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JP3242363B2 - Microbial carrier and method for purifying sewage using the same - Google Patents
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JP3242363B2 - Microbial carrier and method for purifying sewage using the same - Google Patents

Microbial carrier and method for purifying sewage using the same

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Publication number
JP3242363B2
JP3242363B2 JP10204798A JP10204798A JP3242363B2 JP 3242363 B2 JP3242363 B2 JP 3242363B2 JP 10204798 A JP10204798 A JP 10204798A JP 10204798 A JP10204798 A JP 10204798A JP 3242363 B2 JP3242363 B2 JP 3242363B2
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JP
Japan
Prior art keywords
sewage
present
carrier
treatment
tank
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
JP10204798A
Other languages
Japanese (ja)
Other versions
JPH10276777A (en
Inventor
森十 長谷川
鍾玉 韓
Original Assignee
株式会社資源生物研究所
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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

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  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Immobilizing And Processing Of Enzymes And Microorganisms (AREA)
  • Biological Treatment Of Waste Water (AREA)

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、微生物担体及びそれを
用いた汚水の浄化方法に関し、特に、汚泥の発生量を減
少させるのみならず汚水の処理効率を向上させることの
できる、微生物担体及びそれを用いた汚水の浄化方法に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a microorganism carrier and a method for purifying sewage using the same. More particularly, the present invention relates to a microorganism carrier capable of improving not only the amount of sludge generated but also the efficiency of sewage treatment. It relates to a method for purifying sewage using the same.

【0002】[0002]

【従来技術】従来から、有機性廃水処理としては、生物
学的処理が有効であることが知られており、特に活性汚
泥法が最も普遍的な方法として広く使用されている。し
かしながら、この活性汚泥法は、沈澱層における固形物
の沈澱性が良くなる反面、絲状菌の繁殖等に起因して汚
泥発生量が増加し、これに伴う汚泥処理費用が大きいと
いう欠点があった。
2. Description of the Related Art Hitherto, biological treatment has been known to be effective as an organic wastewater treatment, and in particular, activated sludge method is widely used as the most universal method. However, this activated sludge method has a disadvantage that, although the sedimentation of solids in the sedimentation layer is improved, the amount of sludge generated increases due to the growth of filamentous fungi and the associated sludge treatment cost is high. Was.

【0003】更に、この方法の場合には、廃水量、負荷
変動及び毒性物質等の流入などによる衝撃負荷現象によ
り、処理効率が著しく低下することが多い。これらの問
題点を解決するため、従来から、撒水濾床法及び回転円
板接触法等の汚水処理法が試みられているが、これらの
方法の何れにも、微生物が脱離したり、冬季に凍結する
という不都合が生ずる上、悪臭が発生するという欠点が
あっった。
Further, in the case of this method, the treatment efficiency is often remarkably reduced due to the impact load phenomenon due to the amount of wastewater, load fluctuation and inflow of toxic substances. To solve these problems, sewage treatment methods such as the sprinkling filter method and the rotating disk contact method have been tried in the past.However, in any of these methods, microorganisms are desorbed or in winter. In addition to the disadvantage of freezing, there is a drawback that odor is generated.

【0004】斯る欠点は、外面を多数の突出したループ
糸状集積体で構成した有芯又は中空芯の棒状体を螺旋状
に形成した螺旋状微生物単体(特開昭62−3784号
公報、同62−38294号公報)によって改善され
た。そこで、本発明者らは、この螺旋状微生物単体につ
いて更に検討したところ、前記ループ糸状集積体を、特
にアクリル繊維で構成させた場合には、特に有機廃水の
生物処理の効率が良くなる一方、アクリル繊維だけでは
腰が弱くそのループ形状を維持することが困難となるこ
とを見い出し、本発明に到達した。
[0004] Such a disadvantage is that a helical microorganism single body in which a cored or hollow core rod-shaped body composed of a large number of projecting loop-like filaments on the outer surface is spirally formed (Japanese Patent Application Laid-Open No. 62-3784, 1987). 62-38294). Therefore, the present inventors have further studied this single spiral microorganism, the loop filamentous aggregate, especially when constituted by acrylic fiber, while improving the efficiency of biological treatment of organic wastewater, The present inventors have found out that it is difficult to maintain the loop shape due to the weakness of the acrylic fiber alone and arrived at the present invention.

