JP2010188315A - Treating method and facility of raw water containing organic pollutant or toxic substance - Google Patents

Treating method and facility of raw water containing organic pollutant or toxic substance Download PDF

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JP2010188315A
JP2010188315A JP2009037613A JP2009037613A JP2010188315A JP 2010188315 A JP2010188315 A JP 2010188315A JP 2009037613 A JP2009037613 A JP 2009037613A JP 2009037613 A JP2009037613 A JP 2009037613A JP 2010188315 A JP2010188315 A JP 2010188315A
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raw water
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JP5173882B2 (en
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Yasushi Iseri
寧 井芹
Tadao Ito
忠男 伊藤
Masataka Yamagishi
真孝 山岸
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Marsima Aqua System Corp
West Japan Engineering Consultants Inc
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Abstract

<P>PROBLEM TO BE SOLVED: To effectively remove toxicity and malodor of raw water containing organic pollutants or toxic substances like harmful microorganisms and chemical substances, besides algae, without separately setting a reactive gas injection apparatus or a surplus reactive gas treatment apparatus. <P>SOLUTION: The reactive gas is filled in a sealed vessel 2 in advance, the raw water containing organic pollutants or toxic substances is sprayed at a high pressure in the reactive gas atmosphere to impinge onto an impact plate 4 to atomize the raw water, and at the same time, to react the atomized raw water with the reactive gas filled in the sealed vessel 2. A water sump 22 is formed in the sealed vessel 2 to store the treating water after impingement at a given water level of L1-L2. The reactive gas is stored in advance in the sealed vessel 2 at the part above the water level of L1-L2 of the treating water stored in the water sump 22. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、有機汚濁物または毒性物質を含む原水の処理方法および設備に関する。   The present invention relates to a method and equipment for treating raw water containing organic pollutants or toxic substances.

従来、有機汚濁物または毒性物質を含む原水の処理方法および設備の一例として、密閉容器内で、有機汚濁物である藻類を含む原水を高圧で噴射し、衝撃板に衝突させることで、原水中の藻類を衝撃で破壊して殺藻する殺藻方法および装置がある(特許文献1参照)。この技術では、藻類の増殖を抑制して、貯水池等の水質保全を行うことができる。   Conventionally, as an example of a method and facility for treating raw water containing organic pollutants or toxic substances, raw water containing algae that are organic pollutants is jetted at a high pressure in a sealed container and collided with an impact plate. There is an algae-killing method and apparatus for destroying algae by impact and killing algae (see Patent Document 1). With this technology, it is possible to suppress the growth of algae and to preserve the water quality of a reservoir or the like.

そして、処理水は、そのまま貯水池等に戻して、貯水池等の食物連鎖の促進を図るか、浮島等に散布することで食物連鎖の促進をより図るようにしている(特許文献2参照)。   Then, the treated water is returned to the reservoir or the like as it is to promote the food chain of the reservoir or the like, or sprayed on floating islands or the like (see Patent Document 2).

特許文献1,2の技術では、藻類の増殖を抑制することができるが、藻類の持つ毒性や臭気を除去できない。そこで、殺藻装置とは別にオゾンガス(反応性ガス)注入装置を設置し、処理水にオゾンガスを注入して、藻類の持つ毒性や臭気を除去しなければならない。   Although the techniques of Patent Documents 1 and 2 can suppress the growth of algae, the toxicity and odor possessed by algae cannot be removed. Therefore, an ozone gas (reactive gas) injection device is installed separately from the algaecidal device, and ozone gas is injected into the treated water to remove the algae's toxicity and odor.

特許第2835574号公報Japanese Patent No. 2835574 特許第3535819号公報Japanese Patent No. 3535819

しかしながら、処理水の貯水槽等のオゾンガス注入装置を別に設置すると、設備が大型化し、設備コストも高くなるという問題がある。また、オゾンガス注入量のコントロールが難しく、余剰(廃)オゾンガス処理装置も別に必要となるので、設備がさらに大型化し、設備コストもより高くなるという問題がある。   However, when an ozone gas injection device such as a treated water storage tank is separately installed, there is a problem that the equipment is enlarged and the equipment cost is increased. Further, it is difficult to control the amount of ozone gas injected, and a surplus (waste) ozone gas processing apparatus is required separately, which causes the problem that the equipment is further increased in size and the equipment cost is increased.

本発明は、前記のような問題を解消するためになされたもので、反応性ガス注入装置や余剰反応性ガス処理装置等を別に設置する必要がなく、かつ藻類だけではなく、有害な微生物や化学物質のような有機汚濁物または毒性物質を含む原水の毒性や臭気等を効果的に除去できるようにした有機汚濁物または毒性物質を含む原水の処理方法および設備を提供することを目的とするものである。   The present invention has been made to solve the above-described problems, and it is not necessary to separately install a reactive gas injection device, an excess reactive gas processing device, etc., and not only algae but also harmful microorganisms and An object of the present invention is to provide a method and facility for treating raw water containing organic pollutants or toxic substances, which can effectively remove the toxicity and odor of raw water containing organic pollutants such as chemical substances or toxic substances. Is.

