JP2772612B2 - Water filtration method containing dissolved manganese using permeable membrane - Google Patents

Water filtration method containing dissolved manganese using permeable membrane

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Publication number
JP2772612B2
JP2772612B2 JP5206927A JP20692793A JP2772612B2 JP 2772612 B2 JP2772612 B2 JP 2772612B2 JP 5206927 A JP5206927 A JP 5206927A JP 20692793 A JP20692793 A JP 20692793A JP 2772612 B2 JP2772612 B2 JP 2772612B2
Authority
JP
Japan
Prior art keywords
manganese
permeable membrane
water
raw water
reaction tank
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.)
Expired - Fee Related
Application number
JP5206927A
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Japanese (ja)
Other versions
JPH0739872A (en
Inventor
吉次 神保
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.)
Suido Kiko Kaisha Ltd
Original Assignee
Suido Kiko Kaisha Ltd
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Filing date
Publication date
Application filed by Suido Kiko Kaisha Ltd filed Critical Suido Kiko Kaisha Ltd
Priority to JP5206927A priority Critical patent/JP2772612B2/en
Publication of JPH0739872A publication Critical patent/JPH0739872A/en
Application granted granted Critical
Publication of JP2772612B2 publication Critical patent/JP2772612B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Removal Of Specific Substances (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】この発明は、精密ろ過膜もしくは
限外ろ過膜の透過膜を用い、地下水を始めとする溶存マ
ンガン含有水のろ過を行ない、上水道・工業用水道・産
業用水等を造水するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention uses a permeable membrane such as a microfiltration membrane or an ultrafiltration membrane to filter water containing manganese, including groundwater, to produce water supply, industrial water, and industrial water. Water.

【0002】[0002]

【従来の技術】従来、精密ろ過膜もしくは限外ろ過膜を
利用して、上水道・工業用水道・産業用水等のろ過操作
を行なう試みはなされてきた。ところで、これらに用い
られる原水のうちほとんどの地下水には、鉄やマンガン
が含まれており、河川水にもマンガンが含まれているも
のもある。
2. Description of the Related Art Conventionally, attempts have been made to filter water, industrial water, industrial water, etc. using a microfiltration membrane or an ultrafiltration membrane. By the way, most of the raw water used for these contains iron and manganese, and some river water also contains manganese.

【0003】一般にマンガンは溶存状態で水中に存在し
ており、溶存マンガンはそのままでは透過膜では除去で
きない。溶存マンガンを透過膜で除去できるように析出
させるには、過マンガン酸カリウムやオゾンのように酸
化力の強い酸化剤を用いればできるが、これらの酸化剤
は高価であつたり、維持管理が難しいという欠点があつ
た。
Generally, manganese is present in water in a dissolved state, and dissolved manganese cannot be removed by a permeable membrane as it is. In order to precipitate dissolved manganese so that it can be removed by the permeable membrane, oxidizing agents such as potassium permanganate and ozone can be used, but these oxidizing agents are expensive and difficult to maintain. There was a disadvantage.

【0004】[0004]

【発明が解決しようとする課題】透過膜によるろ過は、
従来の砂ろ過に比べ、装置規模がコンパクトであるとい
う特徴や、原水に含まれる濁質や細菌類などの懸濁物質
を完全に除去する特徴があるが、マンガンのようにイオ
ン状態で水中に溶存している物質は除去できないという
欠点がある。一方、従来用いられていた塩素注入後、二
酸化マンガンをコ−テイングしたマンガン砂によるろ過
では、水中に懸濁物質が多い場合、ろ過抵抗が大きくな
るため、高ろ過速度をとれない欠点があつた。
SUMMARY OF THE INVENTION Filtration through a permeable membrane
Compared to conventional sand filtration, it has the feature of a compact device scale and the feature of completely removing suspended substances such as turbidity and bacteria contained in raw water. There is a disadvantage that dissolved substances cannot be removed. On the other hand, the conventional filtration using manganese sand coated with manganese dioxide after injecting chlorine has a drawback that a high filtration rate cannot be obtained because the filtration resistance increases when there are many suspended substances in water. .

