JP2005280089A - Method for manufacturing melt-molded article - Google Patents

Method for manufacturing melt-molded article Download PDF

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JP2005280089A
JP2005280089A JP2004097257A JP2004097257A JP2005280089A JP 2005280089 A JP2005280089 A JP 2005280089A JP 2004097257 A JP2004097257 A JP 2004097257A JP 2004097257 A JP2004097257 A JP 2004097257A JP 2005280089 A JP2005280089 A JP 2005280089A
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additive
raw material
synthetic resin
melt
pipe
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JP2005280089A5 (en
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Sentaro Honda
千太郎 本多
Takeshi Ojiya
剛 小路谷
Naoyuki Kinoshita
直之 木下
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Toray Industries Inc
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for uniformly sticking a liquid additive on the surface of a synthetic resin granular raw material by a simple apparatus and method when the liquid additive is incorporated into the synthetic resin granular raw material continuously fed into a molding machine. <P>SOLUTION: The liquid additive is incorporated into the synthetic resin granular raw material continuously fed into the molding machine by a definite ratio to the amount of feeding of the synthetic resin granular raw material, and melt molding is performed. The method for manufacturing a melt-molded article comprises the steps of spraying the additive in a mist, and sticking and dispersing the mist-like additive in a feeding pipe for the synthetic resin granular raw material on the surface of the synthetic resin granular raw material. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は成形機へ連続供給される合成樹脂粒体原料への液体添加剤の添加に際し、簡単な装置および方法で合成樹脂粒体原料表面に均一に付着させる方法に関する。 The present invention relates to a method for uniformly adhering to the surface of a synthetic resin granule raw material with a simple apparatus and method when adding a liquid additive to the synthetic resin granule raw material continuously supplied to a molding machine.

従来、合成樹脂粒体原料に液体の滑剤や分散剤等の添加剤を添加する方法として、(1)添加剤をギヤポンプやピストンポンプ等の計量機で計量し、合成樹脂粒体原料とともに直接混練機へ供給し、添加剤を練り込む方法、または、(2)同じく添加剤を計量機で計量し、合成樹脂粒体原料に添加した後、合成樹脂原料を容器に供給し、容器内で撹拌翼やスクリュー等を回転させることにより混和したり、あるいは容器自体を回転させて混和させる方法、あるいは(3)添加剤を合成樹脂粒体原料供給配管内に横入れ供給し、配管内を空送中の合成樹脂の粒子表面に添加剤を分散する方法(特許文献1)等が一般的に知られている。
特開平09−057743号公報
Conventionally, as a method of adding additives such as liquid lubricants and dispersants to synthetic resin granule raw materials, (1) the additive is weighed with a measuring machine such as a gear pump or a piston pump and directly kneaded with the synthetic resin granule raw materials. Or (2) Weighing the additive with a measuring machine and adding it to the synthetic resin granule raw material, then supplying the synthetic resin raw material to the container and stirring in the container Mixing by rotating blades, screws, etc., or mixing by rotating the container itself, or (3) Feed additives into the synthetic resin granule raw material supply pipe and feed them by air A method of dispersing an additive on the surface of synthetic resin particles (Patent Document 1) is generally known.
JP 09-057443 A

しかし、前記第1の方法では、成形機内へ原料が供給される前に添加剤が原料表面に均一に付着していることが要求される場合にはその要求を満たすことができない。また前記第2の方法を実施するには、原料の連続供給ラインの一部に、原料と添加剤を容器内の撹拌翼の回転や容器自体の回転により混和させるための装置を組み込むことが必要となり、そのため設備構成が複雑となるため高価となり、また保守的にも好ましくない。また前記第3の方法のように空送を利用する場合には、ある程度の空送を行うための配管長さが必要となるため、添加剤の横入れ供給口から成形機までの距離が長くなり、添加剤の変更による添加剤の切替を行うに際し配管内洗浄が必要となる場合には空送配管内および配管機器内の清掃に多大な労力を費やす等の問題がある。本発明はこれらの課題を解決するためになされたものであり、成形機へ連続供給される合成樹脂粒体原料への液体添加剤の添加に際し、簡単な装置および方法で合成樹脂粒体原料表面に均一に付着させる方法を提供することを課題とするものである。 However, in the first method, when it is required that the additive uniformly adheres to the surface of the raw material before the raw material is supplied into the molding machine, the request cannot be satisfied. In order to carry out the second method, it is necessary to incorporate a device for mixing the raw material and the additive by the rotation of the stirring blade in the container or the rotation of the container itself in a part of the continuous supply line of the raw material. Therefore, the equipment configuration becomes complicated and expensive, and it is not preferable in terms of maintenance. In addition, when using air transport as in the third method, since a certain length of piping is required for air transport, the distance from the additive feed port to the molding machine is long. Thus, there is a problem in that a great deal of labor is required for cleaning the air-feeding pipe and the piping equipment when cleaning of the pipe is required when switching the additive by changing the additive. The present invention has been made in order to solve these problems. When adding a liquid additive to a synthetic resin granule raw material continuously supplied to a molding machine, the surface of the synthetic resin granule raw material can be obtained with a simple apparatus and method. It is an object of the present invention to provide a method for uniformly adhering to a film.

