TW201409188A - Resist removing device and resist removing method - Google Patents

Resist removing device and resist removing method Download PDF

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TW201409188A
TW201409188A TW102125536A TW102125536A TW201409188A TW 201409188 A TW201409188 A TW 201409188A TW 102125536 A TW102125536 A TW 102125536A TW 102125536 A TW102125536 A TW 102125536A TW 201409188 A TW201409188 A TW 201409188A
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sulfuric acid
photoresist
substrate
ozone water
supplied
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TW102125536A
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Chinese (zh)
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TWI497566B (en
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Takatoshi Kinoshita
Takanori Kawanishi
Satoshi Ushida
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Toho Kasei Co Ltd
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/02Manufacture or treatment of semiconductor devices or of parts thereof
    • H01L21/04Manufacture or treatment of semiconductor devices or of parts thereof the devices having at least one potential-jump barrier or surface barrier, e.g. PN junction, depletion layer or carrier concentration layer
    • H01L21/18Manufacture or treatment of semiconductor devices or of parts thereof the devices having at least one potential-jump barrier or surface barrier, e.g. PN junction, depletion layer or carrier concentration layer the devices having semiconductor bodies comprising elements of Group IV of the Periodic System or AIIIBV compounds with or without impurities, e.g. doping materials
    • H01L21/30Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26
    • H01L21/31Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26 to form insulating layers thereon, e.g. for masking or by using photolithographic techniques; After treatment of these layers; Selection of materials for these layers
    • H01L21/3105After-treatment
    • H01L21/311Etching the insulating layers by chemical or physical means
    • H01L21/31127Etching organic layers
    • H01L21/31133Etching organic layers by chemical means
    • 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
    • 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
    • G03F7/422Stripping or agents therefor using liquids only
    • G03F7/423Stripping or agents therefor using liquids only containing mineral acids or salts thereof, containing mineral oxidizing substances, e.g. peroxy compounds
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/67Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere
    • H01L21/67005Apparatus not specifically provided for elsewhere
    • H01L21/67011Apparatus for manufacture or treatment
    • H01L21/67017Apparatus for fluid treatment
    • H01L21/67063Apparatus for fluid treatment for etching
    • H01L21/67075Apparatus for fluid treatment for etching for wet etching
    • H01L21/6708Apparatus for fluid treatment for etching for wet etching using mainly spraying means, e.g. nozzles

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  • Engineering & Computer Science (AREA)
  • General Physics & Mathematics (AREA)
  • Physics & Mathematics (AREA)
  • Microelectronics & Electronic Packaging (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • Manufacturing & Machinery (AREA)
  • Computer Hardware Design (AREA)
  • Power Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Chemical & Material Sciences (AREA)
  • Cleaning Or Drying Semiconductors (AREA)
  • Exposure Of Semiconductors, Excluding Electron Or Ion Beam Exposure (AREA)

Abstract

This resist removing apparatus is provided with: a substrate holding section that holds a substrate having a resist, which has predetermined ions implanted therein, and which has a cured layer formed on the surface thereof; a sulfuric acid supplying section, which has a heater that heats sulfuric acid, and which supplies the sulfuric acid to the substrate being held by means of the substrate holding section, said sulfuric acid being at 200 DEG C or higher by having been heated by means of the heater, and not containing hydrogen peroxide water; and an ozone water supplying section, which supplies ozone water having a concentration of 150 ppm or more to the substrate having been supplied with the sulfuric acid by means of the sulfuric acid supplying section.

Description

光阻去除裝置及光阻去除方法 Photoresist removal device and photoresist removal method 技術領域 Technical field

本發明有關於一種用於去除基板上之光阻之光阻去除裝置及其方法。 The present invention relates to a photoresist removal apparatus and method for removing photoresist on a substrate.

背景技術 Background technique

在半導體裝置之製程中,已利用離子植入技術而進行朝基板及基板之表面上形成之絕緣膜等各種膜植入預定之離子,並改變其表面特性之處理。舉例言之,朝基板表面植入預定之離子,即可於基板表面上形成電晶體之導通部分。 In the process of the semiconductor device, various processes such as an insulating film formed on the surface of the substrate and the substrate are implanted with predetermined ions by ion implantation technology, and the surface characteristics are changed. For example, by implanting a predetermined ion toward the surface of the substrate, a conductive portion of the transistor can be formed on the surface of the substrate.

離子植入處理通常在基板上形成光阻後乃進行,光阻則於離子植入處理後乃去除。然而,業經高劑量離子植入後之光阻將於表面上形成硬化層,故形成難以自基板剝離之狀態。因此,表面設有硬化層之光阻之去除,一般採用對光阻施予電漿灰化處理後,再對基板進行濕洗之方法(參照諸如專利文獻1)。 The ion implantation process is usually performed after the photoresist is formed on the substrate, and the photoresist is removed after the ion implantation process. However, the photoresist after high-dose ion implantation forms a hardened layer on the surface, so that it is difficult to peel off from the substrate. Therefore, the surface is provided with the removal of the photoresist of the hardened layer, and a method of applying a plasma ashing treatment to the photoresist and then wet-cleaning the substrate is generally used (see, for example, Patent Document 1).

濕洗之方法舉例言之,可藉混合有硫酸與過氧化氫水之處理液進行清洗處理。上述清洗處理則稱為 SPM(Sulfuric acid/hydrogen peroxide mixture)清洗。 The method of wet washing can be exemplified by a treatment liquid mixed with sulfuric acid and hydrogen peroxide water. The above cleaning process is called SPM (Sulfuric acid/hydrogen peroxide mixture) cleaning.

【先行技術文獻】 [First technical literature]

【專利文獻】 [Patent Literature]

【專利文獻1】:日本專利特開平7-37780號公報 [Patent Document 1]: Japanese Patent Laid-Open No. Hei 7-37780

發明概要 Summary of invention

然而,依據專利文獻1所揭露之方法,由於實施電漿灰化處理,故基板可能因電漿之破壞而受損。 However, according to the method disclosed in Patent Document 1, since the plasma ashing treatment is performed, the substrate may be damaged by the destruction of the plasma.

且,若考量於電漿灰化後進行濕洗,基板之處理形態大多採用匯總複數基板而加以浸泡於置有處理液之處理槽內以進行處理之批次式。採用批次式,可減少就各片基板使用之處理液量。就各片基板進行處理之單片式使用於各片基板之處理液多於批次式而成本較高,故幾乎未受採用。 Further, in consideration of the wet cleaning after the plasma ashing, the processing form of the substrate is often a batch type in which a plurality of substrates are stacked and immersed in a treatment tank in which the treatment liquid is placed for treatment. The batch type can reduce the amount of treatment liquid used for each substrate. The single-chip type processing for each substrate is more expensive than the batch type, and is hardly used.

