JP6380025B2 - Long fiber filtration device - Google Patents

Long fiber filtration device Download PDF

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JP6380025B2
JP6380025B2 JP2014227856A JP2014227856A JP6380025B2 JP 6380025 B2 JP6380025 B2 JP 6380025B2 JP 2014227856 A JP2014227856 A JP 2014227856A JP 2014227856 A JP2014227856 A JP 2014227856A JP 6380025 B2 JP6380025 B2 JP 6380025B2
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strands
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JP2016087580A (en
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富士夫 小出
富士夫 小出
順 橋口
順 橋口
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Mitsubishi Chemical Aqua Solutions Co Ltd
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Description

本発明は長繊維濾過装置に関する。   The present invention relates to a long fiber filtration device.

長繊維濾過装置は、基本的には、塔の内部には芯紐の周側に濁質捕捉材を形成して成る複数の濾材が装填され、複数の濾材は原水通水時には塔の下流側に押圧されて濁質捕捉材の一部が圧密状態を形成し且つ洗浄水供給時には前記の圧密状態を解除して粗状態を形成し得る様に流水方向に沿って屈曲変形可能な懸垂状態で吊り下げられた構造を有し、原水中の濁質の除去に有効であり、濁質除去装置と呼ばれることもある(特許文献1)。濁質捕捉材には、例えば、特開2002−061041号公報(特許文献2)に記載の各種形状のモールコードを使用することが出来、モールコードの芯紐への固定は接着剤によって行うことが出来る。   In the long fiber filtration device, basically, a plurality of filter media formed by forming a turbidity trapping material on the circumferential side of the core string is loaded inside the tower, and the plurality of filter media are downstream of the tower when raw water is passed through. In a suspended state that can be bent and deformed along the direction of water flow so that a part of the turbidity trapping material forms a consolidated state and is released from the consolidated state when a wash water is supplied to form a rough state. It has a suspended structure, is effective for removing turbidity in raw water, and is sometimes called a turbidity removal device (Patent Document 1). For example, various shapes of molding cords described in JP-A-2002-061041 (Patent Document 2) can be used as the turbidity trapping material, and the molding cord is fixed to the core cord with an adhesive. I can do it.

ところで、長期間の運転においては、前記の圧密状態と粗状態とは繰り返し行われるため、芯紐への固定に使用した接着剤の水中での応力劣化が助長され、長期の運転中にモールコードの芯紐とモールコードとの固定状態に部分的な剥離が生じ、モールコードが濁質捕捉材として機能しなくなるという欠点がある。   By the way, in the long-term operation, since the above-described compaction state and the rough state are repeatedly performed, the deterioration of stress in water of the adhesive used for fixing to the core string is promoted. There is a drawback that partial peeling occurs in the fixed state of the core string and the molding cord, and the molding cord does not function as a turbidity trapping material.

特許第4649799号公報Japanese Patent No. 4649799 特開2002−061041号公報Japanese Patent Laid-Open No. 2002-061041

本発明は、上記実情に鑑みなされたものであり、その目的は、長期間に亘って安定した濁質除去機能を発揮し得る様に改良された長繊維濾過装置を提供することにある。   This invention is made | formed in view of the said situation, The objective is to provide the long fiber filtration apparatus improved so that the stable turbidity removal function could be exhibited over a long period of time.

