JP2000331973A - Cleaning method - Google Patents
Cleaning methodInfo
- Publication number
- JP2000331973A JP2000331973A JP11142434A JP14243499A JP2000331973A JP 2000331973 A JP2000331973 A JP 2000331973A JP 11142434 A JP11142434 A JP 11142434A JP 14243499 A JP14243499 A JP 14243499A JP 2000331973 A JP2000331973 A JP 2000331973A
- Authority
- JP
- Japan
- Prior art keywords
- cleaning
- cleaned
- oxygen gas
- cleaning solution
- ultrapure water
- 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)
- Detergent Compositions (AREA)
- Cleaning Or Drying Semiconductors (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、半導体装置、液晶
表示装置または電子部品の製造工程でなされる洗浄方法
に係り、特に、半導体ウエハや液晶ガラス基板などの基
板に付着する銅などの金属不純物を洗浄除去する洗浄方
法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cleaning method for a semiconductor device, a liquid crystal display device or an electronic component manufacturing process, and more particularly to a metal impurity such as copper adhering to a substrate such as a semiconductor wafer or a liquid crystal glass substrate. The present invention relates to a cleaning method for cleaning and removing the resin.
【0002】[0002]
【従来の技術】近年、半導体基板上に形成される半導体
デバイスは、サブミクロンのレベルに高密度化、微細化
している。2. Description of the Related Art In recent years, semiconductor devices formed on a semiconductor substrate have been increased in density and miniaturized to a submicron level.
【0003】このような高密度を達成するためには、基
板の表面は高清浄な状態に保たれていなければならな
い。すなわち、基板表面から、有機物、金属、微粒子等
は実質的に完全に除去されていなければならない。In order to achieve such a high density, the surface of the substrate must be kept in a highly clean state. That is, organic substances, metals, fine particles, and the like must be substantially completely removed from the substrate surface.
【0004】特に金属不純物は半導体デバイスの電気的
特性を劣化させるものであり、かかる劣化を防止するた
めには、半導体デバイスが形成される基板の表面におけ
る金属不純物濃度を極力低下させる必要があり、このた
め、一般に基板表面の洗浄には洗浄剤を用いることが行
われている。In particular, metal impurities degrade the electrical characteristics of a semiconductor device. To prevent such deterioration, it is necessary to reduce the metal impurity concentration on the surface of the substrate on which the semiconductor device is formed as much as possible. Therefore, a cleaning agent is generally used for cleaning the substrate surface.
【0005】基板表面の金属不純物を除去するために
は、濃塩酸、過酸化水素、超純水を体積で1:1:6乃
至1:1:4程度の比率で混合し、80〜90℃程度に
加温した溶液に浸漬後、超純水ですすぐ方法が行われて
いる。この方法によると、例えば、洗浄前に半導体基板
表面に鉄や銅等の金属不純物が付着していても、デバイ
スの性能に殆ど悪影響を与えないと考えられる1010原
子/cm2 以下の表面濃度まで除去することができると
言われている。In order to remove metal impurities on the substrate surface, concentrated hydrochloric acid, hydrogen peroxide and ultrapure water are mixed at a ratio of about 1: 1: 6 to 1: 1: 4 by volume, and the mixture is mixed at 80 to 90 ° C. After immersion in a moderately heated solution, rinsing with ultrapure water is performed. According to this method, for example, even if metal impurities such as iron and copper adhere to the surface of the semiconductor substrate before cleaning, the surface concentration of 10 10 atoms / cm 2 or less, which is considered to have almost no adverse effect on device performance. It is said that it can be removed up to.
【0006】しかしながら、上記のような方法では、過
酸化水素のように回収再利用が困難な薬品や高濃度の酸
を多量に使用するために、廃液中にこれらが排出され、
廃水処理において多くの経費を必要とする問題があっ
た。また、この方法は、高温工程を含んでいるため、薬
液の蒸気圧も高いものとなり、クリーンルーム環境を必
然的に汚染するという問題もあった。However, in the above-mentioned method, chemicals which are difficult to recover and reuse, such as hydrogen peroxide, and high-concentration acids are used in large amounts, so that these are discharged into waste liquid,
There has been a problem that wastewater treatment requires a lot of expense. In addition, since this method includes a high-temperature step, the chemical solution has a high vapor pressure, and there is a problem that the clean room environment is inevitably contaminated.
【0007】さらに、上記従来の洗浄方法では、基板表
面から一旦離脱した金属不純物が洗浄剤中に混入し、こ
の汚染された洗浄剤から金属不純物が基板に再付着す
る、逆汚染の問題もあった。Further, in the above-mentioned conventional cleaning method, there is also a problem of reverse contamination in which metal impurities once separated from the substrate surface are mixed into the cleaning agent, and the metal impurities are reattached to the substrate from the contaminated cleaning agent. Was.
