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JP4173330B2 - Coating film drying apparatus and coating film drying method - Google Patents

Coating film drying apparatus and coating film drying method Download PDF

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Publication number
JP4173330B2
JP4173330B2 JP2002225870A JP2002225870A JP4173330B2 JP 4173330 B2 JP4173330 B2 JP 4173330B2 JP 2002225870 A JP2002225870 A JP 2002225870A JP 2002225870 A JP2002225870 A JP 2002225870A JP 4173330 B2 JP4173330 B2 JP 4173330B2
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JP
Japan
Prior art keywords
coating film
drying
web
gas
hot air
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.)
Expired - Fee Related
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JP2002225870A
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Japanese (ja)
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JP2004066042A (en
Inventor
秀樹 稲田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dai Nippon Printing Co Ltd
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Dai Nippon Printing Co Ltd
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Priority to JP2002225870A priority Critical patent/JP4173330B2/en
Publication of JP2004066042A publication Critical patent/JP2004066042A/en
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  • Application Of Or Painting With Fluid Materials (AREA)
  • Nozzles (AREA)
  • Coating Apparatus (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、被塗布物に形成した塗膜を乾燥する塗膜乾燥装置及び塗膜乾燥方法に関するものである。
【0002】
【従来の技術】
光学製品及び液晶関連部材等は、高精度に塗布し、乾燥する必要があるので、塗布がなされた後に、塗膜面を乱すことなく塗膜の乾燥が行われる必要がある。
そのために、ウェブの表面に形成された塗膜面の上から直接熱風を吹き付けられることのないように、ウェブの裏面から熱風を吹き付けて乾燥することによって塗膜面の乱れを防止する塗膜乾燥装置が使用される。
【0003】
図3は、従来の塗膜乾燥装置の構成及び動作を示す模式図である。
塗膜乾燥装置20は、コート部11と、乾燥炉22と、複数のロール13a〜13cと、を備えている。
【0004】
コート部11は、圧胴11aと、ブランケット胴11bと、版胴11cとを順に隣接して備えている。
乾燥炉22は、ウェブ下面給気ノズル24と、排気ノズル15と、を備えている。ウェブ下面給気ノズル24は、ウェブ16の下面近傍に設けられ、幅0.5〜5mm程度のスリット26をウェブ幅方向に渡って備えており、そのスリット26から熱風の給気が行われる。また、ウェブ下面給気ノズル24の幅は、塗膜面の幅方向全体を均一に乾燥するために、ウェブ幅より大きくするのが一般的である。排気ノズル15は、ウェブ16の下面でウェブ下面給気のノズル24から排出される熱風の流路に設けられ、乾燥に使用された熱風を乾燥炉22の外部へと排出するノズルである。
【0005】
ウェブ16は、ロール13aによって張力一定にされて、コート部11内へと走行して進入する。ウェブ16は、コート部11内に入ると、裏面が圧胴11aに巻きつけられ、表面が版胴11cから塗布液を移されたブランケット胴11bを介して塗布液を転写されて塗膜面を形成し、ロール13bで張力一定に保持されたまま矢印X方向に走行し、乾燥炉22内へと入る。
