JP2005218888A - Sludge dehydrator and sludge dehydration method - Google Patents

Sludge dehydrator and sludge dehydration method Download PDF

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JP2005218888A
JP2005218888A JP2004026536A JP2004026536A JP2005218888A JP 2005218888 A JP2005218888 A JP 2005218888A JP 2004026536 A JP2004026536 A JP 2004026536A JP 2004026536 A JP2004026536 A JP 2004026536A JP 2005218888 A JP2005218888 A JP 2005218888A
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sludge
dewatering
unit
mud
dehydration
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JP4513344B2 (en
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Yasuhiko Ishii
保彦 石井
Takeshi Shibata
健 柴田
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Kurita Water Industries Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a sludge dehydrator which can effectively use separated liquid, separated by a first dehydration part, in a sludge dehydration process. <P>SOLUTION: The sludge dehydrator comprises the first dehydration part 3 and a second dehydration part 4 for further dehydrating sludge dehydrated in the first dehydration part 3, and the separated liquid W separated in the first dehydration part 3 is supplied onto a water-permeable filtration chamber 12 of the second dehydration part 4. Thereby the outer surface of the water-permeable filtration chamber 12 is always washed with the separated liquid W during dehydration operation to prevent the clogging and the like of the water-permeable filtration chamber 12. Preferably a water-permeable filtration chamber 6 of the first dehydration part 3 is disposed just above the water-permeable filtration chamber 12 of the second dehydration part 4, which dispenses with a special means for supplying the separated liquid W to the second dehydration part 4, and enables the saving of an installation area for the whole sludge dehydrator. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、汚泥脱水装置及び汚泥脱水方法に関するものである。   The present invention relates to a sludge dewatering device and a sludge dewatering method.

下水処理場や、屎尿処理場、製紙工場等で排出される汚泥を脱水するための装置として、従来、凝集剤を添加した汚泥を予備濃縮(予備脱水)する重力式の予備濃縮部と、該予備濃縮部で濃縮された濃縮汚泥を脱水する圧搾式等の脱水部と、を備えた脱水装置が知られている(特許文献1参照)。
特許第3222278号公報(特に、0013段落及び図1参照)
As a device for dewatering sludge discharged from sewage treatment plants, manure treatment plants, paper mills, etc., conventionally, a gravity-type preconcentration unit for preconcentrating (preliminary dewatering) sludge added with a flocculant; There is known a dehydrating apparatus including a dewatering unit such as a compression type that dehydrates concentrated sludge concentrated in a preconcentrating unit (see Patent Document 1).
Japanese Patent No. 3222278 (see in particular paragraph 0013 and FIG. 1)

前記特許文献1には明示的には述べられていないが、従来、前記予備濃縮部で分離された分離液は、そのままで又は所定の処理を施して装置外へと排水されるのが通常であり、汚泥脱水処理を円滑にする等の目的でこれを有効活用する等の提案は未だなされていない。   Although not explicitly stated in Patent Document 1, conventionally, the separated liquid separated in the preliminary concentrating section is usually drained out of the apparatus as it is or after being subjected to a predetermined treatment. There are no proposals to make effective use of this for the purpose of smoothing sludge dehydration.

また、前記脱水装置によれば、汚泥性状の変化又は相違により、添加した特定の凝集剤では十分な汚泥凝集効果が発揮されなかった場合であっても、前記予備濃縮部で濃縮処理された後には、その濃縮汚泥の全てがそのまま前記脱水部へと供給されてしまうので、その場合には、前記脱水部で目標とする脱水率を得ることができない等の問題もあった。   In addition, according to the dewatering apparatus, even if the sludge properties change or difference, even if the added flocculant does not exhibit a sufficient sludge agglomeration effect, after being concentrated in the preliminary concentration unit However, since all of the concentrated sludge is supplied to the dewatering unit as it is, there is a problem that a target dewatering rate cannot be obtained in the dewatering unit.

本発明は、前記の如き事情に鑑みてなされたもので、第一の脱水部と、第二の脱水部と、を備えた汚泥脱水装置において、前記第一の脱水部で分離された分離液を有効活用し得る汚泥脱水装置及び汚泥脱水方法を提供しようとするものである。   The present invention has been made in view of the above circumstances, and in a sludge dewatering device including a first dewatering unit and a second dewatering unit, a separated liquid separated by the first dewatering unit. The present invention intends to provide a sludge dewatering device and a sludge dewatering method that can effectively utilize the above.

