JPS6147562B2 - - Google Patents
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- Publication number
- JPS6147562B2 JPS6147562B2 JP18735983A JP18735983A JPS6147562B2 JP S6147562 B2 JPS6147562 B2 JP S6147562B2 JP 18735983 A JP18735983 A JP 18735983A JP 18735983 A JP18735983 A JP 18735983A JP S6147562 B2 JPS6147562 B2 JP S6147562B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- raw water
- channel
- tank
- ascending
- 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
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Description
【発明の詳細な説明】
本発明は、各種の懸濁水(以下、原水と略称す
る)中から無機固形物や有機固形物等の懸濁物
(以下、SSと略称する)を効率良く沈殿分離して
澄清水を得るための沈殿装置を提供するものであ
る。Detailed Description of the Invention The present invention provides efficient precipitation and separation of suspended solids (hereinafter referred to as SS) such as inorganic solids and organic solids from various types of suspended water (hereinafter referred to as raw water). The present invention provides a precipitation device for obtaining clear water.
即ち本発明の沈殿装置は、第1図及び第2図に
示すように、上槽1と下槽2とを備え、前記上槽
1内には、複数段の傾斜板3a〜3cによつて区
画された多段傾斜沈殿層4、これ等多段傾斜沈殿
層4の上端入口部に連通する原水供給垂直流路
5、前記多段傾斜沈殿層4の下端出口部に連通す
る下降流路6、及び下端開口が前記下降流路6の
下端開口と隣接する上昇流路7とが設けられ、前
記下槽2は前記下降流路6と上昇流路7との下端
開口に連通すると共に、内部には、沈殿物収集用
漏斗部8とこの漏斗部8の上方に開口する集水器
9とを備え、前記漏斗部8の底部には沈殿物を原
水と共に排出する排出管10を連設し、前記上昇
流路7の上端と前記集水器9に連通する上昇水管
11の上端とから澄清水を溢流放出させるように
したものである。 That is, the precipitation apparatus of the present invention, as shown in FIGS. 1 and 2, includes an upper tank 1 and a lower tank 2. A divided multi-stage inclined sedimentation layer 4, a raw water supply vertical channel 5 communicating with the upper end inlet of the multi-stage inclined precipitation layer 4, a downward flow channel 6 communicating with the lower end outlet of the multi-stage inclined precipitation layer 4, and a lower end thereof. An ascending channel 7 is provided, the opening of which is adjacent to the lower end opening of the descending channel 6, and the lower tank 2 communicates with the lower end openings of the descending channel 6 and the ascending channel 7. It is equipped with a funnel part 8 for collecting sediment and a water collector 9 that opens above the funnel part 8, and a discharge pipe 10 for discharging the sediment together with raw water is connected to the bottom of the funnel part 8. Clear water is made to overflow and discharge from the upper end of the channel 7 and the upper end of the rising water pipe 11 communicating with the water collector 9.
以下、第1図乃至第4図に示す一実施例に基づ
いて具体構造を更に詳細に説明すると、12は水
位調整槽であつて、上槽1の上部に支持され、上
部には原水管13と溢流管14とが接続され、下
部には、前記上槽1内の原水供給垂直流路5の上
端部に原水を給水バルブ15を介して供給する給
水管16が接続されている。この実施例では前記
上槽1及び下槽2は円筒形であつて、第3図及び
第4図に示されるように、各傾斜板3a〜3cの
内、最下部の傾斜板3aを除く傾斜板3bは、中
心部に前記原水供給垂直流路5を形成する貫通孔
を有する円形の傘形板から成り、最下部の傾斜板
3aは、前記原水供給垂直流路5の底となる台板
17と傾斜板3aの下側を密閉する底板18とを
備えた密閉中空の円錐状台形体19の周側壁によ
つて構成されている。この最下部の傾斜板3aを
形成する円錐台形体19は周辺複数箇所がブラケ
ツト20を介して下槽2の内側上辺部に支持さ
れ、他の傘形傾斜板3bは、下位の傾斜板3a,
3bの表面(上面)との間に放射状に介装された
堰板21によつて下位の傾斜板3a,3bに支持
されている。第1図及び第2図に示すように、最
上部の傾斜板3cの中心部からは、前記原水供給
流路5の上端を密封する有蓋筒体22が突設さ
れ、この有蓋筒体22内に前記給水管16が挿入
