TW201841250A - Plasma processing device - Google Patents

Plasma processing device Download PDF

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TW201841250A
TW201841250A TW107100435A TW107100435A TW201841250A TW 201841250 A TW201841250 A TW 201841250A TW 107100435 A TW107100435 A TW 107100435A TW 107100435 A TW107100435 A TW 107100435A TW 201841250 A TW201841250 A TW 201841250A
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gas
flow rate
processing
etching
raw material
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TW107100435A
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Chinese (zh)
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TWI781977B (en
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松井久
齊藤英樹
片桐崇良
窪田真樹
冨山和哉
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日商東京威力科創股份有限公司
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01JELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
    • H01J37/00Discharge tubes with provision for introducing objects or material to be exposed to the discharge, e.g. for the purpose of examination or processing thereof
    • H01J37/32Gas-filled discharge tubes
    • H01J37/32431Constructional details of the reactor
    • H01J37/3244Gas supply means
    • H01J37/32449Gas control, e.g. control of the gas flow
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01JELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
    • H01J37/00Discharge tubes with provision for introducing objects or material to be exposed to the discharge, e.g. for the purpose of examination or processing thereof
    • H01J37/32Gas-filled discharge tubes
    • H01J37/32009Arrangements for generation of plasma specially adapted for examination or treatment of objects, e.g. plasma sources
    • H01J37/32082Radio frequency generated discharge
    • H01J37/321Radio frequency generated discharge the radio frequency energy being inductively coupled to the plasma
    • H01J37/3211Antennas, e.g. particular shapes of coils
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01JELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
    • H01J37/00Discharge tubes with provision for introducing objects or material to be exposed to the discharge, e.g. for the purpose of examination or processing thereof
    • H01J37/32Gas-filled discharge tubes
    • H01J37/32431Constructional details of the reactor
    • H01J37/32798Further details of plasma apparatus not provided for in groups H01J37/3244 - H01J37/32788; special provisions for cleaning or maintenance of the apparatus
    • H01J37/32816Pressure
    • H01J37/32834Exhausting
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/02Manufacture or treatment of semiconductor devices or of parts thereof
    • H01L21/027Making masks on semiconductor bodies for further photolithographic processing not provided for in group H01L21/18 or H01L21/34
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/67Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere
    • H01L21/67005Apparatus not specifically provided for elsewhere
    • H01L21/67011Apparatus for manufacture or treatment
    • H01L21/67017Apparatus for fluid treatment
    • H01L21/67063Apparatus for fluid treatment for etching
    • H01L21/67069Apparatus for fluid treatment for etching for drying etching

Abstract

The present invention provides a plasma processing apparatus capable of adjusting a composition of a processing gas in each of a plurality of gas shower heads using a common processing gas raw material supply unit. In the plasma processing apparatus (1) that performs plasma processing on the substrate (G) to be processed, first and second process gas raw material supply units (4a, 4b) for supplying the first and second process gas raw materials in a processing space (100) for accommodating the mounting table (13) on which the substrate to be processed (G) is placed are respectively provided with first and second supply flow rate adjustment sections (41a, 41b), a plurality of first and second distribution flow paths (401, 402) for distributing the first and second process gas materials to the plurality of gas shower heads (30a to 30d) are also respectively provided with first and second distribution flow rate adjustment units (421a to 424a, 421b to 424b).

Description

電漿處理裝置Plasma processing device

本發明係關於藉由被電漿化之處理氣體進行被處理基板之電漿處理的技術。The present invention relates to a technique for plasma treatment of a substrate to be processed by a plasma-treated process gas.

在液晶顯示裝置(LCD)等之平面顯示器(FPD)之製造工程中,存在有對作為被載置於處理空間內之被處理基板的玻璃基板,供給被電漿化之處理氣體而進行蝕刻處理或成膜處理等之電漿處理之工程。在該些電漿處理中,使用電漿蝕刻裝置或電漿CVD裝置等之各種電漿處理裝置。In a manufacturing process of a flat panel display (FPD) such as a liquid crystal display (LCD), there is a glass substrate which is a substrate to be processed placed in a processing space, and a plasma-treated processing gas is supplied for etching treatment. Or plasma processing such as film processing. In the plasma treatment, various plasma processing apparatuses such as a plasma etching apparatus or a plasma CVD apparatus are used.

另一方面,玻璃基板之尺寸朝著大型化進展。例如,在LCD用之矩形狀玻璃基板中,對短邊×長邊之長度為約2200mm×約2400mm,甚至也為約2800mm×約3000mm之尺寸的被處理面之各位置,供給需要量的處理氣體,再者,必須在玻璃基板之面內進行均勻之處理。On the other hand, the size of the glass substrate is progressing toward enlargement. For example, in the rectangular glass substrate for LCD, the required amount is processed for each position of the processed surface of the short side x long side having a length of about 2200 mm × about 2400 mm, or even about 2800 mm × about 3000 mm. The gas, in addition, must be uniformly treated in the plane of the glass substrate.

另外,隨著上述玻璃基板之大型化,到達至玻璃基板之處理氣體之濃度或電漿化之狀態等在被處理面內有變化大之情況。因此,產生由於處理氣體造成玻璃基板之處理狀態在面內不均勻之問題。   再者,本身在對如此之大型玻璃基板之各位置供給需要量之處理氣體上也有困難之情況。In addition, as the size of the glass substrate increases, the concentration of the processing gas reaching the glass substrate, the state of the plasma, and the like may vary greatly in the surface to be processed. Therefore, there is a problem that the processing state of the glass substrate is uneven in the plane due to the processing gas. Furthermore, it is also difficult to supply a required amount of processing gas to each position of such a large glass substrate.

例如,專利文獻1中記載著將噴淋頭內分割成同心圓狀而設置例如三個緩衝室,從共同的氣體供給源,分流至該些緩衝室,對基板被處理的處理容器內供給電漿蝕刻用之蝕刻氣體的技術。當藉由該專利文獻1時,對被供給至上述緩衝室之中,位於周邊部側之兩個緩衝室的蝕刻氣體,供給用以調整蝕刻特性之附加氣體,在基板面內局部性地調整蝕刻氣體之濃度。   但是,記載於專利文獻1之技術,當供給附加氣體的時候,因在朝各緩衝室供給蝕刻氣體之每一個供給路,設置有專用的氣體供給源,故有氣體供給源之構成大型化之虞。 [先前技術文獻] [專利文獻]For example, Patent Document 1 discloses that the inside of the shower head is divided into concentric circles, for example, three buffer chambers are provided, and the common gas supply source is branched to the buffer chambers to supply electric power to the processing chamber in which the substrates are processed. A technique for etching gas for slurry etching. According to Patent Document 1, the etching gas supplied to the two buffer chambers on the peripheral portion side of the buffer chamber is supplied with an additional gas for adjusting the etching characteristics, and is locally adjusted in the substrate surface. The concentration of the etching gas. However, in the technique described in Patent Document 1, when an additional gas is supplied, a dedicated gas supply source is provided for supplying each of the etching gas to each of the buffer chambers, so that the gas supply source is increased in size. Hey. [Prior Technical Literature] [Patent Literature]

[專利文獻1]日本專利第4358727號公報:請求項1、段落0004、0028、0049~0050、圖5[Patent Document 1] Japanese Patent No. 4358727: Request No. 1, paragraphs 0004, 0028, 0049 to 0050, Fig. 5

[發明所欲解決之課題][Problems to be solved by the invention]

本發明係鑒於如此之情形而創作出,其目的在於提供能夠使用共同的處理氣體原料供給部,並且對複數氣體噴淋頭部之每一個調整處理氣體之成分的電漿處理裝置。 [用以解決課題之手段]The present invention has been made in view of such circumstances, and an object thereof is to provide a plasma processing apparatus capable of using a common processing gas raw material supply unit and adjusting a component of a processing gas for each of a plurality of gas shower heads. [Means to solve the problem]

本發明之電漿處理裝置係對被真空排氣之處理空間內之被處理基板,實施藉由被電漿化之處理氣體進行的電漿處理,該電漿處理裝置之特徵在於具備:   處理容器,其係具備載置上述被處理基板之載置台,構成實施上述電漿處理之處理空間;   複數氣體噴淋頭部,其係分別被設置在構成上述處理空間之天頂面,且將上述天頂面從中央部側朝向周邊部側在徑向予以分割而構成的複數區域,形成有對上述處理空間供給處理氣體之氣體吐出孔;   電漿產生部,其係用以將從上述複數噴淋頭部被供給至處理空間之處理氣體予以電漿化;   用以供給上述處理氣體所含之第1處理氣體原料的第1處理氣體原料供給部,及用以供給第2處理氣體原料之第2處理氣體原料供給部;   第1供給流量調節部,其係用以進行從上述第1處理氣體原料供給部被供給至上述處理空間之第1處理氣體原料之流量調節;   複數第1分配流量調節部,其係分別被設置在用以將在上述第1供給流量調節部被流量調節之第1處理氣體原料,分配供給至上述複數氣體噴淋頭部之複數第1分配流路,用以進行被供給至各氣體噴淋頭部之第1原料氣體之流量調節;   第2供給流量調節部,其係用以進行從上述第2處理氣體原料供給部被供給至上述處理空間之第2處理氣體原料之流量調節;及   複數第2分配流量調節部,其係分別被設置在用以將在上述第2供給流量調節部被流量調節之第2處理氣體原料,分配供給至上述複數氣體噴淋頭部之複數第2分配流路,用以進行被供給至各氣體噴淋頭部之第2原料氣體之流量調節。 [發明效果]In the plasma processing apparatus of the present invention, the substrate to be processed in the processing space to be vacuum-exhausted is subjected to plasma treatment by the plasma-treated processing gas, and the plasma processing apparatus is characterized by comprising: a processing container And comprising: a mounting table on which the substrate to be processed is placed, and a processing space for performing the plasma processing; and a plurality of gas shower heads respectively provided on a zenith surface constituting the processing space, and the zenith surface A plurality of regions formed by dividing the radial direction from the central portion side toward the peripheral portion side are formed with a gas discharge hole for supplying a processing gas to the processing space, and a plasma generating portion for discharging the head from the plurality of the plurality of shower heads The processing gas supplied to the processing space is plasma-formed; the first processing gas raw material supply unit for supplying the first processing gas raw material contained in the processing gas; and the second processing gas for supplying the second processing gas raw material a raw material supply unit; the first supply flow rate adjustment unit configured to be supplied from the first process gas raw material supply unit to The flow rate adjustment of the first process gas raw material in the processing space; the plurality of first distribution flow rate adjusting units are respectively provided in the first process gas raw material for adjusting the flow rate of the first supply flow rate adjusting unit a plurality of first distribution channels to the plurality of gas shower heads for regulating the flow rate of the first material gas supplied to each of the gas shower heads; and a second supply flow rate adjusting unit for performing the slave The second processing gas raw material supply unit is configured to adjust the flow rate of the second processing gas raw material supplied to the processing space; and the plurality of second distributed flow rate adjusting units are provided in the second supply flow rate adjusting unit The flow rate-regulated second process gas raw material is distributed to the plurality of second distribution flow paths of the plurality of gas shower heads to adjust the flow rate of the second material gas supplied to each of the gas shower heads. [Effect of the invention]

本發明係在第1、第2處理氣體原料供給部各設置進行第1、第2處理氣體原料之流量調節的第1、第2供給流量調節部,並且對於對複數噴淋頭部分配該些第1、第2處理氣體原料的複數第1、第2分配流路,也各設置第1、第2分配流量調節部。其結果,可以以任意之比例混合從共同的第1、第2處理氣體原料供給部所取得之第1、第2處理氣體原料,而供給至被處理基板之各位置。In the present invention, the first and second supply flow rate adjusting units that adjust the flow rates of the first and second process gas raw materials are provided in the first and second process gas raw material supply units, and the plurality of shower heads are distributed to the plurality of shower heads. The first and second distribution flow rate adjustment units are provided for each of the first and second distribution channels of the first and second process gas materials. As a result, the first and second process gas raw materials obtained from the common first and second process gas raw material supply units can be mixed at an arbitrary ratio and supplied to each position of the substrate to be processed.

說明與本發明之實施形態有關之電漿處理裝置1之具體性構成之前,針對在該電漿處理裝置1被實施之電漿處理之例,在該製程處理之實施時候所掌握的問題點,一面參照圖1、2一面予以說明。   圖1、2表示處理對象之被處理基板G之上面(被處理面)之不同區域的放大縱斷側面圖。該被處理基板G係在玻璃基板701上皆依照作為含矽膜之SiO膜702、SiN膜703之順序疊層,並且,在SiN膜703之上面,圖案製作被曝光顯像之光阻膜704。Before explaining the specific configuration of the plasma processing apparatus 1 according to the embodiment of the present invention, the problems that are grasped during the implementation of the processing of the processing of the plasma processing apparatus 1 are described. One side will be described with reference to Figs. 1 and 2 are enlarged side elevational views showing different regions of the upper surface (processed surface) of the substrate G to be processed. The substrate G to be processed is laminated on the glass substrate 701 in the order of the SiO film 702 and the SiN film 703 as the ruthenium-containing film, and the photoresist film 704 which is exposed and developed is patterned on the upper surface of the SiN film 703. .

例如,被處理基板G藉由矩形狀之FPD用之玻璃基板701被構成。在此,就以FPD而言例示有液晶顯示器(LCD)、電激發光(Electro Luminescence: EL)顯示器,電漿顯示面板(PDP)等。For example, the substrate G to be processed is configured by a glass substrate 701 for a rectangular FPD. Here, a liquid crystal display (LCD), an electroluminescence (EL) display, a plasma display panel (PDP), or the like is exemplified as the FPD.

對上述被處理基板G,藉由將包含第1處理氣體原料亦即四氟化碳(CF4 )氣體或三氟化氮(NF3 )氣體之至少一方,和第2處理氣體原料亦即氧(O2 )氣體的蝕刻氣體電漿化並予以供給,進行一面使光阻膜704逐漸灰化,一面除去不藉由光阻膜704被覆蓋的區域之SiO膜702、SiN膜703的蝕刻處理。SiO膜702或SiN膜703相當於本實施形態之蝕刻對象膜。The substrate G to be processed is made of at least one of a carbon tetrafluoride (CF 4 ) gas or a nitrogen trifluoride (NF 3 ) gas, which is a first processing gas raw material, and a second processing gas raw material, that is, oxygen. The etching gas of the (O 2 ) gas is plasma-treated and supplied, and the SiO film 702 and the SiN film 703 which are not covered by the photoresist film 704 are removed while the photoresist film 704 is gradually ashed. . The SiO film 702 or the SiN film 703 corresponds to the etching target film of the present embodiment.

