JP2003080285A - Water treatment equipment - Google Patents
Water treatment equipmentInfo
- Publication number
- JP2003080285A JP2003080285A JP2001273203A JP2001273203A JP2003080285A JP 2003080285 A JP2003080285 A JP 2003080285A JP 2001273203 A JP2001273203 A JP 2001273203A JP 2001273203 A JP2001273203 A JP 2001273203A JP 2003080285 A JP2003080285 A JP 2003080285A
- Authority
- JP
- Japan
- Prior art keywords
- carrier
- wastewater
- flow
- cylindrical body
- water treatment
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、微生物を保持した
担体を用いて排水を浄化処理する水処理装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water treatment device for purifying waste water by using a carrier holding microorganisms.
【0002】[0002]
【従来の技術】従来、この種の担体法の水処理装置とし
ては、例えば特開2001−29975号公報、特開2
001−38377号公報等に記載された構造のもの知
られている。2. Description of the Related Art Conventionally, water treatment apparatuses of this type of carrier method are disclosed in, for example, JP 2001-29975A and JP 2A.
The structure described in Japanese Patent Publication No. 001-38377 is known.
【0003】この従来の水処理装置は、反応槽内に軸方
向が上下方向に一致するように配置された上下面開口状
で円筒状の筒状体とこの筒状体内に下降流を発生させる
下降流発生手段とを備え、この筒状体内には円筒状の担
体分離部を設け、この担体分離部にて担体の分離除去さ
れた排水を流出管にて反応槽外に流出させる構成となっ
ている。In this conventional water treatment device, a cylindrical cylindrical body having upper and lower openings and arranged in the reaction tank so that the axial directions thereof coincide with each other in the vertical direction, and a downward flow is generated in the cylindrical body. Downstream generating means is provided, and a cylindrical carrier separating portion is provided in the cylindrical body, and the waste water from which the carrier has been separated and removed by the carrier separating portion is made to flow out of the reaction tank through an outflow pipe. ing.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、上記従
来の水処理装置は、例えば筒状体内の下降流を一部とす
る旋回循環流が反応槽内に生じにくく、浄化処理効率を
十分なまでに高めることができないおそれがあるという
問題を有している。However, in the above-mentioned conventional water treatment apparatus, for example, a swirl circulation flow, which is a part of the downward flow in the cylindrical body, is unlikely to occur in the reaction tank, and the purification treatment efficiency is sufficiently high. There is a problem that it may not be possible to increase the value.
【0005】本発明は、このような点に鑑みなされたも
ので、筒状体内の下降流を一部とする旋回循環流を反応
槽内に適切に発生させることができ、浄化処理効率を十
分に高めることができる水処理装置を提供することを目
的とする。The present invention has been made in view of the above points, and can appropriately generate a swirling circulation flow having a downward flow in the tubular body as a part in the reaction tank, thereby sufficiently improving the purification treatment efficiency. It is an object of the present invention to provide a water treatment device that can be improved.
【0006】[0006]
【課題を解決するための手段】請求項1記載の水処理装
置は、微生物を保持した担体を用いて排水を浄化処理す
る水処理装置であって、微生物を保持した担体を含んだ
排水を貯留する反応槽と、この反応槽内に軸方向が上下
方向に一致するように配置され、上面開口部および下面
開口部を有する上下面開口状の筒状体と、この筒状体内
に下降流を発生させる下降流発生手段と、前記筒状体の
下方位置に配置され、前記下降流発生手段による下降流
によって前記筒状体内から前記下面開口部を通って流出
する排水から担体を分離除去するとともに、前記下降流
発生手段による下降流を上下方向に対して傾斜した方向
の傾斜流に変換する担体分離手段とを備えたものであ
る。A water treatment apparatus according to claim 1 is a water treatment apparatus for purifying wastewater by using a carrier holding microorganisms, and storing the wastewater containing the carrier holding microorganisms. And a cylindrical body having upper and lower openings having an upper surface opening and a lower surface opening, which are arranged in the reaction tank such that the axial directions thereof coincide with each other in the vertical direction, and a downward flow in the cylindrical body. The descending flow generating means to be generated and the carrier disposed in a position below the cylindrical body are separated and removed from the drainage flowing out from the cylindrical body through the lower surface opening by the descending flow generated by the descending flow generating means. And carrier separating means for converting the downward flow generated by the downward flow generating means into an inclined flow in a direction inclined with respect to the vertical direction.
【0007】そして、下降流発生手段による下降流によ
って筒状体内から下面開口部を通って流出する排水から
担体を分離除去するとともに下降流発生手段による下降
流を上下方向に対して傾斜した方向の傾斜流に変換する
担体分離手段を筒状体の下方位置に配置したため、筒状
体内の下降流を一部とする旋回循環流が反応槽内に適切
に発生する。Then, the carrier is separated and removed from the drainage flowing out from the cylindrical body through the lower surface opening by the downward flow generated by the downward flow generating means, and the downward flow generated by the downward flow generating means is inclined in the vertical direction. Since the carrier separating means for converting into the inclined flow is arranged at the lower position of the cylindrical body, the swirling circulation flow, which is a part of the downward flow in the cylindrical body, is appropriately generated in the reaction tank.
【0008】請求項2記載の水処理装置は、請求項1記
載の水処理装置において、担体分離手段は、筒状体と同
軸上に位置し、上端から下端に向って徐々に拡径した円
錐状の本体部と、この本体部に開口形成され、担体の通
過を禁止することで排水から担体を分離除去し、この担
体が分離除去された排水を通過させる排水通過部とを有
するものである。According to a second aspect of the present invention, there is provided the water treatment apparatus according to the first aspect, wherein the carrier separating means is located coaxially with the tubular body and has a cone whose diameter gradually increases from the upper end to the lower end. And a drainage passage portion which is formed in an opening in the body portion and which separates and removes the carrier from the wastewater by prohibiting the passage of the carrier, and through which the wastewater separated and removed by the carrier passes. .
