JP4487908B2 - Concentrator for sludge - Google Patents

Concentrator for sludge Download PDF

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JP4487908B2
JP4487908B2 JP2005334198A JP2005334198A JP4487908B2 JP 4487908 B2 JP4487908 B2 JP 4487908B2 JP 2005334198 A JP2005334198 A JP 2005334198A JP 2005334198 A JP2005334198 A JP 2005334198A JP 4487908 B2 JP4487908 B2 JP 4487908B2
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screen
sludge
concentrating
filtration
concentration
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JP2007136346A5 (en
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充志 犬塚
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Ishigaki Co Ltd
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Description

この発明は、下水汚泥や産業排水等のフロックを生成させた凝集汚泥から、ろ液を分離して濃縮させる濃縮装置の改良に関する。   The present invention relates to an improvement of a concentrating device for separating and concentrating a filtrate from agglomerated sludge generated with flocs such as sewage sludge and industrial wastewater.

従来、スクリュープレスやベルトプレスを使用して原液を圧搾脱水、或いは加圧脱水する場合、濃度の薄い原液に凝集剤を供給してフロックを造粒させ、前処理操作として濃縮装置を使用することが良く知られている。従来から使用している濃縮装置としては、遠心濃縮機、常圧浮上濃縮装置などがある。遠心濃縮機は大量処理が可能となるが、高速回転で処理を行うため、設備電力が大きくなる。高速回転のため磨耗しやすく、消耗品等のメンテナンス費用も高くなる。常圧浮上濃縮装置は、メンテナンス費用は安くなるが、長い処理時間を要する。濃縮装置本体が大きくて付帯設備も多く、設置スペースが大きくなる。   Conventionally, when a stock solution is squeezed or dehydrated using a screw press or a belt press, floc is granulated by supplying a flocculant to the stock solution having a low concentration, and a concentrator is used as a pretreatment operation. Is well known. Conventionally used concentrators include centrifugal concentrators and atmospheric pressure flotation concentrators. Centrifugal concentrators can be processed in large quantities, but because the processing is performed at high speed, the equipment power is increased. It is easy to wear due to high-speed rotation, and maintenance costs for consumables and the like are high. The atmospheric pressure levitation concentrator reduces the maintenance cost, but requires a long processing time. The concentrator main body is large and there are many incidental facilities, so the installation space becomes large.

従来の円環状のケーシングの両面にスクリーンを配設して内部にろ過室を形成した先行技術としては、環状のろ過室に回転自在なスクリーンを配設し、ろ過室の環状周壁から汚泥を導入して、スクリーンの回転摩擦力により汚泥を圧縮脱水し、環状周壁からケーキを排出する回転式圧縮ろ過機は、例えば、特許文献1に記載してあるように公知である。また、環状のろ過室にスクリーンを張設し、原液供給路を備えた駆動軸に羽根を止着して、原液の圧入圧と羽根の回転力によりろ液を分離して、環状周壁からケーキを排出する連続圧搾脱水装置も、例えば、特許文献2に記載してあるように,特許出願人が提案している。そして、従来のスクリュープレス等に供給する汚泥の濃縮装置としては、円筒状のタンクの中心部に、螺旋翼を巻き回したスクリーンドラムを垂設した濃縮装置も、例えば、特許文献3に記載してあるように、特許出願人が提案している。   As a prior art in which a screen is formed on both sides of a conventional annular casing and a filtration chamber is formed inside, a rotatable screen is installed in the annular filtration chamber, and sludge is introduced from the annular peripheral wall of the filtration chamber. A rotary compression filter that compresses and dehydrates sludge by the rotational frictional force of the screen and discharges the cake from the annular peripheral wall is known, for example, as described in Patent Document 1. In addition, a screen is stretched in the annular filtration chamber, the blade is fixed to the drive shaft provided with the stock solution supply path, and the filtrate is separated by the press-fitting pressure of the stock solution and the rotational force of the blade. The patent applicant has also proposed a continuous squeezing and dewatering device that discharges slag, as described in Patent Document 2, for example. As a sludge concentrating device to be supplied to a conventional screw press or the like, a concentrating device in which a screen drum having spiral blades wound around a central portion of a cylindrical tank is also described in, for example, Patent Document 3. As proposed, the patent applicant has proposed.

