TWI406111B - Method for removing resist and device - Google Patents

Method for removing resist and device Download PDF

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TWI406111B
TWI406111B TW97145183A TW97145183A TWI406111B TW I406111 B TWI406111 B TW I406111B TW 97145183 A TW97145183 A TW 97145183A TW 97145183 A TW97145183 A TW 97145183A TW I406111 B TWI406111 B TW I406111B
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ozone
gas
substrate
resist
chamber
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TW97145183A
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TW200943001A (en
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Toshinori Miura
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Meidensha Electric Mfg Co Ltd
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Abstract

To remove resist in a substrate without worrying about deformation because of thermal expansion near room temperature. Unsaturated hydrocarbon gas and ozone gas are supplied to a chamber 2 storing a substrate 10 supplied for removing resist 101 at room temperature under pressure lower than atmospheric pressure. The ozone gas is supplied from an ozone generator 4. The ozone generator 4 liquefies and separates only ozone based on a difference in vapor pressure from gas containing ozone and then vaporizes it again to obtain ultra-high concentration ozone gas. The chamber 2 may have a mixing chamber and a treatment chamber. The mixing chamber and the treatment chamber comprise a partition for dividing the chamber 2 into two chambers, namely upper and lower chambers. The unsaturated hydrocarbon gas and ozone gas are supplied into the mixing chamber. The mixed gas of the unsaturated hydrocarbon gas and ozone in the mixing chamber is transferred to the treatment chamber storing the substrate 10. The partition has a shower head for transferring gas in the mixing chamber into the treatment chamber. In the shower head, a plurality of holes are formed in the partition.

Description

阻劑除去方法及其裝置 Receptor removal method and device thereof

本發明係關於用以除去在半導體元件的製造過程被形成在基板表面的阻劑,尤其是高劑量離子注入阻劑之技術。 The present invention relates to a technique for removing a resist formed on a surface of a substrate during a manufacturing process of a semiconductor element, particularly a high-dose ion implantation resist.

就除去基板上的高劑量離子注入阻劑的技術而言,係有例如以下的專利文獻所揭示者。 Techniques for removing high-dose ion implantation resists on a substrate are disclosed, for example, in the following patent documents.

專利文獻1的電漿處理方法及其裝置,係使用具有基板偏壓施加手段及基板加熱手段之螺旋波電漿處理,並對基板施予電漿處理。具體而言係為藉由將根據螺旋波電漿的高離子電流加以利用之離子模式主體的電漿處理、與根據非共鳴的感應耦合電漿之自由基模式主體的電漿處理,除去基板上的阻劑遮罩。 The plasma processing method and apparatus of Patent Document 1 use a spiral wave plasma treatment having a substrate bias application means and a substrate heating means, and a plasma treatment is applied to the substrate. Specifically, the substrate is removed by plasma treatment of the ion mode body according to the high ion current of the spiral wave plasma and plasma treatment of the radical mode body according to the non-resonant inductively coupled plasma. Resistive mask.

專利文獻2的電漿處理方法及其裝置,係藉由具有利用對於UV光為透明介電體材料的透明鐘形罩之電漿處理裝置,灰化基板之阻劑遮罩的硬化變質層。其次,藉由在臭氧環境下照射UV光,灰化前述基板上之阻劑遮罩的未變質層。 The plasma processing method and apparatus of Patent Document 2 are a hardened and deteriorated layer which ashes a resist mask of a substrate by a plasma processing apparatus having a transparent bell jar which is a transparent dielectric material for UV light. Next, the undegraded layer of the resist mask on the substrate is ashed by irradiating the UV light in an ozone environment.

專利文獻3之阻劑除去方法及其裝置,係為加熱基板而在基板表面上的阻劑故意引起爆孔現象。再者在冷卻該基板後利用黏著膠帶剝離前述阻劑,接著利用氧電漿、臭氧(參照專利文獻4等)、或是UV光與臭氧的組合進行 灰化。 The method for removing a resist of Patent Document 3 and its apparatus are methods of heating a substrate and causing a blasting phenomenon on the surface of the substrate. Further, after cooling the substrate, the resist is peeled off by an adhesive tape, followed by oxygen plasma, ozone (see Patent Document 4, etc.), or a combination of UV light and ozone. Ashing.

高劑量(dose)離子注入阻劑係使硬化層在基板表面形成為膜狀。由於在該阻劑的基底有柔軟的阻劑(未變質層),因此當使基板升溫時,例如加熱到比200℃更高溫時,藉由來自前述基底之未變質層的排氣或是熱膨脹差而使表面引起裂紋刮起之所謂爆孔(popping)現象。該刮起的基板表面之硬化層係不僅污染基板也會污染收納基板的腔室內。 A high dose ion implantation resister forms a hardened layer into a film shape on the surface of the substrate. Since there is a soft resist (unmodified layer) on the substrate of the resist, when the substrate is heated, for example, heated to a temperature higher than 200 ° C, exhaust or thermal expansion by the unaltered layer from the substrate A so-called popping phenomenon in which the surface causes a crack to be scratched. The hardened layer on the surface of the scraped substrate not only contaminates the substrate but also contaminates the chamber in which the substrate is housed.

因此,如專利文獻3所例示之具有加熱工程的除去方法係使得從基板得到的元件之成品率降低。又也必須縮短製造裝置的維護周期,而對基板的生產率有所影響。 Therefore, the removal method with heating engineering as exemplified in Patent Document 3 reduces the yield of components obtained from the substrate. It is also necessary to shorten the maintenance cycle of the manufacturing apparatus, which has an influence on the productivity of the substrate.

一方面,在專利文獻1、專利文獻2及專利文獻4所例示的處理方法雖然可以抑制爆孔現象,但是必須具備電漿產生裝置。電漿產生裝置價格高昂的同時,且當具備此裝置時會使用以除去阻劑的裝置構造大型化。又使得在阻劑除去時之能源成本變高。 On the other hand, the processing methods exemplified in Patent Document 1, Patent Document 2, and Patent Document 4 can suppress the blasting phenomenon, but it is necessary to include a plasma generating device. The plasma generating apparatus is expensive, and when the apparatus is provided, the apparatus structure for removing the resist is used to increase the size. This also increases the energy cost when the resist is removed.

