JP2011131200A - Wastewater treatment agent - Google Patents

Wastewater treatment agent Download PDF

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JP2011131200A
JP2011131200A JP2009295741A JP2009295741A JP2011131200A JP 2011131200 A JP2011131200 A JP 2011131200A JP 2009295741 A JP2009295741 A JP 2009295741A JP 2009295741 A JP2009295741 A JP 2009295741A JP 2011131200 A JP2011131200 A JP 2011131200A
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wastewater
treatment agent
membrane
colored
wastewater treatment
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Akira Ikeda
明 池田
Koichi Nozaki
功一 野崎
Takahisa Kanda
鷹久 神田
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Mimaki Engineering Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a wastewater treatment agent which enables cost reduction and can decolorize colored wastewater under a mild condition without exerting a bad influence on the human body and the environment. <P>SOLUTION: The wastewater treatment agent which is added into colored wastewater containing dyes to decolorize the colored wastewater includes enzymes extracted from a waste mushroom bed after cultivation of basidiomycetes. <P>COPYRIGHT: (C)2011,JPO&amp;INPIT

Description

本発明は、例えば染料工場等から排出される着色排水中に投与されて当該着色排水を脱色する排水処理剤に関する。   The present invention relates to a wastewater treatment agent that is administered into, for example, colored wastewater discharged from a dye factory or the like and decolorizes the colored wastewater.

近年、環境問題に関連して染色工場などから多量に排出される染料排水(着色排水)が問題となっており、地方自治体等によっても染料排水に対する規制が強化されている。染料は低濃度でも着色性が高く脱色処理が困難であるため、従来から染料排水は専門処理業者によって引き取られて処理委託され、産業廃棄物として処分されるか、あるいは河川等に放流できるまで脱色・浄化等の処理がなされている。このような場合、廃棄処分する場所や排水処理設備のある場所が限定されてしまう上に、上記のような規制強化等に伴って染料排水の処理コストが上昇傾向にあるため、最近では染料を分解する方法として、染料をオゾンと接触させることにより分解する手段(例えば、特許文献1を参照)や微生物を用いた処理手段(例えば、特許文献2を参照)などが注目を集めている。   In recent years, dye wastewater (colored wastewater) discharged in large quantities from dyeing factories or the like has become a problem in relation to environmental problems, and regulations on dye wastewater have been strengthened by local governments and the like. Dye is highly colored and difficult to decolorize even at low concentrations. Conventionally, dye wastewater is taken up by a specialist processor and outsourced to be disposed of as industrial waste or discharged into rivers, etc.・ Purification and other treatments have been made. In such a case, the place where the waste is disposed and the place where the wastewater treatment facility is located are limited, and the treatment cost of the dye wastewater tends to increase due to the above-mentioned tightening regulations. As a method for decomposing, means for decomposing dye by contacting it with ozone (for example, see Patent Document 1), processing means using microorganisms (for example, see Patent Document 2), and the like are attracting attention.

特開平9−239383号公報JP-A-9-239383 特開平2000−287674号公報Japanese Patent Laid-Open No. 2000-287664

しかしながら、オゾンによる排水処理の場合には、発癌性化合物の生成に関与するため人体への影響が指摘されている。一方、微生物による場合には、反応条件を微生物の増殖条件に合わせる必要があるため処理条件の調節が困難であるとともに、活性汚泥(微生物の死骸)の発生により結果的に排水汚染を引き起こす虞があるという問題がある。また、上記いずれの場合にも、設備(オゾン発生装置、バッキ槽)に関して多大な費用を要するという欠点も有している。   However, in the case of wastewater treatment with ozone, it has been pointed out that it affects the human body because it is involved in the production of carcinogenic compounds. On the other hand, in the case of using microorganisms, it is necessary to adjust the reaction conditions to the growth conditions of the microorganisms, and thus it is difficult to adjust the treatment conditions. There is a problem that there is. Moreover, in any of the above cases, there is also a drawback that a great deal of cost is required for the equipment (ozone generator, backing tank).

本発明は、このような問題に鑑みてなされたものであり、コスト低減を図るとともに、人体や環境に悪影響を及ぼすことなく穏和な条件で着色排水を脱色することが可能な構成の排水処理剤を提供することを目的とする。   The present invention has been made in view of such a problem, and is a wastewater treatment agent having a configuration capable of reducing costs and decolorizing colored wastewater under mild conditions without adversely affecting the human body and the environment. The purpose is to provide.

