Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP4483664B2 - Sludge treatment equipment - Google Patents
[go: Go Back, main page]

JP4483664B2 - Sludge treatment equipment - Google Patents

Sludge treatment equipment Download PDF

Info

Publication number
JP4483664B2
JP4483664B2 JP2005109671A JP2005109671A JP4483664B2 JP 4483664 B2 JP4483664 B2 JP 4483664B2 JP 2005109671 A JP2005109671 A JP 2005109671A JP 2005109671 A JP2005109671 A JP 2005109671A JP 4483664 B2 JP4483664 B2 JP 4483664B2
Authority
JP
Japan
Prior art keywords
sludge
treatment tank
treatment
ultrasonic
tank
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 - Fee Related
Application number
JP2005109671A
Other languages
Japanese (ja)
Other versions
JP2006289180A (en
Inventor
真一郎 淵上
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Corp
Panasonic Holdings Corp
Original Assignee
Panasonic Corp
Matsushita Electric Industrial Co Ltd
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 Panasonic Corp, Matsushita Electric Industrial Co Ltd filed Critical Panasonic Corp
Priority to JP2005109671A priority Critical patent/JP4483664B2/en
Publication of JP2006289180A publication Critical patent/JP2006289180A/en
Application granted granted Critical
Publication of JP4483664B2 publication Critical patent/JP4483664B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Treatment Of Sludge (AREA)

Description

本発明は、排水処理により発生する排液中の有機物の大幅な減量を可能とする汚泥処理装置に関する。   The present invention relates to a sludge treatment apparatus that enables a significant reduction in the amount of organic matter in waste liquid generated by waste water treatment.

従来の汚泥減量化技術には、生物・化学的汚泥処理と、物理的汚泥処理があり、生物・化学的汚泥処理は化学薬品等を使用して短時間(8時間程度)で処理するもので、大容量の汚泥処理に向いており、物理的汚泥処理は超音波等を利用して長時間(24時間程度)掛けて処理するもので、小容量の汚泥処理に向いている(例えば特許文献1、特許文献2参照)。   Conventional sludge reduction technologies include biological / chemical sludge treatment and physical sludge treatment. Biological / chemical sludge treatment is performed in a short time (about 8 hours) using chemicals. It is suitable for large-capacity sludge treatment, and physical sludge treatment is performed for a long time (about 24 hours) using ultrasonic waves, etc., and is suitable for small-capacity sludge treatment (for example, Patent Documents). 1, see Patent Document 2).

そして例えば特許文献2の処理技術では、有機性汚水を好気性生物処理槽で処理し、沈殿槽で固液分離して処理水と汚泥とを得る。この汚泥を返送汚泥として好気性生物処理槽に循環するとともに、一部を余剰汚泥として貯留槽に導入する。貯留槽ではその汚泥を超音波発振子から発振される超音波を用いて可溶化処理を行い、可溶化汚泥として好気性生物処理槽に返して生物分解を行うことにより、汚泥を減容する方法が開示されている。   For example, in the treatment technique disclosed in Patent Document 2, organic sewage is treated in an aerobic biological treatment tank, and solid-liquid separation is performed in a sedimentation tank to obtain treated water and sludge. This sludge is circulated to the aerobic biological treatment tank as return sludge and a part is introduced into the storage tank as surplus sludge. In the storage tank, the sludge is solubilized using ultrasonic waves oscillated from an ultrasonic oscillator, and returned to the aerobic biological treatment tank as solubilized sludge for biodegradation. Is disclosed.

また、特に紫外線照射による汚泥の可溶化率を高めるために、紫外線照射による汚泥の可溶化処理に加えて超音波照射処理を併用する処理装置が提案されている(例えば特許文献3参照)。
特開平5−345192号公報 特開平11−128975号公報 特開2004−113918号公報
Moreover, in order to raise the sludge solubilization rate especially by ultraviolet irradiation, in addition to the sludge solubilization processing by ultraviolet irradiation, a processing apparatus that uses ultrasonic irradiation processing in combination has been proposed (for example, see Patent Document 3).
JP-A-5-345192 Japanese Patent Laid-Open No. 11-128975 JP 2004-113918 A

しかし、上記従来の処理装置は、超音波振動子の長寿命化、低消費電力でコンパクトな装置を図ることは提案されておらず、また超音波処理の安定化や信頼性を高めることについても提案されていない。   However, it has not been proposed that the above-described conventional processing apparatus is a compact apparatus with a long life of the ultrasonic transducer and low power consumption, and it is also about improving the stabilization and reliability of the ultrasonic processing. Not proposed.

そこで、本発明は汚泥濃度が高い場合でも、汚泥の嫌気化による悪臭を防止し、超音波処理を効率よく行うことができる汚泥処理装置を提供することを目的とする。   Therefore, an object of the present invention is to provide a sludge treatment apparatus that can prevent bad odor due to anaerobic formation of sludge and efficiently perform ultrasonic treatment even when the sludge concentration is high.

また、本発明は、超音波処理により発生する泡沫を超音波処理槽から効率良く除去し、超音波処理を安定化し、信頼性を高めることのできる汚泥処理装置を提供することを目的とする。   Another object of the present invention is to provide a sludge treatment apparatus capable of efficiently removing foam generated by ultrasonic treatment from the ultrasonic treatment tank, stabilizing the ultrasonic treatment, and improving reliability.

請求項1記載の本発明の汚泥処理装置は、超音波処理槽に超音波振動子を備えた汚泥処理装置において、前記超音波処理槽を、堰によって第1の処理槽と第2の処理槽に区分し、前記第1の処理槽に汚泥の流入口と前記超音波振動子を備え、前記第2の処理槽に超音波処理汚泥の流出口を備え、前記第2の処理槽を前記第1の処理槽の外部に設け、前記堰の上端面を水平に保持し、前記第1の処理槽に曝気手段を設けたものである。   The sludge treatment apparatus of the present invention according to claim 1 is the sludge treatment apparatus comprising an ultrasonic vibrator in an ultrasonic treatment tank, wherein the ultrasonic treatment tank is divided into a first treatment tank and a second treatment tank by a weir. The first treatment tank is provided with a sludge inlet and the ultrasonic vibrator, the second treatment tank is provided with an ultrasonic treatment sludge outlet, and the second treatment tank is provided with the second treatment tank. It is provided outside the one processing tank, the upper end surface of the weir is held horizontally, and aeration means is provided in the first processing tank.

請求項2記載の本発明は、請求項1に記載の汚泥処理装置において、前記第2の処理槽を前記第1の処理槽の両側部にそれぞれ設け、一方の前記第2の処理槽における前記堰の上端面と、他方の前記第2の処理槽における前記堰の上端面との高さを異ならせたものである。   According to a second aspect of the present invention, in the sludge treatment apparatus according to the first aspect, the second treatment tank is provided on both side portions of the first treatment tank, and the second treatment tank includes the second treatment tank. The upper end surface of the weir is different from the upper end surface of the weir in the other second processing tank.

請求項3記載の本発明は、請求項1または2に記載の汚泥処理装置において、前記第1の処理槽における前記超音波振動子の超音波照射面と超音波反射面とからなる超音波の音場空間の外部に前記曝気手段を設けたものである。   According to a third aspect of the present invention, in the sludge treatment apparatus according to the first or second aspect, an ultrasonic wave comprising an ultrasonic irradiation surface and an ultrasonic reflection surface of the ultrasonic transducer in the first treatment tank. The aeration means is provided outside the sound field space.

