WO2013140620A1 - Curtain coater - Google Patents

Curtain coater Download PDF

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Publication number
WO2013140620A1
WO2013140620A1 PCT/JP2012/057585 JP2012057585W WO2013140620A1 WO 2013140620 A1 WO2013140620 A1 WO 2013140620A1 JP 2012057585 W JP2012057585 W JP 2012057585W WO 2013140620 A1 WO2013140620 A1 WO 2013140620A1
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WIPO (PCT)
Prior art keywords
paint
curtain
coating machine
diluent
coating
Prior art date
Application number
PCT/JP2012/057585
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French (fr)
Japanese (ja)
Inventor
敏弘 片野
弘幸 河野
明男 平野
忠 佐々
克己 石塚
Original Assignee
フォイト パテント ゲゼルシャフト ミット ベシュレンクテル ハフツング
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Application filed by フォイト パテント ゲゼルシャフト ミット ベシュレンクテル ハフツング filed Critical フォイト パテント ゲゼルシャフト ミット ベシュレンクテル ハフツング
Priority to PCT/JP2012/057585 priority Critical patent/WO2013140620A1/en
Publication of WO2013140620A1 publication Critical patent/WO2013140620A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05CAPPARATUS FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05C5/00Apparatus in which liquid or other fluent material is projected, poured or allowed to flow on to the surface of the work
    • B05C5/005Curtain coaters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05CAPPARATUS FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05C9/00Apparatus or plant for applying liquid or other fluent material to surfaces by means not covered by any preceding group, or in which the means of applying the liquid or other fluent material is not important
    • B05C9/06Apparatus or plant for applying liquid or other fluent material to surfaces by means not covered by any preceding group, or in which the means of applying the liquid or other fluent material is not important for applying two different liquids or other fluent materials, or the same liquid or other fluent material twice, to the same side of the work
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H23/00Processes or apparatus for adding material to the pulp or to the paper
    • D21H23/02Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
    • D21H23/22Addition to the formed paper
    • D21H23/46Pouring or allowing the fluid to flow in a continuous stream on to the surface, the entire stream being carried away by the paper
    • D21H23/48Curtain coaters