【0008】[0008]
【発明が解決しようとする課題】上述したように、従来
の金属不純物を除去するための濃塩酸や過酸化水素を用
いる洗浄方法では、廃液中にこれらの成分が排出され、
廃水処理に多くの経費を必要とする上に、これらの蒸気
が発生するためクリーンルーム環境を汚染するという問
題があった。As described above, in the conventional cleaning method using concentrated hydrochloric acid or hydrogen peroxide for removing metal impurities, these components are discharged into waste liquid,
There is a problem that wastewater treatment requires a lot of expense and that the generation of these steams pollutes the clean room environment.
【0009】さらに、この方法では、除去された金属不
純物が再付着する逆汚染が生ずるという問題もあった。Further, this method has a problem that reverse contamination occurs in which the removed metal impurities are re-adhered.
【0010】本発明はかかる従来の難点を解消すべくな
されたもので、濃厚な薬品を使用しないため洗浄排水の
処理コストを低減することができ、従来より低温でも被
洗浄物表面の銅等の金属不純物を効果的に除去すること
ができ、しかも洗浄剤から基板への金属不純物の逆汚染
のない洗浄方法を提供することを目的とする。The present invention has been made in order to solve the above-mentioned conventional problems. Since a concentrated chemical is not used, it is possible to reduce the processing cost of cleaning wastewater, and even at a lower temperature than copper or the like on the surface of an object to be cleaned. It is an object of the present invention to provide a cleaning method that can effectively remove metal impurities and that does not cause reverse contamination of metal impurities from a cleaning agent to a substrate.
【0011】[0011]
【課題を解決するための手段】本発明の洗浄方法は、純
水又は超純水に5ppm以上の酸素ガスと実質的にフッ
素イオンを含まない酸を溶解させた第1の洗浄液を調製
し、この洗浄液に超音波振動を付与しつつ被洗浄物を洗
浄し、さらに、純水又は超純水に5ppm以上の酸素ガ
スとフッ酸を溶解させた第2の洗浄液を調製して前記第
1の洗浄液で洗浄した被洗浄物を洗浄することを特徴と
する。According to the cleaning method of the present invention, a first cleaning liquid is prepared by dissolving oxygen gas of 5 ppm or more and an acid substantially free of fluorine ions in pure water or ultrapure water, The object to be cleaned is cleaned while applying ultrasonic vibration to the cleaning liquid, and a second cleaning liquid in which 5 ppm or more of oxygen gas and hydrofluoric acid is dissolved in pure water or ultrapure water is prepared. The object to be cleaned which has been cleaned with the cleaning liquid is washed.
【0012】また、上記の洗浄方法において、第2の洗
浄液による第2の洗浄作業においても第2の洗浄液に超
音波振動を付与しつつ洗浄することができる。Further, in the above-mentioned cleaning method, the second cleaning liquid can be cleaned while applying ultrasonic vibration to the second cleaning liquid also in the second cleaning operation.
【0013】なお、第1の洗浄液による第1の洗浄工程
と第2の洗浄液による第2の洗浄工程の間に他の洗浄工
程が入っても差し支えない。Note that another cleaning step may be inserted between the first cleaning step using the first cleaning liquid and the second cleaning step using the second cleaning liquid.
【0014】第1の洗浄液のpHは、1以上、7未満で
あることが好ましい。It is preferable that the pH of the first cleaning liquid is 1 or more and less than 7.
【0015】また、第2の洗浄液に溶解されるフッ酸の
濃度は、0.005wt%以上、10wt%未満である
ことが好ましく、より好ましくは、0.03wt%以
上、3wt%未満である。The concentration of hydrofluoric acid dissolved in the second cleaning solution is preferably 0.005 wt% or more and less than 10 wt%, and more preferably 0.03 wt% or more and less than 3 wt%.
【0016】さらに、第1の洗浄液に対する超音波振動
の付与は、超音波の照射により行うことが好ましい。Further, it is preferable that the ultrasonic vibration is applied to the first cleaning liquid by irradiating ultrasonic waves.
【0017】なお、第2の洗浄液による第2の洗浄工程
においても、第2の洗浄液に超音波振動を与えながら洗
浄を行うことが好ましく、この場合、超音波振動は超音
波の照射により与えることがより好ましい。In the second cleaning step using the second cleaning liquid, it is preferable to perform the cleaning while applying ultrasonic vibration to the second cleaning liquid. In this case, the ultrasonic vibration is preferably applied by irradiating ultrasonic waves. Is more preferred.
【0018】なお、本明細書において「純水」とは、2
5℃換算の電気抵抗率が15.0MΩ・cm以上、TO
C濃度50ppb以下、0.2μm以上の微粒子数10
個/ml以下の清浄度の高い水をいい、「超純水」と
は、25℃換算の電気抵抗率が18.0MΩ・cm以
上、TOC濃度5ppb以下、0.05μm以上の微粒
子数10個/ml以下の清浄度の極めて高い水を言う。In this specification, “pure water” refers to 2
5 ° C conversion electric resistivity is 15.0 MΩ · cm or more, TO
Number of fine particles with C concentration of 50 ppb or less and 0.2 μm or more 10
Water having a high degree of cleanliness of particles / ml or less. “Ultra pure water” means 10 particles having an electrical resistivity of 25 ° C. or more of 18.0 MΩ · cm or more, a TOC concentration of 5 ppb or less, and 0.05 μm or more. / Extremely clean water of less than / ml.
