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JP2001293305A - Flocculation/precipitation apparatus - Google Patents

Flocculation/precipitation apparatus

Info

Publication number
JP2001293305A
JP2001293305A JP2000113309A JP2000113309A JP2001293305A JP 2001293305 A JP2001293305 A JP 2001293305A JP 2000113309 A JP2000113309 A JP 2000113309A JP 2000113309 A JP2000113309 A JP 2000113309A JP 2001293305 A JP2001293305 A JP 2001293305A
Authority
JP
Japan
Prior art keywords
stirring
sedimentation
water
mixing
tank
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
JP2000113309A
Other languages
Japanese (ja)
Inventor
Toshihiro Tamura
敏裕 田村
Yoshihiro Tanimoto
好広 谷本
Keiichi Fujimoto
恵一 藤本
Kozo Akamatsu
功三 赤松
Isao Yoneda
勲 米田
Hiroyuki Takami
博之 高見
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric Co Ltd
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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP2000113309A priority Critical patent/JP2001293305A/en
Publication of JP2001293305A publication Critical patent/JP2001293305A/en
Pending legal-status Critical Current

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  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a precipitation separator of a simple structure which can precipitate/separate sludge efficiently and purify drainage. SOLUTION: A flocculation/precipitation tank 9 is divided into an agitation/ mixing part 91 having a flocculant charging means for charging a flocculant directly and an agitation means for agitating/mixing the charged flocculant and introduced treatment water and a precipitation/separation part 92 for precipitating/separating flocculated sludge by a partition 93 with the lower part sides communicating with each other, and the cross-sectional area of the part 92 is formed to be larger than that of the part 91. A partition 94 which is immersed in water with the upper and lower parts communicating with each other is provided in the part 91, the agitation blade 131 of the agitation means and the inlet of the flocculant charging means are formed on the treatment water inflow side seen from the partition 94, and a communication port 96 with the part 92 is formed in the lower part on the opposite side.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本願発明は凝集沈殿装置に係
わり、特に一般家庭用のディスポーザ排水処理システム
などに用いて好適な処理を行うことができる凝集沈殿装
置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a coagulating sedimentation apparatus, and more particularly to a coagulating sedimentation apparatus capable of performing a suitable treatment for use in a general household disposer wastewater treatment system.

【0002】[0002]

【従来の技術】特開平11−192493号公報(C0
2F 1/52)には、攪拌槽及び沈殿槽を一体的に構
成した処理タンクと、上記攪拌槽を複数に分割しつつ一
部を連通させる仕切板と、この仕切板によって分割され
た各室ごとに設置された攪拌機と、該各室のうちの一室
の上方に設けられた凝集剤投入部と、沈殿槽を複数に分
割しつつ一部を連通させる仕切板と、この仕切板によっ
て分割されたうちの一室に設けられた排水部と、攪拌槽
の一室から沈殿槽の一室へフロック含有水を移すための
流水部とを備えてなる濁水処理装置が開示されている。
そして、上記処理タンクは、その半分を攪拌槽とし、残
りの半分を沈殿槽としている。
2. Description of the Related Art Japanese Patent Application Laid-Open No. 11-192493 (C0
2F 1/52), a treatment tank in which a stirring tank and a sedimentation tank are integrally formed, a partition plate that divides the stirring tank into a plurality and partially communicates, and each of the chambers divided by the partition plate. A stirrer installed for each of the chambers, a flocculant charging section provided above one of the chambers, a partition plate that divides the sedimentation tank into a plurality and communicates a part thereof, and is divided by the partition plate. There is disclosed a turbid water treatment apparatus including a drainage unit provided in one of the chambers and a flowing water unit for transferring floc-containing water from one chamber of a stirring tank to one chamber of a sedimentation tank.
The processing tank has a half as a stirring tank and the other half as a sedimentation tank.

【0003】また、一般的に、凝集剤は凝集反応を起こ
しやすくするため、溶解槽などで一度希釈処理してから
投入したり、急速と緩速の攪拌槽が用いられていた。
[0003] In general, a coagulant is generally diluted once in a dissolving tank or the like and then charged, or a fast and slow stirring tank is used in order to easily cause a coagulation reaction.

【0004】[0004]

【発明が解決しようとする課題】上記の公報に開示のも
のでは、攪拌槽及び沈殿槽をそれぞれ複数に分割すると
共に、攪拌槽の複数に分割された各室にはそれぞれ攪拌
機が備えられた複雑な構造をしており、大型化やコスト
高となって、一般家庭用のディスポーザ排水処理システ
ムなどには適さない。
In the apparatus disclosed in the above publication, the stirring tank and the sedimentation tank are each divided into a plurality of parts, and each of the divided chambers is provided with a stirrer in each of the plurality of divided chambers. It is not suitable for general household disposer wastewater treatment systems, etc.

【0005】また、凝集剤を溶解槽で一度希釈処理して
から投入したり、急速と緩速の攪拌槽を用いるものも、
やはり、凝集剤の劣化の進行、大型化やコスト高を招
き、一般家庭用のディスポーザ排水処理システムなどに
は適さない。
[0005] In addition, the coagulant may be diluted once in a dissolving tank and then charged, or those using a rapid and slow stirring tank may be used.
After all, the deterioration of the coagulant, the increase in size, and the increase in cost are caused, so that it is not suitable for a general household disposer wastewater treatment system.

