JPH10314633A - Coating applicator and production of color filters - Google Patents

Coating applicator and production of color filters

Info

Publication number
JPH10314633A
JPH10314633A JP13189797A JP13189797A JPH10314633A JP H10314633 A JPH10314633 A JP H10314633A JP 13189797 A JP13189797 A JP 13189797A JP 13189797 A JP13189797 A JP 13189797A JP H10314633 A JPH10314633 A JP H10314633A
Authority
JP
Japan
Prior art keywords
coating
viscosity
coating liquid
liquid
bar
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.)
Pending
Application number
JP13189797A
Other languages
Japanese (ja)
Inventor
Yasuhiro Hamazuka
康宏 濱塚
Satoshi Sasaki
聡 佐々木
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP13189797A priority Critical patent/JPH10314633A/en
Publication of JPH10314633A publication Critical patent/JPH10314633A/en
Pending legal-status Critical Current

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  • Optical Filters (AREA)
  • Coating Apparatus (AREA)

Abstract

PROBLEM TO BE SOLVED: To decrease the defects of coating films, such as unequal film thickness distribution and coating distribution, for affecting the functions of thin films by film thickness with a coating applicator for forming thin films, such as color filters. SOLUTION: A compounding tank 16 having a stirrer and viscometer 14 in a circulating route in order to control a coating liquid viscosity having a correlative relation to a constant value is installed as a means for suppressing the coating film thickness distribution. A solvent and coating liquid 17 are compounded while the viscosity is measured therein, by which the coating is executed while the fluctuation in the viscosity of the coating liquid 17 is controlled to ±1 to ±5%. As a result, the waste liquid of the coating layer 17 is eliminated and, therefore, the consumption thereof is reduced. The coating system is a bar coating system. The shape defects of the members for supporting the coating bars are eliminated and the defects of the coating films are decreased by the structure of separating the coating layer contact parts.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、ガラス基板などの
非連続性基板に塗布バーを用いて塗布液を塗布する塗布
装置及び該装置を用いたカラーフィルタの製造方法に関
するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a coating apparatus for applying a coating liquid to a discontinuous substrate such as a glass substrate using a coating bar, and a method for manufacturing a color filter using the apparatus.

【0002】[0002]

【従来の技術】カラーフィルタの製造工程には、ガラス
基板などの透明基板に着色感光性樹脂からなる塗布液を
薄く均一な厚さに塗布する工程がある。従来はこの塗布
のために半導体産業において実績のあるスピンコータが
用いられてきた。このスピンコータでは、ガラス基板を
回転させながらその回転中心に塗布液を滴下し、遠心力
により塗布液を広げて塗布する方法である。しかしこの
スピンコータでは、高価な塗布液の90%近くを飛散さ
せてしまうので材料費低減の隘路事項となっている。そ
こで特開平2−258081号公報では、塗布面に塗布
液を滴下し、ワイヤを巻き付けた棒からなる塗布バーを
転がして塗り拡げるというバーコート法を応用した塗布
装置及び、該装置を使用した塗布方法が考案されてい
る。この装置は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ものであり、下のローラとなる塗
布バーの下部を塗布液に浸け、塗布バーが回転すること
により表面張力で塗布液が汲み上げられ、表面のワイヤ
で計量しながら基板の下面側から塗布する方法である。
この方法において塗布面の膜厚は塗布バーのワイヤ径及
び塗布液の粘度により規定され、特開平4−27034
6号公報では赤、青、緑の塗布液の塗布時の粘度が、3
色の塗布時の粘度の平均値に対し±30%にあれば0.
01μmの膜厚変動許容範囲に収めることができるとし
ている。またこの方法では、スピンコータのように回転
による塗布液飛散のような無駄は生じない。
2. Description of the Related Art In a process of manufacturing a color filter, there is a process of applying a coating liquid composed of a colored photosensitive resin to a thin and uniform thickness on a transparent substrate such as a glass substrate. Conventionally, a spin coater proven in the semiconductor industry has been used for this coating. In this spin coater, a coating liquid is dropped onto the center of rotation while rotating a glass substrate, and the coating liquid is spread and applied by centrifugal force. However, with this spin coater, nearly 90% of the expensive coating solution is scattered, which is a bottleneck in reducing material costs. Japanese Patent Application Laid-Open No. Hei 2-258081 discloses a coating apparatus applying a bar coating method in which a coating liquid is dropped on a coating surface and a coating bar formed of a wire-wound rod is rolled to spread the coating, and a coating apparatus using the coating apparatus. A method has been devised. In this device, the substrate is sandwiched between a pair of upper and lower rollers arranged horizontally, and the lower part of the coating bar, which is the lower roller, is immersed in the coating solution, and the coating bar rotates to apply the surface tension. In this method, an application liquid is pumped up and applied from the lower surface side of the substrate while being measured by a wire on the surface.
In this method, the thickness of the coating surface is determined by the wire diameter of the coating bar and the viscosity of the coating solution.
No. 6, the viscosity of the red, blue and green coating liquids when applied is 3
If it is within ± 30% of the average value of the viscosity at the time of application of the color, it is 0.
It is stated that the thickness can be kept within an allowable range of a film thickness variation of 01 μm. Further, in this method, there is no waste such as scattering of the coating liquid due to rotation unlike a spin coater.

