TW200403726A - Low temperature dielectric deposition using aminosilane and ozone - Google Patents

Low temperature dielectric deposition using aminosilane and ozone Download PDF

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TW200403726A
TW200403726A TW92119580A TW92119580A TW200403726A TW 200403726 A TW200403726 A TW 200403726A TW 92119580 A TW92119580 A TW 92119580A TW 92119580 A TW92119580 A TW 92119580A TW 200403726 A TW200403726 A TW 200403726A
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gas
tank
substrate
patent application
silicon
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TW92119580A
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Yoshihide Senzaki
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Asml Us Inc
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    • 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
    • H01L21/02104Forming layers
    • H01L21/02107Forming insulating materials on a substrate
    • H01L21/02109Forming insulating materials on a substrate characterised by the type of layer, e.g. type of material, porous/non-porous, pre-cursors, mixtures or laminates
    • H01L21/02112Forming insulating materials on a substrate characterised by the type of layer, e.g. type of material, porous/non-porous, pre-cursors, mixtures or laminates characterised by the material of the layer
    • H01L21/02123Forming insulating materials on a substrate characterised by the type of layer, e.g. type of material, porous/non-porous, pre-cursors, mixtures or laminates characterised by the material of the layer the material containing silicon
    • H01L21/02126Forming insulating materials on a substrate characterised by the type of layer, e.g. type of material, porous/non-porous, pre-cursors, mixtures or laminates characterised by the material of the layer the material containing silicon the material containing Si, O, and at least one of H, N, C, F, or other non-metal elements, e.g. SiOC, SiOC:H or SiONC
    • H01L21/0214Forming insulating materials on a substrate characterised by the type of layer, e.g. type of material, porous/non-porous, pre-cursors, mixtures or laminates characterised by the material of the layer the material containing silicon the material containing Si, O, and at least one of H, N, C, F, or other non-metal elements, e.g. SiOC, SiOC:H or SiONC the material being a silicon oxynitride, e.g. SiON or SiON:H
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/22Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the deposition of inorganic material, other than metallic material
    • C23C16/30Deposition of compounds, mixtures or solid solutions, e.g. borides, carbides, nitrides
    • C23C16/308Oxynitrides
    • 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
    • H01L21/02104Forming layers
    • H01L21/02107Forming insulating materials on a substrate
    • H01L21/02109Forming insulating materials on a substrate characterised by the type of layer, e.g. type of material, porous/non-porous, pre-cursors, mixtures or laminates
    • H01L21/02205Forming insulating materials on a substrate characterised by the type of layer, e.g. type of material, porous/non-porous, pre-cursors, mixtures or laminates the layer being characterised by the precursor material for deposition
    • H01L21/02208Forming insulating materials on a substrate characterised by the type of layer, e.g. type of material, porous/non-porous, pre-cursors, mixtures or laminates the layer being characterised by the precursor material for deposition the precursor containing a compound comprising Si
    • H01L21/02219Forming insulating materials on a substrate characterised by the type of layer, e.g. type of material, porous/non-porous, pre-cursors, mixtures or laminates the layer being characterised by the precursor material for deposition the precursor containing a compound comprising Si the compound comprising silicon and nitrogen
    • 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
    • H01L21/02104Forming layers
    • H01L21/02107Forming insulating materials on a substrate
    • H01L21/02225Forming insulating materials on a substrate characterised by the process for the formation of the insulating layer
    • H01L21/0226Forming insulating materials on a substrate characterised by the process for the formation of the insulating layer formation by a deposition process
    • H01L21/02263Forming insulating materials on a substrate characterised by the process for the formation of the insulating layer formation by a deposition process deposition from the gas or vapour phase
    • H01L21/02271Forming insulating materials on a substrate characterised by the process for the formation of the insulating layer formation by a deposition process deposition from the gas or vapour phase deposition by decomposition or reaction of gaseous or vapour phase compounds, i.e. chemical vapour deposition
    • H01L21/02274Forming insulating materials on a substrate characterised by the process for the formation of the insulating layer formation by a deposition process deposition from the gas or vapour phase deposition by decomposition or reaction of gaseous or vapour phase compounds, i.e. chemical vapour deposition in the presence of a plasma [PECVD]

Abstract

This invention describes a method of depositing dielectric layers or films with good step coverage and ability to fill high-aspect ratio device structures at low temperature (20-400C) by CVD processes through the use of aminosilane or silicon alkylamide compounds as the silicon precursor with an oxidizerthat includes ozone. The present invention further provides a method of depositing silicon oxynitride (SiOxNy) films at low temperatures using aminosilane or silicon alkylamide compounds as a silicon precursor, with an oxidizer that includes ozone, and ammonia (NH3).