【0006】そこで、本願発明はこのような課題を解決
するためになされたものであり、簡単な構造で、汚泥の
沈殿分離を効率良く行うことができ、排出水を浄化でき
る沈殿分離装置を提供することを目的とするものであ
る。
Accordingly, the present invention has been made to solve such a problem, and provides a sedimentation / separation apparatus capable of efficiently performing sludge sedimentation / separation with a simple structure and purifying discharged water. It is intended to do so.

【0007】[0007]

【課題を解決するための手段】上記のような目的を達成
するために、本願発明は、凝集沈殿槽を、凝集剤を直接
投入する凝集剤投入手段及び投入された凝集剤と流入し
た被処理水を攪拌混合する攪拌手段を備えた攪拌混合部
と、凝集した汚泥を沈殿分離する沈殿分離部とに、下部
側が連通した隔壁で区画すると共に、前記沈殿分離部の
横断面積を前記攪拌混合部の横断面積より大きく形成し
たことを特徴とするものである。
SUMMARY OF THE INVENTION In order to achieve the above object, the present invention relates to a coagulating sedimentation tank, comprising: a coagulant charging means for directly charging a flocculant; A stirring / mixing unit provided with a stirring means for stirring and mixing water, and a sedimentation / separation unit for sedimentation / separation of aggregated sludge, are partitioned by a partition having a lower side communicating therewith, and the cross-sectional area of the sedimentation / separation unit is set to the stirring / mixing unit. Is formed so as to be larger than the cross-sectional area.

【0008】さらに、前記攪拌混合部に、水没して上下
が連通する隔壁を備え、この隔壁から見て被処理水流入
側に前記攪拌手段の攪拌羽根と前記凝集剤投入手段の投
入口が設けられ、その反対側の下部に前記沈殿分離部と
の連通口が形成されて成ることを特徴とするものであ
る。
Further, the stirring and mixing section is provided with a partition which is submerged in water and communicates vertically, and a stirring blade of the stirring means and an input port of the coagulant charging means are provided on the inflow side of the water to be treated as viewed from the partition. And a communication port with the sedimentation / separation part is formed in the lower part on the opposite side.

【0009】また、前記攪拌手段による攪拌水流が攪拌
羽根の位置で上向きに流れるように攪拌羽根の回転方向
を設定したことを特徴とするものである。
Further, the rotation direction of the stirring blade is set so that the stirring water flow by the stirring means flows upward at the position of the stirring blade.

【0010】また、前記沈殿分離部に、前記攪拌混合部
との連通口と間隔を空けて、対向する側壁に向かって上
方に傾斜して配置された整流板を備えたことを特徴とす
るものである。
[0010] Further, the sedimentation separation section is provided with a flow straightening plate which is arranged at an interval from a communication port with the stirring and mixing section and is inclined upward toward an opposing side wall. It is.

【0011】また、前記攪拌手段における攪拌羽根の取
付軸に軸振れを防止する軸振れ防止手段を備えたことを
特徴とするものである。
[0011] Further, the present invention is characterized in that a shaft for preventing shaft runout is provided on a shaft for mounting the stirring blade in the stirring unit.

【0012】[0012]

【発明の実施の形態】以下、本願発明の実施形態を図面
を参照して詳細に説明する。
Embodiments of the present invention will be described below in detail with reference to the drawings.

【0013】図1は、本願発明による凝集沈殿装置が適
用されるディスポーザ排水処理システムにおける排水処
理部の実施形態を示す全体構成図で、(a)は上面図、
(b)は側断面図である。
FIG. 1 is an overall configuration diagram showing an embodiment of a wastewater treatment section in a disposer wastewater treatment system to which a coagulation sedimentation device according to the present invention is applied, (a) is a top view,
(B) is a side sectional view.

【0014】本実施形態の排水処理部1は、図示しない
ディスポーザから流入する排水の流路を切り替える流路
切替装置2と、この流路切替装置2を介してディスポー
ザ使用時以外の通常の台所排水が流入する雑排水流量調
整槽3と、同じく流路切替装置2を介してディスポーザ
使用時の生ごみ破砕液が流入すると共に後述の凝集沈殿
槽9からエアリフトポンプ11により汚泥が返送される
生ごみ流量調整槽4と、この生ごみ流量調整槽4からエ
アリフトポンプ5により移送される固液混合物を固体分
と液体分に分離する固液分離装置6と、この固液分離装
置6で分離された液体分が投入されると共に上記雑排水
流量調整槽3からエアリフトポンプ7により移送される
台所排水及び同じく雑排水流量調整槽3に形成されたオ
ーバーフロー口31からの台所排水が流入する担体流動
槽(曝気槽)8と、この担体流動槽8から自然流下によ
り流入する被処理水中の汚泥分を凝集させて沈殿分離す
る凝集沈殿槽9と、上記固液分離装置6で分離されて投
入される固体分と収納された微生物担体とを攪拌体によ
り攪拌混合して、担体に生息する微生物によりコンポス
ト化(堆肥化)するコンポスト化装置10とから成って
いる。
The wastewater treatment section 1 of the present embodiment includes a flow passage switching device 2 for switching a flow passage of wastewater flowing from a disposer (not shown), and a normal kitchen wastewater except when the disposer is used via the flow passage switching device 2. The garbage crushed liquid at the time of using the disposer flows in through the miscellaneous drainage flow rate adjusting tank 3 and the flow path switching device 2, and sludge is returned from the coagulating sedimentation tank 9 described below by the air lift pump 11. The flow rate adjusting tank 4, a solid-liquid separating device 6 for separating a solid-liquid mixture transferred from the garbage flow adjusting tank 4 by an air lift pump 5 into a solid component and a liquid component, and the solid-liquid separating device 6 Kitchen drainage, which is supplied with liquid and is transferred from the wastewater flow control tank 3 by the air lift pump 7, and an overflow port 3 formed in the wastewater flow control tank 3 as well. A carrier fluidizing tank (aeration tank) 8 into which kitchen wastewater flows from, a coagulating sedimentation tank 9 for aggregating and separating sediment of sludge in the water to be treated which flows in by gravity from the carrier fluidizing tank 8, And a composting device 10 in which the solid component separated and introduced by the separating device 6 and the stored microbial carrier are agitated and mixed by a stirrer and composted (composted) by microorganisms inhabiting the carrier. .

