JP3128828U - Sewage treatment equipment - Google Patents

Sewage treatment equipment Download PDF

Info

Publication number
JP3128828U
JP3128828U JP2006009096U JP2006009096U JP3128828U JP 3128828 U JP3128828 U JP 3128828U JP 2006009096 U JP2006009096 U JP 2006009096U JP 2006009096 U JP2006009096 U JP 2006009096U JP 3128828 U JP3128828 U JP 3128828U
Authority
JP
Japan
Prior art keywords
pipe
water
flow
sewage treatment
water pipe
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.)
Expired - Lifetime
Application number
JP2006009096U
Other languages
Japanese (ja)
Inventor
昭三 岡本
Original Assignee
株式会社ビ−・シ−・オ−
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 株式会社ビ−・シ−・オ− filed Critical 株式会社ビ−・シ−・オ−
Priority to JP2006009096U priority Critical patent/JP3128828U/en
Application granted granted Critical
Publication of JP3128828U publication Critical patent/JP3128828U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

【課題】汚水処理施設の流量調節槽の水深が深いことによって、水流への空気の供給量が少なくなっても、酸素の水への取込み量を十分に確保する。
【解決手段】水中ポンプ2と、流入口30、流出口31、および連結部32を備えた流水管3と、上下端が開口した吸気管4と、磁化処理具5とから成る。磁化処理具5は扁平な断面形状の管状体6を有し、管状体6の通路幅が小さい側の対向する壁面に異なる磁極が向き合うように永久磁石が外付けされる。水中ポンプ2を汚水処理施設の流量調整槽の底面上に水没状態で設置し、流水管3は流出口31を流量調整槽内に位置させかつ流入口30を水中ポンプ2の吐出口21に接続する。吸気管4は上端の開口を水面上に位置させ、下端の開口を流水管3の連結部32に連結する。流水管3の吸気管4が連通する位置の下流に、管状体6を流水管3の途中に介装させるようにして磁化処理具5を配置する。
【選択図】図1
[PROBLEMS] To ensure a sufficient amount of oxygen to be taken into water even when the amount of air supplied to a water flow is reduced due to the deep depth of a flow control tank of a sewage treatment facility.
The submersible pump includes an underwater pump, an inflow pipe having an inlet, an outlet, and a connecting portion, an intake pipe having upper and lower ends opened, and a magnetizing tool. The magnetization processing tool 5 has a tubular body 6 having a flat cross-sectional shape, and a permanent magnet is externally attached so that different magnetic poles face opposite wall surfaces on the side where the passage width of the tubular body 6 is small. The submersible pump 2 is installed on the bottom surface of the flow rate adjustment tank of the sewage treatment facility, and the outlet pipe 3 has the outlet 31 located in the flow adjustment tank and the inlet 30 is connected to the discharge port 21 of the submersible pump 2. To do. The intake pipe 4 has an upper end opening located on the water surface and a lower end opening connected to the connecting portion 32 of the water flow pipe 3. The magnetization processing tool 5 is arranged downstream of the position where the intake pipe 4 of the flowing water pipe 3 communicates with the tubular body 6 in the middle of the flowing water pipe 3.
[Selection] Figure 1

Description

この考案は、例えば汚水処理施設において、一般家庭からの排水やレストランや病院などの施設からの排水(以下、「汚水」という。)を導入して溜める流量調整槽内に設置される汚水処理装置に関し、特にこの考案は、流量調整槽内の水を撹拌しつつ曝気するのに用いられる汚水処理装置に関する。   This device is, for example, a sewage treatment apparatus installed in a flow adjustment tank that introduces and collects wastewater from general households and wastewater from facilities such as restaurants and hospitals (hereinafter referred to as “sewage”) in sewage treatment facilities. In particular, the present invention relates to a sewage treatment apparatus used for aeration while stirring water in a flow rate adjusting tank.

