JP2002172366A - Method and apparatus for wet cleaning of substrate - Google Patents
Method and apparatus for wet cleaning of substrateInfo
- Publication number
- JP2002172366A JP2002172366A JP2000369632A JP2000369632A JP2002172366A JP 2002172366 A JP2002172366 A JP 2002172366A JP 2000369632 A JP2000369632 A JP 2000369632A JP 2000369632 A JP2000369632 A JP 2000369632A JP 2002172366 A JP2002172366 A JP 2002172366A
- Authority
- JP
- Japan
- Prior art keywords
- cleaning
- draft
- air
- substrate
- clean air
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Cleaning By Liquid Or Steam (AREA)
- ing And Chemical Polishing (AREA)
- Weting (AREA)
- Cleaning Or Drying Semiconductors (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、基板の湿式洗浄方
法および湿式洗浄装置に関し、とくに、表面にシリコン
酸化膜を有するシリコン基板または、ガラス基板を洗浄
液に浸漬して洗浄する方法および装置に関するものであ
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for wet cleaning a substrate, and more particularly to a method and an apparatus for immersing a silicon substrate having a silicon oxide film on its surface or a glass substrate in a cleaning liquid for cleaning. It is.
【0002】[0002]
【従来の技術】従来、半導体やLCD(液晶表示装置)
の製造工程において半導体基板、ガラス基板の洗浄に
は、フッ化アンモニウムとフッ化水素酸の混合水溶液、
フッ化アンモニウム水溶液または、フッ化水素酸の水溶
液がそれぞれ洗浄液として用いられている。上記半導体
基板の洗浄は主に、表面に形成された酸化膜(熱酸化膜
または自然酸化膜)をエッチングにより除去するために
行われ、ガラス基板の洗浄は、基板の表面層を同じくエ
ッチングで除去するために行われるものである。なお、
上記フッ化アンモニウム水溶液は、フッ化水素酸とアン
モニアとの任意混合液であって、NH4 Fのかたちで
水に溶解しており、界面活性剤を含んでいる場合もあ
る。2. Description of the Related Art Conventionally, semiconductors and LCDs (liquid crystal display devices)
In the manufacturing process of the above, for cleaning the semiconductor substrate and the glass substrate, a mixed aqueous solution of ammonium fluoride and hydrofluoric acid,
An aqueous solution of ammonium fluoride or an aqueous solution of hydrofluoric acid is used as a cleaning liquid. The cleaning of the semiconductor substrate is mainly performed to remove the oxide film (thermal oxide film or natural oxide film) formed on the surface by etching, and the cleaning of the glass substrate is also performed by removing the surface layer of the substrate by etching. It is done to do. In addition,
The ammonium fluoride aqueous solution is an arbitrary mixture of hydrofluoric acid and ammonia, is dissolved in water in the form of NH4F, and may contain a surfactant.
【0003】上記半導体やLCDの製造技術分野では、
製品の軽量化・小型化・低消費電力化を達成するべく、
集積度をより高くするために、より微細な加工が可能な
技術が求められている。このような事情から、上記洗浄
液による基板洗浄技術においても、より精度の高い洗浄
処理が望まれている。In the field of the above-mentioned semiconductor and LCD manufacturing technologies,
In order to achieve lighter, smaller, and lower power consumption products
In order to further increase the degree of integration, a technology capable of finer processing is required. Under such circumstances, a higher-precision cleaning process is also desired in the above-described substrate cleaning technology using a cleaning liquid.
【0004】ところで従来、半導体基板の湿式洗浄技術
では一般に、洗浄ドラフト内に設けた洗浄槽に洗浄液を
貯留し、多数枚の半導体基板をウエハカセットと呼ばれ
る容器に収納し、この容器ごと洗浄液に浸漬し、洗浄ド
ラフト内にクリーンエアーを、特別な制御を行うことな
く単に流過させながら洗浄している。Conventionally, in the wet cleaning technique for semiconductor substrates, generally, a cleaning liquid is stored in a cleaning tank provided in a cleaning draft, and a large number of semiconductor substrates are stored in a container called a wafer cassette, and this container is immersed in the cleaning liquid. Then, cleaning is performed while simply flowing clean air into the cleaning draft without performing special control.
【0005】このため、図3に示すように、洗浄時間の
経過とともに洗浄液中のフッ化水素酸(HF)の濃度が
増大する。この図3は、洗浄液を洗浄に使用し始めた時
点からの経過時間(洗浄時間)と、洗浄液のフッ化水素
酸濃度との関係を示すグラフである。この結果、図4に
示すように、上記シリコン酸化膜または、ガラス基板表
面層のエッチング速度が経時とともに増加するうえ、こ
の濃度上昇変化に大きなムラがあるため均一、かつ安定
した洗浄ができず、半導体基板や液晶表示装置用基板の
歩留り向上が難しくなるという問題があった。For this reason, as shown in FIG. 3, the concentration of hydrofluoric acid (HF) in the cleaning liquid increases as the cleaning time elapses. FIG. 3 is a graph showing the relationship between the elapsed time (cleaning time) from the time when the cleaning liquid was used for cleaning and the concentration of hydrofluoric acid in the cleaning liquid. As a result, as shown in FIG. 4, the etching rate of the silicon oxide film or the surface layer of the glass substrate increases with time, and the change in the concentration has a large unevenness, so that uniform and stable cleaning cannot be performed. There has been a problem that it is difficult to improve the yield of semiconductor substrates and substrates for liquid crystal display devices.
【0006】上記各洗浄液のフッ化水素酸濃度が洗浄時
間の経過とともに上昇する原因は、(1)この洗浄液か
ら蒸発した水分が、クリーンエアーに同伴して洗浄ドラ
フト外に排出されること、(2)上記フッ化アンモニウ
ム水溶液では、フッ化アンモニウム(NH4 F)が水
酸化アンモニウムとフッ化水素酸とに解離しており、こ
の水酸化アンモニウムがアンモニアガスとなって、同じ
くクリーンエアーとともに洗浄ドラフト外に排出される
ことにある。The causes of the increase in the concentration of hydrofluoric acid in each of the cleaning liquids with the elapse of the cleaning time are as follows: (1) Moisture evaporated from the cleaning liquid is discharged out of the cleaning draft along with clean air; 2) In the above-mentioned aqueous solution of ammonium fluoride, ammonium fluoride (NH4F) is dissociated into ammonium hydroxide and hydrofluoric acid, and this ammonium hydroxide becomes ammonia gas, which is also removed from the cleaning draft together with clean air. To be discharged to
【0007】このため従来は、洗浄液の交換を頻繁に行
うことで、洗浄液内の有効成分濃度の上昇(濃度ムラを
含む)を抑える方法がとられてきた。しかしこのような
方法では、非常に多量の洗浄液を使用することになる。
特にフッ化アンモニウムを含有する洗浄液は、40wt
%前後という高濃度の状態で使用されるため、通常数%
程度の濃度で使用される他の洗浄液に比べて、1回当た
りの液交換で消費される薬品の量が多くなるという問題
があった。Conventionally, therefore, a method has been employed in which the cleaning solution is frequently replaced to suppress an increase in the active ingredient concentration (including the concentration unevenness) in the cleaning solution. However, in such a method, a very large amount of cleaning liquid is used.