【0015】なお、エアリフトポンプとは、水中に挿入
されたパイプの中に空気を吹き込み、その空気の上昇力
により水や固体を持ち上げ、移送する原理のポンプのこ
とであり、エアリフト管とブロワポンプから成り、ブロ
ワポンプは多方弁等を用いて切り替えることにより共用
化することができる。
The air lift pump is a pump that blows air into a pipe inserted into water, lifts and transfers water and solids by the rising force of the air, and includes an air lift pipe and a blower pump. And the blower pump can be shared by switching using a multi-way valve or the like.

【0016】上記システムにおいては、ディスポーザ使
用終了後、生ごみ破砕液が投入された生ごみ流量調整槽
4に凝集沈殿槽9の沈殿汚泥をエアリフトポンプ11に
より返送する。その後、沈殿のための一定時間が経過す
るのを待って、生ごみ流量調整槽4の沈殿物(破砕生ご
み及び返送汚泥)をエアリフトポンプ5により固液分離
装置6に移送し、次に凝集沈殿槽9の沈殿汚泥をエアリ
フトポンプ11により生ごみ流量調整槽4に返送し、さ
らに雑排水流量調整槽3の台所排水をエアリフトポンプ
7により担体流動槽8に移送し、これらを次のディスポ
ーザ使用があるまで一定間隔でそれぞれ定量ずつ繰り返
す。
In the above system, after the use of the disposer is completed, the settled sludge in the coagulation sedimentation tank 9 is returned to the garbage flow rate adjustment tank 4 into which the garbage crushed liquid has been introduced by the air lift pump 11. Thereafter, after a certain period of time for sedimentation has elapsed, the sediment (crushed garbage and returned sludge) in the garbage flow control tank 4 is transferred to the solid-liquid separation device 6 by the air lift pump 5 and then coagulated. The settled sludge in the settling tank 9 is returned to the garbage flow rate adjusting tank 4 by the air lift pump 11, and the kitchen wastewater in the miscellaneous wastewater flow rate adjusting tank 3 is transferred to the carrier flowing tank 8 by the air lift pump 7, and these are used in the next disposer. Repeat at fixed intervals until there is a quantity.

【0017】上記のように、雑排水流量調整槽3の台所
排水や生ごみ流量調整槽4の沈殿物の移送を一定間隔で
定量ずつ行うと共に、雑排水流量調整槽3から担体流動
槽8へのオーバーフロー口31を設けることにより、小
容積の雑排水流量調整槽3や生ごみ流量調整槽4でも溢
れることなく通常のディスポーザ使用や台所排水に対応
することができ、また、後述するようにして簡単な構造
で実現した凝集沈殿槽9により、一般家庭用としてシス
テム全体の小型化や低コスト化を図ることができるよう
になっている。
As described above, the transfer of the kitchen drainage in the gray water flow control tank 3 and the sediment in the raw garbage flow control tank 4 are performed at regular intervals by a fixed amount, and the transfer from the gray water flow control tank 3 to the carrier flow tank 8 is performed. By providing the overflow port 31 of the above, it is possible to cope with a normal disposer use or kitchen drainage without overflowing even in the small volume miscellaneous drainage flow rate adjusting tank 3 and the garbage flow rate adjusting tank 4, and as described later. The coagulation sedimentation tank 9 realized with a simple structure enables the entire system to be reduced in size and cost for general household use.

【0018】図2は上記凝集沈殿槽9の本実施形態によ
る構成及び作用を示す斜視図、図3は側断面図である。
FIG. 2 is a perspective view showing the structure and operation of the coagulation / sedimentation tank 9 according to this embodiment, and FIG. 3 is a side sectional view.

