JPH06304558A - Trihalomethane formation restraining method by low pressure reverse osmosis membrane - Google Patents

Trihalomethane formation restraining method by low pressure reverse osmosis membrane

Info

Publication number
JPH06304558A
JPH06304558A JP12059993A JP12059993A JPH06304558A JP H06304558 A JPH06304558 A JP H06304558A JP 12059993 A JP12059993 A JP 12059993A JP 12059993 A JP12059993 A JP 12059993A JP H06304558 A JPH06304558 A JP H06304558A
Authority
JP
Japan
Prior art keywords
water
reverse osmosis
osmosis membrane
trihalomethane
raw water
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.)
Granted
Application number
JP12059993A
Other languages
Japanese (ja)
Other versions
JP2732190B2 (en
Inventor
Norihiro Kawashima
紀宏 川島
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.)
Kawasaki Heavy Industries Ltd
Original Assignee
Kawasaki Heavy Industries 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 Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP12059993A priority Critical patent/JP2732190B2/en
Publication of JPH06304558A publication Critical patent/JPH06304558A/en
Application granted granted Critical
Publication of JP2732190B2 publication Critical patent/JP2732190B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To effectively remove a trihalomethane precursor and to easily secure safe potable water in a simple water supply, etc., by adding copper ions to a raw water contg. the trihalomethane precursor before passing the raw water through a low pressure reverse osmosis membrane. CONSTITUTION:In a simple water supply using a shallow well as a water source, raw water contg. a lot of a precursor before the formation of trihalonmethane is drawn by a raw water pump 10. First, the raw water is fed into a filter 12, such as a media filter and turbid matter is removed. Next, after copper sulfate is added (added quantity: 0.1-0.5ppm) to the raw water that has been filtered to decompose bacteria without decomposing the trihalomethane precursor, then the raw water is introduced into a low pressure reverse osmosis membrane 16 through a booster pump 14, and the low pressure reverse osmosis membrane 16, the raw water is separated into a permeated water (potable water) and a concentrate (waste water) and the permeated water is fed to places where it is consumed after a final treatment of adding a post-chlorine agent.

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、トリハロメタン前駆体
を含む河川水、湖沼水、井戸水等を水源とする飲料水製
造プラントにおいて、トリハロメタン前駆体を分解する
ことなく、バクテリアを殺菌状態に保ち、低圧逆浸透膜
を用いてトリハロメタン前駆体を除去することにより、
トリハロメタンの生成を抑制する方法に関するものであ
る。
BACKGROUND OF THE INVENTION The present invention, in a drinking water production plant using river water, lake water, well water, etc. containing a trihalomethane precursor as a water source, keeps bacteria in a sterilized state without decomposing the trihalomethane precursor, By removing the trihalomethane precursor using a low pressure reverse osmosis membrane,
The present invention relates to a method for suppressing the production of trihalomethane.

【0002】[0002]

【従来の技術】トリハロメタンは、平成5年末に厚生省
の水質基準の規制対象に加えられる物質であり、その処
理方法が種々検討されている。トリハロメタンは、その
前駆体(フミン酸、フルボ酸、ヒマトメラミン酸等)が
塩素により分解されて生成する物質であり、分子量が小
さく、分離が非常に困難であった(1983年10月3
0日に技報堂から発行された「水道とトリハロメタン」
参照)。
2. Description of the Related Art Trihalomethane is a substance added to the water quality standards of the Ministry of Health and Welfare at the end of 1993, and various treatment methods have been studied. Trihalomethane is a substance produced by decomposing its precursor (humic acid, fulvic acid, hematomelamic acid, etc.) with chlorine, has a small molecular weight, and was very difficult to separate (October 3, 1983).
"Water supply and trihalomethane" issued by Gihodo on 0th
reference).

【0003】従来、トリハロメタンを除去するための対
策としては、殺菌剤として塩素の代わりにオゾンを使用
して、トリハロメタン前駆体を低分子量の炭化水素化合
物に分解し、この低分子化合物を活性炭で吸着する方法
があった。なお、逆浸透膜によるトリハロメタンの生成
抑制及び除去方法について、従来技術を調査したが、該
当する公報は検索できなかった。
Conventionally, as a measure for removing trihalomethane, ozone was used instead of chlorine as a bactericide to decompose a trihalomethane precursor into a low molecular weight hydrocarbon compound, and this low molecular weight compound was adsorbed by activated carbon. There was a way to do it. The prior art was investigated for a method of suppressing and removing trihalomethane by a reverse osmosis membrane, but the corresponding publication could not be searched.

