TW201220006A - Plasma mediated ashing processes - Google Patents
Plasma mediated ashing processes Download PDFInfo
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- TW201220006A TW201220006A TW100126335A TW100126335A TW201220006A TW 201220006 A TW201220006 A TW 201220006A TW 100126335 A TW100126335 A TW 100126335A TW 100126335 A TW100126335 A TW 100126335A TW 201220006 A TW201220006 A TW 201220006A
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- Prior art keywords
- plasma
- gas
- oxygen
- substrate
- ashing
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- Drying Of Semiconductors (AREA)
Abstract
Description
201220006 六、發明說明: 【相關申請案之交互參照】 本案是2010年7月27曰申請之美國非臨時申,之直 利申睛案第12/844,193號和2008年11月7】 〜么丄曰申請之美園 非臨時申請之專利申請案第12/275 394 、° 电、 现的部分接續申請 案’並且主張基於此二前案的權益;以弓丨 … 用方式將此二荦 之整體納入本文中。 示 本發明之背景 本揭示一般關於電漿中介灰化方法,其從半導體基板 有效移除有機材料,同時能夠減少基板於處理期間的氧化 和/或侵蝕;並且特別關於電漿中介灰化方法,其中電漿 實質上不含快速擴散物種。 積體電路製程一般可以分成生產線前端(fr〇nt end 〇f line ’ FEOL)處理和生產線後端(back en(i 〇fUne,be〇l)處 理。FEOL過程乃聚焦於製造構成積體電路的不同元件,而 BEOL過程則一般聚焦於形成積體電路的不同元件之間的 金屬交互連結。審視涿縻芋箏邀存犮發淚屬(Inten^ti〇nal201220006 VI. Description of invention: [Reciprocal reference of relevant application] This case is the US non-provisional application filed on July 27, 2010, and the direct application case No. 12/844,193 and November 7, 2008] The application for the US Park is not a temporary application for patent application No. 12/275 394, ° electricity, the current part of the application for the continuation of the application and claims the rights and interests based on the two previous cases; in. BACKGROUND OF THE INVENTION The present disclosure relates generally to a plasma intermediate ashing process that effectively removes organic materials from a semiconductor substrate while being capable of reducing oxidation and/or erosion of the substrate during processing; and particularly with respect to plasma intermediate ashing methods, The plasma is substantially free of rapidly diffusing species. The integrated circuit process can generally be divided into the front end of the production line (fr〇nt end 〇f line ' FEOL) processing and the back end of the production line (back en(i 〇fUne, be〇l) processing. The FEOL process is focused on manufacturing the integrated circuit. Different components, while the BEOL process generally focuses on the metal interaction between the different components that form the integrated circuit. Reviewing the 涿縻芋 邀 邀 邀 ( (Inten^ti〇nal
Technology Roadmap for Semiconductors,ITRS)有關 FEOL 處理則透露出未來元件在許多關鍵領域(包括電漿灰化)所 .面對的重要表現挑戰。舉例而言,電漿灰化的發展圖預計 45奈米(nm)世代的目標矽漏失為每個清潔步驟不大於 0.4A,.而32奈米世代則不大於〇.3A。 201220006 石一垔而έ,敏感的基板材料(例如佈植以極淺摻雜物的 间k ;|電質、金屬閘極和類似者)乃暴露於光阻 T除過程期間’其於光阻移除過程期間可能會受損。基板 相,-般可能呈基板侵譬如㈣、濺鑛和類似者所造成 :貫體移除部份的基板,譬如碎漏失)、基板氧化、換雜物 漂白/丨農度改變或其組合的形式。這些改變係所不欲的, 因為匕們將改變基板的冑、化學、物理等性質。此外,形 成於下層之做出圖案的分布輪廓若有小偏差,亦可不利地 衝擊最終積體電路的元件表現、產出、可靠度。舉例而言, 於源極和汲極佈植應用,在執行高劑量佈植之前,做出圖 =的光阻層乃形成於矽基板的源極和汲極區域上。於高劑 里佈植過程期間,光阻受到比較高能量的離子,其在光阻 t所引起的交聯反應深度差不多等於或稍微大於離子的範 圍。此父聯反應和造成的氫漏失則產生硬化的光阻層上 邛,其通常稱之為殼層。殼層的物理和化學性質視佈植條 件而變化,它一般要比底下非交聯的光阻更能抵抗電漿申 介灰化過程。因為此點,所以需要更有侵略性的電漿化學 物質來移除阻劑。然而同時,極淺的接合深度要求在組劑 移除過程中有極高的選擇性。於高劑量離子佈植剝除期間 必須避免來自源極/汲極區域的矽漏失或矽氧化。舉例而 言,過度的矽漏失可以有害地改變在給定施加電壓下的電 流飽和度,並且由於減少的接合深度而導致寄生洩漏,其 有害地改變元件的電功能。目前的電漿中介灰化方法一般 不適合此種應用。 201220006 立接= 中介剝除過程典型是基於氧㈣的, 導::!式清潔步驟。然而,基於氧的《過程可以 …=的基板表面氣化,典型是在約ιοΑ或更大的等 擴散。2::夕或㈣的電漿氧化速率是由氧化性物種 散時門乃J 面氧化物的擴散速率所決定。由於擴 物厚度成正比,故氧化物厚度的成長與氧 化迷早成正比,而成長中的窗 平方根成正比。熟於此技藝者把電聚暴露時間的 特徵可《由下面的方程式來表r稱為抛物線成長,其 X2 + AX = B(t) 線ιΐΓι氧化物厚度’t=時間’B=抛物線速率常數,而A/B= 線性速率常數。 面氧化A I已知是由電漿阻劑剝除過程中的石夕表 :控,所以許多人認為使用基於氧㈣的電聚灰化 科枯:不、合用於先進邏輯元件所需的32奈米和更先進的 後者需要幾乎「零」基板漏失並且導人對於表面 為敏感的新材料(例如嵌入的SiGe源極/沒極、高k :極介電質 '金屬閘極和NiSi接觸對於傳統的 ^說,因為抛物線速率常數可以高達每秒⑽,所以.暴露 /僅幾秒就可以發生顯著的氧化物成長。類似而言,已 :::傳:二含敦電聚過程除了有令人無法接受的基板漏失 Ή導致摻雜物漂白。其他的電浆灰化方法 =還^生化學物f ’例如形成氣體(N2/H2);就基板氧化 a ’它提供良好的結果’但是因為較低的阻劑移除速率 201220006 而有產率的問題。此外,基於氣的電聚已經常發現會 摻雜物分布的改變,這有害地影響元件的電性質。 因為此點,所以先前的電毁中介灰化方法一般視為不 適合於先進設計規料咖L流程巾移除光阻。因為體認到 料設計規則下的電聚中介灰化所帶來之不能克服的問 碭’譬如基板漏失、摻雜物漂白和類似者,所以許多關、,主 已導向於渔式化學移除光阻。如將在此所示範的,申請1 已發現適合先進設計規則之可實行的電浆中介剝除過矛:, 其提供最少的基板漏失、最少的摻雜物漂白和類似者。 重要的是注意灰化過程顯著不同於蝕刻過程。雖然二 過程都可以是電漿中介的,但是蝕刻過程顯然不同之 於選擇電聚化學物質以透過光阻遮罩的開口來移除部份的 基板表面,而永久轉移影像到基板裡。蝕刻電裝一般在低 溫和低壓下(毫托耳的等級)將基板暴露於高能量的離 炸以實體移除基板所選的部分。此外’暴露於離子的基板 所選部分-般是以大於光阻遮罩的移除速率而移除。才土目對 而言’灰化過程-般是指移除钮刻期間所形成的光阻遮罩 和任何聚合物或殘餘物。灰化電漿化學物質遠不如敍刻化 學物質來得有侵略性,並且一般選擇使之移除光阻遮舉層 的速率遠大於移除底下基板的速率。此外,大部分的灰化 過程加熱基板以進一步增加電漿反應性和晶圓產率,並且 在比較高的壓力下(托耳的等級)進行。因此,餘刻和灰化過 程是為了極不同的目的來移除光阻和聚合材料,故需要完 全不同的電漿化學物質和方法。成功的灰化方法並非用來 201220006 永久轉移影像到基板裡。成功的灰化方法反而是由光阻、 聚合物和/或殘餘物的移除速率而不影響或移除下層⑷ 基板、氧化和氮化間隔物、低k介電材料和類似者)所定義。 基於前面所言,此技藝所需要的是可實行的解決方案 以,於先進設計規則所需要的光阻移除,特別是關於在高 劑量離子佈植處理之後來移除光阻。 门 【發明内容】 於一具體態樣’從基板移除光阻、聚合物和/或殘餘 物的電漿灰化方法包括:把包括光阻、聚合物和/或殘餘 物的基板放入反應腔室;從包括氧氣(〇2)和/或含氧氣體的 氣體混合物來產生電漿;抑制和/或減少電毁中的快速擴 散物種;以及將基板暴露於電漿,以從基板選擇性地移除 光阻、聚合物和/或殘餘物,其中電漿實質上不含快速擴 散物種。 ' ' 於另一具體態樣,從基板來灰化有機物質的方法包 括.從包括〇2或含氧氣體的氣體混合物來產生電漿丨把電 漿組合以原子氧掃除氣體;把上面具有有機物質的基板暴 露於電漿,以及從基板選擇性地移除有機物質。 於又一具體態樣,從基板來灰化光阻、聚合物和/或 殘餘物的電漿設備包括:用於產生電漿的電漿產生構件, 其中電漿乃建構成實質上不含快速擴散物種,並且是由含 氧氣體和原子氧掃除氣體的氣體混合物所形成;以及流體 連通於電漿.產生構件的處理腔室,該處理腔室罩住基板。 8 201220006 於再一具體態樣,從基板來灰化光阻、聚合物和/或 殘餘物的電聚設備包括:用於產生電聚的電敷產生構件, ”中電漿疋由包括氡氣(〇2)或含氧氣體的氣體混合物所形 成,而再組合以原子氧掃除氣體;位在電漿和基板之間的 掃除性材料,其建構成抑制和/或減少電跟中的快速擴散 物種;以及罩住基板而流體連通於電漿產生構件的處理腔 至’違處理腔室乃建構成把基板暴露於已抑制和/或減少 當中快速擴散物種的電漿’以從基板選擇性地移除光阻、 1合物和/或殘餘物。 從本發明下面配合所圖式的詳細描述,將會更完整了 解本發明之具體態樣的這些和其他特色和優點。注意請求 項的範圍是由當中的敘述所界定,而不是由發明說明所列 之特色和優點的特定討論所界定。 【實施方式】 我們已針對不同的氧化性物種找出拋物線速率常數B 的特铽,如圖19所不。氧之離子和原子物種的拋物線速率 常數要比分子物種(例如⑽或〇2*)的拋物線速率常數高出 -個數量級。由於這項發現,矽的氧化可以藉由二種可能 的機制而戲劇性地降低:⑴以實質較慢擴散的分子物種來 取代例如0+、0_或〇*之快速擴散的物種;⑺使表面氧化 物氮化以'減少物種擴散穿過成長中之氧化物的速率。 在此揭示的是從基板選擇性地移除光阻、離子佈植光 阻、聚合物、殘餘物和/或類似之有機物質的電漿中介灰 201220006 化方法和設備。如在此將會描述的,在諸多優點中,電毁 中介灰化方法和設備尤其提供比較高的灰化速率、最少的 或沒有基板漏失、最少的或沒有損傷到底下的材料(譬如高 k介電材料)、最少的或沒有摻雜物分布改變。結果,在此 所述的電漿中介光阻灰化方法和設備乃適合32奈来的 FEOL處理,並且超越了基板漏失必須保持為最少的㈠、於 1.0A)且電性質須要實質上未被光阻移除過程所改變的科技 節點。 於具體態樣,電漿中介灰化方法一般包括從包括氧 氣(〇2)或含氧氣體的氣體混合物來產生電漿,其中電黎實質 上不含快速擴散物種。電漿所產生而用於灰化的大部分原 子物種具有高擴散常數。已發現具有高擴散常數的原子物 種會造成高度矽氧化,其係電漿中介灰化過程所不欲的效 應。換言之,電漿氧化速率是由快速擴散物種所掌控。因 此’如在此所用的「快速擴散物種」(fast diffusing speeies) 一詞一般是指具有高擴散常數的原子物種,亦即具有每秒 大於約0·003Α2(Α2 /秒)的高拋物線成長速率常數。於一具 體態樣’快速擴散物種在270。(:的拋物線速率常數等於或 大於約0.02A2/S。可以於通常電漿過程中產生之範例性快速 擴散物種包括而不限於活性氧(〇*)、原子氧(〇)、離子氧 (〇+、〇·)和類似者。如在此使用的’雖然詞彙「活性氮」(active nitrogen)、「活性氧」(active 0Xygen)和其他類似的活性物種 (例如活性氫)一般是指具有能量之激發的原子或分子,但卻 是電中·性的物種。 10 201220006 在此揭7F的電漿中介灰化方法是受控制的氧擴散過 :,藉此於電漿產生期間或在暴露於所要處理的基板之 減y可U氧化基板的快速擴散物種之抛物線速率常數 :測得的擴散速率,或者消除和/或抑制電漿裡的快速擴 散物種。為了達到此點’把電漿來源(不論其是由微波或射 頻能量所產生)針對分子物種的產生來加以最佳化,其中使 緩慢擴散之分子物種對快速擴散之原子物種的比例達到最 2降低快速擴散者的效應’或者降低快速擴散者的擴散 虛;5或者兩種方式兼有。更特定而言,快速擴散者的效 應可以藉由使02*或N0*對活性氧(0*)的比例達到最大而 降低。因為存在的活性氧(其係氧氣或含氧氣體電漿的自然 :產物)是氧化的機制’所以減少活性氧對於使石夕氧化減到 二而…度有效的。此外’快速擴散者的擴散速率可 二由使氧化物氮化而降低。更特定而言,可以使活性氮 子乳(〇*)的比例達到最大而減少擴散常數。 “j而°於一具體態樣’電漿中介灰化方法-般包 :加電漿中之活性氮對活性氧物種的比例,使得該比例 於1又可付自氧(〇2)和氮(N2)氣體混合物電漿之 物種對活性氧物種的比例。圖1 μ上示範基於由 和氮⑽氣體所形成的電聚之活性氮和活性氧的可 ::例對照於實施申請人的發明而可得的比例上之差異。 側所示’先前技藝之由氧氣和敗氣混合物所形 其展現的活性氮對活性氧的比例乃包括相對於 活性氣之比較高量的活性氡;中請人已發現這與用來形成 201220006 該電聚的特定氧氣和氮氣組成都無關。相對而言,申請人 已發現多樣的機制來增加電漿中之活性氮對活性氧的比 例,其實質上大於可得自由包含氧氣和氮氣的氣體混合物 所形成之電漿中的比例。Technology Roadmap for Semiconductors (ITRS) related to FEOL processing reveals important performance challenges for future components in many key areas, including plasma ashing. For example, the development of plasma ashing predicts that the target leakage of the 45 nm (nm) generation is no greater than 0.4 A for each cleaning step, while the 32 nm generation is no greater than 〇.3A. 201220006 Stones are smashing, sensitive substrate materials (such as implanted with extremely shallow dopants k; | electrical, metal gates and the like) are exposed to the photoresist during the process of removing photoresist It may be damaged during the removal process. The substrate phase, which may be caused by substrate intrusion such as (4), splashing, and the like: the portion of the substrate that is removed by the body, such as a missing substrate, the oxidation of the substrate, the change of the bleaching/potency of the change, or a combination thereof. form. These changes are undesired because they will change the enthalpy, chemical, physical properties of the substrate. In addition, if there is a small deviation in the distribution profile of the pattern formed in the lower layer, it may adversely affect the component performance, output, and reliability of the final integrated circuit. For example, in source and drain implant applications, a photoresist layer is formed on the source and drain regions of the germanium substrate prior to performing high dose implants. During the implantation process in high doses, the photoresist is subjected to relatively high energy ions whose cross-linking reaction depth caused by the photoresist t is almost equal to or slightly larger than the ion range. This parental reaction and the resulting hydrogen loss result in a hardened photoresist layer, which is commonly referred to as the shell layer. The physical and chemical properties of the shell vary depending on the conditions of the planting. It is generally more resistant to the plasma application ashing process than the underlying non-crosslinked photoresist. Because of this, more aggressive plasma chemicals are needed to remove the resist. At the same time, however, very shallow joint depths require extremely high selectivity during the removal of the agent. Leakage or deuterium oxidation from the source/drain regions must be avoided during high-dose ion implantation stripping. For example, excessive leakage can detrimentally alter the current saturation at a given applied voltage and cause parasitic leakage due to reduced joint depth, which detrimentally alters the electrical function of the component. Current plasma intermediate ashing methods are generally not suitable for this application. 201220006 Standup = Intermediary stripping process is typically based on oxygen (four), guide::! Cleaning steps. However, the oxygen-based process can vaporize the surface of the substrate, typically at about ιοΑ or greater. The plasma oxidation rate of 2:: or (4) is determined by the diffusion rate of the oxidized species. Since the thickness of the expander is proportional, the growth of the oxide thickness is directly proportional to the oxidization fan, and the square root of the growing window is proportional. Those skilled in the art can characterize the exposure time of electropolymerization. "The equation R is called parabolic growth, and its X2 + AX = B(t) line ι ΐΓ oxide thickness 't = time 'B = parabolic rate constant And A/B = linear rate constant. Surface oxidation AI is known to be controlled by the plasma resist stripping process. Therefore, many people think that the use of oxygen-based (IV)-based electro-accumulation is dry: no, 32% required for advanced logic components The latter and the more advanced latter require nearly "zero" substrate leakage and lead to new materials that are sensitive to the surface (eg embedded SiGe source/nopole, high k: very dielectric 'metal gate and NiSi contact for tradition ^, because the parabolic rate constant can be as high as (10) per second, so significant oxide growth can occur in exposure / only a few seconds. Similarly, has::: pass: two contain the electricity gathering process in addition to people Unacceptable substrate loss Ή leads to dopant bleaching. Other plasma ashing methods = also chemical chemistry f 'for example gas formation (N2 / H2); on the substrate oxidation a ' it provides good results' but because Low resist removal rate 201220006 has problems with yield. In addition, gas-based electropolymerization has often found changes in dopant distribution that adversely affect the electrical properties of the component. Because of this, the previous electricity Destructive intermediary ashing method It is considered unsuitable for the removal of photoresist from the advanced design specifications. Because of the inevitable problems caused by the ashing of the electropolymerization under the design rules of the material, such as substrate loss, dopant bleaching and Similarly, so many, the Lord has been directed to fish-type chemical removal of the photoresist. As will be demonstrated here, Application 1 has found a viable plasma-mediated stripping of spears suitable for advanced design rules: Provides minimal substrate loss, minimal dopant bleaching, and the like. It is important to note that the ashing process is significantly different from the etching process. Although both processes can be plasma-mediated, the etching process is clearly different from selective electro-convergence. The chemical removes part of the substrate surface through the opening through the photoresist mask to permanently transfer the image into the substrate. The etched package typically exposes the substrate to high energy at low temperatures and low pressures (millimeters). Desalination removes the selected portion of the substrate by physical removal. In addition, the selected portion of the substrate exposed to ions is generally removed at a rate greater than the removal rate of the photoresist mask. Generally refers to the photoresist mask and any polymer or residue formed during the removal of the button. The ashing plasma chemistry is far less aggressive than the etched chemistry and is generally chosen to remove the photoresist. The rate of lifting the layer is much greater than the rate at which the underlying substrate is removed. In addition, most of the ashing process heats the substrate to further increase plasma reactivity and wafer yield, and at relatively high pressures (the level of the bracket) Therefore, the residual and ashing process removes photoresist and polymeric materials for very different purposes, so completely different plasma chemistries and methods are required. Successful ashing methods are not used to permanently transfer images to substrates in 201220006. The successful ashing method instead consists of the removal rate of photoresist, polymer and/or residue without affecting or removing the underlying layer (4) substrate, oxide and nitride spacers, low-k dielectric materials and the like) Defined. Based on the foregoing, what is needed in this art is a workable solution to remove the photoresist required by advanced design rules, particularly with regard to removing photoresist after high dose ion implantation. [Invention] In one embodiment, a plasma ashing method for removing photoresist, polymer, and/or residue from a substrate includes: placing a substrate including a photoresist, a polymer, and/or a residue into a reaction a chamber; generating a plasma from a gas mixture comprising oxygen (〇2) and/or an oxygen-containing gas; suppressing and/or reducing rapidly diffusing species in electrical destruction; and exposing the substrate to a plasma for selective selectivity from the substrate The photoresist, polymer and/or residue are removed, wherein the plasma is substantially free of rapidly diffusing species. In another embodiment, a method of ashing an organic substance from a substrate includes: generating a plasma from a gas mixture comprising ruthenium or an oxygen-containing gas, and combining the plasma with atomic oxygen to sweep the gas; The substrate of the substance is exposed to the plasma and the organic material is selectively removed from the substrate. In yet another embodiment, a plasma apparatus for ashing photoresist, polymer, and/or residue from a substrate includes: a plasma generating member for generating a plasma, wherein the plasma is constructed substantially free of rapid A diffusing species, and formed by a gas mixture of an oxygen-containing gas and an atomic oxygen sweeping gas; and a processing chamber fluidly coupled to the plasma generating member, the processing chamber housing the substrate. 