JPH1199388A - Reverse osmotic membrane treatment of raw water and device therefor - Google Patents
Reverse osmotic membrane treatment of raw water and device thereforInfo
- Publication number
- JPH1199388A JPH1199388A JP27936797A JP27936797A JPH1199388A JP H1199388 A JPH1199388 A JP H1199388A JP 27936797 A JP27936797 A JP 27936797A JP 27936797 A JP27936797 A JP 27936797A JP H1199388 A JPH1199388 A JP H1199388A
- Authority
- JP
- Japan
- Prior art keywords
- raw water
- water
- air
- storage tank
- dissolved
- 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.)
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- Separation Using Semi-Permeable Membranes (AREA)
- Degasification And Air Bubble Elimination (AREA)
- Physical Water Treatments (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は原水の逆浸透膜処理
方法及び処理装置に関わり、詳しくは電子部品の洗浄用
水、医薬品、食品、飲料等の製造用水等に使用される純
水の製造工程で行われている原水の逆浸透膜処理方法の
改良及びその為の装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for treating a reverse osmosis membrane of raw water, and more particularly, to a process for producing pure water used for washing water of electronic parts, water for producing pharmaceuticals, foods, beverages and the like. The present invention relates to an improvement of a reverse osmosis membrane treatment method of raw water and an apparatus therefor.
【0002】[0002]
【従来の技術】近年、電子部品洗浄用、医薬品、食品、
飲料製造用水として純水が多量使用されているが、その
純水を製造する工程では、市水、河川水、工業用水等を
原水とし、この原水を精密濾過装置、イオン交換装置、
逆浸透膜装置等を種々組み合わせた構成からなる純水製
造装置によって処理し純水としている。逆浸透膜装置は
原水中の塩類の除去の他、有機物、微粒子等も同時に除
去できるので、高純度の純水製造には必須の装置として
広く採用されている。ところが、逆浸透膜装置では原水
中に溶存する炭酸ガスがそのまま逆浸透膜を通過するた
め、処理水の純度が向上しないという問題点を有してい
る。2. Description of the Related Art In recent years, for cleaning electronic parts, pharmaceuticals, foods,
Although a large amount of pure water is used as drinking water, in the process of producing the pure water, city water, river water, industrial water, etc. are used as raw water, and the raw water is used as a microfiltration device, an ion exchange device,
Pure water is processed by a pure water production apparatus having a configuration in which various reverse osmosis membrane devices and the like are combined. A reverse osmosis membrane device is widely used as an essential device for producing high-purity pure water because it can simultaneously remove organic substances and fine particles in addition to removing salts in raw water. However, the reverse osmosis membrane apparatus has a problem that the purity of the treated water is not improved because the carbon dioxide dissolved in the raw water passes through the reverse osmosis membrane as it is.
【0003】そこで、従来は原水中の溶存炭酸ガスを除
去するために、原水を予め空気吹き込み式の脱炭酸塔、
あるいは脱気膜モジュールに通過させる方法、原水に窒
素ガスを接触させて溶存する炭酸ガスと置換させる方
法、更には原水にアルカリを注入してpH調整し、溶存
炭酸ガスを重炭酸イオンに変換する方法等によって処理
を行った後、その処理水を逆浸透膜装置に供給すること
により溶存炭酸ガスの膜透過を防止する方法が用いられ
ている。しかしながら、これらの処理のため逆浸透膜装
置の設備費やランニングコストが高くなり、経済性の点
で不利となっている。[0003] Therefore, conventionally, in order to remove dissolved carbon dioxide gas in raw water, the raw water is previously blown with air in a decarbonation tower,
Alternatively, a method of passing through a degassing membrane module, a method of contacting raw water with nitrogen gas to replace dissolved carbon dioxide, and further adjusting the pH by injecting alkali into raw water to convert dissolved carbon dioxide to bicarbonate ions. After the treatment by a method or the like, a method of preventing the permeation of dissolved carbon dioxide gas by supplying the treated water to a reverse osmosis membrane device is used. However, these treatments increase the equipment cost and running cost of the reverse osmosis membrane device, and are disadvantageous in terms of economy.
