JP2018094469A - Drum type thickener with travelling water-absorbing belt - Google Patents

Drum type thickener with travelling water-absorbing belt Download PDF

Info

Publication number
JP2018094469A
JP2018094469A JP2016239092A JP2016239092A JP2018094469A JP 2018094469 A JP2018094469 A JP 2018094469A JP 2016239092 A JP2016239092 A JP 2016239092A JP 2016239092 A JP2016239092 A JP 2016239092A JP 2018094469 A JP2018094469 A JP 2018094469A
Authority
JP
Japan
Prior art keywords
water
spiral
sludge
belt
absorbing belt
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.)
Granted
Application number
JP2016239092A
Other languages
Japanese (ja)
Other versions
JP6756981B2 (en
Inventor
康昭 西原
Yasuaki Nishihara
康昭 西原
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.)
Ishigaki Co Ltd
Original Assignee
Ishigaki Co 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 Ishigaki Co Ltd filed Critical Ishigaki Co Ltd
Priority to JP2016239092A priority Critical patent/JP6756981B2/en
Publication of JP2018094469A publication Critical patent/JP2018094469A/en
Application granted granted Critical
Publication of JP6756981B2 publication Critical patent/JP6756981B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

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

Abstract

PROBLEM TO BE SOLVED: To provide a drum type thickener with a travelling absorption belt having a filter body composed of a travelling belt.SOLUTION: A drum type thickener includes a rotatable spiral 1 of which both ends are connected to an annular outer ring 6, a travelling absorption belt 2 wound around the spiral 1, dewatering rollers 4 for pressing the absorption belt 2 to discharge water, and a supply pipe 8 inserted in a drum body 3 composed of the spiral 1 around which the absorption belt 2 is wound. Sludge is softened in the drum body 3 by travelling absorption belt 2 and rotating spiral 1. Compactness of the sludge is thus changed leading to efficient solid-liquid separation.SELECTED DRAWING: Figure 1

Description

この発明は、搬送スパイラルの周囲に張設した円筒状のろ過体を有するドラム型濃縮機において、ろ過体を走行自在な吸水ベルトで構成し、吸水ベルトからろ液を回収しつつ連続的に安定した濃縮汚泥を生成する吸水ベルト走行式ドラム型濃縮機に関する。   The present invention provides a drum-type concentrator having a cylindrical filter stretched around a conveying spiral, wherein the filter is composed of a water-absorbing belt that can run freely, and is continuously stable while collecting filtrate from the water-absorbing belt. The present invention relates to a drum-type concentrator that absorbs water and generates a concentrated sludge.

従来、下水、し尿、あるいは食品生産加工排水等の有機性汚泥を濃縮するベルト型濃縮機あるいはドラム型濃縮機は一般に知られている。ベルト型濃縮機あるいはドラム型濃縮機は連続的に汚泥を濃縮する装置であり、連続的に汚泥を装置に供給し、連続的に濃縮汚泥を装置から排出している。 Conventionally, belt-type concentrators or drum-type concentrators that concentrate organic sludge such as sewage, human waste, or food production processing wastewater are generally known. A belt-type concentrator or a drum-type concentrator is a device for continuously concentrating sludge, continuously supplying sludge to the device, and continuously discharging the concentrated sludge from the device.

特許文献1で開示されているように、無端ベルト状の吸水材上に汚泥類を載置して、汚泥中の水分を吸水材に吸収させた後に汚泥類を排除し、吸水材を圧縮して吸着した水を吐出する脱水処理方法は公知である。 As disclosed in Patent Document 1, sludge is placed on an endless belt-shaped water-absorbing material, the water in the sludge is absorbed by the water-absorbing material, the sludge is removed, and the water-absorbing material is compressed. A dehydration method for discharging the adsorbed water is known.

特許文献2で開示されているように、螺旋翼をろ布で囲んだ円筒状のドラム式の脱水機において、内部に汚泥を供給して円筒体を回転させ、ろ布で固液分離を行いつつ螺旋翼で濃縮汚泥を搬送するドラム型濃縮機は公知である。 As disclosed in Patent Document 2, in a cylindrical drum type dehydrator in which a spiral blade is surrounded by a filter cloth, sludge is supplied to the inside to rotate the cylinder, and solid-liquid separation is performed using the filter cloth. Drum type concentrators that convey concentrated sludge with spiral blades are known.

特許文献3で開示されているように、走行自在に配設した吸水性のある無端状のろ布を原液中に浸漬させ、吸水したろ布を濃縮槽外で脱水して原液を濃縮させる濃縮装置は公知である。 As disclosed in Patent Document 3, a water-absorbing endless filter cloth disposed so as to run freely is immersed in the stock solution, and the water-absorbed filter fabric is dehydrated outside the concentration tank to concentrate the stock solution. The apparatus is known.

