200920882 九、發明說明: » 【發明所屬之技術領域】 本發明提供一種流體區域控制裝置及其操作方法,尤指一種 可應用於電鍍(plating)製程清洗(cleaning)製裎或研磨製程的流體 區域控制裝置及其操作方法。 【先前技術】 目前,用以形成金屬材料層的技術包括有物理氣相沈積、化學 氣相沈積、無電電鍍法、及電鍍法等。其中,由於電化學電鑛(electr〇 chemical plating,ECP)技術具有成本便宜以及產出率快的優點,已 被廣泛應用在工業界中。在電鍍過程中,鍍膜品質會受到鑛液的 成分、溫度、電流密度、以及被鑛物表面的潔淨度等等因素的影 響。 請參閱第1圖至第3圖,第1圖至第3圖為習知電化學電鍍製 程之製程示意圖。如第1圖所示,首先提供一晶圓1〇與一電鍍裝 置20。電鍍裝置20包含有一電鍍槽12、一電鍍流體22、陽極系 統(anode system) 14、一陰極電極(cathodeelectrode) 16 與一固 定組件(fixing component)18。電鍍槽12用以盛裝電鑛流體22,而 電鍍流體22的主要成分為含有金屬離子的溶液。陽極系統14包 含有一陽極室(anode chamber)30、一陽極電極24、一過滤薄膜(filter membrane)26、一擴散薄膜(diffuser membrane)28 與一電鑛流體提 供管線32。 200920882 將晶圓ίο放置於陰極電極16與固定組件以之 被陰極電極16與固定έ 使日日圓10 ,、U义組件18夾住。接著,如 傾斜晶圓π·,使晶圓丨。細流體22的液面之:所不文略為 比較不易夾雜氣泡。其後,如第3円所_ :曰® 1〇的表面上 欲電鍍之曰mn i 電連接至 …日回10上,為了增進鑛膜厚度之均勻性 陰極電極16去β合·^ u 又在電鑛日才 、Ά W 專’以確保晶圓10能持續接觸到新鮮的電鍍 /讀田广4鑛裝置20被施予一外在電壓或是電流時,極^ ”先14電鍵流體22、陰極電極所組成的電路便會被導通,°在、 陰極電極16周圍進行還原反應,而將金屬材簡在晶圓10上。 f知電化學魏製程不僅會將金·贿在晶圓1G的晶面 j還曰同時將金屬材料錢在晶圓10的晶邊上。然而,附著於晶 骑制^的金屬材料實際上並非產品所需。後續在進行其他的半導 -衣私時’晶邊表面的金屬材料經常會因為受到熱應力(出_1 或其他因素而發生繼(peeling)的現象,進而造成金屬200920882 IX. INSTRUCTIONS: » Technical Field of the Invention The present invention provides a fluid region control device and an operation method thereof, and more particularly to a fluid region applicable to a plating process cleaning or polishing process. Control device and method of operation thereof. [Prior Art] Currently, techniques for forming a metal material layer include physical vapor deposition, chemical vapor deposition, electroless plating, and electroplating. Among them, the electrorheological electroplating (ECP) technology has been widely used in the industry because of its advantages of low cost and high yield. During the electroplating process, the quality of the coating is affected by factors such as the composition of the mineral fluid, temperature, current density, and the cleanliness of the mineral surface. Please refer to Fig. 1 to Fig. 3, and Fig. 1 to Fig. 3 are schematic views showing the process of the conventional electrochemical plating process. As shown in Fig. 1, a wafer 1 and a plating apparatus 20 are first provided. The electroplating apparatus 20 includes a plating bath 12, a plating fluid 22, an anode system 14, a cathode electrode 16 and a fixing component 18. The plating bath 12 is for holding the electric mineral fluid 22, and the main component of the plating fluid 22 is a solution containing metal ions. The anode system 14 includes an anode chamber 30, an anode electrode 24, a filter membrane 26, a diffuser membrane 28, and an electromineral supply line 32. 200920882 The wafer ίο is placed on the cathode electrode 16 and the fixed assembly to be clamped by the cathode electrode 16 and the fixed έ so that the Japanese yen 10 and the U-shaped component 18 are clamped. Next, the wafer is tilted by tilting the wafer π·. The liquid level of the fine fluid 22: it is not easy to contain bubbles. Thereafter, 曰 mn i to be electroplated on the surface of the _ 曰 曰 〇 〇 电 电 电 电 电 电 电 电 电 电 , , , , , , , , , , , , , , , , , , , , , , , , , , In the electric mine day, Ά W special 'to ensure that the wafer 10 can continue to contact the fresh electroplating / the reading of the 4 mine device 20 is given an external voltage or current, the first 14 key fluid 22 The circuit formed by the cathode electrode is turned on, and the reduction reaction is performed around the cathode electrode 16 to simplify the metal material on the wafer 10. f know that the electrochemical process will not only be gold and bribe on the wafer 1G. The crystal face j also has the metal material money on the crystal edge of the wafer 10. However, the metal material attached to the crystal chip is not actually required by the product. Subsequent to other semi-conductive-clothing' The metal material on the surface of the crystal edge often causes corrosion due to thermal stress (out of _1 or other factors), which in turn causes metal
::二:衣而產生碎駐驗。尤其是當整批之半*體晶片放置於 化子氣相〉儿積(chemical vap〇r dep〇siti〇n, CVD)裝置中進行CVD 一:位置相對上方的晶圓10若發生這種剝落的現象,將會嚴 重其他位置相對下方的晶圓10表面,造成缺陷。此外,在因 A 王所的而移動晶圓1〇時,此金屬材料之碎屑亦往往會掉落至 〇之表面上而污染產品’進而影響產品的功能(performance)。 200920882 為了避免上逑缺陷,習 的清除製程、清洗製程與二:電錢製程刺進行•卜 屬材料。這不但會增加製程時間鮮二去除附=於晶邊表面的金 雜度,進而可能導致產品的良率下本:會增加製程的複 於習知的陽極系、统14、B曰 。、.十對電鍵流體22而言,由 此習知電化學電錢製程需 ’德的液面而浸入,因 22。當電化學電鍍製程進行二時^槽=與大量的電鑛流體 舊的電鑛流體22並注入新的‘;2製程就需暫停’以倒出 οι αλ * ^ 又机體22。如此一來’電鍵户辦 22的更換又纽㈣長的日摘,鱗產铸低。魏机體 先被二二:為了進行f知電化學電鍍製程,單-晶圓10必須::Two: The clothes are broken and the test is broken. In particular, when a half batch of the bulk wafer is placed in a chemical vapor phase CVD apparatus, CVD is performed: if the wafer 10 is positioned at a position higher than the wafer 10, the peeling occurs. The phenomenon will be severe in other locations relative to the surface of the wafer 10 below, causing defects. In addition, when the wafer is moved by the A king, the scrap of the metal material tends to fall onto the surface of the crucible and contaminate the product, thereby affecting the performance of the product. 200920882 In order to avoid the defects of the upper jaw, the cleaning process and the cleaning process of the Xi and the second: the electric money process thorns • Bud material. This will not only increase the process time, but also remove the gold impurity on the surface of the crystal edge, which may lead to the yield of the product: it will increase the process of the conventional anode system, system 14, B曰. For the ten pairs of the key fluid 22, the conventional electrochemical money-making process requires the liquid surface of the German to be immersed because of 22. When the electrochemical plating process is carried out at 2 o'clock = with a large amount of electro-minerals, the old electro-mineral fluid 22 is injected into the new '2 process, it needs to be paused' to pour out οι αλ * ^ and the body 22. In this way, the replacement of the button households 22 and the new (four) long day picks, the scales are cast low. Wei body is first two or two: in order to carry out the electrochemical plating process, the single-wafer 10 must
==安置於陰極電極16與固定組件叫接著傾J 體22中’其後開啟電錄裝置2 再 移出電鍍槽12,並進行丁电戮汉愿冉 可知,受到電鍵裝置21===燥製程等等後續製程。由此 批次處理大量的晶㈣ΓΓ ’f知電辦電織程無法 知的電鑛裝置20難以對晶圓/ ζ翻產品的產量。再者,習 ㈣Α〆 了日日_ 1ϋ進仃即時(in-situ)量測,因此不但 以準確且快速地料電化學電程,量測之步驟 也&必頊耗費額外的時間。 【發明内容】 匕本I明之主要目的之—在於提供一種流體區域控制裝置 200920882 及其操作方法,以解決習知技術所產生的問題。 根據本發明之一實施例,本發明提供一種用於電鍍之流體區 域控制裝置’包含有至少一基底承載基座(substrate holder)、至少 一陰極電極、至少一陽極系統、至少一控制流體提供管線(confming fluid supplying tube)、至少一控制流體回補管線(conflning仙记 rCC(w—g tube)、至少一製程流體提供管線(ptOcess _ supplying tube)與至少一製程流體回補管線(process recovering tube)。基 底承載基座用以承載至少一半導體基底。陰極電極設置於基底承 載基座之表面上,用以電連接至半導體基底。陽極系統位於基底 承载基座上方,本質上對應於半導體基底而設置,並且與基底承 載基座相距一反應高度(rcacti〇n height)。陽極系統與陰極電極之間 定義有至少一待處理區域以及至少一非處理區域。控制流體提供 f線與控制流體回補管線皆對應於非處理區域而設置,分別用於 提供與回收至少一控制流體。製程流體提供管線與製程流體回補 官線皆對應於待處理區域而設置,分別用於提供與回收至少一電 錢流體。 ^根據本發明之另一較佳實施例,本發明另提供—種流體區域 控制裝置之操作方法。首先提供至少—流體區域控制裝置,流體 •it制裝置包含有至少—基底承載基^、至少—控制流體提供 —待處理歧卜鱗麵域。讀,提供至少—^^基 200920882 底,4·導體基底狀縣底承録座上。接著,開啟控制流體提 供管線與控做_補管線’使得至少—控概體_從控制流 體提供她Μ,並赠人控概體_管線,其中㈣流體流 過基底承«座之非處㈣域。然供至少―製赠體 流體接觸絲承縣紅彳核理區域,且製程㈣不溶於 為讓本發明之上述目的、特徵、和優點能更明顯賴,下文 特舉較佳實施方式,並配合所關式,物細說明如下。然而如 下之較佳實施方式與圖式僅供彖考盥 加以限制者。 1、糊,細來對本發明 【實施方式】 請參閱第4圖與第5圖,第變示的是本發明第-較佳實 ====流體_控制裝置22〇的剖面示意圖,而第㈣ -曰^θ所不之陽極系統114的剖面示意圖,其中相同的 = 的符號來表示。需注意的是圖式僅以說明為 原尺寸作圖。如第4圖所示,本實施例提供一種 用於電鍍之流體區域控制F I版仏種 丨與-陽極M 114 包含有一流體區域控制系統 底Τ:減广ηη 流體區域控辩、統12Q包含有一基 底承載基座130、-陰極電 第二管線m、至少弟—官_、至少^ 第二官線142與至少一第四管線144。 10 200920882 陽極系統114位於基底承載基座13〇上方,本質上對應 處理的半導體基底UG而設置。陽辩、統m與基絲載基座⑽ 相距-反應高度Η,-方面可作為電奴應的電壓麵,另—方 面可以協助流體區域控㈣置22G去控制製程流體所佔據的高 度。於流體區域控制裝置220巾,陽極系統114可為一旋轉=統 (_ry SyStem)或一固定系_xed sys_。換句話說,相對於_ 承載基座130而言,陽極系,統114可進行旋轉動作,也可以維土持 在固定位置上m基絲絲座13Q也可以選擇要進行 旋轉動作或是維持在固定位置上。如第5圖所示,陽極系統^ 可包含有一陽極電極124,並且選擇性地包含有至少一第五管線 13 6、一感測器(sensor) 122或偵測器(detect〇r,未示於圖中)。另外, 陽極系統114也可以包含有陽極室118、過濾薄膜〗%或擴散 128等元件。 ”'、 基底承載基座丨30用以承載至少一半導體基底1]〇。其中,本 發明之基底承載基座130可具有一帶狀(belt type)結構或一環狀 (nng type)結構,如第6圖與第7圖所示。第6圖之基底承載基座 130具有至少一輸送帶I3〇a,使眾多待處理的半導體基底丨⑺可 利用基底承載基座13〇依序傳入流體區域控制裝置22〇中。第7 圖之基底承載基座丨3〇則具有一環狀結構隱,以容置待處理的 半導體基底110。需注意的是,基底承載基座13〇亦可同時具有環 狀結構與輸送帶(未示於圖中),利用環狀結構容置半導體基底 no,並利用輸送帶傳送環狀結構與半導體基底u〇。 200920882 陰極電極116設置於基底承載基座〗30之表面上,可電連接 至半導體基底110。其中,陰極電極U6可同時作為一固定組件, 用以將半導體基底110固定於基底承載基座130的一預定位置。 有鑑於此,陰極電極116可具有一靜電吸盤(electrostaticchuck, e_chuck)、一真空吸盤(vacuum Chuck)、一環型(ring type)結構或— 鉗型(clamp type)結構,如第8圖與第9圖所示。第8圖之陰極電 極丨16可從半導體基底n〇的上方往下固定半導體基底"ο,而第 9圖之陰極電極U6可固定於基底承載基座13〇之表面上,從半導 體基底110周圍朝向半導體基底11〇的方向傾倒而箝制住半導體 基底110。基底承載基座130上,陽極系統】14與陰極電極 之間疋義有一待處理區域(未示於圖中)以及一非處理區域(未示於 圖中)° 4分位於彳核理區域_半導體基底11Q預定要接受製程 的處理,而部分位於非處理區域内的半導體基底11〇預定不接受 製程的處理。 比第:管線132、第二管線134、第三管線142與第四管線144 二位方、陽㈣統114周圍’用以提供或者回收製程所需的化學物 質、添加物(additive)、去離子水、氣體、控制流體等等物質。相 對於=處理的半導體基底m而言,第三管線142與第四管線⑷ 位n官線132與第二管線134的外側。第—管線⑶、第二管 線134、第三管線142與第四管線144皆可以具有任意的管線戴面 ^狀,例如圓形、半_、弧形、橢_、長方形或是多邊形等 寺形狀。舉例來說’第10圖所示之第一管線132與第二管線134 200920882 具有圓弧形的截面 皆為圓管,而第三管線H2與第四管線144 第-發Γ述之流體區域控制以切叫含有複數個 :1 132、複數個第二管線134、複數個第三管線14 歿數個第四管線144,並且讓M f 5 渺、主ρηΛ/ j成所需的形狀,例如圓 L , π' ^ ^·1 η,圖所不之第1線132、第二管線丨34、第三管線142 ^弟四管線144皆為圓管,且第三管線142與第四管線144分別 擒列成-圓形圖案。又或者第12圖所示,當流體區域控制裝置挪 具有側壁152作為輔助時,第三管線142與第四管線144可以具 有線形的载面,並且互相平行排列。需特別注意的是,圖中所^ 之各管線皆朝著半導體基底則財心方向傾斜,如第4圖所示。 然而本發明不需侷限於此,本發明流體區域控制裝置220之各管 線亦可垂直於半導體基底Π〇的晶面而設置、背向半導體基底ιι〇 的中心方向傾斜’甚至是平行於半導體基底110的晶面而設置。 除了可以於陽極系統114内部裝設管線之外,流體區域控制 驳置220的各部分實際上都可以裝設管線。如第I〕圖所示,流體 C1域ί工制糸統120可以另包含有至少一第六管線146與至少一第 七管線148 ’設置於基底承载基座130内,並對應於半導體基底 110的外圍。第六管線丨46與第七管線148同樣可以具有上述各式 戴面,也可以由多個第六管線146或第七管線148排列成任意形 狀。流體區域控制裝置220可以利用管線的閥門或是各流體壓力 13 200920882 來調控第一管線132、第二管線134、第三管線142、第四管線丨44、 第五管線136、第六管線146或第七管線148的開啟與關閉,且流 體區域控制裝置220也可以調控各管線内之流動流體種類、流動 方向、流速,甚至是各管線的設置角度與位置。 另一方面,除了可以於陽極系統114内部裝設感測器122或 偵測器之外’流體區域控制裝置220的各部分實際上皆可以裝設 各種感測器122或偵測器,例如裝設一溫度感測器、一流速感測 器’或是一可量測晶圓表面狀況(例如:厚度、平坦度…等)之感測 器。舉例來說’第一管線132内可以包含有一感測器122,第二管 線134内也可以包含有一感測器122。這些感測器可以於製程進行 的過程中對製程狀況或是製程流體進行即時量測,因此可以準確 且快速地掌控製裎狀況,進而能即時自動回饋並調整各項製程參 數或是製程流體的品質。 為了更清楚地說明本發明之特徵所在,以下藉由本發明應用 於一電化學電鍍製程之實例來說明流體區域控制裝置220之一操 作方法。請參閱第14圖,其繪示的是第13圖所示用於電鍍之流 體區域控制裝置220之一操作方法示意圖,其中相同的元件或部 位沿用相同的符號來表示。如第14圖所示,首先提供第13圖所 示之流體區域控制裝置220。之後,提供至少一半導體基底U0, 利用陰極電極116或是其他固定組件將半導體基底110固定於基 底承載基座130上。半導體基底110可以為一晶圓、一石夕基底或 14 200920882 者是矽覆絕緣(silicon-on-insulator,SOI)基底。於本實施例中,半 導體基底110即為一晶圓。由於本實施例晶圓之晶面需接受電鑛 而形成金屬材料層’且晶圓之晶邊不需要形成金屬材料層,因此 流體區域控制裝置220之待處理區域1 〇2係對應至晶圓之晶面, 而非處理區域104係對應至晶圓之晶邊,其中晶圓之晶面可向上 放置而面對陽極系統114。 接著,開啟第三管線142與第四管線144,使得一控制流體 154持續從第四管線144流出,並藉由第三管線142回收,而第六 官線146與第七官線M8則關閉。其中,控制流體154係用以維 持待處理區域内之化學物質或清洗流體等製程流體之形狀與位 置’使得化學物質不會接觸到半導體基底11()之不需接受製程處 理的部分,例如控制流體154可以為減等惰性氣體(inertgas)。 第四管線I44與第三管線142皆設置於半導體基底的周圍, 分別用於提供與回收控制流體j M。此時,控制流體i %從第四管 線144流向第二官線142的路徑可形成一流動動線p。透過第三管 線142與第四管線144的配置,流體區域控制裝置22g會使域控 制流體154流過流體區域控制裝置22〇之非處理區域。 二後開啟Ϊ $線132與第二管線丨’使得-電鑛、流體156 持續從第-管線m流出,並藉由第二管線134时。此處之電 鍍細156即為電化學電鍍製程的製程流體。第-管、線132與第 - s線134》獅於提供細收電賴體156’設置於半導體基底 200920882 110與控制流體〗54的流動動線P之間。為了促使電鍍流體156 與控制流體154持續流動,流體區域控制裝置22〇内部或外部可 以裝設一幫浦作為動力來源,但無須侷限於此。於本發明之其他 實施例中,製程流體甚至可以不用持續地提供與持續地回收,而 是先提供一定量的製程流體來進行反應後,再視情況斟酌是否要 回收製程流體或是提供新的製程流體。 