TW200421433A - Substrate processing equipment - Google Patents

Substrate processing equipment Download PDF

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Publication number
TW200421433A
TW200421433A TW92126222A TW92126222A TW200421433A TW 200421433 A TW200421433 A TW 200421433A TW 92126222 A TW92126222 A TW 92126222A TW 92126222 A TW92126222 A TW 92126222A TW 200421433 A TW200421433 A TW 200421433A
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Taiwan
Prior art keywords
substrate
gas
oxide film
processed
processing container
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TW92126222A
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Chinese (zh)
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TWI238453B (en
Inventor
Takahiro Horiguchi
Ryo Kuwajima
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Tokyo Electron Ltd
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    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/455Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
    • C23C16/45563Gas nozzles
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/455Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
    • 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

Abstract

The purpose of the invented substrate processing apparatus is to have the capability of depositing a film stably and efficiently on a substrate. The substrate processing apparatus is equipped with a holding member, which supports a substrate at a position so as to make it confront a heater unit, and a rotation drive unit, which rotates the holding member that holds the substrate. A processing vessel is equipped with a gas spray nozzle, which is provided on one side of the processing space, and a rectangular exhaust vent, which is extended in a width direction and is provided on the other side of the processing space. The gas spray nozzle is equipped with plural spray openings, which are arranged in a line in the width direction of the processing space, so as to generate a stable flow of gas inside the processing space for enabling gas from the spray openings to pass over the surface of the substrate in a laminar flow. Thus, a film can be stably and efficiently deposited on the surface of the substrate; and the substrate processing apparatus can be improved in productivity.

Description

200421433 玖、發明說明: 【發明所屬之技術領域】 本發明係㈣基板處理裝置,特別是關於對基板施以成 膜等處理之基板處理裝置。 【先前技術】 在今日的超高速半導體裝置中,隨著微小化製程之進步 的同時,o.l# m以下之閘極長逐漸成為可能。一般隨著微 小化之_ ’半導體裝置之動作速度亦提高,但於如此相 當微小化之半導體裝置中,隨著微小化使閉極長之縮短, 有必要使閘極絕緣膜之膜厚按照關原則減少。 但閘極長一旦成為〇.l/zm以下 閘極絕緣膜之厚度於如 目前使用熱氧化膜之時,亦必須設定為卜2 nm或以下,作 在如此極薄之閘極絕緣財,會增大通道電流,其結果是 無法回避閘極漏電流增大之問題。 因為如此之情況’自以往即提案比電容率係較熱氧化膜 甚^ ’因_㈣極絕緣膜適用實際膜厚雖大,但換算成 熱氧化膜時膜厚小之Ta办或A1203、Zr〇2、励2,此外如 2〇4或HfSl〇4等之高電介f材料。#由使用如此之高電 Μ貝材料旦閘極長為G 以下,則儘管是在非常短 之超高速半導體裝置,亦可使㈣咖左右之物理上的膜厚 甲1極、邑緣膜’並可控制通道效果所造成之問極漏電流。 例如以彺所知之Ta2〇5膜,係可藉由法將Ta(〇c办^ 及〇2作為氣相原料而形成。典型之場合為,製程係在 減壓% ^下’約48(rc、或在其以上之溫度來實行。如此形200421433 (1) Description of the invention: [Technical field to which the invention belongs] The present invention relates to a substrate processing apparatus, and more particularly to a substrate processing apparatus that performs a process such as film formation on a substrate. [Previous technology] In today's ultra-high-speed semiconductor devices, with the progress of miniaturization processes, gate lengths below o.l # m have gradually become possible. Generally, with the miniaturization of the semiconductor device's operating speed also increases, but in such a very miniaturized semiconductor device, as the miniaturization shortens the length of the closed electrode, it is necessary to make the film thickness of the gate insulating film Reduced principles. However, once the gate length becomes less than 0.1 / zm, the thickness of the gate insulation film must be set to 2 nm or less, such as when a thermal oxide film is currently used. Increasing the channel current results in the inability to avoid the problem of increased gate leakage current. Because of this situation, 'Since the past, it has been proposed that the thermal conductivity film is more specific than the permittivity system.' Because the actual thickness of the insulating film is large, but the thickness of the Ta film or A1203, Zr is small when converted to a thermal oxide film. 〇2, excitation 2, and other high dielectric f materials such as 204 or HfS104. #From the use of such high-electricity materials, the gate electrode length is less than G, even though it is a very short ultra-high-speed semiconductor device, the physical film thickness of the left and right sides of the coffee can be 1 pole, and the edge film. And can control the leakage current caused by the channel effect. For example, the Ta205 film known by 彺 can be formed by using Ta (〇c ^ and 〇2 as a gas phase raw material. In a typical case, the process is performed under a reduced pressure% ^ 'about 48 ( rc, or at a temperature above this. This shape

OA87\87879.DOC 200421433 成之TaW5膜,進—步在氧氣氛圍中被熱處理,結果,解除 了膜中氧欠缺的情形’而膜本身亦結晶化。如此結晶化之 Ta2〇5膜,顯示出了大的比電容率。 人由提昇通道區域中之載波電流移動性之觀點,可在高電 "貝=極氧化膜及石夕基板間,隔著! nm以下,較佳為U職 2下厚度之極薄的基底氧化膜。基底氧化膜必須為非常 薄,其厚度若厚,則與在閘極絕緣膜使用高電介質膜之效 果相抵消。另一方面,#此非常薄的基底氧化膜,必須一 致地覆蓋住矽基板表面,且須要求不會形成界面位準等之 缺陷。 自以往起,薄閘極氧化膜-般係藉由石夕基板之急速熱氧 化(RTO)處理(例如,參照專利文獻丨)所形成,但若想形成 期望之1 nm以下厚度之熱氧化膜,則必須降低膜形成時之 處理溫度。但是,以如此低溫所形成之熱氧化膜,容易含 有界面位準等之缺陷,不適合作為高電介質閘極氧化膜之 基底氧化膜。 圖1係顯不含有高電介質閘極絕緣膜之半導體裝置1〇之 構成圖。 、圖1,半導體裝置10係形成於石夕基板i 1上,而於石夕基 板11上,隔著基底氧化膜12形成有Ta2〇5、Ai2〇3、Zr〇2、OA87 \ 87879.DOC 200421433 into a TaW5 film, which was further heat-treated in an oxygen atmosphere. As a result, the lack of oxygen in the film was lifted off 'and the film itself crystallized. The Ta205 film thus crystallized showed a large specific permittivity. From the viewpoint of improving the carrier current mobility in the channel area, it can be separated between the high-voltage " shell = polar oxide film and the Shi Xi substrate! Below nm, it is preferably a very thin base oxide film under U 2. The base oxide film must be very thin. If it is thick, the effect of using a high dielectric film for the gate insulating film is offset. On the other hand, #This very thin base oxide film must cover the surface of the silicon substrate uniformly, and it must be required not to form defects such as interface levels. From the past, thin gate oxide films are generally formed by rapid thermal oxidation (RTO) treatment of Shixi substrates (for example, refer to Patent Literature 丨), but if you want to form a desired thermal oxide film with a thickness of less than 1 nm , It is necessary to reduce the processing temperature during film formation. However, a thermal oxide film formed at such a low temperature is apt to contain defects such as an interface level, and is not suitable as a base oxide film for a high-dielectric gate oxide film. FIG. 1 is a diagram showing a configuration of a semiconductor device 10 that does not include a high-dielectric gate insulating film. 1. In FIG. 1, a semiconductor device 10 is formed on a Shi Xi substrate i 1, and Ta Shi 05, Ai 02, Zr 02 are formed on the Shi Xi substrate 11 via a base oxide film 12.

Hf〇2、ZrSiCU、HfSi〇4等之高電介質閘極氧化膜13,此外 於前述高電介質閘極氧化膜13上形成有閘極電極14。 於圖1之半導體裝置10中,於前述基底氧化膜層12之表面 部份,在保持矽基板11與基底氧化膜12間之界面平坦性之 O:\87\87879.DOC -8- 200421433 範圍’參雜氮(N)而形成氧氮化膜12A。藉由於基底氧化膜 12中形成比電容率較矽氧化膜大之氧氮化膜12A,可更加減 少基底氧化臈12之熱氧化膜換算膜厚。 如先前所說明,有關高速半導體裝置10中,前述基底氧 化膜12之較佳厚度為儘可能地薄。 但為了均勻地且安定地形成1 nm以下,例如〇· 8 nm以 下,進而對應2〜3原子層之〇.4nm左右之厚度之基底氧化膜 12,較以往更來得困難。 另外,為實現於基底氧化膜12上所形成之高電介質閘極 絕緣膜13之機能,係藉由熱處理以結晶化所堆積之高電介 質膜13,且必須進行缺氧補償,但對於高電介質膜13進行 如此之熱處理時,因基底氧化膜12之膜厚會增大,故藉由 使用咼電介質閘極絕緣膜13減少閘極絕緣膜之實際膜厚, 實質上即相互抵銷了。 隨著如此熱處理之基底氧化膜12之膜厚增大,暗示了在 矽基板11與基底氧化膜12之界面,氧原子及矽原子之相互 擴散,與隨著此之硅酸鹽過渡層的形成,或者因氧 板中的侵人而使基底氧化膜12成長之可能性。隨著如^ 底氧化膜12之熱處理而來之膜厚增大問題,特別是基底^ 化膜12之膜厚,在作為基底氧化膜時希望能減低至期望數 之原子層以下膜厚之時,會成為非常迫切之問題。 特許文獻1特開平5-47687號公報 【發明内容】 本發明係以提供解決上述課題 之新穎且有用 之基板處理 O:\87\87879.DOC -9- 200421433 裝置為目的。 本發明更詳細之目的係在於提供一種基板處理裝置,可 於矽基板表面,安定地形成非常薄且典型為2〜3原子層分之 厚度之氧化膜,進而將其氮化並形成氧氮化臈。 此外’本發明更詳細之目的係在於提供—種包含基板處 理裝置之叢集型基板處理系統,可於石夕基板表面,安定地 形成非常薄且典型為2〜3原子層分之厚度之氧化膜,進而使 其安定地氮化。 卜本1明之其他課題之目的,係在於提供一種基板 处里裝置’可解決如上述之課題,構成為可謀求氧化膜之 均性、產量之改善與污染的防止。 本發明為達成上述目的具有如以下之特徵。 根據本發明,氣體喷射部係由處理容H之-側起朝向被 於保持構件之被處理基板喷射氣體’而被設置於處理 =他側之排氣口’則排出通過被處理基板之氣體,藉 此了以謀求氧化膜之均一性、產量之改善與污染的防止, 並同時可以特定之流速(層流),自一個方向安定地提供氣體 至被保持於處理空間内之被處理基板表面,安定被處理基 成膜處理,且可有效率地進行而提高生產性。 =外|據本發明,藉由於水平方向配置成一列的複數 a =體噴射口’使得處理空間全體之氣流可保持於一致, :定被處理基板之朗處理q可有效率地進行而提 產性。 另外’根據本發明’藉由於氣體喷射部連接個別供給不The high-dielectric gate oxide film 13 such as Hf02, ZrSiCU, HfSi04, and the like, and a gate electrode 14 is formed on the high-dielectric gate oxide film 13 described above. In the semiconductor device 10 of FIG. 1, in the surface portion of the aforementioned base oxide film layer 12, the range of O: \ 87 \ 87879.DOC -8- 200421433 which maintains the flatness of the interface between the silicon substrate 11 and the base oxide film 12 'Doped with nitrogen (N) to form an oxynitride film 12A. Since the oxynitride film 12A having a larger specific permittivity than the silicon oxide film is formed in the base oxide film 12, the thermal oxide film conversion film thickness of the base oxide 12 can be further reduced. As described above, in the high-speed semiconductor device 10, the preferable thickness of the aforementioned base oxide film 12 is as thin as possible. However, in order to form the base oxide film 12 uniformly and stably below 1 nm, for example, 0.8 nm or less, and further corresponding to a thickness of about 0.4 nm of the 2 to 3 atomic layer, it is more difficult than in the past. In addition, in order to realize the function of the high-dielectric gate insulating film 13 formed on the base oxide film 12, the stacked high-dielectric film 13 is crystallized by heat treatment, and oxygen deficiency compensation must be performed, but for the high-dielectric film When such heat treatment is performed, since the film thickness of the base oxide film 12 is increased, the actual film thickness of the gate insulating film is reduced by using the rhenium dielectric gate insulating film 13, which substantially cancels each other out. With the increase in the thickness of the base oxide film 12 thus heat-treated, the inter-diffusion of oxygen atoms and silicon atoms at the interface between the silicon substrate 11 and the base oxide film 12 is implied, and the formation of a silicate transition layer with this Or the possibility of the base oxide film 12 growing due to the intrusion in the oxygen plate. As the thickness of the base oxide film 12 increases due to heat treatment, especially the thickness of the base oxide film 12, when it is used as the base oxide film, it is desired to reduce the film thickness to below the desired number of atomic layers. Will become a very urgent issue. [Patent Document 1] Japanese Patent Application Laid-Open No. 5-47687 [Summary of the Invention] The present invention aims to provide a novel and useful substrate processing O: \ 87 \ 87879.DOC -9- 200421433 device that solves the above-mentioned problems. A more detailed object of the present invention is to provide a substrate processing device capable of stably forming a very thin oxide film with a thickness of typically 2 to 3 atomic layers on the surface of a silicon substrate, and then nitriding it to form oxynitride. Alas. In addition, a more detailed object of the present invention is to provide a cluster substrate processing system including a substrate processing device, which can stably form a very thin oxide film with a thickness of typically 2 to 3 atomic layers on the surface of the Shixi substrate. , And then make it stable nitriding. The purpose of the other problems of the book 1 is to provide a substrate device. The device can solve the above-mentioned problems, and is configured to improve the uniformity of the oxide film, improve the yield, and prevent pollution. To achieve the above object, the present invention has the following features. According to the present invention, the gas ejection unit ejects the gas' from the-side of the processing volume H toward the substrate to be processed held by the holding member, and the exhaust port provided at the processing = other side exhausts the gas passing through the substrate to be processed, In this way, in order to achieve uniformity of the oxide film, improve the yield and prevent pollution, at the same time, it can provide gas at a specific flow rate (laminar flow) from one direction to the surface of the processed substrate held in the processing space. Stabilization is based on the film-forming treatment process, and can be performed efficiently to improve productivity. = 外 | According to the present invention, since the plural a = horizontal arrangement arranged in a row in the horizontal direction allows the airflow in the entire processing space to be kept uniform, the processing of the substrate to be processed can be efficiently performed to increase the production Sex. In addition, according to the present invention, due to the individual supply

O:\87\87879.DOC -10- 200421433 2種類氣體之複數個的氣體供給管路,可例如選擇性地安 定供給氮化氣體或氧化氣體,且可對處理空間中被處理基 板附近之區域,安定供給任意之氣體。 另外,根據本發明,由於排氣口係形成為較被處理基板 更加寬廣之長方形狀,故可提高通過被處理基板之氣體之 排氣效率’由此點亦可使處理空間全體之氣流保持於一 致,安定被處理基板之成膜處理,且可有效率地進行而提 高生產性。 另外,根據本發明,由於排氣口係由處理容器另一側之 底部連通至延伸形成於下方之排氣途徑,故可提高通過被 處理基板之虱體之排氣效率,由此點亦可使處理空間全體 之氣流保持於-致’安定被處理基板之成膜處理且可有效 率地進行。 【實施方式】 以下圖式說明有關本發明之實施形態。 、圖2係顯示本發明之基板處理裝置之—實施例構成之前 視圖。圖3係顯示本發明之基板處理裝置之—實施例構成之 側視圖。圖4為沿著圖2_八_八線之橫剖面圖。 、如圖2至圖4所示,基板處理裝置2〇如後述,係構成為可 =、.·只進订石夕基板之紫外光自由基氧化處理,與使用如此的 务外光自由基氧化處理所形成之氧化膜之高頻遠距離電聚 之自由基氮化處理。 基板處理裝置2G之主要構成,係包含:内部劃分成處理 空間之處理容器22、於特定溫度加熱被插入於處理容器22O: \ 87 \ 87879.DOC -10- 200421433 A plurality of gas supply lines of two kinds of gases can selectively and stably supply nitriding gas or oxidizing gas, for example, and can be applied to the area near the substrate to be processed in the processing space. , Stable supply of any gas. In addition, according to the present invention, since the exhaust port is formed in a wider rectangular shape than the substrate to be processed, the exhaust efficiency of the gas passing through the substrate to be processed can be improved. Consistently, it is possible to stabilize the film formation process of the substrate to be processed, and it can be performed efficiently to improve productivity. In addition, according to the present invention, since the exhaust port is communicated from the bottom of the other side of the processing container to an exhaust path extending downward, the exhaust efficiency of the lice passing through the substrate to be processed can be improved, and thus The airflow of the entire processing space is kept at a stable level, and the film formation processing of the substrate to be processed can be performed efficiently. [Embodiment] The following drawings explain embodiments of the present invention. Fig. 2 is a front view showing the structure of an embodiment of the substrate processing apparatus of the present invention. Fig. 3 is a side view showing the structure of an embodiment of the substrate processing apparatus of the present invention. FIG. 4 is a cross-sectional view taken along the line 2_8_8 in FIG. As shown in FIG. 2 to FIG. 4, the substrate processing apparatus 20 is structured as described below, and can be configured to only perform ultraviolet light radical oxidation treatment of the substrate of Shi Xi, and use such external light radical oxidation. A radical nitridation treatment of the high-frequency long-distance electropolymerization of the formed oxide film. The main structure of the substrate processing apparatus 2G includes a processing container 22 which is internally divided into a processing space, and is inserted into the processing container 22 by heating at a specific temperature.

O:\87\87879DOC 200421433 内部之被處理基板(石夕基板)之加熱部24、被搭載於處理容器 22上部之紫外線照射部26、供給氮自由基之遠距離電聚部 27、令被處理基板旋轉之旋轉驅動部28、使被插入處理空 間之被處理基板昇降之升降桿機構30、為減壓處理容器22 内部之排氣路徑32,及為供給氣體(氮氣、氧氣等之製程氣 體)於處理容器22内部之氣體供給部34。 另外,基板處理裝置20係具有為支持上述各主要構成部 之框36。框36為立體地組合鐵架者,由被置放於地面之台 狀之底部框38、由底部框38之後部而被豎立成垂直方向之 垂直框40, 4卜由垂直框40之中間部起延伸於水平方向而被 橫向架設之中間框42,及由垂直框4〇,41之上端部橫向架設 於水平方向之上部框44所構成。 於底部框38搭載有冷卻水供給部46、包含電磁閥之排氣 用閥48a,48b、渦輪分子幫浦5〇、真空管路51、紫外線照射 部26之電源單位52、升降桿機構3〇之驅動部136及氣體供給 部34等。 八'σ 於垂直框40之内部形成有可穿插各種電纜線之電纜線導 官40a。另外’於垂直框41之内部形成有排氣導管仏。此 外’在被固定於垂直框4〇中間部之托架58上安裝有緊急停 止開關6G ’而在被固定於垂直框41中間部之托架α上則安 装有由冷卻水進行溫度調整之溫度調整器Μ。 於中間框42上係支持有··上述處理容器22、紫外線照射 部26、遠轉m卩㈣、升轉機構30、 及卿控制器57。另外,於上部框44上則搭載有:可連通O: \ 87 \ 87879DOC 200421433 The heating part 24 of the substrate to be processed (Shiyu substrate) inside, the ultraviolet irradiation part 26 mounted on the upper part of the processing container 22, the long-distance electropolymerization part 27 for supplying nitrogen radicals, and the processed part Rotary drive unit 28 for substrate rotation, lift rod mechanism 30 for lifting and lowering the substrate to be processed inserted into the processing space, exhaust path 32 inside the decompression processing container 22, and supply gas (process gas such as nitrogen, oxygen, etc.) A gas supply portion 34 inside the processing container 22. The substrate processing apparatus 20 includes a frame 36 for supporting the above-mentioned main components. The frame 36 is a three-dimensionally assembled iron frame. The bottom frame 38 is placed on the floor in the shape of a table, and the vertical frame 40 is erected in the vertical direction from the rear portion of the bottom frame 38. The middle portion of the vertical frame 40 The middle frame 42 extending from the horizontal direction and being horizontally erected, and the upper end of the vertical frame 40,41 are horizontally erected from the horizontal upper frame 44. The bottom frame 38 is equipped with a cooling water supply unit 46, exhaust valves 48a and 48b including a solenoid valve, a turbo molecular pump 50, a vacuum line 51, a power supply unit 52 of the ultraviolet irradiation unit 26, and a lifting rod mechanism 30 The driving section 136, the gas supply section 34, and the like. A cable conductor 40a is formed inside the vertical frame 40 through which various types of cables can be inserted. An exhaust duct 仏 is formed inside the vertical frame 41. In addition, 'emergency stop switch 6G is installed on the bracket 58 fixed to the middle portion of the vertical frame 40', and the bracket α fixed to the middle portion of the vertical frame 41 is provided with a temperature adjusted by cooling water Adjuster M. Supported on the middle frame 42 are the above-mentioned processing container 22, ultraviolet irradiation section 26, telescoping m 卩 ㈣, lifting mechanism 30, and controller 57. In addition, the upper frame 44 is equipped with:

O:\87\87879.DOC -12- 200421433 自氣體供給部34所拉出之複數條氣體管路58之氣體箱66、 離子測置控制器68、進行壓力控制之apc控制器70及控制 渦輪分子幫浦5〇之TMP控制器72等。 圖5係顯示被配置於處理容器22下方之機器構成之前視 圖。圖6係顯示被配置於處理容器22下方之機器構成之俯視 圖。圖7係顯示被配置於處理容器22下方之機器構成之側視 圖。圖8A係顯示排氣路徑32之構成之俯視圖;而圖8]g則顯 示排氣路徑32之構成之前視圖;圖8(:為沿著B-B線之縱剖 面圖。 如圖5至圖7所示,於處理容器22之後部下方設置有排出 處理容器22内部氣體之排氣路徑32。該排氣路徑32係被安 裝成與橫向尺寸與形成於處理容器22内部之處理空間之橫 向寬幅大致相同而形成之長方形排氣口 74連通。 如此,由於排氣口 74係延伸形成為對應處理容器22内部 之杈向寬幅尺寸之長度,故自處理容器22之前部22a側供給 至内部之氣體,會如後述般,通過處理容器22内部流向後 方’以一定流速(層流)朝排氣路徑32有效率地排氣。 如圖8A〜圖8C所示,排氣路徑32係具有··被連通至排氣 口74之長方形開口部32a、開口部32a之左右側面朝向下方 而傾斜成錐形狀之錐形部32b、在錐形部32b之下端處通路 面積被集中之底部32c、由底部3 2c向前方突出之[字型之主 排氣管32d、開口於主排氣管32d下端之排出口 32e及向錐形 部32b之下部32f開口之分流用排出口 32g。排出口 32e被連 通至渦輪分子幫浦50之吸氣口。另外,分流用排出口32g被O: \ 87 \ 87879.DOC -12- 200421433 A gas box 66 of a plurality of gas lines 58 drawn from the gas supply section 34, an ion measurement controller 68, an apc controller 70 for pressure control, and a control turbine Molecular pump 50, TMP controller 72 and so on. FIG. 5 is a front view showing the configuration of a machine disposed below the processing container 22. As shown in FIG. FIG. 6 is a plan view showing the structure of a machine arranged below the processing container 22. As shown in FIG. FIG. 7 is a side view showing the structure of a machine arranged below the processing container 22. As shown in FIG. FIG. 8A is a plan view showing the structure of the exhaust path 32; and FIG. 8] g is a front view showing the structure of the exhaust path 32; FIG. 8 (: is a vertical cross-sectional view taken along the line BB. As shown in FIG. 5 to FIG. 7 As shown, an exhaust path 32 for exhausting the gas inside the processing container 22 is provided below the rear part of the processing container 22. The exhaust path 32 is installed to have a lateral size and a lateral width of the processing space formed inside the processing container 22. The same rectangular exhaust port 74 communicates. In this way, since the exhaust port 74 is extended to correspond to the length of the branch inside the processing container 22 to a wide size, the gas supplied to the inside from the front 22a side of the processing container 22 As will be described later, the inside of the processing container 22 flows backward to the exhaust path 32 at a certain flow rate (laminar flow) efficiently. As shown in FIGS. 8A to 8C, the exhaust path 32 has a The rectangular opening portion 32a communicating with the exhaust port 74, the left and right side surfaces of the opening portion 32a, and the tapered portion 32b inclined in a tapered shape facing downward, the bottom portion 32c where the passage area is concentrated at the lower end of the tapered portion 32b, and the bottom portion 3 2c forward The [shaped main exhaust pipe 32d, a discharge opening 32e opened at the lower end of the main exhaust pipe 32d, and a discharge discharge opening 32g opening to the lower portion 32f of the tapered portion 32b. The discharge opening 32e is communicated to the turbo molecular gang Suction port for pu 50. In addition, 32 g

O:\87\87879.DOC -13- 200421433 連通至分流管路5 1 a。 如圖5至圖7所示,由處理容器22之排氣口74所排出之氣 體,係藉由涡輪分子幫浦5〇之吸引力,自形成為長方形之 開口部32a流入,通過錐形部32b至底部32c,再經由主排氣 管32d與排出口 32e被引導至渦輪分子幫浦5〇。 渦輪分子幫浦50之吐出管5〇a·經由閥48a被連通至真空 管路51。因此’充填於處理容器22内部之氣體,當閥他被 打開時則經由渦輪分子幫浦5〇向真空管路5丨排出。另外, 於排氣路徑32之分流用排出口32g係連接有分流管路51&, 而該分流管路51a會因閥48b之打開而與真空管路5i連通。 在此,說明有關構成本發明重要部分之處理容器22及其 周邊機器之構成。 ~ [處理容器22之構成] 圖9係擴大顯示處理容器22及其周邊機器之側面縱剖面 圖。圖1G為從上方所見到拿掉蓋子構件82之處理容器22内 部之俯視圖。 —如圖9與圖10所示,處理容器22係藉由蓋子構件82閉塞住 室80上部開口之構成,其内部成為製程空間(處理空間)84。 處理容器22在前部22a形成有可供給氣體之供給口 %, 而後部现則形成有搬送口 94。於供給π 22g設置有後述之 氣體噴射噴嘴部93,而於搬送口 94則連通有後述之閘極閥 96 〇 圖11為處理容器22之俯視圖。圖12為處理容器22之前視 圖。@13為處理容器22之仰視圖。圖14為沿著圖i2t^c_cO: \ 87 \ 87879.DOC -13- 200421433 is connected to the branch line 5 1 a. As shown in FIGS. 5 to 7, the gas discharged from the exhaust port 74 of the processing container 22 flows through the opening 32 a formed in a rectangular shape by the attraction force of the turbo molecular pump 50 and flows through the cone. The portion 32b to the bottom portion 32c are guided to the turbo molecular pump 50 through the main exhaust pipe 32d and the discharge port 32e. The discharge pipe 50a of the turbo molecular pump 50 is connected to a vacuum line 51 via a valve 48a. Therefore, the gas filled in the processing container 22 is discharged to the vacuum line 5 through the turbo molecular pump 50 when the valve is opened. In addition, a branching outlet port 51g is connected to the branching outlet 51 & in the exhaust path 32, and the branching line 51a is communicated with the vacuum line 5i by the opening of the valve 48b. Here, the configuration of the processing container 22 and its peripheral devices constituting an important part of the present invention will be described. ~ [Configuration of the processing container 22] Fig. 9 is an enlarged side sectional view showing the processing container 22 and its peripheral devices. Fig. 1G is a plan view of the inside of the processing container 22 with the lid member 82 removed from above. -As shown in Figs. 9 and 10, the processing container 22 is constructed by closing the upper opening of the chamber 80 by a cover member 82, and the inside thereof becomes a process space (processing space) 84. The processing container 22 is formed with a gas supply port% in the front portion 22a, and a transport port 94 is now formed in the rear portion. A gas injection nozzle section 93 to be described later is provided at 22 g of supply π, and a gate valve 96 to be described later is communicated to the transfer port 94. FIG. 11 is a plan view of the processing container 22. FIG. 12 is a front view of the processing container 22. @ 13 is a bottom view of the processing container 22. Figure 14 is along figure i2t ^ c_c

