JPH1043784A - Fluid bed type biological treating device - Google Patents

Fluid bed type biological treating device

Info

Publication number
JPH1043784A
JPH1043784A JP8200646A JP20064696A JPH1043784A JP H1043784 A JPH1043784 A JP H1043784A JP 8200646 A JP8200646 A JP 8200646A JP 20064696 A JP20064696 A JP 20064696A JP H1043784 A JPH1043784 A JP H1043784A
Authority
JP
Japan
Prior art keywords
flow area
area
descending
ascending
partition plate
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
JP8200646A
Other languages
Japanese (ja)
Other versions
JP2944522B2 (en
Inventor
Shigekazu Oginoya
茂和 萩野谷
Nobuyuki Machida
信幸 町田
Masako Kimura
真子 木村
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.)
NEC Ameniplantex Ltd
Original Assignee
NEC Ameniplantex 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 NEC Ameniplantex Ltd filed Critical NEC Ameniplantex Ltd
Priority to JP8200646A priority Critical patent/JP2944522B2/en
Publication of JPH1043784A publication Critical patent/JPH1043784A/en
Application granted granted Critical
Publication of JP2944522B2 publication Critical patent/JP2944522B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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 improve the flow property of carriers and to increase an effective capacity to an installation area by providing the top of the one half surface in the bottom of a treating vessel which is a rectangular parallelepiped with an air diffuser forming an ascending flow area and providing the lower part of the descending flow area on the other half surface of the bottom with an inclined bottom wall. SOLUTION: The ascending flow area A side of the treating vessel 1 is provided with an introducing pipe 2 and the air diffuser 3 is installed to the bottom 1c. An underwater partition plate 4 is installed in the central part of the treating vessel 1 by inclining this plate to the ascending flow area A side. The lower part of the descending flow area B side of the treating vessel 1 is provided with the inclined bottom wall 5 rising to a drain side lateral wall 1b. Further, the upper part of the descending flow area B side is provided with an outflow preventive plate 8 having a perpendicular part 6a which falls to the drain side lateral wall 1b side and curves perpendicularly. When the underwater partition plate 4 is inclined to the ascending flow area A side in such a manner, the sectional area is gradually narrowed in the lower part of the descending flow area B and, therefore, the swirling flow velocity is slow in the upper part and fast in the lower part. Consequently, the flow property of the carriers in the lower part of the descending flow area B is improved.

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、有機性排水の処理
に用いられる流動床式処理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 a fluidized bed treatment apparatus used for treating organic wastewater.

【0002】[0002]

【従来の技術】従来、有機性排水の処理に用いられる流
動床式生物処理装置(以下処理装置という)の処理槽と
しては、担体の流出防止と流動性向上のために、図2
(実公平6−34880号公報)に示すように、処理槽
1Aの下降流動域Bに流出防止板6Aと整流板8を設
け、さらに、担体を上昇流動域Aに案内するための、散
気装置3の近傍までテーパー状に切れ込んだ傾斜面の長
い傾斜底壁5Aを形成したものがあった。
2. Description of the Related Art Conventionally, a treatment tank of a fluidized-bed biological treatment apparatus (hereinafter referred to as a treatment apparatus) used for treating organic wastewater has a structure shown in FIG.
As shown in Jpn. Pat. Appln. KOKAI Publication No. 6-34880, an outflow prevention plate 6A and a rectifying plate 8 are provided in a descending flow area B of a processing tank 1A. In some cases, a long inclined bottom wall 5A having a long inclined surface formed in a tapered shape near the device 3 was formed.

【0003】上記処理装置においては、導入管2から導
入された被処理水は、散気装置3からの気泡と共に水中
仕切板4Aを介して上昇流動域A及び下降流動域Bを担
体(図示せず)を伴って循環流動する。沈降域Cでは、
殆んどの担体は下降し下降流動域Bの下降流に案内され
て再び上昇流動域A内に導入される。
In the above treatment apparatus, the water to be treated introduced from the introduction pipe 2 together with the air bubbles from the air diffuser 3 travels through the underwater partition plate 4A to the ascending flow area A and the descending flow area B as carriers (not shown). Circulating). In subsidence area C,
Most of the carrier descends and is guided by the descending flow of the descending flow zone B, and is again introduced into the ascending flow zone A.

