JP2014151278A - Method for cleaning sand filter apparatus - Google Patents

Method for cleaning sand filter apparatus Download PDF

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JP2014151278A
JP2014151278A JP2013023565A JP2013023565A JP2014151278A JP 2014151278 A JP2014151278 A JP 2014151278A JP 2013023565 A JP2013023565 A JP 2013023565A JP 2013023565 A JP2013023565 A JP 2013023565A JP 2014151278 A JP2014151278 A JP 2014151278A
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sand layer
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JP6101099B2 (en
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Katsunori Matsui
克憲 松井
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Mitsubishi Heavy Industries Ltd
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Abstract

PROBLEM TO BE SOLVED: To shorten time required for a rinse step carried out during cleaning operation of a sand filter apparatus.SOLUTION: A method for cleaning a sand filter apparatus comprises: a liquid drain step of discharging raw sea water sw (water to be treated) from a filter sand layer 16 after filtering of the raw sea water sw; a gas cleaning step of introducing air a from the outlet side of a housing 14 after the liquid drain step and removing impurities captured in the filter sand layer 16 from the filter sand layer 16; an impurity discharge step of introducing concentrated sea water cs (cleaning water) from the outlet side of the housing 14 into the filter sand layer 16 and discharging the removed impurities together with the concentrated sea water cs from the filter sand layer 16; a cleaning water discharge step of flowing down the concentrated sea water cs from the filter sand layer 16 by a gravity force after the impurity discharge step; and a rinse step of introducing the raw sea water sw as rinse water into the filter sand layer 16 from the inlet side of the housing 14 and adjusting the layer state of the filter sand layer 16 while replacing the concentrated sea water cs remained in the filter sand layer 16 with the raw sea water sw.

Description

本発明は、例えば、海水淡水化プラント等に設けられる砂ろ過装置において、ろ砂層の洗浄に要する時間を短縮可能にした洗浄方法に関する。   The present invention relates to a cleaning method capable of shortening the time required for cleaning a filter sand layer in a sand filter provided in a seawater desalination plant, for example.

海水淡水化プラントにおいて、海水を淡水化する処理工程は、前処理として、砂ろ過装置で原海水中に含まれる不純物を除去し、その後、海水を蒸留して淡水を生成する多段フラッシュ法や、海水に圧力をかけて逆浸透膜と呼ばれるろ過膜を通すことで海水の塩分を濃縮して分離し、淡水を生成する逆浸透法等を用いて海水から塩分を除去している。特許文献1には、海水から飲料水や工業用水のような無イオン水を製造する工程が開示されている。この製造工程は、砂ろ過装置で原海水中のゴミ類や微生物等の比較的大きな夾雑物を除去した後、イオン交換膜や逆浸透膜を用いた膜分離工程及び蒸発濃縮工程を経て、塩分を除去した無イオン水を製造するものである。   In the seawater desalination plant, the process of desalinating seawater is a pre-treatment that removes impurities contained in the raw seawater with a sand filter, and then distills the seawater to produce fresh water, The salt content of seawater is concentrated and separated by applying a pressure to seawater and passing through a filtration membrane called a reverse osmosis membrane, and the salt content is removed from the seawater using a reverse osmosis method that produces fresh water. Patent Document 1 discloses a process for producing non-ionized water such as drinking water and industrial water from seawater. In this production process, after removing relatively large contaminants such as garbage and microorganisms in the raw seawater using a sand filtration device, the membrane is subjected to a membrane separation process using an ion exchange membrane or a reverse osmosis membrane and an evaporative concentration step, followed by a salt content. Non-ionized water from which water has been removed is produced.

砂ろ過装置に設けられたろ砂層には捕捉された不純物が堆積し、そのままにしておくと閉塞してしまうので、堆積した不純物をろ砂層から除去する必要がある。不純物をろ砂層から除去するために、洗浄水をろ砂層の出口側からろ砂層に導入してろ砂層の表面や内部に捕捉された不純物を剥離させる逆流洗浄方法が用いられる。特許文献2には、かかる砂ろ過装置の逆洗方法が開示されている。   The trapped impurities are deposited on the filter sand layer provided in the sand filter and clogged if left as it is. Therefore, it is necessary to remove the deposited impurities from the filter sand layer. In order to remove impurities from the filter sand layer, a back-flow cleaning method is used in which washing water is introduced into the filter sand layer from the outlet side of the filter sand layer to remove impurities trapped on the surface or inside of the filter sand layer. Patent Document 2 discloses a backwashing method for such a sand filtration device.

