JPH03261128A - Method of removing organic hardening film - Google Patents
Method of removing organic hardening filmInfo
- Publication number
- JPH03261128A JPH03261128A JP2059419A JP5941990A JPH03261128A JP H03261128 A JPH03261128 A JP H03261128A JP 2059419 A JP2059419 A JP 2059419A JP 5941990 A JP5941990 A JP 5941990A JP H03261128 A JPH03261128 A JP H03261128A
- Authority
- JP
- Japan
- Prior art keywords
- organic
- substrate
- gas
- supercritical
- carbon dioxide
- 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
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- Photosensitive Polymer And Photoresist Processing (AREA)
- Exposure Of Semiconductors, Excluding Electron Or Ion Beam Exposure (AREA)
Abstract
Description
【発明の詳細な説明】
廉栗圭立剋里光互
本発明は、有機硬化膜が形成されている基板からその有
機硬化膜を除去する方法に関し、特に、ホトレジスト膜
を形成した半導体ウェハーから有機剥離剤を用いて、そ
の有機硬化膜を剥離した後、その半導体ウェハーに付着
残存している上記剥離剤、有機硬化膜の剥離残渣及びそ
の他の汚染物質を洗浄除去する方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for removing an organic cured film from a substrate on which the organic cured film is formed, and in particular to a method for removing an organic cured film from a semiconductor wafer on which a photoresist film is formed. The present invention relates to a method for removing the above-mentioned peeling agent, peeling residue of the organic cured film, and other contaminants remaining on the semiconductor wafer after peeling off the organic cured film using a method.
藍来坐致歪
標準的なLSIの製造においては、シリコン単結晶板上
にSiO□、SiJいアルミニウム等からなる薄膜が形
成された後、その表面にホトレジストが塗布されて、リ
ソグラフィー、エツチング等の工程を経て、薄膜上に所
定のパターンが形成され、次いで、上記ホトレジスト膜
が剥離除去され、清浄にされて後、不純物が導入される
。In the production of standard LSIs, a thin film of SiO□, SiJ, aluminum, etc. is formed on a silicon single crystal plate, and then a photoresist is applied to the surface and subjected to lithography, etching, etc. Through the process, a predetermined pattern is formed on the thin film, and then the photoresist film is peeled off and cleaned, and then impurities are introduced.
上記ホトレジスト膜を除去するには、従来、例えば、熱
硫酸、硫酸又は過酸化水素のような強力な酸化剤にてホ
トレジスト膜を溶解させる方法が知られている。しかし
、かかる方法によれば、ウェハー表面に破損や損傷を与
えたり、或いは剥離剤である酸化剤中にホトレジスト膜
成分が溶解するために、剥離剤としての効力が薄れ、剥
離剤の寿命が短くなるほか、再使用が困難である等の問
題を有する。また、ホトレジスト膜の下地材料を侵すお
それもある。In order to remove the photoresist film, a method is conventionally known in which the photoresist film is dissolved using a strong oxidizing agent such as hot sulfuric acid, sulfuric acid, or hydrogen peroxide. However, this method causes damage or breakage to the wafer surface, or dissolves photoresist film components in the oxidizing agent, which is the stripping agent, reducing its effectiveness as a stripping agent and shortening the life of the stripping agent. In addition, it has problems such as difficulty in reusing it. Furthermore, there is a possibility that the underlying material of the photoresist film may be attacked.
そこで、ホトレジスト膜の下地材料の耐薬品性を考慮し
て、フェノール系有機溶剤やハロゲン系有機溶剤を剥離
剤として用いて、下地材料を侵すことなく、ホトレジス
ト膜を剥離除去する方法も知られている。しかし、この
ように、有機剥離剤を用いる方法は、有機溶剤によって
は、毒性を有するために、安全衛生上、好ましくなく、
更に、環境保全対策のために、多大の費用を必要とする
。Therefore, in consideration of the chemical resistance of the underlying material of the photoresist film, a method is known in which a phenolic organic solvent or a halogenated organic solvent is used as a stripper to remove the photoresist film without damaging the underlying material. There is. However, this method of using an organic stripper is unfavorable from a safety and health standpoint because some organic solvents are toxic.