上記目的を達成するために、本発明に係る排水処理剤は、染料を含有する着色排水中に投与されて当該着色排水を脱色する排水処理剤であって、担子菌栽培後の廃菌床から抽出した酵素を含有して構成される。   In order to achieve the above object, the wastewater treatment agent according to the present invention is a wastewater treatment agent that is administered into a colored wastewater containing a dye and decolorizes the colored wastewater, from the waste fungus bed after basidiomycete cultivation Consists of extracted enzymes.

なお、上記構成の排水処理剤において、排水処理剤が廃菌床から抽出した酵素液を凍結乾燥して錠剤化したものであることが好ましい。   In the wastewater treatment agent having the above-described configuration, the wastewater treatment agent is preferably freeze-dried and tableted from the enzyme solution extracted from the waste bacteria bed.

本発明に関する排水処理剤によれば、担子菌栽培後に残る廃菌床から抽出した染料分解能力を持つ酵素を有効利用することで、コスト低減を図るとともに、人体や環境に悪影響を及ぼすことなく穏和な条件で着色排水を脱色することが可能になる。   According to the wastewater treatment agent of the present invention, by effectively using an enzyme having a dye-decomposing ability extracted from a waste fungus bed remaining after cultivation of basidiomycetes, it is possible to reduce costs and moderately without adversely affecting the human body and the environment. It is possible to decolor the colored wastewater under various conditions.

また、上記構成において、排水処理剤を廃菌床から抽出した酵素液を凍結乾燥して錠剤化して構成することで、その取り扱いが容易になるとともに、1個当たりの重量が一定になるため、処理対象の着色排水に対して適切な投与量(添加量)を錠剤の個数をもって算定することができる。   In addition, in the above configuration, the enzyme solution extracted from the waste fungus bed is freeze-dried and tableted to make it easy to handle and the weight per piece is constant, An appropriate dose (addition amount) for the colored wastewater to be treated can be calculated from the number of tablets.

本発明に係る排水処理剤を適用するのに好適な排水処理装置の一例を示すフロー図である。It is a flowchart which shows an example of the waste water treatment apparatus suitable for applying the waste water treatment agent which concerns on this invention.

以下、本発明の好ましい実施形態について説明する。本発明に係る排水処理剤は、染料を含有する着色排水中に投与されて当該着色排水を脱色する排水処理剤であって、担子菌栽培後の廃菌床から抽出した酵素を含有して構成されることを特徴とする。   Hereinafter, preferred embodiments of the present invention will be described. The wastewater treatment agent according to the present invention is a wastewater treatment agent that is administered into a colored wastewater containing a dye and decolorizes the colored wastewater, and contains an enzyme extracted from a waste fungus bed after basidiomycete cultivation. It is characterized by being.

本発明において対象となる染料としては、アゾ系染料、フタロシアニン系染料、アクリジン系染料、トリフェニルメタン系染料、トリアジン系染料などが適用可能であるが、これに限定されるものではない。その中でも染料として主に使用されるアゾ系染料としては、Acid Orange20やAcid Violet3等のモノアゾ系染料、Direct Blue2等のジアゾ系染料、トリアゾ系、およびテトラアゾ系などが例示されるが、これに限定されるものではない。   As dyes to be used in the present invention, azo dyes, phthalocyanine dyes, acridine dyes, triphenylmethane dyes, triazine dyes, and the like are applicable, but are not limited thereto. Among them, examples of the azo dye mainly used as the dye include monoazo dyes such as Acid Orange 20 and Acid Violet 3, diazo dyes such as Direct Blue 2, triazo dyes, and tetraazo dyes, but are not limited thereto. Is not to be done.

本発明において使用される担子菌(バシディオミセテス)としては、上記染料の分解能力を有する酵素を持つ担子菌であれば特に限定しないが、例えば、トキイロヒラタケ(Pleurotus salmoneostramineus)、ツクリタケ(Agaricus bisporus)、ナラタケ(Armillariella mellea)、エノキタケ(Flammulina velutipes)、シイタケ(Lentinus edodes)、ムキタケ(Pnellus serotinus)、エリンギ(Pleurotus eryngii)、ヒラタケ(Pleurotus ostreatus)等の食用キノコ類が例示される。なお、担子菌の中でも木材腐朽菌、白色腐朽菌が好適に用いられる。   The basidiomycete used in the present invention is not particularly limited as long as it is a basidiomycete having an enzyme capable of degrading the dye. For example, Pleurotus salmoneostramineus, Agaricus edible mushrooms such as bisporus, armillariella mellea, enokitake (Flammulina velutipes), shiitake (Lentinus edodes), mushroom (Pnellus serotinus), eringi (Pleurotus eryngii), oyster mushroom (Pleurotus ostreatus), etc. Among basidiomycetes, wood-rotting fungi and white-rotting fungi are preferably used.

