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TWI898209B - Substrate processing method and substrate processing device - Google Patents

Substrate processing method and substrate processing device

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Publication number
TWI898209B
TWI898209B TW112117115A TW112117115A TWI898209B TW I898209 B TWI898209 B TW I898209B TW 112117115 A TW112117115 A TW 112117115A TW 112117115 A TW112117115 A TW 112117115A TW I898209 B TWI898209 B TW I898209B
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substrate
hydrogen peroxide
peroxide solution
ozone gas
liquid
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TW112117115A
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Chinese (zh)
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TW202401514A (en
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谷川紘太
太田喬
柴田秀一
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日商斯庫林集團股份有限公司
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    • GPHYSICS
    • G03PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
    • G03FPHOTOMECHANICAL PRODUCTION OF TEXTURED OR PATTERNED SURFACES, e.g. FOR PRINTING, FOR PROCESSING OF SEMICONDUCTOR DEVICES; MATERIALS THEREFOR; ORIGINALS THEREFOR; APPARATUS SPECIALLY ADAPTED THEREFOR
    • G03F7/00Photomechanical, e.g. photolithographic, production of textured or patterned surfaces, e.g. printing surfaces; Materials therefor, e.g. comprising photoresists; Apparatus specially adapted therefor
    • G03F7/26Processing photosensitive materials; Apparatus therefor
    • G03F7/42Stripping or agents therefor
    • H10P50/00
    • H10P50/242
    • H10P52/00
    • H10P76/00

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  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Exposure Of Semiconductors, Excluding Electron Or Ion Beam Exposure (AREA)
  • Cleaning Or Drying Semiconductors (AREA)
  • Photosensitive Polymer And Photoresist Processing (AREA)
  • Drying Of Semiconductors (AREA)
  • Weting (AREA)

Abstract

基板處理方法及基板處理裝置係對形成有抗蝕圖案100之基板W之表面供給過氧化氫溶液。基板處理方法及基板處理裝置係對與基板W接觸之過氧化氫溶液供給臭氧氣體。The substrate processing method and the substrate processing apparatus supply a hydrogen peroxide solution to the surface of the substrate W having the resist pattern 100 formed thereon. The substrate processing method and the substrate processing apparatus supply ozone gas to the hydrogen peroxide solution in contact with the substrate W.

Description

基板處理方法及基板處理裝置Substrate processing method and substrate processing device

本發明係關於一種處理基板之基板處理方法及基板處理裝置。基板例如包括半導體晶圓、液晶顯示裝置、有機EL(electroluminescence,電致發光)顯示裝置等FPD(Flat Panel Display,平板顯示器)用基板、光碟用基板、磁碟用基板、磁光碟用基板、光罩用基板、陶瓷基板、太陽電池用基板等。The present invention relates to a substrate processing method and substrate processing apparatus for processing substrates. Examples of substrates include semiconductor wafers, liquid crystal display (LCD) devices, organic EL (electroluminescence) display (FPD) substrates, optical disk substrates, magnetic disk substrates, magneto-optical disk substrates, photomask substrates, ceramic substrates, and solar cell substrates.

專利文獻1揭示有為了自基板之表面除去具有硬化層之抗蝕劑,一面以150℃以上之溫度加熱基板,一面對基板之表面供給臭氧氣體,其後,對基板之表面供給SPM(sulfuric acid/hydrogen peroxide mixture,硫酸/過氧化氫混合物)等包含硫酸之處理液。 [先前技術文獻] [專利文獻] Patent Document 1 discloses a method for removing a hardened resist from a substrate surface by heating the substrate to a temperature above 150°C while supplying ozone gas to the substrate surface. Subsequently, a treatment solution containing sulfuric acid, such as an SPM (sulfuric acid/hydrogen peroxide mixture), is supplied to the substrate surface. [Prior Art Document] [Patent Document]

[專利文獻1]日本專利特開2022-41077號公報[Patent Document 1] Japanese Patent Publication No. 2022-41077

[發明所欲解決之問題][Identify the problem you want to solve]

本發明之一實施方式提供一種能夠更有效率地自基板剝離或除去抗蝕劑之基板處理方法及基板處理裝置。 [解決問題之技術手段] One embodiment of the present invention provides a substrate processing method and substrate processing apparatus capable of more efficiently stripping or removing an etchant from a substrate. [Technical Solution]

本發明之一實施方式提供一種基板處理方法,其包括:過氧化氫溶液供給步驟,其係對形成有抗蝕圖案之基板之表面供給過氧化氫溶液;及臭氧氣體供給步驟,其係對與上述基板接觸之上述過氧化氫溶液供給臭氧氣體。One embodiment of the present invention provides a substrate processing method, comprising: a hydrogen peroxide solution supplying step of supplying a hydrogen peroxide solution to a surface of a substrate having an anti-etching pattern formed thereon; and an ozone gas supplying step of supplying ozone gas to the hydrogen peroxide solution in contact with the substrate.

根據該方法,使過氧化氫溶液與形成於基板之表面之抗蝕圖案接觸。進而,使臭氧氣體與該過氧化氫溶液接觸。藉由臭氧氣體與過氧化氫之反應而產生羥基自由基。羥基自由基氧化並分解抗蝕圖案。藉此,抗蝕圖案之至少一部分被剝離或除去。羥基自由基之氧化還原電位較臭氧氣體高,氧化能力較臭氧氣體強。因此,相較於用臭氧氣體氧化及分解抗蝕圖案之情形,能夠有效率地除去抗蝕圖案。藉此,能夠削減含有硫酸之抗蝕劑剝離液之使用量或省去其之使用,因此能夠降低環境負載。According to this method, a hydrogen peroxide solution is brought into contact with the resist pattern formed on the surface of the substrate. Furthermore, ozone gas is brought into contact with the hydrogen peroxide solution. Hydroxyl radicals are generated by the reaction between the ozone gas and the hydrogen peroxide. The hydroxyl radicals oxidize and decompose the resist pattern. As a result, at least a portion of the resist pattern is stripped or removed. The redox potential of hydroxyl radicals is higher than that of ozone gas, and their oxidizing power is stronger than that of ozone gas. Therefore, the resist pattern can be removed more efficiently than when ozone gas is used to oxidize and decompose the resist pattern. This reduces the amount of resist stripping solution containing sulfuric acid used or eliminates its use, thereby reducing the environmental burden.

若抗蝕圖案形成於基板之表面,則基板可為進行了離子注入之基板,亦可為未進行離子注入之基板,該離子注入係對基板之表面中自抗蝕圖案露出之部分注入雜質離子。於前者之情形時,抗蝕圖案之表層可藉由離子注入而硬化,亦可不硬化。If the anti-etching pattern is formed on the surface of a substrate, the substrate may be ion-implanted or non-ion-implanted. Ion implantation involves implanting impurity ions into the portion of the substrate surface exposed by the anti-etching pattern. In the former case, the surface layer of the anti-etching pattern may or may not be hardened by ion implantation.

過氧化氫溶液係過氧化氫之水溶液。過氧化氫溶液係以過氧化氫(H 2O 2)及水(H 2O)為主成分之液體。若過氧化氫及水為主成分(例如過氧化氫及水之體積百分比濃度為90%以上),則過氧化氫溶液可包含除過氧化氫及水以外之物質。 A hydrogen peroxide solution is an aqueous solution of hydrogen peroxide. A hydrogen peroxide solution is a liquid primarily composed of hydrogen peroxide ( H2O2 ) and water ( H2O ). If hydrogen peroxide and water are the primary components (e.g., the volume percentage concentration of hydrogen peroxide and water is 90% or greater), the hydrogen peroxide solution may contain substances other than hydrogen peroxide and water.

臭氧氣體係以較空氣中之臭氧之濃度高之濃度包含臭氧的含臭氧氣體。含臭氧氣體係臭氧均勻分散之氣體。含臭氧氣體可為僅包含臭氧之氣體,亦可為亦包含除臭氧以外之成分之氣體。於後者之情形時,含臭氧氣體中可包含氧或二氧化碳等除臭氧以外之成分。Ozone gas is ozone-containing gas that contains ozone at a higher concentration than that in air. Ozone-containing gas is a gas in which ozone is evenly dispersed. Ozone-containing gas can contain only ozone or other components besides ozone. In the latter case, ozone-containing gas can contain components other than ozone, such as oxygen or carbon dioxide.

亦可於上述實施方式中,將以下特徵中之至少1個添加至上述基板處理方法中。In the above embodiment, at least one of the following features may be added to the above substrate processing method.

上述基板處理方法進而包括過氧化氫溶液加熱步驟,其係在將上述過氧化氫溶液供給至上述基板之前或之後,以高於室溫之剝離促進溫度加熱上述過氧化氫溶液。The substrate processing method further includes a hydrogen peroxide solution heating step, which is to heat the hydrogen peroxide solution at a peeling promotion temperature higher than room temperature before or after the hydrogen peroxide solution is supplied to the substrate.

根據該方法,供給至基板之後,間接或直接地加熱過氧化氫溶液。或者,將加熱後之過氧化氫溶液供給至基板。藉此,能夠使臭氧氣體與剝離促進溫度、即高於室溫之溫度之過氧化氫溶液接觸,能夠促進羥基自由基之產生。其結果,能夠增加與抗蝕圖案反應之羥基自由基,從而能夠更有效率地除去抗蝕圖案。According to this method, after being supplied to the substrate, the hydrogen peroxide solution is heated indirectly or directly. Alternatively, the heated hydrogen peroxide solution is supplied to the substrate. This allows the ozone gas to come into contact with the hydrogen peroxide solution at a temperature above room temperature, which is a temperature that promotes the stripping process. This promotes the generation of hydroxyl radicals. As a result, the number of hydroxyl radicals that react with the resist pattern increases, enabling more efficient removal of the resist pattern.

上述過氧化氫溶液加熱步驟可為間接加熱步驟、直接加熱步驟、及預先加熱步驟中之任一種,亦可包括該等中之2種以上。上述間接加熱步驟係如下步驟,即,藉由使加熱後之上述基板及加熱後之氣體中之至少一者與接觸於上述基板之上述過氧化氫溶液接觸,而以上述剝離促進溫度加熱上述過氧化氫溶液。直接加熱步驟係如下步驟,即,藉由對與上述基板接觸之上述過氧化氫溶液照射自燈等熱源放出之電磁波,而以上述剝離促進溫度加熱上述過氧化氫溶液。預先加熱步驟係如下步驟,即,在將上述過氧化氫溶液供給至上述基板之前,以上述剝離促進溫度對應供給至上述基板之上述過氧化氫溶液進行加熱。The hydrogen peroxide solution heating step may be any of an indirect heating step, a direct heating step, and a preheating step, or may include two or more of these. The indirect heating step is a step in which the hydrogen peroxide solution in contact with the substrate is brought into contact with at least one of the heated substrate and the heated gas, thereby heating the hydrogen peroxide solution to the peeling-promoting temperature. The direct heating step is a step in which the hydrogen peroxide solution in contact with the substrate is irradiated with electromagnetic waves emitted from a heat source such as a lamp, thereby heating the hydrogen peroxide solution to the peeling-promoting temperature. The preheating step is a step of heating the hydrogen peroxide solution supplied to the substrate at the peeling promoting temperature before the hydrogen peroxide solution is supplied to the substrate.

上述剝離促進溫度未達上述過氧化氫溶液之沸點。The above-mentioned peeling promotion temperature does not reach the boiling point of the above-mentioned hydrogen peroxide solution.

根據該方法,以低於過氧化氫溶液之沸點之溫度加熱過氧化氫溶液。藉此,能夠降低過氧化氫溶液自基板蒸發之速度,能夠維持過氧化氫溶液位於基板上之狀態。若使大量之過氧化氫溶液保持於基板上,則即便將過氧化氫溶液以沸點以上之溫度加熱,亦能夠在相對長之時間內維持過氧化氫溶液位於基板上之狀態。然而,於該情形時,基板上之過氧化氫溶液之液滴或液膜之厚度變大,到達抗蝕圖案之表面之羥基自由基減少。藉由以低於過氧化氫溶液之沸點之溫度加熱過氧化氫溶液,即便不於基板上形成厚度較大之過氧化氫溶液之液滴或液膜,亦能夠維持過氧化氫溶液位於基板上之狀態。According to this method, the hydrogen peroxide solution is heated to a temperature below its boiling point. This reduces the rate of evaporation from the substrate and maintains the hydrogen peroxide solution on the substrate. If a large amount of hydrogen peroxide solution is retained on the substrate, even if it is heated above its boiling point, the hydrogen peroxide solution can be maintained on the substrate for a relatively long time. However, in this case, the thickness of the hydrogen peroxide solution droplet or film on the substrate increases, reducing the number of hydroxyl radicals reaching the surface of the anti-etching pattern. By heating the hydrogen peroxide solution at a temperature lower than the boiling point of the hydrogen peroxide solution, the hydrogen peroxide solution can be maintained on the substrate even if thick droplets or a liquid film of the hydrogen peroxide solution is not formed on the substrate.

上述剝離促進溫度未達水之沸點。The above-mentioned peeling promotion temperature does not reach the boiling point of water.

根據該方法,以低於水之沸點、即低於100℃之溫度加熱過氧化氫溶液。藉此,能夠降低水自基板上之過氧化氫溶液蒸發之速度,即便不於基板上形成厚度較大之過氧化氫溶之液液滴或液膜,亦能夠維持水位於基板上之狀態。羥基自由基不僅藉由臭氧氣體與過氧化氫之反應而產生,亦藉由臭氧氣體與水之反應而產生。藉此,能夠增加與抗蝕圖案反應之羥基自由基。According to this method, the hydrogen peroxide solution is heated to a temperature below the boiling point of water, that is, below 100°C. This reduces the rate of water evaporation from the hydrogen peroxide solution on the substrate, maintaining the water level on the substrate without forming thick hydrogen peroxide droplets or films on the substrate. Hydroxyl radicals are generated not only by the reaction of ozone gas with hydrogen peroxide, but also by the reaction of ozone gas with water. This increases the number of hydroxyl radicals available for reaction with the resist pattern.

當對抗蝕圖案進行加熱時,抗蝕圖案中所含之溶劑氣化。於抗蝕圖案之表層形成有硬化層之情形時,氣化後之溶劑難以排出,因此抗蝕圖案之內部壓力上升。自抗蝕劑塗佈至抗蝕劑剝離之前之一系列步驟包括預烘烤、後烘烤等加熱基板之步驟。將該一系列步驟中之基板之溫度之最大值定義為最高溫度。於抗蝕圖案之表層形成有硬化層,當加熱抗蝕圖案之溫度大幅高於最高溫度時,抗蝕圖案之內部壓力容易變高。When the resist pattern is heated, the solvent contained in it vaporizes. If a hardened layer forms on the surface of the resist pattern, the vaporized solvent is difficult to expel, causing the internal pressure of the resist pattern to increase. The series of steps from resist application to resist stripping includes pre-baking and post-baking, which involve heating the substrate. The maximum substrate temperature during this series of steps is defined as the maximum temperature. If a hardened layer forms on the surface of the resist pattern, the internal pressure of the resist pattern tends to increase when the temperature of the heated resist pattern is significantly higher than the maximum temperature.

於以高於室溫之剝離促進溫度加熱過氧化氫溶液時,若將該剝離促進溫度設為低於過氧化氫溶液之沸點之溫度或低於水之沸點之溫度,則可使加熱抗蝕圖案之溫度接近於上述一系列步驟中之基板之溫度之最大值、即最高溫度。或者,可將加熱抗蝕圖案之溫度設為最高溫度以下。藉此,即便為於抗蝕圖案之表層形成有硬化層之情形,亦能夠防止抗蝕圖案之內部壓力變高。When heating the hydrogen peroxide solution at a peeling-promoting temperature higher than room temperature, setting the peeling-promoting temperature to a temperature lower than the boiling point of the hydrogen peroxide solution or lower than the boiling point of water allows the temperature of the heated resist pattern to approach the maximum temperature of the substrate during the aforementioned series of steps, i.e., the highest temperature. Alternatively, the temperature of the heated resist pattern can be set below the highest temperature. This prevents the internal pressure of the resist pattern from increasing, even when a hardened layer is formed on the surface of the resist pattern.

上述過氧化氫溶液供給步驟包括:初次供給步驟,其係對上述基板之表面供給上述過氧化氫溶液;及再供給步驟,其係在停止向上述基板之表面供給上述過氧化氫溶液後,對上述基板之表面供給過氧化氫溶液。換而言之,上述過氧化氫溶液供給步驟包括將過氧化氫溶液之供給在中途至少中斷1次之步驟。The hydrogen peroxide solution supplying step includes: an initial supplying step of supplying the hydrogen peroxide solution to the surface of the substrate; and a resupplying step of supplying the hydrogen peroxide solution to the surface of the substrate after terminating the supply of the hydrogen peroxide solution to the surface of the substrate. In other words, the hydrogen peroxide solution supplying step includes interrupting the supply of the hydrogen peroxide solution at least once.

根據該方法,以高於室溫之剝離促進溫度加熱過氧化氫溶液,並且間歇地對基板之表面供給過氧化氫溶液。即,將過氧化氫溶液供給至基板之表面,並使其保持於基板之表面。在停止供給過氧化氫溶液之期間(停止添加過氧化氫溶液之期間),基板上之過氧化氫溶液因蒸發、與臭氧氣體之反應而減少。重新開始向基板之表面供給過氧化氫溶液而對基板之表面添加過氧化氫溶液。藉此,相較於持續供給過氧化氫溶液之情形,能夠削減過氧化氫溶液之消耗量,並且維持過氧化氫溶液位於基板上之狀態。此外,相較於持續供給過氧化氫溶液之情形,能夠使基板上之過氧化氫溶液之液滴或液膜變薄。According to this method, a hydrogen peroxide solution is heated to a peeling-promoting temperature above room temperature and intermittently supplied to the substrate surface. Specifically, the hydrogen peroxide solution is supplied to the substrate surface and maintained there. During the period when the hydrogen peroxide supply is stopped (the period when the addition of hydrogen peroxide is stopped), the amount of hydrogen peroxide on the substrate decreases due to evaporation and reaction with ozone gas. The supply of hydrogen peroxide to the substrate surface is then resumed, and the hydrogen peroxide solution is added to the substrate surface. This reduces the consumption of hydrogen peroxide solution compared to a continuous supply of hydrogen peroxide solution, while maintaining the hydrogen peroxide solution on the substrate. In addition, compared to the case of continuously supplying the hydrogen peroxide solution, the droplets or liquid film of the hydrogen peroxide solution on the substrate can be made thinner.

上述臭氧氣體供給步驟包括在上述過氧化氫溶液之複數個液滴分散於上述基板之表面全域之狀態下,對與上述基板接觸之上述過氧化氫溶液供給上述臭氧氣體之步驟。自與基板之表面垂直之方向觀察基板之表面時之過氧化氫溶液之液滴的形狀可為圓、橢圓、及線中之任一種,亦可為該等以外之形狀。The ozone gas supplying step includes supplying the ozone gas to the hydrogen peroxide solution in contact with the substrate while a plurality of hydrogen peroxide solution droplets are dispersed over the entire surface of the substrate. The shape of the hydrogen peroxide solution droplets when viewed perpendicular to the substrate surface may be any of a circle, an ellipse, and a line, or may be other shapes.

根據該方法,不是在基板之表面全域被過氧化氫溶液之液膜覆蓋之狀態下,而是在過氧化氫溶液之複數個液滴分散於基板之表面全域之狀態下,使臭氧氣體與接觸於基板之過氧化氫溶液接觸。藉此,相較於基板之表面全域被過氧化氫溶液之液膜覆蓋之情形,可有效率地除去抗蝕圖案。理由如下所述。According to this method, ozone gas is brought into contact with the hydrogen peroxide solution in contact with the substrate, rather than with the entire substrate surface being covered by a film of hydrogen peroxide solution. This method allows for more efficient removal of the resist pattern than when the entire substrate surface is covered by a film of hydrogen peroxide solution. The reasons are as follows.

