JPH05301218A - Production of thermoplastic resin particle - Google Patents

Production of thermoplastic resin particle

Info

Publication number
JPH05301218A
JPH05301218A JP4132058A JP13205892A JPH05301218A JP H05301218 A JPH05301218 A JP H05301218A JP 4132058 A JP4132058 A JP 4132058A JP 13205892 A JP13205892 A JP 13205892A JP H05301218 A JPH05301218 A JP H05301218A
Authority
JP
Japan
Prior art keywords
die
heat insulating
resin particles
thermoplastic resin
contact
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
JP4132058A
Other languages
Japanese (ja)
Inventor
Tadanobu Maeda
忠信 前田
Shinya Ogi
晋哉 扇
Yoshi Nakajima
嘉 中島
Yoshinari Ito
良成 伊藤
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 Chemical BASF Co Ltd
Original Assignee
Mitsubishi Chemical BASF Co Ltd
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 Chemical BASF Co Ltd filed Critical Mitsubishi Chemical BASF Co Ltd
Priority to JP4132058A priority Critical patent/JPH05301218A/en
Publication of JPH05301218A publication Critical patent/JPH05301218A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/58Component parts, details or accessories; Auxiliary operations
    • B29B7/582Component parts, details or accessories; Auxiliary operations for discharging, e.g. doors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B9/00Making granules
    • B29B9/02Making granules by dividing preformed material
    • B29B9/06Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion
    • B29B9/065Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion under-water, e.g. underwater pelletizers

Abstract

PURPOSE:To obtain a method for producing thermoplastic resin particles having a small diameter and a high sphericality by an under-water cutting system or a hot cutting system. CONSTITUTION:A die 2 with a heat insulating surface is loaded on the top end of an extruder 1. A rotating cutter is disposed on the die 2 (a heat insulating material) in a contact or non-contact state. A melt resin is extruded into cooling water from a nozzle 5 of the die 2. By cutting the resin by a rotating cutter blade 4, spherical resin particles are produced. The use of the heat insulating die 2 realizes the production of spherical particles having a particle diameter as small as 0.8-2.0mm and a high sphericality. With the cutter blade 4 in non- contact with the die 2 (a heat insulating material), the damages of the cutter blade 4 and the die 2 are also prevented.

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、成形材料として用いら
れる熱可塑性樹脂粒子(ペレット)の製造方法に関する
ものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing thermoplastic resin particles (pellets) used as a molding material.

【0002】[0002]

【従来の技術】熱可塑性樹脂粒子(ペレット)に発泡剤
を含浸させて発泡樹脂粒子を製造する場合等において
は、原料となるペレットは極力小径かつ真球度の高いも
のであることが好ましい。
2. Description of the Related Art In the case of producing expanded resin particles by impregnating thermoplastic resin particles (pellets) with a foaming agent, it is preferable that the raw material pellets have a diameter as small as possible and a high sphericity.

【0003】しかし、広く一般に適用されているストラ
ンドカット方式によると、ペレット形状は円柱状とな
り、又、小径ペレットを製造しようとするとストランド
の乱れ、融着によるペレット形状の乱れが著しく、実質
上粒径約2mm以下のペレットを製造することは極めて
困難であった。
However, according to the widely-used strand cutting method, the pellet shape is columnar, and when trying to manufacture a small-diameter pellet, the strand shape is disturbed and the pellet shape is significantly disturbed due to fusion, and the pellet size is substantially reduced. It was extremely difficult to produce pellets with a diameter of about 2 mm or less.

【0004】そこで、形状、粒径の均質な球状ペレット
を製造することができる水中カット方式、ホットカット
方式によるペレットの製造方法が試みられている。
Under the circumstances, attempts have been made to produce pellets by an underwater cutting method or a hot cutting method capable of producing spherical pellets having a uniform shape and particle size.

【0005】[0005]

【発明が解決しようとする課題】しかし、これら方式に
おいてはダイス外表面に冷却水を直接接触して流動させ
るため、ノズル中において溶融樹脂の温度が急激に低下
して固化してしまい、ノズルの目詰まりが発生し易い。
However, in these methods, since the cooling water is brought into direct contact with the outer surface of the die to flow the cooling water, the temperature of the molten resin in the nozzle is rapidly lowered and solidified, and Clogging easily occurs.