【0003】[0003]

【発明が解決しようとする課題】しかしスピンコータで
は、滴下する直前まで外気に触れることなく塗布液を管
理できるので粘度は変動することなく安定していたが、
この塗布バーを使用する方法では約300ccの塗布液
が循環しているとはいえ、外気に触れるために粘度が変
動している。また、この変動を押さえるために溶剤を塗
布液をためている受け皿に直接供給しているので塗布バ
ーの軸方向に粘度の差異を生じてしまう。したがって、
粘度と相関関係にある膜厚が変動してしまうので粘度調
整のために装置を停止させなければならない。また、系
全体の塗布液量は一定であるので粘度調整するために塗
布液を廃液するという無駄が生じている。したがってこ
の粘度の変動が、稼働率低下及び塗布液の無駄遣いを引
き起こしている。
However, in the spin coater, the coating liquid can be controlled without contacting with the outside air until immediately before dropping, so that the viscosity is stable without fluctuation.
In the method using this coating bar, although the coating liquid of about 300 cc is circulating, the viscosity fluctuates due to contact with the outside air. In addition, since the solvent is directly supplied to the pan in which the coating liquid is stored in order to suppress the fluctuation, a difference in viscosity occurs in the axial direction of the coating bar. Therefore,
Since the film thickness correlated with the viscosity fluctuates, the apparatus must be stopped for adjusting the viscosity. Further, since the amount of the coating solution in the entire system is constant, there is a waste in that the coating solution is wasted in order to adjust the viscosity. Therefore, the fluctuation of the viscosity causes a decrease in the operation rate and a waste of the coating liquid.

【0004】また、該受け皿において塗布バーを支持し
ている部材は、特開平5−309304号公報において
は、耐薬品性と摺動抵抗の低減などから硬質の合成樹脂
が採用されている。しかし、塗布バーの形状精度の影響
で摩耗や傷が生じ、支持部材が形状不良を起こすことや
微調整ができるように受け皿にネジで結合されているた
めに、その隙間に塗布液が残留することになり、洗浄し
ても取り除くことができないので異物が発生することに
より塗布面の面状不良を引き起こしている。
A member supporting the coating bar in the receiving tray is made of a hard synthetic resin in JP-A-5-309304 in view of chemical resistance and reduction of sliding resistance. However, abrasion and scratches occur due to the influence of the shape accuracy of the application bar, and the support member is screwed to the pan so that the shape of the support member may be defective and fine adjustment can be performed, so that the application liquid remains in the gap. In other words, since the particles cannot be removed even by washing, the generation of foreign matter causes poor surface condition of the coated surface.

