It is 20 °. If it is less than 4 °, the effect of suppressing the occurrence of eye blemishes is insufficient. If it exceeds 20 °, the resin is likely to be burnt because the resin is accumulated during cleaning of the edge (4), which is not preferable. Further, the size (depth) (5) of the tapered portion is usually set such that the die hole edge diameter (2) is 1.05 to 1.3 times the die hole inner diameter (3). If it is less than the lower limit, the effect of suppressing the occurrence of eye blemishes is insufficient. Exceeding the upper limit and exceeding the maximum strand diameter at the time of the ballast effect will cause a gap between the die and the resin, and the resin is likely to be burnt because of the accumulation during edge cleaning, which is not preferable.

【0007】本発明はフィルム、シート成形用の直状ス
リットやパイプ成形用の円形状スリットにも通用できる
が、特にペレット成形用の断面形状が円形のノズルに好
適である。以下、ペレット用ノズルの場合について説明
する。ペレット成形の場合、通常、直径1mm〜10mmの
円管状のホールが単数又は複数あるプレート(以下、ダ
イプレートと呼ぶ)がダイとして用いられる。ダイホー
ルの径や個数はペレットの大きさやダイホールでのせん
断速度に応じて定めることができる。せん断速度は粘
度,押出量,ダイホール断面積などから公知の方法で求
めることができる。
The present invention can be applied to straight slits for forming films and sheets and circular slits for forming pipes, but is particularly suitable for a nozzle having a circular cross section for forming pellets. The case of a pellet nozzle will be described below. In the case of pellet molding, a plate having a single or plural circular holes having a diameter of 1 mm to 10 mm (hereinafter referred to as a die plate) is usually used as a die. The diameter and the number of die holes can be determined according to the size of pellets and the shear rate in the die holes. The shear rate can be determined by a known method from the viscosity, extrusion rate, die hole cross-sectional area and the like.

【0008】ダイホール入口部の形状は公知の形状でよ
くテーパを有していてもいなくてもよい。ダイホール入
口部の形状はメルトフラクチュアの発生防止を考慮して
定められる。ダイプレートの材質としては通常ステンレ
ス綱(SUS304など)や工具綱(Cr 11〜13
%,Mo 0.8〜1.2%含有する鉄合金)などが用
いられる。
The shape of the inlet of the die hole may be a known shape and may or may not have a taper. The shape of the die hole inlet is determined in consideration of the prevention of melt fracture. The material of the die plate is usually stainless steel rope (SUS304 etc.) or tool rope (Cr 11-13).
%, An iron alloy containing 0.8 to 1.2% Mo) and the like.

【0009】また、ダイホールの流路面の表面仕上げ精
度は特に問題とならないが、当然のことながらエッジに
は傷のないことが必要である。エッジに傷があると目ヤ
ニが発生しやすくなる。本発明のダイにより成形される
樹脂は熱可塑性樹脂であれば制限はないが、ポリカーボ
ネート,ナイロン,PET,PBTなどのポリエステル
樹脂あるいはこれらにフィラー,ガラスファイバーなど
を添加したコンパウンド樹脂のときに効果が大きく、特
にポリカーボネートに有用であり、ポリカーボネートの
場合でもせん断速度を280 sec-1以上として押出す場
合にとくに効果的である。
Further, the surface finish accuracy of the flow path surface of the die hole does not pose any particular problem, but it is needless to say that the edge is not damaged. If the edge is scratched, eye blemishes are likely to occur. The resin molded by the die of the present invention is not limited as long as it is a thermoplastic resin, but it is effective when it is a polyester resin such as polycarbonate, nylon, PET, PBT or a compound resin obtained by adding a filler, glass fiber or the like to these. It is large and is particularly useful for polycarbonate, and even in the case of polycarbonate, it is particularly effective when extruding at a shear rate of 280 sec -1 or more.

【0010】本発明の押出成形機を用いてポリカーボネ
ートのペレットを成形する場合、ダイから押出されたポ
リマーを常法に従って冷却後、カッターで切断すること
によってペレット化できる。
When polycarbonate pellets are molded using the extruder of the present invention, the polymer extruded from the die can be pelletized by cooling it in a conventional manner and then cutting it with a cutter.

【0011】[0011]

【作用】次に本発明のダイが押出成形時に目ヤニ防止の
効果を奏する機構について説明する。目ヤニが樹脂の酸
化物等であることは従来から知られている。本発明者ら
は鋭意検討した結果、ダイホールエッジ部に溶融樹脂が
付着,滞留し、これが外気によって酸化されることを見
出した。
Next, the mechanism by which the die of the present invention exhibits the effect of preventing eye blemishes during extrusion molding will be described. It has been conventionally known that the eye die is an oxide of resin or the like. As a result of diligent studies, the present inventors have found that the molten resin adheres to and stays at the edge of the die hole and is oxidized by the outside air.

