TWI785510B - Substrate processing apparatus, semiconductor device manufacturing method, and recording medium - Google Patents
Substrate processing apparatus, semiconductor device manufacturing method, and recording medium Download PDFInfo
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
- H01L21/02—Manufacture or treatment of semiconductor devices or of parts thereof
- H01L21/04—Manufacture or treatment of semiconductor devices or of parts thereof the devices having at least one potential-jump barrier or surface barrier, e.g. PN junction, depletion layer or carrier concentration layer
- H01L21/18—Manufacture or treatment of semiconductor devices or of parts thereof the devices having at least one potential-jump barrier or surface barrier, e.g. PN junction, depletion layer or carrier concentration layer the devices having semiconductor bodies comprising elements of Group IV of the Periodic System or AIIIBV compounds with or without impurities, e.g. doping materials
- H01L21/30—Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26
- H01L21/31—Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26 to form insulating layers thereon, e.g. for masking or by using photolithographic techniques; After treatment of these layers; Selection of materials for these layers
Abstract
本發明提供一種技術,其具備:對基板進行處理之處理室;將複數之基板於垂直方向上多段保持的基板支撐具;與電漿生成部,其設於處理室內,具有將氣體進行電漿化之緩衝構造、與外部電極,該外部電極係設於與設有該緩衝構造之位置對應之上述處理室之外側並生成電漿。The present invention provides a technique comprising: a processing chamber for processing a substrate; a substrate supporter for holding a plurality of substrates vertically in multiple stages; The buffer structure and the external electrode are arranged outside the above-mentioned processing chamber corresponding to the position where the buffer structure is installed, and generate plasma.
Description
本發明係關於基板處理裝置、半導體裝置之製造方法及記錄媒體。The present invention relates to a substrate processing device, a method for manufacturing a semiconductor device, and a recording medium.
作為半導體裝置之製造步驟之一,有對搬入至基板處理裝置之處理室內的基板,使原料氣體或反應氣體等藉電漿活性化並供給,於基板上形成絕緣膜或半導體膜、導體膜等各種膜,或者去除各種膜的基板處理。例如,專利文獻1係於反應管內設有生成電漿之緩衝室。 [先前技術文獻] [專利文獻]As one of the manufacturing steps of a semiconductor device, the substrate carried into the processing chamber of the substrate processing device is activated and supplied with a raw material gas or a reactive gas by plasma, and an insulating film, a semiconductor film, a conductive film, etc. are formed on the substrate. Various films, or substrate processing to remove various films. For example, in Patent Document 1, a buffer chamber for generating plasma is provided in the reaction tube. [Prior Art Literature] [Patent Document]
專利文獻1:日本專利特開2016-106415號公報Patent Document 1: Japanese Patent Laid-Open No. 2016-106415
(發明所欲解決之問題)(Problem to be solved by the invention)
本發明之目的在於提供可對基板供給依高效率形成之電漿活性種氣體的技術。 (解決問題之技術手段)An object of the present invention is to provide a technology capable of supplying a plasma active species gas formed with high efficiency to a substrate. (technical means to solve the problem)
根據本發明之一態樣,提供一種技術,其係具有: 對基板進行處理之處理室; 將複數之上述基板於垂直方向上多段保持的基板支撐具;與 電漿生成部,其設於上述處理室內,具有將氣體進行電漿化之緩衝構造、與外部電極,該外部電極係設於與設有該緩衝構造之位置對應之上述處理室之外側並生成電漿。 (對照先前技術之功效)According to one aspect of the present invention, a technology is provided, which has: A processing chamber for processing substrates; A substrate support for holding a plurality of the above-mentioned substrates vertically in multiple stages; and The plasma generation part is provided in the above-mentioned processing chamber, and has a buffer structure for plasmaizing the gas, and an external electrode. Plasma. (compared to the effect of previous technology)
根據本發明,能提供可對基板供給依高效率形成之電漿活性種氣體的技術。According to the present invention, it is possible to provide a technology capable of supplying a plasma active species gas formed with high efficiency to a substrate.
<本發明之實施形態> 以下針對本發明一實施形態,參照圖1至圖5進行說明。<Embodiment of the present invention> An embodiment of the present invention will be described below with reference to FIGS. 1 to 5 .
(1) 基板處理裝置之構成(加熱裝置)
如圖1所示,基板處理裝置所使用之處理爐202係可將基板於垂直方向上多段收容的所謂縱型爐,具有作為加熱裝置(加熱機構)之加熱器207。加熱器207為圓筒形狀,由作為保持板之加熱器基底(未圖示)所支撐而垂直豎立。加熱器207亦具有作為如後述般藉由熱使氣體活性化(激發)之活性化機構(激發部)的機能。(1) Composition of substrate processing equipment (heating equipment)
As shown in FIG. 1 , the
(處理室)
於加熱器207內側,與加熱器207呈同心圓狀地配設反應管203。反應管203係由例如石英(SiO2
)或碳化矽(SiC)等耐熱性材料所構成,形成為上端閉塞、下端開口的圓筒形狀。於反應管203之下方,與反應管203呈同心圓狀地配設岐管(入口凸緣)209。岐管209係由例如不鏽鋼(SUS)等金屬所構成,形成為上端及下端開口的圓筒形狀。於岐管209之上端部,卡合於反應管203之下端部,構成為支撐反應管203。於岐管209與反應管203之間,設有作為密封構件的O型環220a。岐管209係由加熱器基底所支撐,藉此反應管203成為垂直豎立之狀態。主要由反應管203與岐管209構成處理容器(反應容器)。於處理容器內側之筒中空部形成處理室201。處理室201係構成為可收容複數片之作為基板之晶圓200。又,處理容器並不限定於上述構成,亦有僅將反應管203稱為處理容器的情形。(Processing Chamber) Inside the
