JPH05337490A - Device for separating fine solid floating in liquid medium with gas stuck to it - Google Patents

Device for separating fine solid floating in liquid medium with gas stuck to it

Info

Publication number
JPH05337490A
JPH05337490A JP14279292A JP14279292A JPH05337490A JP H05337490 A JPH05337490 A JP H05337490A JP 14279292 A JP14279292 A JP 14279292A JP 14279292 A JP14279292 A JP 14279292A JP H05337490 A JPH05337490 A JP H05337490A
Authority
JP
Japan
Prior art keywords
gas
solid
liquid medium
liquid separation
treated water
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.)
Granted
Application number
JP14279292A
Other languages
Japanese (ja)
Other versions
JP3382636B2 (en
Inventor
Hiroyasu Kanesashi
博康 金刺
Koji Shiraishi
皓二 白石
Toshihiro Yamauchi
敏弘 山内
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.)
Fuji Kasei Kogyo Co Ltd
Original Assignee
Fuji Kasei Kogyo 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 Fuji Kasei Kogyo Co Ltd filed Critical Fuji Kasei Kogyo Co Ltd
Priority to JP14279292A priority Critical patent/JP3382636B2/en
Publication of JPH05337490A publication Critical patent/JPH05337490A/en
Application granted granted Critical
Publication of JP3382636B2 publication Critical patent/JP3382636B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/28Anaerobic digestion processes
    • C02F3/2846Anaerobic digestion processes using upflow anaerobic sludge blanket [UASB] reactors

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Microbiology (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Treatment Of Liquids With Adsorbents In General (AREA)
  • Treatment Of Water By Ion Exchange (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

PURPOSE:To provide sufficient ability to perform solid-gas-liquid separation and to sharply decrease initial cost and running cost by generating turbulence in a liquid medium by flotation force of gas and installing a solid-gas-liquid separation mechanism for separating and recovering fine solid, liquid medium and gas. CONSTITUTION:In a solid-gas-liquid separation device for separating and removing fine solid having higher density than that of a liquid medium and floating or rising in the liquid medium with gas stuck to it from gas, waste water introduced by a pump 15, etc., from the lower part of the device effectively comes into contact with an anaerobic microorganism in the device and at the same time the biomass of the microorganism rises together with treated water and gas by the gas generated by the biodegradation of organic substances. And the biomass, treated water and gas are separated by an upper solid-gas-liquid separation plates 1, 3 and only the treated water is discharged outside the system and the gas is recovered by a gas holder 10 in the upper part and the biomass is circulated through the lower part of the device by the turbulence flowing downward in the device, permitting the anaerobic treatment of the desired waste to be effectively performed.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は液媒体中でガスを付着し
て浮遊する微細な固体を分離する装置に係り、更に詳し
くは、例えば廃水処理リアクターにおいて、廃水をイオ
ン交換樹脂、活性炭、その他の担体又は微生物のフロッ
クと接触させることによって廃水中の不純物や有害物な
どを吸着、分解させる場合に、これらが反応等により発
生するガスに吸着又は付着されて浮遊、浮上して、リア
クターから流出してしまうのを防ぐために用いる液媒体
中でガスを付着して浮遊する微細な固体の分離装置に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for separating fine floating solids by adhering gas in a liquid medium. More specifically, for example, in a wastewater treatment reactor, wastewater is treated with ion exchange resin, activated carbon, etc. When adsorbing or decomposing impurities or harmful substances in wastewater by contacting with the carrier or the flocs of microorganisms, these are adsorbed or attached to the gas generated by the reaction etc. and float, float, and flow out from the reactor. The present invention relates to a device for separating fine solids from which a gas adheres and floats in a liquid medium used to prevent the occurrence of the above.

