JP2022098957A - Filtration device - Google Patents

Filtration device Download PDF

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JP2022098957A
JP2022098957A JP2020212649A JP2020212649A JP2022098957A JP 2022098957 A JP2022098957 A JP 2022098957A JP 2020212649 A JP2020212649 A JP 2020212649A JP 2020212649 A JP2020212649 A JP 2020212649A JP 2022098957 A JP2022098957 A JP 2022098957A
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tank
pipe
filtration
filter medium
filtration device
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JP7469805B2 (en
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正人 増本
Masato Masumoto
佳和 橋詰
Yoshikazu Hashizume
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NAKAJIMA KOMUTEN KK
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Abstract

To provide a filtration device which is suitable for filtration of raw water taken from a flume and can be easily maintained.SOLUTION: An interior of a box-shaped filter main body 12 is divided into three parts: a landing tank 20, an upstream counter flow type filtration tank 30, and a water cleaning tank 40, by a partition wall 14 and an overflow wall 16 standing vertically. The landing tank 20 has: a landing tank inflow pipe 22 in an upper part; a landing tank outflow pipe 24 in a lower part; a landing tank sludge pipe 26 on a bottom part. Below the filtration tank 30, a receiving plate 39 in mesh form is arrange, and on an upper side of the reception plate 39, a filter media layer 32 is arranged. On a lower side of the reception plate 39, an inflow chamber 31 is formed and a filtration tank inflow pipe 34 is arranged. On a top face of the filter media layer 32, the filter medium layer face sludge pipe 36 is provided, and on a bottom part of the filtration tank 30, a filtration tank sludge pipe 38 is arranged. On the water cleaning tank 40, an outflow pipe 42 is arranged in a lower side thereof, and a water cleaning tank sludge pipe 44 is arranged on a bottom thereof. The landing tank outflow pipe 24 and the filtration tank inflow pipe 34 are coupled by a conduit pipe 28, and a spherical floating filter medium 33 is provided in the inflow chamber 31.SELECTED DRAWING: Figure 1

Description

本発明は、中山間地域における谷川などで取水された原水を濾過する濾過装置に関する。 The present invention relates to a filtration device for filtering raw water taken from Tanigawa or the like in a mountainous area.

従来の濾過装置として、緩速濾過装置や上向流式濾過装置が一般的である。また、これらの濾過方式を組み合わせた濾過装置も種々開示されている(例えば、特許文献1及び特許文献2参照。)。特許文献1に開示された濾過装置は、U字型などの槽体内に粒状濾材を充填して該濾材層内を原水が順次下向流、水平流、上向流で通水されるごとく構成し、濾材の洗浄機構として下向流部、上向流部を上向流で洗浄するための洗浄用ノズルをそれぞれ別個に水平流部内に配備したことを特徴とする。この特許文献1に開示された濾過装置によると、濾過効率の向上が図られると共に、濾過装置の維持管理も容易である旨、記載されている。 As a conventional filtration device, a slow sand filter or an upward flow type filtration device is generally used. Further, various filtration devices combining these filtration methods are also disclosed (see, for example, Patent Document 1 and Patent Document 2). The filtration device disclosed in Patent Document 1 is configured such that a U-shaped or the like is filled with a granular filter medium and raw water is sequentially passed through the filter medium layer by downward flow, horizontal flow, and upward flow. However, as a cleaning mechanism for the filter medium, a cleaning nozzle for cleaning the downward flow portion and the upward flow portion with the upward flow is separately provided in the horizontal flow portion. According to the filtration device disclosed in Patent Document 1, it is described that the filtration efficiency is improved and the maintenance of the filtration device is easy.

また、特許文献2に開示された濾過材洗浄装置付き上向濾過装置は、上方に行くに従って次第に粒度が小さくなる濾過材を積層してなる濾過材層の下方より原水を通過させるようにした上向濾過装置において、上方へ向かって洗浄水を噴出する洗浄管を濾過材層の下面に設けるとともに、濾過材層の上面中央部に、水平をなし、かつ両側辺の上縁に、多数の鋸歯状突起を有する排泥樋を設け、かつ排泥樋の一端を、砂捕集箱に接続してなることを特徴とする。この特許文献2に開示された濾過材洗浄装置付き上向濾過装置によると、濾過槽を安価に製造することができるとともに、洗浄水とともに流出しようとする濾過砂は、排泥樋の鋸刃状突起で効果的に食い止められる旨、記載されている。 Further, in the upward filtration device with a filter medium cleaning device disclosed in Patent Document 2, raw water is allowed to pass from below the filter medium layer formed by laminating filter media whose particle size gradually decreases toward the top. In the facing filtration device, a washing tube that ejects washing water upward is provided on the lower surface of the filter material layer, and a large number of saw teeth are formed horizontally at the center of the upper surface of the filter material layer and on the upper edges on both sides. It is characterized in that a mud drainage gutter having a shape protrusion is provided, and one end of the mud drainage gutter is connected to a sand collecting box. According to the upward filtration device with a filter material cleaning device disclosed in Patent Document 2, the filtration tank can be manufactured at low cost, and the filtered sand that is about to flow out together with the cleaning water has a saw blade shape of a mud drain. It is stated that the protrusions can be effectively stopped.

