TWI244134B - Device and method for removing metal in etchant, device and method for etching semiconductor substrate, and etchant for semiconductor substrate - Google Patents
Device and method for removing metal in etchant, device and method for etching semiconductor substrate, and etchant for semiconductor substrate Download PDFInfo
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【發明所屬之技術領域】 本么明係關於一種使得成為無機物並且不包含捕捉對 象之金屬之構件和餘刻液相接觸而捕捉蝕刻液中之金屬之 蝕刻液之金屬去除裝置,蝕刻液之金屬去除方法,半導體 基板之钱刻處理裝置,半導體基板之蝕刻方法及蝕刻液, 甚至關於一種減低金屬含有量之蝕刻液。 【先前技術】 使用在ic晶片等之半導體基板(晶圓)係經過複數個晶 圓製造製程、例如單結晶矽錠塊之切割製程、切割之晶圓 之研磨·蝕刻·拋光製程等而形成。 在這些晶圓製造製程中,習知之蝕刻處理係使用酸系 (hf/hno3系)之蝕刻液,進行於常溫狀況下之酸蝕刻。但 是’在該酸蝕刻,容易形成起因於蝕刻液之濃度之斑紋之 蝕刻斑紋,在平坦性之高品質化,有問題存在。隨著技術 之進步而一直要求晶圓之南平坦性’習知之酸餘刻係無法 配合於該要求。 為了配合於此種平坦性之要求,因此,現在係一直進 行使用鹼系蝕刻液之鹼蝕刻。在鹼蝕刻所使用之蝕刻液, 認為有KOH或NaOH或LiOH等,但是,即使是在其中,也使 用低成本之NaOH。 但是,藉由NaOH所造成之鹼蝕刻係大多進行在所謂60 。(:〜90。(:之高溫以及所謂30wt%〜60wt%之高濃度之狀況 下,由於此種狀況而在晶圓基體’引起金屬之擴散污染。[Technical field to which the invention belongs] The present invention relates to a metal removing device for an etching solution that captures metal in an etching solution by contacting a member that becomes an inorganic substance and does not contain a metal to be captured with the remaining liquid phase, and the metal of the etching solution Removal method, etching device for semiconductor substrate, etching method and etching solution for semiconductor substrate, and even an etching solution for reducing metal content. [Previous technology] Semiconductor substrates (wafers) used in IC wafers are formed through a plurality of wafer manufacturing processes, such as the cutting process of single crystal silicon ingots, and the grinding, etching, and polishing processes of cut wafers. In these wafer manufacturing processes, a conventional etching process uses an acidic (hf / hno3) etching solution, and performs acid etching at normal temperature. However, in this acid etching, there are problems in that the etching streaks due to the streaks due to the concentration of the etching solution are easily formed, and the flatness is improved. With the advancement of technology, the conventional acidity of the wafer, which has been required to be south flatness, cannot meet this requirement. In order to meet the requirements of such flatness, alkali etching using an alkali-based etching solution has been performed at present. As the etchant used for alkali etching, KOH, NaOH, LiOH, etc. are considered, but even among them, low-cost NaOH is used. However, the alkali etching system by NaOH is mostly performed at so-called 60 °. (: ~ 90.) In the condition of high temperature and so-called high concentration of 30% to 60% by weight, due to this condition, diffusion contamination of the metal is caused in the wafer substrate '.
7054-6516-PF(N3);Ahddub.ptd 第5頁 五、發明說明(2) 特別疋Cu或Ni係擴散係數變高,容易擴曰 擴散至晶圓内之金屬係由於後之曰阳圓基體内。 期之保管等而析出於晶圓表面,= 來造成不良影響。此外’鎳係顯著地惡二::羊’ (GOI(Gate Oxide Intogritw 鬥托备儿此 笔特 -^nQT7 . grity(閘極軋化物内摩擦))、使用 巧)或0SF 缺 fe(0xidati〇n_induced stacking (氧 化還原堆積缺陷))等。 作為金屬之污染源係有裝置内之蝕刻液接觸部、或蝕 刻之環境、或蝕刻液、或者是晶圓本身等,必須對於這些 之全部,來進行潔淨化。在以下,就蝕刻液之金屬污染或 蝕刻液之生成技術而進行說明。 圖7係顯示餘刻液中之金屬含有量和矽晶圓基體内之 金屬污染量間之關係之圖。在圖7,顯示關sNa〇H液中之 Cu和N i之結果。 圖7係顯不本發明人進行之實驗結果。在該實驗,作 為鹼蝕刻條件係成為: • Si晶圓處理時間·· 2〇〇sec •NaOH 濃度:48wt% • NaOH 溫度:85 t: ’故意對於超高純度Na〇H來進行金屬污染。此外,作為晶 圓基體之金屬評價係藉由加熱晶圓片侧,而在晶圓表面, 析出金屬。 由圖7而得知:蝕刻液中之離子化之金屬越多,晶圓 基體内之金屬污染量越多。由該結果而可以說是··為了減 7054-6516-PF(N3);Ahddub.ptd 第6頁 1244134 五、發明說明(3) 低晶圓基體内 金屬量。 此外,在 污染量係Cu/N Na〇H之鹼蝕刻 中之金屬含有 所謂使得驗钱 話,也可以說 一般作為 使用螯合劑或 在下列之專利 鎊鋼,還在餘 之技術。 【專利文 【發明内容】 【發明所欲解 但是,在 〉辰度(τ^ρΗ值) 金屬減低能力 由本發明人進 此外,在 或者是消耗電 適合作為使用 獻1 報 之金屬污染量,因此,必須減低钱刻液中之 進行同樣取出量之酸蝕刻後之晶圓基體内之 i = 1 0E9atoms(原子數)/cm2以下。為了藉由 而達成該酸蝕刻之程度,因此,要求Na〇H液 量’維持·管理在1 〇ppt程度。像這樣,由 刻之金屬污染量同等於酸蝕刻之觀點來看的 是必須減低钱刻液中之金屬。 以溶液中之金屬減低來成為目的之技術係有 螯合樹脂之技術、或者是電解法等。此外, 文獻1,記載:所謂在鹼系蝕刻液,浸潰不 刻液中,添加還原劑,在不銹鋼,附著金屬 曰本特開2 0 0 1 - 2 5 0 8 0 7號公 決的課題】 刻下,A就是在高溫且高驗 传顯著地降i而ί合劑或螯合樹脂之技術之 行之實驗而碟認。發揮功能。這個係藉 藉由電解法時,有所士田太 力變大之其他問題C氣體或Η2氣體 於鹼蝕刻之技術。 。因此’電解法係不7054-6516-PF (N3); Ahddub.ptd Page 5 V. Description of the invention (2) Especially the Cu or Ni-based diffusion coefficient becomes higher, and the metal system that diffuses into the wafer is easy to spread. Matrix. Expected storage, etc., comes out of the wafer surface, = to cause adverse effects. In addition, the nickel series is significantly worse than the second: Sheep '(GOI (Gate Oxide Intogritw)-^ nQT7. Grity (grid rolling friction)), or 0SF (feature 0xidati. n_induced stacking). The source of metal contamination is the etchant contact in the device, the etching environment, the etchant, or the wafer itself. All of these must be cleaned. Hereinafter, the metal contamination of the etchant or the technique for producing the etchant will be described. Fig. 7 is a graph showing the relationship between the metal content in the etching solution and the metal contamination amount in the silicon wafer substrate. Fig. 7 shows the results of Cu and Ni in the sNaOH solution. FIG. 7 shows the results of experiments performed by the inventors. In this experiment, the conditions for alkali etching were: • Si wafer processing time • 200 sec • NaOH concentration: 48 wt% • NaOH temperature: 85 t: ’Metal contamination was intentionally performed on ultra-high purity NaOH. In addition, in the evaluation of the metal as the wafer substrate, metal is deposited on the wafer surface by heating the wafer side. It is known from FIG. 7 that the more ionized metal in the etching solution, the more metal contamination in the wafer substrate. From this result, it can be said that ... In order to reduce 7054-6516-PF (N3); Ahddub.ptd page 6 1244134 V. Description of the invention (3) Low amount of metal in the wafer base. In addition, the metal contained in the alkaline etching of the pollution amount of Cu / N NaOH is the so-called technology that can be said to make money check. Generally, it is used as a chelating agent or the following patents. [Patent] [Inventive content] [How to solve the invention, but >> degree (τ ^ ρΗ value) metal reduction ability by the inventor In addition, the power consumption is suitable for use as a report of metal pollution, therefore, It is