JP2002239592A - Apparatus for treating organic wastewater and treatment method using the same - Google Patents

Apparatus for treating organic wastewater and treatment method using the same

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Publication number
JP2002239592A
JP2002239592A JP2001036085A JP2001036085A JP2002239592A JP 2002239592 A JP2002239592 A JP 2002239592A JP 2001036085 A JP2001036085 A JP 2001036085A JP 2001036085 A JP2001036085 A JP 2001036085A JP 2002239592 A JP2002239592 A JP 2002239592A
Authority
JP
Japan
Prior art keywords
carrier
nitrification
organic wastewater
denitrification
microorganism carrier
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
JP2001036085A
Other languages
Japanese (ja)
Inventor
Haruhiko Suzuki
晴彦 鈴木
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric Co 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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP2001036085A priority Critical patent/JP2002239592A/en
Publication of JP2002239592A publication Critical patent/JP2002239592A/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

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

Abstract

PROBLEM TO BE SOLVED: To reduce an equipment and operation cost of an apparatus by performing both a nitrification process and a denitrification process in the apparatus having only one treatment tank to remove nitrogen in addition to the removal of BOD. SOLUTION: One treatment tank 2 is partitioned into a nitrification part 4 on an inlet side and a denitrification part 5 on an outlet side by a microorganism carrier part 3 formed by supporting a large number of string-like carriers 6 by a support frame. In the nitrification part 4, wastewater to be aerated by an aeration pump 9 is aerated to be held to an aerobic state to perform nitrification while generating a convection and the denitrification part 5 is formed so as to have volume larger than that of the nitrification part 4 and partitioned from the nitrification part 4 by the microorganism carrier part 3 to be held to an anaerobic state to perform denitrification.

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、微生物を用いた有
機排水の浄化処理装置及び処理方法に関し、微生物担体
部で処理槽を仕切るという簡単な構成により、排水の硝
化と脱窒を一槽で行うことができる有機排水の浄化処理
装置及び処理方法に関する。なお、本明細書で処理槽に
導入されるこれから処理されるべき排水は「排水」と言
い、処理槽内の処理中乃至処理済みの水は「処理水」と
言う。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus and a method for purifying organic wastewater using microorganisms. The present invention relates to a simple structure in which a treatment tank is partitioned by a microorganism carrier, whereby nitrification and denitrification of wastewater can be performed in one tank. The present invention relates to an apparatus and a method for purifying organic wastewater that can be performed. In this specification, wastewater to be introduced into the treatment tank to be treated is referred to as “drainage”, and water being treated or treated in the treatment tank is referred to as “treated water”.

【0002】[0002]

【従来の技術】微生物を用いて生物学的に処理水中の窒
素成分を除去する技術は、硝化細菌によりアンモニア態
窒素を酸化して硝酸態窒素にすることを目的とした硝化
法と、脱窒菌により亜硝酸・硝酸態窒素を還元して窒素
にすることを目的とした脱窒法があり、それらを組み合
わせた手法を硝化脱窒法と呼んでいる。
2. Description of the Related Art Techniques for biologically removing nitrogen components in treated water using microorganisms include a nitrification method for oxidizing ammonium nitrogen to nitrate nitrogen by nitrifying bacteria, and a denitrifying bacterium. There is a denitrification method aimed at reducing nitrous acid and nitrate nitrogen to nitrogen by using the method, and a method combining them is called a nitrification denitrification method.

【0003】この生物学的硝化脱窒法は、有機態窒素、
アンモニア態窒素、亜硝酸・硝酸態窒素などの幅広い形
態の窒素化合物が対象となり、処理後の窒素の形態が二
次汚染の心配が無い窒素である特徴を持っているので、
一般に広く使用されている。
[0003] This biological nitrification and denitrification method uses organic nitrogen,
A wide range of nitrogen compounds, such as ammonia nitrogen, nitrite and nitrate nitrogen, are targeted, and the form of nitrogen after treatment has the characteristic that there is no worry of secondary pollution,
Generally used widely.