担子菌の廃菌床とは、例えば担子菌の人工栽培後に残る菌床(培地)であって、オガ粉、培地添加物(栄養添加物)、および水等の混合物であるため、人体や環境に悪影響を及ぼすことはない。また、従来大量に廃棄されていた担子菌廃菌床の有効活用を図ることもできる。   The waste bed of basidiomycetes is, for example, a bed (medium) remaining after artificial cultivation of basidiomycetes, and is a mixture of sawdust, medium additive (nutrient additive), water, etc. Will not be adversely affected. Moreover, effective utilization of the basidiomycetes waste microbial bed conventionally discarded in large quantities can also be aimed at.

本発明で利用される担子菌由来の酵素は、担子菌が一般に生成するラッカーゼ(特に、木材腐朽菌や白色腐朽菌等に多く存在する)であり、このラッカーゼ(Laccase)は基本的には種々の基質(例えばフェノール性の化合物)の一電子酸化を触媒する活性酵素である。なお、同じラッカーゼという名前の酵素であっても、上記担子菌の種類によってその性質は異なり、好適に作用する基質や、最適温度、最適pHなどの活性条件が異なってくる。また、同じ担子菌でも性質の異なる複数のラッカーゼを有することもある。よって、上記担子菌群の廃菌床から抽出される少なくとも1種以上のラッカーゼが用いられる。すなわち、複数種のラッカーゼを組み合わせて用いてもよい。   The basidiomycete-derived enzyme used in the present invention is a laccase generally produced by basidiomycetes (especially abundantly in wood-rotting fungi and white-rotting fungi), and this laccase is basically various. It is an active enzyme that catalyzes the one-electron oxidation of a substrate (for example, a phenolic compound). In addition, even if it is the enzyme named the same laccase, the property changes with kinds of said basidiomycete, and active conditions, such as a substrate which acts suitably, optimal temperature, and optimal pH, differ. Moreover, the same basidiomycete may have a plurality of laccases having different properties. Therefore, at least one or more types of laccase extracted from the waste fungus bed of the basidiomycete group are used. That is, you may use combining multiple types of laccase.

ラッカーゼの作用としては、例えば染料中のフェノール類(電子供与体)から電子(水素)を引き抜き、その電子を酸素分子(電子受容体)に渡して水を生成する化学反応の触媒をしている。この過程において、染料の発色団に関係する構造が破壊され、染料の脱色が生じると推定される。このラッカーゼの反応に関しては、穏和な条件下で反応を進行させることが可能である。   As an action of laccase, for example, an electron (hydrogen) is extracted from phenols (electron donor) in a dye, and the electron is passed to an oxygen molecule (electron acceptor) to catalyze a chemical reaction that generates water. . In this process, it is presumed that the structure related to the chromophore of the dye is destroyed and decolorization of the dye occurs. With regard to this laccase reaction, it is possible to proceed under mild conditions.

ここで、上記酵素を用いた脱色能力(脱色活性)の測定法としては、一定時間ごとに着色排水を採取して、当該染料の最大吸収波長の吸光度(吸光度減少率)を測定し、これを脱色率として推定するのが好ましい。   Here, as a method of measuring the decoloring ability (decoloring activity) using the above enzyme, colored waste water is collected at regular intervals, and the absorbance (decrease rate of absorbance) of the maximum absorption wavelength of the dye is measured. It is preferable to estimate the decolorization rate.

次に、本発明の排水処理剤を適用するために好適な排水処理装置について説明する。図1に排水処理装置の一例を示すフロー図を示しており、この図を参照して、本実施形態に係る排水処理剤を適用した排水処理装置の概要構成を説明する。   Next, a wastewater treatment apparatus suitable for applying the wastewater treatment agent of the present invention will be described. FIG. 1 is a flowchart showing an example of a wastewater treatment apparatus, and a schematic configuration of the wastewater treatment apparatus to which the wastewater treatment agent according to the present embodiment is applied will be described with reference to this figure.

