JPH10128201A - Hard substrate coating device and its control method - Google Patents
Hard substrate coating device and its control methodInfo
- Publication number
- JPH10128201A JPH10128201A JP30391496A JP30391496A JPH10128201A JP H10128201 A JPH10128201 A JP H10128201A JP 30391496 A JP30391496 A JP 30391496A JP 30391496 A JP30391496 A JP 30391496A JP H10128201 A JPH10128201 A JP H10128201A
- Authority
- JP
- Japan
- Prior art keywords
- coating liquid
- coating
- level
- liquid
- tank
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000011248 coating agent Substances 0.000 title claims abstract description 144
- 238000000576 coating method Methods 0.000 title claims abstract description 144
- 239000000758 substrate Substances 0.000 title claims abstract description 47
- 238000000034 method Methods 0.000 title claims description 12
- 239000007788 liquid Substances 0.000 claims abstract description 168
- 239000011521 glass Substances 0.000 description 14
- 239000002904 solvent Substances 0.000 description 9
- 239000002184 metal Substances 0.000 description 5
- 230000032258 transport Effects 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 239000004973 liquid crystal related substance Substances 0.000 description 4
- 229920002120 photoresistant polymer Polymers 0.000 description 4
- 238000001514 detection method Methods 0.000 description 3
- 230000006870 function Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000007423 decrease Effects 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 238000004804 winding Methods 0.000 description 2
- 235000010724 Wisteria floribunda Nutrition 0.000 description 1
- 230000003254 anti-foaming effect Effects 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 238000002834 transmittance Methods 0.000 description 1
Landscapes
- Coating Apparatus (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、ガラス基板を用い
た液晶表示板などの製造に用いられ、フォトレジストな
どの塗布液を硬基板に薄く均一に塗布するための硬基板
塗布装置とその制御方法とに関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hard substrate coating apparatus used for manufacturing a liquid crystal display panel or the like using a glass substrate, and a thin substrate coating apparatus for applying a coating liquid such as a photoresist to a hard substrate uniformly. Method and.
【0002】[0002]
【従来の技術】液晶板の製造工程の中には、ガラス基板
などの硬基板にフォトレジストなどの塗布液を薄く均一
な厚さに塗布する工程がある。例えばカラー液晶板の製
造においては、透明電極を予め形成したガラス基板に、
フォトレジストの機能を有する赤のカラ−モザイク液を
均一に塗布した後、露光して赤に対応するカラ−モザイ
クを硬化させ、余分の液を除去することにより赤のカラ
ーモザイクを形成している。そしてこれと同様な処理を
緑、青、黒、透明などの他の色について繰り返してい
る。このようにフォトレジストとなる塗布液を塗布する
場合、この液は均一な厚さ(例えば1μ±3%程度)に
厳密に管理して薄く塗布する必要がある。この塗布の厚
さが不均一であると、光の透過率のむらが生じ、品質の
低下を招くことになるからである。2. Description of the Related Art In a manufacturing process of a liquid crystal plate, there is a process of applying a coating liquid such as a photoresist to a thin and uniform thickness on a hard substrate such as a glass substrate. For example, in the production of a color liquid crystal plate, a transparent electrode is formed on a glass substrate in advance,
After uniformly applying a red color mosaic liquid having the function of a photoresist, the color mosaic corresponding to the red color is cured by exposure, and an excess liquid is removed to form a red color mosaic. . The same processing is repeated for other colors such as green, blue, black, and transparent. When a coating liquid to be a photoresist is applied as described above, the liquid needs to be strictly controlled to have a uniform thickness (for example, about 1 μ ± 3%) and to be applied thinly. This is because if the thickness of the coating is non-uniform, the light transmittance becomes uneven, which leads to a deterioration in quality.
【0003】従来はこの塗布のためにスピンコータが用
いられていた。このスピンコータは回転させた基板の回
転中心付近に塗布液を滴下し、この液を遠心力を利用し
て飛散させることにより塗布するものである。しかしこ
のスピンコータを用いる方法では基板の交換に手間取り
作業能率が悪くなるばかりでなく、飛散して捨てられる
液の量が増えることになる。このためコストアップにな
るという問題があった。Conventionally, a spin coater has been used for this coating. In this spin coater, a coating liquid is dropped near a rotation center of a rotated substrate, and the liquid is applied by scattering using a centrifugal force. However, in the method using the spin coater, not only the time and labor efficiency for replacing the substrate are deteriorated, but also the amount of the liquid scattered and discarded increases. For this reason, there was a problem that the cost was increased.
【0004】そこで水平に配設された上下一対のローラ
間に基板を挟んで塗布する装置を用いることが考えられ
ている。この装置は下のローラとなるマイクロロッドバ
ーの下部を塗布液に浸漬し、このマイクロロッドバーと
この上方に位置するニップローラとの間に基板を挟んで
送りながら、マイクロロッドバーにより基板の下面に塗
布するものである。In view of this, it has been considered to use an apparatus for coating a substrate between a pair of upper and lower rollers disposed horizontally. In this device, the lower part of the micro rod bar, which is the lower roller, is immersed in the coating solution, and the substrate is sandwiched between the micro rod bar and the nip roller located above the micro rod bar. It is to be applied.
