JPS63272040A - Circulating filtering and washing equipment - Google Patents
Circulating filtering and washing equipmentInfo
- Publication number
- JPS63272040A JPS63272040A JP62104546A JP10454687A JPS63272040A JP S63272040 A JPS63272040 A JP S63272040A JP 62104546 A JP62104546 A JP 62104546A JP 10454687 A JP10454687 A JP 10454687A JP S63272040 A JPS63272040 A JP S63272040A
- Authority
- JP
- Japan
- Prior art keywords
- cleaning
- washing
- concentration
- liquid
- pure water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000001914 filtration Methods 0.000 title claims description 5
- 238000005406 washing Methods 0.000 title abstract 10
- 239000000126 substance Substances 0.000 claims abstract description 43
- 239000007788 liquid Substances 0.000 claims abstract description 37
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 25
- 239000012535 impurity Substances 0.000 claims abstract description 12
- 238000004140 cleaning Methods 0.000 claims description 50
- 238000007865 diluting Methods 0.000 claims 1
- 238000004062 sedimentation Methods 0.000 claims 1
- 235000012431 wafers Nutrition 0.000 abstract description 18
- 239000010419 fine particle Substances 0.000 abstract description 9
- 239000002184 metal Substances 0.000 abstract description 9
- 238000005303 weighing Methods 0.000 abstract description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 3
- 229910001873 dinitrogen Inorganic materials 0.000 abstract description 3
- 230000000087 stabilizing effect Effects 0.000 abstract description 2
- 239000003795 chemical substances by application Substances 0.000 abstract 4
- 239000012141 concentrate Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 239000002244 precipitate Substances 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 12
- 238000010586 diagram Methods 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 4
- 239000003638 chemical reducing agent Substances 0.000 description 3
- 238000010790 dilution Methods 0.000 description 3
- 239000012895 dilution Substances 0.000 description 3
- 238000004065 wastewater treatment Methods 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000008367 deionised water Substances 0.000 description 2
- 229910021641 deionized water Inorganic materials 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- -1 polyethylene Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Cleaning Or Drying Semiconductors (AREA)
- Cleaning By Liquid Or Steam (AREA)
- Filtration Of Liquid (AREA)
Abstract
Description
【発明の詳細な説明】
〔概 要〕
循環濾過洗浄装置であって、ウェハー洗浄に使用した薬
品・純水に含まれた有機物・金属不純物・微粒子をフィ
ルター・紫外線殺菌装置等を用いて除去し、且つ薬品濃
度を自動的に調節することにより、薬品・純水中の不純
物及び薬品濃度を一定の値に保持し均一なウェハー洗浄
を行なうことを可能とする。[Detailed Description of the Invention] [Summary] This is a circulating filtration cleaning device that removes organic substances, metal impurities, and fine particles contained in chemicals and pure water used for wafer cleaning using a filter, ultraviolet sterilization device, etc. By automatically adjusting the chemical concentration, impurities in the chemical/pure water and the chemical concentration can be maintained at constant values, and uniform wafer cleaning can be performed.
本発明は、半導体装置の製造工程のウェハー洗浄等に使
用する洗浄装置に関するものである。The present invention relates to a cleaning apparatus used for cleaning wafers and the like in the manufacturing process of semiconductor devices.
従来のウェハー洗浄装置は第3図に示すように、処理槽
2に使用薬品(硫酸等)をポリエチレン。As shown in FIG. 3, conventional wafer cleaning equipment uses chemicals (such as sulfuric acid) in a processing tank 2 as polyethylene.
ガラス等の容器3から入れてバスケットと呼ばれるウェ
ハー収納箱4にウェハー5をセットした後、薬品・純水
でウェハーを洗浄するようになっているが、処理槽2内
の薬品・純水中の微粒子、金属不純物等はウェハー5を
洗浄するたびに増大するため、ウェハー5をある枚数洗
浄したら処理槽2内の薬品・純水を廃棄し、新しい薬品
・純水と交換するようになっている。なお排出ガス及び
俳水は第4図に示す排ガス処理装置及び第5図に示す排
水処理装置により処理している。After wafers 5 are placed in a wafer storage box 4 called a basket from a container 3 made of glass or the like, the wafers are cleaned with chemicals and pure water. Fine particles, metal impurities, etc. increase each time the wafers 5 are cleaned, so after a certain number of wafers 5 have been cleaned, the chemicals and pure water in the processing tank 2 are discarded and replaced with new chemicals and pure water. . Note that exhaust gas and water are treated by an exhaust gas treatment device shown in FIG. 4 and a wastewater treatment device shown in FIG. 5.
