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JP2001000974A - Treatment of ballast water and ship - Google Patents

Treatment of ballast water and ship

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Publication number
JP2001000974A
JP2001000974A JP11176544A JP17654499A JP2001000974A JP 2001000974 A JP2001000974 A JP 2001000974A JP 11176544 A JP11176544 A JP 11176544A JP 17654499 A JP17654499 A JP 17654499A JP 2001000974 A JP2001000974 A JP 2001000974A
Authority
JP
Japan
Prior art keywords
ballast water
ship
electrolytic cell
fixed
ballast
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
JP11176544A
Other languages
Japanese (ja)
Inventor
Yoshichika Noda
義親 野田
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.)
Konica Minolta Inc
Original Assignee
Konica Minolta Inc
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 Konica Minolta Inc filed Critical Konica Minolta Inc
Priority to JP11176544A priority Critical patent/JP2001000974A/en
Publication of JP2001000974A publication Critical patent/JP2001000974A/en
Pending legal-status Critical Current

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  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

PROBLEM TO BE SOLVED: To prevent the pollution of soil or seawater caused by treating ballast water by supplying ballast water for keeping the stability of a ship to the surface of the sea to a fixed bed type electrode electrolytic cell to treatmicroorganisms in ballast water. SOLUTION: A ballast tank 301 for housing ballast water 303 is disposed in the ship body 300 of a ship. The ballast water 303 is introduced into or discharged from the ballast tank 301 by the action of a pump 306 through a piping 320 and treated in the fixed bed type electrode electrolytic tank 304 disposed on the way of the piping 320 to kill microorganisms in the ballast water. The treated ballast water is supplied to the ballast tank 301. When the ship is loaded with ballast water 303 to navigate and arrives at a destination, a cargo is housed in the cargo storehouse 302 of the ship and, at this time, the ballast water 303 is discharged out of the ship through the piping 32 by the action of the pump 306. At this time, microorganisms in the ballast water 303 are killed by the fixed bed type electrode electrolytic cell 304 disposed in the route of the piping 320.

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、船舶の海面に対する安
定性を保つためのバラスト水が海水に廃棄され、海水が
微生物で汚染されることを防止するためのバラスト水の
処理方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of treating ballast water for preventing ballast water from being discarded in seawater for maintaining the stability of the ship against the sea surface and contaminating the seawater with microorganisms.

【0002】[0002]

【従来技術】バラスト水として通常海水が用いられる
が、荷物を船舶が陸揚げし、船舶の重量が軽くなり海水
面から浮くことを防止するため、この陸揚げ地の港の海
水が用いられる。陸揚げを済まし、バラスト水を大量に
積載した船舶は、目的地に着くと、そこで荷物を船揚げ
することになるが、このとき船揚げされる荷物の重量に
より船体が海水中に潜ることを防止するために、バラス
ト水は船舶から排出される。
2. Description of the Related Art Normally, seawater is used as ballast water. However, seawater from a port at the landing site is used in order to prevent a ship from unloading cargo, to reduce the weight of the ship and to float from the sea surface. After landing, a ship loaded with a large amount of ballast water will have its cargo unloaded when it reaches its destination, but the weight of the unloaded cargo will prevent the hull from diving into the seawater. To discharge the ballast water from the ship.

【0003】[0003]

【発明が解決しようとする課題】さて、この船舶の目的
地への航行中、海水中には、微生物が生息しており、こ
れは船舶が航行中に繁殖を繰り返し、バラスト水は汚染
されることになる。こうした汚染されたバラスト水を目
的地で、そのまま廃棄すると目的地の土壌、海水を汚染
し、生態系を破壊することになり極めて問題である。
During the navigation of the ship to the destination, microorganisms inhabit the seawater, which repeats breeding while the ship is navigating, and the ballast water is polluted. Will be. Discarding such contaminated ballast water at the destination as it is is extremely problematic because it will contaminate the soil and seawater at the destination and destroy the ecosystem.

【0004】[0004]

【発明の目的】本発明は、上記の問題を鑑み、バラスト
水の廃棄による土壌や海水の汚染を防止するための方
法、船舶を提供するものである。
SUMMARY OF THE INVENTION In view of the above problems, the present invention provides a method and a ship for preventing soil and seawater from being contaminated by ballast water disposal.

