JPS631411A - Fine dust-free type liquid filtering and feeding device - Google Patents
Fine dust-free type liquid filtering and feeding deviceInfo
- Publication number
- JPS631411A JPS631411A JP61144166A JP14416686A JPS631411A JP S631411 A JPS631411 A JP S631411A JP 61144166 A JP61144166 A JP 61144166A JP 14416686 A JP14416686 A JP 14416686A JP S631411 A JPS631411 A JP S631411A
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- filtration
- container
- passage
- substance
- 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
- 239000007788 liquid Substances 0.000 title claims abstract description 165
- 238000001914 filtration Methods 0.000 title claims abstract description 45
- 239000000126 substance Substances 0.000 claims abstract description 41
- 239000002245 particle Substances 0.000 claims abstract description 8
- 239000012535 impurity Substances 0.000 claims description 9
- 238000004140 cleaning Methods 0.000 claims description 5
- 230000000694 effects Effects 0.000 abstract description 6
- 239000007787 solid Substances 0.000 abstract description 5
- 238000011144 upstream manufacturing Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 21
- 238000011109 contamination Methods 0.000 description 6
- 230000003749 cleanliness Effects 0.000 description 4
- 238000003860 storage Methods 0.000 description 4
- 239000011344 liquid material Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- 239000000356 contaminant Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、液体濾過供給装買に関し、詳しくは、微細な
固体粒子等を不純物として含有する液体物質を濾過し、
高純度の液体物貿を供給しII7る液体濾過供給装置に
関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a liquid filtration supply device, and more specifically, the present invention relates to a liquid filtration and supply device, and more specifically, a device for filtering a liquid substance containing fine solid particles as impurities,
This invention relates to a liquid filtration and supply device for supplying high-purity liquid goods.
近年、医薬品工業,食品工業あるいは電子工業などの分
野で純度の高いしのが要求され、この秤の一過作業が小
要な作業の7つとなって来でいる。In recent years, high purity resin has been required in fields such as the pharmaceutical industry, food industry, and electronics industry, and this one-time operation of the scale has become one of the minor operations.
たとえば、電子工業分野におけるプリント配線Jj板の
製造、苗密なIC.LSI等の電子回路の製造などの分
野においては、使用する液体・k品中に微細な固体粒子
などの不純物が混在していると、不良品の発生率が多く
なるので、特に高純度の製品が要求される。ここでいう
不純物の大きさは、粒径0.1〜10μrrlを指す。For example, manufacturing of printed wiring JJ boards in the electronics industry, Naomi IC. In the field of manufacturing electronic circuits such as LSIs, if the liquids and products used contain impurities such as fine solid particles, the incidence of defective products increases, so it is especially important to avoid high-purity products. is required. The size of impurities here refers to a particle size of 0.1 to 10 μrrl.
このような微細な固体粒子などの不純物は、液体薬品の
製造に際して精密精製して除去しても、液体薬品の輸送
時、あるいは貯蔵時、さらには貯蔵タンクから使川場所
までの配管等に混入するらのの他、液体とその通路との
界面に一口管壁に収着したもの、又は新たに生成する微
細なダストが、常に液中へ供給される。従って使用に際
して液体物質を十分に濾過し、液体物質をダストフリー
な状態を保持して使用場所に供給することが必要である
。Even if these impurities such as fine solid particles are removed by precision purification during the manufacturing of liquid chemicals, they can still get mixed in during transportation or storage of liquid chemicals, or even in the piping from the storage tank to the Shikawa site. In addition to silica particles, particles sorbed to the tube wall or newly generated fine dust at the interface between the liquid and its passage are constantly supplied into the liquid. Therefore, it is necessary to thoroughly filter the liquid substance before use and to maintain the liquid substance in a dust-free state before supplying it to the place of use.