專利文獻1:日本特開平8-69896號公報(段落0010~0016) Patent Document 1: Japanese Laid-Open Patent Publication No. Hei 8-69896 (paragraphs 0010 to 0016)

專利文獻2:日本特開平8-139004號公報(段落0011~0023) Patent Document 2: Japanese Laid-Open Patent Publication No. Hei 8-139004 (paragraphs 0011 to 0023)

專利文獻3:日本特開平9-27473號公報(段落0008~0011) Patent Document 3: Japanese Laid-Open Patent Publication No. Hei 9-27473 (paragraphs 0008 to 0011)

專利文獻4:日本特開2006-294842號公報(段落0016,0026) Patent Document 4: Japanese Laid-Open Patent Publication No. 2006-294842 (paragraph 0016, 0026)

因此,用以解決前述課題之阻劑除去方法,係在比大氣壓更低壓下供給臭氧氣體的同時,並且供給不飽和烴氣體或是不飽和烴的氟置換體氣體至可進行基板加熱的反應系,除去前述基板上的阻劑。 Therefore, the resist removal method for solving the above-mentioned problems is to supply an ozone gas at a lower pressure than atmospheric pressure, and to supply an unsaturated hydrocarbon gas or a fluorine-substituted gas of an unsaturated hydrocarbon to a reaction system capable of heating the substrate. The resist on the aforementioned substrate is removed.

又用以解決前述課題之阻劑除去裝置,係具備:以可加熱的方式收納用來作為阻劑除去的基板之腔室;在比大氣壓更低壓下供給臭氧氣體至前述腔室的手段;及在比大氣壓更低壓下供給不飽和烴氣體或是不飽和烴的氟置換體氣體至前述腔室的手段。 Further, the resist removing device for solving the above-mentioned problems includes: a chamber for arranging a substrate to be removed as a resist to be heated, and means for supplying ozone gas to the chamber at a lower pressure than atmospheric pressure; A means for supplying an unsaturated hydrocarbon gas or a fluorine-substituted gas of an unsaturated hydrocarbon to the chamber at a lower pressure than atmospheric pressure.

若是根據以上的阻劑除去方法及其裝置的話,可在90℃以下進行基板的阻劑除去。因此,即使是高劑量離子注入阻劑的處理也可以防止爆孔現象發生。又因為在比大氣壓更低壓的減壓狀態下進行基板的阻劑除去,因此即使是使用伴隨爆發危險的高濃度臭氧氣體也可以確保安全性。進一步,可以減低對基板基底的損傷。尤其是在高劑量離子注入阻劑中,可以一邊確實抑制爆孔現象,一邊進行阻劑除去。進一步,即使在阻劑下部有易於氧化的物質(例如Cu配線等),也可以將該氧化抑制在最小界限。 According to the above-described resist removal method and apparatus therefor, the resist removal of the substrate can be performed at 90 ° C or lower. Therefore, even a high-dose ion implantation resist can prevent the occurrence of blasting. Further, since the resist removal of the substrate is performed under a reduced pressure state lower than the atmospheric pressure, safety can be ensured even if a high concentration ozone gas accompanying the explosion is used. Further, damage to the substrate substrate can be reduced. In particular, in the high-dose ion implantation resist, the resist removal can be performed while suppressing the blasting phenomenon. Further, even if there is a substance which is easily oxidized (for example, Cu wiring or the like) in the lower portion of the resist, the oxidation can be suppressed to a minimum.

就前述不飽和烴氣體而言,除了舉例如乙烯所例示之具有碳的雙鍵結合之烴(烯烴)、或是乙炔所例示之具有碳的3鍵結合之烴(炔烴)外,也可以舉例如丁烯等低分子量者。就前述不飽和烴的氟置換體氣體而言,可以舉例如前述所例示之烴的氟置換體氣體。 In the above-mentioned unsaturated hydrocarbon gas, in addition to a hydrocarbon (olefin) having a double bond of carbon exemplified by ethylene, or a hydrocarbon having 3 bonds (alkyne) exemplified by acetylene, Examples are low molecular weight such as butene. The fluorine-substituted gas of the unsaturated hydrocarbon may, for example, be a fluorine-substituted gas of a hydrocarbon exemplified above.

在前述阻劑除去方法中,前述臭氧氣體係以使用根據蒸氣壓差從含有臭氧的氣體僅液化分離臭氧後再氣化而得到的超高濃度臭氧氣體為佳。在前述阻劑除去裝置中,前述臭氧氣體的供給係以具備藉由根據蒸氣壓差從含有臭氧的氣體僅液化分離臭氧後再氣化而產生超高濃度臭氧氣體的臭氧產生裝置為佳。藉由利用前述超高濃度臭氧氣體,可以有效率地氧化除去阻劑。又前述臭氧氣體係不限於前述超高濃度臭氧氣體。 In the above-described method for removing a resist, the ozone gas system is preferably an ultra-high concentration ozone gas obtained by liquefying and separating ozone from a gas containing ozone according to a vapor pressure difference and then gasifying. In the above-described resist removal device, it is preferable that the ozone gas is supplied with an ozone generating device that generates an ultra-high concentration ozone gas by liquefying and separating ozone from a gas containing ozone according to a vapor pressure difference. By using the aforementioned ultra-high concentration ozone gas, the resist can be efficiently oxidized and removed. Further, the aforementioned ozone gas system is not limited to the aforementioned ultra-high concentration ozone gas.

在前述阻劑除去方法及阻劑除去裝置中,就基板的加熱手段而言,有將前述基板支撐在載置台,並加熱該載置台的形態。可以舉例如藉由將紅外線照射到載置台而加熱基板的形態。又前述載置台的加熱手段係不限於前述光源,除了使用加熱器或感應加熱等各種加熱手段之外,將加熱器等各種加熱手段內藏設置在載置台的構造亦可。 In the resist removal method and the resist removal device, the substrate heating means has a form in which the substrate is supported on a mounting table and the mounting table is heated. For example, a form in which the substrate is heated by irradiating infrared rays onto the mounting table can be mentioned. Further, the heating means of the mounting table is not limited to the light source, and various heating means such as a heater or induction heating may be used, and various heating means such as a heater may be incorporated in the mounting table.