【0004】[0004]

【発明が解決しようとする課題】しかし、殺菌剤として
オゾンを使用し活性炭で吸着する従来の方法では、オゾ
ン発生装置を使用するので、装置が複雑になり、廃オゾ
ン処理も必要となる。また、活性炭を定期的に交換する
必要があり、メンテナンスコストが高くなるという問題
点もあった。
However, in the conventional method of using ozone as a bactericide and adsorbing with activated carbon, since an ozone generator is used, the apparatus becomes complicated and waste ozone treatment is also required. In addition, it is necessary to regularly replace the activated carbon, resulting in a high maintenance cost.

【0005】トリハロメタンは、上記のように分子量が
小さく、低圧逆浸透膜を用いても分離効率が低いので、
トリハロメタン前駆体からトリハロメタンが生成してし
まうと分離が非常に困難となっていた。一方、トリハロ
メタン前駆体は分子量が大きく、低圧逆浸透膜を用いれ
ば95%以上の分離効率が得られる。したがって、トリ
ハロメタンを除去するためには、その前駆体を低圧逆浸
透膜を用いて分離することが得策である。なお、低圧逆
浸透膜とは、海水淡水化用逆浸透膜とUF(限外ろ過
膜)の中間膜であって、別名、ルーズ逆浸透膜とかナノ
メンブレンとも呼ばれている。
Since trihalomethane has a small molecular weight as described above and has a low separation efficiency even when a low pressure reverse osmosis membrane is used,
If trihalomethane was produced from the trihalomethane precursor, separation was very difficult. On the other hand, the trihalomethane precursor has a large molecular weight, and if a low pressure reverse osmosis membrane is used, a separation efficiency of 95% or more can be obtained. Therefore, in order to remove trihalomethane, it is advisable to separate its precursor using a low pressure reverse osmosis membrane. The low-pressure reverse osmosis membrane is an intermediate membrane between a seawater desalination reverse osmosis membrane and a UF (ultrafiltration membrane), and is also called a loose reverse osmosis membrane or a nanomembrane.

【0006】しかし、一般に、トリハロメタン前駆体を
多く含む河川、湖沼中には、バクテリアが多量に存在
し、低圧逆浸透膜の膜面にバクテリアが繁殖するため
に、装置の運転が不可能になることがあった。一方、低
圧逆浸透膜の膜面にバクテリアが繁殖するのを防止する
ために、塩素の代わりにオゾンを用いて殺菌することも
考えられるが、トリハロメタン前駆体が、オゾンにより
低分子量の炭化水素化合物に分解されてしまい、低圧逆
浸透膜での分離効率が大幅に低下し、その後、塩素で殺
菌すれば、トリハロメタンが生成する可能性があった。
[0006] Generally, however, a large amount of bacteria are present in rivers and lakes containing a large amount of trihalomethane precursors, and the bacteria are propagated on the membrane surface of the low-pressure reverse osmosis membrane. There was an occasion. On the other hand, in order to prevent bacteria from propagating on the membrane surface of the low-pressure reverse osmosis membrane, ozone may be used in place of chlorine for sterilization.However, the trihalomethane precursor is a hydrocarbon compound of low molecular weight due to ozone. If it is sterilized with chlorine after that, there is a possibility that trihalomethane will be generated.

【0007】本発明は上記の諸点に鑑みなされたもの
で、トリハロメタン前駆体を含む河川水、湖沼水、井戸
水等から飲料水を製造するに際し、低圧逆浸透膜を用い
てトリハロメタン前駆体の除去を行ない、低圧逆浸透膜
の膜面にバクテリアが繁殖するのを防止するために、銅
イオンを添加する低圧逆浸透膜によるトリハロメタン生
成抑制方法を提供することを目的としている。
The present invention has been made in view of the above points, and when producing drinking water from river water, lake water, well water, etc. containing a trihalomethane precursor, the trihalomethane precursor is removed using a low pressure reverse osmosis membrane. In order to prevent bacteria from growing on the membrane surface of the low-pressure reverse osmosis membrane, it is an object of the present invention to provide a method for suppressing trihalomethane production by a low-pressure reverse osmosis membrane to which copper ions are added.

【0008】[0008]

【課題を解決するための手段】上記の目的を達成するた
めに、本発明の低圧逆浸透膜によるトリハロメタン生成
抑制方法は、図1に示すように、トリハロメタン前駆体
を含む原水中に銅イオンを添加した後、この原水を低圧
逆浸透膜に通してトリハロメタン前駆体を除去すること
を特徴としている。
In order to achieve the above object, a method for suppressing trihalomethane production by a low pressure reverse osmosis membrane of the present invention is, as shown in FIG. 1, a method in which copper ions are added to raw water containing a trihalomethane precursor. After addition, the raw water is passed through a low pressure reverse osmosis membrane to remove the trihalomethane precursor.