【0005】ここにマイクロロッドバーは断面円形の金
属ロッドの表面に細い金属ワイヤを密着するように巻き
付けたもので、金属ワイヤ間の溝による毛細管現象を利
用して液を塗布するものである。Here, the micro rod bar is formed by winding a thin metal wire in close contact with the surface of a metal rod having a circular cross section, and applies a liquid by utilizing a capillary phenomenon caused by a groove between the metal wires.
【0006】[0006]
【従来技術の問題点】この装置では、タンクから塗布液
槽に塗布液を送る供給系や、塗布液槽内の液が淀んだり
するのを防ぐために定常流を作る循環系を有する。しか
しこれらの送液系配管や循環系配管内の空気が液と混合
して塗布液槽に供給した塗布液に気泡が混入するという
問題があった。この気泡が硬基板の塗布面に付くと、塗
布の欠陥となる。そこで従来は、送液、循環が始まる
と、塗布液槽直前で配管をはずして中の気泡が無くなる
まで塗布液を別の容器に棄て、気泡が無くなった所で配
管を塗布液槽に継ぎ込んでいた。このように配管をはず
して、気泡混入した液を棄てる作業が煩雑で、時間がか
かり、稼働率の低下を招くという問題があった。また無
駄になる塗布液の量も増えるという問題もあった。This apparatus has a supply system for feeding a coating solution from a tank to a coating solution tank and a circulation system for generating a steady flow in order to prevent the solution in the coating solution tank from stagnating. However, there is a problem that air in the liquid supply pipe and the circulation pipe is mixed with the liquid and bubbles are mixed into the coating liquid supplied to the coating liquid tank. If these bubbles adhere to the coating surface of the hard substrate, they cause coating defects. Therefore, conventionally, when liquid supply and circulation start, the pipe is removed immediately before the coating liquid tank, the coating liquid is discarded in another container until the air bubbles disappear, and the pipe is connected to the coating liquid tank when the air bubbles disappear. Was out. Thus, there is a problem that the operation of removing the pipe and discarding the liquid containing bubbles is complicated, takes time, and lowers the operation rate. There is also a problem that the amount of the coating liquid wasted increases.
【0007】[0007]
【発明の目的】この発明はこのような事情に鑑みなされ
たものであり、塗布液槽に混入した気泡を自動で除去
し、作業が簡単で装置の嫁働率を向上させることができ
る硬基板塗布装置の制御方法を提供することを第1の目
的とする。SUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances, and has been made in consideration of the above circumstances. The present invention has been made in consideration of the above circumstances, and has been made in consideration of the above circumstances. A first object is to provide a control method of the device.
【0008】またこの方法の実施に直接使用する硬基板
塗布装置を提供することを第2の目的とする。It is a second object of the present invention to provide a hard substrate coating apparatus used directly for carrying out this method.
【0009】[0009]
【発明の構成】本発明によれば第1の目的は、下部が塗
布液槽に浸漬されたマイクロロッドバーと、このマイク
ロロッドバーの上方に対向配置されたニップローラとの
間に、硬基板を挟んで送ることにより、硬基板の下面に
塗布液を塗布する硬基板塗布装置の制御方法において、
前記塗布液槽に塗布時基準レベルより低い泡抜きレベル
までこの泡抜きレベルより僅かに高い吐出口より塗布液
を供給し、塗布液供給系の配管内の空気を塗布液と置換
した後、前記塗布液槽内の塗布液を循環ポンプとの間で
循環させてこの循環系の配管内の空気を塗布液で完全に
置換し、その後塗布液槽に塗布液を追加供給して前記基
準レベルにすることを特徴とする硬基板塗布装置の制御
方法、により達成される。According to the present invention, a first object is to provide a hard substrate between a micro rod bar whose lower part is immersed in a coating solution tank and a nip roller facing above the micro rod bar. In the control method of the hard substrate coating apparatus that applies the coating liquid to the lower surface of the hard substrate by sandwiching and sending,
The coating solution is supplied to the coating solution tank from a discharge port slightly higher than the bubble removal level up to the bubble removal level lower than the reference level at the time of application, and the air in the pipe of the coating solution supply system is replaced with the coating solution. The coating liquid in the coating liquid tank is circulated between the circulating pump and the air in the piping of the circulation system is completely replaced with the coating liquid, and then the coating liquid is additionally supplied to the coating liquid tank to reach the reference level. And a method for controlling a hard substrate coating apparatus.
【0010】この場合塗布液槽内の液レベルは吐出口よ
り低い位置にあるので、配管内の空気は塗布液槽内の液
と混合して気泡を発生することなく容易に空気中に放散
され、塗布液のみが塗布液槽内に吐出される。In this case, since the liquid level in the coating liquid tank is at a position lower than the discharge port, the air in the pipe is mixed with the liquid in the coating liquid tank and easily diffused into the air without generating bubbles. Only the coating liquid is discharged into the coating liquid tank.