上記従来のウェハー洗浄装置では、■薬品・純水の使用
量が多い。@新しい薬品・純水と廃゛棄前の薬品・純水
の微粒子、金属不純物等のレベルが異なり均一にウェハ
ーが洗浄できない。O薬品・純水の使用量が多いため第
4図の排気ガス処理装置及び第5図に示す排水処理装置
の処理能力を増大させなければならない。■薬品・純水
を加熱ヒータ6を用いて加熱しウェハーを洗浄する場合
、加熱時間により薬品濃度が変化し洗浄能力が変化して
しまう。等の問題があった。In the conventional wafer cleaning equipment described above, ■ large amounts of chemicals and pure water are used; @Wafers cannot be cleaned uniformly because the levels of fine particles, metal impurities, etc. in the new chemicals/deionized water and the chemicals/deionized water before disposal are different. Since the amount of O chemicals and pure water used is large, the processing capacity of the exhaust gas treatment device shown in FIG. 4 and the wastewater treatment device shown in FIG. 5 must be increased. (2) When cleaning wafers by heating chemicals and pure water using the heater 6, the concentration of the chemicals changes depending on the heating time, and the cleaning ability changes. There were other problems.
本発明はこのような点にかんがみて創作されたもので、
薬品の濃度及び薬品・純水中の有機物。The present invention was created in view of these points.
Concentration of chemicals and organic matter in chemicals and pure water.
金属不純物、微粒子の濃度を長時間にわたって一定の値
を保持し均一なウェハー洗浄が行なえる循環濾過洗浄装
置を提供することを目的としている。It is an object of the present invention to provide a circulating filtration and cleaning device that can maintain the concentration of metal impurities and particulates at a constant value over a long period of time and perform uniform wafer cleaning.
〔問題点を解決するための手段〕
このため本発明においては第1図に例示するように、洗
浄槽22と、洗浄液中の不純物を沈澱濾別するオーバー
フロー装置13と、前記洗浄槽22から洗浄液を汲み上
げて前記オーバーフロー装置13に送るポンプIIと、
該ポンプ11とオーバーフロー装置13とをつなぐパイ
プの途中に設けられた紫外線殺菌装置28.ガス・液分
離器29、フィルタ12と、洗浄液の薬品濃度を検出す
る濃度計30 、30’ により洗浄槽22に純水・薬
品を補給して希釈・濃縮を自動的に行なう手段とを少な
くとも具備したことを特徴としている。[Means for Solving the Problems] Therefore, in the present invention, as illustrated in FIG. a pump II that pumps up and sends it to the overflow device 13;
An ultraviolet sterilizer 28 is provided in the middle of the pipe connecting the pump 11 and the overflow device 13. It is equipped with at least a gas/liquid separator 29, a filter 12, and means for automatically performing dilution and concentration by replenishing pure water and chemicals into the cleaning tank 22 using concentration meters 30 and 30' that detect the concentration of chemicals in the cleaning liquid. It is characterized by what it did.
紫外線殺菌装置2 Bにより洗浄液中のレジスト。 Resist in the cleaning solution by ultraviolet sterilizer 2B.
バクテリヤ等の有機物を気体に分解させて除去すること
によりフィルタ12の目づまりを防止し、フィルタ12
とオーバーフロー装置13とで洗浄液中の金属不純物及
び微粒子を除去することで洗浄液を循環して使用でき、
加熱ヒータ32により洗浄液の薬品濃度が高くなったり
、ウェハーからの水分持ち込み等で薬品濃度が低くなっ
たときは、濃度計30 、30’ により純水・薬品を
自動的に補給して希釈・濃縮し一定濃度に保持すること
により洗浄能力を一定に保つことが可能となる。By decomposing organic substances such as bacteria into gas and removing them, clogging of the filter 12 is prevented.
The cleaning liquid can be circulated and used by removing metal impurities and fine particles in the cleaning liquid with the overflow device 13 and the overflow device 13.