本発明者らは、液体の添加剤を合成樹脂粒体原料供給量に対して一定比率で添加する際し、合成樹脂粒体原料供給配管内にて添加剤を霧状にすることにより、添加剤を合成樹脂粒体原料表面に付着させ、分散させることが可能であることを見い出した。即ち、本発明は次の構成から成る。
(1)成形機へ連続供給される合成樹脂粒体原料に液体の添加剤を合成樹脂粒体原料供給量に対して一定比率で添加し溶融成形するに際し、添加剤を霧状にし、合成樹脂粒体原料供給配管内にて霧状となった添加剤を合成樹脂粒体原料表面に付着させ、分散させることを特徴とする溶融成形品の製造方法、
(2)添加剤の添加量が0.01cc/min以上であることを特徴とする請求項1に記載の溶融成型品の製造方法、
(3)添加剤がポリオキシエチレンアルキルエーテルの分散剤であることを特徴とする前記(1)に記載の溶融成形品の製造方法。
When adding the liquid additive at a constant ratio with respect to the synthetic resin particle raw material supply amount, the inventors added the liquid additive by atomizing the additive in the synthetic resin particle raw material supply pipe. The present inventors have found that it is possible to attach and disperse the agent on the surface of the synthetic resin granular material. That is, the present invention has the following configuration.
(1) When a liquid additive is added to a synthetic resin granule raw material continuously supplied to a molding machine at a constant ratio with respect to the synthetic resin granule raw material supply amount and melt-molded, the additive is atomized to form a synthetic resin. A method for producing a melt-molded product, characterized by adhering and dispersing the mist-like additive in the granular material supply pipe on the surface of the synthetic resin granular material,
(2) The method for producing a melt-formed product according to claim 1, wherein the additive is added in an amount of 0.01 cc / min or more,
(3) The method for producing a melt-molded product as described in (1) above, wherein the additive is a polyoxyethylene alkyl ether dispersant.

本発明によれば、液体を一定量で添加した後、添加剤を混和させるための撹拌装置を設置するような複雑な装置構成とすることもなく、また添加位置が押出成形機に近い位置にあるので原料配管内および配管機器内の清掃に多大な労力を費やすこともなく、簡単な装置および方法で合成樹脂粒体原料表面に均一に付着させることが可能になる。 According to the present invention, after adding a certain amount of liquid, there is no complicated device configuration such as installing a stirring device for mixing the additive, and the addition position is close to the extruder. Therefore, it is possible to uniformly adhere to the surface of the synthetic resin granular material with a simple apparatus and method without spending a great deal of labor for cleaning the inside of the raw material piping and the piping equipment.

