JPH02194527A - Removal of film - Google Patents
Removal of filmInfo
- Publication number
- JPH02194527A JPH02194527A JP1338289A JP1338289A JPH02194527A JP H02194527 A JPH02194527 A JP H02194527A JP 1338289 A JP1338289 A JP 1338289A JP 1338289 A JP1338289 A JP 1338289A JP H02194527 A JPH02194527 A JP H02194527A
- Authority
- JP
- Japan
- Prior art keywords
- film
- etching solution
- chamber
- supplied
- etching
- 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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Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、半導体デバイスの製造工程における混酸を利
用したウェット・プロセスにおいて、被膜が形成された
半導体ウェーハ、半導体デバイス製造用の熱拡散炉等に
使用される炉芯管、治工具、ペルジャー等の被被膜除去
物から被膜を除去する被膜除去方法に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention is applied to semiconductor wafers on which a film is formed, thermal diffusion furnaces for semiconductor device manufacturing, etc. in a wet process using mixed acids in the manufacturing process of semiconductor devices. The present invention relates to a coating removal method for removing coatings from coating-removed items such as furnace core tubes, jigs, pel jars, etc. used in
[従来の技術]
従来、この種の被膜除去方法としては、第3図に示すよ
うに、例えばウェーハ1 (Si、 GaAs)を処
理層2に収容されたエツチング液3中に浸漬する方法、
又は、第4図に示すように、例えばペルジャー(石英製
)4の内外に複数のスプレーノズル5を配置してエツチ
ング液をペルジャー4の表面にスプレーする方法がある
。[Prior Art] Conventionally, as shown in FIG. 3, this type of film removal method includes, for example, a method in which a wafer 1 (Si, GaAs) is immersed in an etching solution 3 contained in a processing layer 2;
Alternatively, as shown in FIG. 4, there is a method in which, for example, a plurality of spray nozzles 5 are arranged inside and outside a Pel jar (made of quartz) 4 and the etching solution is sprayed onto the surface of the Pel jar 4.
[発明が解決しようとする課題]
しかしながら、前者の被I!M除去方法においては、例
えばウェーハ1に形成された被膜を除去する場合には、
被膜とエツチング液との化学反応により生ずるガス6(
第1図参照)が、ウェーハ1の表面に気泡となって付着
して被膜を均一に除去することができず、例えば第5図
に示すように、処理層2の上部にチャンバー7を設け、
このチャンバー7内を真空に保持して脱気したり、ある
いは第6図に示すように、移送アーム8を使用してウェ
ーハ1をエツチング液3から一定時間毎に大気中に取り
出してガス6を除去したりする必要がある。[Problem to be solved by the invention] However, the former problem! In the M removal method, for example, when removing a coating formed on the wafer 1,
Gas 6 (
(see FIG. 1) adheres to the surface of the wafer 1 in the form of bubbles, making it impossible to remove the coating uniformly. For example, as shown in FIG. 5, a chamber 7 is provided above the processing layer 2,
The chamber 7 can be kept in a vacuum and degassed, or as shown in FIG. need to be removed.
このため、装置が高価になると共に、故障要因が増大す
る欠点がある。又、化学反応によりエツチング液3の組
成が経時変化するので、頻繁に液交換を行う必要がある
。従って、大量のエツチング液3を使用することとなり
、ランニングコストが増す欠点がある。更に、メモリー
の高集積化に伴い、セルキャパシターは、ブレーナ型か
らトレンチ型へとウェーハ1の厚さ方向の空間を利用す
る方式になっているが、第7図に示すように、ウェーハ
1の巾1μm、深さ4μmの溝9を洗浄することが非常
に難しい問題となっている。For this reason, there are disadvantages in that the device becomes expensive and the number of failure factors increases. Furthermore, since the composition of the etching solution 3 changes over time due to chemical reactions, it is necessary to frequently exchange the solution. Therefore, a large amount of etching solution 3 is used, which has the drawback of increasing running costs. Furthermore, with the increasing integration of memory, cell capacitors have changed from the brainer type to the trench type, which utilizes the space in the thickness direction of the wafer 1. Cleaning the groove 9, which has a width of 1 μm and a depth of 4 μm, has become a very difficult problem.
