JPH06124936A - Surface treatment device - Google Patents

Surface treatment device

Info

Publication number
JPH06124936A
JPH06124936A JP30035492A JP30035492A JPH06124936A JP H06124936 A JPH06124936 A JP H06124936A JP 30035492 A JP30035492 A JP 30035492A JP 30035492 A JP30035492 A JP 30035492A JP H06124936 A JPH06124936 A JP H06124936A
Authority
JP
Japan
Prior art keywords
fluid
container
surface treatment
valve
sample
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
Application number
JP30035492A
Other languages
Japanese (ja)
Inventor
Yoshiki Kobayashi
小林  芳樹
Yoichi Oba
洋一 大場
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.)
INTAAFUEISU GIJUTSU KENKYUSHO KK
INTERFACE GIJUTSU KENKYUSHO
Original Assignee
INTAAFUEISU GIJUTSU KENKYUSHO KK
INTERFACE GIJUTSU KENKYUSHO
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 INTAAFUEISU GIJUTSU KENKYUSHO KK, INTERFACE GIJUTSU KENKYUSHO filed Critical INTAAFUEISU GIJUTSU KENKYUSHO KK
Priority to JP30035492A priority Critical patent/JPH06124936A/en
Publication of JPH06124936A publication Critical patent/JPH06124936A/en
Pending legal-status Critical Current

Links

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  • Manufacturing Of Printed Wiring (AREA)
  • Cleaning Or Drying Semiconductors (AREA)
  • Cleaning By Liquid Or Steam (AREA)

Abstract

PURPOSE:To perform treatment such as washing of the sample surface of a large area in a short time and at low cost in a friendly way to environment by spraying a small quantity of fluid for surface treatment together with a carrier fluid on a low temperature sample inside an airtight container for performing surface dew condensation by washing. CONSTITUTION:An airtight container 2 having an interior finished sample 1 to be subjected to surface treatment is provided with a cooling part 2a and a drain part 2b. A pure water supply 3, an inert gas supply 4, a fluid mixer 5 and a heated and compressed vapor supply 6 are connected to the airtight container 2 through piping and the switching valves a, b, c, d. To a plurality of inlet port of the fluid mixer 5, connected are a surface treatment fluid supply 7 and a pure water supply 3 through a valve e1, the heated and compressed vapor supply 6 through a valve f.

Description

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

【0001】[0001]

【産業上の利用分野】この発明は半導体特にシリコンウ
エハ、液晶表示素子、プリント配線板などの電子部品、
レンズやプリズムなどの光学部品、歯車やリードフレー
ムなどの精密機械部品の製造工程で使用する各種物体の
洗浄、リンス、酸化膜除去、乾燥などの表面処理装置に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to semiconductors, particularly silicon wafers, liquid crystal display devices, electronic parts such as printed wiring boards,
The present invention relates to a surface treatment device for cleaning, rinsing, removing an oxide film, and drying various objects used in the manufacturing process of optical components such as lenses and prisms and precision mechanical components such as gears and lead frames.

【0002】[0002]