又在前述阻劑除去方法及阻劑除去裝置中,在使前述基板為有離子注入的阻劑之情況下,以利用超純水洗淨利用前述臭氧氣體以及不飽和烴氣體或是不飽和烴的氟置換體氣體所處理的基板為佳。此係由於在半導體製造工程所注入的離子在大多的情況都會藉由氧化反應而形成蒸氣壓低的化合物,即使在完全除去阻劑後也會使此化合物附著在基板表面而形成殘渣。由於此等係為水溶性化合物所形成,因此可以很容易溶解於超純水而被除去。 Further, in the resist removal method and the resist removal device, when the substrate is a resist having ion implantation, the ozone gas and the unsaturated hydrocarbon gas or the unsaturated hydrocarbon are washed and washed with ultrapure water. The substrate to be treated with the fluorine replacement gas is preferred. This is because in many cases, ions implanted in a semiconductor manufacturing process form a compound having a low vapor pressure by an oxidation reaction, and even after the resist is completely removed, the compound adheres to the surface of the substrate to form a residue. Since these are formed as water-soluble compounds, they can be easily dissolved in ultrapure water and removed.

進一步,在前述阻劑除去方法及阻劑除去裝置中,在除去前述基板的阻劑時,以使前述基板的溫度成為90℃以 下的方式控制前述反應系及腔室的內壓時,可以確實防止爆孔現象。 Further, in the resist removal method and the resist removal device, when the resist of the substrate is removed, the temperature of the substrate is 90 ° C. When the following method is used to control the internal pressure of the reaction system and the chamber, the phenomenon of blasting can be surely prevented.

若是根據以上發明的話,因為可以在90℃以下的低溫進行阻劑除去,因此不會使基板基底的金屬類氧化。尤其是,可以一邊防止爆孔現象的發生,一邊除去高劑量離子注入阻劑。又可以實現在阻劑除去時之能源成本的減低及裝置構造的簡單化。 According to the above invention, since the resist removal can be performed at a low temperature of 90 ° C or lower, the metal of the substrate base is not oxidized. In particular, it is possible to remove the high-dose ion implantation resist while preventing the occurrence of the blast phenomenon. Further, it is possible to achieve a reduction in energy cost and a simplification of the device structure when the resist is removed.

第1(a)圖係為顯示關於發明實施形態之阻劑除去裝置1的概略構成圖之剖面圖。第1(b)圖係為顯示阻劑除去裝置1的概略構成部之平面圖。 Fig. 1(a) is a cross-sectional view showing a schematic configuration of a resist removal device 1 according to an embodiment of the invention. Fig. 1(b) is a plan view showing a schematic configuration of the resist removal device 1.

阻劑除去裝置1係具備腔室2、真空泵3、及光源4。腔室2係在收納用來阻劑17除去之基板16的同時,並且導入臭氧氣體(O3)及不飽和烴氣體。就阻劑17而言係可以舉例如第7圖所例示之ArF用阻劑;KrF用阻劑;G、I線用阻劑等。 The resist removal device 1 includes a chamber 2, a vacuum pump 3, and a light source 4. The chamber 2 is provided with an ozone gas (O 3 ) and an unsaturated hydrocarbon gas while accommodating the substrate 16 for removing the resist 17 . The resist 17 may, for example, be a resist for ArF exemplified in Fig. 7; a resist for KrF; a resist for G and I, and the like.

由第1(a)及1(b)圖可以明確得知,腔室2係形成為圓筒狀。腔室2係從側面部導入不飽和烴氣體或是不飽和烴的氟置換體氣體,另一方面從天井部導入臭氧氣體。被導入腔室2內的氣體係利用真空泵3從與前述側面部對向的側面部被吸引排出。 As is clear from the figures 1(a) and 1(b), the chamber 2 is formed in a cylindrical shape. The chamber 2 introduces an unsaturated hydrocarbon gas or a fluorine-substituted gas of an unsaturated hydrocarbon from the side surface portion, and introduces ozone gas from the ceiling portion. The gas system introduced into the chamber 2 is sucked and discharged from the side surface portion opposed to the side surface portion by the vacuum pump 3.

前述不飽和烴氣體係可以舉例如在乙烯所例示之具有碳的雙鍵結合之烴(烯烴)、或是乙炔所例示之具有3鍵 結合之烴(炔烴)。前述氟置換體氣體係可以舉例如前述任何一者的烴之氟置換體氣體。可以舉例如四氟乙烯。前述不飽和烴氣體或是前述氟置換體氣體係從此等任一者的氣體供給手段,也就是氣體高壓鋼瓶6介由配管5被導入。四氟乙烯氣體等氟置換體氣體尤其是對於硬化的離子注入阻劑而言,因為更能增加除去效果而有效。 The aforementioned unsaturated hydrocarbon gas system may, for example, be a hydrocarbon having a double bond of carbon (olefin) exemplified as ethylene, or having a triple bond as exemplified by acetylene. Combined hydrocarbon (alkyne). The fluorine-substituted body gas system may, for example, be a fluorine-substituted gas of a hydrocarbon of any of the above. For example, tetrafluoroethylene can be mentioned. The gas supply means of any of the above-mentioned unsaturated hydrocarbon gas or the fluorine-substituted gas system, that is, the gas high-pressure cylinder 6 is introduced through the pipe 5. A fluorine-substituted gas such as a tetrafluoroethylene gas is particularly effective for a hardened ion-implanting resist because it can more effectively remove the effect.

就前述臭氧氣體而言係使用超高濃度臭氧氣體。該臭氧氣體係從其供給手段,也就是臭氧發生裝置8介由配管7被導入。配管7係與密封腔室2之蓋的中心部連接。該蓋係介由輔助密封構件密封腔室2。就輔助密封構件而言係可以採用例如由矽膠之類的耐臭氧性材料所構成的O形環。 In the case of the aforementioned ozone gas, an ultra-high concentration ozone gas is used. The ozone gas system is introduced from the supply means, that is, the ozone generator 8 via the pipe 7. The pipe 7 is connected to the center of the lid of the sealed chamber 2. The cover seals the chamber 2 via an auxiliary sealing member. As the auxiliary sealing member, an O-ring composed of, for example, an ozone-resistant material such as silicone rubber can be used.

