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JPH0570481B2 - - Google Patents
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JPH0570481B2 - - Google Patents

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Publication number
JPH0570481B2
JPH0570481B2 JP4071788A JP4071788A JPH0570481B2 JP H0570481 B2 JPH0570481 B2 JP H0570481B2 JP 4071788 A JP4071788 A JP 4071788A JP 4071788 A JP4071788 A JP 4071788A JP H0570481 B2 JPH0570481 B2 JP H0570481B2
Authority
JP
Japan
Prior art keywords
secondary flow
solids
center
solid matter
solid
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 - Lifetime
Application number
JP4071788A
Other languages
Japanese (ja)
Other versions
JPH01215316A (en
Inventor
Tetsuo Nishida
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP4071788A priority Critical patent/JPH01215316A/en
Publication of JPH01215316A publication Critical patent/JPH01215316A/en
Publication of JPH0570481B2 publication Critical patent/JPH0570481B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は河川表流水を水源とする上水や、産業
用水及び降雨時における都市域の排水の様に、浮
遊物や、砂等の固形、有機物等を含んだ被処理水
を処理して、処理水と、浮遊物や有機物、砂等の
固形とを分離する固液分離装置及びそれ用の二次
流強制装置に関するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention is applicable to clean water sourced from river surface water, industrial water, and wastewater in urban areas during rainfall, such as suspended solids and solids such as sand. The present invention relates to a solid-liquid separator that processes water to be treated containing organic matter and separates the treated water from suspended matter, organic matter, sand, and other solids, and a secondary flow forcing device for the same.

[従来の技術] 一般に、被処理水に含まれている浮遊物や、砂
等の固形物、有機物等を除去するには、従来、沈
砂池や沈澱池、スクリーン等が使用されている。
[Prior Art] Generally, in order to remove floating matter, solid matter such as sand, organic matter, etc. contained in water to be treated, a settling basin, a sedimentation basin, a screen, etc. are conventionally used.

[発明が解決しようとする課題] ところが、従来の沈砂池方式では、沈砂に有機
物が多く含まれてしまうため、揚砂や洗砂がしず
らく、そのための機構装置が複雑で高価となると
いう欠点があつた。又、スクリーンによる除去方
式では、微細な浮遊物まで除去しようとすると、
メツシユを細くしなければならないため、スクリ
ユーンが目詰まりしやすいという欠点があつた。
又、沈澱池方式では、除去物の比重が比較的軽い
場合には、沈澱池の面積を大きくする必要がある
ばかりか、沈澱物を取除く機構装置が複雑で、高
価となるという欠点があつた。
[Problems to be solved by the invention] However, in the conventional sand settling basin method, the sand contains a lot of organic matter, making it difficult to lift and wash the sand, and the mechanical equipment for this purpose is complicated and expensive. There were flaws. Also, with the removal method using a screen, if you try to remove even minute floating particles,
Since the mesh had to be made thinner, the screen had the disadvantage that it was more likely to become clogged.
In addition, the sedimentation tank method has disadvantages in that when the specific gravity of the removed material is relatively light, not only is it necessary to increase the area of the sedimentation tank, but the mechanism for removing the sediment is complicated and expensive. Ta.

本発明は上記従来の欠点に鑑みて提案されたも
ので、被処理水中に含まれている浮遊物や有機物
を、水理的特性をうまり利用して浮上させ、効率
よく取除くことができると共に、被処理水中に砂
等の固形物が含まれている場合には、これらの固
形物を水理的特性をうまく利用して沈降させ、効
率よく取除くことができる、安価で取扱いの容易
な固液分離装置及びそれ用の二次流強制装置を提
供せんとするものである。
The present invention was proposed in view of the above-mentioned conventional drawbacks, and it is possible to efficiently remove suspended matter and organic matter contained in the water to be treated by levitating them by making good use of hydraulic characteristics. In addition, if the water to be treated contains solids such as sand, it is an inexpensive and easy-to-handle method that can effectively remove these solids by making use of its hydraulic properties to settle them. The present invention aims to provide a solid-liquid separation device and a secondary flow forcing device for the same.