本発明はまた、汚泥の凝集状態が悪い場合でも脱水率が低下することのない汚泥脱水装置を提供しようとするものである。   Another object of the present invention is to provide a sludge dewatering device in which the dewatering rate does not decrease even when the sludge aggregation state is poor.

前記課題を解決するため、本発明に係る汚泥脱水装置は、第一の脱水部と、第二の脱水部と、を備え、前記第一の脱水部で分離された分離液が前記第二の脱水部の通水性濾過室上に供給されるようにしたものである(請求項1)。   In order to solve the above problems, a sludge dewatering apparatus according to the present invention includes a first dewatering unit and a second dewatering unit, and the separated liquid separated in the first dewatering unit is the second dewatering unit. It is made to supply on the water-permeable filtration chamber of a dehydration part (Claim 1).

本発明によれば、前記第一の脱水部で分離された分離液が、前記第二の脱水部の前記通水性濾過室上に供給されるので、脱水作業中は常時、前記通水性濾過室の外表面が前記分離液で洗浄されることになり、前記第一の脱水部での分離液が有効活用されるとともに、前記通水性濾過室の目詰まり等が防止されて好適である。   According to the present invention, since the separation liquid separated in the first dehydration unit is supplied onto the water filtration chamber of the second dehydration unit, the water filtration chamber is always used during the dehydration operation. The outer surface is washed with the separation liquid, so that the separation liquid in the first dehydrating part is effectively utilized and the water-permeable filtration chamber is prevented from being clogged.

好適な実施の一形態として、前記第二の脱水部は、前記第一の脱水部で脱水された汚泥をさらに脱水する脱水部であるものとすることもできる(請求項2)。この場合、前記第一の脱水部から前記第二の脱水部へと至る一連の脱水処理工程において、前記第一の脱水部からの分離液が後工程部としての前記第二の脱水部の洗浄の用に供され、一連の脱水処理工程において生ずる分離液を該一連の脱水処理工程で有効に活用することができる。   As a preferred embodiment, the second dewatering part may be a dewatering part for further dewatering the sludge dewatered in the first dewatering part (Claim 2). In this case, in a series of dehydration processing steps from the first dehydration unit to the second dehydration unit, the separation liquid from the first dehydration unit is washed in the second dehydration unit as a post-process unit. Therefore, the separation liquid generated in the series of dehydration processes can be effectively used in the series of dehydration processes.

前記第一の脱水部における分離液は、前記第一の脱水部から前記第二の脱水部へと至る配管や案内溝等を通じて、前記第二の脱水部へと供給することもできる。しかし、好適な実施の一形態として、前記第一の脱水部の通水性濾過室を、前記第二の脱水部の前記通水性濾過室の真上に配置したものとすることもできる(請求項3)。このようにすれば、前記第一の脱水部で分離された分離液をそのまま前記第二の脱水部へと流下せしめることにより、該第二の脱水部の前記通水性濾過室を洗浄することができるので、前記分離液を前記第二の脱水部へと供給するための特別な手段が不要となり、好適である。また、上から見て前記二つの通水性濾過室の輪郭が互いに重なり合うことになるので、前記汚泥脱水装置全体としての据付面積を節約できる利点もある。   The separation liquid in the first dehydration unit can be supplied to the second dehydration unit through a pipe, a guide groove, or the like extending from the first dehydration unit to the second dehydration unit. However, as a preferred embodiment, the water-permeable filtration chamber of the first dewatering unit may be disposed directly above the water-permeable filtration chamber of the second dehydration unit (Claims). 3). In this way, the water filtration chamber of the second dehydrating unit can be washed by allowing the separated liquid separated in the first dehydrating unit to flow down to the second dehydrating unit as it is. Therefore, a special means for supplying the separation liquid to the second dehydrating unit is unnecessary, which is preferable. Moreover, since the outlines of the two water-permeable filtration chambers overlap each other when viewed from above, there is an advantage that the installation area of the entire sludge dewatering device can be saved.

好適な実施の一形態として、前記第一の脱水部と前記第二の脱水部とを連通せしめる汚泥通路が、前記第一の脱水部から前記第二の脱水部へ向けて下向きに延びていて、該第二の脱水部に近づくにつれて拡開しているものとすることもできる(請求項4)。このようにすれば、前記第二の脱水部へ供給される汚泥が前記汚泥通路内に詰まってしまうことが防止されて、好適である。   As a preferred embodiment, a sludge passage for communicating the first dewatering part and the second dewatering part extends downward from the first dewatering part to the second dewatering part. The second dewatering part may be expanded as it approaches (Claim 4). In this way, it is preferable that the sludge supplied to the second dewatering unit is prevented from being clogged in the sludge passage.

