JPH0725995U - Advanced water treatment equipment - Google Patents
Advanced water treatment equipmentInfo
- Publication number
- JPH0725995U JPH0725995U JP6145793U JP6145793U JPH0725995U JP H0725995 U JPH0725995 U JP H0725995U JP 6145793 U JP6145793 U JP 6145793U JP 6145793 U JP6145793 U JP 6145793U JP H0725995 U JPH0725995 U JP H0725995U
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- Prior art keywords
- water
- activated carbon
- ozone
- circulating
- hot water
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- Treatment Of Water By Oxidation Or Reduction (AREA)
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Abstract
(57)【要約】
【目的】 安価で簡単な構成により、殺菌効果を得ると
共に、活性炭の寿命を延長する。
【構成】 本装置は、循環水にオゾン発生装置1で発生
したオゾンを注入した後、活性炭濾過層2aを有する濾
過装置2に循環水を通して処理する装置であり、循環水
を85°C位まで加熱して熱湯にするヒータ3と、加熱
された水を循環水の通る方向とは反対の方向から活性炭
濾過層に通す管路4と、更に、高架水槽5、この中の水
を循環させるためのポンプ6、三方切換電磁弁7、開閉
電磁弁8、9、10、温度センサ11、循環清浄配管
系、逆洗配管系等を備えている。
【効果】 オゾン処理を含む上水高度処理と熱湯逆洗と
を組み合わせることにより、紫外線殺菌装置が不要にな
り、活性炭の寿命が延長し、上水高度処理装置の経済性
が向上する。
(57) [Summary] [Purpose] The sterilization effect is obtained and the life of activated carbon is extended by an inexpensive and simple structure. [Structure] This device is a device for injecting ozone generated by an ozone generator 1 into circulating water and then treating the circulating water by passing the circulating water through a filtering device 2 having an activated carbon filter layer 2a. A heater 3 for heating into hot water, a conduit 4 for passing the heated water through the activated carbon filtration layer from a direction opposite to the direction of circulating water, and an elevated water tank 5, for circulating the water therein. The pump 6, the three-way switching solenoid valve 7, the opening / closing solenoid valves 8, 9, 10, the temperature sensor 11, the circulation clean piping system, the backwash piping system and the like are provided. [Effect] By combining the advanced water treatment including ozone treatment and backwashing with hot water, the ultraviolet sterilizer is not required, the life of activated carbon is extended, and the economical efficiency of the advanced water treatment device is improved.
Description
【0001】[0001]
本考案は、被処理水に高濃度のオゾンを注入した後、活性炭濾過層に前記被処 理水を通して処理する上水高度処理装置に関する。 The present invention relates to a high-grade water treatment device for injecting a high concentration of ozone into water to be treated, and then treating the treated water through the activated carbon filter layer.
【0002】[0002]
例えば高架水槽等の上水を処理する場合に、高濃度のオゾン処理と活性炭濾過 とを併用した処理をすれば、上水中の不純物等の除去率を大幅に向上させ、上水 を高度に浄化することができる。ところが、このような装置では、活性炭の吸着 容量に限界があり、活性炭を3〜6月毎に交換しなければならなかった。又、活 性炭がバクテリヤの温床になった。特に上水を高濃度のオゾンで処理すると、オ ゾンによる強力な殺菌効果が得られると共に、有機物等の分解、凝集により活性 炭濾過槽において水中の汚れ成分が高度に除去されるが、他方、有機物の分解に より活性炭でバクテリヤが通常の活性炭処理の場合よりも格段に著しく増殖する 。このバクテリヤは、活性炭濾過層で処理した水を再度オゾン処理することによ っても殺菌できるが、残留オゾンの問題が発生するため、この方法は必ずしも好 ましくない。このため従来では、通常、紫外線殺菌装置が設けられていた。 For example, when treating clean water such as an elevated water tank, if combined high-concentration ozone treatment and activated carbon filtration are used, the removal rate of impurities in the clean water will be greatly improved and the clean water will be highly purified. can do. However, in such an apparatus, the adsorption capacity of activated carbon was limited, and the activated carbon had to be replaced every 3 to 6 months. Activated charcoal became a hotbed for bacteria. In particular, treating clean water with high-concentration ozone produces a strong bactericidal effect by ozone, and also decomposes and aggregates organic substances to highly remove dirt components in the activated carbon filter tank. The decomposition of organic matter causes activated bacteria to proliferate bacteria significantly more than in the case of normal activated carbon treatment. This bacterium can be sterilized by subjecting the water treated with the activated carbon filter layer to ozone treatment again, but this method is not always preferable because it causes a problem of residual ozone. For this reason, conventionally, an ultraviolet sterilizer is usually provided.
