JP5187540B2 - Sludge concentrator and cleaning method therefor - Google Patents

Sludge concentrator and cleaning method therefor Download PDF

Info

Publication number
JP5187540B2
JP5187540B2 JP2011224047A JP2011224047A JP5187540B2 JP 5187540 B2 JP5187540 B2 JP 5187540B2 JP 2011224047 A JP2011224047 A JP 2011224047A JP 2011224047 A JP2011224047 A JP 2011224047A JP 5187540 B2 JP5187540 B2 JP 5187540B2
Authority
JP
Japan
Prior art keywords
sludge
filtration
cylinder
filter cylinder
cleaning
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 - Fee Related
Application number
JP2011224047A
Other languages
Japanese (ja)
Other versions
JP2012006016A (en
Inventor
忠雄 竹内
克也 丸山
英樹 田中
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP2011224047A priority Critical patent/JP5187540B2/en
Publication of JP2012006016A publication Critical patent/JP2012006016A/en
Application granted granted Critical
Publication of JP5187540B2 publication Critical patent/JP5187540B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Treatment Of Sludge (AREA)
  • Filtration Of Liquid (AREA)

Description

本発明は、濾過筒内でスパイラルスクリューを回転駆動することによって、汚泥凝集槽から濾過筒内に導入される汚泥を搬送しながらこれを濃縮するスクリュープレス型の汚泥濃縮装置及びこれの洗浄方法に関するものである。   TECHNICAL FIELD The present invention relates to a screw press type sludge concentrating device and a cleaning method therefor that concentrates a sludge introduced from a sludge agglomeration tank into a filter cylinder by rotationally driving a spiral screw in the filter cylinder. Is.

各種汚泥を廃棄又は焼却するため、汚泥を脱水機にて脱水処理することが行われるが、脱水機に供給される汚泥は、その濃度が高い程、効率的に脱水処理することができる。このため、汚泥の脱水機による脱水処理に先立って、汚泥を凝集剤で凝集させ、この凝集された汚泥(凝集汚泥)から水分を分離して汚泥を脱水処理に適した濃度まで濃縮することが行われ、これを実施するための汚泥濃縮装置が種々提案されて実用に供されている。   In order to discard or incinerate various types of sludge, the sludge is dehydrated with a dehydrator. The higher the concentration of the sludge supplied to the dehydrator, the more efficiently the dehydration can be performed. Therefore, prior to the sludge dewatering process, the sludge is aggregated with a flocculant, and moisture is separated from the aggregated sludge (aggregated sludge) to concentrate the sludge to a concentration suitable for the dewatering process. Various sludge concentrators have been proposed and put into practical use.

このような汚泥濃縮装置として、本出願人が先に提案したスクリュープレス型の汚泥濃縮装置の一例を図3に示す(例えば、特許文献1参照)。   As such a sludge concentrating device, an example of a screw press type sludge concentrating device previously proposed by the present applicant is shown in FIG. 3 (see, for example, Patent Document 1).

即ち、図3は従来の汚泥濃縮装置1’の基本構成を示す概略図であり、図示の汚泥濃縮装置1’は、上面が開口する円筒タンク状の汚泥凝集槽2と、汚泥を濃縮する固液分離手段3及び分離液を収容する分離液槽4を含んで構成されている。   That is, FIG. 3 is a schematic diagram showing the basic configuration of a conventional sludge concentrating device 1 ′. The sludge concentrating device 1 ′ shown in FIG. 3 includes a cylindrical tank-shaped sludge aggregating tank 2 having an open top surface and a solid sludge condensing tank. The liquid separation means 3 and a separation liquid tank 4 that contains the separation liquid are included.

上記汚泥凝集槽2の底部には汚泥供給管5が接続されており、汚泥凝集槽2の内部には、モータM1によって回転駆動される撹拌機6が収容されている。   A sludge supply pipe 5 is connected to the bottom of the sludge agglomeration tank 2, and a stirrer 6 that is rotationally driven by a motor M <b> 1 is accommodated in the sludge agglomeration tank 2.

前記固液分離手段3は、密閉構造を有する円筒タンク状の外筒7の内部に円筒状の濾過筒8を縦方向に配置し、該濾過筒8内にスパイラルスクリュー9を回転可能に収容して構成されている。   The solid-liquid separation means 3 has a cylindrical filter tube 8 disposed in a vertical direction inside a cylindrical tank-shaped outer tube 7 having a sealed structure, and a spiral screw 9 is rotatably accommodated in the filter tube 8. Configured.

