TWI462162B - Cleaning method of apparatus for depositing carbon containing film - Google Patents
Cleaning method of apparatus for depositing carbon containing film Download PDFInfo
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- TWI462162B TWI462162B TW097127211A TW97127211A TWI462162B TW I462162 B TWI462162 B TW I462162B TW 097127211 A TW097127211 A TW 097127211A TW 97127211 A TW97127211 A TW 97127211A TW I462162 B TWI462162 B TW I462162B
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- 238000004140 cleaning Methods 0.000 title claims description 88
- 238000000034 method Methods 0.000 title claims description 57
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims description 46
- 229910052799 carbon Inorganic materials 0.000 title claims description 46
- 238000000151 deposition Methods 0.000 title claims description 35
- 239000007789 gas Substances 0.000 claims description 101
- 239000006227 byproduct Substances 0.000 claims description 16
- 238000005108 dry cleaning Methods 0.000 claims description 14
- 229910052739 hydrogen Inorganic materials 0.000 claims description 14
- 229910052736 halogen Inorganic materials 0.000 claims description 12
- 150000002367 halogens Chemical class 0.000 claims description 12
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 11
- 239000001257 hydrogen Substances 0.000 claims description 11
- 229910052760 oxygen Inorganic materials 0.000 claims description 11
- 150000001721 carbon Chemical class 0.000 claims description 5
- 230000032683 aging Effects 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 claims description 3
- 235000012431 wafers Nutrition 0.000 description 21
- 230000008021 deposition Effects 0.000 description 15
- 239000004065 semiconductor Substances 0.000 description 12
- 239000007787 solid Substances 0.000 description 5
- 238000011065 in-situ storage Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 239000007795 chemical reaction product Substances 0.000 description 3
- 238000005530 etching Methods 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 230000003213 activating effect Effects 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 238000000231 atomic layer deposition Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000005229 chemical vapour deposition Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000005137 deposition process Methods 0.000 description 2
- 238000011066 ex-situ storage Methods 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000004148 unit process Methods 0.000 description 2
- ITWBWJFEJCHKSN-UHFFFAOYSA-N 1,4,7-triazonane Chemical compound C1CNCCNCCN1 ITWBWJFEJCHKSN-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 1
- 229910052581 Si3N4 Inorganic materials 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- HYXIRBXTCCZCQG-UHFFFAOYSA-J [C+4].[F-].[F-].[F-].[F-] Chemical compound [C+4].[F-].[F-].[F-].[F-] HYXIRBXTCCZCQG-UHFFFAOYSA-J 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- GNPVGFCGXDBREM-UHFFFAOYSA-N germanium atom Chemical compound [Ge] GNPVGFCGXDBREM-UHFFFAOYSA-N 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000005468 ion implantation Methods 0.000 description 1
- 239000004973 liquid crystal related substance Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000004767 nitrides Chemical class 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000000206 photolithography Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 238000005389 semiconductor device fabrication Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- LIVNPJMFVYWSIS-UHFFFAOYSA-N silicon monoxide Chemical compound [Si-]#[O+] LIVNPJMFVYWSIS-UHFFFAOYSA-N 0.000 description 1
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 description 1
- 229910052814 silicon oxide Inorganic materials 0.000 description 1
- 238000004544 sputter deposition Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- TXEYQDLBPFQVAA-UHFFFAOYSA-N tetrafluoromethane Chemical compound FC(F)(F)F TXEYQDLBPFQVAA-UHFFFAOYSA-N 0.000 description 1
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Description
本發明是有關於一種製造半導體之裝置的清潔方法,且特別是有關於一種沈積含碳膜之裝置的反應器的乾式清潔方法。BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to a method of cleaning a device for fabricating a semiconductor, and more particularly to a method of dry cleaning of a reactor for depositing a device containing a carbon film.
