JPH1112498A - Production of powder coating material - Google Patents
Production of powder coating materialInfo
- Publication number
- JPH1112498A JPH1112498A JP9171320A JP17132097A JPH1112498A JP H1112498 A JPH1112498 A JP H1112498A JP 9171320 A JP9171320 A JP 9171320A JP 17132097 A JP17132097 A JP 17132097A JP H1112498 A JPH1112498 A JP H1112498A
- Authority
- JP
- Japan
- Prior art keywords
- powder coating
- rotor
- coating material
- resin
- powder
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Paints Or Removers (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、粉体塗料の製造方
法、特に粉砕工程時に発生する微粉量が少ない粉体塗料
の製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a powder coating, and more particularly to a method for producing a powder coating in which the amount of fine powder generated in a pulverizing step is small.
【0002】[0002]
【従来の技術】粉体塗料の製造方法としては乾式と湿式
がある。湿式法は粉体塗料組成物を溶剤に溶解あるいは
分散させ、塗装後に溶剤を除去させる方法であるため、
溶剤の取り扱いに多くの工程や付帯設備を必要とし、ま
た作業環境の点からもその利用は最近敬遠されつつあ
る。一方、乾式法は粉体塗料の各原料を溶融混練し、こ
れを冷却、粉砕する方法である。2. Description of the Related Art As a method for producing a powder coating, there are a dry method and a wet method. Since the wet method is a method of dissolving or dispersing the powder coating composition in a solvent and removing the solvent after coating,
Solvent handling requires many steps and additional facilities, and its use has recently been shunned from the viewpoint of the working environment. On the other hand, the dry method is a method in which each raw material of the powder coating is melt-kneaded, cooled and pulverized.
【0003】冷却にはクーリングベルトが主として用い
られている。溶融混練組成物の冷却が不十分な場合に
は、冷却効率が低下し、場合によっては目標とする粒径
が得られない。粉砕には、パルペライザー、ビクトリー
ミル、ボールミル、ジェットミル等が用いられ、粉体の
性状と目標粒径に応じて使い分けられる。通常は、粉砕
効率を高めるために、5〜15mm程度の塊状にする粗粉
砕工程と、目標粒径までに粉砕する微粉砕工程に分けて
処理される。[0003] Cooling belts are mainly used for cooling. When the cooling of the melt-kneading composition is insufficient, the cooling efficiency is lowered, and in some cases, a target particle size cannot be obtained. For pulverization, a pulperizer, a Victory mill, a ball mill, a jet mill, or the like is used, and the pulverizer is used depending on the properties of the powder and the target particle size. Usually, in order to increase the pulverization efficiency, the treatment is divided into a coarse pulverization step of forming a block of about 5 to 15 mm and a fine pulverization step of pulverizing to a target particle size.
【0004】流動浸漬法用粉体の場合平均粒径を40〜
80μm、静電塗装用の場合は30〜60μmにコント
ロールする必要があるが、ハンマーミル等の粗砕機を用
いた場合には、平均粒径は2〜5mmと大きく、且つ粒
度分布も数μmから10数mmと広くなる。一般的に、
粗粉砕物の粒径が、微粉砕後の目標粒径に近いほど微粉
砕に要する時間は短くなり、又粒度分布は狭いほど過粉
砕による微粉の発生を抑えることができるため、このよ
うな粗砕物を粉砕した場合には、粉砕時間が長くなると
共に、多くの微粉や粗粒が発生する。製品中に微粉が多
すぎると塗装作業性が悪化し、逆に粗粉が多すぎると塗
膜外観不良や粉体流動性不良に伴う経時劣化等の問題が
生じる。[0004] In the case of a powder for a fluid immersion method, the average particle size is 40 to
80 μm, it is necessary to control to 30 to 60 μm for electrostatic coating, but when using a crusher such as a hammer mill, the average particle size is as large as 2 to 5 mm, and the particle size distribution is from several μm. It is as wide as 10 and several mm. Typically,
The closer the particle size of the coarsely pulverized product is to the target particle size after the fine pulverization, the shorter the time required for the fine pulverization, and the narrower the particle size distribution, the more fine powder can be generated. When the crushed material is crushed, the crushing time becomes long and many fine powders and coarse particles are generated. If the amount of fine powder in the product is too large, the coating workability deteriorates. On the other hand, if the amount of coarse powder is too large, problems such as poor coating film appearance and deterioration over time due to poor powder fluidity occur.
