JP4334084B2 - Start-up method of membrane separation activated sludge treatment tank - Google Patents

Start-up method of membrane separation activated sludge treatment tank Download PDF

Info

Publication number
JP4334084B2
JP4334084B2 JP28743899A JP28743899A JP4334084B2 JP 4334084 B2 JP4334084 B2 JP 4334084B2 JP 28743899 A JP28743899 A JP 28743899A JP 28743899 A JP28743899 A JP 28743899A JP 4334084 B2 JP4334084 B2 JP 4334084B2
Authority
JP
Japan
Prior art keywords
tank
activated sludge
sludge
membrane separation
membrane
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
JP28743899A
Other languages
Japanese (ja)
Other versions
JP2001104978A (en
Inventor
太一 上坂
山田  豊
清司 和泉
進 川上
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP28743899A priority Critical patent/JP4334084B2/en
Publication of JP2001104978A publication Critical patent/JP2001104978A/en
Application granted granted Critical
Publication of JP4334084B2 publication Critical patent/JP4334084B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

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

  • Activated Sludge Processes (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、膜分離活性汚泥処理槽の運転立上方法に関し、し尿処理、下水処理、浄化槽等において膜分離活性汚泥法を用いる曝気槽の運転を立ち上げる技術に係るものである。
【0002】
【従来の技術】
従来、有機性廃水を処理する方法として、古くから活性汚泥法が用いられてきた。この活性汚泥は微生物群の総称であり、排水中に含まれる汚濁成分とその量によって生育する微生物の種類とその数が限定される。
このため、図3に示すように、処理対象のある特定の地域において発生したし尿や下水、またはある特定の施設で発生する廃水を活性汚泥槽(曝気槽)1へ導き、槽内の活性汚泥に汚水中の汚濁物質を捕食させることで、特定の廃水の下で特定の活性汚泥が馴養される。活性汚泥槽1の汚泥混合液は沈殿槽2において活性汚泥と処理水とに分離し、活性汚泥は再び活性汚泥槽1へ返送して汚水処理に供し、処理水を系外へ取り出している。
【0003】
系内において増殖する活性汚泥は、定期的に余剰汚泥として沈殿槽2から汚泥貯留槽3へ引き抜いて貯留し、汚泥が発生した施設内において脱水、乾燥、焼却処分したり、バキューム車4で場外へ搬出して処分している。
ところで、活性汚泥法には、図3に示すように、活性汚泥槽5の内部に浸漬型膜分離装置6を浸漬し、槽内の汚泥混合液を浸漬型膜分離装置6で固液分離し、濾過膜を透過した濾過水を処理水として取り出すことにより、槽内の活性汚泥が系外へ流出することを防止し、槽内に活性汚泥を高濃度に維持する膜分離活性汚泥法がある。
【0004】
この膜分離活性汚泥法においては、新たな施設の初期運転時に、種汚泥を膜分離活性汚泥法を行なう曝気槽に投入して運転の立ち上げを行なっている。この種汚泥は、その施設に流入する被処理水と同等の水質の廃水を処理している既存の水処理施設の曝気槽から採取するもので、活性汚泥を含む曝気槽混合液、もしくは余剰汚泥である。この既存の水処理施設の曝気槽は、膜分離活性汚泥法の他、標準活性汚泥法、長時間曝気法を用いるものや接触曝気槽である場合が多い。
【0005】
ところで、投入する種汚泥の量が運転立上に必要な十分な量よりも少ない場合、あるいは当該施設と同等の水質の廃水を処理している既存の水処理施設の曝気槽混合液、もしくは余剰汚泥を入手できない場合には、便宜的な手法として、異なった水質の廃水を処理している既存の水処理施設の曝気槽混合液、もしくは余剰汚泥を種汚泥として投入し、投入した種汚泥中にわずかに含まれる適性な微生物種を自然増殖させ、槽内の活性汚泥を当該施設に流入する被処理水に適した微生物群に馴養する初期運転を行なっている。
【0006】
また、他の手法として、特公平6−73451号に開示するように、種汚泥を乾燥、固化して保存性を高めるとともに、高濃度化したものを作成し、これを膜分離活性汚泥法のみならず、一般的な活性汚泥法に適用するものがある。
【0007】
【発明が解決しようとする課題】
ところで、種汚泥はその変質を防ぐために、他の施設からの運搬に際しては短時間の内に迅速に行なう必要ある。しかし、新設した膜分離活性汚泥法の施設が既存の水処理施設から地理的に離れている場合には、種汚泥を短時間の内に搬送することは困難であり、その運搬に掛かる費用も高くなるために、種汚泥を多量に採取することをあきらめる場合が多かった。
【0008】
標準活性汚泥法や長時間曝気法を用いる曝気槽、あるいは接触曝気槽から採取する種汚泥は、通常において汚泥中に含まれる微生物濃度が薄く、濃縮操作を行なわない限り、必要量の活性汚泥を確保するために多量に採取して運搬する必要がある。このため、意味のない無駄な水を多量に運搬するために多くの費用が掛かっていた。さらに、これらの種汚泥は、微生物とともに微生物の代謝物も含んでおり、それらの粒径や親水性の関係で、膜分離活性汚泥法に使用する膜が目詰まりし易い傾向があった。
【0009】
特公平6−73451号に開示するように、種汚泥を作成保存する場合には、十分な時間を掛けて乾燥させれば、量を増やすことが可能であるが、上記した質の問題は同様にある。この方法では微生物とともに微生物の代謝物質が多く含まれて固形化しており、被処理水の対象有機物が固形物内部で拡散し難いために生物活性が低い問題があった。また、作成汚泥は固形物質であり、生物膜法、ろ床法のような方法で微生物を固定状態で利用する方法では問題はないが、膜分離活性汚泥法のように、曝気することにより微生物を浮遊状態で利用する方法では、固化した微生物が沈んでしまい、固形物中の微生物が水と接触しにくい。また、仮に曝気強度を強くして浮遊させた場合であっても、固形物質が膜表面を傷つけてしまうことが考えられる。
【0010】
本発明は上記した課題を解決するものであり、種汚泥中に微生物が高濃度に存在し、かつ微生物の代謝物質等のように膜分離に有害な物質が含まれず、種汚泥の微生物が固化しないで容易に水に分散する膜分離活性汚泥処理槽の運転立上方法を提供することを目的とする。
【0011】
【課題を解決するための手段】
上記課題を解決するために、請求項1に係る本発明の膜分離活性汚泥処理槽の運転立上方法は、既存排水処理系から引き抜いた活性汚泥を膜分離馴養槽へ投入し、膜分離馴養槽に既存排水処理系へ流入する廃水の一部を導くとともに、空気を散気して酸素を供給し、僅かな栄養源が流入して栄養源が不足する状態で活性汚泥の微生物群が汚泥中に含まれた有機質からなる粘着性物質を微生物分解して増殖することで活性汚泥を馴養し、膜分離馴養槽内に浸漬した浸漬型膜分離装置で固液分離して分離液を槽外へ取り出すことにより槽内の活性汚泥濃度を高め、膜分離馴養槽から引き抜いた高濃度活性汚泥よりなる湿状種汚泥を新設の膜分離活性汚泥処理槽へ投入して初期運転を行なう構成としたものである。
【0012】
上記した構成により、膜分離馴養槽において、槽内に散気する空気によって酸素を供給し、僅かな栄養源が流入する状態で活性汚泥を馴養すると、活性汚泥の微生物群は、不足する栄養源として汚泥中に含まれた糖分や蛋白質等の有機質からなる粘着性物質を微生物分解して増殖する。