通常,藉由使用多個單元製程來製造半導體元件,諸如離子植入製程(ion implantation process)、成膜製程(film formation process)、擴散製程(diffusion process)、微影製程(photolithography process)以及蝕刻製程(etching process)。在上述單元製程中,為了增加半導體元件製造的再現性及可靠性,改良成膜製程是必要的。Generally, semiconductor components are fabricated by using a plurality of unit processes, such as an ion implantation process, a film formation process, a diffusion process, a photolithography process, and etching. Etching process. In the above unit process, in order to increase the reproducibility and reliability of semiconductor device fabrication, it is necessary to improve the film formation process.
藉由使用以下方法將半導體元件的膜形成於晶圓上,諸如濺鍍、蒸發、化學氣相沈積(chemical vapor deposition,CVD)以及原子層沈積(atomic layer deposition,ALD)等。用以執行上述方法的膜沈積裝置通常包括反應器、供應各種氣體至反應器的氣體管線以及放置晶圓的晶圓塊(wafer block)。A film of a semiconductor element is formed on a wafer by using, for example, sputtering, evaporation, chemical vapor deposition (CVD), and atomic layer deposition (ALD). A film deposition apparatus for performing the above method generally includes a reactor, a gas line supplying various gases to the reactor, and a wafer block in which the wafer is placed.
然而,當藉由使用膜沈積裝置進行成膜製程時,在成膜製程期間産生的反應產物沈積於(附著於)半導體膜的表面及反應器的內壁上。用以進行半導體大規模生産(mass production)的膜沈積裝置處理大量晶圓。因此,當在反應産物附著至反應器的狀態下持續地進行半導體製程時,半導體製程中的膜特性將改變。其最具代表性的例子是膜電 阻或厚度的改變以及由於反應産物的脫落而最終産生的粒子。這些粒子在沈積製程中會導致缺陷並且附著於晶圓上,這將導致半導體元件產量的退化。However, when a film forming process is performed by using a film deposition apparatus, a reaction product generated during the film forming process is deposited (attached) to the surface of the semiconductor film and the inner wall of the reactor. A film deposition apparatus for performing semiconductor mass production processes a large number of wafers. Therefore, when the semiconductor process is continuously performed in a state where the reaction product adheres to the reactor, the film characteristics in the semiconductor process will change. Its most representative example is membrane electricity. The change in resistance or thickness and the resulting particles due to the shedding of the reaction product. These particles can cause defects and adhere to the wafer during the deposition process, which will result in degradation of the yield of the semiconductor device.
因此,在習知的半導體製造方法中,在膜發生變化之前,也就是在晶圓沈積製程進行預定時間後或者沈積預定數量的晶圓後停止膜沈積裝置,並且將反應器暴露於空氣,使得反應器和反應器的各元件彼此分開。在藉由使用揮發性材質(諸如酒精)清潔沈積於反應器以及各元件上的異物後,將分開的反應器重組。通常,這種清潔方法被稱為非原位(ex-situ)清潔。在非原位清潔方法中,當製造半導體時生產力顯著地降低,並且産生設備的改變點(change-point)。Therefore, in the conventional semiconductor manufacturing method, the film deposition device is stopped before the film is changed, that is, after the wafer deposition process is performed for a predetermined time or after depositing a predetermined number of wafers, and the reactor is exposed to the air, so that the reactor is exposed to the air. The reactor and the components of the reactor are separated from one another. After cleaning the foreign matter deposited on the reactor and the various components by using a volatile material such as alcohol, the separate reactors are recombined. Typically, this method of cleaning is referred to as ex-situ cleaning. In the ex-situ cleaning method, productivity is significantly reduced when manufacturing a semiconductor, and a change-point of the device is generated.
