JP2008168204A - Sewage treatment method and sponge carrier used therefor - Google Patents
Sewage treatment method and sponge carrier used therefor Download PDFInfo
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- JP2008168204A JP2008168204A JP2007003669A JP2007003669A JP2008168204A JP 2008168204 A JP2008168204 A JP 2008168204A JP 2007003669 A JP2007003669 A JP 2007003669A JP 2007003669 A JP2007003669 A JP 2007003669A JP 2008168204 A JP2008168204 A JP 2008168204A
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Abstract
Description
本発明は、スポンジ担体を用いた有機性汚水の活性汚泥処理方法及びそのスポンジ担体に関し、特に、曝気槽へ投入するスポンジ担体に処理を施した汚水処理方法及びそのスポンジ担体に関する。 The present invention relates to an activated sludge treatment method for organic sewage using a sponge carrier and its sponge carrier, and more particularly to a sewage treatment method for treating a sponge carrier to be fed into an aeration tank and its sponge carrier.
従来から、下水、排水、し尿等の有機性汚水の活性汚泥処理方法では、有機性汚水を曝気槽で活性汚泥と混合、曝気して、次に固液分離槽において汚泥を分離し、分離液を処理済水として排出すると共に、分離した汚泥の一部を返送汚泥として曝気槽へ返送し、残りの汚泥を余剰汚泥として排出している。 Conventionally, in an activated sludge treatment method for organic sewage such as sewage, wastewater, human waste, etc., organic sludge is mixed with aerated sludge in an aeration tank, then aerated, and then sludge is separated in a solid-liquid separation tank. Is discharged as treated water, part of the separated sludge is returned to the aeration tank as return sludge, and the remaining sludge is discharged as excess sludge.
又、上述のような複数の槽を備えた施設ではなく、1槽で曝気、分離等を行う回分式の活性汚泥処理方法も用いられている。尚、この回分式で用いる槽も、ブロアや散気管等で構成される曝気装置を備えるので、以下で説明する曝気槽には回分式で用いる槽も含まれる。 Further, a batch type activated sludge treatment method in which aeration, separation, and the like are performed in one tank is used instead of a facility having a plurality of tanks as described above. In addition, since the tank used by this batch type is also provided with the aeration apparatus comprised by a blower, a diffuser tube, etc., the tank used by a batch type is also contained in the aeration tank demonstrated below.
そして、曝気槽には、有機物を分解する微生物、この微生物を繁殖させるための栄養剤等が投入されると共に、微生物を保持する担体を投入し、微生物が付着した担体を槽内で流動させて汚水を処理することにより、曝気槽内に微生物を高濃度に保持し、汚水の高負荷処理を可能としている(例えば特許文献1参照。)。 The aeration tank is loaded with microorganisms that decompose organic matter, nutrients for propagating the microorganisms, and a carrier that holds the microorganisms, and the carrier to which the microorganisms are attached flows in the tank. By treating the sewage, the microorganisms are kept at a high concentration in the aeration tank, thereby enabling a high load treatment of the sewage (see, for example, Patent Document 1).
このような微生物を付着させる担体としては、多孔質であれば特に限定されず、セラミック、シリカゲル、ゼオライト、ガラスビーズ等の無機物、セルロース、海綿等の天然高分子、ポリウレタン、ポリスチレン等の合成高分子等様々なものが用いられている。 The carrier for adhering such microorganisms is not particularly limited as long as it is porous. Natural materials such as ceramic, silica gel, zeolite, and glass beads, natural polymers such as cellulose and sponge, and synthetic polymers such as polyurethane and polystyrene. Etc. are used.
しかし、一般的にセラミック等無機物の担体は、汚水との初期馴染みはよいが、比重が大きく、沈降し易く、曝気による水流では、曝気槽底部へ沈積し易く、曝気槽内を充分に流動させることが困難であり、曝気槽内での担体濃度が偏り、処理能力が低下するといった問題点もあった。又、天然高分子はコストが高い等の欠点もある。 However, in general, inorganic carriers such as ceramics have a good initial familiarity with sewage, but have a large specific gravity and are easy to settle. There is also a problem that the carrier concentration in the aeration tank is biased and the processing capacity is lowered. Natural polymers also have disadvantages such as high cost.
そこで、水を含有した際に水と同じ程度の比重となり、流動しやすいこと、即ち比重が小さく、曝気槽内での担体濃度が偏りが生じにくく、取扱いが容易で、しかも廉価な合成高分子である合成スポンジが多用されている。そして、合成高分子の担体としては、ポリエーテル系ウレタンフォームをスポンジ状小片にしたものも提案されている(例えば特許文献2参照。)。 Therefore, when it contains water, it has the same specific gravity as water, it is easy to flow, that is, the specific gravity is small, the carrier concentration in the aeration tank is not easily biased, easy to handle, and inexpensive synthetic polymer. Synthetic sponges are often used. A synthetic polymer carrier in which a polyether urethane foam is formed into a sponge-like piece has also been proposed (see, for example, Patent Document 2).