【0004】従来の一般的な硝化脱窒法の排水処理シス
テムの模式図を図4に示す。排水処理システムは、硝化
工程を行う第1槽と、脱窒工程を行う第2槽の二つの槽
から成る二槽式である。第1槽は、ブロアポンプなどで
空気を送り、好気状態を保ってアンモニア態窒素を微生
物処理して亜硝酸または硝酸態窒素に酸化する。そし
て、第1槽で処理された処理水を嫌気性状態に保った第
2槽に導き、そこで亜硝酸・硝酸態窒素を窒素にして還
元除去する。
FIG. 4 is a schematic view of a conventional general nitrification and denitrification wastewater treatment system. The wastewater treatment system is a two-tank system including a first tank for performing a nitrification step and a second tank for performing a denitrification step. The first tank feeds air with a blower pump or the like, keeps the aerobic state, and treats ammonia-nitrogen with microorganisms to oxidize it into nitrite or nitrate-nitrogen. Then, the treated water treated in the first tank is led to a second tank maintained in an anaerobic state, where nitrous acid and nitrate nitrogen are reduced to nitrogen and removed.

【0005】又、有機物の少ない雰囲気でも担体内に硝
化細菌と脱窒細菌が共存棲息していることを見出し、こ
の共生担体を用いた図5に示すような、一槽式硝化脱窒
の可能性について基礎的に検討されていることが既に紹
介され公知である((株)エヌ・ティー・エス発行、
「新しい水処理シリーズ 微生物固定化法による水処
理」、123〜124頁参照。)。
[0005] Further, they have found that nitrifying bacteria and denitrifying bacteria coexist in the carrier even in an atmosphere containing little organic matter, and it is possible to perform single-tank nitrification denitrification using this symbiotic carrier as shown in FIG. It has already been introduced and publicly known that the nature has been studied fundamentally (NTS Corporation,
See "New Water Treatment Series Water Treatment by Microbial Immobilization", pages 123-124. ).

【0006】[0006]

【発明が解決しようとする課題】従来の二槽式の一般的
な硝化脱窒法の排水処理システムは、上記のとおり、好
気状態と嫌気状態といった相反する状態を維持するため
に二槽を必要としており、そのために装置、操作が複雑
となり建設コスト、運転コストが高くなるという問題が
あった。
As described above, the conventional two-tank type general nitrification denitrification wastewater treatment system requires two tanks to maintain contradictory states such as an aerobic state and an anaerobic state. Therefore, there has been a problem that the equipment and operation are complicated, and the construction cost and operation cost are increased.

【0007】そして、一槽式硝化脱窒では、微生物を担
体に包括固定する手間がかかりコストも上がってしま
い、又担体中を水が必ず透過する保証はない。従って、
後処理として無酸素槽を設置して、脱窒を進行させなく
てはならない。
[0007] In the single-tank nitrification denitrification, it takes time and effort to entrap and fix microorganisms on a carrier, and the cost is increased. Further, there is no guarantee that water permeates the carrier. Therefore,
An anoxic tank must be installed as a post-treatment to promote denitrification.

【0008】本発明は、上記従来の問題を解決すること
を目的とし、微生物担体部で処理槽を仕切るという簡単
な構成により、排水の硝化と脱窒を一槽のみで効果的に
行うことができる有機排水の浄化処理装置及び処理方法
を実現することを課題とするものである。
An object of the present invention is to solve the above-mentioned conventional problems, and it is possible to effectively perform nitrification and denitrification of wastewater in only one tank by a simple structure in which a treatment tank is partitioned by a microorganism carrier. It is an object of the present invention to realize an organic wastewater purification treatment device and treatment method that can be performed.