由於電鍍流體156與控制流體154彼此不易互溶,因此控制 流體154可以控制電鍍流體156的流動範圍,使得電鍍流體丨56 不會接觸到半導體基底110上不需接受製程處理的部分,而只會 接觸到半導體基底上需要接受製程處理的部分。如此一來, 流體區域控制裝置220可以透過控制流體154的流速、電錢流體 I56的流速、各管_位置與各管_㈣料时來控制電鑛流 體156所佔據的空間。 陽極包極124與陰極電極Π6可於電鑛流體]56流出之前或 肌出之後電連接至不同電位,如此—來,由陽極電極丨24、電鑛流 體15卜陰極電極116所組成的電路便會被導通,在陰極電極116 周圍進行_反應,而將金屬材概在半導體基底nQ之晶面上。 ,在前述的狀況下,控制流體154與電鑛流體156彼此不約 订反應’控制流體154係利用其本身與電錢流體156不互溶的丰 性來偈限麵流體〗56的位置與雜。於本發日种,製裎流體岁 200920882 控制流體皆可以為液體狀態、氣 恕、崧汽狀態(v—rs罐 二二:)。例如,電鍍流體⑼係以液體狀態流動, =體154則是以氣體狀態流動。又或者,電鑛流體156與 體154可以賴液體祕。甚至,控制流體⑼可以包 界流體’例如二氧化碳。在本發明之其他實施例中, 體154另可以包含有其他各式物質來輔助製㈣操作或是 輔助控制麵流體丨56的流動。舉例來說,控制流體154可包含 有一料化氣體(腦ized gas)、—熱氣體或是—冷氣體,以改變製 程溫度或是魏流體156的溫度與特性。如此—來,控制流體154 一方面可以維持製程流體之形狀與位置,另一方面可以強化製 私’甚至還可以移除半導體基底丨⑴上殘留的殘留物。 …本發明的主要特徵之-在於利用一控制流體取代習知的容 器’以控制製程所需流體的位置及製程流體佔據的空間。為了達 到上述目的’㈣流體㈣程流體彼此互不相溶,難制流體可 透過本身流動的流動動線p來侷限製程流體佔據的空間、利用控 制机體與製&流體彼此之間的磁力作用來控制製程流體佔據的空 間,或是利用控制流體與製程流體彼此之間的電力作用來控制製 程流體佔據的空間。有鑑於此,控制流體154可包含有具有磁性 的物貝、具有電性的物質、磁流變液(magnet〇_rhe〇丨〇gjca丨制江 MRF)、電流變液(electro-rheo丨〇giCaj f|uid,erf),甚至是固體微粒。 藉此’流體區域控制裝置220可以利用磁力(magnetic f〇rce)或是電 力(electric force)來控制控制流體154或電鍍流體156的特性,進 200920882 而控制電鍍流體156的流動。 前述操作方法僅為本發明其中一種實施方式,控制流體154 與電錄流體156的實際流動方式<依據實際製程需求而調整。換 句話說,針對不同的製程需求,本發明之控制流體154或電鍍流 體】56可以由任何管線流出,在真於適當的管線進行回收。請參 閱第15圖至第〗8圖,其繪示的是第13圖所示用於電鍍之流體區 域控制裝置220的其他操作方法之示意圖,其中相同的元件或部 位仍沿用相同的符號來表示。第15圖至第18圖所示之操作方法 同樣可應用於一電化學電鍍製程,這些操作方法與前述^作方法 的主要不同之處在於,控制流體154與電鍍流體丨56的流動管線 有所更動。 如第15圖所示’控制流體154同樣是從第四管線⑷流出’ 亚错由第三管線142回收。但是電錄流體156 Μ第二管線134 藉由第一管線132回收。如第丨6圖所示,㈣^體⑼ W動動'線ρ同樣不、變,但電鐘流體156較佳 流出’並藉由第一管線132與第二管線m-起回收。如&第17圖 所不,電錢流體156 φ第一管線132流出,並藉由第二管線口* 回收。而控制流體154由第六管線146流出,並#由第三吕管線ι42 回收。又或者* 18圖所示,電鑛流體156自第〜管線132流出, 線134 Μ。而控制流體154由第 七管咖-起流出,並藉由㈣線142與第四管^144回收 18 200920882 _注思的是,Θ述之流體區域控制裝置22G、流體流動動線 ρ與製程流體流動動線皆可應用於—溶劑清洗(solventcleaning)製 程中’且本發明之流體區域控制裝置22〇可應用於任何需要控制 操作流體的製程中,例如-乾燥製程…濕式_製程、一無電 電錢(etoroless —ing)製程、一化學機械研磨(c— polishing, CMP)製程,或是-電化學機械研磨製程等等。當流體區 域控制裝置220應用於清洗製程時,陽極電極124與陰極電極U6 無須電連接至不同電位’且麵流體156可更換為清洗流體,例 如一去離子水(deionized water, Dlwater)或一超臨界流體。因此, 半i體基底110於流體區域控制裝置220中接受電化學電鑛黎j 程之後,可以關閉施加於陽極電極與陰極電極的電壓,並且更換 製程流體,旋即於同一裝置中接受—清洗製程或是一乾燥製程。 由此可知,當應用於清洗製程時,流體區域控制裝置甚至可 以不需要陽極電極與陰極電極二個組件。請參閱第19圖,其綠示 的疋本發明之第二較佳實施例用於清洗之流體區域控制裝置3 的剖面示意圖,其中相同的元件或部位沿用相同的符號來表示。 如第19圖所示,本實施例提供一種用於清洗之流體區域控制裝置 320。流體區域控制裝置320與流體區域控制裝置22〇主要的不同 之處在於,用於清洗之流體區域控制裝置320可以不需要陰極電 極116與陽極系統114。因此,流體區域控制裝置22〇可利用一固 之組件216來固定半導體基底110,並利用一管線系統(饴^ system)214來協助控制製程的反應高度η’其中固定組件216可為 19 200920882 靜電吸盤、真空吸盤或鉗型結構。管線系統214位於基底承載基 座130上方本貝上對應於半導體基底〗而設置,並且與基底 承載基座13G相距-反應高“。絲承絲座13G上定義有一 待處理區域(未示於财)以及—麵理輯(未示於圖巾)。部分位 於待處理區域内的半導體基底11Q預定要接受製程的處理,而部 分位於非處理區域_半導體基底m預定不接受製程的處理。 另外,於本發明之另-實施例中,流體區域控制系統12〇本 身就可以麟清洗製程、_製程或乾燥製程,而湘製程流體 本身的重力與控制流體來維持製程流體的位置,如㈣圖所示。 當流體區域㈣裝置32〇_魏職程或清賴程時,控 制流體與製程越還可以具有其他的流财式。請參㈣Μ圖至 第24圖,麟賴Μ 19 _示祕清洗之流醜域控制裝置 32〇的其他操作方法之示意圖,其中相同的讀或部位仍沿用相同 的符號來表示,且此處之半導體基底⑽同樣可為_日日日圓。如第 =圖所示,當要清洗半導體基底⑽之日日日㈣,第—管㈣2與 第二管線134,提供製㈣需之清洗流體256,並且由第五管線 】36回收清洗流體256。而控制流體1M由第六管線撕斑第七管 線148 —起流出’並由下往上藉著第三管線Η2與第四管線144 回收。或者也可以如同第22圖所示,控制流體154由第三管線142 與第四管線144 -起流出’並由上往下藉著第六管線146與第七 管線148回收。 20 200920882 當要清洗半導體基底110之晶邊時,流體區域控制裝置32〇 之待處理區域可對應至半導體基底110之晶邊,而非處理區域可 對應至半導體基底U〇之晶面。如第23圖所示,第一管線132與 第二管線134 一起提供製程所需之控制流體154,並且由第五管線 136回收控制流體丨54,以保護位於非處理區域之晶圓的晶面不與 清洗流體256接觸。而清洗流體256由第六管線〗46流出,並藉 著第三管線142回收。再者,如第24圖所示,當要清洗半導體基 底110之晶背時,固定組件216可先將半導體基底11〇略為舉起, 由第六官線146提供清洗流體256,第三管線142回收清洗流體 256。而控制流體154由第一管線132與第二管線134流出,並藉 著第五管線】36回收。 本發明之用於電鍍之流體區域控制裝置22〇或用於清洗之流 區域控制裝置32〇亦可應用於化學機械研磨製程,其中該製程 可分為傳統化學機械研磨製程與電化學研磨製程。請參照第 圖其綠不的是本發明之第三較佳實施例用於研磨之流體區域控 制裝置720的剖面示意圖。如第乃圖所示,流體區域控制裝置 可以包3有一研磨系統(p〇llsWng system)7i4與一流體區域控制系 、、先〗20 ’其中研磨系統7M另包含有一研磨墊(polishing pad) 75卜 —研磨墊固定座(padh〇lder)724,以及研賴料(8ΐ_ΐ58。 當應用於電化學研磨製程時,固定組件216可以作為陽極電 極’而研磨塾固定座724可以作為陰極電極,用以通電加速研磨 200920882 f。此外,當應_統化學機械研磨製程時,流體區域” 衣置720可以關閉施加於陽極電極與陰極電極的電壓,即可 一裝置中進行傳統化學機械研磨製程。… 、 、 換句s舌說,透過部分亓株 的更換、_,以及製程流體的更換,半導體基幻 一流體區域控制裝置別中迅速地進行各種不同的製程,例如I 一化學機械研磨製程之後旋即接受—清洗制^ 、 基底承載基座130上絲有—彳錢觀域(絲於圖中)以及 -非處理區域(未示於圖中)。部分位於待處理區_的半導體基底 110預定要接受化學機械研磨製程的處理,而部分位於非處观域 内的半導體基底11G預定不接受化學機_磨製程的處理。尤盆 注意的是,前述之流體流動動線P與製程流體流動動線皆可岸用 於化學機械研磨製程中,且研磨塾751的高度與位置皆可以根據 製程所需崎賴整。要進行化學峨研㈣辦,研磨塾π 可以向下施齡半導縣底nG表面±,或者絲承絲座13〇 或固定組件216也可以將半導體基底u〇上舉至研磨墊π表面。 研磨系統7M可以另包含有一可量測晶圓平坦度或材料層厚 度之感測器722,以對半導體基底no各部位進行一即時的平坦度 量測,並可以將量測結果即時回饋至製程中。此外,研磨系統71 可以包含有各麵型的研磨裝置,例如mQtarytype)研磨 裝置、一線性(lim^type)研磨裝置、一轨道式(〇rbitaUype)研磨裝 置,或是一固定研磨微粒(fixed abrasive web)系統。舉例來說,當 22 200920882 - 研磨系統714為一固定研磨微粒系統時,研磨墊751本身可以具有 各,種類型之研磨微粒,而流體區域控制裝置72〇所供應的製程流體 可以為一去離子水,具有研磨微粒的研磨墊751配合著去離子水即 可滾動研磨整個半導體基底110或是半導體基底11〇之特定區域, 例如半導體絲110表面之材㈣的凸域構。實際操作上,研磨 塾乃1的尺寸可以比半導體基底UG大、比半導體基底⑽小,或是 和半導體基底110—樣大。 由此也可推知,當用於清洗之流體區域控制裝置320裝設有 至少-研磨墊時’流體區域控制裝置32Q即可進行傳統化學賊 研磨製程。 因為流體區域控制裝置72〇可以利用控制流體來控制研磨聚 料158或祕子水的位置’並且㈣研磨墊751的高度與位置來研 磨整個半導縣底U0或是半導縣底m之狀區域,因此流體 區域控制裝置720具有以下幾侧憂點。首先,流體區域控制裝置720 可以輕易地調整待處理區域與非處理區域的位置,也可以輕易地 調整半導縣底位置,_可崎對料縣底11〇之 特足區域進彳T研磨’料必擔雜於其域的半導體基底11〇或 材料層受到研磨而損粍或破壞。 其次’則專統的_製程、傳統的沉積製程,或是傳統的研 磨製程之後,單-半導體基底UG或是其上某—材料層的表面往往 23 200920882 -會出現均勾度⑽f〇_ty)不佳的問題,例如於傳統的研磨製程之 後半基底110的邊緣會較薄而中心會較厚。由於流體區域控 制裝置720可以輕易地調整待處理區域與非處理區域的位置,也可 以即時量測半導體基底110的平坦度或材料層的厚度,所以能自動 研磨出具有良好均勾度的半導體基底⑽或材料層。 再者,由於流·域控姆置7_控織體來控制所需 接父研磨雜置’因此流體區域控概置72()可以具有任意尺寸的 研磨塾7S卜不像傳統研磨機台之研磨塾尺寸通常必須大於半導體 基底110的尺寸。另外,因為流體區域控制裝置72〇可針對待處理 區域施加研磨㈣158或去離子水,目此可叫免研賴料158接 觸到半導體絲HGJi其他易受污染的區域,也可以節省研磨黎料 158或去離子水的使用量,避免不必要的成本損耗。 另外需注思的疋,本發明用於電鑛之流體區域控制裝置Do、 用於清洗之流體區域控制裝置320與用於研磨之流體區域控制裝 置720都可以對晶圓的特定區域進行製程處理。請參閱第26圖,第 26圖緣示的是本發明流體區域控制裝置之一操作示意圖。如第% 圖所示,流體區域控制I置可以包含有一流體區域控制系統12〇與 一系統914,其中系統914可以是陽極系統1丨4、管線系統214或研 磨系統714。流體區域控制裝置可對半導體基底no進行區域性的 電鍍製程、清洗製程或是研磨製程。這裡的待處理區域不需限定 在晶面與晶邊,可以對應至半導體基底110上的任意位置,例如對 24 200920882 應至晶圓上的某触祕域’ *轉縣底⑽上的其餘部分則可 對應至非處理區域,例如非處理區域可以對應至晶圓上的某個周 邊區域。在其他實施射’待處理區域可以制至晶圓的晶面、 晶背、晶邊,或是任何需要處理的局部區域,而晶圓的其餘部分 則可以對應至非處理區域。 、①上所述,^於本發日⑽彻控雛體來㈣製程流體的位 置’因此不像砂電化學賴製程需魏大的魏_大量的電 鑛流體。此外,本發明的控制流體與製程流體都可以循環再利用。 控制流體或製程流體經過管線回收後,可以直接經另一個管線回 流至流體區域控制裝置㈣續彻。或者,回收之製程流體血控 制流體也可⑽過㈣的處理或非即時的處理 ^== Placed in the cathode electrode 16 and the fixed component is called the second body 22, and then the electric recording device 2 is turned on and then the plating tank 12 is removed, and the electric heating device is used, and the electric key device 21 === dry process Wait for the follow-up process. As a result, a large number of crystals (4) 批次 f f 知 电 电 电 电 电 电 电 电 电 电 电 电 电 电 电 电 电 电 电 电 电 电 电 电 电 电 电 电Furthermore, Xi (4) took advantage of the in-situ measurement of the day, so not only the electrochemical path was accurately and quickly measured, but also the measurement steps took extra time. SUMMARY OF THE INVENTION The main object of the present invention is to provide a fluid region control device 200920882 and a method of operating the same to solve the problems caused by the prior art. According to an embodiment of the present invention, there is provided a fluid region control device for electroplating comprising at least one substrate holder, at least one cathode electrode, at least one anode system, at least one control fluid supply line Confling fluid tube, at least one control fluid replenishing line (conflning rCC (w-g tube), at least one process fluid supply line (ptOcess_m tube) and at least one process fluid replenishing line (process recovering tube) The substrate carrying base is configured to carry at least one semiconductor substrate. The cathode electrode is disposed on the surface of the substrate carrying base for electrically connecting to the semiconductor substrate. The anode system is located above the substrate carrying base, substantially corresponding to the semiconductor substrate. Provided, and spaced apart from the substrate carrying base by a reaction height (rcacti〇n height). At least one area to be treated and at least one non-processing area are defined between the anode system and the cathode electrode. The control fluid provides f-line and control fluid replenishment. The pipelines are all arranged corresponding to the non-processing areas, respectively for providing and recycling at least one The process fluid supply line and the process fluid supply line are disposed corresponding to the area to be treated, respectively for providing and recovering at least one wire money fluid. According to another preferred embodiment of the present invention, the present invention Provided is a method for operating a fluid zone control device. First, at least a fluid zone control device is provided, the fluid•it device comprising at least a substrate bearing substrate, at least a control fluid supply, a scaly area to be treated. Providing at least -^^ base 200920882 bottom, 4· conductor base-like county bottom deck. Next, opening the control fluid supply pipeline and controlling the pipeline to make at least the control body _ from the control fluid to provide her, and The gift control system _ pipeline, wherein (4) the fluid flows through the non-located (four) domain of the base bearing. However, at least the donor fluid contacts the silk-bearing red sputum nuclear area, and the process (four) is insoluble for the present invention. The above-mentioned objects, features, and advantages will be more apparent. The preferred embodiments are described below, and the details are as follows. The following preferred embodiments and drawings are only for the purpose of illustration.盥 盥 。 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 A schematic cross-sectional view, and a cross-sectional view of the anode system 114, which is not the same as (4) - 曰^θ, is represented by the same sign of =. It should be noted that the drawing is only for the original size drawing as shown in Fig. 4. The present embodiment provides a fluid area control for electroplating. The FI-type anode-anode M 114 includes a fluid region control system. The bottom-down: ηη fluid region control system, the system 12Q includes a substrate carrying base 130, - a cathode electrical second line m, at least a second official line 142, and at least a second official line 142 and at least a fourth line 144. 