【0019】純水又は超純水へ酸素ガスを溶解させるに
は、例えば酸素ガス透過性を有する材料からなる中空糸
の表面に酸素ガスを供給する一方、前記中空糸の内側に
純水又は超純水を供給し、気液接触により前記純水又は
超純水に酸素ガスを溶解する方法、純水又は超純水供給
ポンプの上流側に酸素ガスを供給し、ポンプ内の撹拌に
よって溶解させる方法、純水又は超純水にエジェクター
を介して酸素ガスを溶解させる方法、純水又は超純水に
酸素ガスをバブリングして溶解させる方法等を採用する
ことができる。In order to dissolve oxygen gas in pure water or ultrapure water, for example, oxygen gas is supplied to the surface of a hollow fiber made of a material having oxygen gas permeability, while pure water or ultrapure water is supplied inside the hollow fiber. A method of supplying pure water and dissolving oxygen gas in the pure water or ultrapure water by gas-liquid contact, supplying oxygen gas to the upstream side of the pure water or ultrapure water supply pump, and dissolving by stirring in the pump A method of dissolving oxygen gas in pure water or ultrapure water through an ejector, a method of dissolving oxygen gas in pure water or ultrapure water by bubbling, and the like can be employed.
【0020】第1および第2の洗浄液に溶解させる純水
又は超純水中の溶存酸素濃度は、被洗浄物表面の性状等
により適宜調整されるが、5ppm以上にすることが好
適である。より好ましくは15ppm以上、さらに好ま
しくは20ppm以上である。前記純水又は超純水中に
溶解させる溶存酸素濃度が5ppmより低くなると、被
洗浄物表面上に付着している金属不純物の除去効果が充
分に得難くなる。The concentration of dissolved oxygen in pure water or ultrapure water to be dissolved in the first and second cleaning solutions is appropriately adjusted depending on the properties of the surface of the object to be cleaned, but is preferably 5 ppm or more. It is more preferably at least 15 ppm, further preferably at least 20 ppm. When the concentration of dissolved oxygen dissolved in the pure water or ultrapure water is lower than 5 ppm, it is difficult to sufficiently obtain the effect of removing metal impurities attached to the surface of the object to be cleaned.
【0021】なお、本発明において純水又は超純水中に
酸素の他に共存ガスがあっても効果に影響はなく、特に
窒素ガスは飽和していても差し支えない。In the present invention, even if coexisting gas other than oxygen is present in pure water or ultrapure water, the effect is not affected. In particular, nitrogen gas may be saturated.
【0022】本発明に使用する酸素ガスは、水の電気分
解によって生成した酸素ガスを好ましく用いることがで
きる。このように酸素ガスとして水の電気分解によって
生成したものを使用することにより、酸素ボンベからの
酸素ガスを溶解する場合のようなボンベの交換や、ボン
ベをストックするための設置場所等の経済的な問題を解
消できるとともに、水を直接電気分解して得られる酸素
ガスが溶解されたアノード電解水のような電極からの不
純物の混入と汚染を防ぐことができる。もちろん、直近
に酸素ガス供給ラインがある場合には、その酸素ガスを
使用する方が、水の電気分解により生成した酸素ガスを
用いるより経済的である。As the oxygen gas used in the present invention, oxygen gas generated by electrolysis of water can be preferably used. The use of oxygen gas produced by electrolysis of water in this way makes it possible to replace cylinders, such as when dissolving oxygen gas from an oxygen cylinder, or to install an economical place for stocking cylinders. And the contamination of impurities such as anode electrolyzed water in which oxygen gas obtained by directly electrolyzing water is dissolved and contamination from electrodes can be prevented. Of course, if there is an oxygen gas supply line in the immediate vicinity, it is more economical to use the oxygen gas than to use the oxygen gas generated by electrolysis of water.
【0023】純水又は超純水への酸素ガスを溶解するに
あたっては、純水又は超純水供給ライン中に例えば隔膜
式の溶存酸素濃度検出器を設置し、酸素ガスの供給経路
に圧力調節弁を設け、前記検出器で純水又は超純水中の
溶存酸素濃度を検出し、これを前記圧力調節弁にフィー
ドバックすることにより前記純水又は超純水中の溶存酸
素濃度を制御するようにしてもよい。In dissolving oxygen gas in pure water or ultrapure water, for example, a dissolved oxygen concentration detector of a diaphragm type is installed in a pure water or ultrapure water supply line, and pressure is adjusted in an oxygen gas supply path. A valve is provided, and the dissolved oxygen concentration in pure water or ultrapure water is detected by the detector, and the dissolved oxygen concentration in the pure water or ultrapure water is controlled by feeding back the dissolved oxygen concentration to the pressure control valve. It may be.