又、半導体デバイス製造用の熱拡散炉、CVD(Che
micaf Vaper Deposition)用炉
、エピタキシャル成長層ディスク形炉等に使用する炉芯
管(石英製、SiC製)、治工具(石英製、SiC製)
、又はペルジャー(石英製)に形成された被膜を除去す
る場合には、例えば炉芯管10は、その長さが3m程度
あることから、第8図に示すように、大きな如埋槽11
を必要とするばかりか大量のエツチング液3を必要とす
る。このため、装置が大型化し、高価となる。In addition, heat diffusion furnaces for semiconductor device manufacturing, CVD (Che
Furnace core tubes (made of quartz, made of SiC), jigs and tools (made of quartz, made of SiC) used in micaf Vaper Deposition furnaces, epitaxial growth layer disc-shaped furnaces, etc.
Or, when removing a coating formed on Pelger (made of quartz), for example, since the furnace core tube 10 has a length of about 3 m, a large burial tank 11 is used as shown in FIG.
Not only that, but also a large amount of etching solution 3 is required. Therefore, the device becomes large and expensive.
一方、後者の被膜除去方法においては、被膜を均一に除
去するため、被被膜除去物を支持する支持具12(第4
図参照)の回転機構や昇降機構(共に図示せず)を必要
とする欠点がある。On the other hand, in the latter film removal method, in order to uniformly remove the film, the support 12 (fourth
This method has the disadvantage that it requires a rotating mechanism (see figure) and a lifting mechanism (both not shown).
そこで、本発明は、被被膜除去物に形成された被膜を少
量のエツチング液により均一かつ十分に除去し得る被膜
除去方法の提供を目的とする。SUMMARY OF THE INVENTION Therefore, an object of the present invention is to provide a film removal method that can uniformly and sufficiently remove a film formed on a film-removed object using a small amount of etching solution.
[課題を解決するための手段]
前記課題を解決するため、本発明は、被被膜除去物を収
容したチャンバー内に、エツチング液を霧状の微粒子に
して供給する方法である。[Means for Solving the Problems] In order to solve the above-mentioned problems, the present invention is a method of supplying an etching solution in the form of fine particles in the form of mist into a chamber containing a film to be removed.
[作 用コ
上記手段においては、エツチング液のn状の微粒子が被
被膜除去物の表面に薄膜状となって均一に付着し、被膜
との化学反応によって生じたガスが薄膜状のエツチング
液の粘性に打ち特)て容易にチャンバー内に放出される
。[Function] In the above means, the n-shaped fine particles of the etching liquid uniformly adhere to the surface of the object from which the film has been removed in the form of a thin film, and the gas generated by the chemical reaction with the film forms a thin film of the etching liquid. It is easily released into the chamber due to its viscosity.
微粒子の大きさは、1〜300timが好ましく、1μ
m未満ではエツチングに時間が長くかかり、300μm
を超えるとエツチング液の均一な付着が困難となる。The size of the fine particles is preferably 1 to 300tim, and 1μ
If it is less than 300 μm, etching will take a long time.
If it exceeds this, it becomes difficult for the etching solution to adhere uniformly.
[実施例]
以下、本発明の一実施例を第1図、第2図と共に説明す
る。[Example] An example of the present invention will be described below with reference to FIGS. 1 and 2.
第1図及び第2図は本発明の実施に供した被膜除去装置
の概略構成図及び部分断面斜視図である。FIGS. 1 and 2 are a schematic configuration diagram and a partially sectional perspective view of a film removing apparatus used for carrying out the present invention.
第1図において15はチャンバーで、その中には、被被
膜除去物である石英製のペルジャー16が、このペルジ
ャー16との接触面積を少なくした支持具17に支持さ
れて収容されている。又、チャンバー15内には、複数
の二流体微噴nノズル18がペルジャー16と対向させ
て上、下に配置されている。これらのチャンバー15等
は、第2図に示すように、正面に吸気用レジスタ19a
を備えた昇降可能な正面扉19と、背面上部に付設した
排気ダクト20に接続される強制通風用の排気レジスタ
21を背面に備えた耐酸性の筺体22内に設けられる。In FIG. 1, reference numeral 15 denotes a chamber, in which a quartz Pelger 16 from which the film is removed is supported and accommodated by a support 17 whose contact area with the Pelger 16 is reduced. Further, in the chamber 15, a plurality of two-fluid fine injection n nozzles 18 are arranged above and below the Pelger 16, facing the same. These chambers 15, etc. have an intake register 19a on the front as shown in FIG.