[課題を解決するための手段] 本発明は上記課題を解決するために、円形状或
はインボリユーム状の外壁と、中心部に固型物溜
りを有する底板からなる減速槽の外壁に、被処理
水の流入口と処理水の流出口を設けると共に、減
速槽の中心部には、垂直に回転する円筒状の一部
又は全部を電磁波を生じる材料で形成した二次流
強制回転体を設け、その二次流強制回転体の中心
部に、下端が固形物溜りに臨む固形物排出用円筒
を、二次流強制回転体と一体に設けて、固液分離
装置を構成したことを特徴とするのである。
[Means for Solving the Problems] In order to solve the above problems, the present invention provides an outer wall of a moderation tank consisting of a circular or involume-shaped outer wall and a bottom plate having a solid matter reservoir in the center. In addition to providing an inlet for treated water and an outlet for treated water, a vertically rotating cylindrical secondary flow forced rotating body made of a material that generates electromagnetic waves is provided in the center of the deceleration tank. , a solid-liquid separation device is constructed by providing a cylinder for discharging solids whose lower end faces the solids reservoir in the center of the secondary flow forcing rotor, integrally with the secondary flow forcing rotor. That's what I do.

なお、有機物の分離浮上を促進させるために、
二次流強制回転体の一部又は全部に電磁波を生じ
る材料を使用したり、脱臭効果を上げるために、
二次流強制回転体に消臭材を内装させてもよい。
In addition, in order to promote the separation and flotation of organic matter,
In order to use materials that generate electromagnetic waves in part or all of the secondary flow forced rotating body, or to increase the deodorizing effect,
A deodorizing material may be incorporated into the secondary flow forced rotating body.

又、固形物を汲み上げるためのポンプ又はスパ
イラル羽根は、上記二次流強制装置の二次流強制
回転体の中心部に一体的に設けられた固形物排出
用円筒内に内蔵させることができ、その二次流強
制装置を有する固液分離装置に、汲み上げられた
固形物を受ける受樋を、固形物排出用円筒の上端
部外周に設けて、この受樋と、減速槽の外側に設
けられた固形物受室とを、案内樋で接続しておけ
ば、汲み上げた固形物を簡単に除去することがで
きる。
Further, the pump or spiral vane for pumping up the solids can be built into a solids discharge cylinder integrally provided in the center of the secondary flow forcing rotating body of the secondary flow forcing device, In the solid-liquid separator having the secondary flow forcing device, a receiving gutter for receiving the pumped solids is provided on the outer periphery of the upper end of the cylinder for discharging solids, and a receiving gutter and a receiving gutter are provided on the outside of the deceleration tank. If the solid matter receiving chamber is connected with a guide trough, the solid matter that has been pumped up can be easily removed.

[作用] 本発明の固液分離装置は上記のように構成され
ているので、流入口を介して減速層内に供給され
た被処理水は、減速槽内で減速され、被処理水中
に含まれていた砂等の固形物は、沈降して底板上
に堆積されることになる。他方、被処理水中に含
まれていた浮遊物や有機物等は、液面上を浮遊す
る。又、被処理水中から砂等の固形物や浮遊物、
有機物等が除去された後の処理水は、流出口より
排出されることになる。なお、減速槽の中心部で
は、円筒状の二次流強制回転体、或は固形物排出
用円筒を兼用した円筒状の二次流強制回転体の回
転によつて、減速槽内の固液分離に有効な縦方向
の二次流が強くなり、砂等の固形物や、浮遊物、
有機物等の分離が促進されることになる。又底板
上に堆積した固形物は、二次流によつて中心部の
固形物溜りに集められ、二次流強制回転体の中心
部に設けられている固形物排出用円筒を介して汲
み上げ可能となる。
[Function] Since the solid-liquid separator of the present invention is configured as described above, the water to be treated that is supplied into the moderation layer through the inlet is decelerated in the moderation tank, and the water contained in the water to be treated is decelerated. Solids such as sand will settle and be deposited on the bottom plate. On the other hand, floating matter, organic matter, etc. contained in the water to be treated float on the liquid surface. In addition, solid matter such as sand and suspended matter are removed from the water being treated.
The treated water after organic substances and the like have been removed will be discharged from the outlet. In addition, in the center of the moderation tank, the solid and liquid in the moderation tank is The vertical secondary flow, which is effective for separation, becomes stronger and solids such as sand, suspended matter,
Separation of organic matter etc. will be promoted. In addition, the solids deposited on the bottom plate are collected in the solids reservoir in the center by the secondary flow, and can be pumped up through the solids discharge cylinder provided at the center of the secondary flow forced rotating body. becomes.

なお、二次流強制回転体の一部又は全部に、電
磁波を生じる材料が使用されていると、減速槽の
中心部に集まりやすい有機物等に集中的に電磁波
が照射され、電磁波によつて有機物等の分離浮上
が促進されることになる。
In addition, if a material that generates electromagnetic waves is used in part or all of the secondary flow forced rotating body, the electromagnetic waves will be intensively irradiated to organic matter that tends to collect in the center of the deceleration tank, and the organic matter will be destroyed by the electromagnetic waves. Separation and flotation of these objects will be promoted.

