JPH0468039B2 - - Google Patents

Info

Publication number
JPH0468039B2
JPH0468039B2 JP61204690A JP20469086A JPH0468039B2 JP H0468039 B2 JPH0468039 B2 JP H0468039B2 JP 61204690 A JP61204690 A JP 61204690A JP 20469086 A JP20469086 A JP 20469086A JP H0468039 B2 JPH0468039 B2 JP H0468039B2
Authority
JP
Japan
Prior art keywords
sludge
screw
closed container
concentrated liquid
supernatant liquid
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
JP61204690A
Other languages
Japanese (ja)
Other versions
JPS6359398A (en
Inventor
Tomio Suzuki
Jun Ishida
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.)
NISHIHARA KANKYO EISEI KENKYUSHO KK
Original Assignee
NISHIHARA KANKYO EISEI KENKYUSHO 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 NISHIHARA KANKYO EISEI KENKYUSHO KK filed Critical NISHIHARA KANKYO EISEI KENKYUSHO KK
Priority to JP61204690A priority Critical patent/JPS6359398A/en
Publication of JPS6359398A publication Critical patent/JPS6359398A/en
Publication of JPH0468039B2 publication Critical patent/JPH0468039B2/ja
Granted legal-status Critical Current

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  • Treatment Of Sludge (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、都市下水や各種産業廃水等の処理
の際に発声する汚泥を回転スクリユーを内蔵した
密閉容器内で濃縮して、濃縮液と上澄液とに分離
するようにした汚泥濃縮装置に関するものであ
る。
[Detailed Description of the Invention] [Industrial Application Field] This invention concentrates sludge produced during the treatment of urban sewage and various industrial wastewater in a closed container equipped with a rotating screw, and converts it into a concentrated liquid. The present invention relates to a sludge thickening device that separates the sludge into a supernatant liquid and a supernatant liquid.

〔従来の技術〕[Conventional technology]

従来から、例えば特公昭60−5323合公報に示さ
れているように、スクリユー筒内に設けられたス
クリユーコンベアのスクリユー羽根に傾斜板の機
能を持たせ、汚泥流入口からスクリユー筒内に流
入された汚泥をスクリユーコンベアによつて濃縮
液排出口へ濃縮しつつ移送しながら、スクリユー
羽根の傾斜板としての機能により、濃縮液から分
離された上澄液を上澄液排出口へ排出させるよう
にしたものがある。
Conventionally, as shown in Japanese Patent Publication No. 60-5323, for example, the screw blades of the screw conveyor installed in the screw tube have been given the function of an inclined plate, and the sludge flows into the screw tube from the inlet. While the sludge is being concentrated and transferred to the concentrate discharge port by the screw conveyor, the supernatant liquid separated from the concentrate is discharged to the supernatant discharge port by the function of the screw blade as an inclined plate. There is something like this.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかしながら、この装置では、上澄液、濃縮液
の排出量を調整する手段を何等有していないの
で、一定濃度の濃縮液を得ることができなかつ
た。
However, since this apparatus does not have any means for adjusting the discharge amounts of the supernatant liquid and the concentrated liquid, it has not been possible to obtain a concentrated liquid of a constant concentration.

即ち、汚泥の濃縮を行う場合、一定濃度の濃縮
液を得るためには、濃縮の度合いを調整すること
が重要である。しかしこの時、濃縮汚泥の流量を
直接調整しようとすると、その濃縮汚泥が詰まり
易かつたり、水量が不足して流動性が悪くなり易
い等、制御が困難になつてしまう等の問題点があ
つた。
That is, when concentrating sludge, it is important to adjust the degree of concentration in order to obtain a concentrated liquid with a constant concentration. However, if you try to directly adjust the flow rate of the thickened sludge at this time, there are problems such as the thickened sludge tends to clog, the flowability tends to deteriorate due to insufficient water volume, and it becomes difficult to control. Ta.