It is provided in an acid-resistant casing 22, which has a front door 19 that can be raised and lowered, and an exhaust register 21 for forced ventilation connected to an exhaust duct 20 attached to the upper part of the rear surface.
第2図において23はエツチング液の飛散防止用の内扉
であって、正面の開口部中心より左右方向へ二分割で開
閉でき、ペルジャー16の出し入ね時には左右に開放さ
れ、被膜除去中には閉鎮されて酸性度の高いエツチング
液が筐体22(チャンバー)内に飛散して腐食を招いた
り、液が外部に飛散して消耗するのを防止する。In Fig. 2, reference numeral 23 denotes an inner door for preventing scattering of the etching solution, which can be opened and closed in two parts from the center of the front opening in the left and right directions, and opened to the left and right when the Pelger 16 is inserted and taken out, and is opened to the left and right during film removal. This prevents the highly acidic etching solution from scattering into the housing 22 (chamber) and causing corrosion, and prevents the solution from scattering to the outside and causing consumption.
前記各二流体微9nノズル18は、第1図に示すように
、エツチング液24を収容したタンク25及び清浄ガス
供給源26と、エツチング液供給用電磁バルブ27を介
在した第1管路28及び清浄ガス供給用電磁バルブ29
を介在した第2管路30によって接続されている。そし
て、第1管路28には、清浄用の常圧ガス供給源31が
、常圧ガス供給用電6nバルブ32を介在した分岐管路
33によって分岐接続されている一方、第2管路30に
は、洗浄用の純水供給源34が、純水供給用電6i1バ
ルブ35を介在した分岐管路36によって分岐接続され
ている。上記タンク25は、実際の装置においては、第
2図に示すように、筺体22内の右側下部に設けられる
。As shown in FIG. 1, each of the two-fluid fine 9n nozzles 18 has a tank 25 containing an etching liquid 24, a clean gas supply source 26, a first conduit 28 with an etching liquid supply electromagnetic valve 27 interposed therebetween, and Solenoid valve 29 for clean gas supply
They are connected by a second conduit 30 interposed therebetween. A normal pressure gas supply source 31 for cleaning is connected to the first pipe line 28 via a branch pipe line 33 with a normal pressure gas supply electric valve 32 interposed therebetween, while the second pipe line 30 A pure water supply source 34 for cleaning is branched and connected through a branch pipe line 36 with a pure water supply electric valve 6i1 interposed therebetween. In the actual device, the tank 25 is provided at the lower right side inside the housing 22, as shown in FIG.
又、チャンバー15の下部は、第1図に示すように、排
出口37と排出用共通電磁バルブ38を介在した排出管
路39によって接続されている。Further, as shown in FIG. 1, the lower part of the chamber 15 is connected by a discharge pipe 39 with a discharge port 37 and a common discharge electromagnetic valve 38 interposed therebetween.
そして、排出管路39は、その排出用共通電磁バルブ3
8の下流において分岐した分岐排出管路40によってタ
ンク25と接続されている。The discharge pipe 39 is connected to the discharge common electromagnetic valve 3.
It is connected to the tank 25 by a branch discharge pipe 40 that branches downstream of the tank 8 .
