JPH08173961A - Warm ultra pure water producing apparatus - Google Patents

Warm ultra pure water producing apparatus

Info

Publication number
JPH08173961A
JPH08173961A JP32053294A JP32053294A JPH08173961A JP H08173961 A JPH08173961 A JP H08173961A JP 32053294 A JP32053294 A JP 32053294A JP 32053294 A JP32053294 A JP 32053294A JP H08173961 A JPH08173961 A JP H08173961A
Authority
JP
Japan
Prior art keywords
water
membrane
raw water
pure water
metal
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
JP32053294A
Other languages
Japanese (ja)
Inventor
Yoshiaki Sakuraba
義昭 桜庭
Katsu Iijima
克 飯島
Kazuhiko Sonomoto
和彦 園元
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.)
Proterial Ltd
Original Assignee
Hitachi Metals 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 Hitachi Metals Ltd filed Critical Hitachi Metals Ltd
Priority to JP32053294A priority Critical patent/JPH08173961A/en
Publication of JPH08173961A publication Critical patent/JPH08173961A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE: To provide pure water with high purity and at the same time extend the life of a filtration membrane by producing a high precision filtration membrane and an ultrafilter membrane from metal films which are produced by forming a metal powder layer on a wire net, respectively. CONSTITUTION: A heating means 1 is installed in a container 2 to make raw water be warm water. The raw water made to be warm is filtered by a separating apparatus 3 with high precision filtration membrane and an ultrafilter membrane separating apparatus 4. Also, after the raw water is introduced into a reverse osmosis separating apparatus RO5 and an ion-exchange apparatus 6, the raw water is further introduced into a ultraviolet-ray sterilizing apparatus 7 and an ion-exchange apparatus 8 installed in series. In this case a metal membrane in which a porous layer is formed by applying a metal powder to the surface of a pressed wire net made of a stainless steel and sintering the resulting metal net is used as a filtration membrane of the separating apparatus 3 and the ultrafilter membrane separating apparatus 4. Consequently, pure water with high purity can be obtained and at the same time the life of the filtration membrance is extended.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、半導体製造工場等で使
用される温超純水の製造装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for producing hot ultrapure water used in semiconductor manufacturing factories and the like.

【0002】[0002]

【従来の技術】精密部品、例えば半導体を製造する工場
では、製品の洗浄のために超純水を使用している。この
超純水を製造する装置は、例えば、精密ろ過膜分離装置
および限外ろ過膜分離装置を含む前処理装置と、逆浸透
膜分離装置およびイオン交換装置を含む1次純水製造装
置と、紫外線殺菌装置とイオン交換装置を含む2次純水
製造装置から構成される。上記の超純水装置によれば、
市水、地下水または工業用水等の原水を前処理装置によ
りろ過して凝集物を分離し、次いでその透過水を1次純
水製造装置に通水してTOC(全有機体炭素)成分を除
去し、そして2次純水装置によりTOC成分を分解する
ことにより超純水を得ることができる。近年、半導体の
集積度の向上に伴ってより高い洗浄効果が要求され、こ
の要求満足するために70℃程度に加熱された超純水
(温超純水)を使用することが検討されている。
2. Description of the Related Art In a factory for manufacturing precision parts such as semiconductors, ultrapure water is used for cleaning products. An apparatus for producing this ultrapure water is, for example, a pretreatment apparatus including a microfiltration membrane separation apparatus and an ultrafiltration membrane separation apparatus, a primary pure water production apparatus including a reverse osmosis membrane separation apparatus and an ion exchange apparatus, It is composed of a secondary pure water production system including an ultraviolet sterilization system and an ion exchange system. According to the above ultrapure water device,
Raw water such as city water, groundwater or industrial water is filtered by a pretreatment device to separate agglomerates, and then the permeated water is passed through a primary pure water production device to remove TOC (total organic carbon) components. Then, ultrapure water can be obtained by decomposing the TOC component by the secondary pure water device. In recent years, a higher cleaning effect has been required as the degree of integration of semiconductors has improved, and in order to satisfy this requirement, the use of ultrapure water (warm ultrapure water) heated to about 70 ° C. has been studied.

