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JPH0812852B2 - Sterilization cleaning method of pure water circulation path for cleaning in semiconductor manufacturing - Google Patents
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JPH0812852B2 - Sterilization cleaning method of pure water circulation path for cleaning in semiconductor manufacturing - Google Patents

Sterilization cleaning method of pure water circulation path for cleaning in semiconductor manufacturing

Info

Publication number
JPH0812852B2
JPH0812852B2 JP2024916A JP2491690A JPH0812852B2 JP H0812852 B2 JPH0812852 B2 JP H0812852B2 JP 2024916 A JP2024916 A JP 2024916A JP 2491690 A JP2491690 A JP 2491690A JP H0812852 B2 JPH0812852 B2 JP H0812852B2
Authority
JP
Japan
Prior art keywords
pure water
cleaning
circulation path
water tank
ozone
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.)
Expired - Lifetime
Application number
JP2024916A
Other languages
Japanese (ja)
Other versions
JPH03229416A (en
Inventor
譲二 清水
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.)
Rohm Co Ltd
Original Assignee
Rohm 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 Rohm Co Ltd filed Critical Rohm Co Ltd
Priority to JP2024916A priority Critical patent/JPH0812852B2/en
Publication of JPH03229416A publication Critical patent/JPH03229416A/en
Publication of JPH0812852B2 publication Critical patent/JPH0812852B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、半導体の製造に際して、ウエハー等を洗浄
するための純水を、純水タンクとウエハー等に対する洗
浄箇所との間を循環するようにした洗浄用純水の循環経
路において、この洗浄用純水の循環経路に繁殖するバク
テリア類を、滅菌洗浄するための方法に関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention is intended to circulate pure water for cleaning a wafer or the like between a pure water tank and a cleaning portion for the wafer or the like when manufacturing a semiconductor. The present invention relates to a method for sterilizing and cleaning bacteria that propagate in the circulation path of pure water for cleaning in the circulation path of pure water for cleaning.

〔従来の技術〕[Conventional technology]

一般に、半導体の製造に際しては、そのウエハー等を
純水によって洗浄することが行なわれるが、この洗浄用
の純水は、純水を蓄えた純水タンクと、洗浄箇所との間
を循環するように構成される。
Generally, in the manufacture of semiconductors, the wafers and the like are washed with pure water. This pure water for cleaning is circulated between a pure water tank storing pure water and a cleaning place. Is composed of.

すなわち、純水製造装置にて製造された純水を、純水
タンク内に蓄え、この純水タンク内の純水を、循環ポン
プにて紫外線殺菌装置、イオン交換装置及びファイナル
フイルターに送って超純水にし、この超純水をクリーン
ルーム内における洗浄箇所に送液し、次いで、この洗浄
箇所から戻り管路を経て前記純水タンクに戻ると云う循
環経路に構成される。
That is, the pure water produced by the pure water producing device is stored in a pure water tank, and the pure water in the pure water tank is sent to an ultraviolet sterilizer, an ion exchange device, and a final filter by a circulation pump. It is made into pure water, and this ultrapure water is sent to a cleaning portion in a clean room, and then, from this cleaning portion to a pure water tank via a return pipe, the circulation path is constituted.

そして、この場合、前記洗浄用純水の循環経路内に
は、バクテリア類が繁殖するものであるから、前記洗浄
用純水の循環経路は、定期的に滅菌洗浄することが必要
である。
In this case, since bacteria propagate in the circulation path of the pure water for cleaning, the circulation path of the pure water for cleaning needs to be regularly sterilized and washed.

そこで、従来は、この洗浄用純水の循環経路の滅菌洗
浄に際して、前記純水タンク内に、過酸化水素を、純水
中における過酸化水素の濃度が2〜3%になるように注
入し、この過酸化水素を含む純水を、前記循環経路を適
宜時間にわたって循環し、次いで、循環を停止した状態
で適宜時間にわたって放置したのち、前記の循環を再開
し、前記純水タンク内に新規の純水を供給する一方、当
該純水タンクへの戻り管路から分岐する排水管路より、
過酸化水素を含む洗浄済排水を排出することを、循環経
路内における洗浄済排水が、新規な純水と完全に入れ代
わるまで継続することにより、前記洗浄用純水の循環経
路内を滅菌洗浄するようにしている。
Therefore, conventionally, when sterilizing and cleaning the circulation path of the pure water for cleaning, hydrogen peroxide is injected into the pure water tank so that the concentration of hydrogen peroxide in the pure water is 2 to 3%. The pure water containing hydrogen peroxide is circulated in the circulation path for an appropriate period of time, then left for a suitable period of time with the circulation stopped, and then the circulation is restarted to newly store in the pure water tank. While supplying the pure water of, from the drain pipe branching from the return pipe to the pure water tank,
By sterilizing the inside of the circulation path of the pure water for cleaning by continuing to discharge the cleaned waste water containing hydrogen peroxide until the cleaned waste water in the circulation path completely replaces the new pure water. I am trying.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

