JP3100096U - Sewage treatment system and continuous expansion culture device used for the system - Google Patents

Sewage treatment system and continuous expansion culture device used for the system Download PDF

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JP3100096U
JP3100096U JP2003003735U JP2003003735U JP3100096U JP 3100096 U JP3100096 U JP 3100096U JP 2003003735 U JP2003003735 U JP 2003003735U JP 2003003735 U JP2003003735 U JP 2003003735U JP 3100096 U JP3100096 U JP 3100096U
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sewage
culture solution
bacterium
continuous expansion
culture
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山家 克弘
森山 紹一
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山家 克弘
森山 紹一
ガーディアン株式会社
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Abstract

【課題】長期にわたって十分な有機物分解能を維持し、汚泥の削減及び臭気の低減を図る。
【解決手段】汚水を一時貯留すると共に汚水に含まれる有機物を有効微生物群と反応させて汚水処理する曝気槽3と、予め設定されたプログラムに従って有効微生物群を連続的に培養すると共に曝気槽3の汚水に対し複数回に分けて有効微生物群を投与する連続拡大培養装置4とを備えた。
【選択図】 図1
An object of the present invention is to maintain a sufficient organic substance resolution for a long period of time to reduce sludge and odor.
An aeration tank for temporarily storing sewage and treating sewage by reacting organic substances contained in the sewage with an effective microorganism group, and continuously cultivating the effective microorganism group in accordance with a preset program, and And a continuous expansion culture device 4 for administering an effective microorganism group to the wastewater in a plurality of times.
[Selection diagram] Fig. 1

Description

【0001】
【考案の属する技術分野】
本考案は、汚水処理システムに関し、特に有効微生物群を使用して悪臭防止、水質保全、余剰汚泥の減量化等を図れるようにした汚水処理システム並びにそれに使用される連続拡大培養装置に関する。
【0002】
【従来の技術】
従来より、有効微生物群を使用した一般的な汚水処理の方式として活性汚泥方式が知られている。この方式は、汚水に曝気(エアレーション)をかけることで、汚水中の好気性微生物の働きを活性化させ、汚水中の有機物を分解して水質を浄化させるというものである。この活性汚泥方式による汚水処理は、優れた浄化能力を有するものの、悪臭の抑制、汚泥の発生量の削減のためには、有効微生物群の強化、改善が必要であり、そのための種々の試みがなされている。
【0003】
例えば、特許文献1には、沈澱池より排出された汚泥を曝気しつつ、硅藻土、パーライト等の混合物の層を通して返送することにより、有機物分解能、臭気減少を図るようにした装置が開示されている。また、特許文献2には、主に好気性菌群が生息する反応槽から送られる汚泥を固液分離して、濃縮され抜き出された汚泥の一部又は全部にケイ酸を含有する溶液を添加すると共に、曝気によって好気状態に保持し、熟成により脱臭効果を安定的に発現させるようにした汚泥処理方法が開示されている。
【0004】
【特許文献1】
特公昭62−016155号公報、第2頁 左欄第10〜18行
【特許文献2】
特開平12−084595号公報、第2頁、段落0009