特開2001−113109号公報(請求項1、段落番号0014乃至段落番号0017、図7)JP 2001-113109 A (Claim 1, paragraph number 0014 to paragraph number 0017, FIG. 7) 特許第3548888号公報(請求項1、図1及び図2)Japanese Patent No. 3548888 (Claim 1, FIG. 1 and FIG. 2) 実公平8−10348号公報(請求項1、図4)Japanese Utility Model Publication No. 8-10348 (Claim 1, FIG. 4)

従来のスクリーンと内輪スペーサを低速で回転させる回転式圧縮ろ過機は、エネルギー消費量と騒音が小さくなる利点があるが、スクリーンの回転摩擦力により圧縮するため処理時間が長くなる。また、従来の羽根を回転させる連続圧搾脱水装置は、原液の圧入圧と羽根の回転力によりろ液を分離するため、簡単な構造となり設置面積が小さくなる。ろ過効率が高く、低速運転で使用されるものであるが、濃縮装置に使用するためには、スクリーンの目詰まりの問題がある。そして、円筒状のタンクの中心部に、螺旋翼を巻き回したスクリーンドラムを垂設した濃縮装置は、後段のスクリュープレスやベルトプレスにおいて、高圧搾脱水が可能となるが、原液の性状によっては、洗浄水だけではスクリーンドラムの目詰まりが解消されない恐れがある。本願発明は、上記従来の円環状のケーシングの両面にスクリーンを配設した脱水装置と従来の濃縮装置の利点を応用して、濃縮効率を高め、目詰まりの解消もできる汚泥等の濃縮装置を提供する。   A conventional rotary compression filter that rotates the screen and the inner ring spacer at a low speed has the advantage of reducing energy consumption and noise. However, since the compression is performed by the rotational frictional force of the screen, the processing time becomes longer. In addition, since the conventional continuous dehydration device for rotating the blades separates the filtrate by the press-fitting pressure of the stock solution and the rotational force of the blades, the structure is simple and the installation area is reduced. Although the filtration efficiency is high and it is used at low speed operation, there is a problem of clogging of the screen for use in a concentrator. The concentrator with a screen drum with spiral blades wound around the center of a cylindrical tank allows high-pressure squeezing and dehydration in subsequent screw presses and belt presses, depending on the nature of the stock solution. There is a risk that clogging of the screen drum will not be resolved with just washing water. The present invention is a sludge and other concentrator that can improve the concentrating efficiency and eliminate clogging by applying the advantages of the conventional dewatering device having screens arranged on both sides of the conventional annular casing and the conventional concentrating device. provide.

この発明に係わる汚泥等の濃縮装置の要旨は、円環状のケーシングの両面に回転自在なスクリーンを配設して内部に濃縮室を形成し、ケーシングの上部にスクリーンの回転方向に拡開する凝集汚泥の供給口と、その下部に濃縮汚泥の排出口を配設すると共に、濃縮室を放射状に分割する回転羽根を配設し、スクリーンと回転羽根を差速回転させるもので、濃縮室の供給部近傍では低濃度による濃縮濃度が急速に進行するが、回転方向に拡開する供給口から分離したろ液分だけ汚泥が供給できる。濃縮の進行に伴い増加する回転羽根で分割する分割ろ室の空隙が少なくなり、スクリーンの無効面積を減少させることができる。そして、濃縮濃度の調整は、回転羽根とスクリーンの差速回転の回転数を調整すれば、濃縮室の滞留時間とろ材再生回数により調整することができ、小さいろ過面積で高い処理能力が得られる。   The gist of the concentrating device for sludge and the like according to the present invention is agglomeration in which a rotatable screen is provided on both sides of an annular casing to form a concentrating chamber inside, and the upper part of the casing expands in the rotating direction of the screen. A sludge supply port and a concentrated sludge discharge port at the bottom, and rotary blades that divide the concentrating chamber radially are arranged to rotate the screen and rotary blades at a different speed. In the vicinity of the part, the concentration by low concentration proceeds rapidly, but sludge can be supplied only by the filtrate separated from the supply port that expands in the rotation direction. The voids in the divided filter chamber divided by the rotating blades that increase as the concentration progresses are reduced, and the ineffective area of the screen can be reduced. The concentration concentration can be adjusted by adjusting the residence time of the concentrating chamber and the number of times of filter medium regeneration by adjusting the rotational speed of the rotary blade and the differential speed rotation of the screen, and high processing capacity can be obtained with a small filtration area. .