特開昭63-291609号公報Japanese Unexamined Patent Publication No. 63-291609 実開昭63-77606号公報Jikkai Sho 63-77606 Gazette

特許文献1に開示された濾過装置や特許文献2に開示された濾過材洗浄装置付き上向濾過装置によると、濾過効率の向上及び維持管理がある程度、容易に行えるものと思料する。 According to the filtration device disclosed in Patent Document 1 and the upward filtration device with a filter material cleaning device disclosed in Patent Document 2, it is considered that the improvement of the filtration efficiency and the maintenance can be easily performed to some extent.

しかし、中山間地域において設置される濾過装置は、設置コストや設置場所等の観点から、コンパクトでありながら濾過効率が高く、何より維持管理が容易な濾過装置が求められる。特に、濾過装置内に堆積した土砂や泥の排出作業や濾過材の洗浄作業は非常に煩雑であるため、これらの作業性を大幅に向上した濾過装置が求められていた。 However, the filtration device installed in the mountainous area is required to be compact, have high filtration efficiency, and above all, be easy to maintain and manage, from the viewpoint of installation cost and installation location. In particular, the work of discharging the earth and sand and mud accumulated in the filtration device and the work of cleaning the filter material are extremely complicated, and therefore, a filtration device having significantly improved workability has been required.

そこで本願発明者らは、上記の問題点に鑑み、谷川などで取水される原水の濾過に好適であるとともに、維持管理が容易である濾過装置を提供するべく鋭意検討を重ねた結果、本発明に至ったのである。 Therefore, in view of the above problems, the inventors of the present application have made extensive studies to provide a filtration device that is suitable for filtering raw water taken from Tanigawa or the like and that is easy to maintain and manage. It came to.

即ち、本発明の濾過装置は、箱状の濾過装置本体内が、垂直方向に立設された隔壁及び越流壁によって、着水槽と、上向流式の濾過槽と、浄水槽とに三分され、着水槽には、該着水槽の上方に着水槽流入管、下方に着水槽流出管、底部に着水槽排泥管が配設され、前記濾過槽の下方にメッシュ状の受板が配設され、該受板の上側に、下方から上方に向かって粒径が小さくなる濾材を積層した濾材層が配設されるとともに、前記受板の下側に流入室が形成されて濾過槽流入管が配設され、前記濾材層の上面に濾材層面排泥管、前記濾過槽の底部に濾過槽排泥管が配設され、前記浄水槽には、該浄水槽の下方に流出管、底部に浄水槽排泥管が配設され、前記着水槽流出管と前記濾過槽流入管とが導通管で連結され、前記流入室に、球状浮遊濾材が配設されていることを特徴とする。 That is, in the filtration device of the present invention, the inside of the box-shaped filtration device main body is divided into a water landing tank, an upward flow type filtration tank, and a water purification tank by means of a partition wall and an overflow wall erected in the vertical direction. The water tank is divided into a water tank inflow pipe above the water tank, a water tank outflow pipe below, a water tank drain pipe at the bottom, and a mesh-shaped receiving plate below the filtration tank. A filter medium layer in which filter media having a smaller particle size from the lower side to the upper side is arranged on the upper side of the receiving plate, and an inflow chamber is formed on the lower side of the receiving plate to form a filtration tank. An inflow pipe is arranged, a filter medium layer surface mud drain pipe is arranged on the upper surface of the filter medium layer, a filter tank mud drain pipe is arranged at the bottom of the filter tank, and the outflow pipe is arranged below the water purification tank in the water purification tank. A water purification tank drain pipe is disposed at the bottom, the landing tank outflow pipe and the filtration tank inflow pipe are connected by a conduction pipe, and a spherical floating filter medium is disposed in the inflow chamber. ..

また、本発明の濾過装置において、前記球状浮遊濾材が中空であることを特徴とする。 Further, in the filtration device of the present invention, the spherical floating filter medium is hollow.

更に、本発明の濾過装置において、前記濾材層内に洗浄管が配設されていることを特徴とする。 Further, the filtration device of the present invention is characterized in that a cleaning tube is disposed in the filter medium layer.