前記課題を解決するために、本発明の第1の手段である請求項1は、密閉容器内に反応性ガスを予め充満させ、この反応性ガス雰囲気中で、有機汚濁物または毒性物質を含む原水を高圧で噴射し、衝撃板に衝突させることで原水を霧状化すると同時に、この霧状化原水を密閉容器内に充満された反応性ガスと反応させることを特徴とする有機汚濁物または毒性物質を含む原水の処理方法を提供するものである。   In order to solve the above-mentioned problems, the first means of the present invention is that the closed container is prefilled with a reactive gas, and an organic pollutant or a toxic substance is contained in the reactive gas atmosphere. An organic pollutant characterized by spraying raw water at a high pressure and atomizing the raw water by colliding with an impact plate, and at the same time reacting the atomized raw water with a reactive gas filled in a sealed container or The present invention provides a method for treating raw water containing toxic substances.

請求項2のように、請求項1において、前記反応性ガスは、オゾンガス、塩素ガス、二酸化塩素ガス、炭酸ガス、アンモニアガス、酸素ガスのいずれか1つであることが好ましい。   As in claim 2, in claim 1, the reactive gas is preferably any one of ozone gas, chlorine gas, chlorine dioxide gas, carbon dioxide gas, ammonia gas, and oxygen gas.

本発明の第2の手段である請求項3は、密閉容器内に反応性ガスを予め充満させ、この反応性ガス雰囲気中で、有機汚濁物または毒性物質を含む原水を高圧で噴射し、衝撃板に衝突させることで原水を霧状化すると同時に、この霧状化原水を密閉容器内に充満された反応性ガスと反応させる有機汚濁物または毒性物質を含む原水の処理設備であって、前記密閉容器内の上部に、前記原水を高圧で噴射するノズルと、このノズルから噴射された原水を衝突させる前記衝撃板とを配置して、密閉容器内の下部に、衝撃板に衝突した後の処理水を所定の水位で溜める水溜め部を形成するとともに、この水溜め部に溜まった処理水の水位より上方の密閉容器内に反応性ガスを予め充満させて、反応性ガス雰囲気を形成する反応性ガス供給装置を設けたことを特徴とする有機汚濁物または毒性物質を含む原水の処理設備を提供するものである。   According to a third aspect of the present invention, the closed container is filled with a reactive gas in advance, and raw water containing organic pollutants or toxic substances is injected at a high pressure in the reactive gas atmosphere. A raw water treatment facility containing organic pollutants or toxic substances that makes the raw water atomized by colliding with a plate and simultaneously reacting the atomized raw water with a reactive gas filled in a sealed container, A nozzle that injects the raw water at high pressure in the upper part of the sealed container and the impact plate that collides the raw water ejected from the nozzle are disposed, and the lower part in the sealed container is subjected to collision with the impact plate. A water reservoir is formed to store the treated water at a predetermined water level, and a reactive gas atmosphere is formed by prefilling the reactive gas in the sealed container above the water level of the treated water accumulated in the water reservoir. A reactive gas supply device was installed. There is provided a raw water treatment facility including organic contaminants or toxic substances, characterized and.

請求項4のように、請求項3において、前記密閉容器内の水溜め部における溜まった処理水の水位の上限と下限を設定し、この処理水の水位が上限と下限の範囲を維持するように、反応性ガスのガス圧を制御する制御装置を設けた構成とすることが好ましい。   As in claim 4, in claim 3, an upper limit and a lower limit of the water level of the treated water accumulated in the water reservoir in the sealed container are set, and the water level of the treated water is maintained within the upper limit and lower limit ranges. It is preferable to provide a control device for controlling the gas pressure of the reactive gas.

請求項5のように、請求項3または4において、前記反応性ガスは、オゾンガス、塩素ガス、二酸化塩素ガス、炭酸ガス、アンモニアガス、酸素ガスのいずれか1つであることが好ましい。   As in claim 5, in claim 3 or 4, the reactive gas is preferably any one of ozone gas, chlorine gas, chlorine dioxide gas, carbon dioxide gas, ammonia gas, and oxygen gas.

本発明の請求項1によれば、密閉容器内の反応性ガス雰囲気中で、有機汚濁物または毒性物質を含む原水を高圧で噴射し、衝撃板に衝突させることで原水を霧状化すると同時に、この霧状化原水を密閉容器内に充満された反応性ガスと反応させるようにしたものである。   According to claim 1 of the present invention, the raw water containing organic pollutants or toxic substances is injected at a high pressure in the reactive gas atmosphere in the sealed container, and at the same time the raw water is atomized by colliding with the impact plate. The atomized raw water is reacted with the reactive gas filled in the sealed container.

したがって、例えば有機汚濁物または毒性物質が藻類であり、反応性ガスがオゾンガスである場合には、藻類を含む原水を高圧で衝撃板に衝突させることで、原水中の藻類が衝撃で破壊されて殺藻されるようになる。また、藻類が持つ毒性も分解されるようになる。   Therefore, for example, when organic pollutants or toxic substances are algae and the reactive gas is ozone gas, the algae in the raw water are destroyed by impact by colliding the raw water containing algae with the impact plate at high pressure. Algae will be killed. In addition, the toxicity of algae will be degraded.