【0024】第1の洗浄液中には、酸素ガスの溶解前後
に、純水又は超純水に実質的にフッ素イオンを含まない
酸を添加することによりpHが調整される。洗浄液のp
Hは被洗浄物表面の性状等により適宜調整されるが、1
以上7未満に調整することが好ましく、より好ましくは
1以上6未満、さらに好ましくは1以上5未満に調整す
る。The pH of the first cleaning solution is adjusted by adding an acid substantially free of fluorine ions to pure water or ultrapure water before and after dissolution of oxygen gas. Cleaning solution p
H is appropriately adjusted depending on the properties of the surface to be cleaned.
It is preferably adjusted to at least 7 and less than 7, more preferably at least 1 and less than 6, more preferably at least 1 and less than 5.
【0025】また、前記第1の洗浄液にフッ素イオンが
含まれないことが重要である。第1の洗浄液にフッ素イ
オンが含まれていると、被洗浄物表面より脱離した金属
不純物が再付着する、逆汚染が発生する。It is important that the first cleaning liquid does not contain fluorine ions. When the first cleaning solution contains fluorine ions, metal impurities detached from the surface of the object to be cleaned are re-adhered, and reverse contamination occurs.
【0026】本発明に使用される実質的にフッ素イオン
を含まない酸としては、塩酸、硝酸、硫酸、炭酸、蟻
酸、酢酸、過酢酸、臭素酸、過臭素酸、ヨウ素酸、過ヨ
ウ素酸等の水溶液や、塩酸ガス、炭酸ガス等のガスが例
示される。水素イオンの対イオンとして金属イオン、有
機物イオンが存在せず、対イオンが揮発性であるため、
被洗浄物表面に不純物が付着しない塩酸および塩酸ガ
ス、炭酸ガスがより好適である。The acid which does not substantially contain fluorine ions used in the present invention includes hydrochloric acid, nitric acid, sulfuric acid, carbonic acid, formic acid, acetic acid, peracetic acid, bromic acid, perbronic acid, iodic acid, periodic acid and the like. And aqueous gases of hydrochloric acid, and gases such as hydrochloric acid gas and carbon dioxide gas. Since metal ions and organic ions do not exist as counter ions of hydrogen ions and the counter ions are volatile,
Hydrochloric acid, hydrochloric acid gas, and carbon dioxide gas, which do not cause impurities to adhere to the surface of the object to be cleaned, are more preferable.
【0027】純水又は超純水への実質的にフッ素イオン
を含まない酸の溶解にあたっては、純水又は超純水供給
ライン中にpH計を設置し、添加する酸の添加量を制御
するように構成することが好ましい。In dissolving an acid substantially free of fluorine ions in pure water or ultrapure water, a pH meter is installed in a pure water or ultrapure water supply line to control the amount of acid to be added. It is preferable to configure as follows.
【0028】第2の洗浄液中には、前記酸素ガスの溶解
前後に、純水又は超純水にフッ酸が添加される。添加さ
れるフッ酸の濃度は被洗浄物表面の性状等により適宜調
整されるが0.005wt%以上、10wt%未満に調
整することが好ましく、より好ましくは0.03wt%
以上、3wt%未満、さらに好ましくは0.03wt%
以上、1wt%未満である。添加するフッ酸の濃度が
0.005wt%未満になると被洗浄物表面からの金属
不純物除去効果が十分に得られない。また、フッ酸濃度
が10wt%以上となっても、添加分に見合った金属不
純物除去効果が得られない。In the second cleaning solution, hydrofluoric acid is added to pure water or ultrapure water before and after dissolution of the oxygen gas. The concentration of the hydrofluoric acid to be added is appropriately adjusted depending on the properties of the surface of the object to be cleaned, but is preferably adjusted to 0.005% by weight or more and less than 10% by weight, more preferably 0.03% by weight.
Or more, less than 3 wt%, more preferably 0.03 wt%
Above, it is less than 1 wt%. If the concentration of the added hydrofluoric acid is less than 0.005 wt%, the effect of removing metal impurities from the surface of the object to be cleaned cannot be sufficiently obtained. Further, even when the hydrofluoric acid concentration is 10 wt% or more, the effect of removing metal impurities corresponding to the amount of addition cannot be obtained.
【0029】また、本発明において、洗浄時に超音波照
射を併用するとより効果的である。洗浄液に付与する超
音波は、30kHz以上の周波数のものが好ましく、よ
り好ましくは100kHz以上、2000kHz以下、
さらに好ましくは700kHz以上、1500kHz以
下である。In the present invention, it is more effective to use ultrasonic irradiation at the time of cleaning. The ultrasonic wave applied to the cleaning liquid preferably has a frequency of 30 kHz or more, more preferably 100 kHz or more and 2000 kHz or less,
More preferably, it is 700 kHz or more and 1500 kHz or less.