另,批次式之電漿灰化與SPM清洗組合而成之習知之光阻去除方法僅就個別之製程各進行1次,而無法充分去除光阻,故可能必須就個別之製程各進行多次。進而,批次式之SPM清洗無法充分去除光阻中所含之金屬等雜質,故可能發生金屬污染。因此,SPM清洗後必須另藉混合有鹽酸與過氧化氫水之處理液進行HPM(hydrochloric acid/hydrogen peroxide mixture)清洗等以去除金屬殘渣。 In addition, the conventional photoresist removal method combined with batch plasma ashing and SPM cleaning is performed only once for each individual process, and the photoresist cannot be sufficiently removed, so it may be necessary to carry out separate processes for individual processes. Times. Further, the batch type SPM cleaning cannot sufficiently remove impurities such as metals contained in the photoresist, so metal contamination may occur. Therefore, after the SPM cleaning, it is necessary to carry out HPM (hydrochloric acid/hydrogen peroxide mixture) cleaning or the like by mixing a treatment liquid containing hydrochloric acid and hydrogen peroxide water to remove the metal residue.

如上所述,習知之光阻去除方法採用批次式,而可較單片式更為減少使用之處理液量,但去除預定量之光 阻所需之製程較多,時間較長。換言之,無法充份兼顧使用之處理液量之減少及光阻之去除效率。 As described above, the conventional photoresist removal method adopts a batch type, and the amount of the treatment liquid used can be reduced more than the single sheet type, but the predetermined amount of light is removed. The process required for the resistance is more and the time is longer. In other words, it is not possible to fully balance the reduction in the amount of the treatment liquid used and the efficiency of removing the photoresist.

因此,本發明之目的即在解決上述問題,而提供可減少對基板造成之損傷,並減少使用之處理液量且有效率地去除光阻之光阻去除裝置及其方法。 Accordingly, an object of the present invention is to solve the above problems, and to provide a photoresist removing apparatus and a method thereof which can reduce damage to a substrate, reduce the amount of processing liquid used, and efficiently remove the photoresist.

為達成上述目的,本發明構成如下。 In order to achieve the above object, the present invention is constituted as follows.

依據本發明第1態樣,可提供一種光阻去除裝置,係用於自基板去除光阻者,其包含有:基板保持部,係用於保持設有已植入預定之離子而於表面上形成有硬化層之光阻之基板者;硫酸供給部,係設有用於加熱硫酸之加熱器,而可朝基板保持部所保持之基板供給已藉加熱器加熱至200℃以上之不含過氧化氫水之硫酸者;及,臭氧水供給部,係可對已藉硫酸供給部供給硫酸之基板供給濃度150ppm以上之臭氧水者。 According to a first aspect of the present invention, there is provided a photoresist removing apparatus for removing a photoresist from a substrate, comprising: a substrate holding portion for holding a predetermined implanted ion on the surface a substrate having a photoresist having a hardened layer; a sulfuric acid supply portion provided with a heater for heating sulfuric acid, and a substrate for holding the substrate held by the substrate holding portion to be heated to 200 ° C or higher without peroxidation And the ozone water supply unit is capable of supplying ozone water having a concentration of 150 ppm or more to a substrate to which sulfuric acid is supplied from a sulfuric acid supply unit.

依據本發明第2態樣,可提供如第1態樣所揭露之光阻去除裝置,且其為單片式。 According to a second aspect of the present invention, there is provided a photoresist removal apparatus as disclosed in the first aspect, which is monolithic.

依據本發明第3態樣,可提供如第1態樣或第2態樣所揭露之光阻去除裝置,其中硫酸供給部係供給已部分熱分解之硫酸。 According to a third aspect of the present invention, there is provided a photoresist removal apparatus as disclosed in the first aspect or the second aspect, wherein the sulfuric acid supply unit supplies the partially thermally decomposed sulfuric acid.

依據本發明第4態樣,可提供如第3態樣所揭露之光阻去除裝置,其係供給整體中之1~20%已熱分解之硫酸。 According to a fourth aspect of the present invention, there is provided a photoresist removal apparatus as disclosed in the third aspect, which supplies 1 to 20% of the thermally decomposed sulfuric acid in the whole.

依據本發明第5態樣,可提供如第1態樣至第4態樣中任一態樣所揭露之光阻去除裝置,其中硫酸供給部所 供給之200℃以上之硫酸可對光阻施加熱應力而對光阻造成損傷。 According to a fifth aspect of the present invention, there is provided a photoresist removal apparatus as disclosed in any of the first aspect to the fourth aspect, wherein the sulfuric acid supply unit Sulfuric acid supplied at 200 ° C or higher can cause thermal stress to the photoresist to cause damage to the photoresist.

依據本發明第6態樣,可提供如第5態樣所揭露之光阻去除裝置,其中損傷為裂痕。 According to a sixth aspect of the present invention, there is provided a photoresist removing apparatus as disclosed in the fifth aspect, wherein the damage is a crack.

依據本發明第7態樣,可提供如第1態樣至第6態樣中任一態樣所揭露之光阻去除裝置,其中臭氧水供給部係供給50℃以上之臭氧水。 According to a seventh aspect of the present invention, there is provided a photoresist removal apparatus according to any one of the first aspect to the sixth aspect, wherein the ozone water supply unit supplies ozone water of 50 ° C or more.

依據本發明第8態樣,可提供如第1態樣至第7態樣中任一態樣所揭露之光阻去除裝置,其係在已藉基板保持部旋轉基板之狀態下對基板進行硫酸及臭氧水之供給。 According to an eighth aspect of the present invention, there is provided a photoresist removal apparatus according to any one of the first aspect to the seventh aspect, wherein the substrate is subjected to sulfuric acid in a state in which the substrate is rotated by the substrate holding portion. And the supply of ozone water.

依據本發明第9態樣,可提供一種光阻去除方法,用於自基板去除光阻,其包含以下步驟:硫酸供給步驟,係於基板上形成之光阻上,朝已藉離子之植入而形成有硬化層之光阻表面上,供給不含過氧化氫水之200℃以上之硫酸;及,臭氧水供給步驟,係朝業經硫酸供給步驟供給硫酸之光阻表面,供給濃度150ppm以上之臭氧水。 According to a ninth aspect of the present invention, a photoresist removal method for removing photoresist from a substrate includes the following steps: a sulfuric acid supply step, which is performed on a photoresist formed on a substrate, and implanted with ions On the surface of the photoresist on which the hardened layer is formed, sulfuric acid containing 200 ° C or more containing no hydrogen peroxide water is supplied; and the ozone water supply step is supplied to the surface of the photoresist of sulfuric acid by a sulfuric acid supply step, and the supply concentration is 150 ppm or more. Ozone water.

依據本發明第10態樣,可提供如第9態樣所揭露之光阻去除方法,其係以單片式進行基板之處理。 According to a tenth aspect of the present invention, there is provided a photoresist removal method as disclosed in the ninth aspect, wherein the substrate is processed in a single chip.

依據本發明第11態樣,可提供如第9態樣或第10態樣所揭露之光阻去除方法,其於硫酸供給步驟中供給已部分熱分解之硫酸。 According to an eleventh aspect of the present invention, there is provided a photoresist removal method as disclosed in the ninth aspect or the tenth aspect, which supplies the partially thermally decomposed sulfuric acid in the sulfuric acid supply step.