【0003】 しかしながら、この殺菌装置では、殺菌灯の容量が大きくなって設備コストが 高くなると共に、著しいバクテリヤの発生に対して殺菌が不十分になるおそれが あった。又、この殺菌装置は、活性炭内のバクテリヤ増殖源自体に対しては何ら 作用せず、これから流出したバクテリヤを殺菌するものであるから、常時殺菌灯 を使用しなければならず、運転コスト及び殺菌灯の交換等のメンテナンスコスト が高くなるという問題があった。更に、紫外線殺菌は、活性炭の寿命延長には何 ら寄与するものではなかった。However, in this sterilizer, the capacity of the sterilizing lamp becomes large, the equipment cost becomes high, and there is a possibility that the sterilization becomes insufficient for the remarkable generation of bacteria. In addition, since this sterilizer does not act on the bacterial growth source itself in the activated carbon and sterilizes the bacteria that flow out from this, a sterilization lamp must be used at all times, which reduces operating costs and sterilization. There was a problem that maintenance costs such as replacement of lights would be high. Furthermore, UV sterilization did not contribute to the extension of the life of activated carbon.
【0004】[0004]
本考案は従来技術に於ける上記問題を解決し、コストの安い簡単な構成により 殺菌効果を得ると共に、活性炭の寿命を延長し、経済性の高い上水高度処理装置 を提供することを課題とする。 SUMMARY OF THE INVENTION The present invention aims to solve the above problems in the prior art, to obtain a sterilizing effect with a low cost and simple structure, to extend the life of activated carbon, and to provide a highly economical advanced water treatment device. To do.
【0005】[0005]
本考案は上記課題を解決するために、被処理水に高濃度のオゾンを注入した後 、活性炭濾過層に前記被処理水を通して処理する上水高度処理装置において、 水を所定温度まで加熱する加熱手段と、該加熱手段で加熱された水を前記活性 炭濾過層に通す管路と、を有することを特徴とする。 In order to solve the above-mentioned problems, the present invention provides a high-grade water treatment device that injects a high concentration of ozone into treated water and then passes the treated water through an activated carbon filter bed to heat water to a predetermined temperature. Means and a conduit for passing the water heated by the heating means through the activated carbon filter layer.
