JPH0739881A - Pretreatment of raw water - Google Patents

Pretreatment of raw water

Info

Publication number
JPH0739881A
JPH0739881A JP18567793A JP18567793A JPH0739881A JP H0739881 A JPH0739881 A JP H0739881A JP 18567793 A JP18567793 A JP 18567793A JP 18567793 A JP18567793 A JP 18567793A JP H0739881 A JPH0739881 A JP H0739881A
Authority
JP
Japan
Prior art keywords
raw water
water
pretreatment
membrane
exchange resin
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.)
Withdrawn
Application number
JP18567793A
Other languages
Japanese (ja)
Inventor
Masaki Yokoyama
正樹 横山
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.)
Renesas Semiconductor Manufacturing Co Ltd
Kansai Nippon Electric Co Ltd
Original Assignee
Renesas Semiconductor Manufacturing Co Ltd
Kansai Nippon Electric Co 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 Renesas Semiconductor Manufacturing Co Ltd, Kansai Nippon Electric Co Ltd filed Critical Renesas Semiconductor Manufacturing Co Ltd
Priority to JP18567793A priority Critical patent/JPH0739881A/en
Publication of JPH0739881A publication Critical patent/JPH0739881A/en
Withdrawn legal-status Critical Current

Links

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)
  • Treatment Of Water By Ion Exchange (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

PURPOSE:To unnecessitate a chemical for raw water pretreatment or to sharply reduce its quantity and to prolong the water gathering time and the resin life of an ion exchange resin by giving raw water activation pretreatment with a water passing utensil packed with granulated electric stones and passing it through a reverse osmosis membrane and an ion exchange resin in order, allowing main treatment to be performed. CONSTITUTION:When raw water 5 is passed through a water passing utensil 10 packed with granulated electric stones E, calcium hydroxide, magnesium hydroxide, etc., are ionized to generate no scale by surface activity action due to hydroxyl ions, and an oxidizing agent, such as chlorine and hydrogen peroxide is reduced by reduction action. In this way, the raw water 5 is pretreated just in front of the 1st RO membrane 1 to prevent the deterioration of the 1st RO membrane 1 due to an oxidizing agent and the clogging of it due to scale without hydrochloric acid and a chemical for pretreatment, such as a reducing agent being used. Or even if the raw water pretreatment effect is detected and hydrochloric acid and the chemical for pretreatment are used, their used quantity is sharply decreased than here to fore. After that, main treatment, such as demineralization is finally performed through an ion exchange resin 4 as in the conventional manner.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は逆浸透膜及びイオン交換
樹脂によって本処理される原水の前処理方法に関するも
のである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for pretreatment of raw water which is main treated with a reverse osmosis membrane and an ion exchange resin.

【0002】[0002]

【従来の技術】例えば市水を原水として純水化処理する
純水製造プラントでは、逆浸透膜及びイオン交換樹脂を
用いており、その装置の一例を図2を参照して次に説明
する。図において(1)は第1逆浸透膜(以下、第1R
O膜と称する。)、(2)は脱気塔、(3)は第2逆浸
透膜(以下、第2RO膜と称する。)、(4)はイオン
交換樹脂塔である。上記第1RO膜(1)は半透膜から
なり、ブライン水(6)の排水バルブを絞った状態で約
20〜25Kg/m2の高圧の市水を原水(5)として
流入させると、膜面に対してかなり高い圧力が加わり、
半透膜を透過した原水(5)は、その中の塩類、イオ
ン、有機物等の水分子よりも大きい粒子が半透膜で塞き
止められて濾過処理される。一方、半透膜を透過せず、
高濃度に濃縮された塩類やイオン、有機物等を含有する
原水(5)はブライン水(6)として処理水と異なる排
水口から排出される。脱気塔(2)は加圧窒素を封入
し、第1RO膜(1)を透過した処理水中の溶存酸素や
炭酸ガスを脱気してポンプ(7)により次段に供給す
る。第2RO膜(3)は、脱気した処理水を再度、濾過
処理する。イオン交換樹脂塔(4)はイオン交換樹脂を
含み、それまでに除去出来なかったイオン等を最終的に
除去するもので、適宜、多段並列に設置し、切り替え使
用しても良い。
2. Description of the Related Art For example, in a pure water production plant for purifying city water as raw water, a reverse osmosis membrane and an ion exchange resin are used. An example of the apparatus will be described below with reference to FIG. In the figure, (1) is the first reverse osmosis membrane (hereinafter referred to as the first R
It is called an O film. ), (2) is a degassing tower, (3) is a second reverse osmosis membrane (hereinafter referred to as a second RO membrane), and (4) is an ion exchange resin tower. The first RO membrane (1) is composed of a semipermeable membrane, and when high-pressure city water of about 20 to 25 Kg / m 2 is introduced as raw water (5) with the drain valve of brine water (6) being throttled, the membrane is formed. A fairly high pressure is applied to the surface,
In the raw water (5) that has passed through the semipermeable membrane, particles larger than water molecules such as salts, ions and organic substances therein are blocked by the semipermeable membrane and filtered. On the other hand, it does not penetrate the semipermeable membrane,
Raw water (5) containing salts, ions, organic matter, etc. concentrated to a high concentration is discharged as brine water (6) from a drain port different from the treated water. The deaeration tower (2) is filled with pressurized nitrogen, and the dissolved oxygen and carbon dioxide gas in the treated water that has permeated the first RO membrane (1) are deaerated and supplied to the next stage by a pump (7). The second RO membrane (3) again filters the degassed treated water. The ion-exchange resin tower (4) contains an ion-exchange resin and finally removes the ions and the like that could not be removed up to that point.