【0009】[0009]

【課題を解決するための手段】本発明は上記課題を解決
するために、処理槽と微生物担体部から成る有機排水の
硝化脱窒を行う有機排水の処理装置であって、上記処理
槽は、微生物担体部で仕切られていることを特徴とする
有機排水の処理装置を提供する。
SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention provides an organic wastewater treatment apparatus for nitrifying and denitrifying organic wastewater comprising a treatment tank and a microorganism carrier, wherein the treatment tank comprises: Provided is an organic wastewater treatment device characterized by being partitioned by a microorganism carrier part.

【0010】上記微生物担体部は、上記処理槽内の処理
水が通過できる構造であることを特徴とする。
[0010] The microorganism carrier is characterized in that it has a structure through which treated water in the treatment tank can pass.

【0011】上記微生物担体部で仕切られた処理槽の一
方は好気状態に保たれ、他方は嫌気状態に保たれること
を特徴とする。
One of the treatment tanks partitioned by the microorganism carrier is maintained in an aerobic state, and the other is maintained in an anaerobic state.

【0012】上記微生物担体部で仕切られた処理槽の一
方は処理水が曝気されて好気状態に保たれ、上記処理槽
の他方は微生物担体部で仕切られていることにより嫌気
状態に保たれることを特徴とする。
One of the treatment tanks partitioned by the microorganism carrier is maintained in an aerobic state by aeration of treated water, and the other of the treatment tanks is maintained in an anaerobic state by partitioning by the microorganism carrier. It is characterized by being performed.

【0013】上記処理槽の中、上記好気状態に保たれる
側に処理すべき排水が導入され、上記嫌気状態に保たれ
る側から処理水が排出されることを特徴とする。
In the treatment tank, wastewater to be treated is introduced into the side maintained in the aerobic state, and treated water is discharged from the side maintained in the anaerobic state.

【0014】上記微生物担体部は、紐状担体、網状担
体、格子状担体、粒状担体及び多孔状担体から選択され
た少なくとも1種以上の担体から成る微生物担体壁を1
又は2以上備えていることを特徴とする。
[0014] The microbial carrier portion comprises a microbial carrier wall composed of at least one carrier selected from the group consisting of a string-shaped carrier, a mesh-shaped carrier, a lattice-shaped carrier, a granular carrier and a porous carrier.
Alternatively, two or more are provided.

【0015】本発明は上記課題を解決するために、処理
槽を微生物担体部で仕切り、一方を好気状態に保ち、他
方を嫌気状態に保つことにより、上記処理槽で有機排水
の硝化脱窒を行うことを特徴とする有機排水の処理方法
を提供する。
In order to solve the above-mentioned problems, the present invention solves the above-mentioned problem by partitioning a treatment tank with a microorganism carrier, maintaining one in an aerobic state and the other in an anaerobic state. And a method for treating organic wastewater.

【0016】[0016]

【発明の実施の形態】本発明に係る有機排水の処理装置
及び処理方法の実施の形態を、実施例に基づいて図面を
参照して以下説明する。本発明は、微生物を用いた有機
排水の硝化脱窒装置において、一槽のみで硝化と脱窒を
同時に行うことができる有機排水の処理装置及び処理方
法に関する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of an apparatus and method for treating organic wastewater according to the present invention will be described below based on embodiments with reference to the drawings. The present invention relates to an apparatus and a method for treating organic wastewater that can simultaneously perform nitrification and denitrification in only one tank in an apparatus for nitrifying and denitrifying organic wastewater using microorganisms.

【0017】図1は、本発明に係る有機排水の処理装置
及び処理方法の実施例を説明する図であり、本発明に係
る有機排水の処理装置1は、一槽の処理槽2を有する一
槽式硝化脱窒装置を特徴とする。この処理槽2は、微生
物担体部3によって入口側(上流側)の硝化部4と出口
側(下流側)の脱窒部5に仕切られている。
FIG. 1 is a view for explaining an embodiment of an organic wastewater treatment apparatus and method according to the present invention. An organic wastewater treatment apparatus 1 according to the present invention has one treatment tank 2. It features a tank type nitrification and denitrification system. The treatment tank 2 is partitioned by a microorganism carrier 3 into a nitrification section 4 on the inlet side (upstream side) and a denitrification section 5 on the outlet side (downstream side).

