JPH01215315A - Solid-liquid separation device - Google Patents

Solid-liquid separation device

Info

Publication number
JPH01215315A
JPH01215315A JP4071688A JP4071688A JPH01215315A JP H01215315 A JPH01215315 A JP H01215315A JP 4071688 A JP4071688 A JP 4071688A JP 4071688 A JP4071688 A JP 4071688A JP H01215315 A JPH01215315 A JP H01215315A
Authority
JP
Japan
Prior art keywords
water
treated
solid
side wall
sand
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.)
Pending
Application number
JP4071688A
Other languages
Japanese (ja)
Inventor
Tetsuo Nishida
哲夫 西田
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 JP4071688A priority Critical patent/JPH01215315A/en
Publication of JPH01215315A publication Critical patent/JPH01215315A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To efficiently separate suspended matters, sand, etc., by floating up the suspended matters and organic substances in the water to be treated to separate in a dust collecting chamber, etc., by utilizing hydraulic properties, and settling down solids such as sand in the water to be treated by utilizing the hydraulic properties. CONSTITUTION:An inlet port 4 is provided on the side wall 2 of a retardation vessel 1 consisting of the side wall 2 of circular or square shape and a bottom plate 3. An outlet port 6 is disposed at the lower position of the side wall than that of the inlet port 4 or at the bottom plate. A retaining chamber 9 opened at the liquid surface position in the retardation vessel to introduce the suspended matters, etc., in the liquid surface, and the dust collecting chamber 10 connected with the retaining chamber 9 to recover and separate the suspended matters introduced to the retaining chamber are provided on the outside of the retardation vessel 1. As a result, the water to be treated containing suspended matters, solids such as sand, and organic substamces, as seen in service water the source of which is the surface flowing water in a river, in industrial water, or in sewage water during a rain fall, is efficiently treated at a low cost to separate suspended matters, organic substances and solids such as sand from the treated water.

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
固形物、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、砂等の固形物とを分離する固液分
離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 substances, organic substances, etc., and separates the treated water from solid substances such as floating substances, organic substances, and sand.

[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] In general, 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,
Screens etc. are 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
めの機械装置が複雑で高価となるという欠点があった。
[Problem to be solved by the invention] However, in the conventional sand settling basin method, the sand contains a large amount of organic matter, making it difficult to lift and wash the sand, and the mechanical equipment for this purpose becomes complicated and expensive. There was a drawback.

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、メツシュを細くしなければならな
いため、スクリーンが目詰まりしやすいという欠点があ
った。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、沈澱物を取除く機械装置が複雑で、高価となるとい
う欠点があった。
Further, in the removal method using a screen, the screen has to be made thinner in order to remove even minute floating particles, which has the disadvantage that the screen is easily clogged. In addition, the sedimentation tank method has the disadvantage 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 mechanical equipment 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、木理的特性
をうまく利用して浮上させ、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、これらの固形物を木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 is capable of efficiently removing suspended matter and organic matter contained in water to be treated by making good use of the woody properties of the water. 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 good use of their woody properties. The purpose is to provide a solid-liquid separation device.

[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、円形状或は四角形
状の側壁と底板からなる減速槽の側壁に、被処理水を供
給する流入口を設け、その流入口より低い位置の側壁若
しくは底板に、処理水を排出する流出口を設けると共に
、その減速槽の外側に、減速槽内の液面位に開口して液
面上の浮遊物等を導く滞流室と、その滞流室に接続して
滞流室内に導かれた浮遊物等を回収分離する集塵室を設
けて、固液分離装置を構成したことを特徴とするもので
ある。
[Means for Solving the Problems] In order to solve the above problems, the present invention provides an inlet for supplying water to be treated on the side wall of a moderation tank consisting of a circular or square side wall and a bottom plate, and An outlet for discharging the treated water is provided on the side wall or bottom plate at a position lower than the inlet, and a stagnation outlet is provided outside the deceleration tank that opens at the liquid level in the deceleration tank to guide floating objects on the liquid surface. A solid-liquid separator is constructed by providing a flow chamber and a dust collection chamber that is connected to the flow chamber and collects and separates suspended matter introduced into the flow chamber.

