JPH0262282B2 - - Google Patents

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Publication number
JPH0262282B2
JPH0262282B2 JP62011916A JP1191687A JPH0262282B2 JP H0262282 B2 JPH0262282 B2 JP H0262282B2 JP 62011916 A JP62011916 A JP 62011916A JP 1191687 A JP1191687 A JP 1191687A JP H0262282 B2 JPH0262282 B2 JP H0262282B2
Authority
JP
Japan
Prior art keywords
raw water
tank
sludge
container body
separator
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
JP62011916A
Other languages
Japanese (ja)
Other versions
JPS63182009A (en
Inventor
Masatake Kano
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.)
SUIREI KK
Original Assignee
SUIREI KK
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 SUIREI KK filed Critical SUIREI KK
Priority to JP1191687A priority Critical patent/JPS63182009A/en
Publication of JPS63182009A publication Critical patent/JPS63182009A/en
Publication of JPH0262282B2 publication Critical patent/JPH0262282B2/ja
Granted legal-status Critical Current

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  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Description

【発明の詳細な説明】 「産業上の利用分野〕 本発明は、主として場所打杭、地中壁構築、泥
水シールド等土木工事により生じる汚泥水その他
産業廃水等を清澄化する装置に関し、その目的と
するところは、優れた分離機能を備えた小型化さ
れた汚泥水の固液分離装置を提供することにあ
る。
[Detailed Description of the Invention] "Industrial Application Field" The present invention relates to an apparatus for clarifying sludge water and other industrial wastewater generated mainly from civil engineering works such as driving-in-place piles, underground wall construction, and muddy water shielding. The purpose of this invention is to provide a compact solid-liquid separation device for sludge water that has an excellent separation function.

「従来の技術」 従来この主土木工事に伴なう汚泥水を清澄化す
る装置としては、現実問題として適切なものがな
く、プール方式による自然沈降方式とか、海中又
は山中への投棄方式等とかが採用されていた。そ
れがために装置の大型化と工事現場で大きな占有
面積をとること。またコストが嵩むこと等幾多の
問題点があつた。そこでこれらの改良として数種
の技術文献が散見される。例えば特公昭61−
46163号の汚泥脱水処理装置があり、その要旨は、
留箱に一定レベルで配設された周辺がストレーナ
となつている回転ドラムと、この回転ドラムには
ジエツトポンプと連通された吸引管が配設されて
いるとともに、この回転ドラムに濾布ベルトを捲
装してなる構成で、この濾布ベルトの表面で、吸
着汚泥を剥離除去することを特徴とするものであ
る。また特公昭61−32078号の汚泥水の固液分離
装置および装置があり、その要旨は、配管の途中
に分流混合羽根を備えたミキサーを数基配設する
とともに、これらのミキサーにそれぞれ薬品槽を
連通し、前記配管に連通された固液分離槽にスク
リユーウコンベヤを立設するとともに、このスク
リユーコンベヤの螺旋翼の面に接してその回転に
伴なつて回転する掻揚補助羽根を配設してなるも
のであり、そのミキサーによるフロツクの積極的
な生成と、固液分離槽で分離されたフロツク群を
スクリユーコンベヤと掻揚補助羽根で確実に排出
することにある。
``Conventional technology'' Conventionally, there is no suitable device for clarifying sludge water associated with main civil engineering works, and there are methods such as natural sedimentation using a pool method, or dumping into the sea or mountains. had been adopted. This means that the equipment becomes larger and occupies a larger area at the construction site. In addition, there were many problems such as increased cost. Therefore, several types of technical documents can be found here and there regarding these improvements. For example, the special public interest public in 1986-
There is a sludge dewatering equipment No. 46163, and its gist is as follows:
A rotating drum whose periphery is a strainer is installed at a certain level in the retention box, and this rotating drum is equipped with a suction pipe that communicates with a jet pump, and a filter cloth belt is wound around this rotating drum. The filter cloth belt has a structure in which the adsorbed sludge is peeled off and removed on the surface of the filter cloth belt. There is also a solid-liquid separator and device for sludge water disclosed in Japanese Patent Publication No. 61-32078.The gist of the device is to install several mixers with split mixing blades in the middle of the piping, and to install chemical tanks in each of these mixers. A screw conveyor is installed upright in the solid-liquid separation tank connected to the pipe, and a scraping auxiliary blade is provided which contacts the surface of the spiral blade of the screw conveyor and rotates with the rotation of the screw conveyor. The purpose of this system is to actively generate flocs using the mixer, and to reliably discharge the flocs separated in the solid-liquid separation tank using a screw conveyor and auxiliary scraping blades.

尚また実公昭57−35366号の沈澱分離装置があ
り、本体容器を合体できる中空円錐体で構成され
る本体容器の上部に、密閉式の混合凝集槽体を、
その下部にスラツジ濃縮槽体をそれぞれ設け、前
記本体容器を構成する上方の中空円錐体には、そ
の内壁に沿つて傾斜する傘状の分離体を設け、ま
た下方の中空円錐体を沈降分離室に形成し、更に
前記混合凝集槽体に原水管を、また前記分離体に
清澄水排出管をそれぞれ設けた構成である。
There is also a sedimentation separation device of Utility Model Publication No. 57-35366, in which a closed type mixing flocculation tank is placed on top of the main container, which is composed of a hollow cone that can be combined with the main container.
A sludge thickening tank body is provided at the lower part of the body, an umbrella-shaped separator is provided on the upper hollow cone constituting the main body vessel, and an umbrella-shaped separator is provided that slopes along its inner wall, and the lower hollow cone body is a sedimentation separation chamber. The mixing flocculation tank body is further provided with a raw water pipe, and the separation body is provided with a clear water discharge pipe.