【0004】[0004]
【発明が解決しようとする課題】本発明は、従来の逆浸
透膜処理に於ける上記の欠点を解消するために、逆浸透
膜装置に供給される前の原水から、その中に溶存してい
る炭酸ガスを、極めて簡便な手段により効率良く除去
し、高純度の処理水が得られる逆浸透膜処理方法及びそ
れに適した装置を提供することを目的とする。SUMMARY OF THE INVENTION The present invention solves the above-mentioned drawbacks of the conventional reverse osmosis membrane treatment by dissolving raw water in raw water before being supplied to a reverse osmosis membrane apparatus. It is an object of the present invention to provide a reverse osmosis membrane treatment method capable of efficiently removing carbon dioxide gas by a very simple means and obtaining high-purity treated water, and an apparatus suitable for the method.
【0005】[0005]
【課題を解決するための手段】本発明は、高品質な純水
製造に適した高純度の逆浸透膜処理水を得るための原水
の処理方法及び装置を提供するものであり、本発明の第
一の要旨は、原水貯槽に貯留した原水を、逆浸透膜処理
する方法において、原水に空気を加圧溶解させ、空気を
溶存した原水を原水貯槽内の上部空間部に設けられた散
水手段により散水して原水貯槽に貯留し、次いで貯留し
た原水を逆浸透膜処理することよりなる原水の逆浸透膜
処理方法に存する。本発明の第二の要旨は、原水に空気
を加圧溶解させる気液混合装置、空気を溶存した原水の
散水手段を槽内上部に備えた原水貯槽及び原水貯槽に貯
留した原水の逆浸透膜処理装置から順次構成されてなる
原水の処理装置に存する。SUMMARY OF THE INVENTION The present invention provides a method and an apparatus for treating raw water for obtaining high-purity reverse osmosis membrane-treated water suitable for producing high-quality pure water. The first gist is that, in a method of treating raw water stored in a raw water storage tank with a reverse osmosis membrane, air is dissolved under pressure in the raw water, and the raw water in which the air is dissolved is provided in a water sprinkling means provided in an upper space in the raw water storage tank. And storing the raw water in a raw water storage tank, and then subjecting the stored raw water to reverse osmosis membrane treatment. A second gist of the present invention is to provide a gas-liquid mixing device for dissolving air in raw water under pressure, a raw water storage tank provided with a means for spraying raw water in which air is dissolved in the upper part of the tank, and a reverse osmosis membrane of raw water stored in the raw water storage tank. There is a raw water treatment device that is sequentially configured from the treatment device.
【0006】[0006]
【発明の実施の形態】以下に、本発明の実施の形態を図
面を用いて詳細に説明する。第1図は、本発明の実施態
様の一例を示すフローの説明図であり、図中、1は原水
供給管、2は気液混合器、3は原水貯槽、5は散水手
段、7は逆浸透膜モジュール、9は吸排気管を表す。本
発明で処理される原水としては、特に制限されず、井
水、河川水等の天然水、市水等が挙げられるが、これら
の原水は必要により凝集沈澱濾過、活性炭処理等の前処
理が施された後使用することもできる。更に、高純度の
純水製造を目的とする場合には、逆浸透膜処理した処理
水を原水として本発明方法に適用することも出来る。Embodiments of the present invention will be described below in detail with reference to the drawings. FIG. 1 is an explanatory diagram of a flow showing an example of an embodiment of the present invention. In the drawing, 1 is a raw water supply pipe, 2 is a gas-liquid mixer, 3 is a raw water storage tank, 5 is a water sprinkling means, and 7 is a reverse water supply means. The osmosis membrane module, 9 represents an intake and exhaust pipe. Raw water to be treated in the present invention is not particularly limited, and includes natural water such as well water and river water, city water and the like, and these raw waters may be subjected to pretreatment such as coagulation sedimentation filtration and activated carbon treatment as necessary. It can also be used after it has been applied. Further, when the purpose is to produce pure water of high purity, the treated water treated with a reverse osmosis membrane can be applied to the method of the present invention as raw water.