請求項4記載の本発明は、請求項1または2に記載の汚泥処理装置において、前記超音波の音場空間と前記曝気手段を設けた曝気部とを仕切板で区切り、前記仕切板の下端と前記第1の処理槽の底部との間に空間を設けたものである。   According to a fourth aspect of the present invention, in the sludge treatment apparatus according to the first or second aspect, the ultrasonic sound field space and the aeration section provided with the aeration means are separated by a partition plate, and the lower end of the partition plate And a space between the bottom of the first treatment tank.

請求項5記載の本発明は、請求項1または2に記載の汚泥処理装置において、前記堰の上端面を凸曲面で構成したことを特徴とする。   According to a fifth aspect of the present invention, in the sludge treatment apparatus according to the first or second aspect, the upper end surface of the weir is a convex curved surface.

請求項6記載の本発明は、請求項1または2に記載の汚泥処理装置において、前記第2の処理槽に前記堰の上端面と前記第2の処理槽の底面とを結ぶ汚泥案内板を設け、前記汚泥案内板と前記堰の角度が0度以上45度以下としたものである。   According to a sixth aspect of the present invention, in the sludge treatment apparatus according to the first or second aspect, a sludge guide plate that connects the upper end surface of the weir and the bottom surface of the second treatment tank to the second treatment tank. Provided, and an angle between the sludge guide plate and the weir is set to 0 degrees or more and 45 degrees or less.

請求項7記載の本発明は、請求項1または2に記載の汚泥処理装置において、前記第2の処理槽の内壁に疎水性の表面処理を施したことを特徴とする。   According to a seventh aspect of the present invention, in the sludge treatment apparatus according to the first or second aspect, a hydrophobic surface treatment is performed on the inner wall of the second treatment tank.

請求項8記載の本発明は、請求項1または2に記載の汚泥処理装置において、 前記超音波処理槽の上部に蓋体を設け、前記蓋体下部より消泡水を噴出することを特徴とする。   The present invention according to claim 8 is the sludge treatment apparatus according to claim 1 or 2, wherein a lid is provided at an upper portion of the ultrasonic treatment tank, and defoamed water is ejected from the lower portion of the lid. To do.

請求項9記載の本発明は、請求項1または2に記載の汚泥処理装置において、前記第1の処理槽内の液面を振動させる手段を有することを特徴とする。   A ninth aspect of the present invention is the sludge treatment apparatus according to the first or second aspect, further comprising means for vibrating the liquid surface in the first treatment tank.

請求項10記載の本発明は、請求項1または2に記載の汚泥処理装置において、 前記第1の処理槽内の液面の浮遊物を、前記第1の処理槽から前記第2の処理槽へ掃きだす手段を有することを特徴とする。   The present invention according to claim 10 is the sludge treatment apparatus according to claim 1 or 2, wherein the suspended matter on the liquid level in the first treatment tank is transferred from the first treatment tank to the second treatment tank. It has a means for sweeping out.

請求項11記載の本発明は、請求項1または2に記載の汚泥処理装置において、 前記第1の処理槽内の液面の浮遊物を、前記第1の処理槽から前記第2の処理槽へ風圧で押し流す送風手段を有することを特徴とする。   The present invention according to claim 11 is the sludge treatment apparatus according to claim 1 or 2, wherein the suspended matter on the liquid level in the first treatment tank is transferred from the first treatment tank to the second treatment tank. It is characterized by having a blower means for sweeping away by wind pressure.

本発明は、超音波処理槽に超音波の音場空間を避けて空気を供給することにより、気泡による超音波の減衰を引き起こすことなく汚泥の溶存酸素濃度を高めることができる。このため、汚泥が高濃度であっても嫌気状態となるのを防ぎ、嫌気性泡沫の発生や悪臭の発生を防止し、かつ溶存酸素がキャビテーションの核となるので超音波によるキャビテーションを効率よく発生させることができるという効果を奏する。   The present invention can increase the dissolved oxygen concentration of sludge without causing ultrasonic attenuation due to bubbles by supplying air to the ultrasonic treatment tank while avoiding the ultrasonic field. This prevents anaerobic conditions even at high concentrations of sludge, prevents the formation of anaerobic foams and odors, and efficiently generates ultrasonic cavitation because dissolved oxygen is the nucleus of cavitation. There is an effect that can be made.

また、本発明は、超音波処理槽を、堰によって第1の処理槽と第2の処理槽に区分し、第1の処理槽に処理汚泥の流入口と超音波振動子を備え、第2の処理槽に処理汚泥の流出口を備え、第2の処理槽を第1の処理槽の外部に設け、凸曲面で構成した堰の上端面を水平に保持し、第2の処理槽に堰の上端面と第2の処理槽の底面とを結ぶ汚泥案内板を設けることで超音波処理により発生する泡沫を超音波処理槽から効率良く除去し、超音波処理を安定化し、装置の信頼性を高めることができるという効果を奏する。   In the present invention, the ultrasonic treatment tank is divided into a first treatment tank and a second treatment tank by a weir, the first treatment tank is provided with a treatment sludge inlet and an ultrasonic vibrator, The treatment tank is provided with a treatment sludge outlet, the second treatment tank is provided outside the first treatment tank, the upper end surface of the weir composed of convex curved surfaces is held horizontally, and the second treatment tank By providing a sludge guide plate that connects the upper end surface of the second treatment tank and the bottom surface of the second treatment tank, foam generated by the ultrasonic treatment can be efficiently removed from the ultrasonic treatment tank, the ultrasonic treatment is stabilized, and the reliability of the apparatus There is an effect that can be increased.

本発明の第1の実施の形態による汚泥処理装置は、超音波処理槽に超音波振動子を備えた汚泥処理装置において、超音波処理槽を、堰によって第1の処理槽と第2の処理槽に区分し、第1の処理槽に処理汚泥の流入口と超音波振動子を備え、第2の処理槽に処理汚泥の流出口を備え、第2の処理槽を第1の処理槽の外部に設け、堰の上端面を水平に保持し、第1の処理槽に曝気手段を設けたものである。本実施の形態によれば、第1の処理槽内の汚泥に空気を送り込むことができるので、第1の処理槽内の汚泥の溶存酸素濃度を維持し、汚泥が嫌気状態となるのを防ぎ、嫌気性泡沫の発生や悪臭の発生を防止することができる。また、堰の上端面が水平であるため、第1の処理槽から流出する超音波処理汚泥は堰の全面に渡って均一に流出し、その結果超音波処理槽内の汚泥の流れが整流されて偏りのない流れとなり、超音波処理が均一に行われる。  The sludge treatment apparatus according to the first embodiment of the present invention is a sludge treatment apparatus provided with an ultrasonic vibrator in an ultrasonic treatment tank. The ultrasonic treatment tank is divided into a first treatment tank and a second treatment by a weir. The first treatment tank is provided with a treatment sludge inlet and an ultrasonic vibrator, the second treatment tank is provided with a treatment sludge outlet, and the second treatment tank is connected to the first treatment tank. It is provided outside, the upper end surface of the weir is held horizontally, and aeration means is provided in the first treatment tank. According to this embodiment, since air can be sent into the sludge in the first treatment tank, the dissolved oxygen concentration of the sludge in the first treatment tank is maintained, and the sludge is prevented from becoming anaerobic. It is possible to prevent the generation of anaerobic foam and the generation of bad odor. Moreover, since the upper end surface of the weir is horizontal, the sonication sludge flowing out from the first treatment tank flows out uniformly over the entire surface of the weir, and as a result, the flow of sludge in the sonication tank is rectified. Therefore, the flow becomes uniform and ultrasonic treatment is performed uniformly.

