JP2604958B2 - Nitrification and denitrification equipment by biofilm filtration - Google Patents

Nitrification and denitrification equipment by biofilm filtration

Info

Publication number
JP2604958B2
JP2604958B2 JP4378193A JP4378193A JP2604958B2 JP 2604958 B2 JP2604958 B2 JP 2604958B2 JP 4378193 A JP4378193 A JP 4378193A JP 4378193 A JP4378193 A JP 4378193A JP 2604958 B2 JP2604958 B2 JP 2604958B2
Authority
JP
Japan
Prior art keywords
nitrification
zone
denitrification
tank
biofilm filtration
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.)
Expired - Fee Related
Application number
JP4378193A
Other languages
Japanese (ja)
Other versions
JPH06254591A (en
Inventor
極 松原
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.)
NGK Insulators Ltd
Original Assignee
NGK Insulators 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 NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP4378193A priority Critical patent/JP2604958B2/en
Publication of JPH06254591A publication Critical patent/JPH06254591A/en
Application granted granted Critical
Publication of JP2604958B2 publication Critical patent/JP2604958B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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、コンパクトな装置で効
率よく廃水の硝化脱窒処理を行うことができる生物膜濾
過による硝化脱窒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 nitrification denitrification apparatus using biofilm filtration, which can efficiently perform a nitrification denitrification treatment of wastewater with a compact apparatus.

【0002】[0002]

【従来の技術】例えば、下水などのように有機性窒素や
アンモニア性窒素を含んだ廃水は生物膜ろ過による硝化
脱窒が行われて浄化処理されるのが一般的であり、この
種の硝化脱窒装置としては、図2に示されるような槽1
内に曝気用散気装置2を配して該曝気用散気装置2の上
部を硝化ゾーン3、下部を脱窒ゾーン4としたものが広
く使用されている(特公平4−50880号公報参
照)。
2. Description of the Related Art For example, wastewater containing organic nitrogen or ammonia nitrogen, such as sewage, is generally subjected to nitrification denitrification by biofilm filtration to be purified. As a denitrification device, a tank 1 as shown in FIG.
An aeration diffuser 2 is disposed therein, and the upper part of the aeration diffuser 2 is a nitrification zone 3 and a lower part is a denitrification zone 4 (see Japanese Patent Publication No. 4-50880). ).

【0003】ところが、このタイプの装置においては硝
化ゾーンと脱窒ゾーンとが一定領域に固定されているた
め、原水の水質によっては硝化は十分に行われるが脱窒
は不十分となる、あるいは逆に硝化は不十分であるが脱
窒は十分に行われる等、処理性が安定しないという問題
点があった。一方、前記処理性を安定させるためには各
ゾーンの容量を十分に大きくする必要があり、設備が過
大にならざるを得ないという問題点があった。
However, in this type of apparatus, since the nitrification zone and the denitrification zone are fixed in a certain area, nitrification is sufficiently performed but denitrification is insufficient depending on the quality of raw water, or vice versa. In addition, there is a problem that the processability is not stable, such as insufficient nitrification but sufficient denitrification. On the other hand, in order to stabilize the processability, it is necessary to make the capacity of each zone sufficiently large, and there is a problem that the equipment must be excessively large.

【0004】[0004]

【発明が解決しようとする課題】本発明は上記のような
従来の問題点を解決して、硝化ゾーンと脱窒ゾーンとの
比率を任意に変えることにより各ゾーンにおける原水の
滞留時間を水質にあわせて適正化することができ十分な
硝化脱窒を行うことができるとともに、処理槽の小型化
が図れて装置全体としてもコンパクトな設計にすること
ができる生物膜濾過による硝化脱窒装置を提供すること
を目的として完成されたものである。
SUMMARY OF THE INVENTION The present invention solves the above-mentioned conventional problems and reduces the residence time of raw water in each zone by changing the ratio between the nitrification zone and the denitrification zone. Provide a nitrification denitrification device by biofilm filtration that can be optimized and sufficient nitrification denitrification can be performed, and the processing tank can be downsized and the whole device can be designed to be compact. It was completed for the purpose of doing.

【0005】[0005]

【課題を解決するための手段】上記の課題を解決するた
めになされた本発明の生物膜濾過による硝化脱窒装置
は、槽内に曝気用散気装置を配して該曝気用散気装置の
上部を硝化ゾーン、下部を脱窒ゾーンとした生物膜ろ過
による硝化脱窒装置において、前記曝気用散気装置に槽
内の垂直方向に並んだ複数個の散気部材を設けるととも
に、該散気部材をそれぞれ選択的に作動可能に配設した
ことを特徴とするものである。
In order to solve the above-mentioned problems, a nitrification denitrification apparatus using biofilm filtration according to the present invention is provided with an aeration device in a tank. In the nitrification denitrification apparatus by biofilm filtration with the upper part being a nitrification zone and the lower part being a denitrification zone, the aeration diffuser is provided with a plurality of vertically diffusing members arranged in a tank in a vertical direction. The air members are selectively operably disposed.

