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JP4578281B2 - Developer clarifier - Google Patents
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JP4578281B2 - Developer clarifier - Google Patents

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JP4578281B2
JP4578281B2 JP2005066742A JP2005066742A JP4578281B2 JP 4578281 B2 JP4578281 B2 JP 4578281B2 JP 2005066742 A JP2005066742 A JP 2005066742A JP 2005066742 A JP2005066742 A JP 2005066742A JP 4578281 B2 JP4578281 B2 JP 4578281B2
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developer
insoluble matter
development
substrate
removing plate
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JP2006251278A (en
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健 堀内
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Panasonic Corp
Panasonic Holdings Corp
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Matsushita Electric Industrial Co Ltd
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Description

本発明は、現像装置における現像液清澄装置およびプラズマディスプレイ用部材の製造方法に関し、更に詳しくは、例えばプラズマディスプレイ用部材として、ガラス基板等の基板上に、電極、誘電体、隔壁(リブ)などのパターンを形成するに際して、パターン現像に用いた後の汚濁した現像液を清澄する装置、さらにこの現像液清澄工程を含むパターン現像工程を有するプラズマディスプレイ用部材の製造方法に関するものである。   The present invention relates to a developer clarifier and a method for producing a member for a plasma display in a developing device. More specifically, for example, as a member for a plasma display, an electrode, a dielectric, a partition (rib), etc. on a substrate such as a glass substrate. The present invention relates to a device for clarifying a contaminated developer after being used for pattern development, and a method for producing a member for a plasma display having a pattern developing step including the developer clarifying step.

従来、例えば、パターン形成基板上に、電極、誘電体、隔壁などのパターンを形成するに際しては、図2にプロセスの概要をモデル的に示したように、
(a)パターン形成基板を現像液中に浸漬することおよび/またはパターン形成基板に現像液を噴射することにより、パターン形成に不要な部分を取り除く現像処理工程、
(b)工程(a)の後、パターン形成基板を洗浄液中に浸漬することおよび/またはパターン形成基板に洗浄液を噴射することにより、パターン形成基板を清浄する清浄処理工程、
(c)エアナイフでパターン形成基板の表面に付着した現像液および/または洗浄液を取り除く液体除去処理工程、
からなるプロセスを採用して行うことが知られている。
Conventionally, for example, when forming a pattern such as an electrode, a dielectric, and a partition wall on a pattern formation substrate, as shown in FIG.
(A) a development processing step of removing a portion unnecessary for pattern formation by immersing the pattern formation substrate in the developer and / or spraying the developer on the pattern formation substrate;
(B) After the step (a), a cleaning process step of cleaning the pattern forming substrate by immersing the pattern forming substrate in the cleaning liquid and / or spraying the cleaning liquid on the pattern forming substrate;
(C) a liquid removal process for removing the developer and / or cleaning liquid adhering to the surface of the pattern forming substrate with an air knife;
It is known to employ a process consisting of:

図2において、1は基板、2は現像液、3は洗浄水、4はシャワー管、5はエアナイフ、6は搬送ローラーである。図2においては、現像処理(a)、清浄処理(b)はそれぞれ、液体を噴射する態様で行うものを示しているが、該液体に基板を浸漬させて行うこと、または浸漬および噴射を併用することによって処理することも可能である。   In FIG. 2, 1 is a substrate, 2 is a developer, 3 is cleaning water, 4 is a shower tube, 5 is an air knife, and 6 is a transport roller. In FIG. 2, the development process (a) and the cleaning process (b) are each performed in a mode in which a liquid is ejected. It is also possible to process by doing.

現像処理工程(a)および清浄処理工程(b)を経た基板は、(c)の液体除去処理工程において、基板1にエアナイフ5から噴射される高圧空気流によって、基板1上に存在している処理液体が吹き飛ばされて除去され、さらに搬送ローラー6によって次の工程に搬送される。   The substrate that has undergone the development processing step (a) and the cleaning processing step (b) is present on the substrate 1 by the high-pressure air flow that is jetted from the air knife 5 to the substrate 1 in the liquid removal processing step of (c). The processing liquid is blown off and removed, and is further transported to the next step by the transport roller 6.