本発明の第2の実施の形態は、第1の実施の形態による汚泥処理装置において、第2の処理槽を第1の処理槽の両側部にそれぞれ設け、一方の第2の処理槽における堰の上端面と、他方の第2の処理槽における堰の上端面との高さを異ならせたものである。本実施の形態によれば、一方の第2の処理槽の流出口が異物などによって閉塞した場合であっても、他方の第2の処理槽に越流することができるので、汚泥の処理を確実に行うことができるとともに、オーバーフローを回避することができる。   The second embodiment of the present invention is the sludge treatment apparatus according to the first embodiment, wherein the second treatment tank is provided on both sides of the first treatment tank, and the weir in one second treatment tank. And the height of the upper end surface of the weir in the other second processing tank are different. According to the present embodiment, even if the outlet of one of the second treatment tanks is blocked by foreign matter or the like, it can overflow to the other second treatment tank, so that the sludge can be treated. This can be performed reliably and overflow can be avoided.

本発明の第3の実施の形態は、第1、第2の実施の形態による汚泥処理装置において、第1の処理槽における超音波振動子の超音波照射面と超音波反射面とからなる超音波の音場空間の外部に曝気手段を設けたものである。本実施の形態によれば、超音波の音場空間を避けて空気を供給することができるために、気泡による超音波の減衰を引き起こすことなく第1の処理槽内の汚泥の溶存酸素濃度を高めることができ、汚泥が嫌気状態となるのを防ぎ、嫌気性泡沫の発生や悪臭の発生を防止し、かつ溶存酸素がキャビテーションの核となるので超音波によるキャビテーションをより効率よく発生させることができる。   According to a third embodiment of the present invention, in the sludge treatment apparatus according to the first and second embodiments, an ultrasonic wave composed of an ultrasonic irradiation surface and an ultrasonic reflection surface of an ultrasonic transducer in the first treatment tank. Aeration means is provided outside the sound field space of the sound wave. According to the present embodiment, since air can be supplied while avoiding the acoustic field space of ultrasonic waves, the dissolved oxygen concentration of the sludge in the first treatment tank is reduced without causing ultrasonic attenuation by bubbles. It is possible to prevent the sludge from becoming anaerobic, to prevent the formation of anaerobic foam and bad odor, and because dissolved oxygen becomes the core of cavitation, it is possible to generate ultrasonic cavitation more efficiently. it can.

本発明の第4の実施の形態は、第1、第2の実施の形態による汚泥処理装置において、音場空間と曝気手段を設けた曝気部とを仕切板で区切り、仕切板の下端と第1の処理槽の底部との間に空間を設けたものである。本実施の形態によれば、超音波の音場空間を避けて空気を供給することができるために、気泡による超音波の減衰を起こすことなく第1の処理槽内の汚泥の溶存酸素濃度を高めることができ、汚泥が嫌気状態となるのを防ぎ、嫌気性泡沫の発生や悪臭の発生を防止し、かつ溶存酸素がキャビテーションの核となるので超音波によるキャビテーションをより効率よく発生させることができる。また、曝気部と音場空間が仕切板で区切られ、仕切板の下端と第1処理槽の底部との間に空間が設けられているために、エアリフト効果による撹拌が効果的に行われ、超音波処理を効率よく行うことができる。   According to a fourth embodiment of the present invention, in the sludge treatment apparatus according to the first and second embodiments, the sound field space and the aeration section provided with the aeration means are separated by a partition plate, and the lower end of the partition plate and the first A space is provided between the bottom of one processing tank. According to the present embodiment, since air can be supplied while avoiding the acoustic field space of ultrasonic waves, the dissolved oxygen concentration of the sludge in the first treatment tank is reduced without causing ultrasonic attenuation due to bubbles. It is possible to prevent the sludge from becoming anaerobic, to prevent the formation of anaerobic foam and bad odor, and because dissolved oxygen becomes the core of cavitation, it is possible to generate ultrasonic cavitation more efficiently. it can. In addition, since the aeration section and the sound field space are separated by a partition plate, and a space is provided between the lower end of the partition plate and the bottom portion of the first treatment tank, stirring by the air lift effect is effectively performed, Sonication can be performed efficiently.

本発明の第5の実施の形態は、第1、第2の実施の形態による汚泥処理装置において、堰の上端面を凸曲面で構成したものである。本実施の形態によれば、第1の処理槽の液面に浮上した異物や泡沫が堰部分に滞留しにくく、効率的に第2の処理槽に排出することができる。   In the fifth embodiment of the present invention, in the sludge treatment apparatus according to the first and second embodiments, the upper end surface of the weir is formed by a convex curved surface. According to this Embodiment, the foreign material and foam which floated on the liquid level of the 1st processing tank are hard to stay in a dam part, and can be efficiently discharged | emitted to a 2nd processing tank.

本発明の第6の実施の形態は、第1、第2の実施の形態による汚泥処理装置において、第2の処理槽に堰の上端面と第2の処理槽の底面とを結ぶ汚泥案内板を設け、汚泥案内板と堰の角度が0度以上45度以下としたものである。本実施の形態によれば、第1の処理槽から第2の処理槽へ越流する汚泥の流れが緩やかに曲がることができるので、堰の上端面や堰の第2の処理槽側の面に異物や泡沫の付着を防止することができる。   The sixth embodiment of the present invention is a sludge guide plate for connecting the upper end surface of the weir and the bottom surface of the second treatment tank to the second treatment tank in the sludge treatment apparatus according to the first and second embodiments. The angle between the sludge guide plate and the weir is 0 degree or more and 45 degrees or less. According to the present embodiment, the sludge flow that overflows from the first treatment tank to the second treatment tank can bend gently, so that the upper end surface of the weir and the surface of the weir on the second treatment tank side It is possible to prevent foreign matter and foam from adhering to the surface.

本発明の第7の実施の形態は、第1、第2の実施の形態による汚泥処理装置において、第2の処理槽の内壁に疎水性の表面処理を施したものである。本実施の形態よれば、第1の処理槽から堰を越流した汚泥が薄く延ばされて第2の処理槽を流下する際に、汚泥中の固形分が第2の処理槽内壁に付着することを防止でき、悪臭の発生を防ぐことができる。   In the seventh embodiment of the present invention, in the sludge treatment apparatus according to the first and second embodiments, a hydrophobic surface treatment is applied to the inner wall of the second treatment tank. According to the present embodiment, when the sludge that has overflowed the weir from the first treatment tank is thinly extended and flows down the second treatment tank, the solid content in the sludge adheres to the inner wall of the second treatment tank. Can be prevented, and the generation of malodor can be prevented.