ここで、上記濾過筒8の前記外筒7内に臨む部位の周面は、パンチングプレート又はウェッジワイヤー等から成る濾過面8aを構成しており、濾過筒8の下部側方には、前記汚泥凝集槽2の上部側方から導出する凝集汚泥導入管10が接続されている。又、濾過筒8の上部側方からは濃縮汚泥排出管11が導出している。   Here, the peripheral surface of the portion of the filtration cylinder 8 facing the outer cylinder 7 constitutes a filtration surface 8a made of a punching plate, a wedge wire, or the like. An agglomerated sludge introduction pipe 10 led out from the upper side of the agglomeration tank 2 is connected. A concentrated sludge discharge pipe 11 is led out from the upper side of the filter cylinder 8.

又、前記スパイラルスクリュー9は、駆動源としてのモータM2によって回転駆動されるものであって、その外径は濾過筒8の濾過面8aの内径よりも僅かに小さく設定されており、該スパイラルスクリュー9の外周縁と濾過筒8の濾過面8aとの間には微小隙間が形成されている。   The spiral screw 9 is rotationally driven by a motor M2 as a drive source, and the outer diameter thereof is set to be slightly smaller than the inner diameter of the filtration surface 8a of the filter cylinder 8, and the spiral screw 9 A minute gap is formed between the outer peripheral edge of 9 and the filtration surface 8 a of the filtration cylinder 8.

更に、前記分離液槽4は、上下2本の接続管12によって外筒7の上下側部に接続されており、その上部側方からは分離液排出管13が導出している。   Further, the separation liquid tank 4 is connected to the upper and lower side portions of the outer cylinder 7 by two upper and lower connecting pipes 12, and a separation liquid discharge pipe 13 is led out from the upper side.

以上の構成を有する汚泥濃縮装置1’においては、前記汚泥供給管5から汚泥凝集槽2に汚泥(原泥)が供給されるが、それ以前に汚泥には凝集剤が添加される。ここで、凝集剤としては、汚泥の凝集・脱水処理に供されるものであれば任意のものを使用することができ、硫酸アルミニウム、ポリ塩化アルミニウム、塩化第二鉄、硫酸第一鉄、ポリ鉄(ポリ硫酸第二鉄)等の無機凝集剤、カチオン性、アニオン性、ノニオン性高分子凝集剤、両性高分子凝集剤等を用いることができ、或は無機凝集剤と高分子凝集剤を併用することもできる。   In the sludge concentrator 1 ′ having the above configuration, sludge (raw mud) is supplied from the sludge supply pipe 5 to the sludge agglomeration tank 2, but before that, a flocculant is added to the sludge. Here, as the flocculant, any one can be used as long as it is used for sludge flocculation / dehydration treatment. Aluminum sulfate, polyaluminum chloride, ferric chloride, ferrous sulfate, poly Inorganic flocculants such as iron (polyferric sulfate), cationic, anionic, nonionic polymer flocculants, amphoteric polymer flocculants can be used, or inorganic flocculants and polymer flocculants can be used. It can also be used together.

而して、凝集剤が添加された汚泥が汚泥凝集槽2内に供給されると、該汚泥凝集槽2内においては、モータM1によって回転駆動される攪拌機6によって汚泥と凝集剤が撹拌され、汚泥は、これに含まれる固形成分が凝集されて凝集汚泥となる。そして、この凝集汚泥は、凝集汚泥導入管10から濾過筒8内にその下部から導入される。   Thus, when the sludge to which the flocculant has been added is supplied into the sludge aggregation tank 2, the sludge and the flocculant are agitated in the sludge aggregation tank 2 by the agitator 6 that is driven to rotate by the motor M1, The sludge is agglomerated sludge by aggregating solid components contained therein. The agglomerated sludge is introduced from the agglomerated sludge introduction pipe 10 into the filter cylinder 8 from below.

固液分離手段3においては、前記スパイラルスクリュー9は、モータM2によって濾過筒8内で所定の速度で回転駆動されており、濾過筒8内に導入された凝縮汚泥は、回転するスパイラルスクリュー9によって上方へと搬送されるとともに、これに含まれる水分が濾過筒8の濾過面8aを通過して外筒7内に分離液として排出され、この分離液は上下2本の接続管12から分離液槽4へと送られて収容される。尚、濾過筒8内の液位は外筒7内の液位よりも僅かに高く設定されており、両液位の差(ヘッド差)に基づく差圧を濾過圧として汚泥から分離された水分が分離液として濾過筒8の濾過面8aを通過して汚泥の濃縮が安定的に行われる。   In the solid-liquid separation means 3, the spiral screw 9 is driven to rotate at a predetermined speed in the filter cylinder 8 by the motor M 2, and the condensed sludge introduced into the filter cylinder 8 is rotated by the rotating spiral screw 9. While being conveyed upward, the water contained therein passes through the filtration surface 8a of the filtration cylinder 8 and is discharged as a separation liquid into the outer cylinder 7, and this separation liquid is separated from the upper and lower connecting pipes 12 into the separation liquid. It is sent to the tank 4 and accommodated. The liquid level in the filter cylinder 8 is set slightly higher than the liquid level in the outer cylinder 7, and the water separated from the sludge using the differential pressure based on the difference between the two liquid levels (head difference) as the filtration pressure. However, the sludge is stably concentrated through the filtration surface 8a of the filter cylinder 8 as a separation liquid.