O:\87\87879 DOC -14- 200421433 線之縱剖面圖。圖15為處理容器22之右側視圖。圖16為處 理容器22之左側視圖。 如圖11至圖16所示,於處理容器22之底部22c設置有:被 插入加熱部24之開口 73,及前述開口成長方形之排氣口 74。於排氣口 74連通有前述之排氣路徑32。另外,室80與 蓋子構件82,係例如切割加工鋁合金,並加工成如上述之 形狀者。 另外,於處理容器22之右側面22e係安裝有:為窺視製程 空間84之第1、第2窗口 75, 76,及為測定製程空間84之溫度 之感應器單元77。 於本實施例中,由於在右側面22e中央之左側配置有形成 為橢圓形之第1窗口 75,而右側面22e中央之右側配置有形 成為圓形之第2窗口 76,因而可由兩方面直接目視被保持於 製程空間84之被處理基板w之狀態,故有利於觀測被處理 基板W之成膜狀況等。 另外’窗口 75, 76之構成為在插入有熱電偶等之溫度測定 器具時,可由處理容器22拆掉。 另外,於處理容器22之左側面22d,係安裝有為測定製程 空間84之壓力之感應器單元85。於該感應器單元85設置有 測定範圍不同的3個壓力計85a〜85c,可高精密度地測定製 程空間84之壓力變化。 另外,於形成製程空間84之處理容器22之内壁之四個角 落’設置有形成為R形狀之彎曲部22h,其不僅可藉由該彎 曲部22h迴避應力集中,並可發揮使由氣體喷射喷嘴部93所 O:\87\87879.DOC -15- 200421433 射喷出之氣體流安定之作用。 [紫外線照射部26之構成] 如圖8至圖11所示,紫外線照射部26係被安裝於蓋子構件 82之上面。於該紫外線照射部26之筐體26a内部,以特定間 隔平行地配置有形成為圓筒狀之2根紫外線光源(uv燈)%, 87。 , 該务、外線光源86,87具有發出波長為172 nm之紫外線之 特性,被设置於經由形成於蓋子構件82之橫向延伸之長方 形開口 82a,82b,可對與保持於製程空間84之被處理基板w 上面相對之製程空間84之前半側(於圖8左半部)區域照射紫 外線之位置。 另外,由延伸成直線狀之紫外線光源86, 87照射在被處理 基板W上之紫外線之強度分佈並不一致,而是因被處理基 板w之半徑方向之位置而變化,一方是越往被處理基板w 之外周圍側則越減少,另一方則是越往内周圍侧則越減 少。如此紫外線光源86, 87雖在被處理基板w上形成單獨且 單調地變化之紫外線強度分佈,但對於被處理基板W之紫 外線強度分佈之變化方向則成相反。 因此’藉由UV燈控制器57的控制來最適化紫外線光源86, 87之驅動能量,故可在被處理基板w上實現非常地一致之 紫外線強度分佈。 另外’如此的驅動能量之最適值,係變化對紫外線光源 86, 87之驅動輸出而評估成膜結果,來求得最適值。 另外’被處理基板W與紫外線光源86, 87之圓筒狀圓筒芯 O:\87\87879.DOC -16- 200421433 中心之距離,例如係設定成50〜3〇〇 mm,較佳為100〜200 mm 左右。 圖17係擴大顯示紫外線光源86, δ7之安裝構造之縱剖面 圖。 如圖17所示,紫外線光源86, 87係被保持於相對於紫外線 照射部26筐體26a之底部開口 2_6b之位置。並且,底部開口 26b係形成為於相對於被保持在製程空間84之被處理基板 W上面之位置處開口,且橫向寬幅尺寸較紫外線光源%, 全長更長之長方形。 於底部開口 26b之邊緣部26c,安裝有由透明石英所形成 之透明窗88。透明窗88將由紫外線光源%,87所照射之紫外 線透射入製程空間84,並且具有可承受製程空間84減壓時 之壓力差之強度。 另外,於透明窗88下面邊緣部,形成有抵接被安裝於底 部開口26b之邊緣部26c之溝内之密封構件(〇環)的之密封 面88a。該密封面88a係由為保護密封構件89之塗層或由黑 石英所形成。藉此,密封構件89之材質不會分解,可防止 劣化保護密封性能,同時並防止密封構件89之材質侵入至 製程空間84。 另外,於透明窗88上面邊緣部與不銹鋼製之防護罩88b 抵接,以提高鎖緊構件91夾住透明窗88時之強度,防止因 鎖緊時之擠壓力造成透明窗88破損。 另外,於本實施例中,係將紫外線光源86,87與透明窗“ 配置為於與由氣體噴射噴嘴部93所噴射之氣體流之流動方 O:\87\87879 DOC •17- 200421433 向垂直而I伸之方向,但不限於此,例如亦可配置成使紫 外線光源86, 87與透明窗88延伸於氣體流之流動之方向。 [氣體喷射噴嘴部93之構成] 如圖9與圖1〇所示,處理容器22在開口於前部22a之供給 口 22g處,設置有對製程空間84内部喷射氮氣或氧氣之氣體 噴射喷嘴部93。該氣體噴射噴嘴部93係如後述,在製程空· 間84之杈向方向配置有一列的複數個噴射口 % ,可使由複 - 數個的喷射口 93a所喷射之氣體,以層流狀態通過被處理基 板W表面,而在製程空間84内部產生安定的氣流。 _ 另外,閉塞製程空間84之蓋子構件82之下面與被處理基 板w之距離,係例如被設定成5〜100 mm,較理想為25〜85 mm左右。 [加熱部24之構成] 如圖9與圖1〇所示,加熱部24之構成為具備有:鋁合金製 之底座110、被固定於底座11〇上之透明之石英鐘罩112、被 收容於石英鐘罩112之内部空間113之SiC加熱器114、由不 透明石英所形成之熱反射構件(反射器)116、由被裝載於石鲁 英鐘罩112上面之SiC加熱器114所加熱之SiC基板設置台 (加熱構件)118。 因此,SiC加熱器114與熱反射構件116係由石英鐘罩112 之内部空間113所隔離,可防止在製程空間84之污染。另 外’於洗淨步驟,因僅需洗淨被露出於製程空間84内之SiC 基板設置台118即可,故可省略洗淨SiC加熱器114與熱反射 構件116之作業。 O:\87\87879.DOC -18 - 200421433 被處理基板W係由保持構件120保持在相對於SiC基板設 置台11 8之上方。另一方面,SiC加熱器114被裝載於熱反射 構件116之上面,而SiC加熱器114所發散之熱係放射至SiC 基板設置台118,且熱反射構件116所反射之熱亦放射至SiC 基板設置台11 8。此外,本實施例之SiC加熱器114係在稍稍 9 離開SiC基板設置台118之狀態下加熱至約700°C。O: \ 87 \ 87879 DOC -14- 200421433 Vertical section view of line. FIG. 15 is a right side view of the processing container 22. FIG. 16 is a left side view of the processing container 22. As shown in Figs. 11 to 16, the bottom 22c of the processing container 22 is provided with an opening 73 inserted into the heating section 24, and an exhaust opening 74 having a rectangular opening as described above. The above-mentioned exhaust path 32 is communicated with the exhaust port 74. The chamber 80 and the cover member 82 are made of, for example, a cut aluminum alloy and processed into a shape as described above. In addition, on the right side 22e of the processing container 22, first and second windows 75, 76 for viewing the process space 84, and a sensor unit 77 for measuring the temperature of the process space 84 are mounted. In this embodiment, the first window 75 formed in an oval shape is arranged on the left side in the center of the right side 22e, and the second window 76 is formed in a circle shape on the right side in the center of the right side 22e. The state of the substrate w to be processed held in the process space 84 is advantageous for observing the film formation status of the substrate W to be processed. The windows 75 and 76 are configured so that they can be removed by the processing container 22 when a temperature measuring instrument such as a thermocouple is inserted. In addition, a sensor unit 85 for measuring the pressure in the process space 84 is mounted on the left side 22d of the processing container 22. The sensor unit 85 is provided with three pressure gauges 85a to 85c having different measurement ranges, and the pressure change in the process space 84 can be measured with high precision. In addition, the four corners of the inner wall of the processing container 22 forming the process space 84 are provided with curved portions 22h formed in an R shape, which not only can avoid stress concentration by the curved portions 22h, but also can exert a gas injection nozzle portion. The role of 93 O: \ 87 \ 87879.DOC -15- 200421433 The stability of the jet gas flow. [Configuration of the ultraviolet irradiation section 26] As shown in Figs. 8 to 11, the ultraviolet irradiation section 26 is mounted on the cover member 82. Inside the housing 26a of the ultraviolet irradiation section 26, two ultraviolet light sources (uv lamps), which are formed in a cylindrical shape, are arranged in parallel at a specific interval, 87, 87. This service, the external light sources 86, 87 have the characteristic of emitting ultraviolet rays with a wavelength of 172 nm, and are arranged in the rectangular openings 82a, 82b formed in the lateral extension of the cover member 82, and can be processed and held in the processing space 84. The position on the upper surface of the substrate w opposite to the front half of the process space 84 (at the left half of FIG. 8) is irradiated with ultraviolet rays. In addition, the intensity distribution of the ultraviolet rays irradiated by the ultraviolet light sources 86 and 87 extending in a straight line on the substrate to be processed W is not uniform, but varies depending on the position in the radial direction of the substrate to be processed w. w The outer peripheral side decreases, and the other side decreases toward the inner peripheral side. In this way, although the ultraviolet light sources 86 and 87 form an ultraviolet intensity distribution that changes individually and monotonously on the substrate to be processed w, the direction of change of the ultraviolet intensity distribution of the substrate to be processed W is opposite. Therefore, the driving energy of the ultraviolet light sources 86, 87 is optimized by the control of the UV lamp controller 57, so that a very uniform ultraviolet intensity distribution can be realized on the substrate w to be processed. In addition, the optimum value of such driving energy is obtained by changing the driving output of the ultraviolet light sources 86 and 87 and evaluating the film formation results to obtain the optimum value. In addition, the distance between the center of the substrate W to be processed and the cylindrical core O: \ 87 \ 87879.DOC -16- 200421433 of the ultraviolet light source 86, 87 is set to, for example, 50 to 300 mm, preferably 100. ~ 200 mm. Fig. 17 is a longitudinal sectional view showing the mounting structure of the ultraviolet light source 86 and δ7 in an enlarged manner. As shown in Fig. 17, the ultraviolet light sources 86 and 87 are held at positions 2-6b with respect to the bottom opening of the housing 26a of the ultraviolet irradiation section 26. In addition, the bottom opening 26b is formed as a rectangle that is open at a position above the substrate W to be held in the process space 84, and has a width in the lateral direction that is larger than that of the ultraviolet light source, and a rectangular shape with a longer overall length. A transparent window 88 made of transparent quartz is attached to the edge portion 26c of the bottom opening 26b. The transparent window 88 transmits the ultraviolet rays irradiated by the ultraviolet light source%, 87 into the process space 84, and has a strength capable of withstanding the pressure difference when the process space 84 is decompressed. In addition, a sealing surface 88a is formed on the lower edge portion of the transparent window 88 to abut a sealing member (o-ring) mounted in the groove of the edge portion 26c of the bottom opening 26b. The sealing surface 88a is formed of a coating for protecting the sealing member 89 or of black quartz. Thereby, the material of the sealing member 89 will not be decomposed, the deterioration of the protective sealing performance can be prevented, and the material of the sealing member 89 can be prevented from penetrating into the process space 84. In addition, the upper edge portion of the transparent window 88 is in contact with a protective cover 88b made of stainless steel to increase the strength of the locking member 91 when the transparent window 88 is sandwiched and prevent the transparent window 88 from being damaged due to the pressing force during the locking. In addition, in this embodiment, the ultraviolet light sources 86, 87 and the transparent window are arranged so as to be perpendicular to the flow direction of the gas flow sprayed from the gas spray nozzle portion 93. O: \ 87 \ 87879 DOC • 17- 200421433 The direction of I extension is not limited to this, for example, the ultraviolet light sources 86, 87 and the transparent window 88 may be arranged to extend in the direction of the flow of the gas flow. [Configuration of the gas injection nozzle portion 93] As shown in FIG. 9 and FIG. As shown, the processing container 22 is provided with a gas injection nozzle portion 93 that injects nitrogen or oxygen into the process space 84 at the supply port 22g opened at the front portion 22a. The gas injection nozzle portion 93 is described later in the process space. A plurality of ejection ports% are arranged in a row in the direction of the branch 84, and the gas ejected from the plurality of ejection ports 93a can pass through the surface of the substrate W to be processed in a laminar flow state, and is generated inside the process space 84. Stable airflow. _ In addition, the distance between the lower surface of the cover member 82 and the substrate w to be closed in the process space 84 is set to, for example, 5 to 100 mm, and preferably 25 to 85 mm. [Configuration of the heating section 24 ] Figure 9 and Figure 10 The heating section 24 is configured to include a base 110 made of aluminum alloy, a transparent quartz bell cover 112 fixed to the base 110, a SiC heater 114 housed in an inner space 113 of the quartz bell cover 112, and an opaque body. A heat reflecting member (reflector) 116 made of quartz, and a SiC substrate mounting table (heating member) 118 heated by a SiC heater 114 mounted on the bell jar 112. Therefore, the SiC heater 114 and the heat reflecting member 116 is isolated by the inner space 113 of the quartz bell cover 112, which can prevent contamination in the process space 84. In addition, in the cleaning step, it is only necessary to clean the SiC substrate setting table 118 exposed in the process space 84. Therefore, the operation of cleaning the SiC heater 114 and the heat reflection member 116 can be omitted. O: \ 87 \ 87879.DOC -18-200421433 The processed substrate W is held above the SiC substrate mounting table 118 by the holding member 120. On the other hand, the SiC heater 114 is mounted on the heat reflection member 116, and the heat emitted by the SiC heater 114 is radiated to the SiC substrate setting table 118, and the heat reflected by the heat reflection member 116 is also radiated to the SiC.8. The mounting base plate 11 Further, the present embodiment of the SiC heater 114 based on Example 9 is slightly away from the SiC substrate 118 is disposed in a state of heating to about 700 ° C.

SiC基板設置台118因其熱傳導率佳,故可有效率地將來 自SiC加熱器114之熱傳達至被處理基板W,並消除被處理 基板W邊緣部份與中心部份之溫度差,防止被處理基板w φ 因溫度差而彎曲。 [旋轉驅動部28之構成] 如圖9與圖1〇所示,旋轉驅動部28係由以下所構成:在sic 基板設置台118之上方保持被處理基板w之保持構件120、 被固定於底座110下面之外殼122、對在由外殼122所劃分之 内部空間124内結合於保持構件12〇之軸I20d之陶瓷軸126 進行旋轉驅動之馬達128、及傳達馬達128之旋轉之磁鐵聯 結裔13 0。 於旋轉驅動部28中,保持構件120之軸I20d係貫通112石 英鐘罩並結合於陶瓷軸126,而於陶瓷軸126與傳達馬達128 之旋轉轴間則是經由磁鐵聯結器π〇以非接觸之方式傳達 驅動能量,故使旋轉驅動系統之構成變得簡潔,亦有助於 裝置全體之小型化。 保持構件120自120d上端起,具有於水平方向延伸成放射 狀之臂部120a〜120c。被處理基板W以被裝載於保持構件The SiC substrate setting table 118 has good thermal conductivity, so it can efficiently transfer heat from the SiC heater 114 to the substrate W to be processed, and eliminate the temperature difference between the edge portion and the central portion of the substrate W to be processed. The processing substrate w φ is bent due to a temperature difference. [Structure of Rotary Drive Unit 28] As shown in FIGS. 9 and 10, the rotary drive unit 28 is composed of a holding member 120 that holds a substrate to be processed w above the sic substrate setting table 118, and is fixed to the base. The housing 122 below 110, the motor 128 for rotationally driving the ceramic shaft 126 of the shaft I20d coupled to the holding member 12 in the internal space 124 divided by the housing 122, and a magnet coupling 13 for transmitting the rotation of the motor 128 . In the rotation driving part 28, the shaft I20d of the holding member 120 is penetrated through the 112 quartz bell cover and coupled to the ceramic shaft 126, and the ceramic shaft 126 and the rotation shaft of the transmission motor 128 are connected in a non-contact manner through a magnet coupling π. The method transmits driving energy, so that the structure of the rotary driving system is simplified, and it contributes to the miniaturization of the entire device. The holding member 120 has arm portions 120a to 120c extending radially in a horizontal direction from the upper end of 120d. The substrate W to be processed is loaded on the holding member

O:\87\87879.DOC -19- 200421433 120之臂部120a〜120c之狀態保持著。如此,被保持之被處 理基板W與保持構件120 —起由傳達馬達丨28以特定之旋轉 速度來旋轉,藉此可平均因114SiC加熱器發熱之溫度分 佈’並使來自紫外線光源8 6,8 7所照射之紫外線之強度分佈 均一,且可對表面施以均一之成膜。 [升降桿機構3〇之構成] 如圖9與圖10所示’升降桿機構3〇係被設置於室之下方 且112石英鐘罩之側面,由被插入於室8〇内之昇降臂132、 被連結於昇降臂132之昇降軸134、使昇降軸134昇降之驅動 部136所構成。昇降臂132係例如由陶瓷或石英所形成,如 圖10所示’具有:結合著昇降軸134上端之結合部13 2a,及 包圍SiC基板設置台118外周之環狀部n2b。並且,於昇降 臂132,在圓周方向上以120度之間隔,設置有由環狀部132b 之内周起向中心延伸之3支抵接銷138a〜138c。 抵接銷138a〜138c會下降至嵌合由SiC基板設置台118之 外周向中心延伸而形成之溝118a〜118c之位置,藉由昇降臂 132上昇而再移動至Sic基板設置台ι18之上方。另外,抵接 銷138a〜13 8c係配置成不干涉到較sic基板設置台118中 心’延伸於外周側所形成之保持構件120之臂部120a〜120c。 昇降臂132其搬送自動機98之機械臂在取出被處理基板 W之前’係使上述抵接銷n8a〜138c抵接於被處理基板冒之 下面’再由保持構件120之臂部120a〜120c拿起被處理基板 W °藉此’搬送自動機98之機械臂可移動至被處理基板w 之下方’而可以降下昇降臂132來搬送並保持被處理基板 O:\87\87879.DOC -20- 200421433 w 〇 [石英塾圈100之構成] 如圖9與圖10所示,於處理容器22之内部,為遮蔽紫外線 而安裝有例如由白色等之不透明石英所形成之石英墊圈 1〇〇。又,石英墊圈100係如後所述,為組合下部盒體1〇2、 侧面盒體104、上部盒體1〇6及包覆石英鐘罩112外周之圓筒 狀盒體108之構成。 該石英墊圈1〇〇,藉由覆蓋形成製程空間84之處理容器22 與蓋子構件82之内壁,可得到防止處理容器。與蓋子構件 82之熱膨脹之隔熱效果,並防止處理容器22與蓋子構件82 之内壁因紫外線而氧化,且具有防止金屬污染之任務。 [遠距離電漿部27之構成] 如圖9與圖1〇所示,於製程空間84供給氮自由基之遠距離 電漿部27,係被安裝於處理容器22之前部22a,並經由供給 管路90連通至處理容器22之供給口 92。 於该遠距離電漿部27中,供給有Ar等之惰性氣體與氮氣 體’藉由電漿將此活性化,可形成氮自由基。如此所形成 之氮自由基會沿著被處理基板w之表面流動而氮化基板表 面。 另外’於其他之氮氣體,亦可實施使用〇2、NO、n2〇、 NH3氣體等之氧化、氮氧化自由基製程。 [閘極閥96之構成] 如圖9與圖1〇所示,於處理容器22之後部設置有為搬送被 處理基板w之搬送口 94。該搬送口94係由閘極閥96所閉塞O: \ 87 \ 87879.DOC -19- 200421433 The state of the arms 120a ~ 120c of 120 is maintained. In this way, the substrate W to be processed and the holding member 120 are rotated by the conveying motor 28 at a specific rotation speed, so that the temperature distribution of heat generated by the 114SiC heater can be averaged and the ultraviolet light source 8 6, 8 can be obtained. 7. The intensity distribution of the irradiated ultraviolet rays is uniform, and the surface can be uniformly formed into a film. [Configuration of the lifting rod mechanism 30] As shown in FIG. 9 and FIG. 10, 'the lifting rod mechanism 30 is provided below the chamber and on the side of the 112 quartz bell cover, and the lifting arms 132, A lifting shaft 134 connected to the lifting arm 132 and a driving portion 136 for lifting the lifting shaft 134 are configured. The elevating arm 132 is made of, for example, ceramics or quartz. As shown in FIG. 10 ', the elevating arm 132 includes a joint portion 13 2a to which the upper end of the elevating shaft 134 is joined, and an annular portion n2b surrounding the outer periphery of the SiC substrate mounting base 118. In addition, at the lifting arm 132, three contact pins 138a to 138c extending from the inner periphery of the annular portion 132b toward the center are provided at intervals of 120 degrees in the circumferential direction. The abutment pins 138a to 138c are lowered to the positions where the grooves 118a to 118c formed by extending from the outer periphery of the SiC substrate setting table 118 to the center are fitted, and are raised by the lifting arm 132 to move above the Sic substrate setting table 18. In addition, the contact pins 138a to 13c are arranged so as not to interfere with the arms 120a to 120c of the holding member 120 formed to extend from the center of the sic substrate mounting base 118 to the outer peripheral side. The lifting arm 132 and the robot arm of the transfer robot 98 'before taking out the substrate W to be processed', the above-mentioned abutment pins n8a to 138c are brought into contact with the bottom surface of the substrate to be processed, and then taken by the arms 120a to 120c of the holding member 120 Lifting the substrate to be processed W ° This means that the robot arm of the transfer robot 98 can be moved below the substrate w to be processed, and the lifting arm 132 can be lowered to transfer and hold the substrate to be processed. O: \ 87 \ 87879.DOC -20- 200421433 w 〇 [Configuration of quartz ring 100] As shown in FIG. 9 and FIG. 10, a quartz gasket 100 made of, for example, white opaque quartz is installed inside the processing container 22 to shield ultraviolet rays. The quartz washer 100 is a combination of a lower case 102, a side case 104, an upper case 106, and a cylindrical case 108 covering the outer periphery of the quartz bell cover 112, as described later. This quartz gasket 100 can prevent the processing container by covering the inner wall of the processing container 22 and the lid member 82 forming the process space 84. The thermal expansion effect with the lid member 82 prevents the inner walls of the processing container 22 and the lid member 82 from being oxidized by ultraviolet rays, and has the task of preventing metal contamination. [Configuration of the remote plasma unit 27] As shown in FIG. 9 and FIG. 10, the remote plasma unit 27 that supplies nitrogen radicals to the process space 84 is installed at the front portion 22a of the processing container 22 and is supplied through The pipeline 90 is connected to the supply port 92 of the processing container 22. In this long-distance plasma unit 27, an inert gas such as Ar and a nitrogen gas are supplied and activated by a plasma to form nitrogen radicals. The nitrogen radicals thus formed will flow along the surface of the substrate w to be processed to nitride the surface of the substrate. In addition, in other nitrogen gas, oxidation, nitrogen oxidation radical processes using 02, NO, n2O, NH3 gas and the like can also be performed. [Configuration of Gate Valve 96] As shown in FIG. 9 and FIG. 10, a transfer port 94 for transferring the substrate w to be processed is provided at the rear of the processing container 22. The transfer port 94 is closed by a gate valve 96

O:\87\87879 DOC -21 - 200421433 住,僅於搬送被處理基板W時由閘極閥%之打開動作而開 放。 於閘極閥96之後方設置有搬送自動機98。並且,配合閘 極閥96之打開動作,搬送自動機98之機械臂會由搬送口 進入至製程空間84之内部,並進行送被處理基板%之交換 作業。 L上述各構成部之詳細] (1)在此,詳細說明關於上述氣體噴射喷嘴部93之構成。 圖18係擴大顯示氣體噴射喷嘴部93之構成之縱剖面圖。 圖B係擴大顯示氣體喷射喷嘴部93之構成之橫剖面圖。圖 20係擴大顯示氣體噴射噴嘴部93之構成之前視圖。 如圖18至圖20所示,氣體喷射噴嘴部%於前面中央,具 有可連通上述遠距離電漿部27之供給管路9〇之 而於連通孔92之上方,則安裝有複數個喷射口叫〜队於橫 方向配設成-列之喷嘴板93bi〜93b3。噴射口 9%〜93an係例 如為直徑1 mm的小孔’而以10麵之間隔設置。 另外,於本實施例中,雖設有包含小孔之喷射口 %〜931但不限於此’例如亦可為以細小狹縫做為喷射 口之構成。 、 卜喷嘴板931931^係被鎖緊於氣體喷射嗔嘴部^之 因此’自切口 93ai〜93an所噴射之氣體會由氣 射噴嘴部93之壁面流向前方。 、 .在喷射口 93a丨〜93an被設置於管狀之喷嘴管路時, 、射口 93ai〜93an所噴射之氣體—部份會發生回流至喷嘴O: \ 87 \ 87879 DOC -21-200421433, only when the substrate W to be processed is transported, it is opened by the gate valve% opening operation. A transfer robot 98 is provided behind the gate valve 96. In addition, in cooperation with the opening operation of the gate valve 96, the robot arm of the transfer robot 98 will enter the processing space 84 through the transfer port, and perform the exchange operation of sending the processed substrate%. [Details of the above-mentioned constituent parts] (1) Here, the configuration of the gas injection nozzle part 93 will be described in detail. FIG. 18 is a longitudinal sectional view showing an enlarged configuration of the gas injection nozzle portion 93. FIG. FIG. B is a cross-sectional view showing the structure of the gas injection nozzle section 93 in an enlarged manner. Fig. 20 is an enlarged front view showing the configuration of the gas injection nozzle portion 93. As shown in FIG. 18 to FIG. 20, the gas injection nozzle portion is located at the center of the front surface, and has a supply pipe 90 that can communicate with the above-mentioned long-range plasma portion 27 above the communication hole 92, and a plurality of injection ports are installed. It is called ~ the nozzle plate 93bi ~ 93b3 arranged in a row in the horizontal direction. The spray ports 9% to 93an are, for example, small holes with a diameter of 1 mm, and are provided at intervals of 10 faces. In addition, in this embodiment, although the ejection ports% to 931 including small holes are provided, it is not limited to this. For example, a configuration may be adopted in which a small slit is used as the ejection port. The nozzle plate 931931 ^ is locked to the nozzle portion of the gas injection nozzle. Therefore, the gas sprayed from the cutouts 93ai ~ 93an will flow forward from the wall surface of the gas injection nozzle portion 93. When the injection ports 93a 丨 ~ 93an are installed in the tube of the tubular nozzle, the gas sprayed by the injection ports 93ai ~ 93an will return to the nozzle.