(従来技術および問題点〕
従来、ダストフリーの液体物質を供給する装置として特
公昭58−24166号公報に記載の装置が提供されて
いるが、この装置は濾過手段が極めて簡単である上に一
過式であり十分な一過効果が得られない。(Prior Art and Problems) Conventionally, a device described in Japanese Patent Publication No. 58-24166 has been provided as a device for supplying a dust-free liquid substance, but this device has an extremely simple filtration means and is It is a long-term formula and a sufficient temporary effect cannot be obtained.
又、特公昭38−4539号公報、あるいは特開昭60
−71012号公報に2個の固定容器間で液体物質を濾
過手段を多数回循環させて濾過効果を高めた後、使用場
所へ供給する8i置が提供されている。これらは濾過手
段を液体物質が多数回循環されることから、一過式のも
のに比べ濾過効果は高くなるが、濾過手段を経た後、使
用場所まで液体物質を輸送ずる過程で清浄化された液体
物質が汚染される危険性がある。Also, Japanese Patent Publication No. 38-4539, or Japanese Patent Application Laid-open No. 1983
Japanese Patent No. 71012 discloses an 8i system in which a liquid substance is circulated between two fixed containers through a filtration means many times to increase the filtration effect, and then supplied to a place of use. In these methods, the liquid substance is circulated through the filtration means many times, so the filtration effect is higher than that of the one-time type. Risk of contamination of liquid substances.
また、液体物質の使用場所で液体物質(薬液)の使用が
中断ざれた場合、濾過手段からユースポイントまでの液
体通路中に停?Iilシた液体物質に液体通路の内壁に
付着した汚染物質が離脱する等により液体物質の汚染の
進行を許し、ユースボインl−での液体物質の使用が再
開された時に、汚染された液体物質をユースポイントへ
供給してしまう危険性がある。特にこの中断の場合、ユ
ースボイン1までの液体通路が長いときには液体物質の
汚染度は高くなる。そして、この汚染の危険度は、供給
を再開する時に限らず液体通路中に残留した液体物質を
その容器に戻すときにも、返戻管中に生じ混入した不純
物によって容器内の清浄液を再汚染するという危険性を
常にもっている。Also, if the use of a liquid substance (medicinal solution) is interrupted at the place where the liquid substance is used, will it stop in the liquid path from the filtration means to the point of use? Contaminants adhering to the inner walls of the liquid passages are released from the contaminated liquid substances, allowing the contamination of the liquid substances to progress, and when the use of liquid substances in the youth boiler is resumed, the contaminated liquid substances are removed. There is a risk of supplying it to the point of use. Particularly in the case of this interruption, if the liquid path to the youth boiler 1 is long, the degree of contamination of the liquid substance will be high. The risk of this contamination is not limited to when restarting the supply, but also when returning the liquid substance remaining in the liquid path to the container, re-contaminating the clean liquid in the container by impurities that are generated in the return pipe and mixed in. There is always a risk that this will happen.
本発明は、上記した様な従来の濾過供給装置における欠
点に鑑み発明した装置であって、ユースポイントにおい
て液体物質が未使用状態であっても液体物質を液体通路
内に停滞させることなく、濾過効果を高めて、常に清浄
化されたダストフリーの状態で液体物質利用部に供給す
ることにある。The present invention is a device invented in view of the drawbacks of the conventional filtration and supply devices as described above, and is a device that filters the liquid material without stagnation in the liquid passage even if the liquid material is unused at the point of use. The purpose is to enhance the effectiveness and always supply the liquid material utilization section in a clean and dust-free state.