10 200920882 The anode system 114 is located above the substrate carrier pedestal 13 , and is essentially disposed corresponding to the processed semiconductor substrate UG. The arguing, the system m and the base wire carrier base (10) are separated from each other - the height of the reaction is Η, the side can be used as the voltage surface of the electric slave, and the other can assist the fluid zone control (4) to set 22G to control the height occupied by the process fluid. In the fluid zone control device 220, the anode system 114 can be a rotation = _ry SyStem or a fixed system _xed sys_. In other words, with respect to the _ bearing base 130, the anode system 114 can perform a rotating motion, or the soil can be held at a fixed position. The m-based wire holder 13Q can also be selected to be rotated or maintained. Fixed position. As shown in FIG. 5, the anode system can include an anode electrode 124 and optionally include at least a fifth line 136, a sensor 122 or a detector (detect 〇r, not shown In the picture). Alternatively, the anode system 114 may also include elements such as an anode chamber 118, a filter membrane, or a diffusion 128. The substrate carrier base 30 is used to carry at least one semiconductor substrate 1 . The substrate carrier base 130 of the present invention may have a belt type structure or a nng type structure. As shown in Fig. 6 and Fig. 7, the substrate carrier base 130 of Fig. 6 has at least one conveyor belt I3〇a, so that a plurality of semiconductor substrate rafts (7) to be processed can be sequentially introduced by the substrate carrier pedestal 13 The substrate supporting base 22 of the seventh embodiment has a ring structure hidden to accommodate the semiconductor substrate 110 to be processed. It should be noted that the substrate carrying base 13 can also be At the same time, it has a ring structure and a conveyor belt (not shown), and the semiconductor substrate no is accommodated by the ring structure, and the ring structure and the semiconductor substrate u are transported by the conveyor belt. 200920882 The cathode electrode 116 is disposed on the substrate carrier base The surface of the frame 30 can be electrically connected to the semiconductor substrate 110. The cathode electrode U6 can simultaneously serve as a fixing component for fixing the semiconductor substrate 110 to a predetermined position of the substrate carrier base 130. In view of this, the cathode electrode 116 There is an electrostatic chuck (e_chuck), a vacuum chuck (vacuum Chuck), a ring type structure or a clamp type structure, as shown in Figs. 8 and 9. Figure 8 The cathode electrode 16 can fix the semiconductor substrate from above the semiconductor substrate n〇, and the cathode electrode U6 of FIG. 9 can be fixed on the surface of the substrate carrier pedestal 13 from the periphery of the semiconductor substrate 110 toward the semiconductor substrate. The semiconductor substrate 110 is clamped in the direction of 11 倾. On the substrate carrying pedestal 130, between the anode system 14 and the cathode electrode, there is a region to be treated (not shown) and a non-processing region (not shown). In the figure, 4 points are located in the 彳-nuclear region _ semiconductor substrate 11Q is scheduled to accept the processing of the process, and the semiconductor substrate 11 partially located in the non-processing region is not intended to accept the processing of the process. Ratio: pipeline 132, second pipeline 134, the third pipeline 142 and the fourth pipeline 144 two squares, around the yang (four) system 114 'to provide or recycle the chemicals, additives, deionized water, gas, control fluid required for the process The third line 142 and the fourth line (4) are opposite to the outer side of the second line 134 and the second line 134. The first line (3), the second line 134, and the third line 142 are opposite to the semiconductor substrate m. Both the fourth pipeline 144 and the fourth pipeline 144 may have any shape of a pipeline, such as a circular shape, a semi-circle, an arc, an ellipse, a rectangle, or a polygonal shape. For example, the first pipeline shown in FIG. 132 and the second line 134 200920882 have a circular arc-shaped cross section, and the third pipeline H2 and the fourth pipeline 144, the first to describe the fluid area control, to cut into a plurality of: 1 132, a plurality of Two pipelines 134, a plurality of third pipelines 14 and a plurality of fourth pipelines 144, and let M f 5 渺, the main ρηΛ / j into a desired shape, such as a circle L, π' ^ ^·1 η, The first line 132, the second line 34, and the third line 142 are all round tubes, and the third line 142 and the fourth line 144 are respectively arranged in a circular pattern. Alternatively or as shown in Fig. 12, when the fluid region control means has the side wall 152 as an aid, the third line 142 and the fourth line 144 may have a linear load surface and be arranged in parallel with each other. It is important to note that the various lines in the figure are tilted towards the semiconductor substrate, as shown in Figure 4. However, the present invention is not limited thereto, and the pipelines of the fluid region control device 220 of the present invention may also be disposed perpendicular to the crystal plane of the semiconductor substrate, inclined toward the center of the semiconductor substrate ', even parallel to the semiconductor substrate. Set on the crystal face of 110. In addition to being able to install lines within the anode system 114, portions of the fluid zone control bar 220 can be actually lined. As shown in FIG. 1 , the fluid C1 domain system 120 may further include at least a sixth pipeline 146 and at least a seventh pipeline 148 ′ disposed in the substrate carrier pedestal 130 and corresponding to the semiconductor substrate 110 . The periphery. The sixth line port 46 and the seventh line 148 may have the above-described various types of wearing surfaces, or may be arranged in any shape by a plurality of sixth lines 146 or seventh lines 148. The fluid zone control device 220 can utilize the valve of the pipeline or each fluid pressure 13 200920882 to regulate the first line 132, the second line 134, the third line 142, the fourth line 丨 44, the fifth line 136, the sixth line 146 or The seventh line 148 is opened and closed, and the fluid area control device 220 can also regulate the flow fluid type, flow direction, flow rate, and even the set angle and position of each line in each line. On the other hand, in addition to the presence of the sensor 122 or the detector inside the anode system 114, various portions of the fluid region control device 220 can be provided with various sensors 122 or detectors, such as A temperature sensor, a flow sensor, or a sensor that measures the surface condition of the wafer (eg, thickness, flatness, etc.). For example, a sensor 122 may be included in the first line 132, and a sensor 122 may be included in the second line 134. These sensors can measure the process conditions or process fluids in real time during the process, so you can accurately and quickly control the enthalpy conditions, and then automatically feedback and adjust various process parameters or process fluids. quality. In order to more clearly illustrate the features of the present invention, one of the operational methods of fluid zone control device 220 will now be described by way of example in which the present invention is applied to an electrochemical plating process. Referring to Fig. 14, there is shown a schematic diagram of the operation of one of the fluid region control devices 220 for electroplating shown in Fig. 13, wherein the same elements or portions are denoted by the same reference numerals. As shown in Fig. 14, first, the fluid region control device 220 shown in Fig. 13 is provided. Thereafter, at least one semiconductor substrate U0 is provided, and the semiconductor substrate 110 is fixed to the substrate carrier base 130 by the cathode electrode 116 or other fixing components. The semiconductor substrate 110 can be a wafer, a slab substrate, or a semiconductor-based silicon-on-insulator (SOI) substrate. In the present embodiment, the semiconductor substrate 110 is a wafer. Since the crystal plane of the wafer of the embodiment needs to receive the electric ore to form the metal material layer 'and the crystal edge of the wafer does not need to form the metal material layer, the area to be processed of the fluid region control device 220 corresponds to the wafer. The crystal face, rather than the processing region 104, corresponds to the crystal edge of the wafer, wherein the crystal face of the wafer can be placed up facing the anode system 114. Next, the third line 142 and the fourth line 144 are opened such that a control fluid 154 continues to flow from the fourth line 144 and is recovered by the third line 142, while the sixth official line 146 and the seventh official line M8 are closed. Wherein, the control fluid 154 is used to maintain the shape and position of the process fluid such as the chemical substance or the cleaning fluid in the area to be treated, so that the chemical substance does not contact the semiconductor substrate 11 (the portion of the semiconductor substrate 11 that does not need to be subjected to process processing, for example, control Fluid 154 can be an inert gas. The fourth line I44 and the third line 142 are both disposed around the semiconductor substrate for providing and recovering the control fluid j M , respectively. At this time, the path of the control fluid i% flowing from the fourth line 144 to the second official line 142 may form a flow line p. Through the configuration of the third line 142 and the fourth line 144, the fluid zone control device 22g causes the domain control fluid 154 to flow through the non-treatment zone of the fluid zone control device 22. After the second opening Ϊ $ line 132 and the second line 丨 ' so that the electric ore, fluid 156 continues to flow from the first line m, and by the second line 134. Here, electroless plating 156 is a process fluid for an electrochemical plating process. The first tube, the line 132 and the first s line 134 are provided between the semiconductor substrate 200920882 110 and the flow line P of the control fluid 54. In order to promote continuous flow of the plating fluid 156 and the control fluid 154, a pump may be installed inside or outside the fluid zone control device 22 as a power source, but is not limited thereto. In other embodiments of the present invention, the process fluid may not be continuously provided and continuously recovered, but may provide a certain amount of process fluid to carry out the reaction, and then consider whether to recycle the process fluid or provide new ones depending on the situation. Process fluid. Since the plating fluid 156 and the control fluid 154 are not mutually soluble, the control fluid 154 can control the flow range of the plating fluid 156 such that the plating fluid 丨 56 does not contact the portion of the semiconductor substrate 110 that does not require process processing, but only contacts. The part of the semiconductor substrate that needs to be processed by the process. In this way, the fluid region control device 220 can control the space occupied by the electric ore fluid 156 by controlling the flow rate of the fluid 154, the flow rate of the money flow I56, and the respective tube_positions and the respective tubes. The anode envelope 124 and the cathode electrode 6 can be electrically connected to different potentials before or after the outflow of the electromineral fluid 56, so that the circuit composed of the anode electrode 24, the electro-mineral fluid 15 and the cathode electrode 116 It will be turned on, and the reaction will be performed around the cathode electrode 