供給至抗蝕圖案與過氧化氫溶液之界面即固液界面(參照圖4)之羥基自由基(OH)隨著接近於臭氧氣體、過氧化氫溶液及抗蝕圖案之邊界即三態邊界(參照圖4)而增加。其原因在於:羥基自由基在短時間內會變回過氧化氫,因此若自過氧化氫溶液之液滴或液膜之表面至固液界面之最短距離較長,則羥基自由基在到達固液界面之前就會消失。因此,相較於距三態邊界較遠之位置,在三態邊界附近能夠有效率地除去與過氧化氫溶液接觸之抗蝕圖案。The number of hydroxyl radicals (OH) supplied to the interface between the resist pattern and the hydrogen peroxide solution, known as the solid-liquid interface (see Figure 4), increases as the distance from the ozone gas, hydrogen peroxide solution, and resist pattern, known as the three-state boundary (see Figure 4), increases. This is because hydroxyl radicals quickly transform back into hydrogen peroxide. Therefore, if the shortest distance from the surface of the hydrogen peroxide solution droplet or film to the solid-liquid interface is long, the hydroxyl radicals will disappear before reaching the solid-liquid interface. Therefore, resist patterns in contact with the hydrogen peroxide solution are more effectively removed near the three-state boundary than at locations farther from it.

過氧化氫溶液之複數個液滴分散於基板之表面全域時的三態邊界之全長(長度之合計值),大於基板之表面全域被過氧化氫溶液之液膜覆蓋時的三態邊界之全長。如上所述,相較於距三態邊界較遠之位置,在三態邊界附近能夠有效率地除去與過氧化氫溶液接觸之抗蝕圖案。由於以上原因,相較於基板之表面全域被過氧化氫溶液之液膜覆蓋之情形,能夠有效率地除去抗蝕圖案。The total length (aggregate length) of the three-state boundary when multiple hydrogen peroxide droplets are dispersed over the entire surface of the substrate is greater than the total length of the three-state boundary when the entire substrate surface is covered by a liquid film of hydrogen peroxide. As described above, the resist pattern in contact with the hydrogen peroxide solution can be removed more efficiently near the three-state boundary than at locations farther from the three-state boundary. For these reasons, the resist pattern can be removed more efficiently than when the entire substrate surface is covered by a liquid film of hydrogen peroxide solution.

上述過氧化氫溶液供給步驟包括霧供給步驟,其係對上述基板之表面供給上述過氧化氫溶液之霧。The hydrogen peroxide solution supplying step includes a mist supplying step of supplying a mist of the hydrogen peroxide solution to the surface of the substrate.

根據該方法,對基板之表面供給霧狀之過氧化氫溶液。過氧化氫溶液之霧係由多個過氧化氫溶液之粒子構成。基板上之過氧化氫溶液之粒子與其他過氧化氫溶液之粒子結合,從而於基板之表面形成過氧化氫溶液之液滴(直徑較過氧化氫溶液之粒子大之過氧化氫溶液之集合體)。於抗蝕圖案之表面為疏水性之情形時,形成過氧化氫溶液之複數個液滴,並分散於基板之表面全域。於抗蝕圖案之表面為親水性之情形時,形成覆蓋基板之表面全域的過氧化氫溶液之液膜。藉此,相較於形成自液柱噴嘴至基板之表面連續之過氧化氫溶液之液柱之情形,能夠形成較薄之過氧化氫溶液之液滴或液膜。According to this method, a hydrogen peroxide solution mist is applied to the surface of the substrate. The hydrogen peroxide solution mist is composed of multiple hydrogen peroxide solution particles. The hydrogen peroxide solution particles on the substrate combine with other hydrogen peroxide solution particles, forming hydrogen peroxide solution droplets (aggregates of hydrogen peroxide solution with a diameter larger than the hydrogen peroxide solution particles) on the substrate surface. If the surface of the anti-etching pattern is hydrophobic, multiple hydrogen peroxide solution droplets are formed and dispersed over the entire surface of the substrate. If the surface of the anti-etching pattern is hydrophilic, a hydrogen peroxide solution film is formed that covers the entire surface of the substrate. Thus, thinner droplets or liquid films of hydrogen peroxide solution can be formed compared to the case where a continuous liquid column of hydrogen peroxide solution is formed from the liquid column nozzle to the surface of the substrate.

上述過氧化氫溶液供給步驟包括液柱供給步驟,其係藉由形成自液柱噴嘴至上述基板之表面連續之上述過氧化氫溶液之液柱來將上述過氧化氫溶液供給至上述基板之表面。The hydrogen peroxide solution supplying step includes a liquid column supplying step of supplying the hydrogen peroxide solution to the surface of the substrate by forming a liquid column of the hydrogen peroxide solution continuously from a liquid column nozzle to the surface of the substrate.

根據該方法,自液柱噴嘴朝向基板之表面連續地噴出過氧化氫溶液,使過氧化氫溶液與基板之表面碰撞。自液柱噴嘴噴出之過氧化氫溶液形成自液柱噴嘴至基板之表面連續之過氧化氫溶液之液注。於抗蝕圖案之表面為疏水性之情形時,形成過氧化氫溶液之複數個液滴並分散於基板之表面全域。於抗蝕圖案之表面為親水性之情形時,形成覆蓋基板之表面全域的過氧化氫溶液之液膜。藉此,相較於對基板之表面供給過氧化氫溶液之霧之情形,能夠在短時間內形成過氧化氫溶液之液滴或液膜。According to this method, a hydrogen peroxide solution is continuously sprayed from a liquid column nozzle toward the surface of a substrate, causing the hydrogen peroxide solution to collide with the substrate surface. The hydrogen peroxide solution ejected from the liquid column nozzle forms a continuous stream of hydrogen peroxide solution from the liquid column nozzle to the surface of the substrate. If the surface of the anti-etching pattern is hydrophobic, multiple droplets of hydrogen peroxide solution are formed and dispersed over the entire surface of the substrate. If the surface of the anti-etching pattern is hydrophilic, a liquid film of hydrogen peroxide solution is formed covering the entire surface of the substrate. This method enables the formation of droplets or a liquid film of hydrogen peroxide solution in a shorter time than when a mist of hydrogen peroxide solution is supplied to the substrate surface.

上述基板處理方法進而包括親水化步驟,其係藉由在對上述基板之表面供給上述過氧化氫溶液之前,使上述臭氧氣體與上述基板之表面接觸來減小水相對於上述抗蝕圖案之表面之接觸角。The substrate processing method further includes a hydrophilization step, which is to reduce the contact angle of water with the surface of the anti-etching pattern by allowing the ozone gas to contact the surface of the substrate before supplying the hydrogen peroxide solution to the surface of the substrate.

根據該方法,使臭氧氣體與基板之表面接觸而減弱抗蝕圖案之表面之疏水性。藉此,水相對於抗蝕圖案之表面之接觸角減小。於該狀態下,對基板之表面供給過氧化氫溶液。於抗蝕圖案之表面為疏水性之情形時,若不以較大之流量供給過氧化氫溶液,則無法形成覆蓋基板之表面全域的過氧化氫溶液之液膜。然而,於該情形時,過氧化氫溶液之消耗量增加,形成較厚之過氧化氫溶液之液膜。若在將抗蝕圖案之表面親水化後供給過氧化氫溶液,則能夠削減過氧化氫溶液之消耗量,形成覆蓋基板之表面全域的較薄之過氧化氫溶液之液膜。此外,由於不僅使用臭氧氣體除去抗蝕圖案,而且使用臭氧氣體對抗蝕圖案之表面進行親水化,因此相較於使用除臭氧氣體以外之液體或氣體來對抗蝕圖案之表面進行親水化之情形,能夠減少配管、閥等用於處理基板之流體機器之數量。According to this method, ozone gas is brought into contact with the substrate surface, weakening the hydrophobicity of the anti-etching pattern. This reduces the contact angle of water with the anti-etching pattern. Under this condition, a hydrogen peroxide solution is supplied to the substrate surface. If the anti-etching pattern surface is hydrophobic, a hydrogen peroxide film that covers the entire substrate surface cannot be formed unless the hydrogen peroxide solution is supplied at a high flow rate. However, in this case, hydrogen peroxide consumption increases, resulting in a thicker hydrogen peroxide film. Applying hydrogen peroxide solution after the surface of the resist pattern has been hydrophilized can reduce hydrogen peroxide consumption and form a thinner hydrogen peroxide film covering the entire surface of the substrate. Furthermore, since ozone gas is used not only to remove the resist pattern but also to hydrophilize the surface of the resist pattern, the number of fluid equipment such as piping and valves used to process the substrate can be reduced compared to using liquids or gases other than ozone to hydrophilize the surface of the resist pattern.

上述基板處理方法進而包括剝離液供給步驟,其係在對與上述基板接觸之上述過氧化氫溶液供給上述臭氧氣體之後,對上述基板之表面供給用於將上述抗蝕圖案自上述基板之表面剝離之抗蝕劑剝離液。The substrate processing method further includes a stripping liquid supplying step, which is to supply the ozone gas to the hydrogen peroxide solution in contact with the substrate, and then supply an anti-etching agent stripping liquid to the surface of the substrate for stripping the anti-etching pattern from the surface of the substrate.

根據該方法,在使用藉由臭氧氣體與過氧化氫反應而產生之羥基自由基剝離或除去抗蝕圖案之全部或一部分後,對基板之表面供給抗蝕劑剝離液。即便抗蝕圖案之一部分殘留於基板之表面,該抗蝕圖案亦會因與抗蝕劑剝離液接觸而自基板之表面剝離。即便抗蝕圖案之殘渣殘留於基板之表面,該殘渣亦會被抗蝕劑剝離液沖洗掉。藉此,能夠減少殘留於基板之表面之抗蝕劑。According to this method, after stripping or removing all or part of the resist pattern using hydroxyl radicals generated by the reaction of ozone gas and hydrogen peroxide, a resist stripping liquid is applied to the substrate surface. Even if a portion of the resist pattern remains on the substrate surface, it will be stripped from the substrate surface due to contact with the resist stripping liquid. Even if residue from the resist pattern remains on the substrate surface, it will be washed away by the resist stripping liquid. This reduces the amount of resist remaining on the substrate surface.

用於達成上述目的之本發明之另一實施方式係提供一種基板處理裝置,其包括:過氧化氫溶液噴嘴,其對形成有抗蝕圖案之基板之表面供給過氧化氫溶液;及臭氧噴嘴,其對與上述基板接觸之上述過氧化氫溶液供給臭氧氣體。該裝置能夠起到與上述基板處理方法相同之效果。可將關於基板處理方法之上述特徵中之至少1個添加至該實施方式之基板處理裝置中。Another embodiment of the present invention, used to achieve the above-mentioned objectives, provides a substrate processing apparatus comprising: a hydrogen peroxide solution nozzle for supplying a hydrogen peroxide solution to the surface of a substrate having a resist pattern formed thereon; and an ozone nozzle for supplying ozone gas to the hydrogen peroxide solution in contact with the substrate. This apparatus can achieve the same effects as the above-mentioned substrate processing method. At least one of the features described above with respect to the substrate processing method can be incorporated into the substrate processing apparatus of this embodiment.

本發明中之上述內容或進而其他目的、特徵及效果,藉由以下參照隨附圖式所述之實施方式之說明而變得明確。The above contents and further other purposes, features and effects of the present invention will become clear through the following description of the embodiments described with reference to the accompanying drawings.

圖1係表示本發明之一實施方式之包括抗蝕劑剝離的基板W之處理之一例之步驟圖。圖2係表示本發明之一實施方式之抗蝕圖案100之一例的概略剖視圖。FIG1 is a diagram showing an example of a process for processing a substrate W including resist stripping according to an embodiment of the present invention. FIG2 is a schematic cross-sectional view showing an example of a resist pattern 100 according to an embodiment of the present invention.

於圖1所示之基板W之處理中,進行抗蝕劑塗佈(圖1之步驟S1),其係藉由在矽晶圓等基板W之表面塗佈包含樹脂及溶劑之光阻劑液,形成覆蓋基板W之表面全域之抗蝕膜。其後,進行預烘烤(圖1之步驟S2),其係於基板W之表面全域被抗蝕膜覆蓋之狀態下,以預烘烤溫度加熱基板W,來使抗蝕膜中所含之溶劑蒸發。其後,進行曝光(圖1之步驟S3),其係藉由將紫外線等光經由光罩照射至基板W上之抗蝕膜,而將形成於光罩上之電路圖案轉印至抗蝕膜。In the processing of the substrate W shown in Figure 1 , resist coating is performed (step S1 in Figure 1 ). This is achieved by coating the surface of a substrate W, such as a silicon wafer, with a photoresist solution containing a resin and a solvent, forming a resist film that covers the entire surface of the substrate W. Subsequently, a pre-bake (step S2 in Figure 1 ) is performed. With the entire surface of the substrate W covered by the resist film, the substrate W is heated at a pre-bake temperature to evaporate the solvent contained in the resist film. Subsequently, an exposure step (step S3 in Figure 1 ) is performed. This is achieved by irradiating the resist film on the substrate W with light such as ultraviolet light through a photomask, thereby transferring the circuit pattern formed on the photomask to the resist film.

曝光後進行顯影(圖1之步驟S3),其係藉由對基板W供給顯影液,自抗蝕膜除去不需要之部分,而於基板W之表面形成相當於殘留之抗蝕膜之抗蝕圖案100。其後,進行後烘烤(圖1之步驟S4),其係以後烘烤溫度加熱基板W。可於曝光後、顯影前,進行加熱基板W之曝光後烘烤。後烘烤之後,進行離子注入(圖1之步驟S5),其係於基板W之表面對自抗蝕圖案100露出之部分注入雜質離子。其後,進行抗蝕劑剝離(圖1之步驟S6),其係將自基板W之表面除去不需要之抗蝕圖案100。After exposure, development is performed (step S3 of FIG. 1 ), which involves supplying a developer solution to the substrate W to remove unwanted portions of the resist film, thereby forming a resist pattern 100 on the surface of the substrate W that corresponds to the remaining resist film. Subsequently, post-baking is performed (step S4 of FIG. 1 ), which involves heating the substrate W at a post-baking temperature. A post-exposure bake, in which the substrate W is heated after exposure and before development, may be performed. After post-baking, ion implantation is performed (step S5 of FIG. 1 ), which involves implanting impurity ions into portions of the surface of the substrate W exposed from the resist pattern 100. Subsequently, resist stripping is performed (step S6 of FIG. 1 ), which removes unwanted portions of the resist pattern 100 from the surface of the substrate W.

於離子注入中,雜質離子不僅與基板W之表面之一部分碰撞,亦與相當於抗蝕遮罩之抗蝕圖案100碰撞。因此,抗蝕圖案100之表層之全域或大部分由於碳化等變質而變化為硬化層101。另一方面,抗蝕圖案100之內部在未硬化之狀態下殘留於硬化層101之內側。圖2示出如下之例,即,相當於抗蝕圖案100中未硬化之部分之非硬化部102與基板W之表面接觸,非硬化部102之前端面及兩個側面被硬化層101覆蓋。以下,對自基板W之表面除去此種抗蝕圖案100之抗蝕劑剝離進行說明。During ion implantation, impurity ions collide not only with a portion of the surface of substrate W but also with resist pattern 100, which acts as an anti-etching mask. Consequently, the entire or majority of the surface layer of resist pattern 100 undergoes degradation, such as carbonization, transforming into hardened layer 101. Meanwhile, the interior of resist pattern 100 remains unhardened, inside hardened layer 101. Figure 2 illustrates an example in which a non-hardened portion 102, corresponding to the unhardened portion of resist pattern 100, contacts the surface of substrate W, with the front end and both side surfaces of non-hardened portion 102 covered by hardened layer 101. The following describes the resist stripping process for removing such a resist pattern 100 from the surface of substrate W.

以下,對本發明之一實施方式之抗蝕劑剝離之2個例子進行說明。Two examples of resist stripping according to one embodiment of the present invention are described below.

於以下之說明中,只要無特別說明,則基板W表示相當於母材之基板W及形成於母材上之抗蝕圖案100之兩者,基板W之表面表示抗蝕圖案100之表面及基板W之表面中自抗蝕圖案100露出部分之兩者。In the following description, unless otherwise specified, the substrate W refers to both the substrate W equivalent to the base material and the anti-etching pattern 100 formed on the base material, and the surface of the substrate W refers to both the surface of the anti-etching pattern 100 and the portion of the surface of the substrate W exposed from the anti-etching pattern 100.

圖3A、圖3B、圖3C、圖3D、圖3E、及圖3F係用於對本發明之一實施方式之抗蝕劑剝離之一例進行說明的概略圖。圖3A~圖3F示出水平觀察基板W之狀態。圖4係用於說明溶解於基板W上之過氧化氫溶液之液滴中之臭氧氣體與過氧化氫溶液中所含之過氧化氫反應而產生羥基自由基的概略圖。圖4中之粗實線係表示抗蝕圖案100與過氧化氫溶液之界面即固液界面111。圖5係表示於硬化層101形成有空洞103之抗蝕圖案100之圖像之一例的鉛直剖視圖。Figures 3A, 3B, 3C, 3D, 3E, and 3F are schematic diagrams illustrating an example of resist stripping according to an embodiment of the present invention. Figures 3A to 3F show a horizontal view of a substrate W. Figure 4 is a schematic diagram illustrating the reaction between ozone gas dissolved in a hydrogen peroxide solution droplet on a substrate W and hydrogen peroxide contained in the hydrogen peroxide solution to generate hydroxyl radicals. The thick solid line in Figure 4 represents the interface between the resist pattern 100 and the hydrogen peroxide solution, namely, the solid-liquid interface 111. Figure 5 is a vertical cross-sectional view showing an example of an image of the resist pattern 100 with voids 103 formed in the hardened layer 101.

如圖3A所示,自基板W除去具有硬化層101之抗蝕圖案100時,以高於室溫(15~30℃內之固定或大致固定之溫度)之剝離促進溫度均勻地加熱基板W,將基板W整體維持在剝離促進溫度。圖3A示出如下之例,即,在使形成有抗蝕圖案100之基板W之表面朝上之狀態下,於發熱之加熱板30之上水平配置基板W,藉由基板W之下表面與加熱板30接觸而以剝離促進溫度均勻地加熱基板W。除了此種基板W之加熱以外或代替此,可藉由高於室溫之溫度之加熱氣體或加熱液與基板W接觸來加熱基板W,亦可藉由對基板W照射自燈等熱源放出之電磁波來加熱基板W。As shown in FIG3A , when removing the anti-etching pattern 100 having the hardened layer 101 from the substrate W, the substrate W is uniformly heated at a peeling-promoting temperature higher than room temperature (constant or substantially constant temperature within the range of 15-30°C), maintaining the entire substrate W at the peeling-promoting temperature. FIG3A illustrates an example in which the substrate W, with the surface of the substrate W having the anti-etching pattern 100 formed thereon facing upward, is horizontally positioned on a heated heating plate 30. The substrate W is uniformly heated at the peeling-promoting temperature by contacting the lower surface of the substrate W with the heating plate 30. In addition to or instead of heating the substrate W in this manner, the substrate W may be heated by contacting a heating gas or a heating liquid having a temperature higher than room temperature with the substrate W, or by irradiating the substrate W with electromagnetic waves emitted from a heat source such as a lamp.