されている。 Hereinafter, the specific structure will be explained in more detail based on an embodiment shown in FIGS. and an overflow pipe 14, and a water supply pipe 16 for supplying raw water to the upper end of the raw water supply vertical channel 5 in the upper tank 1 via a water supply valve 15 is connected to the lower part. In this embodiment, the upper tank 1 and the lower tank 2 are cylindrical, and as shown in FIGS. The plate 3b is a circular umbrella-shaped plate having a through hole in the center that forms the raw water supply vertical flow path 5, and the lowermost inclined plate 3a is a base plate that forms the bottom of the raw water supply vertical flow path 5. 17 and a bottom plate 18 that seals the lower side of the inclined plate 3a. The truncated conical body 19 forming the lowermost inclined plate 3a is supported at a plurality of peripheral points on the inner upper side of the lower tank 2 via the bracket 20, and the other umbrella-shaped inclined plates 3b are supported by the lower inclined plates 3a,
It is supported by the lower inclined plates 3a and 3b by a weir plate 21 interposed radially between the upper surface (upper surface) of the lower inclined plate 3b. As shown in FIGS. 1 and 2, a covered cylindrical body 22 that seals the upper end of the raw water supply flow path 5 projects from the center of the uppermost inclined plate 3c, and inside this covered cylindrical body 22. The water supply pipe 16 is inserted into.
前記下降流路6及び上昇流路7は円心円筒状で
あつて、23はその両流路6,7間を区画する有
蓋内筒であり、上端は前記有蓋筒体22の位置で
密閉され、第4図に示すように周方向複数箇所に
於て垂直な支持板24により上槽1の周壁に支持
されている。前記上昇流路7の上端は開放され、
その外側に上昇流路7からの溢流水を受ける環状
の澄清水受槽25が設けられている。26は、前
記澄清水受槽25からの澄清水と前記上昇水管1
1からの澄清水とを受け入れる流量調節槽であつ
て、溢流堰27と放出管28とを備えている。2
9は上昇水管11内に介装された流量調整バル
ブ、30は排出管10中に介装された排出バルブ
である。 The descending flow path 6 and the ascending flow path 7 have a circular cylindrical shape, and 23 is a covered inner cylinder that partitions the two flow paths 6 and 7, and the upper end is sealed at the position of the covered cylinder body 22. As shown in FIG. 4, it is supported on the peripheral wall of the upper tank 1 by vertical support plates 24 at multiple locations in the circumferential direction. The upper end of the ascending flow path 7 is open,
An annular clear water receiving tank 25 for receiving overflow water from the ascending channel 7 is provided on the outside thereof. 26 is the clear water from the clear water receiving tank 25 and the rising water pipe 1
This is a flow rate regulating tank that receives clear water from 1, and is equipped with an overflow weir 27 and a discharge pipe 28. 2
Reference numeral 9 indicates a flow rate adjustment valve interposed in the rising water pipe 11, and reference numeral 30 indicates a discharge valve interposed in the discharge pipe 10.
次に使用方法及び作用を説明すると、原水は原
水管13より水位調整槽12に流入し、溢流管1
4によつて一定水位に保たれた状態で給水バルブ
15によつて調整された給水量で給水管16より
原水供給垂直流路5に入り、下に向かつて流れ
る。ここでSS排出バルブ30が閉止されている
と、原水は上槽1の上端まで充満し、継続して送
水すれば原水供給垂直流路5より流入する原水
は、上昇流路7より連続的に上昇し、原水の大部
分は上昇流路7の上端より溢流し、その外周の澄
清水受槽25を経由して流量調節槽26に流入す
る。原水の一部分は下槽2内の集水器9を経由し
て上昇水管11を上昇し、流量調節槽26に入
る。 Next, to explain the usage and function, raw water flows into the water level adjustment tank 12 from the raw water pipe 13, and the overflow pipe 1
4, the raw water enters the raw water supply vertical channel 5 through the water supply pipe 16 at a water supply amount adjusted by the water supply valve 15, and flows downward. If the SS discharge valve 30 is closed, the raw water will fill up to the upper end of the upper tank 1, and if the water is continuously fed, the raw water flowing from the raw water supply vertical flow path 5 will continue to flow from the upward flow path 7. The raw water rises, and most of the raw water overflows from the upper end of the rising channel 7 and flows into the flow rate regulating tank 26 via the clear water receiving tank 25 on its outer periphery. A portion of the raw water passes through the water collector 9 in the lower tank 2, ascends the rising water pipe 11, and enters the flow rate adjustment tank 26.
