JPH0672605U - Coagulating sedimentation equipment - Google Patents
Coagulating sedimentation equipmentInfo
- Publication number
- JPH0672605U JPH0672605U JP2004993U JP2004993U JPH0672605U JP H0672605 U JPH0672605 U JP H0672605U JP 2004993 U JP2004993 U JP 2004993U JP 2004993 U JP2004993 U JP 2004993U JP H0672605 U JPH0672605 U JP H0672605U
- Authority
- JP
- Japan
- Prior art keywords
- feed well
- water
- settling tank
- water surface
- treated water
- 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
Links
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
(57)【要約】
【目的】 フィードウェルの上端から一部の汚泥がリー
クして処理水に混入するのを防止する。
【構成】 沈殿槽10内の水面下にスラッジブランケッ
ト層14を内部に有するフィードウェル11を上下方向
に設け、原水を上記フィードウェルの底部上に接線方向
に供給し、処理水を沈殿槽の上部から排水するようにし
た凝集沈殿装置において、上記フィードウェル11より
も大径な短絡防止筒18を、その上端が水面上、下端が
フィードウェルの上端よりも下になるようにフィードウ
ェルを囲んで設ける。
(57) [Summary] [Purpose] To prevent some sludge from leaking from the upper end of the feed well and mixing into the treated water. [Structure] A feed well 11 having a sludge blanket layer 14 therein is provided vertically below the water surface in a settling tank 10, raw water is tangentially supplied onto the bottom of the feed well, and treated water is provided above the settling tank. In the coagulation-sedimentation device configured to drain water from the feed well 11, a short-circuit prevention cylinder 18 having a diameter larger than that of the feed well 11 is surrounded by the upper end of the cylinder 18 above the water surface and the lower end thereof below the upper end of the feed well. Set up.
Description
【0001】[0001]
この考案は、廃水中のSSを凝集し、且つ沈降分離して清澄な処理水を得るス ラッジブランケット型の凝集沈殿装置に関する。 The present invention relates to a sludge blanket type coagulation-sedimentation apparatus that coagulates SS in wastewater and sediments and separates it to obtain clear treated water.
【0002】[0002]
沈殿槽内の水面下にスラッジブランケット層を内部に有するフィードウェルを 上下方向に設け、原水を上記フィードウェルの底部上に接線方向に供給し、処理 水を沈殿槽の上部から排水するようにしたスラッジブランケット型の凝集沈殿装 置は公知である。 上記従来装置では、フィードウェルの内部に、高さがフィードウェルよりも少 し低く、下端はフィードウェルの底の開口と連通する内筒を同心状に設け、フィ ードウェル内を上昇したスラッジを内筒の上端から筒内に溢入させ沈殿槽の底に 沈降させる。 A feedwell having a sludge blanket layer inside was set vertically below the water surface in the settling tank, raw water was tangentially supplied to the bottom of the feedwell, and treated water was drained from the upper part of the settling tank. Sludge blanket type coagulating sedimentation devices are known. In the above conventional apparatus, the height of the feed well is lower than that of the feed well, and the lower end of the feed well is concentrically provided with an inner cylinder communicating with the opening at the bottom of the feed well. Overflow from the top of the cylinder into the cylinder and settle to the bottom of the settling tank.
【0003】[0003]
しかし、原水はフィードウェルの内部に接線方向に供給されるのでフィードウ ェルの内部では旋回流が生じ、この旋回流によってスラッジの一部はフィードウ ェルの上端から外に出、処理水に混ざって排出され、処理水の水質を低下させる 。 However, since the raw water is supplied tangentially to the inside of the feedwell, a swirl flow is generated inside the feedwell, and this swirl flow causes a part of the sludge to flow out from the upper end of the feedwell and mix with the treated water. Is discharged as a wastewater and reduces the quality of treated water.