すなわち、本発明の要旨は、下向流形式で原水が通水され且つ上向流形式で洗浄水が供給される長繊維濾過装置であって、塔(1)頂部には原水通水配管と洗浄排水排出配管とが設けられ、塔(1)底部には処理水排出配管と洗浄水供給配管とが設けられ、塔(1)内部には芯紐(41)の周側に濁質捕捉材を形成して成る複数の濾材(4)が装填され、複数の濾材(4)は原水通水時には塔(1)の下流側に押圧されて濁質捕捉材の一部が圧密状態を形成し且つ洗浄水供給時には前記の圧密状態を解除して粗状態を形成し得る様に流水方向に沿って屈曲変形可能な懸垂状態で吊り下げられ、前記の濁質捕捉材は、芯紐(41)の周側に形成された編組状モールコード(42)から成り、編組状モールコード(42)は、組紐を構成する素線(紐状体)のうち右回り、左回りのどちらか1方向の素線でループ(42a)を形成し、この素線及び他方向の素線で芯部の組紐体(42b)を形成した構造を有し、編組状モールコード(42)の組紐体(42b)は、50〜600mm間隔毎に2〜20mmの幅の縫付加工(42c)によって芯紐(41)に固定されていることを特徴とする長繊維濾過装置に存する。   That is, the gist of the present invention is a long fiber filtration device in which raw water is passed in a downward flow format and cleaning water is supplied in an upward flow format, and a raw water flow piping is provided at the top of the tower (1). A cleaning drain discharge pipe is provided, a treated water discharge pipe and a cleaning water supply pipe are provided at the bottom of the tower (1), and a turbidity trapping material is provided around the core string (41) inside the tower (1). A plurality of filter media (4) are formed, and the plurality of filter media (4) are pressed downstream of the tower (1) when the raw water is passed, and a part of the turbid trapping material forms a consolidated state. In addition, when supplying the washing water, the suspended state is suspended in a suspended state that can be bent and deformed along the flowing water direction so that a rough state can be formed by releasing the compacted state. The braided molding cord (42) is formed on the circumferential side of the braided cord, and the braided molding cord (42) is a strand constituting the braid. The loop (42a) is formed by strands in one of the clockwise and counterclockwise directions, and the braided body (42b) of the core is formed by the strands and strands in the other direction. The braided body cord (42b) of the braided molding cord (42) is fixed to the core cord (41) by sewing processing (42c) having a width of 2 to 20 mm every interval of 50 to 600 mm. In the featured long fiber filtration device.

本発明に係る長繊維濾過装置によれば、芯紐と濁質捕捉材であるモールコードとの固定状態の劣化が起こり難く、長期間に亘って安定した濁質除去機能を発揮することが出来る。   According to the long fiber filtration device according to the present invention, the fixed state of the core cord and the mould cord as the turbidity trapping material is hardly deteriorated, and a stable turbidity removal function can be exhibited over a long period of time. .

本発明で好適に使用し得る長繊維濾過装置の一例の模式的説明図Schematic explanatory diagram of an example of a long fiber filtration device that can be suitably used in the present invention 本発明で好適に使用し得る濾材の一例の模式的説明図Schematic explanatory diagram of an example of a filter medium that can be suitably used in the present invention 本発明で好適に使用し得る濾材の一例の外観の図面代用写真Drawing substitute photograph of the appearance of an example of a filter medium that can be suitably used in the present invention

以下、本発明を詳細に説明する。   Hereinafter, the present invention will be described in detail.

先ず、図1に示す長繊維濾過装置について説明する。分図(a)は原水処理運転の説明図であり、分図(b)は洗浄運転の説明図である。この長繊維濾過装置は、基本的には、前述の先行技術(特許第4649799号公報)に記載の濁質除去装置と同一である。   First, the long fiber filtration apparatus shown in FIG. 1 will be described. The partial diagram (a) is an explanatory diagram of the raw water treatment operation, and the partial diagram (b) is an explanatory diagram of the cleaning operation. This long fiber filtration device is basically the same as the turbidity removal device described in the above-mentioned prior art (Japanese Patent No. 4649799).

本発明で使用する長繊維濾過装置は、下向流形式で原水が通水され且つ上向流形式で洗浄水が供給される長繊維濾過装置である。従って、塔(1)の頂部にはバルブ付であって且つ原水タンクに連結された原水通水配管とバルブ付の洗浄排水排出配管とが設けられ、塔(1)の底部にはバルブ付の処理水排出配管と洗浄水供給配管と空気供給配管とが設けられている。図1に示す装置においては、原水処理運転および洗浄運転で使用される配管は共通しており、バルブ操作によって水の流れ方向が変更される。   The long fiber filtration device used in the present invention is a long fiber filtration device in which raw water is passed in a downward flow format and cleaning water is supplied in an upward flow format. Therefore, the top of the tower (1) is provided with a valve and a raw water passage pipe connected to the raw water tank and a washing drain discharge pipe with a valve, and the bottom of the tower (1) is provided with a valve. A treated water discharge pipe, a cleaning water supply pipe, and an air supply pipe are provided. In the apparatus shown in FIG. 1, the pipes used in the raw water treatment operation and the washing operation are common, and the water flow direction is changed by the valve operation.