116, and the metal material will be on the crystal plane of the semiconductor substrate nQ. Under the foregoing conditions, the control fluid 154 and the electro-mineral fluid 156 are not subject to each other's reaction. The control fluid 154 utilizes the abundance of itself that is immiscible with the electromotive fluid 156 to align the position and flux of the confining fluid. On the date of this issue, the age of the system fluid is 200920882. The control fluid can be in the state of liquid, gas, and steam (v-rs tank 22:). For example, the plating fluid (9) flows in a liquid state, and the body 154 flows in a gaseous state. Alternatively, the electromineral fluid 156 and the body 154 may be liquid. Even the control fluid (9) can enclose a fluid such as carbon dioxide. In other embodiments of the invention, body 154 may additionally contain other materials to assist in (4) operation or to assist in the flow of control surface fluid enthalpy 56. For example, the control fluid 154 can include a fluidized gas, a hot gas, or a cold gas to vary the process temperature or the temperature and characteristics of the Wei fluid 156. As such, the control fluid 154 maintains the shape and position of the process fluid on the one hand, and enhances the manufacturing process on the other hand, and even removes residual residues on the semiconductor substrate (1). The main feature of the present invention is the use of a control fluid in place of the conventional container ' to control the position of the fluid required for the process and the space occupied by the process fluid. In order to achieve the above objectives, (4) fluid (four) process fluids are mutually incompatible, and the difficult fluid can pass through the flow line p which flows by itself to limit the space occupied by the process fluid, and utilize the magnetic force between the control body and the fluid. The function is to control the space occupied by the process fluid, or to control the space occupied by the process fluid by controlling the interaction between the fluid and the process fluid. In view of this, the control fluid 154 may include a magnetic material, an electrically conductive substance, a magnetorheological fluid (magnet〇_rhe〇丨〇gjca丨江江 MRF), an electrorheological fluid (electro-rheo丨〇) giCaj f|uid, erf), even solid particles. Thereby, the fluid region control device 220 can control the characteristics of the control fluid 154 or the plating fluid 156 by using a magnetic force or an electric force, and control the flow of the plating fluid 156 in 200920882. The foregoing method of operation is only one of the embodiments of the present invention, and the actual flow pattern of the control fluid 154 and the electro-recording fluid 156 is adjusted according to actual process requirements. In other words, for different process requirements, the control fluid 154 or electroplating fluid 56 of the present invention can be discharged from any line and recovered in a proper pipeline. Please refer to FIG. 15 to FIG. 8 , which are schematic diagrams showing other operation methods of the fluid region control device 220 for electroplating shown in FIG. 13 , wherein the same elements or parts are still represented by the same symbols. . The operation methods shown in Figs. 15 to 18 are also applicable to an electrochemical plating process, and the main difference between these operation methods and the above-described method is that the flow line of the control fluid 154 and the plating fluid 丨 56 has Changed. As shown in Fig. 15, the control fluid 154 is also discharged from the fourth line (4) and the error is recovered by the third line 142. However, the dying fluid 156 Μ second line 134 is recovered by the first line 132. As shown in Fig. 6, the (4) body (9) W motion 'line ρ also does not change, but the electric clock fluid 156 preferably flows out' and is recovered by the first line 132 and the second line m. As in <17, the first line 132 of the money flow fluid 156 φ flows out and is recovered by the second line port*. The control fluid 154 is discharged from the sixth line 146 and is recovered by the third line ι42. Alternatively, or as shown in Fig. 18, the electric ore fluid 156 flows out from the first to the line 132, and the line 134 is Μ. The control fluid 154 flows out from the seventh tube and is recovered by the (four) line 142 and the fourth tube 144. 200920882 _ Intention is made, the fluid area control device 22G, the fluid flow line ρ and the process The fluid flow line can be applied in a solvent cleaning process and the fluid zone control device 22 of the present invention can be applied to any process requiring control of the operating fluid, for example, a drying process, a wet process, a process An electroporation (etoroless-ing) process, a chemical mechanical polishing (c-drawing, CMP) process, or an electrochemical mechanical polishing process, and the like. When the fluid region control device 220 is applied to the cleaning process, the anode electrode 124 and the cathode electrode U6 need not be electrically connected to different potentials' and the surface fluid 156 can be replaced with a cleaning fluid, such as a deionized water (Dlwater) or a super Critical fluid. Therefore, after the semi-i-body substrate 110 receives the electrochemical electro-mineralization in the fluid region control device 220, the voltage applied to the anode electrode and the cathode electrode can be turned off, and the process fluid is exchanged, and immediately accepted in the same device--cleaning process Or a dry process. It can be seen that the fluid region control device does not even require two components of the anode electrode and the cathode electrode when applied to the cleaning process. Referring to Fig. 19, a green schematic view of a second preferred embodiment of the present invention for cleaning a fluid region control device 3, wherein the same elements or portions are denoted by the same reference numerals. As shown in Fig. 19, the present embodiment provides a fluid region control device 320 for cleaning. The fluid zone control device 320 differs primarily from the fluid zone control device 22 in that the fluid zone control device 320 for cleaning may not require the cathode electrode 116 and the anode system 114. Therefore, the fluid region control device 22 can fix the semiconductor substrate 110 by using a solid component 216, and utilize a pipeline system 214 to assist in controlling the reaction height η' of the process, wherein the fixing component 216 can be 19 200920882 Suction cup, vacuum cup or clamp structure. The pipeline system 214 is disposed above the substrate carrier pedestal 130 corresponding to the semiconductor substrate and is spaced apart from the substrate carrier pedestal 13G. "The reaction is high on the wire carrier 13G." And the surface plan (not shown in the figure). The semiconductor substrate 11Q partially located in the area to be processed is intended to be subjected to the processing of the process, and the portion located in the non-processing area_semiconductor substrate m is not intended to be subjected to the process of the process. In another embodiment of the present invention, the fluid zone control system 12 itself can clean the process, the process, or the drying process, while the gravity of the process fluid itself and the control fluid maintain the position of the process fluid, as shown in (4) When the fluid zone (4) device 32〇_魏职程 or clearance process, the control fluid and process can have other flow-saving formulas. Please refer to (4) to map 24, Lin Lai Μ 19 _ A schematic diagram of other methods of operation of the ugly domain control device 32, wherein the same read or portion is still represented by the same symbol, and the semiconductor substrate (10) herein may also be _day Japanese yen. As shown in Fig. =, when the semiconductor substrate (10) is to be cleaned (D), the first tube (four) 2 and the second line 134, the (four) required cleaning fluid 256 is supplied, and the cleaning fluid is recovered by the fifth line 36 256. The control fluid 1M is discharged from the sixth line tearing seventh line 148 and is recovered from the bottom up by the third line Η2 and the fourth line 144. Alternatively, as shown in Fig. 22, the fluid may be controlled. 154 is flowed out from the third line 142 and the fourth line 144 and is recovered from the top to the bottom by the sixth line 146 and the seventh line 148. 20 200920882 When the crystal edge of the semiconductor substrate 110 is to be cleaned, the fluid area control device The 32 Å area to be processed may correspond to the crystal side of the semiconductor substrate 110, and the non-processing area may correspond to the crystal plane of the semiconductor substrate U. As shown in Fig. 23, the first line 132 and the second line 134 together provide a process The desired control fluid 154 is recovered and the control fluid enthalpy 54 is recovered by the fifth line 136 to protect the crystal face of the wafer located in the non-treated region from contact with the cleaning fluid 256. The cleaning fluid 256 exits from the sixth line 46. And by the first The line 142 is recovered. Further, as shown in Fig. 24, when the crystal back of the semiconductor substrate 110 is to be cleaned, the fixing member 216 may first lift the semiconductor substrate 11 slightly, and the cleaning fluid 256 is provided by the sixth official line 146. The third line 142 recovers the cleaning fluid 256. The control fluid 154 flows out of the first line 132 and the second line 134 and is recovered by the fifth line 36. The fluid area control device 22 for electroplating of the present invention is used or used. The cleaning flow area control device 32 can also be applied to a chemical mechanical polishing process, wherein the process can be divided into a conventional chemical mechanical polishing process and an electrochemical polishing process. Referring to the figure, the green is not the third comparison of the present invention. A cross-sectional view of a fluid region control device 720 for use in polishing. As shown in the first diagram, the fluid region control device can include a polishing system (p〇llsWng system) 7i4 and a fluid region control system, and a first 20' wherein the polishing system 7M further includes a polishing pad 75. A polishing pad holder (padh〇lder) 724, and a research material (8ΐ_ΐ58. When applied to an electrochemical polishing process, the fixing component 216 can serve as an anode electrode] and the polishing crucible holder 724 can serve as a cathode electrode for Power-on accelerated grinding 200920882 f. In addition, when the chemical mechanical polishing process is applied, the fluid region "coating 720 can close the voltage