【0009】そして、円錐状の本体部およびこの本体部
に開口形成した排水通過部を有する担体分離手段によ
り、簡単な構成であるにも拘わらず、筒状体内の下降流
を一部とする旋回循環流が反応槽内に適切に発生する。The carrier separating means having the conical main body and the drainage passage formed in the main body has a simple structure, but the swirl is caused by a downward flow in the tubular body. Circulating flow is properly generated in the reaction vessel.
【0010】請求項3記載の水処理装置は、請求項1記
載の水処理装置において、担体分離手段は、筒状体と同
軸上に位置し、上端から下端に向って徐々に拡がった角
錐状の本体部と、この本体部に開口形成され、担体の通
過を禁止することで排水から担体を分離除去し、この担
体が分離除去された排水を通過させる排水通過部とを有
するものである。According to a third aspect of the present invention, in the water treatment apparatus according to the first aspect, the carrier separating means is located on the same axis as the cylindrical body and has a pyramidal shape that gradually expands from the upper end to the lower end. And a drainage passage portion which is formed in the body portion and has an opening formed in the body portion to separate and remove the carrier from the wastewater by passing through the wastewater.
【0011】そして、角錐状の本体部およびこの本体部
に開口形成した排水通過部を有する担体分離手段によ
り、簡単な構成であるにも拘わらず、筒状体内の下降流
を一部とする旋回循環流が反応槽内に適切に発生する。The carrier separating means having the pyramid-shaped main body and the drainage passage formed in the main body has a simple structure, but a swirl part of which is the downward flow in the tubular body. Circulating flow is properly generated in the reaction vessel.
【0012】請求項4記載の水処理装置は、請求項2ま
たは3記載の水処理装置において、排水通過部は、傾斜
流の方向に長手方向を有する複数の長孔にて構成されて
いるものである。According to a fourth aspect of the present invention, there is provided the water treatment apparatus according to the second or third aspect, wherein the drainage passage comprises a plurality of elongated holes having a longitudinal direction in the direction of the inclined flow. Is.
【0013】そして、排水通過部を傾斜流の方向に長手
方向を有する複数の長孔にて構成したので、例えば排水
中に混入した繊維状物等の絡みを防止可能である。Further, since the drainage passage is composed of a plurality of elongated holes having a longitudinal direction in the direction of the inclined flow, it is possible to prevent entanglement of fibrous substances mixed in the drainage.
【0014】請求項5記載の水処理装置は、請求項1な
いし4のいずれかに記載の水処理装置において、下降流
発生手段は、筒状体内で駆動回転してこの筒状体内に下
降流を発生させる複数の回転羽根を有するものである。According to a fifth aspect of the present invention, there is provided the water treatment apparatus according to any of the first to fourth aspects, wherein the descending flow generating means is driven and rotated in the cylindrical body to descend into the cylindrical body. It has a plurality of rotating blades for generating.
【0015】そして、複数の回転羽根を筒状体内で駆動
回転させることにより、筒状体内に下降流を確実に発生
させることが可能である。By driving and rotating the plurality of rotary blades in the cylindrical body, it is possible to reliably generate a downward flow in the cylindrical body.
【0016】[0016]
【発明の実施の形態】以下、本発明の水処理装置の一実
施の形態の構成を図面を参照して説明する。BEST MODE FOR CARRYING OUT THE INVENTION A configuration of an embodiment of a water treatment apparatus of the present invention will be described below with reference to the drawings.
【0017】図1において、1は水処理装置で、この水
処理装置1は、生活排水、産業排水、埋立浸出水等の排
水2を、微生物を保持した担体(微生物固定化担体)3
を用いて生物学的に浄化処理する担体法の水処理装置で
ある。なお、担体3は、例えば排水2に対して不溶性で
排水2に浮遊可能な多孔質粒状体等にて構成され、その
表面および微細孔に微生物が固定化されているものであ
る。In FIG. 1, reference numeral 1 denotes a water treatment device, which is a carrier (microorganism immobilization carrier) 3 for holding wastewater 2 such as domestic wastewater, industrial wastewater, landfill leachate, etc.
This is a carrier-type water treatment device for biological purification treatment using. The carrier 3 is composed of, for example, a porous granular material that is insoluble in the wastewater 2 and can float in the wastewater 2, and has microorganisms immobilized on its surface and fine pores.
【0018】そして、水処理装置1は、図1に示すよう
に、微生物を保持した複数の担体3を含んだ排水2を貯
留する貯留槽である反応槽5を備え、この反応槽5内に
排水流入手段である流入管6から浄化処理すべき排水2
が流入されるとともに所定の方法にて複数の担体3が投
入される構成となっている。As shown in FIG. 1, the water treatment device 1 is provided with a reaction tank 5 which is a storage tank for storing the waste water 2 containing a plurality of carriers 3 holding microorganisms. Wastewater 2 to be purified from the inflow pipe 6 which is the wastewater inflow means
And a plurality of carriers 3 are introduced by a predetermined method.
【0019】この反応槽5は、例えば上面開口状の箱形
状、すなわち、水平状の底板部8およびこの底板部8の
周縁から立ち上った垂直状の側板部9を有する有底の筒
形状(例えば、円筒状、或いは、3角、4角等の多角筒
状)に形成されている。また、反応槽5は、例えば脱窒
槽等の嫌気性反応槽であり、固定化微生物はそれに応じ
た脱窒菌等の嫌気性微生物である。The reaction tank 5 has, for example, a box shape with an open top, that is, a bottomed tubular shape having a horizontal bottom plate portion 8 and a vertical side plate portion 9 rising from the peripheral edge of the bottom plate portion 8 (for example, , A cylindrical shape, or a polygonal tubular shape such as a triangular shape or a triangular shape). The reaction tank 5 is, for example, an anaerobic reaction tank such as a denitrification tank, and the immobilized microorganisms are anaerobic microorganisms such as denitrification bacteria.
【0020】そして、反応槽5内には、上面開口部11お
よび下面開口部12を有する上下面開口状の筒形状(例え
ば、円筒状、或いは、3角、4角等の多角筒状)に形成
された整流体である筒状体13が、この筒状体13の軸方向
が上下方向に一致した状態で反応槽5内の略中央位置に
配置されている。Then, in the reaction tank 5, there is formed a cylindrical shape having an upper surface opening 11 and a lower surface opening 12 and having upper and lower openings (for example, a cylindrical shape, or a polygonal cylindrical shape such as a triangle or a square). The formed tubular body 13, which is a rectifying body, is arranged at a substantially central position in the reaction tank 5 with the axial direction of the tubular body 13 aligned with the vertical direction.
