TWI278927B - Fluid assisted cryogenic cleaning - Google Patents

Fluid assisted cryogenic cleaning Download PDF

Info

Publication number
TWI278927B
TWI278927B TW92113360A TW92113360A TWI278927B TW I278927 B TWI278927 B TW I278927B TW 92113360 A TW92113360 A TW 92113360A TW 92113360 A TW92113360 A TW 92113360A TW I278927 B TWI278927 B TW I278927B
Authority
TW
Taiwan
Prior art keywords
cleaning
substrate
fluid
removing contaminants
vapor
Prior art date
Application number
TW92113360A
Other languages
Chinese (zh)
Other versions
TW200426928A (en
Inventor
Souvik Banerjee
Harlan Forrest Chung
Original Assignee
Boc Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Boc Inc filed Critical Boc Inc
Publication of TW200426928A publication Critical patent/TW200426928A/en
Application granted granted Critical
Publication of TWI278927B publication Critical patent/TWI278927B/en

Links

Abstract

The present invention is directed to fluid assisted cryogenic cleaning of a substrate surface requiting precision cleaning such as semiconductors, metals, and dielectric films. The process comprises the steps of applying a fluid selected from the group consisting of high vapor pressure liquids, reactive gases, and vapors of reactive liquids onto the substrate surface followed by or simultaneously with cryogenic cleaning of the substrate surface to remove contaminants.

Description

1278927 玖、發明說明: 【發明所屬之技術領域】 本發明係關於一種使用流體或蒸汽清洗的程序,其係藉由同時或隨後實 施的低溫清洗過程來幫助除去半導體表面或其他涉及到精密清洗表面的異 物和污染物。 【先前技術】 清洗或製備具有或不具有各種薄膜層的石夕晶圓表面,係積體電路製程中 的關鍵技術。在積體電路製造過程中,須在若干重要程序步驟中從晶圓表 面除去顆粒及污染物;在0·18μιη技術中,整個製程400步驟中有8〇步驟, 即20%的製造步驟用於清洗,各種類型的膜、表面形狀、及在前段製程 (front-end-of-line ; FEOL)和後段製程(back-end-of-line ; BE〇L)清洗過程中 需要除去的污染物,加劇了對清洗技術的挑戰性,除去顆粒係為此清洗程 序中的重要部分。 為製造無缺陷之積體電路,國際半導體技術藍圖(Intemati〇nai1278927 玖, INSTRUCTION DESCRIPTION: TECHNICAL FIELD The present invention relates to a process for cleaning with a fluid or steam, which assists in the removal of semiconductor surfaces or other precision cleaning surfaces by a simultaneous or subsequent low temperature cleaning process. Foreign bodies and pollutants. [Prior Art] The cleaning or preparation of the surface of the wafer substrate with or without various film layers is a key technology in the process of the integrated circuit. In the manufacturing process of integrated circuits, particles and contaminants must be removed from the wafer surface in several important process steps; in the 0.18μιη technique, there are 8 steps in the entire process 400 steps, ie 20% of the manufacturing steps are used Cleaning, various types of membranes, surface shapes, and contaminants that need to be removed during the front-end-of-line (FEOL) and back-end-of-line (BE〇L) cleaning processes, The challenge of cleaning technology is exacerbated, and the removal of particles is an important part of this cleaning process. International semiconductor technology blueprint for the manufacture of defect-free integrated circuits (Intemati〇nai

Technology R〇admap for Semiconductors ; ITRS)指出:關鍵顆粒尺寸為 DRAM 1/2間距的一半⑴。因此,在13〇nm的技術令,間距為 130nm,關鍵顆粒尺寸為65nm,所以大於65nm的顆粒必須除去,以保證 其為無缺陷裝置。 對小顆粒而言,由於其附著力與移除之力比率增大,因此難以除去這些 小顆粒。對於次微米顆粒’顆粒對表面之主要附著力為凡得瓦力加鈿 Waals) ’該附著力取決於顆粒的尺寸、顆粒與基板表面之距離及 1278927 常數。在平坦基板上球形顆粒的凡得瓦力可由方程式1計算出: 其中An2係為顆粒、表面及介入媒介組成的系統之Hamaker常數;咚係顆 粒直從,Z〇係顆粒與表面的距離。該複合系統的Hama]<;er常數可由方程式 (2)計算出:Technology R〇admap for Semiconductors; ITRS) pointed out that the key particle size is half of the DRAM 1/2 pitch (1). Therefore, at a 13 〇nm technique, the pitch is 130 nm and the critical particle size is 65 nm, so particles larger than 65 nm must be removed to ensure that it is a defect-free device. For small particles, it is difficult to remove these small particles because the ratio of their adhesion to the force of removal increases. For submicron particles, the primary adhesion of the particles to the surface is van der Waals. The adhesion depends on the size of the particles, the distance between the particles and the substrate surface, and the 1278927 constant. The van der Waals force of a spherical particle on a flat substrate can be calculated by Equation 1: where An2 is the Hamaker constant of the system consisting of particles, surfaces, and intervening media; the lanthanide particles are straight from the Z-series particles and the surface. The Hama]<;er constant of the composite system can be calculated from equation (2):

