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JP2004160437A - Water purification method and apparatus - Google Patents

Water purification method and apparatus Download PDF

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Publication number
JP2004160437A
JP2004160437A JP2003093236A JP2003093236A JP2004160437A JP 2004160437 A JP2004160437 A JP 2004160437A JP 2003093236 A JP2003093236 A JP 2003093236A JP 2003093236 A JP2003093236 A JP 2003093236A JP 2004160437 A JP2004160437 A JP 2004160437A
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water
steam
ozone
treated
injected
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JP4261955B2 (en
Inventor
Yutaka Fujita
裕 藤田
Sumihisa Shimomura
純央 下村
Shunsuke Hosokawa
俊介 細川
Zenji Shimamura
善治 島村
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ESUMAKKU KK
MASUDA KENKYUSHO KK
Nippon Yusen KK
NYK Trading Corp
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ESUMAKKU KK
MASUDA KENKYUSHO KK
Nippon Yusen KK
NYK Trading Corp
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Abstract

【課題】大量でしかも流速が速い汚水や海水等であっても、充分な殺菌浄化効果が得られるようにする。
【解決手段】船舶のバラストタンク内のバラスト水2を船外に排出するためのバラスト配管1に、オゾン注入管4および蒸気注入管5をそれぞれ接続する。バラスト配管1内を流れるバラスト水2に対し、オゾン注入管4からオゾンを注入するとともに、このオゾン注入と同時または相前後して、蒸気注入管5から蒸気を注入する。すると、オゾンと蒸気との相乗効果により、大きな殺菌浄化効果が得られる。
【選択図】 図1
An object of the present invention is to provide a sufficient sterilizing and purifying effect even for a large amount of wastewater or seawater having a high flow rate.
An ozone injection pipe and a steam injection pipe are connected to a ballast pipe for discharging ballast water in a ballast tank of a ship outboard. Ozone is injected into the ballast water 2 flowing through the ballast pipe 1 from the ozone injection pipe 4, and steam is injected from the steam injection pipe 5 simultaneously with or before or after the ozone injection. Then, a large sterilizing and purifying effect can be obtained by the synergistic effect of ozone and steam.
[Selection diagram] Fig. 1

Description

【0001】
【発明の属する技術分野】
本発明は、例えば船舶のバラスト水、プールや風呂の循環水等の被処理水を浄化する際に用いられる水浄化方法およびその装置に係り、特に被処理水を送給過程で処理することができる水浄化方法およびその装置に関する。
【0002】
【従来の技術】
従来から、大きな水タンク内で、凝集剤や好気性菌,嫌気性菌,さらにはオゾン等を用い時間をかけて汚水を浄化する方法は汎く知られており、この方法を用いた浄化設備は、例えば浄水場やその他で実用化されている。
【0003】
【発明が解決しようとする課題】
前記従来の水浄化方法は、流れが全くないか、あるいは非常に流速の遅い湖沼や浄水場等に適用した場合には、一定の効果が期待できることが確認されているが、大量でしかも流速が速い汚水や海水等の殺菌浄化に適用した場合には、充分な殺菌浄化効果が得られないという問題がある。