一般的な汚水処理施設には、図5に示すように、大きなゴミや砂などが除去された後の汚水を導入して一旦貯留するための流量調整槽10が設けられている。この流量調整槽10に溜められた汚水はポンプ11によって吸い上げられ、一定の流量で曝気槽12へ送られる。曝気槽12には槽内の汚水中に空気を導入するためのブロワー13が接続されている。汚水には好気性の微生物が生息しており、空気の導入によって微生物に酸素を供給して水質の浄化を行わせる。曝気処理後の水は曝気槽12から沈殿槽14へ送られる。沈殿槽14では泥を沈殿させ、その上澄み液を処理済水として放流槽15へ送る。なお、沈殿槽14で沈殿した泥はポンプ16によって吸い出され、その泥の濃縮と脱水とを経て脱水ケーキになる。前記放流槽15では処理済水を次亜塩素ナトリウムなどを用いて殺菌した後、川などへ放流する。   In a general sewage treatment facility, as shown in FIG. 5, a flow rate adjusting tank 10 is provided for introducing and temporarily storing sewage after large trash or sand is removed. The sewage stored in the flow rate adjusting tank 10 is sucked up by the pump 11 and sent to the aeration tank 12 at a constant flow rate. A blower 13 for introducing air into the sewage in the tank is connected to the aeration tank 12. Aerobic microorganisms inhabit sewage, and oxygen is supplied to the microorganisms by introducing air to purify the water quality. The water after the aeration treatment is sent from the aeration tank 12 to the precipitation tank 14. In the settling tank 14, mud is precipitated, and the supernatant liquid is sent to the discharge tank 15 as treated water. The mud precipitated in the settling tank 14 is sucked out by the pump 16 and becomes a dehydrated cake through concentration and dehydration of the mud. In the discharge tank 15, the treated water is sterilized using sodium hypochlorite or the like and then discharged to a river or the like.

前記曝気槽12での曝気処理だけでは十分でない場合が多いことから、図6に示すように、流量調整槽10の内部に汚水処理装置100を設置して補助的な曝気処理を行っている。
この汚水処理装置100は、流量調整槽10内に水没状態で設置されるもので、流量調整槽10に溜まった汚水を撹拌しつつ曝気を行う。図示例の汚水処理装置100は、前記流量調整槽10内の汚水を吸い込んで吐き出す水中ポンプ2と、一端は水中ポンプ2の吐出口に接続され他端は流量調整槽10内に開口する流水管3と、下端の開口を流水管3内の流路に連通させ上端の開口は水面上に位置させる吸気管4とで構成されている。前記吸気管4の内部は流水管3内の水流により負圧化される結果、吸気管4が外気を引き込んで流水管3内に空気を導入する。この空気の導入現象は一般に「エゼクター作用」と呼ばれている。このエゼクター作用によって流水管3を流れる水中に導入された空気は気泡となって混入し、この気液混合流が流量調整槽10内に噴射されて撹拌と曝気とが行われる。
Since the aeration process in the aeration tank 12 is not always sufficient, as shown in FIG. 6, a sewage treatment apparatus 100 is installed inside the flow rate adjustment tank 10 to perform an auxiliary aeration process.
The sewage treatment apparatus 100 is installed in the flow adjustment tank 10 in a submerged state, and performs aeration while stirring the sewage collected in the flow adjustment tank 10. The illustrated sewage treatment apparatus 100 includes a submersible pump 2 that draws in and discharges sewage in the flow rate adjusting tank 10, and a water pipe that has one end connected to the discharge port of the submersible pump 2 and the other end opened in the flow rate adjusting tank 10. 3 and an intake pipe 4 whose lower end opening communicates with the flow path in the water pipe 3 and whose upper end opening is located on the water surface. As a result of the negative pressure generated in the intake pipe 4 by the water flow in the flowing water pipe 3, the intake pipe 4 draws outside air and introduces air into the flowing water pipe 3. This phenomenon of air introduction is generally called “ejector action”. The air introduced into the water flowing through the water flow pipe 3 by this ejector action is mixed as bubbles, and this gas-liquid mixed flow is injected into the flow rate adjusting tank 10 to perform stirring and aeration.