Ai32==Ai2+A33-Ai3-A23 (2) 兩種不同材料的Hamaker常數之關係,係使用單個Hamaker常數的幾 何平均值AijKA^Ay)"2表示,其中Aii及~係為材料i及』的Hamaker常 數,理論上其可使用Lifshitz或London模型計算。文獻[2、3]提供在積體電 路製造過程中使用的顆粒及表面的Hamaker常數,當介入媒介為流體時, Hamaker常數值小於介入媒介為空氣時的值。因此,當在顆粒與表面之間 有一層流體時,與Hamaker常數成正比的凡得瓦力會變小。 除了難以將小顆粒從表面除去的困難外,還有各類必須除去的有機及金 屬有機污染物。為了達到更快的開關速度及更好的電路性能的要求,因此 需要新的介電材料(其介電常數<3)及金屬,以減少電路中Rc延遲常數。選< 擇銅金屬係增加了積體製程系統的挑戰性。對鋁互連線(interc〇nnect)而言, 其金屬圖案化係藉由鋁的反應性離子蝕刻(1:eactive丨〇n etching ; )及隨後 的介電質沈積而實施;若使用銅,則首先沈積該介電膜,然而後钱刻形成 通道及溝渠’隨後在此敍刻溝槽内沈積鋼,並使用化學機械拋光(chemical mechanical polishing ; CMP)除去過量的鋼及平坦化該表面以形成後續薄膜 層;此一於後段製程(back_end-0f-line ; BE0L)形成銅互連線的方法稱作雙 6 1278927 鑲叙程序(Dual Damascene process) 〇 在介電質姓刻形成通道及溝渠後,大量的含氟聚合物殘留物留在晶圓的 表面及溝槽的内部,如第一圖所示。此等殘留物係於蝕刻製程中產生,部 分來自非等向蝕刻所造成的側壁侵蝕,在後續的薄膜層沈積製程之前必須 除去該蝕刻殘留物,前述之薄膜層沈積製程係包括:銅障蔽Ta/TaN膜、銅 種晶層及最後在鑲嵌過程中用銅金屬電化學填充溝槽。 目前在後段製程中使用於互連線中的溝槽尺寸大約為〇13μιη,為在低 溫清洗時從溝槽内部有效除去側壁殘留物,該低溫顆粒之尺寸必須小於 0·13μπι,如第一圖所示;而且,這些顆粒必須以足夠的速度到達晶圓表面, 以產生除去側壁殘留物所需的動量傳遞(111〇11161^111:11 transfer)。 貫施表面清洗的機制有三種··丨)藉由低溫顆粒動量轉移以克服漿料顆粒 對晶圓表面的附著力;2)藉由清洗氣體之拉力從晶圓表面除去顆粒;及3) 藉由在低溫顆粒與晶圓表面間的介面所形成的流體溶解有機污染物的顆 粒。 在C〇2低⑽α洗中,在晶圓表面的氣流產生一邊界層,[a低溫顆粒必 須穿過該邊界層以到達晶圓表面及待除去的污綠粒子;在通過邊界層期 間,由於在邊界層内的氣態CO2對低溫顆粒產生拉力,使其速度降低,假 定邊界層的厚度為h,雪狀顆粒進人該層時,其速度之垂直分量必須至少等 於h/t,其中t為穿過該邊界層到達晶圓表面所需要的時間。該顆粒穿過該 邊界層的鬆弛時間(relaxation time)由下面的方程式⑴表示·· 0) 9η 7 1278927 其中: a為顆粒半控^Ai32==Ai2+A33-Ai3-A23 (2) The relationship between the Hamaker constants of two different materials is expressed by the geometric mean AijKA^Ay)"2 of a single Hamaker constant, where Aii and ~ are materials i and The Hamaker constant, in theory, can be calculated using the Lifshitz or London model. Literature [2, 3] provides the Hamaker constant for particles and surfaces used in the fabrication of integrated circuits. When the intervening medium is a fluid, the Hamaker constant value is less than the value of the intervening medium when it is air. Therefore, when there is a layer of fluid between the particles and the surface, the van der Waals force proportional to the Hamaker constant becomes smaller. In addition to the difficulty of removing small particles from the surface, there are various organic and metal organic contaminants that must be removed. In order to achieve faster switching speeds and better circuit performance requirements, new dielectric materials (with dielectric constant <3) and metals are needed to reduce the Rc delay constant in the circuit. The choice of < copper metal system increases the challenge of the integrated system. For the aluminum interconnect (interc〇nnect), the metal patterning is performed by reactive ion etching of aluminum and subsequent dielectric deposition; if copper is used, The dielectric film is first deposited, but then the channels and trenches are formed. Then the steel is deposited in the trenches, and chemical mechanical polishing (CMP) is used to remove excess steel and planarize the surface. Forming a subsequent thin film layer; this method of forming a copper interconnect line in the back-end process (back_end-0f-line; BE0L) is called a double 6 1278927 Dual Damascene process 〇 forming channels and trenches in the dielectric surname Thereafter, a large amount of fluoropolymer residue remains on the surface of the wafer and inside the trench, as shown in the first figure. These residues are generated in the etching process, partly from sidewall erosion caused by non-isotropic etching. The etching residue must be removed before the subsequent thin film layer deposition process. The foregoing thin film layer deposition process includes: copper barrier Ta The /TaN film, the copper seed layer, and finally the trenches are electrochemically filled with copper metal during the damascene process. At present, the size of the trench used in the interconnect in the back-end process is about μ13μηη, which is effective for removing sidewall residues from the inside of the trench during low-temperature cleaning. The size of the low-temperature particle must be less than 0·13μπι, as shown in the first figure. Also shown; these particles must reach the wafer surface at a sufficient rate to produce the momentum transfer required to remove sidewall residues (111〇11161^111:11 transfer). There are three mechanisms for the surface cleaning: the low-temperature particle momentum transfer to overcome the adhesion of the slurry particles to the wafer surface; 2) the removal of particles from the wafer surface by the pulling force of the cleaning gas; and 3) The fluid formed by the interface between the low temperature particles and the surface of the wafer dissolves particles of organic contaminants. In the C〇2 low (10) alpha wash, the airflow at the surface of the wafer creates a boundary layer, [a low temperature particles must pass through the boundary layer to reach the surface of the wafer and the green particles to be removed; during passage through the boundary layer, The gaseous CO2 in the boundary layer generates a tensile force on the low temperature particles, which reduces the velocity. Assuming that the thickness of the boundary layer is h, when the snow particles enter the layer, the vertical component of the velocity must be at least equal to h/t, where t is The time it takes to reach the wafer surface through the boundary layer. The relaxation time of the particles passing through the boundary layer is represented by the following equation (1)·· 0) 9η 7 1278927 where: a is the particle half control^

Pp為顆粒密度 η為氣體的黏度Pp is the particle density η is the viscosity of the gas

Cc為在方程式(2)中所給的Cunningham滑動修正係數Cc is the Cunningham slip correction factor given in equation (2)