膜沈積裝置的另一種清潔方法是所謂原位(in-situ)清潔的乾式清潔方法,藉由此方法可在不停止膜沈積裝置運轉的情况下透過使用腐蝕性氣體來移除反應器內部的沈積産物。例如,將CF4 、C2 F6 、C3 F8 、C4 F8 、CHF3 、SF6 或NF3 等全氟化合物氣體(perfluorized compound gas)作爲清潔氣體注入到反應器內,以清潔沈積矽(Si)、氧化矽(SiOx )或氮化矽(SiNx )等膜之裝置,而移除上述膜。Another cleaning method of the film deposition apparatus is a so-called in-situ cleaning dry cleaning method by which the inside of the reactor can be removed by using a corrosive gas without stopping the operation of the film deposition apparatus. Deposition product. For example, a perfluorized compound gas such as CF 4 , C 2 F 6 , C 3 F 8 , C 4 F 8 , CHF 3 , SF 6 or NF 3 is injected into the reactor as a cleaning gas to clean , silicon oxide (SiO x) or silicon nitride (SiN x), etc. the film deposition apparatus silicon (Si), and said film is removed.
特別是,隨著半導體元件的積集度不斷上升,為了降低漏電流,已嘗試將碳加入膜內,例如沈積諸如SiOCH的低介電常數(low-k)膜。金屬氮化物膜(例如TaN)可包含10-20%的碳。因此,在沈積含碳爲5%或更多的膜之裝置中,當藉由使用習知的腐蝕氣體進行乾式清潔時,會産 生基於氟化碳(CF*)之白色粉末的副產物。因此,需要一種沈積含碳膜之裝置的改良乾式清潔方法。In particular, as the degree of integration of semiconductor elements continues to increase, in order to reduce leakage current, attempts have been made to add carbon into the film, for example, to deposit a low dielectric constant (low-k) film such as SiOCH. The metal nitride film (e.g., TaN) may comprise 10-20% carbon. Therefore, in a device for depositing a film containing 5% or more of carbon, when dry cleaning is performed by using a conventional etching gas, it is produced. A by-product of a white powder based on carbon fluoride (CF*). Therefore, there is a need for an improved dry cleaning method for depositing a carbon containing film.
本發明提供了一種沈積含碳膜之裝置的乾式清潔方法。The present invention provides a dry cleaning method for depositing a carbon-containing film.
根據本發明的一方面,提供了一種沈積含碳膜之裝置的乾式清潔方法,此方法包括清潔此裝置的反應器的內部,其中清潔此裝置的反應器的內部包括供應清潔氣體至反應器,清潔氣體包括藉由使用遠程電漿産生器激活之鹵素,並同時供應未激活之碳移除氣體至反應器。According to an aspect of the present invention, there is provided a dry cleaning method for depositing a carbonaceous film-containing apparatus, the method comprising cleaning an interior of a reactor of the apparatus, wherein cleaning the interior of the reactor of the apparatus comprises supplying a cleaning gas to the reactor, The cleaning gas includes a halogen activated by using a remote plasma generator and simultaneously supplies an unactivated carbon removal gas to the reactor.
在本發明中,清潔氣體可以是從由NF3 、C2 F6 、CF4 、CHF3 、F2 及其組合所組成的群組中選擇的一種氣體。碳移除氣體可以是包括氧(O)或氫(H)的氣體。碳移除氣體可以是從由O2 、N2 O、O3 、NH3 、H2 及其組合所組成的群組中選擇的一種氣體。In the present invention, the cleaning gas may be a gas selected from the group consisting of NF 3 , C 2 F 6 , CF 4 , CHF 3 , F 2 , and combinations thereof. The carbon removal gas may be a gas including oxygen (O) or hydrogen (H). The carbon removal gas may be a gas selected from the group consisting of O 2 , N 2 O, O 3 , NH 3 , H 2 , and combinations thereof.
在供應清潔氣體及碳移除氣體之前,此方法更包括進行O2 處理,以預先移除存在於反應器內部之副産物表面上的碳。在清潔反應器的內部之後,此方法更包括藉由使用含氫氣體處理沈積含碳膜之裝置,以移除清潔氣體的殘留。在此情况下,含氫氣體可以是從由H2 、NH3 、SiH4 、H2 O及其組合所組成的群組中選擇的一種氣體。Prior to supplying the cleaning gas and the carbon removal gas, the method further includes an O 2 treatment to pre-removal of carbon present on the surface of the by-products present inside the reactor. After cleaning the interior of the reactor, the method further includes removing the residue of the cleaning gas by treating the carbon-containing film with a hydrogen-containing gas. In this case, the hydrogen-containing gas may be a gas selected from the group consisting of H 2 , NH 3 , SiH 4 , H 2 O, and combinations thereof.