【0005】[0005]

【課題を解決するための手段】そこで本発明は、水平に
配設された塗布バーとローラの間を通過させて基板に塗
布液を塗布する装置において、塗布液を循環している配
管の途中に攪拌装置と粘度計を備えた調合タンクを設け
て、粘度計から粘度信号を制御器に取り込み、粘度が許
容範囲を逸脱すると溶剤ポンプもしくは塗布液ポンプに
供給信号を送り、許容範囲内に戻れば停止信号を送るこ
とで粘度を±1〜5%に制御することで粘度及び膜厚の
変動を押さえたことを特徴とする塗布装置を提供する。
SUMMARY OF THE INVENTION Accordingly, the present invention is directed to an apparatus for applying a coating solution to a substrate by passing the coating solution between a horizontally disposed coating bar and a roller. A mixing tank equipped with a stirrer and a viscometer is provided, and the viscosity signal from the viscometer is taken into the controller, and when the viscosity deviates from the allowable range, a supply signal is sent to the solvent pump or coating liquid pump to return to the allowable range. For example, there is provided a coating apparatus characterized in that fluctuations in viscosity and film thickness are suppressed by sending a stop signal to control the viscosity to ± 1 to 5%.

【0006】また本発明は、上記塗布装置において塗布
液をためておく受け皿の塗布バー支持部と塗布液と接す
る部分すなわち塗布液接触部をポリフェニレンサルファ
イド系の樹脂を使用して一体化することにより間隙に残
留する塗布液起因の異物をなくし、かつこの樹脂により
塗布バー支持部の形状不良がなくなるためにすじむらを
低減した塗布装置を提供する。
Further, in the present invention, in the above-mentioned coating apparatus, the coating bar supporting portion of the tray for storing the coating solution and the portion in contact with the coating solution, that is, the coating solution contact portion are integrated by using a polyphenylene sulfide resin. Provided is a coating apparatus that eliminates foreign matter caused by a coating liquid remaining in a gap and reduces unevenness in the shape of a coating bar supporting portion by using the resin.

【0007】この発明はまた、着色感光性樹脂からなる
塗布液を透明基板に塗布する工程と、フォトリソグラフ
ィーにより着色パターンを形成する工程を繰り返すこと
によりカラーフィルタを製造する方法において、上記塗
布装置を用いて塗布液粘度を±1〜±5%に制御して塗
布し、塗布液起因の残留異物をなくし、すじむらを低減
したことを特徴とするカラーフィルタの製造方法を提供
する。
The present invention also provides a method of manufacturing a color filter by repeating a step of applying a coating liquid comprising a colored photosensitive resin to a transparent substrate and a step of forming a colored pattern by photolithography. The present invention provides a method for producing a color filter, characterized in that the coating liquid is applied while controlling the viscosity of the coating liquid to ± 1% to ± 5% to eliminate residual foreign matter caused by the coating liquid and to reduce line unevenness.

【0008】[0008]