しかしながら、上記した構成の汚水処理装置では、流量調整槽10の容量が大きく、水深が深い場合には、吸気管4より流水管3内の水流へ導入される空気の量が少なくなり、水流に混入する気泡の大きさも大きくなる。その結果、水と空気との接触面積が小さくなり、水への酸素の取込み量が少なくなる。そのため、曝気による浄化機能が十分に発揮されず、曝気槽における曝気処理を補うことができない。   However, in the sewage treatment apparatus having the above-described configuration, when the capacity of the flow rate adjusting tank 10 is large and the water depth is deep, the amount of air introduced into the water flow in the water flow pipe 3 is smaller than the intake pipe 4 and the water flow is reduced. The size of the bubbles to be mixed also increases. As a result, the contact area between water and air is reduced, and the amount of oxygen taken into water is reduced. Therefore, the purification function by aeration is not sufficiently exhibited, and the aeration process in the aeration tank cannot be supplemented.

この考案は、上記した問題に着目してなされたもので、流量調整槽の水深が深いことによって、水流への空気の導入量が少なくなっても、水への酸素の取込み量を十分に確保し得る汚水処理装置を提供することを目的とする。   This device was made by paying attention to the above-mentioned problems. By deepening the water depth of the flow control tank, sufficient intake of oxygen into the water is ensured even when the amount of air introduced into the water flow is reduced. An object of the present invention is to provide a sewage treatment apparatus that can be used.

この考案による汚水処理装置は、汚水処理施設の曝気槽へ汚水を一定の流量で送り出すための流量調整槽に設けられるもので、吸込口および吐出口を有する水中ポンプと、一端に流入口、他端に流出口、前記流入口に近い位置に連結部をそれぞれ備えた流水管と、上端および下端が開口した吸気管と、両端が開口した扁平な断面形状の管状体を有し、前記管状体の通路幅が小さい側の対向する壁面に異なる磁極が向き合うように複数の永久磁石が外付けされて成る磁化処理具とから成るものである。前記水中ポンプおよび流水管を前記流量調整槽の底面上に水没状態で設置し、前記流水管は、流出口を流量調整槽内に位置させかつ流入口を水中ポンプの吐出口に接続するとともに、前記吸気管は、上端の開口を水面上に位置させかつ流水管内の流路に連通するように下端の開口を流水管の連結部に連結している。前記流水管の吸気管が連通する位置の下流に、前記管状体を流水管の途中に介装させるようにして前記磁化処理具を配置して、流水管を流れる水と、前記流水管内の水流により負圧化された吸気管によって流水管に導入された空気とに前記磁化処理具による磁界を作用させるようにしている。   The sewage treatment apparatus according to this device is provided in a flow rate adjusting tank for sending sewage at a constant flow rate to an aeration tank of a sewage treatment facility, and includes a submersible pump having a suction port and a discharge port, an inlet at one end, and the like. An outlet at the end, and a water pipe provided with a connecting portion at a position close to the inlet, an intake pipe having an upper end and a lower end, and a tubular body having a flat cross-sectional shape with both ends opened. And a magnetizing tool in which a plurality of permanent magnets are externally attached so that different magnetic poles face opposite wall surfaces on the side where the passage width is small. The submersible pump and the water pipe are installed in a submerged state on the bottom surface of the flow rate adjusting tank, the water pipe has an outlet located in the flow rate adjusting tank and the inlet is connected to the outlet of the submersible pump, The intake pipe has an opening at the upper end located on the water surface and has a lower end opening connected to a connecting portion of the flowing water pipe so as to communicate with a flow path in the flowing water pipe. The magnetizing treatment tool is arranged downstream of the position where the intake pipe of the water pipe communicates with the tubular body in the middle of the water pipe, and the water flowing in the water pipe and the water flow in the water pipe A magnetic field generated by the magnetization processing tool is caused to act on the air introduced into the flowing water pipe by the intake pipe that has been made negative by the above.

