JP2011031168A - Sludge digestion apparatus - Google Patents

Sludge digestion apparatus Download PDF

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JP2011031168A
JP2011031168A JP2009179409A JP2009179409A JP2011031168A JP 2011031168 A JP2011031168 A JP 2011031168A JP 2009179409 A JP2009179409 A JP 2009179409A JP 2009179409 A JP2009179409 A JP 2009179409A JP 2011031168 A JP2011031168 A JP 2011031168A
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sludge
tank
draft tube
pipe
heating
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Takuzo Kinoshita
卓三 木下
Hidejiro Hayamizu
秀次郎 速水
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Furukawa Industrial Machinery Systems Co Ltd
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Furukawa Industrial Machinery Systems Co Ltd
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Priority to JP2009179409A priority Critical patent/JP2011031168A/en
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Abstract

<P>PROBLEM TO BE SOLVED: To provide an indirect heating sludge digestion apparatus whose equipment cost is lower than that of conventional apparatuses. <P>SOLUTION: An outer pipe 28 is disposed outside a draft tube 2 to form an outside passage between the draft tube 2 and the outer pipe 28. A heating medium introduction pipe 41 and a heating medium delivery pipe 42 are connected to the outer pipe 28. In a part where the outer pipe 28 is arranged, sludge passes through the inside of the draft tube 2 and a heating medium passes through the outside passage, thereby heating the sludge in the draft tube 2. <P>COPYRIGHT: (C)2011,JPO&amp;INPIT

Description

この発明は、下水処理等の過程で発生する汚泥の消化(有機物の嫌気性分解)工程で使用される汚泥消化装置に関する。   The present invention relates to a sludge digester used in a process of digesting sludge (anaerobic decomposition of organic matter) generated in a process such as sewage treatment.

汚泥消化槽で汚泥を消化する工程を行う際には、槽内の汚泥を底部に堆積させないように撹拌するとともに、槽内の汚泥を適温に加熱する必要がある。
消化槽内の汚泥の撹拌方法に関しては、例えば、消化槽内の中心に鉛直方向に延びるドラフトチューブ(縦管)を設け、ドラフトチューブ内に設置した攪拌機で槽内の汚泥をドラフトチューブ内に導いて循環させることが行われている。
特許文献1に記載されている例では、スクリューポンプのスクリュー羽根をドラフトチューブ内の上端部に配置し、その回転軸を作動させるモータを槽外に配置している。そして、モータの作動により、槽内の汚泥を、下端開口(または上端開口)からドラフトチューブ内に導入し、上端開口(または下端開口)から導出して循環させている。
When performing the process of digesting sludge in the sludge digestion tank, it is necessary to stir so that the sludge in the tank does not accumulate on the bottom and to heat the sludge in the tank to an appropriate temperature.
Regarding the method of stirring sludge in the digestion tank, for example, a draft tube (vertical tube) extending in the vertical direction is provided at the center of the digestion tank, and the sludge in the tank is guided into the draft tube with a stirrer installed in the draft tube. It is done to circulate.
In the example described in Patent Document 1, the screw blade of the screw pump is arranged at the upper end portion in the draft tube, and the motor for operating the rotating shaft is arranged outside the tank. And by the action | operation of a motor, the sludge in a tank is introduce | transduced in a draft tube from a lower end opening (or upper end opening), is derived | led-out from the upper end opening (or lower end opening), and is circulated.

消化槽内の汚泥の加熱方法としては、例えば、特許文献2に記載されているように、槽内に熱源を入れて加熱する直接法と、槽内の汚泥を外部に出して槽内に戻す循環管を設けて、この循環管内の汚泥を熱交換器で加熱する間接法がある。
直接法は、例えば図3に示すように、汚泥5を入れた槽1の上部に吹き込み管6を設けて、ボイラ設備等から発生した蒸気を槽1内の汚泥5に吹き込む方法である。この方法には、蒸気を入れることで消化槽内の汚泥が水で薄められて、汚泥濃度が低下するという問題点がある。
As a method for heating the sludge in the digestion tank, for example, as described in Patent Document 2, a direct method in which a heat source is put in the tank and heated, and the sludge in the tank is taken out and returned to the tank. There is an indirect method in which a circulation pipe is provided and the sludge in the circulation pipe is heated by a heat exchanger.
For example, as shown in FIG. 3, the direct method is a method in which a blowing pipe 6 is provided in the upper part of the tank 1 in which the sludge 5 is put, and steam generated from boiler equipment or the like is blown into the sludge 5 in the tank 1. This method has a problem in that the sludge in the digestion tank is diluted with water by adding steam, and the sludge concentration decreases.

