JP2007090144A - Filtering apparatus for ballast water - Google Patents

Filtering apparatus for ballast water Download PDF

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JP2007090144A
JP2007090144A JP2005279659A JP2005279659A JP2007090144A JP 2007090144 A JP2007090144 A JP 2007090144A JP 2005279659 A JP2005279659 A JP 2005279659A JP 2005279659 A JP2005279659 A JP 2005279659A JP 2007090144 A JP2007090144 A JP 2007090144A
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ballast water
specific gravity
slit
foreign matter
high specific
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JP4759669B2 (en
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Yoshiyuki Inohara
祥行 猪原
Nobuhiko Fujiki
信彦 藤木
Makiko Inoue
真紀子 井上
Takeo Aya
威雄 綾
Kenji Yamane
健次 山根
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National Maritime Research Institute
Daiko Sangyo Co Ltd
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National Maritime Research Institute
Daiko Sangyo Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a centrifugal filtering apparatus especially separating and removing high-specific-gravity foreign matter from ballast water. <P>SOLUTION: The centrifugal filtering apparatus 1 is used to separate and remove high-specific-gravity sludge, e.g. sludge, from ballast water taken. The cylindrical body 11 of the apparatus 1 is connected to an inlet conduit 12 in the lower part and to an outlet conduit 13 in the upper part, and ballast water W fed from the inlet conduit 12 is raised while swirling along the side surface 111 and discharged from the outlet conduit 13. A slit 6 intersecting with the side surface 111 in the swirling direction of the ballast water W is disposed. High-specific-gravity foreign matter, e.g. sludge, is released from the slit 16 out of the cylindrical body 11 by utilizing the centrifugal force produced by the swirling with ballast the water W and removed. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、取水したバラスト水から汚泥をはじめとする高比重異物を分離、除去する遠心分離型の濾過装置に関する。本発明に言う「高比重異物」は、バラスト水(海水)に比べて比重が高く、濾過により物理的にバラスト水と分離可能な異物を意味する。   The present invention relates to a centrifugal type filtration apparatus that separates and removes high specific gravity foreign substances such as sludge from water taken in ballast water. The “high specific gravity foreign matter” referred to in the present invention means a foreign matter that has a higher specific gravity than ballast water (seawater) and can be physically separated from the ballast water by filtration.

船舶において、取水したバラスト水から異物を分離、除去するため、取水口からバラストタンクへ至る取水経路に濾過装置を介在させる。特に汚泥をはじめとする高比重異物(以下、高比重異物で代表)は、バラストタンクの容積を減少させたり、バラストタンク内の発錆を招くことから、十分に除去されることが望まれる。こうした高比重異物を分離、除去する濾過装置としては、例えば特許文献1に見られるように、単純に「こし網(スクリーンフィルタ)」を用いる構成がある。しかし、スクリーンフィルタは目詰まりしやすいため、バラスト水から高比重異物を分離、除去する濾過装置としては、特許文献2に見られる遠心分離型が好ましい。   In a ship, in order to separate and remove foreign substances from the taken ballast water, a filtration device is interposed in the water intake path from the water intake to the ballast tank. In particular, high specific gravity foreign matters such as sludge (hereinafter represented by high specific gravity foreign materials) are desirably removed sufficiently because they reduce the volume of the ballast tank and cause rusting in the ballast tank. As a filtering device that separates and removes such a high specific gravity foreign substance, for example, as seen in Patent Document 1, there is a configuration in which a “strain net (screen filter)” is simply used. However, since the screen filter is easily clogged, the centrifugal separation type found in Patent Document 2 is preferable as a filtration device that separates and removes the high specific gravity foreign matter from the ballast water.

遠心分離型の濾過装置は、下方に絞り形状の略円錐本体に送り込んだバラスト水を旋回させ、遠心力により高比重異物を半径方向外側にあたる側面に集め(遠心分離作用)、旋回中心付近のバラスト水から前記高比重異物を分離する。略円錐本体は下方に絞り形状になっているから、旋回する高比重異物は失速しながら沈降し、略円錐本体の底面から除去される。特許文献2が開示する濾過装置(サイクロンセパレータ)は、略円錐本体からバラストタンクに延びる出口管路(給水管)を絞ることにより、略円錐本体からバラスト水を送り出しにくくし、バラスト水からの高比重異物の分離効果を高めるとしている。   Centrifugal type filtration device swirls ballast water sent to a substantially conical main body in the downward shape, collects high-specific gravity foreign substances on the side of the outer side in the radial direction by centrifugal force (centrifugal action), and ballast near the swivel center The high specific gravity foreign matter is separated from water. Since the substantially conical body has a downwardly drawn shape, the rotating high-specific gravity foreign matter settles while stalling and is removed from the bottom surface of the substantially conical body. The filtration device (cyclone separator) disclosed in Patent Document 2 makes it difficult to send ballast water from the substantially conical body by narrowing an outlet pipe (water supply pipe) extending from the substantially conical body to the ballast tank. The specific gravity foreign matter separation effect is enhanced.

特開平05-116675号公報Japanese Patent Laid-Open No. 05-116675 特開平05-124573号公報JP 05-124573 A

遠心分離型の濾過装置は、遠心分離作用により、バラスト水と高比重異物とを半径方向内外に分離する。高比重異物を除去するには、旋回する高比重異物を失速させながら沈降させる必要があるが、バラスト水中における高比重異物の沈降は緩慢であり、再びバラスト水中に混ざり合う虞がある。特許文献2にいう「高比重異物を分離したバラスト水を送り出しにくくして分離効果を高める」とは、バラスト水の送り出しに伴う高比重異物の吸い上げを防止する働きを意味すると考えられるが、依然高比重異物の除去は沈降に頼っている。そこで、バラスト水から特に高比重異物を分離、除去する遠心分離型の濾過装置について、前記高比重異物を分離後、確実に除去する構成又は構造を検討した。   The centrifugal filtration device separates the ballast water and the high specific gravity foreign substance inward and outward in the radial direction by a centrifugal separation action. In order to remove the high-specific gravity foreign matter, it is necessary to settle the swirling high-specific gravity foreign matter while stalling. However, the sedimentation of the high-specific gravity foreign matter in the ballast water is slow and may be mixed with the ballast water again. Although it is considered that the phrase “to increase the separation effect by making it difficult to send out the ballast water from which the high specific gravity foreign matter has been separated” as referred to in Patent Document 2, it is considered to mean the function of preventing the high specific gravity foreign matter from being sucked up when the ballast water is sent out. The removal of high specific gravity foreign substances relies on sedimentation. Therefore, a configuration or structure for reliably removing the high-specific gravity foreign matter after separating the high-specific gravity foreign matter was examined for a centrifugal filter device that separates and removes the high-specific gravity foreign matter from the ballast water.