在清潔反應器的內部之後,此方法更包括藉由使用含碳膜來陳化反應器的內部。After cleaning the interior of the reactor, the method further includes aging the interior of the reactor by using a carbonaceous film.
現在將參照附圖更全面地描述本發明,本發明的範例性實施例顯示於附圖中。然而,本發明可具體化爲不同形式,並不應解釋爲侷限於本案所闡述的實施例。更確切地,提供這些實施例是爲了使本發明透徹且完整,並向本領域熟知此項技藝者全面地傳達本發明的概念。The invention will now be described more fully hereinafter with reference to the appended claims, However, the present invention may be embodied in different forms and should not be construed as being limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete.
首先,根據本發明的清潔方法可用於清潔圖1所示的膜沈積裝置。First, the cleaning method according to the present invention can be used to clean the film deposition apparatus shown in Fig. 1.
圖1的膜沈積裝置1包括具有內部空間的反應器10、安裝在反應器10的內部空間內可升降且放置晶圓W的晶圓塊12、噴射氣體的噴頭11,噴頭11使得膜形成於放置在晶圓塊12上之晶圓W上。The film deposition apparatus 1 of FIG. 1 includes a reactor 10 having an internal space, a wafer block 12 mounted in the internal space of the reactor 10 for lifting and placing the wafer W, and a shower head 11 for injecting gas, and the shower head 11 allows the film to be formed on the film Placed on the wafer W on the wafer block 12.
裝置1用以在半導體晶圓W(例如,矽晶圓或液晶顯示器(LCD)玻璃基板)上沈積含碳膜。裝置1更包括氣體供應裝置20,其可經由氣體管線供應某一製程的源氣體及惰性氣體到反應器10。在根據本發明的清潔方法中,清潔氣體包括鹵素,並且藉由使用遠程電漿産生器22激活清潔氣體並其供應至反應器10。The device 1 is for depositing a carbon-containing film on a semiconductor wafer W, such as a germanium wafer or a liquid crystal display (LCD) glass substrate. The apparatus 1 further includes a gas supply unit 20 that supplies a source gas of a certain process and an inert gas to the reactor 10 via a gas line. In the cleaning method according to the present invention, the cleaning gas includes halogen, and the cleaning gas is activated and supplied to the reactor 10 by using the remote plasma generator 22.
包括鹵素的清潔氣體可以是從由NF3 、C2 F6 、CF4 、CHF3 、F2 及其組合所組成的群組中選擇的一種清潔氣體。碳移除氣體可以是包括氧或氫的氣體。例如,碳移除氣體可以是從由O2 、N2 O、O3 、NH3 、H2 及其組合所組成的群組中選擇的一種氣體。The cleaning gas including halogen may be a cleaning gas selected from the group consisting of NF 3 , C 2 F 6 , CF 4 , CHF 3 , F 2 , and combinations thereof. The carbon removal gas may be a gas including oxygen or hydrogen. For example, the carbon removal gas may be a gas selected from the group consisting of O 2 , N 2 O, O 3 , NH 3 , H 2 , and combinations thereof.
接下來,將描述根據本發明實施例的圖1的裝置1之反應器10的清潔方法。Next, a cleaning method of the reactor 10 of the apparatus 1 of Fig. 1 according to an embodiment of the present invention will be described.
圖2是根據本發明第一實施例的清潔方法的流程圖。2 is a flow chart of a cleaning method in accordance with a first embodiment of the present invention.