於處理室201內,噴嘴249a、配管249b係設置成貫通岐管209之側壁。於噴嘴249a、配管249b,分別連接氣體供給管232a、232b。如此,於處理室201中設有1根噴嘴249a、1根配管249b、與2根氣體供給管232a、232b,可對處理室201內供給複數種氣體。In the
於氣體供給管232a、232b,由氣流之上游側起依序分別設置屬於流量控制器(流量控制部)之質量流量控制器(MFC)241a、241b及屬於開關閥之閥243a、243b。在氣體供給管232a、232b之較閥243a、243b更下游側,分別連接供給惰性氣體的氣體供給管232c、232d。於氣體供給管232c、232d,由氣流之上游側起依序分別設置MFC241c、241d及閥243c、243d。Mass flow controllers (MFC) 241a, 241b belonging to flow controllers (flow control parts) and
如圖2所示般,噴嘴249a係在反應管203之內壁與晶圓200之間的空間中,設置成由反應管203內壁之下部沿著上部、朝晶圓200之積載方向上方立起。亦即,噴嘴249a係依在晶圓200所配列(載置)之晶圓配列區域(載置區域)之側方中、水平包圍晶圓配列區域之區域,沿著晶圓配列區域的方式設置。亦即,噴嘴249a係於被搬入至處理室201內之各晶圓200之端部(周緣部)的側方,設置成與晶圓200之表面(平坦面)呈垂直的方向上。於噴嘴249a之側面,設置供給氣體之氣體供給孔250a。氣體供給孔250a係朝反應管203之中心呈開口,可朝晶圓200供給氣體。氣體供給孔250a係由反應管203之下部涵括至上部而複數設置,分別具有相同之開口面積,並依相同之開口間距設置。As shown in FIG. 2 , the
於氣體供給管232b之前端部,連接配管249b。配管249b係連接至緩衝構造237內。本實施形態中,俯視下2個之緩衝構造237係包夾著通過反應管203(處理室201)中心與噴嘴249a之直線而配置,或包夾著通過反應管203(處理室201)中心與排氣管(排氣部)231之直線而配置,相對於連結噴嘴249a與排氣管231之線使2個緩衝構造237對稱地配置。於緩衝構造237設有區隔板237a,藉由區隔板237a區隔為由配管249b導入氣體之氣體導入區237b與將氣體電漿化之電漿區237c。電漿區237c亦稱為屬於氣體分散空間的緩衝室237c。緩衝室237c係配置於噴嘴249a側,氣體導入區237b係配置於排氣管231側。The
如圖2所示般,緩衝室237c係在反應管203之內壁與晶圓200之間於俯視時呈圓環狀之空間中、且由反應管203內壁之下部涵括至上部的部分,沿著晶圓200之積載方向設置。亦即,緩衝室237c係依在晶圓配列區域之側方、水平包圍晶圓配列區域之區域,沿著晶圓配列區域的方式,由緩衝構造237所形成。緩衝構造237係由石英或SiC等屬於耐熱性材料之絕緣物所構成,於緩衝構造237之形成為圓弧狀的壁面,形成有供給氣體之氣體供給口302、304。氣體供給口302、304係於所積載之複數片晶圓200之水平方向上複數設置,朝反應管203之中心開口,可朝晶圓200供給氣體。氣體供給口302、304係由反應管203之下部涵括至上部、沿著晶圓200之積載方向複數設置,分別具有相同之開口面積,並依相同開口間距設置。As shown in FIG. 2 , the
於氣體導入區237b係設置成由反應管203內壁之下部沿著上部、朝晶圓200之積載方向上方立起。於區隔板237a,設有由氣體導入區237b對電漿區237c供給氣體的氣體供給孔237d。藉此,使供給至氣體導入區237b之反應氣體於緩衝室237c內分散。氣體供給孔237d係與氣體供給孔250a同樣地,由反應管203之下部涵括至上部複數設置。又,亦可取代配管249b及氣體導入區237b,將噴嘴、例如與噴嘴249a同樣之多孔噴嘴設於緩衝室237c內而供給處理氣體。The
如此,本實施形態中,係經由在由反應管203之側壁內壁、與配置於反應管203內之複數片晶圓200之端部所定義的俯視下呈圓環狀的縱長空間內(亦即圓筒狀之空間內)所配置的噴嘴249a及緩衝室237c,搬送氣體。然後,由在噴嘴249a與緩衝室237c分別開口之氣體供給孔250a、氣體供給口302、304,在晶圓200附近首先使氣體噴出至反應管203內。然後,使反應管203內之氣體之主要流動,成為與晶圓200表面平行之方向、亦即水平方向。藉由此種構成,可對各晶圓200均勻地供給氣體,可提升形成於各晶圓200之膜之膜厚均勻性。於晶圓200表面上流動的氣體、亦即反應後之剩餘氣體係朝排氣口、亦即後述排氣管231之方向流動。惟,此剩餘氣體之流動方向係由排氣口之位置所適當特定,並不限定於垂直方向。In this way, in the present embodiment, it passes through the circular ring-shaped vertical space defined by the inner wall of the side wall of the
由氣體供給管232a,係使含有既定元素之原料的例如含有作為既定元素之矽(Si)的矽烷原料氣體,經由MFC241a、閥243a、噴嘴249a供給至處理室201內。From the
所謂原料氣體,係指氣體狀態的原料,例如藉由將常溫常壓下呈液體狀態之原料氣化而得的氣體,或常溫常壓下呈氣體狀態之原料等。本說明書中,於使用「原料」一語時,係有意指「呈液體狀態之液體原料」之情形、意指「呈氣體狀態之原料氣體」之情形、或意指此等兩者之情形。The so-called raw material gas refers to a raw material in a gaseous state, such as a gas obtained by vaporizing a raw material that is in a liquid state at normal temperature and pressure, or a raw material that is in a gaseous state at normal temperature and pressure. In this specification, when the term "raw material" is used, it means the case of "liquid raw material in liquid state", the case of "raw material gas in gaseous state", or both of these cases.
作為矽烷原料氣體,可使用例如含有Si及鹵元素的原料氣體、亦即鹵矽烷原料氣體。鹵矽烷原料氣體係指具鹵基之矽烷原料。鹵元素係包含選自由氯(Cl)、氟(F)、溴(Br)、碘(I)所構成群之至少1種。亦即,鹵矽烷原料係含有選自由氯基、氟基、溴基、碘基所構成群之至少1種鹵基。鹵矽烷原料亦可謂為鹵化物之一種。As the silane source gas, for example, a source gas containing Si and a halogen element, that is, a halosilane source gas can be used. Halosilane raw material gas system refers to silane raw materials with halogen groups. The halogen element system contains at least one kind selected from the group consisting of chlorine (Cl), fluorine (F), bromine (Br), and iodine (I). That is, the halosilane raw material contains at least one halogen group selected from the group consisting of chlorine, fluorine, bromine, and iodine. Halosilane raw materials can also be described as a kind of halides.
作為鹵矽烷原料氣體,可使用例如含有Si及Cl之原料氣體、亦即氯矽烷原料氣體。作為氯矽烷原料氣體,可使用例如二氯矽烷(SiH2 Cl2 ,簡稱:DCS)氣體。As the halosilane source gas, for example, a source gas containing Si and Cl, that is, a chlorosilane source gas can be used. As the chlorosilane raw material gas, for example, dichlorosilane (SiH 2 Cl 2 , abbreviated: DCS) gas can be used.
由氣體供給管232b,構成為將作為含有與上述既定元素不同之元素的反應物(反應體)、例如作為反應氣體之含氮(N)氣體,經由MFC241b、閥243b、配管249b、氣體導入區237b供給至緩衝室237c內。作為含N氣體,可使用例如氮化氫系氣體。氮化氫系氣體亦稱為僅由N及H之2元素構成的物質,可作用為氮化氣體、亦即N源。作為氮化氫系氣體,可使用例如氨(NH3
)氣。The
由氣體供給管232c、232d,將作為惰性氣體之例如氮(N2
)氣分別經由MFC241c、241d、閥243c、243d、氣體供給管232a、232b、噴嘴249a、配管249b供給至處理室201內。From the
主要由氣體供給管232a、MFC241a、閥243a構成作為第1氣體供給系統的原料氣體供給系統。主要由氣體供給管232b、MFC241b、閥243b構成作為第2氣體供給系統的反應體供給系統(反應物供給系統)。主要由氣體供給管232c、232d、MFC241c、241d、閥243c、243d構成惰性氣體供給系統。亦將原料供給系統、反應體供給系統及惰性氣體供給系統總稱、簡稱為氣體供給系統(氣體供給部)。The raw material gas supply system which is a 1st gas supply system is comprised mainly by the
(電漿生成部) 接著使用圖1至圖3說明電漿生成部。(Plasma Generation Department) Next, the plasma generation unit will be described using FIGS. 1 to 3 .