繼而,如圖3B所示,於以剝離促進溫度均勻地加熱水平姿勢之基板W之狀態下,對基板W之表面供給自作為過氧化氫溶液噴嘴之一例之霧噴嘴51A噴出的過氧化氫溶液之霧,使過氧化氫溶液之複數個液滴分散於基板W之表面全域。對基板W供給過氧化氫溶液之霧可藉由對基板W之表面噴射過氧化氫溶液之霧來進行,亦可藉由使過氧化氫溶液之霧擴散於基板W之上方之空間,且使擴散之過氧化氫溶液之霧下落在基板W之表面來進行。亦可藉由該等以外之方法來將過氧化氫溶液之霧供給至基板W之表面。Next, as shown in FIG3B , while the substrate W is uniformly heated at the peeling-promoting temperature in a horizontal position, a mist of hydrogen peroxide solution is supplied from a mist nozzle 51A, which is an example of a hydrogen peroxide solution nozzle, onto the surface of the substrate W, so that a plurality of hydrogen peroxide solution droplets are dispersed over the entire surface of the substrate W. The supply of the hydrogen peroxide solution mist onto the substrate W can be performed by spraying the hydrogen peroxide solution mist onto the surface of the substrate W, or by diffusing the hydrogen peroxide solution mist into the space above the substrate W and allowing the diffused hydrogen peroxide solution mist to fall onto the surface of the substrate W. Alternatively, the hydrogen peroxide solution mist can be supplied to the surface of the substrate W by methods other than these.

過氧化氫溶液之霧係由多個過氧化氫溶液之粒子構成。供給至基板W之過氧化氫溶液之粒子與其他過氧化氫溶液之粒子結合而於基板W之表面上形成過氧化氫溶液之液滴。當繼續供給過氧化氫溶液之霧時,基板W上之過氧化氫溶液之液滴逐漸變大。然而,由於抗蝕圖案100之表面為疏水性,故而並未形成覆蓋基板W之表面全域的過氧化氫溶液之液膜,而是如圖3B所示,相互分開之複數個過氧化氫溶液之液滴分散於基板W之表面全域,僅基板W之表面之一部分被過氧化氫溶液覆蓋。The hydrogen peroxide mist is composed of multiple hydrogen peroxide particles. The hydrogen peroxide particles supplied to the substrate W combine with other hydrogen peroxide particles to form hydrogen peroxide droplets on the surface of the substrate W. As the hydrogen peroxide mist continues to be supplied, the hydrogen peroxide droplets on the substrate W gradually grow larger. However, because the surface of the anti-etching pattern 100 is hydrophobic, a hydrogen peroxide film does not form that covers the entire surface of the substrate W. Instead, as shown in FIG3B , multiple, separate hydrogen peroxide droplets are dispersed across the entire surface of the substrate W, covering only a portion of the surface of the substrate W.

繼而,如圖3C所示,於以剝離促進溫度均勻地加熱水平姿勢之基板W,並且使過氧化氫溶液之複數個液滴分散於基板W之表面全域之狀態下,使臭氧氣體與基板W上之過氧化氫溶液之複數個液滴接觸。例如,藉由一面將收容基板W之熱處理腔室34(參照圖10A及圖10B)內之氣體排出,一面對熱處理腔室34內繼續供給臭氧氣體,從而維持臭氧氣體充滿熱處理腔室34內之狀態,並且對基板W繼續供給新的臭氧氣體。Next, as shown in FIG3C , while the horizontal substrate W is uniformly heated at the peeling-promoting temperature and the plurality of hydrogen peroxide solution droplets are dispersed over the entire surface of the substrate W, ozone gas is brought into contact with the plurality of hydrogen peroxide solution droplets on the substrate W. For example, by exhausting the gas in the heat treatment chamber 34 (see FIG10A and FIG10B ) containing the substrate W while continuously supplying ozone gas into the heat treatment chamber 34, the heat treatment chamber 34 is kept filled with ozone gas, and new ozone gas is continuously supplied to the substrate W.

代替此,亦可在使臭氧氣體充滿熱處理腔室34內之後,停止對熱處理腔室34內供給臭氧氣體,密閉熱處理腔室34之內部。於此情形時,亦可每經過固定時間時,以新的臭氧氣體替換熱處理腔室34內之臭氧氣體。供給至熱處理腔室34內之臭氧氣體可為室溫,亦可為較室溫高之溫度。Alternatively, after the heat treatment chamber 34 is filled with ozone gas, the supply of ozone gas to the heat treatment chamber 34 may be stopped, and the interior of the heat treatment chamber 34 may be sealed. In this case, the ozone gas in the heat treatment chamber 34 may be replaced with new ozone gas at a predetermined interval. The ozone gas supplied to the heat treatment chamber 34 may be at room temperature or a temperature higher than room temperature.

如圖4所示,臭氧氣體溶解於基板W上之過氧化氫溶液中,與過氧化氫溶液中所含之過氧化氫反應。藉此,藉由「O 3+H 2O 2→OH+HO 2+O 2」所示之化學反應而產生羥基自由基(圖4中之「OH」)及過氧化氫自由基(圖4中之「HO 2」)。在過氧化氫溶液之液滴內產生之羥基自由基之一部分在該液滴中擴散,並到達抗蝕圖案100與過氧化氫溶液之界面即固液界面111。亦有在固液界面111產生之羥基自由基。羥基自由基在固液界面111與抗蝕圖案100之硬化層101(參照圖5)反應,以氧化及分解硬化層101。到達非硬化部102(參照圖5)之羥基自由基氧化及分解非硬化部102。藉此,抗蝕圖案100之至少一部分氣化而被自基板W除去。 As shown in Figure 4 , ozone gas dissolves in the hydrogen peroxide solution on substrate W and reacts with the hydrogen peroxide contained in the hydrogen peroxide solution. This generates hydroxyl radicals ("OH" in Figure 4 ) and hydrogen peroxide radicals ("HO" in Figure 4 ) through the chemical reaction "O 3 + H 2 O 2 → OH + HO 2 + O 2 ." Some of the hydroxyl radicals generated within the hydrogen peroxide solution droplet diffuse within the droplet and reach the interface between the resist pattern 100 and the hydrogen peroxide solution, namely, the solid-liquid interface 111. Hydroxyl radicals are also generated at the solid-liquid interface 111. Hydroxyl radicals react with the hardened layer 101 (see FIG. 5 ) of the resist pattern 100 at the solid-liquid interface 111, oxidizing and decomposing the hardened layer 101. Hydroxyl radicals that reach the non-hardened portion 102 (see FIG. 5 ) oxidize and decompose the non-hardened portion 102. As a result, at least a portion of the resist pattern 100 is vaporized and removed from the substrate W.

如上所述,於以剝離促進溫度均勻地加熱水平姿勢之基板W,並且使過氧化氫溶液之複數個液滴分散於基板W之表面全域之狀態下,使臭氧氣體與基板W上之過氧化氫溶液之複數個液滴接觸。藉由加熱基板W,可間接地加熱基板W上之過氧化氫溶液,能夠提高臭氧氣體與過氧化氫之反應性。藉此,能夠增加羥基自由基之總數,能夠增加與硬化層101反應之羥基自由基。As described above, while the horizontal substrate W is uniformly heated at the peeling-promoting temperature and multiple hydrogen peroxide solution droplets are dispersed over the entire surface of the substrate W, ozone gas is brought into contact with the multiple hydrogen peroxide solution droplets on the substrate W. Heating the substrate W indirectly heats the hydrogen peroxide solution on the substrate W, increasing the reactivity between the ozone gas and hydrogen peroxide. This increases the total number of hydroxyl radicals, thereby increasing the number of hydroxyl radicals available to react with the hardened layer 101.

另一方面,當對基板W上之過氧化氫溶液進行加熱時,過氧化氫溶液自基板W蒸發之速度增加。因此,可在停止向基板W供給過氧化氫溶液之霧之後,對基板W補給新的過氧化氫溶液之霧。或者,可在開始供給臭氧氣體之後,亦繼續供給(追加)過氧化氫溶液之霧。圖3D示出基板W上之過氧化氫溶液之液滴變小之狀態,圖3E示出藉由補給過氧化氫溶液之霧,基板W上之過氧化氫溶液之液滴變大之狀態。即便不對基板W上之過氧化氫溶液進行加熱,過氧化氫亦因臭氧氣體與過氧化氫反應而自基板W減少,因此可再次對基板W供給新的過氧化氫溶液之霧以對此進行補償。On the other hand, when the hydrogen peroxide solution on the substrate W is heated, the rate of evaporation of the hydrogen peroxide solution from the substrate W increases. Therefore, after stopping the supply of hydrogen peroxide solution mist to the substrate W, a new hydrogen peroxide solution mist can be supplied to the substrate W. Alternatively, the supply of hydrogen peroxide solution mist can be continued (added) even after the supply of ozone gas begins. Figure 3D shows a state where the hydrogen peroxide solution droplets on the substrate W are reduced in size, while Figure 3E shows a state where the hydrogen peroxide solution droplets on the substrate W are increased in size by the replenishment of hydrogen peroxide solution mist. Even if the hydrogen peroxide solution on the substrate W is not heated, the hydrogen peroxide is reduced from the substrate W due to the reaction between the ozone gas and the hydrogen peroxide. Therefore, a new mist of the hydrogen peroxide solution may be supplied to the substrate W to compensate for this.

圖4係表示基板W上之過氧化氫溶液之液滴之鉛直剖面(以鉛直之平面切斷之剖面)。圖4中之符號112表示臭氧氣體、過氧化氫溶液及抗蝕圖案100之邊界即三態邊界,圖4中之影線區域表示羥基自由基之供給量相對較多之區域。供給至固液界面111之羥基自由基隨著接近三態邊界112而增加。其原因在於:羥基自由基在短時間內會變回過氧化氫,因此若自過氧化氫溶液之液滴或液膜之表面至固液界面111之最短距離較長,則羥基自由基在到達固液界面111之前就會消失。換而言之,於三態邊界112附近,自過氧化氫溶液之液滴或液膜之表面至固液界面111之最短距離較短,羥基自由基容易到達或產生。Figure 4 shows a vertical cross-section (a cross-section cut along a vertical plane) of a hydrogen peroxide solution droplet on a substrate W. Symbol 112 in Figure 4 indicates the boundary between the ozone gas, hydrogen peroxide solution, and the anti-etching pattern 100, namely the three-state boundary. The hatched area in Figure 4 represents a region where the supply of hydroxyl radicals is relatively high. The supply of hydroxyl radicals to the solid-liquid interface 111 increases as it approaches the three-state boundary 112. This is because hydroxyl radicals quickly convert back to hydrogen peroxide. Therefore, if the shortest distance from the surface of the hydrogen peroxide solution droplet or liquid film to the solid-liquid interface 111 is long, the hydroxyl radicals will disappear before reaching the solid-liquid interface 111. In other words, near the three-state boundary 112 , the shortest distance from the surface of the hydrogen peroxide solution droplet or liquid film to the solid-liquid interface 111 is shorter, and hydroxyl radicals can easily reach or be generated.

圖5係表示形成於三態邊界112附近之硬化層101之空洞103之一例。於該例中,3個過氧化氫溶液之液滴中,兩側之2個配置於2個抗蝕圖案100之上,剩餘之1個配置於2個抗蝕圖案100之間。5個空洞103中之3個自兩側之2個過氧化氫溶液之液滴之外周附近向基板W之厚度方向延伸,2個自2個抗蝕圖案100之側面向基板W之面方向(與基板W之厚度方向垂直之方向。在圖5中為紙面之左右方向)延伸。任一空洞103均貫通硬化層101到達非硬化部102。Figure 5 shows an example of a cavity 103 formed in the hardened layer 101 near the three-state boundary 112. In this example, two of the three hydrogen peroxide droplets are placed on the two anti-etching patterns 100, and the remaining one is placed between the two anti-etching patterns 100. Three of the five cavities 103 extend from the periphery of the two hydrogen peroxide droplets in the thickness direction of the substrate W, while two extend from the sides of the two anti-etching patterns 100 in the in-plane direction of the substrate W (a direction perpendicular to the thickness of the substrate W, or horizontally in Figure 5). Each cavity 103 penetrates the hardened layer 101 and reaches the non-hardened portion 102.

如上所述,供給至固液界面111之羥基自由基隨著接近三態邊界112而增加。因此,如圖5所示,於過氧化氫溶液之液滴之外周附近形成空洞103,其後,硬化層101之剩餘部分被羥基自由基分解。向基板W供給臭氧氣體可在經過假定空洞103到達非硬化部102之時間後停止,亦可在經過如下之時間後停止,即,假定硬化層101中與過氧化氫溶液接觸之所有部分被羥基自由基分解。As described above, the number of hydroxyl radicals supplied to the solid-liquid interface 111 increases as the three-state boundary 112 is approached. Consequently, as shown in FIG5 , a cavity 103 is formed near the periphery of the hydrogen peroxide solution droplet, and the remaining portion of the cured layer 101 is subsequently decomposed by the hydroxyl radicals. The supply of ozone gas to the substrate W may be stopped after a time period assuming that the cavity 103 reaches the non-cured portion 102, or after a time period assuming that all portions of the cured layer 101 in contact with the hydrogen peroxide solution are decomposed by the hydroxyl radicals.

如上所述,由於抗蝕圖案100之表面為疏水性,因此當向基板W供給過氧化氫溶液之霧時,並不是形成覆蓋基板W之表面全域的過氧化氫溶液之液膜,而是過氧化氫溶液之複數個液滴分散於基板W之表面全域。然而,在抗蝕圖案100之表面上,與過氧化氫溶液接觸之部分因與過氧化氫溶液或羥基自由基之反應而使得疏水性減弱。在抗蝕圖案100之表面上,未與過氧化氫溶液接觸之部分亦因與臭氧氣體之反應而使得疏水性減弱。因此,當一面繼續向基板W供給新的過氧化氫溶液之霧,或者一面間歇地向基板W補給過氧化氫溶液之霧,一面使臭氧氣體與過氧化氫反應時,抗蝕圖案100之表面之疏水性減弱,基板W上之過氧化氫溶液之複數個液滴變為覆蓋基板W之表面全域的過氧化氫溶液之液膜。As described above, because the surface of the anti-etching pattern 100 is hydrophobic, when a hydrogen peroxide solution mist is supplied to the substrate W, a hydrogen peroxide solution film is not formed that covers the entire surface of the substrate W. Instead, multiple hydrogen peroxide solution droplets are dispersed across the entire surface of the substrate W. However, the hydrophobicity of the portion of the anti-etching pattern 100 that comes into contact with the hydrogen peroxide solution decreases due to reaction with the hydrogen peroxide solution or hydroxyl radicals. The hydrophobicity of the portion of the anti-etching pattern 100 that does not come into contact with the hydrogen peroxide solution also decreases due to reaction with the ozone gas. Therefore, while the substrate W is continuously supplied with a new mist of hydrogen peroxide solution, or while the substrate W is intermittently supplied with a mist of hydrogen peroxide solution, the ozone gas reacts with the hydrogen peroxide, and the hydrophobicity of the surface of the anti-etching pattern 100 is weakened, and the multiple droplets of hydrogen peroxide solution on the substrate W are transformed into a liquid film of hydrogen peroxide solution covering the entire surface of the substrate W.

當過氧化氫溶液之複數個液滴分散於基板W之表面全域時,存在抗蝕圖案100之表面之一部分未與基板W上之過氧化氫溶液接觸之情形。與此相對,當過氧化氫溶液之液膜覆蓋基板W之表面全域時,抗蝕圖案100之表面全域或大致全域與基板W上之過氧化氫溶液接觸。因此,當形成過氧化氫溶液之液膜時,在抗蝕圖案100之表面上供給羥基自由基之範圍擴大,硬化層101中被羥基自由基分解之部分增加。藉此,可藉由羥基自由基分解更多之硬化層101。When multiple droplets of hydrogen peroxide solution are dispersed over the entire surface of substrate W, a portion of the surface of anti-etching pattern 100 may not be in contact with the hydrogen peroxide solution on substrate W. In contrast, when a hydrogen peroxide solution film covers the entire surface of substrate W, the entire or substantially entire surface of anti-etching pattern 100 is in contact with the hydrogen peroxide solution on substrate W. Therefore, when the hydrogen peroxide solution film is formed, the area of the surface of anti-etching pattern 100 that is supplied with hydroxyl radicals expands, and the portion of hardened layer 101 decomposed by hydroxyl radicals increases. Consequently, more hardened layer 101 can be decomposed by hydroxyl radicals.

在藉由羥基自由基分解抗蝕圖案100之硬化層101之至少一部分後,自收容基板W之熱處理腔室34(參照圖10A及圖10B)之內部排出臭氧氣體。進而,待機直至所有之過氧化氫溶液藉由過氧化氫溶液之蒸發而自基板W消失為止,其後,停止對基板W之加熱。此時,可繼續以剝離促進溫度加熱基板W,亦可藉由以高於剝離促進溫度之乾燥溫度加熱基板W,而縮短直至基板W乾燥為止所需之時間。停止對基板W之加熱後,可將基板W強制冷卻至室溫或其附近之溫度。除了加熱基板W以外或代替此,亦可藉由降低氣壓或向基板W供給氣體等其他乾燥方法而自基板W除去過氧化氫溶液。After at least a portion of the hardened layer 101 of the resist pattern 100 is decomposed by hydroxyl radicals, ozone gas is exhausted from the interior of the heat treatment chamber 34 (see Figures 10A and 10B) housing the substrate W. The process then waits until all of the hydrogen peroxide solution has evaporated from the substrate W, after which heating of the substrate W is discontinued. At this point, the substrate W can continue to be heated at the peeling-promoting temperature, or the time required to dry the substrate W can be shortened by heating the substrate W at a drying temperature higher than the peeling-promoting temperature. After terminating heating of the substrate W, the substrate W can be forcefully cooled to room temperature or a temperature near room temperature. In addition to or instead of heating the substrate W, the hydrogen peroxide solution may be removed from the substrate W by other drying methods such as reducing the gas pressure or supplying gas to the substrate W.

繼而,如圖3F所示,將抗蝕劑剝離液供給至基板W之表面而自基板W剝離殘留之抗蝕圖案100。圖3F示出剝離液噴嘴85向旋轉之基板W之上表面(表面)噴出作為抗蝕劑剝離液之一例的SPM(硫酸與過氧化氫溶液之混合液)之例。抗蝕劑剝離液係包含與抗蝕圖案100化學反應之化合物之藥液。抗蝕劑剝離液亦稱為抗蝕劑除去液。抗蝕劑剝離液可為SPM或SC1(氨水、過氧化氫溶液及水之混合液),亦可為該等以外之藥液。Next, as shown in FIG3F , a resist stripping liquid is supplied to the surface of the substrate W to strip the remaining resist pattern 100 from the substrate W. FIG3F shows an example of a stripping liquid nozzle 85 spraying SPM (a mixture of sulfuric acid and hydrogen peroxide solution) as an example of a resist stripping liquid onto the upper surface (surface) of the rotating substrate W. The resist stripping liquid is a liquid containing a compound that chemically reacts with the resist pattern 100. The resist stripping liquid is also called a resist removal liquid. The resist stripping liquid can be SPM or SC1 (a mixture of ammonia, hydrogen peroxide, and water), or other liquids.

