JP4421349B2 - Powder feeder - Google Patents

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JP4421349B2
JP4421349B2 JP2004104108A JP2004104108A JP4421349B2 JP 4421349 B2 JP4421349 B2 JP 4421349B2 JP 2004104108 A JP2004104108 A JP 2004104108A JP 2004104108 A JP2004104108 A JP 2004104108A JP 4421349 B2 JP4421349 B2 JP 4421349B2
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powder
air
fluid tank
supply apparatus
tank
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JP2005288236A (en
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晴久 海住
研二 堀田
真也 奥村
多門 郡司
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Asahi Sunac Corp
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Description

この発明は、粉末、特に、10μm以下の微粉末を、塊(ブツ)のない状態で均一に取出して散布装置に供給することができる粉末供給装置に関するものである。   The present invention relates to a powder supply apparatus that can uniformly take out powder, particularly fine powder of 10 μm or less, without lump and supply it to a spraying apparatus.

静電塗装装置は、図4に示すように、粉末塗料14を、底面の多孔板12から流動エアーが供給される流動タンク11内に収容し、流動タンク11内で粉末塗料をほぐし、インジェクター15の吸引管13を流動タンク11内の粉末塗料14の蓄積層に差し入れて、粉末塗料14を静電ガン16に吸引搬送することにより、被塗物Aに粉末塗料14を散布するようにしている。
このような静電塗装装置では、粉末塗料の塊(ブツ)のない平滑な塗膜の形成が要求され、特許文献1には、粉末塗料の粒度を均一に揃えて均一な塗膜を得る技術も開示されている。
As shown in FIG. 4, the electrostatic coating apparatus accommodates the powder paint 14 in a fluid tank 11 to which fluid air is supplied from the bottom porous plate 12, loosens the powder paint in the fluid tank 11, and injectors 15. The suction pipe 13 is inserted into the accumulation layer of the powder paint 14 in the fluid tank 11, and the powder paint 14 is sucked and conveyed to the electrostatic gun 16 so that the powder paint 14 is sprayed on the article A to be coated. .
In such an electrostatic coating apparatus, formation of a smooth coating film without powder coating lump is required, and Patent Document 1 discloses a technique for obtaining a uniform coating film by uniformizing the particle size of the powder coating material. Is also disclosed.

特開2002−113409号公報JP 2002-113409 A

ところで、近年は、粉末塗料の微粉化により、塗膜の美肌性がより要求されるようになっている。
ところが、粉末が微粉化すればするほど、流動タンク内で粉末が流動し難く、粉末同士がくっついて、塊が生じ易く、アルミナ粉やシリカ粉等の10μm以下の微粉末の場合には、流動タンク内で流動エアーが底から供給されても、あたかも粉末層が水が底面に淀んだような状態になっている。
特に、1μm以下のアルミナ粉のような場合には、流動タンク内で流動はおろか、自然放置によって、すぐに塊が生じて被塗物の表面にブツが発生しやすい。
このような場合に、底面からの流動エアーを強くして、流動タンク内の粉末を流動させようとしても、淀んだ底面の粉末層に、ブツブツとエアーの抜け穴が開く状態になるだけで、流動性は改善され難い。
By the way, in recent years, the fine skin of the powder coating has been demanded more beautiful skin.
However, the finer the powder is, the more difficult it is to flow in the fluid tank, the powders stick together, more likely to form lumps, and in the case of a fine powder of 10 μm or less such as alumina powder or silica powder, Even if fluid air is supplied from the bottom in the tank, it is as if the powder layer is filled with water on the bottom.
In particular, in the case of alumina powder having a size of 1 μm or less, not only does it flow in the fluid tank, but it naturally forms lumps and is easily generated on the surface of the object to be coated.
In such a case, even if you try to strengthen the flowing air from the bottom and flow the powder in the fluid tank, it will only flow in the state where the powder layer on the stagnated bottom is open with air holes. Sex is difficult to improve.

