JP2001054767A - Cleaning method - Google Patents
Cleaning methodInfo
- Publication number
- JP2001054767A JP2001054767A JP11233268A JP23326899A JP2001054767A JP 2001054767 A JP2001054767 A JP 2001054767A JP 11233268 A JP11233268 A JP 11233268A JP 23326899 A JP23326899 A JP 23326899A JP 2001054767 A JP2001054767 A JP 2001054767A
- Authority
- JP
- Japan
- Prior art keywords
- ozone
- water
- dissolved
- cleaning
- cleaned
- 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.)
- Pending
Links
Landscapes
- Cleaning By Liquid Or Steam (AREA)
- Cleaning Or Drying Semiconductors (AREA)
Abstract
(57)【要約】
【課題】オゾンが有する強い酸化力を利用して、半導体
用シリコン基板、液晶用ガラス基板などの電子材料や、
高度に清浄な表面を要求される機械部品などに付着した
有機物汚染を、ウエット洗浄により効果的に除去するこ
とができる洗浄方法を提供する。
【解決手段】還元性物質の存在下に、オゾン気泡含有水
と被洗浄物とを接触させることを特徴とする洗浄方法。(57) [Summary] An electronic material such as a silicon substrate for a semiconductor and a glass substrate for a liquid crystal,
Provided is a cleaning method capable of effectively removing organic contaminants adhering to a machine part or the like requiring a highly clean surface by wet cleaning. A cleaning method includes contacting ozone-bubble-containing water with an object to be cleaned in the presence of a reducing substance.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、洗浄方法に関す
る。さらに詳しくは、本発明は、オゾンが有する強い酸
化力を利用して、半導体用シリコン基板、液晶用ガラス
基板などの電子材料や、高度に清浄な表面を要求される
機械部品などに付着した有機物汚染を、ウエット洗浄に
より効果的に除去することができる洗浄方法に関する。[0001] The present invention relates to a cleaning method. More specifically, the present invention utilizes the strong oxidizing power of ozone to apply organic substances adhering to electronic materials such as silicon substrates for semiconductors and glass substrates for liquid crystals, and mechanical parts that require highly clean surfaces. The present invention relates to a cleaning method capable of effectively removing contamination by wet cleaning.
【0002】[0002]
【従来の技術】被洗浄物表面の不純物を取り除くため
に、従来からウェット洗浄が広く行われている。除去す
べき不純物としては、微粒子、金属、有機物などがあ
り、目的に応じて適当な洗浄液、洗浄方法が採用されて
いる。このうち、空気由来の有機物やレジスト残渣のよ
うな有機物汚染を除去するためには、有機物を低分子化
して溶解させ液中に取り込む能力の高い、酸化力の強い
薬液が使われてきた。硫酸と過酸化水素水の混合液(S
PM)が、その代表的な例である。このような薬液を高
温で用いると、被洗浄物の表面に付着した有機物が酸化
されて優れた洗浄効果が得られるが、さらに近年にいた
って、薬液コストの低減や、洗浄後のリンス工程の簡略
化、排水処理の負担低減などを目的として、酸化力が強
くかつ分解によって無害な酸素に転換するオゾンを利用
したウエット洗浄技術が開発され、実用化されるように
なった。オゾン溶解水は、確かに被洗浄物表面の有機物
汚染を除去することができるが、その洗浄力は、従来な
がらの硫酸過酸化水素水混合液による洗浄には一歩を譲
るところがあった。数十mg/Lのような高濃度のオゾン
溶解水を用いると、硫酸過酸化水素水混合液に匹敵する
高い洗浄力が得られるが、このような高濃度のオゾン溶
解水は製造及び濃度の維持が容易でなく、実用性におい
て改善の必要があった。2. Description of the Related Art Conventionally, wet cleaning has been widely performed to remove impurities on the surface of an object to be cleaned. The impurities to be removed include fine particles, metals, organic substances, and the like, and an appropriate cleaning solution and cleaning method are adopted according to the purpose. Among them, in order to remove airborne organic matter and organic matter contamination such as resist residue, a chemical solution having a high ability to reduce the molecular weight of the organic matter, dissolve the organic matter, and take it into the solution has been used. A mixture of sulfuric acid and hydrogen peroxide (S
PM) is a typical example. When such a chemical is used at a high temperature, an organic substance adhered to the surface of the object to be cleaned is oxidized to obtain an excellent cleaning effect, but more recently, the cost of the chemical has been reduced, and a rinsing step after the cleaning has been required. For the purpose of simplification, reduction of the burden of wastewater treatment, and the like, wet cleaning technology using ozone that has a strong oxidizing power and is converted into harmless oxygen by decomposition has been developed and put into practical use. Ozone-dissolved water can certainly remove organic matter contamination on the surface of the object to be cleaned, but its detergency is one step further than conventional cleaning with a mixed solution of sulfuric acid and hydrogen peroxide. When high-concentration ozone-dissolved water such as tens of mg / L is used, high detergency equivalent to a mixed solution of sulfuric acid and hydrogen peroxide can be obtained, but such high-concentration ozone-dissolved water can be produced and concentrated. Maintenance was not easy and there was a need for improvement in practicality.