於如圖5所示之到達非硬化部102之空洞103形成於硬化層101之情形時,當將抗蝕劑剝離液供給至基板W時,抗蝕劑剝離液與非硬化部102反應,非硬化部102與硬化層101一同被自基板W剝離(舉離)。藉此,抗蝕圖案100被自基板W除去。即便於所有或幾乎所有硬化層101被羥基自由基分解之情形時,抗蝕劑剝離液亦與非硬化部102反應,從而非硬化部102自基板W剝離。因此,若為抗蝕劑剝離液能夠到達非硬化部102之狀態,則即便殘留有硬化層101,藉由供給抗蝕劑剝離液,亦能夠將所有或幾乎所有抗蝕圖案100自基板W除去。When a cavity 103 is formed in the hardened layer 101 by reaching the unhardened portion 102 as shown in FIG5 , when a resist stripping liquid is supplied to the substrate W, the resist stripping liquid reacts with the unhardened portion 102, and the unhardened portion 102 and the hardened layer 101 are both stripped (lifted) from the substrate W. This removes the resist pattern 100 from the substrate W. Even if all or nearly all of the hardened layer 101 is decomposed by hydroxyl radicals, the resist stripping liquid reacts with the unhardened portion 102, and the unhardened portion 102 is stripped from the substrate W. Therefore, if the resist stripping liquid can reach the non-hardened portion 102, even if the hardened layer 101 remains, all or almost all of the resist pattern 100 can be removed from the substrate W by supplying the resist stripping liquid.

對基板W供給抗蝕劑剝離液後,用純水等沖洗液沖洗附著於基板W上之抗蝕劑剝離液,其後,使基板W乾燥。關於向基板W供給抗蝕劑剝離液,可藉由如下方式進行:一面使基板W於水平面內繞通過基板W之中心之鉛直之直線旋轉,一面向基板W之上表面或下表面噴出抗蝕劑剝離液;亦可藉由使基板W浸漬於抗蝕劑剝離液中來進行。向基板W供給沖洗液亦同樣。關於基板W之乾燥,可藉由如下之旋轉乾燥來進行:其係藉由基板W之高速旋轉來使附著於基板W之液體飛散;亦可藉由減壓乾燥等除旋轉乾燥以外之乾燥方法來進行。After applying the resist stripping liquid to the substrate W, the resist stripping liquid adhering to the substrate W is rinsed with a rinse solution such as pure water, and then the substrate W is dried. The resist stripping liquid can be applied to the substrate W by spraying the resist stripping liquid onto the upper or lower surface of the substrate W while rotating the substrate W horizontally about a line passing through the center of the substrate W. Alternatively, the substrate W can be immersed in the resist stripping liquid. The same procedure applies to the rinse solution applied to the substrate W. The substrate W may be dried by spin drying, which involves spinning the substrate W at high speed to disperse the liquid adhering to the substrate W. Alternatively, the substrate may be dried by other drying methods other than spin drying, such as vacuum drying.

如上所述,在臭氧氣體與基板W上之過氧化氫溶液接觸時,以高於室溫之剝離促進溫度均勻地加熱基板W。剝離促進溫度可與預烘烤溫度相等,亦可為高於或低於預烘烤溫度之溫度。同樣地,剝離促進溫度可與後烘烤溫度相等,亦可為高於或低於烘烤溫度之溫度。剝離促進溫度可未達過氧化氫溶液之沸點,亦可未達水之沸點。過氧化氫之沸點為150.2℃。因此,剝離促進溫度可為未達150.2℃,亦可為未達100℃。過氧化氫溶液之濃度可為30~40 wt%(質量百分比濃度),亦可處於該範圍外。30 wt%之過氧化氫溶液之沸點為106℃,35 wt%之過氧化氫溶液之沸點為108℃。As described above, when ozone gas contacts the hydrogen peroxide solution on substrate W, substrate W is uniformly heated at a stripping-promoting temperature above room temperature. The stripping-promoting temperature can be equal to, higher than, or lower than the pre-bake temperature. Similarly, the stripping-promoting temperature can be equal to, higher than, or lower than the post-bake temperature. The stripping-promoting temperature can be lower than the boiling point of the hydrogen peroxide solution or lower than the boiling point of water. The boiling point of hydrogen peroxide is 150.2°C. Therefore, the stripping-promoting temperature can be lower than 150.2°C or lower than 100°C. The concentration of the hydrogen peroxide solution can be between 30 and 40 wt% (mass percent concentration), or outside this range. The boiling point of a 30 wt% hydrogen peroxide solution is 106°C, and the boiling point of a 35 wt% hydrogen peroxide solution is 108°C.

繼而,對本發明之一實施方式之抗蝕劑剝離之另一例進行說明。Next, another example of resist stripping according to one embodiment of the present invention will be described.

圖6A、圖6B、圖6C、及圖6D係用於對本發明之一實施方式之抗蝕劑剝離之另一例進行說明的概略圖。圖6A~圖6D示出水平觀察基板W之狀態。圖7係用於說明如下情況之概略圖,即,溶解於基板W上之過氧化氫溶液之液膜中之臭氧氣體與過氧化氫溶液中所含之過氧化氫反應而產生羥基自由基。Figures 6A, 6B, 6C, and 6D are schematic diagrams illustrating another example of resist stripping according to an embodiment of the present invention. Figures 6A to 6D illustrate a horizontal view of a substrate W. Figure 7 is a schematic diagram illustrating the reaction of ozone gas dissolved in a hydrogen peroxide solution film on substrate W with hydrogen peroxide contained in the hydrogen peroxide solution to generate hydroxyl radicals.

於抗蝕劑剝離之另一例中,與抗蝕劑剝離之一例同樣地,以剝離促進溫度均勻地加熱水平姿勢之基板W。其後,並不是對基板W供給過氧化氫溶液之霧,而是如圖6A所示,使臭氧氣體與基板W之表面全域接觸。接觸之方法與抗蝕劑剝離之一例相同。當臭氧氣體與抗蝕圖案100之表面反應時,水相對於抗蝕圖案100之表面之接觸角減小,抗蝕圖案100之表面之疏水性減弱。藉此,抗蝕圖案100之表面變為親水性。In another example of resist stripping, similar to the first example of resist stripping, a horizontally positioned substrate W is uniformly heated at a stripping-promoting temperature. Subsequently, rather than supplying a mist of hydrogen peroxide solution to substrate W, ozone gas is brought into contact with the entire surface of substrate W, as shown in FIG6A . The contacting method is the same as in the first example of resist stripping. When ozone gas reacts with the surface of resist pattern 100, the contact angle of water with respect to the surface of resist pattern 100 decreases, weakening the hydrophobicity of the surface of resist pattern 100. As a result, the surface of resist pattern 100 becomes hydrophilic.

繼而,於以剝離促進溫度均勻地加熱水平姿勢之基板W之狀態下,對基板W供給過氧化氫溶液,形成覆蓋基板W之表面全域的過氧化氫溶液之液膜。具體而言,與上述之抗蝕劑剝離之一例同樣地,對基板W之表面供給過氧化氫溶液之霧。當繼續供給過氧化氫溶液之霧時,過氧化氫溶液之複數個液滴形成於基板W上,並逐漸變大。由於與臭氧氣體之反應而使得抗蝕圖案100之表面之疏水性減弱,因此並不是過氧化氫溶液之複數個液滴分散於基板W之表面全域,而是該等之液滴在基板W之表面上結合。藉此,形成覆蓋基板W之表面全域的過氧化氫溶液之液膜。Next, while the horizontal substrate W is uniformly heated at the stripping-promoting temperature, a hydrogen peroxide solution is supplied to the substrate W, forming a hydrogen peroxide solution film covering the entire surface of the substrate W. Specifically, similar to the aforementioned anti-etching agent stripping example, a hydrogen peroxide solution mist is supplied to the surface of the substrate W. As the hydrogen peroxide solution mist is continued to be supplied, multiple hydrogen peroxide solution droplets form on the substrate W and gradually grow larger. Due to the reaction with the ozone gas, the hydrophobicity of the surface of the anti-etching pattern 100 is weakened. As a result, the multiple hydrogen peroxide solution droplets are not dispersed across the entire surface of the substrate W, but rather coalesce on the surface of the substrate W. Thereby, a liquid film of the hydrogen peroxide solution covering the entire surface of the substrate W is formed.

在形成過氧化氫溶液之液膜時,除了對基板W之表面供給過氧化氫溶液之霧以外或者代替此,亦可對基板W之表面連續地噴出過氧化氫溶液。具體而言,如圖6B所示,藉由自作為過氧化氫溶液噴嘴之一例之液柱噴嘴51B連續地噴出過氧化氫溶液,而形成自液柱噴嘴51B朝向基板W之表面之中央部流動之、與液柱噴嘴51B相同程度之直徑(例如,直徑為5~20 mm之範圍內)之連續的過氧化氫溶液之液柱,亦可使形成該液柱之過氧化氫溶液與以水平姿勢靜止之基板W之表面的中央部碰撞。When forming a hydrogen peroxide solution film, in addition to or in lieu of supplying a hydrogen peroxide solution mist to the surface of the substrate W, the hydrogen peroxide solution may be continuously sprayed onto the surface of the substrate W. Specifically, as shown in FIG6B , by continuously spraying the hydrogen peroxide solution from a liquid column nozzle 51B, which is an example of a hydrogen peroxide solution nozzle, a continuous liquid column of hydrogen peroxide solution having a diameter approximately the same as that of the liquid column nozzle 51B (e.g., a diameter in the range of 5 to 20 mm) is formed, flowing from the liquid column nozzle 51B toward the center of the surface of the substrate W. The hydrogen peroxide solution forming this liquid column can also be caused to collide with the center of the surface of the substrate W, which is stationary in a horizontal position.

當一面使基板W以水平之姿勢靜止,一面朝向基板W之表面之中央部連續地噴出過氧化氫溶液時,所噴出之過氧化氫溶液與基板W之表面之中央部碰撞,其後,沿著基板W之表面自基板W之表面之中央部放射狀地流動。基板W上之過氧化氫溶液被後續之過氧化氫溶液推著流向外方,自基板W之表面之外周向外方排出。藉此,形成覆蓋基板W之表面全域的過氧化氫溶液之液膜。While holding the substrate W in a horizontal position, hydrogen peroxide solution is continuously sprayed toward the center of the substrate W's surface. The sprayed hydrogen peroxide solution collides with the center of the substrate W's surface and then flows radially from the center along the surface of the substrate W. The hydrogen peroxide solution on the substrate W is pushed outward by subsequent hydrogen peroxide solution and discharged outward from the outer periphery of the substrate W's surface. This forms a hydrogen peroxide solution film covering the entire surface of the substrate W.

向基板W供給過氧化氫溶液亦可一面使基板W以水平之姿勢旋轉一面進行,並非一面使基板W以水平之姿勢靜止一面進行。具體而言,可一面使基板W在水平面內繞通過基板W之中心之鉛直之直線旋轉,一面向基板W之上表面(表面)連續地噴出過氧化氫溶液。於該情形時,由於基板W之旋轉產生之離心力施加至基板W上之過氧化氫溶液,因此能夠縮短形成覆蓋基板W之表面全域的過氧化氫溶液之液膜所需之時間。The supply of hydrogen peroxide solution to the substrate W can also be performed while the substrate W is rotated in a horizontal position, rather than while the substrate W is stationary in a horizontal position. Specifically, the substrate W can be rotated in a horizontal plane about a straight line passing through the center of the substrate W while the hydrogen peroxide solution is continuously sprayed onto the upper surface (surface) of the substrate W. In this case, the centrifugal force generated by the rotation of the substrate W applies to the hydrogen peroxide solution on the substrate W, thereby shortening the time required to form a hydrogen peroxide solution film covering the entire surface of the substrate W.

相較於僅對基板W之表面供給過氧化氫溶液之霧之情形,藉由朝向基板W之表面連續地噴出過氧化氫溶液,能夠在短時間內形成覆蓋基板W之表面全域的過氧化氫溶液之液膜。於一面使基板W以水平之姿勢旋轉,一面朝向基板W之表面連續地噴出過氧化氫溶液之情形時,藉由控制所噴出之過氧化氫溶液之流量及基板W之旋轉速度,可形成較薄之過氧化氫溶液之液膜。於對基板W供給過氧化氫溶液之霧之情形時,可形成較朝向基板W之表面連續地噴出過氧化氫溶液之情形薄的過氧化氫溶液之液膜。Compared to simply supplying a hydrogen peroxide solution mist onto the surface of the substrate W, continuously spraying the hydrogen peroxide solution onto the surface of the substrate W allows a hydrogen peroxide solution film to be formed covering the entire surface of the substrate W in a shorter time. When the hydrogen peroxide solution is continuously sprayed onto the surface of the substrate W while the substrate W is rotated in a horizontal position, a thinner hydrogen peroxide solution film can be formed by controlling the flow rate of the sprayed hydrogen peroxide solution and the rotation speed of the substrate W. When supplying a hydrogen peroxide solution mist onto the substrate W, a thinner hydrogen peroxide solution film can be formed than when the hydrogen peroxide solution is continuously sprayed onto the surface of the substrate W.

在形成覆蓋基板W之表面全域的過氧化氫溶液之液膜後,可停止亦可繼續向基板W供給過氧化氫溶液之霧。於前者之情形時,可在自停止供給過氧化氫溶液之霧起經過固定時間後,重新開始向基板W供給過氧化氫溶液之霧。同樣地,在形成覆蓋基板W之表面全域的過氧化氫溶液之液膜後,可停止亦可繼續自液柱噴嘴51B噴出過氧化氫溶液。於前者之情形時,可在自停止噴出過氧化氫溶液起經過固定時間後,重新開始噴出過氧化氫溶液。After forming a liquid film of hydrogen peroxide solution covering the entire surface of the substrate W, the supply of hydrogen peroxide solution mist to the substrate W may be stopped or continued. In the former case, the supply of hydrogen peroxide solution mist to the substrate W may be resumed after a predetermined time has elapsed since the supply of hydrogen peroxide solution mist was stopped. Similarly, after forming a liquid film of hydrogen peroxide solution covering the entire surface of the substrate W, the spraying of hydrogen peroxide solution from the liquid column nozzle 51B may be stopped or continued. In the former case, the spraying of hydrogen peroxide solution may be resumed after a predetermined time has elapsed since the spraying of hydrogen peroxide solution was stopped.

繼而,如圖6C所示,於以剝離促進溫度均勻地加熱水平姿勢之基板W,並且基板W之表面全域被過氧化氫溶液之液膜覆蓋之狀態下,使臭氧氣體與基板W上之過氧化氫溶液之液膜接觸。向基板W供給臭氧氣體可自對抗蝕圖案100之表面進行親水化時起繼續進行,亦可在形成過氧化氫溶液之液膜後重新開始。於後者之情形時,可在形成過氧化氫溶液之液膜之前,自熱處理腔室34之內部排出臭氧氣體。Next, as shown in FIG6C , after the horizontal substrate W is uniformly heated at the peeling-promoting temperature and the entire surface of the substrate W is covered by the hydrogen peroxide film, ozone gas is brought into contact with the hydrogen peroxide film on the substrate W. The supply of ozone gas to the substrate W may continue from the time the surface of the resist pattern 100 is hydrophilized, or it may be resumed after the hydrogen peroxide film is formed. In the latter case, ozone gas may be exhausted from the interior of the heat treatment chamber 34 before the hydrogen peroxide film is formed.

當臭氧氣體與基板W上之過氧化氫溶液接觸時,與抗蝕劑剝離之一例同樣地,藉由臭氧氣體與過氧化氫之反應而產生羥基自由基,分解抗蝕圖案100之硬化層101(參照圖5)。藉此,到達非硬化部102(參照圖5)之空洞103(參照圖5)形成於硬化層101上。向基板W供給臭氧氣體可在到達非硬化部102之空洞103形成於硬化層101之時刻停止,亦可繼續直至所有或幾乎所有之硬化層101被羥基自由基分解為止。When ozone gas comes into contact with the hydrogen peroxide solution on the substrate W, similar to the resist stripping example, the ozone gas reacts with the hydrogen peroxide to generate hydroxyl radicals, which decompose the hardened layer 101 of the resist pattern 100 (see FIG. 5 ). Consequently, cavities 103 (see FIG. 5 ) that reach the non-hardened portion 102 (see FIG. 5 ) are formed in the hardened layer 101. The supply of ozone gas to the substrate W may be stopped when the cavities 103 that reach the non-hardened portion 102 are formed in the hardened layer 101, or may be continued until all or nearly all of the hardened layer 101 is decomposed by the hydroxyl radicals.

如圖6C及圖7所示,自過氧化氫溶液之液膜之表面至抗蝕圖案100與過氧化氫溶液之界面即固液界面111之最短距離除過氧化氫溶液之液膜之外周部以外為固定或大致固定。因此,能夠將羥基自由基均勻地供給至固液界面111,能夠在基板W之表面全域均勻地剝離抗蝕圖案100。另一方面,若過氧化氫溶液之液膜之厚度較大,則到達固液界面111之羥基自由基減少。因此,較佳為儘量減少過氧化氫溶液之液膜之厚度(膜厚)。As shown in Figures 6C and 7 , the shortest distance from the surface of the hydrogen peroxide film to the interface between the anti-etching pattern 100 and the hydrogen peroxide solution, i.e., the solid-liquid interface 111, is constant or substantially constant except at the periphery of the hydrogen peroxide film. Therefore, hydroxyl radicals can be uniformly supplied to the solid-liquid interface 111, enabling uniform stripping of the anti-etching pattern 100 across the entire surface of the substrate W. On the other hand, if the hydrogen peroxide film is thicker, fewer hydroxyl radicals will reach the solid-liquid interface 111. Therefore, it is preferable to minimize the thickness of the hydrogen peroxide film.

在停止向基板W供給臭氧氣體後,與抗蝕劑剝離之一例同樣地使基板W乾燥。其後,如圖6D所示,對基板W供給抗蝕劑剝離液,將抗蝕圖案100自基板W除去。圖6D示出如下例子,即,剝離液噴嘴85向旋轉之基板W之上表面(表面)噴出作為抗蝕劑剝離液之一例的SPM。After stopping the supply of ozone gas to the substrate W, the substrate W is dried in the same manner as in the resist stripping process. Subsequently, as shown in FIG6D , a resist stripping liquid is supplied to the substrate W to remove the resist pattern 100 from the substrate W. FIG6D illustrates an example in which the stripping liquid nozzle 85 sprays SPM, an example of a resist stripping liquid, onto the upper surface (surface) of the rotating substrate W.

如上所述,於抗蝕劑剝離之2個例子中,進行抗蝕劑剝離步驟,其係藉由對基板W之表面供給臭氧氣體及過氧化氫溶液,而將抗蝕圖案100之至少一部分自基板W之表面剝離。其後,進行對基板W之表面供給抗蝕劑剝離液之殘留抗蝕劑剝離步驟。即便在進行抗蝕劑剝離步驟後基板W之表面殘留有抗蝕劑,亦可藉由抗蝕劑剝離液將殘留之抗蝕劑自基板W之表面剝離。藉此,能夠將所有抗蝕劑自基板W除去。或者,能夠減少殘留於基板W之抗蝕劑。As described above, in the two examples of resist stripping, a resist stripping step is performed by supplying ozone gas and hydrogen peroxide solution to the surface of the substrate W to strip at least a portion of the resist pattern 100 from the surface of the substrate W. Subsequently, a residual resist stripping step is performed by supplying a resist stripping solution to the surface of the substrate W. Even if residual resist remains on the surface of the substrate W after the resist stripping step, the residual resist can be stripped from the surface of the substrate W using the resist stripping solution. In this way, all resist can be removed from the substrate W. Alternatively, the amount of resist remaining on the substrate W can be reduced.

圖8係表示本發明之一實施方式之基板處理裝置1之佈局的概略俯視圖。FIG8 is a schematic top view showing the layout of a substrate processing apparatus 1 according to an embodiment of the present invention.