依據本發明第12態樣,可提供如第11態樣所揭露之光阻去除方法,其於硫酸供給步驟中供給整體中之1~20%已熱分解之硫酸。 According to a twelfth aspect of the present invention, there is provided a photoresist removal method as disclosed in the eleventh aspect, which supplies 1 to 20% of the thermally decomposed sulfuric acid in the whole in the sulfuric acid supply step.

依據本發明第13態樣,可提供如第9態樣至第12態樣中任一態樣所揭露之光阻去除方法,其於硫酸供給步驟中所供給之200℃以上之硫酸對光阻施加熱應力而對光阻造成損傷。 According to a thirteenth aspect of the present invention, there is provided a photoresist removal method as disclosed in any one of the ninth aspect to the twelfth aspect, wherein the sulfuric acid to the photoresist which is supplied at a temperature of 200 ° C or higher supplied in the sulfuric acid supply step Applying heating stress causes damage to the photoresist.

依據本發明第14態樣,可提供如第13態樣所揭露之光阻去除方法,其中損傷為裂痕。 According to a fourteenth aspect of the present invention, there is provided a photoresist removal method as disclosed in the thirteenth aspect, wherein the damage is a crack.

依據本發明第15態樣,可提供如第9態樣至第14態樣中任一態樣所揭露之光阻去除方法,其於臭氧水供給步驟中供給50℃以上之臭氧水。 According to a fifteenth aspect of the present invention, there is provided a photoresist removal method as disclosed in any one of the ninth aspect to the fourteenth aspect, which supplies ozone water of 50 ° C or more in the ozone water supply step.

依據本發明第16態樣,可提供如第9態樣至第15態樣中任一態樣所揭露之光阻去除方法,其於硫酸供給步驟及臭氧水供給步驟中使基板呈旋轉狀態。 According to a sixteenth aspect of the present invention, there is provided a photoresist removal method as disclosed in any one of the ninth aspect to the fifteenth aspect, wherein the substrate is rotated in the sulfuric acid supply step and the ozone water supply step.

光阻去除裝置及其方法可減少對基板造成之損傷,並減少使用之處理液量且可有效率地去除光阻。 The photoresist removing device and method thereof can reduce damage to the substrate, reduce the amount of processing liquid used, and efficiently remove the photoresist.

1‧‧‧光阻去除裝置 1‧‧‧Light removal device

2‧‧‧基板 2‧‧‧Substrate

3‧‧‧基板保持裝置 3‧‧‧Substrate holder

4‧‧‧硫酸供給部 4‧‧‧Sulphuric Acid Supply Department

5‧‧‧臭氧水供給部 5‧‧‧Ozone Water Supply Department

6‧‧‧載台 6‧‧‧ stage

7‧‧‧旋轉軸 7‧‧‧Rotary axis

8‧‧‧旋轉台 8‧‧‧Rotating table

9‧‧‧光阻 9‧‧‧Light resistance

10‧‧‧導通部分 10‧‧‧Connected section

11‧‧‧硬化層 11‧‧‧ hardened layer

12‧‧‧加熱器 12‧‧‧heater

13‧‧‧供給口 13‧‧‧ supply port

14‧‧‧供給口 14‧‧‧ supply port

15‧‧‧裂痕 15‧‧‧ crack

C-G‧‧‧測定點 C-G‧‧‧ measuring point

S1-S4‧‧‧流程步驟 S1-S4‧‧‧ Process Steps

本發明之上述態樣與特徵可由附圖相關之較佳實施形態之相關以下記載而清楚明瞭。 The above-described aspects and features of the present invention are apparent from the following description of the preferred embodiments.

圖1為本發明之實施形態之光阻去除裝置1之截面圖。 Fig. 1 is a cross-sectional view showing a photoresist removal apparatus 1 according to an embodiment of the present invention.

圖2(a)~(b)為本實施形態所使用之基板2之截面圖。 2(a) to 2(b) are cross-sectional views of the substrate 2 used in the present embodiment.

圖3為本實施形態所使用之硫酸供給部4之截面圖。 Fig. 3 is a cross-sectional view showing the sulfuric acid supply unit 4 used in the present embodiment.

圖4為顯示光阻去除之步驟之流程圖。 Figure 4 is a flow chart showing the steps of photoresist removal.

圖5(a)~(c)為顯示圖4之流程圖所對應之光阻去除裝置1之動作之截面圖。 5(a) to 5(c) are cross-sectional views showing the operation of the photoresist removing device 1 corresponding to the flowchart of Fig. 4.

圖6(a)~(d)為說明光阻去除裝置1所進行之光阻去除之原理之說明圖。 6(a) to 6(d) are explanatory views for explaining the principle of photoresist removal by the photoresist removing device 1.

圖7為實施例中使用之基板2之俯視圖。 Fig. 7 is a plan view of the substrate 2 used in the embodiment.

圖8(a)~(b)顯示實施例1之金屬殘渣量之測定結果。 8(a) to (b) show the results of measurement of the amount of metal residue in Example 1.

圖9(a)~(b)顯示實施例2之金屬殘渣量之測定結果。 9(a) to (b) show the results of measurement of the amount of metal residue in Example 2.

用以實施發明之形態 Form for implementing the invention

以下,參照附圖詳細說明本發明之實施形態。 Hereinafter, embodiments of the present invention will be described in detail with reference to the accompanying drawings.

圖1為本發明之實施形態之光阻去除裝置1之截面圖。光阻去除裝置1包含可保持基板2之基板保持裝置3、硫酸供給部4及臭氧水供給部5。 Fig. 1 is a cross-sectional view showing a photoresist removal apparatus 1 according to an embodiment of the present invention. The photoresist removal device 1 includes a substrate holding device 3 that can hold the substrate 2, a sulfuric acid supply unit 4, and an ozone water supply unit 5.

基板保持裝置3包含載台6與旋轉台8。載台6可於上面載置藉未圖示之搬送機構送至之基板2而加以保持。旋轉台8則可支持載台6,並以朝垂直方向延伸之旋轉軸7為中心而使載台6及載台6上所載置之基板2一體進行旋轉。圖1即顯示已藉基板保持裝置3而保持基板2之狀態。 The substrate holding device 3 includes a stage 6 and a rotary table 8. The stage 6 can hold and hold the substrate 2 to which the transport mechanism (not shown) is transported. The turntable 8 supports the stage 6, and integrally rotates the stage 6 and the substrate 2 placed on the stage 6 around the rotating shaft 7 extending in the vertical direction. FIG. 1 shows a state in which the substrate 2 has been held by the substrate holding device 3.

硫酸供給部4設於基板保持裝置3之載台6之上方,並連接未圖示之硫酸供給源,內部則保存有硫酸(不含過氧化氫水)。硫酸供給部4構成可朝位在下方之載台6上之基板2之表面上滴下內部所保存之硫酸。另,本實施形態中,硫酸供給部4所供給之硫酸之溫度設為200℃以上。 The sulfuric acid supply unit 4 is provided above the stage 6 of the substrate holding device 3, and is connected to a sulfuric acid supply source (not shown), and contains sulfuric acid (without hydrogen peroxide water) inside. The sulfuric acid supply unit 4 constitutes the sulfuric acid stored inside the substrate 2 which can be placed on the lower stage 6 below. In the present embodiment, the temperature of the sulfuric acid supplied from the sulfuric acid supply unit 4 is set to 200 ° C or higher.