この発明は上記のような問題点を解消するため
になされたもので、臭気対策が完全に達成できる
と共に、汚泥流入側での制御が可能で、且つ、流
入汚泥の沈殿促進機能が得られ、しかも、汚泥濃
縮度合を調整できることによつて、濃縮汚泥の目
詰りや粘度影響を受けることなく一定濃度の濃縮
液を得ることができて濃縮汚泥の管理が非常に容
易な汚泥濃縮装置を提供することを目的とする。
This invention was made to solve the above-mentioned problems, and it is possible to completely eliminate odor, control on the sludge inflow side, and provide a function to promote sedimentation of inflow sludge. Furthermore, by being able to adjust the degree of sludge concentration, it is possible to obtain a concentrated liquid of a constant concentration without being affected by clogging or viscosity of the thickened sludge, thereby providing a sludge thickening device that is extremely easy to manage the thickened sludge. The purpose is to

〔問題点を解決するための手段〕[Means for solving problems]

この発明に係る汚泥濃縮装置は、一端に汚泥流
入口を有して他端下部に濃縮液排出口が、且つ、
他端上部に上澄液排出口がそれぞれ設けられた密
閉容器の内底部に回転スクリユーを収納配置する
と共に、前記密閉容器内における前記回転スクリ
ユーの上方には、該回転スクリユーのスクリユー
羽根の外周に下端が近接して斜め上方に並行難間
状態で傾斜し、且つ、前記密閉容器の上部壁との
間で流路を形成する複数の傾斜板を収納配置し、
また、前記上澄液排出口の系統に流量調整手段を
設けると共に、前記汚泥流入口から前記密閉容器
内に原汚泥を圧入供給する汚泥圧入手段を備えた
構成としたものである。
The sludge thickening device according to the present invention has a sludge inlet at one end, a concentrated liquid outlet at the lower part of the other end, and
A rotary screw is housed in the inner bottom of a closed container having a supernatant liquid outlet at the top of the other end, and above the rotary screw in the closed container, the outer circumference of the screw blade of the rotary screw A plurality of inclined plates are housed and arranged, the lower ends of which are close to each other and are inclined diagonally upward in a parallel manner, and which form a flow path with the upper wall of the closed container,
Further, a flow rate adjusting means is provided in the system of the supernatant liquid discharge port, and a sludge injection means is provided for press-feeding raw sludge into the closed container from the sludge inlet.

〔作用〕[Effect]

この発明における汚泥濃縮装置は、回転スクリ
ユーと複数の傾斜板とを収納し、且つ、汚泥が圧
入される容器が密閉容器となつているため、この
種の開放形容器の場合に比して臭気対策が万全の
ものとなる。
The sludge thickening device according to the present invention houses a rotating screw and a plurality of inclined plates, and the container into which the sludge is press-fitted is a closed container, so the sludge thickening device has less odor than this type of open container. All measures will be taken.

また、上述のような密閉容器の汚泥流入口側に
汚泥圧入手段を設けたことにより、汚泥流入側で
の制御が可能となる。
Further, by providing the sludge injection means on the sludge inlet side of the closed container as described above, control on the sludge inflow side becomes possible.

そして、前記密閉容器内に圧入された流入汚泥
は、複数の傾斜板のそれぞれによつて回転スクリ
ユー側に向つてその略全長に亘る沈殿が促進され
る。
The inflow sludge press-fitted into the closed container is promoted to settle over substantially its entire length toward the rotating screw by each of the plurality of inclined plates.

このようにして沈殿した汚泥は、回転スクリユ
ーによつて濃縮されながら濃縮液排出口に向つて
移送される。この場合、前記回転スクリユーのス
クリユー羽根の外周に前記各傾斜板のそれぞれの
下端が近接していることにより、これらの傾斜板
によつて、前記回転スクリユーによる汚泥濃縮効
率および汚泥濃縮液の移送効率が向上する。
The sludge thus precipitated is transported toward the concentrate outlet while being concentrated by the rotating screw. In this case, since the lower ends of each of the inclined plates are close to the outer periphery of the screw blade of the rotating screw, these inclined plates improve the sludge concentration efficiency and the sludge concentrate transfer efficiency of the rotating screw. will improve.