また、本発明の濾過装置において、前記越流壁の上端縁にVノッチが形成されていることを特徴とする。 Further, the filtration device of the present invention is characterized in that a V notch is formed at the upper end edge of the overflow wall.

本発明の濾過装置によると、コンパクトでありながら、谷川などで取水される原水に含まれる枯れ葉等の浮遊ゴミや土砂、泥、細砂等を段階的に除去することができ、濾過効率の非常に高い濾過装置を提供することができる。 According to the filtration device of the present invention, although it is compact, it is possible to gradually remove floating dust such as dead leaves, earth and sand, mud, fine sand, etc. contained in the raw water taken from Tanigawa, etc., and the filtration efficiency is very high. Can provide a high filtration device.

また、本発明の濾過装置によると、簡単なバルブ操作のみで濾過装置内に堆積した土砂や泥等の排出作業、濾過材の洗浄作業を行うことができ、維持管理が非常に容易である。 Further, according to the filtration device of the present invention, it is possible to discharge the earth and sand and mud accumulated in the filtration device and to clean the filter material with only a simple valve operation, and the maintenance is very easy.

更に、本発明の濾過装置において、濾過槽内の受板の下側に形成される流入室に球状浮遊濾材を配設することによって、濾過効率の更なる向上を図ることができる。 Further, in the filtration device of the present invention, the filtration efficiency can be further improved by disposing the spherical floating filter medium in the inflow chamber formed under the receiving plate in the filtration tank.

また、本発明に係る球状浮遊濾材の浮力によって受板が押し上げられることとなるため、受板に作用する濾材層の荷重軽減を図ることができ、受板の強度軽減、更には濾過装置本体に掛かる荷重の軽減を図ることができる。 Further, since the receiving plate is pushed up by the buoyancy of the spherical floating filter medium according to the present invention, the load of the filter medium layer acting on the receiving plate can be reduced, the strength of the receiving plate can be reduced, and the filtering device main body can be used. It is possible to reduce the applied load.

また更に、本発明に係る球状浮遊濾材を中空とすることによって、受板の強度軽減効果及び濾過装置本体の荷重軽減効果の向上を図ることができるとともに、中空の球状浮遊濾材による保温効果によって、中山間地域の冬期における濾過装置内の凍結防止効果が期待できる。 Furthermore, by making the spherical floating filter medium according to the present invention hollow, it is possible to improve the effect of reducing the strength of the receiving plate and the effect of reducing the load of the main body of the filtration device, and the heat retaining effect of the hollow spherical floating filter medium makes it possible to improve the effect. It can be expected to have an antifreeze effect in the filtration device in the winter in the hilly and mountainous areas.

また、本発明の濾過装置において、濾材層内に洗浄管が配設されていることによって、濾材層の洗浄作業を容易に実施できる。 Further, in the filtration device of the present invention, the cleaning operation of the filter media layer can be easily performed by disposing the cleaning pipe in the filter media layer.

更に、本発明の濾過装置において、越流壁の上端縁にVノッチが形成されていることによって、濾過速度の調整を容易に実施することができる。 Further, in the filtration device of the present invention, the filtration rate can be easily adjusted by forming the V notch on the upper end edge of the overflow wall.

本発明の一実施形態に係る濾過装置の正面視断面図である。It is a front view sectional view of the filtration apparatus which concerns on one Embodiment of this invention. 図1に示した濾過装置の平面図である。It is a top view of the filtration apparatus shown in FIG. 図1におけるA-A断面図である。FIG. 3 is a sectional view taken along the line AA in FIG.

以下、本発明の一実施形態について、図面に基づいて説明する。図1は、本発明の一実施形態に係る濾過装置10を示す正面視断面図、図2は図1に示した濾過装置10の平面図、図3は図1に示した濾過装置10におけるA-A断面図である。なお、本来であれば、本実施形態の濾過装置10の正面視断面図を示す図1中には、濾過装置10の正面側に配設される着水槽流出管24、濾過槽流入管34、濾材層面排泥管36、濾過槽排泥管38は表れないが、本実施形態を説明するため、便宜的に図示したものである。 Hereinafter, an embodiment of the present invention will be described with reference to the drawings. 1 is a front sectional view showing a filtration device 10 according to an embodiment of the present invention, FIG. 2 is a plan view of the filtration device 10 shown in FIG. 1, and FIG. 3 is A in the filtration device 10 shown in FIG. -A sectional view. Originally, in FIG. 1 showing a front view sectional view of the filtration device 10 of the present embodiment, the landing tank outflow pipe 24 and the filtration tank inflow pipe 34 arranged on the front side of the filtration device 10 are included. Although the filter medium layer surface mud drain pipe 36 and the filter tank mud drain pipe 38 do not appear, they are shown for convenience in order to explain the present embodiment.