検討の結果開発したものが、取水したバラスト水から汚泥をはじめとする高比重汚泥を分離、除去する遠心分離型の濾過装置であって、円筒本体は下方に入口管路、上方に出口管路を接続し、入口管路から送り込んだバラスト水を側面に沿って旋回させながら上昇させ、出口管路から送り出すようにして、前記側面にバラスト水の旋回方向に交差するスリットを設け、汚泥をはじめとする高比重異物を、バラスト水と共に旋回することによる遠心力を利用し、前記スリットから円筒本体の外部に離脱させて、除去するバラスト水の濾過装置である。スリットから円筒本体の外部に離脱した高比重異物は、例えば円筒本体に付設した異物溜まりに蓄積させ、一定量蓄積した後に適宜廃棄すればよい。   What was developed as a result of the study is a centrifugal type filtration device that separates and removes sludge and other high-density sludge from the collected ballast water. The cylindrical body has an inlet pipe on the bottom and an outlet pipe on the top. The ballast water sent from the inlet pipe is raised while swirling along the side surface, and is sent out from the outlet pipe. This is a ballast water filtration device that uses the centrifugal force generated by swirling the high specific gravity foreign material together with the ballast water to remove it from the slit to the outside of the cylindrical body. The high-specific gravity foreign matter that has left the outside of the cylindrical main body from the slit may be accumulated in, for example, a foreign matter reservoir attached to the cylindrical main body, and may be discarded as appropriate after accumulating a certain amount.

本発明の濾過装置は、遠心分離作用により半径方向外側にあたる側面に集まる高比重異物を、前記側面に設けたスリットから円筒本体の外部に離脱させて分離し、同時に除去する。これから、スリットはバラスト水の旋回方向に交差して延在する、好ましくは前記旋回方向に略直交して延在することが望ましい。こうしたスリットによる高比重異物の分離、除去を用いたことにより、本発明の濾過装置は、バラスト水から分離した高比重異物を失速させて沈降させる必要がなく、入口管路の下方の延在部分を省略して、小型化できる。また、高比重異物を失速させる必要がないから、装置本体も略円錐本体ではなく、円筒本体として、小型化を図りながら必要十分な容積を確保できる。   The filtering device of the present invention separates and removes high specific gravity foreign substances gathering on the side surface that is radially outward due to the centrifugal separation action by separating them from the slit provided on the side surface to the outside of the cylindrical body. From this, it is desirable that the slit extends so as to intersect with the swirling direction of the ballast water, and preferably approximately perpendicular to the swirling direction. By using such separation / removal of high-specific gravity foreign matter by the slit, the filtration device of the present invention does not need to stall the high-specific gravity foreign matter separated from the ballast water and settle it, and the extended portion below the inlet pipe The size can be reduced by omitting. Further, since it is not necessary to stall the high specific gravity foreign substance, the apparatus main body is not a substantially conical main body but a cylindrical main body, so that a necessary and sufficient volume can be ensured while downsizing.

旋回途中のバラスト水から直接高比重異物を分離、除去する本発明の濾過装置は、入口管路は、円筒本体の側面の下方にこの側面の接線方向に接続し、出口管路は、円筒本体の上面に接続する。これは、従来の遠心分離型の濾過装置が、入口管路より出口管路の開口端を低くしている構成と異なる。これにより、バラスト水は旋回しながら上昇していくため、円筒本体の内部上方の旋回中心付近は高比重異物を含まないバラスト水のみとなり、高比重異物を分離したバラスト水のみを出口管路から送り出すことができる。   In the filtering device of the present invention, which separates and removes high specific gravity foreign substances directly from the ballast water in the middle of turning, the inlet pipe is connected to the tangential direction of this side below the side of the cylindrical main body, and the outlet pipe is connected to the cylindrical main body. Connect to the top of the. This is different from a configuration in which a conventional centrifugal separator has a lower opening end of an outlet pipe than an inlet pipe. As a result, the ballast water rises while swirling, so that only the ballast water that does not contain high specific gravity foreign matter is present in the vicinity of the swivel center above the inside of the cylindrical body, and only the ballast water from which high specific gravity foreign matter has been separated is removed from the outlet pipe. Can be sent out.

また、本発明の濾過装置では、旋回するバラスト水をそのまま送り出すことが考えられる。この場合、入口管路は、円筒本体の側面の下方にこの側面の接線方向に接続し、出口管路は、前記側面の上方にこの側面の接線方向かつ前記入口管路と逆方向に接続する。ここで、出口管路を「入口管路と逆方向に接続する」とは、入口管路から送り込まれたバラスト水がそのまま送り出される方向に、出口管路を接続することを意味する。入口管路と出口管路は上下方向に離隔しているから、平面視で周方向同位置の側面に入口管路及び出口管路が接続していれば両者は同一直線上に並び、平面視で周方向180度の離れた位置の側面に入口管路及び出口管路が接続していれば両者は同方向かつ平行に延びる。   Moreover, in the filtration apparatus of this invention, it is possible to send out the swirling ballast water as it is. In this case, the inlet pipe is connected to the tangential direction of the side face below the side face of the cylindrical body, and the outlet pipe is connected to the tangential direction of the side face and opposite to the inlet pipe line above the side face. . Here, “connecting the outlet pipe in the opposite direction to the inlet pipe” means connecting the outlet pipe in a direction in which the ballast water fed from the inlet pipe is sent out as it is. Since the inlet pipe and the outlet pipe are separated from each other in the vertical direction, if the inlet pipe and the outlet pipe are connected to the side surface at the same position in the circumferential direction in plan view, they are aligned on the same straight line. If the inlet pipe and the outlet pipe are connected to the side face at a position 180 degrees apart in the circumferential direction, both extend in the same direction and in parallel.

高比重異物は、遠心力によってスリットから円筒本体の外部へ離脱するが、側面に沿って旋回していることから、旋回速度によってスリットを通過してしまう割合が増加してしまう虞もある。そこで、スリットは、バラスト水の旋回方向下流側にある縦縁部に沿って半径方向内向きに突出する誘導板を設けておくとよい。この誘導板は、半径方向に突出する範囲で、側面に沿ってバラスト水と共に旋回する高比重異物を衝突させて、前記高比重異物がスリットを通過しないようにする。また、誘導板は、前記衝突した高比重異物をスリットから円筒本体の外部へ導く働きを有する。こうした誘導板は、円筒本体の側面を切り起こすことで、スリットの形成と同時に設けることができる。   Although the high specific gravity foreign substance separates from the slit to the outside of the cylindrical main body due to centrifugal force, since it swirls along the side surface, there is a possibility that the ratio of passing through the slit increases due to the swirling speed. Therefore, the slit may be provided with a guide plate that protrudes inward in the radial direction along the vertical edge portion on the downstream side in the swirling direction of the ballast water. This guide plate collides with high specific gravity foreign matter swirling with the ballast water along the side surface in a range protruding in the radial direction so that the high specific gravity foreign matter does not pass through the slit. The guide plate has a function of guiding the collided high specific gravity foreign substance from the slit to the outside of the cylindrical main body. Such a guide plate can be provided simultaneously with the formation of the slits by cutting and raising the side surface of the cylindrical body.