臭氧水供給部5設於載台6之上方而位置與配置硫酸供給部4之位置不同,並連接未圖示之臭氧水供給源,內部保存有臭氧水。與硫酸供給部4相同,臭氧水供給部5 構成可朝位在下方之基板2之表面上滴下內部保存之臭氧水。本實施形態中,臭氧水供給部5所供給之臭氧水之濃度設為150ppm以上,溫度設為50℃以上。 The ozone water supply unit 5 is disposed above the stage 6 at a position different from the position at which the sulfuric acid supply unit 4 is disposed, and is connected to an ozone water supply source (not shown), and contains ozone water therein. The ozone water supply unit 5 is the same as the sulfuric acid supply unit 4. The internally stored ozone water is dripped on the surface of the substrate 2 which is positioned below. In the present embodiment, the concentration of the ozone water supplied from the ozone water supply unit 5 is 150 ppm or more, and the temperature is 50 ° C or higher.

上述之硫酸供給部4及臭氧水供給部5均構成可朝沿行基板2之表面之方向(本實施形態中為圖中之左右方向)而移動。 Each of the sulfuric acid supply unit 4 and the ozone water supply unit 5 described above is configured to be movable in the direction along the surface of the row substrate 2 (the horizontal direction in the drawing in the present embodiment).

另,上述光阻去除裝置1之基板保持裝置3、硫酸供給部4及臭氧水供給部5之動作並為同樣設於光阻去除裝置1之未圖示之控制裝置所控制。 The operation of the substrate holding device 3, the sulfuric acid supply unit 4, and the ozone water supply unit 5 of the photoresist removal device 1 is controlled by a control device (not shown) similarly provided in the photoresist removal device 1.

以下,參照圖2說明本實施形態之處理對象之基板2。 Hereinafter, the substrate 2 to be processed in the present embodiment will be described with reference to Fig. 2 .

圖2為顯示本實施形態所使用之基板2之製造方法之截面圖。本實施形態中,特別使用可植入高劑量離子(諸如砷等)之基板2。圖2(a)顯示離子植入前之基板2,圖2(b)顯示離子植入後之基板2(本實施形態所使用之基板2)。 Fig. 2 is a cross-sectional view showing a method of manufacturing the substrate 2 used in the embodiment. In the present embodiment, the substrate 2 implantable with a high dose of ions such as arsenic or the like is particularly used. Fig. 2(a) shows the substrate 2 before ion implantation, and Fig. 2(b) shows the substrate 2 after ion implantation (substrate 2 used in the present embodiment).

如圖2(a)所示,對離子植入前之基板2於其上面配置已圖案化之光阻9。一旦對上述基板2植入高劑量離子,則相鄰之光阻9之間露出之基板2之表面上將形成諸如導通部分10。 As shown in FIG. 2(a), the patterned photoresist 1 is placed on the substrate 2 before ion implantation. Once the high dose ion is implanted into the substrate 2, a surface such as the conductive portion 10 will be formed on the surface of the substrate 2 exposed between the adjacent photoresists 9.

另,直接曝露於高劑量離子之光阻9之表面上,將因與離子之反應而形成難以剝離之硬化層11。如圖2(b)所示,本實施形態所使用之基板2上配置有表面上形成有硬化層11之光阻9。 Further, it is directly exposed to the surface of the high-dose ion photoresist 9, and a hardened layer 11 which is difficult to peel off is formed by the reaction with ions. As shown in FIG. 2(b), the substrate 2 used in the present embodiment is provided with a photoresist 9 having a hardened layer 11 formed on its surface.

以下,參照圖3說明本實施形態之光阻去除裝置1 之硫酸供給部4。 Hereinafter, the photoresist removal apparatus 1 of the present embodiment will be described with reference to FIG. Sulfuric acid supply unit 4.

圖3為本實施形態所使用之硫酸供給部4之截面圖。如圖3所示,保存有硫酸之硫酸供給部4內,於中央部配置有加熱用之加熱器12。藉加熱器12加熱硫酸供給部4內之硫酸,即可自位在硫酸供給部4之下游側端部之供給口13供給已調整為200℃以上之硫酸。 Fig. 3 is a cross-sectional view showing the sulfuric acid supply unit 4 used in the present embodiment. As shown in FIG. 3, in the sulfuric acid supply unit 4 in which sulfuric acid is stored, a heater 12 for heating is disposed in the center portion. By heating the sulfuric acid in the sulfuric acid supply unit 4 by the heater 12, the sulfuric acid adjusted to 200 ° C or higher can be supplied from the supply port 13 at the downstream end of the sulfuric acid supply unit 4 .

進而詳細說明硫酸供給部4之內部,則硫酸供給部4內,硫酸之溫度隨著與加熱器12之距離而不同。即,位在加熱器12附近之硫酸易受加熱而溫度較高,相對於此,位置遠離加熱器12之硫酸不易受加熱而溫度相對較低。硫酸供給部4內存在加熱至200℃以下之硫酸及加熱至200℃以上之硫酸,但混合該等不同溫度之硫酸而加以供給,即可自供給口13供給最終仍為200℃以上之硫酸。 Further, the inside of the sulfuric acid supply unit 4 will be described in detail, and the temperature of the sulfuric acid in the sulfuric acid supply unit 4 will differ depending on the distance from the heater 12. That is, the sulfuric acid located in the vicinity of the heater 12 is easily heated and the temperature is high. On the other hand, the sulfuric acid which is located away from the heater 12 is not easily heated and the temperature is relatively low. In the sulfuric acid supply unit 4, sulfuric acid heated to 200 ° C or lower and sulfuric acid heated to 200 ° C or higher are present, but by supplying sulfuric acid at different temperatures and supplying them, sulfuric acid which is finally at 200 ° C or higher can be supplied from the supply port 13 .

又,硫酸之熱分解溫度約為292℃。因此,構成如上之硫酸供給部4中,存在已於292℃以上之溫度下熱分解之硫酸,以及於292℃以下之溫度下尚未熱分解之硫酸。最後則在該等已熱分解之硫酸與未熱分解之硫酸之混合狀態下加以供給,即可自供給口13供給呈部分熱分解狀態之硫酸。 Further, the thermal decomposition temperature of sulfuric acid is about 292 °C. Therefore, in the sulfuric acid supply unit 4 configured as described above, sulfuric acid which has been thermally decomposed at a temperature of 292 ° C or higher and sulfuric acid which has not been thermally decomposed at a temperature of 292 ° C or lower are present. Finally, it is supplied in a state in which the thermally decomposed sulfuric acid and the non-thermally decomposed sulfuric acid are mixed, and the sulfuric acid in a partially thermally decomposed state can be supplied from the supply port 13.

依據構成如上之硫酸供給部4,即可自供給口13供給呈部分熱分解狀態之200℃以上之硫酸。 According to the sulfuric acid supply unit 4 configured as described above, sulfuric acid of 200 ° C or higher in a partially thermally decomposed state can be supplied from the supply port 13 .