【0019】本実施形態の凝集沈殿槽9は、図3に示す
ように、凝集剤を濃縮状態のまま直接投入する凝集剤投
入装置12及び投入された凝集剤と流入した被処理水を
攪拌混合する攪拌装置13を備えた攪拌混合部91と、
凝集した汚泥を沈殿分離する沈殿分離部92とに、下部
側が連通した隔壁93で区画されている。上記隔壁93
は、沈殿分離部92の横断面積の方が攪拌混合部91の
横断面積より大きくなるような位置に形成されている。
As shown in FIG. 3, the coagulating sedimentation tank 9 of the present embodiment includes a coagulant charging device 12 for directly charging the coagulant in a concentrated state, and a stirring and mixing of the supplied coagulant and the inflowing water to be treated. A stirring and mixing section 91 provided with a stirring device 13 for performing
The lower part is partitioned by a partition wall 93 communicating with a sedimentation / separation part 92 that sediments and separates the flocculated sludge. The partition 93
Is formed at a position such that the cross-sectional area of the sedimentation / separation section 92 is larger than the cross-sectional area of the stirring / mixing section 91.

【0020】さらに、上記攪拌混合部91には、水没し
て上下が連通する隔壁94が備えられており、この隔壁
94から見て、担体流動槽8からの被処理水流入口95
側の上部に攪拌装置13の攪拌羽根131と凝集剤投入
装置12の投入口121が設けられ、その反対側の下部
に沈殿分離部92との連通口96が形成されている。
Further, the stirring and mixing section 91 is provided with a partition wall 94 which is submerged in water and communicates with the upper and lower sides.
A stirring blade 131 of the stirring device 13 and a charging port 121 of the flocculant charging device 12 are provided in an upper portion on the side, and a communication port 96 with the sedimentation / separation section 92 is formed in a lower portion on the opposite side.

【0021】上記攪拌装置13は、攪拌モータ132で
駆動される攪拌羽根131の回転によって生じる攪拌水
流aが攪拌羽根131の位置で上向きに流れるように回
転方向が設定されている。すなわち、この攪拌水流a
は、矢印で示すように、攪拌羽根131から水面に向か
って上昇し、隔壁94の反対側に回って、隔壁94の下
部から攪拌羽根131に戻る循環水流となる。
The rotation direction of the stirring device 13 is set so that the stirring water flow a generated by the rotation of the stirring blade 131 driven by the stirring motor 132 flows upward at the position of the stirring blade 131. That is, this stirring water flow a
As shown by an arrow, a circulating water flow rises from the stirring blade 131 toward the water surface, turns to the opposite side of the partition 94, and returns from the lower part of the partition 94 to the stirring blade 131.

【0022】また、上記攪拌装置13は、攪拌羽根13
1の取付軸133が片持ち構造となるため、軸振れが生
じ易く、使用者が旅行などで不在の時など、排水の流入
が長期間なく蒸発等により凝集沈殿槽9の水位が下がっ
て攪拌羽根131が水面上に現れ、無負荷状態で高速回
転するような場合には、攪拌羽根131の軸振れによる
振動(暴れ)が生じて、攪拌羽根131等が側壁に当た
って破損することがある。
The stirring device 13 includes a stirring blade 13
Since the first mounting shaft 133 has a cantilever structure, shaft runout is likely to occur, and when the user is absent on a trip or the like, there is no long-term inflow of wastewater, and the water level of the coagulating sedimentation tank 9 is lowered due to evaporation or the like, and stirring is performed. When the blade 131 appears on the water surface and rotates at a high speed in a no-load state, vibration (roughness) due to the shaft runout of the stirring blade 131 occurs, and the stirring blade 131 may hit the side wall and be damaged.

【0023】そこで、本実施形態においては、攪拌モー
タ132を保持するモータホルダー134の下部側を下
方に伸ばして、その上下端の間隔を空けた2箇所に攪拌
羽根131の取付軸133を支持する軸受135,13
5を設けて、攪拌羽根131の取付軸133の軸振れを
防ぐようにしている。これは、上記のような形状のモー
タホルダー134を樹脂で成形して、攪拌羽根131の
取付軸133を通す孔を形成し、その上下端にメタル軸
受等の軸受135を固着することにより、比較的容易に
実現することができる。
Therefore, in the present embodiment, the lower side of the motor holder 134 holding the stirring motor 132 is extended downward, and the mounting shaft 133 of the stirring blade 131 is supported at two places spaced apart at the upper and lower ends. Bearings 135, 13
5 is provided to prevent the shaft 133 of the stirring blade 131 from swinging. This is achieved by molding the motor holder 134 having the above-mentioned shape with resin, forming a hole through which the mounting shaft 133 of the stirring blade 131 passes, and fixing a bearing 135 such as a metal bearing at upper and lower ends thereof. Can be easily achieved.

【0024】一方、沈殿分離部92には、前記攪拌混合
部91との隔壁93に沿って汚泥返送用のエアリフト管
111とこのエアリフト管111の下部側に図示しない
ブロワポンプからの送気を供給するための送気管112
が挿入されており、このエアリフト管111の下部側に
沈殿汚泥が溜まるように槽底部の片側は傾斜面97とな
っている。また、この沈殿分離部92の上部には、上澄
み水を下水道等に排出するための排出口98が形成され
ている。
On the other hand, an air lift pipe 111 for returning sludge and air supplied from a blower pump (not shown) are supplied to the sedimentation / separation section 92 along a partition wall 93 with the stirring / mixing section 91 and a lower portion of the air lift pipe 111. Air pipe 112 for
Is inserted, and one side of the tank bottom has an inclined surface 97 so that sedimentation sludge accumulates on the lower side of the air lift pipe 111. In addition, a discharge port 98 for discharging the supernatant water to a sewer or the like is formed at an upper portion of the sedimentation / separation unit 92.

