JPH05190523A - Washing device - Google Patents

Washing device

Info

Publication number
JPH05190523A
JPH05190523A JP8764592A JP8764592A JPH05190523A JP H05190523 A JPH05190523 A JP H05190523A JP 8764592 A JP8764592 A JP 8764592A JP 8764592 A JP8764592 A JP 8764592A JP H05190523 A JPH05190523 A JP H05190523A
Authority
JP
Japan
Prior art keywords
pure water
tank
temperature
cleaning
liquid
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.)
Granted
Application number
JP8764592A
Other languages
Japanese (ja)
Other versions
JP3308586B2 (en
Inventor
Kenji Yokomizo
賢治 横溝
Shinya Murakami
信也 村上
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.)
Tokyo Electron Ltd
Tokyo Electron Kyushu Ltd
Original Assignee
Tokyo Electron Ltd
Tokyo Electron Kyushu 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 Tokyo Electron Ltd, Tokyo Electron Kyushu Ltd filed Critical Tokyo Electron Ltd
Priority to JP08764592A priority Critical patent/JP3308586B2/en
Publication of JPH05190523A publication Critical patent/JPH05190523A/en
Application granted granted Critical
Publication of JP3308586B2 publication Critical patent/JP3308586B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Cleaning Or Drying Semiconductors (AREA)

Abstract

PURPOSE:To cut down the time required for temperature adjustment for washing chemical liquid used for washing of semiconductor wafers, for example. CONSTITUTION:The feeding holes of a chemical solution feeding tube 3 and a pure water feeding tube 4 are arranged on the upper part of a washing treatment vessel 1 provided with a wafer retaining member 2 which can be freely moved vertically. A pure water tank 5 is connected to the inlet side of the pure water feeding tube 4. A heater 6 and an air feeding tube 7, with which nitrogen gas is fed, are provided in the tank 5, and at the same time, liquid level detecting parts 52 and 53, with which pure water is weighed, are arranged on the upper and the lower parts of the tank. After the prescribed quantity of pure water of room temperature has been introduced into the tank 5, the tank is heated up by a heater 6, bubbles are generated, and pure water is fed to a washing treatment vessel 1 after the set temperature is obtained.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、洗浄装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cleaning device.

【0002】[0002]

【従来の技術】半導体デバイスの製造工程においては、
半導体層、絶縁層、電極層など種々の膜が積層されてい
くが、ある層の表面に他の層を形成する場合、成膜時の
残渣、パーティクルや重金属などの不要な粒子が介在す
ると所定の特性が得られないため、これらの粒子がデバ
イス中に取り込まれないようにするために例えば成膜工
程間においてウエハに対して薬液により洗浄が行われ
る。
2. Description of the Related Art In the manufacturing process of semiconductor devices,
Various films such as semiconductor layers, insulating layers, and electrode layers are laminated, but when other layers are formed on the surface of a certain layer, residues such as particles during film formation, unnecessary particles such as heavy metals, etc. intervene in a predetermined amount. Therefore, in order to prevent these particles from being incorporated into the device, the wafer is cleaned with a chemical solution during the film forming process, for example.

【0003】このような洗浄を行うための装置として
は、例えば多数枚のウエハを保持する保持部材や、加熱
手段が設けられた洗浄処理槽と、アルカリ系あるいは酸
系の薬液を貯留した薬液タンクと、薬液を希釈して所定
濃度に設定するための純水を貯留する純水タンクなどか
ら構成される。そしてウエハを洗浄するためには、薬液
タンクから洗浄処理槽内に薬液を所定量注入すると共
に、純水タンクから純水を所定量注入し、洗浄処理槽内
で薬液と純水との混合液である洗浄液を循環させながら
加熱手段で加熱して所定温度に調整し、その後ウエハを
保持部材で保持した状態で洗浄液内に浸漬して洗浄を行
うようにしている。ここで洗浄液を室温から例えば40
〜90℃程度に昇温するためには長い時間がかかるた
め、簡易な手法の一つとして予め純水タンク内にてヒー
タにより純水を洗浄液の所定温度よりも若干高めに加熱
しておき、加熱された純水と薬液とを洗浄処理槽内にて
混合して洗浄液の温度の立上りを早めるようにすること
も行われている。
As an apparatus for performing such cleaning, for example, a holding member for holding a large number of wafers, a cleaning treatment tank provided with a heating means, and a chemical liquid tank storing an alkaline or acid chemical liquid. And a pure water tank for storing pure water for diluting the chemical liquid to set a predetermined concentration. Then, in order to clean the wafer, a predetermined amount of the chemical liquid is injected from the chemical liquid tank into the cleaning treatment tank, and a predetermined amount of pure water is injected from the pure water tank to mix the chemical liquid and the pure water in the cleaning treatment tank. The cleaning liquid is heated by a heating means while being circulated to adjust the temperature to a predetermined temperature, and then the wafer is held in a holding member and immersed in the cleaning liquid for cleaning. Here, the cleaning solution is heated from room temperature to,
Since it takes a long time to raise the temperature to about 90 ° C., one simple method is to previously heat pure water to a temperature slightly higher than the predetermined temperature of the cleaning liquid by the heater in the pure water tank. It has also been practiced to mix heated pure water and a chemical solution in a cleaning treatment tank so that the temperature of the cleaning solution rises faster.