Definitions

  • the present invention relates to a curtain coating machine for applying a paint to a substrate by flowing a paint into a curtain film.
  • a curtain coating machine for forming a coating film on a tape-like substrate such as paper
  • This curtain coating machine smoothly guides the defoamed paint supplied to the head for the curtain coating machine to the lower nozzle part without stagnation, and the nozzle part rectifies the flow of paint uniformly in the width direction. Flow down from the nozzle tip. The paint that has flowed down is formed into a uniform and stable curtain film shape, and is supplied onto a substrate that travels at a high speed (see, for example, Patent Document 1).
  • the above curtain coating machine is excellent in that it can be applied at high speed without using wasteful paint.
  • the coating material is caused to flow down at a low flow rate, it is difficult to form a curtain film that is uniform in the width direction at, for example, about 3 L / min / m or less.
  • an air flow is generated in the curtain film when the substrate is run at a high speed, it is difficult to maintain the curtain shape by the air flow when the flow rate is low.
  • the present invention has been made in view of the above-described circumstances, and is a curtain coating machine capable of forming a uniform curtain film in the width direction even when the paint is allowed to flow down at a low flow rate with the curtain coating machine. It is for providing.
  • the present invention has a paint chamber which is formed in a long shape along the width direction of a substrate to be coated and extends in the width direction.
  • a curtain coating machine provided with a curtain coating machine head that flows down the paint in the form of a curtain film, the low viscosity liquid is brought into contact with a low viscosity liquid having a viscosity lower than that of the paint.
  • a guide plate is provided for guiding to the vicinity of the substrate.
  • a low-viscosity liquid chamber can be provided inside the curtain coating machine head for storing the low-viscosity liquid and flowing it downward.
  • the low-viscosity liquid may be a dilute solution obtained by diluting the paint, an aqueous solution such as a surfactant, or water.
  • a guide plate is provided for guiding the low viscosity liquid to the vicinity of the base material while being in contact with the low viscosity liquid having a viscosity lower than that of the paint.
  • a paint curtain film can be formed on the opposite side of the curtain film. Therefore, the curtain film can flow down in a state where the viscosity resistance is low as compared with the case where the paint is in direct contact with the guide plate. As a result, the deceleration phenomenon of the paint at the interface between the curtain and the plate due to viscous resistance is reduced, and the curtain becomes close to free fall.
  • the curtain film can be accelerated to an appropriate speed, defects such as coating film skip can be prevented, and coating can be performed while traveling at a higher speed.
  • the paint near the interface is hardly decelerated, there is no speed difference between the paint near the interface and the surface side, and the phenomenon of the curtain undulating can be prevented.
  • the coating film to be coated on the substrate can be made thin.
  • the vertical lower part of the paint is guided by the guide plate, so the curtain film is disturbed by the air current when the substrate is run at high speed. There is no.
  • FIG. 3 is a side cross-sectional view taken along the line AA in FIG. 2 and shows a state in which a coating material and a diluent are flowing down. It is an expanded sectional view of the part which attached the guide plate of FIG.
  • FIG. 1 is a perspective view of a curtain coating machine 1 according to an embodiment of the present invention as viewed obliquely from above and shows a right side in section.
  • 2 is a front view of the curtain coating machine 1
  • FIG. 3 is a cross-sectional view taken along the line AA in FIG. 2
  • FIG. 4 is an enlarged cross-sectional view of a portion where the guide plate is attached in FIG.
  • the top / bottom / left / right, the front / rear direction, and the width direction used in the following description refer to directions when the curtain coating machine 1 of FIG.
  • the curtain coating machine 1 includes a curtain coating machine head 2 (hereinafter referred to as a head 2) that extends in the left-right direction (the width direction of the coated paper 60).
  • a head 2 As shown in FIGS. 1 and 3, the head 2 is provided with two chambers, a paint chamber 10 and a diluent chamber 20. These chambers 10 and 20 have a semicircular cross section, and are provided continuously in the extending direction (left and right direction and width direction) of the head 2.
  • the paint chamber 10 is formed by assembling a paint-side main body 13 located on the front side and a triangular intermediate portion 14 with fixing bolts 15 (see FIGS. 1 and 2). Front and rear walls are configured.
  • the diluent chamber 20 is configured with front and rear wall portions by assembling the diluent side main body portion 23 and the intermediate portion 14 located on the back side with fixing bolts (not shown).
  • side walls 5 are respectively provided on both sides of the paint chamber 10 and the diluent chamber 20 as shown in FIG.
  • the side wall 5 is formed in a flat plate shape and closes the semicircular side portions of the respective chambers 10 and 20.
  • the side wall portion 5 is detachably attached to the paint side main body portion 13, the intermediate portion 14, and the diluent side main body portion 23 by fixing bolts 6. Thereby, each chamber 10 and 20 comprises the sealed chamber.
  • the side wall 5 is provided with supply pipes 3 and 4, which will be described in detail later, in a manner communicating with the chambers 10 and 20.
  • the curtain coating machine 1 includes a supply tank (not shown) in which the paint 30 is stored, a defoaming machine (not shown) that removes bubbles in the paint 30, a circulation pump (not shown), and the like. Is provided.
  • the paint chamber 10 is connected to these via the supply pipe 3 (see FIG. 2), and the paint 30 described above is supplied into the paint chamber 10.
  • the curtain coating machine 1 is also provided with a supply tank (not shown) for supplying the diluent 40 to the diluent chamber 20.
  • the diluent chamber 20 is connected to these via the supply pipe 4 (see FIG. 2), and the diluent 40 described above is supplied into the diluent chamber 20.
  • a nozzle 11 is formed on the lower side of the paint chamber 10.
  • the nozzle 11 extends from the paint chamber 10 toward the rear obliquely lower side, and the paint 30 naturally flows down.
  • the flow rate of the paint 30 that naturally flows down from the nozzle 11 is adjusted by the gap between the nozzles 11, and the curtain film 12 of the paint 30 that is uniform in the left-right direction of the head 2 is formed.
  • a nozzle 21 extending from the diluent chamber 20 toward the vertically lower side and allowing the diluent 40 to naturally flow down is formed on the lower side of the diluent chamber 20, a nozzle 21 extending from the diluent chamber 20 toward the vertically lower side and allowing the diluent 40 to naturally flow down is formed.