針對上述處理,本發明者們因應被處理基板G之被處理面內之位置,找出被圖案製作之光阻膜704之縱剖面形狀不同,其結果,有蝕刻處理之結果互相不同的傾向。In response to the above-described processing, the present inventors have found that the longitudinal cross-sectional shape of the patterned photoresist film 704 is different depending on the position in the processed surface of the substrate G to be processed, and as a result, the results of the etching treatment tend to be different from each other.

例如,在被形成在被處理基板G之周邊部側之光阻膜704,如圖1(a)所示般,有被圖案製作後之光阻膜704之端部之傾斜(錐度)變大之情形。For example, in the photoresist film 704 formed on the peripheral portion side of the substrate G to be processed, as shown in FIG. 1(a), the inclination (taper) of the end portion of the patterned photoresist film 704 becomes large. The situation.

對於該被圖案製作之後的光阻膜704之端部之傾斜大的部分,使用O2 氣體之濃度(分壓)低(例如,O2 氣體/CF4 氣體之流體比為1:3)之蝕刻氣體而進行蝕刻處理時,如圖1(b)所示般,在玻璃基板701上之SiO膜702、SiN膜703為良好之狀態下被蝕刻除去。   另外,使用O2 濃度高(例如,O2 氣體/CF4 氣體之流量比為3:2)之蝕刻氣體而進行蝕刻處理時,如圖1(c)所示般,有在SiO膜702、SiN膜703之端部,殘留依存於光阻膜704之錐度之形狀的殘渣物(錐形殘渣71a),或很小的針狀蝕刻殘渣71b之情況。Inclined end portions 704 of the resist film after the pattern is made large portion of the gas concentration O 2 (partial pressure) is low (e.g., O 2 gas / CF 4 gas fluid ratio is 1: 3) of When the etching process is performed by etching the gas, as shown in FIG. 1(b), the SiO film 702 and the SiN film 703 on the glass substrate 701 are etched and removed in a good state. Further, when etching is performed using an etching gas having a high O 2 concentration (for example, a flow ratio of O 2 gas/CF 4 gas of 3:2), as shown in FIG. 1(c), there is an SiO film 702, The end portion of the SiN film 703 remains in the form of a residue (cone residue 71a) depending on the taper shape of the photoresist film 704, or a small needle-shaped etching residue 71b.

再者,例如在被形成在被處理基板G之中央部側之光阻膜704,如圖2(a)所示般,有被圖案製作後之光阻膜704之端部之傾斜(錐度)變小之情形。Further, for example, as shown in FIG. 2(a), the photoresist film 704 formed on the central portion side of the substrate G to be processed has the inclination (taper) of the end portion of the patterned photoresist film 704. Smaller situation.

對於該被圖案製作之後的光阻膜704之端部之傾斜小的部分,使用O2 氣體之濃度低(例如,與圖1(b)相同之O2 氣體/CF4 氣體之流量比)之蝕刻氣體而進行蝕刻處理時,如圖2(b)所示般,可以見到在從玻璃基板701上被除去之SiO膜702、SiN膜703之端部,殘存針狀蝕刻殘渣71b之傾向。   另外,使用O2 氣體之濃度高(例如,與圖1(c)之情況相同的O2 氣體/CF4 氣體之流量比)之蝕刻氣體而進行蝕刻處理時,如圖2(c)所示般,在玻璃基板701上之SiO膜702、SiN膜703良好之狀態下被蝕刻除去。For the portion where the inclination of the end portion of the photoresist film 704 after the patterning is small, the concentration of the O 2 gas is low (for example, the flow ratio of the O 2 gas/CF 4 gas which is the same as that of FIG. 1(b)). When the etching process is performed by etching the gas, as shown in FIG. 2(b), the SiO film 702 and the end portion of the SiN film 703 which are removed from the glass substrate 701 tend to have the needle-shaped etching residue 71b remaining. Further, when etching is performed using an etching gas having a high concentration of O 2 gas (for example, a flow ratio of O 2 gas/CF 4 gas which is the same as in the case of FIG. 1(c)), as shown in FIG. 2(c) In general, the SiO film 702 and the SiN film 703 on the glass substrate 701 are etched and removed in a good state.

若藉由上述說明的蝕刻氣體中之O2 氣體之濃度,和被處理基板G之各位置中之蝕刻處理之結果的對應關係時,為了在被處理基板G之周邊部側取得良好的蝕刻處理結果,當對被處理基板G之全面供給O2 氣體之濃度低之蝕刻氣體時,有在被處理基板G之中央部側之SiO膜702、SiN膜703之端部,殘存針狀之蝕刻殘渣71b之虞。When the relationship between the concentration of the O 2 gas in the etching gas described above and the result of the etching treatment in each position of the substrate G to be processed is performed, a good etching treatment is performed on the peripheral portion side of the substrate G to be processed. As a result, when the etching gas having a low concentration of the O 2 gas is supplied to the entire substrate G to be processed, there are residual acicular residues in the end portions of the SiO film 702 and the SiN film 703 on the central portion side of the substrate G to be processed. After the 71b.

再者,為了在被處理基板G之中央部側取得良好之蝕刻處理結果,當對被處理基板G之全面供給O2 氣體之濃度高的蝕刻氣體時,有在被處理基板G之周邊部側之SiO膜702、SiN膜703之端部,殘存錐形殘渣71a或針狀之蝕刻殘渣71b之虞。   因與上述說明之問題點對應,故與本實施形態有關之電漿處理裝置1成為能夠因應被處理基板G之位置而使蝕刻氣體中之O2 氣體之濃度變化。Further, in order to obtain a good etching treatment result on the central portion side of the substrate G to be processed, when the etching gas having a high concentration of O 2 gas is supplied to the entire substrate G to be processed, there is a peripheral portion side of the substrate G to be processed. At the end portions of the SiO film 702 and the SiN film 703, the conical residue 71a or the needle-shaped etching residue 71b remains. Since the plasma processing apparatus 1 according to the present embodiment corresponds to the position of the substrate G to be processed, the concentration of the O 2 gas in the etching gas can be changed in accordance with the problem described above.

使用圖3、4,說明與本發明之實施形態有關之電漿處理裝置1之構成。   如圖3之縱斷側面圖所示般,電漿處理裝置1具備由導電性材料,例如內壁面被陽極氧化處理之鋁所構成的角筒形狀之容器本體10,該容器本體10被電性接地。在容器本體10之上面形成開口,該開口藉由設置成與該容器本體10絕緣的矩形狀之金屬窗3被氣密密封。The configuration of the plasma processing apparatus 1 according to the embodiment of the present invention will be described with reference to Figs. As shown in the longitudinal side view of Fig. 3, the plasma processing apparatus 1 is provided with a container body 10 having a rectangular tube shape made of a conductive material such as aluminum whose inner wall surface is anodized, and the container body 10 is electrically Ground. An opening is formed in the upper surface of the container body 10, and the opening is hermetically sealed by a rectangular metal window 3 provided to be insulated from the container body 10.

藉由該些容器本體10及金屬窗3所包圍之空間成為被處理基板G之處理空間100。金屬窗3之上方側之空間成為配置高頻天線(電漿天線)5之天線室50。   再者,在容器本體10之側壁,設置有用以搬入搬出被處理基板G之搬入搬出口101及關閉搬入搬出口101之閘閥102。The space surrounded by the container body 10 and the metal window 3 becomes the processing space 100 of the substrate G to be processed. The space on the upper side of the metal window 3 serves as an antenna room 50 in which a high frequency antenna (plasma antenna) 5 is disposed. Further, a gate valve 102 for loading and unloading the loading/unloading port 101 of the substrate G to be processed and closing the loading/unloading port 101 is provided on the side wall of the container body 10.

在處理空間100之下部側,以與上述金屬窗3相向之方式,設置有用以載置被處理基板G之載置台13。載置台13係由導電性材料,例如表面被陽極氧化處理之鋁所構成,在俯視觀看時之形狀成為矩形狀。被載置於載置台13之被處理基板G係藉由無圖示之靜電夾具被吸附保持。載置台13被收納在絕緣體框14內,經由該絕緣體框14被配置在容器本體10之底面。On the lower side of the processing space 100, a mounting table 13 for placing the substrate G to be processed is disposed so as to face the metal window 3 described above. The mounting table 13 is made of a conductive material, for example, aluminum whose surface is anodized, and has a rectangular shape in plan view. The substrate G to be processed placed on the mounting table 13 is sucked and held by an electrostatic chuck (not shown). The mounting table 13 is housed in the insulator frame 14 and is disposed on the bottom surface of the container body 10 via the insulator frame 14.

在載置台13,經由匹配器151連接有第2高頻電源152。第2高頻電源152對載置台13施加偏壓用之高頻電力,例如頻率為3.2MHz之高頻電力。藉由基於該偏壓用之高頻電力所生成之自偏壓,將在處理空間100內生成之電漿中之離子導入至被處理基板G。   另外,在載置台13內,為了控制被處理基板G之溫度,設置有由陶瓷加熱器等之加熱手段和冷媒流路所構成之溫度控制機構、溫度感測器、用以對被處理基板G之背面供給熱傳達用之He氣體的氣體流路(皆無圖示)。The second high frequency power supply 152 is connected to the mounting table 13 via the matching unit 151. The second high-frequency power source 152 applies high-frequency power for biasing to the mounting table 13, for example, high-frequency power having a frequency of 3.2 MHz. The ions in the plasma generated in the processing space 100 are introduced into the substrate G to be processed by the self-bias generated by the high-frequency power for the bias voltage. Further, in the mounting table 13, in order to control the temperature of the substrate G to be processed, a temperature control mechanism composed of a heating means such as a ceramic heater and a refrigerant flow path, a temperature sensor, and a substrate G to be processed are provided. The gas flow path of the He gas for heat transmission is supplied to the back surface (all are not shown).

再者,在容器本體10之底面形成排氣口103,在該排氣口103連接有包含真空泵等之真空排氣部12。處理空間100之內部,藉由該真空排氣部12被真空排氣成電漿處理時之壓力。如圖3所示般,排氣口103被設置複數個在載置台13之周圍,被配置在俯視觀看時呈矩形狀之載置台13之四角落附近位置,沿著載置台13之四邊的位置等。Further, an exhaust port 103 is formed on the bottom surface of the container body 10, and a vacuum exhaust unit 12 including a vacuum pump or the like is connected to the exhaust port 103. The inside of the processing space 100 is evacuated by vacuum to a pressure at the time of plasma treatment. As shown in FIG. 3, the exhaust port 103 is provided at a plurality of positions around the mounting table 13, and is disposed at a position near the four corners of the mounting table 13 which is rectangular in plan view, and is located along the four sides of the mounting table 13. Wait.

如圖3及從處理空間100側觀看金屬窗3之俯視圖的圖4所示般,在容器本體10之側壁之上面側,設置有由鋁等之金屬所構成之矩形狀之框體亦即金屬框11。在容器本體10和金屬框11之間設置有用以將處理空間100保持氣密之密封構件110。在此,容器本體10及金屬框11構成本實施形態之處理容器。As shown in FIG. 3 and the top view of the metal window 3 viewed from the side of the processing space 100, a rectangular frame body made of metal such as aluminum is provided on the upper surface side of the side wall of the container body 10. Box 11. A sealing member 110 for holding the processing space 100 airtight is provided between the container body 10 and the metal frame 11. Here, the container body 10 and the metal frame 11 constitute the processing container of this embodiment.

而且,本例之金屬窗3被分割成複數部分窗30,該些部分窗30被配置在金屬框11之內側,整體構成矩形狀之金屬窗3。各部分窗30係藉由例如非磁性體且導電性之金屬、鋁或包含鋁之合金等被構成。Further, the metal window 3 of this example is divided into a plurality of partial windows 30 which are disposed inside the metal frame 11 and integrally constitute a rectangular metal window 3. Each of the partial windows 30 is configured by, for example, a non-magnetic, electrically conductive metal, aluminum, or an alloy containing aluminum.

各部分窗30兼作為處理氣體供給用之氣體噴淋頭部30a~30d。例如圖3所示般,在各氣體噴淋頭部30a~30d之內部,形成有使蝕刻氣體擴散之氣體擴散室301。再者,在形成有氣體擴散室301之區域的下面側,形成有用以對處理空間100供給處理氣體之多數氣體吐出孔302。   具備有該些構成之部分窗30(氣體噴淋頭部30a~30d)經由無圖示之保持部而被保持,構成先前所述之金屬窗3,同時構成處理空間100之天頂面。Each of the partial windows 30 also serves as a gas shower heads 30a to 30d for supplying a processing gas. For example, as shown in FIG. 3, a gas diffusion chamber 301 for diffusing an etching gas is formed inside each of the gas shower heads 30a to 30d. Further, a plurality of gas discharge holes 302 for supplying a processing gas to the processing space 100 are formed on the lower surface side of the region where the gas diffusion chamber 301 is formed. The partial window 30 (gas shower heads 30a to 30d) having such a configuration is held by a holding portion (not shown) to constitute the metal window 3 described above, and constitutes a zenith surface of the processing space 100.

一面參照圖4一面針對各氣體噴淋頭部30a~30d之平面形狀及配置予以說明時,氣體噴淋頭部30a~30d係從中央部側朝向周邊部側,在徑向進行3分割而構成的複數區域設置有天頂面亦即金屬窗3。   在上述被3分割之區域中,在中央部側之矩形區域,設置有氣體噴淋頭部30a,再者,在該氣體噴淋頭部30a之周圍之角環狀之區域,設置有氣體噴淋頭部30b。When the planar shape and arrangement of the gas shower heads 30a to 30d are described with reference to FIG. 4, the gas shower heads 30a to 30d are divided into three in the radial direction from the center portion side toward the peripheral portion side. The plural area is provided with a zenith surface, that is, a metal window 3. In the above-described divided area, a gas shower head 30a is provided in a rectangular region on the central portion side, and a gas jet is provided in a ring-shaped region around the gas shower head 30a. Sprinkle the head 30b.

並且,在將天頂面進行分割而構成的上述複數區域中,最周邊部側之角環狀的區域,被分割成包含角環之角部(矩形狀之天頂面之角部)的4個區域,和包含被挾於相鄰之上述角部之間的上述角環(矩形狀)之邊部的4個區域。而且,在包含角部之4個區域,設置周邊氣體噴淋頭部30d,在包含邊部之4個區域,設置有周邊氣體噴淋頭部30c。Further, in the plural region in which the zenith surface is divided, the annular region on the outermost peripheral portion is divided into four regions including corner portions of the corner ring (corner portions of the rectangular zenith surface). And four regions including the side portions of the above-mentioned corner rings (rectangular shapes) between the adjacent corner portions. Further, the peripheral gas shower head 30d is provided in four regions including the corner portions, and the peripheral gas shower head 30c is provided in four regions including the side portions.

