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JPS5923843B2 - Coagulation sedimentation device - Google Patents
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JPS5923843B2 - Coagulation sedimentation device - Google Patents

Coagulation sedimentation device

Info

Publication number
JPS5923843B2
JPS5923843B2 JP16427481A JP16427481A JPS5923843B2 JP S5923843 B2 JPS5923843 B2 JP S5923843B2 JP 16427481 A JP16427481 A JP 16427481A JP 16427481 A JP16427481 A JP 16427481A JP S5923843 B2 JPS5923843 B2 JP S5923843B2
Authority
JP
Japan
Prior art keywords
tank
sedimentation
sedimentation separation
flocs
rectifying plate
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
Application number
JP16427481A
Other languages
Japanese (ja)
Other versions
JPS5867307A (en
Inventor
正 村岡
志朗 村上
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.)
Hitachi Construction Machinery Co Ltd
Original Assignee
Hitachi Construction Machinery 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 Hitachi Construction Machinery Co Ltd filed Critical Hitachi Construction Machinery Co Ltd
Priority to JP16427481A priority Critical patent/JPS5923843B2/en
Publication of JPS5867307A publication Critical patent/JPS5867307A/en
Publication of JPS5923843B2 publication Critical patent/JPS5923843B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は濁液(水)に凝集剤を添加して濁液中の微細粒
子を凝集させ、これを沈降分離する凝集沈殿装置に関す
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a coagulation-sedimentation apparatus that adds a flocculant to a turbid liquid (water) to flocculate fine particles in the turbid liquid and separates the fine particles by sedimentation.

凝集沈殿装置には横流れ方式のものと、上向流方式のも
のとがある。
There are two types of coagulation-sedimentation equipment: horizontal flow type and upward flow type.

横流れ方式の凝集沈殿装置は、上向流方式のものと比較
して分離効率がよいが、広い設置面積が必要である。
A cross-flow coagulation-sedimentation device has better separation efficiency than an up-flow type, but requires a larger installation area.

また、上向流方式の凝集沈殿装置は設置面積が狭くてす
むが、分離効率が悪い。
Further, although an upflow type coagulation-sedimentation apparatus requires a small installation area, it has poor separation efficiency.

このため、横流れ方式と上向流方式とを組合せ1 た凝
集沈殿装置が提案され、実用化されている。
For this reason, a coagulation-sedimentation device that combines a horizontal flow method and an upward flow method has been proposed and put into practical use.

第1図は横流れ方式と上向流方式とを組合わせた従来の
凝集沈殿装置を示す平面図、第2図はその断面正面図を
示している。
FIG. 1 is a plan view showing a conventional coagulation sedimentation apparatus that combines a horizontal flow system and an upward flow system, and FIG. 2 is a cross-sectional front view thereof.

図において、1は装置本体、2は凝集撹拌槽、3は濁水
流入管、4は凝集剤注入管、5は凝集撹拌槽2内に設け
られた撹拌翼、6は撹拌翼5の駆動装置、7はフロック
成長槽で、その人ロアaが下方に、出ロアbが上方に形
成され、かつフロツク成長槽7自体を形成する仕切壁8
は傾斜して設けられて、フロック族□ 長槽7の容積が
出口Ib側に向う程大きくなっている。
In the figure, 1 is the apparatus main body, 2 is a coagulation stirring tank, 3 is a turbid water inflow pipe, 4 is a flocculant injection pipe, 5 is a stirring blade provided in the coagulation stirring tank 2, 6 is a drive device for the stirring blade 5, Reference numeral 7 denotes a floc growth tank, in which a lower part a is formed at the bottom and a lower part b is formed at the upper part, and a partition wall 8 forms the floc growth tank 7 itself.
is provided in an inclined manner, and the volume of the floc group □ long tank 7 increases toward the exit Ib side.

9は沈降分離槽、10は沈降分離槽9内に設けられた複
数枚の整流板で、各整流板10は垂直に、かつ互に離間
して設置されている。
Reference numeral 9 denotes a sedimentation separation tank, and 10 denotes a plurality of rectifying plates provided in the sedimentation separation tank 9. Each rectifying plate 10 is installed vertically and spaced apart from each other.

また各整流板10には多数の孔があけられている。Further, each rectifying plate 10 is provided with a large number of holes.