以下,說明使用本發明之光阻去除裝置1而進行之光阻去除之具體步驟。進行說明時,以圖4為顯示光阻去除之步驟之流程圖,並以圖5顯示用於說明圖4之流程圖所 示之各步驟之光阻去除裝置1之動作。 Hereinafter, specific steps of photo-resistance removal using the photoresist removal apparatus 1 of the present invention will be described. For the description, a flow chart showing the steps of photoresist removal is shown in FIG. 4, and FIG. 5 is used to illustrate the flowchart of FIG. The operation of the photoresist removal device 1 shown in each step.

(基板旋轉步驟) (substrate rotation step)

如圖4所示,先使基板保持裝置3上所保持之基板2進行旋轉(步驟S1)。具體而言,乃如圖5(a)所示,藉基板保持裝置3之旋轉台8以旋轉軸7為中心而旋轉載台6,以使載台6及載台6上所載置之基板2一體進行旋轉。 As shown in FIG. 4, the substrate 2 held on the substrate holding device 3 is first rotated (step S1). Specifically, as shown in FIG. 5( a ), the stage 6 is rotated around the rotary shaft 7 by the rotary table 8 of the substrate holding device 3 so that the substrate 6 and the substrate placed on the stage 6 are placed. 2 rotates in one.

(硫酸供給步驟) (sulfuric acid supply step)

其次,對已以旋轉軸7為中心而旋轉之基板2,自硫酸供給部4供給硫酸(步驟S2)。具體而言,乃如圖5(b)所示,控制硫酸供給部4而使其朝沿行基板2之表面之方向移動,並自硫酸供給部4之供給口13朝下方滴下不含過氧化氫水之硫酸。藉此,而朝基板2之表面供給硫酸。朝旋轉狀態之基板2供給硫酸,即可朝基板2表面整體上供給不含過氧化氫水之200℃以上之硫酸。 Next, sulfuric acid is supplied from the sulfuric acid supply unit 4 to the substrate 2 that has been rotated around the rotating shaft 7 (step S2). Specifically, as shown in FIG. 5(b), the sulfuric acid supply unit 4 is controlled to move in the direction along the surface of the row substrate 2, and is dripped downward from the supply port 13 of the sulfuric acid supply unit 4 without peroxidation. Sulfuric acid in hydrogen water. Thereby, sulfuric acid is supplied to the surface of the substrate 2. By supplying sulfuric acid to the substrate 2 in a rotating state, sulfuric acid of 200 ° C or higher containing no hydrogen peroxide water can be supplied to the entire surface of the substrate 2 .

然後,待預定時間經過後,停止硫酸供給部4之硫酸供給及硫酸供給部4之移動。 Then, after the lapse of the predetermined time, the supply of sulfuric acid in the sulfuric acid supply unit 4 and the movement of the sulfuric acid supply unit 4 are stopped.

(臭氧水供給步驟) (Ozone water supply step)

接著,對已於步驟S2中業經供給硫酸之基板2,自臭氧水供給部5供給臭氧水(步驟S3)。具體而言,與步驟S2相同而如圖5(c)所示,乃控制臭氧水供給部5而使其朝沿行基板2之表面之方向移動,並自臭氧水供給部5之供給口14朝下方滴下臭氧水。藉此,即可朝基板2表面整體上供給濃度150ppm以上、溫度50℃以上之臭氧水。 Next, ozone water is supplied from the ozone water supply unit 5 to the substrate 2 to which sulfuric acid has been supplied in step S2 (step S3). Specifically, similarly to step S2, as shown in FIG. 5(c), the ozone water supply unit 5 is controlled to move in the direction along the surface of the row substrate 2, and from the supply port 14 of the ozone water supply unit 5. Drain the ozone water downwards. Thereby, ozone water having a concentration of 150 ppm or more and a temperature of 50 ° C or higher can be supplied to the entire surface of the substrate 2.

然後,待預定時間經過後,停止臭氧水供給部5 之臭氧水供給及臭氧水供給部5之移動。 Then, after the predetermined time elapses, the ozone water supply unit 5 is stopped. The ozone water supply and the movement of the ozone water supply unit 5.

(基板旋轉停止步驟) (substrate rotation stop step)

最後,停止基板2之旋轉(步驟S4)。具體而言,乃停止旋轉台8所致載台6之旋轉,而使基板2之旋轉停止。 Finally, the rotation of the substrate 2 is stopped (step S4). Specifically, the rotation of the stage 6 caused by the rotary table 8 is stopped, and the rotation of the substrate 2 is stopped.

如上所述,實施步驟S1-S4,即可在朝基板2之表面供給不含過氧化氫水之200℃以上之硫酸後,再供給濃度150ppm以上之臭氧水。 As described above, by performing steps S1 to S4, it is possible to supply ozone water having a concentration of 150 ppm or more after supplying sulfuric acid of 200 ° C or higher containing no hydrogen peroxide water to the surface of the substrate 2 .

以下,參照圖6所示之基板2之截面圖說明上述步驟S1-S4所進行光阻去除之原理。 Hereinafter, the principle of photoresist removal performed in the above steps S1 - S4 will be described with reference to a cross-sectional view of the substrate 2 shown in FIG.

圖6(a)顯示硫酸及臭氧水之供給前之基板2。如圖6(a)所示,對設有表面上形成有硬化層11之光阻9之基板2,如步驟S2之說明般供給硫酸,將損傷光阻9表面上形成之硬化層11。具體而言,朝硬化層11上供給之硫酸乃在200℃以上之高溫狀態下進行供給,而對硬化層11施加熱應力。如圖6(b)所示,熱應力所致損傷之一例之裂痕15將形成於硬化層11上。形成裂痕15,藉此即可使溶劑等經裂痕15而滲入至位在硬化層11下方之未硬化之光阻9。 Fig. 6(a) shows the substrate 2 before the supply of sulfuric acid and ozone water. As shown in Fig. 6(a), the substrate 2 provided with the photoresist 9 having the hardened layer 11 formed on its surface is supplied with sulfuric acid as described in the step S2, and the hardened layer 11 formed on the surface of the photoresist 9 is damaged. Specifically, the sulfuric acid supplied to the hardened layer 11 is supplied at a high temperature of 200 ° C or higher, and thermal stress is applied to the hardened layer 11 . As shown in Fig. 6(b), a crack 15 which is one example of damage due to thermal stress is formed on the hardened layer 11. The crack 15 is formed, whereby the solvent or the like is allowed to penetrate into the uncured photoresist 9 under the hardened layer 11 via the crack 15 .

如上所述,在硬化層11上形成有裂痕15之狀態下,繼續自硫酸供給部4供給硫酸,硫酸將滲入裂痕15內。滲入裂痕15內之硫酸將進而朝下方滲透,而可滲入至未硬化之光阻9。 As described above, in a state where the crack 15 is formed on the hardened layer 11, sulfuric acid is continuously supplied from the sulfuric acid supply unit 4, and sulfuric acid penetrates into the crack 15. The sulfuric acid that has penetrated into the crack 15 will in turn penetrate downward and penetrate into the uncured photoresist 9 .