【0005】[0005]

【発明が解決しようとする課題】従って本発明の第1の
目的は、汚泥発生量を減少させるのみならず、微生物の
付着量を増大させ、有機廃水の生物処理を、従来以上
に、効率的に行わせることのできる微生物担体を提供す
ることにある。本発明の第2の目的は、微生物が脱離し
たり、冬季に凍結するという現象を防止することができ
るのみならず、嫌気性処理から好気性処理までの処理を
行い、汚泥発生量を減少させると共に悪臭の発生をも抑
制することのできる汚水の浄化方法を提供することにあ
る。
Accordingly, a first object of the present invention is not only to reduce the amount of sludge generated, but also to increase the amount of microorganisms attached, thereby making the biological treatment of organic wastewater more efficient than ever. It is an object of the present invention to provide a microorganism carrier which can be carried out by a microorganism carrier. A second object of the present invention is to not only prevent the phenomenon that microorganisms are detached or freeze in winter, but also reduce the amount of sludge generated by performing processes from anaerobic to aerobic. It is another object of the present invention to provide a method for purifying sewage that can also suppress generation of offensive odor.

【0006】[0006]

【課題を解決するための手段】本発明の上記の諸目的
は、ポリ塩化ビニリデン繊維及びアクリル繊維を、基幹
に多数のU字形ループを形成する如く植立せしめてなる
ことを特徴とする微生物担体によって達成された。
SUMMARY OF THE INVENTION The above objects of the present invention are attained by providing a microbial carrier characterized by comprising polyvinylidene chloride fibers and acrylic fibers planted so as to form a large number of U-shaped loops on a backbone. Achieved by

【0007】本発明の微生物担体は、基幹に、微生物を
担持する作用を有する繊維を横糸として多数U字状に固
定したものであり、その詳細は、特開昭62−3784
号に記載されている。基幹に植立され、U字状のループ
を形成する横糸として、本発明においては、特に、ポリ
塩化ビニリデン繊維とアクリル繊維を組み合せて使用す
る。
[0007] The microorganism carrier of the present invention is formed by fixing a large number of U-shaped fibers having a function of carrying microorganisms to the backbone thereof, as described in Japanese Patent Application Laid-Open No. Sho 62-3784.
No. In the present invention, in particular, poly- wefts are planted on the backbone and form U-shaped loops.
Use a combination of vinylidene chloride fiber and acrylic fiber.

【0008】これによって、1種の繊維を使用した場合
よりも微生物担持能力が増大し、汚水処理能力が高ま
る。アクリル繊維と組み合わせることが特に汚水の浄化
に有効であるということの理由は明らかではないが、ア
クリル繊維が適度の親水性を有することが一因ではない
かと推定される。
As a result, the ability to carry microorganisms is increased as compared with the case where one type of fiber is used, and the ability to treat sewage is enhanced. Although the reason that the combination with the acrylic fiber is particularly effective for purifying wastewater is not clear, it is presumed that one reason is that the acrylic fiber has appropriate hydrophilicity.

【0009】塩化ビニリデン繊維のみを横糸として使用
した微生物担体(以下、BMと略す)と、ポリ塩化ビニ
リデン繊維とアクリル繊維とを容量比で1/1となるよ
うに、両者を横糸に用いた微生物担体(以下、SMと略
す)とを比較すると、SMの方がBMよりも比表面積が
大きく、また、担体表面の凹凸が大きい。即ち、微生物
にとっては、SMの方が媒体表面に付着するのに有利な
条件を備えているということができ、実際、揮発性有機
物質の実際付着量も、後記する実施例で示される如く、
SMの場合の方がBMの場合よりも、驚くべきことに3
0〜64%程度も多い。
A microorganism carrier (hereinafter abbreviated as BM) using only vinylidene chloride fiber as the weft, and a microorganism using both the polyvinylidene chloride fiber and the acrylic fiber in the weft so that the volume ratio becomes 1/1. Comparing with a carrier (hereinafter abbreviated as SM), SM has a larger specific surface area than BM, and has more irregularities on the surface of the carrier. That is, for microorganisms, SM can be said to have more favorable conditions for adhering to the medium surface, and in fact, the actual adhering amount of volatile organic substances is also as shown in the examples described later.
Surprisingly, the case of SM was 3 more than that of BM.
There are many about 0 to 64%.