When the chemical concentration in the cleaning solution increases due to the heating heater 32, or when the chemical concentration decreases due to moisture brought in from the wafer, etc., the concentration meters 30 and 30' automatically replenish pure water and chemicals for dilution and concentration. By maintaining the concentration at a constant level, it is possible to maintain the cleaning ability at a constant level.
第1図は本発明の実施例を示す図である。 FIG. 1 is a diagram showing an embodiment of the present invention.
本実施例は第1図に示すように、洗浄槽22と、該洗浄
槽22から洗浄液を汲み上げるポンプ11と、該ポンプ
11に接続された紫外線殺菌装置28、ガス・液分離器
29.フィルタ12及びオーバーフロー装置13と、薬
品供給装置33等を具備して構成されている。As shown in FIG. 1, this embodiment includes a cleaning tank 22, a pump 11 that pumps cleaning liquid from the cleaning tank 22, an ultraviolet sterilizer 28 connected to the pump 11, a gas/liquid separator 29. It is configured to include a filter 12, an overflow device 13, a chemical supply device 33, and the like.
そして前記洗浄槽22には窒素ガスを用いる攪拌装22
3と、液面を一定にするための液面センサ19と、薬品
濃度を検出する濃度計30とが設けられ、オーバーフロ
ー装置13は第2図a、bに示す角筒形又は第2図c、
dに示す円筒形の槽の上端に多数の■形又はU形の溝が
形成されており、該清からオーバーフローする洗浄液は
四方に流れて洗浄槽22に戻り粒子は沈澱して槽の中に
残るようになっている。またこのオーバーフロー装置1
3には第1図に示すように洗浄液を加熱するためのヒー
タ32と、薬品濃度を検出する濃度計30°が設けられ
、該濃度計30°は前記洗浄槽に設けられた濃度計30
と共に洗浄液の薬品濃度を監視し、それが規定以上にな
ったときは純水バルブ31を開いて規定濃度になるまで
純水を補給し、濃度が規定以下になったときは、バルブ
21を開いて規定濃度になるまで薬品を補給するように
なっている。また薬品供給装置33は薬品を貯蔵する液
体容器14と、エアシリンダ15により前記容器14に
挿抜てきるノズル16と、該ノズル16に接続した秤量
槽18と、該秤量槽に液体容器14の薬品を吸入するた
めの減圧器 17等を具備している。The cleaning tank 22 has a stirring device 22 that uses nitrogen gas.
3, a liquid level sensor 19 for keeping the liquid level constant, and a concentration meter 30 for detecting the drug concentration, and the overflow device 13 has a rectangular cylinder shape as shown in FIGS. ,
A large number of ■-shaped or U-shaped grooves are formed at the upper end of the cylindrical tank shown in d, and the cleaning liquid that overflows from the cleaning liquid flows in all directions and returns to the cleaning tank 22, where particles settle and enter the tank. It is meant to remain. Also, this overflow device 1
3 is provided with a heater 32 for heating the cleaning liquid and a concentration meter 30° for detecting the chemical concentration, as shown in FIG.
At the same time, the chemical concentration of the cleaning liquid is monitored, and when it exceeds a specified value, the pure water valve 31 is opened to replenish pure water until the specified concentration is reached, and when the concentration falls below the specified value, the valve 21 is opened. The system replenishes chemicals until they reach the specified concentration. Further, the chemical supply device 33 includes a liquid container 14 for storing chemicals, a nozzle 16 that is inserted into and removed from the container 14 by an air cylinder 15, a weighing tank 18 connected to the nozzle 16, and a medicine in the liquid container 14 in the weighing tank. It is equipped with a pressure reducer 17 etc. for inhaling.