基板處理裝置1係逐片處理基板W之單片式裝置。基板W例如為半導體晶圓等。基板處理裝置1包括:複數個裝載埠LP,其分別保持收容基板W之複數個載具C;及複數個處理單元2,其用處理液、處理氣體等處理流體對自複數個裝載埠LP搬送來之基板W進行處理。The substrate processing apparatus 1 is a single-wafer device that processes substrates W one by one. Substrates W are, for example, semiconductor wafers. The substrate processing apparatus 1 includes a plurality of loading ports LP, each of which holds a plurality of carriers C that accommodate substrates W, and a plurality of processing units 2, which process the substrates W transferred from the loading ports LP using processing fluids such as processing liquids and processing gases.

基板處理裝置1進而包括搬送基板W之搬送單元(IR、SH、CR)、及控制基板處理裝置1之控制裝置(控制器)3。控制裝置3典型地為電腦,包括:記憶體3m,其記憶程式等資訊;及處理器3p,其根據記憶體3m中記憶之資訊來控制基板處理裝置1。The substrate processing apparatus 1 further includes transport units (IR, SH, CR) for transporting substrates W, and a control device (controller) 3 for controlling the substrate processing apparatus 1. The control device 3 is typically a computer and includes a memory 3m for storing information such as programs, and a processor 3p for controlling the substrate processing apparatus 1 based on the information stored in the memory 3m.

搬送單元(IR、SH、CR)包括配置於自複數個裝載埠LP延伸至複數個處理單元2之搬送路徑上之分度機械手IR、梭子SH及中心機械手CR。分度機械手IR在複數個裝載埠LP與梭子SH之間搬送基板W。梭子SH在分度機械手IR與中心機械手CR之間往復移動而搬送基板W。中心機械手CR在梭子SH與複數個處理單元2之間搬送基板W。中心機械手CR進而在複數個處理單元2之間搬送基板W。圖8所示之粗實線之箭頭表示分度機械手IR及梭子SH之移動方向。The transport units (IR, SH, CR) include an indexing robot IR, a shuttle SH, and a center robot CR, which are arranged on a transport path extending from a plurality of loading ports LP to a plurality of processing units 2. The indexing robot IR transports substrates W between the plurality of loading ports LP and the shuttle SH. The shuttle SH reciprocates between the indexing robot IR and the center robot CR to transport substrates W. The center robot CR transports substrates W between the shuttle SH and a plurality of processing units 2. The center robot CR, in turn, transports substrates W between the plurality of processing units 2. The thick solid arrows shown in FIG8 indicate the movement directions of the indexing robot IR and the shuttle SH.

複數個處理單元2形成分別配置於水平上分開之4個位置之4個塔。各塔包括於上下方向上積層之複數個處理單元2。4個塔兩個兩個地配置於搬送路徑之兩側。複數個處理單元2包括:複數個前處理單元2D,其等一面對基板W進行加熱或冷卻一面進行處理;及複數個後處理單元2W,其等用處理液對經複數個前處理單元2D處理之基板W進行處理。裝載埠LP側之2個塔由複數個前處理單元2D形成,剩餘之2個塔由複數個後處理單元2W形成。The processing units 2 form four towers, each arranged at four horizontally spaced locations. Each tower includes a plurality of processing units 2 stacked vertically. The four towers are arranged two by two on either side of the transport path. The processing units 2 include: a plurality of pre-processing units 2D, which process substrates W while heating or cooling them; and a plurality of post-processing units 2W, which use a processing liquid to treat the substrates W processed by the pre-processing units 2D. The two towers on the loading port LP side are formed by the pre-processing units 2D, and the remaining two towers are formed by the post-processing units 2W.

繼而,對前處理單元2D進行說明。Next, the 2D pre-processing unit is explained.

圖9係表示前處理單元2D之鉛直剖面之一例之剖視圖。圖10A係表示熱處理單元8之鉛直剖面之一例之剖視圖。圖10B係表示熱處理單元8之鉛直剖面之另一例之剖視圖。於以下之說明中,「線路」係指由配管、閥等流體機器所形成之流路。例如,氣體供給線路49相當於用於供給氣體之流路。Figure 9 is a cross-sectional view showing an example of a vertical cross-section of pre-treatment unit 2D. Figure 10A is a cross-sectional view showing an example of a vertical cross-section of heat treatment unit 8. Figure 10B is a cross-sectional view showing another example of a vertical cross-section of heat treatment unit 8. In the following description, "line" refers to a flow path formed by fluid devices such as piping and valves. For example, gas supply line 49 corresponds to a flow path for supplying gas.

前處理單元2D包括:腔室4,其設置有供基板W通過之搬入搬出口4a;擋板5,其開閉腔室4之搬入搬出口4a;熱處理單元8,其一面於腔室4內加熱基板W,一面將處理液、處理氣體等處理流體供給至基板W;冷卻單元7,其在腔室4內對經熱處理單元8加熱之基板W進行冷卻;室內搬送機構6,其在腔室4內搬送基板W。中心機械手CR經由搬入搬出口4a將基板W搬入搬出於腔室4。於搬入搬出口4a之附近之腔室4內配置有冷卻單元7。The pre-processing unit 2D includes a chamber 4 with a loading/unloading port 4a through which substrates W pass; a shutter 5 that opens and closes the loading/unloading port 4a; a thermal treatment unit 8 that heats the substrates W within the chamber 4 while supplying processing fluids such as a processing liquid and a processing gas to the substrates W; a cooling unit 7 that cools the substrates W heated by the thermal treatment unit 8 within the chamber 4; and an in-chamber transfer mechanism 6 that transfers the substrates W within the chamber 4. The central robot CR transfers substrates W into and out of the chamber 4 through the loading/unloading port 4a. The cooling unit 7 is located within the chamber 4 near the loading/unloading port 4a.

冷卻單元7包括冷卻板20、貫通冷卻板20而上下移動之頂起銷22、及使頂起銷22上下移動之銷升降驅動機構23。冷卻板20具備載置基板W之冷卻面20a。冷卻板20之內部形成有冷媒(典型地為冷卻水)循環之冷媒路徑(省略圖示)。頂起銷22於在較冷卻面20a更上方支持基板W之上位置與前端沒入於較冷卻面20a更下方之下位置之間上下移動。The cooling unit 7 includes a cooling plate 20, lifting pins 22 that extend through the cooling plate 20 and move vertically, and a pin-lifting drive mechanism 23 that moves the lifting pins 22 vertically. The cooling plate 20 includes a cooling surface 20a on which substrates W are placed. A cooling medium path (not shown) circulates a coolant (typically cooling water) within the cooling plate 20. The lifting pins 22 move vertically between an upper position, where they support the substrates W, and a lower position, where their tips are submerged below the cooling surface 20a.

熱處理單元8具備加熱器33。更具體而言,熱處理單元8包括加熱板30、收容加熱板30之熱處理腔室34、貫通加熱板30而上下移動之頂起銷38、及使頂起銷38上下移動之銷升降驅動機構39。加熱板30具備載置基板W之加熱面30a,內藏有加熱器33。Heat treatment unit 8 includes a heater 33. More specifically, heat treatment unit 8 comprises a heating plate 30, a heat treatment chamber 34 that houses heating plate 30, lift pins 38 that extend through heating plate 30 and move up and down, and a pin lift drive mechanism 39 that moves lift pins 38 up and down. Heating plate 30 includes a heating surface 30a on which substrate W is placed and houses heater 33.

加熱器33構成為能夠以高於室溫之固定溫度對配置於加熱面30a之基板W進行加熱,例如可構成為能夠將基板W加熱至250℃。加熱面30a仿照基板W之形狀,具有較基板W大一圈之平面形狀。具體而言,若基板W為圓形,則加熱面30a形成為較基板W大一圈之圓形。The heater 33 is configured to heat the substrate W placed on the heating surface 30a at a constant temperature above room temperature, for example, up to 250°C. The heating surface 30a follows the shape of the substrate W, having a planar shape slightly larger than the substrate W. Specifically, if the substrate W is circular, the heating surface 30a is formed into a circular shape slightly larger than the substrate W.

熱處理腔室34具備腔室本體35、及在腔室本體35之上方上下移動之蓋36。熱處理單元8具備升降蓋36之蓋升降驅動機構37。腔室本體35具有向上方開放之開口35a,蓋36開閉該開口35a。蓋36在堵塞腔室本體35之開口35a而於熱處理腔室34之內部形成密閉處理空間的關閉位置(下位置)與向上方退避以打開開口35a之上位置之間上下移動。頂起銷38於在較加熱面30a更上方支持基板W之上位置與前端沒入於較加熱面30a更下方的下位置之間上下移動。The heat treatment chamber 34 includes a chamber body 35 and a lid 36 that moves up and down above the chamber body 35. The heat treatment unit 8 includes a lid lift drive mechanism 37 that lifts and lowers the lid 36. The chamber body 35 has an opening 35a that opens upward, and the lid 36 opens and closes the opening 35a. The lid 36 moves up and down between a closed position (lower position) in which it blocks the opening 35a of the chamber body 35 and forms a sealed processing space within the heat treatment chamber 34, and an upper position in which it retracts upward to open the opening 35a. The lift pin 38 moves up and down between an upper position in which it supports the substrate W above the heating surface 30a and a lower position in which its tip is submerged below the heating surface 30a.

於腔室本體35之底部形成有排氣埠41。排氣埠41較佳為在圓周方向上隔開間隔地配置於複數個部位(例如3個部位)。排氣埠41經由排氣線路42連接於排氣設備。An exhaust port 41 is formed at the bottom of the chamber body 35. The exhaust ports 41 are preferably arranged at multiple locations (e.g., three locations) spaced apart in the circumferential direction. The exhaust ports 41 are connected to an exhaust device via an exhaust line 42.

蓋36包括與加熱面30a平行地延伸之板部45及自板部45之周緣向下方延伸之筒部46。板部45具體而言為大致圓形,筒部46具有圓筒形狀。筒部46之下端與腔室本體35之上端對向。藉此,可藉由蓋36之上下移動而開閉腔室本體35之開口35a。The lid 36 comprises a plate portion 45 extending parallel to the heating surface 30a and a cylindrical portion 46 extending downward from the periphery of the plate portion 45. Specifically, the plate portion 45 is generally circular, while the cylindrical portion 46 is cylindrical. The lower end of the cylindrical portion 46 faces the upper end of the chamber body 35. Thus, the opening 35a of the chamber body 35 can be opened and closed by moving the lid 36 up and down.

如圖10A所示,朝向基板W之上表面噴射過氧化氫溶液之霧之霧噴嘴51A、及朝向基板W之上表面噴射臭氧氣體之臭氧噴嘴55安裝於蓋36。圖10A示出如下例子,即,霧噴嘴51A及臭氧噴嘴55插入於上下貫通蓋36之板部45之2個孔中。霧噴嘴51A及臭氧噴嘴55相對於蓋36之位置不限於該例。As shown in FIG10A , a mist nozzle 51A for spraying a hydrogen peroxide solution mist toward the upper surface of substrate W and an ozone nozzle 55 for spraying ozone gas toward the upper surface of substrate W are mounted on cover 36 . FIG10A illustrates an example in which mist nozzle 51A and ozone nozzle 55 are inserted into two holes in plate portion 45 extending vertically through cover 36 . The positions of mist nozzle 51A and ozone nozzle 55 relative to cover 36 are not limited to this example.

霧噴嘴51A連接於過氧化氫溶液線路52,該過氧化氫溶液線路52將過氧化氫溶液自過氧化氫溶液供給源54引導至霧噴嘴51A。過氧化氫溶液閥53配置於過氧化氫溶液線路52上。當控制裝置3打開過氧化氫溶液閥53時,過氧化氫溶液被供給至霧噴嘴51A,霧噴嘴51A噴出過氧化氫溶液之霧。當控制裝置3關閉過氧化氫溶液閥53時,停止向霧噴嘴51A供給過氧化氫溶液,並停止自霧噴嘴51A噴出過氧化氫溶液之霧。Mist nozzle 51A is connected to a hydrogen peroxide solution line 52, which directs hydrogen peroxide solution from a hydrogen peroxide solution supply source 54 to mist nozzle 51A. A hydrogen peroxide solution valve 53 is disposed on hydrogen peroxide solution line 52. When control device 3 opens hydrogen peroxide solution valve 53, hydrogen peroxide solution is supplied to mist nozzle 51A, and mist nozzle 51A sprays hydrogen peroxide solution mist. When control device 3 closes hydrogen peroxide solution valve 53, the supply of hydrogen peroxide solution to mist nozzle 51A ceases, and the spraying of hydrogen peroxide solution mist from mist nozzle 51A stops.

臭氧噴嘴55連接於臭氧線路56,該臭氧線路56將臭氧氣體自臭氧產生器58引導至臭氧噴嘴55。臭氧閥57配置於臭氧線路56上。當控制裝置3打開臭氧閥57時,臭氧氣體被供給至臭氧噴嘴55,臭氧噴嘴55噴出臭氧氣體。當控制裝置3關閉臭氧閥57時,停止向臭氧噴嘴55供給臭氧氣體,並停止自臭氧噴嘴55噴出臭氧氣體。The ozone nozzle 55 is connected to an ozone line 56, which directs ozone gas from an ozone generator 58 to the ozone nozzle 55. An ozone valve 57 is disposed on the ozone line 56. When the control device 3 opens the ozone valve 57, ozone gas is supplied to the ozone nozzle 55, and the ozone nozzle 55 begins to discharge ozone gas. When the control device 3 closes the ozone valve 57, the supply of ozone gas to the ozone nozzle 55 ceases, and ozone gas discharge from the ozone nozzle 55 also ceases.

在霧噴嘴51A及臭氧噴嘴55與加熱板30上之基板W之間配置有簇射板59。自霧噴嘴51A噴出之過氧化氫溶液之霧在簇射板59與蓋36之間之空間中擴散,並通過貫通簇射板59之複數個孔。藉此,過氧化氫溶液之霧被均勻地供給至加熱板30上之基板W之上表面。同樣地,自臭氧噴嘴55噴出之臭氧氣體在簇射板59與蓋36之間之空間中擴散,並通過貫通簇射板59之複數個孔。藉此,臭氧氣體被均勻地供給至加熱板30上之基板W之上表面。A shower plate 59 is positioned between the mist nozzle 51A and the ozone nozzle 55 and the substrate W on the heating plate 30. The hydrogen peroxide solution mist sprayed from the mist nozzle 51A diffuses in the space between the shower plate 59 and the lid 36 and passes through the plurality of holes extending through the shower plate 59. This uniformly supplies the hydrogen peroxide solution mist to the upper surface of the substrate W on the heating plate 30. Similarly, the ozone gas sprayed from the ozone nozzle 55 diffuses in the space between the shower plate 59 and the lid 36 and passes through the plurality of holes extending through the shower plate 59. This uniformly supplies the ozone gas to the upper surface of the substrate W on the heating plate 30.

如圖10B所示,熱處理單元8亦可代替霧噴嘴51A或除霧噴嘴51A之外,具備連續地噴出過氧化氫溶液之液柱噴嘴51B。於該情形時,較佳為省略簇射板59。進而,液柱噴嘴51B較佳為朝向加熱板30上之基板W之上表面之中央部噴出過氧化氫溶液。可將自排氣線路42內之排氣中分離液體之氣液分離器60配置於排氣設備之上游。As shown in Figure 10B, heat treatment unit 8 may also include a liquid column nozzle 51B that continuously sprays hydrogen peroxide solution, instead of or in addition to mist nozzle 51A. In this case, shower plate 59 is preferably omitted. Furthermore, liquid column nozzle 51B preferably sprays hydrogen peroxide solution toward the center of the upper surface of substrate W on heating plate 30. A gas-liquid separator 60, which separates liquid from the exhaust gas in exhaust line 42, may be positioned upstream of the exhaust system.

當控制裝置3打開過氧化氫溶液閥53時,過氧化氫溶液被供給至液柱噴嘴51B,液柱噴嘴51B開始噴出過氧化氫溶液。藉此,形成自液柱噴嘴51B至基板W之上表面連續之過氧化氫溶液之液柱。與基板W之上表面之中央部碰撞之過氧化氫溶液沿著基板W之上表面向外方流動,而自基板W之上表面之外周部向外方排出。當控制裝置3關閉過氧化氫溶液閥53時,停止向液柱噴嘴51B供給過氧化氫溶液,並停止自液柱噴嘴51B噴出過氧化氫溶液。When the control device 3 opens the hydrogen peroxide solution valve 53, hydrogen peroxide solution is supplied to the liquid column nozzle 51B, and the liquid column nozzle 51B begins to spray hydrogen peroxide solution. This forms a continuous liquid column of hydrogen peroxide solution from the liquid column nozzle 51B to the upper surface of the substrate W. The hydrogen peroxide solution collides with the center of the upper surface of the substrate W and flows outward along the upper surface of the substrate W, and is discharged outward from the outer periphery of the upper surface of the substrate W. When the control device 3 closes the hydrogen peroxide solution valve 53, the supply of hydrogen peroxide solution to the liquid column nozzle 51B and the spraying of hydrogen peroxide solution from the liquid column nozzle 51B cease.

如圖9所示,室內搬送機構6在腔室4之內部搬送基板W。更具體而言,室內搬送機構6具備在冷卻單元7與熱處理單元8之間搬送基板W之室內搬送手6H。室內搬送手6H構成為能夠在與冷卻單元7之頂起銷22之間接收基板W,且能夠在與熱處理單元8之頂起銷38之間接收基板W。藉此,室內搬送手6H自冷卻單元7之頂起銷22接收基板W,並將該基板W交遞至熱處理單元8之頂起銷38。進而,室內搬送手6H自熱處理單元8之頂起銷38接收基板W,並將該基板W交遞至冷卻單元7之頂起銷22。As shown in FIG9 , the indoor transfer mechanism 6 transfers substrates W within the chamber 4 . More specifically, the indoor transfer mechanism 6 includes an indoor transfer hand 6H for transferring substrates W between the cooling unit 7 and the thermal treatment unit 8 . The indoor transfer hand 6H is configured to receive substrates W between the lifting pins 22 of the cooling unit 7 and the lifting pins 38 of the thermal treatment unit 8 . Thus, the indoor transfer hand 6H receives substrates W from the lifting pins 22 of the cooling unit 7 and transfers them to the lifting pins 38 of the thermal treatment unit 8 . Furthermore, the indoor transfer hand 6H receives substrates W from the lifting pins 38 of the thermal treatment unit 8 and transfers them to the lifting pins 22 of the cooling unit 7 .

前處理單元2D之典型動作如下所述。Typical actions of the 2D pre-processing unit are described below.

於中心機械手CR(參照圖8)將基板W搬入腔室4時,擋板5被控制在打開搬入搬出口4a之打開位置。於該狀態下,中心機械手CR之手H進入腔室4,將基板W配置於冷卻板20之上方。於是,頂起銷22上升至上位置,自中心機械手CR之手H接收基板W。其後,中心機械手CR之手H後退至腔室4外。繼而,室內搬送機構6之室內搬送手6H自頂起銷22接收基板W,並將基板W搬送至熱處理單元8之頂起銷38。此時,蓋36處於打開位置(上位置),頂起銷38在上位置支持所接收之基板W。於室內搬送手6H自熱處理腔室34退避後,頂起銷38下降至下位置,將基板W載置於加熱面30a上。另一方面,蓋36下降至關閉位置(下位置),形成收容加熱板30之密閉處理空間。於該狀態下,進行對基板W之熱處理。When the central robot CR (see FIG8 ) carries the substrate W into the chamber 4, the baffle 5 is controlled to be in the open position to open the loading and unloading port 4a. In this state, the hand H of the central robot CR enters the chamber 4 and places the substrate W above the cooling plate 20. Then, the lifting pin 22 rises to the upper position and receives the substrate W from the hand H of the central robot CR. Thereafter, the hand H of the central robot CR retreats to the outside of the chamber 4. Subsequently, the indoor transfer hand 6H of the indoor transfer mechanism 6 receives the substrate W from the lifting pin 22 and transfers the substrate W to the lifting pin 38 of the heat treatment unit 8. At this time, the cover 36 is in the open position (upper position), and the lifting pin 38 supports the received substrate W in the upper position. After the indoor transfer arm 6H retreats from the heat treatment chamber 34, the lift pins 38 descend to their lower positions, placing the substrate W on the heating surface 30a. Meanwhile, the lid 36 descends to its closed position (lower position), creating a sealed processing chamber that houses the heating plate 30. In this state, the substrate W undergoes heat treatment.