【0004】[0004]

【発明が解決しようとする課題】ところでウエハの製造
工場内には一般に多数の処理ステーションや搬送系が密
集しているため、各処理ステーションをできるだけコン
パクト化する必要がある。このような事情に加えて洗浄
装置では通常夫々異なった薬液が供給される複数の洗浄
処理槽が設けられかつこれら洗浄処理槽間には各々リン
ス槽が配列されており、従って一つの洗浄処理槽ユニッ
トの占有面積を小さくするために種々の工夫がなされて
いる。例えば純水タンクについても底面積が狭く高さの
大きい構造とされているが、この場合ヒータの加熱時に
純水タンク内の上層部は設定温度まで昇温していても、
下層部の温度は設定温度より可成り低く、このため上層
部が設定温度になったときに当該純水を洗浄処理槽に供
給して薬液と混合しても、純水全体の温度は、上下に大
きな温度差があるため設定温度よりも可成り低いので、
結局洗浄処理槽内における洗浄液の温度調整時間の短縮
化を十分に図ることができない。特に今後ウエハが6イ
ンチから8インチへと移行しつつあるように大口径化し
てくると洗浄処理槽及び純水タンクも大型化してくるた
め、洗浄の温度調整時間は増々長くなって、スループッ
トの向上を妨げてしまうことになる。
By the way, since a large number of processing stations and transfer systems are generally concentrated in a wafer manufacturing factory, it is necessary to make each processing station as compact as possible. In addition to such a situation, the cleaning device is usually provided with a plurality of cleaning treatment tanks to which different chemicals are respectively supplied, and a rinse tank is arranged between these cleaning treatment tanks. Various measures have been taken to reduce the area occupied by the unit. For example, the deionized water tank also has a structure with a small bottom area and a large height. In this case, even if the upper layer of the deionized water tank is heated to the set temperature when the heater is heated,
The temperature of the lower layer is much lower than the set temperature.Therefore, when the upper layer reaches the set temperature, even if the pure water is supplied to the cleaning treatment tank and mixed with the chemical solution, the temperature of the entire pure water rises and falls. Since there is a large temperature difference in
After all, it is not possible to sufficiently shorten the time for adjusting the temperature of the cleaning liquid in the cleaning treatment tank. In particular, as the wafer size increases from 6 inches to 8 inches in the future, the cleaning processing tank and the deionized water tank also increase in size, so the cleaning temperature adjustment time becomes longer and throughput increases. It will hinder improvement.

【0005】なお、純水タンクにポンプを備えた循環路
を外付けするなどの構造を採用することも考えられる
が、この場合純水タンク及びその周辺の構造が複雑にな
ってしまい、先述したように簡易な手法で洗浄液の温度
調整時間を短縮化するという趣旨から大きく外れてしま
う。
It is also possible to adopt a structure in which a pure water tank is provided with a circulation path equipped with a pump, but in this case, the structure of the pure water tank and its surroundings becomes complicated, and the structure described above is adopted. As described above, the purpose of shortening the temperature adjustment time of the cleaning liquid by a simple method is largely deviated.

【0006】本発明は、このような事情のもとになされ
たものであり、その目的は、簡易な手法で洗浄液の温度
調整時間を短縮することのできる洗浄装置を提供するこ
とにある。
The present invention has been made under such circumstances, and an object thereof is to provide a cleaning device which can shorten the temperature adjustment time of the cleaning liquid by a simple method.

【0007】[0007]

【課題を解決するための手段】請求項1の発明は、薬液
と希釈液との混合液よりなり、温度調整された洗浄液に
被処理体を接触させて洗浄処理する洗浄装置において、
前記希釈液を温度調整するための温度調整手段と、前記
希釈液中に気泡を形成するためのバブリング手段とを設
けたことを特徴とする。
According to a first aspect of the present invention, there is provided a cleaning apparatus comprising a mixed solution of a chemical solution and a diluting solution, the cleaning solution having a temperature adjusted and brought into contact with an object to be cleaned,
A temperature adjusting means for adjusting the temperature of the diluent and a bubbling means for forming bubbles in the diluent are provided.

【0008】請求項2の発明は、薬液と希釈液槽よりの
希釈液よりなる温度調整された洗浄液に被処理体を接触
させて洗浄する洗浄装置において、前記希釈液槽の底面
部の一部領域に加熱手段を設け、この加熱手段により当
該一部領域と前記底面部のうち加熱手段の配置されてい
ない他部領域との間で対流による液流を形成することを
特徴とする。
According to a second aspect of the present invention, there is provided a cleaning apparatus for contacting and cleaning an object to be treated with a temperature-controlled cleaning liquid consisting of a chemical liquid and a diluting liquid from a diluting liquid tank. A heating means is provided in the area, and the heating means forms a convective liquid flow between the partial area and the other area of the bottom surface portion where the heating means is not arranged.

【0009】[0009]

【作用】請求項1の発明によれば希釈液槽内に例えば室
温の希釈液を所定量だけ供給し、温度調整手段例えば加
熱手段により希釈液を加熱すると共にバブリング手段に
よりバブリングすることによって希釈液が撹拌されるた
め均一に加熱される。
According to the first aspect of the invention, the diluent is supplied by supplying a predetermined amount of the diluent at room temperature into the diluent tank, heating the diluent by the temperature adjusting means such as the heating means and bubbling by the bubbling means. Is heated because it is stirred.

【0010】請求項2の発明によれば、希釈液槽内に例
えば室温の希釈液を所定量だけ供給して加熱手段をオン
にすると、加熱された希釈液が上昇し、更に加熱手段の
配置されていない領域に向かって横方向に流動すると共
に、加熱手段の配置されていない領域から加熱手段側に
温度の低い希釈液が流動して対流を形成するため希釈液
槽内の希釈液が均一に加熱される。従って例えば希釈液
の上層部が設定温度になった時点で洗浄処理槽内に薬液
と希釈液とが供給され、混合されながら加熱されるが、
希釈液全体の温度が高いため洗浄処理槽内における洗浄
液の温度調整が短くなる。その後被処理体が洗浄液内に
浸漬され洗浄が行われる。
According to the second aspect of the present invention, when the heating means is turned on by supplying a predetermined amount of the diluent at room temperature into the diluent tank, the heated diluent rises, and the heating means is arranged. The diluting liquid in the diluting liquid tank is uniform because the diluting liquid having a low temperature flows from the region in which the heating means is not arranged to the heating means side while flowing laterally toward the unheated area, thereby forming convection. Is heated to. Therefore, for example, when the upper layer of the diluting liquid reaches the set temperature, the chemical liquid and the diluting liquid are supplied into the cleaning treatment tank and heated while being mixed,
Since the temperature of the entire diluting liquid is high, the temperature adjustment of the cleaning liquid in the cleaning treatment tank becomes short. After that, the object to be processed is immersed in the cleaning liquid for cleaning.

