JPS6045924B2 - Sheep drum for sludge treatment - Google Patents
Sheep drum for sludge treatmentInfo
- Publication number
- JPS6045924B2 JPS6045924B2 JP58183291A JP18329183A JPS6045924B2 JP S6045924 B2 JPS6045924 B2 JP S6045924B2 JP 58183291 A JP58183291 A JP 58183291A JP 18329183 A JP18329183 A JP 18329183A JP S6045924 B2 JPS6045924 B2 JP S6045924B2
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- sieve drum
- drum
- 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.)
- Expired
Links
Description
【発明の詳細な説明】
本発明は下水処理場より回収された汚泥の脱水処理を行
うのに適したシーブドラムに関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a sieve drum suitable for dewatering sludge collected from a sewage treatment plant.
従来下水処理場より回収された汚泥は含水率が高くその
ままでは投棄あるいは埋立さらに発酵処理が行えないた
め脱水処理をしている。Conventionally, sludge collected from sewage treatment plants has a high water content and cannot be dumped, landfilled, or fermented as it is, so it is dehydrated.
しかしこの脱水法は回収された高含水率の汚泥に凝集剤
を添加した後、凝集混和槽へ投入し、次にベルトプレス
式の脱水機へ供給し、所望の脱水を行なつた後、脱水ケ
ーキとして次の工程へ送出すると共に脱水機て排出され
た排水を沈殿槽へー旦導びき、汚泥粒子を沈殿せしめた
上澄水を脱水機の洗浄水として使用している。しカルこ
の方法ては汚泥が凝集剤て凝集した後直接脱離水ととも
脱水機へ供給し、脱水するため脱水効率が悪く、又洗浄
水としての脱離水の再利用効率も悪いものてある。本発
明はこれに鑑みて脱離水を効率的に再利用しつつ脱水効
率を向上せしめるようになした汚泥処理用シーブ下ラム
を提案するもので、次に図示の実施例について本発明を
詳細に説明する。図に於て1は下水処理場等より回収さ
れた汚泥の処理用シーブドラム本体で、この汚泥処理用
シーブドラム1は図示の如く横方向に配してコロ3等に
より回動自在に支持する。シーブドラム1はその内部を
前段IAと後段IBとに分け、シーブドラム前段IA内
に凝集混和槽4を設ける。この凝集混和槽4内には攪拌
用の羽根5があり、その前部には汚泥供給管2を設ける
。予じめ粗大ごみ等を除いた汚泥は、凝集液と混合しス
タティックミキサー等で混合した後、適当な移送手段で
汚泥供給管2を経て凝集混和槽4に供給される。シーブ
ドラム回動時該ドラムと一体となつた凝集混和槽もとも
に回動し、羽根5にて所望の混合攪拌が行なわれるよう
になす。またこの凝集混和槽4のJ外周部には処理水例
えは脱水機から脱離水等を給水管6を介して供給し、シ
ーブドラム前後部外周にてろ過される。またシーブドラ
ムの後端部内には羽根7を設け、前段部にて凝集剤と充
分に混合された汚泥が供給されてここでさらに混合攪拌
さiれつつ一次脱水が行なわれる。脱水後の汚泥はシー
ブドラム開口端より順次排出され、脱離水はシーブ下ラ
ム前後段よりシーブドラム下方に設けた集水シュート8
内へ落下して排出されるものである。シーブドラム1の
外周面の洗浄はシーブドラム上方に配した洗浄ノズル9
より噴出する洗浄水にて行なわれる。而して下水処理場
等より回収された汚泥は凝集液と予め混合されてシーブ
ドラム内に設けられた凝集混和槽内へ供給され、しかも
シーブドラム内で、この凝集混和槽の外周部内には脱水
機等よりの脱離水その他からの処理水の供給をうけ、汚
泥は回転する該槽4内で凝固され、また排水中の固形物
はシーブ下ラムにてろ過され除去され脱離水はシーブド
ラムより淵過排水して固形物と水とを分離すると共にシ
ーブドラムの目詰りはシーブドラム外周上方より洗浄ノ
ズルより洗浄水が噴射されて防止される。However, this dewatering method involves adding a flocculant to the collected sludge with a high water content, feeding it into a flocculating mixing tank, then feeding it to a belt press type dehydrator, performing the desired dewatering process, and then dewatering the sludge. The cake is sent to the next process, and the wastewater discharged from the dehydrator is first led to a settling tank, and the supernatant water in which the sludge particles are precipitated is used as washing water for the dehydrator. In this method, the sludge is flocculated using a flocculant and then directly supplied to the dehydrator together with the dehydrated water for dehydration, resulting in poor dewatering efficiency and poor reuse efficiency