11は沈降分離槽9の出口側上部において装置本体1に
形成された溢流せき、12は溢流せき11から溢流する
浄化水を溜める処理液溜、13は処理水流出管、14は
沈降分離槽9の下部に設置されたレーキ、15はフロッ
ク成長槽7の下部に形成されたスラッジ濃縮槽、16は
スラッジ排出管である。
11 is an overflow weir formed in the apparatus body 1 at the upper part of the outlet side of the sedimentation separation tank 9; 12 is a treated liquid reservoir for collecting purified water overflowing from the overflow weir 11; 13 is a treated water outflow pipe; and 14 is a sedimentation tank. A rake is installed at the bottom of the separation tank 9, 15 is a sludge concentration tank formed at the bottom of the floc growth tank 7, and 16 is a sludge discharge pipe.

この凝集沈殿装置においては、濁水を凝集剤との混合液
が濁水流入管3を介して凝集撹拌槽2に供給され、この
混合液は撹拌翼5によって撹拌され、凝集剤の凝集反応
によりフロックが生成され、このフロックはフロック成
長槽7内で成長する。
In this coagulation-sedimentation device, a mixture of turbid water and a flocculant is supplied to a flocculation stirring tank 2 through a turbid water inlet pipe 3, and this mixture is stirred by stirring blades 5, and flocs are formed by the flocculation reaction of the flocculant. The flocs are generated and grown in the floc growth tank 7.

フロック成長槽7から沈降分離槽9内に流入したフロッ
クの一部はそのままスラッジ濃縮槽15に沈降して堆積
し、他のフロックは整流板10を通過して溢流せき11
の方向へ流れながら次第に沈降して、沈降分離槽9の底
部に堆積する。
Some of the flocs that flowed into the sedimentation separation tank 9 from the floc growth tank 7 settle and accumulate in the sludge thickening tank 15, and other flocs pass through the rectifier plate 10 and are deposited in the overflow weir 11.
It gradually settles while flowing in the direction of , and is deposited at the bottom of the sedimentation separation tank 9.

そして沈降分離槽9底部に堆積したスラッジは、レーキ
14によりスラッジ濃縮槽15へかき寄せられ、スラッ
ジ濃縮槽15に集められたスラッジはスラッジ排出管1
6から装置外へ排出される。
The sludge accumulated at the bottom of the sedimentation separation tank 9 is scraped into the sludge concentration tank 15 by the rake 14, and the sludge collected in the sludge concentration tank 15 is transferred to the sludge discharge pipe 1.
6 and is discharged from the device.

一方、浄化された水は溢流せき11から処理液溜12へ
溢流した後、処理水流出管13から装置外に流出する。
On the other hand, the purified water overflows from the overflow weir 11 into the treated liquid reservoir 12 and then flows out of the apparatus from the treated water outflow pipe 13.

ところで、前述の凝集沈殿装置においては、その沈降分
離槽9内に設置した整流板10の孔を通過させることに
よって水平流に整流すると共に水平流速を均一にしてフ
ロックを含むスラッジの分離効率を高めるようにしてい
る。
By the way, in the above-mentioned coagulation sedimentation device, the flow is rectified into a horizontal flow by passing through the holes of the rectifier plate 10 installed in the sedimentation separation tank 9, and the horizontal flow velocity is made uniform to increase the separation efficiency of sludge containing flocs. That's what I do.

しかし、前記沈降分離槽9の下部にはレーキ14が設置
されているため、各整流板10を、その下端がレーキ1
4と適宜の隙間を保って設置せざるを得す、当該隙間で
は整流板10による抵抗がないため、水の流速が整流板
10を通過する流速に比べて速くなる。
However, since the rake 14 is installed at the bottom of the sedimentation separation tank 9, the lower end of each current plate 10 is connected to the rake 14.
Since there is no resistance due to the current plate 10 in this gap, the flow rate of water becomes faster than the flow rate passing through the current plate 10.

即ち、沈降分離槽9内での水平流速が不均一となって、
スラッジの分離効率が低下してしまう。
That is, the horizontal flow velocity within the sedimentation separation tank 9 becomes non-uniform,
Sludge separation efficiency decreases.