すなわち、本発明の装置は微細な固形粒子を不純物とし
て含有する液体物質を液体容器群よりユースポイントへ
濾過手段を有ずる液体通路を介して、清浄液として供給
し得る濾過供給装貿であって、該ユースポイント直前よ
り、該液体容器群との間に開閉弁と濾過手段とを有する
返送手段を設けたことを特徴として構成されており、濾
過効果を高め、かつ、液体物質を液体通路内に停7mさ
せることなく、常に清浄化されたダストフリーの状態で
利用場所に供給できるようになっている。That is, the apparatus of the present invention is a filtration supply device capable of supplying a liquid substance containing fine solid particles as impurities from a group of liquid containers to a point of use as a cleaning liquid through a liquid passage having a filtration means. The structure is characterized in that a return means having an on-off valve and a filtration means is provided between the liquid container group and the liquid container group immediately before the use point, thereby increasing the filtration effect and directing the liquid substance into the liquid passage. It is possible to supply the product to the place of use in a clean and dust-free condition without having to stop the product for 7 meters.
本発明の濾過供給装置は、硝酸,過酸化水素,アンモニ
ア水等,その他の化学桑品を清浄化し、ダストフリーの
状態として供給するために好適である。The filtration supply device of the present invention is suitable for cleaning other chemical products such as nitric acid, hydrogen peroxide, ammonia water, etc. and supplying them in a dust-free state.
次に、本発明に係る濾過供給装置の実施態様の一例を示
す添付図面により、本発明の詳細を説明ずる。Next, details of the present invention will be explained with reference to the accompanying drawings showing an example of an embodiment of the filtration supply device according to the present invention.
第1図は本発明に係る濾過供給装置における液体容器を
収納するクリーンベンチの外観斜視図を示し、Aはクリ
ーンベンチ本体、AI.A2は液体容器の収納部をそれ
ぞれ示す。FIG. 1 shows an external perspective view of a clean bench that accommodates a liquid container in a filtration supply device according to the present invention, where A is the clean bench main body, AI. A2 each indicates a housing section for a liquid container.
第2図は本発明に係る濾過供給Vt置の配管図を示ず。FIG. 2 does not show a piping diagram of the filtration supply Vt position according to the present invention.
第2図において、1.2は液体容器を示し、3は気体濾
過手段を、4,5は液体濾過手段を、6は減圧弁をそれ
ぞれ示す。液体容器1および2には、液体輸送用気体通
路14.15および液体物質の排出入用液体通路20.
21が付設されている。該気体通路14および15はそ
れぞれ気体通路12および13に接続し、気体通路12
,13は開開弁42,43を介して、液体輸送用気体供
給口に連通寸る気体通路11の一端に接続している。該
気体通路11には気体濾過手段3、間閉弁41および減
圧弁6が介設されている。又、気体通路14.15は開
閉弁44.45を介して気体排出通路16に接続してい
る。In FIG. 2, 1.2 represents a liquid container, 3 represents a gas filtration means, 4 and 5 represent a liquid filtration means, and 6 represents a pressure reducing valve. The liquid containers 1 and 2 are provided with gas passages 14.15 for liquid transport and liquid passages 20.15 for the discharge and entry of liquid substances.
21 is attached. The gas passages 14 and 15 are connected to the gas passages 12 and 13, respectively, and the gas passages 12 and 15 are connected to the gas passages 12 and 13, respectively.
, 13 are connected to one end of a gas passage 11 which communicates with a gas supply port for liquid transport via opening/opening valves 42 and 43. The gas passage 11 is provided with a gas filtering means 3, an intermittent valve 41, and a pressure reducing valve 6. Further, the gas passage 14.15 is connected to the gas discharge passage 16 via an on-off valve 44.45.
一方、液体物質の排出入用液体通路20.21は、開閉
弁46a,46b,47a,47bを介して、液体通路
22.23および27.28にそれぞれ接続している。On the other hand, liquid passages 20.21 for discharging and inputting liquid substances are connected to liquid passages 22.23 and 27.28, respectively, via on-off valves 46a, 46b, 47a, and 47b.