Cc=l+1.246(X/a)+0.42(^/a)exp[-0.87(aA^)] 其中λ係氣體分子的平均自由路徑。由於取低溫清洗係在大氣壓下實施, 對於尺寸大於0·1 μπι的低溫顆粒,Cunningham滑動修正因子在方程式⑴ 中為1。 因此,為使C〇2雪狀顆粒具有足夠的動量從晶圓表面及溝槽内部除去異 物,穿過邊界層的時間必須小於鬆弛時間,在此情況下,其到達該表面時 的速度大於起始速度的36%。方程式1顯示鬆弛時間隨著顆粒尺寸而縮短。 因此,尺寸更小的顆粒不能以足夠大的速度到達晶圓表面,因而不能有效 地清洗次微米通道及溝渠的内壁。 先前技術方法通常使用C〇2或氬氣低溫喷射以從表面清除異物,例如: 美國專利第5,931,721號之「喷霧表面處理」、美國專利第6,036,581號之「基 板清洗方法及裝置」的、美國專利第5,853,962號之「使用二氧化碳噴射除 去光阻層及再沈積」、美國專利第6,203,406號之「噴霧表面處理」及美國 專利第5,775,127號之「高分散二氧化碳造雪裝置」;在以上所有關於先前 技術的專利案中,都是藉由動量傳遞到污染物的物理力量將異物從平坦表 面清除。由於污染物顆粒與基板之間的附著力很大,因此先前技術方法不 1278927 能有效清除小於〇·3μηι顆粒;而且,此等清洗方法對於具有高深寬比(high aspect ratio)的溝槽效果不好,例如:在後段積體裝置製程令製造的通道及 溝渠,其要除去在製程中(例如:介電質钱刻)所產生的次微米小顆粒及複 雜的聚合物殘留物。 美國專利第6,332,470號之「噴霧基板清洗劑」係揭露單獨使用蒸汽或 使用與高壓液滴相結合的蒸氣來清洗半導體基板;不幸的是,該流體產生 的衝擊不像固態C〇2那樣具有足夠的動量傳遞能力,因而不能有效地除去 小尺寸的顆粒。美國專利第5,9〇8,510號之「藉由超臨界流體除去殘留物」 係揭露使用結合超臨界流體或液態C〇2的低溫噴霧,但由於c〇2&非極性 分子’因此其對極性異物的溶解能力大大降低;另外,由於流體或超臨界 c〇2之形成需要高壓(流體需要大於75psi,而超臨界流體需要大於 l〇80psi),該設備亦非常昂貴。美國專利第6,231,775號提出在灰化㈣㈣ 過权中單獨使用二氧化硫氣體或結合三氧化硫與其他氣體從基板上除去有 機物,然而,該汽相清洗不能除去使用低1^材料(例如:含碳摻質的氧化物) 的典型雙鑲嵌積體化製程在蝕刻期間形成的交聯光阻層。 由於先前技術的缺點,因此仍需要更有效除去污染物之高效率方法,這 些污染物係包括來自於半導體晶圓的表面、金屬膜、需要精密清洗的其他 基板以及高深寬_賴⑽,包含雜、異物、化學殘_及由交聯和 塊狀光阻層、省虫刻後殘留物及次微米大小顆粒組成的均勻或非均勻污染物。 【發明内容】 本發明提供-麵I貞的改良方法,时清洗需錄歸洗的基板表面 1278927 (例如:半導體、金屬及介電膜)。 本發明包含一種從需要精密清洗的基板表面除去污染物的清洗方法,係 可在低洗之别使用或與低溫清洗同時使用,以除去基板表面上的異物 及污染物。丽述之清洗方法係可根據要從基板表面上除去的污染物而使用 選自下列群組的流體:高壓蒸汽流體、反應性氣體或反應性流體之蒸汽。 该流體农好與该表面保持接觸長達2〇分鐘,形成一可從基板表面除去污染 物或降低污染物對該表面附著力的環境,以使其能在後續的低溫清洗過程 中除去。 【實施方式】 流體輔助清洗方法及範例 在本範例中使用的流體為高壓蒸汽流體,其能降低異物與基板表面(如 半導體晶1Η表®或薄縣面)之_凡得瓦力。該高壓蒸汽雜係喷射到基 板表面,最初噴射的流體會降低凡得瓦力,進而使後續的低溫清洗更容易 將異物從基板表面除去;如果低溫清洗前的上游程序係為水相的程序,則 在低溫清洗前該流體也除去大部分的水,如在共同待審的美國專利申請案 10/215,859號中内容。此外,該高壓蒸汽流韙可用於從該表面溶解有機污染 物,根據基板表面含有的有機污染物,可選擇一特定的高壓蒸汽流體;熟 知本技藝之人士應知曉能溶解普通有機污染物的流體類型。 適於在本發明47使用的高壓蒸汽流體係包含,但不限於:乙醇、丙_、 乙醇丙酮混合物、異丙醇、甲醇、甲酸曱酯、碘甲烷、溴乙烷,氰甲烷 (acetomtnle)、氣甲烷、比咯啶(py汀〇Udine)及四氫呋喃(tetrahydr〇fo 10 1278927 而’任何具有高蒸汽壓的流體都可使用。高壓蒸汽流體會很容易從該基板 表面洛發’不需要加熱乾燥或旋轉該基板烘乾;該流體最好具有低凝固點 並且本身即具有極性,流體的低凝固點能保證在低溫清洗時,留在晶圓表 面上的任何殘留流體,不會由於低溫清洗期間晶圓溫度下降而凝固;流體 的極性則會有助於溶解晶圓表面的有機或無機污染物;該高壓蒸氣流體的 洛汽壓在25。(:下最好大於5kPa,凝固點最好低於-50°C,而其偶極矩最好 大於1.5D。 高壓蒸汽流體可用於任何需要精密清洗之基板表面,然而,較佳的表面 係包括:半導體表面、金屬以及介電膜。因此,本文中所使用的術語「半 導體」、「金屬膜」、「介電膜」或「晶圓」,係表示同樣的程序均可應用於其 他基板表面,包含在化合物半導體(C〇mpOUIKj§;emic〇ncjuct〇r)元件製造過程 中的硬碟媒體、光學元件、GaAs基板及膜。本文提供的範例及實施例並非 用於限定本發明。 在本發明的一項具體實施例令,在30。至50°C之溫度下將該高壓蒸汽 流體噴射到半導體晶圓的表面,噴射出的流體可成為一厚膜或一薄層,該 層的厚度較佳至少為5至1〇A,並且最好使用將去離子水喷射到晶圓表面 的濕式清洗台中所用的由鐵氟龍製造的喷霧喷嘴,但亦可使用在本項技術 中使用任何其他噴嘴。前述之晶圓表面最好至少由該流體覆蓋一分鐘,若 月色覆蓋十分鐘更佳;在此覆蓋期間,該流體可只喷射一次,也可喷射多次 以保證晶圓表面保持濕潤;同樣地,當喷射該流體時,可用大約lOOrpm的 速度旋轉晶圓,以保證流體均勻覆蓋在晶圓表面。 1278927 在濕潤期之後,卩絲低溫翁,低溫喷射可使用二氧化碳、氮氣或 本項技術中熟知的其他氣體,並且可使用任何熟知的低溫清洗技術,下面 將說明co2低溫清洗的-項範例。噴塗縫蒸汽流體的最初結果是降低了Cc=l+1.246(X/a)+0.42(^/a)exp[-0.87(aA^)] where the mean free path of the λ-type gas molecules. Since the low temperature cleaning system is carried out under atmospheric pressure, the Cunningham slip correction factor is 1 in the equation (1) for low temperature particles having a size larger than 0·1 μπι. Therefore, in order for the C〇2 snow-like particles to have sufficient momentum to remove foreign matter from the wafer surface and the inside of the trench, the time to pass through the boundary layer must be less than the relaxation time, in which case the speed at which it reaches the surface is greater than 36% of the starting speed. Equation 1 shows that the relaxation time is shortened with the particle size. Therefore, particles of smaller size cannot reach the surface of the wafer at a sufficiently large speed, and thus the submicron channels and the inner walls of the trenches cannot be effectively cleaned. The prior art method generally uses C〇2 or argon low-temperature spraying to remove foreign matter from the surface, for example, "spray surface treatment" of U.S. Patent No. 5,931,721, and "substrate cleaning method and apparatus" of U.S. Patent No. 6,036,581. U.S. Patent No. 5,853,962, "Using Carbon Dioxide Ejection to Remove Photoresist Layers and Re-Deposition", U.S. Patent No. 6,203,406, "Spray Surface Treatment" and U.S. Patent No. 5,775,127, "Highly Dispersed Carbon Dioxide Snow Making Apparatus"; All of the above prior art patents remove foreign matter from a flat surface by the physical force transmitted by momentum to the contaminants. Since the adhesion between the contaminant particles and the substrate is large, the prior art method 1272827 can effectively remove particles smaller than 〇·3μηι; moreover, these cleaning methods do not have a groove effect with a high aspect ratio. For example, in the latter stage of the integrated device process, the channels and trenches are manufactured to remove submicron small particles and complex polymer residues generated during the process (for example, dielectric stamping). U.S. Patent No. 6,332,470, "Spray Substrate Cleaner" discloses the use of steam alone or in combination with high pressure droplets to clean a semiconductor substrate; unfortunately, the fluid does not have as much impact as solid C〇2. The momentum transfer capability does not effectively remove small sized particles. U.S. Patent No. 5,9,8,510, "Removing Residues by Supercritical Fluids" discloses the use of cryogenic sprays in combination with supercritical fluids or liquid C〇2, but due to c〇2 & non-polar molecules' The dissolving power of the foreign matter is greatly reduced; in addition, since the formation of fluid or supercritical c〇2 requires high pressure (fluid needs to be greater than 75 psi and supercritical fluid needs to be greater than l 〇 80 psi), the device is also very expensive. U.S. Patent No. 6,231,775 teaches the use of sulfur dioxide gas alone or in combination with sulfur trioxide and other gases to remove organic matter from the substrate in the ashing (four) (iv) weighting. However, the vapor phase cleaning cannot remove the use of low material (for example: A typical dual damascene build-up process for carbon-doped oxides) forms a crosslinked photoresist layer during etching. Due to the shortcomings of the prior art, there is still a need for a highly efficient method for removing contaminants more efficiently, including surfaces from semiconductor wafers, metal films, other substrates requiring precision cleaning, and high depth and width (10), including impurities. , foreign matter, chemical residues _ and uniform or non-uniform contaminants consisting of crosslinked and bulk photoresist layers, post-soil residues and submicron sized particles. SUMMARY OF THE INVENTION The present invention provides an improved method of surface I, which is required to be cleaned on the surface of a substrate to be washed 1278927 (for example, a semiconductor, a metal, and a dielectric film). SUMMARY OF THE INVENTION The present invention comprises a cleaning method for removing contaminants from the surface of a substrate requiring precision cleaning, which can be used at low wash or simultaneously with low temperature cleaning to remove foreign matter and contaminants on the surface of the substrate. The cleaning method of the Lisa can use a fluid selected from the group consisting of a high pressure vapor fluid, a reactive gas, or a vapor of a reactive fluid depending on the contaminants to be removed from the surface of the substrate. The fluid is maintained in contact with the surface for up to 2 minutes to form an environment that removes contaminants from the surface of the substrate or reduces the adhesion of contaminants to the surface so that it can be removed during subsequent low temperature cleaning. [Embodiment] Fluid-assisted cleaning method and example The fluid used in this example is a high-pressure vapor fluid, which can reduce the van der Waals force of foreign matter and the surface of the substrate (such as semiconductor wafers or thin county surfaces). The high-pressure steam is sprayed onto the surface of the substrate, and the initially injected fluid reduces the van der Waals force, thereby making it easier for subsequent low-temperature cleaning to remove foreign matter from the substrate surface; if the upstream program before the low-temperature cleaning is a water phase procedure, The fluid also removes most of the water prior to the low temperature cleaning, as in the copending U.S. Patent Application Serial No. 10/215,859. In addition, the high pressure steam can be used to dissolve organic contaminants from the surface, and a specific high pressure vapor fluid can be selected according to the organic contaminants contained on the surface of the substrate; those skilled in the art should be aware of fluids capable of dissolving common organic contaminants. Types of. High pressure steam stream systems suitable for use in the present invention 47 include, but are not limited to, ethanol, propane, ethanol acetone mixtures, isopropanol, methanol, decyl methacrylate, methyl iodide, ethyl bromide, acetomtnle, Methane, pyrrolidine (Udine) and tetrahydrofuran (tetrahydr〇fo 10 1278927 and 'any fluid with high vapor pressure can be used. High pressure steam fluid can easily be released from the surface of the substrate' does not require heat drying Or rotating the substrate to dry; the fluid preferably has a low freezing point and has a polarity in itself, and the low freezing point of the fluid ensures any residual fluid remaining on the surface of the wafer during low temperature cleaning, without wafers during low temperature cleaning The temperature drops and solidifies; the polarity of the fluid helps dissolve the organic or inorganic contaminants on the surface of the wafer; the pressure of the high-pressure vapor fluid is at 25° (: preferably greater than 5 kPa, and the freezing point is preferably less than -50) °C, and its dipole moment is preferably greater than 1.5D. High pressure vapor fluid can be used on any substrate surface that requires precision cleaning. However, preferred surface systems include: semiconductor surface, gold And a dielectric film. Therefore, the terms "semiconductor", "metal film", "dielectric film" or "wafer" as used herein mean that the same procedure can be applied to other substrate surfaces, including compound semiconductors. (C〇mpOUIKj§;emic〇ncjuct〇r) hard disk media, optical components, GaAs substrates, and films in the fabrication of components. The examples and embodiments provided herein are not intended to limit the invention. For example, the high pressure vapor fluid is sprayed onto the surface of the semiconductor wafer at a temperature of 30 to 50 ° C, and the ejected fluid may be a thick film or a thin layer, and the layer preferably has a thickness of at least 5 Up to 1 A, and preferably a Teflon-made spray nozzle for use in a wet cleaning station that sprays deionized water onto the wafer surface, but any other nozzle used in the art may be used. Preferably, the surface of the wafer is covered by the fluid for at least one minute, and if the moonlight is covered for ten minutes, the fluid may be sprayed only once or multiple times to ensure that the surface of the wafer remains wet; Similarly, when the fluid is ejected, the wafer can be rotated at a speed of about 100 rpm to ensure uniform coverage of the fluid on the surface of the wafer. 1278927 After the wet period, the low temperature jet can be carbon dioxide, nitrogen or this technology. Other gases well known in the art, and any well known cryogenic cleaning technique can be used. An example of co2 cryogenic cleaning will be described below. The initial result of the spray seam vapor fluid is reduced.