また、前記汚泥濃縮液から分離された分離液は
密閉容器の上澄液排出口から排出されるが、この
際、その上澄液排出量を流量調整手段で調整する
ことによつて、汚泥の濃縮度合を適度に調整する
ことができる。これによつて、濃縮汚泥の目詰ま
りや粘度影響を受けることなく一定濃度の濃縮液
を得ることができ、濃縮汚泥の管理が頗ぶる容易
となる。
In addition, the separated liquid separated from the sludge concentrate is discharged from the supernatant liquid outlet of the sealed container. The degree of concentration can be adjusted appropriately. This makes it possible to obtain a concentrated liquid of a constant concentration without being affected by the clogging or viscosity of the thickened sludge, making the management of the thickened sludge extremely easy.

〔実施例〕〔Example〕

以下、第1図及び第2図に従つてこの発明の一
実施例を説明する。密閉容器1は横長であり、上
部側が長方形状をなし、下部側が半円筒状をなし
ている。この密閉容器1内の下部側に回転スクリ
ユー2が水平状に収納されていて、この回転スク
リユー2は水平なスクリユー軸3の外周にリード
ピツチが比較的大きい多重スクリユー構造のスク
リユー羽根4を取り付けたものである。尚、スク
リユー軸3の一端は軸受5で支持され、スクリユ
ー軸3の他端は密閉容器1外に設けられたモータ
6のモータ軸7にカツプリング8を介して連結さ
れている。
An embodiment of the present invention will be described below with reference to FIGS. 1 and 2. The airtight container 1 is horizontally long, with an upper side having a rectangular shape and a lower side having a semi-cylindrical shape. A rotary screw 2 is housed horizontally in the lower part of the airtight container 1, and the rotary screw 2 has screw blades 4 of a multi-screw structure with a relatively large lead pitch attached to the outer periphery of a horizontal screw shaft 3. It is. One end of the screw shaft 3 is supported by a bearing 5, and the other end of the screw shaft 3 is connected via a coupling 8 to a motor shaft 7 of a motor 6 provided outside the closed container 1.

また、密閉容器1内の上部には複数の傾斜板1
0が所定の角度に傾斜されて設けられている。
In addition, a plurality of inclined plates 1 are provided at the upper part of the airtight container 1.
0 is provided inclined at a predetermined angle.

尚、これらの傾斜板10の上端と密閉容器1の
上部壁1aとの間には流路11が形成されてお
り、これらの傾斜板10の下端にはスクリユー羽
根4の外周に近接して円弧面12が形成されてい
る。また、密閉容器1の下部壁1bはスクリユー
羽根4の外周に近接し円筒状に形成されている。
Note that a flow path 11 is formed between the upper ends of these inclined plates 10 and the upper wall 1a of the closed container 1, and a circular arc is formed at the lower end of these inclined plates 10 close to the outer periphery of the screw blade 4. A surface 12 is formed. Further, the lower wall 1b of the closed container 1 is close to the outer periphery of the screw blade 4 and is formed in a cylindrical shape.

そして、この横長の密閉容器1の一端部14側
でその密閉容器1の一方の側面壁1cに汚泥流入
口16が開口されていて、この汚泥流入口16に
は汚泥流入管17が接続されている。また、この
横長の密閉容器1の他端15側でその密閉容器1
の下部壁1bに濃縮液排出口18が開口され、上
部壁1aに上澄液排出口19が開口されている。
そして、これら濃縮液排出口18および上澄液排
出口19にはそれぞれ濃縮液排出管20および上
澄液排出管21が接続されている。そして、濃縮
液排出管20には、その先端が密閉容器1の上方
まで延出するように立ち上げられているか、弁等
が設けられている。
A sludge inlet 16 is opened in one side wall 1c of the closed container 1 at one end 14 side of the horizontally long closed container 1, and a sludge inlet pipe 17 is connected to the sludge inlet 16. There is. In addition, the airtight container 1 is placed on the other end 15 side of this horizontally long airtight container
A concentrated liquid outlet 18 is opened in the lower wall 1b, and a supernatant liquid outlet 19 is opened in the upper wall 1a.
A concentrated liquid discharge pipe 20 and a supernatant liquid discharge pipe 21 are connected to the concentrated liquid discharge port 18 and the supernatant liquid discharge port 19, respectively. The concentrated liquid discharge pipe 20 is raised such that its tip extends above the closed container 1, or is provided with a valve or the like.