図1~図3に示すように、本発明の一実施形態に係る濾過装置10は、中山間地域における谷川などで取水した原水を濾過するのに好適であって、まず箱状の濾過装置本体12内が、垂直方向に立設された隔壁14と越流壁16とによって、着水槽20と、上向流式の濾過槽30と、浄水槽40とに三分されている。 As shown in FIGS. 1 to 3, the filtration device 10 according to the embodiment of the present invention is suitable for filtering raw water taken from a valley river or the like in a mountainous area, and first, a box-shaped filtration device main body. The inside of the 12 is divided into a water landing tank 20, an upward flow type filtration tank 30, and a water purification tank 40 by a partition wall 14 erected in the vertical direction and an overflow wall 16.

本実施形態の濾過装置10に係る着水槽20には、この着水槽20の上方に着水槽流入管22が配設され、下方には着水槽流出管24が配設され、底部には着水槽排泥管26が配設されている。谷川などで取水された原水は、着水槽20の上方に配設された着水槽流入管22から、着水槽20内に流入する。この着水槽20では、原水に含まれる枯れ葉等の浮遊ゴミや、粒径が比較的大きめの土砂が除去され、ある程度濾過された原水が、着水槽20の下方に配設された着水槽流出管24から、後述する濾過槽30へ送られる。 In the landing tank 20 according to the filtration device 10 of the present embodiment, a landing tank inflow pipe 22 is disposed above the landing tank 20, a landing tank outflow pipe 24 is disposed below, and a landing tank is provided at the bottom. A mud drain pipe 26 is arranged. The raw water taken in by Tanigawa or the like flows into the landing tank 20 from the landing tank inflow pipe 22 arranged above the landing tank 20. In this landing tank 20, floating debris such as dead leaves contained in the raw water and earth and sand having a relatively large particle size are removed, and the raw water filtered to some extent is arranged below the landing tank 20 in the water tank outflow pipe. From 24, it is sent to the filtration tank 30 described later.

本実施形態に係る濾過槽30は上向流式であって、この濾過槽30の下方にメッシュ状の受板39が配設され、この受板39の上側には、下方から上方に向かって粒径が小さくなる濾材を積層した濾材層32が配設されており、受板39の下側には、流入室31が形成されている。本実施形態に係る濾材層32は、下方から上方に向かって順に、粒径20~30mmの濾過砂利で形成された濾材層32a、12~20mmの濾過砂利で形成された濾材層32b、2~4mmの濾過砂利で形成された濾材層32c、0.6mmの濾過砂で形成された濾材層32d、そして0.3~0.45mmの濾過砂で形成された濾材層32eが積層されることによって構成されている。なお、本発明に係る濾材層は当該構成に限定されるものではなく、濾材の種類や積層数等は任意に設定することができる。 The filtration tank 30 according to the present embodiment is an upward flow type, and a mesh-shaped receiving plate 39 is arranged below the filtration tank 30, and on the upper side of the receiving plate 39, from the lower side to the upper side. A filter medium layer 32 in which filter media having a smaller particle size are laminated is arranged, and an inflow chamber 31 is formed under the receiving plate 39. The filter medium layer 32 according to the present embodiment is, in order from the bottom to the top, a filter medium layer 32a formed of filtered gravel having a particle size of 20 to 30 mm, a filter medium layer 32b formed of filtered gravel having a particle size of 12 to 20 mm, 2 to 2. By laminating a filter medium layer 32c formed of 4 mm filtered gravel, a filter medium layer 32d formed of 0.6 mm filtered sand, and a filter medium layer 32e formed of 0.3 to 0.45 mm filtered sand. It is configured. The filter medium layer according to the present invention is not limited to the configuration, and the type of the filter medium, the number of layers, and the like can be arbitrarily set.

また、本実施形態に係る濾材層32には、洗浄管50が予め配設されている。洗浄管50を配設することによって、濾材層32を含む濾過槽30の洗浄作業を容易に行うことができる。具体的な洗浄方法については後述する。 Further, a cleaning pipe 50 is previously arranged in the filter medium layer 32 according to the present embodiment. By disposing the cleaning pipe 50, the cleaning operation of the filtration tank 30 including the filter medium layer 32 can be easily performed. The specific cleaning method will be described later.

本実施形態に係る濾過槽30における受板39の下側に形成された流入室31には、濾過槽流入管34が配設され、受板39の上側に配設された濾材層32の最上面位置に濾材層面排泥管36、濾過槽30の底部(=流入室31の底部)に濾過槽排泥管38が配設されている。 In the inflow chamber 31 formed on the lower side of the receiving plate 39 in the filtering tank 30 according to the present embodiment, the filtration tank inflow pipe 34 is arranged, and the most of the filter medium layer 32 arranged on the upper side of the receiving plate 39. The filter medium layer surface mud drain pipe 36 is arranged at the upper surface position, and the filter tank mud drain pipe 38 is arranged at the bottom of the filter tank 30 (= the bottom of the inflow chamber 31).

