TW507015B - In-situ, preclean of wafers prior to a chemical vapor deposition titanium deposition step - Google Patents
In-situ, preclean of wafers prior to a chemical vapor deposition titanium deposition step Download PDFInfo
- Publication number
- TW507015B TW507015B TW87118298A TW87118298A TW507015B TW 507015 B TW507015 B TW 507015B TW 87118298 A TW87118298 A TW 87118298A TW 87118298 A TW87118298 A TW 87118298A TW 507015 B TW507015 B TW 507015B
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- Taiwan
- Prior art keywords
- gas
- deposition
- titanium
- substrate
- chemical vapor
- Prior art date
Links
- 238000000151 deposition Methods 0.000 title claims abstract description 131
- 230000008021 deposition Effects 0.000 title claims abstract description 118
- 239000010936 titanium Substances 0.000 title claims abstract description 109
- 229910052719 titanium Inorganic materials 0.000 title claims abstract description 108
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 title claims abstract description 106
- 238000005229 chemical vapour deposition Methods 0.000 title claims abstract description 48
- 235000012431 wafers Nutrition 0.000 title description 79
- 238000011065 in-situ storage Methods 0.000 title 1
- 239000007789 gas Substances 0.000 claims abstract description 174
- 238000000034 method Methods 0.000 claims abstract description 118
- 238000012545 processing Methods 0.000 claims abstract description 115
- 230000008569 process Effects 0.000 claims abstract description 96
- 239000000758 substrate Substances 0.000 claims abstract description 65
- 239000001257 hydrogen Substances 0.000 claims abstract description 10
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 10
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000011261 inert gas Substances 0.000 claims abstract description 8
- 239000010408 film Substances 0.000 claims description 31
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 claims description 21
- 230000002079 cooperative effect Effects 0.000 claims description 20
- 238000006243 chemical reaction Methods 0.000 claims description 16
- 239000010409 thin film Substances 0.000 claims description 15
- NRTOMJZYCJJWKI-UHFFFAOYSA-N Titanium nitride Chemical compound [Ti]#N NRTOMJZYCJJWKI-UHFFFAOYSA-N 0.000 claims description 13
- 238000010438 heat treatment Methods 0.000 claims description 12
- 238000004519 manufacturing process Methods 0.000 claims description 12
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 10
- 239000012495 reaction gas Substances 0.000 claims description 7
- 229910052814 silicon oxide Inorganic materials 0.000 claims description 6
- 238000011049 filling Methods 0.000 claims description 5
- 238000002203 pretreatment Methods 0.000 claims description 3
- 230000002441 reversible effect Effects 0.000 claims description 3
- 229910021341 titanium silicide Inorganic materials 0.000 claims description 3
- 239000011521 glass Substances 0.000 claims description 2
- 238000000427 thin-film deposition Methods 0.000 claims description 2
- 239000000376 reactant Substances 0.000 claims 3
- 239000005380 borophosphosilicate glass Substances 0.000 claims 2
- PCTMTFRHKVHKIS-BMFZQQSSSA-N (1s,3r,4e,6e,8e,10e,12e,14e,16e,18s,19r,20r,21s,25r,27r,30r,31r,33s,35r,37s,38r)-3-[(2r,3s,4s,5s,6r)-4-amino-3,5-dihydroxy-6-methyloxan-2-yl]oxy-19,25,27,30,31,33,35,37-octahydroxy-18,20,21-trimethyl-23-oxo-22,39-dioxabicyclo[33.3.1]nonatriaconta-4,6,8,10 Chemical compound C1C=C2C[C@@H](OS(O)(=O)=O)CC[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@H]([C@H](C)CCCC(C)C)[C@@]1(C)CC2.O[C@H]1[C@@H](N)[C@H](O)[C@@H](C)O[C@H]1O[C@H]1/C=C/C=C/C=C/C=C/C=C/C=C/C=C/[C@H](C)[C@@H](O)[C@@H](C)[C@H](C)OC(=O)C[C@H](O)C[C@H](O)CC[C@@H](O)[C@H](O)C[C@H](O)C[C@](O)(C[C@H](O)[C@H]2C(O)=O)O[C@H]2C1 PCTMTFRHKVHKIS-BMFZQQSSSA-N 0.000 claims 1
- 229910003074 TiCl4 Inorganic materials 0.000 claims 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims 1
- 229940104869 fluorosilicate Drugs 0.000 claims 1
- 235000012054 meals Nutrition 0.000 claims 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims 1
- 238000005137 deposition process Methods 0.000 abstract description 14
- 239000003989 dielectric material Substances 0.000 abstract description 3
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- 238000004140 cleaning Methods 0.000 description 25
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- 230000001965 increasing effect Effects 0.000 description 8
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 7
- 239000012159 carrier gas Substances 0.000 description 7
- 230000001276 controlling effect Effects 0.000 description 7
- 238000001514 detection method Methods 0.000 description 7
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- 239000010703 silicon Substances 0.000 description 7
- 229910052782 aluminium Inorganic materials 0.000 description 6
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 6
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- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
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- 150000003608 titanium Chemical class 0.000 description 3
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- FFBHFFJDDLITSX-UHFFFAOYSA-N benzyl N-[2-hydroxy-4-(3-oxomorpholin-4-yl)phenyl]carbamate Chemical compound OC1=C(NC(=O)OCC2=CC=CC=C2)C=CC(=C1)N1CCOCC1=O FFBHFFJDDLITSX-UHFFFAOYSA-N 0.000 description 2
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- 239000010931 gold Substances 0.000 description 1
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- -1 hafnium nitride Chemical class 0.000 description 1
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- WUAPFZMCVAUBPE-UHFFFAOYSA-N rhenium atom Chemical compound [Re] WUAPFZMCVAUBPE-UHFFFAOYSA-N 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
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- LIVNPJMFVYWSIS-UHFFFAOYSA-N silicon monoxide Chemical group [Si-]#[O+] LIVNPJMFVYWSIS-UHFFFAOYSA-N 0.000 description 1
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Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
- H01L21/70—Manufacture or treatment of devices consisting of a plurality of solid state components formed in or on a common substrate or of parts thereof; Manufacture of integrated circuit devices or of parts thereof
- H01L21/71—Manufacture of specific parts of devices defined in group H01L21/70
- H01L21/768—Applying interconnections to be used for carrying current between separate components within a device comprising conductors and dielectrics
- H01L21/76838—Applying interconnections to be used for carrying current between separate components within a device comprising conductors and dielectrics characterised by the formation and the after-treatment of the conductors
- H01L21/76841—Barrier, adhesion or liner layers
- H01L21/76853—Barrier, adhesion or liner layers characterized by particular after-treatment steps
- H01L21/76855—After-treatment introducing at least one additional element into the layer
- H01L21/76856—After-treatment introducing at least one additional element into the layer by treatment in plasmas or gaseous environments, e.g. nitriding a refractory metal liner
-
- C—CHEMISTRY; METALLURGY
- C23—COATING 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
- C23C—COATING 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
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/02—Pretreatment of the material to be coated
- C23C16/0227—Pretreatment of the material to be coated by cleaning or etching
- C23C16/0245—Pretreatment of the material to be coated by cleaning or etching by etching with a plasma
-
- C—CHEMISTRY; METALLURGY
- C23—COATING 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
- C23C—COATING 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
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/06—Chemical 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 metallic material
- C23C16/08—Chemical 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 metallic material from metal halides
- C23C16/14—Deposition of only one other metal element
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
- H01L21/02—Manufacture or treatment of semiconductor devices or of parts thereof
- H01L21/04—Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer
- H01L21/18—Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer the devices having semiconductor bodies comprising elements of Group IV of the Periodic Table or AIIIBV compounds with or without impurities, e.g. doping materials
- H01L21/28—Manufacture of electrodes on semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/268
- H01L21/283—Deposition of conductive or insulating materials for electrodes conducting electric current
- H01L21/285—Deposition of conductive or insulating materials for electrodes conducting electric current from a gas or vapour, e.g. condensation
- H01L21/28506—Deposition of conductive or insulating materials for electrodes conducting electric current from a gas or vapour, e.g. condensation of conductive layers
- H01L21/28512—Deposition of conductive or insulating materials for electrodes conducting electric current from a gas or vapour, e.g. condensation of conductive layers on semiconductor bodies comprising elements of Group IV of the Periodic Table
- H01L21/28556—Deposition of conductive or insulating materials for electrodes conducting electric current from a gas or vapour, e.g. condensation of conductive layers on semiconductor bodies comprising elements of Group IV of the Periodic Table by chemical means, e.g. CVD, LPCVD, PECVD, laser CVD
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
- H01L21/70—Manufacture or treatment of devices consisting of a plurality of solid state components formed in or on a common substrate or of parts thereof; Manufacture of integrated circuit devices or of parts thereof
- H01L21/71—Manufacture of specific parts of devices defined in group H01L21/70
- H01L21/768—Applying interconnections to be used for carrying current between separate components within a device comprising conductors and dielectrics
- H01L21/76838—Applying interconnections to be used for carrying current between separate components within a device comprising conductors and dielectrics characterised by the formation and the after-treatment of the conductors
- H01L21/76841—Barrier, adhesion or liner layers
- H01L21/76843—Barrier, adhesion or liner layers formed in openings in a dielectric
-
- H—ELECTRICITY
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Abstract
Description
507015 A7 B7 五、發明説明() 經濟部中央標準局員工消費合作社印製 發明領域: 本發明係關係於一耐火金屬層之沉籍 曰又1儿積於一半導體基 板上。更明確地,本發明關於一改良化學氣相沉積方法及 設備’用以於接觸處沉積具有改良片電阻均均性及優良底 覆蓋之鈥層。本發明可以應用至各種鈦沉積製程,並特別 可應用以包含四氯化鈦(TiCl4)作為鈦來源之製程中。 發明背景: 於製造現代半導體裝置之主要步驟之一是形成各種 層,包含介電層及金屬層於半導體基板上。如同本技藝中 所知,這些層可以於這些方法藉由化學氣相沉積(CVD)或 物理氣相沉積(PVD)加以沉積。於傳統熱CVD製程中,反 應氣體係被供給至基板表面,其上發生熱感應化學反應, 以產生一想要之薄膜。於傳統電漿CVD製程中,一受控 制電漿係被形成,以分解及/或激勵反應種類以產生想要之 薄膜。一般而言,於熱及電漿製程中之反應速率可以藉由 控制以下之一或多種因素加以控制··溫度,壓力,電漿密 度,反應氣體流速,電力頻率,功率位準,室實體幾何及 其他因素。 於例示PVD系統中,於一面對靶之基板支持件被接 地,浮接,偏壓,加熱,冷卻或其組合之同時,一靶(一 予以沉積之材料板)係連接至一負電壓源(直流(DC)或射頻 (RF))。一氣體,例如氬氣係被典型地引入pvD系統中, 典型地被保持於幾毫托耳(mt〇rr)及約1 〇〇 mtorr之間之壓 第4頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公董) (請先閱讀背面之注意事項507015 A7 B7 V. Description of the invention () Printed by the Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economics Field of the Invention: The invention relates to a refractory metal layer, which is accumulated on a semiconductor substrate. More specifically, the present invention relates to an improved chemical vapor deposition method and equipment 'for depositing a layer having improved sheet resistance uniformity and excellent bottom coverage at the contact. The present invention can be applied to various titanium deposition processes, and is particularly applicable to processes containing titanium tetrachloride (TiCl4) as a titanium source. BACKGROUND OF THE INVENTION One of the main steps in manufacturing modern semiconductor devices is to form various layers including a dielectric layer and a metal layer on a semiconductor substrate. As is known in the art, these layers can be deposited in these methods by chemical vapor deposition (CVD) or physical vapor deposition (PVD). In a conventional thermal CVD process, a reaction gas system is supplied to the substrate surface, and a thermally induced chemical reaction occurs thereon to produce a desired thin film. In a conventional plasma CVD process, a controlled plasma system is formed to decompose and / or stimulate the reaction species to produce the desired film. Generally speaking, the reaction rate in the heat and plasma process can be controlled by controlling one or more of the following factors: temperature, pressure, plasma density, reaction gas flow rate, power frequency, power level, room physical geometry And other factors. In the illustrated PVD system, a target (a plate of material to be deposited) is connected to a negative voltage source while a substrate supporting member facing the target is grounded, floating, biased, heated, cooled, or a combination thereof. (Direct current (DC) or radio frequency (RF)). A gas, such as argon, is typically introduced into a pvD system, and is typically maintained at a pressure between a few millitorr (mtorr) and about 100 mtorr. Page 4 This paper's dimensions apply Chinese national standards ( CNS) A4 specification (210X297 public director) (Please read the notes on the back first
本頁) 訂 507015 A7 B7 經濟部中央標準局員工消費合作社印製 五、發明説明( 力,以提供一媒介,其中一發光放電可以被啟始及維持。 當發光放電開始時,正離子撞擊靶,以及,靶原子被動量 移轉所除去。這些靶原子隨後凝結成一薄膜於被定位於基 板支持件上之基板上。 自從半導體裝置於幾十年前被引入後,其幾何大小上 已經大大地減少。今日之晶圓製造廠係現行用以生產〇.5 微米甚至G.35微米特性大小之裝置,明日之製造廠將很快 地生產更小特性大小之裝置.因為裝置之特性大小變小及 積集密度増加時,以前並不被本產業所認為是問題之事件 •k:成重要,而需要加以考量。例如,具有高積集密度之裝 置具有高深寬比特性(例如對於0·35微米之特性大小裝置 、〆 或更大之木寬比)。(深寬比被定義為兩相鄰步階 之高至寬比例)。高深寬比特性,例如間隙需要能被適當 地填以很多應用中之沉積層。 用以製程這些高積集度裝之嚴格需求增加,及傳統基 板處理系統變成不能符合這些需求。另外,當裝置設計進 灯時,則需要更先進之能力,於基板處理系統中,以用以 沉積具有需要以實現這些裝置之特性之薄膜。例如,鈦之 使用增加應用於積體電路製造處理中。於使用於半導體裝 置中鈦具有很多之想要特性。鈦可以作為於例如金焊接 熱及一半導體間之一擴散阻障層,以防止一原子種類遷移 入下層中。同時,鈦也可以使用以作為改良於兩層,例 如於矽及鋁間之黏著性。再者,當與矽作為合金,使用 ' >成碎化鈥(TiSix)可以例如形成歐姆接觸。一種用以 广请先聞讀背命之注意事項本 1:This page) Order 507015 A7 B7 Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs. 5. Description of the invention (to provide a medium in which a luminous discharge can be initiated and maintained. When the luminous discharge starts, positive ions hit the target And, the passive atoms of the target atoms are removed. These target atoms are then condensed into a thin film on the substrate positioned on the substrate support. Since the semiconductor device was introduced decades ago, its geometric size has been greatly improved. Decrease. Today's wafer manufacturing plants are currently used to produce devices with characteristic sizes of 0.5 microns or even G.35 microns. Tomorrow's manufacturing plants will soon produce devices with smaller characteristic sizes. Because the characteristics of the devices become smaller And accumulation density increase, events that were not previously considered a problem by the industry • k: becomes important and needs to be considered. For example, devices with high accumulation density have high aspect ratio characteristics (for example, 0 · 35 Micron characteristic size device, 〆 or larger wood width ratio). (Aspect ratio is defined as the height-to-width ratio of two adjacent steps). High aspect ratio characteristics For example, the gap needs to be able to be properly filled with deposited layers in many applications. The stringent requirements for manufacturing these high-integration packages have increased, and traditional substrate processing systems have become unable to meet these requirements. In addition, when the device is designed into a lamp, More advanced capabilities are needed in substrate processing systems to deposit thin films with the characteristics needed to achieve these devices. For example, the increased use of titanium is used in integrated circuit manufacturing processes. Titanium used in semiconductor devices Has many desirable properties. Titanium can be used as a diffusion barrier between, for example, gold welding heat and a semiconductor to prevent an atomic species from migrating into the lower layer. At the same time, titanium can also be used as an improvement in two layers, such as Adhesiveness between silicon and aluminum. Furthermore, when used as an alloy with silicon, the use of '> fragmentation' (TiSix) can, for example, form an ohmic contact. A precautionary note for reading your fate :
發明説明() :成此-鈥膜之常用類型之沉積系統係鈥機鍍(PVD)系 然而’此等錢鍵系統經常是不適用以形成具有高處理 k 4求之裝置。明確地說,濺鍍可能楣 j此钿壞於此等裝置 ^先前沉積之諸層及結構,而造成效能及/或良率問題。 欽濺鍍系統可能不能沉積均句保角層於高深寬比間 繁中’因為發生於濺鍍中之陰影效應之故。 相反於濺鍍系統,一電漿加強化學氣相沉積(PECVD) 系統可以更適以形成一鈦薄膜於具有高深寬比間隙之基 板上。如所知的,一離子及氣體分子混合之電漿可以藉由 施加能量,例如射頻(RF)能量至沉積室中之處理氣體,於 例如室壓,室内溫度,RF㈣及其他等之適當條件下, 而加以形《。電漿到達一臨限密度,以形成一被稱為發光 放電(經常被稱為"撞擊”或”激勵”電漿)之自侷限狀況。該 RF能量提升於處理氣體中之分子之能量狀況並由分子形 成離子種類《受激勵分子及離子種類典型地係較處理氣體 活躍,因此,更能形成想要薄膜。有利地,電漿同時加強 了於整合基板表面之反應種類之遷移率,當鈦薄膜形成及 造成形成良好填補間隙能力之薄膜。 一已知沉積鈦薄膜之CVD方法包含由一處理氣體形 成一電漿,於標準PECVD處理中,該氣體包含TiCl4氣體 源及氫氣還原劑。此TiCl4/H2 PECVD處理造成具有良好 通孔填補,均勻性及接觸特性之鈦薄膜沉積,使得薄膜可 以用以製造很多不同商用積體電路。儘管這些處理已經合 適於某些製程,但對於由TiCl4及H2沉積而得之鈦薄膜之Description of the Invention: A commonly used type of film deposition system is a machine-plating (PVD) system. However, these money-key systems are often not suitable for forming devices with high processing requirements. Specifically, sputter plating may be worse than these devices ^ previously deposited layers and structures, resulting in performance and / or yield issues. The Qin sputtering system may not be able to deposit uniform conformal layers between high-aspect-ratio ratios because of the shadow effect that occurs during sputtering. In contrast to a sputtering system, a plasma enhanced chemical vapor deposition (PECVD) system can be more suitable for forming a titanium film on a substrate having a high aspect ratio gap. As is known, a plasma of a mixture of ions and gas molecules can be applied to the processing gas in the deposition chamber by applying energy, such as radio frequency (RF) energy, under appropriate conditions such as chamber pressure, room temperature, RF, and others. , And be shaped. The plasma reaches a threshold density to form a self-limiting condition called a glow discharge (often referred to as " impact " or " excitation " plasma). This RF energy is enhanced by the energy condition of the molecules in the processing gas. Ion species are formed by molecules. Excited molecules and ion species are typically more active than the process gas, so they can form the desired film. Advantageously, the plasma also enhances the mobility of the reaction species on the surface of the integrated substrate. Titanium film formation and formation of a film with good gap-filling ability. A known CVD method for depositing titanium films includes forming a plasma from a process gas. In a standard PECVD process, the gas includes a TiCl4 gas source and a hydrogen reducing agent. The TiCl4 / H2 PECVD process results in the deposition of titanium thin films with good through-hole filling, uniformity and contact characteristics, allowing the films to be used to fabricate many different commercial integrated circuits. Although these processes are already suitable for certain processes, for TiCl4 and H2 deposition of titanium film
/ U1 J / U1 J A7 B7 五、發明説明( 通孔填補’均勻性及接觸電阻之改良仍持續地進行。 炎星且勺及椒見/ U1 J / U1 J A7 B7 V. Explanation of the invention (Improvement of uniformity and contact resistance of through-hole filling ’is still ongoing.