參照圖1和圖2,在圖2的操作S1中,裝置1的反應器10的內部壓力被調節成適合進行清潔。反應器10內部的壓力爲0.3-10托爾(torr)。隨著反應器10的內部壓力降低,清潔效率增加。反應器10的內部壓力維持在0.5-4torr。Referring to Figures 1 and 2, in operation S1 of Figure 2, the internal pressure of the reactor 10 of the apparatus 1 is adjusted to be suitable for cleaning. The pressure inside the reactor 10 is from 0.3 to 10 torr. As the internal pressure of the reactor 10 decreases, the cleaning efficiency increases. The internal pressure of the reactor 10 is maintained at 0.5-4 torr.
接下來,在操作S2中,藉由供應清潔氣體至反應器10,此清潔氣體包括藉由使用遠程電漿産生器22激活之鹵素,並且同時供應未被激活之碳移除氣體至反應器10,在不停止運轉裝置1的情况下清潔反應器10的內部。清潔操作S2的時間根據反應器10的污染程度而變化,並且可根據處理了1000個還是500個晶圓而變化。儘管根據條件而有所變化,但含碳膜是以大約1000Å/min的速度來移除。因此,當處理1000個具有膜厚為200Å的晶圓時,清潔要進行200分鐘。Next, in operation S2, by supplying a cleaning gas to the reactor 10, the cleaning gas includes a halogen activated by using the remote plasma generator 22, and simultaneously supplies an unactivated carbon removal gas to the reactor 10. The inside of the reactor 10 is cleaned without stopping the operation device 1. The time of the cleaning operation S2 varies depending on the degree of contamination of the reactor 10, and can vary depending on whether 1000 or 500 wafers are processed. The carbon-containing film is removed at a rate of about 1000 Å/min, although it varies depending on conditions. Therefore, when processing 1000 wafers having a film thickness of 200 Å, the cleaning is performed for 200 minutes.
當使用裝置1沈積諸如TaCN的膜時,包括鹵素的清潔氣體可以是NF3 ,而碳移除氣體可以是O2 。藉由操作遠程電漿産生器22、電漿化清潔氣體並供應清潔氣體至反應器10可進一步最大化清潔效率。氬(Ar)可作爲用以産生電漿的基本製程氣體(base process gas)。When a film such as TaCN is deposited using the device 1, the cleaning gas including halogen may be NF 3 and the carbon removal gas may be O 2 . The cleaning efficiency can be further maximized by operating the remote plasma generator 22, plasmaizing the cleaning gas, and supplying the cleaning gas to the reactor 10. Argon (Ar) can be used as a base process gas for generating plasma.
當僅使用一般乾式清潔氣體的腐蝕氣體來進行清潔時,存在於反應器內的碳及氟化物會彼此反應而形成氟化碳(fluoride carbon)並且産生固體形式的副產物。因此, 反應器10無法完全地清潔。在本發明中,藉由使用包括鹵素的清潔氣體且將碳移除氣體添加至包括鹵素的清潔氣體來移除反應器10中的金屬副產物,可在不產生固體形式之副産物的情况下清潔反應器10。因此,在處理預定數量之晶圓後,在不停止運轉膜沈積裝置的情况下進行原位清潔,使得膜沈積裝置的生産力得以最大化。特別是,藉由部份激活的氣體來實現本發明。清潔氣體在激活狀態下使用,而碳移除氣體在未被激活的情況下使用。When cleaning is performed using only the corrosive gas of a general dry cleaning gas, the carbon and fluoride present in the reactor react with each other to form fluoride carbon and produce by-products in solid form. therefore, Reactor 10 cannot be completely cleaned. In the present invention, by removing the metal by-product in the reactor 10 by using a cleaning gas including a halogen and adding a carbon removing gas to a cleaning gas including a halogen, it can be cleaned without producing a by-product of a solid form. Reactor 10. Therefore, after processing a predetermined number of wafers, in-situ cleaning is performed without stopping the operation of the film deposition apparatus, so that the productivity of the film deposition apparatus is maximized. In particular, the invention is achieved by a partially activated gas. The cleaning gas is used in an activated state, and the carbon removal gas is used without being activated.
