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JPH028786B2 - - Google Patents
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JPH028786B2 - - Google Patents

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Publication number
JPH028786B2
JPH028786B2 JP4026582A JP4026582A JPH028786B2 JP H028786 B2 JPH028786 B2 JP H028786B2 JP 4026582 A JP4026582 A JP 4026582A JP 4026582 A JP4026582 A JP 4026582A JP H028786 B2 JPH028786 B2 JP H028786B2
Authority
JP
Japan
Prior art keywords
liquid
knife
coating
discharge port
pool
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
Application number
JP4026582A
Other languages
Japanese (ja)
Other versions
JPS58159868A (en
Inventor
Teruo Furusawa
Joichi Saito
Toshihiko Fujita
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.)
Nippon Polyurethane Industry Co Ltd
Original Assignee
Nippon Polyurethane Industry Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nippon Polyurethane Industry Co Ltd filed Critical Nippon Polyurethane Industry Co Ltd
Priority to JP4026582A priority Critical patent/JPS58159868A/en
Publication of JPS58159868A publication Critical patent/JPS58159868A/en
Publication of JPH028786B2 publication Critical patent/JPH028786B2/ja
Granted legal-status Critical Current

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  • Coating Apparatus (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)

Description

【発明の詳細な説明】 本発明はシヨツトマークがなく、外観や物性の
均質な硬化製品が得られる改良された塗工方法に
関する。本発明はまた、反応硬化性樹脂液を混合
装置から連続的あるいは間歇的に吐出させた場
合、硬化製品に生じる表面欠陥を解消する方法に
かかわるものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improved coating method that provides a cured product free of shot marks and with uniform appearance and physical properties. The present invention also relates to a method for eliminating surface defects that occur in a cured product when a reactively curable resin liquid is discharged continuously or intermittently from a mixing device.

配合機等で計量混合した反応硬化性樹脂液を、
紙、布、プラスチツクフイルムあるいは金属箔の
ようなシート状物や、木板、金属板、プラスチツ
ク板のような板物の基材上に吐出流下し、これを
ナイフコーター等の延べ塗り装置で塗工した後、
室温で放置するか、オーブンやヒートプレートそ
の他のキユアリング装置を通過させて硬化製品を
得る加工方法がよく行われている。このような加
工方法では、硬化製品の表面の液を吐出流下した
部位にのみ他の表面と異なつた外観が現出する。
この表面の模様は“シヨツトマーク”と呼ばれ、
硬化製品の美的価値を著しく低下させるだけでな
く表面性状が物性が不均質であるため商品価値を
著しく害するものである。このシヨツトマーク
は、吐出流下する液と、既に吐出されコーターの
液溜りに滞留する液との物性差や反応性差によつ
て生じるものと思われるが、上述のような加工方
法では不可避なものであつた。
The reactive hardening resin liquid is measured and mixed using a compounding machine, etc.
It is discharged onto a sheet material such as paper, cloth, plastic film, or metal foil, or onto a base material such as a wooden board, metal plate, or plastic board, and then coated with a spreading coating device such as a knife coater. After that,
Common processing methods include leaving the product at room temperature or passing it through an oven, heat plate, or other curing device to obtain a cured product. In such a processing method, only the portions of the surface of the cured product where the liquid has been discharged and flowed appear to have an appearance that is different from the rest of the surface.
This surface pattern is called a “shot mark”.
This not only significantly reduces the aesthetic value of the cured product, but also significantly impairs its commercial value due to its non-uniform surface properties. These shot marks are thought to be caused by differences in physical properties and reactivity between the liquid flowing down and the liquid that has already been discharged and remains in the coater's pool, but they are unavoidable in the processing method described above. Ta.

一方、このシヨツトマークをなくすためにナイ
フコーター等の延べ塗り装置を廃し、吐出液をダ
イストリツトから薄膜にして流下させる方法があ
るが、この場合均一な厚みに塗工するためには厳
密なダイ設計が必面であり、吐出液の送液やその
粘度範囲に十分な注意を払う必要がある。従つ
て、このような塗工設備は非常に高価であり、ま
た塗工条件等の管理を厳しく行わなければならな
い。
On the other hand, in order to eliminate this shot mark, there is a method of eliminating the need for a continuous coating device such as a knife coater and letting the discharged liquid flow down a die strip in the form of a thin film, but in this case, strict die design is required to ensure uniform coating thickness. This is essential, and it is necessary to pay sufficient attention to the delivery of the ejected liquid and its viscosity range. Therefore, such coating equipment is very expensive, and coating conditions etc. must be strictly controlled.