その特徴は、本体容器の下部が収れんされた中
空円錐体であり、スラツジの流下を図り得るこ
と。またこの中空円錐体の下部に、円筒状のスラ
ツジ濃縮槽体を設けたので、スラツジの確実な集
積と、排出が可能となることにある。
Its feature is that the lower part of the main container is a convergent hollow cone, which allows the sludge to flow down. Further, since a cylindrical sludge concentration tank body is provided at the lower part of this hollow cone, it is possible to reliably collect and discharge sludge.

「発明が解決しようとする問題点」 上記技術文献は、前記従来の問題点を解決する
ための布石となることは明らかである。しかしな
がら少なからず問題があること。即ち特公昭61−
46163号の汚泥脱水処理装置では、機構上大量の
汚泥水を迅速に処理することは困難視されるこ
と、濾布ベルトを採用していることから目詰りの
対策が必要となり、その清掃とともに保守管理と
か耐久性等とかに問題がある。また特公昭61−
32078号の汚泥水の固液分離方法および装置では、
パイプミキサーを配管中に介設して汚泥水と凝集
剤との混合を図つているが、このパイプミキサー
一基では到底十分な撹拌、混合が達成されず、や
はり図示の如く三基とか四基の如く数基を配備す
る必要があり、究極のところ装置が複雑となるこ
と、比較的大型化すること及び目詰りの問題も少
なくなく保守管理が大変である。また固液分離槽
はフロツク群の積極的な排出には効果があるが、
比重差を利用した清澄水とフロツクとの分離が必
ずしも十分とは思われないものである。更に実公
昭57−35366号の発明では、原水は原水管より狭
い誘導路に導入されることから、この誘導路での
フロツクの生成は期待できず、汚い原水がいきな
り本体容器に導入される。したがつて、効率的な
固液分離、殊に本発明が目的とする汚泥水の分離
には不向きなものである。また本体容器に大きな
沈降分離の為のチヤンバーが形成されず、処理時
間の長時間比は、歪めない処である。
"Problems to be Solved by the Invention" It is clear that the above technical documents serve as a starting point for solving the conventional problems. However, there are quite a few problems. Namely, Special Public Interest Publication in 1986-
The sludge dewatering equipment No. 46163 has mechanical problems that make it difficult to quickly process a large amount of sludge water, and since it uses a filter cloth belt, countermeasures against clogging are required, and cleaning and maintenance are required. There are problems with management, durability, etc. Also, special public service in 1987-
In the solid-liquid separation method and device for sludge water of No. 32078,
A pipe mixer is installed in the piping to mix the sludge water and flocculant, but one pipe mixer cannot achieve sufficient agitation and mixing, so three or four mixers are required as shown in the diagram. In the end, it is necessary to install several units such as the above, and in the end, the apparatus becomes complicated and relatively large, and there are many problems of clogging, and maintenance management is difficult. In addition, solid-liquid separation tanks are effective in actively discharging flocs, but
Separation of clear water and floc using the difference in specific gravity is not always considered to be sufficient. Furthermore, in the invention of Utility Model Publication No. 57-35366, since raw water is introduced into a guideway narrower than the raw water pipe, no flocs can be expected to form in this guideway, and dirty raw water is suddenly introduced into the main container. Therefore, it is unsuitable for efficient solid-liquid separation, especially for separating sludge water, which is the object of the present invention. In addition, a large chamber for sedimentation separation is not formed in the main container, and the long processing time ratio is not distorted.

「問題点を解決するための手段」 そこで本発明は、大量の汚泥水を効率的かつ能
率的に処理するとともに、略完全に沈降分離され
て清澄化された水、処理液を確保すること。また
コンパクト化された固液分離装置を提供すること
にある。その要旨は、原水導入管と仕切板を介し
て並設される原水流入部を有する容器本体とは分
離され、かつ前記原水導入管より原水流入部への
原水の流れを確保することにより原水の十分な滞
留を許す環状の凝集槽と、この原水の凝集槽が着
脱自在に設けられる上面開口部を有する円筒分離
室及び下方の大きな沈降分離室とでなる容器本体
であつて、かつこの容器本体と原水の凝集槽とが
前記原水流入部とで連通されているとともに、こ
の容器本体の円筒分離室に重畳状に配備される分
離体は、上方の位置する分離体の傾斜長さを極度
に短く、また下方に位置する分離体の傾斜長さを
長く構成した複数個の傘状の分離体と、この分離
体で形成される傾斜長さの異なる複数の流下方式
の分離流路と、前記分離体の下段の分離体の収歛
部に流入口を臨ませると共に、清澄水の排出を司
る容器本体外に排出口を臨ませてなる上澄水排出
管と、前記容器本体の固液分離槽底面に設けたス
ラツジ排出口及びこのスラツジ排出口に連通する
スラツジ排出管とを設け、前記固液分離槽の下部
に大きな沈降分離室を形成し、この沈降分離室に
回転自在の掻寄板を設けてなるスラツジを底面の
窪部に集積する構成の汚泥水等原水の固液分離装
置である。
``Means for Solving the Problems'' Therefore, the present invention is to efficiently and efficiently treat a large amount of sludge water, and to secure water and treated liquid that have been substantially completely sedimented and separated and clarified. Another object of the present invention is to provide a compact solid-liquid separator. The gist is that the raw water inlet pipe is separated from the main body of the container, which has a raw water inlet installed in parallel via a partition plate, and that the raw water is allowed to flow from the raw water inlet pipe to the raw water inlet. A container body consisting of an annular flocculation tank that allows sufficient retention, a cylindrical separation chamber having an upper opening in which the raw water flocculation tank is removably installed, and a large sedimentation separation chamber below; and the raw water aggregation tank are communicated with the raw water inlet, and the separators arranged in an overlapping manner in the cylindrical separation chamber of this container body are arranged so that the inclination length of the separator located above is extremely a plurality of umbrella-shaped separators that are short and have a long inclination length of the separator located below; a plurality of downstream type separation flow channels formed by these separators with different inclination lengths; A supernatant water discharge pipe having an inlet facing the storage part of the lower stage of the separator and a discharge port facing outside the container body that controls the discharge of clear water, and a solid-liquid separation tank of the container body. A sludge discharge port provided at the bottom and a sludge discharge pipe communicating with the sludge discharge port are provided, a large sedimentation separation chamber is formed at the bottom of the solid-liquid separation tank, and a rotatable scraping plate is provided in the sedimentation separation chamber. This is a solid-liquid separation device for raw water such as sludge water, which has a structure in which sludge is accumulated in a depression on the bottom surface.