特開昭55−94694号公報JP 55-94694 A 実開昭56−44819号公報Japanese Utility Model Publication No. 56-44819 特許第3636355号公報Japanese Patent No. 3636355

特許文献1のような吸水性ベルトで構成したベルト型濃縮機は、ベルト上に残留する固形分が大きく姿勢を変えることがないので、固形分内部および上面の水分までは吸収されることがなく濃縮度が低い。また、ベルト状にすき返し装置を配設して固形分の姿勢を変えることも可能であるが、ベルトの搬送距離が長くなり設置スペースが大きくなる。 The belt-type concentrator configured with a water-absorbing belt as in Patent Document 1 has a large solid content remaining on the belt and does not change its posture, so that the moisture inside the solid content and the upper surface is not absorbed. Concentration is low. In addition, it is possible to change the posture of the solid content by arranging a crushing device in the form of a belt, but the conveying distance of the belt becomes long and the installation space becomes large.

特許文献2のようなドラム式の円筒体をろ布で構成している濃縮機は、目詰まりに対するろ布の洗浄が必要となる。円筒体の外部から圧縮空気を噴射して目詰まりを解消しているが、圧縮空気では洗浄効果が低く、電気代等によるコストも高くなる。
他に洗浄水でろ布を洗浄している事例もあるが、円筒体の外部からろ布洗浄を行うためには、内部に洗浄水が流入するため、濃縮運転を停止する必要がある。なお、洗浄水がろ布に含侵することにより、汚泥に吸着している液分の吸水性が悪くなるという課題もある。
The concentrator which comprises the drum-type cylindrical body like patent document 2 with the filter cloth needs washing | cleaning of the filter cloth with respect to clogging. Although clogging is eliminated by injecting compressed air from the outside of the cylindrical body, the cleaning effect is low with compressed air, and the cost due to electricity costs and the like also increases.
There are other cases in which the filter cloth is washed with washing water. However, in order to wash the filter cloth from the outside of the cylindrical body, the washing operation flows into the inside, so it is necessary to stop the concentration operation. In addition, when the washing water impregnates the filter cloth, there is a problem that the water absorption of the liquid adsorbed on the sludge is deteriorated.

また、特許文献3のような吸水ろ布を原液中に浸漬させて濃縮する濃縮装置は、濃縮槽内で濃縮された汚泥量を検知して所定量に達した場合に排出している。したがって、後行程に本濃縮装置で生成した濃縮汚泥を連側的に供給することができない。さらに、原液の供給量が少ないと濃縮汚泥が濃縮槽内で留まる期間が長くなり、濃縮汚泥が濃縮槽内で変質して後行程での処理が安定しないという課題がある。 Moreover, the concentration apparatus which immerses and concentrates the water absorption filter cloth like patent document 3 is discharged | emitted when the amount of sludge concentrated in the concentration tank is detected and it reaches predetermined amount. Therefore, the concentrated sludge produced | generated with this concentration apparatus in the back stroke cannot be supplied continuously. Furthermore, when the supply amount of the stock solution is small, there is a problem that the period during which the concentrated sludge stays in the concentration tank becomes long, and the concentrated sludge is denatured in the concentration tank and the treatment in the subsequent process is not stable.

この発明は、濃縮性汚泥を安定して濃縮するために、吸水ベルト型濃縮機とドラム型濃縮機の優れた機能を組み合わせたもので、汚泥の姿勢を変化させつつ安定的に濃縮し、連続運転可能な吸水ベルト走行式ドラム型濃縮機を提供する。   This invention combines the excellent functions of a water-absorbing belt type concentrator and a drum type concentrator in order to concentrate concentrated sludge in a stable manner. Provided is a drum-type concentrator capable of running a water-absorbing belt.

この発明は、周囲にろ過体を張設したドラム体の内部に汚泥を供給し、ドラム体を回転させつつ汚泥を濃縮する吸水ベルト走行式ドラム型濃縮機において、両端に円環状の外環を接続した回転自在な螺旋状のスパイラルと、スパイラルに掛け回し、吸水体で構成した走行自在な吸水ベルトと、吸水ベルトを押圧して吸収した水分を排出する脱水ロールと、吸水ベルトを巻き掛けたスパイラルで構成したドラム体の内部に挿通する供給管と、を備えるので、ドラム体内で汚泥を揉み解し、圧密度を変化させることで効率的な固液分離が可能となる。 The present invention relates to a water-absorbing belt traveling drum type concentrator that supplies sludge to the inside of a drum body having a filter body stretched around it, and concentrates the sludge while rotating the drum body. A rotating spiral spiral connected, a running water absorbing belt constructed of a water absorbing body, wound around the spiral, a dewatering roll that presses the water absorbing belt to discharge the absorbed water, and a water absorbing belt is wound around And a supply pipe inserted through the inside of the drum body constituted by a spiral, so that efficient solid-liquid separation can be achieved by dissolving sludge in the drum body and changing the pressure density.

