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JP5582863B2 - Kneading method of kneading material - Google Patents
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JP5582863B2 - Kneading method of kneading material - Google Patents

Kneading method of kneading material Download PDF

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Publication number
JP5582863B2
JP5582863B2 JP2010108125A JP2010108125A JP5582863B2 JP 5582863 B2 JP5582863 B2 JP 5582863B2 JP 2010108125 A JP2010108125 A JP 2010108125A JP 2010108125 A JP2010108125 A JP 2010108125A JP 5582863 B2 JP5582863 B2 JP 5582863B2
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kneading
distribution
kneaded
kneaded material
gear
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JP2011235516A (en
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穂高 三浦
秀夫 船橋
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Kobe Steel Ltd
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Kobe Steel Ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/505Screws
    • B29C48/585Screws provided with gears interacting with the flow
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/505Screws
    • B29C48/57Screws provided with kneading disc-like elements, e.g. with oval-shaped elements

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Description

本発明は、例えば、混練機などによって混練材料を混練する混練方法に関するものである。   The present invention relates to a kneading method in which a kneaded material is kneaded by, for example, a kneader.

一般に、樹脂材料を混練する混練機として、例えば、特許文献1に示すものがある。特許文献1の混練機は、材料供給口と材料排出口を有するチャンバ内に互いに平行な左右一対の混練ロータがその軸方向両端を支持された状態で回転自在に挿通され、この各混練ロータの外周面に、被混練材料を下流側へ搬送するフィード部が形成されているとともに、被混練材料に高剪断力を付与して混練する第一混練部と第二混練部とが前記混練ロータの軸方向に離れて設けられているものである。   In general, as a kneader for kneading resin materials, for example, there is one shown in Patent Document 1. In the kneading machine of Patent Document 1, a pair of left and right kneading rotors that are parallel to each other are rotatably inserted into a chamber having a material supply port and a material discharge port. A feed portion for conveying the material to be kneaded downstream is formed on the outer peripheral surface, and a first kneading portion and a second kneading portion for kneading the material to be kneaded by applying a high shear force are provided on the kneading rotor. It is provided apart in the axial direction.

特開平11−58369号公報JP-A-11-58369

ところで、近年は混練される材料(混練樹脂材料)の種類が多くなり、混練された材料も最終的には極薄のフィルムなどに様々な形状に成形されることも多い。特に極薄フィルムを製造する場合など、混練材料内における成分の偏りや気泡の巻き込み(フィッシュアイ)が存在することは極力避けなければ状況であり、そのために、混練機には、材料の均一混練などに関し従来よりも高い混練能力が求められている。特許文献1に示した混練機は、係る性能をほぼ満足し、ある程度フィッシュアイを抑制することができる混練材料を製造することが可能である。   By the way, in recent years, the types of materials to be kneaded (kneaded resin materials) have increased, and the kneaded materials are often finally formed into various shapes such as extremely thin films. In particular, when manufacturing ultra-thin films, the presence of component bias and bubble entrainment (fish eyes) in the kneaded material is a situation that must be avoided as much as possible. Therefore, higher kneading ability than before is required. The kneader shown in Patent Document 1 can produce a kneaded material that substantially satisfies such performance and can suppress fish eyes to some extent.

しかしながら、特許文献1に開示された混練機であっても、近年要求されている均一混練の要求に対しては十分ではない場合もあり、フィッシュアイを確実に抑制することができる混練材料の混練方法が望まれている。
本発明は、上述の問題に鑑みてなされたものであり、フィルム等の元材となる混練材料を適切に混練することによって、フィルム等のフィッシュアイを抑制することができる混練材料の混練方法を提供することを目的とする。
However, even the kneading machine disclosed in Patent Document 1 may not be sufficient for the recent demand for uniform kneading, and kneading of the kneaded material that can reliably suppress fish eyes. A method is desired.
The present invention has been made in view of the above problems, and a kneading method for a kneading material capable of suppressing fish eyes such as a film by appropriately kneading a kneading material as a base material such as a film. The purpose is to provide.