8 201220006 In yet another embodiment, an electro-convergence device for ashing photoresist, polymer, and/or residue from a substrate includes: an electro-distribution generating member for generating electro-convergence, (〇2) or a mixture of gases containing oxygen gas, and combined with atomic oxygen to sweep the gas; a sweeping material located between the plasma and the substrate, which is constructed to inhibit and/or reduce rapid diffusion in the electrical heel a species; and a processing chamber that covers the substrate and is in fluid communication with the plasma generating member to the 'violation chamber is configured to expose the substrate to a plasma that has suppressed and/or reduced rapidly diffusing species' to selectively The photoresist, the composition and/or the residue are removed. These and other features and advantages of the specific aspects of the present invention will be more fully understood from the following detailed description of the invention. It is defined by the narratives and not by the specific discussion of the features and advantages listed in the description of the invention. [Embodiment] We have identified the parabolic rate constant B for different oxidative species. As shown in Figure 19. The parabolic rate constants of oxygen ions and atomic species are orders of magnitude higher than the parabolic rate constants of molecular species (eg, (10) or 〇2*). Due to this discovery, the oxidation of ruthenium can be Two possible mechanisms are dramatically reduced: (1) replacing rapidly diffusing species such as 0+, 0_, or 〇* with a substantially slower diffusing molecular species; (7) nitriding surface oxides to 'reduce species diffusion through The rate of oxides in growth. Disclosed herein is a plasma intercalation ash 201220006 method for selectively removing photoresist, ion implantation photoresist, polymer, residue, and/or the like from a substrate. Apparatus. As will be described herein, among many advantages, the electro-disruption intermediate ashing method and apparatus provide, in particular, a relatively high ashing rate, minimal or no substrate loss, minimal or no damage to the underlying material (eg, High-k dielectric material), minimal or no dopant distribution change. As a result, the plasma-intermediate photoresist ashing method and apparatus described herein are suitable for 32-minute FEOL processing and exceed the base. Leakage must be kept to a minimum (1) at 1.0A) and the electrical properties need to be substantially unaltered by the photoresist removal process. In a specific aspect, the plasma intermediate ashing process generally involves the inclusion of oxygen (〇2). Or a gas mixture of oxygen-containing gases to produce a plasma, wherein the electricity is substantially free of rapidly diffusing species. Most of the atomic species produced by the plasma for ashing have high diffusion constants. It has been found to have a high diffusion constant. Atomic species can cause high levels of deuterium oxidation, which is an unwanted effect of the plasma ashing process. In other words, the plasma oxidation rate is controlled by rapidly spreading species. Therefore, 'fast diffusion species' as used herein (fast The term diffusing speeies generally refers to an atomic species having a high diffusion constant, i.e., a high parabolic growth rate constant of greater than about 0.0003 Α2 (Α2 / sec) per second. In a body-like 'rapidly diffusing species' at 270. (The parabolic rate constant is equal to or greater than about 0.02 A2/S. Exemplary rapid diffusion species that can be produced during normal plasma processing include, without limitation, reactive oxygen species (〇*), atomic oxygen (〇), ionic oxygen (〇 +, 〇·) and the like. As used herein, the terms "active nitrogen", "active oxygen" (active 0Xygen) and other similar active species (eg active hydrogen) generally refer to energy. The atom or molecule that is excited, but the species that is electrically neutral. 10 201220006 It is disclosed herein that the plasma intermediate ashing method of 7F is controlled by oxygen diffusion: thereby during plasma generation or during exposure to The subtraction of the substrate to be treated y can oxidize the parabolic rate constant of the rapidly diffusing species of the substrate: the measured diffusion rate, or the elimination and/or suppression of rapidly diffusing species in the plasma. To achieve this, the source of the plasma is Whether it is generated by microwave or radio frequency energy, it is optimized for the production of molecular species, in which the proportion of slowly diffusing molecular species to rapidly diffusing atomic species is reduced to a minimum of 2 The effect of the person's or the diffusion of the fast diffuser is reduced; 5 or both. In particular, the effect of the fast diffuser can be achieved by making the ratio of 02* or N0* to active oxygen (0*) Maximum and lower. Because the presence of active oxygen (which is the natural: product of oxygen or oxygen-containing gas plasma) is the mechanism of oxidation', reducing the active oxygen is effective in reducing the oxidation of the stone to two degrees. The diffusion rate of the diffuser can be reduced by nitriding the oxide. More specifically, the proportion of the active nitrogen emulsion (〇*) can be maximized to reduce the diffusion constant. "j and ° in a specific aspect" Plasma Intermediary Ashing Method - General Package: The ratio of reactive nitrogen to reactive oxygen species in the plasma is such that the ratio is 1 and can be paid from the plasma pair of oxygen (〇2) and nitrogen (N2) gas mixtures. Proportion of Reactive Oxygen Species. Figure 1 μ demonstrates the difference in the ratio of available reactive nitrogen and reactive oxygen species formed by electrolysis with nitrogen (10) gas: a comparison of the ratios available in the practice of the Applicant's invention. Shown in the 'previous skill' by oxygen and gas mixture It exhibits a ratio of reactive nitrogen to active oxygen that includes a relatively high amount of active hydrazine relative to the active gas; it has been found that this has nothing to do with the specific oxygen and nitrogen composition used to form the electrical polymerization of 201220006. Applicants have discovered a variety of mechanisms to increase the ratio of reactive nitrogen to reactive oxygen in the plasma, which is substantially greater than the ratio of plasma available from a gas mixture containing free oxygen and nitrogen.
------- g /小丁乳的獷散。 參見圖2’其圖形化顯示先前技藝的氧化物成長為同時 包括氧(〇2)和氮(Nz)氣體來形成電漿之氣體混合物的氧氣 (〇2)含量的函數。評估的氣體混合物包括含有氧氣和氮氣的 混合物以及包含氧氣和形成氣體的混合物,其中形成氣體 於氮氣中包含3 %的氫。如所示,即使微量氧的衝擊亦對基 板氧化造成,€、化效果。最小的「非零」(non-zero)表面改質則 在〇%的氧才觀察到。關於這二種氣體混合物,車交高的氧化 速率疋在包括形成氣體所形成的電漿觀察到,這指出形成 於一具體態樣,電漿中介灰化方法 合物來產生反應性物種,其包括活性------- g / small butyl milk loose. Referring to Figure 2', it is graphically shown that the oxide of the prior art is grown as a function of the oxygen (〇2) content of the gas mixture comprising both oxygen (〇2) and nitrogen (Nz) gases to form a plasma. The gas mixture evaluated included a mixture containing oxygen and nitrogen and a mixture comprising oxygen and forming gas, wherein the forming gas contained 3% hydrogen in nitrogen. As shown, even the impact of a trace amount of oxygen causes oxidation of the substrate, and the effect is reduced. The smallest "non-zero" surface modification is observed in 〇% of oxygen. With regard to the two gas mixtures, the oxidation rate of the car's high enthalpy is observed in the plasma formed by the formation of the gas, which indicates that it is formed in a specific state, and the plasma intervenes the ashing method to produce a reactive species. Including activity
一般包括從氣體混 其包括活性氮和活性氧,並且將 電漿氣體混合物的特定成分一般 12 201220006 視用於改變活性網·,工VlL & 與"+ 氮對活性氧之比例的特定具體態樣而定。 ::而5 ’電漿可以由氣態一氧化二氮本身所產生,或者 由,氧化二氮氣體與含_、氧化性氣體、惰性氣體、 退原錢體及其多樣組合的混合物所ϋ n 一“ 一氮氣體或一氧化-氣条辨、^·人At- 乳化一氮氣體此合物可以進一步包括多樣的 添加物’以增加光阻移除速率和/或使對底下的材料(譬如 電材料、基板、金屬、摻雜物濃度和類似者)的損傷降到 最低。應該注意雖然上面特定參照一氧化二氮而做為適合 相對於使用氧(〇2)和氮(N2)氣體所獲得者來增加電漿中之 活性氮對活性氧的比例,但是也料想到包括氧氣和含氧的 其他氣體。 再者,此合物可以由二或更多種電聚所形成,它們係 J處理腔至卡組合。舉例而言,由含氧氣體所形成的電漿 可以混合以由含氮氣體所形成的電毁。以此方式,其中一 種《可以由氧氣(02)所形成,而另一電漿可以由提供增加 活性氮的含氮氣體所形成。反過來說’其中一種電漿可以 由氮氣(N2)所形成,而另—電漿可以由含氧氣體所形成。 於又一具體態樣,添加或存在活性氫物種(H*)而組合以 活性氮(N*)以及可選用的活性氧(〇*)物種,則對於某些應用 來說可以是有利的,譬如於某些佈植後的應用(特別是關於 殘餘物移除)以及於金屬氧化可以影響元件表現的某些高K /金屬閘極結構。藉由提供活性氮、活性氫物種以及可選 用的活性氧之受控制混合物的電漿,則提供了低基板損傷 (譬如Si氧化和/或Si漏失)和低金屬基板氧化(譬如TiN、 13 201220006It generally consists of mixing reactive gases from nitrogen and reactive oxygen species, and treating the specific components of the plasma gas mixture generally 12 201220006 as a specific specificity for changing the active web, and the ratio of VlL &+ nitrogen to active oxygen. Depending on the situation. ::5' plasma may be produced by gaseous nitrous oxide itself, or by a mixture of oxidized dinitrogen gas and _, oxidizing gas, inert gas, retort body and various combinations thereof. "A nitrogen gas or a gas-gas strip, a human At- emulsified nitrogen gas compound may further comprise a variety of additives' to increase the rate of photoresist removal and / or to make the material underneath (such as electricity) Damage to materials, substrates, metals, dopant concentrations, and the like is minimized. It should be noted that although the above specific reference to nitrous oxide is suitable as appropriate for use with oxygen (〇2) and nitrogen (N2) gases To increase the ratio of reactive nitrogen to active oxygen in the plasma, but it is also conceivable to include oxygen and other gases containing oxygen. Furthermore, the compound can be formed by two or more kinds of electropolymerization, which are treated by J. Cavity-to-card combination. For example, a plasma formed of an oxygen-containing gas may be mixed to cause electrical destruction by a nitrogen-containing gas. In this manner, one of the "can be formed by oxygen (02), and the other Plasma can be supplied by increasing the amount of reactive nitrogen The formation of a nitrogen-containing gas. In contrast, one of the plasmas may be formed of nitrogen (N2), and the other may be formed of an oxygen-containing gas. In yet another embodiment, an active hydrogen species is added or present ( H*) combined with reactive nitrogen (N*) and optional reactive oxygen species (〇*) species may be advantageous for certain applications, such as certain post-plant applications (especially with respect to residues) Removal of material) and certain high K/metal gate structures that can affect the performance of the element by metal oxidation. Provides low plasma by providing a controlled mixture of reactive nitrogen, active hydrogen species, and optional reactive oxygen species. Substrate damage (such as Si oxidation and / or Si loss) and low metal substrate oxidation (such as TiN, 13 201220006