特開2009−95821号公報JP 2009-95821 A 特開2005−211804号公報Japanese Patent Laid-Open No. 2005- 211804

砂ろ過装置の洗浄作業は、洗浄水の主成分である原海水の性状が清澄な場合は、ろ砂層への不純物の堆積が緩やかなため、逆洗の頻度は少なくて済むが、原海水が不純物を多く含む汚れた海水の場合は、ろ砂層への不純物の堆積が速くなるので、洗浄作業の頻度を多くする必要がある。
一方、砂ろ過装置の洗浄時に処理設備の稼動を中断させないため、通常、2基以上の砂ろ過装置が、被処理水の導入路に対して並列に設けられている。ここでいう被処理水とは、砂ろ過装置で処理される原水のことであり、海水淡水化プラントにおいては、原海水のことである。また、処理設備の処理能力が大のとき多数の砂ろ過装置が設けられる。この場合、1基の砂ろ過装置の洗浄時間が長くなると、処理設備の稼動時間に影響を与えると共に、他の砂ろ過装置の洗浄時間を十分に取れなくなる。
The washing operation of the sand filtration device requires less frequent backwashing because the accumulation of impurities in the filter sand layer is slow when the properties of the raw seawater, which is the main component of the washing water, are clear. In the case of dirty seawater containing a large amount of impurities, the accumulation of impurities in the filter sand layer is accelerated, and therefore the frequency of cleaning work must be increased.
On the other hand, in order not to interrupt the operation of the treatment facility during the cleaning of the sand filtration device, usually two or more sand filtration devices are provided in parallel to the introduction path of the water to be treated. The to-be-processed water here is the raw water processed with a sand filtration apparatus, and is a seawater in a seawater desalination plant. In addition, a large number of sand filtration devices are provided when the processing capacity of the processing equipment is large. In this case, if the cleaning time of one sand filter device becomes long, the operation time of the processing facility is affected, and the cleaning time of other sand filter devices cannot be taken sufficiently.

そこで、本発明者等は、不純物の除去効果を維持しつつ、洗浄時間を短縮可能な洗浄方法を検討し、以下説明する洗浄方法を考えた。この洗浄方法を図2の(A)及び(B)により説明する。図2(A)は、海水淡水化プラントにおいて、清澄な海水を扱う場合を示し、(B)は不純物を多く含む汚れた海水を扱う場合を示す。   Accordingly, the present inventors examined a cleaning method capable of shortening the cleaning time while maintaining the effect of removing impurities, and considered a cleaning method described below. This cleaning method will be described with reference to FIGS. FIG. 2A shows a case where clear seawater is handled in a seawater desalination plant, and FIG. 2B shows a case where dirty seawater containing a large amount of impurities is handled.

図2(A)において、まず、ろ砂層に残存した原海水を除去する液抜きを行う(液抜き工程)。次に、ろ砂層の出口側から空気を吹き込み、ろ砂層の内部及び入口側表面に付着した不純物を剥離させる(空気洗浄工程)。さらに、洗浄水をろ砂層の出口側から導入し、ろ砂層を洗浄する(水洗浄工程)。洗浄水として、例えば、逆浸透装置等を用いて行われる後工程の分離工程で分離された濃縮海水や砂ろ過装置により不純物が除去されたろ過海水を用いてもよい。水洗浄工程の後で、ろ砂層に残った洗浄水をリンス水(例えば原海水や原海水と同等の水質を有する海水等)と置換すると共に、逆流洗浄で層状態が乱れたろ砂層を整えるリンス処理を行う(リンス工程)。この洗浄方法によれば、空気洗浄工程と水洗浄工程とを併用させたことで、短時間で不純物の除去を可能にしている。   In FIG. 2 (A), first, the liquid is removed to remove the raw seawater remaining in the filter sand layer (liquid draining step). Next, air is blown in from the outlet side of the filter sand layer, and impurities adhering to the inside of the filter sand layer and the inlet side surface are peeled off (air washing step). Furthermore, washing water is introduced from the outlet side of the filter sand layer to wash the filter sand layer (water washing step). As the washing water, for example, concentrated seawater separated in a subsequent separation step performed using a reverse osmosis device or the like, or filtered seawater from which impurities have been removed by a sand filtration device may be used. After the water washing process, the washing water remaining in the filter sand layer is replaced with rinse water (for example, sea water having sea water having the same quality as the raw sea water or the like) and the filter sand layer in which the layer state is disturbed by backwashing is prepared. Processing is performed (rinse process). According to this cleaning method, it is possible to remove impurities in a short time by using both the air cleaning step and the water cleaning step.

しかし、リンス工程は、水洗浄工程で使用していた洗浄水(濃縮海水等)とリンス水とがろ砂層内で混合してしまうため、すべてリンス水と置き換わるまでになお多くの時間を要することがわかった。特に、図2(B)に示すように、不純物を多く含む汚れた海水の場合、清澄な海水より長いリンス時間を必要としている。逆に、リンス工程の時間を短縮すると、置換不足となり、洗浄水が後工程に流出するおそれがある。その場合、後段に設けられている保安用フィルタや逆浸透装置に設けられた逆浸透膜が閉塞する原因となり、膜前後の差圧の上昇や寿命の低下を招く。そのため、洗浄水とリンス水との置換を早期に行い、リンス工程に要する時間を短縮する必要がある。   However, in the rinsing process, the washing water (concentrated seawater, etc.) used in the water washing process and the rinsing water are mixed in the filter sand layer, so it takes a lot of time to completely replace the rinsing water. I understood. In particular, as shown in FIG. 2B, dirty seawater containing a large amount of impurities requires a longer rinsing time than clear seawater. On the other hand, if the time for the rinsing process is shortened, the replacement is insufficient and the washing water may flow out to the subsequent process. In that case, the reverse osmosis membrane provided in the security filter and the reverse osmosis device provided in the subsequent stage may be clogged, resulting in an increase in the differential pressure before and after the membrane and a decrease in the life. For this reason, it is necessary to replace the cleaning water with the rinsing water at an early stage to shorten the time required for the rinsing process.