【従来の技術】従来、各種物体の洗浄、リンス、酸化膜
除去、乾燥などの湿式及び乾式表面処理は、処理槽や処
理装置を並列に設置し、1つの工程ごとに順次送って行
くバッチ方式や、ベルトコンベアで被処理物を定速で送
りながら、これに順次処理を行って行く枚葉方式が主流
である。
2. Description of the Related Art Conventionally, for wet and dry surface treatments such as cleaning, rinsing, oxide film removal, and drying of various objects, a batch system in which treatment tanks and treatment devices are installed in parallel and sequentially sent for each process Also, the single-wafer method in which the object to be processed is fed at a constant speed by a belt conveyor and sequentially processed is mainly used.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、これら
の方法は 装置が大形になり、大きな設置面積が必要になる 装置内及び装置を設置した大容積のスペースのクリ
ーン度を維持するために、大きなエネルギが必要となる 処理に必要な高純度の水、ガス、薬品など高価な物
質の使用量が多く、多くの場合使い捨てであるため、不
経済であるし、廃液・廃ガスの処理に多大の設備と処理
経費がかかる 特にバッチ式の浸漬処理において薬品や水など処理
液は、繰り返し使用されるため、処理液の経時的劣化が
避けらず、それが処理品質の経時的低下になりやすいな
どの問題点が有った。
However, these methods require a large apparatus and require a large installation area. In order to maintain the cleanliness of the apparatus and the large volume space in which the apparatus is installed, a large size is required. High-purity water, gas, chemicals and other expensive substances required for energy-consuming processing are used in large amounts, and in many cases they are disposable, which is uneconomical and requires a large amount of waste liquid / gas treatment. Equipment and processing cost are high. Especially in batch type dipping treatment, treatment liquid such as chemicals and water is repeatedly used, so deterioration of the treatment liquid with time cannot be avoided, which tends to cause deterioration of treatment quality with time. There was a problem.

【0004】この発明は前記した各問題点を除去するた
めに、密閉容器内の低温度試料にキャリヤ流体と共に少
量の表面処理用流体を吹き付けることで表面結露させた
後、水洗することで大面積の試料表面に短時間でしかも
コスト安に環境に優しく洗浄等の処理を施こすことを目
的とする。
According to the present invention, in order to eliminate the above-mentioned problems, a low temperature sample in a closed container is sprayed with a small amount of a surface treatment fluid together with a carrier fluid to cause dew condensation on the surface, and then washed with water to form a large area. The purpose is to subject the surface of the sample to a treatment such as cleaning in a short time at a low cost and environmentally friendly.

【0005】[0005]

【課題を解決するための手段】上記したこの発明の目的
は、表面処理をすべき試料を内装した密閉容器(以下単
に容器と略称する)に冷却部とドレイン部とを設けると
共に、前記密閉容器には純水源、不活性ガス源、流体混
合器および加熱加圧蒸気源の各出口側をそれぞれ開閉バ
ルブを経て配管接続し、前記流体混合器の複数の流入口
にそれぞれ切換バルブを介して表面処理用流体源、純水
源および開閉バルブを経て前記加熱加圧蒸気源を配管接
続することで達成できる。
The above-mentioned object of the present invention is to provide a cooling part and a drain part in a closed container (hereinafter simply referred to as a container) containing a sample to be surface-treated, and to provide the closed container. Is connected to each outlet side of a pure water source, an inert gas source, a fluid mixer, and a heating and pressurized steam source through an on-off valve, respectively, and a plurality of inflow ports of the fluid mixer are respectively connected to the surface via switching valves. This can be achieved by connecting the heated and pressurized steam source through a pipe through a processing fluid source, a pure water source, and an opening / closing valve.

【0006】[0006]

【作用】以上のような装置を用いて例えばシリコンウエ
ハの洗浄等の表面処理を行うには、まず容器に収納した
常温以下の温度のシリコンウエハにアンモニア水、過酸
化水素水(H2 O2 )を加熱加圧蒸気による媒体(キャ
リア)と共に容器内に導入し、アンモニアやH2 O2 を
シリコンウエハに凝縮させることができる。
In order to carry out a surface treatment such as cleaning of a silicon wafer using the above-mentioned apparatus, first, ammonia water and hydrogen peroxide solution (H2O2) are stored in a silicon wafer at a temperature below room temperature stored in a container. Ammonia and H2 O2 can be condensed into a silicon wafer by introducing it into a container together with a medium (carrier) by heating and pressurized steam.

【0007】次に冷却した純水で試料をスプレーリンス
してから加熱蒸気を導入し、容器内の空気を追い出して
容器内を高温水蒸気で充満させた後、容器を密閉状態に
してから、容器内の一部を冷却することによって、容器
内を真空に近い状態とし、シリコンウエハの表面から急
速に水を蒸発させ除去することができる。
Next, after spray rinsing the sample with cooled pure water, introducing heated steam, expelling the air in the container to fill the container with high temperature steam, and then sealing the container, and then the container By cooling a part of the inside, the inside of the container can be brought into a state close to a vacuum, and water can be rapidly evaporated and removed from the surface of the silicon wafer.