本発明は、機構が簡単であり塗工管理も容易な
ナイフコーター等の延べ塗り装置による塗工で、
シヨツトマークがなく外観や物性の均質な硬化製
品が得られる改良された塗工方法を提供するもの
である。
The present invention is a coating method using a continuous coating device such as a knife coater, which has a simple mechanism and easy coating management.
The object of the present invention is to provide an improved coating method that allows a cured product with uniform appearance and physical properties to be obtained without shot marks.

ナイフコーター等の延べ塗り装置による塗工で
は塗工方向に対して直角に交叉する方向にナイフ
等の障壁が配置されているので、この障壁の前面
に吐出された液の一部が堰止められて滞留し液溜
りをつくる。この液溜り液はナイフ障壁に接触し
ながら基材の進行によつて、進行方向に対して直
角に交叉する回転軸をもつて回転する。液溜り液
の上部表面は、進行方向に対して手前から見ると
上部から下部に回り込んで基材に接触付着し、液
溜り中に潜り込む。このようにして、液溜り液の
一部は、ナイフブレード等の先端の間隙を通過し
て塗工されていくが、この減少分は液の吐出口か
ら連続的または間歇的に供給される。
When coating with a spreading coating device such as a knife coater, a barrier such as a knife is placed in a direction perpendicular to the coating direction, so a portion of the liquid discharged in front of this barrier is dammed up. The liquid accumulates and forms a puddle. This pooled liquid rotates with a rotation axis perpendicular to the direction of movement as the substrate advances while contacting the knife barrier. The upper surface of the puddle liquid, when viewed from the front in the direction of travel, wraps around from the top to the bottom, contacts and adheres to the base material, and sinks into the puddle. In this way, a portion of the pooled liquid passes through the gap at the tip of the knife blade or the like and is applied, but this reduced amount is supplied continuously or intermittently from the liquid outlet.

したがつて、従来のような反応硬化性樹脂液を
基材上に直接吐出流下する場合や液溜り上に吐出
流下する場合では、既に吐出されて液溜りとして
滞留する液と新たに吐出流下された液が十分に拡
散混合しない状態で基材に接触するのでシヨツト
マークを生じてしまうものと思われる。
Therefore, when discharging a reaction-curable resin liquid directly onto a substrate or discharging it down onto a liquid pool as in the past, there is a difference between the liquid that has already been discharged and remains in the pool and the liquid that is newly discharged and flowing down. It is thought that shot marks are produced because the liquid comes into contact with the substrate without being sufficiently diffused and mixed.

我々は液溜り液の滞留について詳細な検討を行
つた結果、混合装置から連続的あるいは間歇的に
吐出される反応硬化性樹脂液をナイフコーター等
の延べ塗り装置で塗工する場合、硬化製品にシヨ
ツトマークがなく外観や物性が均質であるような
次のような改良された塗工方法の発明に到達し
た。すなわち、ナイフコーター等において回転す
る液溜り液の回転中心軸近傍に液吐出口を位置さ
せ、これを液溜り中でナイフ等の障壁に沿う方向
に左右に往復運動させ塗工を行う方法である。こ
の場合、混合装置から吐出される液は、回転して
いる液溜り液の回転中心軸近傍の軸方向全域にわ
たつて絶えず供給されることになる。
As a result of a detailed study on the retention of liquid puddles, we found that when applying reactive curing resin liquid that is continuously or intermittently discharged from a mixing device with a continuous coating device such as a knife coater, The following improved coating method has been invented which has no shot marks and has uniform appearance and physical properties. That is, in a knife coater or the like, a liquid discharge port is located near the central axis of rotation of a rotating liquid pool, and the coating is performed by reciprocating the liquid from side to side in the direction along a barrier such as a knife in the liquid pool. . In this case, the liquid discharged from the mixing device is constantly supplied over the entire axial direction of the rotating liquid pool near the rotation center axis.

本発明を実施するにあたり混合装置としては、
ウレタン発泡機のようなギヤーポンプで連続的に
ミキシングヘツドに送液し、ここで回転撹拌して
直ちに吐出できる装置や、エポキシ樹脂等の配合
機としてよく使用されているプランジヤーで間歇
的にミキシングヘツドに導き静的混合エレメント
を通して混合吐出するような装置、あるいはこれ
らの組合せからなるような装置が使用できる。こ
れらの中、ギヤーポンプで連続的に送液し、連続
的に混合吐出するような装置が特に好ましい。
In carrying out the present invention, the mixing device includes:
A gear pump such as a urethane foaming machine is used to continuously send the liquid to the mixing head, where it is rotated and stirred, and the liquid is immediately discharged. Alternatively, a plunger, which is often used as a compounding machine for epoxy resin, etc., is used to intermittently send the liquid to the mixing head. Devices that mix and discharge through guided static mixing elements, or combinations thereof, can be used. Among these, a device that continuously feeds the liquid with a gear pump and continuously mixes and discharges the liquid is particularly preferred.