そして、分離液槽4内に収容された分離液は、分離液排出管13を通って外部へと排出される。又、スパイラルスクリュー9の回転によって濾過筒8内を上方へと搬送される凝集汚泥は、その途中で水分が分離されることによって濃縮されて濃縮汚泥となり、この濃縮汚泥は、前記濃縮汚泥排出管11を通って外部へと排出され、不図示の脱水機による脱水処理に供される。   Then, the separation liquid stored in the separation liquid tank 4 is discharged to the outside through the separation liquid discharge pipe 13. Further, the aggregated sludge conveyed upward in the filter cylinder 8 by the rotation of the spiral screw 9 is concentrated by separating the water in the middle thereof to become concentrated sludge, and this concentrated sludge is the concentrated sludge discharge pipe. 11 is discharged to the outside and is subjected to a dehydration process by a dehydrator (not shown).

ところで、斯かる汚泥濃縮装置1’においては、濃縮運転を続けると濾過筒8の濾過面8aの濾過孔内に懸濁物質等の固形物が付着して目詰まりが発生する。   By the way, in such a sludge concentrating device 1 ′, if the concentration operation is continued, solid substances such as suspended substances adhere to the filtration holes of the filtration surface 8 a of the filtration cylinder 8 and clogging occurs.

そこで、濾過筒8の濾過面8aを定期的に逆洗によって洗浄することが行われているが、その一例を図4に示す(特許文献2参照)。   Therefore, the filtration surface 8a of the filter cylinder 8 is regularly cleaned by backwashing, and an example is shown in FIG. 4 (see Patent Document 2).

図4は従来の洗浄手段を備えた汚泥濃縮装置1’の構成図であり、同図において、14は逆洗流体貯留槽であって、この逆洗流体貯留槽14には洗浄水供給管15から供給された洗浄水が貯留されており、この洗浄水は、圧縮空気供給管16から逆洗流体貯留槽14内に供給される圧縮空気によって所定圧に加圧されている。そして、逆洗流体貯留槽14から導出する逆洗水供給管17は、固液分離手段3の外筒7の側部に接続されており、その途中にはバルブV1’が設けられている。尚、図4において、18は排水管、V2’,V3’はバルブである。   FIG. 4 is a block diagram of a conventional sludge concentrating device 1 ′ equipped with a cleaning means. In FIG. 4, reference numeral 14 denotes a backwash fluid storage tank, and the backwash fluid storage tank 14 has a wash water supply pipe 15. The cleaning water supplied from is stored, and this cleaning water is pressurized to a predetermined pressure by the compressed air supplied from the compressed air supply pipe 16 into the backwash fluid storage tank 14. And the backwash water supply pipe | tube 17 derived | led-out from the backwash fluid storage tank 14 is connected to the side part of the outer cylinder 7 of the solid-liquid separation means 3, and valve | bulb V1 'is provided in the middle. In FIG. 4, 18 is a drain pipe, and V2 'and V3' are valves.

而して、汚泥濃縮装置1’の運転によって濾過筒8の濾過面8aに目詰まりが発生すると、バルブV1’が開けられ、逆洗流体貯留槽14内に貯留されている加圧水が逆洗水として逆洗水供給管17から外筒7内へと噴射され、図5(a)に示すように、濾過筒8の濾過面8aに目詰まりを生じさせている懸濁物質等の固形物が逆洗水によって除去され、これによって濾過面8aの目詰まりが解消される。   Thus, when clogging occurs on the filtration surface 8a of the filter cylinder 8 due to the operation of the sludge concentrating device 1 ', the valve V1' is opened, and the pressurized water stored in the backwash fluid reservoir 14 is backwashed. As shown in FIG. 5A, solid matter such as suspended matter that is clogged in the filtration surface 8a of the filtration cylinder 8 is injected from the backwash water supply pipe 17 into the outer cylinder 7. It is removed by backwashing water, thereby eliminating clogging of the filtration surface 8a.