【0009】この場合、銅イオンの添加量は、0.1〜
0.5ppmであることが好ましい。すなわち、銅イオン
の添加量が0.1ppm未満の場合は、低圧逆浸透膜の膜
面にバクテリアが繁殖しやすいという不都合があり、一
方、銅イオンの添加量が0.5ppmを越える場合は、逆
浸透膜の濃縮水側(排水側)の銅イオン濃度が高くな
り、環境省の排水排出基準をクリアできないという不都
合がある。
In this case, the amount of copper ions added is 0.1 to 0.1%.
It is preferably 0.5 ppm. That is, when the added amount of copper ions is less than 0.1 ppm, there is a disadvantage that bacteria are easily proliferated on the membrane surface of the low pressure reverse osmosis membrane, while when the added amount of copper ions exceeds 0.5 ppm, There is an inconvenience that the copper ion concentration on the concentrated water side (drainage side) of the reverse osmosis membrane becomes high and the wastewater discharge standard of the Ministry of the Environment cannot be met.

【0010】[0010]

【実施例】以下、本発明を実施例に基づいてさらに詳細
に説明するが、本発明は下記実施例に何ら限定されるも
のではなく、その要旨を変更しない範囲において適宜変
更して実施することが可能なものである。 実施例1 図1は、本発明の方法を実施する装置の一例を示してい
る。本設備は、浅井戸を水源とする簡易水道であり、原
水中には、トリハロメタン前駆体を多量に含んでいる。
図1において、原水ポンプ10により供給された原水
は、まず、メディアフィルター等のろ過器12で濁質が
除去され、その後、トリハロメタン前駆体を分解するこ
となくバクテリアを殺菌するために、硫酸銅が添加され
る。なお、濁質が除去される前に、あるいは濁質除去の
前及び後に、硫酸銅が添加される場合もある。硫酸銅が
添加された原水は、ブースターポンプ14を経て、低圧
逆浸透膜16に導入される。この場合の運転圧力は、例
えば15〜20kg/cm2である。低圧逆浸透膜16によ
り、原水は、透過水(飲料水)と濃縮水(排水)とに分
離され、透過水(飲料水)には、後塩素剤が塩素で約
0.5mg/l添加され、最終処理がなされる。
EXAMPLES The present invention will be described in more detail based on the following examples, but the invention is not intended to be limited to the following examples, and various modifications may be made without departing from the scope of the invention. Is possible. Example 1 FIG. 1 shows an example of an apparatus for carrying out the method of the present invention. This facility is a simple water supply system that uses shallow wells as a water source, and the raw water contains a large amount of trihalomethane precursors.
In FIG. 1, raw water supplied by a raw water pump 10 is first subjected to removal of suspended solids by a filter 12 such as a media filter, and thereafter, in order to kill bacteria without decomposing a trihalomethane precursor, copper sulfate is added to the raw water. Is added. Incidentally, copper sulfate may be added before the suspension is removed, or before and after the suspension is removed. Raw water to which copper sulfate has been added is introduced into the low-pressure reverse osmosis membrane 16 via the booster pump 14. The operating pressure in this case is, for example, 15 to 20 kg / cm 2 . The low-pressure reverse osmosis membrane 16 separates the raw water into permeated water (drinking water) and concentrated water (drainage), and to the permeated water (drinking water), a post-chlorine agent is added by about 0.5 mg / l of chlorine. , Final processing is done.

【0011】図1に示すフローにおいて、トリハロメタ
ン前駆体を分解せずに、バクテリアの殺菌効果がある硫
酸銅を銅イオンで0.2ppm添加したところ、その後に
低圧逆浸透膜の膜面でバクテリアが繁殖することはな
く、銅イオンによる膜性能の劣化もほとんど起こらなか
った。表1に、実施例1における装置の処理結果を示
す。なお、トリハロメタン生成能は、原水及び透過水に
それぞれ10mg/lの次亜塩素酸ソーダを注入したとき
に生成する総トリハロメタン濃度で示している。
In the flow shown in FIG. 1, 0.2 ppm of copper sulfate, which has a bactericidal effect on bacteria, was added with copper ions without decomposing the trihalomethane precursor. After that, bacteria were formed on the surface of the low-pressure reverse osmosis membrane. It did not propagate and there was almost no deterioration of the membrane performance due to copper ions. Table 1 shows the processing results of the apparatus in Example 1. The trihalomethane production ability is shown by the total concentration of trihalomethane produced when 10 mg / l of sodium hypochlorite is injected into the raw water and the permeated water, respectively.

