JPS627402A - Apparatus for making pure water - Google Patents
Apparatus for making pure waterInfo
- Publication number
- JPS627402A JPS627402A JP14589985A JP14589985A JPS627402A JP S627402 A JPS627402 A JP S627402A JP 14589985 A JP14589985 A JP 14589985A JP 14589985 A JP14589985 A JP 14589985A JP S627402 A JPS627402 A JP S627402A
- Authority
- JP
- Japan
- Prior art keywords
- pure water
- water
- evaporation
- cooler
- condensing
- 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
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の利用分野〕
本発明は純水製造装置に係り、特に気化透過膜を用いて
純水を得るのに好適な装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a pure water production device, and particularly to a device suitable for obtaining pure water using a vapor permeable membrane.
半導体を製造する電子工業、医薬品を製造する装架工業
等においては各種のイオンやコロイド物質、そして一般
細菌を除去した高純度の純水を必要としている。特に、
集積回路(1,C)や大規模集積回路(L、S、I)等
の精密な半導体装置を製造する場合にはその純水の純度
が直接製品の良否に関与するので、純度の高い純水の製
造が重要な課題となっている。The electronic industry, which manufactures semiconductors, and the mounting industry, which manufactures pharmaceuticals, require highly purified water from which various ions, colloidal substances, and general bacteria have been removed. especially,
When manufacturing precision semiconductor devices such as integrated circuits (1, C) and large-scale integrated circuits (L, S, I), the purity of the pure water directly affects the quality of the product. Water production has become an important issue.
従来の純水製造装置の系統を第2図について説明する。The system of a conventional pure water production apparatus will be explained with reference to FIG.
図において、純水の製造装置にi集沈澱1、濾過2、逆
浸透膜3、イオン交換樹脂塔4からなる一次純水系と、
プレフィルタ−5、ポリシャ6、紫外線殺菌灯7、限外
濾過膜8からなる二次純水系からなっている。原水A′
は一次純水系、二次純水系を経て純水Aになる。この種
の純水の製造装置では多数の要素機器からなっており、
大型の装置になり、設置面積が大となる問題がある。ま
た、要素機器が多いためメンテナンスコストが大となる
と共に、要素機器の後にタンクを設けて貯水するためタ
ンク内で細菌の発生等再汚染を生じ水質が低下する問題
があった。In the figure, the pure water production apparatus includes a primary pure water system consisting of a collection sedimentation 1, a filtration 2, a reverse osmosis membrane 3, and an ion exchange resin column 4,
It consists of a secondary pure water system consisting of a prefilter 5, a polisher 6, an ultraviolet germicidal lamp 7, and an ultrafiltration membrane 8. Raw water A'
becomes pure water A after passing through the primary pure water system and the secondary pure water system. This type of pure water production equipment consists of many elemental devices.
There is a problem that the device becomes large and requires a large installation area. Furthermore, since there are many component devices, maintenance costs are high, and since tanks are provided after the component devices to store water, there is a problem in that re-contamination such as the generation of bacteria occurs in the tank and the water quality deteriorates.
尚、この種の装置に関連するものには例えば特開昭57
−174189号がある。In addition, related to this type of device, for example, Japanese Patent Application Laid-open No. 57
There is No.-174189.
本発明の目的は要素機器が少なくて純度の高い純水を得
る純水製造装置を提供することにある。An object of the present invention is to provide a pure water production apparatus that uses fewer component devices and produces highly purified water.
〔発明の概要〕
本発明は気化透過膜によって蒸気部と凝縮部に区画され
る蒸発装置と凝縮部内に配置された原水冷却器と、この
冷却器からの原水を加熱蒸発する加熱器を介して蒸発装
置の蒸発部に送り込む送水ポンプと、凝縮部から純水を
導出する純水送出管とから構成し、純水を製造する要素
機器を少なくして装置の小型化を達成すると共に純度の
高い純水が得られるようにしたものである。[Summary of the Invention] The present invention comprises an evaporator that is divided into a vapor section and a condensing section by a vaporization permeable membrane, a raw water cooler disposed in the condensing section, and a heater that heats and evaporates the raw water from the cooler. Consisting of a water pump that sends water to the evaporation section of the evaporator and a pure water delivery pipe that brings out pure water from the condensing section, it reduces the number of elemental devices that produce pure water, making the device more compact and achieving high purity. This allows pure water to be obtained.