特開2003−164899号公報JP 2003-164899 A 特開2004−121955号公報JP 2004-121955 A

ところで、濾過筒8の濾過面8aの内面に付着する固形物等の汚れは、濾過筒8内で回転するスパイラルスクリュー9によって常時掻き取られるために濾過面8aの内面には汚れは発生しないが、濾過面8aの外面側では、濾過面8aを通って外筒7内の分離液側へリークした固形物が分離液中に残存する凝集剤によってフロック化されて大きくなり、図5(b)に示すように、この大きくなった固形物が濾過面8aの外面に汚れとして付着するとともに、濾過面8aに目詰まりを生じさせるという問題があった。   By the way, since dirt such as solid matter adhering to the inner surface of the filtration surface 8a of the filtration cylinder 8 is always scraped off by the spiral screw 9 rotating in the filtration cylinder 8, no dirt is generated on the inner surface of the filtration surface 8a. On the outer surface side of the filtration surface 8a, the solid matter leaked to the separation liquid side in the outer cylinder 7 through the filtration surface 8a is flocked and enlarged by the coagulant remaining in the separation liquid, and FIG. As shown in FIG. 2, there is a problem that the enlarged solid matter adheres to the outer surface of the filtration surface 8a as dirt and clogs the filtration surface 8a.

このように、濾過筒8の濾過面8aの目詰まりに関する問題に対しては図4に示す従来の洗浄手段及び洗浄方法によって対処することができるが、濾過面8aの外面の汚れの問題には従来の洗浄手段及び洗浄方法によっては対処することができず、この問題に対する解決策が望まれていた。   As described above, the problem related to the clogging of the filtration surface 8a of the filtration cylinder 8 can be dealt with by the conventional washing means and washing method shown in FIG. 4, but the problem of the contamination of the outer surface of the filtration surface 8a is considered. A conventional cleaning means and cleaning method cannot cope with it, and a solution to this problem has been desired.

本発明は上記問題に鑑みてなされたもので、その目的とする処は、濾過筒の濾過面外面の汚れを防いで所要の処理量と固形物回収率を確保することができる汚泥濃縮装置及びこれの洗浄方法を提供することにある。   The present invention has been made in view of the above problems, and its intended treatment is a sludge concentrating device capable of preventing the dirt on the outer surface of the filter cylinder and ensuring the required treatment amount and solids recovery rate, and It is to provide a cleaning method for this.

上記目的を達成するため、請求項1記載の発明は、外筒内に濾過筒を収容し、該濾過筒の内部にスパイラルスクリューを回転可能に収容し、該スパイラルスクリューを回転駆動することによって、汚泥凝集槽から前記濾過筒内に導入される汚泥を搬送しながら、該汚泥に含まれる水分を前記濾過筒の濾過面を通過させて分離液として前記外筒内に収容して汚泥を濃縮するとともに、濃縮された汚泥を濾過筒の内部より排出する汚泥濃縮装置において、前記濾過筒の濾過面外周に弾性的に接触する弾性リングの両面を金属リングで挟持して構成された洗浄体を濾過筒の長さ方向に移動可能に設けたことを特徴とする。
In order to achieve the above object, the invention according to claim 1 is characterized in that a filter cylinder is accommodated in an outer cylinder , a spiral screw is rotatably accommodated in the filter cylinder, and the spiral screw is driven to rotate. While conveying the sludge introduced into the filter cylinder from the sludge aggregation tank, the water contained in the sludge passes through the filtration surface of the filter cylinder and is stored in the outer cylinder as a separation liquid to concentrate the sludge. At the same time, in the sludge concentrating device for discharging the concentrated sludge from the inside of the filter cylinder, the cleaning body constituted by sandwiching both sides of the elastic ring elastically contacting the outer periphery of the filter cylinder with the metal ring is filtered. It is provided to be movable in the length direction of the cylinder.

請求項記載の発明は、請求項1記載の発明において、前記洗浄体をロープで吊り下げ、該ロープを引き上げることによって洗浄体を濾過筒の長さ方向に移動させることを特徴とする。
According to a second aspect of the invention of claim 1 Symbol placement, the cleaning body suspended by ropes, characterized in that moving the cleaning body in the longitudinal direction of the filtration tube by pulling the rope.

請求項記載の発明は、外筒内に濾過筒を収容し、該濾過筒の内部にスパイラルスクリューを回転可能に収容し、該スパイラルスクリューを回転駆動することによって、汚泥凝集槽から前記濾過筒内に導入される汚泥を搬送しながら、該汚泥に含まれる水分を前記濾過筒の濾過面を通過させて分離液として前記外筒内に収容して汚泥を濃縮するとともに、濃縮された汚泥を濾過筒の内部より排出する汚泥濃縮装置の洗浄方法として、
前記濾過筒の濾過面外周に弾性的に接触する弾性リングの両面を金属リングで挟持して構成された洗浄体を濾過筒の長さ方向に移動させることによって、前記濾過筒の濾過面外面に付着した汚れを除去することを特徴とする。
According to a third aspect of the present invention, a filtration cylinder is accommodated in an outer cylinder, a spiral screw is rotatably accommodated in the filtration cylinder, and the spiral screw is driven to rotate, whereby the filtration cylinder is removed from the sludge aggregation tank. While conveying the sludge introduced into the inside, the water contained in the sludge is passed through the filtration surface of the filter cylinder and stored in the outer cylinder as a separation liquid to concentrate the sludge. As a cleaning method of the sludge concentrator that discharges from the inside of the filter cylinder,
By moving a cleaning body configured by sandwiching both sides of an elastic ring elastically contacting the outer periphery of the filtration surface of the filtration tube with a metal ring in the length direction of the filtration tube, the outer surface of the filtration tube is filtered. It is characterized by removing attached dirt.