この活性汚泥を浸漬型膜分離装置で固液分離して、槽内の活性汚泥の固形物濃度を例えばSS20000mg/L以上に保持することにより、種汚泥中に微生物が高濃度に存在し、新設の膜分離活性汚泥処理槽へ搬送する種汚泥の運搬量を軽減できる。また、微生物の代謝物である多糖類、細胞壁の残骸などの粘着性物質を微生物分解によって除去することにより、膜分離馴養槽から引き抜いた活性汚泥は、新設の膜分離活性汚泥処理槽における膜を目詰まりさせることなく、容易に水に分散して短日時に微生物群が増殖するので、速やかな運転の立ち上げを行なえる。
【0015】
【発明の実施の形態】
以下、本発明の実施の形態を図面に基づいて説明する。図1において、既存排水処理系10は標準活性汚泥法を行なう施設であり、処理対象のある特定の地域において発生したし尿や下水、またはある特定の施設で発生する廃水を活性汚泥槽(曝気槽)11へ導き、廃水を活性汚泥処理する。この既存排水処理系10は、その廃水の水質が新設の処理施設における被処理水の水質に似たものであることが望ましい。
【0016】
活性汚泥槽11の汚泥混合液は沈殿槽12において活性汚泥と処理水とに分離し、活性汚泥は再び活性汚泥槽11へ返送して汚水処理に供し、処理水を系外へ取り出す。沈殿槽12の活性汚泥は汚泥貯留槽13へ引き抜いて貯留し、種汚泥原料として膜分離馴養槽14へ投入する。この標準活性汚泥法の種汚泥はSS5000mg/Lである。膜分離馴養槽14に既存排水処理系10へ流入する廃水の一部を導くとともに、空気を散気して活性汚泥を馴養する。
【0017】
膜分離馴養槽14は内部に浸漬型膜分離装置15を浸漬しており、浸漬型膜分離装置15は膜モジュール16と膜モジュール16の下方に配置した散気装置17を有し、散気装置17に接続してブロア(図示省略)を設けている。膜モジュール16は、鉛直方向に沿って配置する複数枚の平板状膜カートリッジを平行に配列したものであり、膜カートリッジはABS樹脂等の剛体からなる濾板の両表面に有機膜からなる濾過膜を配置したものである。膜モジュール16は駆動方式として槽内の水頭を利用する重力濾過方式を採用している。膜モジュール13の駆動方式は強制吸引方式でも良い。
【0018】
膜分離馴養槽14において、散気装置17から槽内に散気する空気によって酸素を供給し、僅かな栄養源が流入する状態で活性汚泥を馴養すると、活性汚泥の微生物群は、不足する栄養源として汚泥中に含まれた糖分や蛋白質等の有機質からなる粘着性物質を微生物分解して増殖する。
この膜分離馴養槽14の活性汚泥混合液を浸漬型膜分離装置15により固液分離し、分離液を透過液管18を通して処理水槽19に取り出す。このとき、散気装置17から散気する空気のエアリフト作用によって生起する上向流が膜モジュール16の膜面に掃流として作用し、ケーキ層の付着を抑制する。
【0019】
この操作によって、槽内の活性汚泥濃度(固形物濃度)を例えばSS20000mg/L以上に保持し、膜分離馴養槽14の高濃度活性汚泥を汚泥引抜管20を通して汚泥貯留槽21に取り出して貯留する。
この汚泥貯留槽21の高濃度活性汚泥を湿状種汚泥としてバキューム車22で、新設の膜分離活性汚泥処理槽23へ投入する。この湿状種汚泥中には微生物が高濃度に存在するので、新設の膜分離活性汚泥処理槽23へ搬送する種汚泥の運搬量を軽減できる。
【0020】
膜分離活性汚泥処理槽23は内部に浸漬型膜分離装置24を浸漬しており、浸漬型膜分離装置24は先に説明したものと同様であるので説明を省略する。新設の膜分離活性汚泥処理槽23では、処理対象となる新たな地域において発生したし尿や下水、または施設で発生する廃水を槽へ導いて活性汚泥処理の初期運転を行ない、微生物を馴養する。
【0021】
このとき、種汚泥は粘着性物質を微生物分解によって除去しているので、新設の膜分離活性汚泥処理槽23における浸漬型膜分離装置24の膜を目詰まりさせることなく、容易に水に分散して膜分離活性汚泥法に適した浮遊性微生物が短日時に増殖するので、速やかな運転の立ち上げを行なえる。また、種汚泥は湿状であるために、浸漬型膜分離装置24の膜面を傷つけることがない。
【0022】
図2は本発明の他の実施の形態を示すものである。図2においては、汚泥貯留槽21の高濃度活性汚泥を原料汚泥として取り出し、脱水機25および乾燥機26において脱水・乾燥・粉末化して乾燥種汚泥を形成し、新設の膜分離活性汚泥処理槽23へ投入して初期運転を行なう。
このことにより、種汚泥の減量化、高濃度化を図ることができ、乾燥種汚泥を搬送車両27で運搬することが容易に行なえる。乾燥汚泥は粘着性物質を微生物分解によって除去してあるので、種汚泥の浮遊性微生物が固化しないで容易に水に分散し、新設の膜分離活性汚泥処理槽23における膜を目詰まりさせることなく、短日時に微生物群が増殖して速やかな運転の立ち上げを行なえる。また、保存性の高まりによって、種汚泥を貯留して一度に多くの微生物を投入することが可能となる。
【0023】
【発明の効果】
以上のように、本発明によれば、膜分離馴養槽において活性汚泥を馴養することにより、活性汚泥の微生物群が不足する栄養源として汚泥中に含まれた糖分や蛋白質等の有機質からなる粘着性物質を微生物分解して増殖するので、種汚泥中に微生物が高濃度に存在し、かつ膜を目詰まりさせる微生物の代謝物である多糖類、細胞壁の残骸などの粘着性物質を除去することができ、新設の膜分離活性汚泥処理槽において、種汚泥が容易に水に分散して短日時に微生物群が増殖するので、速やかな運転の立ち上げを行なえる。乾燥種汚泥においては、保存性の高まりによって一度に多くの微生物を投入することが可能となる。
【図面の簡単な説明】
【図1】本発明の実施の形態における運転立上方法を示すフローシートである。
【図2】本発明の他の実施の形態における運転立上方法を示すフローシートである。
【図3】従来の活性汚泥法による排水処理を示すフローシートである。
【符号の説明】
10 既存排水処理系
11 活性汚泥槽
14 膜分離馴養槽
15 浸漬型膜分離装置
16 膜モジュール
17 散気装置
21 汚泥貯留槽
23 膜分離活性汚泥処理槽
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for starting up a membrane separation activated sludge treatment tank, and relates to a technique for starting up an operation of an aeration tank using a membrane separation activated sludge method in human waste treatment, sewage treatment, septic tank, and the like.
[0002]
[Prior art]
Conventionally, the activated sludge method has been used as a method for treating organic wastewater. This activated sludge is a collective term for a group of microorganisms, and the types and number of microorganisms that grow are limited by the pollutant components contained in the wastewater and the amount thereof.
For this reason, as shown in FIG. 3, human waste and sewage generated in a specific area to be treated or waste water generated in a specific facility is led to an activated sludge tank (aeration tank) 1 to activate the activated sludge in the tank. By precipitating pollutants in the wastewater, specific activated sludge is acclimatized under specific wastewater. The sludge mixed liquid in the activated sludge tank 1 is separated into activated sludge and treated water in the sedimentation tank 2, and the activated sludge is returned again to the activated sludge tank 1 for sewage treatment, and the treated water is taken out of the system.
[0003]
