JPS6089B2 - Sludge dewatering treatment method and its equipment - Google Patents
Sludge dewatering treatment method and its equipmentInfo
- Publication number
- JPS6089B2 JPS6089B2 JP55123781A JP12378180A JPS6089B2 JP S6089 B2 JPS6089 B2 JP S6089B2 JP 55123781 A JP55123781 A JP 55123781A JP 12378180 A JP12378180 A JP 12378180A JP S6089 B2 JPS6089 B2 JP S6089B2
- Authority
- JP
- Japan
- Prior art keywords
- sieve drum
- sludge
- dehydrator
- water
- supplied
- 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
- 239000010802 sludge Substances 0.000 title claims description 35
- 238000000034 method Methods 0.000 title claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 37
- 238000004140 cleaning Methods 0.000 claims description 23
- 239000004744 fabric Substances 0.000 claims description 13
- 239000007788 liquid Substances 0.000 claims description 11
- 230000003311 flocculating effect Effects 0.000 claims description 8
- 239000007787 solid Substances 0.000 claims description 8
- 238000005406 washing Methods 0.000 claims description 8
- 239000002351 wastewater Substances 0.000 claims description 8
- 230000008719 thickening Effects 0.000 claims description 4
- 230000015271 coagulation Effects 0.000 claims description 3
- 238000005345 coagulation Methods 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims 1
- 238000005189 flocculation Methods 0.000 description 4
- 230000016615 flocculation Effects 0.000 description 4
- 239000010865 sewage Substances 0.000 description 4
- 230000003068 static effect Effects 0.000 description 4
- 230000001112 coagulating effect Effects 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000010782 bulky waste Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 235000014366 other mixer Nutrition 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
- Filtration Of Liquid (AREA)
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法及
びその装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus 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第4図に示す如く回収された高舎水
率の汚泥を汚泥貯留槽1より汚泥輸送管にて輸送する途
中で凝集液タンク8から適量の凝集剤を添加した後、凝
集混和濃縮槽6へ投入し、次にベルトプレス式の脱水機
12へ供給し、所望の脱水を行なった後、脱水ケーキと
して次の工程へ送出すると共に脱水機12で排出された
排水を沈殿槽24へ一旦導びき、汚泥粒子を沈殿せしめ
た上燈水を脱水機12の洗浄ノル18,19へ供給して
洗浄水として使用している。However, as shown in Fig. 4, this dewatering method involves adding an appropriate amount of flocculant from the flocculant tank 8 while transporting the collected sludge with a high water content from the sludge storage tank 1 through the sludge transport pipe, and then flocculating it. It is fed into the mixing concentration tank 6, then supplied to the belt press type dehydrator 12, and after the desired dehydration is performed, it is sent to the next process as a dehydrated cake, and the wastewater discharged from the dehydrator 12 is sent to the settling tank. 24, and the sludge particles are precipitated therein, and the top water is supplied to the washing nozzles 18 and 19 of the dehydrator 12 and used as washing water.
しかしこの方法では汚泥が凝集剤で凝集した後直接分離
水とともに脱水機へ供給し、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。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んとしてなされたもので、次
に図示の実施例について本発明を詳細に説明する。However, in this method, the sludge is flocculated with a coagulant and then directly supplied to the dehydrator together with the separated water for dewatering, resulting in poor dewatering efficiency and poor reuse efficiency of the desorbed water as washing water. In view of this, the present invention has been devised to improve dewatering efficiency while efficiently reusing desorbed water. Next, the present invention will be described in detail with reference to the illustrated embodiments.
図に於て1は下水処理場等より回収された汚泥を貯留せ
しめる汚泥貯留槽で、該糟内には適当な移送手段で回収
された高含水率の汚泥を移送する。In the figure, reference numeral 1 denotes a sludge storage tank for storing sludge collected from a sewage treatment plant, etc., into which sludge with a high water content is transferred using an appropriate transfer means.
2はこの汚泥貯留槽1より汚泥輸送管3を経て供給され
、且粗大ごみを予じめ除去するためのストレ−ナで、こ
のストレーナ2より汚泥ポンプ4、スタティックミキサ
ー5を介して凝集混和濃縮槽6へ汚泥を供給すると共に
このスタティックミキサー5に凝集剤溶解タンク7より
溶解された凝集薬剤の供給をうけ、貯液されている凝集
液タンク8より凝集液を凝集液供給管10より供給され
、このスタティックミキサー5内で汚泥とこの凝集液と
を混合せしめる。Reference numeral 2 denotes a strainer which is supplied from the sludge storage tank 1 through the sludge transport pipe 3 and which removes bulky waste in advance. While supplying sludge to the tank 6, the static mixer 5 is supplied with the dissolved flocculant from the flocculant dissolving tank 7, and the flocculant is supplied from the flocculating liquid tank 8 stored therein through the flocculating liquid supply pipe 10. In this static mixer 5, the sludge and this flocculated liquid are mixed.