また、ベルトを無端状に構成し、スパイラルと駆動ロールに掛け回すとともに、吸水ベルトを洗浄するための洗浄装置を備えるので、連続的な濃縮運転が可能となる。 In addition, since the belt is configured in an endless manner, wound around the spiral and the drive roll, and provided with a cleaning device for cleaning the water absorbing belt, continuous concentration operation is possible.

また、スパイラルの上方に一対のリターンロールを配設し、一対のリターンロールの間隔を、スパイラルの直径以下とすると、ベルト上に残留する汚泥が、ドラム体の底部からベルトの走行に沿って中心軸近くまで搬送された後、確実に自重によって底部に落泥する。落泥時の揉み解し作用により汚泥内部の液分が表面に抽出され、ベルトによる固液分離が促進される。 Further, if a pair of return rolls are arranged above the spiral and the distance between the pair of return rolls is equal to or less than the diameter of the spiral, sludge remaining on the belt is centered along the running of the belt from the bottom of the drum body. After being transported to the vicinity of the shaft, it surely falls to the bottom by its own weight. The sludge disintegration during sludge extraction extracts the liquid content inside the sludge to the surface, facilitating solid-liquid separation by the belt.

供給管を中心軸とし、中心軸に螺旋状のスパイラルを巻き掛けると、運転中に隣段への汚泥の越流の心配がなく、多量の処理運転にも対応できる。 When the supply pipe is the central axis and a spiral spiral is wound around the central axis, there is no risk of sludge overflowing to the adjacent stage during operation, and a large amount of treatment operation can be handled.

この発明によれば、ドラム型濃縮機のろ過体を走行自在な吸水ベルトで構成しているので、吸水ベルトで定量の水分を吸収しつつ連続的な濃縮運転となる。
吸水ベルトの走行と、スパイラルの回転によってドラム体内で汚泥を揉み解し、圧密度を変化させることで、例えば、特に長尺な紐状をしている汚泥や繊維分が絡み合った汚泥でも、効率的な固液分離が可能となる。
According to this invention, since the filter body of the drum type concentrator is constituted by the water absorption belt that can run freely, the water absorption belt absorbs a fixed amount of water, and the continuous concentration operation is performed.
By absorbing the sludge in the drum body by running the water absorption belt and rotating the spiral, and changing the pressure density, for example, even sludge in a long string shape or sludge with intertwined fibers is efficient. Solid-liquid separation becomes possible.

本発明に係る吸水ベルト走行式ドラム型濃縮機の概略正面図である。It is a schematic front view of the water-absorbing belt traveling drum type concentrator according to the present invention. 同じく、吸水ベルト走行式ドラム型濃縮機の概略縦断側面図である。Similarly, it is a schematic longitudinal side view of a water-absorbing belt traveling drum type concentrator. 同じく、吸水ベルト走行式ドラム型濃縮機の背面図である。Similarly, it is a rear view of a water-absorbing belt traveling type drum type concentrator. 他の実施例1の吸水ベルト走行式ドラム型濃縮機の概略正面図である。It is a schematic front view of the water absorption belt traveling type drum type concentrator of other Example 1. 他の実施例2の吸水ベルト走行式ドラム型濃縮機の正面図である。It is a front view of the water absorption belt traveling type drum type concentrator of other Example 2. 他の実施例3の吸水ベルト走行式ドラム型濃縮機の正面図である。It is a front view of the water absorption belt traveling type drum type concentrator of other Example 3. 他の実施例4の吸水ベルト走行式ドラム型濃縮機の一部縦断側面図である。It is a partial longitudinal cross-sectional side view of the water absorption belt traveling type drum type concentrator of other Example 4.

図1は吸水ベルト走行式ドラム型濃縮機の正面図である。平板を螺旋状に成形したリボン状の中空スパイラル1の外周端に、吸水体(吸水ベルト2)を走行自在に巻き掛けてドラム体3を構成している。吸水ベルト2は横軸のスパイラル1の底部を含んで覆うように掛け回す。吸水ベルト2は不織布、スポンジ等で外部から内部に液分を吸収し、内部に保水する公知の材質を使用できる。   FIG. 1 is a front view of a water-absorbing belt traveling drum type concentrator. A drum body 3 is configured by winding a water absorbent body (water absorbent belt 2) around an outer peripheral end of a ribbon-shaped hollow spiral 1 in which a flat plate is spirally formed. The water absorption belt 2 is hung so as to cover the bottom of the spiral 1 on the horizontal axis. The water-absorbing belt 2 can be made of a known material that absorbs liquid from the outside with a nonwoven fabric, sponge, or the like and retains the water inside.