In particular, the cleaning solution containing ammonium fluoride is 40 wt.
% Because it is used in a high concentration state of around%
There is a problem that the amount of chemical consumed per liquid exchange is increased as compared with other cleaning liquids used at a concentration of about one level.
【0008】また、上記フッ化水素酸系の洗浄液(フッ
酸系洗浄液)が使用済となった場合、図5に示すような
工程による廃液処理(排水処理)が必要となるが、この
廃液処理では多量の資源すなわち排水処理剤が消費され
るだけでなく、これに伴い、図6の物質収支図で明らか
なように、多量の廃棄物(排水と汚泥)が発生すること
になる。図5は、使用済洗浄液の廃液処理工程を示すフ
ローシート(半導体製造工程からのフッ化アンモニウム
廃液の処理フロー)である。図6は、図5の廃液処理工
程に係る物質収支を示す説明図である。When the hydrofluoric acid-based cleaning liquid (hydrofluoric acid-based cleaning liquid) has been used, a waste liquid treatment (drainage treatment) by a process as shown in FIG. 5 is required. In this case, not only a large amount of resources, that is, a wastewater treatment agent, is consumed, but also a large amount of waste (drainage and sludge) is generated as is apparent from the material balance diagram of FIG. FIG. 5 is a flow sheet (processing flow of ammonium fluoride waste liquid from a semiconductor manufacturing process) showing a waste liquid processing step of a used cleaning liquid. FIG. 6 is an explanatory diagram showing a material balance relating to the waste liquid treatment step of FIG.
【0009】ところで近年、地球環境問題は世界的な関
心事となっており、半導体やLCD等の基板製造工程が
環境に与える影響が問題視されるようになってきた昨今
では、基板製造工程での洗浄コストの削減対策だけでは
足りず省資源や、廃棄物の発生量低減・環境浄化等の、
環境保全での対応が社会的に強く求められている。In recent years, global environmental problems have become a global concern, and the influence of the manufacturing process of substrates such as semiconductors and LCDs on the environment has become a problem in recent years. It is not enough to reduce washing costs of resources, and it is necessary to save resources, reduce the amount of waste generated, and purify the environment.
There is a strong social demand for environmental protection.
【0010】このため、洗浄液の交換を頻繁に行うこと
なく洗浄槽内の洗浄液の薬液組成を所定範囲内に維持す
ることができるようにした洗浄装置として、温湿度・ク
リーンエア風量等が制御された雰囲気下に洗浄槽を設置
したものが提案されている(特開平9−22891号公
報)。しかしながら、この洗浄装置では、加湿されたエ
アーカーテンを用いているものの、クリーンエアーの流
れが水平方向であるため、被洗浄基板の清浄度の維持が
困難であるだけでなく、被洗浄基板の出し入れに際して
エアーの流れを中断せねばならないため、操作が面倒に
なるという問題点があった。For this reason, the temperature, humidity, clean air volume and the like are controlled as a cleaning apparatus which can maintain the chemical composition of the cleaning liquid in the cleaning tank within a predetermined range without frequently changing the cleaning liquid. (Japanese Patent Application Laid-Open No. Hei 9-22891) has been proposed in which a cleaning tank is installed in an atmosphere that has been heated. However, in this cleaning apparatus, although the humidified air curtain is used, since the flow of the clean air is horizontal, not only is it difficult to maintain the cleanness of the substrate to be cleaned, but also it is necessary to insert and remove the substrate to be cleaned. At that time, the flow of air must be interrupted, which causes a problem that the operation is troublesome.
【0011】[0011]
【発明が解決しようとする課題】本発明は、上記事情に
鑑みなされたもので、その目的は、有効成分としてフッ
化水素酸を水に溶解した洗浄液を使用する基板の湿式洗
浄技術において、洗浄処理を均一・安定化するととも
に、洗浄液使用に伴う環境負荷を低減すること、すなわ
ち洗浄用薬品の消費量低減、廃棄物発生量の低下、環境
汚染の抑制等を実現することにある。SUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances, and it is an object of the present invention to provide a wet cleaning technique for a substrate using a cleaning solution in which hydrofluoric acid is dissolved in water as an active ingredient. An object of the present invention is to make the treatment uniform and stable, and to reduce the environmental burden associated with the use of the cleaning liquid, that is, to reduce the consumption of cleaning chemicals, reduce the amount of waste generated, and suppress environmental pollution.
【0012】[0012]
【課題を解決するための手段】本発明に係る基板の湿式
洗浄方法は、有効成分を水に溶解してなる洗浄液を、洗
浄ドラフト内に設けた洗浄槽に貯留し、該洗浄液に被洗
浄基板を浸漬し、洗浄ドラフト内にクリーンエアーを流
しながら洗浄する方法において、加湿により相対湿度を
所定範囲内に制御したクリーンエアーを、洗浄槽の洗浄
液液面に向けて鉛直方向下向きに供給するとともに、洗
浄ドラフト内の空気を所定範囲内の排気量で排気しなが
ら被洗浄基板の洗浄を行うことを特徴とする。In a wet cleaning method for a substrate according to the present invention, a cleaning liquid obtained by dissolving an active ingredient in water is stored in a cleaning tank provided in a cleaning draft, and the substrate to be cleaned is added to the cleaning liquid. In the method of immersing and cleaning while flowing clean air in the cleaning draft, the clean air whose relative humidity is controlled within a predetermined range by humidification is supplied vertically downward toward the cleaning liquid level of the cleaning tank, The substrate to be cleaned is cleaned while exhausting the air in the cleaning draft with a displacement within a predetermined range.
【0013】上記洗浄方法では、相対湿度を40%〜5
0%の範囲に、温度を常温にそれぞれ制御したクリーン
エアーを供給することが望ましく、これにより、本発明
の効果がより顕著なものになる。また、洗浄ドラフト内
の気圧を外部の大気圧より高めに制御することにより、
洗浄ドラフト外の大気が洗浄ドラフトに侵入するのを防
止することが好ましい。こうすることで、洗浄ドラフト
内のクリーンエアーのクリーン度が維持されるととも
に、クリーンエアーの流過状態や温湿度が安定化するた
め、より安定した湿式洗浄を継続することができる。In the above-mentioned cleaning method, the relative humidity is set at 40% to 5%.