【0004】
本発明は、かかる現況に鑑みなされたもので、流れが全くないか、あるいは非常に流速の遅い場合はもとより、大量でしかも流速が速い被処理水であっても、確実に浄化処理することができる水浄化方法およびその装置を提供するにある。
【0005】
本発明の他の目的は、オゾン単独で使用した場合に比較して、オゾンによるCOD等の有害物質や被処理水中の微生物,細菌,バクテリア等(以下、単に微生物等と称す)の殺菌,浄化効果を向上させ、オゾンの使用量を低減することができるようにすることにある。
【0006】
本発明の他の目的は、紫外線を単独で使用した場合に比較して、その殺菌,浄化効果を向上させることができるようにすることにある。
【0007】
本発明の他の目的は、水タンク等の特別な処理設備を設けることなく被処理水を浄化処理することができ、スペースに余裕がない既存のプラント等にも容易に適用することができるようにすることにある。
【0008】
本発明の他の目的は、タンク等の処理設備が既にある場合には、この処理設備を利用して水浄化を効率的に行なうことができるようにすることにある。
【0009】
本発明の他の目的は、オゾンによる殺菌,浄化効果を、より向上させることができるようにすることにある。
【0010】
本発明のさらに他の目的は、紫外線の照射による殺菌,浄化効果を、より向上させることができるようにすることにある。
【0011】
【課題を解決するための手段】
前記目的を達成するため本発明は、被処理水が存在する処理領域内に、蒸気を注入するようにしたことを特徴とする。
【0012】
ところで、処理領域内に蒸気を注入すると、被処理水中に気泡群が生成されることになるが、これらの気泡群は、被処理水により急冷されて崩壊する。そしてその際に発生する非平衡局所場の物理化学作用により、被処理水中の微生物等が死滅,不活性化するとともに、有害化学物質が分解されて水質が浄化される。
【0013】
本発明はまた、蒸気の注入と同時または相前後してオゾンを注入するようにしたことを特徴とする。そしてこれにより、気泡群の崩壊に伴なう衝撃波によってオゾンが微細化,活性化され、被処理水への溶解が促進されるとともに、オゾンがより酸化力の強いヒドロキシラジカルに変換され、オゾンによる有害物質や微生物等の殺菌,浄化効果の向上が図られる。
【0014】
本発明はまた、蒸気の注入と同時または相前後して紫外線を照射するようにしたことを特徴とする。そしてこれにより、紫外線を単独で使用した場合よりも、その殺菌,浄化効果を向上させることが可能となる。
【0015】
本発明はまた、処理領域を、被処理水が送給される配管としたことを特徴とする。そしてこれにより、水タンク等の特別な処理設備を設けることなく、被処理水を浄化処理することが可能となる。
【0016】
本発明はまた、処理領域を、被処理水が一時滞留するタンクとしたことを特徴とする。そしてこれにより、タンク等の処理設備が既にある場合には、この処理設備を利用して水浄化を効率的に行なうことが可能となる。
【0017】
本発明はまた、蒸気とオゾンとを用いる場合に、注入された蒸気にオゾンが巻き込まれるようにしたことを特徴とする。そしてこれにより、オゾンの微細化,活性化がより促進され、オゾンの殺菌,浄化効果をより向上させることが可能となる。
【0018】
本発明はまた、蒸気注入処理された被処理水に、紫外線を照射するようにしたことを特徴とする。そしてこれにより、死滅,不活性化した微生物に紫外線が照射されることになり、紫外線による殺菌,浄化を効率的に行なうことが可能となる。
【0019】
本発明はさらに、蒸気により微細気泡化されたオゾンガスを含有する被処理水に、紫外線を照射するようにしたことを特徴とする。そしてこれにより、紫外線による殺菌,浄化効果を、より向上させることが可能となる。
【0020】
【発明の実施の形態】
以下、本発明を図面を参照して説明する。
図1は、本発明の第1の実施の形態に係る水浄化装置を示すもので、図中、符号1は、船舶のバラストタンク(図示せず)からのバラスト水2を船外に排出するためのバラスト配管であり、このバラスト配管1には、バラストポンプ3が設けられ、このバラストポンプ3の上流側位置には、オゾンを注入するためのオゾン注入管4および蒸気を注入するための蒸気注入管5がそれぞれ接続されている。そして、バラストタンクからのバラスト水2は、バラスト配管1内を送給される間に、前記各注入管4,5から注入されるオゾンおよび蒸気により殺菌,浄化され、浄化水6として船外に排出されるようになっている。
【0021】
次に、本実施の形態の作用について説明する。
バラスト水2の浄化処理に際しては、バラストポンプ3を起動して、バラストタンク内のバラスト水2をバラスト配管1を介し船外に排出する。そしてその際に、オゾン注入管4からオゾンを注入するとともに、このオゾン注入と同時あるいは相前後して、蒸気注入管5から蒸気を注入する。すると、オゾンと蒸気との相乗効果により、有害物質の分解や微生物等の殺菌,浄化が効果的に行なわれ、バラスト配管1内を流れるバラスト水2が確実に浄化処理される。そして、処理後の浄化水6は船外に排出される。
【0022】
以下、このオゾンと蒸気との相乗効果を、図2を参照して詳細に説明する。
オゾン注入管4から、バラスト水2中にオゾン11を注入すると、バラスト水2中の微生物等の細胞膜が、注入されたオゾンにより攻撃されてダメージを受ける。図中、符号12が、ダメージを受けた微生物等を示している。
【0023】
