JP3241645B2 - Advanced treatment of wastewater - Google Patents

Advanced treatment of wastewater

Info

Publication number
JP3241645B2
JP3241645B2 JP26986997A JP26986997A JP3241645B2 JP 3241645 B2 JP3241645 B2 JP 3241645B2 JP 26986997 A JP26986997 A JP 26986997A JP 26986997 A JP26986997 A JP 26986997A JP 3241645 B2 JP3241645 B2 JP 3241645B2
Authority
JP
Japan
Prior art keywords
treatment
wastewater
subjected
biofilm
anaerobic
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
JP26986997A
Other languages
Japanese (ja)
Other versions
JPH11104692A (en
Inventor
宏 山田
徳彦 平野
牧克 高橋
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.)
Teijin Ltd
Original Assignee
Teijin 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 Teijin Ltd filed Critical Teijin Ltd
Priority to JP26986997A priority Critical patent/JP3241645B2/en
Publication of JPH11104692A publication Critical patent/JPH11104692A/en
Application granted granted Critical
Publication of JP3241645B2 publication Critical patent/JP3241645B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Biological Treatment Of Waste Water (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、生活排水、食品排
水等の有機排水の高次処理、窒素成分の高次除去に適し
た排水の高次処理方法に関する。
The present invention relates to a high-order treatment of organic wastewater such as domestic wastewater and food wastewater, and a high-order treatment of wastewater suitable for high-order removal of nitrogen components.

【0002】[0002]

【従来の技術】高濃度生活排水(下水)、有機工業排水
等の有機排水の処理方法としては、古くは活性汚泥法、
近時は粒状担体に微生物を付着させ生物処理と同時に濾
過を行う生物濾過法に代表される浮遊生物懸濁法、接触
材の表面に生物膜を形成処理する生物膜法、微生物を包
括固定した担体を用いる包括固定生物膜法あるいは微生
物自身が粒体を形成する自己造粒生物膜法等の生物処理
方法が使用されている。
2. Description of the Related Art As a method of treating organic wastewater such as high-concentration domestic wastewater (sewage) and organic industrial wastewater, an activated sludge method,
In recent years, a suspended organism suspension method typified by a biological filtration method in which microorganisms are attached to a granular carrier and filtration is performed simultaneously with biological treatment, a biofilm method in which a biofilm is formed on the surface of the contact material, and microorganisms are comprehensively fixed. Biological treatment methods such as an inclusive immobilized biofilm method using a carrier or a self-granulating biofilm method in which microorganisms themselves form granules are used.

【0003】従来、特に下水処理に関しては、接触材を
用いた接触酸化生物膜法が採用されてきているが、処理
速度が比較的遅い、生物膜の剥落、逆洗が必要といった
問題から、近時、活性汚泥法に代表される浮遊生物法が
採用されることが多い。しかし、この浮遊微生物法では
窒素成分の除去いわゆる脱窒が困難で、排水の高次処理
ができないといった問題がある。従って、高次処理に対
しては、種々の変法(嫌気・好気回分式活性汚泥法、嫌
気・好気活性汚泥法)が開発されているが、十分な脱窒
効果が得られない上、管理が煩瑣という問題がある。
Conventionally, especially for sewage treatment, a contact oxidation biofilm method using a contact material has been adopted. However, due to problems such as a relatively slow treatment speed, peeling of the biofilm, and necessity of backwashing, there is a problem. At times, the floating organism method represented by the activated sludge method is often employed. However, the suspended microorganism method has a problem that it is difficult to remove nitrogen components, that is, denitrify, and it is not possible to perform high-order treatment of wastewater. Therefore, various modified methods (anaerobic / aerobic batch activated sludge method, anaerobic / aerobic activated sludge method) have been developed for high-order treatment, but a sufficient denitrification effect cannot be obtained. However, there is a problem that management is complicated.

【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
従来技術の問題点を解決した新たな排水の高次処理方
法、特に脱窒性能に優れた方法を提供するものである。
SUMMARY OF THE INVENTION The present invention is to provide a new high-order treatment method for wastewater, especially a method excellent in denitrification performance, which solves the above-mentioned problems of the prior art.

【0005】[0005]

【課題を解決するための手段】本発明は、排水の生物処
理方法において、好気的生物処理した一次処理水を、炭
素繊維を接触材とした嫌気的生物膜処理で脱窒処理する
ことを特徴とする排水の高次処理方法である。
SUMMARY OF THE INVENTION The present invention relates to a method for treating wastewater, comprising the steps of denitrifying primary treated water subjected to aerobic biological treatment by anaerobic biofilm treatment using carbon fiber as a contact material. This is a high-level treatment method for wastewater.

