TW200422424A - Low temperature deposition of silicon oxides and oxynitrides - Google Patents

Low temperature deposition of silicon oxides and oxynitrides Download PDF

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Publication number
TW200422424A
TW200422424A TW092122655A TW92122655A TW200422424A TW 200422424 A TW200422424 A TW 200422424A TW 092122655 A TW092122655 A TW 092122655A TW 92122655 A TW92122655 A TW 92122655A TW 200422424 A TW200422424 A TW 200422424A
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Taiwan
Prior art keywords
deposition
patent application
silicon
ozone
substrate
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Application number
TW092122655A
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English (en)
Inventor
Yoshihide Senzaki
Sang-In Lee
Sang-Kyoo Lee
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Asml Us Inc
Integrated Process Systems Ltd
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Publication of TW200422424A publication Critical patent/TW200422424A/zh

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    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/455Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
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    • 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
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    • 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
    • C23C16/40Oxides
    • C23C16/401Oxides containing silicon
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    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/455Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
    • C23C16/45523Pulsed gas flow or change of composition over time
    • C23C16/45525Atomic layer deposition [ALD]
    • C23C16/45527Atomic layer deposition [ALD] characterized by the ALD cycle, e.g. different flows or temperatures during half-reactions, unusual pulsing sequence, use of precursor mixtures or auxiliary reactants or activations
    • C23C16/45531Atomic layer deposition [ALD] characterized by the ALD cycle, e.g. different flows or temperatures during half-reactions, unusual pulsing sequence, use of precursor mixtures or auxiliary reactants or activations specially adapted for making ternary or higher compositions
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    • C23C16/45523Pulsed gas flow or change of composition over time
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    • 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
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    • H01L21/02164Forming 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 being a silicon oxide, e.g. SiO2
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    • H01L21/0226Forming insulating materials on a substrate characterised by the process for the formation of the insulating layer formation by a deposition process
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  • Chemical Vapour Deposition (AREA)

Description

200422424 (1) 玖、發明說明 相關申請案 此申請案係關於2002年 8月18日提出申請的 U.S.Provisional Patent Application Serial No.60/404,363 ’其標題爲 ’’Low Temperature Deposition of Silicon Oxides and Oxynitrides(矽氧化物和矽氮氧化物之低溫澱 積法)’’,並聲明其優先權。 【發明所屬之技術領域】 本發明係關於半導體範圍。更特定言之,本發明係關 於自矽有機先質和臭氧形成矽氧化物和/或矽氮氧化物之 低溫化學蒸鍍法(CVD)和低溫原子層澱積法(ALD)。 【先前技術】 CVD是一種已知澱積法。CVD中,二或多種反應物 氣體於澱積槽中混在一起,氣體於此處以氣相反應並在基 板表面上澱積成膜或直接於基板表面上反應。藉CVD法 澱積進行特定時間長度,此依所欲澱積膜厚度爲基礎。因 爲特定時間與反應物進入槽的通量有關,所以各槽所須時 間會不同。 ALD也是一種已知方法。慣用ALD澱積循環中,各 反應物氣體先後引至槽中,因此沒有氣相內部混合情況發 生。第一種反應物(即,先質)單層物理或化學吸附於基板 表面上。之後去除過多的第一種反應物,此通常藉惰性滌 -5 - (2) (2)200422424 氣氣體和/或抽取之助。