TaN和/或W金屬),同時以比較高的產率來有效移除光阻 和殘餘物。於某些具體態樣,電聚是由NH3所構成的氣體 而形成。於其他具體態樣,電漿是由包#顺3的氣體混合 物所形成,其中Μ%構成了氣體混合物的主要部分。舉^ 來說,某些具體態樣的氣體混合物可以包括大於5〇%的 NH3,於其他具體態樣則大於75%,並且另外還有其他的具 體態樣則大於85%。對於大部分的灰化應用來說,氣體^ 合物偏好有大於或等於90%的脚範例性的氣體混合物包 括而不限於nh3和形成氣體、Nh3和n2、顺3和形成氣體 和氧。存在氧則增加灰化速率,並且藉由控制氣體混合物 中存在的氧量,則觀察到有最少的矽漏失而又提供 的製程。 如在此將詳細討論的,減少電毁中之快速擴散物種(例 如原子氧物種)的多樣機制包括使用過濾器、掃除性氣體、 掃除性材料、錢劑和類似者,以在激發Q2時以及暴露於 光阻之前先移除和/或吸收電毁中產生的快速擴散物種, 藉此減少電聚裡之快速擴散物種的量。此外,這些集氣材 料產生了歸態的分子氧,其在料絲而不氧化基板材 料方面疋有效的。另外可以選擇的是選擇電毁來源和氣體 ^合物,以使緩慢擴散的氧化劑(例如分子氧化劑)對快速擴 =的氧化劑(例如原子或離子氧)之比例達到最大,其可以組 :、面注思到的任何增進方法或自行為之。這麼做則電 h以進_步包括活性氫物種’纟已發現讓電襞對於離子 佈植阻祕層而言會有更具侵略性的灰化行為而有最少的 201220006 摘傷“如基板氧化、基板侵飯和類似者卜更有侵略性的灰 化行為可以用來有效率地灰化典型視為難以灰化的光阻材 料’例如暴露於高能劑量離子佈植剝除(high咖哪d〇se — implantation strip,画8)之後而形成於光阻的殼層蝕刻 後的殘餘物和類似者。 圖3示範產生多重電漿流的範例性設備,其概括以參 考數字10所指示。電漿設備10一般包括氣體傳遞構件12、 電漿產生構件14、處理腔室16、排放管18。氣體傳遞構件 12 了以包括氣體純化器(未顯示),其流體連通於一或更多 個氣體來源20,後者則流體連通於電漿產生構件。使用微 波激發做為從氣體混合物來產生電漿的適合能量來源範 例,則電漿產生構件34包括微波封殼36,其一般是分割過 的矩形盒而具有電漿管38從中通過。如此技藝所已知的, 微波電聚產生構件Η乃建構成使輸入氣體激發成電漿,如 此以產出反應性物種。除了微波能量以外,電漿產生構件 3 04也可能是以RF能量激發來源、RF和微波能量的組合或 類似者來操作。電漿管38包括多個氣體入口 22 (顯示其中 二個)’來自氣體傳遞構件12的氣體20則由此饋入◊電漿 管延伸自氣體入口的部分則連接於電漿能量來源下游。以 此方式,不同的電漿在設備裡產生,它們然後在暴露於基 板之前加以混合。 一旦激發,則活性物種便引入處理腔室16的内部區域 以均勻傳送反應性物種到工件24 (例如彼覆阻劑的半導體 晶圓)的表面。關於此點,一或更多個擋板26、28乃包括於 15 201220006 處理腔室1 6裡。雖然下文並未詳細敘述擋板的特定操作方 式’但是此種操作的額外資訊可以發現於受讓給Axceiis科 技公司的美國專利申請案第10/249,964號,其整個併於此 以為參考。為了增進光阻和/或蝕刻後之殘餘物與上游電 漿所產出之活性物種的反應速率,工件24可以由加熱元件 陣列(譬如鎢鹵素燈或電阻加熱的夾盤,其未顯示於圓中) 來加熱。排放管18的入口 34乃流體連通於底板的開口以 接收排放氣體進入排放管丨8。 再次地應該了解電漿灰化設備1 〇代表一種或可配合實 施本發明而使用的裝置範例,如此以在基板暴露於電漿之 前而從後續混合的不同氣流來產生不同的電漿。其他適合 的電漿設備包括操作在約1〇〇托耳的中等壓力電漿(medium pressure Plasma ’ MPP)系統’如此以提供較低的電子溫度, 以及包括單一電漿管組態和沒有擋板的電漿來源(例如寬廣 來源面積電漿)》 可應用於不同具體態樣之適合的含氮氣體包括而不限 於 N2、N20、NO、N2〇3、NH3、NF3、N2F4、C2N2、HCN、 NOCM、C1CN、(CH3)2NH、(CH3)NH2、(CH3)3N、C2H5NH2、 其混合物和類似者。 適合添加於氣體混合物的惰性氣體包括而不限於氦、 氫、氮、氪、氣、氖和類似者。 想要有活性氟之適合的含氟氣體包括那些被電漿激發 時產生氟反應性物種的氣態化合物^於一具體態樣,氟氣 態化合物在電漿形成條件下是氣體,並且選自一般式為 16 201220006 • CxHyFz之化合物所構成的群組’其+ x是從0到4的整數, Υ是從0到9的整數’ Ζ是從1到9的整數,附帶條件為备 χ=〇則都等於卜並且當y為〇則…到…: 或選自此類化合物的組合。另外可以選擇的是含氣 氣體為f2、sf6及其混合物,如果想要的話,其包括上面一 般式CxHyFz所定義的含氟氣體。 當暴露於電漿時,含氟氣體乃小於電蒙氣體混合物換 體積的約5%以使選擇性達到最大。於其他具體態樣,當暴 露於電漿時,含說化合物乃小於電聚氣體混合物總體積的 ’勺3%於另外其他的具體態樣,當暴露於電漿時,含氟化 。物乃小於電漿氣體混合物總體積的約1%。 適合的還原性氣體包括而不限於含氣氣體,例如仏、 CH4、冊3、CxHy (其中χ是從t到4的整數,乂是從【到8 的整數)及其組合。所用的含氫化合物乃產生足夠的原子氫 物種,以增加敍刻期間所形成之聚合物和钮刻殘餘物的移 除選擇性。特別偏好的含氫化合物乃存在於氣態並且在 〜灵形成條件下釋放氫以形成原子氫物種例如自由基或 風離子。基於碳氫化合物的含氫化合物氣體或許可以由函 素(例―如填、氣或氣)或由氧、氮、經和胺基而部分取代。 〃氫氣(H2)最好是呈氣體混合物的形式。於—具體態樣, 虱氣混合物是包含氫氣和惰性氣體的氣體。適合的惰性氣 範例。括氬、氮、氖、氦和類似者。特別偏好的氫氣混 3物是所謂的形成氣體(f_inggas,FG),其基本上由氮氣 和氮氣所構成。特別偏好的是形成氣體’其中氫氣的量是 17 201220006 總形成氣體組成的約1M%到約5體積%。雖然可以利用 大於5體積%的量,但是由於氫氣爆炸風險而使安全性 一項問題。 战 適合的氧化性氣體包括而不限於〇2、〇3、C〇、ch、 H2〇、N2〇、N〇2和類似者。當使用氧化性氣體時,如上所 述 I偏好在暴露於基板之前先從電漿移除任何〇*和〇· 物*種。如上面所注意的’已發現基板氧化的因素是基板與 0 〇和/或0_物種反應。這些物種可以輕易擴散穿過成 長中的Si〇x表面氧化物,藉此導致比較厚的氧化物成長。 卜這二物種的快速擴散可以被表面氧化物所存在或减 應的電場而増進。因為此點,所以使氧化物成長減到最少 的策略應該解決幾項議S,亦π:抑制原?或離子氧的形 成(或任何其他快速擴散物種的形成),減少剩餘之快速擴散 者的擴散速率,並且減少或消除電場和氧化物帶電。如上 面所注意的,移除可以藉由於電漿處理期間增加反應腔室 裡的壓力、改變功率密度、加入添加物,加入同時包含氮 和氧70素的氣體(譬如一氧化氮)、使用過濾器(譬如原子和 離子過濾器)而實現。 電漿中介灰化方法可以實施於傳統的電漿灰化系統。 本發明不打算受限於任何特定的電漿灰化硬體。舉例而 。,或可使用採取感應耦合電漿反應器的電漿灰化器,或 者也可使用下游電漿灰化器,譬如微波驅動的、RF驅動的 和類似者。鑒於本揭示,特定電漿灰化器的設定和最佳化 將會是熟於此技藝者所熟悉的。電漿灰化器一般包括電聚 201220006 產生腔室和電漿反應腔室。僅舉例來說,於可得自Axcelis 科技公司(本案申請人)之3〇〇毫米RpS320的下游微波電漿 灰化器,基板於反應腔室中加熱到室溫和45〇〇c之間的溫 度。用於處理期間的溫度可以固定不變的,或者另外可以 選擇的是於處理期間漸變或階梯式的。增加溫度是熟於此 技了者所承用以增加灰化速率的方法。反應腔室裡的壓 力最好減少到約〇.丨托耳或更高。更佳而言,壓力係操作於 從、力0.5托耳到約4托耳的範圍。於某些應用(例如不要的 氧物種(譬如0*、〇-)做氣相重新組合係想要的,如此以增 加電漿中之活性氮對活性氧的比例),可以利用大於4托耳 的更高操作壓力,而某些具體態樣使用大於1〇托耳。 用於激發氣體和形成電漿能量來源的功率一般在約 1000瓦(W)和約10000瓦之間。對於某些氣體混合物,功率 大於5000瓦到小於約1〇〇〇〇瓦。舉例而言當氣體混合物 包括NH3做為主要成分(大於5〇%)時,已發現增加功率到大 於5000瓦而小於1〇〇〇〇瓦可以用以增加電漿裡形成的活性 氫虿,其可以有利地增加灰化速率❶此外,增加活性氫物 種的罝則減少金屬氧化。於某些具體態樣,電漿乃暴露於 集氣劑,如此以當想要時減少活性氫的量。也可以調整功 率设定以控制電漿中之活性氮對活性氧的比例,其可以應 用於其他種類的電漿灰化工具。 也可以調整電漿來源的功率密度(亦即每氣體體積的功 率)’以增加中性和激發態分子物種(例如和類似者) 的量。於一具體態樣,電漿可以在每立方公分至少約75瓦 19 201220006 (瓦/立方公分)的功率密度來產生;尤其是在每立方公分至 少約⑽瓦’更特“言是在每立方公分至少肖⑼瓦, ::特疋而。疋在每立方公分至少約2〇〇〖,最特定而言 是在母立方公分至少約300瓦。 包括丽3、氧或氧和氮(於某些具體態樣還有含氮氣體) 的氣體混合物乃經由氣體入口而饋入電毁產生腔室。氣體 然後暴露於電漿產生腔室裡的能量來源,譬如微波能量, 其最好在約1000瓦和約1〇_瓦之間,以從氣體混合物產 生激發的或具有能量的原子。產生的電聚包括電中性的和 帶電的粒子以及激發的氣體物種,其由電I氣體混合物中 所使用的氣體所形成。於一具體態樣,在電設抵達晶圓之 前,選擇性地移除帶電粒子。 :對於3GG毫米下游電衆灰化器而言,總氣體流動速率 最好是從每分鐘約500到12〇〇〇標準立方公分…⑽如以 eubic centimetei· per minute,sccm)。已發現總氣體流動速 率可以影響某些氣體混合物的發射光譜。舉例而言,較低 的總氣體流動速率可以偏好用於包括NH3做為主要成分的 氣體混合物,以增加電漿中之活性氫的量以及增加活性分 子物種的濃度。於一具體態樣,含NH3氣體或氣體混合物 的總氣體流動速率是每分鐘小於5標準公升(standar(1 nter per minute ’ Slm)。於其他具體態樣,小於4 sim ;而於另外 其他的具體態樣,小於3.5 Slm。 光阻、離子佈植光阻、聚合物、殘餘物或類似的有機 物質了以藉由與電漿產生之激發的或具有能量的原子(亦即 20 201220006 活性物種)反應而從基板選擇性地移除。反應可加以光學κ 視來偵測終點,如熟於此技藝者所認知的。可選用地而古, 電漿灰化過程之後進行沖洗步驟’如此以移除揮發性化人 物和/或洗去電漿處理期間所形成之可移除的化合物。於 一具體態樣,雖然沖洗步驟採用去離子水,但是也可以包 括氫氧化銨、硫酸、氫氟酸或類似者。沖洗步驟(如果採用 的話)可以包括旋轉沖洗約1到10分鐘,接著再接受旋轉乾 燥過程。 舉例來說,可以修改電漿硬體組態以增加緩慢擴散物 種對快速擴散物種的比例或增加活性氮對活性氧的比例。 於一具體態樣’掃除性材料(例如原子和/或離子氧過濟器) 和/或催化劑材料乃配置於基板和電漿來源之間,如此以 產生激發態的分子氧以及減少電漿中之快速擴散物種的 量。此過濾器可以是催化性過濾材料、表面重新組合過渡 器、氣相重新組合過濾器或類似者。舉例來說,過濾器可 以是表面反應性金屬或金屬性合金、陶瓷、石英或藍寳石 材料,而反應性氣體在與晶圓表面交互作用之前先通過過 濾益。此過濾器的功效可以藉由控制反應性表面的溫度以 及反應性表面的形狀和表面粗糙度而增進。此掃除性材料 的位置可以緊密鄰近於基板,因為激發態的分子具有比較 紐的壽命。更特定而言,掃除性材料可以位在離工件(基板) 約8公分或更少。 於另一具體態樣’修改了利用雙重擋板的電漿灰化工 具,使得上擋板是由石英所形成(相對於藍寶石而言),其也 21 201220006 已發現增加活性氮對活性氧的比例。以藍寶石或其他材料 而非石英來形成電漿管則觀察到類似的效果。可以用於減 少電漿裡之快速擴散物種(特定而言為〇、〇*、〇 +和/或〇-) 含量的適合之掃除性材料,其重新組合係數乃等於或大於 約 5xl0·4 〇 雖然用於掃除原子氧的範例性材料乃列於圖2〇的表, 但是也可以包括而不限於:金屬(例如B、Mg、A卜Be、Ti、 Cr、Fe、Μη、Νί、Rb、Ir、Pb、Sr、Ba、Cs、其合金)、金 屬間化合物(例如PrNi5、NtNi”和類似者)、陶瓷(例如TaN and/or W metal) while effectively removing photoresist and residue in relatively high yields. In some specific aspects, electropolymerization is formed by a gas composed of NH3. In other embodiments, the plasma is formed from a gas mixture of package #3, wherein Μ% constitutes a major portion of the gas mixture. For example, some specific aspects of the gas mixture may include greater than 5% by weight of NH3, and in other specific aspects, greater than 75%, and in addition other specific aspects are greater than 85%. For most ashing applications, gas compounds that have a preferred embodiment of the gas mixture of greater than or equal to 90% include, but are not limited to, nh3 and forming gases, Nh3 and n2, cis 3, and forming gases and oxygen. The presence of oxygen increases the rate of ashing, and by controlling the amount of oxygen present in the gas mixture, the process is provided with minimal leakage. As will be discussed in detail herein, various mechanisms for reducing rapidly diffusing species (eg, atomic oxygen species) in electrical destruction include the use of filters, sweeping gases, sweeping materials, money, and the like to excite Q2 and The rapidly diffusing species produced in the electrical destruction are removed and/or absorbed prior to exposure to the photoresist, thereby reducing the amount of rapidly diffusing species in the electropolymer. In addition, these gas-gathering materials produce a state-of-the-art molecular oxygen that is effective in terms of filaments without oxidizing the base material. Alternatively, the source of electrical destruction and the gas compound may be selected such that the proportion of slowly diffusing oxidant (eg, molecular oxidant) to the rapidly expanding oxidant (eg, atomic or ionic oxygen) is maximized, which may be: Any thought of any enhancements or self-contained. In doing so, the electric h includes the active hydrogen species. The enthalpy has been found to have a more aggressive ashing behavior for the ion implant blocking layer and has the least 201220006 sniper "such as substrate oxidation. The more aggressive ashing behavior of substrate invaders and similar ones can be used to efficiently ash photoresist materials that are typically considered to be difficult to ash, such as exposure to high energy dose ion implants. 〇se — implantation strip, drawing 8) Residues and similarities formed after shell etching of the photoresist. Figure 3 illustrates an exemplary apparatus for generating multiple plasma streams, generally indicated by reference numeral 10. The slurry apparatus 10 generally includes a gas transfer member 12, a plasma generating member 14, a processing chamber 16, and a discharge tube 18. The gas transfer member 12 includes a gas purifier (not shown) that is in fluid communication with one or more gases. Source 20, the latter being in fluid communication with the plasma generating member. Using microwave excitation as an example of a suitable energy source for generating plasma from a gas mixture, the plasma generating member 34 includes a microwave enclosure 36, which is generally divided into The cut rectangular box has a plasma tube 38 therethrough. As is known in the art, the microwave electropolymer generating member is constructed to excite the input gas into a plasma to produce a reactive species. The plasma generating member 304 may also be operated with a combination of RF energy excitation source, RF and microwave energy, or the like. The plasma tube 38 includes a plurality of gas inlets 22 (two of which are shown) 'from the gas transfer member 12 The gas 20 is thus fed into the portion of the plasma tube extending from the gas inlet and is connected downstream of the plasma energy source. In this manner, different plasmas are produced in the apparatus which are then mixed prior to exposure to the substrate. Once excited, the active species are introduced into the interior region of the processing chamber 16 to evenly transfer the reactive species to the surface of the workpiece 24 (e.g., the semiconductor wafer of the resist). In this regard, one or more baffles 26 28 is included in 15 201220006 processing chamber 16. Although the specific operation of the baffle is not described in detail below, additional information on such operations can be found in the transfer. U.S. Patent Application Serial No. 10/249,964, the disclosure of which is incorporated herein by reference in its entirety the entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire entire all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all all It may be heated by an array of heating elements, such as a tungsten halogen lamp or a resistive heated chuck, which is not shown in the circle. The inlet 34 of the discharge tube 18 is in fluid communication with the opening of the bottom plate to receive the exhaust gas into the discharge tube 8 . Again, it should be understood that the plasma ashing apparatus 1 〇 represents an example of a device that may be used in conjunction with the practice of the present invention to produce different plasmas from subsequent mixing of different gas streams before the substrate is exposed to the plasma. The plasma equipment consists of a medium pressure plasma 'MPP system' operating at approximately 1 Torr to provide a lower electronic temperature, as well as a single plasma tube configuration and no baffle Slurry source (eg broad source area plasma) can be applied to different specific nitrogen-containing bodies including, but not limited to, N2, N20, NO, N2〇3 NH3, NF3, N2F4, C2N2, HCN, NOCM, C1CN, (CH3) 2NH, (CH3) NH2, (CH3) 3N, C2H5NH2, mixtures thereof and the like. Inert gases suitable for addition to the gas mixture include, without limitation, helium, hydrogen, nitrogen, helium, gas, helium, and the like. Suitable fluorine-containing gases which have active fluorine include those which are fluorine-reactive species upon excitation by a plasma. In a specific aspect, the fluorine gaseous compound is a gas under plasma formation conditions and is selected from the general formula. 16 201220006 • Group of CxHyFz compounds 'its + x is an integer from 0 to 4, Υ is an integer from 0 to 9' Ζ is an integer from 1 to 9, with the condition that χ = 〇 Both equal Bu and when y is 〇 ... to...: or a combination of such compounds. Alternatively, the gas containing gas may be f2, sf6 and mixtures thereof, if desired, including the fluorine-containing gas as defined by the above general formula CxHyFz. When exposed to the plasma, the fluorine-containing gas is less than about 5% of the volume of the electric monoxide gas mixture to maximize selectivity. In other specific aspects, when exposed to the plasma, the compound containing less than 3% of the total volume of the electropolymerized gas mixture is in other specific aspects, and when exposed to the plasma, it is fluorinated. The amount is less than about 1% of the total volume of the plasma gas mixture. Suitable reducing gases include, but are not limited to, gas-containing gases such as hydrazine, CH4, 3, CxHy (where χ is an integer from t to 4, 乂 is an integer from [to 8), and combinations thereof. The hydrogen-containing compound used produces sufficient atomic hydrogen species to increase the removal selectivity of the polymer and button residue formed during the characterization. A particularly preferred hydrogen-containing compound is present in the gaseous state and releases hydrogen under conditions of formation to form atomic hydrogen species such as free radicals or wind ions. The hydrocarbon-based hydrogen-containing compound gas may be partially substituted by a function (e.g., filling, gas or gas) or by oxygen, nitrogen, a trans- and an amine group. The helium hydrogen (H2) is preferably in the form of a gas mixture. In a specific aspect, the helium gas mixture is a gas containing hydrogen and an inert gas. A suitable inert gas example. Including argon, nitrogen, helium, neon and the like. A particularly preferred hydrogen mixture is the so-called forming gas (f_inggas, FG) which consists essentially of nitrogen and nitrogen. It is particularly preferred to form a gas' wherein the amount of hydrogen is from about 1 M% to about 5% by volume of the total formed gas composition of 17 201220006. Although an amount greater than 5% by volume can be utilized, safety is a problem due to the risk of hydrogen explosion. Suitable oxidizing gases include, but are not limited to, 〇2, 〇3, C〇, ch, H2〇, N2〇, N〇2, and the like. When an oxidizing gas is used, I prefer to remove any 〇* and 〇* species from the plasma prior to exposure to the substrate. As noted above, the factor that has been found to oxidize the substrate is that the substrate reacts with the 0 〇 and/or 0_ species. These species can easily diffuse through the growing Si〇x surface oxide, thereby resulting in a relatively thick oxide growth. The rapid diffusion of these two species can be accelerated by the electric field in which the surface oxide is present or reduced. Because of this, the strategy of minimizing the growth of oxides should solve several arguments, and also π: suppress the original? Or the formation of ionic oxygen (or the formation of any other rapidly diffusing species), reducing the rate of diffusion of the remaining fast diffusers and reducing or eliminating electric field and oxide charging. As noted above, the removal can be accomplished by increasing the pressure in the reaction chamber during the plasma treatment, changing the power density, adding the additive, adding a gas containing both nitrogen and oxygen (such as nitric oxide), using filtration. Implemented by devices such as atomic and ion filters. The plasma intermediate ashing process can be implemented in a conventional plasma ashing system. The invention is not intended to be limited to any particular plasma ashing hardware. For example. Alternatively, a plasma asher in which an inductively coupled plasma reactor is employed, or a downstream plasma asher, such as microwave driven, RF driven, and the like, may be used. In view of the present disclosure, the setting and optimization of a particular plasma asher will be familiar to those skilled in the art. Plasma ashers typically include electropolymerization 201220006 generation chambers and plasma reaction chambers. By way of example only, in a downstream microwave plasma asher of a 3 mm RpS320 available from Axcelis Technologies, Inc. (applicant), the substrate is heated in the reaction chamber to a temperature between room temperature and 45 ° C. . The temperature used during processing may be fixed or alternatively may be graded or stepped during processing. Increasing the temperature is a method used by those skilled in the art to increase the rate of ashing. The pressure in the reaction chamber is preferably reduced to about 〇. Torr or higher. More preferably, the pressure system operates in the range of from 0.5 Torr to about 4 Torr. For some applications (such as unwanted oxygen species (such as 0*, 〇-) to do the gas phase recombination system, so as to increase the ratio of reactive nitrogen to active oxygen in the plasma), can use more than 4 Torr Higher operating pressures, while some specific aspects use more than 1 Torr. The power used to excite gases and form a source of plasma energy is typically between about 1000 watts (W) and about 10,000 watts. For certain gas mixtures, the power is greater than 5000 watts to less than about 1 watt. For example, when the gas mixture includes NH3 as a main component (greater than 5〇%), it has been found that increasing the power to more than 5000 watts and less than 1 watt can be used to increase the active hydroquinone formed in the plasma, The rate of ashing can be advantageously increased. Furthermore, increasing the enthalpy of the active hydrogen species reduces metal oxidation. In some embodiments, the plasma is exposed to a gassing agent such that the amount of active hydrogen is reduced when desired. The power setting can also be adjusted to control the ratio of reactive nitrogen to active oxygen in the plasma, which can be applied to other types of plasma ashing tools. The power density of the plasma source (i.e., the power per gas volume) can also be adjusted to increase the amount of neutral and excited molecular species (e.g., and the like). In a specific aspect, the plasma can be produced at a power density of at least about 75 watts per 19,200,200,6,200,000 cubic meters per cubic centimeter; especially at least about 10 watts per cubic centimeter. The centimeters are at least XI (9) watts, :: special 疋. 疋 at least about 2 每 per cubic centimeter 〖, most specifically at least 300 watts in the mother cubic centimeter. Included 3, oxygen or oxygen and nitrogen (in a certain The gas mixture containing the nitrogen gas is fed into the chamber through the gas inlet. The gas is then exposed to a source of energy in the plasma generating chamber, such as microwave energy, preferably at about 1000 watts. And between about 1 〇 watt to generate excited or energetic atoms from the gas mixture. The resulting electropolymer comprises electrically neutral and charged particles and excited gas species, which are used in the gas I gas mixture. The gas is formed. In a specific aspect, the charged particles are selectively removed before the electrical device reaches the wafer. For a 3GG mm downstream electric ash, the total gas flow rate is preferably from about every minute. 500 to 12 inches 〇〇 standard cubic centimeters... (10) as eubic centimetei per minute, sccm) It has been found that the total gas flow rate can affect the emission spectrum of certain gas mixtures. For example, a lower total gas flow rate may be preferred for inclusion. NH3 is used as the main component of the gas mixture to increase the amount of active hydrogen in the plasma and increase the concentration of active molecular species. In one specific aspect, the total gas flow rate of the NH3 containing gas or gas mixture is less than 5 standards per minute. Standar (1 nter per minute 'Slm). In other specific cases, less than 4 sim; and in other specific aspects, less than 3.5 Slm. Photoresist, ion implantation photoresist, polymer, residue or A similar organic substance is selectively removed from the substrate by reaction with an atom that is excited or energized by the plasma (ie, 20 201220006 active species). The reaction can be optically detected to detect the endpoint, such as It is known to those skilled in the art. Alternatively, the plasma ashing process is followed by a rinsing step 'to remove volatile characters and/or wash away a removable compound formed during the plasma treatment. In one embodiment, although the rinsing step employs deionized water, it may also include ammonium hydroxide, sulfuric acid, hydrofluoric acid, or the like. The rinsing step (if used) It can include a spin rinse for about 1 to 10 minutes, followed by a spin drying process. For example, the plasma hardware configuration can be modified to increase the ratio of slow-diffusing species to rapidly diffusing species or increase the ratio of reactive nitrogen to reactive oxygen species. In one embodiment, a sweeping material (eg, an atomic and/or ionic oxygen interposer) and/or a catalyst material is disposed between the substrate and the plasma source such that an excited state of molecular oxygen is produced and the plasma is reduced. The amount of rapidly spreading species in the medium. This filter may be a catalytic filter material, a surface recombination transition, a gas phase recombination filter or the like. For example, the filter can be a surface reactive metal or metallic alloy, ceramic, quartz or sapphire material, while the reactive gas passes through the filter prior to interaction with the wafer surface. The efficacy of this filter can be enhanced by controlling the temperature of the reactive surface and the shape and surface roughness of the reactive surface. The location of the sweeping material can be in close proximity to the substrate because the excited state molecules have a relatively long lifetime. More specifically, the sweeping material can be located about 8 cm or less from the workpiece (substrate). In another embodiment, the plasma ashing tool using a double baffle is modified such that the upper baffle is formed of quartz (as opposed to sapphire), and it is also found in 2012 20126 that the addition of reactive nitrogen to reactive oxygen species has been found. proportion. A similar effect was observed when sapphire or other materials were used instead of quartz to form a plasma tube. A suitable sweeping material that can be used to reduce the content of rapidly diffusing species (specifically 〇, 〇*, 〇+ and/or 〇-) in the plasma, with a recombination coefficient equal to or greater than about 5x10·4 〇 Although exemplary materials for sweeping atomic oxygen are listed in the table of FIG. 2A, they may include, without limitation, metals (eg, B, Mg, A Be, Ti, Cr, Fe, Μη, Νί, Rb, Ir, Pb, Sr, Ba, Cs, alloys thereof, intermetallic compounds (for example, PrNi5, NtNi) and the like), ceramics (for example)
Ti02、Ta205、Zr〇2、a12〇3、FeO 和類似者)、半導體(例如Ti02, Ta205, Zr〇2, a12〇3, FeO, and the like), semiconductor (for example
Si、Ge和類似者)或有機金屬。範例性的原子氧掃除氣體包 括而不限於腿3、C0、N0、CH4、其他碳氮化合物、說碳 化合物和類似者。適合形成活性氣的催化劑包括而不限於 金屬(例如 Fe、Co、Ni、Ru、Re、pt、M〇、pd 和類似者) 或陶竞(例如MgAl2〇4和類似者)。活性氮的形成也可以藉由 以下方式而促進:採用氣體添加物(例如He、Ar、Kr、Xe)、 電聚來源的元件設計(例如電梁來源表面材料和溫度)、電聚 來源的操作方法(例如激發頻率、功率密度、電子溫度、氣 體混合比例)或類似者。 2另一具體態樣’掃除性材料直接或間接加熱到2〇〇〇c 或更高的溫度,以增進片早葡沾舌 _ ·曰琨席于氧的重新組合。圖17圖形化顯 :ai2〇3和Sl〇2的重新組合增加為溫度的函數。大部分材 料的重新組合速率在升高溫度下會有所增加。 於.另一具.體態樣,可以#用搞队ω· ΛΓ 使用%除性氣體來取代或者附 22 201220006 加於掃除性材料和/或集氣材料。原子氧掃除氣體可以組 合以上述的電漿來源,其中掃除氣體有效之處在於進一步 減少原子氡含量成約1/4或更少。用於進一步減少快速擴散 物種的範例性掃除氣體是NH3,其中氣體混合物中之題3 對〇2的比例會超過2比1。 於另-具體態樣,利用下游電漿灰化器而在反應性物 種暴露於基板之前便選擇性地移除帶電粒子,例如市售可 得自美國麻州Beverly的Axcelis科技公司之商標為RpS32〇 的下游微波電談灰化器。對於FE0L處理來說,—般在將基 板暴露於反應性物種之前便想要從反應性物種移除實質上 所有的帶電粒子。以此方式,基板不會暴露於可能有害地 影響基板電性質的帶電粒子。基板乃暴露於電中性的反應 性物種以進行光阻、聚合物和/或殘餘物的移除,依據本 即暴露於氮⑽)、氧(〇*)、可選料氫⑼)和類似者 的活性物種。 先進設計規則之額外的/冒出的要求是須要維持電聚 又化方法與高k介電質和金屬間極材料的相容性。為了促 進相容性,—氧化二氮氣體混合物或上面討論之任何可以 來日加活性氮對活性氧比例的多樣機制可以包括 物,其經選擇以減少對這些材料的損傷,同時維持足夠的 反應性以移除光阻和佈植的殼> 白杯品 I層材枓。適合的化學添加物 匕括而不限於含_素材料,例如CF4、CHF3、Si, Ge and the like) or organometallic. Exemplary atomic oxygen sweep gases include, but are not limited to, legs 3, C0, N0, CH4, other carbonitrides, carbon compounds, and the like. Catalysts suitable for forming an active gas include, without limitation, metals (e.g., Fe, Co, Ni, Ru, Re, pt, M?, pd, and the like) or Tao Jing (e.g., MgAl2?4 and the like). The formation of reactive nitrogen can also be promoted by the use of gas additives (eg He, Ar, Kr, Xe), elemental design of electropolymer sources (eg, beam-derived surface materials and temperatures), operation of electropolymer sources Methods (eg, excitation frequency, power density, electron temperature, gas mixing ratio) or the like. 2 Another specific aspect of the sweeping material is directly or indirectly heated to a temperature of 2 〇〇〇 c or higher to enhance the re-combination of the tablets. Figure 17 graphically shows that the recombination of ai2〇3 and S1〇2 is a function of temperature. The rate of recombination of most materials increases at elevated temperatures. In addition, the other body shape can be used to replace the material with ω· ΛΓ using % degassing gas or add 2012 201220006 to sweeping materials and/or gas gathering materials. The atomic oxygen sweep gas may be combined with the above-described plasma source, wherein the sweep gas is effective in further reducing the atomic germanium content to about 1/4 or less. An exemplary sweep gas used to further reduce rapidly diffusing species is NH3, where the ratio of the 3 to 〇2 in the gas mixture will exceed 2 to 1. In another aspect, the downstream plasma ashing device is utilized to selectively remove charged particles prior to exposure of the reactive species to the substrate, such as commercially available from Axcelis Technologies, Inc. of Beverly, MA, under the trademark RpS32. The downstream microwave oven talks about the ashes. For FEOL treatment, it is desirable to remove substantially all of the charged particles from the reactive species before exposing the substrate to reactive species. In this manner, the substrate is not exposed to charged particles that may adversely affect the electrical properties of the substrate. The substrate is exposed to an electrically neutral reactive species for removal of photoresist, polymer and/or residue, which is exposed to nitrogen (10), oxygen (〇*), optional hydrogen (9), and the like. Active species. The additional/emergence requirement of advanced design rules is the need to maintain the compatibility of the electropolymerization method with high-k dielectric and intermetallic materials. To promote compatibility, the oxidized dioxane mixture or any of the various mechanisms discussed above for the ratio of active nitrogen to active oxygen can be included, selected to reduce damage to these materials while maintaining adequate response. Sex to remove photoresist and implanted shells> White Cup I layer. Suitable chemical additives include, but are not limited to, materials containing _, such as CF4, CHF3,
Br、HCl、Cl2、BCl3、CH3C1、CH2ci2 和類似者。r、 可以有效地使用上面討論的含齒素添加物,以增進移 23 201220006 除光阻層中稱為離子佈植光阻殼層的部分。於其他具體態 樣,可以使用包括活性氮、活性氧、活性氫物種的電漿以 有效移除殼層。舉例來說,電漿可以由Nh3、〇2、形成氣 體的氣體混合物所形成,其有效移除殼層和底下的光阻。 於其他具體態樣,可以使用多步驟的電漿灰化方法以移除 殼層,接著是侵略性的電漿化學物質,再來是較不具侵略 性的電漿化學物質,如此以移除底下之非交聯的光阻、聚 合物、殘餘物,其可選用地再接著做鈍化或殘餘物移除電 漿步驟。舉例而言,為了於離子佈植光阻的電漿灰化期間 保護閘極和/或閘極介電質,第一步驟或可包括以包括含 齒素添加物的一氧化二氮氣體混合物來形成電漿以移除光Br, HCl, Cl2, BCl3, CH3C1, CH2ci2 and the like. r. The dentate-containing additive discussed above can be effectively used to enhance the migration of the portion of the photoresist layer called the ion-implanted photoresist layer. In other specific aspects, a plasma comprising reactive nitrogen, active oxygen, active hydrogen species can be used to effectively remove the shell. For example, the plasma can be formed from a gas mixture of Nh3, 〇2, which forms a gas which effectively removes the underlayer and the underlying photoresist. In other embodiments, a multi-step plasma ashing process can be used to remove the shell layer, followed by an aggressive plasma chemistry, followed by a less aggressive plasma chemistry, to remove the underlying The non-crosslinked photoresist, polymer, residue, which is optionally followed by a passivation or residue removal plasma step. For example, to protect the gate and/or gate dielectric during plasma ashing of the ion implant photoresist, the first step may alternatively include a nitrous oxide gas mixture comprising a dentate-containing additive. Forming plasma to remove light
性氮對活性氧比例的電漿。A plasma of a ratio of nitrogen to active oxygen.