すなわち、原水処理運転の場合、バルブ(61)及び(62)のみが開状態とされ、濁質を含む原水は、バルブ(61)から配管(51)を経由して塔(1)内に通水される。この際、濾材(4)は後述する様に圧密状態を呈し、原水に同伴された濁質は濾材(4)によって捕捉される。濁質を含まない処理水は、配管(52)を経由してバルブ(62)から排出される。   That is, in the raw water treatment operation, only the valves (61) and (62) are opened, and the raw water containing turbidity is passed from the valve (61) through the pipe (51) into the tower (1). Watered. At this time, the filter medium (4) exhibits a compacted state as will be described later, and the suspended matter entrained in the raw water is captured by the filter medium (4). The treated water containing no turbidity is discharged from the valve (62) via the pipe (52).

一方、洗浄運転の場合、原水処理運転時に開状態であったバルブ(61)及び(62)が閉止され、洗浄水は、バルブ(64)から配管(52)を経由して塔(1)内に供給される。一方、空気は、バルブ(63)から配管(53)を経由して塔(1)内に供給される。濾材(4)は後述する様に圧密状態を解除し、濾材(4)から濁質が除去される。空気のバブリング作用により、濾材(4)が振動させられ、濾材(4)に付着した濁質の剥離が促進される。濁質を含む洗浄水は、配管(51)を経由してバルブ(65)から排出される。   On the other hand, in the case of the washing operation, the valves (61) and (62) that were open during the raw water treatment operation are closed, and the washing water passes through the pipe (52) from the valve (64) into the tower (1). To be supplied. On the other hand, air is supplied into the tower (1) from the valve (63) via the pipe (53). As will be described later, the filter medium (4) is released from the compacted state, and turbidity is removed from the filter medium (4). The bubbling action of the air causes the filter medium (4) to vibrate, and the separation of turbidity adhering to the filter medium (4) is promoted. Wash water containing turbidity is discharged from the valve (65) via the pipe (51).

塔内部には上部支持体(2)と下部支持体(3)とが配置され、上部支持体(2)と下部支持体(3)との間には複数の濾材(4)が当該濾材の端部の上部吊り紐(7)と下部吊り紐(8)とによって懸垂状態で固定されている。   An upper support (2) and a lower support (3) are arranged inside the tower, and a plurality of filter media (4) are placed between the upper support (2) and the lower support (3). The upper suspension string (7) and the lower suspension string (8) at the end are fixed in a suspended state.

上部支持体(2)及び下部支持体(3)の構造は、水の流れを妨げず且つ吊り紐(7)及び(8)によって濾材(4)を固定し得る構造である限り、特に制限されず、例えば、格子構造、目皿構造、編目構造などを適宜採用し得る。   The structure of the upper support (2) and the lower support (3) is not particularly limited as long as the structure does not hinder the flow of water and the filter medium (4) can be fixed by the hanging strings (7) and (8). For example, a lattice structure, an eye plate structure, a stitch structure, or the like can be appropriately employed.

濾材(4)は、後述するように芯紐の周側に特定構造の濁質捕捉材を形成して成る。濾材(4)、芯紐、上部吊り紐(7)及び下部吊り紐(8)は、流水方向に沿って屈曲変形可能に構成される。斯かる構成は、素材の種類、形態、太さ等の選択によって達成される。上記の各要素は、通常、ポリエステル、ナイロン、ポリ塩化ビニリデン等の合成樹脂素材にて構成される。なお、濾材(4)の芯紐(41)が長く濁質捕捉材の両端(具体的には後述の組紐体(42b)の両端)から突出している場合は、両端突出部の芯紐を上部吊り紐(7)及び下部吊り紐(8)として使用することが出来る。   The filter medium (4) is formed by forming a turbidity trapping material having a specific structure on the peripheral side of the core string as will be described later. The filter medium (4), the core string, the upper suspension string (7), and the lower suspension string (8) are configured to be bent and deformed along the flowing water direction. Such a configuration is achieved by selecting the type, form, thickness, etc. of the material. Each of the above elements is usually made of a synthetic resin material such as polyester, nylon, or polyvinylidene chloride. In addition, when the core string (41) of the filter medium (4) is long and protrudes from both ends of the turbidity trapping material (specifically, both ends of the braided body (42b) described later), It can be used as a hanging string (7) and a lower hanging string (8).