また、各整流板10の下端とレーキ14との隙間を通過
する流速が速いため、沈降分離槽9底部に堆積したスラ
ッジ中のフロックの巻上げ現象が発生し、そのフロック
が溢流せき11を越えてしまい清澄度の高い処理水を得
ることができない。
In addition, since the velocity of the flow passing through the gap between the lower end of each rectifying plate 10 and the rake 14 is high, the flocs in the sludge accumulated at the bottom of the sedimentation separation tank 9 are rolled up, and the flocs exceed the overflow weir 11. As a result, highly clear treated water cannot be obtained.

本発明の目的は、前述した従来技術の問題点を解消し、
沈降分離槽内の水平流速を均一にして分離効率を高める
ことができ、かつ沈降分離槽底部に堆積したスラッジ中
のフロックの巻上げ現象を招くことなく清澄度の高い処
理水を得ることができる凝集沈殿装置を提供するにある
The purpose of the present invention is to solve the problems of the prior art described above,
Coagulation can improve separation efficiency by making the horizontal flow velocity in the sedimentation separation tank uniform, and can obtain highly clear treated water without causing the flocs in the sludge accumulated at the bottom of the sedimentation separation tank to be rolled up. is to provide precipitation equipment.

この目的を達成するため、本発明は、濁液と凝集剤とを
撹拌する凝集撹拌槽と、入口を下方に、出口を上方に形
成し、かつ凝集撹拌槽の撹拌液からフロックを成長させ
るフロック成長槽と、複数枚の整流板を垂直に、かつ互
に離間して設置させた沈降分離槽と、前記フロック成長
槽で成長したフロックを堆積するスラッジ濃縮槽と、前
記沈降分離槽で沈降したスラッジをスラッジ濃縮槽へ移
送させる手段と、沈降分離槽の出口側上部に設置され、
沈降分離槽の浄化液を処理液溜へ溢流させる溢流せきと
を備えて成る凝集沈殿装置において、前記沈降分離槽の
各整流板のうち、フロック成長槽と隣合う整流板を、フ
ロック成長槽の出口より下方位置まで延出する垂直整流
板部と、該垂直整流板部の下端に連設し、かつフロック
成長槽を形成する傾斜仕切壁と同方向に傾斜する傾斜整
流板部とで構成したことを特徴とする。
In order to achieve this object, the present invention provides a flocculation stirring tank for stirring a turbid liquid and a flocculant, and a flocculation tank having an inlet downward and an outlet upward, and for growing flocs from the stirred liquid of the flocculation stirring tank. A growth tank, a sedimentation separation tank in which a plurality of rectifying plates are installed vertically and spaced apart from each other, a sludge concentration tank in which the flocs grown in the floc growth tank are deposited, and flocs that have settled in the sedimentation separation tank are A means for transferring sludge to a sludge thickening tank, and a means installed at the upper part of the exit side of the sedimentation separation tank,
In a coagulation-sedimentation apparatus comprising an overflow weir for overflowing purified liquid from a sedimentation separation tank into a treated liquid reservoir, among the rectifying plates of the sedimentation separation tank, the one adjacent to the floc growth tank is connected to the floc growth tank. A vertical baffle plate section extending to a position below the outlet of the tank, and an inclined baffle plate section connected to the lower end of the vertical baffle plate section and inclined in the same direction as the inclined partition wall forming the floc growth tank. It is characterized by having been configured.

以下、本発明の詳細な図面に従って説明する。Hereinafter, the present invention will be explained with reference to detailed drawings.

第3図は本発明による凝集沈殿装置を示す平面図、第4
図は第3図の断面正面図である。
FIG. 3 is a plan view showing the coagulation sedimentation apparatus according to the present invention;
The figure is a sectional front view of FIG. 3.

図において、第1図及び第2図と同じ符号のものは同じ
もの、もしくは等価のものを表わしている。
In the figures, the same reference numerals as in FIGS. 1 and 2 represent the same or equivalent items.