再者,為了進行處理空間100內之真空排氣,配置複數在載置台13之周圍的已經敘述的排氣口103被設置在設置有周邊氣體噴淋頭部30c、30d之環狀區域之下方位置,或較該下方位置更外方側之位置(圖3)。Further, in order to perform vacuum evacuation in the processing space 100, a plurality of already described exhaust ports 103 disposed around the mounting table 13 are disposed below the annular region where the peripheral gas shower heads 30c, 30d are disposed. The position, or the position on the outer side of the lower position (Fig. 3).

互相被分割之氣體噴淋頭部30a~30d(部分窗30)藉由絕緣構件31與金屬框11或其下方側之容器本體10電性絕緣,同時相鄰之氣體噴淋頭部30a~30d彼此也藉由絕緣構件31互相絕緣(參照圖3、圖4)。The gas shower heads 30a to 30d (partial windows 30) which are divided from each other are electrically insulated from the metal frame 11 or the container body 10 on the lower side thereof by the insulating member 31, while the adjacent gas shower heads 30a to 30d They are also insulated from each other by the insulating member 31 (see FIGS. 3 and 4).

再者,為了提升部分窗30之耐電漿性,各部分窗30之處理空間100側之面(氣體噴淋頭部30a~30d之下面)被耐電漿塗佈。作為耐電漿塗佈之具體例而言,可以舉出藉由陽極化氧化處理或陶瓷熔射進行之介電質膜的形成。Further, in order to improve the plasma resistance of the partial window 30, the surface of the partial window 30 on the processing space 100 side (the lower surface of the gas shower heads 30a to 30d) is plasma-resistant. Specific examples of the plasma-resistant coating include the formation of a dielectric film by anodizing oxidation treatment or ceramic spraying.

如圖3所示般,各氣體噴淋頭部30a~30d之氣體擴散室301係經氣體供給管43a~43d而被連接於CF4 氣體供給部4a及O2 氣體供給部4b。   CF4 氣體供給部4a相當於本實施形態之第1處理氣體原料供給部(圖3、5中表示「第1處理氣體原料供給部」),從該CF4 氣體供給部4a供給第1處理氣體原料亦即CF4 氣體。另外,即使設置NF3 氣體供給部,以取代CF4 氣體供給部4a,供給NF3 氣體作為第1處理氣體原料當然亦可。As shown in Fig. 3, the gas diffusion chambers 301 of the gas shower heads 30a to 30d are connected to the CF 4 gas supply unit 4a and the O 2 gas supply unit 4b via the gas supply tubes 43a to 43d. The CF 4 gas supply unit 4a corresponds to the first process gas raw material supply unit (the "first process gas raw material supply unit" shown in Figs. 3 and 5), and the first process gas is supplied from the CF 4 gas supply unit 4a. The raw material is also CF 4 gas. In addition, it is a matter of course that the NF 3 gas supply unit is provided instead of the CF 4 gas supply unit 4a, and the NF 3 gas is supplied as the first processing gas source.

在CF4 氣體供給部4a之下游側,設置用以進行被供給至處理空間100之CF4 氣體之流量調節之第1供給流量調節部41a,而且,在第1供給流量調節部41a之下游側,經開關閥V1連接有複數根列如4根之第1分配流路401。各第1分配流路401被連接於氣體噴淋頭部30a~30d側之氣體供給管43a~43d,發揮將在第1供給流量調節部41a被流量調節之CF4 氣體,分配供給至複數氣體噴淋頭部30a~30d之功能。例如,第1供給流量調節部41a係藉由質量流量控制器(MFC)而構成。On the downstream side of the CF 4 gas supply unit 4a, a first supply flow rate adjustment unit 41a for adjusting the flow rate of the CF 4 gas supplied to the processing space 100 is provided, and is provided on the downstream side of the first supply flow rate adjustment unit 41a. The first distribution flow path 401 having a plurality of roots, for example, four, is connected via the switching valve V1. Each of the first distribution channels 401 is connected to the gas supply pipes 43a to 43d on the gas shower heads 30a to 30d, and the CF 4 gas whose flow rate is adjusted by the first supply flow rate adjustment unit 41a is distributed and supplied to the plurality of gases. The functions of the shower heads 30a to 30d. For example, the first supply flow rate adjustment unit 41a is configured by a mass flow controller (MFC).

並且,在各第1分配流路401,設置有用以進行被供給至各個的氣體噴淋頭部30a~30d之CF4 氣體之流量調節的第1分配流量調節部421a~424a。例如,第1分配流量調節部421a~424a係藉由MFC而構成。   因將在上游側之第1供給流量調節部41a被流量調整之CF4 氣體在下游側之第1分配流量調節部421a~424a分配成任意之流量比,故當將在第1供給流量調節部41a之CF4 氣體之流量設定值設為F1 ,將第1分配流量調節部421a~424a之各流量設定值設為f11 ~f14 之時,F1 =f11 +f12 +f13 +f14 之關係成立。Further, the first distribution flow rate adjustment units 421a to 424a for adjusting the flow rate of the CF 4 gas supplied to each of the gas shower heads 30a to 30d are provided in each of the first distribution flow paths 401. For example, the first distribution flow rate adjustment units 421a to 424a are configured by MFC. The first distribution flow rate adjustment units 421a to 424a on the downstream side of the CF 4 gas whose flow rate is adjusted by the first supply flow rate adjustment unit 41a on the upstream side are distributed at an arbitrary flow rate ratio, and therefore will be in the first supply flow rate adjustment unit. When the flow rate setting value of the CF 4 gas of 41a is F 1 and the flow rate setting values of the first distribution flow rate adjusting units 421a to 424a are f 11 to f 14 , F 1 = f 11 + f 12 + f 13 The relationship of +f 14 was established.

在各第1分配流量調節部421a~424a下游側設置開關閥V31~V34,第1分配流路401在該些開關閥V31~V34之下游側之位置與氣體供給管43a~43d連接。   此時,將從各第1分配流量調節部421a~424a至複數氣體噴淋頭部30a~30d之氣體流路之長度和剖面積予以統一而使氣體流路之傳導度相等,依此可以從複數氣體噴淋頭部30a~30d更均等地供給氣體。On the downstream side of each of the first distribution flow rate adjustment units 421a to 424a, on-off valves V31 to V34 are provided, and the first distribution flow path 401 is connected to the gas supply pipes 43a to 43d at a position downstream of the on-off valves V31 to V34. At this time, the lengths and cross-sectional areas of the gas flow paths from the respective first distribution flow rate adjusting units 421a to 424a to the plurality of gas shower heads 30a to 30d are unified to make the conductivity of the gas flow paths equal, and thus the The plurality of gas shower heads 30a to 30d supply gas more uniformly.

另外,O2 氣體供給部4b相當於本實施形態之第2處理氣體原料供給部(圖3、5中表示「第2處理氣體原料供給部」),從該O2 氣體供給部4b供給第2處理氣體原料亦即O2 氣體。   在O2 氣體供給部4b之下游側,設置用以進行被供給至處理空間100之O2 氣體之流量調節之第2供給流量調節部41b,而且,在第2供給流量調節部41b之下游側,經開關閥V2連接有複數根例如第1分配流路401,同樣連接有4根第2分配流路402。各第2分配流路402與互相不同的第1分配流路401合流,該些經由第1分配流路401而連接於氣體噴淋頭部30a~30d側之已經敘述的氣體供給管43a~43d。即使針對各第2分配流路402,也發揮將在第2供給流量調節部41b被流量調節之O2 氣體,分配供給至複數氣體噴淋頭部30a~30d之功能。例如,第2供給流量調節部41b係藉由MFC而構成。In addition, the O 2 gas supply unit 4b corresponds to the second process gas raw material supply unit of the present embodiment (the "second process gas raw material supply unit" shown in Figs. 3 and 5), and the second process gas supply unit 4b supplies the second The gaseous feedstock, i.e., O 2 gas, is treated. On the downstream side of the O 2 gas supply unit 4b, a second supply flow rate adjustment unit 41b for adjusting the flow rate of the O 2 gas supplied to the processing space 100 is provided, and on the downstream side of the second supply flow rate adjustment unit 41b A plurality of, for example, the first distribution flow path 401 are connected via the on-off valve V2, and four second distribution flow paths 402 are also connected. Each of the second distribution channels 402 merges with the first distribution channel 401 that is different from each other, and the gas supply tubes 43a to 43d are connected to the gas shower heads 30a to 30d via the first distribution channel 401. . Even in the second distribution flow path 402, the O 2 gas whose flow rate is adjusted by the second supply flow rate adjustment unit 41b is distributed and supplied to the plurality of gas shower heads 30a to 30d. For example, the second supply flow rate adjustment unit 41b is configured by MFC.

並且,在各第2分配流路402,設置有用以進行被供給至各個的氣體噴淋頭部30a~30d之O2 氣體之流量調節的第2分配流量調節部421b~424b。例如,第2分配流量調節部421b~424b係藉由MFC而構成。   因將在上游側之第2供給流量調節部41b被流量調整之O2 氣體在下游側之第2分配流量調節部421b~424b分配成任意之流量比,故當將在第2供給流量調節部41b之O2 氣體之流量設定值設為F2 ,將在第2分配流量調節部421b~424b之各流量設定值設為f21 ~f24 之時,F2 =f21 +f22 +f23 +f24 之關係成立。Further, in each of the second distribution channels 402, second distribution flow rate adjustment units 421b to 424b for adjusting the flow rate of the O 2 gas supplied to each of the gas shower heads 30a to 30d are provided. For example, the second distribution flow rate adjustment units 421b to 424b are configured by MFC. The second distribution flow rate adjustment units 421b to 424b on the downstream side of the O 2 gas whose flow rate is adjusted by the second supply flow rate adjustment unit 41b on the upstream side are distributed at an arbitrary flow rate ratio, so that the second supply flow rate adjustment unit 41b flow rate of O 2 gas to the set value F 2, when f 21 ~ f 24 of the flow rate setting value set in the allocation of the second portion 421b ~ 424b adjusting the flow rate of, F 2 = f 21 + f 22 + f The relationship between 23 +f 24 was established.

在各第2分配流量調節部421b~424b下游側設置開關閥V41~V44,各第2分配流路402在該些開關閥V41~V44之下游側之位置,與連接於氣體供給管43a~43d之第1分配流路401合流。   此時,將從各第2分配流量調節部421b~424b至複數氣體噴淋頭部30a~30d之氣體流路之長度和剖面積予以統一而使氣體流路之傳導度相等,依此可以從複數氣體噴淋頭部30a~30d更均等地供給氣體。On the downstream side of each of the second distribution flow rate adjustment units 421b to 424b, on-off valves V41 to V44 are provided, and each of the second distribution flow paths 402 is connected to the gas supply pipes 43a to 43d at a position downstream of the on-off valves V41 to V44. The first distribution flow paths 401 merge. At this time, the lengths and cross-sectional areas of the gas flow paths from the respective second distribution flow rate adjusting units 421b to 424b to the plurality of gas shower heads 30a to 30d are unified to make the conductivity of the gas flow paths equal, and thus the The plurality of gas shower heads 30a to 30d supply gas more uniformly.

圖5係表示設置有構成金屬窗3之各氣體噴淋頭部30a~30d,和第1、第2分配流量調節部421a~424a、421b~424b的第1、第2分配流路401、402之連接關係。   當依據圖5時,對於中央部側之氣體噴淋頭部30a及其周圍之氣體噴淋頭部30b,藉由第1分配流量調節部421a、422a、第2分配流量調節部421b、422b進行各氣體之流量調節。Fig. 5 shows first and second distribution flow paths 401 and 402 in which the gas shower heads 30a to 30d constituting the metal window 3 and the first and second distribution flow rate adjustment units 421a to 424a and 421b to 424b are provided. The connection relationship. According to FIG. 5, the gas shower head 30a on the center side and the gas shower head 30b around the center are provided by the first distribution flow rate adjusting units 421a and 422a and the second distribution flow rate adjusting units 421b and 422b. The flow rate of each gas is adjusted.

另外,對於構成周邊部側之角環之邊部的4個周邊氣體噴淋頭部30c,分配供給使用共同的第1、第2分配流量調節部423a、423b而被流量調節的氣體。再者,對於構成上述角環之角部的4個周邊氣體噴淋頭部30d,分配供給使用與邊部側不同之共同的第1、第2分配流量調節部424a、424b而被流量調節的氣體。In addition, the four peripheral gas shower heads 30c constituting the side portions of the corner ring on the side of the peripheral portion are supplied with a gas whose flow rate is adjusted by using the common first and second distributed flow rate adjusting portions 423a and 423b. Further, the four peripheral gas shower heads 30d constituting the corner portions of the corner ring are distributed and supplied with the first and second distributed flow rate adjusting portions 424a and 424b which are different from the side portions, and are adjusted in flow rate. gas.

並且,如圖3所示般,在金屬窗3之上方側配置頂板部61,該頂板部61係藉由被設置在金屬框11上之側壁部63被支持。以金屬窗3、側壁部63及頂板部61所包圍之空間構成天線室50,在天線室50之內部,以面對部分窗30之方式配置有高頻天線5。Further, as shown in FIG. 3, a top plate portion 61 is provided on the upper side of the metal window 3, and the top plate portion 61 is supported by the side wall portion 63 provided on the metal frame 11. The antenna room 50 is constituted by a space surrounded by the metal window 3, the side wall portion 63, and the top plate portion 61, and the high frequency antenna 5 is disposed inside the antenna chamber 50 so as to face the partial window 30.

高頻天線5被配置成經例如無圖示之絕緣構件所構成之間隔件而與部分窗30間隔開。高頻天線5係在與各部分窗30對應之面內,以沿著矩形狀之金屬窗3之周方向環繞之方式,形成漩渦狀(省略平面圖示)。另外,高頻天線5之形狀並不限定於渦旋,即使為使一條或複數之天線線成為環狀之環狀天線亦可。而且,即使採用一面偏移角度一面捲繞複數天線,且使全體成為漩渦狀之多重天線亦可。如此一來,若在與金屬窗3或各部分窗30對應之面內,以沿著其周方向環繞之方式設置天線線時,則不論高頻天線5之構造如何。The high frequency antenna 5 is disposed to be spaced apart from the partial window 30 by a spacer formed of, for example, an insulating member (not shown). The high-frequency antenna 5 is formed in a spiral shape (not shown in a plan view) so as to surround the circumferential direction of the rectangular metal window 3 in a plane corresponding to each of the partial windows 30. Further, the shape of the radio-frequency antenna 5 is not limited to the vortex, and may be a loop antenna in which one or a plurality of antenna wires are annular. Further, even if a plurality of antennas are wound with one side of the offset angle and the entire antenna is formed into a spiral shape. In this way, when the antenna line is provided so as to surround the metal window 3 or each of the partial windows 30 so as to surround the circumferential direction thereof, the structure of the radio-frequency antenna 5 is different.