しかし、この過酸化水素による滅菌洗浄において、洗
浄用純水の循環経路内を略完全に滅菌洗浄するために
は、過酸化水素を含む純水の循環を、約2時間にわたっ
て行うことに加えて、その後における循環を停止しての
放置を約1時間にわたって行うようにしなければならな
いのである。
However, in this sterilization cleaning with hydrogen peroxide, in order to almost completely sterilize the circulation path of the pure water for cleaning, in addition to circulating pure water containing hydrogen peroxide for about 2 hours, It is necessary to stop the circulation thereafter and leave it for about 1 hour.

しかも、その後において、循環を再開し、純水タンク
に新規の純水を供給する一方、当該純水タンクへの戻り
管路から分岐する排水管路より、過酸化水素を含む洗浄
済の排水を排出する場合において、前記純水タンク内、
紫外線殺菌装置内、ファイナルフイルター及び戻り管路
内における過酸化水素を含む洗浄済排水の総てが、新規
の純水と完全に入れ代わるまでには、15〜18時間もの長
い時間がかかるのである。
Moreover, after that, the circulation is restarted and new pure water is supplied to the pure water tank, while the drainage pipe branching from the return pipe to the pure water tank is used to wash the wastewater containing hydrogen peroxide. When discharging, in the pure water tank,
It takes as long as 15 to 18 hours for all of the cleaned wastewater containing hydrogen peroxide in the ultraviolet sterilizer, the final filter and the return line to be completely replaced with new pure water.

従って、過酸化水素を使用する従来の滅菌洗浄方法で
は、その滅菌洗浄に、きわめて長い時間がかかるので、
著しく非能率的であるばかりか、この滅菌洗浄に際して
は、過酸化水素を含む洗浄済排水が多量に排出されるの
で、この過酸化水素を含む洗浄済排水を浄化処理するこ
とに多大の設備と経費とを必要すると言う問題があっ
た。
Therefore, in the conventional sterilization cleaning method using hydrogen peroxide, the sterilization cleaning takes an extremely long time.
Not only is it extremely inefficient, but since a large amount of washed wastewater containing hydrogen peroxide is discharged during this sterilization cleaning, a large amount of equipment is required to purify this washed wastewater containing hydrogen peroxide. There was the problem of needing expense.

本発明は、循環経路の滅菌洗浄に要する時間を大幅に
短縮すると共に、洗浄済排水の量を大幅に低減できるよ
うにした滅菌洗浄方法を提供することを目的とするもの
である。
It is an object of the present invention to provide a sterilization cleaning method capable of significantly reducing the time required for sterilization cleaning of a circulation path and significantly reducing the amount of cleaned drainage.

〔課題を解決するための手段〕[Means for solving the problem]

本発明者は、バクテリアの滅菌には、オゾンがきわめ
て効果的であり、且つ、オゾンは、大気中にきわめて容
易に分解・消失する性質を有するものである点に着目し
て本発明を完成するに至った。
The present inventor completes the present invention by paying attention to the fact that ozone is extremely effective for sterilizing bacteria and that ozone has a property of decomposing and disappearing into the atmosphere very easily. Came to.