of the dehydrated water as washing water. In view of this, the present invention proposes a ram under a sieve for sludge treatment that improves dewatering efficiency while efficiently reusing desorbed water. explain. In the figure, reference numeral 1 denotes a sieve drum body for treating sludge collected from a sewage treatment plant, etc. This sieve drum 1 for sludge treatment is arranged laterally as shown in the figure and rotatably supported by rollers 3 and the like. The inside of the sieve drum 1 is divided into a front stage IA and a rear stage IB, and a flocculation mixing tank 4 is provided in the front stage IA of the sieve drum. There are stirring blades 5 in the flocculation mixing tank 4, and a sludge supply pipe 2 is provided in front of the blades 5. The sludge, from which bulky waste and the like have been removed in advance, is mixed with a flocculating liquid using a static mixer or the like, and then supplied to the flocculation mixing tank 4 via the sludge supply pipe 2 by an appropriate transfer means. When the sieve drum rotates, the flocculation mixing tank integrated with the drum also rotates, so that the desired mixing and agitation is performed by the blades 5. Also, treated water, such as desorbed water from a dehydrator, is supplied to the J outer periphery of the flocculation mixing tank 4 via a water supply pipe 6, and is filtered at the front and rear outer peripheries of the sieve drum. Further, blades 7 are provided in the rear end of the sieve drum, and sludge sufficiently mixed with a flocculant is supplied to the front end of the sieve drum, where it is further mixed and agitated and primary dewatering is performed. The sludge after dewatering is sequentially discharged from the opening end of the sieve drum, and the desorbed water flows from the front and back stages of the sieve lower ram to a water collection chute 8 installed below the sieve drum.
It falls inside and is ejected. The outer peripheral surface of the sheave drum 1 is cleaned using a cleaning nozzle 9 placed above the sheave drum.
This is done using washing water that is spouted out. The sludge collected from sewage treatment plants, etc. is mixed in advance with flocculating liquid and supplied to the flocculation-mixing tank installed in the sieve drum, and inside the sieve drum, a dewatering machine is installed inside the outer periphery of this flocculation-mixing tank. The sludge is solidified in the rotating tank 4, solids in the waste water are filtered and removed by the ram under the sieve, and the desorbed water is passed through the sieve drum. Water is drained to separate solids and water, and clogging of the sieve drum is prevented by spraying cleaning water from a cleaning nozzle from above the outer periphery of the sieve drum.