流量調節槽26は澄清水受槽25と連通してい
るので、上昇水管11の上昇水位は上昇流路7か
らの溢流水位と同一である。上昇流路7からの溢
流水量と上昇水管11の上昇水量の流量比は、両
水路の断面積の比と略等しいので、原水の性質に
応じて両水路の断面積の比を決定すれば良い。具
体的には、上昇水管11中に介装した流量調整バ
ルブ29によつて上昇水量の流量を調整し、以て
上昇流路7からの溢流水量と上昇水管11の上昇
水量の流量比を調整することが出来る。流量調節
槽26からの放水は溢流堰27によつて加減され
た状態で放出管28より放流される。 Since the flow rate adjustment tank 26 is in communication with the clear water receiving tank 25, the rising water level of the rising water pipe 11 is the same as the overflow water level from the rising channel 7. The flow rate ratio between the overflowing water volume from the rising water channel 7 and the rising water volume in the rising water pipe 11 is approximately equal to the ratio of the cross-sectional areas of both water channels, so if the ratio of the cross-sectional areas of both water channels is determined according to the nature of the raw water, good. Specifically, the flow rate of the rising water is adjusted by a flow rate regulating valve 29 installed in the rising water pipe 11, thereby adjusting the flow rate ratio between the overflowing water from the rising flow passage 7 and the rising water volume of the rising water pipe 11. It can be adjusted. The water discharged from the flow rate regulating tank 26 is controlled by the overflow weir 27 and then discharged from the discharge pipe 28.
原水は大略上記のように流動するが、上槽1内
に充満している原水の流れを第5図に基づいて更
に詳述する。尚、第5図中、黒点で示すのが原水
中のSS、矢印は原水の流れを示す。原水供給垂
直流路5に入り下に向かつて流れる原水は、各段
の傾斜沈殿層4に上端入口より流入し、各傾斜板
3a,3bの表面に沿つて下向き(外向き)に流
れ、この間に原水中のSSは逐次傾斜板3a,3
bの表面上に沈降する。この沈降分離したSS
は、重力と傾斜沈殿層4内の原水の流れとを受け
て傾斜板3a,3b上を滑り落ち、各傾斜沈殿層
4の下端外周の下降流路6内に於て、内側寄りの
位置(傾斜板3a,3bの下端周縁寄りの位置)
で原水中を重力により垂直に下降する。このよう
にSSの沈降分離作用を受けた原水の大部分は、
下降流路6の下端開口からその外側に位置する上
昇流路7の下端開口に向かつて外側寄りの位置で
Uターンし、一次澄清水として上昇流路7を上昇
し、前記のように澄清水受槽25に流入すること
になる。 Although the raw water flows roughly as described above, the flow of the raw water filling the upper tank 1 will be explained in more detail based on FIG. 5. In Fig. 5, black dots indicate SS in the raw water, and arrows indicate the flow of the raw water. The raw water that enters the raw water supply vertical channel 5 and flows downward flows into the inclined sedimentation layer 4 of each stage from the upper end inlet, flows downward (outward) along the surface of each inclined plate 3a, 3b, and during this period. The SS in the raw water is successively tilted plates 3a and 3.
It settles on the surface of b. This sedimentation separated SS
slides down on the inclined plates 3a and 3b under the influence of gravity and the flow of raw water in the inclined sedimentation layer 4, and is located at an inner position ( position near the lower edge of the inclined plates 3a, 3b)
It descends vertically through the raw water due to gravity. Most of the raw water that has undergone the sedimentation and separation action of SS in this way is
From the lower end opening of the descending channel 6 to the lower end opening of the ascending channel 7 located outside thereof, it makes a U-turn at a position closer to the outside, ascends the ascending channel 7 as primary clear water, and as described above clear water It will flow into the receiving tank 25.