排水処理装置1は、大別的には、染料を含む排水(以下、着色排水と称する)を一時的に貯留する貯留槽2と、貯留槽2から送給される着色排水を脱色処理する分解処理槽4と、分解処理槽4で脱色された処理液中に残留する生成物を捕捉する膜濃縮装置11とを備えて構成される。   The waste water treatment apparatus 1 is broadly divided into a storage tank 2 for temporarily storing waste water containing dye (hereinafter referred to as colored waste water), and a decomposition for decolorizing the colored waste water supplied from the storage tank 2. A treatment tank 4 and a membrane concentrator 11 that captures a product remaining in the treatment liquid decolorized in the decomposition treatment tank 4 are configured.

貯留槽2は、例えば印刷装置や染色工場等から排出される着色排水(染料排水)を原水として一時的に貯留する。貯留槽2の着色排水は送給ポンプ3によって吸い上げられて分解処理槽4へ送給される。なお、分解処理槽4での処理の効率化のために、分解処理槽4に導入する前の貯留槽2に滞留する着色排水を、予め酵素活性に適した水温に予熱するための予熱手段を設けてもよい。   The storage tank 2 temporarily stores, as raw water, colored wastewater (dye wastewater) discharged from, for example, a printing apparatus or a dyeing factory. The colored wastewater in the storage tank 2 is sucked up by the feed pump 3 and fed to the decomposition treatment tank 4. In order to increase the efficiency of the treatment in the decomposition treatment tank 4, a preheating means for preheating the colored wastewater staying in the storage tank 2 before being introduced into the decomposition treatment tank 4 to a water temperature suitable for the enzyme activity in advance. It may be provided.

分解処理槽4は、送給ポンプ3によって導入された染色排水で満たされており、この染色排水中に染料を分解するための酵素(ラッカーゼ)を含有する排水処理剤6が投入されている。排水処理剤6に使用する酵素については、担子菌の廃菌床もしくはこれを粉砕したものに緩衝液を加えて攪拌することで当該酵素を溶出された後、濾過等によって抽出する。   The decomposition treatment tank 4 is filled with the dye wastewater introduced by the feed pump 3, and the wastewater treatment agent 6 containing an enzyme (laccase) for decomposing the dye is introduced into the dye wastewater. The enzyme used in the wastewater treatment agent 6 is extracted by filtration or the like after the enzyme is eluted by adding a buffer solution to a basidiomycete waste bed or a pulverized product thereof and stirring.

緩衝液としては、例えば酢酸アンモニウムや燐酸などが適用され、抽出対象の酵素活性が維持されればpHは特に限定されない。排水処理剤6としては、緩衝液からの抽出液を遠心分離して得た上澄み液である酵素液や、この酵素液を凍結乾燥処理した酵素製剤などが例示される。酵素製剤は、粉末化したものや、これを整形して錠剤化(タブレット化)したものが例示される。特に、排水処理剤6を錠剤にすれば、その取り扱いが容易になるとともに、1個当たりの重量が一定になるため、処理対象の着色排水に対して適切な投与量(添加量)を錠剤の個数をもって算定することができる。なお、排水処理剤6を、例えば所定時間間隔で分解処理槽4内に自動的に投与する処理剤投入装置を設けて構成してもよい。   As the buffer, for example, ammonium acetate or phosphoric acid is applied, and the pH is not particularly limited as long as the enzyme activity to be extracted is maintained. Examples of the waste water treatment agent 6 include an enzyme solution which is a supernatant obtained by centrifuging an extract from a buffer solution, and an enzyme preparation obtained by freeze-drying the enzyme solution. Examples of the enzyme preparation include powdered ones and those obtained by shaping the tablets into tablets (tablets). In particular, if the wastewater treatment agent 6 is made into a tablet, its handling becomes easy and the weight per one becomes constant. Therefore, an appropriate dose (addition amount) for the colored wastewater to be treated is set to the tablet. It can be calculated with the number. In addition, you may comprise the processing agent injection | throwing-in apparatus which administers the waste water processing agent 6 automatically in the decomposition processing tank 4 at predetermined time intervals, for example.