【0006】[0006]
本考案によれば、加熱手段により水を加熱して所定温度まで上昇させ、管路に より加熱された水を活性炭濾過層に通すことができるので、活性炭濾過層を熱湯 により殺菌・洗浄することができる。この熱湯により、活性炭濾過層内のバクテ リヤが死滅するので、オゾン処理をする場合でも、活性炭におけるバクテリヤ増 殖の問題が解決される。又、熱湯逆洗により、活性炭に吸着された物質が脱着さ れる。この場合、オゾン酸化された処理水では、有機物等の異物が親水化された 結合になり易いため、熱湯逆洗により脱着され易くなっていて、逆洗効果が向上 する。なお、加熱手段で水を加熱する所定の温度とは、このような殺菌作用及び 活性炭に吸着された物質を脱着させる作用が発揮される程度の温度をいい、例え ば80°C程度をいう。 According to the present invention, it is possible to heat the water by the heating means to raise it to a predetermined temperature and pass the water heated by the pipe through the activated carbon filter layer, so that the activated carbon filter layer is sterilized and washed with hot water. You can This hot water kills the Bacteria in the activated carbon filter bed, so the problem of bacterial multiplication in activated carbon is solved even when ozone treatment is performed. Also, by backwashing with hot water, the substances adsorbed on the activated carbon are desorbed. In this case, in the treated water that has been subjected to ozone oxidation, foreign matters such as organic substances are likely to be hydrophilized bonds, so that they are easily desorbed by backwashing with hot water, and the backwashing effect is improved. The predetermined temperature at which the water is heated by the heating means is a temperature at which the sterilizing action and the action of desorbing the substance adsorbed on the activated carbon are exhibited, for example, about 80 ° C.
【0007】[0007]
図1は上水高度処理装置の一例である高架水槽水循環清浄装置の概略構成を示 す。 本装置は、被処理水である水槽循環水にオゾン発生装置1で発生したオゾンを 注入した後、活性炭濾過層2aを有する濾過装置2に水槽循環水を通して処理す る装置であり、循環水を所定温度として例えば85°Cまで加熱して熱湯にする 加熱手段としてのヒータ3と、加熱された水を水槽循環水の通る方向とは反対の 方向から活性炭濾過層に通す管路4と、を有する。本装置は更に、高架水槽5、 この中の水を循環させるためのポンプ6、三方切換電磁弁7、開閉電磁弁8、9 、10、温度センサ11、循環清浄配管系、逆洗配管系等を備えている。 Figure 1 shows the schematic configuration of an elevated water tank water circulation cleaning device, which is an example of an advanced water treatment device. This device is a device for injecting ozone generated by the ozone generator 1 into the water tank circulating water which is the water to be treated, and then treating the circulating water through the water tank circulating water through the filtering device 2 having the activated carbon filter layer 2a. A heater 3 as a heating means for heating to a predetermined temperature of, for example, 85 ° C. to turn it into hot water, and a pipe 4 for passing the heated water through the activated carbon filtration layer from the direction opposite to the direction in which the aquarium circulating water passes. Have. The apparatus further includes an elevated water tank 5, a pump 6 for circulating water in the tank, a three-way switching solenoid valve 7, opening / closing solenoid valves 8, 9, 10, a temperature sensor 11, a circulation clean piping system, a backwash piping system, etc. Is equipped with.
【0008】 オゾン発生装置1は、例えば、固体高分子電解質膜を用いた電解セルにより純 水を電気分解して10〜15%程度の高濃度のオゾンガスを取り出し、これをオ ゾンガス溶解槽に導入して高濃度のオゾン水を得るようにした電解式オゾン発生 装置である。濾過装置2の底部には、管路4から導入する逆洗用の熱湯を分配す る多孔板等から成る熱湯分配機構2bを配設し、逆洗水を分散させて活性炭濾過 層2aに流し、逆洗効果を上げるようにしている。ヒータ3は、内部に電熱器3 aを備え、水が流されると共に電熱器3aが通電されることにより、その出口部 から温度85°C程度の熱湯が出るようになっている。ヒータ3の出口管4は循 環清浄を行うメインラインよりも細い管とし、熱湯逆洗のために必要なだけの水 量が流れるようにし、熱湯の消費量を少なくすることが望ましい。一方、バイパ ス電磁弁8を含む管は、熱湯逆洗後の常温循環水による逆洗効果が上がるように 、管4より大きいサイズの管にするのがよい。又、電磁弁9を含む逆洗水の排水 管を細い管としてもよい。なお、ヒータ3としては、電熱式のものに限らず、蒸 気加熱式その他の形式のものを用いることができる。又、独立のヒータを設ける ことなく、他の用途に用いられるヒータやボイラー等を、本用途のヒータとして 兼用してもよいことは勿論である。高架水槽5の水は、本装置により循環清浄さ れると共に、図示しない上水供給系統に送られ、又、水道本管等から消費分を補 給される。