【0012】このため例えばエッジにキズがあると樹脂
が更に滞留しやすくなるため目ヤニの発生が著しく多く
なる。また、エッジにキズがなくとも、成形時に樹脂は
バラス効果により膨張し、エッジに接するため、エッジ
に樹脂が滞留することとなる。本発明ではダイホール出
口部にテーパを設けることにより、バラス効果による樹
脂の膨張がエッジ部より手前で終了し、エッジに樹脂が
付着,滞留しないため、ポリマーの滞留及び酸化,熱劣
化がなく目ヤニの発生を著しく抑制できる。
For this reason, for example, if the edge has scratches, the resin is more likely to stay, and the occurrence of eye blemishes remarkably increases. Further, even if the edge is not scratched, the resin expands due to the loosening effect during molding and comes into contact with the edge, so that the resin stays at the edge. In the present invention, by providing a taper at the die hole outlet, the expansion of the resin due to the ballast effect ends before the edge, and the resin does not adhere to or stay at the edge, so that there is no polymer retention, oxidation, or thermal deterioration, and there is no eye stain. Can be remarkably suppressed.

【0013】[0013]

【実施例】以下に本発明を実施例により具体的に説明す
るが、本発明はその要旨を超えない限り、実施例により
何ら限定されるものではない。 実施例1 樹脂としてポリカーボネート樹脂(三菱化成(株)製,
商品名NOVAREX7030A)を用いて実験した。
ダイとして図1に概略を示すようなダイホールを有する
ものを用いた。ダイホールの内径は2.2mmφ(図1の
(3))、長さ11mmとした。ダイホールの先端には、
角度(θ)10°,奥行(5)1mmのテーパを形成し
た。上述のようなダイを用い、ポリカーボネート樹脂を
温度320℃,せん断速度340 sec-1の条件で180
分間押出成形を行ない、15分間隔で目ヤニの有無を調
べたが、目ヤニの発生はなかった。
EXAMPLES The present invention will be specifically described below with reference to examples, but the present invention is not limited to the examples as long as the gist thereof is not exceeded. Example 1 A polycarbonate resin (made by Mitsubishi Kasei Co., Ltd.,
Experiments were carried out using the trade name NOVAREX 7030A).
A die having a die hole as shown in FIG. 1 was used. The inner diameter of the die hole was 2.2 mmφ ((3) in FIG. 1) and the length was 11 mm. At the tip of the die hole,
A taper having an angle (θ) of 10 ° and a depth (5) of 1 mm was formed. Using a die as described above, the polycarbonate resin is heated at a temperature of 320 ° C. and a shear rate of 340 sec −1 for 180 times.
Extrusion molding was carried out for one minute and the presence or absence of eye blemishes was checked at intervals of 15 minutes, but no eye blemishes were found.

【0014】比較例1 ダイホール出口部にテーパを形成せず、エッジが直角で
ある他は実施例1と同様にした。成形開始後15分で目
ヤニが発生した。
Comparative Example 1 The same procedure as in Example 1 was carried out except that the exit of the die hole was not tapered and the edge was right angled. Eye fogging occurred 15 minutes after the start of molding.

【0015】比較例2 エッジに半径1mmのアールを形成した他は比較例1と同
様にした。開始後30分で目ヤニが発生した。
Comparative Example 2 The same as Comparative Example 1 except that a radius of 1 mm was formed on the edge. Eye blemishes occurred 30 minutes after the start.

【0016】比較例3 テーパを角度(θ)3°,奥行(5)1mmとした他は実
施例1と同様にした。開始後30分で目ヤニが発生し
た。
Comparative Example 3 The same as Example 1 except that the taper was set at an angle (θ) of 3 ° and a depth (5) of 1 mm. Eye blemishes occurred 30 minutes after the start.

【0017】比較例4 テーパを角度(θ)30°,奥行(5)1mmとした他は
実施例1と同様にした。目ヤニの発生はなかったが、掃
除時にテーパに樹脂が残ってしまい、次の成形時に焼け
てしまった。
Comparative Example 4 The same as Example 1 except that the taper was 30 ° in angle (θ) and 1 mm in depth (5). There was no eye blemishes, but the resin remained on the taper during cleaning, and it burned during the next molding.