前述超高濃度臭氧氣體係可以從例如根據蒸氣壓差將含有臭氧的氣體僅液化分離臭氧後再氣化而得到。更具體而言係可以舉例如從揭示在日本特開2001-304756或是日本特開2003-20209之專利文獻的臭氧產生裝置所得到的臭氧氣體。前述臭氧產生裝置係根據臭氧與其他氣體成份(例如氧)的蒸氣壓差,僅液化分離臭氧而製造超高濃度(臭氧濃度≒100%)的臭氧氣體。尤其是日本特開2003-20209之臭氧供給裝置係具備複數個僅使臭氧液化及氣化的腔室,並藉由各自溫度控制此等腔室而能夠連續供給超高濃度臭氧氣體。再者,就根據該超高濃度臭氧氣體連續供給方法之市售的臭氧產生裝置而言係可以舉例如明電舍製造的純臭氧產生機(MPOG-HM1A1)。 The ultra-high-concentration ozone gas system can be obtained, for example, by liquefying and separating ozone with a gas containing ozone according to a vapor pressure difference. More specifically, for example, ozone gas obtained from an ozone generating apparatus disclosed in JP-A-2001-304756 or JP-A-2003-20209 can be used. The ozone generating device produces ozone gas having an ultrahigh concentration (ozone concentration ≒ 100%) based on a vapor pressure difference between ozone and other gas components (for example, oxygen), and liquefying only ozone. In particular, the ozone supply device of JP-A-2003-20209 includes a plurality of chambers for liquefying and vaporizing only ozone, and the chambers can be continuously supplied with ultra-high concentration ozone gas by controlling the chambers at respective temperatures. Further, a commercially available ozone generator according to the ultrahigh-concentration ozone gas continuous supply method may be, for example, a pure ozone generator (MPOG-HM1A1) manufactured by Tosoh Corporation.

前述臭氧氣體係沒有限定為前述超高濃度臭氧氣體。可以舉例如臭氧濃度為數十%以上的臭氧氣體。該臭氧氣體雖然在大氣壓下反應性為高而伴隨危險,但是在阻劑除去裝置1中係因為利用真空泵3使腔室2成為減壓狀態而可以安全處理。在大氣壓下14.3~38vol%的臭氧濃度為持續性分解領域、~44vol%的臭氧濃度為突燃領域、44vol%~的臭氧濃度為爆發領域(杉光英俊、臭氧的基礎與應用、光琳社、1996年第187頁)。 The aforementioned ozone gas system is not limited to the aforementioned ultra-high concentration ozone gas. For example, ozone gas having an ozone concentration of several tens of % or more can be mentioned. Although the ozone gas has high reactivity at atmospheric pressure and is dangerous, in the resist removal device 1, the chamber 2 can be safely treated by the vacuum pump 3 in a reduced pressure state. At atmospheric pressure, the concentration of ozone in the range of 14.3 to 38 vol% is in the field of continuous decomposition, the concentration of ozone in ~44 vol% is in the field of deflagration, and the concentration of ozone in 44 vol% is the field of explosion (Shuguang Handsome, Foundation and Application of Ozone, Guanglin Society, 1996) Year 187).

第8圖係顯示僅根據各種臭氧氣體(超高濃度臭氧氣體(臭氧濃度≒100%)、臭氧濃度8vol%的臭氧氣體、慣用(Conventional)的臭氧氣體),灰化處理Si基板的情況下之基板溫度[℃]與灰化速度[μm/min]的關係特性圖。第9圖係顯示僅根據各種臭氧氣體(超高濃度臭氧氣體(臭氧濃度≒100%)、臭氧濃度8vol%的臭氧氣體、慣用的臭氧氣體),灰化處理Si基板的情況下之阿列尼厄圖表的特性圖。超高濃度臭氧氣體係為利用明電舍製造的臭氧產生機(MPOG-HM1A1)所產生者。慣用係意指利用既存之使用臭氧的阻劑除去裝置(莎姆克股份有限公司的UV乾式去光阻機/清洗機UV-300H)進行灰化處理的情況。該慣用的阻劑除去裝置係在大氣壓下一邊流通低濃度臭氧氣體(臭氧濃度≒2vol%),一邊照射UV光。由此等特性圖可以明確得知,藉由使用超高濃度臭氧氣體可以使灰化速度(阻劑除去效率)明顯提高。又在使用超高濃度臭氧氣體之400℃狀況下的處理雖然可以除去高劑量離子注入 阻劑(如第4圖所例示的樣子),但是可以確認的是由於高溫而在升溫中會發生爆孔(如第3圖所例示的樣子),並在腔室內部附著成為細小粒子的阻劑表面硬化層。 Fig. 8 shows the case where the Si substrate is ashed only in accordance with various ozone gases (ultra-high concentration ozone gas (ozone concentration ≒ 100%), ozone concentration 8 vol% ozone gas, conventionally-used ozone gas). A characteristic diagram of the relationship between the substrate temperature [°C] and the ashing speed [μm/min]. Fig. 9 shows an Aleni case in the case of ashing a Si substrate based on various ozone gases (ultra-high concentration ozone gas (ozone concentration ≒ 100%), ozone concentration 8 vol% ozone gas, conventional ozone gas) The characteristic diagram of the erg diagram. The ultra-high concentration ozone gas system is produced by an ozone generator (MPOG-HM1A1) manufactured by Mingdian. The conventional system means a case where ashing treatment is performed using an existing ozone-removing agent removing device (Sumke Co., Ltd. UV dry-type photoresist/cleaner UV-300H). This conventional resist removal apparatus irradiates UV light while flowing a low-concentration ozone gas (ozone concentration ≒ 2 vol%) under atmospheric pressure. From this characteristic map, it is clear that the ashing speed (resistance removal efficiency) can be remarkably improved by using an ultra-high concentration ozone gas. In addition, the treatment at 400 ° C using ultra-high concentration ozone gas can remove high dose ion implantation. Resistor (as exemplified in Fig. 4), but it can be confirmed that blasting occurs at a high temperature due to high temperature (as exemplified in Fig. 3), and a small particle is attached to the inside of the chamber. Surface hardened layer.