分解処理槽4においては、着色排水中の染料と排水処理剤6の酵素とが反応して、当該染料(着色排水)が脱色される。この分解処理槽4内には着色排水を攪拌させるための攪拌装置5が設置されており、これにより着色排水の染料と排水処理剤6の酵素との接触の機会を増大させている。また、染料と酵素との反応を促進させるために、着色排水の温度を調整する水温調整手段や、着色排水に塩酸や燐酸液等を加えてpHを調整するpH調整手段を設けてもよい。   In the decomposition treatment tank 4, the dye in the colored wastewater reacts with the enzyme of the wastewater treatment agent 6 to decolorize the dye (colored wastewater). A stirring device 5 for stirring the colored waste water is installed in the decomposition treatment tank 4, thereby increasing the chance of contact between the dye of the colored waste water and the enzyme of the waste water treatment agent 6. Further, in order to promote the reaction between the dye and the enzyme, a water temperature adjusting means for adjusting the temperature of the colored waste water, or a pH adjusting means for adjusting the pH by adding hydrochloric acid or phosphoric acid solution to the colored waste water may be provided.

また、分解処理槽4には、脱色処理後の排水(以下、処理水と称する)の吸光度を計測する吸光度計測装置7が接続されている。この吸光度計測装置7は、処理水の一部を間欠的もしくは連続的に抜き出して処理水の吸光度を測定し、この測定情報を制御部8へ出力する。吸光度計測装置7としては、例えばフローセル型紫外可視吸光光度計が例示される。この吸光光度計は、染料の色素波長と同じ波長帯域の光を透過させて、当該透過率を計測することで染料の吸光度を求めるものである。   The decomposition treatment tank 4 is connected with an absorbance measuring device 7 for measuring the absorbance of the waste water after decoloring treatment (hereinafter referred to as treated water). The absorbance measurement device 7 intermittently or continuously extracts part of the treated water, measures the absorbance of the treated water, and outputs this measurement information to the control unit 8. As the absorbance measuring device 7, for example, a flow cell type ultraviolet visible absorptiometer is exemplified. This absorptiometer transmits light in the same wavelength band as the dye pigment wavelength and measures the transmittance to determine the absorbance of the dye.

制御部8は、吸光度計測装置7から入力される計測情報に基づいて、計測された吸光度が予め設定された所定値以下、すなわち脱色処理が十分に行われていると判定すると、分解槽に設けられた電磁弁9を開いて送給ポンプ10を介して分解処理槽4と膜濃縮装置11とを連通させる。なお、吸光度計測装置7を設けることなく、例えば、タイマカウンタによって分解処理槽4での着色排水の滞留時間(処理時間)を計測して、規定の滞留時間の経過に伴って電磁弁9を開弁させる構成としてもよい。   When the control unit 8 determines that the measured absorbance is equal to or less than a predetermined value set in advance based on the measurement information input from the absorbance measurement device 7, that is, the decolorization process is sufficiently performed, the control unit 8 is provided in the decomposition tank. The opened electromagnetic valve 9 is opened, and the decomposition treatment tank 4 and the membrane concentrator 11 are communicated with each other via the feed pump 10. For example, the residence time (treatment time) of the colored wastewater in the decomposition treatment tank 4 is measured by a timer counter without providing the absorbance measurement device 7, and the electromagnetic valve 9 is opened as the prescribed residence time elapses. It is good also as a structure made to valve.

分解処理槽4で脱色された処理水は、送給ポンプ10によって吸い上げられて次段の膜濃縮装置11へ送給される。ここで、染料の脱色とは、無色透明への脱色のみに限定されるものではなく、変色や減色をも含む概念である。   The treated water decolorized in the decomposition treatment tank 4 is sucked up by the feed pump 10 and fed to the membrane concentrator 11 at the next stage. Here, decolorization of a dye is not limited to decolorization to colorless and transparent, but is a concept including discoloration and color reduction.

膜濃縮装置11は、排水処理剤6によって脱色された処理水を膜透過水W1と膜濃縮液W2とに分離するための分離膜12を有している。分離膜12としては、精密濾過膜(マイクロフィルタ)或いは限外濾過膜等の有機膜や無機膜が適用可能である。また、分離膜12の形態は、膜モジュールとして平膜型、中空糸型、スパイラル型、円筒(管状)型、プリーツ型等を適宜採用することができる。分離膜の孔径としては、例えば精密濾過膜の場合と限外濾過膜の場合で異なるが、トラップ対象の生成物に応じて適宜なものが選定される。   The membrane concentrating device 11 has a separation membrane 12 for separating the treated water decolorized by the waste water treatment agent 6 into the membrane permeated water W1 and the membrane concentrated liquid W2. As the separation membrane 12, an organic membrane or an inorganic membrane such as a microfiltration membrane (microfilter) or an ultrafiltration membrane can be applied. In addition, as the form of the separation membrane 12, a flat membrane type, a hollow fiber type, a spiral type, a cylindrical (tubular) type, a pleat type, and the like can be appropriately employed as the membrane module. The pore size of the separation membrane varies depending on, for example, the case of the microfiltration membrane and the case of the ultrafiltration membrane, but an appropriate one is selected according to the product to be trapped.