又、二次流強制回転体に消臭材が内装されてい
れば、減速槽の中心部に集まつた有機部等の臭気
が消臭されることになる。
Furthermore, if a deodorizing material is installed in the secondary flow forcing rotating body, the odor of organic parts etc. that has gathered in the center of the deceleration tank will be deodorized.

又、減速槽の底板上に堆積して中央部の固形物
溜りに溜められた固形物は、固形物排出用円筒内
に内蔵されたポンプ又はスパイラル羽根によつて
汲み上げられ、汲み上げられた固形物は、固形物
排出用円筒の上端部外周に設けられた受樋によつ
て受けられ、案内樋を介して減速槽の外側に設け
られている固形物受室へ順次導かれることにな
る。
In addition, the solids deposited on the bottom plate of the deceleration tank and stored in the solids reservoir in the center are pumped up by the pump or spiral vanes built into the solids discharge cylinder, and the solids are pumped up. is received by a receiving gutter provided on the outer periphery of the upper end of the solid material discharge cylinder, and is sequentially guided to a solid material receiving chamber provided outside the deceleration tank via the guide gutter.

[実施例] 以下、本発明を図面に示す実施例に基づいて具
体的に説明する。
[Example] Hereinafter, the present invention will be specifically described based on an example shown in the drawings.

第1図は本発明の1実施例を示す固液分離装置
及びそれ用の二次流強制装置の断面図で、第2図
及び第3図は、その固液分離装置の異なる配置を
示す平面図である。
FIG. 1 is a sectional view of a solid-liquid separator and a secondary flow forcing device for the same, showing one embodiment of the present invention, and FIGS. 2 and 3 are plan views showing different arrangements of the solid-liquid separator. It is a diagram.

図中1は減速槽で、円形状或はインボリユート
状の外壁2と底板3から構成されている。
In the figure, 1 is a deceleration tank, which is composed of a circular or involute outer wall 2 and a bottom plate 3.

なお、第4図A,B,Cは、それぞれ形状の異
なる減速槽1の断面図であるが、減速槽1の底板
3の中心部には、固形物溜り4が設けられてい
る。第4図Aは底板3が水平な基準断面形で、第
4図Bは底板3が中心下り形で、又第4図Cは底
隅を解消した中心上り形の形状を示し、どのタイ
プの形状を採用するかは、底板3上に堆積される
固形物の性状や、減速槽1内の流れ状態等を配慮
して、最適の形状のものが検討され、場合によつ
ては、他の形状のものを採用してもよい。又、側
壁2の形状は、第4図Bで示すように、一部を縮
径させる等、必要に応じ変形させ、減速槽1内の
流れ状態が最適になるように設計することができ
る。但し、第1図に示す実施例は、第4図Aに示
す基準断面形の底板3を使用した場合を示し、以
下これについて説明する。
Note that FIGS. 4A, B, and C are cross-sectional views of deceleration tanks 1 having different shapes, and a solid matter reservoir 4 is provided in the center of the bottom plate 3 of the deceleration tank 1. Figure 4A shows the standard cross-sectional shape with the bottom plate 3 horizontal, Figure 4B shows the bottom plate 3 with the center down, and Figure 4C shows the bottom corner with the center up. When deciding which shape to adopt, the optimum shape is considered, taking into account the properties of the solids deposited on the bottom plate 3, the flow conditions in the deceleration tank 1, etc., and in some cases, other shapes may be selected. You may adopt the shape. Further, the shape of the side wall 2 can be deformed as necessary, such as by reducing the diameter of a part of the side wall 2, as shown in FIG. 4B, and can be designed to optimize the flow condition within the deceleration tank 1. However, the embodiment shown in FIG. 1 shows a case where the bottom plate 3 having the standard cross-sectional shape shown in FIG. 4A is used, and this will be described below.

図中5は減速槽1の外壁に設けられた、被処理
水W′の流入口で、6は処理水Wの流出口である。
In the figure, 5 is an inlet for the water to be treated W' provided on the outer wall of the deceleration tank 1, and 6 is an outlet for the treated water W.

なお、流入口5及び流出口6の配置は、第2図
に示すように、被処理水W′の流入口5に対し、
処理水Wの流出口6が、減速槽1内の一次流れS1
に沿つて、三直角位置に配置してもよく、或は第
3図に示すように、四直角位置に配置してもよ
い。但し、流入口5に対し、流出口6をある程度
高い位置に配置し、流入と流出の流れが互いに干
渉しないように配慮する。
In addition, the arrangement of the inlet 5 and the outlet 6 is as shown in FIG.
The outflow port 6 of the treated water W is the primary flow S 1 in the deceleration tank 1
They may be arranged in three orthogonal positions along the same line, or they may be arranged in four orthogonal positions as shown in FIG. However, care should be taken to arrange the outlet 6 at a somewhat higher position than the inlet 5 so that the inflow and outflow flows do not interfere with each other.