上記した構成の汚水処理装置を流量調整槽内に設置して水中ポンプを駆動すると、水中ポンプにより吸い込まれた流量調整槽内の汚水は吐出口から流水管の流入口へ送り込まれる。流水管に送り込まれた汚水は流水管内の流路を流れて流出口より流量調整槽内へ流出する。この流路の途中において、吸気管から流水管に空気が導入され、水流に気泡となって混入するので、前記流水管の流出口からは気液混合流が噴射されることになり、これにより槽内の撹拌と曝気とが行われる。
流水管を流れる汚水は磁化処理具によって磁化処理される。また、磁化処理具が吸気管との連通位置の下流に配置されているので、気泡にも磁界が作用する。水が磁界の作用を受けて磁化されると、水のクラスタが細分化されるので、水が周囲から酸素を奪う作用(還元作用)が高められて酸素の水への取込み量が増す。このため、たとえ流量調整槽の容量が大きく水深が深くても、曝気による浄化機能が十分に発揮される。さらに、気泡が磁界の作用を受けると、気泡の細分化も促進され、水と空気との接触面積が増す結果、酸素の水への取込み量が増し、曝気による浄化機能が一層促進される。
When the sewage treatment apparatus having the above configuration is installed in the flow rate adjusting tank and the submersible pump is driven, the sewage in the flow rate adjusting tank sucked by the submersible pump is sent from the discharge port to the inlet of the water pipe. The sewage sent to the water pipe flows through the flow path in the water pipe and flows out from the outlet into the flow rate adjusting tank. In the middle of this flow path, air is introduced from the intake pipe to the water flow pipe and mixed into the water flow as bubbles, so that a gas-liquid mixed flow is jetted from the outlet of the water flow pipe. The tank is stirred and aerated.
The sewage flowing through the water pipe is magnetized by the magnetizing tool. Further, since the magnetization processing tool is disposed downstream of the communication position with the intake pipe, the magnetic field also acts on the bubbles. When water is magnetized by the action of a magnetic field, the water clusters are subdivided, so that the action of water depriving oxygen from the surroundings (reduction action) is enhanced, and the amount of oxygen taken into water is increased. For this reason, even if the capacity | capacitance of a flow control tank is large and the water depth is deep, the purification function by aeration is fully exhibited. Furthermore, when the bubbles are subjected to the action of a magnetic field, the fragmentation of the bubbles is also promoted, the contact area between water and air is increased, the amount of oxygen taken into water is increased, and the purification function by aeration is further promoted.

さらに、前記磁化処理具は、扁平な断面形状の管状体と、前記管状体の通路幅が小さい側の対向する壁面に異なる磁極が向き合うように外付けされる複数の永久磁石とを含むものであり、前記管状体が流水管の途中に介装されているので、管状体を流れる水に強い磁界を作用させることができ、磁化処理の効果が高められる。   Further, the magnetization processing tool includes a tubular body having a flat cross-sectional shape, and a plurality of permanent magnets externally attached so that different magnetic poles face opposite wall surfaces on the side where the passage width of the tubular body is small. In addition, since the tubular body is interposed in the middle of the flowing water pipe, a strong magnetic field can be applied to the water flowing through the tubular body, and the effect of the magnetization process is enhanced.

この考案によると、水のクラスターや気泡が細分化されるので、たとえ水流への空気の供給量が少なくても、水への酸素の取込み量を十分に確保でき、容量が大きく水深が深い流量調整槽についても曝気による浄化機能を十分に発揮できる。   According to this device, water clusters and bubbles are subdivided, so even if the amount of air supplied to the water flow is small, sufficient amount of oxygen can be secured in the water, and the flow rate is large and the water depth is deep. The adjustment tank can also fully perform the purification function by aeration.