Furthermore, a large amount of cost is required for environmental protection measures.
他方、近年、石英結晶やポリイミド等の固体重合体を含
む固体物品の表面を洗浄する方法として、特許出願公表
昭和59年502137号公報には、このような固体物
品の表面に炭酸ガスのような超臨界ガスを接触させて、
表面を洗浄する方法が提案されており、更に、特開昭6
0−192333号公報には、ホトレジスト膜が形成さ
れた半導体ウェハーに液化ガス又は超臨界ガスを接触さ
せた後、上記ガスの温度や圧力条件を変動させ、ガスを
膨張させて、その膨張力を利用して、ホトレジスト膜を
半導体ウェハーから剥離除去する方法も提案されている
。しかし、このような方法では、ホトレジスト膜の剥離
除去に長時間を要するのみならず、ホトレジスト膜が完
全に剥離されず、得られる素子の特性に有害な影響を与
え、また、その歩留りを低下させる。On the other hand, in recent years, as a method for cleaning the surfaces of solid articles containing solid polymers such as quartz crystals and polyimide, Patent Application Publication No. 502137 of 1981 describes a method of cleaning the surfaces of solid articles such as carbon dioxide gas on the surfaces of such solid articles. By contacting supercritical gas,
A method of cleaning the surface has been proposed, and furthermore,
0-192333 discloses that after a semiconductor wafer on which a photoresist film is formed is brought into contact with a liquefied gas or a supercritical gas, the temperature and pressure conditions of the gas are varied to expand the gas and reduce its expansion force. A method has also been proposed in which a photoresist film is peeled off and removed from a semiconductor wafer. However, with this method, not only does it take a long time to remove the photoresist film, but the photoresist film is not completely removed, which has a detrimental effect on the characteristics of the resulting device, and also reduces its yield. .
が”′ しようとする1
本発明は、基板上に形成された有機硬化膜、特に、半導
体ウェハー上に形成されたホトレジスト膜の従来の剥離
除去方法における上記した問題を解決するためになされ
たものであって、基板から有機硬化膜を短時間で容易に
完全に除去する方法を提供することを目的とする。The present invention has been made to solve the above-mentioned problems in the conventional peeling and removal method of organic cured films formed on substrates, especially photoresist films formed on semiconductor wafers. The object of the present invention is to provide a method for easily and completely removing an organic cured film from a substrate in a short time.
9 を解゛するための
本発明による有機硬化膜の除去方法は、有機硬化膜が形
成された基板を有機@離削に浸漬して、上記有機硬化膜
を基板から剥離し、次いで、液化ガス又は亜臨界状態を
含む超臨界ガスに上記基板を接触させて、基板に付着し
ている上記剥離剤、有機硬化膜の剥離残渣及びその他の
汚染物質を除去することを特徴とする。9, the method for removing an organic cured film according to the present invention is to immerse the substrate on which the organic cured film is formed in an organic @exfoliation solution to peel off the organic cured film from the substrate, and then to remove the organic cured film from the substrate using liquefied gas. Alternatively, the substrate is brought into contact with a supercritical gas containing a subcritical state to remove the stripping agent, peeling residue of the organic cured film, and other contaminants adhering to the substrate.
本発明において、亜臨界ガスとは、圧力−温度状態図に
おいて臨界点付近の状態にあるガスをいい、この領域で
は、ガスは、物性的に不安定な状態であるので、超臨界
ガスとは区別される。In the present invention, a subcritical gas refers to a gas in a state near the critical point in a pressure-temperature phase diagram, and since the gas is physically unstable in this region, it is not a supercritical gas. distinguished.
超臨界ガスとは、圧力−温度状態図において、臨界温度
以上であって、且つ、臨界圧力以上の状態にあるガスを
いい、この状態においては、僅かな圧力変化や温度変化
によって、密度が大きく変化し、それが物質の溶解能に
大きく影響するところから、本発明においては、特に、
超臨界ガスが好ましく用いられる。A supercritical gas is a gas in a state where the temperature is above the critical temperature and the pressure is above the critical pressure in the pressure-temperature phase diagram. In this state, the density increases due to a slight change in pressure or temperature. In the present invention, in particular, since it greatly affects the dissolution ability of substances,
Supercritical gas is preferably used.