一方、前記下降流路6と上昇流路7との下端開
口真下の原水Uターン部、即ち分離部31から内
側寄り位置で更に下降する、SS濃度の高くなつ
た原水は、下槽2に於て第二次のSS沈降分離作
用を受ける。即ち、この原水は分離部31より垂
直に下降した後、中心部上方の集水器9に向かつ
てUターンするため、この原水中の高濃度のSS
は下槽2の漏斗部8上に沈降し、漏斗部8の中心
底部に集められる。そして集水器9に導入される
原水は二次澄清水として上昇水管11を上昇し、
前記一次澄清水と一緒になつて放出される。漏斗
部8の中心底部に集められたSSは排出バルブ3
0を開放することにより、排出管10より流出す
る原水と一緒に槽外に排出される。この排出管1
0からのSS排出作業は連続的に行うことも出来
るし、定期的に行うことも出来る。連続的に行う
場合は、排出管10よりSSと共に排出される原
水量が原水供給量に比べて十分少量であるように
排出バルブ30の開度を調整すれば良い。 On the other hand, the raw water with increased SS concentration that further descends from the U-turn portion of the raw water immediately below the lower end openings of the descending flow path 6 and the rising flow path 7, that is, from the separating portion 31 at a position closer to the inside, is transferred to the lower tank 2. and undergoes a second SS sedimentation separation action. That is, this raw water descends vertically from the separation section 31 and then makes a U-turn toward the water collector 9 above the center, so that the high concentration of SS in this raw water
sediments on the funnel part 8 of the lower tank 2 and is collected at the center bottom of the funnel part 8. Then, the raw water introduced into the water collector 9 rises through the rising water pipe 11 as secondary clear water,
It is released together with the primary clear water. The SS collected at the center bottom of the funnel part 8 is connected to the discharge valve 3.
By opening 0, the raw water flowing out from the discharge pipe 10 is discharged to the outside of the tank. This discharge pipe 1
SS discharge work from 0 can be performed continuously or periodically. In the case of continuous operation, the opening degree of the discharge valve 30 may be adjusted so that the amount of raw water discharged from the discharge pipe 10 together with the SS is sufficiently small compared to the amount of raw water supplied.
尚、上記のSS沈殿分離作用に於て、原水供給
垂直流路5内の原水の流速は、最上段の傾斜沈殿
層4に対応する箇所で最高流速をとり、以下、下
際するに従つて低下し、最下段の傾斜沈殿層4に
対応する下端に於て最低流速(最高流速÷傾斜沈
殿層4の段数)となる。各傾斜沈殿層4に流入す
る原水流量は略等しく、この各傾斜沈殿層4内で
の原水の流速は、当該傾斜沈殿層4が下端出口側
程放射状に広がるため、原水供給垂直流路5側の
上端入口から下降流路6側の下側出口に近付くに
従つて漸次低下する(実験例、0.230〜0.083cm/
秒)。下降流路6内の原水流速は、最上段の傾斜
沈殿層4に対応する箇所で最低流速をとり、以
下、下降するに従つて増大し、最下段の傾斜沈殿
層4に対応する箇所に於て最高流速(最低流速×
傾斜沈殿層4の段数)となる。勿論、この下降流
路6の下端部に於ける最高流速は、原水供給垂直
流路5の上端部に於ける最高流速より十分低い。 In addition, in the above-mentioned SS precipitation separation action, the flow velocity of raw water in the raw water supply vertical channel 5 reaches the highest flow velocity at the location corresponding to the uppermost inclined sedimentation layer 4, and as The flow rate decreases and reaches the lowest flow velocity (maximum flow velocity ÷ number of inclined precipitation layers 4) at the lower end corresponding to the lowest inclined precipitation layer 4. The flow rate of raw water flowing into each inclined sedimentation layer 4 is approximately equal, and the flow rate of raw water within each inclined sedimentation layer 4 spreads radially toward the lower end exit of the sloped sedimentation layer 4, so the raw water flow rate on the raw water supply vertical channel 5 side It gradually decreases from the upper end inlet to the lower outlet on the downward flow path 6 side (experimental example, 0.230 to 0.083 cm/
seconds). The raw water flow velocity in the descending channel 6 reaches its lowest flow velocity at a location corresponding to the uppermost slanted sedimentation layer 4, increases as it descends, and reaches a minimum flow velocity at a location corresponding to the lowermost slanted sedimentation layer 4. Maximum flow velocity (minimum flow velocity ×
(number of stages of inclined sedimentation layer 4). Of course, the maximum flow velocity at the lower end of the downward flow path 6 is sufficiently lower than the maximum flow velocity at the upper end of the raw water supply vertical flow path 5.
