JP2500732B2 - Adsorbent for chemical liquid purification and method for preparing the same - Google Patents
Adsorbent for chemical liquid purification and method for preparing the sameInfo
- Publication number
- JP2500732B2 JP2500732B2 JP874093A JP874093A JP2500732B2 JP 2500732 B2 JP2500732 B2 JP 2500732B2 JP 874093 A JP874093 A JP 874093A JP 874093 A JP874093 A JP 874093A JP 2500732 B2 JP2500732 B2 JP 2500732B2
- Authority
- JP
- Japan
- Prior art keywords
- adsorbent
- hydrofluoric acid
- silicon particles
- chemical liquid
- silicon
- 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.)
- Expired - Lifetime
Links
Landscapes
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Weting (AREA)
- Cleaning Or Drying Semiconductors (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は半導体装置の製造工程で
用いられる薬液、特にフッ酸含有薬液の精製に用いる吸
着剤とその調製方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an adsorbent used for refining a chemical used in a semiconductor device manufacturing process, particularly a hydrofluoric acid-containing chemical, and a method for preparing the same.
【0002】[0002]
【従来の技術】超LSIの高集積化にともない、シリコ
ンウエハ表面の清浄化の要求は厳しくなっている。シリ
コンウエハ表面の汚染物質として、微粒子,金属,有機
物,酸化膜などがある。2. Description of the Related Art With the high integration of VLSI, the requirement for cleaning the surface of a silicon wafer has become strict. The contaminants on the surface of the silicon wafer include fine particles, metals, organic substances, oxide films and the like.
【0003】酸化膜はフッ酸含有薬液によりエッチング
除去される。この処理により酸化膜は除去できるが、フ
ッ酸含有薬液中に有害金属イオンが含有されると、ウエ
ハに付着し、電気特性に影響を与える。このためウエハ
の投入に伴い有害金属イオンが蓄積されたフッ酸含有薬
液は、精製により再生利用するかあるいは交換されなけ
ればならない。The oxide film is removed by etching with a chemical solution containing hydrofluoric acid. Although the oxide film can be removed by this treatment, if harmful metal ions are contained in the hydrofluoric acid-containing chemical solution, they adhere to the wafer and affect the electrical characteristics. Therefore, the hydrofluoric acid-containing chemical solution in which harmful metal ions are accumulated as the wafer is charged must be recycled or replaced by purification.
【0004】従来、有害金属イオンの除去法として、蒸
留法,イオン交換樹脂法及びシリコン粒子吸着法が用い
られていた。Conventionally, the distillation method, the ion exchange resin method, and the silicon particle adsorption method have been used as a method for removing harmful metal ions.
【0005】蒸留法は、蒸留後の溶液の組成比が変わる
ためフッ酸含有薬液のような混合溶液の精製には適さな
い。イオン交換樹脂法は希フッ酸にしか適用できず、高
濃度フッ酸(数10%)やフッ化アンモニウムが共存す
る薬液には適用できなかった。また、イオン交換樹脂か
らの有機物の溶出が問題になっていた。これらの問題を
解決する方法としてシリコン粒子吸着法が開発された。The distillation method is not suitable for refining a mixed solution such as a hydrofluoric acid-containing chemical solution because the composition ratio of the solution after distillation changes. The ion exchange resin method can be applied only to dilute hydrofluoric acid, and cannot be applied to a chemical solution in which high-concentration hydrofluoric acid (several 10%) and ammonium fluoride coexist. Further, the elution of organic substances from the ion exchange resin has been a problem. A silicon particle adsorption method has been developed as a method for solving these problems.
【0006】従来のシリコン粒子吸着法(特開平3−1
02827号公報)によるフッ酸含有薬液の精製法は、
フッ酸含有薬液をフッ酸含有薬液供給系に設けられたシ
リコン粒子混入フィルタを通過させ、フッ酸含有薬液中
のCuイオン等の有害金属イオンをシリコン粒子に吸着
させ除去するものである。A conventional silicon particle adsorption method (Japanese Patent Laid-Open No. 3-1
No. 02827) discloses a method for purifying a hydrofluoric acid-containing chemical solution.