【0011】本発明の第2の目的は、下部が塗布液槽に
浸漬されたマイクロロッドバーと、このマイクロロッド
バーの上方に対向配置されたニップローラとの間に、硬
基板を挟んで送ることにより、硬基板の下面に塗布液を
塗布する硬基板塗布装置において、前記塗布液槽に塗布
液を供給する供給系と、前記塗布液槽内の塗布液が塗布
時基準レベルおよびこれより低い泡抜きレベルにあるこ
とを検出するレベルセンサと、前記泡抜きレベルより僅
かに高い吐出口から塗布液を塗布液槽内へ供給しつつ塗
布液槽内の塗布液を循環させる循環系と、前記供給系の
配管内の空気を塗布液と置換しつつ前記泡抜きレベルま
で塗布液を供給し前記循環系の配管内の空気を塗布液で
置換しつつ塗布液を循環させて泡抜きしてから塗布液を
塗布時基準レベルまで追加供給する制御部とを備えるこ
とを特徴とする硬基板塗布装置、により達成される。A second object of the present invention is to feed a hard substrate between a micro rod bar whose lower part is immersed in a coating solution tank and a nip roller facing above the micro rod bar. In a hard substrate coating apparatus that applies a coating liquid to the lower surface of a hard substrate, a supply system that supplies the coating liquid to the coating liquid tank, and the coating liquid in the coating liquid tank is foamed at a reference level at the time of application and lower than this A level sensor for detecting that the liquid is at the draining level, a circulation system for circulating the coating liquid in the coating liquid tank while supplying the coating liquid from the discharge port slightly higher than the bubble releasing level to the coating liquid tank, While replacing the air in the piping of the system with the coating liquid, the coating liquid is supplied to the bubble removal level, the coating liquid is circulated while the air in the piping of the circulating system is replaced with the coating liquid, and the bubble is removed before coating. Reference level when applying liquid In hard substrate coating apparatus, characterized in that it comprises an additional supply control unit is achieved by.
【0012】ここにレベルセンサを2つ設け、それぞれ
が塗布時基準レベルと泡抜きレベルとを検出するものと
することができ、この場合には液面レベルの検出が非常
に正確になる。しかし泡抜きレベルは高精度に管理する
必要性がないから、塗布時基準レベルを検出するレベル
センサにこの泡抜きレベルのセンサも兼用させてもよ
い。Here, two level sensors can be provided, each of which detects a reference level at the time of application and a bubble removal level. In this case, the detection of the liquid level becomes very accurate. However, since it is not necessary to manage the bubble removal level with high accuracy, the bubble removal level sensor may also be used as a level sensor for detecting the reference level at the time of application.
【0013】循環系には気泡を捕獲して消すための消泡
手段を設けるのが望ましい。例えばこの循環系に塗布液
のフィルタを設け、このフィルタに気泡を捕獲させ消滅
させることが可能である。It is desirable to provide an antifoaming means for capturing and eliminating air bubbles in the circulation system. For example, it is possible to provide a filter for the coating liquid in the circulation system, and to capture and eliminate bubbles in the filter.
【0014】[0014]
【実施態様】図1は本発明の一実施例の全体配置図、図
2はその要部の斜視図、図3は制御系統図、図4は動作
の流れ図である。FIG. 1 is an overall layout view of an embodiment of the present invention, FIG. 2 is a perspective view of a main part thereof, FIG. 3 is a control system diagram, and FIG. 4 is a flow chart of operation.
【0015】図1、2において、符号10は液晶板のカ
ラーフィルタに用いるガラス基板であり、硬基板となる
ものである。このガラス基板10は例えば幅300〜7
00mm、長さ400〜900mm、厚さ0.7mmの
ものである。In FIGS. 1 and 2, reference numeral 10 denotes a glass substrate used for a color filter of a liquid crystal plate, which serves as a hard substrate. The glass substrate 10 has a width of, for example, 300 to 7
It is 00 mm, 400-900 mm in length and 0.7 mm in thickness.
【0016】12は塗布液槽、14はマイクロロッドバ
ーである。マイクロロッドバー14は断面円形のロッド
の表面に細い金属線を密着するように巻き付けたもので
あり、金属線間の溝による毛細管現象を利用して液を塗
布するものである。マイクロロッドバー14は塗布液槽
12の中に設けたバックアップ材16に載った状態でモ
ータ駆動される。Reference numeral 12 denotes a coating solution tank, and 14 denotes a micro rod bar. The micro rod bar 14 is formed by winding a thin metal wire tightly around the surface of a rod having a circular cross section, and applies a liquid by utilizing the capillary phenomenon caused by a groove between the metal wires. The micro rod bar 14 is driven by a motor while being mounted on a backup material 16 provided in the coating liquid tank 12.
【0017】塗布液18はマイクロロッドバー14の下
部が十分に浸るようにその液面が一定に管理されてい
る。なおマイクロロッドバー14の外径(直径)は約6
〜12mmである。20はニップローラであり、マイク
ロロッドバー14の上方に所定間隙を保ちつつ回転自在
に保持されている。The liquid surface of the coating liquid 18 is controlled to be constant so that the lower part of the micro rod bar 14 is sufficiently immersed. The outer diameter (diameter) of the micro rod bar 14 is about 6
1212 mm. A nip roller 20 is rotatably held above the micro rod bar 14 while maintaining a predetermined gap.
【0018】ガラス基板10はその左右両縁を搬送ロー
ラに載せた状態で図8の左側から搬送され、その前縁が
マイクロロッドバー14とニップローラ20の間に進入
する。そしてそれ以後はニップローラ20とマイクロロ
ッドバー14の回転により右側へ一定速度で送られ、そ
の間にマイクロロッドバー14よってガラス基板10の
下面に液が塗布されるものである。The glass substrate 10 is conveyed from the left side in FIG. 8 with both left and right edges placed on conveyance rollers, and its front edge enters between the micro rod bar 14 and the nip roller 20. Thereafter, the liquid is fed to the right side at a constant speed by the rotation of the nip roller 20 and the micro rod bar 14, and the liquid is applied to the lower surface of the glass substrate 10 by the micro rod bar 14 during that time.