【0030】前記洗浄液に超音波振動を付与しつつ洗浄
するには、例えば、振動子が取り付けられた洗浄槽内に
供給した前記洗浄液に、被洗浄物を浸漬した状態で超音
波を照射する方法、洗浄液を被洗浄物にノズル等から供
給しながら供給液に超音波振動を付与して洗浄する方法
等が用いられる。洗浄液を被洗浄物にノズル等から供給
しながら供給液に超音波振動を付与して洗浄する後者の
方法の場合には、振動子を内蔵する洗浄液噴射ノズルに
より超音波を照射する方法、あるいは、振動子を内蔵し
たバー型の音波トランスミッタ、もしくは振動子を石英
ロッドに取り付けた音波トランスミッタより超音波を照
射する方法等が採用される。In order to perform cleaning while applying ultrasonic vibration to the cleaning liquid, for example, a method of irradiating an ultrasonic wave with the object to be cleaned immersed in the cleaning liquid supplied to a cleaning tank provided with a vibrator is used. For example, a method of applying ultrasonic vibration to a supply liquid while supplying the cleaning liquid to the object to be cleaned from a nozzle or the like and performing cleaning is used. In the case of the latter method in which the cleaning liquid is applied to the object to be cleaned from a nozzle or the like while applying the ultrasonic vibration to the supply liquid to perform cleaning, a method of irradiating ultrasonic waves with a cleaning liquid injection nozzle incorporating a vibrator, or A method of irradiating ultrasonic waves from a bar-type sound wave transmitter having a built-in vibrator or a sound wave transmitter having a vibrator mounted on a quartz rod is employed.
【0031】[0031]
【作用】一般に、金属不純物の除去に関しては、洗浄液
のpHと酸化還元電位から金属不純物の除去の条件が設
定されている。しかるに、本発明者の実験によれば、洗
浄液にシリコン酸化膜(SiO2 )を除去するための成
分であるフッ酸を添加したところ、pHと酸化還元電位
からウエハ表面の金属不純物(銅)が本来除去可能であ
るべき条件下でもほとんど除去できず、フッ酸を添加せ
ずに他の酸を用いることにより除去できたという知見を
得た。In general, conditions for removing metal impurities are set based on the pH of the cleaning solution and the oxidation-reduction potential. However, according to the experiments of the present inventor, when hydrofluoric acid, which is a component for removing the silicon oxide film (SiO 2 ), was added to the cleaning solution, the metal impurities (copper) on the wafer surface were found to have a pH and oxidation-reduction potential. It was found that it could hardly be removed even under conditions that should be able to be removed, and that it could be removed by using another acid without adding hydrofluoric acid.
【0032】本発明はかかる知見に基づいてなされたも
ので、本発明においては、5ppm以上の酸素ガスと実
質的にフッ素イオンを含まない酸を溶解させた第1の洗
浄液により金属不純物を除去され、次いで、このとき形
成される薄いシリコン酸化膜をフッ酸を溶解させた第2
の洗浄液により除去される。The present invention has been made based on this finding. In the present invention, metal impurities are removed by a first cleaning solution in which 5 ppm or more of oxygen gas and an acid substantially free of fluorine ions are dissolved. Next, the thin silicon oxide film formed at this time is
Is removed by the washing liquid.
【0033】なお、前記シリコン酸化膜が成長すると
き、洗浄液中にアルミニウムやニッケルなどの金属不純
物が存在すると、シリコン酸化膜はこれらの金属不純物
を取り込みながら成長する。第2の洗浄液は、このシリ
コン酸化膜を除去することにより、シリコン酸化膜に取
り込まれたこれらの金属不純物も除去する作用をする。When the silicon oxide film grows, if metal impurities such as aluminum and nickel are present in the cleaning solution, the silicon oxide film grows while taking in these metal impurities. By removing the silicon oxide film, the second cleaning liquid also functions to remove these metal impurities taken into the silicon oxide film.
【0034】[0034]
【発明の実施の形態】以下に、実施例を挙げて本発明を
さらに詳細に説明する。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in more detail with reference to examples.