回転羽根の羽根板の両側面にスクレーパを止着してスクリーンの内周面に摺接させ、濃縮汚泥排出ゾーンの後方部のスクリーンの外周面に洗浄管を対設したもので、スクリーンに捕捉されたろ滓をスクレーパで掻き取って、常にろ過面の再生が行える。そして、濃縮汚泥排出ゾーンの濃縮汚泥を排出したスクリーンに洗浄水を噴射するので、スクリーンに付着する残渣を洗い流し、内側に抜けた洗浄排水を濃縮汚泥に混入させて排出できる。残渣がスクリーンのろ過孔内部に滞留することがなく、ろ過面積を減少させることがない。   A scraper is fixed to both sides of the blades of the rotating blades and brought into sliding contact with the inner peripheral surface of the screen, and a cleaning pipe is provided on the outer peripheral surface of the screen at the rear of the concentrated sludge discharge zone. The filter cake is scraped off with a scraper to always regenerate the filtration surface. And since wash water is sprayed on the screen which discharged | emitted the concentrated sludge of the concentrated sludge discharge zone, the residue adhering to a screen can be washed away, and the washing waste_water | drain which went inside can be mixed and discharged to a concentrated sludge. The residue does not stay inside the filtration hole of the screen, and the filtration area is not reduced.

本願発明は上記のように構成してあり、水抜け分の追加供給を考慮して供給口を大きく開口したので、スクリーンの無効面積を減少させることができる。スクレーパと洗浄管でスクリーンの両面からろ過面を再生させるので、常にろ過面の再生が行われ、目詰まりによるろ過性能の低下がなく、ろ過面積を減少させることがない。そして、洗浄管の洗浄水圧を高くすれば、高濃度に濃縮されて残留する濃縮汚泥でもスクリーンから洗い流すことができる。   The invention of the present application is configured as described above, and the supply opening is greatly opened in consideration of the additional supply of water leakage, so that the ineffective area of the screen can be reduced. Since the filtration surface is regenerated from both sides of the screen by the scraper and the washing tube, the filtration surface is always regenerated, the filtration performance is not deteriorated by clogging, and the filtration area is not reduced. If the washing water pressure in the washing tube is increased, even the concentrated sludge remaining after being concentrated to a high concentration can be washed away from the screen.

本願発明に係わる汚泥等の濃縮装置を図面に基づき詳述すると、先ず、図1はこの発明に係る濃縮装置の横断面図であって、濃縮装置1は、円環状のケーシング2の両面に回転自在なスクリーン3、3を配設して、内部に濃縮室4を形成してある。スクリーン3はパンチングメタルやウエッジワイヤーなどの金属ろ材で円板状に形成してある。スクリーン3の中心部を貫通して濃縮室4に配設した羽根回転軸5に、複数枚の平板状の羽根板6・・・を放射状に配設した回転羽根7が嵌着してあり、濃縮室4を均等に分割した分割ろ室8・・・を形成してある。ケーシング2の上部に四角形状の供給口9とその下部に濃縮汚泥の排出口10を配設してあり、供給口9は投入間口を回転方向に大きく開口して、凝集汚泥供給ゾーンAを広くしてある。水抜け分の追加供給を考慮する供給口9は、スクリーン3の直径の1/2〜1/3にするのが好ましい。凝集汚泥供給ゾーンAを広くすれば、濃縮室4の供給口9近傍の供給汚泥量が多くなり、供給部近傍での分離したろ液分だけ汚泥が供給される。濃縮の進行に伴い増加する分割ろ室8の空隙が少なくなり、スクリーン3の無効面積を減少させることができる。   The concentration device for sludge and the like according to the present invention will be described in detail with reference to the drawings. First, FIG. 1 is a cross-sectional view of the concentration device according to the present invention, and the concentration device 1 rotates on both sides of an annular casing 2. Free screens 3 and 3 are arranged, and a concentration chamber 4 is formed inside. The screen 3 is formed in a disk shape with a metal filter medium such as punching metal or wedge wire. Rotary blades 7 in which a plurality of flat blade plates 6... Are radially attached to blade rotation shafts 5 that pass through the center of the screen 3 and are disposed in the concentration chamber 4. Divided filter chambers 8 are formed by dividing the concentration chamber 4 equally. A rectangular supply port 9 is provided at the upper part of the casing 2 and a discharge port 10 for concentrated sludge is provided at the lower part thereof. The supply port 9 has a large opening in the rotation direction to widen the coagulated sludge supply zone A. It is. The supply port 9 considering the additional supply of water leakage is preferably set to 1/2 to 1/3 of the diameter of the screen 3. If the aggregated sludge supply zone A is widened, the amount of supplied sludge near the supply port 9 of the concentrating chamber 4 increases, and sludge is supplied by the amount of filtrate separated in the vicinity of the supply unit. The voids in the divided filter chamber 8 that increase with the progress of concentration are reduced, and the ineffective area of the screen 3 can be reduced.