図1は、この考案の一実施例である汚水処理装置1の構成を示す。
図示例の汚水処理装置1は、汚水処理施設における流量調整槽内に水没状態で設置されるもので、底面f上に設置された基板9上に支持されている。前記流量調整槽は、曝気槽に送る汚水を一旦溜めて一定の流量で曝気槽へ送り出すためのものである。
FIG. 1 shows a configuration of a sewage treatment apparatus 1 according to an embodiment of the present invention.
The illustrated sewage treatment apparatus 1 is installed in a submerged state in a flow rate adjusting tank in a sewage treatment facility, and is supported on a substrate 9 installed on a bottom surface f. The flow rate adjusting tank is for temporarily storing sewage to be sent to the aeration tank and sending it to the aeration tank at a constant flow rate.

この汚水処理装置1は、水中ポンプ2、流水管3、吸気管4、および磁化処理具5により構成される。前記水中ポンプ2は槽内の水を吸込口20より吸い込んで吐出口21より吐き出す。前記流水管3は、一端に流入口30、他端に流出口31を備え、一端の流入口30は前記水中ポンプ2の吐出口21に接続され、他端の流出口31は槽内に位置させる。   The sewage treatment apparatus 1 includes a submersible pump 2, a flowing water pipe 3, an intake pipe 4, and a magnetization treatment tool 5. The submersible pump 2 sucks water in the tank from the suction port 20 and discharges it from the discharge port 21. The outlet pipe 3 has an inlet 30 at one end and an outlet 31 at the other end, the inlet 30 at one end is connected to the outlet 21 of the submersible pump 2, and the outlet 31 at the other end is located in the tank. Let

この流水管3には流入口30に近い位置に上向きの連結部32が形成されている。この連結部32には前記吸気管4の下端の開口が連結され、吸気管4を流水管3の流路に連通させる。この吸気管4は、上端を水面上より突出させることができる長さに形成されている。吸気管4の下端の開口は前記連結部32を介して流水管3内の流路に臨ませるとともに、上端の外周の開口41は水面w上に位置させているので、流水管3内の水流により吸気管4内が負圧化され、吸気管4より流水管3に空気が導入される。   An upward connecting portion 32 is formed in the water pipe 3 at a position close to the inlet 30. An opening at the lower end of the intake pipe 4 is connected to the connecting portion 32, and the intake pipe 4 is communicated with the flow path of the flowing water pipe 3. The intake pipe 4 is formed in such a length that its upper end can protrude from the water surface. Since the opening at the lower end of the intake pipe 4 faces the flow path in the flowing water pipe 3 through the connecting portion 32 and the opening 41 at the outer periphery of the upper end is located on the water surface w, the water flow in the flowing water pipe 3 As a result, the pressure in the intake pipe 4 is reduced to a negative pressure, and air is introduced from the intake pipe 4 into the flowing water pipe 3.

前記磁化処理具5は、この実施例では、流水管3に吸気管4が連通する位置の下流に配置されている。磁化処理具5を構成する管状体6は流水管3の中間に介装されている。このため、流水管3は上流管3Aと下流管3Bとに分離され、上流管3Aの出口33に管状体6の流入口60が、下流管3Bの入口34に管状体6の流出口61が、それぞれ連結される。   In this embodiment, the magnetization processing tool 5 is disposed downstream of the position where the intake pipe 4 communicates with the flowing water pipe 3. The tubular body 6 constituting the magnetization processing tool 5 is interposed in the middle of the flowing water pipe 3. For this reason, the water flow pipe 3 is separated into an upstream pipe 3A and a downstream pipe 3B. An inlet 60 of the tubular body 6 is provided at the outlet 33 of the upstream pipe 3A, and an outlet 61 of the tubular body 6 is provided at the inlet 34 of the downstream pipe 3B. , Respectively.