一方、蒸気注入管5から、バラスト水2中に蒸気13を注入すると、注入された蒸気13は、バラスト水2中で拡大して、バラスト水2中に気泡群が生成される。図中、符号14が、生成された気泡を示している。
【0024】
この気泡14は、バラスト水2で急冷されて崩壊し、気相反応場16と液相反応場17とからなる非平衡局所場15が発生する。そして、この非平衡局所場15の物理化学作用により、バラスト水2中の微生物等が死滅,不活性化するとともに、有害化学物質が分解されて水質が浄化される。
【0025】
また、前記気泡14が崩壊すると、衝撃波18が発生することになるが、この衝撃波18により、オゾン11が微細化,活性化され、バラスト水2中への溶解が促進される。図中、符号19は、溶解が促進されたオゾンを示している。また、微生物等は、前記衝撃波18により物理的に破壊される。図中、符号20は、物理的に破壊された微生物等を示している。
【0026】
また、前記オゾン11は、前記衝撃波18により、より酸化力の強いヒドロキシラジカル21に変換され、このヒドロキシラジカル21により、微生物等は化学的に殺菌されるとともに、有害化学物質は分解される。図中、符号22は、化学的に殺菌された微生物等を示し、また図中、符号23は、分解された有害化学物質を示している。
【0027】
以上の総合作用により、流速の速いバラスト水2であっても、短い搬送距離の間に確実に浄化処理され、浄化水6として船外に排出される。
【0028】
しかして、オゾン11と蒸気13とを同時に用いることにより、流速の速いバラスト水2を大量に浄化処理することができる。このため、バラスト配管1にオゾン注入管4および蒸気注入管5を接続するだけで装置が完成し、特別な処理設備を必要としない。また、オゾンの使用量を低減できるので、オゾン発生装置の小型化および使用電力の節減も可能となる。
【0029】
また、蒸気については、船舶では主要設備または付帯設備として、ボイラーを設置しているのが通例であるので、このボイラーからの蒸気を用いることで、新たにボイラーを設置する必要がない。このため、オゾン発生装置の小型化と相俟って、大幅なコスト削減が可能となる。
【0030】
なお、前記実施の第1の実施の形態においては、蒸気とオゾンとの両方を用いて浄化水6を得る場合について説明したが、後に詳述する実施例からも明らかなように、蒸気のみでも所期の水浄化効果は得られる。このため、蒸気のみをバラスト水2に注入して浄化水6を得るようにしてもよい。
【0031】
図3は、本発明の第2の実施の形態を示すもので、オゾン注入管4を蒸気注入管5に近接して配置し、オゾン注入管4からバラスト水2中に注入されたオゾン11が、蒸気注入管5からバラスト水2中に注入された蒸気13に巻き込まれるようにしたものである。
なお、その他の点については、前記第1の実施の形態と同一構成となっており、作用も同一である。
【0032】
しかして、蒸気注入管5からバラスト水2中に蒸気13を注入すると、蒸気13の気泡が崩壊することに伴ない、蒸気注入管5の下流側には、図3に示すように、衝撃波発生領域31が形成されることになる。このため、オゾン注入管4からバラスト水2中に注入されたオゾン11が、蒸気13に巻き込まれるようにすると、蒸気13の気泡崩壊に伴なう衝撃波により、オゾン11の気泡も、迅速に微細化,活性化されることになる。図3中において、符号32は、前記衝撃波によって微細化されたオゾン微細気泡流を示している。
【0033】
このように、オゾン11が微細化されると、オゾン11のバラスト水2中への溶解が促進され、オゾン11による水浄化効果を向上させることができる。
【0034】
図4は、本発明の第3の実施の形態を示すもので、前記第2の実施の形態におけるオゾン微細気泡流32中に、紫外線ランプ41を配設し、蒸気注入管5からの蒸気13の注入と同時あるいは相前後して、オゾン微細気泡流32中に紫外線42を照射できるようにしたものである。
なお、その他の点については、前記第2の実施の形態と同一構成となっており、作用も同一である。
【0035】
しかして、バラスト水2中に紫外線42が照射されることになるので、水浄化効果をより向上させることができる。しかも、紫外線42は、オゾン微細気泡流32中に照射されることになるので、蒸気13およびオゾン11でダメージを受けた微生物等に紫外線42が照射されることになり、紫外線42による水浄化効率を向上させることができる。
【0036】
なお、前記各実施の形態においては、船舶のバラスト水2の浄化処理を例に採って説明したが、上水場や下水場の水処理,プールや温泉等の水処理,工場や畜産施設等の廃水処理,水産加工の海水浄化処理,貯水池や貯水タンクの循環水の処理あるいは湖沼等の浄化処理にも同様に適用でき、同様の効果が期待できる。
【0037】
【実施例】
(第1実施例)
本発明者等は、図1に示す水浄化装置を用い、船舶のバラスト水2の浄化実験を行なった。
なお、オゾン注入率は0.05mg/リットル(バラスト水1リットル当たりオゾンを0.05mg注入)、蒸気注入率は0.12g/リットル(バラスト水1リットル当たり蒸気を0.12g注入)とした。
【0038】
その結果、植物プランクトン,有殻渦鞭毛藻,動物プランクトン等の海洋生物にダメージ(運動停止,鞭毛脱落,色素脱色等生物の生態状況に影響)が現われ、充分な浄化処理が可能であることが確認された。
【0039】