In the ozone generator 1, pure water is electrolyzed by, for example, an electrolytic cell using a solid polymer electrolyte membrane to extract ozone gas having a high concentration of about 10 to 15%, and the ozone gas is introduced into an ozone gas dissolving tank. This is an electrolytic ozone generator that obtains high-concentration ozone water. At the bottom of the filtration device 2, there is provided a hot water distribution mechanism 2b including a perforated plate or the like for distributing the hot water for backwashing introduced from the pipe line 4, and the backwash water is dispersed and flowed to the activated carbon filtration layer 2a. , I try to improve the backwash effect. The heater 3 is provided with an electric heater 3a inside, and when water is flowed and the electric heater 3a is energized, hot water having a temperature of about 85 ° C is discharged from its outlet. It is desirable that the outlet pipe 4 of the heater 3 be made thinner than the main line for circulation cleaning so that the amount of water necessary for backwashing with hot water flows and the consumption of hot water is reduced. On the other hand, it is preferable that the pipe including the bypass solenoid valve 8 has a size larger than that of the pipe 4 so that the backwashing effect by the normal temperature circulating water after the backwashing with hot water is enhanced. Further, the drain pipe of the backwash water including the solenoid valve 9 may be a thin pipe. The heater 3 is not limited to an electric heating type, but a steam heating type or any other type can be used. Further, it is needless to say that a heater, a boiler or the like used for other purposes may also be used as the heater for this purpose without providing an independent heater. The water in the elevated water tank 5 is circulated and purified by this device, sent to a clean water supply system (not shown), and the water consumption is supplemented from a water main.
【0009】 以上のような構成により本装置は次のように運転される。 通常の循環清浄においては、オゾン発生装置1及びポンプ6が運転され、電磁 弁7の主循環経路側が開くと共に電磁弁10が開き、高架水槽の水は、濾過装置 2を含む主循環経路を通って循環清浄される。オゾン発生装置で製造された高濃 度のオゾン水は、図示しないエダクタ等で濾過装置2の入口側に導入され、循環 水中の細菌類の殺菌及び有機物質の分解、凝集等の作用をなし、濾過装置2では 、活性炭濾過槽2aによって汚れ成分等が吸着され、循環水が高度に浄化処理さ れる。With the above-mentioned structure, the present apparatus operates as follows. In normal circulation cleaning, the ozone generator 1 and the pump 6 are operated, the main circulation path side of the solenoid valve 7 is opened and the solenoid valve 10 is opened, and the water in the elevated water tank passes through the main circulation path including the filtration device 2. Is circulated and cleaned. The high-concentration ozone water produced by the ozone generator is introduced into the inlet side of the filtration device 2 by an eductor (not shown), etc., and acts to sterilize bacteria in the circulating water and decompose and aggregate organic substances, In the filtration device 2, the activated carbon filtration tank 2a adsorbs dirt components and the like, and the circulating water is highly purified.
【0010】 一方、濾過装置2の活性炭は、汚れ成分等の付着により次第に目詰まりすると 共に、バクテリヤを増殖させる。特に高濃度オゾン処理を併用する高度上水処理 装置においては、オゾンの有する有機物質の分解作用により、バクテリヤの増殖 が著しくなる。このため、本装置では、例えば1日に1回夜間に熱湯を用いて活 性炭濾過層を逆洗する。この逆洗は、機側手動操作や遠隔手動操作によっても行 うことができるが、本実施例では、次のように自動逆洗するようにしている。On the other hand, the activated carbon of the filtration device 2 is gradually clogged due to the attachment of dirt components and the like, and also causes bacteria to grow. Particularly in advanced water treatment equipment that also uses high-concentration ozone treatment, the growth of bacteria becomes remarkable due to the decomposition action of the organic substances contained in ozone. Therefore, in this apparatus, for example, hot water is used once a day to backwash the activated carbon filtration layer. This backwashing can be performed by a machine-side manual operation or a remote manual operation, but in this embodiment, automatic backwashing is performed as follows.
