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JP2023048697A - SUBSTRATE DRYING APPARATUS, SUBSTRATE PROCESSING APPARATUS, AND SUBSTRATE DRYING METHOD - Google Patents

SUBSTRATE DRYING APPARATUS, SUBSTRATE PROCESSING APPARATUS, AND SUBSTRATE DRYING METHOD Download PDF

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JP2023048697A
JP2023048697A JP2021158152A JP2021158152A JP2023048697A JP 2023048697 A JP2023048697 A JP 2023048697A JP 2021158152 A JP2021158152 A JP 2021158152A JP 2021158152 A JP2021158152 A JP 2021158152A JP 2023048697 A JP2023048697 A JP 2023048697A
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substrate
volatile solvent
liquid
film
drying
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JP7504850B2 (en
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淳 松下
Atsushi Matsushita
陽子 埀野
Yoko Taruno
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Shibaura Mechatronics Corp
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    • H01L21/6704Apparatus for fluid treatment for cleaning followed by drying, rinsing, stripping, blasting or the like for wet cleaning or washing
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    • H01L21/677Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere for conveying, e.g. between different workstations
    • H01L21/67739Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere for conveying, e.g. between different workstations into and out of processing chamber
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Abstract

【課題】簡素な構成で、パターン閉塞の発生を低減できる基板乾燥装置、基板処理装置及び基板乾燥方法を提供する。【解決手段】基板処理装置1において、基板乾燥装置300は、加熱部36と、第1の揮発性溶剤供給部34と、撥水化剤を含み、気化する際の表面張力が、第1の揮発性溶剤Vよりも小さい第2の揮発性溶剤を供給する第2の揮発性溶剤供給部35と、液膜が形成された基板Wが搬入される乾燥室31と、基板を回転させる駆動機構と、第1の揮発性溶剤供給部から第1の揮発性溶剤を供給させて液膜を第1の揮発性溶剤へ置換させ、第2の揮発性溶剤供給部から第2の揮発性溶剤Hを供給させて基板に形成された第1の揮発性溶剤を第2の揮発性溶剤へ置換させるとともに撥水化膜を形成させ、加熱部に基板を加熱させて第2の揮発性溶剤の液膜と基板との間に気層を生じさせ、第2の揮発性溶剤の液膜を回転による遠心力により排出させる。【選択図】図2A substrate drying apparatus, a substrate processing apparatus, and a substrate drying method capable of reducing the occurrence of pattern clogging with a simple configuration are provided. A substrate drying device (300) in a substrate processing apparatus (1) includes a heating section (36), a first volatile solvent supply section (34), and a water repellent agent whose surface tension when vaporized is a first level. A second volatile solvent supply unit 35 for supplying a second volatile solvent smaller than the volatile solvent V, a drying chamber 31 into which the substrate W on which the liquid film is formed is carried, and a driving mechanism for rotating the substrate. Then, the first volatile solvent is supplied from the first volatile solvent supply unit to replace the liquid film with the first volatile solvent, and the second volatile solvent supply unit supplies the second volatile solvent H to replace the first volatile solvent formed on the substrate with the second volatile solvent and form a water-repellent film, and the heating unit heats the substrate to produce the second volatile solvent liquid An air layer is generated between the film and the substrate, and the liquid film of the second volatile solvent is discharged by centrifugal force due to rotation. [Selection drawing] Fig. 2

Description

本発明は、基板乾燥装置、基板処理装置及び基板乾燥方法に関する。 The present invention relates to a substrate drying apparatus, a substrate processing apparatus, and a substrate drying method.

半導体や液晶パネルなどを製造する製造工程では、ウェーハや液晶基板などの基板の被処理面に処理液を供給して被処理面を処理し、処理後、被処理面を洗浄、乾燥させる基板処理装置が用いられる。 In the manufacturing process of semiconductors and liquid crystal panels, etc., substrate processing involves supplying a processing liquid to the processing surface of a substrate such as a wafer or liquid crystal substrate, processing the processing surface, and then washing and drying the processing surface after processing. A device is used.

この基板処理装置の乾燥工程においては、パターン同士の間隔や構造、処理液の表面張力などに起因して、例えばメモリセルやゲート周りなどのパターンが倒壊して閉塞することがある。特に、近年の半導体の高集積化や高容量化に伴う微細化に伴って、配線幅や開口幅に対する深さの比率であるアスペクト比が高くなっているため、パターン倒壊は発生しやすくなっている。 In the drying process of this substrate processing apparatus, patterns such as those around memory cells and gates may collapse and become clogged due to the spacing and structure of the patterns, the surface tension of the processing liquid, and the like. In particular, the aspect ratio, which is the ratio of the depth to the wiring width and opening width, has increased with the recent miniaturization associated with the high integration and high capacity of semiconductors, making pattern collapse more likely to occur. there is

このようなパターン倒壊を抑制するために、DIW(超純水)によるリンス処理後に、IPA(2-プロパノール:イソプロピルアルコール)を用いる基板乾燥方法が提案されている。この基板乾燥方法は、基板表面上のDIW(超純水)を、DIWよりも表面張力が小さいIPAに置換することにより、乾燥処理時における表面張力によるパターン倒壊を低減するものである。 In order to suppress such pattern collapse, a substrate drying method using IPA (2-propanol: isopropyl alcohol) after rinsing with DIW (ultra-pure water) has been proposed. This substrate drying method replaces DIW (ultra-pure water) on the substrate surface with IPA, which has a lower surface tension than DIW, thereby reducing pattern collapse due to surface tension during the drying process.

特開2008-034779号公報JP 2008-034779 A

しかしながら、半導体の微細化は益々進んでおり、IPAのように揮発性が高い有機溶媒(揮発性溶剤)を使用する乾燥を行った場合でも、ウェーハの微細パターンは液体の表面張力などにより倒れることがある。 However, the miniaturization of semiconductors is progressing more and more, and even when drying using a highly volatile organic solvent (volatile solvent) such as IPA, the fine pattern of the wafer collapses due to the surface tension of the liquid. There is

例えば、液体が乾燥していく過程で基板表面の乾燥速度に不均一が生じ、一部のパターン間に液体が残ると、その部分の液体の表面張力によってパターンが倒壊する。詳しくは、液体が残った部分のパターン同士が、液体の表面張力による弾性変形によって倒れ、その液中にわずかに溶けた残渣が凝集する。そして、液体が完全に気化すると、倒れたパターン同士が固着して閉塞する。 For example, when the drying speed of the substrate surface becomes non-uniform during the process of drying the liquid, and if the liquid remains between some patterns, the pattern collapses due to the surface tension of the liquid in that part. Specifically, the patterns of the portion where the liquid remains are collapsed due to elastic deformation due to the surface tension of the liquid, and the residue slightly dissolved in the liquid aggregates. Then, when the liquid is completely vaporized, the fallen patterns adhere to each other and block.

これに対処するため、IPAに加えて、基板Wの表面を撥水化可能な修飾剤である撥水化剤を供給することにより、IPAの液膜に浸透した撥水化剤によって、基板の表面の水酸基を、官能基へ置換することにより、撥水化膜を形成することが行われている。これにより、パターン間にも撥水化膜が形成され、親液性が低下して液体の接触角が上がる。つまり、基板の表面上にある液体の表面張力がより一層低くなるため、パターン同士が引き合う力を弱くすることができ、パターン倒壊を抑制できる。 In order to deal with this, in addition to IPA, a water-repellent agent, which is a modifier capable of making the surface of the substrate W water-repellent, is supplied. A water-repellent film is formed by replacing hydroxyl groups on the surface with functional groups. As a result, a water-repellent film is formed also between the patterns, the lyophilicity is lowered, and the contact angle of the liquid is increased. That is, since the surface tension of the liquid on the surface of the substrate is further lowered, the force of attraction between the patterns can be weakened, and collapse of the patterns can be suppressed.

撥水化剤を用いる場合、撥水化剤の供給による撥水化膜の形成後、IPA等によってリンス処理を行って余分な撥水化剤を除去してから、乾燥処理を行う。しかし、乾燥処理を行った後にも、基板表面に形成された撥水化膜は残存する。このため、基板表面の撥水化膜を除去する撥水化膜除去処理を行う必要がある。撥水化膜の除去は、例えば、アッシングに用いるようなプラズマ処理又はUV照射処理によって行う。 When a water-repellent agent is used, after the water-repellent film is formed by supplying the water-repellent agent, the excess water-repellent agent is removed by rinsing with IPA or the like, followed by drying. However, even after the drying treatment, the water-repellent film formed on the substrate surface remains. Therefore, it is necessary to perform a water-repellent film removal process for removing the water-repellent film on the substrate surface. The removal of the water-repellent film is performed, for example, by plasma treatment such as ashing or UV irradiation treatment.

このため、基板処理装置に、乾燥装置とは独立したプラズマ処理装置又はUV照射装置などの除去装置を追加する必要があるとともに、乾燥装置から除去装置への搬送工程が必要となる。すると、基板処置装置が複雑化、大型化するとともに、工程数が多くなり、基板処理の生産性が低下する。さらに、パターンが深くなりアスペクト比が増すと、UV照射ではパターン底部まで撥水化膜を除去できない可能がある。 For this reason, it is necessary to add a removal device such as a plasma processing device or a UV irradiation device to the substrate processing apparatus independently of the drying device, and a transfer process from the drying device to the removal device is required. As a result, the substrate processing apparatus becomes complicated and large, the number of processes increases, and the productivity of substrate processing decreases. Furthermore, when the pattern becomes deeper and the aspect ratio increases, UV irradiation may not be able to remove the water-repellent film to the bottom of the pattern.

本発明の実施形態は、簡素な構成で、パターン閉塞の発生を低減できる基板乾燥装置、基板処理装置及び基板乾燥方法を提供することを目的とする。 An object of the embodiments of the present invention is to provide a substrate drying apparatus, a substrate processing apparatus, and a substrate drying method that can reduce the occurrence of pattern clogging with a simple configuration.