ここで、上記した本実施形態に係る着水槽20の下方に配設された着水槽流出管24と、本実施形態に係る流入室31に配設された濾過槽流入管34とは、導通管28によって連結されている。従って、着水槽20においてある程度濾過された原水は着水槽流出管24から流出し、導通管28を介して濾過槽流入管34から濾過槽30に係る流入室31に流入することとなる。 Here, the water tank outflow pipe 24 arranged below the water tank 20 according to the present embodiment and the filtration tank inflow pipe 34 arranged in the inflow chamber 31 according to the present embodiment are conductive pipes. It is connected by 28. Therefore, the raw water filtered to some extent in the landing tank 20 flows out from the landing tank outflow pipe 24, and flows into the inflow chamber 31 related to the filter tank 30 from the filter tank inflow pipe 34 via the conduction pipe 28.

そして、本実施形態に係る流入室31には、複数の球状浮遊濾材33が配設されていることを特徴とする。球状浮遊濾材33はポリプロピレン製の濾材であって、流入室31に流入する原水によって浮遊する。球状浮遊濾材33の素材は、原水によって浮遊するものであれば特に限定されないが、ポリプロピレンは汎用樹脂の中でも比重が最も小さく、耐熱性に優れ、強度が高く、吸湿性が無い、といった特徴を有するため、球状浮遊濾材33の素材として好適である。 The inflow chamber 31 according to the present embodiment is characterized in that a plurality of spherical floating filter media 33 are arranged. The spherical floating filter medium 33 is a polypropylene filter medium and is suspended by the raw water flowing into the inflow chamber 31. The material of the spherical floating filter medium 33 is not particularly limited as long as it is suspended by raw water, but polypropylene has the characteristics of having the smallest specific gravity among general-purpose resins, excellent heat resistance, high strength, and no hygroscopicity. Therefore, it is suitable as a material for the spherical floating filter medium 33.

なお、球状浮遊濾材33の外径サイズも特に限定されず、濾過装置本体12や流入室31の大きさ等に応じて適宜選択されるが、概ね外径10mm~50mmであることが好ましい。 The outer diameter size of the spherical floating filter medium 33 is not particularly limited, and is appropriately selected depending on the size of the filtration device main body 12 and the inflow chamber 31, but the outer diameter is preferably 10 mm to 50 mm.

また、球状浮遊濾材33の投入量も特に限定されず、球状浮遊濾材33が流入室31内で浮遊した状態で、少なくとも受板39の下面側の全面を覆って配列される程度であればよく、特に、図1及び図3で示すように、受板39の下面側の全面を覆って上下2段に配列される程度であることが好ましい。このように、球状浮遊濾材33が受板39の下面側の全面を覆って上下2段に配列されることによって、濾過槽流入管34から流入した原水が、原水の流れによって遊動する球状浮遊濾材33同士の隙間を通過することで濾過に有利な層流となって濾材層32に送られることとなり、濾過効率の更なる向上が図られる。 Further, the input amount of the spherical floating filter medium 33 is not particularly limited, and it is sufficient that the spherical floating filter medium 33 is arranged so as to cover at least the entire lower surface side of the receiving plate 39 in a state of being suspended in the inflow chamber 31. In particular, as shown in FIGS. 1 and 3, it is preferable that the receiving plate 39 is arranged in two upper and lower stages so as to cover the entire lower surface side. In this way, the spherical floating filter medium 33 covers the entire lower surface side of the receiving plate 39 and is arranged in two upper and lower stages, so that the raw water flowing from the filter tank inflow pipe 34 is idled by the flow of the raw water. By passing through the gaps between the 33, it becomes a laminar flow advantageous for filtration and is sent to the filter medium layer 32, so that the filtration efficiency can be further improved.

なお、流入室31に球状浮遊濾材33が配設されておらず、原水が流入室31から濾材層32に直接流入する場合は、原水の水流や濾材層32への汚れの固着等によって、原水が通過しやすい部分と通過しにくい部分とが生じる流れムラが発生しやすい。しかし、流入室31に球状浮遊濾材33を配設することによって原水の流れが拡散され、流れムラが生じにくくなるため、濾材層32に係る水平方向の濾過面積を有効に活用することができ、濾過効率の一層の向上を図ることができる。 If the spherical floating filter medium 33 is not arranged in the inflow chamber 31 and the raw water directly flows into the filter medium layer 32 from the inflow chamber 31, the raw water may flow due to the flow of the raw water or the adhesion of dirt to the filter medium layer 32. There is a tendency for uneven flow to occur, with parts that are easy to pass through and parts that are difficult to pass through. However, by disposing the spherical floating filter medium 33 in the inflow chamber 31, the flow of raw water is diffused and uneven flow is less likely to occur. Therefore, the horizontal filtration area of the filter medium layer 32 can be effectively utilized. It is possible to further improve the filtration efficiency.

