JP2002079283A - Aerobic treatment tank - Google Patents

Aerobic treatment tank

Info

Publication number
JP2002079283A
JP2002079283A JP2000267905A JP2000267905A JP2002079283A JP 2002079283 A JP2002079283 A JP 2002079283A JP 2000267905 A JP2000267905 A JP 2000267905A JP 2000267905 A JP2000267905 A JP 2000267905A JP 2002079283 A JP2002079283 A JP 2002079283A
Authority
JP
Japan
Prior art keywords
treatment tank
treated
water
flow
carrier
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.)
Pending
Application number
JP2000267905A
Other languages
Japanese (ja)
Inventor
Masayoshi Sakuma
正芳 佐久間
Makoto Tanaka
真 田中
Naomichi Mori
直道 森
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.)
Hitachi Plant Technologies Ltd
Original Assignee
Hitachi Plant Technologies 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 Hitachi Plant Technologies Ltd filed Critical Hitachi Plant Technologies Ltd
Priority to JP2000267905A priority Critical patent/JP2002079283A/en
Publication of JP2002079283A publication Critical patent/JP2002079283A/en
Pending 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Biological Treatment Of Waste Water (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an aerobic treatment tank capable of being prevented from the lowering of treatment capacity accompanied by the deposition of a carrier. SOLUTION: Water 14 to be treated is stored in the aerobic treatment tank 10 and a carrier 16 having microorganisms fixed thereon is charged in the water 14 to be treated. The interior of the treatment tank 10 is divided into compartments 10A and 10B by a flow guide plate 22 and an air diffuser 24 is arranged in the compartment 10A. A rectifying plate 28 is provided under the air diffuser 24 and the deviation of the circulating flow of water to be treated is prevented by the rectifying plate 28.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は好気性処理槽に係
り、特に、下水・し尿・産業排水等の有機性排水を、微
生物固定化担体を利用して生物学的に処理する好気性処
理槽に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an aerobic treatment tank, and more particularly, to an aerobic treatment tank for biologically treating organic wastewater such as sewage, human waste, and industrial wastewater using a microorganism-immobilized carrier. About.

【0002】[0002]

【従来の技術】下水や産業排水中のBODや窒素を高速
・短時間で処理するため、微生物を固定化した担体を用
いる方法が実施されている。この方法は、密度が水より
数%程度大きい担体に微生物を固定化して処理槽に投入
し、この担体を散気手段によって発生する槽内の循環流
によって流動させながら、被処理水を生物学的に処理し
ている。
2. Description of the Related Art In order to treat BOD and nitrogen in sewage and industrial wastewater at high speed and in a short time, a method using a carrier on which microorganisms are immobilized has been practiced. In this method, microorganisms are immobilized on a carrier having a density about several percent greater than that of water, and the microorganisms are introduced into a treatment tank. Processing.

【0003】従来の好気性処理槽の構造図の一例を図5
に示す。処理槽1には、流入管2から供給された被処理
水3が貯留され、該被処理水3中には、微生物を固定化
した担体4、4…が投入されている。処理槽1の中央部
には、処理槽1の内部を2つの区画1A、1Bに区分け
する導流板5が設置され、該導流板5の上下端には、被
処理水3と担体4とが流動可能な開口が形成される。
FIG. 5 shows an example of a structural diagram of a conventional aerobic treatment tank.
Shown in In the treatment tank 1, the water to be treated 3 supplied from the inflow pipe 2 is stored. In the water to be treated 3, carriers 4, 4,. In the center of the treatment tank 1, a flow guide plate 5 for dividing the inside of the treatment tank 1 into two sections 1A and 1B is installed. An opening through which the fluid can flow is formed.