上記半径方向内向きに突出する誘導板は、少なからず旋回するバラスト水の抵抗となる。そこで、スリットは、バラスト水の旋回方向上流側にある縦縁部に沿って半径方向外向きに突出する誘導板を設けてもよい。この半径外向きの誘導板は、側面に沿ってバラスト水と共に旋回する高比重異物を衝突させるのではなく、遠心力を利用して円筒本体の側面より外側へ高比重異物を導くことにより、前記高比重異物がスリットを通過しないようにする。   The guide plate projecting inward in the radial direction serves as a resistance to the ballast water that turns. Therefore, the slit may be provided with a guide plate protruding outward in the radial direction along the vertical edge portion on the upstream side in the swirling direction of the ballast water. This radially outward guide plate does not collide with high specific gravity foreign matter swirling with the ballast water along the side surface, but guides the high specific gravity foreign material from the side surface of the cylindrical body by utilizing centrifugal force. Prevent foreign matter with high specific gravity from passing through the slit.

ここで、バラスト水の旋回速度が低い場合(例えばバラスト水を送り込み始めた段階等)、高比重異物に十分な遠心力が働かず、スリットから分離及び除去できなくなる虞がある。もっとも、この場合は従来同様に、高比重異物は失速して沈降することから、円筒本体は、バラスト水が旋回する円筒本体の内部空間と底面とを隔てる通水性の下部フィルタ区画を設けておき、失速して沈降する高比重異物を底面に堆積させて、バラスト水から分離するとよい。底面に堆積した高比重異物は、適宜回収する。本発明は、沈降した高比重異物が堆積する底面を、バラスト水が旋回する円筒本体の内部空間と下部フィルタ区画により隔てることで、バラスト水の旋回により高比重異物が巻き上げられ、再びバラスト水に混ざり込む機会をなくしている。   Here, when the turning speed of the ballast water is low (for example, when the ballast water starts to be fed), there is a possibility that sufficient centrifugal force does not act on the high specific gravity foreign substance and cannot be separated and removed from the slit. However, in this case, as in the conventional case, foreign bodies with high specific gravity stall and settle, so that the cylindrical main body is provided with a water-permeable lower filter section that separates the inner space and the bottom surface of the cylindrical main body through which the ballast water turns. It is preferable to deposit a high specific gravity foreign substance that settles upon stalling and separates it from the ballast water. The high specific gravity foreign matter deposited on the bottom is collected as appropriate. The present invention separates the bottom surface on which the sedimented high specific gravity foreign matter is accumulated by the inner space of the cylindrical body in which the ballast water swirls and the lower filter compartment, so that the high specific gravity foreign matter is wound up by the swirling of the ballast water, and again into the ballast water. Eliminate opportunities to mix.

下部フィルタ区画は、沈降する高比重異物を通過させながら、旋回するバラスト水による前記高比重異物の巻き上げを防止できる範囲で通水性を有すればよい。具体的な下部フィルタ区画としては、パンチングメタル又はエキスパンドメタルからなるスクリーンフィルタを例示できる。この場合、円筒本体の側面に接続した入口管路直下に前記スクリーンフィルタを設けると、この入口管路から送り込まれるバラスト水が底面側に流れ込まなくなり、流れ方向が上向きの旋回方向に特定付けられる利点がある。   The lower filter section only needs to have water permeability within a range in which it is possible to prevent the high specific gravity foreign matter from being rolled up by the swirling ballast water while allowing the high specific gravity foreign matter to settle to pass therethrough. As a specific lower filter section, a screen filter made of punching metal or expanded metal can be exemplified. In this case, if the screen filter is provided immediately below the inlet pipe connected to the side surface of the cylindrical main body, the ballast water fed from the inlet pipe does not flow to the bottom surface side, and the flow direction is specified as the upward turning direction. There is.

また、バラスト水から完全に高比重異物が分離及び除去できなかったり、仮にバラスト水に巻き上げられた高比重異物がある場合、この高比重異物が出口管路へ送り込まれることを防止するため、円筒本体は、バラスト水が旋回する円筒本体の内部空間とこの円筒本体に接続した出口管路とを隔てる通水性の上部フィルタ区画を設けるとよい。この上部フィルタ区画は、バラスト水を出口管路から送り出す際の抵抗となり、特許文献2同様、バラスト水から高比重異物の分離効果を高める働きも有する。この上部フィルタ区画としては、金属メッシュからなる筒状フィルタを例示できる。   In addition, in order to prevent the high specific gravity foreign matter from being completely separated and removed from the ballast water, or if there is a high specific gravity foreign matter wound up in the ballast water, a cylinder is used to prevent the high specific gravity foreign matter from being fed into the outlet pipe. The main body may be provided with a water-permeable upper filter section that separates the internal space of the cylindrical main body through which the ballast water turns and the outlet pipe connected to the cylindrical main body. The upper filter section serves as a resistance when the ballast water is sent out from the outlet pipe, and has a function of enhancing the effect of separating high specific gravity foreign substances from the ballast water, as in Patent Document 2. As this upper filter section, a cylindrical filter made of a metal mesh can be exemplified.

本発明により、バラスト水から汚泥をはじめとする高比重異物を分離後、確実に除去できる遠心分離型の濾過装置が提供できるようになる。これは、バラスト水から分離した高比重異物を沈降によって除去するのではなく、バラスト水と共に旋回する高比重異物を側面のスリットから円筒本体の外部へ離脱させ、前記高比重異物を分離と同時に除去することによる効果である。前記スリットから高比重異物を分離及び除去する効果は、スリットに対して設ける誘導板により、更に高められる。また、スリットから分離、除去する異物は汚泥等の高比重異物に限らず、シストや甲殻類に及ぶことから、本発明はバラスト水の汚染防止に寄与する効果もある。   According to the present invention, it is possible to provide a centrifugal type filtration device that can reliably remove foreign substances such as sludge from ballast water after separation. This does not remove the high specific gravity foreign matter separated from the ballast water by sedimentation, but removes the high specific gravity foreign matter swirling with the ballast water from the side slit to the outside of the cylindrical body and removes the high specific foreign matter at the same time as the separation. It is an effect by doing. The effect of separating and removing the high specific gravity foreign substance from the slit is further enhanced by the guide plate provided for the slit. In addition, the foreign matter to be separated and removed from the slit is not limited to the high specific gravity foreign matter such as sludge, but extends to cysts and crustaceans. Therefore, the present invention also has an effect of contributing to prevention of ballast water contamination.