本発明は、かかる従来技術の課題に鑑み、砂ろ過装置の洗浄作業の中で行うリンス工程に要する時間を短縮することを目的とする。   An object of this invention is to shorten the time which the rinse process performed in the washing | cleaning operation | work of a sand filter apparatus in view of the subject of this prior art.

かかる目的を達成するため、本発明の砂ろ過装置の洗浄方法は、前記逆流洗浄方法を用いた洗浄方法であって、被処理水のろ過処理後、砂ろ過装置に残存した被処理水を排出させる液抜き工程と、液抜き工程の後で、砂ろ過装置のろ過水の出口側から気体を導入し、ろ砂層に捕捉された不純物をろ砂層から剥離させる気体洗浄工程と、ろ砂層に砂ろ過装置のろ過水の出口側から洗浄水を導入し、剥離した不純物を洗浄水と共に砂ろ過装置から排出する不純物排出工程と、不純物排出工程の後で、洗浄水をろ砂層から重力で流下させ、砂ろ過装置から排出する洗浄水排出工程と、リンス水を砂ろ過装置の入口側からろ砂層に導入し、ろ砂層に残った洗浄水をリンス水に置換すると共に、ろ砂層の層状態を整えるリンス工程とからなるものである。   In order to achieve this object, the sand filtration device cleaning method of the present invention is a cleaning method using the backflow cleaning method, and after the water to be treated is filtered, the water to be treated remaining in the sand filtration device is discharged. A liquid draining process, a gas cleaning process for introducing gas from the filtered water outlet side of the sand filtration device after the liquid draining process, and separating impurities trapped in the sand filter layer from the sand filter layer; The washing water is introduced from the outlet side of the filtered water of the filtration device, and the separated impurities are discharged from the sand filtration device together with the washing water. After the impurity discharging step, the washing water is caused to flow down from the filtered sand layer by gravity. The washing water discharge process for discharging from the sand filtration device, the rinse water is introduced into the filter sand layer from the inlet side of the sand filter device, the washing water remaining in the filter sand layer is replaced with the rinse water, and the layer state of the filter sand layer is changed. A rinsing process to prepare

本発明では、不純物排出工程の後で、洗浄水をろ砂層から重力で落下させる洗浄水排出工程をもうけている。この洗浄水排出工程でろ砂層中の洗浄水を排出した後、リンス工程を行うことで、リンス工程において洗浄水とリンス水との混合が起らなくなる。これによって、リンス水への置換を速めることができるため、リンス工程に要する時間を短縮できると共に、砂ろ過装置の稼動を速やかに再開できる。また、洗浄水とリンス水との混合が生じないので、リンス工程に要する時間を短縮しても、置換不足とはならず、砂ろ過装置の稼動再開後においても、洗浄水や剥離した不純物が後工程に流出するおそれはなくなる。従って、後段に配置された機器のフィルタ等の目詰りをなくし、寿命低下を防止できる。   In the present invention, after the impurity discharge step, a wash water discharge step is provided in which the wash water is dropped from the filter sand layer by gravity. After the washing water in the filter sand layer is discharged in the washing water discharging step, the rinsing step is performed, so that the washing water and the rinsing water are not mixed in the rinsing step. Thereby, since the replacement with rinsing water can be accelerated, the time required for the rinsing process can be shortened, and the operation of the sand filter can be resumed promptly. In addition, since mixing of washing water and rinsing water does not occur, even if the time required for the rinsing process is shortened, replacement does not become insufficient, and even after resuming operation of the sand filtration apparatus, washing water and separated impurities are not present. There is no risk of spilling into subsequent processes. Therefore, clogging of a filter or the like of the device arranged in the subsequent stage can be eliminated, and the life reduction can be prevented.

本発明の一態様において、洗浄水排出工程で、ろ砂層から流下する洗浄水が連続的な水流から断続的な水滴に変わった時点を洗浄水の排出が完了した時点とすることができる。
ろ砂層から流下する洗浄水が連続的な水流から断続的な水滴に変わる様子は、砂ろ過装置の外部から容易に目視可能である。そのため、洗浄水の排出完了時点を砂ろ過装置の外部から容易に知ることができ、速やかにリンス工程に移行できる。
In one embodiment of the present invention, the time when the wash water flowing down from the filter sand layer is changed from a continuous water flow to intermittent water droplets in the wash water discharge step can be set as the time when discharge of the wash water is completed.
It can be easily observed from the outside of the sand filtration device that the washing water flowing down from the filter sand layer changes from a continuous water flow to intermittent water droplets. Therefore, it is possible to easily know from the outside of the sand filtration device when the washing water is completely discharged, and it is possible to quickly move to the rinsing process.