しかし、このようなスポンジを担体として使用した場合、汚水処理装置・施設の立ち上げ時やスポンジ担体の交換時に、新たなスポンジ担体を曝気槽に投入する際に、スポンジ担体は汚水との馴染みが悪く、即ち吸水性が低いので、ただ投入しただけでは全く水を吸収せずに、汚水表面に浮いてしまい、更に、浮いた担体の上に他の担体が積層し、全く汚水に接しない担体が多数存在してしまい、しかもそのまま放置しておいた場合には、曝気槽の大きさや投入する担体の量にもよるが、投入した略総ての担体が水を吸収して、曝気槽内を流動するためには数時間から数十日はかかり、その間は微生物担体としての役割を全く果たせず、汚水処理装置・施設の処理能力が著しく低い状態となり或いは低下し、立ち上げに長い時間を要し、その間は安定した処理が行えないといった問題点があった。 However, when such a sponge is used as a carrier, when the new sponge carrier is introduced into the aeration tank at the time of starting up the sewage treatment apparatus / facility or replacing the sponge carrier, the sponge carrier is familiar with the sewage. It is bad, that is, its water absorption is low, so if it is just added, it will not absorb water at all and will float on the surface of sewage, and other carriers will be laminated on the floated carrier and will not come into contact with sewage at all. However, depending on the size of the aeration tank and the amount of carrier to be introduced, almost all of the introduced carriers absorb water, It takes several hours to several tens of days to flow, and during that time it does not play a role as a microbial carrier at all, and the treatment capacity of the sewage treatment equipment / facility becomes extremely low or decreases, and it takes a long time to start up. In short, that There is a problem that can not perform stable processing.
そこで、本発明は、従来技術の欠点を解消し、曝気槽に投入するスポンジ担体を、迅速に汚水と馴染ませて、吸水させ、曝気槽内を流動可能として、汚水処理装置・施設の立ち上げ時間を短縮すること、スポンジ担体の投入直後よりその機能を充分に発揮させ、立ち上げ時でも処理能力を高い状態とすること、担体の交換時にも処理能力を高い状態に保つことを目的とする。 Therefore, the present invention eliminates the drawbacks of the prior art and allows the sponge carrier to be put into the aeration tank to quickly become familiar with the sewage, absorb the water, and flow inside the aeration tank, thereby starting up the sewage treatment apparatus / facility. The purpose is to shorten the time, to fully demonstrate its functions immediately after the sponge carrier is charged, to keep the processing capacity high even at startup, and to keep the processing capacity high even when the carrier is replaced. .
上記課題を解決するための手段としての本発明は、スポンジ担体の親水性を向上させるための親水性向上剤をスポンジ担体に塗布・含浸させるものであり、又、このようなスポンジ担体に有機物を分解する微生物、更にはこの微生物の栄養分を担持させるものである。 The present invention as a means for solving the above problems is to apply and impregnate a sponge carrier with a hydrophilicity improver for improving the hydrophilicity of the sponge carrier. It is intended to carry the microorganisms to be decomposed and the nutrients of these microorganisms.
具体的には、活性汚泥法を用いて有機性汚水を処理する設備において、曝気槽へ投入され、微生物を保持するためのスポンジ担体であって、親水性向上剤を含浸させたことを特徴とするスポンジ担体である。 Specifically, in a facility for treating organic sewage using an activated sludge method, a sponge carrier for retaining microorganisms, which is introduced into an aeration tank, and is characterized by being impregnated with a hydrophilicity improver. Sponge carrier.
又、前記スポンジ担体に、微生物及び/又は栄養成分を担持させたスポンジ担体である。 Further, the sponge carrier is a sponge carrier in which microorganisms and / or nutrient components are supported.
又、活性汚泥法を用いて有機性汚水を処理する設備において、微生物を保持するためのスポンジ担体の曝気槽への新規投入において、親水性向上剤を含浸させたスポンジ担体を用いることを特徴とする汚水処理方法である。 In addition, in a facility for treating organic sewage using the activated sludge method, a sponge carrier impregnated with a hydrophilicity improver is used in a new introduction of a sponge carrier for holding microorganisms into an aeration tank. This is a wastewater treatment method.
又、前記スポンジ担体は、曝気槽への新規投入前に、予め親水性向上剤を含浸させておくことを特徴とする汚水処理方法である。 The sponge carrier is a sewage treatment method in which a hydrophilicity improver is impregnated in advance before the sponge carrier is newly introduced into the aeration tank.
又、前記スポンジ担体は、曝気槽内で親水性向上剤を含浸させることを特徴とする汚水処理方法である。 The sponge carrier is a sewage treatment method characterized by impregnating a hydrophilicity improver in an aeration tank.
