JPH07275885A - Granule recovery apparatus - Google Patents

Granule recovery apparatus

Info

Publication number
JPH07275885A
JPH07275885A JP6599494A JP6599494A JPH07275885A JP H07275885 A JPH07275885 A JP H07275885A JP 6599494 A JP6599494 A JP 6599494A JP 6599494 A JP6599494 A JP 6599494A JP H07275885 A JPH07275885 A JP H07275885A
Authority
JP
Japan
Prior art keywords
granules
granule
treated water
reactor
returning
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
JP6599494A
Other languages
Japanese (ja)
Other versions
JP3451709B2 (en
Inventor
Sakae Fukunaga
栄 福永
Toru Matsumoto
徹 松本
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.)
IHI Corp
Original Assignee
IHI Corp
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 IHI Corp filed Critical IHI Corp
Priority to JP06599494A priority Critical patent/JP3451709B2/en
Publication of JPH07275885A publication Critical patent/JPH07275885A/en
Application granted granted Critical
Publication of JP3451709B2 publication Critical patent/JP3451709B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

PURPOSE:To prevent the lowering of the concn. of granules in a reactor and to keep the original treatment capacity of the reactor, in performing the decomposition treatment of org. industrial waste water by anaerobic bacteria, by separating and regenerating granules flowing out along with treated water to again return the same to the reactor. CONSTITUTION:The treated water containing granules overflowing from an ascending flow type anaerobic treatment reactor A passes through the screen 5 of a granule separation means 2 to be stored in the bottom part of a box body 4 and subsequently drained from a drain pipe 7. The granules caught by the screen 5 pass through the opening part 8a of a base stand 8 to be recovered in the granule recovery tank 9 of a granule return means 3. The granules are subjected to stirring treatment along with a part of the treated water introduced from a treated water introducing line 12 and the fine pulverization of granules or the removal of the gas or oil component bonded to the granules is performed and, thereafter, the granules are returned to the reactor A by a return pump 11.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は有機性産業廃水を嫌気性
微生物で分解処理するためのUASBリアクタ(上昇流
式嫌気性処理リアクタ)に用いられるグラニュールの回
収装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for recovering granules used in a UASB reactor (upflow anaerobic treatment reactor) for decomposing organic industrial wastewater with anaerobic microorganisms.

【0002】[0002]

【従来の技術】従来、高濃度の有機物を含んだ有機性産
業廃水(原水)を生物学的に処理する装置としてはUA
SB法(上昇流式嫌気性汚泥床法)を用いた上昇流式嫌
気性処理リアクタ(UASBリアクタ)がある。この上
昇流式嫌気性処理リアクタは図3に示すように、下部に
原水を導入する流入配管bが接続された矩体状の処理容
器aの内部に気固液分離手段cが設けられ、さらに、そ
の上部に処理水流出部dと排気管eが設けられた構成を
しており、流入配管bから導入された原水を上昇流で通
過させる際に、原水中に含まれている有機物をメタン生
成細菌等の嫌気性微生物でメタン醗酵して分解処理する
と共に、分解された処理水とバイオガスを気固液分離手
段cによってさらに処理水とバイオガスと嫌気性微生物
に分離した後、処理水は処理容器aの上端部よりオーバ
ーフローして流出し、バイオガスは排気管eから抜き出
して燃料等として用いられるようになっている。
2. Description of the Related Art Conventionally, UA has been used as an apparatus for biologically treating organic industrial wastewater (raw water) containing a high concentration of organic substances.
There is an upflow anaerobic treatment reactor (UASB reactor) using the SB method (upflow anaerobic sludge bed method). As shown in FIG. 3, this upflow type anaerobic treatment reactor is provided with a gas-solid separation means c inside a rectangular treatment container a to which an inflow pipe b for introducing raw water is connected. In addition, a treated water outflow portion d and an exhaust pipe e are provided on the upper portion thereof, and when the raw water introduced from the inflow pipe b is passed in an upward flow, the organic matter contained in the raw water is converted into methane. The methane is fermented and decomposed by anaerobic microorganisms such as producing bacteria, and the decomposed treated water and biogas are further separated into treated water, biogas and anaerobic microorganisms by the gas-solid separation means c, and then treated water. Is overflowed from the upper end of the processing container a and flows out, and the biogas is extracted from the exhaust pipe e and used as fuel or the like.