本發明提供一種用於鈦薄膜之改良CM 用以形成該鈦薄膜之改$ #借彷媸+ 積處理及 艮&#。依據本發明之方法,㈣ 用以沉積鈦薄膜於基板上之多 製程。典型地,本發明 个知< 鈦層係 >儿積於經由介 如氧化秒薄膜之接觸區域中 切’免 f上,但其可以同時被用於其一積應用 步聲jlT步驟’儿積處理《弟一步驟包含一電漿預處理 卞二、Γ具有含氫氣體之預處理氣體及一惰性氣體係 Μ入基板處理室之沉積區域中。於第一沉積階段中,一# 經濟部中央標準局員工消費合作社印製 漿係由預處理氣體形成並被保持至少5秒,以_殘留: 基板之接觸區域之介電材料,並於沉積鈦層之前,清2接 觸區域。再者,於第一階段後,於第二沉積階段時,一含 鈦源及一還原劑係被引入沉積區域及形成於第一階段= 之電槳係被維持,以沉積鈦層於基板上。於較佳實:例 中,包含於第一沉積階段之處理氣體中之預處理氣體及還 原劑係相同之氫流體。同時,於另一實施例中,電漿預處 理步騾堅持於約5至60秒之間。 或者,鈦層可以被鈍化,以避免來自例如氧及/或碳 < 2氣有關雜質之污染。鈍化係藉由提供—或兩個以下之 步驟加以完成(1)氮之流通及7或(2)衝撞一氮電漿於接近鈦 第7頁 本紙張级朗中關家標準(CNS ) A#!# ( 21GX297公釐) 丄 經濟部中央標隼局員工消費合作社印製 五、發明説明( 二I:積:域中。將&層曝露至氮形成-薄層之氮化鈥, 入°氮化鈇層純化鈥層,阻擋了雜質被吸收 因此鈦層具有穩定特性,例如表面電阻並提 供了一 i杳泡士主^ 木· 足表面,用於隨後氮化鈦阻障層沉積。再者, Γ皮移動至另—處理室,作為隨後處理時,藉由提供-穩 疋,純化欽層,晶圓可以曝露至大氣,而不會有鈇層污染 (危險。結果’本發明之室可以被用作為單—鈦薄膜沉積 室。 依據本發明之另一實施例,鈦源之流動係開始於第二 况積階段前至少6至8秒。然而,反相於引入該流量至該 1中,該流量係被分流至預抽管道。於此方式中,於沉積 步驟 < 可’欽源之流量係被穩定,以於晶圓處理中,進/ 步改良/儿積於多數晶圓上之鈇薄膜間之薄膜均勻性。 本發明之這些及其他實施例,以及,其優點及特性將 藉由參考以下之文章及附圖加以詳細說明。 圖式簡軍銳明: 第1A圖為依據本發明之簡化電漿加強化學氣相沉積系統 之實施例之剖面圖。 罘1B圖為依據本發明之一實施例之示於第1A圖中之陶資 托架3 6之簡化剖面圖。 第1C圖為依據本發明之一實施例之示於第1A圖中之沉積 室3 0之簡化剖面圖。 弟1D圖為於使用者及一處理機間’可以控制本發明之沉 第8頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210X:W公釐) 請 先 閲 % 之 注 項The present invention provides an improved CM for a titanium thin film to form a modified titanium thin film. According to the method of the present invention, there are multiple processes for depositing a titanium film on a substrate. Typically, the present invention < titanium layer system > is deposited on the contact area through the contact region via an oxide second film, but it can be used at the same time for its one-step application step jlT step. The first step includes a plasma pretreatment. Second, a pretreatment gas with a hydrogen-containing gas and an inert gas system M are deposited into the deposition area of the substrate processing chamber. During the first deposition stage, # 1 The Printing Cooperative Department of the Consumer Standards Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs is formed of pretreatment gas and is maintained for at least 5 seconds to _residue: the dielectric material of the contact area of the substrate, and deposit titanium Before layering, clear 2 contact areas. Furthermore, after the first stage, during the second deposition stage, a titanium-containing source and a reducing agent system were introduced into the deposition area and the electric paddle system formed in the first stage = was maintained to deposit a titanium layer on the substrate . In a better case: the pretreatment gas and the reducing agent contained in the processing gas in the first deposition stage are the same hydrogen fluid. Meanwhile, in another embodiment, the plasma pre-processing step is maintained for about 5 to 60 seconds. Alternatively, the titanium layer may be passivated to avoid contamination from related impurities such as oxygen and / or carbon < 2 gas. Passivation is accomplished by providing—or two or less of the following steps: (1) nitrogen flow and 7 or (2) impacting a nitrogen plasma near titanium. Page 7 of this paper-grade Langzhongguanjia Standard (CNS) A #! # (21GX297 mm) Printed by the Consumer Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs. 5. Description of the Invention (II: Product: Domain. Exposing the & layer to nitrogen formation-thin layer of nitridation), nitrogen The chemical layer is purified, which prevents impurities from being absorbed, so the titanium layer has stable characteristics, such as surface resistance and provides a surface of the glass foot for subsequent deposition of the titanium nitride barrier layer. The Γ skin is moved to another processing chamber. As a subsequent processing, by providing -stable, purified layer, the wafer can be exposed to the atmosphere without contamination of the layer (danger. As a result, the room of the present invention can Used as a single-titanium thin film deposition chamber. According to another embodiment of the present invention, the flow of the titanium source begins at least 6 to 8 seconds before the second phase. However, the inversion is introduced into the flow into the 1 This flow is diverted to the pre-pumping pipeline. In this way, in the deposition step < The flow rate of Qinyuan is stabilized to further improve / uniform the thin film uniformity between the thin films deposited on most wafers during wafer processing. These and other embodiments of the present invention, and Its advantages and characteristics will be explained in detail by referring to the following articles and drawings. Figure Jian Jian Rui Ming: Figure 1A is a sectional view of an embodiment of a simplified plasma enhanced chemical vapor deposition system according to the present invention. 罘 1B The figure is a simplified cross-sectional view of a ceramic holder 36 shown in Fig. 1A according to an embodiment of the present invention. Fig. 1C is a deposition chamber 3 shown in Fig. 1A according to an embodiment of the present invention. The simplified cross-sectional view of 0. The 1D drawing is between the user and a processing machine, which can control the depth of the present invention. Page 8 This paper size is applicable to China National Standard (CNS) A4 specification (210X: W mm) Please read first % Note
訂 •"f 507015 A7 B7 經濟部中央標準局員工消費合作社印裝 五、發明説明() 積系統之界面。 第1E圖示出流過晶圓芬浪;4南4 # 、 9 口及依據本發明之一實施例之排氣系 統之流之簡化部份剖面圖。 第1F圖為示出依據本於明夕 ^ +心明足一貫施例之系統控制軟體之 架構控制結構方塊圖。 第2A圖為一例示接觸結構之簡化剖面圖,其中,依據本 發明沉積之鈦層可以加以使用。 第2 B圖為於弟2 A圈夕3立總沾4·座丄 圖 < 接觸結構中之缺陷形成之剖面圖。 弟3圖為依據本發明乏勒r接鲁、> 、rci . _ Λ β又权佳實施例之用以沉積一鈦層之處 理程序流程圖。 第4圖為-圖,其示出於室清洗步驟中,量測反射功率為 時間及沉積長度之函數。 第5Α及5Β圖為薄、膜厚度量測,例示本發明之實驗結果。 圖號#照說明: 4 選擇遠端電漿系統 5 低頻RF電源供應 6 熱交換系統 10 化學氣相沉積系統 22 内藏電極 26 陶瓷支持柄 28 水冷铭軸 30 反應室 32 托架 33 加熱元件 36 晶圓 38 拾起銷 40 喷氣頭 42 路徑 44 中央氣體入口 45 饋氣蓋板 46 流量限制環 48 碟型歧管 第9頁 本紙張尺度適用中國國豕標準(CNS ) A4規格(210X297公董) )U7〇l5 五、發明説明() 52 折流板 54 碟型歧警 56 閥 58 處理區 60 抽氣通遒 64 陶瓷環 66 室蓋 69 突緣 70 室蓋襯墊 72 襯墊 74 排氣孔徑 76 抽氣器 78 閥 80 排氣孔 82 真空泵 S3 節流閥 85 處理機 86 記憶體 88 真空系統 89 氣體傳送系統 90 氣體供給面板 91 氣體源 200 氧化層 205 基板 210 接觸孔 215 鈦層 220 氮化鈦層 225 銘層 Γ請先閱讀背面之注意事項 t^w ! 本頁,> -訂 經濟部中央標準局員工消費合作社印製 第10頁 畳__明詳細說明: I.介紹 本發明允許沉積一改良鈦薄膜,藉由預處王 其中,鈦薄膜係被以預處理電漿步騾加里基板, 〇 ^JL· 同時發現此一電漿預處理步驟係特別有用,者 天明人 層被用為多層堆疊(例如鈦/氮化鈦堆疊)之部1所’几積之鈦 體基板作成一歐姆接觸於經由一如氧化碎^層&、’以對半導 刻之接觸區域中。電漿預處理步驟㈣殘留^介電層麵 區域中之介電材料,並清除接觸區域,於纩籍板之接觸 、此積鈦層之前。 本紙張適用中國國家標準(CNS ) A4驗(2齡297公慶) 507015 A7 B7 五、發明説明() 於電漿預處理步驟之完成後,鈦層可以藉由引入一含鈦氣 &源同時維持先前形成之電漿加以沉積❹由本發明之方法 所加以沉積之鈦層係合適用於具有特性大小〇·35微米至 0.11微米或更小之積體電路製作。同時,本發明可以用以 ’儿積鈦薄膜於傳統使用現行可得氣體之設計之CVD室 中。 II.例示CVD室 第1Α圖例示一簡化平行板化學氣相沉積(CVD)系統 iO之實施例,其中,依據本發明之鈦層可以加以沉積。 CVD系統1〇包含一反應室3〇,其由一氣體分配系統89 經由氣體管路92A-C(也可以是其他管路,但未示出)接收 氣體。一真£系統8 8可以用以維持一指定壓力於室中, 並除去氣體副產物,並由室放出氣體。流低頻RF電源5 提供提供射頻電力至室,以於沉積時,由沉積氣體形成一 包漿,並於室清洗操作中,由室清洗氣體形成電漿。一熱 交換系統6使用一液熱傳送媒體,例如,水或水-乙二醇 混合劑,以由反應室除去熱量並保持室之某些部份適當地 被冷卻,以維持室内溫度於一穩定處理溫度,或若必要 時,加熱室之部份❶一處理機85依據儲存於記憶體86中 之指令,而經由控制線3, 3A-D(只有部份被示出)控制室 及次系統之操作。 氣體分配系,统89包含t體供給面板9〇及氣體或液體 源91A-C(若有必要的話,其*他源可以被加入),諸源包含 (請先閲讀背面之注意事項 •丨— 本頁) 訂 經濟部中央標準局員工消費合作社印装Order " f 507015 A7 B7 Printed by the Consumer Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs 5. The interface of the product description system. Fig. 1E shows a simplified partial cross-sectional view of the flow of the fin waves flowing through the wafer; 4 South 4 #, 9 and the exhaust system according to an embodiment of the present invention. FIG. 1F is a block diagram showing the architecture control structure of the system control software according to the conventional embodiment of Ming Yu ^ + Mingmingzu. Fig. 2A is a simplified cross-sectional view illustrating a contact structure in which a titanium layer deposited according to the present invention can be used. Figure 2B is a cross-sectional view of the formation of defects in the contact structure. Figure 3 is a flowchart of a processing procedure for depositing a titanium layer according to the present invention. Fig. 4 is a diagram showing the measurement of reflected power as a function of time and deposition length during the chamber cleaning step. Figures 5A and 5B are thin and film thickness measurements, illustrating the experimental results of the present invention. Drawing ## Description: 4 Select remote plasma system 5 Low-frequency RF power supply 6 Heat exchange system 10 Chemical vapor deposition system 22 Built-in electrode 26 Ceramic support handle 28 Water-cooled shaft 30 Reaction chamber 32 Bracket 33 Heating element 36 Wafer 38 Pick-up pin 40 Air jet head 42 Path 44 Central gas inlet 45 Inlet cover 46 Flow restriction ring 48 Disc manifold Page 9 This paper is applicable to China National Standard (CNS) A4 (210X297) ) U7〇l5 5. Description of the invention (52) Baffle plate 54 Disc alarm 56 Valve 58 Processing area 60 Exhaust vent 64 Ceramic ring 66 Chamber cover 69 Flange 70 Chamber cover gasket 72 Gasket 74 Exhaust aperture 76 Aspirator 78 Valve 80 Exhaust port 82 Vacuum pump S3 throttle 85 Processor 86 Memory 88 Vacuum system 89 Gas delivery system 90 Gas supply panel 91 Gas source 200 Oxidation layer 205 Substrate 210 Contact hole 215 Titanium layer 220 Nitriding Titanium layer 225 Ming layer Γ Please read the notes on the back t ^ w! This page, >-Order printed by the Consumers' Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs page 10 ___ Detailed description: I. Introduction to this Ming was allowed to deposit an improved titanium thin film. By pre-treating it, the titanium thin film was pretreated with a plasma step on the Gary substrate. ^ JL · At the same time, this plasma pretreatment step was found to be particularly useful. Used as part of a multi-layer stack (eg, titanium / titanium nitride stack). One of the several layers of the titanium body substrate is made into an ohmic contact in the contact region etched by the sintered layer & . Plasma pretreatment steps: Residue the dielectric material in the ^ dielectric plane area and remove the contact area before the titanium plate contacts before this titanium layer. This paper applies the Chinese National Standard (CNS) A4 inspection (297-year-old 2nd birthday) 507015 A7 B7 5. Description of the invention () After the completion of the plasma pretreatment step, the titanium layer can be introduced with a titanium-containing gas & source At the same time, the previously formed plasma is maintained for deposition. The titanium layer deposited by the method of the present invention is suitable for the fabrication of integrated circuits having a characteristic size of 0.35 μm to 0.11 μm or less. At the same time, the present invention can be used to deposit titanium films in a CVD chamber that is conventionally designed using currently available gases. II. Illustrating a CVD Chamber FIG. 1A illustrates an embodiment of a simplified parallel plate chemical vapor deposition (CVD) system iO, in which a titanium layer according to the present invention can be deposited. The CVD system 10 includes a reaction chamber 30, which receives gas from a gas distribution system 89 via gas lines 92A-C (also other lines, but not shown). A true system 8 8 can be used to maintain a specified pressure in the chamber, remove gas by-products, and release gas from the chamber. The low-frequency RF power supply 5 provides RF power to the chamber, so that a deposition slurry is formed from the deposition gas during deposition, and a plasma is formed from the chamber cleaning gas during the chamber cleaning operation. A heat exchange system 6 uses a liquid heat transfer medium, such as water or a water-glycol mixture, to remove heat from the reaction chamber and keep some parts of the chamber properly cooled to maintain the room temperature at a stable temperature. Process temperature, or if necessary, a part of the heating chamber-a processor 85, according to instructions stored in memory 86, via control lines 3, 3A-D (only part of which is shown) control room and sub-system Operation. The gas distribution system, the system 89 includes a t-body supply panel 90 and a gas or liquid source 91A-C (if necessary, other sources can be added), the sources include (please read the precautions on the back first. (This page) Ordered by the Consumer Standards Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs
507015 A7 B7 經濟部中央標準局員工消費合作社印製 五、發明説明() 可以取決於用於特定應用之想要處理而改變之氣體或液 體。液體源可以被保持於遠高於室内溫度之溫度,以降低 由於罜内溫度之改變造成之源溫度變化。氣體供應面板9〇 具有一混合系統,其由源91A_C接收沉積處理及載氣(或 氣化液體),用以混合並經由供給管路92A-c;送至於氣體 饋送蓋板45中 < 中央氣體入口 44。液體源可以被加熱以 提供於S:操作壓力上之壓力之蒸汽,或載氣,例如氦,氬, 或氮’可以被經由液體(或受熱液體)發泡,以產生一蒸汽。 一般而言,用於每一處理氣體之供給管路包含一關閉閥 (未示出),其可以用以自動或手動關閉處理氣體流,及一 質流控制器(未示出),其量測氣體或液體流經過供給管 路◎當有毒氣體(例如臭氧或自素氣體)被用於處理中時, 幾個關閉閥可以以傳統架構被定位於每一供氣管路中。包 含被供給至反應應30之例如四氯化鈥(TicI#)蒸汽,氫 (H2),氦(He),氬(Ar)及氮(No及/或其他摻雜物或反應源 之沉積及載氣之速率係同時被液體或氣體質流控制器 (MFC)(未示出)及/或閥(未示出)所控制β於較佳實施例 中,一氣體混合系統(未示出)包含一液體喷氣系統,用以 蒸汽化反應液體(例如TiC“)。一液體噴氣系統係較佳地, 因為其相較於發泡式型源能提供對導入氣體混合系統中 之反應液體之較佳控制。蒸汽化氣體然後於被傳送至供應 管路前被與載氣混合於氣體面板中,載氣係例如氦。當 然’已被認、為其他元件也可以使用作為一沉積源。熱交換系統6傳送冷卻劑至室30中之各種元件中, _____第12貫 (請先閲讀背面之注意事項再IPr本頁} 丨-_· 再 、?τ507015 A7 B7 Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention () Gases or liquids that can be changed depending on the intended treatment for a particular application. The liquid source can be kept at a temperature much higher than the indoor temperature to reduce the change in source temperature caused by the temperature change in the plutonium. The gas supply panel 90 has a mixing system, which receives a deposition process and a carrier gas (or a gasified liquid) from a source 91A_C for mixing and passing through the supply lines 92A-c; it is sent to the gas feed cover 45 < center The gas inlet 44. The liquid source can be heated to provide steam at a pressure of S: operating pressure, or a carrier gas such as helium, argon, or nitrogen 'can be bubbled through a liquid (or heated liquid) to produce a vapor. In general, the supply line for each process gas includes a shut-off valve (not shown) that can be used to automatically or manually shut off the process gas flow, and a mass flow controller (not shown). Gas or liquid flows through the supply line. When toxic gases (such as ozone or autogenous gas) are used in the process, several shut-off valves can be positioned in each gas supply line in a conventional architecture. Contains deposits such as tetrachloride (TicI #) steam, hydrogen (H2), helium (He), argon (Ar), and nitrogen (No and / or other dopants or reaction sources) that are supplied to the reaction chamber and The rate of the carrier gas is controlled simultaneously by a liquid or gas mass flow controller (MFC) (not shown) and / or a valve (not shown). In a preferred embodiment, a gas mixing system (not shown) Contains a liquid jet system for vaporizing the reaction liquid (such as TiC "). A liquid jet system is preferred because it provides a comparison of the reaction liquid introduced into the gas mixing system compared to a foamed source. The vaporized gas is then mixed in a gas panel with a carrier gas, such as helium, before being transferred to the supply line. Of course, it has been recognized that other components can also be used as a deposition source. Heat exchange System 6 sends coolant to various components in chamber 30. _____12th (please read the precautions on the back before IPr page) 丨 -_ · Then,? Τ