【0003】ここで、市水(5)はCa、Mg、Al等
の金属成分を多く含有する一方、使用済みの水を市水
(5)中に回収して再利用しているため、それが塩基性
を帯びると、水酸化カルシウムや水酸化マグネシウム等
の結晶が析出し、それがスケールとなって第1の半透膜
(1)の目詰まりの原因となる。そのため、前処理とし
て市水(5)のpH値を自動測定して設定値と比較し、
それに応じて適宜、第1RO膜(1)の前段で所定量の
塩酸(8)等を注入して市水(5)を酸性にし、水酸化
カルシウム等の析出を防止している。又、一部回収した
使用済み水を使用する場合は塩素や過酸化水素等の酸化
剤を若干含有するため、酸化剤を含む水が第1RO膜
(1)を透過すると、RO膜は劣化するため、上記同
様、市水(5)の酸化還元値を自動測定して設定値と比
較し、第1RO膜(1)の前段で所定量の還元剤(9)
を注入し、市水(5)中に含まれる酸化剤を還元してR
O膜の劣化を防止している。
Here, the city water (5) contains a large amount of metal components such as Ca, Mg and Al, while the used water is recovered and reused in the city water (5). Becomes basic, crystals of calcium hydroxide, magnesium hydroxide, etc. are deposited, which becomes scale and causes clogging of the first semipermeable membrane (1). Therefore, as a pretreatment, the pH value of city water (5) is automatically measured and compared with the set value,
Correspondingly, a predetermined amount of hydrochloric acid (8) or the like is injected before the first RO membrane (1) to acidify the city water (5) to prevent precipitation of calcium hydroxide or the like. Further, when the used water that is partially recovered is used, it contains a small amount of an oxidizing agent such as chlorine or hydrogen peroxide, and therefore, when the water containing the oxidizing agent passes through the first RO membrane (1), the RO membrane deteriorates. Therefore, similarly to the above, the redox value of the city water (5) is automatically measured and compared with the set value, and a predetermined amount of the reducing agent (9) is provided before the first RO membrane (1).
Is injected to reduce the oxidant contained in the city water (5) and R
It prevents the deterioration of the O film.

【0004】[0004]

【発明が解決しようとする課題】解決しようとする課題
は、原水(5)の前処理として第1RO膜(1)の前段
で塩酸や還元剤等を原水(1)に注入すると、後段で交
換イオンが過剰となってイオン交換樹脂塔(4)が過負
荷状態となり、イオン交換樹脂の採水時間や寿命が大幅
に低下する点である。
The problem to be solved is to inject hydrochloric acid, a reducing agent, etc. into the raw water (1) at the front stage of the first RO membrane (1) as a pretreatment of the raw water (5) and replace it at the rear stage. This is the point that the ion becomes excessive and the ion exchange resin tower (4) becomes overloaded, and the water collection time and life of the ion exchange resin are significantly reduced.

【0005】[0005]

【課題を解決するための手段】本発明は、多数の粒状電
気石を充填した通水器具内に原水を通水して活水化前処
理した後、上記原水を逆浸透膜及びイオン交換樹脂に順
次、通水して本処理することを特徴とする。
According to the present invention, raw water is passed through a water-passing device filled with a large number of tourmaline particles to perform pretreatment for activation, and then the raw water is converted into a reverse osmosis membrane and an ion exchange resin. The feature is that the main treatment is carried out by sequentially passing water.