前記各電磁バルブは、第2図に示すように、筺体22の
正面に取付けられた操作盤41及びこれに連動して働く
シーケンス制御装置(図示せず)により、所定の順序と
所定の時間間隔のもとに開閉される。As shown in FIG. 2, the electromagnetic valves are controlled in a predetermined order and at predetermined time intervals by an operation panel 41 attached to the front of the housing 22 and a sequence control device (not shown) that works in conjunction with the operation panel 41. It is opened and closed under the
上記構成の被膜除去装置においては、ペルジャー16を
チャンバー15内に収容した後、エツチング液供給用電
磁バルブ27と清浄ガス供給用電磁バルブ29とを開状
態にすることにより、タンク25内のエツチング液24
が、二流体徹噴霧ノズル18に供給される清浄ガス(霧
化空気圧3.0kg/cm2)の吸引力によって吸い上
げられ、ノズルからガスが出ると同時に霧化されて霧状
の微粒子(粒径1〜300μm)となってチャンバー1
5内に供給される。一定時間供給後、エツチング液供給
用電磁バルブ27及び清浄ガス供給用電磁バルブ29を
閉状態とし、所要時間待機する。In the film removal apparatus having the above structure, after the Pel jar 16 is housed in the chamber 15, the etching liquid in the tank 25 is removed by opening the etching liquid supply electromagnetic valve 27 and the clean gas supply electromagnetic valve 29. 24
is sucked up by the suction force of the clean gas (atomization air pressure 3.0 kg/cm2) supplied to the two-fluid through-spray nozzle 18, and at the same time as the gas exits from the nozzle, it is atomized into atomized fine particles (particle size 1 ~300μm) and chamber 1
Supplied within 5 days. After supplying the etching solution for a certain period of time, the electromagnetic valve 27 for supplying etching liquid and the electromagnetic valve 29 for supplying clean gas are closed, and the etching solution is waited for a required period of time.
上記待機時間中に、エツチング液24の霧状の微粒子は
、ペルジャー16の全表面に薄膜状となって均一に付着
し、ペルジャー16に形成された被膜と化学反応を起こ
す。この化学反応によって生じたガスは、薄膜状のエツ
チング液24の粘性に打ち勝って容易にチャンバー15
内に放出される。During the waiting time, the fine particles of the etching liquid 24 uniformly adhere to the entire surface of the Pel Jar 16 in the form of a thin film, causing a chemical reaction with the coating formed on the Pel Jar 16. The gas generated by this chemical reaction overcomes the viscosity of the thin film of etching liquid 24 and easily fills the chamber 15.
released within.
所要待機時間経過後、常圧ガス供給用電磁バルブ32、
純水供給用電磁バルブ35及び排出用共通電磁バルブ3
8を開状態にすることにより、二流体徴噴πノズル18
に供給される純水(供給圧2.0kg/cm2)の吸引
力によって常圧ガスと純水が混合されて霧状となって洗
浄効果の増した純水が、各二流体徹噴露ノズル18から
ペルジャー16の全表面に供給され、エツチング液24
と被膜との化学反応後の液を洗浄し、この洗浄液は、排
出口37から機外に排出さる。After the required standby time has passed, the normal pressure gas supply solenoid valve 32,
Pure water supply solenoid valve 35 and discharge common solenoid valve 3
By opening 8, the two-fluid characteristic jet π nozzle 18
The atmospheric pressure gas and pure water are mixed by the suction force of the pure water (supply pressure 2.0 kg/cm2) supplied to the unit, and the pure water, which has an increased cleaning effect and is atomized, is delivered to each two-fluid continuous spray nozzle. The etching liquid 24 is supplied from 18 to the entire surface of the Pelger 16.
The liquid after the chemical reaction between the cleaning liquid and the coating is washed, and this cleaning liquid is discharged from the outlet 37 to the outside of the machine.
上記エツチング液24の微噴霧は、エツチング液24の
被膜との化学反応による経時変化に対応するため、数回
繰り返すことが望ましく、又、被膜との化学変化を起こ
さなかったエツチング液24は、分岐排出管路40を経
てタンク25へ還流させる。It is desirable to repeat the fine spraying of the etching liquid 24 several times in order to cope with changes over time due to chemical reactions between the etching liquid 24 and the film. It is refluxed to the tank 25 via the discharge pipe 40.
