JPH11186217A - Wafer processor - Google Patents

Wafer processor

Info

Publication number
JPH11186217A
JPH11186217A JP35296097A JP35296097A JPH11186217A JP H11186217 A JPH11186217 A JP H11186217A JP 35296097 A JP35296097 A JP 35296097A JP 35296097 A JP35296097 A JP 35296097A JP H11186217 A JPH11186217 A JP H11186217A
Authority
JP
Japan
Prior art keywords
processing
phosphoric acid
temperature
acid solution
substrate
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.)
Abandoned
Application number
JP35296097A
Other languages
Japanese (ja)
Inventor
Hiroyuki Araki
浩之 荒木
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.)
Dainippon Screen Manufacturing Co Ltd
Original Assignee
Dainippon Screen Manufacturing Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Dainippon Screen Manufacturing Co Ltd filed Critical Dainippon Screen Manufacturing Co Ltd
Priority to JP35296097A priority Critical patent/JPH11186217A/en
Publication of JPH11186217A publication Critical patent/JPH11186217A/en
Abandoned legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To obtain desired chemical processing, such as for the amount of etching, even at the time of putting in wafers into a processing liquid. SOLUTION: A wafer processor has a structure that a control means 30 controls a current to a temperature adjuster 28 so as to raise previously the temperature of a processing liquid 21 by the amount of heat corresponding to the thermal capacity of the whole members including a plurality of wafers 2 before the wafers 2 are dipped into the liquid 21 in a phosphoric acid tank 22 by a lifter 23, therefore, the temperature, which is reduced at the time of putting in the wafers 2 into the liquid 21, of the liquid 21 can be significantly inhibited, etching of the wafers 2 can be performed at the optimum temperature and even at the time of putting in the wafers 2 into the liquid 21, a desired amount of etching is obtained.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、例えば薬液または
処理液(例えば薬液および純水液などを総称して処理液
という)を貯留する処理槽に、半導体ウエハや液晶表示
パネル用ガラス基板などの薄板状の被処理基板(以下単
に基板という)を浸漬して基板に所定の処理を施す基板
処理装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a process tank for storing, for example, a chemical solution or a processing solution (for example, a chemical solution and a pure water solution are collectively referred to as a processing solution). The present invention relates to a substrate processing apparatus for immersing a thin substrate to be processed (hereinafter simply referred to as a substrate) and performing predetermined processing on the substrate.

【0002】[0002]

【従来の技術】従来、半導体ウエハや液晶表示パネル用
ガラス基板などを用いた精密電子基板の製造プロセスに
おいては、基板を処理液に浸漬して種々の表面処理を施
す基板処理装置が用いられている。このような表面処理
においては、エッチング液(燐酸溶液など)などの薬液
を貯留した薬液槽、さらに、リンス液である純水を貯留
した水洗槽に順次基板を浸漬して、基板に薬液処理を施
した後に、さらに、水洗槽にて基板に付着した薬液やそ
れによって発生したパーティクルを洗い流すリンス処理
を行っている。
2. Description of the Related Art Conventionally, in a manufacturing process of a precision electronic substrate using a semiconductor wafer, a glass substrate for a liquid crystal display panel, or the like, a substrate processing apparatus that performs various surface treatments by immersing the substrate in a processing liquid has been used. I have. In such a surface treatment, the substrate is sequentially immersed in a chemical tank storing a chemical such as an etching solution (a phosphoric acid solution, etc.) and a washing tank storing pure water as a rinsing liquid. After the application, a rinsing process is further performed to wash out the chemical solution attached to the substrate and particles generated by the chemical solution in the washing tank.

【0003】この薬液槽内に純水が供給される処理液供
給システムが設けられており、一定量の純水を燐酸溶液
に加えることによって蒸発分を補って所望の濃度が得ら
れるようになっている。また、薬液槽内で基板表面から
脱落したパーティクルなどの汚染物質と共に薬液槽から
オーバーフローした薬液は、循環ポンプにてヒータ電子
冷熱による温度調節器さらにフィルタを介して、その温
度調節器で薬液を一定温度に保持すると共に、そのフィ
ルタでその汚染物質が取り除かれてリフレッシュされた
後に再び薬液槽内に戻されて循環されるようになってい
る。
A treatment liquid supply system for supplying pure water to the chemical solution tank is provided. By adding a certain amount of pure water to a phosphoric acid solution, a desired concentration can be obtained by compensating for evaporation. ing. In addition, the chemical liquid overflowing from the chemical liquid tank together with contaminants such as particles that have fallen off the substrate surface in the chemical liquid tank passes through a temperature controller using electronic cooling and heating by a heater and a filter using a circulation pump. While maintaining the temperature, the filter removes the contaminants and is refreshed, and then returned to the chemical tank and circulated again.

【0004】このように、一定温度で一定濃度の燐酸溶
液に複数の基板を一定時間浸漬させてエッチング処理な
どの薬液処理を行うことによって、所望のエッチング量
などの薬液処理量を得るようになっている。
As described above, a plurality of substrates are immersed in a phosphoric acid solution having a constant concentration at a constant temperature for a certain period of time to perform a chemical treatment such as an etching process, thereby obtaining a desired chemical treatment amount such as an etching amount. ing.

【0005】[0005]

【発明が解決しようとする課題】上記従来の構成では、
薬液槽内に供給された燐酸溶液は、燐酸溶液に一定量の
純水が加えられ蒸発分が補われて所望の濃度を得るよう
になっているが、薬液槽内の燐酸溶液に複数の基板を投
入(lot in)した際には、図5に示すようにその燐酸溶
液の温度が低下してエッチング対象であるシリコン窒化
膜のエッチングレートも低下する。このため、図6に示
すように基板投入(lot in)後の所定時間(T1)だけ、そ
の下がった燐酸溶液の温度を早く回復させるべく燐酸溶
液に対する純水の補充を停止していた。このような基板
投入時の純水補充の停止で、その燐酸溶液の下がった温
度の回復が早められることになるが、その純水補充の停
止期間(T1)には燐酸溶液だけが供給されているため、図
6に示すように燐酸溶液の濃度が高い方に変化するよう
になる。したがって、上記した燐酸溶液の温度低下によ
るシリコン窒化膜のエッチングレートの低下に加えてさ
らに、燐酸溶液の濃度上昇によってシリコン酸化膜のエ
ッチングレートが上昇して、所定時間内にシリコン窒化
膜をシリコン酸化膜に対して所望の選択比で所望のエッ
チング量をエッチングすることができないという問題を
有していた。
In the above-mentioned conventional configuration,
A certain amount of pure water is added to the phosphoric acid solution to supply the phosphoric acid solution into the chemical solution tank to compensate for the evaporation, thereby obtaining a desired concentration. In this case, as shown in FIG. 5, the temperature of the phosphoric acid solution decreases, and the etching rate of the silicon nitride film to be etched also decreases. For this reason, as shown in FIG. 6, the replenishment of pure water to the phosphoric acid solution has been stopped for a predetermined time (T1) after the substrate is loaded (lot in) in order to quickly recover the lowered temperature of the phosphoric acid solution. By stopping the replenishment of pure water at the time of loading the substrate, the recovery of the lowered temperature of the phosphoric acid solution is accelerated, but during the suspension period of the pure water replenishment (T1), only the phosphoric acid solution is supplied. Therefore, as shown in FIG. 6, the concentration of the phosphoric acid solution changes to a higher one. Therefore, in addition to the decrease in the etching rate of the silicon nitride film due to the decrease in the temperature of the phosphoric acid solution, the etching rate of the silicon oxide film further increases due to the increase in the concentration of the phosphoric acid solution. There is a problem that a desired etching amount cannot be etched at a desired selection ratio with respect to the film.