本発明の実施形態の基板乾燥装置は、基板を加熱する加熱部と、前記基板の被処理面上に第1の揮発性溶剤を供給する第1の揮発性溶剤供給部と、前記基板の被処理面上に、撥水化膜を形成する撥水化剤を含み、気化する際の表面張力が前記第1の揮発性溶剤よりも小さい第2の揮発性溶剤を供給する第2の揮発性溶剤供給部と、前記加熱部、前記第1の揮発性溶剤供給部及び前記第2の揮発性溶剤供給部が収容され、被処理面上に処理液による液膜が形成された状態の前記基板が搬入される乾燥室と、前記乾燥室に搬入された前記基板を受け取る支持部と、前記支持部に支持された前記基板を回転させる駆動機構と、前記第1の揮発性溶剤供給部から前記第1の揮発性溶剤を供給させることにより、前記基板の被処理面上に形成された前記処理液による液膜を前記第1の揮発性溶剤へ置換させ、前記第2の揮発性溶剤供給部から前記第2の揮発性溶剤を供給させることにより、前記基板の被処理面上に形成された前記第1の揮発性溶剤を前記第2の揮発性溶剤へ置換させるとともに、前記基板の被処理面に前記撥水化膜を形成させ、前記加熱部に前記基板を加熱させることにより、前記撥水化剤を含む前記第2の揮発性溶剤の液膜と前記基板との間に気層を生じさせることによって、前記第2の揮発性溶剤の液膜を前記基板の回転による遠心力により排出させる制御装置と、を有する。 A substrate drying apparatus according to an embodiment of the present invention includes a heating section for heating a substrate, a first volatile solvent supply section for supplying a first volatile solvent onto a surface to be processed of the substrate, and A second volatile solvent that contains a water repellent agent that forms a water repellent film on the treated surface and that supplies a second volatile solvent that has a lower surface tension than the first volatile solvent when vaporized. The substrate in which the solvent supply unit, the heating unit, the first volatile solvent supply unit, and the second volatile solvent supply unit are accommodated, and a liquid film of the processing liquid is formed on the surface to be processed. a drying chamber into which is carried in; a supporting portion that receives the substrate carried into the drying chamber; a drive mechanism that rotates the substrate supported by the supporting portion; By supplying a first volatile solvent, a liquid film of the processing liquid formed on the surface to be processed of the substrate is replaced with the first volatile solvent, and the second volatile solvent supply unit By supplying the second volatile solvent from the substrate, the first volatile solvent formed on the surface to be processed of the substrate is replaced with the second volatile solvent, and the substrate to be processed is replaced with the second volatile solvent. By forming the water-repellent film on the surface and heating the substrate with the heating unit, an air layer is formed between the liquid film of the second volatile solvent containing the water-repellent agent and the substrate. and a control device for discharging the liquid film of the second volatile solvent by centrifugal force generated by the rotation of the substrate.

本発明の実施形態の基板処理装置は、前記基板を回転させながら第1の処理液を供給することにより処理する処理装置と、前記処理装置により処理済の前記基板を回転させながら第2の処理液を供給することにより洗浄する洗浄装置と、前記基板乾燥装置と、前記洗浄装置において洗浄された前記基板を、前記洗浄装置で供給された前記第2の処理液による液膜が形成された状態で搬出し、前記基板乾燥装置に搬入する搬送装置と、を有する。 A substrate processing apparatus according to an embodiment of the present invention includes a processing apparatus that processes the substrate by supplying a first processing liquid while rotating the substrate, and a substrate that has been processed by the processing apparatus and performs a second processing while rotating the substrate. A cleaning device for cleaning by supplying a liquid, a substrate drying device, and a state in which a liquid film is formed on the substrate cleaned by the cleaning device by the second processing liquid supplied by the cleaning device. and a conveying device for carrying out the substrate at the substrate drying device and carrying it into the substrate drying device.

本発明の実施形態の基板乾燥方法は、処理液による液膜が形成され、支持部に支持された基板を駆動機構により回転させながら、第1の揮発性溶剤供給部からの第1の揮発性溶剤の供給により前記処理液による液膜を前記第1の揮発性溶剤へ置換し、第2の揮発性溶剤供給部から、撥水化膜を形成する撥水化剤を含み、気化する際の表面張力が前記第1の揮発性溶剤よりも小さい第2の揮発性溶剤の供給により、前記第1の揮発性溶剤の液膜を前記第2の揮発性溶剤に置換するとともに、前記基板に撥水化膜を形成させ、加熱部による前記基板の加熱により、前記撥水化剤を含む前記第2の揮発性溶剤の液膜と前記基板との間に気層を生じさせることによって、前記第2の揮発性溶剤の液膜を前記基板の回転による遠心力により排出させる。 In the substrate drying method according to the embodiment of the present invention, the first volatile solvent supplied from the first volatile solvent supply unit is rotated by the drive mechanism while the substrate on which the liquid film of the treatment liquid is formed and supported by the support unit is rotated. By supplying the solvent, the liquid film of the treatment liquid is replaced with the first volatile solvent. By supplying a second volatile solvent whose surface tension is lower than that of the first volatile solvent, the liquid film of the first volatile solvent is replaced with the second volatile solvent, and the substrate is repellent. By forming a hydrated film and heating the substrate by a heating unit, an air layer is generated between the liquid film of the second volatile solvent containing the water repellent agent and the substrate. The liquid film of the volatile solvent of 2 is discharged by the centrifugal force caused by the rotation of the substrate.

本発明の実施形態は、簡素な構成で、パターン閉塞の発生を低減できる基板乾燥装置、基板処理装置及び基板乾燥方法を提供することができる。 The embodiments of the present invention can provide a substrate drying apparatus, a substrate processing apparatus, and a substrate drying method that can reduce the occurrence of pattern clogging with a simple configuration.

実施形態の基板処理装置を示す簡略構成図である。1 is a simplified configuration diagram showing a substrate processing apparatus according to an embodiment; FIG. 図1の基板処理装置の洗浄装置及び乾燥装置を示す構成図である。2 is a configuration diagram showing a cleaning device and a drying device of the substrate processing apparatus of FIG. 1; FIG. 乾燥装置の基板搬入時(A)、第1の揮発性溶剤供給時(B)を示す内部構成図である。FIG. 4 is an internal configuration diagram showing the time (A) when the substrate is loaded into the drying device and the time (B) when the first volatile solvent is supplied. 乾燥装置の第2の撥水性溶剤供給時(A)、第1の揮発性溶剤供給時及び膜厚測定時(B)を示す内部構成図である。It is an internal configuration diagram showing the time of supplying the second water-repellent solvent (A), the time of supplying the first volatile solvent, and the time of film thickness measurement (B) of the drying device. 乾燥装置の基板乾燥時を示す内部構成図である。FIG. 4 is an internal configuration diagram showing the substrate drying time of the drying apparatus; 実施形態の基板乾燥処理の手順を示すフローチャートである。4 is a flow chart showing a procedure of substrate drying processing according to the embodiment; ライデンフロスト現象を利用した乾燥処理の流れを模式的に示す説明図である。FIG. 4 is an explanatory diagram schematically showing the flow of drying processing using the Leidenfrost phenomenon; パターン内に残留する液膜を示す説明図である。FIG. 4 is an explanatory diagram showing a liquid film remaining in a pattern;

以下、本発明の実施形態を、図面を参照して説明する。
[概要]
図1に示すように、本実施形態の基板処理装置1は、各種の処理を行う装置を収容した複数のチャンバ1aを備え、前工程でカセット(FOUP)1bに複数枚収容されて搬送されてきた基板Wに対して、各チャンバ1a内で1枚ずつ処理を行う枚葉処理の装置である。未処理の基板Wは、カセット1bから搬送ロボット1cによって1枚ずつ取り出され、バッファユニット1dに一時的に載置された後、以下に説明する各種装置により、各チャンバ1aへの搬送及び処理が行われる。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, embodiments of the present invention will be described with reference to the drawings.
[overview]
As shown in FIG. 1, a substrate processing apparatus 1 of the present embodiment includes a plurality of chambers 1a containing apparatuses for performing various types of processing. This is a single-wafer processing apparatus that processes the substrates W one by one in each chamber 1a. The unprocessed substrates W are taken out one by one from the cassette 1b by the transport robot 1c, temporarily placed in the buffer unit 1d, and then transported to each chamber 1a and processed by various devices described below. done.

基板処理装置1は、処理装置110、洗浄装置120、搬送装置200、乾燥装置300、制御装置400を含む。処理装置110は、例えば、回転する基板Wに、第1の処理液(例えば、リン酸水溶液、フッ酸及び硝酸の混合液、酢酸、硫酸及び過酸化水素水の混合液(SPM:Sulfuric hydrogen Peroxide Mixture)等)を供給することによって、不要な膜を除去して回路パターンを残すエッチング装置である。洗浄装置120は、エッチング装置でエッチング処理された基板Wを、洗浄液(第2の処理液)により洗浄する。搬送装置200は、バッファユニット1dと各チャンバ1aとの間、各チャンバ1aの間で基板Wを搬送する。例えば、搬送装置200は、処理装置110において処理済の基板Wを洗浄装置120に搬送し、洗浄装置120において洗浄された基板Wを乾燥装置300に搬送する。乾燥装置(基板乾燥装置)300は、洗浄液により洗浄された基板Wを回転させながら加熱することにより、乾燥処理を行う。制御装置400は、上記の各装置を制御する。 The substrate processing apparatus 1 includes a processing apparatus 110 , a cleaning apparatus 120 , a transfer apparatus 200 , a drying apparatus 300 and a control apparatus 400 . The processing apparatus 110 applies, for example, a first processing liquid (for example, a phosphoric acid aqueous solution, a mixed liquid of hydrofluoric acid and nitric acid, a mixed liquid of acetic acid, sulfuric acid, and hydrogen peroxide water (SPM: Sulfuric hydrogen peroxide solution) to the rotating substrate W. Mixture, etc.) to remove unnecessary films and leave a circuit pattern. The cleaning device 120 cleans the substrate W etched by the etching device with a cleaning liquid (second processing liquid). The transport device 200 transports the substrate W between the buffer unit 1d and each chamber 1a and between each chamber 1a. For example, the transport device 200 transports the substrate W processed in the processing device 110 to the cleaning device 120 and transports the substrate W cleaned in the cleaning device 120 to the drying device 300 . The drying device (substrate drying device) 300 performs a drying process by heating the substrate W cleaned with the cleaning liquid while rotating it. The control device 400 controls each device described above.

なお、本実施形態により処理される基板Wは、例えば、半導体ウェーハである。以下、基板Wのパターン等が形成された面を被処理面とする。洗浄処理のための処理液である洗浄液としては、アルカリ洗浄液(APM)、超純水(DIW)、第1の揮発性溶剤(IPA)を使用する。АPMは、アンモニア水と過酸化水素水を混合した薬液であり、残留有機物を除去するために使用する。DIWは、APM処理後、基板Wの被処理面上に残留するAPMを洗い流すために使用する。IPAは、表面張力がDIWよりも小さく、揮発性が高いため、DIWを置換して表面張力によるパターン倒壊を低減するために使用する。 The substrate W processed according to this embodiment is, for example, a semiconductor wafer. Hereinafter, the surface of the substrate W on which a pattern or the like is formed will be referred to as a surface to be processed. Alkaline cleaning liquid (APM), ultrapure water (DIW), and first volatile solvent (IPA) are used as the cleaning liquid, which is the processing liquid for the cleaning process. APM is a chemical mixture of ammonia water and hydrogen peroxide water, and is used to remove residual organic matter. DIW is used to wash away APM remaining on the processed surface of the substrate W after APM processing. IPA has lower surface tension and higher volatility than DIW, so it is used to replace DIW and reduce pattern collapse due to surface tension.