O:\87\87879.DOC -22- 200421433 管路之後方,而在製程空間84產生氣體滯留,引發被處理 基板W周邊之氣體流不安定之問題。 但於本實施例中,因射喷孔93ai〜93an為形成於氣體噴射 噴鳥部93之壁面之構成,故不會產生如此之氣體返·回到噴 嘴後方之現象,可保持於安定被處理基板W周邊氣體流之 層流狀態。藉此,可均一地形成被處理基板w上之成膜。 另外,在各噴嘴板931^〜93133相對之内壁,形成有具有使 氣體滯留之機能之凹部93ci〜93C3。因該凹部93q〜93以係被 设置於喷射口 93ai〜93an之上流,故可平均自各喷射口 1 9 3 an所喷射之氣體之流速。藉此,能平均於製程空間 84全區域之流速。 此外,各凹部93Cl〜93c3可連通貫穿氣體喷射噴嘴部93之 供給孔93dl〜93d3。又,中央之氣體供給孔93d2不與連通孔 92父又而形成於錯開之位置,折彎成彎曲形狀。 並且,於中央之氣體供給孔934,藉由第1質量控制器97a 而被控制其流量之氣體經由氣體供給管路992而被供應。 又,於被配置於氣體供給孔93d2左右之氣體供給孔93dl, 93d3藉由第2質置控制器97b而被控制其流量之氣體經由 氣體供給管路99!、9%而被供應。 广另外’第1質量控制器97a與第2質量控制器97b,係經由 氣體in &路994、995與氣體供給部34連接,並將來自氣體 U 34所#給之氣體流量控制於預先所設定之流量。 少第1質置控制裔97a與第2質量控制器97b所供給之氣體, ’系由氣體(、給官路99^993到達氣體供給孔93山〜93七,而O: \ 87 \ 87879.DOC -22- 200421433 Behind the pipeline, gas retention occurs in the process space 84, causing the problem of unstable gas flow around the substrate W being processed. However, in this embodiment, since the injection nozzle holes 93ai to 93an are formed on the wall surface of the gas injection bird injection section 93, such a phenomenon that the gas returns to and returns to the rear of the nozzle does not occur, and it can be kept stable and processed. The laminar state of the gas flow around the substrate W. Thereby, the film formation on the to-be-processed substrate w can be uniformly formed. In addition, recessed portions 93ci to 93C3 having a function of retaining gas are formed on the inner wall of each of the nozzle plates 931 to 93133. Since the recesses 93q to 93 are provided above the injection ports 93ai to 93an, the flow velocity of the gas injected from each injection port 193 an can be averaged. As a result, the flow velocity over the entire area of the process space 84 can be averaged. In addition, each of the recesses 93Cl to 93c3 can communicate with the supply holes 93dl to 93d3 penetrating through the gas injection nozzle section 93. In addition, the central gas supply hole 93d2 is not formed at a different position from the communication hole 92, and is bent into a curved shape. The gas supply hole 934 in the center is supplied with a gas whose flow rate is controlled by the first mass controller 97a through a gas supply line 992. In addition, the gas supply holes 93d1 and 93d3 disposed around the gas supply holes 93d2 and 93d3 are supplied with the gas whose flow rate is controlled by the second mass controller 97b through the gas supply lines 99! And 9%. In addition, the first quality controller 97a and the second quality controller 97b are connected to the gas supply unit 34 via gas in & circuits 994 and 995, and control the gas flow rate from the gas U 34 to a predetermined location. Set flow. The gas supplied by the first mass control source 97a and the second mass controller 97b is ′ caused by the gas (, to Guanguan Road 99 ^ 993 reaching the gas supply hole 93 ~ 93, and

O:\87\87879.DOC -23- 200421433 充填於各凹部93Cl〜93c:3後,再由喷射口 93ai〜93an喷向製程 空間84。 製程空間84内之氣體,為了可由延伸於處理容器22之前 部22a之橫向寬幅方向之各喷嘴板9扑广93匕之射噴孔 932^93^向製程空間84之全區域噴射,在製程空間料之全 區域以特定流速(層流)流向處理容器22之後部2孔側。 此外於處理谷器22之後部22b側,由於延伸於後部22b 之橫向寬幅方向之長方形排1口74呈現開口,古丈製程空間 84内之氣體變成流向後方,照特定流速(層旬朝排氣路徑w 排氣。 另外,於本實施例中,因可控制2個系統之流量,故例如 亦可以第1夤里控制器97a與第2質量控制器9几控制不同之 流量。 藉此’設定使供給於製程空間84内之氣體流量(流速)不 同,亦可使製程空間84内之氣體濃度分佈變化。此外,亦 mi質量控制器97a與第2質量控制器97b供給不同種類 之氣體,例如亦可以第1質量控制器97a進行氮氣體之流量 控制’而以第2質量控制器97b進行氧氣體之流量控制。 使用之孔體例如可為含氧氣體、含氮氣體及稀有氣體等。 (2)在此,洋細說明關於加熱部之構成。 圖係擴大顯不加熱部24構成之縱剖面圖。圖Μ係擴大 顯示加熱部24之仰視圖。 如圖21及圖22所示,加熱部24係於紹合金製之底座11〇裝 載石英鐘罩112 ’經由凸緣14〇固定於處理容器22之底部O: \ 87 \ 87879.DOC -23- 200421433 is filled into each of the recesses 93Cl ~ 93c: 3, and then sprayed into the process space 84 from the ejection ports 93ai ~ 93an. The gas in the process space 84 is sprayed in the entire area of the process space 84 so that the nozzle plates 9 extending in the widthwise direction of the front portion 22a of the processing container 22 can be blown into the entire area of the process space 84. The entire area of the space material flows at a specific flow rate (laminar flow) toward the two-hole side of the rear portion of the processing container 22. In addition, on the side of the rear portion 22b of the processing trough 22, the opening 74 of the rectangular row 1 extending in the widthwise direction of the rear portion 22b is opened, and the gas in the Guzhang process space 84 flows backward, according to a specific flow rate The air path w exhausts. In addition, in this embodiment, since the flow rates of the two systems can be controlled, for example, the first flow controller 97a and the second quality controller 9 can control different flow rates. By setting the flow rate (flow rate) of the gas supplied to the process space 84 to be different, the gas concentration distribution in the process space 84 can also be changed. In addition, the mi mass controller 97a and the second mass controller 97b supply different types of gases. For example, the first mass controller 97a may perform flow control of a nitrogen gas, and the second mass controller 97b may perform flow control of an oxygen gas. The pore body used may be, for example, an oxygen-containing gas, a nitrogen-containing gas, or a rare gas. (2) Here, the details of the structure of the heating section are illustrated. The figure is a longitudinal sectional view showing the structure of the heating section 24 in an enlarged manner. Figure M is an enlarged bottom view of the heating section 24. As shown in FIGS. 21 and 22, heating The part 24 is attached to a base 11 made of Sau alloy. The quartz bell cover 112 ′ is fixed to the bottom of the processing container 22 through a flange 14.

O:\87\87879.DOC -24 - 200421433 22c。並且,於石英鐘罩112之内部空間ii3,收容有Sic加 熱器114與熱反射構件116。因此,SiC加熱器114與熱反射 構件116,與處理容器22之製程空間84隔離,不與製程空間 84之氣體接觸,而為不會產生污染之構成。 S i C基板δ又置台11 8係被載置於與S i C加熱器114相對之石 英鐘罩112上,並可藉由高溫計119來測定溫度。該高溫計 119係藉由隨著Sic基板設置台118被加熱而產生之熱電效 果來測定SiC基板設置台us之溫度者,而於控制電路中, 由藉由高溫計119所檢測之溫度信號來推測被處理基板w 之溫度’再根據該推測溫度控制SiC加熱器114之發熱量。 另外’石英鐘罩112之内部空間113,如後述於處理容器 22之製程空間84減壓時,減壓系統作動並同時減壓以使與 製程空間84之壓力差變小。因此,石英鐘罩i 12不必考慮減 壓步驟時之壓力差而加大殼厚(例如3〇mm左右),熱容量小 即可,也因此可提高加熱時之反應性。 底座110形成為圓盤狀,於中央具有穿插有保持構件12〇 之軸120d之中央孔142,而於内部則設置有在圓周方向延伸 而形成之冷卻水用之第丨水路144。因底座11〇為鋁合金製, 其熱膨脹率雖大,但可藉由在第1水路144流動冷卻水來冷 卻。 另外’凸緣140為組合介於底座11〇與處理容器22之底部 22c間之第1凸緣146,與嵌合於第1凸緣146之内周之第2凸 緣148之構成。於第丨凸緣146之内周面,係設置有在圓周方 向延伸而形成之冷卻水用之第2水路15()。O: \ 87 \ 87879.DOC -24-200421433 22c. A Sic heater 114 and a heat reflecting member 116 are housed in the inner space ii3 of the quartz bell cover 112. Therefore, the SiC heater 114 and the heat reflecting member 116 are isolated from the process space 84 of the processing container 22, and are not in contact with the gas in the process space 84, and have a structure that does not cause pollution. The S i C substrate δ is set on the stage 11 8 and placed on the stone bell cover 112 opposite to the Si C heater 114, and the temperature can be measured by the pyrometer 119. The pyrometer 119 measures the temperature of the SiC substrate setting table us by the thermoelectric effect generated as the Sic substrate setting table 118 is heated, and in the control circuit, it uses the temperature signal detected by the pyrometer 119 to The estimated temperature 'of the substrate w to be processed' is then used to control the amount of heat generated by the SiC heater 114 based on the estimated temperature. In addition, when the internal space 113 of the 'quartz bell cover 112' is decompressed in the process space 84 of the processing container 22 as described later, the decompression system operates and decompresses simultaneously to reduce the pressure difference with the process space 84. Therefore, it is not necessary to increase the thickness of the case (for example, about 30 mm) in consideration of the pressure difference during the depressurization step, and the heat capacity of the quartz bell cover i 12 can be small, thereby improving the reactivity during heating. The base 110 is formed in a disc shape, and has a central hole 142 in the center through which a shaft 120d of the holding member 120 is inserted, and an inner water passage 144 for cooling water extending in the circumferential direction is provided in the center. The base 11 is made of aluminum alloy, and although its thermal expansion coefficient is large, it can be cooled by flowing cooling water through the first water passage 144. The flange 140 is a combination of a first flange 146 interposed between the base 11 and the bottom 22c of the processing container 22, and a second flange 148 fitted to the inner periphery of the first flange 146. On the inner peripheral surface of the first flange 146, a second water path 15 () for cooling water formed by extending in the circumferential direction is provided.

O:\87\87879.DOC -25- 200421433 上冷卻水供給部46所供給之冷卻水,係藉由在上述水路 144與150流動,冷卻由SiC加熱器J14發熱所加熱之底座i 1〇 與凸緣140,並抑制底座110與凸緣14〇之熱膨脹。 另外’於底座110下面設置有:連通有使冷卻水流入於水 路144之第1流入管路152之第1流入口 154,與連通有排出通 過水路144之冷卻水之流出管路156之第1流出口 158。此 外’於底座110下面之外周附近,在圓周方向設置有複數個 (例如8〜12處左右)用於穿插鎖緊於第i凸緣146之螺栓16〇之 安裝孔162。 另外’於底座110下面之半徑方向上之中間位置附近設置 有:包含測定SiC加熱器114之溫度用之熱電偶之溫度感應 器164,與供給電源至siC加熱器114之電源纜線連接用端子 166a〜166f。又,在SiC加熱器114形成有3個區域,而電源 纜線連接用端子166a〜166f則分別設置有供給電源至各區 域之+側端子、一側端子。 另外,於凸緣140下面設置有:連通有使冷卻水流入於水 路150之第2流入管路168之第2流入口 170,與連通有排出通 過水路150之冷卻水之流出管路172之第2流出口 174。 圖23係擴大顯示第2流入口 170,及第2流出口 174之安裝 構造之縱剖面圖。圖24係擴大顯示凸緣140之安裝構造之縱 剖面圖。 如圖23所示,於第1凸緣146係設置有可連通第2流入口 170之L字形之連通孔146a。該連通孔146a之邊緣部則被連 通至水路150。又,第2流出口 174亦以與上述第2流入口 17〇 O:\87\87879.DOC -26- 200421433 相同之構成被連通至水路150。 由於水路150係在凸緣140之内部延伸形成於圓周方向, 故藉由冷卻凸緣140,亦間接地冷卻在第1凸緣146之階狀部 146b與底座110間所挾持之石英鐘罩n2之突出部112a之溫 度。藉此,石英鐘罩112之突出部U2a可在半徑方向抑制熱 膨脹。 # 如圖23及圖24所示,於石英鐘罩u 2之突出部112a下面, , 在圓周方向於特定間隔設置有複數個位置決定孔丨78。該位 置决疋孔17 8係肷合被螺入於底座11 q上面之栓17 6之孔,但 熱膨脹率大之底座11〇,在半徑方向熱膨脹時為不增加突出 部112a之負荷,故形成為較栓176之外徑更大之大口徑。 即,僅能容許栓176與位置決定孔178之間隙部份,對石英 鐘罩112之突出部i12a之底座11〇之熱膨脹。 另外,因石英鐘罩112之突出部U2a,對第i凸緣146之階 狀部146b設置有半徑方向之間隙,故因此點之故亦僅能容 許間隙之份之底座110之熱膨脹。 石英鐘罩112之犬出部112&下面,係.藉由被安裝於底座 · 11〇上面之岔封構件(〇環)18〇而密封,石英鐘罩之突出 , 部112a上面,則藉由被安裝於第1凸緣146之密封構件(〇環)、 182而密封。 此外,第1凸緣146與第2凸緣148之上面,係藉由被安裝 於處理容器22之底部22c之密封構件(〇環)184, 186所密 封而第2凸緣148之下面,則是藉由被安裝於底座11〇上面 之也、封構件(〇環)188所密封。O: \ 87 \ 87879.DOC -25- 200421433 The cooling water supplied by the cooling water supply unit 46 flows through the water channels 144 and 150 to cool the base i 1〇 heated by the heat generated by the SiC heater J14 and The flange 140 suppresses thermal expansion of the base 110 and the flange 140. In addition, below the base 110, a first inflow port 154 that communicates with a first inflow pipe 152 through which cooling water flows into the water passage 144, and a first inflow pipe 156 that communicates with cooling water that passes through the water passage 144 are provided. Outlet 158. In addition, a plurality of mounting holes 162 (for example, about 8 to 12 locations) are provided in the circumferential direction near the outer periphery of the lower surface of the base 110 for inserting and locking the bolt 160 of the i-th flange 146. In addition, a temperature sensor 164 including a thermocouple for measuring the temperature of the SiC heater 114 is provided near a middle position in a radial direction below the base 110, and a terminal for connecting a power cable to a power supply to the siC heater 114 is provided. 166a ~ 166f. In addition, three areas are formed in the SiC heater 114, and the power supply cable connection terminals 166a to 166f are respectively provided with a + side terminal and a side terminal for supplying power to each area. In addition, a second inflow port 170 is provided below the flange 140 to communicate with a second inflow pipe 168 through which cooling water flows into the waterway 150, and a second inflow pipe 172 is connected to an outflow pipe 172 through which cooling water is discharged through the waterway 150. 2flow outlet 174. Fig. 23 is a longitudinal sectional view showing the mounting structure of the second inflow port 170 and the second outflow port 174 in an enlarged manner. Fig. 24 is a longitudinal sectional view showing the mounting structure of the flange 140 in an enlarged manner. As shown in FIG. 23, the first flange 146 is provided with an L-shaped communication hole 146a that can communicate with the second inlet 170. An edge portion of the communication hole 146a is connected to the water path 150. In addition, the second outflow port 174 is also connected to the water path 150 with the same structure as the second inflow port 170O: \ 87 \ 87879.DOC -26- 200421433. Since the water path 150 extends in the circumferential direction inside the flange 140, the cooling flange 140 also indirectly cools the quartz bell cover n2 held between the stepped portion 146b of the first flange 146 and the base 110. The temperature of the protruding portion 112a. Thereby, the projection U2a of the quartz bell cover 112 can suppress thermal expansion in the radial direction. # As shown in FIGS. 23 and 24, a plurality of position determination holes 78 are provided below the protruding portion 112a of the quartz bell cover u 2 at a specific interval in the circumferential direction. At this position, the hole 17 8 is a hole that is screwed into the bolt 17 6 on the base 11 q, but the base 11 with a large thermal expansion coefficient does not increase the load of the protruding portion 112a during thermal expansion in the radial direction, so it is formed. It has a larger diameter than the outer diameter of the bolt 176. That is, only the gap between the plug 176 and the position determining hole 178 can be allowed to thermally expand to the base 11 of the protruding portion i12a of the quartz bell cover 112. In addition, since the protruding portion U2a of the quartz bell cover 112 has a gap in the radial direction to the stepped portion 146b of the i-th flange 146, it can only allow the thermal expansion of the base 110 as a gap. The lower part of the dog bell 112 of the quartz bell cover 112 is sealed by a fork seal member (〇ring) 18o which is mounted on the upper surface of the base. The protrusion of the quartz bell cover and the upper part of the part 112a is mounted by being mounted. Sealed to the sealing members (o-rings) and 182 of the first flange 146. The upper surfaces of the first flange 146 and the second flange 148 are sealed by a sealing member (o-ring) 184, 186 attached to the bottom 22c of the processing container 22, and the lower surfaces of the second flange 148 are sealed. It is sealed by a sealing member (0 ring) 188 mounted on the base 11.

O:\87\87879.DOC -27- 如此,由於在底座110與凸緣140之間及凸緣140與處理容 ^之底邛22(:之間成為雙重密封構造,無論其中何者的密 封構件有破h時亦可由其他密封構件來密封住,故更能提 回處理谷器22與加熱部24間密封構造之信賴性。 例如石英麵罩112破裂時或突出部112a產生裂痕時,可 由被配置於較突出部丨12a更外側之密封構件丨8〇,確保石英 鐘罩112内部之氣密性,並阻止處理容器22内之氣體流出至 外部。 或者,即使是接近加熱部24之密封構件180, 182產生劣化 ¥ ’亦可藉由安裝於較加熱部24更為遠遠之位置處之外側 密封構件186,188,維持處理容器22與底座110間之密封性 能而,故亦能防止因長年變化之氣體漏洩。 如圖21所示,SiC加熱器114於石英鐘罩112之内部空間 113中’係被載置於熱反射構件116之上面,且藉由立在底 座110上面之複數個夾鉗機構19〇,而被保持於特定高度。 該夹鉗機構190係具有:抵接於熱反射構件116下面之外 筒190a,貫通外筒i9〇a並抵接於SiC加熱器114上面之軸 190b,及對著軸i90b擠壓外筒190a之螺旋彈簧192。 並且,由於夾鉗機構19〇之構成係以螺旋彈簧192之彈簧 力夾住SiC加熱器114與熱反射構件116,故例如即使在搬運 時有所振動,SiC加熱器114與熱反射構件116亦能保持不會 接觸到石英鐘罩112。另外,因上述螺旋彈箐192之彈簧力 為經常保持作用著,故亦可防止因熱膨脹而引起之螺絲鬆 弛,SiC加熱器Π4與熱反射構件116可被保持於不會鬆動之 O:\87\87879.DOC -28- 200421433 安定狀態。 另外,各夾鉗機構190係構成為可對底座11〇調整sic加熱 器H4與熱反射構件116之高度位置於任意位置,藉由調整 複數個夾钳機構190之高度位置,能保持於SiC加熱器114與 熱反射構件116之水平。 此外’於石英鐘罩112之内部空間113中安裝有:sic加熱 器U4之各端子,與用於電連接被穿插於底座丨1〇之電源繞 線連接用端子166a〜166f之連接構件194a〜194f(但,於圖21 圖示有連接構件194a、194c)。 圖25係擴大顯示夾钳機構190上端部之安裝構造之縱剖 面圖。 如圖25所示,夾鉗機構190係鎖緊被栓入於穿插於熱反射 構件116之穿插孔116a與SiC加熱器114之穿插孔1146之轴 190b上端之螺母193,經由墊片195於軸方向擠壓[字形墊片 197, 199並挾持SiC加熱器114。O: \ 87 \ 87879.DOC -27- In this way, since the seal between the base 110 and the flange 140 and between the flange 140 and the bottom of the processing container 邛 22 (: becomes a double seal structure, no matter which of them is the seal member When broken, it can be sealed by other sealing members, so the reliability of the sealing structure between the trough device 22 and the heating portion 24 can be brought back. For example, when the quartz mask 112 is broken or the protruding portion 112a is cracked, it can be sealed by A sealing member 8o disposed outside the protruding portion 12a ensures the airtightness inside the quartz bell cover 112 and prevents the gas in the processing container 22 from flowing to the outside. Or, even the sealing member 180 close to the heating portion 24 , 182 Deterioration ¥ 'It can also be installed at a position farther away from the heating section 24 than the outer sealing members 186, 188 to maintain the sealing performance between the processing container 22 and the base 110, so it can also prevent long-term The changing gas leaks. As shown in FIG. 21, the SiC heater 114 is placed on the heat reflecting member 116 in the inner space 113 of the quartz bell cover 112, and is clamped by a plurality of clamps standing on the base 110. Institution 19〇 while insured The clamp mechanism 190 has an outer cylinder 190a that abuts on the lower surface of the heat reflecting member 116, a shaft 190b that penetrates the outer cylinder i90 and abuts on the upper surface of the SiC heater 114, and faces the shaft i90b. The coil spring 192 of the outer cylinder 190a is squeezed. Further, since the structure of the clamp mechanism 19 is configured to sandwich the SiC heater 114 and the heat reflection member 116 with the spring force of the coil spring 192, for example, even when it is transported, The SiC heater 114 and the heat reflecting member 116 can also keep from contacting the quartz bell cover 112. In addition, because the spring force of the above-mentioned spiral spring 192 is constantly maintained, it can also prevent the screw from loosening due to thermal expansion. SiC The heater Π4 and the heat reflecting member 116 can be kept in a stable state of O: \ 87 \ 87879.DOC -28- 200421433. In addition, each clamp mechanism 190 is configured to adjust the sic heater to the base 11 The height position of H4 and the heat reflection member 116 is at any position. By adjusting the height positions of the plurality of clamp mechanisms 190, it can be maintained at the level of the SiC heater 114 and the heat reflection member 116. In addition, 'in the inner space of the quartz bell cover 112 11 Installed in 3: the terminals of the sic heater U4 and the connection members 194a to 194f for electrically connecting the power winding connection terminals 166a to 166f inserted through the base 丨 10 (however, as shown in FIG. 21 Connecting members 194a, 194c). FIG. 25 is a longitudinal sectional view showing the mounting structure of the upper end portion of the clamp mechanism 190 in an enlarged manner. As shown in FIG. 25, the clamp mechanism 190 is locked and inserted into the heat reflection member 116. The nut 193 at the upper end of the shaft 190b of the insertion hole 116a and the insertion hole 1146 of the SiC heater 114 is pressed through the gasket 195 in the axial direction [shaped gaskets 197, 199 and holds the SiC heater 114.

SiC加熱器114,於穿插孔iue插入有L字形之墊片197 199之圓筒部197a,199a,而於圓筒部197a,199a内則穿插有 夾鉗機構190之軸190b。並且,L字形墊片197, 199之突出部 197b,199b係抵接於SiC加熱器114之上面、下面。 夾鉗機構190之軸190b,係藉由上述螺旋彈簧192之彈簧 力而被施予向下方之力,且夾鉗機構19〇之外筒19〇a藉由上 述螺旋彈簧丨92之彈簧力而被施予向上方之力。如此i使螺 旋彈簧192之彈簧力產生做為夹鉗力之作用,故熱反射構件 116與SiC加熱器114安定地被保持著,可防止因搬運時之振 O:\87\87879.DOC -29- 200421433 動所引起之破損。In the SiC heater 114, cylindrical portions 197a and 199a of L-shaped gaskets 197 and 199 are inserted into the insertion holes iue, and shafts 190b of the clamp mechanism 190 are inserted into the cylindrical portions 197a and 199a. The protruding portions 197b and 199b of the L-shaped spacers 197 and 199 are in contact with the upper and lower surfaces of the SiC heater 114. The shaft 190b of the clamp mechanism 190 is applied with a downward force by the spring force of the coil spring 192, and the clamp mechanism 19o and the outer cylinder 19oa are caused by the spring force of the coil spring 92. Forced upward. In this way, the spring force of the coil spring 192 is generated as a clamping force, so the heat reflecting member 116 and the SiC heater 114 are stably held, which can prevent vibration due to transportation O: \ 87 \ 87879.DOC- 29- 200421433 damage caused by movement.