如圖2所示,電漿係使用電容耦合電漿(Capacitively Coupled Plasma,簡稱:CCP),在反應氣體供給時於由石英等所製成之屬於真空隔壁的反應管203(處理室201)內部之緩衝構造237生成。As shown in Figure 2, the plasma system uses capacitively coupled plasma (CCP for short), and when the reaction gas is supplied, it is inside the reaction tube 203 (processing chamber 201) which is made of quartz and belongs to the vacuum partition. The
如圖2及圖3(a)所示,外部電極300係由於晶圓200之配列方向上具有長邊之矩形形狀的薄板所構成。如圖1及圖3(b)所示,外部電極300係使經由整合器272連接高頻電源273的第1外部電極(Hot電極)300-1、與基準電位0V並經大地接地之第2外部電極(接地電極)300-2依等間隔配置。本發明中,在不需要特別區別並說明的情況下,記載為外部電極300進行說明。As shown in FIG. 2 and FIG. 3( a ), the
外部電極300係於反應管203與加熱器207之間,設於與設有緩衝構造237之位置相對應的處理室201之外側。具體而言,緩衝構造係設置電漿區(緩衝室)237c作為用於將氣體電漿化之區,外部電極300係沿著與設有緩衝室237c之位置相對應的反應管203之外壁(處理室201之外側)並配置為略圓弧狀。外部電極300係例如固定於形成為中心角為30度以上且240度以下之圓弧狀的石英蓋之內壁面而配置。亦即,外部電極300係配置於與設有緩衝室(電漿區)237c之位置相對應之反應管203的外周(處理室201之外側)。又,緩衝構造237係設有氣體供給部(氣體導入區)237b作為用於對緩衝室237c供給氣體的區。外部電極300並未配置於與設有氣體導入區(氣體供給部)237b之位置相對應之反應管203的外周(處理室201之外側)。外部電極300係由高頻電源273經由整合器272,輸入例如頻率13.56MHz之高頻,藉此於緩衝室237c內生成電漿活性種306。藉由如此生成的電漿,可由晶圓200周圍將用於基板處理之電漿活性種306供給至晶圓200表面。主要由緩衝構造237與外部電極300與高頻電源273構成電漿生成部。The
外部電極300亦可由鋁或銅、不鏽鋼等金屬所構成,但藉由鎳等耐氧化材料構成,可抑制導電率劣化、可進行基板處理。尤其,藉由以添加了鋁之鎳合金材料構成,可於電極表面形成耐熱性及耐腐蝕性高之屬於氧化被膜的AlO膜。藉由此被膜形成的效果,可抑制劣化朝電極內部的進行,故可抑制因導電率降低所造成的電漿生成效率降低。The
(電極固定治具)
接著使用圖3,說明作為固定外部電極300之電極固定治具的石英蓋301。如圖3(a)、(b)所示,複數根設置之外部電極300,係將其缺口部(未圖示)掛扣於彎曲形狀之屬於電極固定治具之石英蓋301之內壁面所設置的突起部310,使其滑動並固定,依與此石英蓋301成為一體的方式進行單元化(鉤式電極單元)設置於反應管203外周。於此,包括外部電極300與屬於電極固定治具之石英蓋301在內稱為電極固定單元。又,作為石英蓋301與外部電極300之材料,分別採用石英與鎳合金。(Electrode Fixture)
Next, a
為了依基板溫度500℃以下獲得高處理能力,較佳係將石英蓋301之占有率設為中心角30度以上且240度以下之圓弧形狀,並為了避免發生顆粒而避開屬於排氣口之排氣管231或噴嘴249a等的配置。若構成為中心角小於30度,則所配置之外部電極300之根數變少,電漿之生產量減少。若構成為中心角大於240度,則由石英蓋301覆蓋反應管203側面的面積變得過大,而阻斷來自加熱器207的熱能量。本實施形態中,係將中心角110度之石英蓋2片配置成左右對稱。In order to obtain high processing capacity according to the substrate temperature below 500°C, it is preferable to set the occupancy rate of the
於反應管203,設有作為將處理室201內之環境進行排氣之排氣部的排氣管231。於排氣管231,係經由作為檢測處理室201內之壓力的壓力檢測器(壓力檢測部)的壓力感應器245、及經由作為排氣閥(壓力調整部)之APC(Auto Pressure Controller,自動壓力控制器)閥244,連接著作為真空排氣裝置的真空泵246。APC閥244係構成為:依使真空泵246作動之狀態進行閥之開關,而進行處理室201內之真空排氣及真空排氣停止;進而依使真空泵246作動之狀態,根據由壓力感應器245所檢測出之壓力資料進行閥開度調節,藉此可調整處理室201內之壓力。主要由排氣管231、APC閥244、壓力感應器245構成排氣系統。又,亦可將真空泵246視為含於排氣系統中。排氣管231並不限定於設置於反應管203的情況,亦可與噴嘴249a同樣地設於歧管209。The
於歧管209下方,設有可將岐管209下端開口氣密地閉塞之作為爐口蓋體的密封蓋219。密封蓋219係構成為對歧管209之下端由垂直方向下側抵接。密封蓋219係由例如SUS等金屬材所構成,並形成為圓盤狀。於密封蓋219上面,設有與岐管209下端抵接之作為密封構件的O型環220b。於密封蓋219之與處理室201相反側,設置使後述晶舟217旋轉的旋轉機構267。旋轉機構267之旋轉軸255係貫通密封蓋219而連接至晶舟217。旋轉機構267係構成為藉由使晶舟217旋轉而使晶圓200旋轉。密封蓋219係構成為藉由垂直設置於反應管203外部之作為升降機構的晶舟升降器115而於垂直方向升降。晶舟升降器115係構成為藉由使密封蓋219升降,而可將晶舟217於處理室201內外進行搬入及搬出。晶舟升降器115係構成為將晶舟217、亦即晶圓200於處理室201內外進行搬送的搬送裝置(搬送機構)。又,於歧管209下方,設置在藉由晶舟升降器115使密封蓋219下降的期間,可將歧管209之下端開口氣密地閉塞之作為爐口蓋體的擋門219s。擋門219s係由例如SUS等金屬所構成,並形成為圓盤狀。於擋門219s上面,設有與岐管209下端抵接之作為密封構件的O型環220c。擋門219s之開關動作(升降動作或旋動動作等)係由擋門開關機構115s所控制。Below the manifold 209, there is provided a sealing
(基板支撐具)
如圖1所示,作為基板支撐具之晶舟217係構成為使複數片、例如25~200片晶圓200以水平姿勢、且以彼此的中心對齊之狀態,於垂直方向上整齊排列而多段地支撐,亦即,隔著既定間隔而配列。晶舟217係由例如石英或SiC等耐熱性材料所構成。於晶舟217之下部係使例如以石英或SiC等耐熱性材料所構成之隔熱板218多段地支撐著。(substrate support)
As shown in FIG. 1 , the
如圖1所示,於反應管203內部,設置有作為溫度檢測器之溫度感應器263。根據藉由溫度感應器263檢測出之溫度資訊而調整對加熱器207之通電狀況,使處理室201內之溫度成為所需之溫度分佈。溫度感應器263與噴嘴249a同樣地沿著反應管203的內壁設置。As shown in FIG. 1 , inside the
(控制裝置)