また、本実施形態においては、第2の揮発性溶剤を用いる。第2の揮発性溶剤は、第1の揮発性溶剤よりも、気化する際の表面張力が小さい溶剤である。また、第2の揮発性溶剤の気化の温度は、第1の揮発性溶剤よりも高い。このような第2の揮発性溶剤としては、PGMEA(プロピレングリコールモノエチルアセテート)を使用することができる。また、第2の揮発性溶剤は、撥水化剤を含むものを用いる。撥水化剤は、基板Wの被処理面の水酸基(-OH)を、官能基(例えば、-CH、C)へ置換して撥水化膜(Si-O-R(R:官能基))を形成可能な修飾剤である。例えば、撥水化剤としては、シランカップリング剤であるHMDS(ヘキサメチルジシラザン)を用いることができる。以下の説明での第2の揮発性溶剤の供給は、撥水化剤を含む第2の揮発性溶剤を供給する態様で行われる。 Moreover, in this embodiment, a second volatile solvent is used. The second volatile solvent is a solvent that has a smaller surface tension when vaporized than the first volatile solvent. Also, the vaporization temperature of the second volatile solvent is higher than that of the first volatile solvent. As such a second volatile solvent, PGMEA (propylene glycol monoethyl acetate) can be used. Also, the second volatile solvent used contains a water repellent agent. The water repellent agent replaces the hydroxyl groups (--OH) on the surface to be treated of the substrate W with functional groups (eg, --CH 3 , C 2 H 5 ) to form a water-repellent film (Si--O--R (R : is a modifier capable of forming a functional group)). For example, HMDS (hexamethyldisilazane), which is a silane coupling agent, can be used as the water repellent agent. The supply of the second volatile solvent in the following description is performed in a mode of supplying the second volatile solvent containing the water repellent agent.

PGMEAにHMDSを含めたものを用いる理由は、HMDSは水分と反応しやすいためである。つまり、HMDSは、空気中の水分と反応すると、基板W上での撥水効果を失う。このため、HMDSをPGMEAに混合することにより、空気中の水分と反応することを防いで、基板Wに供給することができる。なお、PGMEAが気化する際の表面張力は、IPAが気化する際の表面張力より小さい。例えば、IPAの沸点温度が82.5℃である時(気化する時)の表面張力の値は、15.7mN/mである。一方、PGMEAの沸点が145.8℃である時(気化する時)の表面張力の値は、11.72~15.47mN/mである。 The reason for using PGMEA containing HMDS is that HMDS readily reacts with moisture. That is, HMDS loses its water-repellent effect on the substrate W when it reacts with moisture in the air. Therefore, HMDS can be supplied to the substrate W while being prevented from reacting with moisture in the air by mixing PGMEA with HMDS. The surface tension when PGMEA is vaporized is smaller than the surface tension when IPA is vaporized. For example, when IPA has a boiling point temperature of 82.5° C. (at the time of vaporization), the surface tension value is 15.7 mN/m. On the other hand, when the boiling point of PGMEA is 145.8° C. (at the time of vaporization), the surface tension value is 11.72 to 15.47 mN/m.

[洗浄装置]
洗浄装置120は、図2に示すように、内部で洗浄処理を行う容器である洗浄室11、基板Wを支持する支持部12、支持部12を回転させる回転機構13、飛散する洗浄液Lを基板Wの周囲から受けるカップ14、洗浄液Lを供給する供給部15を有する。供給部15は、洗浄液Lを滴下するノズル15a、ノズル15aを移動させる移動機構15bが設けられている。
[Washing equipment]
As shown in FIG. 2, the cleaning apparatus 120 includes a cleaning chamber 11 which is a container in which cleaning processing is performed, a support section 12 that supports the substrate W, a rotation mechanism 13 that rotates the support section 12, and a cleaning liquid L that is scattered around the substrate. It has a cup 14 that receives from the periphery of W and a supply part 15 that supplies the cleaning liquid L. As shown in FIG. The supply unit 15 is provided with a nozzle 15a for dropping the cleaning liquid L and a moving mechanism 15b for moving the nozzle 15a.

支持部12に支持され、回転機構13により回転する基板Wの被処理面に、ノズル15aから洗浄液Lを供給することにより、洗浄処理が行われる。洗浄処理は、処理装置110でエッチング処理された基板Wの被処理面にAPMを供給してAPM洗浄を行い、APM洗浄後に、DIWによる純水リンス処理を行うことにより、基板Wの被処理面に残留していたAPMを純水により洗い流す。これにより、基板Wの被処理面はDIWの洗浄液Lにより液盛りされる。洗浄室11には、基板Wを搬出入する開口11aが設けられ、開口11aは扉11bによって開閉可能に構成されている。 The cleaning process is performed by supplying the cleaning liquid L from the nozzle 15 a to the surface to be processed of the substrate W which is supported by the support section 12 and rotated by the rotation mechanism 13 . In the cleaning process, APM is supplied to the surface of the substrate W etched by the processing apparatus 110 to perform APM cleaning. The APM remaining in is washed away with pure water. As a result, the surface to be processed of the substrate W is heaped up with the cleaning liquid L of the DIW. The cleaning chamber 11 is provided with an opening 11a for loading and unloading the substrate W, and the opening 11a can be opened and closed by a door 11b.

[搬送装置]
搬送装置200は、ハンドリング装置20を有する。ハンドリング装置20は、基板Wを把持するロボットハンド21と、移動機構22を有する。ロボットハンド21は、基板Wを把持する。移動機構22は、ロボットハンド21を移動させる。搬送装置200は、バッファユニット1dと各種装置との間、各種装置の間で、基板Wを搬送する。例えば、エッチング処理を終えた基板Wを処理装置110から搬出して、基板Wの被処理面上に洗浄液(DIW)Lの液膜が形成された状態で、洗浄装置120へ搬入する。また、移動機構22は、ロボットハンド21を移動させることにより、洗浄を終えた基板Wを洗浄装置120から搬出してし、基板Wの被処理面上に洗浄液(DIW)Lの液膜が形成された状態で、乾燥装置300へ搬入する。なお、基板Wの被処理面上に洗浄液(DIW)Lの液膜が形成された状態で搬送するのは、基板Wの搬送中に、基板Wの被処理面にパーティクルが付着するのを防止するためである。
[Conveyor]
The transport device 200 has a handling device 20 . The handling device 20 has a robot hand 21 that grips the substrate W and a moving mechanism 22 . The robot hand 21 grips the substrate W. As shown in FIG. The moving mechanism 22 moves the robot hand 21 . The transport device 200 transports the substrate W between the buffer unit 1d and various devices, and between various devices. For example, the substrate W that has undergone the etching process is unloaded from the processing apparatus 110 and loaded into the cleaning apparatus 120 in a state in which a liquid film of the cleaning liquid (DIW) L is formed on the surface of the substrate W to be processed. Further, the moving mechanism 22 moves the robot hand 21 to unload the cleaned substrate W from the cleaning apparatus 120, and a liquid film of the cleaning liquid (DIW) L is formed on the surface of the substrate W to be processed. In this state, it is carried into the drying device 300 . The reason why the substrate W is transported with the liquid film of the cleaning liquid (DIW) L formed on the surface to be processed of the substrate W is to prevent particles from adhering to the surface to be processed of the substrate W while the substrate W is being transported. It is for

[乾燥装置]
図2に示すように、乾燥装置300は、乾燥室31、支持部32、駆動機構33、第1の揮発性溶剤供給部34、第2の揮発性溶剤供給部35、加熱部36、カップ37、測定部38を有する。乾燥室31は、内部において基板Wを乾燥処理するためのチャンバ1aである。乾燥室31は、例えば直方体や立方体などの箱形状である。乾燥室31の内壁は、防塵性を高めるために、シリカによりコーティングされている。乾燥室31には、基板Wを搬出入させるための開口31aが設けられている。開口31aは、扉31bによって開閉可能に設けられている。このような乾燥室31には、後述する第1の揮発性溶剤供給部34、第2の揮発性溶剤供給部35、加熱部36が収容されている。
[Drying device]
As shown in FIG. 2, the drying device 300 includes a drying chamber 31, a support section 32, a driving mechanism 33, a first volatile solvent supply section 34, a second volatile solvent supply section 35, a heating section 36, a cup 37 , a measuring unit 38 . The drying chamber 31 is a chamber 1a for drying the substrate W inside. The drying chamber 31 has, for example, a box shape such as a rectangular parallelepiped or a cube. The inner wall of the drying chamber 31 is coated with silica to improve dust resistance. The drying chamber 31 is provided with an opening 31a through which the substrate W is carried in and out. The opening 31a is provided so as to be opened and closed by a door 31b. The drying chamber 31 accommodates a first volatile solvent supply unit 34, a second volatile solvent supply unit 35, and a heating unit 36, which will be described later.

また、乾燥室31には、導入口31c、排気口31dが設けられている。導入口31cには、配管、吸気弁及び清浄なガス(N等)を供給する給気装置を含む給気部31eが接続されている。排気口31dには、配管、排気弁及びガスを排気する排気装置を含む排気部31fが接続されている。導入口31cから清浄なガスを乾燥室31内に供給することで、乾燥室31内を正常な雰囲気にすることができる。また、導入口31cからガスを乾燥室31内に供給し、排気口31dから乾燥室31内のガスを排出する構成を作ることで、乾燥室31内の気体の流れを作るようにしている。これにより、基板Wを加熱する際に発生する処理液の蒸気が乾燥室31内に充満することなく、乾燥室31から排出できる構成になっている。 The drying chamber 31 is also provided with an inlet 31c and an exhaust port 31d. The inlet 31c is connected to an air supply unit 31e including a pipe, an intake valve, and an air supply device for supplying clean gas (such as N2 ). An exhaust part 31f including a pipe, an exhaust valve, and an exhaust device for exhausting gas is connected to the exhaust port 31d. By supplying clean gas into the drying chamber 31 from the inlet 31c, the inside of the drying chamber 31 can be made into a normal atmosphere. In addition, a gas flow in the drying chamber 31 is created by supplying the gas into the drying chamber 31 from the inlet 31c and discharging the gas in the drying chamber 31 from the exhaust port 31d. As a result, the vapor of the processing liquid generated when the substrate W is heated can be discharged from the drying chamber 31 without filling the inside of the drying chamber 31 .

