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JPH06114388A - Biological filtering method - Google Patents

Biological filtering method

Info

Publication number
JPH06114388A
JPH06114388A JP26343092A JP26343092A JPH06114388A JP H06114388 A JPH06114388 A JP H06114388A JP 26343092 A JP26343092 A JP 26343092A JP 26343092 A JP26343092 A JP 26343092A JP H06114388 A JPH06114388 A JP H06114388A
Authority
JP
Japan
Prior art keywords
biological filtration
filtration tank
biological filter
tank
stage biological
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
JP26343092A
Other languages
Japanese (ja)
Inventor
Masahiko Tsutsumi
正彦 堤
Kyozo Kawachi
恭三 河内
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toshiba Corp filed Critical Toshiba Corp
Priority to JP26343092A priority Critical patent/JPH06114388A/en
Publication of JPH06114388A publication Critical patent/JPH06114388A/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)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

PURPOSE:To always keep a denitrifying ratio high and to obtain stable treated water quality by connecting two biological filter tanks in series or in parallel and removing a suspended substance in the front stage biological filter tank and performing denitrifying treatment in the post stage biological filter tank and performing the alteration of a passage accompanied by washing operation at every predetermined time. CONSTITUTION:Two biological filter tanks 1, 2 are arranged to front and post stages and, after the post stage biological filter tank 2 is washed, the passage from an upstream part is connected to the post and front stage biological filter tanks 2, 1 to perform water treatment operation. Immediately after denitrification is performed in the front stage biological filter tank 1, the suspended substance in inflow raw water can be caught in the post stage biological filter tank 2. Therefore, the advance of breakthrough can be suppressed and the denitrifying ratio of the front stage biological filter tank 1 can be kept. After the front stage biological filter tank 1 is washed, the passage from the upstream part is connected to the front and post stage biological filter tanks 1, 2 to perform water treatment operation. By this constitution, the suspended substance in raw water can be removed in the front stage biological filter tank 1 and denitrification can be performed in the post stage biological filter tank 2. Therefore, the treated water is kept in good quality.

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、下水、産業廃水等の有
機性廃水もしくは有機性廃水の2次処理水等の浄化技術
に係わり、特に生物膜を利用して脱窒処理する生物ろ過
方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a technique for purifying organic wastewater such as sewage and industrial wastewater, or secondary treated water of organic wastewater, and more particularly to a biological filtration method for denitrifying using a biofilm. Regarding

【0002】[0002]

【従来の技術】生物学的脱窒法としては、(1)嫌気好
気循環法、(2)C源(炭素源)添加非循環法、(3)
C源無添加非循環法(内生脱窒法)等が知られている。
2. Description of the Related Art Biological denitrification methods include (1) anaerobic and aerobic circulation method, (2) C source (carbon source) addition non-circulation method, and (3)
C source-free non-circulation method (endogenous denitrification method) and the like are known.

【0003】図4は、上記した従来の内生脱窒法による
生物ろ過装置の概略構成図である。同図において、前段
の硝化槽で硝化された水、つまり硝化液は、開閉弁91
を有する管92を介して生物ろ過槽93に供給される。
供給された水は、ろ材94を通過して管95を介して処
理水として放流される。この水処理運転でろ材94に生
物膜が付着する。この生物膜は、開閉弁91を閉じ開閉
弁96を開けることによって空気源から管97を介して
加圧空気を生物ろ過槽93内に供給し、空気洗浄により
剥離される。この剥離された生物膜は開閉弁98を開く
ことによって管99から排泥される。
FIG. 4 is a schematic configuration diagram of a biological filtration device by the above-mentioned conventional endogenous denitrification method. In the figure, the water nitrified in the preceding nitrification tank, that is, the nitrification liquid, is stored in the open / close valve 91.
It is supplied to the biological filtration tank 93 via a pipe 92 having a.
The supplied water passes through the filter medium 94 and is discharged as treated water through the pipe 95. A biofilm adheres to the filter medium 94 by this water treatment operation. This biofilm is separated by supplying air with pressurized air from the air source to the biofiltration tank 93 through the pipe 97 by closing the open / close valve 91 and opening the open / close valve 96, and by air washing. The separated biofilm is discharged from the pipe 99 by opening the opening / closing valve 98.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、上記従
来の生物ろ過装置においては、以下の問題があった。図
5に示すように、TN(Total Nitrogen:全窒素)除去
率つまり脱窒率が水処理運転を開始して約3〜4日で約
70%と上昇するが、それまでは低く、特に洗浄直後T
N除去率は0%であった。つまり、脱窒が安定しないと
いった問題があった。
However, the above-mentioned conventional biological filtration device has the following problems. As shown in FIG. 5, the TN (Total Nitrogen: total nitrogen) removal rate, that is, the denitrification rate, increases to about 70% within about 3 to 4 days after the water treatment operation is started, but it is low until then, especially for cleaning. Immediately after T
The N removal rate was 0%. In other words, there was a problem that denitrification was not stable.