【0003】[0003]

【発明が解決しようとする課題】しかし従来の超純水製
造装置により温超純水を製造する場合、次のような問題
がある。従来の超純水製造装置では、精密ろ過膜分離装
置および限外ろ過膜分離装置におけるろ過膜としてセル
ロース、ビニル系重合体又は芳香族系重合体等の有機重
合体で形成された樹脂膜を使用しているので、前述した
温度に加熱された原水を通すと、樹脂膜の一部が溶出し
て純水の純度が低下するおよび樹脂膜が熱により劣化し
て寿命が短くなるといった問題が生ずる。したがって本
発明の目的は、上述した従来技術の問題点を解消し、高
純度の純水を得ることができ且つろ過膜の寿命を長くす
ることができる温超純水製造装置を提供することであ
る。
However, when hot ultrapure water is produced by the conventional ultrapure water producing apparatus, there are the following problems. In a conventional ultrapure water production system, a resin membrane formed of an organic polymer such as cellulose, vinyl polymer or aromatic polymer is used as a filtration membrane in a microfiltration membrane separation device and an ultrafiltration membrane separation device. Therefore, when the raw water heated to the above-mentioned temperature is passed through, there arises a problem that a part of the resin film is eluted and the purity of the pure water is lowered, and the resin film is deteriorated by heat and its life is shortened. . Therefore, an object of the present invention is to solve the above-mentioned problems of the prior art, and to provide a hot ultrapure water production system capable of obtaining high-purity pure water and extending the life of the filtration membrane.

【0004】[0004]

【課題を解決するための手段】上記目的を達成するため
に、本発明においては、原水を温水化する加熱手段と、
温水化された原水をろ過する精密ろ過膜分離装置及び限
外ろ過膜分離装置を含む前処理装置と、逆浸透膜分離装
置およびイオン交換装置を含む1次純水製造装置と、紫
外線殺菌装置とイオン交換装置を含む2次純水製造装置
とを有し、前記精密ろ過膜分離装置と限外ろ過膜分離装
置は、圧下されたステンレス鋼製金網の表面に金属粉末
を塗布、焼結して得られた多孔質層を形成した金属膜を
有する、という技術的手段を採用した。
In order to achieve the above object, in the present invention, a heating means for heating raw water is provided, and
A pretreatment device including a microfiltration membrane separation device and an ultrafiltration membrane separation device for filtering warmed raw water, a primary pure water production device including a reverse osmosis membrane separation device and an ion exchange device, and an ultraviolet sterilizer A secondary pure water producing apparatus including an ion exchange apparatus, wherein the microfiltration membrane separation apparatus and the ultrafiltration membrane separation apparatus apply metal powder to the surface of a pressed stainless steel wire mesh and sinter it. The technical means of having the obtained metal film in which the porous layer was formed was adopted.

【0005】[0005]

【実施例】以下に本発明の実施例を図面に基づいて詳細
に説明する。図1に本発明の一実施に好適な温超純水製
造装置の一例を示す系統図である。図1に示す通り、原
水を温水化するためにヒータ等の加熱手段1を容器2に
設置する。温度23〜25℃の原水を容器2に導入し7
0℃程度に加熱し、温水化された原水を精密ろ過膜分離
装置(MF)3および限外ろ過膜分離装置(UF)4に
よりろ過する。続いて原水を逆浸透膜分離装置(RO)
5およびイオン交換装置6に通し、さらに紫外線殺菌装
置7とイオン交換装置8を直列に設置した中を通す。こ
こで、限外ろ過膜分離装置4までを前処理装置9とい
い、イオン交換装置6までを1次純水製造装置10とい
い、イオン交換装置8までを2次純水製造装置11とい
い、12は原水の導入配管を示す。
Embodiments of the present invention will be described below in detail with reference to the drawings. FIG. 1 is a system diagram showing an example of a hot ultrapure water producing apparatus suitable for carrying out the present invention. As shown in FIG. 1, a heating means 1 such as a heater is installed in a container 2 to heat the raw water. Introduce raw water at a temperature of 23 to 25 ° C into the container 7
The raw water which has been heated to about 0 ° C. and warmed is filtered by the microfiltration membrane separation device (MF) 3 and the ultrafiltration membrane separation device (UF) 4. Subsequently, the raw water is reverse osmosis membrane separation device (RO)
5 and the ion exchange device 6, and then the ultraviolet sterilization device 7 and the ion exchange device 8 are placed in series. Here, up to the ultrafiltration membrane separation device 4 is referred to as a pretreatment device 9, up to the ion exchange device 6 is referred to as a primary pure water production device 10, and up to the ion exchange device 8 is referred to as a secondary pure water production device 11. , 12 are the pipes for introducing raw water.

