JPH022406Y2 - - Google Patents
Info
- Publication number
- JPH022406Y2 JPH022406Y2 JP13151283U JP13151283U JPH022406Y2 JP H022406 Y2 JPH022406 Y2 JP H022406Y2 JP 13151283 U JP13151283 U JP 13151283U JP 13151283 U JP13151283 U JP 13151283U JP H022406 Y2 JPH022406 Y2 JP H022406Y2
- Authority
- JP
- Japan
- Prior art keywords
- water
- inclined plates
- angle
- filtration device
- continuous
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 47
- 239000000463 material Substances 0.000 claims description 46
- 238000005507 spraying Methods 0.000 claims description 9
- 238000001914 filtration Methods 0.000 claims description 8
- 230000005484 gravity Effects 0.000 claims description 4
- 230000008929 regeneration Effects 0.000 claims description 2
- 238000011069 regeneration method Methods 0.000 claims description 2
- 239000008400 supply water Substances 0.000 claims description 2
- 239000007787 solid Substances 0.000 description 13
- 238000004140 cleaning Methods 0.000 description 5
- 230000006866 deterioration Effects 0.000 description 5
- 230000000694 effects Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 230000002542 deteriorative effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Description
【考案の詳細な説明】
この考案は連続過装置に係り、特に処理水質
の悪化防止に好適な過装置に関するものであ
る。[Detailed Description of the Invention] This invention relates to a continuous filtration device, and particularly to a filtration device suitable for preventing deterioration of treated water quality.
従来のこの種装置は、第1図に示す通り、多段
状配設の傾斜板11Aにより形成され、かつ内部
が散水部3とされた垂直の通水性内部筒体12
と、多段状の傾斜板11Bにより形成され、かつ
外部が集水部4とされた垂直の通水性外部筒体1
3と、過塔1の底部から上記内部筒体12を貫
通して上方へ達する濁質捕捉材の移送用エアリ
フト管7とから主に構成されている。このような
装置において、内部筒体12と外部筒体13間の
空所に砂等の材(層)2が充填され(この材
層は傾斜板11Aおよび11B間に保持される)、
この材層を介して被処理水の過処理が行われ
る。 As shown in FIG. 1, a conventional device of this type includes a vertical water-permeable inner cylinder 12 formed of inclined plates 11A arranged in a multi-stage manner and having a water sprinkling section 3 inside.
and a vertical water-permeable external cylindrical body 1 formed by multi-stage inclined plates 11B and having a water collecting section 4 on the outside.
3, and an air lift pipe 7 for transporting the suspended solids trapping material, which extends from the bottom of the filter tower 1 through the internal cylinder 12 and reaches upward. In such a device, the space between the inner cylinder 12 and the outer cylinder 13 is filled with a material (layer) 2 such as sand (this material layer is held between the inclined plates 11A and 11B),
Overtreatment of the water to be treated is performed through this material layer.
その際、被処理水は供給管5を経たのち散水部
3に導かれ、次いで傾斜板11Aの相互間隙部を
通つて材層2内へ送られる。このようにして送
られた被処理水は材層内を水平方向へ流れ、そ
の間に含有濁質の除去が行われるが、その後傾斜
板11Bの相互間隙部を通つて集水部4に集めら
れ、次いで排水管6を経て系外へ排出される。 At this time, the water to be treated is led to the water spraying section 3 after passing through the supply pipe 5, and then sent into the material layer 2 through the mutual gap between the inclined plates 11A. The treated water sent in this way flows horizontally within the material layer, during which suspended solids are removed, and is then collected in the water collection section 4 through the mutual gap between the inclined plates 11B. Then, it is discharged to the outside of the system through the drain pipe 6.
一方、濁質を捕捉した材層2は、下記するエ
アリフト管7の吸込み作用を受けて連続的に重力
方向へ移動する。そして、最終的にエアリフト管
7の入口に達した濁質捕捉材層は、空気供給管
8を経て導入される空気に同拌されてエアリフト
管7内を上昇し、過塔1の上部に設けられた
材洗浄槽9内へ排出され、ここで洗浄後再使用さ
れる。なお、上記洗浄後の排液は排出管10を経
て系外へ排出される。 On the other hand, the material layer 2 that has captured the suspended solids moves continuously in the direction of gravity under the suction action of the air lift tube 7, which will be described below. The suspended solids trapping material layer that has finally reached the inlet of the air lift pipe 7 is stirred by the air introduced through the air supply pipe 8 and rises inside the air lift pipe 7, and is placed in the upper part of the overcoat 1. The washed material is discharged into the cleaning tank 9, where it is reused after cleaning. Note that the waste liquid after the cleaning is discharged to the outside of the system through the discharge pipe 10.