【0005】これは、内生脱窒法が適度な生物膜量で起
こるためであり、洗浄直後は生物膜が大部分剥離され、
脱窒されなくなる。内生脱窒法の脱窒が起こる条件は、
DO(溶存酸素濃度)が低く、生物膜中の炭素源が溶出
するまで生物膜量が高くならなければならない。しかし
ながら、生物膜量を脱窒が起こるまで高めると、ろ材9
4が閉塞し、破過して水が流れなくなり、洗浄しなけれ
ば水処理運転が継続できなくなる。
This is because the endogenous denitrification method occurs with an appropriate amount of biofilm, and most of the biofilm is peeled off immediately after washing,
It will not be denitrified. The conditions for denitrification in the endogenous denitrification method are
The DO (dissolved oxygen concentration) must be low and the amount of biofilm must be high until the carbon source in the biofilm elutes. However, if the amount of biofilm is increased until denitrification occurs, the filter medium 9
4 is closed, breaks through and water does not flow, and the water treatment operation cannot be continued unless it is washed.

【0006】本発明は上記問題を解決するためになされ
たもので、その目的は、常に脱窒率が高く保持でき、常
に安定した処理水質を得ることができる生物ろ過方法を
提供することにある。
The present invention has been made to solve the above problems, and an object of the present invention is to provide a biological filtration method capable of always maintaining a high denitrification rate and always obtaining a stable treated water quality. .

【0007】[0007]

【課題を解決するための手段】上記目的を達成するため
に、本発明は生物ろ過槽内に充填されたろ材表面に形成
される生物膜の有機物分解作用および吸着作用により被
処理水を浄化処理するとともに、生物ろ過槽を洗浄する
機能を有する生物ろ過方法において、少くとも2槽の生
物ろ過槽を直列あるいは並列に連結すると共にその被処
理水の流路を変更できるように開閉弁及び管を配置し、
被処理水の通水時は前段の生物ろ過槽で浮遊物除去、次
段の生物ろ過槽で脱窒処理し、また次段の生物ろ過槽を
洗浄した後、被処理水の流路を洗浄された生物ろ過槽を
前段となるように変更し、以下所定時間毎に洗浄操作に
ともなう同様の流路変更を行うことを特徴とする。
In order to achieve the above object, the present invention purifies the water to be treated by decomposing and adsorbing the organic matter of the biofilm formed on the surface of the filter medium filled in the biological filtration tank. In addition, in the biological filtration method having the function of cleaning the biological filtration tank, at least two biological filtration tanks are connected in series or in parallel, and an opening / closing valve and a pipe are provided so that the flow path of the treated water can be changed. Place and
When water to be treated is passed, the suspended matter is removed in the biological filtration tank in the previous stage, denitrification is performed in the biological filtration tank in the next stage, and the biological filtration tank in the next stage is washed, and then the flow path of the treated water is washed. It is characterized in that the biological filtration tank thus prepared is changed to a former stage, and thereafter, the same flow path change is carried out at every predetermined time with the washing operation.

【0008】[0008]

【作用】本発明の生物ろ過方法によると、少なくとも2
槽の生物ろ過槽を前段と後段に配置しており、後段の生
物ろ過槽を洗浄した後、上流からの流路を後段の生物ろ
過槽、前段の生物ろ過槽にして水処理運転を行うので、
前段の生物ろ過槽で脱窒が行った直後、流入する原水の
浮遊物を後段の生物ろ過槽で捕獲できるので破過の進行
を抑制でき、前段の生物ろ過槽の脱窒率を維持できる。
さらに、前段の生物ろ過槽を洗浄した後、上流からの流
路を前段の生物ろ過槽、後段の生物ろ過槽にして水処理
運転を行うので、上記と同様に前段の生物ろ過槽で浮遊
物を除去して後段の生物ろ過槽で脱窒することができ
る。したがって、良好な処理水が維持される。
According to the biological filtration method of the present invention, at least 2
Since the biological filtration tank of the tank is arranged at the front stage and the rear stage, after cleaning the biological filtration tank of the latter stage, the water treatment operation is performed by setting the flow path from the upstream to the biological filtration tank of the latter stage and the biological filtration tank of the former stage. ,
Immediately after denitrification in the front biological filtration tank, the suspended matter of the inflowing raw water can be captured in the rear biological filtration tank, so that the progress of breakthrough can be suppressed and the denitrification rate of the front biological filtration tank can be maintained.
Furthermore, after washing the front biological filtration tank, the water treatment operation is performed by setting the flow path from the upstream to the front biological filtration tank and the rear biological filtration tank. Can be removed and denitrification can be performed in the biological filtration tank in the latter stage. Therefore, good treated water is maintained.