【0006】[0006]

【作用】このように構成されたものにおいては、硝化液
と混合され槽内へ供給された被処理液である原水が曝気
用散気装置の下部にある脱窒ゾーンにおいて脱窒処理さ
れたうえ、上部にある硝化ゾーンで硝化処理されるもの
である点は従来のこの種の生物膜濾過による硝化脱窒装
置と同様であるが、前記曝気用散気装置には槽内の垂直
方向に並んだ複数個の散気部材が設けられ該散気部材の
いずれかが原水の水質に応じて選択されて作動するの
で、硝化ゾーンと脱窒ゾーンにおける原水の滞留時間が
適正化され効率的な処理が行われることとなる。
With the above-mentioned structure, the raw water, which is the liquid to be treated, mixed with the nitrification liquid and supplied into the tank, is subjected to the denitrification treatment in the denitrification zone below the aeration diffuser. The point that the nitrification treatment is performed in the upper nitrification zone is the same as a conventional nitrification denitrification apparatus using this type of biofilm filtration, but the aeration diffuser is arranged vertically in the tank. Since a plurality of diffuser members are provided and one of the diffuser members is selected and operated in accordance with the quality of the raw water, the residence time of the raw water in the nitrification zone and the denitrification zone is optimized and the treatment is efficient. Will be performed.

【0007】[0007]

【実施例】次に、本発明を図示の実施例について詳細に
説明する。図中1は槽、2は該槽1内のほぼ中央部に配
された曝気用散気装置、3、4は該曝気用散気装置2の
上下部にそれぞれ形成された硝化ゾーンと脱窒ゾーンで
ある。また、前記曝気用散気装置2には槽1内の垂直方
向に三段に並んだ散気部材5、5、5が設けられている
とともに、該散気部材5はそれぞれモータバルブ6の調
整により選択的に作動可能となるよう配設されている。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. In the figure, reference numeral 1 denotes a tank, 2 denotes an aeration diffuser disposed substantially at the center of the tank 1, and 3 and 4 denote nitrification zones and denitrification formed respectively at upper and lower portions of the aeration diffuser 2. Zone. The aeration diffuser 2 is provided with three vertically dispersing members 5, 5 and 5 in the tank 1, and each of the dispersing members 5 adjusts a motor valve 6. , So that it can be selectively operated.

【0008】前記複数個の散気部材5は、原水の水質に
応じて任意に選択され作動するものので、これによって
硝化ゾーン3と脱窒ゾーン4の容積比を変更し各ゾーン
における原水の滞留時間を適正化するものである。ここ
で、三段ある散気部材5の垂直方向長さ分のゾーンを硝
化と脱窒の共用ゾーン7とすると、各ゾーンの割り振り
は(硝化ゾーン+脱窒ゾーン):共用ゾーン=1:1〜
2:1程度が好ましく、また硝化ゾーン:脱窒ゾーン=
1:1が好ましい。従って、硝化ゾーン:脱窒ゾーン:
共用ゾーン=1:1:2〜1:1:1を標準とする。ま
た、各ゾーンには担体が充填されているが、その比重は
硝化ゾーンが1.2 〜1.4 、脱窒ゾーンが1.8 〜2.0 、共
用ゾーンが1.5 〜1.7 程度が好ましい。これは逆洗の時
に各担体が混ざり合わないようにするためである。
The plurality of air diffusing members 5 are arbitrarily selected and operated in accordance with the quality of the raw water, so that the volume ratio between the nitrification zone 3 and the denitrification zone 4 is changed so that the raw water stays in each zone. This is to optimize the time. Here, assuming that a zone corresponding to the vertical length of the three-stage diffuser member 5 is a common zone 7 for nitrification and denitrification, the allocation of each zone is (nitrification zone + denitrification zone): common zone = 1: 1. ~
About 2: 1 is preferable, and nitrification zone: denitrification zone =
1: 1 is preferred. Therefore, nitrification zone: denitrification zone:
Shared zone = 1: 1: 2 to 1: 1: 1 is standard. Each zone is filled with a carrier. The specific gravity is preferably about 1.2 to 1.4 in the nitrification zone, about 1.8 to 2.0 in the denitrification zone, and about 1.5 to 1.7 in the common zone. This is to prevent the carriers from mixing during backwashing.