このように、従来の装置は、各筒体の通水面は
ともに垂直構造であるため、処理水量の増加を望
む場合であつても単に過塔の塔高を増加させれ
ばよく、従つて敷地面積の増大を要しないという
長所がある。しかしながら、材層が連続的に重
力方向へ移動するという方式であるため、濁質の
付着量は上部の材層より下部のそれの方が多く
なり、このため、塔高の増大につれて処理水質が
悪化するという問題を生じる。 In this way, in conventional equipment, the water flow surfaces of each cylinder have a vertical structure, so even if it is desired to increase the amount of water to be treated, it is only necessary to increase the height of the tower, and therefore the site It has the advantage of not requiring an increase in area. However, because the material layer continuously moves in the direction of gravity, the amount of suspended solids attached to the lower material layer is greater than that of the upper material layer, and as a result, the quality of treated water deteriorates as the tower height increases. This causes the problem of deterioration.
この考案の目的は、前記した従来技術の欠点を
解消し、処理水量を増大させる場合であつても、
敷地面積の増大をともなうことなく処理水質の悪
化を防止できる連続過装置を提供することにあ
る。 The purpose of this invention is to eliminate the drawbacks of the prior art described above, and even when increasing the amount of treated water,
An object of the present invention is to provide a continuous filtration device that can prevent deterioration of treated water quality without increasing the site area.
上記の目的を達成するため、この考案は、傾斜
板を多段状に配設して通水性の筒体としたものを
垂直方向に沿つて二重状に設け、該筒体間は材
充填部、その内外部は被処理水を材充填部へ向
け水平方向に供給するための散水部および過水
を受け入れるための散水部とし、かつ材の重力
方向への連続移動とこれにともなう再生を可能と
した連続過装置において、上記散水部に相当す
る筒体を構成する多段状の傾斜板を、隣接する傾
斜板の上端と下端とを結ぶ線分と水平面とのなす
角が、材を堆積させたときにその面がくずれず
に安定する最大傾斜角よりも大きくなるように配
設したことを特徴とする。 In order to achieve the above object, this invention consists of a water-permeable cylindrical body formed by arranging inclined plates in multiple stages, which are arranged in double form along the vertical direction, and between the cylindrical bodies is a material-filled section. The inner and outer parts are a water sprinkling part to horizontally supply water to be treated to the material filling part and a water sprinkling part to receive excess water, and also enable continuous movement of the material in the direction of gravity and regeneration associated with this. In a continuous filtration device, the angle formed by the horizontal plane and the line connecting the upper and lower ends of the adjacent inclined plates is arranged such that the multi-stage inclined plates constituting the cylinder corresponding to the water spraying section are used to deposit material. It is characterized by being arranged so that the angle of inclination is larger than the maximum angle at which the surface is stable without collapsing when the surface is tilted.
このような構成とすることにより、傾斜板相互
間の隙部から濁質を捕捉した材を散水部内へ流
入させるとともに、これをエアリフト管により回
収することが可能となり、これにより筒体を高く
して処理水量を増大させる場合であつても、濁質
の付着量増大により処理水質が悪化するという欠
点はなくなる。上記傾斜板相互間の線分と水平面
とのなす角は、材のを堆積させたときにその面
がくずれずに安定する最大傾斜角より大きい限
り、散水部の垂直方向に沿つて変化させる必要は
ないが、処理水質の悪化防止は捕捉した濁質付着
量の多い下方の材を回収する程、効果的に達成
されることから、下方の傾斜板になる程大きくす
ることが望ましい。 With this configuration, it is possible to flow the material that has captured suspended solids into the water spraying section from the gap between the inclined plates, and to collect this through the air lift pipe, thereby increasing the height of the cylindrical body. Even when the amount of water to be treated is increased, the disadvantage that the quality of the treated water deteriorates due to an increase in the amount of attached turbidity is eliminated. The angle between the line segment between the inclined plates and the horizontal plane must be varied along the vertical direction of the watering area, as long as it is greater than the maximum angle of inclination that will ensure that the surface is stable without collapsing when the material is deposited. However, since prevention of deterioration of treated water quality is achieved more effectively as the lower material with a larger amount of trapped suspended solids is recovered, it is desirable to increase the size of the lower inclined plate.