在各高頻天線5,經由匹配器511連接有第1高頻電源512。在各高頻天線5,從第1高頻電源512經匹配器511被供給例如13.56MHz之高頻電力。依此,在電漿處理之間、部分窗30之各個表面激起渦電流,藉由該渦電流在處理空間100之內部形成感應電場。從氣體吐出孔302被吐出之處理氣體藉由感應電場在處理空間100之內部被電漿化。The first high frequency power supply 512 is connected to each of the high frequency antennas 5 via the matching unit 511. In each of the high-frequency antennas 5, high-frequency power of, for example, 13.56 MHz is supplied from the first high-frequency power source 512 via the matching unit 511. Accordingly, an eddy current is excited between the plasma treatments and the respective surfaces of the partial windows 30, and the eddy current forms an induced electric field inside the processing space 100. The process gas discharged from the gas discharge hole 302 is plasma-treated inside the processing space 100 by an induced electric field.

而且,如圖3所示般,在該電漿處理裝置1設置有控制部6。控制部6係由具備有無圖示之CPU(Central Processing Unit)和記憶部之電腦所構成,在該記憶部記錄有編排用以輸出控制訊號或各流量調節部41a、41b、421a~424a、421b~424b之流量設定值之步驟(命令)群的程式,且該控制訊號係實行使配置有被處理基板G之處理空間100內真空排氣,且使用高頻天線5將蝕刻氣體(處理氣體)予以電漿化而處理被處理基板G的動作。該程式係被儲存於例如硬碟、CD、光磁性碟、記憶卡等之記憶媒體,自此被安裝於記憶部。Further, as shown in FIG. 3, the plasma processing apparatus 1 is provided with a control unit 6. The control unit 6 is composed of a computer including a CPU (Central Processing Unit) and a memory unit (not shown), and is arranged in the memory unit for outputting control signals or flow rate adjusting units 41a, 41b, 421a to 424a, 421b. a program of the step (command) group of the flow rate setting value of 424b, and the control signal performs vacuum evacuation in the processing space 100 in which the substrate G to be processed is disposed, and the etching gas (processing gas) is used using the high frequency antenna 5. The operation of the substrate G to be processed is processed by plasma. The program is stored in a memory medium such as a hard disk, a CD, a magneto-optical disk, a memory card, etc., and is installed in the memory unit.

針對具備以上說明之構成之電漿處理裝置1之作用進行說明。   首先,打開閘閥102,從相鄰之真空搬運室藉由搬運機構(任一者皆無圖示),經搬入搬出口101將被處理基板G搬入至處理空間100內。接著,在載置台13上載置被處理基板G,藉由無圖示之靜電夾具固定,另外,使上述搬運機構從處理空間100退避而關閉閘閥102。The operation of the plasma processing apparatus 1 having the configuration described above will be described. First, the gate valve 102 is opened, and the substrate to be processed G is carried into the processing space 100 through the loading/unloading port 101 from the adjacent vacuum transfer chamber by a transport mechanism (none of which is not shown). Then, the substrate G to be processed is placed on the mounting table 13 and fixed by an electrostatic chuck (not shown), and the transport mechanism is retracted from the processing space 100 to close the gate valve 102.

然後,開啟各開關閥V1、V2、V31~V34、V41~V44,開始供給分別藉由第1供給流量調節部41a、第2供給流量調節部41b而被流量調節的CF4 氣體、O2 氣體。   O2 氣體係在4個第2分配流路402被分流,在第2分配流量調節部421b~424b被流量調節之後,在第1分配流路401合流。另外,CF4 氣體係在4個第1分配流路401被分流,在第1分配流量調節部421a~424a被流量調節之後,與從第2分配流路402側被供給之O2 氣體混合。Then, each of the on-off valves V1, V2, V31 to V34, and V41 to V44 is turned on to supply CF 4 gas and O 2 gas whose flow rate is adjusted by the first supply flow rate adjustment unit 41a and the second supply flow rate adjustment unit 41b, respectively. . The O 2 gas system is branched in the four second distribution channels 402, and after the second distribution flow rate adjustment units 421b to 424b are adjusted in flow rate, they are merged in the first distribution channel 401. In addition, the CF 4 gas system is branched in the four first distribution channels 401, and after the first distribution flow rate adjustment units 421a to 424a are adjusted in flow rate, they are mixed with the O 2 gas supplied from the second distribution channel 402 side.

針對CF4 氣體、O2 氣體分別藉由第1供給流量調節部41a、第2供給流量調節部41b及第1分配流量調節部421a~424a、第2分配流量調節部421b~424b,藉由在分流之前後,進行2階段之流量調節,可以以比較簡易的構成,以互相獨立之任意比例混合從第1、第2處理氣體原料供給部所取得之第1、第2處理氣體原料,而供給至被處理基板之各位置。其結果,可以對玻璃基板701之每一個區域,以對應光阻膜704之端部之傾斜的O2 氣體/CF4 氣體之流量比進行蝕刻處理。   混合CF4 氣體和O2 氣體而取得的蝕刻氣體,係經氣體供給管43a~43d而被導入至各氣體噴淋頭部30a~30d之氣體擴散室301。The CF 4 gas and the O 2 gas are respectively supplied by the first supply flow rate adjustment unit 41a, the second supply flow rate adjustment unit 41b, the first distribution flow rate adjustment units 421a to 424a, and the second distribution flow rate adjustment units 421b to 424b. After the two-stage flow rate adjustment, the first and second process gas raw materials obtained from the first and second process gas raw material supply units are mixed in an arbitrary ratio and supplied to each other in a relatively simple configuration. To each position of the substrate to be processed. As a result, etching treatment can be performed on each of the regions of the glass substrate 701 at a flow ratio of the O 2 gas/CF 4 gas corresponding to the inclination of the end portion of the photoresist film 704. The etching gas obtained by mixing the CF 4 gas and the O 2 gas is introduced into the gas diffusion chamber 301 of each of the gas shower heads 30a to 30d via the gas supply pipes 43a to 43d.

當針對O2 氣體/CF4 氣體之流量比予以敘述時,被分配至氣體噴淋頭部30a之蝕刻氣體被調節成O2 氣體/CF4 氣體=1:3~3:2之範圍內的值,被分配至周邊氣體噴淋頭部30c、30d之蝕刻氣體被調節成O2 氣體/CF4 氣體=1:3~3:2之範圍內的值。而且,針對被分配至位於氣體噴淋頭部30a和周邊氣體噴淋頭部30c、30d之間的氣體噴淋頭部30b的蝕刻氣體,O2 氣體/CF4 氣體之流量比被調節至上述各範圍內的值。   再者,如後述般,邊部之周邊氣體噴淋頭部30c,和角部之周邊氣體噴淋頭部30d即使供給O2 氣體/CF4 氣體之流量比互相不同的蝕刻氣體亦可。When the flow ratio of the O 2 gas/CF 4 gas is described, the etching gas distributed to the gas shower head 30a is adjusted to be in the range of O 2 gas / CF 4 gas = 1:3 to 3:2. The value of the etching gas to be distributed to the peripheral gas shower heads 30c and 30d is adjusted to a value in the range of O 2 gas / CF 4 gas = 1:3 to 3:2. Further, with respect to the etching gas distributed to the gas shower head 30b located between the gas shower head 30a and the peripheral gas shower heads 30c, 30d, the flow ratio of the O 2 gas / CF 4 gas is adjusted to the above Values in each range. Further, as will be described later, the peripheral gas shower head portion 30c of the side portion and the peripheral gas shower head portion 30d of the corner portion may supply an etching gas having a flow ratio of O 2 gas/CF 4 gas different from each other.

另外,在容器本體10側,藉由真空排氣部12進行處理空間100內之真空排氣,將處理空間100內調節至例如0.66~26.6Pa左右之壓力氛圍。再者,進行被載置於載置台13上之被處理基板G之溫度調節,同時對被處理基板G之背面側,供給熱傳達用之He氣體。Further, on the container main body 10 side, the vacuum exhaust unit 12 performs vacuum evacuation in the processing space 100 to adjust the inside of the processing space 100 to a pressure atmosphere of, for example, about 0.66 to 26.6 Pa. In addition, the temperature of the substrate G to be processed placed on the mounting table 13 is adjusted, and He gas for heat transfer is supplied to the back side of the substrate G to be processed.

接著,從第1高頻電源512對高頻天線5施加高頻電力,依此經金屬窗3在處理空間100內生成均勻之感應電場。其結果,藉由感應電場,蝕刻氣體在處理空間100內電漿化,生成高密度之感應耦合電漿。而且,藉由從第2高頻電源152被施加至載置台13之偏壓用之高頻電力,電漿中之離子朝向被處理基板G被導入,進行被處理基板G之蝕刻處理。Next, high-frequency power is applied to the high-frequency antenna 5 from the first high-frequency power source 512, whereby a uniform induced electric field is generated in the processing space 100 via the metal window 3. As a result, the etching gas is plasmatized in the processing space 100 by the induced electric field to generate a high-density inductively coupled plasma. By the high-frequency power for bias applied to the mounting table 13 from the second high-frequency power source 152, ions in the plasma are introduced toward the substrate G to be processed, and etching of the substrate G to be processed is performed.

此時,第1、第2分配流量調節部421a~424a、421b~424b,以比起位於天頂面亦即金屬窗3之周邊部側之周邊氣體噴淋頭部30c、30d,從位於中央部側之氣體噴淋頭部30b、30a被供給之蝕刻氣體中之O2 氣體濃度較高之方式,分別進行CF4 氣體、O2 氣體之流量設定。   換言之,第1、第2分配流量調節部421a~424a、421b~424b係因應被圖案製作於SiO膜702或SiN膜703(蝕刻對象膜)之上面側的光阻膜704之端部之錐度之大小互相不同的區域,以比起對該錐度大之區域供給蝕刻氣體之位置的氣體噴淋頭部30c、30d,從對錐度小之區域,供給蝕刻氣體之位置的氣體噴淋頭部30b、30a被供給之蝕刻氣體中之氧濃度較高之方式,分別設定CF4 氣體、O2 氣體之流量。At this time, the first and second distribution flow rate adjustment units 421a to 424a and 421b to 424b are located at the center portion from the peripheral gas shower heads 30c and 30d located on the zenith surface, that is, the peripheral portion side of the metal window 3 The flow rate of CF 4 gas and O 2 gas is set to be higher so that the concentration of O 2 gas in the etching gas supplied from the gas shower heads 30b and 30a on the side is higher. In other words, the first and second distribution flow rate adjustment units 421a to 424a and 421b to 424b are tapered in accordance with the end portion of the photoresist film 704 on the upper surface side of the SiO film 702 or the SiN film 703 (etching target film). The gas shower heads 30b and 30d which are different in size from each other, and the gas shower heads 30c and 30d which supply the position of the etching gas to the region where the taper is large, the gas shower head 30b which supplies the position of the etching gas from the region where the taper is small, The flow rate of CF 4 gas and O 2 gas is set so that the oxygen concentration in the etching gas supplied to 30a is high.

藉由上述CF4 氣體、O2 氣體之流量設定,在端部之錐度大的光阻膜704被圖案製作之被處理基板G之周邊部側之區域(圖1(a)),能夠使用O2 氣體之濃度低之蝕刻氣體而進行蝕刻處理。其結果,可以在良好之狀態下蝕刻除去玻璃基板701之SiO膜702、SiN膜703(圖1(b))。By the flow rate setting of the CF 4 gas and the O 2 gas, the region on the peripheral side of the substrate G to be processed (the FIG. 1(a)) is patterned on the photoresist film 704 having a large taper at the end portion, and O can be used. 2 of the low-concentration gas etch gas for etching. As a result, the SiO film 702 and the SiN film 703 of the glass substrate 701 can be removed and removed in a good state (FIG. 1(b)).

此時,藉由周邊部側之邊部之周邊氣體噴淋頭部30c,和角部之周邊氣體噴淋頭部30d被連接於不同之第1、第2分配流量調節部423a、424a、423b、424b,亦可以使被供給至各周邊氣體噴淋頭部30c、30d之蝕刻氣體中之O2 氣體之濃度不同。At this time, the peripheral air shower head 30c of the side portion on the peripheral portion side and the peripheral gas shower head portion 30d at the corner portion are connected to the different first and second distribution flow rate adjusting portions 423a, 424a, and 423b. Further, 424b may have different concentrations of O 2 gas in the etching gas supplied to each of the peripheral gas shower heads 30c and 30d.

另外,圖案製作有端部之錐度小之光阻膜704的被處理基板G之中央部側之區域中(圖2(a)),能夠使用O2 氣體之濃度高的蝕刻氣體而進行蝕刻處理。其結果,可以在良好之狀態下從玻璃基板701蝕刻除去SiO膜702、SiN膜703(圖2(c))。Further, in the region where the central portion side of the substrate G to be processed of the photoresist film 704 having a small tapered portion is formed in the pattern (Fig. 2(a)), etching treatment can be performed using an etching gas having a high concentration of O 2 gas. . As a result, the SiO film 702 and the SiN film 703 can be removed from the glass substrate 701 in a good state (Fig. 2(c)).

而且,若僅以事先設定的時間進行電漿處理時,即使停止從各高頻電源512、152供給電力,及從CF4 氣體供給部4a、O2 氣體供給部4b供給CF4 氣體、O2 氣體,亦進行從處理空間100內進行排氣處理。之後,以與搬入時相反之順序,搬出被處理基板G。Further, if the preset time only for plasma processing, even when stopping the supply of power from each of the high-frequency power source 512,152, and CF 4 gas is supplied from a CF 4 gas supply portion 4a, O 2 gas supplying unit 4b, O 2 The gas is also subjected to exhaust treatment from within the processing space 100. Thereafter, the substrate G to be processed is carried out in the reverse order of the loading.