Hamaker常數,進而降低了凡得瓦力,噴塗該流體降低了污染物對晶圓表 面的附著力’與單獨應用低溫清洗程序相比,污祕更容倾晶圓表面除 去。 除前述之清洗程序外,該高壓蒸氣流體亦可與低溫清洗同時應用。例 如’在此h況下’將用於喷射該高壓蒸氣流體的第二嗔嘴與用於c〇2低溫 清洗的第-噴嘴-起安裝,儒出的高壓蒸氣越最好形成—薄層,並在 流體喷射到該基板的同時繼續實施C〇2低溫清洗。 由於使用該南麼蒸汽流體,藉由低溫清洗除去顆粒污染物的過程得到 明顯改進。第二圖細示鮮低溫清洗及流翻祕溫清洗中顆粒清除效 率與顆粒尺寸之間_係,對尺寸小於㈣叫之縣的清除而言,相較於 與標準C02fe溫清洗程序,細本流翻助呢低溫清洗程序能得到顯著 改善;當顆粒尺寸在〇·98μπι至2·50μηι之間時,使用本流體輔助低溫清洗 過程與標準C〇2低溫清洗過程之間無顯著差別。 蒸汽辅助清洗及範例 反應性氣體或流體的反應性蒸汽可用來幫助清除污染物。反應性氣體或 瘵汽通常用於清除基板表面上的有機光阻層及溝槽内部的含氟聚合物之蝕 刻殘留物,係可根據與基板表面的污染物之反應性來選擇;在與污染物反 應後,該氣體/蒸汽最好產生氣體形式的副產物。(為參考之方便,以下在本 12 1278927 知明之㈣書t所提及反應性氣體都可包括流體的反應性蒸汽,所提及反 應性蒸汽都可包括反應性氣體。) 在半導體晶圓清洗過程中,要清除的污染物不僅包括顆粒污染物,也包 括在微電子元件製造的前段製雕ontof4ine)及後段製程中各步驟產生 的有機、無機及金屬有顧餘物之賴,藉由純㈣物理機制魏清除此 等膜,故s要料除的物理機讎敎化學方絲滿足清㈣要求。在本 發明中’ ru相清洗係化學清洗方法,而低溫清洗的卿主要係物理清洗;The Hamaker constant, which in turn reduces the van der Waals force, sprays the fluid to reduce the adhesion of contaminants to the wafer surface. The smudge is more visibly removed than the cryogenic cleaning process alone. In addition to the aforementioned cleaning procedures, the high pressure vapor fluid can also be used simultaneously with low temperature cleaning. For example, 'in this case, the second nozzle for spraying the high-pressure vapor fluid is installed with the first nozzle for c低温2 low-temperature cleaning, and the higher the high-pressure vapor of Confucian is formed, the thinner layer is formed. The C〇2 low temperature cleaning is continued while the fluid is sprayed onto the substrate. The process of removing particulate contaminants by low temperature cleaning is significantly improved by the use of the south vapor fluid. The second figure shows the difference between the particle removal efficiency and the particle size in the fresh low temperature cleaning and the flow-through temperature cleaning. For the cleaning of the county with a size smaller than (4), compared with the standard C02fe temperature cleaning program, the fine flow The low-temperature cleaning procedure can be significantly improved; when the particle size is between 〇·98μπι and 2·50μηι, there is no significant difference between the use of the fluid-assisted low-temperature cleaning process and the standard C〇2 low-temperature cleaning process. Steam-assisted cleaning and examples Reactive steam from reactive gases or fluids can be used to help remove contaminants. Reactive gas or helium vapor is usually used to remove the organic photoresist layer on the surface of the substrate and the etch residue of the fluoropolymer inside the trench, which can be selected according to the reactivity with the surface of the substrate; Preferably, the gas/steam produces by-products in the form of a gas. (For convenience of reference, the reactive gases mentioned in the following t. 12 1278927 (4) book t may include reactive vapors of the fluid, and the reactive vapors mentioned may all include reactive gases.) Cleaning in semiconductor wafers In the process, the pollutants to be removed include not only particulate pollutants, but also the front-end engraving ontof4ine in the manufacture of microelectronic components and the organic, inorganic and metallic residues produced in the subsequent stages of the process. (4) The physical mechanism Wei removes these membranes, so the physical machine 雠敎 chemical square wire to be removed is required to meet the requirements of Qing (4). In the present invention, the 'ru phase cleaning is a chemical cleaning method, and the low temperature cleaning is mainly a physical cleaning;