なお、上記固液分離装置には、減速槽の中心部に、垂直
軸回りに回転する円筒状或は円板上の二次流強制回転体
を設けてもよく、その場合には、二次流強制回転体の上
端を可撓性接手を介して駆動源と接続して、下端の軸受
を省略することができる。
In addition, the solid-liquid separator described above may be provided with a cylindrical or disc-shaped secondary flow forcing rotating body that rotates around a vertical axis in the center of the deceleration tank. The upper end of the flow forcing rotor can be connected to the drive source via a flexible joint, and the bearing at the lower end can be omitted.

[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槽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
面上を浮遊して滞流室に導かれ、集塵室で回収分離され
ることになる。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。このとき、二次流強制回転体を回
転させれば、減速槽内に発生する二次流が強くなり、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。
[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 deceleration tank through the inlet is
The speed is decelerated in the deceleration tank, and solid matter such as sand contained in the water to be treated settles and is 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 and are led to the retention chamber, where they are collected and separated in the dust collection chamber. Further, the treated water after solid matter such as sand, floating matter, organic matter, etc. have been removed from the water to be treated is discharged from the outlet. At this time, if the secondary flow forcing rotating body is rotated, the secondary flow generated in the deceleration tank will become stronger, and the separation of solid matter such as sand, suspended matter, organic matter, etc. will be promoted.

又、二次流強制回転体は、回転時に複雑な流れの影響を
受けて微妙に振動するが、二次流強制回転体の下端の軸
受が省略されていると、軸受が振動によって故障するこ
とはないばかりか、二次流強制回転体の上端に作用する
振動は、可撓性接手によって許容されるので、二次流強
制回転体はスムーズに回転されることになる。
In addition, the secondary flow forced rotating body vibrates slightly due to the influence of complex flows when rotating, but if the bearing at the lower end of the secondary flow forced rotating body is omitted, the bearing may fail due to vibration. Not only is there no vibration, but the vibration acting on the upper end of the secondary flow forcing rotor is tolerated by the flexible joint, so the secondary flow forcing rotor is rotated smoothly.

[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の平面図
で、第2図、第3図及び第4図は、それぞれ第1図に示
す矢視A−A線、B−B線及びC−C線に沿って切断し
た断面図である。
FIG. 1 is a plan view of a solid-liquid separator showing one embodiment of the present invention, and FIGS. 2, 3, and 4 are arrow views A-A and B-B shown in FIG. 1, respectively. FIG. 4 is a cross-sectional view taken along line C-C.

図中1は減速槽で、円形状の側壁2と底板3から構成さ
れている。4は減速槽lの側壁2に設けられた被処理水
W′を供給する流入口で、流入管5と接続されている。
In the figure, 1 is a deceleration tank, which is composed of a circular side wall 2 and a bottom plate 3. Reference numeral 4 denotes an inlet provided on the side wall 2 of the deceleration tank l for supplying the water to be treated W', and is connected to the inlet pipe 5.

6は流入口4より低い位置の側壁2に設けられた、処理
水Wを排出する流出口で、流出路7を介して流出管8と
接続されている。
Reference numeral 6 denotes an outlet for discharging the treated water W, which is provided on the side wall 2 at a position lower than the inlet 4, and is connected to an outlet pipe 8 via an outlet passage 7.

9は減速槽lの外側に設置された滞流室で、減速槽1内
の液面位に開口し、液面上の浮遊物等を導くようになっ
ている。10は滞流室9に接続して設けられた集塵室で
、集塵室10内には、滞流室9内に導かれた浮遊物等を
回収分離する、回転ドラムスクリーン又は除塵カゴ等の
回収分離装置11が設置されている。なお、12は滞流
室9と集塵室10との接続部に設けられたゲートで、こ
のゲート12を開ければ、滞流室9内に導かれた浮遊物
等が、集塵室lO内の回収分離装置ll内に導かれるよ
うになっている。
Reference numeral 9 denotes a retention chamber installed outside 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 on the liquid surface. Reference numeral 10 denotes a dust collection chamber connected to the retention chamber 9. Inside the dust collection chamber 10, there is a rotating drum screen, a dust removal basket, etc., for collecting and separating floating matter introduced into the retention chamber 9. A recovery and separation device 11 is installed. Reference numeral 12 is a gate provided at the connection between the retention chamber 9 and the dust collection chamber 10. When this gate 12 is opened, floating objects etc. introduced into the retention chamber 9 are removed from the dust collection chamber IO. It is designed to be guided into the recovery and separation device 11.

