JP2893493B2 - Silicon wafer cleaning method - Google Patents

Silicon wafer cleaning method

Info

Publication number
JP2893493B2
JP2893493B2 JP3351260A JP35126091A JP2893493B2 JP 2893493 B2 JP2893493 B2 JP 2893493B2 JP 3351260 A JP3351260 A JP 3351260A JP 35126091 A JP35126091 A JP 35126091A JP 2893493 B2 JP2893493 B2 JP 2893493B2
Authority
JP
Japan
Prior art keywords
cleaning
purifying
liquid
silicon
unit
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 - Fee Related
Application number
JP3351260A
Other languages
Japanese (ja)
Other versions
JPH05166781A (en
Inventor
悦郎 森田
次郎 龍田
真理 桜井
康 島貫
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Materials Silicon Corp
Mitsubishi Materials Corp
Original Assignee
Mitsubishi Materials Silicon Corp
Mitsubishi Materials Corp
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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、半導体シリコンウェー
ハの洗浄において、洗浄工程を簡略化し廃液処理の容易
な洗浄方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for cleaning semiconductor silicon wafers, which simplifies the cleaning process and facilitates waste liquid treatment.

【0002】[0002]

【従来技術とその課題】半導体シリコンウェーハの製造
時には種々の工程でシリコンウェーハが洗浄され、研磨
後に最終洗浄が行なわれる。一般的な洗浄工程は、(イ)
アンモニア過酸化水素水からなる洗浄液を用いてパーテ
イクル汚染の汚染源となる微粒子や有機物を洗浄除去
し、(ロ)純水でリンスした後に、(ハ)フッ酸で洗浄して
鉄、亜鉛、アルミニウム等の金属汚染物を除去し、(ニ)
純水でリンスした後に、(ホ)塩酸過酸化水素水からなる
洗浄液を用いて銅等の重金属汚染物を除去している。従
来の洗浄工程でアルカリ系洗浄と酸系洗浄を組合わせて
行なう理由は、アンモニア系洗浄では汚染源の微粒子を
洗浄除去できるもののウェーハ表面に金属不純物が付着
し易くなり金属汚染源を除去できず、また一方、酸系洗
浄は金属汚染源を除去できるものの微粒子汚染には効果
が低いためである。
2. Description of the Related Art When manufacturing a semiconductor silicon wafer, the silicon wafer is cleaned in various steps, and final polishing is performed after polishing. The general washing process is (a)
Fine particles and organic substances that are the source of particle contamination are cleaned and removed using a cleaning solution composed of aqueous ammonia hydrogen peroxide, (b) rinsed with pure water, (c) washed with hydrofluoric acid, and iron, zinc, aluminum, etc. (D)
After rinsing with pure water, (e) heavy metal contaminants such as copper are removed using a cleaning solution comprising hydrochloric acid and hydrogen peroxide solution. The reason for performing a combination of alkali-based cleaning and acid-based cleaning in the conventional cleaning process is that ammonia-based cleaning can clean and remove the fine particles of the contamination source, but metal impurities easily adhere to the wafer surface and the metal contamination source cannot be removed. On the other hand, acid-based cleaning can remove metal contamination sources, but is less effective for particulate contamination.