【0009】[0009]

【実施例】本発明の実施例を図面を参照して説明する。
図1は本発明の一実施例に係る生物ろ過装置の概略構成
図である。同図に示すように、本実施例に係る生物ろ過
装置は、第1生物ろ過槽1と第2生物ろ過槽2とから構
成される。第1生物ろ過槽1の上部には上部越流端3と
下部越流端4を有し、第2生物ろ過槽2の上部には上部
越流端5と下部越流端6を有している。また、第1生物
ろ過槽1の下部には散気管7を配し、第2生物ろ過槽2
の下部には散気管8を配している。
Embodiments of the present invention will be described with reference to the drawings.
FIG. 1 is a schematic configuration diagram of a biological filtration device according to an embodiment of the present invention. As shown in the figure, the biological filtration device according to the present embodiment includes a first biological filtration tank 1 and a second biological filtration tank 2. The upper part of the first biological filtration tank 1 has an upper overflow end 3 and a lower overflow end 4, and the upper part of the second biological filtration tank 2 has an upper overflow end 5 and a lower overflow end 6. There is. Further, an air diffusing pipe 7 is arranged below the first biological filtration tank 1 and the second biological filtration tank 2 is provided.
An air diffuser 8 is arranged in the lower part of the.

【0010】第1生物ろ過槽1の下部には管10が配さ
れ、この管10は連結部11、開閉弁12を有する管1
3、連結部14を順次介して管15と接続される。連結
部14は開閉弁16を有する管17、連結部18、管1
9を順次介して第2生物ろ過槽2の下部と接続される。
連結部11は開閉弁20を有する管21を介して第2生
物ろ過槽2の上部越流端5と連結される。連結部18は
開閉弁22を有する管23と接続され、第1生物ろ過槽
1の上部越流端3と連結される。また下部越流端4は開
閉弁24を有する管25と接続され、下部越流端6は開
閉弁26を有する管27と接続される。さらに、第1生
物ろ過槽1の底部には開閉弁30を有する管31が配さ
れ、第2生物ろ過槽2の底部には開閉弁32を有する管
33が配されている。
A pipe 10 is arranged below the first biological filtration tank 1, and the pipe 10 has a connecting portion 11 and an opening / closing valve 12.
3, and the pipe 15 is connected through the connecting portion 14 in sequence. The connecting portion 14 includes a pipe 17 having an opening / closing valve 16, a connecting portion 18, and a pipe 1.
It is connected to the lower part of the second biological filtration tank 2 via 9 sequentially.
The connecting portion 11 is connected to the upper overflow end 5 of the second biological filtration tank 2 via a pipe 21 having an opening / closing valve 20. The connecting portion 18 is connected to a pipe 23 having an opening / closing valve 22 and is connected to the upper overflow end 3 of the first biological filtration tank 1. The lower overflow end 4 is connected to a pipe 25 having an opening / closing valve 24, and the lower overflow end 6 is connected to a pipe 27 having an opening / closing valve 26. Further, a pipe 31 having an opening / closing valve 30 is arranged at the bottom of the first biological filtration tank 1, and a pipe 33 having an opening / closing valve 32 is arranged at the bottom of the second biological filtration tank 2.

【0011】第1生物ろ過槽1の下部に設けた散気管7
は、開閉弁40を有する管41、連結部42、管43を
順次介して空気源44と接続される。また第2生物ろ過
槽2の下部に設けた散気管8は、開閉弁45を有する管
46を介して連結部42と接続される。
An air diffuser 7 provided at the bottom of the first biological filtration tank 1.
Is connected to an air source 44 through a pipe 41 having an opening / closing valve 40, a connecting portion 42, and a pipe 43 in this order. Further, the air diffusing pipe 8 provided in the lower portion of the second biological filtration tank 2 is connected to the connecting portion 42 via a pipe 46 having an opening / closing valve 45.

【0012】一方、第1生物ろ過槽1の内部には、上部
の支持板50と下部の支持板51の間にプラスチック、
セメントボール、アンスラサイト等のろ材52が充填さ
れている。同様に第2生物ろ過槽2の内部には、上部の
支持板53と下部の支持板54の間にろ材52と同じろ
材55が充填されている。なお、図中には示していない
が、前記すべての開閉弁をON−OFF制御するタイマ
ー制御器が配されている。
On the other hand, inside the first biological filtration tank 1, plastic is provided between the upper support plate 50 and the lower support plate 51.
A filter medium 52 such as cement balls and anthracite is filled. Similarly, inside the second biological filtration tank 2, the same filter medium 55 as the filter medium 52 is filled between the upper support plate 53 and the lower support plate 54. Although not shown in the figure, a timer controller for ON / OFF controlling all the on-off valves is provided.