以下本発明の実施の形態を図を用いて説明する。図1に示すように、合成樹脂粒体原料は原料供給配管3を通って成形機1へ連続供給される。本発明の方法で使用する合成樹脂粒体原料はその種類に特に限定されるものではなく、ポリエステルやポリアミドに代表される合成樹脂の粒体原料であれば何れでもよい。原料形状については球状、円筒形状、楕円筒形状など特に限定されるものではないが、大きさとしては一粒の粒子径が0.5〜10mm程度の大きさが好ましい。本発明で使用される添加剤は分散剤等の液体である。また添加剤の粘度としては0.1〜100センチポアズであることが好ましく、より好ましくは1〜30センチポアズである。液体を霧状にする霧化方式としては、一定量の液体をポンプ等によりベンチュリノズルへ供給し、圧縮気体を作用させ霧化させる方法等、特に限定されるものではないが、その霧粒子径は10μm以下が好ましい。また作用させる圧縮気体としては一般的に圧縮空気や不活性ガスが使用されるが、製造プロセスに適したものであれば特に限定されるものではない。添加剤の添加は図1に示すように、霧化装置5により霧化された添加剤を原料供給配管3に横入れすることにより行うものであり、その添加部の詳細について図2に示す。図2に示すように、霧状添加剤8はノズル7により配管内へ導入させ合成樹脂粒体原料6に付着させる。霧状添加剤8は最初に粒面9の原料表面に接触し、その後は合成樹脂粒体原料6の各々の粒子が移動する際の流動により添加剤は粒子表面上で拡散され、ついには成形機1へ供給される全粒子表面に添加剤が均一に付着する。この時、成形機1へ供給される全粒子表面に添加剤をいきわたらせ均一に付着させるためには、添加剤添加部の配管を霧状添加剤8が粒面9の原料表面に接触する際の接触面積、つまり粒面9の面積が大きい程好ましく、原料供給配管内の原料流路断面積の10倍以上、より好ましくは20倍以上となるような形状にした方がよい。またその後の原料の成形機への移動に際しては粒子をより流動させながら移動させることが好ましく、成形機へ至るまでの原料供給配管に屈曲部を設けたり、じゃま板を設けたり、原料に移動速度差を生じさせるのが好ましい。 Embodiments of the present invention will be described below with reference to the drawings. As shown in FIG. 1, the synthetic resin granule raw material is continuously supplied to the molding machine 1 through the raw material supply pipe 3. The synthetic resin granule raw material used in the method of the present invention is not particularly limited to the type thereof, and any synthetic resin granule raw material represented by polyester or polyamide may be used. The shape of the raw material is not particularly limited, such as a spherical shape, a cylindrical shape, or an elliptical cylindrical shape, but the size is preferably about 0.5 to 10 mm. The additive used in the present invention is a liquid such as a dispersant. Moreover, it is preferable that it is 0.1-100 centipoise as a viscosity of an additive, More preferably, it is 1-30 centipoise. The atomization method for atomizing the liquid is not particularly limited, such as a method of supplying a certain amount of liquid to the venturi nozzle with a pump or the like and causing the compressed gas to act, but the atomized particle diameter Is preferably 10 μm or less. In addition, compressed air or inert gas is generally used as the compressed gas to be actuated, but it is not particularly limited as long as it is suitable for the manufacturing process. As shown in FIG. 1, the addition of the additive is performed by putting the additive atomized by the atomizer 5 into the raw material supply pipe 3, and details of the addition portion are shown in FIG. 2. As shown in FIG. 2, the mist additive 8 is introduced into the pipe by the nozzle 7 and adhered to the synthetic resin granular material 6. The mist additive 8 first contacts the raw material surface of the grain surface 9, and thereafter, the additive is diffused on the particle surface by the flow of each particle of the synthetic resin granular raw material 6 moving, and finally molded. The additive uniformly adheres to the surface of all particles supplied to the machine 1. At this time, in order for the additive to spread and uniformly adhere to the surface of all the particles supplied to the molding machine 1, when the mist additive 8 contacts the raw material surface of the grain surface 9 in the pipe of the additive addition part. The contact area, that is, the area of the grain surface 9 is preferably as large as possible, and it is better to have a shape that is at least 10 times, more preferably at least 20 times the cross-sectional area of the raw material flow path in the raw material supply pipe. In addition, when moving the raw material to the molding machine after that, it is preferable to move the particles while fluidizing, and the raw material supply pipe leading to the molding machine is provided with a bent part, a baffle plate, the moving speed of the raw material It is preferable to make a difference.

以下、実施例を挙げて本発明を詳細に説明するが、本発明は以下の実施例にのみ限定されるものではない。 EXAMPLES Hereinafter, although an Example is given and this invention is demonstrated in detail, this invention is not limited only to a following example.