  • the flow rate of the diluent 40 that naturally flows down from the nozzle 21 is adjusted by the gap between the nozzles 21, and the curtain film 22 of the diluent 40 that is uniform in the left-right direction of the head 2 is formed.
  • the nozzle 11 extending from the paint chamber 10 and the nozzle 21 extending from the diluent chamber 20 are joined at their lower ends G as shown in FIGS. Therefore, the paint 30 and the diluting liquid 40 that flow down join each other at the lower end G.
  • the coating material 30 and the dilution liquid 40 will be described later in detail, but will form two layers without being mixed with each other.
  • a guide plate 24 is provided so as to extend below the diluent side main body portion 23 (a mode in which the diluent side main body portion 23 extends downward).
  • the guide plate 24 is provided over the entire length of the head 2 in the left-right direction.
  • the surface 24 c of the guide plate 24 is formed to be flush with the surface 22 c of the lip portion 22 in a state where the guide plate 24 is attached to the lip portion 22.
  • the diluent 40 in the diluent chamber 20 flows downward while contacting the surface 22c at the lip 22 and, after flowing down from the lip 22, contacts the surface 24c of the guide plate 24. It will flow down without resistance.
  • the lower side of the guide plate 24 extends to the vicinity of the coated paper 60 as shown in FIG.
  • the guide plate 24 guides the diluent 40 to the vicinity of the coated paper 60, and the airflow generated when the coated paper 60 is fed in the B direction at high speed hits the curtain films 12 and 22, and the curtain film. 12 and 22 are not disturbed.
  • the coating material 30 stored in the coating chamber 10 and the diluent 40 stored in the diluent chamber 20 naturally flow down from the nozzles 11 and 21 simultaneously with their own weight.
  • the diluent 40 contacts the surface 24c of the guide plate 24 and flows downward along the surface 24c to form the curtain film 22 of the diluent 40.
  • the coating material 30 contacts the surface 22c of the curtain film 22 of the diluent 40 and flows down along the surface 22c to form the curtain film 12 of the coating material 30.
  • the curtain film 22 of the diluent 40 and the curtain film 12 of the coating material 30 flow down while constituting two layers without being mixed together.
  • the above-described paint 30 is a paint generally used in the curtain coating machine 1 and has a viscosity as low as possible so that the curtain film 12 can be formed when it flows down.
  • the dilution liquid 40 for example, a dilution obtained by diluting the paint 40 with water or the like is used. Alternatively, it may be water or a surfactant solution. That is, as the dilution liquid 40, a liquid having a lower viscosity than the paint 30 is used. Therefore, the above-described coating material 30 flows down along the surface 22c of the low-viscosity diluent 40, and the coating material 30 has a higher viscosity than the diluent 40. Therefore, the coating material 30 is separated into two layers without mixing each other. It will flow down as it is.
  • the diluent 40 since the diluent 40 has a low viscosity, the viscosity resistance is low when it comes into contact with the surface 24c of the guide plate 24 as compared with the paint 30. Therefore, in the absence of the diluent 40, when the coating material 30 and the surface 24c of the guide plate 24 come into contact with each other, the viscosity resistance increases, and the curtain film cannot be accelerated to an appropriate speed. Therefore, by interposing the diluent 40 between the surface 24c of the guide plate 24 and the coating material 30, the curtain end speed is appropriately controlled so that coating defects such as coating film skip do not occur.
  • the coating material 30 and the diluent 40 flow down onto the coated paper 60 that travels at a high speed in a state where the two-layered structure is left and right, and a coating film surface is formed on the coated paper 60.
  • the coated paper 60 after coating is dried in a drying process that is a subsequent process.
  • the diluent 40 is a solution obtained by thinning the paint 30 or water, only the paint 30 remains on the coated paper 60 after drying in the drying process. Therefore, the same quality as the case where it coats using only the coating material 30 is ensured on the coating surface.
  • the guide plate 24 that guides the diluted solution to the vicinity of the coated paper 60 while being in contact with the diluted solution 40 having a viscosity lower than that of the paint 30 is provided. Therefore, the curtain film 12 of the paint 30 can be formed on the opposite side of the dilution liquid 40 across the curtain film 22. Therefore, compared with the case where the coating material 30 is in direct contact with the guide plate 24, the curtain film 12 can be caused to flow down with a low viscous resistance. As a result, even if the paint 30 from the paint chamber 10 is flowed at a low flow rate, the curtain film 12 that is uniform in the width direction and has high stability can be formed.
  • the paint 30 sometimes drops in the form of water droplets instead of the curtain film 12, but since the curtain film 12 can be formed at a low flow rate, the curtain can be formed.
  • the coating flow rate can be reduced.
  • the coating film applied on the coated paper 60 can be thinned.
  • the coated paper 60 can be coated at a higher speed as compared with the case of coating with a die coater.
  • the reason why the die coater can be applied only at a low speed is that the termination speed of the paint film and the blowing speed are equal, so that acceleration due to free fall of the paint is not performed. For this reason, at a high speed, the stretch rate of the film becomes too large, the film cannot follow the stretch, and a phenomenon that the film is cut off occurs, resulting in a defect.
  • the conventional curtain system is accelerated by free fall, it is suitable for coating at a higher speed, but has a disadvantage that a curtain film cannot be formed with a low coating amount.
  • the curtain coating machine 1 according to the embodiment of the present invention satisfies both of these merits.
  • an air cut device may be additionally provided in the vicinity of the curtain film.
  • the diluent chamber 40 is provided in the curtain coating machine head 2 to store the diluent 40 and flow downward, not only the paint 30 but also the diluent is provided in the head 10. 40 can also be stored and flowed down.
  • the curtain coating machine 1 according to the embodiment of the present invention has been described above, but the present invention is not limited to the above-described embodiment, and various modifications and changes can be made based on the technical idea of the present invention. Is possible.
  • the coating is performed on the coated paper 60 such as paper or cardboard, but the present invention is not limited to this.
  • the present invention can also be applied when a film is formed on a base material other than paper such as a plastic film.
  • the head 10 is provided with one paint chamber 10 and one diluent chamber 20, but a plurality of them may be provided to cope with multicolor printing.
  • the diluent chamber 20 for storing the diluent 40 is provided inside the head 10, but may be configured separately from the head 10.