【0009】前記の共用ゾーン7には垂直方向に複数個
の散気部材5、5、5が設けられ、これらがそれぞれモ
ータバルブ6、6、6に接続されて制御装置8の指令に
より空気量や曝気箇所などが任意に選択作動され制御で
きるようになっている。また、それぞれの散気部材5の
やや下部には亜硝酸・硝酸検出器9が設けられていると
ともに、最下段の散気部材5を除いてアンモニア検出器
10が設けられており、更に該アンモニア検出器10は
硝化ゾーン3の出口にも設けられている。そして、これ
ら検出器の信号は制御装置8に入力されるよう構成され
ている。なお、脱窒ゾーン4の底部には逆洗処理用の空
気供給器11と水供給器12が配設されており、また硝
化ゾーン3と脱窒ゾーン4が硝化液の返送管13で連結
されている点は従来と同様である。
The common zone 7 is provided with a plurality of air diffusing members 5, 5, 5 in the vertical direction, which are connected to motor valves 6, 6, 6, respectively, and which are controlled by a control device 8 to control the air flow. And the aeration point can be arbitrarily selected and controlled. Further, a nitrite / nitric acid detector 9 is provided slightly below each diffusing member 5, and an ammonia detector 10 is provided except for the lowermost diffusing member 5. The detector 10 is also provided at the outlet of the nitrification zone 3. The signals from these detectors are configured to be input to the control device 8. At the bottom of the denitrification zone 4, an air supply device 11 and a water supply device 12 for backwashing treatment are provided, and the nitrification zone 3 and the denitrification zone 4 are connected by a nitrate return pipe 13. This is the same as in the prior art.

【0010】このように構成されたものにおいては、ま
ず硝化ゾーン3から返送された硝化液と原水とが混合さ
れて槽1の下部の脱窒ゾーン4へ供給され、硝化液中の
亜硝酸及び硝酸が原水中のBOD を水素供与体として脱窒
される。次いで、硝化ゾーン3で曝気されて原水中の有
機性窒素、アンモニア性窒素が硝化されるとともに一部
が処理水として放流され、残部が再び脱窒ゾーン4に返
送される。ここで、原水中の有機性窒素、アンモニア性
窒素が多いと硝化ゾーン3だけでの処理では硝化しきれ
ず、硝化液中に残留するようになる。この場合は、硝化
ゾーン3の出口のアンモニア検出器10の信号により硝
化ゾーン底部(共用ゾーンの最上段)の散気部材5の空
気量を増加する。これでもまだ硝化が不十分のときは共
用ゾーン7の中段にある散気部材5の曝気も追加する。
そして、このような空気量を増加および散気部材5の曝
気の追加操作を硝化ゾーン出口において有機性窒素、ア
ンモニア性窒素が検出されなくなるまで続ける。なお、
原水中の有機性窒素やアンモニア性窒素が少なくなる場
合には、各散気部材5の下部にあるアンモニア検出器1
0の信号により上記の操作を逆に行えばよい。
[0010] In the above-mentioned structure, the nitrification liquid returned from the nitrification zone 3 and the raw water are first mixed and supplied to the denitrification zone 4 at the lower part of the tank 1. Nitric acid is denitrified using BOD in raw water as a hydrogen donor. Next, the nitrogen is aerated in the nitrification zone 3, and the organic nitrogen and the ammonia nitrogen in the raw water are nitrified, a part is discharged as treated water, and the remainder is returned to the denitrification zone 4 again. Here, if the raw water contains a large amount of organic nitrogen and ammonia nitrogen, the treatment in only the nitrification zone 3 is not sufficient for nitrification, and remains in the nitrification liquid. In this case, the amount of air in the air diffusion member 5 at the bottom of the nitrification zone (the uppermost stage of the common zone) is increased by the signal of the ammonia detector 10 at the exit of the nitrification zone 3. If the nitrification is still insufficient, the aeration of the diffuser member 5 in the middle stage of the common zone 7 is also added.
Then, such an additional operation of increasing the air amount and aerating the diffuser member 5 is continued until organic nitrogen and ammonia nitrogen are not detected at the nitrification zone outlet. In addition,
When the amount of organic nitrogen or ammonia nitrogen in the raw water is reduced, the ammonia detector 1 provided at the lower part of each diffuser 5
The above operation may be performed in reverse with a signal of 0.