本発明の第8の実施の形態は、第1、第2の実施の形態による汚泥処理装置において、超音波処理槽の上部に蓋体を設け、蓋体下部より消泡水を噴出するようにしたものである。本実施の形態によれば、第1の処理槽や第2の処理槽に泡沫が発生し、蓄積した場合でも、蓋体下部より消泡水を噴出することにより泡沫を消すことができ、悪臭の発生を防ぐことができる。   In the eighth embodiment of the present invention, in the sludge treatment apparatus according to the first and second embodiments, a lid is provided at the upper part of the ultrasonic treatment tank, and defoamed water is ejected from the lower part of the lid. It is a thing. According to the present embodiment, even when foam is generated and accumulated in the first processing tank or the second processing tank, the foam can be erased by ejecting defoaming water from the lower part of the lid, and bad odor Can be prevented.

本発明の第9の実施の形態は、第1、第2の実施の形態による汚泥処理装置において、第1の処理槽内の液面を振動させる手段を有したものである。本実施の形態によれば、第1の処理槽に泡沫が発生し、蓄積した場合でも、第1の処理槽内の液面を振動させることにより、泡沫を堰を越流させて第2の処理槽へ押し流すことができ、悪臭の発生を防止することができる。   The ninth embodiment of the present invention has means for vibrating the liquid surface in the first treatment tank in the sludge treatment apparatus according to the first and second embodiments. According to the present embodiment, even when foam is generated and accumulated in the first processing tank, the foam is caused to overflow the weir by vibrating the liquid surface in the first processing tank, and the second It can be washed away into the treatment tank, and the generation of malodor can be prevented.

本発明の第10の実施の形態は、第1、第2の実施の形態による汚泥処理装置において、第1の処理槽内の液面の浮遊物を、第1の処理槽から第2の処理槽へ掃きだす手段を有したものである。本実施の形態によれば、第1の処理槽に泡沫が発生し、蓄積した場合でも、第1の処理槽内の液面の浮遊物を第2の処理槽へ掃きだすことにより、泡沫を堰を越流させて第2の処理槽へ押し流すことができ、悪臭の発生を防止することができる。   In the sludge treatment apparatus according to the first and second embodiments, the tenth embodiment of the present invention applies the second treatment from the first treatment tank to the suspended matter on the liquid surface in the first treatment tank. It has a means to sweep into the tank. According to the present embodiment, even when foam is generated and accumulated in the first treatment tank, the foam is removed by sweeping the liquid level floating material in the first treatment tank to the second treatment tank. Overflow of the weir can be carried out to the second treatment tank, and generation of malodor can be prevented.

本発明の第11の実施の形態は、第1、第2の実施の形態による汚泥処理装置において、第1の処理槽内の液面の浮遊物を、第1の処理槽から第2の処理槽へ風圧で押し流す送風手段を有したものである。本実施の形態によれば、第1の処理槽に泡沫が発生し、蓄積した場合でも、第1の処理槽内の液面の浮遊物を第2の処理槽へ風圧によって泡沫を堰を越流させて第2の処理槽へ押し流すことができ、悪臭の発生を防止することができる。   In an eleventh embodiment of the present invention, in the sludge treatment apparatus according to the first and second embodiments, liquid surface floating matter in the first treatment tank is transferred from the first treatment tank to the second treatment. It has an air blowing means that pushes it into the tank with wind pressure. According to the present embodiment, even when foam is generated and accumulated in the first treatment tank, the suspended matter on the liquid level in the first treatment tank is passed through the weir to the second treatment tank by wind pressure. It can be made to flow and be washed away into the second treatment tank, and the generation of malodor can be prevented.

以下、本発明による実施例の汚泥処理装置について、図面を参照して説明する。図1は本発明の一実施例による汚泥処理装置を示す構成図、図2は超音波処理槽50を上面からみた概略図、図3は超音波処理槽50を正面から見た断面の概略図、図4は超音波反応槽50を側面から見た断面の概略図である。工場や下水処理場などから排出される排液や汚泥は、図示しない排液貯留槽に貯留されている。この排液や汚泥に対して何らかの処理を施して再利用や減容を行う場合には、まず排液に含まれる異物を除去することが重要である。   Hereinafter, the sludge treatment apparatus of the Example by this invention is demonstrated with reference to drawings. FIG. 1 is a block diagram showing a sludge treatment apparatus according to an embodiment of the present invention, FIG. 2 is a schematic view of an ultrasonic treatment tank 50 as viewed from above, and FIG. 3 is a schematic view of a cross section of the ultrasonic treatment tank 50 as seen from the front. 4 is a schematic cross-sectional view of the ultrasonic reaction tank 50 as viewed from the side. Drainage and sludge discharged from factories and sewage treatment plants are stored in a drainage storage tank (not shown). When reusing or reducing the volume of waste liquid or sludge by performing some kind of treatment, it is important to first remove foreign substances contained in the waste liquid.

本実施例による汚泥処理装置は、図1において本体ケース1内に、高速旋回分離槽20と低速旋回分離槽30と超音波処理槽50とを備えている。ここで高速旋回分離槽20と低速旋回分離槽30とによって異物分離装置が構成される。高速旋回分離槽20は上部が円筒状で、下部が円錐状のケーシングから構成されており、汚泥取込み管Aから取り込んだ汚泥を少量の中間処理汚泥と残りの汚泥に分岐させるとともに、汚泥に含まれる比較的大きく、重い異物を汚泥とともに汚泥返送管Cを通じて汚泥貯留槽へ還流させるものである。低速旋回分離槽30は円筒状の胴部分31とおわん状の底部分32とで構成されており,低速旋回分離槽30の胴部分31には、中間処理汚泥を低速旋回分離槽30に導入する槽間接続管Bと、処理汚泥を流出する処理汚泥流出管Dとを低速旋回分離槽30内に突き出して設けている。汚泥を導入する槽間接続管Bは、処理汚泥流出管Dより下方側で、底部分32よりも上方側に配置されており、槽間接続管Bの流出口33にはエルボが形成されている。   The sludge treatment apparatus according to this embodiment includes a high-speed swirl separation tank 20, a low-speed swirl separation tank 30, and an ultrasonic treatment tank 50 in the main body case 1 in FIG. Here, the high-speed swirl separation tank 20 and the low-speed swirl separation tank 30 constitute a foreign matter separation device. The high-speed swirling separation tank 20 is composed of a cylindrical casing at the upper part and a conical casing at the lower part. The sludge taken in from the sludge intake pipe A is branched into a small amount of intermediate treatment sludge and the remaining sludge and contained in the sludge. The relatively large and heavy foreign matter is returned to the sludge storage tank through the sludge return pipe C together with the sludge. The low-speed swirling separation tank 30 includes a cylindrical body portion 31 and a bowl-shaped bottom portion 32, and intermediate treatment sludge is introduced into the low-speed swirling separation tank 30 in the body portion 31 of the low-speed swirling separation tank 30. The inter-tank connecting pipe B and the treated sludge outflow pipe D for flowing out the treated sludge are provided so as to protrude into the low-speed swirling separation tank 30. The inter-tank connection pipe B for introducing the sludge is disposed below the treated sludge outflow pipe D and above the bottom portion 32, and an elbow is formed at the outlet 33 of the inter-tank connection pipe B. Yes.