當結束熱處理時,蓋36上升至打開位置(上位置)而將熱處理腔室34打開。進而,頂起銷38上升至上位置,將基板W上推至加熱面30a之上方。於該狀態下,室內搬送機構6之室內搬送手6H自頂起銷38接收基板W,並將該基板W搬送至冷卻單元7之頂起銷22。頂起銷22在上位置支持所接收之基板W。等待室內搬送手6H退避而頂起銷22下降至下位置,藉此,基板W載置於冷卻板20之冷卻面20a上。藉此,冷卻基板W。When the heat treatment is complete, the lid 36 rises to the open position (upper position), opening the heat treatment chamber 34. Furthermore, the lift pins 38 rise to the upper position, pushing the substrate W above the heating surface 30a. In this state, the indoor transfer hand 6H of the indoor transfer mechanism 6 receives the substrate W from the lift pins 38 and transfers it to the lift pins 22 of the cooling unit 7. The lift pins 22 support the received substrate W in the upper position. The indoor transfer hand 6H retreats, and the lift pins 22 descend to the lower position, placing the substrate W on the cooling surface 20a of the cooling plate 20. This cools the substrate W.

當結束基板W之冷卻時,頂起銷22上升至上位置,藉此將基板W上推至冷卻面20a之上方。於該狀態下,擋板5被打開,中心機械手CR之手H進入腔室4,配置在由位於上位置之頂起銷22支持之基板W之下方。於該狀態下,藉由頂起銷22下降而將基板W交遞至中心機械手CR之手H。保持基板W之手H退避至腔室4外,其後,擋板5將搬入搬出口4a關閉。When cooling of the substrate W is complete, the lift pins 22 rise to their upper positions, pushing the substrate W above the cooling surface 20a. In this state, the shutter 5 opens, and the hand H of the central robot CR enters the chamber 4 and is positioned beneath the substrate W, which is supported by the lift pins 22 in the upper position. In this state, the lift pins 22 descend, transferring the substrate W to the hand H of the central robot CR. The hand H, holding the substrate W, retreats outside the chamber 4, and the shutter 5 closes the load/unload port 4a.

圖11係表示後處理單元2W之鉛直剖面之一例之剖視圖。FIG11 is a cross-sectional view showing an example of a vertical cross section of the post-processing unit 2W.

後處理單元2W係逐片處理基板W之單片式液體處理單元。後處理單元2W包括:劃分內部空間之箱形之腔室9(參照圖8);旋轉夾盤70(基板保持機構、基板保持器),其係於腔室9內以水平姿勢保持一片基板W,使基板W繞通過基板W之中心之鉛直之旋轉軸線A1旋轉;剝離液供給單元71,其將作為抗蝕劑剝離液之一之SPM供給至保持於旋轉夾盤70之基板W;沖洗液供給單元72;及包圍旋轉夾盤70之筒狀杯73。如圖8所示,腔室9形成有供基板W通過之搬入搬出口9a,且具備開閉該搬入搬出口9a之擋板10。腔室9係於其內部進行使用處理液之基板處理之液體處理腔室之一例。The post-processing unit 2W is a single-wafer liquid processing unit that processes substrates W one by one. It comprises a box-shaped chamber 9 (see Figure 8 ) with a divided interior; a rotary chuck 70 (substrate holding mechanism, substrate holder) that holds a substrate W horizontally within the chamber 9 and rotates it about a linear axis A1 passing through the center of the substrate W; a stripping liquid supply unit 71 that supplies SPM, a type of resist stripping liquid, to the substrate W held on the rotary chuck 70; a rinse liquid supply unit 72; and a cylindrical cup 73 surrounding the rotary chuck 70. 8, the chamber 9 is formed with a loading/unloading port 9a for passing the substrate W, and is provided with a shutter 10 for opening and closing the loading/unloading port 9a. The chamber 9 is an example of a liquid processing chamber in which substrate processing using a processing liquid is performed.

旋轉夾盤70包括:以水平姿勢保持之圓板狀之旋轉基座74;複數個夾盤銷75,其等在旋轉基座74之上方以水平姿勢保持基板W;自旋轉基座74之中央部向下方延伸之旋轉軸76;旋轉馬達77,其藉由使旋轉軸76旋轉而使基板W及旋轉基座74繞旋轉軸線A1旋轉。旋轉夾盤70不限於使複數個夾盤銷75與基板W之周端面接觸之夾持式夾盤,亦可為真空式夾盤,該真空式夾盤藉由使作為非裝置形成面之基板W之背面(下表面)吸附於旋轉基座74之上表面而將基板W保持為水平。 The rotary chuck 70 includes a circular rotating base 74 that holds the substrate W horizontally; a plurality of chuck pins 75 that hold the substrate W horizontally above the rotating base 74; a rotation shaft 76 that extends downward from the center of the rotating base 74; and a rotary motor 77 that rotates the rotation shaft 76 to rotate the substrate W and the rotating base 74 about a rotation axis A1. The rotary chuck 70 is not limited to a clamping chuck in which the plurality of chuck pins 75 contact the peripheral end surface of the substrate W. A vacuum chuck can also be used, which holds the substrate W horizontally by suctioning the back surface (lower surface) of the substrate W, which is not the device forming surface, to the upper surface of the rotating base 74.

杯73配置於較保持在旋轉夾盤70之基板W更外側(遠離旋轉軸線A1之方向)。杯73包圍旋轉基座74之周圍。杯73在以旋轉夾盤70使基板W旋轉之狀態下對基板W供給處理液時,接住排出至基板W之周圍之處理液。由杯73接住之處理液被送至未圖示之回收裝置或排液裝置。Cup 73 is positioned outside the substrate W held on the spin chuck 70 (away from the rotation axis A1). Cup 73 surrounds the spin base 74. When processing liquid is supplied to the substrate W while the spin chuck 70 rotates the substrate W, cup 73 catches the processing liquid that is discharged around the substrate W. The processing liquid caught by cup 73 is then sent to a recovery device or drain unit (not shown).

沖洗液供給單元72包括:沖洗液噴嘴80,其朝向保持於旋轉夾盤70之基板W噴出沖洗液;沖洗液配管81,其向沖洗液噴嘴80供給沖洗液;沖洗液閥82,其切換自沖洗液配管81向沖洗液噴嘴80之沖洗液供給及停止供給。沖洗液噴嘴80可為在沖洗液噴嘴80之噴出口靜止之狀態下噴出沖洗液之固定噴嘴。沖洗液供給單元72可具備沖洗液噴嘴移動單元,其藉由移動沖洗液噴嘴80來移動沖洗液在基板W之上表面之著落位置。The rinse liquid supply unit 72 includes a rinse liquid nozzle 80 that sprays rinse liquid toward the substrate W held on the spin chuck 70; a rinse liquid pipe 81 that supplies rinse liquid to the rinse liquid nozzle 80; and a rinse liquid valve 82 that switches the supply of rinse liquid from the rinse liquid pipe 81 to the rinse liquid nozzle 80 on and off. The rinse liquid nozzle 80 can be a fixed nozzle that sprays rinse liquid while its nozzle is stationary. The rinsing liquid supply unit 72 may include a rinsing liquid nozzle moving unit that moves the rinsing liquid nozzle 80 to move the landing position of the rinsing liquid on the upper surface of the substrate W.

當沖洗液閥82打開時,自沖洗液配管81供給至沖洗液噴嘴80之沖洗液自沖洗液噴嘴80朝向基板W之上表面中央部噴出。沖洗液例如為純水(去離子水:DIW(Deionized Water))。沖洗液不限於純水,亦可為碳酸水、電解離子水、氫水、臭氧水及稀釋濃度(例如10~100 ppm左右)之鹽酸水中之任一種。沖洗液之溫度可為室溫,亦可為高於室溫之溫度(例如70~90℃)。When the rinse liquid valve 82 is opened, the rinse liquid supplied from the rinse liquid pipe 81 to the rinse liquid nozzle 80 is ejected from the rinse liquid nozzle 80 toward the center of the upper surface of the substrate W. The rinse liquid is, for example, pure water (deionized water: DIW). The rinse liquid is not limited to pure water and may also be carbonated water, electrolyzed ionized water, hydrogen water, ozone water, or hydrochloric acid water at a dilute concentration (e.g., approximately 10-100 ppm). The temperature of the rinse liquid may be room temperature or a temperature above room temperature (e.g., 70-90°C).

剝離液供給單元71包括:剝離液噴嘴85,其朝向基板W之上表面噴出SPM;噴嘴臂86,其於前端部安裝有剝離液噴嘴85;噴嘴移動單元87,其藉由移動噴嘴臂86來使剝離液噴嘴85移動。The stripping liquid supply unit 71 includes a stripping liquid nozzle 85 that sprays SPM toward the upper surface of the substrate W; a nozzle arm 86 having the stripping liquid nozzle 85 mounted at its front end; and a nozzle moving unit 87 that moves the stripping liquid nozzle 85 by moving the nozzle arm 86 .

剝離液噴嘴85例如為以連續流之狀態噴出SPM之直噴嘴,例如以在與基板W之上表面垂直之方向上噴出處理液之垂直姿勢安裝於噴嘴臂86上。噴嘴臂86沿水平方向延伸,且設置為能夠在旋轉夾盤70之周圍繞沿鉛直方向延伸之擺動軸線(未圖示)迴轉。The stripping liquid nozzle 85 is, for example, a straight nozzle that ejects SPM in a continuous flow. It is mounted on a nozzle arm 86 in a vertical position, for example, to eject the processing liquid perpendicularly to the upper surface of the substrate W. The nozzle arm 86 extends horizontally and is configured to rotate around a pivot axis (not shown) extending in the vertical direction around the rotary chuck 70.

噴嘴移動單元87藉由使噴嘴臂86繞擺動軸線迴轉,而使剝離液噴嘴85沿著俯視時通過基板W之上表面中央部之軌跡水平移動。噴嘴移動單元87使剝離液噴嘴85在自剝離液噴嘴85噴出之SPM著落於基板W之上表面之處理位置、與剝離液噴嘴85在俯視時位於旋轉夾盤70之周圍之靜止位置之間水平移動。處理位置包括:中央位置,其係自剝離液噴嘴85噴出之SPM著落於基板W之上表面中央部者;及周緣位置,其係自剝離液噴嘴85噴出之SPM著落於基板W之上表面周緣部者。The nozzle moving unit 87 rotates the nozzle arm 86 about a swing axis to horizontally move the stripping liquid nozzle 85 along a trajectory that passes through the center of the upper surface of the substrate W when viewed from above. The nozzle moving unit 87 horizontally moves the stripping liquid nozzle 85 between a processing position where the SPM ejected from the stripping liquid nozzle 85 lands on the upper surface of the substrate W and a stationary position where the stripping liquid nozzle 85 is located around the rotary chuck 70 when viewed from above. The processing positions include: a central position, where the SPM ejected from the stripping liquid nozzle 85 lands on the central portion of the upper surface of the substrate W; and a peripheral position, where the SPM ejected from the stripping liquid nozzle 85 lands on the peripheral portion of the upper surface of the substrate W.

剝離液供給單元71包括:硫酸配管89,其連接於剝離液噴嘴85,自硫酸供給源88供給硫酸(H 2SO 4);及過氧化氫溶液配管95,其連接於剝離液噴嘴85,自過氧化氫溶液供給源94供給過氧化氫溶液(H 2O 2)。 The stripping liquid supply unit 71 includes a sulfuric acid pipe 89 connected to the stripping liquid nozzle 85 and supplied with sulfuric acid (H 2 SO 4 ) from a sulfuric acid supply source 88 ; and a hydrogen peroxide solution pipe 95 connected to the stripping liquid nozzle 85 and supplied with hydrogen peroxide solution (H 2 O 2 ) from a hydrogen peroxide solution supply source 94 .

自硫酸供給源88供給之硫酸及自過氧化氫溶液供給源94供給之過氧化氫溶液均為水溶液。硫酸之濃度例如為90~98%,過氧化氫溶液之濃度例如為30~50%。The sulfuric acid supplied from the sulfuric acid supply source 88 and the hydrogen peroxide solution supplied from the hydrogen peroxide solution supply source 94 are both aqueous solutions. The concentration of the sulfuric acid is, for example, 90-98%, and the concentration of the hydrogen peroxide solution is, for example, 30-50%.

於硫酸配管89自剝離液噴嘴85側依序插裝有開閉硫酸配管89之流路之硫酸閥90、改變硫酸之流量之硫酸流量調整閥91、及加熱硫酸之加熱器92。加熱器92將硫酸加熱為高於室溫之溫度(70~190℃之範圍內之固定溫度。例如90℃)。On the sulfuric acid piping 89 from the stripping liquid nozzle 85, a sulfuric acid valve 90 is installed in this order to open and close the sulfuric acid piping 89, a sulfuric acid flow regulating valve 91 is installed to change the flow rate of the sulfuric acid, and a heater 92 is installed to heat the sulfuric acid. Heater 92 heats the sulfuric acid to a temperature higher than room temperature (a fixed temperature within the range of 70-190°C, for example, 90°C).

於過氧化氫溶液配管95自剝離液噴嘴85側依序插裝有開閉過氧化氫溶液配管95之流路之過氧化氫溶液閥96、及改變過氧化氫溶液之流量之過氧化氫溶液流量調整閥97。未經調溫之室溫(例如約23℃)之過氧化氫溶液通過過氧化氫溶液配管95被供給至過氧化氫溶液閥96。A hydrogen peroxide valve 96 for opening and closing the hydrogen peroxide pipe 95 and a hydrogen peroxide flow regulating valve 97 for varying the flow rate of hydrogen peroxide are sequentially installed on the hydrogen peroxide pipe 95 from the stripping liquid nozzle 85. Unconditioned hydrogen peroxide at room temperature (e.g., approximately 23°C) is supplied to the hydrogen peroxide valve 96 through the hydrogen peroxide pipe 95.

剝離液噴嘴85例如具有大致圓筒狀之外殼。該外殼之內部形成有混合室。硫酸配管89與配置於剝離液噴嘴85之外殼之側壁之硫酸導入口連接。過氧化氫溶液配管95與配置於剝離液噴嘴85之外殼之側壁之過氧化氫溶液導入口連接。The stripping liquid nozzle 85 has, for example, a generally cylindrical housing. A mixing chamber is formed within the housing. A sulfuric acid pipe 89 is connected to a sulfuric acid inlet located on the side wall of the stripping liquid nozzle 85 housing. A hydrogen peroxide solution pipe 95 is connected to a hydrogen peroxide solution inlet located on the side wall of the stripping liquid nozzle 85 housing.

當硫酸閥90及過氧化氫溶液閥96打開時,來自硫酸配管89之硫酸(高溫之硫酸)被自剝離液噴嘴85之硫酸導入口供給至其內部之混合室,並且來自過氧化氫溶液配管95之過氧化氫溶液自剝離液噴嘴85之過氧化氫溶液導入口被供給至其內部之混合室。When the sulfuric acid valve 90 and the hydrogen peroxide solution valve 96 are opened, sulfuric acid (high-temperature sulfuric acid) from the sulfuric acid pipe 89 is supplied to the mixing chamber inside the stripping liquid nozzle 85 from the sulfuric acid inlet, and hydrogen peroxide solution from the hydrogen peroxide solution pipe 95 is supplied to the mixing chamber inside the stripping liquid nozzle 85 from the hydrogen peroxide solution inlet.

流入剝離液噴嘴85之混合室之硫酸及過氧化氫溶液在混合室中被充分攪拌混合。藉由該混合,硫酸及過氧化氫溶液均勻地混合,且藉由其等之反應而產生SPM。SPM包含氧化能力強之過氧單硫酸(Peroxymonosulfuric acid;H 2SO 5)。由於供給加熱為高溫之硫酸,並且硫酸與過氧化氫溶液之混合為發熱反應,故而產生高溫之SPM。具體而言,產生較混合前之硫酸及過氧化氫溶液中之任一者之溫度高之溫度(100℃以上。例如160℃)的SPM。於剝離液噴嘴85之混合室中產生之高溫之SPM自於外殼之前端(下端)開口之噴出口朝向基板W噴出。 The sulfuric acid and hydrogen peroxide solution flowing into the mixing chamber of the stripping liquid nozzle 85 are thoroughly stirred and mixed in the mixing chamber. This mixing uniformly mixes the sulfuric acid and hydrogen peroxide solution, and through their reaction, SPM is produced. SPM contains peroxymonosulfuric acid ( H2SO5 ), which has a strong oxidizing ability. Because the heated sulfuric acid is supplied at a high temperature, and the mixing of the sulfuric acid and hydrogen peroxide solution is an exothermic reaction, high-temperature SPM is produced. Specifically, SPM is produced at a temperature higher than the temperature of either the sulfuric acid or hydrogen peroxide solution before mixing (above 100°C, for example, 160°C). The high-temperature SPM generated in the mixing chamber of the stripping liquid nozzle 85 is ejected toward the substrate W from the nozzle opening at the front end (lower end) of the housing.

圖12係表示由基板處理裝置1執行之基板W之處理之一例的步驟圖。以下,參照圖8、圖9、圖11、及圖12。控制裝置3以使基板處理裝置1執行以下動作之方式編程。FIG12 is a flowchart showing an example of the process of processing a substrate W by the substrate processing apparatus 1. Hereinafter, reference will be made to FIG8, FIG9, FIG11, and FIG12. The control apparatus 3 is programmed so that the substrate processing apparatus 1 performs the following operations.

於基板處理裝置1處理基板W時,分度機械手IR、梭子SH、及中心機械手CR將載置於裝載埠LP之載具C內之基板W搬送至前處理單元2D(圖12之步驟S11)。在前處理單元2D中,進行上述之抗蝕劑剝離之2個例子中之任一個,除去抗蝕圖案100(參照圖5)之至少一部分(圖12之步驟S12)。While substrate processing apparatus 1 is processing substrates W, index robot IR, shuttle SH, and center robot CR transport substrates W placed in carrier C at loading port LP to pre-processing unit 2D (step S11 in FIG. 12 ). In pre-processing unit 2D, one of the two aforementioned resist stripping methods is performed to remove at least a portion of resist pattern 100 (see FIG. 5 ) (step S12 in FIG. 12 ).

具體而言,中心機械手CR將基板W搬入前處理單元2D,室內搬送機構6將基板W搬送至熱處理單元8。其後,於熱處理單元8中進行直至使基板W上之過氧化氫溶液蒸發而使基板W乾燥為止之步驟。於基板W乾燥後,根據需要,室內搬送機構6將基板W自加熱板30搬送至冷卻板20。藉此,基板W被冷卻板20冷卻至室溫或其附近之溫度。於基板W乾燥後或冷卻後,中心機械手CR將基板W自前處理單元2D搬出,並將搬出後之基板W搬入至後處理單元2W(圖12之步驟S13)。Specifically, the central robot CR moves the substrate W into the pre-treatment unit 2D, and the in-chamber transport mechanism 6 transports the substrate W to the thermal treatment unit 8. Subsequently, steps are performed in the thermal treatment unit 8 until the hydrogen peroxide solution on the substrate W evaporates, drying the substrate W. After drying the substrate W, the in-chamber transport mechanism 6 transfers the substrate W from the heating plate 30 to the cooling plate 20, as needed. The cooling plate 20 cools the substrate W to room temperature or a temperature near room temperature. After drying or cooling the substrate W, the central robot CR removes the substrate W from the pre-treatment unit 2D and moves the removed substrate W into the post-treatment unit 2W (step S13 in FIG. 12 ).