【0013】次に、本実施例の生物ろ過方法の作用につ
いて説明する。図2は、本実施例に係る生物ろ過装置の
運転工程、洗浄工程およびTN(全窒素)除去率を時系
列で示したものであり、以下この図を参照して説明す
る。
Next, the operation of the biological filtration method of this embodiment will be described. FIG. 2 shows the operating process, the cleaning process, and the TN (total nitrogen) removal rate of the biological filtration apparatus according to the present embodiment in time series, which will be described below with reference to this drawing.

【0014】<立ち上げ時(t=0〜7日)>水処理運
転の流路は第1生物ろ過槽1(図中は第1槽と略す)か
ら第2生物ろ過槽2(図中では第2槽と略す)の方向
(D)である。つまり、開閉弁16,20,24,3
0,32,40,45を閉じ、開閉弁12,22,26
を開ける。この状態において、下水を硝化した液つまり
硝化液60は管15、連結部14、管13、連結部1
1、管10を順次介して第1生物ろ過槽1に供給され
る。供給された硝化液はろ材52を通過する過程で硝化
液中の浮遊物SSがろ材52に付着され除去される。硝
化液には脱窒菌が混入しているので、浮遊物SSの付着
が進行するにしたがって、TN除去率が徐々に上昇し
て、t=約5日でTN除去率が約70%に達する(A)
と(B)。
<At startup (t = 0 to 7 days)> The flow path of the water treatment operation is from the first biological filtration tank 1 (abbreviated as the first tank in the figure) to the second biological filtration tank 2 (in the figure). It is the direction (D) in the second tank). That is, the on-off valves 16, 20, 24, 3
0, 32, 40, 45 are closed, and open / close valves 12, 22, 26
Open. In this state, the liquid obtained by nitrifying the sewage, that is, the nitrification liquid 60, is connected to the pipe 15, the connecting portion 14, the pipe 13, and the connecting portion 1.
1, and is sequentially supplied to the first biological filtration tank 1 through the pipe 10. In the process of the supplied nitrification liquid passing through the filter medium 52, suspended matter SS in the nitrification liquid is attached to the filter medium 52 and removed. Since the denitrifying bacteria are mixed in the nitrification solution, the TN removal rate gradually increases as the adherence of the suspended matter SS progresses, and reaches about 70% at t = about 5 days ( A)
And (B).

【0015】TNが除去された水は上部越流端3、開閉
弁22、管23、連結部18、管19を順次介して第2
生物ろ過槽2に供給される。供給された水はろ材55を
通過して下部越流端6、開閉弁26、管27を順次介し
て処理水61として河川等に放流される。
The water from which the TN has been removed passes through the upper overflow end 3, the opening / closing valve 22, the pipe 23, the connecting portion 18, and the pipe 19 in this order to the second
It is supplied to the biological filtration tank 2. The supplied water passes through the filter medium 55 and is sequentially discharged through the lower overflow end 6, the on-off valve 26, and the pipe 27 as treated water 61 to a river or the like.

【0016】<第2生物ろ過槽2の洗浄工程及び洗浄時
水処理運転(t=7〜7.1日)>t=7日になると、第
1生物ろ過槽1から第2生物ろ過槽2への運転(D)か
ら、硝化液60を供給する流路を第1生物ろ過槽1のみ
の運転(H)に切り換える。つまり、開閉弁22と開閉
弁26を閉じ、開閉弁24を開けることによって、ろ材
52を通過した水は下部越流端4、開閉弁24、管25
を順次介して処理水62として放流される。
<Cleaning Step of Second Biological Filtration Tank 2 and Water Treatment Operation at Cleaning (t = 7 to 7.1 days)> When t = 7 days, the first biological filtration tank 1 to the second biological filtration tank 2 From the operation (D) to the operation (D), the flow path for supplying the nitrification liquid 60 is switched to the operation (H) of only the first biological filtration tank 1. In other words, by closing the on-off valve 22 and the on-off valve 26 and opening the on-off valve 24, the water that has passed through the filter medium 52 causes the water to pass through the lower overflow end 4, the on-off valve 24, and the pipe 25.
Is sequentially discharged as treated water 62.