なお、比較例として、オゾンのみを用いてバラスト水2の浄化実験を行なった処、前記同様の浄化効果を得るために必要なオゾン注入率は1mg/リットルであり、蒸気との併用により、オゾン使用量を1/20に低減できることも確認された。
【0040】
(第2実施例)
本発明者等はまた、図3に示す水浄化装置を用い、蒸気注入管5から、蒸気圧0.55〜0.65MPa、温度100〜110℃の蒸気13を、20kg/hの注入率でバラスト水2中に注入し、その下流側に、どの程度の衝撃波発生領域31が形成されるのかを確認する実験を行なった。
【0041】
その結果、蒸気注入管5の軸心を中心線として、直径100mm,長さ200mmのラグビーボール状をなす衝撃波発生領域31が形成されることが確認された。
【0042】
(第3実施例)
本発明者等はまた、動物性プランクトンの一種であるアルテミアを20個体/cc含む80リットルの海水を用意し、これをタンク内に投入して、以下の4種類の実験を行なった。
(実験1)
前記タンク内に、第2実施例と同一条件で蒸気のみを注入した。
(実験2)
実験1にプラスして、オゾンを0.7g/hの注入率で注入した。
(実験3)
実験1にプラスして、20wの紫外線ランプを用い紫外線を照射した。
(実験4)
実験2にプラスして、20wの紫外線ランプを用い紫外線を照射した。
【0043】
前記4種類の実験を行なって、アルテミアの処理率(死亡,ダメージ有り)を測定した処、以下に示す表1の結果を得た。
【0044】
【表1】

Figure 2004160437
【0045】
表1からも明らかなように、蒸気のみでも、所期の水浄化効果が得られることが確認された。また、蒸気とオゾンとの併用により、極めて良好な水浄化効果が得られ、これに紫外線照射を加えることにより、水浄化効果をより向上させることができることも確認された。
【0046】
【発明の効果】
以上説明したように本発明は、被処理水が存在する処理領域内に、蒸気を注入するようにしているので、被処理中に蒸気の気泡群が生成され、これらの気泡群は、被処理水により急冷されて崩壊する。そしてその際に発生する被平衡局所場の物理化学作用により、被処理水中の微生物等が死滅,不活性化するとともに、有害化学物質が分解されて水質が浄化される。
【0047】
本発明はまた、蒸気の注入と同時または相前後してオゾンを注入するようにしているので、蒸気の気泡群の崩壊に伴なう衝撃波によってオゾンが微細化,活性化され、被処理水への溶解が促進されるとともに、オゾンがより酸化力の強いヒドロキシラジカルに変換され、オゾンによる有害物質や微生物等の殺菌,浄化効果の向上が図られる。
【0048】
本発明はまた、蒸気の注入と同時または相前後して紫外線を照射するようにしているので、紫外線を単独で使用した場合よりも、その殺菌,浄化効果を向上させることができる。
【0049】
本発明はまた、処理領域として、被処理水が送給される配管を用いるようにしているので、水タンク等の特別な処理設備を設けることなく、被処理水を浄化処理することができる。
【0050】
本発明はまた、処理領域として、被処理水が一時滞留するタンクを用いるようにしているので、タンク等の処理設備が既にある場合には、この処理設備を利用して水浄化を効率的に行なうことができる。
【0051】
本発明はまた、蒸気とオゾンとを用いる場合に、注入された蒸気にオゾンが巻き込まれるようにしているので、オゾンの微細化,活性化がより促進され、オゾンの殺菌,浄化効果をより向上させることができる。
【0052】
本発明はまた、蒸気注入処理された被処理水に、紫外線を照射するようにしているので、死滅,不活性化した微生物に紫外線が照射されることになり、紫外線による殺菌,浄化を効率的に行なうことができる。
【0053】
本発明はさらに、蒸気により微細気泡化されたオゾンガスを含有する被処理水に、紫外線を照射するようにしているので、紫外線による殺菌,浄化効果を、より向上させることができる。
【図面の簡単な説明】
【図1】本発明の第1の実施の形態に係る水浄化装置を示す構成図である。
【図2】図1の装置における水浄化のメカニズムを示す説明図である。
【図3】本発明の第2の実施の形態を示す説明図である。
【図4】本発明の第3の実施の形態を示す説明図である。
【符号の説明】
1 バラスト配管
2 バラスト水
3 バラストポンプ
4 オゾン注入管
5 蒸気注入管
6 浄化水
11,19 オゾン
12,20,22 微生物等
13 蒸気
14 気泡
15 非平衡局所場
16 気相反応場
17 液相反応場
18 衝撃波
21 ヒドロキシラジカル
23 有害化学物質
31 衝撃波発生領域
32 オゾン微細気泡流
41 紫外線ランプ
42 紫外線[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a water purification method and apparatus used for purifying water to be treated, such as ballast water for ships, circulating water for pools and baths, and more particularly, to the treatment of water to be treated in a feeding process. The present invention relates to a water purification method and an apparatus therefor.