【0005】[0005]

【問題点を解決するための手段】(1) 船舶の海面に
対する安定性を保つためのバラスト水を固定床型電極電
解槽に供給し、バラスト水中の微生物を処理することを
特徴とするバラスト水の処理方法。 (2) 前記バラスト水を船舶の中で前記固定床型電極
電解槽で処理することを特徴とする(1)のバラスト水
の処理方法。 (3) 前記バラスト水を船舶の航行中に前記固定床型
電極電解槽で処理することを特徴とする(2)のバラス
ト水の処理方法。 (4) 前記バラスト水を船舶の外で前記固定床型電極
電解槽で処理することを特徴とする(1)のバラスト水
の処理方法。 (5) 海面に対する安定性を保つためのバラスト水中
の微生物を処理する固定床型電極電解槽を有することを
特徴とする船舶。
[Means for Solving the Problems] (1) Ballast water characterized by supplying ballast water for maintaining the stability of a ship to the sea surface to a fixed-bed electrode electrolytic cell and treating microorganisms in the ballast water. Processing method. (2) The method for treating ballast water according to (1), wherein the ballast water is treated in the fixed-bed electrode electrolytic cell in a ship. (3) The method for treating ballast water according to (2), wherein the ballast water is treated in the fixed-bed-type electrode electrolytic cell while the ship is sailing. (4) The method for treating ballast water according to (1), wherein the ballast water is treated outside the vessel in the fixed-bed electrode electrolytic cell. (5) A ship having a fixed-bed electrode electrolytic cell for treating microorganisms in ballast water for maintaining stability against the sea surface.

【0006】[0006]

【発明の実施の形態】以下本発明を詳細に説明する。本
発明は、船舶の海面に対する安定性を保つためのバラス
ト水を固定床型電極電解槽に供給し、バラスト水中の微
生物を処理することを特徴とするものである。本発明の
微生物には、細菌(バクテリア)、プランクトン、菌、
糸状菌(黴)、大腸菌、酵母、変形菌、単細胞の藻類、
原生動物、ウイルス等が含まれる。バラスト水を固定床
型電極電解槽に供給すると、バラスト水中の微生物は液
流動によって前記電解槽の固定床型電極の陽極や陰極に
接触し、それらの表面で高電位のエネルギー供給を受け
強力な酸化還元反応が微生物細胞内で生じ、その活動が
弱まったり微生物自身が死滅して滅菌が行われる。本発
明の固定床型電極電解槽は、分極現象を生じる固定床型
電極と、固定床型電極を分極させる給電用電極を含み、
該固定床型電極としては、前記バラスト水が透過可能な
多孔質材料、例えばフェルト状、織布状、多孔質ブロッ
ク状等の形状を有する活性炭、グラファイト、炭素繊維
等の炭素系材料から、あるいは同形状を有するニッケ
ル、銅、ステンレス、鉄、チタン等の金属材料、更にそ
れらに貴金属のコーティングを施した材料などが用いら
れ、また給電用電極としては、平板状又はエキスパンド
メッシュ状やパーフォレーティッドプレート状等の多孔
板体から成る材料が用いられる。前記固定床型電極とし
て活性炭、グラファイト、炭素繊維等の炭素系材料を使
用しかつ陽極から酸素ガスを発生させながら被処理水を
処理する場合には、前記固定床型電極が酸素ガスにより
酸化され炭酸ガスとして溶解することがある。これを防
止するためには前記固定床型電極の陽分極する側にチタ
ン等の基材上に酸化イリジウム、酸化ルテニウム等の白
金族金属酸化物を被覆し通常不溶性金属電極として使用
される多孔質材料を接触状態で設置し、酸素発生が主と
して該多孔質材料上で生ずるようにすればよい。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail. The present invention is characterized in that ballast water for maintaining stability on the sea surface of a ship is supplied to a fixed-bed electrode electrolytic cell to treat microorganisms in ballast water. The microorganism of the present invention includes bacteria (bacteria), plankton, fungi,
Filamentous fungi (fungi), Escherichia coli, yeast, deformed fungi, unicellular algae,
Protozoa, viruses and the like are included. When ballast water is supplied to the fixed-bed type electrode electrolytic cell, microorganisms in the ballast water contact the anode and cathode of the fixed-bed type electrode of the electrolytic cell by liquid flow, and receive high-potential energy supply on their surface to generate strong power. An oxidation-reduction reaction occurs in the cells of the microorganism, and its activity is weakened or the microorganism itself is killed and sterilized. The fixed bed electrode electrolyzer of the present invention includes a fixed bed electrode that causes a polarization phenomenon, and a power supply electrode that polarizes the fixed bed electrode.
As the fixed-bed electrode, a porous material through which the ballast water can pass, for example, felt, woven, activated carbon having a shape such as a porous block, graphite, carbon-based material such as carbon fiber, or Metal materials having the same shape, such as nickel, copper, stainless steel, iron, titanium, etc., and materials coated with a noble metal are used, and the power supply electrode is a flat plate, expanded mesh, or perforated. A material made of a perforated plate such as a plate is used. When using a carbon-based material such as activated carbon, graphite, and carbon fiber as the fixed bed electrode and treating the water to be treated while generating oxygen gas from the anode, the fixed bed electrode is oxidized by oxygen gas. May dissolve as carbon dioxide. In order to prevent this, a porous material usually used as an insoluble metal electrode is formed by coating a platinum group metal oxide such as iridium oxide or ruthenium oxide on a substrate such as titanium on the side of the fixed bed type electrode which is positively polarized. The materials may be placed in contact so that oxygen evolution occurs primarily on the porous material.