請求項記載の発明は、請求項記載の発明において、更に逆洗空気を前記外筒内に噴射することによって前記濾過筒の濾過孔内の汚れを除去することを特徴とする。
According to a fourth aspect of the present invention, in the third aspect of the present invention, the dirt in the filter hole of the filter cylinder is removed by further injecting backwash air into the outer cylinder.

請求項1及び記載の発明によれば、濾過筒の濾過面外面に付着した汚れは、弾性リングが濾過面外面に摺接しながら濾過筒の長さ方向に移動する洗浄体によって効果的に掻き取られるため、濾過筒の目詰まりも防がれ、所要の処理量と固形物回収率(SS回収率)が確保される。
According to the first and third aspects of the present invention, the dirt adhering to the outer surface of the filter cylinder is effectively scraped by the cleaning body that moves in the length direction of the filter cylinder while the elastic ring is in sliding contact with the outer surface of the filter surface. Therefore, the clogging of the filter cylinder is prevented, and a required processing amount and a solid recovery rate (SS recovery rate) are ensured.

請求項記載の発明によれば、洗浄体を吊り下げるロープを引き上げて洗浄体を濾過筒の長さ方向に移動させることによって、濾過筒外面の汚れを洗浄体によって確実に除去することができる。
According to the second aspect of the present invention, the dirt on the outer surface of the filter cylinder can be reliably removed by the cleaning body by pulling up the rope that suspends the cleaning body and moving the cleaning body in the length direction of the filter cylinder. .

請求項記載の発明によれば、逆洗流体以外に外筒内に噴射される逆洗空気によって濾過筒の濾過面の濾過孔内が逆洗されるため、濾過面外面に付着した汚れの除去と共に濾過面の目詰まりが防がれる。
According to the invention of claim 4, since the inside of the filtration hole of the filtration surface of the filter cylinder is backwashed by the backwash air injected into the outer cylinder in addition to the backwash fluid, the dirt adhering to the outer surface of the filtration surface is removed. Along with the removal, clogging of the filtration surface is prevented.

本発明に係る汚泥濃縮装置の基本構成を示す概略図である。It is the schematic which shows the basic composition of the sludge concentration apparatus which concerns on this invention. (a)は本発明に係る汚泥濃縮装置の洗浄に使用される洗浄体の平面図、(b)は(a)のB−B線断面図である。(A) is a top view of the washing body used for washing | cleaning of the sludge concentration apparatus based on this invention, (b) is the BB sectional drawing of (a). 従来の汚泥濃縮装置の基本構成を示す概略図である。It is the schematic which shows the basic composition of the conventional sludge concentration apparatus. 従来の洗浄手段を備えた汚泥濃縮装置の概略図である。It is the schematic of the sludge concentration apparatus provided with the conventional washing | cleaning means. (a)は濾過面の逆洗による洗浄の様子を示す部分断面図、(b)は濾過面外面の汚れの様子を示す部分断面図である。(A) is a fragmentary sectional view which shows the mode of washing | cleaning by back washing of a filtration surface, (b) is a fragmentary sectional view which shows the mode of the stain | pollution | contamination of a filtration surface outer surface.

以下に本発明の実施の形態を添付図面に基づいて説明する。   Embodiments of the present invention will be described below with reference to the accompanying drawings.

図1は本発明に係る汚泥濃縮装置の基本構成を示す概略図、図2(a)は洗浄体の平面図、図2(b)は同図(a)のB−B線断面図であり、これらの図においては、図3及び図4に示したものと同一要素には同一符号を付しており、以下、それらについての再度の説明は省略する。   FIG. 1 is a schematic view showing a basic configuration of a sludge concentrating device according to the present invention, FIG. 2 (a) is a plan view of a cleaning body, and FIG. 2 (b) is a sectional view taken along line BB of FIG. In these drawings, the same elements as those shown in FIGS. 3 and 4 are denoted by the same reference numerals, and the repetitive description thereof will be omitted below.