又、前記スポンジ担体に、曝気槽への新規投入前に、予め微生物及び/又は栄養成分を担持させることを特徴とする汚水処理方法である。 Further, the present invention is a sewage treatment method characterized in that microorganisms and / or nutrient components are supported in advance on the sponge carrier before new introduction into an aeration tank.
以上のような本発明によれば、活性汚泥法を用いて有機性汚水を処理する設備において、曝気槽へ投入され、微生物を保持するためのスポンジ担体に親水性向上剤を含浸させたので、曝気槽に投入するスポンジ担体を、迅速に汚水と馴染ませて、吸水させ、曝気槽内を流動可能として、汚水処理装置・施設の立ち上げ時間を短縮すること、スポンジ担体の投入直後よりその機能を充分に発揮させ、立ち上げ時でも処理能力を高い状態とすること、担体の交換時にも処理能力を高い状態に保つことが可能となった。 According to the present invention as described above, in the facility for treating organic sewage using the activated sludge method, the sponge carrier for retaining microorganisms was impregnated with the hydrophilicity improver in the aeration tank. The sponge carrier to be put into the aeration tank can be quickly mixed with sewage, absorbed, and flowable in the aeration tank, shortening the start-up time of the sewage treatment equipment / facility, and the function immediately after the sponge carrier is put in It has become possible to make the processing capacity high even at the time of start-up, and to maintain the high processing capacity even when the carrier is replaced.
更に、該スポンジ担体に微生物及び/又は栄養成分を担持させたので、曝気槽内で、スポンジ担体に微生物が付着するまでの待ち期間がなく、更に効率よく、汚水処理装置・施設の立ち上げ時間を短縮すること、スポンジ担体の投入直後よりその機能を充分に発揮させ、立ち上げ時でも処理能力を高い状態とすること、担体の交換時にも処理能力を高い状態に保つことが可能となった。特に栄養分も担持させることにより、微生物の増殖が効率よく図れ、更に上述の効果を高めることが出来た。 Furthermore, since microorganisms and / or nutrient components are supported on the sponge carrier, there is no waiting period until the microorganisms adhere to the sponge carrier in the aeration tank, and the startup time of the sewage treatment apparatus / facility is more efficient. It has become possible to fully demonstrate its functions immediately after the sponge carrier is charged, to maintain a high processing capacity even at startup, and to maintain a high processing capacity even when replacing the carrier. . In particular, by supporting nutrients, microorganisms can be efficiently propagated, and the above-described effects can be further enhanced.
又、活性汚泥法を用いて有機性汚水を処理する設備において、微生物を保持するためのスポンジ担体の曝気槽への新規投入において、親水性向上剤を含浸させたスポンジ担体を用いたので、曝気槽に投入するスポンジ担体を、迅速に汚水と馴染ませて、吸水させ、曝気槽内を流動可能として、汚水処理装置・施設の立ち上げ時間を短縮すること、スポンジ担体の投入直後よりその機能を充分に発揮させ、立ち上げ時でも処理能力を高い状態とすること、担体の交換時にも処理能力を高い状態に保つことが可能となった。 In addition, in a facility for treating organic sewage using the activated sludge method, since a sponge carrier impregnated with a hydrophilicity improver was used in the introduction of a sponge carrier to retain microorganisms into an aeration tank, aeration The sponge carrier to be put into the tank can be quickly mixed with sewage, absorbed, and allowed to flow in the aeration tank, shortening the start-up time of the sewage treatment device / facility, and the function immediately after the sponge carrier is put in. It was made possible to fully demonstrate it, and it was possible to keep the processing capacity high even at the time of start-up, and to keep the processing capacity high even when the carrier was replaced.
又、上記方法において、前記スポンジ担体は、曝気槽への新規投入前に、予め親水性向上剤を含浸させておいたので、スポンジ担体の曝気槽への新規投入時に特別な工程を経ることがなく、容易且迅速に投入することが出来た。 Further, in the above method, the sponge carrier is impregnated with a hydrophilicity improver in advance before being newly introduced into the aeration tank, so that a special process may be performed when the sponge carrier is newly introduced into the aeration tank. And was able to be introduced easily and quickly.
又、上記方法において、前記スポンジ担体は、曝気槽内で親水性向上剤を含浸させるので、投入する曝気槽の実情に合わせてスポンジ担体を用いることが出来、より効率よく上記の効果を奏することが出来、又、親水性向上剤を含浸させたスポンジ担体を保存、運搬する必要がなく容易に作業を行うことが可能となった。 Further, in the above method, since the sponge carrier is impregnated with the hydrophilicity improver in the aeration tank, the sponge carrier can be used according to the actual situation of the aeration tank to be added, and the above effect can be achieved more efficiently. In addition, the sponge carrier impregnated with the hydrophilicity improver need not be stored and transported, and can be easily operated.