【0004】区画1Aには、散気装置6が設けられてい
る。該散気装置6は、空気管7を介して供給された空気
を被処理水3中に散気する。これにより、区画1Aの被
処理水3にエアリフト作用が働いて、被処理水3が上昇
する。上昇した被処理水3は、導流板5の上端を越えて
区画1Bに下降流を形成し、さらに、導流板5の下端か
ら区画1Aに流入して再び上昇流を形成する。担体4
は、この被処理水3の循環流にのって二つの区画1A、
1Bを循環する。これにより、被処理水3が生物学的に
処理される。処理された被処理水3は、スクリーン8を
介して流出管9から排出される。
[0004] In the section 1A, an air diffuser 6 is provided. The air diffuser 6 diffuses the air supplied through the air pipe 7 into the water 3 to be treated. As a result, the air 3 acts on the water 3 to be treated in the section 1A, and the water 3 rises. The raised water to be treated 3 forms a downward flow in the section 1B beyond the upper end of the flow guide plate 5, and flows into the section 1A from the lower end of the flow guide plate 5 to form an upward flow again. Carrier 4
Is divided into two sections 1A along the circulating flow of the water 3 to be treated.
Circulate 1B. As a result, the water to be treated 3 is biologically treated. The treated water 3 is discharged from the outflow pipe 9 via the screen 8.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、従来の
好気性処理槽は、散気装置6の下方において循環流の偏
りが生じ、流速の殆ど得られない領域が発生する欠点が
あった。例えば、処理槽1のコーナー部1Cでは、循環
流の流速が殆ど得られず、担体4が次第に堆積する。こ
の結果、堆積した担体4に酸素を供給できなくなるとと
もに、堆積した担体4と被処理水との接触効率が低下す
るので、微生物によるBODや窒素の処理性能が低下す
る問題があった。
However, the conventional aerobic treatment tank has a drawback in that the circulating flow is biased below the diffuser 6 and a region where the flow velocity is hardly obtained is generated. For example, at the corner 1C of the processing tank 1, almost no flow velocity of the circulation flow is obtained, and the carrier 4 is gradually deposited. As a result, oxygen cannot be supplied to the deposited carrier 4 and the contact efficiency between the deposited carrier 4 and the water to be treated is reduced, so that there is a problem that the performance of treating BOD and nitrogen by microorganisms is reduced.

【0006】本発明はこのような事情に鑑みて成された
もので、担体の堆積に伴う処理性能の低下を防止できる
好気性処理槽を提供することを目的とする。
The present invention has been made in view of such circumstances, and an object of the present invention is to provide an aerobic treatment tank capable of preventing a decrease in treatment performance due to carrier deposition.

【0007】[0007]

【課題を解決するための手段】本発明は前記目的を達成
するために、微生物を担持した担体によって被処理水を
好気的に処理する処理槽であって、該処理槽内を上下端
に開口を有する導流板で縦方向に区分するとともに、区
分された一方の区画に散気装置を配置し、該散気装置か
らのエアによるエアリフト作用により前記一方の区画と
他方の区画との間を循環する循環流を形成し、該循環流
によって前記担体を流動状態で前記被処理水に接触させ
る好気性処理槽において、前記散気装置の下方に、前記
循環流を槽底コーナー部に導く整流板を設けたことを特
徴としている。
In order to achieve the above object, the present invention provides a treatment tank for aerobically treating water to be treated with a carrier carrying microorganisms, wherein the inside of the treatment tank is arranged at upper and lower ends. Along with the flow guide plate having an opening, the air diffusion device is arranged in one of the divided sections, and the air is lifted by the air from the air diffusion apparatus, so that the air is diffused between the one section and the other section. In the aerobic treatment tank in which the carrier is brought into contact with the water to be treated in a flowing state by the circulating flow, the circulating flow is guided to the bottom of the tank below the aeration device. It is characterized in that a current plate is provided.

【0008】本発明によれば、整流板によって循環流を
槽底コーナー部に導くようにしたので、担体が堆積する
ことを防止でき、微生物による処理性能が向上する。
According to the present invention, since the circulating flow is guided to the corner of the bottom of the tank by the flow regulating plate, the accumulation of the carrier can be prevented, and the performance of treating microorganisms is improved.