【0011】 図示しない制御装置において、1日のうち夜間の一定時間になるとタイマが作 動し、電磁弁7の主循環経路側及び電磁弁10が閉鎖すると共に、電磁弁7のヒ ータ側及び電磁弁9が開いて逆洗側に水が流れ、ヒータ3の電源がオンになる。 ヒータ3で逆洗水が加熱され、濾過装置2内の温度が上昇し、温度センサ11に より、濾過装置2を出た後の逆洗水の温度が70°Cまで上昇したことが検出さ れると、それから10分間経過した後ヒータ3への通電を停止し、電磁弁8を開 く。従って、少なくとも10分間、ヒータ3で加熱された熱湯が管路4を通って 濾過装置2内に導入され、熱湯分配機構2bで分配されて活性炭濾過層2aを略 均一に流れ、電磁弁9を通って排出管から排出されることにより、熱湯逆洗が行 われる。In a control device (not shown), a timer operates at a certain time of the night during the day, the main circulation path side of the solenoid valve 7 and the solenoid valve 10 are closed, and the heater side of the solenoid valve 7 is closed. Also, the solenoid valve 9 is opened, water flows to the backwash side, and the heater 3 is turned on. The backwash water is heated by the heater 3, the temperature inside the filtering device 2 rises, and the temperature sensor 11 detects that the temperature of the backwash water after leaving the filtering device 2 has risen to 70 ° C. Then, 10 minutes after that, the energization of the heater 3 is stopped and the solenoid valve 8 is opened. Therefore, for at least 10 minutes, the hot water heated by the heater 3 is introduced into the filtration device 2 through the pipe line 4, distributed by the hot water distribution mechanism 2b and flows substantially uniformly through the activated carbon filtration layer 2a, and the solenoid valve 9 is turned on. The water is backwashed by being discharged through the discharge pipe.
【0012】 熱湯逆洗が終わると、その後数分間、常温水により濾過装置2を冷却逆洗する 。このときには、バイパス用の電磁弁8が開かれているので、濾過装置2を通過 する流量が熱湯逆洗時より多くなる。そして、熱湯逆洗によって活性炭から脱着 され又は脱着され易くなった異物がより完全に脱着、排出される。 逆洗が終了すると、タイマの作動により、電磁弁7のヒータ側の流路及び電磁 弁8、9が閉鎖し、電磁弁7の循環清浄側及び電磁弁10が再び開き、通常の循 環清浄が再開される。After the backwashing with hot water is completed, the filtration device 2 is cooled and backwashed with normal temperature water for a few minutes thereafter. At this time, since the bypass solenoid valve 8 is opened, the flow rate passing through the filtering device 2 becomes larger than that during backwashing with hot water. Then, foreign matter that has been desorbed from the activated carbon or easily desorbed by backwashing with hot water is more completely desorbed and discharged. When backwashing is completed, the operation of the timer closes the flow path on the heater side of the solenoid valve 7 and the solenoid valves 8 and 9, and opens the circulation cleaning side of the solenoid valve 7 and the solenoid valve 10 again, so that normal circulation cleaning is performed. Is resumed.