真空泵3係在減壓狀態下吸引排出腔室2內的氣體。連接腔室2與真空泵3的配管9係具備排氣閥10與臭氧消除器11。排氣閥10係利用控制部21而可控制開度。排氣閥10係以將腔室2的內壓成為既定值的方式控制腔室2內的氣體流量。為此腔室2係具備用以檢測內壓的壓力計19。在真空泵3中係以採用對臭氧有耐性的乾泵為佳。此係為了避免由於在排氣中多少含有臭氧的可能性而使性能減低及劣化所造成的壽命減低。臭氧消除器11係分解包含在從腔室2所吸出的氣體中的臭氧。臭氧消除器11係以半導體製造技術所採用的既知之臭氧分解裝置即可。 The vacuum pump 3 sucks the gas in the discharge chamber 2 under a reduced pressure state. The piping 9 connecting the chamber 2 and the vacuum pump 3 includes an exhaust valve 10 and an ozone canceller 11. The exhaust valve 10 can control the opening degree by the control unit 21. The exhaust valve 10 controls the flow rate of the gas in the chamber 2 so that the internal pressure of the chamber 2 becomes a predetermined value. To this end, the chamber 2 is provided with a pressure gauge 19 for detecting the internal pressure. It is preferable to use a dry pump which is resistant to ozone in the vacuum pump 3. This is to avoid a decrease in the life caused by the performance degradation and deterioration due to the possibility of containing ozone in the exhaust gas. The ozone eliminator 11 decomposes ozone contained in the gas sucked from the chamber 2. The ozone eliminator 11 is a known ozone decomposing device used in semiconductor manufacturing technology.

在腔室2內的底部係如第1(a)圖所示,介由支撐構件14設置載置台15。用來阻劑17除去的基板16係如第1(b)圖所示,置放在載置台15的中心部。載置台15係由SiC構成並形成為略圓板狀。載置台15係與腔室2底部為同心配置。載置台15係與熱電偶18連接。熱電偶18係為了控制載置台15的溫度而將檢測出的載置台15之熱能(溫度)轉換為電氣訊號後供給至控制部21。控制部21係將基於前述電氣訊號之光源4光強度控制訊號供給至光源4。 The bottom portion in the chamber 2 is provided with a mounting table 15 via a support member 14 as shown in Fig. 1(a). The substrate 16 for removing the resist 17 is placed on the center of the mounting table 15 as shown in Fig. 1(b). The mounting table 15 is made of SiC and is formed in a substantially disk shape. The mounting table 15 is concentrically arranged with the bottom of the chamber 2. The mounting table 15 is connected to the thermocouple 18. The thermocouple 18 converts the detected thermal energy (temperature) of the mounting table 15 into an electric signal in order to control the temperature of the mounting table 15, and supplies it to the control unit 21. The control unit 21 supplies the light source 4 light intensity control signal based on the electric signal to the light source 4.

光源4係藉由加熱腔室2內的載置台15而加熱基板16。光源4係配置在腔室2的下方。光源4係以半導體製 造技術中用來作為加熱手段之發射紅外線的光源即可。光源4係利用控制部21而可以控制光強度。在光源4中係適當具備用以使照射光集光的反射板12。一方面,在腔室2底部係設置用以導入從光源4所照射的紅外線之開口部20。再者,以塞住該開口部20的方式設置光導入窗13。光導入窗13係由人工石英所例示之使紅外線透過的材料所構成。 The light source 4 heats the substrate 16 by heating the mounting table 15 in the chamber 2. The light source 4 is disposed below the chamber 2. Light source 4 is made of semiconductor The light source for emitting infrared rays used as a heating means in the art can be used. The light source 4 can control the light intensity by the control unit 21. The light source 4 is appropriately provided with a reflection plate 12 for collecting the irradiation light. On the other hand, an opening portion 20 for introducing infrared rays radiated from the light source 4 is provided at the bottom of the chamber 2. Further, the light introduction window 13 is provided to close the opening portion 20. The light introduction window 13 is composed of a material permeable to infrared rays exemplified by artificial quartz.

一邊參照第1及2圖,一邊針對阻劑除去裝置1的動作例加以說明。在將排氣閥10設定為全開的狀態下,利用真空泵3的吸引力從氣體高壓鋼瓶6供給例如乙烯氣體作為不飽和烴的同時,並且從臭氧產生裝置8將超高濃度臭氧氣體(臭氧濃度≒100%)供給至腔室2內。基板16係藉由利用光源4所加熱的載置台15而保持在80℃以下。其次,排氣泵10係以使腔室2的內壓(壓力計19的檢測值)成為例如400Pa的方式調整開度。在該狀態下大約經過5分鐘處理。在該處理的時間帶中係根據自熱(self-heating)而使載置台15上的基板16溫度上升,但控制在90℃以下。之後,停止超高濃度臭氧氣體及乙烯氣體的供給。在腔室2內的反應過程中係使阻劑藉由被導入的不飽和烴與臭氧所產生的氫自由基以及其他多種自由基而被分解(社團法人日本化學會編、季刊化學總說、第7篇、活性氧的化學、1990年4月20日發行、第36~37頁)。藉由這樣的過程而使基板16上之由烴構成的阻劑17成份分解為碳酸氣體及水。碳酸氣體及水係成為排出氣體並介由 配管9而從腔室2排出。 An operation example of the resist removal device 1 will be described with reference to Figs. 1 and 2 . In a state where the exhaust valve 10 is set to be fully open, the ethylene gas is supplied as an unsaturated hydrocarbon from the gas high-pressure cylinder 6 by the suction force of the vacuum pump 3, and the ultra-high concentration ozone gas (ozone concentration) is taken from the ozone generating device 8. ≒100%) is supplied into the chamber 2. The substrate 16 is held at 80 ° C or lower by the mounting table 15 heated by the light source 4 . Next, the exhaust pump 10 adjusts the opening degree such that the internal pressure of the chamber 2 (the detected value of the pressure gauge 19) is, for example, 400 Pa. In this state, it takes about 5 minutes to process. In the time zone of the treatment, the temperature of the substrate 16 on the mounting table 15 is raised in accordance with self-heating, but is controlled to be 90 ° C or lower. Thereafter, the supply of the ultra-high concentration ozone gas and the ethylene gas is stopped. In the reaction process in the chamber 2, the resist is decomposed by the hydrogen radicals generated by the introduced unsaturated hydrocarbons and ozone, and various other radicals (edited by the Japanese Chemical Society, the quarterly chemical, Chapter 7, Chemistry of Reactive Oxygen, issued on April 20, 1990, pp. 36-37). The composition of the resist 17 composed of hydrocarbons on the substrate 16 is decomposed into carbonic acid gas and water by such a process. Carbonic acid gas and water system become exhaust gases and are interposed The pipe 9 is discharged from the chamber 2.

