JP2005131559A - Re-purification treatment method of tap water and re-purification treatment equipment therefor - Google Patents

Re-purification treatment method of tap water and re-purification treatment equipment therefor Download PDF

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JP2005131559A
JP2005131559A JP2003371373A JP2003371373A JP2005131559A JP 2005131559 A JP2005131559 A JP 2005131559A JP 2003371373 A JP2003371373 A JP 2003371373A JP 2003371373 A JP2003371373 A JP 2003371373A JP 2005131559 A JP2005131559 A JP 2005131559A
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water
activated carbon
treatment
tank
tap water
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Kosuke Takahashi
孝輔 高橋
Mitsumasa Murakami
光正 村上
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KAIHATSU KOGYO KK
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a re-purification treatment method of tap water capable of easily re-purifying tap water in large quantities, and re-purification treatment equipment. <P>SOLUTION: Tap water 10 is guided to an activated carbon adsorbing tank 2 filled with activated carbon having a particle size of a 0.1-2.5 mm to be subjected to activated carbon treatment and the activated carbon-treated water 12 is guided to a fine sand filtration device 3 to be subjected to microbial treatment. The tap water 10 before subjected to activated carbon treatment in the activated carbon adsorbing tank 2 may be subjected to aeration treatment in an aeration tank 1. The purified water 13 microbially treated in the fine sand filtration device 3 is stored in a water tank 4 to be subjected to ultraviolet sterilization treatment or chlorine injection treatment. The water of the water tank 4 is again returned to the activated carbon adsorbing tank 2 to be subjected to circulating water purifying treatment. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、水道水の再浄水処理方法及び再浄水処理設備に関する。   The present invention relates to a tap water repurification method and a repurification facility.

水道水をさらに浄化するものは浄水器と呼ばれている。この方法は水道水を活性炭ろ過後、膜ろ過する方法である。これによって水道水中の有機物、遊離塩素、クロロアミンなどを除去し、結果として異臭味のない浄水を得ている。しかしながら、この方法は台所の飲み水や鍋に入れる水を目的としており、浄水量も一日当たり10リットル程度である。   What purifies tap water further is called a water purifier. In this method, tap water is filtered through activated carbon and then membrane filtered. As a result, organic substances, free chlorine, chloroamine, etc. in tap water are removed, and as a result, purified water having no off-flavor is obtained. However, this method is intended for drinking water in the kitchen and water to be put in a pot, and the amount of purified water is about 10 liters per day.

一方、シャワーでカルキ臭を除去し、髪の変色を防ぐために、活性炭処理だけを行なう方法も実用化されている。活性炭はトリハロメタンの吸着能力は低いが、塩素除去の能力は高いことに注目した方法である。   On the other hand, a method in which only the activated carbon treatment is performed has been put into practical use in order to remove the odor of the salt in the shower and prevent discoloration of the hair. Activated charcoal is a method that pays attention to its low ability to adsorb trihalomethane but high ability to remove chlorine.

浄水器では機能高度化を掲げて、鉛除去、アルカリイオン水、酸性水製造の機能を有した高額な装置も作られている。
しかしながら浄水器はあくまでも飲み水と料理に使う水を目的としており、台所の食器洗浄水、風呂水、シャワー水、洗面水など家庭の大半の水を浄水しようとするものではない。そのため利用者の希望の一部しかかなえられていないのが現状である。
In purifiers, expensive devices with the functions of lead removal, alkaline ionized water, and acidic water production have been made.
However, the water purifier is intended only for drinking water and water used for cooking, and does not attempt to purify most household water such as kitchen dishwashing water, bath water, shower water, and wash water. Therefore, the present situation is that only a part of the user's wishes can be fulfilled.

高度浄水利用を風呂まで拡大する場合、結局家庭で使う全部の水道水を再浄水することが理想である。もちろん全ての家庭がこれを望むのであれば、水道局においてさらなる高度浄水を目指すべきであるが、現実の問題として、コストアップは避けられないのであるから、各家庭で浄水するのが順当である。   When extending the use of advanced water purification to baths, it is ideal to repurify all tap water used at home. Of course, if all households want this, the Waterworks Bureau should aim for further advanced water purification, but as a matter of fact, cost increases are inevitable, so it is appropriate to purify water in each household. .

家庭用の大半の水を再浄水する場合、単に現在の浄水器を大規模化するだけでは不十分である。それはコスト的問題が先ず上げられる。家庭用浄水器には膜ろ過が設けられているが、膜ろ過は基本的には逆洗しない。一方、浄水場では1時間毎に逆洗し、半年毎に薬品洗浄する。しかし、これを家庭用浄水器に求めることは実用的でない。   When repurifying most household water, it is not enough to simply scale up the current water purifier. That raises the cost problem first. Home water purifiers are equipped with membrane filtration, but membrane filtration is basically not backwashed. On the other hand, at the water purification plant, backwashing is performed every hour and chemicals are washed every six months. However, it is impractical to ask a household water purifier for this.

次に、単に活性炭で処理するだけで充分とするのは適当でない。活性炭はどのようなものでも吸着分離するのではなく、水に馴染みやすい有機物は一般的に除去が難しい。そこで、膜処理に代わるろ過方法を有し、活性炭で吸着し難い物質を分解除去する装置とシステムの開発が課題である。   Next, it is not appropriate to simply treat with activated carbon. Any activated carbon is not adsorbed and separated, and it is generally difficult to remove organic substances that are familiar to water. Therefore, the development of an apparatus and system that has a filtration method instead of membrane treatment and decomposes and removes substances that are difficult to adsorb with activated carbon is an issue.

