JP2010036078A - Method for driving rotary drum type sludge concentration device - Google Patents

Method for driving rotary drum type sludge concentration device Download PDF

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JP2010036078A
JP2010036078A JP2008199910A JP2008199910A JP2010036078A JP 2010036078 A JP2010036078 A JP 2010036078A JP 2008199910 A JP2008199910 A JP 2008199910A JP 2008199910 A JP2008199910 A JP 2008199910A JP 2010036078 A JP2010036078 A JP 2010036078A
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water pressure
cleaning water
sludge
water
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JP4964200B2 (en
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Hiromiki Wada
浩幹 和田
Yuzuru Nakanishi
譲 中西
Kenichi Shishida
健一 宍田
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Takuma Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for driving a rotary drum type sludge concentration device which can reduce the load of returned water and the output of an electric motor. <P>SOLUTION: The water pressure of cleaning water jetted for cleaning a drum screen 3 is set to low cleaning water pressure lower than the standard water pressure and to high cleaning water pressure higher than the standard water pressure, and the rotary drum type sludge concentration device 1 is driven in such a manner that the cleaning water is usually jetted at the low cleaning water pressure, and the water pressure of the cleaning water is switched from the low cleaning water pressure into the high cleaning water pressure every fixed time. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、下水汚泥等から固形物を分離除去して濃縮する回転ドラム式汚泥濃縮装置の運転方法に関するものである。   The present invention relates to a method for operating a rotary drum type sludge concentrating apparatus that separates and removes solid matter from sewage sludge and the like and concentrates it.

下水汚泥等を処理する際の重要なプロセスとして、汚泥の濃縮工程がある。この濃縮工程は、水処理施設で発生した低濃度の汚泥を固液分離することで濃縮し、処理汚泥量の減量を図るとともに、後段の脱水工程を効果的に機能させるものである。このような汚泥の濃縮を効率的に行うことで、脱水装置の小型化や脱水性能の向上を図ることが可能となる。   As an important process for treating sewage sludge and the like, there is a sludge concentration step. This concentration step concentrates the low-concentration sludge generated in the water treatment facility by solid-liquid separation, thereby reducing the amount of the treated sludge and effectively making the subsequent dewatering step function. By efficiently concentrating such sludge, it is possible to reduce the size of the dehydrator and improve the dewatering performance.

ところで、例えば下水汚泥の濃縮工程に用いられる汚泥濃縮装置として、遠心力を利用して固液分離を行う遠心濃縮装置が知られている。ところが、この遠心濃縮装置は、電動機の消費動力が大きく、またオーバーホール等の維持管理コストが高いといった欠点がある。これに対し、回転ドラム式汚泥濃縮装置(回転ドラム型濃縮機)は、1)消費電力が小さく、電気代が安価である、2)濃縮機構がシンプルで維持管理コストが安価である、3)小規模容量から大規模容量まで処理可能である、4)コンパクトで設置スペースが小さい、といった特徴を有している(特許文献1〜3参照)。   By the way, for example, as a sludge concentrator used in a sewage sludge concentration step, a centrifugal concentrator that performs solid-liquid separation using centrifugal force is known. However, this centrifugal concentrator has the disadvantages that the electric power consumed by the electric motor is large and the maintenance cost such as overhaul is high. On the other hand, the rotary drum type sludge concentrator (rotary drum type concentrator) has 1) low power consumption and low electricity cost 2) simple concentration mechanism and low maintenance cost 3) It can be processed from a small-scale capacity to a large-scale capacity. 4) It is compact and has a small installation space (see Patent Documents 1 to 3).

特開2005−193105号公報JP-A-2005-193105 特開2007−330920号公報JP 2007-330920 A 特開2008−18359号公報JP 2008-18359 A

次に、従来の回転ドラム式汚泥濃縮装置について、本発明の一実施形態を示す図1を用いて説明する。なお、装置のハード構成については、本発明に係る装置も従来装置と基本的に異なるところがない。   Next, a conventional rotary drum type sludge concentrating device will be described with reference to FIG. 1 showing an embodiment of the present invention. As for the hardware configuration of the apparatus, the apparatus according to the present invention is basically not different from the conventional apparatus.