下降流路6の下端開口と上昇流路7の下端開口
との真下の分離部31を経由して上昇流路7に流
入する原水流量は、原水の性質、SS濃度、及び
要求される澄清度に応じて設定すれば良いが、例
えば原水供給量の2/3を上昇流路7に流入させる
ことが出来る。前記分離部31での流速は必然的
に下降流路6及び上昇流路7での流速より低速と
なるが、一般の上水道の沈殿池に於ける基準流速
以下(実験例、0.453cm/秒)とするのが望まし
い。各傾斜沈殿層4内での原水流速は前記分離部
31での流速以下(実験例、平均0.1226cm/秒)
にとるべきものである。 The flow rate of raw water flowing into the ascending channel 7 via the separation section 31 directly below the lower end opening of the descending channel 6 and the lower end opening of the ascending channel 7 depends on the nature of the raw water, the SS concentration, and the required clarity. For example, 2/3 of the raw water supply amount can be made to flow into the ascending channel 7. The flow velocity in the separation section 31 is necessarily lower than the flow velocity in the descending channel 6 and ascending channel 7, but it is lower than the standard flow velocity in sedimentation tanks of general waterworks (experimental example, 0.453 cm/sec). It is desirable to do so. The flow velocity of raw water in each inclined sedimentation layer 4 is lower than the flow velocity in the separation section 31 (experimental example, average 0.1226 cm/sec)
It is something that should be taken seriously.
傾斜沈殿層4内の原水は傾斜板3a,3bの表
面に沿つて下向きに流れるので、下降流路6に流
入するときの流速は、図示のように傾斜板3a,
3bの傾斜角度が60゜であるとき1/2となり、傾
斜板3a,3bの下端から滑り落ちるSSは、下
降流路6内の下降水流により速やかに垂直下向き
に転向し、下降流路6の内側寄り位置を流れるた
め、分離部31に於ける澄清水の分離が容易に行
われる。 Since the raw water in the inclined sedimentation layer 4 flows downward along the surfaces of the inclined plates 3a and 3b, the flow velocity when flowing into the downward flow path 6 is as shown in the figure.
When the inclination angle of plate 3b is 60 degrees, it becomes 1/2, and the SS that slides down from the lower ends of the inclined plates 3a and 3b is quickly turned vertically downward by the downward flow in the downward flow path 6, and inside the downward flow path 6. Since the water flows at the offset position, clear water can be easily separated in the separating section 31.
第6図乃至第8図は本発明の他の実施例を示
し、第1図乃至第4図に示した実施例と対応する
箇所には同一符号を付してる。この実施例では、
上槽1及び下槽2は横断面矩形状であつて、上槽
1の中央部位置に全巾にわたつて原水供給垂直流
路5が形成され、この原水供給垂直流路5の左右
両側に矩形の傾斜板32によつて区画された傾斜
沈殿層4が左右対称形に形成され、更にこれ等傾
斜沈殿層4の下端に隣接して、上槽1の対向両側
辺全巾にわたつて下降流路6及び上昇流路7が、
垂直区画板33によつて形成されている。又、最
下段の矩形傾斜板32の下側空間34が集水器9
を兼用しており、この空間34内の頂部に上昇水
管11と連通する集水用多孔管35が架設されて
いる。下槽2の漏斗部8は平面矩形状であるか
ら、その中央底部は傾斜した樋状に構成され、こ
の樋状底部8a内に前記排出管10に連通する排
出用多孔管36が配設されている。 6 to 8 show other embodiments of the present invention, and parts corresponding to the embodiment shown in FIGS. 1 to 4 are given the same reference numerals. In this example,
The upper tank 1 and the lower tank 2 have a rectangular cross section, and a raw water supply vertical channel 5 is formed in the center of the upper tank 1 over the entire width. A sloped sedimentation layer 4 partitioned by rectangular sloped plates 32 is formed in a symmetrical shape, and further adjacent to the lower end of the sloped sedimentation layer 4, descends over the entire width of both opposite sides of the upper tank 1. The flow path 6 and the ascending flow path 7 are
It is formed by vertical partition plates 33. In addition, the lower space 34 of the rectangular inclined plate 32 at the lowest stage is the water collector 9.
A water collecting porous pipe 35 communicating with the rising water pipe 11 is installed at the top of this space 34. Since the funnel portion 8 of the lower tank 2 has a rectangular planar shape, its central bottom is configured in the shape of an inclined gutter, and a porous discharge pipe 36 communicating with the discharge pipe 10 is disposed within this gutter-like bottom portion 8a. ing.