The activated sludge that grows in the system is periodically withdrawn from the sedimentation tank 2 to the sludge storage tank 3 as excess sludge and stored, and then dehydrated, dried, incinerated in the facility where the sludge is generated, or removed by vacuum vehicle 4 It is taken out and disposed of.
By the way, in the activated sludge method, as shown in FIG. 3, the submerged membrane separator 6 is immersed inside the activated sludge tank 5, and the sludge mixed liquid in the tank is solid-liquid separated by the submerged membrane separator 6. There is a membrane separation activated sludge method that prevents the activated sludge in the tank from flowing out of the system by taking out the filtered water that has passed through the filtration membrane as treated water, and maintains the activated sludge in the tank at a high concentration. .
[0004]
In this membrane-separated activated sludge method, seeding sludge is thrown into an aeration tank for performing the membrane-separated activated sludge method during the initial operation of a new facility, and the operation is started. This type of sludge is collected from the aeration tank of an existing water treatment facility that treats wastewater of the same quality as the treated water flowing into the facility. The aeration tank mixture containing activated sludge, or excess sludge It is. The aeration tank of this existing water treatment facility is often a contact aeration tank using a standard activated sludge method or a long-time aeration method in addition to a membrane separation activated sludge method.
[0005]
By the way, if the amount of seed sludge to be input is less than a sufficient amount necessary for operation startup, or an aeration tank mixed solution or surplus of an existing water treatment facility that treats wastewater of the same quality as the facility If the sludge is not available, as a convenient method, the aeration tank mixture or surplus sludge from an existing water treatment facility that treats wastewater of different water quality is used as seed sludge. Appropriate microbial species slightly contained in the plant are allowed to grow naturally, and the initial operation is performed to acclimate the activated sludge in the tank to the microorganism group suitable for the treated water flowing into the facility.
[0006]
As another method, as disclosed in Japanese Patent Publication No. 6-73451, the seed sludge is dried and solidified to improve the storage stability, and a high concentration is prepared. There are some that apply to the general activated sludge process.
[0007]
[Problems to be solved by the invention]
By the way, in order to prevent the seed sludge from deteriorating, it is necessary to carry it out quickly within a short time when transporting it from other facilities. However, if the newly established membrane separation activated sludge process facility is geographically distant from the existing water treatment facility, it is difficult to transport the seed sludge within a short time, and the cost of the transport is also low. In many cases, they gave up collecting a large amount of seed sludge because of the increase.
[0008]
Seed sludge collected from an aeration tank using the standard activated sludge method or the long-term aeration method, or from a contact aeration tank, usually has a low concentration of microorganisms contained in the sludge. To secure it, it is necessary to collect and transport a large amount. For this reason, it has been expensive to transport a large amount of useless water. Furthermore, these seed sludges contain microorganism metabolites as well as microorganisms, and the membranes used in the membrane separation activated sludge method tend to be clogged due to their particle size and hydrophilicity.
[0009]