[0002]
[Prior art]
2. Description of the Related Art Conventionally, a method of purifying sewage in a large water tank by using coagulant, aerobic bacteria, anaerobic bacteria, and ozone for a long time is widely known. Has been put to practical use, for example, in water purification plants and others.
[0003]
[Problems to be solved by the invention]
It has been confirmed that the above-mentioned conventional water purification method can be expected to have a certain effect when applied to lakes or marshes or water purification plants having a very low flow velocity or a very low flow velocity. When applied to fast sterilization and purification of sewage and seawater, there is a problem that a sufficient sterilization and purification effect cannot be obtained.
[0004]
The present invention has been made in view of such a situation, and even when there is no flow or very low flow velocity, even in the case of large amounts of water to be treated with high flow velocity, it is possible to reliably perform purification treatment. It is an object of the present invention to provide a water purification method and a device therefor.
[0005]
Another object of the present invention is to sterilize and purify harmful substances such as COD and microorganisms, bacteria, bacteria, and the like (hereinafter, simply referred to as microorganisms, etc.) in the water to be treated by ozone as compared with the case of using ozone alone. An object of the present invention is to improve the effect and reduce the amount of ozone used.
[0006]
Another object of the present invention is to make it possible to improve the sterilizing and purifying effects as compared with the case where ultraviolet light is used alone.
[0007]
Another object of the present invention is to purify the water to be treated without providing a special treatment facility such as a water tank, so that the present invention can be easily applied to an existing plant or the like where there is not enough space. It is to be.
[0008]
Another object of the present invention is to make it possible to efficiently perform water purification using a treatment facility such as a tank when the treatment facility already exists.
[0009]
Another object of the present invention is to improve the sterilizing and purifying effects of ozone.
[0010]
Still another object of the present invention is to make it possible to further improve the sterilization and purification effects by irradiation with ultraviolet rays.
[0011]
[Means for Solving the Problems]
In order to achieve the above object, the present invention is characterized in that steam is injected into a treatment area where water to be treated is present.
[0012]
By the way, when steam is injected into the treatment area, bubbles are generated in the water to be treated. These bubbles are rapidly cooled by the water to be treated and collapse. Then, the physicochemical action of the non-equilibrium local field generated at that time kills and inactivates microorganisms and the like in the water to be treated, decomposes harmful chemical substances, and purifies the water quality.
[0013]
The present invention is also characterized in that ozone is injected simultaneously with or before or after the injection of steam. Ozone is refined and activated by the shock wave accompanying the collapse of the bubble group, thereby dissolving the ozone in the water to be treated is promoted. At the same time, the ozone is converted into a hydroxyl radical having a stronger oxidizing power. The sterilization and purification effects of harmful substances and microorganisms are improved.
[0014]
The present invention is also characterized in that the ultraviolet ray is irradiated simultaneously with or before or after the injection of the steam. As a result, the sterilizing and purifying effects can be improved as compared with the case where ultraviolet light is used alone.
[0015]
The present invention is also characterized in that the treatment area is a pipe through which the water to be treated is fed. Thus, it is possible to purify the water to be treated without providing a special treatment facility such as a water tank.
[0016]
The present invention is also characterized in that the treatment area is a tank in which water to be treated temporarily stays. Thus, when there is already a treatment facility such as a tank, it is possible to efficiently perform water purification using the treatment facility.
[0017]
The present invention is also characterized in that when steam and ozone are used, ozone is involved in the injected steam. Thereby, the miniaturization and activation of ozone are further promoted, and the sterilizing and purifying effects of ozone can be further improved.
[0018]
The present invention is also characterized in that the water to be treated which has been subjected to the steam injection treatment is irradiated with ultraviolet rays. As a result, the dead and inactivated microorganisms are irradiated with ultraviolet light, and sterilization and purification by ultraviolet light can be performed efficiently.
[0019]
The present invention is further characterized in that the water to be treated containing ozone gas finely foamed by steam is irradiated with ultraviolet rays. This makes it possible to further improve the sterilizing and purifying effects of the ultraviolet rays.
[0020]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, the present invention will be described with reference to the drawings.
FIG. 1 shows a water purification apparatus according to a first embodiment of the present invention. In the figure, reference numeral 1 denotes the discharge of ballast water 2 from a ballast tank (not shown) of a ship outboard. The ballast pipe 1 is provided with a ballast pump 3. An ozone injection pipe 4 for injecting ozone and a steam for injecting steam are provided at an upstream side of the ballast pump 3. The injection pipes 5 are respectively connected. The ballast water 2 from the ballast tank is sterilized and purified by the ozone and steam injected from each of the injection pipes 4 and 5 while being sent through the ballast pipe 1, and is discharged outboard as purified water 6. It is being discharged.