【0003】[0003]
【発明が解決しようとする課題】本発明は、オゾンが有
する強い酸化力を利用して、半導体用シリコン基板、液
晶用ガラス基板などの電子材料や、高度に清浄な表面を
要求される機械部品などに付着した有機物汚染を、ウエ
ット洗浄により効果的に除去することができる洗浄方法
を提供することを目的としてなされたものである。SUMMARY OF THE INVENTION The present invention utilizes the strong oxidizing power of ozone to provide electronic materials such as silicon substrates for semiconductors and glass substrates for liquid crystals, and mechanical parts that require highly clean surfaces. An object of the present invention is to provide a cleaning method capable of effectively removing organic contaminants adhering to, for example, by wet cleaning.
【0004】[0004]
【課題を解決するための手段】本発明者らは、上記の課
題を解決すべく鋭意研究を重ねた結果、還元性物質の存
在下に、オゾン気泡含有水と被洗浄物を接触させること
により、気泡からオゾンが水中に連続的に溶解して強い
酸化状態が継続し、優れた洗浄効果が得られることを見
いだし、この知見に基づいて本発明を完成するに至っ
た。すなわち、本発明は、(1)還元性物質の存在下
に、オゾン気泡含有水と被洗浄物とを接触させることを
特徴とする洗浄方法、を提供するものである。さらに、
本発明の好ましい態様として、(2)還元性物質が、過
酸化水素である第(1)項記載の洗浄方法、(3)還元性
物質を溶解した水を満たした、又は、オーバーフローさ
せた洗浄槽に被洗浄物を浸漬し、洗浄槽の下部からオゾ
ン含有ガスをバブリングさせることにより、還元性物質
の存在下にオゾン気泡含有水と被洗浄物を接触させる第
(1)項記載の洗浄方法、(4)還元性物質を溶解した水
を満たした、又は、オーバーフローさせた洗浄槽に、下
部からオゾン含有ガスをバブリングさせながら、被洗浄
物を浸漬することにより、還元性物質の存在下にオゾン
気泡含有水と被洗浄物を接触させる第(1)項記載の洗浄
方法、(5)還元性物質を溶解した水を満たした、又
は、オーバーフローさせた洗浄槽に被洗浄物を浸漬し、
オゾン含有ガスの微細な気泡を含む乳液状の流体を洗浄
槽に注入することにより、還元性物質の存在下にオゾン
気泡含有水と被洗浄物を接触させる第(1)項記載の洗浄
方法、(6)還元性物質を溶解した水を満たした、又
は、オーバーフローさせた洗浄槽に、オゾン含有ガスの
微細な気泡を含む乳液状の流体を注入し、撹拌しつつ、
洗浄槽に被洗浄物を浸漬することにより、還元性物質の
存在下にオゾン気泡含有水と被洗浄物を接触させる第
(1)項記載の洗浄方法、(7)還元性物質を溶解した水
と、オゾン含有ガスの微細な気泡を含む乳液状の流体
を、同時に被洗浄物に注ぎかけることにより、還元性物
質の存在下にオゾン気泡含有水と被洗浄物を接触させる
第(1)項記載の洗浄方法、及び、(8)還元性物質を溶
解した水と、オゾン含有ガス又はオゾン含有ガスの微細
な気泡を含む乳液状の流体の流路を合流させ、両者を混
合した直後に被洗浄物に注ぎかけることにより、還元性
物質の存在下にオゾン気泡含有水と被洗浄物を接触させ
る第(1)項記載の洗浄方法、を挙げることができる。Means for Solving the Problems The inventors of the present invention have made intensive studies to solve the above-mentioned problems, and as a result, by bringing ozone-bubble-containing water into contact with an object to be cleaned in the presence of a reducing substance. It has been found that ozone is continuously dissolved in water from bubbles to maintain a strong oxidation state and an excellent cleaning effect can be obtained, and the present invention has been completed based on this finding. That is, the present invention provides (1) a cleaning method characterized by bringing ozone bubble-containing water into contact with an object to be cleaned in the presence of a reducing substance. further,
As a preferred embodiment of the present invention, (2) the cleaning method according to (1), wherein the reducing substance is hydrogen peroxide, and (3) cleaning filled with water in which the reducing substance is dissolved or overflowed. The object to be cleaned is immersed in the tank, and the ozone-containing gas is bubbled from the lower part of the cleaning tank, whereby the ozone-bubble-containing water is brought into contact with the object to be cleaned in the presence of the reducing substance.
(1) The cleaning method described in (1), (4) by immersing the object to be cleaned while bubbling an ozone-containing gas from below into a cleaning tank filled with water in which a reducing substance is dissolved or overflowed. The cleaning method according to (1), wherein the object to be cleaned is brought into contact with the ozone-bubble-containing water in the presence of a reducing substance, (5) a cleaning tank filled or overflowed with water in which the reducing substance is dissolved. Immerse the object to be cleaned in
The cleaning method according to (1), wherein the emulsion liquid containing fine bubbles of the ozone-containing gas is injected into the cleaning tank, whereby the ozone-bubble-containing water is brought into contact with the object to be cleaned in the presence of a reducing substance. (6) An emulsion liquid containing fine bubbles of an ozone-containing gas is injected into a washing tank filled with water in which a reducing substance is dissolved or overflowed, and stirred,
By immersing the object to be cleaned in the cleaning tank, the ozone bubble-containing water is brought into contact with the object to be cleaned in the presence of the reducing substance.