【0019】図1、2において符号22は搬送ローラで
あり、ガラス基板10の左右両縁部の下面だけに接触す
る。搬送ローラ22は図2に示すケース24に収容され
た駆動機構により駆動され、ガラス基板10を一定速度
で搬送する。In FIGS. 1 and 2, reference numeral 22 denotes a conveying roller, which contacts only the lower surfaces of the left and right edges of the glass substrate 10. The transport roller 22 is driven by a drive mechanism housed in a case 24 shown in FIG. 2, and transports the glass substrate 10 at a constant speed.
【0020】マイクロロッドバー14はその上部が液か
ら露出するように水平に保持されている。またマイクロ
ロッドバー14の中間部分は図2に示したバックアップ
部材16により下方から支持されている。このバックア
ップ部材16は、摺動性に優れた硬質の合成樹脂で作ら
れ、その上面に長手方向に沿って形成された半円形の溝
がマイクロロッドバー14に下方から当接してマイクロ
ロッドバー14のたわみを防止するものである。The micro rod bar 14 is held horizontally so that its upper part is exposed from the liquid. The intermediate portion of the micro rod bar 14 is supported from below by the backup member 16 shown in FIG. The backup member 16 is made of a hard synthetic resin having excellent slidability, and a semicircular groove formed on the upper surface thereof along the longitudinal direction abuts against the micro rod bar 14 from below, and the micro rod bar 14 To prevent deflection.
【0021】マイクロロッドバー14の一端(図1にお
ける奥側の端)は塗布液槽12より後方へ突出し、この
突出端は着脱自在な継手によって電動モータ(図示せ
ず)に接続されている。この電動モータの回転は搬送ロ
ーラ22にも伝えられガラス基板10の送り速度が搬送
ローラ22の搬送速度と等速になるようにされている。
前記ニップローラ20の表面は導電性ゴムで作られ、マ
イクロロッドバー14との間にガラス基板10を挟んだ
状態でガラス基板10に所定の挟圧力を付与するように
保持されている。One end (the end on the rear side in FIG. 1) of the micro rod bar 14 projects rearward from the coating solution tank 12, and this projecting end is connected to an electric motor (not shown) by a detachable joint. The rotation of the electric motor is also transmitted to the transport roller 22 so that the feed speed of the glass substrate 10 is equal to the transport speed of the transport roller 22.
The surface of the nip roller 20 is made of conductive rubber, and is held so as to apply a predetermined clamping force to the glass substrate 10 with the glass substrate 10 sandwiched between the nip roller 20 and the micro rod bar 14.
【0022】次に塗布液槽12に塗布液を供給する供給
系30と、排液型32と、循環系34と、溶媒供給系3
6を説明する。供給系30は、塗布液タンク38から所
定濃度に調整された塗布液を塗布液槽12へ送る。すな
わちこの塗布液タンク38は気密に作られ、その内部を
空気ポンプ40により一定圧に加圧して、塗布液を圧送
するものである。Next, a supply system 30 for supplying the coating liquid to the coating liquid tank 12, a drainage type 32, a circulation system 34, and a solvent supply system 3
6 will be described. The supply system 30 sends the coating liquid adjusted to a predetermined concentration from the coating liquid tank 38 to the coating liquid tank 12. That is, the coating liquid tank 38 is made airtight, and the inside thereof is pressurized to a constant pressure by the air pump 40 to pump the coating liquid.
【0023】42は送液バルブ、44はフィルタ、46
はボールバルブである。この供給系30はバルブ42、
46を開くことにより、タンク38から塗布液を塗布液
槽12に導く。ここにこの供給系30の塗布液槽12内
の吐出口48は、塗布液槽12の一端側から他端方向を
指向して水平に開口している。Reference numeral 42 denotes a liquid sending valve, 44 denotes a filter, 46
Is a ball valve. The supply system 30 includes a valve 42,
By opening 46, the coating liquid is guided from the tank 38 to the coating liquid tank 12. Here, the discharge port 48 in the coating liquid tank 12 of the supply system 30 is horizontally opened from one end of the coating liquid tank 12 toward the other end.
【0024】この吐出口48の高さは、塗布時の基準レ
ベルL0よりも低い泡抜きレベルL1付近に位置する。こ
れらの基準レベルL0および泡抜きレベルL1はそれぞれ
光学式のレベルセンサ50、52により検出される。The height of the discharge port 48 is located near a lower defoaming levels L 1 than the reference level L 0 at the time of application. These reference level L 0 and bubble removal level L 1 are detected by optical level sensors 50 and 52, respectively.
【0025】排液系32は基準レベルL0をオーバーフ
ローした塗布を排液タンク54に導くオーバーフローチ
ューブ56と、バルブ58により塗布液槽12内の液を
底から抜いて排液タンク54に導く排液チューブ60と
を持つ。なお前記供給系30にはフィルタ44からバル
ブ62を介して液をこの排液タンク54に導く排液チュ
ーブ64が設けられている。The drainage system 32 has an overflow tube 56 for guiding the application overflowing the reference level L 0 to the drainage tank 54, and a drainage for draining the liquid in the coating solution tank 12 from the bottom by the valve 58 to the drainage tank 54. And a liquid tube 60. The supply system 30 is provided with a drain tube 64 for guiding the liquid from the filter 44 to the drain tank 54 via a valve 62.