液体通路22.23は液体通路24の一端に運通し、該
液体通路24には液体濾過手段4が配設されている。該
液体通路24は液体通路25の一端と接続しており、該
液体通路25は開閉弁48を介して、液体通路26に接
続し該液体通路26の一端は、液体通路27.28に運
通し、液体容器1又は2に循環する第一液体循環通路が
形成されている。又、前記の液体通路24は、間閉弁5
0を介して液体通路29に連通し、該液体通路29は開
閉弁51を介してユースポイント(図面ではり,Pと表
示)に接続していると共に、開閉弁52を介し液体通路
30に連通している。該液体通路3oには液体濾過手段
5が介段されており、該液体通路30は、開閉弁4つを
介して液体通路26と接続し、前記の液体通路27.2
8を経由して液体容器1および2に循環する第二液体循
環通路(返送手段)が形成されている。The liquid passages 22, 23 communicate with one end of a liquid passage 24, in which liquid filtering means 4 are arranged. The liquid passage 24 is connected to one end of a liquid passage 25, and the liquid passage 25 is connected to a liquid passage 26 via an on-off valve 48, and one end of the liquid passage 26 is connected to a liquid passage 27, 28. , a first liquid circulation passage that circulates in the liquid container 1 or 2 is formed. Further, the liquid passage 24 is connected to the inter-closing valve 5.
The liquid passage 29 is connected to a use point (indicated by P in the drawing) via an on-off valve 51, and communicates with the liquid passage 30 via an on-off valve 52. are doing. A liquid filtering means 5 is interposed in the liquid passage 3o, and the liquid passage 30 is connected to the liquid passage 26 through four on-off valves, and the liquid passage 27.2 is connected to the liquid passage 26 through four on-off valves.
A second liquid circulation path (return means) is formed which circulates to the liquid containers 1 and 2 via 8.
次に、第2図により、本発明装置の運転概略について簡
単に説明する。不活性ガスから成る液体輸送用気体を該
気体供給口から気体通路11,12および14により液
体容器1に圧入することにより、液体容器1を加圧する
。液体容器1中の液体物質は液体通路20.22から前
記した第一液体循環通路により、液体容器2に移送され
る。液体容器1中の液体物質の全部が液体容器2に移送
されたら今度は気体通路13.15より液体容器2に圧
送用気体を送り、液体容器2中の液体物質を液体通路2
1.23を経由して前記第一液休循環通路により、液体
容器1に移送する。Next, referring to FIG. 2, an outline of the operation of the apparatus of the present invention will be briefly explained. The liquid container 1 is pressurized by injecting a liquid transporting gas made of an inert gas into the liquid container 1 from the gas supply port through the gas passages 11, 12, and 14. The liquid substance in the liquid container 1 is transferred from the liquid channel 20.22 to the liquid container 2 by the aforementioned first liquid circulation path. Once all of the liquid substance in the liquid container 1 has been transferred to the liquid container 2, pressurized gas is sent to the liquid container 2 from the gas passage 13.15, and the liquid substance in the liquid container 2 is transferred to the liquid passage 2.
1.23, and is transferred to the liquid container 1 through the first liquid idle circulation passage.
この様に液体容器1と2との間で液体物質を液体i!a
,a手段4を経由する第一液休循環通路により複数回循
環して清浄化した後開閉弁50を経て液体通路29、開
閏弁51を経て液体物質の使用装置に排出するユースポ
イントU.Pに供給される。In this way, the liquid substance is transferred between the liquid containers 1 and 2 into the liquid i! a
, after being circulated and cleaned several times through the first liquid idle circulation passage via the means 4, a, the use point U. Supplied to P.
ここに液体輸送用気体による液体圧入手段に加えて液体
通路24の該液体容器出口側にボンブを配設して輸送し
てもよい。In addition to the liquid pressurization means using gas for transporting the liquid, a bomb may be disposed on the liquid container outlet side of the liquid passage 24 for transportation.