このシーブドラムで分離された汚泥の固形分は次工程の
脱水機へ送られ、さらに脱水され、所望の含水率にして
脱水ケーキとして次工程へ送られて処理されるが、シー
ブドラムより分離された脱離水はタンクにて一時貯水し
てポーンプにてシーブ下ラム洗浄用ノズルや脱水機の沖
布洗浄ノズルへ供給して洗浄水として利用する。また脱
水機等にて脱水された脱離水もポンプにてシーブドラム
内へ供給する。また脱水機等より排水はシーブドラム内
に設けられた通内へ直接供給することもある。本発明に
よる時はシーブドラムを前後に分け前段部には凝集混和
槽を設けているので、凝集剤を汚泥に混入して供給され
てこの槽内で混合攪拌が充分に行なわれて凝集されると
共に該槽内に供給される処理水もともに?過処理され、
しかも該ドラムの後段部ではさらに凝集された汚泥が脱
水されるようになしているため汚泥と脱離水とが分離し
て排出されるため次工程での処理が簡易になると共にさ
らにはシーブドラムも簡単な構造で、安価に提供できる
等の利点を有する。The solid content of the sludge separated in this sieve drum is sent to the next step, a dehydrator, where it is further dehydrated and made to a desired moisture content and sent to the next step as a dehydrated cake for treatment. Separated water is temporarily stored in a tank and supplied by a pump to the nozzle for cleaning the ram under the sheave and the cleaning nozzle for cleaning cloth in the dehydrator for use as cleaning water. In addition, dehydrated water dehydrated using a dehydrator or the like is also supplied into the sieve drum by a pump. In addition, wastewater from a dehydrator or the like may be directly supplied to a passage provided in the sieve drum. According to the present invention, the sieve drum is divided into front and rear parts, and a coagulation mixing tank is provided in the front stage, so the flocculant is mixed with the sludge and supplied, and the sludge is thoroughly mixed and agitated in this tank, and is coagulated. Also the treated water supplied to the tank? overprocessed,
Moreover, since the coagulated sludge is further dewatered in the latter part of the drum, the sludge and desorbed water are separated and discharged, which simplifies the treatment in the next process and also simplifies the construction of the sieve drum. It has the advantage of having a simple structure and being able to be provided at low cost.
第1図は外面図、第2図は断面図てある。
1・・・・・・シーブドラム、2・・・・・汚泥供給管
、3・・・・・・コロ、4・・・・・凝集混和槽、5・
・・・・羽根、6・・・給水管、7・・・・・羽根、8
・・・・・・集水シュート、9・・・・・・洗浄ノズル
。FIG. 1 is an external view, and FIG. 2 is a sectional view. 1... Sieve drum, 2... Sludge supply pipe, 3... Roller, 4... Coagulation mixing tank, 5...
...Blade, 6...Water pipe, 7...Blade, 8
...Water collection chute, 9...Washing nozzle.
Claims (1)
めたシーブドラムを前後二段に分け、この前段内に攪拌
羽根を具備した凝集混和槽を配して、この凝集混和槽の
前部より汚泥を供給し、その後部より汚泥をシーブドラ
ム後段に排出するよう構成すると共に、前記凝集混和槽
とシーブドラム前段との間に処理水を供給してシーブド
ラム前段にてこれを濾過するように構成したことを特徴
とする汚泥処理用シーブドラム。1 A sheave drum rotatably supported opposite the outer circumferential surface cleaning nozzle is divided into two stages, front and rear, and a flocculation mixing tank equipped with stirring blades is arranged in the front stage, and from the front part of this coagulation mixing tank, The sludge is supplied and the sludge is discharged from the rear of the sieve drum to the rear stage of the sieve drum, and the treated water is supplied between the coagulation mixing tank and the front stage of the sieve drum and is filtered at the front stage of the sieve drum. A sieve drum for sludge treatment featuring:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58183291A JPS6045924B2 (en) | 1983-09-30 | 1983-09-30 | Sheep drum for sludge treatment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58183291A JPS6045924B2 (en) | 1983-09-30 | 1983-09-30 | Sheep drum for sludge treatment |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP55123781A Division JPS6089B2 (en) | 1980-09-05 | 1980-09-05 | Sludge dewatering treatment method and its equipment |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60138740A Division JPS6121711A (en) | 1985-06-24 | 1985-06-24 | Sieve drum for sludge treatment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5987012A JPS5987012A (en) | 1984-05-19 |
JPS6045924B2 true JPS6045924B2 (en) | 1985-10-12 |
Family
ID=16133083
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58183291A Expired JPS6045924B2 (en) | 1983-09-30 | 1983-09-30 | Sheep drum for sludge treatment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6045924B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP6141589B2 (en) * | 2011-09-27 | 2017-06-07 | 株式会社タクマ | Rotating drum type concentration system |
-
1983
- 1983-09-30 JP JP58183291A patent/JPS6045924B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5987012A (en) | 1984-05-19 |
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