JPH10273193A - Large-sized container for transport of high purity chemical - Google Patents
Large-sized container for transport of high purity chemicalInfo
- Publication number
- JPH10273193A JPH10273193A JP9080523A JP8052397A JPH10273193A JP H10273193 A JPH10273193 A JP H10273193A JP 9080523 A JP9080523 A JP 9080523A JP 8052397 A JP8052397 A JP 8052397A JP H10273193 A JPH10273193 A JP H10273193A
- Authority
- JP
- Japan
- Prior art keywords
- container
- filter
- chemical
- piping
- chemical solution
- 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
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、半導体製造分野に
使用される電子工業用薬液の輸送用大型容器に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a large container for transporting chemicals for the electronics industry used in the semiconductor manufacturing field.
【0002】[0002]
【従来の技術】電子工業分野では半導体や液晶表示装置
の製造に当たって種々の高純度薬液が使用されている。
例えば、高純度過酸化水素水、高純度アンモニア水、高
純度テトラメチルアンモニウムハイドロオキサイド水溶
液、高純度硫酸、高純度フッ酸等である。これらの薬液
中に微量の不純物や微粒子が存在すると半導体素子や液
晶表示装置の素子特性に悪影響を与えるため、薬液は高
純度品である必要がある。要求される純度は例えば全金
属が1ppb以下、0.2μm以上の大きさの異物、す
なわちパーティクルが100個/ml以下等極めて高純
度である。このため、容器材質からの不純物溶出やパー
ティクル発生は厳密に管理しなければならない。2. Description of the Related Art In the field of the electronics industry, various high-purity chemicals are used for manufacturing semiconductors and liquid crystal display devices.
For example, high-purity hydrogen peroxide solution, high-purity ammonia water, high-purity tetramethylammonium hydroxide aqueous solution, high-purity sulfuric acid, high-purity hydrofluoric acid, and the like. The presence of a trace amount of impurities or fine particles in these chemicals adversely affects the device characteristics of semiconductor elements and liquid crystal display devices, and therefore, the chemicals must be of high purity. The purity required is extremely high, for example, the total metal is 1 ppb or less, and foreign matter having a size of 0.2 μm or more, that is, 100 particles / ml or less. For this reason, elution of impurities and generation of particles from the material of the container must be strictly controlled.
【0003】さて、一般に大量の薬液を輸送するには容
量数百kg以上のコンテナやタンクローリー等が用いら
れる。このような容器を用いた場合、容器からの金属等
の不純物溶出は少ないものの、パーティクル発生につい
ては許容できないほど多く発生する場合があり、問題と
なっている。パーティクルが仮に全て金属からなるとし
ても0.2μm以上のパーティクル100個/mlは金
属濃度としてサブpptにしか相当しない。よって、パ
ーティクルの管理は金属等の不純物溶出よりもはるかに
厳格に行なわなければならない。In general, containers and tank trucks having a capacity of several hundred kg or more are used for transporting a large amount of chemicals. When such a container is used, elution of impurities such as metals from the container is small, but particles may be generated in an unacceptably large amount, which is a problem. Even if all the particles are made of metal, 100 particles / ml of 0.2 μm or more correspond only to the sub-ppt as the metal concentration. Therefore, particle management must be performed much more strictly than elution of impurities such as metals.
【0004】薬液製造元で容器に薬液を充填しユースポ
イントまで輸送する場合、輸送による振動等で更に容器
からパーティクルが発生し、薬液への混入が助長され
る。また近年、海外での高純度薬液の使用が多くなり、
日本国内から当該国へ輸送する機会が多いが、輸送時
間、輸送距離が長くなればなるほど、容器からのパーテ
ィクル混入量は増加してしまう。このため、現状では高
純度薬液を輸送するために大型容器を用いた場合、清浄
に薬液を管理することは極めて難しかった。[0004] When a chemical solution manufacturer fills a container with a chemical solution and transports it to a use point, particles are further generated from the container due to vibration or the like due to the transportation, and mixing into the chemical solution is promoted. In recent years, the use of high-purity chemicals overseas has increased,
There are many opportunities to transport from Japan to the country, but the longer the transport time and transport distance, the greater the amount of particles mixed in from the container. For this reason, at present, when a large container is used to transport a high-purity chemical solution, it has been extremely difficult to cleanly manage the chemical solution.