【0017】続いて、開閉弁45を開けてエアを空気源
44から管43、連結部42、開閉弁45、管46、散
気管8を順次介して第2生物ろ過槽2の炉材55内に供
給し、エア洗浄する運転に入る(G)。このとき、ろ材
55の表面に過剰に付着した生物膜は、エアによる揃断
力によって強制剥離される。次に、開閉弁45を閉じて
開閉弁32を開けて過剰に剥離した生物膜を管33を介
して排泥する。この工程に要する時間は0.1日(約2時
間)である。
Subsequently, the on-off valve 45 is opened to supply air from the air source 44 through the pipe 43, the connecting portion 42, the on-off valve 45, the pipe 46, and the diffuser pipe 8 in the furnace material 55 of the second biological filtration tank 2. To the air and start the operation of washing with air (G). At this time, the biofilm excessively attached to the surface of the filter medium 55 is forcibly peeled off by the cutting force of the air. Next, the on-off valve 45 is closed and the on-off valve 32 is opened, and the excessively separated biofilm is discharged through the pipe 33. The time required for this step is 0.1 day (about 2 hours).

【0018】<第2生物ろ過槽2の洗浄後の水処理運転
(t=7.1〜14日)>洗浄工程終了後、開閉弁32,
12を閉じ、開閉弁16,20,24を開けることによ
って、硝化液60を供給する水の流路を、第1生物ろ過
槽1のみの運転から、第2生物ろ過槽2から第1生物ろ
過槽1への運転に切り換える(E)。
<Water treatment operation after cleaning the second biological filtration tank 2 (t = 7.1 to 14 days)> After completion of the cleaning process, the on-off valve 32,
By closing 12 and opening the on-off valves 16, 20, 24, the flow path of the water supplying the nitrification liquid 60 is changed from the operation of only the first biological filtration tank 1 to the second biological filtration tank 2 Switch to operation to tank 1 (E).

【0019】このとき、第1生物ろ過槽1においてTN
除去率が約70%となっており、第2生物ろ過槽2で硝
化液中の浮遊物SSを除去するので、第1生物ろ過槽1
のろ材52の破過が進行せず、安定したTN除去が行わ
れる。つまり、硝化液60は、管15、連結部14、管
17、開閉弁16、連結部18、管19を順次介して第
2生物ろ過槽2に供給され、このろ材55で硝化液60
中の浮遊物SSを付着除去し、その水を上部越流端5、
開閉弁20、管21、連結部11、管10を順次介して
第1生物ろ過槽1に供給される。この第1生物ろ過槽1
中のろ材52に付着した脱窒菌によって硝化液中の硝酸
性窒素を脱窒する。脱窒された水は、下部越流端4、開
閉弁24、管25を順次介して処理水62として放流さ
れる。
At this time, in the first biological filtration tank 1, the TN
The removal rate is about 70%, and since the suspended matter SS in the nitrification liquid is removed by the second biological filtration tank 2, the first biological filtration tank 1
Stable TN removal is performed without breakthrough of the filter medium 52. That is, the nitrification liquid 60 is supplied to the second biological filtration tank 2 through the pipe 15, the connecting portion 14, the pipe 17, the opening / closing valve 16, the connecting portion 18, and the pipe 19 in this order, and the nitrification liquid 60 is supplied by the filter medium 55.
Suspended matter SS inside is removed and the water is removed from the upper overflow end 5,
It is supplied to the first biological filtration tank 1 through the on-off valve 20, the pipe 21, the connecting portion 11, and the pipe 10 in this order. This first biological filtration tank 1
The nitrate nitrogen in the nitrification solution is denitrified by the denitrifying bacteria attached to the filter medium 52 therein. The denitrified water is discharged as treated water 62 through the lower overflow end 4, the on-off valve 24, and the pipe 25 in this order.

【0020】<第1生物ろ過槽1の洗浄工程及び洗浄時
水処理運転(t=14〜14.1日)>t=14日になる
と、第2生物ろ過槽2から第1生物ろ過槽1への運転
(E)から、硝化液60を供給する流路を第2生物ろ過
槽2のみの運転に切り換える(I)。つまり、開閉弁2
0と24を閉じ、開閉弁26を開けることによって、硝
化液60は、管15、連結点14、開閉弁16、連結点
18、管19を順次介して第2生物ろ過槽2に供給さ
れ、ろ材55に付着した脱窒菌によって脱窒される。脱
窒された水は下部越流端6、開閉弁26、管27を順次
介して処理水61として放流される。
<Washing Step of First Biological Filtration Tank 1 and Water Treatment Operation at Washing (t = 14 to 14.1 Days)> When t = 14 days, from the second biological filtration tank 2 to the first biological filtration tank 1. From the operation (E) to (2), the flow path for supplying the nitrification liquid 60 is switched to the operation of only the second biological filtration tank 2 (I). That is, the on-off valve 2
By closing 0 and 24 and opening the opening / closing valve 26, the nitrification liquid 60 is supplied to the second biological filtration tank 2 through the pipe 15, the connecting point 14, the opening / closing valve 16, the connecting point 18 and the pipe 19 in order, It is denitrified by the denitrifying bacteria attached to the filter medium 55. The denitrified water is discharged as treated water 61 through the lower overflow end 6, the on-off valve 26, and the pipe 27 in this order.