該兩種方法先後或依序進行能夠完全清除均勻或非均勻污染物。 可應用於本發明程序之反應性蒸汽的範例可為一高壓蒸汽流體的蒸 汽,係包含丙酮、乙醇丙酮混合物、異丙醇、甲醇、甲酸甲§旨、蛾甲院及 漠乙院’其也可包括-氣體,例如:臭氧、水蒸汽、氮氣、氣氣、氧化氮 三氟化氮、氦氣、氬氣、氖氣、三氧化硫、氧氣、氟氣或碳氟化合物氣患 或氣體之組合;該氣體或蒸汽應能與賴内部的有機光阻層及含氟聚合物The two methods are performed sequentially or sequentially to completely remove uniform or non-uniform contaminants. An example of a reactive vapor that can be applied to the process of the present invention can be a vapor of a high pressure vapor stream comprising acetone, a mixture of ethanol and acetone, isopropanol, methanol, formic acid, a moth, and a moth. May include - gas, such as: ozone, water vapor, nitrogen, gas, nitrogen trifluoride, helium, argon, helium, sulfur trioxide, oxygen, fluorine or fluorocarbon gas or gas Combination; the gas or vapor should be compatible with the internal organic photoresist layer and fluoropolymer

之触刻殘㈣發生反應;而且,該反應之副產物最好域態,因此其可藉 由氮氣流從清洗f除去。較㈣氣體及流體蒸汽包括異丙醇、乙醇丙嗣混 合物、曱醇、臭氧'水蒸汽、三氟化氮、三氧化硫、氧氣、氣氣及碳氣化 合物氣體。 .. 在後侧清洗過程中,低溫顆粒無法進入具高深寬比的通道及溝渠内 部’因此需要顏或蒸汽以便有效地擴舰人_溝槽。職體或蒸汽隨 後與聚合物之殘留物發生化學反應將其轉化成氣態副產物,該氣體副產物 可藉由流經該基板表面之氮氣流除去;或者,可將其引入—低壓的分離室, 13 1278927 該清洗室中氣體/蒸汽相反應係在高達200°C的溫度下進行。在此清洗過程 之後,晶圓可轉移到一大氣壓下的第二清洗室,在此進行低溫清洗。 在此過程期間,該蒸汽可在晶圓表面冷凝。藉由選擇適當的蒸汽,該冷 凝過程也能降低Hammaker常數,進而降低顆粒與表面的附著力,因而該 冷凝過程也有助於藉由低溫清洗除去顆粒。 該氣體或蒸汽可進一步藉由使用自由基起始劑(例如··產生反應性化學 物種的遠紫外光(ultra violet light)、X-射線(X-ray)、準分子雷射(Excimer laser)、電暈放電(coronadischarge)或電漿(plasma))以產生化學物使其增強與 欲清除的污染物的反應性,其與雪狀或低溫喷霧之物理清洗相結合可清除 非反應性污染物。在濕式清洗及雙頻電漿清洗中,也可看到相同的清洗機 制’雙頻電漿清洗係使用下游MW電漿產生化學物以便與污染物發生反 應,以及使用RF電漿產生離子轟擊。 在本發明結合C〇2低溫清洗的一項具體實施例中,該流體蒸汽係通過與 C〇2低溫噴嘴安裝在同一支臂上的一噴嘴噴射。該噴嘴可能是一個直徑為 1/4至1/2英忖的不銹鋼小孔,或為一特殊設計的噴嘴,其沿著該軸有一電 暈放電線用於在蒸汽中引發放電,並且該喷嘴最好與基板表面形成大約10。 至90。的角度;該蒸汽也可透過位於基板表面上方的—噴淋頭噴出,以保證 均勻覆蓋基板的表面;在釋放蒸汽期間,該基板最好保持在與蒸汽相同的 溫度,如果需要冷凝蒸汽’該基板溫度可保持在蒸汽溫度以下,以引起蒸 汽冷凝並在基板表©形成-液態_ H如果蒸汽的反應性不足以與 給定的污綠類型發生反應,可借助-自由基起始劑增加蒸汽反應性;蒸 14 1278927 汽伽彳基板表_a贿好達到二十分鐘,過程爾續或間歇 触;最好只翻單—_的蒸汽,但如果需要,可同時雜紐順序使 用蒸汽混合物來清除污染物。 根據树_反應性驗或航之噴射可與低溫清洗侧-清洗室進 Ί1或也可在刀開的/月洗室進行,而且,低溫清洗可與使用反應性氣體或 飢同時卩絲,或緊接於紐進行;根據顧的反應性氣體或蒸汽,例如 水蒸a,农好在低溫清洗開始前清潔該蒸汽清洗室。 由於使用反應性氣體或蒸汽,污染物的清除,特別是基板表面蚀刻後溝 槽的>?染物之清除得卿著改善。該清洗絲制有益於雜均句污染 物,如在itii及溝渠側壁上侧後殘留物膜或侧後的光阻層殘留物。 實施例標準<:〇2低溫清洗 不管疋在流體清洗過程後進行還是與其同時進行,都要實施標準低溫清 洗。美國專利第5,853,962號揭露一標準的(χ>2低溫清洗過程,係引入作為 參考。第二圖係一典型的C〇2低溫清洗系統實施例:清洗容器12提供一極 其潔淨、封閉或密封的清洗區域。在該清洗區域内,晶圓丨藉由真空固定 在台板2上,該台板與晶圓保持在最高達1〇〇〇c的控制溫度下;首先讓溫 度為室溫、壓力為850psi的C02流體通過一燒結同軸過濾器4,過濾出非 常小的顆粒,以使二氧化碳盡可能純淨及減少液流中的污染物;接著,讓 C〇2流體通過一小孔徑喷嘴擴張,喷嘴直徑最好為〇.〇5英吋至〇上英吋, 該流體之迅速擴張引起溫度下降,導致形成固態C02雪狀顆粒,其夾帶在 以大約每分鐘1至3立方英尺速度流動的c〇2氣流中,讓該固態及氣態C02 15 1278927 流以大約30。至60。(最好大約為45。)的角度流向晶圓表面,並且該噴嘴最好 置於噴嘴觀測線至晶圓表面大約0.375英吋至0.5英吋的位置;在清洗期 間,台板2在轨道9上沿y方向做前後運動,而清洗噴嘴之支臂在轨道10 上沿X方向做直線運動,其結果在晶圓表面產生了的柵格狀清洗圖案,台 板2與噴嘴支臂的步進大小及掃描速度可按需要預先設定;清洗室_的濕 度應保持盡可能低,例如,<-40°C露點(dewpoint),其係可藉由流動的氮氣 或清潔乾燥的空氣可保持,低濕度可防止清洗期間大氣中的水在晶圓表面 冷凝及凝固’這些冷凝及凝固的水會藉由在污染物顆粒與晶圓表面形成結 晶橋(crystalline bridges)而增加污染顆粒與晶圓之間的附著力。 而且,在整個清洗過程中,中和清洗室中的靜電電荷係非常重要,係可 藉由雙極電暈離子棒(bipolar corona ionization bar)5可達此目的;該系統在 c〇2喷嘴後面還裝有一釙喷嘴(Polonium nozzle),其用於增強安裝在一接地 台板上的晶圓之電荷中和;靜電荷的產生係由於C〇道时嘴及晶圓表面 導致摩擦生電而產生,並藉由清洗室内之低濕度而得到加強。 對於顆粒污染物,其清除機制主要為藉由CO2低溫顆粒之動量傳遞來克 服污染物顆粒與晶圓表面之附著力,一旦顆粒「鬆動」,氣態⑺2的拉力就 會將從其晶S1表面清除。有機薄膜污染物的清洗機制係由於低溫c〇)在晶 圓表面之衝擊壓力,而在有機污染物與絲面之_成_吸流體薄膜, 該C〇2流體隨後能溶解該有機污染物並將其從晶圓表面帶走。 本專利申請案之實施態樣及實施例均係用於說明本發明,而不宜用以限 制本發明’熟知本技術之人士,在不脫離本發明之精神和翻內,當可應 16 1278927 用於其他實施態樣。此等實施態樣係包含在本發明範圍内。 參考文獻 [1] . International Technology Roadmap for Semiconductors 2001 Edition [2] . Handbook of Semiconductor Wafer Cleaning Technology Science,The contact residue (4) reacts; moreover, the by-product of the reaction is preferably in a domain state, so that it can be removed from the cleaning f by a nitrogen stream. (4) Gas and fluid vapors include isopropanol, ethanol propionate mixture, decyl alcohol, ozone 'steam, nitrogen trifluoride, sulfur trioxide, oxygen, gas and carbon gas compounds. .. During the rear side cleaning process, the low temperature particles cannot enter the channels with high aspect ratio and the inside of the ditch. Therefore, it is necessary to have a face or steam to effectively expand the ship_trench. The body or vapor then chemically reacts with the residue of the polymer to convert it into a gaseous by-product which can be removed by a stream of nitrogen flowing through the surface of the substrate; alternatively, it can be introduced into a low pressure separation chamber , 13 1278927 The gas/vapor phase reaction in the cleaning chamber is carried out at temperatures up to 200 °C. After this cleaning process, the wafer can be transferred to a second cleaning chamber at atmospheric pressure where it is cryogenically cleaned. This vapor can condense on the surface of the wafer during this process. By selecting the appropriate vapor, the condensing process also reduces the Hammaker constant, which in turn reduces the adhesion of the particles to the surface, and thus the condensation process also aids in the removal of particles by cryogenic cleaning. The gas or vapor can be further utilized by using a free radical initiator (eg, producing ultra violet light, X-ray, excimer laser for reactive chemical species). , coronadischarge or plasma to produce chemicals that enhance reactivity with contaminants to be removed, combined with physical cleaning of snow or low temperature spray to remove non-reactive contamination Things. In wet cleaning and dual-frequency plasma cleaning, the same cleaning mechanism can be seen. 