ウェブ16は、乾燥炉22内を走行する時に、ウェブ下面給気ノズル24から矢印B方向に吹き付けられる熱風によって浮上させられながら、ウェブ16の裏面から、ウェブ16の表面の塗膜面を乾燥される。
【0006】
【発明が解決しようとする課題】
図4は、図3の塗膜乾燥給気ノズルの構成及び熱風が塗膜上に回りこむ状況を示す拡大模式図である。
ウェブ下面給気ノズル24は、ウェブ16を浮上させるために、ウェブ16の幅に比べてウェブ下面給気ノズル24の幅を大きくされている。
しかし、ウェブ下面給気ノズル24の幅方向の両端部から吹き出した熱風が、ウェブ16上面の塗膜17の両端部に矢印Cのように回り込み、塗膜17の両端部が乱されるという問題がある。
【0007】
そこで、本発明の課題は、塗膜面を乱すことなく、かつ、乾燥効率を低下させることなく、塗膜の乾燥を行うことができる塗膜乾燥装置及び塗膜乾燥方法を提供することである。
【0010】
【課題を解決するための手段】
前記した課題を解決するために、請求項1に記載の発明は、被塗布物の走行面の下面に乾燥用気体を吹き付け、前記被塗布物を浮上させながら前記被塗布物の上面に塗布した塗膜を乾燥する塗膜乾燥装置であって、前記被塗布物の走行面の下面側に配置され、全面に多孔質部材を備える気体給気部(14b)を有し、前記乾燥用気体を給気する塗膜乾燥給気ノズル(14)を備え、前記乾燥用気体は、前記気体給気部を通過して前記被塗布物の走行面の下面に吹き付けられること、を特徴とする塗膜乾燥装置である。
【0011】
請求項に記載の発明は、被塗布物の走行面の下面に乾燥用気体を吹き付け、前記被塗布物を浮上させながら前記被塗布物の上面に塗布した塗膜を乾燥する乾燥工程を備えた塗膜乾燥方法であって、前記乾燥工程は、多孔質部材を通過した前記乾燥用気体を低い流体速度及び広い流体断面積で給気すること(14b)、を特徴とする塗膜乾燥方法である。
【0012】
【発明の実施の形態】
以下、図面を参照しながら、本発明の実施の形態を挙げて、詳細に説明する。
図1は、本発明の実施形態による塗膜乾燥給気ノズルを備えた塗膜乾燥装置の構成及び塗膜乾燥装置の動作を示す模式図である。
以下、前述した従来技術と同様の機能を果たす部分には、同一符号を付して、重複する説明を適宜省略する。
塗膜乾燥措置10は、被塗布物としてのウェブ16を塗工するコート部11と、塗工したウェブ16を乾燥する乾燥炉12と、ウェブ16を張力一定のまま走行させる複数のロール13a〜13cとを備えている。
【0013】
乾燥炉12は、内部に、ウェブ下面給気ノズル14と、排気ノズル15とを備えている。
ウェブ下面給気ノズル14は、ウェブ16の下面の近傍で、ウェブ16の進行方向に向かって、一定の間隔をおいて複数設けられたノズルである。また、ウェブ下面給気ノズル14は、その長手方向が、ウェブ16の進行方向と直交するように設けられている。
排気ノズル15は、気体給気部としてのウェブ下面給気ノズル14から排出された熱風を乾燥炉12の外部へと排出するノズルである。
【0014】
図2は、図1の塗膜乾燥給気ノズルの構成及び熱風の流路を示す拡大模式図である。
ウェブ下面給気ノズル14は、熱風ノズル14aと、熱風給気部14bと、から構成される。熱風給気部14bは、熱風ノズル14aの熱風出口の全面を覆い、多孔質部材を備えている。多孔質部材は、多孔質燒結体材料で構成される。
多孔質燒結体材料とは、粉末又は圧粉粒子を加熱して結合させ、内部に多数の細孔又は空げきを形成した材料をいう。
本実施形態では、多孔質燒結体材料としては、アルミニウム、亜鉛、銅等を用い、多孔の度合いを示す空げき率が50%以下、厚み3〜30mm、孔の大きさ0.1〜1mm、風速0.5〜20m/sのものを用いる。
【0015】
次に、本実施形態にかかるウェブ下面給気ノズル14による塗膜乾燥の動作について説明する。
ウェブ16は、図1で示すように、ロール13aに巻かれて張力一定のまま走行し、コート部11で塗工され、ロール13bを介して乾燥炉12内へと入る。
【0016】
ウェブ16は、乾燥炉12内に入ると、図2で示すように、熱風ノズル14a内を流れる乾燥用気体としての熱風が、熱風給気部14bを通過してウェブ16の裏面に吹き付けるので、ウェブ16の表面に塗布された塗膜17が乾燥されながら、図1及び図2の矢印X方向に走行する。
【0017】
熱風は、熱風給気部14bの多孔質燒結体材料を通過するときに、多孔が多孔質燒結体材料の内部で網目状に張り巡らされているために、網目の間を流動し、給気面の全面から熱風の給気が行われる。全面から給気されるので、広い流体断面積で給気される。
また、網目状の孔は、熱風給気部14bの内部で複雑に入り組んでいるため、熱風は、流動している途中で、流路の至る所で衝突する。給気面積が大きいため、給気量が多くても風速は小さくする。
このようにして、熱風は、低い流体速度で、広い流体断面積になって熱風供給部14bから吹き出し、ウェブ16の下面に矢印Aのように吹き付ける(乾燥工程)。