本発明の一態様において、複数の砂ろ過装置が被処理水の導入路に対して並列に配置されている場合、1基の砂ろ過装置の洗浄が終了した後、他の砂ろ過装置の洗浄作業を開始するようにするとよい。この場合、1基の砂ろ過装置が洗浄されている間、他の砂ろ過器は稼働可能となる。また、本発明によりリンス時間を短縮できるので、複数の砂ろ過装置がある場合でも、1基の砂ろ過装置毎に十分余裕をもって洗浄工程を行うことができる。従って、砂ろ過装置が組み込まれた海水淡水化プラントなどの設備の稼動時間を十分確保できると共に、再稼働後のろ過水の水質低下を招かない。   In one aspect of the present invention, when a plurality of sand filtration devices are arranged in parallel to the introduction path of the water to be treated, after the washing of one sand filtration device is completed, the other sand filtration devices are washed. It is recommended to start work. In this case, the other sand filter can be operated while one sand filter is being cleaned. Moreover, since the rinsing time can be shortened according to the present invention, even when there are a plurality of sand filtration devices, the washing step can be performed with sufficient margin for each sand filtration device. Accordingly, it is possible to secure a sufficient operation time of facilities such as a seawater desalination plant in which a sand filtration device is incorporated, and the quality of filtered water after restart is not reduced.

本発明によれば、砂ろ過装置の洗浄工程において、洗浄水とリンス水との置換不足を生じることなく、リンス工程に要する時間を短縮できる。従って、後段に設けられた保安用フィルタや逆浸透膜等の閉塞を招かず、かつ砂ろ過装置が複数配置された設備でも、余裕をもって逆洗工程を実施できる。   ADVANTAGE OF THE INVENTION According to this invention, in the washing | cleaning process of a sand filtration apparatus, the time which a rinse process requires can be shortened, without producing replacement short with washing water and rinse water. Therefore, the backwashing process can be carried out with a sufficient margin even in a facility in which a plurality of sand filtration devices are arranged without causing clogging of a safety filter, a reverse osmosis membrane, or the like provided in the subsequent stage.

本発明の第1実施形態に係る砂ろ過装置のブロック線図である。It is a block diagram of the sand filtration apparatus concerning a 1st embodiment of the present invention. (A)及び(B)は本発明者等が考えた中間技術としての洗浄工程の工程図であり、(C)は前記第1実施形態における洗浄工程の工程図である。(A) And (B) is a flowchart of the cleaning process as an intermediate technique considered by the present inventors, and (C) is a flowchart of the cleaning process in the first embodiment. 本発明の第2実施形態に係る砂ろ過装置のブロック線図である。It is a block diagram of the sand filter apparatus which concerns on 2nd Embodiment of this invention. 前記第2実施形態の逆洗工程の手順を示す線図である。It is a diagram which shows the procedure of the backwashing process of the said 2nd Embodiment.

以下、本発明を図に示した実施形態を用いて詳細に説明する。但し、この実施形態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い。   Hereinafter, the present invention will be described in detail with reference to embodiments shown in the drawings. However, the dimensions, materials, shapes, relative arrangements, and the like of the component parts described in this embodiment are not intended to limit the scope of the present invention to that unless otherwise specified.

(実施形態1)
本発明の第1実施形態を図1及び図2(C)に基づいて説明する。図1は、例えば海水淡水化プラントに組み込まれた本実施形態に係る砂ろ過装置を示す。図1において、本実施形態に係る砂ろ過装置10Aは、砂ろ過器12を備えている。砂ろ過器12は、ハウジング14の内部に、横断面全域にろ砂層16が充填されている。ろ砂層16より上方のハウジング壁には、原海水導入路18が接続され、ハウジング14の底壁には、ろ砂層16でろ過されたろ過海水fsを排出するろ過海水排出路22が接続されている。原海水導入路18には、原海水swを砂ろ過器12へ送るポンプ20が介設されている。
(Embodiment 1)
1st Embodiment of this invention is described based on FIG.1 and FIG.2 (C). FIG. 1 shows a sand filtration apparatus according to the present embodiment incorporated in, for example, a seawater desalination plant. In FIG. 1, a sand filter device 10 </ b> A according to this embodiment includes a sand filter 12. The sand filter 12 has a housing 14 filled with a filter sand layer 16 over the entire cross section. A raw seawater introduction path 18 is connected to the housing wall above the filter sand layer 16, and a filtered seawater discharge path 22 for discharging the filtered seawater fs filtered by the filter sand layer 16 is connected to the bottom wall of the housing 14. Yes. The raw seawater introduction path 18 is provided with a pump 20 that sends the raw seawater sw to the sand filter 12.