好適な実施の一形態として、前記第一の脱水部と前記第二の脱水部とを連通せしめる汚泥通路を、前記第二の脱水部への汚泥の通過を許容する通泥状態と、前記第二の脱水部への汚泥の通過を阻止して外部へ排出する排泥状態と、に切換え可能な給泥制御機構を備えたものとすることもできる(請求項5)。このようにすれば、例えば、前記第一の脱水部における汚泥の脱水・凝集状況が十分でない等の理由で、前記第一の脱水部から前記第二の脱水部へとそのまま汚泥を供給するのが不適当な場合には、前記給泥制御機構を操作して、前記汚泥通路を前記通泥状態から前記排泥状態へと切換えることにより、前記第二の脱水部への給泥を阻止して外部へ排出することができる。そして、例えば、汚泥の性状に応じた適切な凝集剤を添加して再度前記第一の脱水部に供給することで、脱水率の低下を防止することができる。   As a preferred embodiment, a sludge passage that allows the first dewatering part and the second dewatering part to communicate with each other, a sludge passage state that allows the sludge to pass to the second dewatering part, and the first It is also possible to provide a mud supply control mechanism capable of switching between a sludge state in which sludge is prevented from passing to the second dewatering section and discharged to the outside (Claim 5). In this way, for example, the sludge is supplied from the first dewatering section to the second dewatering section as it is because the sludge is not sufficiently dehydrated and aggregated in the first dewatering section. Is inappropriate, the mud supply control mechanism is operated to switch the sludge passage from the mud passage state to the exhaust mud state, thereby preventing mud supply to the second dewatering unit. Can be discharged to the outside. And the fall of a dehydration rate can be prevented by adding the suitable coagulant | flocculant according to the property of sludge, for example, and supplying it to said 1st dehydration part again.

好適な実施の一形態として、前記給泥制御機構は、前記汚泥通路を画成する通泥時姿勢と、前記汚泥通路を横切るように延びて汚泥を前記汚泥通路の外部へと案内する排泥時姿勢と、に変位自在な流路変更用フラップと、排泥口を閉じて前記汚泥通路を画成する通泥時姿勢と、前記排泥口を開放する排泥時姿勢と、に変位自在な排泥口開閉用フラップと、を備えたものとすることもできる(請求項6)。この場合、前記両フラップを前記通泥時姿勢に保持すると、前記汚泥通路が通泥状態となり、前記両フラップを前記排泥時姿勢に保持すると、前記汚泥通路が排泥状態となる。   As one preferred embodiment, the mud supply control mechanism includes a sludge passage position that defines the sludge passage, and a sludge that extends across the sludge passage and guides the sludge to the outside of the sludge passage. It is freely displaceable between the position changeable flow path changing flap, the mud passage position to close the mud outlet and the sludge passage to open, and the mud position to open the mud opening. It is also possible to provide a flap for opening and closing the mud discharge port (claim 6). In this case, when the flaps are held in the mud posture, the sludge passage is in a mud passage state, and when the flaps are held in the mud posture, the sludge passage is in a mud state.

本発明に係る汚泥脱水方法は、第一の脱水部で脱水した汚泥を第二の脱水部でさらに脱水する汚泥脱水方法であって、前記第一の脱水部で分離された分離液を前記第二の脱水部の洗浄液として用いることを特徴とするものである(請求項7)。   The sludge dewatering method according to the present invention is a sludge dewatering method in which the sludge dehydrated in the first dewatering section is further dewatered in the second dewatering section, and the separated liquid separated in the first dewatering section It is used as a cleaning liquid for the second dehydration part (claim 7).

以下、添付図面を参照して、本発明を実施するための最良の形態について説明する。   The best mode for carrying out the present invention will be described below with reference to the accompanying drawings.

図1は、本発明の一実施の形態に係る汚泥脱水装置の概略図である。   FIG. 1 is a schematic view of a sludge dewatering apparatus according to an embodiment of the present invention.