次に、7は減速槽1の外側に設けらてた滞溜室
で、減速槽1内の液面位に開口し、液面上に浮遊
する浮遊物等が導かれるようになつている。8は
液面上に浮遊する浮遊物等をせき止めて滞溜室に
向わせる遮流板で、クシ歯状にスリツト等が設け
られており、減速槽1の液面位に半径方向に配置
されている。
Next, reference numeral 7 denotes a retention chamber provided on the outside of the deceleration tank 1, which opens at the level of the liquid level in the deceleration tank 1, and is designed to guide floating objects and the like floating on the liquid surface. Reference numeral 8 denotes a flow shielding plate that dams up floating matter floating on the liquid surface and directs it toward the retention chamber, and is provided with comb-shaped slits, etc., and is arranged in the radial direction at the liquid level of the deceleration tank 1. has been done.

9は減速槽1の中心部に設けられた、垂直軸回
りに回転する円筒状の二次流強制回転体で、その
中心部には、下端が固形物溜り4に臨む固形物排
出用円筒10が、二次流強制回転体9と一体に設
けられている。但し、二次流強制回転体9の径が
小さい場合には、固形物排出用円筒10を円筒状
の二次流強制回転体と兼用させることができる。
Reference numeral 9 denotes a cylindrical secondary flow forced rotating body that rotates around a vertical axis and is provided at the center of the deceleration tank 1. At the center thereof, there is a cylinder 10 for discharging solids whose lower end faces the solids reservoir 4. is provided integrally with the secondary flow forcing rotating body 9. However, when the diameter of the secondary flow forcing rotor 9 is small, the solid matter discharge cylinder 10 can also be used as the cylindrical secondary flow forcing rotor.

11はユニバーサルジヨイント等の可撓性接手
で、二次流強制回転体9の上端は、この可撓性接
手11を介して駆動源12のモータと接続されて
おり、二次流強制回転体9の下端の軸受は省略さ
れて、二次流強制装置が構成されている。
11 is a flexible joint such as a universal joint, and the upper end of the secondary flow forced rotation body 9 is connected to the motor of the drive source 12 via this flexible joint 11, and the secondary flow forced rotation body The bearing at the lower end of 9 is omitted to constitute a secondary flow forcing device.

13は二次流強制回転体9の上部外周に設けら
れた中空部である。又、14は固形物排出用円筒
10の下端外周に設けられた掻き板で、固形物溜
り4内の隅部に溜つた固形物を掻きならし、固形
物排出用円筒10の下端の開口部に導くようにな
つている。
Reference numeral 13 denotes a hollow portion provided on the upper outer periphery of the secondary flow forcing rotating body 9. Further, reference numeral 14 denotes a scraping plate provided on the outer periphery of the lower end of the cylinder 10 for discharging solids, which scrapes the solids accumulated in the corners of the solids reservoir 4 and opens the opening at the lower end of the cylinder 10 for discharging solids. It is designed to lead to

15は固形物排出用円筒10の上端から排出さ
れる固形物を受る受樋で、固形物排出用円筒10
の上端部外周にドーナツ状に設けられており、固
形物排出用円筒10の上端部には、そこから排出
される固形物を受樋15に導くための、皿をふせ
たような案内板16が設けられている。
15 is a receiving gutter that receives solids discharged from the upper end of the solids discharge cylinder 10;
A guide plate 16, which is provided in a donut shape on the outer periphery of the upper end and has a plate-covered shape, is provided at the upper end of the solid matter discharge cylinder 10 to guide the solid matter discharged therefrom to the receiving gutter 15. is provided.

17は減速槽1を外側に設けられた固形物受室
で、受樋15と固形物受室17とは、案内樋18
を介して接続されている。
17 is a solid matter receiving chamber provided with the deceleration tank 1 outside, and the receiving gutter 15 and the solid matter receiving chamber 17 are connected to the guide gutter 18.
connected via.

なお、第5図及び第6図は、二次流強制装置
の、それぞれ異なる内部構造を示す断面図であ
る。
Note that FIGS. 5 and 6 are cross-sectional views showing different internal structures of the secondary flow forcing device.