【0006】本発明は、上記従来の問題を解決するもの
で、処理液中への基板投入時にも所望のエッチング量な
どの処理量を得ることができる基板処理装置を提供する
ことを目的とする。
An object of the present invention is to solve the above-mentioned conventional problems, and an object of the present invention is to provide a substrate processing apparatus which can obtain a desired processing amount such as an etching amount even when a substrate is put into a processing solution. .

【0007】[0007]

【課題を解決するための手段】本発明の基板処理装置
は、処理槽内に供給された処理液中に基板を浸漬させて
処理を施す基板処理装置において、処理液の温度を調整
する温度調整手段と、処理液中への基板浸漬前に、その
浸漬する基板全体の熱容量に応じた熱量分だけ予め処理
液温度を変化させるように温度調整手段を制御する制御
手段とを有することを特徴とするものである。
According to the present invention, there is provided a substrate processing apparatus for performing processing by immersing a substrate in a processing liquid supplied to a processing tank. Means, before dipping the substrate in the processing liquid, having a control means for controlling the temperature adjustment means to change the processing liquid temperature in advance by the amount of heat according to the heat capacity of the entire substrate to be dipped, Is what you do.

【0008】この構成により、制御手段は、処理液中へ
の基板浸漬前に、その浸漬する基板全体の熱容量に応じ
た熱量分だけ予め処理液温度を変化させるように温度調
整手段を制御するようになっているので、ウエハ投入時
に低下する処理液温度が大幅に抑制され最適温度による
基板処理が可能となって、処理液中への基板投入時にも
所定時間内に所望のエッチング量などの処理量が得られ
る。
With this configuration, the control means controls the temperature adjusting means so as to change the temperature of the processing liquid by a heat amount corresponding to the heat capacity of the entire substrate to be dipped before dipping the substrate in the processing liquid. , The temperature of the processing solution that drops when the wafer is loaded is greatly suppressed, and substrate processing at the optimum temperature becomes possible. Even when the substrate is loaded into the processing solution, processing such as a desired etching amount can be performed within a predetermined time. The amount is obtained.

【0009】また、本発明の基板処理装置は、処理槽内
に供給された燐酸溶液中に基板を浸漬させて処理を施す
基板処理装置において、処理槽からオーバーフローした
燐酸溶液を処理槽内に戻して循環させる処理液循環手段
に、循環している燐酸溶液の温度を調整する温度調整手
段が設けられ、この温度調整手段に対して、燐酸溶液中
への基板浸漬前に、その浸漬する基板全体の熱容量に応
じた熱量分だけ予め処理液温度を変化させるように温度
調整手段を制御する制御手段が設けられていることを特
徴とするものである。
Further, the substrate processing apparatus of the present invention is a substrate processing apparatus for performing processing by immersing a substrate in a phosphoric acid solution supplied into a processing tank, wherein the phosphoric acid solution overflowing from the processing tank is returned to the processing tank. The processing liquid circulating means for circulating the solution is provided with a temperature adjusting means for adjusting the temperature of the circulating phosphoric acid solution. Control means for controlling the temperature adjusting means so as to change the processing liquid temperature in advance by an amount of heat according to the heat capacity of the processing liquid.

【0010】従来は、処理液がシリコン窒化膜をエッチ
ングする燐酸溶液の場合、表面保護膜としてのシリコン
酸化膜とのエッチング選択比が重要であり、このシリコ
ン酸化膜のエッチング量は、燐酸溶液の温度と濃度共に
高くなると増加し、また、エッチング対象であるシリコ
ン窒化膜のエッチング量は、燐酸溶液の温度が高くなる
と増加するが、その濃度が高くなると減少する。したが
って、基板の燐酸溶液への投入時には燐酸溶液の温度が
下がり、かつ、その期間(T1)における純水補充の停止に
よって燐酸溶液の濃度が上昇するため、エッチング対象
であるシリコン窒化膜のエッチングレートが大幅に低下
して所望のエッチング量が得られないばかりか、表面保
護膜としてのシリコン酸化膜のエッチングレートは燐酸
溶液の濃度上昇で上昇し、エッチングすべきシリコン窒
化膜が大幅にはエッチングできず、エッチング対象では
ないシリコン酸化膜が必要以上にエッチングされてしま
い、所望のエッチング選択比が得られなかった。
Conventionally, when a processing solution is a phosphoric acid solution for etching a silicon nitride film, an etching selectivity with respect to a silicon oxide film as a surface protective film is important. Both the temperature and the concentration increase as the temperature increases, and the etching amount of the silicon nitride film to be etched increases as the temperature of the phosphoric acid solution increases, but decreases as the concentration increases. Therefore, when the substrate is put into the phosphoric acid solution, the temperature of the phosphoric acid solution decreases, and the concentration of the phosphoric acid solution increases by stopping the replenishment of pure water during the period (T1), so that the etching rate of the silicon nitride film to be etched is increased. The etching rate of the silicon oxide film as the surface protective film increases with the increase in the concentration of the phosphoric acid solution, so that the silicon nitride film to be etched can be largely etched. However, the silicon oxide film that was not the object of etching was etched more than necessary, and a desired etching selectivity was not obtained.

【0011】このように、処理液が燐酸溶液の場合に、
純水の補充が燐酸溶液の濃度を決定しており、その燐酸
溶液の濃度がエッチングレートに大きく影響する。従来
では、ウエハ投入による液温度の低下を抑制するために
純水の補充停止制御を行っていたが、燐酸溶液中への基
板浸漬前に、その浸漬する基板全体の熱容量に応じた熱
量分だけ予め処理液温度を変化させるようにすれば、ウ
エハ投入時に低下する処理液温度が大幅に抑制されるこ
とから、その純水補充の停止制御をする必要がなくなっ
て、燐酸溶液の濃度は常に略一定化しており、従来のよ
うな燐酸溶液の濃度の上昇による窒化膜と酸化膜のエッ
チング選択比の低下が大幅に抑制可能となって、所望の
エッチング選択比が得られることになる。
Thus, when the treatment liquid is a phosphoric acid solution,
The replenishment of pure water determines the concentration of the phosphoric acid solution, and the concentration of the phosphoric acid solution greatly affects the etching rate. In the past, pure water replenishment stop control was performed to suppress a drop in the liquid temperature due to wafer input.However, before immersion of the substrate in the phosphoric acid solution, only a heat amount corresponding to the heat capacity of the entire substrate to be immersed was used. If the temperature of the processing solution is changed in advance, the temperature of the processing solution which drops when the wafer is charged is greatly suppressed, so that it is not necessary to control the stoppage of the replenishment of pure water, and the concentration of the phosphoric acid solution is almost always reduced. It is constant, and the decrease in the etching selectivity between the nitride film and the oxide film due to the increase in the concentration of the phosphoric acid solution as in the prior art can be largely suppressed, and a desired etching selectivity can be obtained.