【0018】
本実施形態によれば、熱風給気部が多孔質燒結体材料を備えているので、低い流体速度及び広い流体断面積の熱風を導き出すことができる。
熱風が低い流体速度になるために、ウェブ幅よりも広い部分の給気面から吹き出されても、熱風は、ウェブ16の上面に回り込むことがなく、塗膜17の面、特に、塗膜17の面における幅方向の両端部は、乱されることがなく乾燥されるようになる。
また、熱風が広い流体断面積になるために、低風速でも広い面積のウェブを浮上させて乾燥することができる。
更に、熱風が広い流体断面積になるために、乾燥効率が低下することはなく、風速が低いことにより乾燥効率が悪くなることはない。
【0019】
(変形形態)
以上説明した実施形態に限定されることなく、種々の変形や変更が可能であって、それらも本発明の均等の範囲内である。
(1)本実施形態では、被塗布物としてウェブを使用したが、その他、枚葉紙等を使用してもよい。
【0020】
(2)本実施形態では、多孔質材料として多孔質燒結体材料を使用したが、多孔質材料であれば網又はハニカム状の細かな穴の空いたものでもよい。
【0021】
(3)本実施形態では、乾燥用気体として熱風を使用したが、乾燥に使用できる気体であれば、湿り度が0の気体又は吸湿性のある他の気体でもよい。
【0022】
(4)本実施形態では、気体給気部の全面を多孔質部材としているが、気体給気部の所定範囲に多孔質部材を使用するものでもよい。
【0023】
【発明の効果】
以上、詳しく説明したように、本発明によれば、以下のような効果がある。
(1)気体給気部は、乾燥用気体が通過する多孔質部材を備えているので、乾燥用気体を、多孔質部材によって低い流体速度に変化させて吹き出させることができる。
【0024】
(2)多孔質部材は、気体給気部の全面に備えられているので、気体給気部の一部に備えた場合よりも、乾燥用気体を広い流体断面積に変化させて吹き出させることができる。
【0025】
(3)乾燥用気体が多孔質材料で構成された気体給気部を通過して、被塗布物の下面に吹き付けられるので、塗膜面を乱すことなく、かつ、乾燥効率を低下させることなく、塗膜の乾燥を行うことができる。
【図面の簡単な説明】
【図1】本発明の実施形態による塗膜乾燥給気ノズルを備えた塗膜乾燥装置の構成及び塗膜乾燥装置の動作を示す模式図である。
【図2】図1の塗膜乾燥給気ノズルの構成及び熱風の流路を示す拡大模式図である。
【図3】従来の塗膜乾燥装置の構成及び動作を示す模式図である。
【図4】図3の塗膜乾燥給気ノズルの構成及び熱風が塗膜上に回りこむ状況を示す拡大模式図である。
【符号の説明】
14 ウェブ下面給気ノズル
14a 熱風ノズル
14b 熱風給気部
16 ウェブ
17 塗膜
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a coating film drying apparatus and film drying way to dry the coating film formed on the coating object.
[0002]
[Prior art]
Since optical products and liquid crystal related members need to be applied and dried with high accuracy, it is necessary to dry the coated film without disturbing the coated surface after being coated.
Therefore, coating film drying prevents the coating surface from being disturbed by blowing hot air from the back of the web and drying it so that it cannot be directly blown from the top of the coating formed on the surface of the web. The device is used.
[0003]
FIG. 3 is a schematic diagram showing the configuration and operation of a conventional coating film drying apparatus.
The coating film drying apparatus 20 includes a coat unit 11, a drying furnace 22, and a plurality of rolls 13a to 13c.
[0004]
The coat unit 11 includes an impression cylinder 11a, a blanket cylinder 11b, and a plate cylinder 11c adjacent to each other in order.