同時に、オゾンガス雰囲気中で原水を衝撃板に衝突させるから、衝突で原水が霧状化し、この霧状化(微細粒子化)原水は密閉容器内に充満し、同じく充満されたオゾンガスと接触しやすくなるので(気液混合)、霧状化原水とオゾンガスとの反応が促進されるようになる。このように、反応が促進されることで、藻類が持つ毒性や臭気が酸化分解によって、効果的に除去されるようになる。   At the same time, since the raw water collides with the impact plate in the ozone gas atmosphere, the raw water is atomized by the collision, and this atomized (fine particle) raw water is filled in the sealed container and is easily in contact with the filled ozone gas. As a result (gas-liquid mixing), the reaction between the atomized raw water and ozone gas is promoted. Thus, by promoting the reaction, the toxicity and odor of algae can be effectively removed by oxidative decomposition.

この結果、有機汚濁物または毒性物質が藻類であり、反応性ガスがオゾンガスである場合には、オゾン注入装置を別に設置する必要がなく、既存の衝撃殺藻装置等にオゾンガスの供給装置を付加する等の僅かの改造を加えるだけで、藻類の持つ毒性や臭気等を効果的に除去できるようになる。同様に、反応性ガスが塩素ガス、あるいは二酸化塩素ガスである場合には、藻類が持つ毒性が分解されるようになる。   As a result, when organic pollutants or toxic substances are algae and the reactive gas is ozone gas, there is no need to install an ozone injection device separately, and an ozone gas supply device is added to existing impact algae killing devices, etc. It is possible to effectively remove the toxicity and odors of algae with only a few modifications such as. Similarly, when the reactive gas is chlorine gas or chlorine dioxide gas, the toxicity of algae is decomposed.

一方、有機汚濁物または毒性物質として、例えば有害なウィルス、細菌等の微生物を含む病院等からの排水(原水)、腐敗させる微生物を含むアルコールやジュースの製造工場等からの排水(原水)、有害な農薬を含む農業排水(原水)、有害なダイオキシン、PCB(化学物質)等を含む化学工場等からの排水(原水)、工場跡地や埋め立て地の地下汚染水(原水)であっても、反応性ガスとしてオゾンガスや塩素ガス、あるいは二酸化塩素ガスを用いれば、毒性や臭気等が酸化分解によって、効果的に除去されるようになる。   On the other hand, as organic pollutants or toxic substances, wastewater (raw water) from hospitals containing microorganisms such as harmful viruses and bacteria, wastewater (raw water) from alcohol and juice manufacturing factories containing microorganisms that rot, harmful Reacts even with agricultural wastewater (raw water) containing various agricultural chemicals, wastewater (raw water) from chemical factories, etc. containing harmful dioxins and PCBs (chemical substances), and underground contaminated water (raw water) in factory sites and landfills If ozone gas, chlorine gas, or chlorine dioxide gas is used as the reactive gas, toxicity, odor, and the like can be effectively removed by oxidative decomposition.

また、反応性ガスが炭酸ガスである場合には、アルカリ性の霧状化原水の中和が効果的に促進され、反応性ガスがアンモニアガスである場合には、酸性の霧状化原水の中和が効果的に促進されるようになる。その他、反応性ガスが酸素ガスである場合には、無酸素の霧状化原水(生物が生存できない無酸素水)の酸素溶解が効果的に促進されるようになる。   In addition, when the reactive gas is carbon dioxide, neutralization of the alkaline atomized raw water is effectively promoted, and when the reactive gas is ammonia gas, Sum is effectively promoted. In addition, when the reactive gas is oxygen gas, oxygen dissolution of oxygen-free atomized raw water (oxygen-free water in which living organisms cannot survive) is effectively promoted.

本発明の請求項3によれば、密閉容器内の反応性ガス雰囲気中で、有機汚濁物または毒性物質を含む原水をノズルから高圧で噴射し、衝撃板に衝突させることで原水を霧状化すると同時に、この霧状化原水を、反応性ガス供給装置から供給されて密閉容器内に充満された反応性ガスと反応させるようにしたものである。   According to claim 3 of the present invention, raw water containing organic pollutants or toxic substances is jetted from a nozzle at high pressure in a reactive gas atmosphere in a sealed container, and the raw water is atomized by colliding with an impact plate. At the same time, the atomized raw water is reacted with the reactive gas supplied from the reactive gas supply device and filled in the sealed container.

したがって、例えば有機汚濁物または毒性物質が藻類であり、反応性ガスがオゾンガスである場合には、藻類を含む原水を高圧で衝撃板に衝突させることで、原水中の藻類が衝撃で破壊されて殺藻されるようになる。また、藻類が持つ毒性も分解されるようになる。   Therefore, for example, when organic pollutants or toxic substances are algae and the reactive gas is ozone gas, the algae in the raw water are destroyed by impact by colliding the raw water containing algae with the impact plate at high pressure. Algae will be killed. In addition, the toxicity of algae will be degraded.