【0006】すなわち、市水、工水、地下水等は、まず
前処理装置9に導入されて容器2により洗浄効率を高め
るため加熱処理され、この処理水の凝集物や不純物を除
去するために精密ろ過膜分離装置3および限外ろ過膜分
離装置4に導入され、膜分離される。
That is, city water, industrial water, ground water, etc. are first introduced into the pretreatment device 9 and heat-treated in the container 2 to enhance the cleaning efficiency, and precision water is removed to remove aggregates and impurities of the treated water. It is introduced into the filtration membrane separation device 3 and the ultrafiltration membrane separation device 4 and subjected to membrane separation.

【0007】このような前処理装置9で処理された前処
理水は、次いで1次純水製造装置10において、逆浸透
膜分離装置5にてRO膜分離処理され、さらにイオン交
換装置6でイオン交換される。
The pretreated water treated by such a pretreatment device 9 is then subjected to RO membrane separation treatment by the reverse osmosis membrane separation device 5 in the primary pure water producing device 10 and further ionized by the ion exchange device 6. Will be exchanged.

【0008】さらに、1次純水製造装置10の処理水
は、2次純水製造装置11にて、紫外線殺菌装置7に導
入され、含有されるTOCがイオン化あるいは分解さ
れ、このうちイオン化された有機物質は後のイオン交換
装置8で除去され、温超純水が得られる。
Further, the treated water of the primary pure water producing apparatus 10 is introduced into the ultraviolet sterilizing apparatus 7 in the secondary pure water producing apparatus 11, the TOC contained therein is ionized or decomposed, and of these, it is ionized. The organic substance is removed by the ion exchange device 8 later, and hot ultrapure water is obtained.

【0009】ところで、超純水の洗浄能力を向上させる
ために前述した温度に加熱処理し、温超純水を各々の装
置内を通水させる場合、精密ろ過膜分離装置および限外
ろ過膜分離装置におけるろ過膜として通常はセルロー
ス、ビニル系重合体又は芳香族系重合体等の有機重合体
で形成された樹脂膜を使用しているので、樹脂膜の一部
が溶出して温超純水の純度が低下し且つ樹脂膜が熱によ
り劣化して寿命が短くなる問題が生じる。
By the way, in order to improve the cleaning performance of ultrapure water, when heat treatment is performed at the above-mentioned temperature and hot ultrapure water is passed through each device, in the microfiltration membrane separation device and the ultrafiltration membrane separation device. Since a resin membrane formed of an organic polymer such as cellulose, vinyl polymer or aromatic polymer is usually used as the filtration membrane, a part of the resin membrane is eluted and the purity of the hot ultrapure water is reduced. In addition, there is a problem that the resin film is deteriorated by heat and its life is shortened.

【0010】これに対して、本発明においては、圧下さ
れたステンレス鋼製金網の表面に金属粉末を塗布、焼結
して得られた多孔質層を形成した金属膜を精密ろ過膜分
離装置および限外ろ過膜分離装置におけるろ過膜に使用
する。
On the other hand, in the present invention, a metal membrane having a porous layer obtained by coating and sintering metal powder on the surface of a pressed stainless steel wire mesh is used as a microfiltration membrane separation device and Used for filtration membranes in ultrafiltration membrane separators.