【0011】[0011]

【実施例】以下本発明を半導体ウエハの洗浄装置に適用
した実施例について説明する。
EXAMPLE An example in which the present invention is applied to a semiconductor wafer cleaning apparatus will be described below.

【0012】(実施例1)図1及び図2は夫々本発明の
実施例1の概要を示す斜視図及び縦断正面図である。図
中1は、後述する薬液及び純水の混合液よりなる洗浄液
により被処理体としての半導体ウエハを洗浄するための
洗浄処理槽であって、上縁が越流(オ−バ−フロ−)部
をなすように波形に形成されており、上縁の外側には全
周を取り囲むように越流槽11が設けられている。この
洗浄処理槽1内には、多数のウエハWを垂直に立てた状
態で横方向に並べて保持するように、3本の保持アーム
21を備えた保持部材2が図示しない昇降機構により昇
降自在に配設されると共に、温度調整手段である加熱手
段(図示せず)が設けられている。前記洗浄処理槽1の
底部と越流槽11の底部との間には、図2に示すように
石英ガラス管やフレキシブルな樹脂チューブなどを組み
合わせ、かつポンプPを備えた循環水路12が接続され
ており、この循環水路12によって洗浄液が循環され
る。
(Embodiment 1) FIGS. 1 and 2 are a perspective view and a vertical sectional front view showing an outline of Embodiment 1 of the present invention, respectively. In the figure, reference numeral 1 denotes a cleaning tank for cleaning a semiconductor wafer as an object to be processed with a cleaning liquid composed of a mixed liquid of a chemical liquid and pure water, which will be described later, and an upper edge thereof overflows (overflow). An overflow tank 11 is provided outside the upper edge so as to surround the entire circumference. In the cleaning processing tank 1, a holding member 2 having three holding arms 21 is vertically movable by an elevating mechanism (not shown) so as to hold a large number of wafers W vertically arranged side by side. A heating means (not shown), which is a temperature adjusting means, is provided while being disposed. Between the bottom of the cleaning treatment tank 1 and the bottom of the overflow tank 11, a circulating water passage 12 including a quartz glass tube, a flexible resin tube, and the like and having a pump P is connected as shown in FIG. Therefore, the cleaning liquid is circulated by the circulating water passage 12.

【0013】前記洗浄処理槽1の上部には例えば各々石
英ガラス管よりなる薬液供給管3及び純水供給管4の供
給口が配置されており、薬液供給管3の入口側は図2に
示すようにバルブV1を介して例えば塩酸と過酸化水素
水とよりなる薬液を貯留するための薬液タンク31に接
続されると共に、純水供給管4の入口側はバルブV2を
介して希釈液としての純水を貯留するための希釈液槽を
なす純水タンク5に接続されている。
At the upper part of the cleaning treatment tank 1, there are arranged supply ports for a chemical liquid supply pipe 3 and a pure water supply pipe 4 each made of, for example, a quartz glass pipe, and the inlet side of the chemical liquid supply pipe 3 is shown in FIG. As described above, the valve V1 is connected to the chemical liquid tank 31 for storing the chemical liquid consisting of hydrochloric acid and hydrogen peroxide solution, and the inlet side of the pure water supply pipe 4 is used as a diluting liquid via the valve V2. It is connected to a pure water tank 5 which constitutes a diluting liquid tank for storing pure water.

【0014】前記純水タンク5内には、ガラス管内にニ
クロム線を挿入してなる温度調整手段としてのヒータ6
が底面付近に配置されると共に、ガスの出口が底部付近
に位置するバブリング手段としての例えば石英ガラス管
よりなる送気管7が設置されており、この送気管7はバ
ルブV3を介して例えば窒素ガス供給源71に接続され
ている。更に純水タンク5の底部には、当該タンク5内
に純水を供給するための給水管51の一端が接続されて
おり、この給水管51の他端側はバルブV4を介して工
場内の純水供給システムに接続されている。
In the pure water tank 5, a heater 6 as a temperature adjusting means is formed by inserting a nichrome wire into a glass tube.
Is arranged near the bottom surface, and an air supply pipe 7 made of, for example, a quartz glass pipe is installed as a bubbling means in which the gas outlet is located near the bottom portion. The air supply pipe 7 is provided with, for example, nitrogen gas through a valve V3. It is connected to the supply source 71. Further, one end of a water supply pipe 51 for supplying pure water into the tank 5 is connected to the bottom of the pure water tank 5, and the other end of the water supply pipe 51 is connected to the inside of the factory via a valve V4. It is connected to the pure water supply system.

【0015】そして前記純水タンク5内には、上層部付
近の水温を検出するための温度検出部Tが設けられると
共に、前記給水管51よりの純水が所定量貯留したこと
を検出し、前記純水供給管4よりの排出量(洗浄処理槽
1への供給量)が一定になったことを検出するために、
上下に夫々液面検出部52、53が設けられ、これによ
って秤量機能を持たせている。前記温度検出部T及び液
面検出部52、53は、これらからの検出信号に基づい
てバルブV2〜V4などをコントロールするための制御
部C(図2参照)に接続されている。
A temperature detector T for detecting the water temperature near the upper layer is provided in the pure water tank 5, and it is detected that a predetermined amount of pure water from the water supply pipe 51 is stored. In order to detect that the discharge amount from the pure water supply pipe 4 (supply amount to the cleaning treatment tank 1) has become constant,
Liquid level detectors 52 and 53 are provided on the upper and lower sides, respectively, thereby providing a weighing function. The temperature detection unit T and the liquid level detection units 52 and 53 are connected to a control unit C (see FIG. 2) for controlling the valves V2 to V4 and the like based on detection signals from these.