當清潔氣體及碳移除氣體同時激活並供應至反應器時,它們會彼此反應並産生有機副產物,例如聚四氟乙烯(Teflon)。根據本發明人所進行的實驗結果,清潔氣體及碳移除氣體的各自流量(flux)必須調節到非常窄的範圍內以免産生有機副產物。因此,本發明提供了一種方法,此方法透過僅激活清潔氣體來最大化清洗效率,並且在未被激活碳移除氣體的情况下移除碳,同時不產生有機副産物。在此方法中,不需藉由精細調整清潔氣體及碳移除氣體的各自流量來避免有機副產物的産生。因此,反應器的再現性極好,並且可獲得更寬的清潔製程容限(process margin)。When the cleaning gas and the carbon removal gas are simultaneously activated and supplied to the reactor, they react with each other and produce organic by-products such as Teflon. According to the experimental results conducted by the inventors, the respective fluxes of the cleaning gas and the carbon removal gas must be adjusted to a very narrow range to avoid the production of organic by-products. Accordingly, the present invention provides a method of maximizing cleaning efficiency by activating only a cleaning gas, and removing carbon without activating carbon removal gas while not producing organic by-products. In this method, it is not necessary to avoid the generation of organic by-products by finely adjusting the respective flows of the cleaning gas and the carbon removal gas. Therefore, the reproducibility of the reactor is excellent, and a wider cleaning process margin can be obtained.
當清潔操作S2的反應完成時,進行移除殘留於反應器10內之氣體的清洗操作S3。反應器10、氣體管線及遠程電漿産生器22被清洗。這是因為清潔氣體等可能會殘留於反應器10及氣體管線內。當此類問題不會發生時,可省略清洗操作S3。在此考量上,清洗氣體可以是隋性氣體, 例如Ar或N2 。When the reaction of the cleaning operation S2 is completed, the cleaning operation S3 of removing the gas remaining in the reactor 10 is performed. The reactor 10, gas line and remote plasma generator 22 are cleaned. This is because a cleaning gas or the like may remain in the reactor 10 and the gas line. When such a problem does not occur, the cleaning operation S3 may be omitted. In this regard, the purge gas may be an inert gas such as Ar or N 2 .
圖3是根據本發明第二實施例的清潔方法的流程圖。Figure 3 is a flow chart of a cleaning method in accordance with a second embodiment of the present invention.
根據本發明第二實施例的清潔方法類似於圖2中的清潔方法,但與圖2之清潔方法的不同之處在於還包括其他操作。The cleaning method according to the second embodiment of the present invention is similar to the cleaning method of Fig. 2, but differs from the cleaning method of Fig. 2 in that other operations are also included.
參照圖1和圖3,在圖3的操作S11中,將反應器10的內部壓力調節成適合進行清潔。Referring to Figures 1 and 3, in operation S11 of Figure 3, the internal pressure of the reactor 10 is adjusted to be suitable for cleaning.
接下來,在操作S12中,進行O2 處理。進行O2 處理(操作S12)來氧化反應器10內部之副産物表面上的碳,並預先移除碳。Next, in operation S12, O 2 processing is performed. An O 2 treatment (operation S12) is performed to oxidize carbon on the surface of the by-product inside the reactor 10, and carbon is previously removed.
隨後,在操作S13中,藉由供應清潔氣體至反應器10,此清潔氣體包括藉由使用遠程電漿産生器22激活之鹵素,並且同時供應未被激活之碳移除氣體至反應器10來清潔反應器10的內部。Subsequently, in operation S13, by supplying a cleaning gas to the reactor 10, the cleaning gas includes a halogen activated by using the remote plasma generator 22, and simultaneously supplies an unactivated carbon removal gas to the reactor 10. The interior of the reactor 10 is cleaned.