【0021】この上下に開口した筒状体13は、この筒状
体13全体が反応槽5内に貯留された排水2に浸漬される
ように、反応槽5の容量に対応した所定の寸法となって
いる。すなわち、筒状体13の入口部である上面開口部11
が反応槽5内に貯留された排水2の水面より下方に位置
し、筒状体13の出口部である下面開口部12が反応槽5の
底面(底板部8の上面)より上方に位置し、筒状体13全
体が排水2に浸漬されている。The tubular body 13 having the upper and lower openings has a predetermined size corresponding to the capacity of the reaction tank 5 so that the entire tubular body 13 is immersed in the waste water 2 stored in the reaction tank 5. Has become. That is, the upper surface opening 11 that is the inlet of the tubular body 13.
Is located below the water surface of the waste water 2 stored in the reaction tank 5, and the lower surface opening 12 which is the outlet of the tubular body 13 is located above the bottom surface of the reaction tank 5 (the upper surface of the bottom plate portion 8). The entire tubular body 13 is immersed in the drainage 2.
【0022】また、水処理装置1は、筒状体13内に下降
流Aを発生させる下降流発生手段21を備えている。Further, the water treatment device 1 is provided with the downflow generating means 21 for generating the downflow A in the cylindrical body 13.
【0023】この下降流発生手段21は、駆動源である駆
動モータ22を有し、この駆動モータ22には上下方向の回
転軸23の上端部が取り付けられ、この回転軸23の筒状体
13内に位置する下端部には複数のインペラ等の撹拌翼で
ある回転羽根24が放射状に取り付けられている。これら
複数の回転羽根24は、駆動モータ22からの動力で回転軸
23と一体となって筒状体13内で駆動回転し、この筒状体
13内に排水2の下降流Aを発生させる構成となってい
る。なお、筒状体13および下降流発生手段21にてドラフ
トチューブ式の撹拌手段30が構成されている。The descending flow generating means 21 has a drive motor 22 which is a drive source. The drive motor 22 is provided with an upper end portion of a rotary shaft 23 in the vertical direction, and a cylindrical body of the rotary shaft 23.
Rotating blades 24, which are stirring blades such as a plurality of impellers, are radially attached to the lower end located inside 13. The plurality of rotary vanes 24 are rotated by the power from the drive motor 22.
It is driven and rotated in the tubular body 13 together with the 23
It is configured to generate a downward flow A of the drainage 2 in the inside 13. The tubular body 13 and the downward flow generating means 21 constitute a draft tube type stirring means 30.
【0024】さらに、水処理装置1は、下降流発生手段
21による下降流Aによって筒状体13内から下面開口部12
を通って流出する排水2から担体3を捕捉して分離除去
するとともに、下降流発生手段21による下降流Aを上下
方向に対して所定角度(30°〜60°、好ましくは4
5°)αをもって傾斜した方向の直線状の傾斜流(下降
傾斜流)Bに変換する担体分離手段であるスクリーン31
を備え、このスクリーン31は、筒状体13の下方位置でか
つ反応槽5内の下部位置に配置され、反応槽5の底板部
8上に載置された状態となっている。すなわち、スクリ
ーン31は、反応槽5内から担体3を含まない排水2を取
り出すためのもので、筒状体13の下方近傍位置つまり反
応槽5底部における筒状体13内から吐出つまり噴出する
液流である下降流Aに曝される位置に配置されている。Further, the water treatment device 1 has a downflow generating means.
The downward flow A from 21 causes the lower surface opening 12 from the inside of the cylindrical body 13.
The carrier 3 is captured and separated and removed from the waste water 2 flowing out through the downward flow A, and the downward flow A generated by the downward flow generating means 21 is inclined at a predetermined angle (30 ° to 60 °, preferably 4 °).
5 °) α and a screen 31 which is a carrier separating means for converting into a linear inclined flow (downward inclined flow) B in the inclined direction.
The screen 31 is disposed below the tubular body 13 and at a lower position in the reaction tank 5, and is placed on the bottom plate portion 8 of the reaction tank 5. That is, the screen 31 is for taking out the wastewater 2 not containing the carrier 3 from the inside of the reaction tank 5, and the liquid discharged or ejected from the inside of the cylindrical body 13 at the lower vicinity of the cylindrical body 13, that is, the bottom of the reaction tank 5. It is arranged at a position where it is exposed to a downward flow A which is a flow.
【0025】このスクリーン31は、図2に示されるよう
に、上端から下端に向って徐々に拡径した円錐状の本体
部32を有し、本体部32は筒状体13と同軸上に位置し、本
体部32の中心軸線と筒状体13の中心軸線と回転軸23の回
転中心軸線とが一致している。As shown in FIG. 2, the screen 31 has a conical main body 32 whose diameter gradually increases from the upper end to the lower end, and the main body 32 is positioned coaxially with the tubular body 13. However, the central axis of the main body 32, the central axis of the tubular body 13, and the central axis of rotation of the rotary shaft 23 coincide with each other.
【0026】また、本体部32の頂点である上端側すなわ
ち本体部32の上部には、担体3の通過を禁止することで
排水2から担体3を分離除去し、この担体3が分離除去
された排水2を処理水として通過させる開口部である排
水通過部33が開口形成されている。すなわち、本体部32
の筒状体13との対向部分のみに、筒状体13側である上方
に向って開口する排水通過部33が開口形成されている。The carrier 3 is separated and removed from the drainage 2 by prohibiting passage of the carrier 3 on the upper end side which is the apex of the body 32, that is, on the upper part of the body 32, and the carrier 3 is separated and removed. A drainage passage portion 33, which is an opening through which the wastewater 2 passes as treated water, is formed. That is, the main body 32
A drainage passage portion 33 is formed only at a portion facing the tubular body 13 and opens upward toward the tubular body 13.