ナイフコーター等の延べ塗り装置としては、掻
板や掻棒で液溜りをつくりつつ塗工する装置なら
どれでもよいが、一般にナイフコーターが好まし
い。ナイフコーターの形式としては、フローテイ
ングナイフ、ナイフオーバーロール、ナイフオー
バーブランケツト等のどの形式でもよく、ナイフ
形状も円弧ナイフ、ホツクナイフ、せき板ナイ
フ、スパニツシングナイフ、牛の鼻型ナイフ、丸
棒ナイフ等のどの形状も用いられるが、これらの
選択は、塗布量、液の粘性、塗工速度等の塗工目
的や条件に従つて行えばよい。
As a spreading coating device such as a knife coater, any device that coats while creating a liquid pool with a scraper plate or scraper may be used, but a knife coater is generally preferred. The knife coater may be of any type, such as a floating knife, knife over roll, knife over blanket, etc., and the knife shape may be an arc knife, a hook knife, a weir knife, a spanishing knife, a cow nose knife, or a round knife. Any shape such as a stick knife can be used, and the selection thereof may be made according to the coating purpose and conditions such as coating amount, liquid viscosity, and coating speed.

また、液溜り中に吐出口を導入し、左右に往復
運動させる方法としては、ミキシングヘツドの吐
出口を液溜り中に挿入し、これら一体を油圧や電
動機で駆動されるトラバース装置に接合して運動
させる方法や、静置固定してあるミキシングヘツ
ドの吐出口に可撓性のあるホースを接続し、この
ホース先端を液溜り中に導入してトラバースさせ
る方法などがある。
In addition, a method of introducing a discharge port into a liquid pool and causing it to reciprocate from side to side is to insert the discharge port of the mixing head into the liquid pool and connect the two together to a traverse device driven by hydraulic pressure or an electric motor. There is a method of moving the fluid, and a method of connecting a flexible hose to the discharge port of a stationary mixing head and introducing the end of this hose into a liquid pool and traversing it.

一方、本発明での反応硬化性樹脂液としては、
ウレタン樹脂、エポキシ樹脂、シリコン樹脂、不
飽和ポリエステル樹脂、ポリジエン系液状ゴム、
ポリサルフアイド樹脂などの液状樹脂を硬化剤や
反応開始剤で反応硬化させるようなものであり、
ナイフコーター等の延べ塗り装置で塗工を実施す
るために、これらの混合液の粘度は100〜100000
センチポイズ、特に1000〜10000センチポイズで
あることが望ましい。
On the other hand, the reaction-curable resin liquid in the present invention is as follows:
Urethane resin, epoxy resin, silicone resin, unsaturated polyester resin, polydiene liquid rubber,
It is like curing liquid resin such as polysulfide resin by reaction with a curing agent or a reaction initiator.
The viscosity of these mixed liquids must be 100 to 100,000 in order to perform coating with a spreading coating device such as a knife coater.
Centipoise, especially 1000 to 10000 centipoise, is desirable.

本発明は、ラミネート製品としてフオームパツ
キング付織布、運送用ベルト、シート状製品とし
てパツキングシート、防水材、被覆製品としてデ
コレーシヨンパネル、合成皮革、ターポリンなど
の外観のすぐれた高品質の製品が得られるので、
極めて有用である。
The present invention provides high quality products with excellent appearance, such as laminated products such as woven fabrics with foam packing, transportation belts, sheet products such as packing sheets, waterproof materials, and coated products such as decorative panels, synthetic leather, and tarpaulins. is obtained, so
Extremely useful.

以下に、本発明の実施例、比較例を示す。 Examples and comparative examples of the present invention are shown below.