そこで、この発明は、微粉末であっても、流動タンク内から粉末を塊のない状態で引き出すことができ、被塗物に均一な散布が行える粉末供給装置を提供しようとするものである。   Therefore, the present invention is intended to provide a powder supply apparatus that can draw out powder from a fluid tank without a lump even if it is a fine powder, and that can be uniformly dispersed on an object to be coated.

この発明は、粉末を収容し、底面から流動エアーが供給される流動タンクの上部に、粉末取出し口を設け、上記流動タンクの底面に溜まる粉末層内に埋まる高さ位置に、粉末を舞い上がらせて霧化状態にするエアー噴出手段を設け、上記粉末取出し口から霧化状態の粉末を流動タンク内のエアー圧により取出すようにしたものである。   According to the present invention, a powder take-out port is provided at the top of a fluid tank that contains powder and is supplied with fluid air from the bottom surface, and the powder is raised to a height position embedded in the powder layer accumulated on the bottom surface of the fluid tank. An air jetting means for making the atomized state is provided, and the atomized powder is taken out from the powder take-out port by the air pressure in the fluid tank.

エアー噴出手段としては、流動タンクの内周壁に沿って配置されたエアーチューブに、複数のエアー噴出孔やエアー噴出スリットを形成したものを使用することができる。
このエアー噴出孔やエアー噴出スリットから噴出されるエアーは、流動タンクの底面の流動エアーに対して交わるように供給され、これにより流動タンクの底面に溜まる粉末がモクモクと舞い上がって霧化状態になり、流動タンク内に供給されるエアー量に応じて流動タンク内のエアー圧が上昇し、流動タンク内のエアー圧によって流動タンクの粉末取出し口から霧化状態で粉末を取出すことが可能となる。
As the air ejection means, it is possible to use a plurality of air ejection holes and air ejection slits formed on an air tube disposed along the inner peripheral wall of the fluid tank.
The air ejected from the air ejection holes and the air ejection slits is supplied so as to intersect with the flowing air on the bottom surface of the fluid tank, and as a result, the powder accumulated on the bottom surface of the fluid tank rises and becomes atomized. The air pressure in the fluid tank rises in accordance with the amount of air supplied into the fluid tank, and the air pressure in the fluid tank can take out the powder in an atomized state from the powder outlet of the fluid tank.

また、霧化状態の粉末が充満する流動タンクの上部にも、流動タンクの底面の粉末層内に設置するエアー噴出手段と同様の第二のエアー噴出手段を設けることにより、微粉末をさらに塊のない状態にすることができる。   Further, by providing a second air ejection means similar to the air ejection means installed in the powder layer on the bottom surface of the fluid tank at the top of the fluid tank filled with the atomized powder, the fine powder is further agglomerated. It can be in a state without.

そして、流動タンクの粉末取出し口に、エアー搬送を行うインジェクター装置を設けて、散布装置に粉末を搬送するようにしてもよいが、流動タンクの粉末取出し口からは霧化状態の粉末がモクモクと流出するため、そのまま散布装置に塊のない粉末を供給することができる。   Then, an injector device that performs air conveyance may be provided at the powder extraction port of the fluid tank, and the powder may be conveyed to the spraying device. Since it flows out, the powder without a lump can be supplied to a spreading device as it is.

上記のように、この発明によれば、霧化状態の塊のない粉末を被塗物に供給できるので、特に、10μm以下の微粉末であっても、極めてブツの少ない均一な塗膜の形成が可能になる。   As described above, according to the present invention, since the powder without atomized lump can be supplied to the object to be coated, even with a fine powder of 10 μm or less, it is possible to form a uniform coating film with extremely few irregularities. Is possible.