接著使用圖4說明控制裝置。如圖4所示般,屬於控制部(控制裝置)之控制器121係構成為具備CPU(Central Processing Unit)121a、RAM(Random Access Memory)121b、記憶裝置121c、I/O埠121d的電腦。RAM 121b、記憶裝置121c、I/O埠121d係構成為經由內部匯流排121e而可與CPU 121a進行資料交換。於控制器121係連接有例如構成為觸控面板等之輸出入裝置122。(control device)
Next, the control device will be described using FIG. 4 . As shown in FIG. 4, the
記憶裝置121c係由例如快閃記憶體、HDD(Hard Disk Drive)等所構成。於記憶裝置121c內可讀取地儲存有控制基板處理裝置之動作的控制程式,或記載有後述成膜處理之手續或條件等的製程配方(recipe)等。製程配方係以將後述各種處理(成膜處理)中各手續藉控制器121執行,而可獲得既定之結果之方式組合者,作為程式而發揮機能。以下,亦將製程配方或控制程式等總稱、簡稱為程式。又,有時亦將製程配方簡稱為配方。本說明書中於使用程式一語的情況,係指僅含配方單體的情況、僅含控制程式單體的情況、或含有此等之兩者的情況。RAM121b係構成為使藉由CPU 121a讀出之程式或數據等暫時地保存之記憶區域(工作區域)。The
I/O埠121d係連接於上述MFC241a~241d、閥243a~243d、壓力感應器245、APC閥244、真空泵246、加熱器207、溫度感應器263、整合器272、高頻電源273、旋轉機構267、晶舟升降器115、擋門開關機構115s等。The I/
CPU121a係構成為自記憶裝置121c讀取控制程式並執行,且配合自輸出入裝置122之操作指令之輸入等由記憶裝置121c讀取配方。CPU 121a係構成為依照讀取之配方的內容控制:旋轉機構267之控制、利用MFC 241a~241d進行之各種氣體的流量調整動作、閥243a~243d的開關動作、基於阻抗監測之高頻電源273的調整動作、APC閥244之開關動作及基於壓力感應器245而利用APC閥244進行之壓力調整動作、真空泵246的啟動及停止、基於溫度感應器263之加熱器207的溫度調整動作、利用旋轉機構267進行之晶舟217的正反旋轉、旋轉角度及旋轉速度調節動作、利用晶舟升降機115進行之晶舟217的升降動作、利用高頻電源273及外部電極300進行之電漿生成等。The
控制器121係可藉由將由外部記憶裝置(例如硬碟等磁碟、CD等光碟、MO等磁光碟、USB記憶體等半導體記憶體)123所儲存之上述程式安裝到電腦中而構成。記憶裝置121c或外部記憶裝置123係構成為可被電腦讀取之記錄媒體。以下,亦將此等總稱、簡稱為記錄媒體。本說明書中於使用記錄媒體一語的情況,係指僅含記憶裝置121c單體的情況、僅含外部記憶裝置123單體的情況、或含有此等之兩者的情況。尚且,對電腦之程式提供,亦可不使用外部記憶裝置123,而使用網路或專用線路等通訊手段進行。The
(2)基板處理步驟
接著,使用基板處理裝置,作為半導體裝置的製造步驟之一步驟,針對於晶圓200上形成薄膜的步驟,參照圖5進行說明。以下的說明中,構成基板處理裝置之各部的動作係藉由控制器121所控制。(2) Substrate processing steps
Next, a step of forming a thin film on the
於此,針對藉由將供給DCS氣體作為原料氣體之步驟、供給經電漿激發之NH3
氣體作為反應氣體之步驟非同時、亦即非同期地進行既定次數(1次以上),於晶圓200上形成氮化矽膜(SiN膜)作為含Si及N之膜的例子進行說明。又,例如於晶圓200上亦可事先形成既定膜。又,於晶圓200或既定膜上亦可事先形成既定圖案。Here, by performing the step of supplying DCS gas as the source gas and the step of supplying plasma-excited NH 3 gas as the reaction gas a predetermined number of times (more than 1 time) at the same time, the wafer 200 A silicon nitride film (SiN film) formed thereon will be described as an example of a film containing Si and N. Also, for example, a predetermined film may be formed on the
本說明書中,為了方便亦如以下般表示圖5所示成膜處理之製程流程。 (DCS→NH3 * )×n => SiNIn this specification, the process flow of the film formation process shown in FIG. 5 is also shown as follows for convenience. (DCS→NH 3 * )×n => SiN
本說明書中於使用「晶圓」一語的情況,係有意指晶圓本身的情況、或意指晶圓與其表面所形成之既定之層或膜之積層體的情況。本說明書中於使用「晶圓表面」一語的情況,係有意指晶圓本身之表面的情況、或指晶圓上所形成之既定之層等之表面的情況。本說明書中於記載了「於晶圓上形成既定之層」的情況,係有意指於晶圓本身之表面上直接形成既定之層的情況、或意指對晶圓上所形成之層等之上形成既定之層的情況。本說明書中使用「基板」一語的情況,亦與使用「晶圓」一詞的情況具有相同意義。When the word "wafer" is used in this specification, it means the case of the wafer itself, or the case of the laminated body of the wafer and a predetermined layer or film formed on the surface thereof. When the term "wafer surface" is used in this specification, it means the surface of the wafer itself or the surface of a predetermined layer formed on the wafer. When "a predetermined layer is formed on the wafer" is described in this specification, it means that the predetermined layer is directly formed on the surface of the wafer itself, or it means that the layer formed on the wafer, etc. The situation where a predetermined layer is formed above. When the word "substrate" is used in this specification, it has the same meaning as when the word "wafer" is used.