上記の構成において、低速旋回分離槽30内で胴部分31の接線方向へ中間処理汚泥を流出させ、流出させた中間処理汚泥の流速を使って低速旋回分離槽内に緩やかな旋回液流を形成し、低速旋回分離槽内の流れを整流すると共に、低速旋回液流によって発生する弱い遠心力で中間処理汚泥よりも重い質量の異物、例えばトイレットペーパーや毛髪等、を低速旋回分離槽の内周部へ緩やかに移動させつつ凝集させ、重力によって沈降分離することができる。一方、必要な処理汚泥のみを低速旋回分離槽30から取り出し、分離した異物は低速旋回分離槽30の底部の汚泥返送接続管Eから汚泥貯留槽1へ還流させている。処理汚泥流出管Dの導入口34は低速旋回分離槽30内の水面より下であり、導入口34は上側に開口しており、低速旋回分離槽30の水面に浮上した浮遊性の異物、底部32に沈降した沈降性の異物、及び旋回流による慣性力で低速旋回分離槽30の内周へ分離された異物を導入することなく、処理液の排出が可能となっている。このように、超音波反応槽50へ流入させる汚泥に含まれる異物を極力少なくすることで、超音波処理を効率よく行うことができ、超音波振動子の長寿命化を図ることができる。   In the above configuration, the intermediate treatment sludge is caused to flow out in the tangential direction of the body portion 31 in the low speed swirl separation tank 30, and a gentle swirl liquid flow is formed in the low speed swirl separation tank using the flow rate of the discharged intermediate treatment sludge. The flow in the low-speed swirling separation tank is rectified and the foreign matter having a mass heavier than the intermediate treatment sludge, such as toilet paper and hair, is weakened by the weak centrifugal force generated by the low-speed swirling liquid flow. The particles can be agglomerated while being gently moved to the part, and can be separated by gravity. On the other hand, only necessary treatment sludge is taken out from the low-speed swirl separation tank 30, and the separated foreign matter is returned to the sludge storage tank 1 from the sludge return connection pipe E at the bottom of the low-speed swirl separation tank 30. The inlet 34 of the treated sludge outflow pipe D is below the water surface in the low-speed swirling separation tank 30, and the introducing port 34 is open on the upper side. The treatment liquid can be discharged without introducing the sedimentary foreign matter that has settled in 32 and the foreign matter separated into the inner periphery of the low-speed swirl separation tank 30 by the inertial force caused by the swirling flow. As described above, by reducing the foreign matter contained in the sludge flowing into the ultrasonic reaction tank 50 as much as possible, the ultrasonic treatment can be performed efficiently and the life of the ultrasonic vibrator can be extended.

図1〜3において、超音波処理槽50は、その内部に第1の処理槽51と第2の処理槽52A、52Bとを備え、第1の処理槽51と第2の処理槽52A、52Bとは、それぞれ堰53A、53Bによって区画され、第1の処理槽51内の汚泥は、堰53A、53Bを越流して第2の処理槽52A、52Bに導かれる構成となっている。堰53A、53Bは、第1の処理槽51又は第2の処理槽52A、52Bの内壁間に、内壁全幅に渡って上端面が水平となっている。また、堰53A、53Bの上端面は全幅に渡って凸曲面73とし、凸曲面73の第2の処理槽側から堰53A、53Bと約10度の角度で汚泥案内板74を設けている。更に、一方の第2の処理槽52Aにおける堰53Aの上端面と、他方の第2の処理槽52Bにおける堰53Bの上端面との高さを異ならせており、第2の処理槽52A、52B及び汚泥案内板74の内壁はフッ素樹脂によるコーティングが施してある。   1-3, the ultrasonic treatment tank 50 includes a first treatment tank 51 and second treatment tanks 52A and 52B therein, and the first treatment tank 51 and the second treatment tanks 52A and 52B. Is defined by the weirs 53A and 53B, respectively, and the sludge in the first treatment tank 51 flows through the weirs 53A and 53B and is guided to the second treatment tanks 52A and 52B. The weirs 53A and 53B have horizontal upper ends across the entire inner wall width between the inner walls of the first processing tank 51 or the second processing tanks 52A and 52B. Further, the upper end surfaces of the weirs 53A and 53B have a convex curved surface 73 over the entire width, and a sludge guide plate 74 is provided at an angle of about 10 degrees with the weirs 53A and 53B from the second treatment tank side of the convex curved surface 73. Furthermore, the height of the upper end surface of the weir 53A in one second processing tank 52A and the upper end surface of the weir 53B in the other second processing tank 52B are different from each other, so that the second processing tanks 52A and 52B are different. The inner wall of the sludge guide plate 74 is coated with a fluororesin.

また、第1の処理槽51は仕切板72によって、超音波振動子14の超音波照射面と超音波の反射面とからなる音場空間とエアレーター70によって曝気される曝気部とに仕切られており、仕切板72の下端と超音波処理槽50の底部の間には空間が設けられている。   Further, the first treatment tank 51 is partitioned by a partition plate 72 into a sound field space formed by the ultrasonic wave irradiation surface and the ultrasonic wave reflection surface of the ultrasonic vibrator 14 and an aeration unit aerated by the aerator 70. A space is provided between the lower end of the partition plate 72 and the bottom of the ultrasonic treatment tank 50.

また、第1の処理槽51の、堰53A側の面には、超音波振動子14がその放射面が鉛直方向と平行に向くように取り付けられ、この超音波振動子14の取り付けられた面と対向する面(反射壁)に、排液の流入口54が設けられている。この流入口54は、配管Dに接続されている。一方第2の処理槽52A、52Bの下部には、排液を排出する流出口55が設けられている。この流出口55は、配管Fに接続されている。また第1の処理槽51の底面には、第1の処理槽51の底面に沈殿した排液を排出するドレン口56を設けている。排液は、超音波振動子14の取り付け面の上方の堰53Aによって、超音波振動子14の上方から、堰53Aによって一定の水位を保って溢れさせる。   Further, the ultrasonic transducer 14 is attached to the surface of the first treatment tank 51 on the side of the weir 53A so that the radiation surface thereof is parallel to the vertical direction, and the surface to which the ultrasonic transducer 14 is attached. A drainage inflow port 54 is provided on a surface (reflection wall) opposite to. The inflow port 54 is connected to the pipe D. On the other hand, an outlet 55 for discharging the drainage is provided below the second treatment tanks 52A and 52B. The outlet 55 is connected to the pipe F. Further, a drain port 56 is provided on the bottom surface of the first processing tank 51 to discharge the drained liquid that has settled on the bottom surface of the first processing tank 51. The drainage liquid overflows from above the ultrasonic transducer 14 while maintaining a constant water level by the weir 53A above the attachment surface of the ultrasonic transducer 14.