【0002】[0002]

【従来の技術】例えば、有機性廃水の処理法として、粒
状に自己造粒化された嫌気性微生物を用いた、上向流嫌
気性スラッジブランケット法があり、この方法によれ
ば、有機物と造粒された嫌気性微生物群とを接触させて
廃水を生分解し、その際発生したガスが造粒された嫌気
性微生物に付着してそれらが浮上し、その過程で廃水中
の有機物を更に分解し、廃水を浄化する連続処理方式の
固気液分離装置が知られている。
2. Description of the Related Art For example, as a method for treating organic wastewater, there is an upflow anaerobic sludge blanket method using anaerobic microorganisms that are self-granulated into particles. The wastewater is biodegraded by contact with the granulated anaerobic microorganisms, and the gas generated at that time adheres to the granulated anaerobic microorganisms and floats on them, further decomposing the organic matter in the wastewater in the process. However, a continuous gas-liquid separator for purifying wastewater is known.

【0003】従来、この種の固気液分離装置には、高価
なフィルター等による固体の強制分離が用いられてき
た。その中で、廃水の嫌気性微生物処理装置の固気液分
離機構としては、図1〜図4に見られるように、比較的
簡単な分離構造のものから複雑なものまで様々な形状を
呈している。これらは、矢部で示したように、何れも廃
水の流れは上向流により、装置内部の嫌気性微生物と廃
水が接触して、有機物の分解を施すとともに発生するガ
スにより菌体が浮上し、装置上部の固気液分離機構によ
り菌体、処理水及びガスをそれぞれ分離、回収しようと
するものである。
Conventionally, forcible separation of solids by means of expensive filters has been used in this type of solid-gas separation apparatus. Among them, as a solid-gas liquid separation mechanism of an anaerobic microbial treatment apparatus for wastewater, as shown in FIGS. 1 to 4, various shapes such as a relatively simple separation structure to a complicated structure are exhibited. There is. As shown by the arrow part, these are the flows of the wastewater by the upward flow, the anaerobic microorganisms inside the device and the wastewater come into contact with each other, and the bacteria are levitated by the gas generated together with the decomposition of the organic matter. The solid-gas separation mechanism in the upper part of the device intends to separate and collect the bacterial cells, the treated water and the gas, respectively.

【0004】即ち、図1の例では、下部より流入した廃
水は、装置下部の嫌気性微生物群と接触して、有機物を
分解し、その過程で発生したガスにより、菌体とガスは
浮上するが、上部の固気液分離機構によりガスは装置の
中央部Aに集まり、Bにより回収され、一方菌体は下降
する。また、処理水はC部で上澄み水となって外周囲D
より系外に流出される。図2の例では、下部より流入し
た廃水は、装置下部の嫌気性微生物群と接触して、有機
物を分解し、その過程で発生したガスにより、菌体とガ
スは浮上するが、上部の固気液分離機構によりガスは装
置の周囲Eに集まり、Fにより回収され、一方菌体は下
降する。また、処理水はG部で上澄み水となって外周囲
Hより系外に流出される。図3の例は、図1の例の規模
が大きくなったものである。即ち、図1と同様の処理を
施し、浮上した菌体とガスは上部の固気液分離機構によ
りガスは装置のI部に集まり、Jにより回収され、一方
菌体は下降する。また、処理水はK部で上澄み水となっ
て外周囲Lより系外に流出される。図4の例は、図2の
例の規模が大きくなったものである。即ち、図2と同様
の処理を施し、浮上した菌体とガスは上部の固気液分離
機構によりガスは装置のM部に集まり、Nにより回収さ
れ、一方菌体は下降する。また、処理水はO部で上澄み
水となって外周囲Pより系外に流出される。
That is, in the example of FIG. 1, the wastewater flowing in from the lower part comes into contact with the anaerobic microorganism group at the lower part of the apparatus to decompose organic matter, and the gas generated in the process causes the bacterial cells and gas to float. However, the gas is collected in the central part A of the device by the solid-gas liquid separation mechanism in the upper part and collected by B, while the bacterial cells descend. In addition, the treated water becomes clear water at the C part, and the outer circumference D
More out of the system. In the example of FIG. 2, the wastewater flowing from the lower part comes into contact with the anaerobic microorganisms group at the lower part of the device to decompose organic matter, and the gas generated in the process causes the bacterial cells and gas to float, but The gas is collected by the gas-liquid separation mechanism around the device E and collected by F, while the bacterial cells descend. In addition, the treated water becomes clear water in the G portion and is discharged from the system from the outer circumference H. The example of FIG. 3 is an enlarged version of the example of FIG. That is, the same treatment as in FIG. 1 was performed, and the floating bacterial cells and gas were collected by the solid-liquid separation mechanism in the upper part of the apparatus, and the gas was collected by J, while the bacterial cells descended. Further, the treated water becomes clear water at the K portion and is discharged from the system from the outer periphery L. The example of FIG. 4 is an enlarged version of the example of FIG. That is, the same treatment as in FIG. 2 is performed, and the floating bacterial cells and gas are collected in the M portion of the apparatus by the solid-liquid separation mechanism in the upper part and recovered by N, while the bacterial cells descend. In addition, the treated water becomes clear water in the O portion and flows out of the system from the outer periphery P.