(7) The washing method described in (1), (7) The water in which the reducing substance is dissolved and the milky fluid containing the fine bubbles of the ozone-containing gas are simultaneously poured onto the object to be cleaned, thereby reducing the reducing substance. The cleaning method according to (1), wherein the object to be cleaned is brought into contact with the ozone-bubble-containing water in the presence thereof, and (8) water containing a reducing substance dissolved therein and ozone-containing gas or fine bubbles of ozone-containing gas. The ozone-bubble-containing water is brought into contact with the object to be cleaned in the presence of a reducing substance by merging the flow paths of the emulsion-containing fluid and pouring the mixture immediately after mixing the two. The washing method described above can be used.
【0005】[0005]
【発明の実施の形態】本発明の洗浄方法は、還元性物質
の存在下に、オゾン気泡含有水と被洗浄物とを接触させ
るものである。本発明方法は、半導体用シリコン基板、
液晶用ガラス基板、フォトマスク用石英基板などの電子
材料や、高度に清浄な表面を要求される機械部品などの
洗浄に適用して、表面に付着した有機物汚染を効果的に
除去することができる。本発明方法に用いる還元性物質
に特に制限はなく、例えば、過酸化水素などのほか、水
素ガスなどの還元性気体、ギ酸、アルデヒド、アルコー
ルなどの有機還元性物質、ヒドラジン、硫化水素などの
無機還元性物質、次亜硫酸ナトリウム、次亜硫酸アンモ
ニウムなどの次亜硫酸塩、亜硫酸ナトリウム、亜硫酸ア
ンモニウムなどの亜硫酸塩、亜硫酸水素ナトリウム、亜
硫酸水素アンモニウムなどの亜硫酸水素塩、亜硝酸ナト
リウム、亜硝酸アンモニウムなどの亜硝酸塩などを挙げ
ることができる。過酸化水素は、通常、酸化剤として使
用されるが、酸化力の強いオゾンのような酸化剤が存在
すると還元剤としてふるまうとともに、オゾン分解触媒
としての作用も有する。過酸化水素は、一般的に電子材
料などのウェット洗浄工程で使用されており、高純度品
を容易に得ることができ、電子材料の汚染源となるおそ
れがないので特に好適に用いることができる。また、水
素ガスも副次的な汚染を生ずるおそれがなく、洗浄後の
リンスに対する負荷が小さいので、好適に用いることが
できる。BEST MODE FOR CARRYING OUT THE INVENTION The cleaning method of the present invention involves contacting water to be cleaned with ozone-bubble-containing water in the presence of a reducing substance. The method of the present invention comprises a silicon substrate for a semiconductor,
Applicable to cleaning electronic materials such as glass substrates for liquid crystal and quartz substrates for photomasks, and mechanical parts that require highly clean surfaces, and effectively removes organic contaminants adhering to the surface. . The reducing substance used in the method of the present invention is not particularly limited. For example, in addition to hydrogen peroxide and the like, reducing gases such as hydrogen gas, organic reducing substances such as formic acid, aldehyde, and alcohol, hydrazine, and inorganic substances such as hydrogen sulfide. Reducing substances, sulfites such as sodium hyposulfite and ammonium hyposulfite, sulfites such as sodium sulfite and ammonium sulfite, bisulfites such as sodium bisulfite and ammonium bisulfite, nitrites such as sodium nitrite and ammonium nitrite And the like. Hydrogen peroxide is generally used as an oxidizing agent. When an oxidizing agent such as ozone having a strong oxidizing power is present, it acts as a reducing agent and also has an action as an ozone decomposition catalyst. Hydrogen peroxide is generally used in a wet cleaning step of an electronic material or the like, and can be used particularly preferably because a high-purity product can be easily obtained and there is no possibility of becoming a contamination source of the electronic material. Also, hydrogen gas can be suitably used because there is no risk of secondary contamination and the load on the rinse after cleaning is small.
【0006】本発明方法において、還元性物質として過
酸化水素を用いる場合、過酸化水素を溶解した水として
用いることが好ましい。溶解する過酸化水素の濃度に特
に制限はないが、0.1〜50mg/Lであることが好ま
しく、1〜10mg/Lであることがより好ましい。ま
た、還元性物質として水素ガスを用いる場合は、水素ガ
ス溶解水として用いることが好ましい。水素ガス溶解水
の濃度に特に制限はないが、溶存水素ガス濃度が0.0
1mg/L以上であることが好ましく、0.1mg/L以上
であることがより好ましい。水素ガス溶解水の調製方法
に特に制限はなく、例えば、超純水への水素ガスのバブ
リング、気体透過膜を内臓したモジュールの利用などを
挙げることができる。本発明方法において、オゾン気泡
含有水の調製方法に特に制限はなく、例えば、還元性物
質を溶解した水中に散気管などを通してオゾン含有ガス
をバブリングすることにより直接オゾン気泡含有水とす
ることができ、あるいは、気体の溶解促進を目的とする
撹拌効果の高いポンプを利用し、その吸い込み側に水と
ともにオゾン含有ガスを供給することにより、オゾン含
有ガスの微細な気泡を含む乳液状の流体を得ることもで
きる。オゾン含有ガスの微細な気泡を含む乳液状の流体
のオゾン含有量に特に制限はないが、オゾン含有量とし
て0.1〜30mg/Lであることが好ましく、1〜20m
g/Lであることがより好ましい。In the method of the present invention, when hydrogen peroxide is used as a reducing substance, it is preferable to use water as a solution in which hydrogen peroxide is dissolved. There is no particular limitation on the concentration of dissolved hydrogen peroxide, but it is preferably 0.1 to 50 mg / L, more preferably 1 to 10 mg / L. When hydrogen gas is used as the reducing substance, it is preferably used as hydrogen gas dissolved water. There is no particular limitation on the concentration of the hydrogen gas-dissolved water.
