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JP2008212851A - Filter device cleaning method and liquid purification system provided with the filter device - Google Patents

Filter device cleaning method and liquid purification system provided with the filter device Download PDF

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JP2008212851A
JP2008212851A JP2007055063A JP2007055063A JP2008212851A JP 2008212851 A JP2008212851 A JP 2008212851A JP 2007055063 A JP2007055063 A JP 2007055063A JP 2007055063 A JP2007055063 A JP 2007055063A JP 2008212851 A JP2008212851 A JP 2008212851A
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liquid
cleaning
cleaning liquid
filter device
filter
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Yusuke Kawasaki
祐輔 川嵜
Koji Horizoe
浩司 堀添
Masamichi Asano
昌道 浅野
Eishin Abe
英信 阿部
Hiroyuki Yamamoto
浩之 山本
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Fuji Filter Manufacturing Co Ltd
Mitsubishi Heavy Industries Ltd
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Fuji Filter Manufacturing Co Ltd
Mitsubishi Heavy Industries Ltd
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Abstract

【課題】フィルター装置を備えた液体浄化装置の特に起動時及び停止時におけるフィルターエレメントの固形物の目詰まりの発生を回避して、フィルターエレメント洗浄液への固形物の混入に伴う液体浄化装置の正常運転の阻害を防止するとともに、洗浄液ポンプや弁類等の洗浄液用機器の故障の発生を防止し、さらには、液体浄化装置の停止期間中におけるバラストタンク内の微生物の増殖やタンクの腐食を防止可能なフィルター装置及びこのフィルター装置を備えた液体の浄化システムを提供する。
【解決手段】固形物が混入された未処理液をフィルターエレメントを通すことにより該固形物をろ過してろ過液通路に排出するフィルター装置の洗浄手段であって、前記フィルター装置の作動を開始する起動時及び作動を終了する停止時に、清浄液通路を通して固形物の含有量が一定値以下の清浄液を前記フィルター装置に導入して該清浄液により前記フィルターエレメントを洗浄することを特徴とする。
【選択図】図1
[PROBLEMS] To avoid the occurrence of clogging of solid matter of a filter element, particularly at the time of starting and stopping of a liquid purifying device provided with a filter device, and normality of the liquid purifying device accompanying mixing of the solid matter into a filter element cleaning liquid. Prevents obstruction of operation, prevents failure of cleaning liquid equipment such as cleaning liquid pumps and valves, and prevents growth of microorganisms in the ballast tank and corrosion of the tank while the liquid purification device is stopped A possible filter device and a liquid purification system provided with the filter device are provided.
The filter device is a cleaning means for filtering an untreated liquid mixed with solid matter through a filter element and discharging the solid matter to a filtrate passage, and starts the operation of the filter device. A cleaning liquid having a solid content of a certain value or less is introduced into the filter device through the cleaning liquid passage at the time of starting and when the operation is stopped, and the filter element is washed with the cleaning liquid.
[Selection] Figure 1

Description

本発明は、主として、未処理の海水中の微生物を除去し清浄な処理海水にしてバラストタンクに収容するバラスト水処理に適用されるフィルター装置及びこのフィルター装置を備えた液体の浄化システムに関する。   The present invention mainly relates to a filter device applied to ballast water treatment in which microorganisms in untreated seawater are removed to obtain clean treated seawater and accommodated in a ballast tank, and a liquid purification system including the filter device.

タンカー等の船舶において、オイルを搭載しない状態での航行時に、バラスト水タンクに収容する液体即ちバラスト水は、海洋汚染や公害の発生を回避するため、未処理の液体をフィルター装置や液体電解装置等の固形物除去手段を通すことにより該未処理液体中の微生物を含む固形物を除去する海水無害化処理装置によって、清浄な処理液体にしてバラスト水タンクに収容している。
そして、前記海水無害化処理装置に用いられているフィルター装置については、従来より多くの発明、考案が提供されており、その一つに特許文献1(特許第2714914号公報)の技術がある。
In ships such as tankers, the liquid stored in the ballast water tank, that is, ballast water when navigating with no oil mounted, is used to filter out untreated liquid to prevent marine pollution and pollution. By using a seawater detoxification treatment device that removes solid matter including microorganisms in the untreated liquid by passing the solid matter removing means such as the above, the treated liquid is stored in a ballast water tank.
And about the filter apparatus used for the said seawater detoxification processing apparatus, many inventions and inventions are provided conventionally, and there exists a technique of patent document 1 (patent 2714914 gazette) in one of them.

かかる技術においては、フィルターハウジング内に収納されて回転する筒状のフィルターエレメントの外側に形成される外側室に未処理液体を導入し、該液体を前記フィルターエレメントを通して固形物をろ過してから該フィルターエレメントの内側に形成される内側室に流出させるように構成し、フィルターエレメントの洗浄時には、前記フィルターエレメント洗浄用の洗浄液を、噴出ノズルからフィルターエレメントの外周面に吹き付け、そのドレン排水をフィルターハウジングの下部に開口されたドレン排出口から排出している。   In such a technique, an untreated liquid is introduced into an outer chamber formed outside a cylindrical filter element that is housed in a filter housing and rotates, and the solid is filtered through the filter element before the liquid is filtered. The filter element is configured to flow out into an inner chamber formed inside the filter element. When cleaning the filter element, the cleaning liquid for cleaning the filter element is sprayed from the ejection nozzle to the outer peripheral surface of the filter element, and the drainage is drained from the filter housing. It is discharged from the drain outlet that is open at the bottom of the.

特許第2714914号公報Japanese Patent No. 2714914

前記のように、海水の無害化処理装置には、液体中の固形物を機械的に除去する手段として用いられている特許文献1(特許第2714914号公報)のようなフィルター装置が用いられているが、特許文献1のフィルター装置には次のような解決すべき課題がある。   As described above, a filter device such as Patent Document 1 (Patent No. 2714914) used as a means for mechanically removing solids in a liquid is used for a detoxification device for seawater. However, the filter device of Patent Document 1 has the following problems to be solved.

一般に、液体をフィルターエレメントでろ過することによって液体中の固形物を捕獲する特許文献1(特許第2714914号公報)のようなフィルター装置は、固形物の含有がきわめて少ない燃料や潤滑油のろ過用として用いられることが多く、この場合は所要のろ過機能を発揮する。
しかしながら、フィルター装置を海水のろ過用として用いる場合、海水中にはプランクトンのような微生物、砂のような比重の大きい固形物等の多くの固形物が混入しているため、前記特許文献1のようなフィルター装置をそのまま海水のろ過用として用いると、特に無害化処理装置の起動時に海水中の固形物によってフィルターエレメントが目詰まりを起こし易く、かかるフィルターエレメントの目詰まりの発生によって、固形物を十分に除去してバラスト水タンクに収容し、またフィルターエレメントの洗浄液として用いるに十分なろ過水が得られ難い。
このため、かかるフィルターエレメントのろ過機能の低下によって、無害化処理装置の正常運転が不可能になるという事態が生じる恐れがある。
In general, a filter device such as Patent Document 1 (Patent No. 2714914) that captures solids in a liquid by filtering the liquid with a filter element is used for filtering fuel and lubricating oil that contain very little solids. In this case, the required filtration function is exhibited.
However, when the filter device is used for seawater filtration, the seawater contains many solids such as microorganisms such as plankton and solids such as sand having a large specific gravity. If such a filter device is used as it is for filtering seawater, the filter element is likely to be clogged by solid matter in the seawater, especially when the detoxification treatment device is started up. It is difficult to obtain enough filtered water to be sufficiently removed and accommodated in a ballast water tank and used as a cleaning liquid for the filter element.
For this reason, there exists a possibility that the situation where the normal operation of a detoxification processing apparatus becomes impossible by the fall of the filtration function of this filter element may arise.

また、フィルターエレメントで十分なろ過がなされない海水をフィルターエレメントの洗浄液として用いると、洗浄液ポンプの回転部分や洗浄液通路の開閉弁に固形物が噛みこんで、これらの機器の故障の要因となる。
さらには、バラスト水タンクに収容するためのバラスト水の取水設備は停止期間が長いため、停止前に前記のように十分なろ過がなされない海水をバラスト水タンクに収容すると、バラスト水タンク内において微生物に増殖が発生し、またバラスト水タンクの腐食要因ともなる。
Further, when seawater that is not sufficiently filtered by the filter element is used as the cleaning liquid for the filter element, solid matter is caught in the rotating part of the cleaning liquid pump and the opening / closing valve of the cleaning liquid passage, which causes failure of these devices.
Furthermore, since the ballast water intake equipment to be stored in the ballast water tank has a long stop period, if seawater that is not sufficiently filtered as described above is stored in the ballast water tank before the stop, Proliferation occurs in microorganisms and also causes corrosion of ballast water tanks.

従って、本発明はかかる従来技術の課題に鑑み、フィルター装置を備えた液体浄化装置の、特に起動時及び停止時におけるフィルターエレメントの固形物の目詰まりの発生を回避して、フィルターエレメント洗浄液への固形物の混入に伴う液体浄化装置の正常運転の阻害を防止するとともに、洗浄液ポンプや弁類等の洗浄液用機器の故障の発生を防止し、さらには、液体浄化装置の停止期間中におけるバラストタンク内の微生物の増殖やタンクの腐食を防止可能なフィルター装置及びこのフィルター装置を備えた液体の浄化システムを提供することを目的とする。   Therefore, in view of the problems of the prior art, the present invention avoids occurrence of clogging of the solid matter of the filter element, particularly at the time of starting and stopping of the liquid purifying apparatus provided with the filter device, so that the filter element cleaning liquid can be used. Prevents obstruction of normal operation of the liquid purifier due to mixing of solids, prevents failure of cleaning liquid equipment such as cleaning liquid pumps and valves, and ballast tanks during periods when the liquid purifier is stopped It is an object of the present invention to provide a filter device capable of preventing the growth of microorganisms therein and corrosion of a tank, and a liquid purification system provided with the filter device.