支持部32は、基板Wを支持する。支持部32は、回転テーブル32a、複数の保持部材32b、回転軸32cを有する。回転テーブル32aは、基板Wよりも大きな径の円筒形状であり、上面が平坦な円盤となっている。複数の保持部材32bは、基板Wの外周に沿う位置に等間隔で配置され、回転テーブル32aの上面との間に間隔を空けて、基板Wを水平状態に保持する。複数の保持部材32bは、図示しない開閉機構によって、基板Wの縁部に接する閉位置と、基板Wの縁部から離れる開位置との間を移動可能に設けられている。回転軸32cは、回転テーブル32aを下方から支持し、回転の中心となる鉛直方向の軸である。 The support portion 32 supports the substrate W. As shown in FIG. The support portion 32 has a rotary table 32a, a plurality of holding members 32b, and a rotating shaft 32c. The rotary table 32a has a cylindrical shape with a diameter larger than that of the substrate W, and is a disk with a flat upper surface. The plurality of holding members 32b are arranged at equal intervals along the outer circumference of the substrate W, and hold the substrate W in a horizontal state with a gap between them and the upper surface of the turntable 32a. The plurality of holding members 32b are provided movably between a closed position in contact with the edge of the substrate W and an open position away from the edge of the substrate W by an opening/closing mechanism (not shown). The rotary shaft 32c is a vertical shaft that supports the rotary table 32a from below and serves as the center of rotation.

駆動機構33は、支持部32に支持された基板Wを回転させる機構である。駆動機構33は、モータ等の駆動源を有し、回転軸32cを介して支持部32を回転させる。 The drive mechanism 33 is a mechanism that rotates the substrate W supported by the support portion 32 . The drive mechanism 33 has a drive source such as a motor, and rotates the support portion 32 via a rotating shaft 32c.

第1の揮発性溶剤供給部34は、乾燥室31に搬入され、支持部32に支持された基板W上に、第1の揮発性溶剤Vを供給する。第1の揮発性溶剤供給部34は、ノズル34a、揺動アーム34b、揺動機構34cを有する。ノズル34aは、基板Wの被処理面の中心付近に向けて第1の揮発性溶剤Vを供給する。ノズル34aには、乾燥室31外の貯留部から配管(いずれも不図示)などを介して第1の揮発性溶剤VであるIPAが供給される。 The first volatile solvent supply unit 34 supplies the first volatile solvent V onto the substrate W carried into the drying chamber 31 and supported by the support unit 32 . The first volatile solvent supply section 34 has a nozzle 34a, a swing arm 34b, and a swing mechanism 34c. The nozzle 34a supplies the first volatile solvent V toward the vicinity of the center of the surface of the substrate W to be processed. IPA, which is the first volatile solvent V, is supplied to the nozzle 34a from a reservoir outside the drying chamber 31 through a pipe (none of which is shown) or the like.

洗浄装置120における洗浄処理において、APMによるアルカリ洗浄後のDIWによる純水リンス処理で、最終的に基板Wの被処理面上はDIWの洗浄液Lにより液盛されている。このように液盛された状態で、洗浄装置120から乾燥装置300に搬入された基板Wに対して、IPAが供給されることにより、DIWがIPAに置換される。 In the cleaning process in the cleaning apparatus 120, the surface to be processed of the substrate W is finally filled with the cleaning liquid L of DIW by the pure water rinsing process with DIW after alkaline cleaning with APM. IPA is supplied to the substrate W carried into the drying device 300 from the cleaning device 120 in such a liquid-filled state, thereby replacing the DIW with the IPA.

揺動アーム34bは、先端にノズル34aが設けられ、ノズル34aを、支持部32上の基板Wの被処理面の中心付近に対向する供給位置と、その供給位置から退避して基板Wの搬入や搬出を可能とする退避位置とに移動させる。揺動機構34cは、揺動アーム34bを揺動させる機構である。 The swing arm 34b is provided with a nozzle 34a at its tip. or a retracted position that enables unloading. The swing mechanism 34c is a mechanism for swinging the swing arm 34b.

第2の揮発性溶剤供給部35は、基板W上のDIWを置換したIPAに、第2の揮発性溶剤HであるPGMEA(HMDSを含む溶剤)を供給する(図4(A)参照)。第2の揮発性溶剤供給部35は、ノズル35a、揺動アーム35b、揺動機構35cを有する。ノズル35aは、基板Wの被処理面の中心付近に向けて第2の揮発性溶剤Hを供給する。ノズル35aには、乾燥室31外の貯留部から配管(いずれも不図示)などを介してPGMEAが供給される。 The second volatile solvent supply unit 35 supplies PGMEA (solvent containing HMDS) as the second volatile solvent H to the IPA that replaced the DIW on the substrate W (see FIG. 4A). The second volatile solvent supply section 35 has a nozzle 35a, a swing arm 35b, and a swing mechanism 35c. The nozzle 35a supplies the second volatile solvent H toward the vicinity of the center of the surface of the substrate W to be processed. PGMEA is supplied to the nozzle 35a from a reservoir outside the drying chamber 31 through a pipe (none of which is shown) or the like.

撥水化剤を含む第2の揮発性溶剤Hを供給することにより、基板Wの被処理面に撥水化膜が形成されるので、基板Wの被処理面を親水性のシラノール基から撥水性のメチル基に変えて、基板Wの被処理面上の界面エネルギーを下げることにより、第1の揮発性溶剤Vを浮かび上がらせ、基板Wの被処理面上の液体の除去を促進できる。なお、ここでいう撥水性とは、液体を弾く性質、つまり撥液性をいい、水を弾く性質には限定されない。 By supplying the second volatile solvent H containing a water-repellent agent, a water-repellent film is formed on the surface of the substrate W to be processed, so that the surface of the substrate W to be processed is repelled from hydrophilic silanol groups. By lowering the interfacial energy on the surface to be processed of the substrate W instead of water-based methyl groups, the first volatile solvent V floats and the removal of the liquid on the surface to be processed of the substrate W can be facilitated. The term "water repellency" as used herein refers to the property of repelling liquid, that is, liquid repellency, and is not limited to the property of repelling water.

揺動アーム35bは、先端にノズル35aが設けられ、ノズル35aを、支持部32上の基板Wの被処理面の中心付近に対向する供給位置と、その供給位置から退避して基板Wの搬入や搬出を可能とする退避位置とに移動させる。揺動機構35cは、揺動アーム35bを揺動させる機構である。 The swing arm 35b is provided with a nozzle 35a at its tip. or a retracted position that enables unloading. The swing mechanism 35c is a mechanism for swinging the swing arm 35b.

加熱部36は、基板Wを加熱する装置である。加熱部36は、乾燥室31内の上部に設けられている。加熱部36は、ハロゲンランプ、赤外線ランプ等のランプ36aを有する。なお、ランプ36aは、紫外光、可視光、赤外光を照射可能なランプである。本実施形態のランプ36aは直管形であり、互いに水平状態で平行に配置された複数本のランプ36aが、2段に重ねて配置され、1段目と2段目のランプ36aの方向は直交しているため、全体として格子状となっている。これにより、加熱が均一となるように構成されている。 The heating unit 36 is a device that heats the substrate W. As shown in FIG. The heating unit 36 is provided in the upper part of the drying chamber 31 . The heating unit 36 has a lamp 36a such as a halogen lamp or an infrared lamp. The lamp 36a is a lamp capable of emitting ultraviolet light, visible light, and infrared light. The lamps 36a of this embodiment are of a straight tube type, and a plurality of lamps 36a arranged horizontally and parallel to each other are arranged in two tiers. Since they are orthogonal to each other, they form a grid as a whole. Thereby, the heating is made uniform.

なお、加熱部36は、基板Wの被処理面上の液体自体、つまり第1の揮発性溶剤V及び第2の揮発性溶剤Hよりも、基板W自体が加熱され易い波長の電磁波(赤外線)を用いることにより、基板Wの熱による気層の発生を促進できる。加熱温度としては、例えば、300℃以上とすることが好ましい。 The heating unit 36 uses an electromagnetic wave (infrared radiation) having a wavelength that heats the substrate W itself more easily than the liquid itself on the surface to be processed of the substrate W, that is, the first volatile solvent V and the second volatile solvent H. can promote the generation of an air layer due to the heat of the substrate W. The heating temperature is preferably 300° C. or higher, for example.

なお、乾燥室31には、窓部36bが設けられている。窓部36bは、加熱部36からの電磁波を透過する部材である。窓部36bとしては、たとえば、石英等の板状体を用いることができる。窓部36bは、乾燥室31内の加熱部36の直下に設けられ、加熱部36と支持部32との間を仕切ることにより、ランプ36aの点灯の繰り返しによって、ランプ36aのコネクタ部の部材の伸縮が起こることで発生するパーティクルが、上部から基板Wへ付着して金属汚染が発生することを防止している。 The drying chamber 31 is provided with a window portion 36b. The window portion 36b is a member that allows electromagnetic waves from the heating portion 36 to pass therethrough. As the window portion 36b, for example, a plate-like body such as quartz can be used. The window portion 36b is provided directly below the heating portion 36 in the drying chamber 31, and by partitioning the heating portion 36 and the support portion 32, by repeating lighting of the lamp 36a, the member of the connector portion of the lamp 36a is removed. This prevents particles generated by expansion and contraction from adhering to the substrate W from above and causing metal contamination.

カップ37は、支持部32を周囲から囲むように円筒形状に形成されている(図2参照)。カップ37の周壁の上部は、径方向の内側に向かって傾斜し、支持部32上の基板Wが露出するように開口している。カップ37は、回転する基板Wから飛散した洗浄液Lを受けて、下方に流す。カップ37の底面には、流れ落ちる洗浄液Lを排出するための排出口(不図示)が形成されている。なお、カップ37は、駆動機構33に接続され、支持部32とともに昇降可能に設けられている。 The cup 37 is formed in a cylindrical shape so as to surround the support portion 32 (see FIG. 2). The upper portion of the peripheral wall of the cup 37 is slanted radially inward and is open so that the substrate W on the support portion 32 is exposed. The cup 37 receives the cleaning liquid L scattered from the rotating substrate W and flows it downward. The bottom surface of the cup 37 is formed with a discharge port (not shown) for discharging the washing liquid L that flows down. The cup 37 is connected to the drive mechanism 33 and provided so as to move up and down together with the support portion 32 .

測定部38は、乾燥室31に搬入され、支持部32に支持された基板W上の液体の膜厚を測定する。測定部38は、検出部38a、揺動アーム38b、揺動機構38cを有する。検出部38aとしては、例えば、レーザ変位計やカメラなどを用いる。揺動アーム38bは、先端に検出部38aが設けられ、検出部38aを、支持部32上の基板Wの被処理面の中心と外周縁との間の中央付近に対向させる測定位置と、その測定位置から退避して基板Wの搬入や搬出を可能とする待機位置とに移動させる。揺動機構38cは、揺動アーム38bを揺動させる機構である。 The measuring unit 38 measures the film thickness of the liquid on the substrate W which is carried into the drying chamber 31 and supported by the supporting unit 32 . The measurement unit 38 has a detection unit 38a, a swing arm 38b, and a swing mechanism 38c. For example, a laser displacement meter, a camera, or the like is used as the detection unit 38a. The swing arm 38b is provided with a detection portion 38a at its tip. It is moved to a standby position where it is evacuated from the measurement position and the substrate W can be carried in and out. The swing mechanism 38c is a mechanism for swinging the swing arm 38b.