このような工程でパターン形成がなされてきているが、現像処理工程(a)において用いられるアルカリ水溶液などの現像液は、処理装置により清澄化され再利用される。現像液中の不溶物を分離する方法としては、フィルターや液体サイクロンを用いた方法が知られている(例えば、特許文献1参照)。しかしながら、現像液の汚濁の程度が著しい場合には、フィルターや液体サイクロンでは効率良く不溶物除去を行うことができず、かつフィルター交換も頻繁に行なわなければならないといった問題があった。また、ほかにも液体サイクロンでは効率的な固液分離ができないという課題もあった。
特開2005−4197号公報
Although pattern formation has been performed in such a process, a developer such as an alkaline aqueous solution used in the development processing step (a) is clarified and reused by a processing apparatus. As a method for separating insoluble matters in the developer, a method using a filter or a liquid cyclone is known (for example, see Patent Document 1). However, when the degree of contamination of the developing solution is significant, there is a problem that insoluble matter cannot be removed efficiently with a filter or a liquid cyclone, and the filter must be replaced frequently. In addition, there is another problem that the liquid cyclone cannot perform efficient solid-liquid separation.
Japanese Patent Laid-Open No. 2005-4197

本発明の目的は、潜像が形成された基板にパターンを形成した際に、現像に用いた後の汚濁した現像液中の不溶物を効率よく回収して清澄する現像液清澄装置、およびこの現像液清澄工程を含むパターン現像工程を有するプラズマディスプレイ用部材の製造方法を提供することにある。   An object of the present invention is to provide a developer clarifier that efficiently collects and clarifies insoluble matters in a contaminated developer after use in development when a pattern is formed on a substrate on which a latent image is formed, and this It is providing the manufacturing method of the member for plasma displays which has the pattern image development process including a developing solution clarification process.

すなわち、本発明の現像液清澄装置は、潜像が形成された基板を現像液に接触せしめて現像を行う現像処理工程から排出される現像液を清澄する装置であって、
(a)気泡を発生させる気泡発生手段、
(b)前記現像液中に浮遊する不溶物を不溶物除去板に付着させて引き上げる不溶物除去手段、および
(c)前記不溶物除去板に付着した不溶物をブレードによりかき取って除去する手段、
を具備し、
前記不溶物除去板が前記現像液の液面に対して垂直に配置されていることを特徴とする。
また、本発明のプラズマディスプレイ用部材の製造方法は、潜像が形成された基板を現像液に接触せしめて現像を行う製造方法であって、該現像処理工程が、
(a)気泡を発生させる気泡発生工程、
(b)前記現像液中に浮遊する不溶物を、前記現像液の液面に対して垂直に配置した不溶物除去板に付着させて引き上げる不溶物除去工程、および
(c)前記不溶物除去板に付着した不溶物をブレードによりかき取って除去する工程、
具備したことを特徴とする。
That is, the developer clarifier of the present invention, there is provided a equipment you clarified developer discharged from the development processing step of performing development by contacted the substrate on which the latent image is formed in the developer,
(A) the bubble generation hand stage to generate a bubble,
(B) insoluble matter removing means for pulling up the insoluble matter floating in the developer by attaching it to the insoluble matter removing plate ;
(C) means for scraping off and removing insoluble matter adhering to the insoluble matter removing plate with a blade;
Equipped with,
You wherein insolubles removing plate is arranged perpendicular to the liquid surface of the developer.
A method of manufacturing a member for plasma display of the present invention is a development by contacted the substrate on which the latent image is formed on the developer row cormorants Manufacturing method, developing process is,
(A) as the bubble generation factory to generate a bubble,
(B) an insoluble matter removal step of pulling up the insoluble matter floating in the developer by attaching it to an insoluble matter removing plate disposed perpendicularly to the liquid surface of the developer ; and
(C) a step of scraping off and removing the insoluble matter adhering to the insoluble matter removing plate with a blade;
It characterized by comprising a.

本発明によれば、潜像が形成された基板にパターン形成を行うに当たり、現像に用いた後の汚濁した現像液中の不溶物を効率よく回収して清澄できるため、清澄後の現像液を用いて現像を行った場合であっても、パターン形成基板上に異物発生を生ずることが少なく、歩留まり良くパターンを形成することができる。   According to the present invention, when performing pattern formation on a substrate on which a latent image is formed, insoluble matter in a contaminated developer after use in development can be efficiently recovered and clarified. Even in the case where development is carried out, it is possible to form a pattern with a high yield with little occurrence of foreign matter on the pattern formation substrate.