更に澄清水受槽25は、前記垂直区画板33の
上端が上昇流路7上端からの澄清水の溢流堰を兼
用するように、上槽1内にその全巾にわたつて樋
状に形成され、横長の原水供給垂直流路5の上端
には、給水管16より供給される原水を前記原水
供給垂直流路5の水平方向全長にわたつて均等に
分配するための原水分配樋36が設けられてい
る。37はこの樋36内の原水水位を一定に保つ
ための溢流堰であり、溢流水は槽外に排出され
る。 Further, the clear water receiving tank 25 is formed in the shape of a gutter over the entire width within the upper tank 1 so that the upper end of the vertical partition plate 33 also serves as an overflow weir for clear water from the upper end of the ascending channel 7. A raw water distribution gutter 36 is provided at the upper end of the horizontally long raw water supply vertical channel 5 to evenly distribute the raw water supplied from the water supply pipe 16 over the entire horizontal length of the raw water supply vertical channel 5. ing. 37 is an overflow weir for keeping the raw water level in the gutter 36 constant, and the overflow water is discharged to the outside of the tank.
尚、図示の構造では2組の沈殿装置を一体に並
設しており、従つて互いに隣接する上槽壁は省略
し、この隣接部に共通の上昇流路7を配置してい
る。 In the illustrated structure, two sets of sedimentation devices are installed side by side, so the upper tank walls adjacent to each other are omitted, and a common ascending channel 7 is arranged in the adjacent portion.
この実施例の方形型沈殿装置の使用方法及び作
用は先に第1図乃至第4図に示した円形型沈殿装
置の使用方法及び作用と基本的に同一であるか
ら、説明を省く。 The usage and operation of the rectangular precipitation apparatus of this embodiment are basically the same as the usage and operation of the circular precipitation apparatus shown in FIGS. 1 to 4, so a description thereof will be omitted.
本発明の沈殿装置は以上の実施例のように実施
し且つ使用し得るものであつて、その特徴は、上
槽と下槽とを備え、上槽内には、複数段の傾斜板
によつて区画された多段傾斜沈殿層、これ等多段
傾斜沈殿層の上端入口部に連通する原水供給垂直
流路、前記多段傾斜沈殿層の下端出口部に連通す
る下降流路、及びこの下降流路の下端開口に隣接
して下端開口を有する上昇流路を設け、前記下槽
は前記下降流路と上昇流路との下端開口と連通す
ると共に、内部には、沈殿物収集用漏斗部とこの
漏斗部の上方に開口する集水器とを備え、前記漏
斗部の底部には沈殿物を原水と共に排出する排出
管を連設し、前記上昇流路の上端と前記集水器に
連通する上昇水管の上端とから澄清水を溢流放出
させるようにした点にある。 The precipitation apparatus of the present invention can be implemented and used as in the above embodiments, and its characteristics include an upper tank and a lower tank, and the upper tank has multiple stages of inclined plates. A vertical flow path for supplying raw water communicating with the upper end inlet of the multi-stage inclined sedimentation layer, a downward flow path communicating with the lower end outlet of the multi-stage inclined sedimentation layer, and a downward flow path of the downward flow path. An ascending channel having a lower end opening is provided adjacent to the lower end opening, and the lower tank communicates with the lower end openings of the descending channel and the ascending channel. a water collector that opens above the funnel part, a discharge pipe for discharging sediment together with the raw water is connected to the bottom of the funnel part, and a rising water pipe that communicates with the upper end of the ascending channel and the water collector. The point is that clear water is allowed to overflow and discharge from the upper end of the pipe.