【0007】原水は、原水供給管1を通じて気液混合器
2に供給される。気液混合器2では空気導入管4より空
気が吸引導入され、原水中に空気が加圧溶解される。溶
解条件としては、気液混合器2の入口側圧力を出口側圧
力よりも若干高くなるように圧力差(0.1〜1.0kg/cm2G
あるいはそれ以上の圧力)を保持しつつ原水を流速2〜
5m/hで通過させながら空気を吸引導入する。通常、
その入口側圧力は0.5〜1.5kg/cm2G程度あるいはそれ以
上の圧力であり、その際の原水と空気との混合割合は体
積比で原水:空気=1:1を目途に運転される。また、
空気に付随して塵等の微細な汚染物質が導入されるのを
回避するため、空気導入管4には除塵フィルターの設備
を設けるのが効果的である。気液混合器2の形態として
はエゼクター、ラインミキサー、オリフィス式混合器等
があり、原水供給の配管途中で空気が導入され、気液混
合が可能なものであれば特に制限されるものではない。[0007] Raw water is supplied to a gas-liquid mixer 2 through a raw water supply pipe 1. In the gas-liquid mixer 2, air is sucked in from the air introduction pipe 4, and the air is dissolved under pressure in the raw water. The dissolution conditions are such that the pressure on the inlet side of the gas-liquid mixer 2 is slightly higher than the pressure on the outlet side (0.1 to 1.0 kg / cm 2 G).
Or higher pressure) while maintaining the flow rate of raw water
Air is sucked in while passing at 5 m / h. Normal,
The pressure on the inlet side is about 0.5 to 1.5 kg / cm 2 G or more, and the mixing ratio of raw water and air at that time is set so that raw water: air = 1: 1 in volume ratio. Also,
In order to avoid introduction of fine contaminants such as dust accompanying the air, it is effective to provide a dust filter device in the air introduction pipe 4. Examples of the form of the gas-liquid mixer 2 include an ejector, a line mixer, an orifice-type mixer, and the like. There is no particular limitation as long as air is introduced in the raw water supply pipe and gas-liquid mixing is possible. .
【0008】気液混合器で空気が加圧溶解された原水
は、原水貯槽3の内部の上部空間に設けられた散水手段
5により散水され、原水貯槽3に貯留される。散水手段
5としては、空気を溶存した原水が原水貯槽内の空間部
に広く均一に散水されるものであれば特に制限されず、
例えば、配管に孔径2〜6mmの小孔を複数個あけたも
の、あるいは散水ノズルを取り付けたもの等がある。散
水により原水中に溶存するガス、特に炭酸ガスを放出さ
せるが、出来るだけ多くの炭酸ガスを放出させるために
は、通常、小孔1個に対し原水の散水流速が2〜5m/
secとなるように原水を供給して行うのが好ましい。
また、散水の際には、原水貯槽3において、原水の散水
孔が存在する面と貯槽内の液面との間に少なくとも30
0〜500mmの空間部が確保されるように原水貯槽3
の液面を監視しながら散水するのが良い。散水孔と液面
が近接しすぎると原水からガスの放出効率が低下し、他
方、あまりに離れ過ぎると必要以上に原水貯槽中に空間
部が生じ、放出された溶存炭酸ガスの再吸収があり効率
的ではない。放出された溶存炭酸ガスは空気と共に吸排
気管9より排出される。The raw water in which the air is dissolved under pressure by the gas-liquid mixer is sprinkled by the water spraying means 5 provided in the upper space inside the raw water storage tank 3 and stored in the raw water storage tank 3. The watering means 5 is not particularly limited as long as the raw water in which air is dissolved is widely and uniformly watered in the space in the raw water storage tank.