【0021】続いて、開閉弁40を開けて空気源44か
らエアを管43、連結点42、開閉弁40、管41、散
器管7を順次介して第1生物ろ過槽1に供給する。供給
されたエアは、ろ材52に上昇したエアの揃断力によっ
て生物膜を強制剥離させる。次に、開閉弁40を閉じ開
閉弁30を開けて剥離した生物膜を管31を介して排泥
する。排泥後、開閉弁30を開ける。この洗浄工程およ
び洗浄時水処理運転に要する時間は、0.1日(約2時
間)である。
Subsequently, the on-off valve 40 is opened and air is supplied from the air source 44 to the first biological filtration tank 1 through the pipe 43, the connecting point 42, the on-off valve 40, the pipe 41 and the disperser pipe 7 in this order. The supplied air forcibly separates the biofilm by the uniform force of the air that has risen to the filter medium 52. Next, the opening / closing valve 40 is closed and the opening / closing valve 30 is opened, and the separated biofilm is discharged through the pipe 31. After the mud is discharged, the open / close valve 30 is opened. The time required for this cleaning step and the water treatment operation during cleaning is 0.1 day (about 2 hours).

【0022】続いて、第1生物ろ過槽1の洗浄後(t=
14.1日)、第1生物ろ過槽1から第2生物ろ過槽2へ
の水処理運転に切り換える。このときの操作は前記t=
0〜7日の場合と同様に行う。以下、第1生物ろ過槽1
と第2生物ろ過槽2との流路を交互に切り換える運転を
継続する。
Then, after washing the first biological filtration tank 1 (t =
(14.1 days), switch to the water treatment operation from the first biological filtration tank 1 to the second biological filtration tank 2. The operation at this time is t =
Do as in 0-7 days. Hereinafter, the first biological filtration tank 1
And the operation of alternately switching the flow paths of the second biological filtration tank 2 is continued.

【0023】以上説明したように、本実施例によれば、
以下のような効果が得られる。 (1) 第1生物ろ過槽1と第2生物ろ過槽2との切り換え
運転を、タイマー制御器による開閉弁の開閉操作のみで
ON−OFFでき維持管理が容易となる。 (2) 上部越流端と下部越流端を配し、そのヘッド差によ
って水を流すので、通水のエネルギーが不要であり、ラ
ンニングコストが非常に小さくなる。 (3) 生物ろ過槽の洗浄にエア洗浄を用いたので、水や薬
液洗浄に必要なポンプ、調整槽、水槽等が不要となり、
設置面積が小さくかつランニングコストが小さくなる。
As described above, according to this embodiment,
The following effects can be obtained. (1) Switching operation between the first biological filtration tank 1 and the second biological filtration tank 2 can be turned ON / OFF simply by opening / closing the opening / closing valve by the timer controller, which facilitates maintenance. (2) Since the upper overflow end and the lower overflow end are arranged and water flows according to the head difference between them, the energy for water flow is not required and the running cost is very small. (3) Since air cleaning was used to clean the biological filtration tank, the pump, adjustment tank, water tank, etc. required for cleaning water and chemicals are not required,
The installation area is small and the running cost is small.

【0024】(他の実施例)以上、本発明の代表的な実
施例について述べたが、本発明はこれに限定されるもの
ではなく、例えば以下のような実施例にも適用可能であ
る。 (1) 図1の実施例では第1生物ろ過槽と第2生物ろ過槽
の2つの生物ろ過槽を用いたが、生物ろ過槽の数はこれ
に限定する必要はない。直列に3槽、4槽、…と配置す
ること、あるいは並列に配置することも可能である。
(Other Embodiments) The representative embodiments of the present invention have been described above. However, the present invention is not limited to this, and is applicable to the following embodiments, for example. (1) In the embodiment of FIG. 1, two biological filtration tanks, a first biological filtration tank and a second biological filtration tank, were used, but the number of biological filtration tanks need not be limited to this. It is also possible to arrange three tanks, four tanks, ... In series, or to arrange them in parallel.