また、ハウジング14の底壁には、洗浄作業で空気洗浄工程を行う際に、空気aを導入する空気導入路24が設けられている。また、ハウジング14の底壁には、洗浄作業で水洗浄工程を行う際に、後段に設けられた逆浸透装置34から、洗浄水として濃縮海水csを導入する濃縮海水導入路26が接続されている。また、ハウジング14の上方壁には、水洗浄工程で砂ろ過器12に供給された濃縮海水csを排出する濃縮海水排出路28が接続されている。また、ハウジング14の底壁には、リンス工程実施時に、リンス水(原海水sw)を排出するリンス水排出路30が接続されている。   The bottom wall of the housing 14 is provided with an air introduction path 24 through which air a is introduced when an air cleaning process is performed in a cleaning operation. The bottom wall of the housing 14 is connected with a concentrated seawater introduction path 26 for introducing concentrated seawater cs as cleaning water from a reverse osmosis device 34 provided at a later stage when performing a water washing process in a washing operation. Yes. Further, a concentrated seawater discharge path 28 for discharging the concentrated seawater cs supplied to the sand filter 12 in the water washing step is connected to the upper wall of the housing 14. Further, a rinse water discharge passage 30 for discharging rinse water (raw seawater sw) is connected to the bottom wall of the housing 14 when the rinse process is performed.

かかる構成において、海水淡水化プラントの通常運転時に、原海水swが、ポンプ20により原海水導入路18からハウジング14の内部に導入される。ろ砂層16で、原海水swからゴミ類や微生物等の比較的大きな夾雑物が除去される。不純物を除去されたろ過海水fsは、ろ過海水排出路22を経て後段側へ送られる。ろ過海水排出路22の後段側は、保安用フィルタ装置32に接続され、ここで、ろ過海水fsは、念のため残留している不純物が除去される。   In such a configuration, during normal operation of the seawater desalination plant, the raw seawater sw is introduced into the housing 14 from the raw seawater introduction path 18 by the pump 20. The filter sand layer 16 removes relatively large contaminants such as garbage and microorganisms from the raw seawater sw. The filtered seawater fs from which impurities have been removed is sent to the subsequent stage through the filtered seawater discharge path 22. The rear stage side of the filtered seawater discharge path 22 is connected to the security filter device 32, and the impurities remaining in the filtered seawater fs are removed just in case.

保安用フィルタ装置32の後段側で、ろ過海水排出路22は逆浸透装置34に接続されている。逆浸透装置34は逆浸透膜を有し、ろ過海水fsを塩分が除去されたろ過水wと濃縮された塩分を含む濃縮海水csとに分離する。ろ過水wは、ろ過水供給路36から後処理工程に送られ、濃縮海水csは、濃縮海水排出路38に排出される。なお、後述する洗浄作業時の水洗浄工程において、洗浄水として濃縮海水csの一部を濃縮海水導入路26からハウジング14の内部に導入し、ろ砂層16の洗浄を行う。   The filtered seawater discharge path 22 is connected to the reverse osmosis device 34 on the rear side of the security filter device 32. The reverse osmosis device 34 has a reverse osmosis membrane, and separates the filtered seawater fs into filtered water w from which salt is removed and concentrated seawater cs containing concentrated salt. The filtered water w is sent from the filtered water supply path 36 to the post-processing step, and the concentrated seawater cs is discharged to the concentrated seawater discharge path 38. In the water washing step at the time of a washing operation described later, a part of the concentrated seawater cs is introduced as cleaning water into the housing 14 from the concentrated seawater introduction path 26 to wash the filter sand layer 16.

図2(C)は、本実施形態の洗浄工程を示す。洗浄工程では、まず、ろ砂層16に残留している原海水swを排出する(液抜き工程)。排出方法は、残留している原海水swを重力により自然流下させ、ろ砂層16の上面近傍まで液面を下げる。   FIG. 2C shows the cleaning process of this embodiment. In the washing process, first, the raw seawater sw remaining in the filter sand layer 16 is discharged (liquid draining process). In the discharging method, the remaining raw seawater sw is naturally flowed down by gravity, and the liquid level is lowered to the vicinity of the upper surface of the filter sand layer 16.

液抜き工程後、空気導入路24から空気aをハウジング14の下部に吹き込み、空気aをろ砂層16の内部に通す。これによって、ろ砂層16に捕捉されている不純物をろ砂層16から剥離させる(空気洗浄工程)。次に、濃縮海水導入路26から濃縮海水(洗浄水)csをハウジング14の下部に導入し、ろ砂層16に通す。これによって、剥離した不純物を除去し、該不純物を濃縮海水排出路28から排出する(水洗浄工程)。   After the liquid draining step, air a is blown into the lower portion of the housing 14 from the air introduction path 24, and the air a is passed through the filter sand layer 16. Thus, impurities trapped in the filter sand layer 16 are peeled off from the filter sand layer 16 (air washing step). Next, the concentrated seawater (washing water) cs is introduced from the concentrated seawater introduction path 26 into the lower part of the housing 14 and passed through the filter sand layer 16. Thereby, the peeled impurities are removed, and the impurities are discharged from the concentrated seawater discharge passage 28 (water washing step).