[0021]
Next, the operation of the present embodiment will be described.
In purifying the ballast water 2, the ballast pump 3 is activated to discharge the ballast water 2 in the ballast tank outboard via the ballast pipe 1. At this time, ozone is injected from the ozone injection pipe 4 and steam is injected from the steam injection pipe 5 simultaneously with or before or after the ozone injection. Then, by the synergistic effect of ozone and steam, the decomposition of harmful substances and the sterilization and purification of microorganisms and the like are effectively performed, and the ballast water 2 flowing in the ballast pipe 1 is reliably purified. Then, the treated purified water 6 is discharged outboard.
[0022]
Hereinafter, the synergistic effect of ozone and steam will be described in detail with reference to FIG.
When ozone 11 is injected into the ballast water 2 from the ozone injection pipe 4, the cell membrane of microorganisms and the like in the ballast water 2 is attacked and damaged by the injected ozone. In the figure, reference numeral 12 indicates a damaged microorganism or the like.
[0023]
On the other hand, when the steam 13 is injected into the ballast water 2 from the steam injection pipe 5, the injected steam 13 expands in the ballast water 2, and bubbles are generated in the ballast water 2. In the drawing, reference numeral 14 indicates the generated bubbles.
[0024]
The bubble 14 is rapidly cooled by the ballast water 2 and collapses, and a non-equilibrium local field 15 including a gas phase reaction field 16 and a liquid phase reaction field 17 is generated. By the physicochemical action of the non-equilibrium local field 15, microorganisms and the like in the ballast water 2 are killed and inactivated, and harmful chemical substances are decomposed and water quality is purified.
[0025]
When the bubble 14 collapses, a shock wave 18 is generated. The shock wave 18 makes the ozone 11 finer and activated, and promotes dissolution in the ballast water 2. In the figure, reference numeral 19 indicates ozone whose dissolution has been promoted. Microorganisms and the like are physically destroyed by the shock wave 18. In the figure, reference numeral 20 indicates a physically destroyed microorganism or the like.
[0026]
In addition, the ozone 11 is converted by the shock wave 18 into a hydroxyl radical 21 having a stronger oxidizing power. The hydroxy radical 21 chemically kills microorganisms and decomposes harmful chemical substances. In the figure, reference numeral 22 indicates a chemically sterilized microorganism or the like, and in the figure, reference numeral 23 indicates a decomposed harmful chemical substance.
[0027]
As a result of the above overall operation, even the ballast water 2 having a high flow velocity is reliably purified within a short transport distance, and is discharged outboard as purified water 6.
[0028]
Thus, by using the ozone 11 and the steam 13 at the same time, it is possible to purify the ballast water 2 having a high flow velocity in a large amount. Therefore, the apparatus is completed only by connecting the ozone injection pipe 4 and the steam injection pipe 5 to the ballast pipe 1, and no special processing equipment is required. Further, since the amount of ozone used can be reduced, the size of the ozone generator can be reduced and the power consumption can be reduced.
[0029]
In addition, as for steam, since a boiler is usually installed as a main facility or ancillary equipment in a ship, it is not necessary to newly install a boiler by using steam from the boiler. For this reason, the cost can be significantly reduced in conjunction with the downsizing of the ozone generator.
[0030]
In the first embodiment, the case where the purified water 6 is obtained by using both steam and ozone has been described. However, as will be apparent from an example described later in detail, only purified steam is used. The desired water purification effect is obtained. Therefore, the purified water 6 may be obtained by injecting only steam into the ballast water 2.
[0031]
FIG. 3 shows a second embodiment of the present invention, in which an ozone injection pipe 4 is arranged close to a steam injection pipe 5, and ozone 11 injected into the ballast water 2 from the ozone injection pipe 4. And steam 13 injected from the steam injection pipe 5 into the ballast water 2.
In other respects, the configuration is the same as that of the first embodiment, and the operation is the same.
[0032]
When the steam 13 is injected from the steam injection pipe 5 into the ballast water 2, as the bubbles of the steam 13 collapse, the shock wave is generated downstream of the steam injection pipe 5 as shown in FIG. A region 31 will be formed. For this reason, if the ozone 11 injected into the ballast water 2 from the ozone injection pipe 4 is taken into the steam 13, the bubbles of the ozone 11 are also rapidly reduced by the shock wave accompanying the bubble collapse of the steam 13. Will be activated. In FIG. 3, reference numeral 32 indicates an ozone microbubble flow miniaturized by the shock wave.
[0033]
Thus, when the ozone 11 is miniaturized, the dissolution of the ozone 11 in the ballast water 2 is promoted, and the water purification effect of the ozone 11 can be improved.