【0005】[0005]
【発明が解決しようとする課題】本発明の目的は、高純
度薬液を充填した容器において、高純度薬液を使用する
際に清浄な薬液を提供できる輸送用大型容器に関する。SUMMARY OF THE INVENTION An object of the present invention is to provide a large container for transportation which can provide a clean chemical solution when a high-purity chemical solution is used in a container filled with the high-purity chemical solution.
【0006】[0006]
【課題を解決するための手段】本発明者らは鋭意努力の
結果、輸送時あるいは保管時に容器内の薬液をフィルタ
ーで循環濾過すれば、容器内の薬液を清浄に保持しうる
ことを見いだし本発明に到達した。Means for Solving the Problems As a result of intensive efforts, the present inventors have found that the chemical solution in the container can be kept clean by circulating and filtering the chemical solution in the container during transportation or storage. The invention has been reached.
【0007】即ち本発明は、容器本体1、フィルター
4、送液ポンプ3及び配管からなり、フィルター、送液
ポンプ及び配管が、容器内の薬液をフィルターで循環濾
過するよう配置されていることを特徴とする高純度薬液
輸送用大型容器に関するものである。That is, the present invention comprises a container body 1, a filter 4, a liquid feed pump 3 and a pipe, and the filter, the liquid feed pump and the pipe are arranged so as to circulate and filter the chemical in the container with the filter. The present invention relates to a large container for transporting a high-purity chemical solution.
【0008】[0008]
【発明の実施の形態】本発明を図1により詳細に説明す
る。容器1には配管2、送液ポンプ3,フィルター4が
接続されている。さらにフィルター4からの流出口には
容器1に戻るように配管5が接続されている。必要に応
じて各場所に開閉バルブを設けても良い。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in detail with reference to FIG. The vessel 1 is connected with a pipe 2, a liquid feed pump 3, and a filter 4. Further, a pipe 5 is connected to the outlet from the filter 4 so as to return to the container 1. An on-off valve may be provided at each location as needed.
【0009】このような形態で必要に応じ送液ポンプを
駆動することにより大型容器内の高純度薬液は常に清浄
に保つことができる。濾過を行なう回数、期間に制限は
ない。すなわち、大型容器を輸送中あるいは放置中、連
続して濾過を行なっても良いし、断続的に行なっても良
い。さらには高純度薬液を使用するにあたり、容器から
抜き出す直前に濾過を行なっても良い。By driving the liquid feed pump in such a form as required, the high-purity chemical in the large container can always be kept clean. There is no limitation on the number of times of filtration and the period. That is, filtration may be performed continuously or intermittently while the large container is being transported or left. Further, when using a high-purity chemical solution, filtration may be performed immediately before extracting from the container.
【0010】ここで、配管2、5のタンクへの接続位置
に制限はない。但し、配管2はタンク内の薬液液面よ
り、下部に設置しなければならないし、配管5も無用な
気泡発生を抑えるため薬液液面より下部に設置すること
が望ましい。Here, there is no limitation on the connection positions of the pipes 2 and 5 to the tank. However, the pipe 2 must be provided below the surface of the chemical solution in the tank, and the pipe 5 is also preferably provided below the surface of the chemical solution in order to suppress generation of unnecessary bubbles.