【0006】[0006]

【発明の実施の形態】以下、本発明の一例に基づき発明
の作用、効果を説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The operation and effects of the present invention will be described below based on an example of the present invention.

【0007】図は、本発明方法の一例の簡略化したフロ
ーシートである。
FIG. 1 is a simplified flow sheet of an example of the method of the present invention.

【0008】図に於いて、1は、排水の前処理装置で被
処理水中の固形夾雑物などを除去するスクリーン装置、
必要に応じて流量を調整する流量調整槽等からなり、排
水の性状に応じて適宜の装置により排水の前処理を行
う。2は活性汚泥処理等の浮遊生物処理を行う曝気槽、
3は沈澱槽で曝気槽2からの処理水の固液分離を行い、
上澄水を次の槽に送り、底部の汚泥は曝気槽2に返送す
る。4は炭素繊維条を設置した嫌気濾床槽、5は沈澱
槽、滅菌槽等からなる後処理装置で、放流あるいは再利
用に要求される適宜の後処理を行う。
In the drawing, reference numeral 1 denotes a screen device for removing solid impurities and the like in the water to be treated by a wastewater pretreatment device;
It consists of a flow control tank or the like that adjusts the flow rate as necessary, and performs a pretreatment of the drainage by an appropriate device according to the properties of the drainage. 2 is an aeration tank that performs floating organism treatment such as activated sludge treatment,
3 is a sedimentation tank for solid-liquid separation of the treated water from the aeration tank 2;
The supernatant water is sent to the next tank, and the sludge at the bottom is returned to the aeration tank 2. Reference numeral 4 denotes an anaerobic filter bed tank provided with carbon fiber strips, and reference numeral 5 denotes a post-treatment device comprising a sedimentation tank, a sterilization tank, and the like, which performs an appropriate post-treatment required for discharge or reuse.

【0009】排水の処理開始に当たっては、従来の活性
汚泥法と同じく種汚泥を曝気槽2に投入し必要な期間、
排水を曝気槽2、嫌気濾床槽4を循環させつつ馴養を行
う。この場合、嫌気濾床槽4も好気的条件で馴養し、生
物膜を形成後嫌気化すると汚泥の馴養が短期間で行うこ
とができる。炭素繊維接触材の場合、この方法をとって
も汚泥の剥落が生じない。馴養の結果、排水の性状に対
応した微生物相が各槽内に保持され、好気性処理により
生物酸化が行われSS、BOD成分が除去され、生物酸化に
よりSS、BOD成分が処理された排水(一次処理水)は、次
いで、沈澱槽3で固液分離され、上澄水は、炭素繊維条
を設置した嫌気濾床槽4に導かれ、炭素繊維条に形成さ
れた嫌気性生物膜による脱窒処理(二次処理、高次処
理)を受け、後処理装置5により必要な後処理を受けた
後放流、あるいは再利用される。なお、曝気槽2(浮遊
生物処理槽)には沈澱槽3からの汚泥の一部を返送し、
槽内MLSSを所定のレベルに維持する。
When starting the treatment of the wastewater, seed sludge is introduced into the aeration tank 2 in the same manner as in the conventional activated sludge method,
The acclimatization is performed while circulating the waste water through the aeration tank 2 and the anaerobic filter bed tank 4. In this case, the anaerobic filter bed tank 4 is also acclimated under aerobic conditions, and if the biofilm is formed and then anaerobic, acclimation of the sludge can be performed in a short period of time. In the case of a carbon fiber contact material, sludge does not peel off even if this method is used. As a result of acclimation, the microflora corresponding to the properties of the wastewater is retained in each tank, biological oxidation is performed by aerobic treatment, and SS and BOD components are removed. The primary treated water is then separated into solid and liquid in a settling tank 3, and the supernatant water is guided to an anaerobic filter bed tank 4 provided with carbon fiber strips, and denitrified by an anaerobic biofilm formed on the carbon fiber strips. After being subjected to the processing (secondary processing, high-order processing), and subjected to necessary post-processing by the post-processing device 5, it is discharged or reused. A part of the sludge from the sedimentation tank 3 is returned to the aeration tank 2 (suspension biological treatment tank),
Maintain the MLSS in the tank at a predetermined level.