【0012】[0012]

【発明の実施の形態】以下、本発明の実施形態について
図面を参照して説明するが、本発明は以下に示す実施形
態に限定されるものではない。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, embodiments of the present invention will be described with reference to the drawings, but the present invention is not limited to the following embodiments.

【0013】図1は本発明の一実施形態における基板処
理装置を組み込んでなるウエットステーションの概略構
成を示す平面図であり、矢印Fで示される面が装置の正
面である。
FIG. 1 is a plan view showing a schematic configuration of a wet station incorporating a substrate processing apparatus according to an embodiment of the present invention, and the surface indicated by arrow F is the front of the apparatus.

【0014】図1において、ウエットステーション1
は、複数のウエハ2を収容したキャリア3から、各処理
槽へ複数のウエハ2を搬送するための搬送用ロボット
(図示せず)に対して複数のウエハ2を一括して移載す
る搬入側のウエハ移替部5と、これとは逆に、搬送用ロ
ボット(図示せず)からキャリア3に複数のウエハ2を
一括して移載する搬出側のウエハ移替部6と、このウエ
ハ移替部5に隣接し、薬液または純水である各種処理液
をそれぞれ貯留した複数の処理槽にわたってウエハ2を
順次浸漬させることによりウエハ2に薬液処理や水洗処
理などの一連の各種処理が施される処理ユニット7と、
この処理ユニット7と搬出側のウエハ移替部6との間に
配設され、処理ユニット7で処理後のウエハ2をスピン
乾燥させる乾燥部8とを有している。
In FIG. 1, wet station 1
Is a transfer side for collectively transferring a plurality of wafers 2 from a carrier 3 containing a plurality of wafers 2 to a transfer robot (not shown) for transferring the plurality of wafers 2 to each processing tank. And a conveyer-side wafer transfer unit 6 for transferring a plurality of wafers 2 from the transfer robot (not shown) to the carrier 3 at once, The wafer 2 is successively immersed in a plurality of processing tanks adjacent to the replacement unit 5 and each storing various processing liquids such as a chemical liquid or pure water, thereby performing a series of various processings such as a chemical liquid processing and a water washing processing. Processing unit 7,
A drying unit 8 is provided between the processing unit 7 and the wafer transfer unit 6 on the unloading side and spin-drys the processed wafer 2 by the processing unit 7.

【0015】この処理ユニット7は、これらの各処理槽
に複数のウエハ2を搬送するための搬送用ロボット(図
示せず)のハンド部分を洗浄するハンド洗浄部9と、こ
のハンド洗浄部9側に隣接し、本発明の基板処理装置の
一実施形態であって、処理液としてのエッチング液など
の薬液を貯留した薬液槽を有し、この薬液槽にウエハ2
を浸漬することで薬液処理すると共に、詳細に後述する
が、その薬液中への基板浸漬前に、その浸漬する基板全
体の熱容量に応じた熱量分だけ予め薬液の温度を上げて
おく機能を有した第1の薬液処理部10および第2の薬
液処理部11と、この薬液処理部11側に隣接し、ウエ
ハ2に付いた燐酸を素早く水洗する機能水洗処理部12
と、この機能水洗処理部12側に隣接し、ウエハ2を最
終的に水洗する最終水洗処理部13とを処理工程順に有
している。
The processing unit 7 includes a hand cleaning unit 9 for cleaning a hand portion of a transfer robot (not shown) for transferring a plurality of wafers 2 to each of the processing tanks, and a side of the hand cleaning unit 9. Is an embodiment of the substrate processing apparatus of the present invention, which has a chemical solution tank storing a chemical solution such as an etching solution as a processing solution.
The substrate has a function of preliminarily raising the temperature of the chemical solution by an amount corresponding to the heat capacity of the entire substrate to be immersed before the substrate is immersed in the chemical solution, as will be described in detail later. The first and second chemical treatment units 10 and 11 and a functional water treatment unit 12 that is adjacent to the chemical treatment unit 11 and quickly rinses phosphoric acid attached to the wafer 2 with water.
And a final rinsing section 13 adjacent to the functional rinsing section 12 and finally rinsing the wafer 2 with water.

【0016】第1および第2の薬液処理部10,11を
設けたのは、これらの薬液処理部10,11による薬液
処理が他の処理部による処理に比べて時間がかかるた
め、処理タクトを短縮するべく並行して薬液処理を行う
ためである。
The first and second chemical processing units 10 and 11 are provided because the chemical processing by these chemical processing units 10 and 11 takes a longer time than the processing by other processing units. This is because a chemical solution treatment is performed in parallel to shorten the time.

【0017】ここでは、第1の薬液処理部10について
本発明の基板処理装置の一実施形態を、窒化膜除去用の
薬液として燐酸溶液の場合について以下に詳細に説明す
ることにし、第2の薬液処理部11についても第1の薬
液処理部10の場合と同様の構成である。
Here, an embodiment of the substrate processing apparatus according to the present invention will be described in detail with respect to the first chemical processing section 10 in the case where a phosphoric acid solution is used as a chemical for removing a nitride film. The chemical processing section 11 has the same configuration as that of the first chemical processing section 10.

【0018】図2は図1の第1の薬液処理部10の概略
要部構成を示す模式図である。図2において、本発明の
一実施形態の基板処理装置を構成している第1の薬液処
理部10は、燐酸溶液21を貯留可能で、その燐酸溶液
21中に複数のウエハ2を浸漬自在なように上方が矩形
状に開放された燐酸処理槽22と、複数のウエハ2をア
ーム部材23aで保持した状態で燐酸処理槽22の内外
を上下移動自在なリフタ装置23と、この燐酸処理槽2
2からオーバーフローした燐酸溶液21を燐酸処理槽2
2内に戻して循環させる処理液循環手段24とを有して
いる。
FIG. 2 is a schematic diagram showing a schematic configuration of a main part of the first chemical liquid processing section 10 of FIG. In FIG. 2, a first chemical processing section 10 constituting a substrate processing apparatus according to one embodiment of the present invention can store a phosphoric acid solution 21 and can immerse a plurality of wafers 2 in the phosphoric acid solution 21. A phosphoric acid treatment tank 22 having a rectangular opening at the top as described above, a lifter device 23 capable of vertically moving inside and outside the phosphoric acid treatment tank 22 while holding a plurality of wafers 2 by arm members 23a,
Phosphoric acid solution 21 overflowing from 2
And a treatment liquid circulating means 24 for circulating the treatment liquid back into the apparatus.