前記目的を達成するために、本発明は、次の手段を講じた。
即ち、本発明における課題解決のための技術的手段は、粉体状の母材樹脂とオイルとを含む混練材料を混練するに際し、前記混練材料の母材樹脂の周りにオイルを分配する分配混練処理を行い、前記分配混練処理の後に、混練材料にせん断を加えつつ混練を行う分散混練処理を行う点にある。
In order to achieve the above object, the present invention has taken the following measures.
That is, the technical means for solving the problems in the present invention is a distribution kneading that distributes oil around the matrix resin of the kneaded material when the kneaded material containing the powdery matrix resin and oil is kneaded. In this point, after the distributed kneading process, a dispersion kneading process is performed in which kneading is performed while applying shear to the kneaded material.

前記分配混練処理を、混練機に備えられたギアニーディング部で行い、前記分散混練処理を、チップクリアランスが狭い高位チップ部と、前記高位チップよりもチップクリアランスが広い低位チップ部とを備えたフライトを有し、且つ前記ギアニーディング部の下流側に設けられている可変クリアランス混練部で行うことが好ましい。
前記分配混練処理を行うときの温度を、前記母材樹脂の融点以上とし、前記分散混練処理を行うときの温度を、前記母材樹脂の融点以下にすることが好ましい。
The distribution kneading process is performed in a gear kneading unit provided in a kneader, and the dispersion kneading process includes a high-order chip part with a narrow chip clearance and a low-order chip part with a wider chip clearance than the high-order chip. It is preferable to carry out in a variable clearance kneading section provided with a flight and provided downstream of the gear kneading section.
It is preferable that the temperature at which the distribution kneading treatment is performed is equal to or higher than the melting point of the base material resin, and the temperature at which the dispersion kneading processing is performed is equal to or lower than the melting point of the base material resin.

前記母材樹脂は高密度ポリエチレンとされ、前記オイルはパラフィンオイルであることが好ましい。前記母材樹脂に超高分子量ポリエチレンを混合して混練を行うことが好ましい。
また、本発明に係る混練材料の混練方法の最も好ましい形態は、粉体状の母材樹脂とオ
イルとを含む混練材料を混練するに際し、前記混練材料の母材樹脂の周りにオイルを分配する分配混練処理を行い、前記分配混練処理の後に、混練材料にせん断を加えつつ混練を行う分散混練処理を行い、前記分配混練処理を、混練材料に分配性を付与するギアニーディング部で行い、当該ギアニーディング部で前記分配混練処理を行うときの温度を、前記母材樹脂の融点以上とし、前記分散混練処理を、バレルの内壁とチップ先端とのチップクリアランスが狭い高位チップ部と、前記高位チップよりもチップクリアランスが広い低位チップ部とを備えたフライトを有し、且つ前記ギアニーディング部の下流側に設けられている可変クリアランス混練部で行い、当該可変クリアランス混練部で前記分散混練処理を行うときの温度を、前記母材樹脂の融点以下にすることを特徴とする。
The base material resin is preferably high density polyethylene, and the oil is preferably paraffin oil. It is preferable to mix and knead ultra-high molecular weight polyethylene with the matrix resin.
Further, the most preferable mode of the kneading material kneading method according to the present invention is to distribute oil around the kneading material base material resin when kneading the kneading material containing the powdery base material resin and oil. Performing a distribution kneading process, after the distribution kneading process, performing a dispersion kneading process for kneading while adding shear to the kneaded material, and performing the distribution kneading process in a gear kneading section that imparts a dispersibility to the kneaded material, The temperature when performing the distribution kneading process in the gear kneading part is equal to or higher than the melting point of the base resin, and the dispersion kneading process is performed with the high-order chip part having a narrow chip clearance between the inner wall of the barrel and the tip end, A variable clearance kneading part having a flight with a lower tip part having a wider tip clearance than a higher order chip and provided downstream of the gear kneading part There, the temperature at the time of performing the dispersing kneaded in the variable clearance kneading section, characterized by the following melting point of the matrix resin.

本発明によれば、フィルム等の元材となる混練材料を適切に混練することによって、混練材料における成分の偏りや気泡の巻き込み(フィッシュアイ)の存在を確実に抑制することができる。   According to the present invention, by appropriately kneading a kneading material that is a base material such as a film, it is possible to reliably suppress the occurrence of component bias and bubble entrainment (fish eye) in the kneading material.