The hydrofluoric acid-containing chemical liquid is passed through a silicon particle-containing filter provided in the hydrofluoric acid-containing chemical liquid supply system, and harmful metal ions such as Cu ions in the hydrofluoric acid-containing chemical liquid are adsorbed and removed by the silicon particles.
【0007】[0007]
【発明が解決しようとする課題】上述した従来のシリコ
ン粒子によるフッ酸含有薬液の精製法では、吸着材の吸
着効率(吸着速度)が低い(遅い)ために、有害金属イ
オンを要求されている低濃度レベル(0.1ppb以
下)まで除去できず、また、シリコン粒子混入フィルタ
ーに流す薬液の流速を早くすると有害金属イオンの流出
濃度が高くなるために流量を上げられないという問題が
あった。In the above-described conventional method for purifying a hydrofluoric acid-containing chemical solution using silicon particles, harmful metal ions are required because the adsorption efficiency (adsorption rate) of the adsorbent is low (slow). There was a problem that it could not be removed to a low concentration level (0.1 ppb or less), and that if the flow rate of the chemical solution flowing through the silicon particle-containing filter was increased, the outflow concentration of harmful metal ions would be high and the flow rate could not be increased.
【0008】本発明の目的は、フッ酸含有薬液の精製に
用いて半導体装置の製造プロセスで使用できる純度まで
精製が可能となる吸着剤およびその調製方法を提供する
ことにある。An object of the present invention is to provide an adsorbent which can be used for refining a hydrofluoric acid-containing chemical liquid to a purity that can be used in a semiconductor device manufacturing process, and a method for preparing the adsorbent.
【0009】[0009]
【課題を解決するための手段】前記目的を達成するため
第1の発明の薬液精製用吸着剤は、シリコン粒子を基材
とし、表面にイオン化傾向がシリコンより小さな金属を
部分的に析出させた吸着剤である。析出させる金属は特
に銀または金である。In order to achieve the above-mentioned object, the adsorbent for chemical liquid purification of the first invention uses silicon particles as a base material, and a metal having an ionization tendency smaller than that of silicon is partially deposited on the surface. It is an adsorbent. The metal to be deposited is in particular silver or gold.
【0010】第2の発明の薬液精製用吸着剤の調製方法
は、析出させる金属を所定濃度含有するフッ酸含有薬液
にシリコン粒子を浸せきし、所定時間攪拌した後該シリ
コンを純水で洗浄するものである。In the method for preparing an adsorbent for chemical liquid purification of the second invention, silicon particles are dipped in a hydrofluoric acid-containing chemical liquid containing a metal to be deposited in a predetermined concentration, and after stirring for a predetermined time, the silicon is washed with pure water. It is a thing.
【0011】[0011]
【作用】本発明の吸着剤は表面積の大きいシリコン粒子
を選び、さらにその表面にイオン化傾向がシリコンより
小さな金属を部分的に析出することにより有害金属イオ
ンの吸着速度を高めている。有害金属イオンはシリコン
粒子表面で起こる還元により析出する。シリコン粒子表
面に析出させた金属は有害金属イオンの析出を促進させ
る析出核として働いている。In the adsorbent of the present invention, silicon particles having a large surface area are selected, and a metal having an ionization tendency smaller than that of silicon is partially deposited on the surface to increase the adsorption rate of harmful metal ions. The harmful metal ions are deposited by the reduction that occurs on the surface of the silicon particles. The metal deposited on the surface of the silicon particles acts as a deposition nucleus that promotes the deposition of harmful metal ions.
【0012】[0012]
【実施例】次に本発明の実施例について説明する。図1
はシリコン粒子の表面に析出させる金属が金の場合であ
る第1の実施例を説明するための反応容器の断面図であ
る。EXAMPLES Next, examples of the present invention will be described. FIG.
FIG. 3 is a cross-sectional view of a reaction container for explaining the first embodiment in which the metal deposited on the surface of silicon particles is gold.