水道水には赤水といって鉄が含まれていることがしばしばある。これは水道管のバクテリアが管を侵食して鉄を溶出するなどが原因である。現在の浄水器では溶解性の鉄を除去することが困難である。この赤水を濁りだけでなく溶解鉄も除去する装置やシステムの開発が望まれている。   Tap water is often called red water and contains iron. This is because bacteria in water pipes erode the pipes and elute iron. It is difficult to remove soluble iron with current water purifiers. Development of an apparatus and a system that removes dissolved iron as well as turbidity of red water is desired.

家庭などでは水道の使用は間欠的である。一方、正常なろ過を行なうためには常時あるいは一定速度以下で浄水しなければならない。この点が浄水器では一つの課題であった。すなわち、水道の1つの蛇口は最大20リットル/分程度利用するが、それに対応するためには同じ速度で浄水しなければならない。しかし現実は例えば2リットル/分である。必要量の1/10のみをろ過するのである。2リットル/分以上流してはならないが、それば利用者に任されているのである。したがって性能は保証されていないのである。   Water use is intermittent in homes. On the other hand, in order to perform normal filtration, water must be purified constantly or at a constant speed or less. This was one problem with the water purifier. That is, one tap of the water supply uses up to about 20 liters / minute, but in order to cope with it, water must be purified at the same speed. However, the reality is, for example, 2 liters / minute. Only 1/10 of the required amount is filtered. It should not flow more than 2 liters / minute, but it is left to the user. Therefore, performance is not guaranteed.

そこで本発明者は、特開2003−275782号公報(特許文献1)において、水中の有機物を微生物によって分解する細砂ろ過装置及び方法を提案しているが、水道水の再浄水に応用するには充分といえるものではない。
特開2003−275782号公報
Therefore, the present inventor has proposed a fine sand filtration apparatus and method for decomposing organic substances in water with microorganisms in Japanese Patent Laid-Open No. 2003-275882 (Patent Document 1). Is not enough.
JP 2003-275882 A

本発明は前記問題点を解決し、水道水の再浄水を多量にかつ容易に行える水道水の再浄水処理方法及び再浄水処理設備を提案するものである。   This invention solves the said problem, and proposes the repurification water treatment method and repurification water treatment equipment of the tap water which can perform repurification of tap water in large quantities and easily.

本発明者は上記課題を解決するために鋭意検討を重ねた結果、本発明に至ったものである。すなわち本発明は、水道水を粒径0.1〜2.5mmの活性炭を備えた活性炭吸着槽に導いて活性炭処理し、この活性炭処理水を細砂ろ過装置に導いて微生物処理することを特徴とする水道水の再浄水処理方法を要旨とするものである。   As a result of intensive studies to solve the above problems, the present inventor has arrived at the present invention. That is, the present invention is characterized in that tap water is introduced into an activated carbon adsorption tank equipped with activated carbon having a particle size of 0.1 to 2.5 mm and treated with activated carbon, and this activated carbon treated water is introduced into a fine sand filtration device for microbial treatment. The summary of the repurifying water treatment method is as follows.

この構成によると、前段の活性炭処理によって水道水に含まれるトリハロメタン、クロロアミン類、遊離塩素などを除去することができ、後段の微生物処理によって水道水に含まれる有機物を分解できるため、安全で美味しい水を安価にしかも多量に提供できる。   According to this configuration, trihalomethane, chloroamines, free chlorine, etc. contained in tap water can be removed by the activated carbon treatment in the previous stage, and organic substances contained in tap water can be decomposed by the microbial treatment in the latter stage. Can be provided at low cost and in large quantities.

また、活性炭吸着槽で活性炭処理する前の水道水に、1分〜3時間の曝気処理を施すことで、遊離塩素、クロロアミン類だけでなくトリハロメタンの除去能力を高めることができるだけでなく、その他諸々の低分子物質の除去が可能となり、さらに加えて赤水が発生した場合の鉄の酸化処理や、後段の生物処理において酸素が不足している場合の酸素供給が行なえるという効果が得られる。   In addition, the tap water before activated carbon treatment in the activated carbon adsorption tank is subjected to aeration treatment for 1 minute to 3 hours, so that not only free chlorine and chloroamines but also trihalomethane removal ability can be enhanced, and various others. In addition, it is possible to remove the low molecular weight substance, and in addition, it is possible to perform an iron oxidation process when red water is generated and an oxygen supply when oxygen is insufficient in a biological process at a later stage.

また、細砂ろ過装置で微生物処理した浄水に紫外線殺菌処理若しくは塩素注入処理を施すと、浄水中の無害な雑バクテリアまでも除去でき、より安全性を高めることができる。
さらに、細砂ろ過装置で微生物処理した浄水の少なくとも一部を再び活性炭吸着槽に戻して循環浄水処理すると、活性炭吸着槽と細砂ろ過装置が嫌気性になるのを抑制することができる。
In addition, when the purified water treated with microorganisms by the fine sand filtration device is subjected to ultraviolet sterilization treatment or chlorine injection treatment, even harmless bacteria in the purified water can be removed, and safety can be further improved.
Furthermore, when at least a part of the purified water treated with microorganisms by the fine sand filtration device is returned to the activated carbon adsorption tank again and the circulating water purification treatment is performed, the activated carbon adsorption tank and the fine sand filtration device can be prevented from becoming anaerobic.

また、本発明は、粒径0.1〜2.5mmの活性炭を備えた水道水を活性炭処理する活性炭吸着槽と、前記活性炭吸着槽で処理された活性炭処理水を微生物処理する細砂ろ過装置と、前記細砂ろ過装置で微生物処理された浄水を蓄える貯水槽とを有することを特徴とする水道水の再浄水処理設備を要旨とするものである。   In addition, the present invention is an activated carbon adsorption tank that performs activated carbon treatment on tap water including activated carbon having a particle size of 0.1 to 2.5 mm, and a fine sand filtration device that performs microorganism treatment on activated carbon treated water in the activated carbon adsorption tank. And a water tank for storing purified water that has been subjected to microbial treatment by the fine sand filtration device.