混練材料の混練方法を行うための混練機を示した図である。It is the figure which showed the kneading machine for performing the kneading | mixing method of a kneading | mixing material. 処理毎の単位体積当たりの異物の面積をまとめた第1グラフである。It is the 1st graph which put together the area of the foreign material per unit volume for every process. 処理毎の単位体積当たりの異物の面積をまとめた第2グラフである。It is the 2nd graph which put together the area of the foreign material per unit volume for every processing.

以下、本発明の混練材料の混練方法について図を基に説明する。
[第1実施形態]
図1は、本発明の混練材料の混練方法を行うための混練機を示したものである。まず、混練機について説明する。なお、混練材料の混練方法は、図1に示した混練機に限定されるものではない。
Hereinafter, the kneading method of the kneading material of the present invention will be described with reference to the drawings.
[First Embodiment]
FIG. 1 shows a kneader for carrying out the kneading method of the kneading material of the present invention. First, the kneader will be described. The kneading method of the kneaded material is not limited to the kneader shown in FIG.

図1に示すように、混練機1は、空洞状のバレル2と、このバレル2の内部を軸方向に沿って挿通するように設けられた混練スクリュ4とを備えており、混練スクリュ4を回転させることでバレル2内の混練材料(混練樹脂材料)を混練しつつ下流側に送ることができる構造とされている。
なお、以降の説明において、図1の紙面の左側を混練機1を上流側とし、紙面の右側を下流側とする。また、図1の紙面の左右方向を混練機1を軸方向とする。さらに、軸方向に対して垂直な方向を混練機1を説明する際の軸垂直方向という。
As shown in FIG. 1, the kneading machine 1 includes a hollow barrel 2 and a kneading screw 4 provided so as to pass through the inside of the barrel 2 along the axial direction. By rotating, the kneading material (kneading resin material) in the barrel 2 is kneaded and sent to the downstream side.
In the following description, the left side of the paper surface of FIG. 1 is the kneader 1 as the upstream side, and the right side of the paper surface is the downstream side. Moreover, let the kneading machine 1 be an axial direction in the left-right direction of the paper surface of FIG. Furthermore, a direction perpendicular to the axial direction is referred to as an axial vertical direction when the kneader 1 is described.

バレル2は、軸方向に沿って長い筒状に形成されており、その内部は断面めがね形状の空洞となっている。バレル2の軸方向の上流側にはバレル2内に材料を供給するホッパ5が設けられており、またバレル2の内部には電気ヒーターや加熱した油を用いた加熱装置(図示略)が備えられている。
混練スクリュ4は、バレル2の空洞内部内に左右一対設けられている。各混練スクリュ4、4は、軸方向に沿って形成されたスプライン軸6を内部に備えており、このスプライン軸6により貫通状に複数のセグメントを固定する構成とされている。
The barrel 2 is formed in a long cylindrical shape along the axial direction, and the inside thereof is a cavity having a cross-sectional glasses shape. A hopper 5 for supplying material into the barrel 2 is provided on the upstream side in the axial direction of the barrel 2, and an electric heater or a heating device (not shown) using heated oil is provided inside the barrel 2. It has been.
A pair of left and right kneading screws 4 are provided inside the cavity of the barrel 2. Each kneading screw 4, 4 includes a spline shaft 6 formed along the axial direction, and a plurality of segments are fixed in a penetrating manner by the spline shaft 6.

図1に示されるように、本実施形態の混練スクリュ4においては、上流側から下流側にかけて、供給された材料を溶融しながら下流側に送る送り部10と、送り部10から送られてきた材料を混練する混練部11と、混練部11で混練された材料を下流側に送り出す押出部12とが設けられている。
送り部10は軸方向に配備された複数のスクリュセグメント13で構成されている。スクリュセグメント13は、軸方向に螺旋状に捩れたスクリュフライト(図示略)を備えており、材料を上流側から下流側に送ることができる。
As shown in FIG. 1, in the kneading screw 4 of the present embodiment, from the upstream side to the downstream side, the feeding part 10 that is sent to the downstream side while melting the supplied material and the feeding part 10 are sent. A kneading part 11 for kneading the material and an extruding part 12 for feeding the material kneaded in the kneading part 11 downstream are provided.
The feed unit 10 is composed of a plurality of screw segments 13 arranged in the axial direction. The screw segment 13 includes a screw flight (not shown) spirally twisted in the axial direction, and can feed material from the upstream side to the downstream side.