necessary to reduce i = 10E9atoms (atomic number) / cm2 or less in the wafer substrate after acid etching in the same amount of the etching solution. In order to achieve this degree of acid etching, it is required to maintain and manage the NaOH solution level 'to about 10 ppt. In this way, it is necessary to reduce the amount of metal in the etching solution from the viewpoint that the amount of metal contamination is equal to that of acid etching. Techniques aimed at reducing the amount of metals in a solution include a chelating resin technique or an electrolytic method. In addition, Document 1 describes that the so-called alkali-based etching solution, the impregnating non-etching solution, the addition of a reducing agent, and the adhesion of metal to stainless steel, Japanese Patent Publication No. 2 0 1-2 5 0 8 0] At the moment, A is recognized as an experiment in the technical trip of reducing the agent or chelating resin significantly at high temperature and high transmission. Function. This is a technique in which the C gas or Krypton 2 gas is etched by alkali in other problems when the electrolysis method is used. . Therefore, the electrolytic method does not
1244134 五、發明說明(4) 此外,在記 鐵或鎳之成分, 此’在藉由前述 液之金屬污染之 像這樣,先 屬污染。在通常 污染。也就是可 過而增加。因此 之金屬污染,因 於是,由於蝕刻 刻液之交換作業 問題。 本發明係有 刻液中之金屬而 於蝕刻液進行長 鑒於此種實狀 抑制钱刻處理 壽命化者係成 述專利 這些成 獻1時, 係無法 生產線 刻液之 確實地 須設定 換週期 所謂作 文獻1之不銹鋼,包含所謂 分係容易溶出於蝕刻液。因 ’還仍然發生所謂促進蝕刻 充分於減低鹼系蝕刻液之金 ,蝕刻液係逐漸地受到金屬 金屬污染量係隨著時間之經 防止由於蝕刻所造成之晶圓 餘刻液之壽命非常地短暫。 變短,因此,極度地增加蝕 業效率之惡化、成本上升之 而70成的,藉由減低鹼系蝕 之晶圓之金屬污染並且還對 為解決課題。 【用以解決課題的手段】 ^ 1發明係在去除混入至鹼系蝕蝕 之金屬去除裝置,其特徵在於 金屬之钱刻液 Π::捉對象之金屬之構件和二 if於前述構件的金屬捕 金屬之構# 吏用成為無機物並且不包含捕捉對象之 生屬之構件。在本說明書, Τ豕之 金屬捕捉裝置係使得金屬附^ f f吸附構件。 及附構件和蝕刻液相接觸。於 第8頁 7054-6516-PF(N3);Ahddub.ptd 1244134 五、發明說明(5) — = 附在金屬吸附構件。像這樣 液。 屬係捕捉於金屬吸附構件,生成潔淨之蝕刻 月1J述構件係包含 前述構件之形態 相對於钱刻液1 山第2發明,其特徵在於··在第丨發明 石炭。 少第3發明,其特徵在於··在第1發明 係纖維。 第4發明’其特徵在於:在第^明’相 么升而使得前述構件之表面積成為6〇cm2以上。 第2、第3、第4發明係能夠有效地 為金屬吸附構件之形態係有纖:或第二;月=: 較填充於相同容積之纖維和粒在比 丨大於粒子之表面積。在老纖維之表面積係比較 除處理之对產:具考之尺寸及钱刻液之金屬去 m 、夺,最好是使得金屬吸附構件成為纖維Θ 體地說,如果姓刻液別公升之金屬吸牛成為纖維。具 為60cm2以上的話,則具有金屬 、 表面積成 吸附構件料慮外’作為金屬 第5發明係在去除混入至鹼 之金屬去除方法,其特徵在於\糸括㈣二, 不包含捕捉對象之金屬之構件=丨=為無機物並且 中之金屬吸附;?姑柄於^液相接觸而將银刻液 t之金屬及附及捕捉於前述構件的金屬捕^ 前述金屬捕捉處理後之蝕刻液, ’ 乂及將 處理。 #釋成為既定濃度之稀釋 第5發明係將第1發明取代成為方法之發明,關於一種 第9頁 7054-6516-PF(N3);Ahddub.ptd 1244134 五、發明說明(6) ____ 更加有效地捕捉金屬之方法。金 刻液之濃度越高而越加吸附更多=構件係具有所謂餘 ::,利用該性質。在進行由蝕刻液去;質。在第5發 蝕刻液之蝕刻液生成處理時,使二^屬而生成潔淨之 J構件相接觸’將高濃度蝕刻:::::液和金屬吸 屬吸附構件。然後,稀釋高濃度=二之金屬,吸附於金 蝕刻液。 刻液而生成既定濃度之 發明係在使用驗系韻刻液而钱刻 導體基板之蝕刻處理裝置,苴 導體基板之+ 之餘刻液槽’·使得成為無機物並儲存姓刻液 前述構件之金屬捕捉 f中之金屬吸附及捕捉於 1及第2連通路以二通及 ==捕捉部之第 金屬捕捉部間來循環㈣液之幫第#連通路而在㈣液槽和 浸潰ίΓ。發在明二㈣,槽,儲存㈣液,在其當中, 第2連通路和幫、η儲存槽和金屬捕捉部間’設置第1、 捉部間,s流著蝕刻液啟動像幫二時二在蝕刻液槽*金屬捕 生成♦渗之舳^ 像廷樣進行由蝕刻液去除金屬而 第7發明之蝕刻液生成處理及晶圓之蝕刻處理。 導體基板Χ之ιΛ丨^系㈣液而㈣半導體基板之半 之第广姑刻液/广理曰裝置’其特徵在於包括:儲存姓刻液 金屬之構件和^刻使/^成接為無機物並且不包含捕捉對象之 捉於前述構件之金屬而:蝕刻液中之金屬吸附及捕 屬捕捉邛,連通第〗蝕刻液槽和金屬捕 ! 7054-6516-PF(N3);Ahddub.ptd 第10頁 1244134 五、發明說明(7) 捉部之第1及第2連通路;透過第丨及第2連通路而 刻液槽和金屬捕捉部間來循環蝕刻寶 、在弟1钱 第1蝕刻液槽之不同之第2蝕刻液槽及之寬/南,从及不同於 在第1蝕刻液槽,儲存蝕刻液。在第丨蝕刻 捕捉部間,設置第卜第2連通路和幫浦。在啟動屬 在第1蝕刻液槽和金屬捕捉部間,環流著蝕刻&象、」 由#刻液去除金屬而生成潔淨之餘刻液之蝕刻像^生樣成 蝕刻液係由第1蝕刻液槽開始移送至第2蝕刻液 第2姓刻液槽’儲存钱刻液’在其當中,浸潰晶圓。㈢ 樣’進行晶圓之韻刻處理。 。 第8發明係在使用鹼系蝕刻液而蝕刻半導體基板之 導體ΐϋ製造方法’其特徵在於:在使得成為無機物並 且不包3捕捉對象之金屬之構件和钱刻液相接觸而將蝕刻 液中之金屬吸附及捕捉於前述構件後,在蝕刻液, 導體基板,進行蝕刻。 X S t 在第8發月使用成為無機物並且不包含捕捉對象之 金屬之金屬吸附構件。在使得金屬吸附構件和蝕刻液相接 觸時,包含於蝕刻液之金屬係吸附在金屬吸附構件。像這 樣蝕刻液中之金屬係捕捉於金屬吸附構件,生成潔淨之蝕 刻液。在該蝕刻液,浸潰晶圓而進行蝕刻。 、第9發明係在蝕刻半導體基板時之所使用之鹼系之蝕 刻液’其特徵在於:接觸到成為無機物並且不包含捕捉對 象之金屬之構件而減低金屬含有量。1244134 V. Explanation of the invention (4) In addition, in the composition of iron or nickel, this ’is a kind of contamination by metal contamination with the aforementioned liquid. In general pollution. That is, it can be increased. Therefore, the metal is contaminated, and therefore, there is a problem in exchange operation of the etching etchant. In the present invention, the metal in the etching solution is long and the etching solution is long. In view of such a solid state, the life of the etching process is suppressed. When the patents mentioned above are presented, it is impossible to produce a line of etching solution. The stainless steel of Document 1 contains a so-called branch which is easily dissolved in an etching solution. Because of the fact that the so-called promoting etching is sufficient to reduce the gold of the alkali-based etching solution, the etching solution is gradually contaminated with metal. The amount of time that is used to prevent the etching solution caused by the etching of the wafer is very short. . It is shortened. Therefore, 70% of the deterioration of the etching efficiency is extremely increased, and the cost is increased. By reducing the metal pollution of the alkali-etched wafers, it is also a solution to the problem. [Means to solve the problem] ^ 1 The invention is a device for removing metal mixed with alkali corrosion, and is characterized by a metal engraving solution Π :: a metal member for catching an object, and a metal if the above-mentioned member捕 金属 的 之 # Officials are used as inorganic materials and do not contain the natural genus members of the capture target. In this specification, the metal capture device of TT is a metal attachment device. And the attached components are in contact with the etching liquid. 7054-6516-PF (N3); Ahddub.ptd 1244134 on page 8. V. Description of the invention (5) — = Attached to the metal adsorption member. Like this liquid. The genus is captured on the metal-adsorbed member to produce a clean etch. The component system described above includes the form of the aforementioned member. The second invention is related to the engraved liquid 1 and is characterized by the invention of charcoal. The third invention is characterized in that the first invention is a fiber. The fourth invention 'is characterized in that the surface area of the member is 60 cm2 or more when it is raised at the same time. The 2nd, 3rd, and 4th inventions are capable of effectively forming a metal adsorption member. The form of the fiber is: fiber; or second; month =: the ratio of the fiber and particles filled in the same volume is larger than the surface area of the particles. The surface area of the old fiber is compared