【0010】本発明においては、浮遊生物処理を行い、
十分硝化を行った一次処理水を炭素繊維を接触材とした
嫌気濾床槽(嫌気的生物膜処理)で脱窒処理を行うの
で、その理由は詳らかではないが、後述の実験データか
ら明らかなごとく、嫌気性微生物の親和性が高い炭素繊
維条の生物膜により十分な脱窒処理が行われる。さら
に、一次処理水を二次処理(嫌気濾床槽)に供す前に沈
降処理を行い懸濁成分を除去し、また、二次処理におい
ては炭素繊維条に生物膜が強固に付着するので懸濁性物
質の捕獲効率が高く、懸濁性物質は極端に少なくなり、
後処理における沈澱処理が殆ど不要になる程度の水質が
得られる。
[0010] In the present invention, floating organisms are treated,
Since the denitrification treatment is performed in the anaerobic filter bed tank (anaerobic biofilm treatment) using the carbon fiber as the contact material, the nitrification treatment is performed on the fully nitrified primary treatment water. As described above, a sufficient denitrification treatment is performed by a carbon fiber biofilm having a high affinity for anaerobic microorganisms. Furthermore, before the primary treatment water is subjected to the secondary treatment (anaerobic filter bed tank), sedimentation treatment is performed to remove suspended components. In the secondary treatment, the biofilm strongly adheres to the carbon fiber strips, so the suspension is suspended. The efficiency of capturing turbid substances is high, the amount of suspended substances is extremely small,
Water quality is obtained so that precipitation treatment in post-treatment is almost unnecessary.

【0011】本発明の嫌気的生物膜処理の接触材として
用いる炭素繊維条は、10ミクロン程度の径の低モジュラスPA
N系炭素繊維が生物親和性が高く好ましく用いられる。
また、接触材の形体は、繊維を単に垂下したものでも良
くまた繊維を織編みしたストランド等排水の性質、槽の
形体などを勘案し必要な接触面積を得る様に設計出来
る。上述の説明では一次処理を浮遊微生物法で処理した
例を説明した。この場合一次処理を効率良く行うことが
できるが場合によっては他の生物処理、接触酸化、生物
膜処理の一次処理水にも適用出来ることは言うまでもな
く、また、排水の性状、一次処理方法によっては、沈澱
槽を介さず直接一次処理水を嫌気濾床槽に導くこともで
き、沈降分離を行う場合は沈澱槽に限らず、膜フィルタ
ーを曝気槽に浸漬し、その濾過液を嫌気濾床槽に送って
もよい。
The carbon fiber strip used as the contact material for the anaerobic biofilm treatment of the present invention is a low modulus PA having a diameter of about 10 microns.
N-based carbon fibers are preferably used because they have high biocompatibility.
Further, the shape of the contact material may be a simply hanging fiber, or it may be designed so as to obtain a necessary contact area in consideration of the properties of drainage such as a strand woven of fibers and the shape of the tank. In the above description, an example in which the primary treatment is performed by the suspended microorganism method has been described. In this case, the primary treatment can be performed efficiently, but it is needless to say that it can be applied to other biological treatment, contact oxidation, and primary treatment water for biofilm treatment depending on the case, and depending on the properties of the wastewater and the primary treatment method. The primary treatment water can be directly introduced into the anaerobic filter bed tank without going through the sedimentation tank.When performing sedimentation separation, not only the sedimentation tank but also the membrane filter is immersed in the aeration tank, and the filtrate is anaerobically filtered. May be sent to

【0012】[0012]

【実施例】排水として、下水処理場の前処理済みの処理
下水に付加汚濁成分としてスキムミルクと塩化アンモニ
ウムを若干量添加したものを用い、一次処理として標準
活性汚泥の種を馴養したオキシデーションディッチ法で
処理した処理水を、沈澱処理した後、炭素繊維を垂下し
た嫌気濾床槽に導き脱窒処理を行った。結果および処理
条件を表に示す。
EXAMPLE Oxidation ditch method using pretreated sewage from a sewage treatment plant and adding a small amount of skim milk and ammonium chloride as additional pollutants to the sewage treatment plant and acclimating standard activated sludge seeds as primary treatment The treated water treated with the above was subjected to a sedimentation treatment, and then guided to an anaerobic filter bed tank in which carbon fibers were hung, and subjected to a denitrification treatment. The results and processing conditions are shown in the table.