It is desirable to supply clean air whose temperature is controlled to room temperature in the range of 0%, whereby the effect of the present invention becomes more remarkable. Also, by controlling the pressure inside the cleaning draft higher than the outside atmospheric pressure,
It is preferable to prevent the atmosphere outside the cleaning draft from entering the cleaning draft. By doing so, the cleanness of the clean air in the cleaning draft is maintained, and the flowing state of the clean air and the temperature and humidity are stabilized, so that more stable wet cleaning can be continued.
【0014】また上記洗浄方法では、洗浄液としてフッ
化アンモニウム、フッ化水素酸の少なくとも一方を水に
溶解したものを使用することにより、シリコン基板の表
面に形成されたシリコン酸化膜、またはガラス基板の表
面層を能率良くエッチングにより洗浄除去することがで
きる。Further, in the above-mentioned cleaning method, by using at least one of ammonium fluoride and hydrofluoric acid dissolved in water as a cleaning liquid, a silicon oxide film formed on the surface of the silicon substrate or a glass substrate is removed. The surface layer can be efficiently removed by etching.
【0015】さらに、本発明に係る基板の湿式洗浄装置
は、有効成分を水に溶解してなる洗浄液を、洗浄ドラフ
ト内に設けた洗浄槽に貯留し、該洗浄液に被洗浄基板を
浸漬し、洗浄ドラフト内にクリーンエアーを流しながら
洗浄する装置において、洗浄ドラフト内にクリーンエア
ーを洗浄槽の洗浄液液面に向けて鉛直方向下向きに供給
するクリーンエアー供給手段と、洗浄ドラフト内に水蒸
気または霧状の水滴を供給し、該洗浄ドラフト内のクリ
ーンエアーの相対湿度を所定範囲内に維持する加湿機
と、洗浄槽の洗浄液液面近傍に配置され、加湿機に連絡
された湿度計と、洗浄ドラフト内のエアーを排気する排
気管と、該排気管に設けた排気量制御手段とを備えてな
り、湿度計による湿度測定値を加湿機にフィードバック
して、加湿機からの水蒸気または霧状水滴の供給量を所
定範囲内に制御し、排気量制御手段により洗浄ドラフト
内の空気を所定範囲内の排気量で排気するようにしたこ
とを特徴とする。Further, in the wet cleaning apparatus for a substrate according to the present invention, a cleaning liquid obtained by dissolving an active ingredient in water is stored in a cleaning tank provided in a cleaning draft, and the substrate to be cleaned is immersed in the cleaning liquid. In a device that cleans while flowing clean air into the cleaning draft, clean air supply means that supplies clean air vertically into the cleaning draft toward the cleaning liquid level in the cleaning tank, and steam or mist A humidifier that supplies water droplets and maintains the relative humidity of the clean air in the cleaning draft within a predetermined range, a hygrometer disposed near the cleaning liquid level of the cleaning tank and connected to the humidifier, and a cleaning draft. An exhaust pipe for exhausting the air inside, and an exhaust amount control means provided in the exhaust pipe, and a humidity measurement value by a hygrometer is fed back to the humidifier, and The supply amount of vapor or mist water droplets is controlled within a predetermined range, characterized in that so as to exhaust the exhaust amount within a predetermined range of air in the cleaning draft by the exhaust amount control means.
【0016】上記湿式洗浄装置では、クリーンエアー供
給手段がブロワと、該ブロワの空気吐出側に接続された
除塵フィルタとからなり、加湿機が、水蒸気または霧状
水滴を洗浄槽の洗浄液液面に向けて鉛直方向下向きに供
給するものであり、排気量制御手段が、開度を自動調整
できるダンパーと、排気管に設けられた空気流量計また
は気圧計とからなるとともに、これらの計器がダンパー
に連絡され、該計器による計測値がダンパーにフィード
バックされて、その開度が制御されるように構成するこ
とが好ましい。In the above wet cleaning apparatus, the clean air supply means comprises a blower and a dust filter connected to the air discharge side of the blower, and the humidifier applies water vapor or mist water droplets to the cleaning liquid level of the cleaning tank. The exhaust volume control means consists of a damper that can automatically adjust the opening and an air flow meter or barometer provided in the exhaust pipe, and these instruments are connected to the damper. It is preferable that a communication is made, and the measured value of the meter is fed back to the damper to control the opening thereof.
【0017】さらに、上記湿式洗浄装置では、加湿機と
して、温度を所定範囲内に制御した水蒸気または霧状水
滴を供給するものを設けるとともに、洗浄液液面に向け
て鉛直方向下向きに供給されるクリーンエアーの温度を
所定範囲内に制御する空調機を設けた構成とすることが
望ましい。Furthermore, in the above wet cleaning apparatus, a humidifier for supplying steam or mist-like water drops whose temperature is controlled within a predetermined range is provided, and a clean humidifier supplied vertically downward to the cleaning liquid level is provided. It is preferable to provide an air conditioner for controlling the temperature of air within a predetermined range.
【0018】[0018]
【発明の実施の形態】以下、本発明の実施の形態を、図
面を参照しながら説明する。図1は基板洗浄装置(湿式
洗浄装置)および、これによる基板洗浄方法を示す模式
的説明図である。図2は本発明の洗浄方法と従来の洗浄
方法とにおける、半導体基板表面のシリコン酸化膜のエ
ッチレートを比較して示すグラフである。Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a schematic explanatory view showing a substrate cleaning apparatus (wet cleaning apparatus) and a substrate cleaning method using the apparatus. FIG. 2 is a graph showing a comparison between the etching rate of the silicon oxide film on the surface of the semiconductor substrate in the cleaning method of the present invention and the conventional cleaning method.
【0019】この基板洗浄装置10を以下のように構成
する。開閉扉(図略)を備えた洗浄ドラフト(ドラフト
チャンバ)11内の下方に洗浄槽12を設け、この洗浄
槽12の上端部近傍(洗浄液31の液面近傍)に湿度計
13を設置する。洗浄槽12の直上に加湿機14および
空調機15を設け、この空調機15のエアー流入側に除
塵フィルタ16を連結し、上記湿度計13を加湿機14
に連絡する。除塵フィルタ16のエアー流入側を、給気
ダクトを介してブロワの空気吐出側に連絡する(図
略)。洗浄槽12内には、洗浄時間経過に伴う洗浄液の
温度上昇を抑えて常温に維持するための温度制御手段
(図略)を設けることが望ましい。The substrate cleaning apparatus 10 is configured as follows. A cleaning tank 12 is provided below a cleaning draft (draft chamber) 11 having an opening / closing door (not shown), and a hygrometer 13 is installed near the upper end of the cleaning tank 12 (near the liquid level of the cleaning liquid 31). A humidifier 14 and an air conditioner 15 are provided directly above the washing tank 12, a dust filter 16 is connected to the air inflow side of the air conditioner 15, and the hygrometer 13 is connected to the humidifier 14.