【0011】一方、原水中の有機性窒素やアンモニア性
窒素が少ない場合には、硝化ゾーン3での滞留時間が長
くなる結果、硝化が完全になる反面、硝化液の持ち込み
DOにより脱窒ゾーン4での脱窒が不十分になる。この場
合は、散気部材下部の亜硝酸・硝酸検出器9の信号によ
り上記硝化の場合と逆の操作を行う。このようにして共
用ゾーン7を原水の水質に応じて硝化ゾーン、あるいは
脱窒ゾーンとして任意かつ選択的に使用することによ
り、硝化脱窒処理を極めて効率的に行うことが可能とな
る。
On the other hand, when the amount of organic nitrogen and ammonia nitrogen in the raw water is small, the residence time in the nitrification zone 3 is prolonged, so that the nitrification is completed.
DO makes denitrification in denitrification zone 4 insufficient. In this case, the reverse operation to the above-mentioned nitrification is performed by the signal of the nitrous acid / nitric acid detector 9 below the air diffusion member. By using the common zone 7 arbitrarily and selectively as a nitrification zone or a denitrification zone according to the quality of raw water, nitrification and denitrification can be performed extremely efficiently.

【0012】なお、上記操作において硝化と脱窒のいず
れを優先させるかについては予め制御装置8に組み込ん
でおけばよい。また、硝化脱窒処理→空洗→水洗のサイ
クル及びこれらの時間配分などは従来法と同様である。
It should be noted that which of nitrification and denitrification is prioritized in the above operation may be incorporated in the control device 8 in advance. The cycle of nitrification and denitrification treatment → empty washing → water washing and the time distribution thereof are the same as in the conventional method.

【0013】本装置を用いて下水を1m3/Hr の規模で処
理した結果と、比較例として従来装置で処理した結果を
表1に示す。
Table 1 shows the results of treating the sewage at a scale of 1 m 3 / Hr using the present apparatus and the results of treating the sewage using a conventional apparatus as a comparative example.

【0014】[0014]

【表1】 [Table 1]

【0015】表1からも明らかなように、実施例におい
ては従来法に比べて20%も小さな槽で効率よく処理で
きることが確認できた。また、T−Nについては約35
%も処理効果を高めることができ、使用空気量も約20
%も削減できることが確認できた。
As is clear from Table 1, it was confirmed that in the example, the treatment can be performed efficiently with a tank as small as 20% as compared with the conventional method. In addition, about 35 for TN
% Can improve the treatment effect, and the amount of air used is about 20%.
It was confirmed that the percentage could be reduced by as much as%.

【0016】[0016]

【発明の効果】以上の説明からも明らかなように、本発
明は硝化ゾーンと脱窒ゾーンとの比率を任意に変えるこ
とにより各ゾーンにおける原水の滞留時間を水質にあわ
せて適正化することができ十分な硝化脱窒を行うことが
できるとともに、処理槽の小型化が図れて装置全体とし
てもコンパクトな設計にすることができるものである。
よって本発明は従来の問題点を一掃した生物膜濾過によ
る硝化脱窒装置として、産業の発展に寄与するところは
極めて大である。
As is apparent from the above description, the present invention makes it possible to optimize the residence time of raw water in each zone according to the water quality by arbitrarily changing the ratio between the nitrification zone and the denitrification zone. The nitrification and denitrification can be performed as much as possible, and the processing tank can be downsized, so that the entire apparatus can be designed to be compact.
Therefore, the present invention greatly contributes to industrial development as a nitrification and denitrification apparatus by biofilm filtration that has eliminated the conventional problems.

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

【図1】本発明の実施例を示す正面図である。FIG. 1 is a front view showing an embodiment of the present invention.

【図2】従来技術を示す正面図である。FIG. 2 is a front view showing a conventional technique.

【符号の説明】[Explanation of symbols]

1 槽 2 曝気用散気装置 3 硝化ゾーン 4 脱窒ゾーン 5 散気部材 8 制御装置 9 亜硝酸・硝酸検出器 10 アンモニア検出器 Reference Signs List 1 tank 2 aeration diffuser 3 nitrification zone 4 denitrification zone 5 diffuser 8 controller 9 nitrite / nitric acid detector 10 ammonia detector