押出部12も、送り部10同様に螺旋状に捩れたスクリュフライトを備えたスクリュセグメント13を軸方向に複数有している
練部11は、上流側に位置するギアニーディング部20と、このニーディング部20の下流側に位置するVCMT混練部21(可変クリアランス混練部)とを備えている。
The extrusion unit 12 also has a plurality of screw segments 13 provided with screw flights twisted in a spiral like the feed unit 10 in the axial direction .
Mixing kneading unit 11 is provided with a gear kneading portion 20 located on the upstream side, and a VCMT kneading section 21 located on the downstream side of the kneading section 20 (variable clearance kneading unit).

ギアニーディング部20は、外周面に凹凸が形成されていて断面視でギア形状となっているギアニーディングセグメントで構成されている。このギアニーディング部20は、一対のギアニーディング部20間に材料を導くと共に、バレル2の内壁との間にも材料を導く混練を行うことにより、混練する材料に高い分配性を付与することができる。
ギアニーディング部20の下流側に設けられたVCMT混練部21は、ロータセグメントから構成される。
The gear kneading part 20 is configured by a gear kneading segment having a concavo-convex shape on the outer peripheral surface and having a gear shape in a sectional view. The gear kneading section 20 imparts high distribution to the material to be kneaded by guiding the material between the pair of gear kneading sections 20 and also kneading the material between the inner wall of the barrel 2. be able to.
The VCMT kneading part 21 provided on the downstream side of the gear kneading part 20 is composed of a rotor segment.

このロータセグメントは、チップクリアランス(バレル2の内壁とチップ先端と隙間)が狭い高位チップ部22と、高位チップ部22よりもチップクリアランスが広い低位チップ部23とを軸方向に交互に備えたフライトを有する。即ち、高位チップ部22のチップクリアランスは、低位チップ部23のクリアランスより小さくされており、この小さなチップクリアランスに材料を導いて材料に剪断方向の力を加えながら混練を行うため、混練する材料に高い分配性を付与することができる。   This rotor segment has a high-order tip portion 22 having a narrow tip clearance (inner wall of the barrel 2 and the tip end and a gap), and a low-order tip portion 23 having a tip clearance wider than the high-order tip portion 22 alternately in the axial direction. Have That is, the tip clearance of the high-order tip portion 22 is made smaller than the clearance of the low-order tip portion 23. Since the material is guided to this small tip clearance and kneading is performed while applying a shearing force to the material, High dispersibility can be imparted.

一方、低位チップ部23では、チップクリアランスが高位チップ部22より大きくされており、この大きなチップクリアランスに材料を導いて材料混練を行うため、混練する材料に高い分散性を付与することができる。
以下、本発明の混練材料の混練方法について詳しく説明する。
本発明の混練方法によって混練材料を混練すると、混練後の材料(元材)をフィルムにした場合、フィッシュアイを抑制することができ、例えば、リチウムイオン電池用のセパレータの元材を製造するのに適している。
On the other hand, the low tip portion 23, the chip and clearance is greater than the high tip portion 22, for performing the kneading material leading the material to the large tip clearance, it can impart a high dispersion material is kneaded .
Hereinafter, the kneading method of the kneaded material of the present invention will be described in detail.
When the kneaded material is kneaded by the kneading method of the present invention, when the kneaded material (original material) is made into a film, fish eyes can be suppressed. For example, an original material of a separator for a lithium ion battery is manufactured. Suitable for

フィッシュアイを抑制することができる製造方法、即ち、混練方法では、まず、少なくとも高密度ポリエチレン(HDPE)からなる粉体状の母材樹脂と、この母材樹脂の周りを取り囲むように浸透するパラフィンオイルとをホッパ5に供給する。供給された混練材料は、送り部10により下流側に送られて、ギアニーディング部20によって分配混練処理が行われる。   In a production method capable of suppressing fish eyes, that is, a kneading method, first, a powdery matrix resin made of at least high-density polyethylene (HDPE) and paraffin that permeates so as to surround the matrix resin. Oil is supplied to the hopper 5. The supplied kneading material is sent to the downstream side by the feeding unit 10, and the distribution kneading process is performed by the gear kneading unit 20.