「作用」 次に本発明の作用の概要を説明すると、原水槽
に導入された汚泥水等の原水は、配管を介して反
応槽へと導かれる。この反応槽に到つた原水には
第1薬品槽より配管を介して送給された薬品溶剤
が添加されると同時に、撹拌翼を回転せしめて積
極的に沈降性のよいフロツクに転化せしめる。こ
のように処理された原水は、配管を介して撹拌器
に供給されるとともに、この撹拌器に入る直前で
第2薬品槽より配管を介して送給された薬品溶剤
が添加されて一層沈降性のよいフロツクが生成さ
れる。この撹拌器で処理された薬品添加の原水
は、配管を介して原水導入管より固液分離槽に導
入され、凝集槽中に到つた薬品添加の原水を、凝
集槽内を緩やかに環流させつつ、ここで主として
薬品溶剤と原水との一層の混和を図り、沈降性の
よいフロツクに転化させる。そうして凝集槽に開
設された原水流入部を介して少なくとも二重に重
畳状に配備された複数個の分離体へと導かれる。
この分離体に導かれた原水は複数の分離流路へと
分配流下されていき、その流下過程において原水
は分離体に接触しその摩擦抵抗により一層緩速と
されると共に、機械的な接触衝撃によりフロツク
は更に大きく成長し、かつ分離体の摩擦抵抗によ
り分別され、かくして固液分離が急速に行われ
る。したがつてフロツクは沈降分離室内に流入す
ると、ただちにフロツクはその室内を降下沈降
し、次第に濃縮されスラツジ排出口に到る。そう
してスラツジ排出管を介して外部に排出される。
一方処理原水は、上澄液となつて分離体の収歛部
に一時的に滞溜すると共に、この滞溜時に更にこ
れに含有する微小スラツジと分離され、美麗にな
つた上澄液が微速をもつて上昇していき、上澄液
排出管を介して外部に排出される。一方スラツジ
は配管を介してスラツジ濃縮槽へと導かれ、ここ
でプールされるとともに、その上澄水は配管を介
して原水槽に逆送され、また沈降したスラツジは
フイルタープレスへと配管を介して移送されてい
く。そうしてフイルタープレスを介してスラツジ
塊と清澄水、処理液とに分離される。このスラツ
ジ塊は廃棄されるし、また処理水、処理液は配管
を介して原水槽に送逆される。このような操作を
もつて原水が順次処理されるのである。
"Function" Next, to explain the outline of the function of the present invention, raw water such as sludge water introduced into the raw water tank is guided to the reaction tank via piping. A chemical solvent sent from the first chemical tank via piping is added to the raw water that has reached the reaction tank, and at the same time, a stirring blade is rotated to actively convert the water into flocs with good sedimentation properties. The raw water treated in this way is supplied to the agitator via piping, and immediately before entering the agitator, a chemical solvent sent from the second chemical tank via the piping is added to make it even more sedimentable. A good flock is generated. The chemical-added raw water treated with this agitator is introduced into the solid-liquid separation tank from the raw water introduction pipe via piping, and the chemical-added raw water that reaches the flocculation tank is slowly circulated inside the flocculation tank. Here, the main purpose is to further mix the chemical solvent with the raw water and convert it into a floc with good sedimentation properties. The raw water is then introduced to a plurality of separators arranged in at least a double layered manner through the raw water inlet provided in the flocculation tank.
The raw water led to this separator is distributed and flowed down into multiple separation channels, and in the flow process, the raw water comes into contact with the separator and is slowed down by the frictional resistance, and is also subjected to mechanical contact impact. As a result, the flocs grow larger and are separated by the frictional resistance of the separator, thus rapidly solid-liquid separation. Therefore, when the flocs flow into the sedimentation separation chamber, they immediately descend and settle within the chamber, becoming gradually concentrated and reaching the sludge outlet. The sludge is then discharged to the outside via the sludge discharge pipe.
On the other hand, the treated raw water becomes a supernatant liquid and temporarily accumulates in the collection part of the separator, and during this accumulation, it is further separated from the microscopic sludge contained therein, and the beautiful supernatant liquid flows at a very slow rate. The supernatant liquid rises and is discharged to the outside via the supernatant liquid discharge pipe. On the other hand, the sludge is led via piping to a sludge thickening tank where it is pooled, the supernatant water is sent back to the raw water tank via piping, and the settled sludge is sent to a filter press via piping. being transported. The sludge is then separated into sludge mass, clear water, and treatment liquid through a filter press. This sludge mass is discarded, and the treated water and treated liquid are sent back to the raw water tank via piping. Raw water is sequentially treated through such operations.