【0008】なお容器を密閉状態にしたまま、フッ化水
素を窒素ガスによるキャリアガスと共に容器内に導入し
て、シリコン酸化膜を除去することもできる。
It is possible to remove the silicon oxide film by introducing hydrogen fluoride into the container together with a carrier gas of nitrogen gas while keeping the container closed.

【0009】最後に、容器内に窒素ガスを導入して常圧
に戻してから、蓋を開けて表面処理済シリコンウエハを
取り出すことができる。これらの操作中シリコンウエハ
は、外部からメカニカルシールによる気密軸受で支承し
た支持枠などを介して2秒間に1回転程度にゆっくり回
転する構造にしたり、または/及びスプレーノズル自身
が気密性軸受を介して回転する構造をとることが好まし
い。
Finally, after introducing nitrogen gas into the container to return it to normal pressure, the lid can be opened to take out the surface-treated silicon wafer. During these operations, the silicon wafer has a structure in which it slowly rotates about once every two seconds through a support frame supported by an airtight bearing with a mechanical seal from the outside, and / or the spray nozzle itself has an airtight bearing. It is preferable to adopt a structure that rotates by rotating.

【0010】[0010]

【実施例】実施例について図面を参照して説明する。先
ずこの発明の基本構成は図1に示すように、洗浄や酸化
膜除去などの表面処理をすべきシリコンウエハなどの試
料1 を周知の伝熱性密閉容器2 内に周知の気密軸受等で
支承した支持枠などを介して配置するとともに、前記密
閉容器2 の下部には冷却部 2aとドレイン部 2bとを設
ける。
EXAMPLES Examples will be described with reference to the drawings. First, as shown in FIG. 1, the basic structure of the present invention is that a sample 1 such as a silicon wafer to be subjected to surface treatment such as cleaning and removal of an oxide film is supported in a known heat-conductive closed container 2 by a known hermetic bearing. A cooling unit 2a and a drain unit 2b are provided at the bottom of the closed container 2 while being arranged via a support frame or the like.

【0011】また前記密閉容器2 には15℃程度の低温
純水源3 、窒素ガスなどの不活性ガス源4 、流体混合器
5 およびヒータ8 などによる加熱加圧蒸気源6 の各流出
側をそれぞれ流体作動式などの開閉バルブa,b,c,
dを経て配管接続する。
Further, the closed container 2 includes a low temperature pure water source 3 of about 15 ° C., an inert gas source 4 such as nitrogen gas, a fluid mixer.
5 and the respective outlet sides of the heated pressurized steam source 6 by the heater 8 and the like are connected to fluid-operated on-off valves a, b, c,
Pipe connection via d.

【0012】さらに前記流体混合器5 の複数の流入口に
それぞれ切換バルブe1,e2,e3 を介してアンモニア水
やH2 O2 およびHclなどの複数の表面処理用流体源7,
7 、純水源3 および開閉バルブfを経て前記加熱加圧蒸
気源6 を配管接続してこの発明による表面処理装置の基
本部分を構成する。
Further, a plurality of surface treatment fluid sources 7, such as ammonia water, H2 O2 and Hcl, are provided at a plurality of inlets of the fluid mixer 5 via switching valves e1, e2, e3, respectively.
7, the heating / pressurizing steam source 6 is connected by piping through the pure water source 3 and the open / close valve f to form a basic part of the surface treatment apparatus according to the present invention.

【0013】なお容器2 の冷却部 2aには水冷管9 を巻
装してバルブgを経た周知の冷却器10からの冷水を循環
させるようにしてあり、ドレイン部 2bには開閉バルブ
hを接続して所望時に排水可能としてあり、また容器2
内の気体は所望時に上下の開閉バルブjを個別または同
時に開けて排気可能にしてある。
A water cooling pipe 9 is wound around the cooling part 2a of the container 2 to circulate cold water from a well-known cooler 10 via a valve g, and an opening / closing valve h is connected to the drain part 2b. It can be drained when desired, and the container 2
The gas inside can be exhausted by opening the upper and lower open / close valves j individually or simultaneously when desired.