【0003】このように従来の洗浄工程ではアルカリ系
洗浄と酸系洗浄を組合わせて実施しているが、両工程は
相反する液質の洗浄液を用いるため、両工程を完全に分
離する必要があり設備が大型化し、かつ工程の管理も難
しいという問題がある。さらに各洗浄工程から排出され
る廃液処理も問題となっている。一方、洗浄液中の不純
物除去に関し、フッ酸洗浄液をシリコン粉末に接触させ
て液中の銅などの金属イオンをシリコン粉末に吸着させ
て精製した後に、シリコンウェーハを洗浄する方法が知
られている(特開平3-102827号)が、フッ酸によるシリコ
ンウェーハの洗浄だけでは微粒子汚染を除去することが
できない。
[0003] As described above, in the conventional cleaning process, an alkali-based cleaning and an acid-based cleaning are performed in combination. However, since both processes use cleaning liquids having contradictory qualities, it is necessary to completely separate both processes. There is a problem that equipment becomes large and process management is difficult. Further, disposal of waste liquid discharged from each washing step is also a problem. On the other hand, regarding the removal of impurities in the cleaning liquid, a method of contacting a hydrofluoric acid cleaning liquid with silicon powder, adsorbing metal ions such as copper in the liquid to the silicon powder, purifying the silicon ions, and then cleaning the silicon wafer has been known ( Japanese Unexamined Patent Publication (Kokai) No. 3-102827) cannot remove particulate contamination only by cleaning a silicon wafer with hydrofluoric acid.

【0004】[0004]

【発明の解決課題】本発明は、従来のシリコンウェーハ
洗浄における上記問題を解決した洗浄方法を提供するこ
とを目的とする。本発明においてシリコンウェーハの金
属汚染の状態を検討したところ、アンモニア過酸化水素
水による洗浄では、洗浄液中の金属不純物濃度が1ppb
程度のレベルであるときには、金属汚染を除去すること
はできず、場合によってはウェーハ表面の金属不純物濃
度が高くなるが、洗浄液中の金属不純物濃度が10ppt 以
下のレベルであるときは、酸系洗浄を行なわずにアンモ
ニア過酸化水素水の単独洗浄によっても、ウェーハ表面
の金属不純物濃度は増加せず、むしろ減少する傾向のあ
ることが見出だされた。従来、アンモニア過酸化水素水
を用いたアルカリ系洗浄だけではウェーハ表面に金属不
純物が吸着され易くなり不純物濃度は高くなると考えら
れており、上記知見はこのような従来の通念に対して予
想外のものであった。本発明は上記知見に基づき、金属
不純物濃度を10ppt以下、好ましくは1ppt以下、にした
アンモニア過酸化水素水を用いて洗浄することにより、
従来の酸系洗浄を不要にし洗浄工程を簡略化すると共に
廃液処理を容易にしたものである。
SUMMARY OF THE INVENTION An object of the present invention is to provide a cleaning method which solves the above-mentioned problems in the conventional silicon wafer cleaning. In the present invention, the state of metal contamination of the silicon wafer was examined. In the cleaning with the ammonia hydrogen peroxide solution, the metal impurity concentration in the cleaning solution was 1 ppb.
When the level is on the order of magnitude, metal contamination cannot be removed, and in some cases the concentration of metal impurities on the wafer surface will be high.However, when the concentration of metal impurities in the cleaning solution is below 10 ppt, acid-based cleaning It has been found that the concentration of metal impurities on the wafer surface does not increase but rather tends to decrease even if the aqueous ammonia peroxide solution alone is washed without performing the above. Conventionally, it has been considered that metal impurities are likely to be adsorbed on the wafer surface and the impurity concentration is increased only by alkali-based cleaning using aqueous ammonia hydrogen peroxide, and the above findings are unexpected against such conventional wisdom. Was something. The present invention is based on the above findings, by cleaning with an aqueous solution of ammonia hydrogen peroxide having a metal impurity concentration of 10 ppt or less, preferably 1 ppt or less,
This eliminates the need for conventional acid-based cleaning, simplifies the cleaning process, and facilitates waste liquid treatment.