SiC加熱器114之穿插孔1 i4e,係較L字形之墊片i97a, 197b之圓筒部197(;,197(1之口徑大,故設有間隙。因此,在 因SiC加熱器114之發熱而產生之熱膨脹,使穿插孔丨丨讣與 軸190b相對地變位時,穿插孔1146可在抵接[字形墊片197, 199之突出部19713, 199b之狀態下於水平方向錯位,防止隨 著熱膨脹之應力的發生。 (3)在此,針對SiC加熱器114說明。 如圖26所示,SiC加熱器U4係由:中心部形成為圓形狀 之第1發熱部114a,及包圍住第1發熱部114a之外周而形成 為圓弧狀之第2、第3發熱部114b,114c所構成。又,於SiC 加熱器114中心係設置有:被穿插保持構件12〇之軸12〇(1之 穿插孔114d。 發熱部114a〜114c係並列地連接至發熱控制電路196,再 由溫度調整器198控制於所設定之任意溫度。於發熱控制電 路196中,係藉由控制由電源2〇〇供給至發熱部U4a〜114c之 電壓’來控制自SiC加熱器114所放射之發熱量。 另外’若因發熱部114a〜114c之容量不同則會增大電源 2〇〇之負擔,故於本實施例中,可設定使各發熱部114a〜114c 之容量(2 KW)成為相同之電阻。 發熱控制電路196係可選擇:控制方法I,同時使發熱部 114a〜114c通電並發熱;控制方法π,配合被處理基板界之 溫度分佈狀況,使中心之第1發熱部丨14a,或外側之第2、 第3發熱部114b,114c之其中一者發熱;控制方法m ,配合 O:\87\87879.DOC -30- 200421433 被處理基板W之溫度變化,同時使發熱部114a〜114c發熱, 及使第1發熱部114a或第2、第3發熱部114b,114c之任一發 熱。 被處理基板W在藉由上述保持構件120保持之狀態,邊旋 轉邊由各發熱部114a〜114c發熱而被加熱之際,會因外周側 與中心部份之溫度差而使周邊部份朝上方彎翹。但,於本 實施例中,由於SiC加熱器114係經由熱傳導率佳之SiC基板 設置台118來加熱被處理基板W,故被處理基板W全體是以 來自SiC加熱器114之熱來加熱,可將被處理基板w之周邊 部份與中心部份之溫度差抑制到最小,以防止被處理基板 W的彎輕。 (4)在此,詳細說明有關112石英鐘罩之構成。 圖27A係顯示石英鐘罩112之構造之俯視圖。圖27B係顯 示石英鐘罩112之構造之縱剖面圖。圖28A為從上方所見石 英鐘罩112之構造之立體圖;圖28B為從下方所見石英鐘罩 112之構造之立體圖。 如圖27A、圖27B與圖28A、圖28B所示,石英鐘罩112由 透明石英所形成,其係具有:於前述突出部112a上方形成 之圓筒部112b、覆蓋圓筒部112b上方之頂板ii2c、延伸於 較頂板112c中央之下方之中空部112d、及為補強被橫向架 没於突出部112 a所形成之開口之梁部112 e。 由於突出部112a與頂板112c承受荷重,故形成為較圓筒 部112b為厚。又,石英鐘罩112因延伸於縱方向之中空部 U2d與延伸於橫方向之梁部1126在内部交叉,故可提高上 O:\87\87879.DOC -31 - 200421433 下方向與半徑方向之強度。 另外’於梁部112e之中間位置可結合中空部1 i2d之下端 部份,而中空部112d内之穿插孔112f亦貫通梁部112e。於該 穿插孔112f可穿插保持構件12〇之軸12〇d。 並且’於石英鐘罩112之内部空間U3插入有前述Sic加熱 器114與熱反射構件116。又,雖sic加熱器114與熱反射構 件116形成為圓盤狀,但為可分割成圓弧狀之構成,可避開 梁部112e並於被插入内部空間113後組裝。 此外,於石英鐘罩112之頂板112c有3處(120度間隔)突 _ 出’其係為支持SiC基板設置台U8之輪轂U2g〜112丨。因 此,由輪轂112g〜112i所支持之SiC基板設置台U8,係被載 置成稍微自頂板l12c突出之狀態。因此,即使處理容器22 之内部壓力有變化,或因產生溫度變化之SiC基板設置台 118變動至下方時,亦可防止接觸到頂板ll2c。 另卜石夬鐘罩112之内部壓力,係如後述為進行藉由減 壓系統進行排氣流量的控制,使與處理容器22之製程空間 84之壓力差成為5〇 丁⑽以下,故可將石英鐘罩ιΐ2之厚度製 作成比較薄。因此,由於可將頂板112c之厚度做成薄約6〜10 ^ mm左右,故使得石英鐘罩112之熱容量變小並可藉由提高 · 加”、、時之熱傳導效率提昇反應性。另外,本實施例之石英 鐘罩Π2,係設計成具有可承受1〇〇 T〇rr壓力之強度。 圖29係顯示減壓系統之排氣系統構成之系統圖。 如圖29所示,處理容器22之製程空間料,係如前所述, 閥48a打開後,經由被連通至排氣口”之排氣路徑32,藉由The insertion hole 1 i4e of the SiC heater 114 is larger than the cylindrical portions 197 (;, 197 (1) of the L-shaped gaskets i97a, 197b, so there is a gap. Therefore, the SiC heater 114 has a gap. When the insertion hole 丨 丨 讣 is displaced relative to the shaft 190b due to the thermal expansion caused by the heat, the insertion hole 1146 can be displaced in the horizontal direction in the state of abutting the [protrusions of the letter-shaped gasket 197, 199 19713, 199b]. (3) Here, the SiC heater 114 will be described. As shown in FIG. 26, the SiC heater U4 is composed of a first heat generating portion 114a having a circular center portion, and The arc-shaped second and third heating portions 114b and 114c are formed to surround the outer periphery of the first heating portion 114a. A shaft 12 is provided at the center of the SiC heater 114, and the holding member 12 is inserted therethrough. 〇 (1 through the socket 114d. The heating sections 114a to 114c are connected in parallel to the heating control circuit 196, and then controlled by the temperature adjuster 198 to any set temperature. In the heating control circuit 196, it is controlled by control The voltage ′ supplied from the power source 200 to the heating units U4a to 114c is controlled by the SiC heater 114. In addition, if the capacity of the heating sections 114a to 114c is different, the load on the power supply will be increased. Therefore, in this embodiment, the capacity (2 KW) of each heating section 114a to 114c can be set. The heating resistance control circuit 196 can be selected: control method I, and the heating parts 114a to 114c are energized and generate heat; control method π, according to the temperature distribution of the substrate boundary to be processed, makes the first heating part in the center 丨14a, or one of the second and third heat generating parts 114b, 114c on the outer side; the control method m, in accordance with O: \ 87 \ 87879.DOC -30- 200421433, changes the temperature of the substrate W to be processed, and simultaneously causes the heat generating part 114a to 114c generate heat, and heat is generated by either the first heat generating portion 114a or the second, third heat generating portions 114b, and 114c. The substrate W to be processed is held by the holding member 120 while being rotated by each heat generating portion. When 114a ~ 114c is heated and heated, the peripheral part will warp upward due to the temperature difference between the outer peripheral side and the central part. However, in this embodiment, since the SiC heater 114 is made of SiC with good thermal conductivity Substrate setting table 118 to be heated The substrate W is processed, so the entire processed substrate W is heated by the heat from the SiC heater 114, and the temperature difference between the peripheral portion and the central portion of the processed substrate w can be minimized to prevent the substrate W from being processed. (4) Here, the structure of the 112 quartz bell cover will be described in detail. FIG. 27A is a plan view showing the structure of the quartz bell cover 112. FIG. 27B is a longitudinal sectional view showing the structure of the quartz bell cover 112. Fig. 28A is a perspective view of the structure of the quartz bell jar 112 seen from above; Fig. 28B is a perspective view of the structure of the quartz bell jar 112 seen from below. As shown in FIG. 27A, FIG. 27B, and FIG. 28A and FIG. 28B, the quartz bell cover 112 is formed of transparent quartz, and has a cylindrical portion 112b formed above the protruding portion 112a and a top plate ii2c covering the cylindrical portion 112b. , A hollow portion 112d extending below the center of the top plate 112c, and a beam portion 112e which is reinforced by an opening formed by a lateral frame and protruding from the projecting portion 112a. Since the protruding portion 112a and the top plate 112c receive a load, they are formed thicker than the cylindrical portion 112b. In addition, since the quartz bell cover 112 extends in the longitudinal hollow portion U2d and the beam portion 1126 in the horizontal direction intersects internally, it can increase the strength of the upper O: \ 87 \ 87879.DOC -31-200421433 in the downward and radial directions. . In addition, at the middle position of the beam portion 112e, the lower end portion of the hollow portion 1 i2d may be combined, and the insertion hole 112f in the hollow portion 112d also penetrates the beam portion 112e. A shaft 12Od of the holding member 120 can be inserted into the insertion hole 112f. Further, the Sic heater 114 and the heat reflecting member 116 described above are inserted into the inner space U3 of the quartz bell cover 112. In addition, although the sic heater 114 and the heat reflecting member 116 are formed in a disc shape, they can be divided into arcs, and can be assembled after being inserted into the inner space 113 without the beam portion 112e. In addition, the top plate 112c of the quartz bell cover 112 is protruded at three places (120-degree interval). It is a hub U2g to 112 of the SiC substrate setting table U8. Therefore, the SiC substrate mounting table U8 supported by the hubs 112g to 112i is placed so as to protrude slightly from the top plate l12c. Therefore, even if the internal pressure of the processing container 22 is changed, or the SiC substrate setting table 118 is changed downward due to a temperature change, it is possible to prevent contact with the top plate 112c. In addition, the internal pressure of the stone bell bell 112 is controlled by the decompression system to control the exhaust flow rate, as described later, so that the pressure difference from the process space 84 of the processing container 22 becomes 50 Dn or less, so the quartz bell bell can be used. The thickness of ιΐ2 is made relatively thin. Therefore, since the thickness of the top plate 112c can be made as thin as about 6 to 10 ^ mm, the thermal capacity of the quartz bell cover 112 can be reduced and the reactivity can be improved by increasing the heat conduction efficiency. In addition, the present The quartz bell cover Π2 of the embodiment is designed to have a strength capable of withstanding 100 Torr. FIG. 29 is a system diagram showing the structure of the exhaust system of the pressure reduction system. As shown in FIG. 29, the process of processing the container 22 The space material is as described above. After the valve 48a is opened, it passes through the exhaust path 32 which is connected to the exhaust port.

O:\87\87879.DOC -32- 200421433 渦輪分子幫浦50之吸引力而減壓。此外,被連接至渦輪分 子幫浦50之排氣口之真空管路51下游,連通至吸引被排氣 氣體之幫浦(MBP) 201。 石英鐘罩112之内部空間1丨3係經由排氣管路2〇2而被連 接至分流管路5 1 a ’而由旋轉驅動部28之外殼122所劃分成 之内部空間124,則經由排氣管路2〇4被連接至分流管路 51a 〇 - 排氣管路202係設置有:測定内部空間1丨3壓力之壓力計 205、 及於石英鐘罩112之内部空間113減壓之際會打開之閥修 206。 又,於分流管路51a,如前述係設置有閥48b,且設有 分流閥48b之分歧管路208。而於該分歧管路2〇8設有:在減 壓步驟之初期階段所打開之閥21〇、及為能較閥48b更集中 流量之可變隔膜211。 另外,於渦輪分子幫浦50之排氣側設有:開關用之閥 2 12、測定排氣側之壓力之壓力計214。並且,於渦輪軸清 除用之N2線連通至渦輪分子幫浦5〇之渦輪管路216上設置鲁 有··逆止閥218、隔膜220及閥222。 . 另外,上述閥206、210、212、222係包含電磁閥,依據 來自控制電路之控制信號而打開。 ^ 在如上述所構成之減壓系統中,於進行處理容器22、石 英鐘罩112與旋轉驅動部28之減壓步驟時,並非一口氣地減 壓,而是階段地減壓,使其漸漸地接近真空而減壓。 首先,以打開被設置於石英鐘罩112之排氣管路202之閥 206,使石英鐘罩112之内部空間113與製程空間84之間經由 O:\87\87879.DOC -33- 200421433 排氣路徑3 2成為連通狀態,進行壓力之均一化。藉此,使 得在減壓步驟之開始階段之石英鐘罩112之内部空間113與 製程空間84間之壓力差變小。 其次,使被設置於上述分歧管路208之閥210打開,由可 變隔膜211進行被集中之小流量之減壓。之後,使被設於分 流管路5 1 a之閥48b打開,並階段性地增大排氣流量。 另外,比較由壓力計205所測定之石英鐘罩112之壓力, 與由感應為早元85之壓力計85a〜85c所測定之製程空間84 之壓力,當兩壓力差為50 Torr以下時,即令閥48b打開。藉 此’於減壓步驟,緩和作用於石英鐘罩1丨2之内外之壓力 差’並使不需要之應力不會作用於石英鐘罩112以進行減壓 步驟。 並且’於經過特定時間後使閥4 8 a打開,並增大渴輪分子 幫浦50之吸引力所造成之排氣流量,減壓處理容器22、石 央4里罩112與旋轉驅動部28之内部直到變為真空為止。 (5)在此,針對上述保持構件12〇之構成做說明。 圖30A係顯示保持構件12〇構成之俯視圖;圖3〇b係顯示 保持構件120構成之側面圖。 如圖30A、圖30B所示,保持構件12〇係由支持被處理基 板W之臂部120a〜120c,及可結合臂部12〇a〜120c之軸i2〇d 所構成。臂部120a〜120c為防止於製程空間84之污染,且為 了不遮蔽住來自SiC基板設置台118之熱,而由透明石英所 形成,以軸120d之上端為中心軸而以12〇度間隔在水平方向 成放射狀延伸。 O:\87\87879.DOC -34- 200421433 此外’於臂部12〇a〜120c之長方向之中間位置,突出有抵 接於被處理基板W下面之輪轂120e〜120g。因此,被處理基 板界係由其抵接輪轂120e〜120g之3點所支持。 如此’由於保持構件丨2〇為以點接觸支持被處理基板…之 構成’故對SiC基板設置台11 8可僅以些許之距離保持被處 理基板W於離開之位置。又,Sic基板設置台118與被處理 基板W之離開距離,例如為丨〜2〇 mm,較佳為3〜1〇 mm左右。 即’被處理基板W成為以浮在SiC基板設置台118上方之 狀態旋轉’比起直接被載置於SiC基板設置台丨18者,來自 SiC基板设置台11 8之熱可更均一地放射,不易產生周邊部 份與中心部份之溫度差,亦可防止因溫度差而產生之被處 理基板W之彎翹。 因被處理基板W係被保持在自SiC基板設置台118離開之 位置’故即使因溫度差而產生彎翹,亦不會接觸到sic基板 設置台118 ’而隨著定常時之溫度均一化,可恢復至原來之 水平狀態。 另外’保持構件120之軸l2〇d係以不透明石英形成為棒 狀,穿插於上述SiC基板設置台us與石英鐘罩112之穿插孔 112f並延伸於下方。如此,雖保持構件12〇為在製程空間84 内保持被處理基板W者,但因係由石英所形成,故亦無須 擔心由金屬製品所造成之污染。 (6)在此,洋細說明有關上述旋轉驅動部28之構成。 圖3 1係顯不被配置於加熱部24下方之旋轉驅動部28之構 成之縱剖面圖。圖32則擴大顯示旋轉驅動部28之縱剖面圖。 O:\87\87879.DOC -35- 200421433 如圖31與圖32所示,在加熱部24之底座ιι〇下方鎖緊有用 於支持旋轉驅動部28之托架23〇。於該托架23〇係設有:旋 轉位置檢測機構232,及托架冷卻機構234。 此外於托架230下方插入有穿插固定了保持構件12〇之 軸120d之陶瓷軸126,可藉由螺拴24〇來固定保持了可轉動_ 地支持陶瓷軸126之陶瓷軸承236,237之固定側之外殼122。 於外殼122内,因旋轉部份係由陶瓷軸126與陶瓷軸承236, 237所構成,故可防止金屬之污染。 外殼122係具有:穿插有螺栓24〇之凸緣242,及延伸形成馨 於凸緣238下方之有底筒狀之間隔壁244。於間隔壁244之外 周面,設置有可連通前述減壓系統之排氣管路2〇4之排氣孔 246,而外殼122之内部空間124之氣體,係於前述減壓系統 之減壓步驟中,被排氣而減壓。因此,可防止製程空間84 内之氣體沿著保持構件120之轴12〇d流出於外部。 此外’於内部空間124收容有磁鐵聯結器13〇之從動側磁 鐵248。該從動側磁鐵248為防止污染,係由在陶瓷軸外鲁 周所嵌合之磁鐵罩250所覆蓋住,並安裝成不會與内部空間 · 124之氣體接觸。 ' 磁鐵罩250係由鋁合金形成為環狀之護罩,在内部形成有 , 收容用之環狀空間。收容成内部不會搖晃之狀態。另外, 磁鐵罩250之接合部份係以電子射束溶接成無間隙結合,係 不會如錫焊般地流出銀而造成污染地加工。 此外,於外殼122之外周,嵌合地設置有形成為筒狀之氛 圍側旋轉部252,經由軸承254, 255可旋轉地支持著。並且, O:\87\87879.DOC -36- 200421433 於氛圍側旋轉部252之内周,安裝有磁鐵聯結器130之驅動 側磁鐵2 5 6。 氛圍側旋轉部252下端部252a係經由傳達構件257可結合 馬達128之驅動軸128a。因此,馬達128之旋轉驅動能量, 係經由被設在氛圍側旋轉部252之驅動側磁鐵256,與被設 在外殼122内部之從動側磁鐵248間之磁力,被傳達至陶瓷 轴126並傳達到保持構件120與被處理基板W。 另外,於氛圍側旋轉部252之外側,安裝有檢測氛圍側旋 轉部252旋轉之旋轉檢測單元258。該旋轉檢測單元258係由 被安裝在氛圍側旋轉部252下端部外周之圓盤狀之狹缝板 260, 261,與光學性地檢測狹縫板260, 261之旋轉量之光斷 續器262, 263所構成。 光斷續器262, 263係由軸承架264被固定在固定側之外殼 122。並且,於旋轉檢測單元258中,因由一對的光斷續器 262, 263可同時檢測出配合旋轉速度之脈衝,故藉由比較兩 脈衝能提高旋轉檢測精密度。 圖33A係顯示托架冷卻機構234構成之橫剖面圖,圖33B 則顯示托架冷卻機構234構成之側面圖。 如圖33A、圖33B所示,托架冷卻機構234在托架230之内 部,形成有於圓周方向延伸之冷卻水用之水路230a。並且, 於水路230a之一端連通有冷卻水供給孔230b,而在水路 23 0a之另一端則連通有冷卻水供給排出孔230c。 自冷卻水供給部46所供給之冷卻水,由冷卻水供給孔 230b起通過水路230a後,由於是從冷卻水供給排出孔230c O:\87\87879.DOC -37- 200421433 排出,故可冷卻托架230全體。 圖34係顯示旋轉位置檢測機構232構成之橫剖面圖。 如圖34所示,於托架230之一側面安裝有發光元件266, 而在托架230之另一側面則安裝有接受來自發光元件266之 光之受光元件268。 另外,於托架230中央,在上下方向貫穿可穿插保持構件 120之軸120d之中央孔230d,而在該中央孔230d處設有交叉 般在橫方向貫穿之貫通孔230e,230f。 發光元件266係被插入在一方之貫通孔230e之邊緣部,而 受光元件268則被插入於另一方之貫通孔230f之邊緣部。於 貫通孔230e與230f間由於穿插有軸120d,故可由受光元件 268之輸出變化檢測出軸120d之旋轉位置。 (7)在此,詳細說明有關旋轉位置檢測機構232之構成 與作用。 圖35A係顯示旋轉位置檢測機構232之非檢測狀態之圖, 而圖35B則顯示旋轉位置檢測機構232之檢測狀態之圖。 如圖35A所示,保持構件120之軸120d於外周被施以切線 方向之倒角加工。在發光元件266與受光元件268之中間位 置轉動時,該倒角加工部120i會與自發光元件266所發出之 光平行。 此時,來自發光元件266之光,通過倒角加工部120i之旁 邊而被照射到受光元件268。藉此,受光元件268之輸出信 號S會變成ON並傳達至旋轉位置判定電路270。 如圖35B所示,當保持構件120之軸120d轉動,倒角加工 O:\87\87879.DOC -38- 200421433 部咖之位置自中間位置偏離時,纟自發光元件加的光會 、轴所遮蔽,使得對旋轉位置判定電路謂之輸出信號 s變成OFF。 圖36A係顯示旋轉位置檢測機構加之受光元件⑽之輸 出信號s之波形圖,而圖36B則是從旋轉位置判定電路謂 所輸出之脈衝信號p之波形圖。 如圖36A所示,受光元件268因軸12〇d之轉動位置,使得 λ 土光元件266的光之爻光量(輸出信號S)成放射線狀變 化。於旋轉位置判定電路27G中,設定對該輸出信號s之間 值η,當輪出信號s成為閥值H以上時則輸出脈衝p。 、該脈衝P係做為檢測保持構件12〇轉動位置之檢測信號而 被輸出。即係如圖10所示,旋轉位置判定電路27〇判定保持 構件120之臂部κούρος不會干涉到昇降臂132之抵接銷 138a〜l38c,且在未干涉到搬送自動機%之機械臂之位置, 而輸出該檢測信號(脈衝P)。 (8)在此,根據由上述旋轉位置判定電路27〇所輸出之 檢測信號(脈衝P),針對進行控制電路之旋轉位置控制處理 作說明。 圖37是為了說明控制電路所進行之旋轉位置控制處理之 流程圖。 如圖37所示,控制電路於S11中,當有指示被處理基板w 轉動之控制信號時,則前進至S 12使馬達128啟動。接著, 前進至S13,確認受光元件268之信號是否為ON。當在S13 受光元件268之信號為ON時,則前進至s 14,自檢測信號(脈 O:\87\87879.DOC -39- 200421433 衝p)之周期彳算出保持構件ί2〇與被處理基板w之轉動數。 接著,前進至S15,確認保持構件12〇與被處理基板w之 轉動數η是否為預先所設定之目標轉動數仙。於si5,當保 持構件m與被處理基板w之轉動^為達到目標轉動數仙 時,則返回上述S13,再度確認馬達128之轉動數是否有上 昇0 另外,於上述S15中,當n=na時,由於保持構件12〇與被 處理基板w之轉動數11達到目標轉動數仙,故前進至, 確認是否有馬達停止之控制信號。於S17,當無馬達停止之 控制信號時則返回上述313,而當有馬達停止之控制信號時 則前進至㈣,令馬達停止。緊接著,在⑽確認受光元件 268之信號是否為0N,不斷的重複直到受光元件之信號 變成ON為止。 ° ~ 如此,保持構件12〇之臂部120a〜12〇c不會干涉到昇降臂 132之抵接銷138a〜138c,且可使其停止在未干涉到搬送自 動機98之機械臂之位置。 另外,於上述旋轉位置控制處O: \ 87 \ 87879.DOC -32- 200421433 The attraction of turbo molecular pump 50 reduces pressure. In addition, a vacuum line 51 connected to the exhaust port of the turbo molecular pump 50 is connected to a pump (MBP) 201 that sucks exhaust gas. The internal space 1 丨 3 of the quartz bell cover 112 is an internal space 124 which is connected to the branch line 5 1 a ′ through the exhaust line 202 and is divided by the housing 122 of the rotary driving section 28. The pipeline 204 is connected to the branch pipeline 51a. The exhaust pipeline 202 is provided with a pressure gauge 205 for measuring the pressure in the internal space 1 丨 3, and a pressure gauge 205 which is opened when the internal space 113 of the quartz bell cover 112 is decompressed. Valve repair 206. The branch line 51a is provided with the branch line 208 having the valve 48b and the branch valve 48b as described above. The branch pipe 20 is provided with a valve 21 and a variable diaphragm 211 which can be opened in the initial stage of the pressure reducing step, and can be more concentrated than the valve 48b. In addition, the exhaust side of the turbo molecular pump 50 is provided with a valve 2 12 for opening and closing, and a pressure gauge 214 for measuring the pressure on the exhaust side. In addition, a non-return check valve 218, a diaphragm 220, and a valve 222 are provided on a turbine pipeline 216 that connects the N2 line for turbine shaft cleaning to the turbo molecular pump 50. In addition, the above-mentioned valves 206, 210, 212, and 222 include solenoid valves and are opened in accordance with a control signal from a control circuit. ^ In the decompression system constructed as described above, when the decompression steps of the processing container 22, the quartz bell cover 112, and the rotary driving unit 28 are performed, the pressure is not depressurized at one go, but gradually decompressed to gradually reduce the pressure. Close to vacuum and decompress. First, by opening the valve 206 of the exhaust pipe 202 provided in the quartz bell cover 112, the internal space 113 of the quartz bell cover 112 and the process space 84 pass through the O: \ 87 \ 87879.DOC -33- 200421433 exhaust path 3 2 is in a connected state, and pressure is uniformized. Thereby, the pressure difference between the internal space 113 and the process space 84 of the quartz bell cover 112 at the beginning of the decompression step is made small. Next, the valve 210 provided in the branch line 208 is opened, and the variable diaphragm 211 is used to perform pressure reduction at a small flow rate which is concentrated. Thereafter, the valve 48b provided in the branch line 5 1 a is opened, and the exhaust flow rate is increased stepwise. In addition, compare the pressure of the quartz bell cover 112 measured by the pressure gauge 205 with the pressure of the process space 84 measured by the pressure gauges 85a ~ 85c which are sensed as the early element 85. When the pressure difference is 50 Torr or less, the valve 48b opens. By this, in the decompression step, the pressure difference acting on the inside and outside of the quartz bell cover 1 丨 2 is relaxed, and unnecessary stress is not applied to the quartz bell cover 112 to perform the decompression step. And after a certain time elapses, the valve 4 8 a is opened, and the exhaust gas flow rate caused by the attraction of the thirsty molecular pump 50 is increased. The pressure reduction processing container 22, the inner cover 112 of the stone center 4, and the rotation driving portion 28 Until it becomes a vacuum. (5) Here, the structure of the said holding member 120 is demonstrated. Fig. 30A is a plan view showing the structure of the holding member 120, and Fig. 30b is a side view showing the structure of the holding member 120. As shown in FIGS. 30A and 30B, the holding member 12o is composed of arm portions 120a to 120c that support the substrate W to be processed, and an axis i20d that can be combined with the arm portions 120a to 120c. The arm portions 120a to 120c are formed of transparent quartz to prevent contamination in the process space 84 and not to shield the heat from the SiC substrate setting table 118. The upper end of the axis 120d is used as the central axis at 120 ° intervals. It extends radially in the horizontal direction. O: \ 87 \ 87879.DOC -34- 200421433 In addition, at the middle position in the longitudinal direction of the arm portions 120a to 120c, the hubs 120e to 120g abutting on the substrate W to be processed protrude. Therefore, the boundary of the substrate to be treated is supported by the three points that abut the hub 120e ~ 120g. As described above, since the holding member 20 is configured to support the substrate to be processed with point contact ..., the SiC substrate setting table 118 can hold the substrate to be processed at a distant position only by a small distance. The distance between the Sic substrate mounting table 118 and the substrate to be processed W is, for example, about 20 mm, preferably about 3 to 10 mm. That is, 'the processed substrate W is rotated while floating above the SiC substrate mounting table 118', and the heat from the SiC substrate mounting table 118 can be more uniformly radiated than those directly placed on the SiC substrate mounting table 118. It is not easy to generate a temperature difference between the peripheral portion and the center portion, and it is also possible to prevent warping of the substrate W to be processed due to the temperature difference. Since the substrate W to be processed is held at a position separated from the SiC substrate mounting table 118, even if warping occurs due to a temperature difference, it will not contact the sic substrate mounting table 118 ', and the temperature becomes uniform as it is at regular times. Can return to the original level. In addition, the axis 120d of the 'holding member 120 is formed into a rod shape from opaque quartz, and is inserted through the insertion hole 112f of the SiC substrate setting table us and the quartz bell cover 112 and extends below. In this way, although the holding member 120 holds the substrate W to be processed in the process space 84, since it is formed of quartz, there is no need to worry about contamination caused by metal products. (6) Here, the structure of the rotation drive unit 28 will be described in detail. Fig. 31 is a longitudinal sectional view showing the structure of the rotation driving portion 28 which is not disposed below the heating portion 24. FIG. 32 is an enlarged longitudinal sectional view of the rotation driving section 28. O: \ 87 \ 87879.DOC -35- 200421433 As shown in Fig. 31 and Fig. 32, the bracket 23, which is used to support the rotary drive section 28, is locked below the base ιo of the heating section 24. The bracket 23 is provided with a rotation position detecting mechanism 232 and a bracket cooling mechanism 234. In addition, a ceramic shaft 126 is inserted below the bracket 230 and fixed to the shaft 120d of the holding member 12o. The ceramic bearing 236, 236,237 which can rotate and support the ceramic shaft 126 can be fixed and fixed by a screw 24o.壳 122。 The housing 122. In the housing 122, since the rotating part is composed of the ceramic shaft 126 and the ceramic bearings 236 and 237, the metal can be prevented from being contaminated. The housing 122 has a flange 242 with a bolt 24 inserted therethrough, and a bottomed cylindrical partition wall 244 extending below the flange 238. On the outer peripheral surface of the partition wall 244, there are provided exhaust holes 246 that can communicate with the exhaust pipe 208 of the aforementioned decompression system, and the gas in the internal space 124 of the housing 122 is the decompression step of the aforementioned decompression system. In the middle, it is exhausted and decompressed. Therefore, the gas in the process space 84 can be prevented from flowing to the outside along the axis 120d of the holding member 120. Further, a driven side magnet 248 of the magnet coupling 13 is housed in the internal space 124. The driven-side magnet 248 is covered with a magnet cover 250 fitted to the outer periphery of the ceramic shaft to prevent contamination, and is installed so as not to contact the gas in the internal space 124. 'The magnet cover 250 is a ring-shaped cover made of aluminum alloy, and a ring-shaped space for storage is formed inside. Contained in a state where it will not shake. In addition, the joint portion of the magnet cover 250 is welded with an electron beam to form a gap-free connection, and it does not flow out of silver like soldering to cause contamination. In addition, an outer peripheral side rotating portion 252 formed in a cylindrical shape is fitted on the outer periphery of the housing 122 and is rotatably supported by bearings 254 and 255. In addition, O: \ 87 \ 87879.DOC -36- 200421433 is mounted on the inner periphery of the atmosphere-side rotating portion 252, and the driving-side magnet 2 5 6 of the magnet coupler 130 is attached. The lower end portion 252a of the atmosphere-side rotating portion 252 is connected to the drive shaft 128a of the motor 128 via the transmission member 257. Therefore, the rotational driving energy of the motor 128 is transmitted to the ceramic shaft 126 through the magnetic force between the driving-side magnet 256 provided in the atmosphere-side rotating portion 252 and the driven-side magnet 248 provided inside the housing 122. To the holding member 120 and the substrate W to be processed. Further, a rotation detection unit 258 for detecting the rotation of the atmosphere-side rotating portion 252 is mounted outside the atmosphere-side rotating portion 252. The rotation detection unit 258 is a disc-shaped slit plate 260, 261 mounted on the outer periphery of the lower end portion of the atmosphere-side rotation portion 252, and a photo interrupter 262 that optically detects the rotation amount of the slit plate 260, 261. , 263. The photointerrupters 262 and 263 are fixed to the housing 122 on the fixed side by a bearing frame 264. In addition, in the rotation detection unit 258, since a pair of optical interrupters 262, 263 can simultaneously detect pulses matching the rotation speed, the accuracy of rotation detection can be improved by comparing the two pulses. FIG. 33A is a cross-sectional view showing the structure of the bracket cooling mechanism 234, and FIG. 33B is a side view showing the structure of the bracket cooling mechanism 234. As shown in FIGS. 33A and 33B, the bracket cooling mechanism 234 has a water path 230a for cooling water extending in the circumferential direction inside the bracket 230. A cooling water supply hole 230b is connected to one end of the water path 230a, and a cooling water supply and discharge hole 230c is connected to the other end of the water path 230a. The cooling water supplied from the cooling water supply unit 46 passes through the water passage 230a from the cooling water supply hole 230b and is discharged from the cooling water supply discharge hole 230c O: \ 87 \ 87879.DOC -37- 200421433, so it can be cooled. The entire bracket 230. FIG. 34 is a cross-sectional view showing the configuration of the rotation position detecting mechanism 232. As shown in FIG. 34, a light emitting element 266 is mounted on one side of the bracket 230, and a light receiving element 268 that receives light from the light emitting element 266 is mounted on the other side of the bracket 230. In the center of the bracket 230, a central hole 230d through which the shaft 120d of the holding member 120 can be inserted is penetrated in the up-down direction, and through-holes 230e, 230f are formed in the central hole 230d to cross in the transverse direction. The light emitting element 266 is inserted into the edge portion of the one through hole 230e, and the light receiving element 268 is inserted into the edge portion of the other through hole 230f. Since the shaft 120d is interposed between the through holes 230e and 230f, the rotation position of the shaft 120d can be detected by the output change of the light receiving element 268. (7) Here, the configuration and function of the rotational position detection mechanism 232 will be described in detail. FIG. 35A is a diagram showing a non-detection state of the rotation position detection mechanism 232, and FIG. 35B is a diagram showing a detection state of the rotation position detection mechanism 232. As shown in FIG. 35A, the shaft 120d of the holding member 120 is chamfered in the tangential direction on the outer periphery. When the intermediate position between the light-emitting element 266 and the light-receiving element 268 is rotated, the chamfered portion 120i is parallel to the light emitted from the light-emitting element 266. At this time, the light from the light-emitting element 266 is irradiated to the light-receiving element 268 through the side of the chamfered portion 120i. Thereby, the output signal S of the light receiving element 268 is turned ON and transmitted to the rotation position determination circuit 270. As shown in FIG. 35B, when the axis 120d of the holding member 120 rotates and the chamfering process O: \ 87 \ 87879.DOC -38- 200421433 is shifted from the middle position, the light added by the light-emitting element and the axis The masking causes the output signal s of the rotation position determination circuit to be turned OFF. Fig. 36A is a waveform diagram showing the output signal s of the rotation position detection mechanism plus the light receiving element ,, and Fig. 36B is a waveform diagram of the pulse signal p output from the rotation position determination circuit. As shown in FIG. 36A, the rotation position of the light receiving element 268 causes the light intensity (output signal S) of the light of the λ earth light element 266 to change in a radial pattern. The rotation position determination circuit 27G sets a value η between the output signal s, and outputs a pulse p when the wheel-out signal s becomes the threshold value H or more. The pulse P is output as a detection signal for detecting the rotation position of the holding member 120. That is, as shown in FIG. 10, the rotation position determining circuit 27 judges that the arm κούρος of the holding member 120 does not interfere with the contact pins 138a to 138c of the lifting arm 132, and does not interfere with the mechanical arm of the transport robot Position, and this detection signal (pulse P) is output. (8) Here, based on the detection signal (pulse P) output from the rotation position determination circuit 270, the rotation position control processing of the control circuit will be described. Fig. 37 is a flowchart for explaining a rotational position control process performed by the control circuit. As shown in FIG. 37, in S11, when there is a control signal indicating the rotation of the substrate w to be processed, it proceeds to S12 to start the motor 128. Next, the process proceeds to S13 to check whether the signal of the light receiving element 268 is ON. When the signal of the light-receiving element 268 in S13 is ON, it proceeds to s14, and the period of the self-detection signal (pulse O: \ 87 \ 87879.DOC -39- 200421433 punch p) calculates the holding member 2 and the substrate to be processed. The number of rotations of w. Next, the process proceeds to S15, and it is confirmed whether or not the number of rotations η of the holding member 12 and the substrate w is a target number of rotations set in advance. At si5, when the rotation of the holding member m and the substrate w to be processed reaches the target number of rotations, return to the above S13, and confirm again whether the number of rotations of the motor 128 has increased by 0. In addition, in the above S15, when n = na At this time, since the rotation number 11 of the holding member 12 and the substrate to be processed w reaches the target rotation number of cents, it proceeds to and confirms whether there is a control signal for the motor stop. At S17, when there is no control signal for motor stop, it returns to 313 above, and when there is a control signal for motor stop, it advances to ㈣ to stop the motor. Next, it is checked whether the signal of the light receiving element 268 is 0N, and iteratively repeats until the signal of the light receiving element becomes ON. ° ~ In this way, the arm portions 120a to 120c of the holding member 120 will not interfere with the abutment pins 138a to 138c of the lifting arm 132, and can be stopped at a position that does not interfere with the robot arm of the conveyance motor 98. In addition, at the rotation position control