本紙張又度適用中國國家標準(CNS ) A4規格(210X297公釐) 507015 經濟部中央標準局員工消費合作社印裝 A7 B7 五、發明説明() 以於高溫處理時,冷卻這些元件。熱交換系統6作動以降 低這些至元件之溫度,以減少由於高溫處理而造成之於這 些兀件上之不想要之沉積。熱交換系統6包含連接線(未 示出)’其供給冷卻水經由傳送冷卻劑之冷卻歧管(未示出) 至氣a致刀配系統,該系統包含面板4 q (以下說明)。一水流 檢測器檢測來自一熱夂換器(未示出)之水流,以密封該組 件。 、 一電阻性加熱托架32支撐一晶圓36於一晶圓袋34 中。如於第1B圖中所示,其係為托架32之簡剖面圖,粍 架32包含一内藏電極22,例如為一内藏鉬網,及一加熱 7G件33,例如一内藏鉬線圈。托架32較佳由氮化鋁製造, 以忍受高處理溫度並較佳係擴散結合至陶瓷支撐柄% 上,該柄係被固定至水冷卻鋁軸28(未示於第1B圖中,但 示於第1C圖中),該軸係嚙合至一舉起馬達。陶瓷支撐柄 26及鋁軸28具有一中心通道,其係被一鎳棒25所佔,該 棒使電極22接地。中心通道係被保持於大氣壓力,以避 免腐蝕發生於金屬至金屬連接中。 陶資托架32係被製造以提供均勻電容值,藉由内藏 RF電極22於基板支持件之表面下之均勻深度電極 22係較佳被定位於一最小深度,該深度係取決於陶資材 料,以提供最大電容,同時避免覆蓋RF電極22之薄陶资 層之破裂或剥落。於一實施例中,RF電極22係内藏於托 架32之上表面下40密耳《陶瓷托架32之其他細節係被 說明於申請於1997年12月l·日之共同申請之美國專利案 第13頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) (請先閲讀背面之注意事項β寫本頁) 訂 刈 7015 A7 —一" _________ B7 五、發明説明() ~ ^-— 中,其被命名混合射頻CVE^S及設備",以赛巴斯汀 羅西’大#柏為共同發明人,該案係於此併 入作為參考。 托架32T以使用自料機冑,被垂直移動於處理位 置(示於第1C圖)及低加載位置(未示出)之間’該機制係被 詳細說明於共同讓與之美國專利申請案第〇8/738,42〇 號,申請於1996年十月25曰之命名為,,自對準舉起機制„ 中,該案之揭示係被併入作為參考。參考第1〇圖,拾取 銷3 8(只有兩個被示出)係可滑動於托架32内,以其上端 之圓錐頭使得其不會落下。拾取銷38之下端可以被嚙合 以一垂直可移動拾取環39,因此,可以被拾取於托架之表 面上。於托架32内之下方加載位置(略低於一狹縫閥56) 中’一機械刀片(未示出)係配合以拾取銷及拾取環以經由 狹缝閥56傳送晶圓36入及出室30,該室可以被真空密 封,以防止氣流經由該狹縫閥5 6流入或流出室。拾取銷 38提高被插入晶圓(未示出)離開機械刀片,然後,托架上 升而升高晶圓離開拾取銷進入於托架上表面之晶圓袋 中。一合適機械傳送組件係描述於授與馬單之共同讓與美 國專利案第4,951,601號,其完整揭示係併入作為參考。 托架32然後再提升晶圓36進入處理位置,其係接近 一氣體分配面板(於此後稱為噴氣頭)40,其包含大量之孔 或通道42,用以注入處理氣體至處理區5 8。處理氣體係 經由於饋氣蓋板45中之中心氣體入口 44被注入室30,至 第一碟形歧管43,並由於折流板(或阻擋板52)中之這些通 第η頁 本紙張尺度適用中國國家標準(CNS ) Α4規格(210Χ297公釐) " (請先閲讀背面之注意事項本頁) .¾. 訂 經濟部中央標準局員工消費合作社印裝 507015 經濟部中央標準局員工消費合作社印製 A7 ______ B7 五、發明説明() 道50至第二碟型歧管54。 如由箭頭所指,處理氣體由於噴氣頭4〇由之孔42進 入於喷氣頭及托架間之處理區域58 (其被稱為”沉積區"), 以反應於晶圓36之表面。處理氣體副產物然後徑向地向 外流過晶圓36之邊緣,並穿過一流量限制環46(其隨後將 更詳細說明),當托架於處理位置時,副產物係被沉積於 托架32之上邊緣。因此,處理氣體流經一形成於限制環 46之上及環型絕緣器53間之吸盤孔50,進入抽氣通道 6 0。於進入抽氣通道6 0時,排氣係被循環於予以被真空 泵82所抽真空之處理室之週圍。抽氣通道6〇係經由排氣 孔徑74連接至抽氣器76。排氣孔徑74限制於抽氣通遒及 抽氣器間之流量。一閥7 8管理經由排氣通孔8 〇至抽氣栗 82之閘門。一系統控制器(未示於此圖中)用以依據儲存於 記憶體(未示出)中之壓力控制程式,來控制節流閥8 3,該 程式比較來自壓力感應器(未示出)例如壓力表之量測信 號,與儲存於記憶體中或依據控制程式所產生之值比較。 環型抽氣通道60之側邊大致係為陶瓷環64,一室蓋 襯塾72,及環形絕緣器53所定義。第1E圖為乾架32, 流量限制環46,襯墊70及72,絕緣器53,陶资環64及 抽氣通遒60之簡單部份剖面立體圖。該圖示出於喷氣頭 4〇中之噴嘴42之處理氣體流向晶圓36,然後,其係被徑 向地流84於晶圓36上。隨後,氣體流係被反射向上於限 制環46之上進入抽氣通道60。於抽氣通道60中,氣體流 沿著環周路徑86向真空泵°, 本紙張从適用( CNS )八4麟(21〇/297公釐1 ^ --- (請先閱讀背面之注意事項本頁) -1^ 507015 A7 B7 五、發明説明() 抽氣通道60及其元件係被設計以減少不想要薄膜沉 積之作用,藉由導引處理氣體及副產物進入排氣系統中。 排氣流形成"靜止區",於其中,只發生少量氣體移動。這 些靜止區近似吹氣區,其中,發生反應氣體於該區域中, 並降低不想要之沉積。同時,吹氣(例如,氬)係被由氣體 噴% (未示出)引入區臨界區域,例如陶瓷部,及交熱邊緣 及背面,以降低於這些區域上之不想要沉積。 於托架及室之其他部件上之不想要沉積係被以其他 方式減少。明白地說,流量限制環46減少氣體流出托架 至1:义底部。依據本發明之實施例,使用Ticl4(如以下所 詳述)又鈦之沉積具有流速大大高於用以形成其他鈦膜之 傳統沉積系統中之傳送方法。於一合適於鈦沉積之較佳實 施中,流量限制環46係由融熔矽土作成,因為此材料具 有相當低導熱度,及因為其係不具導電性。於另一實施 例’流量限制器環可以由鈦作成,用於含鈦層之沉積處 理,因為環材料將不會污染沉積層。 於各種實施例中,限制器環覆蓋托架之上及邊緣,使 得不想要薄膜沉積於環上,而不是在托架之上或在室之底 部。有利地,流量限制環減少了不想要之沉積之危險(及 相關問題)’否則,其會發生於較高流速。室蓋66可以容 易地被除去用以清洗,使得可對相當便宜之限制環作接 觸,其將被拾起並使用化學劑及/或機械處理被清洗。 再次參考第1A圖,流量限制環46可以於處理時,被 托架32所支援。當托架被下锋,用於晶圓卸載及加載時, 第16頁 冬紙張尺度通用T國國豕檩準(CNS ) A4規格(210X297公釐) (請先閱讀背面之注意事項本頁) 舄本 訂· 經濟部中央標隼局員工消費合作社印製 ^7015 A7 ^_B7 ____ 五、發明説明() 限制環設立於突緣69中之陶瓷環64上。當支持下一晶圓 之粍架係被提升至處理位置時,其拾起流量限制環。於依 據本發明之實施例之鈦處理之室中之壓力,重力是足夠以 支持(安置於晶圓包裝)晶圓及於托上之限制環。 馬達及光學感應器(未示出)係用以移動及決定例如節 流閥83及托架32之可動機械組件之位置。附著至把架32 及室體76底部之風箱(未示出)形成一可動氣密密封於托 架旁。包含一可取捨遠端電漿系統4(其係用以提供使用一 由例如微波源形成之遠端電漿之室清洗功用)之托架拾取 系統’馬達’閘門閥’電漿系統及其他系統元件係由於控 制線3及3A-3D上之處理機85所控制,控制線只有部份 被示出。 處理機85執行系統控制軟體,其係一儲存連接至處 理機85之記憶體86之電腦程式。較佳地,記憶體86可 以是一硬碟機,當然,記憶體8 6可以是其他記憶體。除 了硬碟機(例如記憶體86),於特定實施例中之CVD裝置 10包含一軟碟機及一卡架。處理機85在系統控制軟體控 制下動作,軟體包含指令組,其表示氣體,氣體流,室壓, 室溫度,RF電力位準,加熱器托架位置,加熱器溫度, 及特定處理之其他參數之定時’混合。例如這些儲存於其 他記憶體之其他電腦程式包含例如一軟碟或其他插入於 磁碟機或其他適當設備之其電腦產品,其係可以用以作動 處理機85。系統控制軟體將如下所述。卡架包含單片電 腦,類比及數位輸入/輸出板•界面板及步進馬達控制板。 __ 第17頁 ( CNS ) ( 210X297/^1 ) " " """""~ (請先閱讀背面之注意事項This paper is again applicable to China National Standard (CNS) A4 (210X297 mm) 507015 Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs A7 B7 V. Description of the invention () To cool these components during high temperature processing. The heat exchange system 6 operates to reduce the temperature of these components to reduce unwanted deposits on these components due to high temperature processing. The heat exchange system 6 includes a connection line (not shown) 'which supplies cooling water through a cooling manifold (not shown) that transfers the coolant to the gas-a-knife distribution system, which includes a panel 4 q (described below). A water flow detector detects the flow of water from a heat exchanger (not shown) to seal the assembly. A resistive heating bracket 32 supports a wafer 36 in a wafer bag 34. As shown in Figure 1B, it is a simplified cross-sectional view of the bracket 32. The bracket 32 includes a built-in electrode 22, such as a built-in molybdenum mesh, and a heated 7G member 33, such as a built-in molybdenum. Coil. The bracket 32 is preferably made of aluminum nitride to withstand high processing temperatures and is preferably diffusion bonded to a ceramic support shank, which is fixed to a water-cooled aluminum shaft 28 (not shown in FIG. 1B, but (Shown in Figure 1C), the shaft is engaged to a lift motor. The ceramic support shank 26 and the aluminum shaft 28 have a central channel, which is occupied by a nickel rod 25, which grounds the electrode 22. The central channel system is maintained at atmospheric pressure to prevent corrosion from occurring in the metal-to-metal connection. The ceramic material bracket 32 is manufactured to provide a uniform capacitance value. The uniform depth of the electrode 22 is preferably positioned at a minimum depth by the built-in RF electrode 22 under the surface of the substrate support. The depth depends on the ceramic material. Material to provide maximum capacitance while avoiding cracking or peeling of the thin ceramic layer covering the RF electrode 22. In one embodiment, the RF electrode 22 is built in 40 mils below the upper surface of the bracket 32. "Other details of the ceramic bracket 32 are described in a commonly-applied US patent filed on December 1, 1997. Page 13 of this case applies the Chinese National Standard (CNS) A4 specification (210X297 mm) (please read the precautions on the back β to write this page) Order 7015 A7 — a " _________ B7 V. Description of the invention () ~ ^ -—, it was named Hybrid RF CVE ^ S and Equipment ", with Sebastian Rosie's # 大 柏柏 as co-inventor, the case is hereby incorporated by reference. The bracket 32T is moved vertically between the processing position (shown in FIG. 1C) and the low-load position (not shown) using a self-propelled machine. The mechanism is described in detail in the commonly assigned US patent application. No. 08 / 738,42, the application was named on October 25, 1996, the self-aligned lifting mechanism, the disclosure of this case is incorporated as a reference. Refer to Figure 10, pick Pins 38 (only two are shown) are slidable in the bracket 32 with a tapered head at the upper end so that they will not fall. The lower end of the picking pin 38 can be engaged with a vertically movable picking ring 39, so Can be picked up on the surface of the bracket. A mechanical blade (not shown) in the loading position (slightly below a slit valve 56) inside the bracket 32 is fitted with a picking pin and a picking ring to pass The slit valve 56 conveys the wafer 36 into and out of the chamber 30, and the chamber may be vacuum-sealed to prevent airflow from flowing into or out of the chamber through the slit valve 56. The pick-up pin 38 raises the inserted wafer (not shown) and leaves The mechanical blade, then, the tray rises and raises the wafer away from the pick-up pin and onto the tray A suitable mechanical transfer assembly is described in US Pat. No. 4,951,601, which was jointly assigned to Ma Dan, and its complete disclosure is incorporated as a reference. The carrier 32 then lifts the wafer 36 Entering the processing position, it is close to a gas distribution panel (hereinafter referred to as a jet head) 40, which contains a large number of holes or channels 42 for injecting the processing gas into the processing area 58. The processing gas system passes through the gas feed cover plate The central gas inlet 44 in 45 is injected into the chamber 30, to the first dish-shaped manifold 43, and because of these through the baffle (or barrier plate 52) on page η, this paper standard applies to China National Standard (CNS) Α4 Specifications (210 × 297 mm) " (Please read the note on the back page first.). ¾. Order printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 507015 Printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economics A7 ______ B7 V. Invention Explanation () Channel 50 to the second dish-type manifold 54. As indicated by the arrow, the processing gas enters the processing area 58 (which is called "deposition") between the jet head and the bracket due to the hole 42 of the jet head 40. Zone "), to Reacts to the surface of the wafer 36. The process gas by-product then flows radially outwardly across the edge of the wafer 36 and passes through a flow restriction ring 46 (which will be described in more detail later). By-products are deposited on the carrier when the carrier is in the processing position. 32 above the edge. Therefore, the processing gas flows through a sucker hole 50 formed on the restriction ring 46 and between the ring-shaped insulators 53 and enters the suction channel 60. When entering the exhaust passage 60, the exhaust system is circulated around the processing chamber to be evacuated by the vacuum pump 82. The exhaust passage 60 is connected to the air extractor 76 via an exhaust hole 74. The exhaust aperture 74 is limited to the flow rate between the exhaust vent and the extractor. A valve 78 manages the gate through the exhaust vent hole 80 to the pump pump 82. A system controller (not shown in the figure) is used to control the throttle valve 8 3 according to a pressure control program stored in a memory (not shown), which is compared with a pressure sensor (not shown) For example, the measurement signal of the pressure gauge is compared with the value stored in the memory or generated according to the control program. The sides of the ring-shaped suction channel 60 are roughly defined by a ceramic ring 64, a chamber cover lining 72, and a ring insulator 53. Fig. 1E is a simple partial cross-sectional perspective view of the dry rack 32, the flow restricting ring 46, the gaskets 70 and 72, the insulator 53, the ceramic material ring 64, and the exhaust air duct 60. The illustration shows that the processing gas from the nozzle 42 in the air-jet head 40 flows to the wafer 36, and then, it flows 84 to the wafer 36 radially. Subsequently, the gas flow is reflected upward above the restriction ring 46 into the extraction channel 60. In the suction channel 60, the gas flow is along the circumferential path 86 to the vacuum pump. This paper is suitable for (CNS) 8 4 Lin (21〇 / 297 mm 1 ^ --- (Please read the precautions on the back first Page) -1 ^ 507015 A7 B7 V. Description of the invention () The extraction channel 60 and its components are designed to reduce the effect of unwanted film deposition by directing the process gas and by-products into the exhaust system. The flow forms " static zones ", in which only a small amount of gas movement occurs. These static zones are similar to gas blowing zones, in which reactive gases occur in the zone and reduce unwanted deposits. At the same time, gas blowing (for example, Argon) is introduced into critical areas of the zone, such as ceramic parts, and cross-heated edges and back surfaces by gas injection (not shown) to reduce unwanted deposition on these areas. On the carrier and other parts of the chamber The unwanted deposition system is reduced in other ways. To be clear, the flow restriction ring 46 reduces gas outflow from the bracket to 1: bottom. According to an embodiment of the present invention, the deposition using Ticl4 (as detailed below) and titanium has Flow rate is much higher than with Transfer method in traditional deposition systems that form other titanium films. In a preferred implementation suitable for titanium deposition, the flow restriction ring 46 is made of fused silica because the material has a relatively low thermal conductivity and because it is Non-conductive. In another embodiment, the 'flow limiter ring can be made of titanium for the deposition of titanium-containing layers, because the ring material will not contaminate the deposited layer. In various embodiments, the limiter ring covers the bracket And edges, such that unwanted thin films are deposited on the ring, rather than on the cradle or on the bottom of the chamber. Advantageously, the flow limiting ring reduces the risk of unwanted deposition (and related issues) 'Otherwise, its Occurs at higher flow rates. The chamber cover 66 can be easily removed for cleaning, allowing access to a relatively inexpensive confinement ring, which will be picked up and cleaned using chemicals and / or mechanical treatment. Refer again to section Figure 1A, the flow restriction ring 46 can be supported by the bracket 32 during processing. When the bracket is lowered for wafer unloading and loading, page 16 Winter Paper Standard General T Country Standard (CNS)) A4 size (210X297 mm) (Please read the note on the back page first) 舄 订 · Printed by the Consumer Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs ^ 7015 A7 ^ _B7 ____ 5. Description of the invention The ceramic ring 64 in the flange 69. When the gantry supporting the next wafer is lifted to the processing position, it picks up the flow restriction ring. The pressure in the titanium-treated chamber according to the embodiment of the present invention, Gravity is sufficient to support (place on the wafer package) the wafer and the retaining ring on the holder. The motor and optical sensor (not shown) are used to move and determine movable machinery such as the throttle valve 83 and the bracket 32 Position of the component. A bellows (not shown) attached to the bottom of the rack 32 and the chamber body 76 forms a movable air-tight seal next to the bracket. Contains an optional remote plasma system 4 (which is used to provide a room cleaning function using a remote plasma formed by, for example, a microwave source) a carriage picking system 'motor' gate valve 'plasma system and other systems The components are controlled by the processor 85 on the control lines 3 and 3A-3D, and only some of the control lines are shown. The processor 85 executes system control software, which is a computer program storing a memory 86 connected to the processor 85. Preferably, the memory 86 may be a hard disk drive. Of course, the memory 86 may be other memories. In addition to the hard disk drive (e.g., memory 86), the CVD apparatus 10 in a particular embodiment includes a floppy disk drive and a card holder. The processor 85 operates under the control of the system control software. The software includes a command group, which indicates the gas, gas flow, chamber pressure, chamber temperature, RF power level, heater bracket position, heater temperature, and other parameters for specific processing. The timing of 'mixing. For example, these other computer programs stored in other memory include, for example, a floppy disk or other computer product inserted into a disk drive or other suitable device, which can be used to operate the processor 85. The system control software will be described below. The card holder contains a single-chip computer, analog and digital input / output boards, interface boards, and stepper motor control boards. __ Page 17 (CNS) (210X297 / ^ 1) " " " " " " " ~ (Please read the precautions on the back first