すなわち、本発明は、前記の目的を達成するために、 「ウエハー等を洗浄するための純水を入れた純水タンク
と、ウエハー等の洗浄を行う洗浄箇所との間を、前記純
水タンク内における純水がイオン交換装置及び前記洗浄
箇所を経て再び前記純水タンクに戻る循環経路を形成し
て成る洗浄用純水循環経路において、前記純水タンク
に、オゾンを注入し、このオゾンを含む純水を、適宜時
間にわたって、前記循環経路中における前記イオン交換
装置をバイパスするように循環したのち、前記循環経路
内から排出する。」 ようにした。
That is, in order to achieve the above-mentioned object, the present invention is to provide the pure water tank between the pure water tank containing pure water for cleaning the wafer and the cleaning portion for cleaning the wafer. In the pure water circulation path for cleaning, which forms a circulation path in which pure water inside returns to the pure water tank through the ion exchange device and the cleaning location, ozone is injected into the pure water tank and the ozone is removed. The pure water contained is circulated for an appropriate time so as to bypass the ion exchange device in the circulation path, and is then discharged from the circulation path. ”

〔作用〕[Action]

本発明は、洗浄用純水の循環経路内における滅菌洗浄
に、オゾンを使用するものであって、このオゾンは、前
記従来から使用していた過酸化水素に比べて、10倍以上
の殺菌力を有するので、このオゾンを含む純水を、適宜
時間(1〜2時間程度)にわたって循環することによ
り、循環経路を、略完全に滅菌洗浄できるのである。
The present invention uses ozone for sterilization cleaning in a circulation path of pure water for cleaning, and this ozone has a sterilizing power 10 times or more as compared with hydrogen peroxide which has been conventionally used. Therefore, by circulating this pure water containing ozone for an appropriate time (about 1 to 2 hours), the circulation path can be almost completely sterilized and washed.

また、オゾンは、自然に分解して酸素になるので、前
記適宜時間にわたって循環したのち、循環経路内から排
出することにより、前記循環経路内に残存するオゾン
は、前記従来のように、純水タンク内に新規の純水を供
給する一方、当該純水タンクへの戻り管路から分岐する
排水管路より洗浄済排水を排出することを行うことな
く、速やかに消失するのである。
Further, since ozone is naturally decomposed into oxygen, it is circulated for the appropriate time and then discharged from the circulation path so that the ozone remaining in the circulation path is pure water as in the conventional case. While supplying new pure water into the tank, the washed waste water is promptly eliminated without being discharged from the drain pipe branching from the return pipe to the pure water tank.

このオゾンを含む純水による循環経路の滅菌洗浄に際
して、前記オゾンを含む純水を、前記循環経路中におけ
るイオン交換装置をバイパスして循環するようにしたこ
とにより、イオン交換装置におけるイオン交換樹脂に、
オゾンによる劣化等の悪影響を及ぼすを回避できるので
ある。
At the time of sterilizing and cleaning the circulation path with pure water containing ozone, the pure water containing ozone is circulated by bypassing the ion exchange apparatus in the circulation path, so that the ion exchange resin in the ion exchange apparatus can be used. ,
It is possible to avoid adverse effects such as deterioration due to ozone.

〔発明の効果〕〔The invention's effect〕

従って、本発明によると、循環経路における滅菌洗浄
に際して、循環経路中におけるイオン交換装置に悪影響
を及ぼすことを回避できるものでありながら、循環経路
内における滅菌洗浄に要する時間を、前記従来とは比較
にならない程短縮できて、滅菌洗浄の作業性を大幅に向
上できるのであり、しかも、前記滅菌洗浄に際して排出
される洗浄済排水の量は、循環経路内を循環させるだけ
の量で良く、洗浄済排水の量が、従来の場合とは比較に
ならない程少なくなるから、洗浄済排水の浄化処理に際
しての設備及び経費を大幅に低減できる効果を有する。
Therefore, according to the present invention, when sterilizing and cleaning the circulation path, it is possible to avoid adversely affecting the ion exchange device in the circulation path, while comparing the time required for the sterilization cleaning in the circulation path with the conventional one. Therefore, the workability of sterilization cleaning can be greatly improved, and the amount of washed drainage discharged during the sterilization cleaning is sufficient to circulate in the circulation path. Since the amount of waste water becomes so small that it is not comparable to the conventional case, it has the effect of significantly reducing the equipment and cost for purification treatment of washed waste water.

〔実施例〕〔Example〕

以下、本発明の実施例を図面(第1図)について説明
する。
An embodiment of the present invention will be described below with reference to the drawings (FIG. 1).