ここで、本実施形態に係る球状浮遊濾材33はポリプロピレン製であるため、中実であっても流入室31内において原水によって浮遊し、濾過効率の向上を図ることができるが、球状浮遊濾材33は中空であることが特に好ましい。本実施形態に係る流入室31に球状浮遊濾材33を配設することによって濾過効率の向上が図られるとともに、球状浮遊濾材33の浮力によって受板39が押し上げられることとなるため、受板39に作用する濾材層32の荷重軽減を図ることができ、受板39の強度軽減、更には濾過装置本体12に掛かる荷重の軽減を図ることができる。そして、この球状浮遊濾材33を中空とすることによって、原水の流れによる遊動も大きくなるため、流れの拡散効果が更に期待できるとともに、球状浮遊濾材33の浮力も大きくなるため、受板39の強度軽減効果及び濾過装置本体12の荷重軽減効果の向上を図ることができる。 Here, since the spherical floating filter medium 33 according to the present embodiment is made of polypropylene, even if it is solid, it can be suspended by raw water in the inflow chamber 31 to improve the filtration efficiency, but the spherical floating filter medium 33 can be improved. Is particularly preferably hollow. By arranging the spherical floating filter medium 33 in the inflow chamber 31 according to the present embodiment, the filtration efficiency is improved, and the receiving plate 39 is pushed up by the buoyancy of the spherical floating filter medium 33. It is possible to reduce the load of the acting filter medium layer 32, reduce the strength of the receiving plate 39, and further reduce the load applied to the filtration device main body 12. By making the spherical floating filter medium 33 hollow, the floating due to the flow of raw water is increased, so that the diffusion effect of the flow can be further expected, and the buoyancy of the spherical floating filter medium 33 is also increased, so that the strength of the receiving plate 39 is increased. It is possible to improve the reduction effect and the load reduction effect of the filtration device main body 12.

また更に、本実施形態に係る球状浮遊濾材33を中空とすることによって、球状浮遊濾材33による保温効果が得られるため、中山間地域の冬期における濾過装置本体12内の凍結防止効果が期待できる。 Furthermore, by making the spherical floating filter medium 33 according to the present embodiment hollow, the heat retention effect of the spherical floating filter medium 33 can be obtained, so that the antifreezing effect in the filtration device main body 12 in the winter in the mountainous area can be expected.

本実施形態に係る浄水槽40には、浄水槽40の下方に流出管42が配設され、底部に浄水槽排泥管44が配設されている。濾過装置本体12内において、濾過槽30に係る流入室31に流入した原水は濾材層32を通過し、越流壁16を越流して浄水槽40へ流入した濾過水は、浄水槽40に配設された流出管42から給水設備等(不図示)へ送られることとなる。 In the water purification tank 40 according to the present embodiment, an outflow pipe 42 is arranged below the water purification tank 40, and a water purification tank mud drain pipe 44 is arranged at the bottom. In the filtration device main body 12, the raw water flowing into the inflow chamber 31 related to the filtration tank 30 passes through the filter medium layer 32, and the filtered water flowing through the overflow wall 16 and flowing into the water purification tank 40 is distributed to the water purification tank 40. It will be sent from the installed outflow pipe 42 to a water supply facility or the like (not shown).

なお、本実施形態に係る濾過槽30と浄水槽40との間に配設される越流壁16の上端縁にはVノッチ52が形成されていることが好ましい。このVノッチ52を形成することによって、Vノッチ52を通過する濾過水の高さを確認することによって濾過速度の把握が容易となるため、濾過速度の調整を容易に実施することができる。なお、図3において、Vノッチ52における高さ方向の中間位置に配設された符号53で示す部材は濾過速度目盛棒である。例えば、濾過槽30から浄化槽40へ流出する濾過水が濾過速度目盛棒53を超えている場合は、着水槽20への原水の流入量を調整したり、着水槽20から濾過槽30に係る流入室31への原水の流入量を調整したりして、濾過速度を容易に調整することができる。 It is preferable that a V notch 52 is formed on the upper end edge of the overflow wall 16 arranged between the filtration tank 30 and the water purification tank 40 according to the present embodiment. By forming the V notch 52, the filtration rate can be easily grasped by confirming the height of the filtered water passing through the V notch 52, so that the filtration rate can be easily adjusted. In FIG. 3, the member indicated by the reference numeral 53 arranged at the intermediate position in the height direction of the V notch 52 is a filtration rate scale bar. For example, when the filtered water flowing out from the filtration tank 30 to the septic tank 40 exceeds the filtration speed scale bar 53, the amount of raw water flowing into the landing tank 20 may be adjusted, or the inflow from the landing tank 20 to the filtration tank 30 may be adjusted. The filtration rate can be easily adjusted by adjusting the amount of raw water flowing into the chamber 31.