to the treatment of the product: metal with a size and money to remove the m, and it is best to make the metal adsorption member into the fiber. Sucking becomes fiber. If it is 60 cm2 or more, the metal and the surface area are considered as adsorption members. As a metal, the fifth invention is a method for removing metal mixed with alkali, which is characterized in that it does not include the metal to be captured. The component = 丨 = is an inorganic substance and the metal is absorbed; The metal in the silver engraving liquid t and the metal attached to the aforementioned member are captured in contact with the liquid phase, and the etching solution after the aforementioned metal capturing treatment is processed. #Release becomes a dilution of a given concentration. The fifth invention is an invention that replaced the first invention as a method. About a page 97054-6516-PF (N3); Ahddub.ptd 1244134 V. Description of the invention (6) ____ is more effective Ways to capture metal. The higher the concentration of the gold engraving solution, the more it absorbs more = the component system has a so-called residual ::. This property is used. Going by etching solution; quality. In the etching solution generation process of the fifth etching solution, the two members are brought into contact with each other to produce a clean J member, and the high-concentration etching is performed. The liquid and metal are adsorbed on the adsorption member. Then, the metal with a high concentration of two is diluted and adsorbed to the gold etchant. The invention of the etching solution to generate a predetermined concentration is an etching treatment device for etching a conductor substrate using a rhyme etching solution. The conductor substrate + + is engraved with a liquid tank. It is made into an inorganic substance and stores the metal of the aforementioned components of the etching solution. The metal in the capture f is adsorbed and captured between the 1st and 2nd communication paths through the second connection and the metal capture part of the == capture part to circulate the liquid ## communication path to the liquid tank and immerse Γ. It is placed in the Mingji Temple, and the tank is used to store the solution. Among them, the second communication path and the gang, the η storage tank and the metal capture section are set between the first and the capture section. Second, in the etching solution tank * metal capture generation ♦ infiltration ^ etch processing of the seventh invention of the etching solution generation process and the wafer etching process to remove metal from the etching solution in the same manner as in the case. The conductor substrate X is a liquid electrolyte and the semiconductor substrate is a half of the semiconductor substrate. The device is characterized in that it includes: a member storing a metal substrate and a metal substrate and an inorganic substrate. And does not include the metal captured in the aforementioned components and the object of capture: metal adsorption in the etching solution and capture is a capture trap, which connects the etching bath and metal capture! 7054-6516-PF (N3); Ahddub.ptd Section 10 Page 1244134 V. Description of the invention (7) The first and second communication paths of the catching department; through the first and second communication paths, the etching bath is etched between the liquid tank and the metal capture section to circulate the etching treasure, and the first etching solution in the first coin. The difference between the second etching bath and the width / south of the bath is different from that in the first etching bath, and the etchant is stored. A second communication path and a pump are provided between the first etching capturing part. Between the first etching solution tank and the metal capturing part, the etching & image, circulated between the first etching solution tank and the metal capturing part, and the metal was removed from the #etching solution to produce a clean etching solution. The etching solution was created by the first etching. The liquid bath starts to be transferred to the second etching liquid, and the second liquid engraving liquid tank 'storage money' is immersed in it, soaking the wafer. ㈢ 样 'performs the wafer engraving process. . The eighth invention is a manufacturing method of a conductor 蚀刻 for etching a semiconductor substrate using an alkali-based etchant. After the metal is adsorbed and captured on the member, the conductive substrate is etched in an etchant. X S t uses a metal adsorption member which becomes an inorganic substance and does not contain a metal to be captured in the eighth month. When the metal adsorption member is brought into contact with the etching liquid phase, the metal system contained in the etching solution is adsorbed on the metal adsorption member. The metal in the etching solution is captured on the metal adsorption member, and a clean etching solution is generated. In this etchant, the wafer is immersed and etched. 9. The ninth invention is an alkali-based etching solution used when etching a semiconductor substrate, and is characterized in that the metal content is reduced by coming into contact with a member that becomes an inorganic substance and does not include a metal that captures an object.