【0014】また容器2 の密閉手段は気密パッキング式
開閉蓋などによる周知手段でよく、さらに気密性軸受と
しては耐薬品性ゴムOリングシールによるものなどを採
用でき、また容器2 内の圧力は圧力計PGで検すること
ができる。
The container 2 may be sealed by a well-known means such as an airtight packing type opening / closing lid. Further, as the airtight bearing, a chemical resistant rubber O-ring seal may be adopted, and the pressure in the container 2 is a pressure. The total PG can be used for inspection.

【0015】この発明による表面処理装置の基本構成は
以上のような構成であるが、図における各切換バルブe
1,e2,e3 には中間閉止タイプの流体作動切換バルブを
用いその配管の具体例としては、各切換バルブの二つの
流入口のうちのそれぞれ一方の流入口i1 に表面処理用
流体源7 を連通接続すると共に、他方の流入口i2 にそ
れぞれ純水源3 を連通接続し、また上記各切換バルブe
1,e2,e3 の一つずつ計三つの流出口Oを前記流体混合
器5 の三つの流入口にそれぞれ個別連通配管して実施す
る。
The basic structure of the surface treatment apparatus according to the present invention is as described above.
Intermediate closing type fluid operated switching valves are used for 1, e2, e3, and as a concrete example of the piping, a surface treatment fluid source 7 is provided at one of the two inlets i1 of each switching valve. In addition to the communication connection, the pure water source 3 is connected to the other inflow port i2.
A total of three outlets O, one each of 1, e2, and e3, are individually connected to the three inlets of the fluid mixer 5 for piping.

【0016】この例の場合には試料1にシリコンウエハ
のようなシビアな表面処理を要する物体の表面処理に適
し、同一試料に対する複数異種の表面処理の各インター
バルを目掛けて各連通配管内の残存流体を三方切換バル
ブe1,e2,e3 の個別操作で純水と共に容器2 内の試料
に当てないようにタレ流し吐出し、容器2 のドレイン部
2bから排水して各配管内の残存流体を洗浄除去した
後、次の表面処理に移行するようにしてある。
In the case of this example, the sample 1 is suitable for the surface treatment of an object such as a silicon wafer which requires a severe surface treatment, and the intervals of a plurality of different surface treatments for the same sample are aimed at and the inside of each communication pipe is examined. Drain the remaining fluid by operating the three-way selector valves e1, e2, and e3 together with pure water so that it does not hit the sample in container 2 and discharge it.
After draining from 2b to wash and remove the residual fluid in each pipe, the next surface treatment is performed.

【0017】本発明は以上のような具体的な構成であ
り、図の構成でシリコンウエハの洗浄を行う手順を以下
に説明する。まず、密閉容器2 内にシリコンウエハによ
る試料1 を収納し、この試料は前記のように外部からメ
カニカルシールを介して支承した支持枠でゆっくり回転
する構造になっている。この状態ではすべてのバルブ
a,b,c,d,e1,e2,e3 ,g,h,jは閉じてあ
る。
The present invention has the above-described specific structure, and the procedure for cleaning a silicon wafer with the structure shown in the figure will be described below. First, the sample 1 made of a silicon wafer is housed in the closed container 2, and the sample is structured so as to slowly rotate by the support frame supported from the outside through the mechanical seal as described above. In this state, all the valves a, b, c, d, e1, e2, e3, g, h, j are closed.