【0010】横糸の繊維径は、微生物担体の比表面積を
大きくするという観点からは、細いことが好ましいが、
製造技術、或いは実際の使用に際する糸切れを防止する
観点から、繊維径には自ら限度が生ずる。例えば、ポリ
塩化ビニリデン繊維の場合には、30〜100μm、ア
クリル及びナイロン繊維にあっては、1〜100μm、
特に5〜50μmの範囲とすることが好ましい。尚、横
糸と共に基幹を構成する縦糸の素材や繊維径について
は、特に限定されない。
[0010] The fiber diameter of the weft is preferably small from the viewpoint of increasing the specific surface area of the microorganism carrier.
From the viewpoint of manufacturing technology or preventing yarn breakage during actual use, the fiber diameter itself has its own limit. For example, in the case of polyvinylidene chloride fiber, 30 to 100 μm, and in the case of acrylic and nylon fiber, 1 to 100 μm,
In particular, the thickness is preferably in the range of 5 to 50 μm. The material and fiber diameter of the warp constituting the backbone together with the weft are not particularly limited.

【0011】本発明の微生物担体を用いて汚水を処理す
るに際しては、集水した汚水から先ず無機性SSや固形
物を除去することが好ましく、その後曝気によって、上
流から下流になるに従い、汚水中の溶存酸素量が多くな
るように調節することが好ましい。このようにすること
により、BODの減少のみならず、窒素分の除去も有効
になされる。
In treating sewage using the microorganism carrier of the present invention, it is preferable to first remove inorganic SS and solids from the collected sewage, and then, by aeration, the sewage proceeds from upstream to downstream. It is preferable to adjust the amount of dissolved oxygen to increase. By doing so, not only the BOD can be reduced but also the nitrogen content can be effectively removed.

【0012】従って、汚水処理装置は、少なくとも汚水
を集水する集水槽と、無機性SSや固形物を沈澱濾過す
る濾過槽と、空気を導入して溶存酸素を調整した曝気槽
とから構成される。そして、例えば、曝気槽を4区画に
分割し、1〜4番目の各区画の溶存酸素を上流側から順
次1、2、3、4ppmに調整し、各槽の滞留時間を総
計12時間程度として連続的に処理する。このようにす
ることによって、嫌気性処理から好気性処理まで、十分
な処理を行うことができる。
Therefore, the sewage treatment apparatus comprises at least a water collecting tank for collecting sewage, a filtration tank for precipitating and filtering inorganic SS and solids, and an aeration tank for introducing dissolved air to adjust dissolved oxygen. You. Then, for example, the aeration tank is divided into four sections, the dissolved oxygen in each of the first to fourth sections is sequentially adjusted to 1, 2, 3, 4 ppm from the upstream side, and the residence time in each tank is set to about 12 hours in total. Process continuously. By doing in this way, sufficient processing from anaerobic processing to aerobic processing can be performed.

【0013】尚、曝気槽の前に濾過槽を設けることは、
重く落下し易い無機物の付着を防止し、微生物の付着状
態を良好に保つ上で重要である。汚水処理の測定項目と
しては、pH、BOD、COD(Mn)、COD(C
r)、SS、リン濃度、窒素濃度及び界面活性剤濃度等
を採用することが好ましい。これらの測定項目の分析
は、適宜公知の方法によって行うことができる。
The provision of a filtration tank before the aeration tank is
It is important to prevent the attachment of inorganic substances that are heavy and easily fall, and to keep the adhesion state of microorganisms good. PH, BOD, COD (Mn), COD (C
It is preferable to employ r), SS, phosphorus concentration, nitrogen concentration, surfactant concentration and the like. The analysis of these measurement items can be appropriately performed by a known method.