従来の回転ドラム式汚泥濃縮装置(以下、「汚泥濃縮装置」という。)1は、本体フレーム2と、ケーシング内部で水平軸線周りに回転される円筒状のスクリーン(以下、「ドラムスクリーン」という。)3を備えている。ここで、ドラムスクリーン3は、これを支持するため前後左右に設けられた回転支持部をプーリー等の伝達手段を用いて回転させるドラム用電動機4により回転駆動されるようになっている。   A conventional rotating drum type sludge concentrating device (hereinafter referred to as “sludge concentrating device”) 1 is a main body frame 2 and a cylindrical screen (hereinafter referred to as “drum screen”) that is rotated around a horizontal axis within a casing. ) 3 is provided. Here, the drum screen 3 is rotationally driven by a drum electric motor 4 that rotates rotation support portions provided on the front, rear, left, and right sides using a transmission means such as a pulley to support the drum screen 3.

ドラムスクリーン3の下方には分離液受け5が設けられ、この分離液受け5の排出端は分離液排出管6に接続されている。また、ドラムスクリーン3を支持するケーシングの一端側の汚泥投入口7には汚泥投入管8が配され、一方、ケーシングの他端側には汚泥排出口9に連通される固形物排出シュート10が取り付けられ、分離液を分離した後の固形物(汚泥)がその汚泥排出口9を介して固形物排出シュート10から排出される。   A separation liquid receiver 5 is provided below the drum screen 3, and a discharge end of the separation liquid receiver 5 is connected to a separation liquid discharge pipe 6. Also, a sludge inlet tube 8 is disposed at the sludge inlet 7 on one end side of the casing that supports the drum screen 3, while a solid discharge chute 10 communicated with the sludge outlet 9 is provided on the other end side of the casing. The solid matter (sludge) after being attached and separating the separation liquid is discharged from the solid matter discharge chute 10 through the sludge discharge port 9.

前記ドラムスクリーン3は、金属製ウェッジワイヤーが互いに並列に所定の目幅を隔てて水平回転軸方向に配されて、全体として円筒状に形成されてなる構成とされている。ここで、ドラムスクリーン3の適正目幅は被処理物の性状によって異なるが、下水汚泥を対象とする場合には、0.15〜0.5mm程度とされる。   The drum screen 3 has a configuration in which metal wedge wires are arranged in parallel to each other in the horizontal rotation axis direction with a predetermined interval between them, and are formed in a cylindrical shape as a whole. Here, the appropriate mesh width of the drum screen 3 varies depending on the properties of the object to be processed, but is about 0.15 to 0.5 mm when sewage sludge is targeted.

また、前記ドラムスクリーン3の内周面には、一端側の汚泥投入口7から他端側の汚泥排出口9に向けて、螺旋状の汚泥搬送用ガイド部材11が設けられている。   A spiral sludge transport guide member 11 is provided on the inner peripheral surface of the drum screen 3 from the sludge inlet 7 on one end side toward the sludge outlet 9 on the other end side.

汚泥の処理に際しては、濃縮しようとする汚泥に高分子凝集剤が添加され、凝集混和槽でフロック化が行われ、このフロック化した汚泥が汚泥投入管8によってドラムスクリーン3内に投入される。この汚泥がドラムスクリーン3の回転に伴って汚泥搬送用ガイド部材11に沿って固液分離されながら出口側へ搬送される。このとき、フロック状の汚泥はドラムスクリーン3上に残り、汚泥中の液分がドラムスクリーン3のウェッジワイヤー間に形成された排液部からろ過されて汚泥の濃縮処理が行われる。ろ過された液分は分離液受け5を経由して分離液排出管6にて排出され、液分をろ過された後の濃縮汚泥は、ドラムスクリーン3の汚泥排出口9を経由して固形物排出シュート10から排出される。   In the treatment of sludge, a polymer flocculant is added to the sludge to be concentrated, flocked in a flocculent mixing tank, and the flocified sludge is put into the drum screen 3 through the sludge inlet pipe 8. The sludge is transported to the outlet side while being separated into solid and liquid along the sludge transport guide member 11 as the drum screen 3 rotates. At this time, the floc sludge remains on the drum screen 3, and the liquid content in the sludge is filtered from the drainage part formed between the wedge wires of the drum screen 3, and the sludge is concentrated. The filtered liquid is discharged through the liquid receiver 5 through the liquid separator 5, and the concentrated sludge after the liquid is filtered is solid matter through the sludge outlet 9 of the drum screen 3. It is discharged from the discharge chute 10.