本発明はかかる目的を達成するもので、固形物が混入された未処理液を、フィルターエレメントを通すことにより該固形物をろ過してろ過液通路に排出するフィルター装置の洗浄方法であって、前記フィルター装置の作動を開始する起動時及び作動を終了する停止時に、固形物の含有量が一定値以下の清浄液を清浄液通路を通して前記フィルター装置に導入して該清浄液により前記フィルターエレメントを洗浄することを特徴とする。
かかる発明において、好ましくは、前記起動時及び停止時以外の運転時に、前記清浄液による前記フィルターエレメントの洗浄操作を行ってからあるいは該洗浄操作を行いながら、前記未処理液をフィルター装置に導入して前記フィルターエレメントによるろ過を行うように構成する。
また、前記清浄液として、前記清浄液として、淡水、前記未処理液に遠心力を付与してこの液体中から固形物を分離する遠心式固液分離装置で処理された液体、もしくは酸化作用を有する物質を含む洗浄液のいずれかを用いる。
The present invention achieves such an object, and is a cleaning method for a filter device in which an untreated liquid mixed with a solid substance is filtered through a filter element and discharged to a filtrate passage. At the time of starting to start the operation of the filter device and at the time of stopping to stop the operation, a cleaning liquid having a solid content of a certain value or less is introduced into the filter device through a cleaning liquid passage, and the filter element is moved by the cleaning liquid. It is characterized by washing.
In such an invention, preferably, the untreated liquid is introduced into the filter device after performing the cleaning operation of the filter element with the cleaning liquid or while performing the cleaning operation at the time of operation other than at the time of starting and stopping. The filter element is configured to perform filtration.
In addition, as the cleaning liquid, as the cleaning liquid, fresh water, a liquid processed by a centrifugal solid-liquid separation device that applies centrifugal force to the untreated liquid and separates solids from the liquid, or an oxidizing action One of the cleaning liquids containing the substance is used.

また、前記洗浄方法によるフィルター装置をそなえた液体浄化システムに関する発明は、固形物が混入された未処理液をフィルターエレメントを通すことにより該固形物をろ過してろ過液通路に排出するフィルター装置と、前記フィルター装置を洗浄する洗浄液を該フィルター装置に給排する洗浄装置とを有する液体無害化処理装置を備えた液体浄化システムにおいて、固形物の含有量が一定値以下の清浄液を前記フィルター装置に供給する清浄液通路からなる第1の洗浄液通路と、該第1の洗浄液通路を開閉する清浄液通路開閉弁と、前記フィルター装置への未処理液供給通路を開閉する未処理液通路開閉弁と、前記フィルター装置に接続される第2の洗浄液通路を開閉する洗浄液通路開閉弁と、前記フィルター装置からのろ過液通路を開閉するろ過液通路開閉弁と、前記フィルター装置からの洗浄排液通路を開閉する排液通路開閉弁とをそなえるとともに、前記液体無害化処理装置の起動時及び停止時に前記清浄液通路開閉弁を開くとともに前記洗浄液通路開閉弁を閉じて前記第1の洗浄液通路を通して前記清浄液をフィルター装置に供給せしめる洗浄液切換え手段をそなえたことを特徴とする。
かかる発明において、好ましくは、前記洗浄液切換え手段は、前記液体無害化処理装置の起動時及び停止時以外の運転時に、前記清浄液通路開閉弁を閉じるとともに前記洗浄液通路開閉弁を開いて前記第2の洗浄液通路からの洗浄液をフィルター装置に供給せしめるように構成される。
The invention relating to the liquid purification system provided with the filter device according to the cleaning method includes a filter device for filtering the solid matter by passing the untreated liquid mixed with the solid matter through the filter element and discharging it to the filtrate passage. In a liquid purification system comprising a liquid detoxification processing device having a cleaning device for supplying and discharging a cleaning liquid for cleaning the filter device to the filter device, a cleaning liquid having a solid content of a certain value or less is applied to the filter device. A first cleaning liquid passage comprising a cleaning liquid passage for supplying to the liquid, a cleaning liquid passage opening / closing valve for opening and closing the first cleaning liquid passage, and an untreated liquid passage opening / closing valve for opening and closing an untreated liquid supply passage to the filter device A cleaning fluid passage opening / closing valve for opening and closing a second cleaning fluid passage connected to the filter device, and opening a filtrate passage from the filter device. And a drain passage opening / closing valve for opening / closing a cleaning drain passage from the filter device, and opening the cleaning fluid passage opening / closing valve when starting and stopping the liquid detoxification treatment device. A cleaning liquid switching means for closing the cleaning liquid passage opening / closing valve and supplying the cleaning liquid to the filter device through the first cleaning liquid passage is provided.
In this invention, it is preferable that the cleaning liquid switching means closes the cleaning liquid passage opening / closing valve and opens the cleaning liquid passage opening / closing valve during operation other than when the liquid detoxification processing apparatus is started and stopped. The cleaning liquid from the cleaning liquid passage is supplied to the filter device.

また、かかる装置発明において、前記洗浄液切換え手段は、前記液体無害化処理装置の運転状態を設定あるいは検出する運転状態設定/検出手段からの入力信号に基づき、前記液体浄化装置の運転状態に応じて前記清浄液通路開閉弁、前記未処理液通路開閉弁、前記洗浄液通路開閉弁、前記ろ過液通路開閉弁、及び前記排液通路開閉弁を開閉制御するとともに、前記洗浄装置に設けられた洗浄ポンプを運転制御する制御装置からなるように構成するのが好ましい。   Further, in the apparatus invention, the cleaning liquid switching means is responsive to an operation state of the liquid purification apparatus based on an input signal from an operation state setting / detection means for setting or detecting an operation state of the liquid detoxification processing apparatus. The cleaning liquid passage opening / closing valve, the untreated liquid passage opening / closing valve, the cleaning liquid passage opening / closing valve, the filtrate passage opening / closing valve, and the drainage passage opening / closing valve are controlled to open / close, and the cleaning pump provided in the cleaning device It is preferable to comprise so that it may consist of a control apparatus which controls driving | operation.

また、前記フィルター装置をそなえた液体浄化システム用液体無害化処理装置の発明は、前記液体無害化処理装置は、未処理の液体中の微生物を除去して清浄な処理液体に転換し、この処理液体をバラストタンクに収容するように構成されるとともに、前記液体に遠心力を付与して該液体中から固形物を分離する遠心式固液分離装置と、前記フィルター装置と、前記液体が通流する液体処理ラインの前記遠心式固液分離装置及びフィルター装置の下流側に設けられ、前記液体の全部または一部を電解槽にて電気分解して塩素含有物質を生成する液体電解装置とを備えたことを特徴とする。   Further, the invention of the liquid detoxification processing apparatus for a liquid purification system provided with the filter apparatus, wherein the liquid detoxification processing apparatus removes microorganisms in the untreated liquid and converts it into a clean processing liquid. A centrifugal solid-liquid separation device configured to store a liquid in a ballast tank and apply a centrifugal force to the liquid to separate solids from the liquid, the filter device, and the liquid flow A liquid electrolysis apparatus that is provided on the downstream side of the centrifugal solid-liquid separation device and the filter device of the liquid processing line, and electrolyzes all or part of the liquid in an electrolytic cell to generate a chlorine-containing substance. It is characterized by that.

さらには、次の構成からなる液体浄化システムも、本発明に含まれる。
(1)フィルターハウジング内に収納され回転可能な筒状のフィルターエレメントの外側に形成される外側室に未処理液体を導入し、該液体を前記フィルターエレメントを通して固形物をろ過してから該フィルターエレメントの内側に形成される内側室に流出させるように構成されたフィルター装置と、洗浄ポンプから送給される前記フィルターエレメントの洗浄用の洗浄液を該フィルターエレメントの外周面に吹き付ける複数の噴出ノズルと、前記洗浄ポンプと前記複数の噴出ノズルとを接続する複数の洗浄液通路をそれぞれ開閉する複数の洗浄液通路開閉弁とをそなえた液体浄化システムにおいて、前記複数の洗浄液通路の前記洗浄液通路開閉弁の前流側に該洗浄液通路開閉弁と同数設けられて該洗浄液通路を開閉する開閉元弁と、前記複数の洗浄液通路の前記洗浄液通路開閉弁の後流側に該洗浄液通路開閉弁と同数設けられて該洗浄液通路を開閉する遮断弁と、前記洗浄液通路の圧力が所定の圧力範囲外となったとき故障発生の前記洗浄液通路開閉弁に対応する前記開閉元弁を閉じて当該洗浄液通路開閉弁への洗浄液の通流を遮断せしめる制御装置を備えたことを特徴とする。
Furthermore, a liquid purification system having the following configuration is also included in the present invention.
(1) An untreated liquid is introduced into an outer chamber formed outside a rotatable cylindrical filter element housed in a filter housing, and the solid is filtered through the filter element before the filter element. A filter device configured to flow out into an inner chamber formed inside, a plurality of ejection nozzles that spray cleaning liquid for cleaning the filter element fed from a cleaning pump onto the outer peripheral surface of the filter element; In the liquid purification system comprising a plurality of cleaning liquid passage opening / closing valves that respectively open and close a plurality of cleaning liquid passages connecting the cleaning pump and the plurality of ejection nozzles, the upstream flow of the cleaning liquid passage opening / closing valves of the plurality of cleaning liquid passages An open / close source valve that opens and closes the cleaning liquid passage by being provided in the same number as the cleaning liquid passage opening / closing valve, A plurality of cleaning liquid passages on the downstream side of the cleaning liquid passage opening / closing valves, the same number as the cleaning liquid passage opening / closing valves, and a shut-off valve for opening / closing the cleaning liquid passage, and when the pressure of the cleaning liquid passage is outside a predetermined pressure range A control device is provided that closes the opening / closing source valve corresponding to the cleaning liquid passage opening / closing valve in which a failure has occurred and blocks the flow of the cleaning liquid to the cleaning liquid passage opening / closing valve.