測定部38による膜厚測定法としては、例えば、光干渉原理を用いることができる。なお、別の例として、支持部32内に重量計を用いることが可能である。この重量計を用いる場合には、基板W上の液膜の重量(液膜の重量=液膜を含む基板の重さ-基板の重さ)を理論的あるいは実験的に液膜の厚さに換算する。 As a film thickness measurement method by the measurement unit 38, for example, the optical interference principle can be used. As another example, it is possible to use a weight scale within the support portion 32 . When using this weighing scale, the weight of the liquid film on the substrate W (weight of the liquid film = weight of the substrate including the liquid film - weight of the substrate) is theoretically or experimentally adjusted to the thickness of the liquid film. Convert.

[制御装置]
制御装置400は、基板処理装置1の各部を制御するコンピュータである。制御装置400は、プログラムを実行するプロセッサと、プログラムや動作条件などの各種情報を記憶するメモリ、各要素を駆動する駆動回路を有する。なお、制御装置400は、情報を入力する入力装置、情報を表示する表示装置を有している。
[Control device]
The control device 400 is a computer that controls each part of the substrate processing apparatus 1 . The control device 400 has a processor that executes programs, a memory that stores various information such as programs and operating conditions, and a drive circuit that drives each element. The control device 400 has an input device for inputting information and a display device for displaying information.

制御装置400は、処理装置110、洗浄装置120、搬送装置200、乾燥装置300を制御する。例えば、制御装置400は、支持部32に支持された基板Wを回転させながら、第1の揮発性溶剤供給部34からの第1の揮発性溶剤Vの供給により液膜を第1の揮発性溶剤Vへ置換させ、第2の揮発性溶剤供給部35からの第2の揮発性溶剤Hの供給により基板Wの被処理面上に供給された第1の揮発性溶剤Vを、第2の揮発性溶剤Hへ置換させた後、加熱部36による基板Wの加熱により、第2の揮発性溶剤HであるPGMEAを気化させた後に、撥水化膜を基板Wの被処理面から離脱させる。これにより、第2の揮発性溶剤Hの液膜を基板Wの回転による遠心力により排出させる。例えば、PGMEAの沸点は、140~150℃であり、撥水化剤であるHMDSの沸点は約300℃であるため、加熱による瞬時の温度上昇の過程で、PGMEAが先に気化した後、撥水化膜の化学結合が熱により断ち切られて除去される。なお、制御装置400は、測定部38による測定結果の膜厚が所定のしきい値の範囲内にあると判定した場合に、加熱部36による加熱を開始させる。 The control device 400 controls the processing device 110 , the cleaning device 120 , the conveying device 200 and the drying device 300 . For example, while rotating the substrate W supported by the support section 32, the control device 400 supplies the first volatile solvent V from the first volatile solvent supply section 34 to convert the liquid film into the first volatile solvent. The first volatile solvent V supplied onto the surface to be processed of the substrate W by the supply of the second volatile solvent H from the second volatile solvent supply unit 35 is replaced with the second solvent V. After the substitution with the volatile solvent H, the substrate W is heated by the heating unit 36 to evaporate the PGMEA, which is the second volatile solvent H, and then the water-repellent film is separated from the surface of the substrate W to be processed. . As a result, the liquid film of the second volatile solvent H is discharged by centrifugal force due to the rotation of the substrate W. As shown in FIG. For example, the boiling point of PGMEA is 140 to 150°C, and the boiling point of HMDS, which is a water repellent agent, is about 300°C. Chemical bonds in the hydrated film are broken and removed by heat. Note that the controller 400 causes the heating unit 36 to start heating when it determines that the film thickness measured by the measuring unit 38 is within the range of the predetermined threshold value.

このような制御装置400は、機構制御部41と、膜厚解析部42と、加熱制御部43を有する。機構制御部41は、各部の機構を制御する。例えば、機構制御部41は、駆動機構33を制御することにより、支持部32の回転速度、回転開始及び回転停止のタイミングを制御する。また、ノズル34aの揺動及び第1の揮発性溶剤Vの吐出、ノズル35aの揺動及び第2の揮発性溶剤Hの吐出、検出部38aの揺動及び測定などの動作を制御する。 Such a control device 400 has a mechanism control section 41 , a film thickness analysis section 42 and a heating control section 43 . The mechanism control section 41 controls the mechanism of each section. For example, the mechanism control section 41 controls the rotation speed of the support section 32 and the timing of rotation start and rotation stop by controlling the drive mechanism 33 . It also controls the swinging of the nozzle 34a and the ejection of the first volatile solvent V, the swinging of the nozzle 35a and the ejection of the second volatile solvent H, the swinging of the detector 38a and the measurement.

膜厚解析部42は、測定部38による測定結果、つまり測定部38により測定された第1の揮発性溶剤V及び第2の揮発性溶剤Hの液膜の厚さを解析する。膜厚解析部42は、測定部38により測定された液膜の厚さ(液膜厚値)が、所定のしきい値の範囲内にあるか否かを判定する。そして、膜厚解析部42は、測定された液膜の厚さが所定のしきい値の範囲内にあると判定した場合、液膜の厚さが適切であるとして、加熱制御部43は、加熱部36に加熱を命令する信号を送信する。 The film thickness analysis unit 42 analyzes the measurement result by the measurement unit 38 , that is, the thickness of the liquid films of the first volatile solvent V and the second volatile solvent H measured by the measurement unit 38 . The film thickness analysis unit 42 determines whether the thickness of the liquid film (liquid film thickness value) measured by the measurement unit 38 is within a predetermined threshold range. Then, when the film thickness analysis unit 42 determines that the measured thickness of the liquid film is within the range of the predetermined threshold value, the thickness of the liquid film is determined to be appropriate, and the heating control unit 43 A signal for instructing heating is transmitted to the heating unit 36 .

なお、HMDS(撥水化剤)を含むPGMEA(第2の揮発性溶剤)を供給した場合の適切な膜厚は、例えば100μm以下である。この膜厚は、加熱部36の加熱による基板Wからの蒸発を遅延させて、ライデンフロスト現象による乾燥処理を行う上で、良好に乾燥できる液膜厚である。但し、これらの数値は例示であり、実際には、予め実験等で適切な液膜厚を求めることができる。また、基板Wの回転速度は、例えば、200~300rpm程度であり、液膜調整されても、このような回転速度の範囲では、液膜厚が所定の厚さに維持できる。 An appropriate film thickness when supplying PGMEA (second volatile solvent) containing HMDS (water repellent agent) is, for example, 100 μm or less. This film thickness delays the evaporation from the substrate W due to the heating of the heating unit 36, and is the film thickness of the liquid that can be satisfactorily dried when the drying process by the Leidenfrost phenomenon is performed. However, these numerical values are examples, and in practice, an appropriate liquid film thickness can be obtained in advance by experiments or the like. Further, the rotation speed of the substrate W is, for example, about 200 to 300 rpm, and even if the liquid film is adjusted, the liquid film thickness can be maintained at a predetermined thickness within such a rotation speed range.

[動作]
以上のような本実施形態の基板処理装置1の動作を、上記の図1及び図2に加えて、図3~図5の説明図、図6のフローチャート、図7及び図8の説明図を参照して説明する。なお、以下のような手順により基板Wを処理することにより基板を製造する基板製造方法、基板Wを乾燥させる基板乾燥方法も、本実施形態の一態様である。
[motion]
In addition to FIGS. 1 and 2, the operation of the substrate processing apparatus 1 of the present embodiment as described above is described with reference to the explanatory diagrams of FIGS. 3 to 5, the flow chart of FIG. will be described with reference to A substrate manufacturing method for manufacturing a substrate W by processing the substrate W according to the following procedure and a substrate drying method for drying the substrate W are also aspects of the present embodiment.

まず、図2に示すように、処理装置110におけるエッチング処理後の基板Wは、搬送装置200により洗浄装置120に搬入される。洗浄装置120においては、基板Wを保持した支持部12が回転しながら、供給部15が基板Wの被処理面の回転中心にAPMを供給してアルカリによるリンス処理を行った後、DIWを供給することによる純水リンス処理を行う。搬送装置200は、洗浄後、DIWである洗浄液Lによって液盛された基板Wを、洗浄装置120から搬出し、乾燥装置300に搬入する。 First, as shown in FIG. 2, the substrate W after etching processing in the processing apparatus 110 is carried into the cleaning apparatus 120 by the transfer apparatus 200 . In the cleaning apparatus 120, while the supporting unit 12 holding the substrate W rotates, the supplying unit 15 supplies APM to the center of rotation of the surface to be processed of the substrate W to perform an alkali rinse treatment, and then supplies DIW. Perform pure water rinsing by After cleaning, the transport device 200 unloads the substrate W, which is filled with the cleaning liquid L, which is DIW, from the cleaning device 120 and carries it into the drying device 300 .

図3(A)に示すように、被処理面に洗浄液Lの液膜(DIW)が形成された状態で、乾燥装置300の乾燥室31の開口31aから搬入された基板Wを、支持部32の保持部材32bが保持する(ステップS01)。図3(B)に示すように、駆動機構33が支持部32とともに基板Wを回転させながら(ステップS02)、第1の揮発性溶剤供給部34が、基板Wの被処理面の回転中心に第1の揮発性溶剤VであるIPAを供給する(ステップS03)。これにより、基板Wの回転による遠心力によって、IPAが基板Wの被処理面の全域に行き渡り、基板Wの被処理面上に液盛されたDIWがIPAに置換されるアルコールリンス処理が行われる。なお、ここでは、DIWよりも表面張力が低いIPAに置換されるため、基板Wの被処理面上に形成されるパターンの間に働く、表面張力が低減される。 As shown in FIG. 3(A), the substrate W loaded from the opening 31a of the drying chamber 31 of the drying device 300 in a state in which a liquid film (DIW) of the cleaning liquid L is formed on the surface to be processed is held by the supporting portion 32. is held by the holding member 32b (step S01). As shown in FIG. 3B, while the drive mechanism 33 rotates the substrate W together with the support portion 32 (step S02), the first volatile solvent supply portion 34 is moved to the center of rotation of the surface of the substrate W to be processed. IPA, which is the first volatile solvent V, is supplied (step S03). As a result, the centrifugal force generated by the rotation of the substrate W spreads the IPA over the entire surface of the substrate W to be processed, and alcohol rinse processing is performed in which DIW deposited on the surface of the substrate W to be processed is replaced with IPA. . Here, since DIW is replaced with IPA, which has a lower surface tension than DIW, the surface tension acting between patterns formed on the surface to be processed of the substrate W is reduced.

