JPS632641B2 - - Google Patents
Info
- Publication number
- JPS632641B2 JPS632641B2 JP60138740A JP13874085A JPS632641B2 JP S632641 B2 JPS632641 B2 JP S632641B2 JP 60138740 A JP60138740 A JP 60138740A JP 13874085 A JP13874085 A JP 13874085A JP S632641 B2 JPS632641 B2 JP S632641B2
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- sieve drum
- water
- supplied
- 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.)
- Expired
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 44
- 239000010802 sludge Substances 0.000 claims description 29
- 238000003756 stirring Methods 0.000 claims description 2
- 238000005406 washing Methods 0.000 description 6
- 230000003311 flocculating effect Effects 0.000 description 5
- 238000005189 flocculation Methods 0.000 description 5
- 230000016615 flocculation Effects 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 239000010865 sewage Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 230000015271 coagulation Effects 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 239000010782 bulky waste Substances 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
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。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
脱水機で排出された排水を沈殿槽へ一旦導びき、
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。しかしこの方法では汚泥が
凝集剤で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である。 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. However, this dewatering method involves adding a flocculant to the collected sludge with a high water content, feeding it into a coagulation mixing tank, then feeding it to a belt press type dehydrator, performing the desired dehydration, and then dewatering the sludge. The cake is sent to the next process, and the wastewater discharged from the dehydrator is once led to the settling tank.
The supernatant water with precipitated sludge particles is used as washing water for the dehydrator. However, in this method, the sludge is flocculated with a flocculant and then directly supplied to the dehydrator together with the dehydrated water for dewatering, resulting in poor dewatering efficiency and poor reuse efficiency of the desorbed water as washing water.
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
処理用シーブド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。 In view of this, the present invention proposes a sieve drum for sludge treatment that improves dewatering efficiency while efficiently reusing desorbed water. Next, the present invention will be explained in detail with reference to the illustrated embodiment. .
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、該シーブドラム内
には適当な移送手段で汚泥供給管2を経て供給さ
れるが、この回収された汚泥中の粗大ごみ等を予
じめ除去し、且これに貯液されている凝集液タン
クより凝集液を供給され、スタテイツクミキサー
等で予め汚泥と凝集液とは混合される。この汚泥
処理用シーブドラム1は図面に詳示する如く横方
向にしてこれをコロ3等にてうけて回動自在に支
持すると共にその内部を前段1Aと後段1Bとに
分け、そしてこのシーブドラム前段内に凝集混和
槽4を設ける。そしてこの凝集混和槽内には撹拌
用の羽根5が設けられ、予め凝集剤と混合された
汚泥もしくは汚泥と凝集剤とをともに汚泥供給管
2より該槽4内へ供給され、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にて所望の混合撹拌が行なわれるよう
になす。またこの凝集混和槽4の外周部には処理
水例えば脱水機からの脱離水等を給水管6と処理
水受部1cを介して供給し、シーブドラム前後部
外周にて過される。 In the figure, 1 is the main body of a sieve drum for processing sludge collected from sewage treatment plants, etc. The sludge is supplied into the sieve drum through a sludge supply pipe 2 using an appropriate transfer means. Bulky waste and the like are removed in advance, and a flocculating liquid is supplied from a flocculating liquid tank stored in the tank, and the sludge and flocculating liquid are mixed in advance with a static mixer or the like. As shown in detail in the drawing, this sieve drum 1 for sludge treatment is oriented horizontally and supported rotatably by rollers 3 etc., and its interior is divided into a front stage 1A and a rear stage 1B. A flocculation mixing tank 4 is provided. A stirring blade 5 is provided in this flocculation mixing tank, and sludge mixed with a flocculant in advance or both sludge and flocculant are supplied into the tank 4 from the sludge supply pipe 2, and when the sieve drum rotates. The aggregation 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 dehydrated water from a dehydrator, is supplied to the outer circumference of the flocculation mixing tank 4 via the water supply pipe 6 and the treated water receiving portion 1c, and is passed around the front and rear outer circumferences of the sheave drum.
この処理水受部1cは前段1Aの汚泥供給側に
取付けられ、給水管6から処理水を受け、その処
理水を凝集混和濃縮槽4へ供給するようになす。
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
されここでさらに混合撹拌さ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、脱離水はシーブドラム前後段よ
りシーブドラム下方に設けた集水シユート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。 This treated water receiving section 1c is attached to the sludge supply side of the front stage 1A, receives treated water from the water supply pipe 6, and supplies the treated water to the coagulation-mixing concentration tank 4.
Further, a blade 7 is provided in the rear end of the sheave drum,
The sludge sufficiently mixed with the flocculant is supplied to the front stage, where it is further mixed and stirred and primary dewatering is performed. The sludge after dewatering is sequentially discharged from the opening end of the sieve drum, and the desorbed water falls from the front and rear stages of the sieve drum into a water collection chute 8 provided below the sieve drum and is discharged. sheave drum 1
The outer circumferential surface of the sheave drum is washed with washing water jetted from a washing nozzle 9 arranged above the sheave drum.