applied to the anode electrode and the cathode electrode, so that a conventional chemical mechanical polishing process can be performed in one device. In other words, through the replacement of some strains, _, and the replacement of process fluids, the semiconductor-based phantom-fluid zone control device quickly performs various processes, such as I-chemical mechanical polishing process. - The cleaning system ^, the substrate carrying base 130 has a wire----------------------------------------------------------------- The semiconductor substrate 110 located in the area to be processed is intended to be subjected to a chemical mechanical polishing process, and the semiconductor substrate 11G partially located in the non-viewing area is not intended to be subjected to the processing of the chemical machine-grinding process. Both the flow line P and the process fluid flow line can be used in the chemical mechanical polishing process, and the height and position of the grinding bowl 751 can be adjusted according to the requirements of the process. It is necessary to carry out chemical research (4), grinding 塾π The semiconductor substrate u〇 can be lifted up to the surface of the polishing pad π. The polishing system 7M can further comprise a measurable crystal. The flatness or material layer thickness sensor 722 performs an instantaneous flat measurement on each part of the semiconductor substrate no, and can directly feed the measurement result into the process. In addition, the grinding system 71 can include each Surface type grinding device, such as mQtary type) grinding device, a lim^type grinding device, a rail type (〇rbita Uype) grinding device, or a fixed abrasive particle (fixed Abrasive web) system. For example, when 22 200920882 - the grinding system 714 is a fixed abrasive particle system, the polishing pad 751 itself may have various types of abrasive particles, and the fluid region control device 72 is supplied with the process fluid It can be a deionized water, and the polishing pad 751 with abrasive particles can be used to roll and polish the entire semiconductor substrate 110 or a specific region of the semiconductor substrate 11 such as the convex region of the surface of the semiconductor wire 110, in conjunction with the deionized water. In practice, the size of the polishing pad 1 may be larger than the semiconductor substrate UG, smaller than the semiconductor substrate (10), or larger than the semiconductor substrate 110. It can also be inferred that the conventional chemical thief polishing process can be performed when the fluid region control device 320 for cleaning is equipped with at least a polishing pad. Because the fluid zone control device 72 can use the control fluid to control the position of the abrasive aggregate 158 or the secret water, and (4) the height and position of the polishing pad 751 to grind the entire semi-conducting county bottom U0 or the semi-conducting county bottom m The area, and thus the fluid area control device 720 has the following side concerns. First, the fluid region control device 720 can easily adjust the position of the to-be-processed region and the non-processing region, and can also easily adjust the position of the semi-conducting county bottom. The semiconductor substrate 11 or the material layer which is required to be in the domain is subjected to grinding to be damaged or destroyed. Secondly, after the special process, the traditional deposition process, or the traditional polishing process, the surface of the single-semiconductor substrate UG or a certain material layer is often 23 200920882 - there will be a uniformity (10) f〇_ty The problem of poorness, for example, after the conventional polishing process, the edge of the substrate 110 will be thinner and the center will be thicker. Since the fluid region control device 720 can easily adjust the positions of the to-be-processed region and the non-processing region, the flatness of the semiconductor substrate 110 or the thickness of the material layer can be measured immediately, so that the semiconductor substrate having a good uniformity can be automatically ground. (10) or material layer. Furthermore, since the flow-domain control sets the 7-control texture to control the required pick-up of the parent's grinding, the fluid area control unit 72() can have any size of grinding 塾7S. Unlike the conventional grinding machine. The size of the abrasive crucible must generally be greater than the size of the semiconductor substrate 110. In addition, since the fluid region control device 72 can apply the grinding (four) 158 or deionized water to the region to be treated, it can be called that the research-free material 158 is in contact with other susceptible regions of the semiconductor wire HGJi, and the grinding material 158 can also be saved. Or use deionized water to avoid unnecessary cost loss. In addition, it should be noted that the fluid region control device Do for the electric ore, the fluid region control device 320 for cleaning, and the fluid region control device 720 for polishing can process the specific region of the wafer. . Referring to Figure 26, a perspective view of one of the fluid zone control devices of the present invention is shown. As shown in the % diagram, the fluid zone control I can include a fluid zone control system 12 and a system 914, wherein the system 914 can be an anode system 1丨4, a line system 214, or a grinding system 714. The fluid region control device can perform a regional plating process, a cleaning process, or a polishing process on the semiconductor substrate no. The area to be treated here need not be limited to the crystal plane and the crystal side, and may correspond to any position on the semiconductor substrate 110, for example, to the rest of the semiconductor substrate 110 on the 24 200920882. It may correspond to a non-processing area, for example, the non-processing area may correspond to a certain peripheral area on the wafer. In other implementations, the area to be processed can be formed into the crystal face, the crystal back, the crystal side of the wafer, or any local area to be processed, and the rest of the wafer can correspond to the non-processed area. According to 1, the above-mentioned day (10) to control the body to (4) the position of the process fluid 'is therefore not like the sand electrochemistry process requires Wei Da Wei _ a large amount of electric mineral fluid. In addition, both the control fluid and the process fluid of the present invention can be recycled. After the control fluid or process fluid is recovered through the pipeline, it can be returned directly to the fluid zone control device (4) via another pipeline. Alternatively, the recovered process fluid blood control fluid can also be processed (10) or not treated immediately.
體_控制裝置中繼續利用。換句糾士义 L MW換句麵,本發明可以根據回收流 =或回收綱_嶋臟_謂程流體 :丁 以對回收流體或回收製裎流體進行適當的分離步 ^接者再咖侧體输輪細細控制裝置 二==輕易且即時地調整製程流體的成分比 大二= 的狀況’無須耗費冗長的時間與龐 =成本去更換製雜體,還可以減少製程流_使用量。此外, 本叙明亦可視製程需求提供一埶 mV,. …裝置5又置於流體控制裝置中, ==或製程流體,進而提昇製程所需之反應溫度 或加快其反應速度。 25 200920882 另一方面’本發明流體區域控制裝置可以透過流速與管線的 控制而使製__財導雜紅需接”减_部分,並 且同時確賴料會作祕半導縣底上不紐受製程處理的部 分’因此可以钱電化學電㈣程於晶_賴上金屬層,省略 邊緣金屬的移除步驟(edge bevd _va丨卿,舰鄉),進而節省 製程時間與製程成本’並且降低製程的複雜度。 由於本發明可湘控制流體取代習知的容器來控制製程流體 的位置因此可以打破出傳統裝置的侷限而發展出各式各樣的製 程_設備。請參_ 27圖至第29圖,第27 示的是本發明 之第四H實;^例之製程操作設備35Q的示意圖,第Μ圖係為第 27圖所示之輸送裝置372的立體示意圖,而第29圖係為第27圖 所不之製程操作設備35G於中層的剖面示意圖,其中相同的元件 或部位沿用相同的符號來表示。如第27圖至第29圖所示,製程 操作設備350包含有一柱狀基台36〇、一自動製程控制系統 (automatic pr〇cess control system,Apc system)324、複數個流體區 域控制裝置322、至少一載入/載出裝置(丨oading/unk)adingdevice) 366與至少一輸送裝置372。柱狀基台36〇可為一直立式基台其 中‘知操作设備350包含有上層、中層與下層,且每一層皆可 連接至六個製程裝置。在本實施例中,中層的其中一個製程裝置 可以為前述之載入/載出裝置366,而其餘製程裝置可以包含有流 體區域控制裝置322或是其他所需的反應艏·室。自動製程控制系 統324能即時偵測製程操作設備35〇的製程效果,以即時調校各 26 200920882 製程之參數設定。 流體區域控制裝置322可具有前述流體區域控制裝置220、流 體區域控制裝置320或流體區域控制裝置720的結構,並位於柱 狀基台360之至少—側面,用以對半導體基底no進行一電化學 電鑛製程、一清洗製程或一化學機械研磨製程等等各式具有流體 之半導體製程。換句話說,各流體區域控制裝置322分別具有一 基底承載基座〗30與一製程系統368。當流體區域控制裝置322 應用於電化學電鍍製程時,製程系統368可以為陽極系統1 η ;當 流體區域控制裝置322應用於清洗製程時,製程系統368可以為 官線系統214;當流體區域控制裝置322應用於化學機械研磨製程 日守,製程系統368則可以為研磨系統714 ; 如第29圖所示’柱狀基台36〇包含有一圓柱形支架362與一 具有角柱形結構的外殼364。於本實施例中’外殼364為一個六角 桎結構,具有六個側面。圓柱形支架362於中層上可連接至五個 製程系統368與-個載入/載出裝置366,且各製程系統规血載 入/載出裝置366可對應至外殼364之—側面。於本發明之其他實 h例中,柱狀基台36G可以包含有任何形狀的支架與外殼,例如 各種角柱形的支架、螺旋形的支架,或是圓柱形的外毅等等。 輸达裝置372位於柱狀基台周圍,用以將複數個半導體 基底no分別傳送至載人/載出裝置366。當要進行製程操作時^ 27 200920882 輸送裝置372之機械手臂374可先滑動至待處理的半導體基底ιι〇 所在之處,以擷取一個半導體基底11〇。之後,利用輸送裝置372 移動並且旋轉半導體基底11〇,使半導體基底110平行放置於載入 /載出裝置366的平台上。載入/載出裝置366係平行於柱狀基台36〇 之側面而設置’用以將半導體基底⑽載人及/或載出(bad and/or unload)柱狀基台36〇,其上亦可具有—真空吸盤,用以固定半導體 ,底110。機械手臂374較佳係為一多片式(muUiple blades)機械手 臂,其關節處皆可自由轉動,以使機械手臂374可以進行三維方 向的攫取與移動。 、 “單一半導體基底110放置於載入/載出裝置366上後,柱狀基 台可以進行水平旋轉及/或上下移動,而把半導體基底110放 置於個隨體區域控制裝置322《基底承載基座13〇丨,接著載 載出裝置366再旋轉回到原來對應至輪送裝置奶的位置。此 才輪达I置372可以重複前述傳送的步驟來傳送下一個半導體 2,直到製程操作設備35〇各層的各基底承載基座—上皆 衣填有一半導體基底110。 =後’可採用前述任—種操作方式同時對各半導體基底⑽ 研磨制4子賴製程、—晶面/晶背/晶邊清洗製程、—化學機械 形^程及/或1化學機械研磨製程。製程處理完畢之後,圓柱 皆載水平旋轉及/或上下移動’以將各半導體基底110 枉狀基台細。其後,圓柱形支架362可以再繼續裝載待處 28 200920882 - 理之半導體基底110。 於本發明之其他實施例中,流體區域控制裝置322與載入/載 出裝置366的位置,以及流體區域控制裝置322所進行的製程皆 可調換或調整,且製程操作設備350也可以包含有其他種類的製 程設備,例如一乾燥裝置。 由於本發明係利用控制流體來控制製程流體的位置,而不像 傳統製程要將半導體基底1 10浸置於溶液槽中,故在此實施例中, 流體區域控制裝置322無須侷限於水平放置方式,而可以使半導 體基底110與流體區域控制裝置322皆直立操作。因此,製程操 作设備350可以設計成直立式的設備,並將載入/載出裝置366垂 直整合於製程操作設備350中,進而有效節省製程操作設備350 的佔地面積。此外,製程操作設備35〇還可以對半導體基底110 進行批次(batch)處理,因此可以大幅地提昇製程的產量。 另外,本發明也可以將流體區域控制裝置與各種不同的反應 裝置整合於同一製程操作設備。請參閱第3〇圖,第3〇圖繪示的是 本發明之第五較佳實施例之製程操作設備45〇的示意圖,其中相同 的凡件或部位仍沿用相同的符號來表示。如第3〇圖所示,製程操 作設備450包含有一自動製程控制系統324、一載入/載出裝置466、 至少一流體區域控制裝置420、至少一輸送裝置472、至少一晶種 >儿積反應室478、至少一阻障層沉積反應室482、至少一乾燥反應 29 200920882 室484與至少一預沉積(pre-deposition)之反應室486(例如:溶劑清洗 或電漿清洗室)。 於此實施例中,輸送裝置472可為一機械手臂。當半導體基底 110置入製程操作設備450之載入/載出裝置466後,輸送裝置472可 以將半導體基底110往返傳送於載入/載出裝置466、流體區域控制 裝置420、晶種沉積反應室478、阻障層沉積反應室482、乾燥反應 室484與預沉積反應室486之間。載入/載出裝置466在此可同時作為 一載出裝置,而於其他實施例中,製程操作設備450亦可另包含有 一載出裝置。 流體區域控制裝置420可具有前述流體區域控制裝置220、流 體區域控制裝置320或流體區域控制裝置720的結構,用以對半導 體基底1〗0進行一電化學電鍍製程、一清洗製程或一化學機械研磨 製程等等各式具有流體之半導體製程。晶種沉積反應室478可用以 對半導體基底110進行一晶種沉積製程,阻障層沉積反應室482可 用以對半導體基底no進行一阻障層沉積製程,乾燥反應室484可 用以對半導體基底110進行一乾燥製程及/或一回火製程,而預沉積 反應室486用以對半導體基底110進行一預沉積製程。 特別注意的是,晶種沉積反應室478、阻障層沉積反應室482、 乾煉反應室484與預沉積反應室牝6等等反應室實際上並非本實施 例之必要元件。本實施例主要的特徵在於,本發明之流體區域控 30 200920882 '制1置4卿需要具錢大的電魅減’ *需要事切半導體基 底η 〇安裝於陰極電極與固定組件之間’也不需褐限於真空環境之 中,因此可以輕易地與其他各式各樣的反應裝置—起整合於同一 個製程操作設備之巾。因此,其所屬技術領域具有通常知識者 應可理解,本實施例之晶種沉積反應室478、阻障層沉積反應室 仙2、乾燥反應室484與預沉積反應室傷實際上也可以被其他製程 反應室所取代’例如後沉積(P〇st_dep〇siti〇n)反應室、研磨製程反應 Ϊ、賴製程反應室、任何化學氣相沉積反應室或任何物理氣相 沉積反應室等等。 請參閱第31圖’第31圖繪示的是本發明之第六較佳實施例之 製程操作設備850的示意圖,其中相同的元件或部位仍沿用相同的 符號來表示。如第31圖所示,製程操作設備85〇為一全功能式系統 (all-in-one system)或一集群系統(c]ustersystem),包含有一自動製 程控制系統324、至少一裝載埠(i〇a(j part)816、至少一單晶圓承載 室(single wafer l〇ad lock chamber, SWLL Chamber)830、二個預清洗 反應室(pre-cleaning chamber)840、822、至少一钽/氮化鈕沉積反應 室(Ta/TaN deposition chamber)852、至少一銅晶種沉積反應室 812、二個緩衝室(bufferchamber)832、842、二個銅電化學電鑛(Cu ECP)反應室860、802、二個銅化學機械研磨(cu cmp)反應室870、 890、至少一覆蓋層(cap layer)反應室880,以及三個機械手臂872, 利用此系統晶片可在不需破真空的情況下進行所有的製程步驟。 