JPH0523686A - Packing for treating waste water and treatment of waste water utilizing the packing - Google Patents

Packing for treating waste water and treatment of waste water utilizing the packing

Info

Publication number
JPH0523686A
JPH0523686A JP3030389A JP3038991A JPH0523686A JP H0523686 A JPH0523686 A JP H0523686A JP 3030389 A JP3030389 A JP 3030389A JP 3038991 A JP3038991 A JP 3038991A JP H0523686 A JPH0523686 A JP H0523686A
Authority
JP
Japan
Prior art keywords
waste water
fibers
packing
treatment
bod
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
JP3030389A
Other languages
Japanese (ja)
Inventor
Hajime Ogishima
一 荻島
Yasuyuki Hayano
靖之 早野
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP3030389A priority Critical patent/JPH0523686A/en
Publication of JPH0523686A publication Critical patent/JPH0523686A/en
Pending legal-status Critical Current

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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)
  • Filtering Materials (AREA)

Abstract

PURPOSE:To increase efficiency in treating waste water, to prevent the generation of sludge and to enhance the BOD removal rate by extruding a heated and melted thermoplastic resin from a nozzle into fibers, piling up the curled fibers, welding the mutual contacts to integrate the fibers and using the obtained porous material to treat waste water. CONSTITUTION:A thermoplastic resin is heated, melt-extruded from a nozzle into fibers, the curled fibers are piled up, the mutual contacts of the fibers are welded, hence the fibers are integrated to give a porous material, and a packing for treating waste water is formed from the porous material. The packing is charged into an aeration tank with the apparent volume of 40-70% and the BOD volumetric load of 0.15-1.20kg BOD/m<3> D. A PP resin which is lightweight and mechanically tough is used as the raw material. The packing 1 is filled in a raw water storage tank 12 and aeration is carried out, and the load of the aeration tank by the standard activated sludge process is reduced and stabilized.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】本発明は、排水処理用の充填材及びそれを
利用した接触曝気法による排水処理方法に関する。
The present invention relates to a wastewater treatment filler and a wastewater treatment method by a contact aeration method using the same.

【0002】[0002]

【従来技術】排水処理の方法としては、古くから用いら
れていた石、プラスチック等の支持体に固定する散水濾
床法の他、現在普及している活性汚泥法がある。活性汚
泥法における最大の問題点は、活性な沈降性のよい汚泥
の維持管理にあり、ほとんどの装置でこの管理に大きな
エネルギーを消耗しているが、それでもなおバルキング
(膨化)や分散の現象がよく起こり、汚泥の流出と、そ
れに伴う処理水の悪化がしばしば認められている。
2. Description of the Related Art As a method of treating waste water, there is a sprinkling filter method which has been used for a long time to fix it to a support such as stone or plastic, and an activated sludge method which is now popular. The biggest problem in the activated sludge method is the maintenance of the activated sludge with good sedimentation property, and most of the equipment consumes a lot of energy for this management, but the phenomenon of bulking (expansion) and dispersion is still present. It often occurs, and sludge outflow and accompanying deterioration of treated water are often observed.

【0003】この活性汚泥法の問題点を改善するため
に、液中に浮遊している汚泥を固定する試みが古くから
なされており、固定体として竹や木の小枝を入れるも
の、プラスチックネットを入れるもの、さらには固定体
を回転させて空中の酸素と接触させる回転円板法(RB
C、BIO−SURF)などとも提案され、実用化され
ているものもある。しかし、これらの試みはまだ、充分
に従来の方法の問題点を改善しているとは言えず、新規
な方法が望まれていた。
In order to improve the problems of this activated sludge method, attempts have been made for a long time to fix the sludge floating in the liquid, such as a fixed body containing bamboo or tree twigs or a plastic net. The rotating disk method (RB) in which the container and the fixed body are rotated to contact oxygen in the air
C, BIO-SURF) and the like have been proposed and put into practical use. However, these attempts have not yet sufficiently improved the problems of the conventional methods, and new methods have been desired.