長繊維濾過装置において、複数の濾材(4)はその芯紐の両端を塔(1)内で固定されることにより原水通水時には塔(1)の下流側に押圧されて濁質捕捉材の一部が圧密状態を形成し且つ洗浄水供給時には前記の圧密状態を解除して粗状態を形成し得る様に流水方向に沿って屈曲変形可能な懸垂状態で吊り下げられる必要がある。斯かる状態は、上部支持体(2)と下部支持体(3)との間の距離(LA)、濾材(4)の長さ(LB)、上部吊り紐(7)の長さ(Lb1)、下部吊り紐(8)の長さ(Lb2)が以下に規定する式(1)〜(3)を満足することによって達成することが出来る。   In the long fiber filtration device, the plurality of filter media (4) are pressed at the downstream side of the tower (1) when the raw water is passed by fixing both ends of the core string in the tower (1) and It is necessary to suspend in a suspended state that can be bent and deformed along the direction of flowing water so that a part can form a consolidated state and when the washing water is supplied, the consolidated state can be canceled to form a rough state. Such a state includes the distance (LA) between the upper support (2) and the lower support (3), the length (LB) of the filter medium (4), and the length (Lb1) of the upper suspension string (7). This can be achieved when the length (Lb2) of the lower suspension string (8) satisfies the following expressions (1) to (3).

[数1]
LA<(Lb1+LB+Lb2) 式(1)
LB<LA 式(2)
(LB+Lb2)<LA<(LB+Lb1) 式(3)
[Equation 1]
LA <(Lb1 + LB + Lb2) Formula (1)
LB <LA Formula (2)
(LB + Lb2) <LA <(LB + Lb1) Formula (3)

すなわち、長繊維濾過装置において、式(1)に示す様に、濾材(4)と上部支持体(2)と下部支持体(3)の合計長さ(Lb1+LB+Lb2)は、上部支持体(2)と下部支持体(3)との間の距離(LA)より長い。従って、上記の各要素の何れかは塔(1)内に弛んだ状態で存在する。   That is, in the long fiber filtration apparatus, as shown in the formula (1), the total length (Lb1 + LB + Lb2) of the filter medium (4), the upper support (2) and the lower support (3) is the upper support (2). Longer than the distance (LA) between the lower support (3) and the lower support (3). Accordingly, any of the above elements exists in a relaxed state in the tower (1).

また、式(2)に示す様に、上部支持体(2)と下部支持体(3)との間の距離(LA)は、濾材(4)の長さ(LB)より長い。従って、上部支持体(2)と下部支持体(3)との間には流水方向に沿って濾材(4)が存在しない領域が形成されている。換言すれば、流水方向に沿って濾材(4)の可動範囲が形成されている。なお、図1の模式的説明図では濾材(4)同士の間に隙間が存在しているが、実際は濾材(4)同士の間に隙間はなく、複数の濾材(4)は圧密状態となる様に懸垂され、従って、複数の濾材(4)の全体は、流水方向(上下方向)に沿ってのみ移動する。   Moreover, as shown in Formula (2), the distance (LA) between the upper support (2) and the lower support (3) is longer than the length (LB) of the filter medium (4). Therefore, a region where the filter medium (4) does not exist is formed along the flowing water direction between the upper support (2) and the lower support (3). In other words, the movable range of the filter medium (4) is formed along the flowing water direction. In addition, although the clearance gap exists between filter media (4) in the schematic explanatory drawing of FIG. 1, there is actually no clearance gap between filter media (4), and several filter media (4) will be in a consolidated state. Therefore, the whole of the plurality of filter media (4) moves only along the flowing water direction (vertical direction).

更に、式(3)に示す様に、濾材(4)と上部吊り紐(7)との合計長さ(LB+Lb1)は、濾材(4)と下部吊り紐(8)との合計長さ(LB+Lb2)より長い。従って、下向流形式で原水が通水される原水処理運転時においては、図1(a)に示す様に、濾材(4)は下部支持体(3)に当接して下部吊り紐(8)と共に塔底部近傍で圧密され、上向流形式で洗浄水が供給される洗浄運転時においては図1(b)に示す様に、濾材(4)は上部支持体(2)に当接せずに下部吊り紐(8)と共に塔内の上方に伸長した状態となる。   Furthermore, as shown in Formula (3), the total length (LB + Lb1) of the filter medium (4) and the upper suspension string (7) is the total length (LB + Lb2) of the filter medium (4) and the lower suspension string (8). ) Longer. Therefore, at the time of raw water treatment operation in which raw water is passed in the downward flow format, as shown in FIG. 1 (a), the filter medium (4) comes into contact with the lower support (3) and lower suspension string (8 ) And in the vicinity of the bottom of the tower, and in the cleaning operation in which cleaning water is supplied in an upward flow manner, the filter medium (4) is brought into contact with the upper support (2) as shown in FIG. 1 (b). Without being extended with the lower suspension string (8) in the tower.