Contact The air inlet side of the dust filter 16 is connected to the air discharge side of the blower via an air supply duct (not shown). In the cleaning tank 12, it is desirable to provide a temperature control means (not shown) for suppressing the temperature rise of the cleaning liquid with the elapse of the cleaning time and maintaining the temperature at a normal temperature.
【0020】洗浄ドラフト11の周壁11aの洗浄槽1
2上端部近傍部位に、排気ダクト17を連結し、この排
気ダクト17にオートダンパ18と、その下流側に風速
計19(またはマノメータ)とを設ける。風速計19を
オートダンパ18の駆動機構に連絡する。なお、風速計
19は、オートダンパ18の上流側に設けてもよいし、
洗浄ドラフト11内に設けることもできる。The cleaning tank 1 on the peripheral wall 11a of the cleaning draft 11
2. An exhaust duct 17 is connected to the vicinity of the upper end, and an automatic damper 18 is provided in the exhaust duct 17, and an anemometer 19 (or a manometer) is provided on the downstream side. The anemometer 19 is communicated to the drive mechanism of the automatic damper 18. The anemometer 19 may be provided on the upstream side of the automatic damper 18,
It can also be provided in the cleaning draft 11.
【0021】図1では、洗浄ドラフト11内に洗浄槽1
2(エッチング槽)のみ示されているが、洗浄ドラフト
11内に、これに隣接してリンス槽および乾燥槽(図
略)を配置することもできる。この場合、リンス槽とし
ては、基板をたとえばイオン交換水に浸漬するものが、
乾燥槽としてはたとえばIPA(イソプロピルアルコー
ル)を基板表面に噴霧した後、クリーンエアーを吹きつ
けて乾燥するものが、それぞれ挙げられる。なお洗浄ド
ラフト11、リンス槽および乾燥槽をこの順に、かつ隔
壁で区画した各区画室に個別に設置し、隣接する区画室
同士を、隔壁に設けた開閉扉を開放することで連通させ
る構造としてもよい。In FIG. 1, a cleaning tank 1 is provided in a cleaning draft 11.
Although only 2 (etching tank) is shown, a rinsing tank and a drying tank (not shown) can be arranged in the cleaning draft 11 adjacent thereto. In this case, as the rinsing tank, one in which the substrate is immersed in, for example, ion-exchanged water,
As the drying tank, for example, a drying tank that sprays IPA (isopropyl alcohol) onto the substrate surface, and then blows the air with clean air to dry the substrate is used. The cleaning draft 11, the rinsing tank, and the drying tank may be arranged in this order and individually in each of the compartments partitioned by the partition walls, and the adjacent compartments may communicate with each other by opening an opening / closing door provided on the partition wall. Good.
【0022】つぎに、この基板洗浄装置10による、シ
リコン基板の洗浄方法の一例について説明する。フッ化
アンモニウムとフッ化水素酸とを水にそれぞれ所定濃度
に溶解して調製した常温の洗浄液31を、洗浄槽12に
所定量投入する。オートダンパ18を適宜開度で開き、
上記ブロア、加湿機14および空調機15の電源をON
にする。洗浄液31からの水分の蒸発を抑えるために
は、洗浄ドラフト11内の雰囲気を水分が乾燥しにくい
相対湿度にする必要があるが、そのため加湿機14によ
り相対湿度の目標値(好ましくは飽和湿度に近い湿度)
を設定する。また、洗浄ドラフト11内の雰囲気を所定
の気温に制御するため、空調機15により気温の目標値
を設定し、洗浄ドラフト11内のエアー排気量(単位時
間当たりの排気エアー量)を制御するため、オートダン
パ18の駆動機構について排気量の目標値を設定する。Next, an example of a method for cleaning a silicon substrate by the substrate cleaning apparatus 10 will be described. A predetermined amount of a room temperature cleaning solution 31 prepared by dissolving ammonium fluoride and hydrofluoric acid at a predetermined concentration in water is charged into the cleaning tank 12. Open the auto damper 18 at an appropriate opening,
Power on the blower, humidifier 14 and air conditioner 15
To In order to suppress the evaporation of water from the cleaning liquid 31, the atmosphere in the cleaning draft 11 needs to be at a relative humidity at which the water is difficult to dry. For this reason, the humidifier 14 is used to set the relative humidity to a target value (preferably, a saturated humidity). Near humidity)
Set. Further, in order to control the atmosphere in the cleaning draft 11 to a predetermined temperature, a target value of the temperature is set by the air conditioner 15 and the amount of air exhausted in the cleaning draft 11 (the amount of exhaust air per unit time) is controlled. The target value of the displacement is set for the drive mechanism of the automatic damper 18.
【0023】多数枚のシリコン基板(シリコンウエハ)
をウエハカセットに鉛直方向に、互いに平行に、かつ相
互間に適宜の隙間をあけて収納し、この容器ごと洗浄液
31に浸漬して洗浄を開始する。この洗浄工程において
シリコン基板は、表面に形成された自然酸化膜がエッチ
ングで除去されることで洗浄される。Many silicon substrates (silicon wafers)
Are stored in a wafer cassette in a vertical direction, parallel to each other, and with an appropriate gap therebetween, and the entire container is immersed in a cleaning liquid 31 to start cleaning. In this cleaning step, the silicon substrate is cleaned by removing a natural oxide film formed on the surface by etching.
【0024】この洗浄工程においては、上記ブロワから
の空気(温度がほぼ常温で、圧力は大気圧より高い)が
除塵フィルタ16、空調機15および加湿機14を介し
て、洗浄槽12の洗浄液31液面の実質的全面に向けて
鉛直方向下向きに供給される。この場合、ブロワからの
空気は除塵フィルタ16で高度に清浄化され、空調機1
5により所定範囲の温度(通常は、ほぼ常温)に制御さ
れ、加湿機14から噴霧される霧状の純水液滴によって
所定範囲の相対湿度に制御される。洗浄液液面に接触し
たクリーンエアは、オートダンパ18を介して所定流量
で外部に排気される。In this cleaning step, the air from the blower (the temperature is almost normal temperature and the pressure is higher than the atmospheric pressure) is passed through the dust removing filter 16, the air conditioner 15 and the humidifier 14, and the cleaning solution 31 The liquid is supplied vertically downward toward substantially the entire liquid surface. In this case, the air from the blower is highly purified by the dust filter 16 and the air conditioner 1
5, the temperature is controlled to a predetermined range (usually, approximately normal temperature), and the relative humidity is controlled to a predetermined range by mist-like pure water droplets sprayed from the humidifier 14. The clean air that has come into contact with the cleaning liquid level is exhausted to the outside at a predetermined flow rate through the auto damper 18.