【0011】金属膜として具体的には、 ステンレス鋼
製繊維を焼結したものや ステンレス鋼製金網あるいは
金網を圧下して得られる基板上に金属粉末層を形成し
たものなどを用い得る。これらの内では、機械的強度お
よびろ過性能の点から が好ましい。上記 の金属膜
は、例えば次のようにして作成すればよい。まず畳織り
またはむしろ織りの金網(ステンレス鋼またはTi等)
を圧延して(圧下率10〜50%)と粘結剤(ポリビニ
ルアルコール)を溶液(水)に分散させたスラリー(固
形分濃度50〜75wt%)を塗布し、乾燥および焼結
し、そして必要に応じ圧延(圧下率2〜10%)する。 金属膜の作成例 基 板:厚さ1.4mm、200メッシュの平畳織りの金
網(SUS316)を圧延(圧下率40%)→厚さ0.
24mm、網目径42μmの基板を作成。 粉末層:平均粒径9.5μmのSUS317L粉70部
とポリビニルアルコール1部と水29部を混合→基板上
に塗布(厚さ60μm)→乾燥→水素雰囲気中で105
0℃、1hr焼結→空孔径0.1〜0.3μm。
Specific examples of the metal film include a sintered product of stainless steel fibers, a stainless steel wire net, or a metal powder layer formed on a substrate obtained by pressing down a metal net. Among these, it is preferable in terms of mechanical strength and filtration performance. The above metal film may be formed, for example, as follows. First tatami or rather weave wire mesh (stainless steel or Ti etc.)
Is rolled (reduction rate 10 to 50%) and a slurry (solid content concentration 50 to 75 wt%) in which a binder (polyvinyl alcohol) is dispersed in a solution (water) is applied, dried and sintered, and Rolling (reduction ratio 2 to 10%) if necessary. Example of making metal film Base plate: Rolling a flat mesh weave wire mesh (SUS316) of 1.4 mm in thickness and 200 mesh (reduction ratio 40%) → thickness of 0.
Created a board with 24mm and 42μm mesh size. Powder layer: 70 parts of SUS317L powder having an average particle size of 9.5 μm, 1 part of polyvinyl alcohol and 29 parts of water are mixed → Coated on a substrate (thickness 60 μm) → Drying → 105 in a hydrogen atmosphere
0 ° C., 1 hr sintering → pore diameter 0.1-0.3 μm.

【0012】[0012]

【発明の効果】以上詳述した通り、本発明によれば、精
密ろ過膜分離装置および限外ろ過膜分離装置におけるろ
過膜に圧下されたステンレス鋼製金網の表面に金属粉末
を塗布、焼結して得られた多孔質層を形成した金属膜を
使用することにより、下記の効果を奏し得る。 (1)金属膜は耐熱性があるため、温超純水を精密ろ過
膜分離装置および限外ろ過膜分離装置に通水しても、熱
により金属膜から不純物が溶出することはなく、温超純
水の純度低下を防止できる。 (2)金属膜を精密ろ過膜分離装置および限外ろ過膜分
離装置に使用することにより、温超純水用ろ過膜の寿命
を長くすることができる。
As described above in detail, according to the present invention, the metal powder is applied to the surface of the stainless steel wire mesh which is pressed down by the filtration membrane in the microfiltration membrane separation device and the ultrafiltration membrane separation device and sintered. By using the metal film having the porous layer thus obtained, the following effects can be obtained. (1) Since the metal membrane has heat resistance, even if hot ultrapure water is passed through the microfiltration membrane separation device and the ultrafiltration membrane separation device, impurities do not elute from the metal film due to heat, and It is possible to prevent a decrease in purity. (2) By using the metal membrane in the microfiltration membrane separation device and the ultrafiltration membrane separation device, the life of the filtration membrane for hot ultrapure water can be extended.