そして、図4(A)に示すように、駆動機構33が支持部32とともに基板Wを回転させながら、第2の揮発性溶剤供給部35が、基板Wの被処理面の回転中心に、第2の揮発性溶剤HであるPGMEAを供給する(ステップS04)。これにより、基板Wの回転による遠心力によって、PGMEAが基板Wの被処理面の全域に行き渡るとともに、HMDSが、基板Wの被処理面に結合して撥水化膜が形成される。つまり、基板Wの被処理面上に存在する第1の揮発性溶剤が、第2の揮発性溶剤のPGMEAに置換され、被処理面の水酸基が官能基に置換して撥水化膜が形成されることになる。第2の揮発性溶剤は、第1の揮発性溶剤よりも基板Wのパターン間に働く表面張力が小さい。このため、パターン間に働く表面張力が低減される。これとともに、測定部38の検出部38aが、基板W上の膜厚を測定する(ステップS06)。 Then, as shown in FIG. 4A, while the drive mechanism 33 rotates the substrate W together with the support portion 32, the second volatile solvent supply portion 35 is moved to the center of rotation of the surface of the substrate W to be processed. PGMEA, which is the volatile solvent H of No. 2, is supplied (step S04). As a result, the centrifugal force generated by the rotation of the substrate W spreads the PGMEA over the entire processed surface of the substrate W, and the HMDS bonds to the processed surface of the substrate W to form a water-repellent film. That is, the first volatile solvent present on the surface to be processed of the substrate W is replaced with the second volatile solvent PGMEA, and the hydroxyl groups on the surface to be processed are replaced with functional groups to form a water-repellent film. will be The second volatile solvent has a smaller surface tension acting between patterns on the substrate W than the first volatile solvent. Therefore, the surface tension acting between the patterns is reduced. Along with this, the detection unit 38a of the measurement unit 38 measures the film thickness on the substrate W (step S06).

測定部38により測定される膜厚が、所定のしきい値の範囲内で適切となった場合には(ステップS07のYES)、図5に示すように、基板Wを回転させながら、加熱部36のランプ36aが所定時間(数秒から十数秒以内の範囲内で)点灯することにより、基板Wをライデンフロスト現象が生じる温度(PGMEAの沸点以上)まで急速に加熱する(ステップS08)。これにより、第2の揮発性溶剤Hの液膜が、瞬時に除去される乾燥処理が行われる。 When the film thickness measured by the measurement unit 38 is appropriate within the range of the predetermined threshold value (YES in step S07), as shown in FIG. By turning on the lamp 36a of 36 for a predetermined time (within a range of several seconds to ten and several seconds), the substrate W is rapidly heated to a temperature at which the Leidenfrost phenomenon occurs (above the boiling point of PGMEA) (step S08). As a result, a drying process is performed in which the liquid film of the second volatile solvent H is instantly removed.

ここで言う乾燥処理は、単なる揮発によるものではなく、急速加熱の過程で生じるライデンフロスト現象及び撥水化膜の離脱と、基板Wの回転による遠心力を利用するものである。つまり、加熱により、基板Wの被処理面と気化しきれないPGMEAの液膜との界面に発生する気層によるライデンフロスト現象によって、液膜が浮上して液玉となる(液玉化)。その後、基板W上の撥水化膜の結合状態が解除されて除去される。化学結合の解除のメカニズムは以下の通りである。まず、高温に加熱することにより、官能基(-CHx)が熱分解によりSiとの結合が断ち切られ、基板W上の周囲にある酸素が、基板W上のSi及び官能基と結びつく。これにより、基板W上のSiは酸化して熱酸化膜が成長する。つまり、基板Wの被処理面には酸化膜が形成されるが、この酸化膜が残存することは特に問題はない。また、酸化した官能基は、HOやCOなどに変化するが、高温下にあるため、HOは蒸発し、COはガスとして排出される。なお、加熱時には、排気部31fにおける排気弁を閉じることにより、気層の発生前の液膜の気化を防ぎ、過加熱状態を発生させてもよい。 The drying process referred to here is not based on mere volatilization, but utilizes the Leidenfrost phenomenon and detachment of the water-repellent film that occur in the process of rapid heating, and the centrifugal force due to the rotation of the substrate W. FIG. That is, due to the Leidenfrost phenomenon caused by the gas layer generated at the interface between the surface of the substrate W to be processed and the liquid film of PGMEA that has not been vaporized due to heating, the liquid film floats and becomes liquid droplets (liquid droplet formation). Thereafter, the bonded state of the water-repellent film on the substrate W is released and removed. The mechanism of releasing the chemical bond is as follows. First, by heating to a high temperature, the functional group (-CHx) is thermally decomposed to break the bond with Si, and the surrounding oxygen on the substrate W bonds with the Si on the substrate W and the functional group. As a result, Si on the substrate W is oxidized to grow a thermal oxide film. In other words, although an oxide film is formed on the surface of the substrate W to be processed, there is no particular problem if this oxide film remains. In addition, the oxidized functional groups change to H 2 O, CO 2 and the like, but because of the high temperature, H 2 O evaporates and CO 2 is discharged as gas. During heating, the exhaust valve in the exhaust portion 31f may be closed to prevent vaporization of the liquid film before the formation of the gas layer, thereby generating an overheated state.

この現象を模式的に示すと、図7(A)に示すように、基板Wの被処理面のパターンP上に、撥水化膜Rを介して存在しているHMDSを含むPGMEAの液膜Fは、図7(B)に示すように、ランプ36aの点灯により基板Wだけが瞬時に加熱されることにより基板Wの撥水化膜とPGMEAとの界面が他の部分のPGMEAよりも早く気化を始めるため、液膜Fが気化したガスの層、すなわち気層Gが生成される。 To schematically show this phenomenon, as shown in FIG. 7A, a liquid film of PGMEA containing HMDS exists on a pattern P on the surface to be processed of the substrate W via a water-repellent film R. In F, as shown in FIG. 7B, only the substrate W is instantaneously heated by lighting the lamp 36a, so that the interface between the water-repellent film of the substrate W and the PGMEA is heated faster than the PGMEA in other portions. Since the vaporization starts, a layer of gas in which the liquid film F is vaporized, that is, a gas layer G is generated.

このため、図7(C)に示すように、パターンP上の液膜Fは気層Gによって瞬時にパターンPから浮き上がり、図7(D)に示すように、直ちに液玉化し(ライデンフロスト現象)、撥水化膜Rは基板Wの被処理面のSiと-CHxの結合が断ち切られて除去される。このように、液膜Fが液玉化してから、撥水化膜Rが基板Wから除去されるが、ランプ36aによって、瞬間的に(数秒で)撥水化膜Rが気化する300℃を達成できるので、液玉化と撥水化膜Rの除去は、ほぼ同時に起こるものとして考えることができる。図中、黒塗りの矢印で示すように、液膜Fには回転による遠心力がかかっており、生成された各液玉及は、遠心力によって基板W上から飛ばされるので、図7(E)に示すように、基板Wの被処理面は乾燥する。なお、上記のように、Siと結合が切れた官能基が酸素と結びつくことによって、HOやCOとなり、撥水化剤であるシランカップリング剤が蒸発するので、乾燥室31内の雰囲気は、酸素を含んでいることが好ましい。 Therefore, as shown in FIG. 7(C), the liquid film F on the pattern P instantly rises from the pattern P due to the air layer G, and as shown in FIG. ), the water-repellent film R is removed by breaking the bond between Si and —CHx on the surface of the substrate W to be processed. In this way, the water-repellent film R is removed from the substrate W after the liquid film F turns into a liquid droplet. Since it can be achieved, it can be considered that the formation of liquid droplets and the removal of the water-repellent film R occur almost simultaneously. As indicated by the black arrows in the figure, centrifugal force is applied to the liquid film F due to rotation, and the generated liquid droplets are flung off from the substrate W by the centrifugal force. ), the surface of the substrate W to be processed is dried. As described above, the functional groups that have broken bonds with Si combine with oxygen to form H 2 O and CO 2 , and the silane coupling agent, which is a water repellent agent, evaporates. The atmosphere preferably contains oxygen.

図8に示すように、基板W上のパターンP間に液膜Fが残った状態だと、液膜Fが残った部分のパターンPが液膜Fの表面張力によって、パターンPを引き寄せることになり、パターンPを倒壊させる。本実施形態では、図7(A)に示すように、基板Wの全体において、パターンPの表面上に撥水化膜Rが存在することにより、パターンP間に液膜Fが形成され難くなり、パターンP間に液膜Fが存在し難い状態となる。このように、パターンP同士を引き付ける液膜Fが無いため、パターンPの倒壊を防ぐことができる。同時に撥水化膜Rを基板Wから離脱させて、基板Wの被処理面には不要である撥水化膜Rを除去できる。このため、パターンPの倒壊を低減して、基板Wを乾燥させることができる。 As shown in FIG. 8, when the liquid film F remains between the patterns P on the substrate W, the pattern P in the portion where the liquid film F remains attracts the pattern P due to the surface tension of the liquid film F. and the pattern P is destroyed. In the present embodiment, as shown in FIG. 7A, the presence of the water-repellent film R on the surface of the pattern P over the entire substrate W makes it difficult for the liquid film F to form between the patterns P. , the liquid film F between the patterns P becomes difficult to exist. In this way, since there is no liquid film F that attracts the patterns P to each other, the patterns P can be prevented from collapsing. At the same time, the water-repellent film R is separated from the substrate W, and the unnecessary water-repellent film R on the surface of the substrate W to be processed can be removed. Therefore, the substrate W can be dried while reducing the collapse of the pattern P.

その後、加熱部36による加熱を停止して、基板Wを回転させながら放置することにより冷却し(ステップS09)、駆動機構33が支持部32とともに基板Wの回転を停止した後(ステップS10)、搬送装置200が基板Wを開口31aから搬出する(ステップS11)。 After that, the heating by the heating unit 36 is stopped, and the substrate W is left to cool while being rotated (step S09). The transport device 200 unloads the substrate W from the opening 31a (step S11).