As disclosed in Japanese Examined Patent Publication No. 6-73451, when creating and storing seed sludge, it is possible to increase the amount if it is dried for a sufficient time, but the above-mentioned quality problems are the same. It is in. This method has a problem that the biological activity is low because a large amount of microbial metabolites are contained together with microorganisms, and the target organic matter of the water to be treated is difficult to diffuse inside the solid matter. The sludge produced is a solid substance, and there is no problem in using microorganisms in a fixed state by methods such as the biofilm method and filter bed method, but the microorganisms can be obtained by aeration as in the membrane separation activated sludge method. In the method of using the cocoon in a floating state, the solidified microorganisms sink, and the microorganisms in the solid matter are difficult to come into contact with water. Further, even if the aeration intensity is increased and suspended, the solid material may damage the film surface.
[0010]
The present invention solves the above-mentioned problems, microorganisms are present in high concentration in the seed sludge, and no substances harmful to membrane separation such as microbial metabolites are contained, and the microorganisms in the seed sludge are solidified. It is an object of the present invention to provide a method for starting up a membrane separation activated sludge treatment tank that can be easily dispersed in water without using it.
[0011]
[Means for Solving the Problems]
In order to solve the above problems, membrane separation active operation start-up process of the sludge treatment tank of the present invention according to claim 1, charged with activated sludge withdrawn from the existing waste water treatment system to membrane separation acclimatization vessel, membrane separation acclimatization A part of the wastewater flowing into the existing wastewater treatment system is introduced into the tank, air is diffused to supply oxygen, and the microorganism group of activated sludge is sludge in a state where a few nutrient sources flow in and nutrient resources are insufficient. The activated sludge is acclimatized by microbial decomposition and growth of the organic adhesive substance contained in it, and the separated liquid is separated from the tank by solid-liquid separation using a submerged membrane separator immersed in the membrane separation habitation tank. The activated sludge concentration in the tank is increased by taking it out to the tank, and wet seed sludge consisting of high-concentration activated sludge extracted from the membrane separation acclimatization tank is introduced into the newly installed membrane separation activated sludge treatment tank for initial operation. Is.
[0012]
With the above configuration, in the membrane separation acclimation tank, oxygen is supplied by air diffused into the tank, and if activated sludge is acclimatized with a small amount of nutrients flowing in, the microorganism group of activated sludge becomes a lack of nutrient sources. As an adhesive substance made of organic substances such as sugar and protein contained in sludge, it is proliferated by microbial decomposition.
This activated sludge is solid-liquid separated with a submerged membrane separator and the solid concentration of the activated sludge in the tank is maintained at, for example, SS20000 mg / L or more, so that microorganisms are present in the seed sludge at a high concentration. The amount of seed sludge transported to the membrane separation activated sludge treatment tank can be reduced. In addition, by removing microbial metabolites such as polysaccharides and cell wall debris by microbial decomposition, the activated sludge extracted from the membrane separation and acclimatization tank is replaced with the membrane in the newly installed membrane separation activated sludge treatment tank. Without clogging, it is easily dispersed in water and the microbial population grows in a short time, so that the operation can be started quickly.