Abstract

Provided is a curtain coater capable of forming a curtain film that is uniform in the transverse direction even when the coating is made to flow downward at a low flow rate with the curtain coater. A curtain coater (1), which is formed to be long in the transverse direction of a substrate (60) that is to be coated, which has a coating chamber (10) that extends in said transverse direction, in which a coating (30) for coating is supplied into the coating chamber (10), and which is provided with a curtain coater head (2) that causes the coating to flow downward as a curtain film (12). The curtain coater is provided with a guide plate (24), which guides a low viscosity liquid (40) with a viscosity lower than the coating (30) to the vicinity of the substrate (60) while in contact with the low viscosity liquid (40).

Description

カーテン塗工機Curtain coating machine
 本発明は、塗料をカーテン膜状に流下させて基材に塗工するためのカーテン塗工機に関する。 The present invention relates to a curtain coating machine for applying a paint to a substrate by flowing a paint into a curtain film.
 従来、紙などのテープ状の基材に塗膜を形成するためのカーテン塗工機(DF(Direct Fountain)コータ)が知られている。このカーテン塗工機は、カーテン塗工機用ヘッドに供給される脱泡された塗料を滞留させることなくスムースに下部のノズル部に導き、このノズル部で塗料の流れを幅方向均一に整流してノズル先端から下方へ流下させる。流下した塗料は、均一な安定したカーテン膜状に形成されて、高速で走行する基材上に供給される(例えば、特許文献1参照)。 Conventionally, a curtain coating machine (DF (Direct Fountain) coater) for forming a coating film on a tape-like substrate such as paper is known. This curtain coating machine smoothly guides the defoamed paint supplied to the head for the curtain coating machine to the lower nozzle part without stagnation, and the nozzle part rectifies the flow of paint uniformly in the width direction. Flow down from the nozzle tip. The paint that has flowed down is formed into a uniform and stable curtain film shape, and is supplied onto a substrate that travels at a high speed (see, for example, Patent Document 1).
特開2000-210607号公報JP 2000-210607 A
 上述したカーテン塗工機では、無駄な塗料を使用しないで、高速で塗工することができる点で優れている。しかしながら、塗料を低流量で流下させる場合、例えば約3L/min/m以下では、幅方向均一なカーテン膜を形成することが難しかった。また、カーテン膜には、基材を高速で走行させたときの気流が生じるため、低流量の場合はその気流によってカーテン形状を保持することが難しかった。 The above curtain coating machine is excellent in that it can be applied at high speed without using wasteful paint. However, when the coating material is caused to flow down at a low flow rate, it is difficult to form a curtain film that is uniform in the width direction at, for example, about 3 L / min / m or less. Further, since an air flow is generated in the curtain film when the substrate is run at a high speed, it is difficult to maintain the curtain shape by the air flow when the flow rate is low.
 一方、基材にノズル部を近接させて塗工するダイコータも知られている。このダイコータでは、ノズルから噴出された塗料が直接基材に当たるため、上述したカーテン膜を形成しないで塗工が可能であるが、塗料の引き伸ばし率の問題から、ごく低速でしか塗工できないという問題がある。 On the other hand, there is also known a die coater for applying the nozzle portion close to the substrate. In this die coater, since the paint sprayed from the nozzle directly hits the substrate, it can be applied without forming the curtain film described above, but due to the problem of the paint stretch rate, it can only be applied at very low speeds. There is.
 本発明は、上述した事情を鑑みてなされたものであり、カーテン塗工機で塗料を低流量で流下させる場合であっても、幅方向均一なカーテン膜を形成することができるカーテン塗工機を提供するためのものである。 The present invention has been made in view of the above-described circumstances, and is a curtain coating machine capable of forming a uniform curtain film in the width direction even when the paint is allowed to flow down at a low flow rate with the curtain coating machine. It is for providing.
 上述課題を解決するため、本発明は、塗工される基材の幅方向に沿って長尺に形成され、この幅方向に延在する塗料チャンバを有し、この塗料チャンバ内に塗工用の塗料が供給され、カーテン膜状に前記塗料を流下するカーテン塗工機用ヘッドを備えたカーテン塗工機において、前記塗料よりも粘度が低い低粘度液と接しながら、この低粘度液を前記基材の近傍まで案内するガイドプレートを設けたことを特徴とする。 In order to solve the above-described problems, the present invention has a paint chamber which is formed in a long shape along the width direction of a substrate to be coated and extends in the width direction. In a curtain coating machine provided with a curtain coating machine head that flows down the paint in the form of a curtain film, the low viscosity liquid is brought into contact with a low viscosity liquid having a viscosity lower than that of the paint. A guide plate is provided for guiding to the vicinity of the substrate.
 また、前記カーテン塗工機用ヘッドの内部に、前記低粘度液を貯留して下側に向けて流下させる低粘度液チャンバを設けることもできる。 Also, a low-viscosity liquid chamber can be provided inside the curtain coating machine head for storing the low-viscosity liquid and flowing it downward.
 さらに、前記低粘度液が、前記塗料を薄めた希釈液、界面活性剤等の水溶液、または水であってもよい。 Furthermore, the low-viscosity liquid may be a dilute solution obtained by diluting the paint, an aqueous solution such as a surfactant, or water.
 本発明に係るカーテン塗工機では、前記塗料よりも粘度が低い低粘度液と接しながら、この低粘度液を前記基材の近傍まで案内するガイドプレートを設けているので、この低粘度液のカーテン膜を挟んだ逆側で、塗料のカーテン膜を形成することができる。そのため、塗料がガイドプレートと直接接する場合と比較して、粘性抵抗が低い状態でカーテン膜を流下させることができる。その結果、粘性抵抗によるカーテンおよびプレート界面での塗料の減速現象が低減し、カーテンは自由落下に近い状態となる。従い、適切な速度までカーテン膜を加速させることができ、塗工膜スキップ等の欠陥を防止でき、より高速で走行させて塗工することが可能となる。また、界面近傍の塗料がほとんど減速されないので、界面近傍と表面側で塗料の速度差が生じず、カーテンが波打つ現象も防止できる。さらに、例えば、3L/min/m未満の低流量においても、幅方向で均一なカーテン膜が形成されるため、基材上に塗工する塗膜を薄くすることができる。
 また、通常のカーテン塗工機(ガイドプレートがないもの)と比較して、塗料の垂直下部がガイドプレートでガイドされているので、基材を高速走行させたときの気流によってカーテン膜が乱れることがない。
In the curtain coating machine according to the present invention, a guide plate is provided for guiding the low viscosity liquid to the vicinity of the base material while being in contact with the low viscosity liquid having a viscosity lower than that of the paint. A paint curtain film can be formed on the opposite side of the curtain film. Therefore, the curtain film can flow down in a state where the viscosity resistance is low as compared with the case where the paint is in direct contact with the guide plate. As a result, the deceleration phenomenon of the paint at the interface between the curtain and the plate due to viscous resistance is reduced, and the curtain becomes close to free fall. Accordingly, the curtain film can be accelerated to an appropriate speed, defects such as coating film skip can be prevented, and coating can be performed while traveling at a higher speed. In addition, since the paint near the interface is hardly decelerated, there is no speed difference between the paint near the interface and the surface side, and the phenomenon of the curtain undulating can be prevented. Furthermore, for example, even at a low flow rate of less than 3 L / min / m, since a uniform curtain film is formed in the width direction, the coating film to be coated on the substrate can be made thin.