於後處理單元2W中,進行濕式處理(圖12之步驟S14),該濕式處理係一面使基板W旋轉,一面將抗蝕劑剝離液等處理液供給至基板W之上表面。具體而言,進行抗蝕劑剝離液供給步驟,其係一面使基板W旋轉,一面使剝離液噴嘴85朝向基板W之上表面噴出抗蝕劑剝離液。其後,進行沖洗液供給步驟,其係一面使基板W旋轉,一面使沖洗液噴嘴80朝向基板W之上表面噴出沖洗液。其後,進行藉由使基板W高速旋轉而使基板W乾燥之乾燥步驟。其後,分度機械手IR、梭子SH、及中心機械手CR將後處理單元2W內之基板W搬送至放置於裝載埠LP之載具C(圖12之步驟S15)。In the post-processing unit 2W, a wet treatment (step S14 in FIG. 12 ) is performed. This wet treatment involves supplying a treatment liquid, such as an anti-etching stripping liquid, onto the upper surface of the substrate W while the substrate W is rotated. Specifically, a resist stripping liquid supply step is performed, in which the stripping liquid nozzle 85 sprays the resist stripping liquid toward the upper surface of the substrate W while the substrate W is rotated. Subsequently, a rinse liquid supply step is performed, in which the rinse liquid nozzle 80 sprays the rinse liquid toward the upper surface of the substrate W while the substrate W is rotated. Subsequently, a drying step is performed, in which the substrate W is dried by rotating the substrate W at high speed. Thereafter, the index robot IR, the shuttle SH, and the central robot CR transport the substrate W in the post-processing unit 2W to the carrier C placed on the load port LP (step S15 in FIG. 12 ).

如上所述,於本實施方式中,使過氧化氫溶液與形成於基板W之表面之抗蝕圖案100接觸。進而,使臭氧氣體與該過氧化氫溶接觸。藉由臭氧氣體與過氧化氫之反應而產生羥基自由基。羥基自由基氧化並分解抗蝕圖案100。藉此,抗蝕圖案100之至少一部分被剝離或除去。羥基自由基之氧化還原電位較臭氧氣體高,氧化能力較臭氧氣體強。因此,相較於用臭氧氣體氧化及分解抗蝕圖案100之情形,可有效率地除去抗蝕圖案100。藉此,能夠削減含有硫酸之抗蝕劑剝離液之使用量或省去其之使用,故而能夠降低環境負載。As described above, in this embodiment, a hydrogen peroxide solution is brought into contact with the anti-etching pattern 100 formed on the surface of the substrate W. Furthermore, ozone gas is brought into contact with the hydrogen peroxide solution. Hydroxyl radicals are generated by the reaction between the ozone gas and the hydrogen peroxide. The hydroxyl radicals oxidize and decompose the anti-etching pattern 100. As a result, at least a portion of the anti-etching pattern 100 is stripped or removed. Hydroxyl radicals have a higher redox potential than ozone gas and possess a stronger oxidizing ability than ozone gas. Therefore, compared to the case where the anti-etching pattern 100 is oxidized and decomposed by ozone gas, the anti-etching pattern 100 can be removed more efficiently. This can reduce the amount of anti-corrosion agent stripping fluid containing sulfuric acid or eliminate its use, thereby reducing the environmental burden.

於本實施方式中,在供給至基板W後對過氧化氫溶液進行間接或直接加熱。或者,將加熱後之過氧化氫溶液供給至基板W。藉此,能夠使臭氧氣體與剝離促進溫度、即高於室溫之溫度之過氧化氫溶液接觸,從而能夠促進羥基自由基之產生。其結果,能夠增加與抗蝕圖案100反應之羥基自由基,從而能夠更有效率地除去抗蝕圖案100。In this embodiment, the hydrogen peroxide solution is heated indirectly or directly after being supplied to the substrate W. Alternatively, the heated hydrogen peroxide solution is supplied to the substrate W. This allows ozone gas to come into contact with the hydrogen peroxide solution at a temperature higher than room temperature, which promotes the generation of hydroxyl radicals. As a result, the number of hydroxyl radicals that react with the resist pattern 100 increases, enabling more efficient removal of the resist pattern 100.

於本實施方式中,以低於過氧化氫溶液之沸點之溫度加熱過氧化氫溶液。藉此,能夠降低過氧化氫溶液自基板W蒸發之速度,能夠維持過氧化氫溶液位於基板W上之狀態。若使大量之過氧化氫溶液保持於基板W,則即便以沸點以上之溫度加熱過氧化氫溶液,亦能夠在相對長之時間內維持過氧化氫溶液位於基板W上之狀態。然而,於該情形時,基板W上之過氧化氫溶液之液滴或液膜之厚度變大,到達抗蝕圖案100之表面之羥基自由基減少。藉由以低於過氧化氫溶液之沸點之溫度加熱過氧化氫溶液,即便不於基板W上形成厚度較大之過氧化氫溶液液滴或液膜,亦能夠維持過氧化氫溶液位於基板W上之狀態。In this embodiment, the hydrogen peroxide solution is heated at a temperature below its boiling point. This reduces the rate at which the hydrogen peroxide solution evaporates from the substrate W, maintaining the hydrogen peroxide solution on the substrate W. If a large amount of hydrogen peroxide solution is retained on the substrate W, even if the hydrogen peroxide solution is heated at a temperature above its boiling point, the hydrogen peroxide solution can be maintained on the substrate W for a relatively long time. However, in this case, the thickness of the hydrogen peroxide solution droplets or film on the substrate W increases, reducing the number of hydroxyl radicals reaching the surface of the anti-etching pattern 100. By heating the hydrogen peroxide solution at a temperature lower than the boiling point of the hydrogen peroxide solution, the hydrogen peroxide solution can be maintained on the substrate W even if thick hydrogen peroxide solution droplets or a liquid film is not formed on the substrate W.

於本實施方式中,以低於水之沸點、即100℃之溫度加熱過氧化氫溶液。藉此,能夠降低水自基板W上之過氧化氫溶液中蒸發之速度,即便不於基板W上形成厚度較大之過氧化氫溶液之液滴或液膜,亦能夠維持水位於基板W上之狀態。羥基自由基不僅藉由臭氧氣體與過氧化氫之反應產生,還藉由臭氧氣體與水之反應而產生。藉此,能夠增加與抗蝕圖案100反應之羥基自由基。In this embodiment, the hydrogen peroxide solution is heated to a temperature below the boiling point of water, namely 100°C. This reduces the rate of water evaporation from the hydrogen peroxide solution on the substrate W, maintaining the water level on the substrate W without forming thick hydrogen peroxide droplets or a film on the substrate W. Hydroxyl radicals are generated not only by the reaction between ozone gas and hydrogen peroxide, but also by the reaction between ozone gas and water. This increases the number of hydroxyl radicals that react with the anti-etching pattern 100.

當加熱抗蝕圖案100時,抗蝕圖案100中所含之溶劑氣化。於抗蝕圖案100之表層形成有硬化層101之情形時,由於氣化後之溶劑不易排出,故而抗蝕圖案100之內部之壓力上升。自抗蝕劑塗佈直至抗蝕劑剝離之前之一系列步驟包括預烘烤或後烘烤等加熱基板W之步驟。將該一系列步驟中之基板W之溫度之最大值定義為最高溫度。抗蝕圖案100之表層形成有硬化層101,當加熱抗蝕圖案100之溫度大幅高於最高溫度時,抗蝕圖案100之內部之壓力不易升高。When the resist pattern 100 is heated, the solvent contained in the resist pattern 100 vaporizes. When a hardened layer 101 forms on the surface of the resist pattern 100, the vaporized solvent is difficult to expel, causing the pressure inside the resist pattern 100 to increase. The series of steps from resist application to resist stripping includes heating the substrate W, such as pre-baking or post-baking. The maximum temperature of the substrate W during this series of steps is defined as the maximum temperature. Because the hardened layer 101 forms on the surface of the resist pattern 100, when the temperature of the resist pattern 100 is significantly higher than the maximum temperature, the pressure inside the resist pattern 100 is unlikely to increase.

於以高於室溫之剝離促進溫度加熱過氧化氫溶液時,若將該剝離促進溫度設為低於過氧化氫溶液之沸點之溫度或低於水之沸點之溫度,則能夠使加熱抗蝕圖案100之溫度接近於上述之一系列步驟中基板W之溫度之最大值、即最高溫度。或者,可將加熱抗蝕圖案100之溫度設為最高溫度以下。藉此,即便於抗蝕圖案100之表層形成有硬化層101之情形時,亦能夠防止抗蝕圖案100之內部之壓力變高。When heating the hydrogen peroxide solution at a peeling-promoting temperature higher than room temperature, setting the peeling-promoting temperature to a temperature lower than the boiling point of the hydrogen peroxide solution or lower than the boiling point of water allows the temperature of the heated resist pattern 100 to approach the maximum temperature of the substrate W during the aforementioned series of steps. Alternatively, the temperature of the heated resist pattern 100 can be set below the maximum temperature. This prevents the internal pressure of the resist pattern 100 from increasing even when a hardened layer 101 is formed on the surface of the resist pattern 100.

於本實施方式中,以高於室溫之剝離促進溫度加熱過氧化氫溶液,並且將過氧化氫溶液間歇地供給至基板W之表面。即,將過氧化氫溶液供給至基板W之表面,並使其保持於基板W之表面。於停止(中斷)供給過氧化氫溶液之期間(停止添加過氧化氫溶液之期間),基板W上之過氧化氫溶液由於蒸發或與臭氧氣體之反應而減少。重新開始向基板W之表面供給過氧化氫溶液而對基板W之表面添加過氧化氫溶液。藉此,相較於持續供給過氧化氫溶液之情形,能夠削減過氧化氫溶液之消耗量,並且將維持過氧化氫溶液位於基板W上之狀態。此外,相較於持續供給過氧化氫溶液之情形,能夠使基板W上之過氧化氫溶液之液滴或液膜變薄。In this embodiment, a hydrogen peroxide solution is heated to a peeling-promoting temperature higher than room temperature and intermittently supplied to the surface of the substrate W. Specifically, the hydrogen peroxide solution is supplied to the surface of the substrate W and maintained there. During the period when the supply of hydrogen peroxide solution is stopped (interrupted) (the period when the addition of hydrogen peroxide solution is stopped), the amount of hydrogen peroxide solution on the substrate W decreases due to evaporation or reaction with ozone gas. The supply of hydrogen peroxide solution to the surface of the substrate W is resumed, and the surface of the substrate W is added with hydrogen peroxide solution. This reduces the consumption of hydrogen peroxide solution compared to a continuous supply of hydrogen peroxide solution, and maintains the hydrogen peroxide solution on the substrate W. In addition, compared to the case of continuously supplying the hydrogen peroxide solution, the droplets or liquid film of the hydrogen peroxide solution on the substrate W can be made thinner.

於本實施方式中,不是在基板W之表面全域被過氧化氫溶液之液膜覆蓋之狀態下,而是在過氧化氫溶液之複數個液滴分散於基板W之表面全域之狀態下,使臭氧氣體與接觸基板W之過氧化氫溶液接觸。藉此,相較於基板W之表面全域被過氧化氫溶液之液膜覆蓋之情形,能夠有效率地除去抗蝕圖案100。理由如下所述。In this embodiment, ozone gas is brought into contact with the hydrogen peroxide solution in contact with the substrate W, rather than with the entire surface of the substrate W being covered by a liquid film of hydrogen peroxide solution. Instead, multiple droplets of hydrogen peroxide solution are dispersed over the entire surface of the substrate W. This allows for more efficient removal of the resist pattern 100 than when the entire surface of the substrate W is covered by a liquid film of hydrogen peroxide solution. The reasons are as follows.

供給至抗蝕圖案100與過氧化氫溶液之界面即固液界面111(參照圖4)之羥基自由基(OH)隨著接近臭氧氣體、過氧化氫溶液及抗蝕圖案100之邊界即三態邊界112(參照圖4)而增加。其原因在於:由於羥基自由基在短時間內會變回過氧化氫,因此若自過氧化氫溶液之液滴或液膜之表面至固液界面111之最短距離較長,則羥基自由基在到達固液界面111之前就會消失。因此,相較於距三態邊界112較遠之位置,於三態邊界112附近,能夠有效率地除去與過氧化氫溶液接觸之抗蝕圖案100。The number of hydroxyl radicals (OH) supplied to the interface between the resist pattern 100 and the hydrogen peroxide solution, namely the solid-liquid interface 111 (see FIG. 4 ), increases as the resist pattern 100 approaches the boundary between the ozone gas, the hydrogen peroxide solution, and the three-state boundary 112 (see FIG. 4 ). This is because hydroxyl radicals quickly transform back into hydrogen peroxide. Therefore, if the shortest distance from the surface of the hydrogen peroxide solution droplet or film to the solid-liquid interface 111 is long, the hydroxyl radicals will disappear before reaching the solid-liquid interface 111. Therefore, the resist pattern 100 in contact with the hydrogen peroxide solution can be more efficiently removed near the three-state boundary 112 than at locations farther from the three-state boundary 112.

過氧化氫溶液之複數個液滴分散於基板W之表面全域時之三態邊界112之全長(長度之合計值),較基板W之表面全域被過氧化氫溶液之液膜覆蓋時之三態邊界112之全長大。如上所述,相較於距三態邊界112較遠之位置,於三態邊界112附近,能夠有效率地除去與過氧化氫溶液接觸之抗蝕圖案100。由於以上之理由,相較於基板W之表面全域被過氧化氫溶液之液膜覆蓋之情形,能夠有效率地除去抗蝕圖案100。The total length (total length) of the three-state boundary 112 when multiple droplets of hydrogen peroxide solution are dispersed over the entire surface of the substrate W is greater than the total length of the three-state boundary 112 when the entire surface of the substrate W is covered by a liquid film of hydrogen peroxide solution. As described above, the resist pattern 100 in contact with the hydrogen peroxide solution can be more efficiently removed near the three-state boundary 112 than at locations farther from the three-state boundary 112. For these reasons, the resist pattern 100 can be more efficiently removed than when the entire surface of the substrate W is covered by a liquid film of hydrogen peroxide solution.

於本實施方式中,對基板W之表面供給霧狀之過氧化氫溶液。過氧化氫溶液之霧係由多個過氧化氫溶液之粒子構成。基板W上之過氧化氫溶液之粒子與其他過氧化氫溶液之粒子結合,於基板W之表面形成過氧化氫溶液之液滴(直徑大於過氧化氫溶液之粒子之過氧化氫溶液之集合體)。於抗蝕圖案100之表面為疏水性之情形時,形成過氧化氫溶液之複數個液滴,並分散於基板W之表面全域。於抗蝕圖案100之表面為親水性之情形時,形成覆蓋基板W之表面全域的過氧化氫溶液之液膜。藉此,相較於形成自液柱噴嘴51B至基板W之表面連續之過氧化氫溶液之液柱之情形,能夠形成較薄之過氧化氫溶液之液滴或液膜。In this embodiment, a hydrogen peroxide solution mist is applied to the surface of the substrate W. The hydrogen peroxide solution mist is composed of a plurality of hydrogen peroxide solution particles. The hydrogen peroxide solution particles on the substrate W combine with other hydrogen peroxide solution particles to form hydrogen peroxide solution droplets (aggregates of hydrogen peroxide solution with a diameter larger than the hydrogen peroxide solution particles) on the surface of the substrate W. If the surface of the anti-etching pattern 100 is hydrophobic, multiple hydrogen peroxide solution droplets are formed and dispersed over the entire surface of the substrate W. If the surface of the anti-etching pattern 100 is hydrophilic, a hydrogen peroxide solution film is formed that covers the entire surface of the substrate W. Thus, compared with the case where a continuous liquid column of hydrogen peroxide solution is formed from the liquid column nozzle 51B to the surface of the substrate W, thinner liquid droplets or liquid films of the hydrogen peroxide solution can be formed.

於本實施方式中,自液柱噴嘴51B朝向基板W之表面連續地噴出過氧化氫溶液,並使過氧化氫溶液與基板W之表面碰撞。自液柱噴嘴51B噴出之過氧化氫溶液形成自液柱噴嘴51B至基板W之表面連續之過氧化氫溶液之液注。於抗蝕圖案100之表面為疏水性之情形時,形成過氧化氫溶液之複數個液滴,並分散於基板W之表面全域。於抗蝕圖案100之表面為親水性之情形時,形成覆蓋基板W之表面全域之過氧化氫溶液之液膜。藉此,相較於向基板W之表面供給過氧化氫溶液之霧之情形,能夠在短時間內形成過氧化氫溶液之液滴或液膜。In this embodiment, hydrogen peroxide solution is continuously ejected from the liquid column nozzle 51B toward the surface of the substrate W, causing the hydrogen peroxide solution to collide with the surface of the substrate W. The hydrogen peroxide solution ejected from the liquid column nozzle 51B forms a continuous stream of hydrogen peroxide solution extending from the liquid column nozzle 51B to the surface of the substrate W. If the surface of the anti-etching pattern 100 is hydrophobic, multiple droplets of hydrogen peroxide solution are formed and dispersed over the entire surface of the substrate W. If the surface of the anti-etching pattern 100 is hydrophilic, a liquid film of hydrogen peroxide solution is formed that covers the entire surface of the substrate W. Thus, compared to the case where a mist of hydrogen peroxide solution is supplied to the surface of the substrate W, liquid droplets or a liquid film of the hydrogen peroxide solution can be formed in a shorter time.

於本實施方式中,使臭氧氣體與基板W之表面接觸,以減弱抗蝕圖案100之表面之疏水性。藉此,水相對於抗蝕圖案100之表面之接觸角減小。於該狀態下,對基板W之表面供給過氧化氫溶液。於抗蝕圖案100之表面為疏水性之情形時,若不以較大之流量供給過氧化氫溶液,則無法形成覆蓋基板W之表面全域的過氧化氫溶液之液膜。然而,於該情形時,過氧化氫溶液之消耗量增加,而且還形成較厚之過氧化氫溶液之液膜。若在對抗蝕圖案100之表面進行親水化後供給過氧化氫溶液,則能夠削減過氧化氫溶液之消耗量,並且形成覆蓋基板W之表面全域的較薄之過氧化氫溶液之液膜。此外,由於不僅使用臭氧氣體除去抗蝕圖案100,還使用臭氧氣體對抗蝕圖案100之表面進行親水化,故而相較於使用臭氧氣體以外之液體或氣體來對抗蝕圖案100之表面進行親水化之情形,能夠減少配管、閥等用於處理基板W之流體機器之數量。In this embodiment, ozone gas is brought into contact with the surface of the substrate W to reduce the hydrophobicity of the surface of the anti-etching pattern 100. This reduces the contact angle of water with the surface of the anti-etching pattern 100. In this state, a hydrogen peroxide solution is supplied to the surface of the substrate W. If the surface of the anti-etching pattern 100 is hydrophobic, a hydrogen peroxide solution film that covers the entire surface of the substrate W cannot be formed unless the hydrogen peroxide solution is supplied at a high flow rate. However, in this case, the consumption of hydrogen peroxide solution increases, and a thicker hydrogen peroxide solution film is formed. By supplying the hydrogen peroxide solution after the surface of the resist pattern 100 has been hydrophilized, the consumption of the hydrogen peroxide solution can be reduced, and a thinner hydrogen peroxide solution film can be formed that covers the entire surface of the substrate W. Furthermore, because ozone gas is used not only to remove the resist pattern 100 but also to hydrophilize the surface of the resist pattern 100, the number of pipes, valves, and other fluid equipment used to process the substrate W can be reduced compared to the use of liquids or gases other than ozone gas to hydrophilize the surface of the resist pattern 100.