一方、ユースポイントU.PにJ5いて液体物質の使用
装置への利用が中断、あるいは一時的に停止された場合
には、液体物質は前記の返送手段により、該液体容器群
1ないし2とユースポイントU.Pの間で循環される。On the other hand, use point U. If the use of the liquid substance in the device is interrupted or temporarily stopped at J5, the liquid substance is transferred to the liquid container group 1 or 2 and the use point U.P by the above-mentioned return means. It is circulated between P.
この返送手段における液体濾過手段5の配設位置は該液
体容器のできるだけ近くとするのがよい。The liquid filtering means 5 in this return means is preferably arranged as close as possible to the liquid container.
本発明5A置は、液体物質内に不純物が混入しないよう
に、ないし混入の可能性があっても、その可能性を極力
抑制した上で濾過手段により清浄度を保持できるJ:う
になっている。従って、本発明が大型の液体供給装置に
実施できるとともに、小型の可搬式装置に適用して液体
物質の清浄度管理を行なうことが望まれる。The device 5A of the present invention is designed to prevent impurities from being mixed into the liquid substance, or even if there is a possibility of mixing, the cleanliness can be maintained by the filtration means while suppressing the possibility as much as possible. . Therefore, it is desirable that the present invention can be implemented in a large-sized liquid supply device, and can also be applied to a small-sized portable device to manage the cleanliness of liquid substances.
本発明が小型の可搬弐B置に実施ずる場合には液体容器
の収納場所をクリーン度i.ooo〜100程度のクリ
ーンベンチ内に設置して、該容器の配管着説場所を清浄
管理した上で、新規充填された液体容器と交換寸る。こ
の管理によって、配管接続箇所から不純物が新たに侵入
しないようにする。When the present invention is implemented in a small portable location, the storage location for the liquid container is kept at a cleanliness level of i. The container is installed in a clean bench of about 100~100 mm, and the piping entry area of the container is cleaned and managed, and then replaced with a newly filled liquid container. This control prevents new impurities from entering through the piping connections.
第1図に示す本発明の液体濾過供給装置において液体容
器はクリーンベンチに収納して、搬入に伴う汚染を防止
すべく清浄手段によって清浄化して用いられる。In the liquid filtration and supply apparatus of the present invention shown in FIG. 1, the liquid container is stored in a clean bench and cleaned by a cleaning means to prevent contamination during transport.
又、液体容器自体は、可搬式のものが一般に使用され、
液体物質が充填された液体容器と適官交換できるように
なっている。In addition, the liquid container itself is generally portable,
It can be exchanged with a liquid container filled with a liquid substance by a competent official.
上記したように、本発明の液体一過供給装置は、液体容
器間で液体濾過手段を経由する液体通路からなる液体循
環通路と、液体容器とユースポイントとの間で液体社過
手段を経由する返送手段とを備えているため、液体循環
通路により液体物質自体の清浄化が十分に行なわれると
共に、ユースポイントからの液体物質の供給が中断又は
停止されても液体容器とユースポイン]一との間で液体
物質が循環されているから、配管中に液体物質が停滞さ
れず、したがって、停滞に伴って起る配管の内壁に付着
した@間の汚染物質は、常に返送手段中の液体濾過手段
に捕捉され、液体物質の汚染が防止でき、常時ダストフ
リーの状態で供給することができる。As described above, the liquid temporary supply device of the present invention includes a liquid circulation path consisting of a liquid passage that passes through a liquid filtering means between liquid containers, and a liquid circulation path that passes through a liquid filtering means between the liquid container and a point of use. Since the liquid circulation passage is equipped with a return means, the liquid substance itself is sufficiently cleaned, and even if the supply of the liquid substance from the use point is interrupted or stopped, the liquid container and the use point are Since the liquid substance is circulated between the pipes, the liquid substance is not stagnated in the pipe, and therefore, the contaminants that adhere to the inner wall of the pipe due to stagnation are always removed from the liquid filtration means in the return means. This prevents contamination of the liquid substance and allows it to be supplied in a dust-free state at all times.