【0005】使用する用途により最適な粒度分布は異な
るが、いずれの場合においても従来の製造方法における
粉砕工程では、得られる粉体の粒度分布は必要以上に広
いために分級工程を必要とする。分級された微粉や粗粒
を廃棄することは歩留まりの低下につながり、生産コス
トが高くなる。また、微粉や粗粒を回収し処理を行い製
品に加工することは加工費が高くなる。つまり、目標と
する粒度分布に対して微粉や粗粒が多い場合には生産効
率が低下し、高コストとなる。特に、微粉の発生は作業
環境の悪化を招く。[0005] Although the optimum particle size distribution varies depending on the use, in any case, in the pulverization step in the conventional production method, a classification step is required because the particle size distribution of the obtained powder is wider than necessary. Discarding the classified fine powder or coarse particles leads to a decrease in yield and an increase in production cost. In addition, collecting fine powder and coarse particles, processing them and processing them into products increases processing costs. That is, when there are many fine powders and coarse particles with respect to the target particle size distribution, the production efficiency is reduced and the cost is high. In particular, the generation of fine powder causes the working environment to deteriorate.
【0006】粉砕の効率を改善した粉体塗料の製造方法
は特開平8−218643号公報や特開平8−2949
16号公報に開示されている。この方法を用いることに
より、従来のハンマーミル等の粗砕工程を経た微粉砕工
程よりも発生する微粉量を低減することは可能である。
しかし、この方法のように溶融混練した樹脂を供給する
回転子がピン型ディスクあるいはベーン型ディスクで遠
心力のみを利用して溶融樹脂を繊維状とする場合には、
得られる生成物の大きさは不均一で且つ、目標とする粒
径に比べ大きくなる。例えばピン型ディスクの場合、供
給する樹脂の溶融粘度が低く糸状で回転子に連続供給し
た時には、樹脂は隣り合った2本のピンの間で遠心力に
より延ばされ、繊維状となるため、繊維の長さはピン間
距離よりも長くなる。A method for producing a powder coating material with improved pulverization efficiency is disclosed in Japanese Patent Application Laid-Open No. 8-218643 and Japanese Patent Application Laid-Open No. 8-2949.
No. 16 discloses this. By using this method, it is possible to reduce the amount of fine powder generated in comparison with a conventional fine pulverizing step that uses a hammer mill or the like.
However, when the rotor for supplying the melt-kneaded resin is a pin type disk or a vane type disk and the molten resin is made into a fibrous form using only centrifugal force as in this method,
The size of the product obtained is non-uniform and larger than the target particle size. For example, in the case of a pin-type disk, when the melt viscosity of the supplied resin is low and the resin is continuously supplied to the rotor in the form of a thread, the resin is stretched by centrifugal force between two adjacent pins and becomes a fibrous form. The fiber length is longer than the distance between the pins.
【0007】繊維長を短くするためにピン間距離を狭く
した場合には、ピン間の樹脂量が少なくなるために作用
する遠心力も小さくなりピン間より離れにくく、樹脂が
回転子内部で滞留することになる。滞留を防ぎ遠心力を
大きくするためには回転速度を上げる必要があり、大き
な動力を必要とすると共に、作業の安全性も低下する。
一方繊維の太さは樹脂供給量に依存するため、供給量が
十分少ないときは細くなるが、生産能力を上げるために
供給量を増やした場合には繊維径は太くなる。When the distance between the pins is reduced to shorten the fiber length, the centrifugal force acting due to the decrease in the amount of resin between the pins is reduced, so that the resin is less likely to separate from the pins, and the resin stays inside the rotor. Will be. In order to prevent stagnation and increase the centrifugal force, it is necessary to increase the rotation speed, which requires large power and reduces the safety of work.
On the other hand, the fiber thickness depends on the resin supply amount, and therefore becomes thin when the supply amount is sufficiently small, but becomes large when the supply amount is increased in order to increase the production capacity.