【0019】この薬液処理槽21内には燐酸溶液21と
共に純水(DIW)が供給されて満たされている。この
燐酸処理槽22の上部外周部分には、オーバーフローし
た燐酸溶液21を受けるオーバーフロー槽25が設けら
れている。また、この燐酸処理槽22の底部には、内部
に燐酸溶液21を循環供給する一対の管状の処理液供給
部26が備えられており、これらの一対の管状の処理液
供給部26にはそれぞれ互いに、燐酸処理槽22内の中
央部に向けて開口した処理液吐出用の複数のノズル口
(図示せず)を有している。
The chemical solution treatment tank 21 is filled with pure water (DIW) together with the phosphoric acid solution 21. An overflow tank 25 for receiving the overflowed phosphoric acid solution 21 is provided on the upper outer peripheral portion of the phosphoric acid treatment tank 22. Further, a pair of tubular processing liquid supply units 26 for circulating and supplying the phosphoric acid solution 21 therein is provided at the bottom of the phosphoric acid processing tank 22. Each has a plurality of nozzle ports (not shown) for discharging the processing liquid, which are opened toward the central part in the phosphoric acid processing tank 22.

【0020】また、処理液循環手段24は、オーバーフ
ロー槽25の底部と配管接続されている循環ポンプ27
と、この循環ポンプ27によって循環している燐酸溶液
21の温度を制御して調整するヒータ電子冷熱による温
度調節器28と、パーティクルなどの汚染物質を燐酸溶
液21から漉して取り除くフィルタ29と、上記一対の
管状の処理液供給部26とが各配管24aで順次連結さ
れている。これによって、この燐酸溶液21は、その燐
酸処理時に、一対の管状の処理液供給部26の複数のノ
ズル口(図示せず)から燐酸処理槽22内に供給され、
槽内下部から上部さらに槽外周側に向かう液流れを形成
しつつ、複数のウエハ2の表面から脱落したパーティク
ルなどの汚染物質と共に燐酸処理槽22の上部開口部2
2aからオーバーフローさせ、これをオーバーフロー槽
25で受けて循環ポンプ27さらに温度調節器28を介
してフィルタ29で漉してリフレッシュさせた後に、一
対の管状の処理液供給部26から再び燐酸処理槽22内
に戻されるようになっている。
The processing liquid circulating means 24 is provided with a circulating pump 27 connected to the bottom of the overflow tank 25 by piping.
A temperature controller 28 for controlling and adjusting the temperature of the phosphoric acid solution 21 circulated by the circulation pump 27 by means of a heater electronic cooling system; a filter 29 for filtering contaminants such as particles from the phosphoric acid solution 21 by filtering; A pair of tubular processing liquid supply units 26 are sequentially connected by respective pipes 24a. Thereby, the phosphoric acid solution 21 is supplied into the phosphoric acid treatment tank 22 from the plurality of nozzle ports (not shown) of the pair of tubular treatment liquid supply units 26 during the phosphoric acid treatment,
The upper opening 2 of the phosphoric acid treatment tank 22 is formed together with contaminants such as particles dropped from the surfaces of the plurality of wafers 2 while forming a liquid flow from the lower part in the tank to the upper part and further to the outer peripheral side of the tank.
After overflowing from the overflow treatment tank 2a and receiving it in the overflow tank 25 and straining it with the filter 29 through the circulation pump 27 and the temperature controller 28 to refresh it, the pair of tubular treatment liquid supply units 26 again feed the phosphoric acid treatment tank 22 Is to be returned to.

【0021】さらに、これらのリフタ装置23の駆動部
(図示せず)、循環ポンプ27および温度調節器28の
各制御端子にそれぞれ接続されている制御手段30は、
シーケンサやマイクロコンピュータなどで構成されてお
り、シーケンサやマイクロコンピュータからの制御信号
でリフタ装置23の駆動部、循環ポンプ27および温度
調節器28をそれぞれ制御することで、燐酸処理槽22
内に供給された燐酸溶液21中にリフタ装置23で複数
のウエハ2を浸漬させる前に、その浸漬する複数のウエ
ハ2全体の熱容量に応じた熱量分だけ予め燐酸溶液23
の温度を変化(上昇または下降)させるように温度調整
手段28を制御するようになっており、これによって、
燐酸溶液21中への複数のウエハ2の投入時にも、燐酸
溶液21による所望のエッチング量などの薬液処理量を
得るように構成されている。
Further, control means 30 respectively connected to the drive section (not shown) of the lifter device 23, the control terminals of the circulation pump 27 and the temperature controller 28,
The phosphating tank 22 includes a sequencer and a microcomputer, and controls the drive unit of the lifter device 23, the circulating pump 27 and the temperature controller 28 by control signals from the sequencer and the microcomputer.
Before the plurality of wafers 2 are immersed in the phosphoric acid solution 21 supplied to the inside by the lifter device 23, the phosphoric acid solution 23 is preliminarily prepared by an amount of heat corresponding to the heat capacity of the plurality of wafers 2 to be immersed.
The temperature adjusting means 28 is controlled so as to change (increase or decrease) the temperature.
Even when a plurality of wafers 2 are put into the phosphoric acid solution 21, a chemical processing amount such as a desired etching amount by the phosphoric acid solution 21 is obtained.

【0022】つまり、複数のウエハ2が燐酸溶液21中
に投入されたときに、その液温度が低下するが、その低
下する液温度分を予めウエハ投入前に上げておき、複数
のウエハ2が燐酸溶液21中に投入されて低下する液温
度を相殺して抑制するようになっている。実際には、制
御手段30は、浸漬すべき複数のウエハ2の口径をセン
サ手段(図示せず)などでセンシングすると共に、その
枚数をカウンタ手段(図示せず)などでカウントするこ
とで、浸漬すべき複数のウエハ2の口径と枚数の情報を
得、その口径と枚数のウエハ2を含む投入物(ウエハ2
の他にリフタ装置23のアーム部材23aなどを含んで
いる)の熱容量を計算し、その計算値に応じて図3に示
すように予め液温度を上げるように、温度調整手段28
に供給する電流量を制御して出力するようになってお
り、従来のようにウエハ投入による液温度の変化(液温
度の低下)はなく、最適温度でエッチングレートは低下
しないようになっている。この熱容量の計算は、ウエハ
2の口径および枚数毎の電流制御における例えば各実験
データ値などのデータをメモリ部(図示せず)に記憶さ
せておき、ウエハ2の口径および枚数に応じたデータよ
って、制御手段30が温度調整手段28に供給する電流
量を制御して出力するようにしている。
That is, when a plurality of wafers 2 are put into the phosphoric acid solution 21, the temperature of the solution decreases. The temperature of the solution that is introduced into the phosphoric acid solution 21 and decreases is offset and suppressed. Actually, the control means 30 senses the diameters of the plurality of wafers 2 to be immersed by the sensor means (not shown) or the like, and counts the number of the wafers by the counter means (not shown) or the like to thereby immerse the wafers. Information on the diameter and the number of wafers 2 to be obtained is obtained, and the input material (the wafer 2
In addition to the above, the heat capacity of the lifter device 23 (including the arm member 23a, etc.) is calculated, and the temperature adjusting means 28 is increased according to the calculated value so as to raise the liquid temperature in advance as shown in FIG.
The amount of current supplied to the wafer is controlled and output, so that there is no change in the liquid temperature (lowering of the liquid temperature) due to the introduction of the wafer as in the prior art, and the etching rate does not decrease at the optimum temperature. . This heat capacity is calculated by storing data such as experimental data values in current control for each diameter and number of wafers 2 in a memory unit (not shown), and using data corresponding to the diameter and number of wafers 2. The control means 30 controls and outputs the amount of current supplied to the temperature adjusting means 28.