【0007】前記固定床型電極は、その平均開孔径を所
定の大きさにしておくことが好ましい。固定床型電極の
開孔径が大きいと該電極にバラスト水中の微生物が接触
することなく電解槽を通過しやすくなるため微生物の死
滅効果が低下する。逆に開孔径が小さすぎるとバラスト
水が固定床型電極を流通することができずに電解電圧の
上昇や電解槽内での液流の圧力損失を招いてしまう。特
に炭素質の固定床型電極を用いる場合は、その平均開孔
径を25〜125 μmとすることが望ましい。次に添付図面
に基づいて本発明に使用できる電解槽の好ましい例を説
明するが、本発明に使用できる電解槽は、この電解槽に
限定されるものではない。
[0007] It is preferable that the fixed-bed type electrode has a predetermined average opening diameter. If the fixed-bed type electrode has a large opening diameter, microorganisms in ballast water can easily pass through the electrolytic cell without contacting the electrode, so that the killing effect of the microorganisms is reduced. Conversely, if the opening diameter is too small, the ballast water cannot flow through the fixed-bed electrode, causing an increase in the electrolytic voltage and a pressure loss of the liquid flow in the electrolytic cell. In particular, when a carbonaceous fixed bed electrode is used, it is desirable that the average pore diameter is 25 to 125 μm. Next, preferred examples of the electrolytic cell that can be used in the present invention will be described with reference to the accompanying drawings, but the electrolytic cell that can be used in the present invention is not limited to this electrolytic cell.

【0008】図1は、本発明方法の電解槽として使用可
能な単極式の固定床型電極電解槽の第1の例を示す概略
縦断面図である。
FIG. 1 is a schematic longitudinal sectional view showing a first example of a monopolar fixed-bed type electrode electrolytic cell which can be used as an electrolytic cell in the method of the present invention.