【0025】そして、本実施形態では、攪拌混合部91
との連通口96と間隔を空けて、対向する側壁に向かっ
て槽底部の傾斜面97とほぼ平行に上方に傾斜して配置
された整流板99が取り付けられており、上記エアリフ
ト管111及び送気管112が通る部分には切欠き99
aが形成されている。この整流板99は、攪拌混合部9
1内で循環する攪拌水流aに伴い連通口96を介して沈
殿分離部92側に生じる攪拌水流bが上昇するのを抑え
る働きをする。
In the present embodiment, the stirring and mixing section 91
A flow rectifying plate 99 is mounted at a distance from the communication port 96 with the air lift pipe 111 and is inclined upward and substantially parallel to the inclined surface 97 of the tank bottom toward the opposing side wall. Notch 99 where trachea 112 passes
a is formed. The current plate 99 is provided in the stirring and mixing section 9.
It functions to suppress the rise of the stirred water flow b generated on the sedimentation / separation section 92 side through the communication port 96 due to the stirred water flow a circulating in 1.

【0026】上述した構成において、担体流動槽8から
流入口95を介して流入した被処理水は、凝集剤投入装
置12から投入される濃縮状態のままの凝集剤が添加さ
れると共に攪拌羽根131で攪拌される。
In the above-described configuration, the water to be treated that has flowed in from the carrier fluidizing tank 8 through the inlet 95 is added with the concentrated coagulant supplied from the coagulant charging device 12 and the stirring blade 131 And stirred.

【0027】本実施形態では、攪拌混合部91には上下
で連通する隔壁94が設置されており、この隔壁94の
上下を通って循環する攪拌水流aが生じるため、直接投
入された凝集剤は循環する攪拌水流aに乗って攪拌羽根
131を通過する時に分散され、被処理水と効率良く混
じり合うことができる。
In this embodiment, the stirring and mixing section 91 is provided with a partition wall 94 communicating vertically, and a stirring water stream a circulating above and below the partition wall 94 is generated. The particles are dispersed when passing through the stirring blade 131 on the circulating stirring water flow a, and can be efficiently mixed with the water to be treated.

【0028】このように、簡単な構造で、直接投入され
た濃縮状態の凝集剤と流入した被処理水とを効率良く攪
拌混合できるため、凝集剤を一度希釈処理してから投入
したり、急速と緩速の攪拌槽を用いることなく、凝集反
応が促進され、凝集剤と汚泥との反応性を良くすること
で、汚泥の沈降性を向上することができる。
As described above, with a simple structure, the directly supplied concentrated coagulant and the inflowing water to be treated can be efficiently stirred and mixed. The coagulation reaction is promoted without using a slow stirring tank and the reactivity between the coagulant and the sludge is improved, whereby the sedimentation of the sludge can be improved.

【0029】また、攪拌混合部91と沈殿分離部92と
を区画する隔壁93の下部に連通口96が設けられてお
り、攪拌混合されて凝集された汚泥を含む被処理水は連
通口96を介して沈殿分離部92に移動し、汚泥が沈殿
分離される。
A communication port 96 is provided below the partition wall 93 for partitioning the stirring / mixing section 91 and the sedimentation / separation section 92, and the water to be treated containing the agitation-mixed and agglomerated sludge passes through the communication port 96. The sediment moves to the sedimentation / separation unit 92 through the sediment, and the sludge is sedimented and separated.

【0030】このとき、沈殿分離部92の横断面積の方
が攪拌混合部91より大きく形成されているので、被処
理水の上昇速度が低下することにより、簡単な構造で凝
集汚泥をより効率良く分離できる。
At this time, since the cross-sectional area of the sedimentation / separation section 92 is larger than that of the stirring / mixing section 91, the rising speed of the water to be treated is reduced, so that the coagulated sludge can be more efficiently formed with a simple structure. Can be separated.

【0031】また、攪拌装置13による攪拌水流aが攪
拌羽根131の位置で上向きに流れるように攪拌羽根1
31の回転方向を設定したことにより、攪拌羽根131
からの水流が下部側に形成された沈殿分離部92への連
通口96に直接流れないので、沈殿分離部96が乱れる
のを最小限に抑えることができると共に、攪拌混合部9
1の水面を盛り上げるように乱して、攪拌混合部91の
喫水部分に浮遊汚泥が付着して成長し水面を塞ぐような
不具合を防ぐことができる。
Also, the stirring blades 1 such that the stirring water flow a by the stirring device 13 flows upward at the position of the stirring blades 131.
By setting the rotation direction of 31, the stirring blade 131
Does not flow directly to the communication port 96 to the sedimentation / separation unit 92 formed on the lower side, so that disturbance of the sedimentation / separation unit 96 can be minimized and the stirring / mixing unit 9 can be used.
In this way, it is possible to prevent a problem in which suspended sludge adheres to the draft portion of the stirring and mixing section 91 and grows to obstruct the water surface.