【0006】これを防止するにはダイス及び冷却水の温
度を高くすることが行われているが、これにより逆にダ
イス出口部で溶融樹脂が冷却不十分となり、ノズルより
吐出される樹脂が柔軟であるため、回転カッターの刃を
ダイス出口端に当接させなくては切断すらできず、ダイ
スや回転カッターの刃を損傷し易いうえ、回転カッター
による切断は良好ではなく、ヒゲ状突起物を有するペレ
ット、扁平形状のペレットとなってしまう。そして、こ
のようなペレットを用いて成形すると、ペレット同士の
融着が起こり易く、成形効率を低下するという問題点が
あった。
In order to prevent this, the temperature of the die and the cooling water is increased, but on the contrary, the molten resin is insufficiently cooled at the die outlet, and the resin discharged from the nozzle is soft. Therefore, even if the blade of the rotary cutter does not come into contact with the exit end of the die, it cannot be cut, and the blade of the die and the rotary cutter is easily damaged. The pellets will have a flat shape. Then, when the pellets are molded using such pellets, there is a problem that the pellets are easily fused with each other and the molding efficiency is lowered.

【0007】本発明は、かかる問題点に鑑みてなされた
ものであり、水中カット方式、ホットカット方式により
樹脂粒子(ペレット)を製造する場合における上記問題
点を解決し、従来にない小径かつ真球度の高い樹脂粒子
(ペレット)を製造できる熱可塑性樹脂粒子の製造方法
を提供せんとするものである。
The present invention has been made in view of the above problems, and solves the above problems in the case of producing resin particles (pellets) by an underwater cutting method or a hot cutting method, and has a small diameter and a true diameter. It is intended to provide a method for producing thermoplastic resin particles capable of producing resin particles (pellets) having high sphericity.

【0008】[0008]

【課題を解決するための手段】上記課題を解決するため
に、本発明は、水中カット方式、ホットカット方式、す
なわち熱可塑性樹脂の溶融物を押出機先端に装着したダ
イスのノズルより冷却水中又は冷却空気中に押出し、回
転カッターにより切断して粒状化する方式を採用するも
のであり、特に表面が断熱されたダイスを用いることを
特徴とするものである。
In order to solve the above-mentioned problems, the present invention relates to an underwater cutting method, a hot cutting method, that is, a method in which a melt of a thermoplastic resin is cooled in water by a nozzle of a die attached to the tip of an extruder. It employs a method of extruding into cooling air, cutting with a rotary cutter and granulating, and is characterized in that a die whose surface is heat-insulated is used in particular.

【0009】本発明は、小径の球状粒子製造のためにノ
ズルを小径のものとした場合に粒子形状に及ぼす要因を
鋭意研究した結果なされたものである。すなわち、表面
が断熱されたダイスを使用することにより、ノズル中で
の溶融樹脂温度の低下を抑制でき、溶融樹脂の固化を防
止できる。これにより、溶融樹脂は効率よくダイス出口
に到りしかる後にダイス出口にて冷却水により急激に冷
却されて固化し、カッター刃による切断は良好となり、
小径のヒゲ状突起物を有しない球状粒子が製造可能とな
る。
The present invention has been made as a result of diligent research on the factors affecting the particle shape when the nozzle has a small diameter for the production of small-diameter spherical particles. That is, by using a die having a heat-insulated surface, it is possible to prevent the temperature of the molten resin in the nozzle from decreasing and prevent the molten resin from solidifying. As a result, the molten resin efficiently reaches the die outlet and is rapidly cooled by the cooling water at the die outlet to be solidified, and the cutting by the cutter blade becomes good,
It becomes possible to manufacture spherical particles having no small-sized beard-like protrusions.

【0010】本発明の製造方法は、各種熱可塑性樹脂粒
子の製造に広く適用できるが、特にはポリエチレン系樹
脂、ポリプロピレン系樹脂、ポリスチレン系樹脂等を原
料として、粒径0.8〜2.0mmの球状樹脂粒子を製
造する場合に最適である。
The production method of the present invention can be widely applied to the production of various thermoplastic resin particles. In particular, polyethylene-based resin, polypropylene-based resin, polystyrene-based resin or the like is used as a raw material, and the particle size is 0.8 to 2.0 mm. It is most suitable for the production of spherical resin particles.