このように構成された本実施例は、洗浄槽22に純水を
指定レベルまで入れ、次に液体容器14を自動的にエア
シリンダ15を利用してノズル16を容器内に入れ、減
圧器17で秤量槽18の容器中に薬品を吸入し、秤量槽
18が一定のレベルまで達したら液面センサ19にてバ
ルブ20を閉にし、同時にバルブ21を開にし洗浄槽2
2に供給する。これを窒素ガスを用いた撹拌器23で攪
拌して洗浄液となし、次いでバルブ24を開きポンプ1
1を作動させ洗浄液を紫外線殺菌装置28、ガス・液分
離器29.フィルタ12.オーバーフロー装置13を通
して洗浄槽22に戻すようにして循環させながらウェハ
ーを洗浄するが、ウェハーを数多く洗浄していくと洗浄
液中に有機物、金属不純物、微粒子等が増えてくる。こ
の中のレジスト、バクテリア等の有機物は紫外線殺菌装
置28でオゾンなどにより気体に分解されガス・液分離
器29を通して除去される。また金属不純物及び微粒子
はフィル゛り12で濾過され、さらにオーバーフロー装
置、13で分離され、微粒子を除去された洗浄液は洗浄
槽22へ戻される。オーバーフロー装置13で除去され
た微粒子はバルブ26を開いて排除する。またオーバー
フロー装置13を使用しないときもバルブ25を開いて
洗浄液を循環させることもできる。In this embodiment configured as described above, pure water is poured into the cleaning tank 22 to a specified level, then the liquid container 14 is automatically placed into the container using the air cylinder 15, and the nozzle 16 is put into the container, and the pressure reducer 17 The chemical is inhaled into the container of the weighing tank 18, and when the weighing tank 18 reaches a certain level, the liquid level sensor 19 closes the valve 20, and at the same time opens the valve 21 to close the cleaning tank 2.
Supply to 2. This is stirred with a stirrer 23 using nitrogen gas to form a cleaning liquid, and then the valve 24 is opened and the pump 1
1 and the cleaning liquid is transferred to the ultraviolet sterilizer 28 and the gas/liquid separator 29. Filter 12. The wafers are cleaned while being circulated through the overflow device 13 and returned to the cleaning tank 22, but as a large number of wafers are cleaned, organic substances, metal impurities, fine particles, etc. increase in the cleaning liquid. Organic substances such as resist and bacteria in this are decomposed into gas by ozone or the like in an ultraviolet sterilizer 28 and removed through a gas/liquid separator 29. Further, metal impurities and fine particles are filtered by a filter 12 and further separated by an overflow device 13, and the cleaning liquid from which fine particles have been removed is returned to the cleaning tank 22. The particulates removed by the overflow device 13 are removed by opening the valve 26. Further, even when the overflow device 13 is not in use, the valve 25 can be opened to circulate the cleaning liquid.
さらに加熱ヒータ32にて洗浄液を加熱させ長時間使用
するときは水分が蒸発し薬品の濃度が上昇するが、この
ようなときは濃度計30 、30’が検知し純水バルブ
31を開いて規定濃度になるまで純水を補給し洗浄能力
を一定に保持することができる。またウェハーからの水
分持ち込み等で薬品の濃度が低下した場合も同様に、濃
度計30 、30’が検知し、バルブ21を開いて規定
濃度になるまで薬品を補給し洗浄能力を一定に保持する
ことができる。Furthermore, when the cleaning liquid is heated by the heater 32 and used for a long time, the water evaporates and the concentration of the chemical increases. In such a case, the concentration meter 30, 30' detects this and opens the pure water valve 31 to adjust the concentration of the chemical. By replenishing pure water until the concentration is reached, the cleaning ability can be maintained at a constant level. Similarly, if the concentration of the chemical drops due to water being brought in from the wafer, etc., the concentration meters 30 and 30' will detect this, and the valve 21 will be opened to replenish the chemical until the specified concentration is reached, keeping the cleaning performance constant. be able to.
以上述べてきたように、本発明によれば、洗浄液中の有
機物、金属不純物、微粒子をフィルタ。As described above, according to the present invention, organic matter, metal impurities, and fine particles in the cleaning liquid can be filtered.
紫外線殺菌装置等により除去し、また薬品濃度を希釈・
濃縮し濃度を一定に保つことにより薬品を廃棄すること
なく循環させて使用することができるので洗浄液の使用
量を削減することができ、また洗浄した製品の品質の向
上、安定化ができ歩留り向上が可能となり、さらに自動
希釈・濃縮ができるため作業工数削減と安全性が向上す
る。また排水、排気の処理設備の能力アップを行なう必
要がなく公害防止能力も向上する等の効果を実現するこ
とができ、実用的には極めて有用である。It is removed using an ultraviolet sterilizer, etc., and the concentration of chemicals is diluted and
By concentrating and keeping the concentration constant, chemicals can be circulated and used without being disposed of, reducing the amount of cleaning fluid used, and improving and stabilizing the quality of cleaned products, increasing yield. Furthermore, automatic dilution and concentration are possible, reducing work hours and improving safety. In addition, it is not necessary to increase the capacity of waste water and exhaust gas treatment equipment, and effects such as improved pollution prevention ability can be achieved, which is extremely useful in practical terms.