本実施の形態に係る汚泥脱水装置1は、汚泥凝集処理部2と、第一の脱水部としての予備濃縮部(予備脱水部)3と、第二の脱水部としての主脱水部4と、を備えている。処理対象としての原泥(汚泥)は、まず、前記汚泥凝集処理部2で凝集剤を添加されて粗大粒状の凝集汚泥とされ、次いで、前記予備濃縮部3で予備的な脱水作用を受けて濃縮汚泥とされ、最後に、前記主脱水部4へと移送されて、さらに脱水処理される。   The sludge dewatering device 1 according to the present embodiment includes a sludge aggregation treatment unit 2, a preconcentration unit (preliminary dehydration unit) 3 as a first dehydration unit, a main dehydration unit 4 as a second dehydration unit, It has. The raw mud (sludge) as a treatment target is first added with a flocculant in the sludge agglomeration processing unit 2 to be coarse granular agglomerated sludge, and then subjected to a preliminary dehydration action in the preconcentration unit 3. The concentrated sludge is finally transferred to the main dewatering unit 4 and further dewatered.

本実施の形態では、最も大きな設置面積を要する前記主脱水部4の真上に前記予備濃縮部3を配設し、脱水装置全体としての据付面積の節約を図っている。   In the present embodiment, the pre-concentration unit 3 is disposed directly above the main dehydrating unit 4 that requires the largest installation area, thereby saving the installation area of the entire dehydrating device.

前記汚泥凝集処理部2においては、原泥に凝集剤が添加されて、攪拌せしめられる。凝集剤は、原泥の性状に応じた適宜のものを選択して使用する。前記汚泥凝集処理部2の具体的構成について限定はないが、例えば、本実施の形態のものように、モータ5等を駆動源として回転駆動されるスクリューコンベア式のものや、攪拌翼を有するもの等を採用することができる。   In the sludge agglomeration processing unit 2, a flocculant is added to the raw mud and stirred. As the flocculant, an appropriate one according to the properties of the raw mud is selected and used. The specific configuration of the sludge aggregation processing unit 2 is not limited. For example, as in the present embodiment, a screw conveyor type driven by a motor 5 or the like as a drive source, or a stirring blade is used. Etc. can be adopted.

前記汚泥凝集処理部2で凝集せしめられた汚泥は、前記予備濃縮部3へと供給されて、適宜の方法で予備濃縮処理を受ける。本実施の形態では、前記予備濃縮部3において、重力による脱水処理が行われる。   The sludge agglomerated in the sludge agglomeration processing unit 2 is supplied to the preconcentration unit 3 and subjected to a preconcentration treatment by an appropriate method. In the present embodiment, the preliminary concentration unit 3 performs a dehydration process by gravity.

すなわち、前記予備濃縮部3は、周壁がパンチングメタル等の通水性多孔板からなる横向き円筒状の予備濃縮用濾過室(予備濃縮用通水性濾過室)6と、該予備濃縮用濾過室6内に同心に配設したスクリューコンベア7と、を備えている。前記予備濃縮用濾過室6は、前記汚泥凝集処理部2側の端部に、前記凝集汚泥を受け入れるための凝集汚泥入口8を備え、その反対側の端部に、濃縮汚泥出口9を備えている。前記スクリューコンベア7は、モータ10等を駆動源として回転駆動され、前記凝集汚泥入口8から供給される前記凝集汚泥を前記濃縮汚泥出口9へ向けて搬送し、この搬送過程において、前記凝集汚泥に予備濃縮処理又は予備脱水処理が施される。脱水による分離液(水分)Wは、前記予備濃縮用濾過室6の網目から流下し、後で述べるように、前記主脱水部4の洗浄液として用いられる。   That is, the pre-concentration unit 3 includes a horizontal cylindrical pre-concentration filtration chamber (pre-concentration water-filtration chamber) 6 whose peripheral wall is made of a water-permeable porous plate such as punching metal, and the pre-concentration filtration chamber 6. And a screw conveyor 7 disposed concentrically. The preconcentration filtration chamber 6 has a coagulated sludge inlet 8 for receiving the coagulated sludge at the end on the sludge coagulation treatment unit 2 side, and a concentrated sludge outlet 9 at the opposite end. Yes. The screw conveyor 7 is rotationally driven using a motor 10 or the like as a drive source, and conveys the aggregated sludge supplied from the aggregated sludge inlet 8 toward the concentrated sludge outlet 9, and in this conveyance process, the aggregated sludge is converted into the aggregated sludge. A pre-concentration process or a pre-dehydration process is performed. The separation liquid (water) W by dehydration flows down from the mesh of the preconcentration filtration chamber 6 and is used as a cleaning liquid for the main dehydration unit 4 as described later.