'Double-frequency plasma cleaning uses downstream MW plasma to generate chemicals to react with contaminants, and RF plasma to generate ion bombardment. . In one embodiment of the present invention in combination with C〇2 cryogenic cleaning, the fluid vapor is injected through a nozzle mounted on the same arm as the C〇2 cryogenic nozzle. The nozzle may be a 1/4 to 1/2 inch diameter stainless steel orifice or a specially designed nozzle having a corona discharge line along the shaft for inducing discharge in the vapor, and the nozzle It is preferable to form about 10 with the surface of the substrate. To 90. The vapor is also ejected through a sprinkler located above the surface of the substrate to ensure uniform coverage of the surface of the substrate; during vapor release, the substrate is preferably maintained at the same temperature as the vapor, if condensation is required. The substrate temperature can be kept below the steam temperature to cause vapor condensation and form on the substrate © liquid_H If the reactivity of the vapor is insufficient to react with a given type of soil, the steam can be added by means of a radical initiator Reactive; steam 14 1278927 Swarovski substrate table _a bribe for twenty minutes, the process is continuous or intermittent touch; it is best to only turn the steam - _, but if necessary, can use the steam mixture at the same time Remove contaminants. According to the tree _reaction test or jetting, it can be carried out with the low-temperature cleaning side-cleaning chamber or the knife-opening/month washing chamber, and the low-temperature cleaning can be performed simultaneously with the use of reactive gas or hunger, or Immediately after the New Zealand; according to Gu's reactive gas or steam, such as water steam a, the farm cleans the steam cleaning chamber before the start of low temperature cleaning. Due to the use of reactive gases or vapors, the removal of contaminants, especially the removal of the grooves after etching of the substrate surface, is improved. The cleaning wire is beneficial for the contamination of the homogenous sentence, such as the residue film on the side of the ipi and the side wall of the trench or the photoresist layer residue behind the side. Example Standard <: 〇 2 Low Temperature Cleaning Standard low temperature cleaning is performed regardless of whether the hydrazine is carried out after the fluid cleaning process or at the same time. U.S. Patent No. 5,853,962 discloses a standard (χ>2 low temperature cleaning process, which is incorporated by reference. The second drawing is a typical C〇2 low temperature cleaning system embodiment: the cleaning container 12 provides an extremely clean, sealed or sealed a cleaning area in which the wafer cassette is fixed to the platen 2 by vacuum, the platen and the wafer being maintained at a control temperature of up to 1 〇〇〇c; first, the temperature is room temperature, pressure The 850 psi CO 2 fluid is passed through a sintered coaxial filter 4 to filter out very small particles to make the carbon dioxide as pure as possible and reduce contaminants in the liquid stream; then, the C〇2 fluid is expanded through a small orifice nozzle, the nozzle Preferably, the diameter is from 〇.〇5 inches to upper 吋, the rapid expansion of the fluid causes a temperature drop, resulting in the formation of solid CO 2 snow particles that are entrained at a flow rate of about 1 to 3 cubic feet per minute. 2 In the gas stream, let the solid and gaseous CO 2 15 1278927 flow flow to the wafer surface at an angle of about 30 to 60 (preferably about 45.), and the nozzle is preferably placed on the nozzle observation line to the wafer surface. a position of about 0.375 inches to 0.5 inches; during cleaning, the platen 2 moves back and forth along the y direction on the track 9, and the arms of the cleaning nozzle move linearly along the X direction on the track 10, and the result is in the crystal. The circular surface creates a grid-like cleaning pattern, and the step size and scanning speed of the platen 2 and the nozzle arm can be preset as needed; the humidity of the cleaning chamber should be kept as low as possible, for example, <-40 ° C Dewpoint, which can be maintained by flowing nitrogen or clean dry air. Low humidity prevents condensation and solidification of water in the atmosphere during cleaning. These condensation and solidified water will be contaminated. The particles form crystalline bridges on the surface of the wafer to increase the adhesion between the contaminated particles and the wafer. Moreover, it is important to neutralize the electrostatic charge in the cleaning chamber throughout the cleaning process. A bipolar corona ionization bar 5 is available for this purpose; the system is also equipped with a nozzle (Polonium nozzle) behind the c〇2 nozzle for enhancing the wafer mounted on a ground plate Electricity Neutralization; the generation of static charge is caused by frictional electricity generation at the mouth and wafer surface during C-channel, and is enhanced by the low humidity in the cleaning chamber. For particulate pollutants, the removal mechanism is mainly through CO2. The momentum transfer of the low temperature particles overcomes the adhesion of the contaminant particles to the surface of the wafer. Once the particles are "loose", the tensile force of the gaseous (7) 2 will be removed from the surface of the crystal S1. The cleaning mechanism of the organic thin film contaminants is due to the low temperature c〇 The impact pressure on the surface of the wafer, while in the organic contaminant and the surface of the filament, the C〇2 fluid can then dissolve the organic contaminant and carry it away from the wafer surface. The embodiments of the present application and the embodiments are intended to illustrate the present invention, and are not intended to limit the present invention to those skilled in the art, without departing from the spirit and scope of the present invention, when it is possible to use 16 1278927 In other implementations. Such embodiments are included within the scope of the invention. References [1] . International Technology Roadmap for Semiconductors 2001 Edition [2] . Handbook of Semiconductor Wafer Cleaning Technology Science,

Technology and Applications, Edited by Wemer Kern, Noyes Publications, 1993 [3] . Particle control for Semiconductor Manufacturing, Edited by R. P.Technology and Applications, Edited by Wemer Kern, Noyes Publications, 1993 [3] . Particle control for Semiconductor Manufacturing, Edited by R. P.