以下、図面に示す実施例によりこの考案をさら
に詳しく説明する。 This invention will be explained in more detail below with reference to embodiments shown in the drawings.
第2図は、第1図の傾斜板11Aに代えて適用
可能な傾斜板の部分拡大側断面を示すものであ
る。この傾斜板11Cにおいては相互の間隔が下
方へ向うにつれて順次拡大するように設定されて
いるが、このような設定は以下により行い得る。 FIG. 2 shows a partially enlarged side cross section of an inclined plate that can be applied in place of the inclined plate 11A of FIG. In this inclined plate 11C, the mutual spacing is set to gradually increase as it goes downward, but such setting can be done as follows.
すなわち、先づ、材が散水部3内へ流入する
ことを防止するに必要な傾斜板の最少長さL0は、
第2図からも明らかなように下記(1)式により与え
られる。 That is, first, the minimum length L 0 of the inclined plate necessary to prevent the material from flowing into the sprinkler section 3 is:
As is clear from FIG. 2, it is given by the following equation (1).
L0=p・cosα/(sinα・cosθ+cosα・sinθ)
…(1)
(式中、p、θおよびαは傾斜板の下端を同一
鉛直線に沿つて一致させた際に得られる値で、そ
れぞれ傾斜板のピツチ、傾斜板の傾斜角および
材を堆積させたときにその面がくずれずに安定す
る最大傾斜角を示す)
このL0は実際に用いられる傾斜板の長さLと
の比較において以下の意味を持つている。 L 0 =p・cosα/(sinα・cosθ+cosα・sinθ)
...(1) (where p, θ, and α are the values obtained when the lower ends of the inclined plates are aligned along the same vertical line, and are the pitch of the inclined plate, the inclination angle of the inclined plate, and the material deposited, respectively. (This indicates the maximum angle of inclination at which the surface remains stable without collapsing when the surface is tilted.) This L 0 has the following meaning in comparison with the length L of the inclined plate actually used.
L0−L≦0のとき:材が散水部へ流入する
ことはない。 When L 0 -L≦0: The material does not flow into the water sprinkling section.
L0−L>0のとき:材は散水部へ流入する。 When L 0 −L>0: the material flows into the water spraying section.
L0−Ln>0でかつLn=L1>L2>L3…のとき:
材はL1,L2,L3…となるにつれて順次散水部
への流入量が増大する。 When L 0 −Ln>0 and Ln=L 1 >L 2 >L 3 ...:
As the material becomes L 1 , L 2 , L 3 . . . , the amount of material flowing into the water sprinkling section increases sequentially.
従つて、上記の実施例においては、傾斜板の長
さLを下方へ向うにつれて順次短かくすればよい
ことが理解される。 Therefore, in the above embodiment, it is understood that the length L of the inclined plate may be gradually shortened as it goes downward.
このような構成の傾斜板11Cとすることによ
り、捕捉した濁質付着量の多い下方の材程多量
に散水部3内へ流入することとなる。そして上記
流入後の材は次いで散水部内を下方へ落下し、
最終的には散水部の外側を下方へ移動してくる
材と混合され、その後第1図の場合と同様にして
エアリフト管7内を上昇し、材洗浄槽9で洗浄
後再使用される。 With the inclined plate 11C having such a configuration, the lower the material with a larger amount of trapped suspended solids, the more the material will flow into the water sprinkling section 3. The material after flowing in then falls downward inside the water sprinkling section,
Finally, it is mixed with the material moving downward outside the water spraying section, and then ascends in the air lift pipe 7 in the same manner as in the case of FIG. 1, and is reused after being cleaned in the material cleaning tank 9.
以上の結果、下方の材層は捕捉した濁質付着
量の低減化が達成され、これにより処理水量の増
加のため塔高を増大させる場合であつても、処理
水質の悪化を防止することが可能となる。 As a result of the above, a reduction in the amount of trapped suspended solids attached to the lower material layer has been achieved, and as a result, even when the tower height is increased to increase the amount of treated water, deterioration of the quality of treated water can be prevented. It becomes possible.