以上の結果、長繊維濾過装置においては、原水処理運転時における濾材の圧密状態と洗浄運転時における濾材の圧密状態の解除とにより、濾材による濁質の捕捉と排出とが効率的に行われる。   As a result, in the long fiber filtration device, trapping and discharging of turbidity by the filter medium are efficiently performed by releasing the compacted state of the filter medium during the raw water treatment operation and releasing the compacted state of the filter medium during the washing operation.

本発明で使用する長繊維濾過装置において、前記の各要素は、以下に規定する式(1’)〜(3’)を満足するのが好ましい。式(1’)〜(3’)中の各要素の大小関係の数値は、装置の経済性を考慮して決定された値である。   In the long fiber filtration device used in the present invention, each of the above elements preferably satisfies the following formulas (1 ') to (3'). The numerical value of the magnitude relationship of each element in the formulas (1 ') to (3') is a value determined in consideration of the economics of the apparatus.

[数2]
1.01×LA<(Lb1+LB+Lb2)<2.00×LA 式(1’)
1.01×LB<LA<1.50×LB 式(2’)
1.01×(LB+Lb2)<LA<1.01×(LB+Lb1) 式(3’)
[Equation 2]
1.01 × LA <(Lb1 + LB + Lb2) <2.00 × LA Formula (1 ′)
1.01 × LB <LA <1.50 × LB Formula (2 ′)
1.01 * (LB + Lb2) <LA <1.01 * (LB + Lb1) Formula (3 ')

長繊維濾過装置の前記した各要素の寸法は次の通りである。すなわち、上部支持体(2)と下部支持体(3)との間の距離(LA)は100〜400cm、濾材(4)の長さ(LB)は70〜300cm、上部吊り紐(7)の長さ(Lb1)は10〜250cm、下部吊り紐(8)の長さ(Lb2)は5〜20cm、塔(1)の直径は20〜360cmである。   The dimensions of the above-mentioned elements of the long fiber filtration device are as follows. That is, the distance (LA) between the upper support (2) and the lower support (3) is 100 to 400 cm, the length (LB) of the filter medium (4) is 70 to 300 cm, and the upper suspension string (7) The length (Lb1) is 10 to 250 cm, the length (Lb2) of the lower suspension string (8) is 5 to 20 cm, and the diameter of the tower (1) is 20 to 360 cm.

次に、図2に示す濾材(4)について説明する。濾材(4)は芯紐(41)の周側に濁質捕捉材である編組状モールコード(42)を形成して成る。洗浄水供給時の圧密状態を解除した状態における編組状モールコード(42)の長さは、特に制限されないが、通常1〜5m以上である。斯かる長さは、塔(1)内部に装填前の濾材(4)について、編組状モールコード(42)の長さ、実際には後述する組紐体(42b)の長さを測定することによって確認することが出来る。   Next, the filter medium (4) shown in FIG. 2 will be described. The filter medium (4) is formed by forming a braided molding cord (42) as a turbidity trapping material on the peripheral side of the core string (41). The length of the braided molding cord (42) in a state in which the compacted state at the time of supplying cleaning water is released is not particularly limited, but is usually 1 to 5 m or more. Such a length is obtained by measuring the length of the braided molding cord (42), in fact, the length of the braided body (42b), which will be described later, for the filter medium (4) before being loaded inside the tower (1). It can be confirmed.

ところで、モールコードの芯紐への固定を接着剤によって行う従来の長繊維濾過装置が大型化された場合、前述の圧密状態と粗状態とが長い距離で行われるため、接着剤の水中での応力劣化が一層助長され、長期の運転中にモールコードの芯紐とモールコードとの固定状態に部分的な剥離が生じ易くなる。これに対し、本発明の長繊維濾過装置は、モールコードの芯紐への固定に接着剤を使用していないため、上記のような問題は全くない。従って、本発明の長繊維濾過装置は、編組状モールコード(42)の前記の長さが1m以上、好ましくは1.5m以上の大型装置の場合に特に有効であると言える。   By the way, when the conventional long fiber filtration device that fixes the molding cord to the core string with an adhesive is enlarged, the above-mentioned compaction state and the rough state are performed at a long distance, so the adhesive in water Stress deterioration is further promoted, and partial peeling easily occurs in the fixed state between the core cord of the molding cord and the molding cord during long-term operation. On the other hand, since the long fiber filtration device of the present invention does not use an adhesive for fixing the molding cord to the core string, there is no problem as described above. Therefore, it can be said that the long fiber filtration device of the present invention is particularly effective in the case of a large-sized device in which the length of the braided molding cord (42) is 1 m or more, preferably 1.5 m or more.