【0004】[0004]
本考案は、フィードウェル内に原水を接線方向に導入し、これによりフィード ウェルの内部でスラッジブランケット層が旋回してもスラッジが処理水にリーク するのを防止するようにしたもので、沈殿槽内の水面下にスラッジブランケット 層を内部に有するフィードウェルを上下方向に設け、原水を上記フィードウェル の底部上に接線方向に供給し、処理水を沈殿槽の上部から排水するようにした凝 集沈殿装置において、上記フィードウェルよりも大径な短絡防止筒を、その上端 が水面上、下端がフィードウェルの上端よりも下になるようにフィードウェルを 囲んで設けたことを特徴とする。 In the present invention, raw water is introduced tangentially into the feed well to prevent the sludge from leaking into the treated water even if the sludge blanket layer swirls inside the feed well. A feed well having a sludge blanket layer inside is vertically provided below the water surface inside, and raw water is tangentially supplied onto the bottom of the feed well, and the treated water is drained from the upper part of the settling tank. In the settling device, a short-circuit prevention cylinder having a diameter larger than that of the feed well is provided so as to surround the feed well such that the upper end thereof is above the water surface and the lower end thereof is below the upper end of the feed well.
【0005】[0005]
10は中心が低い円錐面の底を有する沈殿槽、11は上記沈殿槽内の水面下に 同心状に設けたフィードウェル、12はフィードウェルの内部の底の上に原水を 接線方向に供給する給水管、13は給水管12にポリマー等の凝集剤を注入する 薬注管であり、フィードウェル11は内部にスラッジブランケット層14を有す る。 薬注管13からポリマーが注入された原水はフィードウェルに向かって給水管 中を流れる際と、フィードウェル内に接線方向に流入して旋回しながら上昇する 際に凝集作用を行い、微細なフロックとなる。そして、フィードウェル内で旋回 しながら上昇する微細フロックは、一緒に旋回するスラッジブランケット層の大 きなフロックに捕捉される。 こうしてフィードウェル内のスラッジブランケット層を構成するフロックは次 第に粗大化し、沈降性が良好になる。そして、フィードウェルの上端に達した粗 大フロック(汚泥)は旋回しながらフィードウェルの外に出、沈殿槽の底に沈降 し、沈降した粗大フロックは沈殿槽の底面上で回転するレーキ15によって中央 の集泥ピット16に掻き入れられ、こゝから排泥管17で排出される。 10 is a settling tank having a conical bottom with a low center, 11 is a feed well concentrically provided below the water surface in the settling tank, and 12 is tangential supply of raw water on the inner bottom of the feed well. A water supply pipe 13 is a chemical injection pipe for injecting a coagulant such as a polymer into the water supply pipe 12, and the feed well 11 has a sludge blanket layer 14 inside. The raw water in which the polymer is injected from the chemical injection pipe 13 performs a coagulation action when flowing through the water supply pipe toward the feed well and when flowing upward in a tangential direction into the feed well while swirling, and thus fine flocs are formed. Becomes Then, the fine flocs that rise while swirling in the feedwell are captured by the large flocs of the sludge blanket layer that swirls together. In this way, the flocs composing the sludge blanket layer in the feed well are secondarily coarsened and the sedimentation property is improved. Coarse flocs (sludge) reaching the upper end of the feedwell swirl out of the feedwell and settle to the bottom of the sedimentation tank. The sedimented coarse flocs are raked on the bottom of the sedimentation tank by a rake 15. It is scraped into the central mud collection pit 16 and discharged from this through the mud pipe 17.