前記予備濃縮部3で予備濃縮された汚泥は、上下方向に延びる汚泥通路11を介して前記主脱水部4へと供給され、適宜の方法でさらなる脱水処理を受ける。本実施の形態では、前記主脱水部4において、圧搾による脱水処理が行われる。   The sludge pre-concentrated in the pre-concentration unit 3 is supplied to the main dehydration unit 4 through a sludge passage 11 extending in the vertical direction, and is subjected to further dehydration treatment by an appropriate method. In the present embodiment, the main dewatering unit 4 performs a dewatering process by pressing.

すなわち、前記主脱水部4は、周壁がパンチングメタル等の通水性多孔板からなる横向き円筒状の主脱水用濾過室(主脱水用通水性濾過室)12と、該主脱水用濾過室12内に同心に配設されたスクリュー13と、を備えている。前記主脱水用濾過室12は、その外周面における前記予備濃縮部3側の端部の上部に、前記予備濃縮部3から前記濃縮汚泥を受け入れるための濃縮汚泥入口14を備え、その反対側の端部に、脱水ケーキ出口15を備えている。前記濃縮汚泥入口14は、前記汚泥通路11を介して、前記予備濃縮用濾過室3の前記濃縮汚泥出口9と連通している。   That is, the main dehydrating section 4 includes a horizontal cylindrical main dewatering filtration chamber (main dewatering water-permeable filtration chamber) 12 whose peripheral wall is made of a water-permeable porous plate such as a punching metal, and the inside of the main dehydration filtration chamber 12. And a screw 13 disposed concentrically. The main dewatering filtration chamber 12 is provided with a concentrated sludge inlet 14 for receiving the concentrated sludge from the preliminary concentrating unit 3 at the upper end of the outer peripheral surface of the preconcentrating unit 3 side, on the opposite side. A dewatering cake outlet 15 is provided at the end. The concentrated sludge inlet 14 communicates with the concentrated sludge outlet 9 of the preconcentration filtration chamber 3 through the sludge passage 11.

前記スクリュー13は、前記主脱水用濾過室12の前記濃縮汚泥入口14側から前記脱水ケーキ出口15側に向けて徐々に大径となるテーパー状胴体16を備え、該テーパー状胴体16の外周には、前記主脱水用濾過室12の内径に適合する一様の外径を有するスクリュー羽根17が形成されている。前記スクリュー13は、モータ18等を駆動源として回転駆動され、前記濃縮汚泥入口14から供給される前記濃縮汚泥を前記脱水ケーキ出口15へ向けて搬送する。前記スクリュー13の外周面と前記主脱水用濾過室6の内周面との間の環状の脱水空間19は、前記脱水ケーキ出口15へ近づくにつれて徐々に狭くなっている。したがって、前記濃縮汚泥は、前記脱水ケーキ出口15へ向けての搬送過程で徐々に大きな圧搾作用を受け、水分を搾り取られる。脱水による分離液(水分)は、前記主脱水用濾過室12の網目から流下する。   The screw 13 includes a tapered body 16 that gradually increases in diameter from the concentrated sludge inlet 14 side to the dehydrated cake outlet 15 side of the main dewatering filtration chamber 12, and on the outer periphery of the tapered body 16. A screw blade 17 having a uniform outer diameter that matches the inner diameter of the main dehydration filtration chamber 12 is formed. The screw 13 is rotationally driven using a motor 18 or the like as a drive source, and conveys the concentrated sludge supplied from the concentrated sludge inlet 14 toward the dehydrated cake outlet 15. An annular dewatering space 19 between the outer peripheral surface of the screw 13 and the inner peripheral surface of the main dewatering filtration chamber 6 is gradually narrowed toward the dewatering cake outlet 15. Accordingly, the concentrated sludge is gradually subjected to a large pressing action in the process of transporting toward the dehydrated cake outlet 15 to squeeze out moisture. The separation liquid (water) by dehydration flows down from the mesh of the main dehydration filtration chamber 12.