即ち本発明によれば、上槽に於ては、原水の水
流方向と傾斜板上でのSSの流下方向とが同一で
ある傾斜沈殿層が上下方向多段に積層されている
ため、装置の単位据え付け面積当りの沈殿面積が
増加し、傾斜板上の傾斜沈殿層(原水流路)の断
面積が増加するので、一定の原水供給量に対して
傾斜沈殿層内での原水の流速を低下させて沈殿時
間を延すと共に、傾斜板上の原水層の厚さを薄く
してSSの沈降距離を短縮せしめ、原水中のSSの
沈降分離を極めて効率良く行わせることが出来
る。しかも下降流路では、SS濃度の極めて高い
原水を内側寄りに偏らせて原水を流下させ、この
下降流路の下端と外側の上昇流路下端とが隣接す
る分離部に於て、内側寄り位置を層状に流下する
SS濃度の高い原水から外側寄り位置を層状に流
れる澄清水を良好に分離し、当該澄清水を一次澄
清水として上昇流路から取り出すことが出来る。
そして、SS濃度の高い残りの原水は下槽内に流
入させ、当該原水が下槽内に於ける漏斗部上方の
集水器に向かつてUターンするときSSを沈降分
離させ、二次澄清水を前記集水器に連通する上昇
水管より取り出すことが出来る。 That is, according to the present invention, in the upper tank, the inclined sedimentation layers in which the flow direction of the raw water and the flow direction of the SS on the inclined plate are the same are stacked in multiple stages in the vertical direction, so that the unit of the device is The sedimentation area per installation area increases, and the cross-sectional area of the sloped sedimentation layer (raw water flow path) on the sloped plate increases, so the flow rate of raw water in the sloped sedimentation layer decreases for a constant raw water supply amount. In addition to extending the settling time, the thickness of the raw water layer on the inclined plate is reduced to shorten the settling distance of SS, and the settling and separation of SS in the raw water can be carried out extremely efficiently. Moreover, in the descending flow path, the raw water with extremely high SS concentration is biased toward the inside, and the raw water flows down, and at the separation part where the lower end of the descending flow path and the lower end of the outer ascending flow path are adjacent, the raw water is biased toward the inside. flows down in layers
It is possible to effectively separate the clear water flowing in layers near the outer side from the raw water with a high SS concentration, and take out the clear water from the ascending channel as primary clear water.
The remaining raw water with a high concentration of SS flows into the lower tank, and when the raw water makes a U-turn toward the water collector above the funnel in the lower tank, the SS is sedimented and separated, resulting in secondary clear water. can be taken out from a rising water pipe communicating with the water collector.
このように本発明の沈殿装置は、据え付け占有
面積の小なるコンパクトな装置として実施し得る
ものであり乍ら、極めて効率良く原水中のSSを
沈殿分離し、必要な澄清度の澄清水として取り出
すことが出来るものである。更に、下槽漏斗部の
底部に収集された沈殿物は、装置内の原水を利用
して装置外に流動排出することが出来、沈殿物の
排出に特別な動力を必要としない。 As described above, the precipitation device of the present invention can be implemented as a compact device that occupies a small installation area, and yet can very efficiently precipitate and separate SS in raw water and extract it as clear water with the required clarity. It is something that can be done. Furthermore, the sediment collected at the bottom of the lower tank funnel can be fluidly discharged out of the apparatus using raw water within the apparatus, and no special power is required to discharge the sediment.
尚、実施例に示したように各段の傾斜沈殿層を
形成する傾斜板間に、上段の傾斜板を支持する堰
板21を介装するときは、この堰板21をして、
傾斜沈殿層4内に流動する原水の整流板として機
能させることが出来、傾斜沈殿層4内で原水が短
絡流となつたり偏流となつたりするのを防止する
ことが出来る。 In addition, as shown in the example, when the weir plate 21 that supports the upper stage inclined plate is interposed between the inclined plates forming the inclined sediment layer of each stage, this weir plate 21 is
It can function as a rectifying plate for the raw water flowing in the inclined sedimentation layer 4, and can prevent the raw water from becoming a short-circuit flow or a drifting flow in the inclined sedimentation layer 4.
又、実施例では上昇流路7から溢流する一次澄
清水と上昇水管11から溢流する二次澄清水とを
一緒にして取り出すように構成したが、夫々各別
に取り出すことも可能である。 Further, in the embodiment, the primary clear water overflowing from the ascending flow path 7 and the secondary clear water overflowing from the ascending water pipe 11 are taken out together, but it is also possible to take out each separately.