編組状モールコード(42)は、基本的には、前述の先行技術(特開2002−061041号公報)に数多く記載されたモールコードの1つであり、この先行技術においては、実公昭63−50298号公報に記載の螺旋条の編組状モールコードとして紹介されている。そして、編組法を採用して製造するものであるため、生産性の点でおのずから限界があると指摘されている。   The braided molding cord (42) is basically one of the molding cords described in the above-mentioned prior art (Japanese Patent Laid-Open No. 2002-061041). It is introduced as a spiral-shaped braided molding cord described in Japanese Patent No. 50298. And it is pointed out that there is a limit in terms of productivity because it is manufactured by adopting a braiding method.

しかしながら、長繊維濾過においては、基本的な構造として実公昭63−50298号公報に記載の螺旋条の編組状モールコードが好適である。すなわち、本発明で使用する編組状モールコード(42)は、上記の編組状モールコードと同様に構成され、組紐を構成する素線(紐状体)のうち右回り、左回りのどちらか1方向の素線でループ(42a)を形成し、この素線及び他方向の素線で芯部の組紐体(42b)を形成した構造を有する。   However, in the case of long fiber filtration, a spiral strip braided molding cord described in Japanese Utility Model Publication No. 63-50298 is suitable as a basic structure. That is, the braided molding cord (42) used in the present invention is configured in the same manner as the above braided molding cord, and either one of the clockwise and the counterclockwise rotations of the strands (strings) constituting the braid. A loop (42a) is formed by the strands in the direction, and a braided body (42b) of the core portion is formed by the strands in this direction and the strands in the other direction.

但し、実公昭63−50298号公報に記載の螺旋条の編組状モールコードは、「ループを形成する方向の素線には、天然繊維、化学繊維などの伸度の比較的小さい繊維素材を使用し、他方向の素線のうち少なくとも1本以上を弾性伸縮する天然ゴム、合成ゴム、弾性化学繊維、等の素材で構成し、その弾性回復力によって螺旋状の編組状モールコード形成する」こととしているが、本発明ではループを形成する方向の素線と他方向の素線の材質とが異なる必要はない。むしろ、弾性回復力を利用した螺旋状の形成は本発明における濁質捕捉材としての使用には不利となる。   However, the spiral braided molding cord described in Japanese Utility Model Publication No. 63-50298 is “Uses a fiber material with relatively low elongation, such as natural fiber and chemical fiber, for the strand in the direction of forming the loop. And at least one of the strands in the other direction is made of a material such as natural rubber, synthetic rubber, elastic chemical fiber, etc. that elastically expands and contracts, and a spiral braided molding cord is formed by its elastic recovery force. However, in the present invention, the material of the strands in the direction in which the loop is formed does not have to be different from the material of the strands in the other direction. Rather, the helical formation utilizing the elastic recovery force is disadvantageous for use as a turbidity trapping material in the present invention.

図2においては、ループ(42a)の理解のため、芯部の組紐体(42b)や後述の縫付加工(42c)の説明のため、素線は、便宜的に、1本のモノフィラメント糸によって表現されているが、実際の編組状モールコードは、図3に示すような外観を有する。斯かる編組状モールコードは、素線としてマルチフィラメント糸を使用して制作することが出来る。糸径は、極細のものから極太のものまで任意に選択することが出来る。また、捲縮加工されたものであってもよい。   In FIG. 2, for the sake of understanding the loop (42 a), and for explaining the braided body (42 b) of the core part and the sewing process (42 c) to be described later, the strand is made up of one monofilament thread for convenience. Although represented, the actual braided molding cord has an appearance as shown in FIG. Such a braided molding cord can be produced using multifilament yarn as a strand. The yarn diameter can be arbitrarily selected from a very thin one to a very thick one. Further, it may be crimped.