【0035】(実施例1〜5、比較例1〜3)6インチ
のシリコンウエハ(CZn−100)をオーバーフロー
リンス法によって超純水にて1分間リンスし、次いでこ
のウエハを0.5wt%になるようにフッ酸(50%、
ELグレード、森田化学工業製)と銅イオン濃度が10
ppmになるように分析用銅標準液(Cu 1000、
関東化学製)を超純水に添加して調製した汚染液に2分
間浸漬した後、オーバーフローリンス法によって超純水
にて1分間リンスし、クリーンベンチ内にて乾燥させた
ものを強制汚染サンプルとした。(Examples 1 to 5, Comparative Examples 1 to 3) A 6-inch silicon wafer (CZn-100) was rinsed with ultrapure water for 1 minute by an overflow rinse method, and then the wafer was reduced to 0.5 wt%. Hydrofluoric acid (50%,
EL grade, manufactured by Morita Chemical Industries) and copper ion concentration of 10
ppm for analysis copper standard solution (Cu 1000,
(Kanto Chemical Co., Ltd.) was added to ultrapure water and immersed in a contaminated liquid for 2 minutes, rinsed with ultrapure water for 1 minute by the overflow rinse method, and dried in a clean bench to obtain a forced contamination sample. And
【0036】ウエハ上に付着した銅汚染量の測定には、
フッ酸気相分解−原子吸光法を使用した。強制汚染させ
たサンプルウエハ表面上の銅汚染量は、4.5×1012
原子/cm2 である。尚、洗浄液の溶存酸素濃度の測定
には、溶存酸素テストキット(K−7512、ケメット
製)、洗浄液のpH測定には、ガラス電極式pH計(E
L−9001、アプリクス製)を使用した。To measure the amount of copper contamination adhering to the wafer,
Hydrofluoric acid gas phase decomposition-atomic absorption method was used. The amount of copper contamination on the surface of the forcibly contaminated sample wafer was 4.5 × 10 12
Atoms / cm 2 . The dissolved oxygen concentration of the cleaning solution was measured by a dissolved oxygen test kit (K-7512, manufactured by Kemet), and the pH of the cleaning solution was measured by a glass electrode type pH meter (E).
L-9001, manufactured by Aplix).
【0037】(実施例1〜3)超純水にガス透過膜モジ
ュール(SEPAREL、大日本インキ化学工業製)を
介して超高純度酸素ガス(N60 Ultraox、テ
イサン製)を溶解させた後、厚さ3mmの石英バスに貯
留し、塩酸水(35%、原子吸光分析用、関東化学製)
を添加することにより第1の洗浄液を調製した。(Examples 1 to 3) Ultra-high purity oxygen gas (N60 Ultraox, manufactured by Teisan) was dissolved in ultrapure water via a gas permeable membrane module (SEPAREL, manufactured by Dainippon Ink and Chemicals, Inc.). Stored in a 3 mm quartz bath, hydrochloric acid water (35%, for atomic absorption analysis, manufactured by Kanto Chemical)
Was added to prepare a first washing solution.
【0038】この第1の洗浄液を5リットル満たした石
英バスを超音波洗浄機(950kHz、HI MEGA
ONIC 600、KAIJO製)の水を満たし底に超
音波発振子を設置したSUS製バスにセットし、強制汚
染させた前記サンプル(ウエハ)を超音波を通過させる
ために底を開放したウエハホルダーに保持させ前記石英
バスにセットして200Wの超音波出力にて10分間洗
浄した。さらに、超純水にガス透過膜モジュール(SE
PAREL、大日本インキ化学工業製)を介して超高純
度酸素ガス(N60 Ultraox、テイサン製)を
溶解させた後、別の厚さ3mmの石英バスに貯留し、フ
ッ酸(50%、ELグレード、森田化学工業製)を添加
することにより第2の洗浄液を調製した。前記第2の洗
浄液を5リットル満たした石英バスを超音波洗浄機(9
50kHz、HI MEGAONIC 600、KAI
JO製)の水を満たし底に超音波発振子を設置したSU
S製バスにセットし、第1の洗浄液により洗浄された当
該サンプルを200Wの超音波出力にて10分間洗浄し
た。A quartz bath filled with 5 liters of the first cleaning solution was placed in an ultrasonic cleaner (950 kHz, HI MEGA).
(ONIC 600, manufactured by KAIJO) is set in a SUS bath filled with water and an ultrasonic oscillator is installed on the bottom, and the forcibly contaminated sample (wafer) is placed in a wafer holder having an open bottom for transmitting ultrasonic waves. The wafer was held, set in the quartz bath, and washed with an ultrasonic output of 200 W for 10 minutes. Furthermore, a gas permeable membrane module (SE
After ultra-high purity oxygen gas (N60 Ultraox, manufactured by Teisan) is dissolved through PAREL (manufactured by Dainippon Ink and Chemicals, Inc.), the solution is stored in another 3 mm thick quartz bath, and hydrofluoric acid (50%, EL grade) , Manufactured by Morita Chemical Industry Co., Ltd.). The quartz bath filled with 5 liters of the second cleaning solution is placed in an ultrasonic cleaner (9).
50kHz, HI MEGAONIC 600, KAI
SU made of JO) filled with water and equipped with an ultrasonic oscillator at the bottom
The sample was set in an S bath, and the sample washed with the first washing liquid was washed with an ultrasonic output of 200 W for 10 minutes.
【0039】洗浄後、クリーンベンチ内にて乾燥させ、
ウエハ上に付着残留している表面銅汚染濃度を測定し
た。洗浄液の組成と表面付着銅汚染の除去率を表1に示
す。After the washing, it is dried in a clean bench,
The surface copper contamination concentration remaining on the wafer was measured. Table 1 shows the composition of the cleaning solution and the removal rate of copper contamination on the surface.