第2圖係為顯示根據以上的動作例之載置台溫度與腔室壓力之經時性變化的一例。載置台15的溫度在來自臭氧產生裝置8(臭氧產生機MPOG-HM1A1)之超高濃度臭氧氣體的導入前係大約穩定在80℃,雖然在導入前述臭氧氣體後藉由反應熱而升溫,但是可以確認的是在未滿90℃時就結束。 Fig. 2 is a view showing an example of temporal changes in the stage temperature and the chamber pressure according to the above operation examples. The temperature of the mounting table 15 is stabilized at 80 ° C before the introduction of the ultra-high concentration ozone gas from the ozone generating device 8 (ozone generator MPOG-HM1A1), and the temperature is raised by the reaction heat after the introduction of the ozone gas. It can be confirmed that it ends when it is less than 90 °C.

第10圖係為利用關於阻劑除去裝置1之實施例所處理的情況之基板表面的外觀照片。具體而言為根據第2圖所示之時間圖表處理具有以5E15個/cm2(5×1015個/cm2)注入P(磷)的KrF用阻劑之Si基板(30mm×30mm)的情況之外觀照片。在載置台15的溫度為最高溫度90℃程度沒有發生爆孔現象。可以得知以這樣的低溫之處理係對於基底(Si基板)的影響為非常小。又如第11圖所示,當觀察在利用與關於第10圖之實施例相同的條件下處理非常易於氧化的銅板(40mm×40mm)時之銅板外觀時沒有發現變色。 Fig. 10 is a photograph showing the appearance of the surface of the substrate by the case of the treatment of the embodiment of the resist removal device 1. Specifically, a Si substrate (30 mm × 30 mm) having a resist for KrF in which P (phosphorus) is implanted at 5E15 / cm 2 (5 × 10 15 /cm 2 ) is processed according to the time chart shown in Fig. 2 . Photo of the appearance of the situation. The blasting phenomenon did not occur at the temperature of the mounting table 15 at the maximum temperature of 90 °C. It can be seen that the effect of such a low temperature treatment on the substrate (Si substrate) is very small. Further, as shown in Fig. 11, when the appearance of the copper plate when the copper plate (40 mm × 40 mm) which is very easily oxidized was treated under the same conditions as those of the embodiment of Fig. 10 was observed, no discoloration was observed.

在第12圖係為顯示以同上的處理條件在時間從2分鐘到5分鐘的時間帶進行處理之情況下的各平均阻劑除去速率之變化。試料係使用有離子注入在以酚醛樹脂為主成份之g線用阻劑者、及有離子注入在KrF用阻劑者之2種(離子注入係為與關於第11圖之實施例相同的條件)。在處理時間2~4分鐘中係沒有太大差異,但是在5分鐘的處理係變得非常急速。此係被認為是2~4分鐘為除去表面 硬化層,4~5分鐘為除去基底之未硬化的未變質層。在5分鐘時不論是何種試料都完全被除去。此時的除去速度差異係為根據原來厚度的差異。又當觀察各時間處理後的表面時,可以確認的是隨著時間性(2分鐘後、3分鐘後、4分鐘後、5分鐘後)使表面變色,並使阻劑膜厚跟著變化。 In Fig. 12, the change in the average resist removal rate in the case where the treatment was carried out in the time zone of 2 minutes to 5 minutes under the same processing conditions as above was shown. The sample was prepared by ion implantation in a g-line resist containing a phenol resin as a main component, and in the case of ion-injecting a KrF resist (the ion implantation system is the same as the embodiment of the 11th embodiment). ). There was not much difference in the processing time of 2 to 4 minutes, but the processing in 5 minutes became very rapid. This system is considered to be 2~4 minutes to remove the surface The hardened layer is 4 to 5 minutes to remove the unhardened, unaltered layer of the substrate. No matter what kind of sample was completely removed at 5 minutes. The difference in the removal speed at this time is based on the difference in the original thickness. Further, when the surface after each time treatment was observed, it was confirmed that the surface was discolored with time (after 2 minutes, after 3 minutes, after 4 minutes, and after 5 minutes), and the thickness of the resist film was changed.

一方面,第4圖係為藉由關於比較例的阻劑除去法所處理之基板表面的外觀照片。具體而言為對於具有以5E15個/cm2(5×1015個/cm2)注入P(磷)的KrF用阻劑之Si基板,在載置台15的溫度為400℃下僅供給超高濃度臭氧氣體進行處理的情況下之外觀照片。雖然利用該方法可以除去阻劑,但是可以確認的是由於高溫而發生爆孔,並在腔室內部附著成為微細膜狀的粒子之阻劑表面硬化層。又可以確認的是在載置台15的溫度為400℃下之臭氧濃度8vol%的臭氧氣體單獨處理係會發生爆孔現象(第3圖)。 On the other hand, Fig. 4 is a photograph showing the appearance of the surface of the substrate treated by the resist removal method of the comparative example. Specifically, for a Si substrate having a resist for KrF in which P (phosphorus) is implanted at 5E15/cm 2 (5 × 10 15 /cm 2 ), the temperature of the mounting table 15 is only 400 ° C. Photograph of the appearance in the case where the concentration of ozone gas is treated. Although the resist can be removed by this method, it is confirmed that the blasting occurs due to the high temperature, and a resist hardening layer which becomes a fine film-like particle is attached to the inside of the chamber. Further, it was confirmed that a blasting phenomenon occurred in the ozone gas alone treatment system in which the ozone concentration of 8 vol% of the ozone at the temperature of the mounting table 15 was 400 ° C (Fig. 3).

第5圖係為藉由關於實施例之阻劑除去法所處理之基板的阻劑境界部表面放大照片(放大倍率400倍)。可以得知沒有膜狀的剝離物,並且沒有發生產生粒子的爆孔。 Fig. 5 is an enlarged photograph (magnification: 400 times) of the surface of the resist boundary portion of the substrate treated by the resist removal method of the example. It was found that there was no film-like peeling material, and no blasting of the generated particles occurred.