【0018】微生物担体部3は、微生物を担持する紐状
担体6が支持フレーム7に支持されるように取り付けら
れて構成されている。微生物担体部3の具体的な構造
は、いろいろ考えられるが、処理水が複数の紐状担体6
の間を通過できるように、複数の紐状担体6を支持フレ
ーム7に取付けて微生物担体壁3’が構成され、微生物
担体部3は、この微生物担体壁3’から構成されてい
る。後述するが、微生物担体部3は、複数の微生物担体
壁3’から構成してもよい。紐状担体6の表面には、硝
化菌を含む微生物が付着成長し微生物膜を形成してい
る。
The microorganism carrier portion 3 is configured such that a string-like carrier 6 carrying microorganisms is mounted on the support frame 7. Various structures can be considered for the specific structure of the microbial carrier 3.
A plurality of string-shaped carriers 6 are attached to the support frame 7 so as to allow passage therebetween, thereby forming a microorganism carrier wall 3 ′. The microorganism carrier portion 3 is constituted by the microorganism carrier wall 3 ′. As will be described later, the microorganism carrier section 3 may be composed of a plurality of microorganism carrier walls 3 '. Microorganisms including nitrifying bacteria adhere and grow on the surface of the string-shaped carrier 6 to form a microbial membrane.

【0019】硝化部4では、処理されるべき排水が導入
される入口8が処理槽2の上部に設けられており、処理
槽2の底部には爆気ポンプ9が設けられている。爆気ポ
ンプ9は、硝化部4内を曝気し、硝化部4内に矢印で示
すような対流(水流)を発生させるとともに、硝化部4
内を好気状態に保つように構成されている。
In the nitrification unit 4, an inlet 8 for introducing wastewater to be treated is provided at the upper part of the treatment tank 2, and a detonation pump 9 is provided at the bottom of the treatment tank 2. The detonation pump 9 aerates the inside of the nitrification unit 4 to generate a convection (water flow) as indicated by an arrow in the nitrification unit 4,
It is configured to keep the inside aerobic.

【0020】脱窒部5は、硝化部4より大きな容積(ス
ペース)に形成されており、その下流端の処理槽2の上
部に、処理水(処理済み水)がオーバーフローして導出
される出口10が設けられている。硝化部4は曝気され
ているので対流が生じるが、紐状担体6が妨げとなって
溶存酸素を多く含んだ液体は脱窒部5まではほとんど至
らないので、脱窒部5は嫌気状態に保たれる。
The denitrification section 5 is formed in a larger volume (space) than the nitrification section 4, and an outlet through which treated water (treated water) overflows and is discharged above the treatment tank 2 at the downstream end. 10 are provided. Since the nitrification part 4 is aerated, convection occurs. However, the liquid containing a large amount of dissolved oxygen hardly reaches the denitrification part 5 because the cord-shaped carrier 6 hinders the denitrification part 5. Will be kept.

【0021】以上のような構成からなる本発明に係る有
機排水の処理装置の作用及び処理方法を説明する。処理
されるべき排水は入口8から導入される。爆気ポンプ9
は、硝化部4内を曝気することにより好気状態に保つと
ともに、硝化部4に導入された処理水中に、矢印に示す
ように、硝化部4内で対流を発生させる。
The operation and method of the organic wastewater treatment apparatus according to the present invention having the above-described structure will be described. The wastewater to be treated is introduced from an inlet 8. Explosive pump 9
Aerating the inside of the nitrification unit 4 to maintain an aerobic state by aeration, and also generates convection in the treated water introduced into the nitrification unit 4 as shown by an arrow.