【0026】循環系34は、塗布液槽12の吐出口48
から遠い他端付近に位置する吸入口66と吐出口48と
の間を塗布液槽12の外でつなぐチューブ68と、この
チューブ68に設けた循環ポンプ70およびフィルタ7
2を持つ。このポンプ70は液を吐出口48から吸入口
66に向って静かに流動させ、フィルタ72を通すこと
によって液に含まれた気泡を能率良く除去する。The circulation system 34 is provided with a discharge port 48 of the coating solution tank 12.
A tube 68 that connects between the suction port 66 and the discharge port 48 located near the other end far from the outside of the coating liquid tank 12, a circulation pump 70 and a filter 7 provided in the tube 68.
Have two. The pump 70 allows the liquid to flow gently from the discharge port 48 to the suction port 66, and efficiently removes bubbles contained in the liquid by passing through the filter 72.
【0027】このフィルタ72は元来液中の微細なゴミ
を除去するものであるが、液中の気泡も捕獲するものが
望ましく、通常のフィルタやストレートはこのような機
能を持つ。従ってフィルタ72はできるだけ目が細かい
ものが望ましい。なおこの循環系34は、塗布作業中も
作動させて塗布液槽12内に静かな定常流を発生させ、
液が淀んだりして濃度が場所により不均一になるのを防
止してもよい。Although the filter 72 originally removes fine dust in the liquid, it is desirable that the filter 72 also captures bubbles in the liquid. A normal filter or straight filter has such a function. Therefore, it is desirable that the filter 72 be as fine as possible. The circulating system 34 is also operated during the coating operation to generate a quiet steady flow in the coating liquid tank 12,
It may be possible to prevent the concentration of the liquid from becoming uneven at some places due to the stagnant liquid.
【0028】溶媒供給系36は、溶媒タンク74と、溶
媒補充ポンプ76とを持ち、塗布液槽12内に溶媒を補
充する。すなわち塗布液は循環系34で循環中や塗布中
に溶媒が蒸発して濃度が上がるから、適時にこの溶媒供
給系36から溶媒を補充することにより濃度を一定に保
つものである。The solvent supply system 36 has a solvent tank 74 and a solvent replenishment pump 76, and replenishes the solvent in the coating solution tank 12. That is, since the concentration of the coating solution increases due to evaporation of the solvent during circulation or application in the circulation system 34, the concentration is kept constant by replenishing the solvent from the solvent supply system 36 in a timely manner.
【0029】78は制御部であり、レベルセンサ50、
52や全てのバルブおよびポンプ類が接続され、これら
を所定の動作プログラムに従って制御するものである。
次にこの制御部78による動作例を図4を用いて説明す
る。Reference numeral 78 denotes a control unit, and the level sensor 50,
52 and all valves and pumps are connected, and are controlled according to a predetermined operation program.
Next, an operation example of the control unit 78 will be described with reference to FIG.
【0030】まず最初に制御部78は供給系30により
塗布液を塗布液槽12に供給する(図4のステップ10
0)。すなわち空気ポンプ40で塗布液タンク38内を
加圧し、バルブ42、46を開いて液を塗布液槽12に
送る。First, the control unit 78 supplies the coating liquid to the coating liquid tank 12 by the supply system 30 (step 10 in FIG. 4).
0). That is, the inside of the coating liquid tank 38 is pressurized by the air pump 40, the valves 42 and 46 are opened, and the liquid is sent to the coating liquid tank 12.
【0031】塗布液槽12の液面レベルはレベルセンサ
50、52で監視され(ステップ102)、その一方の
レベルセンサ52が泡抜きレベルL1を検出すると供給
系30は液の供給を停止する(ステップ104)。そし
て次に循環系34が起動する(ステップ106)。The liquid level of the coating liquid tank 12 is monitored by the level sensor 50, 52 (step 102), the supply system 30 and its one level sensor 52 of detecting a defoaming level L 1 stops the supply of the liquid (Step 104). Then, the circulation system 34 is activated (step 106).
【0032】循環ポンプ70が起動すると、塗布液槽1
2内の液は吸入口66からチューブ68を介して吐出口
48に循環する。この時液はフィルタ72を通り、ここ
で気泡が捕獲される。このため吐出口48から流出する
液中に含まれる気泡はほとんど消失するか著しく減少す
る。When the circulation pump 70 is started, the coating liquid tank 1
The liquid in 2 circulates from suction port 66 to discharge port 48 via tube 68. At this time, the liquid passes through the filter 72, where air bubbles are captured. For this reason, bubbles contained in the liquid flowing out from the discharge port 48 almost disappear or are significantly reduced.
【0033】この循環系34は所定の設定時間T0作動
し続けた後(ステップ108)、停止する。この設定時
間T0は実験により決定しメモリしておくものとする。The circulating system 34 stops operating after continuing to operate for a predetermined set time T 0 (step 108). This set time T 0 is determined by experiment and stored in memory.