若藉由與本實施形態有關之電漿處理裝置1時,則有以下之效果。在CF4 氣體供給部4a、O2 氣體供給部4b分別設置進行CF4 氣體、O2 氣體之流量調節的第1、第2供給流量調節部41a、41b,並且,即使對將該些CF4 氣體、O2 氣體分配至複數氣體噴淋頭部30a~30d的複數第1、第2分配流路401、402,也分別設置有第1、第2分配流量調節部421a~424a、421b~424b。其結果,能夠以任意之比例混合從共同的CF4 氣體供給部4a、O2 氣體供給部4b所取得之CF4 氣體、O2 氣體,可以將該些氣體以期待之比例被混合後的蝕刻氣體,供給至被處理基板G之各位置。依此,即使因應被處理基板G之被處理面之位置被圖案製作之光阻膜704之縱剖面形狀不同之情況下,因可以將CF4 氣體和O2 氣體以與其縱剖面形狀對應之流量比供給至複數氣體噴淋頭部30a~30d之每一個,故可以取得良好的蝕刻處理結果。When the plasma processing apparatus 1 according to the present embodiment is used, the following effects are obtained. The CF 4 gas supply unit 4a and the O 2 gas supply unit 4b are provided with first and second supply flow rate adjustment units 41a and 41b for adjusting the flow rates of the CF 4 gas and the O 2 gas, respectively, and even for the CF 4 The gas and O 2 gas are distributed to the plurality of first and second distribution channels 401 and 402 of the plurality of gas shower heads 30a to 30d, and the first and second distribution flow rate adjustment units 421a to 424a and 421b to 424b are also provided. . As a result, it can be mixed in any proportion 4a, O 2 gas supply unit of the CF 4 gas is made from a common CF 4 gas supply portion 4b, O 2 gas, these gases may be at a ratio of the etch is expected after mixing The gas is supplied to each position of the substrate G to be processed. According to this, even if the longitudinal cross-sectional shape of the photoresist film 704 which is patterned in accordance with the position of the surface to be processed of the substrate G to be processed is different, the flow rate of the CF 4 gas and the O 2 gas corresponding to the longitudinal cross-sectional shape thereof can be made. Since the ratio is supplied to each of the plurality of gas shower heads 30a to 30d, a good etching treatment result can be obtained.

在此,被構成能夠從複數氣體噴淋頭部30a~30d供給O2 濃度不同之蝕刻氣體的上述電漿處理裝置1,並不限定於使用圖1、圖2說明的其情況,亦即在錐形殘渣71a或蝕刻殘渣71b之殘存成為問題的製程中,在良好狀態下除去蝕刻對象膜(在上述例中,為含矽膜亦即SiO膜702或SiN膜703)之蝕刻處理的情況。   例如,被形成在光阻膜704之端部的已經敘述的傾斜,被轉印至蝕刻處理後之圖案之時,以對齊被轉印之傾斜的錐形為目的,亦可以利用上述電漿處理裝置1。Here, the plasma processing apparatus 1 configured to be able to supply etching gases having different O 2 concentrations from the plurality of gas shower heads 30a to 30d is not limited to the case described with reference to FIGS. 1 and 2, that is, In the process in which the residual of the tapered residue 71a or the etching residue 71b is a problem, the etching process of the etching target film (in the above example, the SiO film 702 or the SiN film 703 which is a ruthenium film) is removed in a good state. For example, when the already described inclination formed at the end portion of the photoresist film 704 is transferred to the pattern after the etching treatment, it is also possible to align the tapered shape to be transferred, and it is also possible to use the above-mentioned plasma treatment. Device 1.

圖6(a)、7(a)係表示被進行薄膜電晶體之形成的被處理基板G中,在多晶矽或鉬亦即蝕刻對象膜707之上面圖案製作光阻膜704之例(省略蝕刻對象膜707之下層側之記載)。(a) and (a) of FIG. 6 show an example in which a photoresist film 704 is patterned on a substrate G to be processed, which is formed of a thin film transistor, or a molybdenum, that is, an etching target film 707. The description of the lower layer side of the film 707).

多晶矽膜或鉬膜亦即蝕刻對象膜707可以使用使包含從第1處理氣體亦即四氟化碳(CF4 )氣體、六氟化硫(SF6 )氣體、三氟化氮(NF3 )氣體或氯(Cl2 )氣體選擇至少一個的氣體,和第2處理氣體亦即氧(O2 )之氣體電漿化的蝕刻氣體而予以除去。   在本例中,針對與已經敘述的含矽膜(SiO膜702或SiN膜703)之除去相同,針對使用含CF4 氣體和O2 氣體之蝕刻氣體除去上述蝕刻對象膜707之情況予以說明。The polycrystalline tantalum film or the molybdenum film, that is, the etching target film 707 can be used to include a carbon tetrafluoride (CF 4 ) gas, a sulfur hexafluoride (SF 6 ) gas, and a nitrogen trifluoride (NF 3 ) gas from the first processing gas. The gas or the chlorine (Cl 2 ) gas is selected by removing at least one of the gases and the etching gas of the second process gas, that is, the gas of oxygen (O 2 ). In the present example, the case where the etching target film 707 is removed using an etching gas containing CF 4 gas and O 2 gas will be described in the same manner as the removal of the ruthenium-containing film (SiO film 702 or SiN film 703).

在此,光阻膜704膜之錐度,也有受到光阻膜704之塗佈、顯像製程之影響的情況,依該製程不同,也有與圖1(a)、2(a)所示之例相反,在被處理基板G之中央部側,錐度變大,在周邊部側錐度變小之情況。圖6(a)、7(a)表示如此之例。Here, the taper of the film of the photoresist film 704 may be affected by the coating and development process of the photoresist film 704. Depending on the process, there are also examples shown in FIGS. 1(a) and 2(a). On the other hand, on the central portion side of the substrate G to be processed, the taper becomes large, and the taper on the peripheral portion side becomes small. Figures 6(a) and 7(a) show such an example.

如此一來,對於形成有錐度不同之光阻膜704之被處理基板G,例如在被處理基板G之全面,供給CF4 氣體/O2 氣體之混合比(O2 混合比濃度)相等之蝕刻氣體而進行蝕刻處理之情況進行研討。   在利用光阻膜704之蝕刻處理中,藉由蝕刻氣體所含的O2 氣體之作用,使光阻膜704逐漸地灰化,並且進行蝕刻對象膜707之蝕刻。因此,藉由控制蝕刻氣體所含之O2 氣體之濃度,可以變更在蝕刻對象膜707之蝕刻中之光阻膜704之灰化率。In this manner, for the substrate G to be processed on which the tapered photoresist film 704 is formed, for example, etching of the CF 4 gas/O 2 gas mixture ratio (O 2 mixing ratio concentration) is equal to the total of the substrate G to be processed. The case where the gas was etched was examined. In the etching treatment using the photoresist film 704, the photoresist film 704 is gradually ashed by the action of the O 2 gas contained in the etching gas, and etching of the etching target film 707 is performed. Therefore, by controlling the concentration of the O 2 gas contained in the etching gas, the ashing rate of the photoresist film 704 in the etching of the etching target film 707 can be changed.

此時,當在被處理基板G之中央部側和周邊部側之間,蝕刻氣體中之O2 氣體之濃度幾乎相等時,在各位置之光阻膜704之每單位時間之灰化量幾乎相同的條件下,進行蝕刻。   其結果,因在維持光阻膜704之錐度不同的狀態下進行蝕刻,故即使針對被轉印至圖案707a之錐度,也成為在被處理基板G之面內不同的狀態。即是,產生被形成在被處理基板G之中央部側的圖案707a之端部的錐角θ1 ,大於被形成在周邊部側之圖案707a之端部的錐角θ2 的不一致(圖6(b)、7(b))。At this time, when the concentration of the O 2 gas in the etching gas is almost equal between the central portion side and the peripheral portion side of the substrate G to be processed, the amount of ashing per unit time of the photoresist film 704 at each position is almost Etching is performed under the same conditions. As a result, since the etching is performed while maintaining the taper of the photoresist film 704, the taper to the pattern 707a is different in the surface of the substrate G to be processed. In other words, the taper angle θ 1 at the end portion of the pattern 707a formed on the central portion side of the substrate G to be processed is larger than the taper angle θ 2 at the end portion of the pattern 707a formed on the peripheral portion side ( FIG. 6 (b), 7(b)).

另外,藉由來自接著蝕刻處理之後段處理的要求等,也有需要盡可能地地使多晶矽或鉬之圖案707a之錐度在被處理基板G之面內一致的情形。使用圖3說明的電漿處理裝置1即使在如此之情況下亦可以活用。   在此情況下,第1分配流量調節部421a~424a係以在特定之處理時間內完成蝕刻處理之方式,分別被進行CF4 氣體之流量設定。再者,第2分配流量調節部421b~424b,以比起位於天頂面亦即金屬窗3之周邊部側之周邊氣體噴淋頭部30c、30d,從位於中央部側之氣體噴淋頭部30b、30a被供給之蝕刻氣體中之O2 氣體濃度較高之方式,分別進行O2 氣體之流量設定。Further, it is also necessary to make the taper of the pattern 707a of polycrystalline germanium or molybdenum uniform in the plane of the substrate G to be processed as much as possible by the subsequent processing from the subsequent etching process. The plasma processing apparatus 1 explained using Fig. 3 can be used even in such a case. In this case, the first distribution flow rate adjustment units 421a to 424a perform the flow rate setting of the CF 4 gas so that the etching process is completed within a specific processing time. Further, the second distribution flow rate adjusting units 421b to 424b are from the gas shower head located on the center side of the peripheral gas shower heads 30c and 30d on the side of the zenith surface, that is, on the peripheral side of the metal window 3. The flow rate of the O 2 gas is set to be higher so that the concentration of the O 2 gas in the supplied etching gas is higher in 30b and 30a.

換言之,第1、第2分配流量調節部421a~424a、421b~424b,以比起對被圖案製作於蝕刻對象膜707之上面側之光阻膜704之端部之錐度小的區域,供給蝕刻氣體之位置的氣體噴淋頭部30c、30d,從對上述錐度大的區域供給蝕刻氣體之位置的氣體噴淋頭部30b、30a被供給之蝕刻氣體中之氧濃度較高之方式,分別設定CF4 氣體、O2 氣體之流量。In other words, the first and second distribution flow rate adjustment units 421a to 424a and 421b to 424b are etched in a region smaller than the taper of the end portion of the photoresist film 704 which is patterned on the upper surface side of the etching target film 707. The gas shower heads 30c and 30d at the position of the gas are set so as to have a high oxygen concentration in the etching gas supplied from the gas shower heads 30b and 30a at the position where the etching gas is supplied to the region having the large taper. The flow rate of CF 4 gas and O 2 gas.

藉由上述CF4 氣體、O2 氣體之流量設定,使用圖案製作有錐度大之光阻膜704的被處理基板G之中央部側之區域(圖6(a))中,使用O2 氣體之濃度高的蝕刻氣體,進行蝕刻處理,被圖案製作有錐度小之光阻膜704的被處理基板G之周緣部側之區域(圖7(a))中,使用O2 氣體之濃度低之蝕刻氣體而進行蝕刻處理。By setting the flow rate of the CF 4 gas and the O 2 gas, a region on the central portion side of the substrate G to be processed (see FIG. 6( a )) in which the tapered photoresist film 704 is formed by using a pattern is used, and O 2 gas is used. The etching gas having a high concentration is etched, and the region on the peripheral edge side of the substrate G to be processed which is patterned with the tapered thin photoresist film 704 is patterned (Fig. 7 (a)), and etching using a low concentration of O 2 gas is used. The gas is etched.

此時,因錐角大的光阻膜704之灰化速度,大於錐角小之光阻膜704,故在各區域之錐角差異被減緩的方向進行灰化。其結果,可以邊使利用該些光阻膜704所形成之圖案707a之端部的錐度θ’1 、θ’2 互相接近,邊進行蝕刻(圖6(c)、圖7(c))。At this time, since the ashing speed of the photoresist film 704 having a large taper angle is larger than the photoresist film 704 having a small taper angle, ashing is performed in a direction in which the difference in the taper angle of each region is slowed down. As a result, the taper θ' 1 and θ' 2 of the end portion of the pattern 707a formed by the photoresist film 704 can be etched while being close to each other (Fig. 6 (c), Fig. 7 (c)).

接著,一面參照圖8、9,一面針對與第2實施形態有關之電漿處理裝置1a之構程及適用製程予以說明。   圖8(a)係表示處理對象之被處理基板G之上面之放大縱剖側視圖。該被處理基板G中,在玻璃基板701上,形成厚度為數百nm左右的鋁膜705,更在其上面形成數十nm左右的SiO2 膜706。Next, the configuration and application process of the plasma processing apparatus 1a according to the second embodiment will be described with reference to Figs. Fig. 8 (a) is an enlarged longitudinal sectional side view showing the upper surface of the substrate G to be processed. In the substrate G to be processed, an aluminum film 705 having a thickness of about several hundred nm is formed on the glass substrate 701, and an SiO 2 film 706 having a thickness of about several tens of nanometers is formed thereon.

而且,在SiO2 膜706之上面,被圖案製作用以將該些鋁膜705、SiO2 膜706之疊層膜蝕刻成線與間隙狀之光阻膜704a。光阻膜704a被圖案製作成線與間隙之線寬及間隙寬分別成為數十nm左右。Further, on the upper surface of the SiO 2 film 706, a patterned film for etching the aluminum film 705 and the SiO 2 film 706 is formed into a line and gap-shaped photoresist film 704a. The photoresist film 704a is patterned such that the line width and the gap width of the line and the gap are about several tens nm.

藉由對具備上述構成之被處理基板G,供給一種第1處理氣體原料,既也係主要蝕刻氣體的氯(Cl2 )氣,和一種第2處理氣體原料,作為既也係添加氣體的氮(N2 )氣及含鹵氣體的添加氣體(以下,也稱為「含鹵添加氣體」)例如含三氟甲烷(CHF3 )之氣體並使予以電漿化,進行除去不藉由光阻膜704a被覆蓋之區域的鋁膜705、SiO2 膜706之蝕刻處理。在此,含有鹵添加氣體,雖然舉使用三氟甲烷(CHF3 )之例,但是可以使用CF4 、C2 HF5 、C4 F8 、BCl3 、HCl等。By supplying the first processing gas raw material to the substrate G to be processed having the above-described configuration, the chlorine (Cl 2 ) gas which is the main etching gas and the second processing gas raw material are used as the nitrogen which is added as the gas. (N 2 ) gas and an additive gas containing a halogen-containing gas (hereinafter also referred to as "halogen-containing additive gas"), for example, a gas containing trifluoromethane (CHF 3 ) and being plasma-treated to be removed without being blocked by a photoresist The film 704a is etched by the aluminum film 705 and the SiO 2 film 706 in the covered region. Here, the halogen-added gas is used, and although trifluoromethane (CHF 3 ) is used, CF 4 , C 2 HF 5 , C 4 F 8 , BCl 3 , HCl, or the like can be used.

針對進行上述處理之被處理基板G,本發明者發現因應被處理基板G之被處理面內之位置,有容易進行蝕刻處理之區域,和藉由蝕刻處理難取得期望之線與間隙圖案72的區域之情形。With respect to the substrate G to be processed which has been subjected to the above-described processing, the inventors of the present invention have found that it is easy to perform an etching treatment in accordance with the position in the surface to be processed of the substrate G to be processed, and it is difficult to obtain a desired line and gap pattern 72 by etching. The situation of the area.