「実施例」 図面は本発明の一実施例を示しており、先ず第
1の発明の固液分離槽Aについて詳述すると、1
は円筒状の円筒分離室2と、その下方に設けられ
た大きな容積を有する沈降分離室3とでなる円筒
状の容器本体で、この容器本体1の上面開口部1
aには鍔状の係止腕5を有する略ブイ態様をなす
ドーナツ状の凝集槽4が架設されており、この一
例では凝集槽4より放射方向に向つて設けられた
三個所の係止腕5が容器本体1の上面開口部1a
の周壁1bに掛架されている。尚この凝集槽4の
中央には円筒部4aが立設されており、この円筒
部4aには後述する上澄水排出管が挿設されてい
る。また4bは凝集槽4の底面4bの外側に垂下
されたガイド筒である。そして開口部1aと凝集
槽4の外壁との間には略扇型の開放部分Bが形成
される。更に凝集槽4は数枚の隔壁板7を介して
数個の区画室8a〜8eに区画されており、この
各隔壁板7に設けた透孔7aを介して導入された
薬品添加の原水が区画室8aから区画室8eに向
つて迂回するように構成されている。また図示し
ないが各隔壁板7の開口を上下となし、いわゆる
薬品添加の原水を区画室8aから区画室8eに向
つてオバーフロー、アンダーフロー方式とするこ
ともできる。また第3図のように凝集槽4の底面
4dの内側をその中心に向つて傾斜させることが
できるし、更には各隔壁板7にスラツジ等の落下
口4fを設けることもできる。9は凝集槽4に臨
んだ原水導入管である。10は凝集槽4の最後の
区分室8eの底面4dに開設された原水流入部
で、この原水流入部9は容器本体1の円筒分離室
2に連通している。したがつて薬品と十分に混合
された原水がこの原水流入部10を介して円筒分
離室2に流下していき、その後は後述する分離体
で構成される分離流路に分配流下される構造とな
つている。11は前記凝集槽4の円筒部4aにそ
の略上半分が挿設され、その略下半分が容器本体
1に到りこの下半分の先端が容器本体1の円筒分
離室2の略中央まで達している上澄水排出管で、
この上澄水排出管11の流入口10aは後述する
下段の分離体の収歛部に開口すると共に、その排
出口11bは容器本体1外に開口している。そう
してこの上澄水排出管11の内で円筒分離室2に
垂設された部分には下方に向かつて拡開した傘状
の第1、第2分離体12,13が二重状に重畳さ
れており、具体的には、上方に位置する第1分離
体12の傾斜長さを極度に短く、また下方に位置
する第2分離体13の傾斜長さを長く構成した、
変則の分離体12,13である。
"Example" The drawing shows an example of the present invention, and first, the solid-liquid separation tank A of the first invention will be described in detail.
is a cylindrical container body consisting of a cylindrical separation chamber 2 and a sedimentation separation chamber 3 with a large volume provided below the cylindrical separation chamber 2;
A doughnut-shaped agglomeration tank 4 having a substantially buoy shape and having a brim-shaped locking arm 5 is installed in a, and in this example, three locking arms are provided in the radial direction from the flocculation tank 4. 5 is the top opening 1a of the container body 1
It is hung on the peripheral wall 1b of. A cylindrical portion 4a is erected in the center of the coagulation tank 4, and a supernatant water discharge pipe, which will be described later, is inserted into this cylindrical portion 4a. Further, reference numeral 4b is a guide cylinder hanging down from the outside of the bottom surface 4b of the coagulation tank 4. A substantially fan-shaped open portion B is formed between the opening 1a and the outer wall of the aggregation tank 4. Further, the coagulation tank 4 is divided into several compartments 8a to 8e via several partition plates 7, and the chemical-added raw water introduced through the through holes 7a provided in each partition plate 7 is It is configured to take a detour from the compartment 8a to the compartment 8e. Although not shown, each partition plate 7 may have upper and lower openings so that so-called chemical-added raw water can flow from the compartment 8a to the compartment 8e in an overflow or underflow manner. Further, as shown in FIG. 3, the inside of the bottom surface 4d of the coagulation tank 4 can be inclined toward the center, and each partition plate 7 can also be provided with an opening 4f for dropping sludge or the like. 9 is a raw water introduction pipe facing the coagulation tank 4. Reference numeral 10 denotes a raw water inlet section provided on the bottom surface 4d of the last compartment 8e of the coagulation tank 4, and this raw water inlet section 9 communicates with the cylindrical separation chamber 2 of the container body 1. Therefore, raw water sufficiently mixed with chemicals flows down into the cylindrical separation chamber 2 through this raw water inlet 10, and is then distributed to a separation flow path composed of a separator to be described later. It's summery. 11 has its substantially upper half inserted into the cylindrical portion 4a of the aggregation tank 4, its substantially lower half reaches the container body 1, and the tip of this lower half reaches approximately the center of the cylindrical separation chamber 2 of the container body 1. The supernatant water discharge pipe
An inlet 10a of the supernatant water discharge pipe 11 opens into a storage section of a lower separator, which will be described later, and an outlet 11b thereof opens to the outside of the container body 1. Then, in the part of the supernatant water discharge pipe 11 that is vertically installed in the cylindrical separation chamber 2, umbrella-shaped first and second separation bodies 12 and 13 that expand downward are superimposed in a double form. Specifically, the first separator 12 located above has an extremely short slope length, and the second separator 13 located below has a long slope length.
These are irregular separators 12 and 13.