【0006】 18はフィードウェルよりも直径が大きい短絡防止筒で、上端が水面上、下端 はフィードウェルの上端よりも下になるようにフィードウェルを囲んで沈殿槽に 設けてある。 フィードウェルの上端は水面下3〜20cmに位置し、短絡防止筒18の下端 は水面下10〜30cmに位置する。これによりフィードウェルの上端から旋回 しながら外に出る粗大フロックは短絡防止筒18で遮られて沈殿槽の内周の集水 樋19に行くことができずに沈降し、処理水のみが短絡防止筒の下を潜って集水 樋19に溢入し、排水管20で排水される。Reference numeral 18 denotes a short-circuit prevention cylinder having a diameter larger than that of the feed well, and is provided in a sedimentation tank surrounding the feed well so that the upper end is above the water surface and the lower end is below the upper end of the feed well. The upper end of the feed well is located 3 to 20 cm below the water surface, and the lower end of the short-circuit prevention cylinder 18 is located 10 to 30 cm below the water surface. As a result, coarse flocs that come out while swirling from the upper end of the feedwell are blocked by the short-circuit prevention cylinder 18 and cannot settle in the water collecting trough 19 on the inner circumference of the settling tank, and settle down, preventing only short-circuiting of the treated water. It dives under the cylinder, overflows into the water collecting gutter 19, and is drained by the drainage pipe 20.
【0007】 フィードウェルの直径は、沈殿槽の直径1/2〜1/5程度にする。又、フィ ードウェルの上下方向の長さは沈殿槽の深さの0.6〜1.0近くにしてフィー ドウェル内での原水の滞流時間を3〜10分とし、上昇速度の早い微細フロック とスラッジブランケット層を構成するフロックとの接触頻度を高め、フロックの 粗大化を図ることが好ましい。 図中、21はレーキ15を回転するため、フィードウェルを貫通して設けたモ ータで駆動される回転軸を示す。尚、回転軸がフィードウェルを貫通する部分に は、原水中の砂利等の夾雑物を排除できるように0.5〜2cm幅の間隙が設け てある。The diameter of the feed well is set to about 1/2 to 1/5 of the diameter of the settling tank. Also, the vertical length of the feedwell is set to 0.6 to 1.0 of the depth of the settling tank, and the retention time of the raw water in the feedwell is set to 3 to 10 minutes, and the fine floc with a high rising speed is used. It is preferable to increase the frequency of contact between the flocs composing the sludge blanket layer and the flocs to coarsen the flocs. In the figure, reference numeral 21 denotes a rotation shaft driven by a motor provided to penetrate the feed well for rotating the rake 15. A gap having a width of 0.5 to 2 cm is provided at a portion where the rotating shaft penetrates the feed well so that impurities such as gravel in the raw water can be removed.
【0008】[0008]
以上で明らかなように、本考案によればフィードウェルの上端から一部の汚泥 がリークして処理水に混ざるのが確実に防止できる。従って、処理水の水質は低 下せず、清澄な処理水が得られる。 As is clear from the above, according to the present invention, it is possible to reliably prevent a part of sludge from leaking from the upper end of the feedwell and mixing with the treated water. Therefore, the quality of the treated water does not deteriorate, and clear treated water can be obtained.
【図面の簡単な説明】[Brief description of drawings]
【図1】本考案の凝集沈殿装置の断面図である。FIG. 1 is a cross-sectional view of a coagulating sedimentation device of the present invention.
【図2】図1の一部の平面図である。FIG. 2 is a plan view of a part of FIG.