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る。 The sludge collected from sewage treatment plants, etc. is mixed with flocculating liquid in advance 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 treated water is supplied from desorbed water and other sources.
処理水は一旦処理水受部で受けたのち、シーブ
ドラム内に供給されて十分に過される。処理
水、主に汚泥の脱離水には凝集剤と汚泥のフロツ
クが多数存在する。しかしながらそのフロツクの
結合力は弱いので、直接シーブドラムに処理水を
供給するとフロツクがこわれてシーブドラムを通
過してしまう。処理水受部は処理水の流水を調整
してシーブドラム面に横方向から処理水を供給す
る。 After the treated water is once received in the treated water receiving section, it is supplied into the sieve drum and thoroughly filtered. A large number of flocculants and sludge flocs are present in treated water, mainly sludge desorbed water. However, the binding force of the flocs is weak, so if treated water is supplied directly to the sieve drum, the flocs will break and pass through the sieve drum. The treated water receiving section adjusts the flow of treated water and supplies the treated water to the sieve drum surface from the side.
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ドラムにて過され除去され
脱離水はシーブドラムより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。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
してポンプにてシーブドラム洗浄用ノズルや脱水
機の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樋内へ直
接供給することもある。 The sludge is coagulated in the rotating tank 4, and the solids in the waste water are filtered and removed by the sieve drum, and the desorbed water is drained from the sieve drum to separate the solids and water, and the sieve drum is cleared from clogging. Cleaning water is sprayed from the cleaning nozzle from above the outer periphery to prevent this. The solid content of the sludge separated in this sieve drum is sent to the next process, a dehydrator.
The water is further dehydrated to the desired moisture content and sent to the next process as a dehydrated cake for treatment.The dehydrated water separated from the sieve drum is temporarily stored in a tank and pumped to the sieve drum cleaning nozzle and dehydrator. It is supplied to the fabric washing nozzle and used as washing 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 into a gutter provided in the sieve drum.
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撹拌が
充分に行なわれて凝集されと共に談槽の外周部に
設けたシーブドラムに処理水受部を介して供給さ
れる処理水は十分に過処理され、上記二系流の
処理が同時に一括処理され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。 According to the present invention, the sieve drum is divided into front and rear parts, and a flocculating mixing tank is provided in the front part, so that the flocculant is mixed with the sludge and supplied, and the sludge is sufficiently mixed and stirred in this tank, flocculated, and then mixed. The treated water supplied through the treated water receiving part to the sieve drum provided on the outer periphery of the tank is sufficiently overtreated, the two streams mentioned above are simultaneously treated in one batch, and the sieve drum has a simple structure. It has advantages such as being able to be provided at low cost.
第1図は外面図、第2図は断面図である。
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……集水シユート、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 supply pipe, 7... impeller, 8... water collection chute, 9...
...Cleaning nozzle.
Claims (1)
備した凝集混和槽と、該凝集混和槽の外周部に汚
泥の脱離水等の処理水を過する回動自在のシー
ブドラムと、該シーブドラムに隣接して外部から
供給される前記処理水を受けたのち前記シーブド
ラムに供給するようになした処理水受部とを一体
に設けたことを特徴とする汚泥処理用シーブドラ
ム。1. A coagulation-mixing tank equipped with stirring blades on the inner circumferential surface for mixing supplied sludge, a rotatable sieve drum for passing treated water such as desorbed water of sludge on the outer periphery of the coagulation-mixing tank, and A sieve drum for sludge treatment, characterized in that it is integrally provided with a treated water receiving section adjacent thereto which receives the treated water supplied from the outside and then supplies it to the sieve drum.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60138740A JPS6121711A (en) | 1985-06-24 | 1985-06-24 | Sieve drum for sludge treatment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60138740A JPS6121711A (en) | 1985-06-24 | 1985-06-24 | Sieve drum for sludge treatment |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58183291A Division JPS6045924B2 (en) | 1983-09-30 | 1983-09-30 | Sheep drum for sludge treatment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6121711A JPS6121711A (en) | 1986-01-30 |
JPS632641B2 true JPS632641B2 (en) | 1988-01-20 |
Family
ID=15229064
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60138740A Granted JPS6121711A (en) | 1985-06-24 | 1985-06-24 | Sieve drum for sludge treatment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6121711A (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5372717B2 (en) * | 2009-11-26 | 2013-12-18 | 三機工業株式会社 | Coagulation stirring tank, sludge treatment system, and method of operating sludge treatment system |
CN101966406A (en) * | 2010-09-27 | 2011-02-09 | 中国水产科学研究院渔业机械仪器研究所 | Filtering equipment for purifying aquacultural water |
JP6183622B2 (en) * | 2015-01-07 | 2017-08-23 | 株式会社石垣 | Solid recovery system for drum type concentrator |
-
1985
- 1985-06-24 JP JP60138740A patent/JPS6121711A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS6121711A (en) | 1986-01-30 |
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