したがつて、比較的スラツジの多い原水が先ず
第1分離体12で処理された後、この処理水が、
第2分離体13に流下して再度処理されること。
また第2分離体13には、狭隘なガイド筒4bで
幾分処理された原水が流下される合理的な分離構
造となつている。この第1分離体12の外側傾斜
面12aと第2分離体13の内側傾斜面113b
との間、及び第2分離体13の表面には分離流路
14,15が形成されている。これにより前述の
凝集槽4の原水流入部10より流下した原水がこ
の上澄水排出管11の外周面を流下してそれぞれ
分離流路14,15に分配流下されるのである。
図中16は第2分離体13の中央収歛部にラツパ
状に突設された案内筒で、この案内筒16には原
水流入口16aが設けられている。17は容器本
体1の中心に貫設された回転軸で、この回転軸1
7の上端にはモータ18が下端には掻寄板19の
取付用の支持杆20が設けられている。そうして
この掻寄板19は図示の如く適宜の傾斜角度をも
つて設けられており、容器本体1の内底面1aに
堆積されたスラツジを確実にその中心方向へと移
行させるように構成されている。図中21はスラ
ツジ排出口であり、このスラツジ排出口21はス
ラツジ排出管22に連通している。24は油分排
出樋、24aは油分排出樋24と容器本体1との
間に開設した透孔、25はフレームである。
Therefore, after raw water with a relatively large amount of sludge is first treated in the first separator 12, this treated water is
It flows down to the second separator 13 and is processed again.
The second separator 13 has a rational separation structure in which raw water that has been somewhat treated flows down through a narrow guide tube 4b. The outer inclined surface 12a of the first separator 12 and the inner inclined surface 113b of the second separator 13
Separation channels 14 and 15 are formed between the two and on the surface of the second separator 13. As a result, the raw water flowing down from the raw water inlet 10 of the aggregation tank 4 flows down the outer peripheral surface of the supernatant water discharge pipe 11 and is distributed to the separation channels 14 and 15, respectively.
In the figure, reference numeral 16 denotes a guide tube that protrudes like a truss from the central housing part of the second separator 13, and this guide tube 16 is provided with a raw water inlet 16a. Reference numeral 17 denotes a rotating shaft penetrating through the center of the container body 1;
A motor 18 is provided at the upper end of the holder 7, and a support rod 20 for mounting a scraper plate 19 is provided at the lower end. This scraping plate 19 is provided with an appropriate inclination angle as shown in the figure, and is configured to reliably move the sludge deposited on the inner bottom surface 1a of the container body 1 toward its center. ing. 21 in the figure is a sludge discharge port, and this sludge discharge port 21 is connected to a sludge discharge pipe 22. 24 is an oil drain gutter, 24a is a through hole formed between the oil drain gutter 24 and the container body 1, and 25 is a frame.

次に本発明の前記固液分離装置の使用例を、第
4図の模式図に付いて説明すると、汚泥水、産業
廃水等が流入される原水槽30は弁を備えた配管
31(“弁を備えた配管”を以下単に配管とする)
を介して反応槽32と連通されており、ポンプ3
3の作用で配管31を介して反応槽32へ原水を
送給する構成となつている。そうして反応槽32
には配管34を介して第1薬品槽35と連通され
ており、反応槽32に給送されてきた原水に凝集
剤等の薬品溶剤を添加して、原水中に含有するス
ラツジを沈降性のよいフロツクに転化させる。こ
の反応槽32はポンプ36を備えた配管37を介
して撹拌器38に連通されているとともに、この
撹拌器38に接続されている配管37には、配管
40が接続されている。この配管40を介して第
2薬品槽39の薬品溶剤が撹拌器38に給送され
る構成となつているとともに、この撹拌器38内
で処理原水と薬品溶剤の撹拌、混合がなされる。
そうしてこの撹拌器38は配管41を介して既に
詳述した固液分離槽Aに連通され、この固液分離
槽Aで上澄水とスラツジとに分離される。この内
上澄水は固液分離槽Aの上澄水排出管11を介し
て排出され、一方スラツジはスラツジ排出管22
に接続される配管42を介してスラツジ濃縮槽4
4に送給される。このスラツジ濃縮槽44で分離
された上澄水は配管45を介して再び原水槽30
へと逆送されるし、スラツジはポンプ50を備え
た配管46を介してフイルタープレス47に連通
されている。このフイルタープレス47で圧縮分
離された清澄水、処理液は配管48を介して再び
原水槽30へと逆送されるし、スラツジ塊は台車
49上に堆積される構成となつている。
Next, an example of the use of the solid-liquid separator of the present invention will be explained with reference to the schematic diagram in FIG. (hereinafter referred to simply as piping)
The pump 3 is connected to the reaction tank 32 via the
3, raw water is fed to the reaction tank 32 via the piping 31. Then the reaction tank 32
The tank is connected to a first chemical tank 35 via piping 34, and a chemical solvent such as a coagulant is added to the raw water fed to the reaction tank 32 to convert the sludge contained in the raw water into a sedimentary state. Convert it into a good flock. This reaction tank 32 is connected to a stirrer 38 via a pipe 37 equipped with a pump 36, and a pipe 40 is connected to the pipe 37 connected to the stirrer 38. The chemical solvent in the second chemical tank 39 is fed to the stirrer 38 through the piping 40, and the raw water to be treated and the chemical solvent are stirred and mixed within the stirrer 38.
This stirrer 38 is then communicated via a pipe 41 to the solid-liquid separation tank A, which has already been described in detail, and is separated into supernatant water and sludge in this solid-liquid separation tank A. The supernatant water is discharged through the supernatant water discharge pipe 11 of the solid-liquid separation tank A, while the sludge is discharged from the sludge discharge pipe 22.
The sludge thickening tank 4
4. The supernatant water separated in this sludge thickening tank 44 is returned to the raw water tank 30 via piping 45.
The sludge is conveyed back to the filter press 47 via a line 46 equipped with a pump 50. The clarified water and treated liquid compressed and separated by the filter press 47 are sent back to the raw water tank 30 via a pipe 48, and the sludge mass is deposited on a truck 49.