【発明の実施の形態】本発明の塗布装置を図1に示す。
塗布方法としては回転するロール1とこれとは逆回転す
る塗布バー2の間にガラス基板20を挟み込み、塗布バ
ー2の表面に巻きつけているワイヤ(図示せず)により
汲み上げられた塗布液17を下面からガラス基板20に
塗布する方法である。なお、塗布バー2はロール1とは
別のモータ3により駆動されている。まずは従来型の問
題点を示す。図2は従来型の薬液調合の概略図である。
ガラス基板20に塗布液17が塗布されると、受け皿4
内の液量が減るために塗布液タンク10から適正な液面
レベルになるまで循環の入口近傍に供給される。また揮
発による粘度上昇を抑えるために一定時間毎に溶剤タン
ク7から循環の出口近傍に溶剤が供給される。したがっ
て、塗布液17と溶剤の調合は循環ポンプ18によって
生じる流れにより行われる。なお、塗布液中のごみや異
物を取り除くために、循環経路中の循環ポンプ18より
循環入口側にフィルタ5を設けている。しかし、この方
法では塗布液17と溶剤及び受け皿4内の塗布液を確実
に調合できないために図3のように受け皿4の場所によ
り塗布液の固形分濃度分布が生じるために塗布膜の膜厚
分布が発生する。このような場合は、塗布液の調整のた
め廃液が必要となり無駄が生じる。なお、図2のA,
B,Cと図3のA,B,Cはそれぞれ対応する.このデ
ータは300×400のガラス基板20に対して塗布し
た際のデータであり,ガラス基板20は生産効率から今
後拡大される傾向であるので,受け皿4の長さも長くな
るために塗布液17と溶剤の調合も困難になり,膜厚の
分布及び塗布液の廃液量も増大すると予想される。
FIG. 1 shows a coating apparatus according to the present invention.
As a coating method, a glass substrate 20 is sandwiched between a rotating roll 1 and a coating bar 2 rotating in the opposite direction, and a coating liquid 17 drawn up by a wire (not shown) wound around the surface of the coating bar 2. Is applied to the glass substrate 20 from the lower surface. The application bar 2 is driven by a motor 3 different from the roll 1. First, the problems of the conventional type will be described. FIG. 2 is a schematic view of a conventional chemical preparation.
When the coating liquid 17 is applied to the glass substrate 20, the tray 4
The liquid is supplied from the application liquid tank 10 to the vicinity of the circulation inlet until the liquid level reaches an appropriate level because the liquid amount in the tank is reduced. In addition, a solvent is supplied from the solvent tank 7 to the vicinity of the circulation outlet at regular intervals in order to suppress an increase in viscosity due to volatilization. Therefore, the mixing of the coating liquid 17 and the solvent is performed by the flow generated by the circulation pump 18. The filter 5 is provided on the circulation inlet side of the circulation pump 18 in the circulation path in order to remove dust and foreign matter in the application liquid. However, in this method, since the coating liquid 17 and the solvent and the coating liquid in the receiving pan 4 cannot be reliably mixed, the solid concentration distribution of the coating liquid occurs depending on the location of the receiving pan 4 as shown in FIG. Distribution occurs. In such a case, a waste liquid is required for adjusting the coating liquid, and waste occurs. In addition, A of FIG.
B and C correspond to A, B and C in FIG. 3, respectively. This data is the data when applied to a 300 × 400 glass substrate 20. Since the glass substrate 20 tends to be expanded in the future from the viewpoint of production efficiency, the length of the pan 4 becomes longer and the coating liquid 17 It is expected that the dispensing of the solvent becomes difficult, and the distribution of the film thickness and the amount of waste liquid of the coating liquid increase.