【0009】[0009]

【発明の実施の形態】以下添付図面に従って、本発明に
係る好気性処理槽の好ましい実施の形態について詳説す
る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of an aerobic treatment tank according to the present invention will be described below in detail with reference to the accompanying drawings.

【0010】図1は、本発明に係る好気性処理槽の実施
の形態を示す全体構成図である。
FIG. 1 is an overall configuration diagram showing an embodiment of an aerobic treatment tank according to the present invention.

【0011】同図に示すように、処理槽10には、流入
管12が接続され、該流入管12を介して供給された被
処理水14が貯留される。この被処理水14には、密度
が水より数%程度大きい担体16、16…が投入され、
該担体16には、被処理水14を生物学的に処理する微
生物が固定化されている。また、処理槽10には、スク
リーン18を介して流出管20が連通されており、被処
理水14が流出管20から排出されるとともに、担体1
6の流出がスクリーン18によって防止される。
As shown in FIG. 1, an inflow pipe 12 is connected to the treatment tank 10, and water 14 to be treated supplied through the inflow pipe 12 is stored. Carriers 16, 16,... Having a density about several percent higher than water are introduced into the water to be treated 14,
Microorganisms for biologically treating the water to be treated 14 are immobilized on the carrier 16. An outflow pipe 20 is connected to the treatment tank 10 via a screen 18 so that the water 14 to be treated is discharged from the outflow pipe 20 and the carrier 1
The outflow of 6 is prevented by the screen 18.

【0012】処理槽10の中央部には、導流板22が略
鉛直に設けられ、該導流板22によって、処理槽10の
内部が二つの区画10A、10Bに分けられる。導流板
22の上端及び下端には、開口が形成されており、この
開口を介して被処理水14及び担体16が二つの区画1
0A、10Bを流動する。
At the center of the processing tank 10, a flow guide plate 22 is provided substantially vertically, and the inside of the processing tank 10 is divided into two sections 10A and 10B by the flow guide plate 22. Openings are formed at the upper and lower ends of the flow guide plate 22, through which the water 14 to be treated and the carrier 16 are divided into two sections 1.
Flow 0A, 10B.

【0013】区画10Aには、散気装置24が配設され
ている。この散気装置24は、空気管26に連通されて
おり、該空気管26から空気が供給されると、この空気
を被処理水14中に散気する。
An air diffuser 24 is provided in the section 10A. The air diffuser 24 is communicated with an air pipe 26. When air is supplied from the air pipe 26, the air diffuses into the water 14 to be treated.

【0014】散気装置24の下方には、整流板28が設
けられている。整流板28は、被処理水14の循環流が
衝突しやすい位置、例えば、導流板22の下端と略同じ
高さに配設され、その上端が導流板22側に傾斜して設
置される。また、整流板28は、その上端と導流板22
との間に所定の隙間W1を形成するとともに、その下端
と処理槽10の底との間に所定の隙間W2を形成するよ
うに設けられる。ここで、所定の隙間W1、W2は、処
理槽10の大きさや散気装置24の位置によって適宜決
定される値であり、隙間W1は、整流板28の上に担体
16が堆積しないような値に設定される。また、隙間W
2は、担体16を流動させる流速が得られる大きさで、
且つ、担体16によって閉塞しない大きさに設定され
る。
A current plate 28 is provided below the air diffuser 24. The flow straightening plate 28 is disposed at a position where the circulating flow of the water 14 to be treated is likely to collide, for example, at substantially the same height as the lower end of the flow guide plate 22, and the upper end thereof is installed inclined toward the flow guide plate 22. You. In addition, the current plate 28 is connected to the upper end thereof and the flow guide plate 22.
Are formed so as to form a predetermined gap W1 between the lower end of the processing tank 10 and a predetermined gap W2 between the lower end thereof and the bottom of the processing tank 10. Here, the predetermined gaps W1 and W2 are values appropriately determined according to the size of the processing tank 10 and the position of the air diffuser 24. Is set to Also, the gap W
2 is a size capable of obtaining a flow rate at which the carrier 16 flows,
In addition, the size is set so as not to be blocked by the carrier 16.