【0003】[0003]

【発明が解決しようとする課題】ところで、この嫌気性
微生物はグラニュールと呼ばれる直径が1〜3mm程度
の粒子の内外に繁殖して処理容器a内に収容されてお
り、このグラニュールは、有機物を分解した後は気固液
分離手段cによって分離されて流出が防止されるように
なっている。しかしながら、図2に示すように原水の種
類によっては、このグラニュールに油分やガスが強固に
付着したり、グラニュール自体が肥大化して内部にガス
を取り込む等の理由により、このグラニュールが気固液
分離手段cを通過して浮上して処理水と共にリアクター
外へ流出してしまい、リアクター内のグラニュール量が
減少して処理能力が低下してしまうことがあった。
By the way, the anaerobic microorganisms are propagated in and out of particles called granules having a diameter of about 1 to 3 mm and are housed in the processing container a. After being decomposed, it is separated by gas-solid separation means c to prevent outflow. However, as shown in Fig. 2, depending on the type of raw water, oil or gas may adhere strongly to the granules, or the granules themselves may become enlarged and take gas into the inside, so that the granules may become volatile. In some cases, the liquid passed through the solid-liquid separation means c, floated up, and flowed out of the reactor together with the treated water, so that the amount of granules in the reactor decreased and the treatment capacity deteriorated.

【0004】そこで、本発明は上記の問題点を有効に解
決するために案出されたものであり、その目的は処理水
と共に流出したグラニュールを効果的に回収し、再利用
することで上昇流式嫌気性処理リアクタの処理能力の低
下を未然に防止できる新規なグラニュール回収装置を提
供するものである。
Therefore, the present invention has been devised in order to effectively solve the above problems, and its purpose is to effectively recover and recycle the granules that have flowed out together with the treated water. It is intended to provide a novel granule recovery device capable of preventing a reduction in the processing capacity of a flow type anaerobic treatment reactor.

【0005】[0005]

【課題を解決するための手段】上記目的を達成するため
に本発明は有機性産業廃水を、メタン生成細菌等の嫌気
性微生物を含んだ粒状のグラニュールを収容した上昇流
式嫌気性処理リアクタに供給してバイオガスと処理水に
分解処理し、その処理水と共に流出する上記グラニュー
ルを処理水から分離して再度上記上昇流式嫌気性処理リ
アクタ内に戻すためのグラニュール回収装置において、
上記処理水中のグラニュールを分離するグラニュール分
離手段と、このグラニュール分離手段で分離されたグラ
ニュールを再生して上記上昇流式嫌気性処理リアクタ内
に返送するグラニュール返送手段とからなるものであ
り、また、この返送手段は上記グラニュール分離手段で
分離されたグラニュールを攪拌する攪拌機と、この攪拌
機で攪拌されたグラニュールを上記上昇流式嫌気性処理
リアクタ内に戻すための圧送ポンプとからなるものであ
る。
In order to achieve the above object, the present invention provides an upflow anaerobic treatment reactor containing organic industrial wastewater containing granular granules containing anaerobic microorganisms such as methanogenic bacteria. In the granule recovery apparatus for decomposing into biogas and treated water by supplying to, and separating the granules flowing out together with the treated water from the treated water into the upflow anaerobic treatment reactor again.
It comprises a granule separating means for separating granules in the treated water, and a granule returning means for regenerating the granules separated by the granule separating means and returning the granules into the upflow anaerobic treatment reactor. The returning means is a stirrer for stirring the granules separated by the granule separating means, and a pressure pump for returning the granules stirred by the stirrer into the upward flow anaerobic treatment reactor. It consists of and.