之後將第二種反應物引至澱積槽 中並與第一種反應物反應,經由自身限制的表面反應,形 成單層所欲膜。一旦初時吸附的第一種反應物與第二種反 應物完全反應,便會中止此自身限制反應。之後藉惰性氣 體和/或抽取之助,去除過多的第二種反應物。視所需地 重覆澱積循環,以得到所欲膜厚度。藉由簡單計算澱積循 環次數,此膜厚度精確度可控制至原子層(即,埃)。 已經知道將矽氧化物(SiOx)和矽氮氧化物(SiOxNy)膜 用於閘極和電容器應用。但是,隨著積體電路(1C)線寬尺 寸持續降低,此技巧(包括本CVD技巧)越來越不適用。 例如,已經知道使用CVD,藉矽有機先質與氧氣或 水蒸汽之反應澱積氧化矽層。但這樣的CVD法的溫度通 常必須超過60(TC —雖然雙(第三丁基胺基)矽烷(BTBAS) 和二乙基矽烷(Et2SiH2)與氧氣(02)於400 °C:反應。這樣的 高溫導致接觸金屬(如:鎢)的氧化反應,因此提高線阻抗 。此外,這樣的高溫導致金屬催化反應,在裝置結構中形 成所不欲鬚狀物(如:鎢鬚)。因此,須發展使用較低溫度 的澱積法。 另一實例中,在金屬前(pre-metal)介電(PMD)應用中 ,已經知道使用高密度電漿(HDP)CVD,於介於 3 00和 5 5 0 °C的溫度澱積摻磷玻璃(PSG)或未摻雜的矽酸鹽玻璃 (NSG)。但是,HDP CVD的縫隙塡補能力限於縱橫比約3 :1。縱橫比是縫隙高度與其寬度的比値;比値越高越難 塡補。有縫隙或孔洞存在於半導體裝置的金屬之間會導致 -6 - (3) (3)2004224 24 捕集水、細微破裂和短路。因此,須要縫隙塡補能力較高 的澱積法。 【發明內容】 提出低溫(即,低於約45 0 °C )澱積法,以澱積用於隔 絕物和金屬前介電應用的氧化矽和氮氧化矽層。此方法可 爲CVD和ALD法,使用臭氧作爲氧化劑並使甩矽有檄先 質及選用的氮來源。此低溫澱積法提供良好的漸近覆蓋和 縫隙塡補力,提供高縱橫比至6 : 1或以上。 本發明的一個特點中,將氧化矽層澱積於基板上的 CVD法包含至少一個循環包含下列步驟:(i)將矽有機先 質引至有基板位於其中的澱積區中;和(Π)將臭氧引至澱 積區中。本發明的此特點中,步驟可同時或連續進行。先 質和臭氧反應,在基板上形成氧化矽層。 本發明的另一特點中,將氮氧化矽層澱積於基板上的 一個CVD法包含至少一個循環包含下列步驟:(i)將矽有 機先質引至有基板位於其中的澱積區中;(ii)將臭氧引至 澱積區中;和(出)將氮來源(如:氨(NH3))引至澱積區中。 同樣地,這些步驟可同時或連續進行。先質、臭氧和氮來 源反應,在基板上形成氮氧化矽層。 本發明的另一特點中,將氧化矽層澱積於基板上的 C V D法包含至少一個循環包含下列步驟:(i)將矽有機先 質引至有基板位於其中的澱積區中;(Η)對澱積區滌氣; 和(iii)將臭氧引至澱積區中。本發明的此特點中’步驟連 (4) (4)2004224 24 續進行。此循·環多澱積一層氧化矽。可視達到所欲膜厚度 所需地多次重覆此循環,只要各循環之間經額外的癜積區 滌氣處理即可。 本發明的另一特點中,將氮氧化矽層澱積於基板上的 一個CVD法包含至少一個循環包含下列步驟:(i)將矽有 機先質引至有基板位於其中的澱積區中;(ii)對澱積區滌 氣;和(iii)將臭氧和氮來源(如:氨(NH3))引至澱積區中。 這些步驟連續進行。臭氧和氮之引入可分別或同時以任何 順序進行,並可視情況地藉對澱積槽滌氣的步驟區隔。此 循環多澱積一層氮氧化矽。可視達到所欲膜厚度所需地多 次重覆此循環,只要各循環之間經額外的澱積區滌氣處理 即可。 讀完本發明的下列詳述並參考附圖,會瞭解本發明的 其他特點和優點。 【實施方式】 本發明提出CVD和ALD法,其於低溫(即,低於450 °C )將氧化矽和氮氧化矽膜澱積於基板上且同時維持良好 漸近覆蓋性質。本發明之方法中,金屬矽有機先質和臭氧 倂用。本發明之澱積法可用以澱積高k和低k介電物。 欲塗覆的基板可以是具金屬或親水表面且於所用加工 溫度安定的任何材料。嫻於此技術者能夠不費力地辨別出 適當材料。適當基板包括矽、陶瓷、金屬、塑膠、玻璃和 有機聚合物。較佳基板包括矽、鎢和鋁。