図2は濃縮装置の斜視図であって、スクリーン駆動軸11に駆動ギヤー12が嵌着してあり、この駆動ギヤー12をスクリーン3の外周面に噛合せてある。スクリーン3をケーシング2の側面を摺接しながら、スクリーン3と回転羽根7を反対方向に回転させるようにしてある。濃縮濃度の調整は、スクリーン3と回転羽根7の回転数を調整すれば、濃縮室4の滞留時間とろ材再生回数により調整することができ、小さいろ過面積で高い処理能力が得られる。なお、スクリーン3と回転羽根7を同方向に速度差を与えて回転させてもよいものである。   FIG. 2 is a perspective view of the concentrating device, in which a drive gear 12 is fitted on the screen drive shaft 11, and this drive gear 12 is meshed with the outer peripheral surface of the screen 3. While the screen 3 is in sliding contact with the side surface of the casing 2, the screen 3 and the rotary blade 7 are rotated in opposite directions. The concentration concentration can be adjusted by adjusting the residence time of the concentration chamber 4 and the number of times of filter medium regeneration by adjusting the number of rotations of the screen 3 and the rotary blade 7, and a high processing capacity can be obtained with a small filtration area. The screen 3 and the rotary blade 7 may be rotated by giving a speed difference in the same direction.

図3は濃縮室の縦断面図であって、回転羽根7の羽根板6の両側面にスクレーパ13が止着してあり、スクリーン3の内周面に摺接してある。スクリーン3のろ過面に捕捉された固形物をスクレーパ13で掻き取るようにしてある。図2に示すように、濃縮汚泥排出ゾーンBの後方部のスクリーン3の外周面に洗浄管14が配設してあり、排出口10から濃縮汚泥を排出したスクリーン3の外周面に洗浄水を噴射するので、スクリーン3のろ過孔を貫通した洗浄水がスクリーン3のろ過面に付着する残渣を洗い流し、内側に抜けた洗浄排水を濃縮汚泥に混ぜて排出させる。スクリーン3のろ過面にろ滓が滞留することがなく、ろ過面積を減少させることがない。スクリーン3のろ過面に捕捉された固形物をスクレーパ13で掻き取って、スクリーン3の外周面から洗浄水を噴射するので、常にろ過面の再生が行われ、目詰まりによるろ過性能の低下がない。なお、洗浄管14の洗浄水圧を高くすれば、高濃度に濃縮されてろ材孔に残留する濃縮汚泥でもスクリーン3から洗い流すことができる。   FIG. 3 is a longitudinal sectional view of the concentrating chamber. The scraper 13 is fixed to both side surfaces of the blade 6 of the rotary blade 7 and is in sliding contact with the inner peripheral surface of the screen 3. The solid matter trapped on the filtration surface of the screen 3 is scraped off by the scraper 13. As shown in FIG. 2, a cleaning pipe 14 is disposed on the outer peripheral surface of the screen 3 at the rear portion of the concentrated sludge discharge zone B, and cleaning water is supplied to the outer peripheral surface of the screen 3 from which the concentrated sludge has been discharged from the discharge port 10. Since the spraying is performed, the washing water penetrating the filtration hole of the screen 3 ishes away the residue adhering to the filtration surface of the screen 3, and the washing drainage drained inside is mixed with the concentrated sludge and discharged. Filter cake does not stay on the filtration surface of the screen 3, and the filtration area is not reduced. Since the solid matter trapped on the filtration surface of the screen 3 is scraped off by the scraper 13 and the washing water is sprayed from the outer peripheral surface of the screen 3, the filtration surface is always regenerated and the filtration performance is not deteriorated due to clogging. . If the washing water pressure in the washing tube 14 is increased, the concentrated sludge that is concentrated to a high concentration and remains in the filter medium hole can be washed away from the screen 3.