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 槽内に曝気用散気装置を配して該曝気用
散気装置の上部を硝化ゾーン、下部を脱窒ゾーンとした
生物膜ろ過による硝化脱窒装置において、前記曝気用散
気装置に槽内の垂直方向に並んだ複数個の散気部材を設
けるとともに、該散気部材をそれぞれ選択的に作動可能
に配設したことを特徴とする生物膜ろ過による硝化脱窒
装置。
1. A nitrification denitrification apparatus using biofilm filtration, wherein an aeration diffuser is disposed in a tank, and an upper part of the aeration diffuser is a nitrification zone and a lower part is a denitrification zone. A nitrification denitrification apparatus using biofilm filtration, wherein a plurality of air diffusing members arranged in a vertical direction in a tank are provided in a gas device, and the gas diffusing members are selectively operable.
【請求項2】 硝化ゾーンの垂直方向に複数個のアンモ
ニア検出器を設けるとともに脱窒ゾーンの垂直方向には
複数個の亜硝酸・硝酸検出器を設け、該アンモニア検出
器と亜硝酸・硝酸検出器からの信号に基づき散気部材の
いずれかを選択して作動させる制御装置を曝気用散気装
置に連結したことを特徴とする請求項1に記載の生物膜
ろ過による硝化脱窒装置。
2. A plurality of ammonia detectors are provided in the vertical direction of the nitrification zone, and a plurality of nitrite / nitric acid detectors are provided in the vertical direction of the denitrification zone. The nitrification denitrification apparatus according to claim 1, wherein a control device for selecting and operating one of the air diffusion members based on a signal from the vessel is connected to the air diffusion air diffusion apparatus.
JP4378193A 1993-03-04 1993-03-04 Nitrification and denitrification equipment by biofilm filtration Expired - Fee Related JP2604958B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4378193A JP2604958B2 (en) 1993-03-04 1993-03-04 Nitrification and denitrification equipment by biofilm filtration

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4378193A JP2604958B2 (en) 1993-03-04 1993-03-04 Nitrification and denitrification equipment by biofilm filtration

Publications (2)

Publication Number Publication Date
JPH06254591A JPH06254591A (en) 1994-09-13
JP2604958B2 true JP2604958B2 (en) 1997-04-30

Family

ID=12673304

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4378193A Expired - Fee Related JP2604958B2 (en) 1993-03-04 1993-03-04 Nitrification and denitrification equipment by biofilm filtration

Country Status (1)

Country Link
JP (1) JP2604958B2 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101130822B1 (en) * 2005-05-12 2012-03-28 주식회사 포스코 Treatment method of waste water containing nitrogen
CN103466796B (en) * 2013-09-27 2015-01-21 桂林理工大学 Method for carrying out synchronous nitrification treatment and denitrification treatment on percolate by using mineralized refuse reaction bed
CN105645601B (en) * 2016-03-24 2019-02-22 北京泰昌科睿环保科技有限公司 A kind of biofilter and sewage water treatment method
CN108147534A (en) * 2016-12-06 2018-06-12 帕克环保技术(上海)有限公司 Nitration denitrification integrated bioreactor
CN106517519A (en) * 2016-12-06 2017-03-22 中国科学院生态环境研究中心 Aerobic-anoxic integrated moving bed bio-membrane reactor and sewage treatment method thereof

Also Published As

Publication number Publication date
JPH06254591A (en) 1994-09-13

Similar Documents

Publication Publication Date Title
US4179374A (en) Apparatus for the treatment of wastewater
JP3376561B2 (en) Purification system and purification method for wastewater containing nitrogen compounds
US7147778B1 (en) Method and system for nitrifying and denitrifying wastewater
US5192442A (en) Multiple zone batch treatment process
US5611927A (en) System for removing nutrients from wastewater
US7198716B2 (en) Phased activated sludge system
JP3237877B2 (en) Improved biological treatment equipment for wastewater.
US6426004B1 (en) Continuous flow completely mixed waste water treatment method
US7731842B2 (en) Submerged fixed film anoxic bioreactor
JP2020006341A (en) Sewage treatment method and apparatus
JP2604958B2 (en) Nitrification and denitrification equipment by biofilm filtration
US7056438B2 (en) Flood and drain wastewater treatment system and associated methods
JP3677783B2 (en) Nitrification method
JP3373015B2 (en) Wastewater nitrification denitrification treatment equipment
JPH0716595A (en) Operation control method in modified method for circulating active sludge
JPH05154496A (en) Controlling method for operation in anaerobic and aerobic activated sludge treating equipment
JP2017104806A (en) Nitrification-denitrification device
JP3407342B2 (en) Biological denitrification / phosphorus removal equipment
JP3136901B2 (en) Wastewater treatment method
JPH1094796A (en) Treatment of waste water and device therefor
Roustan et al. Separation of the two functions aeration and mixing in oxidation ditches: Application to the denitrification by activated sludge
JPH11685A (en) Circulating device for treated effluent in oxidation ditch
JP2002210484A (en) Method and apparatus for treating organic waste water
JP3376905B2 (en) Intermittent aeration activated sludge treatment equipment
JP2000279992A (en) Waste water treatment and apparatus therefor

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: 19961213

LAPS Cancellation because of no payment of annual fees