本実施の形態では、前記予備濃縮部3で分離された分離液Wは、前記主脱水部4の前記主脱水用濾過室12上に供給される。このため、脱水作業中は常時、前記主脱水用濾過室12の外表面が前記分離液Wで洗浄されることになり、前記予備濃縮部3での分離液Wが有効活用されるとともに、前記主脱水用濾過室12の目詰まり等が防止される。特に、本実施の形態では、前記主脱水用濾過室12の真上に前記予備濃縮用濾過室6が配設されているので、前記予備濃縮部3で脱水されて前記予備濃縮用濾過室6から流れ落ちる分離液Wが、特別な配管や案内部材等を要することなく、そのまま前記主脱水用濾過室12上に降りかかる。このため、脱水装置の構成がシンプルとなり、好適である。   In the present embodiment, the separation liquid W separated by the preliminary concentration unit 3 is supplied onto the main dehydration filtration chamber 12 of the main dehydration unit 4. For this reason, the outer surface of the main dehydration filtration chamber 12 is always washed with the separation liquid W during the dehydration operation, and the separation liquid W in the preliminary concentration unit 3 is effectively utilized, The main dehydration filtration chamber 12 is prevented from being clogged. In particular, in the present embodiment, the preconcentration filtration chamber 6 is disposed directly above the main dehydration filtration chamber 12, so that the preconcentration filtration chamber 6 is dehydrated and dehydrated. The separation liquid W flowing down from the liquid falls on the main dehydration filtration chamber 12 as it is without requiring any special piping or guide members. For this reason, the structure of a dehydrating apparatus becomes simple and suitable.

前記汚泥脱水装置1は、前記汚泥通路11を、前記予備濃縮部3から前記脱水部3への前記濃縮汚泥の通過を許容する通泥状態と、前記予備濃縮部3から前記脱水部4への前記濃縮汚泥の通過を阻止して外部へ排出する排泥状態と、に切換え可能な給泥制御機構20を備えている。該給泥制御機構20は、前記予備濃縮部3での汚泥の凝集状況が悪い場合等に使用する。   The sludge dewatering apparatus 1 is configured to allow the sludge passage 11 to pass through the sludge passage 11 from the preconcentration unit 3 to the dehydration unit 3, and from the preconcentration unit 3 to the dehydration unit 4. A mud supply control mechanism 20 is provided that can be switched to a mud state in which the concentrated sludge is prevented from passing and discharged to the outside. The mud supply control mechanism 20 is used when the state of sludge aggregation in the preliminary concentration unit 3 is poor.

すなわち、汚泥の凝集状況は、前記予備濃縮部3で目視により判定できるので、添加した凝集剤による凝集効果が十分に発揮されていない場合には、前記給泥制御機構20を操作して、前記汚泥通路11を前記通泥状態から前記排泥状態へと切換えることにより、前記脱水部4の手前で汚泥を装置外へと取り出す。これにより、前記脱水部4における脱水率の低下を防止することができる。外部へ取り出した汚泥は、前記凝集処理部2に再投入し、添加する凝集剤を汚泥の性状に応じた適切な種類のものに変更して、再度、前記予備濃縮部3へと供給することができる。   That is, since the coagulation state of sludge can be determined visually by the preliminary concentration unit 3, when the coagulation effect by the added coagulant is not sufficiently exhibited, the mud supply control mechanism 20 is operated, By switching the sludge passage 11 from the mud passage state to the waste mud state, the sludge is taken out of the apparatus before the dewatering unit 4. Thereby, the fall of the dehydration rate in the said dehydration part 4 can be prevented. The sludge taken out to the outside is re-introduced into the agglomeration processing unit 2, and the flocculant to be added is changed to an appropriate type according to the properties of the sludge and supplied again to the preconcentration unit 3. Can do.