Description

200403726 (1) 玖、發明說明 相關申請案 此申請案係關於2 0 0 2年7月1 9日提出申請的美國專利 申請案第60/396,746號,其標題爲”Low Temperature Dielectric Deposition Using Aminosilane and Ozone(利用 胺基甲矽烷和臭氧於低溫沉積介電質的方法)”並聲明其優 先權,茲處將此申請案中所述者列入參考。 【發明所屬之技術領域】 本發明一般係關於半導體範圍。更特定言之,本發明 係關於在半導體裝置和晶圓上之化學蒸鍍法。 【先前技術】 半導體裝置製造上,低壓熱化學蒸鍍(CVD)製造具有 良好逐步覆蓋性質和可接受之塡隙縱橫比的金屬前 (premetal)介電膜。一些先質(如:雙(第三丁基胺基)甲矽 烷(BTBAS)和Et2SiH2)與02於約400 °C反應時,藉化學蒸鍍 (C V D )製造S i Ο 2。但新一代整體電路須要較低溫法用於金 屬前介電(PMD)和定位應用。一個代替降低加工溫度的方 式是使用高密度電漿(HDP)化學蒸鍍(HDPCVD)法。藉此 H D P C V D法,摻磷的玻璃(p s g )或未摻雜的矽酸鹽玻璃 (NSG)於3〇〇- 5 5 0 °C澱積。但HDP化學蒸鍍有著會限制其使 用性的缺點。H D P C V D法的塡隙力限於約3 : 1縱橫比’較 局溫度熱C V D法達到較所欲的6 : 1或更高塡隙縱橫比。因 (2) (2)200403726 此,工業上須要於較低溫度在金屬前介電物上進行化學蒸 鑛且同時維持良好逐步覆蓋率的方法。 【發明內容】 本發明提出於約400 °C或以下的低溫,使Si〇2和其他 氧化物激積在砂底質上,並維持良好逐步覆蓋率和塡隙力 的方法。 本發明之方法可用於經摻雜和未經摻雜的S i Ο 2澱積。 此方法於1C製造的典型應用是金屬前介電物(PMD)、淺溝 隔絕(STI)、溝襯料和定位介電物,但不在此限。 本發明之澱積法亦可使用Ο 3和nh3之混合物作爲反應 物氣體地以氧氮化矽進行。本發明的其他優點包括使用矽 以外的底質,如:Sic、SOI、扁平板、鎢或鋁。 本發明的一個特點中,提出在加工槽中,使介電層澱 積於底質表面上的方法,包含使底質暴於包含氧化劑氣體 和矽先質的反應性氣體中,此處,氧化劑氣體包括臭氧, 矽先質包括甲矽烷基醯胺和胺基甲矽烷中之至少一者。此 方法於約20 °C至400 °c溫度範圍內實行。 本發明的另一特點中,提出一種在槽中使氧氮化矽澱 積於底質上的方法,包含使底質暴於包含氧化劑氣體、氨 和矽先質的反應物氣體中,此處,氧化劑氣體包括臭氧, 矽先質包括甲矽烷基醯胺和胺基甲矽烷中之至少一者。此 方法於約20 °C至400 °C溫度範圍內實行。 (3) 200403726 【實施方式】 本發明提出一種新穎的低熱預算法,其藉化學蒸 (C V D ) ’於等於或低於約4 0 0 °C的溫度,在半導體底質 源積介電層或膜。本發明的一個實施例中,C V D反應以 列式扼要說明:200403726 (1) 发明. Description of the related application This application is related to US Patent Application No. 60 / 396,746, filed on July 19, 2002, entitled "Low Temperature Dielectric Deposition Using "Aminosilane and Ozone (method of depositing dielectrics at low temperature by using aminosilane and ozone)" and declares its priority, and the reference in this application is hereby incorporated by reference. [Technical Field to which the Invention belongs] The present invention relates generally to the field of semiconductors. More specifically, the present invention relates to a chemical vapor deposition method on semiconductor devices and wafers. [Previous Technology] In semiconductor device manufacturing, low-pressure thermochemical evaporation (CVD) manufactures a premetal dielectric film with good progressive coverage properties and an acceptable gap aspect ratio. Some precursors (such as bis (third butylamino) silyl (BTBAS) and Et2SiH2) react with 02 at about 400 ° C to produce Si O 2 by chemical vapor deposition (C V D). However, the new generation of integrated circuits requires lower temperature methods for Pre-Metal Dielectric (PMD) and positioning applications. An alternative to lowering the processing temperature is to use a high-density plasma (HDP) chemical vapor deposition (HDPCVD) method. By this H D P C V D method, a phosphorus-doped glass (p s g) or an undoped silicate glass (NSG) is deposited at 300-550 ° C. However, HDP chemical vapor deposition has the disadvantage of limiting its usability. The gap force of the H D P C V D method is limited to about 3: 1 aspect ratio. The local temperature thermal C V D method achieves a desired gap aspect ratio of 6: 1 or higher. Because of (2) (2) 200403726, industrially, it is necessary to carry out chemical distillation on the pre-metal dielectric at a lower temperature while maintaining a good step