【0016】次に上述実施例1の作用について述べる。
先ず工場内の純水供給システムから、バルブV4を開い
て給水管51を通じて室温の純水を純水タンク5内に導
入し、液面が上方側の液面検出部52の検出位置に達す
ると、バルブV4が閉じられてタンク5内に所定量の純
水が貯留される。そしてこの純水はヒータ6により加熱
されると共に、窒素ガス供給源71よりの窒素ガスが送
気管7より純水内に送気されて気泡が形成され、この結
果気泡の上昇により上下に循環する液流が生じて、純水
は上層部から下層部まで均一に加熱される。純水の温度
が洗浄液の設定温度よりも若干高くなったとき、例えば
洗浄液の設定温度が80℃である場合において、純水の
温度が85℃になったときに、純水供給管4のバルブV
2を開いてタンク5よりの85℃の純水を洗浄処理槽1
内に注入し、タンク5内の液面が下側の液面検出部53
の検出位置に達したときにバルブV2を閉じ、これによ
って所定量だけ純水を洗浄処理槽1内に供給する。
Next, the operation of the first embodiment will be described.
First, when the valve V4 is opened from the deionized water supply system in the factory and pure water at room temperature is introduced into the deionized water tank 5 through the water supply pipe 51, when the liquid level reaches the detection position of the upper liquid level detection unit 52. The valve V4 is closed and a predetermined amount of pure water is stored in the tank 5. The pure water is heated by the heater 6, and nitrogen gas is supplied from the nitrogen gas supply source 71 into the pure water through the air supply pipe 7 to form bubbles. As a result, the bubbles rise and circulate vertically. A liquid flow is generated, and the pure water is uniformly heated from the upper layer portion to the lower layer portion. When the temperature of the pure water becomes slightly higher than the set temperature of the cleaning liquid, for example, when the set temperature of the cleaning liquid is 80 ° C. and the temperature of the pure water reaches 85 ° C., the valve of the pure water supply pipe 4 V
Open 2 to wash pure water at 85 ℃ from tank 5
And the liquid level in the tank 5 is lower than the liquid level detection unit 53.
When the detection position is reached, the valve V2 is closed, so that a predetermined amount of pure water is supplied into the cleaning treatment tank 1.

【0017】ここで純水タンクに純水を一定量だけ導入
し、また一定量だけ排出するときには、バブリングを行
うと液面が揺れて秤量精度が悪くなるおそれがあるた
め、この実施例では、図3に示すように秤量を行ってい
るときにはバブリングを止めておき、温度調整を行って
いる間のみバブリングを行うようにしている。
In this embodiment, when a certain amount of pure water is introduced into the pure water tank and a certain amount of pure water is discharged, if bubbling is performed, the liquid level may fluctuate and the weighing accuracy may be deteriorated. As shown in FIG. 3, bubbling is stopped during weighing, and bubbling is performed only during temperature adjustment.

【0018】一方薬液タンク31より洗浄処理槽1内に
例えば塩酸と過酸化水素水との混合液よりなる常温の薬
液を洗浄処理槽1内に供給し、ポンプPを駆動して純水
と薬液との混合液を上縁部から越流槽11内にオーバー
フローさせ、循環路12を通じて洗浄処理槽1の底部に
戻す。こうして純水と薬液とを混合させながら図示しな
いヒータにより加熱して設定温度例えば80℃に昇温
し、この温度を維持するようにする。その後洗浄処理槽
1内の洗浄液が設定温度になると、保持部材2は上限位
置にて、図示しない搬送アームからウエハWを受け取っ
た後下降し、この結果ウエハWは洗浄液内に浸漬されて
洗浄液と接触し洗浄処理される。しかる後ウエハWは逆
の動作で保持部材2から搬送アームに受け渡され、例え
ば純水によりリンスされる。そして洗浄処理槽1内の洗
浄液は、所定枚数のウエハを洗浄処理する毎に交換さ
れ、例えば1日に数回交換される。洗浄液の交換時に
は、洗浄処理槽1内を例えば純水で洗浄した後同様にし
て洗浄液の温度調整が行われる。
On the other hand, from the chemical solution tank 31, a cleaning solution tank 1 is supplied with a room temperature chemical solution, for example, a mixed solution of hydrochloric acid and hydrogen peroxide, and the pump P is driven to drive the pure water and the chemical solution. The mixed solution of and is overflowed from the upper edge into the overflow tank 11 and returned to the bottom of the cleaning treatment tank 1 through the circulation path 12. Thus, the pure water and the chemical solution are mixed and heated by a heater (not shown) to raise the temperature to a set temperature, for example, 80 ° C., and maintain this temperature. After that, when the cleaning liquid in the cleaning processing bath 1 reaches the set temperature, the holding member 2 is lowered at the upper limit position after receiving the wafer W from the transfer arm (not shown), and as a result, the wafer W is immersed in the cleaning liquid to form the cleaning liquid. Contacted and washed. Then, the wafer W is transferred from the holding member 2 to the transfer arm by the reverse operation, and rinsed with, for example, pure water. Then, the cleaning liquid in the cleaning processing tank 1 is replaced every time a predetermined number of wafers are cleaned, for example, several times a day. At the time of exchanging the cleaning liquid, the temperature of the cleaning liquid is adjusted in the same manner after cleaning the inside of the cleaning treatment tank 1 with pure water, for example.

【0019】ここで洗浄処理槽1内にて塩酸3.9l、
過酸化水素水3.9l、純水19.3lを混合し、その
混合液である洗浄液の温度を80℃に設定するプロセス
に対して本発明装置の効果を調べるために次のようなモ
デル実験を行った。即ち薬液分に相当する室温(25
℃)の純水7.8lを洗浄処理槽1内に注入する一方、
純水タンク5内に室温の純水を貯留した後ヒータ6によ
り加熱して温度検出部Tの温度が設定温度になったとき
に純水タンク5から19.3lの純水を洗浄処理槽1内
に供給し、洗浄処理槽1内のヒータ6により設定温度ま
で加熱し、以下の各条件毎に純水タンク5における温度
変化と洗浄処理槽1における温度変化とを調べた。
Here, in the cleaning treatment tank 1, 3.9 l of hydrochloric acid,
In order to investigate the effect of the device of the present invention on the process of mixing 3.9 liters of hydrogen peroxide water and 19.3 liters of pure water and setting the temperature of the cleaning liquid, which is the mixture, to 80 ° C., the following model experiment was conducted. I went. That is, the room temperature (25
While injecting 7.8 liters of pure water (° C.) into the cleaning treatment tank 1,
When pure water at room temperature is stored in the pure water tank 5 and heated by the heater 6 to bring the temperature of the temperature detecting portion T to a set temperature, 19.3 l of pure water is washed from the pure water tank 5 to the cleaning treatment tank 1 The temperature of the pure water tank 5 and the temperature change of the cleaning treatment tank 1 were examined for each of the following conditions.