【0006】[0006]

【作用】本発明は上述したように構成したことにより、
処理水と共にリアクタ外へ流出したグラニュールはグラ
ニュール分離手段で分離された後に、返送手段によって
再び上昇流式嫌気性処理リアクタ内に返送されることに
なるため、リアクタ内のグラニュール量が減少すること
がなくなり、リアクタの処理能力の低下を未然に防止す
ることができる。また、グラニュール分離手段で分離さ
れたグラニュールはグラニュール返送手段の攪拌機で攪
拌されることによって、付着しているガスや油分が物理
的に除去された後、圧送ポンプによって更に肥大グラニ
ュールは細粒化され、リアクタ内に戻されることになる
ため、直ちに浮上して排出されることはない。
The present invention is constructed as described above,
The granules flowing out of the reactor together with the treated water are separated by the granule separating means and then returned to the upflow anaerobic treatment reactor by the returning means again, so the amount of granules in the reactor decreases. As a result, it is possible to prevent deterioration of the processing capacity of the reactor. Further, the granules separated by the granule separating means are stirred by the stirrer of the granule returning means to physically remove the adhering gas and oil content, and then further enlarge the granules by the pressure pump. Since it is atomized and returned to the inside of the reactor, it is not immediately floated and discharged.

【0007】[0007]

【実施例】以下、本発明の一実施例を添付図面に基づい
て詳述する。
An embodiment of the present invention will be described in detail below with reference to the accompanying drawings.

【0008】図1は本発明に係るグラニュール回収装置
1の一実施例を示したものである。図示するように、こ
のグラニュール回収装置1は上述したような従来の上昇
流式嫌気性処理リアクタAに付設されて用いられるもの
であり、その構成は処理水中のグラニュールを分離する
グラニュール分離手段2と、このグラニュール分離手段
2で分離されたグラニュールを再生して上記上昇流式嫌
気性処理リアクタA内に返送するグラニュール返送手段
3とからなっている。
FIG. 1 shows an embodiment of the granule collecting apparatus 1 according to the present invention. As shown in the figure, this granule collecting apparatus 1 is used by being attached to the conventional upflow type anaerobic treatment reactor A as described above, and its constitution is granule separation for separating granules in treated water. It comprises a means 2 and a granule returning means 3 for regenerating the granules separated by the granule separating means 2 and returning them to the upflow anaerobic treatment reactor A.

【0009】このグラニュール分離手段2はグラニュー
ル返送手段3の上部に設けられた箱体4の一側面に、目
開き0.8〜4mm程度のスクリーン5が傾斜して設け
られており、その上端部には、上記上昇流式嫌気性処理
リアクタAから流出してくる処理水を流すための流出管
6の開口端部が位置させてある。また、この箱体4は処
理水容器となっており、その底部には、溜まった処理水
を排水するための排水管7が接続されている。一方、グ
ラニュール返送手段3は上記グラニュール分離手段2を
支持するための基台8内に設けられ、上記スクリーン5
側から落下してくるグラニュールを回収するグラニュー
ル回収タンク9と、このグラニュール回収タンク9に設
けられた攪拌機10と、返送ポンプ11とからなってお
り、グラニュール回収タンク9内に回収されたグラニュ
ールを返送ポンプ11によってグラニュール回収ライン
14から再び上記上昇流式嫌気性処理リアクタA内に戻
すようになっている。また、このグラニュール回収タン
ク9には上記箱体4から排水される処理水の一部を導入
する処理水導入ライン12と、タンク9内の液を排水す
るドレン13が接続されており、必要に応じて処理水の
供給、排水ができるようになっている。尚、グラニュー
ル回収ライン14にはガス抜き弁15が設けられてお
り、必要に応じてグラニュール回収ライン14内のガス
を抜くことができるようになっている。
The granule separating means 2 is provided with a screen 5 having an opening of about 0.8 to 4 mm inclined on one side surface of a box body 4 provided on the upper part of the granule returning means 3. The open end of the outflow pipe 6 for flowing the treated water flowing out from the upward flow type anaerobic treatment reactor A is located at the upper end portion. The box body 4 is a treated water container, and a drain pipe 7 for draining the accumulated treated water is connected to the bottom of the container body. On the other hand, the granule returning means 3 is provided in the base 8 for supporting the granule separating means 2, and the screen 5 is provided.
It is composed of a granule collection tank 9 for collecting the granules falling from the side, an agitator 10 provided in the granule collection tank 9, and a return pump 11, and is collected in the granule collection tank 9. The granules are returned from the granule recovery line 14 into the upflow anaerobic treatment reactor A by the return pump 11. In addition, a treated water introducing line 12 for introducing a part of the treated water drained from the box body 4 and a drain 13 for draining the liquid in the tank 9 are connected to the granule recovery tank 9, which is required. According to the requirements, treated water can be supplied and drained. A gas vent valve 15 is provided in the granule recovery line 14 so that the gas in the granule recovery line 14 can be vented if necessary.