For example, there is a pipe having a plurality of small holes having a hole diameter of 2 to 6 mm or a pipe provided with a watering nozzle. Spraying releases gas dissolved in raw water, particularly carbon dioxide gas. In order to release as much carbon dioxide gas as possible, the water flow rate of raw water per one small hole is usually 2 to 5 m / m2.
It is preferable to supply the raw water so as to be sec.
In addition, at the time of watering, at least 30 hours between the surface of the raw water storage tank 3 where the water supply holes are present and the liquid level in the storage tank.
Raw water storage tank 3 so that a space of 0 to 500 mm is secured
It is good to sprinkle water while monitoring the liquid level. If the water hole is too close to the liquid level, the efficiency of gas release from the raw water will decrease.On the other hand, if it is too far away, a space will be created in the raw water storage tank more than necessary, and the released dissolved carbon dioxide gas will be re-absorbed and the efficiency will increase. Not a target. The released dissolved carbon dioxide gas is discharged from the intake / exhaust pipe 9 together with the air.
【0009】このようにして、溶存炭酸ガスが放出除去
された原水は、そのまま原水貯槽3に貯留した後、高圧
ポンプ6を経由して逆浸透膜モジュール7に供給し、膜
処理することにより高純度の処理水が得られる。逆浸透
膜モジュールは、純水製造工程において使用されている
ものであれば良く、膜のエレメント構造としてはスパイ
ラル型、中空糸型、チューブラー型等がある。又、膜の
素材としては酢酸セルロース系、ポリアミド系、架橋ポ
リアミン系、架橋ポリエーテル系、スルホン化ポリスル
ホン等が知られている。本発明では、これらの素材から
なる膜で構成される市販の逆浸透膜モジュールを適宜選
択して使用すればよい。原水貯槽3から逆浸透膜モジュ
ールに供給される、炭酸ガスの除去された原水の通水条
件は、処理装置の規模、原水の水質によってもことなる
が、通常、流速1〜100m3/h,通水圧力0.5〜
4MPaの範囲で任意に選ばれる。The raw water from which the dissolved carbon dioxide gas has been released and removed in this way is stored in the raw water storage tank 3 as it is, and then supplied to the reverse osmosis membrane module 7 via the high-pressure pump 6 and subjected to membrane treatment. Purified treated water is obtained. The reverse osmosis membrane module only needs to be used in the pure water production process, and examples of the membrane element structure include a spiral type, a hollow fiber type, and a tubular type. Known materials for the membrane include cellulose acetate, polyamide, crosslinked polyamine, crosslinked polyether, and sulfonated polysulfone. In the present invention, a commercially available reverse osmosis membrane module composed of a membrane made of these materials may be appropriately selected and used. The flow conditions of the raw water from which the carbon dioxide gas is supplied from the raw water storage tank 3 to the reverse osmosis membrane module vary depending on the scale of the treatment apparatus and the quality of the raw water, but usually, the flow rate is 1 to 100 m 3 / h, Water passing pressure 0.5 ~
It is arbitrarily selected in the range of 4 MPa.
【0010】以上、気液混合器、散水手段が付設された
原水貯槽及び逆浸透膜装置から構成される装置ユニット
による原水の膜処理方法を説明したが、より高品質の純
水を製造する場合には、好ましい実施態様として二段階
の逆浸透膜処理がある。その場合には、上記装置ユニッ
トを二段組み合わせ、一段目の逆浸透膜処理で得られる
処理水を二段目の原水として使用して処理を行うことが
できる。また、場合によっては、一段目は通常の逆浸透
膜処理を行い、二段目でその透過水を原水として本発明
の逆浸透膜処理を行うことも出来る。この様に、多段階
で処理することにより一段目の逆浸透膜を透過した炭酸
ガスを二段目で効率良く除去することができるので、よ
り高純度の処理水を得ることができる。In the above, the membrane treatment method of the raw water by the apparatus unit composed of the raw water storage tank provided with the gas-liquid mixer, the water sprinkling means and the reverse osmosis membrane apparatus has been described. In a preferred embodiment, there is a two-stage reverse osmosis membrane treatment. In such a case, the above-described apparatus units can be combined in two stages, and the treatment can be performed using the treated water obtained in the first stage reverse osmosis membrane treatment as the second stage raw water. In some cases, a normal reverse osmosis membrane treatment can be performed in the first stage, and a reverse osmosis membrane treatment of the present invention can be performed in the second stage using the permeated water as raw water. As described above, by performing the treatment in multiple stages, the carbon dioxide gas that has passed through the first-stage reverse osmosis membrane can be efficiently removed in the second stage, so that higher-purity treated water can be obtained.