同時に、オゾンガス雰囲気中で原水を衝撃板に衝突させるから、衝突で原水が霧状化し、この霧状化(微細粒子化)原水は密閉容器内に充満し、同じく充満されたオゾンガスと接触しやすくなるので(気液混合)、霧状化原水とオゾンガスとの反応が促進されるようになる。このように、反応が促進されることで、藻類が持つ毒性や臭気が酸化分解によって、効果的に除去されるようになる。   At the same time, since the raw water collides with the impact plate in the ozone gas atmosphere, the raw water is atomized by the collision, and this atomized (fine particle) raw water is filled in the sealed container and is easily in contact with the filled ozone gas. As a result (gas-liquid mixing), the reaction between the atomized raw water and ozone gas is promoted. Thus, by promoting the reaction, the toxicity and odor of algae can be effectively removed by oxidative decomposition.

さらに、密閉容器内の下部の水溜め部に溜まった処理水の水位より上方の密閉容器内にオゾンガス雰囲気を形成するだけであるから、オゾンガスが外部に排出されることがない。   Furthermore, since the ozone gas atmosphere is only formed in the sealed container above the water level of the treated water collected in the lower water reservoir in the sealed container, the ozone gas is not discharged to the outside.

この結果、有機汚濁物または毒性物質が藻類であり、反応性ガスがオゾンガスである場合には、オゾン注入装置や余剰(廃)オゾン処理装置を別に設置する必要がなく、既存の衝撃殺藻装置等にオゾンガスの供給装置を付加する等の僅かの改造を加えるだけで、藻類の持つ毒性や臭気等を効果的に除去できるようになる。   As a result, when the organic pollutant or toxic substance is algae and the reactive gas is ozone gas, there is no need to separately install an ozone injection device or a surplus (waste) ozone treatment device. By adding a slight modification such as adding an ozone gas supply device, etc., the toxicity and odor of algae can be effectively removed.

なお、有機汚濁物または毒性物質として、有害なウィルス、細菌等の微生物を含む病院等からの排水(原水)等であっても、請求項1と同様の作用効果を奏することができる。   In addition, even if it is the waste water (raw water) from the hospital etc. containing microorganisms, such as harmful viruses and bacteria, as an organic pollutant or a toxic substance, the effect similar to Claim 1 can be show | played.

請求項4によれば、密閉容器内の水溜め部における処理水の水位が上限と下限の範囲を維持するように、制御装置で反応性ガスのガス圧を制御するようにしたから、密閉容器内に常に適正量の反応性ガスを供給できるようになる。   According to the fourth aspect, since the control device controls the gas pressure of the reactive gas so that the water level of the treated water in the water reservoir in the sealed container maintains the upper and lower limits, the sealed container An appropriate amount of reactive gas can always be supplied into the interior.

本発明の実施形態の有機汚濁物または毒性物質を含む原水の処理設備のシステム図である。It is a system diagram of the processing equipment of the raw water containing the organic pollutant or toxic substance of the embodiment of the present invention. 図1の設備の要部の概念図である。It is a conceptual diagram of the principal part of the installation of FIG. ノズルの変形例の斜視図である。It is a perspective view of the modification of a nozzle.

以下、本発明を実施するための形態について、図面を参照しながら詳細に説明する。図1は、本発明に係る有機汚濁物または毒性物質を含む原水の処理設備1のシステム図、図2は、図1の設備の要部の概念図である。   Hereinafter, embodiments for carrying out the present invention will be described in detail with reference to the drawings. FIG. 1 is a system diagram of a raw water treatment facility 1 containing organic pollutants or toxic substances according to the present invention, and FIG. 2 is a conceptual diagram of a main part of the facility of FIG.

先ず、図2を用いて有機汚濁物または毒性物質を含む原水の処理設備1の要部の概略構成と作用を説明する。密閉容器2内に、有機汚濁物または毒性物質を含む原水を高圧で噴射するノズル3と、このノズル3から噴射された原水を衝突させる衝撃板4とを配置している。ここで、有機汚濁物または毒性物質とは、一例として「藻類」とし、有機汚濁物を含む原水とは、「藻類を含む原水」とする。   First, the schematic configuration and operation of the main part of the raw water treatment facility 1 containing organic pollutants or toxic substances will be described with reference to FIG. A nozzle 3 that jets raw water containing organic pollutants or toxic substances at high pressure and an impact plate 4 that collides the raw water jetted from the nozzle 3 are arranged in the sealed container 2. Here, the organic pollutant or the toxic substance is “algae” as an example, and the raw water containing the organic pollutant is “raw water containing algae”.

ノズル3からは、例えば0.7MPaに加圧した原水を、20〜30m/秒の速度で噴射する(矢印a参照)。このノズル3から噴射された原水を衝撃板4に衝突させることで、原水中の藻類が衝撃で破壊されて殺藻されるようになる。   From the nozzle 3, for example, raw water pressurized to 0.7 MPa is injected at a speed of 20 to 30 m / sec (see arrow a). By causing the raw water sprayed from the nozzle 3 to collide with the impact plate 4, the algae in the raw water are destroyed by the impact and are killed.