次に、濃縮海水csの導入を止め、液排出工程に移行する。液抜き工程では、ろ砂層16に残った濃縮海水csを重力によりろ砂層16から流下させる。ろ砂層16から流下する濃縮海水csが連続的な水流から断続的な水滴に変わった時点をもって、液排出工程の完了時とする。次に、原海水導入路18から原海水(リンス水)swをろ砂層16に導入し、ろ砂層16に残存する濃縮海水csを完全に原海水swと置換すると共に、逆洗工程で乱れたろ砂層16を整える(リンス工程)。これで洗浄作業は終了し、通常運転に戻る。   Next, the introduction of the concentrated seawater cs is stopped, and the process proceeds to the liquid discharge process. In the liquid draining step, the concentrated seawater cs remaining in the filter sand layer 16 is caused to flow down from the filter sand layer 16 by gravity. The time when the concentrated seawater cs flowing down from the filter sand layer 16 changes from a continuous water flow to intermittent water droplets is defined as the completion of the liquid discharge step. Next, the raw seawater (rinse water) sw is introduced into the filter sand layer 16 from the raw seawater introduction channel 18, and the concentrated seawater cs remaining in the filter sand layer 16 is completely replaced with the raw seawater sw and is disturbed in the backwash process. The sand layer 16 is prepared (rinse process). This completes the cleaning operation and returns to normal operation.

本実施形態によれば、水洗浄工程の後で、液排出工程を行い、ろ砂層16に残った濃縮海水csを除去した後で、リンスステップを行うことで、濃縮海水csと原海水swとがろ砂層16で混合されない。これによって、原海水swへ置換できる時間を速めることができ、リンス工程に要する時間を短縮できる。従って、汚れた海水を扱う場合でも、図2(A)に示すリンス時間と同等に短縮でき、プラントの稼動に支障をきたさない。また、リンス時間を短縮しても、置換不足とはならず、濃縮海水や不純物が後段の保安用フィルタ装置32や逆浸透装置34に流出するおそれはない。従って、後段に設けられた保安用フィルタ32や逆浸透装置34等の閉塞を招かず、フィルタ等の寿命低下を防止できる。   According to the present embodiment, after the water washing process, the liquid discharge process is performed, and after the concentrated seawater cs remaining in the filter sand layer 16 is removed, the rinse step is performed, whereby the concentrated seawater cs and the raw seawater sw It is not mixed in the grit sand layer 16. Thereby, the time which can be replaced with the raw seawater sw can be accelerated, and the time required for the rinsing process can be shortened. Therefore, even when dirty seawater is handled, it can be shortened to the same time as the rinse time shown in FIG. 2 (A), and the operation of the plant is not hindered. Further, even if the rinsing time is shortened, the replacement does not become insufficient, and there is no possibility that the concentrated seawater or impurities will flow out to the subsequent safety filter device 32 or the reverse osmosis device 34. Therefore, the safety filter 32 and the reverse osmosis device 34 provided in the subsequent stage are not blocked, and the life of the filter or the like can be prevented from being reduced.

また、液排出ステップで、ろ砂層16から流下する濃縮海水csが連続的な水流から断続的な水滴に変わった時点を濃縮海水csの排出が完了した時点とすることで、濃縮海水csの排出完了時を、砂ろ過器12の外部から明瞭に識別できる。また、濃縮海水csの流下が水流から水滴に変わった時点では、実質的にろ砂層16に濃縮海水csは残っていないため、この時点を完了時点とすることで支障をきたすことはない。そのため、液排出ステップの完了時の把握が容易になり、リンスステップへ速やかに移行できる。   Further, in the liquid discharge step, when the concentrated seawater cs flowing down from the filter sand layer 16 is changed from a continuous water flow to intermittent water droplets, the point in time when the discharge of the concentrated seawater cs is completed, thereby discharging the concentrated seawater cs. The completion time can be clearly identified from the outside of the sand filter 12. Moreover, since the concentrated seawater cs does not substantially remain in the filter sand layer 16 when the flow of the concentrated seawater cs changes from a water flow to a water droplet, setting this time as the completion time does not cause any trouble. Therefore, it is easy to grasp when the liquid discharge step is completed, and the transition to the rinse step can be quickly performed.

(実施形態2)
次に、本発明の第2実施形態を図3及び図4に基づいて説明する。本実施形態の砂ろ過装置10Bは、原海水導入路18に対して多数の砂ろ過器12を並列に配置し、海水淡水化プラントの前処理能力を増大させたものである。図3にその構成を示す。図3において、原海水導入路18に対して多数(3個以上)の砂ろ過器12a、12b、12c・・・・・・が並列に配置されている。各砂ろ過器のろ過海水排出路22には、夫々1個の保安用フィルタ装置32a、32b、32c・・・・・・が設けられている。各砂ろ過器には、前記第1実施形態と同様に、原海水導入路18、ろ過海水排出路22、濃縮海水導入路26及び濃縮海水排出路28が接続されている。
(Embodiment 2)
Next, a second embodiment of the present invention will be described with reference to FIGS. In the sand filtration device 10B of the present embodiment, a large number of sand filters 12 are arranged in parallel to the raw seawater introduction path 18 to increase the pretreatment capacity of the seawater desalination plant. FIG. 3 shows the configuration. 3, a large number (three or more) of sand filters 12a, 12b, 12c,... Each filtered seawater discharge path 22 of each sand filter is provided with one security filter device 32a, 32b, 32c,. Similarly to the first embodiment, each sand filter is connected to a raw seawater introduction path 18, a filtered seawater discharge path 22, a concentrated seawater introduction path 26, and a concentrated seawater discharge path 28.