【0004】[0004]

【発明が解決しようとする課題】上述した従来の流動床
式処理装置には、次のような欠点があった。
The above-mentioned conventional fluidized bed processing apparatus has the following drawbacks.

【0005】第1に担体を案内するために散気装置3の
近傍まで切れ込んだテーパー状の傾斜底壁5Aが必要で
あり、処理槽の設置面積に対する有効容量が少ない。
First, a tapered inclined bottom wall 5A cut to the vicinity of the air diffuser 3 is required to guide the carrier, and the effective capacity for the installation area of the processing tank is small.

【0006】第2に傾斜底壁5Aが深く傾斜面が長い
為、傾斜底壁上方に担体が滞留する可能性があるので、
担体の巻き上げに備えて整流板8が必要になり、その結
果、処理槽中の沈降域面積が大きくなるため、処理槽の
設置面積に対する有効容量が少ない。
Second, since the inclined bottom wall 5A is deep and the inclined surface is long, the carrier may stay above the inclined bottom wall.
The current plate 8 is required in preparation for winding up the carrier, and as a result, the area of the sedimentation area in the processing tank increases, so that the effective capacity with respect to the installation area of the processing tank is small.

【0007】本発明の目的は、担体の流動性を向上さ
せ、傾斜底壁を小型化し、設置面積に対する有効容量を
大きくすると共に、沈降域の面積を小さくすることを同
時に達成できる流動床式生物処理装置を提供することに
ある。
It is an object of the present invention to improve the fluidity of a carrier, reduce the size of an inclined bottom wall, increase the effective capacity with respect to the installation area, and simultaneously reduce the area of a sedimentation zone. An object of the present invention is to provide a processing device.

【0008】[0008]

【課題を解決するための手段】本発明の流動床式生物処
理装置は、矩形の底部を有する直方体の処理槽と、前記
底部の一方の半面上に設けられ上昇流動域を形成する散
気装置と、前記底部の他方の半面上の下降流動域の下部
に設けられた傾斜底壁と、前記処理槽の中央部に設けら
れ前記上昇流動域側に傾けられた水中仕切板と、前記下
降流動域の上部に設けられた流出防止板とを含むことを
特徴とするものである。
SUMMARY OF THE INVENTION A fluidized bed biological treatment apparatus according to the present invention comprises a rectangular parallelepiped treatment tank having a rectangular bottom, and an air diffuser provided on one half of the bottom to form an ascending flow area. An inclined bottom wall provided at a lower part of a descending flow area on the other half surface of the bottom, an underwater partition plate provided at a central portion of the treatment tank and inclined toward the ascending flow area, And an outflow prevention plate provided at an upper part of the region.

【0009】[0009]

【作用】本発明の作用について図1に基づいて説明す
る。被処理水である排水は、導入管2より処理槽1に流
入し、曝気によるエアリフト効果により生ずる上昇流動
域Aを通り、曝気の行われない下降流動域Bを下降し、
処理槽1内を旋回し、担体と接触しつつ浄化され排水管
7より排出される。
The operation of the present invention will be described with reference to FIG. Drainage, which is water to be treated, flows into the treatment tank 1 from the introduction pipe 2, passes through the ascending flow area A caused by the air lift effect by aeration, and descends in the descending flow area B in which aeration is not performed.
It turns inside the processing tank 1 and is purified while being in contact with the carrier, and is discharged from the drain pipe 7.

【0010】処理槽1の中央の水中仕切板4を上昇流動
域A側に傾けることにより、下降流動域Bの下部では、
その断面積が徐々に狭くなるために、旋回流速が上部で
は遅く下部では速くなる。その結果、下降流動域Bの下
部での担体の流動性は向上し、担体を再び上昇流動域A
に案内する傾斜底壁5を小型化できる。
By tilting the underwater partition plate 4 at the center of the treatment tank 1 toward the upward flow area A, the lower part of the downward flow area B
Since the cross-sectional area is gradually narrowed, the swirling flow velocity is slower in the upper part and faster in the lower part. As a result, the fluidity of the carrier in the lower part of the descending flow zone B is improved, and the carrier is returned to the upward flow zone A.
Can be made smaller.