【0004】[0004]

【課題を解決するための手段】本発明者らは、このよう
な従来の方法の短所を克服するため、好適な微生物体
(汚泥)の固定体として種々研究、実験を繰り返した結
果、熱可塑性合成樹脂を加熱溶融してノズルより押し出
し、繊篠としたものをカールさせたまま積み重ね、繊篠
の相互接点を溶着成形して一体化したポーラス材を用い
ると、BOD除去率が高く、汚泥管理の必要もなく、余
剰汚泥の引き抜きも不要となることを見出し、本発明を
完成させた。
In order to overcome such disadvantages of the conventional methods, the present inventors repeated various studies and experiments as a suitable microbial cell (sludge) immobilization material, and as a result, thermoplasticity was improved. When the synthetic resin is heated and melted and extruded from the nozzle, piled up while curling the Shinoshino, and using the porous material integrated by fusion molding the mutual contacts of Shinoshino, the BOD removal rate is high and sludge management The present invention has been completed based on the finding that there is no need to remove the excess sludge and there is no need to remove excess sludge.

【0005】即ち、本発明は、熱可塑性樹脂を加熱溶融
してノズルより押し出し、繊篠としたものをカールさせ
たまま積み重ね、繊篠の相互接点を溶着成型して一体化
したポーラス材からなる排水処理用充填材からなる。本
発明は、さらに、BOD容積負荷0.15〜1.20K
gBOD/m3 ・Dの範囲内で、曝気槽内へ、前記の排
水処理用充填材を前記槽に対してみかけ容積で40〜7
0%を投入することを特徴とする接触曝気法による排水
処理方法からなる。
That is, the present invention comprises a porous material in which a thermoplastic resin is heated and melted and extruded from a nozzle, and the fibrous pieces are stacked while curled and the mutual contact points of the fibrous pieces are fusion-molded and integrated. Consists of a filler for wastewater treatment. The present invention further provides a BOD volume load of 0.15 to 1.20K.
Within the range of gBOD / m 3 · D, the above-mentioned wastewater treatment filler is introduced into the aeration tank in an apparent volume of 40 to 7 with respect to the tank.
It consists of a wastewater treatment method by a contact aeration method, which is characterized by inputting 0%.

【0006】本発明の排水処理用充填材は、ハニカム状
のもの、偏平な形のもの、円筒状のもの等種々の形状を
有することができる。原料としては、熱可塑性樹脂の中
でも、最も軽量でかつ機械的に強靭であり、さらに水中
で変質したり、可塑剤を含まず、水中に有機物等の有害
物を溶出することがないポリプロピレン樹脂が好適に用
いられる。これらの樹脂は、酸及びアルカリ有機溶剤な
どに対し、極めて強い抵抗性を有している。
The waste water treatment filler of the present invention can have various shapes such as a honeycomb shape, a flat shape, and a cylindrical shape. As a raw material, among the thermoplastic resins, polypropylene resin, which is the lightest and mechanically tough, and which is further altered in water or does not contain a plasticizer and does not elute harmful substances such as organic substances in water. It is preferably used. These resins have extremely strong resistance to acids and alkaline organic solvents.

【0007】また、本願発明の排水処理用充填剤の空隙
率は、繊篠の密度により相違するが、80〜98%であ
る。このように空隙率が大きいため、曝気槽の有効容量
をあまり減少させない。繊篠の直径は、約1〜2mm程
度であり、比重は約0.93程度で、嵩比重は形状、繊
篠密度によって異なる。またその圧縮強度は高く、通常
の水処理用剤としての使用条件下ではほとんど変形しな
いようになっている。また、荷重が極めて大きいとき
は、繊篠密度によって異なるが、一般的に変形するとし
ても、直線変形であり、復元性が極めて大きい。
The porosity of the waste water treatment filler of the present invention is 80 to 98%, although it varies depending on the density of the fiber. Since the porosity is large as described above, the effective capacity of the aeration tank is not reduced so much. The diameter of the fiber is about 1 to 2 mm, the specific gravity is about 0.93, and the bulk specific gravity depends on the shape and the fiber density. Further, its compressive strength is high, and it hardly deforms under the conditions of use as a usual water treatment agent. Further, when the load is extremely large, although it varies depending on the density of fibers, it is generally a linear deformation even if it is deformed, and the recoverability is extremely large.