200920882 — 裝載埠816,用來裝載晶圓盒,是晶圓盒進出製程操作設備850 之出入口,以提供晶圓加工。為使適用於迷你環境之技術,裝載 埠816可具有至少一晶圓介面81〇。其中,晶圓介面81〇可以是一個 標準機械介面(standard mechanical interface, SMIF),以裝載至少一 標準化之SMIF型晶圓盒。或者,裝載埠816之晶圓介面81〇亦可為 適用如開式整合艙(front opening unified pod,FOUP)形式之晶圓 盒。需注意的是,製程操作設備850可包含有複數個裝載埠816, 且裝載埠816可具有複數個晶圓介面81〇,這些裝載埠8丨6或晶圓介 面810實際上可以裝設於製程操作設備85〇之任何位置。 單曰日圓承載室830可具有一定向平面對準器(〇rjent〇r),用以把 晶圓的定向平面(orientation),或將缺口(n〇tch)對準至所定位的位 置-或者單日日圓承載£ 830可用以對晶圓進行除氣(^叹狀)、冷卻、 吹氣(pump)、潔淨(purge)等等步驟。預清洗反應室84〇與預清洗反 應呈822可於晶圓進行沉積製程之前對晶圓進行—預清洗製程。鈦 復化鈦沉積反應室852係用以於晶圓表面沉積一鈦金屬層及/或一 氣化鈦層,鈦金屬層錢化鈦層可作為介電層與銅層之間的阻障 層鋼a曰種"L積反應室812可以於晶圓表面沉積一銅晶種層。緩衝 钉32與緩衝室842可作為定向平面對準器,也可以對晶圓進行除 氣冷卻17人氣、冷:淨、退火(anneal)或測量(meir〇1〇gy)等等步驟。 、鋼私化子电鑛反應室860與銅電化學電鑛反應室8〇2可具有前 述流體區域控制裝置22〇的結構’用以對半導體基底ιι〇進行一電 32 200920882 化學電鑛製裎,以於前述銅晶種層表面鍍上一層所需的銅層。銅 化學機械研磨反應室87〇與銅化學機械研磨反應室890可具有前述 流體區域控制裝置720的結構,用以對半導體基底110進行一化學 機械研磨製程。此外,銅電化學電鑛反應室、銅電化學電鑛反 應至802、銅化學機械研磨反應室870與銅化學機械研磨反應室890 白T用X對半‘體基底u〇進行一預清洗製程、一後清洗(p〇stContinued use in the body_control device. In other words, the invention can be based on the recovery flow = or recovery class _ 嶋 dirty _ pre-circulation fluid: Ding to the recovery of the fluid or recovery of the sputum fluid for appropriate separation step Body transport wheel fine control device ===Easy and instantaneous adjustment of the composition of the process fluid than the sophomore = the situation of 'no need to spend lengthy time and cost = cost to replace the hybrid, can also reduce the process flow _ usage. In addition, this description can also provide a 埶mV according to the process requirements. The device 5 is placed in the fluid control device, == or process fluid, thereby increasing the reaction temperature required for the process or speeding up the reaction. 25 200920882 On the other hand, 'the fluid zone control device of the present invention can reduce the amount of __ 财 杂 杂 杂 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 The part processed by the process 'so can be electrochemically charged (four) to the metal layer, omitting the edge metal removal step (edge bevd _va丨qing, shiptown), thereby saving process time and process cost' and reducing The complexity of the process. Since the present invention can control the fluid to replace the conventional container to control the position of the process fluid, it can break the limitations of the conventional device and develop a variety of processes _ equipment. Please refer to _ 27 to Figure 29 is a schematic view showing a fourth embodiment of the present invention; a schematic diagram of the process operating device 35Q of the present invention, and a second schematic view of the conveying device 372 shown in Figure 27, and Figure 29 is a Figure 27 is a schematic cross-sectional view of the process operating device 35G in the middle layer, wherein the same elements or parts are denoted by the same reference numerals. As shown in Figures 27 to 29, the process operating device 350 includes a columnar abutment. 36〇, an automatic pr〇cess control system (Apc system) 324, a plurality of fluid region control devices 322, at least one loading/unloading device (adinging/unk) ading device 366 and at least one transport Device 372. The columnar abutment 36A can be an upright vertical abutment wherein the 'operational device 350 includes an upper layer, a middle layer and a lower layer, and each layer can be connected to six process devices. In this embodiment, the middle layer One of the process devices may be the aforementioned loading/unloading device 366, and the remaining process devices may include a fluid region control device 322 or other required reaction chambers. The automatic process control system 324 can instantly detect the process. The process effect of the operating device 35〇 is used to instantly adjust the parameter settings of each of the 26 200920882 processes. The fluid region control device 322 may have the structure of the fluid region control device 220, the fluid region control device 320 or the fluid region control device 720 described above, and is located At least a side of the columnar abutment 360 for conducting an electrochemical ore process, a cleaning process, or a chemical mechanical study on the semiconductor substrate no Processes and the like have fluid semiconductor processes. In other words, each fluid region control device 322 has a substrate carrying base 30 and a process system 368. When the fluid region control device 322 is applied to the electrochemical plating process, The process system 368 can be an anode system 1 η; when the fluid zone control device 322 is applied to the cleaning process, the process system 368 can be the official line system 214; when the fluid zone control device 322 is applied to the chemical mechanical polishing process, the process system 368 Then, it may be a grinding system 714; as shown in Fig. 29, the columnar base 36 includes a cylindrical bracket 362 and a casing 364 having a prismatic structure. In the present embodiment, the outer casing 364 is a hexagonal structure having six sides. The cylindrical bracket 362 can be coupled to five process systems 368 and a load/delivery device 366 on the intermediate layer, and each process system gauge blood loading/unloading device 366 can correspond to the side of the outer casing 364. In other embodiments of the present invention, the columnar abutment 36G may include a bracket and an outer casing of any shape, such as various angular post brackets, spiral brackets, or cylindrical outer diameters and the like. A delivery device 372 is located around the columnar abutment for transferring a plurality of semiconductor substrates no to the manned/loaded device 366, respectively. When the process operation is to be performed, the mechanical arm 374 of the transport device 372 can be slid to the place where the semiconductor substrate to be processed is located to capture a semiconductor substrate 11〇. Thereafter, the semiconductor substrate 11 is moved and rotated by the transport device 372 such that the semiconductor substrate 110 is placed in parallel on the platform of the loading/unloading device 366. The loading/unloading device 366 is disposed parallel to the side of the columnar base 36〇 to "sand" and/or unload the semiconductor substrate (10) to the columnar base 36〇. There may also be a vacuum chuck for holding the semiconductor and the bottom 110. The robot arm 374 is preferably a muUiple blades robot arm that is freely rotatable at its joints so that the robot arm 374 can be grasped and moved in three dimensions. After the single semiconductor substrate 110 is placed on the loading/unloading device 366, the columnar base can be horizontally rotated and/or moved up and down, and the semiconductor substrate 110 is placed on a body area control device 322. After the seat 13 is turned, the loading device 366 is then rotated back to the position corresponding to the milk of the transfer device. The rotation of the I set 372 can repeat the aforementioned transfer step to transfer the next semiconductor 2 until the process operation device 35 Each of the substrate carrying bases of each layer is filled with a semiconductor substrate 110. The latter can be used to simultaneously grind the semiconductor substrate (10) into four sub-processes, crystal planes/crystal backs/crystals. The cleaning process, the chemical mechanical process, and/or the 1 chemical mechanical polishing process. After the process is completed, the cylinders are horizontally rotated and/or moved up and down to thin the bases of the semiconductor substrates 110. Thereafter, The cylindrical holder 362 can be further loaded with the semiconductor substrate 110. In other embodiments of the invention, the fluid region control device 322 and the loading/unloading device 366 The position, and the process performed by the fluid zone control device 322 can be interchanged or adjusted, and the process operating device 350 can also include other types of process equipment, such as a drying device. The present invention utilizes a control fluid to control process fluid. The position, rather than the conventional process, is to immerse the semiconductor substrate 1 10 in the solution tank, so in this embodiment, the fluid region control device 322 is not limited to the horizontal placement mode, but the semiconductor substrate 110 and the fluid region control device can be The 322 is all upright. Therefore, the process operating device 350 can be designed as an upright device and vertically integrate the loading/unloading device 366 into the process operating device 350, thereby effectively saving the floor space of the process operating device 350. In addition, the process operating device 35 can also perform batch processing on the semiconductor substrate 110, thereby greatly increasing the throughput of the process. In addition, the present invention can also integrate the fluid region control device with various different reaction devices. Process operation equipment. Please refer to Figure 3, and Figure 3 shows the present invention. A schematic diagram of a process operating device 45A of the fifth preferred embodiment, wherein the same parts or parts are still indicated by the same symbols. As shown in FIG. 3, the process operating device 450 includes an automatic process control system 324. a loading/unloading device 466, at least one fluid region control device 420, at least one transport device 472, at least one seed crystal> an integrative reaction chamber 478, at least one barrier layer deposition reaction chamber 482, at least one drying reaction 29 200920882 chamber 484 is coupled to at least one pre-deposition reaction chamber 486 (e.g., solvent cleaning or plasma cleaning chamber). In this embodiment, delivery device 472 can be a robotic arm. After the semiconductor substrate 110 is placed in the loading/unloading device 466 of the process operating device 450, the transport device 472 can transfer the semiconductor substrate 110 to and from the loading/unloading device 466, the fluid region control device 420, and the seed deposition reaction chamber. 