【0005】
【考案が解決しようとする課題】
しかし、上述した従来の汚水処理方法では、活性汚泥中に含まれる有効微生物群が相互に影響しあって時間の経過と共に反応槽における有機物分解能が低下し、十分な臭気低減効果が得られないとう問題がある。
【0006】
本考案は、このような問題点に鑑みなされたもので、長期にわたって十分な有機物分解能を維持し、効果的に汚泥の削減及び臭気の低減を図ることができる汚水処理システム並びにそれに使用される連続拡大培養装置を提供することを目的とする。
【0007】
【課題を解決するための手段】
本考案に係る汚水処理システムは、汚水に対して有効微生物群を投与して汚水に含まれる有機質を分解する汚水処理方法において、前記有効微生物群を連続拡大培養装置で連続的に培養しつつ、前記連続拡大培養装置に収容された有効微生物群を複数回に分けて前記汚水に投与するようにしたことを特徴とする。
【0008】
本考案に係る汚水処理システムは、また、汚水を一時貯留すると共に汚水に含まれる有機物を有効微生物群と反応させて汚水処理する反応槽と、予め設定されたプログラムに従って前記有効微生物群を連続的に培養すると共に前記反応槽の汚水に対し複数回に分けて前記有効微生物群を投与する連続拡大培養装置とを備えたことを特徴とする。
【0009】
本考案によれば、有効微生物群の培養と投入とを、複数回に分けて行うようにしているので、一度のセッティングで、有効微生物層は殆ど劣化させずに、長期間に亘る連続運転が可能になる。これにより、効果的に汚泥の削減及び臭気の低減を図ることが可能になる。
【0010】
また、本考案に係る連続拡大培養装置は、第1の嫌気性菌を含む培養液を収容する第1の培養液槽、通性嫌気性・好気性菌を含む培養液を収容する第2の培養液槽、第2の嫌気性菌を含む培養液を収容する第3の培養液槽、前記第1〜第3の培養液槽にそれぞれ水を供給するための給水手段、前記第1〜第3の培養液槽に収容された培養液の液面をそれぞれ検出する第1〜第3の液面検出手段、前記第1〜第3の培養液槽に収容された培養液の温度を検出する第1〜第3の温度検出手段、前記第1〜第3の培養液槽に収容された培養液を加温する第1〜第3の加温手段、及び前記第1〜第3の培養液槽に収容された培養液を所定の割合で汚水に投入する投入手段を備えた培養槽と、予め設定されたプログラムに従って、前記第1〜第3の加温手段を制御すると共に、前記反応槽に対し複数回に分けて前記有効微生物群を前記汚水に投入するように前記投入手段を制御するコントローラとを備えたことを特徴とする。
【0011】
この連続拡大培養装置によれば、前述した利点に加え、有効微生物群は、第1〜第3の培養液槽に別個に培養されることにより、最も望ましい温度条件を含む環境条件で培養がなされ、混合による相互の影響は皆無となる。
【0012】
【考案の実施の形態】
以下、図面に基づいて本考案の実施の形態について説明する。
図1は、本考案の一実施形態に係る汚水処理システムの概略構成を示す図である。
し尿、生活廃水、工業排水等の汚水である原水は、原水ポンプ槽1に一旦貯留され、図示しない圧送ポンプによって後段の処理部に順次供給される。流入調整槽2は、原水に対する脱臭・分解の前処理を行うと共に、後段に供給される汚水の流入量を調整する。曝気槽(反応槽)3は、流入調整槽2から供給された汚水を一旦貯留し、所定の曝気条件のもと、連続拡大培養装置4からの有効微生物群の投与によって、汚水に対して生化学反応を生起し、有機物を分解する。曝気槽3から排出された処理水は、沈澱槽5に供給され、ここで汚泥と上澄み液とに分離される。沈澱された汚泥は、図示しない汚泥脱水気等の汚泥処理装置で適宜処理されるが、その一部が引き抜かれ、流入調整槽2及び/又は曝気槽3に返送されていても良い。また、汚泥の余剰分は、種菌種汚泥(シーディング材)として他の処理施設で活用することもできる。上澄み液は、処理水槽6に貯留されたのち、土壌トレンチ7等を介して中水として再利用される。この中水は、後述する培養層8に上水の代わりに補給水として用いられたり、雑用水として利用される。また、中水は、曝気槽3でエアレーションをかけている場合に発生する気泡を消滅させるための消泡水としてノズルから噴霧されるようにしても良い。
【0013】
連続拡大培養装置4は、培養槽8とコントローラ9とにより構成されている。培養槽8は、例えば図2に示すように構成されている。即ち、この培養槽8は、独立した3つの培養液槽11,12,13を備えている。各培養液槽11〜13には、給水弁14,15,16,17を介して給水がなされ、各培養液槽11〜13の有効微生物群を含む培養液21,22,23は、投入弁18,19,20及び投入ポンプ30によって、流入調整槽2及び曝気槽3に一括投入される。各培養液槽11〜13には、培養液21,22,23を槽内で循環させるための循環ポンプ24,25,26が設けられている。また、各培養液槽11〜13には、培養液21〜23をそれぞれ個別に加温するためのヒータ27,28,29と、培養液21〜23の温度を検出するためのサーモスタット31,32,33と、培養液21〜23の液面を三段階にわたって検出する液面検出用の電極棒34,35,36とが設けられている。更に、各培養液槽11〜13は、内部が密閉された構造をなっているが、上部に空気逃がし弁37,38,39が設けられている。