【0009】底板中央にバラスト水供給口1を、又天板
中央にバラスト水取出口2をそれぞれ有する円筒状の電
解槽本体3内の下部には、炭素質材料や金属焼結体等か
ら形成される短寸円柱形の多孔質固定床型陰極4が前記
本体3の内壁と実質的に液流動の生じないような僅かな
間隙しか形成しないように収容され、該陰極4上には若
干の間隙を介して例えばメッシュ状の白金族金属酸化物
被覆チタン材から成る陽極5が収容されている。前記電
解槽本体3は、長期間の使用又は再度の使用にも耐え得
る電気絶縁材料で形成することが好ましく、特に合成樹
脂であるポリエピクロルヒドリン、ポリビニルメタクリ
レート、ポリエチレン、ポリプロピレン、ポリ塩化ビニ
ル、ポリ塩化エチレン、フェノール−ホルムアルデヒド
樹脂、ポリアクリロニトリル樹脂等が好ましく使用でき
る。
A lower portion of a cylindrical electrolytic cell body 3 having a ballast water supply port 1 in the center of the bottom plate and a ballast water outlet 2 in the center of the top plate is formed of a carbonaceous material, a metal sintered body or the like. The small cylindrical porous fixed bed type cathode 4 to be formed is accommodated so as to form only a small gap with the inner wall of the main body 3 so that liquid flow does not substantially occur. An anode 5 made of, for example, a mesh-shaped platinum group metal oxide-coated titanium material is accommodated through the gap. The electrolytic cell main body 3 is preferably formed of an electrically insulating material that can withstand long-term use or re-use. Particularly, synthetic resins such as polyepichlorohydrin, polyvinyl methacrylate, polyethylene, polypropylene, polyvinyl chloride, and polyvinyl chloride Ethylene, phenol-formaldehyde resin, polyacrylonitrile resin and the like can be preferably used.

【0010】そして、バラスト水中の微生物はバラスト
水供給口1からバラスト水取出口2までを通過する際
に、多孔質固定床型陰極4に接触して死滅する。
When the microorganisms in the ballast water pass from the ballast water supply port 1 to the ballast water outlet 2, they contact the porous fixed-bed cathode 4 and die.

【0011】図2は、本発明方法の電解槽として使用可
能な複極式(1つの電極が陽極と陰極とに分極するこ
と)の固定床型電極電解槽の一例を示す概略縦断面図で
ある。
FIG. 2 is a schematic vertical sectional view showing an example of a bipolar electrode (one electrode is polarized into an anode and a cathode) fixed-bed type electrode electrolytic cell which can be used as an electrolytic cell in the method of the present invention. is there.

【0012】上下にフランジ91を有する円筒形の電解槽
本体92の内部上端近傍及び下端近傍にはそれぞれメッシ
ュ状の給電用陽極ターミナル93と給電用陰極ターミナル
94が設けられている。該両電極ターミナル93、94間には
複数個の図示の例では3個のスポンジ状の固定床95が積
層され、かつ該固定床95間及び該固定床95と前記両電極
ターミナル93、94間に4枚のメッシュ状隔膜又はスペー
サー96が挟持されている。各固定床95は電解槽本体92の
内壁に密着し固定床95の内部を通過せず、固定床95と電
解槽本体92の側壁との間を流れる被処理水の漏洩流がな
るべく少なくなるように配置されている。
A meshed power supply anode terminal 93 and a power supply cathode terminal are provided near the upper end and the lower end of a cylindrical electrolytic cell main body 92 having a flange 91 on the upper and lower sides, respectively.
94 are provided. In the illustrated example, a plurality of sponge-like fixed beds 95 are laminated between the electrode terminals 93 and 94, and between the fixed bed 95 and between the fixed bed 95 and the electrode terminals 93 and 94. Are sandwiched between four mesh-shaped diaphragms or spacers 96. Each fixed bed 95 is in close contact with the inner wall of the electrolytic cell main body 92 and does not pass through the inside of the fixed bed 95, so that the leakage flow of the water to be treated flowing between the fixed bed 95 and the side wall of the electrolytic cell main body 92 is minimized. Are located in