對於矽具有大於10,000 : 10,000 : 1的灰化選擇性。 24 201220006 子侦^具體態樣,該方法是多步驟過程,其有效移除離 、,阻。如上面所注意的,離子佈植光阻一般包括上 卩#下心其中上部的交聯密度高於下部而為暴露於離子 2植的函數°多步驟過程可以包㈣—步驟:將光阻層暴 露於由包括贿3的氣體混合物所形成之每立方公分小於約 70瓦的低密度電漿而移除實質上整個上部,其中NH3構成 了氣體混合物的主要部分。錢可以使料同的.電漿來移 除下部。舉例而言,可以將光阻層暴露於由包括NH3的氣 體混合物所形成之每立方公分至少約7〇瓦的高密度電漿而 移除下。卩其中NH3構成了氣體混合物的主要部分。任何 可能留下的殘餘物然後可以視需要而使用沒有NH3的不同 電漿來移除,例如由氮氣或形成氣體的氣體混合物所形成 的電漿。如果想要的話,表面也可加以鈍化。 光阻一般是有機光敏膜,其用於轉移影像到底下的基 板本發月般可應用於灰化使用於g線、i線、DUV、1 93 奈米、157奈米、電子束、Euv、浸沒式微影術應用或類似 者的那些光阻。它們包括但不限於酚醛清漆、聚乙烯酚、 丙烯酸酯、醛類、聚亞醯胺、酮類、環烯烴或類似者。熟 於此技藝者鑑於本揭示將顯然知道其他適合用於本發明的 光阻配方。光阻可以是正作用或負作用的,此視所選的光 阻化學物質和顯影劑而定。 基板基本上可以是用於製造積體電路的任何半導體基 板。適合的半導體基板一般包括或可以包含矽、應變矽、 矽鍺基板(譬如SiGe)、矽在絕緣體上、高k介電材料、金 25 201220006 屬(:如/、Ti、™、TaN和類似者)、GaAs、碳化物、氮 化、氧化物和類似者。有利而言,該方法可應用 =有材料從半導體基板漏失(例如於換雜區域上)的元件 其不是要限制本 下面的實施例只是為了示範而提出 發明的範圍。 實施例1 於此實施例,彼覆於矽基板上的光阻在市售可得自 Axcelis科技公司的RapidStrip32〇電漿灰化工具中乃暴露 於一氧化二氮剝除性化學物質。光阻是丨線光阻,並且沉積 於矽基板上的厚度有丨.9微米,電漿化學物質是將一氧化二 氮氣體以每分鐘7標準公升(sim)流入壓力t托耳溫度 240°C、功率設定為350〇瓦的電漿灰化工具而形成。又 一氧化二氮電漿剝除過程的灰化速率、跨晶圓均勻 度、氧化物成長是與無氧的還原性電漿(形成氣體)和基於氧 的電漿做比較。還原性電漿是由形成氣體(氮中有3%的氫) 的氣體混合物以流動速率7 slm流入壓力1托耳、溫度 240°C、功率設定為3500瓦的電漿灰化工具而形成。基於 氧的電漿則使用90%的氧(〇2)和1〇%的形成氣體(氮中有3% 的氫)以7 slm流入溫度240。〇、功率設定為3500瓦的電毁 灰化工具而形成。 光阻暴露於個別電漿8或15秒之後,測量灰化速率和 非均勻度。將未彼覆的石夕基板暴露於個別電梁3 0 0秒,藉 此測量氧化物成長。 26 201220006For 矽 there is a ashing selectivity greater than 10,000: 10,000:1. 24 201220006 Sub-detection concrete, this method is a multi-step process, which effectively removes the separation and resistance. As noted above, the ion implantation photoresist generally includes a lower density of the upper part of the upper 而# lower than the lower part and a function of exposure to the ion 2 implant. The multi-step process can be packaged (IV) - step: exposing the photoresist layer The substantially entire upper portion is removed from a low density plasma of less than about 70 watts per cubic centimeter formed by a gas mixture comprising bribes 3, wherein NH3 constitutes a major portion of the gas mixture. Money can be made the same. Plasma to remove the lower part. For example, the photoresist layer can be removed by exposure to a high density plasma of at least about 7 watts per cubic centimeter formed by a gas mixture comprising NH3. NH wherein NH3 constitutes the main part of the gas mixture. Any residue that may remain may then be removed using a different plasma without NH3, such as a plasma formed from a gas mixture of nitrogen or gas. The surface can also be passivated if desired. The photoresist is generally an organic photosensitive film, and the substrate for transferring the image to the bottom can be applied to ashing for use in g-line, i-line, DUV, 193 nm, 157 nm, electron beam, Euv, and the like. Immersion lithography applications or similar photoresists. These include, but are not limited to, novolacs, polyvinyl phenols, acrylates, aldehydes, polyamidones, ketones, cyclic olefins or the like. Those skilled in the art will be aware of other photoresist formulations suitable for use in the present invention in view of this disclosure. The photoresist can be positive or negative depending on the selected photoresist chemical and developer. The substrate can be essentially any semiconductor substrate used to fabricate integrated circuits. Suitable semiconductor substrates generally include or may comprise germanium, strained germanium, germanium substrates (such as SiGe), germanium on insulators, high-k dielectric materials, gold 25 201220006 genus (eg, /, Ti, TM, TaN, and the like) ), GaAs, carbide, nitride, oxide and the like. Advantageously, the method is applicable to an element having material lost from the semiconductor substrate (e.g., over a mismatched area). It is not intended to limit the scope of the invention below for illustrative purposes only. EXAMPLE 1 In this example, the photoresist on the ruthenium substrate was exposed to nitrous oxide flaking chemicals in a RapidStrip 32 〇 plasma ashing tool commercially available from Axcelis Technologies. The photoresist is a tantalum photoresist and has a thickness of 99 μm deposited on the ruthenium substrate. The plasma chemistry is a nitrous oxide gas flowing at a pressure of 7 standard liters per minute (sim) to a pressure tTorr temperature of 240°. C. The power is set to a 350 watt plasma ashing tool. The ashing rate, cross-wafer uniformity, and oxide growth of the nitrous oxide plasma stripping process are compared to oxygen-free reducing plasma (forming gas) and oxygen-based plasma. The reducing plasma was formed by a gas mixture forming a gas (3% hydrogen in nitrogen) at a flow rate of 7 slm into a plasma ashing tool having a pressure of 1 Torr, a temperature of 240 ° C, and a power setting of 3,500 watts. The oxygen-based plasma uses 90% oxygen (〇2) and 1% of the formation gas (3% hydrogen in the nitrogen) to flow to a temperature of 240 at 7 slm. 〇, the power is set to 3500 watts of electric ashing tools. The ashing rate and non-uniformity were measured after the photoresist was exposed to individual plasma for 8 or 15 seconds. Oxide growth was measured by exposing the unexposed Shishi substrate to individual electric beams for 300 seconds. 26 201220006
圖4示範結果。如所預期的 A 貝朋的,基於氧的電漿之氧化物 成長顯著有約12 A,並且展規备八# &,n 敬見母77 4里約7.8微米的最高灰化 速率》相對而t,還原性電衆和—氧化二氮電漿相對於基 於氧的電漿則顯示顯著改善,但是有較低的灰化速率。基 於一氧化二氮的電聚相較於還原性電漿展現.較少的氧化物 成長;相較於還原性電漿的約4人,其於 ^ ,, ^ l ^ ^ J Λ 丞於一氧化二氮的電漿 是約3.0Α。顯而易見地,相較於還原性電漿之每分鐘約1〇 微米的灰化速率,基於一氧化二氮的電漿展現每分鐘約4·4 微米的灰化速率》同時,在相同的處理條件下,基於一氧 化二氮的電漿之灰化非均勻度(非均勻度=2·8%)乃顯著優於 氧/形成氣體(>10%)。 實施例2 於此實施例,小量的CF4添加到不同的電漿氣體混合 物,並且於RapidStripS320電漿灰化工具中處理。石夕基板 暴露於不同的電漿化學物質,並且測量氧化物的成長。結 果顯示於底下表1。於每一情況,多樣的電漿乃使用流動速 率7 s 1 in的氣體合物來流入壓力1托耳、功率設定為3 5 0 0 瓦的電漿灰化工具而形成。 表1 電漿化學物質 過程時間(秒) 氧化物成長 cf4/ n2o 103 3.24 CF4/ 3% 〇2 /形成氣體 103 9.54 CF4 / 90% 〇2 /形成氣體 103 8.76 3% 〇2 /形成氣體 140 9.82 27 201220006 如所示,於形成電漿期間添加小量的CF4導致最少的基 板漏失,如氧化物的成長所證實,並且有利地可以預期產 出更具有能量的物種,相對於實施例工所觀察到的結果而 言這應該會有效增加灰化速率。CF"N2〇的電漿具有最高 的活性氮對活性氧的比例,其也展現最少的氧化量。 實施例3 於此實施例,就碎漏失、氧化物成長和氧化物漏失而 言,使用RapidStrip32〇電漿灰化工具和由一氧化二氮所形 成的電漿(亦即標示為新科技)來測量基板損傷,其與先前技 藝之〇2 /形成氣體混合物所形成而具有和沒有小量四氟化 奴的電漿來比較。形成氣體的組成是氮裡有3。的氫。結果 乃圖形化顯示於圖5A。於每一情況,多樣的電漿乃使用流 動速率7 slm的氣體混合物流入壓力i托耳、溫度24〇£>c、 功率設定為3500瓦的電漿灰化工具而形成。基板損傷包 括·⑴來自矽在絕緣體上(snicon_on_insuiat〇r,s〇I)測試結 構的矽漏失’·(ii)裸矽測試晶圓上的矽氧化物成長;以及來 自矽熱氧化物測試晶圓的矽氧化物漏失。圖5B和5c比較 ρ-MOS高劑量離子佈植清潔應用後的掃描式電子顯微影 像。SEM影像顯示的是電漿剝除之後接著去離子水沖洗, 其中電漿是由〇2和A/H2氣體混合物所形成(圖5C)以及 .是由一氧化二氮氣體所形成,其指出實質上改善了來自一 氧化二氮氣體混合物之電漿的殘餘物移除能力。 結果清楚顯示具有比較高活性氮對活性氧之比例的電 漿實質減少了基板損傷。從沒有四氟化碳的氧化性電漿則 28 201220006 觀察到殘餘物。此外,如圖 。 卜如圖5B和5C所注意的,使用 化-氮電漿則顯著改善了殘餘物的移除。 實施例4 於例,於電聚處理期間監視摻雜物漏失、基板 失和灰化速率,其使用的多種電漿分別是由-氧化-氮 氣體、形成氣體(3%的Η2, 97α/& 匕匕 乳化一氮 俨m。/、w 幻2的⑹、氧氣(9〇%)和形成氣 的κ 有兩氣氣量的形成氣體(亦即9〇%的&和1〇% 、-遠1之二合物)所形成。所有的電聚都是以7Slm的總氣體 机逮和3500瓦的微波功率 形成。基板於電漿處理期間加 ‘、、、到240。(:的溫度。石夕氧化仍 從八 /乳化過程時間為5分鐘。決定阻劑Figure 4 shows the results. As expected, A-Bippen's oxide-based plasma oxide growth is significantly about 12 A, and the exhibition specification 八# &, n respects the mother 77 4, the highest ashing rate of about 7.8 microns. While t, the reducing electricity and the nitrous oxide plasma showed a significant improvement over the oxygen-based plasma, but with a lower ashing rate. The electropolymerization phase based on nitrous oxide shows less oxide growth than the reducing plasma; compared to about 4 people of the reducing plasma, it is in ^, ^ ^ ^ ^ J Λ 一The plasma of nitrous oxide is about 3.0 Torr. Obviously, the nitrous oxide-based plasma exhibits an ashing rate of about 4.4 microns per minute compared to a ashing rate of about 1 〇 micrometer per minute of the reducing plasma. Meanwhile, under the same processing conditions The ashing non-uniformity of the nitrous oxide-based plasma (non-uniformity = 2.8%) is significantly better than the oxygen/forming gas (> 10%). Example 2 In this example, a small amount of CF4 was added to a different plasma gas mixture and processed in a RapidStrip S320 plasma ashing tool. The Shixi substrate is exposed to different plasma chemicals and the growth of oxides is measured. The results are shown in Table 1 below. In each case, a variety of plasmas were formed using a gas composition with a flow rate of 7 s 1 in for a plasma ashing tool with a pressure of 1 Torr and a power setting of 3,500 watts. Table 1 Plasma Chemical Process Time (seconds) Oxide Growth cf4/ n2o 103 3.24 CF4/ 3% 〇2 / Forming Gas 103 9.54 CF4 / 90% 〇2 / Forming Gas 103 8.76 3% 〇2 / Forming Gas 140 9.82 27 201220006 As shown, the addition of a small amount of CF4 during the formation of plasma results in minimal substrate loss, as evidenced by the growth of oxides, and it is advantageously expected to produce more energetic species, as observed with respect to the example work. As a result, this should effectively increase the ashing rate. CF"N2〇 plasma has the highest ratio of reactive nitrogen to active oxygen, which also exhibits the least amount of oxidation. Example 3 In this example, in terms of shatter loss, oxide growth, and oxide loss, a RapidStrip 32 〇 plasma ashing tool and a plasma formed of nitrous oxide (also labeled as new technology) were used. The substrate damage was measured as compared to the prior art 〇2/forming gas mixture with plasma having no small amount of tetrafluorinated. The composition of the forming gas is 3 in the nitrogen. Hydrogen. The results are graphically shown in Figure 5A. In each case, a variety of plasmas were formed using a gas mixture having a flow rate of 7 slm into a pressure iTorr, a temperature of 24 Torr, and a plasma ashing tool with a power setting of 3,500 watts. Substrate damage includes (1) 矽 矽 矽 绝缘 绝缘 绝缘 绝缘 绝缘 绝缘 绝缘 绝缘 绝缘 绝缘 绝缘 绝缘 绝缘 绝缘 ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii ii The ruthenium oxide is lost. Figures 5B and 5c compare scanning electron microscopy images after ρ-MOS high dose ion implantation cleaning applications. The SEM image shows plasma stripping followed by deionized water rinsing, where the plasma is formed from a mixture of 〇2 and A/H2 gases (Fig. 5C) and is formed by nitrous oxide gas, which indicates the essence. The residue removal capability of the plasma from the nitrous oxide gas mixture is improved. The results clearly show that the plasma having a relatively high ratio of active nitrogen to active oxygen substantially reduces substrate damage. The residue was observed from an oxidative plasma without carbon tetrafluoride 28 201220006. In addition, as shown in the figure. As noted in Figures 5B and 5C, the use of a chemical-nitrogen plasma significantly improves the removal of the residue. Example 4 For example, during the electropolymerization process, dopant leakage, substrate loss, and ashing rate were monitored, and the various plasmas used were composed of -oxidized-nitrogen gas, forming gas (3% Η2, 97α/& ; 匕匕 emulsified a nitrogen 俨 m. /, w 幻 2 (6), oxygen (9 〇%) and gas forming κ have two gas volume forming gas (that is, 9 〇% & and 1〇%, - All of the electropolymerization is formed by a total gas generator of 7 Slm and a microwave power of 3,500 watts. The substrate is charged with ',,, to 240 during the plasma treatment. The oxidation of Shixi is still from the eight/emulsification process time of 5 minutes.