【0013】マグネチックスターラー1上の反応容器2
に金を0〜50ppm含有する数種類の4.9%希フッ
酸溶液3を用意する。フッ酸の濃度は0.1%以上であ
ればよい。次でこれらの溶液に粒径0.1〜1mmのシ
リコン粒子4をそれぞれ2g添加し、攪拌子5で15分
間攪拌してシリコン粒子4の表面に金を析出させた後、
純水で十分に水洗した。Reaction vessel 2 on magnetic stirrer 1
First, several kinds of 4.9% dilute hydrofluoric acid solutions 3 containing 0 to 50 ppm of gold are prepared. The concentration of hydrofluoric acid may be 0.1% or more. Next, 2 g of each silicon particle 4 having a particle size of 0.1 to 1 mm was added to these solutions, and the mixture was stirred for 15 minutes with a stirrer 5 to deposit gold on the surface of the silicon particle 4,
It was thoroughly washed with pure water.
【0014】このように調製した各々のシリコン粒子に
は、1g当たり0〜1.25mgの金が析出している。
これらのシリコン粒子2gを銅を50ppb含有する
4.9%の希フッ酸溶液に添加し攪拌した。図2にこの
時のフッ酸溶液中の銅濃度の経時変化を示す。図2より
明らかなように、シリコン粒子1g当たり0.10mg
以上の金が析出したシリコン粒子を用いると、4.9%
希フッ酸溶液中の銅を検出下限(0.02ppb)以下
まで除去できることが分かった。一方、金の析出のない
シリコン粒子では50ppbの銅は除去できないことが
分る。In each of the silicon particles thus prepared, 0 to 1.25 mg of gold is deposited per 1 g of gold.
2 g of these silicon particles were added to a 4.9% dilute hydrofluoric acid solution containing 50 ppb of copper and stirred. FIG. 2 shows the change with time of the copper concentration in the hydrofluoric acid solution at this time. As is clear from FIG. 2, 0.10 mg per 1 g of silicon particles
Using the above-mentioned silicon particles in which gold is deposited, 4.9%
It was found that copper in the dilute hydrofluoric acid solution can be removed up to the detection limit (0.02 ppb) or less. On the other hand, it can be seen that 50 ppb of copper cannot be removed with silicon particles without gold deposition.
【0015】次に第1の実施例で調製した複数種の金を
析出させたシリコン粒子2gを、銅を50ppb含有す
るフッ化アンモニウムとフッ酸の混合溶液に添加し攪拌
した。図3にこの時のフッ酸含有溶液中の銅濃度の経時
変化を示す。シリコン粒子1g当たり0.25mg以上
の金が析出したシリコン粒子を用いると、フッ酸とフッ
化アンモニウムを含む溶液中の銅を検出下限(0.02
ppb)以下まで除去できることが分かった。Next, 2 g of silicon particles prepared by depositing plural kinds of gold prepared in the first embodiment were added to a mixed solution of ammonium fluoride containing 50 ppb of copper and hydrofluoric acid and stirred. FIG. 3 shows the change with time of the copper concentration in the hydrofluoric acid-containing solution at this time. When silicon particles in which 0.25 mg or more of gold is deposited per 1 g of silicon particles are used, copper in a solution containing hydrofluoric acid and ammonium fluoride can be detected at a lower limit (0.02).
It was found that up to ppb) can be removed.
【0016】次に第2の実施例として析出させる金属が
銀の場合について説明する。尚、反応容器は図1に示し
たものを用いた。Next, the case where the metal to be deposited is silver will be described as a second embodiment. The reactor shown in FIG. 1 was used.
【0017】マグネチックスターラー1上の反応容器2
に銀を0〜50ppm含有する数種類の4.9%希フッ
酸溶液3を用意する。次でこれらの溶液にシリコン粒子
4をそれぞれ2g添加し、攪拌子5で15分間攪拌して
シリコン粒子4の表面に銀を析出させた後、純水で十分
に水洗した。Reaction vessel 2 on magnetic stirrer 1
First, several kinds of 4.9% dilute hydrofluoric acid solutions 3 containing 0 to 50 ppm of silver are prepared. Next, 2 g of each silicon particle 4 was added to these solutions, and the mixture was stirred for 15 minutes with a stirrer 5 to deposit silver on the surface of the silicon particles 4, and then thoroughly washed with pure water.