Also, compared to a normal curtain coating machine (without a guide plate), the vertical lower part of the paint is guided by the guide plate, so the curtain film is disturbed by the air current when the substrate is run at high speed. There is no.
本発明の実施の形態に係るカーテン塗工機を上方斜め上側から見た斜視図であって、右側部を断面で示したものである。It is the perspective view which looked at the curtain coating machine which concerns on embodiment of this invention from upper diagonally upper direction, Comprising: The right side part is shown with the cross section. 本発明の実施の形態に係るカーテン塗工機の正面図であって、塗料および希釈液を流下させていない状態を示している。It is a front view of the curtain coating machine which concerns on embodiment of this invention, Comprising: The state which is not flowing down the coating material and dilution liquid is shown. 図2のA-A線で切断した側部断面図であって、塗料および希釈液を流下させている状態を示している。FIG. 3 is a side cross-sectional view taken along the line AA in FIG. 2 and shows a state in which a coating material and a diluent are flowing down. 図3のガイドプレートを取り付けた部分の拡大断面図である。It is an expanded sectional view of the part which attached the guide plate of FIG.
 以下、本発明の実施の形態に係るカーテン塗工機について、図1~図4を用いて詳細に説明する。
 図1は、本発明の実施の形態に係るカーテン塗工機1を上方斜め上側から見た斜視図であって、右側部を断面で示したものである。また、図2はカーテン塗工機1の正面図、図3は図2のA-A断面図、図4は、図3のガイドプレートを取り付けた部分の拡大断面図である。なお、以下の説明で使用する上下左右、前後の方向および幅方向は、図1のカーテン塗工機1を正面(図1の左斜め前側)から見たときの方向をいう。
Hereinafter, a curtain coating machine according to an embodiment of the present invention will be described in detail with reference to FIGS.
FIG. 1 is a perspective view of a curtain coating machine 1 according to an embodiment of the present invention as viewed obliquely from above and shows a right side in section. 2 is a front view of the curtain coating machine 1, FIG. 3 is a cross-sectional view taken along the line AA in FIG. 2, and FIG. 4 is an enlarged cross-sectional view of a portion where the guide plate is attached in FIG. In addition, the top / bottom / left / right, the front / rear direction, and the width direction used in the following description refer to directions when the curtain coating machine 1 of FIG.
 カーテン塗工機1は、図1に示すように、左右方向(塗工紙60の幅方向)に延在するカーテン塗工機用ヘッド2(以下、ヘッド2という)を備えている。このヘッド2には、図1および図3に示すように、その内部に塗料チャンバ10および希釈液チャンバ20の2つのチャンバが設けられている。これらのチャンバ10、20は、その断面が半円形状に形成されており、ヘッド2の延在方向(左右方向、幅方向)に亘って連続して設けられている。 As shown in FIG. 1, the curtain coating machine 1 includes a curtain coating machine head 2 (hereinafter referred to as a head 2) that extends in the left-right direction (the width direction of the coated paper 60). As shown in FIGS. 1 and 3, the head 2 is provided with two chambers, a paint chamber 10 and a diluent chamber 20. These chambers 10 and 20 have a semicircular cross section, and are provided continuously in the extending direction (left and right direction and width direction) of the head 2.
 塗料チャンバ10は、図1および図3に示すように、正面側に位置する塗料側本体部13と、三角形状の中間部14とを固定ボルト15(図1および図2参照)で組み付けることにより前後の壁部が構成されている。また、希釈液チャンバ20も同様に、裏側に位置する希釈液側本体部23と中間部14とを固定ボルト(図示せず)で組み付けることにより前後の壁部が構成されている。 As shown in FIGS. 1 and 3, the paint chamber 10 is formed by assembling a paint-side main body 13 located on the front side and a triangular intermediate portion 14 with fixing bolts 15 (see FIGS. 1 and 2). Front and rear walls are configured. Similarly, the diluent chamber 20 is configured with front and rear wall portions by assembling the diluent side main body portion 23 and the intermediate portion 14 located on the back side with fixing bolts (not shown).
 また、塗料チャンバ10および希釈液チャンバ20の両側部には、図2に示すように、側壁部5がそれぞれ設けられている。この側壁部5は、平板形状に形成され、それぞれのチャンバ10、20の半円形状の側部を塞いでいる。この側壁部5は、固定ボルト6によって塗料側本体部13、中間部14、希釈液側本体部23と着脱自在に取り付けられている。これにより各チャンバ10、20が密閉された室を構成する。また、この側壁部5には、詳細は後述する供給パイプ3、4が各チャンバ10、20と連通する態様で設けられている。 Further, side walls 5 are respectively provided on both sides of the paint chamber 10 and the diluent chamber 20 as shown in FIG. The side wall 5 is formed in a flat plate shape and closes the semicircular side portions of the respective chambers 10 and 20. The side wall portion 5 is detachably attached to the paint side main body portion 13, the intermediate portion 14, and the diluent side main body portion 23 by fixing bolts 6. Thereby, each chamber 10 and 20 comprises the sealed chamber. In addition, the side wall 5 is provided with supply pipes 3 and 4, which will be described in detail later, in a manner communicating with the chambers 10 and 20.
 なお、カーテン塗工機1には、塗料30が貯留される供給タンク(図示せず)や、塗料30内部の気泡を取り除く脱泡機(図示せず)、循環ポンプ(図示せず)などが設けられている。塗料チャンバ10は、これらと供給パイプ3(図2参照)を介して接続されており、塗料チャンバ10内に上述した塗料30が供給されるようになっている。 The curtain coating machine 1 includes a supply tank (not shown) in which the paint 30 is stored, a defoaming machine (not shown) that removes bubbles in the paint 30, a circulation pump (not shown), and the like. Is provided. The paint chamber 10 is connected to these via the supply pipe 3 (see FIG. 2), and the paint 30 described above is supplied into the paint chamber 10.
 また、カーテン塗工機1も同様に、希釈液チャンバ20に希釈液40を供給するための供給タンク(図示せず)などが設けられている。希釈液チャンバ20は、これらと供給パイプ4(図2参照)を介して接続されており、この希釈液チャンバ20内に上述した希釈液40が供給されるようになっている。 Similarly, the curtain coating machine 1 is also provided with a supply tank (not shown) for supplying the diluent 40 to the diluent chamber 20. The diluent chamber 20 is connected to these via the supply pipe 4 (see FIG. 2), and the diluent 40 described above is supplied into the diluent chamber 20.
 塗料チャンバ10の下側には、この塗料チャンバ10から後方斜め下側に向かって延在し、塗料30が自然流下するノズル11が形成されている。このノズル11の隙間により、ノズル11から自然流下する塗料30の流量が調整され、ヘッド2の左右方向で均一な塗料30のカーテン膜12が形成されることになる。 A nozzle 11 is formed on the lower side of the paint chamber 10. The nozzle 11 extends from the paint chamber 10 toward the rear obliquely lower side, and the paint 30 naturally flows down. The flow rate of the paint 30 that naturally flows down from the nozzle 11 is adjusted by the gap between the nozzles 11, and the curtain film 12 of the paint 30 that is uniform in the left-right direction of the head 2 is formed.