【0022】排水が新しく硝化部4内に導入されると、
対流により循環し後述する硝化処理されている処理水
は、徐々に押し出されて紐状担体6の隙間を通り、嫌気
状態に保たれた脱窒部5に移動する。
When waste water is newly introduced into the nitrification section 4,
Treated water circulated by convection and subjected to nitrification treatment, which will be described later, is gradually pushed out, passes through the gaps between the cord-shaped carriers 6, and moves to the denitrification unit 5 maintained in an anaerobic state.

【0023】このように硝化部4内で対流を生じ循環す
る処理水は、循環しながら紐状担体6の微生物膜に接触
する。これにより処理水中に含まれるアンモニア態窒素
は、微生物膜中の硝化菌により酸化されて亜硝酸又は硝
酸態窒素になる。これを化学式で示すと次のようにな
る。 NH +3/2O → NO +HO +2
又は NO +1/2O → NO
As described above, the treated water circulating in the nitrification section 4 due to convection comes into contact with the microbial membrane of the string-shaped carrier 6 while circulating. As a result, the ammonia nitrogen contained in the treated water is oxidized by nitrifying bacteria in the microbial membrane to become nitrite or nitrate nitrogen. This is represented by the following chemical formula. NH 4 + +3/2 O 2 → NO 2 + H 2 O +2
H + or NO 2 + 1 / 2O 2 → NO 3

【0024】硝化部4内で硝化処理された処理水が、紐
状担体6の隙間を通り嫌気状態に保った脱窒部に移動す
ると、そこで処理水中の亜硝酸又は硝酸態窒素は、脱窒
菌により嫌気的に還元され窒素となり除去される。これ
を化学式で示すと次のようになる。 2NO +3H → N ↑ +2HO +
2OH 又は 2NO +5H → N ↑ +4HO +
2OH
When the treated water that has been nitrified in the nitrification section 4 passes through the gap of the cord-shaped carrier 6 and moves to the denitrification section kept in an anaerobic state, the nitrite or nitrate nitrogen in the treatment water is denitrified. Is reduced anaerobically to become nitrogen and removed. This is represented by the following chemical formula. 2NO 2 + 3H 2 → N 2 ↑ + 2H 2 O +
2OH - or 2NO 3 - + 5H 2 → N 2 ↑ + 4H 2 O +
2OH

【0025】このようにして脱窒部5において処理水中
の窒素は除去されるから、処理水中の窒素成分は減少す
ることになる。
As described above, since the nitrogen in the treated water is removed in the denitrification section 5, the nitrogen component in the treated water is reduced.

【0026】本発明では、微生物担体部3で脱窒部5は
硝化部4と仕切られており、しかも硝化部4よりも脱窒
部5の容積を大きく形成されているから、硝化部4から
の影響(溶存酸素の混入などの影響)は少なく抑えら
れ、安定した脱窒が可能となる。
In the present invention, the denitrification section 5 is separated from the nitrification section 4 by the microorganism carrier section 3 and the capacity of the denitrification section 5 is made larger than that of the nitrification section 4. (Resolved oxygen contamination) can be suppressed to a small extent, and stable denitrification becomes possible.

【0027】又、通常、硝化菌の増殖速度はBOD酸化
細菌のそれと比べて1/10程度なので、汚泥日令を多
く(3〜5日程度)取る必要があるが、紐状担体6に硝
化菌が担持されて汚泥の流出が抑制されるので、汚泥日
令を稼ぐことができる。
Also, since the growth rate of nitrifying bacteria is usually about 1/10 of that of BOD oxidizing bacteria, it is necessary to increase the sludge age (about 3 to 5 days). Since bacteria are carried and the outflow of sludge is suppressed, the sludge age can be earned.