【0020】(条件A)純水タンク5の設定温度を80
℃とし、バブリングを行わない(従来方式)。
(Condition A) The set temperature of the pure water tank 5 is set to 80
No bubbling (conventional method).

【0021】(条件B)純水タンク5の設定温度を80
℃とし、窒素ガス流量及び圧力を1Nl/min及び1
気圧としてバブリングを行う。
(Condition B) The set temperature of the pure water tank 5 is set to 80.
℃, nitrogen gas flow rate and pressure 1Nl / min and 1
Bubbling is performed at atmospheric pressure.

【0022】(条件C)純水タンク5の設定温度を90
℃とし、窒素ガス流量及び圧力を1Nl/min及び1
気圧としてバブリングを行う。
(Condition C) The set temperature of the pure water tank 5 is set to 90.
℃, nitrogen gas flow rate and pressure 1Nl / min and 1
Bubbling is performed at atmospheric pressure.

【0023】(条件D)純水タンク5の設定温度を95
℃とし、窒素ガス流量及び圧力を1Nl/min及び1
気圧としてバブリングを行う。
(Condition D) The set temperature of the pure water tank 5 is set to 95.
℃, nitrogen gas flow rate and pressure 1Nl / min and 1
Bubbling is performed at atmospheric pressure.

【0024】図4及び図5は、夫々条件A、Bにおける
純水タンク5内の上層部の温度(実線)と下層部の温度
(点線)とを示す特性図である。この結果からわかるよ
うにバブリングを行わない従来装置では上層部と下層部
との間で約40℃もの温度差が生じるのに対し、本発明
の装置では温度差はほとんどなくなる。
FIGS. 4 and 5 are characteristic diagrams showing the temperature of the upper layer portion (solid line) and the temperature of the lower layer portion (dotted line) in the pure water tank 5 under the conditions A and B, respectively. As can be seen from this result, in the conventional device without bubbling, a temperature difference of about 40 ° C. occurs between the upper layer portion and the lower layer portion, whereas in the device of the present invention, there is almost no temperature difference.

【0025】また図6は洗浄処理槽1内の水温を示し、
A〜Dは夫々条件A〜Dに対応したデータである。図中
に記載した時間は、洗浄液の温度を80℃に設定した場
合に許容される温度までの昇温時間である。AとBはい
ずれも純水タンク5の設定温度を80℃としているの
で、バブリングすることによって昇温時間が39分から
23分まで短縮できることがわかる。更に純水タンク内
の設定温度を90℃、95℃と高めることによって昇温
時間が20分、18分と短縮されていくことがわかる。
このように上述実施例1によれば、バブリングにより純
水タンク5内の純水が均一に温度調整されるので、結局
洗浄液の温度調整の時間の短縮化を図ることができ、し
かもバブリングという手法を純水タンクに適用している
ため洗浄処理槽1内での気泡の発生はなく、洗浄処理槽
1内でバブリングを行う場合に発生する気泡がウエハ表
面に付着し、この気泡により局部的に洗浄処理を遅らせ
るなどの悪影響を及ぼすこともない点で非常に有効であ
る。尚、バブリングについては、窒素ガスに限らず他の
ガス例えば空気を用いてもよいし、1本の送気管を用い
る代わりに多数の穴を有する散気板を希釈液槽の底部に
配置してもよい。
FIG. 6 shows the water temperature in the cleaning treatment tank 1,
A to D are data corresponding to the conditions A to D, respectively. The time shown in the figure is the temperature rising time up to the allowable temperature when the temperature of the cleaning liquid is set to 80 ° C. Since both A and B set the temperature of the pure water tank 5 to 80 ° C., it can be understood that the temperature rising time can be shortened from 39 minutes to 23 minutes by bubbling. Further, it can be seen that the temperature rising time is shortened to 20 minutes and 18 minutes by increasing the set temperature in the pure water tank to 90 ° C and 95 ° C.
As described above, according to the first embodiment, the temperature of the pure water in the pure water tank 5 is uniformly adjusted by the bubbling, so that the time for adjusting the temperature of the cleaning liquid can be shortened and the technique of bubbling can be achieved. Since bubbles are applied to the pure water tank, no bubbles are generated in the cleaning treatment tank 1, and bubbles generated when bubbling is performed in the cleaning treatment tank 1 adhere to the wafer surface, and the bubbles locally cause the bubbles. It is extremely effective in that it does not adversely affect the cleaning process. For bubbling, other gas such as air may be used instead of nitrogen gas, and instead of using one air pipe, a diffuser plate having a large number of holes is arranged at the bottom of the diluting liquid tank. Good.