膜濃縮装置11において、導入された処理水の一部は、膜間差圧によって分離膜12を透過して膜透過水W1として膜透過水受入槽13に流入される。膜透過水受入層13へ導かれた膜透過水W1は、例えばpH処理された後、最終的には河川等公共用水に放流される。一方、前段の酵素分解によって生じた生成物等の不純物は分離膜12によって阻止されて、膜濃縮水W2として系外へ排出される。膜濃縮装置11より間欠的もしくは連続的に系外に引き抜かれた膜濃縮水W2(生成物)は、例えば脱水装置14によって脱水された上で廃棄される。   In the membrane concentrator 11, a part of the treated water introduced permeates through the separation membrane 12 by the transmembrane pressure and flows into the membrane permeate receiving tank 13 as the membrane permeate W1. The membrane permeated water W1 guided to the membrane permeated water receiving layer 13 is finally discharged into public water such as a river after being subjected to pH treatment, for example. On the other hand, impurities such as products produced by the previous enzymatic decomposition are blocked by the separation membrane 12 and discharged out of the system as membrane concentrated water W2. The membrane concentrated water W2 (product) drawn out of the system intermittently or continuously from the membrane concentrator 11 is dehydrated by, for example, the dehydrator 14 and then discarded.

以上説明したように、本実施形態に係る排水処理剤によれば、担子菌の栽培後に残る廃菌床から抽出した染料分解能力を持つ酵素(ラッカーゼ)を有効利用することで、コスト低減を図るとともに、人体や環境に悪影響を及ぼすことなく穏和な条件で着色排水を脱色することが可能となる。   As described above, according to the wastewater treatment agent according to the present embodiment, cost is reduced by effectively using an enzyme (laccase) having a dye-decomposing ability extracted from a waste fungus bed remaining after cultivation of basidiomycetes. At the same time, it is possible to decolor the colored wastewater under mild conditions without adversely affecting the human body and the environment.

また、排水処理剤6を廃菌床から抽出した酵素液を凍結乾燥して錠剤化して構成することで、その取り扱いが容易になるとともに、1個当たりの重量が一定になるため、処理対象の着色排水に対して適切な投与量(添加量)を錠剤の個数をもって算定することが可能になる。   Moreover, since the wastewater treatment agent 6 is lyophilized from the waste bacterial bed and formed into tablets, the handling becomes easy and the weight per piece becomes constant. It is possible to calculate an appropriate dose (addition amount) for the colored wastewater by the number of tablets.

これまで本発明の好ましい実施形態について説明したが、本発明はこの実施形態に限定されるものではない。例えば、廃菌床自体(廃菌床を適宜な大きさに加工したもの等)を排水処理剤として用いたり、排水処理剤に酵素活性(ラッカーゼ活性)を促進させる添加剤を添加して構成してもよい。   Although the preferred embodiment of the present invention has been described so far, the present invention is not limited to this embodiment. For example, the waste bacteria bed itself (such as a waste bacteria bed processed to an appropriate size) is used as a wastewater treatment agent, or an additive that promotes enzyme activity (laccase activity) is added to the wastewater treatment agent. May be.

また、上述の実施形態においては、脱色の対象となる着色排水を一旦、貯留槽2に導入する構成を例示して説明したが、これに限定されるものではなく、分解処理槽4に直接導入する構成であってもよい。   Moreover, in the above-mentioned embodiment, although the structure which introduce | transduces the colored waste water used as the object of decoloration into the storage tank 2 once was illustrated and demonstrated, it is not limited to this and is directly introduced into the decomposition treatment tank 4 It may be configured to.