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

【図1】本発明の温超純水の製造に好適な温超純水製造
装置の一実施例を示す系統図である。
FIG. 1 is a system diagram showing an embodiment of an apparatus for producing hot ultrapure water suitable for producing hot ultrapure water according to the present invention.

【符号の説明】[Explanation of symbols]

1…加熱手段、2…容器、3…精密ろ過膜分離装置、4
…限外ろ過膜分離装置 5…逆浸透膜分離装置、6…イオン交換装置、7…紫外
線殺菌装置、8…イオン交換装置、9…前処理装置、1
0…1次純水製造装置、11…2次純水製造装置、12
…導入配管
1 ... Heating means, 2 ... Container, 3 ... Microfiltration membrane separation device, 4
... ultrafiltration membrane separation device 5 ... reverse osmosis membrane separation device, 6 ... ion exchange device, 7 ... ultraviolet sterilization device, 8 ... ion exchange device, 9 ... pretreatment device, 1
0 ... Primary pure water producing apparatus, 11 ... Secondary pure water producing apparatus, 12
… Introduction piping

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 原水を温水化する加熱手段と、温水化さ
れた原水を精製する精密ろ過手段と、その透過水を精製
する限外ろ過手段と、その透過水を精製する逆浸透膜手
段と、その透過水を殺菌する殺菌手段とを有する温超純
水製造装置において、前記精密ろ過膜および前記限外ろ
過膜は、金網の上に金属粉末層を形成した金属膜からな
ることを特徴とする温超純水製造装置。
1. A heating means for warming raw water, a microfiltration means for purifying the warmed raw water, an ultrafiltration means for purifying the permeated water, and a reverse osmosis membrane means for purifying the permeated water. In the apparatus for producing hot ultrapure water having a sterilizing means for sterilizing the permeated water, the microfiltration membrane and the ultrafiltration membrane are characterized by comprising a metal membrane having a metal powder layer formed on a wire mesh. Water production equipment.
JP32053294A 1994-12-22 1994-12-22 Warm ultra pure water producing apparatus Pending JPH08173961A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32053294A JPH08173961A (en) 1994-12-22 1994-12-22 Warm ultra pure water producing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32053294A JPH08173961A (en) 1994-12-22 1994-12-22 Warm ultra pure water producing apparatus

Publications (1)

Publication Number Publication Date
JPH08173961A true JPH08173961A (en) 1996-07-09

Family

ID=18122491

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32053294A Pending JPH08173961A (en) 1994-12-22 1994-12-22 Warm ultra pure water producing apparatus

Country Status (1)

Country Link
JP (1) JPH08173961A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4525857B1 (en) * 2009-12-11 2010-08-18 住友電気工業株式会社 Pretreatment apparatus and pretreatment method for water treatment system
JP2010269235A (en) * 2009-05-20 2010-12-02 Nomura Micro Sci Co Ltd Method of producing refined water and apparatus for producing the refined water
WO2011016410A1 (en) * 2009-08-06 2011-02-10 住友電気工業株式会社 Water treatment device and water treatment method

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010269235A (en) * 2009-05-20 2010-12-02 Nomura Micro Sci Co Ltd Method of producing refined water and apparatus for producing the refined water
WO2011016410A1 (en) * 2009-08-06 2011-02-10 住友電気工業株式会社 Water treatment device and water treatment method
CN102471103A (en) * 2009-08-06 2012-05-23 住友电气工业株式会社 Water treatment device and water treatment method
JPWO2011016410A1 (en) * 2009-08-06 2013-01-10 住友電気工業株式会社 Water treatment apparatus and water treatment method
JP4525857B1 (en) * 2009-12-11 2010-08-18 住友電気工業株式会社 Pretreatment apparatus and pretreatment method for water treatment system
JP2011121007A (en) * 2009-12-11 2011-06-23 Sumitomo Electric Ind Ltd Pretreatment apparatus of water treatment system and pretreatment method

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