[0015]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings. In FIG. 1, an existing wastewater treatment system 10 is a facility that performs a standard activated sludge method, and excreta and sewage generated in a specific area to be treated, or wastewater generated in a specific facility is an activated sludge tank (aeration tank). ) Lead to 11, and treat the wastewater with activated sludge. In the existing wastewater treatment system 10, it is desirable that the quality of the wastewater is similar to the quality of the water to be treated in the new treatment facility.
[0016]
The sludge mixed liquid in the activated sludge tank 11 is separated into activated sludge and treated water in the sedimentation tank 12, and the activated sludge is returned to the activated sludge tank 11 again for sewage treatment, and the treated water is taken out of the system. The activated sludge in the sedimentation tank 12 is extracted and stored in the sludge storage tank 13, and is put into the membrane separation habitation tank 14 as a seed sludge raw material. The seed sludge of this standard activated sludge method is SS5000 mg / L. A part of the wastewater flowing into the existing wastewater treatment system 10 is guided to the membrane separation habituation tank 14, and the activated sludge is acclimatized by diffusing air.
[0017]
The membrane separation acclimatization tank 14 has a submerged membrane separator 15 immersed therein, and the submerged membrane separator 15 has a membrane module 16 and an air diffuser 17 disposed below the membrane module 16. 17 is provided with a blower (not shown). The membrane module 16 is a parallel arrangement of a plurality of flat membrane cartridges arranged along the vertical direction. The membrane cartridge is a filtration membrane made of an organic membrane on both surfaces of a filter plate made of a rigid body such as ABS resin. Is arranged. The membrane module 16 employs a gravity filtration system that uses the water head in the tank as a drive system. The driving method of the membrane module 13 may be a forced suction method.
[0018]
In the membrane separation acclimatization tank 14, when oxygen is supplied by air diffused from the air diffuser 17 into the tank, and the activated sludge is acclimatized with a small amount of nutrients flowing in, the activated sludge microbial group becomes deficient in nutrients. It grows by microbial degradation of sticky substances made of organic substances such as sugar and protein contained in sludge as a source.
The activated sludge mixed solution in the membrane separation habituation tank 14 is solid-liquid separated by the submerged membrane separation device 15, and the separated liquid is taken out to the treated water tank 19 through the permeate pipe 18. At this time, the upward flow generated by the air lift action of the air diffused from the air diffuser 17 acts as a scavenging on the membrane surface of the membrane module 16 and suppresses the adhesion of the cake layer.
[0019]
By this operation, the activated sludge concentration (solid concentration) in the tank is maintained at, for example, SS 20000 mg / L or more, and the high-concentration activated sludge in the membrane separation habituation tank 14 is taken out into the sludge storage tank 21 through the sludge extraction pipe 20 and stored. .
The high-concentration activated sludge in the sludge storage tank 21 is put into a newly installed membrane separation activated sludge treatment tank 23 by a vacuum wheel 22 as wet seed sludge. Since the microorganisms are present in a high concentration in the wet seed sludge, the amount of seed sludge transported to the newly installed membrane separation activated sludge treatment tank 23 can be reduced.