実施例 1 ナイフオーバーブラケツトコーターと6m長の
オーブンをもつ塗工装置にクリツプテンターで端
部をつかんだ朱子織ガラス布EC#181VT(日東紡
績(株)製)をセツトし、進行方向に30Kg/mガラス
布巾の張力をかけ、ホツクナイフとブランケツト
の間に介在させた。オーブン温度を120℃として
から、ガラス布上にシリコーン樹脂KE1204(A―
B)LTV(信越化学工業(株)製)をオートスペンサ
EP201S配合機((株)オートマシンン開発製)を用
いて計量混合し、430g/分で吐出させながら1
m巾を6m/分の速度で吐出口をトラバースさ
せ、ナイフ障壁前に液溜りをつくつた。同時に塗
布巾1.2mとなるようにエツジダムを設置し、2
m/分の速度でガラス布を送ると液溜り液は約30
mm径のロール状となつてナイフ障壁に付着しなが
ら回転し塗工される。次に、吐出口を液溜りの上
から液溜り中に挿入し、液溜りの回転中心軸近傍
に位置させ、以後この状態で塗工を継続した。
Example 1 A satin woven glass cloth EC#181VT (manufactured by Nitto Boseki Co., Ltd.) whose ends were gripped with a clip tenter was set in a coating device equipped with a knife-over bracket coater and a 6 m long oven, and 30 kg/g was applied in the direction of travel. A glass cloth was placed under tension and interposed between the hook knife and the blanket. After increasing the oven temperature to 120℃, apply silicone resin KE1204 (A-
B) Autospenser LTV (manufactured by Shin-Etsu Chemical Co., Ltd.)
Weigh and mix using an EP201S compounding machine (manufactured by Automachine Kaihatsu Co., Ltd.), and while dispensing at a rate of 430 g/min.
The discharge port was traversed over a width of m at a speed of 6 m/min to create a pool of liquid in front of the knife barrier. At the same time, an edge dam was installed so that the coating width was 1.2 m, and 2
When the glass cloth is fed at a speed of m/min, the liquid pool is approximately 30 m/min.
It is rolled into a roll with a diameter of mm and is applied by rotating while adhering to the knife barrier. Next, the discharge port was inserted into the liquid pool from above and positioned near the central axis of rotation of the liquid pool, and thereafter coating was continued in this state.

硬化した塗工製品の表面を調べたところ、吐出
口を液溜り中に挿入する前は、トラバースした道
筋通りのジグザグ状のシヨツトマークが見られた
が、吐出口を液溜り液中の回転中心軸近傍に位置
させてからは、シヨツトマークが全く見られず、
表面は平滑で美麗であつた。
When we examined the surface of the cured coated product, we found that before the discharge port was inserted into the liquid pool, there were zigzag-like shot marks along the traversed route, but when the discharge port was inserted into the liquid pool, the center of rotation of the product was observed. After positioning it nearby, I could not see any shot marks at all.
The surface was smooth and beautiful.

実施例 2 ナイフオーバーロールコーターと6m長のオー
ブンをもつ塗工装置に離型処理された工程紙EK
―120D2(創研化工(株)製)をセツトし、円弧ナイ
フの間隙を0.5mmに設定した。オーブン温度を135
℃としてから、工程紙上にウレタン樹脂アジプレ
ンL―315/カイチユール21(デユポン社製)をオ
ートスペンサーEP201S配合機((株)オートマシン
開発)を用いて計量混合し、520g/分で吐出さ
せながら1m巾を6m/分の速度で吐出口をトラ
バースさせ、ナイフ障壁前に液溜りをつくつた。
同時に塗布巾1.2mとなるようにエツジダムを設
置し、1.2m/分の速度で工程紙を送ると液溜り
液は、高さ約20mm、巾約100mmの偏平な楕円柱状
となつてナイフ障壁に付着しながら回転し、塗工
される。次に、吐出口を液溜りの上から液溜り中
に挿入し、液溜りの回転中心軸(これは透明なエ
ツジダム板を通して回転体の横断面を観察するこ
とによつて見出される)近傍に位置させ、以後こ
の状態で塗工を継続した。
Example 2 Process paper EK subjected to mold release treatment using a coating device with a knife over roll coater and a 6m long oven.
-120D 2 (manufactured by Soken Kako Co., Ltd.) was set, and the gap between the arc knives was set to 0.5 mm. Oven temperature 135
℃, then measure and mix the urethane resin Adiprene L-315/Kaitiyur 21 (manufactured by Dupont) on process paper using an Auto Spencer EP201S compounding machine (Developed by Auto Machine Co., Ltd.), and dispense it at a rate of 520 g/min for 1 m. The discharge port was traversed across the width at a speed of 6 m/min to create a pool in front of the knife barrier.
At the same time, an edge dam is installed so that the coating width is 1.2 m, and when the process paper is fed at a speed of 1.2 m/min, the pooled liquid becomes a flat elliptical column with a height of about 20 mm and a width of about 100 mm, forming a knife barrier. It rotates while adhering and is coated. Next, insert the discharge port into the liquid pool from above and position it near the central axis of rotation of the liquid pool (this can be found by observing the cross section of the rotating body through a transparent edge dam plate). After that, coating was continued in this state.