1244134 五、發明說明(8) 在含有金屬之鹼系蝕刻液和 捉對象之金屬之構件相接觸 ;無機物並且不包含捕 金屬吸附構件。結果, 斜钱刻液中之金屬係捕捉於 減低蝕刻液中之金屬含有量。 【發明效果】 如果藉由本發明的話, 液中之金屬。像這樣減低蝕刻^ 構件,吸附蝕刻 刻處理之晶圓之金屬污夹。 乏金屬,因此,抑制蝕 之晶圓。 ,、 ^ 可以提供減低金屬污染 此外,蝕刻液係保持在潔淨之能 蝕刻液之壽命。 狀心’因此,可以延長 實施方式】 明 以下,就本發明之實施 。 施形態而參照圖式,來進行說 使用在本發明之金屬 於蝕刻液而且不包含捕彳务牛係成為無機物並且包含 質。具體地說,作屬、例如钢或錄等之物 c(碳)等。在此種金屬件/有5 W碳化物)或 液令之離子化之金屬係析/於件;^刻面液相接觸時,姓刻 二件之表面。此外,金屬吸附構件係不包含 屬,因此,在蝕刻液中,並盔溶 捉對象之金 來作為金屬吸附構件开之:施^〜3係顯示使用w 再于《某-形態’在後面敘述之實施例1244134 V. Description of the invention (8) The alkali-based etching solution containing metal is in contact with the metal-caught member; the inorganic substance does not include the metal-captured adsorption member. As a result, the metal in the oblique coin engraving solution is captured to reduce the metal content in the etching solution. [Effects of the Invention] According to the present invention, the metal in the liquid. In this way, the etched member is reduced, and the metal contamination clips of the etched wafer are adsorbed. Depleted metal, therefore, suppresses etched wafers. ,, ^ can provide to reduce metal pollution. In addition, the etchant is kept clean and the life of the etchant. Centroid 'Therefore, the embodiment can be extended] The following is the implementation of the present invention. The embodiment is described with reference to the drawings, and the metal used in the present invention is used in the etching solution and does not include the catching cattle. It becomes an inorganic substance and contains a substance. Specifically, the material is, for example, steel (c) or the like. In the case of such metal parts / metals with 5 W carbide) or liquid ionized metal parts; when the faceted liquid phase contacts, the surname is carved on the surface of the two parts. In addition, the metal adsorption member system does not include a genus. Therefore, in the etching solution, the target gold is used to dissolve the object as a metal adsorption member. The application of ^ ~ 3 series shows the use of w, and it will be described later in "a certain form". Example
Ml 第12頁 7054-6516-PF(N3);Ahddub.ptd Ι24Φ134 五、發明說明(9) 4、5,顯示使用C來作為金屬吸附構件之某一形能。 【實施例1】 一圖1(a)係第1貫施形態之方塊圖,圖Kb)係SiC過濾器 之示意圖。 在蝕刻液槽1,儲存鹼系蝕刻液。在本實施形態,作 1鹼系姓刻液係使用Na0H液。Na0H液係濃度(質量%)成為 40%〜60%之鹼水溶液。此外,為了有效率地進行由於金屬 吸附構件所造成之金屬捕捉,因此,Na〇H液係最好是7〇t =90 C。,蝕刻液槽1 ,連接在途中設置幫浦2之管路〗丨之 某一端。管路11之其他端係連接在供應切換部3。此外, 在钱刻液槽1,連接管路12之茸一被 ^ ^ 1 〇 ^ &俗丄Z之杲鈿。官路12之其他端係 連接在排出切換部5。在管路11或管路12之途中,設置並 未圖示之聯機加熱器。 u 在供應切換部3,連接Na0H液之供應系統、也就是 路11和HF液之供應系統、也就是管路21。此外,還連接 SiC過濾器4之流體供應側。供應切換部3係藉由切換 而控制供應至SiC過濾器4之流體(Na0H液、叮液)。切換 作係可以配合於來自並未圖示之控制器之切換訊號而進’、 灯,也可以藉由手動而進行。此外,也可以僅是間。 在SiC過濾器4之上游側,連接供應切換部3, 側,連接排出切換部5。SiC過濾器4係正如圖丨(b)所嘀/ 示,大致由柱體41和填充於該柱體41内之Si(:粒子= 成。在本實施形態,使用Sic粒子42者係由於可以 子狀之SiC而使得SiC和NaOH液間之接觸面積變大,曰能夠% 第13頁 7054-6516-PF(N3);Ahddub.ptd 1244134Ml Page 12 7054-6516-PF (N3); Ahddub.ptd Ι24Φ134 V. Description of the invention (9) 4, 5 shows the use of C as a certain energy of the metal adsorption member. [Embodiment 1] Fig. 1 (a) is a block diagram of the first embodiment, and Fig. Kb) is a schematic diagram of a SiC filter. In the etching solution tank 1, an alkali-based etching solution is stored. In this embodiment, NaOH solution is used as the alkali-based surname solution. The NaOH solution concentration (% by mass) is 40% to 60% of an alkaline aqueous solution. In order to efficiently perform metal capture by the metal adsorption member, the NaOH solution is preferably 70t = 90C. , The etching liquid tank 1 is connected to one end of the pipeline 2 of the pump 2 set in the middle. The other end of the pipeline 11 is connected to the supply switching section 3. In addition, in the engraved liquid tank 1, the connecting tube 12 is covered with a blanket ^ ^ 1 〇 ^ &; Z 丄. The other end of the official road 12 is connected to the discharge switching section 5. An on-line heater (not shown) is installed in the middle of the pipeline 11 or the pipeline 12. u In the supply switching section 3, the Na0H liquid supply system, that is, the circuit 11 and the HF liquid supply system, that is, the pipeline 21 is connected. The fluid supply side of the SiC filter 4 is also connected. The supply switching unit 3 controls the fluid (Na0H solution, sting solution) supplied to the SiC filter 4 by switching. The switching operation can be performed in accordance with a switching signal from a controller (not shown), and the lamp can also be performed manually. In addition, it may be only time. On the upstream side of the SiC filter 4, the supply switching section 3 is connected, and on the side, the discharge switching section 5 is connected. The SiC filter 4 is shown in FIG. 丨 (b), and is roughly composed of a pillar 41 and Si (: particles) filled in the pillar 41. In this embodiment, the use of Sic particles 42 is possible because Sub-shaped SiC makes the contact area between SiC and NaOH liquid larger, which means that it can be%. Page 13 7054-6651-PF (N3); Ahddub.ptd 1244134
五、發明說明(10) 大SiC過濾器4之金屬捕捉力之緣故。認為為了像這樣增大 和NaOH間之接觸面積並且成為小型之過濾器,因此,使得 SiC之形態成為粒子,但是,也可以使得Sic成為其他形于 態。如果每1公升Na0H液之siC表面積成為6〇cm2程/度的話, 則具有金屬除去之效果。V. Description of the invention (10) The reason for the metal trapping force of the large SiC filter 4. It is thought that in order to increase the contact area with NaOH and to become a small filter, the shape of SiC is made into particles, but Sic can also be made into other shapes. If the siC surface area per 1 liter of Na0H solution becomes 60 cm 2 range / degree, it has the effect of removing metals.
在排出切換部5,連接Na〇H液之排出系統、也就是管 路12和HF液之排出系統、也就是管路22。此外,還連接 S1C過濾器4之流體排出側。排出切換部3係藉由切換操作 而控制由SiC過濾器4所排出之流體(Na〇II液、HF液)之排出 方向。切換操作係可以配合於來自並未圖示之控制器之切 換訊號而進行,也可以藉由手動而進行。此外,也可以 是閥。 HF液供應部6係為了沖洗設置在Sic過濾器4之3^粒 子,因此,將HF液供應至SiC過濾器4。供應耵液之時間係 任意,,是,必須是不供應心〇{1液至Sic過濾器4之時間。 接著’說明圖1所示之裝置之動作。 在蝕刻液槽1,充滿Na0H液,在藉由並未圖示之聯機 加熱器而升溫NaOH液至70 °c〜9(rc程度後,在Na0H液中, 浸潰晶圓。於是,進行晶圓之蝕刻。The discharge switching section 5 is connected to the discharge system of NaOH solution, that is, the pipe 12 and the discharge system of HF solution, that is, the pipe 22. In addition, the fluid discharge side of the S1C filter 4 is connected. The discharge switching unit 3 controls the discharge direction of the fluid (NaOII liquid, HF liquid) discharged from the SiC filter 4 by a switching operation. The switching operation can be performed in conjunction with a switching signal from a controller (not shown) or manually. It can also be a valve. The HF liquid supply unit 6 supplies the HF liquid to the SiC filter 4 in order to wash the 3 ^ particles provided in the Sic filter 4. The time for supplying mash is arbitrary, but it must be the time when no liquid is supplied to the Sic filter 4. Next, the operation of the device shown in Fig. 1 will be described. The etching bath 1 is filled with Na0H solution, and the NaOH solution is heated to 70 ° C to 9 ° C (about rc) by an on-line heater (not shown), and the wafer is immersed in the Na0H solution. Etching of the circle.