以下1本発明の一実施例を第1図について説明する。 An embodiment of the present invention will be described below with reference to FIG.
第1図は純水製造装置の系統図である。図において、1
0は蒸発装置であり、この蒸発装置10の内部は気化透
過膜11によって蒸発部10aと凝縮部10bに区画さ
れている。凝縮部10bには原水冷却器12が配置され
、この冷却器12を経た冷却水である原水は配管13を
通ってその一部が排水タンク14に排水される。配管工
3を流通する原水は送水ポンプ15の吸込側に導びかれ
加熱器16を通って蒸発装置10の蒸発部10aを経て
排水タンク17に排水される。原水は蒸発部10aで蒸
発し気化透過膜11を経て凝縮部10bに流入し原水冷
却器12によって冷却され凝縮し純水となり純水送出管
18より導出される。FIG. 1 is a system diagram of a pure water production apparatus. In the figure, 1
0 is an evaporator, and the inside of this evaporator 10 is divided by a vaporization permeable membrane 11 into an evaporator section 10a and a condensation section 10b. A raw water cooler 12 is disposed in the condensing section 10b, and the raw water, which is cooling water, that has passed through the cooler 12 passes through a pipe 13, and a part of it is drained into a drainage tank 14. The raw water flowing through the plumber 3 is led to the suction side of the water pump 15, passes through the heater 16, passes through the evaporator section 10a of the evaporator 10, and is drained into the drain tank 17. The raw water is evaporated in the evaporator 10a, passes through the vaporization permeable membrane 11, flows into the condenser 10b, is cooled by the raw water cooler 12, and condenses to become pure water, which is led out from the pure water delivery pipe 18.
このような工程によって一次純水系が構成されている。A primary pure water system is constituted by such a process.
この純水の導出には蒸発装置10の凝縮部10bに取付
けた窒素ガス等の不活性ガスを放出する不活性ガス導入
管19によって圧送される。純水送出管18より導出さ
れた純水は紫外線殺菌灯20を経て殺菌され、さらにポ
リシャ21で微量の金属イオンが除去され、限外濾過脱
装[22を通して残留懸濁固形物が除去される。この工
程によって二次純水系が構成されている。This pure water is brought out under pressure through an inert gas introduction pipe 19 that is attached to the condensing section 10b of the evaporator 10 and discharges an inert gas such as nitrogen gas. The pure water led out from the pure water delivery pipe 18 is sterilized by passing through an ultraviolet germicidal lamp 20, trace amounts of metal ions are removed by a polisher 21, and residual suspended solids are removed by passing through an ultrafiltration desorber [22]. . This process constitutes a secondary pure water system.
限外が過膜装置22を通して得られた純水はユースポイ
ント23に送られ純水の需要に供される。The purified water obtained through the ultrafilter membrane device 22 is sent to the use point 23 and is provided for the demand for pure water.
ユースポイント23において未使用の純水および限外濾
過膜装置22においての排水B、B’は送水ポンプ15
の吸込口に戻され再利用される。また、限外濾過膜装置
22に代えて他のファイナルフィルターを利用すること
も可能である。Unused pure water at the use point 23 and wastewater B and B' from the ultrafiltration membrane device 22 are supplied to the water pump 15.
is returned to the suction port and reused. Moreover, it is also possible to replace the ultrafiltration membrane device 22 with another final filter.
なお、上記蒸発装置10において気化透過膜11を透過
した蒸気は原水冷却器12によって冷却され凝縮し純水
となるが、気化透過膜11を透過しなかった原水は排水
となり、排水タンク17に導びかれる。この排水の溶解
物の溶解度は飽和溶解度を越えないようにする必要があ
る。これは溶解物が結晶となって析出し膜11に付着す
るのを防ぐためである。The vapor that has passed through the vaporization permeable membrane 11 in the evaporator 10 is cooled by the raw water cooler 12 and condensed to become pure water, but the raw water that has not passed through the vaporization membrane 11 becomes wastewater and is led to the drainage tank 17. I'm scared. It is necessary that the solubility of the dissolved substance in this wastewater does not exceed the saturated solubility. This is to prevent the melt from crystallizing and adhering to the precipitated film 11.