經濟部中央標隼局員工消費合作社印製 507015 A7 __B7 五、發明説明() CVD設備10之各種部件符合維莎模組歐洲(Vme)標準, 其定義板,卡及連接器尺寸及種類。VME標準同時定義匯 流排結構,具有1 6位元資料匯流排及24位定址流匯流 排。 於使用者及處理機85間之界面是經由一 CRT監視器 93a及光筆93b(示於第1D圖),其是用於CVD設備10之 系統監視器之間化圖’其所例示是於多室系統之一室。 CVD設備10是較佳地附著至主機單元95,其包含並提供 用於設備1 0之電氣,接管及其他支援功能。例示主機單 元可相容於CVD設備1 〇之例示實施例係可由美國加州聖 塔卡拉之應用材料公司購得之preeisi〇n 5000TM,Centura 5 200TM及Endura 5 5 00TM系統。多室系統具有能力,以傳 送晶圓於其室之間,而不會破壞真空而不必曝露晶圓至多 室系統中之濕氣或其他污染物。多室系統之優點是於多室 系統之不同室可以被用於整個處理之不同目的。例如,於 本發明之較佳實施例中,一室係用於CVD沉積鈦薄膜而 另一個係用於CVD沉積氮化鈦薄膜。於此方式,沉積鈦/ 氮化鈥堆疊’其係可共同用於形成如於第2Α圖所討論之 接觸結構’其係可以持續進行於多室系統中,藉以防止當 晶圓被傳送於各種分離個別室間(不是一多室系統),以作 為不同部份之鈦/氮化鈦堆疊處理時,之晶圓污染。 於較佳實施例中,兩監視器93a被使用,一安裝在無 塵室壁’給操作者使用及另一個則在該壁面之後,給服務 技術員使用。該兩監視器93a同時顯示相同資訊,但只有 ________ 第 18 頁 本紙張尺度適用中國國家標準(CNS )八4規格(21〇X297公釐〉 (請先閱讀背面之注意事項Printed by the Consumers' Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs 507015 A7 __B7 V. Description of the Invention () The various components of the CVD equipment 10 conform to the VISA module European standard (Vme), which defines the size and type of boards, cards and connectors. The VME standard also defines a bus structure with 16-bit data buses and 24-bit addressing buses. The interface between the user and the processor 85 is via a CRT monitor 93a and a light pen 93b (shown in FIG. 1D), which is a schematic diagram of the system monitor used for the CVD device 10. One of the chamber systems. The CVD device 10 is preferably attached to the host unit 95, which contains and provides electrical, takeover, and other support functions for the device 10. Exemplary embodiments exemplifying that the host unit is compatible with the CVD apparatus 10 are preeisiON 5000TM, Centura 5 200TM, and Endura 5 500TM systems, which are commercially available from Applied Materials, Inc. of Santa Cala, California. Multi-chamber systems have the ability to transfer wafers between their chambers without breaking the vacuum without exposing wafers to moisture or other contaminants in the multi-chamber system. The advantage of a multi-chamber system is that different chambers of the multi-chamber system can be used for different purposes throughout the process. For example, in the preferred embodiment of the present invention, one chamber is used for CVD deposition of a titanium film and the other is used for CVD deposition of a titanium nitride film. In this way, the deposition of the titanium / nitride 'stack can be used together to form a contact structure as discussed in FIG. 2A. The system can be continuously performed in a multi-chamber system, thereby preventing when wafers are transferred to various Separation of individual chambers (not a multi-chamber system) for wafer contamination when different parts of the titanium / titanium nitride stack are processed. In the preferred embodiment, two monitors 93a are used, one installed on the clean room wall 'for the operator and the other behind the wall surface for the service technician. The two monitors 93a display the same information at the same time, but only ________ page 18 This paper size is applicable to China National Standards (CNS) 8 4 specifications (21 × 297 mm) (Please read the precautions on the back first
、tr 經濟部中央標準局員工消費合作社印製 ^ 經濟部中央標準局員工消費合作社印製 五 A7 B7 、發明說明( 光筆93b可使用。光筆93b以筆尖中之光感應器檢測由 CRT ·、、、員示器所發射之光。為選擇一特定螢幕或功能,操作 者接觸顯示螢幕之指定區域並按下在筆93b上之按鈕。被 接觸至之區域改變其發亮色彩,或一新名單或螢幕被顯 二而確認於光筆及顯示螢幕間之通訊。當然,其他裝置, 如鍵盤’滑鼠或其他指示或通訊裝置,可以被用以或除 了光筆93b,以允許使用者與處理機85通訊。 用以沉積薄膜及乾淨室之處理係被使用一電腦程式 產品加以實施,該產品係為處理機85(第1A圖)所執行。 孩電腦程式碼可以被以任何傳統電腦可讀取程式語言,例 如68000組合語言,c,c + +,pascai或福傳或其他語言加 以撰窝。合適之程式碼係使用一傳統文字編輯器加以輸入 一單一檔案或多檔案中,並被儲存在例如一電腦中之記憶 &系統之電腦可使用媒體,例如電腦之記憶體系統中。若 所輪入碼文字係高階語言,則碼被編譯,所得編譯碼然後 被連結至預編輯視窗庫常式之目的碼。為了執行所連結之 編譯目的碼,系統使用者呼唤目的碼,使得電腦系統载入 於記憶體中之碼。然後,CPU讀取並執行該碼,以執行指 定於程式中之工作。 第1F圖示出電腦程式160之基礎控制結構之例示方 塊圖。一使用者藉由使用光筆界面而反應於顯示在CRT 監視器上之選單及螢幕,而輸入一處理組數目及處理室數 至一處理選擇器副程式161。該處理組係需用以執行特定 處理之處理參數之預定組,並被預定設定數所指示。該處 第19頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) (請先閲讀背面之注意事項, Tr Printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs ^ Printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs printed five A7 B7, invention description (Light pen 93b can be used. Light pen 93b is detected by the light sensor in the pen tip by CRT · ,,, The light emitted by the indicator. To select a specific screen or function, the operator touches a designated area of the display screen and presses the button on the pen 93b. The area touched changes its bright color, or a new list Or the screen is displayed to confirm the communication between the light pen and the display screen. Of course, other devices, such as a keyboard, mouse or other pointing or communication device, can be used or replaced with the light pen 93b to allow the user to communicate with the processor 85 Communication. The process used to deposit the film and clean room is implemented using a computer program product that is executed by processor 85 (Figure 1A). The computer code can be read by any conventional computer-readable program. Languages, such as 68000 combinatorial languages, c, c ++, pascai or evangelism or other languages. Suitable codes are created using a traditional text editor. Into a single file or multiple files and stored in, for example, a computer's memory & system, a computer usable medium, such as a computer's memory system. If the rounded code text is a high-level language, the code is compiled The resulting code is then linked to the destination code of the pre-edited window library routine. In order to execute the linked compilation destination code, the system user calls the destination code so that the computer system loads the code in memory. Then, the CPU reads the code Take and execute the code to perform the tasks specified in the program. Figure 1F shows an example block diagram of the basic control structure of the computer program 160. A user responds to the display on a CRT monitor by using a light pen interface. Menus and screens, and enter a number of processing groups and number of processing rooms into a processing selector subroutine 161. This processing group is a predetermined group of processing parameters required to perform a specific process and is indicated by the predetermined set number. Page 19 This paper size applies to Chinese National Standard (CNS) A4 (210X297 mm) (Please read the notes on the back first
本頁) ,訂· 507015 A7 B7 五、發明説明( 經濟部中央標準局員工消費合作社印製 理選擇器副程式161識別⑴想要之處理室, ^ 及(11)需用以 操作執行想要處理之處理室之想要處理參數組。用以執行 一特定處理之處理參數關係於處理之條件,例如處理氣體 組成及流率,溫度,壓力,電漿條件,例如,RF偏壓功 率位準及低頻RF頻率,(除了,微波產生電力位準,用於 被裝有遠端微波電漿系統之實施例之位準)冷卻氣體壓力 及壁室溫度。於一些實施例中,其中可能多於一處理選擇 器副程式。處理參數係被以名單方式提供給使用者並利 光筆/CRT監視界面輸入。 該用以監視處理之信號係被系統控制器之類比輸 及數位輸入板所提供,及用以控制處理之信號被輸出在 統控制器10之類比輸出及數位輸出板上。 一製程序向副程式162包含用以接受識別處理室及 自處理選擇田|】程式1 6 1之處理參數組,以及,用以控制 處理1扭作之程式碼。多使用者可以輸入處理組號及處 室號,或一使用者可以輸入多處理組號及處理室號,或一 單一使用者可以輸入多重處理設定號及處理室號,使得序 向副程式162操作以排序選定之處理於想要之順序。較佳 地’序向程式1 62包含一程式碼,以執行以下之步驟: 監視處理室之操作,以決定是否哪些室被使用,(Π)決 被使用處理立中正被執行何處理,及(丨丨丨)基於可用之處一 至及予以執行之處理類型來執行想要之處理。傳統監視處 理1之方法可以加以使用,例如,輪流監視。當排定哪一 處理被執行時’序向副程式162可以被設計以考量予以使 用 入 系 來 各 理 ⑴ 定 理 (請先閱讀背面之注意事項This page), order · 507015 A7 B7 V. Description of the invention (Identified by the subselection program 161 printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs ⑴ Identification of the desired processing room, ^ and (11) need to be used to operate the desired The set of processing parameters that the processing chamber wants to process. The processing parameters used to perform a particular process are related to the processing conditions, such as the composition of the process gas and the flow rate, temperature, pressure, and plasma conditions, such as RF bias power levels And low-frequency RF frequencies (except for the level of microwave-generated power for the level of an embodiment equipped with a remote microwave plasma system) cooling gas pressure and wall temperature. In some embodiments, this may be more than A processing selector subroutine. The processing parameters are provided to the user in a list manner and are input by the light pen / CRT monitoring interface. The signals for monitoring processing are provided by the analog input of the system controller and the digital input board, and The signals used to control the processing are output on the analog output and digital output boards of the integrated controller 10. A system program subroutine 162 includes a processing room for identifying and processing. Select Tian |】 The processing parameter group of program 1 6 1 and the code used to control the processing of 1. The multi-user can enter the processing group number and office number, or one user can enter the multi-processing group number and A processing room number, or a single user can enter multiple processing setting numbers and processing room numbers, so that the sequential subroutine 162 operates to sort the selected processing in the desired order. Preferably, the 'sequential programming 1 62 contains a program Code to perform the following steps: Monitor the operation of the processing room to determine whether the rooms are being used, (Π) determine which processing is being used and what processing is being performed, and (丨 丨 丨) based on where available and execute Process type to perform the desired process. Traditional monitoring process 1 methods can be used, for example, turn-by-turn monitoring. When scheduling which process is performed, the sequence subroutine 162 can be designed to take into account the use of the system. Each theorem Theorem (Please read the notes on the back first
訂Order
507015 A7 B7 五、發明説明( 用之處理室之狀況與選定處理之想要處理狀況,或者每一 特定使用者輸人要求之”年齡,,,或者是U規劃者想要 包含之其他相關因素相比較,以決定排序順序。 一旦序向副程式162決定哪一處理室及處理組組合被 下一個執行時,序向副程式162藉由傳送特定處理組參數 至一室管理副程式163a-c,而使得處理組執行,該副程式 162依據由序向副程式30所決定之處理組來控制於處理 室30或於其他可能室(未示出)中之多處理工作。例如,室 管理器副程式163b包含程式碼,用以控制於處理室“中 之CVD操作。室管理器副程式16扑同時控制各種室元件 副程式之執行,其控制需要以執行選定處理組之室元件之 操作。室元件副程式之例子是基板定位副程式164,處理 氣體控制副程式1 65,壓力控制副程式i 66,加熱器控制 副程式167及電漿控制副程式168。取決於CVD室之特定 架構,一些實施例包含所有副程式,而其他實施例可以包 含部份之副程式。熟習於本技藝者將知道可以包含其他之 室控制副程式,這是取決於想要執行於處理室3〇中之處 理而定。於操作中,室管理副程式163b依據予以執行之 特定處理,而選擇性地排序或呼叫處理元件副程式。由室 管理副程式1 63b所執行之排序係以類似於由序向副程式 162所使用之方式進行,以排序哪一處理室及處理組予以 下一個被執行。典型地,室管理副程式163b包含步驟有: 監視各種室兀件,基於予以執行之處理組之處理參數,而 決定哪一兀件需要被操作,以及,反應於該監視及決定步 第21頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公| ) (請先閱讀背面之注意事項一507015 A7 B7 V. Description of the invention (the status of the processing room used and the status of the processing to be selected, or the "age" required by each specific user, or other relevant factors that U planners want to include Compare to determine the sort order. Once the subroutine 162 decides which processing room and processing group combination is to be executed next, the subroutine 162 sends specific processing group parameters to the one-room management subroutines 163a-c. To cause the processing group to execute, the subroutine 162 controls many processing tasks in the processing room 30 or in other possible rooms (not shown) according to the processing group determined by the sequence subroutine 30. For example, the room manager The subroutine 163b contains code for controlling the CVD operation in the processing chamber. The subroutine 16 of the room manager simultaneously controls the execution of various subroutines of the chamber components. The control needs to perform the operations of the chamber components of the selected processing group. Examples of chamber component subroutines are substrate positioning subroutine 164, process gas control subroutine 1 65, pressure control subroutine i 66, heater control subroutine 167, and plasma control subroutine. Program 168. Depending on the specific architecture of the CVD chamber, some embodiments include all subprograms, while other embodiments may include some subprograms. Those skilled in the art will know that other room control subprograms may be included, depending on It depends on the processing that is to be performed in the processing room 30. In operation, the room management subroutine 163b selectively sorts or calls the processing component subroutine according to the specific processing to be performed. The room management subroutine 1 63b The sorting performed is performed in a manner similar to that used by the sequence subroutine 162 to sort which processing room and processing group are to be executed next. Typically, the room management subroutine 163b includes the steps of: monitoring various rooms Based on the processing parameters of the processing group to be executed, the software must decide which software needs to be operated, and, in response to the monitoring and decision steps, page 21 This paper applies the Chinese National Standard (CNS) A4 specification (210X297) |) (Please read Note 1 on the back first
-訂 經濟部中央標準局員工消費合作社印裝 驟而使得室元件副程式執行。 /於第1F圖中之特定室元件副程式之操作將藉由參 考第1A圖加以說明。基板定位副程式} 包含用以控制 至π件 < 耘式碼,其被用以加載基板至托架W ,可選擇 地,拾起基板至當 — 中 < 想要兩度’以控制於基板及噴 氣;員4〇 ^心間1^。當一基板被加載至一處理1: 30時,加 熱器組件33被降低,以接收於晶圓袋34中之基板,然後, 上升至想要高度。於操作中,基板定位副程式164反應於 由皇&理剎程式1 63b傳送之有關支援高度之處理組參數 而控制托架3 2之動作。 經濟部中央標準局員工消費合作社印製 處理氣體控制副程式165具有程式碼,用以控制處理 氣體成份及流率。處理氣體控制副程式丨65控制安全閥之 開/關位置,及同時升/降質流控制器,以獲得想要之氣體 流速。處理氣體控制副程式丨6 5係被室管理副程式^ 6 3 b 及所有室元件副程式所唤起。副程式165接收來自相關於 想要氣體流速之室管理副程式之處理參數。典型地,處理 氣體控制副私式1 6 5藉由打開氣體供給管線加以操作,及 重覆地⑴1買取所需之質流控制器,(ii)比較讀值與接收自 室管理副程式163b之想要流速,及(iii)於需要時,調整氣 體供給管線之流速。再者,處理氣體控制副程式丨63包含 步驟:監視不安全流速之氣體流速,及當一不安全狀況被 檢出時,作動安全閥。處理氣體控制副程式丨65同時取決 於選定想要製程(清洗或沉積或其他),而控制用以清除氣 體及沉積氣體之氣體成份及流速。其他實施例可以多於一 第22頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 五、 經濟部中央標準局員工消費合作社印製 發明説明() 種-處理氣體控制副程式,每一副程式控制一特定類型之 處理或氣體管路之特定組。 、於二處理中,例如氮或氬之惰性氣體係流入室中, 以在處理氣體被引人室之前穩定室中之壓力。對於這些處 理,處理氣體控制副程式165被規劃以包含步驟有:令惰 =氣體流人室中—段時間,以穩定化室中之壓力,然後執 一迟之步驟。另外,當一處理氣體係由一液態前驅物汽 化時,例如TlCl4,處理氣體控制副程式165將被寫入以 包含步驟:發泡一傳送氣體,例如,t,經由於一發泡組 件中之液態先驅物,或引入一載氣體,例&,氦至一液態 压入系統中。當一發泡室被用於此類型之處理時,處理氣 體控制副程式165調節傳送氣體之流量,於發泡室中之壓 力,及發泡罜溫度,以獲得用於想要處理氣體流速。如上 所述,想要處理氣體流速係被傳送至處理氣體控制副程式 成為處理參數。再者,處理氣體控制副程式165包含 步驟’用以取得想要之傳送氣體流速,發泡室壓力,及用 於想要氣體流速之發泡室溫度,用以藉由存取包含用於一 已知處理氣體流速需要之值之儲存表。一旦所需值被取 得,發泡室壓力及發泡室溫度被監視並比較於所需值及作 調整。 壓力控制副程式1 66包含用以控制室3〇中壓力之程 式碼’其係藉由調節於室排氣系統中之節流閥開口之大小 加以進行。節流閥之孔徑大小係被設定以控制室壓力於一 相對於總處理氣體流量,處理室之大小及用於排氣系統之 第23頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) (請先閱讀背面之注意事項-Ordered the printing of the consumer cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs to make the subprograms of room components execute. / The operation of the specific chamber component subroutine in Fig. 1F will be explained by referring to Fig. 1A. Substrate positioning subroutine} Contains control to π pieces < hard code, which is used to load the substrate to the bracket W, and optionally, pick up the substrate to Dang-zhong < want two degrees' to control at Substrate and air jet; member 4〇 ^ 心 间 1 ^. When a substrate is loaded into a process 1:30, the heater assembly 33 is lowered to receive the substrate in the wafer bag 34, and then raised to a desired height. In operation, the substrate positioning subroutine 164 controls the actions of the carriage 32 in response to the parameters of the processing group related to the support height transmitted by the emperor & brake program 1 63b. Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs. The processing gas control subroutine 165 has code for controlling the composition and flow rate of the processing gas. Process gas control subroutine 丨 65 Controls the on / off position of the safety valve, and simultaneously raises / lowers the mass flow controller to obtain the desired gas flow rate. The process gas control subroutine 丨 6 5 is evoked by the room management subroutine ^ 6 3 b and all the room component subroutines. Subroutine 165 receives processing parameters from a chamber management subroutine related to the desired gas flow rate. Typically, the process gas control sub-private type 1 65 is operated by opening the gas supply line, and repeatedly buying the required mass flow controller, (ii) comparing the reading with the thought received from the room management sub-program 163b. The flow rate, and (iii) adjust the flow rate of the gas supply line when necessary. Furthermore, the process gas control subroutine 63 includes the steps of monitoring the gas flow rate of an unsafe flow rate, and actuating a safety valve when an unsafe condition is detected. The process gas control subroutine 丨 65 also depends on the selected process (cleaning or deposition or other), and controls the gas composition and flow rate to remove the gas and deposition gas. Other embodiments can be more than one page 22. This paper size is applicable to Chinese National Standard (CNS) A4 specification (210X297 mm) 5. The invention specification printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs () species-process gas control subroutine Each subroutine controls a specific type of process or a specific group of gas lines. In the second treatment, an inert gas system such as nitrogen or argon flows into the chamber to stabilize the pressure in the chamber before the processing gas is introduced into the chamber. For these processes, the process gas control routine 165 is planned to include steps such as: let inert gas flow into the chamber for a period of time to stabilize the pressure in the chamber, and then perform a later step. In addition, when a process gas system is vaporized from a liquid precursor, such as TlCl4, the process gas control subroutine 165 will be written to include the step of foaming a transfer gas, such as t, through a foaming module. A liquid precursor, or the introduction of a carrier gas, such as &, helium into a liquid is pressed into the system. When a foaming chamber is used for this type of processing, the processing gas control subroutine 165 adjusts the flow rate of the conveying gas, the pressure in the foaming chamber, and the temperature of the foaming krypton to obtain the flow rate for the desired processing gas. As described above, the desired process gas flow rate is transmitted to the process gas control routine as a process parameter. Further, the process gas control subroutine 165 includes steps' to obtain a desired transfer gas flow rate, a pressure of the foaming chamber, and a temperature of the foaming chamber for the desired gas flow rate. A storage table of the values required for the known process gas flow rate. Once the required values are obtained, the pressure and temperature of the foaming chamber are monitored and compared to the desired value and adjusted. The pressure control subroutine 1 66 contains a program code for controlling the pressure in the chamber 30, which is performed by adjusting the size of the throttle valve opening in the chamber exhaust system. The orifice size of the throttle valve is set to control the pressure of the chamber relative to the total processing gas flow, the size of the processing chamber and the exhaust system. Page 23 This paper applies Chinese National Standard (CNS) A4 specifications (210X297) Mm) (Please read the notes on the back first
訂 A7 --— B7__ 五、發明説明() ~-- 抽氣汉疋點壓力之想要位準。當壓力控制副程式i 66被唤 I時,想要或目標壓力位準係被接收為來自室管理副程式 163b之參數。壓力控制副程式166量測於室3〇中之壓力, 藉由讀取連接至該室之一或多數傳統壓力表,比較量測值 與目標壓力,取得比例積分微分(piD)值,並依據獲得自壓 力表之PID值,來調整節流閥。另一方面,壓力控制副程 式1 6 6可以開啟或關閉節流閥孔徑至一特定開口大小,以 調節室30中之壓力至一想要之壓力或壓力範圍。 加熱器控制副程式167包含用以控制加熱器線圈33 之溫度,用以電阻性加熱托架32(及其上之基板)。加熱器 控制副程式係同時被室管理器副程式所唤起並接收一目 “或設定點溫度參數。加熱器控制副程式藉由量測位於托 架3 2中之熱電耦之電壓輸出加以量測溫度,比較量測溫 度與纟又疋點溫度並增加或減少施加至加熱單元之電流,以 取得設定點溫度。溫度係藉由查看於儲存轉換表中之相對 溫度而量測電壓取得,或者,藉由使用一四階多項式來計 算溫度。當一内藏環係用以加熱托架3 2時,加熱控制副 程式1 67逐漸地控制施加至該環之電流之上升/下降。另 外,可以包含一内建故障安全模式,以用以檢測處理安全 要求,並可以於處理室30未適當設定時,關閉加熱單元 之操作。於加熱器控制之另一種方法係用以一升溫控制演 繹法,其係描述於申請於1 996年十二月1 3日以強納森法 蘭克為發明人之第08/746,657號之"用以控制氣相沉積設 備之溫度之系統與方法"案中,該案於此係併入作為參 第24頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) (請先閱讀背面之注意事 丨-- 項寫本頁) 訂 經濟部中央標準局員工消費合作社印製 5U/Un A7 B7 五、發明説明( 考 經濟部中央標準局員工消費合作社印裝 、-電漿控制副程式168包含程式碼,其係用以設定被 施加至罜30中之處理電極中之低及高頻射頻功率位準, 以及用以⑵疋所使用I低射頻。如同於先前所述之室元件 副程式二電漿控制副程式168係被室管理副程式16补所 喚起員犯例中包含一遠端電漿產生器4,電漿控制副程 式168將同時用以控制遠端電椠產生器之程式碼。 上述之CVD系統之其他細節係被說明於共同申請於 1997年八月22日之美國專利申請號〇8/918,7〇6號,被命 名為用以/儿積鈦層之高溫,高沉積速率處理及設備,,,其 於此係併人作為參考。然而,上述之反應器說明只是為了 說明目的,其他之CVD電漿設備,例如電子環繞共振式 (ECR)電裝CVD裝置,電感耦式RF高密度電漿CVD裝置 等可以被使用。另外,上述系統之變化,例如於托架設計, 加熱設計,抽氣通道,RF電力連接位置及其他之變化也 是有可能的。依據本發明所形成鈦層之方法並不限定於任 何之特定CVD設備中。 III·一改變CVD鈦製程 本發明之方法可以使用以沉積改良鈦薄膜於基板處 理室中’例如上述之例示室中。如上所述,鈇薄膜於現行 積體電路製程中有若干用途。鈦薄膜之主要用途之一是作 為於鈦/氮化鈦堆疊中作為一啟始黏著層,其係為接觸結構 之一部份。此一接觸結構係被示於第2A圖,其係為一例 第25頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) (請先閱讀背面之注意事項Order A7 --- B7__ V. Description of the invention () ~ --- The desired level of the pressure of the pumping Han. When the pressure control subroutine i 66 is called I, the desired or target pressure level is received as a parameter from the room management subroutine 163b. The pressure control subroutine 166 measures the pressure in the chamber 30. By reading one or most of the traditional pressure gauges connected to the chamber, the measured value is compared with the target pressure, and the proportional integral derivative (piD) value is obtained. Obtain the PID value from the pressure gauge to adjust the throttle. On the other hand, the pressure control sub-mode 1 6 6 can open or close the throttle valve aperture to a specific opening size to adjust the pressure in the chamber 30 to a desired pressure or pressure range. The heater control routine 167 includes a temperature for controlling the heater coil 33 for resistively heating the bracket 32 (and the substrate thereon). The heater control subroutine is simultaneously evoked by the room manager subroutine and receives a “or set-point temperature parameter. The heater control subroutine measures temperature by measuring the voltage output of the thermocouple located in the bracket 32 Compare the measured temperature with the temperature at the 纟 and 疋 points and increase or decrease the current applied to the heating unit to obtain the set point temperature. The temperature is obtained by measuring the voltage by looking at the relative temperature in the storage conversion table, or by The temperature is calculated by using a fourth-order polynomial. When a built-in ring is used to heat the cradle 32, the heating control subroutine 1 67 gradually controls the rise / fall of the current applied to the ring. In addition, a Built-in fail-safe mode to detect processing safety requirements, and to turn off the operation of the heating unit when the processing chamber 30 is not properly set. Another method for controlling heaters is to use a temperature control deduction method, which is Described in Application No. 08 / 746,657 No. 08 / 746,657 with Jonathan Frank as inventor on December 13th, 996 " System for controlling temperature of vapor deposition equipment In the "Method" case, the case is incorporated here as a reference on page 24. The paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm) (please read the precautions on the back 丨 --- item to write this page) ) Order 5U / Un A7 B7 printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs. 5. Description of the invention (examine the printing of the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economics.-Plasma control subroutine 168 contains code, which is used to set The low and high-frequency RF power levels applied to the processing electrodes in the , 30 and the low-frequency I used to control the use. As described in the chamber component subroutine two plasma control subroutine 168 is described previously. The room management subroutine 16 complements the aroused criminal's case and includes a remote plasma generator 4. The plasma control subroutine 168 will also be used to control the code of the remote plasma generator. Other details of the above CVD system It is described in U.S. Patent Application No. 08 / 918,708, co-filed on August 22, 1997, and is named as a high temperature, high deposition rate treatment and equipment for depositing titanium layers. It is hereby incorporated by reference. However, the above reactor description is only for the purpose of explanation, other CVD plasma equipments, such as electronic surround resonance (ECR) electrical CVD equipment, inductively coupled RF high-density plasma CVD equipment, etc. can be used. In addition, the above System changes, such as bracket design, heating design, exhaust channel, RF power connection position and other changes are also possible. The method of forming a titanium layer according to the present invention is not limited to any particular CVD equipment. III. A Change in CVD Titanium Process The method of the present invention can be used to deposit a modified titanium film in a substrate processing chamber, such as the example chamber described above. As mentioned above, the rhenium film has several uses in current integrated circuit manufacturing processes. One of the main uses of the titanium film is as an initial adhesion layer in a titanium / titanium nitride stack, which is part of the contact structure. This contact structure is shown in Figure 2A, which is an example. Page 25 This paper size applies the Chinese National Standard (CNS) A4 specification (210X297 mm) (Please read the precautions on the back first)
本頁) 訂· 經濟部中央樣準局員工消費合作社印製 、發明説明( 示接觸結構之剖面圖,該結構中可以採用本發明之實施 例。 如於第2A圖中所示,一氧化層2〇〇(例如—Si〇x薄膜) 係沉積於基板205上至約!微米之厚度,該基板具有結晶 矽或多矽表面。氧化物層200可以作為於一積體電路中之 預金屬介電層或層間介電層。為了提供於層間之電氣接 觸,一接觸孔21〇係蝕刻穿過氧化物層2〇〇,並被填以例 如鋁之金屬。 於很多先進積體電路中,接觸孔21〇是很窄的,經常 是窄於0·35微米寬,並具有約6:1或更大之深寬比;補 此一孔是困難的,但一些標準製程已經被開發出來,其中 孔210係首先被保角地塗覆以一鈦層215。鈦(丁〇層 &後祓怎角地塗覆以一氮化鈦(TiN)層22〇。隨後―鋁層 225經常藉由物理氣相沉積加以沉積,以填滿接觸孔^ 並提供電氣連線於該上層。鈦層215提供一黏著層給在下 之矽層及在側壁上之氧化物層。同時,其可以以層之 矽加以矽化,以形成歐姆接觸。TiN層22〇良好地結 Ti層215,及錯層225良好濕潤至TiN,使得銘可=佳 地填滿接觸孔2 1 0,而不會形成有空隙。同時,芦22 作動為一擴散阻障層,其防止鋁225遷移入於《丄 八哕2〇5中並造 成其導電。 為了適當執行此目的’飲層215相較於其他特性中, 必須具有優良之底覆蓋性,低電阻率,均匀泰 电阻率及均句 沉積厚度於整個日曰圓(中間及/邊緣)之接觸 > 〆、 版邵。同時, (請先閱讀背面之注意事項再ml本頁) •n· VH·This page) Printed and printed by the Consumer Cooperatives of the Central Prototype Bureau of the Ministry of Economic Affairs, and a description of the invention (shows a cross-sectional view of a contact structure in which an embodiment of the invention can be used. As shown in Figure 2A, an oxide layer 200 (for example, SiOx thin film) is deposited on a substrate 205 to a thickness of about 100 microns, the substrate has a crystalline silicon or polysilicon surface. The oxide layer 200 can be used as a pre-metallic interposer in an integrated circuit Electrical layer or interlayer dielectric layer. In order to provide electrical contact between the layers, a contact hole 210 is etched through the oxide layer 200 and filled with a metal such as aluminum. In many advanced integrated circuits, contact The hole 21 is very narrow, often narrower than 0.35 micron wide, and has an aspect ratio of about 6: 1 or greater; it is difficult to fill this hole, but some standard processes have been developed, among which The hole 210 is firstly conformally coated with a titanium layer 215. Titanium (but 0 layer & later is coated with a titanium nitride (TiN) layer 22 °. Then-the aluminum layer 225 is often subjected to physical gas Phase deposition and deposition to fill the contact holes ^ and provide electrical connections to Upper layer. The titanium layer 215 provides an adhesive layer for the underlying silicon layer and the oxide layer on the side wall. At the same time, it can be siliconized with a layer of silicon to form an ohmic contact. The TiN layer 22 is well bonded to the Ti layer 215, And the interlayer 225 is well wetted to TiN, so that Ming Ke = fills the contact hole 2 1 0 without forming voids. At the same time, Lu 22 acts as a diffusion barrier layer, which prevents aluminum 225 from migrating into the " In order to properly perform this purpose, the drinking layer 215 must have excellent underlayability, low resistivity, uniform Thai resistivity, and uniform deposition thickness compared to other characteristics. The contact of the entire Japanese circle (middle and / edge) > 〆, ver. Shao. At the same time, (please read the precautions on the back first, then this page) • n · VH ·
nf HH i nn ·nf HH i nn
本紙張尺度適用中國國家標準(CNS ) Α4規格(210Χ297公釐) A7 B7 經濟部中央標準局員工消費合作社印製 五、發明説明( 較佳地,鈦層215均勻地沿著接觸21〇之底部沉積,但並 不沿著側壁沉積。防止鈇沉積於側壁上,防止所謂之”砍 蔓延”之現象,其中’ |自接觸區切與側壁中切作反 應j並被由接觸底部傳送至侧壁。依據本發明之方法所沉 積之鈦層相較於先前技藝之鈦沉積製程,符合了這些持性 並展現了相當之改良於底部覆蓋性及片電阻均勻性。這些 改良係藉由#主鈥材料沉積步驟前後加以新顆及獨特步 驟而完成。 k些步驟《-是-均勻及特有電聚處理步冑,其係被 執行於鈥沉積步驟之前。於此電漿處理步驟中,晶圓係受 到一相當短暫之(於較佳實施例係約5至6〇秒)由^及& 處理氣體所形漿。於此方《中,晶圓之上表面之小 部份係被於沉積步驟前被蝕刻掉。發明人已經發現此蝕刻 步驟係特別有用於⑴當接觸孔21G形成後,除去已經長於 晶圓之接觸區中之任何氧化物(8丨〇〇,及(2)由層2〇〇除去 於孔形成(蝕刻)步驟後,不經意留於接觸孔2丨〇中之任何 氧化矽。右晶圓於形成接觸前,係曝露於大氣若干時間, 則於1 0 · 5 0埃厚之氧化物之形成係非常普通的。同時,發 明人也注意到很多商用製程並未完全地蝕刻去層2〇〇,相 反地係留下一層薄未姓刻氧化梦層於接觸區上。此一層係 示於第2B圖中之層230,並可以是1〇〇至250埃厚或更 厚,這是取決於該製程而定。 取決於此未蝕刻層230或任何建於晶圓上氧化層之 厚度,當鈥層215被沉積時?該層可以防止電氣接觸至在 第27頁 各紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) (锖先閱讀背面之注意事項再 1P:本貰) 訂 507015 經濟部中央標準局員工消費合作社印製 五 '發明説明( 故障將降低整個製程之^ 猎以造成部份故障,該 建氧化層是到達-厚度,:厚::他::中’…内 許對在下層切作電氣接觸心了二電阻位準時,允 合製造者之性能需求。於 斤:造之元件不能符 驟可以被用以敍刻所有或部;中’本發明之預處理步 /Γ , ^ < 剩餘層2 物,而能改良對基板2〇〇之 丨内建乳化 係參考第3圖加以詳述。讀觸。本發明之其他細節 第3圖是一流程圖,其、 佳f 、I I 、 Μ用以沉積依據本發明之較 ::施: 可以了解的是,示於第3圖之步驟只 較佳製程,同時,本發明之其他實施例也可以運用 :…示步驟或者改變步驟之形式或順序。如於第3圖 广’於沉積一飲層之前,可以開始-晶圓被加載至室3。 (步驟利’以及,處理機85設定現行晶圓計數(I·用 以如下所述之清洗目的)為U步驟3〇5)。於晶圓被加載入 至後,其被移動至一處理位置’纟中托架32係大致離開 配氣嘴頭則250至500密耳之間。於特定及較佳實施 例中,托架32係定位離開噴氣頭4〇有329密耳。於此日 圓定位步驟中’室係被加壓以一非腐姓性氣體,例如氬θ: 於高於發生沉積之壓力。氬將填滿於室中之空隙或空間, 特別是於加熱托架之内部,使得當室壓被降低至沉積壓力 (於特定壓力為5托耳)時’其將出氣。於此方式中,步费 31〇減少了處理氣體之内侵,其可能腐蝕或氧化加熱器托 架或至之部份。風壓力氣係流動成為經由喷氣頭4〇之上 (請先閱讀背面之注意事項本頁) I —.......- 本 -訂 第28頁 本紙張尺度適用中國國家標準(CNS )厶姑1格(210Χ297公釐 • I—----- In ϋ9This paper size applies to Chinese National Standard (CNS) A4 specifications (210 × 297 mm) A7 B7 Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention (preferably, the titanium layer 215 is evenly along the bottom contacting 21 ° Deposition, but not along the side wall. To prevent the plutonium from being deposited on the side wall, to prevent the so-called "chopping and spreading" phenomenon, in which the cut from the contact area and the side wall react to j and are transferred from the bottom of the contact to the side wall Compared with the titanium deposition process of the prior art, the titanium layer deposited according to the method of the present invention conforms to these persistences and shows considerable improvements in bottom coverage and sheet resistance uniformity. These improvements are achieved by # 主 ″ The material deposition step is completed by adding new particles and unique steps. Some steps "-yes-uniform and unique electropolymerization processing steps, which are performed before the" deposition step. "In this plasma processing step, the wafer system A relatively short period (about 5 to 60 seconds in the preferred embodiment) of ^ and & processing gas slurry. In this method, a small portion of the upper surface of the wafer is used in the deposition step. before It is etched away. The inventor has found that this etching step is particularly useful for removing any oxides (8), (2) from the contact area of the wafer that have been longer than the contact area after the contact hole 21G is formed. 