以下、図面に基づいて本発明を詳細に説明する。
図1に本発明の現像液清澄装置の一実施の形態を示す。
本発明の現像液清澄装置は、前述した現像工程における現像処理工程(a)に設置される。
Hereinafter, the present invention will be described in detail with reference to the drawings.
FIG. 1 shows an embodiment of the developer clarification apparatus of the present invention.
The developer clarifier of the present invention is installed in the development processing step (a) in the above-described development step.

現像処理工程(a)において現像に用いた後の汚濁した現像液は、処理槽7に導入される。処理槽7の底部には多孔質物質8が配置されており、外部から送られてきた気体14は多孔質物質8を透過し微細化された気泡13となって浮上する。多孔質物質8は、効率的に現像液中の不溶物12を捕捉するために、タンク底面に液流れの幅方向にわたって、隙間なく、敷き詰められていることが好ましい。装置レイアウト上、隙間なく、敷き詰められない場合は、気泡発生が液流れに対して幅方向に満たされていることが好ましい。通過する液全体が気泡にさらされることで、まんべんなく不要物を浮上させることができる。微細化された気泡13は現像液中の不溶物12とともに浮上し、液面付近に集まる。この際、処理槽7底部から発生する気泡13により、処理槽7において浮遊物引き上げ装置9の方向へ向かう現像液の流れが生じており、液面付近に浮遊している不溶物12は不溶物除去板11に付着する。本実施の形態では、不溶物除去板11はベルトコンベア式となっており付着した不溶物12は順次引き上げられる。引き上げられた不溶物12は浮遊物引き上げ装置9に併設されたブレード10によりかき取られ回収される。   The contaminated developer after being used for development in the development processing step (a) is introduced into the processing tank 7. A porous material 8 is disposed at the bottom of the treatment tank 7, and the gas 14 sent from the outside passes through the porous material 8 and floats as fined bubbles 13. In order to efficiently capture the insoluble matter 12 in the developer, the porous material 8 is preferably spread on the bottom surface of the tank without any gap across the width direction of the liquid flow. In the apparatus layout, when there is no gap and no spread, it is preferable that the bubble generation is satisfied in the width direction with respect to the liquid flow. By exposing the entire liquid that passes through to the air bubbles, it is possible to float the unnecessary material evenly. The micronized bubbles 13 float with the insoluble matter 12 in the developer and gather near the liquid surface. At this time, bubbles 13 generated from the bottom of the processing tank 7 cause a flow of the developing solution in the processing tank 7 in the direction of the suspended matter pulling device 9, and the insoluble matter 12 floating near the liquid surface is insoluble. It adheres to the removal plate 11. In the present embodiment, the insoluble matter removing plate 11 is a belt conveyor type, and the insoluble matter 12 attached is pulled up sequentially. The pulled insoluble matter 12 is scraped off and collected by a blade 10 provided in the suspended matter lifting device 9.

ここで、現像液中の不溶物としては、現像液に溶解しない物質があげられる。特に限定しないが、現像液に溶解しない成分、たとえばアルカリ現像用の感光性ペーストを用いる場合、酸性基を持たない反応性モノマー、紫外線重合開始材、粘度調整剤、分散材、チキソ性付与剤等の添加剤などがあげられる。これらの不溶物には比重の高いガラスフィラーや金属フィラーなども含まれる場合があり、本発明によればこのように比重の高い不溶物も除去することが可能となる。   Here, the insoluble matter in the developer includes a substance that does not dissolve in the developer. Although not particularly limited, when a component that does not dissolve in a developer, for example, a photosensitive paste for alkali development is used, a reactive monomer having no acidic group, an ultraviolet polymerization initiator, a viscosity modifier, a dispersing agent, a thixotropic agent, etc. And the like. These insoluble materials may include glass fillers or metal fillers having a high specific gravity. According to the present invention, it is possible to remove insoluble materials having a high specific gravity.