478, a barrier deposition reaction chamber 482, a drying reaction chamber 484, and a pre-deposition reaction chamber 486. The loading/unloading device 466 can be used as a loading device at the same time, and in other embodiments, the process operating device 450 can further include a loading device. The fluid region control device 420 may have the foregoing structure of the fluid region control device 220, the fluid region control device 320 or the fluid region control device 720 for performing an electrochemical plating process, a cleaning process or a chemical machine on the semiconductor substrate 1 Grinding processes and the like have various semiconductor processes with fluids. The seed deposition reaction chamber 478 can be used to perform a seed deposition process on the semiconductor substrate 110. The barrier layer deposition reaction chamber 482 can be used to perform a barrier layer deposition process on the semiconductor substrate no. The dry reaction chamber 484 can be used to the semiconductor substrate 110. A drying process and/or a tempering process is performed, and the pre-deposition chamber 486 is used to perform a pre-deposition process on the semiconductor substrate 110. It is particularly noted that the reaction chambers such as the seed deposition reaction chamber 478, the barrier deposition reaction chamber 482, the dry reaction chamber 484, and the pre-deposition chamber 牝6 are not actually necessary elements of this embodiment. The main feature of this embodiment is that the fluid region control 30 200920882 of the present invention requires a large electric charm reduction. * It is necessary to cut the semiconductor substrate η 〇 between the cathode electrode and the fixed component. No browning is required in a vacuum environment, so it can be easily integrated with other various reaction devices to integrate the same process equipment. Therefore, it should be understood by those skilled in the art that the seed deposition reaction chamber 478, the barrier deposition reaction chamber 2, the dry reaction chamber 484, and the pre-deposition reaction chamber injury of the present embodiment may actually be The process chamber is replaced by, for example, a post-deposition (P〇st_dep〇siti〇n) reaction chamber, a grinding process reaction crucible, a Lai process chamber, any chemical vapor deposition reaction chamber, or any physical vapor deposition reaction chamber, and the like. Referring to Fig. 31, Fig. 31 is a schematic view showing a process operating device 850 according to a sixth preferred embodiment of the present invention, wherein the same elements or portions are denoted by the same reference numerals. As shown in FIG. 31, the process operating device 85 is an all-in-one system or a cluster system, and includes an automatic process control system 324 and at least one load port (i). 〇a (j part) 816, at least one single wafer l〇ad lock chamber (SWLL Chamber) 830, two pre-cleaning chambers 840, 822, at least one helium/nitrogen a Ta/TaN deposition chamber 852, at least one copper seed deposition reaction chamber 812, two buffer chambers 832, 842, and two copper electrochemical electric (Cu ECP) reaction chambers 860, 802, two copper chemical mechanical polishing (cu cmp) reaction chambers 870, 890, at least one cap layer reaction chamber 880, and three robot arms 872, which can be used without breaking the vacuum Perform all process steps. 200920882 — Load 埠 816, which is used to load the wafer cassette, which is the entrance and exit of the wafer cassette into and out of the process operation equipment 850 to provide wafer processing. To enable the technology suitable for the mini environment, the load 埠 816 can be loaded. Having at least one wafer interface 81〇. The circular interface 81〇 can be a standard mechanical interface (SMIF) for loading at least one standardized SMIF type wafer cassette. Alternatively, the wafer interface 81 of the 埠816 can also be used for an open integrated compartment. A wafer cassette in the form of a front opening unified pod (FOUP). It should be noted that the process operating device 850 can include a plurality of loading ports 816, and the loading port 816 can have a plurality of wafer interfaces 81〇, and the loading ports 8 The 丨6 or wafer interface 810 can be mounted anywhere in the process operating device 85. The single-turn yen carrier chamber 830 can have a directional aligner for aligning the wafer. Orientation, or aligning the notch (n〇tch) to the position it is positioned on - or a single day yen carrying £830 can be used to degas (snap), cool, puff, Purification, etc. The pre-cleaning reaction chamber 84〇 and the pre-cleaning reaction are 822. The wafer can be pre-cleaned before the deposition process of the wafer. The titanium-recovered titanium deposition reaction chamber 852 is used for the crystal. Depositing a titanium metal layer on the round surface / or a vaporized titanium layer, a titanium metal layer of titanium can be used as a barrier layer between the dielectric layer and the copper layer, a "L" reaction chamber 812 can deposit a copper seed layer on the surface of the wafer . The cushioning pin 32 and the buffer chamber 842 can be used as an orientation flat aligner, and the wafer can be degassed to cool 17 air, cold: net, anneal or measurement (meir〇1〇gy) and the like. , the steel private sub-mine reaction chamber 860 and the copper electrochemical electro-mine reaction chamber 8〇2 may have the structure of the aforementioned fluid region control device 22〇 for conducting a semiconductor on the semiconductor substrate 2009ι32 32 200920882 chemical electric mining system The surface of the copper seed layer is coated with a desired copper layer. The copper chemical mechanical polishing reaction chamber 87A and the copper chemical mechanical polishing reaction chamber 890 may have the structure of the aforementioned fluid region control device 720 for performing a chemical mechanical polishing process on the semiconductor substrate 110. In addition, a copper electrochemical electrowinning reaction chamber, a copper electrochemical electrowinning reaction to 802, a copper chemical mechanical polishing reaction chamber 870, and a copper chemical mechanical polishing reaction chamber 890 white T are subjected to a pre-cleaning process for the X-half-body substrate u〇. , after cleaning (p〇st
ClCai—或—乾燥製程。覆蓋層反應室880制以於晶圓表面 ’儿和一復盍層來保護晶圓表面,可用以避免晶圓之銅層離開製程 插作设備850之後氧化而形成氧化物,也可以避免外界之污染物接 觸覆蓋層下方的材料層或裝置。 於此實施例中,機械手臂872可為一單片式(Sing]eblade)機械 手臂或一多片式(multiple blades)機械手臂。當晶圓置入製程操作設 備850後’機械手臂872可以將晶圓往返傳送於裝解816、單晶圓 承載室830、緩衝室832、842與各反應室802、812、822、84〇、852、 860、870、880、890之間。 其所屬技術領域具有通常知識者應可理解,根據所需的產品 產量(throughput)與產品品質(quaHty) ’本實施 爾際上也二 製程反應室所取代,例如後沉積反應室、顧製程反應室、任何 化學氣相沉積反應室或任何物理氣相沉積反應室等等。本實施例 係以一銅製程來說明本發明應用於一後段製程 33 200920882 (back-end-of-the-Hne process, BEOL process)^^^^ ft 程設備,其所屬技術領域具有通常知識者麵理解,本發明不需 偈限於銅製程’而可以用於形成任何所需的材料層或半導體結構而 再者’本發明亦可·輸送帶作為半導職底1U)於製程操作 设備内部的輸送媒介。請參閱第32圖,第32_示的是本發明之 第七較佳實施例之製程操作設備55_示意圖,其中相同的元件或 雜仍沿絲表示。如第32_示,製程操作設備550 已含有-自動製程控制系統324、一載人/載出裝置楊、至少一流 體區域控制裝置520、至少一輸送帶572、至少一晶種沉積反應室 谓、至少一阻障層沉積反應室搬、至少—乾燥反應室彻與至少 一預沉積反射.。射’ 區赌織置5騎具有前述流 體區域控制裝置220、流體區域控制裝置32〇或流體_控制裝置 的結構’用以對半導體基底u〇進行一電化學電鍵製程、一清 洗製裎或一化學機械研磨製程等等製程。 、第五實&例主要的不同處在於’本實施例之輸送裝置包含 有—輪送帶572。當半導體基底崎入製程操作設備別之載入/ ==置爾’輸送帶572可以承載半導體基底卿返傳送於流 n、控制裝置420、晶種沉積反應室478、阻障層沉積反應室 4。82、乾探反應1484與預沉積反應室傷之間^由於本發明之流體 =控繼置52〇不轉事先料導體基仙岐裝於陰極電極與 s德件之間,因此$程操作設備55()只需利用—個簡單的輸送帶 34 200920882 572就可⑽料體基助峰人各反麵接受製程處理。 傳統電化學電鍍裝置、值纪、主冰制1 磨裝置通常為開放式系㈣程先::二蝴統化學機械研 於周圍環境中,使得裝置其中的化學物質容易逸散 中存在具污錄的化學_,因此可能讓周圍環境 裝置互相整合。由於本翻=心置_與其他製程 量減少,且f程化⑽ _置之製程流體的使用 ^且區域控缝置财时,所以 =控制裝置本身與流體區域控讎置_可 的 本發明之流體區域控制裝置可以克服習峨 與f重不同的反應裝置整合於同—製程操作設備。-方面可= 斜導體基祕各·設備間往返 免半導體減讀㈣贿料沖$扣可以避 了去除氧化物㈣二=綠化’進而節省 設備=::::輸Γ機械手f作為製程操作 較佳實施例之_价4二二晴示的是本發明之第八 仍沿用相_时=1 其中相邮元件或部位 右 4表不。如第33圖所示’製程操作設備650包含 ‘程控制系統324、至少一_區域控制裝置62〇、一輸 ^==::rt674。其中,流體區域控織―前 裝控制裝置220、流體區域控織置伽或流體區域控制 -白、、、。構,用以對半導體基底110進行一電化學電鍍製程、 35 200920882 一清洗製程或一化學機械研磨製程等等製程。機械手臂674用以傳 送半導體基底110往返於輸送帶672與流體區域控制裝置62〇之 間,而輸送f672用以將半導體基底110傳進並且傳出製程操作設 備 650。 當要接受流體區域控制裝置62〇之處理時,待處理的半導體基 底1丨〇先藉由輸送帶672傳送至流體區域控制裝置62〇周圍。接著, 機械手臂674失取前述半導縣底u〇,並將半導體基底uq置入流 體區域控制裝置620之基底承載基座130上。其後,流體區域控制 裝置62〇可先對半導縣底11()進行—電化學魏軸或—清洗製 程等等製程。待流魏域控繼置㈣處理完成之後,機械手臂_ 再將半導體基底1職回輸送帶672上,並且&輸送帶672將半導體 基底m送往賴之製程設備。此時,製雜作設備咖則可以繼 續處理下一個半導體基底1丨〇。 由此可知’由於半導縣底無須先安置於陰極電極與固定组 件之間’也不需要傾斜地置入電鑛流體中,所以本發明之繁 攸備可啸次處理大賴半導縣底,有效地提料品的 量。基底承載基座可以個其輸送帶環狀結構直接將: 可以省略半導體基底的載入/載出裝置, 也比習知技術更為簡單。 底傳送至默位置接受製程流_處理,因此製轉料備= 過程 且半導體基底的浸潤 36 200920882 以上所述僅為本發明之較佳實施例,凡依本發明申請專利範 圍所做之均等變化與修飾,皆應屬本發明之涵蓋範圍。 【圖式簡單說明】 第1圖至第3圖為習知電化學電鍍製程之製程示意圖。 第4圖繪示的是本發明第一較佳實施例之流體區域控制裝置的剖 面示意圖。 · 第5圖繪示的是第4圖所示之陽極系統的剖面示意圖。 第6圖繪示的是本發明之一較佳實施例基底承載基座的立體示意 圖。 第7圖繪示的是本發明之另一較佳實施例基底承載基座的俯視示 意圖。 第8圖繪示的是本發明之一較佳實施例陰極電極的立體示意圖。 第9圖繪示的是本發明之另一較佳實施例陰極電極的側視示意圖。 第10圖至第12圖繪示的是本發明第一、第二、第三與第四管線 的截面示意圖。 第13圖繪示的是本發明另一較佳實施例之流體區域控制裝置的剖 面示意圖。 第14圖至第18圖繪示的是第13圖所示之流體區域控制裝置的操 作方法之示意圖。 第19圖繪示的是本發明之第二較佳實施例的流體區域控制裝置的 剖面示意圖。 第2 0圖繪示的是本發明又一較佳實施例之流體區域控制裝置的剖 37 200920882 _ 面示意圖。 第21圖至第24圖繪示的是第19圖所示之流體區域控制裝置的操 作方法之示意圖。 第25圖繪示的是本發明之第三較佳實施例的流體區域控制裝置的 剖面示意圖。 第26圖繪示的是本發明流體區域控制裝置之一操作示意圖。 第27圖繪示的是本發明之第四較佳實施例之製程操作設備的示意 圖。 第28圖係為第27圖所示之輸送裝置的立體示意圖。 第29圖係為第27圖所示之製程操作設備於中層的剖面示意圖。 第30圖繪示的是本發明之第五較佳實施例之製程操作設備的示意 圖。 第31圖繪示的是本發明之第六較佳實施例之製程操作設備的示意 圖。 第32圖繪示的是本發明之第七較佳實施例之製程操作設備的示意 圖。 第33圖繪示的是本發明之第八較佳實施例之製程操作設備的示意 圖。 【主要元件符號說明】 10 晶圓 12 電鍍槽 14 陽極系統 16 陰極電極 18 固定組件 20 電鍍裝置 38 200920882 22 電鍍流體 24 陽極電極 26 過濾薄膜 28 擴散薄膜 30 陽極室 32 電鍍流體提供管線 110 半導體基底 114 陽極系統 116 陰極電極 118 陽極室 120 流體區域控制糸統 124 陽極電極 126 過濾薄膜 128 擴散薄膜 130 基底承載基座 130a 輸送帶 130b 環狀結構 132 第一管線 134 第二管線 136 第五管線 142 第三管線 144 第四管線 146 第六管線 148 第七管線 152 側壁 154 控制流體 156 電鍍流體 158 研磨漿料 214 管線系統 216 固定組件 220 流體區域控制裝置 256 清洗流體 320 流體區域控制裝置 322 流體區域控制裝置 324 自動製程控制系統 350 製程操作設備 360 柱狀基台 362 圓柱形支架 364 外殼 366 載入/載出裝置 368 製程系統 372 輸送裝置 420 流體區域控制裝置 450 製程操作設備 39 200920882 466 載入/載出裝置 472 輸送裝置 478 晶種沉積反應室 482 阻障層沉積反應室 484 乾燥反應室 486 預沉積反應室 520 流體區域控制裝置 550 製程操作設備 572 輸送帶 620 流體區域控制裝置 650 製程操作設備 672 輸送帶 674 機械手臂 720 流體區域控制裝置 714 研磨系統 722 感測器 724 研磨塾固定座 751 研磨塾 802 銅電化學電鍍反應室 810 晶圓介面 812 銅晶種沉積反應室 816 裝載埠 822 預清洗反應室 830 單晶圓承載室 832 緩衝室 840 預清洗反應室 842 緩衝室 850 製程操作設備 852 钽/氮化钽沉積反應室 860 銅電化學電鍍反應室 870 銅化學機械研磨反應室 872 機械手臂 880 覆蓋層反應室 890 銅化學機械研磨反應室 914 系統 40ClCai—or—drying process. The cover layer reaction chamber 880 is formed on the surface of the wafer and a retanning layer to protect the surface of the wafer, so as to prevent the copper layer of the wafer from being oxidized to form an oxide after leaving the process insertion device 850, and the outside can be avoided. The contaminant contacts the layer or device of material beneath the cover. In this embodiment, the robotic arm 872 can be a single-piece mechanical arm or a multiple blade mechanical arm. After the wafer is placed in the process operating device 850, the robot arm 872 can transport the wafer to and from the assembly 816, the single wafer carrier chamber 830, the buffer chambers 832, 842, and the reaction chambers 802, 812, 822, 84, Between 852, 860, 870, 880, and 890. It should be understood by those skilled in the art that it is replaced by the process of the product and the quality of the product (quaHty), which is replaced by the reaction chamber of the second process, such as the post-deposition reaction chamber and the process reaction. Room, any chemical vapor deposition reaction chamber or any physical vapor deposition reaction chamber, and the like. In this embodiment, a copper process is used to illustrate the application of the