哪诉自兄明了使用E 來自受光元件268之輸出信號之周期求出轉動數之方法二 情形,但例如亦可積算由前述光斷續器262,263所輸出之4 號求出轉動數。 12 2之側面所形成 (9)在此,詳細說明有關於處理容器 之窗口 75, 76之構成。 圖38為從上方所見窗口 75、 3 9係擴大顯示窗口 75之橫剖面 76之安裝處之橫剖面圖。圖 圖。圖40係擴大顯示窗口% O:\87\87879.DOC -40- 200421433 之橫剖面圖。 如圖38、圖39所示,第1窗口 75係可供給氣體於處理容器 122内部所形成之製程空間84,由於被減壓成真空,故成氣 密性更高之構成。 窗口 75為具有透明石英272,與遮蔽紫外線UV之玻璃274 之二重構造。透明石英272係於抵接於窗口安裝部276之狀 態下,第1窗框278由小螺釘277栓住而固定於窗口安裝部 276。於窗口安裝部276之外面,安裝有氣密地密封住與透 明石英272之間之密封構件(0環)280。此外,於第1窗框278 之外面,於使IJV玻璃274抵接之狀態下,由小螺釘284拴住 固定第2窗框282。 如此,窗口 75藉由UV玻璃274可遮蔽由紫外光源(UV燈) 86, 87所照射之紫外線,防止其洩漏至製程空間84之外部, 並藉由密封構件280之密封效果,防止被供給至製程空間84 之氣體流出於外部。 另外,貫穿處理容器22側面之開口 286,係以向著處理容 器22之中央,亦即向著被保持於保持構件120之被處理基板 W之中心,斜斜地貫穿。因此,窗口 75係被設置在從處理 容器22之側面中心偏離之位置,但形成為於橫向可看得較 寛廣之橢圓形狀,而可由外部確認被處理基板W之狀態。 另外,第2窗口 76係與上述窗口 75為相同之構成,具有透 明石英292,與遮蔽紫外線UV玻璃294之二重構造。透明石 英292係以抵接於窗口安裝部296之狀態,將第1窗框298以 小螺釘297鎖住並固定於窗口安裝部296。於窗口安裝部296 O:\87\87879.DOC -41 - 株 文敘有氣密地密封住與透明石英292之間之密封構 )〇〇此外,於第1窗框298之外面,以使UV玻璃294 氏接之狀^用小螺釘304鎖住並固定第2窗框逝。 固76藉由UV玻璃294遮蔽由紫外光源(UV燈)86, 7=照射之紫外線防止其$漏至製程空間料之外部,並藉 由在封構件3G0之密封效果,防止被供給至製程空間%之氣 體流出於外部。 、另:,於本實施例中,雖係以處理容器22之側面配置一 75’ 76之構成做為例子作說明,但不限於此,亦可 π置3個以上的窗σ ’或者當然亦可設置在側面以外之 所。 (10)在此,說明關於構成石英墊圈100之各盒體1〇2, 1〇4, 106, 108 〇 ’ ’ =圖9與圖! 0所示,石英塾圈i 〇 〇為組合下部盒體(〇 2、側 面盒體104、上部盒體1〇6與1〇8圓筒狀盒體之構成,其各自 係由不透明石英所形成’以保護銘合金製之處理容器22不 文氣體與紫外線傷害,並防止因處理容器22之金屬污染為 目的而設置。 圖41A係顯示下部盒體1〇2構成之俯視圖,圖41B係顯示 下部盒體102構成之側面圖。 如圖41A、圖41B所示,下部盒體102其輪廓形狀係形成 為對應處理容器22之内壁形狀之板狀,而於其中央則形成 有相對於SiC基板設置台11 8與被處理基板w之圓形開口 310。該圓形開口 310形成為可插入圓筒狀盒體1〇8之尺寸, O:\87\87879.DOC -42- 200421433 於内周以120度間隔,設置有用於插入保持構件12〇之臂部 120a〜120c之前端部之凹部31〇a〜31〇c。 另外,凹部310a〜310c之位置,係保持構件12〇之臂部 120a〜120c不會干涉到昇降臂132之抵接銷n8a〜138c,且不 干涉到搬送自動機98之機械臂之位置。 另外,於下部盒體102設置有相對於形成在處理容器22 底。卩之排氣口 74之長方形開口 3 12。此外,下部盒體1 〇2在 下面於非對稱位置設置有決定位置用之突起314&,3141)。 另外,於上述圓形開口 310之内周,形成有嵌合後述圓筒 狀盒體108之突起之凹部3i〇d。此外,於下部盒體ι〇2之邊 緣部,設置有後合於側面盒體1 〇4之階狀部3 15。Which case can be used to determine the second method of using the period of the output signal from the light receiving element 268 to obtain the number of rotations, but for example, the number of rotations output by the above-mentioned optical interrupters 262, 263 may be used to calculate the number of rotations. Formation of the side of 12 2 (9) Here, the structure of the windows 75 and 76 of the processing container will be described in detail. FIG. 38 is a cross-sectional view of the installation place of the cross section 76 of the enlarged display window 75 when the windows 75 and 39 are seen from above. Figure Figure. Figure 40 is a cross-sectional view of the enlarged display window% O: \ 87 \ 87879.DOC -40- 200421433. As shown in Fig. 38 and Fig. 39, the first window 75 is a process space 84 formed by supplying gas to the inside of the processing container 122. Since it is reduced in pressure to a vacuum, it has a higher airtight structure. The window 75 is a double structure having a transparent quartz 272 and a glass 274 that blocks ultraviolet rays. The transparent quartz 272 is in contact with the window mounting portion 276, and the first window frame 278 is fixed to the window mounting portion 276 by a small screw 277. A sealing member (0 ring) 280 which hermetically seals between the window mounting portion 276 and the transparent quartz 272 is attached. In addition, the second window frame 282 is fastened with a small screw 284 on the outer surface of the first window frame 278 in a state in which the IJV glass 274 abuts. In this way, the window 75 can shield the ultraviolet light irradiated by the ultraviolet light source (UV lamp) 86, 87 by the UV glass 274, prevent it from leaking to the outside of the process space 84, and prevent the supply to The gas in the process space 84 flows out. In addition, the opening 286 penetrating the side surface of the processing container 22 penetrates diagonally toward the center of the processing container 22, that is, toward the center of the substrate W to be held on the holding member 120. Therefore, the window 75 is provided at a position deviated from the center of the side surface of the processing container 22, but is formed in an elliptical shape which can be seen in a wide direction in the lateral direction, and the state of the substrate W to be processed can be confirmed from the outside. The second window 76 has the same structure as the above-mentioned window 75, and has a double structure of transparent quartz 292 and UV-shielding UV glass 294. The transparent stone 292 is in a state of being in contact with the window mounting portion 296, and the first window frame 298 is locked and fixed to the window mounting portion 296 with a small screw 297. At the window mounting section 296 O: \ 87 \ 87879.DOC -41-Zhu Wenxu has a sealing structure that hermetically seals with transparent quartz 292) 〇〇 Also, outside the first window frame 298, The UV glass 294 is connected ^ The second window frame is locked and fixed with a small screw 304. Gu 76 uses UV glass 294 to shield the ultraviolet light source (UV lamp) 86, 7 = the ultraviolet rays irradiated to prevent it from leaking to the outside of the process space, and by the sealing effect on the sealing member 3G0, it is prevented from being supplied to the process space % Of the gas flows out. In addition, in this embodiment, although a configuration in which a 75 ′ 76 is disposed on the side of the processing container 22 is taken as an example for description, it is not limited to this, and three or more windows σ ′ may be provided, or of course Can be placed outside the side. (10) Here, the respective cases 10, 102, 106, and 108 constituting the quartz washer 100 will be described. FIG. 9 and FIG. As shown in FIG. 0, the quartz ring i 〇〇 is a combination of a lower box body (〇2, a side box body 104, an upper box body 106 and 108 cylinder body), each of which is formed of opaque quartz 'It is provided for the purpose of protecting the processing container 22 made of alloy gas from ultraviolet gas and ultraviolet rays, and preventing the metal contamination of the processing container 22. FIG. 41A is a plan view showing the structure of the lower case 102, and FIG. 41B is a view showing the lower part. A side view of the box body 102. As shown in Figs. 41A and 41B, the lower box body 102 is formed in a plate shape corresponding to the shape of the inner wall of the processing container 22, and is provided at the center with respect to the SiC substrate. The circular opening 310 of the stage 11 8 and the substrate to be processed w. The circular opening 310 is formed in a size that can be inserted into the cylindrical box body 10, O: \ 87 \ 87879.DOC -42- 200421433 At 120-degree intervals, recesses 31aa to 31c for inserting the ends of the arms 120a to 120c of the holding member 120 are provided. In addition, the positions of the recesses 310a to 310c are the arms 120a to 120c of the holding member 120. 120c does not interfere with the contact pins n8a ~ 138c of the lifting arm 132, and does not It interferes with the position of the robotic arm of the transfer robot 98. In addition, the lower case 102 is provided with a rectangular opening 3 12 formed on the bottom of the processing container 22. The exhaust port 74 of the ridge is provided. In addition, the lower case 1 〇2 A position determining protrusion 314 & 3141 is provided below the asymmetric position. Further, on the inner periphery of the circular opening 310, a recessed portion 3iod to which a protrusion of a cylindrical case 108 described later is fitted is formed. In addition, a step portion 3 15 is provided on the edge portion of the lower case ι02, which is then closed to the side case 104.