【0025】このように上記洗浄工程では、圧力が大気
圧よりも高く、所定温度および所定の相対湿度に制御さ
れた加湿状態のクリーンエアーが、洗浄槽12の洗浄液
31液面の実質的全面に向けて鉛直方向下向きに供給さ
れる。したがって、クリーンエアーを洗浄液液面に平行
に流過させる場合と比べて、洗浄液からの水分蒸発を抑
える機能が大幅に向上するとともに、洗浄液液面の空気
置換機能が高まる。そのうえ、上記シリコンウエハ入り
のウエハカセットをハンドリングする際に、ウエハ間の
隙間の空気がクリーンエアーで、より効率良く置換され
るという利点もある。As described above, in the above-described cleaning step, the clean air in a humidified state in which the pressure is higher than the atmospheric pressure and is controlled to a predetermined temperature and a predetermined relative humidity is applied to substantially the entire surface of the cleaning liquid 31 in the cleaning tank 12. It is supplied vertically downward. Therefore, as compared with the case where clean air flows in parallel to the cleaning liquid surface, the function of suppressing evaporation of water from the cleaning liquid is greatly improved, and the function of replacing the cleaning liquid surface with air is enhanced. In addition, when handling the wafer cassette containing the silicon wafer, there is an advantage that the air in the gap between the wafers is more efficiently replaced by clean air.
【0026】上記洗浄工程では、洗浄ドラフト11内の
気圧を、外部の大気圧より高めに制御することによっ
て、洗浄ドラフト11外の大気が洗浄ドラフトに侵入す
るのを防止することができる。こうすることで、洗浄ド
ラフト内のクリーンエアーが侵入した外気で汚染された
り、洗浄ドラフト内のクリーンエアーの流過状態や温湿
度が変動したりする不具合がなくなり、より安定した湿
式洗浄を継続することができる。In the above-mentioned cleaning step, the atmospheric pressure outside the cleaning draft 11 can be prevented from entering the cleaning draft by controlling the pressure inside the cleaning draft 11 to be higher than the atmospheric pressure outside. By doing so, there is no problem that the clean air in the cleaning draft is contaminated by the invading outside air, and the clean air flowing state and the temperature and humidity in the cleaning draft fluctuate, and more stable wet cleaning is continued. be able to.
【0027】実施例および比較例 本発明の実施例では、図1の洗浄装置を使用して上記洗
浄方法でシリコンウエハを洗浄した。比較例では、図1
の洗浄装置において空調機15、加湿機14を使用せ
ず、オートダンパ18の開度を一定にした以外は、実施
例と同様にしてシリコンウエハを洗浄した。結果を図2
に示す。Examples and Comparative Examples In Examples of the present invention, a silicon wafer was cleaned by the above-described cleaning method using the cleaning apparatus of FIG. In the comparative example, FIG.
The silicon wafer was cleaned in the same manner as in the example except that the air conditioner 15 and the humidifier 14 were not used in the cleaning device and the opening degree of the auto damper 18 was fixed. Figure 2 shows the results.
Shown in
【0028】図2で明らかなように、実施例では洗浄開
始からの経過時間に対するエッチレートの上昇速度が低
く、しかもほぼ一定の割合で上昇している。このため、
同一洗浄液を長時間使用した場合にも、液交換を行う必
要がなかった。As apparent from FIG. 2, in the embodiment, the rate of increase of the etch rate with respect to the elapsed time from the start of cleaning is low, and increases at a substantially constant rate. For this reason,
Even when the same cleaning solution was used for a long time, there was no need to change the solution.
【0029】一方、比較例では、洗浄開始からの経過時
間に対するエッチレートの上昇速度が実施例に比べて高
く、そのうえ上昇変化にムラが見られたため、途中で液
交換を行った。しかし液交換した後、短時間の洗浄でエ
ッチレートが上昇し、やがて、液交換を行わない実施例
の場合よりもエッチレートが高くなってしまった。On the other hand, in the comparative example, the rate of increase in the etch rate with respect to the elapsed time from the start of cleaning was higher than that in the example, and the change in the increase was uneven. However, after the liquid exchange, the etch rate was increased by short-time washing, and eventually, the etch rate became higher than that in the example in which the liquid exchange was not performed.
【0030】図1の洗浄装置では、超音波を利用した加
湿機を設けてもよいし、沸騰水からのスチームを洗浄ド
ラフト内に供給して加湿することもできる。また、上記
のように温湿度を制御したクリーンエアーを所定流量で
供給する操作は、フッ化アンモニウム、フッ化水素酸、
アンモニア水、水、界面活性剤等の各種成分を洗浄液に
補充する場合にも有効に採用することができる。In the cleaning apparatus shown in FIG. 1, a humidifier using ultrasonic waves may be provided, or steam from boiling water may be supplied into the cleaning draft to humidify. In addition, the operation of supplying the clean air with the controlled temperature and humidity at a predetermined flow rate as described above includes ammonium fluoride, hydrofluoric acid,
It can also be effectively employed when replenishing various components such as aqueous ammonia, water, and surfactant to the cleaning solution.
【0031】また、洗浄液中の有効成分や水の濃度を測
定する方法としては、(1)所定波長の光の吸光度を測
定するもの、(2)赤外・紫外吸収スペクトルを測定す
るもの、(3)屈折率、比重、光の透過率、電導率等を
測定するもの、(4)カールフィッシャーの水分濃度測
定計を用いるもの、(5)液体(イオン)クロマトグラ
フィーによるものなどが採用できる。The methods for measuring the concentration of the active ingredient and water in the cleaning solution include (1) a method for measuring the absorbance of light having a predetermined wavelength, (2) a method for measuring an infrared / ultraviolet absorption spectrum, and ( 3) a device for measuring the refractive index, specific gravity, light transmittance, conductivity, etc., (4) a device using a Karl Fischer moisture concentration meter, (5) a device using liquid (ion) chromatography, and the like can be used.