例如,在被處理基板G之周邊部側,如圖8(b)所示般,形成比較良好之線與間隙圖案72,另外,在被處理基板G之中央部側,如圖8(c)所示般,形成有蝕刻不良所致的不完全圖案73。   在被處理基板G之中央部側,形成不完全圖案73的理由,預測應該係比起被處理基板G之周邊部側,光阻膜704a被蝕刻所生成的碳量比較多,再者,由於所生成之碳的排氣能力低,故該些碳附著在不藉由光阻膜704a被覆蓋的鋁膜705、SiO2 膜706上之主蝕刻氣體亦即Cl2 氣體所致的蝕刻處理被抑制所導致。For example, on the peripheral portion side of the substrate G to be processed, as shown in FIG. 8(b), a relatively good line and gap pattern 72 is formed, and on the central portion side of the substrate G to be processed, as shown in FIG. 8(c) As shown, an incomplete pattern 73 due to poor etching is formed. The reason why the incomplete pattern 73 is formed on the central portion side of the substrate G to be processed is predicted to be larger than the amount of carbon generated by etching the photoresist film 704a on the peripheral portion side of the substrate G to be processed. The generated carbon has a low exhausting ability, so that the carbon is adhered to the aluminum film 705 which is not covered by the photoresist film 704a, and the etching process by the main etching gas, that is, Cl 2 gas, on the SiO 2 film 706 is Inhibition caused.

於是,與第2實施形態有關之電漿處理裝置1a具備使用被分割成複數的氣體噴淋頭部30a~30d,能夠對被處理基板G之各區域,供給不同流量之蝕刻氣體的構成。   圖9係示意性表示從第1處理氣體原料供給部亦即Cl2 氣體供給部4c(在圖9中以「第1處理氣體原料供給部」表示),及第2處理氣體原料供給部亦即N2 氣體供給部4d、含鹵添加氣體供給部4e(在圖9中分別「第2處理氣體原料供給部(1)、第2處理氣體原料供給部(2)表示」,朝各氣體噴淋頭部30a~30d供給各氣體的供給路徑。另外,電漿處理裝置1a之具體裝置構成因與使用圖3、4說明的電漿處理裝置1之情形相同,故省略再次說明。再者,在圖9所載之電漿處理裝置1a,及後述圖10所載之電漿處理裝置1b中,對於與使用圖3、4說明內容共同的構成要素,標示與在該些圖中所使用之符號相同的符號。Then, the plasma processing apparatus 1a according to the second embodiment includes a gas shower heads 30a to 30d divided into a plurality of portions, and is configured to supply etching gas having a different flow rate to each region of the substrate G to be processed. FIG. 9 is a view schematically showing a Cl 2 gas supply unit 4 c (shown as “first processing gas raw material supply unit” in FIG. 9 ), and a second processing gas raw material supply unit, that is, a first processing gas raw material supply unit. The N 2 gas supply unit 4d and the halogen-containing additive gas supply unit 4e (indicated by the second processing gas raw material supply unit (1) and the second processing gas raw material supply unit (2), respectively, in FIG. The heads 30a to 30d are supplied with the supply paths of the respective gases. The specific device configuration of the plasma processing apparatus 1a is the same as that of the plasma processing apparatus 1 described with reference to Figs. 3 and 4, and therefore will not be described again. In the plasma processing apparatus 1a shown in Fig. 9, and the plasma processing apparatus 1b shown in Fig. 10 which will be described later, the components common to those described with reference to Figs. 3 and 4 are denoted by the symbols used in the drawings. The same symbol.

圖9所示之電漿處理裝置1a係在第1、第2處理氣體原料之氣體種類不同之點,及混合從N2 氣體供給部4d、含鹵添加氣體供給部4e被供給之2種類的氣體之後,在第2分配流路402被分流之點,與已經敘述之第1實施形態有關的電漿處理裝置1不同。再者,在本例中,以N2 氣體/含鹵添加體之流量比在氣體噴淋頭部30a~30d間設為相同,另外,可以使從各氣體噴淋頭部30a~30d分配Cl2 氣體之分配比不同之方式,進行藉由第1、第2分配流量調節部421a~424a、421b~424b的流量調節。The plasma processing apparatus 1a shown in Fig. 9 is a type in which the gas types of the first and second process gas raw materials are different, and the two types of the gas are supplied from the N 2 gas supply unit 4d and the halogen-containing additive gas supply unit 4e. After the gas, the second distribution channel 402 is branched, which is different from the plasma processing apparatus 1 according to the first embodiment described above. Further, in this example, the flow ratio of the N 2 gas/halogen-containing additive is the same between the gas shower heads 30a to 30d, and Cl can be distributed from each of the gas shower heads 30a to 30d. The flow rate adjustment by the first and second distribution flow rate adjustment units 421a to 424a and 421b to 424b is performed in a manner in which the gas distribution ratio is different.

若藉由具備上述構成之電漿處理裝置1a時,依據在位於蝕刻時因光阻膜704a所引起的碳容易附著的被處理基板G之中央部側的氣體噴淋頭部30a,使對主蝕刻氣體亦即Cl2 氣體分配添加氣體亦即N2 氣體及含鹵添加氣體之分配比,較位於周邊部側之周邊氣體噴淋頭部30c、30d小,能夠抑制因光阻膜704a所引起之碳的附著而能夠取得良好的線與間隙圖案72。   再者,能夠在圓周方向被分割的周邊氣體噴淋頭部30c、30d間,使第1處理氣體原料亦即主蝕刻氣體和第2處理氣體原料亦即添加氣體之供給流量不同。When the plasma processing apparatus 1a having the above-described configuration is provided, the gas shower head 30a on the central portion side of the substrate G to be processed which is likely to adhere to the carbon due to the photoresist film 704a at the time of etching is used. The distribution ratio of the etching gas, that is, the Cl 2 gas distribution additive gas, that is, the N 2 gas and the halogen-containing additive gas, is smaller than the peripheral gas shower heads 30c and 30d on the peripheral portion side, and can be suppressed by the photoresist film 704a. A good line and gap pattern 72 can be obtained by the adhesion of carbon. In addition, the supply flow rate of the main processing gas raw material, that is, the main etching gas and the second processing gas raw material, that is, the additive gas, can be made different between the peripheral gas shower heads 30c and 30d divided in the circumferential direction.

以上,在使用與圖3、4、7說明的第1、第2實施形態有關之電漿處理裝置1、1a中,針對位於最外周側之角環狀區域的周邊氣體噴淋頭部30c、周邊氣體噴淋頭部30d,雖然表示在圓周方向分割之例,但是朝圓周方向分割的周邊氣體噴淋頭部30c、周邊氣體噴淋頭部30d並不限定於最外周側之區域。As described above, in the plasma processing apparatuses 1 and 1a according to the first and second embodiments described with reference to FIGS. 3, 4 and 7, the peripheral gas shower head 30c located in the angular annular region on the outermost peripheral side, The peripheral gas shower head 30d is an example of division in the circumferential direction, but the peripheral gas shower head 30c and the peripheral gas shower head 30d which are divided in the circumferential direction are not limited to the outermost peripheral side.

即使在徑向4分割天頂面亦即部分窗30,且在圓周方向分割比起最外周一個內側的各環狀區域而配置周邊氣體噴淋頭部30c、30d亦可。   例如,若為位於較從部分窗30之中心位置至周邊位置之距離之1/2更外周側的區域內時,藉由設置在周方向被分割之周邊氣體噴淋頭部30c、30d,可以謀求因應與排氣口103之位置關係而提升藉由蝕刻氣體(處理氣體)之流量比調節、供給流量調整的處理結果。Even if the partial window 30 is divided into the zenith surface in the radial direction, the peripheral gas shower heads 30c and 30d may be disposed in the circumferential direction in each of the annular regions on the innermost side of the outermost circumference. For example, when it is located in a region which is located on the outer peripheral side of 1/2 of the distance from the center position of the partial window 30 to the peripheral position, by providing the peripheral gas shower heads 30c and 30d which are divided in the circumferential direction, In response to the positional relationship with the exhaust port 103, the processing result of adjusting the flow rate ratio of the etching gas (process gas) and adjusting the supply flow rate is improved.

另外,無須在位於部分窗30之外周側之周方向進行分割。如圖10之電漿處理裝置1b所示般,針對被配置在徑向分割矩形狀之部分窗30而形成的外周側之區域的氣體噴淋頭部30e,即使不進行圓周方向之分割,而進行從角環狀之氣體噴淋頭部30e供給處理氣體亦可。In addition, it is not necessary to divide in the circumferential direction of the outer peripheral side of the partial window 30. As shown in the plasma processing apparatus 1b of FIG. 10, the gas shower head 30e disposed in the region on the outer peripheral side formed by dividing the rectangular partial window 30 in the radial direction is not divided in the circumferential direction. The processing gas may be supplied from the gas shower head 30e of the angular ring shape.

圖10係表示藉由將包含第1處理氣體原料亦即四氟化矽(SiF4 )氣體及四氯化矽(SiCl4 )氣體,和第2處理氣體原料亦即氮(N2 )氣體或氧(O2 )氣體的成膜氣體電漿化並予以供給,在被處理基板G上進行SiO2 膜或SiN膜之成膜處理的電漿處理裝置1b之構成例。Fig. 10 is a view showing that a first processing gas raw material, i.e., a silicon tetrafluoride (SiF 4 ) gas and a silicon tetrachloride (SiCl 4 ) gas, and a second processing gas raw material, that is, nitrogen (N 2 ) gas or An example of the configuration of the plasma processing apparatus 1b in which the film forming gas of the oxygen (O 2 ) gas is plasma-treated and supplied to form a film of SiO 2 film or SiN film on the substrate G to be processed.

在圖10中,例示設置SiC14 氣體供給部4f和SiF4 氣體供給部4h作為第1處理氣體原料供給部(在圖10中分別表示「第1處理氣體原料供給部(1)、第1處理氣體原料供給部(2)」,設置N2 氣體供給部4g和O2 氣體供給部4i作為第2處理氣體原料供給部之情況(在圖10中分別表示「第2處理氣體原料供給部(1)、第2處理氣體原料供給部(2)」。在SiCl4 氣體供給部4f及SiF4 氣體供給部4h之下游側,分別設置第1供給流量調節部41a、41c,進一步在第1供給流量調節部41a、41c之下游側,經開關閥V1、V3而共同連接有3條第1分配流路401。再者,在N2 氣體供給部4g及O2 氣體供給部4i之下游側,分別設置第1供給流量調節部41b、41d,進一步在第1供給流量調節部41b、41d之下游側,經開關閥V2、V4而共同連接有3條第2分配流路402。In FIG 10, illustrates a set SiC 1 4 gas supply portion 4f and 4 gas supply portion SiF 4h as the first process gas material supply section (in FIG. 10 respectively as "the first process gas material supply section (1), the first processing In the gas raw material supply unit (2), the N 2 gas supply unit 4g and the O 2 gas supply unit 4i are provided as the second processing gas raw material supply unit (the second processing gas raw material supply unit is shown in Fig. 10). The second processing gas raw material supply unit (2). The first supply flow rate adjusting units 41a and 41c are provided on the downstream side of the SiCl 4 gas supply unit 4f and the SiF 4 gas supply unit 4h, and the first supply flow rate is further provided. On the downstream side of the adjustment units 41a and 41c, three first distribution flow paths 401 are connected in common via the switching valves V1 and V3. Further, on the downstream side of the N 2 gas supply unit 4g and the O 2 gas supply unit 4i, respectively The first supply flow rate adjustment units 41b and 41d are provided, and further, three second distribution flow paths 402 are connected to each other via the on-off valves V2 and V4 on the downstream side of the first supply flow rate adjustment units 41b and 41d.

圖10所示之電漿處理裝置1b係混合從SiCl4 氣體供給部4f和SiF4 氣體供給部4h被供給之2種類氣體之後,在第1分配流路401被分流之點,和從N2 氣體供給部4g和O2 氣體供給部4i中之任一方被供給之氣體,在第2分配流路402被分流之點,與已經敘述之第1實施形態有關之電漿處理裝置1不同。藉由從N2 氣體供給部4g和O2 氣體供給部4i中之任一方,切換供給N2 氣體和O2 氣體,可以切換形成SiN膜或SiO2 膜。   另外,即使針對電漿處理裝置1b之具體裝置構成,因亦與使用圖3、4說明的電漿處理裝置1之情形相同,故省略再次說明。The plasma processing apparatus 1b shown in FIG. 10 mixes the two types of gas supplied from the SiCl 4 gas supply unit 4f and the SiF 4 gas supply unit 4h, and is branched at the first distribution flow path 401, and from N 2 . The gas supplied to one of the gas supply unit 4g and the O 2 gas supply unit 4i is different from the plasma processing apparatus 1 according to the first embodiment described above in that the second distribution flow path 402 is branched. By supplying N 2 gas and O 2 gas from either one of the N 2 gas supply unit 4g and the O 2 gas supply unit 4i, the SiN film or the SiO 2 film can be switched. In addition, the specific device configuration of the plasma processing apparatus 1b is the same as that of the plasma processing apparatus 1 described with reference to Figs. 3 and 4, and therefore will not be described again.

圖11表示從設置有SiCl4 氣體供給部4f或SiF4 氣體供給部4h、N2 氣體供給部4g之氣體箱,至氣體噴淋頭部30a、30b、30e之路徑內之各位置的壓力。   圖11中之四角之描繪係表示不設置第2分配流路402,而在第1分配流量調節部421a~423a之上游側,設置SiCl4 氣體供給部4f、SiCl4 氣體供給部4h、N2 氣體供給部4g,混合被流量調節成例如150sccm之SiF4 氣體,被流量調節成150sccm之SiF4 氣體和被流量調節成4000sccm之N2 氣體,經由第1分配流路401而供給至氣體噴淋頭部30a、30b、30e之情況下之各位置的壓力。Fig. 11 shows the pressure at each position in the path from the gas tank provided with the SiCl 4 gas supply unit 4f, the SiF 4 gas supply unit 4h, and the N 2 gas supply unit 4g to the gas shower heads 30a, 30b, and 30e. In the drawing of the four corners in Fig. 11, the second distribution flow path 402 is not provided, and the SiCl 4 gas supply unit 4f and the SiCl 4 gas supply unit 4h and N 2 are provided on the upstream side of the first distribution flow rate adjustment units 421a to 423a. The gas supply unit 4g mixes the SiF 4 gas whose flow rate is adjusted to, for example, 150 sccm, the SiF 4 gas whose flow rate is adjusted to 150 sccm, and the N 2 gas whose flow rate is adjusted to 4000 sccm, and supplies it to the gas spray through the first distribution flow path 401. The pressure at each position in the case of the heads 30a, 30b, 30e.