第5図に示す実施例は、第1図に示す固形物排
出用円筒10内に、固形物溜り4に溜つた固形物
を汲み上げるためのスパイラル羽根19を内蔵さ
せた例を示し、第6図に示す実施例は、スパイラ
ル羽根19に代えて、固形物排出用円筒10の下
部に、固形物を汲み上げるためのポンプ20を内
蔵させた例を示す。
The embodiment shown in FIG. 5 shows an example in which a spiral blade 19 for pumping up the solids accumulated in the solids reservoir 4 is built into the solids discharge cylinder 10 shown in FIG. The embodiment shown in FIG. 1 shows an example in which a pump 20 for pumping up solid matter is built into the lower part of the solid matter discharge cylinder 10 instead of the spiral vane 19.

但し、二次流制御回転体9は、第6図に示すよ
うに逆梯形円筒状に形成し、減速槽1内における
固液分離に有効な二次流れS2を発生を、さらに促
進させるようにしてもよい。
However, the secondary flow control rotating body 9 is formed in an inverted trapezoidal cylindrical shape as shown in FIG . You can also do this.

なお、第7図は二次流強制回転体9の断面図で
ある。第7図に示すように、二次流強制回転体9
の内外周面に、凹部a、凸部b,c、透孔d等を
設けておけば、二次流れS2の発生をさらに促進さ
せることができる。なお、固形物排出用円筒10
を、二次流強制回転体9と兼用させる場合には、
透孔dや内周面の凸部cを設けることができな
い。
Note that FIG. 7 is a sectional view of the secondary flow forced rotation body 9. As shown in FIG. 7, the secondary flow forced rotating body 9
By providing recesses a, protrusions b and c, through holes d, etc. on the inner and outer circumferential surfaces of the inner and outer circumferential surfaces, the generation of the secondary flow S2 can be further promoted. In addition, the solid matter discharge cylinder 10
When used also as the secondary flow forced rotating body 9,
It is not possible to provide a through hole d or a convex portion c on the inner peripheral surface.

但し、二次流強制回転体9の一部である凸部b
や全部に、セラミツクや磁石のように電磁波を生
じる材料を使用し、有機物等の浮上分離を促進さ
せてもよい。
However, the convex portion b which is a part of the secondary flow forced rotating body 9
A material that generates electromagnetic waves, such as ceramics or magnets, may be used for the entire structure to promote flotation and separation of organic substances.

又、二次流強制回転体9に、フミン系等の消臭
材を内装させて、有機物等の臭気を消臭させても
よい。
Further, the secondary flow forcing rotating body 9 may be provided with a deodorizing material such as a humic material to eliminate odors such as organic substances.

なお、固液分離効率をさらに向上させるため
に、浮上性及び有機物等を対する吸着性の強い添
加物21を供給する場合には、第2図で示すよう
に、上流の被処理水W′中に供給して、均一に混
合させるようにすることが望ましい。
In addition, in order to further improve the solid-liquid separation efficiency, when supplying an additive 21 that has strong floating properties and adsorption properties for organic substances, etc., as shown in Fig. 2, it is necessary to add It is desirable to mix the mixture uniformly.

上記構成よりなる本実施例の固液分離装置にお
いては、流入口5より減速槽1内に供給された被
処理水W′は、減速槽1内を回る間に減速され、
被処理水W′中に含まれていた砂等の固形物は、
沈降して底板3上に堆積されることになる。
In the solid-liquid separator of this embodiment having the above-described configuration, the water to be treated W' supplied into the deceleration tank 1 from the inlet 5 is decelerated while circulating inside the deceleration tank 1,
Solids such as sand contained in the water to be treated W′ are
It will settle and be deposited on the bottom plate 3.

他方、被処理水W′中に含まれていた浮遊物や
有機物等は、液面上を浮遊し、遮流板8によつて
滞溜室7に導かれ分離されることになる。
On the other hand, floating matter, organic matter, etc. contained in the water to be treated W' float on the liquid surface and are led to the retention chamber 7 by the flow shield plate 8 and separated therefrom.

又、被処理水W′中から砂等の固形物や浮遊物、
有機物等が除去された後の処理水Wは、流出口6
を介して排出されることになる。
In addition, solid matter such as sand and suspended matter,
The treated water W from which organic matter has been removed flows through the outlet 6.
It will be discharged through.