図1に示す濃縮汚泥装置においては、凝集汚泥導入管10から固液分離手段3の濾過筒8内の上部に導入された凝縮汚泥は、モータM2によって回転するスパイラルスクリュー9によって濾過筒8内を下方へと搬送されながら、これに含まれる水分が分離されて濾過筒8の濾過面8aを通過し、この水分は、分離液として外筒7と濾過筒8の間の空間に収容され、分離液排出管13から外部に排出される。又、水分が除去された濃縮汚泥は、濾過筒8の下部から濃縮汚泥排出管11へと排出される。   In the concentrated sludge apparatus shown in FIG. 1, the condensed sludge introduced into the upper part of the filtration cylinder 8 of the solid-liquid separation means 3 from the aggregated sludge introduction pipe 10 passes through the inside of the filtration cylinder 8 by the spiral screw 9 rotated by the motor M2. While being transported downward, the moisture contained therein is separated and passes through the filtration surface 8a of the filtration cylinder 8, and this moisture is accommodated in the space between the outer cylinder 7 and the filtration cylinder 8 as a separation liquid. The liquid is discharged from the liquid discharge pipe 13 to the outside. The concentrated sludge from which moisture has been removed is discharged from the lower part of the filter cylinder 8 to the concentrated sludge discharge pipe 11.

ところで、本実施の形態に係る汚泥濃縮装置1においては、濾過筒8の濾過面8aの外面に付着した汚れを除去する清掃手段として、濾過筒8の外周面に沿って上下動する洗浄体25”が設けられている。   By the way, in the sludge concentration apparatus 1 which concerns on this Embodiment, the washing body 25 which moves up and down along the outer peripheral surface of the filter cylinder 8 is used as the cleaning means which removes the dirt adhering to the outer surface of the filter surface 8a of the filter cylinder 8. "Is provided.

ここで、上記洗浄体25”は、図2(b)に示すように、濾過筒8の濾過面8aの外面に弾性的に接触するゴム製の弾性リング29を鋼製の金属リング30で挟持して構成されており、弾性リング29の内径d1は濾過筒8の外径d3よりも小さく(d1<d3)設定され、金属リング30の内径d2は濾過筒8の外径d3よりも大きく(d2>d3)設定されており、金属リング30の内周面は濾過筒8の外周面に対して非接触状態を維持している。   Here, as shown in FIG. 2 (b), the cleaning body 25 ″ sandwiches a rubber elastic ring 29 elastically contacting the outer surface of the filtration surface 8 a of the filtration cylinder 8 with a steel metal ring 30. The inner diameter d1 of the elastic ring 29 is set smaller than the outer diameter d3 of the filter cylinder 8 (d1 <d3), and the inner diameter d2 of the metal ring 30 is larger than the outer diameter d3 of the filter cylinder 8 ( d2> d3) is set, and the inner peripheral surface of the metal ring 30 maintains a non-contact state with respect to the outer peripheral surface of the filter tube 8.

そして、以上のように構成された洗浄体25は、図1に示すように、ロープ31によって吊り下げられており、洗浄時以外には図示のように濾過筒8の下端に位置している。   And the washing | cleaning body 25 comprised as mentioned above is suspended by the rope 31, as shown in FIG. 1, and is located in the lower end of the filter cylinder 8 like illustration at the time of washing | cleaning.

而して、濃縮運転によって濾過筒8の濾過面8aに目詰まり等が生じたために洗浄が必要になった場合には、圧縮空気供給管23から外筒7内に圧縮空気を噴射して濾過筒8の濾過面8aに目詰まりを生じさせている固形物を除去するとともに、ロ^ぷ31を上げ下げして洗浄体25”を濾過筒の外周面に沿って上下動させる。尚、ロープ31を上方へ引っ張れば洗浄体25”が上昇し、ロープ31を引っ張る力を開放すれば洗浄体25”は自重で下降し、これを繰り返すことによって洗浄体25”が濾過筒8の外周面に沿って上下動する。
Thus, when cleaning is necessary because the filtration surface 8a of the filter cylinder 8 is clogged by the concentration operation, the compressed air is injected into the outer cylinder 7 from the compressed air supply pipe 23 and filtered. The solid matter causing clogging on the filtration surface 8a of the tube 8 is removed, and the washing 31 "is moved up and down along the outer peripheral surface of the filtration tube 8 by raising and lowering the rope 31. Note that the rope If the 31 is pulled upward, the cleaning body 25 ″ is raised, and if the force pulling the rope 31 is released, the cleaning body 25 ″ is lowered by its own weight. Move up and down along.

上述のように洗浄体25”が濾過筒8の外周面に沿って上下動すると、その弾性リング29は前述のように濾過面8aの外面に弾性接触しているため、該弾性リング29の内面が濾過面8aの外面に沿って摺動し、濾過面8aの外面に付着している汚れが弾性リング29によって掻き取られる。   When the cleaning body 25 ″ moves up and down along the outer peripheral surface of the filter cylinder 8 as described above, the elastic ring 29 is in elastic contact with the outer surface of the filter surface 8a as described above. Slides along the outer surface of the filtration surface 8a, and the dirt adhering to the outer surface of the filtration surface 8a is scraped off by the elastic ring 29.