[0020]
The membrane separation activated sludge treatment tank 23 has a submerged membrane separation device 24 immersed therein, and the submerged membrane separation device 24 is the same as that described above, and a description thereof will be omitted. In the newly installed membrane separation activated sludge treatment tank 23, human waste and sewage generated in a new area to be treated or waste water generated in the facility is guided to the tank to perform the initial operation of the activated sludge treatment and acclimatize the microorganisms.
[0021]
At this time, since the seed sludge has removed the sticky substance by microbial decomposition, it is easily dispersed in water without clogging the membrane of the submerged membrane separation device 24 in the newly installed membrane separation activated sludge treatment tank 23. As the floating microorganisms suitable for the membrane separation activated sludge method grow in a short time, the operation can be started quickly. Moreover, since the seed sludge is wet, the membrane surface of the submerged membrane separator 24 is not damaged.
[0022]
FIG. 2 shows another embodiment of the present invention. In FIG. 2, the high-concentration activated sludge in the sludge storage tank 21 is taken out as raw material sludge, dehydrated, dried and powdered by the dehydrator 25 and dryer 26 to form dry seed sludge, and a newly installed membrane separation activated sludge treatment tank. 23 to perform initial operation.
This makes it possible to reduce the seed sludge and increase its concentration, and it is possible to easily carry the dried seed sludge by the transport vehicle 27. Since the dry sludge has adhesive substances removed by microbial decomposition, the floating microorganisms of the seed sludge are easily dispersed in water without solidification, and without clogging the membrane in the newly installed membrane separation activated sludge treatment tank 23 In a short time, microorganisms can grow and start up quickly. In addition, the increase in storage stability makes it possible to store seed sludge and introduce many microorganisms at once.
[0023]
【The invention's effect】
As described above, according to the present invention, by acclimatizing activated sludge in a membrane separation habitation tank, an adhesive composed of organic substances such as sugar and protein contained in the sludge as a nutrient source lacking the microorganism group of the activated sludge. Since the microorganisms are decomposed and propagated, the microorganisms are present in high concentrations in the seed sludge, and the sticky substances such as polysaccharides and cell wall debris, which are microbial metabolites that clog the membrane, are removed. In the newly installed membrane separation activated sludge treatment tank, the seed sludge is easily dispersed in the water and the microorganism group grows in a short time, so that the operation can be quickly started up. In dry seed sludge, it becomes possible to input many microorganisms at a time due to an increase in storage stability.
[Brief description of the drawings]
FIG. 1 is a flow sheet showing a method for starting operation in an embodiment of the present invention.
FIG. 2 is a flow sheet showing an operation start-up method according to another embodiment of the present invention.
FIG. 3 is a flow sheet showing wastewater treatment by a conventional activated sludge method.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 10 Existing waste water treatment system 11 Activated sludge tank 14 Membrane separation acclimatization tank 15 Immersion type membrane separator 16 Membrane module 17 Air diffuser 21 Sludge storage tank 23 Membrane separated activated sludge treatment tank