【0032】さらに、攪拌羽根131の回転時には、図
2に矢印で示すように、攪拌混合部91における攪拌水
流aに伴って沈殿分離部92に攪拌水流bが発生する
が、この攪拌水流bの上昇を押さえ込むように傾斜して
配置された整流板99が設けられているので、汚泥が水
流に乗って上昇するのを防ぐことができる。
Further, when the stirring blade 131 rotates, a stirring water stream b is generated in the sedimentation / separation section 92 along with the stirring water stream a in the stirring / mixing section 91 as shown by an arrow in FIG. Since the flow straightening plate 99 is provided so as to be inclined so as to suppress the rise, it is possible to prevent the sludge from rising on the water flow.

【0033】従って、簡単な構造で、沈殿分離部92の
上澄み水に汚れが生じるのを防ぐことができ、浄化され
た排出水(上澄み水)を排出口98から下水道等へ放流
することができる。
Therefore, with a simple structure, it is possible to prevent the supernatant water of the sedimentation / separation section 92 from being contaminated, and to discharge the purified discharged water (supernatant water) from the discharge port 98 to the sewer. .

【0034】なお、上述した本願発明による凝集沈殿装
置は、簡単な構造で汚泥の沈殿分離を効率良く行うこと
ができるため、小型化や低コスト化が要求される一般家
庭用のディスポーザ排水処理システムなどに適用して特
に有効であるが、他の各種の水処理システムに適用して
も同様な作用効果が期待できる。
The above-mentioned coagulation and sedimentation apparatus according to the present invention can efficiently perform sedimentation and separation of sludge with a simple structure, so that a general household disposer wastewater treatment system that requires miniaturization and cost reduction. The present invention is particularly effective when applied to other types of water treatment systems.

【0035】[0035]

【発明の効果】以上のように本願発明によれば、凝集沈
殿槽を、凝集剤を直接投入する凝集剤投入手段及び投入
された凝集剤と流入した被処理水を攪拌混合する攪拌手
段を備えた攪拌混合部と、凝集した汚泥を沈殿分離する
沈殿分離部とに、下部側が連通した隔壁で区画すると共
に、沈殿分離部の横断面積を攪拌混合部の横断面積より
大きく形成したことにより、直接投入される凝集剤と流
入した被処理水を攪拌混合して凝集反応を促進すること
ができると共に、横断面積が大きく形成された沈殿分離
部で凝集汚泥を含んだ被処理水の上昇速度が低下するの
で、簡単な構造で汚泥の沈殿分離を効率良く行うことが
でき、排出水を浄化できるため、一般家庭用のディスポ
ーザ排水処理システムなどに適用して好適な凝集沈殿装
置が得られる。
As described above, according to the present invention, the coagulation sedimentation tank is provided with the coagulant charging means for directly charging the flocculant and the stirring means for stirring and mixing the charged flocculant and the inflowing water to be treated. The stirring and mixing section and the sedimentation and separation section for sedimenting and separating the agglomerated sludge are separated by a partition wall connected to the lower side, and the cross-sectional area of the sedimentation and separation section is formed to be larger than the cross-sectional area of the stirring and mixing section. Aggregation reaction can be promoted by stirring and mixing the supplied coagulant and the inflowing water to be treated, and the rising speed of the water to be treated containing coagulated sludge decreases in the sedimentation separation section with a large cross-sectional area. Therefore, the sedimentation and separation of sludge can be efficiently performed with a simple structure, and the discharged water can be purified, so that a coagulation sedimentation apparatus suitable for use in a general household disposer wastewater treatment system or the like can be obtained.

【0036】さらに、前記攪拌混合部に、水没して上下
が連通する隔壁を備え、この隔壁から見て被処理水流入
側に前記攪拌手段の攪拌羽根と前記凝集剤投入手段の投
入口が設けられ、その反対側の下部に前記沈殿分離部と
の連通口が形成されて成るものであるから、攪拌時には
攪拌羽根を通る循環水流が発生することにより、直接投
入された凝集剤と流入した被処理水とを効率良く攪拌混
合できるため、凝集剤を一度希釈処理してから投入した
り、急速と緩速の攪拌槽を用いることなく、凝集反応が
促進され、凝集剤と汚泥との反応性を良くすることで、
汚泥の沈降性を向上することができる。
Further, the stirring and mixing section is provided with a partition wall which is submerged and vertically communicates, and a stirring blade of the stirring means and an input port of the flocculant charging means are provided on the inflow side of the water to be treated as viewed from the partition wall. Since a communication port with the sedimentation separation section is formed in the lower part on the opposite side, a circulating water flow passing through the stirring blade is generated at the time of stirring, so that the coagulant that has flowed in directly with the coagulant that has been introduced. Since the treated water can be efficiently stirred and mixed, the flocculation reaction is promoted without the need to dilute the flocculant once and then throw it in, or use a rapid and slow stirring tank, and the reactivity between the flocculant and sludge is promoted. By improving
The sedimentation of sludge can be improved.