下部フィルタ区画は、円筒本体の底面に堆積する高比重異物を、バラスト水が旋回する円筒本体の内部空間から隔離して、分離した高比重異物が再びバラスト水に混ざることが防止する。また、上部フィルタ区画は、出口管路から送り出されるバラスト水から、スリットからの分離及び除去、そして沈降により分離及び除去できなかった高比重異物を分離及び除去する働きを有する。こうしたスリットからの分離及び除去、下部フィルタ区画を挟んでの沈降による分離及び除去、そして上部フィルタ区画による分離及び除去を合わせることにより、本発明の濾過装置は高い分離効果を実現している。   The lower filter section isolates the high specific gravity foreign matter accumulated on the bottom surface of the cylindrical body from the internal space of the cylindrical main body where the ballast water swirls, and prevents the separated high specific gravity foreign matter from being mixed with the ballast water again. Further, the upper filter section has a function of separating and removing from the ballast water fed out from the outlet pipe, and separating and removing the high specific gravity foreign matter that could not be separated and removed by sedimentation. By combining such separation and removal from the slit, separation and removal by sedimentation across the lower filter section, and separation and removal by the upper filter section, the filtration device of the present invention achieves a high separation effect.

以下、本発明の実施形態について図を参照しながら説明する。図1は本発明の濾過装置1を組み込んだバラスト水の取水システムの全体構成を示すブロック図、図2は本発明の濾過装置1の一例を示す断面図、図3は図2中A−A断面図、図4は本例の濾過装置1におけるスリット16付近を表した図3中B矢視部拡大図、図5は別例のスリット17付近を表した図4相当拡大図、図6は別例の濾過装置6を示す断面図であり、そして図7は図6中C−C断面図である。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a block diagram showing the overall configuration of a ballast water intake system incorporating the filtration device 1 of the present invention, FIG. 2 is a sectional view showing an example of the filtration device 1 of the present invention, and FIG. 4 is an enlarged view of the portion indicated by the arrow B in FIG. 3 showing the vicinity of the slit 16 in the filtration device 1 of this example, FIG. 5 is an enlarged view corresponding to FIG. 4 showing the vicinity of the slit 17 of another example, and FIG. FIG. 7 is a sectional view showing another example of the filtering device 6, and FIG. 7 is a sectional view taken along the line CC in FIG. 6.

本発明の濾過装置1は単独で使用されるのではなく、例えば図1に見られるように、取水ポスト用の吸入濾過装置3や、微細な異物、すなわち10mm径以下のプランクトン等を除去するバラスト水浄化装置(二次濾過装置)5を併用して、異物のないバラスト水をバラストタンク(図示略)へと取り込む取水システムを構成する。本例の取水システムは、船底に開口した取水口(シーチェスト)2とバラスト水を吸引及び送出するバラストポンプ4との間に前記吸入濾過装置3を介在させ、前記バラストポンプ4とバラスト水浄化装置5との間に本例の濾過装置1を介在させている。これは、本例の濾過装置1がバラスト水浄化装置5に対する一次濾過装置であり、バラスト水浄化装置5が高比重異物を取り込むことにより破損することを防止する保護装置であることを意味する。   The filtration device 1 of the present invention is not used alone, but, for example, as shown in FIG. 1, a suction filtration device 3 for a water intake post and a ballast for removing fine foreign matters, that is, plankton having a diameter of 10 mm or less. A water purification system (secondary filtration device) 5 is used in combination to constitute a water intake system that takes in ballast water without foreign matter into a ballast tank (not shown). In the water intake system of this example, the suction filtration device 3 is interposed between a water intake (sea chest) 2 opened at the bottom of the ship and a ballast pump 4 for sucking and sending ballast water, and the ballast pump 4 and the ballast water purification are interposed. The filtration device 1 of this example is interposed between the device 5 and the device 5. This means that the filtration device 1 of the present example is a primary filtration device for the ballast water purification device 5, and is a protection device that prevents the ballast water purification device 5 from being damaged by taking in high-specific gravity foreign matter.

本例の濾過装置1は、図2及び図3に見られるように、円筒本体11は下方の側面111に接線方向から入口管路12を接続し、また円筒本体11の上方である平坦な上面112に垂直方向から出口管路13を接続している。バラスト水W(各図中白抜矢印で代表、以下同じ)は、入口管路12を側面111の接線方向に接続することにより、側面111に沿った旋回流を円滑に形成する。本例では、入口管路12の開口端121を側面111に寄せて絞り、一種のオリフィスを形成している。これにより、入口管路12から円筒本体11に送り込まれるバラスト水Wの勢いを増し、また側面111に沿った旋回流を下層から押し上げ、バラスト水Wを上昇させるようにしている。   As shown in FIGS. 2 and 3, in the filtering device 1 of this example, the cylindrical main body 11 connects the inlet pipe 12 from the tangential direction to the lower side surface 111, and is a flat upper surface above the cylindrical main body 11. An outlet pipe 13 is connected to 112 from the vertical direction. Ballast water W (represented by white arrows in each figure, the same applies hereinafter) connects the inlet pipe line 12 in the tangential direction of the side surface 111, thereby smoothly forming a swirling flow along the side surface 111. In this example, the opening end 121 of the inlet pipe 12 is brought close to the side surface 111 to form a kind of orifice. As a result, the momentum of the ballast water W fed from the inlet pipe 12 to the cylindrical main body 11 is increased, and the swirl flow along the side surface 111 is pushed up from the lower layer to raise the ballast water W.

円筒本体11は、入口管路12直下に下部フィルタ区画としてスクリーンフィルタ14を設け、円筒本体11の内部空間115と下方に窄んだ漏斗状の底面113とを隔てている。また、円筒本体11は、円筒本体11の上面112に上部フィルタ区画として筒状フィルタ15を設け、円筒本体11の内部空間115と出口管路13とを隔てている。出口管路13は、前記上部フィルタ区画内の上面112に接続している。高比重異物を円筒本体11外部へと離脱させ、除去するスリット16は、高さ方向において、およそ入口管路12と筒状フィルタ15との中間付近の側面111に開口している。   The cylindrical main body 11 is provided with a screen filter 14 as a lower filter section immediately below the inlet pipe line 12, and separates an internal space 115 of the cylindrical main body 11 from a funnel-shaped bottom surface 113 narrowed downward. The cylindrical main body 11 is provided with a cylindrical filter 15 as an upper filter section on the upper surface 112 of the cylindrical main body 11, and the internal space 115 of the cylindrical main body 11 and the outlet pipe line 13 are separated from each other. An outlet line 13 connects to the upper surface 112 in the upper filter compartment. The slit 16 for separating and removing the high specific gravity foreign substance to the outside of the cylindrical main body 11 opens in the side surface 111 in the vicinity of the middle between the inlet pipe 12 and the cylindrical filter 15 in the height direction.