以下、具体例によりこの考案の効果をさらに詳
しく説明する。 The effects of this invention will be explained in more detail below using specific examples.
具体例
下記の条件の下に濁質濃度20mg/の被処理水
を過処理した。Specific example: Under the following conditions, water to be treated with a turbidity concentration of 20 mg/was overtreated.
傾斜板
集水部:傾斜角80゜、ピツチ100mm、長さは既述
の(1)式で算出される必要最少長さL0の1.5
倍とし、全ての傾斜板につき一定とする
散水部:傾斜角80゜、長さは既述の(1)式で算出
される必要最少長さL0の1.0〜0.8倍とし、
下方になる程短かくする
筒体の高さ(層高):内部筒体および外部筒体
ともに4m
材:有効径1.0mmの砂(安息角は約35゜)
処理の結果、集水部に集められた過水中の濁
質濃度は2mg/以下となり、この値は比較のた
め散水部内へ材を流入させない以外は同様に実
施した場合の濁質濃度5mg/より大幅に改善さ
れることが明らかとななつた。Slanted plate Water collection part: Incline angle 80°, pitch 100mm, length is 1.5 of the required minimum length L 0 calculated using the formula (1) mentioned above.
Sprinkling section: Incline angle 80°, length 1.0 to 0.8 times the required minimum length L 0 calculated using formula (1) above,
The height of the cylinder (bed height): 4 m for both the inner cylinder and the outer cylinder Material: Sand with an effective diameter of 1.0 mm (angle of repose is approximately 35°) As a result of treatment, the water collection area The concentration of suspended solids in the collected overwater was less than 2 mg/, and it is clear that this value is significantly improved from the suspended solid concentration of 5 mg/ when the same procedure was carried out except that no material was allowed to flow into the watering section for comparison. It was a long time ago.
以上の説明はこの考案の典型的な実施例につい
て行つたものであるが、この考案はこれに限定さ
れるものではなく、例えば、前記の実施例では一
定値のpおよびθを基にしてL0を求め、このL0
からLを求める手順としたが、これに代えて一定
値のLおよびθからpを適当な値に定めることも
でき(傾斜板の相互間隔は一定となる)、同様な
効果が得られる。要は、隣接する傾斜板の上端と
下端とを結ぶ線分と水平面とのなす角が、材を
堆積させたときにその面がくずれずに安定する最
大傾斜角αよりも大きくなるように各傾斜板を配
設すれば、傾斜板間から材を散水部へ流入させ
ることができる。また、過塔の横断面は円形に
限ることはなく、正方形や矩形と含む任意の形状
でもよい。さらに、内部筒体と外部筒体の機能を
逆転させ、前者を集水部、後者を散水部とするこ
ともできる。 Although the above explanation has been made regarding a typical embodiment of this invention, this invention is not limited to this. For example, in the above embodiment, L is calculated based on constant values of p and θ. Find 0 , this L 0
Although the procedure for calculating L from the above is used, instead of this, p can be set to an appropriate value from constant values L and θ (the mutual spacing between the inclined plates is constant), and the same effect can be obtained. The key is to set each slope so that the angle formed by the horizontal plane and the line connecting the top and bottom ends of adjacent sloped plates is greater than the maximum slope angle α that will ensure that the surface is stable without collapsing when the material is piled up. By providing inclined plates, material can flow into the water spraying section from between the inclined plates. Furthermore, the cross section of the tower is not limited to a circular shape, and may have any shape including a square or a rectangle. Furthermore, the functions of the inner cylindrical body and the outer cylindrical body can be reversed, and the former can be used as a water collection part and the latter as a water sprinkling part.