It is preferably at least 1 mg / L, more preferably at least 0.1 mg / L. The method for preparing hydrogen gas-dissolved water is not particularly limited, and examples thereof include bubbling of hydrogen gas into ultrapure water and use of a module having a gas permeable membrane. In the method of the present invention, the method for preparing ozone-bubble-containing water is not particularly limited. For example, ozone-bubble-containing water can be directly obtained by bubbling an ozone-containing gas through a diffuser or the like into water in which a reducing substance is dissolved. Alternatively, by using a pump having a high stirring effect for the purpose of accelerating the dissolution of gas, and supplying the ozone-containing gas with water to the suction side thereof, an emulsion liquid containing fine bubbles of the ozone-containing gas is obtained. You can also. The ozone content of the emulsion fluid containing fine bubbles of the ozone-containing gas is not particularly limited, but the ozone content is preferably 0.1 to 30 mg / L, and 1 to 20 m / L.
More preferably, it is g / L.
【0007】本発明方法において、還元性物質の存在下
にオゾン気泡含有水と被洗浄物を接触させる方法に特に
制限はなく、例えば、還元性物質を溶解した水を満たし
た、又は、オーバーフローさせた洗浄槽に被洗浄物を浸
漬し、下部からオゾン含有ガスをバブリングさせること
ができ、あるいは、還元性物質を溶解した水を満たし
た、又は、オーバーフローさせた洗浄槽に、下部からオ
ゾン含有ガスをバブリングさせながら、被洗浄物を浸漬
することもできる。本発明方法において、オゾン含有ガ
スの微細な気泡を含む乳液状の流体を用いる場合は、還
元性物質を溶解した水を満たした、又は、オーバーフロ
ーさせた洗浄槽に被洗浄物を浸漬し、オゾン含有ガスの
微細な気泡を含む乳液状の流体を洗浄槽に注入し全体に
行き渡らせることにより、還元性物質の存在下にオゾン
気泡含有水と被洗浄物を接触させることができ、あるい
は、還元性物質を溶解した水を満たした、又は、オーバ
ーフローさせた洗浄槽に、オゾン含有ガスの微細な気泡
を含む乳液状の流体を全体に行き渡るように注入し、撹
拌しつつ、洗浄槽に被洗浄物を浸漬することにより、還
元性物質の存在下にオゾン気泡含有水と被洗浄物を接触
させることもできる。本発明方法において洗浄槽を用い
る場合は、還元性物質を溶解した水をオーバーフローさ
せることが好ましい。還元性物質を溶解した水をオーバ
ーフローさせることにより、被洗浄物の表面から除去さ
れた有機物の酸化分解物を洗浄槽外に排除して、清浄な
状態で洗浄を継続することができる。In the method of the present invention, there is no particular limitation on the method of contacting the object to be cleaned with ozone-bubble-containing water in the presence of a reducing substance. For example, the method is filled with water in which the reducing substance is dissolved or overflowed. The object to be cleaned is immersed in the cleaning tank, and the ozone-containing gas can be bubbled from the lower part, or the ozone-containing gas can be bubbled from the lower part into the cleaning tank filled with water in which the reducing substance is dissolved or overflowed. The object to be cleaned can be immersed while bubbling. In the method of the present invention, when an emulsion liquid containing fine bubbles of an ozone-containing gas is used, the object to be cleaned is immersed in a cleaning tank filled with water in which a reducing substance is dissolved, or overflowed, By injecting the emulsion liquid containing fine bubbles of the contained gas into the washing tank and spreading the whole, the water containing ozone bubbles can be brought into contact with the object to be washed in the presence of the reducing substance, or Injecting a milky fluid containing fine bubbles of ozone-containing gas into the washing tank filled with water or overflowing with water in which the active substance is dissolved, and washing the washing tank with stirring. By immersing the object, the ozone bubble-containing water can be brought into contact with the object to be cleaned in the presence of the reducing substance. When a washing tank is used in the method of the present invention, it is preferable to overflow water in which a reducing substance is dissolved. By overflowing the water in which the reducing substance is dissolved, the oxidized and decomposed products of the organic matter removed from the surface of the object to be cleaned can be eliminated outside the cleaning tank, and the cleaning can be continued in a clean state.