13は集塵室10に接続して設けられた集水室で、集塵
室lOと集水室13は連通口14を介して連通されてお
り、回収分離装置11によって分離された処理水Wが、
集水室13に集水されるようになっている。15は集水
室13内に集水された処理水Wを、補助管16を介して
流出管8に放流する補助ポンプである。
Reference numeral 13 denotes a water collection chamber connected to the dust collection chamber 10. The dust collection chamber lO and the water collection chamber 13 are communicated through a communication port 14, and the treated water W separated by the recovery and separation device 11 is but,
Water is collected into a water collection chamber 13. Reference numeral 15 denotes an auxiliary pump that discharges the treated water W collected in the water collection chamber 13 into the outflow pipe 8 via the auxiliary pipe 16.

上記構成よりなる本実施例の固液分離装置においては、
流入管5より流入口4を介して減速槽1内に供給された
被処理水W′は、減速槽l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 example having the above configuration,
The water to be treated W' supplied into the deceleration tank 1 from the inflow pipe 5 through the inlet 4 is decelerated while circulating in the deceleration tank l, and the sand etc. contained in the water to be treated W' is removed. The solids 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、液面上を浮遊して滞流室9に導かれることになる。
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 9.

滞流室9に導かれた浮遊物や有機物等がある程度たまっ
たら、ゲー)12を開にして、集塵室10内に設置され
ている回収分離装置ll内に導き、浮遊物や有機物等を
回収分離する。浮遊物や有機物等の回収分離を終えたら
、再びゲート12を閉にする。この時、集水室13には
、回収分離装置11によって分離された処理水Wが、し
だいに貯水されることになる。
When the suspended matter and organic matter introduced into the retention chamber 9 have accumulated to a certain extent, the gate 12 is opened and the suspended matter and organic matter are guided into the collection and separation device ll installed in the dust collection chamber 10, and the suspended matter and organic matter are removed. Collect and separate. After completing the recovery and separation of floating matter, organic matter, etc., the gate 12 is closed again. At this time, the treated water W separated by the recovery and separation device 11 is gradually stored in the water collection chamber 13.

なお、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より流出路
7、流出管8を介して排出されることになる。又、集水
室13内にある程度の処理水Wが貯水されたならば、そ
の処理水Wは補助ポンプ15を駆動することになり、補
助管16を介して流出管8に放流され、処理水Wと共に
排出されることになる。
In addition, the treated water W after solids such as sand, suspended matter, organic matter, etc. have been removed from the treated water W′ is discharged from the outlet 6 via the outlet passage 7 and the outlet pipe 8. Become. Moreover, once a certain amount of treated water W is stored in the water collection chamber 13, the treated water W will drive the auxiliary pump 15, and will be discharged to the outflow pipe 8 via the auxiliary pipe 16, and the treated water W will be discharged into the outflow pipe 8 through the auxiliary pipe 16. It will be discharged together with W.

次に、第5図は本発明の別の実施例を示す固液分離装置
の平面図である。
Next, FIG. 5 is a plan view of a solid-liquid separator showing another embodiment of the present invention.

第1図に示す実施例においては、減速槽1の側壁2を円
形状に形成しているが1本実施例で示すように、減速槽
1′の側壁2′を四角形に形成してもよい。
In the embodiment shown in FIG. 1, the side wall 2 of the deceleration tank 1 is formed in a circular shape, but the side wall 2' of the deceleration tank 1' may be formed in a square shape as shown in this embodiment. .

又、第1図に示す実施例においては、流入口4より低い
位置の側壁2に、処理水Wを排出する流出口6を設けて
いるが、本実施例で示すように、底板3′に処理水Wを
排出する流出口6′を設けてもよい。
Further, in the embodiment shown in FIG. 1, an outlet 6 for discharging treated water W is provided in the side wall 2 at a position lower than the inlet 4, but as shown in this embodiment, an outlet 6 is provided in the bottom plate 3'. An outlet 6' for discharging the treated water W may be provided.

又、第1図及び第5図に示す各実施例において、流入管
5内を流れる被処理水W′中に、浮上性及び有機物等に
対する吸着性の強い添加物17を、均一に混合させるよ
うにしておけば、固液分離性能が一段と向上することは
言うまでもない。
Furthermore, in each of the embodiments shown in FIGS. 1 and 5, the additive 17, which has strong floating properties and strong adsorption properties for organic matter, is mixed uniformly into the water to be treated W' flowing in the inflow pipe 5. It goes without saying that if this is done, the solid-liquid separation performance will be further improved.