前記磁化処理具5は、図3および図4に示すように、一端に流入口60、他端に流出口61を有する管状体6と、この管状体6に外付けされる複数個の磁界発生器7とから成るものである。前記管状体6は、長さ中央部が磁化処理領域となっており、通路63の縦方向の通路幅yが横方向の通路幅xより十分に大きな扁平な断面矩形状に形成されている。前記管状体6の側壁面62R,62Lは、狭い通路幅xを隔てて対向しており、この対向する側壁面62R,62Lに複数個の磁界発生器7が取り付けられる。   As shown in FIGS. 3 and 4, the magnetization processing tool 5 includes a tubular body 6 having an inlet 60 at one end and an outlet 61 at the other end, and a plurality of magnetic field generation externally attached to the tubular body 6. And a container 7. The tubular body 6 is a magnetized region at the center of the length, and is formed in a flat cross-sectional rectangular shape in which the longitudinal passage width y of the passage 63 is sufficiently larger than the lateral passage width x. The side wall surfaces 62R and 62L of the tubular body 6 are opposed to each other with a narrow passage width x, and a plurality of magnetic field generators 7 are attached to the opposed side wall surfaces 62R and 62L.

各磁界発生器7は、ケース体70の内部に磁極の向きを揃えて複数の永久磁石71が積層状態で装填されたものであり、異なる磁極N,Sが互いに向き合うように各磁界発生器7が管状体6の外周面にそれぞれ取り付け固定される。   Each magnetic field generator 7 has a plurality of permanent magnets 71 loaded in a laminated state with the magnetic poles aligned in the case body 70, and each magnetic field generator 7 has different magnetic poles N and S facing each other. Are fixedly attached to the outer peripheral surface of the tubular body 6.

なお、この実施例の磁化処理具5は流水管3に吸気管4が連通する位置の下流に配置しているが、図2に示すように、磁化処理具5を流水管3に吸気管4が連通する位置の上流に配置してもよい。なお、図1の実施態様は水深が比較的に浅い場合に適用し、図2の実施態様は水深が比較的深い場合に適用するとよい。   Although the magnetization processing tool 5 of this embodiment is disposed downstream of the position where the intake pipe 4 communicates with the flowing water pipe 3, the magnetization processing tool 5 is connected to the flowing water pipe 3 and the intake pipe 4 as shown in FIG. You may arrange | position upstream of the position which communicates. The embodiment of FIG. 1 is preferably applied when the water depth is relatively shallow, and the embodiment of FIG. 2 is preferably applied when the water depth is relatively deep.

上記した構成の汚水処理装置1を流量調整槽内に設置して水中ポンプ2を駆動すると、水中ポンプ2の吸込口20より吸い込まれた槽内の汚水は水中ポンプ2の吐出口21から流水管3の流入口30へ送り込まれる。流水管3に送り込まれた汚水は流水管3内の流路を流れて流出口31より槽内へ流出されるが、流路の途中で吸気管4から流水管3に導入された空気が気泡となって水流に混入する。その結果、流出口31より槽内へ気液混合流として噴射され、これにより撹拌と曝気とが行われる。   When the sewage treatment apparatus 1 having the above-described configuration is installed in the flow rate adjusting tank and the submersible pump 2 is driven, the sewage in the tank sucked from the suction port 20 of the submersible pump 2 flows from the discharge port 21 of the submersible pump 2 to the flowing water pipe. 3 inflow port 30. The sewage sent to the water flow pipe 3 flows through the flow path in the flow water pipe 3 and flows out from the outlet 31 into the tank, but air introduced into the flow water pipe 3 from the intake pipe 4 in the middle of the flow path is a bubble. Become mixed into the water stream. As a result, it is injected as a gas-liquid mixed flow from the outlet 31 into the tank, whereby stirring and aeration are performed.