図1は、この発明に係る粉末供給装置の第一の実施形態を示す概略図である。
流動タンク1は、内径が400mmの円筒形で、多孔板で形成された内底板2を有し、内底板2の下面側から流動エアー3がタンク内に流入するようになっており、タンク内に収容されている内底板2上に溜まった粉末層4を、流動エアー3によって固まらないようにしている。
FIG. 1 is a schematic view showing a first embodiment of a powder supply apparatus according to the present invention.
The fluid tank 1 has a cylindrical shape with an inner diameter of 400 mm and has an inner bottom plate 2 formed of a perforated plate, and fluid air 3 flows into the tank from the lower surface side of the inner bottom plate 2. The powder layer 4 accumulated on the inner bottom plate 2 accommodated in the container is prevented from being hardened by the flowing air 3.

上記流動タンク1内には、内底板2上に溜まった粉末層4に埋まる高さ位置に、粉末を舞い上がらせて霧化状態にするエアー噴出手段5を設けている。このエアー噴出手段5は、
タンクの内面に沿うように設置した2本のエアーチューブに、流動エアーに交わるように、エアーを噴出する複数のエアー噴出孔5aを設けたものであり、流動エアーに交わる噴出エアーにより、粉末層4の粉末がモクモクと舞い上がって霧化状態の粉末になる。
In the fluid tank 1, air jetting means 5 is provided at a height position buried in the powder layer 4 accumulated on the inner bottom plate 2 so as to cause the powder to rise to an atomized state. This air jetting means 5
The two air tubes installed along the inner surface of the tank are provided with a plurality of air ejection holes 5a for ejecting air so as to intersect with the flowing air. By the ejecting air intersecting with the flowing air, the powder layer No. 4 powder soars and becomes atomized powder.

この実施形態では、エアーチューブとして8φの径のものを使用し、エアー噴出孔は直径0.5mmで、30mmの等間隔で開けられている。   In this embodiment, an air tube having a diameter of 8φ is used, and the air ejection holes are 0.5 mm in diameter and are opened at equal intervals of 30 mm.

また、霧化状態の粉末が充満する流動タンク1の上部にも、エアー噴出手段5と同様のエアー噴出手段6が内面に沿うように設置している。エアー噴出手段6は、タンクの内面に沿うように設置したエアーチューブに、エアーを噴出する複数のエアー噴出孔6aを設けたものであり、このエアー噴出手段6の噴出エアーによって、霧化状態の粉末がさらに分散化され、粉末の塊の形成を防止できる。   In addition, an air ejection means 6 similar to the air ejection means 5 is also installed along the inner surface of the fluid tank 1 filled with the atomized powder. The air jetting means 6 is provided with a plurality of air jetting holes 6a for jetting air on an air tube installed along the inner surface of the tank. The powder is further dispersed to prevent the formation of a lump of powder.

上記エアー噴出手段5、6のエアーチューブは、タンクの内面に沿って設けることが好ましいが、その位置は中央よりの位置でもよい。   The air tubes of the air ejection means 5 and 6 are preferably provided along the inner surface of the tank, but the position may be a position from the center.

上記流動タンク1の上部には、粉末取出し口7が設置され、流動エアーと、エアー噴出手段5、6からのエアー流入量に応じて流動タンク1内のエアー圧が上昇し、粉末取出し口7から霧化状態の粉末が流動タンク1外にモクモクと流出する。   In the upper part of the fluid tank 1, a powder outlet 7 is installed, and the air pressure in the fluid tank 1 rises according to the flowing air and the amount of air inflow from the air ejection means 5, 6. From the fluidized tank 1 flows out of the fluid tank 1.

流動タンク1外に流出した霧化状態の粉末は、ホース8を介して静電ガン9に搬送され、被塗物Aに散布される。   The atomized powder that has flowed out of the fluid tank 1 is conveyed to the electrostatic gun 9 via the hose 8 and dispersed on the article A to be coated.