coverage. [Summary of the Invention] The present invention proposes a method for causing Si02 and other oxides to accumulate on the sandy substrate at a low temperature of about 400 ° C or below, and to maintain a good step coverage and crevice force. The method of the present invention can be used for doped and undoped Si02 deposition. Typical applications of this method in 1C manufacturing are metal front dielectrics (PMD), shallow trench isolation (STI), trench liners, and positioning dielectrics, but not limited to this. The deposition method of the present invention can also be performed with silicon oxynitride using a mixture of 0 3 and nh 3 as a reactant gas. Other advantages of the present invention include the use of substrates other than silicon, such as Sic, SOI, flat plates, tungsten, or aluminum. In a feature of the present invention, a method for depositing a dielectric layer on the surface of a substrate in a processing tank is provided, which comprises exposing the substrate to a reactive gas containing an oxidant gas and a silicon precursor. Here, the oxidant The gas includes ozone, and the silicon precursor includes at least one of silylamidoamine and aminosilane. This method is performed over a temperature range of approximately 20 ° C to 400 ° c. In another feature of the present invention, a method for depositing silicon oxynitride on a substrate in a tank is provided, which comprises exposing the substrate to a reactant gas containing an oxidant gas, ammonia, and a silicon precursor. Here, The oxidant gas includes ozone, and the silicon precursor includes at least one of silylamidoamine and aminosilane. This method is performed over a temperature range of approximately 20 ° C to 400 ° C. (3) 200403726 [Embodiment] The present invention proposes a novel low thermal budget method, which uses chemical vaporization (CVD) 'at a temperature equal to or lower than about 400 ° C to deposit a dielectric layer on a semiconductor substrate or membrane. In one embodiment of the present invention, the C V D reaction is briefly described in terms of:

Si(NRlR2)^ + 氧化劑氣體—Si02 (1) 其中矽先質是3丨"111112)4,111或112 = }1,(:1-(:6烷基 環狀院基、經F取代的院基, 或 SWNRiRi.xLdXMj 或 3),此處 L = H 或 C1 式(1 )中,胺基甲矽烷和甲矽烷基醯胺化合物(作爲 先質)中的S i -N鍵具活性且會與氧化劑氣體於比其他含 的先質來得低的溫度反應。此類型化合物中的較佳矽先 具較小R基團,如:甲基乙基醯胺。此反應於有底質存 的反應器或槽中進行。使用臭氧作爲氧化劑氣體的組份 Si〇2 CVD法溫度可降至低於400 °c並維持低壓熱CVD法 良好逐步覆蓋性和塡隙力。臭氧氣體於比其他氧化 (如:水或〇2)來得低的溫度提供原子態氧。此反應中的 先質之氧化反應於約2 0 0 °C或以下得到良好結果,較佳 度範圍是2 0 °C至3 0 0 °C。加工氣體流率範圍中,就先質 流而言,約〗seem至1 OOOsccm,以在約} 〇至5〇〇sccm範圍 爲佳。氧化劑氣體流率在約1 0至2 0 0 0 s c c m範圍內,以在 1 00-2000sccni範圍內爲佳。 一些情況中亦可以使用稀釋氣流,以改善均勻性, 此非必要。惰性氣體(如:氮、氦、氖、氬、氙和它們 鍍 上 下 矽 Si 質 在 5 的 劑 矽 溫 氣 內 約 但 的 ' 6 - (4) (4)200403726 ’組α )可以作爲稀釋氣體。就成本考量,氮和氬是較佳稀 釋體。惰性氣體流率在約1 s C c ηι至1 Q 〇 〇 s c c 1Ώ範圍內。所 有* 1青況中’氣體流率視槽尺寸和抽取力而定,壓力必須在 所須範圍內’嫻於此技術者可藉慣用實驗定出這樣的變 數。 本發明的其他特點中,形成氧氮化矽。