【0014】
この培養槽8では、三種類の有効微生物群を各培養液槽11,12,13でそれぞれ個別に培養し、所定の割合で混合投入することができる。コントローラ9には、設定パネル(図示せず)が設けられており、この設定パネルによって培養時間、一括投入時間、投入量、培養温度等をコントロールすることができる。
【0015】
図3は、コントローラ9によって制御される連続拡大培養装置の工程を示すフローチャートである。
先ず、各培養液槽11〜13に、別々に有効微生物の原液と糖蜜とを投入し(S1)、給水を行う(S2)。満水状態になったら給水を停止する。続いて予め設定された時間及び温度で培養が行われ(S3)、1回目の投入を行う(S4)。以後、培養(S5,S7,S9)と投入(S6,S8,S10)を繰り返し、最後に培養液槽11〜13の洗浄を行って(S11)、休止状態に入る(S12)。
【0016】
このように、有効微生物群の投入を、4回に分けて行うと、1回の投入では、1週間程度しか運転ができなかったものが、一度の原液と糖蜜のセッティングで、1ヶ月に亘る連続運転が可能になり、管理業務の省力化が促進される。しかも、4回であれば、有効微生物層は殆ど変化しないことも確認されている。しかし、投入回数が増えると、雑菌の繁殖も増えるので、投入回数は最大でも4回と限定することが望ましい。複数回に亘る培養、投入後は、培養液層11〜13を自動洗浄して雑菌を洗い流すことが望ましい。
【0017】
投入の割合は、例えば、1回目が全培養液の7割投入、2回目が残留培養液の6割投入、3回目が残留培養液の5割投入、4回目が残留培養液を全て投入というように投入量を徐々に減じながら投入していくのが望ましい。このような投入方法により、微生物群の密度(培養液の中の有効微生物群の数又は絶対量)を1回目から4回目の投入まで平均的に保つことができバラツキを防止することができるからである。
【0018】
このシステムに用いられる望ましい有効微生物群としては、乳酸菌、光合成菌等の嫌気性菌、放線菌等の通性嫌気性・好気性菌等があげられる。乳酸菌は、有害な微生物の繁殖や汚水中に含まれる残留有機物の急激な腐敗分解を抑制し、悪臭ガスの発生を抑制すると共に、醗酵を進め、有効な養分を生成する。光合成菌は、硫化水素や植物の根から出る分泌物や有機物を餌としてビタミンや植物の養分を合成する。放線菌(グラム陽性放線菌群)は、抗生物質を生成し、カビや病原菌を抑制する。例えば、乳酸菌(第1の嫌気性菌)、放線菌(通性嫌気性・好気性菌)及び光合成菌(第2の嫌気性菌)は、それぞれ培養液槽11〜13に別個に培養されることにより、最も望ましい温度条件を含む環境条件で培養がなされ、混合による相互の悪影響は皆無となる。汚水への投入に際しては、これらのうち嫌気性菌を70%以上、通性嫌気性・好気性菌を5〜10%の割合で混合投入するのが望ましい。嫌気性菌が70%以上であると、曝気量を大幅に削減できるので、曝気による電力量の削減により、ランニングコストを大幅に削減することができるからである。なお、汚水に硫化水素が多く含まれている場合には、嫌気性菌のうち光合成菌の割合を乳酸菌よりも多くすることが望ましい。また、8〜12ppmの酵素、ミネラル分又はアミノ酸を添加すると、汚泥量の減少を促進し、有効微生物を更に活性化させるのでより望ましい。
【0019】
【考案の効果】
以上のように、本考案によれば、有効微生物群の培養と投入とを複数回に分けて行うようにしているので、一度のセッティングで、有効微生物層は殆ど劣化させずに、長期間に亘る連続運転が可能になり、効果的に汚泥の削減及び臭気の低減を図ることができるという効果を奏する。
【図面の簡単な説明】
【図1】本考案の一実施形態に係る汚水処理システムのブロック図である。
【図2】同システムにおける連続拡大培養装置の概略構成図である。
【図3】同システムを用いた汚水処理の工程を示すフローチャートである。
【符号の説明】
1…原水ポンプ槽、2…流入調整槽、3…曝気槽、4…連続拡大培養装置、5…沈澱槽、6…処理水槽、7…土壌トレンチ、8…培養槽、9…コントローラ。
[0001]
[Technical field to which the invention belongs]
The present invention relates to a sewage treatment system, and more particularly to a sewage treatment system capable of preventing odors, preserving water quality, reducing excess sludge, and the like by using effective microorganisms, and a continuous expansion cultivation apparatus used therein.