【0008】本発明の排水処理用充填材は、上記熱可塑
性合成樹脂を加熱溶融してノズルより押し出し、繊篠と
したものをカールさせたまま積み重ね、繊篠の相互接点
を溶着成型して一体化して製造することができる。この
ように相互接点を溶着成型するために、細菌等の作用に
よって剥離することもない。接着剤によって、一体化し
たものは、接着層が細菌の作用によって剥離することが
多く、不安定である。
The waste water treatment filler of the present invention is formed by heating and melting the above-mentioned thermoplastic synthetic resin and extruding from a nozzle, stacking the fibrous products in a curled state, and welding and molding the mutual contact points of the fibrous products. Can be manufactured. Since the mutual contact points are formed by welding as described above, they are not separated by the action of bacteria or the like. The one integrated with an adhesive is unstable because the adhesive layer is often peeled off by the action of bacteria.

【0009】また、本発明の排水処理用充填材の繊篠構
造は極めて不規則に褶曲しているため、処理排水の前記
充填材表面における流れは複雑多岐であり、微生物の付
着に適した部分が多量に生じ、従って、それらの部分に
おいて微生物の付着生育が始まり、次第に付近に拡散付
着していき、様々な処理水の条件下においても容易に微
生物が付着生育する。規則正しい網目状等の充填材は作
り出される条件が画一的であるため、微生物が付着しに
くい場合が多い。本発明の排水処理充填材は、その網目
に汚泥の生物膜が発生し、そこに好気性及び嫌気性の細
菌が繁殖して、有機及び無機物質の分解作用及び自己消
化作用が行われるため、汚泥の発生がない。
Further, since the fibrous structure of the filler for wastewater treatment of the present invention has an extremely irregular fold, the flow of the treated wastewater on the surface of the filler is complicated and diversified, and a portion suitable for the attachment of microorganisms. Therefore, the microorganisms start to adhere and grow in these parts, and gradually diffuse and adhere to the vicinity, and the microorganisms easily adhere and grow even under various treated water conditions. Since a regular mesh-like filler is produced under uniform conditions, it is often difficult for microorganisms to adhere to it. Wastewater treatment filler of the present invention, a biofilm of sludge is generated in the mesh, aerobic and anaerobic bacteria propagate there, because the decomposition action and self-digestion action of organic and inorganic substances is performed, No sludge is generated.

【0010】本発明の排水処理用充填材は、BOD容積
負荷0.15〜1.50KgBOD/m3 ・Dの範囲内
で、曝気層内へみかけ容積として40〜60%、投入さ
れる。曝気量は、使用する通気装置、有効水深、酸素利
用効率によって多少相違があるが、基本的には、下記式
により算出することができる。 空気量(Nm3 /D)=(原水B O D −処理水B O D
P P M ×流水原水量m3 /D×120 即ち、目処としては、kgBOD除去量当たり120倍
Nm3 の空気が吹き込まれるという条件となる。
The waste water treatment filler of the present invention is added in an apparent volume of 40 to 60% within the aeration layer within a BOD volume load of 0.15 to 1.50 KgBOD / m 3 · D. The amount of aeration varies somewhat depending on the ventilation device used, effective water depth, and oxygen utilization efficiency, but basically it can be calculated by the following formula. Air volume (Nm 3 / D) = (raw water BOD -treated water BOD )
PPM × raw water flow rate m 3 / D × 120 That is, the condition is that 120 times Nm 3 of air is blown in per kgBOD removal amount.

【0011】本願発明の方法は、排水の二次及び三次、
高度三次処理用にも好適に使用することができる(添付
の図1及び図2参照)。二次及び三次処理、高度三次用
に使用することによって、余剰汚泥の減少、動力費の低
減、処理水質の安定向上、負荷変動や毒物物質混入に対
する安定性の増大に寄与することができる。また本願発
明の充填材は、原水貯留槽に充填して曝気することによ
り、標準的活性汚泥法による曝気槽の負荷の低減並びに
安定化を図ることができる(図3参照)。また本発明の
充填材は、立体網状ろ材であるため、気液接触処理にお
いても非常に効果的に作用し、ガス洗浄、脱臭塔の悪臭
除去、冷却塔等に有効に使用することができる(図4参
照)。また、回転円板方式における回転体に用いると、
回転体の軽量化、低価格化、除去率向上等を図ることが
できる(図5参照)。さらに、河川その他の大量の流水
浄化にも適している(図6参照)。
According to the method of the present invention, the secondary and tertiary drainage water,
It can also be suitably used for advanced tertiary treatment (see attached FIGS. 1 and 2). By using for secondary and tertiary treatment and advanced tertiary treatment, it is possible to contribute to reduction of excess sludge, reduction of power cost, stable improvement of treated water quality, and increase of stability against load fluctuation and contamination of toxic substances. Further, by filling the raw water storage tank with the filler of the present invention and performing aeration, the load on the aeration tank can be reduced and stabilized by the standard activated sludge method (see FIG. 3). Further, since the packing material of the present invention is a three-dimensional reticulated filter material, it acts very effectively even in the gas-liquid contact treatment, and can be effectively used for gas cleaning, removal of offensive odors in deodorization towers, cooling towers and the like ( (See FIG. 4). Also, when used for a rotating body in the rotating disk system,
It is possible to reduce the weight and cost of the rotating body and improve the removal rate (see FIG. 5). Furthermore, it is also suitable for the purification of large amounts of running water such as rivers (see Fig. 6).