The drying furnace 22 includes a web lower surface air supply nozzle 24 and an exhaust nozzle 15. The web lower surface air supply nozzle 24 is provided near the lower surface of the web 16 and includes a slit 26 having a width of about 0.5 to 5 mm in the web width direction, and hot air is supplied from the slit 26. Further, the width of the web lower surface air supply nozzle 24 is generally larger than the web width in order to uniformly dry the entire width direction of the coating film surface. The exhaust nozzle 15 is provided in a flow path of hot air discharged from the web lower surface supply nozzle 24 on the lower surface of the web 16, and discharges the hot air used for drying to the outside of the drying furnace 22.
[0005]
The web 16 is made constant in tension by the roll 13 a and travels into the coat portion 11 to enter. When the web 16 enters the coating portion 11, the back surface is wound around the impression cylinder 11a, and the coating liquid is transferred to the front surface via the blanket cylinder 11b from which the coating liquid is transferred from the plate cylinder 11c. It is formed, travels in the direction of arrow X while being kept constant in tension by the roll 13 b, and enters the drying furnace 22.
When the web 16 travels in the drying furnace 22, the coating surface on the surface of the web 16 is dried from the back surface of the web 16 while being lifted by hot air blown from the web lower surface air supply nozzle 24 in the direction of arrow B. The
[0006]
[Problems to be solved by the invention]
FIG. 4 is an enlarged schematic diagram showing the configuration of the coating film drying air supply nozzle of FIG. 3 and the situation in which hot air wraps around the coating film.
In the web lower surface air supply nozzle 24, the width of the web lower surface air supply nozzle 24 is made larger than the width of the web 16 in order to float the web 16.
However, the problem is that the hot air blown from both ends in the width direction of the web lower surface air supply nozzle 24 wraps around the both ends of the coating film 17 on the upper surface of the web 16 as indicated by arrows C, and both ends of the coating film 17 are disturbed. There is.
[0007]
An object of the present invention, without disturbing the coating film surface, and without lowering the drying efficiency, to provide a coating film drying apparatus and film drying method Ru can perform drying of the coating film is there.
[0010]
[Means for Solving the Problems]
In order to solve the above-described problems, the invention according to claim 1 is directed to spraying a drying gas on the lower surface of the traveling surface of the object to be coated, and applying the gas to the upper surface of the object to be coated while floating the object to be coated. A coating film drying apparatus for drying a coating film, which is disposed on the lower surface side of the traveling surface of the object to be coated, has a gas supply part (14b) including a porous member on the entire surface, and the drying gas A coating film drying and supply nozzle (14) for supplying air, wherein the drying gas passes through the gas supply section and is sprayed onto the lower surface of the traveling surface of the object to be coated. It is a drying device.
[0011]
The invention according to claim 2 includes a drying step of drying the coating film applied to the upper surface of the object to be coated while spraying a drying gas on the lower surface of the traveling surface of the object to be coated and floating the object to be coated. a coating film drying method, the drying step, the coating film drying method of to supply air to the drying gas passing through the porous member at a low fluid speed and wide fluid sectional area (14b), the said It is.
[0012]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.
FIG. 1 is a schematic diagram showing the configuration of a coating film drying apparatus provided with a coating film drying and supply nozzle according to an embodiment of the present invention and the operation of the coating film drying apparatus.
In the following, parts having the same functions as those of the above-described conventional technology are denoted by the same reference numerals, and repeated description is appropriately omitted.
The coating film drying measure 10 includes a coating unit 11 that coats the web 16 as an object to be coated, a drying furnace 12 that dries the coated web 16, and a plurality of rolls 13 a to 13 that run the web 16 with a constant tension. 13c.
[0013]
The drying furnace 12 includes a web lower surface air supply nozzle 14 and an exhaust nozzle 15 inside.
A plurality of web lower surface air supply nozzles 14 are provided in the vicinity of the lower surface of the web 16 in the direction of travel of the web 16 at a predetermined interval. Further, the web lower surface air supply nozzle 14 is provided such that the longitudinal direction thereof is orthogonal to the traveling direction of the web 16.
The exhaust nozzle 15 is a nozzle that discharges hot air discharged from the web lower surface supply nozzle 14 as a gas supply unit to the outside of the drying furnace 12.
[0014]
FIG. 2 is an enlarged schematic view showing the configuration of the coating film drying air supply nozzle of FIG. 1 and the flow path of hot air.
