JPH091167A - High-degree water purification system - Google Patents

High-degree water purification system

Info

Publication number
JPH091167A
JPH091167A JP7149967A JP14996795A JPH091167A JP H091167 A JPH091167 A JP H091167A JP 7149967 A JP7149967 A JP 7149967A JP 14996795 A JP14996795 A JP 14996795A JP H091167 A JPH091167 A JP H091167A
Authority
JP
Japan
Prior art keywords
ozone
water
air
treated
treatment
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.)
Pending
Application number
JP7149967A
Other languages
Japanese (ja)
Inventor
Sachio Kanbara
左千夫 神原
Keiji Okuma
啓二 大隈
Yoshinari Fujita
良成 藤田
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP7149967A priority Critical patent/JPH091167A/en
Publication of JPH091167A publication Critical patent/JPH091167A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Biological Treatment Of Waste Water (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

PURPOSE: To prevent the dissolved ozone included in water to be treated subjected to a treatment in an ozone contact vessel from adversely affecting the treatment in a biologically active carbon column. CONSTITUTION: The high-degree water purification system including the ozone contact vessel 1 and the biologically active carbon column 2 is provided with an aeration tank 6 having an air diffusion pipe 8 behind the ozone contact vessel and before the biologically active carbon column and is provided with an aeration air quantity controller 20 for controlling the quantity of the air to be sent into the air diffusion pipe 8 in accordance with the dissolved ozone concn. of the water to be treated in the lower bottom of the air diffusion pipe installed in the aeration tank. As a result, the dissolved ozone remaining after the ozone treatment is prevented from adversely affecting the treatment in the biologically active carbon treatment column.

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、オゾン接触槽と生物活
性炭塔とを備えた高度浄水処理システムに係り、特にオ
ゾン接触槽で処理された被処理水に含まれる溶存オゾン
が生物活性炭塔における処理に悪影響を及ぼさないよう
にした高度浄水処理システムに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a highly purified water treatment system provided with an ozone contact tank and a biological activated carbon tower, and in particular, dissolved ozone contained in water to be treated in the ozone contact tank is used in the biological activated carbon tower. The present invention relates to an advanced water purification system that does not adversely affect the treatment.

【0002】[0002]

【従来の技術】産業の発展あるいは都市への人口集中等
により、各種の排水が公共の水域へ流入するようにな
り、水道水の水源である河川,湖沼の水質汚濁が進んで
いる。
2. Description of the Related Art Due to industrial development or population concentration in cities, various kinds of drainage have come into public water bodies, and water pollution of rivers and lakes, which are the sources of tap water, is progressing.

【0003】従来、浄水処理システムにおいては、凝集
沈殿処理と砂濾過処理及び塩素処理等の組合せにより、
被処理水中の濁り成分を除去し、また殺菌処理を行って
きた。
Conventionally, in a water purification system, a combination of coagulation sedimentation treatment, sand filtration treatment, chlorine treatment, etc.
The turbidity components in the water to be treated have been removed and sterilization has been performed.

【0004】しかし、水源の水質汚濁に伴い、臭気物
質,トリハロメタン前駆物質,アンモニア性窒素などが
含まれるようになり、従来の凝集沈殿処理と砂濾過処理
及び塩素処理の組合せだけでは、色,異臭味の除去及び
有機物質の除去に限界が生じている。
However, as the water source becomes polluted with water, odorants, trihalomethane precursors, ammoniacal nitrogen, etc. are added, and the combination of the conventional coagulating sedimentation treatment, sand filtration treatment, and chlorine treatment causes a color and an offensive odor. There are limits to taste removal and organic material removal.

【0005】このようなことから、従来の浄水処理シス
テムに更にオゾン接触槽と生物活性炭塔とを加えた高度
浄水処理システムが注目されるようになった。このよう
な高度浄水処理システムの一例が、特開平5−245484 号
公報に記載されている。
From the above, attention has been paid to an advanced water treatment system in which an ozone contact tank and a biological activated carbon tower are added to the conventional water treatment system. An example of such an advanced water purification system is described in Japanese Patent Laid-Open No. 5-245484.

【0006】[0006]

【発明が解決しようとする課題】オゾン接触槽と生物活
性炭塔とを備えた高度浄水処理システムによれば、色,
異臭味及び有機物質等を酸化分解して除去することがで
きる。
According to an advanced water purification treatment system equipped with an ozone contact tank and a biological activated carbon tower,
The off-flavor and organic substances can be removed by oxidative decomposition.