この第一実施形態の粉体供給装置を使用して、平均粒径1μmのアルミナ粉の散布実験を行った。
エアー噴出手段5、6からのエアーを噴出させない状態で、底面の流動エアーのみを流動タンク1内に供給したところ、エアー圧が0.1Mpaでも粉末層4は、底面に水が淀んだような状態のままであった。このエアー圧をさらに上昇させたところ、粉末層4に針状のエアー孔が多数できるだけで、粉末層4は、水が静止したような状態のままであり、粉末取出し口7からの粉末の流出はなく、静電ガン9によって被塗物Aに粉末を散布することができなかった。
次に、エアー噴出手段5、6から0.1Mpa〜0.15Mpaのエアー圧でエアーを噴出させたところ、次第に粉末層4の流動状態が活発になり、粉末層4の粉末がモクモクと霧状に舞い上がり、流動タンク1内が霧状の粉末で充満し、流動タンク1内のエアー圧により粉末取出し口7から霧化状態の粉末が流動タンク1外に流出し、そのままホース8を介して静電ガン9に搬送して被塗物Aに粉末の散布が行えた。
このようにして散布した被塗物Aの塗膜を目視で確認したところ、被塗物Aの塗膜に残るブツの発生が、表1の通り、エアー噴出手段5、6からのエアーの噴出量に応じて少なくなっていた。
なお、表1は、流動エアーとエアー噴出手段5、6からのエアーの設定を、200mmH×300mmLの被塗物Aに対し、目標付着量を50mmgにして行い、その10回の平均値を示したものである。
Using the powder supply apparatus according to the first embodiment, a dispersion experiment of alumina powder having an average particle diameter of 1 μm was performed.
When only air from the bottom surface is supplied into the fluid tank 1 without air from the air ejection means 5 and 6, the powder layer 4 seems to have water on the bottom surface even at an air pressure of 0.1 Mpa. The state remained. When this air pressure is further increased, the powder layer 4 can only have a large number of needle-like air holes, and the powder layer 4 remains in a state where water is stationary, and the powder flows out from the powder outlet 7. No, the powder could not be sprayed on the article A to be coated by the electrostatic gun 9.
Next, when air was ejected from the air ejection means 5 and 6 at an air pressure of 0.1 Mpa to 0.15 Mpa, the flow state of the powder layer 4 gradually became active, and the powder of the powder layer 4 became muddy and misty. The fluid tank 1 is filled with mist-like powder, and the air pressure in the fluid tank 1 causes the atomized powder to flow out of the fluid tank 1 through the hose 8 as it is. It was conveyed to the electric gun 9 and powder could be sprayed on the article A to be coated.
As a result of visually confirming the coating film of the object A spread as described above, the occurrence of scum remaining on the coating film of the object A is as shown in Table 1 and the ejection of air from the air ejection means 5 and 6 It was decreasing according to the amount.
Table 1 shows the average value of 10 times when the setting of flowing air and air from the air jetting means 5 and 6 is performed with the target adhesion amount set to 50 mmg for the object A of 200 mmH × 300 mmL. It is a thing.

Figure 0004421349
Figure 0004421349

次に、表2は、エアー噴出手段5、6として、8φの径のエアーチューブに、0.3mmのカッターでチューブ長に垂直に縦に5mmのエアー噴出スリットを入れたものを使用した。   Next, Table 2 used air jetting means 5 and 6 having an 8 mm diameter air tube with a 0.3 mm cutter and a vertical 5 mm air jet slit perpendicular to the tube length.

そして、粉末は、ポリエステル系粉体塗料の3回リサイクル回収粉で、粒径が5μm以下のものが55%含むものを使用した。   The powder used was a three-time recycled powder of a polyester powder coating material containing 55% having a particle size of 5 μm or less.

なお、表2は、流動エアーとエアー噴出手段5、6からのエアーの設定を、200mmH×300mmLの被塗物Aに対し、膜厚30μmの目標付着量にして行い、その10回の平均値を示した。   In Table 2, the setting of flowing air and air from the air jetting means 5 and 6 is performed with a target adhesion amount of 30 μm thickness on the object A of 200 mmH × 300 mmL, and the average value of 10 times showed that.