[0002]
[Prior art]
Conventionally, an activated sludge method has been known as a general sewage treatment method using an effective microorganism group. In this method, aeration (aeration) is performed on sewage to activate the action of aerobic microorganisms in the sewage, thereby decomposing organic substances in the sewage and purifying the water quality. Sewage treatment by this activated sludge method has excellent purification ability, but in order to suppress odor and reduce the amount of generated sludge, it is necessary to strengthen and improve effective microorganisms, and various attempts have been made for that purpose. Has been done.
[0003]
For example, Patent Literature 1 discloses an apparatus in which sludge discharged from a sedimentation basin is aerated and returned through a layer of a mixture of diatomaceous earth, perlite, etc., thereby achieving organic matter resolution and odor reduction. ing. Further, in Patent Document 2, a solution containing silicic acid in part or all of concentrated and extracted sludge is obtained by solid-liquid separation of sludge sent from a reaction tank mainly inhabiting aerobic bacteria. There is disclosed a sludge treatment method in which a sludge treatment is performed in which the aerobic state is maintained by aeration while being added, and the deodorizing effect is stably exhibited by aging.
[0004]
[Patent Document 1]
Japanese Patent Publication No. 62-016155, page 2, left column, lines 10 to 18 [Patent Document 2]
JP-A-12-084595, page 2, paragraph 0009
[0005]
[Problems to be solved by the invention]
However, in the above-mentioned conventional sewage treatment method, the effective microorganisms contained in the activated sludge mutually influence each other, and the organic matter resolution in the reaction tank decreases with time, and a sufficient odor reduction effect cannot be obtained. There is.
[0006]
The present invention has been made in view of such problems, and maintains a sufficient organic matter resolution for a long period of time, and can effectively reduce sludge and odor. It is an object to provide an expansion culture device.
[0007]
[Means for Solving the Problems]
The sewage treatment system according to the present invention is a sewage treatment method in which effective microorganisms are administered to sewage to decompose organic substances contained in sewage, while continuously culturing the effective microorganisms in a continuous expansion culture device, The effective microorganism group accommodated in the continuous expansion culture apparatus is divided into a plurality of times and administered to the wastewater.
[0008]
The sewage treatment system according to the present invention also has a reaction tank for temporarily storing sewage and reacting organic substances contained in the sewage with the effective microorganisms to treat the sewage, and continuously treating the effective microorganisms according to a preset program. And a continuous expansion culturing device for administering the effective microorganism group to the sewage in the reaction tank in a plurality of times.
[0009]
According to the present invention, the cultivation and introduction of the effective microorganism group is performed in a plurality of times, so that the continuous operation for a long period of time can be performed with a single setting without substantially deteriorating the effective microorganism layer. Will be possible. This makes it possible to effectively reduce sludge and odor.
[0010]
Further, the continuous expansion culture device according to the present invention includes a first culture solution tank containing a culture solution containing a first anaerobic bacterium and a second culture solution containing a culture solution containing a facultative anaerobic / aerobic bacterium. A culture solution tank, a second culture solution tank containing a culture solution containing a second anaerobic bacterium, a water supply means for supplying water to each of the first to third culture solution tanks, A first to a third liquid level detecting means for respectively detecting the liquid level of the culture solution contained in the third culture solution tank, and detecting the temperature of the culture solution contained in the first to third culture solution tanks; First to third temperature detecting means, first to third heating means for heating the culture solution contained in the first to third culture solution tanks, and the first to third culture solutions A culture tank provided with an input means for inputting the culture solution contained in the tank into the sewage at a predetermined rate, and the first to third heating according to a preset program. Controls the stage, characterized in that said effective microorganisms in several times to the reactor and a controller for controlling the closing means so as to put into the sewerage.
[0011]
According to this continuous expansion culture apparatus, in addition to the above-mentioned advantages, the effective microorganism group is cultured separately in the first to third culture solution tanks, so that culture is performed under environmental conditions including the most desirable temperature conditions. However, there is no mutual influence due to the mixing.
[0012]
[Embodiment of the invention]
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 is a diagram showing a schematic configuration of a sewage treatment system according to an embodiment of the present invention.