図において符号1は、純水製造装置2にて製造された
純水を蓄えるための純水タンクを示し、該純水タンク1
内における純水を、管路3を介して循環ポンプ4にて汲
み出し、管路5を介して紫外線殺菌装置6に導き、この
紫外線殺菌装置6から管路7を介してイオン交換装置8
に導き、このイオン交換装置8から管路9を介してファ
イナルフイルター10に導き、次いで、このファイナルフ
イルター10から管路11を介して、複数の蛇口12aを有す
るウエハー等の洗浄箇所12(この洗浄箇所12は、クリー
ンルーム内に設けられている)に送液したのち、この洗
浄箇所12から戻り管路13を経て前記純水タンク1に戻る
と云う循環経路に構成する。
In the figure, reference numeral 1 denotes a pure water tank for storing pure water manufactured by the pure water manufacturing apparatus 2, and the pure water tank 1
The pure water in the inside is pumped out by a circulation pump 4 through a pipe line 3, guided to an ultraviolet sterilization device 6 through a pipe line 5, and from this ultraviolet sterilization device 6 through a pipe line 7 an ion exchange device 8
To the final filter 10 from the ion exchange device 8 via the pipe line 9, and then from the final filter 10 via the pipe line 11 to the cleaning location 12 for the wafer having a plurality of faucets 12a. The place 12 is provided in a clean room), and then the circulating place is such that it returns from the washing place 12 to the pure water tank 1 via the return pipe 13.

前記イオン交換装置8には、当該イオン交換装置8へ
の入口弁8aと、当該イオン交換装置8からの出口弁8bと
が設けられていると共に、当該イオン交換装置8を迂回
する弁8d付きのバイパス管路8cが設けられている。
The ion exchange device 8 is provided with an inlet valve 8a to the ion exchange device 8 and an outlet valve 8b from the ion exchange device 8 and is provided with a valve 8d that bypasses the ion exchange device 8. A bypass line 8c is provided.

また、前記純水タンク1への戻り管路13には、開閉弁
14が設けられていると共に、弁16を備えた洗浄済排水の
排水用管路15が接続されている。
In addition, the return line 13 to the pure water tank 1 has an open / close valve.
14 is provided and is connected to a drainage line 15 for the washed drainage, which is provided with a valve 16.

更にまた、前記純水タンク1への戻り管路13のうち最
も高い部位には、気液分離室17を挿入して、この気液分
離室17の入口及び出口に各々弁18,19を設ける一方、前
記戻り管路13には、前記気液分離室17を迂回する弁21付
きバイパス管路20を設ける。
Furthermore, a gas-liquid separation chamber 17 is inserted into the highest part of the return pipe 13 to the pure water tank 1, and valves 18 and 19 are provided at the inlet and outlet of the gas-liquid separation chamber 17, respectively. On the other hand, the return conduit 13 is provided with a bypass conduit 20 with a valve 21 that bypasses the gas-liquid separation chamber 17.

そして、前記純水タンク1内の底部には、第2図に示
すように、複数の散気ノズル23を穿設して成る散気体22
を設けて、この散気体22に、オゾン発生装置24にて発生
したオゾンを、弁26付きの管路25を介して導入するよう
に構成する。
Then, as shown in FIG. 2, a diffused gas 22 formed by forming a plurality of diffused nozzles 23 at the bottom of the pure water tank 1.
Is provided, and ozone generated by the ozone generator 24 is introduced into the diffused gas 22 through a pipe line 25 having a valve 26.

この構成において、通常は、前記イオン交換装置8に
おける入口弁8a及び出口弁8bを開き、そのバイパス管路
8cにおける弁8dを閉じる一方、前記気液分離室17の入口
及び出口における弁18,19を閉じ、そのバイパス管路20
中の弁21を開き、更に、前記戻り管路13中における開閉
弁14を開き、排水用管路15中の弁16を閉じた状態で、前
記循環ポンプ4を駆動する。
In this configuration, normally, the inlet valve 8a and the outlet valve 8b in the ion exchange device 8 are opened, and the bypass line
The valve 8d in 8c is closed, while the valves 18 and 19 at the inlet and outlet of the gas-liquid separation chamber 17 are closed, and the bypass line 20 thereof is closed.
The circulation pump 4 is driven with the inside valve 21 opened, the opening / closing valve 14 in the return line 13 opened, and the valve 16 in the drainage line 15 closed.

すると、純水タンク1内における純水は、循環ポンプ
4にて紫外線殺菌装置6、イオン交換装置8及びファイ
ナルフイルター10を経て、クリーンルーム内における洗
浄箇所12に送液され、次いで、この洗浄箇所12から戻り
管路13を経て前記純水タンクに再び戻ると云うように循
環される。
Then, the pure water in the pure water tank 1 is sent to the cleaning location 12 in the clean room through the ultraviolet sterilizer 6, the ion exchange apparatus 8 and the final filter 10 by the circulation pump 4, and then this cleaning location 12 It is circulated so as to return to the pure water tank again via the return pipe line 13.