咏在生成潔淨之Na0H液之狀態下,供應切換部3係連通 1路11和S i C過濾器4,排出切換部5係連通§丨◦過濾器4和 在啟動幫浦2時,NaOH液係由蝕刻液槽!開始,透過管 路11和供應切換部3而供應至Sic過滤器4。供應至sic過滤In the state of generating clean Na0H solution, the supply switching unit 3 is connected to the first channel 11 and the Si C filter 4 and the discharge switching unit 5 is connected to the § 丨 ◦ filter 4 and the NaOH solution when starting pump 2. By the etching bath! Initially, it is supplied to the Sic filter 4 through the pipe 11 and the supply switching section 3. Supply to sic filtering
1244134 ί、發明說明(11) 一 " " 斋4之NaOH液係接觸到填充於柱體41内之SiC粒子42,同 時’流動至下游側,透過排出切換部5及管路丨2而排出至 姓刻液槽1。也就是說,Na0H液係環流於蝕刻液槽1和SiC 過濾器4間。在包含金屬iNa〇H液通液至Sic過濾器4時, NaOH液中之金屬係吸附於Sic粒子。因此,在Na〇H液通液 至SiC過渡器4時,減低含有在Na〇H液中之金屬量。結果, 生成潔淨之鍅刻液。 進行像這樣由蝕刻液來去除金屬而生成潔淨之蝕刻液 之钱刻液生成處理。此外,在生成之蝕刻液,浸潰晶圓而 進行姓刻處理。蝕刻液生成處理係可以一直進行蝕刻處 理,並且,也可以進行在蝕刻處理以外時。 但是,在吸附於SiC粒子42之金屬量,有限度存在。 充为地吸附金屬之S i C粒子4 2係降低金屬捕捉力。因此, 必須定期地進行S i C過濾器4之交換作業或者是接著說明之 S i C過濾器4之沖洗作業。 在沖洗S i C過滤器4之狀態下,供應切換部3係連通管 路21和S i C過濾器4,排出切換部5係連通S i C過濾器4和管 路22。 一 藉由HF液供應部6而使得HF液,透過管路21及供應切 換部3 ’來供應至SiC過渡器4。供應至SiC過濾器4之HF液 係接觸到填充於柱體41内之Si C粒子42,同時,流動至下 游側’透過排出切換部5及管路2 2而排出外部。在jjF液通 液至S i C過濾器4時’吸附於S i C粒子4 2之金屬係溶解於η f 液。因此,SiC粒子42係成為潔淨狀態,復活金屬捕捉1244134, Invention Description (11)-"The NaOH solution of Zhai 4 is in contact with the SiC particles 42 filled in the column 41, and at the same time 'flows to the downstream side through the discharge switching section 5 and the pipeline 丨 2 and Discharge to surname carved liquid tank 1. That is, the Na0H liquid system circulates between the etching liquid tank 1 and the SiC filter 4. When the metal iNaOH solution is passed through the Sic filter 4, the metal in the NaOH solution is adsorbed on the Sic particles. Therefore, when the NaOH solution is passed through the liquid to the SiC transition device 4, the amount of metal contained in the NaOH solution is reduced. As a result, a clean etching solution is generated. An etching solution generation process is performed in which a metal is removed by an etching solution to produce a clean etching solution. In addition, the resulting etching solution is immersed in the wafer and subjected to a lasting treatment. The etching solution generation processing system may perform the etching processing all the time, and may also perform the processing other than the etching processing. However, the amount of metal adsorbed on the SiC particles 42 is limited. The S i C particles 42 that adsorb the metal sufficiently reduce the metal trapping force. Therefore, the replacement operation of the Si C filter 4 or the rinse operation of the Si C filter 4 described below must be performed regularly. In the state where the Si C filter 4 is flushed, the supply switching section 3 is connected to the pipe 21 and the Si C filter 4, and the discharge switching section 5 is connected to the Si c filter 4 and the pipe 22. First, the HF liquid is supplied to the SiC transitioner 4 through the pipe 21 and the supply switching section 3 'by the HF liquid supply section 6. The HF liquid supplied to the SiC filter 4 comes into contact with the Si C particles 42 filled in the column 41, and at the same time flows to the downstream side 'and is discharged through the discharge switching section 5 and the pipe 22 to the outside. When the jjF liquid is passed through the Si C filter 4, the metal system adsorbed to the Si C particles 4 2 is dissolved in the η f liquid. Therefore, the SiC particles 42 are in a clean state, and the metal capture is revived.
7054-6516-PF(N3) ;Ahddub.ptd 第15頁 12441347054-6516-PF (N3); Ahddub.ptd p. 15 1244134
力0 認為金屬離子對於Sic之吸附機構係 解電鍍之作用。也就是說,認為Si 揮不同於士…電 正如前面敘述,钱刻液中之離子化之 及附於固液界面、也就是SiC構件之表面。 圖2〜圖4係顯示本發明人使用本實 驗結果。 个貝施形恶而進仃之貫 圖2係顯示蝕刻液對於SiC過濾器之通液時間和粒 y &之^π吸附戛間之關係之圖。在圖2,顯示關於NaOH 液中之銅和鎳之結果。 以 在該實驗’使得對於Sic過濾器4之通液條件,正如 下0 •在钱刻液槽1浸潰P — Si晶圓(i〇〇g) •NaOH 濃度:48wt%Force 0 considers that the metal ions have an effect on desorbing the Sic adsorption mechanism. In other words, it is considered that Si is different from electricity ... As mentioned earlier, the ionization in the engraved liquid and its attachment to the solid-liquid interface, that is, the surface of the SiC member. Fig. 2 to Fig. 4 show the results of the experiment by the inventors. Figure 2 is a graph showing the relationship between the flow time of the etching solution to the SiC filter and the adsorption of particles y & π. Figure 2 shows the results for copper and nickel in NaOH solution. In this experiment ’, the liquid-passing conditions for the Sic filter 4 are as follows: • P-Si wafer (IOOg) is impregnated in the coin-cut liquid tank 1 • NaOH concentration: 48wt%
• NaOH 溫度:85 °C •SiC粒子之全表面積:250 0cm2 此外’作為S i C表面之金屬評價係使得吸附於s丨c之金 屬’溶解於HF液,進行蒸發乾固,在藉由酸液而進行稀釋 後’藉由icp質量分析法(ICPMS)而進行測定。 圖3係顯示蝕刻液對於s丨c過濾器之通液時間和蝕刻液 中之金屬濃度間之關係之圖。在圖3,顯示關KNa〇H液中 之銅和鎳之結果。 在該實驗’使得對於s i C過濾器4之通液條件,正如以 下0• NaOH temperature: 85 ° C • Total surface area of SiC particles: 250 0cm2 In addition, as the metal evaluation surface of Si C surface, the metal adsorbed on s 丨 c was dissolved in HF liquid, and evaporated to dryness. After diluting the solution, the measurement was performed by icp mass spectrometry (ICPMS). Fig. 3 is a graph showing the relationship between the flow time of the etching solution to the s? C filter and the metal concentration in the etching solution. In Fig. 3, the results of copper and nickel in KNaOH solution are shown. In this experiment ’, the conditions for the liquid flow of the si C filter 4 are as follows:
7054-6516-PF(N3);Ahddub.ptd 第16頁 1244134 五、發明說明(13) •在#刻液槽1浸潰P — Si晶圓(100g) •NaOH?農度:48wt% •^011溫度:85。〇 •SiC粒子之全表面積:250 0cm2 外 此外’故意對於超高純度Na0H液進行金屬污染。此 作為晶圓基體之金屬評價係藉由加熱晶圓單侧,而在 晶圓表面,析出金屬。 圖4係顯示蝕刻液對於s丨c過濾器之通液時間和晶圓基 體之金屬濃度間之關係之圖。在圖4,顯示關於NaOH液中 之鋼和鎳之結果。 在該實驗,使得鹼蝕刻條件,正如以下。 • Si晶圓處理時間·· 2〇〇sec • NaOH 濃度:48wt%7054-6516-PF (N3); Ahddub.ptd Page 16 1244134 V. Description of the invention (13) • P-Si wafer (100g) immersed in # 刻 液槽 1 • NaOH? Agronomy: 48wt% • ^ 011 temperature: 85. 〇 • The total surface area of SiC particles: outside 250 0cm2 In addition, the metal contamination of the ultra-high-purity Na0H solution is intentional. The metal evaluation as a wafer substrate is to deposit metal on the wafer surface by heating one side of the wafer. Fig. 4 is a graph showing the relationship between the flow time of the etchant to the s? C filter and the metal concentration of the wafer substrate. In Figure 4, the results are shown for steel and nickel in NaOH solution. In this experiment, the alkali etching conditions were made as follows. • Si wafer processing time ... 200sec • NaOH concentration: 48wt%
• NaOH 溫度:85 °C 此外,作為NaOH中之金屬評價係藉由ICP質量分析法 (ICPMS)而測定吸附於螯合樹脂之金屬。 長 知 内 此 長 示 正如圖2所示,NaOH液對於SiC過濾器4之通液時間越 貝|JSiC粒子4上之金屬濃度變得越高。由該結果而得 在NaOH液環流於蝕刻液槽1和SiC過濾器4間之時間 NaOH液中之金屬係逐漸地吸附及捕捉SiC粒子42。因 得到圖3、圖4所示之結果。 正如圖3所示,NaOH液對於SiC過濾器4之通液時間越 則NaOH液中之金屬濃度變得越低。此外,正如圖4所 NaOH液對於SiC過濾器4之通液時間越長,則晶圓基體• NaOH temperature: 85 ° C In addition, the evaluation of the metal in NaOH is to measure the metal adsorbed on the chelate resin by ICP mass spectrometry (ICPMS). As shown in Fig. 2, the longer the liquid passing time of the NaOH solution to the SiC filter 4 becomes, the higher the metal concentration on the JSiC particles 4 becomes. From this result, the time during which the NaOH liquid circulates between the etching liquid tank 1 and the SiC filter 4 is obtained. The metal system in the NaOH liquid gradually adsorbs and captures the SiC particles 42. The results shown in Figs. 3 and 4 were obtained. As shown in FIG. 3, the more the liquid passing time of the NaOH solution to the SiC filter 4, the lower the metal concentration in the NaOH solution becomes. In addition, as shown in Fig. 4, the longer the liquid passing time of the NaOH solution to the SiC filter 4, the longer the wafer substrate.