(2)フィルターハウジング内に収納され回転可能な筒状のフィルターエレメントの外側に形成される外側室に未処理液体を導入し、該液体を前記フィルターエレメントを通して固形物をろ過してから該フィルターエレメントの内側に形成される内側室に流出させるように構成されたフィルター装置と、洗浄ポンプから送給される前記フィルターエレメントの洗浄用の洗浄液を該フィルターエレメントの外周面に吹き付ける複数の噴出ノズルと、前記洗浄ポンプと前記複数の噴出ノズルとを接続する複数の洗浄液通路をそれぞれ開閉する複数の洗浄液通路開閉弁とをそなえた液体浄化システムにおいて、前記複数の洗浄液通路開閉弁のうち少なくとも2個の前記洗浄液通路開閉弁について同時に開弁するオーバーラップ期間を設定するとともに、前記洗浄液通路に該洗浄液通路内の圧力変動を吸収するアキュムレータを設置したことを特徴とする。   (2) An untreated liquid is introduced into an outer chamber formed outside a rotatable cylindrical filter element housed in the filter housing, and the solid is filtered through the filter element before the filter element. A filter device configured to flow out into an inner chamber formed inside, a plurality of ejection nozzles that spray cleaning liquid for cleaning the filter element fed from a cleaning pump onto the outer peripheral surface of the filter element; In a liquid purification system comprising a plurality of cleaning liquid passage opening / closing valves that respectively open and close a plurality of cleaning liquid passages connecting the cleaning pump and the plurality of ejection nozzles, at least two of the plurality of cleaning liquid passage opening / closing valves Set an overlap period for the cleaning fluid passage opening and closing valves at the same time. Characterized in that it has been installed accumulator to absorb pressure fluctuations in the cleaning liquid passage into the cleaning liquid passage.

本発明によれば、液体浄化システムの液体無害化処理装置の洗浄液切換え手段によって切換え操作される清浄液通路からなる第1の洗浄液通路の開閉弁とフィルター装置からのろ過液が供給される第2の洗浄液通路を開閉する開閉弁とを、前記洗浄液切換え手段によって切り換えることにより、前記液体無害化処理装置の起動時及び停止時に、前記清浄液通路を通して固形物の含有量が一定値以下の清浄液をフィルター装置に導入して該清浄液により前記フィルターエレメントを洗浄しておき、前記起動時及び停止時以外の定常運転時に、前記清浄液によるフィルターエレメントの洗浄操作を行ってからあるいは該洗浄操作を行いながら、未処理液をフィルター装置に導入してフィルターエレメントによるろ過を行うように構成したので、装置の起動時に、固形物をほとんど含まない清浄液をフィルターエレメントに噴出させて該フィルターエレメントを洗浄することにより、かかる清浄液でフィルターエレメント内の固形物を洗い落としながら、未処理液をフィルター装置に導入してフィルターエレメントによるろ過を行う定常運転に入ることができる。   According to the present invention, the on-off valve of the first cleaning liquid passage composed of the cleaning liquid passage switched by the cleaning liquid switching means of the liquid detoxification processing device of the liquid purification system and the second liquid supplied with the filtrate from the filter device are supplied. When the liquid detoxification treatment apparatus is started and stopped by switching the on-off valve that opens and closes the cleaning liquid passage, the cleaning liquid having a solid content of a certain value or less through the cleaning liquid passage Is introduced into a filter device and the filter element is washed with the cleaning liquid, and after the filter element is cleaned with the cleaning liquid during steady operation other than at the time of starting and stopping, the cleaning operation is performed. As it was configured, the untreated liquid was introduced into the filter device and filtered through the filter element. At the start-up of the filter element, a cleaning liquid containing almost no solid matter is jetted onto the filter element to wash the filter element, and the untreated liquid is introduced into the filter device while washing the solid matter in the filter element with the cleaning liquid. Thus, it is possible to enter a steady operation for performing filtration by the filter element.

要するに本発明においては、起動時にフィルター清浄液を供給して洗浄しながら未処理液も濾過することで、起動時におけるフィルターの目詰まりを防止でき、装置の起動から停止までフィルター装置のろ過液等の多少の固形物が混入されている液を洗浄液として用いている前記従来技術のように、特に起動後に洗浄液中の固形物によってフィルターエレメントが目詰まりを起こすのを回避できる。
従って本発明によれば、かかるフィルターエレメントの目詰まりによる該フィルターエレメントのろ過機能の低下に伴う、洗浄液ポンプの回転部分や洗浄液通路の開閉弁に固形物の噛み込み、及びかかる固形物の噛み込みによる前記機器の故障の発生を回避でき、これにより無害化処理装置の安定運転を実現できて、装置の信頼性を向上できる。
In short, in the present invention, by filtering the untreated liquid while supplying and cleaning the filter cleaning liquid at the start-up, clogging of the filter at the start-up can be prevented, and the filtrate of the filter apparatus from the start-up to the stop of the apparatus, etc. As in the prior art using a liquid in which some solid matter is mixed as a cleaning liquid, it is possible to avoid clogging of the filter element due to the solid substance in the cleaning liquid, especially after activation.
Therefore, according to the present invention, solid matter is caught in the rotating part of the washing liquid pump and the opening / closing valve of the washing liquid passage due to the reduction of the filtering function of the filter element due to clogging of the filter element, and the solid substance is caught Occurrence of the failure of the equipment due to the above can be avoided, and thereby stable operation of the detoxification processing apparatus can be realized, and the reliability of the apparatus can be improved.

また本発明によれば、装置の運転を停止する前の一定時間あるいは装置の停止時に、固形物をほとんど含まない清浄液をフィルター装置に導入して該清浄液により前記フィルターエレメントを洗浄しておくので、停止期間が長いバラスト水の取水設備においても、
停止期間中におけるバラストタンク内での微生物の増殖やバラストタンクの腐食の発生を防止できるとともに、次回の起動を円滑に行うことができる。
また、装置の停止期間中に、フィルターエレメントの表面等にバイオフィルム等の生物が繁殖するのを防止できる。
Further, according to the present invention, a cleaning liquid containing almost no solid matter is introduced into the filter device for a certain time before the operation of the apparatus is stopped or when the apparatus is stopped, and the filter element is washed with the cleaning liquid. So, even in the ballast water intake equipment with a long stoppage period,
While preventing the growth of microorganisms in the ballast tank and the occurrence of corrosion of the ballast tank during the stop period, the next start-up can be performed smoothly.
In addition, it is possible to prevent a living organism such as a biofilm from propagating on the surface of the filter element or the like while the apparatus is stopped.

また本発明によれば、固形物をほとんど含まない清浄液によりフィルター装置を洗浄しながら未処理液体をろ過することで、洗浄ポンプによる吸入に十分なろ過液量を得ることができて、円滑に定常運転に移行できるとともに、1台の洗浄ポンプで装置の起動、定常運転、及び停止時の洗浄を行うことができる。   Further, according to the present invention, by filtering the untreated liquid while washing the filter device with a cleaning liquid containing almost no solid matter, it is possible to obtain a filtrate amount sufficient for suction by the washing pump, and smoothly It is possible to shift to a steady operation, and it is possible to perform the start-up of the apparatus, the steady operation, and the washing at the time of stop with one washing pump.

また本発明によれば、固形物をほとんど含まない清浄液によりフィルター装置を洗浄することで、フィルター装置内及びその付属配管等を効果的に洗浄できるとともに、海水のように金属腐食性を有する液体を浄化処理する装置の場合には、停止期間中の装置の腐食の発生を防止できる。
また、前記清浄液供給用として、備え付けの淡水タンクや淡水化装置を利用することで、洗浄液用のタンクスペースや洗浄液の製造装置を新たに設置することなく、フィルター装置の清浄液による洗浄を実現できる。
Further, according to the present invention, by washing the filter device with a cleaning liquid containing almost no solid matter, the inside of the filter device and its associated piping can be effectively washed, and a liquid having metal corrosive properties such as seawater. In the case of a device for purifying the water, the occurrence of corrosion of the device during the stop period can be prevented.
In addition, by using the provided fresh water tank and desalination equipment for supplying the cleaning liquid, it is possible to clean the filter device with the cleaning liquid without newly installing a tank space for the cleaning liquid or a manufacturing apparatus for the cleaning liquid. it can.

また本発明において、複数の洗浄液通路の洗浄液通路開閉弁の前流側に洗浄液通路開閉弁と同数設けられて洗浄液通路を開閉する開閉元弁と、前記複数の洗浄液通路の洗浄液通路開閉弁の後流側に該洗浄液通路開閉弁と同数設けられて該洗浄液通路を開閉する遮断弁と、前記洗浄液通路の洗浄ポンプ出口側の圧力が所定の圧力範囲外となったとき故障発生の洗浄液通路開閉弁に対応する開閉元弁を閉じて当該洗浄液通路開閉弁への洗浄液の通流を遮断せしめる制御装置とを備える構成とすれば、
各洗浄液通路に対応する洗浄ユニットの圧力低下等によって洗浄液通路の洗浄液通路開閉弁の故障が検知された際には、制御装置により当該洗浄液通路開閉弁に通ずる開閉元弁を閉じるとともに遮断弁を閉じて当該洗浄液通路を完全に遮断状態にし、他の洗浄液通路開閉弁を開いておくことにより、前記洗浄液通路開閉弁の故障に伴って装置の運転を停止することなくフィルター装置を作動させることができる。
In the present invention, the same number of cleaning liquid passage opening / closing valves are provided upstream of the cleaning liquid passage opening / closing valves of the plurality of cleaning liquid passages as opening / closing source valves for opening / closing the cleaning liquid passages, and the cleaning liquid passage opening / closing valves of the plurality of cleaning liquid passages. A shut-off valve that is provided in the same number as the cleaning liquid passage opening and closing valves on the flow side and opens and closes the cleaning liquid passage; and a cleaning liquid passage opening and closing valve that generates a failure when the pressure on the cleaning pump outlet side of the cleaning liquid passage is outside a predetermined pressure range And a control device that closes the opening / closing source valve corresponding to and shuts off the flow of the cleaning liquid to the cleaning liquid passage opening / closing valve,
When a failure of the cleaning liquid passage opening / closing valve of the cleaning liquid passage is detected due to a pressure drop of the cleaning unit corresponding to each cleaning liquid passage, the control device closes the opening / closing source valve connected to the cleaning liquid passage opening / closing valve and the shut-off valve. By completely closing the cleaning liquid passage and opening other cleaning liquid passage opening / closing valves, the filter device can be operated without stopping the operation of the apparatus due to the failure of the cleaning liquid passage opening / closing valve. .