【0012】[0012]

【実施例】以下、実施例により本発明をさらに詳しく説
明する。 実施例1 下記組成を有する合成下水を用いて、No.1(活性汚
泥法)、No.2(本発明の充填材を円筒状として処理
槽に36容量%投入して本発明を実施)及びNo.3
(本発明の充填材をマット状として処理槽に67容量%
投入して本発明を実施)の方法により、排水処理(二次
処理)を行った。温度は室温(17〜23℃)として行
った。
The present invention will be described in more detail with reference to the following examples. Example 1 Using synthetic sewage having the following composition, No. No. 1 (activated sludge method), No. 1 No. 2 (the present invention was carried out by putting the filler of the present invention in a cylindrical shape into a processing tank by 36% by volume) and No. Three
(67% by volume of the filler of the present invention in a treatment tank as a mat
Wastewater treatment (secondary treatment) was carried out by the method of charging and implementing the present invention). The temperature was room temperature (17 to 23 ° C.).

【0013】合成下水の組成(ppm) ペプトン 100 牛肉エキス 70 KH2 PO4 8 NaCl 20 NH4 Cl 50 FeCl3 ・6H2 O 5 グルコース 150(100) 酢酸ソーダ 200(150) Na2 HPO4 ・12H2 O 50 KCl 10 MgSO4 7 上記の成分を水道水に溶解し、pHを7.0〜7.2に調
整し、毎日新たに調整した。( )内の濃度は滞留時間
が24時間の場合にのみ使用した。
[0013] The composition of the synthetic waste water (ppm) peptone 100 beef extract 70 KH 2 PO 4 8 NaCl 20 NH 4 Cl 50 FeCl 3 · 6H 2 O 5 glucose 150 (100) sodium acetate 200 (150) Na 2 HPO 4 · 12H 2 O 50 KCl 10 MgSO 4 7 The above components were dissolved in tap water, the pH was adjusted to 7.0 to 7.2, and freshly adjusted every day. The concentrations in parentheses were used only when the residence time was 24 hours.

【0014】結果を下記の表1に示す。The results are shown in Table 1 below.

【0015】[0015]

【表1】 [Table 1]

【0016】[0016]

【発明の効果】以上、詳しく説明したように、本発明の
排水処理用充填材を使用して、排水処理すると、排水処
理率が極めて高く、汚泥は発生せず、BOD除去率は9
9.5〜100%にも及ぶ。また、本発明によれば、活
性汚泥法に於ける場合のように多量の高圧空気を必要と
せず、排水を網目構造に対して静かに回転させることと
各槽を自然流下させることができるので、運転管理が楽
で、ランニングコストも大幅に減少することができる。
As described above in detail, when the wastewater treatment filler of the present invention is used to perform wastewater treatment, the wastewater treatment rate is extremely high, no sludge is generated, and the BOD removal rate is 9%.
It reaches 9.5 to 100%. Further, according to the present invention, a large amount of high-pressure air is not required as in the case of the activated sludge method, the drainage can be gently rotated with respect to the mesh structure, and each tank can be naturally flowed down. The operation management is easy and the running cost can be greatly reduced.

【0017】また、本発明の方法によれば、排水がアル
カリ性になり、湖沼河川の環境をを悪化する恐れもな
い。
Further, according to the method of the present invention, drainage becomes alkaline and there is no fear of deteriorating the environment of lakes and rivers.

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

【図1】図1は、本発明を排水の二次及び三次処理用に
用いた場合の処理槽を示す図である。
FIG. 1 is a view showing a treatment tank when the present invention is used for secondary and tertiary treatment of waste water.