本実施形態では、高密度ポリエチレン、超高分子量ポリエチレン、パラフィンオイルとを、それぞれ6:9:35(質量比)で混合したものを混練材料としている。ここで、混練材料すなわち母材樹脂である高密度ポリエチレンに、超高分子量ポリエチレン(UHMWPE)を混合してもよい。
このように、分配混練処理では、高密度ポリエチレンとパラフィンオイルとを含む混練材料に対して混練処理を行うことによりパラフィンオイルを母材樹脂等に馴染ませることで膨潤して当該混練材料における分配性を高めている。
In the present embodiment, a mixture of high density polyethylene, ultrahigh molecular weight polyethylene, and paraffin oil in a ratio of 6: 9: 35 (mass ratio) is used as the kneading material. Here, you may mix ultrahigh molecular weight polyethylene (UHMWPE) with the kneading | mixing material, ie, high-density polyethylene which is base material resin.
As described above, in the distribution kneading process, the kneading process is performed on the kneaded material containing high-density polyethylene and paraffin oil, so that the paraffin oil swells by being acclimated to the base material resin, etc. Is increasing.

分配混練処理を行った後は、下流側へ送られ、VCMT混練部21によって分配性が高まった混練材料に対して主に剪断を加えて分散性を高める分散混練処理を行う。なお、VCMT混練部21では低位チップ部23によって混練材料を引き延ばして分配性を高める役割もある。そのため、分配混練処理から分散混練処理を見てみると、分配混練処理にて混練材料の分配性を高めた後、当該分散混練処理とにて、さらに分配性と分散性とを高めている。   After performing the distribution kneading process, the dispersion kneading process is carried out to increase the dispersibility by mainly applying shear to the kneaded material which has been sent to the downstream side and has improved the dispersibility by the VCMT kneading unit 21. The VCMT kneading part 21 also has a role of extending the kneaded material by the lower tip part 23 to improve the distribution. Therefore, when looking at the dispersion kneading process from the distribution kneading process, the distribution property of the kneaded material is increased by the distribution kneading process, and then the distribution property and dispersibility are further improved by the dispersion kneading process.

このように、混練材料の母材樹脂の周りにオイルを分配する分配混練処理を行い、分配混練処理の後に、混練材料に剪断を加えつつ混練を行う分散混練処理を行うことにより、混練材料の分配性や分散性が高まり、その結果、材料が均一に混練されると共に、フィッシアイを確実に抑制することができる。
表1は、本発明の方法によって混練した後にフィルムにした場合と、本発明とは異なる方法によって混練した後にフィルムにした場合の異物の個数をまとめたものである。また、図2は、表1における単位体積当たりの異物の面積をまとめたものである。
In this way, the kneading material is distributed and kneaded to distribute the oil around the base material resin, and after the kneading material, the kneading material is subjected to a dispersion kneading process in which kneading is performed while shearing. As a result, the dispersibility and dispersibility are improved, and as a result, the material can be uniformly kneaded and the fisheye can be reliably suppressed.
Table 1 summarizes the number of foreign matters when the film is kneaded by the method of the present invention and then formed into a film, and when the film is kneaded by a method different from the present invention and formed into a film. FIG. 2 summarizes the areas of foreign matter per unit volume in Table 1.

なお、混練するにあたっては、神戸製鋼所製KTX46の混練機1を用いた。また、混練材料のフィード量を75kg/h、混練機1のスクリュ回転数を200rpmにして混練を行った。   For kneading, a KTX46 kneader 1 manufactured by Kobe Steel was used. The kneading material was kneaded at a feed rate of 75 kg / h and the kneading machine 1 at a screw speed of 200 rpm.