【0008】また、供給する樹脂の溶融粘度が高い場合
や糸状での連続供給ができずに樹脂を断続的に回転ディ
スクに供給する場合には、局所的なピンに対しての樹脂
の供給となる。よって、局所的なピンにおいては樹脂は
過剰供給となり、ピンの空隙部全体より樹脂が押し出さ
れる形となるため不均一な板状で且つ極めて大きな形状
となる。このことはベーン型ディスクについても同様の
ことが言える。つまり、この方法では粉砕工程で効率よ
く目標粒度を得ることは不十分である。従来回転子を利
用した製造方法としては、特開昭50−121529号
公報、特開昭50−121530号公報、特開昭59−
203448号公報等に開示されているが、いずれも綿
状の製品を製造することを目的としており、本発明とは
異なるものである。Further, when the melt viscosity of the resin to be supplied is high or when the resin is intermittently supplied to the rotating disk without being able to be continuously supplied in a thread form, the supply of the resin to the local pins must be reduced. Become. Therefore, the resin is excessively supplied to the local pin, and the resin is extruded from the entire void portion of the pin, so that the pin is nonuniform and extremely large. The same can be said for the vane type disc. That is, in this method, it is insufficient to obtain the target particle size efficiently in the pulverizing step. Conventional manufacturing methods using a rotor include Japanese Patent Application Laid-Open Nos. 50-121529, 50-121530, and 59-121.
Although disclosed in JP-A-203448 and the like, all of them are aimed at producing a cotton-like product, which is different from the present invention.
【0009】[0009]
【発明が解決しようとする課題】本発明は粉砕工程時に
発生する微粉や粗粒を低減することにより、従来の粉体
塗料の製造効率を大きく改善し、より低コストで且つ作
業環境に優れる粉体塗料を作る製造方法を提供すること
を目的とするものである。DISCLOSURE OF THE INVENTION The present invention significantly reduces the production efficiency of conventional powder coatings by reducing the fine powder and coarse particles generated during the pulverizing step, and reduces the cost and the working environment. It is an object of the present invention to provide a manufacturing method for producing a body paint.
【0010】[0010]
【課題を解決するための手段】本発明は、粉体塗料の製
造効率を大きく改善し、より低コストで且つ作業環境に
優れる粉体塗料を作る製造方法について研究した結果な
されたものである。すなわち、回転する回転子の上部に
設置した円筒体を通して溶融混練された粉体塗料樹脂組
成物を開口部より供給でき、その外周上に孔を有する磁
性材料をもって形成された打ち抜き金網を備えた回転子
と打ち抜き金網を加熱する加熱手段を有する粉体塗料の
製造装置において、回転する回転子に溶融混練された粉
体塗料樹脂組成物を供給することにより、径が1.0α
〜20.0α、長さが1.0α〜40.0α(但し、α
は得られる粉体塗料の平均粒径とする)の繊維状組成物
とし、次いでこれを任意の粉砕工程を用い、平均粒径が
αである粉体とすることで粉砕工程時に発生する微粉や
粗粒を低減することができ、従来の粉体塗料の製造効率
を大きく改善し、より低コストで且つ作業環境に優れる
粉体塗料を作る製造方法である。DISCLOSURE OF THE INVENTION The present invention has been made as a result of research on a method of producing a powder coating material which significantly improves the production efficiency of the powder coating material, is lower in cost, and has an excellent working environment. That is, a powder coating resin composition melt-kneaded can be supplied from an opening through a cylindrical body provided on an upper portion of a rotating rotor, and a rotary machine provided with a punched wire mesh formed of a magnetic material having holes on its outer periphery. In a powder coating manufacturing apparatus having a heating means for heating a core and a punched wire mesh, a diameter of 1.0α is supplied by supplying a powder coating resin composition melt-kneaded to a rotating rotor.
~ 20.0α, length 1.0α ~ 40.0α (however, α
Is the average particle size of the powder coating to be obtained), and then, using any pulverization process, and then forming a powder having an average particle size of α, the fine powder generated during the pulverization process This is a production method for producing a powder coating which can reduce coarse particles, greatly improve the production efficiency of conventional powder coatings, and is lower in cost and excellent in working environment.