ドラムスクリーン3の外周の上方位置にはそのドラムスクリーン3の長手方向に沿って洗浄水供給管12が配され、この洗浄水供給管12に複数個の洗浄水ノズル13が取り付けられている。この洗浄水供給管12には昇圧ポンプ14で昇圧された高圧水が供給され、この高圧水が洗浄水ノズル13からドラムスクリーン3に向けて噴出されることで、ドラムスクリーン3の逆洗が行われる。ここで、ドラムスクリーン3を洗浄するための洗浄水は、洗浄水ノズル13から一定の水圧で噴射される。   A cleaning water supply pipe 12 is disposed at a position above the outer periphery of the drum screen 3 along the longitudinal direction of the drum screen 3, and a plurality of cleaning water nozzles 13 are attached to the cleaning water supply pipe 12. The washing water supply pipe 12 is supplied with high-pressure water boosted by a booster pump 14, and this high-pressure water is ejected from the washing water nozzle 13 toward the drum screen 3, thereby backwashing the drum screen 3. Is called. Here, the cleaning water for cleaning the drum screen 3 is ejected from the cleaning water nozzle 13 at a constant water pressure.

しかしながら、この従来装置においては、ドラムスクリーン3の洗浄を確実に行うためには、余裕を持たせた運転となるため、洗浄水圧もしくは洗浄水量が過多となり、結果として返流水が増加し、水処理の負荷が大きくなるという問題点がある。また、洗浄水圧が過多になることによって、装置全体としての電動機出力が過多となり、ランニングコストの増加を招いてしまうという問題点がある。   However, in this conventional apparatus, in order to perform the cleaning of the drum screen 3 with certainty, the operation is performed with a margin, so that the cleaning water pressure or the amount of the cleaning water becomes excessive, resulting in an increase in the return water and the water treatment. There is a problem that the load on the system becomes large. Further, since the washing water pressure becomes excessive, the motor output as the whole apparatus becomes excessive, which causes an increase in running cost.

本発明は、前述のような問題点に鑑みてなされたもので、返流水負荷および電動機出力を低減することのできる回転ドラム式汚泥濃縮装置の運転方法を提供することを目的とするものである。   The present invention has been made in view of the above-described problems, and an object of the present invention is to provide a method for operating a rotary drum type sludge concentrating device capable of reducing the return water load and the motor output. .

前記目的を達成するために、第1発明による回転ドラム式汚泥濃縮装置の運転方法は、
多数の排液部を有する円筒状のスクリーンを水平軸線周りに回転させながら、そのスクリーンの一端側から投入された汚泥を濃縮する回転ドラム式汚泥濃縮装置の運転方法であって、
前記スクリーンを洗浄するために噴射させる洗浄水の水圧を、標準水圧よりも低い低洗浄水圧と、標準水圧よりも高い高洗浄水圧に設定できるようにし、当該回転ドラム式汚泥濃縮装置を、通常時は前記低洗浄水圧で洗浄水を噴射させて運転するとともに、一定時間置きに洗浄水の水圧を低洗浄水圧から高洗浄水圧に切換えて運転することを特徴とするものである。
In order to achieve the above object, the operation method of the rotary drum type sludge concentrator according to the first invention is
A rotating drum type sludge concentrating device operating method for concentrating sludge introduced from one end of the screen while rotating a cylindrical screen having a large number of drainage portions around a horizontal axis,
The water pressure of the washing water sprayed for washing the screen can be set to a low washing water pressure lower than the standard water pressure and a high washing water pressure higher than the standard water pressure. Is operated by jetting cleaning water at the low cleaning water pressure, and is operated by switching the water pressure of the cleaning water from a low cleaning water pressure to a high cleaning water pressure at regular intervals.

また、第2発明による回転ドラム式汚泥濃縮装置の運転方法は、
多数の排液部を有する円筒状のスクリーンを水平軸線周りに回転させながら、そのスクリーンの一端側から投入された汚泥を濃縮する回転ドラム式汚泥濃縮装置の運転方法であって、
前記スクリーンを洗浄するために噴射させる洗浄水の水量を、標準水量よりも少ない少洗浄水量と、標準水量よりも多い多洗浄水量に設定できるようにし、当該回転ドラム式汚泥濃縮装置を、通常時は前記少洗浄水量で洗浄水を噴射させて運転するとともに、一定時間置きに洗浄水の水量を少洗浄水量から多洗浄水量に切換えて運転することを特徴とするものである。
The operation method of the rotary drum type sludge concentrator according to the second invention is as follows:
A rotating drum type sludge concentrating device operating method for concentrating sludge introduced from one end of the screen while rotating a cylindrical screen having a large number of drainage portions around a horizontal axis,
The amount of cleaning water sprayed to clean the screen can be set to a small amount of cleaning water smaller than the standard amount of water and a large amount of cleaning water larger than the standard amount of water. The operation is performed by injecting the cleaning water with the small amount of cleaning water and switching the amount of cleaning water from a small amount of cleaning water to a large amount of cleaning water at regular intervals.