【0011】さらに、フィルター4からの流出口と容器
1に戻る配管にバルブ6、分岐配管7を設けてもよい。
この場合、分岐配管7は容器から薬液を抜き出す際用い
ることができる。この時、送液ポンプ3を稼働させるこ
とで容器内の薬液をフィルター4,分岐配管7を通し、
抜き出しても良いし、容器内を高純度窒素等の圧送ガス
により加圧することで薬液を抜き出しても良い。さらに
は系外のポンプを分岐配管7の先に設置し、抜き出して
も良い。Further, a valve 6 and a branch pipe 7 may be provided at the outlet from the filter 4 and the pipe returning to the container 1.
In this case, the branch pipe 7 can be used when extracting the chemical from the container. At this time, the chemical solution in the container is passed through the filter 4 and the branch pipe 7 by operating the liquid sending pump 3,
The chemical solution may be extracted by pressurizing the inside of the container with a pressure-feeding gas such as high-purity nitrogen or the like. Further, a pump outside the system may be installed at the end of the branch pipe 7 and extracted.
【0012】単位時間当たりの濾過流量にも制限はな
い。但し、循環濾過を行なう場合は濾過にかける時間を
踏まえ、その時間内で大型容器内の薬液が十分清浄にな
るだけの流量で濾過する。[0012] There is no limitation on the filtration flow rate per unit time. However, in the case of performing circulating filtration, the filtration is performed at a flow rate sufficient to sufficiently clean the chemical solution in the large container within the time, taking into account the time required for the filtration.
【0013】大型容器、フィルター、配管、送液ポンプ
の材質に制限はない。しかしながら、それらの接液部が
高純度薬液に接触しても不純物溶出が極めて少ない材質
を用いることが必要である。例としてポリテトラフルオ
ロエチレン(PTFE)、ポリクロロトリフルオロエチ
レン(PCTFE)、テトラフルオロエチレン・パーフ
ルオロアルキルビニルエーテル共重合体(PFA)など
のフッ素樹脂が好適に使用される。また、これらの樹脂
をライニングしたものでもよい。There are no restrictions on the materials of the large container, filter, piping, and liquid feed pump. However, it is necessary to use a material that has extremely little elution of impurities even when those liquid contact portions come into contact with a high-purity chemical solution. For example, fluorine resins such as polytetrafluoroethylene (PTFE), polychlorotrifluoroethylene (PCTFE), and tetrafluoroethylene / perfluoroalkylvinyl ether copolymer (PFA) are preferably used. In addition, those obtained by lining these resins may be used.
【0014】送液ポンプの方式に制限はない。いわゆる
ベローズポンプ、あるいは渦巻ポンプなどが挙げられ
る。但し、不純物溶出、パーティクル発生が少ないこと
からベローズ方式が好適に使用される。There is no limitation on the system of the liquid sending pump. A so-called bellows pump or a centrifugal pump may be used. However, since the elution of impurities and the generation of particles are small, the bellows method is preferably used.
【0015】フィルターは平均孔径0.1μm以下のも
のが使用される。フィルターの孔径を規定するにあたっ
ては、ポリスチレンラテックス標準粒子による方法を用
いている。ポリスチレンラテックス標準粒子としては、
例えばダウケミカル(株)や日本合成ゴム(株)製のも
のが使用される。この方法は平均直径の異なるポリスチ
レンラテックス標準粒子を分散した超純水を該フィルタ
ーにそれぞれ通過させ、その通過前後の超純水について
UV光による濁度測定を行い、通過を阻止される粒子の
割合を求める。通過試験では複数の異なる平均直径を有
する標準粒子を順次通過させる。通過阻止率が初めて7
0%を越えた時点の平均直径をそのフィルターの平均孔
径とする。A filter having an average pore size of 0.1 μm or less is used. In defining the pore size of the filter, a method using polystyrene latex standard particles is used. As polystyrene latex standard particles,
For example, those manufactured by Dow Chemical Co., Ltd. and Nippon Synthetic Rubber Co., Ltd. are used. In this method, ultrapure water in which polystyrene latex standard particles having different average diameters are dispersed is passed through the filters, and the turbidity of the ultrapure water before and after the passage is measured by UV light. Ask for. In the passage test, a plurality of standard particles having different average diameters are sequentially passed. 7 for the first time
The average diameter at the time of exceeding 0% is defined as the average pore size of the filter.