【0009】そこで本発明では、図1に示すように受け
皿4において調合する方法を止め、循環経路の途中にマ
グネット回転モータ11とマグネット12及び攪拌子1
3で構成される攪拌装置を備えた調合タンク16を設
け、そこに塗布液と溶剤を供給して調合する方式とし
た。また膜厚は塗布液の固形分濃度と比例関係にある
が、固形分濃度は粘度と相関しているので、粘度と膜厚
とは約0.1mPasの粘度変化に対して約0.01μ
mの膜厚変化の関係がある。そこで、調合タンク16内
の塗布液17の粘度を一定にすることで膜厚の変動を押
さえ、塗布液の廃液をなくす方式とした。粘度制御の方
法は、調合タンク16に設置している粘度計14により
塗布液17の粘度を計測する。この計測値を粘度計コン
トローラ15で変換して、この外部出力を制御器19に
取り込む。制御器19は内部に塗布液17の基準粘度と
これに対する上限値と下限値を記憶しており、たとえば
図4のように粘度がサンプリング時間Snの時に上限値
を越えると同時に制御器19は溶剤供給ポンプ6に指令
を送り、溶剤タンク7からある決められた量の溶剤を供
給する。そして粘度が変化するまでの反応時間があるの
で、ある一定時間T以降のサンプリング時間、図4では
Smの時の粘度が許容範囲内(上限-下限値内)にあれ
ば制御終了であり、範囲外の時は同様の操作を許容範囲
内に収まるまで繰り返す。なお、富士ハント製カラーモ
ザイクを使用した実験では、富士工業製超音波粘度計F
UV−1により上限値6.4mPas,下限値6.35
mPas,溶剤供給量0.1cc/回,T=10sで制御
可能であることを確認している。また、塗布を繰り返す
と受け皿4内の液量が減少するので液面計21の計測値
により制御器19から圧力制御器9に指令を送り、塗布
液タンク10の加圧を行い、送液制御器8により調合タ
ンク16に塗布液原液を送ることで液量を補充してい
る。また本発明では調合タンクで粘度制御を行っている
が、実際には受け皿4内の粘度が膜厚を規定する。そこ
で、受け皿4内での塗布液の粘度変化を図5に示す。こ
の実験においても、富士ハント製カラーモザイクを使用
しているが、低粘度タイプのものを使用している。粘度
制御時の条件は上限値5.16mPas,下限値5.1
2mPas以外は前述の実験と同一である。調合タンク
16で粘度制御を実行している場合でも受け皿4内の粘
度は約5.2mPasと制御範囲を逸脱するが、基準値
±0.1mPas以内の変動である。しかし、粘度制御
をしない場合は図5で明らかなように塗布液の粘度は単
調増加していき、数時間で膜厚許容変動範囲±0.05
μmに対応する0.5mPasを逸脱することが分か
る。したがって、以上の構成により塗布液粘度を基準値
±0.1mPas以下に制御できかつ、廃液を無くすこ
とが可能である。また、塗布液の粘度は約5〜10mP
asであるので、基準値±1〜±5%に粘度制御できる
と言える。
Therefore, according to the present invention, as shown in FIG. 1, the method of mixing in the tray 4 is stopped, and the magnet rotating motor 11, the magnet 12, and the stirrer 1
A mixing tank 16 provided with a stirrer constituted by No. 3 was provided, and a coating liquid and a solvent were supplied thereto to perform mixing. Further, the film thickness is proportional to the solid concentration of the coating solution, but since the solid concentration is correlated with the viscosity, the viscosity and the film thickness are about 0.01 μm for a viscosity change of about 0.1 mPas.
m is related to the change in film thickness. Therefore, a method was adopted in which the viscosity of the coating liquid 17 in the blending tank 16 was kept constant to suppress fluctuations in the film thickness and eliminate waste liquid of the coating liquid. As a method of controlling the viscosity, the viscosity of the coating liquid 17 is measured by the viscometer 14 installed in the mixing tank 16. The measured value is converted by the viscometer controller 15 and the external output is taken into the controller 19. The controller 19 stores therein the reference viscosity of the coating liquid 17 and the upper and lower limit values thereof. For example, as shown in FIG. A command is sent to the supply pump 6 to supply a predetermined amount of solvent from the solvent tank 7. Then, since there is a reaction time until the viscosity changes, if the viscosity at Sm in the sampling time after a certain time T is within the allowable range (upper-lower limit) in FIG. Otherwise, the same operation is repeated until it falls within the allowable range. In an experiment using a color mosaic manufactured by Fuji Hunt, an ultrasonic viscometer F manufactured by Fuji Kogyo was used.
According to UV-1, the upper limit value is 6.4 mPas, and the lower limit value is 6.35.
It has been confirmed that control is possible at mPas, a solvent supply amount of 0.1 cc / time, and T = 10 s. When the application is repeated, the amount of liquid in the receiving pan 4 decreases. Therefore, a command is sent from the controller 19 to the pressure controller 9 based on the measured value of the liquid level gauge 21 to pressurize the application liquid tank 10 and control the liquid supply. The liquid amount is replenished by sending the undiluted coating solution to the blending tank 16 by the container 8. Further, in the present invention, the viscosity is controlled by the blending tank, but the viscosity in the receiving tray 4 actually determines the film thickness. FIG. 5 shows a change in the viscosity of the coating solution in the receiving tray 4. Also in this experiment, a color mosaic manufactured by Fuji Hunt is used, but a low-viscosity type is used. The conditions at the time of viscosity control are an upper limit of 5.16 mPas and a lower limit of 5.1.
Except for 2 mPas, it is the same as the above-mentioned experiment. Even when the viscosity control is performed in the blending tank 16, the viscosity in the receiving pan 4 deviates from the control range of about 5.2 mPas, but fluctuates within the reference value ± 0.1 mPas. However, when the viscosity control is not performed, the viscosity of the coating liquid monotonously increases as shown in FIG.
It can be seen that it deviates from 0.5 mPas corresponding to μm. Therefore, with the above configuration, the viscosity of the coating liquid can be controlled to the reference value ± 0.1 mPas or less, and the waste liquid can be eliminated. The viscosity of the coating solution is about 5 to 10 mP.
Since it is as, it can be said that the viscosity can be controlled to the reference value ± 1 to ± 5%.