液化ガスとは、圧力−温度状態図において、飽和蒸気圧
線以上の圧力状態にあって、大気圧下での通常の温度条
件では、ガス状であるものをいう。Liquefied gas refers to gas that is in a pressure state equal to or higher than the saturated vapor pressure line in a pressure-temperature phase diagram and is gaseous under normal temperature conditions under atmospheric pressure.
本発明において、液化ガス又は亜臨界状態を含む超臨界
ガスとしては、炭酸ガス、酸化窒素、エタン、プロパン
等が用いられるが、特に、炭酸ガスは、不燃性、無害、
低廉であり、しかも、臨界温度が31℃、臨界圧力が7
9.2気圧であって、取扱いが容易であるうえに、超臨
界状態の炭酸ガスは、粘性が小さく、基板の細部までよ
く浸透して、基板に付着残存している前述したような汚
染物質を迅速に溶解し、除去することができるので、本
発明において好ましく用いられる。In the present invention, carbon dioxide gas, nitrogen oxide, ethane, propane, etc. are used as the liquefied gas or the supercritical gas containing a subcritical state. In particular, carbon dioxide gas is nonflammable, harmless,
It is inexpensive, and has a critical temperature of 31℃ and a critical pressure of 7.
At 9.2 atmospheres, it is easy to handle, and supercritical carbon dioxide gas has low viscosity and can penetrate into the fine details of the substrate, eliminating the aforementioned contaminants that remain attached to the substrate. It is preferably used in the present invention because it can be rapidly dissolved and removed.
本発明においては、有機硬化膜を形成した基板からその
有機硬化膜を除去するのに用いた有機剥離剤又はその有
機剥離剤の収骨として用いられる芳香族有機化合物を液
化ガス又は亜臨界状態を含む超臨界ガスに配合すること
ができる。In the present invention, the organic stripping agent used to remove the organic cured film from the substrate on which the organic cured film is formed, or the aromatic organic compound used as the ashes of the organic stripping agent, is heated in a liquefied gas or subcritical state. It can be blended with supercritical gas containing.
特に、基板に付着残存する有機剥離剤に対しては比較的
高い溶解力を有するが、ホトレジスト膜のような有機硬
化膜に対しては、溶解力が比較的小さいような場合に、
このように、有機剥離剤又はその成分として用いられて
いる芳香族有機化合物を洗浄助剤(エントレーナー)と
して液化ガス又は亜臨界状態を含む超臨界ガスに配合す
ることは有用である。In particular, it has a relatively high dissolving power for organic stripping agents that remain attached to the substrate, but has a relatively low dissolving power for organic cured films such as photoresist films.
Thus, it is useful to blend an organic stripping agent or an aromatic organic compound used as a component thereof into a liquefied gas or a supercritical gas containing a subcritical state as a cleaning aid (entrainer).
このような芳香族有機化合物としては、特に、限定され
るものではないが、好ましくは、ベンゼン、トルエン、
キシレンのような芳香族炭化水素のほか、0−ジクロロ
ベンゼン、フェノール、アルキルベンゼンスルホン酸、
アルキルヒドロキシベンゼン等を挙げることができる。Such aromatic organic compounds are not particularly limited, but preferably benzene, toluene,
In addition to aromatic hydrocarbons such as xylene, 0-dichlorobenzene, phenol, alkylbenzenesulfonic acid,
Examples include alkylhydroxybenzene.