第1図は第一実施例を示す縦断側面図、第2図
は同平面図、第3図は同要部の拡大縦断側面図、
第4図は同要部の拡大横断平面図、第5図はSS
分離作用状態と原水の流れの状態とを示す説明
図、第6図は第二実施例を示す縦断側面図、第7
図は同縦断正面図、第8図は同横断平面図であ
る。
1……上槽、2……下槽、3a〜3c……円形
の傘形傾斜板、4……傾斜沈殿層、5……原水供
給垂直流路、6……下降流路、7……上昇流路、
8……沈殿物収集用漏斗部、9……集水器、10
……排出管、11……上昇水管、12……水位調
整槽、13……原水管、14……溢流管、16…
…給水管、21……堰板、23……有蓋内筒、2
4……支持板、25……澄清水受槽、26……流
量調節槽、28……放出管、31……分離部、3
2……矩形傾斜板、33……垂直区画板、35…
…集水用多孔管、36……排出用多孔管。
FIG. 1 is a vertical side view showing the first embodiment, FIG. 2 is a plan view of the same, and FIG. 3 is an enlarged vertical side view of the same main part.
Figure 4 is an enlarged cross-sectional plan view of the main part, Figure 5 is the SS
An explanatory diagram showing the state of separation action and the state of flow of raw water, FIG. 6 is a vertical cross-sectional side view showing the second embodiment, and FIG.
The figure is a longitudinal sectional front view of the same, and FIG. 8 is a sectional plan view of the same. 1... Upper tank, 2... Lower tank, 3a to 3c... Circular umbrella-shaped inclined plate, 4... Inclined sedimentation layer, 5... Raw water supply vertical channel, 6... Downward channel, 7... rising flow path,
8... Funnel part for collecting sediment, 9... Water collector, 10
... Discharge pipe, 11 ... Rising water pipe, 12 ... Water level adjustment tank, 13 ... Raw water pipe, 14 ... Overflow pipe, 16 ...
... Water supply pipe, 21 ... Weir plate, 23 ... Covered inner cylinder, 2
4...Support plate, 25...Clear water receiving tank, 26...Flow rate adjustment tank, 28...Discharge pipe, 31...Separation section, 3
2... Rectangular inclined plate, 33... Vertical partition plate, 35...
...Porous pipe for water collection, 36...Porous pipe for discharge.
Claims (1)
傾斜板によつて区画された多段傾斜沈殿層、これ
等多段傾斜沈殿層の上端入口部に連通する原水供
給垂直流路、前記多段傾斜沈殿層の下端出口部に
連通する下降流路、及びこの下降流路の下端開口
に隣接して下端開口を有する上昇流路を設け、前
記下槽は前記下降流路と上昇流路との下端開口と
連通すると共に、内部には、沈殿物収集用漏斗部
とこの漏斗部の上方に開口する集水器とを備え、
前記漏斗部の底部には沈殿物を原水と共に排出す
る排出管を連設し、前記上昇流路の上端と前記集
水器に連通する上昇水管の上端とから澄清水を溢
流放出させるようにした沈殿装置。1.Equipped with an upper tank and a lower tank, the upper tank includes a multi-stage inclined sedimentation layer partitioned by multiple stages of inclined plates, and a raw water supply vertical channel communicating with the upper end inlet of these multi-stage inclined sedimentation layers. , a descending channel communicating with the lower end outlet of the multi-stage inclined sedimentation layer, and an ascending channel having a lower end opening adjacent to the lower end opening of the descending channel, and the lower tank is connected to the descending channel and the ascending channel. It communicates with the opening at the lower end of the channel, and is provided with a sediment collecting funnel part and a water collector opening above the funnel part;
A discharge pipe for discharging sediment together with raw water is connected to the bottom of the funnel part, and clear water is overflowed and discharged from the upper end of the ascending flow path and the upper end of the ascending water pipe communicating with the water collector. precipitation equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18735983A JPS6082108A (en) | 1983-10-05 | 1983-10-05 | Precipitation apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18735983A JPS6082108A (en) | 1983-10-05 | 1983-10-05 | Precipitation apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6082108A JPS6082108A (en) | 1985-05-10 |
| JPS6147562B2 true JPS6147562B2 (en) | 1986-10-20 |
Family
ID=16204611
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18735983A Granted JPS6082108A (en) | 1983-10-05 | 1983-10-05 | Precipitation apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6082108A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11679345B2 (en) * | 2020-03-19 | 2023-06-20 | Sudhin Biopharma | Particle settling devices |
| JP7246800B1 (en) * | 2022-10-28 | 2023-03-28 | 龍 静観 | sedimentation tank |
-
1983
- 1983-10-05 JP JP18735983A patent/JPS6082108A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6082108A (en) | 1985-05-10 |
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