本発明の最大の特徴は、編組状モールコード(42)の組紐体(42b)が50〜600mm間隔毎に2〜20mmの幅の縫付加工(42c)によって芯紐(41)に固定されている点に存する。   The greatest feature of the present invention is that the braided cord body (42b) of the braided molding cord (42) is fixed to the core cord (41) by sewing processing (42c) having a width of 2 to 20 mm every 50 to 600 mm. There is in point.

縫付加工(42c)は、図示を省略しているが、通常、組紐体(42b)の両端部から行われる。縫付加工(42c)の間隔が前記の範囲未満の場合は、縫付加工(42c)の形成が密に過ぎて組紐体(42b)の屈曲変形性(柔軟性)が損なわれ、前記の範囲を超える場合は、芯紐(41)への組紐体(42b)の固定が十分とは言えない。一方、縫付加工(42c)の幅が前記の範囲未満の場合は、芯紐(41)への組紐体(42b)の固定が十分とは言えず、前記の範囲を超える場合は、組紐体(42b)の屈曲変形性(柔軟性)が損なわれる。何れの場合にも編組状モールコード(42)の濁質捕捉材としての機能が低下する。縫付加工(42c)は通常ミシン掛けにより行われるが、ミシン掛けは芯紐(41)と直角方向に行われる。縫付加工(42c)に使用する糸は前述の合成樹脂素材にて構成される。   Although the illustration of the sewing process (42c) is omitted, it is usually performed from both ends of the braided body (42b). When the interval of the sewing process (42c) is less than the above range, the formation of the sewing process (42c) is too dense, and the bending deformability (flexibility) of the braided body (42b) is impaired. When exceeding, it cannot be said that fixation of the braided body (42b) to the core string (41) is sufficient. On the other hand, when the width of the sewing process (42c) is less than the above range, it cannot be said that the braid body (42b) is sufficiently fixed to the core string (41), and when the width exceeds the above range, the braid body The bending deformability (flexibility) of (42b) is impaired. In either case, the function of the braided molding cord (42) as a turbidity trapping material is reduced. The sewing process (42c) is usually performed by sewing, but the sewing is performed in a direction perpendicular to the core string (41). The thread used for the sewing process (42c) is made of the aforementioned synthetic resin material.

次に、図1に示す長繊維濾過装置の運転方法について説明する。本長繊維濾過装置の運転方法は、原水処理運転と洗浄運転とを繰り返し行なうことから成る。   Next, an operation method of the long fiber filtration device shown in FIG. 1 will be described. The operation method of this long fiber filtration apparatus consists of repeatedly performing a raw water treatment operation and a washing operation.

原水処理運転(図1(a))においては、前述の様に、バルブ(61)及び(62)のみが開状態とされ、濁質を含む原水は、バルブ(61)から配管(51)を経由して塔(1)内に通水される。原水に同伴された濁質は濾材(4)によって捕捉される。濁質を含まない処理水は、配管(52)を経由してバルブ(62)から排出される。   In the raw water treatment operation (FIG. 1 (a)), as described above, only the valves (61) and (62) are opened, and raw water containing turbidity passes through the pipe (51) from the valve (61). The water is passed through the tower (1). The suspended matter entrained in the raw water is captured by the filter medium (4). The treated water containing no turbidity is discharged from the valve (62) via the pipe (52).

そして、原水処理運転において、例えば、原水通水ポンプ(図示せず)の圧力測定、処理水の水質分析などの手段により、長繊維濾過装置の性能が低下した時点で原水処理運転を停止する。原水処理運転の停止は一定時間経過毎に自動的行なってもよい。   In the raw water treatment operation, for example, the raw water treatment operation is stopped when the performance of the long fiber filtration device is reduced by means such as pressure measurement of a raw water flow pump (not shown) and water quality analysis of the treated water. The stop of the raw water treatment operation may be automatically performed every certain time.