本発明による凝集沈殿装置では、沈降分離槽9内に設置
された各整流板10のうち、フロック成長槽7に隣合う
整流板100が、フロック成長槽7の出ロアbより下方
位置まで延出する垂直整流板部100aと、該垂直整流
板部100aの下端に連設し、かつフロック成長槽7の
傾斜仕切壁8と同方向に傾斜する傾斜整流板部100b
とで構成されている。
In the coagulation sedimentation apparatus according to the present invention, among the current plates 10 installed in the sedimentation separation tank 9, the current plate 100 adjacent to the floc growth tank 7 extends to a position below the outlet lower b of the floc growth tank 7. a vertical rectifier plate part 100a, and an inclined rectifier plate part 100b connected to the lower end of the vertical rectifier plate part 100a and inclined in the same direction as the inclined partition wall 8 of the floc growth tank 7.
It is made up of.

また整流板100の傾斜整流板部100bの下端は、レ
ーキ14の動きをさまたげない位置まで延出している。
Further, the lower end of the inclined current plate portion 100b of the current plate 100 extends to a position where the movement of the rake 14 is not obstructed.

尚、整流板100の傾斜整流板部100bの傾斜角θは
、大きい程望ましいが、フロックの堆積を考慮するとフ
ロック成長槽7の傾斜仕切壁8と同等の角度(30度程
)が良い。
Incidentally, the inclination angle θ of the inclined current plate portion 100b of the current plate 100 is preferably as large as possible, but in consideration of the accumulation of flocs, it is preferable that the angle θ be the same as that of the inclined partition wall 8 of the floc growth tank 7 (about 30 degrees).

しかるに本発明による凝集沈殿装置においては、沈降分
離槽9の下方を除く水流が整流板100の垂直整流板部
100a及び後方の整流板10の合孔を通過することに
よって水平流に整流されると共に水平流速が均一化され
、また沈降分離槽9下方の水流は整流板100の傾斜整
流板部100bの孔を通過することによって垂直整流板
部100a部と同じように抵抗をうけ水平流に整流され
ると共に、その水平流速が前記水平流速と等しくなる。
However, in the coagulation-sedimentation apparatus according to the present invention, the water flow excluding the lower part of the sedimentation separation tank 9 is rectified into a horizontal flow by passing through the vertical baffle plate portion 100a of the baffle plate 100 and the joint holes in the rear baffle plate 10. The horizontal flow velocity is made uniform, and the water flow below the sedimentation separation tank 9 passes through the holes in the inclined rectifying plate portion 100b of the rectifying plate 100, and is subjected to resistance in the same way as the vertical rectifying plate portion 100a, and is rectified into a horizontal flow. At the same time, the horizontal flow velocity becomes equal to the horizontal flow velocity.

従って、沈降分離槽9内の水平流速が均一となるので、
フロックを含むスラッジの分離効率が高くなる。
Therefore, the horizontal flow velocity in the sedimentation separation tank 9 becomes uniform, so
Separation efficiency of sludge containing flocs is increased.

また水平流速が均一化されることによって沈降分離槽9
底部に堆積するスラッジ中のフロックの巻上り現象が発
生するようなことはないので、清澄度の高い処理水を得
られる。
In addition, by equalizing the horizontal flow velocity, the sedimentation separation tank 9
Since the flocs in the sludge deposited at the bottom do not roll up, highly clear treated water can be obtained.

以上説明したように、本発明による凝集沈殿装置によれ
ば、沈降分離槽内の水平流速を均一化できてスラッジの
分離効率を向上でき、しかも沈降分離槽底部に堆積した
スラッジ中のフロックの巻上がり現象を招くことがない
ので清澄度の高い処理水を得ることができる。
As explained above, according to the coagulation and sedimentation apparatus according to the present invention, it is possible to equalize the horizontal flow velocity in the sedimentation separation tank and improve the sludge separation efficiency, and furthermore, the flocs in the sludge deposited at the bottom of the sedimentation separation tank can be rolled up. Treated water with a high degree of clarity can be obtained since the water rise phenomenon does not occur.