ここで、流入口54は、超音波振動子14の高さ方向に、下部から1/3以下の位置に設けるか、または、第1の処理槽51の底面から堰53Aまでの高さの1/3以下の位置に設ける。そしてこの流入口54は、第1の処理槽51内に波長λ以下の長さの突出部を形成して取り付けることが好ましい。なお、波長λとは超音波の発振周波数をf[Hz]、水中の音速をa[m/s]とした時にλ=a/f[m]で表される。   Here, the inflow port 54 is provided at a position of 1/3 or less from the lower side in the height direction of the ultrasonic transducer 14, or 1 in height from the bottom surface of the first treatment tank 51 to the weir 53 </ b> A. / 3 or less. The inflow port 54 is preferably attached by forming a protrusion having a length of λ or less in the first processing tank 51. The wavelength λ is expressed by λ = a / f [m] where the ultrasonic oscillation frequency is f [Hz] and the sound velocity in water is a [m / s].

上記の構成において、堰53A、53Bの上端面が水平で凸曲面となっているので、堰53A、53Bの上端面における表面張力の影響を小さくすることができ、第1の処理槽51から流出する超音波処理汚泥を、堰53A、53Bの全面に渡って均一に流出させることができる。この結果、第1の処理槽51内の汚泥の流れが整流されて偏りのない流れとなり、超音波処理を均一に行うことができ、第1の処理槽51の液面に浮上した異物や泡沫が第1の処理槽51の堰部分53A、53Bに滞留しないようにすることができる。   In the above configuration, since the upper end surfaces of the weirs 53A and 53B are horizontal and convex curved surfaces, the influence of the surface tension on the upper end surfaces of the weirs 53A and 53B can be reduced, and the outflow from the first treatment tank 51 occurs. The ultrasonically treated sludge can be uniformly discharged over the entire surface of the weirs 53A and 53B. As a result, the flow of sludge in the first treatment tank 51 is rectified and becomes a non-biased flow, so that the ultrasonic treatment can be performed uniformly, and the foreign matter or foam that has floated on the liquid surface of the first treatment tank 51 can be obtained. Can be prevented from staying in the weir portions 53A and 53B of the first treatment tank 51.

また、堰53A、53Bの上端面を越流した超音波処理汚泥が汚泥案内板74を流下することで、堰53A、53Bを垂直に流下する場合に比べ、第1の処理槽51から越流する超音波処理汚泥の流れが滑らかに転向することとなり、堰53A、53Bの上端面に異物が付着することを防ぐことができ、特に、髪の毛やトイレットペーパーなどのように細長い形状の異物の付着を防ぐ場合に有効である。なお、第2の処理槽52A、52B及び汚泥案内板74の内壁はフッ素樹脂コーティングにより、汚泥や異物が付着し難くなっている。   Further, the ultrasonic treatment sludge that has flowed over the upper end surfaces of the weirs 53A and 53B flows down the sludge guide plate 74, so that it overflows from the first treatment tank 51 as compared with the case where the weirs 53A and 53B flow down vertically. As a result, the flow of the ultrasonically treated sludge is smoothly turned, and foreign matter can be prevented from adhering to the upper end surfaces of the weirs 53A and 53B. It is effective in preventing The inner walls of the second treatment tanks 52A and 52B and the sludge guide plate 74 are hard to adhere sludge and foreign matter due to the fluororesin coating.

また、汚泥案内板74の表面を超音波処理汚泥が流下する際に、汚泥案内板74に垂直な方向に汚泥の重さの分力が加わることとなり、汚泥と汚泥案内板間に摩擦力が生じ、汚泥案内板74の表面に異物が付着することを防ぐことができる。   In addition, when the ultrasonic treatment sludge flows down the surface of the sludge guide plate 74, a component force of the sludge weight is applied in a direction perpendicular to the sludge guide plate 74, and a frictional force is generated between the sludge and the sludge guide plate. It is possible to prevent foreign matter from adhering to the surface of the sludge guide plate 74.

また、一方の第2の処理槽52Aにおける堰53Aの上端面と、他方の第2の処理槽52Bにおける堰53Bの上端面との高さを異ならせることで、高さの低い堰53Aのみへ超音波処理汚泥を越流させることとなり、堰53Aを越流する超音波処理汚泥の流量を2倍にすることができるので、汚泥中の固形分が第2の処理槽52Aの内壁に付着し、悪臭の原因や流出口55の閉塞の原因となることを防ぐことができる。何らかの原因で、第2の処理槽52Aの流出口55が汚泥などによって詰まった場合であっても、超音波処理汚泥を堰53Aよりも高い53Bより越流させ、他方の第2の処理槽52Bの流出口55より流出させることができるので、汚泥の連続処理を確実に行うことができるとともに、超音波処理槽50のオーバーフローを回避することができる。   Further, by making the height of the upper end surface of the weir 53A in one second processing tank 52A different from the upper end surface of the weir 53B in the other second processing tank 52B, only the weir 53A having a low height is obtained. Since the ultrasonic treatment sludge will overflow, the flow rate of the ultrasonic treatment sludge flowing over the weir 53A can be doubled, so that the solid content in the sludge adheres to the inner wall of the second treatment tank 52A. It is possible to prevent the cause of bad odor and the outflow 55 from being blocked. Even if the outlet 55 of the second treatment tank 52A is clogged with sludge for some reason, the ultrasonic treatment sludge is caused to overflow from 53B higher than the weir 53A, and the other second treatment tank 52B. Therefore, it is possible to reliably perform the sludge continuous treatment and to avoid the overflow of the ultrasonic treatment tank 50.

また、エアレーター70から気泡を第1の処理槽に送り込むことにより、曝気部の汚泥に上昇流を発生させることができ、仕切板72の下端と超音波処理槽50の底部との間の空間より、音場空間中の汚泥を引き込むことができ、音場空間中の汚泥に下降流を発生させることができ、第1の処理槽内を効率よく撹拌することができ、超音波による汚泥処理を効率よく行うことができる。また、超音波の音場空間と遮断された曝気部のみに気泡を供給し、音場空間の汚泥には溶存した状態で空気を供給することができるので、気泡の影響によって超音波の減衰を引き起こすことがなく、超音波によるキャビテーションの核となる溶存空気の濃度を維持することができるために、超音波によるキャビテーションを効率よく発生することができ、超音波により汚泥処理を効率よく行うことができる。   Further, by sending air bubbles from the aerator 70 to the first treatment tank, an upward flow can be generated in the sludge of the aeration section, and the space between the lower end of the partition plate 72 and the bottom of the ultrasonic treatment tank 50 can be generated. Thus, the sludge in the sound field space can be drawn in, the downflow can be generated in the sludge in the sound field space, the inside of the first treatment tank can be efficiently stirred, and the sludge treatment by ultrasonic waves Can be performed efficiently. In addition, bubbles can be supplied only to the ultrasonic field space and the isolated aeration unit, and air can be supplied to the sludge in the sound field space in a dissolved state. Because it can maintain the concentration of dissolved air that is the core of ultrasonic cavitation without causing it, cavitation by ultrasonic waves can be generated efficiently, and sludge treatment can be efficiently performed by ultrasonic waves. it can.