また本発明において、複数の洗浄液通路開閉弁のうち少なくとも2個の洗浄液通路開閉弁について同時に開弁するオーバーラップ期間を設定するとともに、洗浄液通路に該洗浄液通路内の圧力変動を吸収するアキュムレータを設置した構成とすれば、バルブが瞬間的に全閉となって圧力が急激に上昇することを防止できる。   In the present invention, an overlap period for simultaneously opening at least two cleaning liquid passage opening / closing valves among the plurality of cleaning liquid passage opening / closing valves is set, and an accumulator for absorbing pressure fluctuations in the cleaning liquid passage is installed in the cleaning liquid passage. With this configuration, it is possible to prevent the valve from being instantaneously fully closed and the pressure from rapidly rising.

また、前記洗浄液通開閉弁の開閉による圧力変動をアキュムレータによって緩和でき、これにより、洗浄液の安定供給を保持できる。   Further, the pressure fluctuation due to opening / closing of the cleaning liquid passage opening / closing valve can be reduced by the accumulator, so that the stable supply of the cleaning liquid can be maintained.

以下、本発明を図に示した実施例を用いて詳細に説明する。但し、この実施例に記載されている構成部品の寸法、材質、形状、その相対配置などは特に特定的な記載がない限り、この発明の範囲をそれのみに限定する趣旨ではなく、単なる説明例にすぎない。   Hereinafter, the present invention will be described in detail with reference to the embodiments shown in the drawings. However, the dimensions, materials, shapes, relative arrangements, and the like of the component parts described in this example are not intended to limit the scope of the present invention only to specific examples unless otherwise specified. Only.

図7は本発明が適用される船舶用バラスト水の無害化処理装置の系統図である。
図7において、101は未処理海水を濾過してごみ等の異物を捕獲するスクリーン、102は海水を海水処理ライン111に搬送する搬送ポンプである。
該搬送ポンプ102により海水処理ライン111を圧送された海水は、本発明の要旨であるフィルター装置4に導入される。該フィルター装置4及びこれの周辺機器の詳細については後述する。
FIG. 7 is a system diagram of a detoxifying apparatus for marine ballast water to which the present invention is applied.
In FIG. 7, 101 is a screen that filters untreated seawater and captures foreign matters such as dust, and 102 is a transport pump that transports seawater to the seawater treatment line 111.
Seawater pumped through the seawater treatment line 111 by the transport pump 102 is introduced into the filter device 4 which is the gist of the present invention. Details of the filter device 4 and peripheral devices thereof will be described later.

該フィルター装置4で固形物(微粒)を分離した後の海水は海水電解装置60に送り込まれる。また、該フィルター装置4のドレン排出口からのドレン排水はドレン管30を通して排水ライン110bに排出される。
前記海水電解装置60は海水を電気分解して、該海水中から次亜塩素酸ソーダ(以下次亜塩素酸という)を生成するものである。かかる電気分解を行うため電解槽107は、前記海水処理ライン111の前記フィルター装置4の下流部位から分岐してバラスト水タンク80の入口側で合流するバイパスライン107aに配設されている。該電解槽107へは、バイパスライン107aに設けられたポンプ112によって電気分解処理用の海水が導入される。
Seawater after the solid matter (fine particles) is separated by the filter device 4 is sent to the seawater electrolysis device 60. Further, drain drainage from the drain outlet of the filter device 4 is discharged to the drainage line 110 b through the drain pipe 30.
The seawater electrolyzer 60 electrolyzes seawater to produce sodium hypochlorite (hereinafter referred to as hypochlorous acid) from the seawater. In order to perform such electrolysis, the electrolytic cell 107 is disposed in a bypass line 107 a that branches from the downstream portion of the filter device 4 of the seawater treatment line 111 and merges at the inlet side of the ballast water tank 80. Seawater for electrolysis is introduced into the electrolytic cell 107 by a pump 112 provided in the bypass line 107a.

前記海水電解装置60の電解槽107で生成された次亜塩素酸は前記バイパスライン107aを通して海水処理ライン111に注入される。
以上のような、フィルター装置4に設定されたメッシュ以上の容積の固形物の捕獲処理、及び海水電解装置60による次亜塩素酸の生成及び注入処理がなされた処理海水は、バラスト水タンク80に搬入されて該バラスト水タンク80内に収容される。
また、前記バイパスライン107a合流後の海水処理ライン111から、一部の処理海水を再処理ライン111aを通して、前記搬送ポンプ102の吸入側に戻して、以上の処理を行う。
本発明は、かかる海水の無害化処理装置等をそなえた液体浄化システムに適用されるフィルター装置4に関するものである。
Hypochlorous acid generated in the electrolytic bath 107 of the seawater electrolyzer 60 is injected into the seawater treatment line 111 through the bypass line 107a.
The treated seawater that has been subjected to the capture processing of the solid matter having a volume larger than the mesh set in the filter device 4 and the generation and injection processing of hypochlorous acid by the seawater electrolysis device 60 is placed in the ballast water tank 80. It is carried in and accommodated in the ballast water tank 80.
Further, a part of the treated seawater is returned from the seawater treatment line 111 after joining the bypass line 107a to the suction side of the transport pump 102 through the reprocessing line 111a, and the above processing is performed.
The present invention relates to a filter device 4 applied to a liquid purification system having such a seawater detoxification device.

図5は本発明の第1実施例に係るフィルター装置及びその周辺機器の構成を示す系統図、図6は該フィルター装置の軸直角の部分断面図である。
図5において、筒状のフィルターハウジング27の内部には、上部及び下部が閉鎖された円筒体からなるフィルターエレメント21が収納されている。該フィルターエレメント21は中心軸44の上部に連結されたモータ43によって回転可能となっている。
また、前記フィルターハウジング27の外側室24内には前記搬送ポンプ102(図7参照)から未処理液供給管1を通して海水(未処理液)が導入され、該海水はフィルターエレメント21を外側から内側へと通過することにより固形物(微粒)をろ過分離して内側室26(図6参照)に流出し、ろ過液管9を通して海水処理ライン111に送出される。
FIG. 5 is a system diagram showing the configuration of the filter device and its peripheral devices according to the first embodiment of the present invention, and FIG. 6 is a partial cross-sectional view perpendicular to the axis of the filter device.
In FIG. 5, a filter element 21 made of a cylindrical body whose upper and lower parts are closed is housed inside a cylindrical filter housing 27. The filter element 21 can be rotated by a motor 43 connected to the upper part of the central shaft 44.
Seawater (untreated liquid) is introduced into the outer chamber 24 of the filter housing 27 from the transport pump 102 (see FIG. 7) through the untreated liquid supply pipe 1, and the seawater passes the filter element 21 from the outside to the inside. The solid matter (fine particles) is filtered and separated by passing through to the inner chamber 26 (see FIG. 6), and sent to the seawater treatment line 111 through the filtrate pipe 9.

次に、前記フィルター装置4の洗浄システムについて説明すると、前記フィルターエレメント21の高さ方向に沿って、複数組(この例では4組)の噴出ノズル22が配設され、図6のように、各噴出ノズル22から前記フィルターエレメント21の洗浄用の洗浄液を該フィルターエレメント21の外周面に吹き付けるようになっている。
前記各噴出ノズル22には、洗浄ポンプ33によって、ポンプ吸入通路32を通して洗浄液が供給される。前記各噴出ノズル22への洗浄液の供給、遮断は、各噴出ノズル22毎に設けられた開閉弁34によって行われる。
Next, the cleaning system of the filter device 4 will be described. A plurality of sets (four sets in this example) of ejection nozzles 22 are arranged along the height direction of the filter element 21, as shown in FIG. A cleaning liquid for cleaning the filter element 21 is sprayed from each ejection nozzle 22 onto the outer peripheral surface of the filter element 21.
A cleaning liquid is supplied to each jet nozzle 22 through a pump suction passage 32 by a cleaning pump 33. Supplying and shutting off the cleaning liquid to each of the ejection nozzles 22 is performed by an on-off valve 34 provided for each of the ejection nozzles 22.

また、前記フィルターハウジング27の下部にはドレン排出口23が設けられ、このドレン排出口23は前記フィルターエレメント21の外周面に臨んで開口して、該フィルターエレメント21洗浄時のドレン排水を該ドレン排出口23に導入可能となっている。
前記各ドレン排出口23の出口側は、開閉弁5をそなえたドレン管30に接続されている。31は前記ろ過液通路9と洗浄ポンプ33の吸入側に接続されるポンプ吸入通路32とを接続する洗浄液連絡管、6は該洗浄液連絡管31を開閉する連絡通路開閉弁である。
35は制御装置で、該制御装置35は、前記フィルターエレメント21用のモータ43の回転数、前記洗浄ポンプ33の回転数、前記噴出ノズル22用の開閉弁34の開閉のほかに、図4に示されるように、各開閉弁の開閉制御を行う(開閉制御の詳細は後述する)。
In addition, a drain discharge port 23 is provided in the lower part of the filter housing 27, and the drain discharge port 23 opens to face the outer peripheral surface of the filter element 21, and drains drained water when the filter element 21 is washed. It can be introduced into the discharge port 23.
The outlet side of each drain discharge port 23 is connected to a drain pipe 30 having an on-off valve 5. Reference numeral 31 denotes a cleaning fluid communication pipe that connects the filtrate passage 9 and the pump suction passage 32 connected to the suction side of the cleaning pump 33, and reference numeral 6 denotes a communication passage opening / closing valve that opens and closes the cleaning liquid communication pipe 31.
Reference numeral 35 denotes a control device. The control device 35 is arranged in addition to the rotational speed of the motor 43 for the filter element 21, the rotational speed of the cleaning pump 33, and the opening / closing valve 34 for the ejection nozzle 22. As shown, the opening / closing control of each opening / closing valve is performed (details of the opening / closing control will be described later).