又、液体容器は、移動可能な状態となっているから容器
の取換が容易であり、しかも、液体容器はクリーンベン
チ内に収納されているから容器の搬出人に際して十分な
清浄が達成ざれる。In addition, since the liquid container is movable, it is easy to replace the container, and since the liquid container is stored in a clean bench, sufficient cleanliness can be achieved when the container is taken out. .
第1図は本発明に係る液体濾過供給装置における液体容
器を収納するクリーンベンチの外観斜視図を示し、第2
図は本発明に係る液体濾過供給装置の配管図を承り。
A・・・クリーンベンチ本体、Al.A2・・・液体容
器収納部、△3・・・空気清浄化手段、1.2・・・液
体容器、3・・・気体濾過手段、4.5・・・液体濾過
手段、6・・・減圧弁、11,12,13.14.15
・・・気体通路、16・・・気体排出通路、20.21
,22,23.24,25.26.27.28.29.
30・・・液体通路、41,42,43,44,45.
46a,46b,47a,47b,48.,49,50
.51.52・・・開閉弁。FIG. 1 shows an external perspective view of a clean bench that houses a liquid container in a liquid filtration and supply device according to the present invention, and FIG.
The figure shows a piping diagram of a liquid filtration and supply device according to the present invention. A...Clean bench body, Al. A2...Liquid container storage section, △3...Air cleaning means, 1.2...Liquid container, 3...Gas filtration means, 4.5...Liquid filtration means, 6... Pressure reducing valve, 11, 12, 13.14.15
... Gas passage, 16... Gas discharge passage, 20.21
, 22, 23.24, 25.26.27.28.29.
30...Liquid passage, 41, 42, 43, 44, 45.
46a, 46b, 47a, 47b, 48. ,49,50
.. 51.52...Opening/closing valve.
Claims (1)
、液体容器群よりユースポイントへ濾過手段を有する液
体通路を介して、清浄液として供給し得る濾過供給装置
であつて、該ユースポイント直前より、該液体容器群と
の間に開閉弁と濾過手段とを有する返送手段を設けたこ
とを特徴とする微細ダストフリー形液体濾過供給装置。 2)液体容器が移動可能な容器であることを特徴とする
特許請求の範囲第1項記載の微細ダストフリー形液体濾
過供給装置。 3)液体容器をクリーンベンチ内に収納して配設するこ
とを特徴とする特許請求の範囲第1項および第2項記載
の微細ダストフリー形液体濾過供給装置。[Scope of Claims] 1) A filtration supply device capable of supplying a liquid substance containing fine fixed particles as impurities from a group of liquid containers to a point of use as a cleaning liquid through a liquid passage having a filtration means. A fine dust-free type liquid filtration and supply device, characterized in that a return means having an on-off valve and a filtration means is provided between the liquid container group and the liquid container group immediately before the point of use. 2) The fine dust-free liquid filtration and supply device according to claim 1, wherein the liquid container is a movable container. 3) The fine dust-free type liquid filtration and supply device according to claims 1 and 2, characterized in that the liquid container is housed and disposed within a clean bench.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61144166A JPS631411A (en) | 1986-06-20 | 1986-06-20 | Fine dust-free type liquid filtering and feeding device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61144166A JPS631411A (en) | 1986-06-20 | 1986-06-20 | Fine dust-free type liquid filtering and feeding device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS631411A true JPS631411A (en) | 1988-01-06 |
Family
ID=15355733
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61144166A Pending JPS631411A (en) | 1986-06-20 | 1986-06-20 | Fine dust-free type liquid filtering and feeding device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS631411A (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS614587A (en) * | 1984-06-15 | 1986-01-10 | Toshiba Corp | Demineralized water supply system and its method |
-
1986
- 1986-06-20 JP JP61144166A patent/JPS631411A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS614587A (en) * | 1984-06-15 | 1986-01-10 | Toshiba Corp | Demineralized water supply system and its method |
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