上記のように、従来、凝集沈澱、濾過、逆浸透膜、イオ
ン交換樹脂塔等の多数の要素機器からなっていた一次純
水系を蒸発装置に置換えることができ、純水製造装置の
小型化が達成できる。As mentioned above, the primary pure water system, which conventionally consisted of a large number of elemental devices such as coagulation sedimentation, filtration, reverse osmosis membranes, and ion exchange resin towers, can be replaced with an evaporator, making the pure water production equipment more compact. can be achieved.
以上説明したように、本発明によれば、−次純水系にお
ける多数の要素機器を蒸発装置に置換えることができる
ので、小型化が達成できるのはもちろん、原水を冷却水
として利用するようにしたから熱効率を向上できるとい
う効果がある。As explained above, according to the present invention, many elemental devices in a sub-pure water system can be replaced with evaporators, which not only makes it possible to achieve downsizing, but also allows raw water to be used as cooling water. This has the effect of improving thermal efficiency.
第1図は本発明の純水製造装置の系統図、第2図は従来
の純水製造装置の系統図である。
10・・・蒸発装置、10ε−・・・蒸発部、10b・
・・凝縮部、11・・・係化透過膜、12・・・原水冷
却器、15・・・送水ポンプ、1G・・・加熱器、18
・・純水送出管、19・・不活性ガス導入管、20・・
・紫外線殺菌灯。FIG. 1 is a system diagram of a pure water production apparatus according to the present invention, and FIG. 2 is a system diagram of a conventional pure water production apparatus. 10... Evaporation device, 10ε-... Evaporation section, 10b.
... Condensation section, 11 ... Permeable membrane, 12 ... Raw water cooler, 15 ... Water pump, 1G ... Heater, 18
...Pure water delivery pipe, 19...Inert gas introduction pipe, 20...
・Ultraviolet germicidal lamp.
Claims (1)
発装置と、前記凝縮部内に配置された原水冷却器と、該
冷却器からの原水を加熱蒸発する加熱器を介して前記蒸
発装置の蒸発部に送り込む送水ポンプと、凝縮部から純
水を導出する純水送出管とからなり、前記蒸発部に導び
かれた蒸気を前記気化透過膜を透過させて前記凝縮部に
導びき、該凝縮部の蒸気を前記原水冷却器によつて凝縮
させて純水を得ることを特徴とする純水製造装置。 2、特許請求の範囲第1項において、前記蒸発装置の凝
縮部に不活性ガス導入管を取付け、該不活性ガスによつ
て純水を圧送するようにしたことを特徴とする純水製造
装置。 3、特許請求の範囲第1項において、前記蒸発装置の凝
縮部より導出された純水は紫外線殺菌灯、ポリシヤ、限
外ろ過膜によつて純度を高めてユースポイントに導びく
ようにしたことを特徴とする純水製造装置。 4、特許請求の範囲第3項において、ユースポイントに
おいて未使用の純水は前記送水ポンプの吸込口に戻すよ
うにしたことを特徴とする純水製造装置。[Claims] 1. An evaporator divided into a vapor section and a condensing section by a vaporization permeable membrane, a raw water cooler disposed in the condensing section, and a heating device for heating and evaporating the raw water from the cooler. It consists of a water pump that sends water to the evaporation section of the evaporation device through a container, and a pure water delivery pipe that brings out pure water from the condensation section, and the vapor led to the evaporation section is passed through the vaporization permeable membrane. A pure water production apparatus characterized in that pure water is obtained by introducing the steam into the condensing section and condensing the steam in the condensing section by the raw water cooler. 2. The pure water production apparatus according to claim 1, characterized in that an inert gas introduction pipe is attached to the condensing part of the evaporator, and the pure water is pumped by the inert gas. . 3. In claim 1, the pure water drawn out from the condensing section of the evaporator is purified by an ultraviolet germicidal lamp, a polisher, and an ultrafiltration membrane, and then guided to the point of use. A pure water production device featuring: 4. The pure water production apparatus according to claim 3, characterized in that unused pure water at the point of use is returned to the suction port of the water pump.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14589985A JPS627402A (en) | 1985-07-04 | 1985-07-04 | Apparatus for making pure water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14589985A JPS627402A (en) | 1985-07-04 | 1985-07-04 | Apparatus for making pure water |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS627402A true JPS627402A (en) | 1987-01-14 |
Family
ID=15395630
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14589985A Pending JPS627402A (en) | 1985-07-04 | 1985-07-04 | Apparatus for making pure water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS627402A (en) |
-
1985
- 1985-07-04 JP JP14589985A patent/JPS627402A/en active Pending
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