下部フィルタ区画であるスクリーンフィルタ14は、円筒本体11の断面形状に等しい円形状のパンチングメタルからなる。このスクリーンフィルタ14を構成するパンチングメタルは、孔径10mm〜12mmを目安とする。本例のスクリーンフィルタ14は、入口管路12直下に配されており、入口管路12から送り込まれたバラスト水Wが下降しないように規制するほか、バラスト水Wが旋回することの影響を受けにくいため、特に円筒本体11に固着しておらず、四方に設けた支持突起141に周縁部を載せているだけである。このため、本例のスクリーンフィルタ14は、必要に応じて着脱自在であり、孔径の異なるパンチングメタルやエキスパンドメタルに交換したり、メンテナンスのため、一時的に取り外すことができる。   The screen filter 14 that is a lower filter section is made of a circular punching metal that is equal to the cross-sectional shape of the cylindrical main body 11. The punching metal constituting the screen filter 14 has a hole diameter of 10 mm to 12 mm as a guide. The screen filter 14 of this example is arranged directly under the inlet pipe 12 and restricts the ballast water W sent from the inlet pipe 12 from falling, and is affected by the swirling of the ballast water W. Since it is difficult, it is not particularly fixed to the cylindrical body 11, and only the peripheral edge is placed on the support protrusions 141 provided in the four directions. For this reason, the screen filter 14 of this example is detachable as necessary, and can be replaced with a punching metal or an expanded metal having a different hole diameter, or temporarily removed for maintenance.

スクリーンフィルタ14は、既述したように、入口管路12から送り込まれたバラスト水Wが下降しないように規制し、上向きの旋回流を形成することを助ける働きと共に、円筒本体11の内部空間115と底面113とを区画することにより、前記底面113に沈降した高比重異物が巻き上げられることを防ぐ働きを有する。スクリーンフィルタ14を通過して底面113に沈降した高比重異物は、下方に窄んだ漏斗状の底面113の中央最下部から順に堆積する。前記底面113の中央最下部には開閉バルブ(図示略)を接続した底面排出口114が設けてある。この底面排出口114は、前記開閉バルブにより通常閉鎖されており、一定量の高比重異物が堆積した段階で、適宜開閉バルブを開いて高比重異物を回収する。   As described above, the screen filter 14 regulates the ballast water W sent from the inlet pipe 12 so as not to descend, and helps to form an upward swirling flow, and also the inner space 115 of the cylindrical body 11. And the bottom surface 113 have a function of preventing the high specific gravity foreign matter that has settled on the bottom surface 113 from being rolled up. High specific gravity foreign substances that have passed through the screen filter 14 and settled on the bottom surface 113 are sequentially deposited from the lowermost center of the funnel-shaped bottom surface 113 constricted downward. A bottom surface discharge port 114 connected to an open / close valve (not shown) is provided at the lowermost center of the bottom surface 113. The bottom discharge port 114 is normally closed by the opening / closing valve, and when a certain amount of high specific gravity foreign material has accumulated, the open / close valve is appropriately opened to collect the high specific gravity foreign material.

上部フィルタ区画である筒状フィルタ15は、金属メッシュにより構成したメッシュ筒体151で、前記メッシュ筒体151を保形するため、パンチングメタルからなる筒状フレーム152を前記メッシュ筒体151の内側に添わせている。メッシュ筒体151は、後述するスリット16から離脱、除去できなかった高比重異物が出口管路13から出て行かないようにする役割を有するが、取水システム後段のバラスト水浄化装置5に対するプレフィルタの役割も担っている。これから、メッシュ筒体151は、例えば100μm程度までの小さな異物まで遮断できるように目が細かい金属メッシュを用いることが望ましい。   A cylindrical filter 15 that is an upper filter section is a mesh cylinder 151 made of a metal mesh. In order to retain the shape of the mesh cylinder 151, a cylindrical frame 152 made of punching metal is placed inside the mesh cylinder 151. I'll accompany you. The mesh cylinder 151 has a role to prevent the high specific gravity foreign matter that could not be removed and removed from the slit 16 to be described later from exiting the outlet conduit 13, but a prefilter for the ballast water purification device 5 at the latter stage of the water intake system. Also plays a role. From this, it is desirable that the mesh cylinder 151 is made of a fine metal mesh so that even a small foreign object up to, for example, about 100 μm can be blocked.

また、筒状フィルタ15は、上記下部フィルタ区画であるスクリーンフィルタ14と異なり、旋回するバラスト水Wの影響を受けるため、円筒本体11に設けた十字支持桟153にそれぞれ拘束突起154を取り付け、前記拘束突起154内に下面を嵌め込んで、位置固定している。この筒状フィルタ15における筒状フレーム152は、あくまでフィルタ作用を有するメッシュ筒体151を保形することが目的であるから、パンチングメタルの孔径は大きくても構わないし、パンチングメタルに代えて各種鋼材を用いた骨組フレームで構成してもよい。この筒状フィルタ15の通過を遮られた高比重異物は沈降し、上述のスクリーンフィルタ14を通過して底面113に堆積し、回収される。   Further, unlike the screen filter 14 which is the lower filter section, the cylindrical filter 15 is affected by the swirling ballast water W, and therefore, a restraining protrusion 154 is attached to each of the cross support bars 153 provided on the cylindrical body 11, The lower surface is fitted into the restraining protrusion 154 to fix the position. The cylindrical frame 152 in the cylindrical filter 15 is intended only to retain the mesh cylinder 151 having the filter action, so the hole diameter of the punching metal may be large, and various steel materials may be used instead of the punching metal. You may comprise with the framework frame using. The high specific gravity foreign matter blocked from passing through the cylindrical filter 15 settles, passes through the screen filter 14 described above, accumulates on the bottom surface 113, and is collected.