【0014】[0014]

【発明の効果】本発明の微生物担体は、アクリル繊維
ポリ塩化ビニリデン繊維の2種の繊維を、基幹に、多数
のU字形ループを形成するように植立させているので、
微生物の付着状態が極めて良好であり、微生物の汚水処
理能力を最大限に活用することができ、これによって有
機廃水の生物処理を効率的に行わせることができる。
The microorganism carrier of the present invention comprises acrylic fiber and
Since two types of polyvinylidene chloride fibers are planted on the backbone to form a number of U-shaped loops,
The adhesion state of the microorganisms is extremely good, and the sewage treatment capacity of the microorganisms can be maximized, whereby the biological treatment of the organic wastewater can be efficiently performed.

【0015】また、本発明の汚水の浄化方法は、一般的
な活性汚泥法と異なり、2次沈澱槽、脱水設備、汚泥返
送設備及びその他の付帯設備を必要としないにもかかわ
らず、嫌気性処理から好気性処理まで十部に行うことが
できるので汚泥の発生量を従来より減らすことが出来る
上、悪臭の発生などを抑制することもできる。
Further, unlike the general activated sludge method, the method for purifying sewage of the present invention does not require a secondary sedimentation tank, a dewatering facility, a sludge return facility and other auxiliary facilities, but is anaerobic. Since the entire process from the treatment to the aerobic treatment can be performed, the amount of generated sludge can be reduced as compared with the conventional case, and the generation of offensive odor can be suppressed.

【0016】[0016]

【実施例】以下、本発明を実施例によって更に詳述する
が、本発明はこれによって限定されるものではない。
EXAMPLES The present invention will be described in more detail with reference to the following Examples, but it should not be construed that the invention is limited thereto.

【0017】実施例.図1は、基幹に多数のU字形ルー
プを形成する如く繊維a及び繊維bの2種の横糸を植立
せしめてなる、本発明の微生物担体の例であり、図2
は、図1の微生物担体1を曝気槽2内に充填して汚水処
理を行う場合の装置の1例を示す概略図である。
Embodiment 1 FIG. 1 shows an example of the microorganism carrier of the present invention in which two types of weft yarns of fiber a and fiber b are planted so as to form a large number of U-shaped loops on the backbone.
FIG. 2 is a schematic view showing an example of an apparatus in a case where the microorganism carrier 1 of FIG. 1 is filled in an aeration tank 2 to perform sewage treatment.

【0018】図2において、符号2は、微生物担体1を
充填した、それぞれ2つの反応槽5を有する、4つの部
室からなる曝気槽、3は集水槽、4は濾過槽、6はエア
ーブロアーである。微生物担体1は、水の回転を円滑に
するため、反応槽5の壁との間が最小10mmの間隔に
なるように充填され、曝気槽2の中心部下端に酸基石を
取付けてエアーブロアー6と連結させ、それぞれバルブ
7を設けて各反応槽に溶存する酸素量を調節した。
In FIG. 2, reference numeral 2 denotes an aeration tank composed of four compartments, each having two reaction tanks 5 filled with the microorganism carrier 1, reference numeral 3 denotes a water collecting tank, reference numeral 4 denotes a filtration tank, and reference numeral 6 denotes an air blower. is there. The microbial carrier 1 is filled so that the distance between the microbial carrier 1 and the wall of the reaction tank 5 is at least 10 mm in order to facilitate the rotation of water. And the amount of oxygen dissolved in each reaction tank was adjusted by providing valves 7 respectively.