[効果]
(1)以上のような本実施形態の乾燥装置(基板乾燥装置)300は、基板Wを加熱する加熱部36と、基板Wの被処理面上に第1の揮発性溶剤Vを供給する第1の揮発性溶剤供給部34と、基板Wの被処理面上に、撥水化膜を形成する撥水化剤を含み、気化する際の表面張力が、第1の揮発性溶剤Vよりも小さい第2の揮発性溶剤Hを供給する第2の揮発性溶剤供給部35と、加熱部36、第1の揮発性溶剤供給部34及び第2の揮発性溶剤供給部35が収容され、被処理面上に処理液による液膜が形成された状態の基板Wが搬入される乾燥室31と、乾燥室31に搬入された基板Wを受け取る支持部32と、支持部32に支持された基板Wを回転させる駆動機構33と、第1の揮発性溶剤供給部34から第1の揮発性溶剤Vを供給させることにより、基板Wの被処理面上に形成された処理液による液膜を第1の揮発性溶剤Vへ置換させ、第2の揮発性溶剤供給部35から第2の揮発性溶剤Hを供給させることにより、基板Wの被処理面上に形成された第1の揮発性溶剤Vを第2の揮発性溶剤Hへ置換させるとともに、被処理面に撥水化膜を形成させ、加熱部36に基板Wを加熱させることにより、撥水化剤を含む第2の揮発性溶剤Hの液膜と基板Wとの間に気層を生じさせることによって、第2の揮発性溶剤Hの液膜を基板Wの回転による遠心力により排出させる制御装置400と、を有する。
[effect]
(1) The drying apparatus (substrate drying apparatus) 300 of the present embodiment as described above includes the heating unit 36 that heats the substrate W and the first heating unit that supplies the first volatile solvent V onto the surface of the substrate W to be processed. 1 volatile solvent supply unit 34 and a water repellent agent that forms a water repellent film on the surface to be processed of the substrate W, the surface tension of which is higher than that of the first volatile solvent V when vaporized A second volatile solvent supply unit 35 for supplying a small second volatile solvent H, a heating unit 36, a first volatile solvent supply unit 34 and a second volatile solvent supply unit 35 are accommodated, A drying chamber 31 into which a substrate W having a liquid film of the processing liquid formed on the processing surface is loaded, a support section 32 for receiving the substrate W loaded into the drying chamber 31, and a substrate supported by the support section 32. By supplying the first volatile solvent V from the drive mechanism 33 that rotates the substrate W and the first volatile solvent supply unit 34, the liquid film of the processing liquid formed on the surface of the substrate W to be processed is formed into the first liquid film. 1 volatile solvent V, and supply the second volatile solvent H from the second volatile solvent supply unit 35 to form the first volatile solvent on the surface to be processed of the substrate W. V is replaced with a second volatile solvent H, a water-repellent film is formed on the surface to be treated, and the substrate W is heated by the heating unit 36 to remove the second volatile solvent containing the water-repellent agent. a control device 400 for discharging the liquid film of the second volatile solvent H by the centrifugal force caused by the rotation of the substrate W by forming an air layer between the H liquid film and the substrate W;

本実施形態の基板処理装置1は、基板Wを回転させながら第1の処理液を供給することにより処理する処理装置110と、処理装置110により処理済の基板Wを回転させながら第2の処理液を供給することにより洗浄する洗浄装置120と、乾燥装置300と、洗浄装置120において洗浄された基板Wを、洗浄装置120で供給された第2の処理液による液膜が形成された状態で搬出し、乾燥装置300に搬入する搬送装置200と、を有する。 The substrate processing apparatus 1 of the present embodiment includes a processing apparatus 110 that processes a substrate W by supplying a first processing liquid while rotating the substrate W, and a substrate W that has been processed by the processing apparatus 110 and performs a second processing while rotating the substrate W. A cleaning device 120 that cleans by supplying a liquid, a drying device 300, and a substrate W cleaned in the cleaning device 120 in a state where a liquid film is formed by the second processing liquid supplied by the cleaning device 120. and a conveying device 200 for unloading and loading into the drying device 300 .

本実施形態の基板乾燥方法は、処理液による液膜が形成され、支持部32に支持された基板Wを駆動機構33により回転させながら、第1の揮発性溶剤供給部34からの第1の揮発性溶剤Vの供給により液膜を第1の揮発性溶剤Vへ置換し、第2の揮発性溶剤供給部35から、撥水化膜を形成する撥水化剤を含み、気化する際の表面張力が第1の揮発性溶剤Vよりも小さい第2の揮発性溶剤の供給により、第1の揮発性溶剤Vの液膜を第2の揮発性溶剤Hに置換するとともに、基板Wに撥水化膜を形成させ、加熱部36による基板Wの加熱により、撥水化剤を含む第2の揮発性溶剤Hの液膜と基板Wとの間に気層を生じさせることによって、第2の揮発性溶剤Hの液膜を基板Wの回転による遠心力により排出させる。 In the substrate drying method of the present embodiment, the substrate W on which the liquid film of the processing liquid is formed and supported by the supporting portion 32 is rotated by the driving mechanism 33 while the first volatile solvent supplying portion 34 supplies the first liquid. By supplying the volatile solvent V, the liquid film is replaced with the first volatile solvent V, and from the second volatile solvent supply part 35, a water repellent agent that forms a water repellent film is contained, and when vaporized. By supplying the second volatile solvent whose surface tension is smaller than that of the first volatile solvent V, the liquid film of the first volatile solvent V is replaced with the second volatile solvent H, and the substrate W is repelled. A hydrated film is formed, and the heating unit 36 heats the substrate W to generate an air layer between the substrate W and the liquid film of the second volatile solvent H containing a water-repellent agent, whereby the second The liquid film of the volatile solvent H is discharged by the centrifugal force due to the rotation of the substrate W.

このように、基板Wを回転させながら加熱して過加熱状態とする際に、撥水化膜によってパターン間に液膜が形成され難くした上で、ライデンフロスト現象によって液膜を浮上させることにより、遠心力を利用して全体の液膜を瞬時に除去可能となる。 In this manner, when the substrate W is heated while being rotated to create an overheated state, the water-repellent film makes it difficult for the liquid film to form between the patterns, and the liquid film is floated by the Leidenfrost phenomenon. , the centrifugal force can be used to instantaneously remove the entire liquid film.

このため、同一装置内、同一処理室内で基板Wの乾燥が可能となり、乾燥装置300とは独立したプラズマ処理装置又はUV照射装置など、撥水化膜を除去する除去装置が不要となるとともに、乾燥装置300から除去装置への搬送工程が不要となる。従って、基板処理装置1を簡素化、小型化できるとともに、工程数が減少して、生産性が向上する。さらに、UV照射では困難であったパターン底部の液膜の除去も可能となる。 Therefore, the substrate W can be dried in the same apparatus and in the same processing chamber, and a removing apparatus for removing the water-repellent film, such as a plasma processing apparatus or a UV irradiation apparatus, which is independent of the drying apparatus 300, is not required. A transfer process from the drying device 300 to the removing device is unnecessary. Therefore, the substrate processing apparatus 1 can be simplified and miniaturized, and the number of processes can be reduced to improve productivity. Furthermore, it becomes possible to remove the liquid film on the bottom of the pattern, which has been difficult with UV irradiation.

また、第2の揮発性溶剤Hの液膜の全体を、撥水化膜とともに瞬時に除去できるので、基板Wの被処理面上において、部分的な液膜の残留が発生し難くなる。このため、隣接するパターン間で、液膜の残留の有無、残留量の相違によって張力に差が生じて、パターン倒壊が発生する可能性を低減できる。さらに、基板Wの中心と外周との遠心力の差、外周側への液膜の集中等による液膜の残留のばらつきも低減できる。 In addition, since the entire liquid film of the second volatile solvent H can be instantly removed together with the water-repellent film, it is difficult for a partial liquid film to remain on the surface of the substrate W to be processed. Therefore, it is possible to reduce the possibility of pattern collapse due to a difference in tension between adjacent patterns due to differences in the presence or absence of residual liquid film and differences in the amount of residual liquid film. Further, it is possible to reduce variations in residual liquid film caused by the difference in centrifugal force between the center and the outer periphery of the substrate W, concentration of the liquid film on the outer periphery, and the like.

(2)加熱部36が基板Wを加熱することによって、基板Wの被処理面に供給された第2の揮発性溶剤Hの液膜と基板Wとの間に気層を生じさせているとき、基板Wの被処理面に形成された撥水化膜は、基板Wの被処理面上から除去される。このため、加熱により撥水化膜の結合を解除させ、基板Wが回転する遠心力を利用して液膜及び撥水化膜を瞬時に除去可能となる。 (2) When the heating unit 36 heats the substrate W to generate an air layer between the substrate W and the liquid film of the second volatile solvent H supplied to the surface of the substrate W to be processed. , the water-repellent film formed on the surface of the substrate W to be processed is removed from the surface of the substrate W to be processed. Therefore, the bonding of the water-repellent film is released by heating, and the liquid film and the water-repellent film can be instantaneously removed by utilizing the centrifugal force of the rotation of the substrate W.

なお、加熱よる撥水化膜の離脱のために、過熱液をノズルから供給しようとしても、亜臨界液を扱うようなシステムが必要となるため、安全機構が増え、コストが高くなるが、本実施形態では、基板Wを回転させながら、加熱部36により基板Wを加熱することにより、追加の装置を不要として液膜を瞬時に除去することが可能となる。 In addition, even if superheated liquid is supplied from a nozzle in order to detach the water-repellent film by heating, a system that handles subcritical liquid is required, which increases the safety mechanism and increases the cost. In the embodiment, by heating the substrate W with the heating unit 36 while rotating the substrate W, the liquid film can be instantaneously removed without the need for an additional device.

(3)支持部32に支持された基板Wの第1の揮発性溶剤の膜厚を測定する測定部38を有し、制御装置400は、測定部38による測定結果の膜厚が所定のしきい値の範囲内にあると判定した場合に、加熱部36による加熱を開始させる。これにより、基板W上の液膜を適切な膜厚に調整してから、基板Wを乾燥させることができる。膜厚が薄過ぎると、加熱時に基板Wの被処理面上の液膜が不均一に乾燥してしまうため、一部のパターンにおけるパターン倒壊が生じてしまう。また、膜厚が厚過ぎると、液玉数が増えるので、回転する基板Wの遠心力により被処理面外へ液玉が排出されるまでに、基板Wの被処理面と接触する接触箇所が増加することになる。基板Wの被処理面は、液玉との接触時の気化熱により冷却されることから、液玉数が多くなり過ぎると、急速加熱中であっても基板Wの被処理面の一部にライデンフロスト現象が生じる温度以下となる箇所、すなわち、急速乾燥ではなく通常乾燥により乾燥する部分が生じてしまう。本実施形態では、適切な膜厚に調整してから基板Wを加熱するため、このような通常乾燥による乾燥状態が発生することを防止できる。 (3) The control device 400 has a measurement unit 38 that measures the film thickness of the first volatile solvent on the substrate W supported by the support unit 32. When it is determined that the value is within the threshold range, heating by the heating unit 36 is started. Accordingly, the substrate W can be dried after the liquid film on the substrate W is adjusted to have an appropriate film thickness. If the film thickness is too thin, the liquid film on the surface to be processed of the substrate W will be dried unevenly during heating, resulting in partial pattern collapse. Also, if the film thickness is too thick, the number of liquid droplets increases. will increase. Since the surface to be processed of the substrate W is cooled by the heat of vaporization when it comes into contact with the liquid droplets, if the number of liquid droplets becomes too large, even during rapid heating, part of the surface to be processed of the substrate W may be affected. There will be a portion where the temperature is lower than the temperature at which the Leidenfrost phenomenon occurs, that is, a portion that is dried not by rapid drying but by normal drying. In this embodiment, since the substrate W is heated after adjusting the film thickness to an appropriate value, it is possible to prevent the occurrence of such a dry state due to normal drying.