 一方、希釈液チャンバ20の下側にも、この希釈液チャンバ20から鉛直下側に向かって延在し、希釈液40が自然流下するノズル21が形成されている。このノズル21の隙間により、ノズル21から自然流下する希釈液40の流量が調整され、ヘッド2の左右方向で均一な希釈液40のカーテン膜22が形成されることになる。 On the other hand, on the lower side of the diluent chamber 20, a nozzle 21 extending from the diluent chamber 20 toward the vertically lower side and allowing the diluent 40 to naturally flow down is formed. The flow rate of the diluent 40 that naturally flows down from the nozzle 21 is adjusted by the gap between the nozzles 21, and the curtain film 22 of the diluent 40 that is uniform in the left-right direction of the head 2 is formed.
 上述した塗料チャンバ10から延在するノズル11と、希釈液チャンバ20から延在するノズル21は、図3および図4に示すように、それぞれの下端部Gで合流している。そのため、流下する塗料30および希釈液40は、この下端部Gでそれぞれ合流することになる。なお、これらの塗料30および希釈液40は、詳細は後述するが、互いに混じり合うことなく、2層を構成するようになる。 The nozzle 11 extending from the paint chamber 10 and the nozzle 21 extending from the diluent chamber 20 are joined at their lower ends G as shown in FIGS. Therefore, the paint 30 and the diluting liquid 40 that flow down join each other at the lower end G. The coating material 30 and the dilution liquid 40 will be described later in detail, but will form two layers without being mixed with each other.
 また、希釈液側本体部23の下側に延在(希釈液側本体部23を下側に延長するような態様)してガイドプレート24が設けられている。このガイドプレート24は、ヘッド2の左右方向の全長に亘って設けられている。 Further, a guide plate 24 is provided so as to extend below the diluent side main body portion 23 (a mode in which the diluent side main body portion 23 extends downward). The guide plate 24 is provided over the entire length of the head 2 in the left-right direction.
 ガイドプレート24の表面24cは、図4に示すように、ガイドプレート24がリップ部22に取り付けられた状態で、リップ部22の表面22cと面一になるように形成されている。これにより、希釈液チャンバ20の希釈液40は、リップ部22でその表面22cと接触しつつ下側へと流下し、リップ部22から流下した後には、ガイドプレート24の表面24cと接触しつつ、下側に抵抗無く流下していくことになる。 As shown in FIG. 4, the surface 24 c of the guide plate 24 is formed to be flush with the surface 22 c of the lip portion 22 in a state where the guide plate 24 is attached to the lip portion 22. As a result, the diluent 40 in the diluent chamber 20 flows downward while contacting the surface 22c at the lip 22 and, after flowing down from the lip 22, contacts the surface 24c of the guide plate 24. It will flow down without resistance.
 また、このガイドプレート24の下側は、図3に示すように、塗工紙60の近傍まで延びている。これにより、ガイドプレート24は、希釈液40を塗工紙60の近傍まで案内するとともに、塗工紙60が高速でB方向へ送られる際に発生する気流が、カーテン膜12、22に当たってカーテン膜12、22が乱れないようにする機能を果たしている。 Further, the lower side of the guide plate 24 extends to the vicinity of the coated paper 60 as shown in FIG. As a result, the guide plate 24 guides the diluent 40 to the vicinity of the coated paper 60, and the airflow generated when the coated paper 60 is fed in the B direction at high speed hits the curtain films 12 and 22, and the curtain film. 12 and 22 are not disturbed.
 次に、本発明の実施の形態に係るカーテン塗工機1の作用について説明する。
 塗工チャンバ10に貯留された塗料30および希釈液チャンバ20に貯留された希釈液40は、それぞれ同時にノズル11、21から自重で自然流下する。
Next, the effect | action of the curtain coating machine 1 which concerns on embodiment of this invention is demonstrated.
The coating material 30 stored in the coating chamber 10 and the diluent 40 stored in the diluent chamber 20 naturally flow down from the nozzles 11 and 21 simultaneously with their own weight.
 このとき、希釈液40は、ガイドプレート24の表面24cに接触するとともに、この表面24cに沿って下側に流下し、希釈液40のカーテン膜22を形成する。
 一方、塗料30は、希釈液40のカーテン膜22の表面22cと接触するとともに、この表面22cに沿って下側に流下し、塗料30のカーテン膜12を形成する。
At this time, the diluent 40 contacts the surface 24c of the guide plate 24 and flows downward along the surface 24c to form the curtain film 22 of the diluent 40.
On the other hand, the coating material 30 contacts the surface 22c of the curtain film 22 of the diluent 40 and flows down along the surface 22c to form the curtain film 12 of the coating material 30.
 すなわち、希釈液40のカーテン膜22と塗料30のカーテン膜12とは、一緒に混じり合うことなく、2層を構成したまま流下することになる。 That is, the curtain film 22 of the diluent 40 and the curtain film 12 of the coating material 30 flow down while constituting two layers without being mixed together.
 ここで、上述した塗料30は、カーテン塗工機1で一般的に用いられる塗料であって、流下したときにカーテン膜12が形成可能なように、なるべく低粘度のものが使用されている。これに対し、希釈液40は、例えば、塗料40を水等で薄めて希釈したものが用いられている。または、水或いは界面活性剤溶液であってもよい。すなわち、この希釈液40は、塗料30に比べて、粘度が低いものが使用される。そのため、上述した塗料30は、低粘度の希釈液40の表面22cに沿って下側に流下し、塗料30は希釈液40よりも粘度が高いために、それぞれが混じり合うことなく2層に分離された状態でそのまま流下するようになる。 Here, the above-described paint 30 is a paint generally used in the curtain coating machine 1 and has a viscosity as low as possible so that the curtain film 12 can be formed when it flows down. On the other hand, as the dilution liquid 40, for example, a dilution obtained by diluting the paint 40 with water or the like is used. Alternatively, it may be water or a surfactant solution. That is, as the dilution liquid 40, a liquid having a lower viscosity than the paint 30 is used. Therefore, the above-described coating material 30 flows down along the surface 22c of the low-viscosity diluent 40, and the coating material 30 has a higher viscosity than the diluent 40. Therefore, the coating material 30 is separated into two layers without mixing each other. It will flow down as it is.
 また、希釈液40は低粘度であることから、塗料30と比較して、ガイドプレート24の表面24cと接触したときに、粘性抵抗が低くなる。そのため、希釈液40がない状態では、塗料30とガイドプレート24の表面24cとが接触すると粘性抵抗が高くなり、適切な速度までカーテン膜を加速することができない。そのため、ガイドプレート24の表面24cと塗料30との間に希釈液40を介在させることで、カーテン終端速度を適切に制御し、塗工膜スキップ等の塗工欠陥が出ないようにしている。 In addition, since the diluent 40 has a low viscosity, the viscosity resistance is low when it comes into contact with the surface 24c of the guide plate 24 as compared with the paint 30. Therefore, in the absence of the diluent 40, when the coating material 30 and the surface 24c of the guide plate 24 come into contact with each other, the viscosity resistance increases, and the curtain film cannot be accelerated to an appropriate speed. Therefore, by interposing the diluent 40 between the surface 24c of the guide plate 24 and the coating material 30, the curtain end speed is appropriately controlled so that coating defects such as coating film skip do not occur.