(搬入步驟:S1)
將複數片之晶圓200裝填(晶圓充填)於晶舟217,藉由擋門開關機構115s使擋門219s移動,使歧管209之下端開口開放(擋門開放)。其後,如圖1所示般,支持著複數片之晶圓200的晶舟217,係被晶舟升降機115上舉並搬入至處理室201內(晶舟裝載)。於此狀態下,密封蓋219係經由O型環220b使岐管209之下端成為密封之狀態。(Move-in step: S1)
A plurality of
(壓力、溫度調整步驟:S2)
以使處理室201內部、亦即晶圓200所存在之空間成為所需壓力(真空度)之方式,藉由真空幫浦246進行真空排氣(減壓排氣)。此時,處理室201內之壓力係藉由壓力感應器245所測定,根據所測定之壓力資訊回饋控制APC閥244。真空泵246係至少在後述成膜步驟結束為止之期間維持經常作動的狀態。(Pressure and temperature adjustment step: S2)
Vacuum evacuation (decompression evacuation) is performed by the
又,以使處理室201內之晶圓200成為所需溫度之方式,藉由加熱器207加熱。此時,依處理室201內成為所需溫度分佈之方式,根據溫度感應器263所檢測出之溫度資訊,回饋控制對加熱器207的通電程度。藉由加熱器207進行之處理室201內的加熱係至少在後述成膜步驟結束為止之期間持續進行。其中,在成膜步驟為於室溫以下之溫度條件下進行時,亦可不藉由加熱器207進行處理室201內之加熱。又,在進行僅於此種溫度下之處理時,則不需要加熱器207,亦可不將加熱器207設置於基板處理裝置。此時,可使基板處理裝置之構成簡單化。
接著,開始利用旋轉機構267進行晶舟217及晶圓200之旋轉。利用旋轉機構267進行之晶舟217及晶圓200的旋轉係至少在成膜步驟結束為止之期間持續進行。Furthermore, the
(原料氣體供給步驟:S3、S4)
於步驟S3,對處理室201內之晶圓200供給DCS氣體。打開閥243a,於氣體供給管232a內流通DCS氣體。DCS氣體係藉由MFC241a進行流量調整,經由噴嘴249a由氣體供給孔250a供給至處理室201內,並由排氣管231被排氣。在此同時,打開閥243c,於氣體供給管232c內流通N2
氣體。N2
氣體係藉由MFC241c進行流量調整,與DCS氣體一起供給至處理室201內,並由排氣管231被排氣。(Source gas supply steps: S3, S4) In step S3, DCS gas is supplied to the
又,為了抑制DCS氣體侵入至配管249b內,打開閥243d,於氣體供給管232d內流通N2
氣體。N2
氣體係經由氣體供給管232b、配管249b供給至處理室201內,並由排氣管231被排氣。Moreover, in order to suppress the intrusion of DCS gas into the
由MFC241a所控制之DCS氣體的供給流量,係設為例如1sccm以上、6000sccm以下,較佳為3000sccm以上、5000sccm以下之範圍內的流量。藉由MFC241c、241d所控制之N2
氣體的供給流量,係分別設為例如100sccm以上、10000sccm以下之範圍內的流量。處理室201內之壓力係設為例如1Pa以上、2666Pa以下,較佳為665Pa以上、1333Pa以下之範圍內的壓力。晶圓200曝露於DCS氣體的時間,設為係例如每1周期為20秒左右之時間。又,晶圓200曝露於DCS氣體的時間係視膜厚而異。The supply flow rate of the DCS gas controlled by the
加熱器207之溫度係設定為使晶圓200之溫度成為例如0℃以上且700℃以下、較佳為室溫(25℃)以上且550℃、更佳為40℃以上且500℃以下之範圍內的溫度。如本實施形態,藉由將晶圓200之溫度設為700℃以下、進而550℃以下、進而500℃以下,可使施加至晶圓200的熱量減低,可良好地進行晶圓200所接受之熱履歷的控制。The temperature of the
藉由於上述條件下對晶圓200供給DCS氣體,於晶圓200(表面之基底膜)上,形成含Si層。含Si層係除了Si層之外,可含有Cl或H。含Si層係藉由於晶圓200之最表面使DCS物理吸附,或使DCS經部分分解之物質化學吸附,或DCS發生熱分解而使Si堆積等所形成。亦即,含Si層可為DCS或DCS經部分分解之物質的吸附層(物理吸附層或化學吸附層),亦可為Si之堆積層(Si層)。By supplying DCS gas to the
形成含Si層後,關閉閥243a,停止對處理室201內的DCS氣體供給。此時,維持APC閥244打開,藉由真空泵246將處理室201內進行真空排氣,將殘留於處理室201內之未反應或用於形成含Si層後之DCS氣體或反應副產物等自處理室201內排除(S4)。又,維持將閥243c、243d開啟,維持將N2
氣體供給至處理室201內。N2
氣體係作用為沖洗氣體。又,亦可省略此步驟S4。After forming the Si-containing layer, the
作為原料氣體,係除了DCS氣體之外,可適合使用肆二甲胺基矽烷(Si[N(CH3 )2 ]4 ,簡稱:4DMAS)氣體、參二甲胺基矽烷(Si[N(CH3 )2 ]3 H,簡稱:3DMAS)氣體、雙二甲胺基矽烷(Si[N(CH3 )2 ]2 H2 ,簡稱:BDMAS)氣體、雙二乙胺基矽烷(Si[N(C2 H5 )2 ]2 H2 ,簡稱:BDEAS)氣體、雙第三丁基胺基矽烷(SiH2 [NH(C4 H9 )]2 ,簡稱:BTBAS)氣體、二甲胺基矽烷(DMAS)氣體、二乙胺基矽烷(DEAS)氣體、二丙胺基矽烷(DPAS)氣體、二異丙胺基矽烷(DIPAS)氣體、丁胺基矽烷(BAS)氣體、六甲基二矽氮烷(HMDS)氣體等各種胺基矽烷原料氣體,或單氯矽烷(SiH3 Cl,簡稱MCS)氣體、三氯矽烷(SiHCl3 ,簡稱:TCS)氣體、四氯矽烷(SiCl4 ,簡稱:STC)氣體、六氯二矽烷(Si2 Cl6 ,簡稱:HCDS)氣體、八氯三矽烷(Si3 Cl8 ,簡稱:OCTS)氣體等之無機系鹵矽烷原料氣體,或 單矽烷(SiH4 ,簡稱:MS)氣體、二矽烷(Si2 H6 ,簡稱:DS)氣體、三矽烷(Si3 H8 ,簡稱:TS)氣體等之不含鹵基之無機系矽烷原料氣體。As the raw material gas, in addition to DCS gas, tetradimethylaminosilane (Si[N(CH 3 ) 2 ] 4 , abbreviation: 4DMAS) gas, paradimethylaminosilane (Si[N(CH 3 ) 2 ] 4 , 3 ) 2 ] 3 H, referred to as: 3DMAS) gas, bisdimethylaminosilane (Si[N(CH 3 ) 2 ] 2 H 2 , referred to as: BDMAS) gas, bisdiethylaminosilane (Si[N( C 2 H 5 ) 2 ] 2 H 2 , referred to as: BDEAS) gas, bis-tertiary butylaminosilane (SiH 2 [NH(C 4 H 9 )] 2 , referred to as: BTBAS) gas, dimethylaminosilane (DMAS) gas, diethylaminosilane (DEAS) gas, dipropylaminosilane (DPAS) gas, diisopropylaminosilane (DIPAS) gas, butylaminosilane (BAS) gas, hexamethyldisilazane (HMDS) gas and other aminosilane raw material gases, or monochlorosilane (SiH 3 Cl, referred to as MCS) gas, trichlorosilane (SiHCl 3 , referred to as: TCS) gas, tetrachlorosilane (SiCl 4 , referred to as: STC) gas Gas, hexachlorodisilane (Si 2 Cl 6 , abbreviated: HCDS) gas, octachlorotrisilane (Si 3 Cl 8 , abbreviated: OCTS) gas and other inorganic halosilane raw material gases, or monosilane (SiH 4 , abbreviated : MS) gas, disilane (Si 2 H 6 , abbreviation: DS) gas, trisilane (Si 3 H 8 , abbreviation: TS) gas, etc., are halogen-free inorganic silane raw material gases.
作為惰性氣體,除了N2 氣體之外,可使用Ar氣體、He氣體、Ne氣體、Xe氣體等稀有氣體。As the inert gas, in addition to N 2 gas, rare gases such as Ar gas, He gas, Ne gas, and Xe gas can be used.