本発明の実施態様によれば、有機硬化膜を有する基板を
有機剥離剤に浸漬して、有機硬化膜を除去した後、尚、
その有機剥離剤、硬化被膜残渣、その他油脂等の汚染物
質が付着している基板を耐圧容器内に仕込み、この容器
内に液化ガス又は亜臨界状態を含む超臨界ガスを流通さ
せ、基板に接触させることによって、上記汚染物質は、
上記ガスに溶解され、かくして、基板が洗浄されて、清
浄にされる。According to an embodiment of the present invention, after the substrate having the organic cured film is immersed in an organic stripping agent to remove the organic cured film,
The substrate to which the organic stripping agent, cured film residue, and other contaminants such as oils and fats have adhered is placed in a pressure-resistant container, and liquefied gas or supercritical gas containing a subcritical state is passed through the container and brought into contact with the substrate. By causing the above pollutants to
Dissolved in the gas, the substrate is thus cleaned and cleaned.
前述したように、液化ガス又は亜臨界状態を含む超臨界
ガスに有機剥離剤又はその成分である芳香族化合物を配
合したときは、かかるガスを基板に接触させた後、次い
で、そのような有機剥離剤や芳香族化合物を含まないガ
スのみを基板に接触させる。As mentioned above, when an organic stripping agent or an aromatic compound as a component thereof is blended with a liquefied gas or a supercritical gas containing a subcritical state, after the gas is brought into contact with the substrate, such organic stripping agent is Only gas that does not contain stripping agents or aromatic compounds is brought into contact with the substrate.
このように、基板にガスを接触させた後、汚染物質を含
有するガスは、その圧力を低減するか、又は昇温するこ
とによって、ガスのそれら汚染物質や有機剥離剤に対す
る溶解力が著しく低減するので、ガスから汚染物質を容
易に分離することができると共に、ガスを冷却し、液化
して、循環再使用することもできる。尚、ガスに剥離剤
を配合した場合は、汚染物質や有機剥離剤を分離する際
の上記圧力や温度条件を適当に選ぶことによって、有機
剥離剤を一定割合にて保持させたまま、ガスを回収する
こともできる。Thus, after the gas is brought into contact with the substrate, the pressure of the gas containing contaminants is reduced or the temperature is increased, which significantly reduces the ability of the gas to dissolve those contaminants and organic stripping agents. Therefore, contaminants can be easily separated from the gas, and the gas can also be cooled, liquefied, and recycled for reuse. If a stripping agent is added to the gas, by appropriately selecting the pressure and temperature conditions mentioned above when separating contaminants and organic stripping agents, the gas can be released while retaining a certain proportion of the organic stripping agent. It can also be collected.
本発明において、液化ガス又は亜臨界状態を含む超臨界
ガスに基板を接触させるに際して、温度は、−20〜1
50℃、好ましくはo−1oo℃の範囲であり、圧力は
、10〜500 kg/cd、好ましくは40〜300
kg/cdの範囲である。また、接触時間は、通常、
2〜15分間が適当である。In the present invention, when the substrate is brought into contact with liquefied gas or supercritical gas containing a subcritical state, the temperature is -20 to 1
50°C, preferably in the range of o-100°C, and the pressure is 10 to 500 kg/cd, preferably 40 to 300 kg/cd.
kg/cd. Also, the contact time is usually
2 to 15 minutes is appropriate.
以下に、超臨界炭酸ガスを用いる場合を例として、図面
に基づいて本発明を説明する。The present invention will be described below based on the drawings, taking as an example a case where supercritical carbon dioxide gas is used.
第1図は、本発明の方法を実施するための装置構成の一
例を示し、炭酸ガスシリンダー1から供給された炭酸ガ
スは、加熱器2及び加圧器3を経て超臨界状態とされ、
例えば、有機硬化膜を有機剥離剤で処理して除去した後
の半導体ウェハーが仕込まれている洗浄槽としての耐圧
容器4に連続して供給され、半導体ウェハーは、ここで
、超臨界炭酸ガスに接触されて洗浄される。FIG. 1 shows an example of an apparatus configuration for carrying out the method of the present invention, in which carbon dioxide gas supplied from a carbon dioxide gas cylinder 1 is brought into a supercritical state through a heater 2 and a pressurizer 3.
For example, semiconductor wafers whose organic cured films have been removed by treatment with an organic stripping agent are continuously supplied to a pressure vessel 4 serving as a cleaning tank, where semiconductor wafers are exposed to supercritical carbon dioxide gas. touched and cleaned.