[0034]
FIG. 4 shows a third embodiment of the present invention, in which an ultraviolet lamp 41 is provided in the ozone fine bubble stream 32 in the second embodiment, and steam 13 from the steam injection pipe 5 is provided. The ultraviolet rays 42 can be irradiated into the ozone microbubble flow 32 at the same time as or before or after the injection.
In other respects, the configuration is the same as that of the second embodiment, and the operation is the same.
[0035]
Since the ballast water 2 is irradiated with the ultraviolet rays 42, the water purification effect can be further improved. Moreover, since the ultraviolet rays 42 are radiated into the ozone microbubble flow 32, the ultraviolet rays 42 are radiated to the microorganisms and the like damaged by the steam 13 and the ozone 11, and the water purification efficiency by the ultraviolet rays 42 is increased. Can be improved.
[0036]
In each of the above embodiments, the purification process of the ballast water 2 of the ship has been described as an example. However, the water treatment of water supply and sewage plants, the water treatment of pools and hot springs, factories and livestock facilities, It can be similarly applied to wastewater treatment, seawater purification treatment for fishery processing, treatment of circulating water in reservoirs and water tanks, or purification treatment of lakes and marshes, and similar effects can be expected.
[0037]
【Example】
(First embodiment)
The present inventors conducted an experiment for purifying ballast water 2 of a ship using the water purification apparatus shown in FIG.
The ozone injection rate was 0.05 mg / liter (0.05 mg of ozone was injected per liter of ballast water), and the steam injection rate was 0.12 g / liter (0.12 g of steam was injected per liter of ballast water).
[0038]
As a result, damage to marine organisms such as phytoplankton, shelled dinoflagellates, and zooplankton (influence on the biological status of organisms such as cessation of movement, flagella shedding, and pigment decolorization) appears, and sufficient purification treatment is possible. confirmed.
[0039]
As a comparative example, when an experiment for purifying ballast water 2 was performed using only ozone, the ozone injection rate required to obtain the same purifying effect as described above was 1 mg / liter. It was also confirmed that the amount used could be reduced to 1/20.
[0040]
(Second embodiment)
The present inventors also used the water purification apparatus shown in FIG. 3 to supply steam 13 having a steam pressure of 0.55 to 0.65 MPa and a temperature of 100 to 110 ° C. from the steam injection pipe 5 at an injection rate of 20 kg / h. An experiment was performed to inject the ballast water 2 into the ballast water 2 and confirm how much the shock wave generation region 31 was formed downstream of the ballast water 2.
[0041]
As a result, it was confirmed that a rugby ball-shaped shock wave generation region 31 having a diameter of 100 mm and a length of 200 mm was formed around the axis of the steam injection pipe 5 as a center line.
[0042]
(Third embodiment)
The present inventors also prepared 80 liters of seawater containing 20 individuals / cc of artemia, which is a kind of zooplankton, and put it in a tank to conduct the following four types of experiments.
(Experiment 1)
Only steam was injected into the tank under the same conditions as in the second embodiment.
(Experiment 2)
In addition to Experiment 1, ozone was injected at an injection rate of 0.7 g / h.
(Experiment 3)
In addition to Experiment 1, ultraviolet rays were irradiated using a 20-w ultraviolet lamp.
(Experiment 4)
In addition to Experiment 2, ultraviolet rays were irradiated using a 20-w ultraviolet lamp.
[0043]
When the above four types of experiments were performed and the treatment rates (dead and damaged) of Artemia were measured, the results shown in Table 1 below were obtained.
[0044]
[Table 1]
Figure 2004160437
[0045]
As is clear from Table 1, it was confirmed that the desired water purification effect was obtained only with steam. In addition, it was also confirmed that an extremely good water purification effect was obtained by using steam and ozone in combination, and that the water purification effect could be further improved by adding ultraviolet irradiation.
[0046]
【The invention's effect】
As described above, according to the present invention, steam is injected into the treatment area where the water to be treated is present, so that bubbles of steam are generated during the treatment, Collapsed by quenching with water. Microorganisms and the like in the water to be treated are killed and inactivated by the physicochemical action in the equilibrium local field generated at that time, and harmful chemical substances are decomposed and the water quality is purified.
[0047]
According to the present invention, ozone is injected at the same time as or before or after the injection of steam, so that the ozone is miniaturized and activated by the shock wave accompanying the collapse of the vapor bubbles, and the ozone is injected into the water to be treated. Is promoted, and ozone is converted into hydroxy radicals having stronger oxidizing power, thereby improving the sterilizing and purifying effects of ozone on harmful substances and microorganisms.
[0048]
According to the present invention, since the ultraviolet rays are irradiated simultaneously with or before or after the injection of the steam, the sterilizing and purifying effects thereof can be improved as compared with the case where the ultraviolet rays are used alone.