【0026】(実施例2)図7は本発明の実施例2に用
いられる純水タンクを示す斜視図であり、本実施例は上
記実施例1と略同様の構成であるが、バブリング手段と
しての送気管7を設置することに代えて純水タンクの略
片側半分領域にヒ−タを配置したことにおいて異なる。
図7中5は純水タンクであり、この純水タンク5の底面
は略中央部付近より図中左側面に向かって上昇する傾斜
面を形成するように折曲している。前記純粋タンク5内
にはガラス管内にニクロム線を挿入して、例えばU字状
に形成された加熱手段としてのヒ−タ6が底面部の一部
領域、例えば水平な底面に対応する図中右側半分領域に
配置されると共に、上層部付近の水温を検出するための
温度検出部Tが設けられ、更に水平な底面には純水供給
管4が接続されている。 次に上述実施例2の作用につ
いて述べる。上記実施例1と同様に純水タンク5に室温
の純水を導入してヒ−タ6をオンにすると、当該ヒ−タ
6付近の純水は昇温されて上層部に上昇し、更に上層部
をヒ−タ6の配置されていない領域即ち傾斜面の上方領
域に向かって横方向に移動すると共に、ヒ−タ6の配置
されていない領域、即ち傾斜面上の純水は、当該傾斜面
に沿ってヒ−タ6付近に移動し、このヒ−タ6付近に移
動した純水が、上述と同様にして昇温されるので純水タ
ンク5内で図中の矢印方向に純水の対流が生じる。そし
て、純水の温度が洗浄液の設定温度よりも若干高くなっ
たとき、温度検出部Tよりの検出信号に基づいて実施例
1と同様の操作によって所定量だけ純水を洗浄処理槽1
内に供給する一方、薬液タンク31より薬液を洗浄処理
槽1内に供給し、以下実施例1と同様にしてウエハWが
洗浄される。
(Embodiment 2) FIG. 7 is a perspective view showing a deionized water tank used in Embodiment 2 of the present invention. This embodiment has substantially the same structure as that of Embodiment 1, but as a bubbling means. The difference is that a heater is arranged in a half region on one side of the pure water tank instead of installing the air supply pipe 7.
Reference numeral 5 in FIG. 7 denotes a pure water tank, and the bottom surface of the pure water tank 5 is bent so as to form an inclined surface that rises from near the central portion toward the left side surface in the drawing. A nichrome wire is inserted into a glass tube in the pure tank 5, and a heater 6 as a heating means formed in, for example, a U shape corresponds to a partial area of the bottom surface portion, for example, a horizontal bottom surface. A temperature detection unit T for detecting the water temperature near the upper layer is provided in the right half region, and a pure water supply pipe 4 is connected to the horizontal bottom surface. Next, the operation of the above-described second embodiment will be described. When pure water at room temperature is introduced into the pure water tank 5 and the heater 6 is turned on in the same manner as in Example 1, the pure water in the vicinity of the heater 6 is heated and rises to the upper layer portion. The upper layer portion is moved laterally toward the area where the heater 6 is not arranged, that is, the area above the inclined surface, and the pure water on the area where the heater 6 is not arranged, that is, the inclined surface is The pure water that has moved along the inclined surface to the vicinity of the heater 6 and has moved to the vicinity of the heater 6 is heated in the same manner as described above. Water convection occurs. Then, when the temperature of the pure water becomes slightly higher than the set temperature of the cleaning liquid, the pure water is washed by a predetermined amount by the same operation as in the first embodiment based on the detection signal from the temperature detection unit T.
Meanwhile, the chemical solution is supplied from the chemical solution tank 31 into the cleaning treatment tank 1, and the wafer W is cleaned in the same manner as in Example 1.

【0027】ここで純水タンク5の底面部の一部領域に
ヒ−タ6を配置した場合と全体に亘ってヒ−タ6を配置
した場合とについて純水タンク5内の温度分布を調べる
ために次のような実験を行った。
Here, the temperature distribution in the pure water tank 5 is examined for the case where the heater 6 is arranged in a partial area of the bottom surface of the pure water tank 5 and the case where the heater 6 is arranged over the entire area. Therefore, the following experiment was conducted.

【0028】先ず図8(a)に示すように、本実施例に
係る、例えば縦(紙面と垂直方向)横、高さの寸法が夫
々およそ25cm、38cm、37cmである純水タン
ク5内に、ヒ−タ6をU字状部の先端が純水タンク5の
横方向の中央部に位置するように配置し、このタンク5
内に、室温の純水を導入した後温度80℃に設定してヒ
−タ6をオンにし、図8(a)中左右両端の各上層部、
下層部の計4箇所について温度変化を調べた。実験結果
は図9に示すとおりであり、上記いずれの測定箇所にお
いてもその温度変化は図9の斜線で示したゾ−ン内であ
った。
First, as shown in FIG. 8A, in a pure water tank 5 according to the present embodiment, for example, the length (vertical direction to the paper surface) horizontal and height dimensions are about 25 cm, 38 cm and 37 cm, respectively. , The heater 6 is arranged such that the tip of the U-shaped portion is located at the lateral center of the pure water tank 5.
After introducing pure water at room temperature, the temperature is set to 80 ° C., the heater 6 is turned on, and the upper layer portions at the left and right ends in FIG.
The temperature change was examined at a total of four places in the lower layer. The experimental results are as shown in FIG. 9, and the temperature change at any of the above measurement points was within the zone indicated by the diagonal lines in FIG.

【0029】一方図8(b)に示すように縦(紙面と垂
直方向)、横、高さの寸法が夫々およそ32cm、32
cm、23cmの純水タンク5a内に、底面部全体に亘
ってヒ−タ6を配置し、同様にして、上層部、下層部の
2箇所について温度変化を調べた。実験結果は図10に
示すとおりであり、図10中実線及び破線は夫々純水タ
ンク5a内の上層部及び下層部の温度変化を示した曲線
である。
On the other hand, as shown in FIG. 8B, the length (vertical direction to the paper surface), the width, and the height are approximately 32 cm and 32, respectively.
In the pure water tank 5a of cm and 23 cm, the heater 6 was arranged over the entire bottom surface portion, and similarly, the temperature change was examined at two places of the upper layer portion and the lower layer portion. The experimental results are as shown in FIG. 10, and the solid line and the broken line in FIG. 10 are curves showing the temperature changes of the upper layer portion and the lower layer portion in the pure water tank 5a, respectively.