【0011】本発明における溶融混練された粉体塗料樹
脂組成物とは、従来の乾式工程における冷却工程直前の
ものを意味する。すなわち、樹脂、硬化剤、充填材、顔
料、その他添加剤などの各種原料をドライブレンドし、
2軸押出機等の加熱混練機により溶融、均一分散体とな
ったなったものである。樹脂の種類は限定されるもので
はなく、エポキシ樹脂、エポキシ−ポリエステル樹脂、
ポリエステル樹脂、アクリル樹脂、アクリル−ポリエス
テル樹脂、ポリイミド等の熱硬化性樹脂、およびポリ塩
化ビニル、ポリエチレン、ポリアミド、フッ素系樹脂等
の熱可塑性樹脂あるいはこれらの変性系、混合系のいず
れも適応される。硬化剤は樹脂に応じて選ばれる。熱膨
張率の低下や衝撃性向上のためにシリカ粉末、炭酸カル
シウム粉末、タルク粉末、マグネシア粉末、木粉等の充
填剤や必要に応じ顔料、カップリング剤、レベリング剤
等の添加剤を配合することができる。The melt-kneaded powder coating resin composition of the present invention means a resin composition immediately before a cooling step in a conventional dry process. That is, various raw materials such as resin, curing agent, filler, pigment, and other additives are dry-blended,
It was melted by a heating kneader such as a twin screw extruder to form a uniform dispersion. The type of resin is not limited, epoxy resin, epoxy-polyester resin,
Thermosetting resins such as polyester resin, acrylic resin, acryl-polyester resin, and polyimide, and thermoplastic resins such as polyvinyl chloride, polyethylene, polyamide, and fluorine-based resin, or modified or mixed systems thereof are all applicable. . The curing agent is selected according to the resin. Add fillers such as silica powder, calcium carbonate powder, talc powder, magnesia powder, wood powder, etc., and add additives such as pigments, coupling agents, leveling agents, etc. as necessary to reduce the coefficient of thermal expansion and improve impact resistance. be able to.
【0012】本発明によれば、その外周上に孔を有する
磁性材料をもって形成された打ち抜き金網を備えた回転
子と打ち抜き金網上部に設置した励磁コイルに交流電源
を通電させることにより、打ち抜き金網を加熱する粉体
塗料の製造装置において、回転する回転子の上部に設置
した円筒体を通して溶融混練された粉体塗料樹脂組成物
を開口部より供給し、加熱された打ち抜き金網と接触す
ることにより、樹脂の溶融粘度が低下するため遠心力で
飛散させることで容易に微粒子あるいは繊維状物とする
ことができ、粉砕工程時に発生する微粉や粗粒を低減で
きる粉体塗料の製造方法が提供できる。According to the present invention, the punched wire mesh is formed by applying an AC power supply to a rotor having a punched wire mesh formed of a magnetic material having a hole on the outer periphery thereof and an exciting coil provided on the upper portion of the punched wire mesh. In the apparatus for manufacturing the powder coating to be heated, the powder coating resin composition melt-kneaded is supplied from the opening through the cylindrical body installed on the upper part of the rotating rotor, and is brought into contact with the heated punched wire mesh, Since the melt viscosity of the resin decreases, fine particles or fibrous materials can be easily formed by scattering the resin by centrifugal force, and a method for producing a powder coating material that can reduce fine powder and coarse particles generated during the pulverizing step can be provided.