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

第1図は従来の凝集沈殿装置を示す平面図、第2図は第
1図の断面正面図、第3図は本発明による凝集沈殿装置
を示す平面図、第4図は第3図の断面正面図である。 1・・・・・・装置本体、2・・・・・・凝集撹拌槽、
7・・・・・・フロック成長槽、?a、7b・・・・・
・フロック成長槽の入口及び出口、8・・・・・・傾斜
仕切壁、9・・・・・・沈降分離槽、10・・・・・・
整流板、11・・・・・・溢流せき、12・・・・・・
処理液溜、14・・・・・・レーキ、15・・・・・・
スラッジ濃縮槽、100・・・・・・整流板、100a
・・・・・・垂直整流板部、100b・・・・・・傾斜
整流板部。
Fig. 1 is a plan view showing a conventional coagulation sedimentation device, Fig. 2 is a sectional front view of Fig. 1, Fig. 3 is a plan view showing a coagulation sedimentation device according to the present invention, and Fig. 4 is a cross section of Fig. 3. It is a front view. 1... Device main body, 2... Coagulation stirring tank,
7...floc growth tank? a, 7b...
- Inlet and outlet of floc growth tank, 8... Slanted partition wall, 9... Sedimentation separation tank, 10...
Current plate, 11... Overflow weir, 12...
Processing liquid reservoir, 14... Rake, 15...
Sludge concentration tank, 100... Rectifier plate, 100a
...Vertical rectifier plate section, 100b... Inclined rectifier plate section.

Claims (1)

【特許請求の範囲】[Claims] 1 濁液と凝集剤とを撹拌する凝集撹拌槽と、入口を下
方に、出口を上方に形成し、かつ凝集撹拌槽の撹拌液か
らフロックを成長させるフロック成長槽と、複数枚の整
流板を垂直に、かつ互に離間して設置させた沈降分離槽
と、前記フロック成長槽で成長したフロックを堆積する
スラッジ濃縮槽と、前記沈降分離槽で沈降したスラッジ
をスラッジ濃縮槽へ移送させる手段と、沈降分離槽の出
口側上部に設置され、沈降分離槽の浄化液を処理液溜へ
溢流させる溢流せききを備えて成る凝集沈殿装置におい
て、前記沈降分離槽の各整流板のうち、フロック成長槽
と隣合う整流板を、フロック成長槽の出口より下方位置
まで延出する垂直整流板部と、該垂直整流板部の下端に
連設し、かつフロック成長槽を形成する傾斜仕切壁と同
方向に傾斜する傾斜整流板部とで構成したことを特徴と
する凝集沈殿装置。
1. A flocculation stirring tank that stirs the turbid liquid and flocculant, a floc growth tank that has an inlet facing downward and an outlet upward, and that grows flocs from the stirring liquid of the flocculation stirring tank, and a plurality of rectifying plates. Sedimentation separation tanks installed vertically and spaced apart from each other, a sludge concentration tank for depositing flocs grown in the floc growth tank, and means for transferring the sludge settled in the sedimentation separation tank to the sludge concentration tank. , a flocculating sedimentation apparatus comprising an overflow weir which is installed at the upper part of the exit side of the sedimentation separation tank and causes the clarified liquid of the sedimentation separation tank to overflow into the treated liquid reservoir; A rectifying plate adjacent to the growth tank includes a vertical rectifying plate portion extending to a position below the outlet of the floc growth tank, and an inclined partition wall connected to the lower end of the vertical rectifying plate portion and forming a floc growth tank. 1. A coagulation-sedimentation device characterized by comprising: an inclined rectifying plate section inclined in the same direction;
JP16427481A 1981-10-16 1981-10-16 Coagulation sedimentation device Expired JPS5923843B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16427481A JPS5923843B2 (en) 1981-10-16 1981-10-16 Coagulation sedimentation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16427481A JPS5923843B2 (en) 1981-10-16 1981-10-16 Coagulation sedimentation device

Publications (2)

Publication Number Publication Date
JPS5867307A JPS5867307A (en) 1983-04-21
JPS5923843B2 true JPS5923843B2 (en) 1984-06-05

Family

ID=15789966

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16427481A Expired JPS5923843B2 (en) 1981-10-16 1981-10-16 Coagulation sedimentation device

Country Status (1)

Country Link
JP (1) JPS5923843B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100828945B1 (en) 2007-02-22 2008-05-13 충북대학교 산학협력단 Mine Wastewater Treatment Method Using Natural Sedimentation Beams
JP2012228634A (en) * 2011-04-25 2012-11-22 Sowa Engineering:Kk Regenerated water production device
CN107754388A (en) * 2016-08-18 2018-03-06 宜兴市天马环保工程有限公司 Automatic homogenizing tube settling reactive tank

Also Published As

Publication number Publication date
JPS5867307A (en) 1983-04-21

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