【0005】[0005]

【課題を解決するための手段】上水道など飲料水・産業
用水などに用いられる透過膜は、膜孔径0.2μm以下
の精密ろ過膜もしくは限外ろ過膜が多く、これらで透過
すると、水中の非溶解性物質はほぼ100%除去できる
が、溶解性物質はほとんど除去できない。
The permeable membrane used for drinking water and industrial water, such as waterworks, is often a microfiltration membrane or an ultrafiltration membrane having a membrane pore size of 0.2 μm or less. Almost 100% of soluble substances can be removed, but almost no soluble substances can be removed.

【0006】これらに用いる原水には、表流水と地下水
があるが、表流水の一部及び地下水のほとんどに、水道
水水質基準値以上のマンガンが含まれている。マンガン
は、通常イオン状態で溶解しており、そのままでは上記
透過膜では除去できない。
[0006] Raw water used in these methods includes surface water and groundwater, and part of the surface water and most of the groundwater contain manganese that is higher than the standard value of tap water quality. Manganese is usually dissolved in an ionic state and cannot be removed by the above permeable membrane as it is.

【0007】原水には濁質や細菌類といつた非溶解性物
質のほか、溶解性の鉄分なども含まれている場合がある
が、鉄分は塩素剤の注入もしくは空気との接触により析
出し、非溶解性物質となる。しかし、マンガンは中性付
近のpHにおいては、塩素では容易に酸化析出しない。
[0007] Raw water sometimes contains insoluble substances such as turbidity and bacteria, as well as soluble iron, etc., which is precipitated by injection of a chlorinating agent or contact with air. , Becomes a non-soluble substance. However, manganese is not easily oxidized and precipitated with chlorine at around neutral pH.

【0008】一方、除マンガン用接触ろ材を用いたろ過
機では、原水中のマンガンをほぼ完全に除去できるが、
原水中の非溶解性物質によりろ材表層部分が容易に閉塞
してしまうためろ過速度を大きくとれず、前段に凝集沈
殿池や荒ろ過機を付けても、ろ過速度を120〜240
m/日程度しかとれないことが多かつた。
[0008] On the other hand, a filter using a contact filter medium for removing manganese can remove manganese in raw water almost completely.
Since the surface layer of the filter medium is easily clogged by the insoluble material in the raw water, the filtration speed cannot be increased.
In many cases, only about m / day could be taken.

【0009】マンガンは中性付近のpHにおいては、塩
素では容易に酸化析出しないが、二酸化マンガンを触媒
として用いれば、塩素でも容易に酸化析出する。そこで
原水に塩素系酸化剤を注入後、マンガン砂を敷設した反
応槽に通水し、マンガン砂と接触させることにより、マ
ンガンを酸化析出させることができる。この後、透過膜
でろ過すれば、マンガンも容易に分離除去できる。
[0009] Manganese is not easily oxidized and precipitated with chlorine at around neutral pH, but is easily oxidized and precipitated with chlorine when manganese dioxide is used as a catalyst. Then, after injecting a chlorine-based oxidizing agent into the raw water, water is passed through a reaction tank in which manganese sand is laid, and is brought into contact with manganese sand, whereby manganese can be oxidized and precipitated. Thereafter, by filtering through a permeable membrane, manganese can be easily separated and removed.

【0010】[0010]

【作用】マンガン砂を敷設した反応槽での通水は、下降
流で行なうと含有する他の非溶解性物質により砂層表面
を閉塞させ、短期間でろ過抵抗を上昇させてしまうた
め、高ろ過速度を取れない。一方、この考案では後段に
透過膜があるため、反応槽では原水中の非溶解性物質を
除去する必要はなく、単にマンガンを酸化析出させれば
よい。
[Function] If water is passed in a reaction tank with manganese sand laid down, the surface of the sand layer will be blocked by other insoluble substances contained in the downflow and the filtration resistance will increase in a short period of time. I can't take speed. On the other hand, in the present invention, since there is a permeable membrane at the latter stage, it is not necessary to remove insoluble substances in the raw water in the reaction tank, and manganese may be simply precipitated by oxidation.