【0027】この排水通過部33は、例えば傾斜流Bの方
向に長手方向を有する放射状の複数の長孔34にて構成さ
れている。これら複数の長孔34は、担体3より小さい幅
寸法のスリット状に形成され、互いに等間隔をおいて本
体部32の周方向に並んだ状態でこの本体部32の略全周に
わたって位置している。なお、本体部32の長孔34以外の
部分の外周面(周側面)全体が、下降流Aを傾斜流Bに
変換する傾斜状の作用面である案内面35となっている。The drainage passage portion 33 is composed of a plurality of radial elongated holes 34 having a longitudinal direction in the direction of the inclined flow B, for example. The plurality of elongated holes 34 are formed in a slit shape having a width smaller than that of the carrier 3, and are arranged over substantially the entire circumference of the main body 32 in a state of being arranged at equal intervals in the circumferential direction of the main body 32. There is. The entire outer peripheral surface (peripheral side surface) of the main body portion 32 other than the elongated hole 34 is a guide surface 35 that is an inclined action surface that converts the downward flow A into the inclined flow B.
【0028】また、水処理装置1は、スクリーン31によ
って担体3が分離除去された排水2である処理水を反応
槽5外に流出させる排水流出手段である流出管41を備
え、この流出管41は、反応槽5内の下部位置で底板部8
に沿って水平状に配置されている。Further, the water treatment device 1 is provided with an outflow pipe 41 which is a wastewater outflow means for outflowing the treated water, which is the wastewater 2 from which the carrier 3 has been separated and removed by the screen 31, to the outside of the reaction tank 5. Is a bottom plate portion 8 at a lower position in the reaction tank 5.
Are arranged horizontally along the.
【0029】この流出管41の一端部である上流端部がス
クリーン31の本体部32に連結され、流出管41の内部流路
42が本体部32の内部空間43に連通している。また、流出
管41の他端部である下流端部は、次処理工程の図示しな
い槽(反応槽、沈殿槽等)内で開口している。なお、図
示しないが、反応槽5内で発生して排水2とともに排水
通過部33を通過した窒素ガス等による気泡を処理水から
分離除去可能なチャンバー等の気泡除去手段を流出管41
の途中に設けてもよい。The upstream end, which is one end of the outflow pipe 41, is connected to the main body 32 of the screen 31, and the internal flow path of the outflow pipe 41 is connected.
42 communicates with the internal space 43 of the main body 32. The downstream end, which is the other end of the outflow pipe 41, is open in a tank (reaction tank, precipitation tank, etc.) (not shown) in the next treatment step. Although not shown, a bubble removing means such as a chamber capable of separating and removing bubbles caused by nitrogen gas or the like generated in the reaction tank 5 and having passed through the drainage passage 33 together with the drainage 2 from the treated water is provided in the outflow pipe 41.
It may be provided in the middle of.
【0030】次に、上記一実施の形態の水処理装置1の
作用を説明する。Next, the operation of the water treatment device 1 of the above-described embodiment will be described.
【0031】水処理装置1の運転時には、下降流発生手
段21の駆動モータ22からの動力で回転羽根24が回転軸23
と一体となって筒状体13内で所定方向に駆動回転し、筒
状体13内に下降流Aが発生する。When the water treatment device 1 is in operation, the rotary vane 24 is rotated by the power from the drive motor 22 of the downward flow generating means 21.
In combination with the cylinder body 13, the cylinder body 13 is driven and rotated in a predetermined direction, and a downward flow A is generated in the cylinder body 13.
【0032】筒状体13内に下降流Aが発生すると、微生
物を保持した担体3を含んだ排水2は、下降流Aによっ
て筒状体13内すなわち筒状体13の内部流路を下方流動
し、この内部流路から下面開口部12を通って流出(噴
出)し、下方のスクリーン31に向って下方流動する。な
お、筒状体13内から流出する際における下降流Aを形成
する排水2の流速が、例えば1m/s〜3m/sの範囲
の値になるように設定されている。When the downward flow A is generated in the tubular body 13, the wastewater 2 containing the carrier 3 holding the microorganisms flows downward in the tubular body 13 by the downward flow A, that is, in the internal flow path of the tubular body 13. Then, it flows out (jets) from this internal flow path through the lower surface opening 12, and flows downward toward the lower screen 31. The flow velocity of the drainage 2 forming the downward flow A when flowing out of the tubular body 13 is set to a value in the range of 1 m / s to 3 m / s, for example.
【0033】そして、排水2中に浮遊している担体3は
スクリーン31によって捕捉されて分離除去され、この担
体3の分離除去された排水2は、処理水として排水通過
部33を通過して本体部32の内部空間43に入り込み、その
後、流出管41の内部流路42を通って次処理工程の図示し
ない槽内に流れ込む。The carrier 3 floating in the wastewater 2 is captured and separated and removed by the screen 31, and the wastewater 2 separated and removed from the carrier 3 passes through the wastewater passage portion 33 as treated water and passes through the main body. It enters the internal space 43 of the portion 32, and then flows through the internal flow path 42 of the outflow pipe 41 into the tank (not shown) of the next processing step.
【0034】排水2から分離された担体3は、スクリー
ン31の排水通過部33の周囲に一旦付着するが、すぐに傾
斜流B(本体部32の案内面35であるスクリーン面に沿っ
た掃流)により洗い流され、本体部32の案内面35に沿っ
て移動する。このため、排水2中から分離された担体3
でスリット状の各長孔34が閉塞されて詰まるようなこと
がなく、排水通過部33で担体3の分離が連続して適切に
行われる。The carrier 3 separated from the drainage 2 once adheres to the periphery of the drainage passage portion 33 of the screen 31, but immediately the inclined flow B (sweeping along the screen surface which is the guide surface 35 of the main body portion 32) is performed. ), And moves along the guide surface 35 of the main body 32. Therefore, the carrier 3 separated from the wastewater 2
Therefore, the slit-shaped long holes 34 are not blocked and clogged, and the carrier 3 is continuously and appropriately separated at the drainage passage portion 33.