【0034】制御部78は次に供給系30を再び起動さ
せ、塗布液タンク38から液を塗布液槽12に送る(ス
テプ110)。そして液面レベルが基準レベルL0とな
ると供給を停止する(ステプ112)。この時は基準レ
ベルセンサ50で検出する。このようにして基準レベル
L0まで液を供給した後に硬基板10の塗布を開始する
(ステップ114)。Next, the control unit 78 activates the supply system 30 again, and sends the liquid from the coating liquid tank 38 to the coating liquid tank 12 (step 110). The liquid level to stop the supply and the reference level L 0 (Sutepu 112). At this time, it is detected by the reference level sensor 50. After the liquid is supplied to the reference level L 0 in this manner, the application of the hard substrate 10 is started (Step 114).
【0035】[0035]
【他の実施態様】この実施態様では循環系34にフィル
タ72を介在させ、これを気泡の捕獲手段として利用し
た。しかし本発明は他のエアトラップなどを用いた捕獲
手段を組込んでも良い。またフィルタ72あるいは捕獲
手段は省いても、本発明の効果は得られる。従って本発
明はこれらの無いものも包含する。[Other Embodiments] In this embodiment, a filter 72 is interposed in the circulating system 34 and used as a means for capturing air bubbles. However, the present invention may incorporate capture means using another air trap or the like. Further, even if the filter 72 or the capturing means is omitted, the effect of the present invention can be obtained. Therefore, the present invention includes those without these.
【0036】液面レベルは2つのレベルセンサ50、5
2でそれぞれ基準レベルL0と泡抜きレベルL1とを別々
に検出すれば、検出精度が高く望ましい。しかし泡抜き
レベルL1の検出は高精度である必要は無いから、基準
レベルL0のセンサ50を利用してこの泡抜きレベルL1
も検出するようにしてもよい。The liquid level is determined by two level sensors 50, 5
If the reference level L 0 and the bubble removal level L 1 are separately detected in 2, it is desirable that the detection accuracy is high. But since the detection of the bubble removal level L 1 need not be highly accurate, the bubble removing level using the sensor 50 of the reference level L 0 L 1
May also be detected.
【0037】[0037]
【他の実施態様】図5は他の実施態様の概念図、図6は
その動作の流れ図である。図5では図を簡略化するため
排液系など一部を省いて示している。また前記の図と同
一部分には同一符号を付したので、その説明は繰り返さ
ない。FIG. 5 is a conceptual diagram of another embodiment, and FIG. 6 is a flowchart showing the operation thereof. In FIG. 5, for simplification of the drawing, a part such as a drainage system is omitted. The same parts as those in the above-mentioned figures are denoted by the same reference numerals, and therefore, description thereof will not be repeated.
【0038】ここに用いる液面センサ50Aは、例えば
4つの液面レベルLL、LH、L0'、L0を検出できる。
L0は塗布時基準レベル、L0’はこれより僅かに下のレ
ベル、LHは泡抜き上限レベル、LLはこれより低い泡抜
き下限レベルである。The liquid level sensor 50A used here can detect, for example, four liquid level levels L L , L H , L 0 ′, and L 0 .
L 0 is a reference level at the time of application, L 0 ′ is a slightly lower level, L H is a bubble removal upper limit level, and LL is a lower bubble removal lower level.
【0039】まず最初に供給系のバルブ46を開いてタ
ンク38から塗布液を塗布液槽12に送り(図6のステ
ップ200)、泡抜き上限レベルLHにする(ステップ
202)。この時供給系30の配管内の空気は完全に排
出され塗布液で置換される。このレベルLHになると液
の供給を停止し(ステップ204)、循環ポンプ70を
始動する(ステップ206)。このポンプ70の始動に
より循環系34内の配管内の空気が排出される。[0039] First feed from the tank 38 by opening the supply system of the valve 46 to the coating liquid in the coating liquid tank 12 (step 200 in FIG. 6), to defoaming upper limit level L H (step 202). At this time, the air in the pipe of the supply system 30 is completely discharged and replaced with the coating liquid. When this level L H stopping the supply of the liquid (step 204), starting the circulation pump 70 (Step 206). By starting the pump 70, the air in the piping in the circulation system 34 is discharged.
【0040】塗布液内の空気が排出されるのに伴い、液
面レベルは下がってゆく。液面レベルが泡抜き下限レベ
ルLLになれば(ステップ208)、供給系を再び作動
させて(ステップ200)、液面レベルを泡抜き上限レ
ベルLHにする(ステップ202)。As the air in the coating liquid is discharged, the liquid level decreases. Once the liquid level within defoaming lower limit level L L (step 208), the supply system is again activated (step 200), the liquid level to defoaming upper limit level L H (step 202).
【0041】このような動作を繰り返し、循環系に含ま
れる空気が減れば、循環中の液面レベル低下は少なくな
る。従って液面レベルが泡抜き下限レベルLLまで下が
ることなく所定時間(30分以上が好ましい)経過した
ら(ステップ210)、泡抜きは終了したものとする。
そして供給系30を起動して塗布液を追加する(ステッ
プ212)。液面レベルがレベルL0'になったら(ステ
ップ214)、液の供給を間欠供給に切換える(ステッ
プ216)。If such operations are repeated and the air contained in the circulation system is reduced, the decrease in the liquid level during circulation is reduced. Therefore predetermined time (30 minutes or more is preferable) without liquid level drops to defoaming lower limit level L L When elapsed (step 210), debubbling is assumed ended.
Then, the supply system 30 is activated to add the coating liquid (step 212). When the liquid level reaches the level L 0 ′ (step 214), the supply of liquid is switched to intermittent supply (step 216).