さらに、汚泥流入管17には原汚泥がポンプ2
3によつて圧入されるよう構成されている。ま
た、上澄液排出管21には流量調整手段24を構
成する流量調整弁25が設けられている。
Furthermore, the raw sludge is transferred to the sludge inflow pipe 17 from the pump 2.
3, it is configured to be press-fitted. Further, the supernatant liquid discharge pipe 21 is provided with a flow rate adjustment valve 25 that constitutes a flow rate adjustment means 24 .

尚、密閉容器1の他端15側で一方の側壁面1
cの内側には凹溝部27が上下方向に形成されて
いて、この凹溝部27内に汚泥界面計28が設け
られている。
In addition, one side wall surface 1 on the other end 15 side of the airtight container 1
A concave groove 27 is formed in the vertical direction inside c, and a sludge interface meter 28 is provided within this concave groove 27.

次に本願発明の汚泥濃縮装置の作用について説
明する。モータ6によつて回転スクリユー2緩や
かに回転駆動する一方、原汚泥をポンプ23によ
つて加圧して一定の流入量で汚泥流入管17を通
して汚泥流入口16から密閉容器1の一端側14
の内部に流入させる。この流入した原汚泥は、回
転スクリユー2のスクリユー羽根4間で沈殿濃縮
される。ここで、スクリユー羽根4の傾斜板とし
ての機能および複数の傾斜板10によるより効果
的な沈殿促進機能によつて、効果的な濃縮が行な
われる。そして密閉容器1内の下部に沈降分離さ
れた濃縮液は、スクリユー羽根4によつて矢印a
方向に進み濃縮液排出口18側に掻き寄せられ
て、その濃縮液排出口18から濃縮液排出口管2
0を通して排出される。また、濃縮液から分離さ
れた上澄液は、複数の傾斜板10間を密閉容器1
内の上部側に向かつて矢印b方向で示すように斜
めに上昇する。そして、この上昇された上澄液は
密閉容器1内の上部の流路11を上澄液排出口1
9に向かつて矢印c方向に送られ、その上澄液排
出口19から上澄液排出管21を通して排出され
る。
Next, the operation of the sludge thickening device of the present invention will be explained. While the rotary screw 2 is driven to rotate slowly by the motor 6, the raw sludge is pressurized by the pump 23 and passed through the sludge inlet pipe 17 at a constant inflow rate from the sludge inlet 16 to the one end side 14 of the closed container 1.
flow into the interior of the This raw sludge that has flowed in is precipitated and concentrated between the screw blades 4 of the rotating screw 2. Here, effective concentration is achieved by the function of the screw blade 4 as an inclined plate and the more effective precipitation promoting function by the plurality of inclined plates 10. Then, the concentrated liquid that has settled and separated in the lower part of the closed container 1 is moved by the screw blade 4 to the arrow a
direction, the concentrated liquid is scraped up to the side of the concentrated liquid outlet 18, and the concentrated liquid is drawn from the concentrated liquid outlet 18 to the concentrated liquid outlet pipe 2.
Exhausted through 0. Further, the supernatant liquid separated from the concentrated liquid is passed between the plurality of inclined plates 10 into a sealed container 1.
It rises diagonally towards the upper side of the interior as shown in the direction of arrow b. Then, this raised supernatant liquid flows through the upper channel 11 in the closed container 1 to the supernatant liquid outlet 1.
9 in the direction of arrow c, and is discharged from the supernatant liquid discharge port 19 through the supernatant liquid discharge pipe 21.

この際、流量調整弁25を調整すると上澄液の
排出量の調整により、濃縮液の排出量制御を行う
ことができる。尚、この流量調整弁25の調整
は、通常自動調整で行う(流入量との差が濃縮液
量となる)がこの流量調整弁25は手動で調整し
てもよいし、あるいは、ポンプ23の流量コント
ロールに連動させてもよい。
At this time, by adjusting the flow rate regulating valve 25, the discharge amount of the concentrated liquid can be controlled by adjusting the discharge amount of the supernatant liquid. The flow rate adjustment valve 25 is normally adjusted automatically (the difference with the inflow amount is the concentrated liquid amount), but the flow rate adjustment valve 25 may be adjusted manually, or by adjusting the pump 23. It may be linked to flow rate control.