前記各発明によれば、通常時には低洗浄水圧もしくは少洗浄水量で運転されているので、装置の電動機出力もしくは返流水負荷を低減させることができ、電動機出力の低減に伴って温室効果ガス排出量を削減することができる。また、一定時間置きに実施される高洗浄水圧もしくは多洗浄水量でのスクリーン洗浄により、目詰まりをより確実に解消することができ、濃縮汚泥濃度を増加させることができるとともに、装置の長期にわたる安定運転を行うことが可能となる。   According to each of the above-mentioned inventions, since it is normally operated with a low washing water pressure or a small washing water amount, the motor output or return water load of the apparatus can be reduced, and the greenhouse gas emissions accompanying the reduction of the motor output Can be reduced. In addition, clogging can be eliminated more reliably by screen cleaning with a high cleaning water pressure or a large amount of cleaning water carried out at regular intervals, the concentration of concentrated sludge can be increased, and long-term stability of the equipment can be achieved. It becomes possible to drive.

次に、本発明による回転ドラム式汚泥濃縮装置の運転方法の具体的な実施の形態について、図面を参照しつつ説明する。   Next, specific embodiments of the operation method of the rotating drum type sludge concentrating device according to the present invention will be described with reference to the drawings.

図1には、本発明の一実施形態に係る回転ドラム式汚泥濃縮装置の正面図が示されている。   FIG. 1 is a front view of a rotary drum type sludge concentrating device according to an embodiment of the present invention.

本実施形態の回転ドラム式汚泥濃縮装置(汚泥濃縮装置)1については、従来装置として説明したものと基本的に異なるところがない。したがって、従来装置と共通する部分については説明を省略し、以下、本実施形態に特有の点のみについて説明することとする。   The rotating drum type sludge concentrating device (sludge concentrating device) 1 of the present embodiment is basically not different from that described as the conventional device. Therefore, the description of the parts common to the conventional apparatus will be omitted, and only the points peculiar to the present embodiment will be described below.

本実施形態の汚泥濃縮装置1においては、洗浄水ノズル13から噴出される高圧水によってドラムスクリーン3の逆洗を行う際に、洗浄水供給管12に接続される昇圧ポンプ14の洗浄水圧を制御するコントローラ(電動弁と手動弁を組合わせた制御装置など)15が設けられている。そして、このコントローラ15による制御によって、洗浄水圧を、通常時には標準水圧(例えば0.40MPa)より低い低洗浄水圧(例えば0.20MPa以上)に設定し、一定時間置きに(例えば3時間以内に一度)所定時間だけ(例えば3分間以上)、標準水圧よりも高い高洗浄水圧(例えば0.50MPa以上)に増加させて運転するようにしている。このように低洗浄水圧と高洗浄水圧とを組み合わせることで、全体として洗浄水量を減少させることができ、プラント全体の水処理系での負荷を軽減させることができる。また、通常時には洗浄水圧が低く設定されているので、洗浄水ポンプ(昇圧ポンプ14)の電動機出力も低減させることができる。しかも、洗浄水圧を一時的に高洗浄水圧とすることによって、ドラムスクリーン3の目詰まりをより確実に取り除くことが可能となり、長期にわたる安定運転に寄与することができる。   In the sludge concentrating device 1 of the present embodiment, when the drum screen 3 is back-washed with high-pressure water ejected from the washing water nozzle 13, the washing water pressure of the booster pump 14 connected to the washing water supply pipe 12 is controlled. A controller 15 (such as a control device combining an electric valve and a manual valve) is provided. Under the control of the controller 15, the washing water pressure is normally set to a low washing water pressure (eg, 0.20 MPa or more) lower than the standard water pressure (eg, 0.40 MPa), and is set at regular intervals (eg, once within 3 hours). ) Only for a predetermined time (for example, 3 minutes or more), the operation is performed by increasing the cleaning water pressure higher than the standard water pressure (for example, 0.50 MPa or more). By combining the low washing water pressure and the high washing water pressure in this way, the amount of washing water can be reduced as a whole, and the load on the water treatment system of the entire plant can be reduced. In addition, since the washing water pressure is set to be low at normal times, the electric motor output of the washing water pump (boost pump 14) can also be reduced. In addition, by temporarily setting the cleaning water pressure to a high cleaning water pressure, it is possible to more reliably remove clogging of the drum screen 3 and contribute to stable operation over a long period of time.