【0005】[0005]

【発明が解決しようとする課題】しかし、従来の固気液
分離機構を有した固体分離装置には、比較的簡単な分離
構造のものでは、菌体、処理水及びガスの十分な分離が
行えず、しばしば処理水に混じって菌体が流出するた
め、ある一定の廃水通水量に限られ、従って処理量に限
界があったり、装置容量が大きくなってしまったりする
という問題があった。また、複雑な分離構造のもので
は、製作に手間がかかり、またイニシャルコストが高い
という問題があった。
However, in the conventional solid separation apparatus having a solid-gas / liquid separation mechanism, a relatively simple separation structure can sufficiently separate cells, treated water and gas. However, since the bacterial cells often mix with the treated water and flow out, there is a problem that the amount of waste water is limited to a certain amount, so that the treated amount is limited or the device capacity is increased. Further, in the case of a complicated separation structure, there are problems that it takes time to manufacture and the initial cost is high.

【0006】従って、本発明の目的は、前述の従来技術
の問題点を解消し、十分な固気液分離能力を有し、且
つ、構造が簡単でイニシャルコストを低く抑えることの
できる装置を提供することにある。
Therefore, an object of the present invention is to provide a device which solves the above-mentioned problems of the prior art, has a sufficient solid-gas / liquid separation ability, and has a simple structure and can keep the initial cost low. To do.

【0007】[0007]

【課題を解決するための手段】本発明に従えば、液媒体
中において、液媒体の比重より高い比重を有し、かつガ
スを付着しながら液媒体中を浮遊、浮上する微細な固体
をガスより分離除去する分離装置において、そのガスの
浮上する力を利用して装置内の液媒体中に乱流を起こさ
せ、微細な固体、液媒体及びガスをそれぞれ分離回収す
る、内部に固気液分離機構を有する、液媒体中の微細な
固体の分離装置が提供される。
According to the present invention, in a liquid medium, a fine solid having a specific gravity higher than that of the liquid medium and floating or floating in the liquid medium while adhering gas is gas. In a separation device that separates and removes more, a turbulent flow is generated in the liquid medium inside the device by utilizing the floating force of the gas, and fine solids, liquid medium, and gas are separated and recovered, respectively. An apparatus for separating fine solids in a liquid medium having a separation mechanism is provided.

【0008】本発明による固気液分離装置を特徴付ける
構成は固気液分離板1の取付角度及びその位置、さらに
固気液分離板1の取付下側の乱流補助突起部2、他の固
気液分離板3、三角形状のガス捕集補助板4、さらにガ
ス量が少なく乱流を起こしにくい場合に用いられるガス
循環配管5である。
The structure which characterizes the solid-gas liquid separation device according to the present invention is such that the mounting angle and position of the solid-liquid separation plate 1, the turbulent flow assisting projection 2 on the lower side of the mounting of the solid-gas liquid separation plate 1, and other solids. A gas-liquid separation plate 3, a triangular gas collection auxiliary plate 4, and a gas circulation pipe 5 used when the amount of gas is small and turbulence is unlikely to occur.