また凝集液はスタティックミキサー又はその他のミキサ
ーを経て汚泥輸送管内へも注入できるように凝集液供給
管9が設けられると共に之等の凝集液供給管9,10及
び汚泥輸送管11の管路中に流量計12a,12b,1
2cが設けられ汚泥量に対し可調整的に所要の割合で凝
集液が注入混合されるものである。In addition, a flocculating liquid supply pipe 9 is provided so that the flocculating liquid can also be injected into the sludge transport pipe through a static mixer or other mixer. Flowmeter 12a, 12b, 1
2c is provided, and the flocculating liquid is injected and mixed in an adjustable required ratio with respect to the amount of sludge.
凝集混和濃縮槽6は横型にして回動自在に支持されたシ
ーブドラム22内に設けられ、該糟6及びシーブドラム
内で凝集した汚泥と遊離水を炉遇して分離せしめ凝集し
た汚泥を次工程のベルトプレス式の脱水機12へ供給す
るか遊離水はシーブドラムにて炉過された後凝集混和濃
縮槽の下部に設けられたタンク13へ導びかれる。この
時シーブドラム22の上部に設けられ該シーブドラムを
洗浄するためのシーブドラム用洗浄ノズル14より噴出
せしめられた洗浄水とともにタンク13へ導びかれる。
ベルトプレス式の脱水機12の下部には脱離水を受ける
シュート23を設け、シュート内へ集水される脱離水を
ポンプ16にて洗浄水管17を経てシーブドラム22内
へ供給される。またタンク13の洗浄水はポンプPを経
てその一部を脱水機の炉布洗浄ノズル18,19へ供給
するもので、このタンク13には補給水管20と排水管
21とを受けるものである。而して下水処理場等より回
収された汚泥は凝集液と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
内には脱水機よりの脱離水の供給をうけ、汚泥は回転す
る該凝集混和濃縮槽6内で凝固されまた排水中の固形物
はシーブドラムにて炉過され除去され遊離水はシーブド
ラムより炉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を防止するため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いる。The flocculation-mixing concentration tank 6 is installed in a horizontally rotatably supported sieve drum 22, and the sludge and free water flocculated in the sieve drum and the flocculation tank 6 are separated by a furnace, and the flocculated sludge is sent to the next process. The free water is supplied to a belt press type dehydrator 12 or filtered in a sieve drum, and then led to a tank 13 provided at the lower part of the coagulation-mixing thickening tank. At this time, the cleaning water is led to the tank 13 together with the cleaning water jetted out from the sheave drum cleaning nozzle 14 provided on the upper part of the sheave drum 22 for cleaning the sheave drum.
A chute 23 for receiving desorbed water is provided at the lower part of the belt press type dehydrator 12, and the desorbed water collected in the chute is supplied into the sheave drum 22 through a washing water pipe 17 by a pump 16. A portion of the cleaning water in the tank 13 is supplied to the cloth cleaning nozzles 18 and 19 of the dehydrator through a pump P, and this tank 13 receives a makeup water pipe 20 and a drain pipe 21. The sludge collected from sewage treatment plants, etc. is mixed with flocculation liquid and supplied to the flocculation mixing tank installed in the sieve drum.The sieve drum is also supplied with desorbed water from the dehydrator, and the sludge is is coagulated in the rotating coagulation-mixing concentration tank 6, solids in the waste water are filtered and removed in a sieve drum, and free water is drained from the sieve drum to separate the solids and water. To prevent clogging, cleaning water is sprayed from a cleaning nozzle above the outer periphery of the sheave drum.
このシーブドラムで分離された汚泥の固形分は脱水機1
2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るが、シーブドラムより分
離された遊離水はタンクにて一時貯水してポンプにてシ
ーブドラム用洗浄ノズルと脱水機の炉布洗浄ノズルへ供
給して洗浄水として利用し、また脱水機にて脱水された
脱離水はポンプにてシーブドラム内へ供給し、このよう
にして遊離水脱離水を再使用しつつ汚泥の脱水処理を連
続的に行うものである。また脱水機よりの排水はシーブ
ドラム内に設けられた投入シュート15内へ供給するこ
ともある。本発明による時は脱水機の炉布洗浄に必要な
多量の洗浄水を系統外に求めることなく得られると同時
に炉布洗浄によって排水中に混入した固形物を系統内の
他の機器であるシーブドラムによって処理できるので新
たな設備を設けることなく炉布洗浄排水(固形物を含む
)を系統外へ流すことを防止でき、しかも炉布洗浄水の
再利用が図れ、その結果、外部から何んらの水の供給を
受けなくても、しかも新たな設備を付加することないこ
脱水機の炉布洗浄が可能となり新たな設備の付加がない
ので設備のコンパクト化が図れ、しかも装置が簡単で、
汚泥の脱水が連続的にして所望の含水率まで確実に行え
る等の利点を有する。The solid content of the sludge separated by this sieve drum is removed by the dehydrator 1.