【0010】次に、本実施例の作用を説明する。Next, the operation of this embodiment will be described.

【0011】先ず、上昇流式嫌気性処理リアクタAから
オーバーフローした、グラニュールを含んだ処理水は流
出管6からグラニュール分離手段2のスクリーン5の上
端部側に流れ、このスクリーン5を通過して箱体4底部
に溜まった後、排水管7から排水される。一方、このグ
ラニュール分離手段2のスクリーン5に捕捉されたグラ
ニュールは、このスクリーン5上を滑り落ちて基台8の
開口部8aを通過してグラニュール返送手段3のグラニ
ュール回収タンク9内に回収され、ここで処理水導入ラ
イン12から導入された処理水の一部と共に、攪拌機1
0で所定時間攪拌される。これによって、ガスや油分が
付着したグラニュールは細粒化あるいは付着しているガ
スや油分が除去される。そして、このグラニュールは、
返送ポンプ11によってグラニュール回収タンク9から
抜き出され、グラニュール回収ライン14を通過して、
新たに流入する原水と共に上昇流式嫌気性処理リアクタ
A内に戻された後、ここで再び有機物の分解処理を行う
ことになる。
First, the treated water containing granules overflowing from the upward flow type anaerobic treatment reactor A flows from the outflow pipe 6 to the upper end side of the screen 5 of the granule separating means 2 and passes through the screen 5. After being collected at the bottom of the box body 4, it is drained from the drain pipe 7. On the other hand, the granules captured by the screen 5 of the granule separating means 2 slide down on the screen 5 and pass through the opening 8a of the base 8 and the inside of the granule collecting tank 9 of the granule returning means 3. And a part of the treated water introduced from the treated water introduction line 12 together with the stirrer 1
It is stirred at 0 for a predetermined time. As a result, the granules to which the gas or oil adheres are atomized or the adhered gas or oil is removed. And this granule
It is extracted from the granule collection tank 9 by the return pump 11, passes through the granule collection line 14,
After returning to the upflow type anaerobic treatment reactor A together with newly flowing raw water, the decomposition treatment of organic substances is performed again here.

【0012】このように本発明は処理水と共に流れ出し
たグラニュールを分離再生して再びリアクタA内に戻す
ようにしたため、リアクタA内のグラニュール量が減少
することがなくなり、上記上昇流式嫌気性処理リアクタ
の処理能力の低下を未然に防止することができる。尚、
処理水と共に流れ出したグラニュールは、グラニュール
分離手段2において一旦空気に晒されることになるが、
その時間は極短時間であり、また影響を受けるのは表層
に繁殖している僅かな嫌気性微生物のみであるため、グ
ラニュール本来の処理能力には殆ど影響はない。また、
スクリーン5の構成としては、処理水と共に流れ出した
グラニュールのみを捕捉して自由落下させることができ
るものであれば良く、ロッドを平行に並べたバースクリ
ーンや格子状の網でもよい。また、再生されたグラニュ
ールの処理能力を最大限に発揮するために、PH調整装
置等をさらに付設しても良い。
As described above, according to the present invention, the granules flowing out together with the treated water are separated and regenerated and returned to the reactor A again, so that the amount of granules in the reactor A does not decrease, and the above-mentioned upflow anaerobic system is used. It is possible to prevent a decrease in the processing capacity of the sexual processing reactor. still,
The granules flowing out together with the treated water are once exposed to the air in the granule separating means 2,
The time is extremely short, and since only a few anaerobic microorganisms growing on the surface layer are affected, there is almost no effect on the original processing capacity of granules. Also,
The screen 5 may have any structure as long as it can capture only the granules flowing out together with the treated water and allow it to fall freely, and may be a bar screen in which rods are arranged in parallel or a grid-like net. Further, in order to maximize the processing capacity of the regenerated granules, a PH adjusting device or the like may be additionally provided.