【0007】しかし、オゾン接触槽でオゾン処理された
被処理水中には溶存オゾンが含まれており、これが次段
の生物活性炭処理塔における処理に悪影響を及ぼす。特
開平5−245484 号公報では、かかる問題は取り上げてい
ない。
However, the water to be treated which has been subjected to the ozone treatment in the ozone contact tank contains dissolved ozone, which adversely affects the treatment in the biological activated carbon treatment tower in the next stage. Japanese Patent Laid-Open No. 5-245484 does not address such a problem.

【0008】従って、本発明の目的は、オゾン接触槽で
処理された被処理水中に含まれる溶存オゾンが生物活性
炭塔における処理に悪影響を及ぼさないようにした高度
浄水処理システムを提供することにある。
Therefore, an object of the present invention is to provide a highly purified water treatment system in which the dissolved ozone contained in the water to be treated treated in the ozone contact tank does not adversely affect the treatment in the biological activated carbon tower. .

【0009】[0009]

【課題を解決するための手段】本発明は、オゾン接触槽
と生物活性炭塔とを具備して被処理水を処理する高度浄
水処理システムにおいて、前記オゾン接触槽の後段で前
記生物活性炭塔の前段に空気散気管を備えた曝気槽を設
け、該曝気槽に設置された前記空気散気管の下方底部の
被処理水の溶存オゾン濃度に基づいて前記空気散気管に
送る空気の風量を制御する曝気風量制御手段を設けたこ
とを特徴とする高度浄水処理システムにある。
The present invention provides an advanced water purification system for treating water to be treated, which comprises an ozone contact tank and a biological activated carbon tower, and is provided in a stage after the ozone contact tank and before the biological activated carbon tower. An aeration tank provided with an air diffuser, and aeration for controlling the amount of air sent to the air diffuser based on the concentration of dissolved ozone in the water to be treated at the bottom of the air diffuser installed in the aeration tank It is an advanced water purification system characterized by having an air volume control means.

【0010】曝気槽に設置された空気散気管の下方底部
の被処理水の溶存オゾン濃度を検出するために、曝気槽
に設置された空気散気管の設置位置よりも更に下方底部
に溶存オゾン濃度測定器を設置することが望ましい。
In order to detect the dissolved ozone concentration of the water to be treated at the lower bottom of the air diffuser installed in the aeration tank, the dissolved ozone concentration is further lower than the installation position of the air diffuser installed in the aeration tank. It is desirable to install a measuring instrument.

【0011】また、オゾン接触槽を複数の反応室により
構成し、各反応室の気相部は各壁によって分離し、各反
応室の液相部はオーバフローした被処理水が一方から他
方の反応室あるいは隣接する反応室に相互に流れ込むよ
うに構成すること、及び各反応室にはオゾン散気管を設
けることが望ましい。
Further, the ozone contact tank is composed of a plurality of reaction chambers, the gas phase portion of each reaction chamber is separated by each wall, and the liquid phase portion of each reaction chamber causes the treated water that has overflowed to react from one to the other. It is desirable that the reaction chambers or adjacent reaction chambers flow into each other, and that each reaction chamber is provided with an ozone diffusion pipe.

【0012】オゾン接触槽の後段に曝気槽を設置して
も、溶存オゾン濃度に関係無く曝気風量を一定にして供
給したのでは、溶存オゾンを効果的に除去することはで
きない。また、無駄な風量を送ったり、費用を使うこと
にもなりかねない。
Even if an aeration tank is installed after the ozone contact tank, the dissolved ozone cannot be effectively removed if the aeration air volume is kept constant and supplied regardless of the dissolved ozone concentration. In addition, it may result in wasted air volume and cost.

【0013】本発明により、溶存オゾン濃度に見合った
適切な風量を供給することができ、溶存オゾンを効果的
に除去することができる。
According to the present invention, it is possible to supply an appropriate amount of air corresponding to the dissolved ozone concentration, and it is possible to effectively remove the dissolved ozone.