【0011】この作用により、処理槽1の設置面積に対
する有効容量が大きくなると共に、流出防止板6の垂直
部6aでの担体の巻き上げがなくなり、従来用いられて
いた整流板8は必要なくなる。
By this operation, the effective capacity with respect to the installation area of the processing tank 1 is increased, and the carrier is not wound up at the vertical portion 6a of the outflow prevention plate 6, so that the rectifying plate 8 conventionally used becomes unnecessary.

【0012】[0012]

【発明の実施の形態】次に本発明について図面を用いて
説明する。図1は本発明の一実施の形態を説明する為の
処理装置の断面図である。
Next, the present invention will be described with reference to the drawings. FIG. 1 is a sectional view of a processing apparatus for explaining an embodiment of the present invention.

【0013】図1において処理槽1は、正方形の底部1
cの長辺と有効水深の比が1:2以上である直方体から
構成されている。処理槽1の底部1cは正方形でなくて
もよいが、正方形にした場合が設置面積あたりの有効容
量を最も大きくとれるので望ましい。
In FIG. 1, a processing tank 1 has a square bottom 1.
It is composed of a rectangular parallelepiped having a ratio of the long side of c to the effective water depth of 1: 2 or more. The bottom 1c of the processing tank 1 does not have to be a square, but it is preferable to make the bottom 1c since the effective capacity per installation area can be maximized.

【0014】処理槽1の上昇流動域A側に導入管2を設
け、底部1cには散気装置3を導入側側壁1aから約1
/2(半面)のところまで設置する。散気装置3の設置
場所は中央仕切板4の角度によって、導入側側壁1aか
ら1/2以下でも1/2以上でもよいが、曝気停止後担
体、(図示せず)を再び流動させる際、導入側側壁1a
から約1/2のところまで散気装置を設置した状態が最
も速やかに流動を開始する。
An inlet pipe 2 is provided on the ascending flow area A side of the processing tank 1, and an air diffuser 3 is provided on the bottom 1c about 1 mm from the inlet side wall 1a.
/ 2 (half side). Depending on the angle of the central partition plate 4, the location of the diffuser 3 may be 以下 or less or 以上 or more from the introduction side wall 1a, but when the aeration is stopped, the carrier (not shown) flows again. Introducing side wall 1a
The flow starts most quickly when the air diffuser is installed up to about 1/2 of the distance.

【0015】処理槽1の中央部には、上下の隙間が有効
水深の約1/6ずつとなるように、上昇流動域A側に1
5〜25°傾けて水中仕切板4を設置する。水中仕切板
の傾斜角は15°以下でも25°以上でもよいが、15
〜25°に傾けた状態が速やかに排水が流動する。
In the central part of the treatment tank 1, the upper and lower gaps are placed one by one on the ascending flow zone A side so that the upper and lower gaps are each about 1/6 of the effective water depth.
The underwater partition plate 4 is installed at an angle of 5 to 25 °. The angle of inclination of the underwater partition may be 15 ° or less or 25 ° or more.
The wastewater flows quickly when inclined at an angle of about 25 °.

【0016】処理槽1の下降流動域B側下部には、底部
1cの1辺の長さの1/3のところから約45°で排水
側側壁1bに立ち上がる傾斜底壁5を設ける。そして下
降流動域B側上部には、排水側側壁1bから底部1cの
1辺の長さの1/3のところから45°で排水側側壁1
bに落ち込み、排水側側壁1bから底部1c1辺の長さ
の3/20あるいは、底部1cの1辺の長さの3/20
が0.5mを越える場合には、0.5m前後のところで
垂直に屈曲する垂直部6aを有する流出防止板6を設け
る。
An inclined bottom wall 5 is provided at the lower portion of the downward flow zone B of the treatment tank 1 at about 45 ° from one-third of the length of one side of the bottom 1c to rise to the drain side wall 1b. On the upper part of the descending flow area B side, the drain side wall 1 is set at 45 ° from one third of the length of one side of the bottom part 1c from the drain side wall 1b.
b, 3/20 of the length of one side of the bottom 1c from the drain side wall 1b, or 3/20 of the length of one side of the bottom 1c.
Is larger than 0.5 m, an outflow prevention plate 6 having a vertical portion 6a that is bent vertically at about 0.5 m is provided.