なお、このとき、減速層1内の中心部では、二
次流強制回転体9が垂直軸回りに回転されるの
で、減速層1内に導かれた被処理水W′の一次流
れS1に対し、縦方向に発生する二次流れS2が強く
なり、被処理水W′中に含まれている砂等の固形
物や浮遊物、有機物等の分離が促進されることに
なる。
At this time, at the center of the moderation layer 1, the secondary flow forcing rotating body 9 is rotated around the vertical axis, so that the primary flow S1 of the water to be treated W' guided into the moderation layer 1 is On the other hand, the secondary flow S 2 generated in the vertical direction becomes stronger, and the separation of solid matter such as sand, suspended matter, organic matter, etc. contained in the water to be treated W' is promoted.

又、底板3上に沈降して堆積された砂等の固形
物は、発生した二次流れS2によつて底板3の中心
部の固形物溜り4に集められ、固形物排出用円筒
10の内部に内蔵されたスパイラル羽根19又は
ポンプ20により、順次汲み上げられることにな
る。又、こうして汲み上げられた砂等の固形物
は、固形物排出用円筒10の上端より排出され、
案内板16を介して受樋15に導かれた後、案内
樋18を介して固形物受室17に導かれ、分離さ
れることになる。
In addition, solid matter such as sand that has settled and accumulated on the bottom plate 3 is collected in the solid matter reservoir 4 at the center of the bottom plate 3 by the generated secondary flow S2 , and is collected in the solid matter reservoir 4 at the center of the bottom plate 3, and is collected in the solid matter reservoir 4 at the center of the solid matter discharge cylinder 10. The water is successively pumped up by the internal spiral blade 19 or pump 20. Moreover, the solid matter such as sand that has been pumped up in this way is discharged from the upper end of the solid matter discharge cylinder 10,
After being guided to the receiving trough 15 via the guide plate 16, the solids are guided to the solids receiving chamber 17 via the guide trough 18 and separated.

[発明の効果] 以上具体的に説明したように、本発明の固液分
離装置によれば、被処理水中に含まれている砂等
の固形物を、水理的特性をうまく利用して沈降さ
せ、効率よく取除くことができ、さらに、減速槽
の中心部に設けた二次流強制回転体の回転によつ
て、固液分離に有効な二次流が強くなり、砂等の
固形物や、浮遊物、有機物等の分離を促進するこ
とができ、固形物溜りに溜つた砂等の固形物は、
二次流強制回転体と一体に設けた固形物排出用円
筒を介して排出させることができるので、構造が
簡単で安価に製作することができ、取扱いも容易
である。
[Effects of the Invention] As specifically explained above, according to the solid-liquid separator of the present invention, solids such as sand contained in the water to be treated are sedimented by making good use of hydraulic characteristics. In addition, the rotation of the secondary flow forcing rotating body installed in the center of the deceleration tank strengthens the secondary flow that is effective for solid-liquid separation, and solids such as sand can be removed efficiently. It can promote the separation of suspended matter, organic matter, etc., and solid matter such as sand accumulated in the solid matter reservoir can be removed.
Since the solid matter can be discharged through the solid matter discharge cylinder provided integrally with the secondary flow forcing rotary body, the structure is simple, it can be manufactured at low cost, and it is easy to handle.

又、二次流強制回転体の一部又は全部に、電磁
波を生じる材料を使用することにより、有機物等
を分離をさらに促進させることができる。
Furthermore, by using a material that generates electromagnetic waves for part or all of the secondary flow forced rotating body, it is possible to further promote the separation of organic substances and the like.

又、二次流強制回転体に、消臭材を内装させる
ことにより、有機物等の臭気を効果的に消臭させ
ることができる。
Further, by incorporating a deodorizing material into the secondary flow forced rotating body, odors such as organic substances can be effectively deodorized.

又、固形物を汲み上げるためのポンプやスパイ
ラル羽根は、二次流強制回転体の中心部に一体的
に設けられた固形物排出用円筒内に内蔵させるこ
とにより、固液分離装置用の二次流強制装置をよ
りコンパクトに設計することが可能となるばかり
か、特にスパイラル羽根を内蔵させた場合には、
二次流強制回転体の回転によつて、自動的に固形
物溜り内に溜つた固形物を汲み上げることができ
る。又、本発明の固形分離装置においては、上記
のような二次流強制装置を有し、かつ、固形物排
出用円筒の上端部外周に設けた受樋によつて、固
形排出用円筒の上端から排出される固形物を受
け、案内樋を介して固形物受室に導くようにして
いるので、固形物排出用円筒の上端から排出させ
る固形物を、きわめて簡単な機構で分離除去する
ことができ、固形物排出路用の基礎工事を省略す
ることができる。等の利点を有し、被処理水に含
まれている砂等の固形物や浮遊物、有機物等を除
去する上で、実用上きわめて有効な固液分離装置
及びそれ用の二次流強制装置を提供し得るもので
ある。
In addition, the pump and spiral vanes for pumping up solids are built into the solids discharge cylinder that is integrally provided in the center of the secondary flow forcing rotating body, so that the secondary flow for the solid-liquid separation device is Not only is it possible to design the flow forcing device more compactly, but especially when a spiral blade is built in,
By rotating the secondary flow forcing rotating body, the solids accumulated in the solids reservoir can be automatically pumped up. Further, the solid separator of the present invention has the secondary flow forcing device as described above, and the upper end of the solid discharge cylinder is Since the solids discharged from the cylinder are received and guided to the solids receiving chamber through the guide gutter, the solids discharged from the upper end of the solids discharge cylinder can be separated and removed using an extremely simple mechanism. It is possible to omit the foundation work for the solids discharge channel. A solid-liquid separation device and a secondary flow forcing device for the same, which have the following advantages and are extremely effective in practice in removing solid matter such as sand, floating matter, organic matter, etc. contained in water to be treated. It is possible to provide