また、この時、密閉容器1内に設けられている
汚泥界面計28が所定範囲から外れないように、
ポンプ23による原汚泥の流入量および濃縮液の
排出量を調節するのが好ましい。
At this time, in order to prevent the sludge interface meter 28 provided in the closed container 1 from deviating from a predetermined range,
It is preferable to adjust the inflow amount of raw sludge and the discharge amount of concentrated liquid by the pump 23.

しかして、ポンプ23によつて圧入される原汚
泥の流入量が一定である状態で、流量調整弁25
によつて濃縮液の排出量制御を行えば濃縮液の濃
縮比を自由に調整することができて、一定濃度の
濃縮液を得ることができる。しかもこの際、上澄
液排出管21に設けた流量調整弁25の調整によ
つて、濃縮液の排出量を調整するので、その流量
調整弁25が濃縮汚泥によつて目詰まりを生じた
り、粘度の影響を受けることが全くなく、その流
量調整弁25による調整を容易にかつ正確に行え
る。
Therefore, in a state where the inflow amount of raw sludge that is pressurized by the pump 23 is constant, the flow rate regulating valve 25
By controlling the discharge amount of the concentrated liquid, the concentration ratio of the concentrated liquid can be freely adjusted, and a concentrated liquid having a constant concentration can be obtained. Moreover, at this time, since the discharge amount of the concentrated liquid is adjusted by adjusting the flow rate adjustment valve 25 provided in the supernatant liquid discharge pipe 21, the flow rate adjustment valve 25 may become clogged with concentrated sludge. It is completely unaffected by viscosity and can be easily and accurately adjusted by the flow rate adjustment valve 25.

また、濃縮液の排出量制御は、上澄液排出口側
に設けた流量調整手段24によつて行うが、流量
調整弁25を解放した場合、ほぼ全量が上澄液排
出口19より排出されるように濃縮液排出管20
を立ち上げる等の手段を講じてある。
Further, the discharge amount of the concentrated liquid is controlled by the flow rate adjusting means 24 provided on the supernatant liquid outlet side, but when the flow rate adjusting valve 25 is released, almost the entire amount is discharged from the supernatant liquid outlet 19. Concentrate discharge pipe 20
Measures have been taken such as launching a.

ところで、密閉容器1内に流入する原汚泥に凝
集剤(特に、有機高分子凝集剤)を添加すると汚
泥は密なブロツクを形成するので非常に効果的な
濃縮が行える。即ち、原汚泥に凝集剤を添加して
おくと、密閉容器1内で沈降分離された濃縮液が
濃縮液排出口18側へ移動する際に、スクリユー
羽根4によつて移動されるので、上記濃縮液の汚
泥ブロツクがより硬い状態に結合して粒状化され
る。そして、粒状化された汚泥は次工程における
脱水を非常に効果的に行なうことができる。
By the way, when a flocculant (particularly an organic polymer flocculant) is added to the raw sludge flowing into the closed container 1, the sludge forms a dense block, so that very effective concentration can be achieved. That is, if a flocculant is added to the raw sludge, when the concentrated liquid that has been sedimented and separated in the closed container 1 is moved to the concentrated liquid outlet 18 side, it is moved by the screw blade 4, so that the above-mentioned The sludge blocks of the concentrate are combined into a harder state and granulated. The granulated sludge can be very effectively dehydrated in the next step.

尚、上述の実施例では密閉容器1内に沈殿促進
機能を果たす傾斜板10を設けたので、装置自体
を縦型にでき、敷地面積の節約が行える。
In the above-mentioned embodiment, since the inclined plate 10 which performs the function of promoting precipitation is provided in the closed container 1, the apparatus itself can be made vertical, and the site area can be saved.