又、上記方法において、前記スポンジ担体に、曝気槽への新規投入前に、予め微生物及び/又は栄養成分を担持させたので、曝気槽内で、スポンジ担体に微生物が付着するまでの待ち期間がなく、更に効率よく、汚水処理装置・施設の立ち上げ時間を短縮すること、スポンジ担体の投入直後よりその機能を充分に発揮させ、立ち上げ時でも処理能力を高い状態とすること、担体の交換時にも処理能力を高い状態に保つことが可能となった。特に栄養分も担持させることにより、微生物の増殖が効率よく図れ、更に上述の効果を高めることが出来た。 In the above method, since the microorganisms and / or nutrients are loaded in advance on the sponge carrier before the introduction into the aeration tank, there is a waiting period until the microorganisms adhere to the sponge carrier in the aeration tank. Efficiently reduce the start-up time of the sewage treatment equipment / facility, fully demonstrate its functions immediately after the sponge carrier is introduced, and increase the treatment capacity even at the start-up, carrier exchange Sometimes it was possible to keep the processing capacity high. In particular, by supporting nutrients, microorganisms can be efficiently propagated, and the above-described effects can be further enhanced.
以下本発明を詳細に説明する。本発明のスポンジ担体及び汚水処理方法は、有機性汚水の活性汚泥処理方法を用いた汚水処理装置における汚水処理において用いられる。 The present invention will be described in detail below. The sponge carrier and the sewage treatment method of the present invention are used in sewage treatment in a sewage treatment apparatus using an activated sludge treatment method for organic sewage.
このような汚水処理装置100は、流量調整槽1、曝気槽2、固液分離槽3、汚泥濃縮槽4、汚泥貯留槽5等を備えて構成され、集められた下水、排水、し尿等の有機性汚水を流量調整槽1で貯留し、処理する汚水の量を調整して曝気槽2へ送る。曝気槽2には、汚水30と共に、スポンジ担体10、微生物、活性汚泥等が収容されている。このスポンジ担体10には、微生物が付着している。
Such a
曝気槽2の底部には、曝気槽2内に空気等の一定量の酸素を含有する気体を送るブロア21と接続された散気管22を備えた曝気装置が設けられ、該散気管22から空気等の酸素含有気体が曝気槽2内に連続的に供給されている。この気体の供給、曝気により、曝気槽2内で汚水に、図2の矢印Aで示すような対流が生じて、汚水30と活性汚泥が混合されると共に、微生物に酸素を供給している。スポンジ担体10は、散気管22から供給される空気により曝気槽2内で生じている対流に従って、汚水30内を流動する。曝気槽2では、微生物の働きにより、有機性物質を分解し、汚水を処理している。
At the bottom of the
曝気槽2で処理された汚水は、活性汚泥との混合液となって固液分離槽3へ送られ、ここで、処理済水と汚泥に分離される。そして、処理済水は排出され、汚泥の一部は、図示しないポンプで、返送汚泥として返送汚泥ライン6で曝気槽2へ返送され、一部は余剰汚泥として余剰汚泥ライン7で汚泥濃縮槽4へ送られ、汚泥濃縮槽4で濃縮され、汚泥貯留槽5へ送られ、廃棄される。尚、曝気槽2の流出口には、スポンジ担体10の流出を防止するために網等が設けられている。
The sewage treated in the
尚、上記説明では、曝気槽、固液分離槽等複数の槽を備えた処理装置で説明しているが、本発明は、このような処理装置に限定されることなく、複数の槽を備えるのではなく、1槽で曝気、分離等の複数の処理を行う回分式の活性汚泥処理装置においても用いることが出来る。従って、この回分式で用いる槽も、ブロアや散気管等で構成される曝気装置を備えるので、本発明でいう曝気槽には回分式で用いる槽も含まれる。 In the above description, the processing apparatus including a plurality of tanks such as an aeration tank and a solid-liquid separation tank is described. However, the present invention is not limited to such a processing apparatus, and includes a plurality of tanks. Instead, it can also be used in a batch activated sludge treatment apparatus that performs a plurality of treatments such as aeration and separation in one tank. Therefore, since the tank used in the batch type also includes an aeration apparatus constituted by a blower, an air diffuser, etc., the tank used in the batch type is also included in the aeration tank referred to in the present invention.