超臨界炭酸ガスは、耐圧容器を経て減圧弁5にて減圧さ
れた後、分離槽6に導かれて、それが含有する剥離剤、
ホトレジスト膜残渣、その他の汚染物質が槽底から分離
されて、系外に放出される。The supercritical carbon dioxide gas passes through a pressure-resistant container, is depressurized by a pressure reducing valve 5, and is then led to a separation tank 6 where it contains a stripping agent,
Photoresist film residue and other contaminants are separated from the bottom of the tank and discharged outside the system.
また、有機剥離剤を超臨界炭酸ガスに配合するために、
ポンプ7及び弁8を備えた管系9にて剥離剤槽10が超
臨界炭酸ガス管11に接続されていてもよい。剥離剤は
、この管系によって、超臨界炭酸ガスにおいて所定の濃
度を有するように、超臨界炭酸ガスに混合される。In addition, in order to combine organic stripping agent with supercritical carbon dioxide gas,
A stripping agent tank 10 may be connected to a supercritical carbon dioxide gas pipe 11 through a pipe system 9 equipped with a pump 7 and a valve 8 . The stripping agent is mixed with the supercritical carbon dioxide through this tubing so that it has a predetermined concentration in the supercritical carbon dioxide.
第2図は、本発明の方法を実施するための装置構成の別
の一例を示し、炭酸ガスが循環再使用される。即ち、炭
酸ガスシリンダー21から供給された炭酸ガスは、第1
図の場合と同様に、加圧器22及び加熱器23を経て超
臨界状態とされ、耐圧容器24に供給され、半導体ウェ
ハーと接触して、それを洗浄した後、減圧弁25及び分
離槽26を経て、コンデンサー27にて冷却液化された
後、炭酸ガスシリンダー21に戻される。FIG. 2 shows another example of an apparatus configuration for carrying out the method of the present invention, in which carbon dioxide gas is recycled and reused. That is, the carbon dioxide gas supplied from the carbon dioxide gas cylinder 21 is
As in the case shown in the figure, it is made into a supercritical state through a pressurizer 22 and a heater 23, and is supplied to a pressure-resistant container 24, where it comes into contact with a semiconductor wafer and is cleaned. After that, a pressure reducing valve 25 and a separation tank 26 are removed. After being cooled and liquefied in a condenser 27, it is returned to the carbon dioxide cylinder 21.
発里坐盟果
本発明の方法によれば、このように、有機硬化膜が形成
された基板を有機剥離剤に浸漬し、有機硬化膜を剥離さ
せた後、液化ガス又は亜臨界状態を含む超臨界ガスに上
記基板を接触させて、基板に付着している上記剥離剤、
有機硬化膜の剥離残渣及びその他の汚染物質を除去する
ので、液化ガス又は亜臨界状態を含む超臨界ガスを用い
て、直接に有機硬化膜を除去する方法に比べて、極めて
短時間に基板上の有機硬化膜を除去することができるう
えに、基板に付着している上記剥離剤、有機硬化膜の剥
離残渣及びその他油脂等の汚染物質をも完全に除去する
ことができる。According to the method of the present invention, the substrate on which the organic cured film is formed is immersed in an organic stripping agent to peel off the organic cured film, and then the substrate containing liquefied gas or a subcritical state is immersed. the stripping agent attached to the substrate by contacting the substrate with supercritical gas;
Since peeling residue and other contaminants from the organic cured film are removed, the organic cured film can be removed from the substrate in an extremely short time compared to the method of directly removing the organic cured film using liquefied gas or supercritical gas containing a subcritical state. In addition to being able to remove the organic cured film, it is also possible to completely remove the above-mentioned release agent, peeling residue of the organic cured film, and other contaminants such as oils and fats adhering to the substrate.