〇 Remove any silicon oxide left in the contact hole 2 丨 0 after the hole formation (etching) step. The right wafer is exposed to the atmosphere for a certain period of time before the contact is formed. The formation of oxides is very common. At the same time, the inventors have also noticed that many commercial processes do not completely etch away the layer 200, but instead leave a thin oxide oxide layer on the contact area. This layer is The layer 230 shown in FIG. 2B may be 100 to 250 Angstroms or more, depending on the process. Depending on the unetched layer 230 or any oxide layer built on the wafer Thickness when “Layer 215 is deposited? This layer can prevent electrical contact to the Chinese paper standard (CNS) A4 specification (210X297 mm) for each paper size on page 27. (Please read the precautions on the back before 1P: this贳) Set 507015 Central Standard of the Ministry of Economic Affairs Employee Consumer Cooperative printed five 'invention description (faults will reduce the whole process ^ hunting to cause some failures, the build oxide layer is reach-thickness,: thickness :: he :: medium' ... cut in the lower layer The electrical contact is at the level of the two resistors, which meets the performance requirements of the manufacturer. Yu Jin: The components can not be used to describe all or parts of the step; in the preprocessing step of the present invention / Γ, ^ < The remaining layer 2 can be improved, and the built-in emulsification system of the substrate 2000 can be described in detail with reference to Fig. 3. Read the touch. Other details of the present invention. Fig. 3 is a flow chart, which, f, II, M is used to deposit the comparison according to the present invention :: Apply: It can be understood that the steps shown in FIG. 3 are only preferred processes. At the same time, other embodiments of the present invention can also be used: ... show the steps or change the form of the steps Or order. As shown in Figure 3, before a layer is deposited, the wafer can be loaded into the chamber 3. (Step S ') and the processor 85 sets the current wafer count (I. for cleaning purposes as described below) to step S305. After the wafer is loaded into the wafer, it is moved to a processing position ', and the bracket 32 is approximately 250 to 500 mils away from the valve head. In a specific and preferred embodiment, the cradle 32 is positioned 329 mils away from the jet 40. During the yen positioning step, the chamber is pressurized with a non-corrosive gas, such as argon θ: above the pressure at which deposition occurs. Argon will fill the voids or spaces in the chamber, especially inside the heating bracket, so that when the chamber pressure is reduced to the deposition pressure (at a specific pressure of 5 Torr), it will outgas. In this way, the step cost is reduced by 30%, which may corrode or oxidize the heater bracket or parts. Wind pressure and air flow through the air jet head 40 (please read the note on the back page first) I —.......- This-page page 28 This paper applies the Chinese National Standard (CNS)厶 姑 1 block (210 × 297 mm • I —----- In ϋ9
III i三|一一 I 經濟部中央標準局員工消費合作社印製 507015 A7 B7 五、發明説明() 氬氣流及成為由晶圓3 6下一點流動之下氬氣流。較佳地, 於此步驟中,室壓係被設定至於5 · 9 0托耳之間。 同時,於步驟310中,托架溫度也被設定至於實際處 理溫度之土 15°C之間,該處理可以執行於400至7501間 之任何溫度,但於特定實施例中,較佳地托架溫度係設定 於約63 0-7 0 0°C之間(相當於約535至635。(:之晶圓溫度), 更好是約680°C (相當於約6051之晶圓溫度)。於一特定實 施例中,於步騾310中,溫度係被啟始設定至約690°C (10 Ci%於處理溫度),因為當處理氣體開始流動時,其將冷 卻加熱器及晶圓。啟始加熱晶圓於處理溫度上時,導致較 短晶圓周期時間並降低對加熱器由加熱元件及加熱表面 間熱梯度上升之熱陡震’該熱陡震於加熱器功率增加時會 上升,而使得於氣體流開始時加熱器回升處理溫度。 於步驟3 1 0啟始後約1 0秒,溫度係被降低至實際處 理溫度(其係然後較佳被保持於整個沉積處理中),一反應 氣體(較佳HO流係被導通於一啟始流量,及上氬氣流速增 加(步驟315)。反應氣體降低所需以分解(隨後引入)源氣體 之能量,以形成想要薄膜並同時降低沉積副產物之腐蝕 f生’藉由轉換部份之氯成為氯化氫(HCL)而不將其留下成 為C1或Ch。氣體流係然後於步驟320中增加2秒,於步 蘇3 2 5中增加3秒。氣體之流速係被以步階方式增加(或 者斜向增加)於步驟310至325中,由一啟始至一最終流 速’以降低對加熱器之熱陡震·,氣體之最終流速係相當地 南並若被一次導通時將不當地冷卻晶圓。該氣體之步階或 --' 第29貫 本紙張;Clit用巾gj國家標準(⑽〉Μ胁(2似二公楚) (請先閲讀背面之注意事項本頁) 本 訂 ^07015 五、發明説明() 斜向增加對於例如氦或氫之氣體係特別重要,因為這些氣 體展現高度熱轉移特性。 於下一步驟325 m面討論到之電浆預處理。於 電漿預處理步驟中,低頻(例如300至45〇KHz,最好是 350KHZ)射頻能量係被施加至噴氣頭4〇,以由&及氬處 理氣體形成電漿。如上所討論,於接觸孔21〇形成後,或 保留有未蚀刻層230於接觸孔210後,電聚係整個或部份 地姓刻掉長於基板200上之薄氧化層,因此,完成對基板 2〇〇之改良電氣接觸。吾人相信此蝕刻處理可以由基本化 學反應式:Si〇2 + H2— Si^ + hO所代表,其中,珍燒(siH4) 及水(H2〇)均由室中排出。f然’相信會發生其他中間反 應’以及,排出化合物包含來自這些中間反應之離子及其 他分子β 也可能使用被稱為預處理氣體之其他氣體於步驟32〇 中,以蝕刻掉建立之氧化物或所留下之氧化矽。預處理氣 體應展現一高蝕刻選擇性於氧化矽及矽基板之間,使得其 可以蝕刻氧化物或留下氧化物,而不會破壞矽接觸區域。 可以用於步騾320中之其他預處理氣體包含氨(ΝΗ3)及各 種用以蝕刻氧化矽心鹵素種類。含氟氟氣體(例如chF3, CF4,QF6 ’ BF3,NH3等)被認為為較佳齒素種類,而含碘 源係較差的,因為多數碘源於室溫時為固態,並很難用。 同時,含溴種類係較優於含氯種類,因為溴氣體對隨後沉 積處理具有較低之影響。任一預處理氣體可以混合以一載 氣或另一惰性氣體,以協助電漿及所得蝕刻處理之穩定。 第30頁 (請先閲讀背面之注意事項III i three | one one I Printed by the Consumer Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs 507015 A7 B7 V. Description of the invention () Argon gas flow and argon gas flow under the point of the wafer 36. Preferably, in this step, the chamber pressure system is set to between 5.90 Torr. At the same time, in step 310, the temperature of the bracket is also set to 15 ° C, which is the actual processing temperature. The processing can be performed at any temperature between 400 and 7501, but in certain embodiments, the bracket is preferably The temperature is set between approximately 63 0-7 0 ° C (equivalent to approximately 535 to 635. (: wafer temperature), more preferably approximately 680 ° C (equivalent to wafer temperature of approximately 6051). In a specific embodiment, in step 310, the temperature is initially set to about 690 ° C (10 Ci% at the processing temperature), because when the process gas begins to flow, it will cool the heater and wafer. When the wafer is initially heated at the processing temperature, it results in a shorter wafer cycle time and reduces the thermal shock of the thermal gradient between the heating element and the heating surface of the heater. The thermal shock will increase when the heater power increases. The temperature of the heater is raised at the beginning of the gas flow. About 10 seconds after the start of step 3 10, the temperature is reduced to the actual processing temperature (which is then preferably maintained throughout the deposition process). The reaction gas (preferably the HO flow system is conducted at an initial flow, The upper argon gas flow rate is increased (step 315). The reaction gas is reduced to decompose (subsequently introduced) the energy of the source gas to form the desired film and at the same time reduce the corrosion of the deposition by-products. Hydrogen chloride (HCL) without leaving it as C1 or Ch. The gas flow is then increased by 2 seconds in step 320 and 3 seconds in step 3 2 5. The flow rate of the gas is increased in steps (or Increasing obliquely) In steps 310 to 325, from a start to a final flow rate 'to reduce the thermal shock to the heater. The final flow rate of the gas is quite south and will be improperly cooled if it is turned on once. The step of the gas or-'29th paper; Clit gj national standard (⑽> Μ 胁 (2 like Ergongchu) (Please read the precautions on the back page first) This order ^ 07015 V. Description of the invention () Inclined increase is particularly important for gas systems such as helium or hydrogen, because these gases exhibit high heat transfer characteristics. Plasma pretreatment discussed in the next step 325 m. In the plasma pretreatment step Medium and low frequencies (for example, 300 to 45 KHz Preferably 350KHZ) RF energy is applied to the jet head 40 to form a plasma from & and argon processing gas. As discussed above, after the contact hole 21 is formed, an unetched layer 230 remains in the contact hole. After 210, the electropolymerization system engraved the thin oxide layer on the substrate 200 in whole or in part. Therefore, the improved electrical contact with the substrate 200 was completed. I believe that this etching process can be based on the basic chemical reaction formula: Si. 2 + H2—Si ^ + hO is represented, in which both sintering (siH4) and water (H2〇) are discharged from the chamber. However, 'believe that other intermediate reactions will occur' and that the discharged compounds include those from these intermediate reactions. Ions and other molecules β may also use other gases called pretreatment gases in step 32 to etch away the built-up oxide or the silicon oxide left behind. The pretreatment gas should exhibit a high etch selectivity between silicon oxide and the silicon substrate, so that it can etch oxides or leave oxides without damaging the silicon contact area. Other pre-treatment gases that can be used in step 320 include ammonia (N3) and various halogen species used to etch silicon oxide cores. Fluorine-containing fluorine gas (such as chF3, CF4, QF6 'BF3, NH3, etc.) is considered to be a better type of tooth element, while iodine-containing sources are poor because most iodine sources are solid at room temperature and difficult to use. At the same time, bromine-containing species are better than chlorine-containing species because bromine gas has a lower effect on subsequent deposition treatment. Either pretreatment gas can be mixed with a carrier gas or another inert gas to assist in the stabilization of the plasma and the resulting etching process. Page 30 (Please read the notes on the back first
-訂 經濟部中央標準局員工消費合作社印製 丄:) 五、發明説明( 經濟部中央標準局員工消費合作社印製-Order Printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 丄 :) V. Invention Description (Printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs
TiCl4(源氣體备、士 J及虱流量係同時於步驟325中被啟始。 然而,相反於此睡3丨 二 守?1入這些流量入室3 〇中,這些流量係 被分散至預抽管道。t、,,、 以此方式轉向此等流量,特別是 TlCU ’允許了流量能於沉積開始前穩定化,因而,改良了 於一多晶圓沉積程序(例如2000晶圓生產線)中各種欽沉 積步驟間,處理條件之均勻⑯。或者,TiCl4及氦流量可 以於電漿開始為各別步冑33〇之部份後開始。其中,較佳 地,於開始沉積步驟335前,Ticu流量被穩定於至少6_ 8秒。 於沉積步驟335中,Tic。及氦氣流量係被再導入沿 著氬及氫流而流入室3〇,電漿係被藉由持續施加rf功率 至噴氣頭40,而被維持。於混合氦載氣前,Tic“是於液 態形式,並使用例如由STEC公司所製造之氣體面板精密 液體注射系統(GPUS)液態注射系統。如於表!所示,於 較佳實施例中,H2對TiC“之比例是106:1。該比率可以 藉由轉換於表中之TiCU之mgm流速至其相當sccm流速 而為熟習於本技藝者所完成。於此例子中,TiCι4係以 400mg/m之速率被引入,其係相當於47 23sccm之氣體流 速。 只要需要以沉積一選定厚度,沉積步驟335係被維 持。因為高沉積溫度,增加之氣體流速及其他因素,所以 本發明之鈦薄膜係被以至少100埃每分鐘至約4〇〇埃或更 高每分之沉積速率。因此,步騾335之整個時間係一般低 於先前技藝處理所需者,其隨造成於晶圓產出量之增加。 第31頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) (請先閲讀背面之注意事項The TiCl4 (source gas backup, JJ, and lice flow rates are started simultaneously in step 325. However, instead of sleeping here, 3 二 2 guards? 1 into these flows into the chamber 30, these flows are dispersed into the pre-pumping pipeline .T ,,,, and in this way shift to these flows, in particular TlCU 'allows the flow to stabilize before the start of the deposition, thus improving various factors in a multi-wafer deposition process (such as a 2000 wafer production line). During the deposition step, the treatment conditions are uniform. Alternatively, the TiCl4 and helium flow rates can be started after the plasma starts as a separate step of 33 °. Among them, preferably, the Ticu flow rate is Stable for at least 6-8 seconds. In the deposition step 335, Tic. And the helium gas flow are re-introduced into the chamber 30 along the argon and hydrogen flow, and the plasma system is continuously applied rf power to the jet head 40, It is maintained. Before mixing the helium carrier gas, Tic "is in liquid form and uses, for example, a gas panel precision liquid injection system (GPUS) liquid injection system manufactured by STEC. As shown in the table! In the example, H2 vs. TiC The ratio is 106: 1. This ratio can be accomplished by those skilled in the art by converting the mgm flow rate of TiCU in the table to its equivalent sccm flow rate. In this example, TiCι4 is used at a rate of 400mg / m. Introduced, it is equivalent to a gas flow rate of 47 to 23 sccm. The deposition step 335 is maintained as long as it is necessary to deposit a selected thickness. Because of the high deposition temperature, increased gas flow rate, and other factors, the titanium film of the present invention is at least A deposition rate of 100 angstroms per minute to about 400 angstroms or more per minute. Therefore, the overall time of step 335 is generally lower than that required for previous technology processes, which increases with the increase in wafer output. Page 31 This paper size applies Chinese National Standard (CNS) A4 (210X297mm) (Please read the precautions on the back first
本頁} 訂- 507015 A7 B7 五、發明説明( 經濟部中央標準局員工消費合作社印製 於沉積步驟335完成後,H2,TiCl4及氦流量被關閉, 及RF功率被大量地降低,及上氬流量被大量降低(步驟 3 40)以鬆開可能於沉積步驟已經形成於室上之大粒子。 为於3秒後,RF功率係被關閉,及鈦層被鈍化。鈦層係 藉由形成一薄層之氮化鈦於鈦層表面上加以鈍化,使得例 如反及氧之雜質不會被吸入鈦中。這些雜質可能改變鈦層 之私阻值並形成一不適合氮化鈦阻障層沉積之表面。鈍化 可以藉由加入仏及沁流於氬氣流成為鈍化步驟以5及/ 或形成氮電漿於步驟350中加以完成。較佳地,步驟345 及3 50被執仃。冑以此方式完成時,於後沉積電裝處理步 驟350前及由室洗淨Tic“殘餘前,步驟3牦穩定化該室。 同時’氮與鈦表面反應,以開始形成一氮化鈦薄層。 ▲於步驟345冑’鈦層係更進一步於步冑35〇藉由施加 RF施!至室中之η2/Ν2/Αγ純化氣體而加以純化,以形成 -電漿。鈍化電漿可以或者被形成於遠端電漿源中並被接 通至該室。於鈍化電漿中之離子化氮減層之表面反應, 而於約10秒之曝露期,完成氮化鈦薄層之形成。為了形 成電裝於室中,RF功率係大致地被施加至噴氣頭4〇。狹 功率可以施加至托架電極22或至托架電極”及 噴乳頭40。於較佳實施例中,其中步驟345及35〇被採用, 步驟345持續約8秒。於其他實施例中,只有步驟⑷或 只有步驟350被使用,這些步驟可以使用更久些,例如於 約1 0至3 〇秒之間。 於步驟350後’一第二電漿洗淨被執行,以更進一步 本紙張織用?iiiii ( CNS )观 (請先閱讀背面之注意事項This page} Order-507015 A7 B7 V. Description of the invention (printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs after the deposition step 335 is completed, the H2, TiCl4 and helium flows are turned off, and the RF power is greatly reduced, and argon is added The flow rate is greatly reduced (steps 3 to 40) to loosen large particles that may have been formed on the chamber during the deposition step. After 3 seconds, the RF power system was turned off and the titanium layer was passivated. The titanium layer was formed by forming a A thin layer of titanium nitride is passivated on the surface of the titanium layer, so that impurities such as oxygen are not absorbed into the titanium. These impurities may change the private resistance value of the titanium layer and form a layer that is not suitable for the deposition of a titanium nitride barrier layer. Surface. Passivation can be accomplished by adding krypton and argon flow into the argon stream to passivate steps 5 and / or forming a nitrogen plasma in step 350. Preferably, steps 345 and 3 50 are performed. 胄 In this way When completed, stabilize the chamber before step 350 of the post-deposition Denso processing step and before the Tic is cleaned from the chamber. Step 3 牦 At the same time, the nitrogen reacts with the titanium surface to start forming a thin layer of titanium nitride. ▲ 于Step 345 胄 'Titanium layer system goes one step further Step 35: Purify by applying RF to the η2 / N2 / Αγ purification gas in the chamber to form -plasma. Passivation plasma can be either formed in a remote plasma source and connected Pass to the chamber. The surface reaction of the ionized nitrogen reduction layer in the passivation plasma is completed, and the formation of a thin layer of titanium nitride is completed in an exposure period of about 10 seconds. In order to form the electrical equipment in the chamber, the RF power is roughly The ground is applied to the jet head 40. The narrow power can be applied to the carrier electrode 22 or to the carrier electrode "and the nipple 40. In a preferred embodiment, steps 345 and 35 are used, and step 345 lasts about 8 In other embodiments, only step ⑷ or only step 350 is used. These steps can be used longer, such as between about 10 to 30 seconds. After step 350, a second plasma wash is performed. Is implemented to further the use of this paper? Iiiii (CNS) view (Please read the precautions on the back first