【0009】ここで、固気液分離板1(例えば材質ステ
ンレス鋼の板状体)は固液分離装置内の液媒体中の中央
部より上方に傾斜(好ましくは角度:45〜55°)させて
適宜固定し、装置の高さ方向中間部近傍の壁面に設けた
ガス捕集補助板4及び液媒体自由表面との間にそれぞれ
に適当な間隙を介して設置される。また固気液分離板1
の下側面には複数個の乱流補助突起部2(例えば長さ50
〜 150mmの突起) を設け、下方から上昇するガスを付着
した固体がこれに衝突して図5の矢部方向のような下降
流を生ぜしめて、固体を下方へ回収するようにする。第
二の固気液分離板3は例えばガスホルダー10の一部を液
媒体中に延長して第一の固気液分離板3の上部間隙6よ
り十分深い深さまで延ばし、間隙6より流出してきた固
体をここで衝突させて気体と分離させ、固体は間隙7か
ら下方へ戻されるようにする。
Here, the solid-gas separation plate 1 (for example, a plate made of stainless steel) is inclined (preferably at an angle of 45 to 55 °) above the central portion of the liquid medium in the solid-liquid separation device. Are appropriately fixed and installed with appropriate gaps between the gas collection auxiliary plate 4 and the liquid medium free surface provided on the wall surface near the middle portion in the height direction. In addition, solid-liquid separation plate 1
A plurality of turbulent flow assisting projections 2 (for example, a length of 50
(-150 mm protrusion) is provided, and solids attached with gas rising from below collide with this to generate a downward flow as shown by the arrow in FIG. 5 so that solids are collected downward. The second solid-gas liquid separation plate 3 extends, for example, part of the gas holder 10 into the liquid medium to a depth sufficiently deeper than the upper gap 6 of the first solid-gas liquid separation plate 3 and flows out from the gap 6. The solids are then collided and separated from the gas so that the solids are returned downwards through the gap 7.

【0010】[0010]

【作用】本発明に従った固気液分離装置は装置下部より
ポンプ等で導入された廃水が装置内で嫌気性微生物と効
率良く接触され、同時に有機物の生分解により発生する
ガスで微生物菌体が処理水及びガスと共に上昇し、上部
固気液分離板1及び3で菌体、処理水及びガスが分離さ
れ、処理水のみ系外に流出し、ガスは上部のガスホルダ
ー10に回収され、菌体は装置内を下降する乱流にのって
装置下部へ循環されるので、所望の廃水の嫌気性処理を
効率よく行うことができる。
In the solid-gas separation apparatus according to the present invention, waste water introduced by a pump or the like from the lower part of the apparatus is efficiently contacted with anaerobic microorganisms in the apparatus, and at the same time, microbial cells are generated by gas generated by biodegradation of organic matter. Rises along with the treated water and gas, the cells, treated water and gas are separated by the upper solid-gas liquid separation plates 1 and 3, only the treated water flows out of the system, and the gas is recovered in the upper gas holder 10. Since the microbial cells are circulated to the lower part of the device in a turbulent flow that descends inside the device, the desired anaerobic treatment of wastewater can be efficiently performed.

【0011】[0011]

【実施例】図2は本発明による内部に固気液分離機構を
有する、液媒体中でガスを付着して浮遊する微細な固体
の分離装置の一例を示す図面である。図2の装置を用い
て本発明の好ましい態様について以下に説明するが、本
発明の範囲をこの実施例に限定するものでないことはい
うまでもない。
FIG. 2 is a view showing an example of an apparatus for separating fine solids having a gas-liquid separation mechanism according to the present invention, in which a gas adheres and floats in a liquid medium. A preferred embodiment of the present invention will be described below using the apparatus shown in FIG. 2, but it goes without saying that the scope of the present invention is not limited to this embodiment.