ろ過海水排出路22の下流端には、2個の逆浸透装置34a及び34bが並列に接続されている。その他の構成は前記第1実施形態と同一である。各砂ろ過器でろ過されたろ過海水fsは、夫々の保安用フィルタ装置で残存している不純物が除去された後、切換弁40a及び40bの開閉により、逆浸透装置34a又は34bのうちどちらかの逆浸透装置に導入される。逆浸透装置でろ過されたろ過水wは、ろ過水供給路36から後段の処理装置(図示省略)に送られる。   Two reverse osmosis devices 34 a and 34 b are connected in parallel to the downstream end of the filtered seawater discharge passage 22. Other configurations are the same as those of the first embodiment. The filtered seawater fs filtered by each sand filter is removed from the reverse osmosis device 34a or 34b by opening and closing the switching valves 40a and 40b after the remaining impurities are removed by the respective security filter devices. Of reverse osmosis equipment. The filtered water w filtered by the reverse osmosis device is sent from the filtered water supply path 36 to a subsequent processing device (not shown).

逆浸透装置34a又は34bで塩分が濃縮された濃縮海水csは、濃縮海水排出路38から排出される。濃縮海水csの一部は、いずれかの砂ろ過器の洗浄作業のとき、洗浄水として濃縮海水導入路26から砂ろ過器に戻される。
図4は、1基の砂ろ過器の洗浄時間が2時間かかる場合を想定している。図2に示すように、本実施形態における各砂ろ過器の洗浄工程は、1基の砂ろ過器が洗浄されている間、他の砂ろ過器を稼働可能とするため、1基の砂ろ過器毎に行う。即ち、2基以上の砂ろ過器を同時に洗浄せず、1基の砂ろ過器の洗浄が終了した後、別な砂ろ過器の洗浄を開始する。
The concentrated seawater cs whose salinity is concentrated by the reverse osmosis device 34 a or 34 b is discharged from the concentrated seawater discharge path 38. A part of the concentrated seawater cs is returned to the sand filter from the concentrated seawater introduction path 26 as cleaning water when any sand filter is cleaned.
FIG. 4 assumes a case where the cleaning time of one sand filter takes 2 hours. As shown in FIG. 2, in the cleaning process of each sand filter in the present embodiment, since one sand filter can be operated while one sand filter is being cleaned, one sand filter is used. Repeat for each vessel. That is, two or more sand filters are not washed at the same time, and after one sand filter has been washed, another sand filter is started to be washed.

本実施形態によれば、前記第1実施形態と同様にリンス時間を短縮できるので、多数の砂ろ過器が設けられたプラントにおいても、1基の砂ろ過器毎に十分余裕をもって洗浄作業を行うことができる。従って、砂ろ過装置が組み込まれたプラントなどの設備の稼動を支障なく継続できると共に、運転再開後に砂ろ過装置内部に存在する被処理水の水質低下を招かない。   According to this embodiment, since the rinsing time can be shortened as in the first embodiment, even in a plant provided with a large number of sand filters, the washing operation is performed with sufficient margin for each sand filter. be able to. Therefore, the operation of facilities such as a plant in which the sand filtration device is incorporated can be continued without hindrance, and the quality of water to be treated existing in the sand filtration device is not lowered after the operation is resumed.

本発明によれば、砂ろ過装置の洗浄作業を短縮できるので、水質が悪く、不純物を多く含む汚れた海水を処理する場合でも、処理設備の稼動に支障をきたさない。   According to the present invention, since the cleaning operation of the sand filtration device can be shortened, the water quality is poor, and even when dirty seawater containing a large amount of impurities is processed, the operation of the processing equipment is not hindered.