そして、密閉容器2内の底部に溜まった衝突した後の処理水は、排水口5から密閉容器2外に排水されるようになる(矢印b参照)。   And the treated water after the collision which collected on the bottom part in the airtight container 2 comes to be drained out of the airtight container 2 from the drain outlet 5 (refer arrow b).

図1に示したように、前記密閉容器2は、縦長円筒状であり、頂部2aと底部2bとで密閉されている。参考までに、仕切り壁で閉め切きった広大な干拓池の水質保全のために処理設備1で殺藻する場合、処理設備1は、藻類が風等で吹き寄せられる区域に設置され、密閉容器2は、例えば直径Dが2m程度、高さH1が4m程度のものを用いることになる。   As shown in FIG. 1, the sealed container 2 has a vertically long cylindrical shape, and is sealed by a top 2a and a bottom 2b. For reference, when algae is killed by the treatment facility 1 to preserve the water quality of the vast reclaimed pond that has been closed off by the partition wall, the treatment facility 1 is installed in an area where algae are blown by the wind, etc. For example, the one having a diameter D of about 2 m and a height H1 of about 4 m is used.

前記ノズル3は、外部から密閉容器2の底部2bの中心を上方に貫通して、密閉容器2内に臨まされ、上端の上向きノズル口3aは、頂部2aに対向させている。   The nozzle 3 penetrates the center of the bottom 2b of the sealed container 2 from the outside and faces the sealed container 2, and the upward nozzle port 3a at the upper end faces the top 2a.

密閉容器2の外部におけるノズル3の下端には、原水供給管7が接続され、この原水供給管7には、原水を加圧するための高圧ポンプ8と、原水の水量を調整する原水調整バルブ9とが設けられている。   A raw water supply pipe 7 is connected to the lower end of the nozzle 3 outside the sealed container 2, and a high pressure pump 8 for pressurizing the raw water and a raw water adjustment valve 9 for adjusting the amount of raw water are connected to the raw water supply pipe 7. And are provided.

前記衝撃板4は、密閉容器2内の頂部2aの付近で、ノズル3のノズル口3aに所定の間隔を隔てて対向するように、頂部2aから複数の支持部材10で吊り支持された状態で下向きに設置されている。そして、ノズル3のノズル口3aから噴射された原水は、衝撃板4の下面に衝突されるようになる(矢印a参照)。なお、図3に示すように、衝撃板4の外径が大きい場合には、ノズル3から複数個のノズル口3aを分岐させて、噴射された原水が衝撃板4に均等に衝突するようにすることもできる。   The impact plate 4 is suspended and supported by a plurality of support members 10 from the top 2a so as to face the nozzle opening 3a of the nozzle 3 at a predetermined interval in the vicinity of the top 2a in the sealed container 2. It is installed downward. And the raw | natural water sprayed from the nozzle opening 3a of the nozzle 3 comes to collide with the lower surface of the impact board 4 (refer arrow a). As shown in FIG. 3, when the impact plate 4 has a large outer diameter, a plurality of nozzle openings 3 a are branched from the nozzle 3 so that the sprayed raw water collides with the impact plate 4 evenly. You can also

密閉容器2の底部2bの排水口5には、外部の排水管12が接続され、この排水管12には、排水量を調整する仕切りバルブ13が設けられている。そして、密閉容器2内の底部2bに溜まった衝突した後の処理水は、排水口5から排水管12を介して密閉容器2外に排水されるようになる(矢印b参照)。   An external drain pipe 12 is connected to the drain outlet 5 of the bottom 2b of the sealed container 2, and a partition valve 13 for adjusting the amount of drainage is provided in the drain pipe 12. Then, the treated water that has accumulated on the bottom 2b in the sealed container 2 is drained out of the sealed container 2 from the drain port 5 through the drain pipe 12 (see arrow b).

排水管12は、仕切りバルブ13の下流側で、底部2bから上方に高さH2で立ち上げられた後に、ほぼ水平向きに曲げられている。この高さH2については、後で説明する。   The drain pipe 12 is bent in a substantially horizontal direction after being raised at the height H2 from the bottom 2b on the downstream side of the partition valve 13. This height H2 will be described later.

密閉容器2の外部には、密閉容器2内の水位を外部から目視観察可能な水位計14が設けられている。   A water level meter 14 that can visually observe the water level in the sealed container 2 from the outside is provided outside the sealed container 2.

密閉容器2の頂部2aには、オゾンガス供給管16が外部から頂部2aの中心を下方に貫通されて密閉容器2内に臨まされ、下端の下向き供給口16aは、衝撃板4の上面に対向させている。   At the top 2a of the sealed container 2, an ozone gas supply pipe 16 is penetrated downward from the outside through the center of the top 2a so as to face the sealed container 2, and the downward supply port 16a at the lower end faces the upper surface of the impact plate 4. ing.

オゾンガス供給管16の他端は、オゾンガス発生器(反応性ガス供給装置)17に接続され、このオゾンガス供給管16には、オゾンガス量を調整するオゾンガス調整バルブ18と、密閉容器2内のオゾンガスのガス圧を検出する圧力計19と、安全バルブ20とが設けられている。   The other end of the ozone gas supply pipe 16 is connected to an ozone gas generator (reactive gas supply device) 17. The ozone gas supply pipe 16 includes an ozone gas adjustment valve 18 that adjusts the amount of ozone gas, and ozone gas in the sealed container 2. A pressure gauge 19 for detecting the gas pressure and a safety valve 20 are provided.