【0035】一方、スクリーン31の本体部32の内部空間
43に入り込まなかった処理中の排水2は、本体部32の案
内面35の案内作用により下降流Aが変換されて発生した
傾斜流Bによって傾斜状の本体部32に沿って流動してか
ら、水平状の底板部8の案内作用により傾斜流Bが変換
されて発生した水平流Cによって底板部8に沿って水平
流動する。On the other hand, the internal space of the main body 32 of the screen 31
The wastewater 2 during treatment that has not entered 43 flows along the inclined main body 32 by the inclined flow B generated by converting the downward flow A by the guiding action of the guide surface 35 of the main body 32, The inclined flow B is converted by the guiding action of the horizontal bottom plate 8 and horizontally flows along the bottom plate 8 by the horizontal flow C generated.
【0036】その後、この排水2は、垂直状の側板部9
の案内作用により水平流Cが変換されて筒状体13の周囲
に発生した上昇流Dによって側板部9および筒状体13に
沿って上方流動してから、水面近くで発生した水平流E
によって筒状体13内に上面開口部11を通って流入する。Thereafter, the drainage 2 is discharged from the vertical side plate portion 9
The horizontal flow C is converted by the guiding action of the above and the upward flow D generated around the cylindrical body 13 causes the upward flow to flow upward along the side plate portion 9 and the cylindrical body 13, and then the horizontal flow E generated near the water surface.
Flows into the cylindrical body 13 through the upper surface opening 11.
【0037】このように、反応槽5内全体には、筒状体
13内の下降流Aを一部とする旋回循環流、すなわち、下
降流A、傾斜流B、水平流C、上昇流Dおよび水平流E
からなる旋回循環流が発生し、この反応槽5内全体の旋
回循環流により排水2と担体3とが反応槽5内全体で撹
拌されながら循環流動する。このため、排水2の汚濁物
質と担体3の微生物(例えば脱窒菌等の嫌気性微生物)
とが効率よく接触し、この微生物の生物反応により主と
して硝酸性窒素が無害の気体である窒素ガスに変換さ
れ、排水2の浄化処理が効率的に行われる。In this way, the entire reaction vessel 5 has a cylindrical body.
A swirling circulation flow having a downward flow A in 13 as a part, that is, a downward flow A, an inclined flow B, a horizontal flow C, an upward flow D and a horizontal flow E.
A swirl circulation flow consisting of is generated, and by this swirl circulation flow in the entire reaction tank 5, the wastewater 2 and the carrier 3 are circulated while being stirred in the entire reaction tank 5. Therefore, the pollutants of the wastewater 2 and the microorganisms of the carrier 3 (for example, anaerobic microorganisms such as denitrifying bacteria)
And are efficiently brought into contact with each other, and mainly by the biological reaction of the microorganisms, nitrate nitrogen is converted into nitrogen gas, which is a harmless gas, and the wastewater 2 is efficiently purified.
【0038】そして、上記一実施の形態の水処理装置1
によれば、下降流Aによって筒状体13内から下面開口部
12を通って流出してきた排水2中から担体3を分離除去
するとともに下降流Aを傾斜流Bに変換するスクリーン
31を、筒状体13の下方位置に配置したため、筒状体13内
の下降流Aを通る旋回循環流を反応槽5内全体に適切に
発生させることができ、よって、反応槽5内全体を確実
に撹拌でき、浄化処理効率を十分に高めることができ
る。Then, the water treatment apparatus 1 of the above-mentioned one embodiment
According to the downflow A, the lower surface opening from the inside of the cylindrical body 13
A screen that separates and removes the carrier 3 from the wastewater 2 that has flowed through 12 and converts the downward flow A into a tilted flow B.
Since 31 is arranged at the lower position of the tubular body 13, a swirl circulation flow passing through the downward flow A in the tubular body 13 can be appropriately generated in the entire reaction vessel 5, and thus the entire reaction vessel 5 can be produced. Can be reliably stirred, and the purification treatment efficiency can be sufficiently enhanced.
【0039】また、排水2から分離された担体3を傾斜
流Bで洗い流すことができるので、捕捉された担体3で
各長孔34が閉塞されて詰まるようなことがなく、処理水
である排水2をスクリーン31を介して流出管41から反応
槽5外に適切に流出でき、効率的な浄化処理を適切に維
持できる。Further, since the carrier 3 separated from the waste water 2 can be washed away by the inclined flow B, the long holes 34 are not clogged and blocked by the captured carrier 3, and the waste water is treated water. 2 can be appropriately flown out of the reaction tank 5 from the outflow pipe 41 through the screen 31, and an efficient purification treatment can be appropriately maintained.
【0040】さらに、スクリーン31の排水通過部33を傾
斜流Bの方向に長手方向を有するスリット状の複数の長
孔34にて構成したので、例えば排水2中に混入した毛髪
等の繊維状物が絡みつくようなことを防止でき、排水通
過部33の開口状態を確実に維持できる。Further, since the drainage passage portion 33 of the screen 31 is constituted by a plurality of slit-shaped elongated holes 34 having a longitudinal direction in the direction of the inclined flow B, for example, a fibrous material such as hair mixed in the drainage 2 Can be prevented from being entangled with each other, and the open state of the drainage passage portion 33 can be reliably maintained.
【0041】なお、上記実施の形態では、スクリーン31
の本体部32は、頂点を上にして上端から下端に向って徐
々に拡径した円錐状に形成した構成について説明した
が、例えば、図3に示すように頂点を上にして上端から
下端に向って徐々に拡がったつまり拡幅した3角錐状の
本体部32aにしたり、図示しないが上端から下端に向っ
て徐々に拡がった4角錐状、5角錐状、6角錐状等の多
角状の本体部にしたり、上端を切り欠いた截頭円錐状、
截頭角錐状等の本体部としても、円錐状の本体部32と略
同様の作用効果を奏することができる。In the above embodiment, the screen 31
The main body portion 32 has been described as having a conical shape in which the vertex is upward and the diameter is gradually increased from the upper end to the lower end. However, for example, as shown in FIG. The main body 32a has a three-sided pyramid shape that gradually widens toward the side, or widens, or a polygonal main body such as a four-sided pyramid, a five-sided pyramid, and a six-sided pyramid that gradually expands from the upper end to the lower end (not shown). Or a truncated cone shape with the upper end cut out,
Even if the main body has a truncated pyramid shape, it is possible to obtain substantially the same operational effects as the conical main body 32.