そして、滅菌洗浄に際しては、前記純水製造装置2か
ら純水タンク1への純水の供給を停止し、この純水タン
ク1内における純水に、オゾン発生装置24にて発生した
オゾンを散気体22における複数のノズル23から、当該純
水中におけるオゾンの濃度が0.05〜0.2ppmになるように
吹き込みする。
During the sterilization cleaning, the supply of pure water from the pure water producing device 2 to the pure water tank 1 is stopped, and the pure water in the pure water tank 1 is dispersed with ozone generated by the ozone generator 24. The gas 22 is blown from a plurality of nozzles 23 so that the concentration of ozone in the pure water is 0.05 to 0.2 ppm.

次いで、前記イオン交換装置8における入口弁8a及び
出口弁8bを閉じ、そのバイパス管路8cにおける弁8dを開
く一方、前記気液分離室17の入口及び出口における弁1
8,19を開き、そのバイパス管路20中の弁21を閉じた状態
で、前記循環ポンプ4を駆動する。
Then, the inlet valve 8a and the outlet valve 8b in the ion exchange device 8 are closed, and the valve 8d in the bypass pipe line 8c thereof is opened, while the valve 1 at the inlet and the outlet of the gas-liquid separation chamber 17 is closed.
The circulation pump 4 is driven with the valves 8 and 19 opened and the valve 21 in the bypass line 20 closed.

すると、純水タンク1内におけるオゾンを含む純水
は、循環ポンプ4にて紫外線殺菌装置6通過し、次い
で、イオン交換装置8をバイパスしたのち、ファイナル
フイルター10を経て、クリーンルーム内における洗浄箇
所12に送液され、次いで、この洗浄箇所12から戻り管路
13を経て前記純水タンク1に再び戻ると云うように循環
されるから、前記純水タンク1から再び純水タンク1に
至る循環経路内を、前記オゾンを含む純水を前記イオン
交換装置8に流入させることなく、滅菌洗浄できる一
方、この純水中のオゾンの一部は、気液分離室17におい
て純水中から分離するのである。
Then, the pure water containing ozone in the pure water tank 1 passes through the ultraviolet sterilizer 6 by the circulation pump 4, then bypasses the ion exchange device 8, and then passes through the final filter 10 to the cleaning location 12 in the clean room. To the return line from this cleaning point 12.
Since it is circulated so as to return to the pure water tank 1 again via 13, the pure water containing ozone is passed through the ion exchange device 8 in the circulation path from the pure water tank 1 to the pure water tank 1 again. While it can be sterilized and washed without flowing into, the ozone in the pure water is partly separated from the pure water in the gas-liquid separation chamber 17.

そして、前記のようにして滅菌洗浄が終わると、戻り
管路13中における開閉弁14を閉じる一方、排水用管路15
中の弁16を開くことにより、洗浄済排水を、前記排水用
管路15等から排出するのであり、前記純水中におけるオ
ゾンは、自然に分解して酸素になって消失するのであ
る。
When the sterilization cleaning is completed as described above, the on-off valve 14 in the return line 13 is closed and the drainage line 15 is closed.
By opening the inner valve 16, the washed wastewater is discharged from the drainage pipe 15 and the like, and ozone in the pure water is spontaneously decomposed into oxygen and disappears.

この場合において、本発明者の実験によると、純水中
におけるオゾンの濃度を、0.05〜0.2ppmにすることによ
り、1〜2時間程度の循環によって完全に滅菌洗浄でき
ると共に、滅菌洗浄に使用したオゾンは約10分程度で完
全に消失するのであり、一方、オゾンが人体に及ぼす危
険性は殆どなく、安全であった。
In this case, according to the experiment of the present inventor, by setting the ozone concentration in pure water to 0.05 to 0.2 ppm, it was possible to completely sterilize and wash by circulation for about 1 to 2 hours, and used for sterilizing and washing. Ozone completely disappears in about 10 minutes, and on the other hand, ozone was safe with almost no danger to the human body.