多孔質物質としては、孔径10μm〜1mmのものが好ましく、10〜200μmのものがより好ましく、さらには10〜100μmのものがより好ましい。孔径が10μm未満であると圧損が高くなり、流量を確保できなくなり、1mmを超えると、気泡が大きくなり、浮遊物の捕捉率が低くなる。   The porous material preferably has a pore diameter of 10 μm to 1 mm, more preferably 10 to 200 μm, and even more preferably 10 to 100 μm. When the pore diameter is less than 10 μm, the pressure loss becomes high, and the flow rate cannot be secured.

処理槽に送りこまれる気体としては、空気のほかに窒素、酸素、アルゴン等の希ガスなどの現像液と反応しない気体などを用いることができる。この場合、気体に含まれる二酸化炭素濃度は10ppm以下であることが好ましく、5ppm以下であることがより好ましい。気体中の二酸化炭素濃度が10ppmを超えるとアルカリ性の現像液と中和反応し、現像液の濃度を低下させるなどの問題が生じ好ましくない。また、処理槽に送り込まれる気体の流量は、多孔質物質表面1mあたり100〜3000L/分であることが好ましく、200〜2000L/分であることがより好ましい。気体の流量が200L/分未満であると一面に行き渡らなくなり、浮遊物捕捉効率が悪くなり、3000L/分を超えると気体の使用量が膨大となり、コストがかさむだけでなく、発生する泡が多くなり、オーバーフロー防止の脱泡施設の設置等設備コストが重なる。 As a gas sent into the processing tank, in addition to air, a gas that does not react with a developing solution such as a rare gas such as nitrogen, oxygen, or argon can be used. In this case, the concentration of carbon dioxide contained in the gas is preferably 10 ppm or less, and more preferably 5 ppm or less. If the concentration of carbon dioxide in the gas exceeds 10 ppm, problems such as a neutralization reaction with an alkaline developer and a decrease in the concentration of the developer occur. Moreover, it is preferable that it is 100-3000 L / min per 1 m < 2 > of porous material surfaces, and, as for the flow volume of the gas sent into a processing tank, it is more preferable that it is 200-2000 L / min. If the gas flow rate is less than 200 L / min, it will not spread all over, and the suspended matter capture efficiency will be poor. If it exceeds 3000 L / min, the amount of gas used will be enormous and not only will cost increase, but many bubbles will be generated. Therefore, the equipment costs such as the installation of a defoaming facility for preventing overflows overlap.

多孔質物質を透過した後の気泡の大きさは、大気圧で直径1mm以下であることが好ましく、0.5mm以下であることがより好ましく、0.2mm以下であることがとくに好ましい。気泡の直径が1mmを超えると浮遊物の捕捉効率が低下する傾向がある。なお、本発明では、気泡の直径は多孔質物質の孔径で換算している。   The size of the bubbles after passing through the porous material is preferably 1 mm or less in diameter at atmospheric pressure, more preferably 0.5 mm or less, and particularly preferably 0.2 mm or less. When the bubble diameter exceeds 1 mm, the trapping efficiency of suspended matter tends to be reduced. In the present invention, the bubble diameter is converted by the pore diameter of the porous material.

不溶物除去板の引き上げ速度は現像液の汚濁の程度や捕捉場所の現像液の流速などに応じて適宜調整すればよいが、例えば10〜200cm/分とすることが好ましい。引き上げ速度が遅すぎる場合は浮遊物が捕捉しきれなくなり、一方、速すぎる場合は効率が悪くなる。ここで、不溶物除去板とは、特に限定しないが、ベルト状、板状のものが良い。材質としては、樹脂、SUS、鉄等の金属、セラミック等、不要物との性状に応じて選択すればよい。不溶物除去板の材質はとくに限定されないが、例えば、スチール、各種ステンレス材質などの金属のほか、金属メッシュ、樹脂板などを用いても良い。なお、不溶物除去能を向上させるため、不溶物除去板表面に多数の起伏やストライプ状の凸部を設けたものを用いることが好ましい。また、不要物除去板は、図1に記載されているように、現像液の液面に対して略垂直で有っても良いし、液面に対して45〜90°の範囲で傾けて設置しても良い。   The lifting speed of the insoluble matter removing plate may be adjusted as appropriate according to the degree of contamination of the developing solution, the flow rate of the developing solution at the capturing site, etc., but is preferably 10 to 200 cm / min, for example. If the pulling speed is too slow, the suspended matter cannot be captured, while if it is too fast, the efficiency becomes poor. Here, the insoluble matter removing plate is not particularly limited, but a belt-like or plate-like one is preferable. The material may be selected according to the properties of the resin, SUS, a metal such as iron, ceramics, and the like. The material of the insoluble matter removing plate is not particularly limited. For example, a metal mesh or a resin plate may be used in addition to a metal such as steel or various stainless steel materials. In order to improve the insoluble matter removing ability, it is preferable to use the insoluble matter removing plate surface provided with a large number of undulations and stripe-shaped convex portions. Further, as shown in FIG. 1, the unnecessary material removing plate may be substantially perpendicular to the liquid surface of the developer, or inclined at a range of 45 to 90 ° with respect to the liquid surface. May be installed.