此基板可經事先 -8 - (5) (5)200422424 處理以賦予、去除及標準化化學品補充和/或基板表面性 質。基板之選擇視特定應用而定。 矽有機先質包括會揮發的任何分子,其結構中包含一 或多個砂原子和一或多個有機離去基或配位基(其可藉含 有反應性氧的化合物(如:臭氧)和/或含有反應性氮的化 合物(如:氨)而與矽分離)。較佳情況中,矽有機先質僅 含括一或多個矽原子和可藉含有反應性氧的化合物和/或 含有反應性氮的化合物而與矽分離的一或多個離去基。更 佳情況中,矽有機先質可以是於室溫或接近室溫(如:與 室溫差距l〇〇°C爲佳或甚至與室溫差距50°c更佳)爲揮發 性液體者。嫻於此技術者能夠不費力地辨別出適當矽有機 先質。適當矽有機先質的較佳實例包括,但不限於,四甲 基二矽氧烷(TMDSO)、六甲基二矽氧烷(HMDSO)、六甲基 二矽氮烷(HDMSN)和肆(乙基甲基胺)化矽(TEMASi)、烷基 胺基矽烷、烷基胺基二矽烷、烷基矽烷、烷氧基矽烷、烷 基矽醇和烷氧基矽醇。一個實施例中,矽先質是胺基矽烷 或矽烷基胺化物。這些化合物含有S i -N鍵,此鍵極不穩 定且容易於低溫與臭氧反應。先質氣流速率可由1 sccm至 lOOOsccm。先質氣體流率以10至5 00sccm爲佳。 相較於使用慣用氧化劑(如:水(H20)或氧氣(〇2)),臭 氧氣體有助於使矽有機先質於較低溫度之氧化反應。先質 與臭氧之氧化反應於低於約45 0°C (低至約200 °C )的溫度 得到良好結果。此溫度範圍以300t至40(TC爲佳。使用 臭氧代替水的其他優點包括去除羥基鍵結和羥基鍵結造成 -9 - (6) (6)200422424 之膜中之固定/捕集電荷和較少碳的情況。一個較佳實施 例中僅使用臭氧。另一較佳實施例中,臭氧以與氧之摻合 物使用。臭氧氣體流率範圍由1 0至2000sccm。較佳情況 中,臭氧氣體流率由100至2000sccm。較佳情況中,引 至澱積區中的臭氧濃度由10至400克/立方米,150至 3 00克/立方米更佳。至於特定實例,使用TEMASi和臭 氧,於400°C、5托耳,澱積具極佳漸近覆蓋和高縱橫比 溝槽及均勻度的3102膜。先質氣流約30sccm,臭氧濃度 是25 0克/立方米。 所欲膜是氮氧化物時,額外使用氮來源。此氮來源可 以是可揮發且其結構中含有反應性氮的任何化合物。適當 氮來源包括,但不限於,原子態氮、氮氣、氨、聯胺、院 基聯胺、烷基胺之類。以氨爲佳。此氮來源氣體流入澱積 槽的流率範圍由10至2000sccm。氮來源氣體流率以100 至2000sccm爲佳。 許多實施例中,稀釋氣體與一或多種反應物氣體(如 :先質、臭氧、氮來源)倂用以改善均勻度。稀釋氣體可 以是任何非反應性氣體。適當稀釋氣體包括氮、氦、氣、 氬、氣氣。就成本考量,較佳者是氮氣和氬氣。稀釋氣體 流率通常由lsccm至lOOOsccm。 一些CVD實施例和每一個ALD實施例中,藉滌氣步 驟,將一或多種反應物氣體引至澱積槽中。此滌氣可藉低 壓或真空幫浦實施。或者,滌氣的實施方式可以是將惰性 滌氣氣體引至澱積槽中。適當櫞氣氣體包括氮、氦、氣、 -10- (7) 2004224 24 氬、氙氣。或者可以倂用抽取和滌氣氣體。 所有情況中,前述氣體流率視槽尺寸和抽取 壓力必須在要求範圍內。所須加工壓力視澱積法 基本上在1毫托耳至760托耳範圍內,以0.5-7 佳。 本發明的一個特點中,CVD法用以使氧化 於基板上,其包含至少一個循環包含下列步驟: 機先質引至有基板存在的澱積區中;和(Π)將臭 積區中。本發明的此特點中,步驟可同時或連續 質和臭氧反應,在基板上形成氧化矽層。澱積區 於0.5至20托耳且溫度低於400°C爲佳。 此澱積法可以下列式表示:
Si先質 + 〇3 — Si02 + 副產物 例如,此澱積法可以一或多個下列式說明: Si(NR1R2)4 + 〇3 — Si02+ 副產物
Si(NR1R2)4-wLw + 〇3 -> Si02+ 副產物 其中R1和R2分別選自氫、C】-C6烷基、C5-、鹵素和經取代的烷基和環狀烷基,w等於1、 ,L選自氫或鹵素。或者,澱積法可以一或多個 明:
Si2(NR】R2)6 + 03 — Si02 + 副產物