【0013】次に本発明の一例を図面にて説明する。第
1図に本発明の粉体塗料の製造方法を実施するための概
略図、第2図に回転子及び励磁コイル、第3図に回転子
の上部に設置する円筒体を示す。二軸押出機7で溶融混
練された樹脂は内壁と外壁の間に冷媒を通し冷却された
円筒体4を通して回転子1に供給される。この時、円筒
体4が冷却されていない場合には、樹脂が円筒体の壁に
付着しやすく、安定した樹脂の供給が困難となり好まし
くない。回転子1はモーター8と接続されており、任意
の回転数で回転させることができる。回転子の外周上に
設置した上部に設置した孔を有する磁性材料をもって形
成された打ち抜き金網2はその上部に備えられた励磁コ
イル3に交流電源を通電させることによって発生する交
番磁束の通過に伴う、うず電流損やヒステリシス損によ
り発熱する。なお、この磁性材料は例えば鉄材や珪素鋼
等があげられ、1種類あるいは2種類以上の磁性材料を
複合して使用することができる。樹脂は回転子供給後、
遠心力により加熱された打ち抜き金網2に飛行移動す
る。Next, an example of the present invention will be described with reference to the drawings. FIG. 1 is a schematic view for carrying out the method for producing a powder coating material of the present invention, FIG. 2 shows a rotor and an exciting coil, and FIG. 3 shows a cylinder installed on the rotor. The resin melt-kneaded in the twin-screw extruder 7 is supplied to the rotor 1 through the cooled cylindrical body 4 through a coolant between the inner wall and the outer wall. At this time, if the cylindrical body 4 is not cooled, the resin easily adheres to the wall of the cylindrical body, and it is difficult to supply a stable resin, which is not preferable. The rotor 1 is connected to a motor 8 and can be rotated at an arbitrary rotation speed. The punched wire mesh 2 formed of a magnetic material having a hole provided on the upper portion thereof provided on the outer periphery of the rotor is accompanied by the passage of an alternating magnetic flux generated when an AC power supply is supplied to an exciting coil 3 provided on the upper portion. , Heat is generated due to eddy current loss and hysteresis loss. The magnetic material is, for example, an iron material or silicon steel, and one or two or more magnetic materials can be used in combination. After the resin is supplied to the rotor,
It flies to the punched wire net 2 heated by the centrifugal force.
【0014】加熱された打ち抜き金網2に接触した樹脂
は溶融粘度が低下し、容易に打ち抜き金網2の孔を通過
し吐出される。加熱する温度は、適用する樹脂の特性に
より任意に設定することができる。熱硬化性樹脂を用い
る場合は、加熱温度を上げすぎると樹脂の硬化が進み特
性の劣化や打ち抜き金網2の孔で堆積が進むことがある
が、適当な温度条件の場合においては、樹脂と打ち抜き
金網2の接触時間が極めて短いために特性への影響は極
めて少ない。吐出された繊維状組成物は回転子1の周囲
に設置した外槽6で捕集される。外槽6の内径は小さす
ぎると繊維状組成物が十分冷却されないために内壁への
付着や、樹脂同士の融着が生じる恐れがあるため、好ま
しくない。一般には、回転子の回転により空気の流れが
生じ、冷却効果が得られるが必要に応じて冷風を導入し
たり、外槽をチラー等で冷却しても良い。外槽の大きさ
は、例えば回転子の直径が20cmの場合、内径は60
cmあれば付着や融着を防ぐことができる。The resin that has come into contact with the heated wire mesh 2 has a reduced melt viscosity and is easily discharged through the holes of the wire mesh 2. The heating temperature can be set arbitrarily according to the characteristics of the applied resin. In the case of using a thermosetting resin, if the heating temperature is too high, the curing of the resin may proceed, and the properties may be deteriorated or the deposition may proceed in the holes of the punched wire netting 2. Since the contact time of the wire mesh 2 is extremely short, the influence on the characteristics is extremely small. The discharged fibrous composition is collected in an outer tank 6 provided around the rotor 1. If the inner diameter of the outer tub 6 is too small, the fibrous composition is not sufficiently cooled, so that there is a possibility that the fibrous composition may adhere to the inner wall or cause fusion between the resins, which is not preferable. Generally, the rotation of the rotor generates a flow of air to provide a cooling effect. However, if necessary, cool air may be introduced, or the outer tank may be cooled by a chiller or the like. For example, when the diameter of the rotor is 20 cm, the inner diameter is 60 mm.
cm can prevent adhesion and fusion.