 そして、塗料30と希釈液40は、前後に2層構造になったままの状態で、高速で走行する塗工紙60上に流下し、塗工紙60上に塗膜面が形成される。塗工後の塗工紙60は、後工程である乾燥工程で乾燥される。このとき、希釈液40は、上述したように、塗料30を薄めたもの、或いは、水であるため、乾燥工程で乾燥した後には、塗料30のみが塗工紙60に残る。そのため、塗工面は、塗料30のみを用いて塗工した場合と同じ品質が確保される。 Then, the coating material 30 and the diluent 40 flow down onto the coated paper 60 that travels at a high speed in a state where the two-layered structure is left and right, and a coating film surface is formed on the coated paper 60. The coated paper 60 after coating is dried in a drying process that is a subsequent process. At this time, as described above, since the diluent 40 is a solution obtained by thinning the paint 30 or water, only the paint 30 remains on the coated paper 60 after drying in the drying process. Therefore, the same quality as the case where it coats using only the coating material 30 is ensured on the coating surface.
 本発明の実施の形態に係るカーテン塗工機1によれば、塗料30よりも粘度が低い希釈液40と接しながら、この希釈液を塗工紙60の近傍まで案内するガイドプレート24を設けているので、この希釈液40のカーテン膜22を挟んだ逆側で、塗料30のカーテン膜12を形成することができる。そのため、塗料30がガイドプレート24と直接接する場合と比較して、粘性抵抗が低い状態でカーテン膜12を流下させることができる。その結果、塗料チャンバ10からの塗料30を低流量で流しても、幅方向で均一で、かつ、安定性の高いカーテン膜12を形成することができる。 According to the curtain coating machine 1 according to the embodiment of the present invention, the guide plate 24 that guides the diluted solution to the vicinity of the coated paper 60 while being in contact with the diluted solution 40 having a viscosity lower than that of the paint 30 is provided. Therefore, the curtain film 12 of the paint 30 can be formed on the opposite side of the dilution liquid 40 across the curtain film 22. Therefore, compared with the case where the coating material 30 is in direct contact with the guide plate 24, the curtain film 12 can be caused to flow down with a low viscous resistance. As a result, even if the paint 30 from the paint chamber 10 is flowed at a low flow rate, the curtain film 12 that is uniform in the width direction and has high stability can be formed.
 また、従来の低流量時には、塗料30がカーテン膜12状にならずに水滴状になって落下することがあったが、低流量でカーテン膜12を形成することができるので、カーテン形成可能な塗工流量を下げることができる。また、塗工紙60上に塗工する塗膜を薄くすることができる。これに加え、ダイコータで塗工する場合と比較して、塗工紙60をより高速で走行させて塗工することができる。 Further, at the time of the conventional low flow rate, the paint 30 sometimes drops in the form of water droplets instead of the curtain film 12, but since the curtain film 12 can be formed at a low flow rate, the curtain can be formed. The coating flow rate can be reduced. Moreover, the coating film applied on the coated paper 60 can be thinned. In addition to this, the coated paper 60 can be coated at a higher speed as compared with the case of coating with a die coater.
 すなわち、ダイコータが低速でしか塗工できないのは、塗料膜の終端速度と吹出速度とがイコールの関係であるため、塗料の自由落下による加速が為されない。そのため、高速度においては膜の引き伸ばし率が大きくなりすぎ、膜が引き伸ばしに追従できず、千切れる現象が起こり、欠陥が生じることにある。一方で、従来のカーテン方式は、自由落下により加速されるため、より高速度での塗工には向くものの、低塗工量ではカーテン膜が形成できないデメリットがあった。本発明の実施形態に係るカーテン塗工機1は、それらのメリットを両立したものである。 That is, the reason why the die coater can be applied only at a low speed is that the termination speed of the paint film and the blowing speed are equal, so that acceleration due to free fall of the paint is not performed. For this reason, at a high speed, the stretch rate of the film becomes too large, the film cannot follow the stretch, and a phenomenon that the film is cut off occurs, resulting in a defect. On the other hand, since the conventional curtain system is accelerated by free fall, it is suitable for coating at a higher speed, but has a disadvantage that a curtain film cannot be formed with a low coating amount. The curtain coating machine 1 according to the embodiment of the present invention satisfies both of these merits.
 さらには、従来のカーテン塗工機において、塗工紙60の走行気流によってカーテン膜の乱れを防ぐために、カーテン膜の近傍にエアカット装置を追加で装備することがあったが、ガイドプレート24を設けることによってカーテン膜12の乱れを防止できるため、エアカット装置を設ける必要がなくなる。 Furthermore, in the conventional curtain coating machine, in order to prevent the curtain film from being disturbed by the traveling air current of the coated paper 60, an air cut device may be additionally provided in the vicinity of the curtain film. By providing, it is possible to prevent the curtain film 12 from being disturbed, so that it is not necessary to provide an air cut device.
 また、カーテン塗工機用ヘッド2の内部に、希釈液40を貯留して下側に向けて流下させる希釈液チャンバ40を設けているので、ヘッド10の内部に塗料30のみならず、希釈液40も貯留し、流下させることができる。 Moreover, since the diluent chamber 40 is provided in the curtain coating machine head 2 to store the diluent 40 and flow downward, not only the paint 30 but also the diluent is provided in the head 10. 40 can also be stored and flowed down.
 以上、本発明の実施の形態に係るカーテン塗工機1について述べたが、本発明は既述の実施形態に限定されるものではなく、本発明の技術思想に基づいて各種の変形および変更が可能である。 The curtain coating machine 1 according to the embodiment of the present invention has been described above, but the present invention is not limited to the above-described embodiment, and various modifications and changes can be made based on the technical idea of the present invention. Is possible.
 例えば、本実施の形態では、紙、段ボールなどの塗工紙60に塗工するように記載したが、これに限定されない。例えば、プラスチックフィルムなどの紙以外の基材上に膜を形成する場合にも、適用することができる。 For example, in the present embodiment, it is described that the coating is performed on the coated paper 60 such as paper or cardboard, but the present invention is not limited to this. For example, the present invention can also be applied when a film is formed on a base material other than paper such as a plastic film.
 また、本実施の形態では、ヘッド10には、塗料チャンバ10と希釈液チャンバ20とをそれぞれ1つずつ設けているが、複数設けて多色刷りに対応するようにしてもよい。 In this embodiment, the head 10 is provided with one paint chamber 10 and one diluent chamber 20, but a plurality of them may be provided to cope with multicolor printing.
 さらに、本実施の形態では、ヘッド10の内部に希釈液40を貯留する希釈液チャンバ20を設けているが、ヘッド10と別体で構成することもできる。 Furthermore, in the present embodiment, the diluent chamber 20 for storing the diluent 40 is provided inside the head 10, but may be configured separately from the head 10.
 1 カーテン塗工機
 2 カーテン塗工機用ヘッド(ヘッド)
 3、4 供給パイプ
 5 側壁部
 6 固定ボルト
 10 塗料チャンバ
 11 ノズル
 12 塗料のカーテン膜
 13 塗料側本体部
 14 中間部
 15 固定ボルト
 20 希釈液チャンバ(低粘度液チャンバ)
 21 ノズル
 22 希釈液のカーテン膜
 23 希釈液側本体部
 24 ガイドプレート
 30 塗料
 40 希釈液(低粘度液)
 60 塗工紙(基材)
 G 下端部
1 Curtain coating machine 2 Curtain coating machine head (head)
3, 4 Supply pipe 5 Side wall part 6 Fixing bolt 10 Paint chamber 11 Nozzle 12 Paint curtain film 13 Paint side main body part 14 Intermediate part 15 Fixing bolt 20 Diluent chamber (low viscosity liquid chamber)
21 Nozzle 22 Diluted liquid curtain film 23 Diluted liquid side main body 24 Guide plate 30 Paint 40 Diluted liquid (low viscosity liquid)
60 coated paper (base material)
G Lower end