【0016】フィルターの形状にも制限はない。すなわ
ち、平膜、プリーツ型、スパイラル型、中空糸型など、
どのような形状であっても良い。さらに、フィルターに
関しては孔径の異なる複数のフィルターを平均孔径の大
きい順に直列に並べ段階的に薬液中のパーティクルを除
去しても良い。There is no limitation on the shape of the filter. That is, flat membrane, pleated type, spiral type, hollow fiber type, etc.
Any shape may be used. Further, regarding the filters, a plurality of filters having different pore diameters may be arranged in series in ascending order of the average pore diameter to remove particles in the chemical solution step by step.
【0017】[0017]
【実施例】以下に実施例を挙げて本発明を説明するが、
本発明はこれらの実施例により何ら制限されるものでは
ない。なお、パーティクル量の測定には、レーザー光散
乱を利用する方式によるリオン製KL−20を用いた。EXAMPLES The present invention will be described below with reference to examples.
The present invention is not limited by these examples. In addition, KL-20 manufactured by Rion by a method utilizing laser light scattering was used for measuring the amount of particles.
【0018】実施例 容器容量9トンの図1に示すような輸送用大型容器に3
1重量%高純度過酸化水素水を8トン充填した。充填時
の過酸化水素水中のパーティクル数は0.2μm以上で
5個/mlであった。なお、フィルターは平均孔径0.
1μmのフィルターであり、またポンプはベローズ式の
ポンプであった。また、容器を含む全ての過酸化水素水
の接液部はPFAであった。EXAMPLE A large container for transportation as shown in FIG.
Eight tons of 1% by weight high purity hydrogen peroxide solution was filled. The number of particles in the hydrogen peroxide solution at the time of filling was 5 μm / ml at 0.2 μm or more. The filter has an average pore size of 0.
The filter was a 1 μm filter, and the pump was a bellows type pump. In addition, all the liquid contact portions of the hydrogen peroxide solution including the container were PFA.
【0019】この容器を3日かけて距離2000kmの
輸送に供した。輸送中常にポンプを起動させ、循環濾過
を継続した。輸送後大型容器から過酸化水素水を抜き出
し、その中の0.2μm以上のパーティクル数を測定し
たところ10個/mlであった。The container was transported over a distance of 2000 km over a period of 3 days. During the transportation, the pump was always started, and the circulation filtration was continued. After transport, the hydrogen peroxide solution was extracted from the large container, and the number of particles having a particle size of 0.2 μm or more was measured. As a result, it was 10 particles / ml.
【0020】比較例 図1においてフィルター4やポンプ3、配管2等の本発
明による装置が設置されていない大型容器を用い、循環
濾過を行なわなかった以外は実施例と同様に行なった。
輸送後における過酸化水素水中の0.2μm以上のパー
ティクル数は300個/mlであった。COMPARATIVE EXAMPLE The same operation as in the example was carried out except that a large vessel in which the apparatus according to the present invention such as the filter 4, the pump 3, and the pipe 2 was not installed in FIG.
The number of particles having a particle size of 0.2 μm or more in the hydrogen peroxide solution after transportation was 300 / ml.
【0021】[0021]
【発明の効果】本発明の大型容器を用いることで、高純
度薬液を保存、輸送する際の容器に由来するパーティク
ル発生の影響がなく、清浄な薬液を提供することができ
る。As described above, by using the large container of the present invention, a clean chemical solution can be provided without being affected by particles generated from the container when storing and transporting a high-purity chemical solution.
【図1】本発明の高純度薬液輸送用大型容器FIG. 1 is a large container for transporting a high-purity chemical solution of the present invention.