【0018】このようにして調整した各々のシリコン粒
子には、1g当たり0〜1.25mgの銀が析出してい
る。これらのシリコン粒子2gを銅を50ppb含有す
る4.9%希フッ酸溶液に添加し攪拌した。図4にこの
時のフッ酸溶液中の銅濃度の経時変化を示す。図4より
明らかなように、シリコン粒子1g当たり0.025m
g以上の銀が析出したシリコン粒子を用いると、4.9
%希フッ化水素酸溶液中の銅を検出下限(0.02pp
b)以下まで除去できることが分かった。In each of the silicon particles thus prepared, 0 to 1.25 mg of silver is deposited per 1 g of silver particles. 2 g of these silicon particles were added to a 4.9% dilute hydrofluoric acid solution containing 50 ppb of copper and stirred. FIG. 4 shows the change over time in the copper concentration in the hydrofluoric acid solution at this time. As is clear from FIG. 4, 0.025 m per 1 g of silicon particles
If silicon particles in which g or more of silver is deposited are used, 4.9
% Of copper in dilute hydrofluoric acid solution (0.02 pp
b) It was found that up to the following can be removed.
【0019】次に第2の実施例で調整した複数種の銀を
析出させたシリコン粒子2gを、銅を50ppb含有す
るフッ化アンモニウムとフッ酸の混合溶液に添加し攪拌
した。図5にこの時のフッ酸含有溶液中の銅濃度の経時
変化を示す。シリコン粒子1g当たり0.025mg以
上の銀が析出したシリコン粒子を用いると、フッ酸とフ
ッ化アンモニウムを含む溶液中の銅を検出下限(0.0
2ppb)以下まで除去できることが分った。Next, 2 g of silicon particles prepared by depositing plural kinds of silver prepared in the second embodiment were added to a mixed solution of ammonium fluoride containing 50 ppb of copper and hydrofluoric acid and stirred. FIG. 5 shows the change with time of the copper concentration in the hydrofluoric acid-containing solution at this time. When silicon particles in which 0.025 mg or more of silver is deposited per 1 g of silicon particles are used, copper in a solution containing hydrofluoric acid and ammonium fluoride can be detected at a lower limit (0.0
It was found that up to 2 ppb) or less can be removed.
【0020】尚、上記実施例においては、シリコン粒子
1gに金または銀を最大1.25mg析出させて吸着剤
を調整した場合について説明したが、析出させる金また
は銀の量は5〜10mgまでは可能である。In the above examples, the case was explained in which gold or silver was deposited at a maximum of 1.25 mg on 1 g of silicon particles to adjust the adsorbent. However, the amount of gold or silver deposited was up to 5 to 10 mg. It is possible.
【0021】[0021]
【発明の効果】以上説明したように本発明の吸着剤を用
いると、これまで精製が困難だったフッ酸含有溶液の高
純度レベルの精製(金属不純物0.1ppb以下)が可
能となった。本発明の吸着剤を用いてフッ酸含有薬液の
精製を行うことにより、薬液の再生利用ができるため、
半導体装置等のコストダウンと環境負荷の低減を行うこ
とができた。As described above, the use of the adsorbent of the present invention makes it possible to purify a hydrofluoric acid-containing solution at a high purity level (metal impurities of 0.1 ppb or less), which has been difficult to purify. By purifying the hydrofluoric acid-containing chemical liquid using the adsorbent of the present invention, the chemical liquid can be reused,
We were able to reduce the cost of semiconductor devices and the environmental load.
【図1】実施例の吸着剤調製に用いる反応容器の断面
図。FIG. 1 is a cross-sectional view of a reaction container used for preparing an adsorbent of an example.
【図2】第1の実施例の吸着剤を用いた場合の攪拌時間
と希フッ酸溶液中のCu濃度との関係を示す図。FIG. 2 is a diagram showing a relationship between a stirring time and a Cu concentration in a dilute hydrofluoric acid solution when the adsorbent of the first embodiment is used.