[0049]
In the present invention, since the pipe to which the water to be treated is supplied is used as the treatment area, the water to be treated can be purified without providing a special treatment facility such as a water tank.
[0050]
The present invention also uses a tank in which water to be treated temporarily stays as a treatment area, so if there is already a treatment facility such as a tank, water purification can be efficiently performed using this treatment facility. Can do it.
[0051]
Further, in the present invention, when steam and ozone are used, ozone is involved in the injected steam, so that the ozone can be miniaturized and activated, and the ozone sterilization and purification effects can be further improved. Can be done.
[0052]
In the present invention, since the water to be treated which has been subjected to the steam injection treatment is irradiated with ultraviolet rays, the dead and inactivated microorganisms are irradiated with ultraviolet rays, so that sterilization and purification by ultraviolet rays can be efficiently performed. Can be performed.
[0053]
In the present invention, the water to be treated containing ozone gas microbubbled with steam is irradiated with ultraviolet rays, so that the sterilization and purification effects by ultraviolet rays can be further improved.
[Brief description of the drawings]
FIG. 1 is a configuration diagram showing a water purification device according to a first embodiment of the present invention.
FIG. 2 is an explanatory view showing a mechanism of water purification in the apparatus of FIG.
FIG. 3 is an explanatory diagram showing a second embodiment of the present invention.
FIG. 4 is an explanatory diagram showing a third embodiment of the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Ballast piping 2 Ballast water 3 Ballast pump 4 Ozone injection pipe 5 Ozone injection pipe 6 Purified water 11, 19 Ozone 12, 20, 22 Microorganisms 13 Steam 14 Bubbles 15 Non-equilibrium local field 16 Gas phase reaction field 17 Liquid phase reaction field 18 Shock wave 21 Hydroxy radical 23 Harmful chemical substance 31 Shock wave generation area 32 Ozone fine bubble flow 41 Ultraviolet lamp 42 Ultraviolet light

Claims (11)

被処理水が存在する処理領域内に、蒸気を注入することを特徴とする水浄化方法。A water purification method, wherein steam is injected into a treatment area where water to be treated is present. 蒸気の注入と同時または相前後してオゾンを注入することを特徴とする請求項1記載の水浄化方法。2. The water purification method according to claim 1, wherein the ozone is injected simultaneously with or before or after the injection of the steam. 蒸気の注入と同時または相前後して紫外線を照射することを特徴とする請求項1または2記載の水浄化方法。3. The water purification method according to claim 1, wherein the ultraviolet irradiation is performed simultaneously with or before or after the injection of the steam. 処理領域は、被処理水が送給される配管であることを特徴とする請求項1,2または3記載の水浄化方法。4. The water purification method according to claim 1, wherein the treatment area is a pipe through which the water to be treated is supplied. 処理領域は、被処理水が一時滞留するタンクであることを特徴とする請求項1,2または3記載の水浄化方法。4. The water purification method according to claim 1, wherein the treatment area is a tank in which water to be treated temporarily stays. 被処理水に蒸気を注入する蒸気注入手段を設けたことを特徴とする水浄化装置。A water purification apparatus, comprising: steam injection means for injecting steam into the water to be treated. 被処理水に蒸気の注入と同時または相前後してオゾンを注入するオゾン注入手段を設けたことを特徴とする請求項6記載の水浄化装置。7. The water purifying apparatus according to claim 6, further comprising an ozone injecting means for injecting ozone into the water to be treated at the same time as or before or after the steam is injected. オゾン注入手段は、蒸気注入手段から注入される蒸気に、注入されたオゾンを巻き込むことが可能な位置に配されることを特徴とする請求項7記載の水浄化装置。The water purifier according to claim 7, wherein the ozone injection means is arranged at a position where the injected ozone can be involved in the steam injected from the steam injection means. 被処理水に蒸気の注入と同時または相前後して紫外線を照射する紫外線照射手段を設けたことを特徴とする請求項6,7または8記載の水浄化装置。9. The water purification apparatus according to claim 6, further comprising an ultraviolet irradiation means for irradiating the treated water with ultraviolet light at the same time as or before or after injection of steam. 紫外線照射手段は、蒸気注入処理された被処理水に紫外線を照射することを特徴とする請求項9記載の水浄化装置。10. The water purifying apparatus according to claim 9, wherein the ultraviolet irradiation means irradiates the treated water subjected to the steam injection treatment with ultraviolet rays. 紫外線照射手段は、蒸気により微細気泡化されたオゾンガスを含有する被処理水に紫外線を照射することを特徴とする請求項9記載の水浄化装置。10. The water purification apparatus according to claim 9, wherein the ultraviolet irradiation means irradiates the water to be treated containing ozone gas finely foamed with steam with ultraviolet light.
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