【0012】即ち、固気液分離板1は、設置角度を水平
面に対し50°(通常45〜55°)とし、その上部が水面下
約100mm (通常50〜150 mm)として液の移動間隙6を設
け、一方下部は三角形状のガス捕集補助板4との間隔7
を約 200mmとし(通常 150〜250 mm)、さらに固気液分
離板1の下側に乱流補助突起部2を数箇所設けることに
より、図の実線矢印方向への水の流れを作りながら乱流
を起こし、極めて効率の良い固気液分離を行うことがで
きる。また、間隙6から一部水の流れを作ることによ
り、間隙7から菌体、処理水及びガスが破線矢印方向を
通って直接系外に流出するのを防ぐ働きをする。一部間
隙6から流れた菌体と処理水は別の固気液分離板3に当
たり、菌体のみ間隙7を通って再び装置の下部に沈降す
る。この分離板3は間隙6より下側まで液中に突出して
いることが必要である。このようにして処理水は図の右
側上部の上澄み部8で固液分離が完全に行われ、処理水
は樋9を経て系外に流出される。一方、菌体は槽内を実
線矢印のように下降して円滑に槽内を循環し、廃水流入
ポンプ15によって廃水流入管14より導入される廃水との
効率良い接触が常に保たれる。
That is, the solid-gas separation plate 1 has an installation angle of 50 ° (usually 45 to 55 °) with respect to the horizontal plane, and its upper portion is approximately 100 mm below the water surface (usually 50 to 150 mm), and the liquid movement gap 6 On the other hand, the lower part has a space 7 with the triangular gas collecting auxiliary plate 4.
Is set to about 200 mm (usually 150 to 250 mm), and several turbulent flow auxiliary projections 2 are provided below the solid-gas liquid separation plate 1 to create turbulence while creating a water flow in the direction of the solid line arrow in the figure. A flow can be generated, and solid-liquid separation can be performed very efficiently. Further, by making a part of the flow of water from the gap 6, it functions to prevent the bacterial cells, the treated water and the gas from flowing out of the system directly through the gap 7 through the direction of the broken line arrow. The bacterial cells and the treated water that have flowed from a part of the gap 6 hit another solid-gas / liquid separation plate 3, and only the bacterial cells pass through the gap 7 and settle again in the lower part of the apparatus. It is necessary that the separating plate 3 projects into the liquid below the gap 6. In this way, the treated water is completely subjected to solid-liquid separation in the supernatant 8 on the upper right side of the figure, and the treated water flows out of the system through the gutter 9. On the other hand, the fungus body descends in the tank as shown by a solid arrow and smoothly circulates in the tank, and the wastewater inflow pump 15 always maintains efficient contact with the wastewater introduced from the wastewater inflow pipe 14.

【0013】尚、初期段階ではガスの発生量が少なく、
上昇乱流が起こりにくく、菌体が流出してしまう場合
は、ガスホルダー10で捕集した発生ガス又は、系外より
導入した酸素を含まないガス(窒素等)11をポンプ12を
用いて配管5を通して装置の下部より通気することによ
って流れを作り出すことができる。また、ガスを循環さ
せないで運転する場合は、発生したガスを13より系外へ
放散するか、あるいは後処理部へ導く。
In the initial stage, the amount of gas generated is small,
If rising turbulence is unlikely to occur and bacterial cells flow out, the generated gas collected by the gas holder 10 or the oxygen-free gas (nitrogen, etc.) 11 introduced from outside the system is piped using the pump 12. A flow can be created by venting through the bottom of the device through 5. When operating without circulating the gas, the generated gas is diffused from the system 13 to the outside of the system or is led to the post-treatment section.