流水管3を流れる汚水は磁化処理具5によって磁化処理される。図1の実施例では水と気泡とに直接磁界が作用するが、図2の実施例では水にのみ磁界が直接作用する。水が磁界の作用を受けて磁化されると、水のクラスタが細分化されるので、水が周囲から酸素を奪う作用(還元作用)が強くなって酸素の取込み量が増し、流量調整槽の容量が大きく水深が深くても、曝気による浄化機能が十分に発揮される。さらに、気泡が磁界の作用を受けると、気泡の細分化も促進され、水と空気との接触面積が増す結果、水への酸素の取込み量が増し、曝気による浄化機能が一層促進される。   The sewage flowing through the water pipe 3 is magnetized by the magnetizing tool 5. In the embodiment of FIG. 1, a magnetic field directly acts on water and bubbles, whereas in the embodiment of FIG. 2, a magnetic field directly acts only on water. When water is magnetized under the action of a magnetic field, the water clusters are subdivided, so the action of water depriving oxygen from the surroundings (reduction action) increases and the amount of oxygen taken up increases, Even if the capacity is large and the water depth is deep, the purification function by aeration is sufficiently exerted. Further, when the bubbles are subjected to the action of a magnetic field, the fragmentation of the bubbles is also promoted, the contact area between water and air is increased, the amount of oxygen taken into water is increased, and the purification function by aeration is further promoted.

この考案の一実施例である汚水処理装置の側面図である。It is a side view of the sewage treatment apparatus which is one Example of this device. 他の実施例の側面図である。It is a side view of another Example. 磁化処理具の側面図である。It is a side view of a magnetization processing tool. 図3のA−A線に沿う断面図である。It is sectional drawing which follows the AA line of FIG. 汚水処理施設の構成を示す説明図である。It is explanatory drawing which shows the structure of a sewage treatment facility. 流量調整槽に従来の汚水処理装置を設置した状態を示す説明図である。It is explanatory drawing which shows the state which installed the conventional sewage treatment apparatus in the flow control tank.

符号の説明Explanation of symbols

1 汚水処理装置
2 水中ポンプ
3 流水管
4 吸気管
5 磁化処理具
6 管状体
10 流量調整槽
20 吸入口
21 吐出口
30 流入口
31 流出口
32 連結部
71 永久磁石
DESCRIPTION OF SYMBOLS 1 Sewage treatment apparatus 2 Submersible pump 3 Flowing water pipe 4 Intake pipe 5 Magnetization processing tool 6 Tubular body 10 Flow rate adjustment tank 20 Inlet 21 Outlet 30 Outlet 31 Outlet 32 Connecting part 71 Permanent magnet

Claims (1)

汚水処理施設の曝気槽へ汚水を一定の流量で送り出すための流量調整槽に設けられる汚水処理装置であって、
吸込口および吐出口を有する水中ポンプと、一端に流入口、他端に流出口、前記流入口に近い位置に連結部をそれぞれ備えた流水管と、上端および下端が開口した吸気管と、両端が開口した扁平な断面形状の管状体を有し、前記管状体の通路幅が小さい側の対向する壁面に異なる磁極が向き合うように複数の永久磁石が外付けされて成る磁化処理具とから成り、
前記水中ポンプおよび流水管を前記流量調整槽の底面上に水没状態で設置し、前記流水管は、流出口を流量調整槽内に位置させかつ流入口を水中ポンプの吐出口に接続するとともに、前記吸気管は、上端の開口を水面上に位置させかつ流水管内の流路に連通するように下端の開口を流水管の連結部に連結しており、
前記流水管の吸気管が連通する位置の下流に、前記管状体を流水管の途中に介装させるようにして前記磁化処理具を配置して、流水管を流れる水と、前記流水管内の水流により負圧化された吸気管によって流水管に導入された空気とに前記磁化処理具による磁界を作用させるようにした汚水処理装置。
A sewage treatment apparatus provided in a flow rate adjusting tank for sending sewage at a constant flow rate to an aeration tank of a sewage treatment facility,
A submersible pump having a suction port and a discharge port; an inflow port at one end; an outflow port at the other end; an inflow pipe having a connecting portion at a position close to the inflow port; an intake pipe having upper and lower ends opened; And a magnetizing tool comprising a plurality of permanent magnets externally attached so that different magnetic poles face opposite wall surfaces of the tubular body having a small passage width. ,
The submersible pump and the water pipe are installed in a submerged state on the bottom surface of the flow rate adjusting tank, the water pipe has an outlet located in the flow rate adjusting tank and the inlet is connected to the outlet of the submersible pump, The intake pipe has an opening at the upper end located on the water surface and has an opening at the lower end connected to the connecting portion of the water flow pipe so as to communicate with a flow path in the water flow pipe.
The magnetization processing tool is disposed downstream of the position where the intake pipe of the water pipe communicates with the tubular body in the middle of the water pipe, and the water flowing in the water pipe and the water flow in the water pipe A sewage treatment apparatus that causes a magnetic field generated by the magnetization treatment tool to act on the air introduced into the flow water pipe by the intake pipe that has been made negative by the pressure.
JP2006009096U 2006-11-08 2006-11-08 Sewage treatment equipment Expired - Lifetime JP3128828U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2006009096U JP3128828U (en) 2006-11-08 2006-11-08 Sewage treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2006009096U JP3128828U (en) 2006-11-08 2006-11-08 Sewage treatment equipment