かかる第1実施例において、フィルターエレメント21の洗浄時には、前記各噴出ノズル22の開閉弁34を開き、洗浄ポンプ33を運転して、図6のように、各噴出ノズル22からフィルターエレメント21の外面に吹き付けて該フィルターエレメント21に捕獲されている固形物(微粒)25を分離する。
それと同時に、排出側の開閉弁5を開く。固形物(微粒)25を伴った洗浄液は、ドレン排出口23に導入され、前記ドレン管30を通して排水ライン110b(図7参照)に排出される。
In the first embodiment, when the filter element 21 is cleaned, the opening / closing valve 34 of each of the ejection nozzles 22 is opened and the cleaning pump 33 is operated so that the outer surface of the filter element 21 is ejected from each of the ejection nozzles 22 as shown in FIG. The solids (fine particles) 25 captured by the filter element 21 are separated.
At the same time, the discharge-side on-off valve 5 is opened. The cleaning liquid accompanied by the solid matter (fine particles) 25 is introduced into the drain discharge port 23 and is discharged through the drain pipe 30 to the drain line 110b (see FIG. 7).

以上のように構成されたフィルター装置4において、本発明では、液体無害化処理装置の起動時及び停止時に、固形物の含有量が一定値以下、つまり固形物をほとんど含まない清浄液を清浄液通路39を通してフィルター装置4に導入し、該清浄液によってフィルター装置4を洗浄可能としている。
前記清浄液としては、淡水、もしくはいずれか酸化作用を有する物質を添加した洗浄液のいずれかを用いる。
図1〜4はこの第1実施例に係る液体無害化処理装置におけるフィルター装置4周りの洗浄液配管及び開閉弁の開閉動作を示す系統図で、図1は前記液体無害化処理装置の起動時、図2は定常運転時、図3は停止時における各開閉弁の開閉動作を示す。また、図4は起動時における制御装置による弁の開閉操作を示す。各図において、白色の弁は開弁状態、黒色の弁は閉弁状態をそれぞれ示す。
In the filter device 4 configured as described above, according to the present invention, when the liquid detoxification processing device is started and stopped, the content of solid matter is less than a certain value, that is, a cleaning solution containing almost no solid matter is used as a cleaning solution. It introduce | transduces into the filter apparatus 4 through the channel | path 39, and the filter apparatus 4 is washable with this cleaning liquid.
As the cleaning liquid, either fresh water or a cleaning liquid to which any substance having an oxidizing action is added is used.
1 to 4 are system diagrams showing the opening and closing operation of the cleaning liquid piping and the on-off valve around the filter device 4 in the liquid detoxification processing apparatus according to the first embodiment. FIG. FIG. 2 shows the open / close operation of each open / close valve during steady operation and FIG. 3 shows the stop operation. FIG. 4 shows the opening / closing operation of the valve by the control device at the time of activation. In each figure, a white valve indicates a valve open state, and a black valve indicates a valve closed state.

図1及び図4に示す起動時には、図1(A)のように、フィルター装置4への未処理液供給管1を開閉する未処理液通路開閉弁2を閉、フィルター装置4からのろ過液管9を開閉するろ過液通路開閉弁8を閉、前記洗浄液連絡管31を開閉する連絡通路開閉弁6を閉、前記各噴出ノズル22の開閉弁34を開、固形物をほとんど含まない清浄液を供給する清浄液供給管39を開閉する清浄液通路開閉弁7を開、前記ドレン管30を開閉する排液通路開閉弁5を開に操作する。
かかる操作によって、清浄液供給管39からの清浄液は、洗浄ポンプ33によって開閉弁34を介して各噴出ノズル22に圧送され、図6に示すように、該噴出ノズル22からフィルターエレメント21に吹き付けられ、該フィルターエレメント21に付着している固形物を除去する。該フィルターエレメント21から除去された固形物は、洗浄液(前記清浄液)とともにドレン排出口23に導入され、ドレン管30を通して外部に排出される。
1 and 4, the untreated liquid passage opening / closing valve 2 that opens and closes the untreated liquid supply pipe 1 to the filter device 4 is closed and the filtrate from the filter device 4 is closed as shown in FIG. The filtrate passage opening / closing valve 8 that opens and closes the pipe 9 is closed, the communication passage opening / closing valve 6 that opens and closes the cleaning liquid communication pipe 31 is closed, the opening / closing valve 34 of each of the ejection nozzles 22 is opened, and the cleaning liquid contains almost no solid matter. The cleaning liquid passage opening / closing valve 7 for opening and closing the cleaning liquid supply pipe 39 for supplying the liquid is opened, and the drainage passage opening / closing valve 5 for opening and closing the drain pipe 30 is opened.
As a result of this operation, the cleaning liquid from the cleaning liquid supply pipe 39 is pumped to the respective ejection nozzles 22 via the on-off valves 34 by the cleaning pump 33 and sprayed from the ejection nozzles 22 to the filter element 21 as shown in FIG. The solid matter adhering to the filter element 21 is removed. The solid matter removed from the filter element 21 is introduced into the drain outlet 23 together with the cleaning liquid (the cleaning liquid), and is discharged to the outside through the drain pipe 30.

そして、前記のような清浄液によるフィルターエレメント2の洗浄操作を行いながら、図1(B)のように、前記未処理液通路開閉弁2を開き、ろ過液通路開閉弁8を開く。
かかる操作によって、前記未処理液供給管1から海水をフィルター装置4内に導入し、フィルターエレメント21によってろ過する。前記洗浄用の清浄液及びフィルターエレメント21でろ過されたろ過液(ろ過海水)は該フィルターエレメント21から除去された固形物とともに、前記ドレン排出口23に排出される。その後定常運転に入る。
Then, while performing the cleaning operation of the filter element 2 with the cleaning liquid as described above, the untreated liquid passage opening / closing valve 2 is opened and the filtrate passage opening / closing valve 8 is opened as shown in FIG.
By this operation, seawater is introduced into the filter device 4 from the untreated liquid supply pipe 1 and filtered by the filter element 21. The cleaning liquid for cleaning and the filtrate (filtered seawater) filtered by the filter element 21 are discharged to the drain outlet 23 together with the solid matter removed from the filter element 21. Thereafter, steady operation is started.

図2に示す定常運転時には、図2(A)のように、図1(B)の状態から洗浄用の清浄液のラインを遮断する。即ち、前記未処理液通路開閉弁2及びろ過液通路開閉弁8を開いた状態で噴出ノズル22の開閉弁34及び清浄液通路開閉弁7及び連絡通路開閉弁6及び排液通路開閉弁5を閉じる。これにより、前記未処理液供給管1からの未処理の海水はフィルター装置4に導入されて該フィルター装置4で固形物をろ過した後、ろ過液はフィルター装置4からろ過液管9を通して海水処理ライン111(図7参照)に送出される。   At the time of steady operation shown in FIG. 2, as shown in FIG. 2 (A), the cleaning liquid line for cleaning is cut off from the state shown in FIG. 1 (B). That is, with the untreated liquid passage opening / closing valve 2 and the filtrate passage opening / closing valve 8 opened, the opening / closing valve 34, the cleaning liquid passage opening / closing valve 7, the communication passage opening / closing valve 6 and the drainage passage opening / closing valve 5 of the ejection nozzle 22 are opened. close. As a result, the untreated seawater from the untreated liquid supply pipe 1 is introduced into the filter device 4 and the solid matter is filtered by the filter device 4, and then the filtrate is treated with the seawater through the filtrate tube 9 from the filter device 4. It is sent to line 111 (see FIG. 7).

そして、定常運転時における洗浄操作時には、図2(B)のように、図2(A)の状態から前記清浄液通路開閉弁7を閉じたままとし、前記噴出ノズル22の開閉弁34及び連絡通路開閉弁6及び排液通路開閉弁5を開く。これにより、フィルター装置4は未処理海水のろ過動作を続けた状態で、フィルター装置4にはろ過液管9から分岐されたろ過液が洗浄液連絡管31を循環して前記洗浄ポンプ33に吸入され該洗浄ポンプ3から前記噴出ノズル22に圧送され、該噴出ノズル22からフィルターエレメント21に吹き付けられ、該フィルターエレメント21に付着している固形物を除去する。   At the time of the cleaning operation in the steady operation, as shown in FIG. 2 (B), the cleaning fluid passage opening / closing valve 7 is kept closed from the state of FIG. The passage opening / closing valve 6 and the drainage passage opening / closing valve 5 are opened. As a result, the filter device 4 continues the filtration operation of the untreated seawater, and the filtrate branched from the filtrate pipe 9 is circulated through the washing liquid communication pipe 31 and sucked into the washing pump 33 in the filter apparatus 4. The washing pump 3 is pumped to the ejection nozzle 22 and sprayed from the ejection nozzle 22 to the filter element 21 to remove solid matter adhering to the filter element 21.

図3に示す停止時には、停止動作前において図3(A)のように、図2(B)の状態から前記連絡通路開閉弁6を閉じ前記清浄液通路開閉弁7を開く。これによりフィルター装置4は未処理海水のろ過動作を続けた状態で、前記清浄液供給管39からの清浄液が洗浄ポンプ33によって開閉弁3を介して各噴出ノズル22に圧送され該噴出ノズル22からフィルターエレメント21に吹き付けられ、該フィルターエレメント21に付着している固形物を除去する。
そして停止後は図3(B)のように、図3(A)の状態から前記未処理液通路開閉弁2及びろ過液通路開閉弁8を閉じる。これによりフィルター装置4における未処理海水のろ過動作が停止され、前記清浄液供給管39からの清浄液によるフィルターエレメント21の洗浄動作が行われる。
At the time of stop shown in FIG. 3, before the stop operation, as shown in FIG. 3 (A), the communication passage opening / closing valve 6 is closed and the cleaning fluid passage opening / closing valve 7 is opened from the state of FIG. 2 (B). As a result, in the state where the filter device 4 continues the filtering operation of the untreated seawater, the cleaning liquid from the cleaning liquid supply pipe 39 is pressure-fed by the cleaning pump 33 to each of the ejection nozzles 22 via the opening / closing valve 3. The solid matter attached to the filter element 21 is removed by spraying on the filter element 21.
After the stop, as shown in FIG. 3 (B), the untreated liquid passage opening / closing valve 2 and the filtrate passage opening / closing valve 8 are closed from the state shown in FIG. 3 (A). Thereby, the filtering operation of the untreated seawater in the filter device 4 is stopped, and the cleaning operation of the filter element 21 by the cleaning liquid from the cleaning liquid supply pipe 39 is performed.