The web lower surface air supply nozzle 14 includes a hot air nozzle 14a and a hot air supply unit 14b. The hot air supply unit 14b covers the entire surface of the hot air outlet of the hot air nozzle 14a and includes a porous member. The porous member is made of a porous sintered material.
The porous sintered material refers to a material in which powders or compacted particles are heated and combined to form a large number of pores or voids therein.
In the present embodiment, as the porous sintered material, aluminum, zinc, copper or the like is used, the porosity indicating the degree of porosity is 50% or less, the thickness is 3 to 30 mm, the pore size is 0.1 to 1 mm, A wind speed of 0.5 to 20 m / s is used.
[0015]
Next, the coating film drying operation by the web lower surface air supply nozzle 14 according to the present embodiment will be described.
As shown in FIG. 1, the web 16 is wound around a roll 13 a and travels with a constant tension, is applied by the coat unit 11, and enters the drying furnace 12 through the roll 13 b.
[0016]
When the web 16 enters the drying furnace 12, as shown in FIG. 2, hot air as a drying gas flowing in the hot air nozzle 14a passes through the hot air supply section 14b and blows to the back surface of the web 16. The coating film 17 applied to the surface of the web 16 travels in the direction of arrow X in FIGS. 1 and 2 while being dried.
[0017]
When the hot air passes through the porous sintered material of the hot air supply section 14b, the porous air circulates between the meshes because the pores are stretched around inside the porous sintered material. Hot air is supplied from the entire surface. Since air is supplied from the entire surface, air is supplied with a wide fluid cross-sectional area.
Moreover, since the mesh-shaped holes are intricately arranged inside the hot air supply section 14b, the hot air collides everywhere in the flow path while flowing. Since the air supply area is large, the wind speed is reduced even if the air supply amount is large.
In this way, the hot air is blown from the hot air supply unit 14b at a low fluid velocity and has a wide fluid cross-sectional area, and is blown to the lower surface of the web 16 as indicated by an arrow A (drying process).
[0018]
According to the present embodiment, since the hot air supply section includes the porous sintered material, hot air having a low fluid velocity and a wide fluid cross-sectional area can be derived.
Since the hot air has a low fluid velocity, the hot air does not wrap around the upper surface of the web 16 even when blown from the air supply surface wider than the web width, and the surface of the coating film 17, particularly the coating film 17. Both end portions in the width direction on the surface of the surface are dried without being disturbed.
In addition, since the hot air has a wide fluid cross-sectional area, a wide area web can be levitated and dried even at a low wind speed.
Furthermore, since the hot air has a wide fluid cross-sectional area, the drying efficiency does not decrease, and the drying efficiency does not deteriorate due to the low wind speed.
[0019]
(Deformation)
The present invention is not limited to the embodiment described above, and various modifications and changes are possible, and these are also within the equivalent scope of the present invention.
(1) In this embodiment, a web is used as an object to be coated, but a sheet or the like may be used.
[0020]
(2) In the present embodiment, a porous sintered material is used as the porous material. However, as long as the porous material is used, a material having a fine net or honeycomb-like hole may be used.
[0021]
(3) In this embodiment, hot air is used as the drying gas. However, as long as it is a gas that can be used for drying, a gas having a wetness of 0 or another gas having a hygroscopic property may be used.
[0022]
(4) In the present embodiment, the entire surface of the gas supply unit is a porous member, but a porous member may be used in a predetermined range of the gas supply unit.
[0023]
【The invention's effect】
As described above in detail, the present invention has the following effects.
(1) Since the gas supply unit includes a porous member through which the drying gas passes, the drying gas can be blown out by being changed to a low fluid velocity by the porous member.
[0024]
(2) Since the porous member is provided on the entire surface of the gas supply unit, the drying gas is changed to a wider fluid cross-sectional area and blown out as compared with the case where the porous member is provided in a part of the gas supply unit. Can do.
[0025]
(3) Since the drying gas passes through the gas supply section composed of the porous material and is sprayed on the lower surface of the object to be coated, the coating surface is not disturbed and the drying efficiency is not reduced. The coating film can be dried.
[Brief description of the drawings]
FIG. 1 is a schematic diagram showing the configuration of a coating film drying apparatus provided with a coating film drying and supply nozzle according to an embodiment of the present invention and the operation of the coating film drying apparatus.