更に、本発明の方法によれば、種々の汚染物質を含む液
化ガス又は亜臨界状態を含む超臨界ガスは、圧力を低減
させたり、或いは温度を上昇させたりすることによって
、ガスからそれら汚染物質を容易に分離し、ガスを再生
することができるので、その洗浄効果を損なうことなく
、再使用することができる。Furthermore, according to the method of the present invention, the liquefied gas containing various pollutants or the supercritical gas containing subcritical states can be purified from the gas by reducing the pressure or increasing the temperature. can be easily separated and the gas regenerated, so it can be reused without sacrificing its cleaning effectiveness.
また、本発明によれば、トリクレン、パークレン、二塩
化エチレン等の塩素系有機溶剤やフロンによる洗浄を要
せず、環境汚染を招くおそれもない。Further, according to the present invention, there is no need for cleaning with a chlorinated organic solvent such as trichloride, perchlorene, or ethylene dichloride, or with chlorofluorocarbons, and there is no risk of causing environmental pollution.
本発明の方法は、ガリウム、ヒ素等の化合物半導体ウェ
ハーの洗浄にも好適に通用することができる。The method of the present invention can also be suitably applied to cleaning wafers of compound semiconductors such as gallium and arsenic.
実見班
以下に実施例を挙げて本発明を説明するが、本発明はこ
れら実施例により何ら限定されるものではない。Although the present invention will be described below with reference to examples, the present invention is not limited to these examples in any way.
実施例1
厚さ1μmのホトレジスト膜を有するパターンエツチン
グが終了したシリコンウェハーを○−ジクロロベンゼン
、フェノール及びアルキルベンゼンスルホン酸を含有す
る有機剥離剤(東京応化工業特製剥離液71O)に10
0℃で3分間浸漬した後、第1図に示したような耐圧容
器4に仕込み、そこに40℃、100kg/−の超臨界
炭酸ガスを10分間流通させた。Example 1 A pattern-etched silicon wafer having a photoresist film with a thickness of 1 μm was coated with an organic stripping agent (Tokyo Ohka Kogyo Special Stripping Solution 71O) containing dichlorobenzene, phenol, and alkylbenzene sulfonic acid for 10 minutes.
After being immersed for 3 minutes at 0°C, it was placed in a pressure-resistant container 4 as shown in Fig. 1, and 100 kg/- of supercritical carbon dioxide gas was passed through it at 40°C for 10 minutes.
耐圧容器から流出する超臨界炭酸ガスは、減圧弁5にて
減圧し、分離槽6にて剥離剤、ホトレジスト膜残渣等の
汚染物質を分離した後、系外に放出した。The supercritical carbon dioxide gas flowing out from the pressure container was depressurized by a pressure reducing valve 5, and after separating contaminants such as stripping agent and photoresist film residue in a separation tank 6, it was discharged to the outside of the system.
超臨界炭酸ガスの流通を止めて、耐圧容器から取り出し
たウェハーを検査したところ、ウェハーには剥離剤が全
く残存しないことが確認された。When the flow of supercritical carbon dioxide gas was stopped and the wafers removed from the pressure container were inspected, it was confirmed that no stripping agent remained on the wafers.
実施例2
厚さ1μmのホトレジスト膜を有するパターンエツチン
グが終了したシリコンウェハー500枚を実施例1と同
し有機剥離剤(東京応化工業■型判離液710)に10
0℃で2分間浸漬した後、シリコンウェハーを剥離剤及
びホトレジスト膜の一部が付着したまま、第2図に示し
たような内容積50I!の耐圧容器24に仕込み、そこ
に40℃、120kg/a+Iの超臨界炭酸ガスを流通
させた。Example 2 500 pattern-etched silicon wafers having a 1 μm thick photoresist film were treated with the same organic stripping agent (Tokyo Ohka Kogyo Type Separation Liquid 710) as in Example 1 for 10 minutes.
After being immersed for 2 minutes at 0°C, the silicon wafer, with the release agent and part of the photoresist film still attached, has an internal volume of 50 I! as shown in FIG. The mixture was charged into a pressure-resistant container 24, and supercritical carbon dioxide gas at 40° C. and 120 kg/a+I was passed therethrough.