不溶物除去板により引き上げられた不溶物は、例えば該不溶物除去板に併設されたブレードによりかき取られ回収される。   The insoluble matter pulled up by the insoluble matter removing plate is scraped and collected by, for example, a blade attached to the insoluble matter removing plate.

以上の工程により不溶物が除去された現像液は、さらに遠心分離機により微細な不溶物が除去される。その後新液に一部交換、濃度を調整し、フィルタリング後、再度現像液として現像処理工程(a)に用いられる。   From the developer from which the insoluble matter has been removed by the above-described steps, the fine insoluble matter is further removed by a centrifuge. After that, it is partially exchanged with a new solution, the concentration is adjusted, and after filtering, it is again used as a developer in the development processing step (a).

フィルタリングに用いるフィルターの孔径は、それぞれの工程に応じて適切なものを選択すれば良いが、たとえば感光性ペースト法でプラズマディスプレイの隔壁を製造する場合ならば1〜200μmであることが好ましく、1〜100μmであることがより好ましい。孔径が1μm未満であると目詰まりが激しくコスト高となり、200μmを超えると、ノズル穴の口径を越えるため、ノズル詰まりを誘発する。   The pore diameter of the filter used for filtering may be selected appropriately according to each process. For example, in the case of producing a plasma display partition by a photosensitive paste method, it is preferably 1 to 200 μm. More preferably, it is ˜100 μm. If the hole diameter is less than 1 μm, clogging is severely expensive, and if it exceeds 200 μm, the diameter of the nozzle hole is exceeded and nozzle clogging is induced.

フィルタリング後の現像液中の不溶物濃度は200ppm以下であることが好ましく、100ppm以下であることがより好ましい。不溶物濃度が200ppmを超えると使用材料にもよるが、フィルター後の配管ラインで凝集物が発生しやすくなる。   The insoluble matter concentration in the developer after filtering is preferably 200 ppm or less, and more preferably 100 ppm or less. If the insoluble matter concentration exceeds 200 ppm, depending on the material used, aggregates are likely to be generated in the piping line after the filter.

処理後の現像液の温度は、例えば10〜40℃に調整することが好ましく、20〜40℃に調整することがより好ましい。   The temperature of the developer after processing is preferably adjusted to, for example, 10 to 40 ° C, and more preferably adjusted to 20 to 40 ° C.

また、処理後の現像液は新液に一部交換して濃度を調整したのち、再利用される。調整後の現像液濃度は使用材料により適正値を設定すればよいが、たとえばプラズマディスプレイで感光性銀ペーストを用いて、炭酸ナトリウムで電極パターンを現像する場合、0.1〜1重量%であることが好ましく、0.1〜0.7重量%であることがより好ましい。濃度が0.1重量%未満であると現像時間が長くなる、現像残渣が残りやすい結果となり、1重量%を超えると現像時間が早すぎ、制御しにくく、剥がれ等の欠陥を生みやすい。   Further, the processed developer is partially reused after being replaced with a new solution to adjust the concentration. The developer concentration after adjustment may be set to an appropriate value depending on the material used. For example, when the electrode pattern is developed with sodium carbonate using a photosensitive silver paste in a plasma display, it is 0.1 to 1% by weight. It is preferably 0.1 to 0.7% by weight. If the concentration is less than 0.1% by weight, the development time becomes long, and development residues are likely to remain. If the concentration exceeds 1% by weight, the development time is too early, it is difficult to control, and defects such as peeling are likely to occur.