【0015】次に上記の如く構成された好気性処理槽の
作用について説明する。
Next, the operation of the aerobic treatment tank configured as described above will be described.

【0016】散気装置24から被処理水14中に散気す
ると、担体16に固定化された微生物に酸素が供給され
るとともに、散気によって生じた気泡が上昇し、区画1
0Aに被処理水14の上昇流が形成される。区画10A
を上昇した被処理水14は、導流板22の上端を越えて
区画10Bに下降流を形成し、さらに、導流板22の下
端を潜って区画10Aに流入する。これにより、区画1
0Aと区画10Bを循環する被処理水14の循環流が形
成される。担体16は、この循環流にのって流動しなが
ら、被処理水14を生物学的に処理する。処理された被
処理水14は、スクリーン18を介して流出管20から
流出される。
When air is diffused from the air diffuser 24 into the water 14 to be treated, oxygen is supplied to the microorganisms immobilized on the carrier 16, and bubbles generated by the air diffusion rise, and
An upward flow of the water to be treated 14 is formed at 0A. Section 10A
Is formed in the section 10B over the upper end of the flow guide plate 22, and flows into the section 10A below the lower end of the flow guide plate 22. Thereby, section 1
A circulating flow of the water to be treated 14 circulating in the section 0A and the section 10B is formed. The carrier 16 biologically treats the water 14 to be treated while flowing along the circulation flow. The treated water 14 flows out of the outflow pipe 20 via the screen 18.

【0017】ところで、導流板22の下端を潜って区画
10Bから区画10Aに流入する被処理水14の循環流
は、整流板28に衝突することによって、図2に示すよ
うに、隙間W1を通って散気装置24に直接向かう分流
Aと、隙間W2を通って処理槽10のコーナー部10C
から散気装置24に向かう分流Bとに別れる。これによ
り、区画10Aを流れる循環流の偏りが抑制され、コー
ナー部10Cにも、流速の大きい循環流が与えられる。
したがって、担体16は、堆積することなく、処理槽1
0内を流動するので、処理槽10の内部における微生物
濃度が均一化される。
By the way, the circulating flow of the water to be treated 14 flowing from the section 10B into the section 10A under the lower end of the flow guide plate 22 collides with the rectifying plate 28, thereby forming a gap W1 as shown in FIG. The diversion A directly passing through the air diffuser 24 through the air passage 24, and the corner 10C of the processing tank 10 through the gap W2.
From the air flow to the air diffuser 24. Thereby, the bias of the circulating flow flowing through the section 10A is suppressed, and the circulating flow having a high flow velocity is also provided to the corner 10C.
Therefore, the carrier 16 is deposited on the processing tank 1 without being deposited.
Since the fluid flows through the inside of the treatment tank 10, the concentration of microorganisms in the processing tank 10 is uniformed.

【0018】このように本実施の形態の好気性処理槽に
よれば、散気装置24の下方に整流板28を設けること
によって、循環流の偏りを防止できるので、処理槽10
内の微生物濃度を均一化でき、微生物による処理性能が
向上する。
As described above, according to the aerobic treatment tank of the present embodiment, since the rectifying plate 28 is provided below the air diffuser 24, the bias of the circulating flow can be prevented.
The concentration of microorganisms in the inside can be made uniform, and the processing performance by microorganisms is improved.