Si2(NR]R )6-zLz + 〇3 Si〇2 + 副產物 其中R1和R2分別選自氫、(^-(:6烷基、C5-、鹵素和經取代的烷基和環狀烷基,z等於1、2 力而定, 而定,但 .〇托耳爲 矽層澱積 (i)將矽有 氧引至澱 進行。先 壓力維持 (1) (2) (3) C 6環院基 2、3 或 4 下列式說 (4) (5) C 6環烷基 、3、 4、 -11 - (8) (8)200422424 5或6,L選自氫或鹵素。 本發明的另一特點中,CVD法用以使氮氧化矽層澱 積於基板上,其包含至少一個循環包含下列步驟:(i)將矽 有機先質引至有基板存在的澱積區中;(ii)將臭氧引至澱 積區中;和(iii)將氮來源引至澱積區中。同樣地,這些步 驟可同時或連續進行。先質、臭氧和氮來源反應,在基板 上形成氮氧化矽層。澱積區壓力維持於0.5至20托耳且 溫度低於400°C爲佳。 此澱積法可以下列式表示:
Si先質+氮來源+ 03— SiOxNy +副產物 (6) 例如,此澱積法可以一或多個下列式說明:
SiCNR1!^2、十NH3 + Ο 3 — S i Q xNy + 副產物 (7) SKNRWh-wLw + NHs + Ch-^ SiOxNy +副產物 (8) 其中R1和R2分別選自氫、烷基、C5-C6環烷基 、鹵素和經取代的烷基和環狀烷基,w等於1、2、3或4 ,L選自氫或鹵素。或者,澱積法可以一或多個下列式說 明: S i2 (NR 1 R2) 6+ N Η3 + Ο 3 — S i Ο XNy + 副產物 (9)
SiHNI^RyrzLz + NHs + C^— SiOxNy + 副產物 (10) 其中R1和R2分別選自氫、C^-CU烷基、C5-C6環垸基 、鹵素和經取代的烷基和環狀烷基,z等於1、2、3、4、 5或6,L選自氫或鹵素。臭氧和氮來源氣體可以同時或 分別引入。臭氧和氮來源氣體以混合物形式引入爲佳。 於低壓低熱CVD法中澱積膜的前述方法述於附圖1 200422424 Ο) 。附圖1中,矽晶圓100置於澱積槽101中。澱積槽101 中,晶圓100以加熱器102,加熱至澱積溫度。此實例、中, 藉由將惰性稀釋氣流1 03引至槽1 0 1中而建立加工壓力。 之後,使用半導體和薄膜工業中慣用的氣體輸送法,矽有 機先質104和臭氧氧化劑105(和NH3 106,欲澱積SiOxNy 時)氣流引至槽中。經過獲致目標膜厚度所須的適當時間 之後,中止矽先質和氧化劑/ NH3氣流,調整稀釋用惰性 氣流,以滌除槽中的殘留反應物。經適當滌氣時間之後, 晶圓離開加工槽並回到匣。 本發明的另一特點中,ALD法將氧化矽層澱稹於基 板上,其包含至少一個循環包含下列步驟:(i)將矽有機先 質引至有基板位於其中的澱積區中Γ (Π)對澱積區滌氣; 和(iii)將臭氧引至澱.積區中,以於基板上形成氧化矽層。 本發明的此特點中,步驟連續進行。此循環多澱積一層氧 化矽。可視達到所欲膜厚度所需地多次重覆此循環,只要 各循環之間經額外的澱積區滌氣處理即可。此方法的總反 應與前述式1 _5中所示者相同。但藉滌氣將反應分成數個 步驟,以確保單層生長。 本發明的另一特點中,CVD法將氮氧化矽層澱積於 基板上,其包含至少一個循環包含下列步驟:(i)將矽有機 先質引至有基板位於其中的澱積區中;(ii)對澱積區滌氣 •,和(iii)將臭氧和氮來源引至澱積區中。這些步驟連續進 行。臭氧和氮之引入可分別或同時以任何順序進行,並可 視情況地對澱積槽滌氣的步驟區隔。此循環多澱積一層氮 -13- (10) (10)200422424 氧化矽。可視達到所欲膜厚度所需地多次重覆此循環,只 要各循環之間經額外的澱積區滌氣處理即可。此方法的總 反應與則述式6 -1 0中所不者相同。但藉條氣將反應分成 數個步驟,以確保單層生長。 ALD有數個優於傳統CVD之處。第一,ALD可於更 低溫度進行。第二,ALD可製得超薄平整膜。事實上, ALD可以將膜厚度控制至原子規模並可用於”微細設計的” 複合薄膜。第三,ALD在非平面基板上提供薄膜的平整 覆蓋。但ALD的加工時間通常比較長,這是因爲每次循 環所須脈衝數較多之故。 藉ALD澱積膜的前述方法依順序示於附圖2的步驟 序ν'列中。附圖2中,:排徐槽中的氣體之後,晶圓‘200移至 澱積區201中並置於晶圓加熱器202上,晶圓藉此加熱器 加熱至澱積溫度。