スリット16は、図4に見られるように、バラスト水Wと共に旋回する汚泥等の高比重異物を半径方向外側に離脱させ、円筒本体11に付設した異物溜まり162に落とし込んで除去し、前記異物溜まり162から適宜回収する。異物溜まり162は、回収するまでに十分な量の高比重異物を堆積できるように、スリット16より下方に空間を有している。本例のスリット16は、バラスト水Wの旋回方向に略直交する鉛直方向に延在する略長方形の開口で、高比重異物を衝突させてスリット16から円筒本体11の外部へ誘導する誘導板161を、バラスト水Wの旋回方向下流側にある縦縁部に沿って半径方向内向きに突出させている。本例の誘導板161は、円筒本体11の側面111を切り起こして構成し、同時にスリット16を開口している。   As shown in FIG. 4, the slit 16 separates high-specific gravity foreign substances such as sludge swirling with the ballast water W radially outward, drops them into the foreign substance reservoir 162 attached to the cylindrical body 11, and removes them. Collect from 162 as appropriate. The foreign matter reservoir 162 has a space below the slit 16 so that a sufficient amount of high specific gravity foreign matter can be deposited until it is collected. The slit 16 in this example is a substantially rectangular opening extending in a vertical direction substantially orthogonal to the swirling direction of the ballast water W, and a guide plate 161 that guides the high specific gravity foreign material to the outside of the cylindrical body 11 by colliding with the high specific gravity foreign matter. Are protruded inward in the radial direction along the vertical edge portion on the downstream side in the turning direction of the ballast water W. The guide plate 161 of this example is configured by cutting and raising the side surface 111 of the cylindrical main body 11 and simultaneously opening the slit 16.

スリット16及び誘導板161の大きさは、円筒本体11の大きさやバラスト水Wの旋回流の速度等を勘案して決定する。例えば、誘導板161を切り起こしてスリット16を形成する本例の構成の場合、目安として、幅D=30mm〜50mmのスリット16に対して突出量T=10mm〜20mmの誘導板161を設ける。これにより、誘導板161がバラスト水Wの旋回を大きく妨げることなく、側面111に沿って移動する高比重異物のみが誘導板161に衝突し、スリット16から異物溜まり162に向けて離脱させ、除去できる。異物溜まり162の底には開閉バルブ(図示略)を接続した溜まり排出口163が設けてある。この溜まり排出口163は、前記開閉バルブにより通常閉鎖されており、一定量の高比重異物が堆積した段階で、適宜開閉バルブを開いて高比重異物を回収する。   The sizes of the slit 16 and the guide plate 161 are determined in consideration of the size of the cylindrical body 11 and the speed of the swirling flow of the ballast water W. For example, in the case of the configuration of this example in which the guide plate 161 is cut and raised to form the slit 16, as a guide, the guide plate 161 having a protrusion amount T = 10 mm to 20 mm is provided for the slit 16 having a width D = 30 mm to 50 mm. As a result, only the high-specific gravity foreign matter moving along the side surface 111 collides with the guide plate 161 without causing the guide plate 161 to greatly disturb the turning of the ballast water W, and is removed from the slit 16 toward the foreign matter reservoir 162 and removed. it can. At the bottom of the foreign matter reservoir 162, a reservoir outlet 163 connected to an open / close valve (not shown) is provided. This reservoir discharge port 163 is normally closed by the opening / closing valve, and when a certain amount of high specific gravity foreign matter has accumulated, the open / close valve is appropriately opened to collect the high specific gravity foreign matter.

円筒本体11の大きさや、入口管路12から送り込むバラスト水Wの流速等との兼ね合いから、旋回流に対する抵抗が問題となる場合、例えば図5に見られるように、スリット17に設ける誘導板171は、バラスト水Wの旋回方向上流側にある縦縁部に沿って半径方向外向きに突出させることもできる。この誘導板171は、高比重異物を異物溜まり162に導いて離脱させる働きを有する。これから、ほとんど減速することなく異物溜まり162に進入した高比重異物は、異物溜まり162内の壁面に衝突して初めて減速し、異物溜まり162内に沈降する。複数のスリットを設ける場合、各スリットに設ける誘導板は同種でもよいし、異種(図4及び図5参照)の組み合せでもよい。   If resistance to the swirling flow is a problem due to the size of the cylindrical body 11 and the flow velocity of the ballast water W fed from the inlet pipe 12, for example, as shown in FIG. Can be protruded radially outward along the vertical edge on the upstream side of the ballast water W in the turning direction. The guide plate 171 has a function of guiding the high specific gravity foreign material to the foreign material reservoir 162 and releasing it. From this point on, the high specific gravity foreign substance that has entered the foreign substance reservoir 162 without almost decelerating is decelerated only after colliding with the wall surface in the foreign substance reservoir 162, and settles in the foreign substance reservoir 162. When providing a plurality of slits, the guide plates provided in each slit may be of the same type or a combination of different types (see FIGS. 4 and 5).

本例の濾過装置1は、次のように働いて、バラスト水W中から汚泥等の高比重異物を除去、回収する。まず、バラストポンプ4(図1参照)により取水されたバラスト水Wは、同じくバラストポンプ4により入口管路12から円筒本体11に送り込まれる。ここで、既述したように、入口管路12の開口端121は側面111に寄せて絞った形状であるため、円筒本体11に送り込まれるバラスト水Wは流速が増すほか、図2及び図3に見られるように、側面111に沿った旋回流を円滑に形成する。ここで、バラストポンプ4が2kg/cm2〜3kg/cm2の能力を有していれば、円筒本体11に送り込まれるバラスト水Wはおよそ2m/sec〜3m/secの流速で旋回させることができる。バラスト水Wに含まれる高比重異物は、バラスト水Wの旋回に合わせて旋回し始める。 The filtering device 1 of this example works as follows, and removes and collects high specific gravity foreign substances such as sludge from the ballast water W. First, the ballast water W taken by the ballast pump 4 (see FIG. 1) is similarly sent from the inlet pipe 12 to the cylindrical body 11 by the ballast pump 4. Here, as described above, since the opening end 121 of the inlet pipe 12 has a shape narrowed toward the side surface 111, the ballast water W fed into the cylindrical main body 11 has an increased flow velocity, as well as FIGS. As can be seen, a swirl flow along the side surface 111 is smoothly formed. Here, if the ballast pump 4 is capable of 2kg / cm 2 ~3kg / cm 2 , ballast water W fed to the cylindrical body 11 be pivoted at a flow rate of approximately 2m / sec~3m / sec it can. The high specific gravity foreign matter contained in the ballast water W starts to turn in accordance with the turning of the ballast water W.