【0019】濾過槽4で濾過された汚水は、管8を通し
て最初の反応槽5内に流入し、反応槽を通過する間に浄
化される。尚、反応槽5は互いに最小20mmの間隔が
あくように、また、曝気槽2に対して上下共、20mm
の空間が生ずるように設けられ、全ての反応槽内の水温
は、20±1℃を維持するようにした。
The sewage filtered in the filter tank 4 flows into the first reaction tank 5 through the pipe 8 and is purified while passing through the reaction tank. In addition, the reaction tank 5 should be spaced at least 20 mm from each other,
The water temperature in all the reaction vessels was maintained at 20 ± 1 ° C.

【0020】また、曝気槽2内の溶存酸素を、DO−メ
ーターを用いて随時測定し、その量を一定に維持させる
と共に、pH−メーターを用いて、水素イオン濃度を随
時測定した。各反応槽中の溶存酸素量は、上流側から下
流側に、順次1ppm、2ppm、3ppm及び4pp
mとなるように調節した。
Further, the dissolved oxygen in the aeration tank 2 was measured as needed using a DO-meter, and the amount was kept constant, and the hydrogen ion concentration was measured as needed using a pH-meter. The dissolved oxygen amount in each reaction vessel was 1 ppm, 2 ppm, 3 ppm and 4 pp from the upstream side to the downstream side in order.
m.

【0021】微生物担体として32.4リットルのSM
を用いて80日間汚水の連続処理を行った後、曝気槽か
ら、付着した微生物(汚泥)が落ちないように、充填さ
れた微生物担体を抜き出し、担体に付着された汚泥を一
定量の蒸留水中に洗い出した後、ドライオーブンに入れ
て103℃にて3〜4日間完全に乾燥させ、乾燥物の重
量を計った。
32.4 liters of SM as microbial carrier
After performing continuous treatment of sewage for 80 days using, the filled microorganism carrier is extracted from the aeration tank so that the attached microorganisms (sludge) do not fall off, and the sludge attached to the carrier is removed from a fixed amount of distilled water. Then, it was put in a dry oven and completely dried at 103 ° C. for 3 to 4 days, and the dried product was weighed.

【0022】次いでこの乾燥物を600−650℃で完
全に焼いた後、残存重量を測定し、両者の差異によって
微生物担体に付着した微生物量を測定した。この結果
は、曝気槽の第1室から、順次22.5g、24g、2
3.8g及び17.5gであり、第2室でその付着量が
最大であった。また、処理前後の水中のBOD及び窒素
濃度を測定したところ、BODの低下は90%、窒素除
去率は、インドール法で74%、ヘキサン抽出法で61
%であった。
Next, the dried product was completely baked at 600-650 ° C., the remaining weight was measured, and the amount of microorganisms adhering to the microorganism carrier was determined from the difference between the two. The results are as follows: 22.5 g, 24 g, 2 g
The weight was 3.8 g and 17.5 g, and the amount of adhesion was the largest in the second chamber. When the BOD and nitrogen concentrations in water before and after the treatment were measured, the BOD reduction was 90%, the nitrogen removal rate was 74% by the indole method, and 61% by the hexane extraction method.
%Met.

【0023】これに対し、微生物担体として40リット
ルのBMを用いた場合について全く同じ条件で汚水処理
を行い、同様にして各値を測定したところ、微生物の付
着量は、第1室から、順次、13.8g、18.5g、
16g及び12.5gと前記本発明の場合より少なく、
BODの低下は86%、窒素除去率は、インドール法で
64%、ヘキサン抽出法で52%であった。これらの結
果は、本発明の微生物担体の有効性、及び、本発明の汚
水の浄化方法によって嫌気性処理から好気性処理まで充
分に行われることを実証するものである。
On the other hand, when 40 liters of BM was used as a microorganism carrier, sewage treatment was performed under exactly the same conditions, and the respective values were measured in the same manner. , 13.8 g, 18.5 g,
16 g and 12.5 g, which are less than in the case of the present invention,
The BOD reduction was 86%, and the nitrogen removal rate was 64% by the indole method and 52% by the hexane extraction method. These results demonstrate the effectiveness of the microbial carrier of the present invention and that the method for purifying sewage of the present invention sufficiently performs from anaerobic treatment to aerobic treatment.