澱積溫度可由1 00 °C至5 50 °C,但以低 於約450°C爲佳,在3 00°C至400°C範圍內更佳。稀釋氣 體203以穩定流率進入澱積區201。此氣體是Ar、He、 Ne、Xe、N2或其他非反應性氣體。壓力建立於加工壓力 。加工壓力可由1〇〇毫托耳至10托耳,以200毫托耳至 1 ·5托耳爲佳。達穩定壓力條件之後,經過適當時間以將 任何殘留氣體自晶圓200表面移開之後,開始ALD澱積 。首先,開啓適當閥,矽有機先質蒸汽流204脈衝引至澱 積區。蒸汽流率可由1至lOOOsccm,以5至lOOsccm爲 佳。蒸汽可經非反應性氣體(如:Ar、N2、He、Ne或Xe) 稀釋。稀釋氣體流率可由l〇〇sccm至l〇〇〇SCCm。先質脈 (11) (11)2004224 24 衝時間可由0 · 0 1秒至1 0秒並以在〇 · 〇 5至2秒範圍內爲 佳。先質脈衝終了時,电止先質蒸汽流入澱積區201。之 後’至澱積區的蒸汽輸入管線以非反應性氣體2 0 3滌氣達 適當時間。此滌氣期間內,非反應性氣體203經由蒸汽輸 入管線進入槽。此非反應性氣體可以是Ar、He、Ne、Xe 或N2。滌氣氣體流率以與在先質脈衝步驟期間內通過管 線的總氣體流率相同爲佳。蒸汽滌氣時間可由0· 1秒至1 0 秒,但以0.5秒至5秒爲佳。活化適當閥(未示),蒸汽滌 氣步驟終了時,反應物氣流進入澱積區201。反應物氣體 是臭氧205(用以澱積Si02時)及臭氧205和氨206(用以澱 積SiOxNy時)。反應物氣體總流率可由100至2000Sccm, 以在200.至lOOOsccm範圍內爲佳。臭氧濃度範圍是150 至300克/立方米,以約200克/立方米爲佳。用以澱積 Si OxNy,氧化劑和氨流比可由0.2至10,此視所欲組成和 溫度而定。反應物脈衝時間可由0.1秒至10秒,但以0.5 秒至3秒爲佳。反應物脈衝完全之後,至澱積區20 1的反 應物輸送管線以非反應性氣流203滌氣。此非反應性氣體 可以是He、Ne、Ar、Xe或N2。滌氣流率以氣氣體流率 以與在反應物脈衝步驟期間內通過反應物輸送管線的總氣 體流率相同爲佳。反應物脈衝之後,多次重覆下一個先質 脈衝和序列,直到獲致所欲膜厚度爲止。 可以在一或多個使用滌氣氣體的滌氣步驟期間內含括 抽取地修飾前述序列。也可以在一或多個滌氣步驟中以抽 取代替氣體滌氣地修飾前述序列。 -15- (12) (12)200422424 本方法可用於經摻雜和未經摻雜的。(^和Si〇xNyB 成。本方法於積體電路(ic)製造方面的典型應用包括,但 不限於’金屬前介電物(PMD)、淺溝槽隔絕(STI)、隔離器 、金屬矽酸鹽閘極介電物和低k介電物。 已經以專利法要求的細節和特定要求詳細描述本#明 ,Letters Patent欲聲明和欲保護者列於所附申請專利範 圍中。 【圖式簡單說明】 附圖1所示者是本發明的CVD法。 附圖2所示者是本發明的ALD法。 主要元件對照表 100 矽晶圓 101 澱積槽 1 02 加熱器 1 03 稀釋氣體 1 〇4 矽有機先質 105 臭氧 1 06 氮來源(nh3) 2〇〇 晶圓 201 澱積區 202 晶圓加熱器 203 稀釋氣體 200422424 (13) 204 205 206 矽有機先質 臭氧 氮來源(nh3)

Claims (1)

  1. 200422424 (1) 拾、申請專利範圍 1. 一種將氧化矽澱積於基板上之方法,其步驟包含將 矽有機先質和臭氧引至有基板位於其中的澱積區中。 2. 如申請專利範圍第1項之方法,其中澱積藉化學蒸 鍍法進行,並包含至少一個循環包含下列步驟: (i) 將矽有機先質引至有基板位於其中的澱積區中; 和 (ii) 將臭氧引至澱積區中。 3 .如申請專利範圍第2項之方法,其中步驟同時進行 〇 4.如申請專利範圍第2項之方法,其中步驟連續進行 〇 5 .如申請專利範圍第1項之方法,其中澱積藉原子層 澱積法進行,並包含至少一個循環包含下列連續步驟: (i) 將矽有機先質引至有基板位於其中的源積區中; (ii) 對澱積區滌氣;和 (iii) 將臭氧引至澱積區中。 