(反應氣體供給步驟:S5、S6)
成膜處理結束後,對處理室201內之晶圓200供給作為反應氣體之經電漿激發的NH3
氣體(S5)。(Reactive gas supply steps: S5, S6) After the film formation process is completed, plasma-excited NH 3 gas is supplied as a reactive gas to the
於此步驟,係依與步驟S3中之閥243a、243c、243d之開關控制相同的手續,進行閥243b~243d之開關控制。NH3
氣體係藉由MFC241b進行流量調整,經由配管249b供給至緩衝室237c內。此時,對外部電極300供給高頻電力。供給至緩衝室237c內的NH3
氣體被激發為電漿狀態(進行電漿化而活性化),作為活性種(NH3
*)供給至處理室201內,並由排氣管231被排氣。In this step, the switching control of the
由MFC241b所控制之NH3
氣體的供給流量,係設為例如100sccm以上、10000sccm以下,較佳為1000sccm以上、2000sccm以下之範圍內的流量。施加於外部電極300之高頻電力係設為例如50W以上、600W以下之範圍內的電力。處理室201內之壓力係設為例如1Pa以上、500Pa以下之範圍內的壓力。藉由使用電漿,即使處理室201內之壓力為此種較低壓力帶,仍可使NH3
氣體活性化。將藉由使NH3
氣體進行電漿激發而得之活性種對晶圓200進行供給的時間、亦即氣體供給時間(照射時間)係設為例如1秒以上、180秒以下,較佳為1秒以上、60秒以下之範圍內的時間。其他處理條件係設為與上述S3相同的處理條件。The supply flow rate of NH 3 gas controlled by the
藉由於上述條件下對晶圓200供給NH3
氣體,使形成於晶圓200上之含Si層被電漿氮化。此時,藉由經電漿激發之NH3
氣體之能量,使含Si層所具有之Si-Cl鍵、Si-H鍵被切斷。經切開了與Si間之鍵結的Cl、H將由含Si層脫離。然後,藉由Cl等脫離,成為具有未鍵結基(懸鍵)的含Si層中之Si係與NH3
氣體所含之N鍵結,形成Si-N鍵。藉由此反應進行,使含Si層變化(改質)為含有Si及N的層、亦即氮化矽層(SiN層)。By supplying NH 3 gas to the
尚且,在使含Si層改質為SiN層時,需要使NH3 氣體電漿激發而供給。此係由於即使將NH3 氣體於非電漿環境下供給,於上述溫度帶,用於使含Si層氮化之必要能量不足,難以使Cl或H充分地由含Si層脫離、或難以使含Si層充分地氮化而使Si-N鍵結增加。Furthermore, when modifying the Si-containing layer to a SiN layer, it is necessary to excite and supply NH 3 gas plasma. This is because even if NH3 gas is supplied in a non-plasma environment, in the above temperature range, the necessary energy for nitriding the Si-containing layer is insufficient, and it is difficult to sufficiently detach Cl or H from the Si-containing layer, or it is difficult to make the Si-containing layer The Si-containing layer is sufficiently nitrided to increase Si-N bonding.
使含Si層變化為SiN層後,關閉閥243b,停止NH3
氣體之供給。又,停止對外部電極300的高頻電力之供給。然後,藉由與步驟S4相同的處理手續、處理條件,將殘留於處理室201內之NH3
氣體或反應副產物由處理室201內排除(S6)。又,亦可省略此步驟S6。After changing the Si-containing layer to a SiN layer, the
作為氮化劑、亦即被電漿激發之含N氣體,除了NH3 氣體之外,亦可使用二亞胺(N2 H2 )氣體、聯氨(N2 H4 )氣體、N3 H8 氣體等。As the nitriding agent, that is, the N-containing gas excited by the plasma, in addition to NH 3 gas, diimine (N 2 H 2 ) gas, hydrazine (N 2 H 4 ) gas, N 3 H 8 gas etc.
作為惰性氣體,除了N2 氣體之外,可使用例如步驟S4所例示之各種稀有氣體。As the inert gas, for example, various rare gases exemplified in step S4 can be used in addition to N 2 gas.
(實施既定次數:S7)
藉由將上述S3、S4、S5、S6依此順序非同時、亦即非同期地進行者設為1周期,將此周期進行既定次數(n次)、亦即1次以上(S7),可於晶圓200上形成既定組成及既定膜厚之SiN膜。上述周期較佳係重複複數次。亦即,較佳係使每周期所形成之SiN層之厚度小於所需膜厚,重複上述周期複數次直到藉由SiN層積層所形成之SiN膜之膜厚成為所需膜厚為止。(Implement the predetermined number of times: S7)
By setting the above-mentioned S3, S4, S5, and S6 in this order non-simultaneously, that is, asynchronously, as one cycle, and carrying out this cycle for a predetermined number of times (n times), that is, more than one time (S7), you can A SiN film with a predetermined composition and a predetermined film thickness is formed on the
(大氣壓恢復步驟:S8)
上述成膜處理結束後,分別由氣體供給管232c、232d將作為惰性氣體之N2
氣體供給至處理室201內,並由排氣管231排氣。藉此,以惰性氣體沖洗處理室201內,將殘留於處理室201內之氣體等由處理室201內去除(惰性氣體沖洗)。其後,將處理室201內之環境置換為惰性氣體(惰性氣體置換),處理室201內之壓力恢復為常壓(S8)。(Atmospheric Pressure Restoration Step: S8) After the above-mentioned film forming process is completed, N 2 gas as an inert gas is supplied into the
(搬出步驟:S9)
其後,藉由晶舟升降器115使密封蓋219下降,使岐管209之下端開口,並將處理完畢之晶圓200依被晶舟217支持之狀態從岐管209之下端搬出至反應管203的外部(晶舟卸載)(S9)。晶舟卸載後,使擋門219s移動,將岐管209之下端開口經由O型環220c藉由擋門219s密封(擋門關閉)。處理完畢之晶圓200被搬出至反應管203之外部後,由晶舟217取出(晶圓卸除)。尚且,晶圓卸除後,亦可將空的晶舟217搬入至處理室201內。(moving step: S9)
Thereafter, the sealing
(3)本實施形態之效果 根據本實施形態,可獲得以下所示1種或複數種效果。(3) Effects of this embodiment According to the present embodiment, one or more effects shown below can be obtained.
(a)藉由將外部電極設置於與將處理氣體進行電漿化之電漿生成部所形成位置相對應的反應管之外周,可藉由此外部電極將供給至反應管內之處理氣體利用電漿進行活性化,將此經活性化之處理氣體供給至基板。(a) By disposing the external electrode on the outer periphery of the reaction tube corresponding to the position where the plasma generation part for plasmaizing the processing gas is formed, the processing gas supplied into the reaction tube can be utilized by the external electrode The plasma is activated, and the activated process gas is supplied to the substrate.
(b)外部電極係設置於電漿生成部所形成之位置、且對電漿生成部供給氣體之氣體供給部除外的位置,藉此可防止氣體供給部內之電漿形成。(b) The external electrode is provided at the position where the plasma generation part is formed, except for the gas supply part that supplies gas to the plasma generation part, thereby preventing plasma formation in the gas supply part.
(c)沿著反應管之內壁設置緩衝室,於與緩衝室所設置之位置相對應的反應管之外周設置形成電漿的外部電極,藉由此外部電極將供給至緩衝室內之處理氣體以電漿進行活性化,將此經活性化之處理氣體供給至基板,藉此可於緩衝室內形成高效率之電漿,可對基板供給依高效率所形成的電漿活性種氣體。(c) A buffer chamber is arranged along the inner wall of the reaction tube, and an external electrode for forming plasma is arranged on the outer periphery of the reaction tube corresponding to the position where the buffer chamber is installed, and the processing gas supplied to the buffer chamber is supplied to the buffer chamber by the external electrode Activation is performed with plasma, and the activated processing gas is supplied to the substrate, whereby high-efficiency plasma can be formed in the buffer chamber, and the plasma active species gas formed with high efficiency can be supplied to the substrate.