【図2】図2は、本発明を排水の高度三次処理用に用い
た場合の処理槽を示す図である。
FIG. 2 is a diagram showing a treatment tank when the present invention is used for advanced tertiary treatment of wastewater.

【図3】図2は、本発明を原水貯留槽に用いた場合の処
理槽を示す図である。
FIG. 2 is a diagram showing a treatment tank when the present invention is used as a raw water storage tank.

【図4】図4は、本発明を気液接触処理に用いた場合の
処理槽を示す図である。
FIG. 4 is a diagram showing a processing tank when the present invention is used for gas-liquid contact processing.

【図5】図5は、本発明を回転円板方式における回転体
に用いた場合を示す図である。
FIG. 5 is a diagram showing a case where the present invention is applied to a rotating body in a rotating disk system.

【図6】図6は、本発明を河川の流水浄化に用いた場合
を示す図である。 1・・本発明の充填材 2・・二次処理槽 3・・
三次処理槽 4・・原水 5・・処理水 6・・
架台 7・・散気管 8・・逆洗用空気 9・・
洪水時の水路 10・・取り外し蓋 11・・高度三次処理槽 12・・原水貯留槽 13・・気液接触処理槽 14・・回転体
FIG. 6 is a diagram showing a case where the present invention is used for purifying running water in a river. 1 ... Filler of the present invention 2 ... Secondary treatment tank 3 ...
Tertiary treatment tank 4 ... Raw water 5 ... Treated water 6 ...
Stand 7 ... Air diffuser 8 ... Backwashing air 9 ...
Water channel 10 at the time of flooding ··· Removal lid 11 · · Advanced tertiary treatment tank 12 · · Raw water storage tank 13 · · Gas-liquid contact processing tank 14 · · Rotating body

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 熱可塑性樹脂を加熱溶融してノズルより
押し出し、繊篠としたものをカールさせたまま積み重
ね、繊篠の相互接点を溶着成型して一体化したポーラス
材からなる排水処理用充填材。
1. A drainage treatment filling comprising a porous material in which thermoplastic resin is heated and melted and extruded from a nozzle, and the fibrous products are stacked while curled, and the mutual contact points of the fibrous products are fusion-molded and integrated. Material.
【請求項2】 BOD容積負荷0.15〜1.20Kg
BOD/m3 ・Dの範囲内で、曝気槽内へ、請求項1の
排水処理用充填材を前記槽に対してみかけ容積で40〜
70%を投入することを特徴とする接触曝気法による排
水処理方法。
2. BOD volume load 0.15 to 1.20 Kg
Within the range of BOD / m 3 · D, the waste water treatment filler according to claim 1 is introduced into the aeration tank in an apparent volume of 40 to 40.
A wastewater treatment method by the contact aeration method, which is characterized by adding 70%.
JP3030389A 1991-02-25 1991-02-25 Packing for treating waste water and treatment of waste water utilizing the packing Pending JPH0523686A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3030389A JPH0523686A (en) 1991-02-25 1991-02-25 Packing for treating waste water and treatment of waste water utilizing the packing

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3030389A JPH0523686A (en) 1991-02-25 1991-02-25 Packing for treating waste water and treatment of waste water utilizing the packing

Publications (1)

Publication Number Publication Date
JPH0523686A true JPH0523686A (en) 1993-02-02

Family

ID=12302557

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JPH0523686A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009119696A1 (en) * 2008-03-24 2009-10-01 Kureha Engineering Co., Ltd. Process for producing shaped contact-filtration member, shaped contact-filtration member, filtration apparatus, and method of processing soiled water
WO2011102262A1 (en) * 2010-02-16 2011-08-25 株式会社クレハエンジニアリング Contact filter medium compact, production method therefor, and filtration device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5289239A (en) * 1976-01-21 1977-07-26 Tadaki Morimura Method of treating waste water

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5289239A (en) * 1976-01-21 1977-07-26 Tadaki Morimura Method of treating waste water

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009119696A1 (en) * 2008-03-24 2009-10-01 Kureha Engineering Co., Ltd. Process for producing shaped contact-filtration member, shaped contact-filtration member, filtration apparatus, and method of processing soiled water
WO2011102262A1 (en) * 2010-02-16 2011-08-25 株式会社クレハエンジニアリング Contact filter medium compact, production method therefor, and filtration device

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