【0005】[0005]

【課題の解決手段:発明の構成】本発明によれば、金属
不純物の濃度が10ppt以下、好ましくは1ppt以下、のア
ンモニア過酸化水素水からなる洗浄液を用いることによ
り酸系洗浄を省略したシリコンウェーハの洗浄方法が提
供される。また本発明によれば、シリコンウェーハの洗
浄系に、洗浄液を精製して該洗浄系に戻す精製循環ユニ
ットを付設し、該精製循環ユニットには金属不純物を吸
着するゲッタ用シリコンを設けた精製部と微粒子吸着用
フィルターを設けた精製部とを設け、洗浄液を洗浄系か
ら精製循環ユニットに導入し、液中の金属不純物と微粒
子を各々該ゲッタ用シリコンまたはフィルターに吸着さ
せて除去することにより金属不純物濃度を1ppt 以下に
精製し、再び洗浄系に戻してシリコンウェーハを洗浄す
る方法が提供される。更に本発明によれば、洗浄液を洗
浄槽に供給する際、該洗浄液の供給路に精製循環ユニッ
トを設け、該精製循環ユニットには金属不純物を吸着す
るゲッタ用シリコンを設けた精製部と微粒子吸着用フィ
ルターを設けた精製部とを設け、洗浄液を洗浄槽に供給
する前に予め上記精製循環ユニットに導入し、液中の金
属不純物と微粒子を各々該ゲッタ用シリコンまたはフィ
ルターに吸着させて除去することにより金属不純物濃度
を1ppt 以下に精製した後に洗浄槽に供給する洗浄方法
が提供される。
According to the present invention, according to the present invention, there is provided a silicon wafer in which an acid-based cleaning is omitted by using a cleaning solution comprising an aqueous solution of ammonium hydrogen peroxide having a metal impurity concentration of 10 ppt or less, preferably 1 ppt or less. Is provided. Further, according to the present invention, the silicon wafer cleaning system is provided with a purification circulation unit for purifying the cleaning liquid and returning the cleaning liquid to the cleaning system, and the purification circulation unit is provided with a getter silicon for absorbing metal impurities. And a purifying unit provided with a filter for adsorbing fine particles, a cleaning liquid is introduced from the cleaning system into the purifying and circulating unit, and metal impurities and fine particles in the liquid are adsorbed and removed by the silicon or filter for getter, thereby removing metal. A method for cleaning a silicon wafer by purifying an impurity concentration to 1 ppt or less and returning to a cleaning system again is provided. Further, according to the present invention, when the cleaning liquid is supplied to the cleaning tank, a purification circulation unit is provided in the supply path of the cleaning liquid, and the purification unit provided with getter silicon for adsorbing metal impurities is provided in the purification circulation unit. A purifying section provided with a filter for cleaning, a cleaning liquid is introduced into the purifying and circulating unit in advance before the cleaning liquid is supplied to the cleaning tank, and metal impurities and fine particles in the liquid are adsorbed and removed by the getter silicon or the filter, respectively. This provides a cleaning method in which the metal impurity concentration is purified to 1 ppt or less and then supplied to the cleaning tank.