本発明に係わる汚泥等の濃縮装置は、ケーシングの上部に回転方向に大きく開口する凝集汚泥の供給口を設け、濃縮汚泥を排出した濃縮汚泥排出ゾーンの後方部のスクリーンの外周面に洗浄管を対設し、スクリーンと回転羽根を差速回転させるので、回転羽根で分割する分割ろ室の空隙が少なくなり、スクリーンの無効面積を減少させることができる。そして、スクレーパと洗浄水でスクリーンの両面からろ過面を再生させるので、常にろ過面の再生が行われ、目詰まりによるろ過性能の低下がなく、ろ過面積を減少させることがない。従って、下水汚泥や産業排水などの凝集汚泥の濃縮装置として適するもので、後段に設置するスクリュープレスやベルトプレスの高圧搾脱水が可能となる。   The concentration device for sludge and the like according to the present invention has a supply port for agglomerated sludge that opens largely in the rotational direction at the upper part of the casing, and a cleaning pipe is provided on the outer peripheral surface of the screen at the rear of the concentrated sludge discharge zone where the concentrated sludge is discharged. Since the screen and the rotating blades are rotated at a differential speed, the space between the divided filter chambers divided by the rotating blades is reduced, and the ineffective area of the screen can be reduced. Since the filtration surface is regenerated from both sides of the screen with the scraper and the washing water, the filtration surface is always regenerated, the filtration performance is not deteriorated due to clogging, and the filtration area is not reduced. Therefore, it is suitable as a concentrating device for coagulated sludge such as sewage sludge and industrial wastewater, and enables high-pressure squeezing and dehydration of a screw press or a belt press installed in the subsequent stage.

本願発明に係わる汚泥等の濃縮装置の横断面図である。It is a cross-sectional view of a concentration device for sludge and the like according to the present invention. 同じく、濃縮装置の斜視図である。Similarly, it is a perspective view of a concentration apparatus. 同じく、濃縮装置の縦断面図である。Similarly, it is a longitudinal sectional view of the concentrating device.

符号の説明Explanation of symbols

2 ケーシング
3 スクリーン
4 濃縮室
6 羽根板
7 回転羽根
9 供給口
10 排出口
13 スクレーパ
14 洗浄管
B 濃縮汚泥排出ゾーン
2 Casing 3 Screen 4 Concentration chamber 6 Blade plate 7 Rotating blade 9 Supply port 10 Discharge port 13 Scraper 14 Washing tube B Concentrated sludge discharge zone

Claims (2)

円環状のケーシング(2)の両面に回転自在なスクリーン(3、3)を配設して内部に濃縮室(4)を形成し、ケーシング(2)の上部にスクリーン(3)の回転方向に拡開する凝集汚泥の供給口(9)と、その下部に濃縮汚泥の排出口(10)を配設すると共に、濃縮室(4)を放射状に分割する回転羽根(7)を配設し、スクリーン(3)と回転羽根(7)を差速回転させることを特徴とする汚泥等の濃縮装置。   Rotating screens (3, 3) are arranged on both sides of the annular casing (2) to form a concentrating chamber (4) inside, and in the rotational direction of the screen (3) above the casing (2). The aggregated sludge supply port (9) to be expanded and the concentrated sludge discharge port (10) to the lower portion thereof are disposed, and the rotary blades (7) for radially dividing the concentration chamber (4) are disposed, An apparatus for concentrating sludge or the like, characterized in that the screen (3) and the rotating blade (7) are rotated at a differential speed. 上記回転羽根(7)の羽根板(6)の両側面にスクレーパ(13、13)を止着してスクリーン(3)の内周面に摺接させ、濃縮汚泥排出ゾーン(B)の後方部のスクリーン(3)の外周面に洗浄管(14)を対設したことを特徴とする請求項1に記載の汚泥等の濃縮装置。   A scraper (13, 13) is fixed to both side surfaces of the blade (6) of the rotary blade (7) and slidably contacted with the inner peripheral surface of the screen (3), and the rear portion of the concentrated sludge discharge zone (B). The apparatus for concentrating sludge and the like according to claim 1, wherein a cleaning pipe (14) is provided on the outer peripheral surface of the screen (3).
JP2005334198A 2005-11-18 2005-11-18 Concentrator for sludge Expired - Fee Related JP4487908B2 (en)

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JP2005334198A JP4487908B2 (en) 2005-11-18 2005-11-18 Concentrator for sludge

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CN108176118B (en) * 2018-02-26 2023-12-05 无锡华盛橡胶新材料科技股份有限公司 Vacuum filter for insoluble sulfur solid-liquid separation
CN108862738A (en) * 2018-08-17 2018-11-23 重庆工业职业技术学院 Sewage disposal system
KR102574238B1 (en) * 2021-11-17 2023-09-05 (주)필텍코리아시스템 Disk filter type strainer
CN116272031B (en) * 2023-01-31 2023-08-18 滨州金淼水质检测有限公司 Large-particle impurity filtering device for water quality detection
CN116943320B (en) * 2023-09-18 2023-12-05 中国热带农业科学院农产品加工研究所 Centrifugal filtration equipment of pineapple fruit vinegar stoste production

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