【0023】また、このように、処理液としてのエッチ
ング液が燐酸溶液の場合には、蒸発分を補う純水の補充
が燐酸溶液21の濃度を決定しており、その燐酸溶液2
1の濃度がエッチングレートに大きく影響するため、従
来は、ウエハ投入による液温度の低下を抑制するために
純水の補充停止制御を行っていたが、その純水補充の停
止制御の必要がなくなることから図4に示すように燐酸
溶液21の濃度は変化せず、従来のような燐酸溶液21
の濃度上昇によるエッチング選択比の低下を大幅に抑制
することができるようになっている。
As described above, when the etching solution as the processing solution is a phosphoric acid solution, the concentration of the phosphoric acid solution 21 is determined by the replenishment of pure water which compensates for the evaporation.
Since the concentration of 1 has a great influence on the etching rate, conventionally, the control of stopping the replenishment of pure water has been performed in order to suppress a decrease in the liquid temperature due to the introduction of the wafer. Therefore, the concentration of the phosphoric acid solution 21 does not change as shown in FIG.
In this case, a decrease in the etching selectivity due to an increase in the concentration of GaN can be greatly suppressed.

【0024】具体的には、例えば口径8インチで50枚
のウエハ2が、薬液量20リットルの燐酸溶液21中に
浸漬させてエッチング処理をすると共に、循環ポンプ2
7の液供給能力が12リットル/minでオーバーフロ
ー循環させている場合、液温度が摂氏160度設定のと
ころ、ウエハ投入前の所定時間だけ摂氏160度+摂氏
3度に設定し、かつ、それ以外の期間では通常の最適温
度の摂氏160度になるように設定することで、ウエハ
投入による液温度の低下が防止されて最適温度でエッチ
ング処理が為され、従来の液温度低下時に比べて窒化膜
のエッチングレートが早く、また、異なる観点からは、
エッチング処理時間が短く構成でき、さらに、エッチン
グ対象の窒化膜と保護膜としての酸化膜とのエッチング
選択比が大きくなって、酸化膜をエッチングせず窒化膜
をエッチングするように働いて、そのエッチング選択比
を所望どうりに得ることができるようになっている。
More specifically, for example, 50 wafers 2 having a diameter of 8 inches are immersed in a phosphoric acid solution 21 having a chemical volume of 20 liters to perform an etching process and a circulation pump 2
7, when the liquid supply capacity is 12 l / min, the liquid temperature is set to 160 degrees Celsius, and the liquid temperature is set to 160 degrees Celsius + 3 degrees Celsius only for a predetermined time before wafer introduction, and otherwise. In the period, the temperature is set to be 160 degrees Celsius, which is the normal optimum temperature, so that the liquid temperature is prevented from lowering due to the introduction of the wafer, and the etching process is performed at the optimum temperature. Etching rate is fast, and from a different perspective,
The etching processing time can be configured to be short, and the etching selectivity between the nitride film to be etched and the oxide film as a protective film is increased, so that the nitride film is etched without etching the oxide film. The selection ratio can be obtained as desired.

【0025】なお、ここでは、図3に示すように摂氏3
度だけプレヒート処理してウエハ投入時に摂氏2度程度
温度低下があったが、プレヒート処理はこれに限らず、
摂氏4度だけ増えるようにプレヒート処理すればウエハ
投入時に摂氏1度程度の温度低下し、また、摂氏5度だ
け増えるようにプレヒート処理すればウエハ投入時に殆
ど温度低下がない。ところが、その増加させる液温度が
高いほど、蒸発量が多くなって更なる純水の補充が必要
となり、純水の補充で温度上昇が鈍ることになって、プ
レヒート処理に時間がかかるようになる。
In this case, as shown in FIG.
The temperature was lowered by about 2 degrees Celsius when the wafer was loaded after the preheating process, but the preheating process is not limited to this.
If the preheating process is performed so as to increase the temperature by 4 degrees Celsius, the temperature decreases by about 1 degree Celsius when the wafer is input, and if the preheating process is performed so that the temperature increases by 5 degrees Celsius, the temperature hardly decreases when the wafer is input. However, the higher the temperature of the liquid to be increased, the more the amount of evaporation increases, and the need for further replenishment of pure water is required. .

【0026】上記構成により、以下、その動作を説明す
る。まず、クリーンルーム内にウエットステーション1
が設置されており、オペレータは、正面方向からこのウ
エハ搬入側のウエハ移載部5における第1のテーブル上
に各キャリア3をそれぞれ載置する。その後、オペレー
タによるスイッチ操作で駆動を開始して、複数のウエハ
2を収容したキャリア3からウエハ移替部5を介して搬
送用ロボットに複数のウエハ2を一括して移載する。
The operation of the above configuration will be described below. First, wet station 1 in the clean room
The operator places each carrier 3 on the first table in the wafer transfer unit 5 on the wafer loading side from the front direction. Thereafter, driving is started by a switch operation by the operator, and the plurality of wafers 2 are collectively transferred from the carrier 3 containing the plurality of wafers 2 to the transfer robot via the wafer transfer unit 5.

【0027】次に、複数のウエハ2は、搬送用のロボッ
トハンド(図示せず)によってリフタ装置22に受け渡
され、このリフタ装置22にて複数のウエハ2は一括し
て処理ユニット7の第1および第2の薬液処理部10,
11の各燐酸処理槽22内の燐酸溶液中に浸漬されてエ
ッチング処理がそれぞれ施される。
Next, the plurality of wafers 2 are transferred to the lifter device 22 by a transfer robot hand (not shown), and the plurality of wafers 2 are collectively collected by the lifter device 22 in the processing unit 7. The first and second chemical processing units 10,
11 is immersed in a phosphoric acid solution in each of the phosphoric acid treatment tanks 22 to perform an etching treatment.

【0028】この処理ユニット7における第1および第
2の薬液処理部10,11の動作について以下に詳細に
説明する。
The operation of the first and second chemical processing units 10 and 11 in the processing unit 7 will be described in detail below.