【0008】本発明方法は、枚葉式洗浄にも適用するこ
とができる。すなわち、枚葉式洗浄装置において、還元
性物質を溶解した水と、オゾン含有ガスの微細な気泡を
含む乳液状の流体を、同時に被洗浄物に注ぎかけること
により、還元性物質の存在下にオゾン気泡含有水と被洗
浄物を接触させることができ、あるいは、還元性物質を
溶解した水と、オゾン含有ガス又はオゾン含有ガスの微
細な気泡を含む乳液状の流体の流路をノズルなどにおい
て合流させ、両者を混合した直後に被洗浄物に注ぎかけ
ることにより、還元性物質の存在下にオゾン気泡含有水
と被洗浄物を接触させることもできる。枚葉式洗浄にお
いては、律速段階であるオゾンの水への溶解を迅速に進
めることにより高い洗浄効果を得ることができるので、
オゾン含有ガスの気泡は小さいことが好ましい。このた
めに、ポンプを利用して調製したオゾン含有ガスの微細
な気泡を含む乳液状の流体を使用する方法が特に好まし
い。本発明方法によれば、還元性物質の存在下にオゾン
気泡含有水と被洗浄物とを接触させるので、オゾンは気
泡から水中に溶解するとともに、被洗浄物の表面又はそ
の近傍で還元性物質と反応してヒドロキシラジカルなど
の活性物質を発生させ、強い酸化力を発揮する。このた
めに、オゾンの分解を洗浄に無駄なく利用することがで
きる。オゾン気泡含有水の代わりにオゾン溶解水を用い
ると、オゾンの分解が極めて急速に進むので、オゾンの
分解により発生した活性物質と被洗浄物との接触を効果
的に行うことができない。還元性物質を溶解した水中に
オゾン含有ガスの気泡が存在すると、気泡界面で進むオ
ゾンの水への溶解が、オゾンに由来する活性物質の発生
の律速段階となるので、被洗浄物の表面又はその近傍で
オゾンを分解し、活性物質を発生させることができる。[0008] The method of the present invention can also be applied to single wafer cleaning. In other words, in a single-wafer cleaning apparatus, water in which a reducing substance is dissolved and an emulsion liquid containing fine bubbles of an ozone-containing gas are simultaneously poured on the object to be cleaned, thereby reducing the presence of the reducing substance. The ozone-bubble-containing water can be brought into contact with the object to be cleaned, or the flow path of the water in which the reducing substance is dissolved and the emulsion liquid containing the ozone-containing gas or the fine bubbles of the ozone-containing gas can be passed through a nozzle or the like. It is also possible to bring the ozone-bubble-containing water into contact with the object to be cleaned in the presence of a reducing substance by allowing them to join and pouring the mixture immediately after mixing. In single-wafer cleaning, a high cleaning effect can be obtained by rapidly dissolving ozone in water, which is the rate-determining step,
The bubbles of the ozone-containing gas are preferably small. For this reason, a method using an emulsion liquid containing fine bubbles of an ozone-containing gas prepared using a pump is particularly preferable. According to the method of the present invention, the ozone-bubble-containing water is brought into contact with the object to be cleaned in the presence of the reducing substance, so that ozone dissolves in the water from the bubbles and the reducing substance is present on the surface of the object to be cleaned or in the vicinity thereof. Reacts with to generate active substances such as hydroxy radicals and exerts a strong oxidizing power. Therefore, the decomposition of ozone can be used for cleaning without waste. If ozone-dissolved water is used instead of the ozone-bubble-containing water, the decomposition of ozone proceeds very rapidly, so that the active substance generated by the decomposition of ozone and the object to be cleaned cannot be effectively contacted. If bubbles of the ozone-containing gas are present in the water in which the reducing substance is dissolved, the dissolution of ozone into the water at the bubble interface becomes the rate-determining step of the generation of the active substance derived from ozone. Ozone can be decomposed in the vicinity thereof to generate an active substance.
【0009】本発明方法において、還元性物質として過
酸化水素を用いる場合、オゾンの分解を促進するために
必要な過酸化水素の量はごく僅かでよく、例えば、10
mg/Lのオゾンを含有するオゾン気泡含有水から水中に
溶出するオゾンを迅速に分解するためには、濃度5mg/
L以下の過酸化水素水で十分である。この量は、オゾン
に対する当量以下であるが、過酸化水素はオゾンに対し
て還元剤であるばかりでなく、分解触媒としても機能す
るので、このように少ない量で十分である。必要最小限
の過酸化水素を使用した場合、本発明方法により洗浄シ
ステムから排出される排水中に残存するオゾン及び過酸
化水素の量はわずかであり、被洗浄物から除去された不
純物を除けば、酸素ガスが豊富に溶解したのみの純水で
あるために、同収及び再利用を極めて容易に行うことが
できる。なお、本発明方法においては、洗浄効果を高め
るために、酸、アルカリなどの薬液注入を行うこともで
きる。本発明方法によれば、オゾンの分解を促進する清
浄な物質と被洗浄物が共存する場で、オゾンが洗浄水に
溶解していくので、オゾンの溶解直後に発生する活性物
質による強い酸化状態が継続し、効率よく被洗浄物の表
面を洗浄して、有機物汚染を効果的に除去することがで
きる。In the method of the present invention, when hydrogen peroxide is used as the reducing substance, the amount of hydrogen peroxide required to promote the decomposition of ozone may be very small.