【0010】次に受け皿4内の塗布バー支持部材につい
て記す。従来型の構造を斜視断面図で図6に示す。塗布
バー支持部材22はその上面に長手方向に沿って半円形
の溝が形成されている。この溝で塗布バー2を支持し
て、自重によるたわみを防止する役割を持つ。また、こ
の支持部材22は受け皿4に多数のネジ24により固定
され、ネジ24により高さ調整ができるようになってい
る。しかし、支持部材22は合成樹脂でできているため
に加工精度が悪く、上面の溝によって生じる長手方向の
稜線の真直度が0.03mm以上もしくは、使用中の摩
耗などにより図中Aのような突起が生じ、lが0.03
mmを越えるとガラス基板20に塗布した際にすじむら
23が生じやすくなる。塗布バー支持部材22の長手方
向断面図を図7に示す。塗布バー支持部材22は受け皿
4にネジ24で固定されているため、接合面に塗布液の
残留25が生じる。これは洗浄で除去できたか確認でき
ないために、使用中に溶け出し、ガラス基板20に塗布
された際に固形状の異物26として現れることがある。
これらすじむら23や異物26はカラーフィルタの機能
上、欠陥となるので歩留まり低下の要因となる。また、
ガラス基板20の短辺が500mm以上にもなる大形化
に伴い、加工精度は一層悪くなる方向にある。そこで、
本発明では図8に示すように受け皿4内に塗布液接触部
と塗布バー支持部を一体化した液槽部27を持つ構造と
している。液槽部27の材料としてポリフェニレンサル
ファイド樹脂のフォートロン0220(ニップラ化成
製)を採用している。また、受け皿4と液槽部27の結
合は同様にネジ24により固定しているが、接合面全て
が塗布液中には存在しない。接合面が塗布液と接する場
所は、循環用の配管連絡穴の穴28と配管継ぎ手取り付
け穴29である。循環の入り側と出側の2か所で接合面
が塗布液に接触する。従来型の構造と比べ塗布液の残留
する確率は低くなるが液槽部27の反りやひずみによ
り、塗布液が侵入する可能性がある。そこで、穴29の
外径を穴28の外径より1〜4mm大きくしている。ま
たこの液槽部27の構造の特徴として図9に示すよう
に、基板の抜けていく側のB側の段差h2を次式で規定
する。塗布バー2のワイヤ巻線部半径をR1,段付き部
分の半径をR2,支持部高さをhとする。
Next, the coating bar supporting member in the receiving tray 4 will be described. FIG. 6 is a perspective sectional view showing a conventional structure. The coating bar support member 22 has a semicircular groove formed on the upper surface thereof along the longitudinal direction. The groove supports the coating bar 2 and has a role of preventing bending due to its own weight. The support member 22 is fixed to the tray 4 by a number of screws 24, and the height can be adjusted by the screws 24. However, since the support member 22 is made of synthetic resin, the processing accuracy is poor, and the straightness of the longitudinal ridge line generated by the groove on the upper surface is 0.03 mm or more, or as shown in A in FIG. Protrusion occurs, l is 0.03
When the thickness exceeds mm, the line unevenness 23 tends to occur when applied to the glass substrate 20. FIG. 7 shows a longitudinal sectional view of the coating bar support member 22. Since the coating bar support member 22 is fixed to the tray 4 with the screws 24, a coating liquid residue 25 is generated on the joint surface. Since it cannot be confirmed whether or not it has been removed by washing, it may melt during use and appear as a solid foreign matter 26 when applied to the glass substrate 20.
The line unevenness 23 and the foreign matter 26 cause a defect in the function of the color filter, which causes a reduction in yield. Also,
As the short side of the glass substrate 20 is increased to 500 mm or more, the processing accuracy tends to be worse. Therefore,
In the present invention, as shown in FIG. 8, the liquid receiving part 4 has a liquid tank part 27 in which a coating liquid contact part and a coating bar support part are integrated. As a material of the liquid tank portion 27, polytron sulfide resin FORTRON 0220 (manufactured by Nippler Chemical Co., Ltd.) is employed. The connection between the receiving tray 4 and the liquid tank 27 is similarly fixed by the screw 24, but not all of the joining surfaces are present in the coating liquid. The places where the joint surfaces come into contact with the coating liquid are the holes 28 of the circulation pipe connection holes and the pipe joint mounting holes 29. The joining surface comes into contact with the coating liquid at two points, the entry side and the exit side of the circulation. Although the probability that the coating liquid remains is lower than that of the conventional structure, the coating liquid may enter due to warpage or distortion of the liquid tank 27. Therefore, the outer diameter of the hole 29 is set to be larger than the outer diameter of the hole 28 by 1 to 4 mm. As a feature of the structure of the liquid tank section 27, as shown in FIG. 9, a step h2 on the B side where the substrate comes off is defined by the following equation. The radius of the wire winding portion of the coating bar 2 is R1, the radius of the stepped portion is R2, and the height of the support portion is h.