なお、第5図中、第1図に示す部材に対応する部材には
同一符号を付し、重複した説明は省略する。
In FIG. 5, members corresponding to those shown in FIG. 1 are designated by the same reference numerals, and redundant explanation will be omitted.

次に、第6図及び第7図は、それぞれ本発明の他の実施
例を示す固液分離装置の減速槽の断面図である。
Next, FIGS. 6 and 7 are sectional views of a moderating tank of a solid-liquid separator showing other embodiments of the present invention, respectively.

第6図に示す実施例は、減速槽1の中心部に、垂直軸回
りに回転する円筒状の二次法強制回転体18を設けた例
を示し、第7図に示す実施例は。
The embodiment shown in FIG. 6 shows an example in which a cylindrical quadratic forced rotation body 18 that rotates about a vertical axis is provided in the center of the deceleration tank 1, and the embodiment shown in FIG.

減速槽1の中心部に、垂直軸回りに回転する円板状の二
次法強制回転体18′を設けた例を示す。
An example is shown in which a disk-shaped quadratic forced rotation body 18' that rotates around a vertical axis is provided in the center of the deceleration tank 1.

このように、減速槽1の中心部に二次法強制回転体18
.18’を設けて、それを垂直軸回りに回転させると、
流入管5より減速槽l内に導かれた被処理水W′の一次
流れS+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ため、きわめて好都
合である。又、上記円筒状或は円板上の二次法強制回転
体18.18’の表面等に、凹凸や透孔等を多数設けて
おけば、発生する二次流れS2を一段と強くすることが
できる。
In this way, the quadratic forced rotation body 18 is placed in the center of the deceleration tank 1.
.. 18' and rotate it around the vertical axis,
With respect to the primary flow S+ of the water to be treated W' led into the deceleration tank l from the inflow pipe 5, the secondary flow S2 generated in the vertical direction becomes stronger, and the sand, etc. contained in the water to be treated W' becomes stronger. This is extremely advantageous because it facilitates the separation of solid matter, suspended matter, organic matter, etc. Furthermore, if a large number of irregularities, through holes, etc. are provided on the surface of the cylindrical or disk-shaped secondary force rotation body 18, 18', the generated secondary flow S2 can be further strengthened. can.

又、第6図及び第7図に示す実施例においては、二次法
強制回転体18.18’の上端が、ユニバーサルジゴイ
ント等の可撓性接手19を介して、駆動源20であるモ
ータに接続されているが、二次法強制回転体18.18
’の下端は、軸受が省略されてフリーとなっている。
In the embodiment shown in FIGS. 6 and 7, the upper end of the quadratic forced rotation body 18, 18' is connected to the motor, which is the drive source 20, via a flexible joint 19 such as a universal gigo-point. is connected to the quadratic forced rotation body 18.18
The lower end of ' is free because the bearing is omitted.

これは、二次法強制回転体18.18’は、回転時に複
雑な流れの影響を受けて微妙に振動するため、軸受によ
り支持すると、軸受が振動によって短時間で故障しやす
いのと、二次法強制回転体18.18’の下端は、軸受
構造が複雑となるばかりか、常時液面下にあり、保守点
検がしすらいため、下端の軸受を省略し、逆に上端を可
撓性接手19を介して駆動源20に接続したところ、二
次流強制回転体18.18’に作用する振動は、可撓性
接手19によって効果的に吸収され、下端の軸受がなく
ても、二次流強制回転体18゜18′は、液面下で比較
的安定してスムーズに回転されることが確認され、安心
して採用が可能となったものである。
This is because the quadratic forced rotating body 18, 18' vibrates slightly due to the influence of complex flows when rotating, so if it is supported by a bearing, the bearing is likely to break down in a short period of time due to vibration. The lower end of the forced rotating body 18.18' not only has a complicated bearing structure, but also is always under the liquid level, making maintenance and inspection difficult. Therefore, the lower end bearing is omitted, and the upper end is made flexible. When connected to the drive source 20 through the joint 19, the vibrations acting on the secondary flow forcing rotating body 18, 18' are effectively absorbed by the flexible joint 19, and even without the lower end bearing, the It has been confirmed that the downstream forced rotating body 18°18' rotates relatively stably and smoothly under the liquid surface, and can be used with confidence.