【0019】また、上述した実施の形態では、整流板2
8を傾けて設置したので、整流板28の上に担体16が
堆積しにくく、担体16を効率良く循環させることがで
きる。
In the above-described embodiment, the current plate 2
Since the carrier 8 is inclined, the carrier 16 is not easily deposited on the current plate 28, and the carrier 16 can be efficiently circulated.

【0020】なお、整流板28の形状は、上述した実施
の形態に限定されるものではなく、被処理水14の循環
流の偏りを抑制するものであればよい。例えば、図2に
示した整流板28を、鉛直、或いは水平に設置してもよ
い。また、図3に示すように、循環流の流れ方向に湾曲
した整流板30を設けてもよい。この場合には、整流板
30の抵抗が小さくなるので、少ない散気量で効率良く
被処理水14を循環させることができるとともに、強度
の小さい整流板30を用いることができる。
The shape of the current plate 28 is not limited to the above-described embodiment, but may be any shape as long as it suppresses the bias of the circulating flow of the water 14 to be treated. For example, the current plate 28 shown in FIG. 2 may be installed vertically or horizontally. Further, as shown in FIG. 3, a flow straightening plate 30 curved in the flow direction of the circulating flow may be provided. In this case, since the resistance of the current plate 30 is reduced, the water 14 to be treated can be efficiently circulated with a small amount of air diffusion, and the current plate 30 having a small strength can be used.

【0021】また、整流板28や整流板30の個数は、
一つに限定するものではなく、複数であってもよい。例
えば、図4には、3個の整流板32、33、34が設置
されている。整流板32〜34はそれぞれ、上端が導流
板22側に傾斜して配置されるとともに、各整流板32
〜34は、所定の間隔をもって配置される。さらに、整
流板33の下端は、整流板32の下端よりも低く配置さ
れ、整流板34の下端は、整流板33の下端よりも低く
配置される。したがって、区画10Bから区画10Aに
流入した循環流は、各整流板32〜34に衝突して分流
され、各整流板32〜34の間、又は、導流板22に沿
って、或いは、処理槽10のコーナー部10Cに沿って
流れる。これにより、区画10Aに略均一な流速の循環
流が形成される。
The number of the current plates 28 and 30 is as follows.
The number is not limited to one and may be plural. For example, in FIG. 4, three current plates 32, 33, and 34 are provided. Each of the rectifying plates 32 to 34 is disposed so that the upper end is inclined toward the flow guide plate 22, and
Are arranged at predetermined intervals. Further, the lower end of the current plate 33 is arranged lower than the lower end of the current plate 32, and the lower end of the current plate 34 is arranged lower than the lower end of the current plate 33. Therefore, the circulating flow that has flowed into the section 10A from the section 10B collides with each of the straightening plates 32 to 34 and is divided, and is divided between the straightening plates 32 to 34, along the flow guide plate 22, or in the processing tank. It flows along the 10 corners 10C. Thereby, a circulating flow having a substantially uniform flow rate is formed in the section 10A.

【0022】また、上述した実施の形態は、導流板22
によって処理槽10を二つの区画10A、10Bに区画
したが、三つ以上の区画に分けた場合や、区分けしない
場合にも適用することができる。
In the above-described embodiment, the flow guide plate 22
Although the processing tank 10 is divided into two sections 10A and 10B by the above, the present invention can be applied to a case where the processing tank 10 is divided into three or more sections or a case where no division is performed.

【0023】[0023]

【発明の効果】以上説明したように本発明に係る好気性
処理槽によれば、整流板によって槽底コーナー部にも循
環流を導くようにしたので、担体の堆積を防止すること
ができ、微生物による処理性能を向上させることができ
る。
As described above, according to the aerobic treatment tank of the present invention, since the circulating flow is guided to the corner of the tank bottom by the rectifying plate, the accumulation of the carrier can be prevented. The processing performance by microorganisms can be improved.

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

【図1】本発明に係る好気性処理槽の全体構成を示す側
面断面図
FIG. 1 is a side cross-sectional view showing the overall configuration of an aerobic treatment tank according to the present invention.