Donovan, Marcel Dekker Inc., 1990Donovan, Marcel Dekker Inc., 1990

17 1278927 【圖式簡單說明】 第一圖係顯示雙鑲嵌結構中溝渠蝕刻後的殘留物之清洗。左圖係帶有敍 刻殘留物的溝渠蝕刻後結構之SEM影像。右圖係電漿及濕式清洗步驟序列 完成後的溝渠姓刻後結構之SEM影像。 第二圖係顯示標準低溫清洗及本流體輔助低溫清洗中顆粒清除效率與 顆粒尺寸之間關係比較圖表。 第三圖係顯示-傳統C〇2低溫清洗系統之示意圖。 【元件符號對照表】 1 --晶圓 2 --台才反 3 —噴嘴 4- 燒結同軸過濾器 5- 雙極電暈離子棒 6 —超高效率濾網(Ulpamter) 9 -執道 10-執道 12-清洗容器17 1278927 [Simple description of the diagram] The first figure shows the cleaning of the residue after etching in the double damascene structure. The left image is an SEM image of the trench etched structure with the remnant residue. The image on the right shows the SEM image of the structure of the ditch after the completion of the sequence of plasma and wet cleaning steps. The second graph shows a comparison chart of the relationship between particle removal efficiency and particle size in standard low temperature cleaning and this fluid assisted low temperature cleaning. The third figure shows a schematic of a conventional C〇2 cryogenic cleaning system. [Component Symbol Comparison Table] 1 - Wafer 2 - Taiwan Counter 3 - Nozzle 4 - Sintered Coaxial Filter 5 - Bipolar Corona Ion Rod 6 - Ultra High Efficiency Filter (Ulpamter) 9 - Essence 10- Essence 12 - Cleaning Container

Claims (1)

1278927 拾、申請專利範圍: 1· 一種從需要精密清洗之基板表面清除污染物的方法,係包含下列步驟: (a) 將至少一種流體喷塗至基板表面,其中該流體係選自下列群組: 高壓蒸汽流體、反應性氣體及反應性流體之蒸汽;及 (b) 低溫清洗基板表面,以移除污染物。 2.如申請專利範圍第1項所述之從需要精密清洗之基板表面清除污染物 的方法,其中步驟⑻及(b)係為同時實施。 3·如申請專利範圍第1項所述之從需要精密清洗之基板表面清除污染物 的方法,其中步驟(a)及(b)係為依序實施。 4·如申請專利範圍第1項所述之從需要精密清洗之基板表面清除污染物 的方法,其中前述之高壓蒸汽流體係可選自下列群組:乙醇、丙g同、乙 醇丙酮混合物、異丙醇、甲醇、甲酸甲酯、碘甲烷、溴乙烷、氰曱院、 氯乙院、比°各°定及四氧吹喃及其混合物。 5.如申請專利範圍第1項所述之從需要精密清洗之基板表面清除污染物 的方法,其中前述之反應性流體之蒸汽係為選自下列群組之流體:乙 醇、丙酮、乙酵丙酮混合物、異丙醇、甲醇、甲酸甲酯、埃甲烧、溴乙 烷及其混合物。 6·如申請專利範圍第1項所述之從需要精密清洗之基板表面清除污染物 的方法,其中前述之反應性氣體係可為一種或多種選自下列群組之氣 體:臭氧、水蒸汽、氫氣、氮氣、氧化氮、三氟化氮、氦、氬、氖、三 氧化硫、氧、氟或碳氟化合物氣體及其混合物。 19 1278927 7·如申請專利範圍第1項所述之從需要精密清洗之基板表面清除污染物 的方法’其中前述之反應性氣體或蒸汽係可選自下列群組:異兩 -子乙 醇丙酮混合物、甲醇、臭氧、水蒸汽、三氟化氮、三氧化硫、氧、氣、 氟碳化合物氣體及其混合物。 8·如申請專利範圍第1項所述之從需要精密清洗之基板表面清除污染物 的方法,其中前述之流體在開始低溫清洗前,與基板表面保持接觸在 10分鐘内。 9·如申請專利範圍第8項所述之從需要精密清洗之基板表面清除污染物 的方法,其_前述之流體在開始低溫清洗前與基板表面保持接觸時間少 於2分鐘。 10·如申請專利範圍第丨項所述之從需要精密清洗之基板表面清除污染物 的方法,其中前述之污染物尺寸小於〇·76μπι。 11·如申請專利範圍第1項所述之從需要精密清洗之基板表面清除污染物 的方法,其中前述之污染物尺寸小於0·13μπι ° 12. 如申請專利範圍第1項所述之從需要精密清洗之基板表面清除污染物 的方法,其中前述之高壓蒸汽流體在25。(:下之蒸汽壓約大於5kPa,凝 固點約在-50°C以下。 13. 如申請專利範圍第1項所述之從需要精密清洗之基板表面清除污染物 的方法,其中前述之高壓蒸汽流體具有一約大於丨·513之偶極矩。 20 127^927 14. 15. 16. 17. 18. 19. 如申請專利範圍第1項所述之從需要精密清洗之基板表面清除污染物 的方法’其中前述之高壓蒸氣流體在開始低溫清洗前,於基材表面保持 至j 5A之一流體層並維持在1〇分鐘之内,較佳係少於2分鐘。 如申請專利範圍第4項所述之從需要精密清洗之基板表面清除污染物 的方法’其中前述之方法係可進一步包含高壓蒸汽流體從基板表面除去 大部分水之步驟。 如申請專利範圍第1項所述之從需要精密清洗之基板表面清除污染物 的方法’其中前述之基板表面係為半導體、金屬或介電膜。 如申請專利範圍第1項所述之從需要精密清洗之基板表面清除污染物 的方法,其中前述之流體係為反應性氣體或蒸汽,其係與基板表面之污 ^物反應形成一揮發性氣態副產物;前述之方法並進一步包含於開始低 溫清洗前,保持反應性氣體或蒸氣與表面接觸長達2〇分鐘及除去該氣 態副產物之步驟。 如申明專利範圍第17項所述之從需要精密清洗之基板表面清除污染物 的方法,其中前述之反應性氣體或蒸汽係在低壓下及/或高達200°C的 溫度下,被引入含有基板的一清洗室。 如申請專利範圍第18項所述之從需要精密清洗之基板表面清除污染物 的方法,其中前述之方法係包含以氮氣或潔淨乾燥空氣清潔該清洗室以 除去副產物之方法。 如申請專職圍第17項所述之從需要精歸洗之基減崎除污染物 的方法,其中前述之方法包含將該反應性氣體或蒸汽在存在一自由基起 21 20. 1278927 始劑條件下噴塗至該表面,以從反應性氣體或蒸汽與污染物產生反應性 化學副產物。 21.如申請專利範圍第20項所述之從需要精密清洗之基板表面清除污染物 的方法,其甲前述之自由基起始劑係為遠紫外光、X-射線、雷射、電暈 放電或電漿。1278927 Pickup, Patent Application Range: 1. A method for removing contaminants from the surface of a substrate that requires precision cleaning, comprising the steps of: (a) spraying at least one fluid onto the surface of the substrate, wherein the flow system is selected from the group consisting of : high pressure steam fluid, reactive gas and reactive fluid vapor; and (b) low temperature cleaning of the substrate surface to remove contaminants. 2. A method for removing contaminants from a surface of a substrate requiring precision cleaning as described in claim 1 wherein steps (8) and (b) are carried out simultaneously. 3. The method for removing contaminants from the surface of a substrate requiring precision cleaning as described in claim 1 wherein steps (a) and (b) are carried out sequentially. 4. The method for removing contaminants from the surface of a substrate requiring precision cleaning as described in claim 1, wherein the high pressure steam flow system may be selected from the group consisting of ethanol, propylene glycol, ethanol acetone mixture, and different Propanol, methanol, methyl formate, methyl iodide, ethyl bromide, cyanide, chloroform, ratio of tetrahydrofuran and mixtures thereof. 5. The method of removing contaminants from a surface of a substrate requiring precision cleaning as described in claim 1, wherein the vapor of the reactive fluid is a fluid selected from the group consisting of ethanol, acetone, and acetone. Mixture, isopropanol, methanol, methyl formate, ezrin, ethyl bromide and mixtures thereof. 6. The method of removing contaminants from a surface of a substrate requiring precision cleaning as described in claim 1, wherein the reactive gas system may be one or more gases selected from the group consisting of ozone, water vapor, Hydrogen, nitrogen, nitrogen oxides, nitrogen trifluoride, helium, argon, helium, sulfur trioxide, oxygen, fluorine or fluorocarbon gases and mixtures thereof. 19 1278927 7. The method for removing contaminants from the surface of a substrate requiring precision cleaning as described in claim 1, wherein the aforementioned reactive gas or vapor system may be selected from the group consisting of: a mixture of iso---co-ethanol acetone , methanol, ozone, water vapor, nitrogen trifluoride, sulfur trioxide, oxygen, gas, fluorocarbon gases and mixtures thereof. 8. A method of removing contaminants from a surface of a substrate requiring precision cleaning as described in claim 1, wherein the fluid is maintained in contact with the surface of the substrate for 10 minutes before the low temperature cleaning is initiated. 9. The method of removing contaminants from the surface of a substrate requiring precision cleaning as described in claim 8 of the patent application, wherein the fluid is kept in contact with the surface of the substrate for less than 2 minutes before starting the low temperature cleaning. 10. The method of removing contaminants from a surface of a substrate requiring precision cleaning as described in the scope of claim 2, wherein the contaminant size is less than 〇·76 μπι. 11. The method for removing contaminants from the surface of a substrate requiring precision cleaning as described in claim 1, wherein the contaminant size is less than 0·13 μπι ° 12. as described in claim 1 A method of removing contaminants from a surface of a precision cleaned substrate, wherein the aforementioned high pressure vapor fluid is at 25. (The vapor pressure is about 5 kPa and the freezing point is about -50 ° C. 13. The method for removing contaminants from the surface of the substrate requiring precision cleaning as described in claim 1 wherein the high pressure steam fluid Having a dipole moment greater than 丨·513. 20 127^927 14. 15. 16. 17. 18. 19. Method for removing contaminants from the surface of a substrate requiring precision cleaning as described in claim 1 The above-mentioned high-pressure vapor fluid is maintained on the surface of the substrate to a fluid layer of j 5A and maintained within 1 minute, preferably less than 2 minutes, before starting the low-temperature cleaning. The method of removing contaminants from the surface of a substrate requiring precision cleaning, wherein the foregoing method may further comprise the step of removing a large portion of water from the surface of the substrate by the high pressure vapor fluid. The precision cleaning is required as described in claim 1 The method for removing contaminants from the surface of the substrate, wherein the surface of the substrate is a semiconductor, a metal or a dielectric film. The substrate required for precision cleaning as described in claim 1 The method for removing contaminants, wherein the foregoing flow system is a reactive gas or steam, which reacts with the dirt on the surface of the substrate to form a volatile gaseous by-product; the foregoing method is further included before the low temperature cleaning is started, a step of removing a reactive gas or vapor from the surface for up to 2 minutes and removing the gaseous by-product. The method of removing contaminants from the surface of a substrate requiring precision cleaning as described in claim 17 of the patent scope, wherein the aforementioned reactivity The gas or steam is introduced into a cleaning chamber containing the substrate at a low pressure and/or at a temperature of up to 200° C. The method for removing contaminants from the surface of the substrate requiring precision cleaning as described in claim 18, Wherein the foregoing method comprises a method of cleaning the cleaning chamber to remove by-products by using nitrogen or clean dry air. For example, the method for reducing contaminant-removing contaminants from the sub-cleaning base according to Item 17 of the full-time application, wherein the foregoing The method comprises spraying the reactive gas or steam onto the surface in the presence of a radical from 21 20. 1278927 to the surface to Reactive chemical by-products of gaseous or vapors and contaminants. 21. A method for removing contaminants from the surface of a substrate requiring precision cleaning as described in claim 20, wherein the radical initiator system described above For far ultraviolet light, X-ray, laser, corona discharge or plasma. 22twenty two
TW92113360A 2002-04-05 2003-05-16 Fluid assisted cryogenic cleaning TWI278927B (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US36985202P 2002-04-05 2002-04-05
US36985302P 2002-04-05 2002-04-05