【0015】得られる粉体塗料の平均粒径をαとする
と、捕集される繊維状組成物の径は1.0α〜20.0
α、長さが1.0α〜40.0αに調整される。繊維径
及び繊維長は溶融粉体塗料樹脂組成物の供給速度、溶融
粘度や回転子の回転速度、及び打ち抜き金網の孔径、加
熱温度で調整される。繊維状組成物の径が20.0α以
上もしくは繊維長さが40.0αの場合、後の粉砕工程
で発生する微粉や粗粒の低減効果が少なく生産性の向上
や作業環境の改善が十分得られない。Assuming that the average particle size of the obtained powder coating is α, the diameter of the collected fibrous composition is 1.0α to 20.0
α and the length are adjusted to 1.0α to 40.0α. The fiber diameter and fiber length are adjusted by the supply speed of the molten powder coating resin composition, the melt viscosity, the rotation speed of the rotor, the hole diameter of the punched wire mesh, and the heating temperature. When the diameter of the fibrous composition is 20.0α or more or the fiber length is 40.0α, the effect of reducing fine powder and coarse particles generated in the subsequent pulverization process is small and the productivity and work environment can be sufficiently improved. I can't.
【0016】繊維状組成物の粉砕には、任意の粉砕工程
を用いる事ができる。ボールミル、ビクトリーミル、ジ
ェットミル、パルペライザー等いずれの方式も適用可能
である。ついで、ミクロンセパレーター、サイクロン、
ターボスクリーナー、篩い等の分級機により微粉や粗粒
を除去し目標の粒度分布を有する粉体塗料を得る。本発
明により得られた粉体塗料は、粉砕工程で発生する微粉
や粗粒が少ないため、分級工程が省略できるかまたは、
省力化ができる。For the pulverization of the fibrous composition, any pulverization step can be used. Any system such as a ball mill, a Victory mill, a jet mill, and a pulperizer can be applied. Then, micron separator, cyclone,
Fine powder and coarse particles are removed by a classifier such as a turbo screener or a sieve to obtain a powder coating having a target particle size distribution. The powder coating obtained by the present invention has a small amount of fine powder and coarse particles generated in the pulverizing step, or the classification step can be omitted or
Labor saving can be achieved.
【0017】[0017]
【実施例】本発明を実施例により更に詳しく説明する。 《実施例1》 ビスフェノールA型エポキシ樹脂(エポ
キシ当量850)5kg、結晶シリカ粉末5kg、2−
メチルイミダゾール0.06kg、レベリング剤0.0
2kgをヘンシェルミキサーでブレンド後、二軸押出機
にて溶融混練し、120℃の溶融粉体塗料樹脂組成物と
した。これを1.2mmの孔径を有し、励磁コイルで1
20℃に加熱した打ち抜き金網を備えた直径13cmで
3000r.p.mで回転している回転子に供給し、平
均繊維径500μm、平均繊維長1.2mmの繊維状組
成物を得た。これをパルペライザーにて4000回転で
粉砕したところ、5μm以下の微粉および200μm以
上の粗粒を含まない平均粒径70μmの粉体塗料を得
た。EXAMPLES The present invention will be described in more detail with reference to Examples. << Example 1 >> 5 kg of bisphenol A type epoxy resin (epoxy equivalent: 850), 5 kg of crystalline silica powder, 2-
Methyl imidazole 0.06 kg, leveling agent 0.0
After blending 2 kg with a Henschel mixer, the mixture was melt-kneaded with a twin-screw extruder to obtain a 120 ° C. molten powder coating resin composition. This has a hole diameter of 1.2 mm,
13 cm diameter and 3000 r.p. with punched wire mesh heated to 20 ° C. p. m, and a fibrous composition having an average fiber diameter of 500 μm and an average fiber length of 1.2 mm was obtained. This was pulverized at 4000 revolutions with a pulperizer to obtain a powder coating material having an average particle size of 70 μm containing no fine powder of 5 μm or less and coarse particles of 200 μm or more.