【0042】この間欠供給は、液を連続供給して液面が
基準レベルL0以上になるのを防止するため、例えば1
秒間液を供給した後2秒間停止する。供給の停止中に塗
布液槽12内の液面が均一化し、液面センサ50Aが液
面を正しく検出できるようにするものである。このよう
に間欠供給により液面レベルが塗布時基準レベルL0に
なれば(ステップ208)、液の供給を停止し、ガラス
基板10への塗布を開始する(ステップ220)。なお
この間欠供給の方法は、液を泡抜き上限レベルLHまで
供給するステップ200、202の行程でも採用するこ
とができる。The intermittent supply is performed by, for example, 1 to prevent the liquid level from becoming higher than the reference level L 0 by continuously supplying the liquid.
Stop supplying for 2 seconds after supplying liquid for 2 seconds. The liquid level in the coating liquid tank 12 is made uniform while the supply is stopped, so that the liquid level sensor 50A can detect the liquid level correctly. Once this way in the intermittent supply is liquid level during coating reference level L 0 (step 208), it stops the supply of the liquid, for starting the application to the glass substrate 10 (step 220). Note how this intermittent supply, the liquid to can be employed in process of supplying step 200 and 202 until the debubbling upper limit level L H.
【0043】[0043]
【発明の効果】請求項1の発明は以上のように、基準レ
ベルより低い泡抜きレベルまで入れた塗布液を循環ポン
プにより循環させて気泡を自動で除去するから、作業能
率が良く、作業が極めて簡単になる。このため装置の稼
働率が向上する。また泡が入っている液を棄てる必要も
ないから、液を無駄に消費することもなくなる。According to the first aspect of the present invention, as described above, since the coating liquid filled to the bubble removal level lower than the reference level is circulated by the circulation pump to automatically remove bubbles, the work efficiency is good and the work can be carried out. Extremely simple. For this reason, the operation rate of the device is improved. Further, since it is not necessary to discard the liquid containing bubbles, the liquid is not wasted.
【0044】請求項2の発明によれば、この方法の実施
に直接使用する硬基板塗布装置が得られる。ここに基準
レベル検出用のレベルセンサは、泡抜きレベル検出用の
レベルセンサを兼ねるようにすれば、部品点数が減り望
ましい。循環系には気泡を除去する捕獲手段を設けるの
が望ましい(請求項4)。この捕獲手段は例えば液中の
微少なゴミを除去するフィルタとすることができる。According to the second aspect of the present invention, there is provided a hard substrate coating apparatus directly used for carrying out this method. Here, if the level sensor for detecting the reference level also functions as the level sensor for detecting the bubble removal level, the number of components is desirably reduced. It is desirable to provide a trapping means for removing air bubbles in the circulation system (claim 4). This capturing means can be, for example, a filter for removing minute dust in the liquid.
【図1】本発明の一実施態様の全体配置図FIG. 1 is an overall layout view of an embodiment of the present invention.
【図2】その塗布部の拡大斜視図FIG. 2 is an enlarged perspective view of the application section.
【図3】制御系統図FIG. 3 is a control system diagram
【図4】動作の流れ図FIG. 4 is a flowchart of the operation.
【図5】他の実施例の概念図FIG. 5 is a conceptual diagram of another embodiment.
【図6】その動作の流れ図FIG. 6 is a flowchart of the operation.
10 ガラス基板(硬基板) 12 塗布液槽 14 マイクロロッドバー 20 ニップローラ 30 供給系 32 排液系 34 循環系 36 溶媒供給系 50、50A、52 レベルセンサ 70 循環ポンプ 72 捕獲手段としてのフィルタ 78 制御部 L0 基準レベル L1 泡抜きレベル LH 泡抜き上限レベル LL 泡抜き下限レベルDESCRIPTION OF SYMBOLS 10 Glass substrate (hard board) 12 Coating liquid tank 14 Micro rod bar 20 Nip roller 30 Supply system 32 Drainage system 34 Circulation system 36 Solvent supply system 50, 50A, 52 Level sensor 70 Circulation pump 72 Filter 78 as a capture means 78 Control unit L 0 reference level L 1 bubble removal level L H bubble removal upper limit level L L bubble removal lower limit level
───────────────────────────────────────────────────── フロントページの続き (72)発明者 尾崎 正文 神奈川県綾瀬市小園1005番地 富士マイク ログラフイックス株式会社内 (72)発明者 藤倉 利之 神奈川県綾瀬市小園1005番地 富士マイク ログラフイックス株式会社内 (72)発明者 大津 政夫 神奈川県綾瀬市小園1005番地 富士マイク ログラフイックス株式会社内 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Masafumi Ozaki 1005 Koizono, Ayase City, Kanagawa Prefecture Inside Fuji Mike Logigraphics Corporation (72) Inventor Toshiyuki Fujikura 1005 Koizono, Ayase City, Kanagawa Prefecture Fuji Mike Logigraphics Corporation (72) Inventor Masao Otsu 1005 Kozono, Ayase City, Kanagawa Prefecture Fuji Micrographix Co., Ltd.