置於槽中的底 質暴於下列反應物,CVD反應以下列式扼要說明:Si (NRlR2) ^ + oxidant gas—Si02 (1) where the precursor of silicon is 3 丨 " 111112) 4,111 or 112 =} 1, (: 1-(: 6 alkyl cyclic radical, substituted by F Or SWNRiRi.xLdXMj or 3), where L = H or C1 In the formula (1), the Si -N bond in the aminosilyl and silylamidoamine compounds (as precursors) is active And it will react with the oxidant gas at a lower temperature than other precursors. The better silicon in this type of compound has a smaller R group, such as methyl ethyl amidamine. This reaction is based on the presence of a substrate The temperature of the Si02 CVD method using ozone as the oxidant gas component can be reduced to less than 400 ° C and maintain the good step coverage and gap force of the low-pressure thermal CVD method. Ozone gas is better than other Oxidation (such as: water or 〇2) to provide atomic oxygen at a low temperature. The oxidation of the precursor in this reaction gives good results at about 200 ° C or below, and the preferred range is 20 ° C to 3 0 0 ° C. In the process gas flow rate range, in terms of the precursor flow, about [see] to 1000 sccm, preferably in the range of about 0 to 500 sccm. Oxygen The flow rate of the agent gas is in the range of about 10 to 2000 sccm, preferably in the range of 100-2000 sccni. In some cases, a dilute gas stream can also be used to improve uniformity. This is not necessary. Inert gas (such as : Nitrogen, helium, neon, argon, xenon, and their upper and lower silicon coatings with a Si content of about 5 in the temperature of the agent, the temperature of '6-(4) (4) 200403726 (group α) can be used as a dilution gas. In terms of cost considerations Nitrogen and argon are the preferred diluents. The inert gas flow rate is in the range of about 1 s C c η to 1 Q 〇scs 1Ώ. In all * 1 cases, the 'gas flow rate depends on the tank size and extraction force, The pressure must be within the required range. Those skilled in the art can determine such variables by customary experiments. In other features of the present invention, silicon oxynitride is formed. The substrate placed in the tank is exposed to the following reactants, CVD The reaction is briefly described in the following formula:

Si(NRR)4 + NH3 + O3 — SiOxNy (2) 其中矽先質是SKNR1!^2)*,R】或R2 = H,C「C6烷基、 環狀烷基、經F取代的烷基, 或 Si(NR】R2)4_xLx(X=l,2 或 3),此處 L = H 或 C1 式(2)中,使用NH3和03氣體混合物,於低溫澱積氧氮 化矽(SiOxNy)。除了半導體應用以外,SiOxNy也是一種重 要的光學應用材料,這是因爲折射指數變化介於S i 02的 1 · 4 5和氮化矽的2.0之間之故。如式(1)反應,胺基甲矽烷 或甲矽烷基醯胺化合物中的Si-N鍵相當不穩定並與臭氧於 低溫反應,使得於低於400 °C實施低溫CVD法。本發明的 此特點中,氨(N Η 3)的氣體流率在約1 0 s c c m至2 0 0 0 s c c m範 圍內,以在約1 OOsccm至2000sccm範圍內爲佳。此新穎方 法可用於摻雜和未摻雜的Si〇2形成。此方法於1C製造之應 用包括,但不限於,金屬前介電物(PMD)、淺溝隔絕 (STI)、溝襯料和定位介電物。 本發明的另一特點中,改變壓力以使方法最適合不同 應用。參考式(1 )和(2 ),此反應可於大氣壓進行並得到良 (5) (5)200403726 好結果,或者反應可於約1毫托耳高至約8 〇 〇托耳的壓力範 圍內進行。例如,反應可於減低壓力進行以進一步改善在 非平面底質上的逐步覆蓋率。或者,在對於逐步覆蓋率要 求較不嚴苛的P M D應用中,可以使用較高壓力。通常,壓 力越高,反應速率和所得澱積速率越高。 本發明中所用底質基本上是矽。但可以使用其他底質 如·· SiC、SOI、扁平板、鎢或鋁)代替矽並仍屬本發明範 圍和精神內。底質之選擇視特定要求而定。 本發明可以已知澱積系統(如:常用的CVD、 PECVD、噴霧熱解、電弧噴注澱積或ALD系統)進行。參 考附圖1,其爲適用以實施本發明之方法之C v D系統1 〇的 簡化截面圖。矽晶圓100載入澱積槽〗〇1中並以晶圓載體或 載物架102承載。此方法可於低或接近大氣壓力實,施。在 此加工槽1 0 1中,晶圓1 〇〇藉加熱器(以位於載體1 02內爲佳) 加熱至澱積溫度。用於CVD法,稀釋氣體1 03經由注射器 1 1〇引至槽101中建立加工壓力。之後,使用半導體和薄膜 工業中慣用的氣體輸送法,矽先質1 0 4和氧化劑1 〇 5 (欲澱 積SiOxNy時,也有NH3 106)氣體引至槽中。反應物氣體運 送至接近晶圓。反應物氣體混合及反應,在晶圓表面上形 成所欲材料層。經過達到目標厚度的適當時間之後,關掉 矽先質和氧化劑/ NH3氣流,較佳情況中,運送稀釋惰性 氣流至槽以將槽中殘餘反應物滌除通過排放口 1 1 2。經過 適當滌氣時間之後,加工完全並自加工槽移除晶圓。 雖然本發明的說明實施例是CVD澱積,此處所述反應 (6) (6)200403726 和方法亦可有利地藉其他澱積技巧(包括電漿增進的 CVD(PECVD)、噴霧熱解、電弧噴注或陰極電弧噴灑澱積 和旋塗於玻璃上(含水化學)澱積)用以澱積介電膜。本發 明亦可用於原子層澱積(ALD),此處可分別運送反應物。 