密閉容器2内の下部に、衝撃板4に衝突した後の処理水を所定の水位L1〜L2で溜める水溜め部22が形成されている。そして、この水溜め部22に溜まった処理水の水位L1〜L2より上方の密閉容器2内に、オゾンガス(反応性ガス)を予め充満させて、オゾンガス雰囲気を形成するようになる。   A water reservoir 22 is formed in the lower part of the hermetic container 2 to store treated water after colliding with the impact plate 4 at a predetermined water level L1 to L2. Then, ozone gas (reactive gas) is prefilled in the sealed container 2 above the water levels L1 to L2 of the treated water accumulated in the water reservoir 22 to form an ozone gas atmosphere.

密閉容器2内の水溜め部22における溜まった処理水の水位の上限L2と下限L1を設定し、この処理水の水位が上限L2と下限L1の範囲を維持するように、オゾンガスのガス圧を圧力計19で検出しながら、オゾンガス調整バルブ18でオゾンガス量を調整する制御装置23が設けられている。   The upper limit L2 and lower limit L1 of the level of treated water accumulated in the water reservoir 22 in the sealed container 2 are set, and the gas pressure of the ozone gas is set so that the level of this treated water maintains the range between the upper limit L2 and the lower limit L1. A control device 23 that adjusts the amount of ozone gas by the ozone gas adjustment valve 18 while being detected by the pressure gauge 19 is provided.

前述した排水管12は、仕切りバルブ13の下流側で上方に高さH2で立ち上げられている。   The above-described drain pipe 12 is raised at a height H2 upward on the downstream side of the partition valve 13.

その理由は、排水管12が排水口5からほぼ水平向きに曲げられているだけであると(矢印c参照)、密閉容器2に衝突した後の処理水が水溜め部22に溜まらないので、オゾンガスも排水口5から密閉容器2外に排出されるおそれがある。そこで、水溜め部22における溜まった処理水の水位の上限L2と下限L1を設定して、オゾンガスが排水口5から密閉容器2外に排出されないようにするために、排水管12を高さH2で立ち上げたのである。また、排水管12の高さH2は、水位の上限L2よりも低いと、水位の上限L2が維持できないので、水位の上限L2よりも高く設定している。   The reason for this is that if the drain pipe 12 is only bent substantially horizontally from the drain port 5 (see arrow c), the treated water after colliding with the sealed container 2 does not collect in the water reservoir 22. Ozone gas may also be discharged out of the sealed container 2 from the drain port 5. Accordingly, the upper limit L2 and the lower limit L1 of the water level of the treated water accumulated in the water reservoir 22 are set to prevent the ozone gas from being discharged out of the hermetic container 2 from the drain outlet 5 to the height H2. Was launched. Further, if the height H2 of the drain pipe 12 is lower than the upper limit L2 of the water level, the upper limit L2 of the water level cannot be maintained.

前記のように、有機汚濁物または毒性物質である藻類を含む原水の処理設備1であれば、密閉容器2内のオゾンガス雰囲気中で、藻類を含む原水を高圧でノズル3から噴射し、衝撃板に衝突させることで原水を霧状化すると同時に、この霧状化原水を密閉容器2内に充満されたオゾンガスと反応させることができる。   As described above, in the case of the raw water treatment facility 1 containing algae which are organic pollutants or toxic substances, the raw water containing algae is jetted from the nozzle 3 at high pressure in the ozone gas atmosphere in the sealed container 2, and the impact plate The raw water can be atomized by making it collide with the water, and at the same time, the atomized raw water can be reacted with the ozone gas filled in the sealed container 2.

したがって、有機汚濁物または毒性物質が藻類であり、反応性ガスがオゾンガスである場合には、藻類を含む原水を高圧で衝撃板4に衝突させることで、原水中の藻類が衝撃で破壊されて殺藻されるようになる。また、藻類が持つ毒性の分解されるようになる。   Therefore, when the organic pollutant or toxic substance is algae and the reactive gas is ozone gas, the algae in the raw water is destroyed by impact by colliding the raw water containing algae with the impact plate 4 at high pressure. Algae will be killed. In addition, the toxicity of algae will be decomposed.

同時に、オゾンガス雰囲気中で原水を衝撃板4に衝突させるから、衝突で原水が霧状化し、図2を参照すれば、この霧状化(微細粒子)水dは密閉容器2内に充満し、同じく充満されたオゾンガスOと接触しやすくなるので(気液混合)、霧状化水とオゾンガスとの反応が促進されるようになる。このように、反応が促進されることで、藻類が持つ毒性や臭気が酸化分解によって、効果的に除去されるようになる。 At the same time, since the raw water collides with the impact plate 4 in the ozone gas atmosphere, the raw water is atomized by the collision, and referring to FIG. 2, this atomized (fine particle) water d fills the sealed container 2; Similarly, since it becomes easy to come into contact with the filled ozone gas O 3 (gas-liquid mixing), the reaction between the atomized water and the ozone gas is promoted. Thus, by promoting the reaction, the toxicity and odor of algae can be effectively removed by oxidative decomposition.