次に、第8図及び第9図は、それぞれ本発明のさらに他
の実施例を示す固液分離装置の減速槽の断面図である。
Next, FIGS. 8 and 9 are sectional views of a moderating tank of a solid-liquid separator, respectively, showing still other embodiments of the present invention.

第8図に示す実施例は、減速槽1の底板3の中央部に、
固形物溜り21を設けると共に、第6図に示す円筒状の
二次流強制回転体18の中心部に、下端が固形物溜り2
1に臨む固形物排出用円筒22を、二次流強制回転体1
8と一体に設け、その固形物排出用円筒22を固形物の
汲み上げ用通路として利用したもので、本実施例におい
ては、その固形物排出用円筒22内に、固形物溜り21
に溜った固形物を汲み上げるためのポンプ23が内蔵さ
れている。
In the embodiment shown in FIG. 8, in the center of the bottom plate 3 of the deceleration tank 1,
In addition to providing a solid matter reservoir 21, a solid matter reservoir 21 is provided at the lower end at the center of the cylindrical secondary flow forced rotating body 18 shown in FIG.
The solid matter discharge cylinder 22 facing the secondary flow forced rotating body 1
8 and the solid matter discharge cylinder 22 is used as a passage for pumping up the solid matter.In this embodiment, the solid matter reservoir 21 is provided in the solid matter discharge cylinder 22.
A pump 23 is built in to pump up solid matter accumulated in the tank.

又、第9図に示す実施例は、減速槽1の底板3の中央部
に、固形物溜り21を設けると共に、第7図に示す円板
状の二次流強制回転体1B’の中心部に、下端が固形物
溜り21に臨む固形物排出用円筒22を、二次流強制回
転体18’と一体に設け、その固形物排出用円筒22を
固形物の排出用通路として利用したもので、本実施例に
おいては、その固形物排出用円筒22内に、固形物溜り
21に溜った固形物を汲み上げるためのスパイラル羽根
24が内蔵されている。
Further, in the embodiment shown in FIG. 9, a solid matter reservoir 21 is provided at the center of the bottom plate 3 of the deceleration tank 1, and a center portion of the disk-shaped secondary flow forced rotation body 1B' shown in FIG. A solid matter discharge cylinder 22 whose lower end faces the solid matter reservoir 21 is provided integrally with the secondary flow forced rotating body 18', and the solid matter discharge cylinder 22 is used as a solid matter discharge passage. In this embodiment, a spiral blade 24 for pumping up the solids accumulated in the solids reservoir 21 is built into the solids discharge cylinder 22 .

又、第8図及び第9図に示す各実施例において、25は
固形物排出用円筒22の上端より排出される固形物を受
ける受樋で、受樋25により受は取られた固形物は、図
示せざる排出路を介して減速槽1の外側に導かれるよう
になっている。
In each of the embodiments shown in FIGS. 8 and 9, 25 is a receiving gutter for receiving solids discharged from the upper end of the solid material discharge cylinder 22, and the solids received by the receiving gutter 25 are , is led to the outside of the deceleration tank 1 via a discharge path (not shown).

なお、第8図に示す実施例においては、円筒状の二次流
強制回転体18の径が小さい場合には、固形物排出用円
筒22を、円筒状の二次流強制回転体18と兼用させる
ことができる。。但し、その場合には、固形物排出用円
筒22の表面に、凹凸等を設けることはできるが、透孔
は下部の一部に設けても良いが上部には設けない方が良
い。
In the embodiment shown in FIG. 8, when the diameter of the cylindrical secondary flow forced rotation body 18 is small, the solid matter discharge cylinder 22 is also used as the cylindrical secondary flow forced rotation body 18. can be done. . However, in that case, the surface of the solid matter discharge cylinder 22 can be provided with irregularities, and although the through holes may be provided in a part of the lower part, it is better not to provide them in the upper part.

又、第9図に示すスパイラル羽根24を、第8図に示す
固形物排出用円筒22内に内蔵せしめてもよく、逆に第
8図に示すポンプ23を、第9図に示す固形物排出用円
筒22内に内蔵せしめてもよい。
Further, the spiral vane 24 shown in FIG. 9 may be built into the solid matter discharge cylinder 22 shown in FIG. 8, or conversely, the pump 23 shown in FIG. It may be built into the cylinder 22 for use.