【0018】《実施例2》 実施例1で得た120℃の
溶融粉体塗料樹脂組成物を0.6mmの孔径を有し、励
磁コイルで120℃に加熱した打ち抜き金網を備えた直
径13cmで3000r.p.mで回転している回転子
に供給し、平均繊維径270μm、平均繊維長1.0m
mの繊維状組成物を得た。これをパルペライザーにて4
000回転で粉砕したところ、10μm以下の微粉およ
び180μm以上の粗粒を含まない平均粒径65μmの
粉体塗料を得た。Example 2 The resin composition for molten powder coating at 120 ° C. obtained in Example 1 had a hole diameter of 0.6 mm and had a diameter of 13 cm provided with a punched wire mesh heated to 120 ° C. by an exciting coil. 3000r. p. m, the average fiber diameter is 270 μm, and the average fiber length is 1.0 m.
m of a fibrous composition was obtained. This is pulperizer 4
When pulverized at 000 rotations, a powder coating material having an average particle size of 65 μm containing no fine powder of 10 μm or less and coarse particles of 180 μm or more was obtained.
【0019】《比較例1》 ビスフェノールA型エポキ
シ樹脂(エポキシ当量850)5kg、結晶シリカ粉末
5kg、2−メチルイミダゾール0.06kg、レベリ
ング剤0.02kgをヘンシェルミキサーでブレンド
後、二軸押出機にて溶融混練した。クーリングベルトで
冷却後、ハンマーミルにて粗粉砕を行い平均粒径800
μm、粒度分布40μm〜10mmの粗粉砕物を得た。
これをパルペライザーにて4000回転で粉砕したとこ
ろ、10μm以下の微粉を11wt%および180μm
以上の粗粒を8%含んだ平均粒径70μmの粉体塗料を
得た。Comparative Example 1 5 kg of a bisphenol A type epoxy resin (epoxy equivalent: 850), 5 kg of crystalline silica powder, 0.06 kg of 2-methylimidazole and 0.02 kg of a leveling agent were blended with a Henschel mixer, and then mixed with a twin screw extruder. And melt-kneaded. After cooling with a cooling belt, coarse grinding is performed with a hammer mill and the average particle size is 800
A coarsely pulverized product having a particle size distribution of 40 μm to 10 mm was obtained.
This was pulverized at 4000 revolutions with a pulperizer. Fine powder of 10 μm or less was obtained at 11 wt% and 180 μm.
A powder coating material having an average particle size of 70 μm containing 8% of the above coarse particles was obtained.
【0020】[0020]
【発明の効果】 本発明における粉体塗料の製造方法で
は、製品の目標粒度に近い小さな粒径でかつ、粒度分布
の狭い繊維組成物を安定して得ることができるため、粉
砕工程で微粉や粗粒の発生を低減することが可能とな
る。つまり、分級工程の削減あるいは省力化に伴う生産
性の向上および作業環境の改善を行うことができる。EFFECTS OF THE INVENTION In the method for producing a powder coating according to the present invention, a fiber composition having a small particle size close to the target particle size of the product and having a narrow particle size distribution can be stably obtained. The generation of coarse particles can be reduced. That is, it is possible to improve the productivity and the working environment due to the reduction of the classification process or labor saving.
【図1】本発明の粉体塗料製造方法を実施するための、
樹脂の溶融混練から繊維状生成物製造までの一例であ
る。FIG. 1 illustrates a method for producing a powder coating according to the present invention.
It is an example from melt kneading of a resin to production of a fibrous product.
【図2】本発明に使用する回転子及び励磁コイルの断面
図の一例である。FIG. 2 is an example of a sectional view of a rotor and an exciting coil used in the present invention.
【図3】溶融混練された粉体塗料樹脂組成物を回転子に
導入する円筒体の断面図の一例である。FIG. 3 is an example of a cross-sectional view of a cylinder for introducing a melt-kneaded powder coating resin composition into a rotor.