【0011】なお、本発明の製造方法は、押出機の吐出
能力を増大する効果もあることがわかった。
It has been found that the manufacturing method of the present invention also has the effect of increasing the discharge capacity of the extruder.

【0012】ダイス表面を断熱するために使用する断熱
材の材料としては、熱伝導率1.0(kcal/m・h
r・℃)以下の合成樹脂、セラミック、金属等の材料が
好適である。又、断熱材は肉厚0.1〜1.0mmと
し、ダイス表面の全面又はノズル周辺に取り付け、この
断熱材取付部を通過後に溶融樹脂がダイス出口より吐出
するようにする。
The material of the heat insulating material used to insulate the surface of the die has a thermal conductivity of 1.0 (kcal / m · h).
Materials such as synthetic resins, ceramics, and metals having a temperature of r.degree. C. or less are preferable. The heat insulating material has a wall thickness of 0.1 to 1.0 mm and is attached on the entire surface of the die or around the nozzle so that the molten resin is discharged from the die outlet after passing through the heat insulating material attaching portion.

【0013】[0013]

【実施例】次に、実施例と比較例とを対比して本発明を
さらに詳しく説明する。
EXAMPLES Next, the present invention will be described in more detail by comparing Examples with Comparative Examples.

【0014】(実施例1〜12)30mmφ押出機先端
に、その表面を熱伝導率0.1(kcal/m・hr・
℃)のポリエーテルエーテルケトン樹脂で断熱したダイ
スを装着した。所定条件下で、このダイスのノズルより
ポリスチレン、ポリエチレン、ポリプロピレンの溶融物
を冷却水中に押出し、ダイス(断熱材)出口端に接触又
は非接触状態で回転するカッター刃により切断し、樹脂
粒子を製造した。製造された樹脂粒子の形状、粒径等を
表1に示す。
(Examples 1 to 12) The surface of the 30 mmφ extruder had a thermal conductivity of 0.1 (kcal / m · hr ·).
A die insulated with a polyetheretherketone resin (° C.) Was attached. Under predetermined conditions, polystyrene, polyethylene, polypropylene melt is extruded from the die nozzle into cooling water and cut with a cutter blade that rotates in contact with or not in contact with the die (heat insulating material) outlet end to produce resin particles. did. Table 1 shows the shape and particle size of the resin particles produced.

【0015】[0015]

【表1】 [Table 1]

【0016】(比較例1〜6)30mmφ押出機先端
に、その表面を断熱していないダイスを装着した。所定
条件下で、このダイスのノズルよりポリスチレン、ポリ
エチレン、ポリプロピレンの溶融物を冷却水中に押出
し、ダイス出口端に接触状態で回転するカッター刃によ
り切断し、樹脂粒子を製造した。製造された樹脂粒子の
形状、粒径等を表2に示す。
(Comparative Examples 1 to 6) A die whose surface was not heat-insulated was attached to the tip of the 30 mmφ extruder. Under predetermined conditions, a melt of polystyrene, polyethylene, and polypropylene was extruded from the nozzle of this die into cooling water, and cut with a cutter blade that rotates in contact with the exit end of the die to produce resin particles. Table 2 shows the shapes and particle sizes of the resin particles produced.

【0017】[0017]

【表2】 [Table 2]

【0018】本発明の製造方法によれば、実施例から明
らかなように、従来困難であった粒径0.8〜2.0m
mの小径かつ真球度の高い球状粒子を製造することがで
き、又、造粒能力を増大するという効果がある。さら
に、回転カッターの刃をダイス(断熱材)出口端に接触
状態とせずに良好な切断を行うことができ、形状、粒径
の均質な粒子を製造することができる。
According to the manufacturing method of the present invention, as is clear from the examples, the particle diameter of 0.8 to 2.0 m, which was difficult in the prior art, was obtained.
Spherical particles having a small diameter of m and high sphericity can be produced, and the granulating ability is increased. Further, good cutting can be performed without bringing the blade of the rotary cutter into contact with the exit end of the die (heat insulating material), and particles having a uniform shape and particle size can be produced.