【0013】[0013]

【発明の効果】以上要するに本発明によれば、処理水と
共に流れ出したグラニュールを分離再生して再びリアク
タ内に戻ことができるため、リアクタ内のグラニュール
の濃度が低下することがなくなり、リアクタ本来の処理
能力を維持することができる等といった優れた効果を発
揮することができる。
In summary, according to the present invention, since the granules flowing out together with the treated water can be separated and regenerated and returned to the reactor again, the concentration of the granules in the reactor is not lowered and the reactor It is possible to exhibit excellent effects such as maintaining the original processing capacity.

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

【図1】本発明の一実施例を示す構成図である。FIG. 1 is a configuration diagram showing an embodiment of the present invention.

【図2】処理水と共に流れ出すグラニュールの状態を示
す概念図である。
FIG. 2 is a conceptual diagram showing a state of granules flowing out together with treated water.

【図3】従来の上昇流式嫌気性処理リアクタの構成を示
す透視斜視図である。
FIG. 3 is a perspective view showing a configuration of a conventional upflow anaerobic treatment reactor.

【符号の説明】[Explanation of symbols]

1 グラニュール回収装置 2 グラニュール分離手段 3 グラニュール返送手段 10 攪拌機 11 返送ポンプ A 上昇流式嫌気性処理リアクタ DESCRIPTION OF SYMBOLS 1 Granule recovery device 2 Granule separation means 3 Granule return means 10 Stirrer 11 Return pump A Upflow anaerobic treatment reactor

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 有機性産業廃水を、メタン生成細菌等の
嫌気性微生物を含んだ粒状のグラニュールを収容した上
昇流式嫌気性処理リアクタに供給してバイオガスと処理
水に分解処理し、その処理水と共に流出する上記グラニ
ュールを処理水から分離して再度上記上昇流式嫌気性処
理リアクタ内に戻すためのグラニュール回収装置におい
て、上記処理水中のグラニュールを分離するグラニュー
ル分離手段と、このグラニュール分離手段で分離された
グラニュールを再生して上記上昇流式嫌気性処理リアク
タ内に返送するグラニュール返送手段とからなることを
特徴とするグラニュール回収装置。
1. An organic industrial wastewater is supplied to an upflow-type anaerobic treatment reactor containing granular granules containing anaerobic microorganisms such as methanogenic bacteria and decomposed into biogas and treated water, In a granule recovery device for separating the granules flowing out together with the treated water from the treated water and returning the granules again into the upward flow anaerobic treatment reactor, a granule separation means for separating the granules in the treated water and And a granule returning means for regenerating the granules separated by the granule separating means and returning the granules into the upflow anaerobic treatment reactor.
【請求項2】 上記返送手段は上記グラニュール分離手
段で分離されたグラニュールを攪拌する攪拌機と、この
攪拌機で攪拌されたグラニュールを上記上昇流式嫌気性
処理リアクタ内に戻すための返送ポンプとからなること
を特徴とする請求項1記載のグラニュール回収装置。
2. The returning means is a stirrer for stirring the granules separated by the granule separating means, and a returning pump for returning the granules stirred by the stirrer into the upflow anaerobic treatment reactor. The granule collecting apparatus according to claim 1, wherein the granule collecting apparatus comprises:
JP06599494A 1994-04-04 1994-04-04 Granule collection device Expired - Lifetime JP3451709B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP06599494A JP3451709B2 (en) 1994-04-04 1994-04-04 Granule collection device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP06599494A JP3451709B2 (en) 1994-04-04 1994-04-04 Granule collection device

Publications (2)

Publication Number Publication Date
JPH07275885A true JPH07275885A (en) 1995-10-24
JP3451709B2 JP3451709B2 (en) 2003-09-29

Family

ID=13303079

Family Applications (1)

Application Number Title Priority Date Filing Date
JP06599494A Expired - Lifetime JP3451709B2 (en) 1994-04-04 1994-04-04 Granule collection device

Country Status (1)

Country Link
JP (1) JP3451709B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6964741B2 (en) 1995-08-11 2005-11-15 Zenon Environmental Inc. Apparatus for withdrawing permeate using an immersed vertical skein of hollow fiber membranes

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101613711B1 (en) * 2015-07-30 2016-04-20 주식회사 블루뱅크 Apparatus for selecting aerobic granule sludge

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6964741B2 (en) 1995-08-11 2005-11-15 Zenon Environmental Inc. Apparatus for withdrawing permeate using an immersed vertical skein of hollow fiber membranes

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