【0011】[0011]
【実施例】次に、本発明を実施例により更に詳細に説明
するが、本発明はその要旨を超えない限り、この実施例
に限定されるものではない。Next, the present invention will be described in more detail with reference to examples, but the present invention is not limited to these examples unless it exceeds the gist.
【0012】実施例1 第1図に示す本発明の逆浸透膜処理フローに従い、表−
1に示すような水質を有する市水を原水として逆浸透膜
処理を行った。原水を、まず気液混合器としての空気吹
き込み式エジェクターに、原水/吸入空気量=1/1
(体積比)の条件で供給し、原水中に空気を加圧溶解さ
せた。この空気を溶解した原水を、容量2m3の原水貯
槽に、該貯槽内の上部に設けられている水平配管に直径
4mmの複数個の小孔をあけた散水設備により散水させ
ながら貯留した。その際、散水流速は、2m/secで
あった。貯留した原水は逆浸透膜モジュール SU−7
10(商品名;東レ(株)製)に供給圧力12kg/c
m2G(1.2MPa),流量6.0m3/h,回収率6
0%で供給し、得られた処理水の電気伝導率及びpHを
測定した。その結果を表−1に示した。Example 1 According to the reverse osmosis membrane treatment flow of the present invention shown in FIG.
Reverse osmosis membrane treatment was performed using city water having the water quality as shown in FIG. 1 as raw water. Raw water is first supplied to an air-blowing ejector as a gas-liquid mixer, and the raw water / intake air amount is 1/1.
(Volume ratio), and air was pressurized and dissolved in raw water. The raw water in which the air was dissolved was stored in a raw water storage tank having a capacity of 2 m 3 while being sprinkled by a water spray facility having a plurality of small holes having a diameter of 4 mm in a horizontal pipe provided at an upper part of the storage tank. At that time, the watering speed was 2 m / sec. The stored raw water is reverse osmosis membrane module SU-7
10 (trade name; manufactured by Toray Industries, Inc.) with a supply pressure of 12 kg / c
m 2 G (1.2 MPa), flow rate 6.0 m 3 / h, recovery rate 6
The treated water was supplied at 0%, and the electric conductivity and pH of the obtained treated water were measured. The results are shown in Table 1.
【0013】比較例 比較のために、第1図の逆浸透膜処理フローにおいて、
気液混合器及び原水貯槽内の散水手段を取り除いた以外
は実施例1と同様な条件により、表−1の原水を逆浸透
膜処理を行った。その結果を表−1に示す。Comparative Example For comparison, in the reverse osmosis membrane treatment flow of FIG.
The raw water shown in Table 1 was subjected to reverse osmosis membrane treatment under the same conditions as in Example 1 except that the gas-liquid mixer and the watering means in the raw water storage tank were removed. Table 1 shows the results.