7054-6516-PF(N3);Ahddub.ptd 第17頁 1244134 五、發明說明(14) 之金屬濃度變得越低 如果藉由第1實施形態的話,則在Sic構件,吸附蝕 液中之金屬。像這樣減低蝕刻液中之金屬,因此,抑 = 刻處理之晶圓之金屬污染。因此,可以提供減低金今j 之晶圓。 乐 因此,能夠延長 此外,蝕刻液係保持在潔淨之狀態 餘刻液之壽命。 此外,如果藉由第1實施形態的話,則洗淨s i C過濾 器,因此,比起不洗淨s i c過濾器者,還更加可以延長Ί 刻液之壽命。 此外,S i C係對於任何一種驗、酸也具有耐性,因 此,能夠進行前述之鹼系蝕刻液之生成及藉由HF液所造成 之沖洗。 此外,蝕刻液生成裝置和蝕刻處理係成為一個裝置而 進行,因此,系統係成為小型化。 【實施例2】 圖5係第2實施形態之方塊圖。 本實施形態不同於第1實施形態者係潔淨之Na〇H液之 生成和S i C過濾器4之沖洗藉由個別之裝置而進行之方面。 因此,SiC過濾器4係對於Na0H液之循環線及HF液之供應· 排出線’成為可自由裝卸。如果藉由此種裝置的話,則潔 淨之NaOH液之生成係藉由蝕刻液槽1、管路丨丨、Sic過濾器 4和管路1 2之製造線而進行,s i c過渡器4之沖洗係藉由設 置於外部之HF供應部6、管路21,、SiC過濾器4和管路22,7054-6516-PF (N3); Ahddub.ptd Page 17 1244134 V. Description of the invention (14) The lower the metal concentration becomes, if the first embodiment is adopted, the Sic member will adsorb the metal in the etching solution . The metal in the etchant is reduced like this, so the metal contamination of the wafer processed by etching is suppressed. Therefore, it is possible to provide wafers with reduced gold and j. Therefore, it is possible to extend the life of the etching solution while keeping the etching solution clean. In addition, according to the first embodiment, since the si c filter is washed, the life of the etching solution can be prolonged more than that without washing the si c filter. In addition, S i C is resistant to any kind of acid and acid. Therefore, it is possible to perform the aforementioned alkali-based etching solution generation and flushing by HF solution. In addition, since the etching solution generation apparatus and the etching process are performed as a single apparatus, the system is miniaturized. [Embodiment 2] Fig. 5 is a block diagram of a second embodiment. This embodiment is different from the first embodiment in that the generation of clean NaOH solution and the flushing of the Si C filter 4 are performed by separate devices. Therefore, the SiC filter 4 is freely attachable and detachable to and from the circulation line of NaOH solution and the supply and discharge line of HF solution. If such a device is used, the production of clean NaOH solution is performed by the manufacturing line of etching liquid tank 1, pipeline 丨 丨, Sic filter 4 and pipeline 12, and the flushing system of sic transition device 4. With the external HF supply section 6, pipeline 21, SiC filter 4, and pipeline 22,
7054-6516-PF(N3);Ahddub.ptd 第18頁 1244134 五、發明說明(15) 之製造線而進行。 相同於第1貫施形態,#刻液生成處理係可以一直進 行钱刻處理,並且,也可以進行在银刻處理以外時。 如果藉由第2實施形態的話,則得到相同於第1實施形 態之同樣效果。此外,NaOH液之循環線係變得簡單。 【實施例3】 圖6係第3實施形態之方塊圖。7054-6516-PF (N3); Ahddub.ptd Page 18 1244134 V. Production line of invention description (15). Similar to the first embodiment, the #etching liquid generation processing system can always perform the money engraving process, and can also perform the process other than the silver engraving process. According to the second embodiment, the same effect as that of the first embodiment can be obtained. In addition, the circulation line of the NaOH solution becomes simple. [Embodiment 3] Fig. 6 is a block diagram of a third embodiment.
本實施形態係在蝕刻液槽1,儲存Na〇H液,在該Na〇H 液,浸潰SiC過濾器4。NaOH液中之金屬係吸附於Sic過濾、 器4之SiC粒子,因此,減低Na〇H液之金屬濃度。此外,正 如第2實施形態,可以藉由不同個體設置之裝置而進行s i c 過濾器4之沖洗。 相同於第1實施形態,蝕刻液生成處理係可以一直進 行蝕刻處理,並且,也可以進行在蝕刻處理以外時。 如果藉由第3實施形態的話,則抑制蝕刻處理之晶 之金屬污染。此外,裝置整體係變得非常簡單。 【實施例4】 為金屬吸附構件之C而比較於Sic,來進行說^,關於作 圖8係顯示本發明人進行之實驗於果。 圖8係顯示蝕刻液之通液時間和 間之關係之圖。在圖8,顯示在填充加粒子之金屬及附里 液NaOH液之結果,同時,顯示 慮态來通 丹兄C粒子之過濾器來通 第19頁 7054-6516-PF(N3);Ahddub.ptd 1244134 五、發明說明(16) 液NaOH液之結果,此外,顯示關於Na〇H液中之銅和鎳之結 果。 在該實驗,使得對於S i C過濾器、C過濾器之通液條 件,正如以下。 •在蝕刻液槽1浸潰P - Si晶圓(l〇〇g) • NaOH 濃度:48wt%In this embodiment, a NaOH solution is stored in the etching solution tank 1, and the SiC filter 4 is immersed in the NaOH solution. Since the metal in the NaOH solution is adsorbed on the SiC particles in the Sic filter and the device 4, the metal concentration of the NaOH solution is reduced. In addition, as in the second embodiment, the si c filter 4 can be rinsed by a device provided for each individual. Similarly to the first embodiment, the etching solution generation treatment system may be continuously subjected to the etching treatment, or may be performed in addition to the etching treatment. According to the third embodiment, metal contamination of the etched crystal is suppressed. In addition, the entire system becomes very simple. [Example 4] The comparison is made with Sic for C of a metal adsorption member. The drawing 8 shows the results of experiments performed by the present inventors. Fig. 8 is a graph showing the relationship between the flow time and time of the etchant. In Fig. 8, the results of filling the metal with particles and the NaOH solution of the lye are shown. At the same time, the filter of the C particles is shown to pass through the filter. Page 197054-6516-PF (N3); Ahddub. ptd 1244134 V. Description of the invention (16) The results of NaOH solution, and the results of copper and nickel in NaOH solution are shown. In this experiment, the liquid passing conditions of the Si C filter and the C filter were as follows. • Immersion of P-Si wafer (100g) in etching bath 1 • NaOH concentration: 48wt%
• NaOH 溫度:85 °C •粒子之全表面積:25 0 0cm2 此外,作為S i C表面及C表面之金屬評價係使得吸附於 SiC及C之金屬,溶解於HF液,進行蒸發乾固,在藉由酸液 而進行稀釋後,藉由ICP質量分析法(ICPMS)而進行測定。 正如在圖8所示,銅和鎳相對於SiC之吸附量以及銅和 鎳相對於C之吸附量係幾乎相同。由該結果而可以說:關 於金屬捕捉力而言,Sic和C係相同。 C係比較於Sic而在下列方面,變得良好。c係可以 到各種形態,因此,也可以成為粒子&,但是,最好 為纖維狀。在比較填充於a _容積之纖維和 ;表2係比較大於粒子之表面積。也就是說,在填;: Ν 和粒子而通液Na〇H液之狀態下’纖維和 稽:面積係比較大於粒子和_液間之接觸面 :纖=過壚器係比起填充粒子之過遽器還更加::填 【實::5】一般C係比較便宜於SiC,因此,減低成本 第20頁 7054-6516-PF(N3);Ahddub.ptd 1244134 五、發明說明(17) 正如在圖9所示,金屬吸附構件係具有所謂蝕刻液之 濃度越高而吸附更加多之金屬之性質。在此,就利用該性 為而有效率地進行蝕刻液生成處理之實施形態,來進行說 明。 圖9係顯示本發明人進行之實驗結果。 圖9係顯示蝕刻液之濃度和c粒子上之金屬吸附量間之 關係之圖。在圖9,顯示關於Na〇H液中之銅和鎳之結果。 在該實驗,在儲存於蝕刻液槽之Na〇H液,浸潰c粒 子’使得條件正如以下。 •在钱刻液槽浸潰P — Si晶圓(1〇〇g)• NaOH temperature: 85 ° C • Total surface area of particles: 2 500 cm2 In addition, as the metal evaluation of Si C surface and C surface, the metals adsorbed on SiC and C are dissolved in HF liquid, evaporated to dryness. After dilution with an acid solution, measurement was performed by ICP mass spectrometry (ICPMS). As shown in Fig. 8, the adsorption amounts of copper and nickel relative to SiC and the adsorption amounts of copper and nickel relative to C are almost the same. From this result, it can be said that Sic and C are the same in terms of metal capture force. The C system is better than Sic in the following aspects. The c-system can be in various forms, and therefore can be made into particles & In comparison of the fibers filled in a volume and Table 2 are larger than the surface area of the particles. That is to say, in the state of filling with: Ν and particles and passing through the NaOH solution, the fiber and area are larger than the contact surface between the particles and the liquid: the fiber is more than the filler. The converter is even more :: Fill in [Solution :: 5] Generally C series is cheaper than SiC, so reduce the cost. Page 20 7054-6651-PF (N3); Ahddub.ptd 1244134 V. Description of the invention As shown in FIG. 9, the metal adsorption member has a property that the higher the concentration of the etching solution, the more metal is adsorbed. Here, a description will be given of an embodiment in which an etching solution generation process is efficiently performed using this property. FIG. 9 shows the results of experiments performed by the present inventors. Fig. 9 is a graph showing the relationship between the concentration of the etchant and the amount of metal adsorbed on the c particles. In Fig. 9, the results are shown for copper and nickel in NaOH solution. In this experiment, c-particles were impregnated in NaOH solution stored in an etching bath so that the conditions were as follows. • P-Si wafer immersed in a money-cutting liquid bath (100g)
NaOH ?辰度· 30 〜6〇wt% • Na0H液中之金屬離子濃度:Ni =20ppb、Cu =l〇ppb • NaOH 溫度:85 • C粒子之全表面積·· 2500cm2 • C粒子浸潰時間:2小時 此外’作為C粒子表面之金屬評價係使得吸附於c之金 屬,溶解於HF液,進行蒸發乾固,在藉由酸液而進行稀釋 後’藉由1CP質量分析法(ICPMS)而進行測定。 田由圖9曰而得知·· NaOH液之濃度越高,則吸附於c粒子之 ,里及鎳里更加增加。此外,還得知· Na〇H液之濃度越 同’則增加率越大。因此,在高濃度之NaOH液和C相接觸 而使得NaOH液中之金屬吸附於c後,如果稀釋Na〇H液而成 為在蝕刻處理所需要之濃度為止的話,則可以生成更加減 低金屬之蝕刻液。NaOH? 30 ° ~ 60% by weight • Metal ion concentration in Na0H solution: Ni = 20ppb, Cu = 10ppb • NaOH temperature: 85 • Full surface area of C particles · 2500cm2 • C particle immersion time: 2 hours In addition, as the metal evaluation of the surface of C particles, the metal adsorbed on c was dissolved in HF liquid, evaporated to dryness, and diluted with an acid liquid, and then performed by 1CP mass spectrometry (ICPMS). Determination. Tian knows from Figure 9 that the higher the concentration of NaOH solution, the more it is adsorbed on the c particles, and the more it is in the nickel. It was also found that the increase in the concentration of NaOH solution is greater. Therefore, after the high-concentration NaOH solution is brought into contact with C and the metal in the NaOH solution is adsorbed on c, if the NaOH solution is diluted to a concentration required for the etching process, an etching with a reduced metal content can be generated. liquid.
7054-6516-PF(N3) ;Ahddub.ptd 第21頁 1244134 五、發明說明(18) 圖1 0係第5實施形態之方塊圖。 本裝置係由蝕刻液生成處理部5 〇和蝕刻處理部6 G所構 成。、钱刻液生成處理部5 0係藉由管路而連接蝕刻液槽5 j、 幫浦5 2、C過濾器5 3和聯機加熱器5 4,钱刻處理部6 0藉由 管路而連接蝕刻液槽61、幫浦62和聯機加熱器64❾ ^在蝕刻液槽5 1,儲存高濃度之驗系蝕刻液。在本實施 形恕’使用NaOH液,來作為鹼系蝕刻液。在蝕刻液槽5 j, ,接在途中設置幫浦52之管路5 6之某一端。管路56之其他 、係連接在C過濾器5 3之上游側。此外,在蝕刻液槽5 j, ,接管路57之某一端。管路57之其他端係連接在聯機加熱 器54之下游侧。C過濾器53之下游侧和聯機加熱器54之上 游側係透過管路58而進行連通。 在C過滤器5 3,填充C纖維。此外,可以在c過減 53,填充其他形態之c,也可以填充Sic。 似 在钱刻液槽61 ’儲存藉由蝕刻液生成處理部5〇所生成 之蝕刻液。在蝕刻液槽61,連接在途中設置幫浦62之管路 66之某一端。管路66之其他端係連接在聯機加熱器“之上 游侧。此外,在蝕刻液槽61,連接管路67之某一端。管路 6 7之其他端係連接在聯機加熱器6 4之下游侧。 接著,說明圖1 0所示之裝置之動作。 在儲存於蝕刻液槽51之高濃度“〇11液,預先添加Si來 作為還原劑。在啟動幫浦52時,高濃度肫⑽液係由蝕刻液 開始,透過管路56而供應至c過濾器53。供應至c過濾 器53之高濃度Na0H液係接觸到c纖維,同時,流動至下游 12441347054-6516-PF (N3); Ahddub.ptd Page 21 1244134 V. Description of the invention (18) Figure 10 is a block diagram of the fifth embodiment. This apparatus is composed of an etchant generation processing section 50 and an etching processing section 6G. The coin carving solution generation processing unit 50 is connected to the etching liquid tank 5 j, the pump 5 2, the C filter 5 3 and the on-line heater 5 4 through the pipeline, and the coin carving processing unit 60 is connected to the pipeline through the pipeline. The etching solution tank 61, the pump 62 and the online heater 64 are connected. In the etching solution tank 51, a high-concentration test system etching solution is stored. In this embodiment, NaOH solution is used as an alkali-based etchant. In the etching solution tank 5 j,, one end of the pipeline 56 of the pump 52 is set in the middle. The other line 56 is connected upstream of the C filter 53. In addition, in the etching solution tank 5 j,, one end of the pipe 57 is connected. The other end of the pipe 57 is connected to the downstream side of the in-line heater 54. The downstream side of the C filter 53 and the upstream side of the in-line heater 54 are communicated through a pipe 58. C filter 5 3 is filled with C fiber. In addition, you can subtract 53 from c to fill c in other forms, or fill Sic. It seems that the etching solution generated by the etching solution generation processing unit 50 is stored in the coin etching liquid tank 61 '. In the etching solution tank 61, one end of a pipeline 66 provided with a pump 62 in the middle is connected. The other end of the pipeline 66 is connected to the upstream side of the in-line heater. In addition, one end of the pipeline 67 is connected to the etching bath 61. The other ends of the pipeline 66 are connected to the downstream of the in-line heater 64 Next, the operation of the device shown in FIG. 10 will be described. In a high-concentration "0.11" solution stored in the etching bath 51, Si is added in advance as a reducing agent. When the pump 52 is started, the high-concentration rhenium starts from the etchant and is supplied to the c filter 53 through the line 56. The high-concentration Na0H liquid supplied to the c filter 53 comes into contact with the c fiber, and flows downstream 1244134