表1及び図2に示すように、ギアニーディング部20(GN)にて分配混練処理を行った後に、さらに、ギアニーディング部20(GN)にて分配混練処理を行った場合(比較例1:GN+GN)、即ち、ギア分配混練処理を連続して行った場合、単位体積あたりの異物(例えばフィッシュアイ)の面積は0.012程度であった。
また、VCMT混練部21(VCMT)にて分散混練処理を行った後に、さらに、VCMT混練部21(VCMT)にて分散混練部を行った場合(比較例2:VCMT+VCMT)、即ち、分散混練部を連続して行った場合は、単位体積あたりの異物の面積は0.014程度であった。
As shown in Table 1 and FIG. 2, after performing the distribution kneading process in the gear kneading part 20 (GN) and further performing the distribution kneading process in the gear kneading part 20 (GN) (comparative example) 1: GN + GN), that is, when the gear distribution kneading process was continuously performed, the area of foreign matters (for example, fish eyes) per unit volume was about 0.012.
Further, after the dispersion kneading process is performed in the VCMT kneading unit 21 (VCMT), and further the dispersion kneading unit is performed in the VCMT kneading unit 21 (VCMT) (Comparative Example 2: VCMT + VCMT), that is, the dispersion kneading unit Was continuously performed, the area of the foreign matter per unit volume was about 0.014.

これに対して、本発明のように、ギアニーディング部20(GN)にて分配混練処理を行った後に、VCMT混練部21(VCMT)にて分散混練処理を行った場合(実施例1:GN+VCMT)、単位体積あたりの異物の面積を0.00089程度にすることができ、他の比較例に比べて非常に小さくすることができた。さらに、実施例1(GN+VCMT)では、単位体積当たりの異物の個数も非常に少なくすることができた。   On the other hand, as in the present invention, when the dispersion kneading process is performed in the VCMT kneading part 21 (VCMT) after the distribution kneading process is performed in the gear kneading part 20 (GN) (Example 1: GN + VCMT), the area of the foreign matter per unit volume can be reduced to about 0.00089, and can be very small as compared with other comparative examples. Furthermore, in Example 1 (GN + VCMT), the number of foreign matters per unit volume could be reduced very much.

本発明によれば、粉体状の母材樹脂と膨潤させるオイルとを含む混練材料を混練するに際し、分配混練処理を行った後に分散混練処理を行うことにより、フィッシュアイを抑制した異物の少ないものを製造することができる。
[第2実施形態]
第2実施形態では、分配混練処理を行うときと、分散混練処理を行うときの温度を規定したものである。即ち、本発明では、分配混練処理を行うときの温度は、母材樹脂の融点以上としている。例えば、母材樹脂が高密度ポリエチレン(HDPE)であるときは、ギアニーディング部20の温度や処理するときの温度(処理温度)を、加熱装置によって高密度ポリエチレンの融点(130℃程度)よりも高い180℃にしている。これにより、分配混練処理では高密度ポリエチレンが溶けやすくなり、オイルによる芳潤も進むことからさらに分配性をよくすることができる。
According to the present invention, when kneading a kneaded material containing a powdery base resin and a swelling oil, the dispersion kneading process is performed after the distribution kneading process, thereby reducing the number of foreign matters that suppress fish eyes. Things can be manufactured.
[Second Embodiment]
In the second embodiment, the temperature at which the distribution kneading process is performed and the temperature at which the dispersion kneading process is performed are defined. That is, in the present invention, the temperature at which the distribution kneading process is performed is equal to or higher than the melting point of the base resin. For example, when the base material resin is high-density polyethylene (HDPE), the temperature of the gear kneading part 20 and the temperature at the time of processing (processing temperature) are determined from the melting point (about 130 ° C.) of the high-density polyethylene by a heating device. The temperature is also set to 180 ° C. Thereby, in the distribution kneading process, the high-density polyethylene is easily dissolved, and since the richness by the oil advances, the distribution can be further improved.