【0014】[0014]
【表1】 表−1 項 目 原 水 実施例1 比較例 電気伝導率 90〜130 3.4〜5 9.0〜10.0 (μS/cm、25℃) pH 6.0〜6.5 5.5〜6.5 4.0〜5.0[Table 1] Item Raw water Example 1 Comparative example Electric conductivity 90 to 130 3.4 to 5 9.0 to 10.0 (μS / cm, 25 ° C) pH 6.0 to 6.5 5.5 to 6.5 4.0 to 5.0
【0015】[0015]
【発明の効果】以上のように本発明の方法によれば、原
水中に溶存する炭酸ガスが極めて簡単な装置により除去
されるので逆浸透膜装置の設備費及びランニングコスト
を大幅に低下させることができ、かつ高純度の処理水が
得られる。従って、本発明方法を純水製造工程に組み込
むことにより、経済性の改善に寄与するところは大であ
る。As described above, according to the method of the present invention, the carbon dioxide gas dissolved in the raw water is removed by an extremely simple device, so that the equipment cost and running cost of the reverse osmosis membrane device are greatly reduced. And high-purity treated water can be obtained. Therefore, incorporating the method of the present invention into the pure water production process greatly contributes to the improvement of economic efficiency.
【図1】 第1図は、本発明の逆浸透膜処理の実施態様
を示すフローの概略説明図である。FIG. 1 is a schematic explanatory diagram of a flow showing an embodiment of a reverse osmosis membrane treatment of the present invention.
1 原水供給管 2 気液混合器 3 原水貯槽 4 空気導入管 5 散水手段 6 高圧ポンプ 7 逆浸透膜モジュール 8 処理水出口管 9 吸排気管 DESCRIPTION OF SYMBOLS 1 Raw water supply pipe 2 Gas-liquid mixer 3 Raw water storage tank 4 Air introduction pipe 5 Water sprinkling means 6 High pressure pump 7 Reverse osmosis membrane module 8 Treated water outlet pipe 9 Suction and exhaust pipe
Claims (3)
理する方法において、原水に空気を加圧溶解させ、空気
を溶存した原水を原水貯槽内の上部空間部に設けられた
散水手段により散水して原水貯槽に貯留し、次いで貯留
した原水を逆浸透膜処理することを特徴とする原水の逆
浸透膜処理方法。In a method of treating raw water stored in a raw water storage tank with a reverse osmosis membrane, air is pressurized and dissolved in the raw water, and the raw water in which the air is dissolved is dispersed by a watering means provided in an upper space in the raw water storage tank. A reverse osmosis membrane treatment method for raw water, comprising sprinkling water and storing the raw water in a raw water storage tank, and then treating the stored raw water with a reverse osmosis membrane.
置、空気を溶存した原水の散水手段を槽内上部に備えた
原水貯槽及び原水貯槽に貯留した原水の逆浸透膜処理装
置から順次構成されてなる原水の処理装置。2. A gas-liquid mixing device for pressurizing and dissolving air in raw water, a raw water storage tank provided with an air-dissolved raw water sprinkling means in an upper part of the tank, and a reverse osmosis membrane treatment device for raw water stored in the raw water storage tank. A raw water treatment device configured.
特徴とする請求項1記載の原水の逆浸透膜処理方法。3. The method according to claim 1, wherein the raw water is water treated by a reverse osmosis membrane.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27936797A JPH1199388A (en) | 1997-09-29 | 1997-09-29 | Reverse osmotic membrane treatment of raw water and device therefor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27936797A JPH1199388A (en) | 1997-09-29 | 1997-09-29 | Reverse osmotic membrane treatment of raw water and device therefor |
Publications (1)
Publication Number | Publication Date |
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JPH1199388A true JPH1199388A (en) | 1999-04-13 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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JP27936797A Pending JPH1199388A (en) | 1997-09-29 | 1997-09-29 | Reverse osmotic membrane treatment of raw water and device therefor |
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JP (1) | JPH1199388A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104692495A (en) * | 2015-03-23 | 2015-06-10 | 环境保护部南京环境科学研究所 | Iron-carbon micro-electrolysis device and use method thereof |
-
1997
- 1997-09-29 JP JP27936797A patent/JPH1199388A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104692495A (en) * | 2015-03-23 | 2015-06-10 | 环境保护部南京环境科学研究所 | Iron-carbon micro-electrolysis device and use method thereof |
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