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP2003349629A Continuation JP2005111378A (en) 2003-10-08 2003-10-08 Sewage treatment equipment

Publications (1)

Publication Number Publication Date
JP3128828U true JP3128828U (en) 2007-01-25

Family

ID=43279829

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2006009096U Expired - Lifetime JP3128828U (en) 2006-11-08 2006-11-08 Sewage treatment equipment

Country Status (1)

Country Link
JP (1) JP3128828U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113800715A (en) * 2021-09-15 2021-12-17 北京清河北苑水务有限公司 Sewage treatment system and method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113800715A (en) * 2021-09-15 2021-12-17 北京清河北苑水务有限公司 Sewage treatment system and method

Similar Documents

Publication Publication Date Title
CN101704590B (en) Self-discharging cylinder micro/nano-grade sieve air-flotation system for sewage treatment
WO2011001819A1 (en) Water treatment device and method for cleaning filtration material layer for water treatment device
US20200055756A1 (en) Eductor-based membrane bioreactor
KR100843656B1 (en) Advanced drinking water treatment system using two-stage submerged membranes
JP2007275893A (en) Method for producing gas-liquid mixture, and the gas-liquid mixture
JP4538404B2 (en) Water purification apparatus, water pollution organism recovery ship, and water pollution organism treatment method
JP2939704B2 (en) Fine bubble discharge device
WO2007125996A1 (en) Water quality improving unit and water quality improving device
JP2005111378A (en) Sewage treatment equipment
JP5439344B2 (en) Membrane separation biological treatment equipment
JP3128828U (en) Sewage treatment equipment
CN207227211U (en) A kind of micro-nano bubble processing unit of the chlorine dioxide of dyeing waste water
JP4908875B2 (en) Water quality improvement device
CN209276206U (en) A kind of eddy flow magnetic separator
CN205367909U (en) Portable pure oxygen bubbling machine on water
KR101662430B1 (en) Conduit type apparatus for treating wastewater
CN214115164U (en) Waste water treatment equipment for circulating water tank of spray tower
JP3263267B2 (en) Septic tank
KR20060014079A (en) ommitted
JP2002370095A (en) Liquid cleaning apparatus
CN111847563A (en) Air-floatation treatment method for sewage
CN206345719U (en) Handle the reaction unit of organic wastewater
CN201817362U (en) Novel integrated water treatment equipment
JP2004008969A (en) Method for removing iron in water using jet stream generator and system therefor
CN213060274U (en) Air floatation machine

Legal Events

Date Code Title Description
R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

EXPY Cancellation because of completion of term
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20091227

Year of fee payment: 3