【0017】前述の中央仕切板4の上下の隙間、その角
度、また、傾斜底壁5の立ち上がり位置、角度の数値
は、担体が最も良好に流動する数値であり、担体の添加
量に応じて、その数値以上でも以下でもよい。
The above and below gaps and angles of the central partition plate 4, and the rising position and angle of the inclined bottom wall 5 are numerical values at which the carrier flows best, and depend on the amount of carrier added. , May be greater than or less than the numerical value.

【0018】流出防止板6の垂直部6aの長さは有効水
深の1/10〜1/5とするが、この数値は担体が沈降
域に巻き込まれない範囲の数値であり、担体の添加量に
応じて、その数値以上でも以下でもかまわない。排水は
導入管2より処理槽1に流入し、処理槽1中の上昇流動
域Aと下降流動域Bを旋回する微生物の付着した担体と
接触しつつ処理され、配水管7より排出される。
The length of the vertical portion 6a of the outflow prevention plate 6 is set to 1/10 to 1/5 of the effective water depth. This value is a value within a range in which the carrier is not involved in the sedimentation area, May be greater or less than that value, depending on. The wastewater flows into the treatment tank 1 through the introduction pipe 2, is treated while being in contact with the microorganism-adhering carrier rotating in the ascending flow area A and the descending flow area B in the treatment tank 1, and is discharged from the water distribution pipe 7.

【0019】使用する担体は3〜5mm角の直方体ある
いは直径3〜5mmの球体で、含水時の比重は1〜1.
1のものが良く流動する。以下に、本発明の処理装置に
おける実験例を示す。
The carrier used is a rectangular parallelepiped having a size of 3 to 5 mm or a sphere having a diameter of 3 to 5 mm.
One flows well. Hereinafter, an experimental example of the processing apparatus of the present invention will be described.

【0020】容量40L、水中仕切板4の角度20°、
流出防止板6の垂直部6aの長さ8cmとした処理槽1
に被処理水を導入し処理を行った。その結果は表1のと
おりBOD濃度を6〜12%に減少させることができ、
十分な処理能力が得られた。
A capacity of 40 L, an angle of the underwater partition plate 4 of 20 °,
Processing tank 1 with vertical portion 6a of outflow prevention plate 6 having a length of 8 cm
To be treated was introduced. As a result, as shown in Table 1, the BOD concentration can be reduced to 6 to 12%,
Sufficient processing capacity was obtained.

【0021】[0021]

【0022】[0022]

【表1】 [Table 1]

【0023】[0023]

【発明の効果】以上説明したように本発明は、水中仕切
板4を上昇流動域A側に傾けることにより、整流板が不
必要となる為沈降域の容量を少なくできるとともに、傾
斜底壁5を小型化できる。その結果、処理槽の設置面積
に対する有効容量を大きくとれるという効果がある。
As described above, according to the present invention, by inclining the submerged partition plate 4 toward the upward flow area A, the capacity of the sedimentation area can be reduced because the straightening plate is unnecessary, and the inclined bottom wall 5 can be reduced. Can be reduced in size. As a result, there is an effect that the effective capacity with respect to the installation area of the processing tank can be increased.

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

【図1】本発明の実施の形態を説明する為の処理装置の
断面図である。
FIG. 1 is a cross-sectional view of a processing apparatus for describing an embodiment of the present invention.

【図2】従来の処理装置の断面図である。FIG. 2 is a sectional view of a conventional processing apparatus.