【図2】図1の好気性処理槽の作用を示す説明図FIG. 2 is an explanatory view showing the operation of the aerobic treatment tank in FIG.

【図3】図2と異なる整流板を示す側面断面図FIG. 3 is a side sectional view showing a current plate different from FIG. 2;

【図4】図2と異なる整流板を示す側面断面図FIG. 4 is a side sectional view showing a current plate different from FIG. 2;

【図5】従来装置を示す側面断面図FIG. 5 is a side sectional view showing a conventional apparatus.

【符号の説明】[Explanation of symbols]

10…処理槽、10A、10B…区画、12…流入管、
14…被処理水、16…担体、18…スクリーン、20
…流出管、22…導流板、24…散気装置、28…整流
10 ... treatment tank, 10A, 10B ... section, 12 ... inflow pipe,
14 ... water to be treated, 16 ... carrier, 18 ... screen, 20
... outflow pipe, 22 ... flow guide plate, 24 ... diffuser, 28 ... straightening plate

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】微生物を担持した担体によって被処理水を
好気的に処理する処理槽であって、該処理槽内を上下端
に開口を有する導流板で縦方向に区分するとともに、区
分された一方の区画に散気装置を配置し、該散気装置か
らのエアによるエアリフト作用により前記一方の区画と
他方の区画との間を循環する循環流を形成し、該循環流
によって前記担体を流動状態で前記被処理水に接触させ
る好気性処理槽において、 前記散気装置の下方に、前記循環流を槽底コーナー部に
導く整流板を設けたことを特徴とする好気性処理槽。
1. A treatment tank for aerobically treating water to be treated with a carrier carrying microorganisms, wherein the inside of the treatment tank is vertically divided by a flow guide plate having openings at upper and lower ends. A diffuser is arranged in one of the divided sections, and a circulating flow circulating between the one section and the other section is formed by an air lift action by air from the diffuser, and the carrier is formed by the circulating flow. An aerobic treatment tank that contacts the treated water in a fluidized state, wherein a rectifying plate for guiding the circulating flow to a tank bottom corner is provided below the air diffuser.
JP2000267905A 2000-09-05 2000-09-05 Aerobic treatment tank Pending JP2002079283A (en)

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Publications (1)

Publication Number Publication Date
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Family

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006053402A1 (en) * 2004-11-22 2006-05-26 Nubian Water Systems Pty Limited Waste water treatment process system
KR100835844B1 (en) * 2006-03-16 2008-06-09 (주)오리코스포텍 manufacture method of recyclable shock-absorbing popcorn- stuffed packingenvironmently friendly material
US7419594B2 (en) 2003-10-09 2008-09-02 Shaw Environmental & Infrastructure, Inc. Apparatus and method for controlling biomass growth in suspended carrier bioreactor
KR101444791B1 (en) * 2014-03-31 2014-09-26 성지환경기술(주) wastewater treatment system

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7419594B2 (en) 2003-10-09 2008-09-02 Shaw Environmental & Infrastructure, Inc. Apparatus and method for controlling biomass growth in suspended carrier bioreactor
WO2006053402A1 (en) * 2004-11-22 2006-05-26 Nubian Water Systems Pty Limited Waste water treatment process system
US7785469B2 (en) 2004-11-22 2010-08-31 Nubian Water Systems Pty Ltd Waste water treatment process system
GB2425305B (en) * 2005-04-15 2009-01-14 Shaw Environmental & Infrastru Apparatus and method for controlling biomass growth in suspended carrier bioreactor
KR100835844B1 (en) * 2006-03-16 2008-06-09 (주)오리코스포텍 manufacture method of recyclable shock-absorbing popcorn- stuffed packingenvironmently friendly material
KR101444791B1 (en) * 2014-03-31 2014-09-26 성지환경기술(주) wastewater treatment system

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