以上、本発明の実施形態について詳述したが、次に本発明の実施形態に係る濾過装置10の洗浄方法について説明する。本実施形態の濾過装置10においては、濾過槽30に係る流入室31が、最も汚れが沈下して溜まりやすい場所となるが、最も簡易的な洗浄方法は、濾材層面排泥管36、流出管42及び浄水槽排泥管44にそれぞれ配設されたバルブ(不図示)を閉栓するとともに濾過槽排泥管38に配設されたバルブ(不図示)を開栓した状態で、濾過槽流入管34から原水を流入室31に導水することによって、流入室31に堆積した泥や砂等を容易に排出することができる。或いは、導通管28に配設されたバルブ(不図示)を閉栓し、着水槽流入管22に導水される原水を分岐させて洗浄管50に導水することによって、流入室31の洗浄とともに濾材層32の洗浄も行うことができる。 The embodiment of the present invention has been described in detail above, but next, the cleaning method of the filtration device 10 according to the embodiment of the present invention will be described. In the filtration device 10 of the present embodiment, the inflow chamber 31 related to the filtration tank 30 is the place where dirt is most likely to settle and accumulate, but the simplest cleaning method is the filter medium layer surface mud drain pipe 36 and the outflow pipe. The filter tank inflow pipe with the valves (not shown) arranged in the water purification tank drain pipe 44 and the valve (not shown) closed and the valves (not shown) arranged in the filter tank mud drain pipe 38 opened. By guiding the raw water from 34 to the inflow chamber 31, mud, sand and the like accumulated in the inflow chamber 31 can be easily discharged. Alternatively, the valve (not shown) provided in the conduction pipe 28 is closed, and the raw water conducted to the water landing tank inflow pipe 22 is branched and guided to the cleaning pipe 50 to clean the inflow chamber 31 and the filter medium layer. 32 can also be washed.

流入室31の洗浄、更には濾材層32の洗浄が完了すると、濾過槽排泥管38に係るバルブの閉栓及び洗浄管50への原水の導水を停止する。導通管28に係るバルブを閉栓していた場合はこのバルブを開栓し、濾材層面排泥管36に配設されたバルブ(不図示)を開栓することによって、濾材層32内の汚れや濾材層32の上面に堆積した汚れを排出することができる。 When the cleaning of the inflow chamber 31 and the cleaning of the filter medium layer 32 are completed, the valve of the filter tank drain pipe 38 is closed and the raw water is stopped to be introduced to the cleaning pipe 50. When the valve related to the conduction pipe 28 was closed, this valve was opened, and the valve (not shown) arranged on the filter media layer surface mud drainage pipe 36 was opened to prevent the inside of the filter media layer 32 from becoming dirty. Dirt accumulated on the upper surface of the filter medium layer 32 can be discharged.

濾材層32の上面に堆積した汚れが排出できたら濾材層面排泥管36に係るバルブを閉栓し、流出管42に係るバルブを開栓することによって、濾過水が流出管42から送水されることとなる。なお、浄水槽40に貯留される濾過水に濁質がある場合は、流出管42に係るバルブを閉栓した上で浄水槽排泥管44に係るバルブを開栓し、濾過水に濁質が確認できなくなるまで排水する。 When the dirt accumulated on the upper surface of the filter medium layer 32 can be discharged, the valve related to the filter medium layer surface mud drain pipe 36 is closed and the valve related to the outflow pipe 42 is opened, so that the filtered water is sent from the outflow pipe 42. Will be. If the filtered water stored in the water purification tank 40 has turbidity, the valve related to the outflow pipe 42 is closed and then the valve related to the water purification tank drainage pipe 44 is opened, and the filtered water becomes turbid. Drain until no confirmation is possible.

以上のように、本実施形態の濾過装置10は、それぞれの管部材に配設されたバルブの開閉操作によって容易に濾過装置本体12内の洗浄作業を行うことができ、維持管理が非常に容易となる。なお、着水槽20内に堆積した汚れは、導通管28に係るバルブを閉栓し、着水槽排泥管26を開栓することによって容易に排出することができる。 As described above, the filtration device 10 of the present embodiment can easily perform the cleaning work inside the filtration device main body 12 by opening and closing the valves arranged on the respective pipe members, and the maintenance is very easy. Will be. The dirt accumulated in the water landing tank 20 can be easily discharged by closing the valve related to the conduction pipe 28 and opening the water landing tank mud drain pipe 26.