1 回転子 2 打ち抜き金網 3 励磁コイル 4 円筒体 5 交流電源発生装置 6 外槽 7 二軸押出機 8 モーター DESCRIPTION OF SYMBOLS 1 Rotor 2 Punched wire mesh 3 Excitation coil 4 Cylindrical body 5 AC power generator 6 Outer tank 7 Twin screw extruder 8 Motor
Claims (3)
を通して溶融混練された粉体塗料樹脂組成物を開口部よ
り供給でき、その外周上に孔を有する磁性材料をもって
形成された打ち抜き金網を備えた回転子と打ち抜き金網
を加熱する加熱手段を有する粉体塗料の製造装置におい
て、回転する回転子に溶融混練された粉体塗料樹脂組成
物を供給することにより、径が1.0α〜20.0α、
長さが1.0α〜40.0α(但し、αは得られる粉体
塗料の平均粒径とする)の繊維状組成物とし、次いでこ
れを任意の粉砕工程を用い、平均粒径がαである粉体と
することを特徴とする粉体塗料の製造方法。1. A punched wire mesh formed of a magnetic material having a hole on its outer periphery, through which a powder coating resin composition melt-kneaded can be supplied from an opening through a cylindrical body provided above a rotating rotor. In a powder coating manufacturing apparatus having a rotor provided with a heating means for heating a punched wire mesh, a diameter of 1.0α to 20 is supplied by supplying a powder coating resin composition melt-kneaded to a rotating rotor. .0α,
A fibrous composition having a length of 1.0α to 40.0α (where α is the average particle diameter of the obtained powder coating material) is used, and then this is subjected to an optional pulverization step to obtain an average particle diameter of α. A method for producing a powder coating, wherein the method is to form a certain powder.
であり、内壁と外壁の間に冷媒を通すことにより円筒体
を冷却できる請求項1記載の粉体塗料の製造方法。2. The method for producing a powder coating according to claim 1, wherein the cylindrical body installed on the upper part of the rotor is a double tube type, and the cylindrical body can be cooled by passing a refrigerant between the inner wall and the outer wall.
もって形成された打ち抜き金網は、その上部に備えられ
た励磁コイルに交流電源を通電させることによって加熱
できる請求項1記載の粉体塗料の製造方法。3. The powder coating according to claim 1, wherein the punched wire mesh formed of a magnetic material having a hole on the outer periphery of the rotor can be heated by supplying an AC power supply to an exciting coil provided on the upper portion thereof. Manufacturing method.
Priority Applications (1)
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---|---|---|---|
JP17132097A JP3556075B2 (en) | 1997-06-27 | 1997-06-27 | Powder coating manufacturing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17132097A JP3556075B2 (en) | 1997-06-27 | 1997-06-27 | Powder coating manufacturing method |
Publications (2)
Publication Number | Publication Date |
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JPH1112498A true JPH1112498A (en) | 1999-01-19 |
JP3556075B2 JP3556075B2 (en) | 2004-08-18 |
Family
ID=15921068
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JP17132097A Expired - Fee Related JP3556075B2 (en) | 1997-06-27 | 1997-06-27 | Powder coating manufacturing method |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007270043A (en) * | 2006-03-31 | 2007-10-18 | Hosokawa Funtai Gijutsu Kenkyusho:Kk | Powdered coating particle and method for producing the same |
WO2013024669A1 (en) * | 2011-08-15 | 2013-02-21 | 国立大学法人山梨大学 | Means for manufacturing microbeads comprising thermoplastic polymer microparticles |
JP2013072028A (en) * | 2011-09-28 | 2013-04-22 | Sumitomo Bakelite Co Ltd | Porous powder coating particle, method of manufacturing the same, and epoxy resin powder coating composition |
-
1997
- 1997-06-27 JP JP17132097A patent/JP3556075B2/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007270043A (en) * | 2006-03-31 | 2007-10-18 | Hosokawa Funtai Gijutsu Kenkyusho:Kk | Powdered coating particle and method for producing the same |
WO2013024669A1 (en) * | 2011-08-15 | 2013-02-21 | 国立大学法人山梨大学 | Means for manufacturing microbeads comprising thermoplastic polymer microparticles |
US9731260B2 (en) | 2011-08-15 | 2017-08-15 | University Of Yamanashi | Means for manufacturing micro-beads comprising thermoplastic polymer micro-particles |
JP2013072028A (en) * | 2011-09-28 | 2013-04-22 | Sumitomo Bakelite Co Ltd | Porous powder coating particle, method of manufacturing the same, and epoxy resin powder coating composition |
Also Published As
Publication number | Publication date |
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JP3556075B2 (en) | 2004-08-18 |
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