在事先混合SiCl4 氣體和SiF4 氣體和N2 氣體之情況下,MFC亦即第1分配流量調節部421a~423a之上游側之路徑內之全壓升高至33kPa(250torr)左右。當藉由圖12所示之SiCl4 (沸點57.6℃)之蒸氣壓曲線時,該壓力為高於25℃之溫度下的蒸氣壓。因此,當不加熱SiCl4 氣體和SiF4 氣體和N2 氣體之混合氣體(成膜氣體)流動之第1分配流量調節部421a~423a之上流側的配管時,有SiCl4 凝縮之虞。When the SiCl 4 gas, the SiF 4 gas, and the N 2 gas are mixed in advance, the total pressure in the path of the MFC, that is, the upstream side of the first distribution flow rate adjusting portions 421a to 423a is raised to about 33 kPa (250 torr). When the vapor pressure curve of SiCl 4 (boiling point 57.6 ° C) shown in Fig. 12 is used, the pressure is a vapor pressure at a temperature higher than 25 °C. Therefore, when the piping on the upstream side of the first distribution flow rate adjusting portions 421a to 423a through which the mixed gas (film forming gas) of the SiCl 4 gas and the SiF 4 gas and the N 2 gas flows is not heated, the SiCl 4 is condensed.

再者,第1分配流量調節部421a~423a因傳導度變小,在第1分配流量調節部421a~423a之上游,混合氣體之壓力升高,故也有難以正確地供給蒸氣壓低之SiCl4 氣體之問題。In addition, since the first distribution flow rate adjustment units 421a to 423a have a small conductivity, the pressure of the mixed gas rises upstream of the first distribution flow rate adjustment units 421a to 423a, so that it is difficult to accurately supply the SiCl 4 gas having a low vapor pressure. The problem.

於是,如圖10所示般,藉由分離從SiCl4 氣體供給部4f和SiF4 氣體供給部4h被供給之SiCl4 氣體和SiF4 氣體用之第1分配流路401、從N2 氣體供給部4g被供給之N2 氣體供給用之第2分配流路402,如圖11中菱形描繪所示般,可以使第1分配流量調節部421a~423a之上游側之路徑內之全壓降低,抑制蒸氣壓低的SiCl4 氣體之凝縮,同時正確地供給SiCl4 氣體。   再者,即使在切換成從N2 氣體供給部4g供給N2 氣體,從O2 氣體供給部4i供給O2 氣體,使用SiCl4 氣體和SiF4 氣體和O2 氣體之混合氣體(成膜氣體)而進行成膜之情況下,亦能取得同樣的作用效果。Then, as shown in FIG. 10, the first distribution flow path 401 for the SiCl 4 gas and the SiF 4 gas supplied from the SiCl 4 gas supply unit 4f and the SiF 4 gas supply unit 4h is separated and supplied from the N 2 gas. In the second distribution flow path 402 for supplying the N 2 gas to be supplied, the total pressure in the path on the upstream side of the first distribution flow rate adjustment units 421a to 423a can be lowered as shown by a diamond in FIG. inhibition of SiCl 4 vapor pressure of the condensable gas, SiCl 4 gas is simultaneously supplied correctly. Moreover, even in the switched 4g supplied from N 2 gas N 2 gas supplying unit, from the O 2 gas supply portion 4i O 2 gas, using a mixed gas of SiCl 4 gas and SiF 4 gas and O 2 gases (film forming gas In the case of film formation, the same effects can be obtained.

並且,在從SiCl4 氣體供給部4f或SiF4 氣體供給部4h單獨地供給SiCl4 氣體或SiF4 氣體之情況下,構成各個氣體的物質凝縮,或是難以正確地供給之問題的情況下,即使分離SiCl4 氣體或SiF4 氣體用之第1分配流路401,和N2 氣體或O2 氣體供給用之第2分配流路402亦可。依此,可以抑制各物質之凝縮,再者,可以正確地供給SiCl4 氣體或SiF4 氣體。In the case where SiCl 4 gas or SiF 4 gas is separately supplied from the SiCl 4 gas supply unit 4f or the SiF 4 gas supply unit 4h, when the substances constituting the respective gases are condensed or the problem of difficulty in supplying them is difficult, It is also possible to separate the first distribution flow path 401 for the SiCl 4 gas or the SiF 4 gas, and the second distribution flow path 402 for supplying the N 2 gas or the O 2 gas. According to this, it is possible to suppress the condensation of each substance, and further, it is possible to supply the SiCl 4 gas or the SiF 4 gas correctly.

在上述說明之例中,表示使用SiCl4 氣體及SiF4 氣體之例,作為第1處理氣體原料之例。在此,於利用第1處理氣體原料作為Si之原料之情況,就以能夠採用之氣體種而言,除了已經敘述之SiCl4 、SiF4 之外,亦可以組合使用從SiBr4 、SiF2 Cl2 、SiH4 之氣體種群中選擇出之任一氣體種或2個以上之氣體種。   並且,在上述之例中,表示使用N2 氣體和O2 氣體之例,作為第2處理氣體原料之例。在此,在利用第2處理氣體原料作為氧化氣體、氮化氣體、稀釋氣體、清淨氣體之情況下,作為能夠採用之氣體種,亦可以組合使用從O2 、N2 、N2 O、Ar、He、NF3 之氣體種群中所選擇出之任一氣體種,或2個以上之氣體種。In the example described above, an example in which SiCl 4 gas and SiF 4 gas are used is exemplified as the first processing gas raw material. Here, in the case where the first process gas raw material is used as the raw material of Si, it is also possible to use a combination of SiBr 4 and SiF 2 Cl in addition to the already described SiCl 4 and SiF 4 . 2. Any gas species or more than two gas species selected from the gas population of SiH 4 . Further, in the above examples, an example in which N 2 gas and O 2 gas are used is shown as an example of the second processing gas raw material. Here, when the second processing gas raw material is used as the oxidizing gas, the nitriding gas, the diluent gas, or the clean gas, the gas species that can be used may be used in combination from O 2 , N 2 , N 2 O, and Ar. Any gas species selected from the gas population of He, NF 3 , or more than two gas species.

如上述說明般之電漿處理裝置1b般,藉由較氣體噴淋頭部30a、30b、30e更上游側的必要性,在分離SiCl4 氣體供給部4f和SiF4 氣體供給部4h(第1處理氣體原料供給部)、N2 氣體供給部4g或O2 氣體供給部4i(第2處理氣體原料供給部)之情況下,不需要在圓周方向分割外周側之氣體噴淋頭部30e。   但是,從膜厚之調整等之觀點來看,需要在被處理基板G之角部和邊部等周方向分割的每區域,即使變更成膜氣體之供給流量或第1、第2處理氣體原料之流量比之情況下,即使使用在圓周方向被分割之周邊氣體噴淋頭部30c、30d而進行成膜氣體之供給當然亦可。In the same manner as the plasma processing apparatus 1b described above, the SiCl 4 gas supply unit 4f and the SiF 4 gas supply unit 4h are separated by the necessity of being upstream of the gas shower heads 30a, 30b, and 30e (1st) In the case of the processing gas raw material supply unit), the N 2 gas supply unit 4g or the O 2 gas supply unit 4i (the second processing gas raw material supply unit), it is not necessary to divide the outer peripheral side of the gas shower head 30e in the circumferential direction. However, from the viewpoint of the adjustment of the film thickness and the like, it is necessary to change the supply flow rate of the film forming gas or the first and second process gas materials in each of the regions divided in the circumferential direction such as the corner portion and the side portion of the substrate G to be processed. In the case of the flow ratio, the supply of the film forming gas may be performed by using the peripheral gas shower heads 30c and 30d divided in the circumferential direction.

以上,在與使用圖3、4、7、8說明的實施形態有關之電漿處理裝置1、1a、1b中,表示藉由使用高頻天線5之感應電場之形成,使被供給至處理空間100之處理氣體予以電漿化的例。但是,使處理氣體予以電漿化之方法並不限定於感應耦合方式。   例如,即使在圖3所示之電漿處理裝置1中,以在各氣體噴淋頭部30a~30d連接第1高頻電源512,取代高頻天線5之配置,構成載置台13和金屬窗3(氣體噴淋頭部30a~30d)產生的平行平板型電漿產生部,藉由電容耦合使處理氣體予以電漿化亦可。As described above, the plasma processing apparatuses 1, 1a, and 1b according to the embodiment described with reference to Figs. 3, 4, 7, and 8 show that the induced electric field by using the high-frequency antenna 5 is supplied to the processing space. An example of plasma treatment of 100 treatment gases. However, the method of plasmaizing the processing gas is not limited to the inductive coupling method. For example, in the plasma processing apparatus 1 shown in FIG. 3, the first high-frequency power source 512 is connected to each of the gas shower heads 30a to 30d, and the mounting table 13 and the metal window are formed instead of the arrangement of the high-frequency antenna 5. The parallel plate type plasma generating portion generated by the 3 (gas shower heads 30a to 30d) may be plasma-coupled by the capacitive coupling.

再者,即使為使用高頻天線5之感應耦合電漿之情況下,氣體噴淋頭部30a~30d、30e藉由金屬製之部分窗30構成係並非必須要件,即使為由例如石英等之介電質所構成之介電質窗亦可。Further, even in the case of using the inductively coupled plasma of the high-frequency antenna 5, the gas shower heads 30a to 30d, 30e are not necessarily required by the partial window 30 made of metal, even if it is made of, for example, quartz. A dielectric window composed of a dielectric material may also be used.

而且,對於被處理基板G之處理,並不限定於上述蝕刻處理或成膜處理,亦可以使用於形成薄膜電晶體之時的金屬膜、ITO膜、氧化膜等之其他成膜處理或蝕刻該些膜之其他蝕刻處理、光阻膜之灰化處理等之各種電漿處理。Further, the treatment of the substrate G to be processed is not limited to the above-described etching treatment or film formation treatment, and may be used for other film formation treatment or etching of a metal film, an ITO film, an oxide film, or the like at the time of forming a thin film transistor. Various plasma treatments such as other etching treatment of the film and ashing treatment of the photoresist film.

並且,電漿處理裝置1、1a、1b並不限定於FPD用之基板G,亦可以使用於對於太陽電池面板用之基板G之上述各種電漿處理。Further, the plasma processing apparatuses 1, 1a, and 1b are not limited to the substrate G for FPD, and may be used for the above-described various plasma treatments for the substrate G for solar cell panels.

即使分配供給矩形狀之金屬窗3具有短邊和長邊之時,將周邊氣體噴淋頭部30c分成長邊側之周邊噴淋頭部和短邊側之周邊氣體噴淋頭部,而分別使用不同的第1分配流量調節部、第2分配流量調節部而個別被流量調節的氣體亦可。Even when the metal window 3 to which the rectangular shape is distributed has the short side and the long side, the peripheral gas shower head 30c is divided into the peripheral side of the growing side and the peripheral side of the short side of the gas shower head, respectively It is also possible to use a different first distribution flow rate adjustment unit and a second distribution flow rate adjustment unit to individually adjust the flow rate of the gas.

雖然使用MFC作為第1分配流量調節部421a~424a、第2分配流量調節部421b~424b,但是即使取代此,使用因應特定壓力比分配被供給的氣體的壓力式分流量控制器及因應特定流量比而予以分配的流量控制器亦可。Although the MFC is used as the first distribution flow rate adjustment units 421a to 424a and the second distribution flow rate adjustment units 421b to 424b, a pressure type flow rate controller that distributes the supplied gas in response to a specific pressure ratio and a specific flow rate are used instead. It is also possible to assign a flow controller.

G‧‧‧被處理基板G‧‧‧Processed substrate

30a、30b、30e‧‧‧氣體噴淋頭部30a, 30b, 30e‧‧‧ gas shower head

30c、30d‧‧‧周邊氣體噴淋頭部(氣體噴淋頭部)30c, 30d‧‧‧ surrounding gas shower head (gas shower head)

4a‧‧‧CF4氣體供給部4a‧‧‧CF 4 gas supply department

4b‧‧‧O2氣體供給部4b‧‧O 2 gas supply department

4c‧‧‧Cl2氣體供給部4c‧‧‧Cl 2 gas supply department

4d‧‧‧N2氣體供給部4d‧‧‧N 2 gas supply department

4e‧‧‧含鹵添加氣體供給部4e‧‧‧halogen-added gas supply unit

4f‧‧‧SiCl4氣體供給部4f‧‧‧SiCl 4 gas supply department

4g‧‧‧N2氣體供給部4g‧‧‧N 2 gas supply department

4h‧‧‧SiF4氣體供給部4h‧‧‧SiF 4 gas supply department

4i‧‧‧O2氣體供給部4i‧‧O 2 gas supply department

401‧‧‧第1分配流路401‧‧‧1st distribution flow path

402‧‧‧第2分配流路402‧‧‧2nd distribution flow path

41a‧‧‧第1供電流量調節部41a‧‧‧1st power supply flow adjustment unit

41b‧‧‧第2供電流量調節部41b‧‧‧2nd power supply flow adjustment unit

421a~424a‧‧‧第1分配流量調節部421a~424a‧‧‧1st distribution flow adjustment unit

421b~424b‧‧‧第2分配流量調節部421b~424b‧‧‧2nd distribution flow adjustment unit

43a~43d‧‧‧氣體供給管43a~43d‧‧‧ gas supply pipe

5‧‧‧高頻天線5‧‧‧High frequency antenna

6‧‧‧控制部6‧‧‧Control Department

圖1為在與實施形態有關之電漿處理裝置被處理之被處理基板之第1說明圖。   圖2為在電漿處理裝置被處理之被處理基板之第2說明圖。   圖3為電漿處理裝置之縱剖側視圖。   圖4為被設置在上述電漿處理裝置之金屬窗之俯視圖。   圖5為朝構成上述金屬窗之各氣體噴淋頭部供給蝕刻氣體之供給系統圖。   圖6為與在電漿處理裝置被處理之其他被處理基板有關之第1說明圖。   圖7為與上述其他被處理基板有關之第2說明圖。   圖8為在與第2實施形態有關之電漿處理裝置被處理之被處理基板之說明圖。   圖9為對與第2實施形態有關之電漿處理裝置供給處理氣體的供給系統圖。   圖10為對與第3實施形態有關之電漿處理裝置供給處理氣體的供給系統圖。   圖11為表示在處理氣體之供給流路內之各位置之壓力的說明圖。   圖12為SiCl4 氣體之溫度-蒸氣壓特性圖。Fig. 1 is a first explanatory view of a substrate to be processed which is processed by a plasma processing apparatus according to an embodiment. Fig. 2 is a second explanatory view of a substrate to be processed which is processed in a plasma processing apparatus. Figure 3 is a longitudinal sectional side view of the plasma processing apparatus. Fig. 4 is a plan view of a metal window provided in the above plasma processing apparatus. Fig. 5 is a view showing a supply system for supplying an etching gas to each of the gas shower heads constituting the metal window. Fig. 6 is a first explanatory diagram relating to another substrate to be processed which is processed by the plasma processing apparatus. Fig. 7 is a second explanatory view showing the other substrates to be processed. Fig. 8 is an explanatory view of a substrate to be processed which is processed in the plasma processing apparatus according to the second embodiment. Fig. 9 is a view showing a supply system for supplying a processing gas to the plasma processing apparatus according to the second embodiment. Fig. 10 is a view showing a supply system for supplying a processing gas to the plasma processing apparatus according to the third embodiment. Fig. 11 is an explanatory view showing pressure at each position in the supply flow path of the processing gas. Fig. 12 is a graph showing the temperature-vapor pressure characteristics of SiCl 4 gas.