【0040】[0040]
【表1】 [Table 1]
【0041】(実施例4、5)超純水にガス透過膜モジ
ュール(SEPAREL、大日本インキ化学工業製)を
介して超高純度酸素ガス(N60 Ultraox、テ
イサン製)を溶解させた後、厚さ3mmの石英バスに貯
留し、塩酸水(35%、原子吸光分析用、関東化学製)
を添加することにより第1の洗浄液を調製した。前記第
1の洗浄液を5リットル満たした石英バスを、超音波洗
浄機(950kHz、HI MEGAONIC 60
0、KAIJO製)の水を満たし底に超音波発振子を設
置したSUS製バスにセットし、強制汚染させた前記サ
ンプル(ウエハ)を超音波を通過させるために底を開放
にしたウエハホルダーに保持させ前記石英バスにセット
して200Wの超音波出力にて10分間洗浄した。さら
に、超純水にガス透過膜モジュール(SEPAREL、
大日本インキ化学工業製)を介して超高純度酸素ガス
(N60 Ultraox、テイサン製)を溶解させた
後、別の厚さ3mmの石英バスに貯留し、フッ酸(50
%、ELグレード、森田化学工業製)を添加することに
より第2の洗浄液を調製した。(Examples 4 and 5) Ultrapure oxygen gas (N60 Ultraox, manufactured by Teisan) was dissolved in ultrapure water via a gas permeable membrane module (SEPAREL, manufactured by Dainippon Ink and Chemicals, Inc.). Stored in a 3 mm quartz bath, hydrochloric acid water (35%, for atomic absorption analysis, manufactured by Kanto Chemical)
Was added to prepare a first washing solution. A quartz bath filled with 5 liters of the first cleaning liquid is placed in an ultrasonic cleaning machine (950 kHz, HI MEGAONIC 60).
0, made by KAIJO) and set in a SUS bath with an ultrasonic oscillator installed at the bottom, and the forcedly contaminated sample (wafer) is placed in a wafer holder with an open bottom to pass ultrasonic waves. The wafer was held, set in the quartz bath, and washed with an ultrasonic output of 200 W for 10 minutes. Furthermore, a gas permeable membrane module (SEPAREL,
Ultra-high-purity oxygen gas (N60 Ultraox, manufactured by Teisan) was dissolved through Dainippon Ink and Chemicals, and then stored in another 3 mm-thick quartz bath, and hydrofluoric acid (50
%, EL grade, manufactured by Morita Chemical Industry Co., Ltd.) to prepare a second cleaning solution.
【0042】前記第2の洗浄液を5リットル満たした石
英バスに第1の洗浄液により洗浄された当該サンプルを
超音波を照射しないで10分間浸漬した。洗浄後、クリ
ーンベンチ内にて乾燥させ、ウエハ上に付着残留してい
る表面銅汚染濃度を測定した。洗浄液の組成と表面付着
銅汚染の除去率を表2に示す。The sample washed with the first cleaning solution was immersed in a quartz bath filled with 5 liters of the second cleaning solution for 10 minutes without irradiating ultrasonic waves. After the cleaning, the wafer was dried in a clean bench, and the surface copper concentration remaining on the wafer was measured. Table 2 shows the composition of the cleaning solution and the removal rate of copper contamination adhering to the surface.
【0043】[0043]
【表2】 [Table 2]
【0044】(比較例1)第1の洗浄液にアンモニア水
を添加したこと以外は実施例1と同じ条件にてウエハ洗
浄を実施した。洗浄液の組成と表面付着銅汚染の除去率
を表3に示す。Comparative Example 1 Wafer cleaning was performed under the same conditions as in Example 1 except that ammonia water was added to the first cleaning liquid. Table 3 shows the composition of the cleaning solution and the removal rate of copper contamination adhering to the surface.
【0045】(比較例2)第1の洗浄液にフッ酸を添加
したこと以外は実施例1と同じ条件にてウエハ洗浄を実
施した。洗浄液の組成と表面付着銅汚染の除去率を表3
に示す。Comparative Example 2 Wafer cleaning was performed under the same conditions as in Example 1 except that hydrofluoric acid was added to the first cleaning liquid. Table 3 shows the composition of the cleaning solution and the removal rate of copper contamination on the surface
Shown in
【0046】(比較例3)第1の洗浄液による洗浄の際
に、超音波振動を付与しないで10分間浸漬したこと以
外は実施例1と同じ条件にてウエハ洗浄を実施した。洗
浄液の組成と表面付着銅汚染の除去率を表3に示す。(Comparative Example 3) Wafer cleaning was performed under the same conditions as in Example 1 except that the substrate was immersed in the first cleaning liquid for 10 minutes without applying ultrasonic vibration. Table 3 shows the composition of the cleaning solution and the removal rate of copper contamination adhering to the surface.