なお、図3において、符号2はドラフトチューブを、符号31はスクリューポンプの回転軸を、符号32はスクリューポンプのモータ部を、それぞれ示す。
間接法では、例えば図4に示すように、撹拌のために設けたドラフトチューブ2とは別に、加熱のための循環経路7を設けている。この例では、槽1の壁部11を貫通して槽内から槽外まで配置された一対の横管71,72と、両横管を槽外で接続する縦管73とを配置し、出側の横管72と縦管73との間にポンプ74を設け、縦管73のポンプ74と入側の横管71との間の部分に熱交換器4を設けている。
In FIG. 3, reference numeral 2 indicates a draft tube, reference numeral 31 indicates a rotating shaft of the screw pump, and reference numeral 32 indicates a motor part of the screw pump.
In the indirect method, for example, as shown in FIG. 4, a circulation path 7 for heating is provided separately from the draft tube 2 provided for stirring. In this example, a pair of horizontal pipes 71 and 72 that pass through the wall portion 11 of the tank 1 and are arranged from the inside of the tank to the outside of the tank, and a vertical pipe 73 that connects both the horizontal pipes outside the tank are arranged. A pump 74 is provided between the side horizontal pipe 72 and the vertical pipe 73, and the heat exchanger 4 is provided in a portion of the vertical pipe 73 between the pump 74 and the inlet side horizontal pipe 71.

図4の方法では、槽外に配置された配管内の汚泥を熱交換器で加熱しているため、熱交換器の熱源としてボイラ設備等から発生した蒸気を利用した場合でも、蒸気そのものは汚泥に入らないことから、消化槽内の汚泥濃度は低下しない。しかし、この方法には、直接法と比較して設備コストが高くなるという問題点がある。   In the method of FIG. 4, since the sludge in the piping arranged outside the tank is heated by the heat exchanger, even when steam generated from boiler equipment or the like is used as the heat source of the heat exchanger, the steam itself is sludge. The sludge concentration in the digestion tank does not decrease. However, this method has a problem that the equipment cost is higher than the direct method.

特公昭59−46654号公報Japanese Patent Publication No.59-46654 特開平5−269496号公報Japanese Patent Laid-Open No. 5-269596

この発明の課題は、消化槽内の汚泥を、槽内に設置されたドラフトチューブ内に導いて循環させることで撹拌が行われ、消化槽内の汚泥の加熱が間接法で行われる汚泥消化装置であって、従来の間接加熱式汚泥消化装置と比較して設備コストが低いものを提供することである。   An object of the present invention is to introduce sludge in a digestion tank into a draft tube installed in the tank and circulate it so that stirring is performed and the sludge in the digestion tank is heated by an indirect method. And it is providing the thing whose installation cost is low compared with the conventional indirect heating type sludge digester.

上記課題を解決するために、この発明の汚泥消化装置は、汚泥を入れる槽と、槽内に配置されたドラフトチューブと、を備え、前記槽内の汚泥を前記ドラフトチューブ内に導いて循環させることで、槽内の汚泥を撹拌する汚泥消化装置であって、前記ドラフトチューブに、内側に汚泥を通し、外側に熱媒体を通す二重管構造部を設けたことを特徴とする。
この発明の汚泥消化装置では、汚泥を撹拌するために設けたドラフトチューブの前記二重管構造部で、熱媒体により汚泥が加熱されるため、撹拌のための循環経路とは別に加熱のための循環経路を設けている従来の間接加熱式汚泥消化装置と比較して、設備コストが低く抑えられる。また、加熱された汚泥が槽内に戻されて撹拌流を形成するため、槽内全体の加熱が効率よく行われる。
In order to solve the above-mentioned problems, a sludge digesting apparatus of the present invention comprises a tank for containing sludge and a draft tube arranged in the tank, and guides and circulates the sludge in the tank into the draft tube. Thus, a sludge digesting apparatus for stirring the sludge in the tank is characterized in that the draft tube is provided with a double pipe structure part through which sludge passes inside and a heat medium passes outside.
In the sludge digesting apparatus of the present invention, the sludge is heated by the heat medium in the double tube structure portion of the draft tube provided for stirring the sludge, so that the heating is performed separately from the circulation path for stirring. Compared with a conventional indirectly heated sludge digester provided with a circulation path, the equipment cost can be kept low. Further, since the heated sludge is returned into the tank to form a stirring flow, the entire tank is efficiently heated.

この発明の汚泥消化装置は、消化槽内の汚泥を、槽内に配置されたドラフトチューブ内に導いて循環させることで撹拌が行われ、消化槽内の汚泥の加熱が間接法で行われる汚泥消化装置であって、従来の間接加熱式汚泥消化装置と比較して設備コストが低く、槽内全体の加熱効率が高いものとなる。   The sludge digester of the present invention is a sludge in which the sludge in the digestion tank is stirred by being guided and circulated in a draft tube disposed in the tank, and the sludge in the digestion tank is heated by an indirect method. Compared with the conventional indirect heating sludge digester, the equipment cost is low and the heating efficiency of the entire tank is high.