耐圧容器から流出する超臨界炭酸ガスは、減圧弁25に
て50kg/−まで減圧し、分離槽26にて剥離剤、ホ
トレジスト膜残渣等の汚染物質を分離した。炭酸ガスは
、再びコンデンサー25で液化した後、炭酸ガスタンク
21に戻し、再びポンプ22にて耐圧容器24に送り込
んだ。The pressure of the supercritical carbon dioxide flowing out from the pressure container was reduced to 50 kg/- by a pressure reducing valve 25, and contaminants such as stripping agent and photoresist film residue were separated in a separation tank 26. After the carbon dioxide gas was liquefied again in the condenser 25, it was returned to the carbon dioxide tank 21, and then sent into the pressure vessel 24 again by the pump 22.
以上の操作を繰り返して、超臨界炭酸ガスを10分間循
環させた。その後、500枚のシリコンウェハーを耐圧
容器から取り出し、品質検査をしたところ、従来のフロ
ン洗浄と同様の洗浄効果が得られたことが確認された。The above operation was repeated to circulate supercritical carbon dioxide gas for 10 minutes. Thereafter, 500 silicon wafers were removed from the pressure container and inspected for quality, and it was confirmed that the cleaning effect was similar to that of conventional Freon cleaning.
実施例3
実施例1と同しパターンエツチングが終了したシリコン
ウェハー10枚を実施例1と同し有機剥離剤に100℃
で1分間浸漬した後、シリコンウェハーを剥離剤及びホ
トレジスト膜の一部が付着したまま、第1図に示したよ
うな耐圧容器4に仕込んだ。Example 3 Ten silicon wafers that had undergone the same pattern etching as in Example 1 were treated with the same organic release agent as in Example 1 at 100°C.
After being immersed in water for 1 minute, the silicon wafer was placed in a pressure container 4 as shown in FIG. 1, with the release agent and a portion of the photoresist film still attached.
炭酸ガスに対して、濃度が1重量%となるように、管系
9を介して上記剥離剤を混合した40’C1200kg
/cdの超臨界炭酸ガスを上記耐圧容器4に3分間流通
させた。1200 kg of 40'C mixed with the above stripping agent via the pipe system 9 so that the concentration is 1% by weight with respect to carbon dioxide gas
/cd of supercritical carbon dioxide gas was passed through the pressure vessel 4 for 3 minutes.
耐圧容器から流出する超臨界炭酸ガスは、減圧弁5にて
50kg/−まで減圧し、分離槽6にて剥離剤、ホトレ
ジスト膜残渣等の汚染物質を分離し、炭酸ガスは、系外
に放出した。The supercritical carbon dioxide gas flowing out from the pressure container is depressurized to 50 kg/- by a pressure reducing valve 5, and pollutants such as stripping agent and photoresist film residue are separated in a separation tank 6, and the carbon dioxide gas is released outside the system. did.
剥離剤の供給を停止し、その後、5分間、超臨界炭酸ガ
スのみにて耐圧容器4内のシリコンウェハーを洗浄した
。このシリコンウェハーを耐圧容器4から取り出し、品
質検査をしたところ、シリコンウェハーには、剥離剤や
ホトレジスト膜残渣等の汚染物質が全く残存しないこと
が確認された。The supply of the release agent was stopped, and then the silicon wafer in the pressure container 4 was cleaned for 5 minutes using only supercritical carbon dioxide gas. When this silicon wafer was taken out from the pressure container 4 and subjected to quality inspection, it was confirmed that no contaminants such as stripping agent or photoresist film residue remained on the silicon wafer.
第1図は、本発明の方法を実施するための装置構成の一
例を示し、第2図は、炭酸ガスを循環再使用する本発明
の方法を実施するための1ltll威の別の一例を示す
。Fig. 1 shows an example of an apparatus configuration for carrying out the method of the present invention, and Fig. 2 shows another example of the equipment configuration for carrying out the method of the present invention for circulating and reusing carbon dioxide gas. .