さらに、上述の実施形態においては、分解処理槽4を1つのみ設けた構成を例示して説明したが、これに限定されるものではなく、例えば、複数の分解処理槽を直列に接続して設け、これらをダーティタンクとクリーンタンクとに分けて構成したり、複数の分解処理槽の間を循環させる構成であってもよい。   Furthermore, in the above-mentioned embodiment, although the structure which provided only one decomposition treatment tank 4 was illustrated and demonstrated, it is not limited to this, For example, a some decomposition treatment tank is connected in series It may be provided and divided into a dirty tank and a clean tank, or may be configured to circulate between a plurality of decomposition treatment tanks.

また、上述の実施形態においては、分解処理手段の後段に膜濾過手段として膜濃縮装置11を備えた構成を例示して説明したが、これに限定されるものではなく、例えば、膜濾過手段として1段目に精密濾過膜(マイクロフィルタ)を配置し、2段目に限外濾過膜を配置した2段構成の膜濾過手段としてもよい。また、例えば、膜濾過手段の前段もしくは後段に、沈降分離法(沈殿池)や加圧浮上法といった固液分離手段を更に設けて構成してもよい。   Moreover, in the above-mentioned embodiment, although the structure provided with the membrane concentration apparatus 11 as a membrane filtration means in the back | latter stage of the decomposition process means was demonstrated and demonstrated, it is not limited to this, For example, as a membrane filtration means A two-stage membrane filtration means in which a microfiltration membrane (microfilter) is arranged in the first stage and an ultrafiltration membrane is arranged in the second stage may be used. Further, for example, a solid-liquid separation means such as a sedimentation separation method (sedimentation basin) or a pressure flotation method may be further provided before or after the membrane filtration means.

さらに、上述の実施形態においては、分解処理槽4で脱色された処理液を送給ポンプ10によって膜濃縮装置11に導入する構成を例示して説明したが、これに限定されるものではなく、例えば、分解処理槽4の上澄み液が膜濃縮装置11に供給されるものであってもよい。   Furthermore, in the above-described embodiment, the configuration in which the treatment liquid decolorized in the decomposition treatment tank 4 is introduced into the membrane concentration apparatus 11 by the feed pump 10 has been described as an example, but the present invention is not limited thereto. For example, the supernatant liquid of the decomposition treatment tank 4 may be supplied to the membrane concentration apparatus 11.

1 排水処理装置
2 貯留槽
3 送給ポンプ
4 分解処理槽
5 攪拌装置
6 排水処理剤
7 吸光度計測装置
8 制御部
9 電磁弁
10 送給ポンプ
11 膜濃縮装置
12 分離膜
13 膜透過水受入槽
14 脱水装置
W1 膜透過水
W2 膜濃縮水
DESCRIPTION OF SYMBOLS 1 Waste water treatment device 2 Storage tank 3 Feeding pump 4 Decomposition processing tank 5 Stirring device 6 Waste water treatment agent 7 Absorbance measuring device 8 Control part 9 Solenoid valve 10 Feeding pump 11 Membrane concentrator 12 Separation membrane 13 Membrane permeated water receiving tank 14 Dehydrator W1 Membrane permeated water W2 Membrane concentrated water

Claims (2)

染料を含有する着色排水中に投与されて当該着色排水を脱色する排水処理剤であって、
担子菌栽培後の廃菌床から抽出した酵素を含有して構成されることを特徴とする排水処理剤。
A wastewater treatment agent that is administered into a colored wastewater containing a dye and decolorizes the colored wastewater,
A wastewater treatment agent comprising an enzyme extracted from a waste fungus bed after basidiomycete cultivation.
前記排水処理剤が、前記廃菌床から抽出した酵素液を凍結乾燥して錠剤化したものであることを特徴とする請求項1に記載の排水処理剤。   The wastewater treatment agent according to claim 1, wherein the wastewater treatment agent is a tablet obtained by freeze-drying an enzyme solution extracted from the waste fungus bed.
JP2009295741A 2009-12-25 2009-12-25 Wastewater treatment agent Pending JP2011131200A (en)

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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62259564A (en) * 1986-05-02 1987-11-11 Yakult Honsha Co Ltd Production of powder of fomes japonicus extract
JP2004066043A (en) * 2002-08-02 2004-03-04 Toyo Ink Mfg Co Ltd Method of decomposing dye and enzyme for decomposing dye

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62259564A (en) * 1986-05-02 1987-11-11 Yakult Honsha Co Ltd Production of powder of fomes japonicus extract
JP2004066043A (en) * 2002-08-02 2004-03-04 Toyo Ink Mfg Co Ltd Method of decomposing dye and enzyme for decomposing dye

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