【0018】実施例2 ダイホール寸法を内径(3)5.5mmφ,長さ20mm
に、テーパを角度(θ)5.8°,奥行(5)5.0mm
に変えて実施例1と同様に押出成形した。180分間目
ヤニの発生はなかった。また、同装置により、目ヤニが
製品に同伴されることなく72時間連続運転ができた。
結果を表−1にまとめる。
Example 2 A die hole having an inner diameter (3) of 5.5 mmφ and a length of 20 mm
, Taper angle (θ) 5.8 °, depth (5) 5.0 mm
The extrusion molding was performed in the same manner as in Example 1 except that There was no generation of tars for 180 minutes. In addition, the same device allowed continuous operation for 72 hours without the eye escort being entrained in the product.
The results are summarized in Table-1.

【0019】[0019]

【表1】 (注1) テーパのかわりにエッジを1mmRの曲面とし
た。 (注2) 掃除時に樹脂がテーパに残り焼けた。
[Table 1] (Note 1) Instead of the taper, the edge is a curved surface of 1 mmR. (Note 2) The resin remained on the taper and burned during cleaning.

【0020】[0020]

【発明の効果】本発明のダイは押出成形時の目ヤニ発生
を極めて著しく抑制する効果がある。特にせん断速度の
大きいポリカーボネートの高粘度グレードで効果が顕著
となる。
The die of the present invention has the effect of remarkably suppressing the occurrence of eye crevices during extrusion molding. In particular, the effect becomes remarkable in a high viscosity grade of polycarbonate having a high shear rate.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明のダイの出口部縦断面の模式図である。FIG. 1 is a schematic view of a vertical cross section of an outlet of a die of the present invention.

【符号の説明】[Explanation of symbols]

1 テーパー 2 エッジ径 3 ホール内径 4 エッジ 5 テーパの奥行 θ テーパの半頂角 1 Taper 2 Edge diameter 3 Hole inner diameter 4 Edge 5 Taper depth θ Taper half-vertical angle

───────────────────────────────────────────────────── フロントページの続き (72)発明者 芳賀 健一 北九州市八幡西区黒崎城石1番1号 三菱 化成株式会社黒崎工場内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Kenichi Haga, No. 1 Shiroishi Kurosaki, Yawatanishi-ku, Kitakyushu City Mitsubishi Kasei Co., Ltd. Kurosaki Plant

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 ダイの流路の出口部に半頂角4〜20°
のテーパを形成したことを特徴とする押出機用ダイ。
1. A semi-vertical angle of 4 to 20 ° at the outlet of the flow path of the die.
A die for an extruder, which is characterized by forming a taper.
【請求項2】 ポリカーボネートをせん断速度280 s
ec-1以上で押出成形する際に用いるダイである請求項1
に記載の押出機用ダイ。
2. Polycarbonate at a shear rate of 280 s
A die used for extrusion molding at ec -1 or more.
The die for an extruder described in.
JP4052793A 1992-03-11 1992-03-11 Die for extruding machine Pending JPH05253997A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4052793A JPH05253997A (en) 1992-03-11 1992-03-11 Die for extruding machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4052793A JPH05253997A (en) 1992-03-11 1992-03-11 Die for extruding machine

Publications (1)

Publication Number Publication Date
JPH05253997A true JPH05253997A (en) 1993-10-05

Family

ID=12924719

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4052793A Pending JPH05253997A (en) 1992-03-11 1992-03-11 Die for extruding machine

Country Status (1)

Country Link
JP (1) JPH05253997A (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003080518A (en) * 2001-09-10 2003-03-19 Unitika Ltd Pellet granulation device
WO2005011944A3 (en) * 2003-07-30 2005-06-02 Du Pont Process and apparatus for underwater pelletization of polymers
WO2008090673A1 (en) * 2007-01-24 2008-07-31 Mitsubishi Chemical Corporation Process for producing aromatic polycarbonate
JP2008202026A (en) * 2007-01-24 2008-09-04 Mitsubishi Chemicals Corp Process for producing aromatic polycarbonate
JP2011031563A (en) * 2009-08-05 2011-02-17 International Chemical:Kk Polycarbonate co-extruded multilayer sheet
CN102260926A (en) * 2011-07-26 2011-11-30 东华大学 Smelting and spraying die head device for preparing micro and nano fibers
JP2012076052A (en) * 2010-10-05 2012-04-19 Ajinomoto Co Inc Screen of extrusion granulator and extrusion granulator
JP2012232432A (en) * 2011-04-28 2012-11-29 Mitsubishi Engineering Plastics Corp Die for resin extrusion
WO2014111171A1 (en) * 2013-01-17 2014-07-24 Reduction Engineering Gmbh Nozzle and perforated plate for an underwater granulator
KR101446887B1 (en) * 2014-01-14 2014-10-06 (주)한도기공 Extruder dies for forming a sheet
CN105459402A (en) * 2015-12-22 2016-04-06 珠海天威飞马打印耗材有限公司 Printing head and three-dimensional printer
EP3466630A4 (en) * 2016-05-24 2020-04-29 Sumitomo Bakelite Co.,Ltd. Fiber-containing particulate resin structure, method for producing fiber-containing particulate resin structure, cured fiber-reinforced resin product, and fiber-reinforced resin molded article