【0032】以上説明した洗浄方法を用いることで、図
2に示すように、有効成分として少なくともフッ化水素
酸を水に溶解した洗浄液の、洗浄時間経過に伴うエッチ
レートすなわち洗浄効果の変化やムラを、大幅に低下さ
せることができる。そして、これにより上記洗浄液によ
る洗浄の均一化・安定化が実現されることから、液交換
頻度の低減(洗浄液の長寿命化)や、上記洗浄液の廃液
処理(排水処理)に必要とされる薬剤量の大幅な削減が
可能となる。さらには、前記薬剤量削減により廃棄物す
なわち、汚泥や排水(下水)の発生量が低減するという
効果がある。By using the above-described cleaning method, as shown in FIG. 2, the etching rate of the cleaning solution in which at least hydrofluoric acid is dissolved in water as an active ingredient with the lapse of cleaning time, that is, the change and unevenness of the cleaning effect. Can be greatly reduced. In addition, since the uniformity and stabilization of the cleaning with the cleaning liquid are realized, the chemicals required for reducing the frequency of liquid replacement (extending the cleaning liquid life) and for treating the waste liquid of the cleaning liquid (drainage treatment) are provided. A significant reduction in volume is possible. Further, there is an effect that the amount of generated waste, that is, sludge and wastewater (sewage) is reduced by the reduction in the amount of the chemical.
【0033】また本発明による上記洗浄方法では、図2
に示すように、洗浄開始からの経過時間とエッチレート
との間に一定の直線的関係が見られ、洗浄開始時のエッ
チレート(図2において、経過時間ゼロのときの縦軸の
値)がこの洗浄開始時の洗浄液のフッ化水素酸濃度で決
まり、洗浄開始後のエッチレートが、洗浄開始からの経
過時間により自動的に決まる。In the cleaning method according to the present invention, FIG.
As shown in FIG. 2, a constant linear relationship is observed between the elapsed time from the start of cleaning and the etch rate, and the etch rate at the start of cleaning (the value on the vertical axis when the elapsed time is zero in FIG. 2) is shown in FIG. The etch rate is determined by the concentration of hydrofluoric acid in the cleaning solution at the start of the cleaning, and the etch rate after the start of the cleaning is automatically determined by the elapsed time from the start of the cleaning.
【0034】したがって、洗浄開始時の洗浄液のフッ化
水素酸濃度と、上記経過時間とを知ることで、エッチレ
ートを簡単に推測することができる。また、再現性の高
い洗浄が可能となり、均一・一定のエッチング量で洗浄
することができるという効果がある。逆に、必要なエッ
チング量を設定することで、必要なエッチング時間(上
記経過時間)を簡単に求めることができる。さらに、上
記直線関係を数式化することで、必要なエッチング時
間、あるいは調製するべき洗浄液のフッ化水素酸濃度
を、より簡便に求めることができる。Therefore, the etch rate can be easily estimated by knowing the hydrofluoric acid concentration of the cleaning solution at the start of cleaning and the elapsed time. In addition, cleaning with high reproducibility is possible, and there is an effect that cleaning can be performed with a uniform and constant etching amount. Conversely, by setting the required etching amount, the required etching time (the elapsed time) can be easily obtained. Further, by formulating the above linear relationship into a mathematical expression, the required etching time or the concentration of hydrofluoric acid in the cleaning liquid to be prepared can be more easily obtained.
【0035】ところで、特開平9−22891号公報
(発明の名称:ウエット洗浄プロセス装置及び方法)に
は、シリコンウエハ表面の酸化膜を「エッチング・クリ
ーニング」するための装置が開示されている。この装置
では、温度・湿度・クリーンエアー風量が制御された雰
囲気下に、薬液を貯留した洗浄槽を設置し、相対湿度が
70%以上に制御されたクリーンエアーを洗浄槽の薬液
液面の上方に水平方向に流過させながらウエハの洗浄を
行うようにしている。Japanese Patent Application Laid-Open No. 9-22891 (title of invention: wet cleaning process apparatus and method) discloses an apparatus for "etching and cleaning" an oxide film on a silicon wafer surface. In this system, a cleaning tank storing a chemical solution is installed in an atmosphere where the temperature, humidity, and clean air flow rate are controlled, and clean air whose relative humidity is controlled to 70% or more is supplied above the cleaning liquid level of the cleaning tank. The wafer is cleaned while flowing horizontally.
【0036】しかしがなら上記装置では、洗浄後にウエ
ハカセットを洗浄槽から引き上げて、例えば次の水洗槽
に搬送する間も、クリーンエアーを継続して流過させた
場合には、これがウエハ表面に垂直に吹きつけられ、ウ
エハ表面でクリーンエアーの乱流が生じるため、洗浄後
のウエハ表面にいわゆるパーティクル(異物)が付着す
る問題がある。この不具合をなくすには、上記ウエハカ
セット搬送時にクリーンエアーの供給を停止しなければ
ならないという煩雑さが伴う。However, in the above-described apparatus, if the wafer cassette is pulled out of the cleaning tank after the cleaning and the clean air is continuously passed through, for example, while being conveyed to the next water cleaning tank, the wafer cassette is discharged onto the wafer surface. Since the air is blown vertically and turbulence of clean air is generated on the wafer surface, there is a problem that so-called particles (foreign matter) adhere to the cleaned wafer surface. Eliminating this inconvenience involves the necessity of stopping the supply of clean air during the transfer of the wafer cassette.
【0037】これに対し本発明の洗浄方法・装置では、
クリーンエアーを洗浄槽の上方から洗浄液液面に垂直方
向下向きに供給しながら、基板洗浄を行うようにしてい
る。このため、ウエハカセットの搬送時には、クリーン
エアーがウエハ表面に平行に流過するので、上記パーテ
ィクル発生のおそれが殆どなくなる。したがって、クリ
ーンエアーを流し続けたまま、ウエハカセットの搬送を
行うことができる。On the other hand, in the cleaning method / apparatus of the present invention,
The substrate is cleaned while supplying clean air from above the cleaning tank to the cleaning liquid surface in the vertical direction. Therefore, when the wafer cassette is transported, the clean air flows in parallel to the wafer surface, so that there is almost no possibility of the generation of the particles. Therefore, it is possible to carry the wafer cassette while keeping the clean air flowing.
【0038】[0038]
【発明の効果】請求項1に係る湿式洗浄方法によれば、
洗浄処理の均一化が図れて高品質の洗浄処理品を安定し
て得ることができるとともに、洗浄液の交換頻度が減少
する。この結果、洗浄液調製用薬品の消費量が低下する
うえ、使用済洗浄液の廃液排出量が減少するため該廃液
処理の負担が軽減され、該廃液処理用の薬品消費量が削
減されて省資源化が達成されるうえ、廃液処理に伴って
発生する汚泥、排水の量が大幅に低下する。According to the wet cleaning method of the first aspect,
The cleaning process can be made uniform, a high-quality cleaning product can be stably obtained, and the frequency of replacement of the cleaning solution is reduced. As a result, the consumption of the cleaning liquid preparation chemicals is reduced, and the waste liquid discharge amount of the used cleaning liquid is reduced, so that the burden of the waste liquid treatment is reduced, and the consumption of the chemicals for the waste liquid treatment is reduced, thereby conserving resources. Is achieved, and the amount of sludge and wastewater generated during waste liquid treatment is significantly reduced.