【0030】これらの実験結果から分かるとおり、図8
(a)に示す本実施例に係る洗浄装置の純水タンク5を
使用した場合は、純水タンク5内の純水が均一に加熱さ
れているのに対し、図8(b)に示す比較例の純水タン
ク5aを使用した場合は純水タンク5a内の純水の上層
部と下層部との間で約40℃もの大きな温度差が生じて
いる。これは、既述したとおり純水タンク5では図8
(a)に示すようにタンク内全体に矢印方向に純水の対
流がスム−スに形成されるが、純水タンク5aではヒ−
タ6付近で昇温された純水は上昇した後、横方向に殆ど
移動しないので純水タンク5a内で純水の対流が形成さ
れにくいためであると考案される。また、純水タンク5
ではヒ−タ6が配置されていない領域の底面に傾斜面を
形成しているので、当該領域よりこの傾斜面に沿って純
水が流動することから対流がより一層スム−スに行なわ
れると共に、純水タンク5内の純水を純水供給管4より
排液したときに純水タンク5の底面の水溜まりが少なく
なる。以上のように本実施例に係る純水タンク5によれ
ば純水タンク5内の純水が均一に短時間で温度調整され
るので、結局洗浄液の温度調整の時間の短縮化を図るこ
とができる。
As can be seen from the results of these experiments, FIG.
When the pure water tank 5 of the cleaning apparatus according to the present embodiment shown in (a) is used, the pure water in the pure water tank 5 is heated uniformly, while the comparison shown in FIG. When the pure water tank 5a of the example is used, a large temperature difference of about 40 ° C. occurs between the upper and lower layers of pure water in the pure water tank 5a. This is as shown in FIG.
As shown in (a), a convection of pure water is smoothly formed in the direction of the arrow in the entire tank, but in the pure water tank 5a, the convection is pure.
It is considered that the pure water heated in the vicinity of the water 6 hardly moves in the lateral direction after rising, so that convection of pure water is less likely to be formed in the pure water tank 5a. In addition, the pure water tank 5
However, since the inclined surface is formed on the bottom surface of the area where the heater 6 is not arranged, pure water flows along the inclined surface from the area, so that convection is further smoothed. When the pure water in the pure water tank 5 is drained from the pure water supply pipe 4, the pool of water on the bottom surface of the pure water tank 5 is reduced. As described above, according to the pure water tank 5 according to the present embodiment, the temperature of the pure water in the pure water tank 5 is uniformly adjusted in a short time, so that the time for adjusting the temperature of the cleaning liquid can be shortened. it can.

【0031】尚、本実施例に係る純水タンク5は図7に
示す形状に限られず、加熱手段を純水タンク5の底面部
の全体に亘って配置せずに一部領域に配置することによ
り十分な対流を形成する構成であればよく、例えば図1
1に示すように純水タンクの底面に中央部の水平面から
両側に傾斜する傾斜面を形成し、中央部の水平な底面上
にヒ−タを設置することによって左右両側に対流を形成
するような構成であってもよい。また、ヒ−タの形状は
U字状に限られず例えばM字状であってもよい。
The deionized water tank 5 according to the present embodiment is not limited to the shape shown in FIG. 7, and the heating means may be arranged in a partial area instead of being arranged over the entire bottom surface of the deionized water tank 5. The configuration may be such that sufficient convection is formed by, for example, FIG.
As shown in 1, the bottom surface of the pure water tank is formed with an inclined surface that inclines from the horizontal surface of the central part to both sides, and by installing a heater on the horizontal bottom surface of the central part, convection is formed on both left and right sides. It may have any configuration. Further, the shape of the heater is not limited to the U shape, and may be, for example, an M shape.

【0032】更に本実施例に係る純水タンクの構成は図
7及び図11に示すものに限られず、純水タンク内の純
水を撹拌するための例えば送気管等のバブリング手段を
設けたものであってもよい。
Further, the structure of the pure water tank according to this embodiment is not limited to that shown in FIGS. 7 and 11, but a bubbling means such as an air supply pipe for stirring the pure water in the pure water tank is provided. May be

【0033】次に本発明の洗浄装置を適用した洗浄シス
テムの一部の例を図12に示す。このシステムでは、ウ
エハ搬入部91に、ウエハを収納するキャリアの載置台
92(この図ではキャリアが載置台92の上に載ってい
る)とキャリア内のウエハを押し上げて搬送アーム93
に受け渡す押し上げ部94と、既述した洗浄液により洗
浄を行うための洗浄処理槽95と、純水でリンスするた
めのリンス槽96と、水中搬送部97とが設けられ、ウ
エハが搬送アーム93によって洗浄処理槽95、リンス
槽96に順次搬送され、更に水中搬送部97によって図
示しない別の洗浄処理槽に送られる。このように洗浄処
理槽の数が多い場合には、本発明を適用することは非常
に有効である。
Next, FIG. 12 shows an example of a part of a cleaning system to which the cleaning device of the present invention is applied. In this system, a carrier loading table 92 (in this figure, the carrier is placed on the loading table 92) of the carrier that stores the wafer and the wafer in the carrier are pushed up to the wafer loading section 91 and the transfer arm 93 is pushed.
A push-up unit 94 for delivering to the wafer, a cleaning processing tank 95 for cleaning with the above-described cleaning liquid, a rinse tank 96 for rinsing with pure water, and an underwater transfer unit 97 are provided, and the wafer transfer arm 93 is provided. Are successively transported to the cleaning treatment tank 95 and the rinse tank 96, and are further transported to another cleaning treatment tank (not shown) by the underwater transport unit 97. When the number of cleaning treatment tanks is large as described above, the application of the present invention is very effective.

【0034】以上において本発明では、希釈液として純
水に限られるものではないし、温度調整についても加熱
する代わりに冷却する場合であってもよい。
In the above, the present invention is not limited to pure water as the diluting liquid, and the temperature may be adjusted by cooling instead of heating.

【0035】尚、被処理体としては半導体ウエハに限ら
ずガラス基板やLCD基板などであってもよい。
The object to be processed is not limited to a semiconductor wafer, but may be a glass substrate or LCD substrate.