【0019】[0019]

【発明の効果】本発明の熱可塑性樹脂粒子の製造方法に
よれば、従来困難であった粒径0.8〜2.0mmの小
径かつ真球度の高い球状粒子を製造することができ、造
粒能力を増大することができる。
According to the method for producing thermoplastic resin particles of the present invention, it is possible to produce spherical particles having a small diameter of 0.8 to 2.0 mm and a high sphericity, which has been difficult so far. The granulating ability can be increased.

【0020】又、回転カッターの刃をダイス(断熱材)
出口端に非接触状態も造粒できるので、ダイス及び回転
カッタ−の刃の損傷を防止できる。
Further, the blade of the rotary cutter is a die (heat insulating material).
Since it is possible to granulate even in the non-contact state with the outlet end, damage to the die and the blade of the rotary cutter can be prevented.

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

【図1】本発明で使用される押出ダイの一実施例の断面
図である。
FIG. 1 is a cross-sectional view of one example of an extrusion die used in the present invention.

【符号の説明】[Explanation of symbols]

1 押出機 2 ダイス 3 断熱材 4 回転カッター刃 5 ノズル 1 Extruder 2 Die 3 Insulation 4 Rotating Cutter Blade 5 Nozzle

───────────────────────────────────────────────────── フロントページの続き (72)発明者 伊藤 良成 三重県四日市市川尻町1000番地 三菱油化 バーディッシェ株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Yoshinari Ito 1000 Kawajiri-cho, Yokkaichi-shi, Mie Mitsubishi Yuka Birdishe Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 ダイスより押出した溶融樹脂を回転カッ
ターにより切断して樹脂粒子とする熱可塑性樹脂粒子の
製造方法において、表面が断熱されたダイスを使用する
ことを特徴とする熱可塑性樹脂粒子の製造方法。
1. A method of producing thermoplastic resin particles, wherein molten resin extruded from a die is cut by a rotary cutter to form resin particles, and a die having a heat-insulated surface is used. Production method.
JP4132058A 1992-04-24 1992-04-24 Production of thermoplastic resin particle Pending JPH05301218A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4132058A JPH05301218A (en) 1992-04-24 1992-04-24 Production of thermoplastic resin particle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4132058A JPH05301218A (en) 1992-04-24 1992-04-24 Production of thermoplastic resin particle

Publications (1)

Publication Number Publication Date
JPH05301218A true JPH05301218A (en) 1993-11-16

Family

ID=15072534

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4132058A Pending JPH05301218A (en) 1992-04-24 1992-04-24 Production of thermoplastic resin particle

Country Status (1)

Country Link
JP (1) JPH05301218A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001527474A (en) * 1997-04-24 2001-12-25 ポーレックス テクノロジーズ コーポレーション Sintered porous plastic product and method of manufacturing the same
JP2004141733A (en) * 2002-10-23 2004-05-20 Moriyama:Kk Kneading apparatus
WO2008102874A1 (en) * 2007-02-23 2008-08-28 Sekisui Plastics Co., Ltd. Granulating die, granulating apparatus, and process for producing expandable thermoplastic resin grain
WO2009057318A1 (en) * 2007-10-31 2009-05-07 Mitsui Chemicals, Inc. Process for production of polyolefin pellets

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001527474A (en) * 1997-04-24 2001-12-25 ポーレックス テクノロジーズ コーポレーション Sintered porous plastic product and method of manufacturing the same
JP2004141733A (en) * 2002-10-23 2004-05-20 Moriyama:Kk Kneading apparatus
WO2008102874A1 (en) * 2007-02-23 2008-08-28 Sekisui Plastics Co., Ltd. Granulating die, granulating apparatus, and process for producing expandable thermoplastic resin grain
JP4799664B2 (en) * 2007-02-23 2011-10-26 積水化成品工業株式会社 Die for granulation, granulator, and method for producing expandable thermoplastic resin particles
WO2009057318A1 (en) * 2007-10-31 2009-05-07 Mitsui Chemicals, Inc. Process for production of polyolefin pellets
JP4918142B2 (en) * 2007-10-31 2012-04-18 三井化学株式会社 Method for producing polyolefin pellets
US8557154B2 (en) 2007-10-31 2013-10-15 Mitsui Chemicals, Inc. Process for production of polyolefin pellets

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