汚泥に超音波を照射することで、汚泥中の溶存気体がキャビテーションによって脱気され、処理槽内の汚泥が嫌気状態となり、嫌気性の泡沫が発生し、超音波処理槽内に蓄積して超音波の音場を乱すことにより、超音波による汚泥処理の効率が低下したり、超音波処理槽50の流出口55を嫌気性の泡沫が閉塞したり、悪臭を発生するなどの問題があった。特にMLSSが10,000mg/Lを超えるような高濃度の汚泥を処理する場合は、汚泥の流動性が悪いために上記のような問題が発生していた。特に、このような場合は本実施例のように、超音波処理槽50にエアレーター70から気泡を送り込んで曝気することが有効である。曝気は連続でも良いが、汚泥の性状に応じて、間欠的に曝気を行っても良い。   By irradiating the sludge with ultrasonic waves, the dissolved gas in the sludge is degassed by cavitation, the sludge in the treatment tank becomes anaerobic, anaerobic foam is generated, accumulated in the ultrasonic treatment tank, and super Disturbing the sound field of the sonic wave has caused problems such as a decrease in the efficiency of sludge treatment by ultrasonic waves, anaerobic foam blocking the outlet 55 of the ultrasonic treatment tank 50, and a bad odor. . In particular, when treating sludge with a high concentration such that MLSS exceeds 10,000 mg / L, the above-mentioned problems have occurred due to poor fluidity of the sludge. In particular, in such a case, it is effective to aerate by sending bubbles from the aerator 70 to the ultrasonic treatment tank 50 as in this embodiment. Aeration may be continuous, but aeration may be intermittently performed according to the properties of the sludge.

超音波処理槽50の上部には、蓋体60を設けている。この蓋体60は、第1の処理槽51と第2の処理槽52A、52Bとを覆うように設けられ、上部より配管Gによって消泡水が供給され、下部より消泡水を噴出するように構成されている。蓋体60には、複数の箱体61が形成され、これらの箱体61には複数の消泡水噴出孔62を、箱体61の下面だけでなく側壁にも多数設けている。   A lid 60 is provided on the upper part of the ultrasonic treatment tank 50. The lid body 60 is provided so as to cover the first treatment tank 51 and the second treatment tanks 52A and 52B, and the defoaming water is supplied from the upper part through the pipe G, and the defoaming water is ejected from the lower part. It is configured. The lid body 60 is formed with a plurality of box bodies 61, and the box bodies 61 are provided with a plurality of defoaming water ejection holes 62 on the side walls as well as the lower surface of the box body 61.

このように、複数の箱体61内に消泡水を導き、この箱体61内の消泡水を噴出させることで、超音波処理槽50の水面へ均一に散水することができ、第1の処理槽51の水面に発生した泡沫を消泡することができる。なお、消泡水を使用しない場合は、超音波処理槽50の外壁をモーターに取り付けたカムで振動させ、第1の処理槽の液面に波を起こし、第1の処理槽51の水面に発生した泡沫を堰53A、53Bより強制的に越流させてもよい。   Thus, defoaming water is guided into the plurality of boxes 61, and the defoaming water in the boxes 61 is ejected, so that water can be uniformly sprayed onto the water surface of the ultrasonic treatment tank 50. The foam generated on the water surface of the treatment tank 51 can be removed. In addition, when defoaming water is not used, the outer wall of the ultrasonic treatment tank 50 is vibrated by a cam attached to a motor, a wave is generated in the liquid surface of the first treatment tank, and the water surface of the first treatment tank 51 is The generated foam may be forced to overflow from the weirs 53A and 53B.

また、第1の処理槽51の水面に水平に移動できるゴム製の泡沫除去板を設け、間欠的にこの泡沫除去板を移動させることで、第1の処理槽51の水面に発生した泡沫を堰53A、53Bより強制的に越流させてもよい。   In addition, a foam foam removing plate that can move horizontally on the water surface of the first treatment tank 51 is provided, and bubbles generated on the water surface of the first treatment tank 51 are moved intermittently by moving the foam removal plate. It may be forced to overflow from the weirs 53A and 53B.

また、超音波処理槽50の側面にスリットを設け、このスリットから空気を第1の処理槽51の水面に向かって吹き出すことで、第1の処理槽51の水面に発生した泡沫を風圧によって堰53A、53Bより強制的に越流させてもよい。   Further, a slit is provided on the side surface of the ultrasonic treatment tank 50, and air is blown out from the slit toward the water surface of the first treatment tank 51, so that bubbles generated on the water surface of the first treatment tank 51 are dammed by wind pressure. It may be forced to overflow from 53A and 53B.

本発明による汚泥処理装置は、工場や、排水処理施設などから排出される様々な排液に対して適用することができる。   The sludge treatment apparatus according to the present invention can be applied to various effluents discharged from factories, wastewater treatment facilities, and the like.

本発明の一実施例による汚泥処理装置を示す構成図The block diagram which shows the sludge processing apparatus by one Example of this invention 本実施例による超音波処理槽を上面からみた概略図Schematic of the ultrasonic treatment tank according to the present embodiment as seen from above. 本実施例による超音波処理槽を正面からみた断面の概略図Schematic of the cross section seen from the front of the ultrasonic treatment tank according to the present embodiment 本実施例による超音波処理槽を側面からみた断面の概略図Schematic of a cross section of the ultrasonic treatment tank according to the present embodiment as seen from the side.

符号の説明Explanation of symbols

1 本体ケース
2 制御盤
3 漏水センサー
4 アジャスタ
5 本体ケース仕切板
14 超音波振動子
15 超音波発振器
20 高速旋回分離槽
30 低速旋回分離槽
31 胴部分
32 底部
33 流出口
34 導入口
35 バルブ
36 排出口
41 電動制御バルブ
42 流量計
43 三方弁
44 消泡水導入管
50 超音波処理槽
51 第1の処理槽
52A,52B 第2の処理槽
53A,53B 堰
54 流入口
55 流出口
56 ドレン口
57 バルブ
58 UV灯
60 蓋体
61 箱体
62 噴出孔
70 エアレーター
71 空気配管
72 仕切板
73 堰上端凸曲面
A,B,C,D,E,F,G,H 配管
DESCRIPTION OF SYMBOLS 1 Main body case 2 Control panel 3 Water leak sensor 4 Adjuster 5 Main body case partition plate 14 Ultrasonic vibrator 15 Ultrasonic oscillator 20 High-speed swirl separation tank 30 Low-speed swirl separation tank 31 Body part 32 Bottom 33 Outlet 34 Inlet 35 Valve 36 Exhaust Outlet 41 Electric control valve 42 Flow meter 43 Three-way valve 44 Defoaming water introduction pipe 50 Ultrasonic treatment tank 51 First treatment tank 52A, 52B Second treatment tank 53A, 53B weir 54 Inlet 55 Outlet 56 Drain port 57 Bulb 58 UV lamp 60 Lid 61 Box 62 Ejection hole 70 Aerator 71 Air piping 72 Partition plate 73 Weir upper end convex curved surface A, B, C, D, E, F, G, H piping

Claims (11)