【0014】[0014]

【作用】オゾン接触槽の後段で生物活性炭塔の前段に、
空気散気管を有する曝気槽を設けて空気を散気すること
により、オゾン処理された被処理水中より気相中へオゾ
ンを排出し、被処理水が生物活性炭塔に入るときには、
生物活性炭塔における処理へ悪影響を及ぼさないように
溶存オゾンを除去することができる。
[Function] After the ozone contact tank, before the biological activated carbon tower,
By providing an aeration tank having an air diffuser to diffuse air, ozone is discharged into the gas phase from the ozone-treated water to be treated, and when the water to be treated enters the biological activated carbon tower,
Dissolved ozone can be removed without adversely affecting the treatment in the bioactivated carbon tower.

【0015】曝気処理の際に被処理水に含まれる溶存オ
ゾン濃度を検出して、それに基づいて曝気風量をコント
ロールすることにより、被処理水中の溶存オゾン濃度を
生物活性炭塔における処理に悪影響を及ぼさない範囲ま
で効果的に除去することができる。
By detecting the dissolved ozone concentration contained in the water to be treated during the aeration treatment and controlling the amount of aeration air based on the detected concentration, the dissolved ozone concentration in the treated water adversely affects the treatment in the biological activated carbon tower. It is possible to effectively remove even the area that does not exist.

【0016】曝気槽内で空気散気管により噴出された空
気は、液相中を水面に向かって上昇し、その過程でオゾ
ンを気相中へと排出する。従って、被処理水中の真のオ
ゾン濃度を検出するには、空気散気管よりも下方の位置
から被処理水を採取してオゾン濃度を測定する必要があ
る。曝気槽内の空気散気管が設置されている位置よりも
更に下方にオゾン濃度測定器を設置し、そこでオゾン濃
度を測定し、これに基づいて空気散気管に供給する風量
を制御することにより、効果的にオゾンを除去し気相へ
排出することができる。また風量の過不足を防止するこ
とができる。
The air jetted by the air diffuser in the aeration tank rises in the liquid phase toward the water surface and, in the process, discharges ozone into the gas phase. Therefore, in order to detect the true ozone concentration in the water to be treated, it is necessary to sample the water to be treated from a position below the air diffuser and measure the ozone concentration. By installing an ozone concentration measuring device further below the position where the air diffuser in the aeration tank is installed, measuring the ozone concentration there, and controlling the air volume supplied to the air diffuser based on this, It can effectively remove ozone and discharge it into the gas phase. In addition, it is possible to prevent excess and deficiency of the air volume.

【0017】[0017]

【実施例】以下、本発明の高度浄水処理システムの実施
例を、図面に基づいて説明する。図1は、オゾン接触槽
と生物活性炭塔を具備する高度浄水処理システムの概略
構成図を示している。この実施例では、オゾン接触槽1
は、三つの反応室14a,14b,14cにより構成さ
れている。そして、最終段の反応室14cに隣接して空
気散気管8を備えた曝気槽6が設けられている。反応室
14a,14b,14cには、それぞれオゾン散気管3
a,3b,3cが設置されている。これらのオゾン散気
管は、オゾナイザ5に接続されている。
Embodiments of the advanced water purification system of the present invention will be described below with reference to the drawings. FIG. 1 shows a schematic configuration diagram of an advanced water purification treatment system including an ozone contact tank and a biological activated carbon tower. In this embodiment, the ozone contact tank 1
Is composed of three reaction chambers 14a, 14b, 14c. An aeration tank 6 having an air diffuser 8 is provided adjacent to the reaction chamber 14c at the final stage. The reaction chambers 14a, 14b, 14c have ozone diffusing tubes 3 respectively.
a, 3b, 3c are installed. These ozone diffusers are connected to the ozonizer 5.

【0018】浄水場で凝集沈殿処理及び砂濾過処理など
の処理が施された被処理水は、オゾン接触槽1の反応室
14a,14b,14cへ矢印で示すように順次供給さ
れる。被処理水はまず反応室14aへ導入され、オゾン
散気管3より噴出するオゾンにより処理される。次いで
反応室14b及び反応室14cへと導入されてオゾン処
理される。オゾン散気管により被処理水中に注入された
オゾンは、液相中に吸収されて被処理水を酸化処理す
る。これにより、被処理水中の異臭味,色などが除去さ
れ、有機物質が分解される。
The water to be treated which has been subjected to the coagulation sedimentation treatment and the sand filtration treatment in the water purification plant is sequentially supplied to the reaction chambers 14a, 14b and 14c of the ozone contact tank 1 as shown by arrows. First, the water to be treated is introduced into the reaction chamber 14 a and treated with ozone ejected from the ozone diffusing pipe 3. Then, it is introduced into the reaction chamber 14b and the reaction chamber 14c and subjected to ozone treatment. Ozone injected into the water to be treated by the ozone diffuser is absorbed in the liquid phase to oxidize the water to be treated. As a result, the off-flavor, color, etc. in the water to be treated are removed, and the organic substances are decomposed.