圖42A係顯示側面盒體1〇4構成之俯視圖,圖42B為側面 盒體104之前視圖,圖42C為側面盒體1〇4之後視圖,圖42D 為側面盒體104之左側視圖,圖42E為側面盒體} 04之右側視 圖。 如圖42A〜圖42E所示,側面盒體104其外形狀係形成為對 應處理容器22之内壁形狀,四角落成R字狀之大致四角形之 框形狀.。在内側形成有製程空間84。 另外,側面盒體104於正面i〇4a設置有:與前述氣體喷射 喷嘴部93之複數個的射喷口 93a相對並於橫方向延伸之細 長形之狹縫316,及設置在與被連通至遠距離電漿部27之連 通孔92相對之位置之u字形開口317。又,於本實施例中, 係狹縫316與開口 317為連通之構成,但亦可形成為各自獨 立之開口。 O:\87\87879.DOC -43- 200421433 另外,側面盒體104在背面104b上,於與搬送口 94相對之 位置形成有前述搬送自動機98之機械臂通過之凹部318。 另外,側面盒體104在左側面l〇4c,形成有相對於前述感 j器單元85之圓形孔319,在右側面1〇4d,則形成有相對於 月|J述窗口 75, 76,與感應器單元77之孔320〜322。 圖43A係顯示上部盒體1〇6構成之仰視圖,圖43β則顯示 上部盒體106構成之側面圖。 如圖43A、圖43B所示,上部盒體106其輪廓形狀形成為 對應處理容H 22之㈣形狀之板狀,而於相對紫外線光源 (UV燈)86, 87之位置則形成有長方形開口 324, 325。此外, 於上部盒體106之邊緣部設置有嵌合側面盒體1〇4之階狀 326。 ° 另外,上部盒體106設有對應蓋子構件82之形狀之圓形孔 327〜329,與長方形之四角孔33〇。 圖44Α係顯示圓筒狀盒體1〇8構成之俯視圖,圖44β為圓 筒狀盒體108之侧面縱剖面圖,圖44C則是圓筒狀盒體1⑽ 之側面圖。 如圖44A〜圖桃所*,圓筒狀盒體1〇8形成為如覆蓋住石 英鐘罩U2之外周之筒狀,於上端邊緣部設有被插入昇降臂 132之抵接銷138a〜138c之凹部i〇8a〜1〇8c。此外,圓筒狀各 體H)8於上端部之外周’形成有嵌合下部盒體ι〇2之凹; 310d之配合位置用之突起1〇8d。 (11)在此,說明關於升降桿機構3〇之密封構造。 圖45係擴大顯示升降桿機構3G之縱剖面圖。圖_擴大 O:\87\87879.DOC -44- 200421433 顯示升降桿機構30之密封構造之縱剖面圖。 女Η 45〃、圖46所示,升降桿機構3〇係構成為由驅動部I% 令昇降軸134昇降使被插入室8〇内之昇降臂132昇降之際, 由蛇腹形狀之伸縮管332覆蓋住被插入室8〇之貫通孔8如内 之幵降軸134之外周,防止在室内之污染。 伸縮管332其蛇腹部份為可伸縮之形狀,例如由鎳鉻鐵耐 熱合金或耐蝕鎳合金等所形成。另外,貫通孔8〇a由被穿插 幵降轴134之蓋子構件340所閉塞住。 此外,於藉由螺栓334鎖住昇降轴134之上端之昇降臂132 之連接構件336,係嵌合固定有圓筒形狀之陶瓷蓋338。該 陶兗蓋338為延伸形成於較連接構件336更下方,係被設置 成由覆蓋住伸縮管332之周圍而不在室80内直接露出。 因此’伸縮管332於製程空間84在使昇降臂Π2上昇之際 會延伸至上方,而由陶瓷所形成之圓筒狀蓋338所覆蓋住。 故’伸縮管332藉由可昇降地被插入貫通孔8〇a之圓筒狀蓋 338 ’而不會直接曝晒在製程空間84之氣體與熱中,故可防 止因氣體與熱而造成劣化。 (12)以下’ 17兄明關於使用基板處理裝置2 0 ’進行被處理 基板W表面之紫外光自由基氧化處理,與之後所進行之遠 距離電漿自由基氮化處理。 [紫外光自由基氧化處理] 圖47A係顯示使用圖2之基板處理裝置2〇,進行被處理基 板W之自由基氧化情形之側面圖及俯視圖,圖47b係顯示圖 47A構成之俯視圖。 O:\87\87879.DOC -45- ^UU421433 如圖47A所示,於前述製程空間84中,可由氣體喷射噴嘴 部93供給氧氣體,並於沿著被處理基板歡表面流動後, 經由排氣口 74、渦輪分子幫浦50與幫浦201排氣。藉由使用 渴輪分子幫浦50,前述製程空間84之製程麼力,係被設定 在因,板W之氧自由基之氧化所需之丨〇-3〜丨〇.6 τ〇耽範圍。 之氧自由基之氧化,在石夕基板表面,可安定且再現性 佳地形成1 nm以下之膜厚非常薄之氧化膜,特別是相當於 2〜3原子層之約〇.4llm膜厚之氧化膜。 同時,較理想的係藉由驅動產生172 nm之波長之紫外光 之臬外線光源86, 87,而在如此形成之氧氣流中形成氧自由 基。所形成之氧自由基在延著前述被處理基板界之表面流 動之際,會氧化旋轉之基板表面。藉由因如此之被處理基 如圖47B所示,可知紫外線光源86, 87為延伸於與氧氣流 方向交又之方向之管狀光源,渦輪分子幫浦5〇會經由排氣 口 74排出製程空間84之氣體。另一方面,由前述排氣口% 直接通至幫浦50之圖47B中以點線所示之排氣路徑係藉由 關閉住閥48b而被遮蔽。 圖48係顯示於圖2之基板處理裝置2〇中,藉由圖47人、圖 47B之步驟設定基板溫度於450°C,並一邊使紫外光照射強 度與氧氣流量,或氧分壓作各種變化一邊於矽基板表面形 成石夕氧化膜之情形時,膜厚與氧化時間之關係。但於在圖 48之實驗中,係在自由基氧化之前除去矽基板表面之自然 氧化膜’又有時,於紫外光激發氮自由基中除去殘留於基 板表面之碳,此外,更於Ar氛圍中,藉由進行於約950°C之 O:\87\87879.DOC -46- 200421433 高溫熱處理,平坦化基板表面。另外,作為前述紫外線光 源86, 87係使用波長為172 nm之激分子燈。 參照圖48,系列1之資料,係顯示將紫外光照射強度設定 於紫外光源24B之窗面之基準強度(50 mW/cm2)之5%,製程 壓力設定成665 mPa(5m Torr)、氧氣流量設定成30 SCCM時 之氧化時間與氧化膜厚之關係,而系列2之資料,則顯示將 紫外光強度設定成〇,製程壓力設定成133Pa(l Τοιτ)、氧氣 流量設定成3SLM之情形之氧化時間與氧化膜厚之關係。 又,系列3之資料,係顯示將紫外光強度設定成0,製程壓 ® 力設定成2.66Pa(20m Ton*),氧氣流量設定成150 SCCM之情 形之氧化時間與氧化膜厚之關係,而系列4之資料,則顯示 將紫外光強度設定成100%,即設定成前述基準強度,製程 壓力設定成2.66Pa(20m Torr)、氧氣流量設定成150 SCCM 之情形之氧化時間與氧化膜厚之關係。此外,系列5之資 料,係顯示將紫外光強度設定成基準強度之20%,製程壓 力設定成2.66Pa(20m Torr)、氧氣流量設定成150 SCCM之情 φ 形之氧化時間與氧化膜厚之關係,而系列6之資料,則顯示 將紫外光強度設定成基準強度之20%,製程壓力約為67Pa (0.5 Τοιτ)、氧氣流量為0.5SLM時之氧化時間與氧化膜厚之 關係。此外,系列7之資料,係顯示將紫外光強度設定成基 準強度之20%,製程壓力設定成665Pa (5 Τοιτ)、氧氣流量 設定成2SLM時之氧化時間與氧化膜厚之關係,而系列8之 資料,則顯示將紫外光強度設定成基準強度之5%,製程壓 力為2.66Pa(20m Torr)、氧氣流量為150SCCM時之氧化時間 O:\87\87879.DOC -47- 200421433 與氧化膜厚之關係。 =圖48之實驗中,氧化膜之膜厚係由XPS法所求得,但 、、’有可求取如此低於1 nm非常薄的氧化膜膜厚之統 一的方法。 本I月之發明者,對在圖49所示之所觀察之Si2p執道 進行本底修正與3/2及1/2旋轉狀態之分離修 正,而以圖5G所示所得結果之Si2p3/2XPS光譜為主,依。及 ^^(Z. H. Lu5 et al.3 Appl. Phys5 Lett. 71 (1997), pp.2764) 之教不’使用於式⑴所示之式與係數求出氧化膜之膜厚d。 d= Asina · In [I-/(/? I u^(1) λ = 2. 96 β = 0. 75 但於式⑴中,α為圖55所示之XPS光譜之測出角,於圖 不之例中’被設定成3G、又數i中,IX+為對應氧化膜之光 譜峰值之積分強度(户+i2x+i3x+i4x),係對應圖%中於 102〜l〇4eV之能量區域所能見到之峰值。另一方面,广為 對應100eV附近之能量區域中,對應起因於矽基板之光譜峰 值之積分強度。 再度參照圖48可確認,相對於紫外光照射光度小,因而 幵v成之氧自由基密度小之情形下(系列丨,2, 3, 8),雖最初氧 化膜之氧化膜厚為〇 nm者,但隨著氧化時間氧化膜厚會漸 漸地持續增加者,在將紫外光照射光度設定為基準強度之 20/〇以上之系列4, 5, 6, 7中,如於圖51概略所示,氧化膜成 長於成長開始後會在大致到達〇_4 nm2膜厚之時停滯,而 O:\87\87879.DOC -48 - 200421433 在經過某種程度的停滯時間後,會再急速的開始成長。 圖48或圖51之關係,係意味著於矽基板表面之氧化處 理,可安定地形成0.4 nm左右之膜厚非常薄的氧化膜。又, 如於圖48所見,可知由於如此之停滯時間持續了某種程 度’故所形成之氧化膜具有相同之厚度。即,根據本發明, 能於矽基板上形成厚度約〇·4 nm之相同厚度之氧化膜。 圖52A、圖52B係概略地顯示於該矽基板上形成薄氧化膜 之製程。於該等圖中,須注意已非常地單純化矽(1〇〇)基板 上之構造。 參照圖52A,於矽基板表面每丨個矽原子結合2個氧原子, 而形成有1原子層之氧層。於其代表性之狀態中,基板表面 之矽原子係由基板内部的2個矽原子與基板表面的2個氧原 子所定位,形成副氧化物。 對此,於圖52B之狀態中,矽基板最上層之矽原子係由4 個氧原子戟位,取得安定的Si4+之狀態。可能係由於此一 理由’於圖52A之狀態中快速地進行氧化,變成為圖52β之 狀態中氧化停滯。於圖52B之狀態之氧化膜之厚度為〇4 nm,此係與於圖48所觀察到之停滯狀態之氧化膜厚一致。 於圖50之XPS光譜,於氧化膜厚為〇lnm或〇2nm之情況 下,於l〇l〜1〇4eV之能量範圍中可見之低峰值係對應圖52八 之副氧化物,而在氧化膜厚超過〇3 nm2情形下,由於在 該能量範圍所顯示之峰值係起因於Si4+,故可認為顯示超過 1原子層之氧化膜的形成者。 如此於0.4 nm之膜厚上之氧化骐厚停滯現象,並不限定 O:\87\87879.DOC -49- 於圖47A,圖47B之UV02自由其急儿心 2目由基虱化製程,應為只要可以良 好精細度形成同樣薄的氧化膜 朕 < 虱化膜形成方法,皆可見 到相同之情況。 則會使氧化膜之厚度再度 由圖52B之狀態更加繼續氧化 增大。 圖53係顯示在由使用如此之基板處理裝置別之圖47a、圖 ㈣之紫外光自由基氧化製程所形成之氧化膜上,形成厚度 為〇.4 nm之ZrSi04x膜與電極膜(參照後面所說明之圖 54B),對所得到之積層構造,所求得之熱氧化膜換算膜厚 Teq與漏茂電流Ig之關係"但,圖53之_電流特性係於前 述電極膜㈣基板間’以平帶電壓Vfb為基準,以施加之狀 態測定wb-uv之電壓。為了比較,於圖53亦顯示有熱氧 化膜之m流特性。另外’圖示之換算膜厚係關於組合 氧化膜與ZrSi〇x膜之構造者。 參照圖53可知,省略氧化膜時,亦即於氧化膜膜厚為〇 之情形下,漏洩電流密度超過熱氧化膜之漏洩電流密度, 又熱氧化膜換异膜厚Teq亦變成約1 ·7 nm左右之比較大之 對此’可知若使氧化膜之膜厚由〇 nm增大至〇·4 nm,則 熱氧化膜換异膜厚Teq之值開始減少。於如此之狀態中,氧 化膜會成介於石夕基板與ZrSiOx膜之間,其物理膜厚實際上 應是增大但換算膜厚Teq卻呈現減少,此點在矽基板上直接 形成Zr〇2膜之情形下,意味著如圖54A所示,大規模地產生 Zr向著矽基板中的擴散或是Si向著ZrSiOx膜中的擴散,在矽 O:\87\87879.DOC -50- 200421433 基板與加从膜之間形成有厚界面層。對此,可考慮如圖 遍所示,藉由使厚度G.4nm之氧化膜介在其中,可抑制如 此之界面層的形成’結果減少換算膜厚者。隨之,可知漏 茂電流之值亦隨著氧化膜之厚度減少。但圖54a、圖MB係 顯示出如此所形成之實驗材料之概略的剖面,並且顯示在 石夕基板441上形成有氧化膜442,而於氧化膜442上則形成有 2^丨0;(膜443之構造。 另一方面,當前述氧化膜之膜厚超過〇·4 nm,則熱氧化 膜換算膜厚之值會開始再度增大。於氧化膜之膜厚超過“ nm之範圍,隨著膜厚之增大漏茂電流之值亦會減少,可想 成其換算膜厚的增大係起因於氧化膜之物理膜厚的增大。 如此,在圖48所觀察到之氧化膜成長所停滯之〇·4 ^瓜附 近之膜厚,係對應包含氧化膜與高電介質膜之系之換算膜 厚之最小值,可得知藉由圖52(Β)所示之安定的氧化膜,可 有效地阻止Zr等之金屬元素對矽基板中的擴散,並且即使 氧化膜的厚度更大,其金屬元素之擴散阻止效果亦不會提 高許多。 此外’可知使用0.4 nm厚度之氧化膜時之漏洩電流之 值,係較對應之厚度之熱氧化膜之漏洩電流之值小約2位 數,藉由使用如此構造之絕緣膜於MOS電晶體之閘極絕緣 膜中,可最小化閘極漏洩電流。 另外,於圖48或51所說明之氧化膜成長〇·4 nm之停滯現 象之結果,即使如圖55 A所示於石夕基板441上所形成之氧化 膜442存在著最初之膜厚未變化之凹凸,在氧化膜成長之 O:\87\87879.DOC -51 - ’干、▲膜厚增大係如圖55B所示停滯在〇·4 mn之附近,故藉由 τ滯期間内繼續氧化膜成長,可得到如圖55C所示非常地 平坦、相同膜厚的氧化膜442。 如先刖所說明,對於非常薄之氧化膜,目前尚未有統一 之膜厚測$ 士 、疋万法。因此,圖55C之氧化膜442之膜厚值可能 會因浪丨$ t 、 万法相異而有所不同。但由先前所說明之理由可 ^ 〇 ’在氧化膜成長中發生停滯之厚度為2原子層份之厚 产,故 ' 又 ,可認為較理想之氧化膜442之膜厚約為2原子層份 之厚度。於該較理想之厚度係為於氧化膜442整體確保有2 原子層份之厚度,而有在某部份形成有3原子層份厚度區域 之情形。即’可認為較理想之氧化膜442之厚度實際上是2〜3 原子層之範圍。 [遠距離電漿自由基氮化處理] 圖56係顯示於基板處理裝置2〇所使用之遠距離電漿部27 之構成。 如圖56所示,遠距離電漿部27係於内部形成有氣體循環 通路27a、與此連通之氣體入口 27b、及氣體出口 76c之典型 的包含有由鋁構成之區塊27 A,而在前述區塊27A之一部份 形成有鐵氧體磁心27B。 於前述氣體循環通路27a、氣體入口 27b及氣體出口 27c之 内面,係配設有氟素樹脂加工27d,由捲繞在前述鐵氧體磁 心27B之線圈供給頻率為400 kHz之高頻,而於前述氣體循 環通路27a内形成電漿27C。 隨著電漿27C之激發,於前述氣體循環通路27a中雖形成 O:\87\87879.DOC -52- 200421433 有氮自由基與氮離子’但氮離子會於循環於前述氣體循環 通路27a^際消失,故由前述氣體出口2化主要是釋放出氣 自由基Ν2。此外’於圖56之構成中,係藉由設置接地於前 述氣體出n27e之離子過濾||27e,而除去如氮離子等之帶 電粒子,而於前述製程空間84僅供給有氮自由基。另外,. 即使在未使前述離子過濾器27e接地之情形下,前述離子過 遽器27e之構造亦有作為擴散板作用,可充分地除去如氮離’ 子等之帶電粒子。 圖57係顯示由遠距離電漿部27所形成之離子數與電子能· 量之關係’與微波電敷源之比較。 如圖57所示,在由微波激發電漿之情形下,會促進氮分 子之氮離子化,而形成有量多的氮離子。對此,在由5〇〇 kHz 以下之同頻激發電漿之情形下,會大幅度地減少所形成之 氮離子數。在以微波進行電漿處理時,如圖58所示,則需 要1.33x10〜i^xlC^PaGo·1〜i〇_4T〇rr)的高真空,高頻電 漿處理’係可以13.3〜13.3 kPa (0.1〜1〇〇 Torr)之比較高之壓· 力來進行。 以下之表1,係顯示在由微波激發電漿之情形,與由高頻 激發電漿之情形間,離子化能量變換效率、放電可能壓力 範圍、電漿消耗電力及製程氣體流量的比較。 表142A is a plan view showing the structure of the side box 104, FIG. 42B is a front view of the side box 104, FIG. 42C is a rear view of the side box 104, FIG. 42D is a left side view of the side box 104, and FIG. 42E is Side box} 04 right side view. As shown in FIGS. 42A to 42E, the outer shape of the side case 104 is formed into a substantially rectangular frame shape corresponding to the inner wall shape of the processing container 22, and the four corners are R-shaped. A process space 84 is formed on the inside. In addition, the side box 104 is provided on the front surface 104a with an elongated slit 316 opposite to the plurality of injection nozzles 93a of the gas injection nozzle portion 93 and extending in the horizontal direction, and is provided to be communicated with the remote A U-shaped opening 317 located at a distance from the communication hole 92 of the plasma portion 27. In this embodiment, the slits 316 and the openings 317 are connected to each other, but they may be formed as separate openings. O: \ 87 \ 87879.DOC -43- 200421433 In addition, on the back surface 104b, the side box 104 is formed with a recess 318 through which the robot arm of the transport robot 98 passes, at a position opposite to the transport port 94. In addition, the side box 104 is formed with a circular hole 319 on the left side 104b with respect to the sensor unit 85, and on the right side 104d, a window 75, 76 with respect to the month is formed. Holes 320 ~ 322 with the sensor unit 77. Fig. 43A is a bottom view showing the constitution of the upper case 106, and Fig. 43β is a side view showing the constitution of the upper case 106. As shown in FIG. 43A and FIG. 43B, the outline shape of the upper case 106 is formed into a plate shape corresponding to the shape of the handle H 22, and rectangular openings 324 are formed at positions opposite to ultraviolet light sources (UV lamps) 86, 87 , 325. In addition, a stepped shape 326 of the side box body 104 is fitted on an edge portion of the upper box body 106. ° In addition, the upper case 106 is provided with circular holes 327 to 329 corresponding to the shape of the cover member 82, and rectangular rectangular holes 33. Fig. 44A is a plan view showing the structure of the cylindrical case 108, Fig. 44β is a side longitudinal sectional view of the cylindrical case 108, and Fig. 44C is a side view of the cylindrical case 1⑽. As shown in FIG. 44A to FIG. *, The cylindrical box body 108 is formed in a cylindrical shape such as to cover the outer periphery of the quartz bell cover U2, and the upper end edge portion is provided with contact pins 138a to 138c inserted into the lifting arm 132 The recesses i0aa to 108c. In addition, in the cylindrical body PD8, a recess for fitting the lower case ι02 is formed on the outer periphery of the upper end portion; a protrusion 108d for a fitting position of 310d. (11) Here, the sealing structure of the lift lever mechanism 30 will be described. Fig. 45 is a longitudinal sectional view showing an enlarged lever mechanism 3G in an enlarged manner. Figure_Enlarged O: \ 87 \ 87879.DOC -44- 200421433 A longitudinal sectional view showing the sealing structure of the lifting rod mechanism 30. Son-in-law 45Η, as shown in FIG. 46, the lifting rod mechanism 30 is configured to drive the lifting shaft 134 up and down to drive the lifting arm 132 inserted into the chamber 80 up and down, and a bellows-shaped telescopic tube 332 The outer periphery of the through-hole 8 inserted into the chamber 80, such as the inner descending shaft 134, is covered to prevent indoor contamination. The telescopic tube 332 has a telescopic shape, and is formed of, for example, a nickel-chromium-iron heat-resistant alloy or a corrosion-resistant nickel alloy. In addition, the through-hole 80a is closed by a cover member 340 inserted through the lowering shaft 134. In addition, a cylindrical ceramic cover 338 is fitted and fixed to the connecting member 336 of the lifting arm 132 that locks the upper end of the lifting shaft 134 with a bolt 334. The pottery cover 338 is formed so as to extend below the connecting member 336, and is provided so as to cover the periphery of the telescopic tube 332 without being directly exposed in the chamber 80. Therefore, the telescopic tube 332 extends to the upper side when the lifting space Π2 is raised in the process space 84, and is covered by a cylindrical cover 338 formed of ceramics. Therefore, the telescopic tube 332 is inserted into the cylindrical cover 338 of the through hole 80a so as to be vertically adjustable without being directly exposed to the gas and heat of the process space 84, so that deterioration due to the gas and heat can be prevented. (12) The following ‘17 brother Ming ’uses the substrate processing apparatus 2 0 ′ to perform the ultraviolet radical oxidation treatment on the surface of the substrate W to be processed, and the long-distance plasma radical nitridation treatment performed thereafter. [Ultraviolet Radical Oxidation Treatment] Fig. 47A is a side view and a plan view showing the radical oxidation of the substrate W to be processed using the substrate processing apparatus 20 of Fig. 2, and Fig. 47b is a plan view showing the structure of Fig. 47A. O: \ 87 \ 87879.DOC -45- ^ UU421433 As shown in FIG. 47A, in the aforementioned process space 84, oxygen gas can be supplied from the gas injection nozzle portion 93, and after flowing along the surface of the substrate to be processed, it is discharged through The air port 74, the turbo molecular pump 50 and the pump 201 are exhausted. By using the thirsty molecular pump 50, the process force of the aforementioned process space 84 is set to the range of 〇 ~ 3 ~ 丨 0.6 τ〇 required for the oxidation of oxygen radicals of the plate W. Oxidation of oxygen free radicals can form a stable and reproducible oxide film with a film thickness of less than 1 nm on the surface of the Shixi substrate, especially a film thickness of about 0.41m, which is equivalent to 2 ~ 3 atomic layers. Oxide film. At the same time, it is more desirable to form an oxygen radical in the oxygen stream thus formed by driving the external light source 86, 87 which generates ultraviolet light with a wavelength of 172 nm. The formed oxygen radicals oxidize the surface of the rotating substrate while flowing along the surface of the substrate boundary to be processed. As a result, as shown in FIG. 47B, it can be seen that the ultraviolet light sources 86 and 87 are tubular light sources extending in the direction intersecting with the direction of the oxygen flow. The turbo molecular pump 50 will be discharged from the process space through the exhaust port 74. 84 gas. On the other hand, an exhaust path shown by a dotted line in FIG. 47B that leads directly from the aforementioned exhaust port% to the pump 50 is blocked by closing the valve 48b. Fig. 48 is shown in the substrate processing apparatus 20 of Fig. 2. The substrate temperature is set to 450 ° C by the steps of Fig. 47 and Fig. 47B, and the intensity of the ultraviolet light irradiation and the oxygen flow rate, or the oxygen partial pressure are varied. In the case where a silicon oxide film is formed on the surface of a silicon substrate, the relationship between the film thickness and the oxidation time is changed. However, in the experiment in Fig. 48, the natural oxide film on the surface of the silicon substrate was removed before radical oxidation. Sometimes, the carbon remaining on the substrate surface was removed from the UV-excited nitrogen radicals. In addition, it was more in an Ar atmosphere. In the process, the substrate surface was planarized by performing a high temperature heat treatment at O: \ 87 \ 87879.DOC -46- 200421433 at about 950 ° C. As the ultraviolet light source 86, 87, an excimer lamp having a wavelength of 172 nm was used. Referring to Figure 48, the data of Series 1 shows that the UV intensity is set to 5% of the reference intensity (50 mW / cm2) of the window surface of the UV light source 24B, the process pressure is set to 665 mPa (5m Torr), and the oxygen flow rate. The relationship between the oxidation time and the thickness of the oxide film when set to 30 SCCM, and the data of Series 2 shows the oxidation in the case where the ultraviolet light intensity is set to 0, the process pressure is set to 133Pa (l τοτ), and the oxygen flow rate is set to 3SLM. The relationship between time and oxide film thickness. In addition, the data of Series 3 shows the relationship between the oxidation time and the oxide film thickness when the UV light intensity is set to 0, the process pressure is set to 2.66Pa (20m Ton *), and the oxygen flow rate is set to 150 SCCM. The data of Series 4 shows the oxidation time and the thickness of the oxide film when the UV light intensity is set to 100%, that is, the aforementioned reference intensity, the process pressure is set to 2.66Pa (20m Torr), and the oxygen flow rate is set to 150 SCCM. relationship. In addition, the data of Series 5 shows that the ultraviolet light intensity is set to 20% of the reference intensity, the process pressure is set to 2.66Pa (20m Torr), and the oxygen flow rate is set to 150 SCCM. The φ-shaped oxidation time and the thickness of the oxide film The data of Series 6 shows the relationship between the oxidation time and the thickness of the oxide film when the intensity of the ultraviolet light is set to 20% of the reference intensity, the process pressure is about 67Pa (0.5 Tοτ), and the oxygen flow rate is 0.5SLM. In addition, the data of Series 7 shows the relationship between the oxidation time and the oxide film thickness when the ultraviolet light intensity is set to 20% of the reference intensity, the process pressure is set to 665Pa (5 Tοιτ), and the oxygen flow rate is set to 2SLM. The data shows that the ultraviolet light intensity is set to 5% of the reference intensity, the oxidation time when the process pressure is 2.66Pa (20m Torr) and the oxygen flow rate is 150SCCM O: \ 87 \ 87879.DOC -47- 200421433 and the oxide film Thick relationship. In the experiment shown in Fig. 48, the film thickness of the oxide film was obtained by the XPS method. However, there is a unified method for obtaining such a very thin oxide film thickness below 1 nm. The inventor of this month performed background correction and separation correction of 3/2 and 1/2 rotation states on the observed Si2p execution shown in FIG. 49, and the Si2p3 / 2XPS obtained as shown in FIG. 5G Spectrum-based, Yi. And ^^ (Z. H. Lu5 et al. 3 Appl. Phys5 Lett. 71 (1997), pp. 2764) ”is used to calculate the film thickness d of the oxide film using the formula and coefficient shown in Equation (2). d = Asina · In [I-/ (/? I u ^ (1) λ = 2. 96 β = 0.75 But in Equation ⑴, α is the measured angle of the XPS spectrum shown in Figure 55. In the example, '3G and i' are set, and IX + is the integrated intensity corresponding to the spectral peak of the oxide film (house + i2x + i3x + i4x), which corresponds to the energy region between 102 and 104 eV in the figure. The peak value that can be seen. On the other hand, it is broadly corresponding to the integrated intensity of the spectral peak due to the silicon substrate in the energy region around 100eV. Referring to FIG. 48 again, it can be confirmed that the light intensity is small compared to ultraviolet light, so 幵 v In the case where the density of oxygen free radicals is small (series 丨, 2, 3, 8), although the oxide film thickness of the initial oxide film is 0 nm, the oxide film thickness will gradually increase gradually with the oxidation time. In series 4, 5, 6, and 7 in which the ultraviolet light irradiation intensity is set to 20/0 or more of the reference intensity, as schematically shown in Fig. 51, the oxide film grows to approximately _4 nm2 after the growth starts. At that time, it stagnates, and O: \ 87 \ 87879.DOC -48-200421433 After a certain amount of stagnation time, it will start to grow rapidly again. Figure 48 The relationship in Fig. 51 means that the oxidation treatment on the surface of the silicon substrate can stably form a very thin oxide film with a thickness of about 0.4 nm. Also, as seen in Fig. 48, it can be seen that due to such a dwell time, The degree of the oxide film thus formed is the same. That is, according to the present invention, an oxide film having the same thickness as about 0.4 nm can be formed on a silicon substrate. Figs. 52A and 52B are schematically shown on the silicon. The process of forming a thin oxide film on a substrate. In these figures, it must be noted that the structure on the silicon (100) substrate has been very simplistic. Referring to FIG. 52A, 2 oxygen atoms are bonded to each silicon atom on the surface of the silicon substrate. In the typical state, the silicon atoms on the substrate surface are located by two silicon atoms inside the substrate and two oxygen atoms on the substrate surface to form a secondary oxide. In this regard, in the state of FIG. 52B, the silicon atom on the top layer of the silicon substrate is obtained from 4 oxygen atoms to obtain a stable state of Si4 +. It may be because of this reason that the oxidation proceeds rapidly in the state of FIG. 52A. , Becomes Oxidation stagnation in the state of 52β. The thickness of the oxide film in the state of FIG. 52B is 0 4 nm, which is consistent with the thickness of the oxide film in the stagnation state observed in FIG. 48. The XPS spectrum in FIG. In the case of a thickness of 0.01 nm or 02 nm, the low peaks visible in the energy range of 101 to 104 eV correspond to the secondary oxide shown in Figure 52, and in the case of an oxide film thickness of more than 0 3 nm2, The peak shown in this energy range is due to Si4 +, so it can be considered that it shows the formation of an oxide film exceeding 1 atomic layer. The phenomenon of stagnant oxide thickness at a film thickness of 0.4 nm is not limited to O: \ 87 \ 87879.DOC -49- UV02 in Fig. 47A and Fig. 47B is free from the jerk-induced 2nd process by the base tick, It should be the same as long as the same thin oxide film formation method can be formed with good fineness. The thickness of the oxide film will continue to increase from the state of Fig. 52B. FIG. 53 shows that a ZrSi04x film and an electrode film having a thickness of 0.4 nm are formed on the oxide film formed by the ultraviolet light radical oxidation process of FIG. 47a and FIG. Fig. 54B), for the obtained laminated structure, the relationship between the obtained thermal oxide film conversion film thickness Teq and the leakage current Ig " However, the current characteristics of Fig. 53 are between the aforementioned electrode film and substrate ' Based on the flat band voltage Vfb, the voltage of wb-uv was measured in the applied state. For comparison, the m-flow characteristics of the thermal oxidation film are also shown in FIG. In addition, the conversion film thickness shown in the figure is about a structure that combines an oxide film and a ZrSiox film. Referring to FIG. 53, when the oxide film is omitted, that is, when the thickness of the oxide film is 0, the leakage current density exceeds the leakage current density of the thermal oxide film, and the thickness of the thermal oxide film is changed to about 1 · 7. A relatively large value of about nm means that if the film thickness of the oxide film is increased from 0 nm to 0.4 nm, the value of the thermal oxide film exchange film thickness Teq starts to decrease. In this state, the oxide film will be between the Shixi substrate and the ZrSiOx film. The physical film thickness should actually increase but the converted film thickness Teq will decrease. This will directly form Zr on the silicon substrate. In the case of 2 films, as shown in FIG. 54A, the diffusion of Zr into a silicon substrate or the diffusion of Si into a ZrSiOx film occurs on a large scale, as shown in the silicon O: \ 87 \ 87879.DOC -50- 200421433 substrate. A thick interface layer is formed between the film and the film. In this regard, as shown in FIG. 2, it is considered that by forming an oxide film having a thickness of G.4 nm therebetween, the formation of such an interface layer can be suppressed. As a result, the converted film thickness is reduced. It follows that the value of the leakage current decreases with the thickness of the oxide film. However, FIG. 54a and FIG. MB show a schematic cross-section of the experimental material thus formed, and show that an oxide film 442 is formed on the Shixi substrate 441, and 2 ^ 丨 0 is formed on the oxide film 442; (film Structure of 443. On the other hand, when the thickness of the foregoing oxide film exceeds 0.4 nm, the value of the film thickness converted by the thermal oxide film will start to increase again. The thickness of the oxide film exceeds the range of "nm, as As the film thickness increases, the value of the leakage current also decreases, and it can be thought that the increase in the converted film thickness is due to the increase in the physical film thickness of the oxide film. Thus, the growth of the oxide film observed in FIG. 48 The stagnant film thickness of 0.4 is the minimum corresponding to the converted film thickness of the system including the oxide film and the high-dielectric film. It can be seen that the stable oxide film shown in Figure 52 (B) can Effectively prevent the diffusion of metal elements such as Zr to the silicon substrate, and even if the thickness of the oxide film is larger, the effect of preventing the diffusion of metal elements will not be much improved. In addition, 'leakage when using an oxide film with a thickness of 0.4 nm is known The value of the current is the thermal oxidation of the corresponding thickness The value of the leakage current is about two digits smaller. By using the insulating film thus structured in the gate insulating film of a MOS transistor, the gate leakage current can be minimized. In addition, the oxide film described in FIG. 48 or 51 As a result of the stagnation phenomenon of the growth of 0.4 nm, even if the oxide film 442 formed on the Shixi substrate 441 as shown in FIG. 55A has unevenness of the original film thickness, the growth of the oxide film is O: \ 87 \ 87879.DOC -51-'Dry, ▲ film thickness increase stagnates in the vicinity of 0.4 mn as shown in Figure 55B. Therefore, by continuing the oxide film growth during the τ lag period, it can be obtained as shown in Figure 55C. The ground is flat and has the same thickness of the oxide film 442. As explained earlier, for very thin oxide films, there is currently no uniform film thickness measurement method. Therefore, the film thickness of the oxide film 442 in FIG. 55C The value may vary depending on the wave and the method. However, for the reasons explained previously, the thickness of the stagnation in the growth of the oxide film is a thick 2 atomic layer. Therefore, again, It is considered that the ideal film thickness of the oxide film 442 is about 2 atomic layers. The ideal thickness is to ensure a thickness of 2 atomic layers in the entire oxide film 442, and a 3 atomic layer thickness region is formed in a part. That is, 'the ideal thickness of the oxide film 442 can be considered to be actually It is in the range of 2 to 3 atomic layers. [Remote plasma radical nitridation treatment] Fig. 56 shows the structure of the remote plasma unit 27 used in the substrate processing apparatus 20. As shown in Fig. 56, the long distance The plasma section 27 is formed in the inside thereof with a gas circulation path 27a, a gas inlet 27b, and a gas outlet 76c connected thereto, typically including a block 27A made of aluminum, and a part of the aforementioned block 27A A ferrite core 27B is formed. A fluorine resin processing 27d is provided on the inner surfaces of the gas circulation path 27a, the gas inlet 27b, and the gas outlet 27c. A high frequency of 400 kHz is supplied from a coil wound around the ferrite core 27B. A plasma 27C is formed in the gas circulation path 27a. With the excitation of plasma 27C, although O: \ 87 \ 87879.DOC -52- 200421433 is formed in the aforementioned gas circulation path 27a, nitrogen radicals and nitrogen ions are present, but nitrogen ions will circulate in the aforementioned gas circulation path 27a ^ The gas disappears, so the above-mentioned gas outlet 2 is mainly released gas free radical N2. In addition, in the configuration of FIG. 56, the ion filter || 27e grounded to the aforementioned gas outlet n27e is provided to remove charged particles such as nitrogen ions, and only nitrogen radicals are supplied to the aforementioned process space 84. In addition, even if the ion filter 27e is not grounded, the structure of the ion filter 27e also functions as a diffusion plate, and can sufficiently remove charged particles such as nitrogen ions. Fig. 57 shows a comparison between the relationship between the number of ions formed by the remote plasma unit 27 and the amount of electron energy and energy 'and the source of the microwave electrode. As shown in Fig. 57, when the plasma is excited by the microwave, nitrogen ionization of the nitrogen molecules is promoted, and a large amount of nitrogen ions are formed. For this reason, when the plasma is excited by the same frequency below 5000 kHz, the number of nitrogen ions formed will be greatly reduced. When plasma treatment is performed by microwave, as shown in FIG. 58, a high vacuum of 1.33x10 ~ i ^ xlC ^ PaGo · 1 ~ i0_4T〇rr) is required. The high-frequency plasma treatment can be 13.3 ~ 13.3. kPa (0.1 ~ 100 Torr) with a relatively high pressure and force. Table 1 below shows the comparison of ionization energy conversion efficiency, possible discharge pressure range, plasma power consumption, and process gas flow between the case where the plasma is excited by microwaves and the case where the plasma is excited by high frequencies. Table 1