已如專利法所要求的細節和特點描述本發明,所申請 及所欲於專利權證書中保護者乃述於所附申請專利範圍 中〇 【圖式簡單說明】 在詳細說明中和利用附圖進一步描述本發明,其中: 附圖1所示者是適用以實施本發明之方法的c V D設 備。 【符號說明】 10 CVD系統 1 0 0 ί夕晶圓 101 澱積槽 1 0 2 晶圓載體或載物架 103 稀釋氣體 104 矽先質 1 0 5 氧化劑 106 ΝΗ3 1 1 0 注射器 I 1 2 排放口Si (NRR) 4 + NH3 + O3 — SiOxNy (2) where the silicon precursor is SKNR1! ^ 2) *, R] or R2 = H, C "C6 alkyl, cyclic alkyl, F-substituted alkyl , Or Si (NR) R2) 4_xLx (X = 1, 2 or 3), where L = H or C1 In formula (2), a mixture of NH3 and 03 gas is used to deposit silicon oxynitride (SiOxNy) at low temperature. In addition to semiconductor applications, SiOxNy is also an important material for optical applications, because the refractive index changes between 1.25 of Si 02 and 2.0 of silicon nitride. As shown in the reaction of formula (1), amine The Si-N bond in the silyl silane or silyl ammonium amine compound is quite unstable and reacts with ozone at low temperature, so that the low temperature CVD method is performed at less than 400 ° C. In this feature of the present invention, ammonia (N Η 3 The gas flow rate is in the range of about 10 sccm to 2000 sccm, preferably in the range of about 100 sccm to 2000 sccm. This novel method can be used for the formation of doped and undoped Si02. This method Applications manufactured at 1C include, but are not limited to, metal pre-dielectrics (PMD), shallow trench isolation (STI), trench linings, and positioning dielectrics. In another feature of the invention, changing the pressure In order to make the method most suitable for different applications. With reference to formulas (1) and (2), this reaction can be performed at atmospheric pressure with good results (5) (5) 200403726, or the reaction can be as high as about 1 millitorr to about 8 〇〇tor in the pressure range. For example, the reaction can be performed at reduced pressure to further improve the step coverage on non-planar substrates. Alternatively, in PMD applications where step coverage is less stringent, it can be Higher pressure is used. Generally, the higher the pressure, the higher the reaction rate and the resulting deposition rate. The substrate used in the present invention is basically silicon. However, other substrates such as SiC, SOI, flat plate, tungsten or Aluminum) instead of silicon is still within the scope and spirit of the present invention. The choice of substrate depends on specific requirements. The present invention can be known deposition systems (such as: commonly used CVD, PECVD, spray pyrolysis, arc spray deposition) Or ALD system). Referring to FIG. 1, it is a simplified cross-sectional view of a C v D system 10 suitable for implementing the method of the present invention. A silicon wafer 100 is loaded into a deposition tank and a wafer carrier is used. Or carrier 102. This method Can be applied at low or near atmospheric pressure. In this processing tank 101, the wafer 100 is heated to the deposition temperature by a heater (preferably located in the carrier 102). It is used in the CVD method and diluted The gas 103 is introduced into the tank 101 through a syringe 110 to establish a processing pressure. Thereafter, a conventional gas transportation method commonly used