図4の例は、前記各開閉弁を制御装置35によって自動開閉するもので、該制御装置35は、図7に示される液体無害化処理装置の運転状態を設定あるいは検出する運転状態設定/検出手段51からの入力信号に基づき、該液体無害化処理装置の運転状態に応じて、前記清浄液通路開閉弁7、前記未処理液通路開閉弁2、前記連絡通路開閉弁6、前記ろ過液通路開閉弁3、前記排液通路開閉弁5、及び噴出ノズル22の開閉弁34を開閉制御するとともに、前記洗浄ポンプ33を運転制御する。   In the example of FIG. 4, each of the on-off valves is automatically opened and closed by the control device 35, and the control device 35 sets or detects the operation state of the liquid detoxification processing device shown in FIG. 7. Based on the input signal from the means 51, the cleaning liquid passage opening / closing valve 7, the untreated liquid passage opening / closing valve 2, the communication passage opening / closing valve 6, the filtrate passage according to the operating state of the liquid detoxification processing device. The on-off valve 3, the drainage passage on-off valve 5, and the on-off valve 34 of the ejection nozzle 22 are controlled to open and close, and the cleaning pump 33 is controlled to operate.

かかる第1実施例によれば、液体浄化システムの液体無害化処理装置の、前記各開閉弁からなる洗浄液切換え手段によって、清浄液供給管39の開閉弁7とフィルター装置4からのろ過液の一部が循環される洗浄液連絡管31の開閉弁6とを切り換えることにより、前記液体無害化処理装置の起動時及び停止時に、前記清浄液供給管39を通して固形物をほとんど含まない清浄液をフィルター装置4に導入して該清浄液によりフィルターエレメント21を洗浄しておき、前記起動時及び停止時以外の定常運転時に、前記清浄液によるフィルターエレメント21の洗浄操作を行ってから、あるいは該洗浄操作を行いながら、未処理液をフィルター装置4に導入して、フィルターエレメント21によるろ過を行うように構成したので、装置の起動時に、固形物をほとんど含まない清浄液をフィルターエレメント21に噴出させて該フィルターエレメント21を洗浄することにより、かかる清浄液でフィルターエレメント21内の固形物を完全に洗い落としてから、未処理液をフィルター装置4に導入して、フィルターエレメント21によるろ過を行う定常運転に入ることができる。   According to the first embodiment, one of the filtrates from the on-off valve 7 of the clean liquid supply pipe 39 and the filter device 4 by the cleaning liquid switching means comprising the on-off valves of the liquid detoxification processing device of the liquid purification system. By switching the on-off valve 6 of the cleaning liquid communication pipe 31 in which the part is circulated, when the liquid detoxification treatment apparatus is started and stopped, the cleaning liquid containing almost no solid matter is filtered through the cleaning liquid supply pipe 39 4 to clean the filter element 21 with the cleaning liquid, and after the cleaning operation of the filter element 21 with the cleaning liquid is performed during the steady operation other than at the time of starting and stopping, or the cleaning operation is performed. Since the untreated liquid was introduced into the filter device 4 while performing the filtration with the filter element 21, the device was started. In addition, the cleaning liquid containing almost no solid matter is jetted onto the filter element 21 to wash the filter element 21, so that the solid matter in the filter element 21 is completely washed away with the cleaning liquid, and then the untreated liquid is removed. It can introduce into the filter apparatus 4 and can enter the steady operation which performs filtration by the filter element 21.

要するにかかる第1実施例においては、起動時にフィルター清浄液を供給して洗浄しながら未処理液も濾過することで、起動時におけるフィルターエレメント21の目詰まりを防止でき、装置の起動から停止までフィルター装置のろ過液等の多少の固形物が混入されている液を洗浄液として用いている前記従来技術のように、特に起動後に洗浄液中の固形物によってフィルターエレメント21が目詰まりを起こすのを回避できる。   In short, in the first embodiment, the filter element 21 can be prevented from being clogged at the start-up by supplying the filter cleaning liquid at the time of start-up and filtering the untreated liquid while washing. It is possible to avoid clogging of the filter element 21 due to the solid matter in the cleaning liquid, especially after the start-up, as in the above-described prior art using a liquid in which some solid matter such as the filtrate of the apparatus is mixed as the cleaning liquid. .

従ってかかる第1実施例によれば、前記のようなフィルターエレメント21の目詰まりによる該フィルターエレメント21のろ過機能の低下に伴う、洗浄液ポンプの回転部分や洗浄液通路の開閉弁に固形物の噛み込み、及びかかる固形物の噛み込みによる前記機器の故障の発生を回避でき、これにより無害化処理装置の安定運転を実現できて、装置の信頼性を向上できる。   Therefore, according to the first embodiment, solid matter is caught in the rotating part of the cleaning liquid pump and the opening / closing valve of the cleaning liquid passage due to the decrease in the filtering function of the filter element 21 due to the clogging of the filter element 21 as described above. Further, it is possible to avoid the occurrence of the failure of the device due to the biting of the solid matter, thereby realizing the stable operation of the detoxification processing apparatus and improving the reliability of the apparatus.

図8は本発明の第2実施例に係るフィルター装置及びその周辺機器の構成を示す系統図である。
この第2実施例においては、前記噴出ノズル22への複数の洗浄液通路の前記噴出ノズルの開閉弁34の前流側に該開閉弁34と同数(この例では4個)の開閉元弁41を設けるとともに、前記開閉弁34の後流側に該開閉弁34と同数(この例では4個)の遮断弁40を設けて、前記開閉元弁41を制御装置35により開閉制御するように構成されている。
FIG. 8 is a system diagram showing the configuration of the filter device and its peripheral devices according to the second embodiment of the present invention.
In this second embodiment, the same number (four in this example) of open / close valves 41 as the open / close valves 34 are provided on the upstream side of the open / close valves 34 of the jet nozzles of the plurality of cleaning liquid passages to the jet nozzles 22. In addition, the same number (four in this example) of shut-off valves 40 as the on-off valves 34 are provided on the downstream side of the on-off valves 34, and the on-off source valves 41 are controlled to be opened and closed by the control device 35. ing.

そしてこの第2実施例においては、前記洗浄ポンプ33出口側における前記噴出ノズル22毎の各洗浄ユニットの圧力を検出する圧力センサ331を設けて(図8には該圧力センサ331を1個表示している)、該圧力センサ331による各洗浄ユニットの洗浄圧力の検出値を前記制御装置35に入力し、該制御装置35においては、前記洗浄圧力が予め設定された許容値以下になったとき、当該洗浄ユニットの開閉弁34に故障が発生しているものと判断して、当該洗浄ユニットの開閉元弁41を閉じる。続いて当該洗浄ユニットの前記遮断弁40を閉じ、当該洗浄ユニットへの洗浄液の通流を遮断せしめる。
尚、かかる開閉弁34の故障が発生した場合には、前記制御装置35においては、前記洗浄ポンプ33の吐出容量を開閉弁34の故障数におい応じて減少させる。
その他の構成は前記第1実施例(図5)と同様であり、これと同一の部材は同一の符号で示す。
In the second embodiment, a pressure sensor 331 for detecting the pressure of each cleaning unit for each of the ejection nozzles 22 on the outlet side of the cleaning pump 33 is provided (one pressure sensor 331 is displayed in FIG. 8). ), The detection value of the cleaning pressure of each cleaning unit by the pressure sensor 331 is input to the control device 35, and in the control device 35, when the cleaning pressure is less than or equal to a preset allowable value, It is determined that a failure has occurred in the opening / closing valve 34 of the cleaning unit, and the opening / closing source valve 41 of the cleaning unit is closed. Subsequently, the shutoff valve 40 of the cleaning unit is closed, and the flow of the cleaning liquid to the cleaning unit is shut off.
When the on / off valve 34 fails, the control device 35 reduces the discharge capacity of the cleaning pump 33 in accordance with the number of on / off valve 34 failures.
Other configurations are the same as those of the first embodiment (FIG. 5), and the same members are denoted by the same reference numerals.

かかる第2実施例によれば、圧力センサ331による各洗浄ユニットの洗浄圧力の検出値によって、噴出ノズル22毎の各洗浄ユニットの開閉弁34の故障が検知された際には、制御装置35により当該開閉弁34に通ずる開閉元弁41を閉じるとともに遮断弁40を閉じて、当該洗浄液通路を完全に遮断状態にし、他の開閉弁34を開いておくことにより、前記開閉弁34の故障に伴って装置の運転を停止することなく、フィルター装置4を作動させることができる。   According to the second embodiment, when a failure of the opening / closing valve 34 of each cleaning unit 22 for each ejection nozzle 22 is detected by the detection value of the cleaning pressure of each cleaning unit by the pressure sensor 331, the control device 35 When the on-off valve 34 is closed, the on-off valve 41 is closed and the shut-off valve 40 is closed to completely shut off the cleaning liquid passage and keep the other on-off valves 34 open. Thus, the filter device 4 can be operated without stopping the operation of the device.

図9は本発明の第3実施例に係るフィルター装置及びその周辺機器の構成を示す系統図である。
この第3実施例においては、図9(B)のように、複数の前記噴出ノズル22の開閉弁34a〜34dのうち少なくとも2個の開閉弁34a,34bについて同時に開弁するオーバーラップ期間を設定している。
これにより、前記噴出ノズル22の開閉弁34の故障が発生しても、開弁期間がオーバーラップしている他の開閉弁34が開いているので、フィルター装置4への洗浄液の供給を前記故障に支障されることなく円滑に行うことができる。
また、この第3実施例においては、洗浄ポンプ33出口に該洗浄液の通路32内の圧力変動を吸収するアキュムレータ50を設置している。これにより、前記噴出ノズル22の開閉弁34の開閉による圧力変動を前記アキュムレータ50によって緩和でき、洗浄液の安定供給を保持できる。
図9に示す第3実施例において、前記第1実施例と同一の部材は同一の符号で示す。
FIG. 9 is a system diagram showing the configuration of the filter device and its peripheral devices according to the third embodiment of the present invention.
In the third embodiment, as shown in FIG. 9B, an overlap period is set in which at least two on-off valves 34a and 34b among the on-off valves 34a to 34d of the plurality of ejection nozzles 22 are simultaneously opened. is doing.
Thereby, even if the failure of the on-off valve 34 of the ejection nozzle 22 occurs, the other on-off valve 34 whose valve opening period overlaps is open, so that the supply of the cleaning liquid to the filter device 4 is failed. Can be carried out smoothly without any trouble.
In the third embodiment, an accumulator 50 that absorbs pressure fluctuation in the cleaning liquid passage 32 is installed at the outlet of the cleaning pump 33. As a result, pressure fluctuation due to opening / closing of the opening / closing valve 34 of the ejection nozzle 22 can be mitigated by the accumulator 50, and a stable supply of cleaning liquid can be maintained.
In the third embodiment shown in FIG. 9, the same members as those in the first embodiment are denoted by the same reference numerals.