Claims (1)

既存排水処理系から引き抜いた活性汚泥を膜分離馴養槽へ投入し、膜分離馴養槽に既存排水処理系へ流入する廃水の一部を導くとともに、空気を散気して酸素を供給し、僅かな栄養源が流入して栄養源が不足する状態で活性汚泥の微生物群が汚泥中に含まれた有機質からなる粘着性物質を微生物分解して増殖することで活性汚泥を馴養し、膜分離馴養槽内に浸漬した浸漬型膜分離装置で固液分離して分離液を槽外へ取り出すことにより槽内の活性汚泥濃度を高め、膜分離馴養槽から引き抜いた高濃度活性汚泥よりなる湿状種汚泥を新設の膜分離活性汚泥処理槽へ投入して初期運転を行なうことを特徴とする膜分離活性汚泥処理槽の運転立上方法。Activated sludge extracted from the existing wastewater treatment system is introduced into the membrane separation habitation tank, and a part of the wastewater flowing into the existing wastewater treatment system is guided to the membrane separation habitation tank, and air is diffused to supply oxygen. The activated sludge microorganisms break down the organic sticky substances contained in the sludge and proliferate, and the activated sludge is acclimatized and the membrane separation acclimatized. Wet seeds consisting of high-concentration activated sludge extracted from the membrane separation acclimatization tank by increasing the activated sludge concentration in the tank by solid-liquid separation with a submerged membrane separator immersed in the tank and taking out the separated liquid from the tank. An operation start-up method of a membrane separation activated sludge treatment tank, wherein sludge is introduced into a newly installed membrane separation activated sludge treatment tank and an initial operation is performed.
JP28743899A 1999-10-08 1999-10-08 Start-up method of membrane separation activated sludge treatment tank Expired - Fee Related JP4334084B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28743899A JP4334084B2 (en) 1999-10-08 1999-10-08 Start-up method of membrane separation activated sludge treatment tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28743899A JP4334084B2 (en) 1999-10-08 1999-10-08 Start-up method of membrane separation activated sludge treatment tank