本発明で用いるスポンジ担体としては、多孔質で、曝気槽の汚水の中で流動可能であれば特に限定されないが、その密度に関しては、比重が低く、含水した際に水と同程度の比重となるものを用いることにより、曝気槽内で良好に流動可能となるので好ましく、又、高表面積のものが好ましい。スポンジ担体としては、海綿の天然スポンジや、合成スポンジが挙げられ、合成スポンジとしては、エーテル系又はエステル系のポリウレタンフォーム、ポロン・ナンネックス、ポリエチレンスポンジやポリプロピレンスポンジ等のポリオレフィンフォーム、ゴムスポンジ、ラテックススポンジ等が挙げられる。 The sponge carrier used in the present invention is not particularly limited as long as it is porous and can flow in the sewage in the aeration tank, but the density is low and the specific gravity is the same as that of water when it is hydrated. By using this, it is preferable because it can flow well in the aeration tank, and a high surface area is preferable. Examples of sponge carriers include sponge natural sponges and synthetic sponges. Examples of synthetic sponges include ether foams or ester polyurethane foams, polyolefin foams such as polyethylene sponge and polypropylene sponge, rubber sponges, and latex. A sponge etc. are mentioned.
スポンジ担体の形状は特に限定されず、粒状、球状、角柱状、ペレット状、円筒状、繊維状、フィルム状等その他各種の形状とすることが出来る。又、その寸法も特に限定されず、曝気槽の大きさやスポンジ担体の形状、投入量等に応じて、製造及び取扱いが容易で、曝気槽からの漏出を防止でき、汚水との接触効率、微生物の担持効率を考慮して、適宜のサイズのものを用いればよい。 The shape of the sponge carrier is not particularly limited, and may be various other shapes such as a granular shape, a spherical shape, a prism shape, a pellet shape, a cylindrical shape, a fiber shape, and a film shape. Also, the dimensions are not particularly limited, and it is easy to manufacture and handle depending on the size of the aeration tank, the shape of the sponge carrier, the input amount, etc., can prevent leakage from the aeration tank, the efficiency of contact with sewage, microorganisms In consideration of the carrying efficiency, a material having an appropriate size may be used.
スポンジ担体の投入量は、特に限定されず、通常の投入量の範囲で行うが、容積比で、曝気槽の略20〜35%程度の投入量が好ましい。 The input amount of the sponge carrier is not particularly limited, and it is performed within the range of the normal input amount. However, the input amount is approximately 20 to 35% of the aeration tank in terms of volume ratio.
スポンジ担体の親水性向上剤としては、界面活性剤、アルコール類、脂肪酸類、アセトン、アンモニア水、アミン類等が挙げられ、これらのうち1種又は2種以上を適宜混合して用いることが出来る。界面活性剤は陰イオン界面活性剤、陽イオン界面活性剤、非イオン界面活性剤、両性界面活性剤の何れを使用してもよく、アルコール類としては、メタノール、エタノール、プロパノール等特に限定されず、脂肪酸類としては、蟻酸、酢酸、プロピオン酸等特に限定されず、アミン類としては、メチルアミン、エチルアミン等特に限定されずに用いることが出来る。 Examples of the hydrophilicity improver of the sponge carrier include surfactants, alcohols, fatty acids, acetone, ammonia water, amines, and the like, and one or more of these can be used as appropriate. . As the surfactant, any of an anionic surfactant, a cationic surfactant, a nonionic surfactant and an amphoteric surfactant may be used, and alcohols are not particularly limited, such as methanol, ethanol, propanol and the like. The fatty acids are not particularly limited, such as formic acid, acetic acid, propionic acid, and the like, and the amines can be used without being particularly limited, such as methylamine and ethylamine.
これらの親水性向上剤のうち、特に界面活性剤が親水性向上の効果が高く、低濃度でも充分に効果を発揮するので、望ましく、最も実用的である。又、界面活性剤の中では、陰イオン性界面活性剤の効果が高く、好ましく、更に、陰イオン性界面活性剤のうちアルキルベンゼンスルホン酸ソーダは非常に効果が高く、好適に使用出来る。 Among these hydrophilicity improvers, surfactants are particularly desirable and most practical because surfactants are highly effective in improving hydrophilicity and exhibit sufficient effects even at low concentrations. Among the surfactants, an anionic surfactant is highly effective and preferable, and among the anionic surfactants, alkylbenzene sulfonic acid sodium soda is very effective and can be suitably used.
スポンジ担体に親水性向上剤を塗布、含浸させる方法は特に限定されず、液体状の親水性向上剤又はその希釈液を調製し、これらの溶液をスプレー等を用いて噴霧又は散布してスポンジ担体に塗布・含浸させる方法、液体状の親水性向上剤の又はその希釈液の中にスポンジ担体を浸漬して、スポンジ担体に含浸させる方法等を採用することが出来る。 The method of applying and impregnating the hydrophilicity improver to the sponge carrier is not particularly limited, and a liquid hydrophilicity improver or a diluted solution thereof is prepared, and these solutions are sprayed or sprayed using a spray or the like to form a sponge carrier. For example, a method of applying and impregnating a sponge carrier, a method of immersing a sponge carrier in a liquid hydrophilic improver or a diluted solution thereof, and impregnating the sponge carrier can be employed.