當清潔操作S13完成時,進行移除殘留在反應器10內之氣體的操作S14。圖2中的操作S3可作為操作S14。When the cleaning operation S13 is completed, the operation S14 of removing the gas remaining in the reactor 10 is performed. Operation S3 in Fig. 2 can be performed as operation S14.
接下來,在操作S15中,藉由使用含氫氣體進一步進行處理裝置1的操作,以移除清潔氣體的殘留。在此情况下,含氫氣體可以是從由H2 、NH3 、SiH4 、H2 O及其組合組成的群組中選擇的一種氣體。含氫氣體可簡單地進行清洗或藉由在含氫氣體內産生電漿來進行處理。Next, in operation S15, the operation of the processing apparatus 1 is further performed by using a hydrogen-containing gas to remove the residual of the cleaning gas. In this case, the hydrogen-containing gas may be a gas selected from the group consisting of H 2 , NH 3 , SiH 4 , H 2 O, and combinations thereof. The hydrogen-containing gas can be simply washed or treated by generating a plasma in a hydrogen-containing gas.
接下來,藉由使用含碳膜來進行陳化(seasoning)反應器10內部的操作,並且使反應器10最適於進行膜沈積。Next, the operation inside the reactor 10 is seasoned by using a carbon-containing film, and the reactor 10 is most suitable for film deposition.
在清潔完成後,爲了藉由裝載晶圓來進行膜沈積,需組合反應器10內的大氣。這是因爲會發生在清潔完成後第一次沈積的膜與後續製程沈積的膜具有不同屬性(例如膜厚度降低)的問題。因此,作爲清潔方法的最後操作,在加載第一個晶圓之前,預先進行陳化操作S16,也就是在反應器10的內部表面上覆蓋即將沈積於晶圓上之膜。After the cleaning is completed, in order to perform film deposition by loading the wafer, it is necessary to combine the atmosphere in the reactor 10. This is because the problem that the film deposited for the first time after the cleaning is completed has a different property (for example, a decrease in film thickness) from the film deposited in the subsequent process. Therefore, as a final operation of the cleaning method, before the loading of the first wafer, the aging operation S16 is performed in advance, that is, the film to be deposited on the wafer is covered on the inner surface of the reactor 10.
儘管參照其範例性實施例具體顯示且描述了本發明,但本領域熟知此項技術者應理解在不脫離如後續申請專利範圍所定義之本發明的精神和範圍的情況下還可以進行各種形式及細節上的修改。Although the present invention has been particularly shown and described with respect to the exemplary embodiments thereof, those skilled in the art should understand that various forms can be carried out without departing from the spirit and scope of the invention as defined in the appended claims. And the details of the changes.
根據本發明,可有效地清潔沈積含碳膜之裝置。藉由供應清潔氣體至反應器,此清潔氣體包括藉由使用遠程電漿産生器激活之鹵素,並且同時供應未被激活之碳移除氣體至反應器來清潔反應器內部的金屬副產物,使得可以在不産生固體形式之副產物的情况下清潔反應器。因此,在處理預定數量的晶圓後,在不停止運轉沈積含碳膜之裝置的情况下進行原位清潔,使得沈積含碳膜之裝置的生産力得以最大化。According to the present invention, a device for depositing a carbon-containing film can be effectively cleaned. By supplying a cleaning gas to the reactor, the cleaning gas includes a halogen activated by a remote plasma generator, and simultaneously supplies an unactivated carbon removal gas to the reactor to clean the metal by-products inside the reactor. The reactor can be cleaned without producing by-products in solid form. Therefore, after processing a predetermined number of wafers, in-situ cleaning is performed without stopping the operation of the device for depositing the carbon-containing film, so that the productivity of the device for depositing the carbon-containing film is maximized.
特別是,在使用部份激活氣體的反應器清潔方法中,清潔氣體是在激活狀態下使用,而碳移除氣體是在未被激活的情況下使用。故在此方法中,反應器的再現性極好,並且可獲得更寬的清潔製程容限。In particular, in a reactor cleaning method using a partial activation gas, the cleaning gas is used in an activated state, and the carbon removal gas is used without being activated. Therefore, in this method, the reproducibility of the reactor is excellent, and a wider cleaning process tolerance can be obtained.