この再浄水処理設備を用いることで、本発明の再浄水処理方法を容易に実現できる。
また、活性炭吸着槽の前段には曝気槽を設けても良く、貯水槽には紫外線殺菌装置若しくは塩素注入装置のを設けた構成としても良い。さらに、貯水槽の浄水を活性炭吸着槽へ供給する配管を設け浄水を循環させるよう構成することもできる。
By using this repurified water treatment facility, the repurified water treatment method of the present invention can be easily realized.
In addition, an aeration tank may be provided in front of the activated carbon adsorption tank, and an ultraviolet sterilization apparatus or a chlorine injection apparatus may be provided in the water storage tank. Furthermore, it can also comprise the piping which supplies the purified water of a water storage tank to an activated carbon adsorption tank, and circulates purified water.

より詳細には、本発明の水道水の再浄水処理方法及び再浄水処理設備には、上記特許文献1に記載の細砂ろ過方法および装置を適用するが、水道水の再浄水処理において一番の問題は水道水中の消毒剤である。消毒剤は遊離塩素及びクロロアミンの結合塩素である。これがあるとバクテリアは繁殖できず単なるろ過器となる。そこで本発明においては、細砂ろ過装置の前段に活性炭吸着槽を置くこととする。活性炭は塩素類を吸着除去することが出来る。   In more detail, although the fine sand filtration method and apparatus of the said patent document 1 are applied to the repurification water treatment method and repurification water treatment equipment of the tap water of this invention, in the repurification water treatment of tap water, it is the most. The problem is disinfectant in tap water. The disinfectant is free chlorine and chloroamine combined chlorine. With this, the bacteria cannot propagate and become a simple filter. Therefore, in the present invention, an activated carbon adsorption tank is placed in front of the fine sand filter. Activated carbon can adsorb and remove chlorine.

もちろん、活性炭の塩素吸着には限度がある。そこで曝気を行なうことにした。曝気は塩素、クロロアミン類だけでなく、トリハロメタンの除去に効果がある。その他、諸々の低分子物質を除去すると共に、酸素が不足している場合、酸素を供給する効果もある。   Of course, there is a limit to the adsorption of chlorine by activated carbon. I decided to do aeration. Aeration is effective in removing not only chlorine and chloroamines but also trihalomethanes. In addition to removing various low-molecular substances, there is an effect of supplying oxygen when oxygen is insufficient.

細砂ろ過装置は上記特許文献1に記載されたものを基本し、0.25mm以下の細砂を用いる。水道水に含まれる有機物は少なく、赤水は常時ではない。そのため砂粒表面に発生するろ過膜の発達は不十分である。したがって細砂を使わなければならない。   The fine sand filtration device basically uses the one described in Patent Document 1, and uses fine sand of 0.25 mm or less. There are few organic substances in tap water, and red water is not always. Therefore, the development of the filtration membrane generated on the sand grain surface is insufficient. Therefore, fine sand must be used.

細砂槽の逆洗は行なうことを基本とする。逆洗しなくても、通常、長期間目詰まりすることはないが、水道水質によっては容易に目詰まりを起こす。目詰まりは水をさらに浄水している証拠であるが、現実問題として細砂表面を削り取るか、逆洗で泥を除去する必要がある。   Backwashing of the fine sand tank is basically performed. Even without backwashing, clogging usually does not occur for a long time, but clogging easily occurs depending on the quality of tap water. Clogging is evidence that the water is being further purified, but it is necessary to scrape the fine sand surface or remove the mud by backwashing as a real problem.

逆洗する場合は、必ずしも自動逆洗装置を設置する必要はない。配管だけしておくことで、必要な場合、手動で逆洗することも出来る。
浄水器では使用するたびに必要量だけ浄水する。そのため浄水量が蛇口1個であっても必要量の1/10程度であった。これでは安心して使用することが出来ない。本発明では、細砂を通した水は浄水として貯水することを基本とする。浄水器の場合は必要に応じて浄水するのであるが、これでは風呂やシャワーには対応できない。一度に多量の水を使用するのに対応した細砂ろ過を用いるとなれば、設備が相当に大きくなる。そこで、貯水槽を設ける。貯水槽の容量は利用の時間的パターンによって異なる。一度に短時間に多量に使用し、後は使用しない場合は貯水容量は大きく取る。
When backwashing, it is not always necessary to install an automatic backwashing device. If you need only piping, you can backwash manually if necessary.
The water purifier purifies only the required amount each time it is used. Therefore, even if the amount of purified water was one faucet, it was about 1/10 of the required amount. This cannot be used with confidence. In the present invention, the water passing through the fine sand is basically stored as purified water. In the case of a water purifier, water is purified as necessary, but this cannot be used for baths or showers. If fine sand filtration is used to handle a large amount of water at once, the equipment will be considerably larger. Therefore, a water tank is provided. The capacity of the water tank varies with the time pattern of use. Use a large amount of water in a short time at a time, and take a large water storage capacity when not using it later.

水利用パターンは、家庭の場合、平均化されることはない。真夜中から朝は全く利用しないのが普通であるし、日中もほとんど利用しない場合もある。このような場合は水道水流入は止める。しかし単に止めただけでは問題が発生する。   Water use patterns are not averaged in the home. It is normal not to use at all from midnight to morning, and there are also cases where it is rarely used during the day. In such a case, stop inflow of tap water. But simply turning off causes problems.