(変形例)
(1)第1の揮発性溶剤は、IPAには限定されない。例えば、HFE(ハイドロフルオロエーテル)等を用いることができる。撥水化剤としてのシランカップリング剤は、HMDSには限定されない。例えば、TMSDEA(テトラメチルシリルジエチルアミン)等を用いることができる。第2の揮発性溶剤も、上記のPGMEAには限定されない。例えば、IPAを用いてもよい。
(Modification)
(1) The first volatile solvent is not limited to IPA. For example, HFE (hydrofluoroether) or the like can be used. A silane coupling agent as a water repellent agent is not limited to HMDS. For example, TMSDEA (tetramethylsilyldiethylamine) or the like can be used. The second volatile solvent is also not limited to the above PGMEA. For example, IPA may be used.

(2)処理装置110の処理は、最終的に洗浄と乾燥が必要となる処理であれば、処理の内容及び処理液は、上記で例示したものには限定されない。処理対象となる基板W及び処理液についても、上記で例示したものには限定されない。 (2) As long as the processing of the processing apparatus 110 is processing that ultimately requires cleaning and drying, the content of the processing and the processing liquid are not limited to those exemplified above. The substrate W to be processed and the processing liquid are not limited to those exemplified above.

[他の実施形態]
以上、本発明の実施形態及び各部の変形例を説明したが、この実施形態や各部の変形例は、一例として提示したものであり、発明の範囲を限定することは意図していない。前述したこれら新規な実施形態は、その他の様々な形態で実施されることが可能であり、発明の要旨を逸脱しない範囲で、種々の省略、置き換え、変更を行うことができる。これら実施形態やその変形は、発明の範囲や要旨に含まれるとともに、特許請求の範囲に記載された発明に含まれる。
[Other embodiments]
Although the embodiment of the present invention and the modification of each part have been described above, the embodiment and the modification of each part are presented as an example and are not intended to limit the scope of the invention. These novel embodiments described above can be implemented in various other forms, and various omissions, replacements, and modifications can be made without departing from the scope of the invention. These embodiments and modifications thereof are included in the scope and gist of the invention, and are included in the invention described in the claims.

1 基板処理装置
11 洗浄室
11a 開口
11b 扉
12 支持部
13 回転機構
14 カップ
15 供給部
15a ノズル
15b 移動機構
20 ハンドリング装置
21 ロボットハンド
22 移動機構
31 乾燥室
31a 開口
31b 扉
33 窓部
32 支持部
32a 回転テーブル
32b 保持部材
32c 回転軸
33 駆動機構
33a 回転部
33b 昇降部
34 第1の揮発性溶剤供給部
34a、35a ノズル
34b、35b 揺動アーム
34c、35c 揺動機構
35 第2の揮発性溶剤供給部
36 加熱部
36a ランプ
37 カップ
38 測定部
38a 検出部
38b 揺動アーム
38c 揺動機構
41 機構制御部
42 膜厚解析部
43 加熱制御部
100 洗浄装置
200 搬送装置
300 乾燥装置
400 制御装置

1 substrate processing apparatus 11 cleaning chamber 11a opening 11b door 12 support section 13 rotation mechanism 14 cup 15 supply section 15a nozzle 15b movement mechanism 20 handling device 21 robot hand 22 movement mechanism 31 drying chamber 31a opening 31b door 33 window section 32 support section 32a Rotating table 32b Holding member 32c Rotating shaft 33 Driving mechanism 33a Rotating part 33b Lifting part 34 First volatile solvent supply parts 34a, 35a Nozzles 34b, 35b Swing arms 34c, 35c Swing mechanism 35 Second volatile solvent supply Part 36 Heating part 36a Lamp 37 Cup 38 Measurement part 38a Detection part 38b Swing arm 38c Swing mechanism 41 Mechanism control part
42 Film thickness analysis unit 43 Heating control unit 100 Cleaning device 200 Conveying device 300 Drying device 400 Control device

Claims (5)

基板を加熱する加熱部と、
前記基板の被処理面上に第1の揮発性溶剤を供給する第1の揮発性溶剤供給部と、
前記基板の被処理面上に、撥水化膜を形成する撥水化剤を含み、気化する際の表面張力が前記第1の揮発性溶剤よりも小さい第2の揮発性溶剤を供給する第2の揮発性溶剤供給部と、
前記加熱部、前記第1の揮発性溶剤供給部及び前記第2の揮発性溶剤供給部が収容され、被処理面上に処理液による液膜が形成された状態の前記基板が搬入される乾燥室と、
前記乾燥室に搬入された前記基板を受け取る支持部と、
前記支持部に支持された前記基板を回転させる駆動機構と、
前記第1の揮発性溶剤供給部から前記第1の揮発性溶剤を供給させることにより、前記基板の被処理面上に形成された前記処理液による液膜を前記第1の揮発性溶剤へ置換させ、
前記第2の揮発性溶剤供給部から前記第2の揮発性溶剤を供給させることにより、前記基板の被処理面上に形成された前記第1の揮発性溶剤を前記第2の揮発性溶剤へ置換させるとともに、前記基板の被処理面に前記撥水化膜を形成させ、
前記加熱部に前記基板を加熱させることにより、前記撥水化剤を含む前記第2の揮発性溶剤の液膜と前記基板との間に気層を生じさせることによって、前記第2の揮発性溶剤の液膜を前記基板の回転による遠心力により排出させる制御装置と、
を有することを特徴とする基板乾燥装置。
a heating unit that heats the substrate;
a first volatile solvent supply unit that supplies a first volatile solvent onto the surface to be processed of the substrate;
A second volatile solvent that contains a water-repellent agent that forms a water-repellent film and that has a lower surface tension than the first volatile solvent when vaporized is supplied onto the surface to be processed of the substrate. 2 volatile solvent supply;
drying in which the heating unit, the first volatile solvent supply unit, and the second volatile solvent supply unit are accommodated, and the substrate is carried in a state in which a liquid film of the processing liquid is formed on the surface to be processed; room and
a support for receiving the substrate carried into the drying chamber;
a drive mechanism for rotating the substrate supported by the support;
By supplying the first volatile solvent from the first volatile solvent supply unit, the liquid film of the processing liquid formed on the surface to be processed of the substrate is replaced with the first volatile solvent. let
By supplying the second volatile solvent from the second volatile solvent supply unit, the first volatile solvent formed on the surface to be processed of the substrate is transferred to the second volatile solvent. and forming the water-repellent film on the surface to be treated of the substrate,
By causing the heating unit to heat the substrate, an air layer is generated between the liquid film of the second volatile solvent containing the water repellent agent and the substrate, thereby removing the second volatile solvent. a control device for discharging the liquid film of the solvent by centrifugal force due to the rotation of the substrate;
A substrate drying apparatus comprising:
前記加熱部が前記基板を加熱することによって、前記基板の被処理面に供給された前記第2の揮発性溶剤の液膜と前記基板との間に気層を生じさせているとき、前記基板の被処理面に形成された前記撥水化膜は、前記基板の被処理面上から除去されることを特徴とする請求項1記載の基板乾燥装置。 When the heating unit heats the substrate to generate an air layer between the substrate and the liquid film of the second volatile solvent supplied to the surface to be processed of the substrate, the substrate 2. The substrate drying apparatus according to claim 1, wherein said water-repellent film formed on said surface to be treated is removed from said surface to be treated of said substrate. 前記支持部に支持された前記基板の前記第1の揮発性溶剤及び前記第2の揮発性溶剤の液膜の膜厚を測定する測定部を有し、
前記制御装置は、前記測定部による測定結果の膜厚が所定のしきい値の範囲内にあると判定した場合に、前記加熱部による加熱を開始させることを特徴とする請求項2記載の基板乾燥装置。
a measuring unit for measuring the film thickness of the liquid films of the first volatile solvent and the second volatile solvent on the substrate supported by the supporting unit;
3. The substrate according to claim 2, wherein the controller causes the heating unit to start heating when it is determined that the film thickness measured by the measuring unit is within a predetermined threshold range. drying equipment.
前記基板を回転させながら第1の処理液を供給することにより処理する処理装置と、
前記処理装置により処理済の前記基板を回転させながら第2の処理液を供給することにより洗浄する洗浄装置と、
請求項1乃至3のいずれかに記載の基板乾燥装置と、
前記洗浄装置において洗浄された前記基板を、前記洗浄装置で供給された前記第2の処理液による液膜が形成された状態で搬出し、前記基板乾燥装置に搬入する搬送装置と、
を有することを特徴とする基板処理装置。
a processing apparatus for processing the substrate by supplying a first processing liquid while rotating the substrate;
a cleaning device that cleans the substrate processed by the processing device by supplying a second processing liquid while rotating the substrate;
A substrate drying apparatus according to any one of claims 1 to 3;
a conveying device that unloads the substrate cleaned by the cleaning device in a state where a liquid film is formed by the second processing liquid supplied by the cleaning device, and carries the substrate into the substrate drying device;
A substrate processing apparatus comprising:
処理液による液膜が形成され、支持部に支持された基板を駆動機構により回転させながら、第1の揮発性溶剤供給部からの第1の揮発性溶剤の供給により前記処理液による液膜を前記第1の揮発性溶剤へ置換し、
第2の揮発性溶剤供給部から、撥水化膜を形成する撥水化剤を含み、気化する際の表面張力が前記第1の揮発性溶剤よりも小さい第2の揮発性溶剤の供給により、前記第1の揮発性溶剤の液膜を前記第2の揮発性溶剤に置換するとともに、前記基板に撥水化膜を形成させ、
加熱部による前記基板の加熱により、前記撥水化剤を含む前記第2の揮発性溶剤の液膜と前記基板との間に気層を生じさせることによって、前記第2の揮発性溶剤の液膜を前記基板の回転による遠心力により排出させる、
ことを特徴とする基板乾燥方法。
A liquid film of the treatment liquid is formed, and the liquid film of the treatment liquid is formed by supplying the first volatile solvent from the first volatile solvent supply part while rotating the substrate supported by the supporting part by the driving mechanism. replacing with the first volatile solvent,
A second volatile solvent containing a water repellent agent for forming a water repellent film and having a lower surface tension than the first volatile solvent when vaporized is supplied from the second volatile solvent supply unit. replacing the liquid film of the first volatile solvent with the second volatile solvent and forming a water-repellent film on the substrate;
By heating the substrate by the heating unit, an air layer is generated between the liquid film of the second volatile solvent containing the water repellent agent and the substrate, thereby heating the liquid of the second volatile solvent. expelling the film by centrifugal force due to the rotation of the substrate;
A substrate drying method characterized by:
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