【0006】アンモニア過酸化水素水[H2O:H2O2:NH4OH
=5:1:0.25、液温80℃]に金属不純物としてFeイオンを
各々 1ppt、10ppt、1ppb添加した洗浄液にシリコンウ
ェーハを10分間浸漬してウェーハを洗浄し、ウェーハ表
面に付着しているFeイオン濃度を測定したところ図1の
結果が得られた。図示するように、洗浄液のFeイオン濃
度が1ppb の場合(試料No.1)には洗浄後のウェーハ表面
のFe濃度は何れも増加しており、金属不純物を洗浄除去
する効果は認められない。一方、洗浄液のFeイオン濃度
が1ppt、10pptの場合(試料No.2,3)には洗浄後のウェー
ハ表面のFe濃度は何れも減少し、各々109(atoms/cm2)
以下、1010(atoms/cm2)以下であり洗浄効果が明らか
に認められる。従ってウェーハ表面の金属不純物濃度が
109(atoms/cm2)レベル以下の洗浄効果が求められる場
合には酸系洗浄を行なう必要がない。また微粒子汚染に
ついてみると、試料No.2,3のウェーハ表面(6インチ径)に付
着している微粒子は0.1μm以上のものが表面全体で10個
以下であり、本来の微粒子洗浄効果にも優れている。
Ammonia hydrogen peroxide solution [H 2 O: H 2 O 2 : NH 4 OH
= 5: 1: 0.25, liquid temperature of 80 ° C], the silicon wafer was immersed in a cleaning solution containing 1 ppt, 10 ppt, and 1 ppb of Fe ions as metal impurities for 10 minutes to clean the wafer, and the Fe adhering to the wafer surface was removed. When the ion concentration was measured, the result of FIG. 1 was obtained. As shown in the figure, when the Fe ion concentration of the cleaning solution is 1 ppb (Sample No. 1), the Fe concentration on the wafer surface after cleaning is increased, and the effect of cleaning and removing metal impurities is not recognized. On the other hand, when the Fe ion concentration of the cleaning solution was 1 ppt or 10 ppt (Sample Nos. 2 and 3), the Fe concentration on the wafer surface after cleaning was reduced to 10 9 (atoms / cm 2 ).
Below, it is 10 10 (atoms / cm 2 ) or less, and the cleaning effect is clearly recognized. Therefore, when a cleaning effect of a metal impurity concentration on the wafer surface of 10 9 (atoms / cm 2 ) or less is required, it is not necessary to perform acid cleaning. Looking at the particle contamination, the number of particles adhering to the wafer surface (6 inch diameter) of Sample Nos. 2 and 3 was 0.1 μm or more and 10 particles or less on the entire surface. Are better.

【0007】最近、64メカ゛以上の高集積用シリコンウェ
ーハが求められているが、この場合のウェーハ表面の金
属不純物濃度は109(atoms/cm2)程度である。本発明の
洗浄方法によれば、洗浄液として、金属不純物濃度が1
ppt以下のアンモニア過酸化水素水を用いた単独洗浄に
より目的の洗浄効果が得られ、従来のようなフッ酸や塩
酸過酸化水素水などを用いた酸系洗浄を更に行なう必要
がない。
Recently, a silicon wafer for high integration of 64 mechanisms or more has been demanded. In this case, the metal impurity concentration on the wafer surface is about 10 9 (atoms / cm 2 ). According to the cleaning method of the present invention, the cleaning liquid having a metal impurity concentration of 1
The desired cleaning effect can be obtained by single cleaning using an aqueous solution of ammonia hydrogen peroxide of ppt or less, and there is no need to further perform acid-based cleaning using hydrofluoric acid, hydrochloric acid, or hydrogen peroxide as in the related art.

【0008】本発明の洗浄方法に使用する過酸化水素水
およびアンモニア水は市販の30vol%濃度のものを使用
し、アンモニアと過酸化水素の組成は、H2O2:NH4OH=1:
0.25〜1:0.5を基準とし、水に対する過酸化水素の濃度
を5〜0.05%の範囲で調整すればよい。洗浄液の温度は5
0〜90℃が好ましい。液温が50℃より低いと洗浄時間が
長くなる。また液温が90℃より高いと薬液の分解が速く
必要な液組成を維持するのが難しくなるので好ましくな
い。洗浄時間は1〜20分程度でよい。
The hydrogen peroxide solution and the ammonia water used in the cleaning method of the present invention have a concentration of 30 vol% which is commercially available, and the composition of the ammonia and the hydrogen peroxide is H 2 O 2 : NH 4 OH = 1:
The concentration of hydrogen peroxide with respect to water may be adjusted within a range of 5 to 0.05% based on 0.25 to 1: 0.5. Cleaning solution temperature is 5
0-90 ° C is preferred. If the liquid temperature is lower than 50 ° C., the washing time becomes longer. On the other hand, when the liquid temperature is higher than 90 ° C., it is not preferable because the decomposition of the chemical liquid is quick and it becomes difficult to maintain a required liquid composition. The washing time may be about 1 to 20 minutes.