活性炭吸着槽と細砂ろ過装置の細砂ろ過槽にはバクテリアが繁殖している。水流が停止するとバクテリアは部分的に死滅し、嫌気性になることがある。そこで、一度浄水した水を再循環することとした。水を使わなくても使っても水を流し続けるのである。貯水槽の水量が不足した場合は水道水を流し、十分貯留した場合は貯水槽の浄水、若しくは細砂ろ過処理を施した直後の水を再循環するのである。この再循環システムによって活性炭吸着槽と細砂ろ過槽は嫌気性になることはない。   Bacteria are growing in the activated carbon adsorption tank and the fine sand filter tank of the fine sand filter. When the water flow stops, the bacteria can partially die and become anaerobic. Therefore, we decided to recycle the water once purified. It keeps flowing even if you don't use water. When the amount of water in the water storage tank is insufficient, tap water is poured, and when it is sufficiently stored, the water in the water storage tank is purified or the water just after the fine sand filtration is recirculated. This recirculation system does not make the activated carbon adsorption tank and the fine sand filtration tank anaerobic.

貯水槽の浄水は病原菌を有する可能性はほとんどないためそのまま蛇口に送ることが出来る。この場合美味しさそのままの水になる。ただし、全く無菌ということではない。細砂ろ過した場合、無害な一般バクテリアが少量であるが含まれる。バクテリアが含まれていても餌となる有機物はないから繁殖することはないが、長期になると幾らかの無害な雑バクテリアが生存するようになる。   The water in the water tank can be sent to the faucet as it is because there is almost no possibility of having pathogenic bacteria. In this case, the water becomes delicious. However, it is not completely sterile. In case of fine sand filtration, it contains a small amount of harmless general bacteria. Even if it contains bacteria, it will not reproduce because there is no organic matter to feed on, but some harmless miscellaneous bacteria will survive over time.

菌を排除したい場合は貯水槽に紫外線灯(殺菌灯)を設置する。紫外線量は標準的な値でよい。またオゾン線は使用しない。目的はあくまでもバクテリアの除去である。
紫外線によるバクテリアの除去が可能なのは、貯水槽内である。貯水槽に連結される配管内には紫外線を照射することが出来ないため、管内まで殺菌したい場合には、前記した紫外線処理の代わりに塩素消毒をする。水道水には塩素が入っているが浄水後再び塩素を入れるというものである。この場合は水道水と異なり、既にトリハロメタン、アンモニア、有機物などは除去されているから、異臭味は発生しない。塩素臭であるクロロアミンが無いことも特徴である。
If you want to eliminate germs, install a UV lamp (sterilization lamp) in the water tank. The amount of ultraviolet rays may be a standard value. Also, ozone rays are not used. The goal is to remove bacteria.
Bacteria can be removed by ultraviolet rays in the water tank. Since it is impossible to irradiate the pipe connected to the water storage tank with ultraviolet rays, chlorine sterilization is performed instead of the aforementioned ultraviolet treatment when it is desired to sterilize the inside of the pipe. Although tap water contains chlorine, it is refilled with chlorine after clean water. In this case, unlike tap water, trihalomethane, ammonia, organic substances, etc. have already been removed, so no off-flavor is produced. It is also characterized by the absence of chloroamine, a chlorine odor.

本発明の水道水の再浄水処理方法及び設備によると、水道水の再浄水を容易に行なうことができ、安全で美味しい水を多量でかつ安価に作ることができる。このような処理システムは、特に都市の河川水や湖沼水を原水とした上水道水の再浄水に効果的である。また、市販の浄水器とは異なり、一度に多量の水を使用することが出来るため、風呂、シャワーなどにも使えるものである。さらに、家庭用の水だけでなく、超純水の製造や工業用水の浄化にも適用可能である。   According to the method and facility for repurifying tap water of the present invention, repurification of tap water can be performed easily, and a large amount of safe and delicious water can be produced at low cost. Such a treatment system is particularly effective for the repurification of tap water using the river water and lake water of the city as raw water. In addition, unlike commercial water purifiers, a large amount of water can be used at one time, so it can also be used for baths and showers. Furthermore, it can be applied not only to household water but also to production of ultrapure water and purification of industrial water.

以下に本発明の一実施の形態を図面に基づいて説明する。
図1において、曝気槽1に供給された水道水10は、曝気槽1の底部に設けられた曝気装置5によって曝気処理が施される。曝気処理された曝気処理水11は活性炭吸着槽2に導かれ、活性炭吸着槽2に充填された粒径0.1〜2.5mmの活性炭6を通過することによって、前段の曝気処理との効果もあいまって水中のトリハロメタン、クロロアミン及び遊離塩素が除去された活性炭処理水12となる。
Hereinafter, an embodiment of the present invention will be described with reference to the drawings.
In FIG. 1, tap water 10 supplied to the aeration tank 1 is subjected to an aeration process by an aeration apparatus 5 provided at the bottom of the aeration tank 1. The aerated treated water 11 subjected to aeration treatment is guided to the activated carbon adsorption tank 2 and passes through the activated carbon 6 having a particle size of 0.1 to 2.5 mm filled in the activated carbon adsorption tank 2, so that the effect of the previous aeration process is achieved. In combination, the activated carbon-treated water 12 from which trihalomethane, chloroamine and free chlorine in the water have been removed is obtained.

活性炭処理水12は細砂ろ過装置3へと導かれ、細砂ろ過装置3の細砂ろ過槽3aに設けられた細砂ろ過層7に含まれる微生物によって、処理水中の有機物が分解処理される。得られた浄水(細砂ろ過水)13は、貯水槽4に送られる。   The activated carbon treated water 12 is guided to the fine sand filtration device 3, and the organic matter in the treated water is decomposed by microorganisms contained in the fine sand filtration layer 7 provided in the fine sand filtration tank 3a of the fine sand filtration device 3. . The obtained purified water (fine sand filtered water) 13 is sent to the water storage tank 4.