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

図面は本発明の実施例を示し、第1図は洗浄用純水の循
環経路を示す図、第2図はオゾンの散気体の斜視図であ
る。 1……純水タンク、2……純水製造装置、4……循環ポ
ンプ、6……紫外線殺菌装置、8……イオン交換装置、
10……ファイナルフイルター、12……ウエハー等の洗浄
箇所、13……戻り管路、14……開閉弁、15……排水用管
路、22……オゾンの散気体、24……オゾン発生装置。
The drawings show an embodiment of the present invention, FIG. 1 is a view showing a circulation path of pure water for cleaning, and FIG. 2 is a perspective view of ozone diffused gas. 1 ... Pure water tank, 2 ... Pure water production device, 4 ... Circulation pump, 6 ... UV sterilizer, 8 ... Ion exchange device,
10 …… Final filter, 12 …… Wafer cleaning part, 13 …… Return pipeline, 14 …… Open / close valve, 15 …… Drainage pipeline, 22 …… Ozone diffuser, 24 …… Ozone generator .

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】ウエハー等を洗浄するための純水を入れた
純水タンクと、ウエハー等の洗浄を行う洗浄箇所との間
を、前記純水タンク内における純水がイオン交換装置及
び前記洗浄箇所を経て再び前記純水タンクに戻る循環経
路を形成して成る洗浄用純水循環経路において、前記純
水タンクに、オゾンを注入し、このオゾンを含む純水
を、適宜時間にわたって、前記循環経路中における前記
イオン交換装置をバイパスするように循環したのち、前
記循環経路内から排出することを特徴とする半導体製造
における洗浄用純水循環経路の滅菌洗浄方法。
1. Pure water in the pure water tank is between the pure water tank containing pure water for cleaning wafers and the like and a cleaning place for cleaning the wafers, etc. In a pure water circulation path for cleaning, which forms a circulation path that returns to the pure water tank via a portion, ozone is injected into the pure water tank, and pure water containing this ozone is circulated for an appropriate time. A method for sterilizing and cleaning a pure water circulation path for cleaning in semiconductor manufacturing, which comprises circulating so as to bypass the ion exchange device in the path and then discharging from the circulation path.
JP2024916A 1990-02-02 1990-02-02 Sterilization cleaning method of pure water circulation path for cleaning in semiconductor manufacturing Expired - Lifetime JPH0812852B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2024916A JPH0812852B2 (en) 1990-02-02 1990-02-02 Sterilization cleaning method of pure water circulation path for cleaning in semiconductor manufacturing

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2024916A JPH0812852B2 (en) 1990-02-02 1990-02-02 Sterilization cleaning method of pure water circulation path for cleaning in semiconductor manufacturing

Publications (2)

Publication Number Publication Date
JPH03229416A JPH03229416A (en) 1991-10-11
JPH0812852B2 true JPH0812852B2 (en) 1996-02-07

Family

ID=12151486

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2024916A Expired - Lifetime JPH0812852B2 (en) 1990-02-02 1990-02-02 Sterilization cleaning method of pure water circulation path for cleaning in semiconductor manufacturing

Country Status (1)

Country Link
JP (1) JPH0812852B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20220204378A1 (en) * 2017-10-31 2022-06-30 Kitz Corporation Wash water processing apparatus and sterilization and purification unit, and wash water processing method of semiconductor element or liquid-crystal glasses

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08148457A (en) * 1994-11-15 1996-06-07 Tadahiro Omi Wet station, wet cleaning method and wet cleaning apparatus using the wet station
JP2677235B2 (en) * 1995-03-30 1997-11-17 日本電気株式会社 Semiconductor substrate cleaning apparatus, cleaning method, and cleaning liquid generation method
JP3620577B2 (en) * 1999-05-14 2005-02-16 栗田工業株式会社 Cleaning method for ultrapure water production system
CN117181694B (en) * 2023-05-31 2025-11-04 安徽富乐德科技发展股份有限公司 A faceplate component cleaning device and cleaning solution formula

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02203992A (en) * 1989-02-03 1990-08-13 Satoe Yoshinaga Device for washing and purifying article

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20220204378A1 (en) * 2017-10-31 2022-06-30 Kitz Corporation Wash water processing apparatus and sterilization and purification unit, and wash water processing method of semiconductor element or liquid-crystal glasses
US11975995B2 (en) * 2017-10-31 2024-05-07 Kitz Corporation Wash water processing apparatus and sterilization and purification unit, and wash water processing method of semiconductor element or liquid-crystal glasses

Also Published As

Publication number Publication date
JPH03229416A (en) 1991-10-11

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