【0019】オゾンを散気された被処理水は、次に曝気
槽6へ導入される。曝気槽6では、被処理水のオゾン処
理が継続して進行するが、ここでの狙いは空気を空気散
気管8により噴出して溶存オゾンを気相中へ排出するこ
とにある。このためには、液相中のオゾン濃度を精度よ
く測定しておく必要があり、本実施例では、オゾン濃度
測定器9を液相中へ設置して、オゾン濃度を測定するよ
うにしている。この他に、被処理水を採取してオゾン濃
度を測定するようにしてもよい。オゾン濃度を測定した
ならば、この信号を曝気風量制御装置20へ送り、空気
散気管8により噴出する空気の風量を制御する。
The water to be treated in which ozone has been diffused is then introduced into the aeration tank 6. In the aeration tank 6, the ozone treatment of the water to be treated continues to proceed, but the aim here is to eject air by the air diffuser 8 to discharge the dissolved ozone into the gas phase. For this purpose, it is necessary to accurately measure the ozone concentration in the liquid phase. In this embodiment, the ozone concentration measuring instrument 9 is installed in the liquid phase to measure the ozone concentration. . Alternatively, the water to be treated may be sampled to measure the ozone concentration. When the ozone concentration is measured, this signal is sent to the aeration air volume control device 20 to control the air volume of the air blown by the air diffuser 8.

【0020】曝気槽6内の被処理水に含まれる真のオゾ
ン濃度を測定するために、オゾン濃度測定器9を空気散
気管8が設置されている位置よりも更に下方底部に設置
すべきである。
In order to measure the true ozone concentration contained in the water to be treated in the aeration tank 6, the ozone concentration measuring instrument 9 should be installed further below the position where the air diffuser 8 is installed. is there.

【0021】反応室14a,14b,14cにおいて、
液相中へ吸収されずに気相中へ排出されたオゾン、及び
曝気槽6で気相に排出されたオゾンは、オゾン分解触媒
が入っている排オゾン処理塔4へ送られ、無害なガスに
分解されてからブロア15により大気中へ放出される。
排オゾン処理塔4は、触媒によりオゾンを分解する代わ
りに、熱分解,土壌分解,薬液洗浄あるいは活性炭処理
によりオゾンを処理するものであってもよい。排オゾン
処理塔4で排オゾン除去処理を行うにあたっては、オゾ
ン濃度測定器7を設けて排オゾンの濃度を測定すること
が望ましい。
In the reaction chambers 14a, 14b, 14c,
The ozone discharged into the gas phase without being absorbed into the liquid phase and the ozone discharged into the gas phase in the aeration tank 6 are sent to the waste ozone treatment tower 4 containing the ozone decomposition catalyst, and are harmless gas. After being decomposed into air, it is released into the atmosphere by the blower 15.
The exhaust ozone treatment tower 4 may treat ozone by thermal decomposition, soil decomposition, chemical cleaning or activated carbon treatment, instead of decomposing ozone by a catalyst. When performing the exhaust ozone removal processing in the exhaust ozone processing tower 4, it is desirable to provide an ozone concentration measuring device 7 to measure the concentration of the exhaust ozone.

【0022】図2は、空気散気管8に供給する空気の風
量を制御する曝気風量制御装置20の構成図を示してい
る。曝気槽6でオゾン濃度測定器9により得られた信号
は、風量制御コントローラ13に送信される。風量制御
コントローラ13では、このオゾン濃度と空気の設定値
(SV値)及び曝気用ブロア10の風量メータ12によ
り検出された値を基に、曝気用ブロア10に付設してい
る風量弁調整用モータ11の回転数を調整して曝気用ブ
ロア10より送風する空気の風量を制御する。曝気槽6
で溶存オゾンの除去処理を行った被処理水は、次段の生
物活性炭塔2に導入して処理を行う。この実施例では、
生物活性炭塔を2基設けて、1基を逆洗浄等により休止
している間に他方の生物活性炭塔を作動させるようにし
ているが、2基でなくてもかまわない。
FIG. 2 shows a block diagram of an aeration air volume control device 20 for controlling the air volume of the air supplied to the air diffuser 8. The signal obtained by the ozone concentration measuring device 9 in the aeration tank 6 is transmitted to the air volume control controller 13. In the air volume control controller 13, based on the ozone concentration, the set value of air (SV value), and the value detected by the air volume meter 12 of the aeration blower 10, the air volume valve adjusting motor attached to the aeration blower 10 is installed. The rotation speed of 11 is adjusted to control the air volume of the air blown from the aeration blower 10. Aeration tank 6
The water to be treated, which has been subjected to the removal treatment of dissolved ozone in 1., is introduced into the biological activated carbon tower 2 in the next stage and treated. In this example,
Two biological activated carbon towers are provided and the other biological activated carbon tower is operated while the other is activated by back washing or the like. However, the number of biological activated carbon towers does not have to be two.