第6圖係為藉由關於實施例之阻劑除去法所處理之基板的中央部附近表面放大照片(放大倍率400倍)。雖然被認為在中央部附近表面也有殘渣,但是可以確認的是比起第5圖之阻劑境界部的表面明顯變少。該殘渣係在從腔室取出後經過時間越長有越增加的傾向,並且可以利用超 純水洗淨除去。因此,此並非為阻劑殘渣,而被認為是注入阻劑中的離子被氧化者(在此為P2O5或是P2O3)。此係認為是半導體製造工程所使用的注入離子在大多的情況下,由於藉由氧化而形成蒸氣壓低的水溶性化合物,處理後也會殘留在基板上,在從腔室取出後,吸附大氣中的水分而被觀察成為表面殘渣者。 Fig. 6 is an enlarged photograph (magnification: 400 times) of the surface near the center portion of the substrate treated by the resist removal method of the example. Although it is considered that there is residue on the surface near the center portion, it can be confirmed that the surface of the resist boundary portion is significantly smaller than that of Fig. 5. The residue tends to increase as the elapsed time elapses from the chamber, and can be removed by washing with ultrapure water. Therefore, this is not a resist residue, but is considered to be an oxidized ion (here, P 2 O 5 or P 2 O 3 ) in the implanted resist. This is considered to be an implanted ion used in semiconductor manufacturing engineering. In many cases, a water-soluble compound having a low vapor pressure is formed by oxidation, and remains on the substrate after being processed. After being taken out from the chamber, it is adsorbed in the atmosphere. The moisture is observed as a surface residue.

1‧‧‧阻劑除去裝置 1‧‧‧Rejection removal device

2‧‧‧腔室 2‧‧‧ chamber

3‧‧‧真空泵 3‧‧‧vacuum pump

4‧‧‧光源 4‧‧‧Light source

5‧‧‧配管 5‧‧‧Pipe

6‧‧‧氣體高壓鋼瓶 6‧‧‧ gas high pressure cylinder

7‧‧‧配管 7‧‧‧Pipe

8‧‧‧臭氧產生裝置 8‧‧‧Ozone generating device

9‧‧‧配管 9‧‧‧Pipe

10‧‧‧排氣閥 10‧‧‧Exhaust valve

11‧‧‧臭氧消除器 11‧‧‧Ozone eliminator

12‧‧‧反射板 12‧‧‧reflector

13‧‧‧光導入窗 13‧‧‧Light introduction window

14‧‧‧支撐構件 14‧‧‧Support members

15‧‧‧載置台 15‧‧‧mounting table

16‧‧‧基板 16‧‧‧Substrate

17‧‧‧阻劑 17‧‧‧Resist

18‧‧‧熱電隅 18‧‧‧ Thermoelectric

19‧‧‧壓力計 19‧‧‧ pressure gauge

20‧‧‧開口部 20‧‧‧ openings

21‧‧‧控制部 21‧‧‧Control Department

第1圖(a)係顯示關於發明實施形態之阻劑除去裝置的概略構成圖之剖面圖,(b)係顯示阻劑除去裝置的概略構成圖之正視圖。 Fig. 1(a) is a cross-sectional view showing a schematic configuration of a resist removal device according to an embodiment of the invention, and Fig. 1(b) is a front view showing a schematic configuration of a resist removal device.

第2圖係為關於發明實施形態之阻劑除去裝置的載置台溫度與腔室壓力之經時性變化。 Fig. 2 is a graph showing changes with time in the stage temperature and the chamber pressure of the resist removal device according to the embodiment of the invention.

第3圖係為利用關於比較例(只有8%臭氧氣體)之阻劑除去法所處理的Si基板表面之外觀照片。 Fig. 3 is a photograph showing the appearance of the surface of the Si substrate treated by the resist removal method of the comparative example (only 8% ozone gas).

第4圖係為利用關於比較例(只有100%臭氧氣體)之阻劑除去法所處理的Si基板表面之外觀照片。 Fig. 4 is a photograph showing the appearance of the surface of the Si substrate treated by the resist removal method of the comparative example (only 100% ozone gas).

第5圖係為利用關於發明實施例之阻劑除去法所處理的基板之阻劑境界部的表面放大照片(放大倍率400倍)。 Fig. 5 is a magnified surface (magnification: 400 times) of the resist boundary portion of the substrate treated by the resist removal method of the inventive example.

第6圖係為利用關於發明實施例之阻劑除去法所處理的基板之中央部附近的表面放大照片(放大倍率400倍)。 Fig. 6 is an enlarged photograph (magnification: 400 times) of the surface near the center portion of the substrate treated by the resist removal method of the inventive example.

第7圖係為各種阻劑的分子構造。 Figure 7 is the molecular structure of various resists.

第8圖係為僅利用各種臭氧氣體(超高濃度臭氧氣體(臭氧濃度≒100vol%))、臭氧濃度8vol%的臭氧氣體、 關於慣用的臭氧氣體)灰化處理Si基板的情況下之基板溫度[℃]與灰化速度[μm/min]關係的特性圖。 Fig. 8 is an ozone gas using only various ozone gases (ultra-high concentration ozone gas (ozone concentration ≒ 100 vol%)), ozone concentration 8 vol%, A characteristic diagram of the relationship between the substrate temperature [° C.] and the ashing rate [μm/min] in the case of ashing the Si substrate with respect to the conventional ozone gas.

第9圖係為顯示僅利用各種臭氧氣體(超高濃度臭氧氣體(臭氧濃度≒100vol%))、臭氧濃度8vol%的臭氧氣體、關於慣用的臭氧氣體)灰化處理Si基板的情況下之阿列尼厄圖表的特性圖。 Fig. 9 is a view showing a case where only a variety of ozone gases (ultra-high concentration ozone gas (ozone concentration ≒ 100 vol%)), ozone concentration 8 vol% ozone gas, and conventional ozone gas) are used to ash a Si substrate. The characteristic diagram of the Leonier chart.

第10圖係為利用關於實施例所處理的基板表面之外觀照片。 Figure 10 is a photograph of the appearance of the surface of the substrate treated with respect to the examples.

第11圖係為利用關於實施例所處理的銅板表面之外觀照片。 Fig. 11 is a photograph showing the appearance of the surface of the copper plate treated with respect to the examples.

第12圖係為在處理時間為2分鐘至5分鐘之時間帶中處理情況下之各平均阻劑除去速度的變化。 Fig. 12 is a graph showing changes in the average resist removal speed in the case of treatment in a belt having a treatment time of 2 minutes to 5 minutes.