以上のように、この発明の一実施例について述
べたが、これに何等限定されることなく、この発
明の技術的思想にもとづいて各種の有効な変更が
可能である。例えば、原汚泥を圧入させる手段は
ポンプ以外のもの、たとえば高架汚泥槽のように
一定の汚泥を圧入できるものであれば他のもので
あつても良い。また、流量調整手段は流量調整弁
25以外のものであつても流量の調整を行なえる
ものであれば良い。
As described above, one embodiment of the present invention has been described, but the present invention is not limited to this in any way, and various effective changes can be made based on the technical idea of the present invention. For example, the means for pressurizing raw sludge may be other than a pump, such as an elevated sludge tank, as long as it can pressurize a certain amount of sludge. Further, the flow rate adjustment means may be other than the flow rate adjustment valve 25 as long as it can adjust the flow rate.

また、この実施例では、回転スクリユーのスク
リユー羽根を二重スクリユーにしたものを示した
が、一重あるいは三重スクリユーであつてもよ
く、一般的には、つる巻角が大きいほうが良いの
で、多重スクリユーが好ましい。
Also, in this embodiment, the screw blade of the rotary screw is shown as a double screw, but it may be a single screw or a triple screw.Generally speaking, the larger the helical angle, the better. is preferred.

また、実施例では、スクリユー羽根を連続羽根
にしたものを示したが、スクリユー羽根に所定間
で欠除部を設けたカツトスクリユーとしても良
い。これによつて、上澄液による沈殿汚泥の撒き
あげを防止できる。ただし、この時には短絡が生
じないように、欠除部同士が軸方向において一直
線にならないようにするのが好ましい。
Further, in the embodiment, the screw blade is shown as a continuous blade, but a cut screw blade may be used in which the screw blade is provided with cutout portions at predetermined intervals. This can prevent the supernatant liquid from throwing up the settled sludge. However, at this time, it is preferable that the cutout parts are not in a straight line with each other in the axial direction to prevent a short circuit from occurring.

〔発明の効果〕〔Effect of the invention〕

以上のように、この発明によれば、回転スクリ
ユーと複数の傾斜板とを収納した容器が密閉容器
となつているため、この種の開放形容器の場合に
比して臭気対策が万全となり、また、前記密閉容
器の汚泥流入口側に汚泥圧入手段を設けたことに
より、汚泥流入側での制御が可能となる。
As described above, according to the present invention, since the container housing the rotating screw and the plurality of inclined plates is a closed container, odor control is more thorough than in the case of this type of open container. Further, by providing the sludge injection means on the sludge inflow side of the closed container, control on the sludge inflow side becomes possible.

しかも、前記傾斜板のそれぞれの下端が回転ス
クリユーのスクリユー羽根の外周に近接している
ため、前記密閉容器内に圧入された流入汚泥を、
前記各傾斜板のそれぞれによつて回転スクリユー
側の略全長に亘つて効率よく沈殿させることがで
きる。
Moreover, since the lower ends of each of the inclined plates are close to the outer periphery of the screw blades of the rotating screw, the inflow sludge press-fitted into the closed container is
Each of the inclined plates allows efficient precipitation over substantially the entire length on the rotating screw side.

また、前記沈殿汚泥は、回転スクリユーによつ
て濃縮されながら濃縮液排出口に向つて移送され
るが、この場合にあつても、上述のように回転ス
クリユーのスクリユー羽根の外周に下端が近接し
た前記各傾斜板によつて、前記回転スクリユーに
よる汚泥濃縮効率および汚泥濃縮液の移送効率が
向上する。
Further, the settled sludge is transferred toward the concentrated solution outlet while being concentrated by the rotating screw, but even in this case, as described above, the lower end of the rotating screw is close to the outer periphery of the screw blade of the rotating screw. Each of the inclined plates improves the sludge concentration efficiency and the sludge concentrate transfer efficiency by the rotating screw.

さらに、前記汚泥濃縮液から分離した分離液は
密閉容器の上澄液排出口から排出されるが、この
際、その上澄液排出量を流量調整手段で調整する
ことによつて、汚泥の濃縮度合を適度に調整する
ことができ、もつて、濃縮汚泥の目詰まりや粘度
影響を受けることなく一定濃度の濃縮液を得るこ
とができ、濃縮汚泥の管理が頗ぶる容易となるな
どの効果がある。
Further, the separated liquid separated from the sludge concentrate is discharged from the supernatant liquid outlet of the closed container, and at this time, the amount of supernatant liquid discharged is adjusted by the flow rate adjusting means to concentrate the sludge. The concentration can be adjusted appropriately, and in the end, a concentrated liquid with a constant concentration can be obtained without being affected by the clogging or viscosity of the thickened sludge, and the management of the thickened sludge becomes extremely easy. be.