また、分散混練処理を行うときの温度は、母材樹脂の融点以下としている。例えば、母材樹脂が高密度ポリエチレン(HDPE)であるときは、VCMT混練部21の温度や処理するときの温度(処理温度)を、加熱装置によって高密度ポリエチレンの融点(130℃程度)よりも低い100℃にしている。これにより、分散混練処理では高密度ポリエチレンが剪断し易くなり、さらに分散製をよくすることができる。   Further, the temperature at which the dispersion kneading process is performed is set to be equal to or lower than the melting point of the base resin. For example, when the base material resin is high-density polyethylene (HDPE), the temperature of the VCMT kneading unit 21 and the temperature during processing (processing temperature) are set higher than the melting point (about 130 ° C.) of the high-density polyethylene by a heating device. The temperature is low 100 ° C. Thereby, in the dispersion kneading process, the high-density polyethylene can be easily sheared, and the dispersion can be further improved.

表2は、本発明の方法によって混練した後にフィルムにした場合と、本発明とは異なる方法によって混練した後にフィルムにした場合の異物の個数をまとめたものである。また、図3は、表2における単位体積当たりの異物の面積をまとめたものである。
なお、混練するにあたっては、混練材料のフィード量を75kg/h、混練機1のスクリュ回転数を300rpmにして混練を行った。
Table 2 summarizes the number of foreign matters when the film is kneaded by the method of the present invention and then formed into a film, and when the film is kneaded by a method different from the present invention and formed into a film. FIG. 3 summarizes the areas of foreign matter per unit volume in Table 2.
In the kneading, the kneading material was fed at a feed rate of 75 kg / h and the kneading machine 1 was rotated at 300 rpm.

表2及び図3に示すように、分配混練処理での処理温度を180℃として母材樹脂の融点よりも高くし、分散混練処理での処理温度を100℃として母材樹脂の融点よりも低くした場合(実施例3:GN+VCMT)、単位体積あたりの異物の面積を0.00356と小さくでき、他の比較例に比べて、均一混練され且つフィッシアイの発生が少ない混練材料を製造できた。   As shown in Table 2 and FIG. 3, the processing temperature in the distribution kneading process is 180 ° C., which is higher than the melting point of the base resin, and the processing temperature in the dispersion kneading process is 100 ° C., which is lower than the melting point of the base resin. In this case (Example 3: GN + VCMT), the area of the foreign matter per unit volume could be reduced to 0.00356, and a kneaded material that was uniformly kneaded and less likely to generate fisheye than the other comparative examples could be produced.

一方、比較例3では、連続して分配混練処理を行っているのに加えて、分配混練処理と分散混練処理との処理温度が同じとしているため、最も異物の面積が大きかった。比較例4では、後処理(2回目の分配混練処理)を行ったときの処理温度を母材樹脂の融点よりも低くしているため、ある程度、異物の面積を小さくできるものの、本発明の実施例3に比べれば非常に大きいものとなった。   On the other hand, in Comparative Example 3, in addition to continuously performing the distribution kneading process, the processing temperatures of the distribution kneading process and the dispersion kneading process are the same, so the area of the foreign matter was the largest. In Comparative Example 4, since the processing temperature when the post-processing (second distribution kneading processing) is performed is lower than the melting point of the base resin, the area of the foreign matter can be reduced to some extent, but the present invention is carried out. Compared to Example 3, it was very large.

なお、分配混練処理と分散混練処理との処理温度が同じとした比較例3と実施例2とを比較しても、実施例2では分配混練処理を行った後に分散混練処理を行っているため、比較例3に比べて異物の面積を小さくすることができた。
また、実施例及び比較例に示すように、単位体積当たりの異物の個数を見ても、分配混練処理での処理温度を母材樹脂の融点よりも高くし、分散混練処理での処理温度を母材樹脂の融点よりも低くした実施例3の個数が最も少なかった。
Even when Comparative Example 3 and Example 2 in which the processing temperatures of the distribution kneading process and the dispersion kneading process are the same are compared, in Example 2, the dispersion kneading process is performed after the distribution kneading process. Compared with Comparative Example 3, the area of the foreign matter could be reduced.
In addition, as shown in the examples and comparative examples, even when looking at the number of foreign matters per unit volume, the processing temperature in the distribution kneading process is higher than the melting point of the base material resin, and the processing temperature in the dispersion kneading process is The number of Example 3, which was lower than the melting point of the base resin, was the smallest.