硬化した塗工製品の表面を調でたところ、吐出
口を液溜り中に挿入する前は、トラバースした道
筋通りのジグザグ状のシヨツトマークが見られた
が、吐出口を液溜り液中の回転中心軸近傍に位置
させてからは、シヨツトマークが全く見られず、
表面は平滑美麗であつた。
When the surface of the cured coated product was examined, a zigzag-like shot mark was seen along the traversed route before the discharge port was inserted into the liquid pool, but when the discharge port was inserted into the liquid pool as the center of rotation, After positioning it near the axis, no shot marks were visible at all.
The surface was smooth and beautiful.

実施例 3 実施例1で配合機のみを間歇計量混合タイプの
ツインフロー(仲精機(株)製)にかえ、205g/シ
ヨツトで吐出させた。シヨツト数は1分間に約2
回であつた。この場合も、吐出口を液溜り中に挿
入して塗工した硬化製品にはシヨツトマークが全
く見られなかつた。
Example 3 In Example 1, only the blender was changed to an intermittent metering and mixing type Twin Flow (manufactured by Naka Seiki Co., Ltd.), and the mixture was discharged at 205 g/shot. The number of shots is approximately 2 per minute.
It was hot. In this case as well, no shot marks were observed in the cured product coated by inserting the discharge port into the liquid pool.

比較例 実施例1、2及び3で、吐出口を液溜り中に挿
入しながら塗工を行つているとき、吐出口のトラ
バースを停止すると、硬化製品に直線状の太いシ
ヨツトマークが現われた。
Comparative Example In Examples 1, 2, and 3, when coating was performed while inserting the discharge port into the liquid pool, when the traverse of the discharge port was stopped, thick linear shot marks appeared on the cured product.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は塗工設備の斜視図で、フローテイン
グ・ナイフコーターの例である。 主要部分の符号の説明、…ミキシングヘツ
ド、…ナイフコーター、…エツジダム、…
液溜り、…吐出口、…被塗布基材。 第2図は要部の拡大断面図で、吐出口の液溜り
中での位置を示す。 主要部分の符号の説明、…ミキシングヘツ
ド、…ナイフコーター、 3′ …吐出口、…液
溜り、 5′ …被塗布基材、 6′ …バツクロール。
Figure 1 is a perspective view of the coating equipment, which is an example of a floating knife coater. Explanation of the symbols of the main parts, ...mixing head, ...knife coater, ...edge dam, ...
Liquid reservoir,...discharge port,...substrate to be coated. FIG. 2 is an enlarged sectional view of the main part, showing the position of the discharge port in the liquid pool. Explanation of the symbols of the main parts, ...mixing head, ...knife coater, 3' ...discharge port, ...liquid reservoir, 5' ...substrate to be coated, 6' ...back roll.

Claims (1)

【特許請求の範囲】[Claims] 1 混合装置から連続的あるいは間歇的に吐出さ
れる反応硬化性樹脂液をナイフコーター等の延べ
塗り装置を用いて塗工する際、該コーナーにおい
て回転する液溜り液の回転中心軸近傍に液吐出口
を位置させ、液溜り中をナイフ等の障壁に沿う方
向に左右に往復運動させることを特徴とする塗工
方法。
1. When applying a reactive hardening resin liquid that is continuously or intermittently discharged from a mixing device using a spreading coating device such as a knife coater, the liquid is discharged near the central axis of rotation of the liquid puddle that rotates at the corner. A coating method characterized by locating an outlet and causing the liquid to reciprocate from side to side in a direction along a barrier such as a knife in a liquid pool.
JP4026582A 1982-03-16 1982-03-16 Improved method of coating Granted JPS58159868A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4026582A JPS58159868A (en) 1982-03-16 1982-03-16 Improved method of coating

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4026582A JPS58159868A (en) 1982-03-16 1982-03-16 Improved method of coating

Publications (2)

Publication Number Publication Date
JPS58159868A JPS58159868A (en) 1983-09-22
JPH028786B2 true JPH028786B2 (en) 1990-02-27

Family

ID=12575816

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4026582A Granted JPS58159868A (en) 1982-03-16 1982-03-16 Improved method of coating

Country Status (1)

Country Link
JP (1) JPS58159868A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4316757B2 (en) * 1999-12-28 2009-08-19 三井化学株式会社 Method for continuous coating of thermosetting polyurethane and method for producing thermosetting polyurethane sheet
JP4857813B2 (en) * 2005-03-11 2012-01-18 東レ株式会社 Coating apparatus, coating method, and method for producing coating film forming web

Also Published As

Publication number Publication date
JPS58159868A (en) 1983-09-22

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