在此,硫酸供給部4所供給之硫酸一如前述呈部分熱分解狀態。故而,包含藉熱分解而產生之SO3離子。如上所述,SO3離子與硫酸在混合狀態下供至未硬化之光阻 9,將於光阻9發生SO3離子所致之氧化反應及硫酸所致之還原反應。藉此,而如圖6(c)所示,將大幅降低光阻9與其下之基板2之附著力(一部分光阻9將自基板2剝離)。另,硬化層11即便利用上述SO3離子與硫酸之組合所致之氧化還原反應,亦幾乎無法與光阻9發生剝離。 Here, the sulfuric acid supplied from the sulfuric acid supply unit 4 is partially thermally decomposed as described above. Therefore, it contains SO 3 ions generated by thermal decomposition. As described above, the SO 3 ion and the sulfuric acid are supplied to the uncured photoresist 9 in a mixed state, and an oxidation reaction by SO 3 ions and a reduction reaction by sulfuric acid are caused in the photoresist 9 . Thereby, as shown in FIG. 6(c), the adhesion of the photoresist 9 to the substrate 2 under it is greatly reduced (a part of the photoresist 9 is peeled off from the substrate 2). Further, even if the hardened layer 11 is subjected to the redox reaction by the combination of the above SO 3 ions and sulfuric acid, it is almost impossible to peel off from the photoresist 9 .

其次,對如上而設有附著力已降低之光阻9之基板2,如步驟S3之說明般供給臭氧水,將如圖6(d)所示,藉臭氧水所致之光阻9之剝離作用,而可自基板2上去除光阻9及硬化層11。如此即可自基板2去除光阻9。另,將臭氧水之濃度設為150ppm以上,提高臭氧水之反應性,則可安定且快速地去除光阻9。且,將臭氧水之溫度設為50度以上,提高臭氧水之反應性,即可進而安定且快速地去除光阻9。 Next, the substrate 2 having the photoresist 9 having the reduced adhesion as described above is supplied with ozone water as described in the step S3, and as shown in Fig. 6(d), the photoresist 9 is stripped by the ozone water. The photoresist 9 and the hardened layer 11 can be removed from the substrate 2. Thus, the photoresist 9 can be removed from the substrate 2. Further, by setting the concentration of the ozone water to 150 ppm or more and increasing the reactivity of the ozone water, the photoresist 9 can be removed stably and quickly. Further, by setting the temperature of the ozone water to 50 degrees or more and increasing the reactivity of the ozone water, the photoresist 9 can be removed stably and quickly.

以上,依據本實施形態之光阻去除裝置1,可於基板2上形成之光阻9上,朝已藉離子之植入而形成有硬化層11之光阻9表面上,供給不含過氧化氫水之200℃以上之硫酸,再朝業經供給硫酸之光阻9表面上供給濃度150ppm以上之臭氧水。如此,即可藉所謂濕式處理而進行光阻9之去除,故可避免採用電漿灰化等時所發生之電漿所造成對基板2之損傷。且,藉硫酸而降低光阻9與基板2之附著力後,乃藉臭氧水進行光阻9之剝離,並將此時硫酸之溫度設為200℃以上,臭氧水之濃度設為150ppm以上,而將處理液之反應性保持在預定程度以上。藉此,即可有效率地進行光阻之去除,並減少使用之處理液量。且,使用濃度150ppm以上之臭氧水去除光阻9,即可一併去除光阻9中所含之金 屬等。即,可以使用臭氧水之光阻去除處理取代所謂之沖洗處理,故可省略HPM等清洗處理。 As described above, according to the photoresist removal apparatus 1 of the present embodiment, the photoresist 9 formed on the substrate 2 can be supplied to the surface of the photoresist 9 on which the hardened layer 11 is formed by implantation of ions, and the supply is free of peroxidation. Sulfuric acid having a temperature of 200 ° C or higher in hydrogen water is supplied with ozone water having a concentration of 150 ppm or more on the surface of the photoresist 9 to which sulfuric acid is supplied. Thus, the removal of the photoresist 9 can be performed by the so-called wet processing, so that damage to the substrate 2 caused by the plasma generated when plasma ashing or the like is caused can be avoided. Further, after the adhesion between the photoresist 9 and the substrate 2 is lowered by sulfuric acid, the photoresist 9 is stripped by ozone water, and the temperature of the sulfuric acid is set to 200 ° C or higher, and the concentration of the ozone water is 150 ppm or more. The reactivity of the treatment liquid is maintained above a predetermined level. Thereby, the removal of the photoresist can be efficiently performed, and the amount of the treatment liquid used can be reduced. Moreover, by removing the photoresist 9 by using ozone water having a concentration of 150 ppm or more, the gold contained in the photoresist 9 can be removed at the same time. Affiliate. That is, the so-called rinsing treatment can be replaced with the photoresist removal treatment of ozone water, so that the cleaning treatment such as HPM can be omitted.

又,本實施形態中,採用單片式而非批次式進行基板2之處理,而可較批次式更為擴大基板2上之熱分佈,故可提昇硫酸及臭氧水之反應性,而提昇光阻9之去除力。如此,即可有效率地進行光阻之去除。 Moreover, in the present embodiment, the processing of the substrate 2 is performed in a single piece instead of a batch type, and the heat distribution on the substrate 2 can be further enlarged than the batch type, so that the reactivity of sulfuric acid and ozone water can be improved, and Increase the removal force of the photoresist 9. In this way, the removal of the photoresist can be performed efficiently.

又,本實施形態中,乃供給呈部分熱分解狀態之硫酸,故除硫酸之還原反應以外,尚可利用硫酸之熱分解所致生之SO3離子所導致之氧化反應。藉此,而可提昇光阻9之去除力,並有效率地進行光阻去除。另,宜使硫酸整體中之1~20%以上熱分解。依上述比率供給硫酸,即可更有效地利用氧化還原反應。 Further, in the present embodiment, since the sulfuric acid in a partially thermally decomposed state is supplied, in addition to the reduction reaction of sulfuric acid, the oxidation reaction by the SO 3 ions generated by the thermal decomposition of sulfuric acid can be utilized. Thereby, the removal force of the photoresist 9 can be improved, and the photoresist removal can be performed efficiently. In addition, it is preferred to thermally decompose more than 1 to 20% of the entire sulfuric acid. By supplying sulfuric acid at the above ratio, the redox reaction can be utilized more efficiently.

又,本實施形態中,朝基板2供給之硫酸之溫度設為200℃以上,即可對光阻9施加熱應力而損傷之。藉此,而可使硫酸安定地滲入光阻9內,並有效率地進行光阻去除。 Further, in the present embodiment, the temperature of the sulfuric acid supplied to the substrate 2 is set to 200 ° C or higher, and thermal stress can be applied to the photoresist 9 to be damaged. Thereby, sulfuric acid can be stably infiltrated into the photoresist 9 and the photoresist can be removed efficiently.

又,本實施形態中,供給50℃以上之臭氧水,而可提昇臭氧水之光阻去除力。如此即可有效率地進行光阻之去除。 Further, in the present embodiment, ozone water of 50 ° C or more is supplied, and the photoresist removal power of ozone water can be enhanced. In this way, the removal of the photoresist can be performed efficiently.