【0029】まず、薬液循環オーバーフロー工程で、制
御手段30は、処理液循環手段24の循環ポンプ27を
駆動制御して、燐酸溶液21は一対の管状の処理液供給
部26の複数のノズル口(図示せず)から燐酸処理槽2
2内に燐酸溶液21が供給され、燐酸溶液21は槽内を
上昇してさらにその外周側に放射状に流れつつ、燐酸処
理槽22の上方外周の上部開口部22aからオーバーフ
ロー槽25内にオーバーフローし、オーバーフロー槽2
5から循環ポンプ27さらに温度調節器28で設定温度
に調整されてフィルタ29で漉された後に、一対の管状
の処理液供給部26から再び燐酸処理槽22内に循環さ
れる。
First, in the chemical solution circulating overflow step, the control means 30 controls the driving of the circulation pump 27 of the processing liquid circulating means 24 so that the phosphoric acid solution 21 is provided with a plurality of nozzle openings (a plurality of nozzle openings) of a pair of tubular processing liquid supply portions 26. Phosphating tank 2 (not shown)
The phosphoric acid solution 21 is supplied into the tank 2, and the phosphoric acid solution 21 rises in the tank and flows radially to the outer peripheral side thereof, and overflows into the overflow tank 25 from the upper opening 22 a on the upper outer periphery of the phosphoric acid treatment tank 22. , Overflow tank 2
From 5, the temperature is adjusted to a set temperature by a circulation pump 27 and a temperature controller 28, filtered by a filter 29, and then circulated again from the pair of tubular processing solution supply units 26 into the phosphating tank 22.

【0030】次に、燐酸処理槽22に対して上昇した状
態で、図示しない搬送用ロボットから複数のウエハ2を
受け取った後に、ウエハ投入工程に移行するが、そのウ
エハ投入前の所定期間だけ、制御手段30は、浸漬すべ
き複数のウエハ2の口径をセンサ手段(図示せず)など
でセンシングすると共に、その枚数をカウンタ手段(図
示せず)などでカウントすることで、浸漬すべき複数の
ウエハ2の口径と枚数の情報を得、その口径と枚数のウ
エハ2を含む投入物の熱容量を計算し、その計算値に応
じた温度調整手段28への供給電流量を制御して、ウエ
ハ投入時の液温度の低下分を相殺するように予めウエハ
投入前に液温度を上げるようにしておく。
Next, after receiving a plurality of wafers 2 from a transfer robot (not shown) in a state of being raised with respect to the phosphoric acid treatment tank 22, the process proceeds to a wafer loading step. The control means 30 senses the diameters of the plurality of wafers 2 to be immersed by a sensor means (not shown) or the like, and counts the number of the wafers by a counter means (not shown) or the like, so that a plurality of wafers 2 to be immersed. Information on the diameter and the number of wafers 2 is obtained, the heat capacity of the input material including the wafers with the diameter and the number of wafers 2 is calculated, and the amount of current supplied to the temperature adjusting means 28 according to the calculated value is controlled. The liquid temperature is increased in advance before the wafer is charged so as to offset the decrease in the liquid temperature at the time.

【0031】さらに、ウエハ投入工程で、制御手段30
はリフタ装置23を制御して、リフタ装置23を所定の
下位置まで下降させて複数のウエハ2を一括して燐酸処
理槽22内の燐酸溶液21中に浸漬させる。このとき、
燐酸処理槽22内の底部の両側に配設された一対の管状
の処理液供給部26から燐酸溶液21を複数の各ウエハ
2に向けて供給し続けて、燐酸処理槽22の上部開口端
22aから燐酸溶液21をオーバーフローさせた状態を
維持し、複数のウエハ2の表面に対して燐酸溶液21に
よるエッチング処理を行い、この処理で発生したパーテ
ィクルなどの汚染物質を槽外のオーバーフロー槽25内
にオーバーフローさせて流し出す。さらに、オーバーフ
ロー槽25からの燐酸溶液は、循環ポンプ27から温度
調節器28で液温度を一定温度に保持しつつ、さらにフ
ィルタ29でパーティクルなどの汚染物質が漉されてリ
フレッシュされた後に、一対の管状の処理液供給部26
から再び燐酸処理槽22内に戻される。
Further, in the wafer loading step, the control means 30
Controls the lifter device 23, lowers the lifter device 23 to a predetermined lower position, and immerses the plurality of wafers 2 collectively in the phosphoric acid solution 21 in the phosphoric acid treatment tank 22. At this time,
The phosphoric acid solution 21 is continuously supplied to the plurality of wafers 2 from the pair of tubular processing liquid supply units 26 disposed on both sides of the bottom in the phosphoric acid treatment tank 22, and the upper open end 22a of the phosphoric acid treatment tank 22 The surface of the plurality of wafers 2 is etched with the phosphoric acid solution 21 while maintaining the state in which the phosphoric acid solution 21 overflows, and contaminants such as particles generated by this processing are transferred into the overflow tank 25 outside the tank. Let it overflow and pour out. Further, the phosphoric acid solution from the overflow tank 25 is maintained at a constant temperature by the temperature controller 28 from the circulating pump 27, and after the contaminants such as particles are filtered by the filter 29 and refreshed, a pair of the phosphoric acid solution is refreshed. Tubular processing liquid supply unit 26
From the phosphating tank 22 again.

【0032】さらに、制御手段30は各部を制御して所
定の薬液処理時間だけこの状態を維持し所定濃度の燐酸
溶液21内に複数のウエハ2を一括して浸漬することで
所定のエッチング処理を行う。さらに、制御手段30は
薬液処理時間を計時手段(図示せず)で計時すると、ウ
エハ2の払出工程に移行する。
Further, the control means 30 controls each part to maintain this state for a predetermined chemical solution processing time, and immerses a plurality of wafers 2 collectively in a phosphoric acid solution 21 of a predetermined concentration to perform a predetermined etching process. Do. Further, when the control unit 30 measures the chemical solution processing time by a timer unit (not shown), the control unit 30 shifts to the wafer 2 dispensing process.

【0033】このウエハ2の払出工程では、制御手段3
0はリフタ装置23を制御して、リフタ装置23と共に
複数のウエハ2を燐酸溶液21の液面上の所定の上位置
まで上昇制御させる。複数のウエハ2を燐酸溶液21上
に位置させた状態で、図示しない搬送用ロボットに複数
のウエハ2を引き渡して次工程に搬送させることにな
る。
In the step of dispensing the wafer 2, the control means 3
Numeral 0 controls the lifter device 23 so as to raise the plurality of wafers 2 together with the lifter device 23 to a predetermined upper position on the surface of the phosphoric acid solution 21. With the plurality of wafers 2 positioned on the phosphoric acid solution 21, the plurality of wafers 2 are delivered to a transfer robot (not shown) and transferred to the next step.