如上所述,本發明提供了一種沈積含碳膜之裝置的原位清潔方法。一般來說,藉由僅使用腐蝕氣體進行清潔時, 會在反應器內産生固體形式的副產物,並且因此無法完全地清潔反應器。在本發明中,藉由使用包括鹵素的清潔氣體且添加碳移除氣體至包括鹵素的清潔氣體來移除反應器中的金屬副產物,可在不產生固體形式之副産物的情况下清潔反應器。As described above, the present invention provides an in-situ cleaning method for depositing a carbon-containing film. Generally, when cleaning is performed using only corrosive gases, A by-product in the form of a solid is produced in the reactor and thus the reactor cannot be completely cleaned. In the present invention, the reactor can be cleaned without producing by-products in a solid form by removing the metal by-products in the reactor by using a cleaning gas including a halogen and adding a carbon removal gas to a cleaning gas including a halogen. .
特別是,本發明介紹一種使用部份激活氣體的反應器清潔方法。清潔氣體在激活狀態下使用,而碳移除氣體在未被激活的情況下使用。在此方法中,反應器的再現性極好,並且可獲得更寬的清潔製程容限。In particular, the present invention describes a reactor cleaning method that uses a partially activated gas. The cleaning gas is used in an activated state, and the carbon removal gas is used without being activated. In this method, the reproducibility of the reactor is excellent, and a wider cleaning process tolerance can be obtained.
1‧‧‧膜沈積裝置1‧‧‧membrane deposition device
10‧‧‧反應器10‧‧‧Reactor
11‧‧‧噴頭11‧‧‧ sprinkler
12‧‧‧晶圓塊12‧‧‧ Wafer block
20‧‧‧氣體供應裝置20‧‧‧ gas supply unit
22‧‧‧遠程電漿產生器22‧‧‧Remote plasma generator
W‧‧‧晶圓W‧‧‧ wafer
S1、S2、S3‧‧‧步驟S1, S2, S3‧‧‧ steps
S11、S12、S13、S14、S15、S16‧‧‧步驟S11, S12, S13, S14, S15, S16‧‧ steps
圖1繪示了用以進行根據本發明一實施例之清潔方法的沈積含碳膜之裝置。1 illustrates an apparatus for depositing a carbonaceous film for performing a cleaning method in accordance with an embodiment of the present invention.
圖2是根據本發明第一實施例的清潔方法的流程圖。2 is a flow chart of a cleaning method in accordance with a first embodiment of the present invention.
圖3是根據本發明第二實施例的清潔方法的流程圖。Figure 3 is a flow chart of a cleaning method in accordance with a second embodiment of the present invention.
S1、S2、S3‧‧‧步驟S1, S2, S3‧‧‧ steps
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TW200733215A (en) * | 2006-02-21 | 2007-09-01 | Applied Materials Inc | Enhancement of remote plasma source clean for dielectric films |
KR100765128B1 (en) * | 2006-05-30 | 2007-10-11 | 주식회사 아토 | Apparatus for cleaning of chemical vaporization deposition chamber and method of cleaning the same |
WO2007139270A1 (en) * | 2006-05-29 | 2007-12-06 | Ips Ltd. | Cleaning method of apparatus for depositing metal containing film |
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TW200733215A (en) * | 2006-02-21 | 2007-09-01 | Applied Materials Inc | Enhancement of remote plasma source clean for dielectric films |
WO2007139270A1 (en) * | 2006-05-29 | 2007-12-06 | Ips Ltd. | Cleaning method of apparatus for depositing metal containing film |
KR100765128B1 (en) * | 2006-05-30 | 2007-10-11 | 주식회사 아토 | Apparatus for cleaning of chemical vaporization deposition chamber and method of cleaning the same |
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