第1図は本発明の実施例を示す図、
第2図は本発明の実施例に用いるオーバーフロー装置を
示す図、
第3図は従来のウェハー洗浄装置を示す図、第4図は従
来の排ガス処理装置を示す図、第5図は従来の排水処理
装置を示す図である。
第1図において、
11はポンプ、 12 、12’ はフィルタ
、13はオーバーフロー装置、
14は液体容器、 15はエアシリンダ、16
はノズル、 17は減圧器、18は秤量槽、
19は液面センサ、20 、21 、24
〜27はバルブ、22は洗浄槽、 23は攪
拌装置、28は紫外線殺菌装置、
29はガス・液分離器、 30 、30°は濃度計、3
1は純水バルブ、 32は加熱ヒータ、33は薬品
供給袋・置である。Fig. 1 is a diagram showing an embodiment of the present invention, Fig. 2 is a diagram showing an overflow device used in an embodiment of the present invention, Fig. 3 is a diagram showing a conventional wafer cleaning device, and Fig. 4 is a diagram showing a conventional exhaust gas FIG. 5 is a diagram showing a conventional wastewater treatment device. In FIG. 1, 11 is a pump, 12 and 12' are filters, 13 is an overflow device, 14 is a liquid container, 15 is an air cylinder, and 16
is a nozzle, 17 is a pressure reducer, 18 is a weighing tank,
19 is a liquid level sensor, 20 , 21 , 24
~27 are valves, 22 are cleaning tanks, 23 are stirring devices, 28 are ultraviolet sterilizers, 29 are gas/liquid separators, 30 and 30° are concentration meters, 3
1 is a pure water valve, 32 is a heater, and 33 is a chemical supply bag/place.
Claims (1)
るオーバーフロー装置(13)と、前記洗浄槽(22)
から洗浄液を汲み上げて前記オーバーフロー装置(13
)に送るポンプ(11)と、該ポンプ(11)とオーバ
ーフロー装置(13)とをつなぐパイプの途中に設けら
れた紫外線殺菌装置(28)、ガス・液分離器(29)
、フィルタ(12)と、洗浄液の薬品濃度を検出する濃
度計(30、30’)により洗浄槽(22)に純水・薬
品を補給して希釈・濃縮を自動的に行なう手段とを少な
くとも具備したことを特徴とした循環濾過洗浄装置。1. A cleaning tank (22), an overflow device (13) for separating impurities in the cleaning liquid by sedimentation and filtration, and the cleaning tank (22)
The cleaning liquid is pumped up from the overflow device (13
), an ultraviolet sterilizer (28) installed in the middle of the pipe connecting the pump (11) and the overflow device (13), and a gas/liquid separator (29).