【0034】このようにして、第1および第2の薬液処
理部10,11における薬液処理が終了し、さらに、機
能水洗処理部12でウエハ2を機能水洗し、さらに最終
水洗処理部13でウエハ2を最終的に水洗した後に、複
数のウエハ2を乾燥部8でスピン乾燥する。以上のよう
にして、所定の表面処理が為されスピン乾燥された複数
のウエハ2は搬出側のウエハ移替部6のキャリア4内に
搬送用ロボット(図示せず)で搬送されて回収され、搬
出側のウエハ移替部6において、上記ウエハ移替部5の
場合とは逆に、2個の搬送用のキャリア3に2つのウエ
ハ群に分けられて前後のキャリア3内にそれぞれ移し替
えられることになる。オペレータは、処理済みの複数の
ウエハ2が収容された2つのキャリア3を搬出すればよ
い。
In this manner, the chemical processing in the first and second chemical processing units 10 and 11 is completed, the wafer 2 is functionally washed in the functional water washing unit 12, and the wafer 2 is further washed in the final water washing unit 13. After the wafer 2 is finally washed with water, the plurality of wafers 2 are spin-dried in the drying unit 8. As described above, the plurality of wafers 2 that have been subjected to the predetermined surface treatment and spin-dried are transferred into the carrier 4 of the wafer transfer unit 6 on the unloading side by the transfer robot (not shown) and collected. In the wafer transfer unit 6 on the unloading side, contrary to the case of the wafer transfer unit 5, the wafer is divided into two wafer groups into two transfer carriers 3 and transferred into the front and rear carriers 3 respectively. Will be. The operator may unload the two carriers 3 containing the processed wafers 2.

【0035】以上により、複数のウエハ2をリフタ装置
23によって燐酸処理槽22内の燐酸溶液21中に浸漬
させる前に、その複数のウエハ2を含む投入部材全体の
熱容量に応じた熱量分だけ予め処理液温度を上げるよう
に、制御手段30は温度調整器28に対する供給電流量
を制御するため、ウエハ2の投入時に低下する燐酸溶液
21の液温度を大幅に抑制することができて、燐酸溶液
21中へのウエハ2の投入時にも所望のエッチング量を
得ることができる。
As described above, before the plurality of wafers 2 are immersed in the phosphoric acid solution 21 in the phosphoric acid treatment tank 22 by the lifter device 23, the amount of heat corresponding to the total heat capacity of the input member including the plurality of wafers 2 is previously determined. Since the control means 30 controls the amount of current supplied to the temperature controller 28 so as to increase the temperature of the processing solution, the temperature of the solution of the phosphoric acid solution 21 which decreases when the wafer 2 is charged can be greatly suppressed. A desired etching amount can be obtained even when the wafer 2 is loaded into the substrate 21.

【0036】また、処理液が燐酸溶液21の場合に、純
水の補充が燐酸溶液21の濃度を決定しており、その燐
酸溶液21の濃度がエッチングレートに大きく影響する
が、ウエハ2の投入時に低下する燐酸溶液21の温度が
大幅に抑制されることから、その純水補充の停止制御を
する必要がなく、その燐酸溶液21の濃度を一定にする
ことができて、エッチング対象の窒化膜と保護膜として
の酸化膜とのエッチング選択比の低下を大幅に抑制する
ことができる。
When the processing solution is the phosphoric acid solution 21, the replenishment of pure water determines the concentration of the phosphoric acid solution 21, and the concentration of the phosphoric acid solution 21 greatly affects the etching rate. Since the temperature of the phosphoric acid solution 21, which is sometimes reduced, is greatly suppressed, it is not necessary to control the stoppage of the replenishment of the pure water, so that the concentration of the phosphoric acid solution 21 can be kept constant and the nitride film to be etched can be formed. It is possible to greatly suppress a decrease in the etching selectivity between the oxide film and the protective film.

【0037】なお、上記実施形態のウエットステーショ
ン1は、本発明に係る第1および第2の薬液処理部1
0,11が適用される多槽式基板処理装置の一例であっ
て、その具体的な構成は、本発明の要旨を逸脱しない範
囲で適宜変更可能である。例えば、多槽式基板処理装置
だけではなく、単槽式基板処理装置に対しても、処理液
の急速排液を行って滞留部分を解消しつつ処理液を戻す
場合に適用可能なことはいうまでもないことである。ま
た、上記実施形態の処理ユニット7では、一連の各種薬
液処理として、窒化膜除去のエッチング処理の槽構成に
ついて説明してきたが、この窒化膜除去のエッチング処
理の他に、レジスト膜剥離処理、酸化膜エッチング処
理、ライトエッチング処理および拡散前洗浄処理などの
各種薬液処理であってもよいことは言うまでもないこと
である。
It should be noted that the wet station 1 of the above embodiment is provided with the first and second chemical processing units 1 according to the present invention.
This is an example of a multi-tank type substrate processing apparatus to which 0 and 11 are applied, and the specific configuration thereof can be appropriately changed without departing from the gist of the present invention. For example, it can be applied not only to a multi-tank type substrate processing apparatus but also to a single-tank type substrate processing apparatus, in which the processing liquid is rapidly drained to eliminate the stagnation portion and return the processing liquid. It is not even. Further, in the processing unit 7 of the above embodiment, the tank configuration of the etching process for removing the nitride film has been described as a series of various types of chemical solution processes. It goes without saying that various chemical treatments such as a film etching treatment, a light etching treatment and a cleaning treatment before diffusion may be used.

【0038】[0038]

【発明の効果】以上のように本発明の請求項1によれ
ば、基板浸漬前に、その基板全体の熱容量に応じた熱量
分だけ予め処理液温度を変化させるため、ウエハ投入時
に低下する処理液温度を大幅に抑制することができて最
適温度で薬液処理を行うことができ、処理液中への基板
投入時にも所望のエッチング量などの処理量を得ること
ができる。
As described above, according to the first aspect of the present invention, since the temperature of the processing liquid is changed in advance by the amount of heat corresponding to the heat capacity of the entire substrate before immersion of the substrate, the processing temperature is reduced when the wafer is loaded. The temperature of the solution can be greatly suppressed, and the chemical solution can be processed at the optimum temperature, and a desired amount of processing such as an etching amount can be obtained even when the substrate is put into the processing solution.

【0039】また、本発明の請求項2によれば、処理液
がエッチング液としての燐酸溶液の場合に、純水の補充
が燐酸溶液の濃度を決定しており、その燐酸溶液の濃度
がエッチングレートに大きく影響するが、ウエハ投入時
に低下する燐酸溶液の温度が大幅に抑制されることか
ら、その純水補充の停止制御をする必要がなく、燐酸濃
度を一定にすることができて、窒化膜と酸化膜のエッチ
ング選択比の低下を大幅に抑制することができて、所望
のエッチング選択比を得ることができる。
According to the second aspect of the present invention, when the processing solution is a phosphoric acid solution as an etching solution, the replenishment of pure water determines the concentration of the phosphoric acid solution, and the concentration of the phosphoric acid solution is determined by the concentration of the etching solution. Although this greatly affects the rate, the temperature of the phosphoric acid solution, which drops when the wafer is charged, is greatly suppressed. Therefore, it is not necessary to control the stoppage of the replenishment of the pure water, and the phosphoric acid concentration can be kept constant, and A decrease in the etching selectivity between the film and the oxide film can be significantly suppressed, and a desired etching selectivity can be obtained.