【0011】R1/3≦ h1 ≦ 2×R1/3 R2−h1 ≦ h2 ≦ h/2 実験では R1=6.1mm,R2=4mmの時、h=
12mm,h1=3mm,h2=2,4,6mmで欠陥
のない良好な面状が得られた。また、h2<1では塗布
液が基板が抜けていく側のB部に溜まるために、基板が
入ってくる側の液がなくなり、塗布バー2の表面が乾く
ので欠陥が生じる。
R1 / 3 ≦ h1 ≦ 2 × R1 / 3 R2-h1 ≦ h2 ≦ h / 2 In the experiment, when R1 = 6.1 mm and R2 = 4 mm, h =
With 12 mm, h1 = 3 mm and h2 = 2, 4, 6 mm, a good surface without defects was obtained. Also, when h2 <1, the coating liquid is accumulated in the portion B on the side from which the substrate comes off, so that the liquid on the side where the substrate enters disappears, and the surface of the coating bar 2 dries, causing defects.

【0012】以上の構成により、すじむらや異物などの
塗布膜欠陥を低減できる。
With the above configuration, coating film defects such as stripes and foreign matter can be reduced.

【0013】[0013]

【発明の効果】この発明では、塗布液の粘度を自動制御
することで膜厚の均一性が高い塗布が可能となり、かつ
廃液による塗布液の粘度調整がなくなるので塗布液の無
駄がなく、装置の稼働率も向上する。また、異物やむら
が低減できるので高品質なカラーフィルタの製造が可能
となる。
According to the present invention, by automatically controlling the viscosity of the coating liquid, it is possible to perform coating with high uniformity of the film thickness, and since the viscosity of the coating liquid is not adjusted by the waste liquid, there is no waste of the coating liquid. Operating rate also increases. Further, since foreign matters and unevenness can be reduced, a high quality color filter can be manufactured.

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

【図1】本発明の塗布装置の構成図である。FIG. 1 is a configuration diagram of a coating apparatus of the present invention.

【図2】従来の塗布装置受け皿概略図である。FIG. 2 is a schematic view of a conventional applicator tray.

【図3】膜厚分布の一例である。FIG. 3 is an example of a film thickness distribution.

【図4】粘度制御方式の概略図である。FIG. 4 is a schematic diagram of a viscosity control method.

【図5】粘度制御の効果説明図である。FIG. 5 is an explanatory diagram of an effect of viscosity control.

【図6】従来の受け皿斜視断面図である。FIG. 6 is a perspective sectional view of a conventional saucer.

【図7】塗布バー支持部材と受け皿の結合部説明図であ
る。
FIG. 7 is an explanatory diagram of a coupling portion between a coating bar support member and a tray.