続いて図示の例に基づいて、本発明の作用を説
明すると、原水槽30に導入された汚泥水等の原
水は、配管31を介して反応槽32へと導かれ
る。この反応槽32に到つた原水には第1薬品槽
35より配管34を介して送給された高分子凝集
剤等の薬品溶剤が添加されると同時に、撹拌翼を
回転せしめて積極的に沈降性のよいフロツクに転
化せしめる。具体的にはSSの粒径をμかmm単位
に変換する。このように処理された原水は、配管
37を介して撹拌器38に供給されるとともに、
この撹拌器38に入る直前で第2薬品槽39より
配管40を介して給送された商品名スイフロツク
等の薬品溶剤が添加されるとともに、この撹拌器
38内で処理原水と薬品溶剤が十分に撹拌、混合
されて一層沈降性のよいフロツクが生成される。
この撹拌器38で処理された薬品添加の原水は、
配管41を介して原水導入管9より固液分離槽A
に導入され、凝集槽4内に導入された原水は、凝
集槽4の数個の区画室8a空から区画室8eに向
つて迂回又はオーバーフロー、アンダーフローを
繰り返して緩やかに環流し、しかも凝集槽4に流
入される薬品溶剤との一層の混和ることにより沈
降性のよいフロツクに転化させる。そうして凝集
槽4に開設された原水流入部8を介して重畳状に
配備された複数個の第1、第2分離体12,13
へと導かれる。この第1、第2分離体12,13
に導かれた原水は複数の分離流路14,15へと
分配流下されていき、その流下過程において原水
は第1、第2分離体12,13の外側傾斜面12
a,13aに接触し、その摩擦抵抗により一層緩
速とされるとともに、機械的な接触衝撃によりフ
ロツクは更に大きく成長し、かつ第1、第2分離
体12,13の摩擦抵抗により分別され、かくし
て固液分離が急速に行われる。そうして上澄水と
フロツクとは分離流路14,15を流動した後
は、傾斜分離室2と分離体13で形成される環状
の隙間を流下していきこの内上澄水は沈降分離室
3の上部に到るとともに、フロツクは沈降分離室
3内に流下沈降していき、次第に濃縮されるとと
もに、掻寄板19によりスラツジは容器本体1の
内底面1aの中心部へと移送された後、スラツジ
排出口21を介してスラツジ排出管22に到る。
一方処理原水は、上澄水となつて沈降分離室3の
上部と第1分離体12の傘部内側に一時的に滞溜
するとともに、この滞溜時に更にこれに含有する
微小スラツジと分離され、美麗になつた上澄水が
微速をもつて上昇していき、上澄水排出管11を
介して外部に排出されるのである。また前記スラ
ツジ排出管22に到つてスラツジは、配管42を
介してスラツジ濃縮槽44へと導かれ、ここでプ
ールされるとともに、その上澄水は配管45を介
して原水槽30に逆送され再利用される。また沈
降したスラツジはフイルタープレス47へと配管
46を介して移送されていく。そうしてフイルタ
ープレス47を介してスラツジ塊と処理水、処理
液とに分離される。このスラツジ塊は廃棄される
し、また処理水、処理液は配管48を介して原水
槽30に逆送され再利用される。このような操作
をもつて原水が順次処理されるのである。
Next, the operation of the present invention will be explained based on the illustrated example. Raw water such as sludge water introduced into the raw water tank 30 is guided to the reaction tank 32 via the piping 31. A chemical solvent such as a polymer flocculant sent from the first chemical tank 35 through the pipe 34 is added to the raw water that has reached the reaction tank 32, and at the same time, stirring blades are rotated to actively settle the water. It transforms it into a sexy flock. Specifically, the particle size of SS is converted into μ or mm units. The raw water treated in this way is supplied to the agitator 38 via the pipe 37, and
Immediately before entering this agitator 38, a chemical solvent such as SIFLOCK (trade name) supplied from a second chemical tank 39 via piping 40 is added, and the treated raw water and chemical solvent are sufficiently mixed in this agitator 38. Stirring and mixing produces a floc with better settling properties.
The chemical-added raw water treated with this agitator 38 is
Solid-liquid separation tank A from raw water introduction pipe 9 via pipe 41
The raw water introduced into the flocculation tank 4 slowly circulates from the empty compartments 8a of the flocculation tank 4 toward the compartment 8e by repeating detours, overflows, and underflows, and further flows through the flocculation tank 4. By further mixing with the chemical solvent introduced in step 4, it is converted into a floc with good sedimentation properties. A plurality of first and second separators 12 and 13 are arranged in a superimposed manner through the raw water inlet 8 provided in the flocculation tank 4.
be led to. These first and second separation bodies 12, 13
The raw water led to the is distributed and flowed down into the plurality of separation channels 14 and 15, and in the flowing process, the raw water flows down the outer inclined surfaces 12 of the first and second separators 12 and 13.
a, 13a, the flocs are made to move more slowly due to the frictional resistance, and the flocs grow larger due to the mechanical contact impact, and are separated due to the frictional resistance of the first and second separators 12, 13. Solid-liquid separation is thus carried out rapidly. After flowing through the separation channels 14 and 15, the supernatant water and floc flow down the annular gap formed by the inclined separation chamber 2 and the separator 13, and the supernatant water flows into the sedimentation separation chamber 3. As it reaches the upper part of the container body 1, the flocs flow down into the sedimentation separation chamber 3 and are gradually concentrated, and the sludge is transferred to the center of the inner bottom surface 1a of the container body 1 by the scraper plate 19. , and reaches the sludge discharge pipe 22 via the sludge discharge port 21.
On the other hand, the treated raw water becomes supernatant water and temporarily accumulates in the upper part of the sedimentation separation chamber 3 and inside the umbrella part of the first separator 12, and at the time of this accumulation, it is further separated from the minute sludge contained therein. The clean supernatant water rises at a slow speed and is discharged to the outside via the supernatant water discharge pipe 11. Furthermore, the sludge that reaches the sludge discharge pipe 22 is led to a sludge thickening tank 44 via a pipe 42 and pooled there, and the supernatant water is sent back to the raw water tank 30 via a pipe 45 and recycled. used. Further, the settled sludge is transferred to a filter press 47 via a pipe 46. The sludge is then separated into a sludge mass, treated water, and treated liquid through a filter press 47. This sludge mass is discarded, and the treated water and treated liquid are sent back to the raw water tank 30 via piping 48 and reused. Raw water is sequentially treated through such operations.