このように、固形物排出用円筒22内に、ポンプ23又
はスパイラル羽根24を内蔵させて、固形物排出用円筒
22内を固形物22の汲み上げ用通路として利用すれば
、減速槽1の底板の下部に、固形物溜り21に溜った固
形物を排出させるための通路や排出装置を竣設する必要
がなく、基礎工事等も非常に簡単となり、きわめて好都
合である。
In this way, if the pump 23 or the spiral blade 24 is built into the solid matter discharge cylinder 22 and the inside of the solid matter discharge cylinder 22 is used as a passage for pumping up the solid matter 22, the bottom plate of the deceleration tank 1 can be There is no need to construct a passageway or a discharge device in the lower part for discharging the solid matter accumulated in the solid matter reservoir 21, and the foundation work etc. are also very simple, which is extremely convenient.

[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浮遊物や有機物等を
、木理的特性をうまく利用して浮上させ、これらを順次
滞流槽や集塵室に導いて回収分離することにより、効率
よく取除くことができると共に、被処理水中に含まれて
いる砂等の固形物を、木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、安価で取扱いも容易
である。
[Effects of the Invention] As specifically explained above, according to the solid-liquid separator of the present invention, floating matter, organic matter, etc. contained in the water to be treated are brought to the surface by making good use of the woody properties. By sequentially guiding them to a retention tank or a dust collection room to collect and separate them, they can be efficiently removed, and solids such as sand contained in the water to be treated can be removed by changing their wood grain characteristics. It can be effectively used to settle and be removed, and it is inexpensive and easy to handle.

又、減速槽の中心部に設けた二次流強制回転体を回転さ
せると、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、有機物等の分離をさらに促進させるこ
とができる。
In addition, by rotating the secondary flow forcing rotating body installed in the center of the deceleration tank, the secondary flow effective for solid-liquid separation becomes stronger, further separating solids such as sand, suspended matter, organic matter, etc. It can be promoted.

又、二次流強制回転体は、回転時に複雑な流れの影響を
受けて微妙に振動するが、二次流強制回転体の上端を可
撓性接手を介して駆動源と接続することにより、振動を
吸収し、二次流強制回転体の下端の軸受を省略すること
ができるので、振動によって故障しやすい軸受の使用を
避けることができ、二次流強制回転体の回転もスムーズ
で、長期間安定した運転が可能となり、保守・点検等も
容易、である。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、有機物等の除去する上で、実
用上きわめて有効な固液分離装置を提供し得るものであ
る。
In addition, the secondary flow forced rotation body vibrates slightly due to the influence of complicated flows when rotating, but by connecting the upper end of the secondary flow forced rotation body to the drive source via a flexible joint, Since it absorbs vibrations and eliminates the need for a bearing at the lower end of the secondary flow forced rotation body, it is possible to avoid the use of bearings that are prone to failure due to vibration, and the rotation of the secondary flow forced rotation body is smooth and long-lasting. It enables stable operation for a long period of time, and maintenance and inspection are easy. With these advantages, it is possible to provide a solid-liquid separator that is extremely effective in practice for removing solid matter such as sand, suspended matter, organic matter, etc. contained in water to be treated.