又,本實施形態中,在基板2已旋轉之狀態下進行硫酸及臭氧水之供給,而可朝基板2上均勻地供給硫酸及臭氧水,並自基板2上均勻地去除光阻9。 Further, in the present embodiment, the supply of sulfuric acid and ozone water is performed while the substrate 2 is rotated, and sulfuric acid and ozone water can be uniformly supplied onto the substrate 2, and the photoresist 9 can be uniformly removed from the substrate 2.

(實施例) (Example)

以下,參照圖7-9說明使用構成如上之光阻去除裝置1 之實施例。本實施例乃於基板2上預先設定複數之測定點後,再對基板2實施上述步驟S1-S4之相同製程,並就上述實施前後之基板2上之金屬殘渣量進行測定。 Hereinafter, the use of the photoresist removing device 1 configured as above will be described with reference to FIGS. 7-9. An embodiment. In the present embodiment, after a plurality of measurement points are set in advance on the substrate 2, the same processes as the above steps S1 to S4 are performed on the substrate 2, and the amount of metal residue on the substrate 2 before and after the above-described implementation is measured.

圖7為顯示本實施例所使用之基板2之俯視圖。本實施例使用直徑約300mm之基板2。如圖7所示,基板2上設定有5點之測定點C-G。測定點C配置於俯視時呈大致圓形之基板2之中心,其餘之測定點D-G則相隔大致等間隔而配置於距中心之測定點C約70mm之位置上。基板2之種類則準備有在光阻去除裝置1之處理前已業經強制汙染之基板,以及未經強制汙染之基板之2種。 Fig. 7 is a plan view showing the substrate 2 used in the present embodiment. This embodiment uses a substrate 2 having a diameter of about 300 mm. As shown in FIG. 7, the measurement point C-G of 5 points is set on the board|substrate 2. The measurement point C is disposed at the center of the substantially circular substrate 2 in plan view, and the remaining measurement points D-G are disposed at approximately 70 mm from the center measurement point C at substantially equal intervals. The type of the substrate 2 is prepared by a substrate which has been forcibly contaminated before the processing of the photoresist removing device 1 and a substrate which is not subjected to forced contamination.

如上而設定測定點C-G後,再對前述2種之基板2分別使用光阻去除裝置1而進行實驗(實施例1、2)。實施例1、2中,僅有使用之基板2之種類不同,其它實驗條件等則共通。 After the measurement point C-G was set as described above, the experiment was performed using the photoresist removal device 1 for each of the two types of substrates 2 (Examples 1 and 2). In the first and second embodiments, only the types of the substrates 2 to be used are different, and other experimental conditions and the like are common.

以下為實施例1、2所共通之主要處理條件。 The main processing conditions common to the first and second embodiments are as follows.

基板之旋轉速度:150rpm Rotation speed of the substrate: 150 rpm

硫酸之供給溫度:200℃ Supply temperature of sulfuric acid: 200 ° C

硫酸之供給時間:120秒 Sulfuric acid supply time: 120 seconds

硫酸之總供給量:400mL Total supply of sulfuric acid: 400mL

臭氧水之供給濃度:150ppm Ozone water supply concentration: 150ppm

臭氧水之供給溫度:70℃ Ozone water supply temperature: 70 ° C

臭氧水之供給時間:60秒 Ozone water supply time: 60 seconds

臭氧水之總供給量:2000mL Total supply of ozone water: 2000mL

圖8顯示實施例1(非強制汙染)之測定結果,圖9則顯示實施例2(強制汙染)之測定結果。圖8、9中,(a)顯示光阻去除前,(b)則顯示光阻去除後之資料。如圖8、9所示,測定之金屬種類為Ti、Cr、Mn、Fe、Co、Ni、Cu、Zn之8種,並分別就之金屬之各種類顯示金屬殘渣量(單位:atoms/cm2)。 Fig. 8 shows the measurement results of Example 1 (non-mandatory contamination), and Fig. 9 shows the measurement results of Example 2 (forced contamination). In Figs. 8 and 9, (a) shows that the photoresist is removed, and (b) shows the data after the photoresist is removed. As shown in Figs. 8 and 9, the metal species measured are 8 kinds of Ti, Cr, Mn, Fe, Co, Ni, Cu, and Zn, and the amount of metal residue is shown in various types of metals (unit: atoms/cm). 2 ).

如圖8、9所示,不拘光阻去除前之金屬量,使用光阻去除裝置1而進行光阻去除後,除一部分之Fe及Mn外,已可使5個測定點C-G之金屬殘渣量大致為0。且,一部分殘留之Fe及Mn亦已可加以控制在半導體製程上所容許之範圍內。如上所述,依據使用光阻去除裝置1之光阻去除方法,已知可將金屬殘渣量減至極少。此則可推論光阻去除裝置1之光阻去除力較大,而可去除光阻9及大量之金屬之故。 As shown in FIGS. 8 and 9, the amount of metal before removing the photoresist is removed, and after the photoresist is removed by the photoresist removing device 1, the amount of metal residue of the five measurement points CG can be made except for a part of Fe and Mn. It is roughly 0. Moreover, a part of the residual Fe and Mn can also be controlled within the range allowed by the semiconductor process. As described above, according to the photoresist removal method using the photoresist removing device 1, it is known that the amount of metal residue can be minimized. Therefore, it can be inferred that the photoresist removal device 1 has a large photoresist removal force, and can remove the photoresist 9 and a large amount of metal.

又,依據上述本實施例之光阻去除裝置1,可在依1×1015atoms/cm2而植入高劑量離子之砷後之基板2上,在約54秒內去除光阻9。進而,可使除一部分之Fe以外之金屬殘渣量在10秒以內降至預定量以下。 Further, according to the photoresist removing apparatus 1 of the present embodiment described above, the photoresist 9 can be removed in about 54 seconds on the substrate 2 after implanting a high dose of arsenic ions at 1 × 10 15 atoms/cm 2 . Further, the amount of metal residue other than a part of Fe can be reduced to a predetermined amount or less within 10 seconds.

另,本發明不受限於上述實施形態,而可實施為其它各種態樣。舉例言之,本實施形態中,雖說明分別自不同之裝置(硫酸供給部4及臭氧水供給部5)供給硫酸及臭氧水,但不限於此,舉例言之,亦可自同一裝置供給硫酸及臭氧水之雙方。 Further, the present invention is not limited to the above embodiment, and can be implemented in other various aspects. For example, in the present embodiment, the sulfuric acid and the ozone water are supplied from different devices (sulfuric acid supply unit 4 and ozone water supply unit 5), but the present invention is not limited thereto. For example, sulfuric acid may be supplied from the same device. And both sides of ozone water.

又,本實施形態中,雖說明光阻去除裝置1為單 片式,但不限於此,亦可為批次式。 Further, in the present embodiment, the photoresist removing device 1 is described as a single Slice type, but not limited to this, it can also be batch type.

又,本實施形態中,雖說明於硫酸供給部4內之中央部配置加熱器12,但不限於此,加熱器12亦可配置於其它部位。 In the present embodiment, the heater 12 is disposed in the center portion of the sulfuric acid supply unit 4, but the heater 12 is not limited thereto, and the heater 12 may be disposed at another portion.