【0023】被処理水は、生物活性炭塔に導入される前
に、溶存オゾン除去処理が施されているので、活性炭と
して硝化菌等の細菌を付着させた生物活性炭を用いて
も、死滅するようなことはなく、生物活性炭による処理
を効果的に行うことができる。この生物活性炭処理によ
り、通常の活性炭処理では除去することのできないアン
モニアや生物分解性物質を除去することができ、良質の
処理水を需要家へ供給することができる。また、生物活
性炭塔に導入される前に溶存オゾン除去処理が施された
ことにより、生物活性炭処理の時間を短縮できるという
効果もある。
Since the treated water is subjected to the dissolved ozone removal treatment before being introduced into the biological activated carbon tower, even if biological activated carbon to which bacteria such as nitrifying bacteria are attached is used as activated carbon, it will be destroyed. Nonetheless, treatment with biological activated carbon can be effectively performed. By this biological activated carbon treatment, ammonia and biodegradable substances that cannot be removed by the usual activated carbon treatment can be removed, and high-quality treated water can be supplied to consumers. In addition, since the dissolved ozone removal treatment is performed before being introduced into the biological activated carbon tower, there is an effect that the biological activated carbon treatment time can be shortened.

【0024】[0024]

【発明の効果】本発明により、オゾン接触槽と生物活性
炭塔とを備えた高度浄水処理システムにおいて、オゾン
接触槽で処理された被処理水中に含まれる溶存オゾン
が、生物活性炭処理塔における処理に悪影響を及ぼすの
を防止することができた。
INDUSTRIAL APPLICABILITY According to the present invention, in an advanced water purification treatment system equipped with an ozone contact tank and a biological activated carbon tower, dissolved ozone contained in the water to be treated treated in the ozone contact tank can be treated in the biological activated carbon processing tower. It was possible to prevent adverse effects.

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

【図1】本発明の一実施例を示す高度浄水処理システム
の概略構成図。
FIG. 1 is a schematic configuration diagram of an advanced water purification treatment system showing an embodiment of the present invention.

【図2】本発明の高度浄水処理システムにおける曝気風
量制御装置の概略構成図。
FIG. 2 is a schematic configuration diagram of an aeration air volume control device in the advanced water purification treatment system of the present invention.

【符号の説明】[Explanation of symbols]