【0009】次に、本発明に係る洗浄工程の一例を図2
に示す。洗浄工程には洗浄液を供給する供給部20、洗浄
槽1、水洗槽9、乾燥部10が設けられている。供給部20に
は、アンモニア水と過酸化水素水を混合した洗浄液から
汚染金属と微粒子を除去するための精製循環ユニットA
が付設されている。更に洗浄槽1には洗浄槽から溢流し
た洗浄液を精製するための同様の精製循環ユニットBが
付設されている。これら精製循環ユニットA,Bには、
金属不純物を吸着除去するためのゲッタ用シリコンを有
するカートリッジ型の金属不純物精製部4,6と微粒子を
吸着除去するフィルターを具えた微粒子精製部5,7が設
けられている。アンモニア水と過酸化水素水は所定の濃
度比(例えばH2O2:NH4OH=1:0.5)に混合され洗浄液として
予めバッファータンク2に導入される。またバッファー
タンク2には純水が給水管路(図示せず)を通じて供給さ
れる。次いで該洗浄液は精製循環ユニットAに導入され
金属不純物と微粒子が除去される。すなわち洗浄液はゲ
ッタ用シリコンを有するカートリッジ型の精製部4およ
び微粒子吸着用フィルターを具えた精製部5を経由し弁1
1を経て再びバッファタンク2に循環される。この洗浄液
の循環は金属不純物濃度および微粒子数が設定値(例え
ば金属不純物1ppt以下、微粒子0.1μm以上のものが1個/
cc)以下になるまで繰返される。金属不純物濃度および
微粒子数が設定値以下になった洗浄液はバルブ12を開い
て洗浄槽1に供給され、シリコンウェーハの洗浄が行な
われる。洗浄槽1では、ウェーハから除去された金属不
純物や微粒子が再びウェーハ表面に付着しないように洗
浄液が精製循環ユニットBに導かれ精製される。すなわ
ち洗浄槽1から溢流した洗浄液はゲッタ用シリコンを有
するカートリッジ型の精製部6に導かれ、金属不純物が
ゲッタ用シリコンによって吸着除去された後に微粒子吸
着用フィルターを具えた精製部7に導入されここで微粒
子が除去された後に再び洗浄槽1に循環される。洗浄さ
れたシリコンウェーハは水洗槽9で純水を用いて洗浄し
た後に乾燥部10に送られる。なお精製ユニットAを設け
ずに精製ユニットBだけでも金属不純物や微粒子を設定
値以下に除去することは可能であるが、精製ユニットA
を設けた場合に比べて精製時間が長引く。上記精製循環
ユニットA,Bのゲッタ用シリコンは着脱自在に設ける
とよい。また形状は板状、粒子状ないしブロック状の何
れでもよい。ゲッタ用シリコンにはフッ酸処理して表面
の不純物濃度を109/cm2以下にしたものが用いられる。
このゲッタ用シリコンに回収した洗浄液を接触させるこ
とにより洗浄液中の鉄、亜鉛、アルミニウムなどの不純
物金属イオンがゲッタ用シリコンの表面に吸着され除去
される。
Next, an example of the cleaning step according to the present invention is shown in FIG.
Shown in In the washing step, a supply unit 20 for supplying a washing liquid, a washing tank 1, a washing tank 9, and a drying unit 10 are provided. The supply unit 20 includes a purification / circulation unit A for removing contaminant metals and fine particles from the cleaning liquid obtained by mixing the aqueous ammonia and the aqueous hydrogen peroxide.
Is attached. Further, the cleaning tank 1 is provided with a similar purification circulation unit B for purifying the cleaning liquid overflowing from the cleaning tank. These purification circulation units A and B include:
Cartridge-type metal impurity purifying units 4 and 6 having getter silicon for adsorbing and removing metal impurities and fine particle purifying units 5 and 7 including filters for adsorbing and removing fine particles are provided. The aqueous ammonia and the aqueous hydrogen peroxide are mixed at a predetermined concentration ratio (for example, H 2 O 2 : NH 4 OH = 1: 0.5) and are introduced into the buffer tank 2 in advance as a cleaning liquid. Pure water is supplied to the buffer tank 2 through a water supply pipe (not shown). Next, the cleaning liquid is introduced into the purification circulation unit A to remove metal impurities and fine particles. That is, the cleaning liquid passes through a purifying section 4 of a cartridge type having silicon for getter and a purifying section 5 provided with a filter for adsorbing fine particles, and a valve 1 is provided.
It is circulated again to the buffer tank 2 via 1. The circulation of this cleaning solution is performed at a set value of the metal impurity concentration and the number of fine particles (e.g., one metal fine particle of 1 ppt or less, fine particles of 0.1 μm or more /
cc) It is repeated until it becomes below. The cleaning liquid whose metal impurity concentration and the number of fine particles have fallen below the set values is supplied to the cleaning tank 1 by opening the valve 12, and the silicon wafer is cleaned. In the cleaning tank 1, the cleaning liquid is guided to the purification circulation unit B and purified so that the metal impurities and fine particles removed from the wafer do not adhere to the wafer surface again. That is, the cleaning liquid overflowing from the cleaning tank 1 is guided to a cartridge-type purification unit 6 having getter silicon, and is introduced into a purification unit 7 having a fine particle adsorption filter after metal impurities are adsorbed and removed by the getter silicon. Here, after the fine particles are removed, the fine particles are circulated again to the cleaning tank 1. The washed silicon wafer is washed in a washing tank 9 using pure water, and then sent to a drying unit 10. Although it is possible to remove metal impurities and fine particles below the set value by using the purification unit B alone without providing the purification unit A, the purification unit A
, The purification time is longer than that in the case where. It is preferable that the getter silicon of the purification circulation units A and B be provided detachably. The shape may be any of a plate, a particle, and a block. As the getter silicon, one whose surface has an impurity concentration of 10 9 / cm 2 or less by hydrofluoric acid treatment is used.
By bringing the collected cleaning liquid into contact with the getter silicon, impurity metal ions such as iron, zinc, and aluminum in the cleaning liquid are adsorbed on the surface of the getter silicon and removed.