Raw water, which is wastewater such as night soil, domestic wastewater, and industrial wastewater, is temporarily stored in a raw water pump tank 1, and is sequentially supplied to a subsequent processing unit by a pressure pump (not shown). The inflow adjusting tank 2 performs pretreatment for deodorization and decomposition of raw water, and adjusts an inflow amount of sewage supplied to a subsequent stage. The aeration tank (reaction tank) 3 temporarily stores the sewage supplied from the inflow adjustment tank 2, and under the predetermined aeration conditions, administers the effective microorganism group from the continuous expansion cultivation apparatus 4 to generate sewage. Causes chemical reactions and decomposes organic matter. The treated water discharged from the aeration tank 3 is supplied to the settling tank 5, where it is separated into sludge and supernatant. The settled sludge is appropriately treated by a sludge treatment device such as sludge dewatering gas (not shown). A part of the sludge may be withdrawn and returned to the inflow adjusting tank 2 and / or the aeration tank 3. In addition, the surplus sludge can be used as seed-seed sludge (seeding material) in other treatment facilities. After the supernatant is stored in the treated water tank 6, it is reused as middle water through the soil trench 7 and the like. This medium water is used as makeup water instead of clean water for the culture layer 8 described later, or is used as miscellaneous water. The medium water may be sprayed from a nozzle as defoaming water for eliminating bubbles generated when aeration is performed in the aeration tank 3.
[0013]
The continuous expansion culture device 4 includes a culture tank 8 and a controller 9. The culture tank 8 is configured, for example, as shown in FIG. That is, the culture tank 8 includes three independent culture solution tanks 11, 12, and 13. Water is supplied to each of the culture solution tanks 11 to 13 via water supply valves 14, 15, 16, and 17, and the culture solutions 21, 22, and 23 containing the effective microorganism groups in each of the culture solution tanks 11 to 13 are supplied with input valves. 18, 19, 20 and the charging pump 30 collectively charge the inflow adjusting tank 2 and the aeration tank 3. Circulation pumps 24, 25, and 26 for circulating culture solutions 21, 22, and 23 in the culture solution tanks 11 to 13 are provided. Further, in each of the culture solution tanks 11 to 13, heaters 27, 28, and 29 for individually heating the culture solutions 21 to 23, and thermostats 31 and 32 for detecting the temperature of the culture solutions 21 to 23, respectively. , 33 and electrode rods 34, 35, 36 for detecting the liquid surface of the culture solutions 21 to 23 in three stages. Further, each of the culture solution tanks 11 to 13 has a structure in which the inside is sealed, and air release valves 37, 38, and 39 are provided at the upper part.
[0014]
In the culture tank 8, three types of effective microorganism groups can be individually cultured in the respective culture solution tanks 11, 12, and 13, and mixed at a predetermined ratio. The controller 9 is provided with a setting panel (not shown), which can control the culturing time, the batch input time, the input amount, the culturing temperature, and the like.
[0015]
FIG. 3 is a flowchart showing the steps of the continuous expansion culture apparatus controlled by the controller 9.
First, a stock solution of effective microorganisms and molasses are separately charged into each of the culture solution tanks 11 to 13 (S1), and water is supplied (S2). Stop water supply when it is full. Subsequently, culturing is performed for a preset time and temperature (S3), and the first feeding is performed (S4). Thereafter, culturing (S5, S7, S9) and loading (S6, S8, S10) are repeated, and finally, the culture solution tanks 11 to 13 are washed (S11), and the apparatus enters a rest state (S12).
[0016]
As described above, when the input of the effective microorganism group is divided into four times, the operation can be performed only for about one week in one input, but the setting of the undiluted solution and the molasses takes one month. Continuous operation becomes possible, and labor saving of management work is promoted. Moreover, it has been confirmed that the effective microorganism layer hardly changes when the number of times is four. However, as the number of inputs increases, the propagation of various bacteria also increases. Therefore, it is desirable to limit the number of inputs to four at the maximum. After culturing and feeding a plurality of times, it is desirable to automatically wash the culture solution layers 11 to 13 to wash out various bacteria.
[0017]
The input ratio is, for example, that the first time is 70% of the whole culture, the second is 60% of the residual culture, the third is 50% of the residual culture, and the fourth is all of the residual culture. It is desirable to gradually reduce the amount of input as described above. With such an input method, the density of the microorganisms (the number or absolute amount of the effective microorganisms in the culture solution) can be kept average from the first to the fourth injection, and the variation can be prevented. It is.