present invention to a back-end-of-the-H-process (BEOL process) ^^^^ ft process device, which has the general knowledge in the technical field. It is understood that the present invention is not limited to the copper process' and can be used to form any desired material layer or semiconductor structure, and the 'invention can also be used as a semi-conductor 1U in the process operation equipment. Transport medium. Referring to Fig. 32, there is shown a schematic diagram of a process operating device 55_ of a seventh preferred embodiment of the present invention, in which the same elements or impurities are still indicated along the wire. As shown in FIG. 32, the process operating device 550 already includes an automatic process control system 324, a manned/loaded device yang, at least one fluid region control device 520, at least one conveyor belt 572, and at least one seed deposition reaction chamber. At least one barrier layer deposition reaction chamber, at least - the drying reaction chamber is thoroughly and at least one pre-deposited reflection. The 'zone gambling woven 5 rider has the structure of the fluid region control device 220, the fluid region control device 32 or the fluid_control device' for performing an electrochemical keying process, a cleaning process or a semiconductor substrate Chemical mechanical polishing process and other processes. The main difference between the fifth embodiment and the fifth embodiment is that the conveying device of the present embodiment includes a carrier belt 572. When the semiconductor substrate is processed into a process operation device, the load carrier 572 can carry the semiconductor substrate back to the flow n, the control device 420, the seed deposition reaction chamber 478, and the barrier deposition reaction chamber 4 82, between the dry reaction 1484 and the pre-deposition reaction chamber injury ^ because the fluid of the present invention = control relay 52 〇 does not change the pre-material conductor base between the cathode electrode and the s-piece, so the operation The device 55() only needs to use a simple conveyor belt 34 200920882 572 to receive the process processing of the (10) material base. The traditional electrochemical plating device, the value meter, and the main ice 1 grinding device are usually open type (four). First:: The two butterfly chemical machine is studied in the surrounding environment, so that the chemical substances in the device are easily dispersed. The chemical _, therefore, may allow the surrounding devices to integrate with each other. The present invention is controlled by the control device itself and the fluid region control unit because the amount of the process is reduced and the amount of other processes is reduced, and the process flow of the f-process (10) _ is used. The fluid zone control device can overcome the integration of the reaction device with the same weight and the weight of the F-integrated operation device. - Aspects can be = slanted conductors, secrets, equipment, round-trip, semiconductor-free reading (4) bribes, rushing, deductions can avoid oxides (four) two = greening, and then save equipment =:::: transmission robot f as a process operation The preferred embodiment of the _ price of 4 22 is shown in the eighth aspect of the invention is still used phase _ hour = 1 where the elearning element or part of the right 4 is not. As shown in Fig. 33, the process operating device 650 includes a 'process control system 324, at least one_region control device 62, and one input ^==::rt 674. Among them, the fluid area control weaving - the front mounting control device 220, the fluid area control weaving gamma or the fluid area control - white, ,,. The structure is used for performing an electrochemical plating process on the semiconductor substrate 110, a process of 35 200920882, a cleaning process, or a chemical mechanical polishing process. The robot arm 674 is used to transport the semiconductor substrate 110 to and from the conveyor belt 672 and the fluid zone control device 62, and the f672 is used to transfer the semiconductor substrate 110 into and out of the process operating device 650. When the processing of the fluid zone control means 62 is to be performed, the semiconductor substrate 1 to be processed is first transferred by the conveyor belt 672 to the periphery of the fluid zone control means 62. Next, the robot arm 674 loses the aforementioned semiconductor substrate and places the semiconductor substrate uq on the substrate carrier base 130 of the fluid region control device 620. Thereafter, the fluid zone control device 62 may first perform an electrochemical-axis or a cleaning process on the bottom of the semi-conducting county 11 (). After the completion of the process (four), the robot arm _ re-attaches the semiconductor substrate 1 to the conveyor belt 672, and the & conveyor belt 672 sends the semiconductor substrate m to the processing device. At this time, the manufacturing device can continue to process the next semiconductor substrate. It can be seen that 'the bottom of the semi-conducting county does not need to be placed between the cathode electrode and the fixed component' and does not need to be placed obliquely into the electric ore fluid. Therefore, the complexity of the present invention can be handled at the bottom of the semi-conducting county. Effectively extract the amount of the item. The substrate carrying base can be directly connected to its belt loop structure: the loading/unloading device of the semiconductor substrate can be omitted, and it is simpler than the prior art. The bottom transfer to the silent position accepts the process flow_process, so the transfer process = process and the semiconductor substrate infiltration 36 200920882 The above is only a preferred embodiment of the present invention, and the equivalent variation of the patent scope of the present invention And modifications are intended to be within the scope of the invention. [Simple Description of the Drawings] Figs. 1 to 3 are schematic views showing the process of the conventional electrochemical plating process. Fig. 4 is a cross-sectional view showing the fluid region control device of the first preferred embodiment of the present invention. Figure 5 is a cross-sectional view of the anode system shown in Figure 4. Figure 6 is a perspective view of a substrate carrying base of a preferred embodiment of the present invention. Figure 7 is a plan view showing a substrate carrying base of another preferred embodiment of the present invention. Figure 8 is a perspective view showing a cathode electrode of a preferred embodiment of the present invention. Figure 9 is a side elevational view showing a cathode electrode of another preferred embodiment of the present invention. Fig. 10 through Fig. 12 are schematic cross-sectional views showing the first, second, third and fourth lines of the present invention. Figure 13 is a cross-sectional view showing a fluid region control device in accordance with another preferred embodiment of the present invention. Fig. 14 through Fig. 18 are schematic views showing the operation method of the fluid region control device shown in Fig. 13. Fig. 19 is a cross-sectional view showing the fluid region control device of the second preferred embodiment of the present invention. Figure 20 is a cross-sectional view showing a fluid region control device according to still another preferred embodiment of the present invention. 21 to 24 are views showing the operation method of the fluid region control device shown in Fig. 19. Figure 25 is a cross-sectional view showing the fluid region control device of the third preferred embodiment of the present invention. Figure 26 is a schematic view showing the operation of one of the fluid region control devices of the present invention. Figure 27 is a schematic view showing a process operating apparatus of a fourth preferred embodiment of the present invention. Figure 28 is a perspective view of the conveying device shown in Figure 27. Figure 29 is a schematic cross-sectional view showing the process operation apparatus shown in Figure 27 in the middle layer. Figure 30 is a schematic view showing a process operating apparatus according to a fifth preferred embodiment of the present invention. Figure 31 is a view showing the process operation apparatus of the sixth preferred embodiment of the present invention. Figure 32 is a schematic view showing a process operating apparatus of a seventh preferred embodiment of the present invention. Figure 33 is a view showing the process operation apparatus of the eighth preferred embodiment of the present invention. [Main component symbol description] 10 Wafer 12 Plating bath 14 Anode system 16 Cathode electrode 18 Fixing assembly 20 Plating device 38 200920882 22 Electroplating fluid 24 Anode electrode 26 Filter film 28 Diffusion film 30 Anode chamber 32 Electroplating fluid supply line 110 Semiconductor substrate 114 Anode System 116 Cathode Electrode 118 Anode Chamber 120 Fluid Zone Control System 124 Anode Electrode 126 Filter Film 128 Diffusion Film 130 Substrate Carrier Base 130a Conveyor Belt 130b Annular Structure 132 First Line 134 Second Line 136 Fifth Line 142 Third Line 144 Fourth Line 146 Sixth Line 148 Seventh Line 152 Sidewall 154 Control Fluid 156 Plating Fluid 158 Abrasive Slurry 214 Line System 216 Fixing Assembly 220 Fluid Zone Control 256 Cleaning Fluid 320 Fluid Zone Control 322 Fluid Zone Control 324 Automatic Process Control System 350 Process Operating Equipment 360 Column Abutment 362 Cylindrical Bracket 364 Housing 366 Loading/Unloading Device 368 Process System 372 Conveying Device 420 Fluid Zone Control Device 450 Process Operating Device 39 20 0920882 466 Loading/unloading device 472 Conveying device 478 Seeding deposition reaction chamber 482 Barrier layer deposition reaction chamber 484 Drying reaction chamber 486 Pre-deposition reaction chamber 520 Fluid region control device 550 Process operating device 572 Conveyor belt 620 Fluid region control device 650 Process Operating Equipment 672 Conveyor Belt 674 Robotic Arm 720 Fluid Zone Control 714 Grinding System 722 Sensor 724 Grinding 塾 Mounting 751 Grinding 塾 802 Copper Electrochemical Plating Reaction Chamber 810 Wafer Interface 812 Copper Seeding Deposition Reaction Chamber 816 Loading埠 822 Pre-cleaning reaction chamber 830 Single-wafer carrying chamber 832 Buffer chamber 840 Pre-cleaning reaction chamber 842 Buffer chamber 850 Process operating equipment 852 Tantalum/tantalum nitride deposition reaction chamber 860 Copper electrochemical plating chamber 870 Copper chemical mechanical grinding reaction chamber 872 Robot Arm 880 Covering Reaction Chamber 890 Copper Chemical Mechanical Grinding Reaction Chamber 914 System 40