図10は本発明の第4実施例に係る液体の無害化処理装置の系統図である。
この第4実施例においては、搬送ポンプ2により搬送される未処理の液体中の微生物を除去して清浄な処理液体に転換し、この処理液体をバラスト水タンク80に収容するように構成され、前記搬送ポンプ2からの液体に遠心力を付与して該液体中から固形物を分離する液体サイクロン(遠心式固液分離装置)70と、前記フィルター装置4と、前記液体が通流する液体処理ラインの前記液体サイクロン70及びフィルター装置4の下流側に設けられて前記液体の全部または一部を電解槽にて電気分解して塩素含有物質を生成する液体電解装置60とを備えている。
かかる第4実施例によれば、液体サイクロン(遠心式固液分離装置)70で比重の大きい固形物を分離した液体をフィルター装置4に導入するので、フィルター装置4の負荷が軽減される。
FIG. 10 is a system diagram of a liquid detoxifying apparatus according to the fourth embodiment of the present invention.
In this fourth embodiment, the microorganisms in the untreated liquid transported by the transport pump 2 are removed and converted to a clean processing liquid, and this processing liquid is stored in the ballast water tank 80, A liquid cyclone (centrifugal solid-liquid separator) 70 that applies a centrifugal force to the liquid from the transport pump 2 to separate solids from the liquid, the filter device 4, and a liquid process through which the liquid flows. The liquid cyclone 70 provided on the downstream side of the line and the filter device 4 in the line is provided with a liquid electrolyzer 60 that electrolyzes all or part of the liquid in an electrolytic cell to generate a chlorine-containing substance.
According to the fourth embodiment, since the liquid obtained by separating the solid matter having a large specific gravity with the liquid cyclone (centrifugal solid-liquid separation device) 70 is introduced into the filter device 4, the load on the filter device 4 is reduced.

本発明によれば、フィルター装置を備えた液体浄化装置の特に起動時及び停止時におけるフィルターエレメントの固形物の目詰まりの発生を回避して、フィルターエレメント洗浄液への固形物の混入に伴う液体浄化装置の正常運転の阻害を防止するとともに、洗浄液ポンプや弁類等の洗浄液用機器の故障の発生を防止し、さらには、液体浄化装置の停止期間中におけるバラストタンク内の微生物の増殖やタンクの腐食を防止可能なフィルター装置及びこのフィルター装置を備えた液体の浄化システムを提供できる。   According to the present invention, it is possible to avoid the occurrence of clogging of the solid matter of the filter element, particularly when starting and stopping the liquid purification device provided with the filter device, and to purify the liquid accompanying the mixing of the solid matter into the filter element cleaning liquid. In addition to preventing the normal operation of the system from being hindered, it is possible to prevent the failure of cleaning liquid equipment such as cleaning liquid pumps and valves, as well as the growth of microorganisms in the ballast tank and the tank A filter device capable of preventing corrosion and a liquid purification system provided with the filter device can be provided.

(A)、(B)は本発明の第1実施例に係る液体無害化処理装置におけるフィルター装置周りの洗浄液配管及び開閉弁の開閉動作を示す系統図で、液体無害化処理装置の起動時を示す。(A), (B) is a system diagram showing the opening and closing operation of the cleaning liquid pipe and the on-off valve around the filter device in the liquid detoxification processing apparatus according to the first embodiment of the present invention. Show. (A)、(B)は前記第1実施例における図1対応図で、定常運転時を示す。(A) and (B) are diagrams corresponding to FIG. 1 in the first embodiment, and show a steady operation. (A)、(B)は前記第1実施例における図1対応図で、停止時を示す。(A), (B) is a view corresponding to FIG. 1 in the first embodiment, and shows a stop state. 前記第1実施例における図1対応図で、液体無害化処理装置の起動時の自動運転の構成を示す。FIG. 1 is a diagram corresponding to FIG. 1 in the first embodiment, and shows a configuration of automatic operation when the liquid detoxification processing apparatus is activated. 本発明の第1実施例に係るフィルター装置及びその周辺機器の構成を示す系統図である。It is a systematic diagram which shows the structure of the filter apparatus which concerns on 1st Example of this invention, and its peripheral device. 前記第1実施例におけるフィルター装置の軸直角の部分断面図である。It is a fragmentary sectional view at right angles to the axis of the filter device in the first embodiment. 本発明が適用される船舶用バラスト水の無害化処理装置の系統図であるIt is a systematic diagram of the detoxification processing apparatus for ship ballast water to which the present invention is applied. 本発明の第2実施例に係るフィルター装置及びその周辺機器の構成を示す系統図である。It is a systematic diagram which shows the structure of the filter apparatus which concerns on 2nd Example of this invention, and its peripheral device. 本発明の第3実施例に係るフィルター装置及びその周辺機器の構成を示す系統図である。It is a systematic diagram which shows the structure of the filter apparatus which concerns on 3rd Example of this invention, and its peripheral device. 本発明の第4実施例に係る液体の無害化処理装置の系統図である。It is a systematic diagram of the liquid detoxification processing apparatus which concerns on 4th Example of this invention.

符号の説明Explanation of symbols

1 未処理液供給管
2 未処理液通路開閉弁
4 フィルター装置
5 排液通路開閉弁
6 連絡通路開閉弁
7 清浄液通路開閉弁
8 ろ過液通路開閉弁
9 ろ過液管
21 フィルターエレメント
22 噴出ノズル
23 ドレン排出口
24 外側室
26 内側室
27 フィルターハウジング
30 ドレン管
31 洗浄液連絡管
33 洗浄ポンプ
34 開閉弁
35 制御装置
39 清浄液供給管
40 遮断弁
41 開閉元弁
50 アキュムレータ
60 海水電解装置
70 液体サイクロン(遠心式固液分離装置)
111 海水処理ライン
DESCRIPTION OF SYMBOLS 1 Untreated liquid supply pipe 2 Untreated liquid passage opening / closing valve 4 Filter device 5 Drainage passage opening / closing valve 6 Communication passage opening / closing valve 7 Clean liquid passage opening / closing valve 8 Filtrant passage opening / closing valve 9 Filtrate passage opening / closing valve 9 Filter element 22 Filter element 22 Jet nozzle 23 Drain discharge port 24 Outer chamber 26 Inner chamber 27 Filter housing 30 Drain pipe 31 Cleaning liquid communication pipe 33 Cleaning pump 34 On-off valve 35 Control device 39 Clean liquid supply pipe 40 Shut-off valve 41 Opening / closing source valve 50 Accumulator 60 Seawater electrolysis device 70 Liquid cyclone ( Centrifugal solid-liquid separator)
111 Seawater treatment line

Claims (9)