1…オゾン接触槽、2…生物活性炭塔、5…オゾナイ
ザ、6…曝気槽、8…空気散気管、9…オゾン濃度測定
器、14a,14b,14c…反応室、20…曝気風量
制御装置。
DESCRIPTION OF SYMBOLS 1 ... Ozone contact tank, 2 ... Biological activated carbon tower, 5 ... Ozonizer, 6 ... Aeration tank, 8 ... Air diffuser, 9 ... Ozone concentration measuring device, 14a, 14b, 14c ... Reaction chamber, 20 ... Aeration air volume control device.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】オゾン接触槽と生物活性炭塔とを具備して
被処理水を処理する高度浄水処理システムにおいて、前
記オゾン接触槽の後段で前記生物活性炭塔の前段に空気
散気管を備えた曝気槽を設け、該曝気槽に設置された前
記空気散気管の下方底部の被処理水の溶存オゾン濃度に
基づいて前記空気散気管に送る空気の風量を制御する曝
気風量制御手段を設けたことを特徴とする高度浄水処理
システム。
1. A highly purified water treatment system comprising an ozone contact tank and a biological activated carbon tower for treating water to be treated, wherein aeration is provided with an air diffuser pipe after the ozone contact tank and before the biological activated carbon tower. A tank is provided, and aeration air volume control means for controlling the air volume of the air sent to the air diffusion tube based on the dissolved ozone concentration of the water to be treated at the lower bottom of the air diffusion tube installed in the aeration tank is provided. A featured advanced water purification system.
【請求項2】請求項1において、前記曝気槽に設置され
た前記空気散気管よりも下方底部に溶存オゾン濃度測定
器を設置したことを特徴とする高度浄水処理システム。
2. The highly purified water treatment system according to claim 1, wherein a dissolved ozone concentration measuring device is installed at a bottom portion below the air diffuser installed in the aeration tank.
【請求項3】請求項1又は2において、前記オゾン接触
槽を複数の反応室により構成し、各反応室の気相部を各
壁によって分離し、各反応室の液相部をオーバフローし
た被処理水が一方から他方の反応室あるいは隣接する反
応室に流れ込むように構成し、各反応室にオゾン散気管
を設けたことを特徴とする高度浄水処理システム。
3. The ozone contact tank according to claim 1 or 2, wherein the ozone contact tank is composed of a plurality of reaction chambers, the gas phase portion of each reaction chamber is separated by each wall, and the liquid phase portion of each reaction chamber overflows. An advanced water purification system characterized in that the treated water is configured to flow from one reaction chamber to the other reaction chamber or an adjacent reaction chamber, and an ozone diffusion pipe is provided in each reaction chamber.
JP7149967A 1995-06-16 1995-06-16 High-degree water purification system Pending JPH091167A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7149967A JPH091167A (en) 1995-06-16 1995-06-16 High-degree water purification system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7149967A JPH091167A (en) 1995-06-16 1995-06-16 High-degree water purification system

Publications (1)

Publication Number Publication Date
JPH091167A true JPH091167A (en) 1997-01-07

Family

ID=15486538

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7149967A Pending JPH091167A (en) 1995-06-16 1995-06-16 High-degree water purification system

Country Status (1)

Country Link
JP (1) JPH091167A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
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KR100450588B1 (en) * 2002-03-27 2004-09-30 주식회사 다인엔지니어링 Decolorization system of livestock wastewater effluent using ozone oxidation method
JP2007125545A (en) * 2005-10-05 2007-05-24 Ishikawajima Harima Heavy Ind Co Ltd Waste water treatment equipment
JP2008093601A (en) * 2006-10-13 2008-04-24 Ihi Corp Waste water treatment equipment
JP2010234324A (en) * 2009-03-31 2010-10-21 Kazunori Koishi Filtration method, filtration apparatus and filter bed
WO2016103985A1 (en) * 2014-12-26 2016-06-30 ユニ・チャーム株式会社 Method for recycling used absorbent article
JP2016123973A (en) * 2014-12-26 2016-07-11 ユニ・チャーム株式会社 Recycling method of used absorbent article
CN113024033A (en) * 2021-03-15 2021-06-25 云南省设计院集团工程投资有限公司 Process for deeply treating sewage discharge of livestock and poultry breeding industry
WO2022064929A1 (en) * 2020-09-23 2022-03-31 サンデン・アドバンストテクノロジー株式会社 Ozone solution production apparatus

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100450588B1 (en) * 2002-03-27 2004-09-30 주식회사 다인엔지니어링 Decolorization system of livestock wastewater effluent using ozone oxidation method
JP2007125545A (en) * 2005-10-05 2007-05-24 Ishikawajima Harima Heavy Ind Co Ltd Waste water treatment equipment
JP2008093601A (en) * 2006-10-13 2008-04-24 Ihi Corp Waste water treatment equipment
JP2010234324A (en) * 2009-03-31 2010-10-21 Kazunori Koishi Filtration method, filtration apparatus and filter bed
WO2016103985A1 (en) * 2014-12-26 2016-06-30 ユニ・チャーム株式会社 Method for recycling used absorbent article
JP2016123973A (en) * 2014-12-26 2016-07-11 ユニ・チャーム株式会社 Recycling method of used absorbent article
WO2022064929A1 (en) * 2020-09-23 2022-03-31 サンデン・アドバンストテクノロジー株式会社 Ozone solution production apparatus
CN113024033A (en) * 2021-03-15 2021-06-25 云南省设计院集团工程投资有限公司 Process for deeply treating sewage discharge of livestock and poultry breeding industry

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