【0018】次にアンモニア水、過酸化水素水などの表
面処理用流体源7 から処理用流体をバルブe1 の開放で
流体混合器5 に導入し、バルブfとバルブcを開放し
て、加熱加圧蒸気を媒体(キャリア)として容器2 内に
上記処理用流体を導入する。容器内に導入した処理用流
体は水蒸気と共にシリコンウエハなどの試料1 に表面に
凝縮する。
Next, a treatment fluid from a surface treatment fluid source 7 such as aqueous ammonia or hydrogen peroxide is introduced into the fluid mixer 5 by opening the valve e1, and the valves f and c are opened to heat the fluid. The above-mentioned processing fluid is introduced into the container 2 using pressurized steam as a medium (carrier). The processing fluid introduced into the container condenses on the surface of the sample 1 such as a silicon wafer along with water vapor.

【0019】ここでバルブfを閉じ切換バルブe1 を切
換えてから、バルブhを開け、バルブaを開放して約1
5℃の純水を約10秒間容器2 内にノズルnから試料1
に吹き付けて試料1 をスプレーリンスすると共に、切換
バルブe1 を経た純水を流体混合器5 、開閉バルブcを
経て容器2 内に徐々にタレ流して配管内などに残ってい
る残存表面処理用流体を純水と共に流出除去してドレイ
ンバルブhから排水した後バルブa,hを閉じ、切換バ
ルブe1 を元に戻す。
Here, after closing the valve f and switching the switching valve e1, the valve h is opened and the valve a is opened to about 1
Pure water at 5 ° C is put into the container 2 for about 10 seconds from the nozzle n to the sample 1
The sample 1 is sprayed and rinsed onto the surface of the sample 1, and the deionized water that has passed through the switching valve e1 gradually flows into the container 2 through the fluid mixer 5 and the opening / closing valve c to remove the residual surface treatment fluid remaining in the piping. After flowing out with pure water and draining from the drain valve h, the valves a and h are closed and the switching valve e1 is returned to its original state.

【0020】次いで塩酸などの他の表面処理用流体を切
換バルブe2 を経て流体混合器5 に導入し、バルブfと
バルブcを開放して、加圧蒸気を媒体として容器2 内に
導入する。容器2 内に導入した処理用流体は水蒸気と共
にシリコンウエハ等の試料1 の表面に凝縮する。
Next, another surface treatment fluid such as hydrochloric acid is introduced into the fluid mixer 5 through the switching valve e2, the valves f and c are opened, and the pressurized steam is introduced into the container 2 as a medium. The processing fluid introduced into the container 2 condenses on the surface of the sample 1 such as a silicon wafer together with water vapor.

【0021】ここでバルブfを閉じ、切換バルブe2 を
切換えてからバルブhを開け、再びバルブaを開放して
約15℃に冷却した純水を約10秒間容器2 内にノズル
nから試料1 に吹き付けて試料1 を再度純水でスプレー
リンスすると共に、切換バルブe2 を経た純水を流体混
合器5 、開閉バルブcを経て容器2 内に徐々にタレ流し
て配管内などに残っている残存流体を純水と共に流出除
去してドレインバルブhから排水した後バルブa,hを
閉じ、切換バルブe2 を元に戻す。
Here, the valve f is closed, the switching valve e2 is switched, the valve h is opened, the valve a is opened again, and pure water cooled to about 15 ° C. is put into the container 2 from the nozzle n to the sample 1 for about 10 seconds. The sample 1 is spray-rinsed again with pure water, and the pure water that has passed through the switching valve e2 gradually flows into the container 2 through the fluid mixer 5 and the opening / closing valve c, and the residual fluid that remains in the pipe, etc. Is removed together with pure water and drained from the drain valve h, then the valves a and h are closed and the switching valve e2 is returned to its original state.