【0039】請求項2に係る湿式洗浄方法によれば、洗
浄工程において、洗浄液からの水の蒸発逸散量減少効果
が高まるうえ、この逸散量が所定範囲内に制御されるた
め、洗浄に使用した時間と、洗浄液の有効成分濃度との
関係が安定するとともに直線的な関係になり、請求項1
の発明による効果がより顕著になる。According to the wet cleaning method of the second aspect, in the cleaning step, the effect of reducing the amount of evaporation and loss of water from the cleaning liquid is enhanced, and the amount of evaporation is controlled within a predetermined range. 2. The relationship between the used time and the concentration of the active ingredient in the washing solution becomes stable and linear.
The effect of the invention of (1) becomes more remarkable.
【0040】請求項3に係る湿式洗浄方法では、洗浄液
としてフッ化アンモニウム、フッ化水素酸の少なくとも
一方を水に溶解したものを使用し、シリコン基板の表面
に形成されたシリコン酸化膜をエッチングにより洗浄除
去するようにしたため、洗浄処理が均一化し、洗浄時間
とエッチング量との関係が直線的なものになるので、再
現性の高い洗浄処理が行われ、エッチング量を精度良く
管理することが可能となる。In the wet cleaning method according to the third aspect, a cleaning solution obtained by dissolving at least one of ammonium fluoride and hydrofluoric acid in water is used, and the silicon oxide film formed on the surface of the silicon substrate is etched. Since the cleaning process is performed, the cleaning process is uniform, and the relationship between the cleaning time and the etching amount becomes linear. Therefore, the cleaning process with high reproducibility is performed, and the etching amount can be accurately controlled. Becomes
【0041】請求項4に係る湿式洗浄装置によれば、請
求項1に係る洗浄方法を的確に実施することができる。
また、請求項6に係る湿式洗浄装置によれば、請求項1
に係る洗浄方法を、より的確かつ効率良く実施すること
ができる。さらに、請求項7に係る湿式洗浄装置によれ
ば、請求項1に係る洗浄方法を、より精度良く安定して
実施することができる。According to the wet cleaning apparatus of the fourth aspect, the cleaning method of the first aspect can be accurately performed.
Further, according to the wet cleaning apparatus of the sixth aspect, the first aspect of the present invention is the first aspect.
The cleaning method according to the above can be performed more accurately and efficiently. Further, according to the wet cleaning apparatus of the seventh aspect, the cleaning method of the first aspect can be performed more accurately and stably.
【図1】本発明の実施の形態に係る湿式洗浄装置の構造
および、これによる基板洗浄方法を示す模式的説明図で
ある。FIG. 1 is a schematic explanatory view showing a structure of a wet cleaning apparatus according to an embodiment of the present invention and a method for cleaning a substrate using the wet cleaning apparatus.
【図2】本発明の洗浄方法と従来の洗浄方法とにおけ
る、半導体基板表面のシリコン酸化膜のエッチレートを
比較して示すグラフである。FIG. 2 is a graph showing a comparison between an etching rate of a silicon oxide film on the surface of a semiconductor substrate in a cleaning method of the present invention and a conventional cleaning method.
【図3】従来の洗浄方法の問題点に係るもので、洗浄液
を洗浄に使用し始めた時点からの経過時間(洗浄時間)
と、洗浄液のフッ化水素酸濃度との関係を示すグラフで
ある。FIG. 3 relates to a problem of a conventional cleaning method, and an elapsed time (cleaning time) from a time when a cleaning liquid is used for cleaning.
4 is a graph showing a relationship between the cleaning solution and the concentration of hydrofluoric acid in the cleaning solution.
【図4】図3で説明した洗浄液を使用した場合の、洗浄
時間の経過と半導体基板のエッチレートとの関係を示す
グラフである。FIG. 4 is a graph showing the relationship between the elapse of the cleaning time and the etch rate of the semiconductor substrate when the cleaning liquid described with reference to FIG. 3 is used.
【図5】従来の洗浄方法の問題点に係るもので、使用後
の洗浄液の廃液処理工程を示すフローシート、すなわち
半導体製造工程からのフッ化アンモニウム廃液の処理フ
ローである。FIG. 5 relates to the problem of the conventional cleaning method, and is a flow sheet showing a waste liquid processing step of a used cleaning liquid, that is, a processing flow of ammonium fluoride waste liquid from a semiconductor manufacturing process.
【図6】図5の廃液処理工程に係る物質収支を示す説明
図である。FIG. 6 is an explanatory diagram showing a material balance relating to the waste liquid treatment step of FIG. 5;
10…基板洗浄装置、11…洗浄ドラフト(ドラフトチ
ャンバ)、11a…周壁、12…洗浄槽、13…湿度
計、14…加湿機、15…空調機、16…除塵フィル
タ、17…排気ダクト、18…オートダンパ、19…風
速計、31…洗浄浄液。Reference Signs List 10: substrate cleaning device, 11: cleaning draft (draft chamber), 11a: peripheral wall, 12: cleaning tank, 13: hygrometer, 14: humidifier, 15: air conditioner, 16: dust filter, 17: exhaust duct, 18 ... auto damper, 19 ... anemometer, 31 ... cleaning liquid.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) H01L 21/306 H01L 21/306 J ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) H01L 21/306 H01L 21/306 J
Claims (6)
洗浄ドラフト内に設けた洗浄槽に貯留し、該洗浄液に被
洗浄基板を浸漬し、洗浄ドラフト内にクリーンエアーを
流しながら洗浄する方法において、 加湿により相対湿度を所定範囲内に制御したクリーンエ
アーを、洗浄槽の洗浄液液面に向けて鉛直方向下向きに
供給するとともに、 洗浄ドラフト内の空気を所定範囲内の排気量で排気しな
がら被洗浄基板の洗浄を行うことを特徴とする基板の湿
式洗浄方法。1. A washing solution comprising an active ingredient dissolved in water,
In a method of storing in a cleaning tank provided in a cleaning draft, immersing a substrate to be cleaned in the cleaning liquid, and cleaning while flowing clean air in the cleaning draft, clean air whose relative humidity is controlled within a predetermined range by humidification is used. Wet cleaning of a substrate, wherein the substrate to be cleaned is cleaned while supplying air downward in a vertical direction toward a cleaning liquid level of a cleaning tank and exhausting air in a cleaning draft within a predetermined range. Method.