【0028】微生物担体部の構成は、いろいろな構成が
実施可能である。上記実施例では、微生物担体部3は、
紐状担体から成る紐状の微生物担体壁3’を1つから構
成したが、図2に実施例の変形例で示すように、紐状の
微生物担体壁3’を複数(図2では3つ設けている。)
から構成してもよい。この場合、好気側にある微生物担
体壁は硝化菌を高密度に担持した構成とし、嫌気側微生
物担体壁は硝化菌を高密度に担持した構成とすると、よ
りきめ細かい効率的な硝化脱窒が可能となる。
Various configurations can be implemented for the structure of the microorganism carrier. In the above embodiment, the microorganism carrier 3 is
Although a single string-shaped microorganism carrier wall 3 ′ made of a string-shaped carrier is configured, as shown in FIG. 2 as a modified example of the embodiment, a plurality of string-shaped microorganism carrier walls 3 ′ (three in FIG. 2). Provided.)
May be configured. In this case, if the microbial carrier wall on the aerobic side is configured to support nitrifying bacteria at a high density, and the anaerobic microbial carrier wall is configured to support nitrifying bacteria at a high density, finer and more efficient nitrification denitrification can be achieved. It becomes possible.

【0029】又、微生物担体部3を構成する微生物担体
壁3’は、上記実施例のように紐状担体6に限ることな
く、いろいろな構成が実施可能である。図3は、いろい
ろな構造の微生物担体壁をその正面から見た図を示す。
Further, the microorganism carrier wall 3 'constituting the microorganism carrier portion 3 is not limited to the string-shaped carrier 6 as in the above-described embodiment, and various configurations can be implemented. FIG. 3 shows a view of the microbial carrier walls of various structures as viewed from the front.

【0030】図3(a)は、支持フレーム7に取り付け
られた網状担体18から構成される微生物担体壁を示
す。図3(b)は、支持フレーム7に取り付けられた格
子状担体11から構成される微生物担体壁を示す。図3
(c)は、支持フレーム7に取り付けられた粒状担体1
2が水が通過可能な容器13(メッシュ状又は孔付き容
器等)内に収容されて構成される微生物担体壁を示す。
FIG. 3A shows a microorganism carrier wall composed of a mesh carrier 18 attached to the support frame 7. FIG. 3B shows a microorganism carrier wall composed of a lattice-like carrier 11 attached to the support frame 7. FIG.
(C) shows the granular carrier 1 attached to the support frame 7.
Reference numeral 2 denotes a microorganism carrier wall configured to be accommodated in a container 13 (mesh-shaped or perforated container or the like) through which water can pass.

【0031】さらに、図3(d)は、支持フレーム7に
取り付けられた粒状担体14が簾状に結合されて構成さ
れる微生物担体壁を示す。図3(e)は、多孔質担体1
5から構成される微生物担体壁を示す。これらの微生物
担体壁も図2に示すように複数配設してもよい。
FIG. 3D shows a microbial carrier wall formed by connecting the granular carriers 14 attached to the support frame 7 in a cord-like manner. FIG. 3E shows the porous carrier 1.
5 shows a microbial carrier wall composed of 5; A plurality of these microorganism carrier walls may be provided as shown in FIG.

【0032】又、図3(f)は、板体16の両面に微生
物を担持し、しかも板体16で処理槽2を完全に仕切ら
ず、処理水が板体16を通過するようにした微生物担体
壁を示している。即ち、板体16の高さを処理水がオー
バーフロー程度の高さにしたり、板体16に貫通孔17
を形成し貫通孔16を処理水が通過するような構成とし
てもよい。
FIG. 3 (f) shows a microbe prepared by carrying microorganisms on both sides of the plate 16 and not allowing the plate 16 to completely separate the treatment tank 2 so that treated water passes through the plate 16. 3 shows a carrier wall. That is, the height of the plate 16 is set to a height at which the treated water overflows, or the through hole 17
May be formed so that the treated water passes through the through-hole 16.