【0014】[0014]

【発明の効果】以上説明した通り、本発明によれば、極
めて簡易な構造の固気液分離機構により、固気液分離に
おいて十分な能力を持ち、且つ、イニシャルコストを大
幅に軽減することができる。また、本機構16は、例えば
図5、6及び7に示した斜線部のように、廃水処理リア
クターの一部分に設置使用できるために、ランニングコ
ストを大幅に軽減することができる。
As described above, according to the present invention, the solid-gas separation mechanism having an extremely simple structure has sufficient ability in solid-liquid separation, and can significantly reduce the initial cost. it can. Further, since the present mechanism 16 can be installed and used in a part of the wastewater treatment reactor, for example, as shown by the hatched portions in FIGS. 5, 6 and 7, the running cost can be greatly reduced.

【図面の簡単な説明】[Brief description of drawings]

【図1】従来の廃水の嫌気性微生物処理装置の固気液分
離機構の一例を示す図面である。
FIG. 1 is a view showing an example of a solid-liquid separation mechanism of a conventional wastewater anaerobic microbial treatment apparatus.

【図2】従来の廃水の嫌気性微生物処理装置の固気液分
離機構の他の例を示す図面である。
FIG. 2 is a diagram showing another example of a solid-liquid separation mechanism of a conventional wastewater anaerobic microbial treatment apparatus.

【図3】従来の廃水の嫌気性微生物処理装置の固気液分
離機構の更に他の例を示す図面である。
FIG. 3 is a view showing still another example of the solid-gas liquid separation mechanism of the conventional wastewater anaerobic microbial treatment apparatus.

【図4】従来の廃水の嫌気性微生物処理装置の固気液分
離機構の更に他の例を示す図面である。
FIG. 4 is a view showing still another example of a solid-liquid separation mechanism of a conventional wastewater anaerobic microbial treatment apparatus.

【図5】本発明による固気液分離機構を備えた液媒体中
でガスを付着して浮遊する微細な固体の分離装置の一例
を示す概略図である。
FIG. 5 is a schematic view showing an example of an apparatus for separating fine solids to which gas is attached and suspended in a liquid medium provided with a solid-liquid separation mechanism according to the present invention.

【図6】本発明の固気液分離機構の廃水処理リアクター
への配置の一例を示す平面図である。
FIG. 6 is a plan view showing an example of the arrangement of the solid-gas separation mechanism of the present invention in a wastewater treatment reactor.

【図7】本発明の固気液分離機構の廃水処理リアクター
への配置の他の例を示す平面図である。
FIG. 7 is a plan view showing another example of arrangement of the solid-gas liquid separation mechanism of the present invention in a wastewater treatment reactor.

【図8】本発明の固気液分離機構の廃水処理リアクター
への配置の更に他の例を示す平面図である。
FIG. 8 is a plan view showing still another example of arrangement of the solid-gas separation mechanism of the present invention in a wastewater treatment reactor.

【符号の説明】[Explanation of symbols]

1…固気液分離板 2…乱流補助突起板 3…固気液分離板 4…ガス捕集補助板 5…ガス循環配管 6…液移動間隙 7…固気液分離板とガス捕集補助板との間隙 8…上澄み部 9…処理水流出樋 10…ガスホルダー 11…導入ガス 12…ポンプ 13…排出ガス 14…廃水流入管 15…廃水流入ポンプ 16…本発明の固気液分離機構 1 ... Solid-gas separation plate 2 ... Turbulence assisting projection plate 3 ... Solid-gas separation plate 4 ... Gas collection auxiliary plate 5 ... Gas circulation pipe 6 ... Liquid moving gap 7 ... Solid-gas separation plate and gas collection auxiliary Gap between the plates 8 ... Supernatant 9 ... Treated water outflow gutter 10 ... Gas holder 11 ... Introduced gas 12 ... Pump 13 ... Exhaust gas 14 ... Wastewater inflow pipe 15 ... Wastewater inflow pump 16 ... Solid-liquid separation mechanism of the present invention

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 B01D 21/24 A ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Office reference number FI technical display location B01D 21/24 A