10 沈殿槽 11 フィードウェル 12 給水管 13 薬注管 14 スラッジブランケット層 18 短絡防止筒 10 Settling tank 11 Feed well 12 Water supply pipe 13 Chemical injection pipe 14 Sludge blanket layer 18 Short-circuit prevention cylinder
Claims (1)
ト層を内部に有するフィードウェルを上下方向に設け、
原水を上記フィードウェルの底部上に接線方向に供給
し、処理水を沈殿槽の上部から排水するようにした凝集
沈殿装置において、上記フィードウェルよりも大径な短
絡防止筒を、その上端が水面上、下端がフィードウェル
の上端よりも下になるようにフィードウェルを囲んで設
けたことを特徴とする凝集沈殿装置。1. A feed well having a sludge blanket layer inside is provided below the water surface in a settling tank in a vertical direction,
In a coagulating sedimentation apparatus in which raw water is tangentially supplied to the bottom of the feed well and the treated water is drained from the upper part of the sedimentation tank, a short-circuit prevention cylinder having a diameter larger than that of the feed well, the upper end of which is the water surface. An aggregating and precipitating device which is provided so as to surround the feed well so that the upper and lower ends are lower than the upper end of the feed well.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2004993U JPH0672605U (en) | 1993-03-29 | 1993-03-29 | Coagulating sedimentation equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2004993U JPH0672605U (en) | 1993-03-29 | 1993-03-29 | Coagulating sedimentation equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0672605U true JPH0672605U (en) | 1994-10-11 |
Family
ID=12016210
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2004993U Pending JPH0672605U (en) | 1993-03-29 | 1993-03-29 | Coagulating sedimentation equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0672605U (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010023009A (en) * | 2008-07-24 | 2010-02-04 | Sumitomo Heavy Industries Environment Co Ltd | Flocculation and sedimentation apparatus and flocculation and sedimentation method |
JP2010179255A (en) * | 2009-02-06 | 2010-08-19 | Daiki Ataka Engineering Co Ltd | Agitating and mixing device, and precipitating vessel equipped with the same |
JP2010274199A (en) * | 2009-05-28 | 2010-12-09 | Sumitomo Heavy Industries Environment Co Ltd | Coagulation sedimentation apparatus |
JP2013536057A (en) * | 2010-06-10 | 2013-09-19 | エスアイジー テクノロジー アーゲー | Product storage apparatus and method |
WO2014171421A1 (en) * | 2013-04-16 | 2014-10-23 | 住友重機械エンバイロメント株式会社 | Solid-liquid separation apparatus and solid-liquid separation method |
JP2016190210A (en) * | 2015-03-31 | 2016-11-10 | 住友重機械エンバイロメント株式会社 | Flocculation and sedimentation treatment device |
JP2016190185A (en) * | 2015-03-31 | 2016-11-10 | 住友重機械エンバイロメント株式会社 | Coagulating and precipitating treatment apparatus |
JP2021142476A (en) * | 2020-03-11 | 2021-09-24 | 住友重機械エンバイロメント株式会社 | Precipitation processor |
-
1993
- 1993-03-29 JP JP2004993U patent/JPH0672605U/en active Pending
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010023009A (en) * | 2008-07-24 | 2010-02-04 | Sumitomo Heavy Industries Environment Co Ltd | Flocculation and sedimentation apparatus and flocculation and sedimentation method |
JP2010179255A (en) * | 2009-02-06 | 2010-08-19 | Daiki Ataka Engineering Co Ltd | Agitating and mixing device, and precipitating vessel equipped with the same |
JP2010274199A (en) * | 2009-05-28 | 2010-12-09 | Sumitomo Heavy Industries Environment Co Ltd | Coagulation sedimentation apparatus |
JP2013536057A (en) * | 2010-06-10 | 2013-09-19 | エスアイジー テクノロジー アーゲー | Product storage apparatus and method |
WO2014171421A1 (en) * | 2013-04-16 | 2014-10-23 | 住友重機械エンバイロメント株式会社 | Solid-liquid separation apparatus and solid-liquid separation method |
JPWO2014171421A1 (en) * | 2013-04-16 | 2017-02-23 | 住友重機械エンバイロメント株式会社 | Solid-liquid separation device and solid-liquid separation method |
JP2016190210A (en) * | 2015-03-31 | 2016-11-10 | 住友重機械エンバイロメント株式会社 | Flocculation and sedimentation treatment device |
JP2016190185A (en) * | 2015-03-31 | 2016-11-10 | 住友重機械エンバイロメント株式会社 | Coagulating and precipitating treatment apparatus |
JP2021142476A (en) * | 2020-03-11 | 2021-09-24 | 住友重機械エンバイロメント株式会社 | Precipitation processor |
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