超音波処理槽に超音波振動子を備えた汚泥処理装置において、前記超音波処理槽を、堰によって第1の処理槽と第2の処理槽に区分し、前記第1の処理槽に汚泥の流入口と前記超音波振動子を備え、前記第2の処理槽に超音波処理汚泥の流出口を備え、前記第2の処理槽を前記第1の処理槽の外部に設け、前記堰の上端面を水平に保持し、前記第1の処理槽に曝気手段を設けた汚泥処理装置。 In the sludge treatment apparatus provided with an ultrasonic vibrator in the ultrasonic treatment tank, the ultrasonic treatment tank is divided into a first treatment tank and a second treatment tank by a weir, and sludge is contained in the first treatment tank. An inlet and the ultrasonic vibrator, the second treatment tank is provided with an ultrasonic treatment sludge outlet, the second treatment tank is provided outside the first treatment tank, and the top of the weir A sludge treatment apparatus in which an end surface is held horizontally and an aeration means is provided in the first treatment tank. 前記第2の処理槽を前記第1の処理槽の両側部にそれぞれ設け、一方の前記第2の処理槽における前記堰の上端面と、他方の前記第2の処理槽における前記堰の上端面との高さを異ならせた請求項1記載の汚泥処理装置。 The second treatment tank is provided on both sides of the first treatment tank, the upper end surface of the weir in one of the second treatment tanks, and the upper end surface of the weir in the other second treatment tank. The sludge treatment apparatus according to claim 1, wherein the height of the sludge treatment apparatus is made different. 前記第1の処理槽における前記超音波振動子の超音波照射面と超音波反射面とからなる超音波の音場空間の外部に前記曝気手段を設けた請求項1または2に記載の汚泥処理装置。 3. The sludge treatment according to claim 1, wherein the aeration means is provided outside an ultrasonic sound field space composed of an ultrasonic irradiation surface and an ultrasonic reflection surface of the ultrasonic transducer in the first treatment tank. apparatus. 前記超音波の音場空間と前記曝気手段を設けた曝気部とを仕切板で区切り、前記仕切板の下端と前記第1の処理槽の底部との間に空間を設けた請求項1または2に記載の汚泥処理装置。 The ultrasonic field field and the aeration section provided with the aeration means are separated by a partition plate, and a space is provided between a lower end of the partition plate and a bottom portion of the first treatment tank. The sludge treatment apparatus described in 1. 前記堰の上端面を凸曲面で構成したことを特徴とする請求項1または2に記載の汚泥処理装置。 The sludge treatment apparatus according to claim 1 or 2, wherein an upper end surface of the weir is a convex curved surface. 前記第2の処理槽に前記堰の上端面と前記第2の処理槽の底面とを結ぶ汚泥案内板を設け、前記汚泥案内板と前記堰の角度が0度以上45度以下である請求項1または2に記載の汚泥処理。 The sludge guide plate connecting the upper end surface of the weir and the bottom surface of the second treatment tank is provided in the second treatment tank, and an angle between the sludge guide plate and the weir is 0 degree or more and 45 degrees or less. The sludge treatment according to 1 or 2. 前記第2の処理槽の内壁に疎水性の表面処理を施したことを特徴とする請求項1または2に記載の汚泥処理装置。 The sludge treatment apparatus according to claim 1 or 2, wherein a hydrophobic surface treatment is applied to an inner wall of the second treatment tank. 前記超音波処理槽の上部に蓋体を設け、前記蓋体下部より消泡水を噴出することを特徴とする請求項1または2に記載の汚泥処理装置。 The sludge treatment apparatus according to claim 1 or 2, wherein a lid is provided at an upper part of the ultrasonic treatment tank, and defoamed water is ejected from the lower part of the lid. 前記第1の処理槽内の液面を振動させる手段を有することを特徴とする請求項1または2に記載の汚泥処理装置。 The sludge treatment apparatus according to claim 1 or 2, further comprising means for vibrating the liquid level in the first treatment tank. 前記第1の処理槽内の液面の浮遊物を、前記第1の処理槽から前記第2の処理槽へ掃きだす手段を有することを特徴とする請求項1または2に記載の汚泥処理装置。 3. The sludge treatment apparatus according to claim 1, further comprising means for sweeping liquid surface floating matter in the first treatment tank from the first treatment tank to the second treatment tank. 4. . 前記第1の処理槽内の液面の浮遊物を、前記第1の処理槽から前記第2の処理槽へ風圧で押し流す送風手段を有することを特徴とする請求項1または2に記載の汚泥処理装置。 3. The sludge according to claim 1, further comprising a blowing unit that pushes the liquid surface suspended matter in the first treatment tank from the first treatment tank to the second treatment tank by wind pressure. 4. Processing equipment.
JP2005109671A 2005-04-06 2005-04-06 Sludge treatment equipment Expired - Fee Related JP4483664B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2005109671A JP4483664B2 (en) 2005-04-06 2005-04-06 Sludge treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2005109671A JP4483664B2 (en) 2005-04-06 2005-04-06 Sludge treatment equipment

Publications (2)

Publication Number Publication Date
JP2006289180A JP2006289180A (en) 2006-10-26
JP4483664B2 true JP4483664B2 (en) 2010-06-16

Family

ID=37410365

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2005109671A Expired - Fee Related JP4483664B2 (en) 2005-04-06 2005-04-06 Sludge treatment equipment

Country Status (1)

Country Link
JP (1) JP4483664B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4962225B2 (en) * 2007-08-31 2012-06-27 パナソニック株式会社 Continuous emulsification dispersion processing equipment
CN111186975A (en) * 2020-03-11 2020-05-22 金碳环境科技(天津)有限公司 Ultrasonic oil stain treatment process

Also Published As

Publication number Publication date
JP2006289180A (en) 2006-10-26

Similar Documents

Publication Publication Date Title
KR101281514B1 (en) A pressure float type polluted water treatment method using microbubble unit and slanted plate sturcture
CN209396964U (en) Ozone treatment device and water treatment system including the ozone treatment device
KR101964830B1 (en) Water treatment apparatus
JP3631999B2 (en) Fine bubble feeder
EP0829305A2 (en) Flotation type separator
JP2011072982A (en) Sewage treatment system and fine air bubble generator
JP4483664B2 (en) Sludge treatment equipment
KR100694191B1 (en) Water treatment
KR101270236B1 (en) Apparatus for separating waste oil using bubble
JP7423414B2 (en) Carrier separation device, operating method of carrier separation device, multistage carrier separation device, and anaerobic treatment device
KR101774488B1 (en) Settling and floating sludge removal equipment and operating method of the same
JPH1071388A (en) Dleaerator
JP4625291B2 (en) Sludge treatment equipment
JPS6054120B2 (en) water treatment equipment
JP2002263696A (en) Washing apparatus
KR101989833B1 (en) Apparatus for treating drain water of land aquatic plant
EP1218295A1 (en) A process and a plant for purifying of a liquid
JP2021010876A (en) Automatic cleaning device, biofiltration treatment apparatus, and automatic cleaning method of biofiltration treatment apparatus
KR102278779B1 (en) Half-pipe skimmer and water treatment device having the same
KR101219864B1 (en) Water purification system using airfloatation in the river
JP2007330894A (en) Activated sludge treatment equipment
JP4013123B2 (en) Operating method of aerobic treatment tank, aerobic treatment tank and sewage septic tank
KR101070847B1 (en) Water treatment equipment
JP4543874B2 (en) Sludge treatment equipment
JP3561212B2 (en) Freshwater organism breeding water purification method and freshwater organism breeding water purification device

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20071205

RD01 Notification of change of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7421

Effective date: 20080115

RD01 Notification of change of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7421

Effective date: 20091126

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20100225

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20100302

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20100315

R151 Written notification of patent or utility model registration

Ref document number: 4483664

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R151

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130402

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130402

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140402

Year of fee payment: 4

LAPS Cancellation because of no payment of annual fees