【図3】第1の実施例の吸着剤を用いた場合の攪拌時間
とフッ化アンモニウムとフッ酸混合溶液中のCu濃度と
の関係を示す図。FIG. 3 is a diagram showing a relationship between a stirring time and a Cu concentration in a mixed solution of ammonium fluoride and hydrofluoric acid when the adsorbent of the first embodiment is used.
【図4】第2の実施例の吸着剤を用いた場合の攪拌時間
と希フッ酸溶液中のCuの濃度との関係を示す図。FIG. 4 is a diagram showing the relationship between the stirring time and the concentration of Cu in the dilute hydrofluoric acid solution when the adsorbent of the second embodiment is used.
【図5】第2の実施例の吸着剤を用いた場合の攪拌時間
とフッ化アンモニウムとフッ酸混合溶液中のCu濃度と
の関係を示す図。FIG. 5 is a diagram showing a relationship between a stirring time and a Cu concentration in a mixed solution of ammonium fluoride and hydrofluoric acid when the adsorbent of the second embodiment is used.
1 マグネチックスターラー 2 反応容器 3 希フッ酸溶液 4 シリコン粒子 5 攪拌子 1 magnetic stirrer 2 reaction vessel 3 dilute hydrofluoric acid solution 4 silicon particles 5 stirrer
Claims (5)
部分的に析出されイオン化傾向がシリコンより小さな金
属とを含むことを特徴とする薬液精製用吸着剤。1. An adsorbent for chemical liquid purification, comprising silicon particles and a metal partially deposited on the surface of the silicon particles and having an ionization tendency smaller than that of silicon.
である請求項1記載の薬液精製用吸着剤。2. The adsorbent for chemical liquid purification according to claim 1, wherein the metal having a low ionization tendency is gold or silver.
0.1mg以上である請求項2記載の薬液精製用吸着
剤。3. The adsorbent for chemical liquid purification according to claim 2, wherein the amount of gold deposited is 0.1 mg or more per 1 g of silicon particles.
0.02mg以上である請求項2記載の薬液精製用吸着
剤。4. The adsorbent for chemical liquid purification according to claim 2, wherein the amount of precipitated silver is 0.02 mg or more per 1 g of silicon particles.
酸含有薬液にシリコン粒子を浸せきし、所定時間攪拌し
シリコン粒子の表面に金属を析出させ該シリコン粒子を
純水で洗浄することを特徴とする薬液精製用吸着剤の調
製方法。5. A method comprising immersing silicon particles in a hydrofluoric acid-containing chemical solution containing a predetermined concentration of a metal to be precipitated and stirring the solution for a predetermined time to precipitate the metal on the surface of the silicon particle and washing the silicon particle with pure water. A method for preparing an adsorbent for chemical liquid purification.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP874093A JP2500732B2 (en) | 1993-01-22 | 1993-01-22 | Adsorbent for chemical liquid purification and method for preparing the same |
US08/077,440 US5348722A (en) | 1992-06-17 | 1993-06-17 | Removal of detrimental metal ions from hydrofluoric acid solution for cleaning silicon surfaces |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP874093A JP2500732B2 (en) | 1993-01-22 | 1993-01-22 | Adsorbent for chemical liquid purification and method for preparing the same |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH06233930A JPH06233930A (en) | 1994-08-23 |
JP2500732B2 true JP2500732B2 (en) | 1996-05-29 |
Family
ID=11701348
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP874093A Expired - Lifetime JP2500732B2 (en) | 1992-06-17 | 1993-01-22 | Adsorbent for chemical liquid purification and method for preparing the same |
Country Status (1)
Country | Link |
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JP (1) | JP2500732B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP7505179B2 (en) | 2019-12-03 | 2024-06-25 | セイコーエプソン株式会社 | Liquid ejection head and liquid ejection system |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH08131821A (en) * | 1994-11-15 | 1996-05-28 | Nec Corp | Adsorbent for refining liquid chemical and its preparation |
-
1993
- 1993-01-22 JP JP874093A patent/JP2500732B2/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP7505179B2 (en) | 2019-12-03 | 2024-06-25 | セイコーエプソン株式会社 | Liquid ejection head and liquid ejection system |
Also Published As
Publication number | Publication date |
---|---|
JPH06233930A (en) | 1994-08-23 |
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