The free water separated from the sieve drum is temporarily stored in a tank and sent to the sieve drum cleaning nozzle and dewatering machine using a pump. The water is supplied to the furnace cloth cleaning nozzle and used as cleaning water, and the dehydrated water dehydrated by the dehydrator is supplied to the sieve drum by a pump. In this way, the dehydrated water is reused and the sludge is removed. The dehydration process is performed continuously. Further, the waste water from the dewatering machine may be supplied to an input chute 15 provided in the sieve drum. According to the present invention, a large amount of washing water required for cleaning the furnace cloth of the dehydrator can be obtained without requiring outside the system, and at the same time, solids mixed in the waste water by cleaning the furnace cloth can be removed from the sieve drum, which is another equipment in the system. Since the furnace cloth cleaning wastewater (containing solids) can be treated by the system, it is possible to prevent the furnace cloth cleaning wastewater (including solids) from flowing outside the system without installing new equipment.Furthermore, the furnace cloth cleaning water can be reused, and as a result, there is no need to install any new equipment from the outside. This makes it possible to clean the furnace cloth of the dehydrator without having to receive a water supply and without adding new equipment.As there is no need to add new equipment, the equipment can be made more compact, and the equipment is simple.
It has the advantage that sludge can be continuously dehydrated to a desired moisture content.
第1図は本発明の概略説明図、第2図は凝集混和槽の外
面図、第3図は第2図の断面図、第4図は公知のフロー
説明図である。
1・・・汚泥貯留槽、2・・・ストレーナ、3・・・汚
泥輸送管、4・・・汚泥ポンプ、5・・・スタティック
ミキサー、6・・・凝集混和濃縮槽、7・・・凝集剤溶
解タンク、8…凝集液タンク、9,10・・・凝集液供
給管、11・・・汚泥輸送管、12・・・脱水機、12
a,12b,12c…流量計、13・・・タンク、14
・・・シーブドラム用洗浄ノズル、15・・・投入シュ
−ト、16・・・ポンプ、17・・・洗浄水管、18,
19・・・源布洗浄ノズル、20・・・補給水管、21
・・・排水管、22…シーブドラム、23…シュート。
第1図第2図
第3図
第4図FIG. 1 is a schematic explanatory diagram of the present invention, FIG. 2 is an external view of a flocculation mixing tank, FIG. 3 is a cross-sectional view of FIG. 2, and FIG. 4 is an explanatory diagram of a known flow. 1... Sludge storage tank, 2... Strainer, 3... Sludge transport pipe, 4... Sludge pump, 5... Static mixer, 6... Coagulation mixing thickening tank, 7... Coagulation agent dissolution tank, 8... coagulating liquid tank, 9, 10... coagulating liquid supply pipe, 11... sludge transport pipe, 12... dehydrator, 12
a, 12b, 12c...flow meter, 13...tank, 14
...Washing nozzle for sheave drum, 15...Input chute, 16...Pump, 17...Washing water pipe, 18,
19... Source cloth cleaning nozzle, 20... Supply water pipe, 21
...Drain pipe, 22...Sheave drum, 23...Chute. Figure 1 Figure 2 Figure 3 Figure 4
Claims (1)
内に備えた凝集混和濃縮槽へ供給し、上記シーブドラム
で分離水を除去した後、凝集汚泥を脱水機へ供給し、所
望の脱水を行うと共に脱水機よりの脱離水と脱水機の濾
布洗浄排水を上記シーブドラム内へ供給し、固形物を分
離し、この分離固形物を凝集汚泥に合流させ、上記シー
ブドラムより排出される濾過分離水をポンプにて脱水機
の濾布洗浄ノズルとシーブドラム用洗浄ノズルへ圧送し
、洗浄用水として使用するようになしたことを特徴とす
る汚泥の脱水処理法。 2 シーブドラムを横型に配置し、このシーブドラム内
に汚泥に凝集液を混入せしめて供給される凝集混和濃縮
槽を設け、このシーブドラムに隣接して、該シーブドラ
ムによって排出された凝集汚泥を脱水するベルトプレス
式脱水機を設けると共に、前記シーブドラムよりの脱離
水を供給されるようにしてシーブドラム用洗浄ノズル及
び前記脱水機に濾布洗浄ノズルを設け、さらに脱水機よ
りの脱離水と濾布洗浄用排水をシーブドラム内へ供給で
きるように管路を設けてなる汚泥の脱水処理装置。[Scope of Claims] 1. Mixing flocculating liquid with sludge in a required ratio and supplying the mixture to a flocculation-mixing thickening tank provided in a sieve drum, removing separated water in the sieve drum, and then supplying the flocculated sludge to a dehydrator. , At the same time as performing the desired dewatering, the dewatered water from the dehydrator and the filter cloth washing wastewater from the dehydrator are supplied into the above sieve drum, solids are separated, the separated solids are combined with the flocculated sludge, and then discharged from the sieve drum. A method for dewatering sludge, characterized in that the filtered and separated water is pumped to a filter cloth cleaning nozzle and a sieve drum cleaning nozzle of a dehydrator to be used as cleaning water. 