「発明の効果」 本発明は以上で詳述した構成としてあるので、
以下のような効果を有する。
"Effects of the Invention" Since the present invention has the configuration detailed above,
It has the following effects.

本発明は、容器本体の上面開口部にこの容器
本体とは分離された原水の凝集槽を設け、かつ
この凝集槽は前記原水導入管より原水流入部へ
の原水の流れを確保することにより原水の十分
な滞留を許す環状又は形態とするとともに、こ
の凝集槽と前記容器本体とは原水流入部とで連
通され構成となつている。
The present invention provides a raw water aggregation tank separated from the container body at the top opening of the container body, and this aggregation tank secures the flow of raw water from the raw water inlet pipe to the raw water inlet. The flocculation tank and the container body are configured to communicate with each other through a raw water inlet.

したがつて、原水がこの凝集槽で凝集助剤と
十分に混和される効果があり、またフロツクの
生成を助成する効果がある、また複数個の流下
式の分離体への原水の分配の均一化とゆるやか
な自然流下が図れるものである。
Therefore, the raw water is sufficiently mixed with the flocculation aid in this flocculation tank, has the effect of assisting the formation of flocs, and has the effect of uniformly distributing the raw water to the plurality of flowing separators. This allows for natural flow and gradual natural flow.

本発明の傘状の二重式の分離体は、上方に位
置する第1分離体の傾斜長さを極度に短く、ま
た下方に位置する第2分離体の傾斜長さを長く
構成した、変則の分離体である。
The umbrella-shaped double type separator of the present invention has an irregular structure in which the first separator located above has an extremely short slope length, and the second separator located below has a long slope length. It is a separate body of

したがつて、比較的スラツジの多い原水が先
ず第1分離体で処理された後、この処理水が、
第2分離体に流下して再度処理されること。ま
た第2分離体には、狭隘なガイド筒で幾分処理
された原水が流下される合理的な分離構造とな
つている。
Therefore, after raw water with a relatively large amount of sludge is first treated in the first separator, this treated water is
Flowing down to the second separator and being reprocessed. The second separator has a rational separation structure in which raw water that has been treated to some extent flows down through a narrow guide tube.

また本発明は、容器本体の上面開口部に原水
凝集槽を着脱自在とする構成であるので、分離
体へのスラツジの付着等による汚れに対しても
容易に対処できる効果と、容器本体及び分離体
の清掃が簡易であり、保守管理が容易である。
Furthermore, since the present invention has a structure in which the raw water coagulation tank is detachably attached to the upper opening of the container body, it is possible to easily deal with contamination caused by adhesion of sludge to the separator, and the container body and the separator The body is easy to clean and maintenance management is easy.

更に本発明では、容器本体に設けた沈降分離
室が大きな容積となる構成であるので、沈降分
離の為の有益なチヤンバーが形成されること。
また微小なスラツジまでも十分に捕捉凝集する
ことができる等の分離効率の向上が大いに期待
できる。更にその処理時間の短縮化に役立つ。
Furthermore, in the present invention, since the sedimentation chamber provided in the container body has a large volume, a chamber useful for sedimentation separation is formed.
In addition, it is expected that even the smallest sludge can be sufficiently captured and agglomerated, resulting in improved separation efficiency. Furthermore, it is useful for shortening the processing time.

尚本発明の実験データー表を参考資料として
別添の如く提出させていただきましたので、よ
ろしくお願い申し上げます。
Please note that we have submitted the experimental data table for the present invention as a reference material as attached.