以上、本発明の濾過装置の実施形態について詳述したが、本発明の技術的思想を実質的に限定するものと解してはならない。本発明はその要旨を逸脱しない範囲で、当業者の創意と工夫により、適宜に改良、変更又は追加をしながら実施できる。 Although the embodiment of the filtration device of the present invention has been described in detail above, it should not be understood that the technical idea of the present invention is substantially limited. The present invention can be carried out with appropriate improvements, changes or additions by the creativity and ingenuity of those skilled in the art without departing from the gist thereof.

10:濾過装置
12:濾過装置本体
14:隔壁
16:越流壁
20:着水槽
22:着水槽流入管
24:着水槽流出管
26:着水槽排泥管
28:導通管
30:濾過槽
31:流入室
32:濾材層
33:球状浮遊濾材
34:濾過槽流入管
36:濾材層面排泥管
38:濾過槽排泥管
39:受板
40:浄水槽
42:流出管
44:浄水槽排泥管
50:洗浄管
52:Vノッチ
53:濾過速度目盛棒

10: Filtration device 12: Filtration device body 14: Partition 16: Overflow wall 20: Water tank 22: Water tank inflow pipe 24: Water tank outflow pipe 26: Water tank drain pipe 28: Conduction pipe 30: Filtration tank 31: Inflow chamber 32: Filter media layer 33: Spherical floating filter media 34: Filter media inflow pipe 36: Filter media layer surface mud drain pipe 38: Filter tank mud drain pipe 39: Receiving plate 40: Water purification tank 42: Outflow pipe 44: Water purification tank drain pipe 50: Cleaning pipe 52: V notch 53: Filtration speed scale bar

Claims (4)

箱状の濾過装置本体内が、垂直方向に立設された隔壁及び越流壁によって、着水槽と、上向流式の濾過槽と、浄水槽とに三分され、
前記着水槽には、該着水槽の上方に着水槽流入管、下方に着水槽流出管、底部に着水槽排泥管が配設され、
前記濾過槽の下方にメッシュ状の受板が配設され、該受板の上側に、下方から上方に向かって粒径が小さくなる濾材を積層した濾材層が配設されるとともに、前記受板の下側に流入室が形成されて濾過槽流入管が配設され、前記濾材層の上面に濾材層面排泥管、前記濾過槽の底部に濾過槽排泥管が配設され、
前記浄水槽には、該浄水槽の下方に流出管、底部に浄水槽排泥管が配設され、
前記着水槽流出管と前記濾過槽流入管とが導通管で連結され、
前記流入室に、球状浮遊濾材が配設されていることを特徴とする濾過装置。
The inside of the box-shaped filtration device body is divided into a water landing tank, an upward flow type filtration tank, and a water purification tank by a partition wall and an overflow wall erected in the vertical direction.
The landing tank is provided with a water tank inflow pipe above the water tank, a water tank outflow pipe below, and a water tank mud drain pipe at the bottom.
A mesh-shaped receiving plate is arranged below the filtration tank, and a filter medium layer in which filter media having a smaller particle size is arranged from the lower side to the upper side is arranged on the upper side of the receiving plate, and the receiving plate is arranged. An inflow chamber is formed on the lower side and a filter tank inflow pipe is arranged, a filter medium layer surface mud drain pipe is arranged on the upper surface of the filter medium layer, and a filter tank mud drain pipe is arranged on the bottom of the filter tank.
In the water purification tank, an outflow pipe is arranged below the water purification tank, and a water purification tank drainage pipe is arranged at the bottom.
The water tank outflow pipe and the filtration tank inflow pipe are connected by a conduction pipe, and the water tank outflow pipe and the filtration tank inflow pipe are connected by a conduction pipe.
A filtration device characterized in that a spherical floating filter medium is disposed in the inflow chamber.
前記球状浮遊濾材が中空であることを特徴とする請求項1に記載の濾過装置。 The filtration device according to claim 1, wherein the spherical floating filter medium is hollow. 前記濾材層内に洗浄管が配設されていることを特徴とする請求項1または請求項2に記載の濾過装置。 The filtration device according to claim 1 or 2, wherein a cleaning tube is arranged in the filter medium layer. 前記越流壁の上端縁にVノッチが形成されていることを特徴とする請求項1から請求項3の何れかに記載の濾過装置。 The filtration device according to any one of claims 1 to 3, wherein a V notch is formed at the upper end edge of the overflow wall.
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