In order to quickly decompose ozone eluted into water from ozone bubble-containing water containing mg / L ozone, a concentration of 5 mg / L
Hydrogen peroxide solution of L or less is sufficient. Although this amount is equal to or less than the equivalent to ozone, such a small amount is sufficient because hydrogen peroxide functions not only as a reducing agent but also as a decomposition catalyst for ozone. When the minimum required amount of hydrogen peroxide is used, the amount of ozone and hydrogen peroxide remaining in the wastewater discharged from the cleaning system by the method of the present invention is small, and the amount of impurities removed from the object to be cleaned is reduced. Since it is pure water in which only oxygen gas is dissolved abundantly, the same collection and reuse can be performed very easily. In the method of the present invention, a chemical such as an acid or an alkali may be injected to enhance the cleaning effect. According to the method of the present invention, ozone is dissolved in washing water in a place where a clean substance that promotes the decomposition of ozone and an object to be cleaned coexist, so that a strong oxidation state due to an active substance generated immediately after dissolution of ozone is generated. Is continued, and the surface of the object to be cleaned is efficiently cleaned, so that organic matter contamination can be effectively removed.
【0010】[0010]
【実施例】以下に、実施例を挙げて本発明をさらに詳細
に説明するが、本発明はこれらの実施例によりなんら限
定されるものではない。なお、実施例及び比較例におい
ては、被洗浄物として、クリーンルーム内に10日間放
置して、クリーンルームエアによる有機物汚染を生じさ
せた100mm×100mmにカットしたアモルファスシリ
コン(a−Si)製膜を施したガラス基板を用いた。洗
浄効果は、ガラス基板上に滴下した超純水の接触角を接
触角計を用いて測定することにより評価した。10日間
放置して、有機物汚染を生じたガラス基板の接触角は、
51度であった。接触角が小さいことはガラス基板表面
が清浄であることを意味し、接触角が大きいことはガラ
ス基板表面が有機物で汚染されていることを意味する。 実施例1 過酸化水素5mg/Lを溶解した超純水が10L/分でオ
ーバーフローし続ける容積30Lの洗浄槽の下部から、
オゾンの供給量が100mg/分になるようにオゾン含有
ガスを散気管を用いてバブリングさせた。有機物汚染を
生じたガラス基板3枚をカセットに収納し、洗浄槽内の
オゾン含有ガスのバブルが存在する部分に浸漬し、30
秒後に取り出した。ガラス基板を乾燥したのち、超純水
の接触角を測定したところ、3枚のガラス基板の平均値
は18度であった。浸漬時間を90秒及び180秒とし
て同様に洗浄し、接触角を測定したところ、平均値はい
ずれも5度以下であった。 実施例2 超純水1Lに対して、オゾンの供給量が10mgになるよ
うにオゾン含有ガスを注入して、乳液状のオゾン気泡含
有水を連続的に調製した。容積30Lの洗浄槽に、過酸
化水素5mg/Lを溶解した超純水5L/分と上記のオゾ
ン気泡含有水5L/分を両者が混合するように供給して
オーバーフローさせた。有機物汚染を生じたガラス基板
3枚ずつをカセットに収納し、実施例1と同様にして洗
浄槽内に浸漬して、30秒、90秒及び180秒の洗浄
を行った。接触角の平均値は、浸漬時間30秒のとき1
3度、90秒と180秒のときはいずれも5度以下であ
った。 比較例1 容量30Lの洗浄槽に、溶存オゾン濃度5mg/Lのオゾ
ン溶解水を10L/分で供給し、オーバーフローさせ
た。有機物汚染を生じたガラス基板3枚ずつをカセット
に収納し、実施例1と同様にして洗浄槽内に浸漬して、
30秒、90秒及び180秒の洗浄を行った。接触角の
平均値は、浸漬時間30秒のとき30度、90秒のとき
23度、180秒のとき18度であった。 比較例2 オゾン溶解水の代わりに、過酸化水素5mg/Lを溶解し
た超純水を10L/分で供給し、比較例1と同様にして
洗浄を行った。接触角の平均値は、浸漬時間30秒のと
き47度、90秒のとき41度、180秒のとき35度
であった。 比較例3 オゾン溶解水の代わりに、実施例2と同様にして調製し
たオゾン気泡含有水を10L/分で供給し、比較例1と
同様にして洗浄を行った。接触角の平均値は、浸漬時間
30秒のとき32度、90秒のとき26度、180秒の
とき21度であった。実施例1〜2及び比較例1〜3の
結果を、第1表に示す。EXAMPLES The present invention will be described in more detail with reference to the following Examples, which should not be construed as limiting the present invention. In Examples and Comparative Examples, an amorphous silicon (a-Si) film cut into a size of 100 mm × 100 mm, which was left in a clean room for 10 days and caused organic contamination by clean room air, was applied as an object to be cleaned. A glass substrate was used. The cleaning effect was evaluated by measuring the contact angle of ultrapure water dropped on the glass substrate using a contact angle meter. After leaving for 10 days, the contact angle of the glass substrate that caused organic contamination was
It was 51 degrees. A small contact angle means that the glass substrate surface is clean, and a large contact angle means that the glass substrate surface is contaminated with organic matter. Example 1 Ultrapure water in which 5 mg / L of hydrogen peroxide was dissolved overflowed at a rate of 10 L / min.
An ozone-containing gas was bubbled using an air diffuser so that the supply amount of ozone was 100 mg / min. The three glass substrates with organic contamination were stored in a cassette, and immersed in a portion of the cleaning tank where bubbles of the ozone-containing gas existed.