吸水ベルト2の走行方向に向かって、ドラム体3の下流側には一対の脱水ロール4,4を配設している。脱水ロール4で吸水ベルト2を押圧し、吸水ベルト2内部に吸水したろ液を排出する。脱水ロール4の下方には、圧縮された吸水ベルト2から落水するろ液を貯留あるいは配送するろ液受け5を配設している。 A pair of dewatering rolls 4, 4 are disposed on the downstream side of the drum body 3 in the running direction of the water absorbing belt 2. The water absorption belt 2 is pressed by the dewatering roll 4, and the filtrate absorbed in the water absorption belt 2 is discharged. Below the dewatering roll 4, a filtrate receiver 5 that stores or delivers filtrate that falls from the compressed water absorption belt 2 is disposed.

図2は吸水ベルト走行式ドラム型濃縮機の一部縦断側面図である。スパイラル1の前後端は、円環状の外環6,6に接続しており、円筒状に形成している。外環6は、吸水ベルト2両端の走行代を確保するために、軸方向に所定の幅を有している。 FIG. 2 is a partially longitudinal side view of the water-absorbing belt traveling drum concentrator. The front and rear ends of the spiral 1 are connected to the annular outer rings 6 and 6 and are formed in a cylindrical shape. The outer ring 6 has a predetermined width in the axial direction in order to secure a running allowance at both ends of the water absorbing belt 2.

前端部の外環6には内部の汚泥が漏れないよう蓋7を施している。蓋7には汚泥の供給管8を挿通している。蓋7から挿通された供給管8は、前端部の外環6近傍に汚泥を供給する。供給管8は図示しない供給装置に接続している。なお、蓋7は外環6すべてを覆う必要はなく、内部の汚泥が溢れ出ない高さを有していればよい。 The outer ring 6 at the front end is provided with a lid 7 so that internal sludge does not leak. A sludge supply pipe 8 is inserted through the lid 7. The supply pipe 8 inserted from the lid 7 supplies sludge to the vicinity of the outer ring 6 at the front end. The supply pipe 8 is connected to a supply device (not shown). The lid 7 does not need to cover the entire outer ring 6 and may have a height at which the internal sludge does not overflow.

前端部の外環6にはスプロケットを形成しており、チェーン9によりスパイラル駆動機10と連結されている。前後端の外環6,6およびスパイラル1は一体的に回転自在な構成としている。スパイラル1の回転により、内部に供給された汚泥は周囲に掛け回されている吸水ベルト2により水分を吸収されつつ、液分が減少した濃縮汚泥は後端部の外環6方向に搬送される。
後端部の外環6は開放されており、濃縮された汚泥は、外環の下方に配設された濃縮汚泥受け11に排出される。
A sprocket is formed on the outer ring 6 at the front end, and is connected to a spiral drive 10 by a chain 9. The outer rings 6 and 6 and the spiral 1 at the front and rear ends are configured to be rotatable together. Due to the rotation of the spiral 1, the sludge supplied to the inside is absorbed by the water-absorbing belt 2 wound around, and the concentrated sludge having a reduced liquid content is conveyed toward the outer ring 6 at the rear end. .
The outer ring 6 at the rear end is open, and the concentrated sludge is discharged to a concentrated sludge receiver 11 disposed below the outer ring.

図3は吸水ベルト走行式ドラム型濃縮機の背面図である。蓋7の中心部に有する開口12から汚泥の供給管8を挿通しているので、スパイラル1と一体的に蓋7が回転しても供給管8は固定した状態で安定してドラム体3の内部に汚泥を供給できる。   FIG. 3 is a rear view of the water-absorbing belt traveling drum type concentrator. Since the sludge supply pipe 8 is inserted through the opening 12 at the center of the lid 7, even if the lid 7 rotates together with the spiral 1, the supply pipe 8 is stably fixed in a fixed state. Sludge can be supplied inside.

実施例では、スパイラル1をチェーン9で回転自在に駆動しているが、プーリーや歯車等、公知の継ぎ手を用いることができる。   In the embodiment, the spiral 1 is driven to rotate freely by the chain 9, but a known joint such as a pulley or a gear can be used.