, a filter (12), and means for automatically replenishing pure water and chemicals to the cleaning tank (22) and diluting and concentrating them using concentration meters (30, 30') that detect the chemical concentration of the cleaning liquid. A circulating filtration cleaning device that is characterized by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62104546A JPS63272040A (en) | 1987-04-30 | 1987-04-30 | Circulating filtering and washing equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62104546A JPS63272040A (en) | 1987-04-30 | 1987-04-30 | Circulating filtering and washing equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63272040A true JPS63272040A (en) | 1988-11-09 |
Family
ID=14383479
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62104546A Pending JPS63272040A (en) | 1987-04-30 | 1987-04-30 | Circulating filtering and washing equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63272040A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02102725U (en) * | 1989-02-02 | 1990-08-15 | ||
KR20030086659A (en) * | 2002-05-06 | 2003-11-12 | 삼성전자주식회사 | Cleaning apparatus for semiconductor equipment and thereof cleaning method |
KR100455904B1 (en) * | 1997-09-09 | 2005-01-13 | 동경 엘렉트론 주식회사 | Cleaning process and cleaning plant |
JP2006121031A (en) * | 2004-05-19 | 2006-05-11 | Dainippon Screen Mfg Co Ltd | Substrate treating apparatus |
WO2013080580A1 (en) * | 2011-11-29 | 2013-06-06 | 栗田工業株式会社 | Cleaning device and method |
CN107739117A (en) * | 2017-10-24 | 2018-02-27 | 宁波华九文化传媒有限公司 | Domestic two rainwater-collecting filtering tank |
CN108695190A (en) * | 2017-04-07 | 2018-10-23 | 矽品精密工业股份有限公司 | Cleaning equipment |
-
1987
- 1987-04-30 JP JP62104546A patent/JPS63272040A/en active Pending
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02102725U (en) * | 1989-02-02 | 1990-08-15 | ||
KR100455904B1 (en) * | 1997-09-09 | 2005-01-13 | 동경 엘렉트론 주식회사 | Cleaning process and cleaning plant |
KR20030086659A (en) * | 2002-05-06 | 2003-11-12 | 삼성전자주식회사 | Cleaning apparatus for semiconductor equipment and thereof cleaning method |
JP2006121031A (en) * | 2004-05-19 | 2006-05-11 | Dainippon Screen Mfg Co Ltd | Substrate treating apparatus |
WO2013080580A1 (en) * | 2011-11-29 | 2013-06-06 | 栗田工業株式会社 | Cleaning device and method |
JP2013111536A (en) * | 2011-11-29 | 2013-06-10 | Kurita Water Ind Ltd | Cleaning device and method |
CN103889602A (en) * | 2011-11-29 | 2014-06-25 | 栗田工业株式会社 | Cleaning device and method |
CN103889602B (en) * | 2011-11-29 | 2016-04-06 | 栗田工业株式会社 | Cleaning device and method |
CN108695190A (en) * | 2017-04-07 | 2018-10-23 | 矽品精密工业股份有限公司 | Cleaning equipment |
CN107739117A (en) * | 2017-10-24 | 2018-02-27 | 宁波华九文化传媒有限公司 | Domestic two rainwater-collecting filtering tank |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US5364534A (en) | Process and apparatus for treating waste liquids | |
KR960000374B1 (en) | Semiconductor wafer cleaning method and apparatus thereof | |
JP5873020B2 (en) | Recycling method and apparatus for recycling waste water containing slurry from semiconductor processing processes, particularly chemical mechanical polishing processes | |
JP2002530188A (en) | Filtration of water using immersion membrane | |
JPS63272040A (en) | Circulating filtering and washing equipment | |
JPH0225030A (en) | Wet chemical surfa ce treatment of semiconductor wafer | |
TW589284B (en) | Liquid treatment method and apparatus | |
TWI492786B (en) | Method and apparatus for preparing a solution of a shear sensitive material | |
US6055995A (en) | Semiconductor manufacture apparatus | |
DE19507329C2 (en) | Device for dosing calcium hypochlorite in an aqueous system | |
JP2001170656A (en) | Process for removing solid particulate, more particularly silica and/or alumina particulate from waste water | |
KR20030042133A (en) | Method and system for cleaning membrane submersed in reactor | |
CN108911292A (en) | A kind of industrial wastewater efficient process equipment and treatment process | |
WO2015146626A1 (en) | Preprocessing device for online measurement in water system, online measurement device provided with same, and processing method for online measurement | |
TWI656100B (en) | Hydrogen peroxide-containing drainage treatment device and treatment method | |
JP3998997B2 (en) | Disinfection method of ultrapure water supply pipe | |
JP2003145148A (en) | Ultrapure water supply apparatus and ultrapure water supply method | |
EP3725393A1 (en) | Filtering membrane cleaning method | |
KR100483253B1 (en) | Method for recycling of aqueous cleaner solution and synthetic chemical solution using ozone and system thereof | |
JP2005230735A (en) | Apparatus and method for fixation of fluorine | |
US20230249993A1 (en) | Apparatus and methods for treating water for removal of pfas | |
KR100603855B1 (en) | Treatment method of metalworking fluid and cleansing solution and treatment system thereof | |
CN208087336U (en) | A kind of waste emulsified mixture purifying processing device | |
CN207608438U (en) | A kind of sewage disposal system | |
JP2001191094A (en) | Recycling method of washing water and apparatus threfor |