従って、本実施の形態によれば、濾過筒8の濾過面8aの目詰まりは、圧縮空気による逆洗によって防がれ、濾過面8aの外面に付着した汚れは、濾過筒8の外周面に沿って上下動する洗浄体25”によって効果的に除去されるため、所要の処理量と固形物回収率(SS回収率)が確保される。   Therefore, according to the present embodiment, clogging of the filtration surface 8a of the filtration cylinder 8 is prevented by backwashing with compressed air, and dirt adhering to the outer surface of the filtration surface 8a is deposited on the outer circumferential surface of the filtration cylinder 8. Since it is effectively removed by the cleaning body 25 ″ that moves up and down along the way, the required throughput and solids recovery rate (SS recovery rate) are ensured.

本発明は、スクリュープレス型の汚泥濃縮装置及びこれの洗浄方法に対して適用可能であって、その処理対象である汚泥の種類を問わない。   The present invention is applicable to a screw press type sludge concentrating device and a cleaning method therefor, regardless of the type of sludge to be treated.

3 固液分離手段
7 外筒
8 濾過筒
8a 濾過面
9 スパイラルスクリュー
10 凝集汚泥導入管
11 濃縮汚泥排出管
13 分離液排出管
23 圧縮空気供給管
25” 洗浄体
29 弾性リング
30 金属リング
31 ロープ
M2 モータ
DESCRIPTION OF SYMBOLS 3 Solid-liquid separation means 7 Outer cylinder 8 Filter cylinder 8a Filtration surface 9 Spiral screw 10 Aggregated sludge introduction pipe 11 Concentrated sludge discharge pipe 13 Separation liquid discharge pipe 23 Compressed air supply pipe 25 "Washing body 29 Elastic ring 30 Metal ring 31 Rope M2 motor

Claims (4)

外筒内に濾過筒を収容し、該濾過筒の内部にスパイラルスクリューを回転可能に収容し、該スパイラルスクリューを回転駆動することによって、汚泥凝集槽から前記濾過筒内に導入される汚泥を搬送しながら、該汚泥に含まれる水分を前記濾過筒の濾過面を通過させて分離液として前記外筒内に収容して汚泥を濃縮するとともに、濃縮された汚泥を濾過筒の内部より排出する汚泥濃縮装置において、
前記濾過筒の濾過面外周に弾性的に接触する弾性リングの両面を金属リングで挟持して構成された洗浄体を濾過筒の長さ方向に移動可能に設けたことを特徴とする汚泥濃縮装置。
A filter cylinder is accommodated in the outer cylinder, a spiral screw is rotatably accommodated in the filter cylinder, and the sludge introduced into the filter cylinder is conveyed from the sludge agglomeration tank by rotationally driving the spiral screw. Meanwhile, the sludge that passes the water contained in the sludge through the filtration surface of the filter cylinder and stores it in the outer cylinder as a separation liquid to concentrate the sludge and discharge the concentrated sludge from the inside of the filter cylinder. In the concentrator,
A sludge concentrating device comprising a cleaning body configured by sandwiching both surfaces of an elastic ring elastically contacting the outer periphery of the filtration surface of the filtration tube with a metal ring so as to be movable in the length direction of the filtration tube. .
前記洗浄体をロープで吊り下げ、該ロープを引き上げることによって洗浄体を濾過筒の長さ方向に移動させることを特徴とする請求項1記載の汚泥濃縮装置。 Wherein the cleaning body suspended by the rope, according to claim 1 Symbol placement of the sludge concentrating apparatus and moving in the longitudinal direction of the filtration cylinder cleaning member by pulling the rope. 外筒内に濾過筒を収容し、該濾過筒の内部にスパイラルスクリューを回転可能に収容し、該スパイラルスクリューを回転駆動することによって、汚泥凝集槽から前記濾過筒内に導入される汚泥を搬送しながら、該汚泥に含まれる水分を前記濾過筒の濾過面を通過させて分離液として前記外筒内に収容して汚泥を濃縮するとともに、濃縮された汚泥を濾過筒の内部より排出する汚泥濃縮装置の洗浄方法であって、
前記濾過筒の濾過面外周に弾性的に接触する弾性リングの両面を金属リングで挟持して構成された洗浄体を濾過筒の長さ方向に移動させることによって、前記濾過筒の濾過面外面に付着した汚れを除去することを特徴とする汚泥濃縮装置の洗浄方法。
A filter cylinder is accommodated in the outer cylinder, a spiral screw is rotatably accommodated in the filter cylinder, and the sludge introduced into the filter cylinder is conveyed from the sludge agglomeration tank by rotationally driving the spiral screw. Meanwhile, the sludge that passes the water contained in the sludge through the filtration surface of the filter cylinder and stores it in the outer cylinder as a separation liquid to concentrate the sludge and discharge the concentrated sludge from the inside of the filter cylinder. A cleaning method for a concentrator,
By moving a cleaning body configured by sandwiching both sides of an elastic ring elastically contacting the outer periphery of the filtration surface of the filtration tube with a metal ring in the length direction of the filtration tube, the outer surface of the filtration tube is filtered. A method for cleaning a sludge concentrator, characterized by removing attached dirt.
更に逆洗空気を前記外筒内に噴射することによって前記濾過筒の濾過孔内の汚れを除去することを特徴とする請求項3記載の汚泥濃縮装置の洗浄方法。
4. The method for cleaning a sludge concentrating device according to claim 3, wherein the dirt in the filter hole of the filter cylinder is removed by jetting backwash air into the outer cylinder.
JP2011224047A 2011-10-11 2011-10-11 Sludge concentrator and cleaning method therefor Expired - Fee Related JP5187540B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2011224047A JP5187540B2 (en) 2011-10-11 2011-10-11 Sludge concentrator and cleaning method therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2011224047A JP5187540B2 (en) 2011-10-11 2011-10-11 Sludge concentrator and cleaning method therefor