10A、10B 砂ろ過装置
12、12a、12b、12c 砂ろ過器
14 ハウジング
16 ろ砂層
18 原海水導入路
20 ポンプ
22 ろ過海水排出路
24 空気導入路
26 濃縮海水導入路
28、38 濃縮海水排出路
30 リンス水排出路
32、32a、32b、32c 保安用フィルタ装置
34,34a、34b 逆浸透装置
36 ろ過水供給路
40a、40b 切換弁
a 空気(気体)
cs 濃縮海水(洗浄水)
fs ろ過海水
sw 原海水(被処理水、リンス水)
w ろ過水
10A, 10B Sand filtration device 12, 12a, 12b, 12c Sand filter 14 Housing 16 Filter sand layer 18 Raw seawater introduction path 20 Pump 22 Filtration seawater discharge path 24 Air introduction path 26 Concentrated seawater introduction path 28, 38 Concentrated seawater discharge path 30 Rinse water discharge passage 32, 32a, 32b, 32c Safety filter device 34, 34a, 34b Reverse osmosis device 36 Filtrated water supply passage 40a, 40b Switching valve a Air (gas)
cs Concentrated seawater (wash water)
fs filtered seawater sw raw seawater (treated water, rinse water)
w Filtration water

Claims (3)

ハウジング内に設けられたろ砂層を有し、前記ろ砂層を通過することにより被処理水をろ過処理し、ろ過水を生成する砂ろ過装置に、前記砂ろ過装置の前記ろ過水の出口側から洗浄水を導入し前記ろ砂層に捕捉された不純物を逆流洗浄により除去する砂ろ過装置の洗浄方法において、
前記被処理水のろ過処理後、前記砂ろ過装置に残存した前記被処理水を排出させる液抜き工程と、
前記液抜き工程の後で、前記砂ろ過装置の前記ろ過水の出口側から気体を導入し、前記ろ砂層に捕捉された不純物を前記ろ砂層から剥離させる気体洗浄工程と、
前記ろ砂層に前記砂ろ過装置の前記ろ過水の出口側から洗浄水を導入し、剥離した不純物を前記洗浄水(cs)と共に前記砂ろ過装置から排出する不純物排出工程と、
前記不純物排出工程の後で、前記洗浄水を前記ろ砂層から重力で流下させ、前記砂ろ過装置から排出する洗浄水排出工程と、
リンス水(sw)を前記砂ろ過装置の入口側から前記ろ砂層に導入し、前記ろ砂層に残存した前記洗浄水を前記リンス水に置換すると共に、前記ろ砂層の層状態を整えるリンス工程とからなることを特徴とする砂ろ過装置の洗浄方法。
Washing from the outlet side of the filtered water of the sand filtration device to the sand filtration device that has a filtered sand layer provided in the housing, filters the treated water by passing through the filtered sand layer, and generates filtered water In the washing method of the sand filtration device for introducing impurities and removing the impurities trapped in the filter sand layer by backwashing,
A liquid draining step for discharging the treated water remaining in the sand filtration device after the treated water is filtered;
After the liquid draining step, a gas washing step of introducing a gas from the filtered water outlet side of the sand filtration device and separating impurities trapped in the filter sand layer from the filter sand layer;
Impurity discharging step of introducing cleaning water into the filtered sand layer from the filtered water outlet side of the sand filtering device, and discharging the separated impurities from the sand filtering device together with the cleaning water (cs),
After the impurity discharging step, the washing water is caused to flow down from the filter sand layer by gravity, and the washing water discharging step is discharged from the sand filtration device,
A rinsing step of introducing rinsing water (sw) into the filter sand layer from the inlet side of the sand filtration device, replacing the washing water remaining in the filter sand layer with the rinse water, and adjusting a layer state of the filter sand layer; A method for cleaning a sand filtration device, comprising:
前記洗浄水排出工程において、
前記ろ砂層から流下する前記洗浄水が連続的な水流から断続的な水滴に変わった時点を前記洗浄水の排出が完了した時点とすることを特徴とする請求項1に記載の砂ろ過装置の洗浄方法。
In the washing water discharge step,
2. The sand filtration device according to claim 1, wherein the time when the wash water flowing down from the filter sand layer is changed from a continuous water flow to intermittent water droplets is a time point when discharge of the wash water is completed. 3. Cleaning method.
複数の前記砂ろ過装置が前記被処理水の導入路に対して並列に配置され、
1基の前記砂ろ過装置の洗浄工程が終了した後、他の砂ろ過装置の洗浄工程を開始することを特徴とする請求項1又は2に記載の砂ろ過装置の洗浄方法。
A plurality of the sand filtration devices are arranged in parallel to the introduction path of the treated water,
The method for cleaning a sand filter according to claim 1 or 2, wherein a cleaning process for another sand filter is started after the cleaning process for one sand filter is completed.
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WO2016056130A1 (en) * 2014-10-10 2016-04-14 三菱重工業株式会社 Raw water filtration treatment system, and method for cleaning filtration device
WO2017141400A1 (en) * 2016-02-18 2017-08-24 三菱重工業株式会社 Water treatment device and backwash method

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JPS54108066A (en) * 1978-02-13 1979-08-24 Hitachi Zosen Corp Washing method of upward flow sande filter device
JPH08920A (en) * 1994-06-23 1996-01-09 Mitsubishi Heavy Ind Ltd Multistage filter
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Publication number Priority date Publication date Assignee Title
WO2016056130A1 (en) * 2014-10-10 2016-04-14 三菱重工業株式会社 Raw water filtration treatment system, and method for cleaning filtration device
WO2017141400A1 (en) * 2016-02-18 2017-08-24 三菱重工業株式会社 Water treatment device and backwash method

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