[発明の効果]
以上のように本発明によれば、エツチング液の霧状の微
粒子が被被膜除去物の表面に薄膜状となって均一に付着
し、被膜との化学反応によって生じたガスが薄膜状のエ
ツチング液の粘性に打ち勝って容易にチャンバー内に放
出されるので、従来のように被膜除去装置の複雑化、大
型化に伴うエツチング液及び純水の大量の消耗を必要と
せず、少量のエツチング液により被膜を均一かつ十分に
除去することができると共に、エツチング液の使用量が
少量のため、従来に比して純水の使用量を少量とするこ
とができる。[Effects of the Invention] As described above, according to the present invention, the atomized fine particles of the etching solution uniformly adhere to the surface of the film-removed object in the form of a thin film, and the gas generated by the chemical reaction with the film is released. Since the viscosity of the thin film-like etching solution is overcome and it is easily released into the chamber, it is not necessary to consume a large amount of etching solution and pure water, which accompanies the complexity and size of conventional film removal equipment. The film can be removed uniformly and sufficiently using the etching solution, and since the amount of etching solution used is small, the amount of pure water used can be reduced compared to the conventional method.
¥S1図及び第2図は本発明の実施に供した被膜除去装
置の概略構成図及び部分断面斜視図、第3図及び第4図
は従来の浸漬式及びスプレー式の被膜除去方法の説明図
、第5図及び第6図は浸漬式の被膜除去方法におけるガ
ス除去手段の説明図、第7図はウェーハの部分拡大断面
図、第8図は浸漬式の被膜除去方法による炉芯管の被膜
除去手段の説明図である。
15・・・チャンバー 16・・・ペルジャー17・
・・支持具、
18・・・二流体微噴nノズル、
24・・・エツチング液、25・・・タンク、26・・
・清浄ガス供給源、
27・・・エツチング?夜イ共飴用電磁バルブ28・・
・第1管路、
29・・・清浄ガス供給用電磁バルブ
30・・・第2管路。¥S1 Figure and Figure 2 are a schematic configuration diagram and a partial cross-sectional perspective view of a film removal device used for carrying out the present invention, and Figures 3 and 4 are explanatory diagrams of conventional immersion type and spray type film removal methods. , Figures 5 and 6 are explanatory diagrams of gas removal means in the immersion type coating removal method, Figure 7 is a partially enlarged sectional view of a wafer, and Figure 8 is a diagram showing the coating on the furnace core tube by the immersion type coating removal method. It is an explanatory view of a removal means. 15...Chamber 16...Pelger 17.
... Support tool, 18 ... Two-fluid fine spray n nozzle, 24 ... Etching liquid, 25 ... Tank, 26 ...
・Clean gas supply source, 27...Etching? Solenoid valve 28 for nighttime candy...
- First pipe line, 29... Solenoid valve for clean gas supply 30... Second pipe line.
Claims (1)
ング液を霧状の微粒子にして供給することを特徴とする
被膜除去方法。(1) A film removal method characterized by supplying an etching solution in the form of fine particles in the form of mist into a chamber containing a film to be removed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1338289A JPH02194527A (en) | 1989-01-23 | 1989-01-23 | Removal of film |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1338289A JPH02194527A (en) | 1989-01-23 | 1989-01-23 | Removal of film |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02194527A true JPH02194527A (en) | 1990-08-01 |
Family
ID=11831545
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1338289A Pending JPH02194527A (en) | 1989-01-23 | 1989-01-23 | Removal of film |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02194527A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH04215436A (en) * | 1990-12-14 | 1992-08-06 | Shin Etsu Handotai Co Ltd | Washing of silicon and its apparatus |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5918642A (en) * | 1982-07-21 | 1984-01-31 | Nec Kyushu Ltd | Manufacturing device of semiconductor device |
| JPS59115763A (en) * | 1982-12-21 | 1984-07-04 | Fujitsu Ltd | Ultrasonic fog treatment device |
| JPS59213134A (en) * | 1983-05-19 | 1984-12-03 | Toshiba Corp | Semiconductor manufacturing device |
-
1989
- 1989-01-23 JP JP1338289A patent/JPH02194527A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5918642A (en) * | 1982-07-21 | 1984-01-31 | Nec Kyushu Ltd | Manufacturing device of semiconductor device |
| JPS59115763A (en) * | 1982-12-21 | 1984-07-04 | Fujitsu Ltd | Ultrasonic fog treatment device |
| JPS59213134A (en) * | 1983-05-19 | 1984-12-03 | Toshiba Corp | Semiconductor manufacturing device |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH04215436A (en) * | 1990-12-14 | 1992-08-06 | Shin Etsu Handotai Co Ltd | Washing of silicon and its apparatus |
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