【0033】以上、本発明に係る有機排水の処理装置及
び処理方法の実施の形態を実施例に基づいて説明した
が、本発明は特にこのような実施例に限定されることな
く、特許請求の範囲記載の技術的事項の範囲内でいろい
ろな実施例があることはいうまでもない。
The embodiments of the apparatus and method for treating organic wastewater according to the present invention have been described based on the embodiments. However, the present invention is not particularly limited to such embodiments, and claims are not limited thereto. It goes without saying that there are various embodiments within the scope of the technical matters described in the range.

【0034】[0034]

【発明の効果】以上のような本発明に係る有機排水の処
理装置及び処理方法によれば、処理槽を一槽のみ備えた
簡単な処理装置で、硝化工程及び脱窒工程を行うことが
でき、BODの除去に加えて窒素を除去し処理水中の窒
素成分を低減することができ、装置の建設及び運転に要
するコストを低減することができる。
According to the apparatus and method for treating organic waste water according to the present invention as described above, the nitrification step and the denitrification step can be performed with a simple treatment apparatus having only one treatment tank. In addition to removing BOD, nitrogen can be removed and the nitrogen component in the treated water can be reduced, and the cost required for the construction and operation of the apparatus can be reduced.

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

【図1】本発明に係る有機排水の処理装置及び処理方法
の実施例を説明するための図である。
FIG. 1 is a view for explaining an embodiment of an apparatus and method for treating organic wastewater according to the present invention.

【図2】本発明に係る有機排水の処理装置及び処理方法
の実施例の変形例を説明するための図である。
FIG. 2 is a view for explaining a modification of the embodiment of the apparatus and method for treating organic wastewater according to the present invention.

【図3】本発明に係る有機排水の処理装置及び処理方法
の実施例の微生物担体部のいろいろな構成を説明するた
めの図である。
FIG. 3 is a diagram for explaining various configurations of a microorganism carrier portion in an embodiment of an organic wastewater treatment apparatus and treatment method according to the present invention.

【図4】従来の一般的な二槽式の有機排水の処理システ
ムを説明するための模式図である。
FIG. 4 is a schematic diagram for explaining a conventional general two-tank type organic wastewater treatment system.

【図5】公知の一槽式の有機排水の処理システムを説明
するための模式図である。
FIG. 5 is a schematic diagram for explaining a known one-tank type organic wastewater treatment system.

【符号の説明】[Explanation of symbols]

1 有機排水の処理装置 2 一槽からなる処理槽 3 微生物担体部 4 硝化部 5 脱窒部 6 微生物担体 7 微生物担体の支持フレーム 8 原排水を導入する入口 9 曝気ポンプ 10 処理水を導出する出口 11 格子状担体 12、14 粒状担体 13 水通過可能な容器 15 多孔質担体 16 板体 17 貫通孔 18 網状担体 DESCRIPTION OF SYMBOLS 1 Organic wastewater treatment apparatus 2 Treatment tank consisting of one tank 3 Microorganism carrier part 4 Nitrification part 5 Denitrification part 6 Microorganism carrier 7 Microorganism carrier support frame 8 Inlet for introducing raw wastewater 9 Aeration pump 10 Outlet for extracting treated water DESCRIPTION OF SYMBOLS 11 Lattice carrier 12, 14 Granular carrier 13 Container which can pass water 15 Porous carrier 16 Plate 17 Through hole 18 Reticulated carrier