離子化能量變 — 換效率 放電可能 壓力範圍 電漿 消耗電力 製程 氣體流量 微 波一 Ι.ΟΟχΙΟ"2 0.1m〜0.1 Torr 1 〜500W 0〜100 SCCM 南 頻一 l.OOxlO·7 b.l〜100Torr 卜1〜10kW 0.1 〜10SLM O:\87\87879.DOC -53- 200421433 參照表1,可知關於離子化能量變換效率,相對於在微波 激發之情形時約為1X 1 (T2左右,於RF激發之情形則減少至 約1X1 (Γ7為止,另外,關於放電可能壓力,相對於為微波激 發之0.1111丁〇]:1:〜0.111〇1*1>(133111?3〜13.3?&)左右,1^激發之情 形則是0.1〜100 Torr (13.3 Pa〜13.3 kPa)左右。隨之,電漿消 耗電力係RF激發時較微波激發時為大,而製程氣體流量係 RF激發時亦較微波激發時大出很多。 於基板處理裝置20中,係以氮自由基N/而非氮離子來進 行氧化膜之氮化處理,因此被激發之氮離子數量少較為理 想。又,由最小化被加諸於被處理基板之損害之觀點來看, 亦是被激發之氮離子數量少較為理想。此外,於基板處理 裝置20中,以被激發之氮自由基數量少,於高電介質閘極 絕緣膜下非常薄之最多2〜3原子層左右厚度之基底氧化 膜,非常適合於氮化。 圖59A、圖59B係分別顯示使用基板處理裝置2〇進行被處 理基板W之自由基氮化時之側面圖與俯視圖。 如圖59A、圖59B所示,於遠距離電漿部27供給有Ar氣體 與氮氣體,故以數100 kHz之頻率藉由高頻激發電漿,形成 氮自由基。而被形成之氮自由基係延著前述被處理基板W 之表面流動,經由前述排氣口 74與幫浦201被排出。結果, 前述製程空間84可被設定於適合基板w之自由基氮化之 l,3 3Pa〜13.3kPa (0.01〜1〇〇 Torr)範圍的製程壓力。如此被形 成之氮自由基會在延著前述被處理基板W之表面流動之 際,氮化被處理基板W之表面。 O:\87\87879.DOC -54- 200421433 於圖59A、圖59B之氮化步驟中,於氮化步驟之前的清淨 步驟中,前述閥48a與212為被開放,藉由關閉閥術使前述 製程空間84之壓力減壓至〜丨33χΐ〇·4〜之壓力為 止’殘留於製程空間84中之氧及水分會被清除,但於其後 之氮化處理中,其閥48&與212被關閉,而渦輪分子幫浦5〇 . 則不包含於製程空間84之排氣路徑。 如此,藉由使用基板處理裝置20,可在被處理基板W之 表面形成非常薄之氧化膜’並進一步氣化其氧化膜表面。 圖60Α係顯示使用遠距離電漿部27,並以表2所示條件氮籲 化藉由基板處理裝置2〇在矽基板上進行熱氧化處理而形成 之2.0 nm厚之氧化膜時之前述氧化膜中之氮濃度分佈,圖 60B則顯示於相同氧化膜中之氮濃度分佈與氧濃度分佈之 關係圖。 表2Ionization energy change—change efficiency discharge possible pressure range plasma consumption power process gas flow microwave Ⅰ.〇ΟχΙΟ " 2 0.1m ~ 0.1 Torr 1 ~ 500W 0 ~ 100 SCCM South frequency Ⅰ.OOxlO · 7 bl ~ 100Torr 卜 1 ~ 10kW 0.1 ~ 10SLM O: \ 87 \ 87879.DOC -53- 200421433 With reference to Table 1, it can be seen that the ionization energy conversion efficiency is about 1X 1 (about T2, in the case of RF excitation) in the case of microwave excitation. Then it is reduced to about 1X1 (up to Γ7, and the possible discharge pressure is relative to 0.1111 d0 which is microwave excitation): 1: ~ 0.111 〇1 * 1 > (133111? 3 to 13.3? The excitation situation is about 0.1 ~ 100 Torr (13.3 Pa ~ 13.3 kPa). Accordingly, the plasma consumes more power when the RF excitation is greater than the microwave excitation, and the process gas flow is greater when the RF excitation is greater than the microwave excitation. In the substrate processing apparatus 20, the nitridation treatment of the oxide film is performed by using nitrogen radical N / instead of nitrogen ions, so it is desirable that the number of excited nitrogen ions is small. Furthermore, minimization is added to From the perspective of damage to the substrate being processed It is also desirable that the number of excited nitrogen ions is small. In addition, in the substrate processing device 20, the number of excited nitrogen radicals is small, and the thickness under the high-dielectric gate insulating film is very thin, at most about 2 to 3 atomic layers. The underlying oxide film is very suitable for nitriding. Figures 59A and 59B show a side view and a top view, respectively, when radical nitriding of the substrate W to be processed is performed using the substrate processing apparatus 20. As shown in Figures 59A and 59B Since Ar gas and nitrogen gas are supplied to the long-distance plasma unit 27, the plasma is excited by high frequency at a frequency of several hundred kHz to form nitrogen radicals. The formed nitrogen radicals extend along the substrate to be processed. The surface of W flows and is discharged through the exhaust port 74 and the pump 201. As a result, the process space 84 can be set to a free radical nitridation suitable for the substrate w, 3 3 Pa to 13.3 kPa (0.01 to 100). Torr) process pressure. The nitrogen radicals thus formed will nitrate the surface of the substrate W to be processed while flowing along the surface of the substrate W to be processed. O: \ 87 \ 87879.DOC -54- 200421433 Nitriding step in Figure 59A, 59B In the cleaning step before the nitriding step, the valves 48a and 212 are opened, and the pressure in the process space 84 is reduced to a pressure of ~ 丨 33χΐ〇 · 4 ~ by the valve closing operation. The oxygen and moisture in the space 84 will be removed, but in the subsequent nitriding treatment, its valves 48 & and 212 are closed, and the turbo molecular pump 50. is not included in the exhaust path of the process space 84. In this way, by using the substrate processing apparatus 20, a very thin oxide film 'can be formed on the surface of the substrate W to be processed, and the oxide film surface can be further vaporized. FIG. 60A shows the aforementioned oxidation when a long-range plasma unit 27 was used and nitrogen was applied under the conditions shown in Table 2 to form a 2.0 nm-thick oxide film formed by thermal oxidation treatment on a silicon substrate using a substrate processing apparatus 20. The nitrogen concentration distribution in the film, FIG. 60B shows the relationship between the nitrogen concentration distribution and the oxygen concentration distribution in the same oxide film. Table 2

參照表2,於使用基板處理裝置2〇進行RF氮化處理之際, 對製耘空間84内,以50 SCCM之流量供給氮或2 SLM之流量 供給Ar,在1 Ton· (l33Pa)之壓力下進行氮化處理,但於氮 化處理開始前暫時將製程空間84之内壓減壓至1〇_6 T〇rr (1.33x10 Pa)左右為止’並充分地清除殘留於内部之氧或 水份。因此,於以前述i 丁〇]:]:左右之壓力所進行之氮化處理 之際,於製程空間84中,其殘留氧可*Ar或氮來稀釋,殘 留氧濃度,故殘留氧之熱力學上之活動度變的非常地小。 O:\87\87879.DOC -55- 200421433 對此,在使用微波電漿之氮化處理中,氮化處理時之處 理壓力係與清除壓為同樣程度,故可認為於電聚氛圍中, 殘留氧係具有高熱力學上活動度者。 參照圖60 A,於藉由微波激發電漿而氮化之情形時,其被 導入於氧化膜中之氮的濃度為有限的,故可知實質上並未 進行氧化膜之氮化。對此如同本實施例般,於藉由RF激發 電漿而氮化之情形時,可知於氧化膜中其氮濃度會隨著深 度呈現線性變化,而在表面附近則達到將近2〇%之濃度。 圖61係顯示使用xps (X射線光譜)所進行之圖6〇A之測定_ 原理。 參照圖61,於矽基板411上形成氧化膜412之試驗材料, 係由X射線以特定角度斜斜地照射,·再由檢測器DEt 1、 DET2以各種角度檢測被激發之X射線光譜。此時,例如由 被設定成90。之深檢測角之檢測器DET1中,其於激發X射線 之氧化膜412内之路徑短,故於以前述檢測器DET1所檢測 之X射線光譜中包含有許多氧化膜412之下部資訊,相對於_ 此’在被設定成淺檢測角之檢測器DET2中,其於激發X射 線之氧化膜412中之路徑長,故檢測器DET2主要是檢測氧 化膜412表面附近之資訊。 圖60B係顯示於前述氧化膜中之氮濃度與氧濃度之關 係。但圖60B中,氧濃度係由對應〇is執道之X射線強度所 表示。 參照圖60B,在如本發明般以RF遠距離電漿進行氧化膜 氮化之情形中,隨著氮濃度的增大會使氧濃度減少,故可 O:\87\87879.DOC -56- 200421433 知於氧化膜中氮原子會置換氧原子。對此,在以微波電聚 進行氧化膜氮化之情形中,無法見到如此之置換關係,亦 不見氧濃度隨著氮濃度而降低之關係。另外,特別是於圖 60B中,在由微波氮化導入5〜6%的氮之例中可見到氧濃度 的增加,此係意味著隨著氮化而引起氧化膜之增加。隨著 如此之微波氮化之氧濃度的增加,係於高真空中進行微波 氮化,故可認為殘留於處理空間中之氧或水份並非藉由如 高頻遠距離電漿氮化情形之Ar氣體與氮氣體來稀釋,而是 因在氛圍中具有高活動度者。 圖62係顯示於基板處理裝置2〇形成厚度為4Α(〇·4 nm)與 7人(0.7 nm)之氧化膜,並由使用前述遠距離電漿部27之圖 59A、圖59B之氮化步驟,將其氮化時之氮化時間與膜中之 氮濃度之關係。又圖63係顯示對隨著圖62之氮化處理之氮 對氧化膜膜表面之偏析情形。另外,於圖62、圖63亦顯示 出以急速熱氧化處理將氧化膜形成為5人(〇·5 nm)47A (〇7 ηπι)的厚度之情形。 參照圖62,膜中之氮濃度係任一氧化膜皆會隨著氮化處 理時間而一起上昇’但特別是在具有對應由紫外光自由基 氧化所形成之2原子層份之〇 4mn膜厚之氧化膜的情形,或 具有接近於此之〇·5 nm膜厚之熱氧化膜的情形時,由於氧 化膜薄’故於相同成膜條件下膜中之氮濃度會變高。 圖63係顯示於圖61分別將檢測器D]ET1&DET2設定成30。 及90之檢測角所檢測出之氮濃度之結果。 由圖63可知’圖63之縱軸係以9〇。之檢測角所得到由分散Referring to Table 2, when the substrate nitriding device 20 is used for the RF nitriding treatment, nitrogen is supplied to the processing space 84 at a flow rate of 50 SCCM or Ar at a flow rate of 2 SLM at a pressure of 1 Ton · (l33Pa). The nitriding treatment is performed, but the internal pressure of the process space 84 is temporarily decompressed to about 10-6 Torr (1.33x10 Pa) before the nitriding treatment is started, and the oxygen or water remaining inside is fully removed. Serving. Therefore, in the case of nitriding treatment with the aforementioned pressures:]: in the process space 84, the residual oxygen can be diluted by * Ar or nitrogen, and the residual oxygen concentration, so the thermodynamics of residual oxygen The activity on it has become very small. O: \ 87 \ 87879.DOC -55- 200421433 In this regard, in the nitriding process using a microwave plasma, the processing pressure during the nitriding process is the same as the removal pressure, so it can be considered in an electropolymerized atmosphere. Residual oxygen system has high thermodynamic activity. Referring to FIG. 60A, in the case where the plasma is nitrided by exciting the microwave, the concentration of nitrogen introduced into the oxide film is limited, so it can be seen that the nitriding of the oxide film is not substantially performed. As for this example, when the plasma is nitrided by RF excitation, it can be known that the nitrogen concentration in the oxide film will change linearly with the depth, and it will reach a concentration of nearly 20% near the surface. . Fig. 61 shows the principle of the measurement of Fig. 60A using xps (X-ray spectroscopy). Referring to FIG. 61, a test material for forming an oxide film 412 on a silicon substrate 411 is irradiated obliquely by X-rays at a specific angle, and the excited X-ray spectra are detected by the detectors DEt 1, DET 2 at various angles. At this time, for example, is set to 90. The detector DET1 with a deep detection angle has a short path in the oxide film 412 that excites X-rays. Therefore, the X-ray spectrum detected by the aforementioned detector DET1 contains a lot of information about the lower part of the oxide film 412. _ This 'DET2', which is set to a shallow detection angle, has a long path in the oxide film 412 that excites X-rays, so the detector DET2 mainly detects information near the surface of the oxide film 412. Fig. 60B shows the relationship between the nitrogen concentration and the oxygen concentration in the aforementioned oxide film. However, in Fig. 60B, the oxygen concentration is represented by the intensity of X-rays corresponding to Ois. Referring to FIG. 60B, in the case where the oxide film is nitrided by RF remote plasma as in the present invention, as the nitrogen concentration increases, the oxygen concentration decreases, so O: \ 87 \ 87879.DOC -56- 200421433 It is known that nitrogen atoms replace oxygen atoms in the oxide film. On the other hand, in the case where the oxide film is nitrided by microwave electropolymerization, such a replacement relationship cannot be seen, and a relationship in which the oxygen concentration decreases with the nitrogen concentration cannot be seen. In addition, particularly in FIG. 60B, an increase in oxygen concentration is seen in the case where 5 to 6% of nitrogen is introduced by microwave nitridation, which means that the oxide film increases with nitriding. With the increase of the oxygen concentration of such microwave nitriding, the microwave nitriding is performed in a high vacuum, so it can be considered that the oxygen or water remaining in the processing space is not an Ar gas such as the case of high-frequency long-range plasma nitriding. Dilute with nitrogen gas, but because of high activity in the atmosphere. FIG. 62 shows the formation of an oxide film with a thickness of 4A (0.4 nm) and 7 persons (0.7 nm) on the substrate processing apparatus 20, and nitrided from FIG. 59A and FIG. 59B using the aforementioned long-range plasma unit 27. In the step, the relationship between the nitriding time during the nitriding and the nitrogen concentration in the film. Fig. 63 shows the segregation of nitrogen on the oxide film surface with the nitrogen treatment in Fig. 62. In addition, Fig. 62 and Fig. 63 also show the case where the oxide film is formed to a thickness of 5A (0.5 nm) 47A (〇7 ηπ) by a rapid thermal oxidation treatment. Referring to FIG. 62, the nitrogen concentration in the film is that any oxide film will rise together with the nitriding treatment time, but it is particularly thick with a thickness of 0.44 m corresponding to the 2-atomic layer formed by ultraviolet light radical oxidation. In the case of an oxide film or a thermal oxide film having a film thickness close to 0.5 nm, the nitrogen concentration in the film becomes higher because the oxide film is thinner under the same film formation conditions. Fig. 63 shows that the detector D] ET1 & DET2 is set to 30 in Fig. 61, respectively. And the nitrogen concentration detected at a detection angle of 90. It can be seen from FIG. 63 that the vertical axis of FIG. 63 is 90. Scatter angle

O:\87\87879.DOC «57- 200421433 在膜王體之氮原子而來之X射線光譜強度之值,除。之檢 ’則角所得到之由偏析於膜表面之氮原子之χ射線光譜強度 所得到者’並將此定義$氮偏析率。在該值為i以上之情形 下’會產生對表面之氮偏析。 參照圖63,#由紫外光激發氧自由基處理而將氧化膜之 膜厚形成為7A之情形下,其氮偏析率成為丨以上,氮原子於 最初之表面偏析,可認為是如則中之氧氮化膜12八之狀態 者。另外,可知在進行90秒間之氮化處理後,於膜中之分 佈大致相同。X可知即使是其他之膜,以9〇秒之氮化處理, 亦會使氮原子之膜中分佈變成大致相同。 於圖64之實驗中,在基板處理裝置20,針對1〇片晶圓(晶 圓#1〜晶圓#1〇) ’重複進行前述紫外光自由基氧化處理及遠 距離電漿氮化處理。圖64係顯示如此得到之氧氮化膜之每 個晶圓之臈厚變動。但’圖64之結果係關於在基板處理裝 置20驅動紫外線光源86, 87而進行紫外光自由基氧化處理 之際,形成由xps測定所求得之氧化膜厚度為〇 4nm之氧化 膜’接著’將如此所形成之氧化膜,藉由驅動前述遠距離 電漿部27進行氮化處理,變換成包含約4%氮原子之氧氮化 膜之情形者。 參照圖64 ’縱軸係顯示對於如此所求得之氧氮化膜以橢 圓對稱所求得之膜厚,但由圖64可知所求得之膜厚係大致 安定於 8A (0.8 nm)。 圖65係顯示藉由基板處理裝置2〇,於石夕基板上藉由使用 紫外線光源86, 87之自由基氧化處理形成膜厚為G4 nm之 O:\87\87879.DOC -58- 200421433 氧化膜後’藉由遠距離電漿部27將其加以氮化之情形,所 得的因氮化之膜厚增加之調查結果。 參照圖65,可知最初(進行氮化處理前)膜厚約為〇38 之氧化膜,係在氮化處理中導入4〜7%之氮原子之時,膜厚 、、、勺增大至0·5 nm為止。另一方面,在氮化處理中導入約 之氮原子時,其膜厚約增大至L3 nm為止,於該情形時可 涊為被導入之氮原子通過氧化膜侵入至矽基板中而形成氮 化膜。 於圖65中係以▲顯示有關僅導入一層份之氮於厚度為 〇·4 nm之氧化膜中之理想的模型構造中之氮濃度與膜厚之 關係。 參照圖65,於該理想的模型構造中,氮原子導入後之膜 厚約變成0.5 nm,該情形時之膜厚增加約為〇1 nm,而氮濃 度約為12%。若以該模型為基準,則結論為:藉由基板處 理裝置20進行氧化膜之氮化時,其膜厚增加以抑制在相同 程度之0.1〜0.2 nm者為較理想。另外此時亦可預估被取入於 膜中之氮原子量最大為12%左右。 另外,於以上之說明中,係說明使用基板處理裝置2〇而 幵/成非常薄之基底氧化膜之例,但本發明並未限定於如此 特定之實施例,亦可適用在矽基板或矽膠層上,形成所希 望膜厚之高品質氧化膜、氮化膜或氮氧化膜。 以上’以較佳之實施例說明了本發明,但本發明並未限 定於上述之特定實施例,於揭示在申請專利範圍之要旨内 皆可作各種變化、變更。 O:\87\87879.DOC -59- 200421433 【圖式簡單說明】 圖1係顯示含有高電介質閘極絕緣膜之半導體裝置 圖2係顯示本發明之基板處理裝置之一實施例構成之前 視圖。 圖3係顯示本發明之基板處理裝置之一實施例構成之側 視圖。 圖4為沿著圖2中A-A線之橫剖面圖。 圖5係顯示配置於處理容器22下方之機器構成之前視圖。 圖6係顯示配置於處理容器22下方之機器構成之俯視圖。 圖7係顯示配置於處理容器22下方之機器構成之側視圖。 圖8 A係顯示排氣路徑32之構成之俯視圖。 圖8B係顯示排氣路徑32之構成之前視圖。 圖8C為沿著B-B線之縱剖面圖。 圖9係擴大顯示處理容器22及其周邊機器之側面縱剖面 圖。 圖10為從上方所見拿掉蓋子構件82後之處理容器22内部 之俯視圖。 圖Π為處理容器22之俯視圖。 圖12為處理容器22之前視圖。 圖13為處理容器22之仰視圖。 圖14為沿著圖12中C-C線之縱剖面圖。 圖15為處理容器22之右側視圖。 圖16為處理容器u之左側視圖。 O:\87\87879.DOC •60- 200421433 圖17係擴大顯示紫外線光源86、87之安裝構造之縱剖面 圖。 圖18係擴大顯示氣體喷射喷嘴部93之構成之縱剖面圖。 圖19係擴大顯示氣體喷射喷嘴部93之構成之橫剖面圖。 圖20係擴大顯示氣體噴射喷嘴部93之構成之前視圖。 、 圖21係擴大顯示加熱部24之構成之縱剖面圖。 圖22係擴大顯示加熱部24之仰視圖。 圖23係擴大顯示第2流入口 170,及第2流出口 174之安裝 構造之縱剖面圖。 _ 圖24係擴大顯示凸緣14〇之安裝構造之縱剖面圖。 圖25係擴大顯示夾鉗機構19〇之上端部之安裝構造之縱 剖面圖。 圖26係顯示siC加熱器114,及SiC加熱器114之控制系統 構造之圖。 圖27A係顯示石英鐘罩112之構造之俯視圖。 圖27B係顯示石英鐘罩112之構造之縱剖面圖。 圖28A為從上方所見石英鐘罩112之構造之立體圖。 圖28B為從下方所見石英鐘罩112之構造之立體圖。 圖29係顯示減壓系統之排氣系統構成之系統圖。 · 圖3〇A係顯示保持構件12〇構成之俯視圖。 圖3〇B係顯示保持構件12〇構成之側面圖。 圖31係顯示配置於加熱部24下方之旋轉驅動部28之構成 之縱剖面圖。 圖32係擴大顯示旋轉驅動部“之縱剖面圖。O: \ 87 \ 87879.DOC «57- 200421433 The value of the intensity of the X-ray spectrum from the nitrogen atom of the membrane royal body, divided. The test is then obtained from the X-ray spectral intensity of nitrogen atoms segregated on the surface of the film, and this is used to define the nitrogen segregation rate. In the case where the value is i or more, segregation of nitrogen on the surface occurs. Referring to FIG. 63, in the case where the thickness of the oxide film is formed to 7A by the ultraviolet light-excited oxygen radical treatment, the nitrogen segregation rate becomes 丨 or more, and the nitrogen atom segregates on the initial surface, which can be considered as The state of the oxynitride film 12 is eight. In addition, it can be seen that the distribution in the film after the nitriding treatment for 90 seconds was almost the same. It can be seen from X that even in other films, the nitriding treatment at 90 seconds can make the distribution of nitrogen atoms in the film substantially the same. In the experiment shown in FIG. 64, the substrate processing apparatus 20 repeatedly performs the aforementioned ultraviolet light radical oxidation treatment and long-range plasma nitridation treatment on 10 wafers (Crystal Circle # 1 to Wafer # 10). Fig. 64 shows the variation in thickness of each wafer of the oxynitride film thus obtained. However, the result of FIG. 64 is about forming an oxide film having an oxide film thickness of 0.4 nm obtained by xps measurement when the substrate processing apparatus 20 drives the ultraviolet light sources 86 and 87 to perform ultraviolet radical oxidation treatment. The oxide film formed in this way is converted into a case of an oxynitride film containing about 4% nitrogen atoms by driving the aforementioned long-distance plasma unit 27 to perform a nitriding treatment. Referring to Fig. 64 ', the vertical axis shows the film thickness obtained by ellipsoidal symmetry of the oxynitride film thus obtained, but it can be seen from Fig. 64 that the obtained film thickness is approximately stabilized at 8A (0.8 nm). FIG. 65 shows the formation of O: \ 87 \ 87879.DOC -58- 200421433 with a film thickness of G4 nm on a substrate of Shi Xi by a radical oxidation treatment using an ultraviolet light source 86, 87 by using a substrate processing apparatus 20. In the case where the film is nitrided by the remote plasma unit 27 after the film, the result of the investigation that the film thickness due to nitridation is increased is obtained. Referring to FIG. 65, it can be seen that the oxide film having a film thickness of about 038 (before the nitriding treatment) is initially increased to 0 when nitrogen atoms of 4 to 7% are introduced during the nitriding treatment. Up to 5 nm. On the other hand, when nitrogen atoms are introduced during the nitridation process, the film thickness is increased to approximately L3 nm. In this case, the introduced nitrogen atoms may penetrate into the silicon substrate through the oxide film to form nitrogen. Chemical film. In Fig. 65, the relationship between the nitrogen concentration and the film thickness in the ideal model structure for the introduction of only one layer of nitrogen into the oxide film with a thickness of 0.4 nm is shown with ▲. Referring to FIG. 65, in this ideal model structure, the film thickness after the introduction of nitrogen atoms becomes about 0.5 nm, and the film thickness in this case increases by about 0.1 nm, and the nitrogen concentration is about 12%. Based on this model, it is concluded that when nitriding the oxide film by the substrate processing device 20, it is desirable that the film thickness be increased to suppress the same degree of 0.1 to 0.2 nm. In addition, the maximum amount of nitrogen atoms taken into the film at this time can be estimated to be about 12%. In addition, in the above description, an example of using a substrate processing apparatus 20 and forming a very thin base oxide film was described, but the present invention is not limited to such a specific embodiment, and can also be applied to a silicon substrate or silicon On the layer, a high-quality oxide film, nitride film, or oxynitride film having a desired film thickness is formed. The above 'illustrates the present invention with preferred embodiments, but the present invention is not limited to the specific embodiments described above, and various changes and modifications can be made within the spirit of the scope of patent application. O: \ 87 \ 87879.DOC -59- 200421433 [Brief Description of the Drawings] Fig. 1 shows a semiconductor device including a high-dielectric gate insulating film. Fig. 2 shows a front view of an embodiment of a substrate processing device of the present invention. Fig. 3 is a side view showing the structure of an embodiment of a substrate processing apparatus of the present invention. Fig. 4 is a cross-sectional view taken along line A-A in Fig. 2. FIG. 5 is a front view showing the configuration of a machine disposed below the processing container 22. FIG. 6 is a plan view showing the structure of a machine disposed below the processing container 22. FIG. 7 is a side view showing the configuration of a machine disposed below the processing container 22. FIG. 8A is a plan view showing the configuration of the exhaust path 32. FIG. FIG. 8B is a front view showing the configuration of the exhaust path 32. FIG. Fig. 8C is a longitudinal sectional view taken along line B-B. Fig. 9 is an enlarged longitudinal sectional view of the processing container 22 and its peripheral devices. Fig. 10 is a plan view of the inside of the processing container 22 with the lid member 82 removed from above. FIG. 9 is a plan view of the processing container 22. FIG. 12 is a front view of the processing container 22. FIG. 13 is a bottom view of the processing container 22. Fig. 14 is a longitudinal sectional view taken along the line C-C in Fig. 12. FIG. 15 is a right side view of the processing container 22. FIG. 16 is a left side view of the processing container u. O: \ 87 \ 87879.DOC • 60- 200421433 Fig. 17 is a longitudinal sectional view showing the installation structure of the ultraviolet light sources 86 and 87 in an enlarged manner. FIG. 18 is a longitudinal sectional view showing an enlarged configuration of the gas injection nozzle portion 93. FIG. FIG. 19 is a cross-sectional view showing the structure of the gas injection nozzle section 93 in an enlarged manner. FIG. 20 is an enlarged front view showing the configuration of the gas injection nozzle portion 93. FIG. 21 is a longitudinal sectional view showing the structure of the heating section 24 in an enlarged manner. FIG. 22 is an enlarged bottom view of the heating unit 24. Fig. 23 is a longitudinal sectional view showing the mounting structure of the second inflow port 170 and the second outflow port 174 in an enlarged manner. _ FIG. 24 is a longitudinal sectional view showing the mounting structure of the flange 14 in an enlarged manner. Fig. 25 is a longitudinal sectional view showing the mounting structure of the upper end portion of the clamp mechanism 19 in an enlarged manner. FIG. 26 is a diagram showing the configuration of a control system of the siC heater 114 and the SiC heater 114. FIG. FIG. 27A is a plan view showing the configuration of the quartz bell cover 112. FIG. Fig. 27B is a longitudinal sectional view showing the structure of the quartz bell cover 112. FIG. 28A is a perspective view of the structure of the quartz bell cover 112 seen from above. FIG. 28B is a perspective view of the structure of the quartz bell cover 112 seen from below. Fig. 29 is a system diagram showing the structure of an exhaust system of a pressure reduction system. Fig. 30A is a plan view showing the configuration of the holding member 12o. FIG. 30B is a side view showing the configuration of the holding member 12o. FIG. 31 is a longitudinal sectional view showing the configuration of the rotation driving section 28 disposed below the heating section 24. As shown in FIG. Fig. 32 is a longitudinal sectional view showing an enlarged "rotation drive unit".