貯水槽4には紫外線ランプ8が設けられており、浄水中の雑バクテリアが殺菌される。殺菌処理された処理水は、浄水14として家庭の飲料水や風呂水などとして使用される。なお、この貯水槽4には、前段の活性炭吸着槽2に繋がる配管が設けられており、この配管を通って貯水槽4に蓄えられた水の一部が再び活性炭吸着槽2に供給される。このように浄水が循環水19として常に系内を循環することで、活性炭吸着槽2と細砂ろ過槽3a中の微生物の死滅を抑制できる。   The water tank 4 is provided with an ultraviolet lamp 8 to sterilize miscellaneous bacteria in the purified water. The sterilized treated water is used as domestic drinking water or bath water as purified water 14. The water tank 4 is provided with a pipe connected to the activated carbon adsorption tank 2 in the previous stage, and a part of the water stored in the water tank 4 is supplied to the activated carbon adsorption tank 2 again through this pipe. . Thus, the purified water always circulates in the system as the circulating water 19 so that the killing of microorganisms in the activated carbon adsorption tank 2 and the fine sand filtration tank 3a can be suppressed.

なお、図中の9は、曝気槽1、活性炭吸着槽2、細砂ろ過槽3a、貯水槽4に設けられた覆蓋である。また、15、16は活性炭吸着槽2を逆洗するときの活性炭用逆洗水の流れを示すものであり、17、18は細砂ろ過槽3aを逆洗するときの細砂用逆洗水の流れを示すものである。また、この水道水の再浄水処理設備において曝気槽1は省いても良い。   In addition, 9 in the figure is a cover provided in the aeration tank 1, the activated carbon adsorption tank 2, the fine sand filtration tank 3 a, and the water storage tank 4. 15 and 16 indicate the flow of backwash water for activated carbon when the activated carbon adsorption tank 2 is backwashed, and 17 and 18 indicate backwash water for fine sand when the fine sand filtration tank 3a is backwashed. It shows the flow. Moreover, the aeration tank 1 may be omitted in this tap water repurification treatment facility.

以下、上記した水道水の再浄水処理設備の詳細を説明する。
水道水10は曝気槽1で処理される。曝気時間は長い程良いが実用的には3時間が限度である。最短時間にも特に制約はないが、曝気初期の急速な物質の散気を考えると、1分以上で効果がある。したがって、本発明においては、曝気時間を1分〜2時間とすることが好ましい。
The details of the above-described tap water repurification treatment facility will be described below.
The tap water 10 is processed in the aeration tank 1. The longer the aeration time, the better, but 3 hours is the practical limit. There is no particular restriction on the minimum time, but considering the rapid diffusion of the substance at the beginning of aeration, it is effective in 1 minute or more. Therefore, in the present invention, the aeration time is preferably 1 minute to 2 hours.

曝気槽1で除去される物質は低分子化合物のトリハロメタン、消毒剤である遊離塩素およびクロロアミンの結合塩素などである。全塩素は十分曝気するならば2/3程度除去される。トリハロメタンも曝気除去しやすく、後段の活性炭での除去が不完全になりやすいことを考えると意味が大きい。   Substances to be removed in the aeration tank 1 are low molecular weight compounds such as trihalomethane, disinfectant free chlorine and chloroamine combined chlorine. If the total chlorine is sufficiently aerated, about 2/3 is removed. Trihalomethane is also easy to remove by aeration, and it makes sense to consider that removal with activated carbon in the latter stage tends to be incomplete.

その他、酸素供給も重要である。赤水の場合、水道水には2価の鉄イオンが溶解していることが多いが、先ずは酸素を供給し、鉄の酸化を促す必要がある。
曝気処理水11は次段の活性炭処理を受ける。活性炭吸着槽2の大きさは使用する活性炭の種類にもよるが、概ね後段の細砂ろ過槽3aに較べ数分の1程度である。活性炭吸着槽2の意味は遊離塩素とクロロアミンの結合塩素とを除去することが第1目的である。消毒剤が残っていては後段の細砂ろ過の生物処理が働かなくなる。活性炭は塩素除去能力は高いので、塩素除去のみを目的とするときは、さらに10分の1程度でよい。
In addition, oxygen supply is important. In the case of red water, divalent iron ions are often dissolved in tap water, but first it is necessary to supply oxygen to promote oxidation of iron.
The aerated treated water 11 is subjected to the next activated carbon treatment. Although the size of the activated carbon adsorption tank 2 depends on the type of activated carbon used, it is approximately a fraction of that of the fine sand filtration tank 3a in the subsequent stage. The first purpose of the activated carbon adsorption tank 2 is to remove free chlorine and bound chlorine of chloroamine. If the disinfectant remains, the biological treatment of fine sand filtration in the latter stage will not work. Since activated carbon has a high chlorine removal capability, it may be about 1/10 when the purpose is only chlorine removal.

曝気槽1を省いた場合は活性炭を多く入れなければならない。特に曝気槽1を使わず、かつトリハロメタン除去を行なう場合は、特に活性炭量を増やす必要がある。
活性炭の粒径は0.1〜2.5mmである。粒径が2.5mm(10メッシュ)より大きくなると急激に吸着能力が低下する。
When the aeration tank 1 is omitted, a large amount of activated carbon must be added. In particular, when the aeration tank 1 is not used and trihalomethane removal is performed, it is necessary to increase the amount of activated carbon particularly.
The particle size of the activated carbon is 0.1 to 2.5 mm. When the particle size is larger than 2.5 mm (10 mesh), the adsorption capacity is rapidly lowered.

粒径は小さいほど吸着力が大であるとしても限度がある。0.1mm以下ではろ過機能が大となり、しばしば逆洗しなければならない。活性炭吸着槽2は細砂ろ過槽3aに較べ小型であるから、特に逆洗頻度が高くなるため実用的とはいえなくなる。   There is a limit even if the adsorption power is large as the particle size is small. Below 0.1 mm, the filtration function becomes large and often has to be backwashed. Since the activated carbon adsorption tank 2 is smaller than the fine sand filtration tank 3a, it becomes impractical because the frequency of backwashing is particularly high.