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 液媒体中において、液媒体の比重より高
い比重を有し、かつガスを付着しながら液媒体中を浮
遊、浮上する微細な固体をガスより分離除去する分離装
置において、そのガスの浮上する力を利用して装置内の
液媒体中に乱流を起こさせ、微細な固体、液媒体及びガ
スをそれぞれ分離回収する、内部に固気液分離機構を有
する、液媒体中の微細な固体の分離装置。
1. A separation device for separating and removing from a gas a fine solid having a specific gravity higher than that of the liquid medium and floating and floating in the liquid medium while adhering the gas. A turbulent flow is generated in the liquid medium in the device by utilizing the floating force of the liquid to separate and collect fine solids, liquid medium and gas, respectively. Solid separation device.
JP14279292A 1992-06-03 1992-06-03 Separation device for fine solids that adhere and float in a liquid medium Expired - Fee Related JP3382636B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14279292A JP3382636B2 (en) 1992-06-03 1992-06-03 Separation device for fine solids that adhere and float in a liquid medium

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14279292A JP3382636B2 (en) 1992-06-03 1992-06-03 Separation device for fine solids that adhere and float in a liquid medium

Publications (2)

Publication Number Publication Date
JPH05337490A true JPH05337490A (en) 1993-12-21
JP3382636B2 JP3382636B2 (en) 2003-03-04

Family

ID=15323722

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14279292A Expired - Fee Related JP3382636B2 (en) 1992-06-03 1992-06-03 Separation device for fine solids that adhere and float in a liquid medium

Country Status (1)

Country Link
JP (1) JP3382636B2 (en)

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JP2002079291A (en) * 2000-09-08 2002-03-19 Ebara Corp Anaerobic treatment method and apparatus
JP2007190461A (en) * 2006-01-17 2007-08-02 Sumitomo Heavy Ind Ltd Anaerobic treatment apparatus
JP2009522095A (en) * 2006-01-05 2009-06-11 バイオタン システムズ インターナショナル ビー.ブイ. Method and reactor for anaerobic wastewater purification
US20110168021A1 (en) * 2008-09-23 2011-07-14 Paques I.P. B.V. Settling device, purifier comprising a settling device and methods for anaerobic or aerobic purification of waste water
CN102745805A (en) * 2012-07-26 2012-10-24 常州大学 Air flotation oil separation sand setting device and sewage treatment method
JP6048557B1 (en) * 2015-09-25 2016-12-21 栗田工業株式会社 Anaerobic treatment apparatus and anaerobic treatment method
CN109967001A (en) * 2019-04-26 2019-07-05 河南百优福生物能源有限公司 A kind of three phase separator of biomass pyrolysis liquid fluidized bed reactor and its application

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002079291A (en) * 2000-09-08 2002-03-19 Ebara Corp Anaerobic treatment method and apparatus
JP2009522095A (en) * 2006-01-05 2009-06-11 バイオタン システムズ インターナショナル ビー.ブイ. Method and reactor for anaerobic wastewater purification
JP2007190461A (en) * 2006-01-17 2007-08-02 Sumitomo Heavy Ind Ltd Anaerobic treatment apparatus
US20110168021A1 (en) * 2008-09-23 2011-07-14 Paques I.P. B.V. Settling device, purifier comprising a settling device and methods for anaerobic or aerobic purification of waste water
US8728318B2 (en) * 2008-09-23 2014-05-20 Paques I.P.B.V. Settling device, purifier comprising a settling device and methods for anaerobic or aerobic purification of waste water
CN102745805A (en) * 2012-07-26 2012-10-24 常州大学 Air flotation oil separation sand setting device and sewage treatment method
JP6048557B1 (en) * 2015-09-25 2016-12-21 栗田工業株式会社 Anaerobic treatment apparatus and anaerobic treatment method
WO2017051560A1 (en) * 2015-09-25 2017-03-30 栗田工業株式会社 Anaerobic treatment device and anaerobic treatment method
CN109967001A (en) * 2019-04-26 2019-07-05 河南百优福生物能源有限公司 A kind of three phase separator of biomass pyrolysis liquid fluidized bed reactor and its application

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