【0013】このような構成から成る電解槽に下方から
矢印で示すようにバラスト水を供給しながら通電を行う
と、前記各固定床95が図示の如く下面が正に上面が負に
分極して各固定床95の上面に多孔質陰極、下面に多孔質
陽極が形成され、前記バラスト水中の微生物はこれらに
接触して死滅する。図3は、本発明方法に使用できる複
極式の固定床型電極電解槽の他の例を示すもので、該電
解槽は図2の電解槽の固定床95の給電用陰極94に向かう
側つまり陽分極する側にメッシュ状の不溶性金属電極97
を密着状態で設置したものであり、他の部材は図2と同
一であるので同一符号を付して説明を省略する。直流電
圧が印加された固定床95はその両端部において最も大き
く分極が生じ、ガス発生が伴う場合には該両端部におい
てガス発生が生じ易い。従って最も強く陽分極するつま
り最も激しく酸素ガスが発生する固定床95の給電用陰極
94に向かう端部には最も速くかつ激しく酸化反応や電極
基材の溶解反応が生じる。図示の通りこの部分に不溶性
金属電極97を設置しておくと、該不溶性金属電極97の酸
素発生過電圧が固定床95を形成する炭素系材料の前記過
電圧より低いため殆どの酸素ガスが前記不溶性金属電極
97から発生し固定床95は殆ど酸素ガスと接触しなくなる
ため、前記固定床95の溶解は効果的に抑制される。又該
電解槽92に供給されたバラスト水中の微生物は2場合と
同様に処理され死滅することになる。
When power is supplied to the electrolytic cell having such a configuration while supplying ballast water from below as indicated by an arrow, when the fixed bed 95 is polarized, the lower surface becomes positive and the upper surface becomes negative as shown in the figure. A porous cathode is formed on the upper surface of each fixed bed 95, and a porous anode is formed on the lower surface, and the microorganisms in the ballast water are killed by contacting them. FIG. 3 shows another example of a bipolar fixed-bed type electrode electrolytic cell which can be used in the method of the present invention. The electrolytic cell is a side of the fixed bed 95 of the electrolytic cell of FIG. In other words, the mesh-shaped insoluble metal electrode 97
Are provided in close contact with each other, and the other members are the same as those in FIG. The fixed bed 95 to which the DC voltage is applied has the largest polarization at both ends, and when gas is generated, gas is likely to be generated at both ends. Therefore, the feeding cathode of the fixed bed 95 which is the most strongly anodic polarized, that is, generates the most intense oxygen gas
At the end toward 94, the oxidation reaction and the dissolution reaction of the electrode substrate occur fastest and violently. As shown in the figure, if an insoluble metal electrode 97 is installed in this portion, most of the oxygen gas is removed from the insoluble metal electrode 97 because the overvoltage of oxygen generation of the insoluble metal electrode 97 is lower than that of the carbon-based material forming the fixed bed 95. electrode
Since the fixed bed 95 is hardly brought into contact with the oxygen gas and is generated from 97, the dissolution of the fixed bed 95 is effectively suppressed. Further, the microorganisms in the ballast water supplied to the electrolytic cell 92 are treated and killed in the same manner as in the second case.

【0014】図4に図示された電解槽は図2の電解槽を
改良してフィルタを設置したものであり、図2図に示さ
れた電解槽の部材と同一部材には同一符号を付して説明
を省略する。
The electrolytic cell shown in FIG. 4 is a modification of the electrolytic cell of FIG. 2 and is provided with a filter. The same members as those of the electrolytic cell shown in FIG. The description is omitted.

【0015】電解槽本体92の上部のフランジ91上には、
中央部に上向き筒体211 が形成された蓋体212 が載置さ
れ、該筒体211 の上端のフランジ部と被処理水排出管21
3 の下端のフランジ部間にはフィルタ214 が挟持されて
いる。215 は、中央下面に被処理水供給管216 が下向き
に形成された底板である。このような構成から成る電解
槽に下方から矢印で示すようにバラスト水を供給しなが
ら通電を行うと、前記各固定床95が図示の如く下面が正
に上面が負に分極して固定床95内及び固定床95間に電位
が生じ、該電解槽内を流通するバラスト水はこの電位を
有する固定床95に接触してその中に含有される微生物の
処理が行われて、該電解槽本体92の被処理水排出管213
から取り出される。この処理で生じた微生物の死骸等の
固形不純物は、フィルタ214 を通過する際に濾過される
ので、電解槽からそとに微生物の死骸等の固形不純物が
取り出されなくなる。
On the upper flange 91 of the electrolytic cell body 92,
A lid 212 having an upwardly-facing cylinder 211 formed in the center is mounted thereon, and a flange at the upper end of the cylinder 211 and the treated water discharge pipe 21 are provided.
A filter 214 is sandwiched between the flanges at the lower end of the filter 3. Reference numeral 215 denotes a bottom plate in which a treated water supply pipe 216 is formed downward on the center lower surface. When current is supplied to the electrolytic cell having such a configuration while supplying ballast water from below as indicated by an arrow, the fixed beds 95 are polarized such that the lower surface is positive and the upper surface is negative, as shown in the figure. A potential is generated between the inside and the fixed bed 95, and the ballast water flowing through the electrolytic cell contacts the fixed bed 95 having this potential to treat microorganisms contained therein, and the electrolytic cell body 92 treated water discharge pipes 213
Taken out of Solid impurities such as dead microorganisms generated by this treatment are filtered when passing through the filter 214, so that solid impurities such as dead microorganisms cannot be taken out of the electrolytic cell.