(d)藉由使將經活性化之處理氣體供給至基板的處理氣體供給口朝向基板中央、於基板水平方向複數設置,可增加經電漿化之氣體對基板中央的供給量。(d) By making the processing gas supply port for supplying the activated processing gas to the substrate facing the center of the substrate and a plurality of them in the horizontal direction of the substrate, the supply amount of the plasmaized gas to the center of the substrate can be increased.
(e)於形成緩衝室之緩衝構造中,設有區隔板,藉由此區隔板區隔為處理氣體導入區與作為緩衝室之電漿區,可將處理氣體導入區與電漿區分離。(e) In the buffer structure forming the buffer chamber, a partition plate is provided, by which the partition plate is divided into the processing gas introduction area and the plasma area as the buffer chamber, and the processing gas introduction area and the plasma area can be separated separate.
(f)藉由於區隔板設置由處理氣體導入區對電漿區供給氣體的氣體供給孔,可依處理氣體導入區與電漿區分離之狀態,將處理氣體供給至電漿區。(f) By providing the gas supply hole for supplying gas from the process gas introduction area to the plasma area in the area partition plate, the process gas can be supplied to the plasma area according to the separation state of the process gas introduction area and the plasma area.
(g)於區隔板係設有對電漿區供給處理氣體的複數孔,由處理氣體導入區之下部供給處理氣體,並由複數孔對電漿區供給處理氣體,藉此可使緩衝室內之氣體濃度均勻化。(g) A plurality of holes for supplying processing gas to the plasma area are provided in the partition plate, the processing gas is supplied from the lower part of the processing gas introduction area, and the processing gas is supplied to the plasma area through the plurality of holes, so that the buffer chamber can The gas concentration is homogenized.
(h)藉由於與處理氣體導入區所設置之位置相對應的反應管之外周未設置外部電極,可防止處理氣體導入區內之電漿形成。(h) By not providing external electrodes on the outer periphery of the reaction tube corresponding to the position where the process gas introduction area is provided, plasma formation in the process gas introduction area can be prevented.
(i)藉由於與電漿區所設置之位置相對應的反應管之外周設置外部電極,可於電漿區內形成電漿。(i) Plasma can be formed in the plasma region by providing external electrodes on the outer periphery of the reaction tube corresponding to the position where the plasma region is provided.
(j)緩衝構造係在由處理室側之內壁之上部涵括至下部的部分,沿著基板之積載方向設置,並設有對處理室內供給經電漿化之氣體的氣體供給口,藉此可使處理室內之氣體濃度均勻化。(j) The buffer structure is located on the part covering from the upper part to the lower part of the inner wall of the processing chamber side, and is arranged along the loading direction of the substrate, and is provided with a gas supply port for supplying the plasmaized gas to the processing chamber. This homogenizes the gas concentration within the processing chamber.
(k)藉由於俯視下,包夾著原料氣供給噴嘴設置緩衝室,並於與各緩衝室所設置之位置相對應的反應管之外周設置形成電漿的外部電極,可擴大電漿區。(k) By arranging buffer chambers sandwiching the material gas supply nozzles in a plan view, and disposing external electrodes for forming plasma on the outer circumference of the reaction tubes corresponding to the locations where the respective buffer chambers are installed, the plasma region can be enlarged.
以上具體說明了本發明實施形態。然而,本發明並不限定於上述實施形態,在不脫離其要旨之範圍內可進行各種變更。The embodiments of the present invention have been specifically described above. However, this invention is not limited to the said embodiment, Various changes are possible in the range which does not deviate from the summary.
例如於上述實施形態中,說明了於供給了原料後再供給反應氣體的例子。本發明並不限定於此種態樣,原料、反應氣體之供給順序亦可為相反。亦即,亦可於供給了反應氣體後再供給原料。藉由改變供給順序,可改變所形成之膜的膜質或組成比。For example, in the above-mentioned embodiment, the example in which a reaction gas is supplied after supplying a raw material was demonstrated. The present invention is not limited to this aspect, and the supply order of raw materials and reaction gases may be reversed. That is, the raw material may be supplied after supplying the reaction gas. By changing the order of supply, the film quality or composition ratio of the formed film can be changed.
上述實施形態等中,係針對於晶圓200上形成SiN膜的例子進行了說明。本發明並不限定於此種態樣,亦可適合應用於在晶圓200上形成氧化矽膜(SiO膜)、氧碳化矽膜(SiOC膜)、氧碳氮化矽膜(SiOCN膜)、氧氮化矽膜(SiON膜)等之Si系氧化膜的情形,或於晶圓200上形成碳氮化矽膜(SiCN膜)、硼氮化矽膜(SiBN膜)、硼碳氮化矽膜(SiBCN膜)等之Si系氮化膜。此等情況下,作為反應氣體,除了含O氣體之外,可使用C3
H6
等含C氣體、或NH3
等含N氣體、或BCl3
等含B氣體。In the above-mentioned embodiments and the like, an example in which a SiN film is formed on the
又,本發明係可適合應用於在晶圓200上形成含有鈦(Ti)、鋯(Zr)、鉿(Hf)、鉭(Ta)、鈮(Nb)、鋁(Al)、鉬(Mo)、鎢(W)等金屬元素的氧化膜或氮化膜、亦即金屬系氧化膜或金屬系氮化膜的情形。亦即,本發明係可適合應用於在晶圓200上形成TiO膜、TiN膜、TiOC膜、TiOCN膜、TiON膜、TiBN膜、TiBCN膜、ZrO膜、ZrN膜、ZrOC膜、ZrOCN膜、ZrON膜、ZrBN膜、ZrBCN膜、HfO膜、HfN膜、HfOC膜、HfOCN膜、HfON膜、HfBN膜、HfBCN膜、TaO膜、TaOC膜、TaOCN膜、TaON膜、TaBN膜、TaBCN膜、NbO膜、NbN膜、NbOC膜、NbOCN膜、NbON膜、NbBN膜、NbBCN膜、AlO膜、AlN膜、AlOC膜、AlOCN膜、AlON膜、AlBN膜、AlBCN膜、MoO膜、MoN膜、MoOC膜、MoOCN膜、MoON膜、MoBN膜、MoBCN膜、WO膜、WN膜、WOC膜、WOCN膜、WON膜、MWBN膜、WBCN膜等的情形。In addition, the present invention can be suitably applied to the formation of metals containing titanium (Ti), zirconium (Zr), hafnium (Hf), tantalum (Ta), niobium (Nb), aluminum (Al), and molybdenum (Mo) on the
於此等情況下,例如作為原料氣體,可使用肆(二甲胺基)鈦(Ti[N(CH3 )2 ]4 ,簡稱TDMAT)氣體、肆(乙基甲胺基)鉿(Hf[N((C2 H5 )(CH3 )]4 ,簡稱TEMAH)氣體、肆(乙基甲胺基)鉿(Zr[N((C2 H5 )(CH3 )]4 ,簡稱TEMAZ)氣體、三甲基鋁(Al(CH3 )3 ,簡稱TMA)氣體、四氯化鈦(TiCl4 )氣體、四氯化鉿(HfCl4 )氣體等。作為反應氣體可使用上述反應氣體。In such cases, for example, as a raw material gas, tetrakis(dimethylamino)titanium (Ti[N(CH 3 ) 2 ] 4 , abbreviated as TDMAT) gas, tetrakis(ethylmethylamino)hafnium (Hf[ N((C 2 H 5 )(CH 3 )] 4 , referred to as TEMAH) gas, tetra(ethylmethylamino) hafnium (Zr[N((C 2 H 5 )(CH 3 )] 4 , referred to as TEMAZ) gas, trimethylaluminum (Al(CH 3 ) 3 , abbreviated as TMA) gas, titanium tetrachloride (TiCl 4 ) gas, hafnium tetrachloride (HfCl 4 ) gas, etc. The above-mentioned reaction gases can be used as the reaction gas.