【0006】[0006]

【作用】上記技術的手段によれば、多数の粒状電気石を
充填した通水器具内に原水を通水し、塩酸や還元剤等の
原水前処理用薬液に代替して活水化前処理した後、上記
原水を逆浸透膜及びイオン交換樹脂に順次、通水して本
処理すると、原水前処理用薬液の使用が不要又は薬液使
用量が大幅に減少すると同時に後段のイオン交換樹脂の
採水時間や寿命が大幅に増加する。
According to the above technical means, the raw water is passed through the water-passing device filled with a large number of granular tourmaline, and the raw water pre-treatment is performed in place of the raw water pre-treatment chemical solution such as hydrochloric acid or a reducing agent. After that, if the raw water is passed through the reverse osmosis membrane and the ion-exchange resin one after another for main treatment, the use of raw water pretreatment liquid chemical is unnecessary or the chemical liquid consumption is greatly reduced, and at the same time the latter-stage ion-exchange resin water sampling The time and life are greatly increased.

【0007】[0007]

【実施例】本発明に係る原水の前処理方法の実施例を図
1を参照して以下に説明する。図2に示す部分と同一部
分には同一参照符号を付してその説明を省略する。相違
する点は、塩酸や還元剤等の原水前処理用薬液に代替し
て、3〜5mm径のビーズ状電気石(E)を多数、充填
した通水器具(10)を第1RO膜(1)の前段に設置
し、原水(5)としての市水を第1RO膜(1)に通水
するに先立って通水器具(10)内に通水して前処理した
ことである。上記電気石(E)を充填した通水器具(1
0)内を水が通ると、活性化した界面活性物質としての
ヒドロキシルイオン(H32-が生まれ、ヒドロキシ
ルイオンの単分子膜で包まれた界面活性を持つ水が生じ
て次に示す作用を呈する。まず「浸透」、「濡れ」、
「コロイド化」、「分散」、「乳化」等の界面活性作用
を示し、特にカルシウムやシリカ等が界面で析出して生
じる結晶は、界面に配向しているヒドロキシルイオンの
方向性によって付着性のない鱗片状の結晶となり、スケ
ールを作らない。又、界面の水は固体表面に対し還元性
を示して金属の不働態化とその維持に役立ち、更に、水
中の塩素等は加水分解され、その揮発性や刺激性が失わ
れて不活性化される。そこで、上記電気石(E)は現
在、活水器として洗浄用水、飲料・調理用水、給排水管
系等に使用されている。
EXAMPLE An example of a method for pretreating raw water according to the present invention will be described below with reference to FIG. The same parts as those shown in FIG. 2 are designated by the same reference numerals and the description thereof will be omitted. The difference is that instead of a raw water pretreatment chemical such as hydrochloric acid or a reducing agent, a water passing device (10) filled with a large number of bead-shaped tourmaline (E) having a diameter of 3 to 5 mm is attached to the first RO membrane (1). ) Was installed in front of the first RO membrane (1) and pretreated by passing the city water as raw water (5) through the first RO membrane (1). Water passing equipment (1) filled with tourmaline (E)
0) in the the passage of water, hydroxyl ions as activated surfactant (H 3 O 2) - is born, the following occurs water with surfactant wrapped with a monomolecular film of hydroxyl ions Exerts an action. First, "penetration", "wetness",
Crystals that exhibit surface-active effects such as "colloidization", "dispersion", "emulsification", etc., especially when calcium, silica, etc. are deposited at the interface, are formed by the directionality of hydroxyl ions oriented at the interface. It does not have scales and does not form scales. In addition, the water at the interface shows a reducing property to the solid surface to help passivate and maintain the metal, and chlorine in water is hydrolyzed and loses its volatility and irritation and becomes inactive. To be done. Therefore, the tourmaline (E) is currently used as a water-activating device for washing water, drinking / cooking water, water supply / drainage pipe system, and the like.

【0008】上記構成において、第1RO膜(1)の前
段で市水(5)を、粒状電気石(E)を充填した通水器
具(10)内に通水すると、ヒドロキシルイオンによる界
面活性作用により水酸化カルシウムや水酸化マグネシウ
ム等はイオン化してスケールが発生せず、又、還元作用
により塩素や過酸化水素等の酸化剤を還元する。そのた
め、塩酸や還元剤等の前処理用薬液を使用することな
く、第1RO膜(1)の直前で原水(1)を前処理して
第1RO膜(1)の酸化剤による劣化やスケールによる
目詰まりを防止する。或いは、原水前処理効果を検知し
て塩酸や還元剤等の前処理用薬液を適宜、使用しても良
いが、その場合でも、薬液使用量は従来よりも大幅に減
少する。その後、従来同様、イオン交換樹脂塔(4)を
経て最終的に原水(5)を純水化処理等の本処理する。
In the above structure, when the city water (5) is passed through the water passing device (10) filled with the tourmaline particles (E) before the first RO membrane (1), the surface active action by the hydroxyl ions is exerted. As a result, calcium hydroxide, magnesium hydroxide, etc. are ionized and scales are not generated, and the reducing action reduces oxidizing agents such as chlorine and hydrogen peroxide. Therefore, the raw water (1) is pretreated immediately before the first RO membrane (1) without using a pretreatment chemical such as hydrochloric acid or a reducing agent, and the first RO membrane (1) is deteriorated by an oxidant or caused by scale. Prevent clogging. Alternatively, a pretreatment chemical such as hydrochloric acid or a reducing agent may be appropriately used by detecting the raw water pretreatment effect, but even in that case, the amount of the chemical used is significantly reduced as compared with the conventional case. Then, as in the conventional case, the raw water (5) is finally subjected to a main treatment such as a purification treatment through the ion exchange resin tower (4).