【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の平面図
で、第2図、第3図及び第4図は、それぞれ第1図に示
す矢視A−A線、B−B線及びC−C線に沿って切断し
た断面図、第5図は本発明の別の実施例を示す固液分離
装置′の平面図、第6図及び第7図は、それぞれ本発明
の他の実施例を示す固液分離装置の減速槽の断面図で、
第8図及び第9図は、それぞれ本発明のさらに他の実施
例を示す固液分離装置の断面図である。 1.1′・・・減速槽、   2.2′・・・側壁、3
.3′・・・底板、     4.4′・・・流入口、
5・・・流入管、      6,6′・・・流出口、
7・・・流出路、      8・・・流出管、9・・
・滞流室、       10・・・集塵室、11・・
・回収分離装置、   12・・・ゲート、13・・・
集水室、     14・・・連通口、15・・・補助
ポンプ、    16・・・補助管、17・・・添加物
、 18.18’・・・二次流強制回転体、19・・・可撓
性接手、    2・・・駆動源、21・・・固形物溜
り、 22・・・固形物排出用円筒、23・・・ポンプ、24
・・・スパイラル羽根、  25・・・受樋、W′・・
・被処理水、    W、w・・・処理水、Sl・・・
−次流れ、     S2・・・二次流れ。 A」
FIG. 1 is a plan view of a solid-liquid separator showing one embodiment of the present invention, and FIGS. 2, 3, and 4 are arrow views A-A and B-B shown in FIG. 1, respectively. 5 is a plan view of a solid-liquid separator' showing another embodiment of the present invention, and FIGS. 6 and 7 are cross-sectional views taken along line C-C. A cross-sectional view of a moderation tank of a solid-liquid separator showing an example of
FIGS. 8 and 9 are cross-sectional views of solid-liquid separators showing still other embodiments of the present invention. 1.1'...Deceleration tank, 2.2'...Side wall, 3
.. 3'...bottom plate, 4.4'...inlet,
5... Inflow pipe, 6,6'... Outlet,
7... Outflow path, 8... Outflow pipe, 9...
・Retention chamber, 10...dust collection chamber, 11...
・Recovery separation device, 12...gate, 13...
Water collection chamber, 14... Communication port, 15... Auxiliary pump, 16... Auxiliary pipe, 17... Additive, 18.18'... Secondary flow forced rotating body, 19... Flexible joint, 2... Drive source, 21... Solid matter reservoir, 22... Solid matter discharge cylinder, 23... Pump, 24
...Spiral blade, 25...Gutter, W'...
・Water to be treated, W, w... Treated water, Sl...
-Secondary flow, S2...Secondary flow. A”

Claims (1)

【特許請求の範囲】 1)、円形状或は四角形状の側壁と底板からなる減速槽
の側壁に、被処理水を供給する流入口を設け、その流入
口より低い位置の側壁若しくは底板に、処理水を排出す
る流出口を設けると共に、その減速槽の外側に、減速槽
内の液面位に開口して液面上の浮遊物等を導く滞流室と
、その滞流室に接続して滞流室内に導かれた浮遊物等を
回収分離する集塵室を設けたことを特徴とする固液分離
装置。 2)、減速槽の中心部に、垂直軸回りに回転する円筒状
或は円板状の二次流強制回転体を設けたたことを特徴と
する第1請求項記載の固液分離装置。 3)、二次流強制回転体の上端が可撓性接手を介して駆
動源と接続され、二次流強制回転体の下端の軸受が省略
されていることを特徴とする第2請求項記載の固液分離
装置。
[Scope of Claims] 1) An inlet for supplying the water to be treated is provided on the side wall of the moderation tank consisting of a circular or square side wall and a bottom plate, and the side wall or the bottom plate at a position lower than the inlet is provided with an inlet, In addition to providing an outlet for discharging the treated water, a retention chamber is provided outside the deceleration tank that opens at the liquid level in the deceleration tank to guide floating matter on the liquid surface, and is connected to the retention chamber. A solid-liquid separator characterized by being provided with a dust collection chamber for collecting and separating floating matter etc. introduced into the retention chamber. 2) The solid-liquid separator according to claim 1, further comprising a cylindrical or disc-shaped secondary flow forced rotating body that rotates around a vertical axis, provided in the center of the moderation tank. 3) Claim 2 characterized in that the upper end of the secondary flow forced rotation body is connected to the drive source via a flexible joint, and the bearing at the lower end of the secondary flow forced rotation body is omitted. solid-liquid separation equipment.
JP4071688A 1988-02-25 1988-02-25 Solid-liquid separation device Pending JPH01215315A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4071688A JPH01215315A (en) 1988-02-25 1988-02-25 Solid-liquid separation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4071688A JPH01215315A (en) 1988-02-25 1988-02-25 Solid-liquid separation device

Publications (1)

Publication Number Publication Date
JPH01215315A true JPH01215315A (en) 1989-08-29

Family

ID=12588311

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4071688A Pending JPH01215315A (en) 1988-02-25 1988-02-25 Solid-liquid separation device

Country Status (1)

Country Link
JP (1) JPH01215315A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03127678A (en) * 1989-10-11 1991-05-30 Tetsuo Nishida Liquid treating device, method and device for continuously treating liquid thereof

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5241576B2 (en) * 1973-01-17 1977-10-19
JPS5739690B2 (en) * 1975-07-31 1982-08-23

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5241576B2 (en) * 1973-01-17 1977-10-19
JPS5739690B2 (en) * 1975-07-31 1982-08-23

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03127678A (en) * 1989-10-11 1991-05-30 Tetsuo Nishida Liquid treating device, method and device for continuously treating liquid thereof

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