【0042】また、上記いずれの実施の形態において
も、反応槽5は脱窒槽等の嫌気性反応槽であると説明し
たが、例えば、反応槽5は硝化槽等の好気性反応槽でも
よく、この場合には固定化微生物として硝化菌等の好気
性微生物を用いる。また、図示しないが、反応槽5を好
気性反応槽とする場合には、酸素を含有する気体(例え
ば空気等)を筒状体13内に供給する曝気手段を設けるこ
とが好ましい。In each of the above embodiments, the reaction tank 5 is described as an anaerobic reaction tank such as a denitrification tank. However, for example, the reaction tank 5 may be an aerobic reaction tank such as a nitrification tank, In this case, an aerobic microorganism such as nitrifying bacteria is used as the immobilized microorganism. Although not shown, when the reaction tank 5 is an aerobic reaction tank, it is preferable to provide an aeration means for supplying a gas containing oxygen (eg, air) into the cylindrical body 13.
【0043】この曝気手段は、例えば、ブロワ等の送風
機の作動で供給管の先端側から気体を筒状体13内の所定
位置、例えば回転羽根24の下方近傍位置に噴出供給する
構成とする。そして、この曝気手段により供給された気
体の気泡は、回転羽根24の回転で下降流Aとともに筒状
体13内に発生する略水平の旋回流によって裁断され、気
泡単位容積当たりの表面積が増大し、酸素の溶解効率が
高まる。また、曝気手段による気泡と回転羽根24とが直
接接触しないので、回転羽根24近傍に気泡が滞留・蓄積
するようなことがなく、反応槽5内全体にわたり安定し
た旋回循環流が発生する。さらに、反応槽5内の比較的
深い位置で気液接触が行われるので、その水圧により酸
素の溶解効率が高まる。また一方、曝気手段により筒状
体13内に供給された空気等の気泡が流出管41内に流入し
ても排水2の流れが悪くならないように、気泡を除去可
能なチャンバー等の気泡除去手段を流出管41等の排水流
出手段の途中に設けてもよい。The aeration means is constructed such that gas is jetted from the tip side of the supply pipe to a predetermined position in the cylindrical body 13, for example, a position in the vicinity of the lower part of the rotary vane 24, by the operation of a blower such as a blower. The gas bubbles supplied by the aeration means are cut by the substantially horizontal swirling flow generated in the cylindrical body 13 together with the downward flow A by the rotation of the rotary blades 24, and the surface area per bubble volume increases. , The dissolution efficiency of oxygen is increased. Further, since the bubbles generated by the aeration means do not come into direct contact with the rotary blades 24, the bubbles do not stay and accumulate near the rotary blades 24, and a stable swirling circulation flow is generated throughout the reaction tank 5. Furthermore, since gas-liquid contact is performed at a relatively deep position in the reaction tank 5, the water pressure increases the dissolution efficiency of oxygen. On the other hand, a bubble removing means such as a chamber capable of removing bubbles so that the flow of the drainage 2 does not deteriorate even if bubbles such as air supplied into the tubular body 13 by the aeration means flow into the outflow pipe 41. May be provided in the middle of the drainage outflow means such as the outflow pipe 41.
【0044】さらに、下降流発生手段21は、インペラ等
の回転羽根24を用いることなく、例えば筒状体13内への
気体の吹き込みにより筒状体13内に下降流を生じさせる
ようにしてもよい。Further, the descending flow generating means 21 may generate a descending flow in the tubular body 13 by blowing gas into the tubular body 13 without using the rotary vanes 24 such as an impeller. Good.
【0045】また、スクリーン31の排水通過部33は、複
数の長孔34にて構成したものには限定されず、例えば、
図示しない棒状の鋼材を格子状に組んで構成したもので
もよい。Further, the drainage passage portion 33 of the screen 31 is not limited to the one constituted by a plurality of elongated holes 34.
It may be configured by assembling rod-shaped steel materials (not shown) in a grid pattern.
【0046】さらに、担体3を分離して担体3が反応槽
5外に流出することを防ぐスクリーン31等の担体分離手
段は、排水通過部33を所定形状をなす本体部32,32aの
上部略全周にわたって配置して本体部32,32aの略全周
から排水2を処理水として取り出す構成には限定され
ず、例えば本体部32,32aの周方向一部から部分的に排
水2を取り出す構成としてもよい。Further, the carrier separating means such as the screen 31 for separating the carrier 3 and preventing the carrier 3 from flowing out of the reaction tank 5 is the upper portion of the main body 32, 32a having the drainage passage 33 of a predetermined shape. It is not limited to the configuration in which the wastewater 2 is taken out as the treated water from substantially the entire circumference of the main body portions 32, 32a by being arranged over the entire circumference, and for example, the construction in which the wastewater 2 is partially taken out from a part of the main body portions 32, 32a in the circumferential direction. May be
【0047】また、排水流出手段の途中に設けるチャン
バー等の気泡除去手段で捕集した気体(すなわち例えば
嫌気性反応槽の場合は主として窒素ガス、好気性反応槽
の場合は主として空気)を大気中に放出する構成として
もよく、或いは、図示しない返送管でその気体を筒状体
13内に返送する構成としてもよい。Further, the gas collected by the bubble removing means such as a chamber provided in the middle of the drainage outflow means (that is, mainly nitrogen gas in the case of an anaerobic reaction tank, mainly air in the case of an aerobic reaction tank) is exposed to the atmosphere. Alternatively, the gas may be discharged to a cylindrical body or a return pipe (not shown)
It may be configured to return it to the inside of 13.
【0048】また、気泡除去手段で捕集した気体を大気
に放出せずに図示しない回収手段で回収して気体の有効
利用を図ることも可能である。Further, the gas collected by the bubble removing means may be recovered by the recovering means (not shown) without being released to the atmosphere to effectively utilize the gas.