側’藉由聯機加熱器5 4而升溫至4 0 °C以上、最好是8 〇 t程 度透過管路57而排出至儀刻液槽51。也就是說,高濃度 NaOH液係環流於蝕刻液槽5丨和〇過濾器53間。在包含金屬 之高濃度NaOH液通液至C過濾器53時,高濃度NaOH液中之 金屬係吸附於C纖維。因此,在高濃度Na〇H液通液至c過濾 器53時’減低含有在高濃度“〇[1液中之金屬量。在經過既 定時間時,停止幫浦52。 、 南濃度NaOH液係由蝕刻液槽51開始移送至蝕刻液槽 61。儲存於蝕刻液槽61之高濃度心⑽液係藉由純水而^行 稀釋,生成既定濃度之Na〇H液。 在鍅刻液槽61之NaOH液中,浸潰晶圓。於是,進行晶 圓之蝕刻三在啟動幫浦62時,Na〇H液係由蝕刻液槽61開 始,透過管路66而供應至聯機加熱器。供應至聯機加熱 器64之NaOH液係升溫至6〇 °c〜90 °c程度,透過管路67而排 出至蝕巧液槽61。像這樣Na0H液係保持在設定溫度,並 且,進行蝕刻。 此外’相同於第1實施形態,可以僅藉由圖丨〇之蝕刻 液生成處理部5 0而進行蝕刻液生成處理及蝕刻處理。此 外,可以j蝕刻處理部6〇之循環系統,設置c過濾器。此 外,正如^施例1、2,可以成為沖洗c過濾器53之構造。 — 如果藉由第5實施形態的話,則得到相同於第1〜第4 =施形,之同樣效果。此外,本實施形態係比起第丨〜第4 貫施形態’還使得蝕刻液生成處理之效率變得更加良妤, 因此,可以達到蝕刻液生成處理之縮短化。The side 'is heated to 40 ° C or higher by the on-line heater 54, and preferably discharged through the pipe 57 to the engraved liquid tank 51 to a degree of 80 °. That is, a high-concentration NaOH solution is circulated between the etching bath 5 and the filter 53. When the high-concentration NaOH solution containing metal is passed to the C filter 53, the metal in the high-concentration NaOH solution is adsorbed on the C fiber. Therefore, when the high-concentration NaOH solution is passed to the c filter 53, the amount of metal contained in the high-concentration "0 [1 solution is reduced. When the predetermined time elapses, the pump 52 is stopped. The liquid is transferred from the etching solution tank 51 to the etching solution tank 61. The high-concentration palpitate solution stored in the etching solution tank 61 is diluted with pure water to generate a NaOH solution of a predetermined concentration. In the etching solution tank 61 The NaOH solution was used to immerse the wafer. Therefore, when the wafer 62 was started, the NaOH solution was started from the etching solution tank 61 and supplied to the on-line heater through the pipeline 66. Supply to The NaOH liquid system of the on-line heater 64 is heated to a temperature of 60 ° C to 90 ° C, and is discharged to the etching liquid tank 61 through the pipe 67. In this way, the Na0H liquid system is maintained at a set temperature and is etched. Similarly to the first embodiment, the etching solution generation process and the etching process can be performed only by the etching solution generation process unit 50 in FIG. 10. In addition, the c filter can be provided in the circulation system of the etching process unit 60. In addition, as in the first and second embodiments, the structure of the c filter 53 can be washed. — If the fifth embodiment is adopted, the same effect as that of the first to fourth = application forms can be obtained. In addition, the present embodiment makes the etching solution generation process more effective than the first through fourth application forms. The efficiency becomes more favorable, so that the etching solution generation process can be shortened.
1244134 五、發明說明(20) 而、隹ί外二由於蝕刻液之生成和蝕刻處理係藉由不同穿置 而進订,因此,即使是在㈣液生成側之系統=置 礙,也可以進行蝕刻處理。 泰生Ρ早 一在此,將顯示前述各個實施形態之有效性之次 表不。經過各個晶圓製造製程之矽晶圓係評價嚅入 為製品。對於藉由各個實施形態而施行蝕刻處理 ^ ^, 適用將析出在1〇〇 t加熱晶圓30分鐘之晶圓表面 曰曰/ / 里予以測疋之評價法。結果,Cu · Ni量係分別成為 lE10atoms(原子數)/cm2以下。如果以.Ni量成為該程度的 話,則可以說是金屬含有量變少,可以說是良好地成^製 品0 此外,在1C晶片等之元件製造製程,為了去除晶圓表 面之被覆膜,因此’施行蝕刻處理,但是,本發明 以適用在該蝕刻處理。 7054-6516-PF(N3);Ahddub.ptd 第24頁 Τ244Π4 ____ 圖式簡單說明 【圖示簡單說明】 圖1(a)係第1實施形態之方塊圖,圖1(b)係SiC過濾器 之不意圖。 圖2係顯示蝕刻液對於SiC過濾器之通液時間和Sic粒 子上之金屬吸附量間之關係之圖。 圖3係顯示蝕刻液對於S i C過濾器之通液時間和钱刻液 中之金屬濃度間之關係之圖。 圖4係顯示#刻液對於S i C過濾器之通液時間和曰 體之金屬濃度間之關係之圖。 M ^ 圖5係第2實施形態之方塊圖。 圖6係第3實施形態之方塊圖。 圖7係顯示蝕刻液中之金屬含有量和矽晶圓基體 圖8係顯示蝕刻液之通液時間和粒子上之金 間之關係之圖。 屬吸附量 圖9係顯示#刻液之濃度和c粒子上之全屬 關係之圖。 千上之金屬吸附量間之 圖1 0係第5實施形態之方塊圖。 2〜幫浦; 4〜SiC過濾器; 6〜HF液供應部; 1 2〜管路; 【主要元件符號說明】 1〜钮刻液槽; 3〜供應切換部; 5〜與纟出切換部; 11〜管路;1244134 V. Description of the invention (20) In addition, because the generation of the etching solution and the etching process are ordered by different placements, even the system on the generation side of the etching solution = obstacle can be carried out. Etching. As soon as Tyson P is here, it will show the effectiveness of the foregoing embodiments. Silicon wafers that have passed each wafer manufacturing process are evaluated and incorporated into the product. For the etching process performed in each embodiment, an evaluation method is used in which the precipitation is measured on a wafer surface heated at 100 t for 30 minutes. As a result, the amount of Cu · Ni was 1E10 atoms / cm2 or less. If the amount of Ni is at this level, it can be said that the metal content is reduced, and it can be said to be a good product. In addition, in the manufacturing process of components such as 1C wafers, in order to remove the coating on the wafer surface, 'An etching process is performed, but the present invention is applicable to this etching process. 7054-6516-PF (N3); Ahddub.ptd Page 24 T244Π4 ____ Brief description of the diagram [Simplified illustration of the diagram] Figure 1 (a) is a block diagram of the first embodiment, and Figure 1 (b) is a SiC filter No intention. Fig. 2 is a graph showing the relationship between the flow time of the etchant to the SiC filter and the amount of metal adsorbed on the Sic particles. Fig. 3 is a graph showing the relationship between the flow time of the etching solution to the Si C filter and the metal concentration in the etching solution. Fig. 4 is a graph showing the relationship between the flow time of #etching liquid to the Si C filter and the metal concentration of the volume. M ^ FIG. 5 is a block diagram of the second embodiment. Fig. 6 is a block diagram of the third embodiment. Fig. 7 is a graph showing the relationship between the metal content in the etchant and the silicon wafer substrate. Fig. 8 is a graph showing the relationship between the flow time of the etchant and the metal on the particles. Amount of genus adsorption Figure 9 is a graph showing the relationship between the concentration of # 刻 液 and the genus of c particles. Fig. 10 is a block diagram of the fifth embodiment. 2 ~ pump; 4 ~ SiC filter; 6 ~ HF liquid supply unit; 1 ~ 2 ~ pipeline; [Description of main component symbols] 1 ~ button carved liquid tank; 3 ~ supply switching unit; 5 ~ pull-out switching unit ; 11 ~ pipeline;
1244134 圖式簡單說明1244134 Simple illustration
21 - -管 路 9 21, ’〜管路; 22 - ‘管 路 9 22’ '〜管路; 41 - ‘柱 體 9 42 〜SiC粒子; 50 - 刻 液 生 成處理 部;51 〜钮刻液槽; 52〜幫 浦 參 , 53 〜C過濾、器; 54 - -聯 機 加 熱 益 , 56 〜管路; 57〜管 路 9 58 〜管路; 60, -名虫 刻 處 理 部; 61 〜钱刻液槽; 62〜幫 浦 9 64 〜聯機加熱器; 66〜管 路 ; 67 〜管路。 7054-6516-PF(N3);Ahddub.ptd 第26頁21--Pipeline 9 21, '~ Pipeline; 22 -'Pipeline 9 22' '~ Pipeline; 41 -'Pillar 9 42 ~ SiC particles; 50-etch solution generation processing unit; 51-button etch solution Trough; 52 ~ pusam, 53 ~ C filter, filter; 54--online heating benefits, 56 ~ pipeline; 57 ~ pipeline 9 58 ~ pipeline; 60,-famous insect carved processing section; 61 ~ money carved Liquid tank; 62 ~ pump 9 64 ~ on-line heater; 66 ~ pipe; 67 ~ pipe. 7054-6516-PF (N3); Ahddub.ptd Page 26
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