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

第1図はこの発明の一実施例の垂直縦断面図、
第2図は同垂直横断面図である。 1は密閉容器、1aは密閉容器の下部壁、2は
回転スクリユー、14は密閉容器の一端、15は
密閉容器の他端、16は汚泥流入口、18は濃縮
液排出口、19は上澄液排出口、21は上澄液排
出管、24は流量調整手段、25は流量調整弁。
FIG. 1 is a vertical longitudinal sectional view of an embodiment of the present invention;
FIG. 2 is a vertical cross-sectional view of the same. 1 is a sealed container, 1a is a lower wall of the sealed container, 2 is a rotating screw, 14 is one end of the sealed container, 15 is the other end of the sealed container, 16 is a sludge inlet, 18 is a concentrated liquid outlet, and 19 is a supernatant. 21 is a supernatant liquid discharge pipe, 24 is a flow rate adjustment means, and 25 is a flow rate adjustment valve.

Claims (1)

【特許請求の範囲】[Claims] 1 一端に汚泥流入口を有して他端下部に濃縮液
排出口が、且つ、他端上部に上澄液排出口がそれ
ぞれ設けられた密閉容器と、この密閉容器の内底
部に収納配置された回転スクリユーと、前記密閉
容器内における前記回転スクリユーの上方に収納
配置され、該回転スクリユーのスクリユー羽根の
外周に下端が近接して斜め上方に並行離間状態で
傾斜し、且つ、前記密閉容器の上部壁との間で流
路を形成する複数の傾斜板と、前記上澄液排出口
の系統に設けられた流量調節手段と、前記汚泥流
入口から前記密閉容器内に原汚泥を圧入供給する
汚泥圧入手段とを備えて成ることを特徴とする汚
泥濃縮装置。
1. A closed container having a sludge inlet at one end, a concentrated liquid outlet at the lower end of the other end, and a supernatant liquid outlet at the upper end of the other end, and a sealed container which is housed in the inner bottom of the closed container. a rotating screw that is housed above the rotating screw in the sealed container, a lower end of which is close to the outer periphery of the screw blade of the rotating screw, and inclined diagonally upward in a parallel spaced state; A plurality of inclined plates forming a flow path with the upper wall, a flow rate adjusting means provided in the system of the supernatant liquid outlet, and raw sludge being press-injected into the closed container from the sludge inlet. A sludge thickening device comprising: sludge injection means.
JP61204690A 1986-08-29 1986-08-29 Sludge concentration apparatus Granted JPS6359398A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61204690A JPS6359398A (en) 1986-08-29 1986-08-29 Sludge concentration apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61204690A JPS6359398A (en) 1986-08-29 1986-08-29 Sludge concentration apparatus

Publications (2)

Publication Number Publication Date
JPS6359398A JPS6359398A (en) 1988-03-15
JPH0468039B2 true JPH0468039B2 (en) 1992-10-30

Family

ID=16494695

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61204690A Granted JPS6359398A (en) 1986-08-29 1986-08-29 Sludge concentration apparatus

Country Status (1)

Country Link
JP (1) JPS6359398A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2612339B2 (en) * 1989-04-18 1997-05-21 三菱電機株式会社 Electronic equipment housing
CN105413260A (en) * 2015-12-21 2016-03-23 天津焜日科技开发有限公司 Sand settling tank used for sewage treatment

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5335478U (en) * 1976-09-01 1978-03-28
US4419451A (en) * 1981-05-21 1983-12-06 Becton Dickinson And Company Oxygen scavenging system for anaerobiosis
JPS5867503U (en) * 1981-10-27 1983-05-09 壽化工機株式会社 precipitation equipment
JPS618110A (en) * 1984-06-20 1986-01-14 Shigeki Watanabe Precipitation separation apparatus in sewage treatment

Also Published As

Publication number Publication date
JPS6359398A (en) 1988-03-15

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