尚、親水性向上剤として、界面活性剤を用いる場合には、シリコン消泡剤等の消泡剤を配合することが好ましい。 In addition, when using surfactant as a hydrophilic improvement agent, it is preferable to mix | blend antifoamers, such as a silicon antifoamer.
又、このようにしてスポンジ担体に親水性向上剤を含浸させた後、湿潤状態のまま使用する方法もあり、含浸後に、一旦乾燥させて、使用時に水を含浸させて用いてもよい。 Further, there is a method in which the sponge carrier is impregnated with the hydrophilicity improver in this way, and then used in a wet state. After impregnation, the sponge carrier may be once dried and impregnated with water at the time of use.
これらの方法を用いて実際に曝気槽へスポンジ担体を投入する場合に、スポンジ担体を曝気槽に投入後、曝気槽内でスポンジ担体に親水性向上剤を含浸させる方法、予め親水性向上剤を含浸させたスポンジ担体を曝気槽へ投入する方法の何れも採用することが出来る。 When the sponge carrier is actually put into the aeration tank using these methods, after the sponge carrier is put into the aeration tank, the sponge carrier is impregnated with the hydrophilicity improver in the aeration tank. Any method of charging the impregnated sponge carrier into the aeration tank can be employed.
曝気槽内でスポンジ担体に親水性向上剤を含浸させる方法としては、(1)汚水処理装置・施設の立ち上げ時に空の曝気槽にスポンジ担体を投入し、投入されたスポンジ担体に液体状の親水性向上剤又はその希釈液を噴霧又は散布して、スポンジ担体に親水性向上剤を含浸させる。次いで、曝気槽へ少量の水又は汚水を入れ、エアーによる攪拌を行って、スポンジ担体に吸水させる方法。(2)曝気槽に少量の水又は汚水及び親水性向上剤を入れ、エアレーションを行い、ついで、ここにスポンジ担体を投入し、親水性向上剤をスポンジ担体に含浸させる方法等を採用することが出来る。 As a method of impregnating the sponge carrier with the hydrophilicity improver in the aeration tank, (1) the sponge carrier is put into an empty aeration tank when the sewage treatment apparatus / facility is started up, The sponge carrier is impregnated with the hydrophilicity improving agent by spraying or spraying the hydrophilicity improving agent or a diluted solution thereof. Next, a method in which a small amount of water or sewage is put into an aeration tank, and stirring is performed with air so that the sponge carrier absorbs water. (2) It is possible to put a small amount of water or sewage and a hydrophilicity improver into an aeration tank, perform aeration, and then introduce a sponge carrier into the aeration tank and impregnate the sponge carrier with the hydrophilicity improver. I can do it.
又、予め親水性向上剤を含浸させたスポンジ担体を曝気槽へ投入する方法としては、曝気槽等の汚水処理槽とは別個の槽等にスポンジ担体を投入し、投入されたスポンジ担体に液体状の親水性向上剤又はその希釈液を噴霧又は散布して、スポンジ担体に親水性向上剤を含浸させる。次いで、曝気槽に通常使用量の汚水を張り、エアレーションを行っている曝気槽に親水性向上剤を含浸させたスポンジ担体を投入する方法等を採用することが出来る。この方法では、親水性向上剤を含浸させたスポンジ担体を湿潤状態で使用してもよいが、上述のように一旦乾燥させたスポンジ担体を用いることも出来る。 In addition, as a method of charging a sponge carrier impregnated with a hydrophilicity improver in advance into the aeration tank, the sponge carrier is charged into a tank or the like separate from the sewage treatment tank such as the aeration tank, and the sponge carrier is liquidated. A sponge carrier is impregnated with a hydrophilicity improver by spraying or spraying a hydrophilic improver in the form of a liquid or a diluted solution thereof. Next, it is possible to employ a method in which a normal amount of sewage is filled in an aeration tank and a sponge carrier impregnated with a hydrophilicity improver is introduced into an aeration tank in which aeration is performed. In this method, a sponge carrier impregnated with a hydrophilicity improving agent may be used in a wet state, but a sponge carrier once dried as described above can also be used.
スポンジ担体には、曝気槽への投入前に、予め微生物及び/又は栄養成分を担持させることとしてもよい。予め微生物を担持させることにより、スポンジ担体に微生物が付着する間の処理能力が低い状態を経ることなく、新規スポンジ担体の投入直後にも、有機性物質の分解を充分に行うことが出来、汚水の高負荷処理が可能となる。又、栄養成分は微生物を増殖させるためのものであり、栄養成分を担持させることにより、微生物の増殖速度が速まり、新規スポンジ担体の投入直後にも、より有機性物質の分解を充分に行うことが出来、汚水の高負荷処理が可能となる。 The sponge carrier may be loaded with microorganisms and / or nutrients in advance before being introduced into the aeration tank. By supporting microorganisms in advance, organic substances can be sufficiently decomposed immediately after the introduction of the new sponge carrier without passing through a state where the treatment capacity is low while the microorganisms adhere to the sponge carrier. High-load processing is possible. Nutritional components are for growing microorganisms. By supporting the nutritional components, the growth rate of microorganisms is increased, and organic substances are sufficiently decomposed immediately after the introduction of a new sponge carrier. And high load treatment of sewage becomes possible.