【図8】本発明の受け皿構造説明図である。FIG. 8 is an explanatory view of a tray structure of the present invention.

【図9】本発明の受け皿塗布バー支持部断面図である。FIG. 9 is a cross-sectional view of the saucer application bar support of the present invention.

【符号の説明】[Explanation of symbols]

1…押さえロール、 2…塗布バー、 3…モータ、
4…受け皿、5…フィルタ、 6…溶剤供給ポンプ、7
…溶剤タンク、 8…送液制御器、 9…圧力制御器、
10…塗布液タンク、 11…攪拌駆動モータ、 12
…マグネット、13…攪拌子、 14…粘度計、 15
…粘度計コントローラ、16…調合タンク、 17…塗
布液、 18…循環ポンプ、19…制御器、 20…ガ
ラス基板、 21…液面計、22…塗布バー支持部
1 ... holding roll, 2 ... coating bar, 3 ... motor,
4 ... pan, 5 ... filter, 6 ... solvent supply pump, 7
... Solvent tank, 8 ... Liquid feed controller, 9 ... Pressure controller,
10: coating liquid tank, 11: stirring drive motor, 12
... magnet, 13 ... stirrer, 14 ... viscometer, 15
... Viscometer controller, 16 ... Mixing tank, 17 ... Coating liquid, 18 ... Circulation pump, 19 ... Controller, 20 ... Glass substrate, 21 ... Level gauge, 22 ... Coating bar support

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】非連続性基板を塗布バーと押圧部材との間
に水平に保持させて該基板に塗布液を塗布する装置にお
いて、 前記塗布液を撹拌する攪拌装置及び塗布液の粘度を計測
する粘度計を備えた調合タンクと、 前記粘度計の信号を入力信号として塗布液と溶剤の供給
量を制御する制御器とを具備したことを特徴とする塗布
装置。
An apparatus for applying a coating liquid to a substrate by holding a discontinuous substrate horizontally between a coating bar and a pressing member, wherein a stirrer for stirring the coating liquid and a viscosity of the coating liquid are measured. A coating tank having a viscometer for performing the coating, and a controller for controlling the supply amounts of the coating liquid and the solvent using the signal of the viscometer as an input signal.
【請求項2】請求項1記載の塗布装置において、 前記塗布バーを支持し、塗布液をためる受け皿にポリフ
ェニレンサルファイド系樹脂を使用し、該塗布液と接す
る部分を一体化して残留異物を低減することを特徴とす
る塗布装置。
2. The coating apparatus according to claim 1, wherein a polyphenylene sulfide-based resin is used for a tray supporting the coating bar and storing the coating liquid, and a portion in contact with the coating liquid is integrated to reduce residual foreign matter. A coating device characterized by the above-mentioned.
【請求項3】着色感光性樹脂からなる塗布液を透明基板
に塗布する工程と、フォトリソグラフィーにより着色パ
ターンを形成する工程を繰り返すことによりカラーフィ
ルタを製造するカラーフィルタの製造方法において、 前記基板に塗布する塗布液の粘度を±1〜±5%にする
ことを特徴とするカラーフィルタの製造方法。
3. A color filter manufacturing method for manufacturing a color filter by repeating a step of applying a coating liquid comprising a colored photosensitive resin to a transparent substrate and a step of forming a colored pattern by photolithography, A method for producing a color filter, wherein the viscosity of a coating solution to be applied is set to ± 1 to ± 5%.
JP13189797A 1997-05-22 1997-05-22 Coating applicator and production of color filters Pending JPH10314633A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13189797A JPH10314633A (en) 1997-05-22 1997-05-22 Coating applicator and production of color filters

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13189797A JPH10314633A (en) 1997-05-22 1997-05-22 Coating applicator and production of color filters

Publications (1)

Publication Number Publication Date
JPH10314633A true JPH10314633A (en) 1998-12-02

Family

ID=15068723

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13189797A Pending JPH10314633A (en) 1997-05-22 1997-05-22 Coating applicator and production of color filters

Country Status (1)

Country Link
JP (1) JPH10314633A (en)

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