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 処理槽と微生物担体部から成る有機排
水の硝化脱窒を行う有機排水の処理装置であって、上記
処理槽は、微生物担体部で仕切られていることを特徴と
する有機排水の処理装置。
An organic wastewater treatment apparatus for performing nitrification and denitrification of organic wastewater comprising a treatment tank and a microorganism carrier, wherein the treatment tank is partitioned by a microorganism carrier. Processing equipment.
【請求項2】 上記微生物担体部は、上記処理槽内の
処理水が通過できる構造であることを特徴とする請求項
1記載の有機排水の処理装置。
2. The organic wastewater treatment apparatus according to claim 1, wherein the microorganism carrier has a structure through which treated water in the treatment tank can pass.
【請求項3】 上記微生物担体部で仕切られた処理槽
の一方は好気状態に保たれ、他方は嫌気状態に保たれる
ことを特徴とする請求項1又は2記載の有機排水の処理
装置。
3. The organic wastewater treatment apparatus according to claim 1, wherein one of the treatment tanks partitioned by the microorganism carrier is maintained in an aerobic state, and the other is maintained in an anaerobic state. .
【請求項4】 上記微生物担体部で仕切られた処理槽
の一方は処理水が曝気されて好気状態に保たれ、上記処
理槽の他方は微生物担体部で仕切られていることにより
嫌気状態に保たれることを特徴とする請求項1又は2記
載の有機排水の処理装置。
4. One of the treatment tanks partitioned by the microorganism carrier is kept in an aerobic state by aeration of treated water, and the other of the treatment tanks is placed in an anaerobic state by being partitioned by the microorganism carrier. The organic wastewater treatment device according to claim 1, wherein the organic wastewater is kept.
【請求項5】 上記処理槽の中、上記好気状態に保た
れる側に処理すべき排水が導入され、上記嫌気状態に保
たれる側から処理水が排出されることを特徴とする請求
項3又は4記載の有機排水の処理装置。
5. The process tank, wherein wastewater to be treated is introduced into the side maintained in the aerobic state, and treated water is discharged from the side maintained in the anaerobic state. Item 5. An organic wastewater treatment device according to item 3 or 4.
【請求項6】 上記微生物担体部は、紐状担体、網状
担体、格子状担体、粒状担体及び多孔状担体から選択さ
れた少なくとも1種以上の担体から成る微生物担体壁を
1又は2以上備えていることを特徴とする請求項1、
2、3、4又は5記載の有機排水の処理装置。
6. The microorganism carrier portion comprises one or more microorganism carrier walls comprising at least one or more carriers selected from a string carrier, a mesh carrier, a lattice carrier, a granular carrier and a porous carrier. Claim 1, characterized in that
The organic wastewater treatment apparatus according to 2, 3, 4, or 5.
【請求項7】 処理槽を微生物担体部で仕切り、一方
を好気状態に保ち、他方を嫌気状態に保つことにより、
上記処理槽で有機排水の硝化脱窒を行うことを特徴とす
る有機排水の処理方法。
7. The treatment tank is partitioned by a microorganism carrier, and one is kept in an aerobic state and the other is kept in an anaerobic state,
A method for treating organic wastewater, wherein nitrification and denitrification of organic wastewater are performed in the treatment tank.
JP2001036085A 2001-02-13 2001-02-13 Apparatus for treating organic wastewater and treatment method using the same Pending JP2002239592A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001036085A JP2002239592A (en) 2001-02-13 2001-02-13 Apparatus for treating organic wastewater and treatment method using the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001036085A JP2002239592A (en) 2001-02-13 2001-02-13 Apparatus for treating organic wastewater and treatment method using the same

Publications (1)

Publication Number Publication Date
JP2002239592A true JP2002239592A (en) 2002-08-27

Family

ID=18899417

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001036085A Pending JP2002239592A (en) 2001-02-13 2001-02-13 Apparatus for treating organic wastewater and treatment method using the same

Country Status (1)

Country Link
JP (1) JP2002239592A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011235287A (en) * 2011-07-20 2011-11-24 Maezawa Ind Inc Wastewater treatment apparatus
KR101271327B1 (en) * 2011-06-07 2013-06-04 아시아환경 주식회사 Waste water treatment system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101271327B1 (en) * 2011-06-07 2013-06-04 아시아환경 주식회사 Waste water treatment system
JP2011235287A (en) * 2011-07-20 2011-11-24 Maezawa Ind Inc Wastewater treatment apparatus

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