実施例1 合成樹脂粒体原料として、直径1mm長さ2mmのペレット状のナイロン6を用い配管内径80mmの配管にて40kg/Hrの供給量で押出成形機へ供給し、溶融成形を行った。添加剤として粘度3ポアズのポリオキシエチレンアルキルエーテルを用い、供給量0.03cc/minで霧化装置へ供給し、霧状にした添加剤を0.02MPaの圧力で添加した。添加剤の合成樹脂原料への接触面積が大きくなるよう原料供給配管途中に径500mm高さ300mmの円錐形状のポットを設置し、そのポット頂点より垂直線上にノズルを配置した。ノズルと原料粒面との距離は約250mmであり、ノズルから噴射される添加剤の噴射角度は60度とした。この結果、霧状添加剤がポット内原料粒面の原料表面に接触する際の接触面積は原料供給配管内径面積の約15倍となった。ポットを出た後押出成形機へ至るまでの配管の配管内径は50mm、配管長は1m、配管角度は床面鉛直方向より30度である。サンプリングは、押出成形機の原料投入口直前の配管途中のサンプリング管より行った。本添加剤は非イオン系界面活性剤であり正確な定量が困難であることから、次の様に添加剤の付着状況の判定を行った。使用する合成樹脂粒体原料をあらかじめ4〜5kVに帯電させる。このとき帯電した合成樹脂粒体原料は、静電誘導現象により金属表面に容易に付着する。添加剤が原料表面に均一に付着していれば、原料表面の固有抵抗が小さくなり、合成樹脂粒体原料は、金属表面には付着しない。よってサンプルを金属容器に入れ、金属壁面に合成樹脂粒体原料が1粒も付着していなければ添加剤は原料表面に均一に付着していると判定し、金属壁面に合成樹脂粒体原料が1粒でも付着すれば添加剤は原料表面に均一に付着していないと判定することにした。サンプル量を50g、時間間隔10分毎に連続10回サンプリングを行ったところ、いずれも金属壁面に合成樹脂原料が付着することなく目的を達成することができた。   Example 1 As a synthetic resin granule raw material, pellet-shaped nylon 6 having a diameter of 1 mm and a length of 2 mm was used and supplied to an extruder at a supply rate of 40 kg / Hr through a pipe having a pipe inner diameter of 80 mm to perform melt molding. Polyoxyethylene alkyl ether having a viscosity of 3 poise was used as an additive, supplied to the atomizer at a supply rate of 0.03 cc / min, and the atomized additive was added at a pressure of 0.02 MPa. A conical pot with a diameter of 500 mm and a height of 300 mm was installed in the middle of the raw material supply pipe so that the contact area of the additive with the synthetic resin raw material was increased, and a nozzle was arranged on the vertical line from the top of the pot. The distance between the nozzle and the raw material grain surface was about 250 mm, and the spray angle of the additive sprayed from the nozzle was 60 degrees. As a result, the contact area when the mist additive contacts the raw material surface of the raw material grain surface in the pot is about 15 times the inner diameter area of the raw material supply pipe. The pipe inner diameter of the pipe from the pot to the extrusion molding machine is 50 mm, the pipe length is 1 m, and the pipe angle is 30 degrees from the floor vertical direction. Sampling was performed from a sampling pipe in the middle of the piping just before the raw material inlet of the extruder. Since this additive is a nonionic surfactant and accurate quantification is difficult, the adhesion state of the additive was determined as follows. The synthetic resin particle raw material to be used is charged to 4 to 5 kV in advance. At this time, the charged synthetic resin particle material easily adheres to the metal surface due to the electrostatic induction phenomenon. If the additive is uniformly attached to the raw material surface, the specific resistance of the raw material surface becomes small, and the synthetic resin granular raw material does not adhere to the metal surface. Therefore, the sample is put in a metal container, and if no synthetic resin particle raw material is attached to the metal wall surface, it is determined that the additive is uniformly attached to the raw material surface, and the synthetic resin particle raw material is attached to the metal wall surface. If even one grain adhered, it was determined that the additive was not uniformly adhered to the raw material surface. When the sample amount was 50 g and sampling was performed ten times every 10 minutes, the objective could be achieved without any synthetic resin material adhering to the metal wall surface.

実施例2 添加剤の供給量を0.008cc/minとし、それ以外は実施例1と同様の条件で添加剤を添加し、サンプルの添加剤の付着状況を確認した。添加量が少ないため、最初添加剤が原料表面に均一にいきわたるまで時間を要したと考えられるが、10分後の1回目のサンプリング時には実施例1に記載の判定方法により原料表面に添加剤が均一に付着しているのが確認できた。   Example 2 The additive supply amount was set to 0.008 cc / min, and other than that, the additive was added under the same conditions as in Example 1, and the adhesion state of the sample additive was confirmed. Since the amount added is small, it is considered that it took time until the initial additive uniformly spread on the raw material surface, but the additive was added to the raw material surface by the determination method described in Example 1 at the first sampling after 10 minutes. It was confirmed that it was uniformly attached.