【0037】また、前記攪拌手段による攪拌水流が攪拌
羽根の位置で上向きに流れるように攪拌羽根の回転方向
を設定したことにより、攪拌羽根からの水流が下部側に
形成された沈殿分離部への連通口に直接流れないので、
沈殿分離部が乱れるのを最小限に抑えることができると
共に、攪拌混合部の水面を盛り上げるように乱して攪拌
混合部の喫水部分に浮遊汚泥が付着して成長し水面を塞
ぐような不具合を防ぐことができる。
Further, by setting the rotation direction of the stirring blade so that the stirring water flow by the stirring means flows upward at the position of the stirring blade, the water flow from the stirring blade flows to the sedimentation / separation section formed on the lower side. Since it does not flow directly to the communication port,
Disturbance of the sedimentation and separation section can be minimized, and there is a problem that the suspended sludge adheres to the draft portion of the stirring and mixing section and grows, blocking the water surface by raising the water surface of the stirring and mixing section. Can be prevented.

【0038】また、前記沈殿分離部に、前記攪拌混合部
との連通口と間隔を空けて、対向する側壁に向かって上
方に傾斜して配置された整流板を備えたにより、攪拌時
における攪拌混合部の攪拌水流に伴って沈殿分離部に生
じる攪拌水流の上昇を上記整流板で抑えることができる
ため、沈殿分離部から排出される上澄み水に汚泥が混じ
って汚れるのを防ぐことができる。
Further, the sedimentation / separation unit is provided with a rectifying plate which is arranged at an interval from a communication port with the stirring / mixing unit and is inclined upward toward the opposing side wall, so that stirring at the time of stirring is performed. Since the rise of the agitated water flow generated in the sedimentation / separation unit due to the agitation water flow in the mixing unit can be suppressed by the straightening plate, it is possible to prevent the supernatant water discharged from the sedimentation / separation unit from being mixed with the sludge and contaminated.

【0039】また、前記攪拌手段における攪拌羽根の取
付軸に軸振れを防止する軸振れ防止手段を備えたことに
より、被処理水の流入が長期間なく蒸発等により凝集沈
殿槽の水位が下がって攪拌羽根が水面上に現れ無負荷状
態で高速回転するような場合にも、攪拌羽根の軸振れに
よる振動(暴れ)を防止することができるので、攪拌羽
根の破損等を防ぐことができる。
Further, the shaft of the agitating means in the agitating means is provided with the shaft runout preventing means for preventing the shaft runout, so that the water to be treated does not flow for a long time and the water level of the coagulation sedimentation tank is lowered by evaporation or the like. Even in a case where the stirring blade appears on the water surface and rotates at a high speed with no load, vibration (runaway) due to shaft runout of the stirring blade can be prevented, so that damage to the stirring blade can be prevented.

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

【図1】本願発明による凝集沈殿装置が適用されるディ
スポーザ排水処理システムにおける排水処理部の実施形
態を示す全体構成図で、(a)は上面図、(b)は側断
面図。
FIG. 1 is an overall configuration diagram showing an embodiment of a wastewater treatment section in a disposer wastewater treatment system to which a coagulation sedimentation device according to the present invention is applied, (a) is a top view, and (b) is a side sectional view.

【図2】上記実施形態における凝集沈殿槽の斜視図。FIG. 2 is a perspective view of the coagulation sedimentation tank in the embodiment.

【図3】同じく、その側断面図。FIG. 3 is a side sectional view of the same.

【符号の説明】[Explanation of symbols]

1 排水処理部 2 流路切替装置 3 雑排水流量調整槽 4 生ごみ流量調整槽 5,7,11 エアリフトポンプ 6 固液分離装置 8 担体流動槽 9 凝集沈殿槽 10 コンポスト化装置 12 凝集剤投入装置 13 攪拌装置 91 攪拌混合部 92 沈殿分離部 93,94 隔壁 95 流入口 96 連通口 97 傾斜面 98 排出口 99 整流板 111 汚泥返送用エアリフト管 112 送気管 121 凝集剤投入口 131 攪拌羽根 132 攪拌モータ 133 取付軸 134 モータホルダー 135 軸受 DESCRIPTION OF SYMBOLS 1 Drainage processing part 2 Flow-path switching device 3 Miscellaneous wastewater flow control tank 4 Garbage flow control tank 5, 7, 11 Air lift pump 6 Solid-liquid separation device 8 Carrier flow tank 9 Coagulation sedimentation tank 10 Composting device 12 Coagulant injection device Reference Signs List 13 Stirring device 91 Stirring / mixing section 92 Precipitation / separation section 93, 94 Partition wall 95 Inlet 96 Communication port 97 Inclined surface 98 Discharge port 99 Rectifier plate 111 Sludge return air lift pipe 112 Air supply pipe 121 Coagulant inlet 131 Stirring blade 132 Stirring motor 133 Mounting shaft 134 Motor holder 135 Bearing

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C02F 1/52 C02F 1/52 E (72)発明者 藤本 恵一 大阪府守口市京阪本通2丁目5番5号 三 洋電機株式会社内 (72)発明者 赤松 功三 大阪府守口市京阪本通2丁目5番5号 三 洋電機株式会社内 (72)発明者 米田 勲 大阪府守口市京阪本通2丁目5番5号 三 洋電機株式会社内 (72)発明者 高見 博之 大阪府守口市京阪本通2丁目5番5号 三 洋電機株式会社内 Fターム(参考) 4D015 BA19 BA29 BB05 CA01 DC02 EA02 EA06 EA32 4D062 BA19 BA29 BB05 CA01 DC02 EA02 EA06 EA32 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C02F 1/52 C02F 1/52 E (72) Inventor Keiichi Fujimoto 2-5 Keihanhondori, Moriguchi-shi, Osaka No. 5 Sanyo Electric Co., Ltd. (72) Kozo Akamatsu 2-5-5, Keihanhondori, Moriguchi-shi, Osaka Prefecture In-house Sanyo Electric Co., Ltd. (72) Isao Yoneda 2, Keihanhondori, Moriguchi-shi, Osaka 5-5-5 Sanyo Electric Co., Ltd. (72) Inventor Hiroyuki Takami 2-5-5 Keihanhondori, Moriguchi-shi, Osaka F-term in Sanyo Electric Co., Ltd. 4D015 BA19 BA29 BB05 CA01 DC02 EA02 EA06 EA32 4D062 BA19 BA29 BB05 CA01 DC02 EA02 EA06 EA32