於本實施方式中,在使用藉由臭氧氣體與過氧化氫之反應而產生之羥基自由基來剝離或除去抗蝕圖案100之全部或一部分後,對基板W之表面供給抗蝕劑剝離液。即便抗蝕圖案100之一部分殘留於基板W之表面,該抗蝕圖案100亦會因與抗蝕劑剝離液之接觸而自基板W之表面剝離。即便抗蝕圖案100之殘渣殘留於基板W之表面,該殘渣亦會被抗蝕劑剝離液沖洗掉。藉此,能夠減少殘留於基板W之表面之抗蝕劑。In this embodiment, after all or part of the resist pattern 100 is stripped or removed using hydroxyl radicals generated by the reaction of ozone gas and hydrogen peroxide, a resist stripping liquid is supplied to the surface of the substrate W. Even if a portion of the resist pattern 100 remains on the surface of the substrate W, the resist pattern 100 is stripped from the surface of the substrate W due to contact with the resist stripping liquid. Even if residue from the resist pattern 100 remains on the surface of the substrate W, it is washed away by the resist stripping liquid. This reduces the amount of resist remaining on the surface of the substrate W.

另一實施方式 若可藉由對基板W供給臭氧氣體及過氧化氫溶液,而將所有或幾乎所有抗蝕劑自基板W剝離,則亦可在對基板W供給氧氣體及過氧化氫溶液後,不對基板W供給氧化能力較沖洗液高之抗蝕劑剝離液。於該情形時,亦可對基板W之表面供給純水等沖洗液以沖洗抗蝕圖案100之殘渣。尤其是,由於能夠削減如SPM之類之含有硫酸之抗蝕劑剝離液之使用量或省去其之使用,故而能夠降低環境負載。 Another Embodiment If all or nearly all of the resist can be stripped from the substrate W by supplying ozone gas and hydrogen peroxide solution to the substrate W, then after supplying oxygen gas and hydrogen peroxide solution to the substrate W, a resist stripping solution with a higher oxidizing power than the rinse solution may not be supplied to the substrate W. In this case, a rinse solution such as pure water may be supplied to the surface of the substrate W to rinse away residue from the resist pattern 100. In particular, since the use of resist stripping solutions containing sulfuric acid, such as SPM, can be reduced or eliminated, the environmental load can be reduced.

若係使用臭氧氣體及過氧化氫溶液除去抗蝕圖案100之硬化層101之一部之後,則可在到達非硬化部102之空洞103(參照圖5)形成於硬化層101之前,停止向基板W供給臭氧氣體。即便採用上述方式,與在不除去抗蝕圖案100之硬化層101之一部分之情況下對基板W供給抗蝕劑剝離液之情形相比,亦能夠縮短自基板W剝離所有抗蝕圖案100之時間。If ozone gas and hydrogen peroxide solution are used to remove a portion of the hardened layer 101 of the resist pattern 100, the supply of ozone gas to the substrate W can be stopped before the cavity 103 (see FIG. 5 ) is formed in the hardened layer 101 by reaching the non-hardened portion 102. Even with this method, the time required to strip all of the resist pattern 100 from the substrate W can be shortened compared to a case where the resist stripping solution is supplied to the substrate W without removing a portion of the hardened layer 101 of the resist pattern 100.

亦可以過氧化氫溶液之沸點以上之溫度加熱過氧化氫溶液。於該情形時,可以150℃以上之溫度加熱基板W。若採用上述方式,則可經由基板W以150℃以上之溫度加熱臭氧氣體。藉此,能夠提高臭氧氣體之活性,且不僅藉由臭氧氣與過氧化氫之反應所產生之羥基自由基,而且藉由臭氧氣體亦可氧化及分解抗蝕圖案100。Alternatively, the hydrogen peroxide solution can be heated to a temperature above its boiling point. In this case, the substrate W can be heated to a temperature above 150°C. Using this method, the ozone gas can be heated at a temperature above 150°C through the substrate W. This increases the activity of the ozone gas, allowing the ozone gas to not only generate hydroxyl radicals through the reaction between the ozone gas and hydrogen peroxide, but also oxidize and decompose the resist pattern 100.

亦可不使臭氧氣體與高於室溫之溫度之過氧化氫溶液接觸,而使臭氧氣體與室溫之過氧化氫溶液接觸。即,亦可不加熱基板W,或不對基板W供給高於室溫之溫度之過氧化氫溶液。Alternatively, the ozone gas may be in contact with a hydrogen peroxide solution at room temperature instead of the ozone gas. In other words, the substrate W may not be heated, or a hydrogen peroxide solution at a temperature higher than room temperature may not be supplied to the substrate W.

向基板W之表面供給臭氧氣體及過氧化氫溶液及向基板W之表面供給抗蝕劑剝離液,可在不同之基板處理裝置1中進行。更具體而言,亦可在對基板W供給臭氧氣體及過氧化氫溶液之後,將基板W搬送至另一基板處理裝置1,在該基板處理裝置1內對基板W之表面供給抗蝕劑剝離液。或者,亦可在對基板W供給臭氧氣體及過氧化氫溶液之後,不搬送基板W,而對該基板W之表面供給抗蝕劑剝離液。例如,可對保持於旋轉夾盤70之基板W之表面供給臭氧氣體及過氧化氫溶液,其後,對保持於該旋轉夾盤70之基板W之表面供給抗蝕劑剝離液。Supplying ozone gas and hydrogen peroxide solution to the surface of the substrate W and supplying an anti-etching stripping liquid to the surface of the substrate W can be performed in different substrate processing apparatuses 1. More specifically, after supplying ozone gas and hydrogen peroxide solution to the substrate W, the substrate W can be transported to another substrate processing apparatus 1, where the anti-etching stripping liquid can be supplied to the surface of the substrate W within the substrate processing apparatus 1. Alternatively, after supplying ozone gas and hydrogen peroxide solution to the substrate W, the anti-etching stripping liquid can be supplied to the surface of the substrate W without transporting the substrate W. For example, ozone gas and hydrogen peroxide solution may be supplied to the surface of the substrate W held on the spin chuck 70 , and then, an anti-etching agent stripping solution may be supplied to the surface of the substrate W held on the spin chuck 70 .

基板處理裝置1不限於處理圓板狀之基板W之裝置,亦可為處理多邊形之基板W之裝置。The substrate processing apparatus 1 is not limited to an apparatus for processing a circular plate-shaped substrate W, but may also be an apparatus for processing a polygonal substrate W.

可組合上述所有構成中之2個以上。亦可組合上述所有步驟中之2個以上。You can combine two or more of the above components. You can also combine two or more of the above steps.

雖然對本發明之實施方式詳細地進行了說明,但其等僅是用於闡明本發明之技術性內容之具體例,不應限定於該等具體例來解釋本發明,本發明之範圍僅由隨附之專利範圍限定。Although the embodiments of the present invention are described in detail, they are only used to illustrate specific examples of the technical content of the present invention and should not be limited to these specific examples. The scope of the present invention is only defined by the scope of the accompanying patents.

[相關申請案] 本申請案係基於2022年5月17日提出之日本專利申請案2022-080693號並主張其優先權,該申請案之全部內容藉由引用而併入本文中。 [Related Applications] This application is based upon and claims priority from Japanese Patent Application No. 2022-080693, filed on May 17, 2022. The entire contents of that application are incorporated herein by reference.

1:基板處理裝置 2:處理單元 2D:前處理單元 2W:後處理單元 3:控制裝置 3m:記憶體 3p:處理器 4:腔室 4a:搬入搬出口 5:擋板 6:室內搬送機構 6H:室內搬送手 7:冷卻單元 8:熱處理單元 9:腔室 9a:搬入搬出口 10:擋板 20:冷卻板 20a:冷卻面 22:頂起銷 23:銷升降驅動機構 30:加熱板 30a:加熱面 33:加熱器 34:熱處理腔室 35:腔室本體 35a:開口 36:蓋 37:蓋升降驅動機構 38:頂起銷 39:銷升降驅動機構 41:排氣埠 42:排氣線路 45:板部 46:筒部 49:氣體供給線路 51A:霧噴嘴 51B:液柱噴嘴 52:過氧化氫溶液線路 53:過氧化氫溶液閥 54:過氧化氫溶液供給源 55:臭氧噴嘴 56:臭氧線路 57:臭氧閥 58:臭氧產生器 59:簇射板 60:氣液分離器 70:旋轉夾盤 71:剝離液供給單元 72:沖洗液供給單元 73:杯 74:旋轉基座 75:夾盤銷 76:旋轉軸 77:旋轉馬達 80:沖洗液噴嘴 81:沖洗液配管 82:沖洗液閥 85:剝離液噴嘴 86:噴嘴臂 87:噴嘴移動單元 88:硫酸供給源 89:硫酸配管 90:硫酸閥 91:硫酸流量調整閥 92:加熱器 94:過氧化氫溶液供給源 95:過氧化氫溶液配管 96:過氧化氫溶液閥 97:過氧化氫溶液流量調整閥 100:抗蝕圖案 101:硬化層 102:非硬化部 103:空洞 111:固液界面 112:三態邊界 A1:旋轉軸線 C:載具 CR:中心機械手 H:手 IR:分度機械手 LP:裝載埠 S1:步驟 S2:步驟 S3:步驟 S4:步驟 S5:步驟 S6:步驟 S11:步驟 S12:步驟 S13:步驟 S14:步驟 S15:步驟 SH:梭子 W:基板 1: Substrate processing unit 2: Processing unit 2D: Pre-processing unit 2W: Post-processing unit 3: Control unit 3m: Memory 3p: Processor 4: Chamber 4a: Load/unload port 5: Baffle 6: In-chamber transfer mechanism 6H: In-chamber transfer arm 7: Cooling unit 8: Thermal treatment unit 9: Chamber 9a: Load/unload port 10: Baffle 20: Cooling plate 20a: Cooling surface 22: Lifting pin 23: Pin lift drive mechanism 30: Heating plate 30a: Heating surface 33: Heater 34: Thermal treatment chamber 35: Chamber body 35a: Opening 36: Lid 37: Lid lift drive mechanism 38: Lifting pin 39: Pin lift drive mechanism 41: Exhaust port 42: Exhaust line 45: Plate 46: Cylinder 49: Gas supply line 51A: Mist nozzle 51B: Liquid column nozzle 52: Hydrogen peroxide solution line 53: Hydrogen peroxide solution valve 54: Hydrogen peroxide solution supply source 55: Ozone nozzle 56: Ozone line 57: Ozone valve 58: Ozone generator 59: Shower plate 60: Gas-liquid separator 70: Rotary chuck 71: Stripping liquid supply unit 72: Rinse fluid supply unit 73: Cup 74: Rotary base 75: Chuck pin 76: Rotary shaft 77: Rotary motor 80: Rinse fluid nozzle 81: Rinse fluid piping 82: Rinse fluid valve 85: Stripping fluid nozzle 86: Nozzle arm 87: Nozzle movement unit 88: Sulfuric acid supply source 89: Sulfuric acid piping 90: Sulfuric acid valve 91: Sulfuric acid flow control valve 92: Heater 94: Hydrogen peroxide supply source 95: Hydrogen peroxide piping 96: Hydrogen peroxide valve 97: Hydrogen peroxide flow control valve 100: Anti-corrosion pattern 101: Hardened layer 102: Non-hardened area 103: Void 111: Solid-liquid interface 112: Tri-state boundary A1: Rotation axis C: Carrier CR: Center robot H: Hand IR: Indexing robot LP: Loading port S1: Step S2: Step S3: Step S4: Step S5: Step S6: Step S11: Step S12: Step S13: Step S14: Step S15: Step SH: Shuttle W: Substrate

圖1係表示本發明之一實施方式之包括抗蝕劑剝離的基板處理之一例之步驟圖。 圖2係表示本發明之一實施方式之抗蝕圖案之一例的概略剖視圖。 圖3A-C係用於對本發明之一實施方式之抗蝕劑剝離之一例進行說明的概略圖。 圖3D-F係用於對本發明之一實施方式之抗蝕劑剝離之一例進行說明的概略圖。 圖4係用於說明如下情況之概略圖,即,溶解於基板上之過氧化氫溶液之液滴中之臭氧氣體與過氧化氫溶液中所含之過氧化氫反應而產生羥基自由基。 圖5係表示於硬化層形成有空洞之抗蝕圖案之圖像之一例的鉛直剖視圖。 圖6A-C係用於對本發明之一實施方式之抗蝕劑剝離之另一例進行說明的概略圖。 圖6D係用於對本發明之一實施方式之抗蝕劑剝離之另一例進行說明的概略圖。 圖7係用於說明如下情況之概略圖,即,溶解於基板上之過氧化氫溶液之液膜之臭氧氣體與過氧化氫溶液中所含之過氧化氫反應而產生羥基自由基。 圖8係表示本發明之一實施方式之基板處理裝置之佈局的概略俯視圖。 圖9係表示前處理單元之鉛直剖面之一例之剖視圖。 圖10A係表示熱處理單元之鉛直剖面之一例之剖視圖。 圖10B係表示熱處理單元之鉛直剖面之另一例之剖視圖。 圖11係表示後處理單元之鉛直剖面之一例之剖視圖。 圖12係表示由基板處理裝置執行之基板處理之一例之步驟圖。 Figure 1 is a diagram illustrating steps of an example substrate processing including resist stripping according to an embodiment of the present invention. Figure 2 is a schematic cross-sectional view illustrating an example resist pattern according to an embodiment of the present invention. Figures 3A-C are schematic diagrams illustrating an example resist stripping according to an embodiment of the present invention. Figures 3D-F are schematic diagrams illustrating an example resist stripping according to an embodiment of the present invention. Figure 4 is a schematic diagram illustrating a situation in which ozone gas in droplets of a hydrogen peroxide solution dissolved on a substrate reacts with hydrogen peroxide contained in the hydrogen peroxide solution to generate hydroxyl radicals. Figure 5 is a vertical cross-sectional view of a lead sheet showing an example of an image of a resist pattern with voids formed in a hardened layer. Figures 6A-C are schematic diagrams illustrating another example of resist stripping according to an embodiment of the present invention. Figure 6D is a schematic diagram illustrating another example of resist stripping according to an embodiment of the present invention. Figure 7 is a schematic diagram illustrating the reaction of ozone gas dissolved in a hydrogen peroxide solution film on a substrate with hydrogen peroxide contained in the hydrogen peroxide solution to generate hydroxyl radicals. Figure 8 is a schematic top view illustrating the layout of a substrate processing apparatus according to an embodiment of the present invention. Figure 9 is a cross-sectional view showing an example of a vertical cross section of a pre-processing unit. Figure 10A is a cross-sectional view showing an example of a vertical cross section of a heat treatment unit. Figure 10B is a cross-sectional view showing another example of a vertical cross section of a heat treatment unit. Figure 11 is a cross-sectional view showing an example of a vertical cross section of a post-processing unit. Figure 12 is a diagram showing an example of steps in substrate processing performed by the substrate processing apparatus.

100:抗蝕圖案 100: Anti-corrosion pattern

101:硬化層 101: Hardened layer

102:非硬化部 102: Non-hardened part

103:空洞 103: Hollow

112:三態邊界 112: Three-State Boundary

Claims (7)

一種基板處理方法,其包括:過氧化氫溶液供給步驟,其係對形成有抗蝕圖案之基板之表面供給過氧化氫溶液之霧;及臭氧氣體供給步驟,其係對與上述基板接觸之上述過氧化氫溶液供給臭氧氣體;上述臭氧氣體供給步驟包括如下步驟:在上述過氧化氫溶液之複數個液滴分散於上述基板之表面全域之狀態下,對與上述基板接觸之上述過氧化氫溶液供給上述臭氧氣體。A substrate processing method includes: a hydrogen peroxide solution supplying step of supplying a hydrogen peroxide solution mist to a surface of a substrate having an anti-etching pattern formed thereon; and an ozone gas supplying step of supplying ozone gas to the hydrogen peroxide solution in contact with the substrate. The ozone gas supplying step includes the following steps: supplying the ozone gas to the hydrogen peroxide solution in contact with the substrate while a plurality of hydrogen peroxide solution droplets are dispersed over the entire surface of the substrate. 如請求項1之基板處理方法,其進而包括過氧化氫溶液加熱步驟,其係在將上述過氧化氫溶液供給至上述基板之前或之後,以高於室溫之剝離促進溫度加熱上述過氧化氫溶液。The substrate processing method of claim 1 further comprises a hydrogen peroxide solution heating step, which is to heat the hydrogen peroxide solution at a peeling promotion temperature higher than room temperature before or after the hydrogen peroxide solution is supplied to the substrate. 如請求項2之基板處理方法,其中上述剝離促進溫度未達上述過氧化氫溶液之沸點。The substrate processing method of claim 2, wherein the stripping promotion temperature does not reach the boiling point of the hydrogen peroxide solution. 如請求項2之基板處理方法,其中上述剝離促進溫度未達水之沸點。The substrate processing method of claim 2, wherein the above-mentioned stripping promotion temperature does not reach the boiling point of water. 如請求項2之基板處理方法,其中上述過氧化氫溶液供給步驟包括:初次供給步驟,其係對上述基板之表面供給上述過氧化氫溶液;及再供給步驟,其係在停止向上述基板之表面供給上述過氧化氫溶液後,對上述基板之表面供給上述過氧化氫溶液。The substrate processing method of claim 2, wherein the hydrogen peroxide solution supplying step includes: an initial supplying step of supplying the hydrogen peroxide solution to the surface of the substrate; and a resupplying step of supplying the hydrogen peroxide solution to the surface of the substrate after stopping the supply of the hydrogen peroxide solution to the surface of the substrate. 如請求項1至5中任一項之基板處理方法,其進而包括剝離液供給步驟,其在對與上述基板接觸之上述過氧化氫溶液供給上述臭氧氣體之後,對上述基板之表面供給將上述抗蝕圖案自上述基板之表面剝離之抗蝕劑剝離液。The substrate processing method of any one of claims 1 to 5 further includes a stripping liquid supply step, wherein after supplying the ozone gas to the hydrogen peroxide solution in contact with the substrate, an anti-etching agent stripping liquid is supplied to the surface of the substrate to strip the anti-etching pattern from the surface of the substrate. 一種基板處理裝置,其包括:過氧化氫溶液噴嘴,其係對形成有抗蝕圖案之基板之表面供給過氧化氫溶液之霧;及臭氧噴嘴,其係對與上述基板接觸之上述過氧化氫溶液供給臭氧氣體;上述臭氧噴嘴在上述過氧化氫溶液之複數個液滴分散於上述基板之表面全域之狀態下,對與上述基板接觸之上述過氧化氫溶液供給上述臭氧氣體。A substrate processing apparatus includes: a hydrogen peroxide solution nozzle for supplying a mist of hydrogen peroxide solution to a surface of a substrate having an anti-etching pattern formed thereon; and an ozone nozzle for supplying ozone gas to the hydrogen peroxide solution in contact with the substrate. The ozone nozzle supplies the ozone gas to the hydrogen peroxide solution in contact with the substrate while a plurality of hydrogen peroxide solution droplets are dispersed over the entire surface of the substrate.
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