【符号の説明】[Explanation of symbols]

1,1A 処理槽 1a 導入側側壁 1b 排水側側壁 1c 底部 2 導入管 3 散気装置 4,4A 水中仕切板 5,5A 傾斜底壁 6,6A 流出防止板 6a 垂直部 7 配水管 8 整流板 A 上昇流動域 B 下降流動域 C 沈降域 1, 1A Treatment tank 1a Inlet side wall 1b Drain side wall 1c Bottom 2 Introductory pipe 3 Air diffuser 4, 4A Underwater partition plate 5, 5A Inclined bottom wall 6, 6A Outflow prevention plate 6a Vertical part 7 Water distribution pipe 8 Straightening plate A Upflow area B Downflow area C Settling area

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 矩形の底部を有する直方体の処理槽と、
前記底部の一方の半面上に設けられ上昇流動域を形成す
る散気装置と、前記底部の他方の半面上の下降流動域の
下部に設けられた傾斜底壁と、前記処理槽の中央部に設
けられ前記上昇流動域側に傾けられた水中仕切板と、前
記下降流動域の上部に設けられた流出防止板とを含むこ
とを特徴とする流動床式生物処理装置。
1. A rectangular parallelepiped processing tank having a rectangular bottom,
An air diffuser provided on one half of the bottom to form an ascending flow area, an inclined bottom wall provided below a descending flow area on the other half of the bottom, and a central part of the processing tank. A fluidized-bed biological treatment apparatus, comprising: an underwater partition plate provided to be inclined toward the ascending flow region; and an outflow prevention plate provided at an upper portion of the descending flow region.
【請求項2】 水中仕切板の傾斜角は15〜25°であ
る請求項1記載の流動床式生物処理装置。
2. The fluidized bed biological treatment apparatus according to claim 1, wherein the angle of inclination of the underwater partition plate is 15 to 25 °.
JP8200646A 1996-07-30 1996-07-30 Fluidized bed biological treatment equipment Expired - Fee Related JP2944522B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8200646A JP2944522B2 (en) 1996-07-30 1996-07-30 Fluidized bed biological treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8200646A JP2944522B2 (en) 1996-07-30 1996-07-30 Fluidized bed biological treatment equipment

Publications (2)

Publication Number Publication Date
JPH1043784A true JPH1043784A (en) 1998-02-17
JP2944522B2 JP2944522B2 (en) 1999-09-06

Family

ID=16427867

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8200646A Expired - Fee Related JP2944522B2 (en) 1996-07-30 1996-07-30 Fluidized bed biological treatment equipment

Country Status (1)

Country Link
JP (1) JP2944522B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003088355A (en) * 2001-09-13 2003-03-25 Sumitomo Chem Co Ltd Culture apparatus for aerobic microorganism and cultivation using the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003088355A (en) * 2001-09-13 2003-03-25 Sumitomo Chem Co Ltd Culture apparatus for aerobic microorganism and cultivation using the same

Also Published As

Publication number Publication date
JP2944522B2 (en) 1999-09-06

Similar Documents

Publication Publication Date Title
US4622147A (en) Plant for the anaerobic purification of waste water
JP3867481B2 (en) Immersion flat membrane separator
JPS6134877B2 (en)
US3236384A (en) Apparatus for flocculation and clarification of liquids
JPH1043784A (en) Fluid bed type biological treating device
JP4257024B2 (en) Nitrification carrier circulation method in deep tank aeration tank
JPS62298409A (en) Upward flow type inclined settling pond
JPH0634880Y2 (en) Fluid carrier biological treatment equipment
US2024345A (en) Sewage purifying device
JP4994349B2 (en) Nitrification carrier circulation method in deep tank aeration tank
US5332534A (en) Process and system for increasing the gas uptake by a liquid being aerated
JPH09150177A (en) Waste water treating device sing fluidized bed type deep layer type aerating tank
JPS6136475B2 (en)
JPH1076288A (en) Method and apparatus for treating microorganism utilization liquid
JP2002079283A (en) Aerobic treatment tank
JPS6321555B2 (en)
RU2812426C1 (en) Bioreactor for wastewater treatment
JPH01180297A (en) Fluidized type waste water treating device
JPH0131354Y2 (en)
JPH09225491A (en) Anaerobic treating device of organic waste water
JPH03245900A (en) Revolving flow type deep aeration tank and aeration method
SU1353750A1 (en) Device for cleaning waste water
JP2001113295A (en) Aerobic treatment tank
JP2001347259A (en) Floatation apparatus by pressure
JPS6135919B2 (en)

Legal Events

Date Code Title Description
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 19990608

LAPS Cancellation because of no payment of annual fees