図4は、他の実施例1のドラム型濃縮機の概略正面図である。吸水ベルト2は、例えば図4(a)のように、スパイラル1と駆動ロール14に無端状に巻き掛けて走行させてもよく、図4(b)のように、駆動ロール14により一方から他方へ巻き取られるように構成してもよい。 FIG. 4 is a schematic front view of a drum type concentrator of another embodiment 1. For example, as shown in FIG. 4 (a), the water absorbing belt 2 may be run endlessly around the spiral 1 and the driving roll 14, and as shown in FIG. You may comprise so that it may wind up.

図5は、他の実施例2の吸水ベルト走行式ドラム型濃縮機の正面図であって、スパイラル1の上方には、一対のリターンロール13,13と駆動ロール14および従動ロール15を配設し、リターンロール13の内側と、駆動ロール14および従動ロール15の外側から吸水ベルト2を掛け回して無端状に張設している。駆動ロール14には図示しないロール駆動機を接続してあり、駆動ロール14を回転させることで無端状の吸水ベルト2で形成した吸水体を走行自在に構成している。駆動ロール14と従動ロール15間には吸水ベルト2を洗浄するための洗浄装置18を配設している。 FIG. 5 is a front view of a water-absorbing belt traveling drum type concentrator of another embodiment 2, and a pair of return rolls 13, 13, a drive roll 14 and a driven roll 15 are disposed above the spiral 1. And the water absorption belt 2 is wound around from the inner side of the return roll 13 and the outer side of the drive roll 14 and the driven roll 15, and is stretched endlessly. A roll driving machine (not shown) is connected to the driving roll 14, and the water absorbing body formed by the endless water absorbing belt 2 is configured to run by rotating the driving roll 14. A cleaning device 18 for cleaning the water absorbing belt 2 is disposed between the drive roll 14 and the driven roll 15.

ドラム体3の下方には、吸水ベルト2に摺接するように一対のサポートロール17,17を配設している。なお、サポートロール17の位置や数は、ドラム体3の直径や汚泥の供給量等に応じて適宜配設する。 A pair of support rolls 17 and 17 are disposed below the drum body 3 so as to be in sliding contact with the water absorbing belt 2. The position and number of the support rolls 17 are appropriately arranged according to the diameter of the drum body 3, the amount of sludge supplied, and the like.

吸水ベルト2の走行方向に向かって、ドラム体3の下流側には一対の脱水ロール4,4を配設している。脱水ロール4で吸水ベルト2を押圧し、吸水ベルト2内部に吸水したろ液を排出する。   A pair of dewatering rolls 4, 4 are disposed on the downstream side of the drum body 3 in the running direction of the water absorbing belt 2. The water absorption belt 2 is pressed by the dewatering roll 4, and the filtrate absorbed in the water absorption belt 2 is discharged.

なお、本装置に係る構成要件をサポートする部材、例えば、フレーム、軸受、リブ等は、仕様や条件に応じて適宜配設する。 It should be noted that members that support the structural requirements of the present apparatus, such as frames, bearings, ribs, etc., are appropriately arranged according to specifications and conditions.

汚泥は図示しない汚泥供給ポンプ等で供給管8を介してドラム体3内部の前端の外環6近傍に供給される。内部に供給された汚泥は、重力濃縮作用により吸水ベルト2から液分を吸水される。   The sludge is supplied to the vicinity of the outer ring 6 at the front end inside the drum body 3 through a supply pipe 8 by a sludge supply pump or the like (not shown). The sludge supplied to the inside absorbs liquid from the water absorption belt 2 by the gravity concentration action.

吸水ベルト2上に残留する汚泥は、ドラム体3の底部から吸水ベルト2の走行に沿って中心軸近くの高さまで搬送された後、自重によって底部に落泥する。この時、汚泥の揉み解し作用により汚泥内部の液分が表面に抽出され、吸水ベルト2による固液分離が促進される。 The sludge remaining on the water absorbing belt 2 is transported from the bottom of the drum body 3 to a height near the central axis along the running of the water absorbing belt 2 and then falls to the bottom by its own weight. At this time, the liquid content in the sludge is extracted on the surface by the sludge decontamination action, and solid-liquid separation by the water absorption belt 2 is promoted.

ドラム体3内で吸水ベルト2に追随して移動する汚泥を自重によって底部に落泥させるために、スパイラル1に巻き掛けている吸水ベルト2は上方に向かって走行させる。リターンロール13,13の間隔をスパイラル1の直径以下に配置して、吸水ベルト2をスパイラル1の中心軸の上方まで巻き掛けることが望ましい。また、吸水ベルト2の巻き掛け角度、張力等に応じて、リターンロール13の間隔、高さを適宜設定する。   The water absorbing belt 2 wound around the spiral 1 is caused to travel upward so that the sludge that moves following the water absorbing belt 2 in the drum body 3 falls to the bottom by its own weight. It is desirable to arrange the interval between the return rolls 13 and 13 to be equal to or smaller than the diameter of the spiral 1 and wind the water absorbing belt 2 above the central axis of the spiral 1. Moreover, according to the winding angle of the water absorption belt 2, tension | tensile_strength, etc., the space | interval and height of the return roll 13 are set suitably.