Claims (11)

一種電漿處理裝置,其係對被真空排氣之處理空間内之被處理基板,實施藉由被電漿化之處理氣體進行的電漿處理,該電漿處理裝置之特徵在於具備:   處理容器,其係具備載置上述被處理基板之載置台,構成實施上述電漿處理之處理空間;   複數氣體噴淋頭部,其係分別被設置在構成上述處理空間之天頂面,且將上述天頂面從中央部側朝向周邊部側在徑向予以分割而構成的複數區域,形成有對上述處理空間供給處理氣體之氣體吐出孔;   電漿產生部,其係用以將從上述複數噴淋頭部被供給至處理空間之處理氣體予以電漿化;   用以供給上述處理氣體所含之第1處理氣體原料的第1處理氣體原料供給部,及用以供給第2處理氣體原料之第2處理氣體原料供給部;   第1供給流量調節部,其係用以進行從上述第1處理氣體原料供給部被供給至上述處理空間之第1處理氣體原料之流量調節;及   複數第1分配流量調節部,其係分別被設置在用以將在上述第1供給流量調節部被流量調節之第1處理氣體原料,分配供給至上述複數氣體噴淋頭部之複數第1分配流路,用以進行被供給至各氣體噴淋頭部之第1原料氣體之流量調節;   第2供給流量調節部,其係用以進行從上述第2處理氣體原料供給部被供給至上述處理空間之第2處理氣體原料之流量調節;及   複數第2分配流量調節部,其係分別被設置在用以將在上述第2供給流量調節部被流量調節之第2處理氣體原料,分配供給至上述複數氣體噴淋頭部之複數第2分配流路,用以進行被供給至各氣體噴淋頭部之第2原料氣體之流量調節。A plasma processing apparatus for performing plasma treatment by a plasma-treated processing gas on a substrate to be processed in a vacuum evacuated processing space, the plasma processing apparatus comprising: a processing container And comprising: a mounting table on which the substrate to be processed is placed, and a processing space for performing the plasma processing; and a plurality of gas shower heads respectively provided on a zenith surface constituting the processing space, and the zenith surface A plurality of regions formed by dividing the radial direction from the central portion side toward the peripheral portion side are formed with a gas discharge hole for supplying a processing gas to the processing space, and a plasma generating portion for discharging the head from the plurality of the plurality of shower heads The processing gas supplied to the processing space is plasma-formed; the first processing gas raw material supply unit for supplying the first processing gas raw material contained in the processing gas; and the second processing gas for supplying the second processing gas raw material a raw material supply unit; the first supply flow rate adjustment unit configured to be supplied from the first process gas raw material supply unit to the upper portion a flow rate adjustment of the first process gas raw material in the processing space; and a plurality of first distribution flow rate adjusting units respectively provided in the first process gas raw material for adjusting the flow rate of the first supply flow rate adjusting unit a plurality of first distribution channels to the plurality of gas shower heads for regulating the flow rate of the first material gas supplied to each of the gas shower heads; and a second supply flow rate adjusting unit for performing the slave The second processing gas raw material supply unit is configured to adjust the flow rate of the second processing gas raw material supplied to the processing space; and the plurality of second distributed flow rate adjusting units are provided in the second supply flow rate adjusting unit The flow rate-regulated second process gas raw material is distributed to the plurality of second distribution flow paths of the plurality of gas shower heads to adjust the flow rate of the second material gas supplied to each of the gas shower heads. 如請求項1所載之電漿處理裝置,其中   在徑向分割上述天頂面而構成的上述複數區域中,在周邊部側之環狀區域,在圓周方向分割該環狀之區域而構成的複數區域,設置形成有對上述處理空間供給處理氣體之氣體吐出孔之氣體噴淋頭部亦即複數周邊氣體噴淋頭部,   從設置有上述第1分配流量調節部之第1分配流路,及設置有第2分配流量調節部之第2分配流路,也對上述各周邊氣體噴淋頭部,分配供給第1處理氣體原料、第2處理氣體原料。The plasma processing apparatus according to claim 1, wherein in the plurality of regions formed by dividing the zenith surface in the radial direction, the annular region on the peripheral portion side is divided into a plurality of annular regions in the circumferential direction. a first peripheral flow head that is provided with a gas discharge head that supplies a gas discharge hole for the processing space to the processing space, and a first distribution flow path from which the first distribution flow rate adjustment unit is provided, and The second distribution flow path of the second distribution flow rate adjustment unit is provided, and the first process gas material and the second process gas material are distributed and supplied to each of the peripheral gas shower heads. 如請求項2所載之電漿處理裝置,其中   上述天頂面之平面形狀為矩形狀,在上述周邊氣體噴淋頭部,設置包含上述矩形狀之角部的周邊氣體噴淋頭部,和被夾在相鄰之上述角部之間,包含上述矩形狀之邊部的周邊氣體噴淋頭部,   上述角部之周邊氣體噴淋頭部,從共同的第1、第2分配流路分配供給上述第1、第2處理氣體原料,上述邊部之周邊氣體噴淋頭部從與上述角部之周邊噴淋頭部不同之共同的第1、第2分配流路分配供給上述第1、第2處理氣體原料。The plasma processing apparatus according to claim 2, wherein the planar shape of the zenith surface is rectangular, and a peripheral gas shower head including the rectangular corner portion is provided in the peripheral gas shower head, and a peripheral gas shower head including the rectangular side portion between the adjacent corner portions, and the peripheral gas shower head of the corner portion is distributed and supplied from the common first and second distribution channels In the first and second processing gas raw materials, the peripheral gas shower heads of the side portions are distributed and supplied to the first and second distribution channels different from the shower heads around the corner portions. 2 process gas raw materials. 如請求項2或3所載之電漿處理裝置,其中   用以進行上述處理空間內之真空排氣的排氣口,被設置在設置有上述周邊氣體噴淋頭部之環狀區域之下方位置,或較該下方位置更外方側之位置。The plasma processing apparatus of claim 2 or 3, wherein the exhaust port for performing vacuum evacuation in the processing space is disposed below the annular region provided with the peripheral gas shower head , or a position on the outer side of the lower position. 如請求項1至3中之任一項所載之電漿處理裝置,其中   上述第2分配流路分別在上述第1分配流量調節部之下游側之第1分配流路合流。The plasma processing apparatus according to any one of claims 1 to 3, wherein the second distribution flow path merges with the first distribution flow path on the downstream side of the first distribution flow rate adjustment unit. 如請求項1至3中之任一項所載之電漿處理裝置,其中   上述電漿產生部被配置在上述氣體噴淋頭部之上方側,用以藉由感應耦合使上述處理氣體電漿化的電漿天線。   上述複數氣體噴淋頭部分別以由導電性之部分窗組成的金屬窗而構成,相鄰之氣體噴淋頭部彼此互相絕緣。The plasma processing apparatus according to any one of claims 1 to 3, wherein the plasma generating portion is disposed on an upper side of the gas shower head for plasma-treating the processing gas by inductive coupling. Plasma antenna. The plurality of gas shower heads are each formed of a metal window composed of a conductive partial window, and the adjacent gas shower heads are insulated from each other. 如請求項1至3中之任一項所載之電漿處理裝置,其中   上述處理氣體係用以蝕刻被形成在玻璃基板亦即被處理基板上之蝕刻對象膜的蝕刻氣體,   上述第2處理氣體原料為氧氣,   被設置在上述複數第1、第2分配流路之第1、第2分配流量調節部,以因應被圖案製作於上述蝕刻對象膜之上面側之光阻膜之端部的傾斜之大小不同的區域,使從對該些區域供給蝕刻氣體之位置的氣體噴淋頭部被供給的蝕刻氣體之氧濃度變化之方式,進行上述第1、第2處理氣體原料之流量設定。The plasma processing apparatus according to any one of claims 1 to 3, wherein the processing gas system is for etching an etching gas of an etching target film formed on a glass substrate, that is, a substrate to be processed, the second processing The gaseous material is oxygen, and is provided in the first and second distribution flow rate adjusting portions of the plurality of first and second distribution channels, and is patterned in the end portion of the photoresist film on the upper surface side of the etching target film. The flow rate of the first and second process gas raw materials is set such that the oxygen concentration of the etching gas supplied from the gas shower head at the position where the etching gas is supplied to the regions is changed in a region having a different inclination. 如請求項7所載之電漿處理裝置,其中   上述蝕刻對象膜為含矽膜,   上述第1處理氣體原料為四氟碳氣體或三氟氮氣體之至少一方,   被設置在上述複數第1、第2分配流路之第1、第2分配流量調節部,以比起對被圖案製作於上述蝕刻對象膜之上面側的光阻膜之端部之傾斜大的區域供給蝕刻氣體之位置的氣體噴淋頭部,從對上述光阻膜之端部之傾斜小的區域供給蝕刻氣體之位置的氣體噴淋頭部被供給之蝕刻氣體之氧濃度較高之方式,分別進行上述第1、第2處理氣體原料之流量設定。The plasma processing apparatus according to claim 7, wherein the etching target film is a ruthenium containing film, and the first processing gas raw material is at least one of a tetrafluorocarbon gas or a trifluoro nitrogen gas, and is provided in the plural first The first and second distribution flow rate adjustment units of the second distribution flow path supply the gas at the position of the etching gas in a region larger than the inclination of the end portion of the photoresist film patterned on the upper surface side of the etching target film. In the shower head, the first and the first are performed so that the oxygen concentration of the etching gas supplied from the gas shower head where the etching gas is supplied to the region where the inclination of the end portion of the photoresist film is small is high. 2 The flow rate setting of the process gas raw material. 如請求項7所載之電漿處理裝置,其中   上述蝕刻對象膜係多晶矽膜或鉬膜,   上述第1處理氣體原料係從四氟化碳氣體、六氟化硫、三氟化氮或氯氣選擇至少一個的氣體,   被設置在上述複數第1、第2分配流路之第1、第2分配流量調節部,以比起對被圖案製作於上述蝕刻對象膜之上面側的光阻膜之端部之傾斜小的區域供給蝕刻氣體之位置的氣體噴淋頭部,從對上述光阻膜之端部之傾斜大的區域供給蝕刻氣體之位置的氣體噴淋頭部被供給之蝕刻氣體之氧濃度較高之方式,分別進行上述第1、第2處理氣體原料之流量設定。The plasma processing apparatus according to claim 7, wherein the etching target film is a polycrystalline germanium film or a molybdenum film, and the first processing gas raw material is selected from a carbon tetrafluoride gas, sulfur hexafluoride, nitrogen trifluoride or chlorine gas. At least one of the gas is provided in the first and second distribution flow rate adjusting portions of the plurality of first and second distribution channels, and is opposite to the end of the photoresist film patterned on the upper surface side of the etching target film. a gas shower head at a position where an etching gas is supplied in a region where the inclination is small, and an oxygen of an etching gas supplied from a gas shower head at a position where an etching gas is supplied to a region where the inclination of the end portion of the photoresist film is large The flow rate of the first and second process gas raw materials is set to be higher in a higher concentration. 如請求項1至3中之任一項所載之電漿處理裝置,其中   上述處理氣體係用以蝕刻被形成在玻璃基板亦即被處理基板上之鋁膜,及其上層側之二氧化矽膜之蝕刻氣體,   上述第1處理氣體原料為氯氣,上述第2處理氣體原料為氮氣及含鹵氣體,   被設置在上述複數第1、第2分配流路之第1、第2分配流量調節部,以比起位於上述天頂面之周邊部側之氣體噴淋頭部,從位於中央部側之氣體噴淋頭部被供給之蝕刻氣體中對氯氣的氮氣及含鹵氣體之分配比較小之方式,分別進行上述第1、第2處理氣體原料之流量設定。The plasma processing apparatus according to any one of claims 1 to 3, wherein the processing gas system is for etching an aluminum film formed on a glass substrate, that is, a substrate to be processed, and an upper layer of cerium oxide The etching gas for the film, the first processing gas raw material is chlorine gas, and the second processing gas raw material is nitrogen gas and halogen-containing gas, and is provided in the first and second distribution flow rate adjusting units of the plurality of first and second distribution channels The distribution of the nitrogen gas and the halogen-containing gas of the chlorine gas in the etching gas supplied from the gas shower head located on the central portion side is smaller than that of the gas shower head located on the peripheral side of the zenith surface. The flow rate of the first and second processing gas raw materials is set separately. 如請求項1至3中之任一項所載之電漿處理裝置,其中   上述處理氣體係用以形成被形成在玻璃基板亦即被處理基板上之含矽膜的成膜氣體,   上述第1處理氣體原料為四氟化矽氣體或四氯化矽氣體之至少一方,上述第2處理氣體原料為氮氣或氧氣,   上述第2分配流路分別在上述第1分配流量調節部之下游側之第1分配流路合流,   上述第1分配流量調節部及第1分配流量調節部,以供給從該第1分配流量調節部至第1分配流量調節部之流路內之壓力,被維持在低於在室溫下之上述第1處理氣體原料之蒸氣壓之壓力的流量的第1處理氣體原料之方式,進行流量設定。The plasma processing apparatus according to any one of claims 1 to 3, wherein the processing gas system is used to form a film-forming gas containing a ruthenium film formed on a glass substrate, that is, a substrate to be processed, the first The processing gas raw material is at least one of a hafnium tetrafluoride gas or a hafnium tetrachloride gas, the second processing gas raw material is nitrogen gas or oxygen gas, and the second distribution flow path is respectively on a downstream side of the first distribution flow rate adjusting unit. The first distribution flow rate adjustment unit and the first distribution flow rate adjustment unit maintain the pressure in the flow path from the first distribution flow rate adjustment unit to the first distribution flow rate adjustment unit at a lower level. The flow rate is set such that the flow rate of the vapor pressure of the first process gas raw material at the flow rate of the first process gas feedstock is at room temperature.
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