バラスト水Wと共に旋回する高比重異物は、遠心力が加わることにより、側面111に集中する。ここで、前記高比重異物がスリット16に達すると、それまで遠心力に抗していた側面111がなくなる。また、前記高比重異物が誘導板161に衝突すると、旋回方向の力が低減又は滅失するため、結果として高比重異物には遠心力のみが働くことになり、図4に見られるように、スリット16を通じて異物溜まり162に高比重異物Xが落とし込まれる。スリット16の長さL(図2参照)がバラスト水Wの旋回流の上昇ピッチより大きければ、スリット16を通じた前記高比重異物の離脱は複数回繰り返されるため、遠心力によって側面111に集中して旋回する高比重異物は、およそすべてをスリット16から異物溜まり162へと離脱させ、除去できる。本発明の濾過装置1は、バラスト水Wの旋回流自身がより下層の旋回流により押し上げられて上昇していくため、上昇ピッチは小さく抑えられており、スリット16の長さLがよほど小さくない限り、スリット16を通じた高比重異物の離脱は複数回生ずる。   The high specific gravity foreign matter swirling with the ballast water W is concentrated on the side surface 111 due to the centrifugal force. Here, when the high specific gravity foreign substance reaches the slit 16, the side surface 111 that has resisted centrifugal force until then disappears. Further, when the high-specific gravity foreign object collides with the guide plate 161, the force in the turning direction is reduced or lost. As a result, only the centrifugal force acts on the high-specific gravity foreign substance, and as shown in FIG. 16, the high specific gravity foreign matter X is dropped into the foreign matter reservoir 162. If the length L of the slit 16 (see FIG. 2) is larger than the ascending pitch of the swirl flow of the ballast water W, the detachment of the high-specific gravity foreign substance through the slit 16 is repeated a plurality of times. The high-specific gravity foreign matter that swivels can be removed by removing almost all from the slit 16 to the foreign matter reservoir 162. In the filtration device 1 of the present invention, since the swirl flow of the ballast water W is pushed up by the swirl flow of the lower layer and rises, the ascending pitch is kept small, and the length L of the slit 16 is not very small. As long as the high specific gravity foreign matter is released through the slit 16, the separation occurs multiple times.

スリット16から離脱しなかった高比重異物(その他異物を含む)は、スリット16より上に達するが、筒状フィルタ15に遮られて出口管路13からバラスト水浄化装置5に至ることはない。筒状フィルタ15に衝突した高比重異物は、前記衝突により失速し、沈降していく。ここで、図3に見られるように、筒状フィルタ15は円筒本体11の中心に設けられているので、失速して沈降していく高比重異物は、バラスト水Wの旋回流の影響をあまり受けずにスクリーンフィルタ14に達し、このスクリーンフィルタ14を通過して底面113に堆積する。沈降する高比重異物が、仮にバラスト水Wの旋回流に巻き込まれても、新たにスリット16から離脱して除去されるか、再び筒状フィルタ15に遮られ、沈降する。   High specific gravity foreign matter (including other foreign matter) that has not separated from the slit 16 reaches above the slit 16 but is blocked by the cylindrical filter 15 and does not reach the ballast water purification device 5 from the outlet line 13. The high specific gravity foreign matter colliding with the cylindrical filter 15 is stalled by the collision and settles down. Here, as shown in FIG. 3, since the cylindrical filter 15 is provided at the center of the cylindrical body 11, the high specific gravity foreign matter that has stalled and settled is less affected by the swirling flow of the ballast water W. It reaches the screen filter 14 without being received, passes through the screen filter 14 and deposits on the bottom surface 113. Even if the high specific gravity foreign matter that settles is caught in the swirling flow of the ballast water W, it is newly detached from the slit 16 and removed, or is again blocked by the cylindrical filter 15 and settles.

異物溜まり162又は円筒本体11の底面113に堆積した高比重異物は、定期的に底面排出口114又は溜まり排出口163に接続した開閉バルブを開くことにより、排出される。上述したように、バラストポンプ4より圧力をかけてバラスト水Wが送り込まれるため、円筒本体11内部は加圧状態にある。これから、底面排出口114又は溜まり排出口163が常時開口していると前記圧力が抜けてしまい、加圧状態を利用したバラスト水Wの移送を困難にしてしまう。そこで、底面排出口114又は溜まり排出口163は高比重異物を回収する際のみ、それぞれ開放し、堆積した高比重異物を排出すればよい。   The high specific gravity foreign matter accumulated on the foreign matter reservoir 162 or the bottom surface 113 of the cylindrical main body 11 is periodically discharged by opening an on-off valve connected to the bottom outlet 114 or the reservoir outlet 163. As described above, since the ballast water W is fed by applying pressure from the ballast pump 4, the inside of the cylindrical main body 11 is in a pressurized state. Accordingly, if the bottom discharge port 114 or the pool discharge port 163 is always open, the pressure is released, making it difficult to transfer the ballast water W using the pressurized state. Therefore, the bottom discharge port 114 or the pool discharge port 163 may be opened only when the high specific gravity foreign material is collected, and the accumulated high specific gravity foreign material may be discharged.

本発明の濾過装置は、従来の遠心分離型の濾過装置と異なり、高比重異物が沈降するバラスト水の旋回流の中心から前記バラスト水を取り出すのではなく、あくまで旋回過程における高比重異物を直接スリットから離脱させ、除去するものであるから、例えば図6に見られるように、出口管路63をバラスト水Wの旋回方向に接続することもできる。この別例の濾過装置6は、円筒本体61、入口管路62、スリット66及び誘導板661、そしてスクリーンフィルタ64は、上述の例(図1〜図4)と同じであるが、出口管路63も側面611の接線方向から接続している点が異なる。   Unlike the conventional centrifugal separation type filtration device, the filtration device of the present invention does not take out the ballast water from the center of the swirling flow of the ballast water in which the high specific gravity foreign matter settles, but directly removes the high specific gravity foreign matter in the swirling process. Since it is removed from the slit and removed, the outlet pipe 63 can be connected in the swirling direction of the ballast water W as seen in FIG. The filtering device 6 of this other example is the same as the above-described example (FIGS. 1 to 4) except that the cylindrical body 61, the inlet pipe 62, the slit 66 and the guide plate 661, and the screen filter 64 are the outlet pipe. 63 also differs in that it is connected from the tangential direction of the side surface 611.

具体的には、図7に見られるように、上下に離隔した入口管路62と出口管路63とが、平面視で周方向180度の離れた位置関係で側面611にそれぞれ接続し、この入口管路62及び出口管路63が同方向かつ平行に延びている。また、この別例の濾過装置6においては、出口管路63に対する上部フィルタ区画として、出口管路63の開口端631に内蔵したスクリーンフィルタ67を用いている。これにより、円筒本体61の内部空間615を大きく取ることができ、バラスト水Wのより円滑な旋回流の形成が容易になる。   Specifically, as seen in FIG. 7, the inlet pipe 62 and the outlet pipe 63 that are vertically separated are connected to the side surface 611 in a positional relationship of 180 degrees in the circumferential direction in plan view. An inlet pipe 62 and an outlet pipe 63 extend in the same direction and in parallel. Further, in this other example of the filtering device 6, a screen filter 67 built in the open end 631 of the outlet pipe 63 is used as an upper filter section for the outlet pipe 63. Thereby, the internal space 615 of the cylindrical main body 61 can be made large, and the formation of a smoother swirling flow of the ballast water W is facilitated.