【0036】[0036]

【発明の効果】請求項1の発明によれば、希釈液槽内の
希釈液に対してバブリングを行いながら温度調整を行っ
ているため、また請求項2の発明によれば、希釈液槽内
の希釈液が対流を形成するため、これらいずれの発明に
おいても希釈液が均一に温度調整され、従って希釈液と
薬液との混合液についての温度調整に要する時間を簡易
な手法によって短縮することができる。
According to the first aspect of the invention, the temperature is adjusted while bubbling the diluting liquid in the diluting liquid tank, and according to the second aspect of the invention, the diluting liquid tank Since the diluting liquid forms a convection, the temperature of the diluting liquid is uniformly adjusted in any of these inventions. Therefore, it is possible to shorten the time required for the temperature adjustment of the mixed liquid of the diluting liquid and the chemical liquid by a simple method. it can.

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

【図1】本発明の実施例1の要部を示す斜視図である。FIG. 1 is a perspective view showing a main part of a first embodiment of the present invention.

【図2】上記実施例1の要部を示す説明図である。FIG. 2 is an explanatory diagram showing a main part of the first embodiment.

【図3】上記実施例1におけるバブリングのタイミング
を示すフロー図である。
FIG. 3 is a flowchart showing the timing of bubbling in the first embodiment.

【図4】上記実施例1の従来例における純水タンク内の
温度変化を示す特性図である。
FIG. 4 is a characteristic diagram showing a temperature change in a pure water tank in the conventional example of the first embodiment.

【図5】本発明の実施例1における純水タンク内の温度
変化を示す特性図である。
FIG. 5 is a characteristic diagram showing a temperature change in the pure water tank according to the first embodiment of the present invention.

【図6】従来例と実施例1とについて洗浄処理槽内の温
度変化を示す特性図である。
FIG. 6 is a characteristic diagram showing a temperature change in the cleaning treatment tank for the conventional example and the first example.

【図7】本発明の実施例2に係る純水タンクの一例を示
す斜視図である。
FIG. 7 is a perspective view showing an example of a pure water tank according to a second embodiment of the present invention.

【図8】上記実施例2に係る純水タンク及び比較例に係
る純水タンクを示した縦断面図である。
FIG. 8 is a vertical sectional view showing a pure water tank according to the second embodiment and a pure water tank according to a comparative example.

【図9】本発明の実施例2における純水タンク内の温度
変化を示す特性図である。
FIG. 9 is a characteristic diagram showing a temperature change in a pure water tank according to a second embodiment of the present invention.

【図10】上記実施例2の従来例における純水タンク内
の温度変化を示す特性図である。
FIG. 10 is a characteristic diagram showing a temperature change in a pure water tank in the conventional example of the second embodiment.

【図11】本発明の実施例2に係る純水タンクの他の一
例を示す縦断面図である。
FIG. 11 is a vertical cross-sectional view showing another example of the pure water tank according to the second embodiment of the present invention.

【図12】本発明を適用した洗浄システムの一例を示す
平面図である。
FIG. 12 is a plan view showing an example of a cleaning system to which the present invention is applied.

【符号の説明】[Explanation of symbols]

1 洗浄処理槽 2 保持部材 3 薬液供給管 4 純粋供給管 5 純粋タンク 6 ヒ−タ 7 送気管 1 Cleaning Treatment Tank 2 Holding Member 3 Chemical Solution Supply Pipe 4 Pure Supply Pipe 5 Pure Tank 6 Heater 7 Air Pipe

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 薬液と希釈液との混合液よりなり、温度
調整された洗浄液に被処理体を接触させて洗浄処理する
洗浄装置において、 前記希釈液を温度調整するための温度調整手段と、前記
希釈液中に気泡を形成するためのバブリング手段とを設
けたことを特徴とする洗浄装置。
1. A cleaning apparatus comprising a mixed solution of a chemical solution and a diluting solution, wherein the object to be treated is brought into contact with a temperature-controlled cleaning solution, and a temperature adjusting means for adjusting the temperature of the diluting solution is provided, A cleaning device comprising bubbling means for forming bubbles in the diluent.
【請求項2】 薬液と希釈液槽よりの希釈液よりなる温
度調整された洗浄液に被処理体を接触させて洗浄する洗
浄装置において、 前記希釈液槽の底面部の一部領域に加熱手段を設け、こ
の加熱手段により当該一部領域と前記底面部のうち加熱
手段の配置されていない他部領域との間で対流による液
流を形成することを特徴とする洗浄装置。
2. A cleaning apparatus for cleaning an object to be treated by contacting a temperature-controlled cleaning liquid comprising a chemical liquid and a diluent from a diluent tank with a heating means in a partial area of the bottom surface of the diluent tank. A cleaning apparatus, which is provided and forms a liquid flow by convection between the partial region and the other region of the bottom face portion where the heating unit is not provided by the heating unit.
JP08764592A 1991-11-16 1992-03-11 Cleaning equipment Expired - Fee Related JP3308586B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP08764592A JP3308586B2 (en) 1991-11-16 1992-03-11 Cleaning equipment

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP32814491 1991-11-16
JP3-328144 1991-11-16
JP08764592A JP3308586B2 (en) 1991-11-16 1992-03-11 Cleaning equipment

Publications (2)

Publication Number Publication Date
JPH05190523A true JPH05190523A (en) 1993-07-30
JP3308586B2 JP3308586B2 (en) 2002-07-29

Family

ID=26428894

Family Applications (1)

Application Number Title Priority Date Filing Date
JP08764592A Expired - Fee Related JP3308586B2 (en) 1991-11-16 1992-03-11 Cleaning equipment

Country Status (1)

Country Link
JP (1) JP3308586B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100423206C (en) * 2003-07-02 2008-10-01 上海思恩电子技术有限公司 Method and system for processing substrate using mist chemical agent produced by heating chemical gas
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

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100423206C (en) * 2003-07-02 2008-10-01 上海思恩电子技术有限公司 Method and system for processing substrate using mist chemical agent produced by heating chemical gas
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
US9027573B2 (en) 2010-05-31 2015-05-12 Tokyo Electron Limited Substrate processing apparatus for maintaining a more uniform temperature during substrate processing
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

Also Published As

Publication number Publication date
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