O:\87\87879.DOC -61 - 200421433 圖33A係顯示托架冷卻機構234構成之橫剖面圖。 圖33B係顯示托架冷卻機構234構成之側面圖。 圖34係顯示旋轉位置檢測機構232構成之橫剖面圖。 圖35 A係顯示旋轉位置檢測機構232之非檢測狀態之圖。 圖35B係顯示旋轉位置檢測機構232之檢測狀態之圖。 圖36A係顯示旋轉位置檢測機構232之受光元件268之輸 出信號S之波形圖。 圖3 6B為從旋轉位置判定電路270所輸出之脈衝信號P之 波形圖。 圖37為說明控制電路所進行旋轉位置控制處理之流程 圖。 圖38為從上方所見窗口 75、76之安裝處之橫剖面圖。 圖3 9係擴大顯示窗口 7 5之橫剖面圖。 圖40係擴大顯示窗口 76之橫剖面圖。 圖41A係顯示下部盒體102構成之俯視圖。 圖41B係顯示下部盒體102構成之側面圖。 圖42A係顯示側面盒體104構成之俯視圖。 圖42B係顯示側面盒體104構成之前視圖。 圖42C係顯示側面盒體104構成之後視圖。 圖42D係顯示側面盒體104構成之左側視圖。 圖42E係顯示側面盒體104構成之右側視圖。 圖43A係顯示上部盒體106構成之仰視圖。 圖43B係顯示上部盒體106構成之側面圖。 圖44A係顯示圓筒狀盒體108構成之俯視圖。 O:\87\87879.DOC -62- 200421433 圖44B係顯示圓筒狀盒體108構成之側面縱剖面圖。 圖44C係顯示圓筒狀盒體108構成之側面圖。 圖45係擴大顯示升降桿機構30之縱剖面圖。 圖為擴大顯示升降桿機構30之密封構造之縱剖面圖。 圖47A係顯示使用圖2之基板處理裝置2〇,進行被處理基、 板W之自由基氧化情形之側面圖及俯視圖。 圖键係顯示圖47A之構成之俯視圖。 · 圖48係顯示使用基板處理裝置20,所進行之基板氧化處 理步驟之圖。 _ 圖49係顯示根據本發明所使用之xps之膜厚測定方法之 圖。 圖50係顯示根據本發明所使用之xps之膜厚測定方法之 其他圖。 圖5 1係概略地顯示藉由基板處理裝置2〇形成氧化膜之 際’所觀測到氧化膜厚成長之停滯現象之圖。 圖52A係顯示於矽基板表面之氧化膜形成過程1之圖。 ❿ 圖52B係顯示於矽基板表面之氧化膜形成過程2之圖。 圖53係顯示於本發明第1實施例中,所得到之氧化膜之漏 洩電流特性之圖。 - 圖54Α為說明圖53之漏洩電流特性原因之圖。 圖54Β為說明圖53之漏洩電流特性原因之圖。 圖55Α係顯示於基板處理裝置2〇所產生之氧化膜形成步 驟1之圖。 圖55B係顯示於基板處理裝置2〇所產生之氧化膜形成步 O:\87\87879.DOC -63- 200421433 驟2之圖。 圖55C係顯示於基板處理裝置2〇所產生之氧化膜形成步 驟3之圖。 夕 圖56係顯示於基板處理裝置2〇所使用之遠距離電漿源構 成之圖。 圖57為比較RF遠距離電漿與微波電漿特性之圖。 圖58為比較RF遠距離電漿與微波電漿特性之其他圖。 圖59A係顯示使用s板處理裝置2〇所進行之氧化膜之氮 化處理之側面圖。 圖观係顯示使用基板處理裝置2G所進行之氧化膜之氮 化處理之俯視圖。 圖6〇A係顯示使用遠距離電漿部27 ,以表2所示條件對藉 日土^處理裝置⑼在碎基板上以熱氧化處理形成之2.0⑽ 厚之乳化膜,進行氮化時之前述氧化膜中之氮濃度分佈圖。 圖刚係顯示於相同氧化膜中之氮濃度分佈與氧濃度分 佈之關係圖。 圖61係顯示在本發明所使用之XPS之概略圖。 二2係顯示根據氧化膜之遠距離電漿之氮化時間與膜中 亂/辰度之關係圖。 係、顯不軋化膜《氮化時間與氮之膜内分佈之關係 圖0 〜A〜外狂所艰成之鳘個章 膘之日日圓之膜厚變動圖。 圖65係顯示隨著因本實施例之氧化膜氮化處理之辟O: \ 87 \ 87879.DOC -61-200421433 Fig. 33A is a cross-sectional view showing the structure of the bracket cooling mechanism 234. Fig. 33B is a side view showing the structure of the bracket cooling mechanism 234. FIG. 34 is a cross-sectional view showing the configuration of the rotation position detecting mechanism 232. FIG. 35A is a diagram showing a non-detection state of the rotational position detecting mechanism 232. FIG. 35B is a diagram showing a detection state of the rotation position detecting mechanism 232. Fig. 36A is a waveform diagram showing an output signal S of the light receiving element 268 of the rotation position detecting mechanism 232. 3B are waveform diagrams of the pulse signal P output from the rotation position determination circuit 270. FIG. Fig. 37 is a flowchart illustrating a rotational position control process performed by the control circuit. Figure 38 is a cross-sectional view of the installation location of the windows 75, 76 seen from above. Figure 39 is a cross-sectional view of the enlarged display window 75. Fig. 40 is a cross-sectional view of the enlarged display window 76. FIG. 41A is a plan view showing the structure of the lower case 102. FIG. FIG. 41B is a side view showing the structure of the lower case 102. FIG. FIG. 42A is a plan view showing the configuration of the side box body 104. FIG. FIG. 42B is a front view showing the structure of the side box body 104. FIG. FIG. 42C is a rear view showing the configuration of the side box body 104. FIG. FIG. 42D is a left side view showing the structure of the side box 104. FIG. 42E is a right side view showing the structure of the side box 104. FIG. FIG. 43A is a bottom view showing the structure of the upper case 106. FIG. FIG. 43B is a side view showing the structure of the upper case 106. FIG. FIG. 44A is a plan view showing the configuration of the cylindrical case 108. FIG. O: \ 87 \ 87879.DOC -62- 200421433 Fig. 44B is a side longitudinal sectional view showing the configuration of the cylindrical box body 108. Fig. 44C is a side view showing the structure of the cylindrical case 108. FIG. 45 is a longitudinal sectional view showing the lift lever mechanism 30 in an enlarged manner. The figure is an enlarged longitudinal sectional view showing a sealing structure of the lift lever mechanism 30. FIG. 47A is a side view and a plan view showing a situation where radical oxidation of the substrate to be processed and the plate W is performed using the substrate processing apparatus 20 of FIG. 2. The figure key is a plan view showing the structure of FIG. 47A. Fig. 48 is a diagram showing the substrate oxidation processing steps performed using the substrate processing apparatus 20. Fig. 49 is a diagram showing a method for measuring the film thickness of xps used in accordance with the present invention. Fig. 50 is another diagram showing a method for measuring the film thickness of xps used in accordance with the present invention. Fig. 51 is a diagram schematically showing a stagnation phenomenon of the oxide film thickness growth observed when the oxide film is formed by the substrate processing apparatus 20. FIG. 52A is a diagram showing an oxide film formation process 1 on the surface of a silicon substrate. 52 FIG. 52B is a diagram showing an oxide film forming process 2 on the surface of a silicon substrate. Fig. 53 is a graph showing the leakage current characteristics of the obtained oxide film in the first embodiment of the present invention. -Figure 54A is a diagram explaining the cause of the leakage current characteristic of Figure 53. FIG. 54B is a diagram explaining the cause of the leakage current characteristic of FIG. 53. Fig. 55A is a view showing the oxide film forming step 1 generated in the substrate processing apparatus 20. FIG. 55B is a diagram showing step 2 of the oxide film formation step O: \ 87 \ 87879.DOC -63- 200421433 generated in the substrate processing apparatus 20. Fig. 55C is a view showing the oxide film forming step 3 generated in the substrate processing apparatus 20. Fig. 56 is a diagram showing the composition of a remote plasma source used in the substrate processing apparatus 20. Figure 57 is a graph comparing the characteristics of RF long-range plasma and microwave plasma. Fig. 58 is another graph comparing the characteristics of RF long-range plasma and microwave plasma. Fig. 59A is a side view showing the nitriding treatment of the oxide film using the s-plate processing apparatus 20. FIG. 28 is a plan view showing the nitriding treatment of the oxide film using the substrate processing apparatus 2G. FIG. 60A shows the use of a long-range plasma unit 27 under the conditions shown in Table 2 on a 2.0⑽ thick emulsified film formed by a thermo-oxidation process on a burrowing substrate ^ processing device ⑼ on a broken substrate, when nitriding. The nitrogen concentration profile in the aforementioned oxide film. The figure just shows the relationship between the nitrogen concentration distribution and the oxygen concentration distribution in the same oxide film. Fig. 61 is a schematic diagram showing an XPS used in the present invention. The series 2 and 2 show the relationship between the nitriding time of the plasma plasma and the disorder / occurrence in the film. The relationship between the nitriding time and the nitrogen distribution inside the film is shown in Fig. 0 ~ A ~ A chapter of the arduous process of the film. Fig. 65 is a diagram showing the effect of nitriding treatment on the oxide film of this embodiment.

O:\87\87879.DOC -64- 200421433 加圖。 【圖式代表符號說明】 10半導體裝置 11 Si基板 12基底氧化膜 12 A氧氮化膜 13高電介質膜 14 問極電極 20基板處理裝置 22處理容器 22a前部 22b後部 22c底部 22d左側面 22e 右側面 22g供給口 24加熱部 26紫外線照射部 26a筐體 26b底部開口 26c 邊緣部 27遠距離電漿部 27a氣體循環通路 27b 氣體入口 128 馬達 128a驅動軸 130磁鐵聯結器 132昇降臂 134 昇降軸 136 驅動部 138a〜138c抵接銷 140 凸緣 142 中央孔 144 第1水路 146 第1凸緣 146a L字形之連通孔 146b 階狀部 148 第2凸緣 150 第2水路 152第1流入管路 154 第1流入口 156流出管路 158 第1流出口 160螺栓 162安裝孔 164溫度感應器 O:\87\87879.DOC -65- 200421433 27c 氣體出口 27d 氟素樹脂加工 27e離子過濾器 27A 區塊 27B鐵氧體磁心 27C電漿 28 旋轉驅動部 30升降桿機構 32排氣路徑 32a 開口部 32b 錐形部 32c底部 32d主排氣管 32e排出口 32f 下部 32g分流用排出口 34氣體供給部 36框 38底部框 40,41 垂直框 40a電纜線導管 41a排氣導管 42中間框 44 上部框 166a〜166f電源纜線連接用端子 170 第2流入口 174 第2流出口 176栓 178位置決定孔 180密封構件(0環) 182密封構件(0環) 184密封構件(0環) 186密封構件(0環) 188密封構件(0環) 190 夾鉗機構 190a外筒 190b 轴 192螺旋彈簧 193 螺母 195墊片 196發熱控制電路 197, 199 L字形墊片 197a,199a圓筒部 197b,199b 突出部 197c,197d 圓筒部 198溫度調整器 200 電源 201幫浦 O:\87\87879.DOC -66 - 200421433 46 冷卻水供給部 48a,48b 電磁閥之排氣用閥 50渦輪分子幫浦 50a 吐出管 51真空管路 51a分流管路 52 電源單位 57 UV燈控制器 58氣體管路 60緊急停止開關 62托架 64溫度調整器 66氣體箱 68離子測量控制器 70 APC控制器 72 TMP控制器 74排氣口 75 第1窗口 76 第2窗口 77感應器單元 80 室 80a貫通孔 82蓋子構件 84製程空間(處理空間) 202排氣管路 204排氣管路 205壓力計 206 閥 208分歧管路 210 閥 211 可變隔膜 212 閥 214壓力計 216渦輪管路 218 逆止閥 220 隔膜 222 閥 230托架 230a冷卻水用之水路 230b冷卻水供給孔 230c冷卻水供給排出孔 230d 中央孔 230e,230f貫通孔 232旋轉位置檢測機構 234托架冷卻機構 236, 237 陶瓷軸承 238 凸緣 240螺栓 O:\87\87879.DOC -67- 200421433 85感應器單元 85a〜85c壓力計 86, 87外線光源(紫外線光源) 88透明窗 88a 密封面 88b防護罩 89密封構件(0環) 90供給管路 91鎖緊構件 92供給口 93氣體喷射喷嘴部 93al〜93an 喷射口 93bl〜93b3 喷嘴板 93cl〜93c3 凹部 93dl〜93d3供給孔 94搬送口 96閘極閥 97a第1質量控制器 97b第2質量控制器 98搬送自動機 991〜995 氣體供給管路 100石英墊圈 102 下部盒體 104側面盒體 242 凸緣 244 間隔壁 246排氣孔 248 從動側磁鐵 250磁鐵罩 252氛圍側旋轉部 252a下端部 254,255 轴承 256 驅動側磁鐵 257傳達構件 258旋轉檢測單元 260,261 狹縫板 262, 263 光斷續器 264軸承架 266發光元件 268 受光元件 268 受光元件 270旋轉位置判定電路 272 透明石英 274 UV玻璃 276 窗口安裝部 277 小螺釘 278 第1窗框 280密封構件 O:\87\87879.DOC -68- 200421433 104a 正面 282 第2窗框 104b 背面 284 小螺釘 106 上部盒體 286 開口 108 圓筒狀盒體 292 透明石英 108a〜108c 凹部 294 UV玻璃 108d 突起 296 窗口安裝部 110 底座 297 小螺釘 112 石英鐘罩 298 第1窗框 112a 突出部 300 密封構件(0環) 112b 圓筒部 302 第2窗框 112c 頂板 304 小螺釘 112d 中空部 310 圓形開口 112e 梁部 310a〜310c 凹部 112f 穿插孔 310d 凹部 112g〜112i輪轂 312 開口 (長方形) 113 内部空間 314a,314b 突起 114 SiC加熱器 3151 階狀部 114a 第1發熱部 316 狹縫 114b,114c第2,第3發熱部 317 開口 114d 穿插孔 318 凹部 114e 穿插孔 319 圓形孔 116 熱反射構件(反射器) 320〜322 孔 116a 穿插孔 324, 325 長方形開口 118 SiC基板設置台(加熱構件) 326 階狀部 O:\87\87879.DOC -69- 200421433 119 高溫計 120保持構件 120a〜120c 臂部 120d保持構件 120e〜120g輪轂 120i倒角加工部 122 外殼 124 内部空間 126 陶瓷軸 327〜329 圓形孔 330 四角孔 332伸縮管 334螺栓 336連接構件 338 陶瓷蓋 340蓋子構件 411 矽基板 412氧化膜 441 矽基板 442氧化膜 443 ZrSiOx O:\87\87879.DOC -70-O: \ 87 \ 87879.DOC -64- 200421433 [Illustration of Symbols] 10 semiconductor device 11 Si substrate 12 base oxide film 12 A oxynitride film 13 high dielectric film 14 interrogator electrode 20 substrate processing device 22 processing container 22a front 22b rear 22c bottom 22d left side 22e right side Surface 22g supply port 24 heating section 26 ultraviolet irradiation section 26a housing 26b bottom opening 26c edge section 27 remote plasma section 27a gas circulation path 27b gas inlet 128 motor 128a drive shaft 130 magnet coupling 132 lift arm 134 lift shaft 136 drive Parts 138a ~ 138c abutment pin 140 flange 142 center hole 144 first water passage 146 first flange 146a L-shaped communication hole 146b stepped portion 148 second flange 150 second water passage 152 first inflow pipe 154 first Inflow inlet 156 Outflow pipe 158 First outlet 160 Bolt 162 Mounting hole 164 Temperature sensor O: \ 87 \ 87879.DOC -65- 200421433 27c Gas outlet 27d Fluoro resin processing 27e Ion filter 27A Block 27B Ferrite Body core 27C Plasma 28 Rotary drive unit 30 Lifting rod mechanism 32 Exhaust path 32a Opening portion 32b Conical portion 32c Bottom 32d Main exhaust pipe 32e Discharge outlet 32f Lower 32g Diversion discharge outlet 34 Body supply section 36 frame 38 bottom frame 40, 41 vertical frame 40a cable duct 41a exhaust duct 42 middle frame 44 upper frame 166a to 166f terminal for power cable connection 170 second inlet 174 second outlet 176 plug 178 position Decision hole 180 seal member (0 ring) 182 seal member (0 ring) 184 seal member (0 ring) 186 seal member (0 ring) 188 seal member (0 ring) 190 clamp mechanism 190a outer cylinder 190b shaft 192 coil spring 193 Nut 195 Gasket 196 Heating control circuit 197, 199 L-shaped gasket 197a, 199a Cylindrical part 197b, 199b Protruded part 197c, 197d Cylindrical part 198 Temperature regulator 200 Power supply 201 Pump O: \ 87 \ 87879.DOC- 66-200421433 46 Cooling water supply unit 48a, 48b Exhaust valve for solenoid valve 50 Turbo molecular pump 50a Discharge pipe 51 Vacuum line 51a Divert line 52 Power supply unit 57 UV lamp controller 58 Gas line 60 Emergency stop switch 62 Bracket 64 temperature regulator 66 gas box 68 ion measurement controller 70 APC controller 72 TMP controller 74 exhaust port 75 first window 76 second window 77 sensor unit 80 chamber 80a through hole 82 cover member 84 process space ( Processing space) 202 Exhaust line 204 exhaust line 205 pressure gauge 206 valve 208 branch line 210 valve 211 variable diaphragm 212 valve 214 pressure gauge 216 turbine line 218 check valve 220 diaphragm 222 valve 230 bracket 230a water circuit for cooling water 230b cooling water supply hole 230c cooling water supply discharge hole 230d central hole 230e, 230f through hole 232 rotation position detection mechanism 234 bracket cooling mechanism 236, 237 ceramic bearing 238 flange 240 bolt O: \ 87 \ 87879.DOC -67- 200421433 85 Sensor unit 85a ~ 85c Pressure gauge 86, 87 Outside light source (ultraviolet light source) 88 Transparent window 88a Sealing surface 88b Protective cover 89 Sealing member (0 ring) 90 Supply line 91 Locking member 92 Supply port 93 Gas injection nozzle Part 93al ~ 93an Injection port 93bl ~ 93b3 Nozzle plate 93cl ~ 93c3 Concave part 93dl ~ 93d3 Supply hole 94 Transfer port 96 Gate valve 97a 1st quality controller 97b 2nd quality controller 98 Transportation robot 991 ~ 995 Gas supply line 100 Quartz washer 102 Lower case 104 Side case 242 Flange 244 Partition wall 246 Exhaust hole 248 Driven side magnet 250 Magnet cover 252 Atmosphere side rotation part 252a Lower end part 254, 255 Bearing 256 Drive side magnet 257 transmission member 258 rotation detection unit 260,261 slit plate 262, 263 photointerrupter 264 bearing frame 266 light emitting element 268 light receiving element 268 light receiving element 270 rotation position determination circuit 272 transparent quartz 274 UV glass 276 window mounting portion 277 small screw 278 1 Window frame 280 sealing member O: \ 87 \ 87879.DOC -68- 200421433 104a Front side 282 Second window frame 104b Back side 284 Small screw 106 Upper case 286 Opening 108 Cylindrical case 292 Transparent quartz 108a ~ 108c Recess 294 UV glass 108d protrusion 296 window mounting portion 110 base 297 small screw 112 quartz bell cover 298 first window frame 112a protruding portion 300 sealing member (0 ring) 112b cylindrical portion 302 second window frame 112c top plate 304 small screw 112d hollow portion 310 circle Shaped opening 112e beam portion 310a ~ 310c recessed portion 112f through hole 310d recessed portion 112g ~ 112i hub 312 opening (rectangular) 113 internal space 314a, 314b protrusion 114 SiC heater 3151 stepped portion 114a first heating portion 316 slit 114b, 114c The second and third heating parts 317 opening 114d through hole 318 recessed 114e through hole 319 round hole 116 heat reflecting member ( Reflector) 320 ~ 322 holes 116a Through holes 324, 325 Rectangular openings 118 SiC substrate setting table (heating member) 326 Stepped portion O: \ 87 \ 87879.DOC -69- 200421433 119 Pyrometer 120 holding member 120a ~ 120c Arm 120d holding member 120e ~ 120g hub 120i chamfering processing part 122 housing 124 internal space 126 ceramic shaft 327 ~ 329 round hole 330 square hole 332 telescopic tube 334 bolt 336 connection member 338 ceramic cover 340 cover member 411 silicon substrate 412 oxidation Film 441 Silicon substrate 442 Oxide film 443 ZrSiOx O: \ 87 \ 87879.DOC -70-

Claims (1)

200421433 拾、申請專利範園: 一種基板處理裝置,其特徵係具備有·· 内部劃分有處理空間之處理容器、 將被插入於前述處理空間 溫度之加熱部、 ’之破處理基板加熱至特定 现极羼理基板於前 件 述加熱部之上方之保持構 轉動驅動貫通前述加熱部之前 動驅動手段、 ?醫之軸之車 由前述處理容器之一側,向著 义 石散1乐符於刚迹保持構辦 之别述被處理基板,噴射氣體之氣體噴射部、 及設置於前述處理容器之另一側, 徘出通過前述被處 理基板之氣體之排氣口。 2. 3.200421433 Patent application park: A substrate processing device, which is equipped with a processing container with a processing space internally divided, a heating unit inserted at the temperature of the processing space, and a broken processing substrate heated to a specific temperature. The holding mechanism of the substrate on the heating unit above the heating part of the previous part is rotated to drive the driving means before passing through the heating part,? The car of the medical axis is from one side of the aforementioned processing container, and is scattered toward the right stone. A musical note is held on the other substrate to be processed, and a gas injection part for spraying gas is provided on the other side of the aforementioned processing container. Exhaust the gas exhaust port passing through the substrate to be processed. twenty three. 如申請專利範圍第丨項之基板處理裝置,其中 前述氣體噴射部係於水平方向成—列配置複數個氣 體噴射口。 如申請專利範圍第2項之基板處理裝置,其中 於f述處理容器之㈣面設置向著前述處理空間開 口之刖述複數個氣體噴射口。 4·如申請專利範圍第2項之基板處理裝置,其中 前述氣體噴射部係於前述處理容器之壁面,設置具有 複數個氣體喷射口之噴嘴構件。 5 ·如申請專利範圍第4項之基板處理裝置,其中 於前述處理容器之壁面設置前述噴嘴構件,使其由前 O:\87\87879.DOC 200421433 述被處理基板外周 空間噴射氣體。 之側方向著前述被處理基板之上部 6 ·如申明專利範圍第1項之基板處理裝置,其中 前述氣體噴射部連接有個別供給不同種類之氣體之 複數個氣體供給管路。 7·如申請專利範圍第6項之基板處理裝置,其中 前述複數個氣體供給管路,係各自藉由質流控制器安 定供給流量被控制之特定流量之氣體。 8·如申請專利範圍第2項之基板處理裝置,其中 ,前述複數個氣體喷射口連接有個別供給各自不同種 類之氣體之複數個氣體供給管路。 9·如申請專利範圍第8項之基板處理裝置,其中 前述複數個氣體供給管路,係各自藉由質流控制器安 定供給流量被控制之特定流量之氣體。 1〇·如申請專利範圍第1項之基板處理裝置,其中 月’J述排氣口係形成為較前述被處理基板之寬度更寬 之長方形。 11·如申請專利範圍第丨項之基板處理裝置,其中 前述排氣口係被連通至延伸於較前述處理容器之另 一側之底部更下方處之排氣途徑。 O:\87\87879.DOCFor example, the substrate processing apparatus of the scope of application for a patent, wherein the above-mentioned gas ejection sections are arranged in a row in a horizontal direction and a plurality of gas ejection ports are arranged. For example, the substrate processing apparatus according to item 2 of the patent application, wherein a plurality of gas injection ports opening to the processing space are provided on a surface of the processing container. 4. The substrate processing apparatus according to item 2 of the scope of patent application, wherein the gas injection unit is provided on a wall surface of the processing container, and a nozzle member having a plurality of gas injection ports is provided. 5. The substrate processing apparatus according to item 4 of the scope of patent application, wherein the aforementioned nozzle member is provided on the wall surface of the processing container, so that the gas is sprayed from the outer space of the substrate to be processed as described in O: \ 87 \ 87879.DOC 200421433. The side faces the upper part of the substrate to be processed. 6 The substrate processing device as described in the first patent scope, wherein the gas injection section is connected to a plurality of gas supply lines that individually supply different types of gas. 7. The substrate processing apparatus according to item 6 of the scope of patent application, wherein the plurality of gas supply lines are each a gas whose specific flow is controlled by a mass flow controller to stabilize the supply flow. 8. The substrate processing apparatus according to item 2 of the scope of the patent application, wherein the plurality of gas injection ports are connected to a plurality of gas supply lines that individually supply different kinds of gases. 9. The substrate processing apparatus according to item 8 in the scope of the patent application, wherein the plurality of gas supply lines are gasses with a specific flow rate controlled by a mass flow controller. 10. The substrate processing apparatus according to item 1 of the scope of patent application, wherein the exhaust port described above is formed in a rectangular shape wider than the width of the substrate to be processed. 11. The substrate processing apparatus according to item 丨 of the patent application scope, wherein the exhaust port is connected to an exhaust path extending below the bottom of the other side of the processing container. O: \ 87 \ 87879.DOC
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