Claims (4)
ッドバーと、このマイクロロッドバーの上方に対向配置
されたニップローラとの間に、硬基板を挟んで送ること
により、硬基板の下面に塗布液を塗布する硬基板塗布装
置の制御方法において、前記塗布液槽に塗布時基準レベ
ルより低い泡抜きレベルまでこの泡抜きレベルより僅か
に高い吐出口より塗布液を供給し、塗布液供給系の配管
内の空気を塗布液と置換した後、前記塗布液槽内の塗布
液を循環ポンプとの間で循環させてこの循環系の配管内
の空気を塗布液で完全に置換し、その後塗布液槽に塗布
液を追加供給して前記基準レベルにすることを特徴とす
る硬基板塗布装置の制御方法。1. A hard substrate is sandwiched between a micro rod bar whose lower part is immersed in a coating solution tank and a nip roller opposed to and disposed above the micro rod bar, and is sent to the lower surface of the hard substrate. In the method for controlling a hard substrate coating apparatus for applying a coating liquid, a coating liquid is supplied to the coating liquid tank from a discharge port slightly higher than the bubble removal level to a bubble removal level lower than a reference level at the time of coating. After replacing the air in the piping with the coating liquid, the coating liquid in the coating liquid tank is circulated between the circulating pump and the air in the piping of the circulation system is completely replaced with the coating liquid. A method for controlling a hard substrate coating apparatus, characterized in that a coating liquid is additionally supplied to a liquid tank to make the reference level.
ッドバーと、このマイクロロッドバーの上方に対向配置
されたニップローラとの間に、硬基板を挟んで送ること
により、硬基板の下面に塗布液を塗布する硬基板塗布装
置において、前記塗布液槽に塗布液を供給する供給系
と、前記塗布液槽内の塗布液が塗布時基準レベルおよび
これより低い泡抜きレベルにあることを検出するレベル
センサと、前記泡抜きレベルより僅かに高い吐出口から
塗布液を塗布液槽内へ供給しつつ塗布液槽内の塗布液を
循環させる循環系と、前記供給系の配管内の空気を塗布
液と置換しつつ前記泡抜きレベルまで塗布液を供給し前
記循環系の配管内の空気を塗布液で置換しつつ塗布液を
循環させて泡抜きしてから塗布液を塗布時基準レベルま
で追加供給する制御部とを備えることを特徴とする硬基
板塗布装置。2. A hard substrate is sandwiched between a micro-rod bar whose lower part is immersed in a coating liquid tank and a nip roller facing above the micro-rod bar, and is sent to the lower surface of the hard substrate. In a hard substrate coating apparatus for applying a coating liquid, a supply system for supplying the coating liquid to the coating liquid tank, and detecting that the coating liquid in the coating liquid tank is at a reference level at the time of coating and a bubble removal level lower than this. A level sensor, a circulating system for circulating the coating liquid in the coating liquid tank while supplying the coating liquid into the coating liquid tank from a discharge port slightly higher than the bubble removal level, and an air in the pipe of the supply system. Supplying the coating liquid up to the bubble removing level while replacing the coating liquid, circulating the coating liquid while replacing the air in the circulating system piping with the coating liquid and removing bubbles, and then applying the coating liquid to the reference level at the time of coating. Additional supply control unit And a hard substrate coating apparatus.
は泡抜きレベル検出用のレベルセンサを兼ねる請求項2
の硬基板塗布装置。3. A level sensor for detecting a reference level at the time of application also serves as a level sensor for detecting a bubble removal level.
Hard substrate coating equipment.
する消泡手段を有する請求項2の硬基板塗布装置。4. The hard substrate coating apparatus according to claim 2, wherein the circulating system has defoaming means for capturing bubbles contained in the coating liquid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP30391496A JP3722452B2 (en) | 1996-10-30 | 1996-10-30 | Hard substrate coating apparatus and control method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP30391496A JP3722452B2 (en) | 1996-10-30 | 1996-10-30 | Hard substrate coating apparatus and control method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH10128201A true JPH10128201A (en) | 1998-05-19 |
| JP3722452B2 JP3722452B2 (en) | 2005-11-30 |
Family
ID=17926797
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP30391496A Expired - Lifetime JP3722452B2 (en) | 1996-10-30 | 1996-10-30 | Hard substrate coating apparatus and control method thereof |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3722452B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006051474A (en) * | 2004-08-16 | 2006-02-23 | Ckd Corp | Hydraulic control device |
| CN112371436A (en) * | 2020-10-30 | 2021-02-19 | 汕头市达兴钢结构有限公司如皋分公司 | Multifunctional small-sized steel connection structure oil immersion equipment |
| CN116943969A (en) * | 2023-09-20 | 2023-10-27 | 爱德曼氢能源装备有限公司 | Two-way accurate setpoint mucilage binding of electrode plate for fuel cell is put |
-
1996
- 1996-10-30 JP JP30391496A patent/JP3722452B2/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006051474A (en) * | 2004-08-16 | 2006-02-23 | Ckd Corp | Hydraulic control device |
| CN112371436A (en) * | 2020-10-30 | 2021-02-19 | 汕头市达兴钢结构有限公司如皋分公司 | Multifunctional small-sized steel connection structure oil immersion equipment |
| CN116943969A (en) * | 2023-09-20 | 2023-10-27 | 爱德曼氢能源装备有限公司 | Two-way accurate setpoint mucilage binding of electrode plate for fuel cell is put |
| CN116943969B (en) * | 2023-09-20 | 2023-12-12 | 爱德曼氢能源装备有限公司 | Two-way accurate setpoint mucilage binding of electrode plate for fuel cell is put |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3722452B2 (en) | 2005-11-30 |
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