活性炭処理水12は、細砂ろ過を受ける。細砂ろ過速度は2〜100m/日である。細砂は概ね有効径0.05〜0.2mmである。装置概略及びその浄水効果は特許文献1の通りである。   The activated carbon treated water 12 is subjected to fine sand filtration. The fine sand filtration rate is 2 to 100 m / day. Fine sand generally has an effective diameter of 0.05 to 0.2 mm. The outline of the apparatus and its water purification effect are as described in Patent Document 1.

逆洗装置は原則として活性炭吸着槽2、細砂ろ過装置3の両方に必要である。活性炭吸着槽2では粒径を2〜2.5mmと大きくした場合は、目詰まりする前に吸着能力が低下し、活性炭を交換するので、その場合は逆洗装置を省くことが出来る。   In principle, the backwashing device is necessary for both the activated carbon adsorption tank 2 and the fine sand filtration device 3. In the activated carbon adsorption tank 2, when the particle size is increased to 2 to 2.5 mm, the adsorption capability is lowered before clogging and the activated carbon is replaced. In this case, the backwash device can be omitted.

逆洗装置は必ずしも自動化する必要はない。逆洗頻度は水道水の水質にもよるが、概ね2年以上に1回である。したがって、定期点検時に手動で逆洗を行なうことで対応可能である。逆洗水は活性炭吸着槽2では水道水、細砂ろ過槽3aでは活性炭処理水12又は貯水槽4の浄水を用いることが出来る。   The backwash device need not be automated. The frequency of backwashing is approximately once every two years or more, although it depends on the quality of tap water. Therefore, it can be dealt with by backwashing manually at the time of periodic inspection. As the backwash water, tap water can be used in the activated carbon adsorption tank 2, and purified water from the activated carbon treated water 12 or the water storage tank 4 can be used in the fine sand filtration tank 3 a.

本発明は貯水槽4を有し、常時浄水するシステムを採用している。そのため浄水装置が小型であっても時間的な使用量変化にも対応できる。家庭の設備を例にとると、例えば水槽の容量は1mである。それに対して浄水量は100〜150リットル/時である。家庭では実質10時間近く水道水を使用しないことがある。この間に浄水し、貯水槽4を満杯とする。 The present invention employs a system that has a water tank 4 and constantly purifies water. Therefore, even if the water purifier is small, it can cope with changes in usage over time. Taking household equipment as an example, for example, the capacity of the aquarium is 1 m 3 . On the other hand, the amount of purified water is 100 to 150 liters / hour. At home, tap water may not be used for nearly 10 hours. During this time, the water is purified and the water tank 4 is filled.

貯水槽4の水はポンプにて蛇口に送られる。その一部は後述の循環水19となる。
貯水槽4が満杯となった場合、もはや浄水は不要である。しかしながら、本発明では、活性炭吸着槽2と細砂ろ過槽3aの何れもバクテリアが繁殖し、ろ過膜を生成している。この槽の流れが停止すれば、ろ過膜の死滅が起こる場合がある。そこで、貯水槽4の浄水を活性炭吸着槽2に循環することで解決した。貯水槽4が必要量を超えたならば、水道水バルブを停止し、循環バルブを開けるのである。循環水量は定常浄水速度が好ましい。ポンプ動力を考え、循環水量を1/2程度にすることも出来る。
The water in the water storage tank 4 is sent to the faucet by a pump. A part of it becomes the circulating water 19 described later.
When the water tank 4 is full, the water purification is no longer necessary. However, in the present invention, bacteria are propagated in both the activated carbon adsorption tank 2 and the fine sand filtration tank 3a to produce a filtration membrane. If the flow of this tank stops, the filter membrane may die. Then, it solved by circulating the purified water of the water storage tank 4 to the activated carbon adsorption tank 2. If the water tank 4 exceeds the required amount, the tap water valve is stopped and the circulation valve is opened. The amount of circulating water is preferably a steady water purification rate. Considering pump power, the circulating water volume can be reduced to about 1/2.

貯水槽4の殺菌や消毒は行なうことが好ましい。最近は欧州などでは水道水を無塩素とする試みがある。その意味では家庭の設備の時は必ずしも消毒や殺菌が必須条件ではない。   The water tank 4 is preferably sterilized and disinfected. Recently, there are attempts to make tap water chlorine-free in Europe. In that sense, disinfection and sterilization are not necessarily required for household equipment.

塩素殺菌する場合は、循環水19は貯水槽4の水は使えない。細砂ろ過した浄水13をそのまま活性炭吸着槽2に循環する。
紫外線で殺菌することも出来る。この場合は貯水槽4に紫外線ランプ8を入れるが、この水を循環水19とすることが出来る。蛇口用ポンプと循環水ポンプを共用できる。
In the case of chlorine sterilization, the circulating water 19 cannot use the water in the water storage tank 4. The fine water-filtered water 13 is circulated to the activated carbon adsorption tank 2 as it is.
It can be sterilized with ultraviolet rays. In this case, an ultraviolet lamp 8 is placed in the water storage tank 4, and this water can be used as the circulating water 19. The faucet pump and circulating water pump can be shared.