【0010】[0010]

【実施例】金属不純物濃度1pptのアンモニア過酸化水
素水[H2O:H2O2:NH4OH=5:1:0.25、液温70℃]に、表面
の金属不純物濃度が Al=1011,Fe=1011atoms/cm2のシリ
コンウェーハを10分間浸漬し、ウェーハ表面を洗浄した
ところ、AlおよびFeの不純物濃度が何れも109(atoms/cm
2)に低下し優れた洗浄効果が得られた(試料No.10)。一
方、比較のため同一の金属不純物濃度を有するシリコン
ウェーハについて従来のアルカリ系洗浄と酸系洗浄を行
なった。まず、上記シリコンウェーハを従来のアルカリ
系洗浄液(H2O:H2O2:NH4OH=5:1:1)に10分間浸漬して洗浄
した(試料No.11)。更に上記アルカリ系洗浄の後にフッ
酸(H2O:HF=100:1)に1分間浸漬した後に純水でリンス
し、塩酸過酸化水素水[H2O:H2O2:HCl=5:1:1]に10分間
浸漬した後、純水でリンスした(試料No.12)。この結果
を図3に示した。図示するように、洗浄後のウェーハ表
面のFe、Al濃度は本発明の洗浄方法を行なったものに比
べて何れも高く、本発明の洗浄効果に及ばなかった。
EXAMPLE An aqueous solution of ammonia hydrogen peroxide having a metal impurity concentration of 1 ppt [H 2 O: H 2 O 2 : NH 4 OH = 5: 1: 0.25, liquid temperature 70 ° C.] and a metal impurity concentration on the surface of Al = 10 11 , a silicon wafer of Fe = 10 11 atoms / cm 2 was immersed for 10 minutes and the wafer surface was cleaned, and the impurity concentration of Al and Fe was 10 9 (atoms / cm 2).
2 ) and an excellent cleaning effect was obtained (Sample No. 10). On the other hand, for comparison, silicon wafers having the same metal impurity concentration were subjected to conventional alkaline cleaning and acid cleaning. First, the silicon wafer was immersed in a conventional alkaline cleaning solution (H 2 O: H 2 O 2 : NH 4 OH = 5: 1: 1) for 10 minutes to be cleaned (sample No. 11). Further, after the above alkaline cleaning, the substrate was immersed in hydrofluoric acid (H 2 O: HF = 100: 1) for 1 minute, rinsed with pure water, and then treated with a hydrogen peroxide solution [H 2 O: H 2 O 2 : HCl = 5. : 1: 1] for 10 minutes, and then rinsed with pure water (Sample No. 12). The result is shown in FIG. As shown in the figure, the Fe and Al concentrations on the wafer surface after cleaning were both higher than those obtained by the cleaning method of the present invention, and did not reach the cleaning effect of the present invention.