【0013】[0013]

【表1】 [Table 1]

【0014】[0014]

【発明の効果】本発明は、排水の生物処理方法におい
て、好気的生物処理した一次処理水を、炭素繊維を接触
材とした嫌気的生物膜処理で脱窒処理するようになした
ので簡易に高度の脱窒処理(高次処理)を行え、産業上
の利用価値は大きなものがある。
According to the present invention, in the biological treatment method for wastewater, the primary treated water subjected to aerobic biological treatment is subjected to denitrification treatment by anaerobic biofilm treatment using carbon fiber as a contact material. High-grade denitrification treatment (higher-order treatment), which has great industrial utility value.

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

【図1】本発明方法の一実施例を示すフローシートであ
る。
FIG. 1 is a flow sheet showing one embodiment of the method of the present invention.

【符号の説明】 1 前処理装置 2 曝気槽 3 沈澱槽 4 嫌気濾床槽 5 後処理装置[Description of Signs] 1 Pretreatment device 2 Aeration tank 3 Sedimentation tank 4 Anaerobic filter bed tank 5 Posttreatment device

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平8−84997(JP,A) 特開 平3−146197(JP,A) 特開 昭54−160059(JP,A) 特開 平8−290191(JP,A) (58)調査した分野(Int.Cl.7,DB名) C02F 3/34 101 C02F 3/30 C02F 3/00 C02F 3/10 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-8-84997 (JP, A) JP-A-3-146197 (JP, A) JP-A-54-160059 (JP, A) JP-A 8-84 290191 (JP, A) (58) Field surveyed (Int. Cl. 7 , DB name) C02F 3/34 101 C02F 3/30 C02F 3/00 C02F 3/10

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 排水の生物処理方法において、好気的生
物処理した一次処理水を、炭素繊維を接触材とした嫌気
的生物膜処理で脱窒処理することを特徴とする排水の高
次処理方法。
In a biological treatment method for wastewater, a primary treatment water subjected to an aerobic biological treatment is subjected to a denitrification treatment by an anaerobic biofilm treatment using carbon fiber as a contact material. Method.
【請求項2】 一次処理水を一旦固液分離した後、その
上澄水を前記嫌気的生物膜処理することを特徴とする請
求項1記載の排水の高次処理方法。
2. The method for high-level treatment of wastewater according to claim 1, wherein after the primary treatment water is once subjected to solid-liquid separation, the supernatant water is subjected to the anaerobic biofilm treatment.
【請求項3】 前記炭素繊維接触材に好気的条件で微生
物を馴養し、生物膜を形成した後嫌気的処理に供するこ
とを特徴とする請求項1または請求項2記載の排水の高
次処理方法。
3. The high-order drainage water according to claim 1 or 2, wherein the microorganism is acclimated to the carbon fiber contact material under aerobic conditions to form a biofilm and then subjected to anaerobic treatment. Processing method.
JP26986997A 1997-10-02 1997-10-02 Advanced treatment of wastewater Expired - Fee Related JP3241645B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26986997A JP3241645B2 (en) 1997-10-02 1997-10-02 Advanced treatment of wastewater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26986997A JP3241645B2 (en) 1997-10-02 1997-10-02 Advanced treatment of wastewater

Publications (2)

Publication Number Publication Date
JPH11104692A JPH11104692A (en) 1999-04-20
JP3241645B2 true JP3241645B2 (en) 2001-12-25

Family

ID=17478353

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26986997A Expired - Fee Related JP3241645B2 (en) 1997-10-02 1997-10-02 Advanced treatment of wastewater

Country Status (1)

Country Link
JP (1) JP3241645B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103833145A (en) * 2014-03-07 2014-06-04 山东大学 Method for removing perchlorate in water by combining biomass adsorbent and microbial reduction

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012091115A (en) * 2010-10-27 2012-05-17 Nikko Co Water treating apparatus
JP6210514B2 (en) * 2013-03-18 2017-10-11 国立研究開発法人農業・食品産業技術総合研究機構 Nitrous oxide (N2O) -suppressed sewage treatment technology using carbon fiber filled aerobic bioreactor

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103833145A (en) * 2014-03-07 2014-06-04 山东大学 Method for removing perchlorate in water by combining biomass adsorbent and microbial reduction
CN103833145B (en) * 2014-03-07 2015-04-08 山东大学 Method for removing perchlorate in water by combining biomass adsorbent and microbial reduction

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Publication number Publication date
JPH11104692A (en) 1999-04-20

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