【0022】次いでバルブd,jを開いて加熱蒸気を容
器2 内に直接導入し、容器内の空気をバルブjから外部
に追い出して容器2 内を水蒸気で充満させる。バルブd
とj,hを閉じて容器を密閉状態にしてから、バルブ
g,gを開いて冷却源10から冷却水を容器冷却部 2aに
おける水冷管9 に流し、容器2 内の下部を冷却すること
で容器2 内を真空に近い状態とし、シリコンウエハなど
の試料1の表面から水を蒸発させて除去した後、バルブ
g,gを閉じる。
Next, the valves d and j are opened to introduce the heated steam directly into the container 2, and the air in the container is expelled from the valve j to the outside to fill the container 2 with steam. Valve d
By closing j and h to close the container and then opening the valves g and g, cooling water is supplied from the cooling source 10 to the water cooling pipe 9 in the container cooling part 2a to cool the lower part of the container 2. After making the inside of the container 2 close to a vacuum and evaporating and removing water from the surface of the sample 1 such as a silicon wafer, the valves g and g are closed.

【0023】バルブcを開き、切換バルブe3 を切換え
て窒素ガスを媒体として酸化膜除去用のフッ化水素を密
閉容器2 内に導入して、シリコン酸化膜を除去する。そ
の後切換バルブe3 を元に戻しバルブcを閉じる。
The valve c is opened and the switching valve e3 is switched to introduce hydrogen fluoride for removing an oxide film into the closed container 2 using nitrogen gas as a medium to remove the silicon oxide film. After that, the switching valve e3 is returned to the original state and the valve c is closed.

【0024】次にバルブbを開いて容器2 内にN2 ガス
などの不活性ガスを不活性ガス源4から送り込み、前記
のフッ化水素ガスを上下のバルブjから周知の排ガス処
理装置に送り込み容器2 内を不活性ガスと置換して容器
2 内を常圧に戻してから気密用蓋を開けてシリコンウエ
ハなどの表面処理済の試料1 を取出す。
Next, the valve b is opened to feed an inert gas such as N 2 gas into the container 2 from the inert gas source 4, and the hydrogen fluoride gas is fed to the well-known exhaust gas treating apparatus from the upper and lower valves j. 2 Replace the inside with inert gas and
After returning the inside pressure to atmospheric pressure, open the airtight lid and take out the surface-treated sample 1 such as silicon wafer.

【0025】[0025]

【発明の効果】この発明は以上説明したように構成した
ので、以下に記載の効果を奏する。密閉容器に収納した
シリコンウエハにアンモニア水、過酸化水素水を加熱加
圧蒸気による媒体(キャリア)と共に容器内に導入し、
アンモニアやH2 O2 をシリコンウエハに凝縮させるこ
とができる。
Since the present invention is constructed as described above, it has the following effects. Ammonia water and hydrogen peroxide solution are introduced into the container together with the medium (carrier) by heating and pressurized steam in the silicon wafer housed in the closed container.
Ammonia and H2 O2 can be condensed on a silicon wafer.

【0026】冷却した純水をスプレーリンスしてから加
熱蒸気を導入し、容器内の空気を追い出して容器内を高
温水蒸気で充満させた後、容器を密閉状態にしてから、
容器内の一部を冷却することによって、容器内を真空に
近い状態とし、シリコンウエハの表面から急速に水を蒸
発させ除去することができる。
After spray rinsing the cooled pure water, introducing heated steam, expelling the air in the container to fill the container with high temperature steam, and then sealing the container,
By cooling a part of the inside of the container, the inside of the container can be brought into a state close to a vacuum, and water can be rapidly evaporated and removed from the surface of the silicon wafer.

【0027】したがって本発明によれば、試料1 の表面
処理の全工程を小型の密閉容器2 内における清浄な空間
ですべての処理が可能になり、環境からの汚染を受けな
いし、環境を汚染しないコンパクトな表面処理装置を安
価に提供できるという第1の効果が有る。
Therefore, according to the present invention, all the steps of the surface treatment of the sample 1 can be performed in a clean space in the small airtight container 2, and the environment is not polluted and does not pollute the environment. The first effect is that a compact surface treatment device can be provided at low cost.