又,本實施形態中,雖說明臭氧水之供給溫度為50℃以上,但不限於此,舉例言之,亦可供給常溫之臭氧水。 In the present embodiment, the supply temperature of the ozone water is 50° C. or more. However, the present invention is not limited thereto. For example, ozone water at normal temperature may be supplied.

另,適當組合上述各種實施形態中之任意實施形態,則可獲致其等個別之效果。 Further, if any of the above-described various embodiments is appropriately combined, the individual effects such as these can be obtained.

本發明可應用於自設有已藉離子之植入而於表面上形成有硬化層之光阻之基板去除光阻所需之光阻去除裝置及其方法。 The present invention can be applied to a photoresist removal apparatus and a method thereof for removing a photoresist from a substrate provided with a photoresist having a hardened layer formed on the surface by implantation of ions.

本發明雖已參照附圖而就較佳之實施形態加以充分揭露,但熟習本技術之從業人員當可進行各種變形及修正實施。該等變形及修正實施若未超出後附之申請專利範圍所界定之本發明範圍,即應理解為亦包含於本發明範圍之內。 The present invention has been fully described in detail with reference to the accompanying drawings, and those skilled in the art can make various modifications and modifications. Such variations and modifications are intended to be included within the scope of the present invention as defined by the appended claims.

2012年8月29日已提申之日本專利申請No.2012-188899號之說明書、附圖及申請專利範圍之揭露內容整體已予以參照,並加以引用於本說明書中。 The disclosure of the specification, the drawings and the claims of the Japanese Patent Application No. 2012-188899, the entire disclosure of which is incorporated herein in

2‧‧‧基板 2‧‧‧Substrate

9‧‧‧光阻 9‧‧‧Light resistance

10‧‧‧導通部分 10‧‧‧Connected section

11‧‧‧硬化層 11‧‧‧ hardened layer

15‧‧‧裂痕 15‧‧‧ crack

Claims (16)

一種光阻去除裝置,係用於自基板去除光阻者,其包含有:基板保持部,係用於保持設有已植入預定之離子而於表面上形成有硬化層之光阻之基板者;硫酸供給部,係設有用於加熱硫酸之加熱器,而可朝基板保持部所保持之基板供給已藉加熱器加熱至200℃以上之不含過氧化氫水之硫酸者;及臭氧水供給部,係可對已藉硫酸供給部供給硫酸之基板供給濃度150ppm以上之臭氧水者。 A photoresist removal device for removing photoresist from a substrate, comprising: a substrate holding portion for holding a substrate provided with a photoresist having a predetermined layer of ions implanted with a hardened layer on the surface a sulfuric acid supply unit provided with a heater for heating sulfuric acid, and a substrate containing the hydrogen peroxide-free water heated by the heater to 200° C. or higher can be supplied to the substrate held by the substrate holding portion; and the ozone water supply In the part, it is possible to supply ozone water having a concentration of 150 ppm or more to a substrate to which sulfuric acid is supplied from a sulfuric acid supply unit. 如請求項1之光阻去除裝置,其為單片式。 The photoresist removal device of claim 1, which is monolithic. 如請求項1之光阻去除裝置,其中硫酸供給部係供給已部分熱分解之硫酸。 A photoresist removal apparatus according to claim 1, wherein the sulfuric acid supply unit supplies the sulfuric acid which has been partially thermally decomposed. 如請求項3之光阻去除裝置,其中硫酸供給部係供給整體中之1~20%已熱分解之硫酸。 The photoresist removal apparatus of claim 3, wherein the sulfuric acid supply unit supplies 1 to 20% of the thermally decomposed sulfuric acid in the whole. 如請求項1之光阻去除裝置,其中硫酸供給部所供給之200℃以上之硫酸可對光阻施加熱應力而對光阻造成損傷。 The photoresist removal apparatus according to claim 1, wherein the sulfuric acid of 200 ° C or more supplied by the sulfuric acid supply portion applies thermal stress to the photoresist to cause damage to the photoresist. 如請求項5之光阻去除裝置,其中損傷為裂痕。 The photoresist removal device of claim 5, wherein the damage is a crack. 如請求項1之光阻去除裝置,其中臭氧水供給部係供給50℃以上之臭氧水。 The photoresist removal apparatus of claim 1, wherein the ozone water supply unit supplies ozone water of 50 ° C or more. 如請求項1~7中任一項之光阻去除裝置,其係在已藉基板保持部旋轉基板之狀態下對基板進行硫酸及臭氧水 之供給。 The photoresist removal device according to any one of claims 1 to 7, wherein the substrate is subjected to sulfuric acid and ozone water in a state in which the substrate is rotated by the substrate holding portion. Supply. 一種光阻去除方法,用於自基板去除光阻,其包含以下步驟:硫酸供給步驟,係於基板上形成之光阻上,朝已藉離子之植入而形成有硬化層之光阻表面上,供給不含過氧化氫水之200℃以上之硫酸;及臭氧水供給步驟,朝業經硫酸供給步驟供給硫酸之光阻表面上,供給濃度150ppm以上之臭氧水。 A photoresist removal method for removing photoresist from a substrate, comprising the steps of: a sulfuric acid supply step on a photoresist formed on a substrate, on a photoresist surface formed with a hardened layer by implantation of ions The sulfuric acid is supplied at a temperature of 200 ° C or higher containing no hydrogen peroxide water; and the ozone water supply step is supplied to the surface of the photoresist of sulfuric acid via a sulfuric acid supply step, and ozone water having a concentration of 150 ppm or more is supplied. 如請求項9之光阻去除方法,係以單片式進行基板之處理。 According to the photoresist removal method of claim 9, the substrate is processed in a single chip. 如請求項9之光阻去除方法,係於硫酸供給步驟中供給已部分熱分解之硫酸。 The photoresist removal method of claim 9, wherein the partially decomposed sulfuric acid is supplied in the sulfuric acid supply step. 如請求項11之光阻去除方法,係於硫酸供給步驟中供給整體中之1~20%已熱分解之硫酸。 The photoresist removal method of claim 11 is to supply 1 to 20% of the thermally decomposed sulfuric acid in the whole in the sulfuric acid supply step. 如請求項9之光阻去除方法,其於硫酸供給步驟中所供給之200℃以上之硫酸對光阻施加熱應力而對光阻造成損傷。 The photoresist removal method according to claim 9, wherein the sulfuric acid of 200 ° C or more supplied in the sulfuric acid supply step applies thermal stress to the photoresist to cause damage to the photoresist. 如請求項13之光阻去除方法,其中損傷為裂痕。 The method of removing photoresist from claim 13, wherein the damage is a crack. 如請求項9之光阻去除方法,係於臭氧水供給步驟中供給50℃以上之臭氧水。 The photoresist removal method according to claim 9 is characterized in that ozone water of 50 ° C or more is supplied in the ozone water supply step. 如請求項9至15中任一項之光阻去除方法,其於硫酸供給步驟及臭氧水供給步驟中使基板呈旋轉狀態。 The photoresist removal method according to any one of claims 9 to 15, wherein the substrate is rotated in the sulfuric acid supply step and the ozone water supply step.
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