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、發明説明( 經濟部中央標準局負工消費合作社印裝 :叙可能出現於室中之大粒子, 於電聚洗淨步驟34。,除了 2 355係類似 步驟355。最後,*步驟36。中::流係被維持 以及室係被抽真^ & 斤有乳體流係被關閉,、二及,然後,晶圓係被由當釦下f牟_ 365)。因為晶圓已經大致被純 了 (步驟 空氣中,而會有吸收… 斤以-圓可以被曝露至 長時間之曝霞S办" 哥η鈦層。因此,即使 特性H 玉乳,例如曝露幾天,並不會損壞鈥層之 後、#再者,氮化欽純化層提供一”清潔,,表面,其上,隨 理可以沉積一氮化鈇阻障層。於晶圓被拿下後,於 驟41〇)及處理機85增加晶圓計數 (步驟415)前,溫度係被設定至約68代。 除了於每一晶圓沉積後執行之電槳洗淨清洗步驟340 及3 55外,-乾燥清洗處理(其係不必開啟室蓋情形下完 成)係被週期地執行於室上,於若干晶圓沉積處理後,以 進步避免晶圓染。依據本發明,於此清洗處理中,並 ^有晶圓(例如一標片)於室中。該乾燥清洗處理-般係執 行於每"X"晶圓間,較佳係每2_3〇〇晶圓間。於一特定實 施例中,乾燥清洗可以執行於每3至5晶圓中。吾人想要 保持乾燥清洗處理有效,使得其不會大量地影響總系統晶 圓輸出。依據一特定實施例之較佳乾燥清洗處理係更詳細 說明如下。 再次參考第3圖,若Χ(其中例如χ = 3)晶圓已經被處 理(步驟370),該室係受到一乾燥清洗。首先,加熱器係 被移動離開噴氣頭約650密耳之距離(步騾375),並被保 第33貰 .紙張尺度適用中國國家標準(CNS ) Α4規格(210Χ297公着) (請先聞讀背面之注意事項本頁)2. Description of the invention (Printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs: large particles that may appear in the room are washed in step 34 of the electropolymerization, except that 2 355 is similar to step 355. Finally, * step 36. Medium ::: The flow system is maintained and the room system is pumped ^ & The breast flow system is closed, and the second, and then, the wafer system is deducted by Mou 365 (365). Because the wafer has been almost pure (in the air, there will be absorption ... 以 -circle can be exposed to long-term exposure Xia S " Ge η titanium layer. Therefore, even if the characteristics H jade milk, such as exposure After a few days, the layer will not be damaged. Furthermore, the Nitride purification layer provides a "clean," surface, on which a hafnium nitride barrier layer can be deposited. After the wafer is removed Before step 41) and the processor 85 increases the wafer count (step 415), the temperature is set to about 68 generations. In addition to the electric paddle cleaning and cleaning steps 340 and 3 55 performed after each wafer deposition -Dry cleaning process (which is completed without opening the chamber cover) is periodically performed on the chamber, and after a number of wafer deposition processes, the wafer is progressively avoided to prevent dyeing. According to the present invention, in this cleaning process, There is a wafer (for example, a target wafer) in the chamber. The dry cleaning process is generally performed between each "X" wafer, preferably every 2 to 300 wafers. In a specific embodiment Dry cleaning can be performed every 3 to 5 wafers. I want to keep dry cleaning Effective, so that it will not significantly affect the overall system wafer output. The preferred dry cleaning process according to a specific embodiment is explained in more detail below. Referring again to FIG. 3, if the X (for example, χ = 3) wafer has been After being processed (step 370), the chamber is subjected to a dry cleaning. First, the heater is moved away from the jet head by a distance of about 650 mils (step 375), and is guaranteed to be 33rd. The paper size applies the Chinese national standard (CNS) Α4 specification (210 × 297) (Please read this page first)
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* In tn 111 HI A7 B7 經濟部中央標準局員工消費合作社印製 五、發明説明() 持於680°c之處理溫度。於此時,氮或類似非反應氣體係 流入室中,及室係被保持於約O.i至1〇托耳之清洗壓力, 較佳係低於5托耳’於特定實施例係為〇·6托耳。這減少 了由加熱器至喷氣頭之熱流量,因此,相對於加熱器冷卻 噴氣頭。 於步騾375三秒後,氯氣(Ch)係以約25〇seem之流速 流入i中,及托架被提升至離開噴氣頭4〇有6〇〇密耳(步 驟380)。再者,兩秒後,一電漿係以約4〇〇瓦之功率碰撞 (步驟385)。該情況係被保持一段時間,以允許氯種類與 不要之沉積作反應並蝕刻由室元件來之沉積。來自沉積處 理之不想要沉積係一般為最厚,於室之最熱外露部份, 即,加熱器之上表面未被晶圓覆蓋之部份,或者未被流量 限制環所屏蔽之部份。藉由將加熱器移離開喷氣頭,上述 之條件確保了所有室元件之足夠清洗而不會有這些元 件,特別是噴氣頭之過蝕刻。 於這些因素中,步驟390之長度係取決於於室3〇内 之建立沉積之量而定,其然後取決於乾燥清洗間已經處理 過多少晶圓,以及,沉積處理長度(即,沉積於晶圓36上 之鈦薄膜之厚度)。於一特定實施例中,步驟390持續15 秒。或者’步驟390之長度可以使用一清洗點技術加以決 定。此等技術係為習知的並炮含光學端點檢測法及壓力為 主之端點檢測法。光學端點檢測法需要一石英或類似半透 明省於室30之壁中,供操作用,並於某些實施例中並不 是最好的,因為此一窗口對鈦沉積敏感,其與適當端點檢 _______第 34 貫_ 本紙張尺度適用中國國家標準(CNS ) A4規格(210 X297公釐) '"~ --- (請先閲讀背面之注意事項再IPr本頁}* In tn 111 HI A7 B7 Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs. 5. Description of the invention () Maintain the processing temperature at 680 ° c. At this time, nitrogen or a similar non-reactive gas system flows into the chamber, and the chamber system is maintained at a cleaning pressure of about 0 to 10 Torr, preferably less than 5 Torr. In certain embodiments, it is 0.6. Thing. This reduces the heat flow from the heater to the air head and therefore cools the air head relative to the heater. Three seconds after step 375, the chlorine gas (Ch) flowed into i at a flow rate of about 25 seem, and the carriage was lifted up to 600 mils from the jet head (step 380). Furthermore, two seconds later, a plasma system collided with about 400 watts of power (step 385). This condition is maintained for a period of time to allow the chlorine species to react with unwanted deposits and etch the deposits from the chamber elements. The unwanted deposition from the deposition process is generally the thickest, the hottest exposed part of the chamber, that is, the part of the upper surface of the heater that is not covered by the wafer, or the part that is not shielded by the flow restriction ring. By moving the heater away from the air jet head, the conditions described above ensure sufficient cleaning of all chamber components without these elements, especially the over-etching of the air jet head. Among these factors, the length of step 390 depends on the amount of deposition established within the chamber 30, which then depends on how many wafers have been processed in the dry clean room, and the length of the deposition process (i.e., deposited on the wafer) Thickness of titanium film on circle 36). In a particular embodiment, step 390 lasts 15 seconds. Alternatively, the length of 'step 390 can be determined using a cleaning point technique. These techniques are conventional and include optical endpoint detection and pressure-based endpoint detection. The optical endpoint detection method requires a quartz or similar translucency to be saved in the wall of the chamber 30 for operation, and is not optimal in some embodiments because this window is sensitive to titanium deposition, and it is compatible with the appropriate end Check _______ 34th _ This paper size applies Chinese National Standard (CNS) A4 (210 X297 mm) '" ~ --- (Please read the precautions on the back before IPr this page}
•訂• Order
507015 消 五、發明説明( :相衝九。同樣地’已知壓力為主端點檢測法係較不理。士為壓力為王端點檢測法必須個別地加以校正至 每至3〇⑼適當並精確地識別清洗步驟390之結束。 山因此,本案發明人已經發展出—種用於步驟州之新 的騎點檢測設計,其係基於所量剛到之反射Μ功率。該 端點檢測設計量測於整個清洗步驟390中,由室3〇所反 射至用於RF電源供給5(第1A圖)電源 ::::開:時’當沉積物由室壁㈣刻掉時,反2 ^ 反射功率之增加代表清洗電漿之密度增加,於 其併入來自由银刻過欽沉積之離子種類及能量分子時。 沉積材料由室壁㈣㈣,所㈣之反射功率於其開妒 降時到達一高學。這些觀測可以由第4圖中看到,該圖 於清洗步驟390中所量測得之反射功率對時間之函數, 及欽沉積步驟335之長度。如於第4圖所示之資料,代 -實施例,其中X=1,即其中室3〇於單一晶圓被處理後 受到一乾燥清洗處理。 當量測反射功率以_下降速率或更低時,室清洗處 完成。例如’於-實施例中,步驟携於所量測得之反 功率下降至〇瓦/秒之速率後,停止10秒。於步驟39〇 另一實施例中,當量測得之反射功率下降到達2瓦每秒 更少時,則停止。 於電漿清洗後,氯氣係被關閉及電聚電源被關閉, 帮390)。氮氣流係被保持約3秒,用以洗淨室。托架係 後回到約650密耳之間距(步,驟395)及底氬氣流係增加507015 V. Explanation of the invention (: Phase 9). Similarly, the known pressure detection method is more ignored. The pressure detection method must be individually adjusted to a value of 3 to 30. And accurately identify the end of the cleaning step 390. Therefore, the inventor of this case has developed a new riding point detection design for the step state, which is based on the amount of reflected M power that has just arrived. The endpoint detection design Measured during the entire cleaning step 390, reflected by the chamber 30 to the power supply for RF power supply 5 (Figure 1A) :::: on: When 'When the sediment is engraved from the chamber wall, the reverse 2 ^ The increase in the reflected power represents the increase in the density of the cleaning plasma, when it incorporates the ion species and energy molecules from the silver engraved deposits. The deposition material comes from the chamber wall, and the reflected power arrives when it is opened. A high school. These observations can be seen in Figure 4, which shows the reflected power as a function of time measured in the cleaning step 390 and the length of the deposition step 335. As shown in Figure 4 Data, Generation-Example, where X = 1, which means room 3〇 After a single wafer is processed, it is subjected to a dry cleaning process. When the reflected power is measured at a falling rate or lower, the cleaning of the chamber is completed. For example, in the '-embodiment, the steps carry the measured reverse power down. After the rate reaches 0 watts / second, stop for 10 seconds. In step 39, in another embodiment, when the measured reflected power drops to less than 2 watts per second, stop. After the plasma cleaning, the chlorine gas The system was shut down and the polycondensation power was turned off (Help 390). The nitrogen flow was maintained for about 3 seconds to clean the chamber. The bracket system then returned to a distance of about 650 mils (step, step 395) and the bottom argon gas system increased.
當 下 訂 以 表 理射 之或 (步 第35頁 本紙張中國國家標準(CNS )躺驗( 10 507015 A7 B7 經濟部中央標準局員工消費合作社印製 五、發明説明( / ’以洗淨室。最後’室係被抽氣約5秒(步驟4〇〇)。當 然,可以了解到"濕清洗"或預防維護清洗(發生於每幾百2 幾千處理晶圓間)可以藉由打開室蓋加以執行,以人工清 洗室之各種元件。 於晶圓沉積間執行週期性乾燥清洗減少了這些經常 很費時之濕預防維護之頻率,當然被認為増加了沉積處理 之效率並完成更高之沉積速率《再者,使用週期性乾燥清 洗處理改良了於整個晶圓生產線上之鈦沉積處理之重2 2。即,相較於未使前述之週期乾燥清洗之晶圓生產線而 言,於一例如約2000晶圓之晶圓生產線上,所沉積鈦層 於前十個晶圓之特性係更相似於所沉積於最後大個晶圓 之沉積層之特性。 本案發明人同時發現於TiCU流停止後(步驟340)留 於氣體管路中之液態TiC“干擾處理重覆性。即,當Ticu 流於步驟340中藉由關閉適當連接至該管路之流量控制閥 而停止時,部份之殘餘TiC“液態保留於管路中。本發明 人發現這些殘留液態量每一沉積處理均有所不同,及所殘 留之TiC“造成沉積不穩定,否則會負面影響沉積處理。 例如,因為殘留TiCU量變化時’對於任意兩個別基板, 流入室TiCl4量可能不同,最後造成多多少少之沉積於特 定基板上。同時,於其被傳送至室中之時,殘餘TiCl4可 能與於新基板中之濕氣反應’而形成T i 〇 2而造成不想要 之粒子。最後,於晶圓沉積步騾間,殘餘Ticl4可能淺露 入室中,並塗覆室或室元件之部份,因而改變了所塗覆部 第36頁 本紙張尺度適用中國國家標準(CNS)A4規格(2i〇x297公釐) (請先閲讀背面之注意事項再IPr本頁} -訂 五、發明説明( 份之顏色,這同時也改 又了至或70件邵份之發射係盤 表面之發射係數之改變 ’、數。於 其他特性。 又衣面 < 溫度或 為了克服此殘修ΤίΓΐ , 戈餘TiCU又不艮作用,發明人 一種新穎及獨特步驟,f π想出 艾驟茲步騾乾燥TiCl4氣體管路, 於乾燥清洗處理時,佶备$甘从泣γ 猎由 τ 使虱或其他惰性氣體源(一種不4 t 殘餘TiCl4反應之氣體 T m與 轧目豆)泥入m管路中。例如,於步 至395中,流量5〇〇sccm之氮可以被引入τ⑹4管路 以乾燥並洗淨管路中之殘餘Ticl4。於此方式中,本發明 2万法確保氣體管路於沉積每一晶圓前係於可再製狀 〜同時於洗淨TlC“管路後,所流入之氦是被發送至 /儿積至纟中,纟可以協助穩定乾燥清洗電聚。氨流係藉 由使用適當之閥及流量控制器,而流經Ticl4管路,這些 係如同熟習於本技藝者所知道的。 如第3圖所不之依據本發明之現行較佳實施例之氣體 流率’壓力位準及其他資訊係被揭示於以下之表丨(沉積處 理)及表2(清洗處理)。說明於表1及表2之氣體引入速率 係基於利用示於第3圖之處理,於一由應用材料公司所製 造之電阻加熱TixZ CVD室,該室係用於8吋晶圓。如同 熟習於本技藝者所知,於其他實施例中,若採用不同設計 及/或容積之其他室的話,則引入室之氣體實際流速會改 變0 第37頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) {請先閱讀背面之注意事項 丨tiT 本頁、 -訂 經濟部中央標準局員工消費合作社印製 507015 A7 B7 五、發明説明() 表 1 較佳CVD鈦製程 步驟 310 步驟 315 步驟 320 步驟 325 步騾 330 步驟 335 步驟 340 步驟 345 步騾 350 步驟 355 步驟 360 壓力; (托耳) 60 TFO 5 5 5 5 1.5 1.5 1.5 TFO TFO 間隔 (密耳) 329 329 329 329 329 329 329 329 329 329 329 RF 功率 (瓦) 0 0 0 900 900 900 50 0 600 50 0 氬 (底)· (seem) 500 500 500 500 500 500 500 500 500 500 0 氬(上) (seem) 2000 5000 7500 10000 10000 10000 500 500 500 500 0 h2 (seem) 0 1000 3000 5000 5000 5000 0 800 800 800 0 He (seem) 0 0 0 100 (分散) 100 (分散) 100 0 0 0 0 0 TiCl4 (mgm) 0 0 0 400 (分散) 400 (分散) 400 0 0 0 0 0 n2 (seem) 0 0 0 0 0 0 0 800 800 800 0 (請先閲讀背面之注意事 窝本頁) *TFO=節流閥全開The current order is based on the table or the step (page 35 of this paper Chinese National Standards (CNS) lying test (10 507015 A7 B7 printed by the Consumers 'Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs. 5. Description of the invention (/' to clean the room. Finally, the chamber system is evacuated for about 5 seconds (step 400). Of course, it can be learned that " wet cleaning " or preventive maintenance cleaning (which occurs every few hundred to several thousand processing wafers) can be opened by The chamber cover is implemented to manually clean the various components of the chamber. Performing periodic dry cleaning in the wafer deposition room reduces the frequency of these often time-consuming wet preventive maintenance, which is of course considered to increase the efficiency of the deposition process and complete higher Deposition rate "Further, the use of a periodic dry cleaning process improves the weight of the titanium deposition process on the entire wafer production line. 2 That is, compared to a wafer production line that does not have the aforementioned periodic dry cleaning process, For example, on a wafer production line of about 2000 wafers, the characteristics of the deposited titanium layer on the first ten wafers are more similar to the characteristics of the deposited layer on the last large wafer. The liquid TiC remaining in the gas pipeline after the TiCU flow is stopped (step 340) "interferes with the processing repeatability. That is, when the Ticu flow is stopped in step 340 by closing the flow control valve properly connected to the pipeline At the same time, part of the residual TiC "liquid state remains in the pipeline. The inventors found that the amount of these residual liquids varies with each deposition process, and the residual TiC" causes unstable deposition, otherwise it will negatively affect the deposition process. For example, when the amount of residual TiCU changes, 'for any two different substrates, the amount of TiCl4 flowing into the chamber may be different, resulting in more or less deposition on a specific substrate. At the same time, when it is transferred into the chamber, the residual TiCl4 may be Reacts with moisture in the new substrate to form T i 〇2 and cause unwanted particles. Finally, during the wafer deposition step, residual Ticl4 may be exposed into the chamber and coat the part of the chamber or chamber components Therefore, the page size of the coated part is changed. The paper size is applicable to Chinese National Standard (CNS) A4 specification (2i0x297 mm) (Please read the precautions on the back before IPr page}-Order V. Invention (The color of parts is also changed at the same time, or the change of the emission coefficient on the surface of the emission plate of 70 pieces of Shao ', number. In other characteristics. Also the surface < temperature or in order to overcome this residual repair ΤίΓΐ, Ge I TiCU has nothing to do with it. The inventor has a novel and unique step. F π came up with a step to dry the TiCl4 gas pipeline. During the dry cleaning process, prepare $ GAN from crying. An inert gas source (a gas T m that does not react with 4 t of residual TiCl4 and rolled beans) is sludged into the m pipeline. For example, in steps 395, nitrogen at a flow rate of 500 sccm can be introduced into the τ⑹4 pipeline to dry And wash the residual Ticl4 in the pipeline. In this way, the 20,000 method of the present invention ensures that the gas pipeline is in a reshape before depositing each wafer ~ At the same time, after the TlC "pipeline is cleaned, the inflowing helium is sent to / accumulated to 纟In addition, 纟 can help to stabilize and clean the electropolymer. The ammonia flow is through the Ticl4 pipeline by using appropriate valves and flow controllers. These are as known to those skilled in the art. As shown in Figure 3 The gas flow rate 'pressure level and other information according to the presently preferred embodiment of the present invention are disclosed in the following Tables (Deposition Treatment) and Table 2 (Cleaning Treatment). The gases described in Tables 1 and 2 The introduction rate is based on the use of the process shown in Figure 3, in a resistance-heated TixZ CVD chamber manufactured by Applied Materials, which is used for 8-inch wafers. As known to those skilled in the art, it is implemented in other implementations. For example, if other chambers with different designs and / or volumes are used, the actual flow rate of the gas introduced into the chamber will change. Page 37 This paper applies the Chinese National Standard (CNS) A4 specification (210X297 mm) {Please read first Notes on the back 丨 tiT Page,-Order printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs 507015 A7 B7 V. Description of the invention () Table 1 Preferred CVD titanium process steps 310 steps 315 steps 320 steps 325 steps 335 steps 340 steps 340 steps 345 steps 骡 350 Step 355 Step 360 Pressure; (Torr) 60 TFO 5 5 5 5 1.5 1.5 1.5 TFO TFO interval (mil) 329 329 329 329 329 329 329 329 329 329 329 329 RF power (W) 0 0 0 900 900 900 50 0 600 50 0 Argon (bottom) · (seem) 500 500 500 500 500 500 500 500 500 500 500 0 Argon (top) (seem) 2000 5000 7500 10000 10000 10000 500 500 500 500 0 h2 (seem) 0 1000 3000 5000 5000 5000 0 800 800 800 0 He (seem) 0 0 0 100 (dispersed) 100 (dispersed) 100 0 0 0 0 0 TiCl4 (mgm) 0 0 0 400 (dispersed) 400 (dispersed) 400 0 0 0 0 0 n2 (seem ) 0 0 0 0 0 0 0 800 800 800 0 (Please read the caution on the back page first) * TFO = Throttle valve fully open