度を常温にそれぞれ制御したクリーンエアーを供給する
ことを特徴とする請求項1に記載の基板の湿式洗浄方
法。2. The method according to claim 1, wherein clean air is supplied at a relative humidity in the range of 40% to 50% and at a normal temperature.
素酸の少なくとも一方を水に溶解したものであることを
特徴とする請求項1に記載の基板の湿式洗浄方法。3. The method for wet cleaning a substrate according to claim 1, wherein the cleaning liquid is a solution obtained by dissolving at least one of ammonium fluoride and hydrofluoric acid in water.
洗浄ドラフト内に設けた洗浄槽に貯留し、該洗浄液に被
洗浄基板を浸漬し、洗浄ドラフト内にクリーンエアーを
流しながら洗浄する装置において、 洗浄ドラフト内にクリーンエアーを洗浄槽の洗浄液液面
に向けて鉛直方向下向きに供給するクリーンエアー供給
手段と、 洗浄ドラフト内に水蒸気または霧状の水滴を供給し、該
洗浄ドラフト内のクリーンエアーの相対湿度を所定範囲
内に維持する加湿機と、 洗浄槽の洗浄液液面近傍に配置され、加湿機に連絡され
た湿度計と、 洗浄ドラフト内のエアーを排気する排気管と、 該排気管に設けた排気量制御手段と を備えてなり、 湿度計による湿度測定値を加湿機にフィードバックし
て、加湿機からの水蒸気または霧状水滴の供給量を所定
範囲内に制御し、 排気量制御手段により洗浄ドラフト内の空気を所定範囲
内の排気量で排気するようにしたことを特徴とする基板
の湿式洗浄装置。4. A washing solution obtained by dissolving an active ingredient in water,
In an apparatus that stores the cleaning target in a cleaning tank provided in the cleaning draft, immerses the substrate to be cleaned in the cleaning liquid, and flows clean air into the cleaning draft, the clean air flows into the cleaning tank to the cleaning liquid level of the cleaning tank. A clean air supply means for supplying water downward or vertically into the cleaning draft, and a humidifier for maintaining the relative humidity of the clean air in the cleaning draft within a predetermined range; A hygrometer disposed near the liquid level of the cleaning liquid in the tank and connected to a humidifier, an exhaust pipe for exhausting air in the cleaning draft, and a displacement control means provided on the exhaust pipe. The measured humidity value is fed back to the humidifier to control the supply amount of water vapor or water droplets from the humidifier within a predetermined range. Wet cleaning device for the substrate, characterized in that so as to exhaust the air in the exhaust amount in the predetermined range.
ブロワの空気吐出側に接続された除塵フィルタとからな
り、 加湿機は、水蒸気または霧状水滴を洗浄槽の洗浄液液面
に向けて鉛直方向下向きに供給するものであり、 排気量制御手段は、開度を自動調整できるダンパーと、
排気管に設けられた空気流量計または気圧計とからなる
とともに、これらの計器はダンパーに連絡され、 該計器による計測値をダンパーにフィードバックして、
その開度を制御するようにしたことを特徴とする請求項
5に記載の基板の湿式洗浄装置。5. The clean air supply means comprises a blower and a dust filter connected to the air discharge side of the blower, and the humidifier directs water vapor or atomized water droplets toward the cleaning liquid level of the cleaning tank in a vertical direction. The displacement control means includes a damper that can automatically adjust the opening,
It consists of an air flow meter or a barometer provided on the exhaust pipe, and these instruments are connected to a damper, and the measured values by the instrument are fed back to the damper,
The wet cleaning apparatus for a substrate according to claim 5, wherein the opening degree is controlled.
した水蒸気または霧状水滴を供給するものを設けるとと
もに、 洗浄液液面に向けて鉛直方向下向きに供給されるクリー
ンエアーの温度を所定範囲内に制御する空調機を設けた
ことを特徴とする請求項5または6に記載の基板の湿式
洗浄装置。6. A humidifier which supplies steam or mist-like water droplets whose temperature is controlled within a predetermined range, and controls the temperature of clean air supplied vertically downward toward the cleaning liquid level within a predetermined range. The wet cleaning apparatus for a substrate according to claim 5, wherein an air conditioner for controlling the inside is provided.
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000369632A JP4352606B2 (en) | 2000-12-05 | 2000-12-05 | Substrate wet cleaning method |
US09/985,396 US6799589B2 (en) | 2000-11-08 | 2001-11-02 | Method and apparatus for wet-cleaning substrate |
KR1020010069158A KR20020035779A (en) | 2000-11-08 | 2001-11-07 | Method and apparatus for wet-cleaning substrate |
TW090127758A TW517300B (en) | 2000-11-08 | 2001-11-08 | Method and apparatus for wet-cleaning substrate |
EP01402866A EP1205539A3 (en) | 2000-11-08 | 2001-11-08 | Method and apparatus for wet-cleaning a substrate |
US10/898,366 US6938626B2 (en) | 2000-11-08 | 2004-07-26 | Method and apparatus for wet-cleaning substrate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000369632A JP4352606B2 (en) | 2000-12-05 | 2000-12-05 | Substrate wet cleaning method |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2002172366A true JP2002172366A (en) | 2002-06-18 |
JP4352606B2 JP4352606B2 (en) | 2009-10-28 |
Family
ID=18839641
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Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2000369632A Expired - Fee Related JP4352606B2 (en) | 2000-11-08 | 2000-12-05 | Substrate wet cleaning method |
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Country | Link |
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JP (1) | JP4352606B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006216803A (en) * | 2005-02-04 | 2006-08-17 | Daikin Ind Ltd | Processing device |
JP2009059895A (en) * | 2007-08-31 | 2009-03-19 | Tokyo Electron Ltd | Liquid treatment apparatus, liquid treating method, and storage medium |
KR102646155B1 (en) * | 2022-10-05 | 2024-03-12 | 엘에스이 주식회사 | Substrate cleaning apparatus |
-
2000
- 2000-12-05 JP JP2000369632A patent/JP4352606B2/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006216803A (en) * | 2005-02-04 | 2006-08-17 | Daikin Ind Ltd | Processing device |
JP2009059895A (en) * | 2007-08-31 | 2009-03-19 | Tokyo Electron Ltd | Liquid treatment apparatus, liquid treating method, and storage medium |
US8371318B2 (en) | 2007-08-31 | 2013-02-12 | Tokyo Electron Limited | Liquid processing apparatus, liquid processing method, and storage medium |
KR102646155B1 (en) * | 2022-10-05 | 2024-03-12 | 엘에스이 주식회사 | Substrate cleaning apparatus |
Also Published As
Publication number | Publication date |
---|---|
JP4352606B2 (en) | 2009-10-28 |
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