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP2005228120A Division JP4877466B2 (en) 2005-08-05 2005-08-05 Sludge concentrator and cleaning method therefor

Publications (2)

Publication Number Publication Date
JP2012006016A JP2012006016A (en) 2012-01-12
JP5187540B2 true JP5187540B2 (en) 2013-04-24

Family

ID=45537197

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2011224047A Expired - Fee Related JP5187540B2 (en) 2011-10-11 2011-10-11 Sludge concentrator and cleaning method therefor

Country Status (1)

Country Link
JP (1) JP5187540B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6641884B2 (en) * 2015-10-29 2020-02-05 栗田工業株式会社 Sludge thickener
JP6908087B2 (en) * 2015-10-29 2021-07-21 栗田工業株式会社 Sludge concentrator

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0661391U (en) * 1993-01-29 1994-08-30 株式会社フロム工業 Screen cylinder cleaning device for screw dehydrator
JPH0924214A (en) * 1995-07-07 1997-01-28 Toyo Kogyo Kk Continuous dehydrator
JPH11290899A (en) * 1998-04-10 1999-10-26 Ebara Corp Filter pipe type dehydrator and dehydration method
JP2001179492A (en) * 1999-12-21 2001-07-03 Ishigaki Co Ltd Screw press type concentrating machine, and its concentrating method
JP3627810B2 (en) * 2002-10-01 2005-03-09 栗田工業株式会社 Sludge concentrator and cleaning method for sludge concentrator

Also Published As

Publication number Publication date
JP2012006016A (en) 2012-01-12

Similar Documents

Publication Publication Date Title
JP5214424B2 (en) Wastewater treatment equipment
JP4253353B1 (en) Sludge dewatering method and system
JP4877466B2 (en) Sludge concentrator and cleaning method therefor
JP5531330B2 (en) Rotating pressure dehydrator and sludge dewatering method using rotating pressure dehydrator
CN103230949A (en) Magnetic pretreatment device for rolled emulsion
JP5187540B2 (en) Sludge concentrator and cleaning method therefor
KR20170018840A (en) Method for water treatment by adsorption and filtration on a granular material bed
JP2010057997A (en) Sludge dewatering apparatus and method
KR101616503B1 (en) Waste oil and oil sludge treatment system and method thereof
JP2008049275A (en) Sludge thickener
KR20120091553A (en) A solid-and-liquid seperating apparatus for treating effluents, a screw dehydration apparatus and a treatment using them
JP2008149272A (en) Sludge concentration apparatus and its washing method
JP4129479B1 (en) Sludge treatment method and treatment system
KR101939751B1 (en) Compression rotary high-concentration concentrator and concentration method
KR200471174Y1 (en) Filtration apparatus having means for recovering filter material
KR101469634B1 (en) Water treatment system use of tubular filter module
CN208632333U (en) Efficient printing and dyeing wastewater treatment system
JP5481654B2 (en) Sludge treatment method and treatment system
KR101237412B1 (en) Filter washing device in a upward-flowing purification system
KR101889710B1 (en) System for reusing sewage waste water
JP4763670B2 (en) Filtration device
JP4952877B2 (en) Sludge concentration method and sludge concentration apparatus
CN203715430U (en) Electroplating nickel-containing wastewater up-to-standard treatment system for workshops of metallurgical plants
JP2004243185A (en) Solid-liquid separation treatment method and apparatus therefor
JP3176638U (en) Radioactive wastewater treatment equipment

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20111026

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20120906

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20120912

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20121019

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20121226

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20130108

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20160201

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Ref document number: 5187540

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

LAPS Cancellation because of no payment of annual fees