移除的過程時間是8秒哎〗^ A 疋衫次15秒。對於摻雜物分布輪廓測 武,地毯式石夕晶圓乃遵循標準配方而佈植以As或BP"晶 0然後暴露於多樣的灰化電漿達5分鐘,並且在⑼代退 火1 〇秒。進行二次離子質譜(seeQndary -咖“ speet_, SIMS)分析以決定摻雜物公龙 心雜物刀布輪廓,以及進行片電阻(RS)測 以決定片電阻。結果乃圖形化顯示於圖6。 如所不’使用最高的活性氮對活性氧比例所形成的電 ’對於AS和BF2佈植都展現穩健的行為,另外還有比較高 2灰化速率和低氧化速率。此外’如所預期的,由包括氧 之氣體混合物所形成的電漿展現令人無法接受的高石夕氧 化。 實施例5 於此實施例,示範了富含活性氣組態的效果。相較於 石英管的組態(非富含氮的組態),以藍寶石管(富含活性氮 29 201220006 的組態)來建構RPS320電漿來源的確導致矽氧化減少(圖 7) °圖8顯示此實施例性的富含氮組態(藍寶石電漿管,相 較於石英電漿管)的確導致活性氮增加,同時活性氧的量實 質上保持未變,而對應之活性氮對活性氧的比例則增加。 圖7進一步示範一氧化二氮電漿之最佳化的組態,其包括 最佳化的微波功率 '溫度 '電漿管組成,而顯示實質上減 少了矽氧化。 如所示’相對於由標準氧和形成氣體組成所形成的電 毁而言’所有由一氧化二氮所形成的電漿都展現較低的氧 化而為移除阻劑的函數。此外,降低溫度和功率設定導致 較低的氧化和增加的灰化速率。再者,相較於形成氣體的 控制電漿,由一氧化二氮所形成的電漿展現快很多的灰化 速率。 實施例6 於此實施例,使用光學發射光譜儀來分析由一氧化二 氮所形成的電漿相對於由90%的氧氣和10%的形成氣體(3〇/〇 Η2 / 97% NO所形成的標準電漿過程》來自每種氣體的電聚 是以RpS320用3 500瓦、總氣體流速7 slm所產生。以0cean Optics公司的光學發射光譜儀透過處理腔室之晶圓高度的 觀看埠來收集電漿的光學發射。 圖9圖形化示範波長為強度的函數。值得注意的是在 約300和380奈米之間的發射訊號,其對應於n2*活性物種 (由一氧化二氮所形成的電漿而產生)。相對而言,標準電聚 過程在這些波長則並未觀察到可分辨量的n2*。如此,則標 30 201220006 準電漿過程之活性氡對活性氮的比例: 顯著高於一 氧化一氮過程。雖然不想受限於理論,不過相信N2*有助於 降低一氧化二氮過程甲的氧化(因為矽_氧化矽界面有明顯 的氮化’如圖2 1所示),但也顯得會導致降低灰化速率。除 了此觀察以外,該圖還圖形化顯示基於一氧化二氮的過程 產出顯著較多的NO。 實施例7 , 於此實施例,使用光學發射光譜儀來測量活性氮物種 對活性氧物種的比例而為微波電漿的函數,該電漿是由一 氧化二氮氣體所形成,使用RapidStrip32〇電漿灰化工具, 電漿化學物質是將一氧化二氮氣體以每分鐘7標準公升 (slm)流入壓力ίο托耳、溫度24〇〇c的電漿灰化工具而形 成。如圖10所示,比例的增加為降低微波功率的函數,其 中1.2的比例是在2.5千瓦的最低評估設定而觀察到。也顯 示了測試一氧化二氮電漿條件下之矽表面氧化的相對量, 其示範了石夕氧化的量對電漿之活性氮和活性氧物種的比例 有良好的關聯。 實施例8 於此貫施例’使用光學發射光譜儀來測量活性氮對活 性氧物種的比例,其中電漿是由以下所形成:(丨)一氧化二 氮氣體,(η)帶有CF4添加物的一氧化二氮氣體;(出)9〇〇/〇 的氧氣和10%的形成氣體(3% h2/ 97% N2)的混合物;以及 (lv) 9 0%的氧氣和1〇%的氮氣的混合物。為了示範,圖丄丄 所示的不同電漿之活性氧和活性氮的測量量乃加以正規 31 201220006 化,以反映〇2瑪電㈣數值。對應之活性氣對活性氧的 比例實質上高於-氧化二氮氣體混合物所形成的電I,並 且低於由〇2+FG氣體混合物所形成的電漿,這與稍早報導 的矽氧化量有良好的關聯。值得注意的是活性氧的量在所 有四種評估電漿中係比較類似,並且電漿中之活性氮的量 則有顯著差異。 實施例9 於此實施例,圖12圖形化示範氧化性電漿之矽氧化的 量為電子溫度的函數。由90%的氧氣和1〇%的形成氣體所 形成的電漿顯示矽氧化隨著電漿的電子溫度增加而呈指數 乓加。低的石夕氧化需要維持在低於約5 . 〇電子伏特的低電子 溫度。 實施例1 0 於此實施例,測量多樣電漿之矽基板的氧化物成長和 光阻的灰化速率。電漿是以不同的氣體混合物並且使用功 率設定為3500瓦、氣體流速7 Sim、溫度245°c的 RapidStrip320電漿灰化器而形成。氣體混合物包括:(a) 〇2 和形成氣體(3% 氫 / 氮);(b) n2〇 ; (c) n2O + 0.3% 的 CF4 ; (d) 贿3和02;(e)形成氣體(3%氫/氮)+10%的N20;以及⑴ 1^-1^+1〇%的να。光阻移除之前,矽基板具有以下四種佈 植.(!)非晶化佈植;(ii)碳佈植;(iii)鹵素佈植;以及(iv) 延伸佈植+。 在離子佈植、光阻灰化、溼式清潔步驟之後由上而下 的掃描式電子顯微圖,該清潔步驟包括傳統的氫氧化銨-過 32 201220006 氧化氫混合物(ammonium hydroxide-hydrogen peroxide mixture,ΑΡΜ) / 過乳化硫混合物(sulfuric peroxide mixture,SPM)。APM清潔步驟包括將基板暴露於NH4OH : H2〇2 : H2〇混合物(氫氧化銨-過氧化氫混合物),也已知為 SCI (Standard clean 1,標準清潔 1)或 RCA 1。SPM 方法也 稱為「皮蘭那魚清潔」(piranha clean),其包括將基板暴露於 100°C〜130°C的ΗΑ〇4 : Ηζ〇2溶液。基板然後以去離子水 沖洗並乾燥。如所示’所有顯微圖都明顯有殘餘物,例外 的疋以(c) N2〇 + CF4和(d) NH3+〇2二種氣體混合物形成之電 漿所處理的基板。 底下表2提供多樣電聚的氧化物成長和灰化速率沾 果。單次氧化物成長的結果代表以表2對應的電讓化學‘ 質來單次處理晶圓之後所測量的氧化物成長。每個晶圓和 電聚化學條件實質上相同的,藉此顯示不同電t化學物質 =功效。二十次氧化物成長速率代表晶圓以電聚化: 處理2〇次之後所測量的氧化物成長。相信二十次氣化 物成長的測量實質上減少測量誤差。 氣化 表2The process time for removal is 8 seconds ^ ^ A 疋 shirt times 15 seconds. For the measurement of dopant profile, the carpet-type Shixi wafer is implanted with As or BP" crystal 0 and then exposed to various ashing plasmas for 5 minutes, and annealed at (9) generation for 1 sec. . Secondary ion mass spectrometry (seeQndary-cafe "speet_, SIMS" analysis was performed to determine the contour of the doping Gonglongxin knife cloth, and sheet resistance (RS) was measured to determine the sheet resistance. The results are graphically shown in Figure 6. If you do not use the highest active nitrogen to the ratio of active oxygen, the 'electricity' exhibits robust behavior for both AS and BF2 implants, as well as higher 2 ashing rates and lower oxidation rates. In addition, as expected The plasma formed by the gas mixture including oxygen exhibits an unacceptably high oxidation. Example 5 This example demonstrates the effect of an active gas-rich configuration compared to the configuration of a quartz tube. (Non-nitrogen-rich configuration), the construction of the RPS320 plasma source with a sapphire tube (configured with active nitrogen 29 201220006) does result in reduced ruthenium oxidation (Figure 7). Figure 8 shows this example rich The nitrogen configuration (sapphire plasma tube, compared to the quartz plasma tube) does cause an increase in reactive nitrogen, while the amount of active oxygen remains virtually unchanged, while the corresponding proportion of reactive nitrogen to active oxygen increases. demonstration Optimized configuration of nitrous oxide plasma, which includes optimized microwave power 'temperature' plasma tube composition, while showing substantially reduced ruthenium oxidation. As shown by 'relative to standard oxygen formation In the case of electrical destruction due to gas composition, all plasmas formed from nitrous oxide exhibit lower oxidation as a function of removal of the resist. In addition, lowering temperature and power settings results in lower oxidation and increase. The ashing rate. Furthermore, the plasma formed by nitrous oxide exhibits a much faster ashing rate than the gas-forming control plasma. Example 6 This example was analyzed using an optical emission spectrometer. The plasma formed by nitrous oxide is derived from the electropolymerization of each gas with respect to 90% oxygen and 10% of the formation gas (standard plasma process formed by 3〇/〇Η2 / 97% NO). The RpS320 was produced with 3,500 watts and a total gas flow rate of 7 slm. The optical emission of the plasma was collected by the optical emission spectrometer of 0cean Optics Inc. through the wafer height of the processing chamber. Figure 9 graphically demonstrates the wavelength of intensity. Function. worth It is intended to be a signal between about 300 and 380 nm, which corresponds to the n2* active species (produced by a plasma formed by nitrous oxide). In contrast, the standard electropolymerization process is at these wavelengths. No resolvable amount of n2* was observed. Thus, the ratio of active enthalpy to reactive nitrogen in the quasi-plasma process of 201220006 is significantly higher than that of nitric oxide-nitrogen. Although not limited by theory, it is believed that N2* It helps to reduce the oxidation of alpha in the nitrous oxide process (because the yttrium oxide interface has obvious nitridation 'as shown in Figure 21), but it also appears to cause a reduction in the ashing rate. In addition to this observation, the figure It also graphically shows that the nitrous oxide-based process produces significantly more NO. Embodiment 7 In this embodiment, an optical emission spectrometer is used to measure the ratio of reactive nitrogen species to reactive oxygen species as a function of microwave plasma, which is formed by nitrous oxide gas using RapidStrip 32 〇 plasma The ashing tool, the plasma chemistry, is formed by nitrating nitrous oxide gas at a pressure of 7 standard liters per minute (slm) into a pressure ίοTorr, a plasma ashing tool at a temperature of 24 〇〇c. As shown in Figure 10, the increase in ratio is a function of the reduction in microwave power, with a ratio of 1.2 observed at a minimum evaluation setting of 2.5 kW. The relative amount of ruthenium surface oxidation under nitrous oxide plasma conditions was also shown, which demonstrates that the amount of shi oxidized has a good correlation with the ratio of reactive nitrogen to reactive oxygen species in the plasma. Example 8 In this example, an optical emission spectrometer was used to measure the ratio of reactive nitrogen to reactive oxygen species, wherein the plasma was formed by (丨) nitrous oxide gas, (η) with CF4 additive. Nitrous oxide gas; (out) a mixture of 9 〇〇 / 〇 oxygen and 10% forming gas (3% h2 / 97% N2); and (lv) 90% oxygen and 1% nitrogen mixture. For demonstration purposes, the measured amounts of reactive oxygen and reactive nitrogen in the different plasmas shown in Figure 加以 are normalized to reflect the 〇2Ma (4) value. The ratio of the corresponding active gas to active oxygen is substantially higher than the electric I formed by the nitrous oxide gas mixture, and lower than the plasma formed by the 〇2+FG gas mixture, which is related to the amount of ruthenium oxide reported earlier. Have a good connection. It is worth noting that the amount of active oxygen is similar in all four evaluation plasmas, and the amount of reactive nitrogen in the plasma is significantly different. EXAMPLE 9 In this example, Figure 12 graphically illustrates the amount of ruthenium oxidation of an oxidative plasma as a function of electron temperature. The plasma formed by 90% oxygen and 1% by volume of the forming gas shows that the ruthenium oxidation is exponentially added as the electron temperature of the plasma increases. Low Zeolite oxidation needs to be maintained at a low electron temperature below about 5. 〇 electron volts. Example 10 In this example, the oxide growth of the tantalum substrate of various plasmas and the ashing rate of the photoresist were measured. The plasma was formed as a different gas mixture and using a RapidStrip 320 plasma asher with a power setting of 3500 watts, a gas flow rate of 7 Sim, and a temperature of 245 °C. The gas mixture includes: (a) 〇2 and forming gas (3% hydrogen/nitrogen); (b) n2〇; (c) n2O + 0.3% CF4; (d) bribes 3 and 02; (e) gas formation ( 3% hydrogen/nitrogen) + 10% N20; and (1) 1^-1^+1%% να. Prior to photoresist removal, the ruthenium substrate has the following four implants (!) amorphized implants; (ii) carbon implants; (iii) halogen implants; and (iv) extended implants +. A top-down scanning electron micrograph after the ion implantation, photoresist ashing, and wet cleaning steps, the cleaning step including a conventional ammonium hydroxide-over 32 201220006 hydrogen peroxide mixture (ammonium hydroxide-hydrogen peroxide mixture) , ΑΡΜ) / Sulfuric peroxide mixture (SPM). The APM cleaning step involves exposing the substrate to a NH4OH:H2〇2:H2〇 mixture (ammonium hydroxide-hydrogen peroxide mixture), also known as SCI (Standard clean 1, Standard Clean 1) or RCA 1. The SPM method, also known as "piranha clean," involves exposing the substrate to a ΗΑ〇4: Ηζ〇2 solution at 100 °C to 130 °C. The substrate is then rinsed with deionized water and dried. As shown, 'all micrographs are clearly residueed, with the exception of the substrate treated with a plasma formed by a mixture of (c) N2〇 + CF4 and (d) NH3 + 〇2. Bottom Table 2 below provides oxide growth and ashing rate dilution for various electropolymerizations. The results of the single oxide growth represent the oxide growth measured after a single treatment of the wafer with the corresponding electrochemistry of Table 2. Each wafer and electropolymerization chemistry are essentially the same, thereby showing different electrical t chemistries = efficacy. Twenty times the oxide growth rate represents the wafer to be electropolymerized: the oxide growth measured after 2 treatments. It is believed that the measurement of twenty gas growths substantially reduces measurement errors. Gasification Table 2