Removed after seconds. After the glass substrate was dried, the contact angle of ultrapure water was measured. The average value of the three glass substrates was 18 degrees. When the immersion time was set to 90 seconds and 180 seconds for the same cleaning and the contact angle was measured, the average value was 5 degrees or less in all cases. Example 2 An ozone-containing gas was injected into 1 L of ultrapure water so that the supply amount of ozone became 10 mg, and emulsion-type ozone-bubble-containing water was continuously prepared. 5 L / min of ultrapure water in which 5 mg / L of hydrogen peroxide was dissolved and 5 L / min of the above water containing ozone bubbles were supplied to a 30 L washing tank so as to be mixed, and overflowed. Three glass substrates with organic contaminants were stored in a cassette, and immersed in a cleaning tank in the same manner as in Example 1 to perform cleaning for 30 seconds, 90 seconds, and 180 seconds. The average value of the contact angle is 1 when the immersion time is 30 seconds.
At 3 degrees, 90 seconds and 180 seconds, all were 5 degrees or less. Comparative Example 1 Ozone-dissolved water having a dissolved ozone concentration of 5 mg / L was supplied at a rate of 10 L / min to a washing tank having a capacity of 30 L to overflow. Each of the three glass substrates with organic contamination was stored in a cassette and immersed in a cleaning tank in the same manner as in Example 1.
Washing was performed for 30, 90, and 180 seconds. The average value of the contact angle was 30 degrees when the immersion time was 30 seconds, 23 degrees when the immersion time was 90 seconds, and 18 degrees when the immersion time was 180 seconds. Comparative Example 2 Instead of the ozone-dissolved water, ultrapure water in which 5 mg / L of hydrogen peroxide was dissolved was supplied at a rate of 10 L / min. The average value of the contact angle was 47 degrees when the immersion time was 30 seconds, 41 degrees when the immersion time was 90 seconds, and 35 degrees when the immersion time was 180 seconds. Comparative Example 3 Ozone-bubble-containing water prepared in the same manner as in Example 2 was supplied at 10 L / min instead of the ozone-dissolved water, and washing was performed in the same manner as in Comparative Example 1. The average value of the contact angle was 32 degrees when the immersion time was 30 seconds, 26 degrees when the immersion time was 90 seconds, and 21 degrees when the immersion time was 180 seconds. Table 1 shows the results of Examples 1 and 2 and Comparative Examples 1 to 3.
【0011】[0011]
【表1】 [Table 1]
【0012】第1表に見られるように、過酸化水素を溶
解した超純水にオゾン含有ガスをバブリングして洗浄し
た実施例1と、過酸化水素を溶解した超純水とオゾン気
泡含有水を混合して洗浄した実施例2では、90秒後に
は接触角が5度以下となり、ガラス基板の有機物汚染が
効果的に除去されている。これに対して、オゾン溶解水
のみを用いた比較例1、過酸化水素を溶解した超純水の
みを用いた比較例2及びオゾン気泡含有水のみを用いた
比較例3では、180秒後でも接触角は18〜35度で
あり、実施例に比べて有機物汚染の除去が遅い。 実施例3 有機物汚染を生じたガラス基板を枚葉式スピン洗浄機に
取りつけ、500rpmの回転速度で回転しながら、過酸
化水素5mg/Lを溶解した超純水500mL/分と、実施
例2と同様にして調製したオゾン気泡含有水500mL/
分をノズル内で混合し、ガラス基板の中心に20秒間注
ぎかけ、乾燥したのち、超純水の接触角を測定した。3
回の測定の平均値は、7度であった。洗浄時間を60
秒、120秒として、同様に接触角を測定したところ、
平均値はいずれも5度以下であった。 比較例4 洗浄水として、溶存オゾン濃度5mg/Lのオゾン溶解水
1L/分を注ぎかけた以外は、実施例3と同様にして、
有機物汚染を生じたガラス基板の洗浄を行った。接触角
の平均値は、洗浄時間20秒のとき24度、60秒のと
き18度、120秒のとき14度であった。 比較例5 洗浄水として、過酸化水素5mg/Lを溶解した超純水1
L/分を注ぎかけた以外は、実施例3と同様にして、有
機物汚染を生じたガラス基板の洗浄を行った。接触角の
平均値は、洗浄時間20秒のとき42度、60秒のとき
35度、120秒のとき29度であった。 比較例6 洗浄水として、実施例2と同様にして調製したオゾン気
泡含有水1L/分を注ぎかけた以外は、実施例3と同様
にして、有機物汚染を生じたガラス基板の洗浄を行っ
た。接触角の平均値は、洗浄時間20秒のとき26度、
60秒のとき20度、120秒のとき17度であった。
実施例3及び比較例4〜6の結果を、第2表に示す。As can be seen from Table 1, Example 1 in which an ozone-containing gas was washed by bubbling ultrapure water in which hydrogen peroxide was dissolved, ultrapure water in which hydrogen peroxide was dissolved, and water containing ozone bubbles. In Example 2 in which was mixed and washed, the contact angle became 5 degrees or less after 90 seconds, and organic contamination of the glass substrate was effectively removed. In contrast, in Comparative Example 1 using only ozone-dissolved water, Comparative Example 2 using only ultrapure water in which hydrogen peroxide was dissolved, and Comparative Example 3 using only ozone-bubble-containing water, even after 180 seconds. The contact angle is 18 to 35 degrees, and the removal of organic contamination is slower than in the example. Example 3 A glass substrate having organic contamination was attached to a single-wafer spin washer, and 500 mL / min of ultrapure water in which 5 mg / L of hydrogen peroxide was dissolved while rotating at a rotation speed of 500 rpm. Ozone bubble-containing water 500 mL /
The mixture was mixed in a nozzle, poured into the center of the glass substrate for 20 seconds, dried, and then the contact angle of ultrapure water was measured. Three