本実施の形態では、前記給泥制御機構20が、流路変更用フラップ21と、排泥口開閉用フラップ22と、の組み合わせで構成されている。前記両フラップ21,22は、前記汚泥通路11を画成する通路画成筒23の一部を構成しており、上端部の枢支軸を中心として下端部側が揺動自在とされている。前記流路変更用フラップ21は、前記通路画成筒23の外表面に沿って延びた通泥時姿勢(図1に実線で示してある)と、前記汚泥通路11を横切るように斜めに延びて汚泥を前記汚泥通路11の外部へと案内する排泥時姿勢(図1に仮想線で示してある)と、に変位自在である。同じく、前記排泥口開閉用フラップ22は、前記通路画成筒23に形成された排泥口24を閉じる通泥時姿勢(図1に実線で示してある)と、前記排泥口24を開放する排泥時姿勢(図1に仮想線で示してある)と、に変位自在である。そして、前記両フラップ21,22を前記通泥時姿勢に保持すると、前記汚泥通路11が通泥状態となり、前記両フラップ21,22を前記排泥時姿勢に保持すると、前記汚泥通路11が排泥状態となる。   In the present embodiment, the mud supply control mechanism 20 is configured by a combination of a flow path changing flap 21 and a drainage port opening / closing flap 22. Both the flaps 21 and 22 constitute a part of the passage defining cylinder 23 that defines the sludge passage 11, and the lower end side is swingable about the pivot shaft of the upper end portion. The flow path changing flap 21 extends obliquely so as to cross the sludge passage 11 and a posture during mud passage (shown by a solid line in FIG. 1) extending along the outer surface of the passage defining cylinder 23. The sludge can be displaced to a sludge posture (shown in phantom lines in FIG. 1) for guiding the sludge to the outside of the sludge passage 11. Likewise, the flap 22 for opening / closing the mud port opens the mud port 24 (shown by a solid line in FIG. 1) that closes the mud port 24 formed in the passage defining cylinder 23, and the mud port 24. It is freely displaceable in the mud draining posture (shown in phantom lines in FIG. 1). When the flaps 21 and 22 are held in the mud passage position, the sludge passage 11 is in a mud passage state. When the flaps 21 and 22 are held in the mud discharge position, the sludge passage 11 is discharged. It becomes mud.

なお、前記両フラップ21,22は、その姿勢変更操作を手動で行うこととしても良いし、適宜のアクチュエータを設けて動力駆動されるようにしても良い。また、前記両フラップ21,22を、図示しない適宜の連結部材で互いに連結し、前記両フラップ21,22の前記通泥時姿勢と前記排泥時姿勢への姿勢変更操作が、前記連結部材を介して連動して行われるようにすると、好適である。   In addition, both the flaps 21 and 22 may be manually operated to change their posture, or may be driven by power by providing appropriate actuators. In addition, the flaps 21 and 22 are connected to each other by an appropriate connecting member (not shown), and the posture change operation of the flaps 21 and 22 to the posture during mud and the posture during mud discharge is performed. It is preferable that the operations are performed in conjunction with each other.

図1のII矢視図である図2に示すように、前記汚泥通路11を画成する前記通路画成筒23は、前記予備濃縮部3側から前記脱水部4側に近づくにつれて拡開しているものとするのが望ましい。このようにすれば、前記予備濃縮部3で濃縮された汚泥が前記汚泥通路11内に詰まってしまうことが防止されて、一層好適である。   As shown in FIG. 2 which is a view taken in the direction of arrow II in FIG. 1, the passage defining cylinder 23 that defines the sludge passage 11 expands from the preconcentration unit 3 side toward the dehydration unit 4 side. It is desirable to have it. In this way, it is possible to prevent the sludge concentrated in the preliminary concentration unit 3 from being clogged in the sludge passage 11, which is more preferable.

本発明の一実施の形態に係る汚泥脱水装置の概略図である。It is the schematic of the sludge dehydration apparatus which concerns on one embodiment of this invention. 図1のII矢視図である。It is II arrow directional view of FIG.

符号の説明Explanation of symbols

3 予備濃縮部(第一の脱水部)
4 主脱水部(第二の脱水部)
6 通水性濾過室(予備濃縮用濾過室)
11 汚泥通路
12 通水性濾過室(主脱水用濾過室)
20 給泥制御機構
21 流路変更用フラップ
22 排泥口開閉用フラップ
24 排泥口
W 予備濃縮部での分離液
3 Pre-concentration part (first dehydration part)
4 Main dehydration part (second dehydration part)
6 Water-permeable filtration chamber (preconcentration filtration chamber)
11 Sludge passage 12 Water-permeable filtration chamber (main dehydration filtration chamber)
20 Mud supply control mechanism 21 Flap for channel change 22 Flap for opening / closing mud outlet 24 Drain port W Separation liquid in preconcentration section

Claims (7)