洗浄運転(図1(b))においては、前述の様に、原水処理運転時に開状態であったバルブ(61)及び(62)が閉止され、洗浄水は、バルブ(64)から配管(52)を経由して塔(1)内に供給される。一方、空気は、バルブ(63)から配管(53)を経由して塔(1)内に供給される。空気の供給は、洗浄水の供給と同時に始めてもよく、また、洗浄水の供給よりも遅れて始めてもよい。濁質を含む洗浄水は、配管(51)を経由してバルブ(65)から排出される。この際、濾材(4)は上部支持体(2)に当接せずに下部吊り紐(8)と共に塔内の上方に伸長した状態となる。しかしながら、濾材(4)の上部に濃縮された濁質が除去されるまでの長時間の洗浄運転は、多量の洗浄水を使用して不経済となるので行なう必要はない。   In the cleaning operation (FIG. 1B), as described above, the valves (61) and (62) that were open during the raw water treatment operation are closed, and the cleaning water is supplied from the valve (64) to the pipe (52 ) To be fed into the tower (1). On the other hand, air is supplied into the tower (1) from the valve (63) via the pipe (53). The supply of air may be started simultaneously with the supply of cleaning water, or may be started later than the supply of cleaning water. Wash water containing turbidity is discharged from the valve (65) via the pipe (51). At this time, the filter medium (4) does not come into contact with the upper support (2), but extends upward in the tower together with the lower suspension string (8). However, it is not necessary to perform a long-time washing operation until the suspended turbidity concentrated on the upper part of the filter medium (4) is removed because a large amount of washing water is used.

前記の洗浄運転においては、洗浄水として、原水または濁質除去処理水を使用することが出来る。濁質除去処理水としては、濾過器や膜(逆浸透膜、限外濾過膜、精密濾過膜など)で処理された水の他、本発明で使用する濁質除去装置で処理した水が使用される。   In the above-described washing operation, raw water or turbidity removal treated water can be used as washing water. As turbidity removal treated water, water treated with a filter or membrane (reverse osmosis membrane, ultrafiltration membrane, microfiltration membrane, etc.) or water treated with the turbidity removal device used in the present invention is used. Is done.

1:塔
2:上部支持体
3:下部支持体
4:濾材
7:上部吊り紐
8:下部吊り紐
51〜53:配管
61〜67:バルブ
1: Tower 2: Upper support 3: Lower support 4: Filter medium 7: Upper suspension string 8: Lower suspension string 51-53: Piping 61-67: Valve

Claims (1)

下向流形式で原水が通水され且つ上向流形式で洗浄水が供給される長繊維濾過装置であって、塔(1)頂部には原水通水配管と洗浄排水排出配管とが設けられ、塔(1)底部には処理水排出配管と洗浄水供給配管とが設けられ、塔(1)内部には芯紐(41)の周側に濁質捕捉材を形成して成る複数の濾材(4)が装填され、複数の濾材(4)は原水通水時には塔(1)の下流側に押圧されて濁質捕捉材の一部が圧密状態を形成し且つ洗浄水供給時には前記の圧密状態を解除して粗状態を形成し得る様に流水方向に沿って屈曲変形可能な懸垂状態で吊り下げられ、前記の濁質捕捉材は、芯紐(41)の周側に形成された編組状モールコード(42)から成り、編組状モールコード(42)は、組紐を構成する素線(紐状体)のうち右回り、左回りのどちらか1方向の素線でループ(42a)を形成し、この素線及び他方向の素線で芯部の組紐体(42b)を形成した構造を有し、編組状モールコード(42)の組紐体(42b)は、50〜600mm間隔毎に2〜20mmの幅の縫付加工(42c)によって芯紐(41)に固定されていることを特徴とする長繊維濾過装置。   A long fiber filtration device in which raw water is passed in a downward flow format and cleaning water is supplied in an upward flow format, and a raw water flow piping and a cleaning drainage piping are provided at the top of the tower (1). The bottom of the tower (1) is provided with a treated water discharge pipe and a washing water supply pipe, and a plurality of filter media are formed in the tower (1) by forming a turbidity trapping material on the peripheral side of the core string (41). (4) is loaded, and the plurality of filter media (4) are pressed downstream of the tower (1) when the raw water is passed, so that a part of the turbidity trapping material forms a consolidated state and when the washing water is supplied, The suspended matter is suspended in a suspended state that can be bent and deformed along the direction of flowing water so that the rough state can be formed by releasing the state, and the turbidity trapping material is a braid formed on the peripheral side of the core string (41) The braided mall cord (42) is clockwise, left of the strands (strands) constituting the braid. A loop (42a) is formed by the strands in one direction of either of the wires, and the braided molding cord (42) is formed by forming the braided body (42b) of the core portion with the strands of this direction and the strands in the other direction. The braided body (42b) is fixed to the core string (41) by a sewing process (42c) having a width of 2 to 20 mm every interval of 50 to 600 mm.
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