本発明の濾過装置を組み込んだバラスト水の取水システムの全体構成を示すブロック図である。It is a block diagram which shows the whole structure of the ballast water intake system incorporating the filtration apparatus of this invention. 本発明の濾過装置の一例を示す断面図である。It is sectional drawing which shows an example of the filtration apparatus of this invention. 図2中A−A断面図である。FIG. 3 is a cross-sectional view taken along the line AA in FIG. 本例の濾過装置におけるスリット付近を表した図3中B矢視部拡大図である。FIG. 4 is an enlarged view of a portion indicated by an arrow B in FIG. 3 showing the vicinity of a slit in the filtration device of this example. 別例のスリット付近を表した図4相当拡大図である。FIG. 5 is an enlarged view corresponding to FIG. 4 showing the vicinity of another slit. 別例の濾過装置を示す断面図である。It is sectional drawing which shows the filtration apparatus of another example. 図6中C−C断面図である。It is CC sectional drawing in FIG.

符号の説明Explanation of symbols

1 濾過装置
11 円筒本体
12 入口管路
13 出口管路
14 スクリーンフィルタ
15 筒状フィルタ
16 スリット
161 誘導板
17 別例のスリット
171 別例の誘導板
D スリットの幅
T 誘導板の突出量
L スリットの長さ
W バラスト水
X 高比重異物
1 Filtration device
11 Cylindrical body
12 Inlet pipeline
13 Exit pipeline
14 Screen filter
15 Tubular filter
16 slits
161 Guide plate
17 Another slit
171 Other guide plate D Width of slit T Projection amount of guide plate L Length of slit W Ballast water X High specific gravity foreign material

Claims (9)

取水したバラスト水から汚泥をはじめとする高比重汚泥を分離、除去する遠心分離型の濾過装置であって、円筒本体は下方に入口管路、上方に出口管路を接続し、入口管路から送り込んだバラスト水を側面に沿って旋回させながら上昇させ、出口管路から送り出すようにしてなり、前記側面にバラスト水の旋回方向に交差するスリットを設け、汚泥をはじめとする高比重異物を、バラスト水と共に旋回することによる遠心力を利用し、前記スリットから円筒本体の外部に離脱させて、除去することを特徴とするバラスト水の濾過装置。 Centrifugal filter that separates and removes sludge and other high specific gravity sludge from the collected ballast water. The cylindrical body is connected to the inlet pipe on the lower side and the outlet pipe on the upper side. The ballast water that has been fed is raised while swirling along the side surface, and is sent out from the outlet pipe.A slit that intersects the swirling direction of the ballast water is provided on the side surface, and high-specific gravity foreign substances such as sludge are provided. A ballast water filtration device using centrifugal force generated by swirling together with ballast water to remove the ballast water from the slit to the outside of the cylindrical body. 入口管路は、円筒本体の側面の下方に該側面の接線方向に接続し、出口管路は、円筒本体の上面に接続した請求項1記載のバラスト水の濾過装置。 2. The ballast water filtering device according to claim 1, wherein the inlet pipe is connected to a lower side of the side surface of the cylindrical body in a tangential direction of the side surface, and the outlet pipe is connected to the upper surface of the cylindrical body. 入口管路は、円筒本体の側面の下方に該側面の接線方向に接続し、出口管路は、前記側面の上方に該側面の接線方向かつ前記入口管路と逆方向に接続した請求項1記載のバラスト水の濾過装置。 The inlet pipe is connected to a tangential direction of the side surface below the side surface of the cylindrical body, and the outlet pipe is connected to the tangential direction of the side surface and in a direction opposite to the inlet pipe line above the side surface. The ballast water filtration device described. スリットは、バラスト水の旋回方向下流側にある縦縁部に沿って半径方向内向きに突出する誘導板を設けた請求項1〜3いずれか記載のバラスト水の濾過装置。 The ballast water filtering device according to any one of claims 1 to 3, wherein the slit is provided with a guide plate that protrudes inward in the radial direction along a longitudinal edge portion on the downstream side in the swirl direction of the ballast water. スリットは、バラスト水の旋回方向上流側にある縦縁部に沿って半径方向外向きに突出する誘導板を設けた請求項1〜3いずれか記載のバラスト水の濾過装置。 The ballast water filtering device according to any one of claims 1 to 3, wherein the slit is provided with a guide plate that protrudes radially outward along a vertical edge portion on the upstream side in the swirling direction of the ballast water. 円筒本体は、バラスト水が旋回する円筒本体の内部空間と底面とを隔てる通水性の下部フィルタ区画を設けた請求項1〜5いずれか記載のバラスト水の濾過装置。 The ballast water filtering device according to any one of claims 1 to 5, wherein the cylindrical main body is provided with a water-permeable lower filter section that separates an inner space and a bottom surface of the cylindrical main body through which the ballast water turns. 下部フィルタ区画は、パンチングメタル又はエキスパンドメタルからなるスクリーンフィルタである請求項6記載のバラスト水の濾過装置。 The apparatus for filtering ballast water according to claim 6, wherein the lower filter section is a screen filter made of punching metal or expanded metal. 円筒本体は、バラスト水が旋回する円筒本体の内部空間と該円筒本体に接続した出口管路とを隔てる通水性の上部フィルタ区画を設けた請求項1〜6いずれか記載のバラスト水の濾過装置。 The ballast water filtration device according to any one of claims 1 to 6, wherein the cylindrical main body is provided with a water-permeable upper filter section that separates an internal space of the cylindrical main body through which the ballast water swirls and an outlet pipe connected to the cylindrical main body. . 上部フィルタ区画は、金属メッシュからなる筒状フィルタである請求項8記載のバラスト水の濾過装置。 The apparatus for filtering ballast water according to claim 8, wherein the upper filter section is a cylindrical filter made of a metal mesh.
JP2005279659A 2005-09-27 2005-09-27 Ballast water filtration equipment Expired - Fee Related JP4759669B2 (en)

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KR101059864B1 (en) 2009-08-13 2011-08-29 삼성중공업 주식회사 Ship's ballast system
JP2013064349A (en) * 2011-09-16 2013-04-11 Tokiko Techno Kk Pump unit
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JP2016159242A (en) * 2015-03-03 2016-09-05 オルガノ株式会社 Centrifugal separator and high-purity steam generator with use of same
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