in the semiconductor and thin film industries, a silicon precursor 104 and an oxidizing agent 105 is used (for deposition of SiOxNy, there is also NH3 106) gas is introduced into the tank. The reactant gas is transported close to the wafer. The reactant gases are mixed and reacted to form a desired material layer on the wafer surface. After an appropriate time to reach the target thickness, turn off the silicon precursor and oxidant / NH3 gas stream. Preferably, a dilute inert gas stream is sent to the tank to remove residual reactants in the tank through the discharge port 1 1 2. After a suitable scrubbing time, the processing is complete and the wafer is removed from the processing tank. Although the illustrative embodiment of the present invention is CVD deposition, the reactions (6) (6) 200403726 and methods described herein may also advantageously take advantage of other deposition techniques (including plasma enhanced CVD (PECVD), spray pyrolysis, Arc spray or cathodic arc spray deposition and spin-on-glass (aqueous chemical deposition) are used to deposit dielectric films. The invention can also be used for atomic layer deposition (ALD), where reactants can be transported separately. The invention has been described with the details and characteristics required by the patent law. The applicants and those who want to be protected in the patent certificate are described in the scope of the attached application patent. [Simplified illustration of the drawing] In the detailed description and using the drawings The invention is further described, in which: the one shown in Figure 1 is a cVD device suitable for carrying out the method of the invention. [Symbol description] 10 CVD system 1 0 0 ί wafer 101 deposition tank 1 0 2 wafer carrier or carrier 103 dilution gas 104 silicon precursor 1 0 5 oxidant 106 Ν 3 1 1 0 syringe I 1 2 discharge port

Claims (1)

200403726 ⑴ 拾、申請專利範圍 1 · 一種在槽中使介電層源積於底質上的方法,包 含: 使底質暴於包含氧化劑氣體和砂先質的反應物氣體, 其中氧化劑氣體包括臭氧,而矽先質包括甲砂院基醯 胺和胺基甲砂院中之至少一者’且其中當反應物氣體存在 於槽中時,槽溫度在接近20 °C至400 t範圍。 2 .如申請專利範圍第1項之方法,其中當反應物氣 體存在於槽中時,槽中壓力在1毫托耳至76〇托耳範圍。 3 . 如申S靑專利範圍第1項之方法,其中藉著使反應 物氣體在槽中流過底質上,而使底質暴於反應物氣體。 4 . 如申請專利範圍第3項之方法,其中矽先質氣體 流率爲lsccm至lOOOsccm,而臭氧氣體流率爲r〇至 2 0 0 0 s c c m 〇 5 · 如申請專利範圍第4項之方法,其進一步包含倂 流一稀釋氣體於反應物氣體。 6. 如申請專利範圍第1項之方法,其中該反應物氣 體另包括氨。 7. 一種在槽中使氧氮化矽澱積於底質上的方法,包 含: 使底質暴於包含氧化劑氣體、氨和矽先質的反應物氣 體, 其中氧化劑氣體包括臭氧,而矽先質包括甲矽烷基醯 胺和胺基甲矽烷中之至少一者,其中當反應物氣體存在於 -10- U· fr (2) (2)200403726 槽中時,槽溫度接近20°C至40(TC範圍。 8 · 如申請專利範圍第7項之方法,其中當反應物氣 體存在於槽中時,槽中壓力在1毫托耳至7 6〇托耳範圍。 9 · 如申請專利範圍弟8項之方法,其中藉著使反應、 物氣體在槽中流過底質上,而使底質暴於反應物氣p。 10.如申請專利¥(3圍弟9項之方法,其中砂先皙氣體 流率爲1 s c c m至1 0 0 0 s c c m,而臭氧氣體流率爲1 〇至 2 0 0 0 s c c m ° 11·如申請專利範圍第1 〇項之方法,其進一步包含倂 流一稀釋氣體於反應物氣體。 1 2 ·如申請專利範圍第1 1項之方法,其中該稀釋氣體 是惰性氣體。 13.如申請專利範圍第1 2項之方法,其中該惰性氣體 是氣或氮。 14 ·——種在槽中使氧化矽澱積於底質上的方法,包含 在槽中,於底質存在時,使臭氧和矽先質反應,其中 槽溫度低於400 °C,而矽先質包含甲矽烷基醯胺和胺基甲 矽烷中之至少一者,且氧化劑氣體包含臭氧。 15·如申請專利範圍第1 4項之方法,其進一步包含使 氨與氧化劑氣體和砂先質反應。 16. 如申請專利範圍第1 4項之方法,其進一步包含當 在槽中於底質存在時使氧化劑氣體和矽先質反應的步驟期 間,使一惰性氣體流過槽中。 17. 