【0047】[0047]
【表3】 [Table 3]
【0048】[0048]
【発明の効果】以上、詳述したように、本発明によれ
ば、純水又は超純水に5ppm以上の酸素ガスと実質的
にフッ素イオンを含まない酸を溶解させた第1の洗浄液
を調製し、この洗浄液に超音波振動を付与しつつ被洗浄
物を洗浄し、さらに、純水又は超純水に5ppm以上の
酸素ガスとフッ酸を溶解させた第2の洗浄液を調製して
前記第1の洗浄液で洗浄した被洗浄物を洗浄すること
で、廃水処理に多くの経費を要する洗浄剤を使用せず、
また常温で洗浄が行われるため溶解成分の蒸気も発生さ
せることがなく、しかも十分なレベルにまで付着金属不
純物の除去を行うことができる。As described above, according to the present invention, according to the present invention, the first cleaning liquid obtained by dissolving oxygen gas of 5 ppm or more and acid substantially free from fluorine ions in pure water or ultrapure water is used. The cleaning object is cleaned while applying ultrasonic vibration to the cleaning liquid, and a second cleaning liquid in which oxygen gas and hydrofluoric acid of 5 ppm or more are dissolved in pure water or ultrapure water is prepared. By cleaning the object to be cleaned which has been cleaned with the first cleaning liquid, it is possible to use a cleaning agent which requires a large amount of cost for wastewater treatment,
Further, since cleaning is performed at room temperature, vapor of dissolved components is not generated, and moreover, adhered metal impurities can be removed to a sufficient level.
【0049】[0049]
Claims (6)
スと実質的にフッ素イオンを含まない酸を溶解させた第
1の洗浄液を調製し、この洗浄液に超音波振動を付与し
つつ被洗浄物を洗浄し、さらに、純水又は超純水に5p
pm以上の酸素ガスとフッ酸を溶解させた第2の洗浄液
を調製して前記第1の洗浄液で洗浄した被洗浄物を洗浄
することを特徴とする基板の洗浄方法。1. A first cleaning liquid in which 5 ppm or more of oxygen gas and an acid substantially free of fluorine ions are dissolved in pure water or ultrapure water, a first cleaning liquid is prepared, and the cleaning liquid is coated while being subjected to ultrasonic vibration. Wash the object, and add 5p to pure water or ultrapure water.
A method for cleaning a substrate, comprising: preparing a second cleaning solution in which oxygen gas of not less than pm and hydrofluoric acid are dissolved, and cleaning an object to be cleaned which has been cleaned with the first cleaning solution.
スと実質的にフッ素イオンを含まない酸を溶解させた第
1の洗浄液を調製し、この洗浄液に超音波振動を付与し
つつ被洗浄物を洗浄し、さらに、純水又は超純水に5p
pm以上の酸素ガスとフッ酸を溶解させた第2の洗浄液
を調製し、この洗浄液に超音波振動を付与しつつ前記第
1の洗浄液で洗浄した被洗浄物を洗浄することを特徴と
する洗浄方法。2. A first cleaning liquid is prepared by dissolving 5 ppm or more of oxygen gas and an acid substantially free of fluorine ions in pure water or ultrapure water, and the first cleaning liquid is subjected to ultrasonic vibration while being subjected to ultrasonic vibration. Wash the object, and add 5p to pure water or ultrapure water.
a second cleaning solution prepared by dissolving an oxygen gas of at least pm or more and hydrofluoric acid therein, and cleaning the object to be cleaned which has been cleaned with the first cleaning solution while applying ultrasonic vibration to the cleaning solution. Method.
未満であることを特徴とする請求項1又は2に記載の洗
浄方法。3. The method according to claim 1, wherein the pH of the first cleaning solution is 1 or more and 7 or more.
The cleaning method according to claim 1, wherein the cleaning method is less than.
濃度が、0.005wt%以上、10wt%未満である
ことを特徴とする請求項1乃至3のいづれか1項に記載
の洗浄方法。4. The cleaning method according to claim 1, wherein the concentration of hydrofluoric acid dissolved in the second cleaning liquid is 0.005% by weight or more and less than 10% by weight. .
ら、前記被洗浄物を洗浄することを特徴とする請求項1
乃至4のいずれか1項に記載の洗浄方法。5. The apparatus according to claim 1, wherein the object to be cleaned is cleaned while irradiating the first cleaning liquid with ultrasonic waves.
The cleaning method according to any one of claims 1 to 4.
ら、前記被洗浄物を洗浄することを特徴とする請求項2
乃至5のいずれか1項に記載の洗浄方法。6. The object to be cleaned is cleaned while irradiating the second cleaning liquid with ultrasonic waves.
The cleaning method according to any one of claims 1 to 5.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11142434A JP2000331973A (en) | 1999-05-21 | 1999-05-21 | Cleaning method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11142434A JP2000331973A (en) | 1999-05-21 | 1999-05-21 | Cleaning method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2000331973A true JP2000331973A (en) | 2000-11-30 |
Family
ID=15315233
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11142434A Pending JP2000331973A (en) | 1999-05-21 | 1999-05-21 | Cleaning method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2000331973A (en) |
-
1999
- 1999-05-21 JP JP11142434A patent/JP2000331973A/en active Pending
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