本実施例では一対の脱水ロール4,4を配設して吸収した水分を排出しているが、リターンロール13、駆動ロール14あるいは従動ロール15に対向して脱水ロール4を単独で配設してもよい。また、必要に応じて吸水ベルト2を洗浄するための洗浄装置18を配設してもよい。   In this embodiment, a pair of dewatering rolls 4, 4 are disposed to discharge the absorbed moisture, but the dewatering roll 4 is disposed independently facing the return roll 13, the drive roll 14, or the driven roll 15. May be. Moreover, you may arrange | position the washing | cleaning apparatus 18 for wash | cleaning the water absorption belt 2 as needed.

吸水ベルト2の走行と独立して、螺旋状のスパイラル1の回転作用により、内部の汚泥は排出側に搬送され、その間にも揉み解し作用を受けてさらに濃縮される。スパイラル1のピッチや平板の高さ等は、搬送する汚泥が隣段に越流しないよう供給量等に応じて適宜設定する。   Independent of the running of the water absorbing belt 2, the sludge inside is conveyed to the discharge side by the rotating action of the spiral spiral 1, and is further concentrated by receiving the squeezing action therebetween. The pitch of the spiral 1 and the height of the flat plate are appropriately set according to the supply amount so that the sludge to be conveyed does not overflow to the adjacent stage.

濃縮度はスパイラル1の回転速度あるいは吸水ベルト2の走行速度を制御することによって調整できる。 The degree of concentration can be adjusted by controlling the rotational speed of the spiral 1 or the traveling speed of the water absorbing belt 2.

スパイラル1の回転速度を遅くすると、内部の汚泥の滞留時間が長くなり、濃縮度が高くなる。逆に、スパイラル1の回転速度を速くすると、内部の汚泥の滞留時間が短くなり、濃縮度が低くなる。 When the rotation speed of the spiral 1 is slowed down, the sludge residence time inside becomes longer and the concentration becomes higher. Conversely, when the rotational speed of the spiral 1 is increased, the residence time of the internal sludge is shortened, and the degree of concentration is lowered.

吸水ベルト2の走行速度を速くすると、水分を吸収した部分が早期に通り過ぎ、内部に液分を含んでいない吸水ベルト2に汚泥が接触する割合が多くなり、濃縮度が高くなる。逆に、吸水ベルト2の走行速度を遅くすると、水分を吸収した部分が長く滞留し、内部に液分を含んでいない吸水ベルト2に汚泥が接触する割合が少なくなり、濃縮度が低くなる。 When the traveling speed of the water absorbing belt 2 is increased, the portion that has absorbed moisture passes early, and the ratio of the sludge coming into contact with the water absorbing belt 2 that does not contain liquid is increased, and the degree of concentration is increased. On the contrary, when the running speed of the water absorbing belt 2 is slowed down, the portion that has absorbed moisture stays longer, the ratio of sludge coming into contact with the water absorbing belt 2 that does not contain liquid is reduced, and the degree of concentration decreases.

図6は、他の実施例3の吸水ベルト走行式ドラム型濃縮機の正面図であって、2台のドラム体3,3を並設し、1枚の無端状の吸水ベルト2を2台のドラムに掛け回している。   FIG. 6 is a front view of a water-absorbing belt traveling drum type concentrator of another embodiment 3, in which two drum bodies 3 and 3 are juxtaposed and two endless water-absorbing belts 2 are provided. It is hung around the drum.

吸水ベルト2を一方のスパイラル1に掛け回し、その上方のリターンロール13で反転させた後、他方のスパイラル1の上方のリターンロール13を介して他方のスパイラル1に掛け回し、それぞれのリターンロール13から駆動ロール14および従動ロール15に掛け回している。   The water absorption belt 2 is wound around one spiral 1 and reversed by a return roll 13 above the spiral, and then is wound around the other spiral 1 via a return roll 13 above the other spiral 1. From the drive roll 14 and the driven roll 15.

駆動ロール14をロール駆動機で駆動することで吸水ベルト2が複数のスパイラル1,1間を走行する。   The water absorption belt 2 travels between the plurality of spirals 1 and 1 by driving the driving roll 14 with a roll driving machine.