次に実施例によって、この発明をさらに詳細に説明する。
実施例1
15リットル容器に12リットル水道水を入れ、空気量1.75リットル/分で曝気した。その結果、遊離塩素は10分で22%、30分で50%、120分で72%除去された。全塩素は10分で33%、30分で41%除去された。この例では水深は21cmであった。したがって水深を1mとすれば1/5程度の時間でこれだけの効果が得られる。すなわち最短曝気時間は2分程度で10分程度の効果があることになる。さらに曝気量を増やせば効果を高めることが出来るから、曝気の最短時間は約1分となる。
実施例2
活性炭の粒径とトリハロメタンの除去能の試験を行なった。ヤシガラ活性炭を4〜10メッシュ、8〜32メッシュ、30〜60メッシュとし、400ミリリットル用いた。これに水道水を5リットル/分の速度で流した。最初の5時間の平均トリハロメタン除去率はそれぞれ、35%、76%、98%であった。このことから活性炭は粒径が小さいほど良く、最大粒径は10メッシュ程度であることが判明した。
実施例3
塩ビ塔に、0.05〜0.11mm粒径の微細砂を10cm入れた。ろ過速度を30ミリリットル/日とした。ろ過損失水頭は35cmであった。ろ過速度10m/日とすると計算では損失水頭は10cm程度になる。したがって細砂ろ過ではこのような砂を用いることが出来る。しかし活性炭では、槽が小さくろ過速度も高いことを考えると0.1mm以上の大きさが好ましいことになる。
実施例4
細砂ろ過でろ過速度42m/日で処理した水は水道水以上の水であるが、これをろ過速度10m/日で細砂緩速ろ過を行なった。その結果、過マンガン酸消費量は50%になった。このことから細砂ろ過を行なえば、通常の急速ろ過によって作られた水道水は過マンガン酸消費量が50%以上の除去率を有することが明らかとなった。すなわち有機物を半減する能力がある。特に細砂ろ過は活性炭が吸着し難い水溶性成分の分解に適しており、活性炭−細砂ろ過は良いシステムであることが分かる。
実施例5
市販の浄水器の性能検査を行なった。仕様は活性炭約500ミリリットル、浄水速度2リットル/分である。この速度で浄水したところ2000リットル当たりからトリハロメタンの漏出が始まった。この値は仕様書とほぼ一致した。塩素はそれより遥に多く少なくとも5倍以上ろ過が可能であるが途中で中止した。仕様によれば塩素に対しては10倍以上であった。このことからトリハロメタン対策としては曝気による除去が効果的であることが分かる。
実施例6
建物の水道水で赤水が発生するところがあるので、この水を曝気処理と活性炭処理した後、細砂ろ過を行なった。そのろ過水は鉄濃度は0.02mg/リットル以下と完全に除去されていた。
Next, the present invention will be described in more detail by way of examples.
Example 1
12 liters of tap water was placed in a 15 liter container and aerated at an air volume of 1.75 liters / minute. As a result, free chlorine was removed by 22% in 10 minutes, 50% in 30 minutes, and 72% in 120 minutes. Total chlorine was removed at 33% in 10 minutes and 41% in 30 minutes. In this example, the water depth was 21 cm. Therefore, if the water depth is 1 m, such an effect can be obtained in about 1/5 time. That is, the shortest aeration time is about 2 minutes, and the effect is about 10 minutes. If the amount of aeration is further increased, the effect can be enhanced, so the shortest time for aeration is about 1 minute.
Example 2
The activated carbon particle size and trihalomethane removal ability were tested. Coconut activated carbon was made into 4-10 mesh, 8-32 mesh, 30-60 mesh, and 400 ml was used. Tap water was allowed to flow at a rate of 5 liters / minute. The average trihalomethane removal rates for the first 5 hours were 35%, 76% and 98%, respectively. From this, it was found that the activated carbon is better as the particle size is smaller, and the maximum particle size is about 10 mesh.
Example 3
10 cm of fine sand having a particle diameter of 0.05 to 0.11 mm was placed in a vinyl chloride tower. The filtration rate was 30 ml / day. The filtration loss head was 35 cm. When the filtration rate is 10 m / day, the loss head is about 10 cm in the calculation. Therefore, such sand can be used in fine sand filtration. However, for activated carbon, a size of 0.1 mm or more is preferable considering that the tank is small and the filtration rate is high.
Example 4
Water treated by fine sand filtration at a filtration rate of 42 m / day is water higher than tap water, and this was subjected to fine sand slow filtration at a filtration rate of 10 m / day. As a result, the permanganate consumption was 50%. From this fact, it became clear that tap water produced by normal rapid filtration has a removal rate of permanganate consumption of 50% or more if fine sand filtration is performed. That is, it has the ability to halve organic matter. In particular, fine sand filtration is suitable for the decomposition of water-soluble components that are difficult to adsorb activated carbon, and it can be seen that activated carbon-fine sand filtration is a good system.
Example 5
A commercial water purifier was tested for performance. The specifications are about 500 milliliters of activated carbon and a water purification rate of 2 liters / minute. When water was purified at this rate, leakage of trihalomethane started from around 2000 liters. This value almost agreed with the specification. Chlorine is much more than that, and at least 5 times more can be filtered, but it was stopped halfway. According to the specifications, it was more than 10 times with respect to chlorine. This shows that removal by aeration is effective as a countermeasure against trihalomethane.
Example 6
Since red water is generated in the building tap water, this water was subjected to aeration treatment and activated carbon treatment, followed by fine sand filtration. The filtered water was completely removed with an iron concentration of 0.02 mg / liter or less.

本発明の一実施の形態における水道水の再浄水装置の構成を示す模式図である。It is a mimetic diagram showing the composition of the tap water repurification device in one embodiment of the present invention.