【0011】[0011]

【発明の効果】本発明の洗浄方法によれば、酸系洗浄を
行なわなくてもアンモニア過酸化水素水による単独洗浄
だけで金属汚染と微粒子汚染を効果的に除去することが
でき、洗浄工程が大幅に簡略化されると共に酸系洗浄を
行なわないので廃液処理も容易である。
According to the cleaning method of the present invention, metal contamination and fine particle contamination can be effectively removed only by single cleaning with ammonia hydrogen peroxide solution without performing acid cleaning. Since it is greatly simplified and no acid cleaning is performed, waste liquid treatment is easy.

【図面の簡単な説明】[Brief description of the drawings]

【図1】洗浄液中のFeイオン濃度と洗浄後のウェーハ表
面のFe濃度との関係を示すグラフ。
FIG. 1 is a graph showing the relationship between the Fe ion concentration in a cleaning liquid and the Fe concentration on a wafer surface after cleaning.

【図2】本発明の洗浄工程を示す概略工程図。FIG. 2 is a schematic process diagram showing a cleaning process of the present invention.

【図3】本発明の実施例と比較例の洗浄効果を示すグラ
フ。
FIG. 3 is a graph showing the cleaning effect of an example of the present invention and a comparative example.

【符号の説明】[Explanation of symbols]

1−洗浄槽、 2−バッファータンク、 4,6−金属不純物
精製部、 5,7−微粒子精製部、 9−水洗槽、10−乾燥
部、 11,12-弁、 20−供給部、A、B−精製循環ユニッ
1-washing tank, 2-buffer tank, 4,6-metal impurity purification section, 5,7-fine particle purification section, 9-water washing tank, 10-drying section, 11,12-valve, 20-supply section, A, B-Purification circulation unit

───────────────────────────────────────────────────── フロントページの続き (72)発明者 桜井 真理 埼玉県大宮市北袋町1丁目297番地 三 菱マテリアル株式会社 中央研究所内 (72)発明者 島貫 康 東京都千代田区岩本町3−8−16 三菱 マテリアルシリコン株式会社内 (56)参考文献 特開 平3−102827(JP,A) (58)調査した分野(Int.Cl.6,DB名) H01L 21/304 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Mari Sakurai 1-297 Kitabukurocho, Omiya City, Saitama Prefecture, Central Research Laboratory, Mitsubishi Materials Corporation (72) Inventor, Yasushi Shimanuki 3-8-16 Iwamotocho, Chiyoda-ku, Tokyo (56) References JP-A-3-102827 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) H01L 21/304