この発明の実施形態に相当する汚泥消化装置を示す概略構成図である。It is a schematic block diagram which shows the sludge digestion apparatus corresponded to embodiment of this invention. 図1のA−A断面図である。It is AA sectional drawing of FIG. 従来の直接加熱式の汚泥消化装置を示す概略構成図である。It is a schematic block diagram which shows the conventional direct heating type sludge digester. 従来の間接加熱式の汚泥消化装置を示す概略構成図である。It is a schematic block diagram which shows the conventional indirect heating type sludge digester.

以下、この発明の実施形態について説明する。
図1は、この実施形態の汚泥消化装置を示す概略構成図であって、汚泥を入れる槽が奥行き方向中心での断面図となっている。図2は図1のA−A断面図である。
図1に示すように、この汚泥消化装置は、汚泥を入れる槽1と、槽1内に配置されたドラフトチューブ2と、スクリューポンプ3と、を備えている。
Embodiments of the present invention will be described below.
FIG. 1 is a schematic configuration diagram showing the sludge digesting apparatus of this embodiment, in which a tank for putting sludge is a cross-sectional view at the center in the depth direction. 2 is a cross-sectional view taken along the line AA in FIG.
As shown in FIG. 1, the sludge digester includes a tank 1 for containing sludge, a draft tube 2 disposed in the tank 1, and a screw pump 3.

ドラフトチューブ2は、槽1の中心に鉛直方向に沿って配置され、その下部が支持脚15で槽1の底部12に固定されている。また、ドラフトチューブ2の上部が、支持腕16で槽1の壁部11に固定されている。
スクリューポンプ3は回転軸31とモータ部32とを備え、回転軸31の先端にスクリュー羽根31aが付いている。このスクリュー羽根31aの部分が全て、ドラフトチューブ2の上側開口部21内に配置されている。モータ部32は、槽1の蓋部13に取り付けられて槽1の外部に配置されている。
ドラフトチューブ2の外側には、内部に配置された回転軸31の先端部より下側となる範囲に外管28が配置されている。これにより、図2に示すように、ドラフトチューブ2と外管28との間に外側流路20が形成されている。外側流路20の両端部は閉塞されている。
The draft tube 2 is disposed along the vertical direction at the center of the tank 1, and a lower part thereof is fixed to the bottom 12 of the tank 1 by a support leg 15. Further, the upper portion of the draft tube 2 is fixed to the wall portion 11 of the tank 1 by the support arm 16.
The screw pump 3 includes a rotating shaft 31 and a motor unit 32, and a screw blade 31 a is attached to the tip of the rotating shaft 31. All of the screw blades 31 a are disposed in the upper opening 21 of the draft tube 2. The motor part 32 is attached to the lid part 13 of the tank 1 and arranged outside the tank 1.
Outside the draft tube 2, an outer tube 28 is arranged in a range below the tip of the rotary shaft 31 arranged inside. Thereby, as shown in FIG. 2, an outer flow path 20 is formed between the draft tube 2 and the outer tube 28. Both ends of the outer channel 20 are closed.

また、外管28の下端部に熱媒体導入管41が接続され、上端部に熱媒体導出管42が接続されている。熱媒体導入管41と熱媒体導出管42は槽1内に水平に配置され、各端部が槽1の壁部11を貫通して外側に至っている。
よって、ドラフトチューブ2の外管28が配置されている部分は、ドラフトチューブ2内に汚泥を通し、外側流路20に熱媒体を通す二重管構造部となっている。
In addition, a heat medium introduction tube 41 is connected to the lower end portion of the outer tube 28, and a heat medium outlet tube 42 is connected to the upper end portion. The heat medium introduction pipe 41 and the heat medium lead-out pipe 42 are disposed horizontally in the tank 1, and each end penetrates the wall 11 of the tank 1 and reaches the outside.
Therefore, the portion of the draft tube 2 where the outer tube 28 is disposed has a double-pipe structure that allows sludge to pass through the draft tube 2 and heat medium to pass through the outer flow path 20.