[0018]
Desirable effective microorganisms used in this system include anaerobic bacteria such as lactic acid bacteria and photosynthetic bacteria, and facultative anaerobic and aerobic bacteria such as actinomycetes. Lactic acid bacteria suppress the propagation of harmful microorganisms and the rapid decay and decomposition of residual organic matter contained in wastewater, suppress the generation of odorous gas, promote fermentation, and generate effective nutrients. Photosynthetic bacteria synthesize vitamins and plant nutrients by feeding on hydrogen sulfide and secretions and organic matter from plant roots. Actinomycetes (Gram-positive actinomycetes) produce antibiotics to control mold and pathogens. For example, lactic acid bacteria (first anaerobic bacteria), actinomycetes (facultative anaerobic / aerobic bacteria), and photosynthetic bacteria (second anaerobic bacteria) are separately cultured in culture solution tanks 11 to 13, respectively. As a result, the culture is performed under environmental conditions including the most desirable temperature conditions, and there is no mutual adverse effect due to the mixing. At the time of introduction into sewage, it is desirable to mix and introduce anaerobic bacteria at a ratio of 70% or more and facultative anaerobic / aerobic bacteria at a ratio of 5 to 10%. If the anaerobic bacterium is 70% or more, the amount of aeration can be greatly reduced, and the running cost can be greatly reduced by reducing the amount of electric power by the aeration. When the wastewater contains a large amount of hydrogen sulfide, it is desirable that the proportion of photosynthetic bacteria among the anaerobic bacteria be larger than that of the lactic acid bacteria. It is more preferable to add 8 to 12 ppm of an enzyme, a mineral, or an amino acid because it promotes a decrease in sludge amount and further activates effective microorganisms.
[0019]
[Effect of the invention]
As described above, according to the present invention, the cultivation and introduction of the effective microorganism group are performed in a plurality of times, so that in a single setting, the effective microorganism layer is hardly degraded, and for a long period of time. The continuous operation over the entire range is enabled, and the effect of effectively reducing sludge and odor is achieved.
[Brief description of the drawings]
FIG. 1 is a block diagram of a sewage treatment system according to an embodiment of the present invention.
FIG. 2 is a schematic configuration diagram of a continuous expansion culture device in the same system.
FIG. 3 is a flowchart showing a process of sewage treatment using the same system.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 ... Raw water pump tank, 2 ... Inflow regulation tank, 3 ... Aeration tank, 4 ... Continuous expansion culture apparatus, 5 ... Sedimentation tank, 6 ... Treatment water tank, 7 ... Soil trench, 8 ... Culture tank, 9 ... Controller.

Claims (9)

汚水に対して有効微生物群を投与して汚水に含まれる有機質を分解する汚水処理システムにおいて、
前記有効微生物群を連続拡大培養装置で連続的に培養しつつ、前記連続拡大培養装置に収容された有効微生物群を複数回に分けて前記汚水に投与する
ようにしたことを特徴とする汚水処理システム。
In a sewage treatment system that administers effective microorganisms to sewage to decompose organic substances contained in sewage,
Sewage treatment, wherein the effective microorganism group is continuously cultured in a continuous expansion culturing device, and the effective microorganism group accommodated in the continuous expansion culturing device is administered to the sewage in a plurality of times. system.
前記連続拡大培養装置に収容された有効微生物群を、1回の投与量を徐々に減じながら複数回に分けて前記汚水に投与する
ようにしたことを特徴とする請求項1記載の汚水処理システム。
2. The sewage treatment system according to claim 1, wherein the effective microorganism group accommodated in the continuous expansion culturing apparatus is administered to the sewage in a plurality of times while gradually decreasing the dose of the effective microorganisms. .