2 is an enlarged schematic view showing a configuration of a coating film drying air supply nozzle of FIG. 1 and a flow path of hot air.
FIG. 3 is a schematic diagram showing the configuration and operation of a conventional coating film drying apparatus.
4 is an enlarged schematic view showing a configuration of a coating film drying / supplying nozzle of FIG. 3 and a situation in which hot air wraps around the coating film.
[Explanation of symbols]
14 Web lower surface air supply nozzle 14a Hot air nozzle 14b Hot air supply unit 16 Web 17 Coating film

Claims (2)

被塗布物の走行面の下面に乾燥用気体を吹き付け、前記被塗布物を浮上させながら前記被塗布物の上面に塗布した塗膜を乾燥する塗膜乾燥装置であって、
前記被塗布物の走行面の下面側に配置され、全面に多孔質部材を備える気体給気部を有し、前記乾燥用気体を給気する塗膜乾燥給気ノズルを備え、
前記乾燥用気体は、前記気体給気部を通過して前記被塗布物の走行面の下面に吹き付けられること、
を特徴とする塗膜乾燥装置。
A coating film drying apparatus that blows a drying gas on the lower surface of the traveling surface of the object to be coated, and dries the coating film applied to the upper surface of the object to be coated while floating the object,
It is disposed on the lower surface side of the traveling surface of the object to be coated, has a gas air supply portion including a porous member on the entire surface, and includes a coating film drying air supply nozzle for supplying the drying gas,
The drying gas passes through the gas supply section and is sprayed on the lower surface of the traveling surface of the object to be coated;
A coating film drying apparatus characterized by the above.
被塗布物の走行面の下面に乾燥用気体を吹き付け、前記被塗布物を浮上させながら前記被塗布物の上面に塗布した塗膜を乾燥する乾燥工程を備えた塗膜乾燥方法であって、
前記乾燥工程は、多孔質部材を通過した前記乾燥用気体を低い流体速度及び広い流体断面積で給気すること、
を特徴とする塗膜乾燥方法。
A coating film drying method comprising a drying step of drying a coating film applied to the upper surface of the coating object while spraying a drying gas on the lower surface of the traveling surface of the coating object, and floating the coating object,
The drying step is to supply air to the drying gas passing through the porous member at a low fluid speed and wide fluid sectional area,
A coating film drying method characterized by the above.
JP2002225870A 2002-08-02 2002-08-02 Coating film drying apparatus and coating film drying method Expired - Fee Related JP4173330B2 (en)

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Application Number Priority Date Filing Date Title
JP2002225870A JP4173330B2 (en) 2002-08-02 2002-08-02 Coating film drying apparatus and coating film drying method

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JP4173330B2 true JP4173330B2 (en) 2008-10-29

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Cited By (1)

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CN102489438A (en) * 2011-11-25 2012-06-13 深圳市浩能科技有限公司 Drying channel of coating machine

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JP5323343B2 (en) * 2007-12-12 2013-10-23 株式会社ヒラノテクシード Web heat treatment equipment
US9068775B2 (en) 2009-02-09 2015-06-30 Heat Technologies, Inc. Ultrasonic drying system and method
DE102013223150A1 (en) * 2013-11-13 2015-05-28 Sandvik Materials Technology Deutschland Gmbh Dryers and methods for drying sheetlike materials
DE102013223151A1 (en) * 2013-11-13 2015-05-13 Sandvik Materials Technology Deutschland Gmbh Apparatus and method for treating sheet material
US10488108B2 (en) * 2014-07-01 2019-11-26 Heat Technologies, Inc. Indirect acoustic drying system and method
DE102014009945A1 (en) 2014-07-04 2016-01-07 Dürr Systems GmbH Painting process and paint shop for decorative painting
JP2016186377A (en) * 2015-03-27 2016-10-27 日本電気株式会社 Drying apparatus and drying method
CN115157834B (en) * 2022-06-07 2024-06-04 西安新达机械有限公司 Ultrathin film composite system and use method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102489438A (en) * 2011-11-25 2012-06-13 深圳市浩能科技有限公司 Drying channel of coating machine
CN102489438B (en) * 2011-11-25 2015-01-07 深圳市浩能科技有限公司 Drying channel of coating machine

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