微生物としては、通常の活性汚泥法において使用される微生物であれば特に限定されず、具体的には、Achromobacter属、Alcaligenes属、Bacillus属、Pseudomonas属、Saccharomyces属、Lactobacillus属、Streptococcus属、Leuconostoc属、Pediococcus属等が挙げられ、これら微生物を1種又は2種以上を適宜に組合わせてスポンジ担体に担持させる。 The microorganism is not particularly limited as long as it is a microorganism that is used in a normal activated sludge method. , Pediococcus genus and the like, and these microorganisms are supported on a sponge carrier by appropriately combining one or more microorganisms.
栄養成分としては、上記のような微生物の栄養分となるものであれば特に限定されないが、例えば、尿素や、硫酸アンモニウム、クエン酸アンモニウム、硝酸アンモニウム、塩化アンモニウム等のアンモニウム塩や、リン酸や、リン酸一カリウム、リン酸二カリウム、リン酸一ナトリウム、リン酸アンモニウム、ピロリン酸ナトリウム、ヘキサメタリン酸ナトリウム、過リン酸石灰等のリン酸塩や、塩化カルシウム、珪酸カルシウム、硝酸カルシウム等のカルシウム塩や、硫酸マグネシウム、塩化マグネシウム、硝酸マグネシウム等のマグネシウム塩や、塩化第一鉄、塩化第二鉄、硫酸第一鉄、硝酸第二鉄等の鉄塩や、各種糖類、各種アミノ酸等が挙げられ、これら栄養分を1種又は2種以上を適宜に組合わせてスポンジ担体に担持させる。 The nutrient component is not particularly limited as long as it is a nutrient for the microorganism as described above. For example, urea, ammonium sulfate such as ammonium sulfate, ammonium citrate, ammonium nitrate, and ammonium chloride, phosphoric acid, and phosphoric acid Phosphate such as monopotassium, dipotassium phosphate, monosodium phosphate, ammonium phosphate, sodium pyrophosphate, sodium hexametaphosphate, calcium phosphate, calcium salts such as calcium chloride, calcium silicate, calcium nitrate, Examples include magnesium salts such as magnesium sulfate, magnesium chloride, and magnesium nitrate, iron salts such as ferrous chloride, ferric chloride, ferrous sulfate, and ferric nitrate, various sugars, and various amino acids. One or two or more nutrients are appropriately combined and supported on the sponge carrier.
スポンジ担体に微生物や栄養成分を担持させる方法としては特に限定されず、微生物や栄養成分の水溶液を調製し、該水溶液をスプレー等を用いて噴霧又は散布してスポンジ担体に塗布・含浸させる方法、微生物や栄養成分の水溶液の中にスポンジ担体を浸漬して、スポンジ担体に含浸させる方法等を採用することが出来る。 The method for supporting microorganisms and nutritional components on the sponge carrier is not particularly limited, and a method of preparing an aqueous solution of microorganisms and nutritional components, spraying or spraying the aqueous solution using a spray or the like, and applying and impregnating the sponge carrier, A method of immersing a sponge carrier in an aqueous solution of microorganisms or nutritional components and impregnating the sponge carrier can be employed.
スポンジ担体に親水性向上剤を含有させた場合の親水性の効果を確認するために、親水性向上剤の一定濃度水溶液を調製し、ビーカーに入れ、この液面上にスポンジ担体を静かに置き、静置状態でスポンジ担体の吸水状況を観察した。なお、スポンジ担体は、1cm角立方体、重量約0.03gのものを使用した。親水性向上剤と、比較例としての水について試験を行った。使用した親水性向上剤及び結果を以下の表1に示す。尚、表中%は重量%を意味する。 To confirm the hydrophilic effect when the sponge carrier contains a hydrophilicity improver, prepare a constant concentration aqueous solution of the hydrophilicity improver, place it in a beaker, and place the sponge carrier gently on the liquid surface. The water absorption state of the sponge carrier was observed in a stationary state. A sponge carrier having a 1 cm square cube and a weight of about 0.03 g was used. Tests were conducted on a hydrophilicity improver and water as a comparative example. The hydrophilicity improvers used and the results are shown in Table 1 below. In the table, “%” means “% by weight”.
以上の試験から、親水性向上剤により、スポンジ担体の吸水性が高まり、極めて容易に水と馴染むことがわかった。 From the above test, it was found that the hydrophilicity-improving agent increases the water absorption of the sponge carrier, so that it can be easily adapted to water.