【0049】さらに、担体3を分離除去した浄化処理後
の排水2を反応槽5外に流出させる流出管41は必ずしも
必要ではなく、例えば汲み取り手段等の排水取出手段で
処理後の排水2を取り出すようにしてもよい。Further, the outflow pipe 41 for outflowing the wastewater 2 after the purification treatment in which the carrier 3 is separated and removed to the outside of the reaction tank 5 is not necessarily required, and the wastewater 2 after treatment is taken out by a wastewater extraction means such as a pumping means. You may do it.
【0050】また、スクリーン31等の担体分離手段は、
下降流Aを上下方向に対して傾斜した方向の曲線状の傾
斜流に変換するものでもよい。例えば円錐状の本体部
は、直線状の傾斜面を有する形状すなわち側面からみた
場合に直線の斜辺を有する三角形をなす形状には限定さ
れず、例えば、曲線状の傾斜面(凹状または凸状に湾曲
した傾斜面)を有する形状すなわち側面からみた場合に
曲線の斜辺を有する三角形をなす形状でもよい。同様
に、角錐状の本体部は、平面状の傾斜面を有する形状に
は限定されず、例えば、凹状または凸状に湾曲した曲面
状の傾斜面を有する形状でもよい。The carrier separating means such as the screen 31 is
The downward flow A may be converted into a curved inclined flow that is inclined with respect to the vertical direction. For example, the conical body is not limited to a shape having a linear inclined surface, that is, a triangular shape having a straight hypotenuse when viewed from the side, and for example, a curved inclined surface (concave or convex). A shape having a curved inclined surface), that is, a triangular shape having a hypotenuse of a curved line when viewed from the side may be used. Similarly, the pyramidal main body is not limited to a shape having a flat inclined surface, and may have, for example, a shape having a curved inclined surface curved concavely or convexly.
【0051】[0051]
【発明の効果】請求項1記載の発明によれば、下降流発
生手段による下降流によって筒状体内から下面開口部を
通って流出する排水から担体を分離除去するとともに下
降流発生手段による下降流を上下方向に対して傾斜した
方向の傾斜流に変換する担体分離手段を筒状体の下方位
置に配置したため、筒状体内の下降流を一部とする旋回
循環流を反応槽内に適切に発生させることができ、浄化
処理効率を十分に高めることができる。According to the first aspect of the present invention, the carrier is separated and removed from the wastewater flowing out of the cylindrical body through the lower surface opening by the downflow generated by the downflow generating means, and the downflow generated by the downflow generating means. Since the carrier separating means for converting the above into an inclined flow in the direction inclined with respect to the vertical direction is arranged at the lower position of the tubular body, the swirling circulation flow, which is a part of the downward flow in the tubular body, can be properly provided in the reaction tank. It can be generated and the purification treatment efficiency can be sufficiently enhanced.
【0052】請求項2記載の発明によれば、円錐状の本
体部およびこの本体部に開口形成した排水通過部を有す
る担体分離手段により、簡単な構成であるにも拘わら
ず、筒状体内の下降流を一部とする旋回循環流を反応槽
内に適切に発生させることができ、浄化処理効率を十分
に高めることができる。According to the second aspect of the present invention, the carrier separating means having the conical main body portion and the drainage passage portion formed in the main body portion has a simple structure, but has a simple structure. A swirling circulation flow having a downward flow as a part can be appropriately generated in the reaction tank, and the purification treatment efficiency can be sufficiently enhanced.
【0053】請求項3記載の発明によれば、角錐状の本
体部およびこの本体部に開口形成した排水通過部を有す
る担体分離手段により、簡単な構成であるにも拘わら
ず、筒状体内の下降流を一部とする旋回循環流を反応槽
内に適切に発生させることができ、浄化処理効率を十分
に高めることができる。According to the third aspect of the present invention, the carrier separating means having the pyramidal main body and the drainage passage formed in the main body has a simple structure, but has a simple structure. A swirling circulation flow having a downward flow as a part can be appropriately generated in the reaction tank, and the purification treatment efficiency can be sufficiently enhanced.
【0054】請求項4記載の発明によれば、排水通過部
を傾斜流の方向に長手方向を有する複数の長孔にて構成
したので、例えば排水中に混入した繊維状物等の絡みを
防止できる。According to the fourth aspect of the invention, since the drainage passage is composed of a plurality of elongated holes having a longitudinal direction in the direction of the inclined flow, for example, the entanglement of fibrous substances mixed in the drainage is prevented. it can.
【0055】請求項5記載の発明によれば、複数の回転
羽根を筒状体内で駆動回転させることにより、筒状体内
に下降流を確実に発生させることができる。According to the fifth aspect of the present invention, by drivingly rotating the plurality of rotary blades in the cylindrical body, it is possible to reliably generate the downward flow in the cylindrical body.
【図1】本発明の水処理装置の一実施の形態を示す断面
図である。FIG. 1 is a sectional view showing an embodiment of a water treatment device of the present invention.
【図2】同上水処理装置のスクリーンを示す斜視図であ
る。FIG. 2 is a perspective view showing a screen of the same water treatment device.
【図3】同上スクリーンの他の実施の形態を示す斜視図
である。FIG. 3 is a perspective view showing another embodiment of the above screen.
1 水処理装置 2 排水 3 担体 5 反応槽 11 上面開口部 12 下面開口部 13 筒状体 21 下降流発生手段 24 回転羽根 31 担体分離手段であるスクリーン 32,32a 本体部 33 排水通過部 34 長孔 A 下降流 B 傾斜流 1 Water treatment device 2 drainage 3 carriers 5 reaction tanks 11 Top opening 12 Bottom opening 13 tubular 21 Downflow generator 24 rotating blades 31 Screen as carrier separating means 32, 32a body 33 Drainage passage 34 long hole A downflow B inclined flow
Claims (5)
化処理する水処理装置であって、 微生物を保持した担体を含んだ排水を貯留する反応槽
と、 この反応槽内に軸方向が上下方向に一致するように配置
され、上面開口部および下面開口部を有する上下面開口
状の筒状体と、 この筒状体内に下降流を発生させる下降流発生手段と、 前記筒状体の下方位置に配置され、前記下降流発生手段
による下降流によって前記筒状体内から前記下面開口部
を通って流出する排水から担体を分離除去するととも
に、前記下降流発生手段による下降流を上下方向に対し
て傾斜した方向の傾斜流に変換する担体分離手段とを備
えたことを特徴とする水処理装置。1. A water treatment device for purifying wastewater using a carrier holding microorganisms, comprising: a reaction tank for storing wastewater containing a carrier holding microorganisms; and an axial direction up and down in the reaction tank. A cylindrical body having upper and lower openings, which are arranged so as to coincide with each other in direction, and which has an upper surface opening portion and a lower surface opening portion; downflow generating means for generating a downward flow in the cylindrical body; The carrier is separated and removed from the drainage flowing out of the tubular body through the lower surface opening by the downflow generated by the downflow generating means, and the downflow generated by the downflow generating means is vertically moved. And a carrier separating means for converting to a tilted flow in a tilted direction.