1:容器本体 2:配管 3:送液ポンプ 4:フィルター 5:配管 6:バルブ 7:分岐配管 1: Container body 2: Piping 3: Liquid pump 4: Filter 5: Piping 6: Valve 7: Branch piping
Claims (2)
3及び配管からなり、フィルター、送液ポンプ及び配管
が、容器内の薬液をフィルターで循環濾過するよう配置
されていることを特徴とする高純度薬液輸送用大型容
器。1. A container comprising a container body 1, a filter 4, a liquid sending pump 3 and a pipe, wherein the filter, the liquid sending pump and the pipe are arranged so as to circulate and filter the chemical solution in the container with the filter. Large container for transporting high-purity chemicals.
であることを特徴とする請求項1記載の高純度薬液輸送
用大型容器。2. The large container for transporting a high-purity chemical according to claim 1, wherein the filter has an average pore size of 0.1 μm or less.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9080523A JPH10273193A (en) | 1997-03-31 | 1997-03-31 | Large-sized container for transport of high purity chemical |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9080523A JPH10273193A (en) | 1997-03-31 | 1997-03-31 | Large-sized container for transport of high purity chemical |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH10273193A true JPH10273193A (en) | 1998-10-13 |
Family
ID=13720685
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9080523A Pending JPH10273193A (en) | 1997-03-31 | 1997-03-31 | Large-sized container for transport of high purity chemical |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH10273193A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004361132A (en) * | 2003-06-02 | 2004-12-24 | Mitsubishi Gas Chem Co Inc | Lining exfoliation inspection method |
JP2005157361A (en) * | 2003-11-21 | 2005-06-16 | Merck Patent Gmbh | Method and system for packing, transporting, storing and collecting liquid crystal |
JP2015147606A (en) * | 2014-02-07 | 2015-08-20 | 株式会社Ihi | Ammonia storage equipment |
JP2015534256A (en) * | 2012-08-09 | 2015-11-26 | インテグリス・インコーポレーテッド | Ultra-high purity storage and dispensing of liquid reagents |
JP2021097237A (en) * | 2016-03-31 | 2021-06-24 | 富士フイルム株式会社 | Storage container containing processing liquid for semiconductor manufacturing |
-
1997
- 1997-03-31 JP JP9080523A patent/JPH10273193A/en active Pending
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004361132A (en) * | 2003-06-02 | 2004-12-24 | Mitsubishi Gas Chem Co Inc | Lining exfoliation inspection method |
JP2005157361A (en) * | 2003-11-21 | 2005-06-16 | Merck Patent Gmbh | Method and system for packing, transporting, storing and collecting liquid crystal |
JP2015534256A (en) * | 2012-08-09 | 2015-11-26 | インテグリス・インコーポレーテッド | Ultra-high purity storage and dispensing of liquid reagents |
JP2015147606A (en) * | 2014-02-07 | 2015-08-20 | 株式会社Ihi | Ammonia storage equipment |
JP2021097237A (en) * | 2016-03-31 | 2021-06-24 | 富士フイルム株式会社 | Storage container containing processing liquid for semiconductor manufacturing |
US11693321B2 (en) | 2016-03-31 | 2023-07-04 | Fujifilm Corporation | Treatment liquid for manufacturing semiconductor, storage container storing treatment liquid for manufacturing semiconductor, pattern forming method, and method of manufacturing electronic device |
TWI814345B (en) * | 2016-03-31 | 2023-09-01 | 日商富士軟片股份有限公司 | Treatment liquid for semiconductor manufacturing and pattern forming method |
US11892775B2 (en) | 2016-03-31 | 2024-02-06 | Fujifilm Corporation | Storage container storing treatment liquid for manufacturing semiconductor |
TWI847824B (en) * | 2016-03-31 | 2024-07-01 | 日商富士軟片股份有限公司 | Pattern forming method and method for manufacturing semiconductor device |
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