【0013】 以上のような装置によれば、活性炭濾過層の熱湯逆洗により、濾過槽内のバク テリヤが死滅し、オゾン処理を行う場合であっても、その増殖が防止される。従 って、従来設けられていた紫外線殺菌装置が不要になる。又、熱湯逆洗により、 活性炭に付着した異物が効果的に脱着、除去される。この場合、オゾン処理され ることにより有機物等が親水化された結合になり易く、熱湯逆洗の効果が一層向 上され、活性炭に吸着された異物が極めて良好に脱着される。その結果、このよ うな本考案の装置により、活性炭の寿命が、従来3〜6月であったのに対して1 年以上に延長されることが確認された。According to the apparatus as described above, the backwashing of the activated carbon filtration layer with hot water kills the bacteria in the filtration tank, and even when ozone treatment is carried out, the proliferation thereof is prevented. Therefore, the ultraviolet sterilizer that has been conventionally provided is no longer necessary. In addition, foreign matter adhering to the activated carbon is effectively desorbed and removed by backwashing with hot water. In this case, the ozone treatment makes it easier for organic substances and the like to become hydrophilic bonds, further enhances the effect of backwashing with hot water, and foreign substances adsorbed on the activated carbon are desorbed very well. As a result, it was confirmed that such a device of the present invention extends the life of activated carbon to 1 year or more as compared with the conventional 3 to 6 months.
【0014】[0014]
以上の如く本考案によれば、オゾン処理を含む上水高度処理と熱湯逆洗とを組 み合わせることにより、オゾンによるバクテリヤ増殖作用が阻止されると共に、 活性炭濾過層の洗浄が極めて効果的になるという二重の効果が得られる。そして 、紫外線殺菌装置の設置が不要になり、装置全体のコスト及びランニングコスト の低減を図ることができ、且つ、活性炭の寿命を大幅に延長することができる。 その結果、上水高度処理システムをより経済的なものにすることができる。 As described above, according to the present invention, by combining the advanced water treatment including ozone treatment and the backwashing with hot water, the bacterial growth action by ozone is prevented and the activated carbon filter bed is extremely effectively washed. The double effect of becoming is obtained. Further, it is not necessary to install an ultraviolet sterilizer, the cost of the entire apparatus and the running cost can be reduced, and the life of the activated carbon can be greatly extended. As a result, the advanced water treatment system can be made more economical.
【図面の簡単な説明】[Brief description of drawings]
【図1】上水高度処理装置の一例である高架水槽水循環
清浄装置の全体構成を示す説明図である。FIG. 1 is an explanatory diagram showing the overall configuration of an elevated water tank water circulation cleaning device which is an example of an advanced water treatment device.
1 オゾン発生装置 2a 活性炭濾過層 3 ヒータ(加熱手段) 4 管路 1 Ozone Generator 2a Activated Carbon Filtration Layer 3 Heater (Heating Means) 4 Pipeline
Claims (1)
後、活性炭濾過層に前記被処理水を通して処理する上水
高度処理装置において、 水を所定温度まで加熱する加熱手段と、該加熱手段で加
熱された水を前記活性炭濾過層に通す管路と、を有する
ことを特徴とする上水高度処理装置。1. A heating means for heating water to a predetermined temperature in a high-grade water treatment apparatus for treating treated water by injecting a high concentration of ozone into the treated water and then passing the treated water through an activated carbon filter layer, and the heating means. And a pipe for passing the water heated in step 1 through the activated carbon filtration layer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1993061457U JP2607091Y2 (en) | 1993-10-20 | 1993-10-20 | Advanced water treatment equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1993061457U JP2607091Y2 (en) | 1993-10-20 | 1993-10-20 | Advanced water treatment equipment |
Publications (2)
Publication Number | Publication Date |
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JPH0725995U true JPH0725995U (en) | 1995-05-16 |
JP2607091Y2 JP2607091Y2 (en) | 2001-03-19 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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JP1993061457U Expired - Lifetime JP2607091Y2 (en) | 1993-10-20 | 1993-10-20 | Advanced water treatment equipment |
Country Status (1)
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JP (1) | JP2607091Y2 (en) |
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1993
- 1993-10-20 JP JP1993061457U patent/JP2607091Y2/en not_active Expired - Lifetime
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Publication number | Publication date |
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JP2607091Y2 (en) | 2001-03-19 |
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