【0028】またこの発明によれば洗浄処理液などの表
面処理用流体の使用量が少量でよく、しかも新規な処理
流体だけを使用するので処理品質の劣化がなく、廃水・
廃ガス処理に対する負担を軽減でき、ランニングコスト
も安くなるというような第2、第3の効果も有る。
Further, according to the present invention, a small amount of the surface treatment fluid such as the cleaning treatment liquid can be used, and since only the novel treatment fluid is used, the treatment quality is not deteriorated and the waste water.
There are second and third effects that the burden on waste gas treatment can be reduced and the running cost can be reduced.

【0029】特にこの発明では配管内や開閉バルブなど
に残存している不要な表面処理用流体を切換バルブe1
〜e3 の個別操作で同一試料に対する複数異種の表面処
理のインターバルに純水と共に外部にドレイン排出でき
るから異種処理薬剤の混合を防いでその混合による種々
の不具合を確実に防止できるという第4の効果も有る。
In particular, in the present invention, the unnecessary surface treatment fluid remaining in the piping, the on-off valve, etc. is replaced by the switching valve e1.
The fourth effect is to prevent the mixing of different kinds of treatment chemicals and to surely prevent various troubles due to the mixing because it is possible to drain pure water and the drain to the outside at intervals of a plurality of different kinds of surface treatments on the same sample by the individual operations of ~ e3. There is also.

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

【図1】この発明の実施例を示す配管系統図FIG. 1 is a piping system diagram showing an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 表面処理を施こすべき試料 2 密閉容器 2a 冷却部 3 低温純水源 4 不活性ガス源 5 流体混合器 6 加熱加圧蒸気源 7 表面処理用流体源 a〜d,f〜j 開閉バルブ e1,e2,e3 (中間閉止型)切換バルブ 1 Sample to be surface treated 2 Closed container 2a Cooling part 3 Low temperature pure water source 4 Inert gas source 5 Fluid mixer 6 Heated pressurized steam source 7 Surface treatment fluid source a to d, f to j Open / close valve e1, e2, e3 (intermediate closing type) switching valve

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 表面処理をすべき試料1 を内装した密閉
容器2 に冷却部 2aとドレイン部 2bとを設けると共
に、前記密閉容器2 には純水源3 、不活性ガス源4 、流
体混合器5 および加熱加圧蒸気源6 をそれぞれ開閉バル
ブa,b,c,dを経て配管接続し、前記流体混合器5
の複数の流入口にそれぞれ切換バルブe1 を介して表面
処理用流体源7 、純水源3 および開閉バルブfを経て前
記加熱加圧蒸気源6 を配管接続してなる表面処理装置。
1. A closed container 2 containing a sample 1 to be surface-treated is provided with a cooling part 2a and a drain part 2b, and the closed container 2 has a pure water source 3, an inert gas source 4 and a fluid mixer. 5 and the heating / pressurizing steam source 6 are connected to the fluid mixer 5 through the on-off valves a, b, c and d, respectively.
A surface treatment apparatus in which the heating and pressurized steam source 6 is connected to the plurality of inflow ports via a switching valve e1 through a surface treatment fluid source 7, a pure water source 3 and an opening / closing valve f.
JP30035492A 1992-10-13 1992-10-13 Surface treatment device Pending JPH06124936A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30035492A JPH06124936A (en) 1992-10-13 1992-10-13 Surface treatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30035492A JPH06124936A (en) 1992-10-13 1992-10-13 Surface treatment device

Publications (1)

Publication Number Publication Date
JPH06124936A true JPH06124936A (en) 1994-05-06

Family

ID=17883779

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30035492A Pending JPH06124936A (en) 1992-10-13 1992-10-13 Surface treatment device

Country Status (1)

Country Link
JP (1) JPH06124936A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57184677A (en) * 1981-05-07 1982-11-13 Sanyo Kiko Kk Confirming device for clamping of lock nut
JPS6420625A (en) * 1987-07-15 1989-01-24 Hitachi Ltd Surface treatment apparatus

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57184677A (en) * 1981-05-07 1982-11-13 Sanyo Kiko Kk Confirming device for clamping of lock nut
JPS6420625A (en) * 1987-07-15 1989-01-24 Hitachi Ltd Surface treatment apparatus

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