The average of the measurements was 7 degrees. 60 cleaning times
When the contact angle was measured in the same manner for 120 seconds and 120 seconds,
The average value was 5 degrees or less in all cases. Comparative Example 4 In the same manner as in Example 3, except that 1 L / min of ozone-dissolved water having a dissolved ozone concentration of 5 mg / L was poured as washing water,
The glass substrate that caused organic contamination was washed. The average value of the contact angle was 24 degrees for a cleaning time of 20 seconds, 18 degrees for 60 seconds, and 14 degrees for 120 seconds. Comparative Example 5 Ultrapure water 1 in which 5 mg / L of hydrogen peroxide was dissolved as washing water
The glass substrate that caused organic contamination was washed in the same manner as in Example 3 except that L / min was poured. The average value of the contact angle was 42 degrees for a cleaning time of 20 seconds, 35 degrees for 60 seconds, and 29 degrees for 120 seconds. Comparative Example 6 The same procedure as in Example 3 was carried out except that the ozone-bubble-containing water 1 L / min prepared in the same manner as in Example 2 was poured as the wash water, to clean the glass substrate having organic contamination. . The average value of the contact angle is 26 degrees when the cleaning time is 20 seconds,
It was 20 degrees at 60 seconds and 17 degrees at 120 seconds.
Table 2 shows the results of Example 3 and Comparative Examples 4 to 6.
【0013】[0013]
【表2】 [Table 2]
【0014】第2表に見られるように、過酸化水素を溶
解した超純水と、オゾン気泡含有水をノズル内で混合し
た直後にガラス基板に注ぎかけた実施例3では、60秒
後には接触角が5度以下となり、ガラス基板の有機物汚
染が効果的に除去されている。これに対して、オゾン溶
解水のみを用いた比較例4、過酸化水素を溶解した超純
水のみを用いた比較例5及びオゾン気泡含有水のみを用
いた比較例6では、120秒後でも接触角は14〜29
度であり、実施例に比べて有機物汚染の除去が遅い。As can be seen from Table 2, in Example 3 in which ultrapure water in which hydrogen peroxide was dissolved and water containing ozone bubbles were poured into the glass substrate immediately after mixing in the nozzle, after 60 seconds, The contact angle becomes 5 degrees or less, and organic contamination of the glass substrate is effectively removed. In contrast, in Comparative Example 4 using only ozone-dissolved water, Comparative Example 5 using only ultrapure water in which hydrogen peroxide was dissolved, and Comparative Example 6 using only ozone-bubble-containing water, even after 120 seconds. Contact angle 14-29
, And the removal of organic contaminants is slower than in the examples.
【0015】[0015]
【発明の効果】本発明の洗浄方法によれば、還元性物質
の存在下に、オゾン気泡含有水と被洗浄物を接触させる
ことにより、気泡からオゾンが水中に連続的に溶解して
強い酸化状態が継続し、優れた洗浄効果を得ることがで
き、被洗浄物の有機物汚染を効果的に除去することがで
きる。According to the cleaning method of the present invention, by contacting water to be cleaned with ozone-bubble-containing water in the presence of a reducing substance, ozone is continuously dissolved from the bubbles into the water, resulting in strong oxidation. The state is continued, an excellent cleaning effect can be obtained, and organic contamination of the object to be cleaned can be effectively removed.
Claims (1)
と被洗浄物とを接触させることを特徴とする洗浄方法。1. A cleaning method comprising bringing ozone bubble-containing water into contact with an object to be cleaned in the presence of a reducing substance.
Priority Applications (1)
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---|---|---|---|
JP11233268A JP2001054767A (en) | 1999-08-19 | 1999-08-19 | Cleaning method |
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Application Number | Priority Date | Filing Date | Title |
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JP11233268A JP2001054767A (en) | 1999-08-19 | 1999-08-19 | Cleaning method |
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Publication Number | Publication Date |
---|---|
JP2001054767A true JP2001054767A (en) | 2001-02-27 |
Family
ID=16952435
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005353824A (en) * | 2004-06-10 | 2005-12-22 | Fujitsu Ltd | Cleaning device and cleaning method for electronic device |
US8715420B2 (en) | 2009-06-03 | 2014-05-06 | Kurashiki Boseki Kabushiki Kaisha | Method for supplying hydroxyl radical-containing water and apparatus for supplying hydroxyl radical-containing water |
-
1999
- 1999-08-19 JP JP11233268A patent/JP2001054767A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005353824A (en) * | 2004-06-10 | 2005-12-22 | Fujitsu Ltd | Cleaning device and cleaning method for electronic device |
US8715420B2 (en) | 2009-06-03 | 2014-05-06 | Kurashiki Boseki Kabushiki Kaisha | Method for supplying hydroxyl radical-containing water and apparatus for supplying hydroxyl radical-containing water |
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