【0009】[0009]

【発明の効果】本発明によれば、多数の粒状電気石を充
填した通水器具内に原水を通水して前処理した後、原水
を逆浸透膜及びイオン交換樹脂に順次、通水して純水化
等の本処理したから、原水前処理用薬液の使用が不要又
は薬液使用量が大幅に減少し、後段のイオン交換樹脂に
加わる負荷が大幅に軽減してイオン交換樹脂の採水時間
や樹脂寿命の延長を図ることが出来る。
EFFECTS OF THE INVENTION According to the present invention, raw water is passed through a water passing device filled with a large number of granular tourmaline to be pretreated, and then the raw water is passed through a reverse osmosis membrane and an ion exchange resin in sequence. Since the main treatment such as deionized water is not required, the use of raw water pretreatment chemicals is not necessary or the amount of chemicals used is drastically reduced, and the load on the ion-exchange resin in the latter stage is greatly reduced, and the ion-exchange resin water sampling It is possible to extend the time and the resin life.

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

【図1】本発明に係る原水の前処理方法の実施例を示す
ブロック図である。
FIG. 1 is a block diagram showing an embodiment of a raw water pretreatment method according to the present invention.

【図2】従来の原水の前処理方法の一例を示すブロック
図である。
FIG. 2 is a block diagram showing an example of a conventional raw water pretreatment method.

【符号の説明】[Explanation of symbols]

1 逆浸透膜 3 逆浸透膜 4 イオン交換樹脂 5 原水 10 通水器具 E 電気石 1 Reverse osmosis membrane 3 Reverse osmosis membrane 4 Ion exchange resin 5 Raw water 10 Water passing equipment E Tourmaline

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 多数の粒状電気石を充填した通水器具内
に原水を通水して活水化前処理した後、上記原水を逆浸
透膜及びイオン交換樹脂に順次、通水して本処理するこ
とを特徴とする原水の前処理方法。
1. A raw water is passed through a water-flowing device filled with a large number of tourmaline particles for pre-activation treatment, and then the raw water is sequentially passed through a reverse osmosis membrane and an ion exchange resin for main treatment. A method for pretreatment of raw water, which comprises:
【請求項2】 本処理は市水を原水とする純水化処理で
あることを特徴とする請求項1記載の原水の前処理方
法。
2. The pretreatment method for raw water according to claim 1, wherein this treatment is a purification treatment using city water as raw water.
JP18567793A 1993-07-28 1993-07-28 Pretreatment of raw water Withdrawn JPH0739881A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18567793A JPH0739881A (en) 1993-07-28 1993-07-28 Pretreatment of raw water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18567793A JPH0739881A (en) 1993-07-28 1993-07-28 Pretreatment of raw water

Publications (1)

Publication Number Publication Date
JPH0739881A true JPH0739881A (en) 1995-02-10

Family

ID=16174940

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18567793A Withdrawn JPH0739881A (en) 1993-07-28 1993-07-28 Pretreatment of raw water

Country Status (1)

Country Link
JP (1) JPH0739881A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104496097A (en) * 2014-12-23 2015-04-08 广西饮用水研究院 Production method of healthy drinking water
WO2016147414A1 (en) * 2015-03-19 2016-09-22 三菱重工業株式会社 Water treatment system and power generation apparatus

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104496097A (en) * 2014-12-23 2015-04-08 广西饮用水研究院 Production method of healthy drinking water
CN104496097B (en) * 2014-12-23 2016-02-17 广西饮用水研究院 A kind of production method of healthy drinking water
WO2016147414A1 (en) * 2015-03-19 2016-09-22 三菱重工業株式会社 Water treatment system and power generation apparatus
US10399878B2 (en) 2015-03-19 2019-09-03 Mitsubishi Heavy Industries Engineering, Ltd. Water treatment system and power generation facility

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