この実施形態の汚泥消化装置では、スクリューポンプ3を作動させることで、槽1内の汚泥5が、上端開口からドラフトチューブ2内に導入され、下端開口から導出されて循環する。これにより、槽1内の汚泥5が撹拌される。また、ドラフトチューブ2内に導かれた汚泥は、二重管構造部を通る際に、外側流路20を通る熱媒体で加熱される。
この実施形態の汚泥消化装置によれば、汚泥を撹拌するために設けたドラフトチューブ2の二重管構造部で、熱媒体により汚泥が加熱されるため、図4に示すような、撹拌のためのドラフトチューブ2とは別に加熱のための循環経路7を設けている、従来の間接加熱式汚泥消化装置と比較して、設備コストを低く抑えることができる。また、ドラフトチューブ2の二重管構造部で加熱された汚泥が槽1内に戻されて撹拌流を形成するため、槽1内全体の汚泥5が効率よく加熱される。
In the sludge digestion apparatus of this embodiment, the sludge 5 in the tank 1 is introduced into the draft tube 2 from the upper end opening and is circulated by being led out from the lower end opening by operating the screw pump 3. Thereby, the sludge 5 in the tank 1 is stirred. Further, the sludge introduced into the draft tube 2 is heated by the heat medium passing through the outer flow path 20 when passing through the double pipe structure.
According to the sludge digestion apparatus of this embodiment, since the sludge is heated by the heat medium in the double tube structure portion of the draft tube 2 provided for stirring the sludge, for the stirring as shown in FIG. Compared with a conventional indirectly heated sludge digester, which is provided with a circulation path 7 for heating separately from the draft tube 2, the equipment cost can be kept low. Moreover, since the sludge heated by the double pipe structure part of the draft tube 2 is returned in the tank 1 and forms a stirring flow, the sludge 5 of the whole tank 1 is heated efficiently.

1 槽
11 壁部
12 底部
13 蓋部
15 支持脚
16 支持腕
2 ドラフトチューブ
20 外側流路
28 外管
3 スクリューポンプ
31 回転軸
31a スクリュー羽根
32 モータ部
41 熱媒体導入管
42 熱媒体導出管
5 汚泥
6 吹き込み管
7 加熱のための循環経路
71 横管
72 横管
73 縦管
74 ポンプ
81 枝管
82 枝管
DESCRIPTION OF SYMBOLS 1 Tank 11 Wall part 12 Bottom part 13 Cover part 15 Support leg 16 Support arm 2 Draft tube 20 Outer flow path 28 Outer pipe 3 Screw pump 31 Rotating shaft 31a Screw blade 32 Motor part 41 Heat medium introduction pipe 42 Heat medium outlet pipe 5 Sludge 6 Blowing pipe 7 Circulation path 71 for heating Horizontal pipe 72 Horizontal pipe 73 Vertical pipe 74 Pump 81 Branch pipe 82 Branch pipe

Claims (1)

汚泥を入れる槽と、槽内に配置されたドラフトチューブと、を備え、
前記槽内の汚泥を前記ドラフトチューブ内に導いて循環させることで、槽内の汚泥を撹拌する汚泥消化装置であって、
前記ドラフトチューブに、内側に汚泥を通し、外側に熱媒体を通す二重管構造部を設けたことを特徴とする汚泥消化装置。
A tank for containing sludge, and a draft tube arranged in the tank,
A sludge digester that stirs the sludge in the tank by introducing and circulating the sludge in the tank into the draft tube,
A sludge digesting apparatus, wherein the draft tube is provided with a double pipe structure part through which sludge passes inside and a heat medium passes outside.
JP2009179409A 2009-07-31 2009-07-31 Sludge digestion apparatus Pending JP2011031168A (en)

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Application Number Title Priority Date Filing Date
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017535286A (en) * 2014-11-06 2017-11-30 エクシレム アイピー マネージメント エス.エー アール.エル. Temperature control device

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60193599A (en) * 1984-02-16 1985-10-02 タブリユ・エム・シー・リゾース・リカバリー・リミテツド Digester
JPS61111600U (en) * 1984-12-25 1986-07-15
JP2000157255A (en) * 1998-11-30 2000-06-13 Linde Kca Dresden Gmbh Method and apparatus for producing biogas
JP2005169374A (en) * 2003-12-11 2005-06-30 Linde Kca Dresden Gmbh Biological treatment method for suspension using bioreactor having liquid pressure type sediment takeout part and biological treatment apparatus therefor

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60193599A (en) * 1984-02-16 1985-10-02 タブリユ・エム・シー・リゾース・リカバリー・リミテツド Digester
JPS61111600U (en) * 1984-12-25 1986-07-15
JP2000157255A (en) * 1998-11-30 2000-06-13 Linde Kca Dresden Gmbh Method and apparatus for producing biogas
JP2005169374A (en) * 2003-12-11 2005-06-30 Linde Kca Dresden Gmbh Biological treatment method for suspension using bioreactor having liquid pressure type sediment takeout part and biological treatment apparatus therefor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017535286A (en) * 2014-11-06 2017-11-30 エクシレム アイピー マネージメント エス.エー アール.エル. Temperature control device

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