2. A sieve drum is arranged horizontally, and a coagulation mixing thickening tank is provided in the sieve drum to which the sludge is mixed with a flocculating liquid, and a belt press is installed adjacent to the sieve drum to dewater the flocculated sludge discharged by the sieve drum. A type dehydrator is provided, and a cleaning nozzle for the sieve drum and a filter cloth cleaning nozzle are provided in the dehydrator so as to be supplied with dehydrated water from the dehydrator, and dehydrated water from the dehydrator and wastewater for cleaning the filter cloth are provided. A sludge dewatering device that has a pipe line so that it can be supplied into the sieve drum.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55123781A JPS6089B2 (en) | 1980-09-05 | 1980-09-05 | Sludge dewatering treatment method and its equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55123781A 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 |
|---|---|---|---|
| JP58183291A Division JPS6045924B2 (en) | 1983-09-30 | 1983-09-30 | Sheep drum for sludge treatment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5748315A JPS5748315A (en) | 1982-03-19 |
| JPS6089B2 true JPS6089B2 (en) | 1985-01-05 |
Family
ID=14869124
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55123781A Expired JPS6089B2 (en) | 1980-09-05 | 1980-09-05 | Sludge dewatering treatment method and its equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6089B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1984001313A1 (en) * | 1982-09-29 | 1984-04-12 | Ilecard Pty Ltd | Recovery of solids from dispersions |
| EP1870149A4 (en) * | 2005-04-13 | 2009-01-28 | Hitachi Ltd | DEVICE FOR WATER FILTRATION / CLEANING AND METHOD THEREFOR |
| CN114855905A (en) * | 2022-04-20 | 2022-08-05 | 隆生国际建设集团有限公司 | Urban river ecological dredging system and construction process |
-
1980
- 1980-09-05 JP JP55123781A patent/JPS6089B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5748315A (en) | 1982-03-19 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US20050205496A1 (en) | Process and apparatus for treating liquid waste material | |
| CN110255848B (en) | Sludge dewatering system | |
| KR100292225B1 (en) | Method and apparatus of reusing for dirty and waste water including excretion | |
| JPS6089B2 (en) | Sludge dewatering treatment method and its equipment | |
| KR101938024B1 (en) | Sludge-concentrating method and apparatus | |
| CN109516608A (en) | Coking wastewater advanced treatment process and system | |
| JPH1034196A (en) | Mobile sludge dewatering vehicle | |
| JP5481654B2 (en) | Sludge treatment method and treatment system | |
| JP4129479B1 (en) | Sludge treatment method and treatment system | |
| KR200409043Y1 (en) | Sludge Treatment System with Concentration and Dewatering Line | |
| JP2001070997A (en) | Treatment method of filtrate and washing wastewater in sludge dewatering machine | |
| JPS6121711A (en) | Sieve drum for sludge treatment | |
| JP2000246296A (en) | Sludge thickening system | |
| JP2004243185A (en) | Solid-liquid separation treatment method and apparatus therefor | |
| JPS6045924B2 (en) | Sheep drum for sludge treatment | |
| JPS6089309A (en) | Waste water treating method in ready mixed concrete plant | |
| JP2003251114A (en) | Solid-liquid separation device | |
| KR200264109Y1 (en) | A car for dehydrating sludge | |
| JP2677459B2 (en) | Organic wastewater treatment method | |
| JP2005324076A (en) | Sludge dehydrator and sludge flocculating/concentrating tank | |
| JP2004122096A (en) | Method and apparatus for dehydrating sludge | |
| KR970006189A (en) | Fixed algae removal method and apparatus | |
| JPH0783864B2 (en) | Fly ash processing equipment | |
| JPH1024201A (en) | Solid-liquid separator for waste water of ready-mixed concrete | |
| KR0117923Y1 (en) | Wastewater Treatment System of Automatic Car Wash |