本発明によれば、分配混練処理を行った後に分散混練処理を行うことにしたうえで、分配混練処理を行うときの温度を母材樹脂の融点以上とし、分配混練処理を行うときの温度を母材樹脂の融点以下にすることにより、さらに、フィッシュアイを抑制した異物の少ないものを製造することができる。
なお、今回開示された実施の形態はすべての点で例示であって制限的なものではないと考えられるべきである。本発明の範囲は上記した説明ではなくて特許請求の範囲によって示され、特許請求の範囲と均等の意味及び範囲内でのすべての変更が含まれることが意図される。
According to the present invention, the dispersion kneading process is performed after the distribution kneading process, and the temperature at which the distribution kneading process is performed is equal to or higher than the melting point of the base resin, and the temperature at which the distribution kneading process is performed is By making it below the melting point of the base material resin, it is possible to produce a product with less foreign matter with fish eyes suppressed.
The embodiment disclosed this time should be considered as illustrative in all points and not restrictive. The scope of the present invention is defined by the terms of the claims, rather than the description above, and is intended to include any modifications within the scope and meaning equivalent to the terms of the claims.

1 混練機
2 バレル
4 混練スクリュ
5 ホッパ
6 スプライン軸
10 送り部
11 混練部
12 押出部
13 スクリュセグメント
20 ギアニーディング部
21 VCMT混練部(可変クリアランス混練部)
22 高位チップ部
23 低位チップ部
DESCRIPTION OF SYMBOLS 1 Kneading machine 2 Barrel 4 Kneading screw 5 Hopper 6 Spline shaft 10 Feed part 11 Kneading part 12 Extrusion part 13 Screw segment 20 Gear kneading part 21 VCMT kneading part (variable clearance kneading part)
22 Higher chip part 23 Lower chip part

Claims (3)

粉体状の母材樹脂とオイルとを含む混練材料を混練するに際し、
前記混練材料の母材樹脂の周りにオイルを分配する分配混練処理を行い、
前記分配混練処理の後に、混練材料にせん断を加えつつ混練を行う分散混練処理を行い、
前記分配混練処理を、混練材料に分配性を付与するギアニーディング部で行い、当該ギアニーディング部で前記分配混練処理を行うときの温度を、前記母材樹脂の融点以上とし、
前記分散混練処理を、バレルの内壁とチップ先端とのチップクリアランスが狭い高位チップ部と、前記高位チップよりもチップクリアランスが広い低位チップ部とを備えたフライトを有し、且つ前記ギアニーディング部の下流側に設けられている可変クリアランス混練部で行い、当該可変クリアランス混練部で前記分散混練処理を行うときの温度を、前記母材樹脂の融点以下にすることを特徴とする混練材料の混練方法。
When kneading a kneaded material containing a powdery base resin and oil,
Perform a distribution kneading process to distribute oil around the base resin of the kneaded material,
After the distribution kneading process, performing a dispersion kneading process for kneading while adding shear to the kneaded material,
The distribution kneading process is performed in a gear kneading section that imparts distribution to the kneaded material, and the temperature when the distribution kneading process is performed in the gear kneading section is equal to or higher than the melting point of the base resin.
The gear kneading portion has a flight including a high-order tip portion having a narrow tip clearance between the inner wall of the barrel and a tip end of the barrel and a low-order tip portion having a wider tip clearance than the high-order tip. the are performed by the variable clearance kneading section which is provided on the downstream side, the temperature at the time of performing the dispersing kneaded in the variable clearance kneading section, of the kneaded material, characterized by the following melting point of the matrix resin Kneading method.
前記母材樹脂は高密度ポリエチレンとされ、前記オイルはパラフィンオイルであることを特徴とする請求項に記載の混練材料の混練方法。 The method for kneading a kneaded material according to claim 1 , wherein the base resin is high-density polyethylene, and the oil is paraffin oil. 前記母材樹脂に超高分子量ポリエチレンを混合して混練を行うことを特徴とする請求項1または2記載の混練材料の混練方法。
The method for kneading a kneaded material according to claim 1 or 2, wherein ultrahigh molecular weight polyethylene is mixed with the matrix resin and kneaded.
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