訂 經濟部中央標準局員工消費合作社印製 第38頁 紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 507015 A7 B7 五、發明説明() 表 2 較佳CVD鈦清洗製程 步驟375 步驟380 |步驟385 步驟390 步驟395 旁驟400 壓力 (托耳) TFO 0.8 0.8 0.6 4 TFO 間隔 (密耳) 650 600 600 600 650 650 RF功率 (瓦) 0 0 400 0 0 0 氬(底) (seem) 200 200 200 200 500 0 氬(上) (seem) 0 0 0 0 0 0 h2 (seem) 0 0 0 0 0 0 He (seem) 500 (TiCl4管路 500 (TiCl4管路 500 (TiCl4管路 500 _4管路) 500 (丁汇14管勒 0 TiCl4 (mgm) 0 0 0 0 0 0 n2 (seem) 500 500 500 500 500 0 Cl2 (seem) 0 250 250 0 0 0 經濟部中央標隼局員工消費合作社印製 第39頁 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 507015 A7 B7 五、發明説明( 雖然,示於表1及表2之沉積條件及流速代表用於本 發明現行較佳實施例之流速,但可以知道也可以使用其他 沉積條件及其他流速。例如,有關於源及反應氣體於沉積 階段被引入之速率,發明人發現Η:至TiCU之比率應於約 64:1至2034:1之間。較佳比例取決於包含沉積溫度,壓 力托架間隔,RF功率位準及其他因素之其他沉積條件。 然而,本發明人發現上述之比例可以於較佳沉積條件下, 用以沉積良好品質之鈦薄膜,沉積條件包含加熱器溫度範 圍至少630至700°C之間,及沉積壓力範圍至少卜“托 耳。於某些特定測試中,良好品質之鈦薄膜係沉積於64:ι 之Hz/TiCl4比例,使用30〇〇sccm之Η!流量及4〇〇mg/叫相 當於 47.23SCCm)之 TiCl4 流速,及於 2034:1 之 H2/Ticl4 比 率,用12000sccm之h2流速及低至5〇mg/m(相等於5 之TiCl4流速。於H2/TiC“低於64:1之流速比時,反應變 得缺氧及不穩定,當流速比大於2 〇 3 4: i時,沉積薄膜開始 於接觸中展現不可接受之差底覆蓋率,並且,很困難管理 排氣。 IV ·測試結果及量測 為了示出本發明之功效,實驗係被以有本發明之方法 之優點及無本發明之方法所執行之鈦沉積層加以執行。實 驗係被執行於由應用材料公司所製造之電阻加熱Tixz室 中。TixZ罜係適用以200mm之晶圓並被位於同樣地是應 用材料公司所製造之Centura,多室基板處理系統中。 (請先閱讀背面之注意事項 —— 本頁 經濟部中央標準局員工消費合作社印製 507015 A7 ---—------- - B7 五、發明翻() " ~ - 、於這些組實驗之一中,各種預處理步驟(步驟325)係 於對具有氧切層沉積於其上之晶圓作欽沉積步驟前,被 加以執行。這些預處理步驟之第—步驟由氯(ms—,氮 (5〇〇SCCm)及氬(2〇()scem)處理氣體形成電漿。電漿係使用 4〇〇瓦之RF功率位準加以形成並於不同測試中,被保持 於40至1〇〇秒之間。測試結果顯示此步驟以約埃每秒 之速率钮刻氧化珍層,但姓刻並不十分均勾並除了氧切 外’也不可控制地及不可避免地蝕刻掉碎。 其他測試顯示來自Ch電漿預處理步驟之氯與後續鈦 沉積步驟相衝突。明白地說,吾人認為殘餘氯係負貴用以 減緩於步驟335中之鈦薄膜之沉積速率。同時,其也決定 所得之鈦層係較沒有CL電漿預處理步驟所沉積之鈦芦 均勻。 曰 經濟部中央標準局員工消費合作社印製 (請先閱讀背面之注意事本頁) 發明人同時依據本發明之較佳實施例,測試使用& 之電漿預處理步驟。這些測試之結果顯示H2(12slm)& Ar(550〇SCCm)電漿(rf功率900瓦)均勻地以約每秒〇 8埃 之速率蝕刻氧化矽。同時,蝕刻處理也相當溫和,其並未 示出有任何損壞碎之現象。第5A及5B圖示出使用此處理 之姓刻均勻性。第5 A圖示出沉積於晶圓上之氧化碎層之 厚度’於晶圓受到本發明之電漿預處理步驟之前。量測係 使用熟W於本技藝者所知之羅德芬(Rud〇lph)對焦橢圓 計,量測顯示於預處理步驟前,氧化層具有132± ι5·61埃 之厚度。第5B圖代表在90秒預處理步驟後之氧化物層之 厚度。於第5B圖中,氧化物·層具有58±16.7埃之厚度。 第41頁 本紙張尺度適用中國國家標準(CNS ) Α4規格(210Χ297公釐) " ' 507015 A7 B7 五、發明説明() 經濟部中央標準局員工消費合作社印製 可由第5A及5B圖之比較看出,於第5Β_φ 士 一 、 η Y <氧化物層之厚度變化係幾乎相同於示於第5 A圖之變化。因此 以由比較看出,步驟325之蝕刻係很均勻。 可 同時,本發明人量測依據本發明沉積之鈦芦雨 、 曰之電阻率 及依據類似處理所沉積之鈦層之電阻率,.雨 —”、、电漿預處理 步驟及無標準HF浸泡步驟,其係經常為半導體製造者所 使用,以於鈦沉積前除去氧化物。這些測試結果顯示對於 3〇〇埃之鈦層,未被以電漿預處理步驟處理之該層之兩 率係於0.5至1·〇 Ω高於具電漿預處理步驟所處理過者 這些結果證明本發明之電漿預處理步驟可以成功 用以蝕刻於矽基板上之不想要之氧化物,#沉積鈦層 前。如同先前所述,此氧化物係經常性地建立於基板二 將事先需要一個別處理步驟,例如浸泡於一 HF溶劑中 以於傳送基板至-個別室,用以沉積鈥薄膜前,姓刻掉吵 建立物。此HF浸泡步驟需要晶圓被隨後乾燥並然後於其 他氧化發生前,立即被傳送至沉積室。這處理相當複雜 費時及較本發明之處理不可靠。 其他測試顯示本發明之處理並未沉積任何鈦於接 孔,例如第2A圖之孔210之侧壁,同時,形成高於“ 事無補之底覆蓋率。當一 1〇〇埃鈦層被沉積於接觸内時 一展現具有對形成於接觸底部之矽化鈦有3〇〇〇/()底覆蓋 之薄膜具有300埃。 列於上述處理及實驗中之參數應不被限制於如 μ專利範圍所描述者。熟習於本技藝者可以修正上述 阻 地之並 該 觸300 率 此申之本 丄 ΟPrinted on page 38 printed by the Central Consumers Bureau of the Ministry of Economic Affairs, Consumer Cooperatives. Paper size is applicable to Chinese National Standard (CNS) A4 (210X297 mm) 507015 A7 B7 V. Description of the invention () Table 2 Step 375 of the preferred CVD titanium cleaning process 380 | step 385 step 390 step 395 side 400 pressure (torr) TFO 0.8 0.8 0.6 4 TFO interval (mils) 650 600 600 600 650 650 RF power (watts) 0 0 400 0 0 0 argon (bottom) (seem ) 200 200 200 200 500 0 Argon (top) (seem) 0 0 0 0 0 0 h2 (seem) 0 0 0 0 0 0 He (seem) 500 (TiCl4 line 500 (TiCl4 line 500 (TiCl4 line 500 _4 Pipeline) 500 (Dinghui 14 Pipe Le 0 TiCl4 (mgm) 0 0 0 0 0 0 n2 (seem) 500 500 500 500 500 0 Cl2 (seem) 0 250 250 0 0 0 Employee Consumption Printed by the cooperative on page 39. This paper size is applicable to the Chinese National Standard (CNS) A4 specification (210X297 mm) 507015 A7 B7 V. Description of the invention (although the deposition conditions and flow rates shown in Tables 1 and 2 represent those used in the present invention The current preferred embodiment of the flow rate, but it is known that other deposition conditions and their Flow rate. For example, regarding the rate at which the source and reaction gases are introduced during the deposition phase, the inventors have found that the ratio of Η: to TiCU should be between about 64: 1 and 2034: 1. The preferred ratio depends on the temperature and pressure involved in the deposition. Bracket spacing, RF power level, and other deposition conditions. However, the inventors have found that the above ratios can be used to deposit good quality titanium films under better deposition conditions. The deposition conditions include a heater temperature range of at least Between 630 and 700 ° C, and the deposition pressure range is at least "Torr. In some specific tests, a good quality titanium film is deposited at a ratio of Hz: TiCl4 of 64: ι, using 30Ηsccm! The flow rate and the TiCl4 flow rate of 400 mg / equivalent to 47.23 SCCm), and the H2 / Ticl4 ratio at 2034: 1, with an h2 flow rate of 12000 sccm and a TiCl4 flow rate as low as 50 mg / m. When the flow rate ratio of H2 / TiC is less than 64: 1, the reaction becomes hypoxic and unstable. When the flow rate ratio is greater than 203 4: i, the deposited film begins to exhibit unacceptably poor bottom coverage during contact, Also, it is difficult to manage the exhaust. IV. Test Results and Measurements In order to show the efficacy of the present invention, the experiments were performed with a titanium deposited layer having the advantages of the method of the present invention and without the method of the present invention. The experiments were performed in a resistance-heated Tixz chamber manufactured by Applied Materials. TixZ 罜 is suitable for 200mm wafers and is located in Centura, a multi-chamber substrate processing system also manufactured by Applied Materials. (Please read the note on the back first-printed on this page by the Consumer Standards Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs 507015 A7 -------------B7 V. Invention Translation () " ~-、 In one of the group experiments, various pretreatment steps (step 325) were performed before the wafer deposition step on the wafer having the oxygen cutting layer deposited thereon. The first step of these pretreatment steps was chlorine (ms —, Nitrogen (500 SCCm) and argon (20 () scem) treatment gas to form a plasma. The plasma was formed using a RF power level of 400 watts and was maintained at 40 to 40 in different tests. Between 100 seconds. The test results show that this step etches the oxide layer at a rate of about Angstroms per second, but the last name is not very uniform and apart from oxygen cutting, it is also uncontrollably and inevitably etched away. Other tests show that the chlorine from the Ch plasma pretreatment step conflicts with the subsequent titanium deposition step. To be clear, I think the residual chlorine is expensive to slow down the deposition rate of the titanium film in step 335. At the same time, it also Decide that the obtained titanium layer is less deposited than the CL plasma pretreatment step The titanium reed is uniform. It is printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs (please read the caution page on the back). The inventor also tested the plasma pretreatment steps using & according to the preferred embodiment of the present invention. These The test results show that the H2 (12slm) & Ar (550〇SCCm) plasma (rf power 900 watts) uniformly etches silicon oxide at a rate of about 0.8 angstroms per second. At the same time, the etching process is also quite mild, and it has not Shows any signs of damage. Figures 5A and 5B show the uniformity of the last name using this process. Figure 5A shows the thickness of the oxide chip layer deposited on the wafer. Before the plasma pretreatment step, the measurement was performed using a Rudolph focusing ellipsometer, which is known to those skilled in the art. The measurement shows that before the pretreatment step, the oxide layer has a thickness of 132 ± 55 · 61 angstroms. Figure 5B represents the thickness of the oxide layer after the 90-second pre-treatment step. In Figure 5B, the oxide · layer has a thickness of 58 ± 16.7 Angstroms. Page 41 This paper applies Chinese National Standards (CNS) Α4 specification (210 × 297 mm) " '5070 15 A7 B7 V. Description of the invention () Printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs can be seen from the comparison of Figures 5A and 5B. In 5B_φ Shiyi, η Y < the thickness of the oxide layer is almost the same as The change shown in Figure 5A. Therefore, it can be seen from the comparison that the etching system in step 325 is very uniform. At the same time, the inventors measured the titanium reed rain deposited according to the present invention, the resistivity, and the similar treatment. The resistivity of the deposited titanium layer, rain— ", plasma pretreatment steps and no standard HF immersion steps, are often used by semiconductor manufacturers to remove oxides before titanium deposition. These test results show that for a 300 Angstrom titanium layer, the rate of the layer that has not been treated with the plasma pretreatment step is between 0.5 and 1.0 Ω higher than those treated with the plasma pretreatment step. These results It is proved that the plasma pretreatment step of the present invention can be successfully used to etch unwanted oxides on a silicon substrate, before depositing a titanium layer. As mentioned earlier, this oxide system is often built on the substrate. Two additional processing steps are required in advance, such as immersion in an HF solvent to transfer the substrate to a separate chamber for deposition of the thin film. Noisy building. This HF immersion step requires the wafer to be subsequently dried and then transferred to the deposition chamber immediately before other oxidation occurs. This process is quite complicated, time consuming and less reliable than the process of the present invention. Other tests have shown that the treatment of the present invention did not deposit any titanium in the vias, such as the sidewall of hole 210 in Figure 2A, and at the same time, formed a coverage rate higher than "nothing. When a 100 angstrom titanium layer was deposited When exposed within the contact, a film having a 300 / () bottom cover on the titanium silicide formed at the bottom of the contact is shown to have 300 angstroms. The parameters listed in the above treatments and experiments should not be limited to those as in the μ patent range Describer. Those who are familiar with this skill can modify the above ground resistance and should touch the rate of 300.
發明説明( 發明之較佳f 實她例以下之製程,藉由使用化學物,室H 及條件。因眇 于切至參數 ,^ ,上述艾說明係例示性並非限制性,以% 本發明係、 Φ4丨王,以及, 、 以適用以沉積於很多不同沉積及清洗處理 又鈦薄膜。鈿上 Θk理 】如,乾燥清洗處理可以使用遠端電 以分解Γ1 & κ ^ ^ 4 裝系H2氣體分子及/或其他氣體。同樣地,遠端微波 分、,、了以用以於沉積處理間,分解鈦及其他處理氣 2 以及,所分解離子可以被通至室30。本發明可以 ,不同清洗源使用,包纟f2,C1F3及其他,本發明之技 =使用不同鈥源,例#邱(固態)及其他自化飲化合 同時,電漿預處理步驟3 25可以於沉積步驟前,用 加熱晶圓並穩定於整個晶圓之溫度均勻性。其他氣體, 如上述之氮或氨可以用以鈍化於步驟345及35〇中 層。因此,本發明之範圍應不是藉由參考上述之說明 決定,而是參考隨附之申請專利範圍及其等效範圍加 定。 中 電 體 配 術 以 例 之鈥 加以 以決 (請先閲讀背面之注意事項 丨衣-- Hi寫本頁)Description of the Invention (The best invention of the invention is the following process, by using chemicals, chamber H and conditions. Due to the cut to the parameters, ^, the above Ai description is illustrative and not restrictive. Φ4 丨 Wang, and, are suitable for deposition on many different deposition and cleaning treatments and titanium films. 钿 上 Θk 理] For example, the dry cleaning treatment can use remote electricity to decompose Γ1 & κ ^ ^ 4 System H2 Gas molecules and / or other gases. Similarly, the remote microwave is used to decompose titanium and other processing gases 2 in the deposition process chamber, and the decomposed ions can be passed to the chamber 30. The present invention can, Different cleaning sources are used, including f2, C1F3, and others. The technique of the present invention = using different sources, such as Qiu (solid state) and other self-contained beverages. Plasma pretreatment step 3 25 can be performed before the deposition step. Use to heat the wafer and stabilize the temperature uniformity of the entire wafer. Other gases, such as the nitrogen or ammonia described above, can be used to passivate the middle layer in steps 345 and 35. Therefore, the scope of the present invention should not be determined by referring to the above. Explain decision It is determined by referring to the scope of the patent application and its equivalent range attached. CLP's technical examples will be determined (please read the precautions on the back 丨 clothing-Hi write this page)
經濟部中央標準局員工消費合作社印製 本紙張尺度適用中國國家標準(CNS ) A4規格(210X 297公釐)Printed by the Consumer Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs This paper is sized for the Chinese National Standard (CNS) A4 (210X 297 mm)
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US98287297A | 1997-12-02 | 1997-12-02 |
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TW87118298A TW507015B (en) | 1997-12-02 | 1998-11-03 | In-situ, preclean of wafers prior to a chemical vapor deposition titanium deposition step |
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JP (1) | JP4511721B2 (en) |
KR (1) | KR20010032726A (en) |
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KR100703650B1 (en) * | 2005-11-30 | 2007-04-06 | 주식회사 아이피에스 | Apparatus for depositing thin film on wafer |
US7341950B2 (en) | 2005-12-07 | 2008-03-11 | Infineon Technologies Ag | Method for controlling a thickness of a first layer and method for adjusting the thickness of different first layers |
US7790635B2 (en) | 2006-12-14 | 2010-09-07 | Applied Materials, Inc. | Method to increase the compressive stress of PECVD dielectric films |
KR20120103719A (en) * | 2009-12-22 | 2012-09-19 | 어플라이드 머티어리얼스, 인코포레이티드 | Pecvd multi-step processing with continuous plasma |
US20130075262A1 (en) * | 2011-09-22 | 2013-03-28 | Catcher Technology Co., Ltd. | Method of forming anodic titanium oxide layers having dual-color appearance and article having the same |
JP6284786B2 (en) * | 2014-02-27 | 2018-02-28 | 東京エレクトロン株式会社 | Cleaning method for plasma processing apparatus |
KR102141547B1 (en) * | 2019-09-25 | 2020-09-14 | 솔브레인 주식회사 | Method for forming thin film |
KR102156663B1 (en) * | 2019-09-25 | 2020-09-21 | 솔브레인 주식회사 | Method for forming thin film |
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TWI403607B (en) * | 2006-02-24 | 2013-08-01 | Tokyo Electron Ltd | The Ti-based film deposition method and storage medium |
TWI704636B (en) * | 2019-03-08 | 2020-09-11 | 大陸商瀋陽拓荊科技有限公司 | Wafer processing device |
Also Published As
Publication number | Publication date |
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JP2001525613A (en) | 2001-12-11 |
KR20010032726A (en) | 2001-04-25 |
WO1999028955A3 (en) | 1999-09-16 |
JP4511721B2 (en) | 2010-07-28 |
WO1999028955A2 (en) | 1999-06-10 |
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