【0025】例えば、図3に示すように第1生物ろ過槽
70、第2生物ろ過槽71、第3生物ろ過槽72を順次
3槽直列に配することができる。なお、56,57,5
8はろ材、63,64,65は処理水である。この場
合、水処理運転および洗浄のタイミングは、表1に示す
通りである。この表では第1生物ろ過槽を第1槽、同様
に第2槽、第3槽と略した。つまり、上流から2番目の
生物ろ過槽を洗浄した後、洗浄する前の水処理運転の流
路である第3槽→第1槽→第2槽という流路に切り換え
る。この場合も図1と同様に、脱窒が常に良好に維持で
き、かつ第3槽で流出する浮遊物SSを捕獲でき、清澄
な処理水が得られる。
For example, as shown in FIG. 3, three first biological filtration tanks 70, a second biological filtration tank 71, and a third biological filtration tank 72 can be sequentially arranged in series. In addition, 56, 57, 5
8 is a filter medium, and 63, 64 and 65 are treated water. In this case, the water treatment operation and the cleaning timing are as shown in Table 1. In this table, the first biological filtration tank is abbreviated as the first tank, and similarly, the second tank and the third tank. That is, after cleaning the second biological filtration tank from the upstream side, the flow path of the water treatment operation before cleaning is switched to the flow path of the third tank → first tank → second tank. In this case as well, as in the case of FIG. 1, denitrification can always be favorably maintained, the suspended matter SS flowing out in the third tank can be captured, and clear treated water can be obtained.

【0026】[0026]

【表1】 [Table 1]

【0027】(2) 図1の実施例では生物ろ過槽のろ材の
洗浄にエア洗浄を使用しているが、水洗およびエア洗浄
と水洗の組み合わせも可能であり、洗浄方法は上記実施
例のみに限定する必要はない。
(2) In the embodiment of FIG. 1, air cleaning is used for cleaning the filter material of the biological filtration tank, but it is also possible to use water cleaning and a combination of air cleaning and water cleaning. There is no need to limit it.

【0028】(3) 図1の実施例では生物生物ろ過槽上部
の越流位置を変更することによって水の流れを変更して
いるが、水の供給方法としてはポンプやエアリフト等を
使用することも可能である。
(3) In the embodiment shown in FIG. 1, the flow of water is changed by changing the overflow position at the upper part of the biological / biological filtration tank. However, as a water supply method, a pump, an air lift or the like should be used. Is also possible.

【0029】(4) 生物ろ過槽の形状、水の流れ方向、ろ
材の種類は上記実施例のみに限定する必要はない。
(4) The shape of the biological filtration tank, the flow direction of water, and the type of filter medium need not be limited to those in the above embodiments.

【0030】[0030]

【発明の効果】以上説明したように、本発明によれば、
常に脱窒率が高く維持でき、常に安定した処理水質を得
ることが可能な生物ろ過方法を提供することができる。
As described above, according to the present invention,
It is possible to provide a biological filtration method that can always maintain a high denitrification rate and can always obtain stable treated water quality.

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

【図1】本発明の一実施例に係る生物ろ過装置の概略構
成図。
FIG. 1 is a schematic configuration diagram of a biological filtration device according to an embodiment of the present invention.

【図2】図1の作用を説明するための運転及び洗浄工程
を時系列で表した図。
FIG. 2 is a diagram showing the operation and cleaning steps in time series for explaining the operation of FIG.

【図3】本発明の他の実施例に係る生物ろ過装置の概略
構成図。
FIG. 3 is a schematic configuration diagram of a biological filtration device according to another embodiment of the present invention.

【図4】従来の生物ろ過装置の概略構成図。FIG. 4 is a schematic configuration diagram of a conventional biological filtration device.

【図5】図4の廃水処理装置の作用を説明するための運
転及び洗浄工程を説明するための図。
FIG. 5 is a diagram for explaining an operation and a washing process for explaining the operation of the wastewater treatment device of FIG.

【符号の説明】[Explanation of symbols]