固形物が混入された未処理液を、フィルターエレメントを通すことにより該固形物をろ過してろ過液通路に排出するフィルター装置の洗浄方法であって、前記フィルター装置の
作動を開始する起動時及び作動を終了する停止時に、固形物の含有量が一定値以下の清浄液を清浄液通路を通して前記フィルター装置に導入して該清浄液により前記フィルターエレメントを洗浄することを特徴とするフィルター装置の洗浄方法。
A cleaning method of a filter device for filtering untreated liquid mixed with solid matter through a filter element and discharging the solid matter to a filtrate passage, at the start of operation of the filter device and Cleaning the filter device, wherein when the operation is stopped, a cleaning liquid having a solid content of a predetermined value or less is introduced into the filter device through a cleaning liquid passage and the filter element is cleaned with the cleaning liquid. Method.
前記起動時及び停止時以外の運転時に、前記清浄液による前記フィルターエレメントの洗浄操作を行ってからあるいは該洗浄操作を行いながら、前記未処理液をフィルター装置に導入して前記フィルターエレメントによるろ過を行うことを特徴とする請求項1記載のフィルター装置の洗浄方法。   During operation other than at the time of starting and stopping, after performing the cleaning operation of the filter element with the cleaning liquid or while performing the cleaning operation, the untreated liquid is introduced into the filter device and filtered by the filter element. The method for cleaning a filter device according to claim 1, wherein the cleaning is performed. 前記清浄液として、淡水、前記未処理液に遠心力を付与してこの液体中から固形物を分離する遠心式固液分離装置で処理された液体、もしくは酸化作用を有する物質を含む洗浄液のいずれかを用いることを特徴とする請求項1記載のフィルター装置の洗浄方法。   As the cleaning liquid, either fresh water, a liquid processed by a centrifugal solid-liquid separation device that applies a centrifugal force to the untreated liquid to separate solids from the liquid, or a cleaning liquid containing a substance having an oxidizing action The method for cleaning a filter device according to claim 1, wherein: 固形物が混入された未処理液を、フィルターエレメントを通すことにより該固形物をろ過してろ過液通路に排出するフィルター装置と、前記フィルター装置を洗浄する洗浄液を該フィルター装置に給排する洗浄装置とを有する液体無害化処理装置を備えた液体浄化システムにおいて、固形物の含有量が一定値以下の清浄液を前記フィルター装置に供給する清浄液通路からなる第1の洗浄液通路と、該第1の洗浄液通路を開閉する清浄液通路開閉弁と、前記フィルター装置への未処理液供給通路を開閉する未処理液通路開閉弁と、前記フィルター装置に接続される第2の洗浄液通路を開閉する洗浄液通路開閉弁と、前記フィルター装置からのろ過液通路を開閉するろ過液通路開閉弁と、前記フィルター装置からの洗浄排液通路を開閉する排液通路開閉弁とをそなえるとともに、前記液体無害化処理装置の起動時及び停止時に前記清浄液通路開閉弁を開くとともに前記洗浄液通路開閉弁を閉じて前記第1の洗浄液通路を通して前記清浄液をフィルター装置に供給せしめる洗浄液切換え手段をそなえたことを特徴とする液体浄化システム。   A filter device that filters untreated liquid mixed with solid matter through a filter element and discharges the solid matter to a filtrate passage, and cleaning that supplies and discharges a cleaning solution for washing the filter device to the filter device In a liquid purification system comprising a liquid detoxification processing apparatus having a device, a first cleaning liquid passage comprising a cleaning liquid passage for supplying a cleaning liquid having a solid content of a predetermined value or less to the filter device; A cleaning liquid passage opening / closing valve for opening / closing one cleaning liquid passage, an untreated liquid passage opening / closing valve for opening / closing an untreated liquid supply passage to the filter device, and a second cleaning liquid passage connected to the filter device. A cleaning fluid passage opening / closing valve, a filtrate passage opening / closing valve that opens and closes a filtrate passage from the filter device, and a drainage passage that opens and closes a cleaning drain passage from the filter device. The cleaning liquid passage opening / closing valve is opened and the cleaning liquid passage opening / closing valve is closed when the liquid detoxification processing device is started and stopped, and the cleaning liquid passage opening / closing valve is closed, and the cleaning liquid is passed through the first cleaning liquid passage to the filter device. A liquid purification system characterized by comprising cleaning liquid switching means for supply. 前記洗浄液切換え手段は、前記液体無害化処理装置の起動時及び停止時以外の運転時に、前記清浄液通路開閉弁を閉じるとともに前記洗浄液通路開閉弁を開いて前記第2の洗浄液通路からの洗浄液をフィルター装置に供給せしめるように構成されたことを特徴とする請求項4記載の液体浄化システム。   The cleaning liquid switching means closes the cleaning liquid passage opening / closing valve and opens the cleaning liquid passage opening / closing valve and supplies the cleaning liquid from the second cleaning liquid passage during operation other than when the liquid detoxification treatment apparatus is started and stopped. The liquid purification system according to claim 4, wherein the liquid purification system is configured to be supplied to a filter device. 前記洗浄液切換え手段は、前記液体無害化処理装置の運転状態を設定あるいは検出する運転状態設定/検出手段からの入力信号に基づき、前記液体浄化装置の運転状態に応じて前記清浄液通路開閉弁、前記未処理液通路開閉弁、前記洗浄液通路開閉弁、前記ろ過液通路開閉弁、及び前記排液通路開閉弁を開閉制御するとともに、前記洗浄装置に設けられた洗浄ポンプを運転制御する制御装置からなることを特徴とする請求項4または5のいずれかに記載の液体浄化システム。   The cleaning liquid switching means is based on an input signal from an operation state setting / detection means for setting or detecting an operation state of the liquid detoxification processing device, and the cleaning liquid passage opening / closing valve according to the operation state of the liquid purification device, From the control device that controls the opening and closing of the untreated liquid passage opening and closing valve, the cleaning liquid passage opening and closing valve, the filtrate passage passage opening and closing valve, and the drainage passage opening and closing valve and the operation control of the washing pump provided in the washing device The liquid purification system according to claim 4 or 5, wherein 前記液体無害化処理装置は、未処理の液体中の微生物を除去して清浄な処理液体に転換し、この処理液体をバラストタンクに収容するように構成されるとともに、前記液体に遠心力を付与して該液体中から固形物を分離する遠心式固液分離装置と、前記フィルター装置と、前記液体が通流する液体処理ラインの前記遠心式固液分離装置及びフィルター装置の下流側に設けられ、前記液体の全部または一部を電解槽にて電気分解して塩素含有物質を生成する液体電解装置とを備え、フィルター装置のフィルターエレメントを洗浄する洗浄液として前記遠心式固液分離装置で固形物分離後の液体または前記液体電解装置で塩素処理を行った後の液体のいずれかを用いたことを特徴とする請求項4記載の液体浄化システム。   The liquid detoxification treatment device is configured to remove microorganisms in the untreated liquid and convert it into a clean treatment liquid, and to store the treatment liquid in a ballast tank and to apply centrifugal force to the liquid. The solid-liquid separation device for separating solids from the liquid, the filter device, and the centrifugal solid-liquid separation device and the filter device in the liquid processing line through which the liquid flows. A liquid electrolysis apparatus that electrolyzes all or a part of the liquid in an electrolytic cell to produce a chlorine-containing substance, and a solid material is obtained by the centrifugal solid-liquid separation apparatus as a cleaning liquid for cleaning the filter element of the filter apparatus. The liquid purification system according to claim 4, wherein either the liquid after separation or the liquid after chlorination is performed in the liquid electrolysis apparatus is used. フィルターハウジング内に収納され回転可能な筒状のフィルターエレメントの外側に形成される外側室に未処理液体を導入し、該液体を前記フィルターエレメントを通して固形物をろ過してから該フィルターエレメントの内側に形成される内側室に流出させるように構成されたフィルター装置と、洗浄ポンプから送給される前記フィルターエレメントの洗浄用の洗浄液を該フィルターエレメントの外周面に吹き付ける複数の噴出ノズルと、前記洗浄ポンプと前記複数の噴出ノズルとを接続する複数の洗浄液通路をそれぞれ開閉する複数の洗浄液通路開閉弁とをそなえた液体浄化システムにおいて、前記複数の洗浄液通路の前記洗浄液通路開閉弁の前流側に該洗浄液通路開閉弁と同数設けられて該洗浄液通路を開閉する開閉元弁と、前記複数の洗浄液通路の前記洗浄液通路開閉弁の後流側に該洗浄液通路開閉弁と同数設けられて該洗浄液通路を開閉する遮断弁と、前記洗浄液通路の圧力が所定の圧力範囲外となったとき故障発生の前記洗浄液通路開閉弁に対応する前記開閉元弁を閉じて当該洗浄液通路開閉弁への洗浄液の通流を遮断せしめる制御装置を備えたことを特徴とする液体浄化システム。   An untreated liquid is introduced into an outer chamber formed outside a rotatable cylindrical filter element that is housed in a filter housing, and the solid is filtered through the filter element before the inside of the filter element. A filter device configured to flow into the formed inner chamber, a plurality of ejection nozzles for spraying a cleaning liquid for cleaning the filter element fed from a cleaning pump to an outer peripheral surface of the filter element, and the cleaning pump And a plurality of cleaning liquid passage opening / closing valves that respectively open and close a plurality of cleaning liquid passages connecting the plurality of ejection nozzles, the cleaning liquid passages on the upstream side of the cleaning liquid passage opening / closing valves. The same number of cleaning liquid passage opening / closing valves as opening / closing source valves for opening and closing the cleaning liquid passage, A shut-off valve that opens and closes the cleaning liquid passage on the downstream side of the cleaning liquid passage opening and closing valve of the cleaning liquid passage, and a failure when the pressure of the cleaning liquid passage is outside a predetermined pressure range A liquid purification system, comprising: a control device that closes the opening / closing source valve corresponding to the generated cleaning liquid passage opening / closing valve to block the flow of the cleaning liquid to the cleaning liquid passage opening / closing valve. フィルターハウジング内に収納され回転可能な筒状のフィルターエレメントの外側に形成される外側室に未処理液体を導入し、該液体を前記フィルターエレメントを通して固形物をろ過してから該フィルターエレメントの内側に形成される内側室に流出させるように構成されたフィルター装置と、洗浄ポンプから送給される前記フィルターエレメントの洗浄用の洗浄液を該フィルターエレメントの外周面に吹き付ける複数の噴出ノズルと、前記洗浄ポンプと前記複数の噴出ノズルとを接続する複数の洗浄液通路をそれぞれ開閉する複数の洗浄液通路開閉弁とをそなえた液体浄化システムにおいて、前記複数の洗浄液通路開閉弁のうち少なくとも2個の洗浄液通路開閉弁について同時に開弁するオーバーラップ期間を設定するとともに、前記洗浄液通路に該洗浄液通路内の圧力変動を吸収するアキュムレータを設置したことを特徴とする液体浄化システム。   An untreated liquid is introduced into an outer chamber formed outside a rotatable cylindrical filter element that is housed in a filter housing, and the solid is filtered through the filter element before the inside of the filter element. A filter device configured to flow into the formed inner chamber, a plurality of ejection nozzles for spraying a cleaning liquid for cleaning the filter element fed from a cleaning pump to an outer peripheral surface of the filter element, and the cleaning pump And a plurality of cleaning liquid passage opening / closing valves that respectively open and close a plurality of cleaning liquid passages connecting the plurality of ejection nozzles, and at least two cleaning liquid passage opening / closing valves among the plurality of cleaning liquid passage opening / closing valves Set the overlap period to open at the same time and Fluid purification system, characterized in that installed the accumulator to absorb pressure fluctuations in the cleaning liquid passage into the liquid passage.
JP2007055063A 2007-03-06 2007-03-06 Filter device cleaning method and liquid purification system provided with the filter device Pending JP2008212851A (en)

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JP2010094584A (en) * 2008-10-14 2010-04-30 Asahi Kasei Chemicals Corp Method of treating ballast water and apparatus for treating ballast water
JP2013523426A (en) * 2010-03-30 2013-06-17 青▲島▼海▲徳▼威科技有限公司 Ship ballast water treatment method and system
JP2014530099A (en) * 2011-10-14 2014-11-17 パンアジア カンパニー リミテッド Multi-cage type ballast water filtration device and method for automatically controlling sequential backwashing
WO2014188929A1 (en) * 2013-05-23 2014-11-27 住友電気工業株式会社 Ballast-water treatment device and ballast-water management system
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US9908793B2 (en) 2013-05-23 2018-03-06 Sumitomo Electric Industries, Ltd. Ballast water treatment apparatus and ballast water management system
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WO2015104950A1 (en) * 2014-01-08 2015-07-16 住友電気工業株式会社 Water treatment device and water treatment method
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