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

【図1】図1は、基幹に多数のU字形ループを形成する
如く、2種の繊維を植立せしめてなる本発明の微生物担
体の概略図である。
FIG. 1 is a schematic diagram of a microorganism carrier of the present invention in which two types of fibers are planted so as to form a large number of U-shaped loops on a backbone.

【図2】図2は、本発明の汚水処理を行うための、装置
の1例を示す概略図である。
FIG. 2 is a schematic view showing one example of an apparatus for performing the sewage treatment of the present invention.

【符号の説明】[Explanation of symbols]

1 微生物担体 2 曝気槽 3 集水槽 4 濾過槽 5 反応槽 6 エアーブロアー 7 バルブ 1 Microbial carrier 2 Aeration tank 3 Water collecting tank 4 Filtration tank 5 Reaction tank 6 Air blower 7 Valve

フロントページの続き (51)Int.Cl.7 識別記号 FI C12M 1/40 C12M 1/40 Z (58)調査した分野(Int.Cl.7,DB名) C12N 11/08 C02F 3/00 - 3/10 C12M 1/40 Continuation of the front page (51) Int.Cl. 7 identification code FI C12M 1/40 C12M 1/40 Z (58) Field surveyed (Int.Cl. 7 , DB name) C12N 11/08 C02F 3/00-3 / 10 C12M 1/40

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 ポリ塩化ビニリデン繊維及びアクリル繊
維を、基幹に多数のU字形ループを形成する如く植立せ
しめてなることを特徴とする微生物担体。
1. A microbial carrier comprising polyvinylidene chloride fibers and acrylic fibers planted so as to form a large number of U-shaped loops on a backbone.
【請求項2】 U字形ループを形成する繊維の繊維径が
1〜100μmである請求項1に記載された微生物担
体。
2. The fiber diameter of a fiber forming a U-shaped loop is
The microorganism carrier according to claim 1, which has a thickness of 1 to 100 μm.
body.
JP10204798A 1998-03-30 1998-03-30 Microbial carrier and method for purifying sewage using the same Expired - Fee Related JP3242363B2 (en)

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Related Parent Applications (1)

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JP9196993A Division JP3242198B2 (en) 1993-03-26 1993-03-26 Purification method of sewage using microbial carrier

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JP3242363B2 true JP3242363B2 (en) 2001-12-25

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Publication number Priority date Publication date Assignee Title
WO2000049140A2 (en) * 1999-02-19 2000-08-24 Vyzkumny Ústav Pivovarsky A Sladarsky A.S. Carrier of biomass, method of fermentation therewith and devices therefor
KR100439661B1 (en) * 2001-07-11 2004-07-12 곽종운 A microorganism media and method thereof
KR20040000115A (en) * 2002-06-24 2004-01-03 주식회사 동우기업 The system and method sewage and waste water for use a dipnoan netting
KR100464112B1 (en) * 2002-10-17 2005-01-03 (주)담덕 Fixed porous filtering media and manufacturing method the same
JP4836420B2 (en) * 2003-08-06 2011-12-14 旭化成クリーン化学株式会社 Fiber contact material, water treatment apparatus and water treatment method
JP2008006388A (en) * 2006-06-30 2008-01-17 Kankyo Protect:Kk Sewage cleansing system
JP2012045536A (en) * 2010-08-25 2012-03-08 Ando Mitsuo Sewage treatment tank using microbe carrier and sludge suppression
JP2012125741A (en) * 2010-12-17 2012-07-05 Komatsu Seiren Co Ltd Water purification material
JP2013034960A (en) * 2011-08-09 2013-02-21 Komatsu Seiren Co Ltd Water purification apparatus and water purification method
JP5431437B2 (en) * 2011-10-26 2014-03-05 東西化学産業株式会社 Organic wastewater treatment equipment
CN102515359B (en) * 2011-12-29 2013-03-20 武汉理工大学 Preparation method of natural hollow netty plant solid carbon source for bio-denitrification
CN107381789A (en) * 2017-09-13 2017-11-24 北京工业大学 Based on netted net cylinder nano carbon fiber adhesive substrate water treatment filler

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