如申請專利範圍第14項之方法,其中溫度在20至 -11 - 200403726 (3) 4 0 0 °C範圍200403726 ⑴ Pickup, patent application scope 1 · A method for depositing a dielectric layer on a substrate in a tank, comprising: exposing the substrate to a reactant gas containing an oxidant gas and a sand precursor, wherein the oxidant gas includes ozone The silicon precursor includes at least one of methylamine and amidoamine, and when the reactant gas is present in the tank, the tank temperature is in the range of approximately 20 ° C to 400 t. 2. The method according to item 1 of the patent application range, wherein when the reactant gas is present in the tank, the pressure in the tank is in the range of 1 mTorr to 760 Torr. 3. The method of claim 1 of the patent scope, wherein the substrate is exposed to the reactant gas by flowing the reactant gas through the substrate in the tank. 4. The method according to item 3 of the patent application, wherein the silicon precursor gas flow rate is lsccm to 1000 sccm, and the ozone gas flow rate is r0 to 2000 scm 〇5. It further comprises flowing a diluent gas to the reactant gas. 6. The method of claim 1 in which the reactant gas further includes ammonia. 7. A method for depositing silicon oxynitride on a substrate in a tank, comprising: exposing the substrate to a reactant gas containing an oxidant gas, ammonia, and a silicon precursor, wherein the oxidant gas includes ozone, and the silicon first The substance includes at least one of silylamidoamine and aminosilane, wherein when the reactant gas is present in the -10-U · fr (2) (2) 200403726 tank, the tank temperature is close to 20 ° C to 40 ° C. (TC range. 8) The method according to item 7 of the patent application range, wherein when the reactant gas is present in the tank, the pressure in the tank is in the range of 1 millitorr to 760 torr. 9 The method of item 8, wherein the substrate is exposed to the reactant gas p by passing the reaction and material gas through the substrate in the tank. 10. For example, the method of item 9 of the patent application (where the sand is first) The flow rate of white gas is from 1 sccm to 100 sccm, and the flow rate of ozone gas is from 10 to 200 sccm ° 11. As in the method of claim 10, it further includes a flow of diluent gas In reactant gas. 1 2 · The method according to item 11 of the patent application scope, wherein the dilute The gas is an inert gas. 13. The method according to item 12 of the patent application scope, wherein the inert gas is a gas or nitrogen. 14 · ——A method for depositing silicon oxide on a substrate in a tank, including the tank In the presence of a substrate, ozone and silicon precursors are reacted, wherein the tank temperature is lower than 400 ° C, and the silicon precursor contains at least one of silylamidoamine and aminosilane, and the oxidant gas contains Ozone. 15. The method of claim 14 in the scope of patent application, further comprising reacting ammonia with an oxidant gas and a sand precursor. 16. The method of claim 14 in the scope of patent application, further comprising During the step of reacting the oxidant gas with the silicon precursor in the presence of the substrate, an inert gas is caused to flow through the tank. 17. The method according to item 14 of the patent application, wherein the temperature is 20 to -11-200403726 (3) 4 0 0 ° C range
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