それぞれのドラム体3の吸水ベルト2の走行方向に向かって下流側に、一対の脱水ロール4,4を配設しており、ドラム体3で汚泥から吸水した水分を排出する。   A pair of dewatering rolls 4, 4 are disposed on the downstream side of each drum body 3 in the running direction of the water absorption belt 2, and the water absorbed from the sludge by the drum body 3 is discharged.

なお、スパイラル1の回転は、それぞれに独立したスパイラル駆動機10,10を接続してもよく、あるいは、並設したスパイラル1,1を1巻のチェーン9で接続し、単機のスパイラル駆動機10で同時に回転させてもよい。   The spiral 1 may be rotated by connecting independent spiral drivers 10, 10, or the spirals 1, 1 arranged side by side are connected by a single chain 9, and a single spiral driver 10 is connected. May be rotated simultaneously.

図7は、他の実施例4の吸水ベルト走行式ドラム型濃縮機の一部縦断側面図であって、平板で形成したリボン状の中空スパイラルに代わって、中心軸19に螺旋状のスパイラル1aを巻き掛けて形成してもよい。この場合、中心軸19をドラム体3から延出させ、中心軸19をスパイラル駆動機10と接続してもよい。 FIG. 7 is a partially longitudinal side view of a water-absorbing belt traveling drum type concentrator according to another embodiment 4, and instead of a ribbon-shaped hollow spiral formed of a flat plate, a spiral spiral 1a formed on a central shaft 19 is formed. It may be formed by winding. In this case, the central shaft 19 may be extended from the drum body 3, and the central shaft 19 may be connected to the spiral driving machine 10.

汚泥の供給は、中心軸19を中空として、汚泥の供給管8を兼用する。中心軸19の前縁の外環6近傍に供給口20を開口する。中心軸19に螺旋状のスパイラル1aを巻き掛けると、隣段への汚泥の越流の心配がない。 The sludge is supplied by using the sludge supply pipe 8 with the central shaft 19 being hollow. A supply port 20 is opened near the outer ring 6 on the front edge of the central shaft 19. When the spiral spiral 1a is wound around the central shaft 19, there is no fear of overflow of sludge to the next stage.

この発明に係る吸水ベルト走行式ドラム型濃縮機は、複雑な形状をしている固形分を含む汚泥でも連続的に濃縮することができる装置である。例えば、特に長尺な紐状をしている汚泥や繊維分が絡み合った汚泥でも、安定的に濃縮することができ、後段のスクリュープレスやベルトプレス等による脱水処理に負荷が掛からず、全体の管理性が向上するものである。 The water-absorbing belt traveling drum type concentrator according to the present invention is an apparatus that can continuously concentrate even sludge containing solid components having a complicated shape. For example, sludge in the form of a long string or sludge entangled with fibers can be concentrated stably, and no load is applied to the dehydration process by the subsequent screw press or belt press. Manageability is improved.

1,1a スパイラル
2 吸水ベルト
3 ドラム体
4 脱水R−る
6 外環
8 供給管
13 リターンロール
14 駆動ロール
18 洗浄装置
19 中心軸
DESCRIPTION OF SYMBOLS 1,1a Spiral 2 Water absorption belt 3 Drum body 4 Dehydration R-ru 6 Outer ring 8 Supply pipe 13 Return roll 14 Drive roll 18 Cleaning device 19 Center axis

Claims (4)