符号の説明Explanation of symbols

1 曝気槽
2 活性炭吸着槽
3 細砂ろ過装置
3a 細砂ろ過槽
4 貯水槽
5 曝気装置
6 活性炭
7 細砂ろ過層
8 紫外線ランプ
9 覆蓋
10 水道水
11 曝気処理水
12 活性炭処理水
13 浄水(細砂ろ過水)
14 浄水
15 活性炭用逆洗水
16 活性炭用逆洗水
17 細砂用逆洗水
18 細砂用逆洗水
19 循環水
DESCRIPTION OF SYMBOLS 1 Aeration tank 2 Activated carbon adsorption tank 3 Fine sand filtration apparatus 3a Fine sand filtration tank 4 Water storage tank 5 Aeration apparatus 6 Activated carbon 7 Fine sand filtration layer 8 Ultraviolet lamp 9 Cover 10 Tap water 11 Aerated treatment water 12 Activated carbon treatment water 13 Purified water (fine Sand filtration water)
14 Clean water 15 Backwash water for activated carbon 16 Backwash water for activated carbon 17 Backwash water for fine sand 18 Backwash water for fine sand 19 Circulating water

Claims (8)

水道水を粒径0.1〜2.5mmの活性炭を備えた活性炭吸着槽に導いて活性炭処理し、この活性炭処理水を細砂ろ過装置に導いて微生物処理することを特徴とする水道水の再浄水処理方法。 Tap water is introduced into an activated carbon adsorption tank equipped with activated carbon having a particle size of 0.1 to 2.5 mm and treated with activated carbon, and the activated carbon treated water is introduced into a fine sand filter and treated with microorganisms. Re-purifying water treatment method. 活性炭吸着槽で活性炭処理する前の水道水に、1分〜3時間の曝気処理を施すことを特徴とする請求項1記載の水道水の再浄水処理方法。 The tap water before the activated carbon treatment in the activated carbon adsorption tank is subjected to an aeration treatment for 1 minute to 3 hours. 細砂ろ過装置で微生物処理した浄水に紫外線殺菌処理若しくは塩素注入処理を施すことを特徴とする請求項1または2記載の水道水の再浄水処理方法。 The method for repurifying tap water according to claim 1 or 2, wherein the purified water subjected to microorganism treatment with a fine sand filter is subjected to ultraviolet sterilization treatment or chlorine injection treatment. 細砂ろ過装置で微生物処理した浄水の少なくとも一部を再び活性炭吸着槽に戻して循環浄水処理することを特徴とする請求項1から3のいずれか1項記載の水道水の再浄水処理方法。 The repurified water treatment method for tap water according to any one of claims 1 to 3, wherein at least a part of the purified water subjected to the microorganism treatment by the fine sand filter is returned to the activated carbon adsorption tank to perform the circulating water purification treatment. 粒径0.1〜2.5mmの活性炭を備えた水道水を活性炭処理する活性炭吸着槽と、前記活性炭吸着槽で処理された活性炭処理水を微生物処理する細砂ろ過装置と、前記細砂ろ過装置で微生物処理された浄水を蓄える貯水槽とを有することを特徴とする水道水の再浄水処理設備。 An activated carbon adsorption tank for treating activated water with tap water having a particle size of 0.1-2.5 mm, a fine sand filter for microbial treatment of activated carbon treated in the activated carbon adsorption tank, and the fine sand filtration A tap water repurification facility characterized by having a water storage tank for storing purified water that has been microbially treated by the apparatus. 活性炭吸着槽の前段に曝気槽を設けたことを特徴とする請求項5記載の水道水の再浄水処理設備。 6. The tap water repurification facility according to claim 5, wherein an aeration tank is provided in front of the activated carbon adsorption tank. 貯水槽に紫外線殺菌装置若しくは塩素注入装置を設けたことを特徴とする請求項5または6記載の水道水の再浄水処理設備。 The repurification treatment facility for tap water according to claim 5 or 6, wherein an ultraviolet sterilization device or a chlorine injection device is provided in the water storage tank. 貯水槽の浄水を活性炭吸着槽へ供給する配管を設け浄水を循環させるよう構成したことを特徴とする請求項5から7のいずれか1項記載の水道水の再浄水処理設備。 8. The tap water repurification treatment facility according to any one of claims 5 to 7, wherein a pipe for supplying purified water from the water storage tank to the activated carbon adsorption tank is provided to circulate the purified water.
JP2003371373A 2003-10-31 2003-10-31 Re-purification treatment method of tap water and re-purification treatment equipment therefor Pending JP2005131559A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101159512B1 (en) 2011-09-29 2012-07-03 주식회사 미드니 Groundwater purifying apparatus having a sterilizer for removing harmful microorganisms including norovirus and method thereof
KR101289020B1 (en) 2013-03-14 2013-07-23 주식회사 퓨어엔비텍 Apparatus for recycling waste toilet water and method for recycling waste toilet water using the same
JP2015503442A (en) * 2011-12-22 2015-02-02 スリーエム イノベイティブ プロパティズ カンパニー Filtration media containing metal sulfides
CN107758924A (en) * 2017-11-08 2018-03-06 许伟琦 A kind of medical sewage processing method for preventing carcinogen and inorganic agent
CN111302549A (en) * 2020-04-03 2020-06-19 中国华能集团清洁能源技术研究院有限公司 Electrochemical pretreatment system and method for circulating water sewage

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101159512B1 (en) 2011-09-29 2012-07-03 주식회사 미드니 Groundwater purifying apparatus having a sterilizer for removing harmful microorganisms including norovirus and method thereof
JP2015503442A (en) * 2011-12-22 2015-02-02 スリーエム イノベイティブ プロパティズ カンパニー Filtration media containing metal sulfides
KR101289020B1 (en) 2013-03-14 2013-07-23 주식회사 퓨어엔비텍 Apparatus for recycling waste toilet water and method for recycling waste toilet water using the same
CN107758924A (en) * 2017-11-08 2018-03-06 许伟琦 A kind of medical sewage processing method for preventing carcinogen and inorganic agent
CN107758924B (en) * 2017-11-08 2021-04-30 许伟琦 Medical sewage treatment method and treatment agent for preventing carcinogenic substances
CN111302549A (en) * 2020-04-03 2020-06-19 中国华能集团清洁能源技术研究院有限公司 Electrochemical pretreatment system and method for circulating water sewage

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