Publications (2)

Publication Number Publication Date
JP2001104978A JP2001104978A (en) 2001-04-17
JP4334084B2 true JP4334084B2 (en) 2009-09-16

Family

ID=17717332

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28743899A Expired - Fee Related JP4334084B2 (en) 1999-10-08 1999-10-08 Start-up method of membrane separation activated sludge treatment tank

Country Status (1)

Country Link
JP (1) JP4334084B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10259733B2 (en) 2014-03-27 2019-04-16 Mitsubishi Heavy Industries, Ltd. Laundry wastewater biological treatment preparation, and device and method for treating laundry wastewater by using same

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5822260B2 (en) * 2011-06-17 2015-11-24 株式会社クボタ Method for starting up membrane separation activated sludge treatment device and sewage treatment device
JP5822263B2 (en) * 2011-07-25 2015-11-24 株式会社クボタ Method for starting up membrane separation activated sludge treatment equipment
CN107140730A (en) * 2017-07-21 2017-09-08 石家庄顺时科技有限公司 A kind of emergent ancillary equipment of bioanalysis sewage disposal system activated sludge and method
JP2021139661A (en) * 2020-03-03 2021-09-16 国立大学法人 東京大学 Device and method for processing effluent by microorganisms
CN113023885B (en) * 2021-04-07 2022-06-07 知和环保科技有限公司 Process for directionally strengthening sludge and application method thereof
CN113666488B (en) * 2021-09-03 2023-03-14 广西峰之慧科技发展有限公司 Biochemical treatment device for realizing high-concentration activated sludge process

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10259733B2 (en) 2014-03-27 2019-04-16 Mitsubishi Heavy Industries, Ltd. Laundry wastewater biological treatment preparation, and device and method for treating laundry wastewater by using same

Also Published As

Publication number Publication date
JP2001104978A (en) 2001-04-17

Similar Documents

Publication Publication Date Title
US8535532B2 (en) Systems and methods for wastewater treatment
EP1562867A1 (en) Water treatment method using an inorganic powder reagent with high specific surface area including a step of recycling said reagent
WO2012133386A1 (en) Wastewater treatment method and wastewater treatment system
JPH06285496A (en) Hollow fiber membrane separation biological treatment and device for organic drainage
JP4334084B2 (en) Start-up method of membrane separation activated sludge treatment tank
KR100698522B1 (en) Purifying system of excretions using microorganism
KR100872863B1 (en) Treatment apparatus of sewage water for removing stench and improving efficiency of filtration
KR20090049671A (en) Developing resources to excretions in livestock farming and an apparatus for purifying them thereof
JP2010207657A (en) Wastewater treatment apparatus and wastewater treatment method
JPH0957289A (en) Biological treating device of fluidized bed type
JP2012101154A (en) Sewage cleaning apparatus and sewage cleaning method
CN214060279U (en) Mariculture tail water recycling device
JP3629727B2 (en) Organic wastewater treatment method and apparatus
JPH11104698A (en) Drainage treatment method
JP3657153B2 (en) Method for producing seeding agent
CN211170054U (en) Microbial film high efficiency processing device
JPS61271090A (en) Treating device for waste water using immobilized microorganism
KR100714825B1 (en) Method for treating sewage and high organic loading wastewater by anaerobic/oxic process with membrane and biological aerated filter
KR100751002B1 (en) Advanced treatment apparatus for organic wastewater using pyramid-reactor
KR20030097075A (en) Hybrid Submerged Plate Type Membrane Bioreactor Using microfilter Combined With Biofilm-Activated Carbon for Advanced Treatment of Sewage and Wastewater
JP2002223667A (en) Rearing equipment for fish and shell fish
JP2002136952A (en) Jellyfish treatment method and apparatus
WO2006066407A1 (en) Method for treatment of highly-loaded effluent
JP3939108B2 (en) Method for producing seeding agent for membrane separation activated sludge
JP2008092846A (en) Circulation type fish-farming system

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20050908

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20071001

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20071009

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20071207

RD02 Notification of acceptance of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7422

Effective date: 20090323

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20090331

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20090424

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20090526

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20090623

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120703

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Ref document number: 4334084

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120703

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130703

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140703

Year of fee payment: 5

LAPS Cancellation because of no payment of annual fees