以上、この考案によれば、散水部に相当する筒
体を構成する多段状の傾斜板を、隣接する傾斜板
の上端と下端とを結ぶ線分と水平面とのなす角
が、材を堆積させたときにその面がくずれずに
安定する最大傾斜角よりも大きくなるように配設
したことにより、濁質を捕捉した材、特にその
付着量が大きい下方の材を散水部内へ流入させ
るとともに、これを良好に再生使用することが可
能となり、また下方の材層における捕捉した濁
質付着量を軽減することができる。その結果、処
理水量の増加のため塔高を増大させる場合であつ
ても、処理水質の悪化を防止することが可能とな
る。 As described above, according to this invention, the angle between the horizontal plane and the line connecting the upper and lower ends of the adjacent inclined plates of the multi-stage inclined plates constituting the cylindrical body corresponding to the water sprinkling section allows the material to be deposited. By arranging it so that the angle of inclination is greater than the maximum angle at which the surface remains stable without collapsing when the water is exposed to water, the material that has captured suspended solids, especially the lower material with a large amount of adhesion, flows into the water spraying section, and It becomes possible to recycle and reuse this material well, and it is also possible to reduce the amount of trapped suspended solids attached to the lower material layer. As a result, even when the tower height is increased to increase the amount of treated water, it is possible to prevent the quality of the treated water from deteriorating.
第1図は、従来の連続過装置の側断面図、第
2図は、第1図の装置に適用可能なこの考案の実
施例に係る散水部傾斜板の部分拡大側断面図であ
る。
1……過塔、2……材層、3……散水部、
4……集水部、7……エアリフト管、9……材
洗浄槽、11A,11B,11C……傾斜板、1
2……内部筒体、13……外部筒体。
FIG. 1 is a side sectional view of a conventional continuous filtration device, and FIG. 2 is a partially enlarged side sectional view of an inclined plate of a water spraying section according to an embodiment of this invention applicable to the device of FIG. 1... Passing tower, 2... Material layer, 3... Watering part,
4... Water collection section, 7... Air lift pipe, 9... Material cleaning tank, 11A, 11B, 11C... Inclined plate, 1
2...Inner cylinder, 13...Outer cylinder.
Claims (1)
たものを垂直方向に沿つて二重状に設け、該筒
体間は材充填部、その内外部は被処理水を
材充填部へ向け水平方向に供給するための散水
部および過水を受け入れるための集水部と
し、かつ材の重力方向への連続移動とこれに
ともなう再生を可能とした連続過装置におい
て、上記散水部に相当する筒体を構成する多段
状の傾斜板を、隣接する傾斜板の上端と下端と
を結ぶ線分と水平面とのなす角が、材を堆積
させたときにその面がくずれずに安定する最大
傾斜角よりも大きくなるように配設したことを
特徴とする連続過装置。 (2) 実用新案登録請求の範囲第1項において、前
記隣接する傾斜板の上端と下端とを結ぶ線分と
水平面とのなす角が、下部の傾斜板になる程大
きくしたことを特徴とする連続過装置。[Scope of Claim for Utility Model Registration] (1) Water-permeable cylinders formed by arranging inclined plates in multiple stages are provided in a double form along the vertical direction, and between the cylinders there is a material filling part, The inner and outer parts are a water sprinkling part to horizontally supply water to be treated to the material filling part, and a water collection part to receive excess water, and also enable continuous movement of the material in the direction of gravity and regeneration associated with this. In a continuous filtration device, the angle formed by the horizontal plane and the line connecting the upper and lower ends of the adjacent inclined plates is arranged such that the multi-stage inclined plates constituting the cylinder corresponding to the water spraying section are used to deposit material. A continuous filtration device characterized in that the continuous filtration device is arranged so that the angle of inclination is larger than the maximum angle at which the surface is stable without collapsing when the surface is tilted. (2) Utility model registration Claim 1 is characterized in that the angle formed by the horizontal plane and the line segment connecting the upper and lower ends of the adjacent inclined plates is made larger as the lower inclined plates become closer to each other. Continuous passing device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13151283U JPS6039310U (en) | 1983-08-25 | 1983-08-25 | Continuous filtration device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13151283U JPS6039310U (en) | 1983-08-25 | 1983-08-25 | Continuous filtration device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6039310U JPS6039310U (en) | 1985-03-19 |
JPH022406Y2 true JPH022406Y2 (en) | 1990-01-22 |
Family
ID=30297293
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13151283U Granted JPS6039310U (en) | 1983-08-25 | 1983-08-25 | Continuous filtration device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6039310U (en) |
-
1983
- 1983-08-25 JP JP13151283U patent/JPS6039310U/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS6039310U (en) | 1985-03-19 |
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