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の1実施例を示す固液分離装置
及びそれ用の二次流強制装置の断面図で、第2図
及び第3図は、その固液分離装置の異なる配置を
示す平面図、第4図A,B,Cは、それぞれ形状
の異なる減速槽の断面図、第5図及び第6図は、
本発明の二次流強制装置のそれぞれ異なる内部構
造を示す断面図、第7図は二次流強制回転体の断
面図である。 1……減速槽、2……外壁、3……底板、4…
…固形物溜り、5……流入口、6……流出口、7
……滞溜室、8……遮流板、9……二次流強制回
転体、10……固形物排出用円筒、11……可撓
性継手、12……駆動源、13……中空部、14
……掻き板、15……受樋、16……案内板、1
7……固形物受室、18……案内樋、19……ス
パイラル羽根、20……ポンプ、21……添加
物、a……凹部、b,c……凸部、d……透孔、
W′……被処理水、W……処理水、S1……一次流
れ、S2……二次流れ。
FIG. 1 is a sectional view of a solid-liquid separator and a secondary flow forcing device for the same, showing one embodiment of the present invention, and FIGS. 2 and 3 are plan views showing different arrangements of the solid-liquid separator. Figures 4A, B, and C are cross-sectional views of moderation tanks with different shapes, and Figures 5 and 6 are
FIG. 7 is a sectional view showing the different internal structures of the secondary flow forcing device of the present invention, and FIG. 7 is a sectional view of the secondary flow forcing rotating body. 1... Speed reduction tank, 2... Outer wall, 3... Bottom plate, 4...
...Solid matter reservoir, 5...Inflow port, 6...Outflow port, 7
... Retention chamber, 8 ... Current shielding plate, 9 ... Secondary flow forced rotating body, 10 ... Cylinder for discharging solids, 11 ... Flexible joint, 12 ... Drive source, 13 ... Hollow Part, 14
...Scraping board, 15...Gutter, 16...Information board, 1
7... Solids receiving chamber, 18... Guide trough, 19... Spiral vane, 20... Pump, 21... Additive, a... Concave portion, b, c... Convex portion, d... Through hole,
W'...Water to be treated, W...Water to be treated, S1 ...Primary flow, S2 ...Secondary flow.

Claims (1)