この結果、有機汚濁物または毒性物質が藻類であり、反応性ガスがオゾンガスである場合には、オゾン注入装置を別に設置する必要がなく、藻類の持つ臭気や毒性等を効果的に除去できるようになる。   As a result, when the organic pollutant or toxic substance is algae and the reactive gas is ozone gas, it is not necessary to install a separate ozone injection device, and the odor and toxicity of algae can be effectively removed. become.

また、密閉容器2内の下部の水溜め部22に溜まった処理水の水位L1〜L2より上方の密閉容器2内にオゾンガス雰囲気を形成するだけであるから、オゾンガスが外部に排出されることがない。   Moreover, since the ozone gas atmosphere is only formed in the sealed container 2 above the water levels L1 to L2 of the treated water accumulated in the lower water reservoir 22 in the sealed container 2, the ozone gas may be discharged to the outside. Absent.

さらに、密閉容器2内の水溜め部22における処理水の水位が上限L2と下限L1の範囲を維持するように、制御装置23でオゾンガスのガス圧を制御するようにしたから、密閉容器2内に常に適正量のオゾンガスを供給できるようになる。   Furthermore, since the control device 23 controls the gas pressure of the ozone gas so that the water level of the treated water in the water reservoir 22 in the sealed container 2 is maintained in the range between the upper limit L2 and the lower limit L1, the inside of the sealed container 2 It is possible to always supply an appropriate amount of ozone gas.

この結果、反応性ガスがオゾンガスである場合にはオゾン注入装置や余剰(廃)オゾンガス処理装置を別に設置する必要がなく、既存の殺藻装置等にオゾンガス発生器17を付加する等の僅かの改造を加えるだけで、藻類の持つ臭気や毒性等を効果的に除去できるようになる。   As a result, when the reactive gas is ozone gas, there is no need to separately install an ozone injection device or a surplus (waste) ozone gas processing device, and a slight amount such as adding an ozone gas generator 17 to an existing algaecidal device or the like. It is possible to effectively remove the odor and toxicity of algae by simply remodeling.

前記実施形態では、有機汚濁物または毒性物質が藻類であり、反応性ガスがオゾンガスである場合を説明したものである。   In the above embodiment, the case where the organic pollutant or toxic substance is algae and the reactive gas is ozone gas is described.

しかしながら、有機汚濁物または毒性物質として、例えば有害なウィルス、細菌等の微生物を含む病院等からの排水(原水)、腐敗させる微生物を含むアルコールやジュースの製造工場等からの排水(原水)であっても、反応性ガスとしてオゾンガスや塩素ガス、あるいは二酸化塩素ガスを用いれば、微生物が殺滅され、毒性や臭気が酸化分解によって、効果的に除去されるようになる。   However, organic pollutants or toxic substances include, for example, wastewater from hospitals that contain microorganisms such as harmful viruses and bacteria (raw water), and wastewater (raw water) from factories that produce alcohol and juice containing microorganisms that are spoiled. However, if ozone gas, chlorine gas, or chlorine dioxide gas is used as the reactive gas, microorganisms are killed, and toxicity and odor are effectively removed by oxidative decomposition.

また、有機汚濁物または毒性物質として、例えば有害な農薬を含む農業排水(原水)、有害なダイオキシン、PCB(化学物質)等を含む化学工場等からの排水(原水)、工場跡地や埋め立て地の地下汚染水(原水)であっても、反応性ガスとしてオゾンガスや塩素ガス、あるいは二酸化塩素ガスを用いれば、毒性や臭気が酸化分解によって、効果的に除去されるようになる。   In addition, as organic pollutants or toxic substances, for example, agricultural wastewater (raw water) containing harmful pesticides, wastewater (raw water) from chemical factories containing harmful dioxins, PCB (chemical substances), etc. Even if it is underground polluted water (raw water), if ozone gas, chlorine gas, or chlorine dioxide gas is used as a reactive gas, toxicity and odor can be effectively removed by oxidative decomposition.

さらに、反応性ガスが炭酸ガスである場合には、アルカリ性の霧状化原水の中和が効果的に促進され、反応性ガスがアンモニアガスである場合には、酸性の霧状化原水の中和が効果的に促進されるようになる。   Further, when the reactive gas is carbon dioxide, neutralization of the alkaline atomized raw water is effectively promoted, and when the reactive gas is ammonia gas, the acidic atomized raw water is neutralized. Sum is effectively promoted.

その他、反応性ガスが酸素ガスである場合には、無酸素の霧状化原水(生物が生存できない無酸素水)の酸素溶解が効果的に促進されて、有酸素水が作れるようになる。   In addition, when the reactive gas is oxygen gas, oxygen dissolution of oxygen-free atomized raw water (oxygen-free water in which living organisms cannot survive) is effectively promoted, and aerobic water can be produced.