【0016】図5は、実際に船舶で用いられるバラスト
水中の微生物を死滅処理する方法を示す図である。
FIG. 5 is a diagram showing a method for killing microorganisms in ballast water actually used in a ship.

【0017】船舶の船体300中には、バラスト水303を格
納するバラストタンク301が設けられている。バラスト
水303は、配管320を通じて、ポンプ306の作用によりバ
ラストタンク301中に入れられたり(矢印X'方向)、排
出されたり(矢印X方向)する。尚、ポンプ306の作動
時以外にバラスト水の行き来を防止するために弁305が
設けられている。
A ballast tank 301 for storing ballast water 303 is provided in the hull 300 of the ship. The ballast water 303 is put into the ballast tank 301 (in the direction of the arrow X ′) or discharged (in the direction of the arrow X) by the action of the pump 306 through the pipe 320. A valve 305 is provided to prevent the ballast water from flowing except when the pump 306 is operating.

【0018】まず、バラスト水は、バラストタンク301
に供給される前に、配管320の途中に設けられた固定床
型電極電解槽304で処理され、微生物が死滅させられ
る。そして、固定床型電極電解槽304で処理された後に
バラストタンク301に供給される。
First, ballast water is supplied to a ballast tank 301.
Before being supplied to the pipe, the mixture is treated in a fixed-bed type electrode electrolytic cell 304 provided in the middle of the pipe 320 to kill microorganisms. Then, after being processed in the fixed-bed type electrode electrolytic cell 304, it is supplied to the ballast tank 301.

【0019】また、船舶がバラスト水303を積み、航行
し、目的地に着くと荷物格納庫302に、荷物が格納され
ることになるが、その際にバラスト水303は、ポンプ306
の作用により配管320を通じての外に排出される。この
とき、配管320の経路に設けられた固定床型電極電解槽3
04によりバラスト水中の微生物が死滅させられる。
Further, when the ship loads the ballast water 303, sails, and arrives at the destination, the luggage is stored in the luggage storage 302. At this time, the ballast water 303 is pumped by the pump 306.
Is discharged outside through the pipe 320. At this time, the fixed-bed type electrode electrolytic cell 3 provided in the path of the pipe 320
04 kills microorganisms in ballast water.

【0020】上記の例では、固定床型電極電解槽304
は、バラスト水303の船内、船外への通行のためにバラ
ストタンク301と船外を結ぶ配管320の船内にある一部に
設けられているが、これに限らず、船外に、例えば港に
固定床型電極電解槽304を用意しておき、これにより微
生物の死滅処理がなされたバラスト水を船内に導入する
ようにしたり、また船外に排出されたバラスト水中の微
生物を死滅処理するようにしてもよい。
In the above example, the fixed-bed type electrode electrolytic cell 304
The ballast water 303 is provided on a part of the piping 320 connecting the ballast tank 301 and the outboard for passage to the outside of the ballast water 303, but is not limited thereto. A fixed-bed type electrode electrolytic cell 304 is prepared in advance, so that the ballast water treated to kill microorganisms is introduced into the ship, or the microorganisms in the ballast water discharged outboard are killed. It may be.