6·如申請專利範圍第1項之方法,其中矽有機先質選 自四甲基二矽氧烷(TMDSO)、六甲基二矽氧烷(HMDSO)、 六甲基二矽氮烷(HDMSN)和肆(乙基甲基胺)化矽(TEMASi) 、烷基矽烷、烷基胺基矽烷、烷基胺基二矽烷、烷氧基矽 烷、烷基矽醇和烷氧基矽醇。 7.如申請專利範圍第1項之方法,其中矽有機先質具 式 Si(NR】R2)4-wLw, -18- (2) (2)2004224 24 其中R1和R2分別選自氫、C^c6烷基、c5_c6環烷基 、_素和經取代的院基和環,狀院基,w等於1、2、3或;4 ,L選自氫或鹵素。 8 ·如申請專利範圍第1項之方法,其中矽有機先質具 式 SidNI^R2)"!^, 其中R】和R2分別選自氫、C ! - C 6烷基、c 5 - C 6環烷基 、鹵素和經取代的烷基和環狀烷基,z等於]、2、3、4、 5或6,L選自氣或鹵素。 9 ·如申請專利範圍第1項之方法,其中激積區壓力維 持在1毫托耳至760托耳範圍內。 1 〇 ·如申請專利範圍第1項之方法,其中激積法實施 溫度介於200°c至400°C之間。 11·如申請專利範圍第1項之方法,其中臭氧引至澱 積區,使得臭氧濃度在1 0至400克/立方米範圍內。 1 2 ·如申請專利範圍第1項之方法,其中基板是矽基 板、陶瓷、金屬、塑膠、玻璃和有機聚合物。 1 3 . —種用以將氮氧化矽澱積於基板上的方法,其步 驟包含將矽有機先質、臭氧和氮來源引至有基板存在的澱 積區中。 14·如申請專利範圍第13項之方法,其中澱積藉化學 蒸鍍法進行,其包含至少一個循環包含下列步驟: (i) 將矽有機先質引至有基板位於其中的澱積區中; (ii) 將臭氧引至澱積區中;和 (iii) 將氮來源弓丨至澱積區中。 -19 - (3) (3)2004224 24 1 5 .如申J靑專利範圍第1 4項之方法,其中步驟同時進 行。 1 6 .如申請專利範圍第1 4項之方法’其中步驟連續進 行。 1 7 .如申請專利範圍第1 3項之方法,其中澱積藉原子 層澱積法進行,並包含至少一個循環包含下列連續步驟: (i) 將矽有機先質引至有基板位於其中的澱積區中; (ii) 對澱積區滌氣;和 (iii) 將臭氧和氮來源引至澱積區中。 1 8 .如申請專利範圍第1 7項之方法,其中臭氧和氮來 源分別以任何順序引入。 19. 如申請專利範圍第17項之方法,其中臭氧和氮來 源同時引入。 20. 如申請專利範圍第13項之方法,其中矽有機先質 選自四甲基二矽氧烷(TMDSO)、六甲基二矽氧烷(HMDSO) 、六甲基二矽氮烷(HDMSN)和肆(乙基甲基胺)化矽 (TEMASi)、烷基矽烷、烷基胺基矽烷、烷基胺基二矽烷 、烷氧基矽烷、烷基矽醇和烷氧基矽醇。 2 1 .如申請專利範圍第1 3項之方法,其中矽有機先質 具式 , 其中R1和R2分別選自氫、C】-C6烷基、C5-C6環烷基 、鹵素和經取代的烷基和環狀烷基,w等於1、2、3或4 ,L選自氫或鹵素。 2 2 ·如申請專利範圍第1 3項之方法,其中矽有機先質 -20- (4) (4)200422424 具式 , 其中R1和R2分別選自氫、烷基、C5-C6環烷基 、鹵素和經取代的烷基和環狀烷基,z等於1、2、3、4、 5或6,L選自氫或鹵素。 23.如申請專利範圍第13項之方法,其中氮來源選自 原子態氮、氮氣、氨、聯胺、烷基聯胺和烷基胺。 24·如申請專利範圍第13項之方法,其中澱積區維持 於1毫托耳至760托耳壓力範圍內。 2 5 .如申請專利範圍第1 3項之方法,其中澱積於低於 400°C的溫度實施。 2 6 ·如申g靑專利範圍第1 3項之方法,其中引至澱積區 中的臭氧使得臭氧濃度在10至400克/立方米範圍內。 2 7 ·如申請專利範圍第1 3項之方法,其中基板是砂基 板、陶瓷、金屬、塑膠、玻璃和有機聚合物。 -21 -
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US20060178019A1 (en) 2006-08-10
KR20050069986A (ko) 2005-07-05
CN1868041A (zh) 2006-11-22
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