【0011】二酸化マンガン存在下でのマンガン析出は
短時間で完了するため、反応槽内を上向流で通水させれ
ば、多量の非溶解性物質が流入してもマンガン砂を流動
状態にさせ、非溶解性物質の除去率は低下するが、マン
ガンの酸化析出反応はできる。マンガンが酸化析出すれ
ば原水中の濁質や細菌類と共に透過膜で完全除去ができ
る。
Since the precipitation of manganese in the presence of manganese dioxide is completed in a short time, if water is passed through the reaction tank in an upward flow, the manganese sand can be kept in a fluid state even if a large amount of insoluble substances flows. As a result, the removal rate of the insoluble material is reduced, but the manganese oxidative precipitation reaction can be performed. If manganese is oxidized and precipitated, it can be completely removed by a permeable membrane together with turbidity and bacteria in raw water.

【0012】マンガンの酸化析出の触媒としては、必ず
しもマンガン砂でなくとも、酸化析出したマンガンは二
酸化マンガンとなるため、自触媒として利用することが
できる。具体的には、予め少量のマンガン砂もしくは二
酸化マンガンを含むスラリ−を投入した反応槽に通水さ
せることにより、溶存マンガンは酸化析出し、二酸化マ
ンガンとなり自らが反応触媒となつて浮遊する。この現
象は、特に原水中に鉄分が多量に含まれる場合に顕著で
あり、マンガン砂を使用しないでもマンガンを酸化析出
させることができる。
The catalyst for oxidizing and depositing manganese is not necessarily manganese sand, but the manganese that is oxidized and deposited becomes manganese dioxide, and can be used as an autocatalyst. Specifically, by passing water through a reaction tank in which a slurry containing a small amount of manganese sand or manganese dioxide has been charged in advance, the dissolved manganese is oxidized and precipitated, becomes manganese dioxide, and floats itself as a reaction catalyst. This phenomenon is particularly remarkable when raw water contains a large amount of iron, and manganese can be oxidized and precipitated without using manganese sand.

【0013】[0013]

【実施例】図1に示す実施例は、溶解性鉄5mg/l、
溶解性マンガン0.5mg/lを含有する地下水を、マ
ンガン砂を敷設した反応槽で接触酸化析出後、透過膜で
除去し飲料水を造水する方法に関する。
EXAMPLE The embodiment shown in FIG.
The present invention relates to a method for producing drinking water by removing ground water containing 0.5 mg / l of soluble manganese in a reaction tank provided with manganese sand by catalytic oxidative precipitation and then removing the oxidized water with a permeable membrane.

【0014】原水管1から原水が流入する配管途中で、
適量(最終膜ろ過水で遊離残留塩素が0.1〜0.5m
g/l程度残る程度)の次亜塩素酸ナトリウム2が、注
入装置3により注入された後に反応槽4に流入する。こ
の反応槽4は、コーン状になつており、上部に行くほど
断面積を増大させ、ろ速LVを小さくすることにより、
この槽4内での懸濁物質の沈殿効果も出せるよう考慮さ
れている。
In the middle of the pipe through which the raw water flows from the raw water pipe 1,
Appropriate amount (free residual chlorine in final membrane filtered water is 0.1-0.5m
g / l of sodium hypochlorite 2) flows into the reaction tank 4 after being injected by the injection device 3. The reaction tank 4 is formed in a cone shape. The cross-sectional area increases toward the upper part and the filtration speed LV decreases,
Consideration has also been given to the effect of precipitating suspended substances in the tank 4.

【0015】なおマンガン以外の物質をほとんど含有し
ていないような原水の場合は、円柱形などのように上下
同様な断面積を有する形状とすることもある。次亜塩素
酸ナトリウム注入直後もしくは反応槽4内の早い時点で
溶解性鉄は酸化析出する。
In the case of raw water containing almost no substance other than manganese, the raw water may be formed in a shape having the same cross-sectional area as the top and bottom, such as a column. Immediately after the injection of sodium hypochlorite or at an early point in the reaction tank 4, the soluble iron is oxidized and precipitated.