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

【図1】本発明の一実施形態における基板処理装置を組
み込んでなるウエットステーションの概略構成を示す平
面図である。
FIG. 1 is a plan view showing a schematic configuration of a wet station incorporating a substrate processing apparatus according to an embodiment of the present invention.

【図2】図1の第1の薬液処理部の概略要部構成を示す
模式図である。
FIG. 2 is a schematic diagram showing a schematic configuration of a main part of a first chemical liquid processing unit in FIG. 1;

【図3】図2の薬液処理槽内のウエハ投入前後の処理液
温度の様子を示す図である。
FIG. 3 is a view showing a state of a processing liquid temperature before and after a wafer is charged in a chemical liquid processing tank of FIG. 2;

【図4】図2の薬液処理槽内のウエハ投入前後の処理液
濃度の様子を示す図である。
FIG. 4 is a diagram showing a state of a processing solution concentration before and after a wafer is charged in a chemical solution processing tank of FIG. 2;

【図5】従来の薬液処理槽内のウエハ投入前後の処理液
温度の様子を示す図である。
FIG. 5 is a diagram showing a state of a processing liquid temperature before and after a wafer is charged in a conventional chemical liquid processing tank.

【図6】従来の薬液処理槽内のウエハ投入前後の処理液
濃度の様子を示す図である。
FIG. 6 is a diagram showing a state of a processing solution concentration before and after a wafer is charged in a conventional chemical solution processing tank.

【符号の説明】[Explanation of symbols]

1 ウエットステーション 2 半導体ウエハ 7 処理ユニット 10 第1の薬液処理部 11 第2の薬液処理部 22 薬液処理槽 23 リフタ装置 23a アーム部材 24 処理液循環手段 26 処理液供給部 27 循環ポンプ 28 温度調整手段 30 制御手段 Reference Signs List 1 wet station 2 semiconductor wafer 7 processing unit 10 first chemical processing section 11 second chemical processing section 22 chemical processing tank 23 lifter device 23a arm member 24 processing liquid circulation means 26 processing liquid supply section 27 circulation pump 28 temperature adjustment means 30 control means

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 処理槽内に供給された処理液中に基板を
浸漬させて処理を施す基板処理装置において、 前記処理液の温度を調整する温度調整手段と、 前記処理液中への基板浸漬前に、その浸漬する基板全体
の熱容量に応じた熱量分だけ予め処理液温度を変化させ
るように前記温度調整手段を制御する制御手段とを有す
ることを特徴とする基板処理装置。
1. A substrate processing apparatus for performing processing by immersing a substrate in a processing liquid supplied into a processing tank, wherein the substrate is immersed in the processing liquid. And a control means for controlling the temperature adjusting means so as to change the temperature of the processing liquid in advance by an amount of heat corresponding to the heat capacity of the entire substrate to be immersed.
【請求項2】 処理槽内に供給された燐酸溶液中に基板
を浸漬させて処理を施す基板処理装置において、 前記処理槽からオーバーフローした燐酸溶液を前記処理
槽内に戻して循環させる処理液循環手段に、循環してい
る燐酸溶液の温度を調整する温度調整手段が設けられ、
この温度調整手段に対して、燐酸溶液中への基板浸漬前
に、その浸漬する基板全体の熱容量に応じた熱量分だけ
予め処理液温度を変化させるように前記温度調整手段を
制御する制御手段が設けられていることを特徴とする基
板処理装置。
2. A substrate processing apparatus for performing processing by immersing a substrate in a phosphoric acid solution supplied into a processing tank, wherein the processing solution circulation circulates the phosphoric acid solution overflowing from the processing tank back into the processing tank. The means is provided with a temperature adjusting means for adjusting the temperature of the circulating phosphoric acid solution,
Before immersing the substrate in the phosphoric acid solution, the control means for controlling the temperature adjusting means so as to change the temperature of the treatment liquid by an amount of heat corresponding to the heat capacity of the entire substrate to be immersed before the immersion of the substrate in the phosphoric acid solution A substrate processing apparatus provided.
JP35296097A 1997-12-22 1997-12-22 Wafer processor Abandoned JPH11186217A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP35296097A JPH11186217A (en) 1997-12-22 1997-12-22 Wafer processor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP35296097A JPH11186217A (en) 1997-12-22 1997-12-22 Wafer processor

Publications (1)

Publication Number Publication Date
JPH11186217A true JPH11186217A (en) 1999-07-09

Family

ID=18427638

Family Applications (1)

Application Number Title Priority Date Filing Date
JP35296097A Abandoned JPH11186217A (en) 1997-12-22 1997-12-22 Wafer processor

Country Status (1)

Country Link
JP (1) JPH11186217A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20030086660A (en) * 2002-05-06 2003-11-12 삼성전자주식회사 Method and equipment for controlling chemical temperature in semiconductor product device
US7097784B2 (en) 2002-12-27 2006-08-29 Kabushiki Kaisha Toshiba Etching method and apparatus for semiconductor wafers
JP2008217058A (en) * 2007-02-28 2008-09-18 Dainippon Screen Mfg Co Ltd Schedule preparation method for substrate treatment apparatus, and its program
JP2009188048A (en) * 2008-02-04 2009-08-20 Mitsumi Electric Co Ltd Manufacturing method of semiconductor device, and wet etching device
JP2012015490A (en) * 2010-05-31 2012-01-19 Tokyo Electron Ltd Substrate processing device, substrate processing method, and recording medium recording computer program for executing the substrate processing method
CN103969965A (en) * 2014-05-12 2014-08-06 华中科技大学 Device for precisely controlling temperature of immersing liquid of immersed photoetching machine and temperature control method thereof
WO2024004725A1 (en) * 2022-07-01 2024-01-04 東京エレクトロン株式会社 Substrate treatment apparatus and substrate treatment method

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20030086660A (en) * 2002-05-06 2003-11-12 삼성전자주식회사 Method and equipment for controlling chemical temperature in semiconductor product device
US7097784B2 (en) 2002-12-27 2006-08-29 Kabushiki Kaisha Toshiba Etching method and apparatus for semiconductor wafers
JP2008217058A (en) * 2007-02-28 2008-09-18 Dainippon Screen Mfg Co Ltd Schedule preparation method for substrate treatment apparatus, and its program
JP2009188048A (en) * 2008-02-04 2009-08-20 Mitsumi Electric Co Ltd Manufacturing method of semiconductor device, and wet etching device
JP2012015490A (en) * 2010-05-31 2012-01-19 Tokyo Electron Ltd Substrate processing device, substrate processing method, and recording medium recording computer program for executing the substrate processing method
TWI490936B (en) * 2010-05-31 2015-07-01 Tokyo Electron Ltd A substrate processing apparatus, a substrate processing method, and a recording medium on which a computer program for carrying out the substrate processing method is recorded
CN103969965A (en) * 2014-05-12 2014-08-06 华中科技大学 Device for precisely controlling temperature of immersing liquid of immersed photoetching machine and temperature control method thereof
WO2024004725A1 (en) * 2022-07-01 2024-01-04 東京エレクトロン株式会社 Substrate treatment apparatus and substrate treatment method

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