スポンジ担体に、親水性向上剤、微生物、栄養分を担持させるために、以下の表2で示す処方で、水溶液を調製した。尚、海草エキスは海草から抽出したエキスで、カリウム塩等のミネラルを含む栄養分である。 An aqueous solution was prepared according to the formulation shown in Table 2 below in order to support the hydrophilicity improver, microorganisms and nutrients on the sponge carrier. Seaweed extract is an extract extracted from seaweed, and is a nutrient containing minerals such as potassium salts.
この水溶液を適宜の希釈率で水で希釈した水溶液をビーカーに入れ、この液面上にスポンジ担体を静かに置き、静置状態でスポンジ担体の吸水状況を観察した。なお、スポンジ担体は、1cm角立方体、重量約0.03gのものを使用した。親水性向上剤を含有したものと、比較例として親水性向上剤を含有しない水について試験を行った。試験した希釈倍率及び結果を以下の表3に示す。 An aqueous solution obtained by diluting this aqueous solution with water at an appropriate dilution rate was placed in a beaker, and the sponge carrier was gently placed on the liquid surface, and the water absorption state of the sponge carrier was observed in a stationary state. A sponge carrier having a 1 cm square cube and a weight of about 0.03 g was used. Tests were conducted on water containing a hydrophilicity improver and water containing no hydrophilicity improving agent as a comparative example. The dilution factors tested and the results are shown in Table 3 below.
以上の試験から、微生物及び栄養分を担持させたスポンジ担体であっても、親水性向上剤により、スポンジ担体の吸水性が高まり、極めて容易に水と馴染むことがわかった。 From the above test, it was found that even with a sponge carrier carrying microorganisms and nutrients, the hydrophilicity-improving agent increases the water absorption of the sponge carrier, so that it can be easily adapted to water.
表2の処方で調製した水溶液を水を用いて100倍希釈水溶液を調製し、スプレー容器に入れた。1cm角立方体、重量約0.03gのスポンジ担体を100個ビーカーに入れ、スポンジ担体全体の重量と同じ量の前記水溶液をスプレーで噴霧して、担体に均一に含浸させた。このスポンジ担体を、水を張りエアレーションを行っている槽容器量30lの模擬曝気槽に投入し、スポンジ担体の挙動を観察した。比較例として、無処理のスポンジ担体を同様に模擬曝気槽に投入し、スポンジ担体の挙動を観察した。 A 100-fold diluted aqueous solution of the aqueous solution prepared according to the formulation in Table 2 was prepared using water and placed in a spray container. 100 sponge sponges having a 1 cm square cube and a weight of about 0.03 g were put in a beaker, and the same amount of the aqueous solution as the total weight of the sponge carrier was sprayed to uniformly impregnate the carrier. This sponge carrier was put into a 30-liter simulated aeration tank in which water was filled and aerated, and the behavior of the sponge carrier was observed. As a comparative example, an untreated sponge carrier was similarly put into a simulated aeration tank, and the behavior of the sponge carrier was observed.
前記水溶液を含浸させたスポンジ担体は、投入直後に総て水中に入り込み、曝気による水流により流動性を示した。一方、無処理のスポンジ担体は総て5時間経過後にも水上に浮上したままで、全く流動性を示さなかった。 The sponge carrier impregnated with the aqueous solution all entered water immediately after the addition, and showed fluidity by the water flow by aeration. On the other hand, all the untreated sponge carriers remained floating on the water even after 5 hours, and showed no fluidity.
以上の試験から、スポンジ担体に親水性向上剤を含浸させることにより、スポンジ担体は迅速に吸水し、水と馴染んで曝気槽内を流動可能となることがわかる。 From the above test, it can be seen that by impregnating the sponge carrier with the hydrophilicity improver, the sponge carrier quickly absorbs water, becomes familiar with water and can flow in the aeration tank.
1 流量調整槽
2 曝気槽
3 固液分離槽
4 汚泥濃縮槽
5 汚泥貯留槽
6 返送汚泥ライン
7 余剰汚泥ライン
10 スポンジ担体
21 ブロア
22 散気管
30 汚水
100 汚水処理装置
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JP2014124581A (en) * | 2012-12-26 | 2014-07-07 | Maezawa Kasei Ind Co Ltd | Carrier for water treatment, production method thereof, and wastewater treatment system |
JP2016153118A (en) * | 2015-02-16 | 2016-08-25 | 栗田工業株式会社 | Biological treatment tank, method for operating the tank, and method for treating organic waste water |
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JP2014124581A (en) * | 2012-12-26 | 2014-07-07 | Maezawa Kasei Ind Co Ltd | Carrier for water treatment, production method thereof, and wastewater treatment system |
JP2016153118A (en) * | 2015-02-16 | 2016-08-25 | 栗田工業株式会社 | Biological treatment tank, method for operating the tank, and method for treating organic waste water |
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