拡径した円錐状の本体部と、 この本体部に開口形成され、担体の通過を禁止すること
で排水から担体を分離除去し、この担体が分離除去され
た排水を通過させる排水通過部とを有することを特徴と
する請求項1記載の水処理装置。2. The carrier separating means is located concentrically with the cylindrical body, and has a conical main body whose diameter gradually increases from the upper end to the lower end, and an opening is formed in this main body to allow passage of the carrier. The water treatment apparatus according to claim 1, further comprising: a wastewater passage portion that separates and removes the carrier from the wastewater by prohibiting, and allows the wastewater that has been separated and removed from the carrier to pass through.
拡がった角錐状の本体部と、 この本体部に開口形成され、担体の通過を禁止すること
で排水から担体を分離除去し、この担体が分離除去され
た排水を通過させる排水通過部とを有することを特徴と
する請求項1記載の水処理装置。3. The carrier separating means is located on the same axis as the tubular body, and has a pyramidal main body that gradually expands from the upper end to the lower end, and an opening is formed in the main body to prevent the carrier from passing therethrough. The water treatment device according to claim 1, further comprising: a drainage passage portion that separates and removes the carrier from the wastewater, and allows the wastewater that has been separated and removed from the carrier to pass through.
を有する複数の長孔にて構成されていることを特徴とす
る請求項2または3記載の水処理装置。4. The water treatment device according to claim 2, wherein the drainage passage is composed of a plurality of elongated holes having a longitudinal direction in the direction of the inclined flow.
してこの筒状体内に下降流を発生させる複数の回転羽根
を有することを特徴とする請求項1ないし4のいずれか
に記載の水処理装置。5. The descending flow generating means has a plurality of rotating blades that are driven and rotated in the cylindrical body to generate a descending flow in the cylindrical body. Water treatment equipment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001273203A JP2003080285A (en) | 2001-09-10 | 2001-09-10 | Water treatment equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001273203A JP2003080285A (en) | 2001-09-10 | 2001-09-10 | Water treatment equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2003080285A true JP2003080285A (en) | 2003-03-18 |
Family
ID=19098449
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2001273203A Pending JP2003080285A (en) | 2001-09-10 | 2001-09-10 | Water treatment equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2003080285A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013505819A (en) * | 2009-09-25 | 2013-02-21 | インヴェント ウムヴェルト ウント フェアファーレンシュテッヒニク アーゲー | Biological purification method and biological purification apparatus for sewage |
WO2015129707A1 (en) * | 2014-02-25 | 2015-09-03 | 株式会社 東芝 | Anaerobic water-treatment system |
CN113045013A (en) * | 2021-03-18 | 2021-06-29 | 东莞市科绿智能环保科技有限公司 | Solid-liquid separation system and separation method for lithium battery anode cleaning wastewater |
-
2001
- 2001-09-10 JP JP2001273203A patent/JP2003080285A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013505819A (en) * | 2009-09-25 | 2013-02-21 | インヴェント ウムヴェルト ウント フェアファーレンシュテッヒニク アーゲー | Biological purification method and biological purification apparatus for sewage |
WO2015129707A1 (en) * | 2014-02-25 | 2015-09-03 | 株式会社 東芝 | Anaerobic water-treatment system |
JP2015157271A (en) * | 2014-02-25 | 2015-09-03 | 株式会社東芝 | anaerobic water treatment system |
CN113045013A (en) * | 2021-03-18 | 2021-06-29 | 东莞市科绿智能环保科技有限公司 | Solid-liquid separation system and separation method for lithium battery anode cleaning wastewater |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US6032931A (en) | Apparatus for selective aeration | |
CA1050178A (en) | Method and device for oxidizing and purifying water | |
JP3397154B2 (en) | Revolving microbubble generator | |
US4210613A (en) | Water treating device | |
US20090272688A1 (en) | Bioreactor and Method for the Biological Purification of Water | |
KR100352166B1 (en) | Process and plant for the efficiency solubility of gas and sludge mixing | |
JP4318875B2 (en) | Water treatment equipment | |
JP4204020B2 (en) | Stirring aeration device | |
JP2007144401A (en) | Biological reactor | |
JP2003080285A (en) | Water treatment equipment | |
JP4318870B2 (en) | Water treatment equipment | |
JP2005218955A (en) | Gas/liquid contactor | |
JP4374885B2 (en) | Membrane separator | |
US10683221B2 (en) | Gas injection and recycling apparatus and methods | |
KR100301521B1 (en) | A removing device for sludge using foam | |
JP2007209908A (en) | Microbubble generator | |
JPS59206096A (en) | Aerating apparatus | |
JP2002035784A (en) | Agitation and aeration apparatus | |
JP2000512545A (en) | Reaction tank for purification of polluted wastewater | |
JP2008212930A (en) | Membrane separator | |
JPH05146796A (en) | Device for purifying closed natural water area | |
KR102450808B1 (en) | Bubble generator in water tank for air pollution prevention apparatus | |
JPH06335699A (en) | Device for purifying closed water basin | |
CN220550084U (en) | Anoxic tank after denitrification | |
JPH02102792A (en) | Waste water treatment apparatus |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20070111 |
|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20090318 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20090325 |
|
A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 20090715 |