亦即,本發明可適合應用於形成含有半金屬元素之半金屬系膜或含有金屬元素之金屬系膜的情形。此等成膜處理之處理手續、處理條件可設為與上述實施形態或變形例所示成膜處理相同的處理手續、處理條件。於此等情況下,可獲得與上述實施形態或變形例相同的效果。That is, the present invention can be suitably applied to the case of forming a semimetal-based film containing a half-metal element or a metal-based film containing a metal element. The processing procedures and processing conditions of these film-forming treatments can be set to the same processing procedures and processing conditions as those of the film-forming treatments shown in the above-mentioned embodiments or modifications. In such cases, the same effects as those of the above-described embodiment or modifications can be obtained.
成膜處理所使用之配方,較佳係配合處理內容而個別準備,經由電信通路或外部記憶裝置123事先儲存於記憶裝置121c內。然後,較佳係於開始各種處理時,CPU121a由儲存於記憶裝置121c內之複數配方中,配合處理內容適當選擇適合的配方。藉此,可藉由1台基板處理裝置而通用地且再現性佳地形成各種膜種類、組成比、膜質、膜厚的薄膜。又,可減低操作員的負擔、避免操作錯誤,並可迅速地開始各種處理。The recipe used in the film forming process is preferably prepared individually according to the processing content, and stored in the
上述配方並不限定於新穎作成的情況,例如亦可藉由將已安裝於基板處理裝置之既存配方變更而準備。於變更配方的情況,可將變更後之配方經由電信通路或記錄有該配方之記錄媒體,安裝至基板處理裝置。又,亦可操作既存基板處理裝置所具備之輸入裝置122,對基板處理裝置中已安裝之既存配方進行直接變更。The above-mentioned recipe is not limited to the case of novel preparation, for example, it can also be prepared by changing the existing recipe installed in the substrate processing apparatus. In the case of changing the recipe, the changed recipe can be installed in the substrate processing apparatus through a telecommunication channel or a recording medium in which the recipe is recorded. In addition, it is also possible to directly change the existing recipe installed in the substrate processing apparatus by operating the
115:晶舟升降器
115s:擋門開關機構
121:控制器
121a:CPU
121b:RAM
121c:記憶裝置
121d:I/O埠
121e:內部匯流排
122:輸出入裝置
123:外部記憶裝置
200:晶圓(基板)
201:處理室
202:處理爐
203:反應管
207:加熱器
209:岐管
217:晶舟(基板支撐具)
218:隔熱板
219:密封蓋
219s:擋門
220a~220c:O型環
231:排氣管
232a~232d:氣體供給管
237:緩衝構造
237a:區隔板
237b:氣體導入區
237c:緩衝室
237d:氣體供給孔
241a~241d:質量流量控制器(MFC)
243a~243d:閥
244:APC閥
245:壓力感應器
246:真空泵
249a:噴嘴
249b:配管
250a:氣體供給孔
255:旋轉軸
263:溫度感應器
267:旋轉機構
272:整合器
273:高頻電源
300:外部電極
302,304:氣體供給口
306:電漿活性種115:
圖1係本發明實施形態中適合使用之基板處理裝置之縱型處理爐的概略構成圖,以縱剖面圖顯示處理爐部分的圖。 圖2係本發明實施形態中適合使用之基板處理裝置之縱型處理爐的概略構成圖,以圖1之A-A線剖面圖顯示處理爐部分的圖。 圖3(a)係用於說明本發明實施形態中適合使用之基板處理裝置之緩衝構造的橫剖面放大圖;(b)係用於說明本發明實施形態中適合使用之基板處理裝置之緩衝構造的概略圖。 圖4係本發明實施形態中適合使用之基板處理裝置之控制器的概略構成圖,以方塊圖顯示控制器之控制系統的圖。 圖5係表示本發明實施形態之基板處理步驟的流程圖。FIG. 1 is a schematic configuration diagram of a vertical processing furnace of a substrate processing apparatus suitable for use in an embodiment of the present invention, showing a portion of the processing furnace in a vertical cross-sectional view. FIG. 2 is a schematic configuration diagram of a vertical processing furnace of a substrate processing apparatus suitable for use in an embodiment of the present invention, showing a portion of the processing furnace in a sectional view taken along line A-A of FIG. 1 . Fig. 3(a) is an enlarged cross-sectional view for explaining the buffer structure of the substrate processing apparatus suitable for use in the embodiment of the present invention; (b) is for explaining the buffer structure of the substrate processing apparatus suitable for use in the embodiment of the present invention a sketch of the . Fig. 4 is a schematic configuration diagram of a controller of a substrate processing apparatus suitable for use in an embodiment of the present invention, showing a control system of the controller in a block diagram. Fig. 5 is a flow chart showing the substrate processing steps according to the embodiment of the present invention.
200:晶圓(基板) 200: wafer (substrate)
201:處理室 201: Treatment room
203:反應管 203: reaction tube
231:排氣管 231: exhaust pipe
237:緩衝構造 237: Buffer construction
237a:區隔板 237a: Partition board
237b:氣體導入區 237b: gas introduction area
237c:緩衝室 237c: buffer room
237d:氣體供給孔 237d: gas supply hole
249a:噴嘴 249a:Nozzle
250a:氣體供給孔 250a: gas supply hole
300:外部電極 300: external electrodes
302,304:氣體供給口 302, 304: gas supply port
306:電漿活性種 306: Plasma Active Species
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TW200307998A (en) * | 2002-04-05 | 2003-12-16 | Hitachi Int Electric Inc | Treatment device of substrate |
JP2004124234A (en) * | 2002-10-07 | 2004-04-22 | Hitachi Kokusai Electric Inc | Apparatus for treating substrate |
JP2007258580A (en) * | 2006-03-24 | 2007-10-04 | Tokyo Electron Ltd | Plasma treatment equipment and plasma treatment method |
TWI446442B (en) * | 2009-05-01 | 2014-07-21 | Tokyo Electron Ltd | Plasma process apparatus and plasma process method |
TW201903846A (en) * | 2017-03-10 | 2019-01-16 | 日商國際電氣股份有限公司 | Substrate processing apparatus, manufacturing method of semiconductor device, and recording medium |
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TW200307998A (en) * | 2002-04-05 | 2003-12-16 | Hitachi Int Electric Inc | Treatment device of substrate |
JP2004124234A (en) * | 2002-10-07 | 2004-04-22 | Hitachi Kokusai Electric Inc | Apparatus for treating substrate |
JP2007258580A (en) * | 2006-03-24 | 2007-10-04 | Tokyo Electron Ltd | Plasma treatment equipment and plasma treatment method |
TWI446442B (en) * | 2009-05-01 | 2014-07-21 | Tokyo Electron Ltd | Plasma process apparatus and plasma process method |
TW201903846A (en) * | 2017-03-10 | 2019-01-16 | 日商國際電氣股份有限公司 | Substrate processing apparatus, manufacturing method of semiconductor device, and recording medium |
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