前記有効微生物群として第1の嫌気性菌、通性嫌気性菌・好気性菌及び第2の嫌気性菌を前記連続拡大培養装置でそれぞれ別々に培養し、これらの菌を所定の割合で前記汚水に投与するようにしたことを特徴とする請求項1又は2記載の汚水処理システム。A first anaerobic bacterium, a facultative anaerobic bacterium / aerobic bacterium, and a second anaerobic bacterium are separately cultured in the continuous expansion cultivator as the effective microorganism group, and these bacterium are isolated at a predetermined ratio. The sewage treatment system according to claim 1, wherein the sewage is administered to sewage. 前記第1及び第2の嫌気性菌を70%以上、通性嫌気性・好気性菌を5〜10%の割合で前記汚水に投与することを特徴とする請求項3記載の汚水処理システム。4. The sewage treatment system according to claim 3, wherein the first and second anaerobic bacteria are administered to the sewage at a ratio of 70% or more and the facultative anaerobic / aerobic bacteria at a ratio of 5 to 10%. 5. 前記第1の嫌気性菌は乳酸菌、前記通性嫌気性菌・好気性菌は放線菌、前記第2の嫌気性菌は光合成細菌であることを特徴とする請求項2〜4のいずれか1項記載の汚水処理システム。The said 1st anaerobic bacterium is a lactic acid bacterium, said facultative anaerobic bacterium / aerobic bacterium is an actinomycete, and said 2nd anaerobic bacterium is a photosynthetic bacterium. A sewage treatment system according to any one of the preceding claims. 汚水を一時貯留すると共に汚水に含まれる有機物を有効微生物群と反応させて汚水処理する反応槽と、
予め設定されたプログラムに従って前記有効微生物群を連続的に培養すると共に前記反応槽の汚水に対し複数回に分けて前記有効微生物群を投与する連続拡大培養装置と
を備えたことを特徴とする汚水処理システム。
A reaction tank for temporarily storing the sewage and reacting the organic matter contained in the sewage with effective microorganisms to treat the sewage;
Sewage, comprising: a continuous expansion culturing apparatus for continuously culturing the effective microorganisms according to a preset program and administering the effective microorganisms in a plurality of times to the sewage in the reaction tank. Processing system.
前記連続拡大培養装置は、前記反応槽に対する1回の投与量を徐々に減じながら複数回に分けて前記有効微生物群を前記汚水に投与するものであることを特徴とする請求項6記載の汚水処理システム。The sewage according to claim 6, wherein the continuous expansion culturing device is configured to administer the effective microorganism group to the sewage in a plurality of times while gradually reducing a single dose to the reaction tank. Processing system. 第1の嫌気性菌を含む培養液を収容する第1の培養液槽、通性嫌気性・好気性菌を含む培養液を収容する第2の培養液槽、第2の嫌気性菌を含む培養液を収容する第3の培養液槽、前記第1〜第3の培養液槽にそれぞれ水を供給するための給水手段、前記第1〜第3の培養液槽に収容された培養液の液面をそれぞれ検出する第1〜第3の液面検出手段、前記第1〜第3の培養液槽に収容された培養液の温度を検出する第1〜第3の温度検出手段、前記第1〜第3の培養液槽に収容された培養液を加温する第1〜第3の加温手段、及び前記第1〜第3の培養液槽に収容された培養液を所定の割合で汚水に投入する投入手段を備えた培養槽と、
予め設定されたプログラムに従って、前記第1〜第3の加温手段を制御すると共に、前記反応槽に対し複数回に分けて前記有効微生物群を前記汚水に投入するように前記投入手段を制御するコントローラと
を備えたことを特徴とする連続拡大培養装置。
A first culture solution tank containing a culture solution containing a first anaerobic bacterium, a second culture solution tank containing a culture solution containing a facultative anaerobic / aerobic bacterium, and containing a second anaerobic bacterium A third culture solution tank containing a culture solution, water supply means for supplying water to each of the first to third culture solution tanks, and a water supply unit for the culture solution contained in the first to third culture solution tanks. First to third liquid level detecting means for detecting the liquid level, first to third temperature detecting means for detecting the temperature of the culture solution contained in the first to third culture solution tanks, First to third heating means for heating the culture solution contained in the first to third culture solution tanks, and the culture solution contained in the first to third culture solution tanks at a predetermined ratio. A culture tank having an input means for inputting to sewage,
In accordance with a preset program, the first to third heating means are controlled, and the charging means is controlled so that the effective microorganism group is charged into the sewage in the reaction tank in a plurality of times. A continuous expansion culture device comprising a controller.
前記第1の嫌気性菌は乳酸菌、前記通性嫌気性菌・好気性菌は放線菌、前記第2の嫌気性菌は光合成細菌であることを特徴とする請求項8記載の連続拡大培養装置。The continuous expansion culture apparatus according to claim 8, wherein the first anaerobic bacterium is a lactic acid bacterium, the facultative anaerobic bacterium / aerobic bacterium is an actinomycete, and the second anaerobic bacterium is a photosynthetic bacterium. .
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011189249A (en) * 2010-03-12 2011-09-29 Nippon Steel Corp Biological nitrogen treatment method for ammonia-containing waste water

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011189249A (en) * 2010-03-12 2011-09-29 Nippon Steel Corp Biological nitrogen treatment method for ammonia-containing waste water

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