1‧‧‧阻劑除去裝置 1‧‧‧Rejection removal device

2‧‧‧腔室 2‧‧‧ chamber

3‧‧‧真空泵 3‧‧‧vacuum pump

4‧‧‧光源 4‧‧‧Light source

5‧‧‧配管 5‧‧‧Pipe

6‧‧‧氣體高壓鋼瓶 6‧‧‧ gas high pressure cylinder

7‧‧‧配管 7‧‧‧Pipe

8‧‧‧臭氧產生裝置 8‧‧‧Ozone generating device

9‧‧‧配管 9‧‧‧Pipe

10‧‧‧排氣閥 10‧‧‧Exhaust valve

11‧‧‧臭氧消除器 11‧‧‧Ozone eliminator

12‧‧‧反射板 12‧‧‧reflector

13‧‧‧光導入窗 13‧‧‧Light introduction window

14‧‧‧支撐構件 14‧‧‧Support members

15‧‧‧載置台 15‧‧‧mounting table

16‧‧‧基板 16‧‧‧Substrate

17‧‧‧阻劑 17‧‧‧Resist

18‧‧‧熱電隅 18‧‧‧ Thermoelectric

19‧‧‧壓力計 19‧‧‧ pressure gauge

20‧‧‧開口部 20‧‧‧ openings

21‧‧‧控制部 21‧‧‧Control Department

Claims (9)

一種阻劑除去方法,其特徵為:在比大氣壓更低壓下,供給臭氧氣體,以及不飽和烴氣體或是不飽和烴的氟置換體氣體至能夠進行基板加熱的反應系,除去前述基板上的阻劑。 A method for removing a resist, characterized in that an ozone gas is supplied at a lower pressure than atmospheric pressure, and a fluorine-substituted gas of an unsaturated hydrocarbon gas or an unsaturated hydrocarbon is supplied to a reaction system capable of heating the substrate, and the substrate is removed. Resistor. 如申請專利範圍第1項之阻劑除去方法,其中,前述臭氧氣體係為根據蒸氣壓差從含有臭氧的氣體僅液化分離臭氧後再氣化所得到之超高濃度的臭氧氣體。 The method for removing a resist according to the first aspect of the invention, wherein the ozone gas system is an ultra-high concentration ozone gas obtained by liquefying and separating ozone from a gas containing ozone according to a vapor pressure difference and then gasifying. 如申請專利範圍第1或2項之阻劑除去方法,其中,將前述基板支撐在載置台,並藉由對該載置台照射紅外線而能夠加熱前述基板。 The method of removing a resist according to claim 1 or 2, wherein the substrate is supported on a mounting table, and the substrate can be heated by irradiating the mounting table with infrared rays. 如申請專利範圍第1項之阻劑除去方法,其中,在前述基板為有離子注入阻劑之情況下,在利用比大氣壓更低壓下供給臭氧氣體及不飽和烴氣體後,利用超純水洗淨前述基板。 The method of removing a resist according to the first aspect of the invention, wherein, in the case where the substrate is an ion implantation resist, the ozone gas and the unsaturated hydrocarbon gas are supplied at a lower pressure than atmospheric pressure, and then washed with ultrapure water. Clean the aforementioned substrate. 如申請專利範圍第1項之阻劑除去方法,其中,當在除去前述基板上的阻劑之際,以使前述基板的溫度達到90℃以下的方式控制前述反應系的內壓。 The method of removing a resist according to the first aspect of the invention, wherein the internal pressure of the reaction system is controlled such that the temperature of the substrate reaches 90° C. or less when the resist on the substrate is removed. 一種阻劑除去裝置,其特徵為具備:以能夠加熱的方式收納被用來阻劑除去的基板之腔室;在比大氣壓更低壓下供給臭氧氣體至前述腔室之手段;在比大氣壓更低壓下供給不飽和烴氣體或不飽和烴的 氟置換體氣體至前述腔室之手段。 A resist removal device characterized by comprising: a chamber capable of accommodating a substrate for resist removal; a means for supplying ozone gas to the chamber at a lower pressure than atmospheric pressure; and a lower pressure than atmospheric pressure Supply of unsaturated hydrocarbon gas or unsaturated hydrocarbon A means by which a fluorine replaces a gas to the chamber. 如申請專利範圍第6項之阻劑除去裝置,其中,前述臭氧氣體的供給係利用藉由根據蒸氣壓差從含有臭氧的氣體僅液化分離臭氧後再氣化所產生的超高濃度臭氧氣體之臭氧產生裝置加以進行。 The apparatus for removing a ozone gas according to the sixth aspect of the invention, wherein the ozone gas is supplied by using an ultra-high concentration ozone gas generated by liquefying and separating ozone from a gas containing ozone according to a vapor pressure difference. An ozone generating device is carried out. 如申請專利範圍第6或7項之阻劑除去裝置,其中,該腔室係具備:支撐前述基板之載置台;及對該載置台照射紅外線而加熱前述基板之光源。 The apparatus for removing a resist according to claim 6 or 7, wherein the chamber includes: a mounting table that supports the substrate; and a light source that irradiates the mounting table with infrared rays to heat the substrate. 如申請專利範圍第6項之阻劑除去裝置,其中,前述腔室係以使前述基板的溫度達到90℃以下的方式控制內壓。 The apparatus for removing a resist according to claim 6, wherein the chamber controls the internal pressure such that the temperature of the substrate reaches 90 ° C or lower.
TW97145183A 2007-05-23 2008-11-21 Method for removing resist and device TWI406111B (en)

Applications Claiming Priority (2)

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JP2007137290A JP4905253B2 (en) 2007-05-23 2007-05-23 Resist removing method and apparatus
JP2007314078 2007-12-04

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000077387A (en) * 1998-08-28 2000-03-14 Iwatani Internatl Corp Method and system for removing resist
US20020011257A1 (en) * 1997-02-14 2002-01-31 Degendt Stefan Method for removing organic contaminants from a semiconductor surface
TW584893B (en) * 2001-10-23 2004-04-21 Ums Co Ltd Method and apparatus for removing organic films
JP2006156919A (en) * 2004-12-01 2006-06-15 Purex:Kk Method of dislodging organic coating and remover

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20020011257A1 (en) * 1997-02-14 2002-01-31 Degendt Stefan Method for removing organic contaminants from a semiconductor surface
JP2000077387A (en) * 1998-08-28 2000-03-14 Iwatani Internatl Corp Method and system for removing resist
TW584893B (en) * 2001-10-23 2004-04-21 Ums Co Ltd Method and apparatus for removing organic films
JP2006156919A (en) * 2004-12-01 2006-06-15 Purex:Kk Method of dislodging organic coating and remover

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