【0021】また、船舶の航行中にバラスト水中の微生
物を死滅処理ようにしてもよい。例えば、バラストタン
ク301に連結されたバラスト水303の循環用の配管321を
設け、ポンプ309の作用によりバラスト水303を循環させ
て(矢印Y、Y'参照)、配管321の経路の途中に設けら
れた固定床型電極電解槽307で処理するようにしてもよ
い。尚、ポンプによる循環時以外は、配管321でバラス
ト水303が行き来するのを防止するため弁308が設けられ
ている。
Further, the microorganisms in the ballast water may be killed during the navigation of the ship. For example, a pipe 321 for circulating the ballast water 303 connected to the ballast tank 301 is provided, and the ballast water 303 is circulated by the action of the pump 309 (see arrows Y and Y ') and provided in the middle of the path of the pipe 321. The treatment may be performed in the fixed bed type electrode electrolytic cell 307 provided. Note that a valve 308 is provided to prevent the ballast water 303 from flowing back and forth in the pipe 321 except during circulation by the pump.

【0022】以上の説明中の固定床型電極電解槽304、3
07としては、図1乃至図4に示されるものが用いられる
が、これらに限られるものではない。
In the above description, the fixed-bed type electrode electrolyzers 304, 3
1 to 4 are used as 07, but the present invention is not limited to these.

【0023】[0023]

【発明の効果】本発明によれは、バラスト水の廃棄によ
る土壌や海水の汚染を防止することができる。
According to the present invention, soil and seawater pollution due to ballast water disposal can be prevented.

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

【図1】本発明方法の電解槽として使用可能な単極式固
定床型電極電解槽の例を示す概略縦断面図。
FIG. 1 is a schematic longitudinal sectional view showing an example of a monopolar fixed-bed electrode electrolytic cell that can be used as an electrolytic cell in the method of the present invention.

【図2】本発明方法の電解槽として使用可能な複極式固
定床型電極電解槽の第1の例を示す概略縦断面図。
FIG. 2 is a schematic longitudinal sectional view showing a first example of a bipolar fixed-bed electrode electrolytic cell that can be used as an electrolytic cell in the method of the present invention.

【図3】同じく第2の例を示す概略縦断面図。FIG. 3 is a schematic longitudinal sectional view showing a second example.

【図4】同じく第3の例を示す概略断面図。FIG. 4 is a schematic cross-sectional view showing a third example.

【図5】バラスト水中の微生物を死滅処理する方法を示
す図
FIG. 5 is a diagram showing a method for killing microorganisms in ballast water.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 船舶の海面に対する安定性を保つための
バラスト水を固定床型電極電解槽に供給し、バラスト水
中の微生物を処理することを特徴とするバラスト水の処
理方法。
1. A method for treating ballast water, comprising supplying ballast water for maintaining stability to the sea surface of a ship to a fixed-bed electrode electrolytic cell and treating microorganisms in the ballast water.
【請求項2】 前記バラスト水を船舶の中で前記固定床
型電極電解槽で処理することを特徴とする請求項1のバ
ラスト水の処理方法。
2. The method for treating ballast water according to claim 1, wherein the ballast water is treated in the fixed-bed electrode electrolytic cell in a ship.
【請求項3】 前記バラスト水を船舶の航行中に前記固
定床型電極電解槽で処理することを特徴とする請求項2
のバラスト水の処理方法。
3. The fixed ball electrode electrolyzer according to claim 2, wherein the ballast water is treated in the fixed-bed type electrode electrolytic cell during navigation of a ship.
Ballast water treatment method.
【請求項4】 前記バラスト水を船舶の外で前記固定床
型電極電解槽で処理することを特徴とする請求項1のバ
ラスト水の処理方法。
4. The method for treating ballast water according to claim 1, wherein the ballast water is treated outside the vessel in the fixed-bed electrode electrolytic cell.
【請求項5】 海面に対する安定性を保つためのバラス
ト水中の微生物を処理する固定床型電極電解槽を有する
ことを特徴とする船舶。
5. A ship having a fixed-bed electrode electrolytic cell for treating microorganisms in ballast water for maintaining stability to the sea surface.
JP11176544A 1999-06-23 1999-06-23 Treatment of ballast water and ship Pending JP2001000974A (en)

Priority Applications (1)

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Publication Number Publication Date
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Country Link
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Publication number Priority date Publication date Assignee Title
WO2003018394A1 (en) * 2001-08-28 2003-03-06 Statoil Asa Ballast water exchange
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