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

図面は本発明の一実施例を示し、第1図は固液
分離槽の断面図、第2図は一部欠截の平面図、第
3図は凝集槽の他の一例を示す断面図、第4図は
本発明の使用例を示す模式図である。 1…容器本体、2…円筒分離室、3…沈降分離
室、4…凝集槽、4a…円筒部、4b…ガイド
筒、5…係止腕、7…隔壁板、8a〜8e…区画
室、9…原水導入管、10…原水流入部、11…
上澄水排出管、12,13…分離体、14,15
…分離流路、16…案内管、17…回転軸、18
…モータ、19…掻寄板、20…支持杆、22…
スラツジ排出管、24…油分排出樋、25…フレ
ーム、30…原水槽、33,36,43,50…
ポンプ、32…反応槽、35…第1薬品槽、38
…撹拌器、39…第2薬品槽、44…スラツジ濃
縮槽、47…フイルタープレス、49…台車。
The drawings show one embodiment of the present invention; FIG. 1 is a sectional view of a solid-liquid separation tank, FIG. 2 is a partially cutaway plan view, and FIG. 3 is a sectional view showing another example of a coagulation tank. FIG. 4 is a schematic diagram showing an example of use of the present invention. DESCRIPTION OF SYMBOLS 1... Container body, 2... Cylindrical separation chamber, 3... Sedimentation separation chamber, 4... Coagulation tank, 4a... Cylindrical part, 4b... Guide tube, 5... Locking arm, 7... Partition plate, 8a-8e... Compartment chamber, 9... Raw water introduction pipe, 10... Raw water inlet, 11...
Supernatant water discharge pipe, 12, 13...Separator, 14, 15
... Separation channel, 16... Guide tube, 17... Rotating shaft, 18
... Motor, 19... Scraping plate, 20... Support rod, 22...
Sludge discharge pipe, 24...oil discharge gutter, 25...frame, 30...raw water tank, 33, 36, 43, 50...
Pump, 32... Reaction tank, 35... First chemical tank, 38
... Stirrer, 39... Second chemical tank, 44... Sludge concentration tank, 47... Filter press, 49... Cart.

Claims (1)

【特許請求の範囲】[Claims] 1 原水導入管と仕切板を介して並設される原水
流入部を有する容器本体とは分離され、かつ前記
原水導入管より原水流入部への原水の流れを確保
することにより原水の十分な滞留を許す環状の凝
集槽と、この原水の凝集槽が着脱自在に設けられ
る上面開口部を有する円筒分離室及び下方の大き
な沈降分離室とでなる容器本体であつて、かつこ
の容器本体と原水の凝集槽とが前記原水流入部で
連通されているとともに、この容器本体の円筒分
離室に重畳状に配備された傾斜長さの異なる傾斜
面を有する複数個の傘状の分離体と、この分離体
で形成される複数の流下方式の分離流路と、前記
分離体の下段の分離体の収歛部に流入口を臨ませ
ると共に、清澄水の排出を司る容器本体外に排出
口を臨ませてなる上澄水排出管と、前記容器本体
の固液分離槽底面に設けたスラツジ排出口及びこ
のスラツジ排出口に連通するスラツジ排出管とを
設け、前記固液分離槽の下部に大きな沈降分離室
を形成し、この沈降分離室に回転自在の掻寄板を
設けてなる汚泥水等原水の固液分離装置。
1. The raw water inlet pipe is separated from the container main body, which has a raw water inlet section installed in parallel via a partition plate, and by ensuring the flow of raw water from the raw water inlet pipe to the raw water inlet part, sufficient retention of raw water can be achieved. A container body consisting of an annular flocculation tank that allows the raw water to flow, a cylindrical separation chamber with an upper opening in which the raw water flocculation tank is removably installed, and a large sedimentation separation chamber below, and the container body and the raw water A plurality of umbrella-shaped separators having sloped surfaces with different sloped lengths are arranged in a cylindrical separation chamber of the container body in a superimposed manner and communicated with the aggregation tank through the raw water inlet; A plurality of downstream type separation channels formed by the body, an inlet facing the receiving part of the lower separator of the separator, and an outlet facing the outside of the container body which controls the discharge of clear water. A large sedimentation separation chamber is provided at the bottom of the solid-liquid separation tank. A solid-liquid separation device for raw water such as sludge water, which has a sedimentation separation chamber provided with a rotatable scraper plate.
JP1191687A 1987-01-21 1987-01-21 Solid and liquid separator of raw water such as sludge Granted JPS63182009A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1191687A JPS63182009A (en) 1987-01-21 1987-01-21 Solid and liquid separator of raw water such as sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1191687A JPS63182009A (en) 1987-01-21 1987-01-21 Solid and liquid separator of raw water such as sludge

Publications (2)

Publication Number Publication Date
JPS63182009A JPS63182009A (en) 1988-07-27
JPH0262282B2 true JPH0262282B2 (en) 1990-12-25

Family

ID=11791024

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1191687A Granted JPS63182009A (en) 1987-01-21 1987-01-21 Solid and liquid separator of raw water such as sludge

Country Status (1)

Country Link
JP (1) JPS63182009A (en)

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JP2002096078A (en) * 2000-09-25 2002-04-02 Suirei:Kk Purifying unit and purifying system for raw water such as polluted water, waste water or the like equipped with catalyst device
KR200447898Y1 (en) 2009-12-02 2010-03-03 비손푸른엔지니어링 주식회사 Sedimentation tank
JP5444031B2 (en) * 2010-02-12 2014-03-19 株式会社スイレイ Solid-liquid separator
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Publication number Priority date Publication date Assignee Title
JPS5735366U (en) * 1980-08-08 1982-02-24

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019187355A1 (en) * 2018-03-28 2019-10-03 隆 玉城 Device for removing sediment/floating matter in water and on water surface

Also Published As

Publication number Publication date
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