本実施形態では、洗浄水圧を低洗浄水圧と高洗浄水圧に切換えて運転するものについて説明したが、洗浄水圧に代えて、洗浄水量を少洗浄水量と多洗浄水量に切換えるようにした実施形態も可能である。また、洗浄水圧と洗浄水量とを組み合わせて制御することも可能である。なお、洗浄水量については少洗浄水量に対して多洗浄水量を1.6倍以上とするのが、濃縮性能の低下を防ぐ上で好ましい。   In the present embodiment, the operation is described with the washing water pressure being switched between the low washing water pressure and the high washing water pressure. However, the embodiment is configured such that the washing water amount is switched to the small washing water amount and the multiple washing water amount instead of the washing water pressure. Is possible. It is also possible to control the cleaning water pressure and the cleaning water amount in combination. As for the amount of washing water, it is preferable that the amount of washing water is 1.6 times or more with respect to the amount of washing water in order to prevent a reduction in concentration performance.

本実施形態では、金属製ウェッジワイヤーを用いたドラムスクリーンについて説明したが、本発明は、例えばパンチングメタルなどの他のドラムスクリーンに対しても適用できるのは言うまでもない。   In the present embodiment, a drum screen using a metal wedge wire has been described, but it goes without saying that the present invention can also be applied to other drum screens such as punching metal.

本発明の一実施形態に係る回転ドラム式汚泥濃縮装置の正面図The front view of the rotating drum type sludge concentration apparatus which concerns on one Embodiment of this invention.

符号の説明Explanation of symbols

1 回転ドラム式汚泥濃縮装置
3 ドラムスクリーン(円筒状のスクリーン)
5 分離液受け
6 分離液排出管
7 汚泥投入口
8 汚泥投入管
9 汚泥排出口
10 固形物排出シュート
11 汚泥搬送用ガイド部材
12 洗浄水供給管
13 洗浄水ノズル
14 昇圧ポンプ
15 コントローラ
1 Rotating drum type sludge concentrator 3 Drum screen (cylindrical screen)
5 Separation liquid receiver 6 Separator liquid discharge pipe 7 Sludge inlet 8 Sludge inlet pipe 9 Sludge outlet 10 Solid discharge chute 11 Sludge transport guide member 12 Washing water supply pipe 13 Washing water nozzle 14 Booster pump 15 Controller

Claims (2)

多数の排液部を有する円筒状のスクリーンを水平軸線周りに回転させながら、そのスクリーンの一端側から投入された汚泥を濃縮する回転ドラム式汚泥濃縮装置の運転方法であって、
前記スクリーンを洗浄するために噴射させる洗浄水の水圧を、標準水圧よりも低い低洗浄水圧と、標準水圧よりも高い高洗浄水圧に設定できるようにし、当該回転ドラム式汚泥濃縮装置を、通常時は前記低洗浄水圧で洗浄水を噴射させて運転するとともに、一定時間置きに洗浄水の水圧を低洗浄水圧から高洗浄水圧に切換えて運転することを特徴とする回転ドラム式汚泥濃縮装置の運転方法。
A rotating drum type sludge concentrating device operating method for concentrating sludge introduced from one end of the screen while rotating a cylindrical screen having a large number of drainage portions around a horizontal axis,
The water pressure of the washing water sprayed for washing the screen can be set to a low washing water pressure lower than the standard water pressure and a high washing water pressure higher than the standard water pressure. Is operated by jetting wash water at the low wash water pressure, and is operated by switching the wash water pressure from low wash water pressure to high wash water pressure at regular intervals. Method.
多数の排液部を有する円筒状のスクリーンを水平軸線周りに回転させながら、そのスクリーンの一端側から投入された汚泥を濃縮する回転ドラム式汚泥濃縮装置の運転方法であって、
前記スクリーンを洗浄するために噴射させる洗浄水の水量を、標準水量よりも少ない少洗浄水量と、標準水量よりも多い多洗浄水量に設定できるようにし、当該回転ドラム式汚泥濃縮装置を、通常時は前記少洗浄水量で洗浄水を噴射させて運転するとともに、一定時間置きに洗浄水の水量を少洗浄水量から多洗浄水量に切換えて運転することを特徴とする回転ドラム式汚泥濃縮装置の運転方法。
A rotating drum type sludge concentrating device operating method for concentrating sludge introduced from one end of the screen while rotating a cylindrical screen having a large number of drainage portions around a horizontal axis,
The amount of cleaning water sprayed to clean the screen can be set to a small amount of cleaning water smaller than the standard amount of water and a large amount of cleaning water larger than the standard amount of water. The operation of the rotary drum type sludge concentrator is characterized in that it is operated by injecting the cleaning water with the small amount of cleaning water and switching the amount of cleaning water from a small amount of cleaning water to a large amount of cleaning water at regular intervals. Method.
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