33 201220006 NH3 + 30% 〇9 一 0.83 ----* 2 0 NH3+10% FG 一 ----- 0 9 N^O ———· 0.54 ---------- 4 Π 〇2 / FG 1.15 1, ——--- 7 Q n2o+cf4 1.95 / . 〇 ..…----- 3.0 ----~~-___3.0 從20次氧化物成長測量可以看出,自N2〇 + cF4氣體尾 合物所形成的電毁具有比較高的石夕基板損傷(相較於其他’電 漿化學物質而言),如氧化物成長的量所證實。相對而言, 由包括NH3 + 〇2氣體混合物所形成的電毁展現最少的石夕氧 化(0.43A /次,1〇%的〇2混合物),其相當於〇 19人〆次的 矽漏失,遠低於ITRS所設定之32奈米世代的〇·3Α門檻。 於氧化過程期間,假設氧化期間所消耗的每一 Α矽是轉換 成2.2Α的氧化矽。因此,氧化物成長測量到的〇43Α指出 有0.19Α的矽轉換為氧化矽(〇 19Α χ 2 2人=〇 43Α)β改變比 / G ΝΗ3 + 30 /ό 〇2氣體混合物所提供)則增加阻劑的移除速 率,但也增加矽損傷的量。9〇%NH3_F(}混合物具有比9〇% NH3 〇2混合物還低的矽基板氧化,但也展現較低的灰化速 率,其轉而會減少·產率。 實施例11 於此實施例,評估幾種用於高劑量佈植剝除(HDIS)之 電聚灰化化學物質的矽漏失、TiN氧化、灰化速率、定性的 殘餘物移除效果、佈植物種摻雜物的保持性。矽漏失的測 曰- g · 里疋將石夕基板暴露於溫度在245和275〇C之間、壓力在i 34 201220006 和2托耳之間、微波功率在 7干仕J和4千瓦义間的RapidStrip320 電漿灰化工具中的不同雷喈 冤及化學物質。在處理之前和之後 測量厚度。對於TiN氣化每# ^ t 虱化汗估,包括TiN披覆的基板則暴 露於不同的電漿化學物質β金屬惫 t q貝 兔屬軋化的測量則是比較電漿 處理之前和之後的片電阻(Rs)。定性測量殘餘物的移除。進 行二次離子質譜(SIMS)分析以決定摻雜物的分布輪廟。 表333 201220006 NH3 + 30% 〇9 A 0.83 ----* 2 0 NH3+10% FG 一----- 0 9 N^O ———· 0.54 ---------- 4 Π 〇2 / FG 1.15 1, ——--- 7 Q n2o+cf4 1.95 / . 〇.....----- 3.0 ----~~-___3.0 It can be seen from the 20-time oxide growth measurement The electrical breakdown formed from the N2〇+cF4 gas tail compound has a relatively high damage to the Asahi substrate (as compared to other 'plasma chemistries), as evidenced by the amount of oxide growth. In contrast, the electro-destruction formed by the gas mixture including NH3 + 〇 2 gas exhibited the least amount of Shixia oxidation (0.43 A / time, 1% 〇2 mixture), which is equivalent to the loss of 〇19 people. It is far below the 奈·3Α threshold of the 32nm generation set by ITRS. During the oxidation process, it is assumed that each enthalpy consumed during oxidation is converted to 2.2 Å of cerium oxide. Therefore, 〇43Α measured by oxide growth indicates that 0.19Α of yttrium is converted to yttrium oxide (〇19Α χ 2 2 people = 〇43Α) β change ratio / G ΝΗ3 + 30 /ό 〇2 gas mixture is provided) The rate of removal of the resist, but also increases the amount of damage to the sputum. The 9〇%NH3_F(} mixture has a lower ruthenium substrate oxidation than the 9〇% NH3 〇2 mixture, but also exhibits a lower ashing rate, which in turn reduces the yield. Example 11 In this example, Several types of electro-accumulating chemistries for high-dose implant stripping (HDIS) were evaluated for enthalpy loss, TiN oxidation, ashing rate, qualitative residue removal, and plant species dopant retention.矽 的 曰 - g · 疋 疋 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石 石Different Thunder and Chemicals in the RapidStrip320 Plasma Ashing Tool. Thickness is measured before and after processing. For TiN gasification, every #^t 虱化汗, including TiN-coated substrates, is exposed to different electricity. The measurement of the slurry chemical β metal 惫tq beech is to compare the sheet resistance (Rs) before and after the plasma treatment. Qualitative measurement of residue removal. Perform secondary ion mass spectrometry (SIMS) analysis to determine the blending Distribution of debris in the temple of the wheel. Table 3
V 應用 灰化 化學 物質V application ashing chemicals
Si漏失(A / 次)Si loss (A / time)
關鍵 的 HDIS n2o 0.24Key HDIS n2o 0.24
FG 0.20 90% NH3 和〇2 70% NH3 和〇2 丨.19 0.37 金屬 氧化 TiN △ Rs (%) 47 -10 2 灰化 殘 迷率 餘 As摻 B摻 (微米 物 雜物 雜物 /分 移 漏失 漏失 、鐘) 除 (%) (%) 優 4.〇〇 異 -5.3 -3 -i〇0_ 差 -2 -7 優 — i.i — 異 優 2.〇〇 — 異 35 201220006 90% NH3 和 〜0.2 〜0 0.9 優 異 一 — FG S〇2 和 FG 0.52 45 7.80 良 好. 2.5 13 NH3 / 〇2做法提供了最低的矽漏失 '最少的金屬(Ti)氧 化、優異的光阻和殘餘物移除性質,.藉此提供有效的電激 化學物質以用於高劑量離子佈植剝除後的應用。 實施例12 於此實施例,以光學發射光譜儀來監視不同功率設定 下由90%的NH3和1 0%的02之氣體混合物所產生之電漿的 多樣活性物種。電漿使用功率設定為4000瓦或7800瓦、 總氣體流速5 slm、壓力1托耳、夾盤溫度275°C、腔室壁 溫度140oC的RapidStrip320電漿灰化器而形成。圖13圖 形化示範OH*(在309奈米)、N2*(在337奈米)、H2*(在486 奈米)、H* (在656奈米)、〇2*(在777奈米)於不同功率設定 的發射強度。如所示’增加功率到大於5〇0〇瓦則顯著增加 活性氫(H*和Η/)的發射。此外,也觀察到活性n2*有增加 發射。光谱中明顯沒有任何與原子氧(〇*)有關的顯著發射強 度’雖然乳體混合物裡顯然有一些氧與活性氮反應而形成 活I·生OH 。刖面的資料清楚暗示當使用NR]氣體及其混合 物來產生電及時可以使用功率設定來調整活性說的量,其 36 201220006 可以用於設定想要的灰化速率。 實施例13 於此實施例,以光學發射光譜儀監視NH3/ 1〇%〇2氣體 混合物電漿所產生之多樣活性物種的發射強度而為總氣體 流速和壓力的函數。電漿使用功率設定為7〇〇〇瓦、總氣體 流速3.5 slm或7slm、壓力〇.65、1〇、1.5或2 〇托耳、夾 盤溫度275°C的IntegraES電漿灰化器而形成。圖14圖形 化示範OH*(在309奈米)、N2*(在337奈米)、Η2*(在486 奈米)、Η*(在656奈米)、Ο,(在777奈米)於不同的壓力和 總氣體流速設定的發射強度。如所示,壓力對於多樣活性 物種的形成具有最少的效果或沒有效果。然而,活性氫(Hslt 和Η,)展現對總氣體流動速率很強的依附性。相對於較高 的總氣體流動速率’顯著較面量的活性氫(Η*和η2*)是在較 低的總氣體流動速率下產生。相對而言,活性氮(Ν/)和活 性氧(〇*)沒有展現出對於壓力或流動速率有可感受的回應。 實施例14 於此實施例,示範控制氧擴散過程的效果。圖15顯示 產生自Ν2〇氣體之電漿的最佳化組態和產生自ΝΗ3 / 〇2氣 體混合物之電梁的最佳化組態,兩者皆包括操作於27〇〇c 之最佳化的微波功率密度(>1〇〇瓦/立方公分)。圖16所示 的光學發射光譜則顯示添加的NH3掃除性氣體如何完全移 除所有可測量的原子氧。這二種電漿組態都顯示實質減少 了矽氧化;因為於NH3的情況,掃除性氣體已有效移除= 有的原子氧,而於ΝΖ0的情形,掃除性氣體已增進分子對 37 201220006 原子的比例而提供表面氧化物有效的氮化。另外第三種組 L貝丨示範最大置的氧化物成長和石夕漏失,其代表標準的ο] 和形成氣體電漿剝除,此者尚未最佳化以減少當中之快速 擴散物種的量。-氧化二氮電漿和氨/氧電漿已充分減少 拋物線成長速率,使得所造成的矽氧化僅約為一單層。 實施例1 5 於此實施例,使用光學發射光譜儀來分析使用在此所 述的控制氧擴散方法而由氨和氧所形成的電漿,而相對於 由9〇%的氧氣和10%的形成氣體(3。/。H2 / 97% N2)所形成的 標準電漿過程。來自每種氣體的電漿是於RpS32〇中產生。 以Ocean Optics公司的光學發射光譜儀透過處理腔室之晶 圓高度的觀看埠來收集電漿的光學發射光譜。 圖1 ό圖形化示範波長為強度的函數。值得注意的是在 約3 00和400奈米之間的發射訊號(其對應於〇Η*活性物種) 以及在約750和800奈米之間的發射訊號(其對應於〇*活性 物種)。二種快速擴散物種都是於由標準氧氣和形成氣體過 程所形成的電漿中而產生。相對來看,由ΝΗ3 / 〇2所形成 的電聚則在這些波長觀察不到可體會量的〇 *,因此指出該 電漿沒有這些快速擴散物種。同時,值得注意的是在約3 〇 〇 和400奈米之間的發射訊號(其對應於ο,活性物種)。如上 所述,已發現增加〇2*對0*的比例會減少氧化和石夕漏失。 如此,則分子氧對原子氧的比例(〇2* : 〇*)乃顯著高於標準 電漿過程中的比例。 '實施例16 38 201220006 於此實施例,石英和氧化鋁的重新組合係數乃於圖工7 顯示為溫度的函數。該圖圖形化示範相較於標準石英材料 來看,氡化铭(一種快速擴散原子物種的掃除劑)的重新組人 係數有所增加。一般而言,隨著溫度上升,則大部分材料 會經歷原子氧重新組合的增加。如圖1 7可以看出,當溫度 増加到300。(:或更高,重新組合係數增加超過5倍。為了 逹成更有效的原子重新組合,重新組合表面應該直接或間 接加熱到300°C或更高的溫度。 實施例1 7 斤於此實施例,測量使用在此所述的控制氧擴散方法而 由氨和氧所形成的電漿之中Ο/和〇*的濃度,而為電漿來 源功率密度的函數。圖1 8圖形化示範增加功率密度超過每 立方公吩100瓦則會有效增加〇2*的濃度。不受限於理論並 且如上丨所述,相信增加令性之激發態分子物種(例如相 對於原子物種(例如0*或〇)的比例將會改善整體的灰化過 :’包括較少的矽氧化。如&,則使功率密度最佳化並配 :控制的氧擴散電漿形成以及可選用的掃除性氣體或材 料’砭些對於實質消除電漿中的快速擴散物種以及減少氧 化物成長和矽漏失而言都是有效的。 在此使用的巧彙只是要描述特定的具體態樣而已,並 不是^限制本發明。如在此使用的,單數形式「-」和「該」 _ 也包括複數形式,除非上下文做出明顯相反的指 τ、使用@彙「第_」、「第二」和類似者並非暗示任何特定 序而疋包括以辨別個別的元件。將會進一步了解詞 39 201220006 彙「包括」和/或「包含」和/或「含有」當用於本說 其指出存在了所述的特色、區域、整數、步驟、操作、元 明書時 ^ ,T ^ j ^^ ^ ^ $ 数、步驟、操作、元 素和/或構件,但是並未排除存在或添加了一或更多個其 他的特色、區域、整數、步驟、操作、元素、構件和/或 其群組。 除非另外定義,否則在此使用的所有詞彙(包括技術性 和科學性詞彙)具有與本發明之具體態樣所屬技藝甲具一般 技術者所共同理解的相同意義。將會進_步了解例如通常 使用:字典所定義的詞彙應該解讀成具有與相關技藝和本 2不月景下—致的意義’而將不會以理想化或過度正式的 忍味來解讀,除非在此是這樣明確地定義。 2然已經參考了實施例性具體態樣來敘述本發明的具 以:等^過熟於此技藝者將會了解可以做出多樣的改變 的範圍。此I以取代其冗件’而不偏離本發明之具體態樣 料適於2 ㈣出許多的修改以使特殊的狀況或材 的具髋態樣’而不偏離其基本的範圍。因此, 料想到之畀U, 又限於揭不做為執行本發明所 τq之最佳模式的特定且 而是將包& m t β ,、體W樣,本發明的具體態樣反 外,使用第—、笛_ *竹味求項範圍裡的具體態樣。此 使用第—、m ^等3彙並非指出任何次序或重要性, 件。再者,使用疋要區分某—兀件與另一元 指出存在了至不定冠詞並非指出數量的限制,而是 ^ —個所參考的項目。 201220006 【圖式簡單說明】 當配合圖式來閱讀時,可以最能了解本發明上述具體 態樣的詳細描述,該等圖式是範例性具體態樣,其中: 圖1示範的長條圖顯示由氧氣(〇2)和氮氣(n2)所形成的 先前技藝電漿相較於根據本發明形成的電漿所產出之活性 氮對活性氧的相對量’其中活性氮對活性氧的比例實質上 大於可得自先前技藝的氧氣和氮氣電漿。 圖2圖形化示範正規化的氧化矽成長為用於形成電漿 的氣體混合物之氧含量的函數,其中氣體組成包括氧(〇2) 和氮(NO混合物以及氧(〇2)和形成氣體(Η] / Μ?)混合物。 圖3示意地示範範例性電漿設備,其建構成增進活性 氮對活性氧的比例,該比例實質上大於可得自先前技藝的 氧氣和氮氣電漿.。 圖Μ ·示範的長條圖顯示基於一氧化二氮的電漿(N2〇)相 較於由氧(〇2)和形成氣體(N2 / Ηζ)之氣體混合物所形成的 先前技藝電毁以及由形成氣體⑺2/%)所形成的另一先前 技藝電漿的氧化矽成長和光阻灰化速率。 圖5A〜C示範的長條圖顯示基於—氧化二氮的電榮相 較於先前技藝之基於氧(〇2)的電漿之基板損傷,以及示範 ρ-MOS高劑量離子佈植清潔應用後的掃描電子顯微影像。 失,⑻料測試晶圓上的⑦氧化物成長;以及㈣來自石夕 熱氧化物測試晶圓的矽氧化物漏失,化和 像圖像式示範電聚剝除之後再以去離子水沖洗之由上二 201220006 的汾像其中圖5B是關於由〇2和n2 / h2氣體混合物所形 k 成的電漿,而圖5C是關於由一氧化二氣氣體所形成的電渡。 圖6示範的長條圖顯示基於一氧化二氮的電漿、基於 形成氣體的電漿、基於氧和形成氣體的電漿、具有高氫含 量的H2 / N2電毁之石夕基板漏失、捧雜物漏失、光阻灰化速 率為電漿化學物質的函數。 圖7圖形化示範基於一氧化二氮的電毁、氧和形成氣 體的電漿之矽氧化為阻劑移除的函數。此圖示範具有和沒 有虽含活性氮組態的一氧化二氮電漿條件以及最佳化的一 氧化二氮剝除電漿條件。 圖8圖形化不範的長條圖顯示得自圖7具有和沒有富 含活性氮組態的一氧化二氮電聚之活性氧和活性氮的相: 量以及對應之活性氧和活性氮的比例。 圖9圖形化示範基於一氧化二氮的電毁相較於由氧氣 和形成氣體所形纟的電聚之電聚光學發射強度為波長的函 數。 —圖10圖形化示範基於一氧化二氮的電漿在不同功率設 定下之活性氮和活性氧的相對量以及對應之活性氣對活性 氧的比例。也顯示的是這些電漿下之對應的氧化矽成長。 圖11圖形化示範基於-氧化二氮的電t、帶有CF4添 加物之基於-氧化二氮的電漿、由〇2氣體和形成氣體所形 成的電漿、由〇2氣體和N2氣體所形成的電漿之活性氮和活 性氧的相對量以及對應之活性氮對活性氧的比例。 圖12圖形化示範氧化性電漿之矽氧化的量為電子溫度 42 201220006 的函數。 〇2 函 圖13圖形化示範示範產生自9〇%的NH3和〗〇%的 之電4在不同功率設定下之微波功率為光學發射強度的 數。 圖14圖形化示範產生自90%的丽3和1〇%的〇2之電 漿在固定不變的功率設定下之總氣體流動速率和壓力為光 學發射強度的函數。 ‘ 形成氣體的電漿、產生自 氨氣和氧氣的電漿之矽漏 圖15圖形化示範產生自氧和 一氧化一氮氣體的電漿、產生自 失和氧化物成長為時間的函數。 圖16圖形化不範產生自氨和氧氣體混合物的電漿相較 於氧氣和形成氣體(N2裡有5%氫氣)所形成的電聚之光學發 射光譜的相對強度為波長的函數。 圖17圖形化示範石英和氡化紹材料之重新組合係數與 溫度的相依性。 圖1 8圖形化示範激發的分 刀于氧相較於活性原子氧之正 規化濃度而為電漿來源功率密度的函數。 圖19圖形化示範多樣的氧 科1性物種在270oC下所測得 的拋物線成長速率。 圖20是幾種材料的原子 圖2 1圖形化示範把氮併 表面氧化物。 氣重新纟且合速率表。 入來自Ν*對0*高比例電漿的 的元件乃為了簡潔明確而 熟於此技藝者將體會圖式中 示範,而未必是按照比例來繪製 43 201220006 【主要元件符號說明】 無 44FG 0.20 90% NH3 and 〇2 70% NH3 and 〇2 丨.19 0.37 Metal oxidation TiN △ Rs (%) 47 -10 2 Ashing residual rate As-doping B-doping (micron impurity/dispensing Missing loss, clock) Except (%) (%) Excellent 4. Distinct -5.3 -3 -i〇0_ Poor -2 -7 Excellent - ii - Heterogeneous 2. 〇〇 - Different 35 201220006 90% NH3 and ~ 0.2 ~ 0 0.9 Excellent - FG S〇2 and FG 0.52 45 7.80 Good. 2.5 13 NH3 / 〇2 practices provide the lowest leakage [minimum metal (Ti) oxidation, excellent photoresist and residue removal properties Thereby providing effective electrokinetic chemicals for applications after high dose ion implantation. Example 12 In this example, an optical emission spectrometer was used to monitor the diverse active species of plasma produced by a gas mixture of 90% NH3 and 10% 02 at different power settings. The plasma was formed using a RapidStrip 320 plasma asher with a power setting of 4000 watts or 7800 watts, a total gas flow rate of 5 slm, a pressure of 1 Torr, a chuck temperature of 275 ° C, and a chamber wall temperature of 140 °C. Figure 13 graphical representation of OH* (at 309 nm), N2* (at 337 nm), H2* (at 486 nm), H* (at 656 nm), 〇2* (at 777 nm) The emission intensity set at different powers. As shown, 'increasing the power to more than 5 〇 0 〇 watts significantly increases the emission of active hydrogen (H* and Η/). In addition, an increase in activity was observed for active n2*. There is clearly no significant emission intensity associated with atomic oxygen (〇*) in the spectrum. Although some oxygen in the milk mixture apparently reacts with reactive nitrogen to form a living I. The information in the face clearly indicates that when using NR] gas and its mixture to generate electricity, the power setting can be used to adjust the amount of activity. 36 201220006 can be used to set the desired ashing rate. Example 13 In this example, the emission intensity of the various active species produced by the plasma of the NH3/1〇%〇2 gas mixture was monitored by an optical emission spectrometer as a function of total gas flow rate and pressure. The plasma is formed using an IntegraES plasma asherder with a power setting of 7 watts, a total gas flow rate of 3.5 slm or 7 slm, a pressure of 65.65, 1 〇, 1.5 or 2 Torr, and a chuck temperature of 275 °C. . Figure 14 graphical representation of OH* (at 309 nm), N2* (at 337 nm), Η 2* (at 486 nm), Η* (at 656 nm), Ο, (at 777 nm) The emission intensity set by different pressures and total gas flow rates. As shown, the pressure has minimal or no effect on the formation of diverse active species. However, active hydrogen (Hslt and Η,) exhibits a strong dependence on the total gas flow rate. Significantly comparable amounts of active hydrogen (Η* and η2*) relative to higher total gas flow rates are produced at lower total gas flow rates. In contrast, reactive nitrogen (Ν/) and active oxygen (〇*) did not exhibit a sensible response to pressure or flow rate. Example 14 In this example, the effect of controlling the oxygen diffusion process is exemplified. Figure 15 shows an optimized configuration of the plasma generated from Ν2〇 gas and an optimized configuration of the electric beam generated from the ΝΗ3 / 〇2 gas mixture, both of which include optimization at 27〇〇c Microwave power density (> 1 watt / cubic centimeter). The optical emission spectrum shown in Figure 16 shows how the added NH3 sweeping gas completely removes all measurable atomic oxygen. Both of these plasma configurations show a substantial reduction in helium oxidation; because in the case of NH3, the sweeping gas has been effectively removed = some atomic oxygen, while in the case of ΝΖ0, the sweeping gas has enhanced the molecular pair of 37 201220006 atoms The ratio provides effective nitridation of the surface oxide. In addition, the third group, L-Bell, demonstrates the largest oxide growth and the loss of the stone, which represents the standard ο] and the formation of gas plasma stripping, which has not been optimized to reduce the amount of rapidly diffusing species among them. - Nitrous oxide plasma and ammonia/oxygen plasma have substantially reduced the rate of parabolic growth such that the resulting ruthenium oxidation is only about a single layer. EXAMPLE 1 In this example, an optical emission spectrometer was used to analyze the plasma formed by ammonia and oxygen using the controlled oxygen diffusion method described herein, with respect to the formation of 9% oxygen and 10%. Standard plasma process formed by gas (3. /.H2 / 97% N2). The plasma from each gas was produced in RpS32. The optical emission spectrum of the plasma was collected by an optical optical spectrometer from Ocean Optics through a viewing height of the crystal height of the processing chamber. Figure 1 ό Graphical demonstration of wavelength as a function of intensity. Of note are the emission signals between about 300 and 400 nm (which correspond to the 〇Η* active species) and the emission signals between about 750 and 800 nm (which correspond to the 〇* active species). Both rapidly diffusing species are produced in a plasma formed by standard oxygen and gas forming processes. In contrast, the electrowinning formed by ΝΗ3 / 〇2 does not observe the achievable amount of 〇* at these wavelengths, thus indicating that the plasma does not have these rapidly diffusing species. At the same time, it is worth noting that there is a transmission signal between about 3 〇 400 and 400 nm (which corresponds to ο, active species). As noted above, it has been found that increasing the ratio of 〇2* to 0* reduces oxidation and loss. Thus, the ratio of molecular oxygen to atomic oxygen (〇2* : 〇*) is significantly higher than that in the standard plasma process. 