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 凝集沈殿槽を、凝集剤を直接投入する凝
集剤投入手段及び投入された凝集剤と流入した被処理水
を攪拌混合する攪拌手段を備えた攪拌混合部と、凝集し
た汚泥を沈殿分離する沈殿分離部とに、下部側が連通し
た隔壁で区画すると共に、前記沈殿分離部の横断面積を
前記攪拌混合部の横断面積より大きく形成したことを特
徴とする凝集沈殿装置。
An agitation and mixing section provided with an aggregating agent introducing means for directly introducing an aggregating agent and an agitating means for agitating and mixing the introduced aggregating agent and the inflowing water to be treated. A coagulating sedimentation apparatus, wherein a partitioning section is provided with a lower part communicating with a sedimentation separation part for sedimentation separation, and a cross-sectional area of the sedimentation separation part is formed larger than a cross-sectional area of the stirring and mixing part.
【請求項2】 前記攪拌混合部に、水没して上下が連通
する隔壁を備え、この隔壁から見て被処理水流入側に前
記攪拌手段の攪拌羽根と前記凝集剤投入手段の投入口が
設けられ、その反対側の下部に前記沈殿分離部との連通
口が形成されて成ることを特徴とする請求項1記載の凝
集沈殿装置。
2. The stirring and mixing section is provided with a partition which is submerged and vertically communicates, and a stirring blade of the stirring means and an input port of the coagulant input means are provided on an inflow side of the water to be treated as viewed from the partition. 2. The coagulating sedimentation apparatus according to claim 1, wherein a communication port with the sedimentation separation part is formed in a lower part on the opposite side.
【請求項3】 前記攪拌手段による攪拌水流が攪拌羽根
の位置で上向きに流れるように攪拌羽根の回転方向を設
定したことを特徴とする請求項1又は請求項2記載の凝
集沈殿装置。
3. The coagulating sedimentation apparatus according to claim 1, wherein the rotation direction of the stirring blade is set so that the stirring water flow by the stirring means flows upward at the position of the stirring blade.
【請求項4】 前記沈殿分離部に、前記攪拌混合部との
連通口と間隔を空けて、対向する側壁に向かって上方に
傾斜して配置された整流板を備えたことを特徴とする請
求項1ないし請求項3のいずれかに記載の凝集沈殿装
置。
4. The rectifying plate provided in the sedimentation / separation unit and spaced from the communication port with the stirring / mixing unit and inclined upward toward the opposing side wall. The coagulation sedimentation apparatus according to any one of claims 1 to 3.
【請求項5】 前記攪拌手段における攪拌羽根の取付軸
に軸振れを防止する軸振れ防止手段を備えたことを特徴
とする請求項1ないし請求項4のいずれかに記載の凝集
沈殿装置。
5. The coagulating sedimentation apparatus according to claim 1, wherein the stirring shaft of the stirring means is provided with a shaft run-out preventing means for preventing shaft run-out.
JP2000113309A 2000-04-14 2000-04-14 Flocculation/precipitation apparatus Pending JP2001293305A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000113309A JP2001293305A (en) 2000-04-14 2000-04-14 Flocculation/precipitation apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000113309A JP2001293305A (en) 2000-04-14 2000-04-14 Flocculation/precipitation apparatus

Publications (1)

Publication Number Publication Date
JP2001293305A true JP2001293305A (en) 2001-10-23

Family

ID=18625298

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000113309A Pending JP2001293305A (en) 2000-04-14 2000-04-14 Flocculation/precipitation apparatus

Country Status (1)

Country Link
JP (1) JP2001293305A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100354053C (en) * 2003-03-26 2007-12-12 住友金属工业株式会社 Method of manufacturing seamless tube.
JP2011156496A (en) * 2010-02-02 2011-08-18 Fuji Clean Co Ltd Wastewater treatment apparatus
CN114105272A (en) * 2021-11-30 2022-03-01 深圳同道环保科技有限公司 High-efficient sewage treatment plant that deposits

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100354053C (en) * 2003-03-26 2007-12-12 住友金属工业株式会社 Method of manufacturing seamless tube.
JP2011156496A (en) * 2010-02-02 2011-08-18 Fuji Clean Co Ltd Wastewater treatment apparatus
CN114105272A (en) * 2021-11-30 2022-03-01 深圳同道环保科技有限公司 High-efficient sewage treatment plant that deposits
CN114105272B (en) * 2021-11-30 2022-07-05 深圳同道环保科技有限公司 High-efficient sewage treatment plant that deposits

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