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 金属不純物の濃度が10ppt以下、好まし
くは1ppt以下、のアンモニア過酸化水素水からなる洗
浄液を用いることにより酸系洗浄を省略したシリコンウ
ェーハの洗浄方法。
1. A method for cleaning a silicon wafer in which an acid-based cleaning is omitted by using a cleaning solution containing an aqueous solution of ammonium hydrogen peroxide having a metal impurity concentration of 10 ppt or less, preferably 1 ppt or less.
【請求項2】 シリコンウェーハの洗浄系に、洗浄液を
精製して該洗浄系に戻す精製循環ユニットを付設し、該
精製循環ユニットには金属不純物を吸着するゲッタ用シ
リコンを設けた精製部と微粒子吸着用フィルターを設け
た精製部とを設け、洗浄液を洗浄系から精製循環ユニッ
トに導入し、液中の金属不純物と微粒子を各々該ゲッタ
用シリコンまたはフィルターに吸着させて除去すること
により金属不純物濃度を1ppt 以下に精製し、再び洗浄
系に戻してシリコンウェーハを洗浄する請求項1の洗浄
方法。
2. A purifying unit for purifying a cleaning liquid and returning the cleaning liquid to the cleaning system, wherein the purifying unit includes getter silicon for adsorbing metal impurities and fine particles. A purification unit provided with an adsorption filter is provided, a cleaning liquid is introduced from the cleaning system into the purification circulation unit, and metal impurities and fine particles in the liquid are adsorbed and removed by the getter silicon or the filter to remove the metal impurity concentration. 2. The cleaning method according to claim 1, wherein the silicon wafer is purified by purifying the silicon wafer to 1 ppt or less and returning to the cleaning system again.
【請求項3】 洗浄液を洗浄槽に供給する際、該洗浄液
の供給路に精製循環ユニットを設け、該精製循環ユニッ
トには金属不純物を吸着するゲッタ用シリコンを設けた
精製部と微粒子吸着用フィルターを設けた精製部とを設
け、洗浄液を洗浄槽に供給する前に予め上記精製循環ユ
ニットに導入し、液中の金属不純物と微粒子を各々該ゲ
ッタ用シリコンまたはフィルターに吸着させて除去する
ことにより金属不純物濃度を1ppt 以下に精製した後に
洗浄槽に供給する請求項1の洗浄方法。
3. A purifying unit provided with a purifying and circulating unit in a supply path of the cleaning liquid when supplying the cleaning liquid to the cleaning tank, wherein the purifying and circulating unit is provided with a getter silicon for adsorbing metal impurities and a filter for adsorbing fine particles. A purifying section provided with a cleaning liquid is introduced into the purifying and circulating unit before supplying the cleaning liquid to the cleaning tank, and metal impurities and fine particles in the liquid are respectively adsorbed to the getter silicon or the filter to remove them. The cleaning method according to claim 1, wherein the metal impurity is purified to a concentration of 1 ppt or less and then supplied to a cleaning tank.
JP3351260A 1991-12-13 1991-12-13 Silicon wafer cleaning method Expired - Fee Related JP2893493B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3351260A JP2893493B2 (en) 1991-12-13 1991-12-13 Silicon wafer cleaning method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3351260A JP2893493B2 (en) 1991-12-13 1991-12-13 Silicon wafer cleaning method

Publications (2)

Publication Number Publication Date
JPH05166781A JPH05166781A (en) 1993-07-02
JP2893493B2 true JP2893493B2 (en) 1999-05-24

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ID=18416118

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Country Link
JP (1) JP2893493B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3473063B2 (en) 1993-11-15 2003-12-02 松下電器産業株式会社 Cleaning method for silicon substrate
JP7186095B2 (en) * 2019-01-08 2022-12-08 東京エレクトロン株式会社 SUBSTRATE PROCESSING APPARATUS, SUBSTRATE PROCESSING METHOD, AND STORAGE MEDIUM

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62252141A (en) * 1986-04-24 1987-11-02 Kyushu Denshi Kinzoku Kk Cleanser for silicon semiconductor substrate
JP2685596B2 (en) * 1989-09-18 1997-12-03 株式会社日立製作所 Silicon wafer etching method

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