このように、有機汚濁物または毒性物質の種類に応じて、反応性ガスを、オゾンガス、塩素ガス、二酸化塩素ガス、炭酸ガス、アンモニアガス、酸素ガス等のように、必要に応じて使い分けることができる。   Thus, depending on the type of organic pollutant or toxic substance, reactive gas can be properly used as necessary, such as ozone gas, chlorine gas, chlorine dioxide gas, carbon dioxide gas, ammonia gas, oxygen gas, etc. it can.

1 有機汚濁物または毒性物質を含む原水の処理設備
2 密閉容器
3 ノズル
4 衝撃板
17 オゾン発生器(反応性ガス供給装置)
18 オゾン調整バルブ
19 圧力計
22 水溜め部
23 制御装置
L1,L2 水位
1 Processing equipment for raw water containing organic pollutants or toxic substances 2 Sealed container 3 Nozzle 4 Impact plate 17 Ozone generator (reactive gas supply device)
18 Ozone adjustment valve 19 Pressure gauge 22 Reservoir 23 Control device L1, L2 Water level

Claims (5)

密閉容器内に反応性ガスを予め充満させ、この反応性ガス雰囲気中で、有機汚濁物または毒性物質を含む原水を高圧で噴射し、衝撃板に衝突させることで原水を霧状化すると同時に、この霧状化原水を密閉容器内に充満された反応性ガスと反応させることを特徴とする有機汚濁物または毒性物質を含む原水の処理方法。   Reactive gas is filled in the sealed container in advance, and raw water containing organic pollutants or toxic substances is injected at high pressure in this reactive gas atmosphere, and at the same time, the raw water is atomized by colliding with the impact plate. A method for treating raw water containing organic pollutants or toxic substances, characterized in that the atomized raw water is reacted with a reactive gas filled in a sealed container. 前記反応性ガスは、オゾンガス、塩素ガス、二酸化塩素ガス、炭酸ガス、アンモニアガス、酸素ガスのいずれか1つであることを特徴とする請求項1に記載の有機汚濁物または毒性物質を含む原水の処理方法。   2. The raw water containing organic pollutant or toxic substance according to claim 1, wherein the reactive gas is any one of ozone gas, chlorine gas, chlorine dioxide gas, carbon dioxide gas, ammonia gas and oxygen gas. Processing method. 密閉容器内に反応性ガスを予め充満させ、この反応性ガス雰囲気中で、有機汚濁物または毒性物質を含む原水を高圧で噴射し、衝撃板に衝突させることで原水を霧状化すると同時に、この霧状化原水を密閉容器内に充満された反応性ガスと反応させる有機汚濁物または毒性物質を含む原水の処理設備であって、
前記密閉容器内の上部に、前記原水を高圧で噴射するノズルと、このノズルから噴射された原水を衝突させる前記衝撃板とを配置して、密閉容器内の下部に、衝撃板に衝突した後の処理水を所定の水位で溜める水溜め部を形成するとともに、この水溜め部に溜まった処理水の水位より上方の密閉容器内に反応性ガスを予め充満させて、反応性ガス雰囲気を形成する反応性ガス供給装置を設けたことを特徴とする有機汚濁物または毒性物質を含む原水の処理設備。
Reactive gas is filled in the sealed container in advance, and raw water containing organic pollutants or toxic substances is injected at high pressure in this reactive gas atmosphere, and at the same time, the raw water is atomized by colliding with the impact plate. A raw water treatment facility containing organic pollutants or toxic substances for reacting the atomized raw water with a reactive gas filled in a sealed container,
After the nozzle that jets the raw water at a high pressure and the impact plate that collides the raw water jetted from the nozzle are arranged at the upper part in the sealed container, and after the impact plate hits the lower part in the sealed container In addition to forming a water reservoir that accumulates the treated water at a predetermined water level, a reactive gas atmosphere is formed by prefilling the closed vessel above the water level of the treated water accumulated in the water reservoir in advance. An apparatus for treating raw water containing organic pollutants or toxic substances, characterized in that a reactive gas supply device is provided.
前記密閉容器内の水溜め部における溜まった処理水の水位の上限と下限を設定し、この処理水の水位が上限と下限の範囲を維持するように、反応性ガスのガス圧を制御する制御装置を設けたことを特徴とする請求項3に記載の有機汚濁物または毒性物質を含む原水の処理設備。   Control for controlling the gas pressure of the reactive gas so that the upper and lower limits of the level of the treated water accumulated in the water reservoir in the sealed container are set and the level of the treated water is maintained within the upper and lower limits. 4. The facility for treating raw water containing organic pollutants or toxic substances according to claim 3, wherein an apparatus is provided. 前記反応性ガスは、オゾンガス、塩素ガス、二酸化塩素ガス、炭酸ガス、アンモニアガス、酸素ガスのいずれか1つであることを特徴とする請求項3または4に記載の有機汚濁物または毒性物質を含む原水の処理設備。   The organic pollutant or toxic substance according to claim 3 or 4, wherein the reactive gas is any one of ozone gas, chlorine gas, chlorine dioxide gas, carbon dioxide gas, ammonia gas, and oxygen gas. Including raw water treatment facilities.
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