【0012】[0012]

【表1】 [Table 1]

【0013】本実施例では、特別な装置として、銅イオ
ンを注入するための装置と低圧逆浸透膜装置を必要とす
るのみであるので、設備がコンパクトで済み、操作も簡
単であり、中小の簡易水道にも容易に適用することがで
きる。なお、銅イオンも厚生省の水質基準の規制対象に
入っているが、注入された銅イオンは、低圧逆浸透膜に
より90%以上が分離除去可能であるので、厚生省の水
質基準は十分クリアすることができる。
In the present embodiment, only a device for injecting copper ions and a low-pressure reverse osmosis device are required as special devices, so the equipment is compact, the operation is simple, and small and medium-sized It can be easily applied to simple water supply. Although copper ions are also subject to the water quality standards of the Ministry of Health, 90% or more of the injected copper ions can be separated and removed by the low pressure reverse osmosis membrane, so the water quality standards of the Ministry of Health must be sufficiently cleared. You can

【0014】比較例1 図1に示す装置を硫酸銅の添加なしで運転した場合、運
転後1週間で低圧逆浸透膜の膜面にスライムが発生し、
運転が不可能となったので、中性洗剤を用いて化学洗浄
を行なってスライムを除去し、運転を再開したが、再び
スライムが発生し、運転が不可能となった。
Comparative Example 1 When the apparatus shown in FIG. 1 was operated without the addition of copper sulfate, slime was generated on the surface of the low pressure reverse osmosis membrane one week after the operation.
Since the operation was impossible, the chemical cleaning was performed using a neutral detergent to remove the slime and the operation was restarted, but the slime was generated again and the operation became impossible.

【0015】[0015]

【発明の効果】本発明は上記のように構成されているの
で、つぎのような効果を奏する。 (1) トリハロメタンを生成する前の前駆体の形で除
去するので、前駆体除去率も高く、また、膜面でのバク
テリアの繁殖も防止することができるので、トリハロメ
タン前駆体を多く含む、いわゆる汚れた水源でも飲料水
源として使用することができる。 (2) 装置が簡単であるので、簡易水道のような小型
飲料水プラントのトリハロメタン除去対策にも適用する
ことができる。 (3) 低圧逆浸透膜の寿命は3年程度と長いので、ラ
ンニングコスト、メンテナンスコストが低い。 (4) 操作が簡単なので、特別な技能を必要とするこ
となく、簡単に装置を運転することができる。
Since the present invention is configured as described above, it has the following effects. (1) Since trihalomethane is removed in the form of the precursor before it is produced, the precursor removal rate is high, and since the proliferation of bacteria on the membrane surface can be prevented, so-called trihalomethane precursor is contained in a large amount. Even dirty water sources can be used as drinking water sources. (2) Since the device is simple, it can be applied to measures for removing trihalomethane in small drinking water plants such as simple tap water. (3) Since the low-pressure reverse osmosis membrane has a long life of about 3 years, running costs and maintenance costs are low. (4) Since the operation is simple, the device can be easily operated without requiring special skill.

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

【図1】本発明の方法を実施する装置の一例を示す説明
図である。
FIG. 1 is an explanatory view showing an example of an apparatus for carrying out the method of the present invention.

【符号の説明】[Explanation of symbols]

10 原水ポンプ 12 ろ過器 14 ブースターポンプ 16 低圧逆浸透膜 10 Raw Water Pump 12 Filter 14 Booster Pump 16 Low Pressure Reverse Osmosis Membrane

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 トリハロメタン前駆体を含む原水中に銅
イオンを添加した後、この原水を低圧逆浸透膜に通して
トリハロメタン前駆体を除去することを特徴とする低圧
逆浸透膜によるトリハロメタン生成抑制方法。
1. A method for suppressing trihalomethane production by a low pressure reverse osmosis membrane, which comprises adding copper ions to raw water containing a trihalomethane precursor and then passing the raw water through a low pressure reverse osmosis membrane to remove the trihalomethane precursor. .
【請求項2】 銅イオンの添加量が0.1〜0.5ppm
であることを特徴とする請求項1記載の低圧逆浸透膜に
よるトリハロメタン生成抑制方法。
2. The amount of copper ion added is 0.1 to 0.5 ppm.
The method for suppressing trihalomethane production by the low-pressure reverse osmosis membrane according to claim 1, wherein
JP12059993A 1993-04-23 1993-04-23 Method for controlling trihalomethane formation by low pressure reverse osmosis membrane Expired - Fee Related JP2732190B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12059993A JP2732190B2 (en) 1993-04-23 1993-04-23 Method for controlling trihalomethane formation by low pressure reverse osmosis membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12059993A JP2732190B2 (en) 1993-04-23 1993-04-23 Method for controlling trihalomethane formation by low pressure reverse osmosis membrane

Publications (2)

Publication Number Publication Date
JPH06304558A true JPH06304558A (en) 1994-11-01
JP2732190B2 JP2732190B2 (en) 1998-03-25

Family

ID=14790252

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12059993A Expired - Fee Related JP2732190B2 (en) 1993-04-23 1993-04-23 Method for controlling trihalomethane formation by low pressure reverse osmosis membrane

Country Status (1)

Country Link
JP (1) JP2732190B2 (en)

Also Published As

Publication number Publication date
JP2732190B2 (en) 1998-03-25

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