Figure 0004421349
Figure 0004421349

上記の実施形態では、いずれも霧化状態の粉末を、流動タンク1内に供給するエアー圧によってそのまま静電ガン9まで搬送するようにしたが、図2に示すように、粉末取出し口7に、インジェクター10を設置し、インジェクター10による強制吸引によって静電ガン9まで粉末を圧送するようにしてもよいが、この場合、図3に示すように、インジェクター10の内部に粉末の塊(ブツ)Bができやすい。   In the above embodiment, the atomized powder is conveyed to the electrostatic gun 9 as it is by the air pressure supplied into the fluid tank 1, but as shown in FIG. The injector 10 may be installed, and the powder may be pumped to the electrostatic gun 9 by forced suction by the injector 10, but in this case, as shown in FIG. B is easy.

(a)はこの発明の第一の実施形態の概略図、(b)はエアーチューブの平面図である。(A) is the schematic of 1st embodiment of this invention, (b) is a top view of an air tube. この発明の第二の実施形態の概略図である。It is the schematic of 2nd embodiment of this invention. 図2の実施形態のインジェクター部分の説明図である。It is explanatory drawing of the injector part of embodiment of FIG. 静電塗装装置の全体概略図である。It is the whole electrostatic coating apparatus schematic.

符号の説明Explanation of symbols

1 流動タンク
2 内底板
3 流動エアー
4 粉末層
5、6 エアー噴出手段
5a、6a エアー噴出孔
7 粉末取出し口
8 ホース
9 静電ガン
10 インジェクター
DESCRIPTION OF SYMBOLS 1 Fluid tank 2 Inner bottom board 3 Fluid air 4 Powder layer 5, 6 Air ejection means 5a, 6a Air ejection hole 7 Powder extraction port 8 Hose 9 Electrostatic gun 10 Injector

Claims (6)

粉末を収容し、底面から流動エアーが供給される流動タンクの上部に、粉末取出し口を設け、上記流動タンクの底面に溜まった粉末層内に埋まる高さ位置に、粉末を舞い上がらせて霧化状態にするエアー噴出手段を設け、上記粉末取出し口から霧化状態の粉末を流動タンク内のエアー圧により取出すことを特徴とする粉末供給装置。   A powder take-out port is provided in the upper part of the fluid tank that contains the powder and fluid air is supplied from the bottom. An apparatus for supplying powder, characterized in that an air jetting means is provided, and the atomized powder is taken out from the powder outlet by air pressure in a fluid tank. 流動タンクの内周壁に沿って配置されたエアーチューブに、複数のエアー噴出孔を形成して、上記エアー噴出手段を構成した請求項1記載の粉末供給装置。   The powder supply apparatus according to claim 1, wherein a plurality of air ejection holes are formed in an air tube arranged along the inner peripheral wall of the fluid tank to constitute the air ejection means. 流動タンクの内周壁に沿って配置されたエアーチューブに、複数のエアー噴出スリットを形成して、上記エアー噴出手段を構成した請求項1記載の粉末供給装置。   2. The powder supply apparatus according to claim 1, wherein a plurality of air ejection slits are formed in an air tube arranged along the inner peripheral wall of the fluid tank to constitute the air ejection means. 粉末流動タンク内の上部に、第二のエアー噴出手段を設けた請求項1〜3のいずれかの項に記載の粉末供給装置。   The powder supply apparatus according to any one of claims 1 to 3, wherein a second air blowing means is provided in an upper part of the powder flow tank. 流動タンクの粉末取出し口に、エアー搬送を行うインジェクター装置を設けた請求項1〜4のいずれかの項に記載の粉末供給装置。   The powder supply apparatus of any one of Claims 1-4 which provided the injector apparatus which performs air conveyance in the powder extraction opening of a fluid tank. 請求項1〜5のいずれかの項に記載の粉末供給装置によって粉末を取出して散布装置に供給する粉末塗装装置。   The powder coating apparatus which takes out powder with the powder supply apparatus in any one of Claims 1-5, and supplies it to a dispersion device.
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