実施例3 添加剤をモノオレイン酸ポリエチレングリコールとしそれ以外は実施例1と同様の条件で添加剤を添加した。実施例1に記載の判定方法によりサンプルの添加剤の付着状況を確認した結果、原料表面に添加剤が均一に付着しているのが確認できた。   Example 3 The additive was added under the same conditions as in Example 1 except that polyethylene glycol monooleate was used as the additive. As a result of confirming the adhesion state of the sample additive by the determination method described in Example 1, it was confirmed that the additive was uniformly adhered to the raw material surface.

比較例1 実施例1に記載の添加剤をギヤポンプで計量し、40kg/Hrの供給量で押出成形機へ連続供給される実施例1に記載の合成樹脂粒体原料とともに直接押出成形機原料投入口のホッパへ供給量0.03cc/minで連続供給した。原料ホッパ下限でサンプリングし、実施例1に記載の判定方法によりサンプルの添加剤の付着状況を確認した結果、添加剤は均一に付着していないと判定された。   Comparative Example 1 The additive described in Example 1 is weighed with a gear pump, and the raw material is directly fed into the extruder together with the synthetic resin granule material described in Example 1, which is continuously supplied to the extruder at a supply rate of 40 kg / Hr. It was continuously supplied to the hopper at the mouth at a supply rate of 0.03 cc / min. Sampling was performed at the lower limit of the raw material hopper, and the adhesion state of the sample additive was confirmed by the determination method described in Example 1. As a result, it was determined that the additive was not uniformly adhered.

比較例2 撹拌翼を持つ混合機に2kgのペレット状ナイロン6を入れ、実施例1に記載の添加剤をギヤポンプで0.1cc計量して容器内に供給し、容器内で撹拌翼を回転させることにより混合させ、実施例1に記載の判定方法によりサンプルの添加剤の付着状況を確認した結果、得られた原料表面には添加剤が均一に付着していたが、撹拌することで合成樹脂原料が削れ、長時間使用後には粉が蓄積されるため品質維持のための清掃を行う必要があり保守的には好ましくなかった。   Comparative Example 2 2 kg of pelletized nylon 6 is placed in a mixer having a stirring blade, 0.1 cc of the additive described in Example 1 is weighed by a gear pump and supplied into the container, and the stirring blade is rotated in the container. As a result of confirming the adhesion state of the sample additive by the determination method described in Example 1, the additive was uniformly adhered to the surface of the obtained raw material. Since the raw material was shaved and the powder accumulated after long-term use, it was necessary to perform cleaning to maintain the quality, which was not preferable from a maintenance standpoint.

比較例3 配管を内径50mmとし、長さ10mの配管を垂直に立ち上げ、90°のエルボを介して水平方向に配管を延長した配管内を流速20m/sec、固気重量比10:1で空送し、垂直配管から5mの位置で添加剤を横入れし、配管途中に10m間隔で設けたサンプリング管より原料をサンプリングし、実施例1に記載の判定方法によりサンプルの添加剤の付着状況を確認した結果、添加剤添加位置から少なくとも50m以上離れていないと、原料表面に添加剤が均一に付着しないことが確認できた。このように配管長さが長い場合、添加剤の変更による添加剤の切替を行うに際し配管内洗浄が必要となる場合には空送配管内および配管機器内の清掃に多大な労力を費やすことが予想される。   Comparative Example 3 A pipe having an inner diameter of 50 mm, a pipe having a length of 10 m was set up vertically, and the pipe was extended horizontally through a 90 ° elbow with a flow rate of 20 m / sec and a solid-gas weight ratio of 10: 1. Feed by air, put the additive horizontally at a position 5m from the vertical pipe, sample the raw material from the sampling pipe provided at intervals of 10m in the middle of the pipe, and use the determination method described in Example 1 As a result, it was confirmed that the additive did not uniformly adhere to the raw material surface unless it was at least 50 m away from the additive addition position. If the pipe length is long in this way, when switching the additive by changing the additive, it is necessary to clean the inside of the piping and the piping equipment if cleaning inside the pipe is necessary. is expected.