'Example 16 38 201220006 In this example, the recombination coefficient of quartz and alumina is shown as a function of temperature in Figure 7. The graphical representation of the graph shows that the regrouping factor of Sui Huaming, a sweeper for rapidly diffusing atomic species, has increased compared to standard quartz materials. In general, as the temperature rises, most of the material undergoes an increase in atomic oxygen recombination. As can be seen in Figure 17, when the temperature 増 is added to 300. (: or higher, the recombination factor is increased by more than 5 times. In order to achieve a more efficient atomic recombination, the recombined surface should be heated directly or indirectly to a temperature of 300 ° C or higher. Example 1 7 kg For example, the concentration of Ο/ and 〇* in the plasma formed by ammonia and oxygen using the controlled oxygen diffusion method described herein is measured as a function of the power density of the plasma source. A power density exceeding 100 watts per cubic metric will effectively increase the concentration of 〇2*. Without being bound by theory and as described above, it is believed to increase the molecular species of the excited state (eg relative to atomic species (eg 0* or The proportion of 〇) will improve the overall ashing: 'including less bismuth oxidation. For example, &, optimize power density and match: controlled oxygen diffusion plasma formation and optional sweep gas or Materials 'some of these are effective in virtually eliminating rapidly diffusing species in plasma and reducing oxide growth and loss. The use of Qiaohui here is only to describe specific specific aspects, not to limit this hair As used herein, the singular forms "-" and "the" _ also include the plural unless the context clearly dictates the τ, and the use of @汇"第_", "第二", and the like is not implied. Any specific order is included to identify individual components. Further understanding of the word 39 201220006 "includes" and / or "includes" and / or "contains" when used in this statement, indicates that there are features, areas , integers, steps, operations, Yuan Mingshu ^ , T ^ j ^^ ^ ^ $ number, steps, operations, elements and/or components, but does not preclude the presence or addition of one or more other features, A region, an integer, a step, an operation, an element, a component, and/or a group thereof. Unless otherwise defined, all terms (including technical and scientific terms) used herein have the same meaning as the embodiment of the present invention. The same meaning that is commonly understood by the general practitioners. It will be understood that, for example, the commonly used words: the vocabulary defined by the dictionary should be interpreted as having the meaning associated with the related art and the second, and will not be ideal. Or an over-formal tolerance to interpret, unless explicitly defined as such. 2 has already referred to the embodiment of the present invention with reference to the specific embodiments: etc. Those skilled in the art will understand that it can be done a variety of variations. This I replaces its redundancy' without deviating from the specific state of the invention. It is suitable for 2 (four) many modifications to make the special condition or material have a hip-like shape without deviating from its The basic scope. Therefore, it is contemplated that U is not limited to the specific mode of performing the τq of the present invention, but is a package & mt β , body W, a specific aspect of the present invention. In contrast, the use of the first, flute _ * bamboo flavor in the scope of the specific aspect. This use of -, m ^, etc. 3 sink does not indicate any order or importance. Furthermore, the use of a distinction between a certain element and another element indicates that there is a limit to the indefinite article that does not indicate the quantity, but rather a reference item. 201220006 [Simplified Description of the Drawings] A detailed description of the above specific aspects of the present invention can be best understood by reading the drawings, which are exemplary embodiments, in which: Figure 1 shows a bar graph display The relative amount of reactive nitrogen produced by oxygen (〇2) and nitrogen (n2) compared to the reactive oxygen produced by the plasma formed according to the present invention, wherein the ratio of reactive nitrogen to active oxygen is substantial It is larger than the oxygen and nitrogen plasma available from the prior art. Figure 2 graphically demonstrates that normalized yttrium oxide grows as a function of the oxygen content of the gas mixture used to form the plasma, wherein the gas composition includes oxygen (〇2) and nitrogen (NO mixture and oxygen (〇2) and forming gas ( Η] / Μ?) Mixture. Figure 3 schematically illustrates an exemplary plasma apparatus constructed to enhance the ratio of reactive nitrogen to active oxygen, which is substantially greater than oxygen and nitrogen plasma available from prior art. Μ · Demonstration bar graph showing the prior art electro-destruction and formation of nitrous oxide-based plasma (N2〇) compared to a gas mixture of oxygen (〇2) and forming gas (N2 / Ηζ) The yttria growth and photoresist ashing rate of another prior art plasma formed by gas (7) 2/%). The bar graphs illustrated in Figures 5A-C show substrate damage based on nitrous oxide based on prior art oxygen-based (〇2)-based plasma, and after demonstration of ρ-MOS high-dose ion implantation cleaning applications. Scanning electron microscopy image. Loss, (8) the growth of the 7 oxide on the test wafer; and (4) the loss of the tantalum oxide from the Shixi thermal oxide test wafer, and the image-like demonstration of the electrical stripping and then rinse with deionized water. From the previous two figures of 201220006, FIG. 5B is about the plasma formed by the gas mixture of 〇2 and n2 / h2, and FIG. 5C is about the electric charge formed by the gas of oxidizing gas. Figure 6 shows a bar graph showing the nitrous oxide-based plasma, the gas-based plasma, the oxygen-based and gas-forming plasma, and the H2/N2 electro-destruction of the high-hydrogen content. The loss of debris and the rate of light ashing are a function of the plasma chemistry. Figure 7 graphically demonstrates the enthalpy oxidation of ruthenium oxide based electrolysis, oxygen, and gas forming plasma as a function of resist removal. This figure demonstrates nitrous oxide plasma conditions with and without active nitrogen configuration and optimized nitrous oxide stripping plasma conditions. Figure 8 is a graphical representation of the bar graph showing the phase of active oxygen and reactive nitrogen from the nitrous oxide electropolymerization without the active nitrogen configuration and the corresponding reactive oxygen and reactive nitrogen. proportion. Figure 9 is a graphical representation of the function of the wavelength of the electro-optic emission of nitrous oxide based on the electro-optic emission intensity of the electropolymer formed by oxygen and forming gas. - Figure 10 graphically demonstrates the relative amounts of reactive nitrogen and reactive oxygen in a nitrous oxide-based plasma at different power settings and the corresponding ratio of active gas to active oxygen. Also shown is the corresponding yttrium oxide growth under these plasmas. Figure 11 is a graphical representation of a nitrous oxide-based electricity t, a nitrous oxide-based plasma with a CF4 additive, a plasma formed by a ruthenium 2 gas and a gas, and a gas of 〇2 and N2. The relative amount of reactive nitrogen and active oxygen of the formed plasma and the corresponding ratio of active nitrogen to active oxygen. Figure 12 graphically illustrates the amount of ruthenium oxidation of an oxidative plasma as a function of electron temperature 42 201220006. Figure 2 is a graphical representation of the amount of microwave power at a different power setting for the power 4 generated from 9〇% of NH3 and 〇%. Figure 14 graphically illustrates the total gas flow rate and pressure as a function of optical emission intensity at a fixed power setting of plasma from 90% Li 3 and 1% 〇2. ‘The formation of a gas-like plasma, a plasma generated from ammonia and oxygen. Figure 15 graphically demonstrates the generation of plasma from oxygen and nitrous oxide gas, resulting in loss of self-loss and oxide growth as a function of time. Figure 16 is a graphical representation of the relative intensity of the optical emission spectrum of the electropolymer formed from the mixture of ammonia and oxygen gas compared to oxygen and forming gas (5% hydrogen in N2) as a function of wavelength. Figure 17 graphically demonstrates the recombination coefficient of quartz and bismuth oxide materials and temperature dependence. Figure 18. Graphical demonstration of the splitting of the knife as a function of plasma source power density over the normalized concentration of oxygen compared to the active atomic oxygen. Figure 19 graphically demonstrates the parabolic growth rate measured at 270oC for a diverse variety of oxygen species. Figure 20 is an atomic representation of several materials. Figure 2 shows a graphical representation of nitrogen and surface oxides. The gas is re-twisted and combined with the rate table. The components from Ν* to 0* high-ratio plasma are for the sake of brevity and clarity. Those skilled in the art will demonstrate in the schematic diagram, but not necessarily in proportion. 43 201220006 [Main component symbol description] None 44
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US12/844,193 US20120024314A1 (en) | 2010-07-27 | 2010-07-27 | Plasma mediated ashing processes |
| US13/117,488 US20110226280A1 (en) | 2008-11-21 | 2011-05-27 | Plasma mediated ashing processes |
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| TW201220006A true TW201220006A (en) | 2012-05-16 |
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