本発明において、基板に形成されるパターンの種類はとくに限定されるものではないが、凹凸形態またはマトリックス構造を含むパターンであることが好ましく、具体的には、電極、蛍光体層、誘電体、隔壁、ブラックマトリックス、ブラックストライプ、またはカラーフィルターなどがあげられる。   In the present invention, the type of pattern formed on the substrate is not particularly limited, but is preferably a pattern including a concavo-convex form or a matrix structure, specifically, an electrode, a phosphor layer, a dielectric, A partition, a black matrix, a black stripe, or a color filter can be used.

以下に本発明を実施例を用いて具体的に説明する。ただし、本発明はこれに限定されるものではない。なお、実施例中の%は断りのない限り重量%を示す。   Hereinafter, the present invention will be specifically described with reference to examples. However, the present invention is not limited to this. In addition, unless otherwise indicated,% in an Example shows weight%.

実施例1
図2に示すような、現像処理工程(a)、清浄処理工程(b)、液体除去処理工程(c)の3つから構成されたパターン現像装置を用いて基板にパターンを形成した。
Example 1
As shown in FIG. 2, a pattern was formed on the substrate using a pattern developing apparatus composed of a development processing step (a), a cleaning processing step (b), and a liquid removal processing step (c).

現像処理工程にはシャワー管が設置されており、その下を基板が一定の速度で移動し、ノズルから現像液が噴射され、不要部分を化学反応により除去した。   A shower tube was installed in the development processing step, the substrate was moved under the shower tube at a constant speed, the developer was sprayed from the nozzle, and unnecessary portions were removed by chemical reaction.

清浄処理工程(b)においては、シャワー管1本につきノズルがピッチ100mm毎に下向きに設置されており、その下を前記現像部で不要部分を除去された基板を一定の速度で移動させた。ノズルから基板の上に水を噴射させ、現像物を洗い流した。   In the cleaning process step (b), nozzles were installed downward with a pitch of 100 mm per shower tube, and the substrate from which unnecessary portions were removed by the developing unit was moved at a constant speed. Water was sprayed onto the substrate from the nozzle to wash away the developer.

最後に液体除去処理工程(c)には、スリット上に空気を吹き出させる、いわゆるエアナイフが設置されており、基板表面に付着した液体をエアの力により吹き飛ばした。   Finally, in the liquid removal treatment step (c), a so-called air knife for blowing air onto the slit was installed, and the liquid adhering to the substrate surface was blown off by the force of air.

この装置を用いて、感光性ペースト法により60インチ基板に焼成前高さ200μmの隔壁を形成した。現像により1枚あたり、およそ300gのペーストが現像液内に残渣として混入することになるが、これをタクト1分で200枚現像した。   Using this apparatus, a partition wall having a height of 200 μm before firing was formed on a 60-inch substrate by a photosensitive paste method. About 300 g of paste per sheet is mixed as a residue in the developer by development, and 200 sheets were developed in 1 minute.

ここで、現像処理工程(a)で使用された現像液中の不溶物は本発明の現像液清澄装置により除去し、さらに遠心分離装置により現像液中に溶けている成分以外を取り除いた。最後に現像タンクを経て、35℃に液温調整、新液に一部交換、濃度を0.5%に調整したのち、濾過フィルター(商標名:ウルチプリーツハイフロー(HFU640UY1000JU)、pall社製、孔径100μm)を3本用いてフィルタリング後、再度現像液として使用した。   Here, the insoluble matter in the developer used in the development processing step (a) was removed by the developer clarifier of the present invention, and components other than the components dissolved in the developer were removed by a centrifugal separator. Finally, after passing through the development tank, the liquid temperature is adjusted to 35 ° C, partly replaced with a new liquid, and the concentration is adjusted to 0.5%. 100 μm) was used for filtering, and then again used as a developer.