1…第1生物ろ過槽、2…第2生物ろ過槽、3,5…上
部越流端、4,6…下部越流端、44…空気源、52,
55,56,57,58…ろ材、60…硝化液、61,
62,63,64,65…処理水。
1 ... 1st biological filtration tank, 2 ... 2nd biological filtration tank, 3, 5 ... upper overflow end, 4, 6 ... lower overflow end, 44 ... air source, 52,
55, 56, 57, 58 ... Filter medium, 60 ... Nitrification liquid, 61,
62, 63, 64, 65 ... Treated water.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 生物ろ過槽内に充填されたろ材表面に形
成される生物膜の有機物分解作用および吸着作用により
被処理水を浄化処理するとともに、生物ろ過槽を洗浄す
る機能を有する生物ろ過方法において、少くとも2槽の
生物ろ過槽を直列あるいは並列に連結すると共にその被
処理水の流路を変更できるように開閉弁及び管を配置
し、被処理水の通水時は前段の生物ろ過槽で浮遊物除
去、次段の生物ろ過槽で脱窒処理し、また次段の生物ろ
過槽を洗浄した後、被処理水の流路を洗浄された生物ろ
過槽を前段となるように変更し、以下所定時間毎に洗浄
操作にともなう同様の流路変更を行うことを特徴とする
生物ろ過方法。
1. A biological filtration method having a function of purifying treated water by an organic substance decomposing action and an adsorbing action of a biological film formed on the surface of a filter medium filled in the biological filtration tank, and having a function of washing the biological filtration tank. In, at least two biological filtration tanks are connected in series or in parallel, and on-off valves and pipes are arranged so that the flow path of the treated water can be changed. After removing suspended solids in the tank, denitrifying in the next-stage biological filtration tank, and cleaning the next-stage biological filtration tank, the flow path of the water to be treated was changed to the previous biological filtration tank. Then, the biological filtration method is characterized in that the same flow path change is carried out with a washing operation every predetermined time.
JP26343092A 1992-10-01 1992-10-01 Biological filtering method Pending JPH06114388A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26343092A JPH06114388A (en) 1992-10-01 1992-10-01 Biological filtering method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26343092A JPH06114388A (en) 1992-10-01 1992-10-01 Biological filtering method

Publications (1)

Publication Number Publication Date
JPH06114388A true JPH06114388A (en) 1994-04-26

Family

ID=17389395

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26343092A Pending JPH06114388A (en) 1992-10-01 1992-10-01 Biological filtering method

Country Status (1)

Country Link
JP (1) JPH06114388A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004031084A1 (en) * 2002-09-30 2004-04-15 Nippon Steel Chemical Co., Ltd. Method of removing nitrate nitrogen and device used for the method
FR2858316A1 (en) * 2003-08-01 2005-02-04 Suez Environnement DENITRIFICATION REACTOR WITH FIXED CULTURE
JP2006122874A (en) * 2004-11-01 2006-05-18 Hitachi Plant Eng & Constr Co Ltd Treatment method and apparatus for ammonia-containing liquid
CN104150597A (en) * 2014-08-27 2014-11-19 武汉大学 Anaerobic natural ventilation integrated composite vertical-flow biological water treatment filtering tank
CN108408821A (en) * 2018-05-02 2018-08-17 广东溢达纺织有限公司 Water purification railing
CN111186965A (en) * 2020-03-03 2020-05-22 安徽绿衡环保科技有限公司 Sewage upgrading and modifying method adopting ultra-high filtration speed denitrification biological filter system
CN112744911A (en) * 2021-01-11 2021-05-04 光大水务科技发展(南京)有限公司 Nitrogen release-free high-denitrification-rate shallow bed filter denitrification water treatment system and operation method thereof

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004031084A1 (en) * 2002-09-30 2004-04-15 Nippon Steel Chemical Co., Ltd. Method of removing nitrate nitrogen and device used for the method
FR2858316A1 (en) * 2003-08-01 2005-02-04 Suez Environnement DENITRIFICATION REACTOR WITH FIXED CULTURE
WO2005014493A1 (en) * 2003-08-01 2005-02-17 Suez Environnement Denitrification reactor with a fixed culture
US7390400B2 (en) 2003-08-01 2008-06-24 Suez Environnement Denitrification reactor with a fixed culture
JP2006122874A (en) * 2004-11-01 2006-05-18 Hitachi Plant Eng & Constr Co Ltd Treatment method and apparatus for ammonia-containing liquid
JP4645157B2 (en) * 2004-11-01 2011-03-09 株式会社日立プラントテクノロジー Method and apparatus for treating ammonia-containing liquid
CN104150597A (en) * 2014-08-27 2014-11-19 武汉大学 Anaerobic natural ventilation integrated composite vertical-flow biological water treatment filtering tank
CN108408821A (en) * 2018-05-02 2018-08-17 广东溢达纺织有限公司 Water purification railing
CN108408821B (en) * 2018-05-02 2024-04-30 广东溢达纺织有限公司 Water purifying railing
CN111186965A (en) * 2020-03-03 2020-05-22 安徽绿衡环保科技有限公司 Sewage upgrading and modifying method adopting ultra-high filtration speed denitrification biological filter system
CN112744911A (en) * 2021-01-11 2021-05-04 光大水务科技发展(南京)有限公司 Nitrogen release-free high-denitrification-rate shallow bed filter denitrification water treatment system and operation method thereof

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