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003080518A (en) * 2001-09-10 2003-03-19 Unitika Ltd Pellet granulation device
EP2228188A3 (en) * 2003-07-30 2012-08-29 Ticona LLC Process and apparatus for underwater pelletization of polymers
WO2005011944A3 (en) * 2003-07-30 2005-06-02 Du Pont Process and apparatus for underwater pelletization of polymers
US7658874B2 (en) * 2003-07-30 2010-02-09 E.I. Du Pont De Nemours And Company Polymer pelletization process and apparatus
EP2228188A2 (en) 2003-07-30 2010-09-15 E.I. Du Pont De Nemours And Company Underwater Melt Cutter and Process for Underwater Melt Cutting of a Polymer
WO2008090673A1 (en) * 2007-01-24 2008-07-31 Mitsubishi Chemical Corporation Process for producing aromatic polycarbonate
JP2008202026A (en) * 2007-01-24 2008-09-04 Mitsubishi Chemicals Corp Process for producing aromatic polycarbonate
US8715552B2 (en) 2007-01-24 2014-05-06 Mitsubishi Chemical Corporation Production method of aromatic polycarbonate
JP2011031563A (en) * 2009-08-05 2011-02-17 International Chemical:Kk Polycarbonate co-extruded multilayer sheet
JP2012076052A (en) * 2010-10-05 2012-04-19 Ajinomoto Co Inc Screen of extrusion granulator and extrusion granulator
JP2012232432A (en) * 2011-04-28 2012-11-29 Mitsubishi Engineering Plastics Corp Die for resin extrusion
CN102260926A (en) * 2011-07-26 2011-11-30 东华大学 Smelting and spraying die head device for preparing micro and nano fibers
WO2014111171A1 (en) * 2013-01-17 2014-07-24 Reduction Engineering Gmbh Nozzle and perforated plate for an underwater granulator
KR101446887B1 (en) * 2014-01-14 2014-10-06 (주)한도기공 Extruder dies for forming a sheet
CN105459402A (en) * 2015-12-22 2016-04-06 珠海天威飞马打印耗材有限公司 Printing head and three-dimensional printer
EP3466630A4 (en) * 2016-05-24 2020-04-29 Sumitomo Bakelite Co.,Ltd. Fiber-containing particulate resin structure, method for producing fiber-containing particulate resin structure, cured fiber-reinforced resin product, and fiber-reinforced resin molded article

Similar Documents

Publication Publication Date Title
JPH05253997A (en) Die for extruding machine
RU2457109C2 (en) Method and device for extrusion into pellets and pellets thus produced
KR100250095B1 (en) Polymer extrusion die
JP5638882B2 (en) Method for extrusion molding of thermoplastic resin composition
JP2021100824A (en) Pelletizer and pellet production method using the same
JP3728891B2 (en) Method for producing polycarbonate resin pellets
CA1084786A (en) Method and apparatus for manufacturing an even laminated product by extrusion
AU2002301682B2 (en) Die apparatus for use in resin extrusion machine, and extrusion molding method
JPH081662A (en) Production of fiber-reinforced thermoplastic resin pellet, fiber-reinforced thermoplastic resin pellet, and die device
WO1998039147A1 (en) Underwater cutting pelletizer, knife used for the same pelletizer, and underwater cutting pelletization method using the same knife
JP2001191326A (en) Granulating die for pelletizer
JPH07117047A (en) Production of thermoplastic resin pellet
DE102012008564A1 (en) Continuous casting apparatus for producing granules of melt material and method for their operation
JP2740748B2 (en) Conform extrusion equipment
JP3684040B2 (en) Method for producing thermoplastic resin sheet
EP0501773A1 (en) Resin molding die
US3833705A (en) Process for controlling strand drop-off
JP2000242971A (en) Polycarbonate forming material for optical disk substrate
JP3294923B2 (en) Manufacturing method of synthetic resin tube
JPS6021213Y2 (en) Strand forming equipment
TW201036778A (en) Device and method for continuous casting and granulation of strands from thermoplastic
JPH11254430A (en) Manufacture of molding resin material and its device
JP2002120222A (en) Resin cutting device for pelletizing and method for pelletizing
JPH1171510A (en) Polycarbonate molding material for optical disc substrate
JP6808947B2 (en) Molded product manufacturing method