現像液清澄装置の処理槽底部には、多孔質物質(商標名:フィルトロプラスト#80、pall社製、孔径80μm)を設置した。多孔質物質を透過した後の気泡は大気圧下(水面浮上時に)平均径100μm以下だった。使用した空気は炭酸ガス濃度が5ppmのものを用い、多孔質物質表面1mあたりに750L/分(大気圧下)の流量で空気を送り込んだ。現像液中に浮遊する不溶物は、浮遊物引き上げ装置(商標名:オイルスキマー、アコージャパン(株)製)および処理槽幅一杯のサイズに設定された引き上げベルト(材質:SUS631)を用いて気泡とともに150cm/分の速度で引き上げられた。 A porous substance (trade name: Filtroplast # 80, manufactured by Pall Inc., pore size 80 μm) was placed at the bottom of the processing tank of the developer clarifier. Bubbles after passing through the porous material had an average diameter of 100 μm or less under atmospheric pressure (when the water surface floated). The air used had a carbon dioxide concentration of 5 ppm, and air was fed at a flow rate of 750 L / min (under atmospheric pressure) per 1 m 2 of the porous material surface. The insoluble matter floating in the developer is bubbled using a suspended matter lifting device (trade name: Oil Skimmer, manufactured by Accor Japan Co., Ltd.) and a lifting belt (material: SUS631) set to the size of the processing tank. At the same time, it was raised at a speed of 150 cm / min.

前記現像液清澄処理後の現像液中の不溶物濃度(SS:標準法1GFP濾過法)は常に30ppmで一定となり、フィルターの寿命が基板7000枚の現像処理につき1回の交換となった。   The insoluble matter concentration (SS: standard method 1 GFP filtration method) in the developer after the developer clarification treatment was always constant at 30 ppm, and the filter life was changed once per 7000 substrates.

また、異物検査装置(SATURN9000、Vテクノロジー(株)製)を用いて、検出条件20ミクロン角以上を検出するよう設定し、現像後の基板表面の異物について評価したところ、以下に定義する異物検出率が0.3%となった。   Also, using a foreign substance inspection apparatus (SATURN9000, manufactured by V Technology Co., Ltd.), detection conditions were set to detect 20 micron square or more, and the foreign substance on the substrate surface after development was evaluated. The rate was 0.3%.

異物検出率(%)={(異物の検出された基板数)/(全検査基板数)}×100。     Foreign matter detection rate (%) = {(number of substrates on which foreign matter is detected) / (total number of test substrates)} × 100.

実施例2
多孔質物質としてフィルトロプラスト♯80の代わりにフィルトロプラスト#150(孔径150μm)を用いた以外は実施例1と同様の操作を行ったところ、現像液中の不溶物濃度が50ppmで一定となり、フィルターの寿命が基板4000枚の現像処理つき1回の交換となった。また異物検出率が0.5%となった。
実施例3
多孔質物質としてフィルトロプラスト♯80の代わりにフィルトロプラスト#30(孔径30μm)を用いた以外は実施例1と同様の操作を行ったところ、現像液中の不溶物濃度が20ppmで一定となり、フィルターの寿命が基板10000枚の現像処理つき1回の交換となった。また異物検出率が0.2%となった。
Example 2
When the same operation as in Example 1 was carried out except that Filtroplast # 150 (pore size 150 μm) was used instead of Filtroplast # 80 as the porous material, the concentration of insoluble matter in the developer became constant at 50 ppm. The life of the filter was replaced once with a development process of 4000 substrates. Further, the foreign matter detection rate was 0.5%.
Example 3
When the same operation as in Example 1 was carried out except that Filtroplast # 30 (pore diameter 30 μm) was used instead of Filtroplast # 80 as the porous material, the concentration of insoluble matter in the developer became constant at 20 ppm. The lifetime of the filter was changed once with a development process of 10,000 substrates. Further, the foreign matter detection rate was 0.2%.

比較例1
現像液清澄装置において、多孔質物質および浮遊物引き上げ装置を用いなかった以外は実施例1と同様の操作を行ったところ、浮遊物質量が200ppmで一定となり、フィルターの寿命が基板1000枚の現像処理につき1回の交換となった。また異物検出率が5%と悪化した。
Comparative Example 1
In the developer clarification device, the same operation as in Example 1 was performed except that the porous material and the suspended matter lifting device were not used. As a result, the suspended matter amount became constant at 200 ppm, and the lifetime of the filter was developed for 1000 substrates. One replacement per treatment. Moreover, the foreign matter detection rate deteriorated to 5%.