周囲にろ過体を張設したドラム体(3)の内部に汚泥を供給し、ドラム体(3)を回転させつつ汚泥を濃縮する吸水ベルト走行式ドラム型濃縮機において、
両端に円環状の外環(6,6)を接続した回転自在な螺旋状のスパイラル(1)と、
スパイラル(1)に掛け回し、吸水体で構成した走行自在な吸水ベルト(2)と、
吸水ベルト(2)を押圧して吸収した水分を排出する脱水ロール(4)と、
吸水ベルト(2)を巻き掛けたスパイラル(1)で構成したドラム体(3)の内部に挿通する汚泥の供給管(8)と、
を備えたこと
を特徴とする吸水ベルト走行式ドラム型濃縮機。
In the water-absorbing belt traveling drum type concentrator for supplying sludge to the inside of the drum body (3) having a filter body stretched around it and concentrating the sludge while rotating the drum body (3),
A rotatable spiral spiral (1) having an annular outer ring (6, 6) connected to both ends;
A water-absorbing belt (2) that can run around the spiral (1) and is composed of a water-absorbing body,
A dewatering roll (4) for discharging the absorbed moisture by pressing the water absorbing belt (2);
A sludge supply pipe (8) inserted into the drum body (3) constituted by the spiral (1) around which the water absorption belt (2) is wound;
A water-absorbing belt traveling type drum type concentrator.
前記吸水ベルト(2)を無端状に構成し、スパイラル(1)と駆動ロール(14)に掛け回すとともに、
吸水ベルト(2)を洗浄するための洗浄装置(18)を備えた
ことを特徴とする請求項1に記載の吸水ベルト走行式ドラム型濃縮機。
The water-absorbing belt (2) is endlessly configured and is wound around the spiral (1) and the drive roll (14).
The water-absorbing belt traveling type drum concentrator according to claim 1, further comprising a cleaning device (18) for cleaning the water-absorbing belt (2).
前記スパイラル(1)の上方に一対のリターンロール(13,13)を配設し、
リターンロール(13,13)の間隔を、
スパイラル(1)の直径以下とする
ことを特徴とする請求項1または2に記載の吸水ベルト走行式ドラム型濃縮機。
A pair of return rolls (13, 13) is disposed above the spiral (1),
The interval between the return rolls (13, 13)
The water-absorbing belt traveling drum type concentrator according to claim 1 or 2, wherein the diameter is equal to or less than the diameter of the spiral (1).
前記供給管(8)を中心軸(19)とし、
中心軸(19)に螺旋状のスパイラル(1a)を巻き掛けた
ことを特徴とする請求項1〜3の何れか1項に記載の吸水ベルト走行式ドラム型濃縮機。
The supply pipe (8) is the central axis (19),
The water-absorbing belt traveling drum type concentrator according to any one of claims 1 to 3, wherein a spiral spiral (1a) is wound around the central shaft (19).
JP2016239092A 2016-12-09 2016-12-09 Water absorption belt traveling drum type concentrator Active JP6756981B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2016239092A JP6756981B2 (en) 2016-12-09 2016-12-09 Water absorption belt traveling drum type concentrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2016239092A JP6756981B2 (en) 2016-12-09 2016-12-09 Water absorption belt traveling drum type concentrator

Publications (2)

Publication Number Publication Date
JP2018094469A true JP2018094469A (en) 2018-06-21
JP6756981B2 JP6756981B2 (en) 2020-09-16

Family

ID=62633938

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2016239092A Active JP6756981B2 (en) 2016-12-09 2016-12-09 Water absorption belt traveling drum type concentrator

Country Status (1)

Country Link
JP (1) JP6756981B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112159010A (en) * 2020-09-24 2021-01-01 湖南诚至环保科技有限公司 Water source pollution treatment method and system
CN112672805A (en) * 2018-12-07 2021-04-16 月岛机械株式会社 Solid-liquid separation device and filter device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112672805A (en) * 2018-12-07 2021-04-16 月岛机械株式会社 Solid-liquid separation device and filter device
CN112159010A (en) * 2020-09-24 2021-01-01 湖南诚至环保科技有限公司 Water source pollution treatment method and system
CN112159010B (en) * 2020-09-24 2023-09-12 湖南诚至环保科技有限公司 Water source pollution treatment method and system

Also Published As

Publication number Publication date
JP6756981B2 (en) 2020-09-16

Similar Documents

Publication Publication Date Title
CN207031231U (en) A kind of split type automation concentration and belt pressing type sludge dewatering equipment
JP2010104892A (en) Solid-liquid separator, filter equipment and solid-liquid separation method
JP6038679B2 (en) Sludge treatment system
JP2018094469A (en) Drum type thickener with travelling water-absorbing belt
JP6109587B2 (en) Sludge dewatering system
CN105040316A (en) Textile fabric fold removing device
JP6703765B2 (en) Drum type concentrator
JP5864306B2 (en) Sludge concentrator
JP6730679B2 (en) Belt-running drum type concentrator
CN201785297U (en) High-efficiency energy-saving belt type sludge concentrating and pressing integrated drying machine
KR101437908B1 (en) Vertical type screw dehydrator
CN204619471U (en) A kind of grid maker
CN207755855U (en) Down wastewater separator
CN104963181A (en) Automatic wrinkle removing and processing device for textile fabrics
CN210438608U (en) Belt type concentration filter press
RU2349367C2 (en) Belt filter press
KR101949946B1 (en) Tube press sludge dewatering device
JP2018094466A (en) Drum type concentrator
CN206896969U (en) Large belt filter press press filtration processing system
CN2481397Y (en) Band type dewatering machine
CN204848622U (en) Drum -type mud squeezes mummification machine
CN104944734B (en) Drum-type sludge pressing desiccation machine
CN201746437U (en) Multi-roll type continuous paired-pressing dehydrator
CN101863607B (en) Multi-roll continuous press dehydrator
KR200412540Y1 (en) Belt press

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20181130

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20190911

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20190918

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20191101

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20200406

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20200410

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: 20200729

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20200811

R150 Certificate of patent or registration of utility model

Ref document number: 6756981

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250