本発明の形態を説明するための全体構成を示した図である。It is the figure which showed the whole structure for demonstrating the form of this invention. 本発明の形態を説明するための添加剤添加部詳細を示した図である。It is the figure which showed the additive addition part detail for demonstrating the form of this invention.

符号の説明Explanation of symbols

1:成形機
2:原料ホッパ
3:原料供給配管
4:バルブ
5:霧化装置
6:合成樹脂粒体原料
7:ノズル
8:霧状添加剤
9:粒面
1: Molding machine 2: Raw material hopper 3: Raw material supply piping 4: Valve 5: Atomizer 6: Synthetic resin granular material 7: Nozzle 8: Atomized additive 9: Grain surface

Claims (3)

成形機へ連続供給される合成樹脂粒体原料に液体の添加剤を合成樹脂粒体原料供給量に対して一定比率で添加し溶融成形するに際し、添加剤を霧状にし、合成樹脂粒体原料供給配管内にて霧状となった添加剤を合成樹脂粒体原料表面に付着させ、分散させることを特徴とする溶融成形品の製造方法。 When a liquid additive is added to a synthetic resin granule raw material continuously supplied to a molding machine at a fixed ratio to the synthetic resin granule raw material supply amount and melt-molded, the additive is atomized to form a synthetic resin granule raw material. A method for producing a melt-molded product, comprising: adhering an atomized additive in a supply pipe to a surface of a synthetic resin granule material and dispersing the additive. 添加剤の添加量が0.01cc/min以上であることを特徴とする請求項1に記載の溶融成型品の製造方法。 The method for producing a melt-molded product according to claim 1, wherein the additive is added in an amount of 0.01 cc / min or more. 添加剤がポリオキシエチレンアルキルエーテルの分散剤であることを特徴とする請求項1に記載の溶融成形品の製造方法。 The method for producing a melt-molded article according to claim 1, wherein the additive is a polyoxyethylene alkyl ether dispersant.
JP2004097257A 2004-03-30 2004-03-30 Method for manufacturing melt-molded article Pending JP2005280089A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Application Number Priority Date Filing Date Title
JP2004097257A JP2005280089A (en) 2004-03-30 2004-03-30 Method for manufacturing melt-molded article

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JP2005280089A true JP2005280089A (en) 2005-10-13
JP2005280089A5 JP2005280089A5 (en) 2007-05-24

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Family Applications (1)

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Country Link
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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05278028A (en) * 1992-03-31 1993-10-26 Sekisui Chem Co Ltd Applying method of liquid dispersant to granular resin raw material
JPH0957743A (en) * 1995-08-24 1997-03-04 Asahi Chem Ind Co Ltd Method for adding additive to synthetic resin particle
JPH11216723A (en) * 1998-02-03 1999-08-10 Teijin Ltd Manufacture of thermoplastic resin composition
JPH11511400A (en) * 1995-08-30 1999-10-05 ラフバロウ ユニヴァシティ イノベーションズ リミテッド How to mix rubber or plastic materials
JP2000313774A (en) * 1999-04-28 2000-11-14 Dainichiseika Color & Chem Mfg Co Ltd Colored resin composition for blow moldling and its production
JP2003320528A (en) * 2002-04-30 2003-11-11 Mitsubishi Chemicals Corp Thermoplastic resin pellet

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05278028A (en) * 1992-03-31 1993-10-26 Sekisui Chem Co Ltd Applying method of liquid dispersant to granular resin raw material
JPH0957743A (en) * 1995-08-24 1997-03-04 Asahi Chem Ind Co Ltd Method for adding additive to synthetic resin particle
JPH11511400A (en) * 1995-08-30 1999-10-05 ラフバロウ ユニヴァシティ イノベーションズ リミテッド How to mix rubber or plastic materials
JPH11216723A (en) * 1998-02-03 1999-08-10 Teijin Ltd Manufacture of thermoplastic resin composition
JP2000313774A (en) * 1999-04-28 2000-11-14 Dainichiseika Color & Chem Mfg Co Ltd Colored resin composition for blow moldling and its production
JP2003320528A (en) * 2002-04-30 2003-11-11 Mitsubishi Chemicals Corp Thermoplastic resin pellet

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