Claims (5)
して、上記有機硬化膜を基板から剥離し、次いで、液化
ガス又は亜臨界状態を含む超臨界ガスに上記基板を接触
させて、基板に付着している上記剥離剤、有機硬化膜の
剥離残渣及びその他の汚染物質を除去することを特徴と
する有機硬化膜の除去方法。(1) The substrate on which the organic cured film is formed is immersed in an organic release agent to peel the organic cured film from the substrate, and then the substrate is brought into contact with liquefied gas or supercritical gas containing a subcritical state. . A method for removing an organic cured film, which comprises removing the above-mentioned release agent, peeling residue of the organic cured film, and other contaminants adhering to the substrate.
とする請求項第1項記載の有機硬化膜の除去方法。(2) The method for removing an organic cured film according to claim 1, wherein the organic stripping agent contains an aromatic compound.
ガスであることを特徴とする請求項第1項記載の有機硬
化膜の除去方法。(3) The method for removing an organic cured film according to claim 1, wherein the liquefied gas or the supercritical gas containing a subcritical state is carbon dioxide gas.
を2〜15分間接触させることを特徴とする請求項第1
項記載の有機硬化膜の除去方法。(4) Claim 1, characterized in that the substrate is brought into contact with liquefied gas or supercritical gas containing a subcritical state for 2 to 15 minutes.
The method for removing an organic cured film described in .
レジスト膜であることを特徴とする請求項第1項記載の
有機硬化膜の除去方法。(5) The method for removing an organic cured film according to claim 1, wherein the substrate is a semiconductor wafer and the organic cured film is a photoresist film.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2059419A JPH03261128A (en) | 1990-03-09 | 1990-03-09 | Method of removing organic hardening film |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2059419A JPH03261128A (en) | 1990-03-09 | 1990-03-09 | Method of removing organic hardening film |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH03261128A true JPH03261128A (en) | 1991-11-21 |
Family
ID=13112728
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2059419A Pending JPH03261128A (en) | 1990-03-09 | 1990-03-09 | Method of removing organic hardening film |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03261128A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6475403B2 (en) * | 2000-01-31 | 2002-11-05 | Matsushita Electric Industrial Co., Ltd. | Etching method and apparatus |
| JP2006508307A (en) * | 2002-11-26 | 2006-03-09 | ウーデ・ハイ・プレッシャー・テクノロジーズ・ゲゼルシャフト・ミト・ベシュレンクテル・ハフツング | High pressure device that closes the container in the clean room |
| CN115739844A (en) * | 2022-10-28 | 2023-03-07 | 浙江大学 | Supercritical wafer cleaning/drying medium recovery method and system |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60192333A (en) * | 1984-03-13 | 1985-09-30 | Hitachi Ltd | Method for removal of organic coated and hardened film |
| JPS63179530A (en) * | 1987-01-21 | 1988-07-23 | Hitachi Ltd | Method and apparatus for cleaning a substrate using supercritical gas or liquefied gas |
| JPH01286314A (en) * | 1988-05-12 | 1989-11-17 | Matsushita Electric Ind Co Ltd | Manufacture of semiconductor device |
-
1990
- 1990-03-09 JP JP2059419A patent/JPH03261128A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60192333A (en) * | 1984-03-13 | 1985-09-30 | Hitachi Ltd | Method for removal of organic coated and hardened film |
| JPS63179530A (en) * | 1987-01-21 | 1988-07-23 | Hitachi Ltd | Method and apparatus for cleaning a substrate using supercritical gas or liquefied gas |
| JPH01286314A (en) * | 1988-05-12 | 1989-11-17 | Matsushita Electric Ind Co Ltd | Manufacture of semiconductor device |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6475403B2 (en) * | 2000-01-31 | 2002-11-05 | Matsushita Electric Industrial Co., Ltd. | Etching method and apparatus |
| JP2006508307A (en) * | 2002-11-26 | 2006-03-09 | ウーデ・ハイ・プレッシャー・テクノロジーズ・ゲゼルシャフト・ミト・ベシュレンクテル・ハフツング | High pressure device that closes the container in the clean room |
| CN115739844A (en) * | 2022-10-28 | 2023-03-07 | 浙江大学 | Supercritical wafer cleaning/drying medium recovery method and system |
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