第一の脱水部と、第二の脱水部と、を備え、前記第一の脱水部で分離された分離液が前記第二の脱水部の通水性濾過室上に供給されるようにせしめてなる、汚泥脱水装置。   A first dehydrating unit and a second dehydrating unit, wherein the separated liquid separated in the first dehydrating unit is supplied onto the water-permeable filtration chamber of the second dehydrating unit. Become a sludge dewatering device. 前記第二の脱水部は、前記第一の脱水部で脱水された汚泥をさらに脱水する脱水部である、請求項1に記載の汚泥脱水装置。   The sludge dewatering device according to claim 1, wherein the second dewatering unit is a dewatering unit that further dewaters the sludge dewatered in the first dewatering unit. 前記第一の脱水部の通水性濾過室を、前記第二の脱水部の前記通水性濾過室の真上に配置してなる、請求項1又は2に記載の汚泥脱水装置。   The sludge dewatering device according to claim 1 or 2, wherein the water-permeable filtration chamber of the first dewatering unit is disposed immediately above the water-permeable filtration chamber of the second dewatering unit. 前記第一の脱水部と前記第二の脱水部とを連通せしめる汚泥通路が、前記第一の脱水部から前記第二の脱水部へ向けて下向きに延びていて、該第二の脱水部に近づくにつれて拡開している、請求項2又は3に記載の汚泥脱水装置。   A sludge passage that allows the first dewatering unit and the second dewatering unit to communicate with each other extends downward from the first dewatering unit to the second dewatering unit. The sludge dewatering device according to claim 2 or 3, wherein the sludge dewatering device expands as it approaches. 前記第一の脱水部と前記第二の脱水部とを連通せしめる汚泥通路を、前記第二の脱水部への汚泥の通過を許容する通泥状態と、前記第二の脱水部への汚泥の通過を阻止して外部へ排出する排泥状態と、に切換え可能な給泥制御機構を備えている、請求項2,3又は4に記載の汚泥脱水装置。   A sludge passage that allows the first dewatering unit and the second dewatering unit to communicate with each other; a mud passing state that allows the sludge to pass to the second dewatering unit; and the sludge to the second dewatering unit. The sludge dewatering device according to claim 2, 3 or 4, further comprising a mud supply control mechanism that can be switched between a mud discharge state that blocks passage and is discharged to the outside. 前記給泥制御機構は、前記汚泥通路を画成する通泥時姿勢と、前記汚泥通路を横切るように延びて汚泥を前記汚泥通路の外部へと案内する排泥時姿勢と、に変位自在な流路変更用フラップと、排泥口を閉じて前記汚泥通路を画成する通泥時姿勢と、前記排泥口を開放する排泥時姿勢と、に変位自在な排泥口開閉用フラップと、を備えている、請求項5に記載の汚泥脱水装置。   The mud supply control mechanism is freely displaceable between a mud posture that defines the sludge passage and a drainage posture that extends across the sludge passage and guides the sludge to the outside of the sludge passage. A flap for changing the flow path, a mud posture that closes the mud port and defines the sludge passage, and a mud port opening / closing flap that is displaceable to the mud posture that opens the mud port, The sludge dewatering device according to claim 5. 第一の脱水部で脱水した汚泥を第二の脱水部でさらに脱水する汚泥脱水方法であって、前記第一の脱水部で分離された分離液を前記第二の脱水部の洗浄液として用いることを特徴とする、汚泥脱水方法。   A sludge dewatering method in which the sludge dehydrated in the first dewatering section is further dewatered in the second dewatering section, and the separated liquid separated in the first dewatering section is used as a cleaning liquid for the second dewatering section. A sludge dewatering method characterized by
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JP2006088005A (en) * 2004-09-22 2006-04-06 Shinagawa Tekkojyo Corp Ltd Sewage treatment device
JP2017205691A (en) * 2016-05-17 2017-11-24 水ing株式会社 Sludge dehydrator and cleaning method therefor
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JPS61262498A (en) * 1985-05-17 1986-11-20 Nippon Kokan Kk <Nkk> High-pressure dehydration treatment device
JPS63154298A (en) * 1986-10-21 1988-06-27 アルバート、ベール Dehydrator for sludge and similar substance
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006088005A (en) * 2004-09-22 2006-04-06 Shinagawa Tekkojyo Corp Ltd Sewage treatment device
JP2017205691A (en) * 2016-05-17 2017-11-24 水ing株式会社 Sludge dehydrator and cleaning method therefor
JP6271069B1 (en) * 2017-08-04 2018-01-31 株式会社鶴見製作所 Solid-liquid separator
JP2019030825A (en) * 2017-08-04 2019-02-28 株式会社鶴見製作所 Solid-liquid separator

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