比較例2
現像液清澄装置において、多孔質物質を用いなかった以外は実施例1と同様の操作を行ったところ、浮遊物質量が170ppmで一定となり、フィルターの寿命が基板1500枚の現像処理につき1回の交換となった。また異物検出率が3%と悪化した。
Comparative Example 2
In the developer clarification apparatus, the same operation as in Example 1 was performed except that no porous material was used. As a result, the amount of suspended solids was constant at 170 ppm, and the filter life was once per 1500 substrate development processes. It became an exchange. Moreover, the foreign matter detection rate deteriorated to 3%.

Figure 0004578281
Figure 0004578281

現像処理工程(a)において用いられる現像液清澄装置の図を示す。The figure of the developing solution clarifier used in the image development process (a) is shown. 本発明で採用する現像処理工程(a)、清浄処理工程(b)および液体除去処理工程(c)の3工程を有するパターン形成工程の概要をモデル的に示したものである。The outline of the pattern formation process which has three processes, the development process process (a), the cleaning process process (b), and the liquid removal process process (c) which are employ | adopted by this invention is shown in model.

符号の説明Explanation of symbols

1 基板
2 現像液
3 洗浄水
4 シャワー管
5 エアナイフ
6 搬送ローラー
7 現像液処理槽
8 多孔質物質
9 浮遊物引き上げ装置
10 ブレード
11 不溶物除去板
12 不溶物
13 気泡
14 気体
a 現像処理工程
b 清浄処理工程
c 液体除去処理工程
DESCRIPTION OF SYMBOLS 1 Substrate 2 Developer 3 Washing water 4 Shower tube 5 Air knife 6 Transport roller 7 Developer processing tank 8 Porous material 9 Floating substance lifting device 10 Blade 11 Insoluble matter removal plate 12 Insoluble matter 13 Bubble 14 Gas a Development process b Clean Treatment process c Liquid removal treatment process

Claims (2)

潜像が形成された基板を現像液に接触せしめて現像を行う現像処理工程から排出される現像液を清澄する現像液清澄装置であって、
(a)気泡を発生させる気泡発生手段、
(b)前記現像液中に浮遊する不溶物を不溶物除去板に付着させて引き上げる不溶物除去手段、および
(c)前記不溶物除去板に付着した不溶物をブレードによりかき取って除去する手段、
を具備し、
前記不溶物除去板が前記現像液の液面に対して垂直に配置されていることを特徴とする現像液清澄装置。
A developer clarifier that clarifies a developer discharged from a development processing step in which development is performed by bringing a substrate on which a latent image is formed into contact with the developer,
(A) the bubble generation hand stage to generate a bubble,
(B) insoluble matter removing means for pulling up the insoluble matter floating in the developer by attaching it to the insoluble matter removing plate ;
(C) means for scraping off and removing insoluble matter adhering to the insoluble matter removing plate with a blade;
Equipped with,
The developer clarification apparatus, wherein the insoluble matter removing plate is disposed perpendicular to the liquid level of the developer.
潜像が形成された基板を現像液に接触せしめて現像を行う現像処理工程を含むプラズマディスプレイ用部材の製造方法であって、該現像処理工程が、
(a)気泡を発生させる気泡発生工程、
(b)前記現像液中に浮遊する不溶物を、前記現像液の液面に対して垂直に配置した不溶物除去板に付着させて引き上げる不溶物除去工程、および
(c)前記不溶物除去板に付着した不溶物をブレードによりかき取って除去する工程、
具備したことを特徴とするプラズマディスプレイ用部材の製造方法。
A method for producing a member for a plasma display, which includes a development processing step in which development is performed by bringing a substrate on which a latent image is formed into contact with a developing solution,
(A) as the bubble generation factory to generate a bubble,
(B) an insoluble matter removal step of pulling up the insoluble matter floating in the developer by attaching it to an insoluble matter removing plate disposed perpendicularly to the liquid surface of the developer ; and
(C) a step of scraping off and removing the insoluble matter adhering to the insoluble matter removing plate with a blade;
The manufacturing method of the member for plasma displays characterized by comprising.
JP2005066742A 2005-03-10 2005-03-10 Developer clarifier Expired - Fee Related JP4578281B2 (en)

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