【0016】反応槽4内に流入した原水は、ストレ−ナ
5及び小砂利支持層6を経由し、敷設されているマンガ
ン砂層7を通過接触する途中で、マンガン砂にコ−テイ
ングされた二酸化マンガンもしくは既に酸化析出した二
酸化マンガンを触媒として、塩素により酸化析出する。
その後反応槽4内を上昇し、通水樋8から一次処理水槽
9に流出する。一次処理水は透過膜加圧ポンプ10によ
り透過膜11に圧送され、膜ろ過後浄水となり、処理水
流出管12から流出する。
The raw water flowing into the reaction tank 4 passes through the strainer 5 and the small gravel support layer 6, passes through the manganese sand layer 7 laid, and contacts the manganese sand. Using manganese or manganese dioxide which has already been oxidized and precipitated as a catalyst, oxidized and precipitated with chlorine.
Thereafter, it rises in the reaction tank 4 and flows out of the water passage gutter 8 into the primary treatment water tank 9. The primary treated water is pumped to the permeable membrane 11 by the permeable membrane pressurizing pump 10, becomes purified water after membrane filtration, and flows out of the treated water outlet pipe 12.

【0017】反応槽4内では、原水中の懸濁物質や酸化
析出物質の一部が沈殿し、スラリ−状となることもある
が、これらのスラリ−内を通過時に、溶解性マンガンの
酸化析出を促進したり、高速凝集沈殿池と同様の効果に
より、原水中の懸濁物質除去を促進し、透過膜の粗ろ過
的な効果をもたらす。
In the reaction tank 4, some of the suspended solids and oxidized precipitates in the raw water precipitate and may form a slurry, but when passing through these slurries, oxidation of soluble manganese occurs. By promoting the precipitation and the same effect as the high-speed coagulation sedimentation basin, the removal of suspended substances in the raw water is promoted and the effect of the permeable membrane is roughly filtered.

【0018】なお反応槽4内にスラリ−が多量に蓄積し
た場合は、適時スラリ−排水弁13を開き、スラリ−配
水管14から系外に濃縮スラリ−を排出する。また反応
槽4内に排出しがたい沈殿物が堆積した場合や、マンガ
ン砂に多量にマンガンが付着した場合などは、ブロア−
15により圧搾空気を反応槽4内下部から吹き込み、マ
ンガン砂層7を流動化させ洗浄することも可能である。
If a large amount of slurry accumulates in the reaction tank 4, the slurry drain valve 13 is opened at an appropriate time, and the concentrated slurry is discharged from the slurry distribution pipe 14 to the outside of the system. In the case where sediment which cannot be discharged is deposited in the reaction tank 4 or a large amount of manganese adheres to the manganese sand, the blower is used.
With 15, compressed air can be blown from the lower part inside the reaction tank 4 to fluidize and wash the manganese sand layer 7.

【0019】次に図2に示す実施例において、前記図1
の実施例と同一又は等効の部分には同一符号を付してそ
の説明を省略するが、原水は前記例と同様に、反応槽4
で酸化析出した後、この反応槽4内を上昇する。反応槽
4内上方に懸吊した透過膜すなわち中空糸型精密ろ過膜
束16の二次側配管17を真空ポンプ18及び吸引水槽
19により減圧し、その圧力差を利用して膜ろ過する。
膜ろ過水は処理水流出管12から系外に流出する。なお
膜ろ過水量より多量の原水が流入した場合は、越流管2
0により系外に排出する。その他の作用は前記図1に示
した実施例におけると同様である。
Next, in the embodiment shown in FIG.
The same reference numerals are given to the same or equivalent effect parts as in the embodiment, and the description is omitted.
Then, the inside of the reaction tank 4 is raised. The pressure of the permeable membrane suspended above the inside of the reaction tank 4, that is, the secondary pipe 17 of the hollow fiber type microfiltration membrane bundle 16 is reduced by the vacuum pump 18 and the suction water tank 19, and membrane filtration is performed using the pressure difference.
The membrane filtered water flows out of the system from the treated water outflow pipe 12. If a large amount of raw water flows in from the membrane filtration water,
It is discharged out of the system by 0. Other operations are the same as those in the embodiment shown in FIG.