【特許請求の範囲】 1 円形状或はインボリユーム状の外壁と、中心
部に固型物溜りを有する底板からなる減速槽の外
壁に、被処理水の流入口と処理水の流出口を設け
ると共に、減速槽の中心部には、垂直に回転する
円筒状の一部又は全部を電磁波を生じる材料で形
成した二次流強制回転体を設け、その二次流強制
回転体の中心部に、下端が固形物溜りに臨む固形
物排出用円筒を、二次流強制回転体と一体に設け
たことを特徴とする固液分離装置。 2 円形状或はインボリユーム状の外壁と、中心
部に固型物溜りを有する底板からなる減速槽の外
壁に、被処理水の流入口と処理水の流出口を設け
ると共に、減速槽の中心部には、垂直に回転する
消臭材を内装した円筒状の二次流強制回転体を設
け、その二次流強制回転体の中心部に、下端が固
形物溜りに臨む固形物排出用円筒を、二次流強制
回転体と一体に設けたことを特徴とする固液分離
装置。 3 円形状或はインボリユーム状の外壁と、中心
部に固型物溜りを有する底板からなる減速槽の外
壁に、被処理水の流入口と処理水の流出口を設け
ると共に、減速槽の中心部には、垂直に回転する
円筒状の二次流強制回転体を設け、その二次流強
制回転体の中心部に、下端に固形物を扱み上げる
ためのポンプを内蔵した固形物排出用円筒を固形
物溜りに臨ませ、二次流強制回転体と一体に設け
たことを特徴とする固液分離装置用の二次流強制
装置。 4 前記請求項3においてポンプの代わりに固形
物排出用円筒内に固形物を扱み上げるスパイラル
羽根を内蔵したことを特徴とする固液分離装置。 5 円形状或はインボリユーム状の外壁と、中心
部に固形物溜りを有する底板からなる減速槽の外
壁に、被処理水の流入口と処理水の流出口を設け
ると共に、減速槽の中心部には、垂直に回転する
円筒状を二次流強制回転体を設け、その二次流強
制回転体の中心部に、下端が固形物溜りに臨む固
形物排出用円筒を、二次流強制回転体と一体に設
け、固形物排出用円筒の上端部外周に、固形物排
出用円筒の上端から排出される固形物を受ける受
樋を設けると共に、減速槽の外側に固形物受室を
設け、受樋と固形物受室を案内樋で接続したこと
を特徴とする固液分離装置用の二次流強制装置。
[Claims] 1. An inlet for water to be treated and an outlet for treated water are provided on the outer wall of a moderation tank consisting of a circular or involume outer wall and a bottom plate having a solid matter reservoir in the center. At the same time, a vertically rotating cylindrical secondary flow forced rotating body made of a material that generates electromagnetic waves is provided in the center of the deceleration tank, and at the center of the secondary flow forced rotating body, A solid-liquid separator characterized in that a cylinder for discharging solids whose lower end faces a solids reservoir is provided integrally with a secondary flow forcing rotating body. 2 An inlet for treated water and an outlet for treated water are provided on the outer wall of the moderation tank, which consists of a circular or involume-shaped outer wall and a bottom plate with a solid matter reservoir in the center, and the center of the moderation tank is The section is equipped with a cylindrical secondary flow forced rotation body containing a vertically rotating deodorizing material, and a solid matter discharge cylinder whose lower end faces the solid matter reservoir is installed in the center of the secondary flow forced rotation body. A solid-liquid separator characterized in that it is integrated with a secondary flow forced rotating body. 3 An inlet for treated water and an outlet for treated water are provided on the outer wall of the moderation tank, which consists of a circular or involume-shaped outer wall and a bottom plate with a solid matter reservoir in the center, and the center of the moderation tank is The section is equipped with a vertically rotating cylindrical secondary flow forced rotating body, and a solid matter discharge system is installed in the center of the secondary flow forced rotary body, with a built-in pump at the lower end for handling solid matter. A secondary flow forcing device for a solid-liquid separator, characterized in that a cylinder faces a solid matter reservoir and is provided integrally with a secondary flow forcing rotating body. 4. A solid-liquid separator according to claim 3, characterized in that a spiral vane for lifting up solids is built into the cylinder for discharging solids instead of the pump. 5 An inlet for treated water and an outlet for treated water are provided on the outer wall of the moderation tank, which consists of a circular or involume-shaped outer wall and a bottom plate with a solids reservoir in the center, and the central part of the moderation tank is A vertically rotating cylindrical secondary flow forced rotating body is provided, and a cylinder for discharging solids with its lower end facing the solids reservoir is placed in the center of the secondary flow forced rotating body. A receiving gutter is provided on the outer periphery of the upper end of the solid matter discharging cylinder to receive the solids discharged from the upper end of the solid matter discharging cylinder, and a solid matter receiving chamber is provided on the outside of the deceleration tank, A secondary flow forcing device for a solid-liquid separator, characterized in that a receiving gutter and a solids receiving chamber are connected by a guide gutter.
JP4071788A 1988-02-25 1988-02-25 Solid-liquid separation device and its secondary flow forcing unit Granted JPH01215316A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4071788A JPH01215316A (en) 1988-02-25 1988-02-25 Solid-liquid separation device and its secondary flow forcing unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4071788A JPH01215316A (en) 1988-02-25 1988-02-25 Solid-liquid separation device and its secondary flow forcing unit

Publications (2)

Publication Number Publication Date
JPH01215316A JPH01215316A (en) 1989-08-29
JPH0570481B2 true JPH0570481B2 (en) 1993-10-05

Family

ID=12588344

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4071788A Granted JPH01215316A (en) 1988-02-25 1988-02-25 Solid-liquid separation device and its secondary flow forcing unit

Country Status (1)

Country Link
JP (1) JPH01215316A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2614554B2 (en) * 1991-06-24 1997-05-28 哲夫 西田 Water treatment equipment

Also Published As

Publication number Publication date
JPH01215316A (en) 1989-08-29

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