Publications (2)

Publication Number Publication Date
TW200426928A TW200426928A (en) 2004-12-01
TWI278927B true TWI278927B (en) 2007-04-11

Family

ID=38645255

Family Applications (1)

Application Number Title Priority Date Filing Date
TW92113360A TWI278927B (en) 2002-04-05 2003-05-16 Fluid assisted cryogenic cleaning

Country Status (1)

Country Link
TW (1) TWI278927B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20230178363A1 (en) * 2021-12-03 2023-06-08 Ncc Nano, Llc Method and apparatus for removing particles from the surface of a semiconductor wafer

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9925639B2 (en) * 2014-07-18 2018-03-27 Applied Materials, Inc. Cleaning of chamber components with solid carbon dioxide particles
KR20170134925A (en) * 2016-05-27 2017-12-07 세메스 주식회사 Substrate treating apparatus and substrate treating method
TWI674629B (en) * 2017-01-12 2019-10-11 國立中山大學 Method for processing electronic components by supercritical fluid
US11101141B2 (en) 2017-01-12 2021-08-24 National Sun Yat-Sen University Kz Method for reducing defects of electronic components by a supercritical fluid
CN114078692B (en) * 2022-01-07 2024-02-20 浙江大学杭州国际科创中心 Wafer cleaning method and wafer cleaning equipment

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20230178363A1 (en) * 2021-12-03 2023-06-08 Ncc Nano, Llc Method and apparatus for removing particles from the surface of a semiconductor wafer
US11769660B2 (en) * 2021-12-03 2023-09-26 Pulseforge, Inc. Method and apparatus for removing particles from the surface of a semiconductor wafer

Also Published As

Publication number Publication date
TW200426928A (en) 2004-12-01

Similar Documents

Publication Publication Date Title
US6852173B2 (en) Liquid-assisted cryogenic cleaning
US6949145B2 (en) Vapor-assisted cryogenic cleaning
US11011392B2 (en) Stiction-free drying process with contaminant removal for high-aspect ratio semiconductor device structures
JP4393268B2 (en) Drying method of fine structure
US8197603B2 (en) Method and apparatus for treating a substrate with dense fluid and plasma
US6763840B2 (en) Method and apparatus for cleaning substrates using liquid carbon dioxide
JP2005252234A (en) Method and equipment for processing article
KR20160041023A (en) Systems and methods for treating substrates with cryogenic fluid mixtures
US20060081273A1 (en) Dense fluid compositions and processes using same for article treatment and residue removal
US20080004194A1 (en) Processing of semiconductor components with dense processing fluids
TWI278927B (en) Fluid assisted cryogenic cleaning
US20080000505A1 (en) Processing of semiconductor components with dense processing fluids
WO2003086668A1 (en) Fluid assisted cryogenic cleaning
TWI386281B (en) CMP polishing method, CMP polishing apparatus, and manufacturing method of semiconductor element
US20100167552A1 (en) Methods for particle removal during integrated circuit device fabrication
US20050217706A1 (en) Fluid assisted cryogenic cleaning
JP2011187703A (en) Substrate cleaning method, and semiconductor manufacturing device
JP4844912B2 (en) Photoresist removal method and removal apparatus
Banerjee Cryoaerosol cleaning of particles from surfaces
TW478059B (en) Dynamic semiconductor-memory device and method to initialize a dynamic semiconductor-memory device
Banerjee et al. Cryogenic aerosols and supercritical fluid cleaning
Reidy et al. Cryogenic Aerosols and Supercritical Fluid Cleaning and Surface Conditioning
JP2004088095A (en) Washing method
Reinhardt et al. AN ADVANCED BEOL CLEANING METHOD
Mertens et al. Challenges and novel approaches for photo resist removal and post-etch residue removal for 22 nm interconnects

Legal Events

Date Code Title Description
MK4A Expiration of patent term of an invention patent