【0020】[0020]

【発明の方法】この発明の方法によれば、マンガン砂ろ
材は粒状であるので、上向流で原水を通水するとマンガ
ン砂ろ材粒子間が拡大し(ろ材層の膨張)、ろ材粒子が
浮遊状態となって、原水と接触しながら溶存マンガンを
酸化析出させ、析出された二酸化マンガンの大部分は吸
着されずに、マンガン砂ろ材間を通過して、懸濁物質と
共に反応層の上方に流出するので、上水道、工業用水
道、産業用水等を造水するのに有効である。
According to the method of the present invention, since the manganese sand filter medium is granular, when the raw water is passed in an upward flow, the space between the manganese sand filter medium particles expands (expansion of the filter medium layer), and the filter medium particles float. In this state, dissolved manganese is oxidized and precipitated while coming into contact with raw water, and most of the precipitated manganese dioxide is not adsorbed, but passes between manganese sand filter media and flows out of the reaction layer together with suspended solids. Therefore, it is effective in producing fresh water, industrial water, industrial water and the like.

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

【図1】この発明の一実施例の系統図である。FIG. 1 is a system diagram of one embodiment of the present invention.

【図2】この発明の他の実施例の系統図である。FIG. 2 is a system diagram of another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

4 反応槽 11,16 透過膜 4 Reaction tank 11, 16 Permeable membrane

フロントページの続き (51)Int.Cl.6 識別記号 FI C02F 9/00 502 C02F 9/00 502P 502R 503 503G 504 504B Continued on the front page (51) Int.Cl. 6 Identification code FI C02F 9/00 502 C02F 9/00 502P 502R 503 503G 504 504B

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 原水に含まれる溶存マンガンを除去する
方法において、原水に塩素系酸化剤を注入し、反応槽下
方に敷設したマンガン接触ろ材層を上向流で通過さ
せ、該ろ材層で溶存マンガンを析出させ、反応槽上方で
原水中の懸濁物質を沈降分離させた後、反応槽上方で沈
降分離できなかった原水中の懸濁物質及び前記析出させ
た溶存マンガンを透過膜でろ過することを特徴とする溶
存マンガンの除去方法。
1. A method of removing dissolved manganese contained in the raw water, the chlorine-based oxidizing agent is injected into the raw water passes a manganese sand contact filter media layer which is laid into the reaction vessel downwardly in upflow,該Rozai Dissolved manganese is precipitated in the layer, and the suspended matter in the raw water is settled and separated above the reaction tank. A method for removing dissolved manganese, characterized by filtering with manganese.
【請求項2】 前記請求項1において、前記透過膜を反
応槽上方に浸漬し、透過膜二次側とサイフォン水圧差も
しくは透過膜二次側を減圧することにより、原水中の懸
濁物質及び溶存マンガンを透過膜でろ過することを特徴
とする溶存マンガンの除去方法。
2. The method according to claim 1, wherein the permeable membrane is immersed in the upper portion of the reaction tank, and the pressure difference between the secondary side of the permeable membrane and the siphon water pressure or the secondary side of the permeable membrane is reduced. A method for removing dissolved manganese, comprising filtering dissolved manganese through a permeable membrane.
JP5206927A 1993-07-30 1993-07-30 Water filtration method containing dissolved manganese using permeable membrane Expired - Fee Related JP2772612B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5206927A JP2772612B2 (en) 1993-07-30 1993-07-30 Water filtration method containing dissolved manganese using permeable membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5206927A JP2772612B2 (en) 1993-07-30 1993-07-30 Water filtration method containing dissolved manganese using permeable membrane

Publications (2)

Publication Number Publication Date
JPH0739872A JPH0739872A (en) 1995-02-10
JP2772612B2 true JP2772612B2 (en) 1998-07-02

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JP (1) JP2772612B2 (en)

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KR101958285B1 (en) * 2017-06-30 2019-03-15 주식회사 미래지앤씨 Fluid filtration apparatus
JP6484355B2 (en) * 2018-01-23 2019-03-13 オルガノ株式会社 Iron / manganese-containing water treatment apparatus and treatment method

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JPH03151095A (en) * 1989-11-02 1991-06-27 Yokohama Metsukin Kogyo Kk Filtering device for manganese

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