Claims (3)

  1.  塗工される基材の幅方向に沿って長尺に形成され、この幅方向に延在する塗料チャンバを有し、この塗料チャンバ内に塗工用の塗料が供給され、カーテン膜状に前記塗料を流下するカーテン塗工機用ヘッドを備えたカーテン塗工機において、
     前記塗料よりも粘度が低い低粘度液と接しながら、この低粘度液を前記基材の近傍まで案内するガイドプレートを設けたことを特徴とするカーテン塗工機。
    The paint chamber is formed in a length along the width direction of the substrate to be coated, and extends in the width direction. In curtain coating machine equipped with a head for curtain coating machine that flows down the paint,
    A curtain coating machine provided with a guide plate that guides the low-viscosity liquid to the vicinity of the substrate while in contact with the low-viscosity liquid having a viscosity lower than that of the paint.
  2.  前記カーテン塗工機用ヘッドの内部に、前記低粘度液を貯留して下側に向けて流下させる低粘度液チャンバを設けたことを特徴とする請求項1に記載のカーテン塗工機。 The curtain coating machine according to claim 1, wherein a low-viscosity liquid chamber for storing the low-viscosity liquid and flowing it downward is provided inside the curtain coating machine head.
  3.  前記低粘度液が、前記塗料を薄めた希釈液または水であることを特徴とする請求項1または請求項2に記載のカーテン塗工機。 The curtain coating machine according to claim 1 or 2, wherein the low-viscosity liquid is a diluted liquid or water in which the paint is diluted.
PCT/JP2012/057585 2012-03-23 2012-03-23 Curtain coater WO2013140620A1 (en)

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PCT/JP2012/057585 WO2013140620A1 (en) 2012-03-23 2012-03-23 Curtain coater

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Cited By (1)

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Publication number Priority date Publication date Assignee Title
WO2020203616A1 (en) * 2019-03-29 2020-10-08 日本製紙株式会社 Method for manufacturing paper-making barrier substrate

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JP2001046939A (en) * 1999-08-11 2001-02-20 Mitsubishi Paper Mills Ltd Coating device and coating method
JP2008525649A (en) * 2004-12-23 2008-07-17 ボイス パテント ゲーエムベーハー Method for directly coating multiple layers on paper, cardboard or other moving webs of fiber material

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JP2001046939A (en) * 1999-08-11 2001-02-20 Mitsubishi Paper Mills Ltd Coating device and coating method
JP2008525649A (en) * 2004-12-23 2008-07-17 ボイス パテント ゲーエムベーハー Method for directly coating multiple layers on paper, cardboard or other moving webs of fiber material

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020203616A1 (en) * 2019-03-29 2020-10-08 日本製紙株式会社 Method for manufacturing paper-making barrier substrate
JP7331314B2 (en) 2019-03-29 2023-08-23 日本製紙株式会社 Method for producing paper barrier substrate
US11834791B2 (en) 2019-03-29 2023-12-05 Nippon Paper Industries Co., Ltd. Method for manufacturing paper barrier base material

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